SAVING ENERGY THROUGH IMPROVING CONVECTION IN A MUFFLE FURNACE. Alina Adriana MINEA and Adrian DIMA

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THERMAL SCIENCE: Vol. 12 (2008), No. 3, pp. 121-125 121 SAVING ENERGY THROUGH IMPROVING CONVECTION IN A MUFFLE FURNACE by Alina Adriana MINEA and Adrian DIMA Orig i nal sci en tific pa per UDC: 536.331:66.046 BIBLID: 0354-9836. 12 (2008), 3, 121-125 DOI: 10.2298/TSCI0803121M In com press ible forced con vec tion heat trans fer prob lems nor mally ad mit an ex - tremely im por tant sim pli fi ca tion: the fluid flow prob lem can be solved with out ref - er ence to the tem per a ture dis tri bu tion in the fluid. Thus, it can first find the ve loc ity dis tri bu tion and then put it in the en ergy equa tion as known in for ma tion and solve for the tem per a ture dis tri bu tion. In this pa per it is in tended to ex pand the the o retic re searches con cern ing heat pro - cesses in ten si fi ca tion and their use in in dus trial prac tice. In con clu sion the fun da - men tal re search with con crete tech ni cal ap pli ca tions rep re sents a sig nif i cant con - tri bu tion to the de vel op ment of knowl edge in do main. By cen tral iz ing the ex per i men tal re sults, there can be said that there has been ob tained an en er getic sav ing of ap prox i mate 20% by us ing ra di ant pan els. By fit - ting the ex per i men tal data there has been ob tained an op ti mum of the pan els po si - tion ing of x = 118.71 mm. In con clu sion, chang ing the work ing space by in tro duc ing some ra di ant pan els in - side the fur nace leads to im por tant en ergy sav ings in the heat ing pro cess, by in creas ing the heat ing rate of charge and by de creas ing its res i dence time in the ther mal equip ment. Key words: convection, fluid flow, applications, furnace Back ground The crit i cal anal y sis of the in ten si fi ca tion tech niques of the trans fer pro cesses is re al - ized by the very iden ti fi ca tion of the meth ods that can be ap plied, re gard less of the pro cess na - ture. In this con text, the study of the heat trans fer pro cesses has be come an es sen tial thing for en sur ing an op ti mum func tion ing of the in dus trial heat ing pro cesses and this fact cre ates the base of the multidisciplinary study of these pro cesses. The main pri or ity is the de vel op ment of a con sis tent meth od ol ogy that will rep re sent the base of the spe cific prac ti cal meth ods de vel op - ment [1, 2]. Our aim in this pa per is to pres ent the anal y sis of a few prob lems and to show the pro - gres sion to ward in creas ingly em pir i cal so lu tions as the prob lems be come pro gres sively more un wieldy. As in any forced con vec tion prob lem, it first de scribes the flow field. The ve loc ity pro file changes greatly near the in let to the wall. A bound ary layer builds up from the front, gen - er ally ac cel er at ing the oth er wise un dis turbed core. The bound ary layer even tu ally oc cu pies the en tire flow area and de fines a ve loc ity pro file that changes very lit tle there af ter.

122 Minea, A. A., Dima, A.: Saving Energy through Improving Convection in a Muffle Furnace Dur ing this ex per i men tal study, dif fer ent study cases have been care fully cho sen in or - der to com pare and mea sure the ef fects of ap ply ing dif fer ent in ten si fi ca tion meth ods of the heat trans fer pro cesses. The study cases have also been cho sen ac cord ing to the tech no log i cal needs for cer tain pro cesses that re quire heat at av er age tem per a tures in op ti mum con di tions [3]. Meth od ol ogy Es tab lish ing the re search di rec tions has been per formed by a crit i cal anal y sis of the in - ter ven tion pos si bil i ties over the heat ing pro cesses at av er age tem per a tures. Thus, for the study of trans fer pro cesses ef fi ciency there has been cho sen a muf fle fur nace of ther mal treat ment, pre - sented in fig. 1. This is a Vul can fur nace, muf fle type, with ver - ti cal door drive which as sures a good seal ing of the work ing space as well as dif fer ent heat ing rates due to the ex tremely ef - fi cient con trol ler. The fur nace has a very good pro duc tiv ity and as sures a great se cu rity when ex ploited due to the heat ing cy cles that can be au to mat i cally pro grammed and op er ated. Af ter pro gram - ming, the heat ing pa ram e ters re main reg is tered in the pro gram mem ory even if in ter rup tions oc cur in elec tri cal power sup ply - ing. The work ing method pro posed for study ing the con struc - tive and func tional im prove ment of the oval fur nace used at av - er age tem per a tures has the fol low ing steps: Fig ure 1. Gen eral view of the fur nace choosing a charge pattern and a technological process, choosing a heating temperature, changing the working space by using some adjustable radiant panels, and performing the experiment and interpreting analytically the results. Programming the experiment In or der to per form the heat ing pro cess op ti mi za tion there has to be es tab lished ex actly the ther mal in ter val that shall rep re sent the ba sis of the ex per i men tal con di tions [4, 5]. The se lec tion of the heat ing tem per a ture has been per formed ac cord ing to the usual ther mal field for so lu tion heat treat ment by putt ing the alu mi num al - loys at a tem per a ture of 400-500 C. Chang ing the work ing space, as it is pre sented in fig. 2, has as pur - pose the heat trans fer in ten si fi ca tion by con vec tion and ra di a tion. The con vec tion in side the work ing cam era suf fers ma jor changes by re-dimensioning power lines and trans form ing the nat u ral con vec tion in forced con vec tion by mod i fy ing the air cir cu la tion rate in side the fur nace. In this case, we do not talk any more of a smooth mix ing move ment of air, the air Fig ure 2. Plac ing the ra di ant pan els in side the work ing area of the fur nace be ing di rected by the in clined pan els to wards the charge and main tained near it. Be sides the mod i fied

THERMAL SCIENCE: Vol. 12 (2008), No. 3, pp. 121-125 123 con vec tion, the phe nom e non that rep re sents the ba sis of heat ing is the ther mal ra di a tion to wards the part and the air near it. In or der to ac com plish the de sired math e mat i cal mod el ing, the ex per i ment has to be pro grammed and this im plies the fol low ing: establishing the necessary and sufficient number of experiences and the necessary conditions in order to accomplish them, establishing the regression equation which represent the process model, and establishing the conditions necessary to accomplish the optimum value of the process performance fulfilled. In this con text, for each vari able, there have been es tab lished the ba sic lev els as well as the vari a tion in ter vals. By add ing the vari a tion level to the ba sic level there has been ob tained the su pe rior level, and by de creas ing it the in fe rior level of the vari able. Choos ing the vari a tion in ter val must of fer the most ac cu rate val ues from the func tional point of view. A first step is to es tab lish the ba sic lev els and the vari a tion in ter vals. In tab. 1, the vari a tion in ter val and the ba sic level for pro gramming the experiment are presented. The in ter pre ta tion of the ex per i men tal re sults con sists of es tab lish ing the ex per i - men tal vari a tion curves of the ra di ant pan - els po si tion ac cord ing to en er getic con - sump tion of the equip ment; the interpretation of the ex per i men tal re sults shall be fi nal ized by de ter min ing the an a lyt i cal equa tions that de scribe the ex per i men tal curves ob tained. Experimental The ac tive ex per i ment has started with a pre lim i nary ex per i ment per formed in or der to es tab lish the en er getic ef fi ciency of us ing the ra di ant pan els. Thus, there has been cre ated a di a - gram of the stud ied fur nace run ning idle. Af ter wards, the ra di ant pan els have been in tro duced in the fur nace and dra matic de - crease of the heat ing time has been no ticed. The ex per i men tal re sults shall not be pre sented un der a graphic form. Thus, tab. 2 rep re sents the fur nace heat - ing re gime for all the ex per i men tal cases. In ad di tion, there have been con - ducted some re searches con cern ing other ma jor pa ram e ters in the in dus trial fur naces func tion ing, like en ergy con - sump tion. The to tal en ergy con sumed when heat ing has been cal cu lated by Table 1. Experiment programming Fac tor Ba sic level Vari a tion in ter val Pan els ad just ment dis tance, x [mm] 140 mm 20 mm Superior level (+1) 160 mm In fe rior level ( 1) 120 mm Supplementary 200 mm Ta ble 2. Ex per i men tal re sults for heat ing up to 400 C Pan els' distance Heat ing time [s] Energy [Wh] 200 1070 535 160 964 482 140 973 486.5 120 940 470 tak ing into con sid er ation the func tion ing time at a max i mum power of the equip ment, hav ing in mind the re la tion E = Pt.

124 Minea, A. A., Dima, A.: Saving Energy through Improving Convection in a Muffle Furnace Experimental data analysis The ex per i ment has been rig or ously con ducted in or der to as sure its re peat abil ity. As a study charge, a cy lin dri cal part of the fol low ing di men sions 15 x 100 mm, made of AlCu4Mg1 has been used. The ex per i ments have been per formed in dif fer ent days, thus main tain ing the ini tial heat ing con di tions for equip ment as well as for charges. The data col lec tion has been per formed with the help of the com puter by a Nomadics ther mo cou ple ac qui si tion sys tem. For each panel po si tion three ex per i ments were con ducted, in the ta bles be ing writ ten the arith me tic av er age of the reg is tered val ues. In tab. 2 the re sults for the cen tral ized ex per i ments are pre sented for all the sit u a tions. The in ter pre ta tion of the re sults has as pur pose find ing a math e mat i cal model that can de scribe as pre cisely as pos si ble the phys i cal pro cesses that take place in that sit u a tion. Thus, in fig. 3 the ex per i men tal curves and the poly no mial fit ted curves are pre sented for sav ing en ergy study. Fig ure 3. The vari a tion di a gram of the con sumed en ergy with the pan els po si tion Thus, af ter the anal y sis and the math e mat i cal in ter pre ta tion of the ex per i ments data we have ob tained the re gres sion equa tions: E = 0.0093x 2 2.208x + 605 R 2 = 0.9422 (1) The re gres sion was ob tained by least squares method (with R 2 as mean of square er ror) and rep re sents a cor re la tion be tween panel po si tion (x) and en ergy (E). So, eq. (1) serves for the cor re la tion of the work ing space form with the tech no log i cal ob jec tives of the alu mi num al loys heat ing and is con sid ered to be the most im por tant, of fer ing pre cise quan ti ta tive in for ma tion re - gard ing the en ergy sav ing that is ob tained with the help of the pro posed so lu tion con cern ing the chang ing of the work ing space. In this case, an in ter pre ta tion has been done fol low ing this equa - tion. Thus, eq. (1) ad mits a min i mum in the fol low ing point: x = 118.71 mm (2)

THERMAL SCIENCE: Vol. 12 (2008), No. 3, pp. 121-125 125 Con clu sions The cho sen re search meth od ol ogy al lows the per for mance of the ex per i ments in or der to study the en er getic con sump tion of the cho sen heat ing equipments by: adopting the proper thermal processing technology for the study charge, choosing a high quality furnace with the help of which the heating process for the performed operations can be controlled, changing the efficiency of the working space, and performing the active programmed experiment and the possibility of interpreting analytically the results. Af ter cen tral iz ing the re sults, we can say that: there has been obtained an energetic saving of 11.32% by using the radiant panels, and by fitting the experimental data there has been obtained an optimum of the panels positioning of x = 118.71 mm. In con clu sion, chang ing the work ing space by in tro duc ing some ra di ant pan els in side the build ing leads to im por tant en ergy sav ings in the heat ing pro cess, by in creas ing the heat ing rate of charge, and by de creas ing its res i dence time in the fur nace. Acknowledgment These stud ies were pos si ble through a na tional grant spon sored by NURC Ro ma nia, ct. 81/2007. Ref er ences [1] Minea, A. A, Mass and En ergy Trans fer, Editura Cermi, Iasi, Ro ma nia, 2005 [2] Minea, A. A., Sandu, I. G, Heat Treat ing Op ti mi za tion on AlCuMg Alu mi num Al loy, Revista de Chimie, 6 (2006), 57, pp. 586-590 [3] Minea, A. A., Met al lur gi cal Im pli ca tions of Heat Treat ing of Alu mi num Al loys in Elec tri cal Fur naces, Pro ceed ings, Na tional Con fer ence of Met al lurgy and Ma te rial Sci ence ROMAT, Bu cha rest, 2006, pp. 311-315 [4] Stoecker, W. F., De sign of Ther mal Sys tems, 3 rd ed., McGraw-Hill, New York, USA, 1989 [5] Jaluria, Y., Lombardi, D., Use of Ex pert Sys tems in the De sign of Ther mal Equip ment and Pro cesses, Res. Eng. Des., 2 (1991) 4, pp. 239-253 Authors' address: A. A. Minea, A. Dima Technical University Gh. Asachi, Str. C. Negri no.62, code 700070 Iasi, Romania Corresponding author A. A. Minea E-mail: aminea@tuiasi.ro Paper submitted: January 30, 2008 Paper revised: April 4, 2008 Paper accepted: April 18, 2008