• Impact of COD/N values of feed wastewater on COD, nitrogen removal and biomass growth in a sequencing fed batch reactor (SFBR) operation was investigated.

    采用序半连续反应器就新鲜废水COD/N比对COD、氮化合物去除效率微生物生长影响进行研究。

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  • The process of jet mixing in the reactor was studied with tracer technique and the effects of the opening structure on the wall of the feed ring and the momentum ratio to the jet mixing were analyzed.

    文中采用示研究了四氯化钛氧化反应器内径向射流混合特征,探讨射流开孔结构动量比等因素射流混合效果影响。

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  • The effect of different feed COD concentrations on the removal of phosphorus and nitrogen in a sequencing batch moving bed biofilm reactor(SBMBBR) was studied.

    研究批式移动生物膜反应器SBMBBRCOD进水浓度对同步脱效果影响。

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  • A newly down flow reactor with new ways of feed atomization and oil catalyst contact was developed according to the characteristic of ultra short contact time catalytic cracking process.

    根据接触时间催化裂化工艺特点,开发具有新型原料雾化剂、接触方式下行式反应器

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  • The method further comprises reacting an additional feed with the spent catalyst in the reactor to deposit additional coke on the spent catalyst, defining a gas product.

    方法进一步包括反应器中使额外原料废弃催化剂反 应从而在废弃催化剂沉积额外的焦炭生成一种气体产品

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  • The pulse flow is induced in a downflow boiling point reactor by vaporization of a portion of the liquid feed at proper conditions.

    通过适当条件汽化一部分液体进料在下流式沸点反应器引发脉冲流动

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  • Based on the properties of carbonaceous catalyst, composition of feed gas and the size parameters of reforming reactor, heat and material balance of reactor were established.

    基于催化剂特性原料组成重整转化反应器尺寸参数,建立了重整反应器体系的物料平衡和热平衡方程;

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  • The results showed that the solid holdup in the reactor was higher than that in feed, the pressure drop remained unchanged along the axial bed but was influenced by the content of solid in feed;

    结果表明反应器内含率高于进料中的固体含量床层轴向保持不变固相含量影响;

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  • The evaluation of catalytic pyrolysis catalyst using Daqing vacuum gas oil as feed stock was carried out on a heavy oil micro reactor.

    采用重油微反应装置,以大庆蜡油原料催化裂解催化剂进行了反应评价

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  • The upper part of the reactor is provided with feed injectors, which atomize the feed so that feed vaporization and feed and catalyst admixture is optimized.

    反应器上部配有原料注射器述原料注射器雾化原料,以便使原料气化优化原料催化剂混合物

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  • Elaborate main transformer and reactor plus steady wire feed circuit, ensure advanced welding performance.

    精心设计变压器电抗器平稳的送电路使焊接性能达到同类焊机极限。

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  • Feed material was led into the central slurry-bed reactor of lu 'an CTL demonstration unit on July 7th and output on-spec oil on July 10th.

    潞安示范项目核心浆态床装置77日投料进入试车运行,7月10日生产出合成油品,预计将7月底进入成品油装置试车。

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  • When the volume of the reactor is 20ml and other conditions are not changed, the volume of feed water should be adjusted to 10~ 11ml;

    反应体积20毫升,在其它反应条件不变时,反应给水量控制1011毫升;

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  • When the volume of the reactor is 20ml and other conditions are not changed, the volume of feed water should be adjusted to 10~ 11ml;

    反应体积20毫升,在其它反应条件不变时,反应给水量控制1011毫升;

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