fermenterseries | | | I designed astandardtypetank fermentertype,thistype whenthe nominaltank volume in 6M3 less when using jacketedtank. Fermentation gas cooling or heating, bythe jacketto complete. When morethan nominal volume of 6M3, cool fermentation gas fromthe vertical rows oftubesto bear, interms ofthetank drainpipe connection we have made improvements.this is mainlyto avoid multiple openings inthetank, open into a corner.this continuous mannersatisfactory results inpractical use. Fermentation equipment cantype can be divided intotwo categories: one is anaerobic fermentation cone (such as alcohol fermentation), andthe other is forthetype of gas fermentationtanks (such asthestandardstyle, Wustyle,self-priming, etc.).such equipment especially inthestandardtanktype most commonly usedtype. Fermenterseries I designedthe drawings belongtothestandardtypetanktype. Fermentation equipment in a variety of design,the design ofthestructureto achievetight,there is enoughstrength andservice life, andstriveto internal accessory equipment lesssmoothsurface, notedto have good contact withthe gas vapor andsteamthorn jujube mixedsolidperformance,thatthe masstransfer,the gas exchange effectively.there issufficient heat exchange area,to ensurethatthe fermentation can beperformed atthe optimumtemperature. Attentiontothesealingperformance ofthe deviceto ensuresterilization. | | Nominal volume (M3) | Cylinder diameter (Dgmm) | Cylinder height H (mm) | Heattransfer area M2 | shaftspeed rpm | stirringshaftpower KW | 10 | 1800 | 3800 | 14 | 160-260 | 17-22 | 15 | 2000 | 4800 | 18 | 166-260 | 22-30 | 20 | 2200 | 5000 | 22 | 180-260 | 30-37 | 30 | 2400 | 6600 | 34 | 150-250 | 45-55 | 40 | 2600 | 7500 | 45 | 150-250 | 55-75 | 50 | 2800 | 8000 | 58 | 150-250 | 55-90 | 60 | 3000 | 8300 | 65 | 150-250 | 60-115 | 75 | 3200 | 8800 | 84 | 150-250 | 90-145 | 100 | 3600 | 9400 | 114 | 150-250 | 120-125 | 150 | 4200 | 10800 | 165 | 150-250 | 165-275 | 200 | 4600 | 11500 | 220 | 140-240 | 215-360 |
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