SU148072A1 - Heat transfer method - Google Patents

Heat transfer method

Info

Publication number
SU148072A1
SU148072A1 SU732138A SU732138A SU148072A1 SU 148072 A1 SU148072 A1 SU 148072A1 SU 732138 A SU732138 A SU 732138A SU 732138 A SU732138 A SU 732138A SU 148072 A1 SU148072 A1 SU 148072A1
Authority
SU
USSR - Soviet Union
Prior art keywords
heat transfer
transfer method
pressure
inversion
hydrogen
Prior art date
Application number
SU732138A
Other languages
Russian (ru)
Inventor
А.Г. Зельдович
Ю.К. Пилипенко
Original Assignee
А.Г. Зельдович
Ю.К. Пилипенко
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 А.Г. Зельдович, Ю.К. Пилипенко filed Critical А.Г. Зельдович
Priority to SU732138A priority Critical patent/SU148072A1/en
Application granted granted Critical
Publication of SU148072A1 publication Critical patent/SU148072A1/en

Links

Landscapes

  • Separation By Low-Temperature Treatments (AREA)

Description

Способы теплообмена в концевых теплообменниках водородного ИЛИ гелиевого ожижителей известны.Heat transfer methods in the end heat exchangers of hydrogen or helium liquefiers are known.

По предлагаемому способу, в отличие от известных, давление сжатого газа в теплообменнике измен ют по инверсионной кривой. При этом теплопередача интенсифицируетс  благодар  созданию наибольших разностей температур.According to the proposed method, unlike the known ones, the pressure of the compressed gas in the heat exchanger is varied according to the inversion curve. At the same time, heat transfer is intensified due to the creation of the greatest temperature differences.

Способ основан на том, что хладоороизводительность водородного ИЛИ гелиевого цикла с дросселированием максимальна, если давление сжатого газа равно давлению в точке инверсии при температуре газа после предварительного охлаждени  жидким азотом или водородом соответственно . При этом максимальные разности температур в концевом теплообменнике будут в том случае, если в каждом сечении теплообменника давлениепр мого потока равно инверсионному. Таким образом, дросселиру  сжатый и охлажденный газ до давлений, соответствующих инверсионным точкам, иначе говор , измен .ч давление сжатого газа по инверсионной кривой, можно получить наибольшие разности температур , а следовательно, и интенсифицировать теплопередачу.The method is based on the fact that the cooling capacity of the hydrogen OR helium cycle with throttling is maximum if the pressure of the compressed gas is equal to the pressure at the inversion point at the gas temperature after preliminary cooling with liquid nitrogen or hydrogen, respectively. In this case, the maximum temperature differences in the end heat exchanger will be if in each section of the heat exchanger the pressure of the direct flow is equal to the inversion flow. Thus, throttling the compressed and cooled gas to pressures corresponding to the inversion points, in other words, by changing the pressure of the compressed gas along the inversion curve, it is possible to obtain the greatest temperature differences, and consequently, to intensify the heat transfer.

Предмет изобретени Subject invention

Способ теплообмена в концевых теплообменниках водородного или гелиевого ожижителей, отл ич а ющи йс  тем, что, с целью интенсификации теплопередачи путем создани  наибольших разностей температур , давление, сжатого газа в теплообменнике измен ют по инверсионной кривой.The method of heat exchange in the end heat exchangers of hydrogen or helium liquefiers, differing from the fact that, in order to intensify heat transfer by creating the greatest temperature differences, the pressure of the compressed gas in the heat exchanger is changed according to the inversion curve.

SU732138A 1961-05-27 1961-05-27 Heat transfer method SU148072A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
SU732138A SU148072A1 (en) 1961-05-27 1961-05-27 Heat transfer method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
SU732138A SU148072A1 (en) 1961-05-27 1961-05-27 Heat transfer method

Publications (1)

Publication Number Publication Date
SU148072A1 true SU148072A1 (en) 1961-11-30

Family

ID=48303375

Family Applications (1)

Application Number Title Priority Date Filing Date
SU732138A SU148072A1 (en) 1961-05-27 1961-05-27 Heat transfer method

Country Status (1)

Country Link
SU (1) SU148072A1 (en)

Similar Documents

Publication Publication Date Title
SU606042A1 (en) Method of generating cold
GB1030600A (en) The liquefaction of gases with low boiling points
GB1290377A (en)
GB860723A (en) Low temperature refrigeration
GB974542A (en) Liquefaction of gases
SU148072A1 (en) Heat transfer method
ATE125350T1 (en) LOW TEMPERATURE COOLING SYSTEM.
ES315031A1 (en) Energy production procedure for recovery of the heat generated in a nuclear reactor refrigerated by carbonic gas. (Machine-translation by Google Translate, not legally binding)
US3327495A (en) Gas cooling system
IT974652B (en) IMPROVEMENT IN HEAT EXCHANGERS AND METHOD FOR RELIEVING THERMAL STRESS IN THEM
ES352910A1 (en) A process and apparatus for producing energy, using thermodynamic cycles with gases condensible at ambient temperature
SU142311A1 (en) Method of liquefying gases
SU148417A1 (en) The method of obtaining cold by the method of gas expansion
ES312309A3 (en) Improvements in the construction of bottle refrigerators. (Machine-translation by Google Translate, not legally binding)
SE304294B (en)
SU75818A1 (en) Method for improving operation of heat exchangers of deep-cooling plants
SU143815A1 (en) The method of operation of thermal power plants on low-boiling substances
SU1629596A1 (en) Thermo-compressor
Geist et al. Compact Joule-Thomson refrigeration systems 15–60 K
SU603818A1 (en) Method of cold generation in cryogenic plant
GB1245621A (en) Air separation process
SU146744A1 (en) Method of liquefying gels
SU504055A2 (en) Method for the production of cold in cryogenic plants
SU85541A1 (en) Method for "unbalanced flow" in deep cold installations
FR1370321A (en) Process of cooling by adiabatic expansion of a compressed gaseous refrigerant, through a series of expansion valves connected in parallel, in a refrigeration zone with several stages