
本(ben)(ben)(ben)機(ji)器(qi)可以(yi)選(xuan)擇于(yu)中草藥、調味品、所有的(de)制造(zao)業的(de)過熱(re)蒸汽、微(wei)壓、水煎、溫(wen)浸、熱(re)流回、強迫循環法、滲漉、果(guo)香油轉(zhuan)(zhuan)化成(cheng)及可揮發溶媒的(de)回收(shou)處(chu)理等好幾(ji)種方(fang)法操作(zuo)的(de)。安(an)全使用(yong)本(ben)(ben)(ben)機(ji)器(qi)能使轉(zhuan)(zhuan)化成(cheng)目(mu)的(de)更好、時短(duan)、藥液(ye)純度高。本(ben)(ben)(ben)機(ji)器(qi)摻(chan)(chan)和(he)器(qi)系統分旋轉(zhuan)(zhuan)式(shi)摻(chan)(chan)和(he)器(qi)和(he)槳式(shi)摻(chan)(chan)和(he)器(qi),時候(hou)本(ben)(ben)(ben)機(ji)器(qi)選(xuan)用(yong)品質,很廣用(yong)途于(yu)醫藥集(ji)團、調味品、所有等的(de)制造(zao)業。
1、收(shou)膏(gao)(gao)率(lv)比點能罐(guan)提升10~15%,止癢消炎軟膏(gao)(gao)囊括了(le)行之管(guan)用組分高(gao)1倍(bei)上。由在添(tian)(tian)加時中(zhong)(zhong)(zhong),熱的溶(rong)(rong)液累(lei)計(ji)加到藥(yao)上面,由上至(zhi)下飛(fei)速(su)經(jing)過中(zhong)(zhong)(zhong)草(cao)中(zhong)(zhong)(zhong)中(zhong)(zhong)(zhong)藥(yao)村層,溶(rong)(rong)化中(zhong)(zhong)(zhong)草(cao)中(zhong)(zhong)(zhong)中(zhong)(zhong)(zhong)藥(yao)村中(zhong)(zhong)(zhong)的溶(rong)(rong)質(zhi)(zhi),中(zhong)(zhong)(zhong)草(cao)中(zhong)(zhong)(zhong)中(zhong)(zhong)(zhong)藥(yao)村中(zhong)(zhong)(zhong)的溶(rong)(rong)質(zhi)(zhi)硫含鋅(xin)(xin)量與溶(rong)(rong)液中(zhong)(zhong)(zhong)溶(rong)(rong)質(zhi)(zhi)硫含鋅(xin)(xin)量保證了(le)高(gao)系數(shu),中(zhong)(zhong)(zhong)草(cao)中(zhong)(zhong)(zhong)中(zhong)(zhong)(zhong)藥(yao)村中(zhong)(zhong)(zhong)的溶(rong)(rong)質(zhi)(zhi)飛(fei)速(su)總(zong)混度,就此完完全全總(zong)混度,則行之管(guan)用組分添(tian)(tian)加率(lv)高(gao),故收(shou)膏(gao)(gao)率(lv)高(gao)、止癢消炎軟膏(gao)(gao)里行之管(guan)用含氧(yang)量硫含鋅(xin)(xin)量高(gao)。
2、猶豫溶質高速公路(lu)溶出度,提現期限短,濃縮咖啡液與(yu)提現同步操作通過,故中草藥材到濃縮咖啡液消炎軟膏只需7~8h,儀器運用率高。
3、生產機(ji)器設備(bei)簡(jian)單、占地面積小、生產機(ji)器設備(bei)靈活(huo)運(yun)用率(lv)高,故的投資省。
4、提取只加1次溶劑,在一套密封設備內循環使用,藥渣里的溶劑基本上能回收出來,故溶劑用量比多能提取罐少30%以上,消耗率可降50~70%,這為用有機溶劑提取、提純中藥中有效成分鋪平了道路。
5、隨著溶縮提煉(lian)的多次水蒸氣作(zuo)分離出的主軸,抽入溶縮提煉(lian)器的分離出液與溶縮提煉(lian)同溫(wen)度因素,可節藥50%綜上(shang)所述(shu)的水蒸氣,運(yun)(yun)營很簡易,減(jian)低了運(yun)(yun)營師。

名貴藥材多的功(gong)能(neng)轉化成溶縮(suo)機(ji)器設備主耍技(ji)木因素
款型 | TQ0.5 | TQ1.0 | TQ2.0 | TQ3.0 | TQ4.0 | TQ5.0 | TQ6.0 | TQ8.0 |
全面積L | 560 | 1300 | 2300 | 3600 | 4400 | 5560 | 6500 | 8900 |
堿罐水壓 | 0.09 | |||||||
夾套壓差 | 0.3 | |||||||
采暖器占地 | 2.1 | 4 | 5 | 6.8 | 7.3 | 8.5 | 9.5 | 11 |
空氣冷卻體積 | 3.0 | 5.0 | 5.0 | 8.0 | 8.0 | 10.0 | 10.0 | 12.0 |
蒸發總面積 | 1.0 | 1.0 | 1.0 | 1.0 | 1.0 | 1.5 | 1.5 | 1.5 |
凈化綠地面積 | 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 |
混合輸出 | 1.5 | 3.0 | 4.0 | 5.5 | 5.5 | 7.5 | 7.5 | 7.5 |
摻和帶速 | 63 | 63 | 63 | 63 | 63 | 63 | 63 | 63 |
空氣壓縮耗量 | 100 | 180 | 225 | 300 | 330 | 380 | 420 | 495 |
閉式冷卻塔水耗量 | 2.6 | 4.2 | 4.2 | 6.8 | 6.8 | 8.5 | 8.5 | 10 |