The Effect of Temperature and Time of Gasification Process and The Addition of Catalyst to The Composition of The Combustible Gas from The Wastes of Tobacco Leaves With Gasifier Updraft

F. Sulaiman, Endang Suhendi, N. Prastuti, Okta Abdul Choir
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引用次数: 1

Abstract

The increasing industrial production is causing more of energy consumption needed. Tobacco leaves are waste from cigarette production that can be use as alternative biomass energy  to solve the problems of the energy crisis in the near future. Gasification is the conversion of solid carbon raw materials from biomass by the partial oxidation to be combustible gas (CO, H 2 , and CH 4 ) as an energy source. This research uses the fixed-bed reactor with capacity of 300 grams by the flow of updraft and raw material of waste tobacco leaves that have a size -14 + 18 mesh. The influence of temperature was research on 700 o C, 800 o C, and 900 o C with the reaction time for 20 minutes and the addition of a catalyst K 2 CO 3 . gasification medium used air and steam with the constant flow rate 0.504 m3/hour air and 0.0555 kg/minutes steam. Step of the process with the preparation of raw materials, the gasification process, and analysis of gas products. The result of the gasification process analysed using the gas chromatography, and the best results were obtained on the temperature 700 o C in the process time for 10 minutes produced combustible gas are CO = 22.82 % v, H 2 =  26.82 % v, CH 4 = 7.09 % v. increasing production gas happened when a catalyst K 2 CO 3 is added, the producting  of combustible gasses are CO = 52.76 % v, H 2 = 23.46 % v, CH 4 , = 3.23 % v
气化温度、气化时间及催化剂的添加对烟叶废弃物烟气组成的影响
不断增长的工业生产造成了更多的能源消耗。烟叶是卷烟生产的废物,可以用作替代生物质能源,在不久的将来解决能源危机的问题。气化是将生物质中的固体碳原料通过部分氧化转化为可燃气体(CO, h2和ch4)作为能源的过程。本研究采用上升气流流动的300克容量的固定床反应器,原料为-14 + 18目的废烟叶。研究了温度对700℃、800℃和900℃反应的影响,反应时间为20 min,添加催化剂k2co3。气化介质采用空气和蒸汽,空气流量为0.504 m3/小时,蒸汽流量为0.0555 kg/分钟。该过程的步骤包括原料的制备,气化过程,以及气体产物的分析。气化过程的结果分析了使用气相色谱法,最好的结果在温度700度C过程中时间10分钟产生可燃气体有限公司= 22.82% v, v H 2 = 26.82%, CH 4 = 7.09%诉增产气体发生K 2 . 3添加催化剂时,可燃气体的生产公司v = 52.76%, H v 2 = 23.46%, CH 4 v = 3.23%
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