EP0231014A1 - Procedure and means for vaporizing freon - Google Patents
Procedure and means for vaporizing freon Download PDFInfo
- Publication number
- EP0231014A1 EP0231014A1 EP87101093A EP87101093A EP0231014A1 EP 0231014 A1 EP0231014 A1 EP 0231014A1 EP 87101093 A EP87101093 A EP 87101093A EP 87101093 A EP87101093 A EP 87101093A EP 0231014 A1 EP0231014 A1 EP 0231014A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- freon
- boiler
- oil
- vaporizing
- close
- 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.)
- Withdrawn
Links
- 230000008016 vaporization Effects 0.000 title claims abstract description 30
- 238000000034 method Methods 0.000 title claims abstract description 23
- 239000007788 liquid Substances 0.000 claims abstract description 17
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 8
- 238000001704 evaporation Methods 0.000 claims abstract description 7
- 239000000126 substance Substances 0.000 claims abstract description 6
- 239000012530 fluid Substances 0.000 claims abstract description 5
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 4
- 238000010438 heat treatment Methods 0.000 claims description 5
- 230000000630 rising effect Effects 0.000 claims description 2
- 230000001174 ascending effect Effects 0.000 abstract 1
- VOPWNXZWBYDODV-UHFFFAOYSA-N Chlorodifluoromethane Chemical compound FC(F)Cl VOPWNXZWBYDODV-UHFFFAOYSA-N 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
- F22B1/16—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being hot liquid or hot vapour, e.g. waste liquid, waste vapour
- F22B1/167—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being hot liquid or hot vapour, e.g. waste liquid, waste vapour using an organic fluid
Definitions
- the present invention concerns a procedure for vaporizing a substance evaporating at relatively low temperature, preferably about 60-90°C to be circulated in a process utilizing vapour pressure, such as a piston engine process, e.g. freon or ammonia, in a vaporizing boiler, into the lower part of which liquid freon is conducted, and from the upper part of which the pressurized, vaporized freon emerges, and a vaporizing boiler in which the procedure is applied.
- vapour pressure such as a piston engine process, e.g. freon or ammonia
- Such apparatus includes freon radiators, in which freon is present in an enclosed space heated from below, for instance with an electrical resistance.
- freon evaporates and, being lighter than air, rises upwards, at the same time releasing its heat and ultimately, condensing.
- the utilization of evaporated pressurized freon, as well as of other gaseous substances in various other processes in which a pressure cylinder motor is operated with the aid of vapour is equally known in prior art.
- the object of the present invention is to provide a procedure for vaporizing liquid freon or equivalent substance evaporating at relatively low temperature and pressurizing it in a vaporizing boiler, and a vaporizing boiler in which the procedure is applied.
- the procedure of the invention is characterized in that the boiler is partly filled with a fluid heavier than liquid freon, such as oil, which is heated substantially close to the surface so that the temperature of the oil close to the surface is higher than or equal to the evaporation temperature of freon, whereby the freon conducted to the lower part of the vaporizing boiler in among the oil, while rising upwards, is heated at the same time and ultimately, evaporates before leaving the boiler.
- a fluid heavier than liquid freon such as oil
- the vaporizing boiler applying the procedure of the invention is characterized in that the vaporizing boiler is partly filled with a fluid heavier than liquid freon, such as oil, and that close to the oil surface has been provided a unit heating the oil, such as an electrical resistance, which heats the oil in such manner that it is warmer close to the surface than in the lower part of the boiler.
- a fluid heavier than liquid freon such as oil
- Vaporizing liquid freon with the aid of the procedure and the vaporizing boiler of the invention is more efficient than before, and is accomplished with low energy consumption.
- Fig. 1 is presented a vaporizing boiler indicated by reference numeral 1, into which liquid freon, ammonia or another equivalent substance having evaporating temperature about 60-90°C is supplied with the aid of a pump 2 through a feed pipe 3.
- the gaseous, pressurized freon produced in the vaporizing boiler 1 is conducted out of the boiler by an outlet pipe 4 in the direction indicated by arrow 5.
- the vaporized freon has in the present embodiment example been conducted to a motor 6, which may be for instance motor operating with pressure cylinder, so that there is one or several cylinders and the movement of the pistons therein is controlled by pressurized freon in a manner known in itself in the art.
- To the rotating shaft of the motor 6 may be connected for instance an electric generator.
- the gaseous freon goes from the motor 6 by the pipe 8 to a condenser 9 where it is again converted into a liquid.
- the liquid freon is again pumped with the pump 2 into the vaporizing boiler 1, and the cycle continues in the manner already described above.
- Fig. 2 is depicted the vertical section of the vaporizing boiler 1.
- the boiler 1 contains 11, e.g. to about 3/4. Close to the surface of the oil 11, yet under its surface, has been provided a heating unit 10, for instance an electrical resistance. Instead of the electrical resistance, any other heating method may be contemplated.
- the unit 10 may e.g. be a pipe in which hot water circulates. The heating unit placed in this manner heats the oil in such a way that the temperature of the oil close to the surface is higher than that in the lower part of the vaporizing boiler.
- Oil is heavier than liquid freon; therefore, when freon is supplied with the aid of the pump 2 through the pipe 3 into the vaporizing boiler 1, the liquid freon begins to ascend. On the way up, the temperature of the oil 11 rises, whereby the freon begins to evaporate and freon bubbles 12 are formed.
- an open space 13 is arranged above the oil space, in which the pressurized, evaporated freon accumulates and whence it departs by an outlet pipe 4 to the process described above.
- freon 22 which binds a small quantity of oil which serves to lubricate the motor and other components of the apparatus while the freon is circulating in the process.
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
- Application Of Or Painting With Fluid Materials (AREA)
Abstract
A procedure for vaporizing a substance evaporating at relatively low temperature, preferably about 60-90°C, to be circulated in a process utilizing vapour pressure, such as a piston motor process, e.g. freon or ammonia in a vaporizing boiler (1), into the lower part of which liquid freon is conducted and from the upper part of which the pressurized, vaporized freon emerges. With the procedure of the invention it has been possible to improve the efficiency of the system in that the boiler (1) is partly filled with a fluid heavier than liquid freon, such as oil (11), which is heated substantially close to the surface in such manner that the temperature of the oil close to the surface is higher than or equal to the vaporizing temperature of freon, whereby the freon conducted to the lower part of the boiler in among the oil, while ascending, is heated at the same time and ultimately, evaporates before leaving the boiler.
Description
- The present invention concerns a procedure for vaporizing a substance evaporating at relatively low temperature, preferably about 60-90°C to be circulated in a process utilizing vapour pressure, such as a piston engine process, e.g. freon or ammonia, in a vaporizing boiler, into the lower part of which liquid freon is conducted, and from the upper part of which the pressurized, vaporized freon emerges, and a vaporizing boiler in which the procedure is applied.
- At present such apparatus is known in which liquid freon or equivalent is heated, whereby the freon evaporates and its pressure increases. Such apparatus includes freon radiators, in which freon is present in an enclosed space heated from below, for instance with an electrical resistance. The freon evaporates and, being lighter than air, rises upwards, at the same time releasing its heat and ultimately, condensing. The utilization of evaporated pressurized freon, as well as of other gaseous substances in various other processes in which a pressure cylinder motor is operated with the aid of vapour is equally known in prior art.
- The object of the present invention is to provide a procedure for vaporizing liquid freon or equivalent substance evaporating at relatively low temperature and pressurizing it in a vaporizing boiler, and a vaporizing boiler in which the procedure is applied. The procedure of the invention is characterized in that the boiler is partly filled with a fluid heavier than liquid freon, such as oil, which is heated substantially close to the surface so that the temperature of the oil close to the surface is higher than or equal to the evaporation temperature of freon, whereby the freon conducted to the lower part of the vaporizing boiler in among the oil, while rising upwards, is heated at the same time and ultimately, evaporates before leaving the boiler.
- The vaporizing boiler applying the procedure of the invention is characterized in that the vaporizing boiler is partly filled with a fluid heavier than liquid freon, such as oil, and that close to the oil surface has been provided a unit heating the oil, such as an electrical resistance, which heats the oil in such manner that it is warmer close to the surface than in the lower part of the boiler.
- Vaporizing liquid freon with the aid of the procedure and the vaporizing boiler of the invention is more efficient than before, and is accomplished with low energy consumption.
- The invention is described in the following more in detail, referring to the drawing attached, in which -
- Fig. 1 presents a process in which the vaporizing boiler of the invention can be applied.
- Fig. 2 presents the vaporizing boiler of the invention in vertical section.
- In Fig. 1 is presented a vaporizing boiler indicated by
reference numeral 1, into which liquid freon, ammonia or another equivalent substance having evaporating temperature about 60-90°C is supplied with the aid of apump 2 through afeed pipe 3. The gaseous, pressurized freon produced in the vaporizingboiler 1 is conducted out of the boiler by anoutlet pipe 4 in the direction indicated byarrow 5. The vaporized freon has in the present embodiment example been conducted to amotor 6, which may be for instance motor operating with pressure cylinder, so that there is one or several cylinders and the movement of the pistons therein is controlled by pressurized freon in a manner known in itself in the art. To the rotating shaft of themotor 6 may be connected for instance an electric generator. Having lost some of its pressure, the gaseous freon goes from themotor 6 by thepipe 8 to a condenser 9 where it is again converted into a liquid. The liquid freon is again pumped with thepump 2 into the vaporizingboiler 1, and the cycle continues in the manner already described above. - In Fig. 2 is depicted the vertical section of the vaporizing
boiler 1. Theboiler 1 contains 11, e.g. to about 3/4. Close to the surface of theoil 11, yet under its surface, has been provided aheating unit 10, for instance an electrical resistance. Instead of the electrical resistance, any other heating method may be contemplated. Theunit 10 may e.g. be a pipe in which hot water circulates. The heating unit placed in this manner heats the oil in such a way that the temperature of the oil close to the surface is higher than that in the lower part of the vaporizing boiler. - Oil is heavier than liquid freon; therefore, when freon is supplied with the aid of the
pump 2 through thepipe 3 into the vaporizingboiler 1, the liquid freon begins to ascend. On the way up, the temperature of theoil 11 rises, whereby the freon begins to evaporate andfreon bubbles 12 are formed. In the upper part of the vaporizingboiler 1, anopen space 13 is arranged above the oil space, in which the pressurized, evaporated freon accumulates and whence it departs by anoutlet pipe 4 to the process described above. - It is advantageous to use for freon for instance freon 22 which binds a small quantity of oil which serves to lubricate the motor and other components of the apparatus while the freon is circulating in the process.
- It is obvious to a person skilled in the art that the invention is not restricted to the above embodiment examples presented in the foregoing, and that it can be varied within the scope of the claims following below.
Claims (2)
1. A procedure for vaporizing a substance evaporating at relatively low temperature, preferably about 60-90°C, to be circulated in a process utilizing vapour pressure, such as a piston motor process, e.g. freon or ammonia, in a vaporizing boiler (1), into the lower part of which liquid freon is conducted, and from the upper part of which the pressurized, vaporized freon emerges, characterized in that the vaporizing boiler (1) is partly filled with a fluid heavier than liquid freon, such as oil (11), which is heated substantially close to its surface so that the temperature of the oil close to the surface is higher that or equal to the evaporating temperature of freon, whereby the freon conducted in the lower part of the vaporizing boiler in among the oil, while rising upwards, is heated at the same time and ultimately, evaporates before leaving the boiler.
2. A vaporizing boiler (1) in which the procedure according to claim 1 is applied and in the lower part of which has been provided a feed pipe (3) for liquid freon and in the upper part, an outlet pipe (4) for evaporated freon, characterized in that the vaporizing boiler (1) is partly filled with a fluid heavier than liquid freon, such as oil (11), and that close to the oil surface therebelow has been provided a unit (10) for heating the oil, such as an electrical resistance, to heat the oil in such manner that it is warmer close to the surface than in the lower part of the boiler.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FI860410 | 1986-01-28 | ||
| FI860410A FI72884C (en) | 1986-01-28 | 1986-01-28 | Procedure and apparatus for evaporating Freon. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| EP0231014A1 true EP0231014A1 (en) | 1987-08-05 |
Family
ID=8522051
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| EP87101093A Withdrawn EP0231014A1 (en) | 1986-01-28 | 1987-01-27 | Procedure and means for vaporizing freon |
Country Status (4)
| Country | Link |
|---|---|
| EP (1) | EP0231014A1 (en) |
| JP (1) | JPS62248901A (en) |
| FI (1) | FI72884C (en) |
| NO (1) | NO870340L (en) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE301836C (en) * | ||||
| US1807783A (en) * | 1931-06-02 | Steam generating system | ||
| DE845990C (en) * | 1951-01-06 | 1952-08-07 | Johann Patzelt | Electric steam generator |
| US3939803A (en) * | 1973-10-09 | 1976-02-24 | Institute Of Gas Technology | High temperature boiler and method |
| US4084379A (en) * | 1975-08-22 | 1978-04-18 | Schwartzman Everett H | Energy conversion system |
| US4207840A (en) * | 1978-09-14 | 1980-06-17 | Dauvergne Hector A | Oil bath boiler |
| JPS59213909A (en) * | 1983-05-20 | 1984-12-03 | Hitachi Ltd | Rankine cycle system |
-
1986
- 1986-01-28 FI FI860410A patent/FI72884C/en not_active IP Right Cessation
-
1987
- 1987-01-27 JP JP1532587A patent/JPS62248901A/en active Pending
- 1987-01-27 EP EP87101093A patent/EP0231014A1/en not_active Withdrawn
- 1987-01-27 NO NO870340A patent/NO870340L/en unknown
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE301836C (en) * | ||||
| US1807783A (en) * | 1931-06-02 | Steam generating system | ||
| DE845990C (en) * | 1951-01-06 | 1952-08-07 | Johann Patzelt | Electric steam generator |
| US3939803A (en) * | 1973-10-09 | 1976-02-24 | Institute Of Gas Technology | High temperature boiler and method |
| US4084379A (en) * | 1975-08-22 | 1978-04-18 | Schwartzman Everett H | Energy conversion system |
| US4207840A (en) * | 1978-09-14 | 1980-06-17 | Dauvergne Hector A | Oil bath boiler |
| JPS59213909A (en) * | 1983-05-20 | 1984-12-03 | Hitachi Ltd | Rankine cycle system |
Non-Patent Citations (1)
| Title |
|---|
| PATENT ABSTRACTS OF JAPAN; vol. 9, no. 84 (M-371)[1807], 13th April 1985; & JP-A-59 213 909 (HITACHI SEISAKUSHO K.K.) 03-12-1984 * |
Also Published As
| Publication number | Publication date |
|---|---|
| FI72884B (en) | 1987-04-30 |
| NO870340D0 (en) | 1987-01-27 |
| NO870340L (en) | 1987-07-29 |
| FI860410A0 (en) | 1986-01-28 |
| JPS62248901A (en) | 1987-10-29 |
| FI72884C (en) | 1987-08-10 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
| AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): AT BE CH DE ES FR GB GR IT LI LU NL SE |
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| STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN |
|
| 18D | Application deemed to be withdrawn |
Effective date: 19880206 |
|
| RIN1 | Information on inventor provided before grant (corrected) |
Inventor name: EKMAN, HEINZ |