The two-stage hydrogenation refining and reforming of coal-derived light distillate

煤液化轻油馏份的 两 段加氢精制和 重整

This process realizes the semi self-heating equilibrium of the reforming system and so the consume natural gas in ration ammonia is about 850Nm3 / tNH3 therefore the cost of the ammonia is cut down greatly when compared with the traditional two-stage reforming process .

换热式并联转化工艺实现了转化系统的半自热平衡，天然气消耗定额约为850Nm~3／tNH3，与传统 两 段 转化工艺比较，大大降低了合成氨制造成本。

Study on two-stage reforming process using CB-6 and CB-7 reforming catalysts

CB-6/CB-7催化剂 两 段 重整工艺的研究