NO145853B - PROCEDURE FOR OPERATION OF A REFRIGERATOR MADE IN A MOBILE REFRIGERATOR. - Google Patents
PROCEDURE FOR OPERATION OF A REFRIGERATOR MADE IN A MOBILE REFRIGERATOR. Download PDFInfo
- Publication number
- NO145853B NO145853B NO781899A NO781899A NO145853B NO 145853 B NO145853 B NO 145853B NO 781899 A NO781899 A NO 781899A NO 781899 A NO781899 A NO 781899A NO 145853 B NO145853 B NO 145853B
- Authority
- NO
- Norway
- Prior art keywords
- refrigerating
- refrigerator
- mobile
- condensed
- trailer
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims description 5
- VJYFKVYYMZPMAB-UHFFFAOYSA-N ethoprophos Chemical compound CCCSP(=O)(OCC)SCCC VJYFKVYYMZPMAB-UHFFFAOYSA-N 0.000 title 1
- 238000001816 cooling Methods 0.000 claims description 9
- 239000003507 refrigerant Substances 0.000 claims description 3
- 239000003570 air Substances 0.000 description 11
- 239000007788 liquid Substances 0.000 description 9
- 230000006835 compression Effects 0.000 description 7
- 238000007906 compression Methods 0.000 description 7
- 230000000694 effects Effects 0.000 description 3
- 239000012080 ambient air Substances 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000005057 refrigeration Methods 0.000 description 2
- 230000002441 reversible effect Effects 0.000 description 2
- 238000012512 characterization method Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000002349 favourable effect Effects 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
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
-
- 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
- F25B30/00—Heat pumps
- F25B30/02—Heat pumps of the compression type
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Devices That Are Associated With Refrigeration Equipment (AREA)
- Sorption Type Refrigeration Machines (AREA)
- Central Heating Systems (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
- Cold Air Circulating Systems And Constructional Details In Refrigerators (AREA)
Description
Foreliggende oppfinnelse vedrører en fremgangsmåte av den art som er angitt i kravets ingress. The present invention relates to a method of the type stated in the preamble of the claim.
Et vesentlig element ved tapt arbeide i dampkompresjons-maskiner såsom luftkondisjoneringsapparater er tapet som skyldes struping av den kondenserte væske til fordamperen. Effekt-koeffisienten, The Coeficient of Performance (COPH) for et slikt system er gitt av den følgende ligning: A significant element of lost work in vapor compression machines such as air conditioners is the loss due to throttling of the condensed liquid to the evaporator. The Coefficient of Performance (COPH) for such a system is given by the following equation:
hvor hc er den overopphetede damps entalpi etter kompresjon, og h^ er dampens entalpi etter oppvarmning i fordamperen og ved inn-gangen til kompressoren, og hg er den kondenserte væskes entalpi etter avkjøling i konden-seren . where hc is the enthalpy of the superheated steam after compression, and h^ is the enthalpy of the steam after heating in the evaporator and at the entrance to the compressor, and hg is the enthalpy of the condensed liquid after cooling in the condenser.
Fra formelen fremgår det at COPH forøkes for en kjølemaskin ved å ekstrahere varme fra den kondenserte væske. Hvor underkjøling av etter-kondensatorvæske oppnås uten å på-virke kompresjonsarbeide oppnås det en forøkning i kjøle-effekt med derav følgende forøkelse i COPH og kapasitet. Den beskrevne lav-temperaturvarme-effektivitet er enda mer gunstig for COPH enn det som ville være effekten av reversibel ekspansjon av væsken å anvende dette ekspansjonsar-beidet for å redusere kompresjonsarbeidet. Et eksempel ville være et kjøleanlegg som fordampet ved -15°C og kondenserte ved 38°C med en kompresjonseffektivitet på 55 % og en .kondensator underkjølt til 30°C vil resultere i en COPH på ca. 3,2. En reversibel væskeekspansjon fra 30°C til 9°C vil gi tilbake ca. 5 % av det totale kompresjonsarbeidet og forøke COPH til ca. 3,45 mens underkjøling fra 30°C til 9°C ville forøke kapasiteten med ca. 19,4 % og heve COPH til ca. 3,85. From the formula it appears that COPH is increased for a refrigerating machine by extracting heat from the condensed liquid. Where subcooling of after-condenser liquid is achieved without affecting compression work, an increase in cooling effect is achieved with a consequent increase in COPH and capacity. The described low-temperature heating efficiency is even more favorable to COPH than would be the effect of reversible expansion of the fluid to use this work of expansion to reduce the work of compression. An example would be a refrigeration plant that evaporated at -15°C and condensed at 38°C with a compression efficiency of 55% and a .condenser subcooled to 30°C would result in a COPH of approx. 3.2. A reversible liquid expansion from 30°C to 9°C will return approx. 5% of the total compression work and increase the COPH to approx. 3.45, while subcooling from 30°C to 9°C would increase the capacity by approx. 19.4% and raise COPH to approx. 3.85.
En hensikt er å tilveiebringe en fremgangsmåte av den beskrevne type hvor væsken etter kjøleren avkjøles for å for-øke COPH og kapasiteten. One purpose is to provide a method of the type described where the liquid after the cooler is cooled to increase the COPH and the capacity.
For avkjøling av et bevegelig kammer leder en kanal inneluf-ten for avkjøling i en bane som føres ut fra det lukkede rom i en retning mot bevegelsesretningen for å hjelpe til med å trekke ut den underkjølende gass. Fremgangsmåten er særpreget ved det som er angitt i kravets karakteriser- For cooling a moving chamber, a duct directs the indoor air for cooling in a path which is led out from the closed space in a direction against the direction of movement to assist in extracting the subcooling gas. The procedure is characterized by what is stated in the requirement's characterization
ende del. end part.
De nevnte og ytterligere hensikter og trekk ved oppfinnel- The aforementioned and further purposes and features of the invention
sen vil fremgå av den etterfølgende beskrivelse...... as will be apparent from the subsequent description......
Fig. 1 viser en utførelsesform for oppfinnelsen anvendt for kjøling av et volum. I denne utførelsesform utgjøres kjøle-volumet 40 av et mobilt kammer, illustrert som en kjøletrailer 41. Fig. 1 shows an embodiment of the invention used for cooling a volume. In this embodiment, the cooling volume 40 is made up of a mobile chamber, illustrated as a cooling trailer 41.
En dampkompresjonskjølemaskin 42 er anordnet på traileren. Maskinen innbefatter en kompressor 4 4 som komprimerer en arbeids-væske såsom "R22" kjølemiddel til kondenserspiralen 46 montert inne i et hus 48 trailerens tak. Huset er forsynt med innløps-og uløpsåpninger gjennom hvilke en strøm av omgivende luft rettes under den relative bevegelse av traileren. Den omgivende luft avkjøler den komprimerte damp som deretter innføres til en underkjølerspiral 50 montert inne i en kanal 52 i trailerens volum. En innløpsdel 54 av denne kanalen konsentrerer en strøm av utgående kald luft fra traileren og inn i varmevekslende forhold med underkjøler spiralen. Et utløp 56 av kanalen ut-strekker seg over trailerens tak og utfører luftstrømmen i en retning motsatt trailerens bevegelses retning. Trailerens frem-adrettede bevegelse vil derved danne et partsielt våkum i et ut-løp hvilket bevirker en uttrekning av luft gjennom kanalen. Væske fra underkjøleren ekspanderes gjennom en strupeventii 58. Strømmen gjennom strupeventilen kontrolleres ved passende midler så som en underkjølingstype kontroll forsynt med en temperaturføler 60 montert ved kondenserens utløp. Damp ekspanderer fra ventilen 58 og inn i fordampnings spiralen 62 montert inne i huset 64 inne i traileren. En vifte 66 pumper luft inn i fordamperhuset hvor luften avkjøles og deretter rettes ut gjennom utløpet 68 mot trailerens volum. A vapor compression refrigeration machine 42 is provided on the trailer. The machine includes a compressor 44 which compresses a working fluid such as "R22" refrigerant to the condenser coil 46 mounted inside a housing 48 on the roof of the trailer. The housing is provided with inlet and outlet openings through which a stream of ambient air is directed during the relative movement of the trailer. The ambient air cools the compressed steam which is then introduced to a subcooler coil 50 mounted inside a channel 52 in the volume of the trailer. An inlet part 54 of this channel concentrates a stream of outgoing cold air from the trailer into heat-exchange conditions with the subcooler coil. An outlet 56 of the duct extends above the roof of the trailer and conducts the air flow in a direction opposite to the direction of movement of the trailer. The forward movement of the trailer will thereby form a partial vacuum in an outlet, which causes an extraction of air through the channel. Liquid from the subcooler is expanded through a throttle valve 58. The flow through the throttle valve is controlled by suitable means such as a subcooler type control provided with a temperature sensor 60 mounted at the condenser outlet. Steam expands from the valve 58 into the evaporation coil 62 mounted inside the housing 64 inside the trailer. A fan 66 pumps air into the evaporator housing where the air is cooled and then directed through the outlet 68 towards the volume of the trailer.
Ved bruk og drift av utførelsesformen ifølge fig. 1 vil COPH When using and operating the embodiment according to fig. 1 will COPH
og kapasiteten for frysemaskinen forøkes ved underkjøling av den kondenserte væske ved at kald luft fra traileren, som ellers ville lekke ut som følge av trykket av den innførte and the capacity of the freezer is increased by subcooling the condensed liquid by cold air from the trailer, which would otherwise leak out as a result of the pressure of the introduced
luft forårsaket av trailerens bevegelse. Med andre ord vil air caused by the movement of the trailer. In other words, will
varme ekstraheres fra væsken som kommer ut av kondensatoren ved hjelp av en konsentrert unnslippende varmluftstrøm (som derved oppvarmes), en kjøleeffekt som ellers ville gå tapt som følge av et luftinnsig. heat is extracted from the liquid exiting the condenser by means of a concentrated escaping stream of hot air (which is thereby heated), a cooling effect that would otherwise be lost as a result of an air ingress.
Claims (1)
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US83228377A | 1977-09-12 | 1977-09-12 |
Publications (3)
Publication Number | Publication Date |
---|---|
NO781899L NO781899L (en) | 1979-03-13 |
NO145853B true NO145853B (en) | 1982-03-01 |
NO145853C NO145853C (en) | 1982-06-09 |
Family
ID=25261221
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
NO781899A NO145853C (en) | 1977-09-12 | 1978-05-31 | PROCEDURE FOR OPERATING A REFRIGERATOR MADE IN A MOBILE REFRIGERATOR |
Country Status (8)
Country | Link |
---|---|
JP (1) | JPS5444339A (en) |
CA (1) | CA1082935A (en) |
DE (1) | DE2822965A1 (en) |
DK (1) | DK238678A (en) |
FR (1) | FR2402845A1 (en) |
GB (1) | GB1587709A (en) |
NO (1) | NO145853C (en) |
SE (1) | SE7806199L (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
IT1192407B (en) * | 1982-04-22 | 1988-04-13 | S I E T T E Soc Impianti Elett | HEAT PUMP SYSTEM FOR AIR CONDITIONING OF RAILWAY CARRIAGES FOR PASSENGERS |
US4683726A (en) * | 1986-07-16 | 1987-08-04 | Rejs Co., Inc. | Refrigeration apparatus |
JP5183521B2 (en) * | 2009-02-12 | 2013-04-17 | 能美防災株式会社 | Sprinkler fire extinguishing equipment and sprinkler head used in this sprinkler fire extinguishing equipment |
Family Cites Families (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2100867A (en) * | 1936-07-31 | 1937-11-30 | Gen Electric | Air conditioning system |
US2474304A (en) * | 1946-01-28 | 1949-06-28 | Drayer Hanson | Reversible cycle heat pump |
FR1023656A (en) * | 1950-08-22 | 1953-03-23 | Arrangement of the condenser circuits of the refrigerating machines for the use of the heat released | |
FR1032737A (en) * | 1951-01-19 | 1953-07-03 | Ruhrstahl Ag | Refrigeration machine powered by compressed air, for cooling air used for ventilation of mines |
US2841963A (en) * | 1956-10-18 | 1958-07-08 | Gen Motors Corp | Refrigerating apparatus |
GB942688A (en) * | 1961-06-22 | 1963-11-27 | Bfrtram Robert Leigh | Improvements relating to space and water heating systems |
JPS5129170Y2 (en) * | 1971-04-30 | 1976-07-22 | ||
US3783629A (en) * | 1972-09-13 | 1974-01-08 | C Phillips | Refrigeration system |
FR2256381A1 (en) * | 1973-12-27 | 1975-07-25 | Tour Agenturer Ab | Arrangement for heating or cooling a flow medium - part of air currents diverted to a circuit containing e.g. ammonia in a heat exchanger |
FR2282606A1 (en) * | 1974-08-22 | 1976-03-19 | Rellier Eugene | Building heating and cooling system - extracts heat from removed air by refrigeration fluid and transfers to air delivered to rooms |
SE396126B (en) * | 1975-02-18 | 1977-09-05 | Projectus Ind Produkter Ab | PROCEDURE AND DEVICE FOR TEMPERATING A SEVERAL PREMISES WITH INBOARD DIFFERENT AND VARIING HEATING NEEDS |
FR2323963A1 (en) * | 1975-09-11 | 1977-04-08 | Rellier Eugene | Heat pump for air conditioning - uses baffles to selectively circulate air through set of heat exchangers |
-
1978
- 1978-05-17 GB GB20103/78A patent/GB1587709A/en not_active Expired
- 1978-05-26 DE DE19782822965 patent/DE2822965A1/en not_active Withdrawn
- 1978-05-30 SE SE7806199A patent/SE7806199L/en unknown
- 1978-05-30 DK DK238678A patent/DK238678A/en unknown
- 1978-05-30 JP JP6486778A patent/JPS5444339A/en active Granted
- 1978-05-31 FR FR7816238A patent/FR2402845A1/en not_active Withdrawn
- 1978-05-31 CA CA304,485A patent/CA1082935A/en not_active Expired
- 1978-05-31 NO NO781899A patent/NO145853C/en unknown
Also Published As
Publication number | Publication date |
---|---|
JPS5444339A (en) | 1979-04-07 |
DE2822965A1 (en) | 1979-03-15 |
NO145853C (en) | 1982-06-09 |
DK238678A (en) | 1979-03-13 |
FR2402845A1 (en) | 1979-04-06 |
CA1082935A (en) | 1980-08-05 |
JPS5517305B2 (en) | 1980-05-10 |
SE7806199L (en) | 1979-03-13 |
NO781899L (en) | 1979-03-13 |
GB1587709A (en) | 1981-04-08 |
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