化工技术与开发
化工技術與開髮
화공기술여개발
TECHNOLOGY & DVELOPMENT OF CHEMICAL INDUSTRY
2013年
12期
11-14
,共4页
刘贤响%刘姣%苏胜培%尹笃林
劉賢響%劉姣%囌勝培%尹篤林
류현향%류교%소성배%윤독림
活性炭%负载型%固体碱%催化%酯交换
活性炭%負載型%固體堿%催化%酯交換
활성탄%부재형%고체감%최화%지교환
activated carbon%supported%solid base%catalyze%transesteriifcation
采用浸渍法制备了活性炭负载KOH固体碱催化剂,考察了它们在三醋酸甘油酯与甲醇酯交换反应中的催化性能,及时间、温度、催化剂用量、醇酯摩尔比等因素对酯交换反应的影响。结果表明,当醇酯比为9∶1,催化剂用量为0.3g(三醋酸甘油酯为0.02mol),KOH浸渍液浓度为20.0wt%,反应温度为65℃,反应1.0h,三醋酸甘油酯转化率可达到94.7%。该工艺操作简单,催化剂可以回收,过程无三废污染。
採用浸漬法製備瞭活性炭負載KOH固體堿催化劑,攷察瞭它們在三醋痠甘油酯與甲醇酯交換反應中的催化性能,及時間、溫度、催化劑用量、醇酯摩爾比等因素對酯交換反應的影響。結果錶明,噹醇酯比為9∶1,催化劑用量為0.3g(三醋痠甘油酯為0.02mol),KOH浸漬液濃度為20.0wt%,反應溫度為65℃,反應1.0h,三醋痠甘油酯轉化率可達到94.7%。該工藝操作簡單,催化劑可以迴收,過程無三廢汙染。
채용침지법제비료활성탄부재KOH고체감최화제,고찰료타문재삼작산감유지여갑순지교환반응중적최화성능,급시간、온도、최화제용량、순지마이비등인소대지교환반응적영향。결과표명,당순지비위9∶1,최화제용량위0.3g(삼작산감유지위0.02mol),KOH침지액농도위20.0wt%,반응온도위65℃,반응1.0h,삼작산감유지전화솔가체도94.7%。해공예조작간단,최화제가이회수,과정무삼폐오염。
Transesteriifcation of glycerol triacetate and methanol catalyed by KOH supported on activated carbon was studied. The catalyst was prepared by impregnation and had a high catalysis activity. Effects of some factors on the transesteriifcation were inves-tigated systematically and reaction conditions were optimized. The optimized reaction conditions on the catalyst were:molar ratio of methanol to oil 9:1, the amount of catalyst 0.3g(the amount of glycerol triacetate 0.02mol), the consistency of KOH 20.0wt%, reac-tion temperature 65℃and reaction time 1.0h, under these conditions the conversion of biodiesel reached 94.7%. The new technology featured simplicity, reusable catalyst, zero pollution.