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HEAT EXCHANGE BLOCK FOR REGENERATIVE BURNER

https://doi.org/10.17073/0368-0797-2017-8-643-650

Abstract

 Modern regenerative burners for heating and thermal furnaces  have rather larger sizes and small heat exchange period time that is  connected with a low thermal capacity of the refractory materials  applied to production of a nozzle. Considerable decrease in the sizes  of nozzle and increase in heat exchange period time can be reached  by using the hidden warmth of metals melting, which can be placed  in the closed thin-walled reservoirs. In addition, the paper propose  section design and a heat exchange unit enable to solve the problem  of reducing the size of regenerative unit and increase the time of the  swap, compared to existing regenerators that are used for air heating  in regenerative burners. The proposed design can be used to create  regenerative burners, a new class of highly effective, high temperature air preheating, and considerable time of swap. Such reservoirs,  in which temperature of metal melting is equal, are packed in the sections. The next sections’ melting temperature differs approximately by 100  °C. It allows to maintain the fixed section temperature, which  is equal the temperature of metal melting in this section, and removing from its surface or giving it, by products of combustion, warmth,  which sets out in case of crystallization or is absorbed when metal  kernel melts. Calculation of the swap time and the metal mass in one  section, based on the joint solution of equations of heat balance and  heat transfer between the heated air and the surface of tanks, allows  to determine the overall dimensions of each section, filled with melting or crystallizing metal and its heat exchange surface. Fusible kernel mass, sizes of section and heat exchange period time calculations  for regenerative block consisting of ten sections with a fusible kernel  is given in this work. Calculation proves a possibility of decrease in  dimensions of a regenerative nozzle for a 200 kW burner, and increase in heat exchange period time, while air heating temperature  remains constant. The technical solution can be used in a thin-walled  container in which are placed the metals with different heat of fusion. Large size regenerative burners hamper their use in heating and  thermal furnaces, and fast parecidos leads to a decrease in period of  operation of the changeover valve.

About the Authors

D. M. Druzhynin
OJSC “Scientific Research Institute of Metallurgical Heat Engineering” (“VNIIMT”); Ural Federal University named after the first President of Russia B.N. Yeltsin.
Russian Federation

Dr. Sci. (Eng.), Deputy Director for Science, Professor of the Chair “Thermal Physics and Informatics in Metallurgy”. 

 Ekaterinburg.



N. B. Loshkarеv
Ural Federal University named after the first President of Russia B.N. Yeltsin.
Russian Federation

Cand. Sci. (Eng.), Assist. Professor of the Chair “Thermal Physics and Informatics in Metallurgy”. 

Ekaterinburg.



A. N. Loshkarеv
Ural Federal University named after the first President of Russia B.N. Yeltsin.
Russian Federation

Senior Lecturer of the Chair “Thermal Physics and Informatics in Metallurgy”. 

Ekaterinburg.



A. Kh. Mukhamadieva
Ural Federal University named after the first President of Russia B.N. Yeltsin.
Russian Federation

 MA Student of the Chair “Thermal Physics and Informatics in Metallurgy”. 

Ekaterinburg.



D. F. Muksinov
Ural Federal University named after the first President of Russia B.N. Yeltsin.
Russian Federation

 MA Student of the Chair “Thermal Physics and Informatics in Metallurgy”.

Ekaterinburg.



References

1. Biryukov A.B. Modern aspects of use of regenerative burners for  heating of blast furnaces. Chernaya metallurgiya. Byul. in­ta “Chermetinformatsiya”. 2015, no.11, pp. 31–36. (In Russ.). 

2. Contarin F., Barcellos W.M., Saveliev A.V., Kennedy L.A. Energy  extraction from a porous media reciprocal flow burner with embedded heat exchangers. Journal of Heat Transfer. 2005, vol. 127,  no.  2, pp. 123–130.

3. Contarin F., Barcellos W.M., Saveliev A.V., Kennedy L.A A porous  media reciprocal flow burner \with embedded heat exchangers. In:  Proceedings of the 2003 ASME Summer Heat Transfer Conference, Las Vegas, Nevada, USA, July 21–23, 2003, vol. 2, pp. 35–42. 

4. Chatys R. Bloom reheating with regenerative burners. Steel Times.  2000, vol. 228, no. 2, pp. 65. 

5. Orman  L.J.  NKK’s  low  NOx  energy  regenerative  burner.  Steel Times. 2000, vol. 228, no. 2, p. 62. 

6. Malcho M. Evaluating low NOx burners. Steel Times. 2000, vol.  228,  no. 2, pp. 64–65.

7. Rafidi N., Blasiak W. Heat transfer characteristics of hitac heating  furnace using regenerative burners. Applied Thermal Engineering. 2006, vol. 26, no. 16, pp. 2027–2034.

8. Nellis G.F., Klein S.A. Regenerative heat exchangers with significant entrained fluid heat capacity. International Journal of Heat and Mass Transfer. 2006, vol. 49, no. 1-2, pp. 329–340.

9. Saastamoinen J.J. Heat transfer in crossflow regenerators. International Journal of Heat and Mass Transfer. 1999, vol. 42, no. 17.  P.  3205–3216.

10. Erk H. F., Dudukovic M. P. Phase-change heat regenerators: modeling and experimental studies. Aiche Journal. 1996, vol. 42, no. 3,  pp. 791–808.

11. Mitrovic J., Stephan K. Mean fluid temperatures in direct contact  heat exchangers without phase change. International Journal of Heat and Mass Transfer. 1996, vol. 39, no. 13, pp. 2745–2750.

12. Chatys R., Orman L.J., Malcho M. Heat transfer enhancement  in phase-change heat exchangers. Aviation. 2014, vol. 18, no.  1,  pp.  40–43.

13. Radchenko N. A concept of the design and operation of heat exchangers with change of phase. Archives of Thermodynamics. 2004,  vol. 25, no.4, pp. 3–18.

14. Gordon Ya.M., Shvydkii V.S., Sovetkin V.L., Yaroshenko Yu.G. Regenerativnyi teploobmennik [Regenerative heat exchanger]. Certificate of authorship USSR no. 1 366 791. Byulleten’ izobretenii. 1988,  no. 2. (In Russ.).

15. Zobnin  B.F.,  Kazyaev  M.D.,  Kitaev  B.I.,  Lisienko  V.G.,  Telegin  A.S., Yaroshenko Yu.G. Teplotekhnicheskie raschety metallurgicheskikh pechei: uchebnoe posobie dlya studentov vuzov [Thermal  technical calculations of metallurgical furnaces: Manual for universities]. Moscow: Metallurg, 1982, 360 p. (In Russ.).

16. Gol’dfarb E.M., Kravtsov A.F., Radchenko I.I. Raschety nagrevatel’nykh pechei [Calculations of heating furnaces]. Taits N.Yu. ed. Kiev:  Gosudarstvennoe izdatel’stvo tekhnicheskoi literatury USSR, 1958,  420 p. (In Russ.).

17. Fizicheskie svoistva stalei i splavov, primenyaemykh v energetike: Sprav. [Physical properties of steels and alloys for energy industry:  Reference book]. Neimark B.E. ed. Moscow-Leningrad: Energiya,  1967, 240 p. (In Russ.).

18. Timoshpol’skii V.I. Teplotekhnicheskie osnovy metallurgicheskikh protsessov i agregatov vysshego tekhnicheskogo urovnya [Fundamentals of metallurgical heat engineering processes and units of the  highest technical level]. Moscow: Nauka i tekhnika, 1995, 296 p.  (In Russ.).

19. Timofeev V.N., Karasina E.S. Izluchenie gazov (nomogrammy)  [Emission gases (nomograms)]. Izd. VTI, 1948, no. 9–10. (In Russ.).

20. Idel’chik  I.E.  Spravochnik po gidravlicheskim soprotivleniyam [Reference  book  on  hydraulic  resistances].  Moscow-Leningrad:  Gosudarstvennoe  energeticheskoe  izdatel’stvo,  1960,  465  p.  (In  Russ.).


Review

For citations:


Druzhynin D.M., Loshkarеv N.B., Loshkarеv A.N., Mukhamadieva A.Kh., Muksinov D.F. HEAT EXCHANGE BLOCK FOR REGENERATIVE BURNER. Izvestiya. Ferrous Metallurgy. 2017;60(8):643-650. (In Russ.) https://doi.org/10.17073/0368-0797-2017-8-643-650

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ISSN 0368-0797 (Print)
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