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    • 7. 发明授权
    • Apparatus and process for the discharge of quenched or unquenched coke from a coke quenching car into a receiving device
    • 将淬火或未淬火的焦炭从焦炭淬火车排放到接收装置中的装置和方法
    • US09303210B2
    • 2016-04-05
    • US13511862
    • 2010-11-12
    • Sven Badura
    • Sven Badura
    • C10B39/12C10B33/10C10B33/08C10B39/04C10B45/00
    • C10B39/12C10B33/08C10B33/10C10B39/04C10B45/00
    • An apparatus for the discharge of quenched or unquenched coke from a coke quenching car into a receiving device, providing that there is an extension of the pusher machine beside at least one coke-oven chamber, which is arranged in one line with the coke-oven chambers, and which is to be operated by the pusher machine, and that there is a receiving device behind the quenching car as seen from the coke-oven battery into which the coke can be pushed from the quenching car by the extension, the receiving device preferably being a wharf. A process for the discharge of the hot coke from a coke quenching car into a receiving device is also disclosed. Capacity bottlenecks of the quenching equipment are compensated so that the coke need not stay in the coke-oven chamber after the end of the coking process, or disturbances of the quenching equipment can be compensated temporarily.
    • 一种用于将淬火或未熄焦的焦炭从焦化淬火车排放到接收装置中的装置,只要在至少一个焦炉室之间存在推进器机器的延伸部分,该焦炉室与焦炉一起排列 并且由推进器操作,并且在从焦化炉电池观察到的淬火车后面存在接收装置,焦炭可以通过延伸从淬火车推到该接收装置中,接收装置 最好是一个码头。 还公开了一种将焦炭从焦炭熄灭车排放到接收装置中的方法。 淬火设备的容量瓶颈被补偿,使得焦炭在焦化过程结束后不需要停留在焦炉室中,或者可以暂时补偿淬火设备的干扰。
    • 10. 发明授权
    • Method and apparatus for making a methane-rich gas from syngas
    • 从合成气制造富含甲烷的气体的方法和装置
    • US09045708B2
    • 2015-06-02
    • US13876002
    • 2011-10-05
    • Holger ThielertJohannes Menzel
    • Holger ThielertJohannes Menzel
    • C07C1/06C10L3/08B01J8/04
    • C10L3/08B01J8/0453B01J8/0492C07C1/06C07C9/04
    • A methane-rich gas from synthesis gas is made in a methane reactor with a row of methanation stages and, at an upstream end of the row of methanation stages, a CO conversion stage. An incoming stream of synthesis gas containing CO and H2 is split into a plurality of partial streams, one of which is fed to the reactor upstream of the CO conversion stage. Each of the other partial syngas streams is fed to the reactor upstream of a respective one of the methanation stages such that methanation takes place in each of the methanation stages and gas exits from the stages and mixes with the partial syngas stream being fed to the next downstream stage. A plurality of partial streams are diverted from a product-gas stream issuing from the furthest downstream stage and are each fed to the reactor upstream of a respective one of the methanation stages.
    • 来自合成气的富甲烷气体在具有甲烷化阶段的甲烷反应器中制备,并且在甲烷化阶段的上游端具有CO转化阶段。 含有CO和H2的合成气的进料流被分成多个部分气流,其中一个部分气体被供给到CO转化段上游的反应器。 每个其他部分合成气流在相应的一个甲烷化阶段的上游进料到反应器,使得甲烷化在每个甲烷化阶段中发生,并且气体从该阶段排出,并且与部分合成气流混合并进料到下一个 下游阶段。 多个部分流从从最远的下游阶段发出的产物气流转向,并且分别在相应的甲烷化阶段的上游进料到反应器。