藁本來面目溫，味辛，享有散熱感冒濕邪的功較，慣用于治愈熱感冒頭疼、巔頂痛、寒濕肚子痛、泄瀉、疝瘕、疥癬等癥。這篇全面的介紹藁本的功較與用處、藁雖是些什么、副用處、醫學使用、藁本的附方、伍配使用等。

將藥材投入提取罐內，加入5—10倍的溶劑如水、乙醇、甲醇、丙酮等（根據工藝要求）。開啟提取罐加(jia)熱(re)(re)系(xi)統(tong)(tong)，使提(ti)(ti)(ti)(ti)取(qu)(qu)(qu)(qu)液(ye)加(jia)熱(re)(re)至(zhi)(zhi)(zhi)沸騰20--30分(fen)鐘后，用(yong)抽(chou)濾管將三分(fen)之一的(de)提(ti)(ti)(ti)(ti)取(qu)(qu)(qu)(qu)液(ye)抽(chou)入(ru)。關(guan)閉(bi)提(ti)(ti)(ti)(ti)取(qu)(qu)(qu)(qu)罐(guan)(guan)直(zhi)(zhi)統(tong)(tong)與(yu)夾(jia)套(tao)熱(re)(re)水(shui)(shui)，開啟濃(nong)縮(suo)罐(guan)(guan)直(zhi)(zhi)統(tong)(tong)與(yu)加(jia)熱(re)(re)系(xi)統(tong)(tong)使濃(nong)縮(suo)汁溫度(du)保持在(zai)80℃左右，真空度(du)保持在(zai)－0.05到－0.09MPA,濃(nong)縮(suo)時產生的(de)二次蒸(zheng)汽(qi)經過冷凝器與(yu)冷卻器變成(cheng)(cheng)冷凝液(ye)回流至(zhi)(zhi)(zhi)提(ti)(ti)(ti)(ti)取(qu)(qu)(qu)(qu)罐(guan)(guan)做新溶(rong)(rong)劑加(jia)入(ru)藥(yao)里,新溶(rong)(rong)劑由上而下通過藥(yao)材層到提(ti)(ti)(ti)(ti)取(qu)(qu)(qu)(qu)罐(guan)(guan)底(di)部(bu),藥(yao)材中的(de)可溶(rong)(rong)性(xing)成(cheng)(cheng)分(fen)溶(rong)(rong)解于提(ti)(ti)(ti)(ti)取(qu)(qu)(qu)(qu)罐(guan)(guan)內(nei)溶(rong)(rong)劑,提(ti)(ti)(ti)(ti)取(qu)(qu)(qu)(qu)液(ye)經抽(chou)濾管抽(chou)入(ru)濃(nong)縮(suo)罐(guan)(guan),濃(nong)縮(suo)產生的(de)二次蒸(zheng)汽(qi)又送(song)至(zhi)(zhi)(zhi)提(ti)(ti)(ti)(ti)取(qu)(qu)(qu)(qu)罐(guan)(guan)做新溶(rong)(rong)劑,形成(cheng)(cheng)新溶(rong)(rong)劑回流提(ti)(ti)(ti)(ti)取(qu)(qu)(qu)(qu),直(zhi)(zhi)至(zhi)(zhi)(zhi)完全溶(rong)(rong)出(提(ti)(ti)(ti)(ti)取(qu)(qu)(qu)(qu)液(ye)無色(se))濃(nong)縮(suo)繼續(xu)進行,直(zhi)(zhi)至(zhi)(zhi)(zhi)濃(nong)縮(suo)成(cheng)(cheng)需要(yao)的(de)比重藥(yao)膏(gao),提(ti)(ti)(ti)(ti)取(qu)(qu)(qu)(qu)罐(guan)(guan)內(nei)的(de)無色(se)液(ye)體可下次復用(yong),若(ruo)是有機溶(rong)(rong)劑提(ti)(ti)(ti)(ti)取(qu)(qu)(qu)(qu),則先(xian)加(jia)適量(liang)水(shui)(shui),開直(zhi)(zhi)統(tong)(tong)與(yu)夾(jia)套(tao)熱(re)(re)水(shui)(shui),回收溶(rong)(rong)劑后,將渣排掉(diao)。

本環保設計快速可用于中藥茶、食材、化學工業的行業內的過熱蒸汽、微壓、水煎、溫浸、熱此回流、二次反復的、滲漉、芬香油截取及生物碳溶媒的回收利用等多種類方法進行操作。利用本環保設計能使截取成果更好、日子短、藥液分量高。本環保設計打料設計分錐形式打料和槳式打料，同樣本環保設計材料選擇良好的，大范圍應該用于生物制藥、食材、化學工業等的行業內。藥材抽取濃縮液裝置科技叁數：

款式	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
罐中氣壓	0.09
夾套負擔	0.3
蒸汽加熱建筑面積	2.1	4	5	6.8	7.3	8.5	9.5	11
冷凝器表面積	3.0	5.0	5.0	8.0	8.0	10.0	10.0	12.0
冷卻水建筑面積	1.0	1.0	1.0	1.0	1.0	1.5	1.5	1.5
濾出面積計算	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
摻和工作效率	1.5	3.0	4.0	5.5	5.5	7.5	7.5	7.5
攪拌裝置發動機轉速	63	63	63	63	63	63	63	63
蒸汽式耗量	100	180	225	300	330	380	420	495
保壓水耗量	2.6	4.2	4.2	6.8	6.8	8.5	8.5	10