确定了万吨级生产装置适宜的设计及操作参数，并对反应器上段催化剂稀释与不稀释，以及双段熔盐循环的方案进行了比较。
Options for diluting catalyst in the upper section of the reactor with or without inerts or using dual-salt recycling system are carried out.
确定了万吨级生产装置适宜的设计及操作参数，并对反应器上段催化剂稀释与不稀释，以及双段熔盐循环的方案进行了比较。
Options for diluting catalyst in the upper section of the reactor with or without inerts or using dual-salt recycling system are carried out.
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