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product distribution
    THE ECONOMIC OPTIMAZATION OF PETROLEUM HYDROCRACKING(HC)PROCESS(Ⅲ)MULTI-PRODUCT SYSTEM WITH EMPIRICAL PRODUCT DISTRIBUTION MODEL
    石油加氢裂化过程的经济最优化 (Ⅲ)按经验产品分布关系处理的多产品系统
    EFFECT OF TEMPERATURE DISTRIBUTION IN INNER TUBES AND WATER OIL RATIO ON PRODUCT DISTRIBUTION OF MILLISECOND STEAM CRACKING FURNACE
    管内温度分布及水油比对毫秒炉裂解产品分布的影响
    The Reaction of Aromatization of C_6 Paraffin over Pt/K- L Moleeular Sieve Ⅱ. Reaction Product Distribution and Reaction Mechanism at Different Temneratures
    碳六烷烃在铂-L型分子筛催化剂上的反应规律Ⅱ.不同反应温度的产品分布与反应历程
    PREDICTION OF FCC PRODUCT DISTRIBUTION FROM RESIDUE STRUCTURAL PARAMETERS
    利用渣油结构参数预测催化裂化反应产品分布
    The paper reconstructs the first condition of process capability indices calculation,gives expression of process capability indices under two kinds of transformation methods,and elaborates the important meaning of process capability indices real calculation and restricted limitation by comparing inside relation of the product distribution unqualified rate.
    文章分析了过程能力指数计算的先决条件,给出了两种变换方法下过程能力指数的表达式,并通过与产品分布不合格率的内在关系的比较,阐述了过程能力指数计算真实性的重要意义和受限制的局限性。
    Study on Mathematical Correlation Between Regenerated Catalyst Carbon Contents and FCC Product Distribution
    再生剂碳含量与FCC产品分布的数学关联研究
    THE EFFECT OF COKING TEMPERATURE ON PRODUCT DISTRIBUTION FOR VACUUM RESIDUE I.Product Distribution and Optimum Coking Temperature
    减压渣油焦化温度对产品分布的影响I.产品分布与适宜焦化温度
    PRODUCT DISTRIBUTION FOR SERIES REACTIONS IN CASSON LAMINAR FLOW REACTOR
    Casson流体层流反应器中连串反应的产品分布
    The reaction product distribution of n-C_6 and methyl cyclopentane(MCP)on a series of Pt-catalysts with different basic supports at different temperatures have been studied.
    在相同铂含量、不同碱性载体Pt/K-L,Pt/AlPO_4-5催化剂上,以下已烷和甲基环戊烷反应分为探针,考察不同反应温度下,n-C_6和MCP的反应产品分布
    BrC2F4Br+C2F4 reaction induced by different light source (KrF laser, Xelamp, low pressure Hg-lamp) has been investigated. Experiments show that the reaction product distribution depends not only on reaction composition, but on light intensity and light source as well.
    实验发现,在光引发BrC2F4Br+C2F4调聚反应中,光强(或光功率密度)能影响产品分布
    Influences of the LST 1 on the transfer efficiency of SOx,activity of FCC catalyst,product distribution and quality were investigated in bench-scale apparatus.
    并在小型及中型装置上考察了LST 1液体硫转移助剂的脱SOx 效率 ,及其对FCC催化剂活性、产品分布以及产品性质的影响。
    The results showed that the LST 1 can reduce the emission of SOx by 50% and has no unfavourable influences on product distribution,product properties and the activity of FCC catalyst.
    工业试验表明 ,LST 1液体硫转移助剂能降低SOx 排放量 5 0 %左右 ,对产品分布、产品性质和FCC催化剂活性无不利影响。
    Catalyst content has great influence on product distribution and quality.
    它适用于石蜡基原料 ,催化剂含量对产品分布和产品性能有很大的影响。
    Operation conditions, product distribution and product properties were analyzed based on the comparison of unit evaluation and design data.
    根据装置标定和设计数据的对比 ,对有关操作条件、产品分布及产品性质等进行了分析。
    On the basis of first generation DCC catalysts, CRP-land CIP-1, CIP-2,3,4 and 5 have been successively developed and commercially produced in recent years for keeping abreast of the requirements of individual DCC units in refineries, such as suited for various feedstock, different operation parameters and particular product distribution.
    为适应各炼油厂DCC装置原料油性质、操作参数的差异及产品分布要求的不同,在原有第一代催化裂解催化剂CRP-1、CIP-1的基础上,近年来又开发了CIP-1~CIP-5催化剂。
    We analyze the influence on product characteristic and product distribution through the application of new type passivation MB-1 in RFCCU,the results showed that the passivator is characterized by rapid response and prominent effect,the content of H2 in the catalytic dry gas have decreased averagely by 40 percent points,H2/CH4 have decreased by 37 percent points,the yield of dry gas and coke have little decrease,and creating good economic benefits.
    通过MB-1金属钝化剂在重油催化装置的工业应用,考察了其对产品性质、产品分布的影响,结果表明:该钝化剂具有响应速度快、效果显著的特点,使用后,催化干气H2含量平均下降幅度为40%,H2/CH4降低幅度达37%,干气和焦炭产率有所下降,液收提高,取得良好的经济效益。
    Results from the RU apparatus both showed the influence of different feed oil on the product distribution, and reflected application properties of the RFCC catalyst.
    结果发现,RU小型提升管催化剂评价装置既能反映原料油性质差别对产品分布的影响,又能反映催化剂的使用性能。
    The secondary reactions of FCC nathpha on REUSY, ZRP and MO-REY zeolite catalysts were investigated in a FCC pilot plant with riser reactor to determine the product distribution of secondary reactions and properties of the upgraded gasoline.
    用小型提升管催化裂化实验装置考察了FCC粗汽油在REUSY、ZRP和MO REY沸石催化剂上二次反应的产品分布和改质汽油组成;
    The effect of decompression on product distribution and product property in a 250 kt/a semi-regeneration reformer was studied.
    在青岛石油化工有限责任公司250 kt/a的半再生催化重整装置上进行了降低操作压力对产品分布和产品性质影响的试验研究。
    PRODUCT DISTRIBUTION AND REACTION KINETICS OF THE CATALYTIC CRACKING OF VACUUM GAS OIL ON A HZSM-5 CATALYST
    在HZSM-5分子筛催化剂上的减压瓦斯油催化裂化产品分布及动力学
 

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