1) methanol to olefins

甲醇制低碳烯烃
1.
The thermodynamics of methanol to olefins reaction was analyzed, in which the reaction heat, Gibbs free energy, equilibrium constant of main - side MTO reaction and the equilibrium relation among the main olefin products were focused and calculated.
对甲醇制低碳烯烃反应过程进行了热力学分析。
2.
In order to simplify calculation process,the method of atomic matrix was applied to determine independent reactions of methanol to olefins reaction,and the method of Gibbs free energy minimization to establish mathematical model of calculating the equilibrium relation among the main olefin products for methanol to olefins reaction.
采用原子矩阵法确定了甲醇制低碳烯烃独立的反应数,采用Gibbs自由能最小化方法,建立了计算烯烃产物之间平衡关系的数学模型,简化了计算过程。
2) making low carbon olefin hydrocarbon by methanol(MTO/MTP)

甲醇制取低碳烯烃(MTO/MTP)
3) MTO(methanol-to-Olefins)

MTO(甲醇转化制低碳烯烃)
4) MTO (Methanol To Olefin)

MTO(甲醇制低碳烯烃)
5) methanol to olefin

甲醇制烯烃
1.
Besides,methanol to olefin is also a development orientation.

甲醇在传统下游化工产品领域的消耗是有限的;甲醇作为燃料具有较大的市场潜力;二甲醚可替代民用液化石油气和柴油作车用燃料,亦具有良好的市场前景;甲醇制烯烃是一发展方向。
2.
Syngas production,gas to liquid by using Fisher-Tropsch synthesis,production of oxygenates,including methanol and dimethyl ether,and methanol to olefin were covered.
主要评述了自1995年以来,全球天然气转化利用商业化技术的重大进展,包括合成气生产、天然气制合成油、含氧化合物生产(主要是甲醇和二甲醚)、甲醇制烯烃。
3.
The State industrial policy on coal-based chemical industry was ana-lyzed and the technical development and its present industrial status on coal gasification,coal to SNG,to gasoline and methanol,and also methanol to olefin,etc.
分析了国家相关煤化工产业政策,综述了煤气化、煤制天然气、煤制油、甲醇、甲醇制烯烃等煤化工领域的技术进展及产业现状。
6) methanol to olefins

甲醇制烯烃
1.
Progress of separation technologies for methanol to olefins;

甲醇制烯烃分离技术进展及评述
2.
The effects of reaction temperature on the byproducts formation in methanol to olefins were investigated based on the SAPO-34 zeolite catalyst in a fluidized bed reactor.
在流化床反应器中,以SAPO-34分子筛为催化剂,研究了反应温度对甲醇制烯烃反应副产物生成规律的影响。
补充资料:烯烃低聚
分子式:
CAS号:
性质:在烯烃聚合反应中,一般包括两个反应步骤,即烯烃插入催化剂中金属-碳(M—R)键该两步反应速率决定了产物的分子量,得到高分子量聚合物;将得到二聚物;则主要是低聚反应(或称齐聚反应),得到低分子量的α-烯烃。
CAS号:
性质:在烯烃聚合反应中,一般包括两个反应步骤,即烯烃插入催化剂中金属-碳(M—R)键该两步反应速率决定了产物的分子量,得到高分子量聚合物;将得到二聚物;则主要是低聚反应(或称齐聚反应),得到低分子量的α-烯烃。
说明:补充资料仅用于学习参考,请勿用于其它任何用途。
参考词条