SU794059A1 - Working agent for absorptional cooling machines - Google Patents
Working agent for absorptional cooling machines Download PDFInfo
- Publication number
- SU794059A1 SU794059A1 SU792721936A SU2721936A SU794059A1 SU 794059 A1 SU794059 A1 SU 794059A1 SU 792721936 A SU792721936 A SU 792721936A SU 2721936 A SU2721936 A SU 2721936A SU 794059 A1 SU794059 A1 SU 794059A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- absorptional
- working agent
- cooling machines
- solution
- machines
- Prior art date
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/27—Relating to heating, ventilation or air conditioning [HVAC] technologies
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02B—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
- Y02B30/00—Energy efficient heating, ventilation or air conditioning [HVAC]
- Y02B30/62—Absorption based systems
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
Как видно из табл. 1 и 2, давление насыщенных паров воды над растворами отличаютс незначительно, однако при (температура абсорбции) кристаллизаци CaCpj aa водного раствора начинаетс при 51,3%, а смеси . Ca(NOi), ( et 5/1) при 60,2%. Следовательно, предельна рабоча Область концентраций раствора НчО (МО j)j , по сравнению с раствором - CaCPj, будет увеличена, примерно на 9 абс.%, что свидетельств ет о большей эксплуатационной надежности машины, использующей раствор HjO - ,-Ca{N05)i по сравнению с хлористокальциевой АХМ.As can be seen from the table. 1 and 2, the pressure of saturated water vapor above the solutions differs slightly, but at (absorption temperature) the CaCpj aa crystallization of the aqueous solution begins at 51.3%, and the mixture. Ca (NOi), (et 5/1) at 60.2%. Consequently, the limiting working area of the concentration of the NCHO solution (MO j) j, as compared with the solution — CaCPj, will be increased by approximately 9 abs.%, Which indicates a greater operational reliability of the machine using the solution HjO -, -Ca {N05) i compared to chloride calcium AHM.
Сравнение параметров теоретических циклов абсорбционных холодильных маПолитермы растворимости в воде СаСР- и смеси CaCP2 -Ca{NO)2 (масс. %)Comparison of the parameters of theoretical cycles of absorption refrigeration solubility maapolimer in water СaСР- and mixtures CaCP2 -Ca {NO) 2 (wt.%)
Температура, °СTemperature, ° С
АбсорбентAbsorbent
сасеSasa
38,438.4
СаСБ2-Са(ме), 51,6 56,8 60,2СаСБ2-Са (ме), 51.6 56.8 60.2
Давление насыщенных паров воды (.CT.) при над растворами - - CaCC2 -Ca(NO)j с Л 5/1Pressure of saturated water vapor (.CT.) When above solutions - - CaCC2 -Ca (NO) j with L 5/1
шин показало уменьшение кратности циркул ции и, как следствие, уменьшение тепловых нагрузок на теплообменник и абсорбер АХМ, использующей раствор HjrO - CaCSj,- Са(МО), по сравнению с хлористокальциевой АХМ. При этом сохран етс термодинамическа эффективность на уровне хлористокальциевой АХМ. Увеличение зоны дегазации , по сравнению с раствором Hj O-CaCC позвол ет использовать дл предлагаемой АХМ греющие источники более низкого потенциала.tires showed a decrease in the rate of circulation and, as a result, a decrease in heat loads on the heat exchanger and the AXM absorber using the HjrO – CaCSj, –Ca (MO) solution, as compared to the chloride-calcium AHM. At the same time, thermodynamic efficiency is maintained at the level of chloride-calcium AXM. The increase in the degassing zone, as compared with the HjO-CaCC solution, allows the heating sources to use a lower potential for the proposed AHM.
Технико-экономическа эффективность заключаетс в повьвиении эксплуатационной надежности мгопины и в расширении диапазона получаемых температур .Technical and economic efficiency consists in improving the operational reliability of the system and in expanding the range of temperatures obtained.
Таблица 1Table 1
3535
5050
2020
56,856,8
51,351.3
42,742.7
65-,265-, 2
ТаблицаTable
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU792721936A SU794059A1 (en) | 1979-02-07 | 1979-02-07 | Working agent for absorptional cooling machines |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU792721936A SU794059A1 (en) | 1979-02-07 | 1979-02-07 | Working agent for absorptional cooling machines |
Publications (1)
Publication Number | Publication Date |
---|---|
SU794059A1 true SU794059A1 (en) | 1981-01-07 |
Family
ID=20809065
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU792721936A SU794059A1 (en) | 1979-02-07 | 1979-02-07 | Working agent for absorptional cooling machines |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU794059A1 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5643858A (en) * | 1992-02-15 | 1997-07-01 | Brunner Mond & Company Limited | High density aqueous compositions |
-
1979
- 1979-02-07 SU SU792721936A patent/SU794059A1/en active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5643858A (en) * | 1992-02-15 | 1997-07-01 | Brunner Mond & Company Limited | High density aqueous compositions |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
ES361089A1 (en) | Absorption refrigeration system | |
SU794059A1 (en) | Working agent for absorptional cooling machines | |
ES2013529A6 (en) | Process and apparatus for cooling a fluid | |
SE8505530D0 (en) | ABSORP TYPE HEAT PUMP | |
AU623079B2 (en) | Absorbent solution for use with absorption refrigeration apparatus | |
SE8505531L (en) | ABSORPTION TYPE COOLING SYSTEM | |
SU794060A1 (en) | Working agent for absorptional cooling machines | |
SU382667A1 (en) | WORKING BODY VACUUM-ABSORPTION REFRIGERATING | |
SU581732A1 (en) | Apparatus for producing gas media and refrigerant | |
GB800310A (en) | Improvements in or relating to absorption refrigeration | |
SU583153A1 (en) | Binary mixture for absorption refrigerating machine | |
CN103540295A (en) | Absorption type lithium bromide circulating mixed medium and preparation method thereof | |
US2185040A (en) | Method of refrigeration and absorbent therefor | |
US2357431A (en) | Refrigeration | |
SU567042A1 (en) | Method of regeneration of a solution in a two-stage generator | |
SU986914A1 (en) | Working fluid for absorption refrigerating machine | |
US1960368A (en) | Artificial refrigeration | |
SU565171A1 (en) | Absorption lithium-bromic refrigerating unit | |
Ray et al. | Part 1: Absorption chilling process, types, and comparison to compression chilling | |
SU446721A1 (en) | Heat and Cooling System | |
SU453536A1 (en) | ABSORPTION REFRIGERATION INSTALLATION :::: - ^: pТПУ I and | |
SU583354A1 (en) | Method of operation of absorption refrigerating installation | |
SU503100A1 (en) | The method of operation of lithium absorption lithium absorption chiller | |
WO1988010290A1 (en) | High-temperature non-oxidizing water vapor absorbent | |
SU798449A1 (en) | Plant for absorbing steam at sublimation drying |