利索-全球专利检索

  1. 登录
  2. 注册

搜索结果

65 条记录 (耗时 0.013 秒)

    Power plant and method of operation
    1.
    发明公开
    Power plant and method of operation 有权
    电厂和操作方法

    公开(公告)号：EP2562386A2

    公开(公告)日：2013-02-27

    申请号：EP12180609.5

    申请日：2012-08-16

    申请人： General Electric Company

    发明人： Popovic, Predrag

    IPC分类号： F02C3/34

    CPC分类号： F02C3/34 ,  F01K23/10 ,  F05D2260/61 ,  F25J3/04018 ,  F25J3/04127 ,  F25J3/04533 ,  F25J3/04569 ,  F25J3/046 ,  F25J2260/80

    摘要： A power plant and method of operation is provided. The power plant comprises at least one main air compressor (12), an oxidizer unit (62) configured to deliver a compressed oxygen-rich gas flow (24) to at least one gas turbine assembly. Each assembly comprises a turbine combustor (32) for mixing the compressed oxygen-rich gas flow (24) with a recirculated gas flow (50) and a fuel stream (28) to burn a combustible mixture and form the recirculated gas flow (50). A recirculation loop (52) recirculates the recirculated gas flow (50) from a turbine (34) to a turbine compressor (30). A recirculated gas flow extraction path (63) extracts a portion of the recirculated gas flow (50) and delivers this to a gas separation system (65). The gas separation system (65) separates the second portion of the recirculated gas flow (50) into a nitrogen portion and a carbon dioxide portion.

    摘要翻译： 提供发电厂和操作方法。 该动力设备包括至少一个主空气压缩机（12），配置成将压缩的富氧气流（24）输送到至少一个燃气涡轮机组件的氧化器单元（62）。 每个组件包括用于将压缩的富氧气流（24）与再循环气流（50）和燃料流（28）混合以燃烧可燃混合物并形成再循环气流（50）的涡轮燃烧室（32） 。 再循环回路（52）将再循环气流（50）从涡轮（34）再循环到涡轮压缩机（30）。 再循环气流提取路径（63）提取再循环气流（50）的一部分并将其输送到气体分离系统（65）。 气体分离系统（65）将再循环气流（50）的第二部分分离成氮部分和二氧化碳部分。

    GAS- UND DAMPFTURBINENANLAGE
    3.
    发明公开
    GAS- UND DAMPFTURBINENANLAGE 有权
    GAS- UND DAMPFTURBINENLAGE

    公开(公告)号：EP1105624A1

    公开(公告)日：2001-06-13

    申请号：EP99952298.0

    申请日：1999-08-04

    申请人： SIEMENS AKTIENGESELLSCHAFT

    发明人： SCHIFFERS, Ulrich ,  HANNEMANN, Frank

    IPC分类号： F01K23/06 ,  F02C3/28

    CPC分类号： F01K23/068 ,  F25J3/04018 ,  F25J3/04127 ,  F25J3/04545 ,  F25J3/04575 ,  F25J3/046 ,  F25J3/04606 ,  F25J3/04618 ,  F25J2240/70 ,  F25J2240/82 ,  Y02E20/16 ,  Y02E20/18 ,  Y02P80/154 ,  Y02T10/16

    摘要： The invention relates to a gas- and steam turbine unit (1) comprising a steam generator (30) which uses waste heat and is mounted downstream from the gas turbine (2) on the flue gas side. The heating surfaces of the generator are mounted in the water-steam circuit (24) of said steam turbine (20). A gasification device (132) is mounted downstream from the gas turbine (2) through a fuel duct (130) for integrated gasification of a fossil fuel (B). A saturator (150) is mounted in the fuel duct (130). Reliable operation of said saturator (150) is required for such a gas- and steam turbine unit (1) irrespective of the operation mode of said gasification device (132). In addition, a steam water-heat exchanger (184), mounted on the secondary side of said saturator circuit (132), is fed on its primary side with feeding water (S) drawn from the water-steam circuit (24) of the steam turbine (20). The feed water (S) which is cooled in the water-heat exchanger of the saturator (184) can be heated by means of a partial stream (T) of compressed air, whereby said partial stream (T) of compressed air can transferred to an air separation facility (138) mounted upstream from said gasification device.

    摘要翻译： 本发明涉及一种包括蒸汽发生器（30）的燃气轮机和蒸汽轮机单元（1），该蒸汽发生器使用废热并且安装在烟气侧的燃气轮机（2）的下游。 发电机的加热表面安装在所述蒸汽轮机（20）的水蒸汽回路（24）中。 气化装置（132）通过用于化石燃料（B）的整体气化的燃料管（130）安装在燃气轮机（2）的下游。 饱和器（150）安装在燃料管道（130）中。 无论所述气化装置（132）的操作模式如何，对于这种气体和蒸汽涡轮机单元（1）都需要所述饱和器（150）的可靠操作。 另外，安装在所述饱和器回路（132）的次级侧上的蒸汽 - 水 - 热交换器（184）在其初级侧上供给有从水蒸汽回路（24）抽出的供水（S） 蒸汽轮机（20）。 在饱和器（184）的水 - 热交换器中冷却的供给水（S）可以借助于压缩空气的部分流（T）加热，由此所述压缩空气的部分流（T）可以转移到 安装在所述气化装置上游的空气分离装置（138）。

    Operation of integrated gasification combined cycle power generation systems at part load
    5.
    发明公开
    Operation of integrated gasification combined cycle power generation systems at part load 失效
    Teillast的Betrieb-integrierter Vergasungs- und kombinierter Zykluskraftwerke

    公开(公告)号：EP0773416A2

    公开(公告)日：1997-05-14

    申请号：EP96307986.8

    申请日：1996-11-04

    申请人： AIR PRODUCTS AND CHEMICALS, INC.

    发明人： Smith, Arthur Ramsden ,  Woodward, Donald Winston

    IPC分类号： F25J3/04

    CPC分类号： F25J3/04127 ,  F01K23/068 ,  F25J3/04018 ,  F25J3/0403 ,  F25J3/04036 ,  F25J3/04545 ,  F25J3/04563 ,  F25J3/04575 ,  F25J3/04606 ,  F25J3/04618 ,  F25J3/04836 ,  F25J2290/10 ,  Y02E20/16 ,  Y02E20/18

    摘要： An integrated gas turbine/air separation system is operated at or below full system load by feeding the air separation unit (39) with air from a dedicated air feed compressor (43) and optionally with extracted air (37) from the gas turbine air compressor (3). When the gas turbine air compressor discharge (5) drops below a selected pressure at part load conditions, the flow of extracted air (37) to the air separation unit (39) is discontinued and the air separation unit (39) operates at constant pressure supplied only by the air feed compressor (43). This mode of operation is particularly useful in an integrated gasification combined cycle (IGCC) power generation system and allows the design of the oxygen and nitrogen product compressors (51,61,67) such that the compressors operate at high efficiency during full load IGCC operation.

    摘要翻译： 通过向空气分离单元（39）供应来自专用空气进料压缩机（43）的空气和可选地从燃气轮机空气压缩机（37）抽出的空气（37），将整体式燃气轮机/空气分离系统运行在全系统负荷或低于整个系统负荷 （3）。 当部分负荷条件下，当燃气轮机空气压缩机排气（5）下降到选定压力以下时，抽出空气（37）到空气分离单元（39）的流动停止，空气分离单元（39）以恒压 仅由供气压缩机43提供。 这种操作模式在综合气化联合循环（IGCC）发电系统中特别有用，并允许设计氧气和氮气产品压缩机（51,61,67），使得压缩机在全负载IGCC运行期间以高效率运行 。

    Multiple reboiler, double column, elevated pressure air separation cycles and their integration with gas turbines
    6.
    发明公开
    Multiple reboiler, double column, elevated pressure air separation cycles and their integration with gas turbines 无效
    高压空气分离循环与多个再沸器和双塔和它们在燃气涡轮机整合。

    公开(公告)号：EP0556516A2

    公开(公告)日：1993-08-25

    申请号：EP92311270.0

    申请日：1992-12-10

    申请人： AIR PRODUCTS AND CHEMICALS, INC.

    发明人： Xu, Jianguo ,  Agrawal, Rakesh

    IPC分类号： F25J3/04

    CPC分类号： F25J3/04618 ,  F25J3/04018 ,  F25J3/0406 ,  F25J3/0409 ,  F25J3/04127 ,  F25J3/04212 ,  F25J3/04303 ,  F25J3/04309 ,  F25J3/04315 ,  F25J3/04321 ,  F25J3/04351 ,  F25J3/04357 ,  F25J3/04393 ,  F25J3/04418 ,  F25J3/04575 ,  F25J3/046 ,  F25J2200/20 ,  F25J2200/54 ,  F25J2205/02 ,  F25J2250/20 ,  F25J2250/40 ,  F25J2250/50 ,  F25J2250/52 ,  Y10S62/915 ,  Y10S62/939

    摘要： The present invention is a liquid nitrogen reflux means improvement capable of allowing the operation of conventional dual and triple reboiler air separation cycles at elevated pressures. The improvement comprises: (a) heat exchanging (148) a portion (162) of the liquid oxygen bottoms of the lower pressure column (116) against a nitrogen vapor stream (146) removed from the higher or lower pressure columns (110,116) or derived from the gaseous nitrogen product (152), wherein prior to such heat exchange the pressure of the liquid oxygen bottoms portion or the nitrogen vapor stream or both the pressure of the liquid oxygen bottoms portion and the nitrogen vapor stream is adjusted by an effective amount so that an appropriate temperature difference exists between the liquid oxygen bottoms and the nitrogen vapor stream so that upon heat exchange the nitrogen vapor is totally condensed and the liquid oxygen bottoms portion is at least partially vaporized; (b) utilizing the condensed nitrogen as reflux in at least one of the two distillation columns; and (c) warming the vaporized oxygen to recover refrigeration.

    摘要翻译： 本发明能够允许操作传统的双和三再沸器空气分离循环的在升高的压力的液态氮回流液的手段改善。 改进之处包括：（A）热交换（148）一个从较高或较低的压力柱（110.116）中除去低压塔（116）抵靠氮蒸汽流（146）的液态氧塔底的部分（162）或 从气态氮气产品（152）worin谋求热交换之前得到的液氧底部部分或氮蒸气流或液氧底部部分的两个中的压力和氮蒸气流的压力是通过在有效量的调节 所以没有在合适的温度差的液氧底部和氮蒸气流所以没有在热交换的氮蒸汽全部冷凝和液氧底部部分至少部分汽化之间存在; （B）利用所述冷凝氮如在两个蒸馏塔中的至少一个回流; 和（c）加热所述汽化的氧以回收致冷。

    VERFAHREN UND VORRICHTUNG ZUR ERZEUGUNG VON DRUCKSTICKSTOFF
    8.
    发明公开
    VERFAHREN UND VORRICHTUNG ZUR ERZEUGUNG VON DRUCKSTICKSTOFF 审中-公开

    公开(公告)号：EP3027988A2

    公开(公告)日：2016-06-08

    申请号：EP14744775.9

    申请日：2014-07-29

    申请人： Linde Aktiengesellschaft

    发明人： ALEKSEEV, Alexander ,  GOLOUBEV, Dimitri ,  ECKERT, Thomas

    IPC分类号： F25J3/04

    CPC分类号： F25J3/04424 ,  F25J3/04018 ,  F25J3/04024 ,  F25J3/04048 ,  F25J3/04054 ,  F25J3/0406 ,  F25J3/04084 ,  F25J3/04115 ,  F25J3/04121 ,  F25J3/04127 ,  F25J3/04145 ,  F25J3/04175 ,  F25J3/04296 ,  F25J3/04303 ,  F25J3/04339 ,  F25J3/04351 ,  F25J3/04387 ,  F25J3/04393 ,  F25J3/04412 ,  F25J3/04569 ,  F25J3/04781 ,  F25J3/04787 ,  F25J3/04872 ,  F25J3/04878 ,  F25J2200/52 ,  F25J2200/54 ,  F25J2205/04 ,  F25J2230/40 ,  F25J2235/52 ,  F25J2240/04 ,  F25J2240/10 ,  F25J2245/02 ,  F25J2245/40 ,  F25J2270/02

    摘要： The invention relates to a method and to a device that serve for producing compressed nitrogen by low-temperature decomposition of air in a distillation column system which has a high-pressure column (202), a low-pressure column (203), a high-pressure column head condenser (204) and a low-pressure column head condenser (205). A main air compressor (9) constitutes the only gas compressor powered by external energy. In the main air compressor (9) the feed air is compressed to a total air pressure which is at least 5 bars above the operating pressure of the high-pressure column (202). A first part-stream (56) of the high-pressure total air stream (11, 811) from the main air compressor (9) is expanded to perform work as operating pressure of the high-pressure column or a higher pressure (57) and is introduced into the distillation column system (201). A second part-stream (52, 55) of the high-pressure total air stream (11, 811) is cooled in a main heat exchanger (51) and is introduced at least partially in liquid form into the distillation column system (206, 210). An internally compressed nitrogen stream is formed by a part-stream (319) of the liquid nitrogen stream (215) from the high-pressure column head condenser (204) and/or a part-stream (234, 334) of the liquid nitrogen stream (232) from the low-pressure column head condenser (205); the internally compressed nitrogen stream is brought in the liquid state to a product pressure (235, 335a, 335b) which is between 15 and 100 bars; then the internally compressed nitrogen stream is heated in the main heat exchanger (51) and then extracted as a gaseous compressed nitrogen product (60) below the product pressure.

    摘要翻译： 一种用于在具有高压塔，低压塔，高压塔塔冷凝器和低压塔的蒸馏塔系统中通过空气低温分解来生产压缩氮的方法和装置 头冷凝器。 主要的空气压缩机构成了由外部能源供电的唯一的气体压缩机。 通过来自高压塔塔冷凝器的液氮流的一部分流和/或来自低压塔头冷凝器的液氮流的一部分流形成内部压缩的氮气流; 将内部压缩的氮气流引入液体状态至15至100巴之间的产品压力; 然后将内部压缩的氮气流在主热交换器中加热，然后以低于产品压力的气态压缩氮气产物提取。

    Power plant and method of operation
    10.
    发明公开
    Power plant and method of operation 有权
    电厂和操作程序

    公开(公告)号：EP2562386A3

    公开(公告)日：2013-12-25

    申请号：EP12180609.5

    申请日：2012-08-16

    申请人： General Electric Company

    发明人： Popovic, Predrag

    IPC分类号： F02C3/34 ,  F01D13/02 ,  F02C6/00 ,  F25J3/04

    CPC分类号： F02C3/34 ,  F01K23/10 ,  F05D2260/61 ,  F25J3/04018 ,  F25J3/04127 ,  F25J3/04533 ,  F25J3/04569 ,  F25J3/046 ,  F25J2260/80

    摘要： A power plant and method of operation is provided. The power plant comprises at least one main air compressor (12), an oxidizer unit (62) configured to deliver a compressed oxygen-rich gas flow (24) to at least one gas turbine assembly. Each assembly comprises a turbine combustor (32) for mixing the compressed oxygen-rich gas flow (24) with a recirculated gas flow (50) and a fuel stream (28) to burn a combustible mixture and form the recirculated gas flow (50). A recirculation loop (52) recirculates the recirculated gas flow (50) from a turbine (34) to a turbine compressor (30). A recirculated gas flow extraction path (63) extracts a portion of the recirculated gas flow (50) and delivers this to a gas separation system (65). The gas separation system (65) separates the second portion of the recirculated gas flow (50) into a nitrogen portion and a carbon dioxide portion.