US4289586A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Solvent recovery method
Assignee: Finishing Equipment Inc
•
Filing: 1979-10-12
•
Granted: 1981-09-15
•
Expires: 1999-10-12
Abstract
Abstract A dirty or otherwise contaminated volatile solvent or other treatment fluid including relatively more volatile non-flammable and relatively less volatile flammable constituents is recovered or reclaimed by boiling it off from its impurities. As the remainder is concentrated, the evaporated vapor becomes increasingly flammable. In a work process, a treatment tank is used for chemically treating work pieces in a volatile treatment fluid which has a liquid phase and a relatively non-flammable heavier-than-air vapor phase. In this process, heat energy is added to the fluid to maintain the upper vapor phase surface at a substantial distance above the upper liquid phase surface in the tank. When the treatment fluid becomes sufficiently contaminated with dirt introduced by the work pieces or otherwise, it must be removed from the tank and replaced with clean treatment fluid. The invention involves reclaiming the used volatile treatment fluid by confining it in a closed boiling vessel and boiling it off through a conduit back into the vapor phase of the fresh fluid in an active operating treatment tank to immediately combine the increasingly flammable evaporated vapors into the relatively non-flammable treatment fluid vapor in the treatment tank where the flammable constituents of those vapors will be condensed to join the liquid phase of the fresh fluid in the treatment tank.
Inventors
- 👤 Winston E. Sabatka
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-04 08:23
CPC Classifications
C; C23; C23C; C23C22/00; C23C22/02; C23C22/03; B; B01; B01D; B01D3/00
Claims Analysis
Total Claims: 9
Claim 1
Independent Claim
159 words
A method of safely removing from a closed boiling vessel most of a first volatile fluid having at least some volatile constituents which are flammable in vapor phase from a mixture of such fluid and not so volatile constituents in said vessel including the steps of: (a) providing an open treatment tank with a second volatile, non-flammable fluid therein, said second fluid being so constituted when heated as to initially form a vapor phase that is heavier than air and which is more volatile than the vapor phase of the flammable constituents of said first fluid; (b) heating said second volatile fluid in said tank to form said second fluid into a liquid phase and a vapor phase over the liquid phase; (c) continually heating said mixture in said vessel to cause said first fluid to vaporize progressively; and (d) introducing this vapor from said first fluid continuously into the vapor phase of said second fluid in said tank.
Claim 2
Independent Claim
159 words
A method of safely removing from a closed boiling vessel most of a first volatile fluid having at least some volatile constituents which are flammable in vapor phase from a mixture of such fluid and not so volatile constituents in said vessel including the steps of: (a) providing an open treatment tank with a second volatile, non-flammable fluid therein, said second fluid being so constituted when heated as to initially form a vapor phase that is heavier than air and which is more volatile than the vapor phase of the flammable constituents of said first fluid; (b) heating said second volatile fluid in said tank to form said second fluid into a liquid phase and a vapor phase over the liquid phase; (c) continually heating said mixture in said vessel to cause said first fluid to vaporize progressively; and (d) introducing this vapor from said first fluid continuously into the vapor phase of said second fluid in said tank.
Claim 3
Independent Claim
164 words
A method of safely removing from a closed boiling vessel most of a first volatile solution including at least a first volatile fluid which is non-flammable in vapor phase and at least a second volatile fluid which is flammable in vapor phase and has a relatively higher boiling point than that of the first fluid from a mixture of said first and second fluids and not so volatile constituents in said vessel including the steps of: (a) providing an open treatment tank with a similarly constituted first volatile solution therein; (b) heating said first volatile solution in said tank to form and maintain said first fluid into a liquid phase and a relatively non-flammable vapor phase over the liquid phase; (c) continuously heating said mixture in said vessel to progressively cause the first fluid and then the second fluid of said solution to vaporize; and (d) continually introducing the vapor from said vessel into the vapor phase of said first solution in said tank.
Claim 4
Independent Claim
164 words
A method of safely removing from a closed boiling vessel most of a first volatile solution including at least a first volatile fluid which is non-flammable in vapor phase and at least a second volatile fluid which is flammable in vapor phase and has a relatively higher boiling point than that of the first fluid from a mixture of said first and second fluids and not so volatile constituents in said vessel including the steps of: (a) providing an open treatment tank with a similarly constituted first volatile solution therein; (b) heating said first volatile solution in said tank to form and maintain said first fluid into a liquid phase and a relatively non-flammable vapor phase over the liquid phase; (c) continuously heating said mixture in said vessel to progressively cause the first fluid and then the second fluid of said solution to vaporize; and (d) continually introducing the vapor from said vessel into the vapor phase of said first solution in said tank.
Claim 5
Dependent Claim
51 words
The method of claim 2 and the step of sensing the presence of the vapor phase of the first fluid above the location where the vapor from the first fluid in the vessel is to be introduced into the tank before beginning the continuous heating of said mixture in said vessel.
Claim 6
Dependent Claim
34 words
The method of claim 1 and the step of sensing the presence of the vapor phase over the liquid phase in said tank before beginning the continuous heating of said mixture in said vessel.
Claim 7
Dependent Claim
173 words
In association with a first volatile solution existing in both a liquid and a vapor phase in an open top treatment tank to perform an industrial process, said solution including a first volatile, flammable fluid and a second more volatile, non-flammable fluid; the method of processing a contaminated mixture including non-volatile impurities and a solution of the first volatile fluid and the second volatile fluid to transfer without explosion or fire danger most of the first and second fluids from the contaminated mixture into the two-phase solution in the industrial process taking place in the treatment tank, said method including the steps of: (a) encompassing the contaminated mixture in a closed boiling vessel; (b) heating the contaminated mixture in the boiling vessel to tend to drive each of the first and second fluids progressively from its liquid to its vapor phase; and (c) introducing the vapor so formed in the boiling vessel directly into the treatment tank well below the top of the vapor phase of the first volatile solution in that tank.
Claim 8
Dependent Claim
173 words
In association with a first volatile solution existing in both a liquid and a vapor phase in an open top treatment tank to perform an industrial process, said solution including a first volatile, flammable fluid and a second more volatile, non-flammable fluid; the method of processing a contaminated mixture including non-volatile impurities and a solution of the first volatile fluid and the second volatile fluid to transfer without explosion or fire danger most of the first and second fluids from the contaminated mixture into the two-phase solution in the industrial process taking place in the treatment tank, said method including the steps of: (a) encompassing the contaminated mixture in a closed boiling vessel; (b) heating the contaminated mixture in the boiling vessel to tend to drive each of the first and second fluids progressively from its liquid to its vapor phase; and (c) introducing the vapor so formed in the boiling vessel directly into the treatment tank well below the top of the vapor phase of the first volatile solution in that tank.
Claim 9
Dependent Claim
34 words
The method of claim 5 wherein the vapor from the boiling vessel is introduced into the treatment tank well above the top of the liquid phase of the first volatile solution in that tank.
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) | 1984-09-14 | 1985-03-16 | 1985-09-15 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1988-09-14 | 1989-03-16 | 1989-09-15 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1992-09-14 | 1993-03-16 | 1993-09-15 | $7700.00 | Window Closed / Lapsed |