SU1193395A1 - Heat and cold producing plant - Google Patents
Heat and cold producing plant Download PDFInfo
- Publication number
- SU1193395A1 SU1193395A1 SU843745130A SU3745130A SU1193395A1 SU 1193395 A1 SU1193395 A1 SU 1193395A1 SU 843745130 A SU843745130 A SU 843745130A SU 3745130 A SU3745130 A SU 3745130A SU 1193395 A1 SU1193395 A1 SU 1193395A1
- Authority
- SU
- USSR - Soviet Union
- Prior art keywords
- generator
- power circuit
- heat
- heat exchanger
- condenser
- 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
;о со; about with
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Изобретение относитс к области холодильной техники, а точнее к устновкам дл производства тепла и х,олода .The invention relates to the field of refrigeration, and more specifically to installations for the production of heat and x, oloda.
Цель изобретени - повьшёние экономичности .The purpose of the invention is higher efficiency.
На чертеже схематично изображена описываема установка.The drawing schematically shows the described installation.
Установка дл производства тепла и холода содержит силовой кон . тур, в котором установлены парообразователь 1, ступень 2 высокого давлени и ступень 3 низкого давлени турбогенератора Л, конденсатор 5 и пнтательньш насос 6, а также абсорбционную холодильную машину с генератором 7, конденсатором, служащим парообразоват.елем 1 силового контзфа,. дросселем 8, испарителем 9 и абсорбером- 10, подключенным посредством регенеративного теплообменника 11 к генератору 7, включенные в силовой контур пароперегреватели 12 и 13, и жидкостной теплообменник 14, св занный насосом 15 и замкнутым контуром 16 с абсорбером . 10, и лини 17 подвода тепла низког потенциала..The plant for the production of heat and cold contains a power con. a tour in which a steam generator 1, a high pressure stage 2 and a low pressure stage 3 of the turbogenerator L, a condenser 5 and a pilot pump 6, as well as an absorption chiller with a generator 7, a condenser serving as a steam generator 1 of the power train, are installed. the choke 8, the evaporator 9 and the absorber-10 connected via a regenerative heat exchanger 11 to the generator 7, the superheaters 12 and 13 connected to the power circuit, and the liquid heat exchanger 14 connected by the pump 15 and the closed loop 16 to the absorber. 10, and a low potential heat supply line 17.
Кроме этого, содержит насос 18 дл перекачивани крепкого раство .ра. .In addition, it contains a pump 18 for pumping a strong solution. .
Работа.установки осуществл етс следующим образом.The operation of the installation is carried out as follows.
Тепло низкого потенциала подводитс по линии в генератор 7 холодильной машины и в пароперегреватели 12 и 13. При этом в генерато-ре 7 из крепкого раствора выдел ютс пары 5сладагента, которые кон3395 Heat of low potential is supplied via a line to the generator 7 of the refrigerating machine and to the steam superheaters 12 and 13. In this case, in the generator 7 of the strong solution, vapors 5 of the coolant are released, which are 3395
денсируютс в. парообразователе 1, образу в нем из наход щейс здесь жидкости пар рабочего агента, направл емого последовательнов пароперегреватель 12, ступень 2 высокого давлени турбогенератора 4, пароперегр еватель 13 и ступень 3 .низкого давлени .- Пар агента низкого давлени сжимаетс в конденсаторе densiruyuts in the steam generator 1, which forms from it a liquid of the working agent steam sent sequentially to the steam superheater 12, the high-pressure stage 2 of the turbo-generator 4, the steam superheater 13 and the low-pressure stage 3.
10 5, а образующийс жидкий агент10 5 and the resulting liquid agent
питательным насосом 6 направл етс через жидкостной теплообменник -14 снова в парообразователь -1. Жидкий хладагент, образующийс в паро 5 образователе, снижает Ьвое давление в дросселе 8 и направл етс в испаритель 9 и конденсатор 5, в первом из которых производит холодильное действие, охлажда хладоноск20 тель,направл емый потребителю холода , а во втором, как указано, снижает пар агента 1шзкого давлени . Образующиес и испарителе 9 и конден саторе .5 пары хладагента направл ютс в абсорбер 10, .в .котором поглощаютс выпаренным в генератот ре 7 бинарным раствором, предварительно охлажденным крепким раствором в регенеративном теплообменнике 11.feed pump 6 is directed through liquid heat exchanger -14 back to steam generator -1. The liquid refrigerant formed in the steam generator reduces the pressure in the throttle 8 and is directed to the evaporator 9 and condenser 5, in the first of which produces a cooling effect, cooling the refrigerant that is directed to the cold consumer, and in the second, as indicated, reduces vapor pressure agent. The refrigerant vapors formed in both the evaporator 9 and the condenser .5 are sent to the absorber 10, in which they are absorbed by the binary solution evaporated into the generator 7, previously cooled by a strong solution in the regenerative heat exchanger 11.
,д Теплота, выдел ема в процессе абсорбции -в абсорбере 10 с помощью насоса 15 и замкнутого контура 16, . подводитс к жидкостному теплообмен .нику 14,в котором используетс дл нагрева жидкого агента, подаваемого, d The heat released during the absorption process is in the absorber 10 by means of a pump 15 and a closed loop 16,. supplied to a liquid heat exchanger 14, in which it is used to heat the liquid agent supplied
питательным насосом 6 в парообразователь 1 . На этом заканчиваетс рабо- . чий цикл агента в силовом контуре и хладагента в абсорбционной холодильной машине. feed pump 6 to the steam generator 1. This ends the job. which agent cycle in the power circuit and the refrigerant in the absorption chiller.
Claims (1)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU843745130A SU1193395A1 (en) | 1984-05-29 | 1984-05-29 | Heat and cold producing plant |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
SU843745130A SU1193395A1 (en) | 1984-05-29 | 1984-05-29 | Heat and cold producing plant |
Publications (1)
Publication Number | Publication Date |
---|---|
SU1193395A1 true SU1193395A1 (en) | 1985-11-23 |
Family
ID=21120711
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
SU843745130A SU1193395A1 (en) | 1984-05-29 | 1984-05-29 | Heat and cold producing plant |
Country Status (1)
Country | Link |
---|---|
SU (1) | SU1193395A1 (en) |
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1984
- 1984-05-29 SU SU843745130A patent/SU1193395A1/en active
Non-Patent Citations (1)
Title |
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Авторское свидетельство СССР 569735,кл. F. 25 В 29/00, 1977. * |
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