提出了以饱和烃、一环芳烃和二环芳烃组成的理想催化裂化组分的概念。
A concept of FCC ideal feed components consisting of saturates, mono and dicyclic aromatic is then suggested.
烟气轮机是催化裂化装置的关键设备。
The flue gas turbine - expander is the key equipment in catalytic cracking unit.
不过石油催化裂化仍是其最大的用途。
However, catalytic cracking of crude oil remains its largest application.
这就带来一种裂化效应。
这就是所谓的催化裂化。
提升管的进料段是裂化反应最复杂的区域。
The most complex part of RFCC is in the feed injection zone.
论述了以脱油沥青为原料的减粘裂化新工艺。
The new visbreaking process with de-oiled asphalt feedstock is discussed.
(流化催化裂化)是炼厂生产汽油的主要方法之一。
The Fluid Catalytic Cracking (FCC) is the major gasoline - producing process in refinery.
并进行了天然岩石模拟分区碎裂化现象的实验研究。
And experimental studying on natural rock simulating the phenomenon of zonal disintegration.
具有良好的传热效率，更好地抵抗热裂化和化学氧化。
They have good heat transfer efficiency with better resistance to thermal cracking and chemical oxidation.
加氢尾油可作为优质的催化裂化或加氢裂化掺炼原料。
The hydrogenation tail oil obtained from process could be used as superior FCC or hydrocracking feedstock.
讨论了不同催化原料油组成情况及其对催化裂化反应的影响。
The effects of the compost ions of different catalytic stocks on catalytic cracking reaction was discussed.
氢转移反应的进行程度可以在较大范围内改变裂化产品的分布。
The profile of cracked products can be adjusted in a wide range by the degree of hydrogen transfer reaction.
岩石分区碎裂化现象是伴随深部岩体的特殊工程响应问题之一。
The phenomenon of zonal disintegration is a special technical problem which comes with deep mass.
吲哚需先加氢生成二氢吲哚，二氢吲哚快速裂化转化为苯胺和氨。
Indole must be hydrogenated into indoline, and then indoline would be cracked into aniline and ammonia quickly.
研究分析了催化裂化装置的主分馏塔与稳定塔之间操作控制的关联性。
The operation and control interaction analysis between main fractionator and stabilizer of FCCU was studied.
为生产清洁能源，采用光催化氧化法对催化裂化汽油进行了脱硫研究。
To produce clean energy, the study on oxidation desulfurization from catalytic cracking gasoline by photocatalysis is investigated.
烯烃催化裂化技术具有操作简单和成本低廉等优势，应加快研究开发。
Catalytic cracking of olefins features simplicity in operation and low cost, and should be developed in preference.
在实验室采用固定流化床反应器，研究了催化裂化汽油裂化时的焦炭生成。
Study of coke formation during FCC naphtha cracking was carried on a laboratory fixed-fluidized bed reactor.
为改善催化裂化原料油雾化状况，降低结焦和干气收率，将原料重油进行乳化。
To improve the heavy oil atomization situation of FCC feed stock and decrease the yield of carbon and dry gas, the feed stock, heavy oil, is emulsified.
结果表明，二烯值大、酚含量低是加氢渣油催化裂化汽油诱导期短的主要原因。
Results show that the main causes of low induction period of cracked naphtha are the high diene number and low phenol content.
非加氢精制催化裂化柴油工艺解决了重油催化裂化柴油产品质量不达标的问题。
The quality problems of diesel oil with catalytic cracking of heavy oil was solved by using non hydrogenation purified catalytic cracking technology.
以不同原料研究了硫对重整催化剂芳构化、脱氢、异构化和加氢裂化活性的影响。
The effect of sulfur on aromatization, dehydrogenation, hydroisomerization and hydrocracking activities of the catalyst has been studied with different hydrocarbon feedstocks.
本文结合实例介绍了TS3000系统在加氢裂化装置紧急泄压联锁上的应用过程。
This paper introduces the application of TS3000 in the emergency pressure release interlock system for hydrocracking unit by the example.
主要介绍基于RASYS农话接入网基站裂化的技术，详细阐述了扇区裂化设计要点。
It mainly introduces the base station cracking technology based on RASYS rural access. The Outlines of sector cracking design are expatiated.
面对催化裂化工艺所遇到的挑战，提出了催化裂化过程反应化学的多维反应结构模式。
Faced the stringent challenge of FCC process, the multi-dimensional reaction structure was pro- posed for FCC process reaction chemistry.
研究了催化裂化轻汽油临氢醚化工艺，以降低催化裂化汽油的烯烃含量并提高辛烷值。
The hydroetherification process of catalytic cracking light gasoline is investigated for increasing octane number and decreasing the content of olefins of catalytic cracking gasoline.
研究了催化裂化轻汽油临氢醚化工艺，以降低催化裂化汽油的烯烃含量并提高辛烷值。
The hydroetherification process of catalytic cracking light gasoline is investigated for increasing octane number and decreasing the content of olefins of catalytic cracking gasoline.
应用推荐