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Hydrogen production and TOC reduction from gasification of lactose by supercritical water

机译:通过超临界水将乳糖气化制氢和减少TOC

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New data were obtained for production of H-2 and reduction of total organic carbon (TOC) by gasification of lactose in supercritical water with(out) the presence of catalysts (NaOH, KOH and Na2CO3) in a continuous Inconel 625 flow reactor. The gasification reactions were carried out at 550-700 degrees C, 22.5 MPa, lactose concentrations in the range of 0.5-2.5 wt%, feed flow rates of 5 and 7 g min(-1) and a total reaction time of 30 min. The optimum condition for the production of H-2 yielded approximately 4.5 mol H-2/mol lactose with a TOG reduction of similar to 95%. In addition, supercritical gasification of whey was carried out using the same operating conditions as the lactose system. A reduction of 92% on the TOG and 0.45 molar fraction of H-2 production was achieved, similar to the gasification of lactose at a concentration of 0.5 wt%. Copyright (C) 2015, Hydrogen Energy Publications, LLC. Published by Elsevier Ltd. All rights reserved.
机译:通过在连续Inconel 625流动反应器中在不存在催化剂(NaOH,KOH和Na2CO3)的情况下,在超临界水中将乳糖气化,获得了H-2的产生和总有机碳(TOC)减少的新数据。气化反应在550-700摄氏度,22.5 MPa,乳糖浓度在0.5-2.5 wt%的范围内,进料流速为5和7 g min(-1)的条件下进行,总反应时间为30分钟。产生H-2的最佳条件可产生约4.5 mol H-2 / mol乳糖,TOG降低约95%。另外,使用与乳糖系统相同的操作条件进行了乳清的超临界气化。与浓度为0.5 wt%的乳糖气化相似,TOG降低了92%,H-2产生的摩尔分数为0.45。 Hydrogen Energy Publications,LLC版权所有(C)2015。由Elsevier Ltd.出版。保留所有权利。

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