SU684265A1 - Method of producing cold in absorption refrigeration plant - Google Patents

Method of producing cold in absorption refrigeration plant

Info

Publication number
SU684265A1
SU684265A1 SU782580866A SU2580866A SU684265A1 SU 684265 A1 SU684265 A1 SU 684265A1 SU 782580866 A SU782580866 A SU 782580866A SU 2580866 A SU2580866 A SU 2580866A SU 684265 A1 SU684265 A1 SU 684265A1
Authority
SU
USSR - Soviet Union
Prior art keywords
absorption refrigeration
refrigeration plant
producing cold
stage
evaporation
Prior art date
Application number
SU782580866A
Other languages
Russian (ru)
Inventor
Николай Михайлович Ткач
Борис Адольфович Минкус
Александр Гаврилович Дергачев
Original Assignee
Одесский Технологический Институт Холодильной Промышленности
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Одесский Технологический Институт Холодильной Промышленности filed Critical Одесский Технологический Институт Холодильной Промышленности
Priority to SU782580866A priority Critical patent/SU684265A1/en
Application granted granted Critical
Publication of SU684265A1 publication Critical patent/SU684265A1/en

Links

Classifications

    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A30/00Adapting or protecting infrastructure or their operation
    • Y02A30/27Relating to heating, ventilation or air conditioning [HVAC] technologies
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02BCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO BUILDINGS, e.g. HOUSING, HOUSE APPLIANCES OR RELATED END-USER APPLICATIONS
    • Y02B30/00Energy efficient heating, ventilation or air conditioning [HVAC]
    • Y02B30/62Absorption based systems

Landscapes

  • Sorption Type Refrigeration Machines (AREA)

Description

Изобретение относитс  к холодильной технике, а точнее к способам получени  холода в абсорбционной холодильной установке .The invention relates to refrigeration, and more specifically to methods for producing cold in an absorption refrigeration unit.

Известны способы получени  холода в абсорбционной холодильной установке путем двухстадийного выпаривани  раствори: на первой стадии теплотой, выдел ющейс  при абсорбции в цикле «превышени  температур , а на второй - посторонним теплоносителем с одновременны.м отбором паров, образующихс  на первой стадии выпаривани  и подачей их в паровой поток, образующийс  во второй стадии, последующей ректификации , дефлегмации и конденсации паров и испарени  полученной жидкости при низком давлении с производством холода 1.There are known methods for obtaining cold in an absorption refrigeration unit by two-stage evaporation of the solution: in the first stage, the heat released during absorption in the cycle of temperature rises, and in the second stage by an external heat carrier with simultaneous removal of vapors formed in the first stage of evaporation and feeding them into vapor stream formed in the second stage, subsequent rectification, refluxing and condensation of the vapor and evaporation of the resulting liquid at low pressure with the production of cold 1.

Недостатком известных способов  вл етс  их мала  экономичность вследствие больщой величины теплоты дефлегмации.A disadvantage of the known methods is their low efficiency due to the large heat of reflux.

Целью изобретени   вл етс  повыщение экономичности способа путем снижени  теплоты дефлегмации.The aim of the invention is to increase the efficiency of the process by reducing the heat of reflux.

Указанна  цель достигаетс  тем, что отбор паров, образующихс  на первой стадии выпаривани  раствора, осуществл ют наThis goal is achieved in that the selection of vapors formed in the first stage of evaporation of the solution is carried out on

различных температурных услови х, и подают их на процесс ректификации в соответствующие температурные зоны потока паров хладагента, образующихс  на второй стадии выпаривани .various temperature conditions, and they are fed to the rectification process to the corresponding temperature zones of the refrigerant vapor stream formed in the second evaporation stage.

На чертеже схематично представлена установка , в которой осуществл ют описываемый способ.The drawing shows schematically the installation in which the described method is carried out.

Установка содержит генератор I, ректификатор 2, дефлегматор 3, конденсатор 4, испаритель 5, абсорбер 6, теплообменник-регенератор 7, паровой перео.хладитель 8, смеситель 9, насос 10, отборы 11 -13 паров .хладагента и дроссельные вентили 14-16.The installation contains a generator I, a rectifier 2, a reflux condenser 3, a condenser 4, an evaporator 5, an absorber 6, a heat exchanger-regenerator 7, a steam re-cooler 8, a mixer 9, a pump 10, selections 11-13 refrigerant vapor and throttle valves 14-16 .

Установка работает следующим образом.The installation works as follows.

Пары хладагента из испарител  5 поступают частично в абсорбер 6, а оставша с  часть - Б смеситель 9, где поглощаетс  слабым раствором, который сюда поступает через дроссельный вентиль 14 из генератора 1. Выдел юща с  при этом теплота абсорбции используетс  на частичное выпаривание крепкого раствора, подаваемого в теплообменникрегенератор 7 насосом 10 из абсорбера 6.The refrigerant vapor from the evaporator 5 comes partly to the absorber 6, and the remaining part - B mixer 9, where it is absorbed by the weak solution that flows through the throttle valve 14 from generator 1. The heat of absorption absorbed is used to partially evaporate the strong solution, supplied to the heat exchanger regenerator 7 by the pump 10 from the absorber 6.

SU782580866A 1978-02-20 1978-02-20 Method of producing cold in absorption refrigeration plant SU684265A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU782580866A SU684265A1 (en) 1978-02-20 1978-02-20 Method of producing cold in absorption refrigeration plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU782580866A SU684265A1 (en) 1978-02-20 1978-02-20 Method of producing cold in absorption refrigeration plant

Publications (1)

Publication Number Publication Date
SU684265A1 true SU684265A1 (en) 1979-09-05

Family

ID=20749403

Family Applications (1)

Application Number Title Priority Date Filing Date
SU782580866A SU684265A1 (en) 1978-02-20 1978-02-20 Method of producing cold in absorption refrigeration plant

Country Status (1)

Country Link
SU (1) SU684265A1 (en)

Similar Documents

Publication Publication Date Title
SU427531A3 (en) METHOD FOR PRODUCTION OF COLD
US4337625A (en) Waste heat driven absorption refrigeration process and system
CA2013680C (en) Absorption refrigeration method and apparatus
KR19980032389A (en) Distillation plant
CN106964174B (en) Method and system for rectifying/purifying ammonia
US3486985A (en) Flash distillation apparatus with refrigerant heat exchange circuits
SU1486614A1 (en) Method of utilizing the heat of absorption-type power plant for generating electric or mechanical power
US2272856A (en) Refrigeration
SU684265A1 (en) Method of producing cold in absorption refrigeration plant
US3461460A (en) Flash distillation with condensed refrigerant as heat exchanger
US4014183A (en) Absorption refrigerator of natural circulation type
US2357612A (en) Refrigeration
US2278889A (en) Refrigerating machines arranged in cascade relationship
CN1641292A (en) Absorption refrigerator
SU1128068A1 (en) Adsorption solar refrigerating unit
SU1068671A1 (en) Absorption lithium-bromide refrigerating plant
SU1097868A1 (en) Absorption refrigerating unit
SU759810A1 (en) Method of controlling absorption refrigeration unit
SU721645A1 (en) Reflux circulating method
SU861892A1 (en) Absorption-ejection refrigerating plant
SU1070393A1 (en) Method of creating refrigeration in solar refrigerator
SU1021887A1 (en) Cascade-type heat pump installation
SU1437640A1 (en) Two-stage absorption-resorption refrigerating plant
SU1537979A1 (en) Steam-ejector bi-agent refrigeration unit
SU1373982A1 (en) Method of distant steam-heat supply