共查询到19条相似文献,搜索用时 62 毫秒
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以乙醇-正丙醇精馏分离为模拟对象,利用Aspen Plus模拟软件中的WILSON模型对模拟体系中的相关参数进行回归。此外,相关的物性方法选择精馏模块RADFRAC对精馏过程进行模拟及建立,然后对精馏模拟过程中影响产品纯度的因素进行分析。最后得出进料中乙醇的百分含量为0.25,正丙醇的百分含量为0.75时进行精馏分离得到乙醇产品纯度最高且能耗低的最佳操作条件。 相似文献
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有机硅单体是一种多组分混合物,其组分沸点相近,产品纯度要求高,因此其分离纯化相当困难。目前工业上主要有5种有机硅单体分离系统的工艺流程,文中采用流程模拟软件对5种工艺流程进行严格模拟计算,将模拟结果带入相关的费用计算模型,计算不同工艺流程的设备费用与操作费用,并计算比较各工艺流程的年度总费用(TAC)。中切流程在5种工艺流程中的年度总费用最低。以中切流程为初始序列,利用调优法进行调优并找出4组相邻分离序列。采用流程模拟软件对4组分离序列进行精确模拟计算,计算并比较4组序列的年度总费用。结果表明:调优序列3的年度总费用最低,较初始中切流程总费用降低了1.74%,因此选定调优序列3为分离有机硅单体的最优序列。 相似文献
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采用模拟软件Aspen Plus对某厂大型煤化工甲醇四塔精馏过程进行稳态模拟计算和分析,结果表明,应用物性方法 UNIFAC-DMD能有效模拟汽液平衡数据,模拟结果与工厂采集数据吻合良好。进行了常压塔侧线抽提位置分析、回流比对产品各组分浓度影响及精馏塔水力学分析等研究,提供了可行的精馏操作方案。 相似文献
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I. V. Zhigacheva L. S. Evseenko E. B. Burlakova M. G. Voronkov L. V. Krivosheeva 《Catalysis in Industry》2011,3(2):170-175
Natural zeolites (klinoptiolits) were treated with Onkosorb adsorbent (N,N′-bis(3-triethoxysilyl-propyl-thiocarbamide)) to attain greater nitrosamine (NA) and polycyclic aromatic hydrocarbon (PAH) adsorption capacity. The efficiency of volatile NA recovery rose from 30 to 77%; that of PAH recovery, from 20 to 63.7 %. The increased adsorption efficiency of the toxicants from an air-gas mixture was also reflected in biological indicators. Prolonged exposure of rats to the air-gas mixture (similar in composition to the air in industrial zones) led to a 25% reduction in the maximum rates of succinate oxidation and the efficiency of oxidative phosphorylation in liver mitochondria. The changes in the energetics of mitochondria were apparently associated with the action of the toxicants, as is indicated by a 22 % increase of P-450 cytochrome content in the liver tissue. An air-gas mixture passed through an Onkosorb adsorbent layer on zeolite did not produce any of the above changes in the mitochondrion energetics or the effect on P-450 cytochrome content in the liver tissue. We assume a high level of efficiency for Onkosorb adsorbent on zeolite in PAH and NA absorption. 相似文献
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Gas-to-liquid (GTL) involves the chemical conversion of natural gas into synthetic crude that can be upgraded and separated into different useful hydrocarbon fractions including liquid transportation fuels. Such technology can also be used to convert other abundant natural resources such as coal and biomass to fuels and value added chemicals (referred to as coal-to-liquid (CTL) and biomass-to-liquid (BTL)). A leading GTL technology is the Fischer-Tropsch (FT) process. The objective of this work is to provide a techno-economic analysis of the GTL process and to identify optimization and integration opportunities for cost saving and reduction of energy usage while accounting for the environmental impact. First, a base-case flowsheet is synthesized to include the key processing steps of the plant. Then, a computer-aided process simulation is carried out to determine the key mass and energy flows, performance criteria, and equipment specifications. Next, energy and mass integration studies are performed to address the following items: (a) heating and cooling utilities, (b) combined heat and power (process cogeneration), (c) management of process water, (c) optimization of tail gas allocation, and (d) recovery of catalyst-supporting hydrocarbon solvents. Finally, these integration studies are conducted and the results are documented in terms of conserving energy and mass resources as well as providing economic impact. Finally, an economic analysis is undertaken to determine the plant capacity needed to achieve the break-even point and to estimate the return on investment for the base-case study. 相似文献
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电石法生产的乙炔气中常含有H2S、PH3等杂质,产品达不到GB6819-1996《溶解乙炔》的要求,因此,用电石法生产的产品必须采用净化工艺除杂质。净化方法有干法和湿法两种,由于干法净化使用固体净化剂,净化后净化剂大都带有毒性物质,直接排放会造成环境污染,回收利用又不经济,这种方法已被禁止采用。现在推行湿法净化,使用液体净化剂,最常用的是NaClO和浓H2SO4,利用这两种物质具有氧化性的特点,将乙炔气中的气相:H2S,PH3等杂质氧化生成可溶性物质而转入液相,使乙炔气达到净化的目的。不同的净化剂采用不同的工艺流程,下面从净化工艺和生产过程的经济价值加以比较。 相似文献
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《Gas Separation & Purification》1988,2(1):9-15
Membrane gas separation processes, while becoming more widespread, suffer from inherent limitations in their use. Combining membranes with other gas separation processes has been found to be an effective means of overcoming these limitations. A combination of hybrid process comprising a membrane unit with a cryogenic process has been found of value for producing hydrogen from a rather dilute source such as FCC off-gas. The success of the hybrid stems from the use of each component part of the process in its region of greatest efficiency. The judicious combination of processes leads to an overall process that is not only more efficient than either of the component processes, but more cost-effective as well. 相似文献
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《化学工业与工程技术》2016,(5):71-76
介绍了低温甲醇洗流程和聚醇醚流程的应用现状,评述了低温甲醇洗流程和聚醇醚流程的工艺特点,分析比较了2种工艺的主要技术指标,着重比较了2种工艺的关键运行参数如溶液消耗、冷量消耗、消耗指标、设备以及投资费用等,并对2种工艺流程的适应性进行了分析。分析和比较后认为:酸性气体吸收流程的选择需综合考虑能耗、装置规模、投资、可操作性、装置稳定性等因素;低温甲醇洗适用于净化度要求高、高压、大规模的工业化装置;聚醇醚工艺适用于净化度要求较低的装置,如IGCC多联产装置,可降低能耗,节省投资。 相似文献
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生物质制油过程可分为生物质收集、生物质快速热解、生物油气化、水汽变换、酸性气体净化和二氧化碳捕集、费托(FT)合成和合成原油提炼,以及尾气处理等部分。公用工程系统通过燃料燃烧产生蒸汽、发电、做功,以满足生产过程所需的蒸汽、水、电、功等。公用工程系统燃料为生产过程尾气,外购天然气或其他燃料。生产过程尾气主要包括费托合成过程和合成原油提炼过程尾气,其主要成分为CO、H2、CH4、C2H6、C3H8。生产过程尾气既可以作为公用工程系统燃料,也可以通过重整操作回收其有效组分CO和H2在生产系统循环利用,但公用工程系统需补充外购燃料。本研究以麦秆为生物质原料,基于生产过程和公用工程系统ASPEN模拟,分析生产过程操作参数和尾气处理方式对生产过程产品产量,公用工程系统燃料选择的影响,根据年总收益最大化确定最优的麦秆制油过程和公用工程系统设计。 相似文献