WO1993016340A1 - Dispositif et procede visant a ameliorer le coefficient de rendement de systemes frigorifiques - Google Patents
Dispositif et procede visant a ameliorer le coefficient de rendement de systemes frigorifiques Download PDFInfo
- Publication number
- WO1993016340A1 WO1993016340A1 PCT/DE1992/000342 DE9200342W WO9316340A1 WO 1993016340 A1 WO1993016340 A1 WO 1993016340A1 DE 9200342 W DE9200342 W DE 9200342W WO 9316340 A1 WO9316340 A1 WO 9316340A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- pump
- expansion valve
- condenser
- refrigerant
- compressor
- Prior art date
Links
- 238000000034 method Methods 0.000 title abstract description 9
- 239000003507 refrigerant Substances 0.000 claims description 18
- 239000007788 liquid Substances 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract 1
- 238000001816 cooling Methods 0.000 description 9
- 238000010586 diagram Methods 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 230000008020 evaporation Effects 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- VOPWNXZWBYDODV-UHFFFAOYSA-N Chlorodifluoromethane Chemical compound FC(F)Cl VOPWNXZWBYDODV-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 238000004804 winding Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B41/00—Fluid-circulation arrangements
Definitions
- the common refrigerant cycle is maintained by the
- Time period of the condenser is too large.
- the systems of conventional design have a relatively low overall efficiency with a relatively high power consumption.
- the invention specified in claim 1 is based on the problem of maintaining the refrigerant circuit, particularly in the cold winter months, and to achieve an increase in the overall efficiency of the system while reducing the power consumption.
- a modification of the cycle is achieved by installing a refrigerant pump.
- a Hermetic pump can be installed after your liquid collector. This pump must be arranged in such a way that it is always supplied with sufficient refrigerant. After the refrigerant pump on the pressure side is a Q-max orifice, which must be installed and calculated in such a way that overloading of the stator winding is avoided.
- Refrigerant mass flow is moved in gaseous form via the suction line to the compressor.
- the compressor compresses the refrigerant gas to a fairly low pressure level, which means that very little compression work is required.
- the pressure line goes to the condenser, the condenser, which is always too large in the winter months, is now fully usable. Accordingly, performance figures from 7.0.9 can even be driven up to performance figure 10. This means that with 1 KW of power supplied in the compressor, we transport up to 10 KW of cooling power via the evaporator.
- the refrigerant from the condenser returns to the liquid collector with a very strong subcooling. This has the consequence that - seen from the circular process - quite high enthalpy differences arise.
- Performance figure improvements can be achieved that are between 5 and 6 in the climate range, which was previously not considered possible.
- the main use of the invention is that the above problems can be solved in all process and air conditioning systems.
- a refrigerant pump was used in a customer's system in order to ensure a sufficient refrigerant mass flow through the system with a lower pressure on the condenser side.
- a Bock motor compressor type DAM 5 / 724-4, refrigerant R22 was used.
- the system mentioned above is a system with 2 compressors.
- the built-in refrigerant pump has an absorption capacity of 2 KW.
- the actual state of the system was evaporation temperature: - 10 ° C; the condensation temperature was at 53 ° C; the
- the evaporation temperature was + - 0 C; the condensing temperature at 32 ° C; the net cooling capacity at 83 KW; at lower power consumption of the compressor.
- the supply of mechanical energy can be done by the usual methods such as Electric motor or turbocharger.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Structures Of Non-Positive Displacement Pumps (AREA)
Abstract
Dans les systèmes frigorifiques habituels, il survient fréquemment des pannes, notamment pendant les mois d'hiver, car à cette période le condenseur est surdimensionné. Le rendement global des installations demeure de ce fait dans des limites relativement basses. Afin de pallier ce problème technique, de l'énergie mécanique a été introduite dans le circuit à l'aide d'une pompe, entre le collecteur de liquide et la soupape de détente. Afin de protéger la source d'énergie, on y a monté un régulateur-maxi, ainsi qu'un régulateur-mini. L'énergie mécanique peut également être introduite autrement que par une pompe, en appliquant par exemple le principe du turbocompresseur. Ce procédé et le dispositif correspondant peuvent être utilisés pour tous les groupes à pistons à eau froide ainsi que les installations de traitement par le froid.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE19924203983 DE4203983A1 (de) | 1992-02-11 | 1992-02-11 | Vorrichtung und verfahren zur leistungszifferverbesserung im kaeltemittelkreislauf |
| DEP4203983.5 | 1992-02-11 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1993016340A1 true WO1993016340A1 (fr) | 1993-08-19 |
Family
ID=6451422
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/DE1992/000342 WO1993016340A1 (fr) | 1992-02-11 | 1992-04-29 | Dispositif et procede visant a ameliorer le coefficient de rendement de systemes frigorifiques |
Country Status (3)
| Country | Link |
|---|---|
| AU (1) | AU1795292A (fr) |
| DE (1) | DE4203983A1 (fr) |
| WO (1) | WO1993016340A1 (fr) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7052847B2 (en) | 1999-05-19 | 2006-05-30 | Cornell Research Foundation, Inc. | Method for sequencing nucleic acid molecules |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2949750A (en) * | 1956-05-28 | 1960-08-23 | Mercer Engineering Co | Heat exchange system of the evaporative type with means for maintaining liquid supply line pressure |
| DE1095670B (de) * | 1956-11-06 | 1960-12-22 | Integral Ltd | Fluessigkeitspumpe |
| US3081606A (en) * | 1961-03-06 | 1963-03-19 | United Aircraft Corp | Refrigeration system for low temperature operation |
| US3111815A (en) * | 1962-04-20 | 1963-11-26 | Westinghouse Electric Corp | Controls for refrigeration systems having air cooled condensers |
| US3600108A (en) * | 1968-08-26 | 1971-08-17 | Toyoda Machine Works Ltd | Rotary pump |
| DE2716559A1 (de) * | 1976-04-14 | 1977-10-20 | Micron Lubrotec Ateliers Elect | Hydraulische schmierzentrale |
| US4096706A (en) * | 1977-03-09 | 1978-06-27 | Sterling Beckwith | Free condensing liquid retro-pumping refrigerator system and method |
| DE3415000A1 (de) * | 1984-04-19 | 1985-10-31 | Linde Ag, 6200 Wiesbaden | Verfahren und vorrichtung zum betreiben eines kreislaufsystems |
| US4599873A (en) * | 1984-01-31 | 1986-07-15 | Hyde Robert E | Apparatus for maximizing refrigeration capacity |
-
1992
- 1992-02-11 DE DE19924203983 patent/DE4203983A1/de not_active Ceased
- 1992-04-29 AU AU17952/92A patent/AU1795292A/en not_active Withdrawn
- 1992-04-29 WO PCT/DE1992/000342 patent/WO1993016340A1/fr active Application Filing
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2949750A (en) * | 1956-05-28 | 1960-08-23 | Mercer Engineering Co | Heat exchange system of the evaporative type with means for maintaining liquid supply line pressure |
| DE1095670B (de) * | 1956-11-06 | 1960-12-22 | Integral Ltd | Fluessigkeitspumpe |
| US3081606A (en) * | 1961-03-06 | 1963-03-19 | United Aircraft Corp | Refrigeration system for low temperature operation |
| US3111815A (en) * | 1962-04-20 | 1963-11-26 | Westinghouse Electric Corp | Controls for refrigeration systems having air cooled condensers |
| US3600108A (en) * | 1968-08-26 | 1971-08-17 | Toyoda Machine Works Ltd | Rotary pump |
| DE2716559A1 (de) * | 1976-04-14 | 1977-10-20 | Micron Lubrotec Ateliers Elect | Hydraulische schmierzentrale |
| US4096706A (en) * | 1977-03-09 | 1978-06-27 | Sterling Beckwith | Free condensing liquid retro-pumping refrigerator system and method |
| US4599873A (en) * | 1984-01-31 | 1986-07-15 | Hyde Robert E | Apparatus for maximizing refrigeration capacity |
| DE3415000A1 (de) * | 1984-04-19 | 1985-10-31 | Linde Ag, 6200 Wiesbaden | Verfahren und vorrichtung zum betreiben eines kreislaufsystems |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7052847B2 (en) | 1999-05-19 | 2006-05-30 | Cornell Research Foundation, Inc. | Method for sequencing nucleic acid molecules |
Also Published As
| Publication number | Publication date |
|---|---|
| AU1795292A (en) | 1993-09-03 |
| DE4203983A1 (de) | 1992-08-20 |
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