化工进展
化工進展
화공진전
CHEMICAL INDUSTRY AND ENGINEERING PROGRESS
2014年
10期
2700-2706
,共7页
正渗透%膜%分离%选择性%三乙酸纤维素
正滲透%膜%分離%選擇性%三乙痠纖維素
정삼투%막%분리%선택성%삼을산섬유소
forward osmosis%membranes%separation%selectivity%cellulose triacetate
以三乙酸纤维素(CTA)为膜材料,1,4-二氧六环、丙酮为溶剂,甲醇、乳酸为添加剂,采用相转换法制备了三乙酸纤维素正渗透膜。研究了不同1,4-二氧六环/丙酮配比、添加剂乳酸含量、挥发时间、膜厚度、热处理温度条件下正渗透膜性能的变化规律。研究表明,当采用纯水为原料液,0.56mol/L CaCl2为汲取液时,优化制备的CTA正渗透膜的水通量达到14.10L/(m2·h),溶质反扩散量为0.031mol/(m2·h);采用0.1mol/L NaCl为原料液,4mol/L葡萄糖为汲取液时,优化制备的CTA正渗透膜的水通量保持在5L/(m2·h)以上,对NaCl的截留率大于99%。CTA正渗透膜相比于HTI膜,具有较高的亲水性、水通量、截留率,稳定性更好。
以三乙痠纖維素(CTA)為膜材料,1,4-二氧六環、丙酮為溶劑,甲醇、乳痠為添加劑,採用相轉換法製備瞭三乙痠纖維素正滲透膜。研究瞭不同1,4-二氧六環/丙酮配比、添加劑乳痠含量、揮髮時間、膜厚度、熱處理溫度條件下正滲透膜性能的變化規律。研究錶明,噹採用純水為原料液,0.56mol/L CaCl2為伋取液時,優化製備的CTA正滲透膜的水通量達到14.10L/(m2·h),溶質反擴散量為0.031mol/(m2·h);採用0.1mol/L NaCl為原料液,4mol/L葡萄糖為伋取液時,優化製備的CTA正滲透膜的水通量保持在5L/(m2·h)以上,對NaCl的截留率大于99%。CTA正滲透膜相比于HTI膜,具有較高的親水性、水通量、截留率,穩定性更好。
이삼을산섬유소(CTA)위막재료,1,4-이양륙배、병동위용제,갑순、유산위첨가제,채용상전환법제비료삼을산섬유소정삼투막。연구료불동1,4-이양륙배/병동배비、첨가제유산함량、휘발시간、막후도、열처리온도조건하정삼투막성능적변화규률。연구표명,당채용순수위원료액,0.56mol/L CaCl2위급취액시,우화제비적CTA정삼투막적수통량체도14.10L/(m2·h),용질반확산량위0.031mol/(m2·h);채용0.1mol/L NaCl위원료액,4mol/L포도당위급취액시,우화제비적CTA정삼투막적수통량보지재5L/(m2·h)이상,대NaCl적절류솔대우99%。CTA정삼투막상비우HTI막,구유교고적친수성、수통량、절류솔,은정성경호。
Cellulose triacetate based membranes for forward osmosis were prepared by immersion precipitation. The polymer solution consisted of cellulose triacetate as the membrane material, 1,4-dioxane and acetone as solvent,methanol and lactic acid as additives. Casting composition and preparation conditions-1,4-dioxane/acetone ratio,lactic acid content,evaporation time,casting thickness and annealing temperature-were tested for their effects on membrane performance. The optimized membrane showed 14.10L/(m2·h) water flux and 0.031mol/(m2·h) reverse solute flux using a feed solution of pure water and draw solution of 0.56mol/L CaCl2. When 0.1mol/L NaCl was used as the feed solution and 4mol/L glucose was used as the draw solution,water flux was above 5L/(m2·h) and rejection for NaCl was above 99%. The optimized membrane had a more hydrophilic surface, higher water flux,higher salt resistance and better membrane performance than the HTI membrane.