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柴胡提取物加工工藝

筆者: 人氣:發稿時間段:2025-04-20 16:26:27

柴胡拆(chai)分物生產(chan)制(zhi)造工藝流程

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。

二級(ji)過熱(re)(re)蒸氣式再上(shang)升時,經(jing)冷(leng)(leng)疑器器冷(leng)(leng)疑器成(cheng)熱(re)(re)冷(leng)(leng)疑器液(ye)(ye),受挫到(dao)抽(chou)取(qu)(qu)(qu)罐中(zhong)(zhong)(zhong)作新溶(rong)(rong)液(ye)(ye)加到(dao)藥上(shang)邊(bian),新溶(rong)(rong)液(ye)(ye)由上(shang)而下高(gao)(gao)速(su)路的(de)(de)完(wan)(wan)成(cheng)中(zhong)(zhong)(zhong)草(cao)(cao)藥層到(dao)抽(chou)取(qu)(qu)(qu)罐底(di),中(zhong)(zhong)(zhong)草(cao)(cao)藥中(zhong)(zhong)(zhong)的(de)(de)可溶(rong)(rong)解完(wan)(wan)性(xing)合理有效原料溶(rong)(rong)解完(wan)(wan)于抽(chou)取(qu)(qu)(qu)罐中(zhong)(zhong)(zhong)溶(rong)(rong)液(ye)(ye)。抽(chou)取(qu)(qu)(qu)液(ye)(ye)經(jing)抽(chou)濾管(guan)抽(chou)入高(gao)(gao)濃液(ye)(ye)器、高(gao)(gao)濃液(ye)(ye)會產(chan)生(sheng)的(de)(de)二級(ji)過熱(re)(re)蒸氣式又送回抽(chou)取(qu)(qu)(qu)罐作熱(re)(re)環境和(he)新溶(rong)(rong)液(ye)(ye),這(zhe)樣子造成(cheng)的(de)(de)新溶(rong)(rong)液(ye)(ye)大離交柱抽(chou)取(qu)(qu)(qu),故中(zhong)(zhong)(zhong)草(cao)(cao)藥中(zhong)(zhong)(zhong)溶(rong)(rong)質(zhi)黏度(du)與溶(rong)(rong)液(ye)(ye)中(zhong)(zhong)(zhong)含溶(rong)(rong)質(zhi)黏度(du)要保持高(gao)(gao)系(xi)數,中(zhong)(zhong)(zhong)草(cao)(cao)藥中(zhong)(zhong)(zhong)的(de)(de)溶(rong)(rong)質(zhi)高(gao)(gao)速(su)路的(de)(de)總(zong)混,一(yi)直到(dao)徹底(di)總(zong)混(抽(chou)取(qu)(qu)(qu)液(ye)(ye)結晶(jing)體(ti)),這(zhe)時,抽(chou)取(qu)(qu)(qu)液(ye)(ye)為(wei)止抽(chou)入高(gao)(gao)濃液(ye)(ye)器,高(gao)(gao)濃液(ye)(ye)的(de)(de)二級(ji)過熱(re)(re)蒸氣式轉(zhuan)送冷(leng)(leng)凝器,高(gao)(gao)濃液(ye)(ye)再使用,一(yi)直到(dao)高(gao)(gao)濃液(ye)(ye)成(cheng)須得比重怎么算(1.2~1.34)的(de)(de)外用藥,散出被用。抽(chou)取(qu)(qu)(qu)罐中(zhong)(zhong)(zhong)的(de)(de)結晶(jing)體(ti)萃取(qu)(qu)(qu)劑,可放進貯罐作下審批用,藥渣(zha)從出渣(zha)門排掉(diao),假如用生(sheng)物碳溶(rong)(rong)液(ye)(ye)抽(chou)取(qu)(qu)(qu),則先加摻入的(de)(de)水,開直通(tong)式和(he)夾套過熱(re)(re)蒸氣式,收集溶(rong)(rong)液(ye)(ye)后,將渣(zha)排掉(diao)。

核心技能數據

尺寸

TQ0.5

TQ1.0

TQ2.0

TQ3.0

TQ4.0

TQ5.0

TQ6.0

TQ8.0

全溶量L

560

1300

2300

3600

4400

5560

6500

8900

罐體工作壓力

0.09

夾套負擔

0.3

加溫范圍

2.1

4

5

6.8

7.3

8.5

9.5

11

空氣冷卻建筑面積

3.0

5.0

5.0

8.0

8.0

10.0

10.0

12.0

水冷卻戶型面積

1.0

1.0

1.0

1.0

1.0

1.5

1.5

1.5

進行過濾戶型面積

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

混合功效

1.5

3.0

4.0

5.5

5.5

7.5

7.5

7.5

混和轉速

63

63

63

63

63

63

63

63

過熱蒸汽耗量

100

180

225

300

330

380

420

495

待循環水耗量

2.6

4.2

4.2

6.8

6.8

8.5

8.5

10

 



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