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 <!DOCTYPE article PUBLIC "-//NLM//DTD JATS (Z39.96) Journal Publishing DTD v1.0 20120330//EN" "http://jats.nlm.nih.gov/publishing/1.0/JATS-journalpublishing1.dtd"> <article xmlns:mml="http://www.w3.org/1998/Math/MathML" xmlns:xlink="http://www.w3.org/1999/xlink" xmlns:xsi="http://www.w3.org/2001/XMLSchema-instance" article-type="Research-article" dtd-version="1.0" xml:lang="en">
  <front>
    <journal-meta>
      <journal-id journal-id-type="publisher-id">JNDC</journal-id>
      <journal-title-group>
        <journal-title>Journal of New Developments in Chemistry</journal-title>
      </journal-title-group>
      <issn pub-type="epub">2377-2549</issn>
      <publisher>
        <publisher-name>Open Access Pub</publisher-name>
        <publisher-loc>United States</publisher-loc>
      </publisher>
    </journal-meta>
    <article-meta>
      <article-id pub-id-type="publisher-id">JNDC-19-2701</article-id>
      <article-id pub-id-type="doi">10.14302/issn.2377-2549.jndc-19-2701</article-id>
      <article-categories>
        <subj-group>
          <subject>Research-article</subject>
        </subj-group>
      </article-categories>
      <title-group>
        <article-title>Assessing Performance of Cattle Dung and Waste Cooked Foods in Producing Biogas as Single Substrate and Mixed Substrates in Kampala Uganda</article-title>
      </title-group>
      <contrib-group>
        <contrib contrib-type="author">
          <name>
            <surname>Mutesasira,</surname>
            <given-names>J</given-names>
          </name>
          <xref ref-type="aff" rid="idm1841840724">1</xref>
          <xref ref-type="corresp" rid="cor1">*</xref>
        </contrib>
        <contrib contrib-type="author">
          <name>
            <surname>Mukasa-Tebandeke,</surname>
            <given-names>I.Z</given-names>
          </name>
          <xref ref-type="aff" rid="idm1841931924">2</xref>
        </contrib>
        <contrib contrib-type="author">
          <name>
            <surname>Wasajja,</surname>
            <given-names>HZ</given-names>
          </name>
          <xref ref-type="aff" rid="idm1841930556">3</xref>
        </contrib>
        <contrib contrib-type="author">
          <name>
            <surname>Nankinga,</surname>
            <given-names>R</given-names>
          </name>
          <xref ref-type="aff" rid="idm1841930556">3</xref>
        </contrib>
      </contrib-group>
      <aff id="idm1841840724">
        <label>1</label>
        <addr-line>External studies department, Institute of distance Education, Makerere University</addr-line>
      </aff>
      <aff id="idm1841931924">
        <label>2</label>
        <addr-line>Chemistry Department, School of Physical Sciences, Makerere University</addr-line>
      </aff>
      <aff id="idm1841930556">
        <label>3</label>
        <addr-line>Departments of Earth Sciences, Wesleyan University, Connecticut USA</addr-line>
      </aff>
      <contrib-group>
        <contrib contrib-type="editor">
          <name>
            <surname>Yujia</surname>
            <given-names>Liang</given-names>
          </name>
          <xref ref-type="aff" rid="idm1841686852">1</xref>
        </contrib>
      </contrib-group>
      <aff id="idm1841686852">
        <label>1</label>
        <addr-line>University of Maryland, College Park, MD, USA.</addr-line>
      </aff>
      <author-notes>
        <corresp id="cor1">Correspondence: J. Mutesasira, External Studies Department, Institute of Distance Education, Makerere University, Uganda; Email: <email>ishamukasa@cns.amk.ac.ug</email>; <email>mukasatz@gmail.com</email>.</corresp>
        <fn fn-type="conflict" id="idm1843599932">
          <p>The authors have declared that no competing interests exist.</p>
        </fn>
      </author-notes>
      <pub-date pub-type="epub" iso-8601-date="2019-04-12">
        <day>12</day>
        <month>4</month>
        <year>2019</year>
      </pub-date>
      <volume>2</volume>
      <issue>2</issue>
      <fpage>29</fpage>
      <lpage>38</lpage>
      <history>
        <date date-type="received">
          <day>05</day>
          <month>03</month>
          <year>2019</year>
        </date>
        <date date-type="accepted">
          <day>02</day>
          <month>04</month>
          <year>2019</year>
        </date>
      </history>
      <permissions>
        <copyright-statement>© </copyright-statement>
        <copyright-year>2019</copyright-year>
        <copyright-holder>Mutesasira, J, et al.</copyright-holder>
        <license xlink:href="http://creativecommons.org/licenses/by/4.0/" xlink:type="simple">
          <license-p>This is an open-access article distributed under the terms of the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original author and source are credited.</license-p>
        </license>
      </permissions>
      <self-uri xlink:href="http://openaccesspub.org/jndc/article/1062">This article is available from http://openaccesspub.org/jndc/article/1062</self-uri>
      <abstract>
        <p>Biogas is anaerobic degradation product formed from aqueous slurry of organic waste in a digester. It can be produced from cattle dung,(cd)chicken droppings, decaying leaves, kitchen waste foods(kwf), sewage sludge, slaughter house, goat, pig or sheep manure, Aqueous slurry of 200g/L of mixed or single substrate of cattle dung or/and kitchen waste evolved up to 400mL of biogas at ambient temperatures.  The rate of gas evolution reached 5mL/day on the 15<sup>th</sup> day using 25% cd mixed slurry.  The rates of degradation attained in the mixtures were 1.42ml/g for cd; 1.58mL/g for kwf; 1.78mL/g for 75% cd mixed substrate; 1.78mL/g for 50% cd mixed substrate; 1.92mL/g for 25% cd mixed substrate slurries. The comparative rate of biogas formation ranged from1.25 to 1.35 which was in agreement with the range published in literature of 0.8 to 5.5. Biogas can be synthesized efficiently at ambient temperature in Kampala as was done at mesophilic temperatures elsewhere. However, it may be necessary to attempt producing biogas at different pH and temperatures as well as using other substrates and inoculums.</p>
      </abstract>
      <kwd-group>
        <kwd>Substrate</kwd>
        <kwd>co-generation</kwd>
        <kwd>digester</kwd>
        <kwd>cattle dung</kwd>
        <kwd>bio-waste</kwd>
        <kwd>kitchen waste</kwd>
      </kwd-group>
      <counts>
        <fig-count count="4"/>
        <table-count count="0"/>
        <page-count count="10"/>
      </counts>
    </article-meta>
  </front>
  <body>
    <sec id="idm1841682244" sec-type="intro">
      <title>Introduction</title>
      <p>Biogas was defined as gas formed by biological decomposition of organic matter in absence of oxygen and it originates from biogenic materials so it is a biofuel. Interest in synthesis of gas formed by decomposing organic matter was first reported in the 17<sup>th</sup> century. Later it was found that gas produced from cattle manure and kitchen waste can be used for lighting and cooking in much the same as natural gas is used. It is now known that it contains up to 50% methane, a renewable source of energy that can be used for heating, generating electricity and other operations based on internal combustion engines <xref ref-type="bibr" rid="ridm1842704140">1</xref>.  Biogas was reported as mixture of gases including methane, carbon dioxide, hydrogen and others <xref ref-type="bibr" rid="ridm1842704788">2</xref><xref ref-type="bibr" rid="ridm1842786324">3</xref><xref ref-type="bibr" rid="ridm1842777900">4</xref>. Whereas kitchen waste is any substance raw or cooked which is discharged or remains after <xref ref-type="bibr" rid="ridm1842558516">5</xref> cattle dung is                          black-greenish material that passes out of the rumen of herbivores after feeding on grass and other                   materials <xref ref-type="bibr" rid="ridm1842557580">6</xref>.  It was reported that digestion of kitchen waste as single substrate yielded 27% of gas <xref ref-type="bibr" rid="ridm1842547108">7</xref> yet cattle dung as single substrate yielded 17.9%<xref ref-type="bibr" rid="ridm1842548980">8</xref> . There are variations in quantities of gas formed when single or mixed substrates are digested <xref ref-type="bibr" rid="ridm1842541180">9</xref>.  </p>
      <p>The processes yielding biogas involve anaerobiosis whereby archaea bacteria, algae, fungi, protozoa and or viruses degrade organic matter.  Bio digestion has been employed to treat organic wastes to recover renewable <sup>10</sup><xref ref-type="bibr" rid="ridm1842537940">11</xref>. Anaerobiosis involves a series of processes in which microbes biodegrade organic materials <xref ref-type="bibr" rid="ridm1842704140">1</xref><xref ref-type="bibr" rid="ridm1842526972">12</xref>.  Synthesis of biogas can be coupled to waste management because it produces bio residue which serves a s manure and a gas suitable to replace fossil fuels <xref ref-type="bibr" rid="ridm1842525820">13</xref><xref ref-type="bibr" rid="ridm1842520564">14</xref>.   The process of bio digestion starts with bacteria hydrolyzing organic matter placed in a digester to transform insoluble organic polymers like cellulose to soluble products, on which different protozoa act <xref ref-type="bibr" rid="ridm1842525820">13</xref>.  Acetogenic bacteria convert amino acids and sugars to methane, hydrogen, carbon dioxide and ammonia <xref ref-type="bibr" rid="ridm1842514804">15</xref>.</p>
      <sec id="idm1841682028">
        <title>Flow Diagram for Biogas Formation was Summarized by Babel et al 2016 <xref ref-type="bibr" rid="ridm1842498156">16</xref> as Follows; </title>
        <fig id="idm1842543772">
          <graphic xlink:href="images/image1.jpg" mime-subtype="jpg"/>
        </fig>
        <p>The two key processes in bio digestion were reported to be mesophilic and thermophilic in nature. Further, it was shown that digesters that generate biogas from kitchen waste involve thermophilic       microbes <xref ref-type="bibr" rid="ridm1842496140">17</xref>.</p>
        <p>Cogeneration or co-digestion of biogas is simultaneous decomposition of homogeneous slurry of two or more substrates <sup>10</sup>. Cogeneration of biogas from mixed slurry of solid from slaughter house, manure, fruits and vegetables was reported to have increase the yield of methane by 44% as compared to single substrate digestion of cattle dung or kitchen waste <xref ref-type="bibr" rid="ridm1842492108">18</xref>. It was further reported that sodium hydroxide added to kitchen waste increased the yield of biogas formed <xref ref-type="bibr" rid="ridm1842490668">19</xref>. Waste food materials were shown to have high potential for the production of methane because it can be digested rapidly <xref ref-type="bibr" rid="ridm1842492108">18</xref>. Further food waste was shown to be highly desired substrate for anaerobic digestion because it accomplishes 80% of           the theoretical methane yield in 10 days of                                  digestion <xref ref-type="bibr" rid="ridm1842486492">20</xref>.  It has been shown further that fats and oils produced higher volumes of gas than other organic wastes of different biochemical composition <xref ref-type="bibr" rid="ridm1842502116">21</xref>. Fats and oils reduced organic wastes possessing higher gas potentials than sugars or alcohols <xref ref-type="bibr" rid="ridm1842469612">22</xref>. </p>
        <p>Fats and oils were degraded in high percentages in cogeneration with simulated organic fractions of municipal solid waste with result indicating anaerobic digestion of lipids <xref ref-type="bibr" rid="ridm1842502116">21</xref><xref ref-type="bibr" rid="ridm1842469612">22</xref><xref ref-type="bibr" rid="ridm1842466948">23</xref>. To alleviate expenditure on treating organic waste, it was necessary to use                         co-digestion to produce the renewable energy source in addition to manure <xref ref-type="bibr" rid="ridm1842463348">24</xref>. The volume of gas formed from such digesters fluctuates, but can be stabilized by use a variety of substrates applied simultaneously in cogeneration processes <sup>10</sup>. Sewage sludge in mixture with other substrates yielded more gas than single substrate <xref ref-type="bibr" rid="ridm1842520564">14</xref>. This has been associated with positive synergism established in the digestion medium                together with supply of missing nutrients from the                              co-substrates <sup>25</sup>. In addition to synergism, cogeneration provides a better nutrient balance for the anaerobes, so it results in high yield of gas <xref ref-type="bibr" rid="ridm1842704788">2</xref>. Thus slurry containing slaughter house manure, fruit and vegetable waste yielded even bigger volume of gas than slaughter house manure mixed with fruit                               waste <xref ref-type="bibr" rid="ridm1842514804">15</xref>. Cogeneration was shown to increase yield of biogas to 26% <xref ref-type="bibr" rid="ridm1842476668">26</xref> because it supplied additional nutrients to the anaerobes. Digestion of mixed slurry of manure and organic waste consisted of combining several wastes with complimentary characteristics                 in order to improve production of the                                         gas <xref ref-type="bibr" rid="ridm1842455212">27</xref>. Cogeneration of biogas is based on trial and error practices so different yields are obtained with different substrates but gas operators need to know the effects of cogeneration <sup>10</sup>. Food residues from homes, restaurants or hotels serve as good substrate for anaerobiosis satisfying up to 80% of the theoretical yield of methane <xref ref-type="bibr" rid="ridm1842496140">17</xref>. Cogeneration slurries containing fats, greases and oils, waste waters, manure from slaughter houses, diary industries and fat refineries have higher methane potential as fats and oils are reduced organic materials []13, 22, 23]. This study has targeted cogeneration of gas from cattle dung and kitchen waste in ratios of 1:1, 1: 3 and 3:1 in comparison to generation of gas using cattle dung and kitchen waste as single substrates.</p>
        <p>The yield of biogas was shown to be affected by type and composition of the substrate, microbial composition, temperature, moisture, bioreactor design and pH <xref ref-type="bibr" rid="ridm1842452620">28</xref>. Anaerobic digestion is catalyzed by microorganisms that convert macro molecules to low molar mass substances. The common sources of inoculums is sewage <xref ref-type="bibr" rid="ridm1842449020">29</xref>, however, all aggregates like flocs, biofilms, granules and mats may be used<xref ref-type="bibr" rid="ridm1842444772">30</xref>.  Heterotrophic organisms like <italic>clostridium</italic> species are common anaerobic digesters but a consortium of microbial like achtinmycytes,  <italic>Thermomonospis</italic><italic>Ralslsttonia</italic><italic><xref ref-type="bibr" rid="ridm1842456868">31</xref><xref ref-type="bibr" rid="ridm1842426436">32</xref></italic>.</p>
        <p>Low temperatures were reported to decrease microbial growth, rates, substrate utilization and rate of biogas formation <xref ref-type="bibr" rid="ridm1842420892">33</xref><xref ref-type="bibr" rid="ridm1842418372">34</xref>.   It also leads to exhaustion      of cell energy and leaking of intra cellular                     substances <xref ref-type="bibr" rid="ridm1842413908">35</xref>. High temperatures lower gas yield because volatile gases like ammonia are produced <xref ref-type="bibr" rid="ridm1842412828">36</xref>. The best operating temperature is 35<sup>o</sup>C, a mesophilic         temperature <xref ref-type="bibr" rid="ridm1842408796">37</xref>. Neutral to alkaline pH were reported suitable for anaerobiosis of organic waste <xref ref-type="bibr" rid="ridm1842777900">4</xref><xref ref-type="bibr" rid="ridm1842404764">38</xref>. High moisture content facilitates anaerobiosis <xref ref-type="bibr" rid="ridm1842401380">39</xref>. The availability and complexity of organic materials affect anaerobic digestion. The digester consists of pressure resistant container mounted with stirrer and reservoir. The volume of gas formed collected over sodium hydroxide solution was measured very after three-day interval for 28 days. On the 28<sup>th</sup> day, the digestion mixture was discharged. The digester was cleaned and used over again. This study has aimed at using cattle dung and cooked waste foods singly or mixed to produce biogas.</p>
      </sec>
    </sec>
    <sec id="idm1841652252" sec-type="materials">
      <title>Materials and Methods</title>
      <sec id="idm1841654124">
        <title>Sampling</title>
        <p>From a kraal (zero-grazing facility), wet cattle dung (10kg) was collected. From the same kraal, cattle urine (10L) was collected.  From the garbage dumping site, cooked waste food materials (10kg) from nearby restaurant at Wandegeya market was collected.</p>
        <sec id="idm1841653476">
          <title>Cattle Dung Digestion</title>
          <p>Wet cattle dung (50g) was put in a can and cattle urine (200ml) and sludge inoculum (50mL) was added. The mixture was stirred to form slurry. </p>
        </sec>
        <sec id="idm1841653908">
          <title>Kitchen Waste Digestion</title>
          <p>Waste food materials (50g) were put in a can and cattle urine (200ml) and sludge inoculum (50mL) was added. The mixture was stirred to form slurry.  The slurry was fed in the digester.</p>
        </sec>
      </sec>
      <sec id="idm1841653764">
        <title>Co-Digestion of Cattle Dung and Food Waste</title>
        <sec id="idm1841653116">
          <title>This was Carried out in Three Different wats as Shown Below</title>
          <p>Wet cattle dung (25g) and food waste (25g) were put in a can and cattle urine (200mL) and sludge inoculum (50mL) was added. The mixture was stirred to form slurry.  The slurry was fed in the digester and carbon dioxide bubbled through slurry to eliminate oxygen.</p>
          <p>Wet cattle dung (13g) and waste food (37g) were put in a can and cattle urine (200mL) and sludge inoculum (50mL) was added. The mixture was stirred to form a slurry.  The slurry was fed in the digester and carbon dioxide bubbled through slurry to eliminate oxygen.</p>
          <p>Wet cattle dung (37g) and waste food (13g) were put in a can and cattle urine (200mL) and sludge inoculum (50mL) was added. The mixture was stirred to form a slurry.  The slurry was fed in the digester and carbon dioxide bubbled through slurry to eliminate oxygen.</p>
        </sec>
      </sec>
      <sec id="idm1841650668">
        <title>Instrumentation</title>
        <p>The slurry was fed in the digester shown below through the reservoir while tap leading to out the effluent was open to allow air out of the reactor. Once the reservoir was nearly full, addition of slurry was stopped, carbon dioxide was bubbled through the slurry for five minutes and tap leading to the effluent was closed. The stirring started and slurry left to decompose while the electric stirrer was running. The gas formed was collected in graduated glass tube over sodium hydroxide solution to absorb carbon dioxide. (<xref ref-type="fig" rid="idm1842518932">Figure 1</xref>).</p>
        <fig id="idm1842518932">
          <label>Figure 1.</label>
          <caption>
            <title> Layout of instruments in experiment</title>
          </caption>
          <graphic xlink:href="images/image2.jpg" mime-subtype="jpg"/>
        </fig>
      </sec>
    </sec>
    <sec id="idm1841649876" sec-type="results">
      <title>Results and Discussion</title>
      <p>The volume of biogas formed by degradation of cattle dung, kitchen waste and admixtures of these two were measured and recorded using the apparatus shown in <xref ref-type="fig" rid="idm1842517708">Figure 2</xref>. Each experiment was repeated thrice and the average volume recorded over the 28 days’ period was used to plot <xref ref-type="fig" rid="idm1842517708">Figure 2</xref> below;</p>
      <fig id="idm1842517708">
        <label>Figure 2.</label>
        <caption>
          <title> Plot of volume of gas formed against time</title>
        </caption>
        <graphic xlink:href="images/image3.jpg" mime-subtype="jpg"/>
      </fig>
      <p>Production of gas from 50g of cattle dung, 50g of kitchen food waste and their admixtures in 50%, 75% and 25% cattle dung in slurry with cattle urine (200mL) and sludge inoculums yielded graphs in <xref ref-type="fig" rid="idm1842517708">Figure 2</xref> for which the coefficients of linearity were and the equations were respectively.</p>
      <p>The production of biogas started by day 3 of experiment showing that the time between set up of experiment and initial formation of gas was not utilized by the   anaerobes to act on the slurry. This has been explained as time used by the anaerobes to use up oxygen present in the slurry; and after oxygen is depleted, acid forming anaerobes became active so gas production started <xref ref-type="bibr" rid="ridm1842398644">40</xref>.</p>
      <p>Production of biogas increased steadily at first and the sharply after day 9 until it attained its peak on day 18.  When gas production had just begun, the microbes in the slurry had just become active and began increasing their population <xref ref-type="bibr" rid="ridm1842398644">40</xref>, and the microbes needed acclimatization period <xref ref-type="bibr" rid="ridm1842382804">41</xref>. The steady increase in biogas was explained by the fact that the microbes’ population was fully established in large enough numbers and were therefore progressively acting on more and more substrate as their numbers                  increased <xref ref-type="bibr" rid="ridm1842398644">40</xref>.</p>
      <p>By the time the peak production was attained, the anaerobes were acting on maximum quantity of organic matter suspended in the slurry <xref ref-type="bibr" rid="ridm1842452620">28</xref>.</p>
      <p>The drop in volume of gas formed beyond the peak may have resulted from decrease in quantity of substrate available to the microbes to act on or even shift in the balance of carbon to nitrogen ration available to the anaerobes to use <xref ref-type="bibr" rid="ridm1842382804">41</xref>. The volume of gas formed from different generating substrates varied with cattle dung yielding least yet cogeneration mixture made of 50% cattle dung produced highest volume. It was observed that after day 9, the volume gas formed from all digestion mixtures kept increasing steadily. </p>
      <p>The rate of change in volume with time in <xref ref-type="fig" rid="idm1842520876">Figure 3</xref> revealed that the higher the rate of evolution of gas was attained by the 15<sup>th</sup> day for single substrate and mixed substrate digestions. However, smaller rates of evolution of gas occurred for single substrate than for mixed substrates due to positive synergism brought about by balance of the carbon to nitrogen ratio getting closer to 30:1 <xref ref-type="bibr" rid="ridm1842382804">41</xref>. After day 15, the rate of degradation decreased due to depletion suspended ingredients.  It would therefore be recommendable that if biogas is generated for commercial needs, one needs six to seven digesters arranged in series such that thy are started one after the other after a day and left to run up to the 15<sup>th</sup> day the restarted on the 18<sup>th</sup> day by feeding the first in the same series as was done at the beginning.</p>
      <p>By comparison, the volume of biogas formed from slurry of cattle dung was less than that formed from kitchen food waste in cattle urine probably due to kitchen food waste providing a better nutrient balance for carbon to nitrogen than cattle dung which was largely lignified cellulose <xref ref-type="bibr" rid="ridm1842398644">40</xref>. The microbes survive better in media containing more nitrogen than those containing less because nitrogen is an essential element for their life.  The anaerobes metabolize organic matter with aid of enzymes reducing carbohydrates, proteins and fats to methane.   There is dependency of quantity of gas formed on the carbon to nitrogen (C/N) ratio of the slurry digested <xref ref-type="bibr" rid="ridm1842376684">43</xref>. The optimum ratio of C/N is 30:1 was reported.  The anaerobes consume carbon 30 times faster than nitrogen <xref ref-type="bibr" rid="ridm1842382804">41</xref> to convert organic waste to a renewable energy source, biogas.  The chemical composition and structure of lignocellulosic materials hinders the rate of bio digestion of slurry as hydrolysis of complex matter to soluble compounds must be the are determining or limiting step for the decomposition of the slurry with high solid content like cattle dung                       slurry <xref ref-type="bibr" rid="ridm1842452620">28</xref><xref ref-type="bibr" rid="ridm1842375100">44</xref>.</p>
      <p>Cogeneration is simultaneous generation of biogas using homogeneous slurry of two or more substrates, each of which can produce the gas if digested singly.  The results on cogeneration of biogas using slurries containing cattle dung cd and kitchen food wastes kwf in a laboratory scale digester at ambient temperatures is shown in <xref ref-type="fig" rid="idm1842520876">Figure 3</xref>.</p>
      <p>As shown on <xref ref-type="fig" rid="idm1842520876">Figure 3</xref>, the average rate of evolution biogas from aqueous slurry of cd and kwf because the combination brought together the positive characteristic of feed stocks and potentially bringing better digestion performance as well as more rapid growth of microbial population in the mixed substrate than in the single substrate <xref ref-type="bibr" rid="ridm1842398644">40</xref><xref ref-type="bibr" rid="ridm1842372148">45</xref>. </p>
      <fig id="idm1842520876">
        <label>Figure 3.</label>
        <caption>
          <title> Plot of rate of biogas formation against time</title>
        </caption>
        <graphic xlink:href="images/image4.jpg" mime-subtype="jpg"/>
      </fig>
      <p>It can be observed that very significant evolution of gas started after day 3. Evolution of biogas was slower for cd than kwf because cd slurry had higher content of lignified cellulose than kwf. Cellulose requires more time and adverse conditions to hydrolyze than ordinary carbohydrates in present kwfs. Additionally, cooking could have weakened bonds in kwfs.  So the retention time for cd was higher than for kwf <xref ref-type="bibr" rid="ridm1842366316">46</xref>. The maximum rate of volume increase biogas formed was for mixture made of 25% cd on the 15<sup>th</sup> day.  This was interpreted as showing that the slurry contained the best C/N ratio of all the samples tested <xref ref-type="bibr" rid="ridm1842382804">41</xref>. So this mixed substrate slurry containing cd and kwf approached the optimum C/N ratio of 30:1 <xref ref-type="bibr" rid="ridm1842365812">47</xref>. </p>
      <p>The average rate of decomposition expresses volume of gas formed/g of substrate digested is shown in <xref ref-type="fig" rid="idm1842498260">Figure 4</xref> below for cd, kwf and mixtures cd and kwfs <xref ref-type="fig" rid="idm1842498260">Figure 4</xref> above illustrates that when equal total masses of substrates were fed in the digesters at ambient temperatures differing mean rates of decomposition resulted because the volumes of biogas registered were different.  The cogeneration slurries showed higher average rates of decomposition than single substrate slurries of cd or kwf.  The average rate of decomposition for cd was1.42+ 0.29ml/g that for kwf was 1.58+ 0.21ml/g that made of 75% cd was 1.78+ 0.35mL/g; for 50% cd was 1.80+ 0.37mL/g and for 25% cd was 1.92+ 0.40mL/g. </p>
      <fig id="idm1842498260">
        <label>Figure 4.</label>
        <caption>
          <title> Rate of degradation in slurries containing 200g/L at ambient temperatures</title>
        </caption>
        <graphic xlink:href="images/image5.jpg" mime-subtype="jpg"/>
      </fig>
      <p>The mean rate of biogas formation for the cogeneration slurries containing cd and kwfs was obtained to be higher than for cd by the respective factors of 1.254 for 75% cd; 1.268 for 75% cd and 1.352 for 25% cd and these values lie within the range of values of enhancement that were reported to lie between 0.8 to 5.5 as compared to single substrate digestion slurries alone <xref ref-type="bibr" rid="ridm1842398644">40</xref><xref ref-type="bibr" rid="ridm1842372148">45</xref> and this brought about by synergistic tendencies whereby carbohydrates, fats and proteins simultaneously contribute to formation of biogas. </p>
    </sec>
    <sec id="idm1841707772" sec-type="conclusions">
      <title>Conclusions</title>
      <p>The average optimum amount of biogas was produced by anaerobic digestion of cd and kwf in a period of 18 days, the slurry of cd 50g/200mL yielded 275+ 2.03mL/L; kwf 50g/200mL yielded 329.2+ 5.77mL/L;  50% cd yielded329.2+ 3.10mL/L; 75% cd yielded 422.0+ 3.56 mL/L;  25% yielded  431.5+ 4.65 mL/L.</p>
      <p>The average rate of gas evolution reached 5mL/day on the 15<sup>th</sup> day using 25% cd mixed slurry.  The overall rates of degradation attained in the mixtures were 1.42 + 0.26ml/g for cd; 1.58+0.33mL/g for kwf; 1.78+ 0.38mL/g for 75% cd mixed substrate; 1.78+ 0.29 mL/g for 50% cd mixed substrate; 1.92+ 0.21 mL/g for 25% cd mixed substrate slurries in the 200g/L load. The comparative rate of biogas formation ranged from1.25 to 1.35 which was in agreement with the range published in literature of 0.8 to 5.5. </p>
      <p>Biogas can be synthesized efficiently at ambient temperatures in Kampala as was done at mesophilic temperatures elsewhere. </p>
      <p>Cd and kwf can produce significant quantities of biogas if digested anaerobically.</p>
    </sec>
    <sec id="idm1841705252">
      <title>Recommendation</title>
      <p>The digestion of slurry of single cd, kwf and mixed substrates of cd, kwf should be tested for evolution of gas at 37<sup>o</sup>C, the reported optimum temperatures.</p>
      <p>Attempts to test on the effect of pH on yield of biogas need be determined.</p>
      <p>Studies on C/N ratios for cd and kwf should be documented to assert the nutrient balance levels.</p>
      <p>However, it may be necessary to attempt producing biogas at different pH and temperatures as well as using other substrates and inoculums.</p>
    </sec>
  </body>
  <back>
    <ack>
      <p>We are indebted to Prof G.W. Nyakairu and Mr. Moses Mutenyo for the design and technical advice on the design of the bio-digester.</p>
    </ack>
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