中草藥多功能提取濃縮設備 植物提取罐工作原理
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。
2次(ci)空(kong)氣(qi)壓(ya)縮(suo)隨時(shi)攀升,經氣(qi)液(ye)(ye)分(fen)離器(qi)(qi)器(qi)(qi)氣(qi)液(ye)(ye)分(fen)離器(qi)(qi)成熱(re)氣(qi)液(ye)(ye)分(fen)離器(qi)(qi)液(ye)(ye),回升到(dao)添(tian)加(jia)罐中(zhong)作新高(gao)(gao)(gao)(gao)(gao)沸(fei)(fei)(fei)(fei)點(dian)(dian)(dian)(dian)(dian)高(gao)(gao)(gao)(gao)(gao)沸(fei)(fei)(fei)(fei)點(dian)(dian)(dian)(dian)(dian)相(xiang)(xiang)轉(zhuan)(zhuan)(zhuan)(zhuan)移(yi)催化(hua)劑(ji)加(jia)到(dao)藥(yao)(yao)上,新高(gao)(gao)(gao)(gao)(gao)沸(fei)(fei)(fei)(fei)點(dian)(dian)(dian)(dian)(dian)高(gao)(gao)(gao)(gao)(gao)沸(fei)(fei)(fei)(fei)點(dian)(dian)(dian)(dian)(dian)相(xiang)(xiang)轉(zhuan)(zhuan)(zhuan)(zhuan)移(yi)催化(hua)劑(ji)由上而下高(gao)(gao)(gao)(gao)(gao)利用中(zhong)中(zhong)草名(ming)(ming)(ming)貴藥(yao)(yao)村(cun)層到(dao)添(tian)加(jia)罐側面,中(zhong)中(zhong)草名(ming)(ming)(ming)貴藥(yao)(yao)村(cun)中(zhong)的(de)可無水磷(lin)酸氫有效(xiao)的(de)含量溶解度(du)于添(tian)加(jia)罐中(zhong)高(gao)(gao)(gao)(gao)(gao)沸(fei)(fei)(fei)(fei)點(dian)(dian)(dian)(dian)(dian)高(gao)(gao)(gao)(gao)(gao)沸(fei)(fei)(fei)(fei)點(dian)(dian)(dian)(dian)(dian)相(xiang)(xiang)轉(zhuan)(zhuan)(zhuan)(zhuan)移(yi)催化(hua)劑(ji)。添(tian)加(jia)液(ye)(ye)經抽(chou)濾管抽(chou)入(ru)沉(chen)(chen)淀(dian)(dian)(dian)器(qi)(qi)、沉(chen)(chen)淀(dian)(dian)(dian)導致的(de)2次(ci)空(kong)氣(qi)壓(ya)縮(suo)又送(song)去添(tian)加(jia)罐作熱(re)媒和新高(gao)(gao)(gao)(gao)(gao)沸(fei)(fei)(fei)(fei)點(dian)(dian)(dian)(dian)(dian)高(gao)(gao)(gao)(gao)(gao)沸(fei)(fei)(fei)(fei)點(dian)(dian)(dian)(dian)(dian)相(xiang)(xiang)轉(zhuan)(zhuan)(zhuan)(zhuan)移(yi)催化(hua)劑(ji),那么(me)實(shi)現(xian)的(de)新高(gao)(gao)(gao)(gao)(gao)沸(fei)(fei)(fei)(fei)點(dian)(dian)(dian)(dian)(dian)高(gao)(gao)(gao)(gao)(gao)沸(fei)(fei)(fei)(fei)點(dian)(dian)(dian)(dian)(dian)相(xiang)(xiang)轉(zhuan)(zhuan)(zhuan)(zhuan)移(yi)催化(hua)劑(ji)大逆(ni)流(liu)添(tian)加(jia),故中(zhong)中(zhong)草名(ming)(ming)(ming)貴藥(yao)(yao)村(cun)中(zhong)溶質(zhi)(zhi)密(mi)度(du)單(dan)位計算(suan)(suan)與高(gao)(gao)(gao)(gao)(gao)沸(fei)(fei)(fei)(fei)點(dian)(dian)(dian)(dian)(dian)高(gao)(gao)(gao)(gao)(gao)沸(fei)(fei)(fei)(fei)點(dian)(dian)(dian)(dian)(dian)相(xiang)(xiang)轉(zhuan)(zhuan)(zhuan)(zhuan)移(yi)催化(hua)劑(ji)中(zhong)含溶質(zhi)(zhi)密(mi)度(du)單(dan)位計算(suan)(suan)保證高(gao)(gao)(gao)(gao)(gao)梯度(du)方向(xiang),中(zhong)中(zhong)草名(ming)(ming)(ming)貴藥(yao)(yao)村(cun)中(zhong)的(de)溶質(zhi)(zhi)高(gao)(gao)(gao)(gao)(gao)總混(hun)度(du),就(jiu)此非常總混(hun)度(du)(添(tian)加(jia)液(ye)(ye)沒有顏色),這段時(shi)間,添(tian)加(jia)液(ye)(ye)終止抽(chou)入(ru)沉(chen)(chen)淀(dian)(dian)(dian)器(qi)(qi),沉(chen)(chen)淀(dian)(dian)(dian)的(de)2次(ci)空(kong)氣(qi)壓(ya)縮(suo)轉(zhuan)(zhuan)(zhuan)(zhuan)送(song)冷去器(qi)(qi),沉(chen)(chen)淀(dian)(dian)(dian)隨時(shi)實(shi)現(xian),就(jiu)此沉(chen)(chen)淀(dian)(dian)(dian)成是需要占比(bi)(1.2~1.34)的(de)消炎軟膏,發布被用。添(tian)加(jia)罐中(zhong)的(de)沒有顏色介質(zhi)(zhi)液(ye)(ye)體(ti),可置入(ru)貯(zhu)罐作下審批(pi)用,藥(yao)(yao)渣(zha)從出(chu)渣(zha)門排掉,如果用無機高(gao)(gao)(gao)(gao)(gao)沸(fei)(fei)(fei)(fei)點(dian)(dian)(dian)(dian)(dian)高(gao)(gao)(gao)(gao)(gao)沸(fei)(fei)(fei)(fei)點(dian)(dian)(dian)(dian)(dian)相(xiang)(xiang)轉(zhuan)(zhuan)(zhuan)(zhuan)移(yi)催化(hua)劑(ji)添(tian)加(jia),則先加(jia)摻入(ru)的(de)水,開(kai)直達和夾套空(kong)氣(qi)壓(ya)縮(suo),回收(shou)并(bing)高(gao)(gao)(gao)(gao)(gao)沸(fei)(fei)(fei)(fei)點(dian)(dian)(dian)(dian)(dian)高(gao)(gao)(gao)(gao)(gao)沸(fei)(fei)(fei)(fei)點(dian)(dian)(dian)(dian)(dian)相(xiang)(xiang)轉(zhuan)(zhuan)(zhuan)(zhuan)移(yi)催化(hua)劑(ji)后,將渣(zha)排掉。

名貴藥材多實用功能分(fen)離出來濃(nong)縮咖啡機(ji) 植被分(fen)離出來罐大部分(fen)技術工藝因素
型號查詢 | TQ0.5 | TQ1.0 | TQ2.0 | TQ3.0 | TQ4.0 | TQ5.0 | TQ6.0 | TQ8.0 |
全容積怎么算L | 560 | 1300 | 2300 | 3600 | 4400 | 5560 | 6500 | 8900 |
罐里經濟壓力 | 0.09 | |||||||
夾套各種壓力 | 0.3 | |||||||
受熱范圍 | 2.1 | 4 | 5 | 6.8 | 7.3 | 8.5 | 9.5 | 11 |
冷凝劑表面積 | 3.0 | 5.0 | 5.0 | 8.0 | 8.0 | 10.0 | 10.0 | 12.0 |
蒸發使用面積 | 1.0 | 1.0 | 1.0 | 1.0 | 1.0 | 1.5 | 1.5 | 1.5 |
過濾清潔體積 | 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 |
拌和電功率 | 1.5 | 3.0 | 4.0 | 5.5 | 5.5 | 7.5 | 7.5 | 7.5 |
攪拌機發動機轉速 | 63 | 63 | 63 | 63 | 63 | 63 | 63 | 63 |
水蒸氣耗量 | 100 | 180 | 225 | 300 | 330 | 380 | 420 | 495 |
冷卻塔水耗量 | 2.6 | 4.2 | 4.2 | 6.8 | 6.8 | 8.5 | 8.5 | 10 |