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合成气

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The primary product is syngas, which is a mixture of carbon monoxide and hydrogen.

主要产品是合成气,即一氧化碳和氢的混合物。

The process to produce synthetic gas (H2 and CO) by methanol decomposition is animportant research field in C1 chemical industry. In rescent years, the great interest has beencaused in the process of methanol decomposition because of it's wide application and specialadvantage, and which has become one of the research hotspots.

甲醇裂解制备合成气(H2和 CO)是 C1 化学领域的重要课题,近年来,甲醇低温催化裂解过程由于其广阔的应用前景和特殊的优点倍受关注,成为当前催化研究的热点之一。

JHO-2 catalyst can be used in purification and deoxygenation of concentrated carbon monoxide gas, and the deoxygenation and purification of syngas (CO+H2) in chemical industry as well.

JHO-2型催化剂可用于高浓度一氧化碳气体净化脱氧,同时,也可用于化工行业合成气( CO+H2)脱氧净化。

Off-design flow field analysis and radial force prediction of centrifugal pump

合成气在催化剂床层内的流动方向既有轴向,又有径向。

Hydrogenolysis results show that the activity and selectivity of methanol produced from synthesis gas are smaller than those from pure H2.With increasing reaction temperature,the activity of methanol synthesis increases gradually,with simultaneously speeding up of side reactions.

结果表明,合成气氢解反应活性和甲醇选择性明显低于纯氢氢解反应活性和甲醇选择性,反应温度高对提高催化剂活性有利,但同时也加速了副反应的进行。

Under syngas or pure H2, methyl formate hydrogenolysis was carried out over ultrafine CuO-BaO/SiO2 catalysts with various copper content,which had been previously investigated by TEM,BET and TPR techniques.

研究了在合成气或纯氢气气氛下CuO-BaO/SiO2催化剂甲酸甲酯氢解反应活性的变化,并对催化剂进行了TPR、TEM和BET表征。

The synthesis gas is fed to the Fischer-Tropsch reactor where it is catalytically reacted to produce heavy hydrocarbons.

合成气送入费-托合成反应器,在那里催化反应,生成较重的烃类。

ABSTRACT In this paper, a novel process for dimethyl ether synthesis from syngas has been studied by using fluidized-bed reactor syst...

本文对合成气一步法合成二甲醚的流化床反应新技术进行了系统研究。

The single-pass Fischer-Tropsch synthesis with N_2-containing syngas thatwas produced from CH_4-Air-CO_2-H_2O reaction was also studied in fixed-bedreactor in this paper.

论文还采用由模拟抽放煤层气经CH_4-Air-CO_2-H_2O 反应制备的含有大量N_2 的合成气为原料,在固定床反应器上开展了原料单程通过的Fischer-Tropsch合成制液态烃的研究工作。

Thermodynamic analysis is carried out for the compound reaction system of diethyl ether and methanol from synthesis gas. The equilibrium composition and the selectivities in equilibrium are calculated for different initial compositions, temperature and pressure.

确定了合成气直接合成二甲醚与甲醇的复合反应体系独立方程数,并进行了热力学计算与分析,计算了不同初始组成、温度、压力下复合反应体系的平衡组成及平衡条件下二甲醚与甲醇的选择率。

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