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No 12 (2015)

Full Issue

Open Access Open Access
Restricted Access Access granted
Restricted Access Subscription or Fee Access

Articles

Rezul'taty proizvodstvennoy deyatel'nosti «NPF «Khimkholodservis»

Tovaras N.V.
Refrigeration Technology. 2015;(12):4-6
pages 4-6 views
pages 7-17 views
pages 18-20 views

Rynok teplovykh nasosov «vozdukh - voda»

- -.
Refrigeration Technology. 2015;(12):21-22
pages 21-22 views

Kogda nachnutsya prodazhi bytovykh konditsionerov vozdukha na R290?

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Refrigeration Technology. 2015;(12):23-24
pages 23-24 views
pages 25-27 views
pages 28-32 views

Obobshchennye raschetnye zavisimosti dlya opredeleniya intensivnosti teploobmena pri kipenii smesevykh khladagentov

Ovsyannik A.V., Makeeva E.N.

Abstract

The results of the experimental research of the heat exchange at bubble boiling of R404А, R407С and R410А refrigerants on finned tubes are cited. The experiments were carried out at 13...28,5 оС saturation temperatures. It was established by experiments as well as theoretically that at the developed bubble boiling the intensity of the heat transfer didn’t depend on the type or profile of the nonisothermic finned surface but it was defined only by operation parameters, thermophysical properties of the liquid, geometrical dimensions of the finned surface as well as by the internal characteristics of the boiling process. The heat transfer coefficients at the refrigerant boiling on a finned surface was rather higher than on the smooth one, i.e. at developed bubble boiling the heat exchange on finned surfaces was 2-4 times higher than on the smooth ones. The empiric dependences were defined that allowed finding the heat transfer coefficient at R404А, R407С and R410А refrigerants boiling on the finned surface of a big volume; they were satisfactorily agreed with the experimental data, the error was 15-20%. The possibility of using the derived dependences to calculate heat exchange apparatuses of the evaporating type with finned surfaces was shown. Keywords: heat exchange at boiling, vaporization, mixed ozone safe refrigerant, heat exchange intensity, heat transfer coefficient, finned surfaces, evaporator, heat exchange apparatus, refrigerating plant, empiric dependence.
Refrigeration Technology. 2015;(12):33-37
pages 33-37 views

Programmnye i apparatnye sredstva sistemy upravleniya slivom zhidkogo geliya

Ageev A.I., Alferov V.N., Kozub S.S., Stolyarov M.N.

Abstract

To provide the experimental physical plants with liquid helium the GNTs IFVE developed, created and put into exploitation the system of the liquid helium overflow (LHO) into transport Dewar vessels at 100 and 200 l capacity based on the KVU 500 cryogenic vacuum plant. When solving the problem the authors took into account the necessity to provide other experimental physical plants with liquid helium that operated at the same time with a superconductive separator that was a principal consumer of the KVU. Also the reason was that it was necessary to use an automation due to a shortage of the maintenance staff. The system developed allows accumulating the liquid helium surplus during excess production of KVU and transmitting it automatically to the buffer accumulation vessel. The Dewar vessels are fulfilled from this vessel without stopping the operation when the necessary refrigerant level is reached. The system of the liquid helium overflow is described in the paper as well as its timing and hardware units. Keywords: cryogenics, automation, low temperatures, refrigerating systems, refrigerants, Dewar vessels, automated systems.
Refrigeration Technology. 2015;(12):38-41
pages 38-41 views

Analiz sostoyaniya i perspektiv razvitiya kislorodnogo i kriogennogo mashinostroeniya

Lavrenchenko G.K.
Refrigeration Technology. 2015;(12):42-45
pages 42-45 views

Kriogen-Ekspo. Promyshlennye gazy

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Refrigeration Technology. 2015;(12):46-48
pages 46-48 views
pages 48-48 views
pages 49-55 views

Tekhnologiya zamorazhivaniya vodonasyshchennykh granul sfericheskoy formy

Marinyuk B.T., Serenov I.I.

Abstract

The freezing spherical watersaturated granules using the negative temperature air blowoff of their surface was examined. A generalized equation for calculation of the frozen layer thickness of the spherical watersaturated granule depending on the duration of the process was derived. The experimental bench and the method of the research carrying out were described. The experimental data were compared with the calculated indices obtained on the basis of the generalized process equation. A construction arrangement of a cold accumulating watercooling tower that uses the negative temperatures potential of the ambient air to accumulate water ice was offered. The results of the research may be used when designing the cold accumulating watercooling towers. Keywords: spherical granules, water ice accumulation, electric power saving, lowpotential energy source, cold accumulating watercooling tower, negative temperatures, ice water, phase transition.
Refrigeration Technology. 2015;(12):56-59
pages 56-59 views

Kalendar' vystavok na I polugodie 2016 g

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Refrigeration Technology. 2015;(12):60-60
pages 60-60 views
pages 61-64 views

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