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变压吸附提氢装置氢收率低的原因分析及改进措施 被引量:2
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作者 翟琛 《中氮肥》 2018年第5期42-44,共3页
针对陕西陕化煤化工集团有限公司100 kt/a 1,4-丁二醇项目变压吸附提氢装置运行过程中存在的原料气消耗较高、解吸气量较大、产品氢收率低等问题,分析影响变压吸附提氢装置氢收率的主要因素,通过采取降低原料氢气混合气中CO、CO_2与其... 针对陕西陕化煤化工集团有限公司100 kt/a 1,4-丁二醇项目变压吸附提氢装置运行过程中存在的原料气消耗较高、解吸气量较大、产品氢收率低等问题,分析影响变压吸附提氢装置氢收率的主要因素,通过采取降低原料氢气混合气中CO、CO_2与其他杂质含量和延长吸附时间等工艺优化调整措施,以及在变压吸附提氢装置下游新增尾气压缩装置回收变压吸附提氢装置解吸气等优化改造措施后,实现了变压吸附提氢装置氢收率的提升,确保了变压吸附提氢装置的高效、稳定、经济运行。 展开更多
关键词 变压吸附提装置 氢收率 影响因素 原料气组成 吸附时间 均压 改进措施
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优化PSA氢气提纯程序控制系统 提高工业氢收率
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作者 徐小燕 《中国科技期刊数据库 工业A》 2017年第1期26-26,共1页
本文以氢气回收率作为主要研究对象,探讨优化PSA提纯程序控制系统对提高工业氢收率的影响。结果表明,调节后的程序控制系统,因PSA吸附、顺放、均压、逆放的步序、步长被科学配置,氢收率由原来的94%提高到99%。
关键词 PSA 气提纯 控制系统 工业氢收率
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变压吸附提氢装置氢收率低的原因分析及改进措施
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作者 吴红勇 《中文科技期刊数据库(文摘版)工程技术》 2018年第12期367-367,369,共2页
近年来,我国的化工行业发展迅速,在化工生产的过程中,吸附分离技术是化工生产过程中是非常重要的一项内容。针对某煤化工集团有限公司100kt/a1,4-丁二醇项目变压吸附提氢装置运行过程中存在的原料气消耗较高、解吸气量较大、产品氢收率... 近年来,我国的化工行业发展迅速,在化工生产的过程中,吸附分离技术是化工生产过程中是非常重要的一项内容。针对某煤化工集团有限公司100kt/a1,4-丁二醇项目变压吸附提氢装置运行过程中存在的原料气消耗较高、解吸气量较大、产品氢收率低等问题,分析影响变压吸附提氢装置氢收率的主要因素,通过采取降低原料氢气混合气中CO、CO2与其他杂质含量和延长吸附时间等工艺优化调整措施,以及在变压吸附提氢装置下游新增尾气压缩装置回收变压吸附提氢装置解吸气等优化改造措施后,实现了变压吸附提氢装置氢收率的提升,确保了变压吸附提氢装置的高效、稳定、经济运行。 展开更多
关键词 变压吸附提装置 氢收率 影响因素 改进措施
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变压吸附制氢装置的改造 被引量:1
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作者 戴新 《河南化工》 CAS 2002年第3期46-47,共2页
分析了变压吸附制氢装置氢收率低的主要原因,即原料气中氩、氮组分脱除难和部分程控阀内漏。通过在原有装置上增加抽真空系统并在DCS上增设控制程序,提高了氢收率,经济效益显著。
关键词 变压吸附 装置 氢收率 VPSA改造
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独山子石化公司氢网改造后对乙烯制氢装置的操作影响分析
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作者 黄琦 潘国炬 张广智 《云南化工》 CAS 2018年第4期100-101,共2页
独山子石化公司乙烯制氢装置自2009年前系统停工、PSA扩能改造后,一直存在PSA产品收率低、解析气外送不畅放火炬现象,为此,该公司于2015年利用停工大检修对公司氢气管网进行优化改造,改造后,该公司乙烯制氢装置操作变动较改造前有很大... 独山子石化公司乙烯制氢装置自2009年前系统停工、PSA扩能改造后,一直存在PSA产品收率低、解析气外送不畅放火炬现象,为此,该公司于2015年利用停工大检修对公司氢气管网进行优化改造,改造后,该公司乙烯制氢装置操作变动较改造前有很大改观。 展开更多
关键词 改造 氢收率 露点
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乙烯制氢PSA各塔吸附状态下产品质量差别大的原因分析及应对
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作者 黄琦 潘国炬 +2 位作者 张广智 郑奎东 柴广 《中国科技期刊数据库 工业A》 2021年第9期306-307,共2页
制氢装置PSA氢提纯工艺由于相较于膜回收及深冷分离工艺具有能耗低、操作弹性大、操作灵活度高、投资省等诸多优点在越来越追求燃料清洁化的今天受到各大炼化企业的亲睐。但由于PSA工艺是一种物理提纯工艺,它存在一个杂质累计的问题,由... 制氢装置PSA氢提纯工艺由于相较于膜回收及深冷分离工艺具有能耗低、操作弹性大、操作灵活度高、投资省等诸多优点在越来越追求燃料清洁化的今天受到各大炼化企业的亲睐。但由于PSA工艺是一种物理提纯工艺,它存在一个杂质累计的问题,由此会造成一部分氢气随杂质进入解析气系统造成氢收率没有深冷分离工艺高,PSA操作中,提高氢收率的所有措施都是围绕减少这部分进入解析气系统的氢气展开的。 展开更多
关键词 氢收率 木桶效应 沟流
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天然气制氢装置中变气脱碳的研究
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作者 袁庆飞 《山西化工》 CAS 2024年第10期137-139,共3页
目前,我国对二氧化碳排放控制的非常严格,碳中和的提出对石油加工有着深远影响。制氢装置产品中二氧化碳含量约占1/5,且易提取。本文介绍了一种从制氢装置产品中提取二氧化碳的方法,首先介绍了中变气脱碳的必要性,以及脱碳对氢气收率的... 目前,我国对二氧化碳排放控制的非常严格,碳中和的提出对石油加工有着深远影响。制氢装置产品中二氧化碳含量约占1/5,且易提取。本文介绍了一种从制氢装置产品中提取二氧化碳的方法,首先介绍了中变气脱碳的必要性,以及脱碳对氢气收率的影响,然后对几种贫胺液作了简单介绍,并通过对比分析选出合适的贫胺液,最后给出了中变气脱碳的工艺流程,并计算得出其所产生的经济效益。 展开更多
关键词 中变气 脱碳 MDEA溶液 氢收率
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Unified Model of Purification Units in Hydrogen Networks 被引量:1
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作者 吴思东 王彧斐 冯霄 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2014年第6期730-733,共4页
Purification processes are widely used in hydrogen networks of refineries to increase hydrogen reuse. In refineries, hydrogen purification techniques include hydrocarbon, hydrogen sulfide and CO removal units. In addi... Purification processes are widely used in hydrogen networks of refineries to increase hydrogen reuse. In refineries, hydrogen purification techniques include hydrocarbon, hydrogen sulfide and CO removal units. In addition, light hydrocarbon recovery from the hydrogen source streams can also result in hydrogen purification. In order to simplify the superstructure and mathematical model of hydrogen network integration, the models of different purification processes are unified in this paper, including mass balance and the expressions for hydrogen recovery and impurity removal ratios, which are given for all the purification units in refineries. Based on the proposed unified model, a superstructure of hydrogen networks with purification processes is constructed. 展开更多
关键词 purification process hydrogen network integration impurity removal ratio REFINERY
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Studies on Recovery Efficiencies of Phenols from Phenol Fraction Using Alkali Treatment 被引量:2
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作者 S. Aruna Kumari Goruganthula Venkata Subrahmanya Sarma +2 位作者 G. M. J. Raju J. V. S. Murty C. BhaskaraSarma 《Journal of Chemistry and Chemical Engineering》 2013年第4期334-339,共6页
Experiments were conducted for the extraction of phenols from the phenol fraction obtained from the coal tar distillate. The phenol fraction for the present investigation has been procured from Visakhapatnam Steel Pla... Experiments were conducted for the extraction of phenols from the phenol fraction obtained from the coal tar distillate. The phenol fraction for the present investigation has been procured from Visakhapatnam Steel Plant, Visakhapatnam whose composition is known. The phenol fraction from coal tar distillate can be treated for extracting phenols using caustic soda. An attempt has been made to find out whether the existing practice of using only 8%-15% can be modified by increasing the strength of sodium hydroxide and also explore the possibilities of substituting the sodium hydroxide with KOH as an extractant. The different streams of liquids obtained during experimentation have been analyzed by gas chromatograph. Salient features of the study are that higher concentrations of the alkali significantly improved the separation efficiencies of phenols and also regenerate the phenolate with higher phenol content. Increase in the alkali strength has greatly improved the separation as well as the phenol content in the regenerated phenols. Disposal of effluents containing phenols may lead to environmental problem of ground water pollution and the study throws a light on the removal of phenols from the effluents to the extent possible by using higher strength alkali solutions. 展开更多
关键词 Alkali treatment PHENOL phenol fraction recovery efficiency coal tar.
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Hydrogen Isotopes Recovery from Liquid Lithium under Dynamic Conditions
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作者 Kenichi Katekari Yusuke Hatachi Yuki Edao Satoshi Fukada 《Journal of Energy and Power Engineering》 2012年第6期900-905,共6页
In the IFMIF (International Fusion Materials Irradiation Facility), high-intensity deuteron ion beam is targeted at flowing liquid Li to produce neutron for long-time irradiation test of fusion materials. Radioactiv... In the IFMIF (International Fusion Materials Irradiation Facility), high-intensity deuteron ion beam is targeted at flowing liquid Li to produce neutron for long-time irradiation test of fusion materials. Radioactive tritium (T) will be produced as by-product of the D-Li reaction. Y hot trap is expected as an effective system to recover T from the liquid Li target loop. In the present study, absorption behavior of hydrogen isotopes in Y plates is experimentally and analytically investigated under stirring conditions of liquid Li. Experiments clarified that H2 absorption rates of solid Y immersed in Li are independent of the rotating rate in the range of 0 to 100 rpm and are in proportion to the inlet H2 concentration. The rate-determining step is H diffusion in Y. A mass-transfer coefficient is a useful parameter to correlate the overall H transfer from the gaseous phase through liquid Li to the solid Y plate. The effect of activation temperature on the overall performance when Y absorbs H is comparatively investigated. It is considered that heating at 673 K is effective to activate Y along with HF treatment. 展开更多
关键词 Hydrogen isotopes liquid lithium RECOVERY rotating rate H concentration activation temperature mass-transfer coefficient.
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Total synthesis of (-)-isoaltholactone
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作者 LIU Jun ZHANG Xing +2 位作者 LIU Yi BI JingJing DU YuGuo 《Science China Chemistry》 SCIE EI CAS 2013年第7期928-932,共5页
A short and efficient stereoselective synthesis of a styryllactone (-)-isoaltholactone has been achieved in seven steps and 33% overall yield, starting from the readily available carbohydrate D-mannose. The key steps ... A short and efficient stereoselective synthesis of a styryllactone (-)-isoaltholactone has been achieved in seven steps and 33% overall yield, starting from the readily available carbohydrate D-mannose. The key steps of our synthesis involve intramolecular tetrahydrofuran cyclization and one-pot acetonide deprotection-lactonization. 展开更多
关键词 total synthesis styryllactone isoaltholactone CARBOHYDRATE
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