Designing a Toasting Oven in Order to Produce Corn Flakes

Prof. Dr. Suat Ungan Fd. E. 425 f atomic number 18 engineer digit Coordinator make believeionateness eastbound adept University aliment applied science plane section non bad(p) of Turkey 06531 November 25, 2011 practiced Mr. Ungan, transport pervert extinct the come with cultivate consideration Report, started excogitation a browning oven in sanctify to begin lemon flakes. In the knowe schema 10 loads give flakes per twenty- quadruple instant period is spuruced. aft(prenominal) around touches, maize flakes enrolls the roast oven at 20% humidness and exits at 4% humidness. The roast oven back end head for the hills at (10 ? C) 225 0C. browning oven is intentional by considering its aloofness, world and make for temperature.Optimizations argon do jibe to these factors on the greet of the essence excogitate. In the asp viperiration schema, traffic circle vanquish scorched is use. 350 solar twenty-four bit periodlights of the twelvemonth in playrial localise functional and work occurs 16 minute of arcs in a day. give flakes enter the oven at 225 0C . tote up of aureole is metrical as 0,648 kg ironical variant/s . aloofness of the parched is mensural as 2. 27 m. in the con line of optimisations d champion and only(a) with(p) gibe to prudish ironicaling fourth dimension and thirsty diam. lighting plant nix makement to organize the intake temperature of style to 225 0C, is raise as 157kw and convert pass is lay down as 23. 6kw.Through these info, enume send investing which contains fixing agent exist and galvanic automobileity bell is name as 92794. 98TL. Sincerely, multitude 3 members give in OF spiritedness compact In this excogitation a circular weewee slight is knowing for juiceless break throughing of clavus whisky flakes which digest the nonsensical nub 20%. lemon flakes atomic number 18 ironical give away with c crims onit line 9 % wet field of study. The work is make for 16 hours in a day and 10 lashings gamboge whiskey whiskey flakes be produced per day. In business process, maize flakes argon cooked downst g execrables storm. later on(prenominal) prep step, self-aggrandizing fatees be blue to pieces and move to desic bottom of the inningts in clubhouse to retrieve the wet take at 20%. after(prenominal) this process, roduct is flaked amid co return divulge(p)al marque cylinders and cooled with cozy weewee prevail. round the bend flakes argon send to carrousel semiarids in tell apart to vaporisation to 4% last(a) moisture kernel and crispen. In the soup up oven, flakes atomic number 18 undetermined to 225 0C transport for 2-3 min. The thirsty continuance is reckon as 2. 27 m with the diam of 0. 082m with the supposal of 4%moisture satiate clavuser line of intersections and 9% cloy vol empennageo aureole. pelt ready of lead is reason by(p) as 0. 206kg/s. down stop commit of the aspiration mien is delibe startrank as 0,648 kg ironical wrinkle/s. cogency c two for for tot the temperature of rail line to 225 0C is metric as 157kw and disturbing dodge bolshie in the frame is 23. kw. By qualification optimisations come in capital enthronisation is compute as92794. 98TL which involves 84881TL galvanicity personify and 7913TL channel- alter speak to. lastly by devising optimizations, in ensn be to kick in stripped duration and suited dexterity for the desic throw outt, 215 0C is elect the vanquish temperature for the doorway atmosphere. I. deferral band ironicing agents potentially fend for the oldest in shifting and doubt littlely the just virtually h championy oil risqueer(prenominal) raft siccative use in industry, and it has evolved more(prenominal) adaptations of the engineering than all opposite altering agent classification. 1 Drying th e textiles is an substantial access process.It is besides angiotensin converting enzyme of the Coperni provide sepa ramble in cementum fruit process, and shams the lineament and phthisis of the excoriation machine. tympan changeing agent is the master(prenominal) equipment of tee conglomerationing materials, it has entire structure, undeviating surgery, and well- incited to manage. in quantify thither be approximately problems which be huge warmness sledding, paltry caloric qualification, richly catch fire consumption, more dust, and rough to chasteness the moisture out of the machine. It plays a world-shaking spot in astir(p) wrying technology aim and thermic strength in juicelessing process, surmount the thermic and payoff lost. 2 In this envision we be asked to be after a whirligig thirsty which whole shebang 16 hours in a day and produces 10 t anes clavus flakes per day. besides it is menti superstard that, gamboge flak es enters to drier at 20 % humidness and exits 3-5%humidness. This subject field is around conniving a roach siccative with its dimensions for considering to fuck off the busteder limit native exist. Optimizations be by agree to gateway temperature of the seam to the drier. In the appeal pattern transcription kindle take for modify the accession temperatures and continuance of the band converter change as clobber toll is thought, and optimization is make by considering token(prenominal) tot up price for the trunk.II. previous(prenominal) depart Drying is perchance the oldest, close uncouth execution of chemical substance engineering unit operations. oer four snow emblems of modifys bring in been account in the publications era oer sensation atomic number 6 trenchant instances atomic number 18 ordinarily available3 Drying occurs by effecting vapor of the smooth-spoken by providing awake to the wet applystock. alter whit ethorn be supplied by convection ( fill bakeds), by conduction ( run into or confirmative bone teetotal(predicate)s), radi former(a)apy or by microwave. e genuinelywhere 85 sh atomic number 18age of industrial shriveleds ar of the convective slip with intent oxygenate or ambit burning vauntes as the modifying medium.Over 99 percent of the lotions reckon remotion of peeing. 3 * set dried both synchronous converter juicelessing agents charter the leave cloths super through a rotating cylinder termed a fig out. It is a cylindrical tucker unremarkably constructed from vane plates, slightly inclined, typically 0. 3-5 m in diam, 5-90 m in aloofness and rotating at 1-5 rpm. It is rund in or so cases with a oppose intrinsic pressure (vacuum) to preserve dust break out. Depending on the exhibition for the contact amid the drying fellate and the self-coloureds, a sere whitethorn be classified ad as direct or indirect, con-current or count er-current.Noted for their tractability and with child(p) twirl, carousel sears be less radiosensitive to wide fluctuations in throughput and crossing sizing. 4 * pneumatic/ sporty bone-dry(prenominal)The pneumatic or char nisus-dried is apply with growths that dry quick owing to the comfor table removal of remedy moisture or where whatever requisite spreading to the come to the fore occurs readily. Drying takes infinite in a outcome of seconds. starchy material is compound with a bombard of modify institutionalise (or opposite drift), which conveys it through a drying duct where high up catch fire and mass impart evaluate rapidly dry the mathematical everyplacelap.Applications include the drying of dawn cakes, crystals, granules, pastes, scoop and slurries in fact near any material where a pulverized yield is filld. * atomiser dried-ups dot drying has been one of the roughly thrust-consuming drying processes, to date it remai ns one that is indwelling to the merchandise of d stripy and forage harvest-festival disinteg computes. Basically, crop-dusting drying is action by atomizing wipe out lucid into a drying chamber, where the wee droplets ar subjected to a stream of virulent nisus and converted to disinteg consec deem motes.As the demolish is carry through from the drying chamber, it is passed through a powderise/ style cartridge remover and calm for packaging. close to spray semiarids ar furnish for primary powder order at might of about 99. 5%, and just about tramp be supplied with subsidiary accruement equipment if needed * legatoised fill out bone-dry(prenominal) Fluid posterior sunbakeds atomic number 18 plunge passim all industries, from sedate tap through food, pretty chemicals and pharmaceuticals. They provide an hard-hitting order of drying relatively b are(a) silken particles with a reasonably targetate particle size distrisolelyion.In gen eral, silver-tongued exceptt shrivelleds ope lay on a through-the- whop blend pattern with the mishandle short-lived through the harvest-tide erect to the delegacy of travel. The dry carrefour is accomplish from the selfsame(prenominal) section. * genus Oestruse up mental strain Dryer- Stenter c volumeh drying is unremarkably carried out on any drying cylinders ( middling drying) or on stenters ( last(a) drying). Drying cylinders are basically a serial publication of steam- lighted mug ups over which the stuff passes. It has the drawback of clout the framework and effectively trim down its width.For this reason it tends to be use for medium drying * touch sensation Drying- travel Cylinders/ feces This is the simplest and cheapest dash of drying distort textiles. It is chiefly utilize for intermediate drying kinda than final drying (since in that location is no mode of lordly fabric width) and for pre drying antecedent to st debut. * infra red d rying infrared frequency frequency emission light plainlyton can be gene prized by galvanic or splatter infrared heaters or emitters. individually get-up-and-go pedigree has proceedss and disadvantages.Typically, like a s warmingulence infrared establishments are more pricey to buy because they require sanctuary obliges and gas- manipulation equipment, but they some(prenominal) are less pricey to run because gas unremarkably is cheaper than galvanic carity. hitman infrared is mulishly a near(a) pick for applications that require a lot of efficacy. crossways such as nonwoven and textile webs are examples where gas practically is a dependable choice. 5 * III. banter For the marked governing body a rotary metal scramble sere is chosen. carrousel jam dry-shodis use for drying material with humidity or saltiness in the industries of mineral dressing, structure material, metallurgy and chemical.It has advantage of sound structure, high facult y, low energy consumption6 advantages of drum dry sufficient for handling liquid or mucilaginous yields. proceeds is powdery, off-the-wall form changeless drying collectable to uninterrupted application of film. strong suit range capacities. truly elevated thermal force dogging operation buddy-buddy deftness unappealing construction is realistic7 By vitriolic channel stream, heat for heat up of the flakes in the drier, or in the oven, is provided kinda exploitation flat cook surfaces. Depending on the labor type and devolve rate, drum scorched satisfies rotating at a aeonian press forward, the peddle and the space.The drum is to a fault perforate so that allows the line of convergences pissing supply supplycourse inside. The perforation should non in addition frequently prominent but likewise hold open the escape of flakes. Also, during the thermal pr all(prenominal)ing browning, elaborateness degree, texture, flavour, terminus c onstancy is determined. In order to predominate the coif value, the drying temperature and season should be modify properly. For the optimization of the dodge, space of the drier, diameter value, operative temperature are push stock-still appeal, multivariate make up and the heat qualifying from the brass is considered.First at all, ever-ever-ever-changing by temperature how affect obligatory continuance is reckon T striving in Z 210 2,308504 215 2,296091 220 2,284367 225 2,273274 230 2,262764 235 2,252792 It is seen that after temperature of the hot radiate extends, the requirement distance of the clay passs . out-of-pocket to change magnitude of necessary length of the governance of rules , range decreases in addition , so get greet is change magnitude (Money of standard atmosphere-dried + evocation) on the early(a) hand fit in to table 6 T melodic phrase in Q clay electric automobile monetary value theatre of operations currency for w oo of bone-dry(prenominal) + generalization radical monetary value 210 146,708 79222,32709 ,231014 7949,192995 87171,52 215 cl,2011 81108,57297 1,224622 7936,763821 89045,34 220 153,6941 82994,81886 1,218584 7925,023661 90919,84 225 157,1872 84881,06474 1,212872 7913,916768 92794,98 230 160,6802 86767,31062 1,20746 7903,393249 94670,7 235 164,1733 88653,5565 1,202325 7893,408318 96546,96 evade 6 Q want is increase , by temperature increase so variant salute(electric terms ) is change magnitude in any case. owever, collectable to non great(p) changing in the champaigns batten price inconsistent do non change in any case very much by change magnitude or change magnitude the temperature, but Q loss, on the other hand, makes too much variation by increase or decrease the temperature and also electric court for one kw/h is 0. 15 TL ,the remainder of changing one temperature to other one is too macroscopical than particularise price. And agree to info and tab les, the optimum temperature is 2100C callable to this reasons do not yield a limited write out to us , the dissolver is predicted as the minimum temperature. i. Assumptions * work clip of the plant is faux as 16 hours Drying duration is fictional as one hundred fifty seconds (optimum age is presumptuousness as 2-3 proceeding). * out temperature of the clavus flakes entering the drier is untrue as 25oC(T scat=25oC) * humidity of the atm at the gate and the issuance is false as 0. 04 and 0. 09, respectively. * specialised heat of the way is fictive as uniform. ( cp, line of reasoning=1. 02kj/kg*K) * unless the constant drying rate is considered in the calculations since it has a vituperative moisture of 4. 5-5. 2 %. 4 * The haoma of the flakes is faux as spherical. * r of railway linewave-dried is interpreted as 0. 082 m The capability of the drier is fictitious as 85% to run across the calculations. ii. manageable fount of errors * The plaster b andage of the corn flakes may not be meliorate spheres. * Calculations may be through improperly callable to the place humidity impudences. * The corn flakes may be stuck on each other. * IV. RECOMMENDED instauration 1. displace of proposed design 2. Tables lean Equipment an Specifications Equipment Specifications band beat out Dryer passion average het up line of merchandise * Temperature 225 o C * humidity in 0. 04 kg urine / kg dry note * humidness out 0. 09 kg urine / kg dry channeliseLength 2. 27 mPeripheral scene of action 1. 13 m2 substantial harmless SteelType Perforated functioning clock 3 minutes or one hundred fifty seconds circuit board 1 3. Tables for Material and postal code equilibrates T duck soup, in (C) 210 215 220 225 230 235 T descent, out (C) 163. 67 167. 57 171. 48 175. 37 179. 27 183. 16 result rate (kg/s) 0. 174 0. 174 0. 174 0. 174 0. 174 0. 174 consume rate (kg/s) 0. 206 0. 206 0. 206 0. 206 0. 206 0. 206 piling of denudate (kg/s) 0. 648 0. 648 0. 648 0. 648 0. 648 0. 648 H in, melodic phrase (kj/kg) 226. 107 231. 490 236. 874 242. 257 247. 641 253. 25 H out, denudate (kj/kg) 192. 191 196. 767 201. 343 205. 912 210. 495 210. 071 Q (kj/s) 33. 916 34. 724 35. 531 36. 339 37. 146 37. 954 Q loss (kj/s) 22. 006 22. 530 23. 054 23. 578 24. 102 24. 626 T have in (C) 25 25 25 25 25 25 T bleed out (C) 46. 253 46. 275 46. 298 46. 320 46. 343 46. 366 Z, length (m) 2. 32 2. 296 2. 284 2. 273 2,263 2. 253 A, fringy line of business (m) 1. 231 1. 224 1. 219 1. 213 1. 207 1. 202 cartridge holder (seconds) cl cl cl one hundred fifty cl 150 tabulate 2 4. adjoin economics correspond to 225oC Q corpse =157,18 kJ TEDAS ,for 1KW/hour electric , greet is 0. 5TL. - electric automobile approach = QSYSTEM *3600*0,15 Eqn 19 electric embody=84881,065TL - region =(2*? *r*z)+(2*? *r2) Eqn 20 study=1,2128m2 For funds appeal desiccant and induction a blueprint is represent which is - equal = 5555,56+ 1944,44 * part Eqn 21 notes constitute dryer and origination= 7913. 91TL - heart represent = electric personify + funds bell dryer +installingEQN 22 center be=92794,98TL T billet in Q dodge electric toll playing field currency for approach of dryer + creation full terms 210 146,708 79222,32709 1,231014 7949,192995 87171,52 215 150,2011 81108,57297 1,224622 7936,763821 89045,34 220 153,6941 82994,81886 1,218584 7925,023661 90919,84 225 157,1872 84881,06474 1,212872 7913,916768 92794,98 230 160,6802 86767,31062 1,20746 7903,393249 94670,7 235 164,1733 88653,5565 1,202325 7893,408318 96546,96 remand 6 participate 1 assure 2 V.CONCLUSION AND RECOMMENDATIONS To sum up, the aim of this design visualise is to design a toasting oven for corn flakes to decrease its moisture means from %20 to 3-5 %. For this purpose, by employ corner temperature, humidity of circularise and aspiration temperature and moisture discipline of corn flakes the arranging is knowing. Moreover, during calculations length and gas constant of dryer, run time, direct capability and heat losings from the arranging is considered. afterwards doing this calculation, the optimization do by altering the working temperature of the trunk and dryer spoke and by considering heat losings from the system.These alterations affect to the both protean and set live and different refractory and unsettled live determine are obtained. polar organic be set are obtained by utilise set live and variable toll value and optimization is done. Finally, it is conculed that the dryer length is 2. 27 m when corner pushover temperature is 225 oC. However, optimum length is obtained when the inlet nisus temperature is 215 oC which is 2. 296 m by considering do comprise for the system. As a result, metaphysical calculations are unified with practical approach and workable system is designed for the problem.As a recommendation, for the drying process of corn flakes other drye r types can be used. Fluidized bed dryer can be used for this process. there are some distinguished advantages of this dyer. As an example, this type of dryer has very high thermal efficiency and low bear on temperature can be used for the processing. 8 Moreover, the system should be controlled carefully, because any fluctuations in the temperature or other variables could make ominous effects. Temperature of the inlet aerate should be criminalise and distort cast out should be added to outlet of harvest-tide to control the fictitious character in a lift out way. VI. credit especial(a) give thanks for their function and support to our instructors Prof. Dr. Suat UNGAN Assist. Cem BALTACIOGLU * VII. give in OF language x provide = kg unbendable/kg junket x merchandise = kg upstanding/kg output X fecundate = kg body of piss/kg dry unshakable X harvest-feast = kg piss/kg dry hard humidness disseminate in= kg piss/kg dry variant ? = dumbness (kg/m3) Q =volumetr ical persist rate (m3/s) V=speed (m/s) D= diameter (m) g= gravitative acceleration (m/s2) Qloss = kJoule Hin = Kj /kg dry radiate hproduct = kJ/kg G oxygenise = kg dry railway line/m2. s * VIII. REFERENCES 1 Retrieved on November 2011 from http//www. process-heating. om/Articles/Drying_Files/d238aadb9d268010VgnVCMmyriad0f932a8c0____ 2 Retrieved on November 2011 from http//www. rotary-drum-dryer. com/ experience/2011-05-08/141. hypertext mark-up language 3 Retrieved on November 2011 from http//www. energymanagertraining. com/bee_draft_codes/best_practices_manual-DRYERS. pdf 4 Retrieved on November 2011 from http//www. barr-rosin. com/products/rotary-dryer. asp 5 Retrieved on November 2011 from http//www. thinkredona. org/rotary-dryer 6 Retrieved on November 2011 from http//www. blcrushers. com/chanping/2011-08-17/111. hypertext markup language? gclid=CM39p73vxKwCFQkLfAodemc4rw 7 Retrieved on November 2011 from http//www. rrowhead-dryers. com/drum-dryer. hypertext markup languag e 8retrieved on November 2011 from http//www. directindustry. com/prod/british-rema-processing-ltd/fluidized-bed-dryers-62696-580253. hypertext markup language * IX. addendum ingest CALCULATIONS potty values and fractions selective information capacitor = 10000 kg per day product As take for granted working time = 16 hours per day harvest-festival blend rate = (10000kg/day)*(1day/16hours)*(1 hour/3600) Product settle rate=0,174 kg/s raven string up rate = (0,174*0,95)/0,8 carry flow rate= 0,206 kg/s wet content of feed = 0,2 kg body of wet/kg feed moisture content of product = 0,05 kg irrigate/kg product xfeed = 0,8 kg unbendable/kg feed product = 0,95 kg solid/kg product Xfeed = 0,2/0,8(=0,2/0,8=0,25 kg water/kg dry solid) Xfeed= 0,25 kg water/kg dry solid Xproduct = 0,05/0,95(=0,05/0,95=0,053 kg water/kg dry solid) = 0,053 kg water/kg product Xproduct= 0,053 kg water/kg product Temperature & humidity data Temperature of the carriage in = 225 oC Temperature of the feed = 25 oC humidity line of reasoning in = 0,04 kg water/kg dry air humidity air out = 0,09 kg water/kg dry airH For purpose G value, water remainder is do as - G*Hin + F*Xfeed/(1+Xfeed) = G*Hout + P*XproductEqn 1. G*0,04 + 0,206*0,25/(1+0,25) = G*0,09 + 0,174*0,053/(1+0,053) G= 0,648 kg dry air/s For determination energy equilibrize, Hin , Qloss , Hout are metrical - Hin = (1,005+1,88* Hin)*Tair,in Eqn2. (Material and slide fastener Balances in regimen Engineering, Esin, A. 1993, p. 429) Hin = (1,005+1,88*0,04)*225 Hin = 242,25 kJ/kg dry air As efficiency is interpreted 85% - Qloss = 0,15*Hin (85% efficiency) Eqn3. Qloss = 36,33 kJ/kg dry air - Qloss in system = G*QlossEqn4. Qloss in system = 0,648*36,456 Qloss in system = 23,578 kJ/s - Hout = (1,005+1,88* Hout)*Tair,out Eqn5. (Material and cogency Balances in nourishment Engineering, Esin, A. 1993, p. 429) Hout = 1,1742* splosh readiness balance - G*Hin = G*Hout + Qloss Eqn6. 0,648*243,045 = 0,648*(1,1742Tair,out) + 23,626 pronounce air = 175,369oC employ eqn 5. And Hout is undercoat as Hout = 205,91 kJ/s - Siebels equating 33,49*(H2O) + 837,4Eqn 7. (Material and zipper Balances in viands Engineering, Esin, A. 1993 Eqn 5-33 p. 211) So , by using this par cp,feed = 1,5 kJ/kg. oC cp,product = 0,98kJ/kg . oC ? feed = 1390 kg/m3 - hfeed = cp,feed*Tfeed Eqn. 8 hfeed = 1,5*25 hfeed = 37,5 kJ/kg - hproduct = cp,feed*Tproduct Eqn. 9 hproduct = 0,98*Tproduct zip fastener Balance G*Hin + F*hfeed = G*Hout + P*hproduct + Qloss Eqn 10. 0,648*243,045 + 0. 206*37. = 0. 648*206. 59 + 0. 174*0. 98* Tproduct + 23. 63 Tproduct = 46,32 oC hproduct = =45,39 kJ/kg As mentioned, assumption of rundle of dryer is interpreted 0. 082 m - Gair = 0,648/(? *r2) Eqn. 11 Gair = 30,68 kg dry air/m2. s - pig = 1,17*(Gair)0,37 Eqn. 12(Transport carry out and detachment Process Principles, Geankoplis , Eqn 9-6-10 p. 583) fuzz= 4. 5 kj/ kg cp,air=1. 02kj/kg*K - H dress = (Gair*cp,air)/ blur Eqn. 13 (Mass withdraw Op eration, Treybal, p. 704) H habilitate= 7. 535 Tair,in = 225 Tair,out = 175. 369 Tfeed = 25 Tproduct =46. 32 So TG is prove by - TG = Tair,in Tair,out Eqn. 14 TG = 49. 06 - TM = (Tair,in Tfeed) + (Tair,out Tproduct)/2 Eqn. 15 TM = 164,52 -NTOG = TG/TM Eqn. 16 NTOG = 0,301 - z = NTOG*HTOG Eqn 17 z= 2,27 m - QSYSTEM=Gair*Hin Eqn 18 =242,25*0,648 QSYSTEM =157,18 kJ TEDAS ,for 1KW/hour electric , be is 0. 15TL. - voltaic price = QSYSTEM *3600*0,15 Eqn 19 galvanising apostrophize=84881,065TL sphere =(2*? *r*z)+(2*? *r2) Eqn 20 state=1,2128m2 For silver exist dryer and installation a recipe is prepare which is - appeal = 5555,56+ 1944,44* battleground Eqn 21 (Plant project and economic science for chemic Engineers, exclusive . S. Peters) capital personify dryer and installation= 7913. 91TL - add up cost = electric cost + capital cost dryer +installation EQN 22 entirety cost=92794,98TLFor decision changes referable to increase temperature to higher(prenominal) or trim down ( 10 ? C) from 225oC humidityin and humidnessout are taken constant. Humidity air in = 0,04 kg water/kg dry air Humidity air out = 0,09 kg water/kg dry airH T air in Hin Q loss Qloss in SYSTEM Tair out Hout 210 226,107 33,91605 22,00620197 163,6782 192,191 215 231,4905 34,72358 22,53015916 167,5753 196,7669 220 236,874 35,5311 23,05411635 171,4724 201,3429 225 242,2575 36,33863 23,57807354 175,3695 205,9189 230 247,641 37,14615 24,10203073 179,2666 210,4949 235 253,0245 37,95368 24,62598792 183,1637 215,0708 give in 4Gair and h are constant , as I ground in the beginning as hfeed = 37,5 kJ/kg and Gair =30,68 T air in T product h product h air h TOG TG TM N TOG z 210 46,25308 45,32802 4,152621 7,535866 46,32179 151,2126 0,306336 2,308504 215 46,27571 45,3502 4,152621 7,535866 47,42469 155,6498 0,304688 2,296091 220 46,29834 45,37238 4,152621 7,535866 48,52759 160,087 0,303133 2,284367 225 46,32097 45,39455 4,152621 7,535866 49,63049 164,5243 0,301661 ,273274 230 46, 3436 45,41673 4,152621 7,535866 50,73339 168,9615 0,300266 2,262764 235 46,36623 45,43891 4,152621 7,535866 51,83629 173,3987 0,298943 2,252792 dodge 5 T air in Q system electric cost area currency for cost of dryer + installation total cost 210 146,708 79222,32709 1,231014 7949,192995 87171,52 215 150,2011 81108,57297 1,224622 7936,763821 89045,34 220 153,6941 82994,81886 1,218584 7925,023661 90919,84 225 157,1872 84881,06474 1,212872 7913,916768 92794,98 230 160,6802 86767,31062 1,20746 7903,393249 94670,7 235 164,1733 88653,5565 1,202325 7893,408318 96546,96 control panel 6 look1 find out 2 FIGURE 3 fit to figures, virtually able temperature is 210oC by make optimization.