US2241600A - Means for removal of vapor from gases - Google Patents
Means for removal of vapor from gases Download PDFInfo
- Publication number
- US2241600A US2241600A US231884A US23188438A US2241600A US 2241600 A US2241600 A US 2241600A US 231884 A US231884 A US 231884A US 23188438 A US23188438 A US 23188438A US 2241600 A US2241600 A US 2241600A
- Authority
- US
- United States
- Prior art keywords
- wool
- vapor
- gases
- fragments
- removal
- 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 - Lifetime
Links
- 239000007789 gas Substances 0.000 title description 19
- 239000012634 fragment Substances 0.000 description 17
- 210000002268 wool Anatomy 0.000 description 16
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 9
- 239000001110 calcium chloride Substances 0.000 description 9
- 229910001628 calcium chloride Inorganic materials 0.000 description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 8
- 239000010425 asbestos Substances 0.000 description 7
- 150000001875 compounds Chemical class 0.000 description 7
- 229910052895 riebeckite Inorganic materials 0.000 description 7
- 150000003839 salts Chemical class 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- 239000011490 mineral wool Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 230000002745 absorbent Effects 0.000 description 3
- 239000002250 absorbent Substances 0.000 description 3
- 239000002657 fibrous material Substances 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 239000011491 glass wool Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
Images
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
- B01D53/02—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
-
- 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
- B01D53/26—Drying gases or vapours
- B01D53/261—Drying gases or vapours by adsorption
Definitions
- This invention relates generally to apparatus and methods for the treatment of gaseous mediumsl and is particularly applicable for the removal of water vapor from gases.
- Another object of the invention is to aiord apparatus or means of the above character which will readily adapt itself to repeated re-cycling operations without material deterioration.
- Fig. 1 is a side elevational view, partly in crosssection, illustrating apparatus incorporating the present invention. y
- FIG. 2 is a cross-sectional detail taken along the line 2--2 of Fig. 1.
- the apparatus illustrated in the drawing consists of a conduit I0 which can be of any convenient contour, and which is adapted to convey a stream of gas to be treated.
- a conduit I0 which can be of any convenient contour, and which is adapted to convey a stream of gas to be treated.
- one end of this conduit is shown coupled toa pipe or conduit ll,l for inflow of gas, while the other end is connected to the outflow or discharge conduit l2,
- the space Within conduitY Il! is occupied by a mass I3 of uncompacted filamentary wool.
- a wool made of non-corrodible metal can be used to advantage, as for example a ⁇ wool of stainless steel.
- glass wool made of threads or filaments of spun glass.
- fragments Interspersed throughout the mass of lamentary wool, and enmeshed within the same. are the fragments il., These fragments are made of loose fibrous material impregnated with a salt or compound having the desired absorptive properties. I prefer in this connection to make use of asbestos or mineral wool, as the fibrous structure of this material is particularly desirable for my purpose, and because mineral wool is inert to most chemicals and gases.
- the compound with which the fragments are impregnated is preferably calcium chloride.
- calcium chloride has the property of deliquescence and is capable of absorbing a relatively large amount of moisture.
- the mineral wool can be impregnated by soaking it in a. hot concenl trated solution of calcium chloride.
- the apparatus shown in the drawing iS equipped with eleci asbestos are impregnated' with calcium chloride, there is maximum surface contact with the calcium chloridewith the result that there is an eiective and eflicient absorption of water vapor.
- a relatively large amount of water may be absorbed by the calcium chloride, Without occasioning any displacement of the salt with respect -to the fragments of asbestos. This is attributed to the fact that even though sufficient water is absorbed by the calcium chloride to cause lthe salt to completely deliquesce to form a liquid. the liquid is retained by the asbestos fiber.
- the apparatus it is simply necessary to apply ⁇ heat by supplying current to the heating elements I6.
- fragments of mineral vwool carrying a vapor absorbing compound said fragments being enmeshed in a mass of uncompacted iilamentary wool, the lamentary wool having non-absorbent characteristics, being of a material which is substantially inert with respect'to chemical reaction with the compound.
- an uncompacted mass of non-absorbent wool adapted for disposition in a stream of gas to be ltreated, and fragments'of mineral wool carrying a. vapor absorbing' compound, said fragments being enmeshed in and interspersed through said mass.
- fragments of fibrous material carrying a vapor absorbing compound said fragmentsbeing enmeshed in a mass of filamentary wool and supported by said wool in spaced apart relation, said wool being uncompacted and being free oi.' coating and said fragments providing the only vapor absorbing medium in said mass.
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)
- Treating Waste Gases (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Description
May-39 @4L c. L. HUNSICKER MEANS FOR REMOVAL OF VAPOR FROM GASES INVEN'TOR C/yoe Z. #M75/crer ATTORNEY Patented May 13, 1941 PATET ris azimut MEANS FOR REMOVAL 0F VAPOR FROM GASES Clyde L. Hunsicker, San Francisco, Calif. Application September 27, 1938, Serial No. 231,884
5 Claims.
- This invention relates generally to apparatus and methods for the treatment of gaseous mediumsl and is particularly applicable for the removal of water vapor from gases.
It is an object of the invention to provide apparatus of the above character which will afford utmost effective contact between gases and a chemical absorbing medium.
More particularly it is an object of the invention to afford means for effective contact between a stream of gas and a moisture absorbing chemi` cal like calcium chloride, whereby al maximum amount of moisture can be absorbed by apparatus of a given size.
Another object of the invention is to aiord apparatus or means of the above character which will readily adapt itself to repeated re-cycling operations without material deterioration.
. Additionalobjects of the invention will appear from the following description in which the preferred embodiment of the invention has been set forth in detail in conjunction with the accompanying drawing.
Fig. 1 is a side elevational view, partly in crosssection, illustrating apparatus incorporating the present invention. y
`Fig. 2 is a cross-sectional detail taken along the line 2--2 of Fig. 1.
The apparatus illustrated in the drawing consists of a conduit I0 which can be of any convenient contour, and which is adapted to convey a stream of gas to be treated. In Fig. 1, one end of this conduit is shown coupled toa pipe or conduit ll,l for inflow of gas, while the other end is connected to the outflow or discharge conduit l2, The space Within conduitY Il! is occupied by a mass I3 of uncompacted filamentary wool. A wool made of non-corrodible metal can be used to advantage, as for example a`wool of stainless steel. Also I can employ so-called glass wool, made of threads or filaments of spun glass.
Whatever is the character of the filamentary wool employed, it should be such that gas may iiow through theiwool without undue flow resstance.
Interspersed throughout the mass of lamentary wool, and enmeshed within the same. are the fragments il., These fragments are made of loose fibrous material impregnated with a salt or compound having the desired absorptive properties. I prefer in this connection to make use of asbestos or mineral wool, as the fibrous structure of this material is particularly desirable for my purpose, and because mineral wool is inert to most chemicals and gases.
For the purpose of removing moisture from gases, the compound with which the fragments are impregnated is preferably calcium chloride. As is well known; calcium chloride has the property of deliquescence and is capable of absorbing a relatively large amount of moisture. Assuming use ofthis salt, the mineral wool can be impregnated by soaking it in a. hot concenl trated solution of calcium chloride.
After being impregnated lthefragments are enmeshed and distributed throughout the mass of iilamentary wool by applying the fragments to the surface of the wool, after which they are4 worked into the filaments. This working Vin process can be carried out manually, by repeated spreading or distorting the filaments of the wool to cause the fragments of asbestos to penetrate into the interior of the mass. It will be evident that the amount of asbestos fragments so introduced into the lam'entary wool should be insufficient to seriously block flow of gas, but should .be sumcient to afford adequate surface contactA with the stream of gas. i
To facilitate re-cycling operations, the apparatus shown in the drawing iS equipped with eleci asbestos are impregnated' with calcium chloride, there is maximum surface contact with the calcium chloridewith the result that there is an eiective and eflicient absorption of water vapor. A relatively large amount of water may be absorbed by the calcium chloride, Without occasioning any displacement of the salt with respect -to the fragments of asbestos. This is attributed to the fact that even though sufficient water is absorbed by the calcium chloride to cause lthe salt to completely deliquesce to form a liquid. the liquid is retained by the asbestos fiber. To re-genera-te the apparatus it is simply necessary to apply `heat by supplying current to the heating elements I6. vWhen heated vto an elevated temperature, water vapor '.evaporates from the calcium chloride, and the salt is again deposited as a solid upon the asbestos nbers in such form liquid to evaporate Water a hard caked mass resuits which affords a minimum of exposed surface area.
While use of calcium chloride is preferred for absorption of moisture, other chemicals can be employed, as for example potassium lhydroxide which also has the property of deliquescence.
I claim:
1. In means for the removal of vapor irom gases, fragments of fibrous material carrying a vapor absorbing compound, said fragments being enmeshed in a mass of uncompacted lamentary wool.
2. In means for the removal of vapor from gases, fragments of mineral vwool carrying a vapor absorbing compound, said fragments being enmeshed in a mass of uncompacted iilamentary wool, the lamentary wool having non-absorbent characteristics, being of a material which is substantially inert with respect'to chemical reaction with the compound.
3. In means for the removal of water from gases, fragments of brous material carrying a moisture absorbing chemical, said fragments being enmeshed in a mass of uncompacted lamentary wool having non-absorbent characteristics.
4. In means for the removal of watervapor from gases, an uncompacted mass of non-absorbent wool adapted for disposition in a stream of gas to be ltreated, and fragments'of mineral wool carrying a. vapor absorbing' compound, said fragments being enmeshed in and interspersed through said mass.
5. In means for the removal of vapor from gases, fragments of fibrous material carrying a vapor absorbing compound, said fragmentsbeing enmeshed in a mass of filamentary wool and supported by said wool in spaced apart relation, said wool being uncompacted and being free oi.' coating and said fragments providing the only vapor absorbing medium in said mass.
CLYDE L.l HUNSICKER.
Vapor
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US231884A US2241600A (en) | 1938-09-27 | 1938-09-27 | Means for removal of vapor from gases |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US231884A US2241600A (en) | 1938-09-27 | 1938-09-27 | Means for removal of vapor from gases |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US2241600A true US2241600A (en) | 1941-05-13 |
Family
ID=22870999
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US231884A Expired - Lifetime US2241600A (en) | 1938-09-27 | 1938-09-27 | Means for removal of vapor from gases |
Country Status (1)
| Country | Link |
|---|---|
| US (1) | US2241600A (en) |
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2957828A (en) * | 1956-04-04 | 1960-10-25 | Stanley J Mansfield | Desiccant for odor and moisture control |
| US3382141A (en) * | 1963-11-08 | 1968-05-07 | Mead Corp | Desiccant paper |
| US4615823A (en) * | 1985-01-31 | 1986-10-07 | Nippon Gohsei Kagaku Kogyo Kabushiki Kaisha | Desiccating agent |
| US5298231A (en) * | 1989-03-08 | 1994-03-29 | Rocky Research | Method for achieving high reaction rates in solid-gas reactor systems |
| US5441716A (en) * | 1989-03-08 | 1995-08-15 | Rocky Research | Method and apparatus for achieving high reaction rates |
| US5598721A (en) * | 1989-03-08 | 1997-02-04 | Rocky Research | Heating and air conditioning systems incorporating solid-vapor sorption reactors capable of high reaction rates |
| US5628205A (en) * | 1989-03-08 | 1997-05-13 | Rocky Research | Refrigerators/freezers incorporating solid-vapor sorption reactors capable of high reaction rates |
| US5666819A (en) * | 1989-03-08 | 1997-09-16 | Rocky Research | Rapid sorption cooling or freezing appliance |
| US6224842B1 (en) | 1999-05-04 | 2001-05-01 | Rocky Research | Heat and mass transfer apparatus and method for solid-vapor sorption systems |
| US6276166B1 (en) | 1999-07-20 | 2001-08-21 | Rocky Research | Auxiliary thermal storage heating and air conditioning system for a motor vehicle |
| US6282919B1 (en) | 1999-07-20 | 2001-09-04 | Rocky Research | Auxiliary active motor vehicle heating and air conditioning system |
| US6453576B2 (en) * | 2000-03-27 | 2002-09-24 | Clearwater, Inc. | Control of solids deposition from used desiccant solution |
| FR2831083A1 (en) * | 2001-10-19 | 2003-04-25 | Solvay | Desiccant, e.g. for dehydrating humid areas, controlling humidity in air conditioning systems and combating rising damp, comprises blend of fibers and alkali(ne earth) metal halide |
| US20220219116A1 (en) * | 2019-05-28 | 2022-07-14 | W. L. Gore & Associates, Inc. | Apparatus comprising a contaminant-resistant and non-corrosive desiccant composite with high moisture capacity |
-
1938
- 1938-09-27 US US231884A patent/US2241600A/en not_active Expired - Lifetime
Cited By (21)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2957828A (en) * | 1956-04-04 | 1960-10-25 | Stanley J Mansfield | Desiccant for odor and moisture control |
| US3382141A (en) * | 1963-11-08 | 1968-05-07 | Mead Corp | Desiccant paper |
| US4615823A (en) * | 1985-01-31 | 1986-10-07 | Nippon Gohsei Kagaku Kogyo Kabushiki Kaisha | Desiccating agent |
| US5298231A (en) * | 1989-03-08 | 1994-03-29 | Rocky Research | Method for achieving high reaction rates in solid-gas reactor systems |
| US5384101A (en) * | 1989-03-08 | 1995-01-24 | Rocky Research | Method and apparatus for achieving high reaction rates in solid-gas reactor systems |
| US5441716A (en) * | 1989-03-08 | 1995-08-15 | Rocky Research | Method and apparatus for achieving high reaction rates |
| US5598721A (en) * | 1989-03-08 | 1997-02-04 | Rocky Research | Heating and air conditioning systems incorporating solid-vapor sorption reactors capable of high reaction rates |
| US5628205A (en) * | 1989-03-08 | 1997-05-13 | Rocky Research | Refrigerators/freezers incorporating solid-vapor sorption reactors capable of high reaction rates |
| US5666819A (en) * | 1989-03-08 | 1997-09-16 | Rocky Research | Rapid sorption cooling or freezing appliance |
| US6736194B2 (en) | 1999-05-04 | 2004-05-18 | Rocky Research | Heat and mass transfer apparatus and method for solid-vapor sorption systems |
| US6224842B1 (en) | 1999-05-04 | 2001-05-01 | Rocky Research | Heat and mass transfer apparatus and method for solid-vapor sorption systems |
| US6276166B1 (en) | 1999-07-20 | 2001-08-21 | Rocky Research | Auxiliary thermal storage heating and air conditioning system for a motor vehicle |
| US6415625B1 (en) | 1999-07-20 | 2002-07-09 | Rocky Research | Auxiliary active motor vehicle heating and air conditioning system |
| US6282919B1 (en) | 1999-07-20 | 2001-09-04 | Rocky Research | Auxiliary active motor vehicle heating and air conditioning system |
| US6453576B2 (en) * | 2000-03-27 | 2002-09-24 | Clearwater, Inc. | Control of solids deposition from used desiccant solution |
| FR2831083A1 (en) * | 2001-10-19 | 2003-04-25 | Solvay | Desiccant, e.g. for dehydrating humid areas, controlling humidity in air conditioning systems and combating rising damp, comprises blend of fibers and alkali(ne earth) metal halide |
| WO2003035247A1 (en) * | 2001-10-19 | 2003-05-01 | Solvay (Société Anonyme) | Desiccant mass, method for obtaining same and use thereof |
| AU2002340570B2 (en) * | 2001-10-19 | 2008-03-06 | Solvay (Societe Anonyme) | Desiccant mass, method for obtaining same and use thereof |
| RU2348452C2 (en) * | 2001-10-19 | 2009-03-10 | Солвей (Сосьете Аноним) | Moisture absorbing material, method for its production and its application |
| US20220219116A1 (en) * | 2019-05-28 | 2022-07-14 | W. L. Gore & Associates, Inc. | Apparatus comprising a contaminant-resistant and non-corrosive desiccant composite with high moisture capacity |
| US12121852B2 (en) * | 2019-05-28 | 2024-10-22 | W. L. Gore & Associates, Inc. | Apparatus comprising a contaminant-resistant and non-corrosive desiccant composite with high moisture capacity |
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