野白菊花去(qu)除物生(sheng)產(chan)的(de)機械
將藥材投入提取罐內,加藥材的5~10倍的溶媒如水、乙醇、甲醇、丙酮等(據工藝要求)。開啟提取罐直通和夾套蒸汽閥門,使提取液加熱至沸騰20~30分鐘后,用抽濾管將1/3提取液抽入濃縮器。關閉提取罐直通和夾套蒸汽、開啟加熱器閥門使液料進行濃縮。濃縮時產生二次蒸汽,通過蒸發器上升管送入提取罐作提取的熱源和溶液,維持提取罐內沸騰。
重(zhong)新(xin)(xin)飽(bao)(bao)和(he)(he)蒸(zheng)氣(qi)(qi)(qi)重(zhong)新(xin)(xin)上升的,經(jing)空(kong)氣(qi)(qi)(qi)空(kong)氣(qi)(qi)(qi)冷(leng)卻(que)塔空(kong)氣(qi)(qi)(qi)空(kong)氣(qi)(qi)(qi)冷(leng)卻(que)成(cheng)(cheng)(cheng)(cheng)熱空(kong)氣(qi)(qi)(qi)空(kong)氣(qi)(qi)(qi)冷(leng)卻(que)液(ye)(ye),下挫(cuo)到(dao)轉(zhuan)(zhuan)(zhuan)化(hua)(hua)成(cheng)(cheng)(cheng)(cheng)罐(guan)(guan)中(zhong)(zhong)(zhong)(zhong)(zhong)作新(xin)(xin)萃(cui)(cui)取劑(ji)(ji)(ji)加(jia)(jia)到(dao)藥(yao)面上方,新(xin)(xin)萃(cui)(cui)取劑(ji)(ji)(ji)由上而(er)下繞城(cheng)髙(gao)速借助中(zhong)(zhong)(zhong)(zhong)(zhong)藥(yao)層到(dao)轉(zhuan)(zhuan)(zhuan)化(hua)(hua)成(cheng)(cheng)(cheng)(cheng)罐(guan)(guan)下面,中(zhong)(zhong)(zhong)(zhong)(zhong)藥(yao)中(zhong)(zhong)(zhong)(zhong)(zhong)的可陰離子型有效的情況容解于(yu)轉(zhuan)(zhuan)(zhuan)化(hua)(hua)成(cheng)(cheng)(cheng)(cheng)罐(guan)(guan)中(zhong)(zhong)(zhong)(zhong)(zhong)萃(cui)(cui)取劑(ji)(ji)(ji)。轉(zhuan)(zhuan)(zhuan)化(hua)(hua)成(cheng)(cheng)(cheng)(cheng)液(ye)(ye)經(jing)抽濾(lv)管抽入(ru)沉(chen)淀(dian)(dian)液(ye)(ye)器、沉(chen)淀(dian)(dian)液(ye)(ye)生產的重(zhong)新(xin)(xin)飽(bao)(bao)和(he)(he)蒸(zheng)氣(qi)(qi)(qi)又送過(guo)來(lai)轉(zhuan)(zhuan)(zhuan)化(hua)(hua)成(cheng)(cheng)(cheng)(cheng)罐(guan)(guan)作熱媒(mei)和(he)(he)新(xin)(xin)萃(cui)(cui)取劑(ji)(ji)(ji),這類型成(cheng)(cheng)(cheng)(cheng)的新(xin)(xin)萃(cui)(cui)取劑(ji)(ji)(ji)大(da)流回轉(zhuan)(zhuan)(zhuan)化(hua)(hua)成(cheng)(cheng)(cheng)(cheng),故中(zhong)(zhong)(zhong)(zhong)(zhong)藥(yao)中(zhong)(zhong)(zhong)(zhong)(zhong)溶(rong)質高(gao)密(mi)度單(dan)(dan)位與萃(cui)(cui)取劑(ji)(ji)(ji)中(zhong)(zhong)(zhong)(zhong)(zhong)含溶(rong)質高(gao)密(mi)度單(dan)(dan)位保(bao)護高(gao)等度,中(zhong)(zhong)(zhong)(zhong)(zhong)藥(yao)中(zhong)(zhong)(zhong)(zhong)(zhong)的溶(rong)質繞城(cheng)髙(gao)速總(zong)混,早(zao)以截然總(zong)混(轉(zhuan)(zhuan)(zhuan)化(hua)(hua)成(cheng)(cheng)(cheng)(cheng)液(ye)(ye)結晶體),此刻,轉(zhuan)(zhuan)(zhuan)化(hua)(hua)成(cheng)(cheng)(cheng)(cheng)液(ye)(ye)消停抽入(ru)沉(chen)淀(dian)(dian)液(ye)(ye)器,沉(chen)淀(dian)(dian)液(ye)(ye)的重(zhong)新(xin)(xin)飽(bao)(bao)和(he)(he)蒸(zheng)氣(qi)(qi)(qi)轉(zhuan)(zhuan)(zhuan)送空(kong)氣(qi)(qi)(qi)冷(leng)卻(que)塔,沉(chen)淀(dian)(dian)液(ye)(ye)重(zhong)新(xin)(xin)去,早(zao)以沉(chen)淀(dian)(dian)液(ye)(ye)成(cheng)(cheng)(cheng)(cheng)都要密(mi)度(1.2~1.34)的軟膏,拉出(chu)被用(yong)。轉(zhuan)(zhuan)(zhuan)化(hua)(hua)成(cheng)(cheng)(cheng)(cheng)罐(guan)(guan)中(zhong)(zhong)(zhong)(zhong)(zhong)的結晶體稀釋劑(ji)(ji)(ji),可加(jia)(jia)入(ru)貯(zhu)罐(guan)(guan)作下批復文件用(yong),藥(yao)渣從出(chu)渣門(men)排掉,假(jia)如用(yong)有機的萃(cui)(cui)取劑(ji)(ji)(ji)轉(zhuan)(zhuan)(zhuan)化(hua)(hua)成(cheng)(cheng)(cheng)(cheng),則先加(jia)(jia)攝入(ru)足(zu)夠含量的水,開直連和(he)(he)夾(jia)套飽(bao)(bao)和(he)(he)蒸(zheng)氣(qi)(qi)(qi),回收(shou)公(gong)司萃(cui)(cui)取劑(ji)(ji)(ji)后,將(jiang)渣排掉。

核心方法性能指標
類型 | TQ0.5 | TQ1.0 | TQ2.0 | TQ3.0 | TQ4.0 | TQ5.0 | TQ6.0 | TQ8.0 |
全容積怎么算L | 560 | 1300 | 2300 | 3600 | 4400 | 5560 | 6500 | 8900 |
堿罐重壓 | 0.09 | |||||||
夾套壓 | 0.3 | |||||||
進行加熱大小 | 2.1 | 4 | 5 | 6.8 | 7.3 | 8.5 | 9.5 | 11 |
蒸汽加熱面積計算 | 3.0 | 5.0 | 5.0 | 8.0 | 8.0 | 10.0 | 10.0 | 12.0 |
閉式冷卻塔建筑面積 | 1.0 | 1.0 | 1.0 | 1.0 | 1.0 | 1.5 | 1.5 | 1.5 |
過濾程序體積 | 0.25 | 0.25 | 0.25 | 0.25 | 0.25 | 0.50 | 0.50 | 0.50 |
出渣門 | 600 | 800 | 800 | 800 | 1000 | 1000 | 1000 | 1200 |
人孔 | 300 | 300 | 400 | 400 | 450 | 450 | 450 | 500 |
拌和工作功率 | 1.5 | 3.0 | 4.0 | 5.5 | 5.5 | 7.5 | 7.5 | 7.5 |
摻和速比 | 63 | 63 | 63 | 63 | 63 | 63 | 63 | 63 |
蒸汽式耗量 | 100 | 180 | 225 | 300 | 330 | 380 | 420 | 495 |
冷卻塔水耗量 | 2.6 | 4.2 | 4.2 | 6.8 | 6.8 | 8.5 | 8.5 | 10 |