柴(chai)胡導(dao)出物制造的工藝
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。
兩(liang)次(ci)水(shui)飽和壓(ya)縮(suo)空(kong)氣(qi)不斷回(hui)升,經冷卻塔(ta)器(qi)冷卻塔(ta)成(cheng)熱(re)冷卻塔(ta)液,回(hui)降到(dao)添加罐(guan)中(zhong)(zhong)作(zuo)(zuo)新石(shi)(shi)油(you)(you)(you)(you)(you)醚(mi)(mi)加到(dao)藥(yao)(yao)(yao)(yao)表(biao)面上(shang)(shang),新石(shi)(shi)油(you)(you)(you)(you)(you)醚(mi)(mi)由(you)上(shang)(shang)而下高路依據中(zhong)(zhong)草藥(yao)(yao)(yao)(yao)層(ceng)到(dao)添加罐(guan)左(zuo)下角,中(zhong)(zhong)草藥(yao)(yao)(yao)(yao)中(zhong)(zhong)的(de)(de)可(ke)可(ke)溶合理化(hua)學成(cheng)分溶解度(du)(du)于添加罐(guan)中(zhong)(zhong)石(shi)(shi)油(you)(you)(you)(you)(you)醚(mi)(mi)。添加液經抽濾(lv)管抽入浸提器(qi)、浸提有的(de)(de)兩(liang)次(ci)水(shui)飽和壓(ya)縮(suo)空(kong)氣(qi)又寄(ji)到(dao)添加罐(guan)作(zuo)(zuo)電熱(re)鍋(guo)爐和新石(shi)(shi)油(you)(you)(you)(you)(you)醚(mi)(mi),這樣一來造成(cheng)的(de)(de)新石(shi)(shi)油(you)(you)(you)(you)(you)醚(mi)(mi)大(da)循環添加,故中(zhong)(zhong)草藥(yao)(yao)(yao)(yao)中(zhong)(zhong)溶質規格(ge)計算(suan)與石(shi)(shi)油(you)(you)(you)(you)(you)醚(mi)(mi)中(zhong)(zhong)含溶質規格(ge)計算(suan)實現高均值,中(zhong)(zhong)草藥(yao)(yao)(yao)(yao)中(zhong)(zhong)的(de)(de)溶質高路總混度(du)(du),以至完成(cheng)總混度(du)(du)(添加液結晶體),倘(tang)若,添加液立即停(ting)止抽入浸提器(qi),浸提的(de)(de)兩(liang)次(ci)水(shui)飽和壓(ya)縮(suo)空(kong)氣(qi)轉(zhuan)送冷卻塔(ta)器(qi),浸提不斷來進(jin)行,以至浸提成(cheng)是需(xu)要重量比例(1.2~1.34)的(de)(de)軟(ruan)膏,發出被用。添加罐(guan)中(zhong)(zhong)的(de)(de)結晶體液態物質,可(ke)置(zhi)入貯罐(guan)作(zuo)(zuo)下批準用,藥(yao)(yao)(yao)(yao)渣從(cong)出渣門排掉,倘(tang)若用有機的(de)(de)石(shi)(shi)油(you)(you)(you)(you)(you)醚(mi)(mi)添加,則(ze)先加摻入的(de)(de)水(shui),開直(zhi)達和夾套水(shui)飽和壓(ya)縮(suo)空(kong)氣(qi),回(hui)收處理石(shi)(shi)油(you)(you)(you)(you)(you)醚(mi)(mi)后(hou),將渣排掉。

常見技術(shu)設備參數表
材質 | TQ0.5 | TQ1.0 | TQ2.0 | TQ3.0 | TQ4.0 | TQ5.0 | TQ6.0 | TQ8.0 |
全容量L | 560 | 1300 | 2300 | 3600 | 4400 | 5560 | 6500 | 8900 |
堿罐壓力差 | 0.09 | |||||||
夾套氣壓 | 0.3 | |||||||
供暖大小 | 2.1 | 4 | 5 | 6.8 | 7.3 | 8.5 | 9.5 | 11 |
冷卻面積計算 | 3.0 | 5.0 | 5.0 | 8.0 | 8.0 | 10.0 | 10.0 | 12.0 |
散熱體積 | 1.0 | 1.0 | 1.0 | 1.0 | 1.0 | 1.5 | 1.5 | 1.5 |
過慮面積計算 | 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 |
攪伴工作效率 | 1.5 | 3.0 | 4.0 | 5.5 | 5.5 | 7.5 | 7.5 | 7.5 |
拌和電機轉速 | 63 | 63 | 63 | 63 | 63 | 63 | 63 | 63 |
蒸汽發生器耗量 | 100 | 180 | 225 | 300 | 330 | 380 | 420 | 495 |
一系列冷卻系統耗量 | 2.6 | 4.2 | 4.2 | 6.8 | 6.8 | 8.5 | 8.5 | 10 |