°</sup>C 、真空壓力 0.09MPa 和進料體積流量 600L/h ;當進料溫度從 40% 升至 60<sup>°</sup>C 時,系統(tǒng)運行末期膜通量相對初始值的減小率從 71.05% 增至 79.18% ,當真空壓力從 0.07MPa 增至 0.09MPa 時,該減小率從 71.63% 增至 79.18% ,當進料體積流量從 400L/h 增至 600L/h 時,該減小率從 83.49% 減至 79.18% ;進料流量增大會減緩膜污染,進料溫度升高或真空壓力增大會加劇膜污染。-龍源期刊網(wǎng)" />

特黄三级爱爱视频|国产1区2区强奸|舌L子伦熟妇aV|日韩美腿激情一区|6月丁香综合久久|一级毛片免费试看|在线黄色电影免费|国产主播自拍一区|99精品热爱视频|亚洲黄色先锋一区

真空膜蒸餾濃縮黃芩苷提取液過程中的膜污染機制

  • 打印
  • 收藏
收藏成功


打開文本圖片集

中圖分類號:TU992.3 文獻標志碼:A

Membrane Fouling Mechanism During Concentration of Baicalin Extract by Using Vacuum Membrane Distillation Technology

SHAO Ruonan 1 ,YU Jun 2 ,ZHU Youbing 3 , LIU Chao 1 , LIU Guicail (1.School of Civil Engineering and Architecture,University of Jinan,Jinan 25OO22,Shandong,China; 2.Qingdao Jiaozhou Construction Engineering Design Co.,Ltd.,Qingdao 2663Oo,Shandong,China; 3.Shanghai Urban Construction and Municipal Engineering Group Co.,Ltd.,Shanghai 2Ooo65,China)

Abstract:To investigate membrane fouling issues in a vacuum membrane distilation system,membrane flux and baicalin retentionratio were selected as indicators to evaluate eficiencyof the system.Feed temperature,vacuum pressre,and feedflowrate were chosen as process parameters of the system,and orthogonal experiments wereused tooptimize the three processparameters.Onthebasis of theoptimized process parameters,efects of diferent process parameterson efficiencyof the system were explored. Morphology and elemental composition of membrane surface were analyzed by using scanning electron microscopy -X -ray energy dispersive spectroscopy to reveal intrinsic relationships between membrane fouling and processparameters.Theresultsshow that theoptimal process parameters for thesystem are feed temperature of 60 C ,vacuum pressure of O.09 MP a ,and feed volume flow rate of 600L/h . When the feed temperature increases from 40‰ to 60‰ ,decrease rate of membrane flux relative to the initial value at the end of system operation increases from 71.05% to 79.18% . When the vacuum pressure increases from O. O7 MPa to 0. O9 MPa, the decrease rate increases from 71.63% to 79.18% . When the feed volume flow rate increases from 4Oo L/h to 600L/h ,the decrease rate decreases from 83.49% to 79.18% . An increase in feed flow rate mitigates the membrane fouling,whereas an increase in feed temperature or vacuum pressure intensifies the membrane fouling.

Keywords:vacuum membrane distilation;membrane fouling mechanism;baicalin extract;orthogonal experiment;membrane flux;retention ratio

近年來,中藥產(chǎn)業(yè)在迎來新的發(fā)展機遇的同時也面臨許多挑戰(zhàn),例如,中藥濃縮工序的水資源消耗大,有效成分被高溫破壞等[1]。(剩余9205字)

monitor