Kombinovani kompresiono-apsorpcioni ciklus - uticaj nekih važnih parametara na koeficijent grejanja i poređenje sa kompresionim ciklusom

##plugins.themes.bootstrap3.article.main##

Magnus Hulten Thore Berntsson

Apstrakt

Ovaj rad opisuje dve glavne analize: parametarsku i uporednu analizu. U parametarskoj analizi posmatra se kompresiono-apsorpciona toplotna pumpa (engleska skraćenica CAHP). Proučava se osetljivost njenog koeficijenta grejanja (engl. skraćenica COP) na promenu dužine cevi duž kojih se sliva film tečnosti u apsorberu i desorberu, raspodelu površine razmenjivača toplote i promenu koncentracije rastvora u apsorberu. Utvrđeno je da relativna raspodela između desorbera i apsorebra ima mali uticaj na koeficijent grejanja. Površina razmenjivača toplote za rastvor i promena koncentracije u apsorberu imaju veliki uticaj na koeficijent grešaka kada se posmatraju odvojeno, međutim kada se posmatraju zajedno i uz optimiziranu promenu koncentracije za svaku raspodelu površina, ukupan uticaj je mali. Prikazano je da ceviniz koje se sliva rastvor treba projektovati tako da budu što duže kako bi se povećao koeficijent grejanja. Uporedna analiza obuhvata novi postupak za poređenje performansi (COP) kompresiono-apsorpcione pumpe (CAHP) sa kompresionom toplotnom pumpom (engleska skraćenica CHP). U ovom postupku uzeti su u obzir lokalni koeficijenti prelaza toplote i pada pritiska. Dalje, poređenje se vrši za različite primene u oblasti grejanja i za određeni nivo ulaganja. Primene u oblasti grejanja i izabrane su za proučavanje tri različite vrste uticaja i to: veličine promene temperature (temperaturskog klizanja) ponora i izvora toplote, porasta temperature za dato temperatursko klizanje ponora i izvora toplote i temperaturski nivo "klizajućih" ponora i izvora toplote. Smeša amonijka i vode se koristi kao radni fluid kod CAHP, a izobutan kodn CHP. Pretpostavlja se relevantno industrijsko rešenje za CHP (uključujući indirektnu spregu sa ekonomajzerom, razmenjivač toplote usisne pare, pothlađivač i povećanje površine kod isparivača i kondenzatora), što nije slučaj u prethopdnim poređenjima ovog tipa.  Apsorber i desorber u CAHP su modelirani kao vertikalni dobošasti razmenjivači toplote. Glavni rezultati ove uporedne analize su sledeći: (1) koeficijent grejanja CAHP je dobar kao i kod CHP kada su klizanje temperatura ponora i izvora toplote 10K; (2) kada se klizanje temperature ponora i izvora toplote povećava na 20K, CAHP ima bolje performanse za 12%; i (3) veći porst temperature i veći temperaturski nivo daju relativno loš koeficijent grejanja kao CAHP. Za CAHP su predloženi neki projektni parametri za povećanje koeficijenata grejanja koje treba još proučavati.

##plugins.themes.bootstrap3.article.details##

Kako citirati
HULTEN, Magnus; BERNTSSON, Thore. Kombinovani kompresiono-apsorpcioni ciklus - uticaj nekih važnih parametara na koeficijent grejanja i poređenje sa kompresionim ciklusom. KGH – Klimatizacija, grejanje, hlađenje, [S.l.], v. 30, n. 2, p. 63-74, nov. 2016. ISSN 2560-340X. Dostupno na: <https://izdanja.smeits.rs/index.php/kgh/article/view/766>. Datum pristupa: 08 oct. 2026
Sekcija
Tematski članci

Reference

[1] Osenbruck, A.: Verfaren Kalteerzeugung bei Absorptionsmaschinen, Deutsches Patent, 1895.
[2] Brunin, O., M. Feidt, B. Hiver: Comparison of the working domains of some compression heat pumps and a compression-absorption heat pump, Int. J. Refrig. 20(5),1997, pp. 308-318.
[3] Ahlby, L., D. Hodgett: Compression-absorption heat pumps. In: Proc. of the 3rd International Energy Agency Heat Pump Conference, Tokyo, 1990.
[4] Itard, L. C. M., Machielsen, C. H. M.: Design of a wet compression-resorption heat pump with the mixture NH3/H20, In: International Absorption Heat Pump Conference, 1996, pp. 709-716.
[5] Brunin, O. : Pompe a chaleur a compression-absorption; Etude et realisation experimentale, Mechanique Energetique, PhD thesis, Henri Poincare -Nancy 1, Nancy, 1995, pp. 208.
[6] Sveine, T., S. Grandum, H. S. Baksaas: Design of high temperature absorption/compression heat pump, Natural Working Fluids '98, IIR -Gustav Lorentzen Conference, Oslo, 1998, pp. 491-500.
[7] Ziegler, F., U. Spindler: An ammonia refrigerator with an absorption circuit as economizer, Int. J. Refrig., 16(4), 1993, pp. 230-239.
[8] Mehendale, S. S., R. Radermacher: Simulation of hybrid heat pumps with two-and three-stage solution circuits for high-lift applications, ASHRAE Trans. 102(1), 1996, pp.1101-1109.
[9] Ahlby, L., D. Hodgett, R. Radermacher: NH3/H20-LiBr as working fluid for the compression absorption cycle, Int. J. Refrig. , 16 (4), 1993, pp. 265-273.
[10] Schnitzer, H., T. Berntsson: Improvement of COP of compressing heat pumps through the use of nonazeotropic mixtures, Papers presented at the Second International Symposium on the Large Scale Applications of Heat Pumps, York, 1984, pp. 13-20.
[11] Ahlby, L., D. Hodgett, T. Berntsson: Optimization study of the compression/absorption cycle, Int. J. Refrig. 14(1), 1991, pp. 16-23.
[12]Itard, L C. M.: Wet compression versus dry compression in heat pumps working with pure refrigerants or non-azeotropic mixtures, Int. J. Refrig., 18(7), 1995, pp. 495-504.
[13] Hewitt, N. J., J. T. McMullan, G. Molyneaux: Design aspects and applications of resorption cycles, Sci. Tech. Froi, 3, 1996, pp. 347-350.
[14]Itard, L. C. M., C. H. M. Machielsen: Parameter study for the optimization of a wet compression hybrid cycle for the working pair NH3/H20, In: Proc. of the International Absorption Heat Pump Conference, New Orleans, 1994, pp. 17-24.
[15] Stokar, M., C. Trepp: Compression heat pump with solution circuit, Part 1 : Design and experimental results, Int. J. Refrig. 10(2), 1987, pp. 87-96
[16] Hogberg, M.: Non-azeotropic mixtures as working fluids in heat pumps: a theoretical and experimental study, PhD thesis, Department of Heat and Power Technology, Chalmers University of Technology, Gothenburg, 1995, p. 124.
[17] Hogberg, M., L. Vamling: Impact of uncertainties on estimations of heat pump cycle performance, Int. J. Refrig., 19(1), 1996, pp. 34-42.
[18] Thorin, E.: Ammonia-water mixture as working fluid in power cycles, Licentiate thesis, Department of Chemical Engineering and Technology/Energy Processes, Royal Institute of Technology, Stockholm, 1998
[19] Reid, R. C., J. M. Prausnitz, B. E. Poling, In: Sun B, Fleck GH, editors, The properties of gases and liquids, 4th ed. McGraw-Hili, New York, 1987
[20] Taborek, J., editor: Heat exchanger design handbook, Shell-and-tube heat exchangers: single-phase flow, Hemisphere Publishing, 1994.
[21] Niederhauser, T., C. Trepp: Heat and mass transfer in water-ammonia falling films in smooth and rough tubes, Warme Stoffubertragung/Thermo-and Fluid Dynamics, 29(4),1994, pp. 251-264.
[22] Asblad, A., T. Berntsson: Surface evaporation of turbulent falling films, Int. J. Heat Mass Transfer, 34(3) , 1991, pp. 835-841.
[23] Marsh, W. F., I. Mudawar: Predicting the onset of nucleate boiling in wavy free-falling turbulent liquid films, Int. J. Heat Mass Transfer, 32(2), 1989, pp. 361-378.
[24] Berntsson, K. M.: Nonazeotropic mixtures as working fluids in large heat pumps - heat transfer in a falling film evaporator and system simulations, PhD thesis , Department of Heat and Power Technology, Chalmers University of Technology, Gothenburg, 1986, p. 226.
[25) McNaught, J. M., D. Butterworth, editors: Heat exchanger design handbook. Fluid mechanics and heat transfer, Hemisphere Publishing, 1994.
[26] Sajjan, D.: Personal communication, Chalmers University of Technology, Department of Heat and Power Technology, Sweden, 1997.
[27] Pamlin, R.: Personal communication, Svenska rotormaskiner (SRM), Sweden, 1997.
[28] Gabrielli, C., L. Vamling: Changes in optimal distribution of heat exchanger area between the evaporator and suction gas heat exchanger when replacing R22 with R407C, Int. J. Refrig., accepted.
[29] Gabrielli, C., L. Vamling: Replacement of R22 in tube-and-shell condensers: Experiments and simulations, Int. J. Refrig., 20(3), 1997, pp. 165-178.
[30] Hogberg, M., T. Berntsson: Non-azeotropic mixtures as working fluids in two-stage economizer-type heat pumps, Int. J. Refrig., 17(6), 1994, pp. 417-429.
[31] Itard, L. C. M., C. H. M. Machielsen: Considerations when modelling compression/resorption heat pumps, Int. J. Refrig., 17(7), 1994, pp. 453-460.
[32] Hogberg, M., L. Vamling, T. Berntsson: Calculation methods for comparing the performance of pure and mixed working fluids in heat-pump applications, Int. J. of Refrig., 16(6) , 1993, pp. 403-413.
[33] Mclinden, M. O., R. Radermacher: Methods for comparing the performance of pure and mixed refrigerants in the vapour compression cycle, Int. J. Refrig. 10(6), 1987, pp. 318-325.
[34] Herold, K. E., R. Radermacher, S. A. Klein: Absorption cycle fundamentals, Absorption chillers and heat pumps, CRC Press, 1996, p. 9.
[35] Saffar-Avval, M., E. Damangir: A general correlation for determining optimum baffle spacing for all types of shell and tube exchangers, Int. J. Heat Mass Transfer, 38(13), 1995, pp. 2501-2506.
[36] Ramananda, Rao K., U. Shrinivasa, J. Srinivasan: On the weak coupling between geometry and heat transfer in heat exchanger optimization, Chem. Eng. Res. Des. A, 70(6), 1992, pp. 565-571.
[37] Jegede, F. O ., G. T. Polley: Optimum heat exchanger design, Chem. Eng. Res. Des., 70(2), 1992, pp. 133-141.
[38] Brocheriou, F.: Design improvements of an ammonia-water compression-absorption heat pump, Diploma work, Department of Heat and Power Technology, Chalmers University of Technology, Gothenburg, 1998.
[39] Ahlby, L., D. Hodgett: Compression/absorption systems -Simulation of two cycles for different applications, In: Proc. of XVIIth International Congress of Refrigeration, Vienna, 1987, pp. 785-792.