对不饱和聚酯树脂(upr)废料裂解制原料油技术进行了研究，系统地考察了催化裂解反应工艺条件。
Unsaturated polyester resin (UPR) wastes pyrolysis was cracked to prepare feed stock, and process conditions of catalytic cracking reaction were introduced systematically.
利用自制的催化剂对催化裂解稳定汽油全馏分进行了精制，并研究了其最佳工艺条件。
And gasoline refining was carried by using this catalyst, and the optimum processing conditions were also investigated.
重点分析了裂解碳九加氢工艺和催化剂技术，强调了原料预处理、反应工艺和催化剂设计等要点。
The hydrogenation technologies, as well as catalysts used in hydrotreating, were analyzed and compared, and feedstock pretreatment, reaction process and catalyst design were discussed.
本论文主要探讨通过废食用油脂催化裂解，裂解气催化改质，燃料油后处理的工艺，将废油脂制备成合格的燃料油。
In this paper technological process of catalytic cracking and catalytic reforming and post-processing of waste fat and oil are discussed to prepare the qualified liquid fuel oil.
根据天然气循环催化裂解改制技术的工艺过程，计算出基本的工艺参数，结合工程实际给出了实际生产参数。
According to the technological process of reforming technology through cyclic catalytic cracking of natural gas, the basic technological parameters are calculated.
根据天然气循环催化裂解改制技术的工艺过程，计算出基本的工艺参数，结合工程实际给出了实际生产参数。
According to the technological process of reforming technology through cyclic catalytic cracking of natural gas, the basic technological parameters are calculated.
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