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1)  catalytic cracking gas
催化裂解富气
1.
NO_x and SO_2 from catalytic cracking gas containing in triethanol amine(TEA) solutions were determined by ion chromatography.
催化裂解富气吸收液为测定对象,建立吸收液中目标离子(包括NO2-,NO3-,SO42-)的离子色谱分析方法。
2)  Vapor phase catalytic cracking
气相催化裂解
3)  catalytic cracking
催化裂解
1.
ZSM-5 catalysts modified with lanthanum for catalytic cracking of C_4-olefins to propylene;
La修饰ZSM-5分子筛催化剂用于C_4烯烃催化裂解制丙烯
2.
Study on production of propylene and ethene from 1-butene by catalytic cracking;
1-丁烯催化裂解制丙烯和乙烯反应性能的研究
3.
Study on activity stability of catalytic cracking catalyst for producing lube base oil from hydrocracking bottoms;
加氢尾油催化裂解生产润滑油基础油催化剂活性稳定性研究
4)  catalytic pyrolysis
催化裂解
1.
Maximizing yield of propylene by two-stage riser catalytic pyrolysis of heavy oil;
两段提升管催化裂解多产丙烯研究
2.
Study on the catalysts for catalytic pyrolysis of heavy oil to ethylene and propylene;
重油催化裂解多产乙烯丙烯催化剂的研究
3.
Study on lumping kinetic model of heavy oil catalytic pyrolysis;
重油催化裂解集总动力学模型研究
5)  catalytic decomposition
催化裂解
1.
Study on coal gas catalytic decomposition in rotating packed bed reactor;
旋转超重力场反应器催化裂解煤矿瓦斯的研究
2.
Research on advances of converting organosilicon high-boiling components to methylchlorosilane by catalytic decomposition;
有机硅高沸物催化裂解制单硅烷催化剂研究进展
3.
Study on production of methylchlorosilane from the organosilicon high-boiling components by catalytic decomposition;
有机硅高沸物催化裂解制甲基氯硅烷工艺研究
6)  deep catalytic cracking
催化裂解
1.
Molecular reaction kinetics simulation of deep catalytic cracking: Molecular simulation of feedstock;
催化裂解过程分子尺度的反应动力学模拟:原料油分子尺度的模拟
2.
Study on FCC Gasoline Deep Catalytic Cracking;
催化裂化汽油催化裂解反应规律研究
3.
This paper introduced the characteristics of Deep Catalytic Cracking (DCC) technology in aspects of feedstock, catalyst, typical commercial test results, and focused mainly on the latest commercial applications.
文章介绍了DCC技术的主要特点、原料油和催化剂、典型工业试验结果 ,并重点介绍催化裂解技术的最新工业应用情况。
补充资料:催化裂解
分子式:
CAS号:

性质:以石油烃类为原料,在催化剂作用下进行热裂解,生产低分子烯烃和其他产品的过程。近年在流化催化裂化的基础上进行研究,发明了一个此类过程。由于提高了操作温度,选择了适当催化剂,提高了转化深度,得到了较高的烯烃气体产率和辛烷值较高的高含芳烃汽油。过程中催化剂上的焦炭仍可在装置内再生。现已有工业化装置。它是提供石油化工原料的一个新途径。

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