苦瓜(gua)分離出(chu)物生產(chan)的方式(shi)機(ji)械(xie)專(zhuan)用(yong)(yong)設備,苦瓜(gua)多糖(tang)生產(chan)的方式(shi)機(ji)械(xie)專(zhuan)用(yong)(yong)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(ji)蒸氣(qi)(qi)式依然(ran)回(hui)升(sheng),經(jing)冷卻(que)(que)塔器(qi)(qi)冷卻(que)(que)塔成熱(re)冷卻(que)(que)塔液(ye)(ye)(ye)(ye)(ye),暴(bao)跌到(dao)分(fen)(fen)離(li)出(chu)罐中(zhong)(zhong)(zhong)作(zuo)(zuo)新(xin)萃取(qu)劑(ji)(ji)加(jia)(jia)到(dao)藥(yao)(yao)表面,新(xin)萃取(qu)劑(ji)(ji)由(you)上而(er)下(xia)公(gong)路(lu)的(de)(de)采用名貴(gui)(gui)中(zhong)(zhong)(zhong)藥(yao)(yao)村(cun)層到(dao)分(fen)(fen)離(li)出(chu)罐底層,名貴(gui)(gui)中(zhong)(zhong)(zhong)藥(yao)(yao)村(cun)中(zhong)(zhong)(zhong)的(de)(de)可無水磷酸氫更好含量(liang)熔化分(fen)(fen)解(jie)于分(fen)(fen)離(li)出(chu)罐中(zhong)(zhong)(zhong)萃取(qu)劑(ji)(ji)。分(fen)(fen)離(li)出(chu)液(ye)(ye)(ye)(ye)(ye)經(jing)抽濾管抽入(ru)提(ti)(ti)(ti)(ti)液(ye)(ye)(ye)(ye)(ye)咖(ka)(ka)啡提(ti)(ti)(ti)(ti)煉(lian)器(qi)(qi)、提(ti)(ti)(ti)(ti)液(ye)(ye)(ye)(ye)(ye)咖(ka)(ka)啡提(ti)(ti)(ti)(ti)煉(lian)產生了的(de)(de)二級(ji)蒸氣(qi)(qi)式又寄回(hui)分(fen)(fen)離(li)出(chu)罐作(zuo)(zuo)熱(re)力(li)和(he)新(xin)萃取(qu)劑(ji)(ji),這(zhe)類確立的(de)(de)新(xin)萃取(qu)劑(ji)(ji)大流入(ru)分(fen)(fen)離(li)出(chu),故名貴(gui)(gui)中(zhong)(zhong)(zhong)藥(yao)(yao)村(cun)中(zhong)(zhong)(zhong)溶質導熱(re)系(xi)(xi)數(shu)與(yu)萃取(qu)劑(ji)(ji)中(zhong)(zhong)(zhong)含溶質導熱(re)系(xi)(xi)數(shu)始終(zhong)保持高(gao)梯度方向(xiang),名貴(gui)(gui)中(zhong)(zhong)(zhong)藥(yao)(yao)村(cun)中(zhong)(zhong)(zhong)的(de)(de)溶質公(gong)路(lu)的(de)(de)總混(hun),終(zhong)將(jiang)根(gen)本總混(hun)(分(fen)(fen)離(li)出(chu)液(ye)(ye)(ye)(ye)(ye)沒顏(yan)色(se)),此刻,分(fen)(fen)離(li)出(chu)液(ye)(ye)(ye)(ye)(ye)暫停抽入(ru)提(ti)(ti)(ti)(ti)液(ye)(ye)(ye)(ye)(ye)咖(ka)(ka)啡提(ti)(ti)(ti)(ti)煉(lian)器(qi)(qi),提(ti)(ti)(ti)(ti)液(ye)(ye)(ye)(ye)(ye)咖(ka)(ka)啡提(ti)(ti)(ti)(ti)煉(lian)的(de)(de)二級(ji)蒸氣(qi)(qi)式轉送冷卻(que)(que)塔器(qi)(qi),提(ti)(ti)(ti)(ti)液(ye)(ye)(ye)(ye)(ye)咖(ka)(ka)啡提(ti)(ti)(ti)(ti)煉(lian)依然(ran)進行,終(zhong)將(jiang)提(ti)(ti)(ti)(ti)液(ye)(ye)(ye)(ye)(ye)咖(ka)(ka)啡提(ti)(ti)(ti)(ti)煉(lian)成必(bi)須(xu)比重(zhong)是什么(me)(1.2~1.34)的(de)(de)膏藥(yao)(yao),拉(la)出(chu)被(bei)用。分(fen)(fen)離(li)出(chu)罐中(zhong)(zhong)(zhong)的(de)(de)沒顏(yan)色(se)全自動,可裝入(ru)貯罐作(zuo)(zuo)下(xia)批準用,藥(yao)(yao)渣從出(chu)渣門排掉,要是用巧妙萃取(qu)劑(ji)(ji)分(fen)(fen)離(li)出(chu),則先加(jia)(jia)恰當的(de)(de)水,開(kai)直達和(he)夾套蒸氣(qi)(qi)式,回(hui)收處理萃取(qu)劑(ji)(ji)后,將(jiang)渣排掉。

首(shou)要工藝叁數
應用 | 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 |
罐中負荷 | 0.09 | |||||||
夾套壓力值 | 0.3 | |||||||
煮沸表面積 | 2.1 | 4 | 5 | 6.8 | 7.3 | 8.5 | 9.5 | 11 |
氣液分離器戶型 | 3.0 | 5.0 | 5.0 | 8.0 | 8.0 | 10.0 | 10.0 | 12.0 |
急冷體積 | 1.0 | 1.0 | 1.0 | 1.0 | 1.0 | 1.5 | 1.5 | 1.5 |
過濾系統占地面積 | 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 |
混合電率 | 1.5 | 3.0 | 4.0 | 5.5 | 5.5 | 7.5 | 7.5 | 7.5 |
拌和轉速比 | 63 | 63 | 63 | 63 | 63 | 63 | 63 | 63 |
水汽耗量 | 100 | 180 | 225 | 300 | 330 | 380 | 420 | 495 |
放置冷卻液耗量 | 2.6 | 4.2 | 4.2 | 6.8 | 6.8 | 8.5 | 8.5 | 10 |