采用微库仑法对重整汽油中的氯含量进行了测定，探讨了影响氯转化率的主要因素。
The chlorine content in reformed gasoline was determined by microcoulometry, and the main factors influenced the conversion of chlorine were discussed.
在重整操作中，一个轻质烃类进料与一个合适的催化剂接触而异构化得到具有高辛烷值的汽油。
In the reforming operation a light hydrocarbon feed isomerizes on contact with a suitable catalyst to produce gasoline with a higher octane number.
该技术拓宽了重整原料来源，较好地解决了焦化汽油的出路问题。
The technology widened the reforming feedstock source and solved the way out of the coker gasoline.
促进汽油沸程原料烃类分子重排以生成催化重整过程所要求产物所用的催化剂。
Catalyst for promoting rearrangement of hydrocarbon molecules in a gasoline boiling-range feedstock to form desired product in catalytic reforming process.
催化重整是生产高辛烷值汽油组分和芳烃的重要工艺，并且能为炼厂提供廉价的氢气。
The catalytic reforming is an important technology providing high-octane gasoline and aromatic hydrocarbon, and also offering a great deal of cheap hydrogen to refinery.
介绍了抚顺石油化工研究院开发的FCC重汽油深度加氢生产催化重整进料技术及其性能特点。
This article introduces the technology of FCC heavy gasoline via hydrogenation producing catalytic reforming feed stock which developed by FRIPP.
它于1967年商业化，与石脑油重整工艺结合从石脑油中生产高辛烷值汽油。
This process, commercialized in 1967 operates in conjunction with a naphtha reforming process to produce high octane gasolines from naphthas.
甲醇重整燃料电池发电系统使用甲醇和水的混合物作为能源载体，安全性优于汽油。
The energy carrier for this fuel cell system is Methanol mixture with water, which are safer than gasoline.
该法可有效提高焦化汽油的辛烷值，延长重整催化剂的使用寿命。
The said process has effectively raised octane number of the coker gasoline and prolonged service life of the reforming catalyst.
质谱分析验证了结果的正确性，为重整生成汽油样品中烃的类别分析提供了一种新方法。
A new method was proposed for the hydrocarbon-type analysis of reformed gasoline with gas chromatography under programming temperature condition.
结果表明，焦化汽油加氢精制后可作重整原料，且掺炼比可达35%。
The result indicated that the hydrotreated delayed coking naphtha was qualified for reforming feedstock, its blending ratio could be up to 35%.
着重讨论了实行新配方汽油后对催化裂化、催化重整等炼油工艺过程的影响，并提出了一些相应的对策。
The influence of implementing reformulated gasoline on catalytic cracking and catalytic reforming is emphasized and some countermeasures are proposed.
着重讨论了实行新配方汽油后对催化裂化、催化重整等炼油工艺过程的影响，并提出了一些相应的对策。
The influence of implementing reformulated gasoline on catalytic cracking and catalytic reforming is emphasized and some countermeasures are proposed.
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