BR9904754A - Processo de adsorção com oscilação de pressão para extração de oxigênio de elevada pureza a partir do ar. - Google Patents
Processo de adsorção com oscilação de pressão para extração de oxigênio de elevada pureza a partir do ar.Info
- Publication number
- BR9904754A BR9904754A BR9904754-3A BR9904754A BR9904754A BR 9904754 A BR9904754 A BR 9904754A BR 9904754 A BR9904754 A BR 9904754A BR 9904754 A BR9904754 A BR 9904754A
- Authority
- BR
- Brazil
- Prior art keywords
- oxygen
- high purity
- stage
- air
- pressure oscillation
- Prior art date
Links
Classifications
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
- C01B13/02—Preparation of oxygen
- C01B13/0229—Purification or separation processes
- C01B13/0248—Physical processing only
- C01B13/0259—Physical processing only by adsorption on solids
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
- B01D53/047—Pressure swing adsorption
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/106—Silica or silicates
- B01D2253/108—Zeolites
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2256/00—Main component in the product gas stream after treatment
- B01D2256/12—Oxygen
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2256/00—Main component in the product gas stream after treatment
- B01D2256/18—Noble gases
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/10—Single element gases other than halogens
- B01D2257/102—Nitrogen
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/10—Single element gases other than halogens
- B01D2257/104—Oxygen
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/10—Single element gases other than halogens
- B01D2257/11—Noble gases
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/50—Carbon oxides
- B01D2257/504—Carbon dioxide
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/80—Water
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40003—Methods relating to valve switching
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40011—Methods relating to the process cycle in pressure or temperature swing adsorption
- B01D2259/40043—Purging
- B01D2259/4005—Nature of purge gas
- B01D2259/40052—Recycled product or process gas
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40011—Methods relating to the process cycle in pressure or temperature swing adsorption
- B01D2259/40058—Number of sequence steps, including sub-steps, per cycle
- B01D2259/40075—More than ten
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40011—Methods relating to the process cycle in pressure or temperature swing adsorption
- B01D2259/40077—Direction of flow
- B01D2259/40079—Co-current
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/40011—Methods relating to the process cycle in pressure or temperature swing adsorption
- B01D2259/40077—Direction of flow
- B01D2259/40081—Counter-current
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/402—Further details for adsorption processes and devices using two beds
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/41—Further details for adsorption processes and devices using plural beds of the same adsorbent in series
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/40—Further details for adsorption processes and devices
- B01D2259/414—Further details for adsorption processes and devices using different types of adsorbents
- B01D2259/4141—Further details for adsorption processes and devices using different types of adsorbents within a single bed
- B01D2259/4145—Further details for adsorption processes and devices using different types of adsorbents within a single bed arranged in series
- B01D2259/4146—Contiguous multilayered adsorbents
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2210/00—Purification or separation of specific gases
- C01B2210/0043—Impurity removed
- C01B2210/0046—Nitrogen
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2210/00—Purification or separation of specific gases
- C01B2210/0043—Impurity removed
- C01B2210/0051—Carbon dioxide
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2210/00—Purification or separation of specific gases
- C01B2210/0043—Impurity removed
- C01B2210/0062—Water
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02C—CAPTURE, STORAGE, SEQUESTRATION OR DISPOSAL OF GREENHOUSE GASES [GHG]
- Y02C20/00—Capture or disposal of greenhouse gases
- Y02C20/40—Capture or disposal of greenhouse gases of CO2
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/151—Reduction of greenhouse gas [GHG] emissions, e.g. CO2
Landscapes
- Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Separation Of Gases By Adsorption (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
"PROCESSO DE ADSORçãO COM OSCILAçãO DE PRESSãO PARA EXTRAçãO DE OXIGêNIO DE ELEVADA PUREZA A PARTIR DO AR". A presente invenção refere-se a um processo de PSA de dois estágios para produção de oxigênio de elevada pureza a partir de corrente de ar de alimentação. água, dióxido de carbono e nitrogênio são removidos em um primeiro estágio. Um adsorvente seletivo para oxigênio é usado para adsorver oxigênio no segundo estágio. Oxigênio produto de elevada pureza é recuperado durante regeneração do segundo estágio. De modo importante, o oxigênio produto de elevada pureza é obtido sem inclusão de uma etapa de enxague de oxigênio no ciclo de processo. O oxigênio produto de elevada pureza é obtido pela coleta do corte médio da corrente de efluente do segundo estágio durante regeneração.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US09/176,336 US6475265B1 (en) | 1998-10-22 | 1998-10-22 | Pressure swing adsorption method for production of an oxygen-enriched gas |
Publications (1)
Publication Number | Publication Date |
---|---|
BR9904754A true BR9904754A (pt) | 2000-08-29 |
Family
ID=22643951
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
BR9904754-3A BR9904754A (pt) | 1998-10-22 | 1999-10-20 | Processo de adsorção com oscilação de pressão para extração de oxigênio de elevada pureza a partir do ar. |
Country Status (7)
Country | Link |
---|---|
US (1) | US6475265B1 (pt) |
JP (1) | JP2000153124A (pt) |
KR (1) | KR20000029194A (pt) |
CN (1) | CN1252322A (pt) |
BR (1) | BR9904754A (pt) |
CA (1) | CA2287039A1 (pt) |
ID (1) | ID23451A (pt) |
Families Citing this family (51)
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JP3891773B2 (ja) * | 2000-10-20 | 2007-03-14 | 大陽日酸株式会社 | ガスの分離精製方法及びその装置 |
AU2002214858A1 (en) | 2000-10-27 | 2002-05-06 | Questair Technologies, Inc. | Systems and processes for providing hydrogen to fuel cells |
JPWO2002051523A1 (ja) * | 2000-12-26 | 2004-04-22 | 住友精化株式会社 | 目的ガスの分離方法および分離装置 |
SE523278C2 (sv) * | 2001-10-11 | 2004-04-06 | Ifoe Ceramics Ab | Förfarande och anordning för framställning av syre eller syreberikad luft |
US6736879B2 (en) * | 2002-05-01 | 2004-05-18 | Chevron Phillips Chemical Company Lp | Process to prepare low carbon disulfide containing dimethyl sulfide |
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JP4469841B2 (ja) * | 2003-05-23 | 2010-06-02 | ヨンセ ユニバーシティー | 酸素生成装置及びその制御方法 |
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CN1250322C (zh) * | 2004-06-11 | 2006-04-12 | 成都天立化工科技有限公司 | 采用三段变压吸附装置从空气中分离氮气和氧气的方法 |
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CN1287886C (zh) * | 2004-06-11 | 2006-12-06 | 成都天立化工科技有限公司 | 一种改进的两段变压吸附制富氧方法 |
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US8491704B2 (en) | 2011-01-11 | 2013-07-23 | Praxair Technology, Inc. | Six bed pressure swing adsorption process operating in normal and turndown modes |
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CN104057208A (zh) * | 2013-03-21 | 2014-09-24 | 吴宁 | 一种多功能焊机 |
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CN103953993A (zh) * | 2014-05-14 | 2014-07-30 | 烟台冰轮高压氧舱有限公司 | 一种富氧空调 |
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DE102015013561A1 (de) * | 2015-10-20 | 2017-04-20 | Linde Aktiengesellschaft | Verfahren und Anlage zur Gewinnung eines Gasprodukts |
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CN112742170B (zh) * | 2019-10-31 | 2023-04-07 | 中国石油化工股份有限公司 | 一种高含氮能源气体净化方法 |
KR102208032B1 (ko) * | 2020-06-12 | 2021-01-27 | 주식회사 오투트리 | Rvsa 방식의 고순도 산소 발생 장치 |
CN113041782B (zh) * | 2021-03-15 | 2021-12-17 | 西南化工研究设计院有限公司 | 一种气体变压吸附分离提纯系统及其分离提纯方法 |
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1998
- 1998-10-22 US US09/176,336 patent/US6475265B1/en not_active Expired - Fee Related
-
1999
- 1999-09-13 ID IDP990861D patent/ID23451A/id unknown
- 1999-10-20 BR BR9904754-3A patent/BR9904754A/pt not_active Application Discontinuation
- 1999-10-20 KR KR1019990045493A patent/KR20000029194A/ko active IP Right Grant
- 1999-10-20 CN CN99123114A patent/CN1252322A/zh active Pending
- 1999-10-20 CA CA002287039A patent/CA2287039A1/en not_active Abandoned
- 1999-10-20 JP JP11298194A patent/JP2000153124A/ja not_active Abandoned
Also Published As
Publication number | Publication date |
---|---|
JP2000153124A (ja) | 2000-06-06 |
CN1252322A (zh) | 2000-05-10 |
KR20000029194A (ko) | 2000-05-25 |
ID23451A (id) | 2000-04-27 |
CA2287039A1 (en) | 2000-04-22 |
US6475265B1 (en) | 2002-11-05 |
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