减压渣油供氢剂减黏裂化研究

减黏裂化作为一种不生成焦炭的热加工方法主要涉及两类化学反应，裂解反应和缩合反应。裂解反应使减压渣油的平均分子量及其胶团直径变小，改善渣油的倾点和黏度；缩合反应使减压渣油及其中间产物中的芳烃、烯烃等缩合成大分子量产物，产生新的胶核，甚至生成焦炭。常规减黏裂化过程中，这两类化学反应主要与反应温度和反应时间有关。在热作用下渣油中的大分子裂解为H／C原子比相对较高的饱和烃自由基和H／C原子比相对较低的芳香性自由基。后者还可失去自身的环烷氢而使其H／C原子比进一步降低。如果体系中有足量的氢化芳烃存在，那么氢化芳烃分子上的活泼氢就可能转移到芳香性自由基的单电子位，将自由基封闭，从而阻止芳香性自由基之间的相互缩合，抑制使分子长大的缩合反应。如果体系中的氢化芳烃含量不足。则热反应体系中就没有足够的活泼氢将芳香性自由基封闭，芳香性自由基缩合反应的几率较高，造成过早地生焦。这种来自渣油分子自身的活泼氢的化学行为与渣油热反应生焦诱导期有一定关系。

Roles of hydrogen donor in visbreaking of vacuum residue

The roles of such classical hydrogen-donor solvents as tetralin, decahydronaphthalene, dihydrophenanthrene and dihydroanthracene in visbreaking of vacuum residue were examined. It revealed that the effect of the hydrogen donor solvents could be ranked as dihydrophenanthrene≈dihydroanthracene> tetralin> dihydrophenanthrene and that the appropriate amount added was around 15％. Further studies showed that the coke formation can be greatly reduced by adding hydrogen-donor solvents, consequently the hydrogen-donor approach allowed the operation of visbreaking at higher severity. The effect of hydrogen could be negligible when the hydrogen pressure was lower than 2.5MPa.