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Apri Wiyono
Investigasi karakteristik co-gasifikasi pada komposisi pelet WCF sekam padi dan pelet WCF pelet sekam dengan teknologi downdraft fixed bed gassifier = Investigation of co gasification characteristics of WCFw pellet rice husk and WCF pellet rice husk pellet in a downdraft fixed bed gasifier
"ABSTRAK
Kebutuhan energi yang terus meningkat, sejalan dengan laju pertambahan penduduk selalu diikuti dengan laju timbunan sampah. Dimana persentase terbesar berasal dari sampah organik, hal ini berpotensi dimanfaatkan sebagai bahan baku campuran biomassa untuk upaya reduksi emisi pada konversi bahan bakar dari energi sampah. Tujuan utama dari makalah ini adalah untuk mempelajari karakteristik co-gasifikasi, temperatur tungku reaktor, LHV producer gas dan output ash, terhadap kinerja proses gasifikasi biomassa pada downdraft fixed bed gassifier. Pada penelitian ini, sampah organik yang digunakan ranting, serabut kelapa dan sekam padi yang di peletisasi sebagai bahan baku pada pembakaran dengan teknologi Downdraft Gassifier. Metode yang dilakukan dengan teknik co-gasifikasi antara WCF wood-coconut fibers pelet dan sekam padi pada komposisi 100 pelet, 75:25, 50:50, 25:75 dan sekam padi 100 . Dimana pengujian syngas dilakukan pengukuran langsung dengan gas cromatograph tipe TCD Shimadzu 8A. Temperatur reaktor tertinggi pada zona pirolisis sebesar 400 C ndash; 850 C and temperatur pada zona oksidasi sebesar 1000 C ndash; 1200 C. Hasil dari pengujian syntetic gas didapatkan lower heating value tertinggi pada komposisi WCF pelet 100 sebesar 4.51 MJ/Nm3. Lower heating value syngas paling rendah pada komposisi pelet 100 sebesar 2.99 MJ/Nm3, dimana pertambahan WCF pelet akan meningkatkan nilai LHV syngas. Hal ini menyebabkan konten tar rendah dan rendahnya partikel ash pada semua komposisi kira-kira 30-35 massa awal tiap komposisi, dengan ash terendah pada komposisi sekam padi 100 sebesar 0.29 gr. Kata Kunci : Biomassa, peletisasi, co-gasifikasi, downdraft gassifier, syntetic gas
ABSTRACT
Increasing energy demand, in line with the rate of population growth is always with the pile of garbage. The largest percentage of organic waste, it can be used as raw material. This is primarily to discuss co gasification characteristics, reactor furnace temperatures, LHV gas producers and ash output, on the performance of biomass gasification at. In this study, organic waste used twigs, coconut fibers and rice husks in the pelletization as raw materials on technology with downdraft gassifier. The method is performed by co gasification technique between WCF coconut wood fiber pellet and rice husk on the composition of 100 pellets, 75 25, 50 50, 25 75 and 100 rice husk. Where the syngas testing is done directly with TCD Shimadzu gas cromatograph 8A. The reactor temperature in the pyrolysis zone of 400 C 850 C and the temperature in the oxidation zone 1000 C 1200 C. The results of testing the synthetic gas obtained lower heating value in the WCF 100 pellet composition of 4.51 MJ Nm3. The lower heating value of syngas is lowest in 100 pellet composition of 2.99 MJ Nm3, where the increase of WCF pellets will increase LHV syngas. The effect makes low tar content and low ash particles in all compositions approximately 30 35 of the initial mass of each composition, with minimal ash on 100 rice husk composition of 0.29 g. Keywords Biomass, pelletization, co gasification, downdraft gassifier, synthetic gas"
2017
T48475
UI - Tesis Membership  Universitas Indonesia Library
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Apri Wiyono
Investigation of co-gasification characteristics of wood-coconut fibers pellet and rice husk mixtures in a downdraft fixed bed gasifier
"Increasing energy demand, in line with the rate of population growth, is always followed by the pace of the waste dump. Where the largest percentage comes from organic waste, it is potentially utilized as raw material of biomass mixture for emission reduction efforts in fuel conversion from waste energy. The main objective of this paper is to study the characteristics of co-gasification, especially gasification temperature, lower heating value and gas emission, on the performance of the biomass gasification process in a downdraft fixed bed gasifier. In this study, organic waste used twigs, coconut fibers and rice husks in the pelletization as raw materials on the combustion technology Downdraft Gasifier. Methods were carried out by co-gasification techniques between WCF (wood-coconut fibers) pellet and rice husk on 100% pellet composition, 75:25, 50:50, 25:75 and 100% rice husk. Syngas testing is done with direct measurement on the burner with TCD type Shimadzu 8A gas chromatography. The highest reactor temperature in the pyrolysis zone was 400oC to 850oC and the temperature in the oxidation zone was 1000oC to 1200oC. The result of the synthetic gas testing obtained the highest lower heating value (LHV) in WCF 100% pellet composition at 4.07 MJ/Nm3 with 85% efficiency. The lower heating value of the lowest syngas in a 100% pellet composition was 2.99 MJ/Nm3, where the increase of WCF pellets will increase the LHV syngas value. This resulted in visually low tar content and low ash particles in all compositions of approximately 30 to 35% of the initial mass of each composition, with the lowest ash in 100% rice husk composition at 0.29 g."
Depok: Faculty of Engineering, Universitas Indonesia, 2017
UI-IJTECH 8:7 (2017)
Artikel Jurnal  Universitas Indonesia Library
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Andika Akbar Hermawan
Kajian implementasi venturi scrubber pada sistem reaktor gasifikasi biomassa sekam padi tipe fixed-bed downdraft = Assesment of venturi scrubber implementation on biomass gasification fixed bed downdraft reactor fueled by rice husk
"
ABSTRAK
Gasifikasi biomassa adalah proses konversi bahan baku biomassa padat menjadi bahan bakar gas yang dapat dibakar combustible gas dengan suplai udara yang terbatas Basu, 2010 . Gas mampu bakar dan tidak mampu bakar producer gas yang berasal dari gasifikasi biomassa mengandung pengotor atau kontaminan partikel dan organik, seperti tar, yang jika tidak dihilangkan dapat menyebabkan masalah operasional yang sangat berat Hasler Nussbaumer, 1999 . Venturi Scrubber terbukti efektif untuk menghilangkan pengotor atau kontaminan partikel dan organik, seperti tar Thana, 2010 . Pada penelitian ini pengaruh rasio laju air scrubbing liquid dari venturi scrubber terhadap laju producer gas Ql/Qg telah teridentifikasi. Efek dari rasio tersebut dapat terlihat berdasarkan tiga parameter yaitu penurunan suhu, perubahan tekanan dan efisiensi penangkapan tar. Rasio Ql/Qg = 0.040 telah diketahui sebagai penyumbang penurunan suhu terbesar yaitu sebesar 39.91o C dan perubahan tekanan terbesar yaitu 1004.72 Pa. Namun, hal ini belum tentu sebanding dengan performa penangkapan tar. Dalam penelitian ini, ditemukan Ql/Qg = 0.014 telah ditemukan sebagai titik optimal dalam penangkapan tar, dimana efisiensi penangkapan tar pada rasio tersebut mencapai 88.
ABSTRAK
Biomass gasification is the process of converting raw solid biomass materials into combustible gas fuels with a limited air supply Basu, 2010 . Gas capable of burning and incapable of fuel gas producer derived from biomass gasification contains impurities or particulate and organic contaminants, such as tar, which, if not eliminated, can cause severe operational problems Hasler Nussbaumer, 1999 . Venturi Scrubber is proven to be effective for removing impurities or particulate and organic contaminants, such as tar Thana, 2010 . In this study, the effect of the ratio of the rate of liquid scrubbing water from the venturi scrubber to the gas producer rate Ql Qg has been identified. The effect of these ratios can be seen based on three parameters temperature drop, pressure change and tar capture efficiency. The ratio Ql Qg 0.040 has been known as the largest contributor to the temperature drop of 39.91o C and the largest pressure change is 1004.72 Pa. However, this is not necessarily proportional to tar fishing performance. In this study, found Ql Qg 0.014 has been found as an optimal point in tar fishing, where tar capture efficiency at the ratio reached 88 ."
2017
S-Pdf
UI - Skripsi Membership  Universitas Indonesia Library
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Simatupang, Felly Rihlat Gibran
Optimasi secondary air intake pada reaktor tipe fixed bed downdraft gasifikasi biomassa sekam padi = Secondary air intake optimization on fixed bed downdraft reactor type rice husk biomass gasification
" ABSTRAK
Sekam padi merupakan limbah pertanian terbesar dengan potensi 13.662 MWe per tahun. Melalui proses gasifikasi biomassa, sekam padi dapat dikonversi menjadi producer gas yang dapat digunakan untuk kebutuhan energi panas maupun listrik. Untuk menghasilkan producer gas berkualitas baik, sistem gasifikasi dengan kandungan tar rendah menjadi fokus utama penelitian. Penelitian menggunakan open top fixed bed downdraft gasifier sistem batch dilakukan dengan memvariasikan posisi injeksi udara sekunder Z dan Air Ratio AR . Hasilnya, pada AR 80 , saat Z = 38 cm, tercipta flaming pyrolysis dengan durasi terpanjang selama 400 sekon yang mengindikasikan kandungan tar terendah, serta saat Z = 50 cm, dihasilkan producer gas dengan energi pembakaran tertinggi sebesar 734,64 kJ.
ABSTRACT Rice husk is one of agricultural waste with the largest annual potency of 13,662 MWe. Using biomass gasification, rice husk can be converted into producer gas for thermal and electrical energy needs. In order to produce a good in quality producer gas, gasification with low tar content become the main focus in this research. Experiment using open top fixed bed downdraft gasifier batch system was conducted by variying the secondary air injection position Z and Air Ratio AR . As a result, when AR 80 , at Z 38 cm, flaming pyrolysis with the longest duration of 400 seconds was created which indicated that this condition had the lowest tar content, meanwhile, at Z 50 cm, producer gas with the highest combustion energy of 734.64 kJ was obtained"
Depok: Fakultas Teknik Universitas Indonesia, 2017
S66125
UI - Skripsi Membership  Universitas Indonesia Library
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Resky Ervaldi Saputra
Kajian Simulasi Gasifikasi Sekam Padi Dan Serbuk Gergaji Pada Tipe Fixed Bed Downdraft Gasifier Dengan Variasi Rasio Ekivalensi, Suhu Dan Campuran Biomassa = Simulation Study of Fixed Bed Downdraft Gasifier for Rice Husk and Sawdust With Variation of Equivalence Ratio, Temperature and Feedstock Mixture
"Sekam padi dan serbuk gergaji adalah biomassa yang melimpah di Indonesia sebagai negara agraris sehingga dapat dimanfaatkan dengan baik sebagai bahan bakar energi terbarukan pada proses gasifikasi. Tipe reaktor gasifikasi Fixed Bed Downdraft menjadi pilihan karena jenis reaktor yang sederhana, memungkinkan berbagai bahan bakar, dan menghasilkan syngas relatif bersih dengan kandungan tar dan partikel yang kecil sehingga memiliki efisiensi tinggi. Tujuan dari tesis ini adalah mengetahui nilai optimum kalor dan efisiensi termal pada variasi nilai rasio ekivalensi, suhu gasifikasi dan campuran sekam dan sebuk gergaji melalui proses simulasi berbasis semi kesetimbangan. Hasil simulasi data gas sintesis yang disajikan berupa CH4, H2, CO dan CO2 yang divalidasi dengan literatur eksperimen dan simulasi. Variabel terikat dalam tesis ini adalah laju alir massa feedstock senilai 1,7 kg/jam dengan variasi rasio ekivalensi 0,18, 0,23, 0,27, dan 0,31, variasi suhu gasifikasi 400oC hingga 1000oC dan variasi campuran umpan senilai 100% sekam, 75:25, 50:50, 25:75 dan 100% serbuk gergaji. Adapun olah data yang diperlukan yaitu menghitung rasio ekivalensi, berat molekul gas dan biomassa, densitas syngas, massa syngas per massa biomassa dan nilai Lower Heating Value (LHV). Pada akhirnya, hasil riset ini menunjukkan bahwa rasio ekivalensi optimum ditemukan senilai 0,27 dengan kalor syngas paling maksimum sebesar 3,05 MJ/kg untuk sekam dengan effsiensi 29,26% dan 4,99 MJ/kg untuk serbuk gergaji dengan effsiensi 34,51%. Sedangkan suhu optimum ditemukan senilai 700oC pada sekam dengan kalor syngas 3,38 MJ/kg effsiensi 32,36% dan 750oC pada serbuk gergaji sebesar 5,84 MJ/kg effisiensi 40,42%. Ditambah lagi seiring tambahan campuran 25% serbuk gergaji pada sekam dapat meningkatkan rata-rata kalor syngas dan termal effisiensi masing-masingnya sebesar 3% dan 1,93%.
Rice husks and sawdust are abundant biomass in Indonesia as an agricultural country so that they can be utilized properly as renewable energy fuels in the gasification process. The Fixed Bed Downdraft gasification reactor type was chosen because the reactor type is simple, allows for a variety of feedstocks, and produces relatively clean producer gas with small tar and particle content so that it has high efficiency. The purpose of this research is to determine the optimum value of energy and thermal efficiency for variations of the equivalence ratio, gasification temperature and mixture of rice husks and sawdust through simulation process based a semi-equilibrium method. The results of the simulation of the syngas data presented the content of CH4, H2, CO and CO2 were validated by the experimental and simulation literature. The dependent variable in this research is the feedstock mass flow rate of 1.7 kg/hour with variations of the equivalence ratio of 0.18, 0.23, 0.27, and 0.31, the variation of the gasification temperature from 400oC to 1000oC and the variation of the feedstock mixture as 100% rice husk, 75:25, 50:50, 25:75 and 100% sawdust. Then data processing required is to calculate the equivalence ratio, gas and biomass molecular weight, syngas density, syngas mass per biomass mass and Lower Heaing Value (LHV) value. Finally, the results of this research showed that the optimum equivalence ratio was found to be 0.27 with the maximum syngas energy as 3.05 MJ/kg for husk with an efficiency of 29.26% and 4.99 MJ/kg for sawdust with an efficiency of 34, 51%. Meanwhile, the optimum temperature was found to be 700oC in husk with syngas energy of 3.38 MJ/kg efficiency of 32.36% and 750oC on sawdust of 5.84 MJ/kg efficiency of 40.42%. In addition, adding 25% sawdust to the rice husks can increase the average syngas energy and thermal efficiency by 13% and 1.93%, respectively."
Depok: Fakultas Teknik Universitas Indonesia, 2022
T-pdf
UI - Tesis Membership  Universitas Indonesia Library
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Imaduddin Haq
Pengaruh massa abu sekam padi terhadap sustainability zona pirolisis pada gasifier tipe downdraft fixed bed kapasitas 10 KG/Jam = Effect of mass of rice husk ash towards sustainability pyrolysis zone in gasifier downdraft fixed bed type with capacity 10 KG/Hr
"Pembentukan pirolisis yang keberlanjutan (sustainable pyrolysis) adalah kunci dari keberhasilan proses gasifikasi. Zona pirolisis pada proses gasifikasi merupakan akibat reaksi endotermis yang mendapatkan energi panas dari proses oksidasi (combustion) antara bahan bakar dengan oksigen. Perekahan biomassa sekam padi hasil pirolisis yang berupa arang, uap air, uap tar, dan gas - gas (CO, H2, CH4, CO2, dan N2) harus dijaga pada temperatur pirolisis untuk mendapatkan gas hasil (producer gas) atau syngas (synthetic gas) yang berlimpah. Keberhasilan proses gasifikasi diperoleh dengan mendapatkan debit syngas secara kontinyu dan diindikasikan oleh konsistensi nyala api pada gas burner. Hal ini sangat dipengaruhi oleh faktor pengoperasian gasifier dan kesetimbangan massa (mass balance) antara feeding rate sekam padi dengan laju pembuangan abu (ash removal rate). Eksperimental yang dilakukan adalah menggunakan gasifier tipe downdraft fixed bed kapasitas 10 kg/jam dimana sebelum terjadinya modifikasi gasifier pada sistim pembuangan abu sekam padi sangat sulit untuk mendapatkan kontinuitas syngas. Kekurangstabilan laju alir syngas diperkirakan adanya akumulasi abu sisa gasifikasi pada zona combustion dan plenum chamber.
Dengan melihat zona pirolisis yang terjadi pada temperatur antara 400 - 800 oC terlihat laju temperatur yang cepat yang mengakibatkan tidak stabilnya proses pirolisis sehingga didapat kurangnya debit syngas. Selain itu, pengaturan (laju) massa sekam padi yang masuk kedalam gasifier dan pengaturan pembuangan abu dapat mempengaruhi sustainability proses pirolisis. Modifikasi sistim pembuangan abu dan angsang (grate) abu dapat mempermudah pengaturan sejumlah massa abu yang dikeluarkan sehingga dapat mengendalikan zona temperatur pirolisis dengan baik.
Kajian eksperimental dilakukan untuk mengetahui pengaruh jumlah massa abu sekam padi yang dibuang terhadap sustainability zona pirolisis. Didapat bahwa jumlah abu sekam padi yang dibuang sebesar 60 ? 90 gram per satu kali pembuangan (operasi sistim ash removal) untuk setiap 20 menit atau rata ? rata laju pembuangan abu sekam sebesar 5 gram/menit. Dari beberapa eksperimental ini, diharapkan dapat terlihat fenomena proses gasifikasi sekam padi dan pengaruhnya terhadap zona pirolisis akibat pembuangan sejumlah massa abu sekam padi. Sehingga penelitian ini dapat menemukan suatu korelasi untuk mendapatkan unjuk kerja (performance) gasifier yang optimal.
The establishment of sustainable pyrolysis is key to the success of the gasification process. Pyrolysis zone in the gasification process is the result of an endothermic reaction that get hot energy from the oxidation process of the fuel with oxygen. Cracking of rice husk biomass pyrolysis results in the form of charcoal, water vapor, tar vapors, and gases (CO, H2, CH4, CO2, and N2) must be maintained at a pyrolysis temperature to obtain synthetic gas (syngas) with plantyful harvest. Success of the gasification process to obtain syngas continuously and are indicated by the consistency of the flame on a gas burner. It is highly influenced by the operation of the gasifier and the mass balanced beetwen rice husk feeding rate and ash removal rate. The experiment was performed under gasifier downdraft fixed bed type with capacity 10 kg/hour, previously to the modification of the gasifier on rice husk ash removal system is very difficult to obtain syngas. Unstable syngas flow rate is estimated from the accumulation of ash residue gasification process of combustion area and plenum chamber.
By looking at the pyrolysis zone occurs at temperatures between 400 ? 800 oC seen rapidly of temperature rate results in insteability of the pyrolysis process in order to get a lack of producer gas. Besides of setting rice husk rate into the gasifier and ash removal rate arrangements affecting sustainable pyrolysis process. Ash removal system modifications can facilitate setting a mass of ash removed so that it can control the pyrolysis temperature zone well.
The experimental study was conducted to determine the effect of mass quantities of rice husks ash is removed towards sustainability pyrolysis zone. Founded that the amount of rice husk ash removed are 60-90 grams per one removal for every 20 minutes or an average of rice husk ash removal rate of 5 gr/minutes. Some of this experimental phenomena is expected to be seen rice husks gasification process and its effect on the pyrolysis zone as a results of the removing of a mass of rice husks ash. So that this research can be find a correlation to obtain optimal performance of the gasifier."
Depok: Fakultas Teknik Universitas Indonesia, 2016
T45410
UI - Tesis Membership  Universitas Indonesia Library
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Hafif Dafiqurrohman
Modifikasi air intake pada gasifier sekam padi tipe fixed bed downdraft kapasitas maksimum 30 kg/jam = Air intake modification for rice husk gasifier downdraft fixed bed types with maximum capacity 30 kg/h
"Sekam padi menjadi salah satu limbah biomassa yang melimpah di Indonesia. Salah satu cara konversi sekam padi menjadi energi alternatif adalah gasifikasi biomassa. Gasifikasi biomassa merupakan proses termokimia untuk mengonversi bahan baku biomassa menjadi bahan bakar gas atau bahan baku gas kimia (producer gas). Gasifikasi biomassa yang tengah dikembangkan adalah tipe fixed bed downdraft. Tipe ini dipilih karena hasil tar yang sedikit dan cocok untuk skala mikro. Salah satu permasalahan dari desain reaktor gasifikasi biomassa yang digunakan adalah kurang meratanya proses oksidasi parsial, sehingga memengaruhi zona pirolisis. Proses oksidasi parsial yang kurang merata ini disebabkan oleh pada bagian tengah reaktor tidak tersuplai udara dengan merata.
Pada penelitian sebelumnya yang menggunakan cangkang kelapa dan sekam padi, equivalence ratio (ER) untuk proses gasifikasi adalah 0,4. Maka untuk melakukan optimasi zona pirolisis, dilakukan modifikasi air intake dengan menambahkan circular air intake. Setelah dilakukan modifikasi dan pengujian pada temperatur operasional zona pirolisis 300-700 oC, dengan melakukan variasi ER yaitu 0,19, 0,24, 0,27, dan 0,31, akhirnya didapatkan ER paling optimal untuk menghasilkan producer gas dengan kualitas baik yaitu pada ER 0,24. ER paling optimal ini sesuai dengan standar gasifikasi biomassa, yaitu sekitar 0,25.
Rice husks into one of abundant biomass waste in Indonesia. One way of converting rice husks into alternative energy is biomass gasification. Biomass gasification is a thermochemical process to convert biomass feedstock into fuel gas or chemical feedstock gas (producer gas). Gasification of biomass that is being developed is a type of fixed bed downdraft. This type is chosen because the results were a little tar and suitable for the micro scale. One of the problems of biomass gasification reactor design used is less inequality partial oxidation process, thus affecting the pyrolysis zone. Partial oxidation process is uneven due to the middle part of the reactor is not well supplied with evenly distributed air.
Previous studies using coconut shells and rice husks, equivalence ratio (ER) for the gasification process is 0.4. Then to optimize the pyrolysis zone, be modified by adding circular air intake. After the modification and testing the operating temperature pyrolysis zone of 300-700 °C, by doing ER variation is 0.19, 0.24, 0.27, and 0.31, eventually obtained the most optimal ER to produce gas producer with good quality, namely the ER 0.24. This ER is the most optimized according to the standard gasification of biomass, which is about 0.25."
Depok: Fakultas Teknik Universitas Indonesia, 2015
S59768
UI - Skripsi Membership  Universitas Indonesia Library
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Ubaedi Susanto
Analisa Teknis Uji Bakar Pelet Sekam Padi dan Kajian Keekonomian Co-Firing Pada Pulverizer Coal (PC) Boiler Sub-Critical 300 MW Studi di PLTU Indramayu = Technical Analysis Of Rice Husk Pellet Combustion Test And Economic Study Of Co-Firing In 300 MW Sub-Critical Pulverizer Coal (PC) Boiler Study in Indramayu Power Plant
"Peningkatan jumlah penduduk telah mendorong peningkatan kebutuhan energi, terutama untuk transportasi dan listrik. Sementara itu, produksi energi fosil yang terus menurun memaksa pemerintah mengimpor minyak bumi untuk memenuhi kebutuhan dalam negeri. Untuk mengantisipasi cadangan energi fosil nasional yang semakin terbatas dan kebutuhan energi masyarakat yang semakin meningkat, pemerintah menggalakkan penggunaan energi terbarukan. Salah satu upayanya adalah dengan co-firing biomassa di pembangkit listrik berbahan bakar batu bara. Di PLTU Indramayu, biomassa yang dipilih adalah sekam padi yang telah mengalami perlakuan pemadatan dan pemanasan, untuk mendapatkan biomassa dengan densitas dan nilai kalor yang lebih baik dari bentuk fisik sekam padi. Batubara sebagai bahan bakar di PLTU Indramayu memiliki nilai kalori rata-rata 4200 kCal/kg, sedangkan pelet sekam padi memiliki nilai kalori rata-rata 3400 kCal/kg. Uji bakar untuk co-firing perlu dilakukan untuk mengetahui kinerja operasi peralatan unit pembangkit. Uji co-firing pada penelitian ini masih terbatas pada komposisi 1% biomassa dan 3% biomassa yang membutuhkan pelet sekam padi sebanyak 43,2 ton dan batubara sebanyak 3196,8 ton. Sebelum dilakukan uji pembakaran boiler, juga dilakukan simulasi numerik Computational Fluid Dynamics (CFD) untuk mendapatkan gambaran awal. Hasil simulasi dan pengujian bahan bakar dengan komposisi sampai 3% biomassa menunjukkan bahwa parameter operasi berada dalam batas normal. Daya output masih bisa mencapai 300 MW, temperatur FEGT 908 oC, fuel flow di pulverizer berkisar 34 – 37 ton/jam, arus pulverizer 33 A. Emisi yang dihasilkan masih di bawah baku mutu sesuai Peraturan Menteri Lingkungan Hidup Nomor 15 Tahun 2019, yaitu emisi SO2 51,46 mg/Nm3 dan NO2 37,19 mg/Nm3. Ditinjau dari keekonomiannya, harga pelet sekam padi Rp 551.558,00 / ton, masih di bawah Harga Patokan Tertinggi di PLTU Indramayu yaitu Rp 552.129,00 / ton.
The increase in population has driven increased demand for energy, especially for transportation and electricity. Meanwhile, fossil energy production continues to decline, forcing the government to import petroleum to meet domestic needs. In order to anticipate the increasingly limited national fossil energy reserves and the increasing public energy needs, the government is promoting the use of renewable energy. One of the efforts is by co-firing biomass in coal-fired power plants. At PLTU Indramayu, the selected biomass is rice husk which has undergone pelletization treatment, compaction, and heating, to obtain biomass with a high density and calorific value better than the physical form of rice husk. Coal as fuel in PLTU Indramayu has an average calorific value of 4200 kCal/kg, while rice husk pellets have an average calorific value of 3500 kCal/kg. Combustion tests for co-firing need to be carried out to determine the operating performance of generating unit equipment. Co-firing tests in this study were still limited to a composition of 1% biomass and 3% biomass which required a total of 43.2 tonnes of rice husk pellets and 3196.8 tonnes of coal. Before the boiler combustion test, computational fluid dynamics (CFD) numerical simulations were also carried out to get an initial description. The results of the simulation and fuel tests show that the operating parameters are in normal limits. The output power is 300 MW, FEGT temperature is 908 oC, fuel flow in the pulverizer ranges from 34 – 37 tons/hour, pulverizer current is 33 A. The emissions are produced below the quality standards according to the Minister of Environment Regulation Number 15 of 2019, which is SO2 emissions 51.46 mg/Nm3 and NO2 37.19 mg/Nm3. From an economic perspective, the price of rice husk pellets is IDR 551,558.00 / ton, still below the highest benchmark price at PLTU Indramayu, which is IDR 552,129.00 / ton."
Jakarta: Fakultas Teknik Universitas Indonesia, 2023
T-pdf
UI - Tesis Membership  Universitas Indonesia Library
cover
Hafif Dafiqurrohman
Air intake modification for pyrolysis optimization on rice husk fixed bed downdraft gasifier with maximum capacity of 30 kg/hour
"Rice husk is one of the
most abundant biomass wastes in Indonesia. One way to convert it into an
alternative source of energy is biomass gasification. This is a thermochemical
process which converts biomass feedstock into fuel gas or chemical feedstock
gas (producer gas). The gasification type which is developed in this study is
fixed bed downdraft type due to its low tar content and compatibility in
microscale implementation. One major problem with the implemented biomass
gasification reactor was ruggedness of the partial oxidation process due to the
absence of air in the reactor?s middle section, which consequently affected the
pyrolysis zone. Several experiments were conducted previously using coconut
shells and rice husks as solid feedstock, where an equivalence ratio (ER) of
0.4 was obtained. Therefore, in order to optimize the pyrolysis zone, the
modification conducted involves adding a circular air intake into the gasifier.
Experiments were conducted in a pyrolysis temperature range of 300?700oC
with ER variation of 0.19, 0.24, 0.27 and 0.31. The results show that a good
quality producer gas is produced at an ER value of 0.24. This value shows a
promising result because the ER value of biomass gasification standard is 0.25."
2016
J-Pdf
Artikel Jurnal  Universitas Indonesia Library
cover
Hafif Dafiqurrohman
Air intake modification for pyrolysis optimization on rice husk fixed bed downdraft gasifier with maximum capacity of 30 kg/hour
"Rice husk is one of the most abundant biomass wastes in Indonesia. One way to convert it into an alternative source of energy is biomass gasification. This is a thermochemical process which converts biomass feedstock into fuel gas or chemical feedstock gas (producer gas). The gasification type which is developed in this study is fixed bed downdraft type due to its low tar content and compatibility in microscale implementation. One major problem with the implemented biomass gasification reactor was ruggedness of the partial oxidation process due to the absence of air in the reactor’s middle section, which consequently affected the pyrolysis zone. Several experiments were conducted previously using coconut shells and rice husks as solid feedstock, where an equivalence ratio (ER) of 0.4 was obtained. Therefore, in order to optimize the pyrolysis zone, the modification conducted involves adding a circular air intake into the gasifier. Experiments were conducted in a pyrolysis temperature range of 300–700oC with ER variation of 0.19, 0.24, 0.27 and 0.31. The results show that a good quality producer gas is produced at an ER value of 0.24. This value shows a promising result because the ER value of biomass gasification standard is 0.25."
Depok: Faculty of Engineering, Universitas Indonesia, 2017
UI-IJTECH 7:8 (2016)
Artikel Jurnal  Universitas Indonesia Library
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