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1、辽宁石油化工大学毕业设计（论文）用纸325吨/年硫酸双氢链霉素生产装置工艺设计摘要本课题为325吨/年硫酸双氢链霉素生产装置的工艺设计。在发酵过程中，每天需完成至少51.055m3（53607.75kg）发酵全液的生产。经计算，生产中选用8个75m3的发酵罐，发酵周期为8d，一、二、三级种子罐各4个，发酵周期为4d。菌种经一、二、三级种子罐逐级扩大培养后放罐入发酵罐中，在发酵罐中经8d发酵，产成51.055m3的发酵全液，后放入预处理罐内进行硫酸双氢链霉素的合成提取。发酵液进入预处理罐后，用草酸酸
2、化至pH3.0左右，通过板框过滤，除去大量杂质，再用NaOH中和至pH在6.7~7.2范围内。离开预处理罐的发酵液进入稀释罐进行稀释，后进入交换罐。在交换罐中采用1103Na型树脂对稀释液进行吸附，再经7%H2SO4溶液进行解吸，解吸完毕，采用活性炭粉对解吸液脱色。解吸后的解吸液在补还原罐中用NaBH4将硫酸链霉素还原为硫酸双氢链霉素，还原后的硫酸双氢链霉素经稀释、吸附、解吸精制、精脱、薄膜蒸发、成脱和离心喷雾干燥等步骤形成成品。关键词：硫酸双氢链霉素；生产装置；工艺流程；设计辽宁石油化工大学毕业
3、设计（论文）用纸Atechnologicaldesignof325t/adihydrostreptomycinsulphateproductionfacilityChengWei(Class0901,Departmentofbiologicalengineering,SchoolofEnvironmentalandbiologicalengineering,LiaoningShihuaUniversity,LiaoningFushun,113001,China)AbstractThistopici
4、sthetechnologicaldesignof325t/adihydrostreptomycinsulphateproductionfacility.Inthefermentationprocess,ithavetocompleteatleast51.055m3(53607.75kg)fermentationliquidproductioneveryday.Aftercalculation,theresultsisthattheproductiondesignselecteeight75m3f
5、ermenter,thefermentationperiodwas8d,the1st,2nd,3rdseedtankisfour,respectively.After8dfermentation,51.055m3fermentationbrothisobtained.Thenthefermentationbrothisputintothepretreatmenttankforthesynthesisofdihydrostreptomycinsulfateextraction.Afterthefer
6、mentationbrothintothepretreatmenttanks,itisacidifiedtonearlypH3.0withoxalicacid.Thenitcanremovelargeamountsofimpuritiesthroughtheplateandframefilter,anditisneutralizedtoapHrangeof6.7to7.2withNaOH.Afterfermentationbrothleavingthetankintothedilutiontank
7、fordilution,thefermentationbrothflowsintotheexchangetank.Inexchangetank,ituses1103Natyperesinforadsorptionondilution.Thenthedilutionisdesorbedcompletelyby7%H2SO4solution.Afterdesorption,desorptionsolutionisdecoloredusingactivatedcarbonpowder.Afterdeso
8、rption,thestreptomycinsulfateindesorptionsolutionwillbereducedtodihydrostreptomycinsulfateusingNaBH4inthereductionpot.Afterreduced,dihydrostreptomycinsulfateformsfinishedgoodsthroughdilution,II辽宁石油化工大学毕业设计（论文）用纸adsorption,desorptionrefined,los
