• The CO shift reaction uses heat transfer technique by the sections of shift converter to remove heat.

    CO变换反应催化剂床层排热多采用变换炉段间换热方式。

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  • The equilibrium of the water gas shift reaction in slit pores has been simulated by the Reactive Canonical Monte Carlo (RCMC) method.

    采用反应蒙特卡罗(RCMC)方法模拟了狭缝孔内水煤气变换反应的化学平衡。

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  • Both iron oxide and its supported gold catalyst for water-gas shift reaction were prepared under various conditions through co-precipitation method.

    采用共沉淀法在多种条件下分别制备氧化铁及其负载金催化剂,测定其水煤气变换反应活性。

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  • The run results showed that the strength, activity and regeneratibility of QDB-04 catalyst met the requirement of the plant on raw coal gas CO shift reaction.

    运行结果表明,该催化剂的强度、催化活性和烧炭再生性能均能满足该厂粗煤气变换装置的要求。

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  • A large amount of steam will be consumed in the course of its shift reaction, and its consumption of steam is more than 30% of the amount steam of synthetic ammonia production.

    在变换反应过程中要消耗大量蒸汽,其蒸汽消耗量占合成氨生产总蒸汽消耗量的30%以上。

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  • This paper deals with the study of intrinsic kinetic behavior of the CO high temperature shift reaction at atmospheric pressure over BX catalysts in an isothermal-integral-reactor.

    本文采用常压等温直流积分反应器,研究在BX型中温变换催化剂上CO变换反应的本征动力学。

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  • The results show that an appropriate quantity of circulating water exists under certain conditions in the system and decreases with a reduction in the steam gas ratio of the shift reaction.

    结果表明,系统在一定条件下存在一较为适宜的循环水量,且此适宜的循环水量随变换反应汽气比的降低而降低。

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  • In this paper, the intrinsic kinetics of CO shift reaction on NBC-1 type non-chromium iron-based catalysts at ambient pressure is studied by means of isothermal tube-type differential reactor.

    本文采用等温管式微分反应器,研究了常压下在NBC - 1型铁系无铬催化剂上CO变换反应的本征动力学。

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  • In this paper a sequential experimental program used for model discrimination and parameter estimation of kinetic models for the high temperature-shift reaction over "B109" catalyst is presented.

    本文介绍了应用序贯实验设计方法对“B109”型催化剂中温变换反应动力学竞争模型进行模型筛选及参数估计的过程。

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  • In this paper a sequential experimental program used for model discrimination and parameter estimation of kinetic models for the high temperature-shift reaction over "B109" catalyst is presented.

    本文介绍了应用序贯实验设计方法对“B109”型催化剂中温变换反应动力学竞争模型进行模型筛选及参数估计的过程。

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