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外文期刊>Jurnal Energi Dan Manufaktur
>Pengaruh Temperatur Operasi Dan Kecepatan Superfisial Terhadap Komposisi Gas Produser Pada Gasifikasi Fluidized Bed Berbahan Bakar Sampah Terapung
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Pengaruh Temperatur Operasi Dan Kecepatan Superfisial Terhadap Komposisi Gas Produser Pada Gasifikasi Fluidized Bed Berbahan Bakar Sampah Terapung
Management of waste into energy that is economically possible with fluidized bed gasification technology. Gasification is athermo-chemical process that converts biomass/solid waste into producer gas (CO, H2, CO2 and HC) by using air, steam, oxygenor its mixtures as a gasification agent. In a study of floating waste fuel gasification in pellet form with 1,25 cm diameter and 1.25cm height and of 1.22 gram mass, where is used oxygen enriched air as gasification agent. The operating temperature (Top) atreactor selected 500oC and 600oC with superficial velocities (Uo) are 0.105 m/sec, 0.125 m/sec, 0,145 m/sec., and 0,165 m/sec.From the research results showed that by increasing the operating temperature of 500oC to 600oC and increasing the superficialvelocity of 0.105 m/sec to 0.125 m/sec, did not influence directly the increasing of percentage/levels of CO, CO2 and HC gas thatproduced.
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机译:使用流化床气化技术可以经济地将废物转化为能源。气化是一种热化学工艺,通过使用空气,蒸汽,氧气或其混合物作为气化剂,将生物质/固体废物转化为生产气(CO,H2,CO2和HC)。在对直径为1.25厘米,高度为1.25厘米,质量为1.22克的颗粒状漂浮废物燃料气化的研究中,使用了富氧空气作为气化剂。从500oC和600oC选择的反应器的工作温度(Top),表观速度(Uo)为0.105 m / sec,0.125 m / sec,0,145 m / sec和0,165 m / sec。温度从500oC升高到600oC,并将表面速度从0.105 m / sec增加到0.125 m / sec,并没有直接影响所产生的CO,CO2和HC气体的百分比/水平的增加。
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