Material balances, properties of feedstock, product and catalyst, energy consumption of the unit and the operation parameters before and after the revamping have been compared.
着重从物料平衡、原料及产品性质、催化剂性质、装置能耗、操作参数等方面与改造前进行了对比。
Online monitoring system for fan on catalyst reforming unit.
催化重整装置风机在线监测系统。
By adopting this technique, continuous catalyst regeneration was realized, operating severity decreased and running period of the unit was prolonged.
采用该技术可实现催化剂连续再生，降低了装置操作难度，提高了装置运行周期。
The weight method is used to measure the solid quantity (catalyst contain) in slurry oil of catalytic cracking unit.
采用重量法测定催化装置油浆中的固体含量(催化剂含量)。
The deactivation kinetics for the vapor-phase disproportionation of toluene over mordenite catalyst has been studied by using a combined unit of micro-reactor under pressure and gas chromatography.
本文采用加压微反-包谱-数据处理机联合装置研究了在丝光沸石催化剂上甲苯歧化反应的失活动力学。
The in situ regeneration of RN-10 hydrofining catalyst by diluent air, and the corrosion prevention measures of the hydrofining unit in Fujian Refinery and Petrochemical Company were introduced.
介绍福建炼油化工有限公司加氢精制装置中RN-10催化剂器内稀释空气烧焦再生过程及防腐措施。
The catalyst has been used in the heavy oil FCC unit of WEPEC Dalian and compared with an imported advanced heavy oil cracking catalyst.
该催化剂在大连西太平洋石油有限公司重油催化裂化装置上与国外的优良重油催化剂进行了工业对比试验。
The successful application of domestic catalyst 481 - 3 in the unit at high space velocity showed that the catalyst had good activity and suitability.
国产催化剂481-3在高空速条件下应用并取得成功，表现出良好的活性及适应性。
The FCC unit continuously circulates a fluidized zeolite catalyst that allows rapid cracking reactions to occur in the vapor phase.
在催化裂化装置一个不断循环流态化沸石催化剂允许快速裂解反应发生在气相。
Catalyst MIP-CGP specially designed and produced for FCC unit revamped with MIP process was tested in Qingdao Petrochemical Branch Co. , SINOPEC.
青岛石油化工有限责任公司（简称青岛石化公司）在重油催化裂化装置上试用了根据M IP工艺改造后的特点而专门设计生产的催化剂MIP-CGP。
The advanced second generation patented ultra-low pressure continuous reforming process of UOP and the R-134 reforming catalyst were used in the unit.
该装置采用美国UOP公司先进成熟的第二代超低压连续重整工艺专利技术及r- 134重整催化剂。
The first industrial use is summed up of the new-type sulfur-tolerant CO shift conversion catalyst QDB-04 in a methanol unit based on the Texaco coal-water slurry gasification process.
总结了新型一氧化碳耐硫变换催化剂QDB-04在德士古水煤浆气化制甲醇装置上的首次工业应用情况。
The bipolymer special resin was test-operated by applying domestic catalyst in polypropylene unit of Fushun Ethylene Chemical Plant and the consumer had favourable applying effect.
在抚顺乙烯pp装置上采用国产催化剂进行了二元共聚专用料的试生产并进行了加工应用。
This catalyst has very good stability and nitrogen-resisting properties and fully meets the requirements for the quality of products from the production unit.
此催化剂具有良好的稳定性和抗氮性，完全满足装置产品质量的要求。
With excellent reaction performance and good stability, WSI catalyst was commercialized on the low pressure hydrogenation unit in Jinling Petrochemical Corporation of SINOPEC.
该剂的反应性能优越，稳定性良好，并在金陵石化低压加氢装置上实现了工业应用。
Effects of na +, heavy metal nickel and vanadium, sulfur and viscosity of residue on activity of catalyst for S-RHT were investigated on a residue hydrotreating pilot unit.
在中型渣油加氢试验装置上考察了钠离子、镍、钒、硫和渣油粘度对s -RHT催化剂活性的影响。
Reaction rules of FCC light naphtha upgrading and FCC naphtha recycle and reflux upgrading have been investigated with FCC catalyst in the bench scale riser FCC unit.
利用催化裂化催化剂在小型提升管催化裂化试验装置上考察了催化裂化汽油轻馏分改质和催化裂化汽油循环回炼改质的反应规律。
The operation condition of indigenous palladium-carbon catalyst was analyzed, two batches of the catalysts used in purified terephthalic acid(PTA) unit sequentially.
分析了中国石油化工股份有限公司天津分公司精对苯二甲酸（PTA）装置先后采用的两批国产钯碳催化剂使用状况。
Production capacity of unit weight catalyst for the novel catalytic column reactor is 4.23 times higher than that for a bubble fixed bed reactor.
从单位体积反应器生产能力进行比较，新型催化剂装填方式是固定床鼓泡反应器的4倍以上。
This article summarizes the commercial application of the Z-18 catalyst molecular sieve retarder activator in the residuum fluid catalytic cracking unit (RFCC) of Khartoum Refinery co.
介绍了Z—18催化分子筛抗焦活化剂在苏丹喀土穆炼油有限公司重油催化裂化装置(简称KRC)上的工业应用。
Considering the existing production unit and its process conditions, the projects to regenerate the low activity catalyst were made and were successfully applied to industrial production line.
结合现有生产装置及工艺条件，确定了低活性NDC - 4型脱氢催化剂的再生方案，并成功应用于工业生产。
We evaluated novel catalyst-CXM-03 with small scale riser test unit for FCC and examined its commercial application at FCC plant.
对新型高效催化裂化助剂CXM -03的小型提升管催化裂化试验装置进行了评价，并在一催化装置上进行了工业应用。
The application, reaction mechanism and selection of liquid or gas atmospheric temperature arsenic removal catalyst in olefin unit are introduced in the article.
介绍液态或气态常温脱胂催化剂在烯烃工业中的应用、反应机理及其选用。
The kinetic model of hydrothermal deactivation and the model of unit balance activity for FCC catalyst were established.
依据催化裂化催化剂水热失活过程伴随着超稳化过程，确定了催化剂自抑制水热失活动力学模型方程。
Taking nickel catalyst system as an example, the effects of dissolved oxygen on butadiene polymerization and the result of using the pressure-self-raising-unit were analyzed.
以镍系催化剂为例，考察了溶解氧对丁二烯聚合系统的影响，并考察了使用升压器后的作用效果。
The process is carried out by using Soxhlet set, as experiment unit, with methyl sulfonic acid as a catalyst and magnesium sulfite as dehydrating agent, giving 97.
报道了合成乳酸丁酯的新方法 ，以乳酸和正丁醇为原料 ，在甲基磺酸催化下以亚硫酸镁为脱水剂 ，用索氏提取器进行回流合成。
The status and trend in development of catalyst cooler in residue fluid catalytic cracking unit (RFCCU) were introduced.
介绍了重油催化裂化取热技术的现状及发展趋势。
When the unit capacity is not well cooperating with the pressure at certain process conditions, product quality decreases or catalyst loss increases.
工艺条件一定，压力决定了整个装置的处理量，处理量与压力条件不匹配，会造成产品分布不达标或者剂耗增大。
Bis(p-hydroxybenzonic acid butanediolate)(BBHB)as mesogenic unit was prepared with methyl p-hydroxybenzoate, 1,4-butanediol and catalyst by melting transesterification.
以对羟基苯甲酸甲酯、1，4丁二醇为主要原料，经熔融酯交换合成介晶基元双-对羟基苯甲酸丁二醇酯（BBHB）；
Bis(p-hydroxybenzonic acid butanediolate)(BBHB)as mesogenic unit was prepared with methyl p-hydroxybenzoate, 1,4-butanediol and catalyst by melting transesterification.
以对羟基苯甲酸甲酯、1，4丁二醇为主要原料，经熔融酯交换合成介晶基元双-对羟基苯甲酸丁二醇酯（BBHB）；
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