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野菊花提取物生產設備

作著: 人氣:先生發表的時間:2025-04-20 16:25:42

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

 



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