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1)  hyperthermic reduction
升温还原方法
2)  lifting temperature reduction method under load
荷重升温还原法
1.
Experiment on checked reducing—powdered property of high Titanium sinter with lifting temperature reduction method under load was done.
进行了荷重升温还原法检验高钛型烧结矿的还原粉化性实验 ,分析研究了高钛型烧结矿在高炉内中低温区的还原粉化行为以及 F e O含量对烧结矿还原粉化和透气性的影响 ,结果表明 ,提高高钛型烧结矿的 Fe O含量可改善其还原粉化性能 ,Fe O含量以 8%~ 10 %为
3)  heating/reducing
升温还原
1.
introduction was made for structure features of 2400mm inner-heat change type of low pressure radial flow ammonia converter internals in china and for process flow of ammonia synthesis system,the filling of catalyst,heating/reducing schemes and operating data were discussed for internals of ammonia converter,the operating effect of actual production was summarized.
介绍了国内2400mm内换热式低压径向氨合成塔内件的结构特点及合成系统工艺流程;论述了氨合成塔内件触媒的装填、升温还原方案和操作数据,总结了实际生产运行效果。
2.
the extracted gas was separated from third stage outlet of shifting,the process flow sheet and process features were introduced;the improvement for heating/reducing process and production operation w.
介绍了工艺流程和工艺特点;论述了新增的2套甲醇合成装置催化剂的升温还原过程和生产操作的改进;分析了影响催化剂使用寿命的因素;提出了延长甲醇催化剂使用寿命的生产操作控制方法;总结了改进后装置生产运行效果。
4)  heating reduction
升温还原
1.
Heating reduction and application of NC74-1 ammonia synthesis catalyst;
NC74-1型氨合成催化剂的升温还原及应用
2.
Filling data,distribution of temperature measuring points and heating reduction scheme were introduced for NC501 type methanol catalyst,the reduction process and production operation situation for this catalyst were discussed,through the comparison of production operation data for two furnaces of catalyst i.
介绍了NC501型甲醇催化剂的装填数据、测温点分布和升温还原方案,论述了该催化剂的还原过程和生产运行情况,通过NC501型和C207型两炉催化剂生产运行数据的对比,对NC501型催化剂的使用效果进行了总结。
5)  temperature-increasing reduction
升温还原
1.
This article introduces the layer-by-layer temperature-increasing reduction of A203 Low-temperature ammonia Synthesis catalyst.
介绍A203型低温氨合成催化剂的分层升温还原,对它的装填及升温还原的控制进行总结。
6)  reduction [英][rɪ'dʌkʃn]  [美][rɪ'dʌkʃən]
升温还原
1.
In this article,the author briefly introduced the application condition of C307 catalyst for LP methanol synthesis in our plant,primary analyzed the influence of reduction status of catalyst,ingredient of inlet syngas,H/C ratio,space-velocity to methanol synthesis,put forward the suitable measures for catalyst protection and operation method.
介绍了C307型低压甲醇催化剂在我厂的实际运行情况,初步探讨了催化剂升温还原状况、入塔气气体成分、氢碳比、空速等因素对甲醇合成反应的影响,并提出了行之有效的催化剂保护措施和合理的生产运行方式。
2.
Loading and reduction of catalyst A202Q, A110-5Q is described.
简述A2 0 2Q、A110 - 5Q催化剂的装填及升温还原过程 ,并对该过程中出现的问题及教训加以总结。
补充资料:程序升温还原
分子式:
CAS号:

性质:使还原气(一般体积分数为6%~15%H2)通过催化剂层,按一定升温程序使催化剂还原,根据热导池(或质谱)检测器给出氢气浓度随温度变化的信号,研究催化剂还原的方法。金属氧化物被还原的温度取决于金属的性质。如果加入其他氧化物,且两者因相互作用而使原氧化物性质有所变化,其还原温度也会有相应变化。反之,根据混合物还原温度偏离纯化合物还原温度的程度,可以推测各组分间的相互作用。

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