GB235129A - Improvements in or relating to the manufacture of hydrogen by the partial liquefaction of gaseous mixtures containing the same - Google Patents
Improvements in or relating to the manufacture of hydrogen by the partial liquefaction of gaseous mixtures containing the sameInfo
- Publication number
- GB235129A GB235129A GB26286/24A GB2628624A GB235129A GB 235129 A GB235129 A GB 235129A GB 26286/24 A GB26286/24 A GB 26286/24A GB 2628624 A GB2628624 A GB 2628624A GB 235129 A GB235129 A GB 235129A
- Authority
- GB
- United Kingdom
- Prior art keywords
- column
- tubes
- liquefaction
- liquid
- pipe
- 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.)
- Expired
Links
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
- F25J3/0228—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 characterised by the separated product stream
- F25J3/0276—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 characterised by the separated product stream separation of H2/N2 mixtures, i.e. of ammonia synthesis gas
-
- 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
- F25J3/0204—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 characterised by the feed stream
- F25J3/0219—Refinery gas, cracking gas, coke oven gas, gaseous mixtures containing aliphatic unsaturated CnHm or gaseous mixtures of undefined nature
-
- 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
- F25J3/0204—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 characterised by the feed stream
- F25J3/0223—H2/CO mixtures, i.e. synthesis gas; Water gas or shifted synthesis gas
-
- 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
- F25J3/0228—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 characterised by the separated product stream
- F25J3/0261—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 characterised by the separated product stream separation of carbon monoxide
-
- 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
- F25J2210/00—Processes characterised by the type or other details of the feed stream
- F25J2210/14—Coke-ovens gas
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)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
235,129. Soc. l'Air Liquide, Soc. Anon. pour l'Etude et l'Exploitation des ProcÚdÚs G. Claude. June 3, 1924, [Convention date]. Separating gaseous mixtures by liquefaction.-In the separation of hydrogen from gaseous mixtures, such as coke oven or illuminating gas, by partial liquefaction, the liquid which contains nitrogen produced in the process is subjected in an auxiliary column to a progressive rectification or vaporization under the pressure of the liquefaction, the gas rich in nitrogen thus produced being returned to the place where the liquid is produced, and the residual liquid substantially free from nitrogen being evaporated to effect the partial liquefaction. The liquefaction column is provided with an upper nest of tubes B for the final liquefaction, and an auxiliary rectification column C is in open communication with the collector D at the bottom of this nest of tubes. The cooled compressed gas to be treated is delivered by a pipe G partly to the lower nest of tubes H in the main column and partly to the vaporizer V at the base of the column C. The liquid from the vaporizer is passed through the pipe E to the compartment I surrounding the tubes B. The liquid produced in the nest of tubes in the vaporizer V is passed through the pipe L to mix with the liquid in the main column. The unliquefied gases in these tubes are passed through a pipe Z into the collector D. The compressed gas may be admitted to the main column at a lower pressure than to the auxiliary column, by manipulation of the valve X. Specification 174,327 is referred to.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR502906X | 1924-06-03 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB235129A true GB235129A (en) | 1926-02-04 |
Family
ID=8906732
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB26286/24A Expired GB235129A (en) | 1924-06-03 | 1924-11-04 | Improvements in or relating to the manufacture of hydrogen by the partial liquefaction of gaseous mixtures containing the same |
Country Status (5)
Country | Link |
---|---|
US (1) | US1782287A (en) |
DE (1) | DE502906C (en) |
FR (1) | FR594711A (en) |
GB (1) | GB235129A (en) |
NL (1) | NL19260C (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2582068A (en) * | 1948-12-30 | 1952-01-08 | Elliott Co | Method and apparatus for separating gases |
DE944308C (en) * | 1952-01-07 | 1956-06-14 | Lurgi Ges Fuer Waermetechnik M | Process for the production of hydrogen or gases containing hydrogen |
NL207434A (en) * | 1955-06-02 | |||
US6347533B1 (en) * | 2000-03-04 | 2002-02-19 | Peter Tung | Hydraulically balanced fully thermally coupled system |
-
0
- NL NL19260D patent/NL19260C/xx active
-
1924
- 1924-06-03 FR FR594711D patent/FR594711A/en not_active Expired
- 1924-11-04 GB GB26286/24A patent/GB235129A/en not_active Expired
-
1925
- 1925-05-08 US US28940A patent/US1782287A/en not_active Expired - Lifetime
- 1925-05-30 DE DEA45113D patent/DE502906C/en not_active Expired
Also Published As
Publication number | Publication date |
---|---|
NL19260C (en) | |
DE502906C (en) | 1930-07-23 |
US1782287A (en) | 1930-11-18 |
FR594711A (en) | 1925-09-17 |
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