Inhibition of Ammonia and Hydrogen Sulphide Using Plant Waste Materials for Faecal Sludge Odour Control in Dry Sanitation Toilet Facilities

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This study investigated plant waste materials as biocovers to suppress hydrogen sulphide and ammonia odors in dry sanitation facilities, finding sawdust biochar to be the most effective at reducing both gases.

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The preprint studied odour levels in two dry sanitation toilet facilities by measuring hydrogen sulphide (H2S) and ammonia (NH3) from faecal sludge, and then tested whether locally sourced plant wastes (biomasses), their ashes, or derived biochars used as biocovers could suppress these gases over a 12-day period in a lab setting. It found that baseline odour was high: H2S peaked at 3.17 ppm in facility T1 and 0.22 ppm in T2 (with T1 above and T2 below the cited 0.05 ppm unpleasantness threshold), while NH3 peaked at 6.88 ppm in T1 and 3.16 ppm in T2 (both below the cited 30 ppm limit). Acidic materials (biomasses) reduced NH3 emission by 12.5%–64.8%, whereas basic materials (ashes and biochar) more strongly reduced H2S emission by 80.9%–96.2%, with sawdust biochar achieving the highest H2S and NH3 abatement (96.2% and 74.7%). The main limitation is that the biocover performance was evaluated on fresh faecal sludge samples in a laboratory setting rather than as full field trials of toilet performance. This paper does not explicitly discuss endometriosis or adenomyosis; it was included in the corpus via a keyword match in the upstream search index.

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Abstract

On-site dry sanitation facilities, although cheaper than wet sanitation systems, suffer from high malodour and insect nuisance as well as poor aesthetics. The high odour deters users from utilizing dry sanitation toilet as an improved facility leading to over 20% open defecation in Sub-Saharan Africa. To address this malodour concern, this study first assessed odour levels, using hydrogen sulphide (H 2 S) and ammonia (NH 3 ) as indicators, on two (2) dry sanitation facilities (T1 and T2). The potential of using biomass (sawdust, rice husk, moringa leaves, neem seeds), ash (coconut husk, cocoa husk) or biochar (sawdust, rice husk, bamboo) as biocovers to remove or suppress odour from fresh faecal sludge (FS) over a 12-day period was investigated. Results showed high odour levels, beyond and below the threshold limit for unpleasantness for humans on H 2 S (peak value: T1 = 3.17 ppm; T2 = 0.22 ppm > 0.05 ppm limit) and NH 3 (peak value: T1 = 6.88 ppm; T2 = 3.16 ppm < 30 ppm limit), respectively. The biomasses exhibited low pH (acidic = 5-7) whereas the biochars and ashes had higher pHs (basic = 8-13). Acidic biocovers generally reduced NH 3 emission significantly (12.5% to 64.8%) whereas basic biocovers were more effective at H 2 S emission reduction (80.9% to 96.2%). In terms of H 2 S and NH 3 removal, sawdust biochar was the most effective biocover with odour abatement values of 96.2% and 74.7%, respectively. The results suggest that locally available waste plant-based materials, like sawdust, when converted to biochar can serve as a cost-effective and sustainable way to effectively combat odour-related issues associated with dry sanitation facilities to help stop open defecation.
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Inhibition of Ammonia and Hydrogen Sulphide Using Plant Waste Materials for Faecal Sludge Odour Control in Dry Sanitation Toilet Facilities | Research Square window.SnipcartSettings = { analytics: { enabled: false } }; (function() { var accessVector = localStorage.getItem('access_vector') || ''; window.dataLayer = window.dataLayer || []; if (accessVector) { window.dataLayer.push({ user: { profile: { profileInfo: { snid: accessVector } } } }); } })(); (function(w,d,s,l,i){w[l]=w[l]||[];w[l].push({'gtm.start':new Date().getTime(),event:'gtm.js'});var f=d.getElementsByTagName(s)[0],j=d.createElement(s),dl=l!='dataLayer'?'&l='+l:'';j.async=true;j.src='https://www.googletagmanager.com/gtm.js?id='+i+dl;f.parentNode.insertBefore(j,f);})(window,document,'script','dataLayer','GTM-K279D39R'); Browse Preprints In Review Journals COVID-19 Preprints AJE Video Bytes Research Tools Research Promotion AJE Professional Editing AJE Rubriq About Preprint Platform In Review Editorial Policies Our Team Advisory Board Help Center Sign In Submit a Preprint Cite Share Download PDF Research Article Inhibition of Ammonia and Hydrogen Sulphide Using Plant Waste Materials for Faecal Sludge Odour Control in Dry Sanitation Toilet Facilities Bernice Mawumenyo Senanu, Patrick Boakye, Sampson Oduro-Kwarteng, and 4 more This is a preprint; it has not been peer reviewed by a journal. https://doi.org/ 10.21203/rs.3.rs-659004/v1 This work is licensed under a CC BY 4.0 License Status: Under Review Version 1 posted 8 You are reading this latest preprint version Abstract On-site dry sanitation facilities, although cheaper than wet sanitation systems, suffer from high malodour and insect nuisance as well as poor aesthetics. The high odour deters users from utilizing dry sanitation toilet as an improved facility leading to over 20% open defecation in Sub-Saharan Africa. To address this malodour concern, this study first assessed odour levels, using hydrogen sulphide (H 2 S) and ammonia (NH 3 ) as indicators, on two (2) dry sanitation facilities (T1 and T2). The potential of using biomass (sawdust, rice husk, moringa leaves, neem seeds), ash (coconut husk, cocoa husk) or biochar (sawdust, rice husk, bamboo) as biocovers to remove or suppress odour from fresh faecal sludge (FS) over a 12-day period was investigated. Results showed high odour levels, beyond and below the threshold limit for unpleasantness for humans on H 2 S (peak value: T1 = 3.17 ppm; T2 = 0.22 ppm > 0.05 ppm limit) and NH 3 (peak value: T1 = 6.88 ppm; T2 = 3.16 ppm < 30 ppm limit), respectively. The biomasses exhibited low pH (acidic = 5-7) whereas the biochars and ashes had higher pHs (basic = 8-13). Acidic biocovers generally reduced NH 3 emission significantly (12.5% to 64.8%) whereas basic biocovers were more effective at H 2 S emission reduction (80.9% to 96.2%). In terms of H 2 S and NH 3 removal, sawdust biochar was the most effective biocover with odour abatement values of 96.2% and 74.7%, respectively. The results suggest that locally available waste plant-based materials, like sawdust, when converted to biochar can serve as a cost-effective and sustainable way to effectively combat odour-related issues associated with dry sanitation facilities to help stop open defecation. Environmental Engineering Health Economics & Outcomes Research ammonia biocover biochars dry sanitation hydrogen sulphide odour removal Figures Figure 1 Figure 2 Figure 3 Figure 4 Figure 5 1. Introduction Poor sanitation is a major cause of poverty and some preventable diseases like diarrhoea, intestinal worms and dysentery (WHO 2017). The lowest sanitation coverage is concentrated mainly in countries in Sub-Sahara Africa and Southern Asia (Deshpande et al. 2020). Populations living in urban centres in many developing countries lack household toilets and the only toilet facility is the shared toilet systems (Peprah et al. 2015) meant for public use – markets, transport stations and schools. Ghana’s sanitation coverage, as of 2017–2018 was 21%; which is below the millennium development goal (MDG) target of 54% (Appiah-Effah et al. 2019, Ghana Statistical Service 2018). On-site sanitation technology in Ghana serves 85% of the population (Rose et al. 2015), of which 68.2% use public toilets and 19.3% practice open defecation (Ghana Statistical Service 2016). For dry sanitation toilets, 29% of the population use pit or ventilated improved pit (VIP) (Ghana Statistical Service 2016) whereas users of water closets account for 15.4% of the population. Dry on-site sanitation technologies are relatively cheaper, require little or no water and occupy relatively less land, but the facility is usually characterized by malodour and insect nuisance (Obeng et al. 2016), which can discourage users of the facility from patronizing it and rather resort to open defecation (Duke Sanitation Solutions 2016, Obeng et al. 2015). Malodours are normally indicators that protect humans from potential illness caused by infection through contaminated food and matter (St Croix Sensory 2005). The odours are generally attributed to the evolution of different smell-causing substances (volatile compounds) arising from the anaerobic decomposition of the faecal matter (Mara 1984, Nakagiri et al. 2015, Wagner et al. 1958). The type of volatile compound evolved is also dependent on the age of faecal matter where fresh ones have rancid odour whereas aged ones in latrines have sewage, malodorous smell, like rotten egg due to the anaerobic decomposition process (Nakagiri et al. 2015). The rancid and cheesy odour in dry latrines is associated with the evolution of volatile compounds such as phenylacetic acids, butyric, isovaleric, 2-methyl butyric, isobutyric valeric and hexanoic. Sewage, rotten egg and rotten vegetable odours have been attributed to sulphur-based volatile compounds – arising from protein degradation and activities of sulphur-reducing bacteria (Oh et al. 2000, Persson et al. 1990) – such as dimethyl trisulphide, hydrogen sulphide (H 2 S), dimethyl disulphide, methyl mercaptan and dimethyl sulphide. Also, skatole, p-cresol, some carboxylic acids, phenol and indole have been associated with farmyard manure-like odours (Lin et al. 2013, Moore et al. 1987, Nakagiri et al. 2015, Sato et al. 2002). That notwithstanding, the sulphur and nitrogen-containing compounds, particularly ammonia (NH 3 ) and H 2 S, are of particular importance since they are the primary odorous substances and possess a distinctive odour that is readily noticeable even in small concentrations [H 2 S = 0.005 ppm (Atia et al. 2004); NH 3 = 0.05 ppm (van Thriel et al. 2006)] (Ying et al. 2012). In fact, a positive correlation between H 2 S concentration and user perception of odour have been recorded; otherwise for NH 3 concentration (Obeng et al. 2016). It is, therefore, no wonder that recommendations about the odour-irritation threshold concentrations of the NH 3 and H 2 S have been enacted and thus, respectively, ranges from 4 to 8 ppm and from 2.5 to 20 ppm (Schiffman and Williams 2005). Also, to avoid complaints from the facility users, it is recommended that the concentration of the H 2 S should not exceed (0.05 ppm) 7 µg/m 3 for a 30-minute averaging period (WHO 2000). Many approaches such as pH alteration, specialized/engineered microorganisms usage, microbial growth inhibition and use of biological covers (biocovers) have been investigated to address the malodorous nuances associated with the usage of dry sanitation toilets (Arogo et al. 2001, Ndegwa et al. 2008). Biocovers, in particular, are materials that serve as covers over faecal matter to help suppress gas emissions by either physically limiting the emissions of gases from the surface of the faecal matter or creating a biologically active zone on the top of the biocovers where gases are aerobically decomposed by microorganisms (Atia et al. 2004). Biocovers may be impermeable or permeable to gases depending on the material used. Impermeable biocovers only trap the odorous substances and are therefore normally used in conjunction with other treatment methods such as biofilters or scrubbers (Ndegwa et al. 2008). Examples include glued layers of polyethylene film and tarpaulin (Funk et al. 2004). Permeable biocovers, however, act like biofilters and can trap and subsequently biotransform odorous gases to harmless or less odorous forms (Ndegwa et al. 2008). For instance, H 2 S evolution can be inhibited via components in the biocovers reacting with and converting the dissolved sulphide into other intermediate forms, or inert metallic sulphides, or bisulphide ions (Atia et al. 2004). The performance of the biocovers is therefore dependent on their physicochemical properties – surface area, porosity, mineral composition, organic matter content and pH amongst many others (He et al. 2011) – and thickness of the applied biocover layer (Atia et al. 2004). It is known that NH 3 evolution can be attenuated in low pH (Ndegwa et al. 2008). High organic matter, surface area, porosity and cation exchange capacities (CEC) of waste biocover soil were effective at mitigating H 2 S evolution via adsorption, principally (He et al. 2011). It is, therefore, no wonder that permeable biocovers with the aforementioned properties have been investigated. These include waste lignocellulosic agricultural biomass – mulched wood material (Hurst et al. 2005), cornstalks, straws and wood chip (Guarino et al. 2006) –, geotextile fabrics (Bicudo et al. 2004), polystyrene foams (Miner and Suh 1997), silicates or clays (Balsari et al. 2006), fly ash (Hurst et al. 2005) and combinations of zeolite and agricultural biomass (Miner and Pan 1995). Lignocellulosic agricultural biomass, for instance, generally contains high organic matter content, helpful as food for microorganisms. Ash is known to contain inorganic constituents especially of alkali and alkaline-earth metals, which renders it highly basic (Sewu et al. 2017) and as such can abate H 2 S release via its adsorption capability and potential acid-base reactions with acidic H 2 S (Ducom et al. 2009) when used as a biocover. Another potential biocover seldom researched is biochar. Biochar, the carbonaceous product of biomass pyrolysis, has gained much popularity as a promising material for different high-value applications such as waste management and climate change mitigation tool (Sewu et al. 2019, Shaheen et al. 2019). Biomass for biochar production can be sourced from locally available agricultural wastes, making it cheap and conducive to the environment (Tan et al. 2017, Tran et al. 2018, Tran et al. 2017). It is hypothesized that owing to the unique physical and chemical characteristics, such as large specific surface area, high porosity, moderate CEC, abundant surface functionality, and excellent thermal, mechanical and chemical stability (Tran et al. 2016, Weber and Quicker 2018), biochar may serve as a potentially excellent biocover to mitigate odour release from dry sanitation toilets. This study, therefore, investigates the application of biomass, ash and biochar as potential biocovers to attenuate odour evolution from fresh FS generated in dry sanitation toilets. The specific objectives of this study are to (1) determine the on-site odour levels of dry-sanitation public toilets using NH 3 and H 2 S, as the primary odour-indicators; (2) acquire, produce and characterize different materials as potential biocovers for odour mitigation; and (3) evaluate the odour-suppression or odour-removal efficiencies of the as-produced biocovers on fresh human excreta samples from the dry sanitation toilets in a laboratory setting. 2. Materials And Methods 2.1. Study setting and description of the VIP latrines Faecal samples for this study were obtained from public toilets in Ayeduase. Ayeduase is a community located in the Oforikrom Sub-Metro of Kumasi Metropolitan Assembly in the Ashanti Region in Ghana with a human population estimated at 29,748 and has 6 o 40'0"N and 1 o 34'0"W in DMS (Degree Minutes Seconds) as its coordinates (Tasiame et al. 2019). Apart from student hostels and other well-built houses with wet toilet facilities, the majority of the natives use dry on-site toilet systems including shared facilities. This is because many of the houses are old structures built without toilet facilities. So inhabitants are compelled to use the nearest available public toilets. Some dwellers share public toilets intended for public schools. For this research, two public, dry on-site toilets (VIP latrines) were considered. The first public toilet (TI), which is located close to the Ayeduase market has depth beyond 2.5 m and houses ten (10) squat holes; one-half dedicated to each sex with an inter-squat hole concrete-partition-separation. An average of seventy-five (75) people use the toilet daily with a quarterly de-sludging frequency every year. The second public toilet (T2), is located close to the Ayeduase school, has a depth of almost 2 m and equipped with twelve (12) squat holes – two sets of five squat holes placed back to back on opposite sides of a dividing wall, with one set assigned to males and the other set to females. Every squat hole within a set is separated from each other by a concrete partition. The remaining two squat holes were adjacent to the five squat holes and contained in enclosed rooms. Over ninety (90) residents and school children patronize this toilet facility and are de-sludged every other week. Both TI and T2 were fitted with vent pipes at heights exceeding 500 mm above the roof of the superstructure. 2.2. Determination of on-site odours from VIP latrines To determine the degree to which odour was a nuisance in the use of VIP latrines, direct on-site measurements of H 2 S and NH 3 concentrations, representing odour, were carried out in the enclosures of T1 and T2 without the need for gas collection. Odour readings were taken from both T1 and T2, consistently for ten (10) days; three times daily: morning (6:30 − 7:30), afternoon (12:30 − 13:30) and evening (17:30 − 18:30) in greenwish mean time (GMT). The odour-causing gases were detected and quantified via direct air measurements in the enclosures of T1 and T2 using an aeroqual potable gas analyser (series 200, New Zealand). 2.3. Sampling protocol of FS for laboratory-based experiments Faecal sludge (FS) from both T1 and T2 was sampled from the surface of the pile of excreta beneath the pit pedestal. At the time of sampling, FS level in TI and T2 was, respectively, about 2 m and 10 cm, away from the squat hole. The sampling was undertaken by scraping off the top of the excreta with a one-meter-long ladle-like tool, to obtain a representative “fresh” faecal matter sample. The samples were collected into a tightly capped, 2000 ml plastic bucket and transported to an environmental laboratory in the civil engineering department of Kwame Nkrumah University of Science and Technology (KNUST) for analysis. 2.4. Acquisition and production of biocovers for odour mitigation Locally available materials including agricultural waste were used as potential biocovers for the mitigation of odour release from FS. Seven (7) biomasses were obtained for this experiment: sawdust (SD) from Celtis Mildbraedii , rice husk (RH), moringa leaves (M), neem seeds (NS), cocoa husk (CH), coconut husk (C N H) and bamboo (B) (See Fig. 1 ). Some of these biomasses were used, as is – sawdust, rice husk, moringa leaves, neem seeds – or were thermally treated via pyrolysis and ashing operations. For pyrolysis, only biomasses from rice husk, bamboo and sawdust were utilized as feedstock. The desired biomass was weighed and fed into the pyrolysis reactor with pyrolysis conditions of 400 o C for 90 min of sustained pyrolysis. After pyrolysis, the produced biochar was left to cool in the reactor for about 30 min before transferring into tightly capped vials to be stored for further experiments. For ash production, only biomasses from the cocoa husk and coconut husk were used. Each biomass was fed into a kiln (HT13T7, Kiln and Furnace Limited, Keele St. Tunstall, Stoke-On-Trant) where ashing was undertaken at a temperature of 700 o C. After ashing, the kiln was switched off and allowed to cool to within 60 o C and 80 o C. The ashes were collected and stored in tightly capped glass vials to be used for further experiments. Note that all acquired and produced biocovers were ground to within 210 to 75 µm and used for further experiments. Acronyms of B for biomasses, BC for biochars and A for ash were attached to the feedstocks for each process to help in identifying the thermal condition employed. Consequently, the obtained biocovers were tagged as SD-B, RH-B, M-B, and NS-B for biomasses of sawdust, rice husk, moringa powder and neem seeds powder, respectively. Tags were also assigned to sawdust biochar (SD-BC), rice husk biochar (RH-BC) and bamboo biochar (B-BC). Biocovers from the ash were also tagged for cocoa husk ash (CH-A) and coconut husk ash (C N H-A). 2.5. Evaluating the effect of additive application as biocovers for malodour mitigation The experimental setup is shown in Fig. 2 . The experimental design is a completely randomized design with two replicate measurements. The desired mass of each additive – biomass from sawdust, powdered rice husk, powdered moringa leaves and neem cake; ash from the cocoa husk and coconut husk and; biochar from sawdust, rice husk and bamboo – corresponding to 5wt.% (1:20 w/w) was determined and transferred into a 500 ml conical flask containing 300 g of fresh FS. Care was taken to ensure complete coverage of the FS in the conical flask with the applied biocovers. A control sample, which contained only FS without additives, was also include to facilitate the determination of the odour-removal efficiencies of the biosolid additives. Each conical flask was fitted with a single-perforated tightly fitting cork connected with a latex tubing that ends in 500 ml air-bag for gas trapping for further analysis. Analysis of the trapped gases was undertaken every three (3) days for 12 days. To prevent leakages, all openings around the corks were sealed with a sealant. The experiments were performed in two replicates. The performance of the biocover was evaluated based on the per cent reduction in odour – NH 3 or H 2 S – using Eq. (1). $$% Odour reduction=\left(\frac{{C} {1}-{C} {2} }{{C}_{1}}\right)\times 100 \left(1\right)$$ Where C 1 is the odour of the control sample (faecal sample without biocover) at a gas sampling time; C 2 is the odour of the biocover-applied faecal sample at that same gas sampling time. 2.6. Characterization experiments and statistical analysis The fresh FS samples were analysed for chemical oxygen demand (COD - dichromate approach) following (APHA-AWWA-WEF 2001) and biochemical oxygen demand (BOD) using the Winkler method. Both the FS and biosolid additives (biocovers) were analysed following the standard methods described in APHA-AWWA-WEF (2001) for water and wastewater analysis for the determination of total organic carbon (TOC), fixed solids (ash), total volatile solids (TVS) and total solids (TS). TKN content for FS and biosolid additives (biocovers) was determined following the EN 13342 standard (Janssen and Koopmann 2005). Also, pH was determined using a calibrated pH meter (Palintest micro 800 Mult, Singapore). The trapped gases in the airbags from the experimental setup in Sect. 2.5 were analysed qualitatively and quantitatively for H 2 S and NH 3 gases – representative of the malodorous gases – using the biogas 5000 gas analyser. Also, a comprehensive statistical analysis [two-way and one-way analysis of variance (ANOVA)] using the data analysis add-in in Microsoft® Excel was performed. The effect of two independent variables (biocover type and duration of biocover application) on suppression of odour (response variables: H 2 S and NH 3 ) were investigated using the two-way ANOVA without replication function. The one-way ANOVA was, however, employed to assess the statistical differences between the applied biocover types (biomass, biochar, ash) on the overall odour suppression for the entire duration of the experiment. A confidence level of 0.05 was chosen as the basis to either reject or fail to reject the null hypothesis of no statistically significant difference for the comparison. The Tukey-Kramer multiple comparison test was utilized for specificities in cases where the null hypothesis was rejected. 3. Results And Discussions 3.1. On-site odour evolution 3.1.1. Variations in H 2 S \(\) concentration on public toilets The daily H 2 S concentrations collected over different times within the day for both T1 and T2 during the 10-day survey are available in the Supplementary Fig. S1 and the corresponding daily averages shown in Fig. 3 a. Generally, the highest H 2 S concentration in the public toilet occurred during the mornings and evenings (Supplementary Fig. S1); expectedly a consequence of the most patronized times in the day. Other factors such as user conduct and effectiveness of cleaning activities may have played a role. From Fig. 3 a, it was evident that, except for day 6, daily averages of H 2 S was higher in T2 than T1, with some concentrations as high as 26.8 (day 5), 34.0 (day 8) and 39.2 (day 3) times that of T1. This could be attributed to the depth of the sludge in the pit of T1 (less than one-third of the pit depth) and T2 (almost filled to the brim), which is a consequence of the patronage frequency and cleaning activities. Consequently, more H 2 S will escape from the pit into the privy room in the case of T2 than T1, even though both facilities were fitted with vent pipes. Also, H 2 S is heavier (density of 1.36 kg/m 3 ) than air (density of 1.225 kg/m 3 ) and as such usually lingers at the base of the latrine (Safety and Administration 2005) even when fitted with vent pipes. Similar observations have been made by other authors who ascribed the observations to a large number of users (Strande and Brdjanovic 2014). Clearly odour in both T1 and T2 was detectable [> 0.005 ppm (Atia et al. 2004)]. Except for day 1 (0.021 ppm) and 7 (0.018 ppm) for T1, the daily H 2 S averages exceeded the guideline value of 0.05 ppm (Obeng et al. 2016, WHO 2000) for all toilet facilities investigated, which will inevitably elicit complaints from users and residents, and hamper patronage of the toilet facilities. 3.1.2. Variations in NH 3 concentration on public toilets The concentration of NH 3 was another component of odour that was measured in the two public latrines. Supplementary Fig. S1 shows the NH 3 concentration detected at different times in the day, during the 10-day experiment in T1 and T2. There was no observable trend for NH 3 evolution based on the sampling times. However, the daily averages (Fig. 3 b) showed a higher evolution of NH 3 for T1 than for T2 (except for day 4). Except for day 2, 3, 4 and 5, most of the daily NH 3 released were within the detectable threshold of 4 to 8 ppm for humans for T1 (day 1 = 4.90 ppm; day 6 = 7.04 ppm; day 7 = 4.70 ppm; day 8 = 4.88 ppm; day 9 = 6.88 ppm; day 10 = 5.49 ppm). For T2, however, none of the readings went beyond the detectable threshold for humans. It is noteworthy that all measured NH 3 concentrations were below the threshold of unbearableness and irritation for humans [(10 min exposure at 30 ppm – slight irritation; 10 min to 2 h exposure at 50 ppm – moderate irritation to the eyes, nose, throats and chest) (National Research Council 2008)]. According to Strande and Brdjanovic (2014), factors such as diet, climate, type of toilet facility, number of users among others influence odour release. Differences in the NH 3 measurement for T1 and T2 were attributed to the level of FS in the pit. Level of FS in TI and T2 were respectively, about 2 m and 10 cm away from the squat hole suggesting a poor maintenance regime especially for T2 since desludging should be undertaken when the sludge is about 50 cm from the slab. As such, NH 3 which is less dense (0.73 kg/m 3 ) than air (1.23 kg/m 3 ) at 15 o C at sea level, is more likely to escape easily into the atmosphere for T2 since the FS, in this case, was much closer to the squat hole; this may explain why less NH 3 was measured in T2 compared to T1. As such, the gas detector potentially recorded less NH 3 concentration in the privy room. For T1 because the sludge depth in the pit was less than one-third the depth of the pit, enough room was available for NH 3 to linger in the pit, which accounted for the reported higher NH 3 concentrations. Generally, it can be observed that NH 3 concentrations recorded in both toilets were higher than that for H 2 S in the latrine (Fig. 3 ). The NH 3 and H 2 S results in this study were in agreement with that obtained by Obeng et al. (2016), where mean NH 3 concentration in ventilated improved pit public toilets was higher (2.99 ppm) than that for H 2 S (0.13 ppm). 3.2. Characterization of FS Table 1 shows the characteristics of FS. The quotient of COD to BOD (COD/BOD ratio) obtained in this study was two (2); which is low compared to others reported in the literature. For instance, FS with a COD/BOD ratio of 5 and 6 was reported by Strande and Brdjanovic (2014) and Jeuland et al. (2004) for public toilets, respectively. Strande and Brdjanovic (2014) intimated that the higher value of 5 was indicative of the slow degradation of organic matter. Besides, it is also known that the characteristics of FS vary depending on parameters such as diet, type of toilet technology, climate and the type of cleansing material utilised (Obeng et al. 2016). These can thus explain the variations of the COD/BOD ratio. Moisture content in FS obtained from the public toilet was high (80.5%) as expected. Strande and Brdjanovic (2014) reported a similar result of high moisture content (83%) for dry VIP latrine sludge. Moisture content values ranging from 53–92% have been reported (Nishimuta et al. 2006). The weather condition was identified as a contributing factor to the variations obtained. The pH of FS in this study was slightly acidic (pH 5.7) with a TKN of 15,500 mg/l (1.5%), which is particularly low. Nevertheless, according to Rodhe et al. (2004) although FS is usually rich in nitrogen, changes in the expected nitrogen content in FS is largely subject to the diet of the user. For example, a highly proteinaceous diet will result in higher nitrogen content in FS (Strande and Brdjanovic 2014). Table 1 Characteristics of the fresh faecal sludge Parameter Unit Mean Standard deviation Chemical oxygen demand mg/l 181,900 ± 17678 Biochemical oxygen demand mg/l 102,300 ± 3818 Total kjeldahl nitrogen mg/l 15,500 ± 0.03196 Moisture content % 80.5 ± 2.120 Total volatile solids % 80.5 ± 2.121 Total organic carbon % 44.73 ± 1.181 Ash % 17.75 ± 0.3536 pH 5.7 ± 0.02121 3.3. Characterization of biocovers employed as odour-reducing additives The physicochemical properties of the different biocovers employed as odour-reducing additives in this study are presented in Table 2 . Biocovers from ash [pH: 13 (C N H-A); 12 (CH-A)] and biochar [pH: 9 (B-BC); 8 (RH-BC); 9 (SD-BC)] were alkaline, whereas that from the biomasses [pH: 5 (NS-B); 5 (M-B); 6 (RH-B)] were acidic except for SD-B, which was neutral (pH 7). It is worthy of mention that the pHs of the biochar (RS-BC and SD-BC) were higher than their precursors (RS-B and SD-B). The above results may be a consequence of the thermal treatment processes utilized for the ash and biochar production. Similar reports have been documented in the literature. For instance, Afful et al. (2016) recorded a high pH of 10.49 for coconut fibre and 10.35 for cocoa husk and ascribed the results to the thermal processing of the raw materials. That notwithstanding, the acidic or basic properties of additives influence the microbial growth of organisms and may affect the emission of NH 3 and H 2 S. This is because at higher pH nitrogen is released as NH 3 whilst, on the other hand, H 2 S forms sulphides at higher pH thereby reducing the H 2 S release. Moisture content for all biocovers was relatively low (< 5% for ash and biochars; within 8.6 to 11.2% for biomass) except for SD-B (30.8%). Less moisture content tends to hinder the growth of organisms therefore additives with less moisture content play a significant role in reducing bacterial growth and consequently, potentially lessening odour-production and release. Interestingly, the contents of fixed solids were observed to be inversely proportional to the volatile solids. It has been established that, upon increasing temperature for the determination of volatiles, the volatile matter is driven off, burnt away leaving ash, or fixed solids. C N H-A and CH-A both had higher fixed solids (respectively, 95.8% and 84.2%) compared to the other biocovers. This is because of the higher temperature they were subjected to, for ashing to take place; thus essentially eliminating the existing volatiles and leaving behind the fixed solids. Also, notice that the fixed solids in the biochars (RH-BC = 39.6%; SD-BC = 10.2%) were higher than that of their corresponding biomasses (RH-B = 15.9%; SD-B = 1.9%). Reasons are similar to those described earlier on in the text. Carbon content was also generally high for biochars (B-BC = 53.7%; RH-BC = 35%; SD-BC = 52.1%) and biomasses (NS-B = 52.8%; M-B = 52.3%; RH-B = 48.8%; SD-B = 56.9%), and extremely low for ash biocovers (C N H-A = 2.4%; CH-A = 9.2%) for reasons attributed to the extent of thermal treatment each biocover precursor material underwent. That notwithstanding, SD-B’s high carbon content may be a consequence of the source of the biomass, Celtis Mildbraedii ; which is woody (Maua et al. 2020). Similar results of the high carbon content of woody biomass have been reported by Sewu et al. (2017). For C/N ratio, CH-A recorded the highest value of 125 followed by RH-B at 103. Moringa and neem seed powder recorded the lowest C/N ratio of 17 and 13, respectively suggesting higher nitrogen contents relative to carbon contents in these materials. A high C/N ratio has been reported to have an impact on the reduction of odour levels in compost (Cornell Waste Management Institute 1996). Table 2 Physicochemical properties of biocovers employed as odour-reducing additives Category Additives pH Moisture content (%) Total volatile solids (%) Fixed solids (%) Carbon (%) C/N ratio Ash C N H-A 13 3.9 4.2 95.8 2.4 33 CH-A 12 3.2 15.8 84.2 9.2 125 Biochar B-BC 9 2.3 92.6 7.4 53.7 98 RH-BC 8 2.9 60.4 39.6 35 60 SD-BC 9 5 89.8 10.2 52.1 89 Biomass NS-B 5 11.1 91.1 8.9 52.8 17 M-B 5 8.7 90.2 9.8 52.3 13 RH-B 6 9 84.1 15.9 48.8 103 SD-B 7 30.8 98.1 1.9 56.9 97 3.4. Evaluation of the odour-reduction/removal performances of the applied biocovers 3.4.1. Effect of biocovers as additives on H 2 S reduction The effect of biocovers on the suppression or inhibitions of H 2 S evolution from FS for each studied sampling day over 12 days are shown in Fig. 4 a. Results show that apart from the inherent properties of biocovers – its efficacy on H 2 S reduction was time-dependent. Generally, biocovers with pHs in the acidic range required more time to be as effective as biocovers in the basic range. In addition, there was a general decline in H 2 S evolution with FS ageing. H 2 S was released most when FS was freshest at the time of sampling (day 3). This was particularly the case for the control sample and the biomasses (acidic biocovers). The basic biocovers, except for C N H-A, rather showed the most release of H 2 S on sampling day 6; with a trend consistently following the order: 6th day > 3rd day > 9th day > 12th day (in terms of concentration of H 2 S released). Furthermore, the application of basic biocovers led to a dramatic decrease in H 2 S evolution on the first sampling day (day 3); which was impressive. For instance, except for C N H-A, decreases were over 80% from the control value of 1245 ppm to 37 ppm for B-BC (97%); 198 ppm for RH-BC (84.1%); and 24 ppm for both SD-BC and CH-A (98.1%). This suggests biocovers of basic origin are effective for the rapid attenuation of H 2 S evolution by over 80%. The results of the overall per cent reduction in H 2 S over the entire study period of 12 days are shown in Fig. 4 b. It is evident that, generally, all biocovers performed well (over 55%) in mitigating H 2 S release. However, the extent of H 2 S reduction (%) was greater in the basic biocovers than in the acidic biocovers. Basic materials are known to reduce H 2 S release best since the increase in pH converts H 2 S to sulphides; essentially trapping it within the FS (Atia et al. 2004). That notwithstanding, amongst the basic biocovers, biochars were more effective at diminishing H 2 S evolution than ash with a near-complete reduction in H 2 S evolution [biochars: 96.2% (B-BC and SD-BC), 81.6% (RH-BC); ash: 80.9% (C N H-A) and 89.1% (CH-A)]. This contrary result of better reduction of H 2 S for biochar than ash, despite the higher pH of ash, may be due to the high surface area, surface functionality and porosity of biochar. Consequently, biochar may adsorb H 2 S thus limiting its release into the atmosphere. The carbon contents may likely be another reason, as the highest performing biocovers [biochar = 96.2% (B-BC and SD-BC); ash = 89.1% (CH-A)] also exhibited the highest carbon contents within the category of biochar (B-BC = 53.7%; SD-BC = 52.1%) and ash (CH-A = 9.2%) for the basic biocovers. Nevertheless, the higher performance of basic biocovers with high carbon content than acidic biocovers with comparable carbon contents for H 2 S reduction suggests that the earlier reasoning about surface area, pH, porosity and surface functionality may better explain the observations than carbon contents. 3.4.2. Effect of biocovers on NH 3 reduction The effect of biocovers on the suppression or inhibitions of NH 3 evolution from FS for each studied sampling day over the 12 days are shown in Fig. 5 a. Generally, there seem not to be a clear trend in NH 3 suppression with time given the utilized biocovers. No trend consistent with pH values, C/N ratio or carbon content was found in this study. Nevertheless, contrasting results were observed for biomasses and their corresponding biochars. For instance, whilst RH-B exhibited a general gradual decline in NH 3 evolution with time [6th day (4.5%v/v) < 9th day (1.7%v/v) 6th day (6.8%v/v) > 9th day (8.7%v/v)]. In addition, compared to the control, the decline in NH 3 evolution was drastic and rapid for all sampling days over the 12 days with the application of SD-BC [3rd day (3.8%v/v); 6th day (1.8%v/v); 9th day (1.3%v/v); 12th day (0.2%v/v)]. A similar observation was also seen for the SD-BC precursor (SD-B) except on day 6; where a heightened NH 3 evolution rather occurred. The results of the overall percentage reduction in NH 3 over the entire study period of 12 days are shown in Fig. 5 b. It is evident that majority of the acidic biocovers reduced the emission of NH 3 much better than the basic materials. In fact, except for SD-BC, all basic biocovers were not just extremely poor at attenuating NH 3 , but rather facilitated its release when compared to the control sample; by 58% (B-BC), 1.8% (RH-BC), 68.7% (C N H-A) and 49.1% (CH-A). Conversely, however, except for M-B, the acidic biocovers were good attenuators of NH 3 evolution. Particularly, RH-B (64.8%) was the most effective amongst the acidic biocovers at attenuating NH 3 evolution, followed by NS-B (17.4%) and SD-B (12.5%). Interestingly, not only was SD-BC the only effective biocover amongst the basic biocovers, it was also the most effective (74.7%) amongst all the investigated biocovers in this study in attenuating NH 3 evolution. According to Atia et al. (2004) the application of the biocovers reduces emissions of NH 3 and other odorous gases in two ways: (1) physically limiting the emissions of NH 3 and other gases; (2) creating a biologically active zone on the top of the covers where the emitted NH 3 and other gases are aerobically decomposed by microorganisms. The effectiveness of different covers or odour-reducing material in mitigating H 2 S and NH 3 emissions vary and it is also dependent on the quantity of the materials added as a cover. In theory, the effective suppression of odour is influenced by the pH which creates an unfavourable environment for microbial growth, and the physical masking ability of the additives (Arogo et al. 2001, Atia et al. 2004). 3.5. Statistical analysis of the effect of biocover type and duration of application on the suppression of odour from FS The results of the applied statistical analytical tools generated by Microsoft® Excel are shown in Table 3 . From the two-way ANOVA, the computed F values for the source of the variations [biocover source = 3.78 (H 2 S), 3.39 (NH 3 ); duration of application = 5.04 (H 2 S), 4.76 (NH 3 )] were all, greater than that of the F crit values (2.36 for biocover source; 3.01 for the duration of application). In addition, the P-values were lower than the level of significance at 0.05. From the aforementioned results, it was evident that the effects of the independent variables (biocover source and duration of application) on the suppression of both H 2 S and NH 3 evolution were statistically significant. These deductions were made based on two criteria: F value and the P-value . Values of F greater than reference F crit , and P-values lesser than the set level of significance at 0.05 (95% confidence limit) are indicative of a significant contribution to the variation by the group under investigation. Also, it was evident from the one-way ANOVA that variations in the means between the biocover type (biomass, biochar, ash) were statistically significant for H 2 S [ F (26.34) > F crit (5.148); P-value (0.0011) < 0.05] and insignificant for NH 3 [ F (1.956) 0.05]. Consequently, for the H 2 S, Tuker-Kramer multiple comparison test was used to evaluate which pair or combination of biocover type was the source of the variations for suppression of H 2 S evolution from FS. Clearly, the significant variations arose with biomass (low pH) and biochar/ash (higher pH) pairs suggesting that for effective H 2 S suppression, the pH of the biocovers is essential. Table 3 Results of the applied statistical analysis tools for the interpretation of odour suppression data (%) Two-way ANOVA without replication Source of Variation H 2 S suppression NH 3 suppression df F crit F P-value F P-value Biocover source 8 2.36 3.78 (S) 0.0058 3.39 (S) 0.0097 Duration of application 3 3.01 5.04 (S) 0.0075 4.76 (S) 0.0096 One-way ANOVA df F crit F P-value F P-value Between the groups of biocover type 2 5.143 26.34 (S) 0.0011 1.956 (NS) 0.223 Tukey-Kramer multiple comparison test results on the effect of biocover type on overall odour suppression efficiency Tukey-Kramer multiple comparison Biocover type H 2 S suppression (C.R. = 4.339) NH 3 suppression (C.R.= n.a.) Biomass Biochar Ash Biomass Biochar Ash Biomass X 9.68 (S) 6.82 (S) - - - Biochar - X 1.63 (NS) - - - Ash - - X - - - NB : Biocover source = (NS-B, M-B, RH-B, SD-B, B-BC, RH-BC, SD-BC, C N H-A, CH-A); Biocover type = (biomass, biochar, ash); duration of experiment, days = (3, 6, 9, 12); C.R. = critical range; df = degree of freedom; F = determined from experimental data using the F- test; F crit = F statistic obtained from the F -distribution; P-value = probability value; S = significant (absolute difference between mean odour suppression efficiencies is significant); NS = not significant (absolute difference between mean odour suppression efficiencies is not significant); n.a. = not applicable. 4. Conclusions Odour levels, assessed with H 2 S and NH 3 as indicators, in the two public latrines were above the perceptible threshold for humans and peaked in the mornings and evenings. Comparing the odour-causing substances, H 2 S and NH 3, only the former was above the threshold of unbearableness/annoyance to humans in the toilets investigated. Biocovers of biomass, biochar and ash origins were also successfully produced and utilized as potential inhibitors of odour-evolution from fresh FS generated in dry sanitation toilets in this study. Characterization studies showed that the pH of biomasses was lower (acidic) than that of the biochars and ashes; which were basic. Odour-suppression results showed that generally, high pH biocovers were more effective at suppressing H 2 S, whereas low pH biocovers were more effective at suppressing NH 3 evolution from FS. The per cent H 2 S and NH 3 reduction values were the highest for biocover from sawdust biochar; 96.2% and 74.7%, respectively. These results suggest that waste and readily available resources such as sawdust biomass, when converted to biochar, can serve as an effective tool to attenuate odour evolution from fresh faecal sludge in dry sanitation public toilets. Declarations Acknowledgements and Funding Authors would like to acknowledge and thank the Regional Water and Environmental Sanitation Centre Kumasi (RWESCK) at the Kwame Nkrumah University of Science and Technology, Kumasi for fully funding this research work with funds from the Ghana Government through the World Bank Africa Centres of Excellence project. Availability of data and materials Authors declare that data can be available upon request from the corresponding author Contributions Conceptualization : Sampson Oduro-Kwarteng, Esi Awuah; Methodology : Bernice Mawumenyo Senanu, Sampson Oduro-Kwarteng, Esi Awuah; Formal analysis and investigation : Bernice Mawumenyo Senanu; Writing - original draft preparation : Bernice Mawumenyo Senanu, Sampson Oduro-Kwarteng, Patrick Boakye; Writing - review and editing : Patrick Boakye, Divine Damertey Sewu, Peter Appiah Obeng, Kobina Afful; Funding acquisition : Sampson Oduro-Kwarteng; Resources : Sampson Oduro-Kwarteng, Esi Awuah; Supervision : Sampson Oduro-Kwarteng, Esi Awuah. 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Also discoverable on Platform About Our Team In Review Editorial Policies Advisory Board Help Center Resources Author Services Accessibility API Access RSS feed Manage Cookie Preferences © Research Square 2026 | ISSN 2693-5015 (online) Privacy Policy Terms of Service Do Not Sell My Personal Information {"props":{"pageProps":{"initialData":{"identity":"rs-659004","acceptedTermsAndConditions":true,"allowDirectSubmit":false,"archivedVersions":[],"articleType":"Research Article","associatedPublications":[],"authors":[{"id":37790510,"identity":"a954708e-b8a9-43c2-ba16-ca905ee98658","order_by":0,"name":"Bernice Mawumenyo Senanu","email":"","orcid":"","institution":"Kwame Nkrumah University of Science and Technology","correspondingAuthor":false,"prefix":"","firstName":"Bernice","middleName":"Mawumenyo","lastName":"Senanu","suffix":""},{"id":37790511,"identity":"68d5c125-c868-40e3-b419-e083ee7cb576","order_by":1,"name":"Patrick 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Technology","correspondingAuthor":false,"prefix":"","firstName":"Sampson","middleName":"","lastName":"Oduro-Kwarteng","suffix":""},{"id":37790513,"identity":"2fbfebf3-685b-471a-adb3-3d0bbfdc0cf9","order_by":3,"name":"Divine Damertey Sewu","email":"","orcid":"","institution":"Hanbat National University","correspondingAuthor":false,"prefix":"","firstName":"Divine","middleName":"Damertey","lastName":"Sewu","suffix":""},{"id":37790514,"identity":"89b91cb6-31c4-4d99-b218-8b914bd1e61d","order_by":4,"name":"Esi Awuah","email":"","orcid":"","institution":"Kwame Nkrumah University of Science and Technology","correspondingAuthor":false,"prefix":"","firstName":"Esi","middleName":"","lastName":"Awuah","suffix":""},{"id":37790515,"identity":"a33c2131-0a8c-45a3-9c85-472089b61211","order_by":5,"name":"Peter Appiah Obeng","email":"","orcid":"","institution":"University of Cape Coast","correspondingAuthor":false,"prefix":"","firstName":"Peter","middleName":"Appiah","lastName":"Obeng","suffix":""},{"id":37790516,"identity":"c0e26710-38ab-4e29-9c36-15bf13c7697b","order_by":6,"name":"Kobina Afful","email":"","orcid":"","institution":"Kwame Nkrumah University of Science and Technology","correspondingAuthor":false,"prefix":"","firstName":"Kobina","middleName":"","lastName":"Afful","suffix":""}],"badges":[],"createdAt":"2021-06-25 16:59:05","currentVersionCode":1,"declarations":"","doi":"10.21203/rs.3.rs-659004/v1","doiUrl":"https://doi.org/10.21203/rs.3.rs-659004/v1","draftVersion":[],"editorialEvents":[],"editorialNote":"","failedWorkflow":false,"files":[{"id":11299650,"identity":"291c00e8-e82f-4731-bab9-d95ad34241f3","added_by":"auto","created_at":"2021-07-09 14:18:02","extension":"png","order_by":1,"title":"Figure 1","display":"","copyAsset":false,"role":"figure","size":2181013,"visible":true,"origin":"","legend":"Photographs of the various waste biomasses and their corresponding ashes or biochars employed as biocovers in this study","description":"","filename":"Fig01.png","url":"https://assets-eu.researchsquare.com/files/rs-659004/v1/dcaa23942caa2e5bcb593f47.png"},{"id":11299653,"identity":"eaf81a12-0074-495b-8c1b-cfce6f360bbf","added_by":"auto","created_at":"2021-07-09 14:18:02","extension":"png","order_by":2,"title":"Figure 2","display":"","copyAsset":false,"role":"figure","size":385766,"visible":true,"origin":"","legend":"Experimental setup depicting additive application as biocovers for malodour mitigation","description":"","filename":"Fig02.png","url":"https://assets-eu.researchsquare.com/files/rs-659004/v1/4de56dbe3f6142740e02ed99.png"},{"id":11299750,"identity":"645e43ea-b330-456a-843c-07d0dcf99ddd","added_by":"auto","created_at":"2021-07-09 14:21:02","extension":"png","order_by":3,"title":"Figure 3","display":"","copyAsset":false,"role":"figure","size":78190,"visible":true,"origin":"","legend":"The concentration of H2S (a) and NH3 (b) released from T1 and T2 over 10 days as daily averages of the three sampling periods (mornings, afternoons and evenings)","description":"","filename":"Onlinefloatimage4.png","url":"https://assets-eu.researchsquare.com/files/rs-659004/v1/8da368c2fe0ddd36413cf83e.png"},{"id":11299655,"identity":"d43074e4-a936-4abb-8e47-e53c322bb8c7","added_by":"auto","created_at":"2021-07-09 14:18:02","extension":"jpeg","order_by":4,"title":"Figure 4","display":"","copyAsset":false,"role":"figure","size":583037,"visible":true,"origin":"","legend":"Effect of biocover type and acidity (pH) on mitigation of H2S on a (a) daily and (b) 12 days basis","description":"","filename":"floatimage6.jpeg","url":"https://assets-eu.researchsquare.com/files/rs-659004/v1/535def3111b20e2bdc846926.jpeg"},{"id":11299871,"identity":"2c853ce4-8c94-4bac-8a92-bc2a23f11d7c","added_by":"auto","created_at":"2021-07-09 14:24:02","extension":"png","order_by":5,"title":"Figure 5","display":"","copyAsset":false,"role":"figure","size":125399,"visible":true,"origin":"","legend":"Effect of biocover type and acidity (pH) on mitigation of NH3 on a (a) daily and (b) 12 days basis","description":"","filename":"Onlinefloatimage7.png","url":"https://assets-eu.researchsquare.com/files/rs-659004/v1/eca2fa2f251247dd4a9a2935.png"},{"id":13703023,"identity":"0ad0d45a-f511-49b0-a7f4-289d0dfa54ff","added_by":"auto","created_at":"2021-09-17 13:38:50","extension":"pdf","order_by":0,"title":"","display":"","copyAsset":false,"role":"manuscript-pdf","size":3322785,"visible":true,"origin":"","legend":"","description":"","filename":"manuscript.pdf","url":"https://assets-eu.researchsquare.com/files/rs-659004/v1/dc519a0d-fae4-4724-b7a7-876335837f1b.pdf"},{"id":11299748,"identity":"dcedc5d1-6c35-49c8-a0fd-03a00000297e","added_by":"auto","created_at":"2021-07-09 14:21:02","extension":"docx","order_by":1,"title":"","display":"","copyAsset":false,"role":"supplement","size":700201,"visible":true,"origin":"","legend":"","description":"","filename":"SupplementaryinformationPB.docx","url":"https://assets-eu.researchsquare.com/files/rs-659004/v1/ade01c03e575b1699e5badab.docx"},{"id":11299656,"identity":"8d6f8ec9-4573-41eb-9371-595a562e51d4","added_by":"auto","created_at":"2021-07-09 14:18:02","extension":"jpeg","order_by":2,"title":"","display":"","copyAsset":false,"role":"supplement","size":610012,"visible":true,"origin":"","legend":"","description":"","filename":"floatimage1.jpeg","url":"https://assets-eu.researchsquare.com/files/rs-659004/v1/dc3605bf0154f3ff8f625df0.jpeg"}],"financialInterests":"No competing interests reported.","formattedTitle":"\u003cp\u003eInhibition of Ammonia and Hydrogen Sulphide Using Plant Waste Materials for Faecal Sludge Odour Control in Dry Sanitation Toilet Facilities\u003c/p\u003e","fulltext":[{"header":"1. Introduction","content":"\u003cp\u003ePoor sanitation is a major cause of poverty and some preventable diseases like diarrhoea, intestinal worms and dysentery (WHO 2017). The lowest sanitation coverage is concentrated mainly in countries in Sub-Sahara Africa and Southern Asia (Deshpande et al. 2020). Populations living in urban centres in many developing countries lack household toilets and the only toilet facility is the shared toilet systems (Peprah et al. 2015) meant for public use \u0026ndash; markets, transport stations and schools. Ghana\u0026rsquo;s sanitation coverage, as of 2017\u0026ndash;2018 was 21%; which is below the millennium development goal (MDG) target of 54% (Appiah-Effah et al. 2019, Ghana Statistical Service 2018). On-site sanitation technology in Ghana serves 85% of the population (Rose et al. 2015), of which 68.2% use public toilets and 19.3% practice open defecation (Ghana Statistical Service 2016). For dry sanitation toilets, 29% of the population use pit or ventilated improved pit (VIP) (Ghana Statistical Service 2016) whereas users of water closets account for 15.4% of the population. Dry on-site sanitation technologies are relatively cheaper, require little or no water and occupy relatively less land, but the facility is usually characterized by malodour and insect nuisance (Obeng et al. 2016), which can discourage users of the facility from patronizing it and rather resort to open defecation (Duke Sanitation Solutions 2016, Obeng et al. 2015).\u003c/p\u003e \u003cp\u003eMalodours are normally indicators that protect humans from potential illness caused by infection through contaminated food and matter (St Croix Sensory 2005). The odours are generally attributed to the evolution of different smell-causing substances (volatile compounds) arising from the anaerobic decomposition of the faecal matter (Mara 1984, Nakagiri et al. 2015, Wagner et al. 1958). The type of volatile compound evolved is also dependent on the age of faecal matter where fresh ones have rancid odour whereas aged ones in latrines have sewage, malodorous smell, like rotten egg due to the anaerobic decomposition process (Nakagiri et al. 2015). The rancid and cheesy odour in dry latrines is associated with the evolution of volatile compounds such as phenylacetic acids, butyric, isovaleric, 2-methyl butyric, isobutyric valeric and hexanoic. Sewage, rotten egg and rotten vegetable odours have been attributed to sulphur-based volatile compounds \u0026ndash; arising from protein degradation and activities of sulphur-reducing bacteria (Oh et al. 2000, Persson et al. 1990) \u0026ndash; such as dimethyl trisulphide, hydrogen sulphide (H\u003csub\u003e2\u003c/sub\u003eS), dimethyl disulphide, methyl mercaptan and dimethyl sulphide. Also, skatole, p-cresol, some carboxylic acids, phenol and indole have been associated with farmyard manure-like odours (Lin et al. 2013, Moore et al. 1987, Nakagiri et al. 2015, Sato et al. 2002). That notwithstanding, the sulphur and nitrogen-containing compounds, particularly ammonia (NH\u003csub\u003e3\u003c/sub\u003e) and H\u003csub\u003e2\u003c/sub\u003eS, are of particular importance since they are the primary odorous substances and possess a distinctive odour that is readily noticeable even in small concentrations [H\u003csub\u003e2\u003c/sub\u003eS\u0026thinsp;=\u0026thinsp;0.005 ppm (Atia et al. 2004); NH\u003csub\u003e3\u003c/sub\u003e\u0026thinsp;=\u0026thinsp;0.05 ppm (van Thriel et al. 2006)] (Ying et al. 2012). In fact, a positive correlation between H\u003csub\u003e2\u003c/sub\u003eS concentration and user perception of odour have been recorded; otherwise for NH\u003csub\u003e3\u003c/sub\u003e concentration (Obeng et al. 2016). It is, therefore, no wonder that recommendations about the odour-irritation threshold concentrations of the NH\u003csub\u003e3\u003c/sub\u003e and H\u003csub\u003e2\u003c/sub\u003eS have been enacted and thus, respectively, ranges from 4 to 8 ppm and from 2.5 to 20 ppm (Schiffman and Williams 2005). Also, to avoid complaints from the facility users, it is recommended that the concentration of the H\u003csub\u003e2\u003c/sub\u003eS should not exceed (0.05 ppm) 7 \u0026micro;g/m\u003csup\u003e3\u003c/sup\u003e for a 30-minute averaging period (WHO 2000).\u003c/p\u003e \u003cp\u003eMany approaches such as pH alteration, specialized/engineered microorganisms usage, microbial growth inhibition and use of biological covers (biocovers) have been investigated to address the malodorous nuances associated with the usage of dry sanitation toilets (Arogo et al. 2001, Ndegwa et al. 2008). Biocovers, in particular, are materials that serve as covers over faecal matter to help suppress gas emissions by either physically limiting the emissions of gases from the surface of the faecal matter or creating a biologically active zone on the top of the biocovers where gases are aerobically decomposed by microorganisms (Atia et al. 2004). Biocovers may be impermeable or permeable to gases depending on the material used. Impermeable biocovers only trap the odorous substances and are therefore normally used in conjunction with other treatment methods such as biofilters or scrubbers (Ndegwa et al. 2008). Examples include glued layers of polyethylene film and tarpaulin (Funk et al. 2004). Permeable biocovers, however, act like biofilters and can trap and subsequently biotransform odorous gases to harmless or less odorous forms (Ndegwa et al. 2008). For instance, H\u003csub\u003e2\u003c/sub\u003eS evolution can be inhibited via components in the biocovers reacting with and converting the dissolved sulphide into other intermediate forms, or inert metallic sulphides, or bisulphide ions (Atia et al. 2004). The performance of the biocovers is therefore dependent on their physicochemical properties \u0026ndash; surface area, porosity, mineral composition, organic matter content and pH amongst many others (He et al. 2011) \u0026ndash; and thickness of the applied biocover layer (Atia et al. 2004). It is known that NH\u003csub\u003e3\u003c/sub\u003e evolution can be attenuated in low pH (Ndegwa et al. 2008). High organic matter, surface area, porosity and cation exchange capacities (CEC) of waste biocover soil were effective at mitigating H\u003csub\u003e2\u003c/sub\u003eS evolution via adsorption, principally (He et al. 2011). It is, therefore, no wonder that permeable biocovers with the aforementioned properties have been investigated. These include waste lignocellulosic agricultural biomass \u0026ndash; mulched wood material (Hurst et al. 2005), cornstalks, straws and wood chip (Guarino et al. 2006) \u0026ndash;, geotextile fabrics (Bicudo et al. 2004), polystyrene foams (Miner and Suh 1997), silicates or clays (Balsari et al. 2006), fly ash (Hurst et al. 2005) and combinations of zeolite and agricultural biomass (Miner and Pan 1995). Lignocellulosic agricultural biomass, for instance, generally contains high organic matter content, helpful as food for microorganisms. Ash is known to contain inorganic constituents especially of alkali and alkaline-earth metals, which renders it highly basic (Sewu et al. 2017) and as such can abate H\u003csub\u003e2\u003c/sub\u003eS release via its adsorption capability and potential acid-base reactions with acidic H\u003csub\u003e2\u003c/sub\u003eS (Ducom et al. 2009) when used as a biocover. Another potential biocover seldom researched is biochar.\u003c/p\u003e \u003cp\u003eBiochar, the carbonaceous product of biomass pyrolysis, has gained much popularity as a promising material for different high-value applications such as waste management and climate change mitigation tool (Sewu et al. 2019, Shaheen et al. 2019). Biomass for biochar production can be sourced from locally available agricultural wastes, making it cheap and conducive to the environment (Tan et al. 2017, Tran et al. 2018, Tran et al. 2017). It is hypothesized that owing to the unique physical and chemical characteristics, such as large specific surface area, high porosity, moderate CEC, abundant surface functionality, and excellent thermal, mechanical and chemical stability (Tran et al. 2016, Weber and Quicker 2018), biochar may serve as a potentially excellent biocover to mitigate odour release from dry sanitation toilets.\u003c/p\u003e \u003cp\u003eThis study, therefore, investigates the application of biomass, ash and biochar as potential biocovers to attenuate odour evolution from fresh FS generated in dry sanitation toilets. The specific objectives of this study are to (1) determine the on-site odour levels of dry-sanitation public toilets using NH\u003csub\u003e3\u003c/sub\u003e and H\u003csub\u003e2\u003c/sub\u003eS, as the primary odour-indicators; (2) acquire, produce and characterize different materials as potential biocovers for odour mitigation; and (3) evaluate the odour-suppression or odour-removal efficiencies of the as-produced biocovers on fresh human excreta samples from the dry sanitation toilets in a laboratory setting.\u003c/p\u003e"},{"header":"2. Materials And Methods","content":"\u003cdiv id=\"Sec3\" class=\"Section2\"\u003e \u003ch2\u003e2.1. Study setting and description of the VIP latrines\u003c/h2\u003e \u003cp\u003eFaecal samples for this study were obtained from public toilets in Ayeduase. Ayeduase is a community located in the Oforikrom Sub-Metro of Kumasi Metropolitan Assembly in the Ashanti Region in Ghana with a human population estimated at 29,748 and has 6\u003csup\u003eo\u003c/sup\u003e40'0\"N and 1\u003csup\u003eo\u003c/sup\u003e34'0\"W in DMS (Degree Minutes Seconds) as its coordinates (Tasiame et al. 2019). Apart from student hostels and other well-built houses with wet toilet facilities, the majority of the natives use dry on-site toilet systems including shared facilities. This is because many of the houses are old structures built without toilet facilities. So inhabitants are compelled to use the nearest available public toilets. Some dwellers share public toilets intended for public schools.\u003c/p\u003e \u003cp\u003eFor this research, two public, dry on-site toilets (VIP latrines) were considered. The first public toilet (TI), which is located close to the Ayeduase market has depth beyond 2.5 m and houses ten (10) squat holes; one-half dedicated to each sex with an inter-squat hole concrete-partition-separation. An average of seventy-five (75) people use the toilet daily with a quarterly de-sludging frequency every year. The second public toilet (T2), is located close to the Ayeduase school, has a depth of almost 2 m and equipped with twelve (12) squat holes \u0026ndash; two sets of five squat holes placed back to back on opposite sides of a dividing wall, with one set assigned to males and the other set to females. Every squat hole within a set is separated from each other by a concrete partition. The remaining two squat holes were adjacent to the five squat holes and contained in enclosed rooms. Over ninety (90) residents and school children patronize this toilet facility and are de-sludged every other week. Both TI and T2 were fitted with vent pipes at heights exceeding 500 mm above the roof of the superstructure.\u003c/p\u003e \u003c/div\u003e \u003cdiv id=\"Sec4\" class=\"Section2\"\u003e \u003ch2\u003e2.2. Determination of on-site odours from VIP latrines\u003c/h2\u003e \u003cp\u003eTo determine the degree to which odour was a nuisance in the use of VIP latrines, direct on-site measurements of H\u003csub\u003e2\u003c/sub\u003eS and NH\u003csub\u003e3\u003c/sub\u003e concentrations, representing odour, were carried out in the enclosures of T1 and T2 without the need for gas collection. Odour readings were taken from both T1 and T2, consistently for ten (10) days; three times daily: morning (6:30\u0026thinsp;\u0026minus;\u0026thinsp;7:30), afternoon (12:30\u0026thinsp;\u0026minus;\u0026thinsp;13:30) and evening (17:30\u0026thinsp;\u0026minus;\u0026thinsp;18:30) in greenwish mean time (GMT). The odour-causing gases were detected and quantified via direct air measurements in the enclosures of T1 and T2 using an aeroqual potable gas analyser (series 200, New Zealand).\u003c/p\u003e \u003c/div\u003e \u003cdiv id=\"Sec5\" class=\"Section2\"\u003e \u003ch2\u003e2.3. Sampling protocol of FS for laboratory-based experiments\u003c/h2\u003e \u003cp\u003eFaecal sludge (FS) from both T1 and T2 was sampled from the surface of the pile of excreta beneath the pit pedestal. At the time of sampling, FS level in TI and T2 was, respectively, about 2 m and 10 cm, away from the squat hole. The sampling was undertaken by scraping off the top of the excreta with a one-meter-long ladle-like tool, to obtain a representative \u0026ldquo;fresh\u0026rdquo; faecal matter sample. The samples were collected into a tightly capped, 2000 ml plastic bucket and transported to an environmental laboratory in the civil engineering department of Kwame Nkrumah University of Science and Technology (KNUST) for analysis.\u003c/p\u003e \u003c/div\u003e \u003cdiv id=\"Sec6\" class=\"Section2\"\u003e \u003ch2\u003e2.4. Acquisition and production of biocovers for odour mitigation\u003c/h2\u003e \u003cp\u003eLocally available materials including agricultural waste were used as potential biocovers for the mitigation of odour release from FS. Seven (7) biomasses were obtained for this experiment: sawdust (SD) from \u003cem\u003eCeltis Mildbraedii\u003c/em\u003e, rice husk (RH), moringa leaves (M), neem seeds (NS), cocoa husk (CH), coconut husk (C\u003csub\u003eN\u003c/sub\u003eH) and bamboo (B) (See Fig.\u0026nbsp;\u003cspan refid=\"Fig1\" class=\"InternalRef\"\u003e1\u003c/span\u003e). Some of these biomasses were used, as is \u0026ndash; sawdust, rice husk, moringa leaves, neem seeds \u0026ndash; or were thermally treated via pyrolysis and ashing operations.\u003c/p\u003e \u003cp\u003eFor pyrolysis, only biomasses from rice husk, bamboo and sawdust were utilized as feedstock. The desired biomass was weighed and fed into the pyrolysis reactor with pyrolysis conditions of 400 \u003csup\u003eo\u003c/sup\u003eC for 90 min of sustained pyrolysis. After pyrolysis, the produced biochar was left to cool in the reactor for about 30 min before transferring into tightly capped vials to be stored for further experiments.\u003c/p\u003e \u003cp\u003eFor ash production, only biomasses from the cocoa husk and coconut husk were used. Each biomass was fed into a kiln (HT13T7, Kiln and Furnace Limited, Keele St. Tunstall, Stoke-On-Trant) where ashing was undertaken at a temperature of 700 \u003csup\u003eo\u003c/sup\u003eC. After ashing, the kiln was switched off and allowed to cool to within 60 \u003csup\u003eo\u003c/sup\u003eC and 80 \u003csup\u003eo\u003c/sup\u003eC. The ashes were collected and stored in tightly capped glass vials to be used for further experiments. Note that all acquired and produced biocovers were ground to within 210 to 75 \u0026micro;m and used for further experiments. Acronyms of B for biomasses, BC for biochars and A for ash were attached to the feedstocks for each process to help in identifying the thermal condition employed. Consequently, the obtained biocovers were tagged as SD-B, RH-B, M-B, and NS-B for biomasses of sawdust, rice husk, moringa powder and neem seeds powder, respectively. Tags were also assigned to sawdust biochar (SD-BC), rice husk biochar (RH-BC) and bamboo biochar (B-BC). Biocovers from the ash were also tagged for cocoa husk ash (CH-A) and coconut husk ash (C\u003csub\u003eN\u003c/sub\u003eH-A).\u003c/p\u003e \u003cp\u003e \u003c/p\u003e \u003c/div\u003e \u003cdiv id=\"Sec7\" class=\"Section2\"\u003e \u003ch2\u003e2.5. Evaluating the effect of additive application as biocovers for malodour mitigation\u003c/h2\u003e \u003cp\u003eThe experimental setup is shown in Fig.\u0026nbsp;\u003cspan refid=\"Fig2\" class=\"InternalRef\"\u003e2\u003c/span\u003e. The experimental design is a completely randomized design with two replicate measurements. The desired mass of each additive \u0026ndash; biomass from sawdust, powdered rice husk, powdered moringa leaves and neem cake; ash from the cocoa husk and coconut husk and; biochar from sawdust, rice husk and bamboo \u0026ndash; corresponding to 5wt.% (1:20 w/w) was determined and transferred into a 500 ml conical flask containing 300 g of fresh FS. Care was taken to ensure complete coverage of the FS in the conical flask with the applied biocovers. A control sample, which contained only FS without additives, was also include to facilitate the determination of the odour-removal efficiencies of the biosolid additives. Each conical flask was fitted with a single-perforated tightly fitting cork connected with a latex tubing that ends in 500 ml air-bag for gas trapping for further analysis. Analysis of the trapped gases was undertaken every three (3) days for 12 days. To prevent leakages, all openings around the corks were sealed with a sealant. The experiments were performed in two replicates. The performance of the biocover was evaluated based on the per cent reduction in odour \u0026ndash; NH\u003csub\u003e3\u003c/sub\u003e or H\u003csub\u003e2\u003c/sub\u003eS \u0026ndash; using Eq.\u0026nbsp;(1).\u003cdiv id=\"Equa\" class=\"Equation\"\u003e\u003cdiv format=\"TEX\" class=\"mathdisplay\" id=\"FileID_Equa\" name=\"EquationSource\"\u003e\n\n$$\\% Odour reduction=\\left(\\frac{{C}_{1}-{C}_{2} }{{C}_{1}}\\right)\\times 100 \\left(1\\right)$$\u003c/div\u003e\u003c/div\u003e\u003c/p\u003e \u003cp\u003eWhere \u003cem\u003eC\u003c/em\u003e\u003csub\u003e\u003cem\u003e1\u003c/em\u003e\u003c/sub\u003e is the odour of the control sample (faecal sample without biocover) at a gas sampling time; \u003cem\u003eC\u003c/em\u003e\u003csub\u003e\u003cem\u003e2\u003c/em\u003e\u003c/sub\u003e is the odour of the biocover-applied faecal sample at that same gas sampling time.\u003c/p\u003e \u003cp\u003e \u003c/p\u003e \u003c/div\u003e \u003cdiv id=\"Sec8\" class=\"Section2\"\u003e \u003ch2\u003e2.6. Characterization experiments and statistical analysis\u003c/h2\u003e \u003cp\u003eThe fresh FS samples were analysed for chemical oxygen demand (COD - dichromate approach) following (APHA-AWWA-WEF 2001) and biochemical oxygen demand (BOD) using the Winkler method. Both the FS and biosolid additives (biocovers) were analysed following the standard methods described in APHA-AWWA-WEF (2001) for water and wastewater analysis for the determination of total organic carbon (TOC), fixed solids (ash), total volatile solids (TVS) and total solids (TS). TKN content for FS and biosolid additives (biocovers) was determined following the EN 13342 standard (Janssen and Koopmann 2005). Also, pH was determined using a calibrated pH meter (Palintest micro 800 Mult, Singapore). The trapped gases in the airbags from the experimental setup in Sect.\u0026nbsp;\u003cspan refid=\"Sec7\" class=\"InternalRef\"\u003e2.5\u003c/span\u003e were analysed qualitatively and quantitatively for H\u003csub\u003e2\u003c/sub\u003eS and NH\u003csub\u003e3\u003c/sub\u003e gases \u0026ndash; representative of the malodorous gases \u0026ndash; using the biogas 5000 gas analyser. Also, a comprehensive statistical analysis [two-way and one-way analysis of variance (ANOVA)] using the data analysis add-in in Microsoft\u0026reg; Excel was performed. The effect of two independent variables (biocover type and duration of biocover application) on suppression of odour (response variables: H\u003csub\u003e2\u003c/sub\u003eS and NH\u003csub\u003e3\u003c/sub\u003e) were investigated using the two-way ANOVA without replication function. The one-way ANOVA was, however, employed to assess the statistical differences between the applied biocover types (biomass, biochar, ash) on the overall odour suppression for the entire duration of the experiment. A confidence level of 0.05 was chosen as the basis to either reject or fail to reject the null hypothesis of no statistically significant difference for the comparison. The Tukey-Kramer multiple comparison test was utilized for specificities in cases where the null hypothesis was rejected.\u003c/p\u003e \u003c/div\u003e"},{"header":"3. Results And Discussions","content":"\u003cdiv id=\"Sec10\" class=\"Section2\"\u003e \u003ch2\u003e3.1. On-site odour evolution\u003c/h2\u003e \u003cdiv id=\"Sec11\" class=\"Section3\"\u003e \u003ch2\u003e3.1.1. Variations in H\u003csub\u003e2\u003c/sub\u003eS\u003cspan class=\"InlineEquation\"\u003e\u003cspan class=\"mathinline\"\u003e\\(\\)\u003c/span\u003e\u003c/span\u003econcentration on public toilets\u003c/h2\u003e \u003cp\u003eThe daily H\u003csub\u003e2\u003c/sub\u003eS concentrations collected over different times within the day for both T1 and T2 during the 10-day survey are available in the Supplementary Fig. S1 and the corresponding daily averages shown in Fig.\u0026nbsp;\u003cspan refid=\"Fig3\" class=\"InternalRef\"\u003e3\u003c/span\u003ea. Generally, the highest H\u003csub\u003e2\u003c/sub\u003eS concentration in the public toilet occurred during the mornings and evenings (Supplementary Fig. S1); expectedly a consequence of the most patronized times in the day. Other factors such as user conduct and effectiveness of cleaning activities may have played a role. From Fig.\u0026nbsp;\u003cspan refid=\"Fig3\" class=\"InternalRef\"\u003e3\u003c/span\u003ea, it was evident that, except for day 6, daily averages of H\u003csub\u003e2\u003c/sub\u003eS was higher in T2 than T1, with some concentrations as high as 26.8 (day 5), 34.0 (day 8) and 39.2 (day 3) times that of T1. This could be attributed to the depth of the sludge in the pit of T1 (less than one-third of the pit depth) and T2 (almost filled to the brim), which is a consequence of the patronage frequency and cleaning activities. Consequently, more H\u003csub\u003e2\u003c/sub\u003eS will escape from the pit into the privy room in the case of T2 than T1, even though both facilities were fitted with vent pipes. Also, H\u003csub\u003e2\u003c/sub\u003eS is heavier (density of 1.36 kg/m\u003csup\u003e3\u003c/sup\u003e) than air (density of 1.225 kg/m\u003csup\u003e3\u003c/sup\u003e) and as such usually lingers at the base of the latrine (Safety and Administration 2005) even when fitted with vent pipes. Similar observations have been made by other authors who ascribed the observations to a large number of users (Strande and Brdjanovic 2014). Clearly odour in both T1 and T2 was detectable [\u0026gt;\u0026thinsp;0.005 ppm (Atia et al. 2004)]. Except for day 1 (0.021 ppm) and 7 (0.018 ppm) for T1, the daily H\u003csub\u003e2\u003c/sub\u003eS averages exceeded the guideline value of 0.05 ppm (Obeng et al. 2016, WHO 2000) for all toilet facilities investigated, which will inevitably elicit complaints from users and residents, and hamper patronage of the toilet facilities.\u003c/p\u003e \u003cp\u003e \u003c/p\u003e \u003c/div\u003e \u003cdiv id=\"Sec12\" class=\"Section3\"\u003e \u003ch2\u003e3.1.2. Variations in NH\u003csub\u003e3\u003c/sub\u003e concentration on public toilets\u003c/h2\u003e \u003cp\u003eThe concentration of NH\u003csub\u003e3\u003c/sub\u003e was another component of odour that was measured in the two public latrines. Supplementary Fig. S1 shows the NH\u003csub\u003e3\u003c/sub\u003e concentration detected at different times in the day, during the 10-day experiment in T1 and T2. There was no observable trend for NH\u003csub\u003e3\u003c/sub\u003e evolution based on the sampling times. However, the daily averages (Fig.\u0026nbsp;\u003cspan refid=\"Fig3\" class=\"InternalRef\"\u003e3\u003c/span\u003eb) showed a higher evolution of NH\u003csub\u003e3\u003c/sub\u003e for T1 than for T2 (except for day 4). Except for day 2, 3, 4 and 5, most of the daily NH\u003csub\u003e3\u003c/sub\u003e released were within the detectable threshold of 4 to 8 ppm for humans for T1 (day 1\u0026thinsp;=\u0026thinsp;4.90 ppm; day 6\u0026thinsp;=\u0026thinsp;7.04 ppm; day 7\u0026thinsp;=\u0026thinsp;4.70 ppm; day 8\u0026thinsp;=\u0026thinsp;4.88 ppm; day 9\u0026thinsp;=\u0026thinsp;6.88 ppm; day 10\u0026thinsp;=\u0026thinsp;5.49 ppm). For T2, however, none of the readings went beyond the detectable threshold for humans. It is noteworthy that all measured NH\u003csub\u003e3\u003c/sub\u003e concentrations were below the threshold of unbearableness and irritation for humans [(10 min exposure at 30 ppm \u0026ndash; slight irritation; 10 min to 2 h exposure at 50 ppm \u0026ndash; moderate irritation to the eyes, nose, throats and chest) (National Research Council 2008)]. According to Strande and Brdjanovic (2014), factors such as diet, climate, type of toilet facility, number of users among others influence odour release. Differences in the NH\u003csub\u003e3\u003c/sub\u003e measurement for T1 and T2 were attributed to the level of FS in the pit. Level of FS in TI and T2 were respectively, about 2 m and 10 cm away from the squat hole suggesting a poor maintenance regime especially for T2 since desludging should be undertaken when the sludge is about 50 cm from the slab. As such, NH\u003csub\u003e3\u003c/sub\u003e which is less dense (0.73 kg/m\u003csup\u003e3\u003c/sup\u003e) than air (1.23 kg/m\u003csup\u003e3\u003c/sup\u003e) at 15 \u003csup\u003eo\u003c/sup\u003eC at sea level, is more likely to escape easily into the atmosphere for T2 since the FS, in this case, was much closer to the squat hole; this may explain why less NH\u003csub\u003e3\u003c/sub\u003e was measured in T2 compared to T1. As such, the gas detector potentially recorded less NH\u003csub\u003e3\u003c/sub\u003e concentration in the privy room. For T1 because the sludge depth in the pit was less than one-third the depth of the pit, enough room was available for NH\u003csub\u003e3\u003c/sub\u003e to linger in the pit, which accounted for the reported higher NH\u003csub\u003e3\u003c/sub\u003e concentrations.\u003c/p\u003e \u003cp\u003eGenerally, it can be observed that NH\u003csub\u003e3\u003c/sub\u003e concentrations recorded in both toilets were higher than that for H\u003csub\u003e2\u003c/sub\u003eS in the latrine (Fig.\u0026nbsp;\u003cspan refid=\"Fig3\" class=\"InternalRef\"\u003e3\u003c/span\u003e). The NH\u003csub\u003e3\u003c/sub\u003e and H\u003csub\u003e2\u003c/sub\u003eS results in this study were in agreement with that obtained by Obeng et al. (2016), where mean NH\u003csub\u003e3\u003c/sub\u003e concentration in ventilated improved pit public toilets was higher (2.99 ppm) than that for H\u003csub\u003e2\u003c/sub\u003eS (0.13 ppm).\u003c/p\u003e \u003c/div\u003e \u003c/div\u003e \u003cdiv id=\"Sec13\" class=\"Section2\"\u003e \u003ch2\u003e3.2. Characterization of FS\u003c/h2\u003e \u003cp\u003eTable\u0026nbsp;\u003cspan refid=\"Tab1\" class=\"InternalRef\"\u003e1\u003c/span\u003e shows the characteristics of FS. The quotient of COD to BOD (COD/BOD ratio) obtained in this study was two (2); which is low compared to others reported in the literature. For instance, FS with a COD/BOD ratio of 5 and 6 was reported by Strande and Brdjanovic (2014) and Jeuland et al. (2004) for public toilets, respectively. Strande and Brdjanovic (2014) intimated that the higher value of 5 was indicative of the slow degradation of organic matter. Besides, it is also known that the characteristics of FS vary depending on parameters such as diet, type of toilet technology, climate and the type of cleansing material utilised (Obeng et al. 2016). These can thus explain the variations of the COD/BOD ratio.\u003c/p\u003e \u003cp\u003eMoisture content in FS obtained from the public toilet was high (80.5%) as expected. Strande and Brdjanovic (2014) reported a similar result of high moisture content (83%) for dry VIP latrine sludge. Moisture content values ranging from 53\u0026ndash;92% have been reported (Nishimuta et al. 2006). The weather condition was identified as a contributing factor to the variations obtained. The pH of FS in this study was slightly acidic (pH 5.7) with a TKN of 15,500 mg/l (1.5%), which is particularly low. Nevertheless, according to Rodhe et al. (2004) although FS is usually rich in nitrogen, changes in the expected nitrogen content in FS is largely subject to the diet of the user. For example, a highly proteinaceous diet will result in higher nitrogen content in FS (Strande and Brdjanovic 2014).\u003c/p\u003e \u003cp\u003e \u003cdiv class=\"gridtable\"\u003e\u003ctable float=\"Yes\" id=\"Tab1\" border=\"1\"\u003e \u003ccaption language=\"En\"\u003e \u003cdiv class=\"CaptionNumber\"\u003eTable 1\u003c/div\u003e \u003cdiv class=\"CaptionContent\"\u003e \u003cp\u003eCharacteristics of the fresh faecal sludge\u003c/p\u003e \u003c/div\u003e \u003c/caption\u003e \u003ccolgroup cols=\"4\"\u003e \u003cthead\u003e \u003ctr\u003e \u003cth align=\"left\" colname=\"c1\"\u003e \u003cp\u003eParameter\u003c/p\u003e \u003c/th\u003e \u003cth align=\"left\" colname=\"c2\"\u003e \u003cp\u003eUnit\u003c/p\u003e \u003c/th\u003e \u003cth align=\"left\" colname=\"c3\"\u003e \u003cp\u003eMean\u003c/p\u003e \u003c/th\u003e \u003cth align=\"left\" colname=\"c4\"\u003e \u003cp\u003eStandard deviation\u003c/p\u003e \u003c/th\u003e \u003c/tr\u003e \u003c/thead\u003e \u003ctbody\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e \u003cp\u003eChemical oxygen demand\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003emg/l\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c3\"\u003e \u003cp\u003e181,900\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e\u0026plusmn;\u0026thinsp;17678\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e \u003cp\u003eBiochemical oxygen demand\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003emg/l\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c3\"\u003e \u003cp\u003e102,300\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e\u0026plusmn;\u0026thinsp;3818\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e \u003cp\u003eTotal kjeldahl nitrogen\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003emg/l\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c3\"\u003e \u003cp\u003e15,500\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e\u0026plusmn;\u0026thinsp;0.03196\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e \u003cp\u003eMoisture content\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003e%\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c3\"\u003e \u003cp\u003e80.5\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e\u0026plusmn;\u0026thinsp;2.120\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e \u003cp\u003eTotal volatile solids\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003e%\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c3\"\u003e \u003cp\u003e80.5\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e\u0026plusmn;\u0026thinsp;2.121\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e \u003cp\u003eTotal organic carbon\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003e%\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c3\"\u003e \u003cp\u003e44.73\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e\u0026plusmn;\u0026thinsp;1.181\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e \u003cp\u003eAsh\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003e%\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c3\"\u003e \u003cp\u003e17.75\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e\u0026plusmn;\u0026thinsp;0.3536\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e \u003cp\u003epH\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colname=\"c3\"\u003e \u003cp\u003e5.7\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e\u0026plusmn;\u0026thinsp;0.02121\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003c/tbody\u003e \u003c/colgroup\u003e \u003c/table\u003e\u003c/div\u003e \u003c/p\u003e \u003c/div\u003e \u003cdiv id=\"Sec14\" class=\"Section2\"\u003e \u003ch2\u003e3.3. Characterization of biocovers employed as odour-reducing additives\u003c/h2\u003e \u003cp\u003eThe physicochemical properties of the different biocovers employed as odour-reducing additives in this study are presented in Table\u0026nbsp;\u003cspan refid=\"Tab2\" class=\"InternalRef\"\u003e2\u003c/span\u003e. Biocovers from ash [pH: 13 (C\u003csub\u003eN\u003c/sub\u003eH-A); 12 (CH-A)] and biochar [pH: 9 (B-BC); 8 (RH-BC); 9 (SD-BC)] were alkaline, whereas that from the biomasses [pH: 5 (NS-B); 5 (M-B); 6 (RH-B)] were acidic except for SD-B, which was neutral (pH 7). It is worthy of mention that the pHs of the biochar (RS-BC and SD-BC) were higher than their precursors (RS-B and SD-B). The above results may be a consequence of the thermal treatment processes utilized for the ash and biochar production. Similar reports have been documented in the literature. For instance, Afful et al. (2016) recorded a high pH of 10.49 for coconut fibre and 10.35 for cocoa husk and ascribed the results to the thermal processing of the raw materials. That notwithstanding, the acidic or basic properties of additives influence the microbial growth of organisms and may affect the emission of NH\u003csub\u003e3\u003c/sub\u003e and H\u003csub\u003e2\u003c/sub\u003eS. This is because at higher pH nitrogen is released as NH\u003csub\u003e3\u003c/sub\u003e whilst, on the other hand, H\u003csub\u003e2\u003c/sub\u003eS forms sulphides at higher pH thereby reducing the H\u003csub\u003e2\u003c/sub\u003eS release.\u003c/p\u003e \u003cp\u003eMoisture content for all biocovers was relatively low (\u0026lt;\u0026thinsp;5% for ash and biochars; within 8.6 to 11.2% for biomass) except for SD-B (30.8%). Less moisture content tends to hinder the growth of organisms therefore additives with less moisture content play a significant role in reducing bacterial growth and consequently, potentially lessening odour-production and release.\u003c/p\u003e \u003cp\u003eInterestingly, the contents of fixed solids were observed to be inversely proportional to the volatile solids. It has been established that, upon increasing temperature for the determination of volatiles, the volatile matter is driven off, burnt away leaving ash, or fixed solids. C\u003csub\u003eN\u003c/sub\u003eH-A and CH-A both had higher fixed solids (respectively, 95.8% and 84.2%) compared to the other biocovers. This is because of the higher temperature they were subjected to, for ashing to take place; thus essentially eliminating the existing volatiles and leaving behind the fixed solids. Also, notice that the fixed solids in the biochars (RH-BC\u0026thinsp;=\u0026thinsp;39.6%; SD-BC\u0026thinsp;=\u0026thinsp;10.2%) were higher than that of their corresponding biomasses (RH-B\u0026thinsp;=\u0026thinsp;15.9%; SD-B\u0026thinsp;=\u0026thinsp;1.9%). Reasons are similar to those described earlier on in the text.\u003c/p\u003e \u003cp\u003eCarbon content was also generally high for biochars (B-BC\u0026thinsp;=\u0026thinsp;53.7%; RH-BC\u0026thinsp;=\u0026thinsp;35%; SD-BC\u0026thinsp;=\u0026thinsp;52.1%) and biomasses (NS-B\u0026thinsp;=\u0026thinsp;52.8%; M-B\u0026thinsp;=\u0026thinsp;52.3%; RH-B\u0026thinsp;=\u0026thinsp;48.8%; SD-B\u0026thinsp;=\u0026thinsp;56.9%), and extremely low for ash biocovers (C\u003csub\u003eN\u003c/sub\u003eH-A\u0026thinsp;=\u0026thinsp;2.4%; CH-A\u0026thinsp;=\u0026thinsp;9.2%) for reasons attributed to the extent of thermal treatment each biocover precursor material underwent. That notwithstanding, SD-B\u0026rsquo;s high carbon content may be a consequence of the source of the biomass, \u003cem\u003eCeltis Mildbraedii\u003c/em\u003e; which is woody (Maua et al. 2020). Similar results of the high carbon content of woody biomass have been reported by Sewu et al. (2017).\u003c/p\u003e \u003cp\u003eFor C/N ratio, CH-A recorded the highest value of 125 followed by RH-B at 103. Moringa and neem seed powder recorded the lowest C/N ratio of 17 and 13, respectively suggesting higher nitrogen contents relative to carbon contents in these materials. A high C/N ratio has been reported to have an impact on the reduction of odour levels in compost (Cornell Waste Management Institute 1996).\u003c/p\u003e \u003cp\u003e \u003cdiv class=\"gridtable\"\u003e\u003ctable float=\"Yes\" id=\"Tab2\" border=\"1\"\u003e \u003ccaption language=\"En\"\u003e \u003cdiv class=\"CaptionNumber\"\u003eTable 2\u003c/div\u003e \u003cdiv class=\"CaptionContent\"\u003e \u003cp\u003ePhysicochemical properties of biocovers employed as odour-reducing additives\u003c/p\u003e \u003c/div\u003e \u003c/caption\u003e \u003ccolgroup cols=\"8\"\u003e \u003cthead\u003e \u003ctr\u003e \u003cth align=\"left\" colname=\"c1\"\u003e \u003cp\u003eCategory\u003c/p\u003e \u003c/th\u003e \u003cth align=\"left\" colname=\"c2\"\u003e \u003cp\u003eAdditives\u003c/p\u003e \u003c/th\u003e \u003cth align=\"left\" colname=\"c3\"\u003e \u003cp\u003epH\u003c/p\u003e \u003c/th\u003e \u003cth align=\"left\" colname=\"c4\"\u003e \u003cp\u003eMoisture content (%)\u003c/p\u003e \u003c/th\u003e \u003cth align=\"left\" colname=\"c5\"\u003e \u003cp\u003eTotal volatile solids (%)\u003c/p\u003e \u003c/th\u003e \u003cth align=\"left\" colname=\"c6\"\u003e \u003cp\u003eFixed solids (%)\u003c/p\u003e \u003c/th\u003e \u003cth align=\"left\" colname=\"c7\"\u003e \u003cp\u003eCarbon (%)\u003c/p\u003e \u003c/th\u003e \u003cth align=\"left\" colname=\"c8\"\u003e \u003cp\u003eC/N ratio\u003c/p\u003e \u003c/th\u003e \u003c/tr\u003e \u003c/thead\u003e \u003ctbody\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e \u003cp\u003eAsh\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003eC\u003csub\u003eN\u003c/sub\u003eH-A\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c3\"\u003e \u003cp\u003e13\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e3.9\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c5\"\u003e \u003cp\u003e4.2\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c6\"\u003e \u003cp\u003e95.8\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c7\"\u003e \u003cp\u003e2.4\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c8\"\u003e \u003cp\u003e33\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003eCH-A\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c3\"\u003e \u003cp\u003e12\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e3.2\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c5\"\u003e \u003cp\u003e15.8\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c6\"\u003e \u003cp\u003e84.2\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c7\"\u003e \u003cp\u003e9.2\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c8\"\u003e \u003cp\u003e125\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e \u003cp\u003eBiochar\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003eB-BC\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c3\"\u003e \u003cp\u003e9\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e2.3\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c5\"\u003e \u003cp\u003e92.6\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c6\"\u003e \u003cp\u003e7.4\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c7\"\u003e \u003cp\u003e53.7\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c8\"\u003e \u003cp\u003e98\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003eRH-BC\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c3\"\u003e \u003cp\u003e8\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e2.9\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c5\"\u003e \u003cp\u003e60.4\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c6\"\u003e \u003cp\u003e39.6\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c7\"\u003e \u003cp\u003e35\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c8\"\u003e \u003cp\u003e60\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003eSD-BC\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c3\"\u003e \u003cp\u003e9\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e5\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c5\"\u003e \u003cp\u003e89.8\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c6\"\u003e \u003cp\u003e10.2\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c7\"\u003e \u003cp\u003e52.1\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c8\"\u003e \u003cp\u003e89\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e \u003cp\u003eBiomass\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003eNS-B\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c3\"\u003e \u003cp\u003e5\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e11.1\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c5\"\u003e \u003cp\u003e91.1\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c6\"\u003e \u003cp\u003e8.9\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c7\"\u003e \u003cp\u003e52.8\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c8\"\u003e \u003cp\u003e17\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003eM-B\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c3\"\u003e \u003cp\u003e5\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e8.7\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c5\"\u003e \u003cp\u003e90.2\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c6\"\u003e \u003cp\u003e9.8\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c7\"\u003e \u003cp\u003e52.3\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c8\"\u003e \u003cp\u003e13\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003eRH-B\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c3\"\u003e \u003cp\u003e6\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e9\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c5\"\u003e \u003cp\u003e84.1\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c6\"\u003e \u003cp\u003e15.9\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c7\"\u003e \u003cp\u003e48.8\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c8\"\u003e \u003cp\u003e103\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003eSD-B\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c3\"\u003e \u003cp\u003e7\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e30.8\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c5\"\u003e \u003cp\u003e98.1\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c6\"\u003e \u003cp\u003e1.9\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c7\"\u003e \u003cp\u003e56.9\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"char\" char=\".\" colname=\"c8\"\u003e \u003cp\u003e97\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003c/tbody\u003e \u003c/colgroup\u003e \u003c/table\u003e\u003c/div\u003e \u003c/p\u003e \u003c/div\u003e \u003cdiv id=\"Sec15\" class=\"Section2\"\u003e \u003ch2\u003e3.4. Evaluation of the odour-reduction/removal performances of the applied biocovers\u003c/h2\u003e \u003cdiv id=\"Sec16\" class=\"Section3\"\u003e \u003ch2\u003e3.4.1. Effect of biocovers as additives on H\u003csub\u003e2\u003c/sub\u003eS reduction\u003c/h2\u003e \u003cp\u003eThe effect of biocovers on the suppression or inhibitions of H\u003csub\u003e2\u003c/sub\u003eS evolution from FS for each studied sampling day over 12 days are shown in Fig.\u0026nbsp;\u003cspan refid=\"Fig4\" class=\"InternalRef\"\u003e4\u003c/span\u003ea. Results show that apart from the inherent properties of biocovers \u0026ndash; its efficacy on H\u003csub\u003e2\u003c/sub\u003eS reduction was time-dependent. Generally, biocovers with pHs in the acidic range required more time to be as effective as biocovers in the basic range. In addition, there was a general decline in H\u003csub\u003e2\u003c/sub\u003eS evolution with FS ageing. H\u003csub\u003e2\u003c/sub\u003eS was released most when FS was freshest at the time of sampling (day 3). This was particularly the case for the control sample and the biomasses (acidic biocovers). The basic biocovers, except for C\u003csub\u003eN\u003c/sub\u003eH-A, rather showed the most release of H\u003csub\u003e2\u003c/sub\u003eS on sampling day 6; with a trend consistently following the order: 6th day\u0026thinsp;\u0026gt;\u0026thinsp;3rd day\u0026thinsp;\u0026gt;\u0026thinsp;9th day\u0026thinsp;\u0026gt;\u0026thinsp;12th day (in terms of concentration of H\u003csub\u003e2\u003c/sub\u003eS released). Furthermore, the application of basic biocovers led to a dramatic decrease in H\u003csub\u003e2\u003c/sub\u003eS evolution on the first sampling day (day 3); which was impressive. For instance, except for C\u003csub\u003eN\u003c/sub\u003eH-A, decreases were over 80% from the control value of 1245 ppm to 37 ppm for B-BC (97%); 198 ppm for RH-BC (84.1%); and 24 ppm for both SD-BC and CH-A (98.1%). This suggests biocovers of basic origin are effective for the rapid attenuation of H\u003csub\u003e2\u003c/sub\u003eS evolution by over 80%.\u003c/p\u003e \u003cp\u003eThe results of the overall per cent reduction in H\u003csub\u003e2\u003c/sub\u003eS over the entire study period of 12 days are shown in Fig.\u0026nbsp;\u003cspan refid=\"Fig4\" class=\"InternalRef\"\u003e4\u003c/span\u003eb. It is evident that, generally, all biocovers performed well (over 55%) in mitigating H\u003csub\u003e2\u003c/sub\u003eS release. However, the extent of H\u003csub\u003e2\u003c/sub\u003eS reduction (%) was greater in the basic biocovers than in the acidic biocovers. Basic materials are known to reduce H\u003csub\u003e2\u003c/sub\u003eS release best since the increase in pH converts H\u003csub\u003e2\u003c/sub\u003eS to sulphides; essentially trapping it within the FS (Atia et al. 2004). That notwithstanding, amongst the basic biocovers, biochars were more effective at diminishing H\u003csub\u003e2\u003c/sub\u003eS evolution than ash with a near-complete reduction in H\u003csub\u003e2\u003c/sub\u003eS evolution [biochars: 96.2% (B-BC and SD-BC), 81.6% (RH-BC); ash: 80.9% (C\u003csub\u003eN\u003c/sub\u003eH-A) and 89.1% (CH-A)]. This contrary result of better reduction of H\u003csub\u003e2\u003c/sub\u003eS for biochar than ash, despite the higher pH of ash, may be due to the high surface area, surface functionality and porosity of biochar. Consequently, biochar may adsorb H\u003csub\u003e2\u003c/sub\u003eS thus limiting its release into the atmosphere. The carbon contents may likely be another reason, as the highest performing biocovers [biochar\u0026thinsp;=\u0026thinsp;96.2% (B-BC and SD-BC); ash\u0026thinsp;=\u0026thinsp;89.1% (CH-A)] also exhibited the highest carbon contents within the category of biochar (B-BC\u0026thinsp;=\u0026thinsp;53.7%; SD-BC\u0026thinsp;=\u0026thinsp;52.1%) and ash (CH-A\u0026thinsp;=\u0026thinsp;9.2%) for the basic biocovers. Nevertheless, the higher performance of basic biocovers with high carbon content than acidic biocovers with comparable carbon contents for H\u003csub\u003e2\u003c/sub\u003eS reduction suggests that the earlier reasoning about surface area, pH, porosity and surface functionality may better explain the observations than carbon contents.\u003c/p\u003e \u003cp\u003e \u003c/p\u003e \u003c/div\u003e \u003cdiv id=\"Sec17\" class=\"Section3\"\u003e \u003ch2\u003e3.4.2. Effect of biocovers on NH\u003csub\u003e3\u003c/sub\u003e reduction\u003c/h2\u003e \u003cp\u003eThe effect of biocovers on the suppression or inhibitions of NH\u003csub\u003e3\u003c/sub\u003e evolution from FS for each studied sampling day over the 12 days are shown in Fig.\u0026nbsp;\u003cspan refid=\"Fig5\" class=\"InternalRef\"\u003e5\u003c/span\u003ea. Generally, there seem not to be a clear trend in NH\u003csub\u003e3\u003c/sub\u003e suppression with time given the utilized biocovers. No trend consistent with pH values, C/N ratio or carbon content was found in this study. Nevertheless, contrasting results were observed for biomasses and their corresponding biochars. For instance, whilst RH-B exhibited a general gradual decline in NH\u003csub\u003e3\u003c/sub\u003e evolution with time [6th day (4.5%v/v)\u0026thinsp;\u0026lt;\u0026thinsp;9th day (1.7%v/v)\u0026thinsp;\u0026lt;\u0026thinsp;12th day (0.3%v/v)], its biochar (RH-BC) rather displayed an enhancement in NH\u003csub\u003e3\u003c/sub\u003e evolution with time [3rd day (6.3%v/v)\u0026thinsp;\u0026gt;\u0026thinsp;6th day (6.8%v/v)\u0026thinsp;\u0026gt;\u0026thinsp;9th day (8.7%v/v)]. In addition, compared to the control, the decline in NH\u003csub\u003e3\u003c/sub\u003e evolution was drastic and rapid for all sampling days over the 12 days with the application of SD-BC [3rd day (3.8%v/v); 6th day (1.8%v/v); 9th day (1.3%v/v); 12th day (0.2%v/v)]. A similar observation was also seen for the SD-BC precursor (SD-B) except on day 6; where a heightened NH\u003csub\u003e3\u003c/sub\u003e evolution rather occurred.\u003c/p\u003e \u003cp\u003eThe results of the overall percentage reduction in NH\u003csub\u003e3\u003c/sub\u003e over the entire study period of 12 days are shown in Fig.\u0026nbsp;\u003cspan refid=\"Fig5\" class=\"InternalRef\"\u003e5\u003c/span\u003eb. It is evident that majority of the acidic biocovers reduced the emission of NH\u003csub\u003e3\u003c/sub\u003e much better than the basic materials. In fact, except for SD-BC, all basic biocovers were not just extremely poor at attenuating NH\u003csub\u003e3\u003c/sub\u003e, but rather facilitated its release when compared to the control sample; by 58% (B-BC), 1.8% (RH-BC), 68.7% (C\u003csub\u003eN\u003c/sub\u003eH-A) and 49.1% (CH-A). Conversely, however, except for M-B, the acidic biocovers were good attenuators of NH\u003csub\u003e3\u003c/sub\u003e evolution. Particularly, RH-B (64.8%) was the most effective amongst the acidic biocovers at attenuating NH\u003csub\u003e3\u003c/sub\u003e evolution, followed by NS-B (17.4%) and SD-B (12.5%). Interestingly, not only was SD-BC the only effective biocover amongst the basic biocovers, it was also the most effective (74.7%) amongst all the investigated biocovers in this study in attenuating NH\u003csub\u003e3\u003c/sub\u003e evolution. According to Atia et al. (2004) the application of the biocovers reduces emissions of NH\u003csub\u003e3\u003c/sub\u003e and other odorous gases in two ways: (1) physically limiting the emissions of NH\u003csub\u003e3\u003c/sub\u003e and other gases; (2) creating a biologically active zone on the top of the covers where the emitted NH\u003csub\u003e3\u003c/sub\u003e and other gases are aerobically decomposed by microorganisms. The effectiveness of different covers or odour-reducing material in mitigating H\u003csub\u003e2\u003c/sub\u003eS and NH\u003csub\u003e3\u003c/sub\u003e emissions vary and it is also dependent on the quantity of the materials added as a cover. In theory, the effective suppression of odour is influenced by the pH which creates an unfavourable environment for microbial growth, and the physical masking ability of the additives (Arogo et al. 2001, Atia et al. 2004).\u003c/p\u003e \u003cp\u003e \u003c/p\u003e \u003cp\u003e \u003cem\u003e3.5. Statistical analysis of the effect of biocover type and duration of application on the suppression of odour from FS\u003c/em\u003e \u003c/p\u003e \u003cp\u003eThe results of the applied statistical analytical tools generated by Microsoft\u0026reg; Excel are shown in Table\u0026nbsp;\u003cspan refid=\"Tab3\" class=\"InternalRef\"\u003e3\u003c/span\u003e. From the two-way ANOVA, the computed \u003cem\u003eF\u003c/em\u003e values for the source of the variations [biocover source\u0026thinsp;=\u0026thinsp;3.78 (H\u003csub\u003e2\u003c/sub\u003eS), 3.39 (NH\u003csub\u003e3\u003c/sub\u003e); duration of application\u0026thinsp;=\u0026thinsp;5.04 (H\u003csub\u003e2\u003c/sub\u003eS), 4.76 (NH\u003csub\u003e3\u003c/sub\u003e)] were all, greater than that of the \u003cem\u003eF crit\u003c/em\u003e values (2.36 for biocover source; 3.01 for the duration of application). In addition, the \u003cem\u003eP-values\u003c/em\u003e were lower than the level of significance at 0.05. From the aforementioned results, it was evident that the effects of the independent variables (biocover source and duration of application) on the suppression of both H\u003csub\u003e2\u003c/sub\u003eS and NH\u003csub\u003e3\u003c/sub\u003e evolution were statistically significant. These deductions were made based on two criteria: \u003cem\u003eF\u003c/em\u003e value and the \u003cem\u003eP-value\u003c/em\u003e. Values of \u003cem\u003eF\u003c/em\u003e greater than reference \u003cem\u003eF crit\u003c/em\u003e, and \u003cem\u003eP-values\u003c/em\u003e lesser than the set level of significance at 0.05 (95% confidence limit) are indicative of a significant contribution to the variation by the group under investigation. Also, it was evident from the one-way ANOVA that variations in the means between the biocover type (biomass, biochar, ash) were statistically significant for H\u003csub\u003e2\u003c/sub\u003eS [\u003cem\u003eF\u003c/em\u003e (26.34)\u0026thinsp;\u0026gt;\u0026thinsp;\u003cem\u003eF crit\u003c/em\u003e (5.148); \u003cem\u003eP-value\u003c/em\u003e (0.0011)\u0026thinsp;\u0026lt;\u0026thinsp;0.05] and insignificant for NH\u003csub\u003e3\u003c/sub\u003e [\u003cem\u003eF\u003c/em\u003e (1.956)\u0026thinsp;\u0026lt;\u0026thinsp;\u003cem\u003eF crit\u003c/em\u003e (5.148); \u003cem\u003eP-value\u003c/em\u003e (0.223)\u0026thinsp;\u0026gt;\u0026thinsp;0.05]. Consequently, for the H\u003csub\u003e2\u003c/sub\u003eS, Tuker-Kramer multiple comparison test was used to evaluate which pair or combination of biocover type was the source of the variations for suppression of H\u003csub\u003e2\u003c/sub\u003eS evolution from FS. Clearly, the significant variations arose with biomass (low pH) and biochar/ash (higher pH) pairs suggesting that for effective H\u003csub\u003e2\u003c/sub\u003eS suppression, the pH of the biocovers is essential.\u003c/p\u003e \u003cp\u003e \u003cdiv class=\"gridtable\"\u003e\u003ctable float=\"Yes\" id=\"Tab3\" border=\"1\"\u003e \u003ccaption language=\"En\"\u003e \u003cdiv class=\"CaptionNumber\"\u003eTable 3\u003c/div\u003e \u003cdiv class=\"CaptionContent\"\u003e \u003cp\u003eResults of the applied statistical analysis tools for the interpretation of odour suppression data (%)\u003c/p\u003e \u003c/div\u003e \u003c/caption\u003e \u003ccolgroup cols=\"12\"\u003e \u003cthead\u003e \u003ctr\u003e \u003cth align=\"left\" colspan=\"12\" nameend=\"c12\" namest=\"c1\"\u003e \u003cp\u003eTwo-way ANOVA without replication\u003c/p\u003e \u003c/th\u003e \u003c/tr\u003e \u003c/thead\u003e \u003ctbody\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\" morerows=\"1\" rowspan=\"2\"\u003e \u003cp\u003e\u003cem\u003eSource of Variation\u003c/em\u003e\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colspan=\"3\" nameend=\"c5\" namest=\"c3\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colspan=\"4\" nameend=\"c9\" namest=\"c6\"\u003e \u003cp\u003eH\u003csub\u003e2\u003c/sub\u003eS suppression\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c10\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c12\" namest=\"c11\"\u003e \u003cp\u003eNH\u003csub\u003e3\u003c/sub\u003e suppression\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003e\u003cem\u003edf\u003c/em\u003e\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"3\" nameend=\"c5\" namest=\"c3\"\u003e \u003cp\u003e\u003cem\u003eF crit\u003c/em\u003e\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c7\" namest=\"c6\"\u003e \u003cp\u003e\u003cem\u003eF\u003c/em\u003e\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c9\" namest=\"c8\"\u003e \u003cp\u003e\u003cem\u003eP-value\u003c/em\u003e\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c10\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colname=\"c11\"\u003e \u003cp\u003e\u003cem\u003eF\u003c/em\u003e\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c12\"\u003e \u003cp\u003e\u003cem\u003eP-value\u003c/em\u003e\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e \u003cp\u003eBiocover source\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003e8\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"3\" nameend=\"c5\" namest=\"c3\"\u003e \u003cp\u003e2.36\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c7\" namest=\"c6\"\u003e \u003cp\u003e3.78 (S)\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c9\" namest=\"c8\"\u003e \u003cp\u003e0.0058\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c10\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colname=\"c11\"\u003e \u003cp\u003e3.39 (S)\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c12\"\u003e \u003cp\u003e0.0097\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e \u003cp\u003eDuration of application\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003e3\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"3\" nameend=\"c5\" namest=\"c3\"\u003e \u003cp\u003e3.01\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c7\" namest=\"c6\"\u003e \u003cp\u003e5.04 (S)\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c9\" namest=\"c8\"\u003e \u003cp\u003e0.0075\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c10\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colname=\"c11\"\u003e \u003cp\u003e4.76 (S)\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c12\"\u003e \u003cp\u003e0.0096\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colspan=\"12\" nameend=\"c12\" namest=\"c1\"\u003e \u003cp\u003eOne-way ANOVA\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003e\u003cem\u003edf\u003c/em\u003e\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"3\" nameend=\"c5\" namest=\"c3\"\u003e \u003cp\u003e\u003cem\u003eF crit\u003c/em\u003e\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c7\" namest=\"c6\"\u003e \u003cp\u003e\u003cem\u003eF\u003c/em\u003e\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c9\" namest=\"c8\"\u003e \u003cp\u003e\u003cem\u003eP-value\u003c/em\u003e\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c10\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colname=\"c11\"\u003e \u003cp\u003e\u003cem\u003eF\u003c/em\u003e\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c12\"\u003e \u003cp\u003e\u003cem\u003eP-value\u003c/em\u003e\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e \u003cp\u003eBetween the groups of biocover type\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c2\"\u003e \u003cp\u003e2\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"3\" nameend=\"c5\" namest=\"c3\"\u003e \u003cp\u003e5.143\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c7\" namest=\"c6\"\u003e \u003cp\u003e26.34 (S)\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c9\" namest=\"c8\"\u003e \u003cp\u003e0.0011\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c10\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colname=\"c11\"\u003e \u003cp\u003e1.956 (NS)\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c12\"\u003e \u003cp\u003e0.223\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colspan=\"12\" nameend=\"c12\" namest=\"c1\"\u003e \u003cp\u003eTukey-Kramer multiple comparison test results on the effect of biocover type on overall odour suppression efficiency\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\" morerows=\"2\" rowspan=\"3\"\u003e \u003cp\u003eTukey-Kramer multiple\u003c/p\u003e \u003cp\u003ecomparison\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"11\" nameend=\"c12\" namest=\"c2\"\u003e \u003cp\u003eBiocover type\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colspan=\"5\" nameend=\"c6\" namest=\"c2\"\u003e \u003cp\u003eH\u003csub\u003e2\u003c/sub\u003eS suppression (C.R. = 4.339)\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c8\" namest=\"c7\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colspan=\"4\" nameend=\"c12\" namest=\"c9\"\u003e \u003cp\u003eNH\u003csub\u003e3\u003c/sub\u003e suppression (C.R.= n.a.)\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c3\" namest=\"c2\"\u003e \u003cp\u003eBiomass\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003eBiochar\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c6\" namest=\"c5\"\u003e \u003cp\u003eAsh\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c8\" namest=\"c7\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c10\" namest=\"c9\"\u003e \u003cp\u003eBiomass\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c11\"\u003e \u003cp\u003eBiochar\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c12\"\u003e \u003cp\u003eAsh\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e \u003cp\u003eBiomass\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c3\" namest=\"c2\"\u003e \u003cp\u003eX\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e9.68 (S)\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c6\" namest=\"c5\"\u003e \u003cp\u003e6.82 (S)\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c8\" namest=\"c7\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c10\" namest=\"c9\"\u003e \u003cp\u003e-\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c11\"\u003e \u003cp\u003e-\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c12\"\u003e \u003cp\u003e-\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e \u003cp\u003eBiochar\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c3\" namest=\"c2\"\u003e \u003cp\u003e-\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003eX\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c6\" namest=\"c5\"\u003e \u003cp\u003e1.63 (NS)\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c8\" namest=\"c7\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c10\" namest=\"c9\"\u003e \u003cp\u003e-\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c11\"\u003e \u003cp\u003e-\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c12\"\u003e \u003cp\u003e-\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003ctr\u003e \u003ctd align=\"left\" colname=\"c1\"\u003e \u003cp\u003eAsh\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c3\" namest=\"c2\"\u003e \u003cp\u003e-\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c4\"\u003e \u003cp\u003e-\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c6\" namest=\"c5\"\u003e \u003cp\u003eX\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c8\" namest=\"c7\"\u003e\u0026nbsp;\u003c/td\u003e \u003ctd align=\"left\" colspan=\"2\" nameend=\"c10\" namest=\"c9\"\u003e \u003cp\u003e-\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c11\"\u003e \u003cp\u003e-\u003c/p\u003e \u003c/td\u003e \u003ctd align=\"left\" colname=\"c12\"\u003e \u003cp\u003e-\u003c/p\u003e \u003c/td\u003e \u003c/tr\u003e \u003c/tbody\u003e \u003c/colgroup\u003e \u003ctfoot\u003e \u003ctr\u003e\u003ctd colspan=\"12\"\u003e\u003cb\u003eNB\u003c/b\u003e: Biocover source = (NS-B, M-B, RH-B, SD-B, B-BC, RH-BC, SD-BC, C\u003csub\u003eN\u003c/sub\u003eH-A, CH-A); Biocover type = (biomass, biochar, ash); duration of experiment, days = (3, 6, 9, 12); C.R. = critical range; \u003cem\u003edf\u003c/em\u003e\u0026thinsp;=\u0026thinsp;degree of freedom; \u003cem\u003eF\u0026thinsp;=\u003c/em\u003e\u0026thinsp;determined from experimental data using the \u003cem\u003eF-\u003c/em\u003etest; \u003cem\u003eF crit\u003c/em\u003e\u0026thinsp;=\u0026thinsp;\u003cem\u003eF\u003c/em\u003e statistic obtained from the \u003cem\u003eF\u003c/em\u003e-distribution; \u003cem\u003eP-value\u003c/em\u003e\u0026thinsp;=\u0026thinsp;probability value; S\u0026thinsp;=\u0026thinsp;significant (absolute difference between mean odour suppression efficiencies is significant); NS\u0026thinsp;=\u0026thinsp;not significant (absolute difference between mean odour suppression efficiencies is not significant); n.a. = not applicable.\u003c/td\u003e\u003c/tr\u003e \u003c/tfoot\u003e \u003c/table\u003e\u003c/div\u003e \u003c/p\u003e \u003c/div\u003e \u003c/div\u003e"},{"header":"4. Conclusions","content":"\u003cp\u003eOdour levels, assessed with H\u003csub\u003e2\u003c/sub\u003eS and NH\u003csub\u003e3\u003c/sub\u003e as indicators, in the two public latrines were above the perceptible threshold for humans and peaked in the mornings and evenings. Comparing the odour-causing substances, H\u003csub\u003e2\u003c/sub\u003eS and NH\u003csub\u003e3,\u003c/sub\u003e only the former was above the threshold of unbearableness/annoyance to humans in the toilets investigated. Biocovers of biomass, biochar and ash origins were also successfully produced and utilized as potential inhibitors of odour-evolution from fresh FS generated in dry sanitation toilets in this study. Characterization studies showed that the pH of biomasses was lower (acidic) than that of the biochars and ashes; which were basic. Odour-suppression results showed that generally, high pH biocovers were more effective at suppressing H\u003csub\u003e2\u003c/sub\u003eS, whereas low pH biocovers were more effective at suppressing NH\u003csub\u003e3\u003c/sub\u003e evolution from FS. The per cent H\u003csub\u003e2\u003c/sub\u003eS and NH\u003csub\u003e3\u003c/sub\u003e reduction values were the highest for biocover from sawdust biochar; 96.2% and 74.7%, respectively. These results suggest that waste and readily available resources such as sawdust biomass, when converted to biochar, can serve as an effective tool to attenuate odour evolution from fresh faecal sludge in dry sanitation public toilets.\u003c/p\u003e"},{"header":"Declarations","content":"\u003cp\u003e\u003cstrong\u003e\u003cem\u003eAcknowledgements and Funding\u003c/em\u003e\u003c/strong\u003e\u003c/p\u003e\n\u003cp\u003eAuthors would like to acknowledge and thank the Regional Water and Environmental Sanitation Centre Kumasi (RWESCK) at the Kwame Nkrumah University of Science and Technology, Kumasi for fully funding this research work with funds from the Ghana Government through the World Bank Africa Centres of Excellence project.\u0026nbsp;\u003c/p\u003e\n\u003cp\u003e\u003cstrong\u003e\u003cem\u003eAvailability of data and materials\u003c/em\u003e\u003c/strong\u003e\u003c/p\u003e\n\u003cp\u003eAuthors declare that data can be available upon request from the corresponding author\u003c/p\u003e\n\u003cp\u003e\u003cstrong\u003e\u003cem\u003eContributions\u003c/em\u003e\u003c/strong\u003e\u003c/p\u003e\n\u003cp\u003e\u003cstrong\u003eConceptualization\u003c/strong\u003e: Sampson Oduro-Kwarteng, Esi Awuah; \u003cstrong\u003eMethodology\u003c/strong\u003e: Bernice Mawumenyo Senanu, Sampson Oduro-Kwarteng, Esi Awuah; \u003cstrong\u003eFormal analysis and investigation\u003c/strong\u003e: Bernice Mawumenyo Senanu; \u003cstrong\u003eWriting - original draft preparation\u003c/strong\u003e: Bernice Mawumenyo Senanu, Sampson Oduro-Kwarteng, Patrick Boakye; \u003cstrong\u003eWriting - review and editing\u003c/strong\u003e: Patrick Boakye, Divine Damertey Sewu, Peter Appiah Obeng, Kobina Afful; \u003cstrong\u003eFunding acquisition\u003c/strong\u003e: Sampson Oduro-Kwarteng; \u003cstrong\u003eResources\u003c/strong\u003e: Sampson Oduro-Kwarteng, Esi Awuah; \u003cstrong\u003eSupervision\u003c/strong\u003e: Sampson Oduro-Kwarteng, Esi Awuah.\u003c/p\u003e\n\u003cp\u003e\u003cstrong\u003e\u003cem\u003eEthics approval\u0026nbsp;\u003c/em\u003e\u003c/strong\u003e\u003c/p\u003e\n\u003cp\u003eNot applicable\u003c/p\u003e\n\u003cp\u003e\u003cstrong\u003e\u003cem\u003eConsent to participate\u003c/em\u003e\u003c/strong\u003e\u003c/p\u003e\n\u003cp\u003eAll authors confirm participatory consent\u0026nbsp;\u003c/p\u003e\n\u003cp\u003e\u003cstrong\u003e\u003cem\u003eConsent for publication\u003c/em\u003e\u003c/strong\u003e\u003c/p\u003e\n\u003cp\u003eAll authors accept to publishing in this journal\u003c/p\u003e\n\u003cp\u003e\u003cstrong\u003e\u003cem\u003eConflict of interest\u003c/em\u003e\u003c/strong\u003e\u003c/p\u003e\n\u003cp\u003eThe authors declare no competing interests\u003c/p\u003e"},{"header":"References","content":"\u003col\u003e\n \u003cli\u003eAfful K, Oduro-Kwarteng S, Antwi EO, Awuah E (2016): Odour Impact Determination of a Communal Toilet: Field Measurement with Panellists Using Dynamic Plume Method and Dispersion Modelling. 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Waste Manage. 32, 317-326\u003c/li\u003e\n\u003c/ol\u003e"}],"fulltextSource":"","fullText":"","funders":[],"hasAdminPriorityOnWorkflow":false,"hasManuscriptDocX":true,"hasOptedInToPreprint":true,"hasPassedJournalQc":"","hasAnyPriority":false,"hideJournal":false,"highlight":"","institution":"","isAcceptedByJournal":true,"isAuthorSuppliedPdf":false,"isDeskRejected":"","isHiddenFromSearch":false,"isInQc":false,"isInWorkflow":false,"isPdf":false,"isPdfUpToDate":true,"isWithdrawnOrRetracted":false,"journal":{"display":true,"email":"[email protected]","identity":"scientific-reports","isNatureJournal":false,"hasQc":true,"allowDirectSubmit":false,"externalIdentity":"scirep","sideBox":"Learn more about [Scientific Reports](http://www.nature.com/srep/)","snPcode":"","submissionUrl":"","title":"Scientific Reports","twitterHandle":"","acdcEnabled":true,"dfaEnabled":true,"editorialSystem":"stoa","reportingPortfolio":"Scientific Reports","inReviewEnabled":true,"inReviewRevisionsEnabled":true},"keywords":"ammonia, biocover, biochars, dry sanitation, hydrogen sulphide, odour removal","lastPublishedDoi":"10.21203/rs.3.rs-659004/v1","lastPublishedDoiUrl":"https://doi.org/10.21203/rs.3.rs-659004/v1","license":{"name":"CC BY 4.0","url":"https://creativecommons.org/licenses/by/4.0/"},"manuscriptAbstract":"\u003cp\u003eOn-site dry sanitation facilities, although cheaper than wet sanitation systems, suffer from high malodour and insect nuisance as well as poor aesthetics. The high odour deters users from utilizing dry sanitation toilet as an improved facility leading to over 20% open defecation in Sub-Saharan Africa. To address this malodour concern, this study first assessed odour levels, using hydrogen sulphide (H\u003csub\u003e2\u003c/sub\u003eS) and ammonia (NH\u003csub\u003e3\u003c/sub\u003e) as indicators, on two (2) dry sanitation facilities (T1 and T2). The potential of using biomass (sawdust, rice husk, moringa leaves, neem seeds), ash (coconut husk, cocoa husk) or biochar (sawdust, rice husk, bamboo) as biocovers to remove or suppress odour from fresh faecal sludge (FS) over a 12-day period was investigated. Results showed high odour levels, beyond and below the threshold limit for unpleasantness for humans on H\u003csub\u003e2\u003c/sub\u003eS (peak value: T1 = 3.17 ppm; T2 = 0.22 ppm \u0026gt; 0.05 ppm limit) and NH\u003csub\u003e3 \u003c/sub\u003e(peak value: T1 = 6.88 ppm; T2 = 3.16 ppm \u0026lt; 30 ppm limit), respectively. The biomasses exhibited low pH (acidic = 5-7) whereas the biochars and ashes had higher pHs (basic = 8-13). Acidic biocovers generally reduced NH\u003csub\u003e3 \u003c/sub\u003eemission significantly (12.5% to 64.8%) whereas basic biocovers were more effective at H\u003csub\u003e2\u003c/sub\u003eS emission reduction (80.9% to 96.2%). In terms of H\u003csub\u003e2\u003c/sub\u003eS and NH\u003csub\u003e3\u003c/sub\u003e removal, sawdust biochar was the most effective biocover with odour abatement values of 96.2% and 74.7%, respectively. The results suggest that locally available waste plant-based materials, like sawdust, when converted to biochar can serve as a cost-effective and sustainable way to effectively combat odour-related issues associated with dry sanitation facilities to help stop open defecation.\u003c/p\u003e","manuscriptTitle":"Inhibition of Ammonia and Hydrogen Sulphide Using Plant Waste Materials for Faecal Sludge Odour Control in Dry Sanitation Toilet Facilities","msid":"","msnumber":"","nonDraftVersions":[{"code":1,"date":"2021-07-09 14:18:00","doi":"10.21203/rs.3.rs-659004/v1","editorialEvents":[{"type":"communityComments","content":0},{"type":"decision","content":"Major revision","date":"2021-07-27T09:09:09+00:00","index":"","fulltext":""},{"type":"editorInvitedReview","content":"","date":"2021-07-26T07:07:34+00:00","index":"hide","fulltext":""},{"type":"reviewerAgreed","content":"71f383c3-9316-4c95-b2ae-69c923cc365c","date":"2021-07-10T17:33:21+00:00","index":"hide","fulltext":""},{"type":"reviewersInvited","content":"","date":"2021-07-10T12:33:42+00:00","index":"","fulltext":""},{"type":"editorAssigned","content":"","date":"2021-07-10T12:28:03+00:00","index":"","fulltext":""},{"type":"editorInvited","content":"","date":"2021-07-07T11:56:46+00:00","index":"","fulltext":""},{"type":"checksComplete","content":"","date":"2021-07-07T11:42:56+00:00","index":"","fulltext":""},{"type":"submitted","content":"Scientific Reports","date":"2021-06-25T16:53:04+00:00","index":"","fulltext":""}],"status":"published","journal":{"display":true,"email":"[email protected]","identity":"scientific-reports","isNatureJournal":false,"hasQc":true,"allowDirectSubmit":false,"externalIdentity":"scirep","sideBox":"Learn more about [Scientific Reports](http://www.nature.com/srep/)","snPcode":"","submissionUrl":"","title":"Scientific Reports","twitterHandle":"","acdcEnabled":true,"dfaEnabled":true,"editorialSystem":"stoa","reportingPortfolio":"Scientific Reports","inReviewEnabled":true,"inReviewRevisionsEnabled":true}}],"origin":"","ownerIdentity":"ab9d47a9-beff-4977-b3d9-174be17ebd54","owner":[],"postedDate":"July 9th, 2021","published":true,"recentEditorialEvents":[],"rejectedJournal":[],"revision":"","amendment":"","status":"under-review","subjectAreas":[{"id":5599332,"name":"Environmental Engineering"},{"id":5599333,"name":"Health Economics \u0026 Outcomes Research"}],"tags":[],"updatedAt":"2021-08-18T05:29:09+00:00","versionOfRecord":[],"versionCreatedAt":"2021-07-09 14:18:00","video":"","vorDoi":"","vorDoiUrl":"","workflowStages":[]},"version":"v1","identity":"rs-659004","journalConfig":"researchsquare"},"__N_SSP":true},"page":"/article/[identity]/[[...version]]","query":{"redirect":"/article/rs-659004","identity":"rs-659004","version":["v1"]},"buildId":"_2-kVJe1T_tPrBINL-cwx","isFallback":false,"isExperimentalCompile":false,"dynamicIds":[84888],"gssp":true,"scriptLoader":[]}

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