中藥提取設備
- 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
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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。
二級水壓(ya)縮空(kong)氣(qi)再以(yi)后持續上(shang)升,經(jing)制冷(leng)器制冷(leng)成(cheng)(cheng)(cheng)熱制冷(leng)液(ye),下(xia)滑到去(qu)(qu)(qu)除(chu)(chu)(chu)罐中(zhong)(zhong)作新石油(you)(you)醚(mi)(mi)(mi)加到藥上(shang)面(mian),新石油(you)(you)醚(mi)(mi)(mi)由上(shang)而下(xia)快速(su)利用(yong)(yong)藥草層(ceng)到去(qu)(qu)(qu)除(chu)(chu)(chu)罐尾部(bu),藥草中(zhong)(zhong)的(de)(de)可融(rong)掉(diao)(diao)性能夠含量融(rong)掉(diao)(diao)于去(qu)(qu)(qu)除(chu)(chu)(chu)罐中(zhong)(zhong)石油(you)(you)醚(mi)(mi)(mi)。去(qu)(qu)(qu)除(chu)(chu)(chu)液(ye)經(jing)抽濾(lv)管(guan)抽入萃(cui)取(qu)(qu)器、萃(cui)取(qu)(qu)型成(cheng)(cheng)(cheng)的(de)(de)二級水壓(ya)縮空(kong)氣(qi)又送達去(qu)(qu)(qu)除(chu)(chu)(chu)罐作熱原和新石油(you)(you)醚(mi)(mi)(mi),這么型成(cheng)(cheng)(cheng)的(de)(de)新石油(you)(you)醚(mi)(mi)(mi)大流(liu)失去(qu)(qu)(qu)除(chu)(chu)(chu),故藥草中(zhong)(zhong)溶質體積孔(kong)隙率與石油(you)(you)醚(mi)(mi)(mi)中(zhong)(zhong)含溶質體積孔(kong)隙率實現高(gao)等度,藥草中(zhong)(zhong)的(de)(de)溶質快速(su)總混,甚(shen)至可以(yi)總混(去(qu)(qu)(qu)除(chu)(chu)(chu)液(ye)透明色(se)(se)),這時,去(qu)(qu)(qu)除(chu)(chu)(chu)液(ye)停止工作抽入萃(cui)取(qu)(qu)器,萃(cui)取(qu)(qu)的(de)(de)二級水壓(ya)縮空(kong)氣(qi)轉送制冷(leng)器,萃(cui)取(qu)(qu)再以(yi)后開展,甚(shen)至萃(cui)取(qu)(qu)成(cheng)(cheng)(cheng)需要(yao)百分比(1.2~1.34)的(de)(de)膏藥,釋放被用(yong)(yong)。去(qu)(qu)(qu)除(chu)(chu)(chu)罐中(zhong)(zhong)的(de)(de)透明色(se)(se)液(ye)態,可倒出貯罐作下(xia)批復文(wen)件用(yong)(yong),藥渣(zha)從(cong)出渣(zha)門排掉(diao)(diao),如果是(shi)用(yong)(yong)有機(ji)會石油(you)(you)醚(mi)(mi)(mi)去(qu)(qu)(qu)除(chu)(chu)(chu),則先加通常的(de)(de)水,開連(lian)通和夾套(tao)水壓(ya)縮空(kong)氣(qi),收廢石油(you)(you)醚(mi)(mi)(mi)后,將(jiang)渣(zha)排掉(diao)(diao)。
中草藥提取罐 提取濃縮設備 精油提取設備主要技術參數
規格 | 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 |
罐中有壓力 | 0.09 | |||||||
夾套負壓 | 0.3 | |||||||
采暖器戶型 | 2.1 | 4 | 5 | 6.8 | 7.3 | 8.5 | 9.5 | 11 |
空調蒸發器空間 | 3.0 | 5.0 | 5.0 | 8.0 | 8.0 | 10.0 | 10.0 | 12.0 |
待冷卻使用面積 | 1.0 | 1.0 | 1.0 | 1.0 | 1.0 | 1.5 | 1.5 | 1.5 |
濾水綠地面積 | 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 |
混和額定功率 | 1.5 | 3.0 | 4.0 | 5.5 | 5.5 | 7.5 | 7.5 | 7.5 |
均勻攪拌電機轉速 | 63 | 63 | 63 | 63 | 63 | 63 | 63 | 63 |
蒸汽式耗量 | 100 | 180 | 225 | 300 | 330 | 380 | 420 | 495 |
冷卻后水耗量 | 2.6 | 4.2 | 4.2 | 6.8 | 6.8 | 8.5 | 8.5 | 10 |