AR011356A1 - Procedimiento de separacion de acetileno en fraccionamiento criogenico de aire - Google Patents
Procedimiento de separacion de acetileno en fraccionamiento criogenico de aireInfo
- Publication number
- AR011356A1 AR011356A1 ARP980100021A ARP980100021A AR011356A1 AR 011356 A1 AR011356 A1 AR 011356A1 AR P980100021 A ARP980100021 A AR P980100021A AR P980100021 A ARP980100021 A AR P980100021A AR 011356 A1 AR011356 A1 AR 011356A1
- Authority
- AR
- Argentina
- Prior art keywords
- acetylene
- cryogenic air
- separation procedure
- air fractionation
- heat exchanger
- Prior art date
Links
- HSFWRNGVRCDJHI-UHFFFAOYSA-N Acetylene Chemical compound C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 title abstract 4
- 238000005194 fractionation Methods 0.000 title abstract 2
- 238000000034 method Methods 0.000 title abstract 2
- 238000000926 separation method Methods 0.000 title 1
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 abstract 2
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 abstract 2
- 229910002092 carbon dioxide Inorganic materials 0.000 abstract 1
- 239000001569 carbon dioxide Substances 0.000 abstract 1
- 238000004821 distillation Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
Classifications
-
- 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
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8668—Removing organic compounds not provided for in B01D53/8603 - B01D53/8665
-
- 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
- B01D53/002—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 condensation
-
- 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
- F25J3/04151—Purification and (pre-)cooling of the feed air; recuperative heat-exchange with product streams
- F25J3/04163—Hot end purification of the feed air
-
- 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
- F25J3/04248—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion
- F25J3/04284—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched (waste-)streams
- F25J3/0429—Generation of cold for compensating heat leaks or liquid production, e.g. by Joule-Thompson expansion using internal refrigeration by open-loop gas work expansion, e.g. of intermediate or oxygen enriched (waste-)streams of feed air, e.g. used as waste or product air or expanded into an auxiliary column
- F25J3/04303—Lachmann expansion, i.e. expanded into oxygen producing or low 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
- 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
- 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
- F25J3/04763—Start-up or control of the process; Details of the apparatus used
- F25J3/04769—Operation, control and regulation of the process; Instrumentation within the process
- F25J3/04854—Safety aspects of operation
-
- 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
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/24—Processes or apparatus using other separation and/or other processing means using regenerators, cold accumulators or reversible heat exchangers
-
- 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
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/82—Processes or apparatus using other separation and/or other processing means using a reactor with combustion or catalytic reaction
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- General Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Health & Medical Sciences (AREA)
- Biomedical Technology (AREA)
- Separation By Low-Temperature Treatments (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
Un procedimiento para separar acetileno en el fraccionamiento de aire a baja temperatura. Para dicha finalidad se comprime en primer término el aire,se enfría al menos en un intercambiador conmutable de calor y se fracciona a continuacion ena l menos una columna de destilacion. Se oxida el acetileno porvía catalítica a una temperatura comprendida entre 70 y 130°C, preferentemente entre 80 y 110°C, antes que el aire entre al intercambiador de calor. Agua ydioxido de carbono se separandel aire por el contrario sustancialmente en el intercambiador de calor.
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19700644A DE19700644A1 (de) | 1997-01-10 | 1997-01-10 | Entfernung von Acetylen bei der Luftzerlegung |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| AR011356A1 true AR011356A1 (es) | 2000-08-16 |
Family
ID=7817115
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| ARP980100021A AR011356A1 (es) | 1997-01-10 | 1998-01-02 | Procedimiento de separacion de acetileno en fraccionamiento criogenico de aire |
Country Status (11)
| Country | Link |
|---|---|
| EP (1) | EP0852964A1 (es) |
| JP (1) | JPH10202060A (es) |
| KR (1) | KR19980070370A (es) |
| AR (1) | AR011356A1 (es) |
| AU (1) | AU728970B2 (es) |
| BR (1) | BR9800276A (es) |
| CA (1) | CA2226592A1 (es) |
| DE (1) | DE19700644A1 (es) |
| NO (1) | NO980101L (es) |
| TW (1) | TW357255B (es) |
| ZA (1) | ZA98156B (es) |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| TWI363655B (en) | 2004-03-30 | 2012-05-11 | Taiyo Nippon Sanso Corp | Pre-processing refining device of air liquefying/separating apparatus, hydrocarbon absorption agent, and pre-processing method of air material |
| DE102006058082A1 (de) * | 2006-12-07 | 2008-06-12 | Beko Technologies Gmbh | Reinigungsanlage für Gase |
| RU2419481C2 (ru) * | 2008-07-02 | 2011-05-27 | Михаил Юрьевич Савинов | Способ получения криптоно-ксеноновой смеси и устройство для его осуществления |
| JP6580848B2 (ja) * | 2015-03-30 | 2019-09-25 | 積水化学工業株式会社 | ガス浄化方法及び装置、並びに有価物生成方法及び装置 |
| JP6841878B2 (ja) * | 2019-08-29 | 2021-03-10 | 積水化学工業株式会社 | ガス浄化方法及び装置、並びに有価物生成方法及び装置 |
| CN113786830B (zh) * | 2021-08-24 | 2023-08-15 | 万华化学(四川)有限公司 | 一种治理乙炔装置碳黑水解吸含炔烃废气的催化剂制备方法及应用 |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US295439A (en) * | 1884-03-18 | Mail-bag | ||
| US1836927A (en) * | 1929-12-04 | 1931-12-15 | Ig Farbenindustrie Ag | Removal of acetylene from gases |
| NL178757B (nl) * | 1952-06-02 | British Steel Corp | Werkwijze en inrichting voor het continu produceren van een metaalstrook uit metaalpoeder. | |
| FR1398874A (fr) * | 1964-04-02 | 1965-05-14 | Azote & Prod Chim | Perfectionnements aux procédés d'épuration catalytique des gaz de fours à coke |
| DE2014655A1 (en) * | 1969-05-23 | 1970-11-26 | VEB Leuna-Werke Walter Ulbricht, χ 4220 Leuna | Removal of acetylene impurities from air - by palladium catalysed hydrogenation |
| GB1471496A (en) * | 1974-04-26 | 1977-04-27 | Le Tek I Kholodilnoi Promy | Process for low-temperature separation of air |
| DE3322473A1 (de) * | 1983-06-22 | 1985-01-03 | Linde Ag, 6200 Wiesbaden | Verfahren und vorrichtung zur vermeidung einer anreicherung unerwuenschter komponenten in einem fluessigen medium |
| JPS61190277A (ja) * | 1985-02-16 | 1986-08-23 | 大同酸素株式会社 | 高純度窒素および酸素ガス製造装置 |
-
1997
- 1997-01-10 DE DE19700644A patent/DE19700644A1/de not_active Withdrawn
- 1997-05-22 EP EP97108305A patent/EP0852964A1/de not_active Withdrawn
-
1998
- 1998-01-02 AR ARP980100021A patent/AR011356A1/es not_active Application Discontinuation
- 1998-01-07 KR KR1019980000166A patent/KR19980070370A/ko not_active Withdrawn
- 1998-01-07 JP JP10011985A patent/JPH10202060A/ja active Pending
- 1998-01-09 TW TW087100229A patent/TW357255B/zh active
- 1998-01-09 ZA ZA98156A patent/ZA98156B/xx unknown
- 1998-01-09 NO NO980101A patent/NO980101L/no not_active Application Discontinuation
- 1998-01-09 AU AU50403/98A patent/AU728970B2/en not_active Ceased
- 1998-01-12 BR BR9800276-7A patent/BR9800276A/pt unknown
- 1998-01-12 CA CA002226592A patent/CA2226592A1/en not_active Abandoned
Also Published As
| Publication number | Publication date |
|---|---|
| NO980101D0 (no) | 1998-01-09 |
| TW357255B (en) | 1999-05-01 |
| BR9800276A (pt) | 2001-03-20 |
| ZA98156B (en) | 1998-07-09 |
| AU5040398A (en) | 1998-07-16 |
| KR19980070370A (ko) | 1998-10-26 |
| AU728970B2 (en) | 2001-01-25 |
| NO980101L (no) | 1998-07-13 |
| CA2226592A1 (en) | 1998-07-10 |
| EP0852964A1 (de) | 1998-07-15 |
| DE19700644A1 (de) | 1998-07-16 |
| JPH10202060A (ja) | 1998-08-04 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| FA | Abandonment or withdrawal |