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"Sampah organik sebagian besar berasal dari sampah makanan yang menyebabkan karakteristiknya memiliki konsentrasi nitrogen dan lemak tinggi, kelembaban tinggi. Limbah domestik di Indonesia memiliki karakteristik kandungan organik yang sesuai dengan kondisi anaerobik. Limbah minyak dan lemak dapat membantu dalam proses AD yang dijadikan sebagai ko-substrat.Penelitian ini bertujuan untuk menganalisis kinerja reaktor dry anaerobic digestion sampah makanan dan menganalisis pengaruh penambahan limbah minyak dan lemak terhadap kinerja reaktor dry anaerobic digestion. Penelitian dilakukan menggunakan Continuous Stirred Tank Reactor CSTR dengan volume terisi 400 L yang beroperasi pada suhu rata-rata 27,8 1,07oC.Penelitian operasi skenario pertama dilakukan dengan input substrat sampah makanan dengan Organic Loading Rate OLR 10 kg VS/m3 selama 43 hari dan diaduk menggunakan variasi intensitas pengadukan 30 rpm dan 60 rpm secara konstan.Operasi skenario kedua dilakukan selama 59 hari menggunakan substrat sampah makanan dan kotoran sapi banding limbah Fat Oil and Grease FOG dengan Organic Loading Rate OLR yang sama dengan skenario pertama dan diaduk menggunakan intensitas 30 rpm secara konstan.Hasil penelitian menunjukkan terdapat perbedaan yang signifikan antara input substrat sampah makanan dengan penambahan limbah minyak dan lemak.

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Organic waste mostly comes from food waste that has characteristics of high concentrations of nitrogen and fat, high humidity. Domestic waste in Indonesia has characteristics of organic content which is suitable with anaerobic conditions. Waste oil and fat can help in the process of AD which is used as co substrate.

This research is intended to analyze the performance of dry anaerobic digestion reactor of food waste and analyze the effect of oil and waste addition on dry anaerobic digestion reactor performance. The research was conducted using Continuous Stirred Tank Reactor CSTR with a volume of 400 L applied at an average temperature of 27.8 1.07oC.

The first scenario operation study was performed with food waste substrate input with Organic Loading rate OLR is 10 kg VS m3 for 43 days and stirred using constantly strirring intensity variation of 30 rpm and 60 rpm.

The second scenario operation was conducted for 59 days using food waste and cow dung substrate of Fat Oil and Grease waste FOG with Organic Loading Rate OLR which is similar to the first scenario and stirred using constant 30 rpm intensity.

The results of study showed that there was a significant difference between the input of food waste substrate with the addition of Fat Oil and Grease p."

"Organic waste mostly comes from food waste, which has characteristics of high concentrations of nitrogen and fat, and high humidity. Domestic waste in Indonesia has a high organic content, which is suitable for anaerobic conditions. Waste oil and fat can be used as co-substrates and are helpful in yielding biogas in an anaerobic digestion (AD) process. The aim of this research is to analyze the performance of a food waste dry anaerobic digestion reactor after the addition of fat oil and grease (FOG) waste. The research was conducted using a semi-continuous stirred tank reactor (SCSTR) with an active volume of 400 L, operated at an average temperature of 27.8±1.07oC. Two experimental scenarios were performed, using varying types of food waste, food waste with cow dung as substrate, and FOG waste as co-substrate. The experiment was conducted using an Organic Loading Rate (OLR) of approximately 10 kg VS/m3, with a constant mixing intensity of 30 rpm. The results show that there was a significant difference between the input of food waste substrate with and without the addition of FOG (p<0.05). The average reduction of volatile solids (VS) and chemical oxygen demand (COD) removal in the substrate input with FOG addition was higher than without the addition. The mean percentages of COD removal and VS reduction in the substrate input with FOG addition were 63.3±2.71% and 89.30±1.55%, whereas those for substrate input without FOG addition were 59.45±4% and 77.65±1.46%, respectively. The study concludes that the use of FOG as a co-substrate in a dry AD food waste reactor is not only beneficial in reducing FOG waste generation, but also has a significant impact on reducing COD and VS, which can enhance potential biogas yield."

"Penambahan substrat sampah makanan dan limbah minyak dan lemak berpotensi menghasilkan akumulasi VFA yang berdampak kepada ketidakseimbangan proses AD. Penelitian ini bertujuan untuk menentukan kesesuaian limbah minyak dan lemak dengan sampah makanan dan kotoran sapi yang dioperasikan menggunakan AD terhadap parameter kualitas efluen dengan mengidentifikasi hubungan antara akumulasi VFA dan LCFA dalam pembentukan biogas dan VSD. Penelitian ini dilakukan selama 245 hari menggunakan Continuous Stirred Tank Reactor CSTR dengan kapasitas 400 L dengan rata-rata suhu 29 0,90 C dan pH 6,2 0,71. Reaktor dioperasikan dengan Organic Loading Rate OLR 10 Kg VS/m3.2-3hari dan pengadukan 30 rpm selama 4 jam/hari. Penelitian terdiri dari tiga variasi, yang terdiri dari variasi 1 sampah makanan dan kotoran sapi dengan perbandingan 9:1, variasi 2 limbah minyak dan lemak dengan sampah makanan dan kotoran sapi dengan perbandingan 1:7, dan variasi 3 limbah minyak dan lemak dengan sampah makanan dan kotoran sapi dengan perbandingan 1:2. Pada kondisi steady state, Variasi 1 menunjukan rata-rata reduksi COD 54,24 7,11 ; VSD 75,8 6,47 ; amonia 1,17 6,74 ; dan pH 6,0 3,87. Penambahan limbah minyak dan lemak dengan variasi 2 menunjukan hasil pengujian yang berbeda secara signifikan dengan variasi 1 yang ditandai dengan uji test-T dengan tingkat kepercayaan 95. Hasil pengujian varasi 2 menunjukan rata-rata reduksi COD mencapai 57,6 6,9 ; VSD 88,9 5,49 ; amonia 1,08 11,55 ; pH 5,82 3,6 , dan rasio VFA/TA akhir proses dengan nilai 0,36 yang menunjukan proses AD berjalan stabil dan tidak ada akumulasi VFA dan LCFA. Sedangkan variasi 3 lebih efisien dalam mengolah limbah minyak dan lemak menggunakan reaktor AD sampah makanan yang dibuktikan dengan reduksi COD diatas 50 dengan range 52,21 ndash; 68,27, rata-rata VSD 93,46, rasio VFA/TA akhir proses 0,69 yang menunjukan ada beberapa ketidakstabilan akan terjadi pada proses AD, akan tetapi, tetap tidak terjadi akumulasi VFA pada dan LCFA pada variasi 3, serta menghasilkan volume biogas tertinggi hingga 980 L/hari.

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The addition of food waste substrate and waste oils and fats has the potential to produce VFA accumulation which has an impact on the imbalance of the AD process. This research was aimed to determine the suitability between of fat, oil, and grease FOG wastes, and food waste and cow mannure that was operated using AD on effluent quality parameter by identifying the relationship between VFA and LCFA accumulation in the formation of biogas and VSD. This research was conducted for 245 days used Continuous Stirred Tank Reactor CSTR with it area of capacity 400 by its averages temperature and pH, were 29 0,90 C and pH 6,2 0,71, respectively. To operate the reactor using Organic Loading Rate OLR 10 Kg VS m3.2 3day and steering 30 rpm for 4 hours day. The study consisted of three variations, consisting of variation 1 food waste and cow mannure in the ratio of 9 1 , variation 2 waste of fat, oil, and grease with food waste and cow mannure in the ratio of 1 7 , and variation 3 waste of fat, oil, and grease with food waste and cow mannure with a ratio of 1 2. In steady state conditions, Variation 1 shows the average COD reduction reached 54,24 7,11 VSD 75.81 6,47 ammonia 1,17 6,74 and pH 6,0 3,87, respectively. The addition of FOG waste with variation 2 have significantly different test results with variation 1 characterized by a test T with a 95 confidence level. The test results of variation 2 obtained that the average reduction of COD reached 57,6 6,9 VSD 88,9 5,49 ammonia 1,08 11,55 pH 5,82 3,6, and a final process VFA TA ratio of 0,36 indicating that the AD process is stable and there is no accumulation of VFA and LCFA, respectively. While the addition of FOG waste variation 3 more efficient in treating FOG waste using AD reagent food waste as evidenced by the reduction of COD above 50 with a range of 52.21 68.27 and average VSD 93.46, a final process VFA TA ratio of 0,69 indicates that some instability will occur in the AD process, however, there is no VFA accumulation in and LCFA in variation 3 with produce highest biogas volume up to 980 L day. "

"Anaerobic digestion(AD) dapat menjadi solusi dalam mengolah limbah organik. Pengadukan dalam AD dapat meningkatkan kinerja proses di dalam AD. Penelitian ini bertujuan untuk menganalisis pengaruh pengadukan terhadap pembentukan biogas dari degradasi TS dan VS pada AD dengan menggunakan pengadukan dengan kecepatan 30 rpm selama 4 jam/hari dibandingkan dengan AD tanpa pengadukan. Perbandingan substrat sampah makanan dan feses sapi yang digunakan adalah 9:1 dan organic loading rate (OLR) 7,83 kg VS/m3-hari. Operasional reaktor menggunakan 2 buah dry AD satu tahap dengan volume 51 L dalam kondisi suhu mesofilik selama 31 hari. Hasil uji menunjukkan substrat cocok untuk dry AD dengan total solids (TS) sebesar 20,50-28,5%; nilai volatile solid (VS) 86,75-87,53%TS; rasio C/N sebesar 14,12-16,35 dan tingkat inhibitor <3.000 mg/L amonia.Hasil penelitian menunjukan penyisihan COD pada reaktor dengan pengadukan 66,2±11,0% sedangkan pada reaktor tanpa pengadukan 58,4±17,4%. Penyisihan TS dan VS pada reaktor dengan pengadukan 59,6±7,11% dan 5,71±3,56% sedangkan pada reaktor tanpa pengadukan 64,8±4,80% dan 8,10±2,31%. Perhitungan produksi biogas dari degradasi TS dan VS pada reaktor pengadukan lebih tinggi dengan 2,77±0,57 L CH4/kg VS dibandingkan dari reaktor tanpa pengadukan 2,35±0,37 L CH4/kg VS.Untuk mendapat kesimpulan dilakukan uji statistik dengan hasil statistik menunjukan tidak terdapat perbedaan yang signifikan antara produksi biogas pada reaktor dengan pengadukan dan tanpa pengadukan. Penelitian ini menyimpulkan bahwa pengadukan tidak berpengaruh pada penurunan TS, VS, COD, dan produksi biogas.

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Anaerobic digestion (AD) can be a solution in treating organic waste. Stirring in AD can improve process performance in AD. This study aims to analyze the effect of stirring on biogas formation with degradation of TS and VS in AD using stirring at a speed of 30 rpm for 4 hours per day compared with an AD without stirring. The comparison of food waste substrate and cow feces used was 9:1 and organic loading rate (OLR) 7.83 kg VS/m3-day. The reactor operation uses 2 dry AD one stage with a volume of 51 L in mesophilic conditions for 31 days. The test results show that the substrate is suitable for dry AD with total solids (TS) of 20.50-28.5%; volatile solid (VS) value of 86.75-87.53% TS; C/N ratio of 14.12-16.35; and inhibitor level <3,000 mg/L of ammonia.

The results showed that removal of COD in the reactor with stirring 66.2±11.0% while in the reactor without stirring 58.4±17.4%. The removal for TS and VS in the reactor with stirring 59.6±7.11% and 5.71±3.56% while in the reactor without stirring 64.8±4.80% and 8.10±2.31%. Meanwhile, biogas production from TS and VS degradation in the stirring reactor produce higher volume of biogas with 2.77±0.57 L CH4/kg VS compared to biogas production from the reactor without stirring which 2.35±0.37 L CH4/kg VS.

To conclude, a statistical test was performed with the results of statistics showing that there was no significant difference between the production of biogas in the reactor with stirring and without stirring. This study concluded that stirring had no effect on decreasing TS, VS, COD, and biogas production."

"Adanya kecenderungan masyarakat Indonesia untuk mengonsumsi makanan mengandung minyak dan lemak menjadi pemicu peningkatan timbulan limbah minyak dan lemak serta nilai COD dan VS air limbah. Penelitian ini bertujuan untuk mengetahui potensi biogas dan rasio limbah minyak dan lemak dengan sampah makanan yang paling optimum.Penelitian dilaksanakan selama 42 hari inkubasi pada suhu 37˚C dengan tiga variasi rasio VS limbah minyak dan lemak dan sampah makanan yaitu 1:7, 1:2, dan 1:1 dengan metode biochemical methane potential. Limbah minyak dan lemak memiliki karakteristik COD 148 g/L, TS 763 g/L, dan VS 759 g/L.Penelitian ini menunjukkan bahwa limbah minyak dan lemak memiliki potensi menghasilkan biogas tertinggi melalui proses anaerobic co- digestion dengan sampah makanan dan menghasilkan 485 mLCH4/grVS dari variasi 1:7. Sementara variasi rasio limbah minyak dan lemak dengan sampah makanan 1:2 dan 1:1 hanya menghasilkan 128 dan 4 mLCH4/grVS.

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Tendency of Indonesian people to eat foods containing oils dan fats trigger increasing in generation of fat, oil, and grease waste and increasing in wastewater?s COD and VS. This research is conducted to know potential of fat, oil, and grease and its ratio with food waste that obtain the highest biogas production through biochemical methane potential method.

The research was conducted over 42 days incubation at 37˚C including three variation of volatile solids (VS) ratio of fat, oil, and grease waste with food waste, that is 1:7, 1:2, and 1:1. As co- substrate of the anaerobic co- digestion process, fat, oil, and grease characteristics are COD 148 g/L, TS 763 g/L, and VS 759 g/L.

Result showed that fat, oil, and grease waste has potential to produce biogas through anaerobic co- digestion process with food waste and produce 485 mLCH4/grVS as the highest methane yield of 1:7 ratio. While the variation of ratio fat, oil, and grease waste with food waste at 1:2 and 1:1 only produce 128 and 4 mLCH4/grVS, respectively."

"Inokulum merupakan suatu media pertumbuhan bagi mikroorganisme untuk menguraikan bahan organik yang dapat mengoptimalkan pertumbuhan mikroorganisme dan kinerja reaktor Anaerobic Digestion (AD). Kinerja inokulum dapat dioptimalkan dengan beberapa cara, salah satunya adalah aditif asetat yang dapat mendorong pertumbuhan archaea metanogen agar fermentasi anaerob berjalan lebih baik.Tujuan dari penelitian ini adalah untuk menganalisis pengaruh penambahan asetat dalam inokulum pada populasi mikroorganisme penghasil metana dan pengaruhnya pada populasi mikroorganisme, pembentukan biogas, penyisihan Volatile Solids (VS) dan Chemical Oxygen Demand (COD). Terdapat 2 jenis inokulum yang digunakan pada penelitian ini, inokulum alami yang terbuat dari kotoran sapi dan inokulum buatan yang terbuat dari terasi, gula pasir, batang pohon pisang busuk, susu, dan dedak, ekstrak ragi, Lactobacillus MRS Broth, cairan rumen, dan penambahan asetat sebagai sumber karbon. Percobaan dilakukan pada reaktor AD berbahan fiber dan tanpa pengaduk yang memiliki volume keseluruhan 1 m3 dan volume isi 0,8 m3 selama 71 hari kerja.Hasil penelitian menunjukkan bahwa penambahan asetat tidak terbukti memperkaya populasi archaea metanogen dan produksi biogas. Metana dihasilkan dari genus Methanosaeta yang jumlahnya sangat sedikit yaitu hanya 0,004% dan genus Prevotella dalam jumlah cukup banyak yaitu 26,6% pada akhir operasional. Prevotella membentuk metana melalui penggunaan asam laktat yang dihasilkan genus Lactobacillus. Namun, inokulum buatan dengan aditif asetat terbukti meningkatkan konsentrasi metana hingga 41,7%, VSD hingga 91%, dan CODr hingga 99,5%. Hal ini menunjukkan inokulum buatan memiliki potensi yang sangat baik sebagai media pertumbuhan untuk menunjang pengolahan sampah makanan pada Anaerobic Digestion (AD) dengan bantuan pengontrolan pH yang sesuai dengan rentang pH optimum untuk tahap metanogenesis.

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The inoculum is a growth medium for microorganisms to decompose organic matter that can optimize the growth of microorganisms and the performance of the Anaerobic Digestion (AD) reactor. The performance of the inoculum can be optimized in several ways, one of which is acetate additives which can encourage the growth of archaea methanogens so that anaerobic fermentation runs better.

The purpose of this study was to analyze the effect of the addition of acetate in the inoculum on the population of methane-producing microorganisms and their effect on microorganism populations, biogas formation, removal of Volatile Solids (VS) and Chemical Oxygen Demand (COD). There are 2 types of inoculums used in this study, natural inoculum made from cow dung and modified inoculum made from shrimp paste, granulated sugar, rotten banana tree trunks, milk, and bran, yeast extract, Lactobacillus MRS Broth, rumen liquid, and additions acetate as a carbon source. The experiments were carried out on an AD reactor made from fiber and without stirrer which had an overall volume of 1 m3 and a volume of contents of 0.8 m3 for 71 working days.

The results showed that the addition of acetate was not proven to enrich the archaea methanogen population and biogas production. Methane is produced from the genus Methanosaeta, which is very small, only 0.004% and the genus Prevotella in considerable numbers, which is 26.6% at the end of operation. Prevotella forms methane through the use of lactic acid produced by the genus Lactobacillus. However, the modified inoculum with acetate additives was proven to increase the concentration of methane to 41.7%, VSD to 91%, and CODr to 99.5%. This shows that the modified inoculum has very good potential as a growth medium to support food waste processing in Anaerobic Digestion (AD) with the help of pH control that is in accordance with the optimum pH range for the methanogenesis stage."

"Pengadukan dalam Anaerobic Digestion AD dapat dikontrol untuk meningkatkan kinerja proses AD. Penelitian ini bertujuan untuk mengetahui pengaruh intensitas pengadukan terhadap kinerja proses AD, transfer panas di dalam digester dan untuk menganalisis kesetimbangan energi. Penelitian dilakukan menggunakan Continuous Stirred Tank Reactor CSTR dengan volume terisi 400 L yang beroperasi pada suhu rata-rata 27,8 1,07oC. Penelitian operasi skenario pertama dilakukan dengan input substrat sampah makanan dengan Organic Loading Rate OLR 10 kg VS/m3 selama 43 hari dan diaduk menggunakan variasi intensitas pengadukan 30 rpm dan 60 rpm selama 4 jam/hari untuk melihat kinerja proses AD. Operasi skenario kedua dilakukan menggunakan substrat sampah makanan dan kotoran sapi banding limbah Fat Oil and Grease FOG sebesar 10:1 dengan OLR 10 kg VS/m?3 dan dilakukan variasi pengadukan berkala 30 rpm, 15 menit/1,5 jam dan kontinu 30 rpm, 4 jam/hari untuk melihat tansfer panas dalam digester. Hasil penelitian operasi skenario pertama menunjukkan terdapat perbedaan yang signifikan pada kedua intensitas pengadukan.

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Mixing in Anaerobic Digestion AD can be controlled to improve the performance of the AD process. This study aims to determine the effect of mixing intensity on the performance of the AD process, heat transfer in the digester and to analyze the energy balance. The study was conducted using a Continuous Stirred Tank Reactor CSTR with 400 L working volume which operates at an average temperature of 27,8 1,07 C. In the first scenario operation study, reactor was fed with food waste with Organic Loading Rate OLR 10 kg VS m3 for 43 days and mixed using variation of mixing intensity 30 rpm and 60 rpm for 4 hours day to see AD process performance. The second operation was carried out using food and cow dung with Fat Oil and Grease FOG waste ratio 10 1 and mixed intermittent 30 rpm, 15 min 1.5 hour and continuous 30 rpm, 4 hour day to see heat transfer in the digester. The results of the first scenario operation study showed that there was a significant difference in both mixing intensity p."

"Limbah organik terutama sampah makanan memiliki volume yang sangat tinggi dan membutuhkan pengolahan di sumber. Dry anaerobic digestion merupakan salah satu teknologi pengolahan limbah organik yang cukup sederhana, kebutuhan air yang lebih sedikit dan tidak membutuhkan alat pengadukan yang terpasang pada reaktor. Pada penelitian ini substrat yang digunakan berupa sampah makanan yang berasal dari Kantin Fakultas Universitas Indonesia dengan inokulum air lindi dari anaerobic digester yang berada di Pasar Timbul Petamburan, Jakarta Barat. Penelitian ini dilakukan dengan reaktor dry anaerobik batch (TS 19,78%) selama 43 hari dengan nilai C/N campuran 9. Penambahan air lindi dilakukan dua kali pada minggu ke-5 dan ke-6 sebanyak 2 L yang terdiri dari 30% lindi dan 70% air suling. Selama operasi reaktor proses degradasi material organik berjalan dengan baik, dengan penurunan nilai VS dari 82,4% mencapai nilai 57,78% dengan efisiensi penurunan sebesar 30% dengan nilai VSremoved 70,77%. Namun pembentukan metana kurang berjalan dengan baik karena pH yang rendah 3,7-5 pada awal operasi. Volume metana yang dihasilkan sebanyak 0,2452 L dengan presentase gas metana tertinggi pada minggu ke-6 sebesar 8,66%. Pengaruh penambahan air lindi menjaga moisture 93% selama proses operasi di minggu 5 dan 6, meningkatkan nilai COD 9115 mg/l dan peningkatan nilai amonia mencapai 1002 mg/l N NH3 tetapi masih dalam batas toleransi dan belum bersifat toksik.

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Organic waste especially food waste have a very high volume and requires processing at the source. Dry anaerobic digestion is one of the organic waste processing technology was quite simple, less water needs and required no stirring tool attached to the reactor. On this study substrate which is used in the form of food waste that comes from the University of Indonesia Faculty Canteen with inokulum leachete from anaerobic digester are in the Timbul market Petamburan, West Jakarta. This research was conducted with reactors dry anaerobic batch (TS 19,78%) during the 43-day with a grade of C/N mix 9. The addition of leachete performed twice in week 5 and 6 as much as 2 L consisting of leachete 30% and 70% distilled water. During the operation of the reactor the process of degradation of organic material went well, with the declining value of its 82.4% VS reached 57.78% efficiency with a decrease of 30% with a value of VSremoved 70,77%. However the formation of methane less going well because of the low pH of 3.7-5 at the start of the operation. The volume of methane produced as much as 0.2452 L with the highest percentage of methane gas on weeks 6 of 8,66%. Influence of addition of leachete moisture keep in ± 93% during the process of operation in weeks 5 and 6, increase the value of COD 9115 mg/l and increased the value of ammonia reached 1002 mg/l NH3 N but still within the boundaries of tolerance and yet are toxic."

"Minimnya informasi terkait waktu tinggal substrat di dalam digester untuk menghasilkan gas yang optimum menjadikan salah satu permasalahan dalam pengoperasian digester anaerobik, sehingga perlu dilakukan penelitian terkait waktu tinggal. Penelitian terhadap waktu tinggal ini dilakukan dalam reaktor berukuran 51 L dengan sistem batch selama 40 hari dengan perbandingan substrat lumpur tinja:sampah makanan:sampah kebun adalah 1:1:1 dan dilakukan pengecekan karakteristik awal substrat setelah pencampuran.Berdasarkan penelitian didapatkan hasil bahwa C/N substrat adalah 12,5 dengan TS sebesar 1,25%. Biogas maksimum yang dihasilkan terjadi pada waktu tinggal 40 hari yaitu sebanyak 127,13 L per kg VS dengan persentase metan sebesar 37,4% dan persentase penghilangan COD sebesar 73,5%. Namun, pada penelitian ini belum dapat menentukan waktu tinggal optimum dikarenakan belum adanya fluktuasi dari produksi gas.

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The lack of information regarding the substrate residence time in the digester to produce optimum gas has affected to an appearance of certain problems in the operation of an anaerobic digester, so it is necessary to study related residence time. Research on the residence time in the reactor was done by measuring 51 L in a batch system for 40 days with a ratio of substrates, fecal sludge:food waste:garden waste is 1: 1: 1 and checking the initial characteristics of the substrate after mixing.

Based on the research, it showed that the C/N substrate is 12,5 with 1,25% TS. Biogas produced maximum occur at the time of stay of 40 days was as much as 127,13 per kg VS L with a percentage of 37,4% methane and COD removal percentage of 73,5%. However, this study have not been able to determine the optimum detention time fluctuations due to the lack of gas production."

"Pengelolaan limbah lumpur tinja yang sangat terbatas dapat ditingkatkan dengan memanfaatkannya menjadi biogas. Penelitian ini bertujuan untuk mengoptimalkan potensi biogas pada lumpur tinja dengan menambahkan sampah makanan dan sampah taman. Sistem yang digunakan berupa Anaerobic Co-digestion dengan variasi konsentrasi lumpur tinja, yaitu sebesar 25% dan 50% berdasarkan nilai Volatile Solids (VS). Inokulum yang digunakan adalah rumen sapi. Penelitian dilakukan menggunakan reaktor batch skala lab berukuran 51 L dengan masa operasi selama 42 hari. Biogas yang dihasilkan pada konsentrasi lumpur tinja sebesar 25% adalah 0,30 m3CH4/kg VS dengan destruksi VS sebesar 71,93% dan COD sebesar 72,42%. Sedangkan, biogas yang dihasilkan pada konsentrasi lumpur tinja sebesar 50% adalah 0,56 m3CH4/kg VS dengan destruksi VS sebesar 92,43% dan COD sebesar 87,55%. Penelitian ini menyimpulkan bahwa potensi biogas pada konsentrasi lumpur tinja sebesar 50% lebih besar dibandingkan pada konsentrasi lumpur tinja sebesar 25%.

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Faecal sludge management can be optimized by converting the sludge into biogas. The purpose of this study is to optimize the biogas potential of faecal sludge with food waste and garden waste. The system use Anaerobic Co-digestion with variation of 25% and 50% concentration of faecal sludge based on Volatile Solids (VS). Inoculum used was cow?s rumen. The study was operated using lab-scale batch reactor 51 L for 42 days. Biogas produced from 25% concentration of faecal sludge is 0,30 m3CH4/kg with 71,93% VS and 72,42% COD destruction. Meanwhile, 50% concentration of faecal sludge produced 0,56 m3CH4/kg VS biogas with 92,43% VS and 87,55% COD destruction. This study concludes that biogas potential from 50% concentration of faecal sludge is greater than 25% concentration of faecal sludge."