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二氧化氯生产其摩尔比和摩尔转化率的测算方法研究
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作者 王儒富 蒲丽 《四川化工》 CAS 2021年第6期50-55,共6页
已知一元、三元固体酸与亚氯酸钠反应的最高摩尔比分别为3.0和3.5,可以分别通过作图法求得1倍摩尔比的摩尔转化率,进而计算生产配方和二氧化氯产量;为了测定、计算未知二元固体酸与亚氯酸钠反应和二元液体酸与氯酸钠+双氧水反应的最高... 已知一元、三元固体酸与亚氯酸钠反应的最高摩尔比分别为3.0和3.5,可以分别通过作图法求得1倍摩尔比的摩尔转化率,进而计算生产配方和二氧化氯产量;为了测定、计算未知二元固体酸与亚氯酸钠反应和二元液体酸与氯酸钠+双氧水反应的最高摩尔比,需分别测定在1倍摩尔比条件下亚氯酸钠和氯酸钠+双氧水的摩尔转化率,再分别用作图法求得最高摩尔比为2.5和2.4,据此可以分别计算二者的生产配方和二氧化氯产量。 展开更多
关键词 足量酸 摩尔 最高摩尔 摩尔转化率 最高摩尔转化率
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利用克雷伯肺炎杆菌限制性底物发酵生产1,3-丙二醇 被引量:3
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作者 苗茂栋 吴敏 +2 位作者 邵千飞 马全红 蒋知欲 《中国生物工程杂志》 CAS CSCD 北大核心 2008年第10期49-54,共6页
研究了克雷伯肺炎杆菌(Klebsiella pneumoniae)批式流加发酵生产1,3-丙二醇的发酵工艺,根据1,3-丙二醇(1,3-PD)的生产和菌体生长相关的特点,采用营养基质限制性流加的发酵工艺,通过控制氮源氯化铵以保持细胞稳定生长。结果表明:过低的... 研究了克雷伯肺炎杆菌(Klebsiella pneumoniae)批式流加发酵生产1,3-丙二醇的发酵工艺,根据1,3-丙二醇(1,3-PD)的生产和菌体生长相关的特点,采用营养基质限制性流加的发酵工艺,通过控制氮源氯化铵以保持细胞稳定生长。结果表明:过低的氮源浓度,细胞生长受到限制,影响产物1,3-PD的合成;过高的氮源浓度,细胞比生长速率增加,但1,3-PD关于消耗甘油的得率降低,用于生长和维持代谢所消耗的甘油量增加。以0.41g/(L.h)的氮源流加速率,残余氯化铵浓度在0.1g/L时,转化率和生产强度最高。发酵25h~28h后,1,3?丙二醇最终浓度达到52.03g/L,生产强度为2.04g/(L.h),相对于甘油的摩尔转化率为0.66,分别比氮源限制前提高了28.0%、35.1%及29.4%。通过限制性流加氯化铵,控制细胞的比生长速率,使底物甘油有效转变为发酵的目标产物1,3-PD,有效实现产物1,3-PD的高生产强度以及对甘油的高转化率。 展开更多
关键词 1 3-丙二醇 氮源限制流加 比生长速率 生产强度 摩尔转化率
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Hydrogenation of Silicon Tetrachloride in Microwave Plasma 被引量:2
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作者 卢振西 张伟刚 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2014年第2期227-233,共7页
This study investigated the hydrogenation of silicon tetrachloride (SIC14) in microwave plasma. A new launcher of argon (Ar) and hydrogen (Ha) plasma was introduced to produce a non-thermodynamic equilibrium act... This study investigated the hydrogenation of silicon tetrachloride (SIC14) in microwave plasma. A new launcher of argon (Ar) and hydrogen (Ha) plasma was introduced to produce a non-thermodynamic equilibrium activation plasma. The plasma state exhibited a characteristic temperature related to the equilibrium constant, which was termed "Reactive Temperature" in this study. Thus, the hydrogenation of SIC14 in the plasma could easily be handled with high conversion ratio and very high selectivity to trichlorosilane (SiHC13). The effects of SiC14/Ar and H2/Ar ratios on the conversion were also investigated using a mathematical model developed to determine the op- timum experimental parameters. The highest hydrogenation conversion ratio was produced at a H2/SiCl4 molar ratio of 1, with mixtures of SICl4 and H2 to Ar molar ratio of 1.2 to 1.4. In this plasma, the special system pressure and incident power were required for the highest energy efficiency of hydrogenating SIC14, while the optimum system pressure varies from 26.6 to 40 kPa depending on input power, and the optimum feed gas (He and SiCI4) molar en- ergy input was about 350 kJ. mo1-1. 展开更多
关键词 HYDROGENATION silicon tetrachloride non-thermodynamic equilibrium plasma equilibrium constant plasma temperature
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Circulating Fluidized Bed Gasification of Low Rank Coal:Influence of O2/C Molar Ratio on Gasification Performance and Sulphur Transformation 被引量:4
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作者 ZHANG Haixia ZHANG Yukui +1 位作者 ZHU Zhiping LU Qinggang 《Journal of Thermal Science》 SCIE EI CAS CSCD 2016年第4期363-371,共9页
To promote the utilization efficiency of coal resources,and to assist with the control of sulphur during gasification and/or downstream processes,it is essential to gain basic knowledge of sulphur transformation assoc... To promote the utilization efficiency of coal resources,and to assist with the control of sulphur during gasification and/or downstream processes,it is essential to gain basic knowledge of sulphur transformation associated with gasification performance.In this research we investigated the influence of O_2/C molar ratio both on gasification performance and sulphur transformation of a low rank coal,and the sulphur transformation mechanism was also discussed.Experiments were performed in a circulating fluidized bed gasifier with O_2/C molar ratio ranging from 0.39 to 0.78 mol/mol.The results showed that increasing the O_2/C molar ratio from 0.39 to 0.78 mol/mol can increase carbon conversion from 57.65%to 91.92%,and increase sulphur release ratio from 29.66%to63.11%.The increase of O_2/C molar ratio favors the formation of H_2S,and also favors the retained sulphur transforming to more stable forms.Due to the reducing conditions of coal gasification,H_2S is the main form of the released sulphur,which could be formed by decomposition of pyrite and by secondary reactions.Bottom char shows lower sulphur content than fly ash,and mainly exist as sulphates.X-ray photoelectron spectroscopy(XPS)measurements also show that the intensity of pyrite declines and the intensity of sulphates increases for fly ash and bottom char,and the change is more obvious for bottom char.During CFB gasification process,bigger char particles circulate in the system and have longer residence time for further reaction,which favors the release of sulphur species and can enhance the retained sulphur transforming to more stable forms. 展开更多
关键词 gasification circulating fluidized bed sulphur transformation O2/C molar ratio
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