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INDONESIA
Jurnal Energi dan Lingkungan (Enerlink)
Published by Badan Pengkajian dan Penerapan Teknologi
ISSN : 02169541     EISSN : -     DOI : -
Core Subject : Science,
Energy
Enerlink adalah jurnal yang diterbitkan 2 kali setahun oleh Pusat Teknologi Pengembangan Sumberdaya Energi dan Industri Kimia BPPT di bidang energi dan lingkungan. Enerlink is a scientific journal that publishes twice annually by Centre of Energy Technology and Chemical Industry of BPPT.
Arjuna Subject : -
Articles 322 Documents
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EFEK GAYA ANTAR PARTIKEL DAN DIAMETER PARTIKEL TERHADAP KECEPATAN MINIMUM FLUIDISASI Febijanto, Irhan
Jurnal Energi dan Lingkungan (Enerlink) Vol 5, No 2 (2009)
Publisher : Jurnal Energi dan Lingkungan (Enerlink)

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Abstract

In this study, the effect of diameter particle and the effect of inter-particlecohesion force due to liquid bridge formation on the minimum fluidization velocityin the fluidized bed have investigated. Also the effect of inter-particle cohesionforce on a fluidization condition of the bed has observed by video camera. Theinvestigation results showed bigger diameter can give higher minimumfluidization velocity, and stronger inter-particle force can give higher minimumfluidization velocity, and then make a quality of fluidization of bed lower. Usingwith this investigation results, the mechanism of fouling and slaggingphenomena, which are happen in the coal-fired boiler can be explained.Kata kunci: fluidized bed, minimum fluidization velocity, particle diameter,relative humidity, inter-particle cohesion force
PENGARUH WAKTU REAKSI TERHADAP KARAKTERISTIK PENCAIRAN BATUBARA BANKO SELATAN Artanto, Yuli; Yusnitati, Yusnitati
Jurnal Energi dan Lingkungan (Enerlink) Vol 2, No 1 (2006)
Publisher : Jurnal Energi dan Lingkungan (Enerlink)

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Abstract

Investigation of Limonite for catalyst on South Banko coal liquefaction werecarried out under standard condition which has developed by BPPT.Limonite Soroako is a natural mineral that found at Nickel Mining onSoroako, South Sulawesi. Four samples of limonite was examined using 5Lautoclave at our coal liquefaction laboratory in order to investigate theisactivities to produce high distillate yield at standard condition (450oC, 9MPacold H2). The results showed that limonite SYY-E-MY gave a higher distillateyield than those of other limonite (difference about 10-30%daf coal or%bkta). Further investigations were conducted to compare with othercatalysts: synthetic g –FeOOH and pyrite (FeS2). Again, the activity of limonitS99-E-MY was still superior compared to those of synthetic and pyritecatalysts. The yield difference was about 10-16%daf coal or %bkta).Experiment revealed that the factor of FeOOH critically affected the coalliquefaction reaction to improve the distillate yield and to reduce CLB yield.Besides, the representative of Co metal in the limonite (≥5-10 %bk) couldgive synergism effect with FeOOH to improve the activity of limonite.
PEMANFAATAN TUNGKU BERBAHAN BAKAR LPG DAN MODIFIKASI RUANG BAKAR UNTUK PEMBAKARAN KERAMIK UKIR BERGLASIR Effendi, M. Dachyar
Jurnal Energi dan Lingkungan (Enerlink) Vol 6, No 1 (2010)
Publisher : Jurnal Energi dan Lingkungan (Enerlink)

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Abstract

A downdraft kiln using LPG as energy source with capacity 1 m3 and maximumfiring temperature 13000C has been constructed and midified to give better heatdistribution. For firing ceramic process, most of Balinese and Lombok craftsmenuse firewood as energy source. This method is inefficient from the production rate.Point of view, downdraft kiln can help the craftsmen to process ceramic easier,faster and cheaper. Downdraft kiln using LPG has been selected as an alternativekiln due to minimum pollutant produced compare with updraft kiln using coal orfirewood. The kiln constructed has fulfilled the requirement of kiln firing processquality in which the firing causes sintering process in the ceramics body. The kilnwith a capacity of 1m3 can reach a maximum firing temperature which of 13000C.To test this modified kiln, some carved ceramic has burned into the kiln. Carvedceramic has been chosen caused by need more good heat distribution than otherceramic design product and have differ thickennes in all bodies.The final productgive a better product whithout defect compare to product burned into unmodifiedkilnKata kunci: tungku hemat energi, keramik ukir, stoneware
FRONT COVER Yusnitati, Yusnitati
Jurnal Energi dan Lingkungan (Enerlink) Vol 7, No 1 (2011)
Publisher : Jurnal Energi dan Lingkungan (Enerlink)

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Abstract

EFEK KATALITIK Natrium-AlO2 PADA PROSES PENCAIRAN BATUBARA TANPA PELARUT HIDROGEN DONOR Artanto, Yuli; Yusnitati, Yusnitati
Jurnal Energi dan Lingkungan (Enerlink) Vol 2, No 2 (2006)
Publisher : Jurnal Energi dan Lingkungan (Enerlink)

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Abstract

Indonesian brown coal, South Banko coal, was liquefied into oil in the presence ofcarbon monoxide and water using alkali base catalyst, NaAlO2. Liquefaction testwas carried out using microautoclave in the absence of donor solvent. Experimentwas conducted at 365oC and 400oC in order to examine the effect of temperatureon coal conversions.Kata kunci: south banko, brown coal, liquefaction, catalyst, donor solvent
KOMPARASI KARAKTERISTIK PENCAIRAN BATUBARA BANKO SELATAN DAN YALLOURN AKIBAT PERUBAHAN TEMPERATUR Artanto, Yuli; Hartiniati, Hartiniati
Jurnal Energi dan Lingkungan (Enerlink) Vol 3, No 1 (2007)
Publisher : Jurnal Energi dan Lingkungan (Enerlink)

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Abstract

A coal liqueafaction test was carried out to investigate the reactivity of anIndonesian brown coal, called South Banko, and an Australian brown coal, calledYallourn. The liquefaction reaction was conducted to ascertain the effect ofreaction temperature on the reactivity of both brown coals and it represents onthe oil, CLB, CO+CO2 and C1~C4 yields. The result shows that South Banko coalis more reactive than Yallourn coal. South Banko coal gives a higher oil yieldthan that of Yallourn. Oil derived from South Banko coal increases as reactiontemperature rises. In contrast, oil derived from Yallourn decreased as reactiontemperature increased. This result indicated that South Banko has more labilestructure than that of Yallourn and it can easily break down the structure of SouthBanko coal. In term of hydrocarbon gas, Yallourn produces higher yield than thatof South Banko. This suggests that Yallourn coal has alkyl groups in its structure.It was also found that CO+CO2 yields are similar to both brown coals. SouthBanko has less CLB yield than that of Yallourn but the CLB yield of South Bankocoal is higher than that of Yallourn while temperature is increased to 470oC. Inshort, the study shows that South Banko coal is more reactive than that ofYallourn coal and it is very potential for the coal liquefaction feedstock.Kata kunci: batubara muda, Banko Selatan, Yallourn, distillate yield, CLB,CO+CO2,C1-C4, feedstock
Evaluasi Hate Rate dan Efisiensi suatu PLTU dengan menggunakan Batubara yang Berbeda dari Spesifikasi Design Aziz, Amiral; Hasan, Andi Rinaldi
Jurnal Energi dan Lingkungan (Enerlink) Vol 11, No 1 (2015)
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Abstract

Tulisan ini menampilkan beberapa hasil penelitian yang dilakukan untuk mengevaluasi hate rate dan efisiensi PLTU batubara berkapasitas 300 MW yang menggunakan spesifikasi batubara yang berbeda dari spesifikasi rancangan setelah beroprasi sekitar dua tahun. Hasil dari penelitian ini memperlihatkan bahwa efisiensi boiler (HHV basis) pada pengujian aktual 100% LRC mengalami penurunan sebesar 3,25% dan pada pengujian dengan komposisi 50% LRC dan 50% MRC mengalami mengalami penurunan sebesar 2,91% dibandingkan dengan hasil komisioning. Kehilngan panas karena gas buang kering, kandungan air dalam bahan bakar dan pembakaran hidrogen memberikan kontrobusi yang besar terhadap penurunan efisiensi boiler dibandingkan dengan hasil komisioning. Pada beban maksimun, turbine hate rate pada 2 (dua) pengujian aktual 100% LRC masing-masing sebesar 1.994, 67 kcal/kWh dan 1.918,55 kcal/kWh, sedangkan pada pengujian dengan komposisi 50% LRC dan 50% MRC turbine hate rate adalah 1.977,52 kcal/kWh. Nilai tersebut lebih rendah 4,47% dan 3,78% untuk pengujian aktual 100% LRC dan lebih rendah 3,45% untuk pengujian 50% LRC dan 50% MRC dibandingkan dengan hasil komisioning. Gross plant hate rate (HHV basis) pada 2 (dua) pengujian 100% LRC masing-masing 2.320,60 kcal/kg dan 2.293,63% kcal/kg, sedangkan pengujian 50% LRC dan 50% MRC gross plant hate rate (HHV basis) adalah 2.290,75 kcal/kg.  Nilai ini lebih besar masing-masing sebesar 3,28%, 2,08% dan 1,95% dibandinkan hasil komisioning (2.246.84 kcal/kWh)
FUNDAMENTAL STUDY ON LIQUEFACTION OF KALIMANTAN BROWN COALS Hartiniati, Hartiniati; Silalahi, Lambok Hlarius
Jurnal Energi dan Lingkungan (Enerlink) Vol 3, No 2 (2007)
Publisher : Jurnal Energi dan Lingkungan (Enerlink)

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Abstract

Efek karakateristik batubara terhadap yield produk pencairan batubaradiinvetigasi menggunakan sampel batubara dari Berau (Lati dan Kelai), Mulia,Wara dan Kideco. Batubara Banko dari Tanjung Enim, Sumatera Selatan,digunakan sebagai batubara rujukan. Pengujian pencairandilaksanakanmenggunakan gas-flow type autoclave (5L) dengan umpanbatubara 2002 (daf), pelarut batubara turunan (b.p.300-420oC) 400g, katalis Fe1.0-3.0 wt% (daf), elemen sulfur (rasio atom S/Fe 2.,0) pada tekanan 14.7MPa,suhu 450oC selama 60menit. Sampel limonit dari Soroako Indonesia dan YandiYellow dari Australia, yang terutama terdiri dari α-FeOOH, digunakan sebagaibahan katalis pada pengujian pencairan batubara. Studi ini merekomendasikanbertambahnya minyak yield akibat peningkatan kandungan oksigen dalambatubara, rasio atom H/C dan kandungan besi dalam batubara, mengingat besidalam batubara dapat berfungsi sebagai katalis dalam pencairan batubara.Limonit Soroako medium grade (MGL) menunjukkan aktifitas lebih tinggidibandingkan Yandi Yellow (YY) karena sifat transformasinya membentuk kristalkristalpyrrhotite (Fe1-XS), fase aktif dalam pencairan batubara. Sejumlahsenyawa nitrogen dan sulfur dalam minyak batubara telah berhasil dihilangkanmelalui proses hydrotreatment selanjutnya memperbaiki mutu produk.Keywords: pencairan, batubara berau, limonit, pyrrhotite, soroako,hydrotreatment
REAKTIFITAS BERBAGAI JENIS PELARUT DARI RESIDU KILANG MINYAK PLAJU PADA PENCAIRAN BATUBARA BANKO TENGAH Hartiniati, Hartiniati
Jurnal Energi dan Lingkungan (Enerlink) Vol 5, No 1 (2009)
Publisher : Jurnal Energi dan Lingkungan (Enerlink)

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Abstract

An effect of two different residue for liquefaction of Central Banko coal isdisccused. The residue was obtained from side-stream of refinery plant, whichso-called long residue and short residue solvents. The liquefaction test wascarried out under the reference conditions that have been developed in BPPTcoal liquefaction laboratory, at temperature of 450oC and initial H2 pressure of12MPa for 1 hour. The result shows that the distillate yield, Bottom (BTM) yield,and hydrogen consumption were dependent on the nature of solvent. Shortresidue solvent shown higher reactivity than the long residue. Reaction betweenCentral Banko and Short Residue gave distillate yield higher than the longresidue. Moreover, its BTM yield was also lower than that of long residue solvent.This result confirmed the lower hydrogen consumption for reaction short residueand Central Banko coal compared to that for reaction long residue and CentralBanko. In this study, it also confirmed that the yield of H2O and CO+CO2 weredependent on the material input condition. However, the yield of hydrocarbongases (C1~C4) was mainly affected by de-alkylation in the solvent and coal duringthe reactionKata kunci: residu minyak bumi, proses pencairan batubara, central Banko
PEMANFAATAN RESIDU KILANG MINYAK PLAJU SEBAGAI PELARUT PADA PROSES PENCAIRAN BATUBARA (Co-Processing) Rasyid, Muhamad Hanif; Hidayat, Herman
Jurnal Energi dan Lingkungan (Enerlink) Vol 4, No 2 (2008)
Publisher : Jurnal Energi dan Lingkungan (Enerlink)

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Abstract

This study presents the investigation on the reactivity of vacuum oil residue(VOR) as solvent in Banko coal liquefaction, so called “Co-processing”. Processsolvent derived from BSU tests is used as reference solvent in this study. Theliquefaction tests are carried out using a gas-flow type autoclave (5L) with 200gcoal (daf), 400g of coal-derived solvent (b.p.300-420 oC), 1.0-3.0 wt% daf as Feof catalyst and elemental sulfur (S/Fe atomic ratio of 2.0) at 14.7MPa, 450oC for60min under a constant gas flow of H2-0.5%H2S. The study suggests that VORas solvent is much more reactive than process solvent under the same condition.Therefore the co-processing gives higher oil yield than coal liquefaction usingprocess solvent derived from BSU tests. It also produces lower CLB, CO+CO2and hydrocarbons yields. This indicates that there is a synergism effect betweenthe VOR as a donor solvent and the coal. The molecular structure of VOR at thefirst time was decomposed into molecular fragments. These fragments were thenattached onto the coal’s structure and lead to decompose the structure of thecoal. It was also found that co-processing consumed less hydrogen gas thanreference liquefaction process. In short, this finding obtained in this study cangive promising sight for implementing the coal liquefaction plant in Indonesia at acommercial scale.Kata kunci: vacuum oil residue, Banko, liquefaction, co-processing reactive,synergism effect

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