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转酯化

转酯化的相关文献在1997年到2022年内共计107篇,主要集中在化学工业、化学、石油、天然气工业 等领域,其中期刊论文58篇、会议论文3篇、专利文献6569篇;相关期刊43种,包括百色学院学报、中山大学学报(自然科学版)、生物工程学报等; 相关会议3种,包括2010国际农业工程大会、第六届全国化学工程与生物化工年会、第三届全国研究生生物质能研讨会等;转酯化的相关文献由256位作者贡献,包括严宗诚、陈砺、吕鹏梅等。

转酯化—发文量

期刊论文>

论文:58 占比:0.87%

会议论文>

论文:3 占比:0.05%

专利文献>

论文:6569 占比:99.08%

总计:6630篇

转酯化—发文趋势图

转酯化

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  • 张晓东
  • 杨立荣
  • 谭天伟
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    • Justina Gaidukevič; Jurgis Barkauskas; Anna Malaika; Paulina Rechnia-Gorący; Aleksandra Możdżyńska; Vitalija Jasulaitienė; Mieczysław Kozłowski
    • 摘要: 本文研究了不同石墨烯基材料用作转酯化反应制备生物柴油催化剂的性能.将磺酸基或磷酸盐基嫁接到热还原的氧化石墨烯表面,制备了固体酸石墨烯基样品.并采用扫描电镜、X射线衍射、热重分析、X射线光电子能谱、N2吸附-脱附法、电位滴定法、元素分析以及红外光谱法对所制样品进行了全面表征.将所制样品用于130 oC带压力的条件下菜籽油与甲醇转酯化反应中,并将其催化活性与商用的多相酸催化剂Amberlyst-15的进行了比较.结果表明,所有改进的样品在转酯化反应中均表现出催化活性,但各样品上生物柴油产率差别较大.其中以苯二氮磺酸基功能化的热还原氧化石墨烯样品上脂肪酸甲酯产率最高,反应6 h后达70%,也明显高于商用催化剂Amberlyst-15.该样品也表现出良好的重复使用性能.
    • 王东军; 姜伟; 赵仲阳; 金书含; 何昌洪; 何玉莲
    • 摘要: The biodiesel produced by oils and fatsplays an important role in reducing the environmental pressure, optimizing the energy structure, alleviating the energy crisis and promoting the sustainable development of the economy. Thispaper briefly described the feedstocks and technical principles of the industrial production of biodiesel with emphasis on the transesterification and hydrogenation processes, including the progress in the catalysts for them. The present situation and existing problems of biodiesel production were analyzed, and the reasonable and scientific development suggestions were put forward.%油脂制备的生物柴油对减轻环境压力、优化能源结构、缓解能源危机及促进经济可持续发展具有重要作用,文章简要阐述了油脂制备生物柴油工业化生产原料、技术原理,着重指出了工业上有代表性的油脂转酯化法、加氢法生产生物柴油技术工艺,同时介绍了转酯化催化剂、加氢催化剂的研究进展,分析了油脂制备生物柴油工业化现状及存在的问题,提出了合理、科学的发展建议.
    • 成磊; 李泉; 葛保胜; 于道永
    • 摘要: We studied transesterification of peanut oil with methanol catalyzed by immobilized Pseudomonas cep acia lipase ,investigated the effects of reaction time ,reaction temperature ,enzyme dosage ,methanol-oil ratio , and water content on transesterification rate ,and discussed transesterification characteristics of major fatty acids in peanut oil .The optimal transesterification conditions were obtained by an orthogonal experiment as follows :peanut oil dosage of 3 g ,reaction time of 48 h ,reaction temperature of 35 °C ,enzyme dosage of 450 mg ,metha-nol-oil ratio of 3:1 ,and water content of 8% .Under above conditions ,the transesterification rate of peanut oil reached 90 .58% .T he significance of influencing factors and the optimal reaction conditions for transesterifica-tion of major fatty acids in peanut oil were not identical ,which indicated that different fatty acids in peanut oil had different transesterification characteristics catalyzed by immobilized Pseudomonas cep acia lipase.%利用固定化洋葱假单胞菌脂肪酶催化花生油与甲醇进行酯交换反应,考察了反应时间、反应温度、酶用量、醇油比、含水量等因素对转酯化率的影响,研究了花生油中主要脂肪酸的酶催化转酯化特性.通过正交实验确定最优转酯化条件为:花生油用量3 g、反应时间48 h、反应温度35°C 、酶用量450 mg、醇油比3:1、含水量8%,在此条件下,花生油转酯化率达到90.58%.花生油中主要脂肪酸转酯化的影响因素显著性以及转酯化的最优反应条件并不相同,表明花生油中不同脂肪酸的固定化洋葱假单胞菌脂肪酶催化转酯化特性有所不同.
    • 高可可12; 陈沁1; 胡雁鸣2; 郑强1; 谢海波1
    • 摘要: 基于1,8-二氮杂二环十一碳-7-烯(DBU)存在下,纤维素与CO2在二甲基亚砜(DMSO)中反应生成纤维素可逆聚离子液体反应的原理,实现纤维素溶解与活化,同时实现原位DBU催化棉浆纤维素与苯甲酸甲酯的转酯化反应,成功制备了不同取代度的纤维素苯甲酸酯.探索了不同反应时间、反应温度、苯甲酸甲酯与纤维素脱水葡萄糖单元(AGU)比例对纤维素取代度的影响,并对纤维素苯甲酸酯进行核磁共振氢谱、碳谱、红外光谱、差示扫描量热法(DSC)、热重分析(TGA)及X射线衍射(XRD)表征.结果表明,转酯化反应温度为115°C,苯甲酸甲酯与AGU比例为5:1,反应24h时取代度最高能达到0.53.和纤维素相比,纤维素苯甲酸酯有明显的玻璃化转变温度,但其热稳定性下降.
    • 黄贤校; 邹彦平; 高媛媛; 杨苗
    • 摘要: With shea olein as raw material, low acid value shea olein was obtained by methyl esterification, then triglyceride was transformed into fatty acid methyl ester by transesterification. After the fatty acid methyl ester and bioactive compounds were separated into light fraction and heavy fraction by molecular dis-tillation, the heavy fraction ( bioactive compounds) was crystallized with solvent to further improve the con-tent of active compounds. The optimal methyl esterification conditions were determined by single factor ex-periment as follows:reaction temperature 70°C, reaction time 3 h, mass ratio of methanol to oil 3∶10, dos-age of concentrated sulfuric acid 3%. Under these conditions, acid value of shea olein reduced from 56. 1 mgKOH/g to 2. 1 mgKOH/g, and the conversion rate of free fatty acids reached 96. 3%. The optimal con-ditions of molecular distillation were obtained by single factor experiment as follows:feed rate 2 mL/min, scraper speed 250 r/min, distillation temperature 150°C, vacuum degree 0. 1 Pa. Under these conditions, the recovery of the bioactive compounds in heavy fraction was 95. 9% and the content of bioactive com-pounds was up to 68. 8%. By the methods of methyl esterification, transesterification, molecular distillation and crystallization, the total content of triterpene and sterol in the product could reach 69. 80%, and the content of bioactive compounds could achieve 83. 18%.%以乳木果液油为原料,经甲酯化后得到低酸值的乳木果液油,通过转酯化把甘三酯转化为脂肪酸甲酯,通过分子蒸馏把脂肪酸甲酯和生物活性物质分为轻组分和重组分,重组分(生物活性物质)再经过溶剂结晶进一步提高生物活性物质含量。通过单因素实验确定较好的甲酯化工艺条件为:反应温度70°C,反应时间3 h,醇油质量比3∶10,浓硫酸添加量3%;在此条件下,乳木果液油的酸值(KOH)从56.1 mg/g降至2.1 mg/g,游离脂肪酸转化率达到96.3%。通过单因素实验确定的较佳分子蒸馏条件为:进料速率2 mL/min,刮膜转速250 r/min,蒸馏温度150°C,真空度0.1 Pa;在此条件下蒸馏,生物活性物质在重组分中的回收率达95.9%,生物活性物质含量可达68.8%。乳木果液油经过甲酯化、转酯化、分子蒸馏和结晶得到的产品中三萜醇和甾醇总含量可达69.80%,生物活性物质含量可达83.18%。
    • 单锐; 陈冠益; 陈鸿; 颜蓓蓓
    • 摘要: 以廉价的稻壳(RH)为原料,制备了 K2CO3负载稻壳灰(RHA)的固体碱催化剂,用于催化制备生物柴油.利用 X-射线衍射(XRD)、N2吸脱附、X 射线能谱(EDS)对催化剂的结构进行了表征,并考察了 K2CO3负载量、催化剂用量、反应物的醇油摩尔比和反应时间等因素对生物柴油产率的影响以及催化剂的可重复性使用.实验结果表明:稻壳在800°C下焙烧后制备的K2CO3/HRA催化剂,当K2CO3负载量为50%、催化剂用量为16%、醇油摩尔比为12∶1、在60°C下反应70,min 后,生物柴油产率为92.6%.催化剂在重复使用5次以后,生物柴油产率降至66.8%,主要原因是催化剂中K元素的流失.%Rice husk ash as solid waste from agriculture was served as the support for K2CO3 to prepare solid base catalyst for biodiesel production. The structures of the catalysts were characterized by X-ray diffraction (XRD),N2 adsorption-desorption and energy dispersive X-ray spectroscopy (EDS). The effects of various parameters such as mass fraction of K2CO3 loading,catalyst loading,molar ratio of methanol to oil and reaction time on the yield of biodiesel and the catalyst reusability were investigated. The experimental results revealed by using the rice husk burned at 800°Cas the support,a maximum biodiesel yield of 92.6%was obtained under the optimal conditions with catalyst loading being 16%,molar ratio of methanol to oil 12∶1,reaction time being 70 min and K2CO3 loading being 50%.The biodiesel yield decreased to be 66.8%after five runs of reuse and the deactivation of the catalyst was mainly caused by potassium leaching in the reaction mixture.
    • 贾义刚; 刘维明; 倪潇; 黄和; 胡燚
    • 摘要: 研究了在有机相中脂肪酶催化转酯化反应动力学拆分左旋帕罗醇,考察了酶种类、溶剂、酰基供体、温度、底物与酰基供体摩尔比等因素对反应的影响。结果表明:以 Novozym 435为催化剂,在30°C下,以乙腈为反应溶剂,乙酸乙烯酯为酰基供体,底物浓度40mmol/L 及其与酰基供体摩尔比为1∶8时,反应8h 后,底物转化率为48.1%,ee s为53.3%,E 值为6.20。%The kinetic resolution of transesterification reaction of trans-paroxol catalyzed by lipase was studied in organic media.The influence factors including enzyme source,solvent,acyl donor, temperature,substrate and the molar ratio of substrate with acyl donor were researched.The optimal conditions were obtained as following:Acetonitrile as solvent, viny acetate as acyl donor,concentration of substrate of 40mmol/L,the molar ratio substrate with acyl donor of 1∶8 and reaction temperature 30°C.The conversion,the ees and the E value reached 48.1%,53.3%and 6.20 under the optimal conditions after 8h.
    • 周后波; 张庆英; 曹顺
    • 摘要: 生物柴油作为一种对环境友好的可再生燃料,对解决能源和环境问题具有重要意义,所以生物柴油技术得到广泛研究.文章综述了生物柴油制备的反应机理和运用酯交换反应制备生物柴油的几种方法的研究进展,并结合实际生产对其优缺点和研究趋势进行了归纳总结和展望.
    • 单锐; 陈冠益; 陈鸿; 颜蓓蓓
    • 摘要: 以廉价的稻壳(RH)为原料,制备了K2CO3负载稻壳灰(RHA)的固体碱催化剂,用于催化制备生物柴油.利用X-射线衍射(XRD)、N2吸脱附、X射线能谱(EDS)对催化剂的结构进行了表征,并考察了K2CO3负载量、催化剂用量、反应物的醇油摩尔比和反应时间等因素对生物柴油产率的影响以及催化剂的可重复性使用.实验结果表明:稻壳在800°C下焙烧后制备的K2CO3/HRA催化剂,当K2CO3负载量为50%、催化剂用量为16%、醇油摩尔比为12∶1、在60°C下反应70,min后,生物柴油产率为92.6%.催化剂在重复使用5次以后,生物柴油产率降至66.8%,主要原因是催化剂中K元素的流失.
    • 王丹; 李涛; 罗兴; 杨景昌
    • 摘要: 以羊毛脂为原料,采用甲醇钠、氢氧化钠2种催化剂,考察了反应温度、时间、催化剂用量、醇用量等因素对甲酯化的影响.结果表明:甲醇钠为催化剂时,在反应温度60°C、甲醇与羊毛脂质量比1.6、反应时间60 min、催化剂质量分数4%的条件下,酯转化率达到94.3%.用响应面法优化氢氧化钠为催化剂的羊毛脂甲酯化工艺,得到最佳工艺条件为:反应温度65.3°C、甲醇与羊毛脂质量比1.85、催化剂质量分数6%、反应时间90 min,在此条件下酯转化率可达94.2%.
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