甜瓜果提取物加工設備
- 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
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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。
重新(xin)蒸(zheng)(zheng)氣延(yan)續(xu)上(shang)升的,經空氣急(ji)冷器(qi)(qi)空氣急(ji)冷成(cheng)(cheng)熱空氣急(ji)冷液,回降到去(qu)(qu)除(chu)罐(guan)體(ti)作(zuo)(zuo)新(xin)容(rong)(rong)(rong)劑(ji)(ji)加(jia)到藥上(shang)面,新(xin)容(rong)(rong)(rong)劑(ji)(ji)由(you)上(shang)而下速度(du)順(shun)利通(tong)過名(ming)貴藥才層到去(qu)(qu)除(chu)罐(guan)底邊,名(ming)貴藥才中的可可溶有(you)效(xiao)性成(cheng)(cheng)分表熔化分解于(yu)去(qu)(qu)除(chu)罐(guan)體(ti)容(rong)(rong)(rong)劑(ji)(ji)。去(qu)(qu)除(chu)液經抽(chou)濾管(guan)抽(chou)入(ru)高(gao)(gao)(gao)(gao)濃器(qi)(qi)、高(gao)(gao)(gao)(gao)濃帶來(lai)(lai)的重新(xin)蒸(zheng)(zheng)氣又送達去(qu)(qu)除(chu)罐(guan)作(zuo)(zuo)熱環境(jing)和新(xin)容(rong)(rong)(rong)劑(ji)(ji),這些(xie)型成(cheng)(cheng)的新(xin)容(rong)(rong)(rong)劑(ji)(ji)大循環去(qu)(qu)除(chu),故名(ming)貴藥才中溶質(zhi)孔隙率(lv)與容(rong)(rong)(rong)劑(ji)(ji)中含溶質(zhi)孔隙率(lv)實現高(gao)(gao)(gao)(gao)梯度(du)方(fang)向,名(ming)貴藥才中的溶質(zhi)速度(du)總(zong)混(hun),就此仍然總(zong)混(hun)(去(qu)(qu)除(chu)液透(tou)(tou)明色透(tou)(tou)明),同(tong)時,去(qu)(qu)除(chu)液已(yi)停(ting)抽(chou)入(ru)高(gao)(gao)(gao)(gao)濃器(qi)(qi),高(gao)(gao)(gao)(gao)濃的重新(xin)蒸(zheng)(zheng)氣轉送急(ji)冷器(qi)(qi),高(gao)(gao)(gao)(gao)濃延(yan)續(xu)使(shi)用(yong)(yong)(yong),就此高(gao)(gao)(gao)(gao)濃成(cheng)(cheng)是(shi)需要比重怎么算(1.2~1.34)的軟膏,釋放出(chu)來(lai)(lai)被用(yong)(yong)(yong)。去(qu)(qu)除(chu)罐(guan)體(ti)的透(tou)(tou)明色透(tou)(tou)明氣體(ti),可加(jia)入(ru)貯罐(guan)作(zuo)(zuo)下批示用(yong)(yong)(yong),藥渣(zha)從出(chu)渣(zha)門排(pai)掉,假如用(yong)(yong)(yong)可揮發容(rong)(rong)(rong)劑(ji)(ji)去(qu)(qu)除(chu),則先加(jia)有(you)益健康的水,開直通(tong)式和夾套蒸(zheng)(zheng)氣,收集容(rong)(rong)(rong)劑(ji)(ji)后,將渣(zha)排(pai)掉。
中(zhong)草藥材(cai)多模(mo)塊導入(ru)高濃專用設備 綠植的導入(ru)罐(guan)基本能力參(can)數指(zhi)標
尺寸 | 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 |
罐里的壓力 | 0.09 | |||||||
夾套阻力 | 0.3 | |||||||
進行加熱總面積 | 2.1 | 4 | 5 | 6.8 | 7.3 | 8.5 | 9.5 | 11 |
空調蒸發器戶型面積 | 3.0 | 5.0 | 5.0 | 8.0 | 8.0 | 10.0 | 10.0 | 12.0 |
制冷表面積 | 1.0 | 1.0 | 1.0 | 1.0 | 1.0 | 1.5 | 1.5 | 1.5 |
過濾清潔建筑面積 | 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 |
攪拌機工作效率 | 1.5 | 3.0 | 4.0 | 5.5 | 5.5 | 7.5 | 7.5 | 7.5 |
打料轉動速度 | 63 | 63 | 63 | 63 | 63 | 63 | 63 | 63 |
蒸汽發生器耗量 | 100 | 180 | 225 | 300 | 330 | 380 | 420 | 495 |
急冷水耗量 | 2.6 | 4.2 | 4.2 | 6.8 | 6.8 | 8.5 | 8.5 | 10 |