CN111406192A - 通过与氮气膨胀机联动制动的膨胀机增压机来产生增压空气的深冷精馏方法与设备 - Google Patents
通过与氮气膨胀机联动制动的膨胀机增压机来产生增压空气的深冷精馏方法与设备 Download PDFInfo
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- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
- F25J3/02—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
- F25J3/04—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
- F25J3/04406—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using a dual pressure main column system
- F25J3/04412—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air using a dual pressure main column system in a classical double column flowsheet, i.e. with thermal coupling by a main reboiler-condenser in the bottom of low pressure respectively top of high pressure column
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Abstract
提供了一种深冷精馏空气以产生氮气和氧气的方法和设备。氮气产品仅从一塔(11)的顶部抽取,如果客户需要更低压力的氮气,部分位于第一氮气产品压力的纯氮气(124)在主换热器(1)中部分复热后,经氮气膨胀机(23)减压至第二氮气产品压力,再经过主换热器(1)进一步复热后,作为低压氮气产品输出,氮气膨胀机(23)可以由压缩空气的膨胀机增压机(24)制动。该方法可以灵活地生产不同压力的氮气,且同时利用氮气膨胀的功减少生产增压空气的能耗。
Description
PCT国内申请,说明书已公开。
Claims (17)
- PCT国内申请,权利要求书已公开。
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PCT/CN2017/113525 WO2019104524A1 (zh) | 2017-11-29 | 2017-11-29 | 通过与氮气膨胀机联动制动的膨胀机增压机来产生增压空气的深冷精馏方法与设备 |
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EP (1) | EP3719427A4 (zh) |
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Cited By (5)
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CN112320764A (zh) * | 2020-10-14 | 2021-02-05 | 杭州电子科技大学 | 一种节能型便携制氧装置 |
CN112361716A (zh) * | 2020-10-26 | 2021-02-12 | 乔治洛德方法研究和开发液化空气有限公司 | 用于从空气分离装置中制备高压气体的方法和装置 |
CN112414003A (zh) * | 2020-11-24 | 2021-02-26 | 乔治洛德方法研究和开发液化空气有限公司 | 一种基于深冷精馏生产空气产品的方法及设备 |
CN113405318A (zh) * | 2021-06-29 | 2021-09-17 | 杭州制氧机集团股份有限公司 | 一种使用单个精馏塔生产纯氮的装置及其使用方法 |
CN113654302A (zh) * | 2021-08-12 | 2021-11-16 | 乔治洛德方法研究和开发液化空气有限公司 | 一种低温空气分离的装置和方法 |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP4215856A1 (en) * | 2022-08-30 | 2023-07-26 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Process and apparatus for air separation by cryogenic distillation |
EP4163576A1 (en) * | 2021-10-06 | 2023-04-12 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Apparatus and process for the separation of air by cryogenic distillation |
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CN112361716A (zh) * | 2020-10-26 | 2021-02-12 | 乔治洛德方法研究和开发液化空气有限公司 | 用于从空气分离装置中制备高压气体的方法和装置 |
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CN113405318A (zh) * | 2021-06-29 | 2021-09-17 | 杭州制氧机集团股份有限公司 | 一种使用单个精馏塔生产纯氮的装置及其使用方法 |
CN113405318B (zh) * | 2021-06-29 | 2024-04-05 | 杭氧集团股份有限公司 | 一种使用单个精馏塔生产纯氮的装置的使用方法 |
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CN113654302B (zh) * | 2021-08-12 | 2023-02-24 | 乔治洛德方法研究和开发液化空气有限公司 | 一种低温空气分离的装置和方法 |
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KR20200088399A (ko) | 2020-07-22 |
EP3719427A4 (en) | 2021-12-01 |
KR102389110B1 (ko) | 2022-04-21 |
US20200355429A1 (en) | 2020-11-12 |
WO2019104524A1 (zh) | 2019-06-06 |
CN111406192B (zh) | 2022-04-08 |
EP3719427A1 (en) | 2020-10-07 |
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