US3543540A - Drycleaning machine with solvent recovery means - Google Patents
Drycleaning machine with solvent recovery means Download PDFInfo
- Publication number
- US3543540A US3543540A US598808A US59880866A US3543540A US 3543540 A US3543540 A US 3543540A US 598808 A US598808 A US 598808A US 59880866 A US59880866 A US 59880866A US 3543540 A US3543540 A US 3543540A
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- United States
- Prior art keywords
- cleaning
- vapor
- drum
- compressor
- pressure
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- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
- D06F43/00—Dry-cleaning apparatus or methods using volatile solvents
- D06F43/08—Associated apparatus for handling and recovering the solvents
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
- D06F43/00—Dry-cleaning apparatus or methods using volatile solvents
- D06F43/007—Dry cleaning methods
-
- D—TEXTILES; PAPER
- D06—TREATMENT OF TEXTILES OR THE LIKE; LAUNDERING; FLEXIBLE MATERIALS NOT OTHERWISE PROVIDED FOR
- D06F—LAUNDERING, DRYING, IRONING, PRESSING OR FOLDING TEXTILE ARTICLES
- D06F43/00—Dry-cleaning apparatus or methods using volatile solvents
- D06F43/02—Dry-cleaning apparatus or methods using volatile solvents having one rotary cleaning receptacle only
Definitions
- This invention relates to apparatus for cleaning fabrics, articles of apparel, furs, leather, and the like.
- Certain hydrocarbons are known to possess good cleaning properties.
- these materials have not heretofore been used for cleaning purposes, despite their relatively low cost, because the cleaning fluid vaporizes at atmospheric pressure in the range of average ambient temperature, and in a pressurized container excessive pressure is quickly built up, while in a non-pressurized container the vapor escapes into the atmosphere.
- the vapor of this type of material may come into contact with heated bodies and, upon decomposition, produce chemically active substances.
- the advantage of the invention resides in the fact that the vapor produced in the cleaning area is immediately drawn off, so that no undesirable excess pressure can be built up.
- the exhausted vapor has a temperature at atmospheric pressure on the order of the average internal temperature of the cleaning area.
- the vapor of the cleaning medium can be condensed and returned as a fluid to the cleaning area.
- the pressure of the vapor is increased in the simplest manner to such an extent and the vaporization temperature is such that,
- cleaning fluid is supplied from tanks 10 through a supply line 12, which includes a check valve 14, to a cleaning drum or vat 16.
- the tanks 10 are insulated, in accordance with temperature conditions. A cycle of operations is started when the lid of the cleaning drum is closed.
- the cleaning medium used is such that it vaporizes at atmospheric pressure in the range of average ambient temperature, that is to say that through heat transfer from without and the heat generated within the drum 16, a certain vaporization of the cleaning fluid takes place.
- This vapor is then evacu ated, in accordance with a feature of the invention, by means of a compressor 18, which is connected by an exhaust line 20 to the interior of the drum 16, preferably to the uppermost portion thereof.
- a filter 22 is provided in line 20 to prevent the admission of foreign matter to the compressor.
- a preferred cleaning medium employed in the practice of the method is selected from the group of fluorochloromethanes and ethanes known commercially under the trademark Freon, more particularly Freon 11, which is a trichloromonofluoromethane (CClgF).
- the compressor 18 compresses the evacuated cleaning medium and subjects it to pressure in a reservoir or container, herein shown in the form of a separator vessel 24. It is not generally possible to evacuate cleaning medium vapor alone fromthe drum 16. At least at the beginning, the evacuated medium consists of a mixture of vapor and air. This mixture is separated into its components in the vessel 24. The air is collected above, While the lower portion of the vessel is filled with cleaning medium vapor. Backflow is prevented by a check valve 26 in a pressure line 28 of the compressor 18.
- the compressed vapor is carried from the separator vessel 24 through a connecting pipe 30 to an air cooler 32 provided with air blowers 34.
- the compression pressure of the mixture adapts itself to the condition of the mixture.
- a partial pressure of about 29 p.s.i.a. is adequate, which corresponds to a vaporization temperature of about 113 F.
- ambient air at about 77 F. or about 86 F., the cleaning medium vapor in the cooler 32 can be readily liquefied.
- the cooler 32 is controlled by a high pressure floater valve 36, from which the cleaning fluid is conducted through an accumulator 38, a connecting line 40, and supply line 12, to the drum 16, or back to the tanks 10.
- Air present in the separator vessel 24 may be returned to the drum 16 through a return line 42, which is closed by a shutoff valve 44.
- Such air return is necessary when too high a vacuum is created in the drum, as, for example, on completion of a cleaning operation, in order to prevent too low pressure, since under such conditions the drum hatch cannot be opened.
- the cleaning fluid within the drum 16 must be regenerated from time to time or continually, to free it of impurities.
- the cleaning fluid is conducted from the drum 16 through a pipe 46 to a distiller 48.
- the distiller is heated so that the cleaning fluid is converted into vapor which is exhausted through a line 50,
- the distiller 48 may be heated electrically. This is advantageous from the standpoint of the economics of the electrical installation, provided that no unusual heating is required.
- the distiller 48 may be conveniently heated by heating means, as illustrated in the drawing, through lines 52 leading from the connecting pipe 30 between the separator vessel 24 and the cooler 32.
- a valve 54 in the line When a valve 54 in the line is closed, the compressed cleaning fluid vapor flows out of the separator vessel 24 through the distiller 48, where it gives up heat and is then carried into the cooler 32.
- a corresponding coil connected to the air return line 42, is not shown.
- the distiller 48 may be heated very eflFectively by the heat withdrawn from the warm, compressed air. Whether the distiller is heated by warm air or warm cleaning fluid vapor depends largely upon the ratio of air and cleaning fluid vapor in the mixture in the separator vessel 24.
- a pressure control device 60 which, through an electrical connection 62, automatically renders the compressor operative or inoperative when the pressure in the exhaust line 20 exceeds or falls below a predetermined value.
- the compressor 18 accordingly need not be set in operation immediately upon starting a cleaning operation. It is sutficient to open a valve 64 in the line 20 connected to the drum 16. If, during a cleaning operation, a portion of the cleaning fluid vaporizes, a pressure is built up which passes into the exhaust line 20. If the pressure increases, the pressure control device 60 becomes operative to actuate the compressor 18.
- the valve '64 is closed when no cleaning operation is taking place in the drum, particularly when the drum is entirely out of operation, as for example, when its hatch is opened.
- cleaning drum a compressor, an exhaust line connecting the cleaning drumand the compressor, a vessel, a pressure line connecting the compressor to the vessel, a cooling device, a vapor line connecting the vessel to the cooling device, means connecting the cooling device to the supply tank and to the cleaning drum, valve means in said connecting means controlling the return of the cleaning fluid to the cleaning drum or the supply tank, and pressure control means for automatically actuating the compressor when the pressure exceeds an adjustable value and for shutting off the compressor when the pressure falls below said value.
- Apparatus for cleaning wearing apparel and the like comprising at least one supply tank, a cleaning drum, a compressor, an exhaust line connecting the cleaning drum and the compressor, a vessel, a cooling device, a vapor line connecting the vessel to the cooling device, means connecting the cooling device to the supply tank and to the cleaning drum, valve means in said connecting means controlling the return of the cleaning fluid to the cleaning drum or the supply tank, and a vapor exhaust line which connects the supply tank to the exhaust line of the compressor and includes a return valve which remains open when the pressure in the supply tank exceeds a determined value until the pressure drops to said determined value and valve means for cutting ofl? communication between the cleaning drum and the exhaust line of the compressor.
- Apparatus for cleaning wearing apparel and the like comprising at least one supply tank, a cleaning drum, a compressor, an exhaust line connecting the cleaning drum and the compressor, a vessel, a pressure line connecting the compressor to the vessel, a cooling device, a vaporline connecting the vessel to the cooling device, means connecting the cooling device to the supply tank and to the cleaning drum, valve means in said connecting means controlling the return of the cleaning fluid to the cleaning drum or the supply tank, an air return line connecting the upper end of the vessel to the cleaning drum and including valve means, said vapor line connecting the vessel to the cooling device opening into the lower end of the vessel to separate air from vapor in the vessel.
Description
H. GUNTNER 3543 DRYCLEANING MACHINE WITH SOLVENT RECOVERY MEANS Dec. 1,1970
Filed Dec. 2, 19 5 United States Patent US. Cl. 68-18 4 Claims ABSTRACT OF THE DISCLOSURE An apparatus for cleaning wearing apparel and the like, in which, after starting the cleaning operation, a mixture of air and vaporized cleaning fluid is exhausted by a compressor from a tightly closed cleaning drum, compressed, and separated into its components. The vaporized cleaning fluid is then condensed and recirculated to the cleaning drum or a storage tank; the compressor being automatically actuated by pressure control means dependent upon the pressure in the cleaning drum and/or the storage tank. Air from the separating vessel can be recirculated to the cleaning drum at the end of the cleaning operation for pressure equalization. During the cleaning operation, cleaning liquid can be distilled in a distiller, vaporized and exhausted by the compressor.
This invention relates to apparatus for cleaning fabrics, articles of apparel, furs, leather, and the like.
Certain hydrocarbons, particularly those marketed under the trademark Freon, are known to possess good cleaning properties. However, these materials have not heretofore been used for cleaning purposes, despite their relatively low cost, because the cleaning fluid vaporizes at atmospheric pressure in the range of average ambient temperature, and in a pressurized container excessive pressure is quickly built up, while in a non-pressurized container the vapor escapes into the atmosphere. In addition to the fact that this causes substantial loss, there is also the danger that the vapor of this type of material may come into contact with heated bodies and, upon decomposition, produce chemically active substances.
It is an object of the invention to provide an apparatus for cleaning fabrics, Wearing apparel, furs, leathers, and the like, in which materials of the type mentioned above are employed as cleaning media.
It is a further object of the invention to provide apparatus adapted to carry into practice the method disclosed.
In the practice of the method, a cleaning medium is used which vaporizes at atmospheric pressure within a range of average ambient temperature. A mixture of air and the vapor produced by the cleaning medium is evacuated by suction from the cleaning area, compressed, and subsequently separated into its air and vapor components. The vapor, by heat exchange with cooling water or ambient air, is condensed, and the condensate is supplied to the cleaning area directly or collected in intermediate supply tanks.
The advantage of the invention resides in the fact that the vapor produced in the cleaning area is immediately drawn off, so that no undesirable excess pressure can be built up. The exhausted vapor has a temperature at atmospheric pressure on the order of the average internal temperature of the cleaning area. With the use of a cooling system, the vapor of the cleaning medium can be condensed and returned as a fluid to the cleaning area. In accordance with the invention, the pressure of the vapor is increased in the simplest manner to such an extent and the vaporization temperature is such that,
upon contact of the vapor with normal surrounding air, heat can be withdrawn from the vapor to thereby liquefy it. In this manner the use of a cooling system is rendered unnecessary.
The single figure in the drawing illustrates apparatus provided by the invention for carrying into practice the method disclosed.
Refering now to the drawing, cleaning fluid is supplied from tanks 10 through a supply line 12, which includes a check valve 14, to a cleaning drum or vat 16. The tanks 10 are insulated, in accordance with temperature conditions. A cycle of operations is started when the lid of the cleaning drum is closed.
In accordance with the invention, the cleaning medium used is such that it vaporizes at atmospheric pressure in the range of average ambient temperature, that is to say that through heat transfer from without and the heat generated within the drum 16, a certain vaporization of the cleaning fluid takes place. This vapor is then evacu ated, in accordance with a feature of the invention, by means of a compressor 18, which is connected by an exhaust line 20 to the interior of the drum 16, preferably to the uppermost portion thereof. A filter 22 is provided in line 20 to prevent the admission of foreign matter to the compressor.
A preferred cleaning medium employed in the practice of the method is selected from the group of fluorochloromethanes and ethanes known commercially under the trademark Freon, more particularly Freon 11, which is a trichloromonofluoromethane (CClgF).
The compressor 18 compresses the evacuated cleaning medium and subjects it to pressure in a reservoir or container, herein shown in the form of a separator vessel 24. It is not generally possible to evacuate cleaning medium vapor alone fromthe drum 16. At least at the beginning, the evacuated medium consists of a mixture of vapor and air. This mixture is separated into its components in the vessel 24. The air is collected above, While the lower portion of the vessel is filled with cleaning medium vapor. Backflow is prevented by a check valve 26 in a pressure line 28 of the compressor 18.
The compressed vapor is carried from the separator vessel 24 through a connecting pipe 30 to an air cooler 32 provided with air blowers 34. The compression pressure of the mixture adapts itself to the condition of the mixture. In any case, it is essential that the partial pressure of the cleaning medium vapor be such that the appropriate vaporizing temperature is sufliciently high in relation to the surrounding air. When Freon 11 is used as a cleaning medium, a partial pressure of about 29 p.s.i.a. is adequate, which corresponds to a vaporization temperature of about 113 F. With ambient air at about 77 F. or about 86 F., the cleaning medium vapor in the cooler 32 can be readily liquefied.
The cooler 32 is controlled by a high pressure floater valve 36, from which the cleaning fluid is conducted through an accumulator 38, a connecting line 40, and supply line 12, to the drum 16, or back to the tanks 10. Air present in the separator vessel 24 may be returned to the drum 16 through a return line 42, which is closed by a shutoff valve 44. Such air return is necessary when too high a vacuum is created in the drum, as, for example, on completion of a cleaning operation, in order to prevent too low pressure, since under such conditions the drum hatch cannot be opened.
The cleaning fluid within the drum 16 must be regenerated from time to time or continually, to free it of impurities. For this purpose, the cleaning fluid is conducted from the drum 16 through a pipe 46 to a distiller 48. The distiller is heated so that the cleaning fluid is converted into vapor which is exhausted through a line 50,
3 which empties in the line 20 of the compressor 18. The vapor is compressed by the compressor in the same manner as the vapor withdrawn from the drum, and is then condensed in the cooler 32 and returned to the tanks through lines 40 and 12.
The distiller 48 may be heated electrically. This is advantageous from the standpoint of the economics of the electrical installation, provided that no unusual heating is required. The distiller 48 may be conveniently heated by heating means, as illustrated in the drawing, through lines 52 leading from the connecting pipe 30 between the separator vessel 24 and the cooler 32. When a valve 54 in the line is closed, the compressed cleaning fluid vapor flows out of the separator vessel 24 through the distiller 48, where it gives up heat and is then carried into the cooler 32. To avoid complicating the drawing, a corresponding coil, connected to the air return line 42, is not shown. By means of such a coil, the distiller 48 may be heated very eflFectively by the heat withdrawn from the warm, compressed air. Whether the distiller is heated by warm air or warm cleaning fluid vapor depends largely upon the ratio of air and cleaning fluid vapor in the mixture in the separator vessel 24.
It is essential to protect the tanks 10 against the building up of undesirable high pressure as a result of the admission of heat. To this end, the tanks are connected by a vapor exhaust line 56, provided with a check valve 58, to the exhaust line 20 of the compressor 18. Vapor building up in the tanks 10 is thus exhausted by thecompressor through the lines 56 and 20.
In the exhaust line 20 there is provided a pressure control device 60 which, through an electrical connection 62, automatically renders the compressor operative or inoperative when the pressure in the exhaust line 20 exceeds or falls below a predetermined value. The compressor 18 accordingly need not be set in operation immediately upon starting a cleaning operation. It is sutficient to open a valve 64 in the line 20 connected to the drum 16. If, during a cleaning operation, a portion of the cleaning fluid vaporizes, a pressure is built up which passes into the exhaust line 20. If the pressure increases, the pressure control device 60 becomes operative to actuate the compressor 18. The valve '64 is closed when no cleaning operation is taking place in the drum, particularly when the drum is entirely out of operation, as for example, when its hatch is opened. It is important that the vapor developed in the tanks 10 should not escape through the line 56 and return valve 58 into the interior of the cleaning drum 16 but should flow into the exhaust line 20 of the compressor 18. Exen a slight pressure build-up puts the pressure control device 60 into operation to actuate the compressor 18 which, the valve 64 being closed, simply withdraws the vapor from the tanks 10.
What I claim is:
1. Apparatus for cleaning wearing apparel and the like, said apparatus comprising at least one supply tank, a
cleaning drum, a compressor, an exhaust line connecting the cleaning drumand the compressor, a vessel, a pressure line connecting the compressor to the vessel, a cooling device, a vapor line connecting the vessel to the cooling device, means connecting the cooling device to the supply tank and to the cleaning drum, valve means in said connecting means controlling the return of the cleaning fluid to the cleaning drum or the supply tank, and pressure control means for automatically actuating the compressor when the pressure exceeds an adjustable value and for shutting off the compressor when the pressure falls below said value.
2. Apparatus for cleaning wearing apparel and the like, comprising at least one supply tank, a cleaning drum, a compressor, an exhaust line connecting the cleaning drum and the compressor, a vessel, a cooling device, a vapor line connecting the vessel to the cooling device, means connecting the cooling device to the supply tank and to the cleaning drum, valve means in said connecting means controlling the return of the cleaning fluid to the cleaning drum or the supply tank, and a vapor exhaust line which connects the supply tank to the exhaust line of the compressor and includes a return valve which remains open when the pressure in the supply tank exceeds a determined value until the pressure drops to said determined value and valve means for cutting ofl? communication between the cleaning drum and the exhaust line of the compressor.
3. Apparatus for cleaning wearing apparel and the like, comprising at least one supply tank, a cleaning drum, a compressor, an exhaust line connecting the cleaning drum and the compressor, a vessel, a pressure line connecting the compressor to the vessel, a cooling device, a vaporline connecting the vessel to the cooling device, means connecting the cooling device to the supply tank and to the cleaning drum, valve means in said connecting means controlling the return of the cleaning fluid to the cleaning drum or the supply tank, an air return line connecting the upper end of the vessel to the cleaning drum and including valve means, said vapor line connecting the vessel to the cooling device opening into the lower end of the vessel to separate air from vapor in the vessel.
4. Apparatus as claimed in claim 3, further comprising a distiller, including heating means, connected via a liquid line to the cleaning drum; said liquid line having valve means and said distiller being connected via a vapor line to the exhaust line between the cleaning drum and the compressor.
References Cited UNITED STATES PATENTS 3,222,896 12/1965 Schneider 68--18 x 3,426,446 2/1969 Lotzsch 68-18 x 3,426,555 2/1969 McCutcheon 68-18 x WILLIAM I. PRICE, Primary Examiner
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE19651460403 DE1460403A1 (en) | 1965-12-03 | 1965-12-03 | Method and device for cleaning textiles |
DEG0045355 | 1965-12-03 |
Publications (1)
Publication Number | Publication Date |
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US3543540A true US3543540A (en) | 1970-12-01 |
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ID=25752157
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US598808A Expired - Lifetime US3543540A (en) | 1965-12-03 | 1966-12-02 | Drycleaning machine with solvent recovery means |
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US (1) | US3543540A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3783650A (en) * | 1969-06-02 | 1974-01-08 | Ciba Ltd | Apparatus for the processing of textiles, fibres and the like |
US3990273A (en) * | 1974-06-01 | 1976-11-09 | Hoechst Aktiengesellschaft | Apparatus for cleaning textiles, leather and furs by means of organic solvents, and for working up the solvent |
WO1997010905A1 (en) * | 1995-09-22 | 1997-03-27 | Mansur Industries Inc. | General washer apparatus |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3222896A (en) * | 1962-12-06 | 1965-12-14 | Engelhard Hanovia Inc | Dry cleaning machine |
US3426555A (en) * | 1964-06-26 | 1969-02-11 | Charles E Mccutcheon Jr | Dry cleaning |
US3426446A (en) * | 1965-08-23 | 1969-02-11 | Etma Mas Fab Gmbh | Apparatus for cooling and condensing gases |
-
1966
- 1966-12-02 US US598808A patent/US3543540A/en not_active Expired - Lifetime
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3222896A (en) * | 1962-12-06 | 1965-12-14 | Engelhard Hanovia Inc | Dry cleaning machine |
US3426555A (en) * | 1964-06-26 | 1969-02-11 | Charles E Mccutcheon Jr | Dry cleaning |
US3426446A (en) * | 1965-08-23 | 1969-02-11 | Etma Mas Fab Gmbh | Apparatus for cooling and condensing gases |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3783650A (en) * | 1969-06-02 | 1974-01-08 | Ciba Ltd | Apparatus for the processing of textiles, fibres and the like |
US3990273A (en) * | 1974-06-01 | 1976-11-09 | Hoechst Aktiengesellschaft | Apparatus for cleaning textiles, leather and furs by means of organic solvents, and for working up the solvent |
WO1997010905A1 (en) * | 1995-09-22 | 1997-03-27 | Mansur Industries Inc. | General washer apparatus |
US5669401A (en) * | 1995-09-22 | 1997-09-23 | Mansur Industries Inc. | General washer apparatus |
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