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采用DCS控制系统JX300对变压吸附提纯CO进行了顺序控制.介绍了变压吸附CO的工艺流程、吸附程序和操作要求;根据系统的组态软件特点和相应功能顺序论述了变压吸附CO顺序控制的过程和方法.结果表明,功能模块化更便于程序的维护和功能程序块的升级优化. 相似文献
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实验室及小规模用CO可通过甲酰胺分解或甲酰分解等方法制得。工业上CO的来源是从各种含CO的混合气中分离提取。目前已实现的工业提纯CO工艺主要有以下三类。 相似文献
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前言
醋酸尾气中含有60v%~85v%的CO,以一套年产200kt/a的羰基合成醋酸装置计,每小时产生1500~2000Nm3高压尾气,其中CO量占合成醋酸原料气CO量的15v%多。采用一种有效、合理的方法回收醋酸尾气中CO既可降低醋酸的生产成本,又可减少污染气体的排放量。 相似文献
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Using pressure swing adsorption (PSA) technology to purify carbon monoxide (CO) discharged from industrial gases is a high-efficiency and economical method. In this article, a four-bed PSA experiment for CO purification was improved and optimized, in which a set of 120 m^3·h^-1 pilot-scale PSA device was developed to purify CO from industrial tail gases, a set of control systems suitable for industry production was developed, and the influences of the operating parameters on CO purification were investigated. The experimental results indicated that the pilot-scale PSA device could produce qualified product gas and get high CO recovery ratio under optimized conditions. The research may provide reliable fundamental data, for industrial scale utilization of CO, from industrial tail gases, and have strong market competitive power and a broad promoted application prospect. 相似文献
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采用分别装载活性炭和NA型吸附剂的复合床层的变压吸附工艺来脱除合成气中微量的CO和CO2,并利用Aspen-Adsim软件对其进行模拟和优化。模拟结果表明,吹扫气量对工艺性能有较大的影响,吹扫气由处在顺放步骤的吸附塔提供,因此在顺放步骤将床层压力降至较低压力,可获得较大的吹扫气量,此时的工艺性能也较优。模拟结果还表明,均压次数对工艺性能也有影响。在相同的顺放压降下,将变压吸附过程中的3次均压变为2次均压,可减少吸附剂用量,吸附剂产率更高,但塔底尾气量要相应增加。 相似文献
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混合气组分对CO在稀土复合吸附剂上吸附的影响 总被引:1,自引:0,他引:1
采用吸附柱动态实验装置,分别考察了混合气组分H2O、CO2、CH4对稀土复合吸附剂变压吸附CO的影响。实验结果表明,原料气中微量的H2O的存在对稀土复合吸附剂的吸附性能有较大影响,当水质量浓度仅为250mg/L时,CO的变压吸附量下降约35%;与CO相比,CO2在稀土复合吸附剂上为弱吸附组分,但对CO的吸附性能有一定影响,当CO2体积分数为1%时,CO的变压吸附量可维持在12.5 ml/g左右;而CH4的存在对CO在稀土复合吸附剂上的吸附量影响不大。 相似文献
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《Gas Separation & Purification》1991,5(4):242-246
A pressure swing adsorption (PSA) process with a single stage for recovering high purity CO was developed with an original chemical adsorbent that adsorbs CO selectively. A pilot test was made to optimize the process and confirm the stability of the adsorbent. A first commercial plant was constructed at the Kakogawa Works of Kobe Steel in March 1989. Subsequently, a second commercial plant was constructed at the Kobe Works of Kobe Steel in October 1990. The two plants have been producing high purity CO stably and consistently. 相似文献
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选择碳分子筛,以CH4和CO2为原料气,对变压吸附法提纯沼气中生物甲烷的分离性能进行了研究。采用高精度智能重量分析仪IGA-100测定了25℃下CH4、CO2和N2纯组分气体在碳分子筛上的吸附平衡等温线,计算了3种气体在碳分子筛内的扩散速率CO2>N2>CH4。使用单塔变压吸附装置测量了动态吸附穿透曲线,考察了吸附压力、气体流量和少量氮气等因素对吸附分离的影响,并对吸附机理做了初步探讨。实验结果表明,在吸附压力为0.4MPa、气体流量为200mL/min时,在碳分子筛上CO2穿透吸附量为35.9mL/g,CH4穿透吸附量为5.4mL/g,CO2/CH4分离系数高达12.6,可直接从吸附塔顶富集纯净的CH4,而且碳分子筛可以通过抽真空完全再生,是一种理想的吸附材料;在有少量氮气存在的实验条件下,由于碳分子筛对CH4和N2具有动力学分离效应,仍能在塔顶富集高浓度的CH4。 相似文献
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变压吸附技术是工业上生产高纯氢气最常用的方法之一。然而,在实际生产过程中无法观察到塔内各组分在不同时刻的分布状态,因此借助模拟的手段来研究从投料至系统达到循环稳态期间各组分在塔内的动态变化规律,进而指导工艺改进是很有必要的。采用活性炭和5A分子筛为吸附剂,设计了八塔变压吸附工艺从蒸汽甲烷重整气中纯化氢气,模拟了变压吸附制氢开车过程,分析了开车过程中塔内各组分在吸附、顺放以及冲洗三个阶段以及循环稳态后吸附阶段瞬态吸附行为和塔内温度变化。结果表明,在吸附以及顺放等过程中重组分会随着循环周期向塔顶移动。这一现象是组分间竞争吸附和冲洗再生方式下重组分在床层底部累积两个作用因素共同导致的。这些因素在一定程度上也会造成CO的吸附前沿在吸附阶段就过多进入5A分子筛上,使得CO含量成为限制工艺性能的主要因素。 相似文献
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《Gas Separation & Purification》1990,4(3):141-148
The original pressure swing air separation process, developed almost simultaneously by Exxon and Air Liquide, uses a nitrogen selective zeolite adsorbent to produce a high purity oxygen product. The same basic process is still widely used in small scale units although, for larger scale units, many modifications to the cycle have been introduced in order to reduce power consumption. Although nitrogen can in principle be recovered from the blowdown stream of such systems, if high purity nitrogen is the required product, it is more economic to use an oxygen selective adsorbent. Most adsorbents show either no selectivity or preferential adsorption of nitrogen. However, in small pore carbon molecular sieves or 4A zeolite there is a substantial difference in diffusion rates so that an efficient kinetic separation is possible. Somewhat different cycles are generally used in such processes. Progress in modelling the dynamic behaviour of both types of PSA system is reviewed and comparisons between experimental performance and the model predictions are shown. A simple linear driving force model provides a good overall prediction of the effects of process variables but the computationally more cumbersome diffusion model gives better quantitative agreement with experiment. Comparisons are drawn between the performance achieved (in nitrogen production) with two different kinetically selective adsorbents; RS-10 (a modified 4A zeolite) and Bergbau Forschung carbon molecular sieve. 相似文献