| 1. | Gas - aqueous catalytic systems for water - gas shift reaction 水溶液体系水煤气变换催化反应 |
| 2. | Preparation of cu - ce ox catalysts for water - gas shift reaction and their characteristics 变换催化剂的制备和性能考察 |
| 3. | Study on coupling of dehydrogenation of propane with reversed water - gas shift reaction for propylene synthesis 丙烷脱氢与逆水煤气变换耦合制丙烯反应的研究进展 |
| 4. | These results can be used as a reference for optimization of polygeneration systems . the syngas generated from coal needs shifting reaction to adjust h2 / co ratio to fit the methanol synthesis requirement 由煤制得的合成气经过变换反应达到满足甲醇合成要求的氢碳比,这一过程消耗了能量但提高了甲醇产率,在不同的甲醇产率下多联产系统的效率随之改变。 |
| 5. | The shifting reaction consumed energy but increased the methanol synthesis ratio and the system efficiency . the energy method was used to analyse the effect of methanol synthesis ratio on system efficiency to show the advantages of polygeneration system 本文以能量分析的结果来说明多联产系统效率随甲醇合成产率(以接近平衡态的程度表示)的变化规律,指出了变换反应在能量利用和环境保护上的合理性。 |
| 6. | There are six systems of biohydrogen production which include biophotolysis , organic degradation of light , hydrogen synthesis via the water - gas shift reaction of photoheterotrophic bacteria , hybrid system of photo - fermentation , anaerobic fermentation and in vitro hydrogen production by hydrogenase 讨论了光合成生物制氢系统、光分解生物制氢系统、水气交换反应生物制氢系统、光合发酵杂交生物制氢系统和厌氧发酵生物制氢系统、离体氢酶生物制氮系统等6个生物制氢系统。 |
| 7. | Thermodynamic methods were used to optimize gasifier , shift reaction and co2 removal , and methanol synthesis processes . polygeneration is a promising system to make the best use of thermal energy with different qualities to achieve high environmental and economic benefits 本文以热力学方法研究了多联产系统的热效率和火用损失,对气化炉、水煤气变换和脱碳以及甲醇合成等单元作了优化分析,指出了多联产系统在能量利用方面的合理性,对其环境效益和经济效益的综合评估方法进行了初步探索。 |
| 8. | Studying the heat - mass transfer and multi - spices electric - chemical reaction , a dynamic temperature model was deduced for molten - carbonate fuel cell stack . the thermal radiation , shift reaction , and the change of gas spices were considered in this model . establishing momentum equation , the paper has developed a 3d temperature and flow fields model for mcfc stack based on cfd technique 建立了熔融碳酸盐燃料电池堆内部单体的暂态温度模型,并考虑了电堆的辐射换热、转换反应、反应气体组分变化对温度场的影响;根据mcfc的微分控制方程组,考虑气体组分的热力学性质及动量变化的影响,利用数值分析方法求解熔融碳酸盐燃料电池堆的三维流场与温度场,分析了各作用因素对熔融碳酸盐燃料电池堆温度分布的影响机制。 |