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US4753016A Expired / Lapsed US ⏱️ 0.0 years remaining

Condensation process and apparatus for water vapor that is under a vacuum

Assignee: Individual
•
Filing: 1987-04-08
•
Granted: 1988-06-28
•
Expires: 2007-04-08
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Abstract

Abstract A condensation process and apparatus for water vapor under vacuum which is taken preferably from a drying apparatus. The vacuum is produced by a water ring vacuum pump through which water flows, and the water vapor in the liquid ring vacuum pump is condensed into the liquid. The water is carried in a water circuit with at least one heat exchanger yielding heat from the water for heating purposes. Before flowing into the water ring vacuum pump, the water carried in the circuit is passed through a heat exchanger transferring waste heat from the pump and the pump drive to the water. Heat losses are prevented by a casing of thermal insulation surrounding the pump as well as the heat exchanger.

Inventors

  • 👤 Heinz Eichholz

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-07 13:54
CPC Classifications
F; F26; F26B; F26B23/00; F26B23/001; F26B23/002; F26B17/00; F26B17/18; F26B5/00; F26B5/04; F26B5/041; Y; Y02; Y02P; Y02P70/00; Y02P70/10

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 149 words
In a condensation process for water vapor that is under a vacuum and which is preferentially taken from a drying apparatus, the vacuum being produced by a liquid ring vacuum pump through which a liquid flows, and the vapor being condensed in the liquid ring vacuum pump into the liquid flowing through the latter, the improvement wherein water is used as the liquid flowing through the liquid ring vacuum pump; wherein the water is carried in a water circuit with at least one heat exchanger yielding heat from the water for heating purposes; wherein the water carried in the circuit, before flowing into the water ring vacuum pump, is passed through a heat exchanger transferring to the water waste heat from the pump and pump drive; and wherein heat losses are prevented by a thermal insulation casing surrounding the pump and its drive as well as the heat exchanger.
Claim 2
Dependent Claim 149 words
In a condensation process for water vapor that is under a vacuum and which is preferentially taken from a drying apparatus, the vacuum being produced by a liquid ring vacuum pump through which a liquid flows, and the vapor being condensed in the liquid ring vacuum pump into the liquid flowing through the latter, the improvement wherein water is used as the liquid flowing through the liquid ring vacuum pump; wherein the water is carried in a water circuit with at least one heat exchanger yielding heat from the water for heating purposes; wherein the water carried in the circuit, before flowing into the water ring vacuum pump, is passed through a heat exchanger transferring to the water waste heat from the pump and pump drive; and wherein heat losses are prevented by a thermal insulation casing surrounding the pump and its drive as well as the heat exchanger.
Claim 3
Dependent Claim 24 words
The condensation process according to claim 1, wherein the liquid ring vacuum pump is operated as a forepump preceded by a separate vacuum pump.
Claim 4
Dependent Claim 18 words
The condensation process according to claim 2, wherein the separate vacuum pump is a rotary valve vacuum pump.
Claim 5
Dependent Claim 18 words
The condensation process according to claim 2, wherein the separate vacuum pump is a gas ring vacuum pump.
Claim 6
Dependent Claim 24 words
The condensation process according to claim 1, wherein the water vapor is taken as waste vapor from an apparatus for vacuum drying of materials.
Claim 7
Dependent Claim 27 words
The condensation process according to claim 1, wherein the heat-yielding heat exchanger is part of the vacuum drying apparatus and yields heat to the material being dried.
Claim 8
Dependent Claim 63 words
The condensation process according to claim 1, wherein the vapor is produced by spraying water tapped for the water circuit of the liquid ring vacuum pump in a closed vacuum spray chamber and wherein at least one of the water before spraying and the vapor produced by the spraying are carried through an absorber for the absorption of ambient heat and waste heat.
Claim 9
Dependent Claim 161 words
In apparatus for the performance of the process recited in claim 1, comprising (a) a liquid ring vacuum pump with a water vapor feed line connected to the intake side; (b) a feed line feeding liquid to the liquid ring vacuum pump; and (c) a discharge line discharging the liquid from the liquid ring vacuum pump; the improvement wherein water is used as the liquid flowing through the liquid feed line, the liquid ring vacuum pump and the liquid discharge line; and wherein the apparatus further comprises (1) at least one heat exchanger connected between the water discharge line and the water feed line and yielding heat from the water carried in the circuit for heating purposes; (2) a heat exchanger transferring waste heat from the pump and pump drive to the water, which is inserted into the water feed line ahead of the pump; and (3) a thermally insulated housing surrounding the pump with its drive and having pipe lead-throughs.
Claim 10
Dependent Claim 20 words
The apparatus according to claim 8, further comprising a separate vacuum pump connected ahead of the liquid ring vacuum pump.
Claim 11
Dependent Claim 17 words
The apparatus according to claim 9, wherein the separate vacuum pump is a rotary valve vacuum pump.
Claim 12
Dependent Claim 17 words
The apparatus according to claim 9, wherein the separate, vacuum pump is a gas ring vacuum pump.
Claim 13
Dependent Claim 20 words
The apparatus according to claim 8, further comprising a preheating and booster heating device disposed in the water discharge line.
Claim 14
Dependent Claim 44 words
The apparatus according to claim 8, wherein the thermal insulating casing additionally encloses a vacuum drying apparatus that feeds water vapor to the vacuum pump through the water vapor feed line, and in which goods to be dried are heated by the heat exchanger.

References Cited (Backward Citations)

US2021012A Cited
US2478889A Cited
US3392455A Cited
US3605273A Cited
US4276701A Cited
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US4331085A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1991-06-28 1991-12-28 1992-06-28 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1995-06-28 1995-12-28 1996-06-28 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1999-06-28 1999-12-28 2000-06-28 $7700.00 Window Closed / Lapsed

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