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CO-GASIFICATION OF BLACK LIQUOR AND PULP SLUDGE FOR FUEL PRODUCTION

机译:黑液和纸浆污泥的共气化,用于燃料生产

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In this research, product distribution and energy efficiency from co-gasification of pulp sludge mixedwith black liquor has been suggested as a relatively new technology that can be used in addition to recovery boiler inthe chemical recovery process. This research was carried out in a fixed bed reactor. The operating parametersincluding temperature of 700, 800 and 900°C, equivalence ratio (ER) of 0.2, 0.4 and 0.6 and ratio of pulp sludge toblack liquor of 50:50 and 40:60 at feeding rate of 5 g/min were examined. In addition, Ni-La-Mg/Al_2O_3 catalyst wasprepared by co-impregnation method and mixed with raw material before feeding into system to study its effect onthermochemical conversion reaction. Major gaseous products such as CO, CO_2, H_2 and CH_4 were analyzed by TCDNDIRanalyzer. Char and tar residue were collected and calculated by measured weight. The results of non-catalyticcases indicated that the optimal condition was temperature of 900°C, ER of 0.2 and raw material ratio 40:60 with gasyield of 69.18%, H_2 to CO ratio of 0.96, lower heating value of 5.91 MJ/m~3 and cold gas efficiency of 79.55%. Forcatalytic cases, it was found that the catalyst can improve the percentage of gas yield around 10 wt%. Lower heatingvalue and cold gas efficiency of catalytic cases were 3.78-6.73 MJ/m3 and 46.02-90.13% while those obtained fromnon catalytic trials were 3.37-5.91 MJ/m3 and 34.63-79.55%, respectively. From these results, co-gasificationprocess can be considered as alternative option for conversion pulp sludge mixed with black liquor to usable fuelproducts.
机译:在这项研究中,纸浆污泥混合气化产生的产品分布和能源效率 有人建议将黑液作为一种相对新的技术,除了回收锅炉中可以使用的之外。 化学回收过程。这项研究是在固定床反应器中进行的。运行参数 包括温度700、800和900°C,当量比(ER)为0.2、0.4和0.6以及纸浆污泥与 检查进料速度为5 g / min的50:50和40:60的黑液。另外,Ni-La-Mg / Al_2O_3催化剂为 通过共浸渍法制备并与原料混合后再进料,以研究其对体系的影响 热化学转化反应。 TCDNDIR分析了主要气体产物,例如CO,CO_2,H_2和CH_4 分析仪。收集焦炭和焦油残渣,并通过测得的重量进行计算。非催化的结果 案例表明,最佳条件是温度为900°C,ER为0.2,原料比为40:60(含气体) 产率为69.18%,H 2与CO的比率为0.96,较低的发热量为5.91 MJ / m〜3,冷气效率为79.55%。为了 在催化情况下,发现该催化剂可以将气体产率的百分比提高约10wt%。降低加热 催化箱的热值和冷气效率分别为3.78-6.73 MJ / m3和46.02-90.13%,而催化箱为 非催化试验分别为3.37-5.91 MJ / m3和34.63-79.55%。从这些结果来看,共气化 该工艺可被视为将与黑液混合的纸浆污泥转化为可用燃料的替代选择 产品。

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