1) water-gas shift reactor
水煤气变换反应器
2) adiabatic water-gas shift converter
绝热水煤气变换反应器
3) water gas shift reaction
水煤气变换反应
1.
The catalyst activity for the water gas shift reaction (WGSR) was tested in a differential fixed-bed reactor at atmospheric pressure.
用X射线衍射、差热热重测定、程序升温还原、N2 吸附、N2 O滴定和常压微反活性评价技术考察了沉淀温度对CuO/ZnO/Al2 O3 系催化剂及其前驱体的物相和催化水煤气变换反应活性的影响 。
2.
The activation energies of elementary steps in surface redox mechanism of water gas shift reaction over Cu(111)、Ni(111) and Pd(111) were estimated by Bond Order Conservation Morse Potential (BOC MP) empirical method.
分别采用单晶 Ni(1 1 1 )、Cu(1 1 1 )和 Pd(1 1 1 )作为水煤气变换反应的模板催化剂 ,运用键级守恒 -Morse势(BOC-MP)方法对 Ni(1 1 1 )、Cu(1 1 1 )和 Pd(1 1 1 )表面上催化的 WGS反应的 surface redox机理中的基元反应动力学参数进行了计算 。
4) water-gas shift reaction
水煤气变换反应
1.
The water-gas shift reaction on the Cu base catalyst for the one-step dimethyl ether synthesis process was studied in a fixed bed under the reaction conditions of 260℃ and 5.
0MPa的条件下,研究了固定床反应器中不同CO空速和CO/H2O比例在甲醇合成催化剂上进行水煤气变换反应的情况,并对催化剂的稳定性进行了考察。
2.
The water-gas shift reaction was carried out in a Pd/ceramic hollow fiber membrane reactor using a commercial iron-based catalyst with additive chromium.
采用化学镀法制备了钯/陶瓷中空纤维复合膜,并将该膜反应器用于水煤气变换反应,考察了水碳摩尔比、反应温度及压力对反应的影响。
3.
The Au/Fe 2O 3 catalyst prepared by the microemulsion method in Triton X-100 was characterized by XRD, BET, H 2-TPR, TEM and XPS techniques, and the catalytic activity and active species of the catalyst for water-gas shift reaction were discussed.
氧化态金的含量及金的粒径和分散度是影响Au/Fe2 O3 催化水煤气变换反应活性的主要因素 。
5) Water gas shift(WGS) reaction
水煤气变换反应(WGS)
6) sulfur tolerant water gas shift reaction
耐硫水煤气变换反应
补充资料：变换器式电压表(见变换器式电表)
变换器式电压表(见变换器式电表)
transducer type voltmeter
匕一。亡lht了。一1口一s}〕一d{(」rlyo匕}。o变换器式电压表(transdueer type voltmeter) 见变换器式电表。
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