• The catalyst deactivation kinetics of pyridine chlorination was investigated in an integral fixed reactor.

    采用积分反应器,研究了吡啶氯化反应中催化剂失活动力学。

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  • The technology of nonylphenol production is using strong acidic cation resin DC604, C104 as catalysts and two-stage fixed reactor in the nonylphenol plant of Heilongjiang Petrochemical Works.

    黑龙江石油化工厂壬基酚装置以强酸性阳离子交换树脂d C604、C104作催化剂,采用二段式固定床反应器流程合成壬基酚的工艺。

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  • Routine shunt reactor fixed on the EHV transmission system can not guarantee the transmission capability and steady state voltage of system under different operation modes.

    常规并联电抗器固定接入超高压输电系统,不能保证各种运行方式下系统输送能力和母线的稳态电压。

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  • The oxidation and molecular recomposition proceeded in the same time, when the isobutanol gas and air passed the fixed bed catalytic reactor continuously.

    异丁醇气体和空气混合后通过催化剂层的固定床反应器,使氧化反应和分子重排反应同时进行。

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  • Through 3 months 'steady operation, the fixed small balls in NO. 3 reactor have a better performance and a better permanence.

    经过3个月的稳定运行,3号反应器内固定化小球性能较好,表现出较好的持久性。

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  • Be favor of industrialization using fixed bed reactor.

    采用固定床反应器,有利于工业化。

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  • Fatty acid methyl esters were prepared by esterification in a fixed bed reactor from methanol and fatty acids in palm oil deodorizer distillate (PODD) using a cation exchange resin as catalyst.

    以强酸性阳离子交换树脂为催化剂,经过自制的固定床反应器,使棕榈油脱臭馏出物(PODD)中的脂肪酸与甲醇起酯化反应,合成脂肪酸甲酯。

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  • Thus the hot spot which causes catalyst deactivation in conventional fixed bed reactor is avoided.

    这样就避免了一般固定床反应器中过热部位使催化剂减活的现象。

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  • In recent years, the irregular shape methane steam reforming catalyst development progresses rapidly with the goal to increase catalyst effectiveness and reduce the pressure drop in fixed bed reactor.

    近年来,甲烷蒸汽转化催化剂异形化研究取得了很大进展,其主要目的是提高催化剂的效率因子,降低固定床反应器中的压降。

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  • The fixed bed reactor, fluidized bed reactor and slurry reactors were compared on their structure, production capacity, materials, products and operating conditions.

    并对固定床、流化床和浆态床反应器的结构、生产能力、原料及产物组成和操作条件等进行了比较。

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  • The synthesis and processing conditions of the bifunctional catalyst for dimethyl ether were studied by using fixed bed reactor in the paper.

    本论文采用固定床反应器,对合成二甲醚双功能催化剂及其工艺条件进行了研究。

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  • A new cascade nonlinear inferential control strategy for a nonadiabatic fixed bed reactor based on improved hybrid model is proposed.

    提出了非绝热式固定床反应器基于改进混合模型的串级非线性推断控制策略。

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  • A new equipment-column type suspension reactor with multiple trays, has been developed for the condensation of phenol with acetone in the production of BPA instead of conventional fixed bed reactor.

    开发了一种被称为多段悬浮床塔式反应器的新型装置,以代替双酚a生产中苯酚与丙酮缩合反应所使用的固定床反应器。

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  • The oligomerization test of mixed olefins in light coke gasoline was carried out in a fixed bed reactor.

    在实验室小型固定床反应器上,以焦化汽油轻馏分为原料,进行了混合烯烃的叠合反应。

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  • Based on fixed fluid bed reactor and GOR Q catalyst, the influence of process parameters on decreasing gasoline olefin was studied.

    在实验室小型固定流化床反应器上考察了工艺参数对国产GOR- Q催化剂降低催化汽油烯烃的影响。

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  • Three kinds of light oil were cracked as feedstocks on regenerated zeolite catalysts in a laboratorial fixed fluidized bed reactor.

    以三种轻燃料油为反应原料,在实验室固定流化床反应器上用工业平衡催化剂进行催化裂化反应。

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  • The oxidative dehydrogenation of butane to butene and butadiene was studied by using conventional fixed bed reactor (FBR), inert membrane reactor (IMR) and mixed inert membrane reactor (MIMR).

    比较了固定床反应器(FBR)、惰性膜反应器(IMR)与混合式惰性膜反应器(MIMR)用于丁烷氧化脱氢制丁烯和丁二烯反应的性能。

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  • The reactions were carried out in an isocratic reactor and an oil bath fixed bed reactor, which are designed by us.

    反应是在实验室自行设计的无梯度反应器和油浴固定床反应器中进行。

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  • The characteristics of fixed bed reactor, fluidized bed reactor, membrane reactor and other reactors which were developed recently were summarized.

    另外还对固定床、流化床、膜反应器以及一些新开发的反应器的特点进行了讨论。

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  • Etherification activities of various molecular sieve catalysts were investigated with FCC light ends as feedstock carrying on a fixed bed micro reactor.

    以炼油厂催化裂化汽油轻馏分为原料,在固定床微型反应器中对几种分子筛催化剂的醚化活性进行了考察。

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  • The performance of the catalysts for hydrodeoxygenation of model organic compounds, butyric acid and butanol, was investigated in a continuous fixed bed reactor.

    以有机含氧化合物丁酸和丁醇为合成油品的模型化合物,在连续流动固定床反应器中考察了催化剂的加氢脱氧性能。

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  • In this paper lead in industrial wastewater can be removed by scrap-iron fixed bed reactor.

    采用铁屑固定床反应器去除工业废水中的铅。

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  • The effect of mineral on conversion of coal and sulfur with different forms in Yima during pyrolysis and hydropyrolysis in a fixed bed reactor was studied.

    在加压固定床上研究了矿物质对义马煤热解和加氢热解产物分布规律以及不同形态硫转化的影响。

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  • Three different kinds of catalysts for methanol pyrolysis are screened out on a continuous fixed bed reactor system.

    在固定床连续流动式反应装置上评选出了三种不同类型的甲醇裂解催化剂。

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  • The catalyst was prepared by impregnating depositing process and the catalyst activity was evaluated with a continuous flow fixed bed reactor.

    采用固定床连续流动反应装置,对此催化剂用于气相苯加氢制环已烷的活性进行评价。

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  • The selective catalytic synthesis of dimethylamine from ammonia and methylalcohol over cerium modified mordenite under ambient pressure in a fixed bed reactor has been studied.

    研究了氨和甲醇以铈改性丝光沸石为催化剂,在常压固定床上选择性合成二甲胺的反应。

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  • In the fixed bed reactor the rate increases with the temperature and the high conversion rate is achieved.

    在固定床内随着温度的提高,反应速率增大,并能达到较高的转化率。

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  • The nickel distribution of residue feedstock and products obtained from fixed bed reactor were studied and focused on the effect of reaction temperature and various hydrotreating catalysts.

    对混合渣油及其经固定床加氢处理后生成油的镍分布进行了研究,考察反应温度和加氢处理催化剂对油样中镍分布的影响。

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  • The nickel distribution of residue feedstock and products obtained from fixed bed reactor were studied and focused on the effect of reaction temperature and various hydrotreating catalysts.

    对混合渣油及其经固定床加氢处理后生成油的镍分布进行了研究,考察反应温度和加氢处理催化剂对油样中镍分布的影响。

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