介绍了新型CO低温变换催化剂的研制情况。
Development of a new CO low temperature shift(LTS) catalyst was described.
本发明涉及一种用柱撑粘土制备一氧化碳变换催化剂的方法。
The invention relates to a method for preparing a CO shift catalyst by using pillared clay.
介绍新型耐硫变换催化剂QCS-01工业地线试验和工业应用结果。
The results of industrial sideline experiment and application of QCS-01 sulfur-resistant CO shiftcatalyst are given in this paper.
介绍QCS 0 4小颗粒耐硫变换催化剂物化性能、工业侧线试验情况。
Presents the physio-chemical properties of the small granule sulfur tolerant shift catalyst QCS-04 and its commercial side-stream test.
本文介绍了QCS-04型耐硫变换催化剂在山西化肥厂首次工业应用情况。
The first commercial use of QCS04 sulfur tolerant shift catalyst in Shanxi Fertiliser Plant was described in this article.
QDB - 04耐硫变换催化剂具有活性稳定性高和有机硫水解性能好等特点。
Type QDB-04 sulfur-tolerant shift conversion catalyst displays the characteristics of high stability of its activity and satisfactory organic sulfur hydrolysis performance.
工艺关键是使用耐硫变换催化剂，使气化后的含硫工艺气不经脱硫而直接进行变换。
The key of the CO shift process is applying sulfidation resistance shift catalyst, so that the feed gas with sulfide can be shifted directly without removing sulfide.
介绍了B302Q、B303Q球形耐硫变换催化剂在中变串低变工艺中的应用情况。
This paper introduces the application conditions of B302Q, B303Q spherical sulphur-tolerant shift catalysts in medium temperature shift union low temperature shift process.
实验室研究了添加氧化铝对中温变换催化剂堆密度、机械强度、活性和热稳定性的影响。
The influence of alumina addition on the bulk density, mechanical strength, activity and thermal stability of high temperature shift (HTS) catalyst was studied in laboratory.
首先，用直链烯烃和单质硫为原料合成硫化剂，再将该硫化剂负载到耐硫变换催化剂中；
First, the use of straight-chain olefins and sulfur were synthesized as curing agent, then loaded the curing agent to the sulfur-tolerant shift catalyst;
本文主要阐述从生产钴钼系统低温变换催化剂所产生的废料中回收钼的工艺条件和操作方法。
This thesis expound the conditions and methods for reclaiming molybdenum from wastage which was produced by preparation of low-temperature catalysts of Co-Mo series.
本文采用常压等温直流积分反应器，研究在BX型中温变换催化剂上CO变换反应的本征动力学。
This paper deals with the study of intrinsic kinetic behavior of the CO high temperature shift reaction at atmospheric pressure over BX catalysts in an isothermal-integral-reactor.
该技术使变换后的气体组成简单易于分离，其关键是开发或优选以焦炉气为原料的CO变换催化剂。
The key point is to develop or to optimize co shift catalyst which could be applied to COG.
简介了国内外耐硫变换催化剂的研究和工业应用情况，并对耐硫变换催化剂提出研究方向和发展趋势。
A brief introduction is given to the study and industrial use of sulfur-tolerant shift catalyst at home and abroad, and the research direction and development trend of this catalyst are proposed.
总结了新型一氧化碳耐硫变换催化剂QDB-04在德士古水煤浆气化制甲醇装置上的首次工业应用情况。
The first industrial use is summed up of the new-type sulfur-tolerant CO shift conversion catalyst QDB-04 in a methanol unit based on the Texaco coal-water slurry gasification process.
利用钢铁厂平炉尘制备中温变换催化剂，制备成本低，工艺简单，活性达到部颁标准，具有明显的经济效益。
With the action of some bivalent cation, high temperature shift catalyst has been prepared by mixture precipitation method using open-hearth dust as a raw material.
本文介绍了采用工业硝酸酸化废旧铁屑、制取硝酸亚铁溶液，并以该溶液为主要原料研制新型铁-铬系中温变换催化剂。
A new process that industrial nitric acid reacts with iron chippings and shavings to produce ferrous nitrate solution is presented.
介绍新型高温变换催化剂CB -3在以天然气为原料的合成氨厂的升温、还原及应用情况，并对其经济效益进行了分析。
A description is given of the heating, reduction and use of a new type of high temperature shift catalyst CB 3 for ammonia plants based on natural gas, and an analysis is made of its economic benefit.
对脱氧反应的类型、耐硫变换催化剂硫化物形态和载体水解功能对催化剂脱氧性的影响进行了研究，得出了对开发新型耐硫变换催化剂具有一定参考价值的结论。
The influence of deoxy reaction type, mode of sulfide species and hydrolytic ability for catalyst supporter on the de-oxygenation of sulfur-tolerant shift catalysts is studied.
本文介绍了应用序贯实验设计方法对“B109”型催化剂中温变换反应动力学竞争模型进行模型筛选及参数估计的过程。
In this paper a sequential experimental program used for model discrimination and parameter estimation of kinetic models for the high temperature-shift reaction over "B109" catalyst is presented.
介绍CO变换的原理、工艺条件的选择、工艺流程、催化剂的升温和还原。
The principle, technological condition selection and process of co conversion as well as catalyser's heating-up and reduction are discussed.
采用化学清洗和空气爆破相结合的方法，清除换热器中由变换气及催化剂粉末等形成的垢物，降低换热器的阻力，提高热效。
Combining the chemical cleaning and air blasting method, this paper introduces a new method of removing the deposit resulting from the shift gas and catalyst powder, etc.
介绍中低低变换工艺的应用情况，给出了工艺流程和主要设备，阐述了催化剂的升温还原过程和生产运行及存在的问题。
Application of "mid low low temperature" shift process is introduced. The flowsheet, main equipment, catalyst reduction and operation are described.
采用共沉淀法在多种条件下分别制备氧化铁及其负载金催化剂，测定其水煤气变换反应活性。
Both iron oxide and its supported gold catalyst for water-gas shift reaction were prepared under various conditions through co-precipitation method.
结果表明，采用一步法合成二甲醚如果存在水汽变换反应，CO2的转化率为负值，如果催化剂可以控制不发生水汽变换反应，CO2的转化率为零。
The results indicated that the conversion of CO2 is negative if the watergas shift reaction exist and it will be zero if the catalyst can control no watergas shift reaction to take place.
运行结果表明，该催化剂的强度、催化活性和烧炭再生性能均能满足该厂粗煤气变换装置的要求。
The run results showed that the strength, activity and regeneratibility of QDB-04 catalyst met the requirement of the plant on raw coal gas CO shift reaction.
对煤气厂几种变换方案及催化剂用量进行分析对比， 并推荐出较佳的方案。
Several cases of partial shift for Lanzhou Gas Plant are analyzed. The better one is recommended.
介绍了转化反应后的CO中温变换技术，其中包括工艺原理、开工变换、催化剂还原和正常操作要领。
The process theory, start-up shift, catalyst reduction and the main points of normal operation of the CO medium temperature shift technology after the reaction are introduced.
本文采用等温管式微分反应器，研究了常压下在NBC - 1型铁系无铬催化剂上CO变换反应的本征动力学。
In this paper, the intrinsic kinetics of CO shift reaction on NBC-1 type non-chromium iron-based catalysts at ambient pressure is studied by means of isothermal tube-type differential reactor.
介绍了Q CS - 0 4催化剂在中压耐硫变换装置上的工业应用情况。
Application of QCS-04 catalyst in middle pressure sulfur proof shift section is introduced.
应用推荐