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    • 83. 发明授权
    • Heat recovery in absorption and desorption processes
    • 吸收和解吸过程中的热回收
    • US09573093B2
    • 2017-02-21
    • US14235049
    • 2012-06-27
    • Johannes Menzel
    • Johannes Menzel
    • B01D53/14C01B3/52C10L3/10
    • B01D53/1475B01D53/1425B01D53/1456B01D2252/2021B01D2252/2025B01D2252/2026B01D2252/20431B01D2259/65C01B3/52C10L3/102C10L2290/541Y02P20/124Y02P20/57
    • A method for removing components to be separated from industrial gases using an absorption and desorption processes having liquid absorbents. At least one absorption device and one desorption device are provided, at least a part of the laden solution leaving the absorption device is diverted before being heated and delivered to the head of the heat transfer section. The laden partial stream is heated by the steam rising from the lower part of the desorption device through heat exchange in the heat transfer section. The remaining stream of cold, laden solution leaving the absorption device is expanded by so the relief valve and the heat exchanger into a pressure relief vessel, such that the stream leaving the heat exchanger separates into a liquid and a gaseous state. The pressure in the pressure relief vessel pressure is lowered so that the total energy demand in absorption and desorption processes is reduced.
    • 一种使用具有液体吸收剂的吸收和解吸工艺除去与工业气体分离的组分的方法。 提供至少一个吸收装置和一个解吸装置,离开吸收装置的载体溶液的至少一部分在被加热并转移到传热部分的头部之前被转移。 负载的部分气体通过在传热部分中通过热交换从解吸装置的下部升起的蒸汽被加热。 剩下的离开吸收装置的冷的载满溶液的流通过溢流阀和热交换器扩张到压力释放容器中,使得离开热交换器的流分离成液体和气态。 压力释放容器压力的压力降低,使得吸收和解吸过程中的总能量需求降低。
    • 84. 发明申请
    • HEAT RECOVERY IN ABSORPTION AND DESORPTION PROCESSES
    • 吸收和解吸过程中的热回收
    • US20150078973A1
    • 2015-03-19
    • US14235049
    • 2012-06-27
    • Johannes Menzel
    • Johannes Menzel
    • B01D53/14
    • B01D53/1475B01D53/1425B01D53/1456B01D2252/2021B01D2252/2025B01D2252/2026B01D2252/20431B01D2259/65C01B3/52C10L3/102C10L2290/541Y02P20/124Y02P20/57
    • A method for removing components to be separated from industrial gases using an absorption and desorption processes having liquid absorbents. At least one absorption device and one desorption device are provided, at least a part of the laden solution leaving the absorption device is diverted before being heated and delivered to the head of the heat transfer section. The laden partial stream is heated by the steam rising from the lower part of the desorption device through heat exchange in the heat transfer section. The remaining stream of cold, laden solution leaving the absorption device is expanded by so the relief valve and the heat exchanger into a pressure relief vessel, such that the stream leaving the heat exchanger separates into a liquid and a gaseous state. The pressure in the pressure relief vessel pressure is lowered so that the total energy demand in absorption and desorption processes is reduced.
    • 一种使用具有液体吸收剂的吸收和解吸工艺除去与工业气体分离的组分的方法。 提供至少一个吸收装置和一个解吸装置,离开吸收装置的载体溶液的至少一部分在被加热并转移到传热部分的头部之前被转移。 负载的部分气体通过在传热部分中通过热交换从解吸装置的下部升起的蒸汽被加热。 剩下的离开吸收装置的冷的载满溶液的流通过溢流阀和热交换器扩张到压力释放容器中,使得离开热交换器的流分离成液体和气态。 压力释放容器压力的压力降低,使得吸收和解吸过程中的总能量需求降低。
    • 88. 发明授权
    • Methods for depleting hydrogen sulfide in natural gas from the exploitation of crude oil/natural gas mixtures
    • 从开采原油/天然气混合物中消耗天然气中的硫化氢的方法
    • US08361201B2
    • 2013-01-29
    • US11921197
    • 2006-05-24
    • Johannes MenzelGeorg Saecker
    • Johannes MenzelGeorg Saecker
    • B01D53/14
    • B01D53/1493B01D53/1468C10L3/10C10L3/102E21B43/40
    • The hydrogen sulphide content of natural gas obtained from the extraction of sour-gas containing crude oil/ natural gas mixtures, is reduced by reducing the high pressure of a raw crude oil/ natural gas mixture to 70-130 bar, separating an outgassing raw gas from the crude oil, cooling the outgassed raw gas and simultaneously drawing off a liquid medium which condenses from the outgassing raw gas during cooling. The outgassed raw gas is subjected, after pressure reduction, to gas scrubbing by a physically active solvent. The laden solvent is directed to at least one pressure reduction step to obtain H2S outgas from the solvent. The pressure of the crude oil is further reduced in two subsequent steps to 20-40 bar and 2-15 bar and additional H2S rich raw gas streams are separated from the crude oil which outgas therefrom. The H2S containing gas outgassed from the solvent is brought to the same pressure as the H2S rich raw gases outgassed from the crude oil and all outgassed H2S containing streams are combined and brought to a pressure above that of the crude oil reservoir and fed into a well in the reservoir.
    • 通过将原始原油/天然气混合物的高压降低至70-130巴,从提取含有原油/天然气混合物的含酸气体获得的天然气中的硫化氢含量降低,将脱气原料气 从原油中冷却脱气的原料气体,同时从冷却过程中从脱气原料气体中冷凝出来的液体介质。 脱气后的原料气经减压后经物理活性溶剂进行气体洗涤。 负载溶剂被引导至至少一个减压步骤以从溶剂中获得H 2 S废气。 原油的压力在随后的两个步骤中进一步降低至20-40巴和2-15巴,并且将另外的富H 2原料气流与从其中排出的原油分离。 从溶剂中脱气的含H2S的气体达到与从原油排出的富H2S的原料气体相同的压力,并且将所有脱气的含H 2 S的料流合并,并使其压力高于原油储层的压力,并进料到井 在水库里。