GB402479A - Improvements in or relating to the adsorption of gases or vapors - Google Patents

Improvements in or relating to the adsorption of gases or vapors

Info

Publication number
GB402479A
GB402479A GB16111/32A GB1611132A GB402479A GB 402479 A GB402479 A GB 402479A GB 16111/32 A GB16111/32 A GB 16111/32A GB 1611132 A GB1611132 A GB 1611132A GB 402479 A GB402479 A GB 402479A
Authority
GB
United Kingdom
Prior art keywords
air
adsorbent
pipe
adsorber
heater
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
Application number
GB16111/32A
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Silica Gel Corp
Original Assignee
Silica Gel Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Silica Gel Corp filed Critical Silica Gel Corp
Publication of GB402479A publication Critical patent/GB402479A/en
Expired legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation 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
    • B01D53/02Separation 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

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Analytical Chemistry (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Drying Of Gases (AREA)
  • Separation Of Gases By Adsorption (AREA)

Abstract

<PICT:0402479/III/1> Condensible gases or vapours are removed from gaseous mixtures by passing them successively into contact with two batches of adsorbent such as silica gel, conditioning the mixture to activate one batch and charge the other with the condensible components, removing any condensible gases in passing between the batches, and periodically reversing the position of the batches in the circuit. According to the arrangement shown, the gas mixture, for example moist compressed air, enters by pipe 15 and is heated by the steam heater 17, its relative humidity being lowered. It is then passed by suitable valves through the adsorber 10 which contains partially saturated absorbent from a prior operation. The heated air takes up the mixture in the absorbent until it is saturated, thus activating the adsorbent. The air is then passed via the pipe 22 through the cooling jacket 31 where it is cooled sufficiently to cause the moisture to condense. The condensed moisture is removed by the trap 25 and the air is then passed via pipe 27 to the adsorber 11 containing adsorbent activated in a previous operation, so that final traces of moisture are removed, and dry air is discharged through pipe 41. When the adsorbent in adsorber 11 is saturated, the position of the adsorbers in the cycle of operations is reversed by suitable valve means. The activated adsorbent, e.g. in adsorber 10 in the above example, may be cooled after activation by shutting off steam in the heater 17 or bye-passing the heater by means of pipe 36. This elimination of heating may be performed at the latter end of the activating cycle. More than two adsorbers may be used, and the spare adsorbers may be cooled by radiation or a cooling fluid, or they may be placed in the stream of effluent dried air, which may be previously cooled. The process may be applied to the dehydration of compressed air, atmospheric air or other gases, and the recovery of volatile solvents. Where the gas mixtures are at an elevated temperature, the heater 17 may be reduced in size or omitted.
GB16111/32A 1931-06-08 1932-06-07 Improvements in or relating to the adsorption of gases or vapors Expired GB402479A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US402479XA 1931-06-08 1931-06-08

Publications (1)

Publication Number Publication Date
GB402479A true GB402479A (en) 1933-12-07

Family

ID=21909951

Family Applications (1)

Application Number Title Priority Date Filing Date
GB16111/32A Expired GB402479A (en) 1931-06-08 1932-06-07 Improvements in or relating to the adsorption of gases or vapors

Country Status (1)

Country Link
GB (1) GB402479A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE9201713U1 (en) * 1992-02-12 1992-06-17 Hankison GmbH, 4130 Moers Dryer combination of refrigeration and heat-regenerated adsorption dryer for economical treatment of compressed air at low dew points

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE9201713U1 (en) * 1992-02-12 1992-06-17 Hankison GmbH, 4130 Moers Dryer combination of refrigeration and heat-regenerated adsorption dryer for economical treatment of compressed air at low dew points

Similar Documents

Publication Publication Date Title
US3534529A (en) Process for recovering organic vapors from airstream
ES466109A1 (en) Process and plant for the recovery of water from humid air
ES398297A1 (en) Process and apparatus for the adsorptive purification of gases
DE3575524D1 (en) METHOD AND PLANT FOR CLEANING WORKPIECES BY MEANS OF A LIQUID SOLVENT.
GB1447266A (en) Method of and apparatus for removing a vapour component from a gas stream
Matsumura et al. The effects of hydrophilic structures of active carbon on the adsorption of benzene and methanol vapors
US2017779A (en) Process for recovering carbon dioxide from a gas mixture
US1682588A (en) Production of dry gases
US2712981A (en) Gas generator and process for producing dry gas
GB402479A (en) Improvements in or relating to the adsorption of gases or vapors
ES321957A1 (en) A procedure for the elimination of acid gases of gaseous mixtures. (Machine-translation by Google Translate, not legally binding)
US1959389A (en) Adsorption system
CN212468136U (en) Online activation device for adsorption material
CN209093024U (en) Absorption for handling methylene chloride tail gas activates device
GB2020566A (en) Treatment of gas streams to remove condensible vapours
NO842650L (en) PROCEDURE FOR RECOVERY OF SOLVENTS IN TEXTILE TREATMENT
CN111482164A (en) Online adsorption material activation device and method
GB713612A (en) Process and apparatus for the recovery of solvents on long webs
KR930701219A (en) Use of crystalline molecular sieves containing charged octahedral sites in a cyclic drying method
GB644371A (en) Recovery of nitrogen dioxide and the production thereof
GB398010A (en) Process and arrangement for the recovery of gases or vapours by means of solid adsorbent substances with recovery of heat units
JPS54114859A (en) Air dehumidifying method for ozone generator
SU931215A1 (en) Solvent recuperation method
JPH01130717A (en) Method for dehumidifying compressed air
SU1690826A1 (en) Installation for adsorptive desiccation of gases