• 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。

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  • The results showed that the catalyst maintained high characteristics, stationary acrylonitrile yield was obtained and the operation of fluidized bed reactor was optimized.

    采取自动连续补加方式,可以使催化剂保持高性能,从而获得稳定的丙烯腈收率,实现反应器平稳优化操作。

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  • Benzene and its compounds were degraded with this catalyst in a three-phase fluidized bed photo-catalytic reactor and the reaction conditions for photo-catalytic degradation were investigated.

    并用该催化剂在自制的三相流态化反应器内对苯及苯化合物进行了光催化降解反应的研究,并对各种情况下的反应条件进行了探索。

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  • China Xinsu Corporation has 10 kinds of th series high-performance catalyst which suitable for polyethylene production equipment with UNIPOL and BP gas phase fluidized bed process.

    中国新塑公司目前有适用于Unipol和BP气相流化床工艺聚乙烯生产装置的10种TH系列高效催化剂产品。

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  • The performance of oxide catalyst for naphtha cracking was studied in a fixed-fluidized bed reactor.

    使用固定流化床,考察了氧化物催化剂催化裂解石脑油制乙烯的反应。

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  • A type of fluidized bed in which catalyst particles are held in suspension by the upward movement of the liquid reactant and gas flow.

    借助上升的液体反应物和气流使催化剂颗粒维持在悬浮状态的一种流化床。

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  • A gaseous reaction mixture flows from the bottom to the top of a heterogeneous particulate catalyst that forms a fluidized bed in which baffles are arranged.

    气态反应混合物从形成流化床的非均相颗粒催化剂的底部流动到其顶部,其中流化床中排列有隔板。

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  • A process in which the oil is cracked in the presence of finely divided catalyst which is maintained in an aerated or fluidized state by the oil vapors.

    在微粒催化剂存在的条件下油发生裂化的过程,催化剂借助油蒸气维持在松散和流化状态。

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  • The organosilicon wastewater was treated by the combined process of iron shaving fluidized bed pretreatment-catalytic oxidation with loaded activated carbon catalyst-coagulating sedimentation.

    采用铁屑流化床预处理、负载活性炭催化剂催化氧化和混凝沉淀组合工艺处理有机硅废水。

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  • The prepared catalyst on pilot scale was evaluated on fixed-fluidized bed reactor. The results showed that application of the large pore matrix could enhance the heavy oil cracking.

    试验主要对载体和分子筛以及二者的匹配对催化剂重油裂化能力和产品降烯烃效果的影响进行了考察。

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  • The influences of the particle size distribution of equilibrium catalyst on product distribution of fluidized-bed catalytic cracking were investigated.

    研究了催化裂化平衡剂的粒度分布对裂化产品分布的影响。

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  • The influences of the particle size distribution of equilibrium catalyst on product distribution of fluidized-bed catalytic cracking were investigated.

    研究了催化裂化平衡剂的粒度分布对裂化产品分布的影响。

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