US4210461A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Method for recovering heat in a vapor degreasing apparatus
Assignee: Boliden Kemi AB
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Filing: 1978-06-29
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Granted: 1980-07-01
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Expires: 1998-06-29
Abstract
Abstract Heat is supplied to the solvent bath of a vapor degreasing apparatus by a heat pump system to maintain the solvent bath in a constantly boiling state and generate a zone of solvent vapor above the bath. The solvent vapor is condensed on a cooling coil through which the heat-carrying medium of the heat pump system is being circulated, thereby transferring heat from the solvent vapors to the heat-carrying medium. Thereafter, the heat-carrying medium is compressed and discharged directly into the solvent bath while a portion of the condensed solvent vapors is diverted into the cooling coil.
Inventors
- 👤 Hans G. E. Moree
- 👤 Helmut Grunewald
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-01 14:05
CPC Classifications
C; C23; C23G; C23G5/00; C23G5/02; C23G5/04; B; B01; B01D; B01D3/00; B01D3/007; Y; Y02; Y02B; Y02B30/00; Y02B30/52; Y02P; Y02P70/00; Y02P70/10
Claims Analysis
Total Claims: 4
Claim 1
Independent Claim
242 words
A method of heat control in a solvent vapor degreasing apparatus, said apparatus comprising a tank containing a liquid solvent bath in the bottom thereof, and with a solvent vapor zone for degreasing objects above said liquid solvent bath, said method comprising the steps of: a. heating the bottom of said tank for heating said liquid to be continuously at the boiling point, thereby generating vapor from said liquid solvent bath; b. cooling a region defined by a cooling coil at least partially surrounding the inside of said tank at a level above said solvent vapor zone; c. recovering the vapor in a liquid form from said cooling region and returning a first portion of the recovered liquid to said liquid solvent bath and diverting a second portion of the recovered liquid into said cooling coil of a heat pump means; d. supplying heat absorbed by said cooling coil in said cooling region from said solvent vapor to a circulating heat-carrying medium of a system including said heat pump means, in which the medium is vaporized and thereafter is compressed and discharging the vaporized and compressed medium at high temperature and pressure directly into the liquid solvent bath, said heat-carrying medium including said second portion of said recovered liquid solvent; and e. supplying extra energy from outside the system including the heat pump means for operation of said system and cooling away excess heat outside the degreasing apparatus for balancing said system.
Claim 2
Independent Claim
242 words
A method of heat control in a solvent vapor degreasing apparatus, said apparatus comprising a tank containing a liquid solvent bath in the bottom thereof, and with a solvent vapor zone for degreasing objects above said liquid solvent bath, said method comprising the steps of: a. heating the bottom of said tank for heating said liquid to be continuously at the boiling point, thereby generating vapor from said liquid solvent bath; b. cooling a region defined by a cooling coil at least partially surrounding the inside of said tank at a level above said solvent vapor zone; c. recovering the vapor in a liquid form from said cooling region and returning a first portion of the recovered liquid to said liquid solvent bath and diverting a second portion of the recovered liquid into said cooling coil of a heat pump means; d. supplying heat absorbed by said cooling coil in said cooling region from said solvent vapor to a circulating heat-carrying medium of a system including said heat pump means, in which the medium is vaporized and thereafter is compressed and discharging the vaporized and compressed medium at high temperature and pressure directly into the liquid solvent bath, said heat-carrying medium including said second portion of said recovered liquid solvent; and e. supplying extra energy from outside the system including the heat pump means for operation of said system and cooling away excess heat outside the degreasing apparatus for balancing said system.
Claim 3
Dependent Claim
59 words
A method according to claim 1, wherein step c. comprises cooling the region above the level of said solvent vapor zone by vaporizing said solvent heat-carrying medium on the suction side of said heat pump means and step a. comprises heating the bottom of said tank by condensing the solvent heat-carrying medium on the output side of said pump.
Claim 4
Dependent Claim
40 words
A method according to claim 1 or 2 including the added step of selecting the solvent from one or more low-boiling solvents taken from the class consisting of methyldichloride, or other alkylated fluoric hydrocarbons and/or other mixtures of such solvents.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1983-07-01 | 1983-12-31 | 1984-07-01 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1987-07-01 | 1987-12-31 | 1988-07-01 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1991-07-01 | 1991-12-31 | 1992-07-01 | $7700.00 | Window Closed / Lapsed |