格尔木炼油厂 0 .1 5Ｍｔ/ａ催化重整装置于 1 997年 9月投产 ,在试生产中重整下游用氢的催化裂化柴油加氢精制装置增压机过滤器经常被氯化铵堵塞 ,原因是重整原料油中氯含量达 8μｇ/ｇ(原试验研究时未发现原料含氯 )。决定在重整装置原料预加氢反应器后加热脱氯罐 ,采用高温 Golmud refinery 0 .1 5Mt / a catalytic reforming unit put into operation in September 1997, in the trial production of catalytic hydrogenation of downstream catalytic hydrogenation refining unit turbocharger filter is often clogged with ammonium chloride, The reason is that the chlorine content in the reforming feedstock oil is up to 8 μg / g (no chlorine was found in the original test study). It is decided to heat the dechlorination tank after the pre-hydrogenation reactor of the reformer unit and adopt high temperature