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鲁奇低温甲醇洗酸气提浓的操作优化 被引量:2
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作者 张成祥 张先春 宋淑群 《化肥设计》 CAS 2014年第4期38-40,共3页
针对兖矿国宏化工有限责任公司50万t/a甲醇项目鲁奇低温甲醇洗装置酸气浓度较低的问题,依据德国鲁奇公司提供的低温甲醇洗物料平衡表,对热再生塔和甲醇水分离塔进行了物料平衡计算。计算结果表明,CO2浓度为65.682%,降低CO2含量可提高酸... 针对兖矿国宏化工有限责任公司50万t/a甲醇项目鲁奇低温甲醇洗装置酸气浓度较低的问题,依据德国鲁奇公司提供的低温甲醇洗物料平衡表,对热再生塔和甲醇水分离塔进行了物料平衡计算。计算结果表明,CO2浓度为65.682%,降低CO2含量可提高酸气浓度,故采取了关闭预洗甲醇调节阀、提高酸气浓度的操作方法,使酸气中H2S浓度由32%上升至44%。 展开更多
关键词 鲁奇低温甲醇洗 预洗甲醇 硫回收
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提高稀酸浓度在净化洗涤中的应用
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作者 熊伟 杨德贵 《化工管理》 2014年第30期65-65,67,共2页
介绍瓮福化工公司800kt/a硫铁矿制酸装置,净化工段由原来浓度10%稀酸喷淋洗涤改为浓度大于20%浓度的稀酸进行洗涤。通过新增过滤器FBL对稀酸进行循环提浓,再将稀酸进行多级利用,减少工艺水耗及稀酸排放量,同时降低硫元素损失。对装置水... 介绍瓮福化工公司800kt/a硫铁矿制酸装置,净化工段由原来浓度10%稀酸喷淋洗涤改为浓度大于20%浓度的稀酸进行洗涤。通过新增过滤器FBL对稀酸进行循环提浓,再将稀酸进行多级利用,减少工艺水耗及稀酸排放量,同时降低硫元素损失。对装置水平衡及水资源合理利用有着重要作用。 展开更多
关键词 硫铁矿制 净化水平衡
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用于干燥氯的硫酸的循环利用新工艺 被引量:2
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作者 童新洋 《氯碱工业》 CAS 2013年第2期25-27,共3页
简述我国离子膜法烧碱生产中氯干燥废硫酸使用现状,分析了稀硫酸真空提浓技术和新型组合干燥塔技术的可行性,设计了用于干燥氯的硫酸的循环利用新工艺。
关键词 氯气 干燥 稀硫 循环利用
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耦合酸气提浓的脱硫脱碳工艺
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作者 刘慧敏 诸林 +2 位作者 郁辰阳 曹文浩 陈建良 《过程工程学报》 CAS CSCD 北大核心 2018年第4期879-885,共7页
针对高碳硫比的酸性天然气的净化,提出了一种耦合酸气提浓的脱硫脱碳新工艺.以某高碳硫比原料气为例,采用PROMAX和AMSIM模拟软件进行工艺模拟和参数分析.结果表明,二级闪蒸压力为300 k Pa、闪蒸温度为118℃时,闪蒸气量和二次吸收塔顶的... 针对高碳硫比的酸性天然气的净化,提出了一种耦合酸气提浓的脱硫脱碳新工艺.以某高碳硫比原料气为例,采用PROMAX和AMSIM模拟软件进行工艺模拟和参数分析.结果表明,二级闪蒸压力为300 k Pa、闪蒸温度为118℃时,闪蒸气量和二次吸收塔顶的尾气量均较大,再生后的酸气浓度较高,能耗比常规工艺低.该工艺在满足产品质量要求的同时能将再生后的酸气浓度由20.65vol%提升至30.16vol%,提高了天然气处理单元操作的稳定性,降低了一次性投资和操作运行成本. 展开更多
关键词 碳硫比 脱硫脱碳 二级闪蒸 二次吸收 节能降耗
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氯化氢工段改造总结
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作者 宋军芳 吴仁奇 《中国氯碱》 CAS 2013年第9期6-8,共3页
介绍了氯化氢工段合成炉的技术改造情况,分析了改造效果,提出了改进建议。
关键词 氯化氢二段 二合一炉 三合一炉 提浓酸 高纯
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Nickel extraction from low grade laterite by agitation leaching at atmospheric pressure 被引量:3
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作者 Fatahi Mohammadreza Noaparast Mohammad Shafaei Seyyed Ziaeddin 《International Journal of Mining Science and Technology》 SCIE EI 2014年第4期543-548,共6页
This research work deals with the extraction of nickel from a low grade nickel laterite ore, taken from a deposit located in southwestern of Iran, through agitation leaching at atmospheric pressure. The assaying and m... This research work deals with the extraction of nickel from a low grade nickel laterite ore, taken from a deposit located in southwestern of Iran, through agitation leaching at atmospheric pressure. The assaying and mineralogical studies carried out on the nickel laterite sample, showed the 0.88% Ni, and principally consisted of oxide and silicate crystalline phases i.e. dolomite, quartz, magnetite, and goethite. Among numerous factors affecting such process, four major parameters i.e. temperature, agitator speed(r/min), leaching agents and their concentration were considered in a two-level full factorial experimental design. The agitation leach tests showed that the ore could be leached at atmospheric pressure with sulfuric acid while citric acid was almost unpromising. Analysis of variance(ANOVA) using DX7 software was employed to identify effective parameters. Sulfuric acid concentration and temperature were the most effective parameters on Ni extraction. Furthermore, the factorial models for experiment responses were developed. The results showed 83% Ni extraction after 4 h leaching, under optimized conditions i.e.temperature at 95 ℃, acid concentration at 5 N and agitator speed at 1000 r/min. This study revealed that factorial experimental design can be implemented to identify effective parameters on the agitation leaching process of nickel laterite. 展开更多
关键词 Laterite Nickel extraction Agitation leaching Factorial design Sulfuric acid
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双乙烯酮的环保生产 被引量:1
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作者 沈德智 陈小萍 +1 位作者 孙静 王正龙 《上海化工》 CAS 2011年第10期31-33,共3页
以醋酸为原料经催化、裂解脱水是目前国内外制取双乙烯酮、醋酐等产品的主要生产方法,由于醋酸裂解生成一分子的水致使生产过程中会有大量稀醋酸产生,为了回收利用稀醋酸,稀醋酸提浓将会产生较大量的废水。目前国内双乙烯酮产品收率基... 以醋酸为原料经催化、裂解脱水是目前国内外制取双乙烯酮、醋酐等产品的主要生产方法,由于醋酸裂解生成一分子的水致使生产过程中会有大量稀醋酸产生,为了回收利用稀醋酸,稀醋酸提浓将会产生较大量的废水。目前国内双乙烯酮产品收率基本上维持在80%左右(以醋酸计),损失的20%中约50%为双乙烯酮精馏残渣,另有50%为醋酸裂解的副反应生成一氧化碳、二氧化碳等气体所消耗,科学合理地利用好双乙烯酮生产过程中产生的废水、废气、废渣是双乙烯酮环保生产的主要研究方向。 展开更多
关键词 双乙烯 酮醋裂解 环保生产 三废利用
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Novel Gas-assisted Three-liquid-phase Extraction System for Simultaneous Separation and Concentration of Anthraquinones in Herbal Extract
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作者 杨兴福 梁向峰 +3 位作者 杨良嵘 潘峰 邓伏礼 刘会洲 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2014年第9期968-973,共6页
Gas-assisted three-liquid-phase extraction(GATE), which has the advantages of both three-liquid-phase extraction and solvent sublation, is a novel separation technique for separation and concentration of two organic c... Gas-assisted three-liquid-phase extraction(GATE), which has the advantages of both three-liquid-phase extraction and solvent sublation, is a novel separation technique for separation and concentration of two organic compounds into different phases in one step. This highly effective and economically applicable method has been developed for separating emodin and rhein from herbal extract. In a GATE system composed of butyl acetate/PEG4000/ammonium sulfate aqueous solution, influence of various parameters including gas flow rate, flotation time, salt concentration, initial volume of PEG and butyl acetate was investigated. Within 50 min of 30 ml·min-1nitrogen flow, removal ratio of emodin and rhein from aqueous phase could be over 99% and 97%, respectively.Mass fraction of emodin in the BA phase and rhein in the PEG phase could reach 97% and 95%, respectively. It is demonstrated that gas bubbling is effective for partitioning of emodin and rhein into butyl acetate and PEG phase respectively, and dispersed PEG and butyl acetate could be captured from the aqueous solution. Experimental results show that GATE could be an effective and economical technology for concentration and separation of co-existed products in medicinal plants. 展开更多
关键词 Three-liquid-phase extractionGas-assisted solvent extractionSeparationAnthraquinones
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