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    • 2. 发明申请
    • Power station and method for operating the same
    • 电站及其运行方法
    • US20120060728A1
    • 2012-03-15
    • US13138977
    • 2010-04-03
    • Jewgeni NazarkoErnst RienscheReinhard MenzerWilhelm Albert MeulenbergStefan Baumann
    • Jewgeni NazarkoErnst RienscheReinhard MenzerWilhelm Albert MeulenbergStefan Baumann
    • F23C9/00F23L15/00F23L7/00F23J15/00
    • F23L7/007F23C9/00F23C2202/30F23J15/06F23J15/08F23J2215/50F23L2900/07001Y02E20/322Y02E20/344Y02E20/363
    • A combustion system comprising a burner and a combustion chamber, is connected by way of a line to a membrane unit having a high-temperature membrane for extracting the combustion oxygen from the air, the membrane unit having a feed line for a flushing gas on the permeate side. The combustion system further comprises a circulation element for recirculated flue gas, a heat exchanger being disposed upstream of the membrane unit inside the flue gas line. Disclosed is a method for operating this combustion system, in which carbon-containing fuel is burned in an oxygen-flue gas atmosphere, and in which the oxygen for combustion is produced from air by means of a membrane unit comprising a high-temperature membrane, and in which the flue gas is in part recirculated. Disclosed are the steps of first cooling the recirculated flue gas, optionally for a flue gas scrubbing process, subsequently reheating the cooled flue gas to ensure the necessary operating temperature of the membrane, the heating energy being extracted by way of a heat exchange with the flue gas having the corresponding temperature level of the combustion process, and feeding the flue gas heated in this manner to the membrane unit as a flushing gas.
    • 包括燃烧器和燃烧室的燃烧系统通过管线连接到具有用于从空气中提取燃烧氧的高温膜的膜单元,所述膜单元具有用于冲洗气体的进料管线 渗透面 燃烧系统还包括用于再循环烟道气的循环元件,热交换器设置在烟道气管线内部的膜单元的上游。 公开了一种操作该燃烧系统的方法,其中含碳燃料在氧 - 烟气气氛中燃烧,其中通过包含高温膜的膜单元由空气产生用于燃烧的氧, 并且其中烟道气部分地再循环。 公开了首先冷却再循环烟道气的步骤,任选地用于烟道气洗涤过程,随后重新加热冷却的烟道气以确保膜的必要操作温度,加热能量通过与烟道的热交换提取 气体具有相应的燃烧过程的温度水平,并将以这种方式加热的烟道气供给到膜单元作为冲洗气体。
    • 3. 发明申请
    • IGCC POWER PLANT HAVING FLUE GAS RECIRCULATION AND FLUSHING GAS
    • IGCC发电厂有气体回收和冲洗气体
    • US20110162382A1
    • 2011-07-07
    • US12737982
    • 2009-08-05
    • Ernst RienscheReinhard MenzerLudger Blum
    • Ernst RienscheReinhard MenzerLudger Blum
    • F02C6/18F02C6/00
    • F01K23/068C01B3/16C01B3/501C01B13/0248C01B2203/0475C01B2210/0046F02C3/20F02C3/28F02C6/18F05D2220/31F05D2220/32F22B1/1815F22B1/1846Y02E20/16Y02E20/18Y02P20/123Y02P20/124Y02P20/126Y02P20/129
    • Disclosed is a method for operating an IGCC power plant, wherein the coal gas from a gasifier, comprising CO and hydrogen, is supplied to at least one shift stage, wherein this is converted primarily into CO2 and hydrogen and the coal gas is subjected to at least one gas cleaning step. The coal gas is conducted over a membrane, which at least partially selectively separates the hydrogen from the coal gas. In order to achieve driving potential in the membrane, a flushing gas is used on the permeate side. The hydrogen depleted retentate is fed to a CO2 conditioning process, while the separated hydrogen is fed together with the flushing gas to a gas turbine as fuel gas. The flushing gas used for the membrane is a component of the waste gas produced in the gas turbine after the waste gas has left the waste heat recovery boiler, which is connected downstream of the gas turbine. In the power plant, the gas turbine also functions as a means for providing the flushing gas. The power plant comprises a line from the waste heat recovery boiler connected downstream of the gas turbine to the permeate side of the membrane.
    • 公开了一种用于操作IGCC发电厂的方法,其中来自包括CO和氢气的气化器的煤气被供应到至少一个换档阶段,其中主要转化为CO 2和氢气,并且煤气经受 至少一个气体清洁步骤。 煤气在膜上传导,膜至少部分地选择性地将氢气与煤气分离。 为了实现膜中的驱动电位,在渗透侧使用冲洗气体。 将耗尽氢的滞留物进料到CO 2调节过程中,而将分离的氢气与冲洗气体一起供给燃气轮机作为燃料气体。 用于膜的冲洗气体是废气在离开燃气轮机下游的废热回收锅炉之后在燃气轮机中产生的废气的一部分。 在发电厂中,燃气轮机也用作提供冲洗气体的手段。 发电厂包括从燃气轮机下游连接到膜的渗透侧的废热回收锅炉的管线。
    • 4. 发明申请
    • DEVICE AND METHOD FOR REDUCING CO2-EMISSIONS FROM THE WASTE GASES OF COMBUSTION PLANTS
    • 用于减少燃烧废物的二氧化碳排放的装置和方法
    • US20100172813A1
    • 2010-07-08
    • US12451966
    • 2008-05-30
    • Jewgeni NazarkoErnst RienscheLudger BlumReinhard MenzerWilhelm Albert MeulenbergMartin Bram
    • Jewgeni NazarkoErnst RienscheLudger BlumReinhard MenzerWilhelm Albert MeulenbergMartin Bram
    • B01D53/62B01D53/86
    • B01D53/229B01D2257/30B01D2257/504Y02C10/04Y02C10/10
    • A method for separating carbon dioxide from a flue gas using a membrane (membrane module) is characterized in that the flue gas is at temperatures above the condensation point of the water vapor before entering the membrane separation stage. In this way, condensation of any potentially entrained water vapor out of the flue gas is avoided, so as to consistently prevent clogging of the membrane pores. The high temperatures can be achieved in different ways. The temperature of the flue gas can easily be increased to the necessary temperatures by way of an upstream heat exchanger or a burner. A compressor, which is connected upstream of the membrane module and also advantageously increases the CO2 partial pressure, brings about the necessary temperature increase at the same time. As a further alternative for the invention, the CO2 separation is performed even before desulfurizing the flue gas. This notably has the advantage of the flue gas in this process stage still being at temperatures above the condensation point of the water vapor, and thus not having to be heated separately, in addition to which, it generally carries little water vapor at this stage of the scrubbing operation.
    • 使用膜(膜组件)从烟道气中分离二氧化碳的方法的特征在于,在进入膜分离阶段之前,烟道气处于高于水蒸汽冷凝点的温度。 以这种方式,避免任何潜在夹带的水蒸气从烟道气中冷凝,从而始终防止膜孔堵塞。 高温可以通过不同的方式实现。 烟气的温度可以通过上游热交换器或燃烧器容易地增加到必要的温度。 连接在膜组件上游的压缩机也有利地增加CO 2分压,同时带来必要的温度升高。 作为本发明的另一替代方案,即使在烟道气脱硫之前也进行CO 2分离。 这显着地具有在该工艺阶段中的烟道气仍然处于高于水蒸气冷凝点的温度的优点,因此不必单独加热,除此之外,其通常在该阶段几乎没有水蒸汽 擦洗操作。
    • 6. 发明授权
    • Power plant that uses a membrane and method for operating the same
    • 使用膜的发电厂及其操作方法
    • US08506678B2
    • 2013-08-13
    • US12734682
    • 2008-10-29
    • Wilhelm Albert MeulenbergStefan BaumannLudger BlumErnst Riensche
    • Wilhelm Albert MeulenbergStefan BaumannLudger BlumErnst Riensche
    • B01D53/22
    • B01D53/22B01D2256/12F23C9/00F23C2202/30F23L7/007F23L15/00F23L2900/07001Y02E20/322Y02E20/344Y02E20/348
    • Provided is a power plant for generating electrical energy comprising a combustion chamber for producing steam, at least one downstream flue gas purification stage, a separation stage for CO2, a recycling circuit for the flue gas, and a high-temperature O2 membrane, which is connected upstream of the combustion chamber. The high-temperature O2 membrane has an inlet and an outlet on the feed side which are thermally coupled by way of a heat exchanger. On the permeate side, the high-temperature O2 membrane has only an outlet which is connected to the combustion chamber and/or the flue gas recycling circuit and a means for cooling and/or compression which is disposed in this outlet. The power plant, in which coal is burned using substantially pure oxygen, and in which the combustion waste gas is purified and partially recirculated to the combustion process, is operated in such a way that the oxygen that is used is obtained by separation from air using a high-temperature O2 membrane, wherein the membrane is operated with atmospheric air at a pressure of up to 2 bar on the feed side and a negative pressure of between 0.02 and 0.5 bar is applied on the permeate side.
    • 提供一种用于产生电能的发电厂,其包括用于产生蒸汽的燃烧室,至少一个下游烟道气净化级,用于CO 2的分离级,用于烟道气的回收回路和高温O 2膜,其是 连接在燃烧室的上游。 高温O 2膜在进料侧具有通过热交换器热耦合的入口和出口。 在渗透侧,高温O 2膜仅具有连接到燃烧室和/或烟道气回收回路的出口以及设置在该出口中的用于冷却和/或压缩的装置。 使用基本纯净的氧燃烧煤并且其中燃烧废气被净化并部分地再循环到燃烧过程的发电厂以这样的方式运行,使得使用的氧气通过使用 高温O2膜,其中膜在进料侧的压力为2巴的大气中进行操作,并且在渗透侧施加0.02至0.5巴的负压。
    • 9. 发明申请
    • POWER PLANT THAT USES A MEMBRANE AND METHOD FOR OPERATING THE SAME
    • 使用膜的动力装置及其操作方法
    • US20100263377A1
    • 2010-10-21
    • US12734682
    • 2008-10-29
    • Wilhelm Albert MeulenbergStefan BaumannLudger BlumErnst Riensche
    • Wilhelm Albert MeulenbergStefan BaumannLudger BlumErnst Riensche
    • F01K13/00F01K7/16
    • B01D53/22B01D2256/12F23C9/00F23C2202/30F23L7/007F23L15/00F23L2900/07001Y02E20/322Y02E20/344Y02E20/348
    • Provided is a power plant for generating electrical energy comprising a combustion chamber for producing steam, at least one downstream flue gas purification stage, a separation stage for CO2, a recycling circuit for the flue gas, and a high-temperature O2 membrane, which is connected upstream of the combustion chamber. The high-temperature O2 membrane has an inlet and an outlet on the feed side which are thermally coupled by way of a heat exchanger. On the permeate side, the high-temperature O2 membrane has only an outlet which is connected to the combustion chamber and/or the flue gas recycling circuit and a means for cooling and/or compression which is disposed in this outlet. The power plant, in which coal is burned using substantially pure oxygen, and in which the combustion waste gas is purified and partially recirculated to the combustion process, is operated in such a way that the oxygen that is used is obtained by separation from air using a high-temperature O2 membrane, wherein the membrane is operated with atmospheric air at a pressure of up to 2 bar on the feed side and a negative pressure of between 0.02 and 0.5 bar is applied on the permeate side.
    • 提供一种用于产生电能的发电厂,其包括用于产生蒸汽的燃烧室,至少一个下游烟道气净化级,用于CO 2的分离级,用于烟道气的回收回路和高温O 2膜,其是 连接在燃烧室的上游。 高温O 2膜在进料侧具有通过热交换器热耦合的入口和出口。 在渗透侧,高温O 2膜仅具有连接到燃烧室和/或烟道气回收回路的出口以及设置在该出口中的用于冷却和/或压缩的装置。 使用基本纯净的氧燃烧煤并且其中燃烧废气被净化并部分地再循环到燃烧过程的发电厂以这样的方式运行,使得使用的氧气通过使用 高温O2膜,其中膜在进料侧的压力为2巴的大气中进行操作,并且在渗透侧施加0.02至0.5巴的负压。