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"The main focus of this article was to investigate the potential of natural zeolite adsorbent for the removal of CO2 and H2S in biogas produced from palm oil mill effluent (POME) in fixed-bed column adsorption. The effects of the flowrates and dosage of the adsorbent on the CO2 adsorption were also studied. The surface area of the adsorbent was determined using the Brunauer, Emmett, and Teller (BET) model, while the pore size distribution was calculated according to the Barrett, Joyner, and Halenda (BJH) model. The morphology of the adsorbent was determined by field emission scanning electron microscopy and energy dispersive x-ray (FESEM-EDX) analysis. Before and after purification, the biogas was analyzed by gas chromatography with a thermal conductivity detector and polydimethylsiloxane as a column. Biogas from the POME, via the anaerobic digestion process, produced 89% CH4 and 11% CO2. The surface and structure of the clinoptilolite zeolites was modified by a strong acid (1M HCl), strong base (1M NaOH), and calcination at 450°C, and the surface area of the natural zeolites was reduced up to 16%. The working capability of CO2 adsorption by the modified zeolites decreased with increasing flow rates (100, 200, and 300 mL/min) of the biogas, with levels of CO2 at 106,906, 112,237, and 115,256 mg/L. The removal of the CO2 in the biogas by using adsorbent dosages of 1.5, 2.0, and 2.5 g was 97,878, 97,404 and 93,855 mg/L, respectively. The optimum purification of the biogas occurred under the flow rate of 100 mL/min and adsorbent dosage of 2.5 g. The high working capability of the modified zeolites for the removal of CO2 in the biogas was a key factor, and the most important characteristic for the adsorbent. The results indicate that clinoptilolite zeolites are promising adsorbent materials for both the purification and upgrading of biogas."

"The main focus of this article was to investigate the potential of natural zeolite adsorbent for the removal of CO2 and H2S in biogas produced from palm oil mill effluent (POME) in fixed-bed column adsorption. The effects of the flowrates and dosage of the adsorbent on the CO2 adsorption were also studied. The surface area of the adsorbent was determined using the Brunauer, Emmett, and Teller (BET) model, while the pore size distribution was calculated according to the Barrett, Joyner, and Halenda (BJH) model. The morphology of the adsorbent was determined by field emission scanning electron microscopy and energy dispersive x-ray (FESEM-EDX) analysis. Before and after purification, the biogas was analyzed by gas chromatography with a thermal conductivity detector and polydimethylsiloxane as a column. Biogas from the POME, via the anaerobic digestion process, produced 89% CH4 and 11% CO2. The surface and structure of the clinoptilolite zeolites was modified by a strong acid (1M HCl), strong base (1M NaOH), and calcination at 450°C, and the surface area of the natural zeolites was reduced up to 16%. The working capability of CO2 adsorption by the modified zeolites decreased with increasing flow rates (100, 200, and 300 mL/min) of the biogas, with levels of CO2 at 106,906, 112,237, and 115,256 mg/L. The removal of the CO2 in the biogas by using adsorbent dosages of 1.5, 2.0, and 2.5 g was 97,878, 97,404 and 93,855 mg/L, respectively. The optimum purification of the biogas occurred under the flow rate of 100 mL/min and adsorbent dosage of 2.5 g. The high working capability of the modified zeolites for the removal of CO2 in the biogas was a key factor, and the most important characteristic for the adsorbent. The results indicate that clinoptilolite zeolites are promising adsorbent materials for both the purification and upgrading of biogas."

"Material ZSM-5 berhasil disintesis dari zeolit alam Bayat ndash; Klaten dan Kaolin Belitung sebagai sumber mineralnya dengan melakukan 2 tahap, yaitu pre-treatment terhadap zeolit alam dan kaolin terlebih dahulu dan kemudian sintesis material zeolit ZSM-5. Zeolit alam bayat sebagai sumber mineral Si/Al untuk sintesis terlebih dahulu diberi perlakuan sebagai berikut : aktivasi, purifikasi, fragmentasi dan dealuminasi, sedangkan kaolin sebagai sumber silika yang menutupi kekurangan silika pada saat sintesis diberi perlakuan : aktivasi, purifikasi dan ekstraksi terlebih dahulu. Berdasarkan hasil karakterisasi EDX didapatkan rasio Si/Al sebesar 24,8 setelah perlakuan dealuminasi pada zeolit alam bayat, dan persen silika sebesar 98 setelah diekstraksi. Kemudian sintesis ZSM-5 dengan sumber mineral alam ini menggunakan template TPAOH sebagai pengarah struktur pori mikro, dan diimpregnasi dengan logam Mn sebesar 2 untuk kemudian menjadi katalis pada reaksi konversi -Selulosa menjadi asam levulinat. Dari hasil karakterisasi FTIR, SEM dan XRD ZSM-5 mikropori berhasil disintesis, dan dari hasil karakterisasi AAS diketahui persen loading logam Mn pada material ZSM-5 sebesar 2.2 . Sebelum reaksi konversi dilakukan-Selulosa diberi perlakuan ultrasonikasi dengan variasi waktu sonikasi, dan diyakini semakin lama sonikasi dilakukan maka semakin renggang ikatan 1-4 glikosidik pada-Selulosa, dari hasil pemantauan menggunakan mikroskop. Reaksi konversi berlangsung dengan variasi waktu yaitu 0, 2, 4, 6, 8 dan 10 jam pada suhu 130 C, dengan menggunakan instrumen HPLC dibuktikan bahwa reaksi konversi selama 6 jam mendapatkan yield asam levulinat terbanyak, sebesar 5.5.

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Material ZSM 5 was synthesized from natural zeolite Bayat Klaten and Kaolin Belitung as its mineral source by doing 2 stages, first is pre treatment of natural zeolite and kaolin and then synthesis of ZSM 5 zeolite material. Natural zeolite Bayat Klaten as source of Si Al minerals for synthesis was first treated as follows activation, purification, fragmentation and dealumination, whereas kaolin as the source of silica to cover silica deficiency at the time of synthesis was treated activation, purification and extraction first.

Based on EDX characterization result Si Al ratio was 24,8 after treatment of dealumination in natural zeolite bayat, and 98 percent silica after extracting. Then the synthesis of ZSM 5 with this natural mineral source using the TPAOH as a template for steering the micropore structure, and impregnated with 2 Mn metal to then become the catalyst in the conversion of Cellulose into levulinic acid.

From the characterization of FTIR, SEM and XRD ZSM 5 micropore were successfully synthesized, and from AAS characterization result was known percent loading of Mn metal on ZSM 5 material is 2.2. Before doing the conversion reaction, Cellulose is treated with ultrasonication with variation of time of sonication, and it is believed that the longer the sonication is the more gap that formed between 1 4 glycosidic bonded on Cellulose, from microscopic monitoring results. The conversion reaction with variation of 0, 2, 4, 6, 8 and 10 hours at 130 C, using HPLC instrument as evidenced by the conversion reaction for 6 hours obtaining the highest yield of levulinic acid."

"Potensi endapan zeolit di Indonesia tersebar luas dl berbagai lokasi diantaranya : Yogyakarta dan Lampung. Zeollt alam Yogya dan Lampung mengandung mineral mordenit dan klinoptllolit. Zeollt alam ini dapat dimanfaatkan untuk mengadsorpsi ion logam yang berleblh dalam air tanah, sehingga air tanah tersebut layak digunakan untuk air minum. Penelitian ini bertujuan untuk mengetahui pengaruh aktivasi asam, pemanasan, impregnasi menggunakan Ion Mn2+ terhadap zeolit alam Yogya dan Lampung. Penelitian ini juga ingin membandingkan bila zeolit tersebut dicampur dengan 10 % zeollt alam Lampung. Zeolit alam terleblh dahulu diaktivasi baik secara kimia maupun dengan pemanasan. Zeolit yang telah diaktivasi diimpregnasi dengan larutan KMn04 1000 ppm ataupun dengan larutan MnGIa 3 %. Kadar Mn yang teradsorpsi pada zeolit diukur dengan menggunakan AAS. Hasll optimal yang didapatkan yaitu : Zeolit hasil impregnasi menggunakan larutan KMn04 yang telah diaktivasi larutan HCI 0,5 M menghasilkan daya serap zeolit sebesar 23,513 mg/g zeolit, sedangkan zeolit hasil impregnasi menggunakan larutanMnCl2 yang telah diaktivasi pemanasan 200°G menghasilkan daya serap zeolit sebesar 95,188 mg/g zeolit. Zeolit hasil impregnasi digunakan sebagai adsorben ion Fe pada larutan FeCb 5223 ppm dengan menggunakan metode kolom. Setiap efluen yang keluar diukur kadar Fe dan Mn dengan menggunakan AAS. Zeolit alam Yogya tanpa aktivasi dapat menurunkan kadar Fe sebesar 99,960 %, Mn-Zeolit baik yang diimpregnasi dengan larutan KMn64 ataupun dengan larutan MnCb dapat menurunkan kadar Fe sebesar 99,970 %, tetapi dengan kadar Mn yang cukup besar. Zeolit alam Yogya yang dicampur dengan 10 % zeolit alam Lampung menghasilkan penurunan kadar Fe sebesar 99,970 %. Pengujian air tanah dengan menggunakan zeolit alam Yogya tanpa impregnasi menghasilkan penurunan kadar Fe sebesar 93,081 % dan kadar Mn sebesar 95,278 %, sedangkan Mn-Zeolit dapat menurunkan kadar Fe sebesar 96,475%, tetapi mengalami peningkatan kadar Mn sebesar 8,141 %."

"Indonesia merupakan negara yang padat penduduknya. Dengan kepadatan penduduk yang tinggi menyebabkan banyaknya kawasan industri rumah tanggga maupun industri di kota-kota besar yang dapat menghasilkan berbagai macam limbah logam berat. Penelitian ini mempelajari proses pembuatan komponen DGT serta aplikasinya pada pengukuran sampel larutan Cd2+. Komponen DGT berasal dari reaksi polimerisasi akrilamida yang menghasilkan diffusive gel serta resin chelex yang diimpreg ke dalam larutan gel menghasilkan resin gel. Selain itu dilakukan juga variasi resin gel dengan menggunakan zeolit yang menghasilkan zeolit gel. Pengukuran dalam penelitian ini menggunakan AAS. Waktu optimum yang diperlukan oleh resin gel dan zeolit gel untuk menyerap logam yaitu 24 jam sehingga didapatkan CDGT 1,36 µg/ml dan CDGT oleh zeolit gel sebesar 0,825 µg/ml. Pada variasi konsentrasi, CDGT maksimum resin gel yang diperoleh sebesar 59,950 µg/ml dan 1,315 µg/ml pada zeolit gel. Sedangkan pH optimum yang diperoleh pada penelitian ini baik chelex maupun zeolit pada pH 7 dengan nilai CDGT 1,428 µg/ml untuk resin gel dan 0,881 µg/ml untuk zeolit gel. Adanya agen pengompleks EDTA mempengaruhi jumlah ion Cd2+ yang dapat diserap dan dapat dilihat dari kecilnya nilai CDGT yaitu 0,0182 µg/ml untuk resin gel dan 0,0148 µg/ml untuk zeolit gel. Dilakukan juga uji homogenitas resin dan zeolit gel yang dilakukan dengan 3 kali pengukuran sehingga diperoleh nilai standar deviasi dan %RSD resin gel sebesar 0,0066 dan 0,345 % serta nilai standar deviasi dan %RSD zeolit gel sebesar 0,0083 dan 0,774 % yang menunjukkan material tersebut relatif cukup homogen untuk digunakan pada DGT.

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Indonesia is a populous country. With a high population density causes many home industries and industries in large cities could produce various kinds of heavy metals waste. This research studies the process of making DGT components and its application to the measurement of sample solutions of Cd2+. DGT components derived from acrylamide polymerization reactions that produce diffusive gel and chelex resins impregnated into the gel solution to produce the resin gel. Beside that, there are also variations in the resin gel by using zeolite that produces zeolite gel. Measurement in this study used the AAS. The optimum time required by the resin gel and zeolite gel to absorb the metal that is 24 hours so that got CDGT 1.36 µg /ml for resin gel and CDGT 0.825 µg/ml by zeolite gel. On the variation of concentration, the maximum CDGT resin gel obtained at 59.950 µg/ml and 1.315 µg/ml in the zeolite gel. While the optimum pH obtained in this study both Chelex and zeolite at pH 7 with CDGT value 1.428 µg/ml for the resin gel and 0.881 µg/ml for zeolite gel. The presence of EDTA complexing agent affect the number of Cd2 + that can be absorbed and can be seen by the small value of CDGT, ie 0.0182 µg/ml for resin gel and 0.0148 µg/ml for zeolite gel. Homogeneity tests were also carried out for the resin and zeolite gel for triplicate measurement with value of standard deviation and % RSD resin gel at 0.0066 and 0.345% and the standard deviation and% RSD zeolite gel at 0.0083 and 0.774% showing relative good homogen of the materials using for DGT. "

"ABSTRAKBiogas diproduksi dari limbah cair kelapa sawit dengan proses digesting anaerob memiliki kadar CH4 dan CO2 masing-masing sebesar ± 86,2% dan ± 13,8 %. Pengotor pada biogas yaitu CO2 perlu dihilangkan, karena dapat menurunkan nilai kalor pada biogas dan bersifat korosif. Metode simultan absorpsi dan adsorpsi dipilih pada penelitian ini. Absorpsi menggunakan larutan Ca(OH)2 0,0619 M dan adsorpsi menggunakan dua kolom unggun tetap dan zeolit klinoptilolit termodifikasi sebagai adsorben. Zeolit Klinoptilolit dimodifikasi struktur dan luas permukaannya dengan menggunakan HCl (2M), NaOH (2M), kalsinasi pada suhu 450 oC dan pelapisan kitosan 0,5% (b/v). Karakterisasi adsorben dilakukan dengan analisis XRD, FTIR, SEM-EDX dan analisis permukaan dan porositas dengan BET dan analisis biogas dengan GC dan GC-MS. Efektivitas penyerapan CO2 dengan metode simultan absorpsi-adsorpsi dua kolom didapatkan sebesar 82,5% dengan waktu jenuh pada menit ke-30. Adsorben diregenerasi didapatkan hasil efektivitas penyerapan CO2 sebesar 74,3% dengan menggunakan NaOH 1,5 M dan pemanasan pada suhu 200oC.

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ABSTRACTBiogas produced from palm oil mill effluent by digesting anaerobic contains of CH4 and CO2 each ± 86,2% and ± 13,8 %. Biogas purified necessary to remove impurity, that CO2 can reduce calorie value of biogas and corrosive. In this research biogas purified using simultaneous absorption-adsorption method because simply and applicative. Absorption using Ca(OH)2 0,0619 M and adsorption method using two fixed bed column and zeolite clinoptilolite as adsorbent. Structure and surface area of zeolite clinoptilolite can be modified using strong acid and strong base with concentration each 2 M, calcination at 450 oC and coated chitosan 0,5 %. Adsorbent characterization by XRD, FTIR, SEM-EDX, surface area and porosity analyse with BET and biogas analyse using GC and GC-MS.. Research result found 82,5% CO2 adsorption effectiveness of using simultaneous absorption-adsorption double column method with saturated time at 30 minute. Adsorbent can be regenerated founded CO2 adsorption effectiveness 74,3% with using NaOH 1,5 M and 200oC."

"Proses produksi pada reaktor biogas dari limbah cair pabrik kelapa sawit atau Palm Oil Mill Effluent (POME) sering menghadapi masalah karena keterbatasan laju hidrolisis. Keterbatasan ini terjadi akibat terbentuknya lumpur dan gumpalan yang mengurangi voulme efektif digester biogas serta mengurangi potensi biogas yang dihasilkan. Lumpur dan gumpalan yang dihasilkan berasal dari tingginya kandungan dan juga serat yang ada pada POME. Berbagai upaya telah dilakukan seperti pengambilan secara manual maupun pengadukan secara mekanik atau dengan turbulensi melalui pemompaan cairan dengan kuat. Namun, upaya tersebut memerlukan tambahan alat, SDM dan energi sehingga biaya proses produksi terus meningkat. Sebagai alternatif lain, maka pemanfaatan lipase dan xilanase menjadi alternatif yang menjanjikan untuk pretreatment yang dapat meminimalisir kandungan padatan hemiselulosa dan minyak atau lemak di dalam POME. Lipase dapat menghidrolisa lemak dan minyak menjadi asam lemak rantai pendek dan xilanase dapat menghidrolisa hemiselulosa menjadi monomernya, sehingga memudahkan produksi biogas. Pada penelitian ini telah terbukti bahwa pretreatment dengan xilanase dan lipase mampu menurunkan total suspended solid (TSS) sebesar 49,21 %; total solid (TS) sebesar 34, 52 % dan meningkatkan gula pereduksi sebesar 44,37 %, selain itu mampu menurunkan minyak dan lemak sebesar 88,82 pada konsentrasi 4 %. Serta menignkatkan produksi biogas sebanyak 52,17 % dan penghilangan chemical oxygen demand (COD) sebesar 49,7 %.

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The production process at biogas reactors from Palm Oil Mill Effluent (POME) often faces problems due to limited hydrolysis rates. This limitation occurs due to the formation of mud and lumps which reduce the effective volume of the biogas digester and reduce the potential for biogas produced. The sludge and lumps produced come from the high content and fiber present in the POME. Various treatments have been made such as manual extraction or mechanical stirring or by turbulence through strong fluid pumping. However, these treatments require additional tools, human resources and energy so the production process costs continue to increase. As an alternative, the use of lipase and xylanase is a promising alternative for pretreatment that can minimize the content of hemicellulose and oil or fat in POME. Lipase can hydrolyze fat and oil into short-chain fatty acids and xylanase can hydrolyze hemicellulose into its monomer, thus facilitating biogas production. In this study it was proven that pretreatment with xylanase and lipase was able to reduce total suspended solid (TSS) by 49.21%; total solid (TS) of 34, 52% and increasing reducing sugar by 44.37%, besides that it can reduce oil and fat by 88.82 % at a concentration of 4%. As well as increasing biogas production by 52.17% and removal chemical oxygen demand (COD) by 49.7%."

"Currently the world’s second largest palm oil producer Malaysia produces a large amount of oil palm biomass each year. Although some oil palm parts and derivatives like empty fruit bunch and fibre have been commercialized as fuel, less attention has been given to oil palm fronds (OPF). Initial feasibility and characterization studies of OPF showed that it is highly feasible as fuel for gasification to produce high value gaseous fuel or syngas. This paper discusses the experimental gasification attempt carried out on OPF using a 50 kW lab scale downdraft gasifier and its results. The conducted study focused on the temperature distributions within the reactor and the characteristics of the dynamic temperature profile for each temperature zones during operation. An average pyrolysis zone temperature of 324oC and an average oxidation zone temperature of 796oC were obtained over a total gasification period of 74 minutes. A maximum oxidation zone temperature of 952oC was obtained at 486 lpm inlet air flow rate and 10 kg/hr feedstock consumption rate. Stable bluish flare was produced for more than 70% of the total gasification time. Similar temperature profile was obtained comparing the results from OPF gasification with that of woody biomass. Furthermore, the successful ignition of the syngas produced from OPF gasification ascertained that OPF indeed has a higher potential as gasification feedstock. Hence, more detailed studies need to be done for better understanding in exploiting the biomass as a high prospect alternative energy solution. In addition, a study of the effect of initial moisture content of OPF feedstock on the temperature distribution profile along the gasifier bed showed that initial moisture content of feedstock in the range of 15% gives a satisfactory result, while experiments with feedstock having higher moisture content resulted in lower zone temperature values."

"[Produksi biogas menggunakan limbah cair kelapa sawit (LCKS) dengan prosesdigesting anaerob menggunakan tangki digester menghasilkan CH4 sebesar ±87% dangas CO2 sebsar ±13%. Metode absorpsi dan kolom adsorpsi adalah beberapa prosessederhana yang mudah untuk diaplikasikan, aplikasinya dapat menggunakan zeolitalam sebagai adsorben dan larutan Ca(OH)2 sebagai absorben. Kedua metode tersebutdapat digunakan secara simultan untuk proses purifikasi biogas dengan cara biogasdialirkan terlebih dahulu ke dalam larutan Ca(OH)2 dan kemudian akan dilewatkan kedalam kolom dengan ukuran tinggi dan diameter dalam sebesar 15cm dan 0,8cm yangberisi zeolit alam termodifikasi. Untuk meningkatkan daya adsorpsi dapat dilakukanmodifikasi permukaan zeolit alam dengan perlakuan asam kuat-basa kuat denganvariasi konsentrasi 1, 2, dan 3M, kalsinasi pada suhu 450°C, dan melapisi permukaanzeolit alam dengan beberapa variasi konsentrasi kitosan yaitu 0,25; 0,5; dan 1%.Penggunaan asam kuat-basa kuat dapat meningkatlkan luas permukaan dan diameter,sedangkan pelapisan kitosan dapat meningkatkan kapasitas adsorpsi pada zeolit alamkarena adanya gugus amine pada kitosan. Hasil modifikasi dan aktivasi zeolit akandiuji menggunakan SEM-EDX, BET, FTIR, dan XRD, sedangkan hasil purifikasibiogas akan diuji menggunakan gas chromatography (GC). Adsorben terbaik yangdidapatkan dari penelitian ini adalah adsorben dengan perlakuan asam-basa 2M yangkemudian dilapisi kitosan 0,5%. Hasil purifikasi yang didapatkan adalah pengurangankadar CO2 pada biogas menjadi 0.42% dan peningkatan kadar CH4 menjadi 99.58%.;Production of biogas from POME by anaerobic digestion process using digester has been shown able to produce CH4 87 and CO2 13 The methods of absorption and adsorption is simple to be applied this method can be done with zeolite as adsorbent and Ca OH 2 as absorbent Both methods can be applied simultaneous for purification which the gas will pass through the chamber Ca OH 2 solution and then passed the column filled with modified natural zeolite Enhancing the adsorption capability done with modified the zeolite using some concentration in strong acid base 1 2 and 3M calcination at 450 C and coating with chitosan 0 25 0 5 and 1 Usage of strong acid and strong base can increase the surface area and diameter of the zeolite pores while coating with chitosan can increase the adsorption capacity because the amine functional group from chitosan The result of the modification of zeolite will be tested with SEM EDX BET FTIR and XRD while the result of the purification will be characterized with GC The best adsorbent from this research is zeolite modified with acid base 2M and coated with 0 5 of chitosan The final result from this research is CO2 about 0 42 and the CH4 become 99 58 , Production of biogas from POME by anaerobic digestion process using digester has been shown able to produce CH4 87 and CO2 13 The methods of absorption and adsorption is simple to be applied this method can be done with zeolite as adsorbent and Ca OH 2 as absorbent Both methods can be applied simultaneous for purification which the gas will pass through the chamber Ca OH 2 solution and then passed the column filled with modified natural zeolite Enhancing the adsorption capability done with modified the zeolite using some concentration in strong acid base 1 2 and 3M calcination at 450 C and coating with chitosan 0 25 0 5 and 1 Usage of strong acid and strong base can increase the surface area and diameter of the zeolite pores while coating with chitosan can increase the adsorption capacity because the amine functional group from chitosan The result of the modification of zeolite will be tested with SEM EDX BET FTIR and XRD while the result of the purification will be characterized with GC The best adsorbent from this research is zeolite modified with acid base 2M and coated with 0 5 of chitosan The final result from this research is CO2 about 0 42 and the CH4 become 99 58 ]"

"ABSTRAKRasio elektrifikasi di Provinsi Jambi merupakan yang terendah di Sumatera dengan rasio eletrifikasi sebesar 39,59 . Dibutuhkan adanya tambahan energi listrik di daerah Jambi, terutama di daerah yang belum terjangkau energi listrik salah satunya adalah dengan memanfaatkan biogas yang berasal dari limbah cair pengolahan kelapa sawit atau sering disebut Palm Oil Mill Effluent POME , menjadi energi listrik. Sebagaimana diketahui kelapa sawit merupakan komoditas perkebunan yang terbesar di jambi, limbah cair dari pengolahan kelapa sawit masih belum dimanfaatkan hanya ditampung pada kolam terbuka yang dapat menyebabkan terbentuknya emisi gas rumah kaca. Pada penelitian ini akan digunakan data-data dari salah satu perkebunan kelapa sawit di Jambi, dengan produksi POME sekitar 144.859 ton/tahun. Dengan COD sebesar 64.005 mg/l. Berdasarkan kajian teknologi yang dilakukan dipilih tipe bioreaktor anaerob jenis Continues Stirred Tank Reactor CSTR dengan volume bioreaktor sebesar 2808 m3 dan HRT selama 6,79 hari . Digunakan simulasi untuk memprakirakan proses dan hasil yang terjadi pada sistem Pembangkit Listrik Biogas dari POME PLTBg POME .Berdasarkan hasil simulasi bahan baku POME sebesar 167766 kg/jam dapat menghasilkan 2777 kg/jam. Hasil simulasi Gas Engine menghasilkan energi listrik sebesar 1050 kW. Produksi biogas sebesar 2.988.889 m3/ tahun, serta energi listrik yang dihasilkan sekitar 5380 MWh per tahunnya.Nilai investasi sekitar 3.663.119 USD dapat menarik para investor jika harga jual tarif listrik diwilayah sumatera lebih dari 1.500 IDR/kWh, dengan IRR sebesar 11,2 dan NPV sebesar USD 43.010. dan payback period sekitar 8 tahun.

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ABSTRACT

Electrification ratio Jambi Province is the lowest in Sumatra with eletrification ratio around to 39.59 . Needed the addition of electrical energy in Jambi, especially in areas which not reached by electricity. One of choice is using biogas derived from liquid waste from palm oil mill or called Palm Oil Mill Effluent POME into electrical energy.As it is known palm oil is the largest plantation commodity in Jambi, liquid waste from palm oil mill is still not used only accommodated in open ponds which can lead to the formation of greenhouse gas emissions.In this research will be using data from one of the oil palm plantations in Jambi, with POME production about 144 859 tonnes year. With COD 64 005 mg l. Based on studies conducted chosen technology type anaerobic bioreactor types Continues Stirred Tank Reactor CSTR with volume of bioreaktor 2808 m3 and HRT for 6,79 days Using a simulation to predict the processes and outcomes that occur on the system of POME Biogas Power Plant PLTBg POME .Based on simulation results feed POME 16766 kg hour will be produce methane 2777 kg hour, it can be generate electicity 1050 kW.Biogas production amounted to 2,988,889 m3 year, and the electrical energy produced approximately 5380 MWh per year.Investment value approximately 3,663,119 , will be attractive for investors if the sale price of electricity tariffs in the region of Sumatra more than 1,500 IDR kWh, with an IRR of 11 2 and a NPV of USD 43 010. and payback period of about 8 years."