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 |