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Energy Process-Step Model of Hydrogen Production in the U.S. Chemical Industry

机译:美国化学工业中氢气生产的能量过程步骤模型

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This paper gives a representative energy process-step model of hydrogen production in the U.S. Chemical Industry based on federal data. There have been prior efforts to create energy process-step models for other industries. However, among all manufacturing industries, creating energy flow models for the U.S. Chemical Industry is the most challenging one due to the complexity of this industry. This paper gives concise comparison of earlier studies and provides thorough description of the methodology to develop energy process-step model for hydrogen production in the U.S. Chemical Industry. Results of the energy process-step model of hydrogen production in the U.S. Chemical Industry show that steam allocations among the end-uses are 68% to process cooling (steam injection to product combustion gases), 25% to process heating, and 7% to other process use (CO_2 converter). The model also shows that the major energy consuming step in hydrogen production is the reformer, which consumes approximately 16 Peta Joules (PJ) fuels. During the course of this study, the most recent U.S. federal energy database available was for the year 1998. Currently, the most recent available U.S. federal energy database is given for the year 2002 based on the data collected from 15,500 establishments.
机译:本文根据联邦数据提供了美国化学工业中氢气生产的代表性能源过程步骤模型。先前已经做出努力来为其他行业创建能源过程步骤模型。但是,在所有制造业中,由于该行业的复杂性,为美国化学工业创建能流模型是最具挑战性的模型。本文对早期研究进行了简要的比较,并对开发美国化学工业中氢气生产的能源工艺步骤模型的方法进行了详尽的描述。美国化学工业中氢气生产的能源过程步骤模型的结果表明,最终用途之间的蒸汽分配分别为过程冷却的68%(向产品燃烧气体注入蒸汽),过程加热的25%,以及最终的7%。其他过程使用(CO_2转换器)。该模型还显示,制氢中的主要能源消耗步骤是重整器,该重整器消耗约16皮塔焦耳(PJ)燃料。在此研究过程中,可用的最新美国联邦能源数据库是1998年。当前,根据从15500家企业收集的数据,给出了2002年的可用的美国联邦能源数据库。

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