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)系統(tong),使提(ti)(ti)(ti)(ti)(ti)取(qu)(qu)液加(jia)熱(re)(re)至(zhi)(zhi)沸(fei)騰20--30分(fen)鐘后,用(yong)(yong)抽濾管將(jiang)三分(fen)之一的(de)提(ti)(ti)(ti)(ti)(ti)取(qu)(qu)液抽入(ru)。關閉提(ti)(ti)(ti)(ti)(ti)取(qu)(qu)罐(guan)(guan)直統(tong)與(yu)夾套熱(re)(re)水(shui)(shui),開(kai)(kai)啟濃(nong)(nong)縮(suo)(suo)(suo)罐(guan)(guan)直統(tong)與(yu)加(jia)熱(re)(re)系統(tong)使濃(nong)(nong)縮(suo)(suo)(suo)汁溫度保持(chi)在80℃左(zuo)右(you),真空度保持(chi)在-0.05到(dao)-0.09MPA,濃(nong)(nong)縮(suo)(suo)(suo)時(shi)產生的(de)二(er)次蒸汽經(jing)過(guo)冷凝(ning)器與(yu)冷卻器變(bian)成冷凝(ning)液回(hui)(hui)流至(zhi)(zhi)提(ti)(ti)(ti)(ti)(ti)取(qu)(qu)罐(guan)(guan)做(zuo)(zuo)新(xin)溶(rong)(rong)(rong)(rong)(rong)劑(ji)(ji)(ji)加(jia)入(ru)藥里,新(xin)溶(rong)(rong)(rong)(rong)(rong)劑(ji)(ji)(ji)由上而下通(tong)過(guo)藥材(cai)層到(dao)提(ti)(ti)(ti)(ti)(ti)取(qu)(qu)罐(guan)(guan)底部,藥材(cai)中(zhong)的(de)可(ke)溶(rong)(rong)(rong)(rong)(rong)性成分(fen)溶(rong)(rong)(rong)(rong)(rong)解于(yu)提(ti)(ti)(ti)(ti)(ti)取(qu)(qu)罐(guan)(guan)內溶(rong)(rong)(rong)(rong)(rong)劑(ji)(ji)(ji),提(ti)(ti)(ti)(ti)(ti)取(qu)(qu)液經(jing)抽濾管抽入(ru)濃(nong)(nong)縮(suo)(suo)(suo)罐(guan)(guan),濃(nong)(nong)縮(suo)(suo)(suo)產生的(de)二(er)次蒸汽又送至(zhi)(zhi)提(ti)(ti)(ti)(ti)(ti)取(qu)(qu)罐(guan)(guan)做(zuo)(zuo)新(xin)溶(rong)(rong)(rong)(rong)(rong)劑(ji)(ji)(ji),形成新(xin)溶(rong)(rong)(rong)(rong)(rong)劑(ji)(ji)(ji)回(hui)(hui)流提(ti)(ti)(ti)(ti)(ti)取(qu)(qu),直至(zhi)(zhi)完全(quan)溶(rong)(rong)(rong)(rong)(rong)出(提(ti)(ti)(ti)(ti)(ti)取(qu)(qu)液無色)濃(nong)(nong)縮(suo)(suo)(suo)繼(ji)續(xu)進行(xing),直至(zhi)(zhi)濃(nong)(nong)縮(suo)(suo)(suo)成需要的(de)比重(zhong)藥膏(gao),提(ti)(ti)(ti)(ti)(ti)取(qu)(qu)罐(guan)(guan)內的(de)無色液體(ti)可(ke)下次復(fu)用(yong)(yong),若是(shi)有機溶(rong)(rong)(rong)(rong)(rong)劑(ji)(ji)(ji)提(ti)(ti)(ti)(ti)(ti)取(qu)(qu),則先加(jia)適量水(shui)(shui),開(kai)(kai)直統(tong)與(yu)夾套熱(re)(re)水(shui)(shui),回(hui)(hui)收溶(rong)(rong)(rong)(rong)(rong)劑(ji)(ji)(ji)后,將(jiang)渣排掉。
儀器通常樣式有正錐式、口蘑式、直筒式、斜錐式、倒錐式。可以作為動態圖生成,也可選擇生孩子流程要,調試攪拌裝置器作動態圖生成。1、主罐體,帶夾套及隔熱,中有人孔,下有汽缸操作出渣門旋轉開關,勞動就業密度低。2、 氣體吸附器,包括用于清除煎煮中藥配方時制造的泡沫板,并以防藥流過熱蒸汽中的藥渣邁入冷凝劑器。3、 空調蒸發器器,包括反應為藥液蒸汽加熱做空調蒸發器與純酒精收舊。3、 制冷塔器,主要的功能對制冷液與溶媒實現制冷塔。4、 油和水量離器,一般效用在提油時,經放涼的回收分類處理液實行油破乳出來,以才能得到須要的香味油。5、 液固脫離處理器,脫離處理汽液處理放空時的液態物質帶出罐外。6、 混和器,混和缸內的廢料,使之提煉的固態垃圾內外部很好的組成能平均加水與齊全煎煮到,利用于出渣。 
| 指標/產品型號 | 0.5m3 | 1m3 | 2m3 | 3m3 | 4m3 | 6m3 | 8m3 | 10m3 | |||||||
| 全容量(L) | 650 | 1200 | 2300 | 3300 | 4300 | 6400 | 8600 | 11000 | |||||||
| 堿罐設計方案水壓(Mpa) | <0.1 | ||||||||||||||
| 夾套設定壓為(Mpa) | ≤0.3 | ||||||||||||||
| 壓縮視頻室內空氣工作壓力(Mpa) | 0.6-0.7 | ||||||||||||||
| 進料口直徑不低于(mm) | 350 | 400 | 400 | 400 | 400 | 450 | 500 | 500 | |||||||
| 排渣口直徑怎么算(mm) | 500 | 800 | 800 | 800 | 800 | 1000 | 1000 | 1000 | |||||||
| 熱處理加熱占地面積(m2) | 2.7 | 3.6 | 5 | 6.5 | 7.5 | 11 | 13 | 15 | |||||||
| 冷卻建筑面積(m2) | 3 | 4 | 5 | 6 | 8 | 8 | 12 | 15 | |||||||
| 閉式冷卻塔綠地面積(m2) | 0.5 | 0.5 | 1 | 1 | 1 | 1.5 | 1.5 | 1.5 | |||||||