JPH03271685A - 空気液化分離方法及び装置 - Google Patents
空気液化分離方法及び装置Info
- Publication number
- JPH03271685A JPH03271685A JP279691A JP279691A JPH03271685A JP H03271685 A JPH03271685 A JP H03271685A JP 279691 A JP279691 A JP 279691A JP 279691 A JP279691 A JP 279691A JP H03271685 A JPH03271685 A JP H03271685A
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen
- boiling point
- nitrogen gas
- low
- fractionating
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000000034 method Methods 0.000 title claims abstract description 5
- 238000000926 separation method Methods 0.000 title claims description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 29
- 238000009835 boiling Methods 0.000 claims abstract description 15
- 239000001257 hydrogen Substances 0.000 claims abstract description 14
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 14
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 8
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract 13
- 229910001873 dinitrogen Inorganic materials 0.000 claims abstract 13
- 239000000470 constituent Substances 0.000 abstract 7
- 230000001174 ascending effect Effects 0.000 abstract 2
- 230000001105 regulatory effect Effects 0.000 abstract 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract 1
- 238000005194 fractionation Methods 0.000 abstract 1
- 239000007789 gas Substances 0.000 abstract 1
- 239000007788 liquid Substances 0.000 abstract 1
- 239000001301 oxygen Substances 0.000 abstract 1
- 229910052760 oxygen Inorganic materials 0.000 abstract 1
- 239000001307 helium Substances 0.000 description 1
- 229910052734 helium Inorganic materials 0.000 description 1
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 description 1
- -1 liquefied Substances 0.000 description 1
- 229910052754 neon Inorganic materials 0.000 description 1
- GKAOGPIIYCISHV-UHFFFAOYSA-N neon atom Chemical compound [Ne] GKAOGPIIYCISHV-UHFFFAOYSA-N 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- 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
- F25J2200/00—Processes or apparatus using separation by rectification
- F25J2200/90—Details relating to column internals, e.g. structured packing, gas or liquid distribution
- F25J2200/94—Details relating to the withdrawal point
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- 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
- F25J2215/00—Processes characterised by the type or other details of the product stream
- F25J2215/42—Nitrogen or special cases, e.g. multiple or low purity N2
- F25J2215/44—Ultra high purity nitrogen, i.e. generally less than 1 ppb impurities
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- 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
- F25J2220/00—Processes or apparatus involving steps for the removal of impurities
- F25J2220/42—Separating low boiling, i.e. more volatile components from nitrogen, e.g. He, H2, Ne
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Separation By Low-Temperature Treatments (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
め要約のデータは記録されません。
Description
[0001)
本発明は、水素、ヘリウム、ネオン等の低沸点成分の含
有量が少ない高純度窒素を採取する空気液化分離方法及
び装置に関するものである。 [00021 【従来の技術] 従来より、工業的に窒素を製造する方法、装置として、
空気を原料としてこれを液化し、その組成分をその沸点
差によって精留分離するいわゆる空気液化分離方法が採
用されているが、これを図2の複式精留塔を用いた装置
で説明する。 (0003]
有量が少ない高純度窒素を採取する空気液化分離方法及
び装置に関するものである。 [00021 【従来の技術] 従来より、工業的に窒素を製造する方法、装置として、
空気を原料としてこれを液化し、その組成分をその沸点
差によって精留分離するいわゆる空気液化分離方法が採
用されているが、これを図2の複式精留塔を用いた装置
で説明する。 (0003]
Claims (4)
- 【請求項1】高純度窒素を採取する空気液化分離方法に
おいて、複式精留塔の上部塔頂部より水素等の低沸点成
分の含有量の多い窒素ガスを導出すると共に、該上部塔
頂部より数段下の精留段より水素等の低沸点成分の含有
量の少ない高純度の窒素ガスまたは液化窒素を導出する
ことを特徴とする空気液化分離方法。 - 【請求項2】原料空気を液化し、複式精留塔により精留
分離して高純度窒素を採取する空気液化分離装置におい
て、前記複式精留塔の上部塔頂部より水素等の低沸点成
分の含有量の多い窒素ガスを導出する経路と、該上部塔
頂部より数段下の精留段より水素等の低沸点成分の含有
量の少ない高純度の窒素ガスまたは液化窒素を導出する
経路を設けたことを特徴とする空気液化分離装置。 - 【請求項3】前記複式精留塔は、精留段が数段多く設け
られていることを特徴とする請求項2記載の空気液化分
離装置。 - 【請求項4】前記水素等の低沸点成分の含有量の多い窒
素ガスを導出する経路は、その量を調節しつつ導出する
手段を備えていることを特徴とする請求項2記載の空気
液化分離装置。
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP279691A JPH0615947B2 (ja) | 1991-01-14 | 1991-01-14 | 空気液化分離方法及び装置 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP279691A JPH0615947B2 (ja) | 1991-01-14 | 1991-01-14 | 空気液化分離方法及び装置 |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP25179983A Division JPS60142183A (ja) | 1983-12-28 | 1983-12-28 | 空気液化分離方法及び装置 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03271685A true JPH03271685A (ja) | 1991-12-03 |
JPH0615947B2 JPH0615947B2 (ja) | 1994-03-02 |
Family
ID=11539336
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP279691A Expired - Fee Related JPH0615947B2 (ja) | 1991-01-14 | 1991-01-14 | 空気液化分離方法及び装置 |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0615947B2 (ja) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103055529A (zh) * | 2012-12-27 | 2013-04-24 | 淄博特普化工技术有限公司 | 带有塔内压力调节装置的减压间歇精馏塔及其使用方法 |
CN104034123A (zh) * | 2014-06-27 | 2014-09-10 | 莱芜钢铁集团有限公司 | 一种空气分离装置积液调纯一体化作业方法 |
CN109595877A (zh) * | 2018-11-29 | 2019-04-09 | 杭州杭氧股份有限公司 | 一种适用于抽压氮空分的粗氖氦提取装置及其提取方法 |
-
1991
- 1991-01-14 JP JP279691A patent/JPH0615947B2/ja not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103055529A (zh) * | 2012-12-27 | 2013-04-24 | 淄博特普化工技术有限公司 | 带有塔内压力调节装置的减压间歇精馏塔及其使用方法 |
CN104034123A (zh) * | 2014-06-27 | 2014-09-10 | 莱芜钢铁集团有限公司 | 一种空气分离装置积液调纯一体化作业方法 |
CN109595877A (zh) * | 2018-11-29 | 2019-04-09 | 杭州杭氧股份有限公司 | 一种适用于抽压氮空分的粗氖氦提取装置及其提取方法 |
CN109595877B (zh) * | 2018-11-29 | 2020-12-01 | 杭州制氧机集团股份有限公司 | 一种适用于抽压氮空分的粗氖氦提取装置及其提取方法 |
Also Published As
Publication number | Publication date |
---|---|
JPH0615947B2 (ja) | 1994-03-02 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
EXPY | Cancellation because of completion of term |