磷钨杂多酸盐催化氧化环己烯合成己二酸的研究
详细信息    本馆镜像全文|  推荐本文 |  |   获取CNKI官网全文
摘要
本文采用我国有着充足供应的过氧化氢(H_2O_2)为氧化剂,开展环己烯“绿色”氧化合成己二酸的研究。主要开展了如下几方面工作:
     1.针对烯烃—H_2O_2反应体系的特殊性,根据过渡金属催化氧化理论,进行了W(Ⅵ)价态催化剂分子水平上的结构设计。选用具有两亲性结构特点的季铵盐大阳离子,组装入具有特定W(Ⅵ)价态且有优良氧化活性和选择性的磷钨杂多酸根构成杂多酸季铵盐。用红外光谱法及元素分析法对设计、制备出的催化剂进行了表征。
     2.对H_2O_2氧化环己烯合成己二酸反应中的催化剂进行了筛选,结果表明磷钨酸十六烷基吡啶铵在不加入任何助剂时,就可达到较好的催化效果;
     3.将筛选出的催化剂用于催化H_2O_2氧化环己烯合成己二酸的反应,探讨了反应时间、反应温度、H_2O_2与环己烯摩尔比、催化剂加入量等对反应的影响。采用两次正交实验技术对反应条件进行优化,较适宜的反应条件为:反应时间5.5 h,反应温度90℃,n(H_2O_2):,n(环己烯)=5.5:1(以0.045 mol环己烯计),催化剂用量0.3 mmol。在该条件下实验重复性较好,己二酸的平均收率为73.88%,催化剂平均回收率为51.82%;
     4.将回收催化剂用于H_2O_2氧化环己烯合成己二酸的反应,在使用五次后,己二酸收率为70.89%,催化活性没有降低。将反应前后的催化剂进行红外光谱分析,发现回收催化剂的IR谱图与Keggin结构[PW_(12)O_(40)]~(3-)的IR谱带的位置、形状及相对强度有很好的一致性。
     本研究的工作特点在于:
     1.用“绿色”氧化剂H_2O_2进行环己烯氧化合成己二酸,其还原产物为水,无毒、无有害物质,不会给环境带来新的污染,为“绿色”合成过程;
     2.本文较系统的考察了不同的磷钨酸季铵盐的催化H_2O_2氧化环己烯的性能,且此类催化剂能够有大部分回收利用。
In this work, H_2O_2 with ample supply in China was used as oxidant in the synthesis of adipic acid from cyclohexene. And we mainly carried out the following aspects of research works:
    1. Based on transition metal catalytic oxidation theory, the structure design in the molecule of W(VI) catalyst was carried out in allusion to the particularity of cycloalkene-H_2O_2 reaction system. The amphiphilic structure of quaternary ammonium ions was encased in the excellent oxidation activity and selectiveity of phospho-tungstic acid root that formed quaternary ammonium salts of heteropolyacids. These quaternary ammonium salts of heteropolyacids were characterized by IR and elemental analysis.
    2. The filtering catalysts was used in the oxidation of cyclohexene to adipic acid. The result indicated that, in the absence of cocatalysts and acids, the catalytic activity have been very high if cation of quaternary ammonium phospho-tungstic acid was cetypyridine quaternary ammonium ions.
    3. The filtering catalysts was used in synthesis of adipic acid reaction. The key factors influencing the oxidation were also studied, such as reaction time, reaction temperature, mole ratio between H_2O_2 and cyclohexene, the amount of catalysts. Orthognol technique was used twice to optimize the reaction conditions, optimal synthesis condition was detailed as: reaction time 5.5 h, reaction temperature 90 ℃, n (H_2O_2): n (C_6H_(10)) - 5.5:1 (based on 0.045 mol cyclohexene), amounts of catalyst was 0.3 mmol. On the condition, the repetition of experiment result were better, the average yield of adipic acid was 73.88%, the average recovery rate of catalyst was 51.82%.
    4. The recovery catalyst was used in the oxidation of cyclohexene to adipic acid oxidized by H_2O_2. After catalysis cycle was quintic, catalysis activity didn't reduce. The new catalyst and the used catalyst were analysed by IR, and found IR spectra of recovery catalyst in accord with IR spectra of the Keggin structure of [PW_(12)O_(40)]~(3-).
    The points of this work were listed as follows:
    1. The green oxidant H_2O_2 is used in this work with the reductive production of H_2O. So there is no baneful materials to release and it can be ascribed to a kind of green progress.
    2. A series of quaternary ammonium salts of phospho-tungstic acids catalysts were systematically studied in the oxidation of cyclohexene. And the catalysts could be mostly recovered and utilized.
引文
[4] Castellan A, Bart J C J, Cavallaro S . Industrial production and use of adipic acid[J]. Catalysis Today, 1991, 9(3): 237-254.
    [1] 田文平,贾飞,张华.己二酸的国内外生产消费现状及发展[J].化工中间体,2005,2(3):1-4.
    [2] 陈银生,周亚明,王霞.己二酸市场状况及发展趋势[J].江苏化工,2005,33(3):69-71.
    [3] 周亚明.己二酸的市场、生产和发展前景[J].增塑剂,2004,18(3):9-16.
    [5] 化工百科全书编写组.化工百科全书[M].北京:科学出版社,2001,853.874.
    [6] 陈银生,周亚明,王霞.己二酸的各种生产工艺及污染物处理[J].皮革化工2005,22(3):30-34.
    [7] 戴新民.己二酸生产工艺技术路线评述[J].河南化工,1996,13(12):2-5
    [8] Tanabe K, Holderich W F. Industrial application of solid acid-base catalysts[J]. Applied Catalysis, A: General, 1999, 181(2): 399-434.
    [9] Chavan SA, Srinivas D, Ratnasamy P. Oxidation of cyclohexane, cyclohexanone and cyclohexanol to adipic acid by a Non-HNO3 route over Co/Mn cluster complexes[J]. Joumal of Catalysis, 2002, 212(1): 39-45.
    [10] Alessandro N , Liberatore L , Tonucci L , Morvillo A , Bressan M . Direct synthesis of adipic acid by monopersulfate oxidation of cyclohexane, cyclohexanone or cyclohexanol catalyzed by water-soluble transition-metal complexes[J]. New Journal of Chemistry, 2001, 25(10): 1319-1324.
    [11] Iwahama T, Syojyo K, Sakaguchi S, Ishii Y. Direct conversion of cyclohexane into adipic acid with molecular oxygen catalyzed by n-hydroxyphthalimide combined with Mn(acac)2 and Co(OAc)2[J]. Organic Process Research & Development, 1998, 2(4): 255-260.
    [12] Belkhir I, Germain A, Fajula F, Fache E. Role of cobalt molecular sieves in the liquid-phase oxidation of cyclohexane to adipic acid[J]. Journal of the Chemical Society, Faraday Transactions, 1998, 94(12), 1761-1764.
    [13] Belkhir I , Germain A , Fajula F , Fache E . Liquid-phase oxidation of cyclohexane to adipic acid catalyzed by manganese-containing zeolites[J]. Special Publication - Royal Society of Chemistry, 1998, 216: 48-53.
    [14] Belkhir I , Germain A , Fajula F , Fache E . Liquid-phase oxidation of cyclohexane to adipic acid catalyzed by cobalt-containing zeolites[J]. Studies in Surface Science and Catalysis, 1997, 110: 577-584.
    [15] Dugal M, Sankar G, Raja R, Thomas J M. Designing a heterogeneous catalyst for the production of adipic acid by aerial oxidation of cyclohexane[J]. Angewandte Chemic, International Edition, 2000, 39(13): 2310-2313.
    [16] Khan L , Khan S . Catalytic conversion of cyclohexane to adipic acid using oxygen under mild conditions[J]. Journal of Scientific and Industrial Research,1999.42(6): 336-338.
    [17] 潘强,盛琳,曹莉,赵军辉.己二酸生产工艺比较J].河南化工,2004,21(5):10.11[18] Kulsrestha G N , Shankar U , Sharma J S , Singh J . One-step oxidation of cyclohexane to adipic acid[J]. Journal of Chemical Technology and Biotechnology, 1991, 50(1): 57-65.
    [19] Steinmetz G R, Lafferty N L, Sumner C E, Jr. The cobalt/zirconium-catalyzed oxidation of cyclohexane to adipic acid[J]. Journal of Molecular Catalysis, 1988,49(1): 39-42.
    [20] Rao D G. A semiempirical model for the oxidation of cyclohexane[J]. Industrial & Engineering Chemistry Research, 1990, 29(4): 696-699.
    [21] Rao D G, Tirukkoyilur R S . liquid-phase oxidation of cyclohexane to adipic acid in a single stage[J]. Industrial & Engineering Chemistry Process Design and Development, 1986, 25(1): 299-304.
    [22] 何秉忠,朱圣东.己二酸生产技术与市场[J].化工时刊,2001,14(4):50-51.
    [23] 杨杏生.己二酸生产工艺的新进展[J].合成纤维工业,1995,18(2):39-45
    [24] 冯美平.丁二烯法制己二酸[J].合成纤维工业,1999,22(2):22-25
    [25] 饶兴鹤.世界己二酸产需现状和生产技术进展[J].中国石油和化工,2005,3(7):70-73.
    [26] 吴毓林,龙亚秋.合成化学——新世纪再创辉煌[J].大学化学,2001,16(3):1.6
    [27] Anastas P T , Williamson T C Green Chemistry-Designing for the Environment[Z]. ACS Symposium Seres, Amerrican Chemical Society Washington D.C., 1996.
    [28] 王艳丹,陈春茂,王海涛.钨酸钠催化环己酮清洁合成己二酸的研究[J].精细化工中间体,2004,34(5):39-42.
    [29] 王艳丹,陈春茂.N~a_2 W~O_4·2~H_2~O催化氧化环己醇/环己酮合成己二酸反应的研究[J].沈阳化工学院学报,2004,18(3):173·175
    [30] 张世刚,姜恒,宫红.催化氧化环己酮/环己醇清洁合成己二酸[J].化工科技,2002.10(5):4-6.
    [31] Razumovskii S D, Zaikov G E, Mushenko D V, Klimenko V L, Tsyskovskii V.K., Yur'ev Yu.N.. Dicarboxylic acids[P]. U.S. 3911000, 1975.
    [32] Habib R M, Chin-Yun Chiang, Philip S. Dicarboxylic acids from ozonolysis of cycloalkenes[J]. Journal Organic Chemistry, 1984, 49(15): 2780-2784.
    [33] Raja R, Thomas J M, Xu M, Harris K D M, Greenhill-Hooper M, Quill K. Highly efficient one-step conversion of cyclohexane to adipic acid using single-site heterogeneous catalysts[J]. Chemical Communications, 2006, (4):448-450.
    [34] Yuan Ying, Ji Hong-bing, Chen Yi-xia, Han Yong, Song Xu-feng, She Yuan-bin, Zhong Ru-gang. Oxidation ofcyclohexane to adipic acid using Fe-porphyrin as a biomimetic catalyst[J]. Organic Process Research & Development, 2004, 8(3):418-420.
    [35] 古玲,陈俊霞,吴玉龙,米镇涛.己二酸的洁净生产[J].化学工业与工程,2002,19(5):380-384.
    [36] Knoth W H, Parshall Jr, George W. Catalytic manutactuer tor adipic acid[P].U.S. 3701804, 1972.
    [37] Mooney W, Chauveau F. Catalytic photooxidation of cyclohexene by aqueous??ranyl/polymolybdate(VI) systems[J]. Journal of Chemical Society, Perkin Transaction 2, 1988, 8:1479-1484.
    [38] Venturello C, Ricci M. Carboxylic acids from vicinal water-soluble diols[P]. European Patent 123495, 1984.
    [39] Ishii Y, Yamawaki K, Ura T, Yamada H, Yoshida T, Ogawa M F E, Kansai U. Hydrogen peroxide oxidation catalyzed by heteropoly acids combined with cetylpy-ridinium chloride. Epoxidation of olefins and allylic alcohols, ketoniza-tion of alcohols and diols, and oxidative cleavage of 1,2-diols and olefins[J].Journal of Organic Chemistry, 1988, 53(15): 3587-3593.[41] Sato K, Aoki M, Noyori R. A "Green"route to adipic acid: direct oxidation of cyclohexenes with 30 percent hydrogen peroxide[J]. Science, 1998, 281:1646-1647.
    [42] Reed S M, Hutchison J E. Green chemistry in the organic teaching laboratory:an environmentally benign synthesis of adipic acid [J]. Journal Chemical Education. 2000. 77(12):1627-1629.
    [43] 宫红,姜恒,吕振波.己二酸绿色合成新途径[J].高等学校化学学报,2000,21(7):1121·1123.
    [44] 梁红玉,宫红,姜恒.清洁催化氧化环己烯合成己二酸传质过程的研究[J].化学工程师,2001,87(6):61.62.
    [45] 张英群,王春,李贵深,李敬慈.磷钨酸催化过氧化氢氧化环己烯合成己二酸[J].有机化学,2003,23(1):104-105
    [46] 李华明,纪明慧,林海强,舒火明,柳镇安.H_3 PW_(12)O_(40)催化合成己二酸[J].精细化工,2003,20(6):377-380.
    [47] 马祖福,邓友全,王坤,陈静.清洁催化氧化合成己二酸[J].化学通报,2001,67(2):116-118.
    [48] 曹发斌,姜恒,宫红,王锐.Na_2 WO_4/1,2,3,4.丁烷四羧酸催化氧化环己烯合成己二酸[J].化工科技,2004,12(5):1-4.
    [49] 曹发斌,姜恒,宫红.钨酸催化氧化环己烯合成己二酸[J].有机化学,2005,25(1):96-100.
    [50] 李华明,纪明慧,林海强,舒火明,王思远,梁永伟.过氧杂多化合物催化环己烯氧化合成己二酸[J].石油化工,2003,32(5):374-377.
    [51] 张金辉,宫红.杂多酸清洁催化氧化环己烯制备己二酸[J].石油化工高等学校学报,2003,16(2):25-28.
    [52] 李华明,纪明慧,林海强,舒火明,邢福标,陈曼莉.杂多酸催化环己烯氧化合成己二酸[J].应用化学,2003,20(6):570-573.
    [53] 纪明慧,李华明,王心良,周冬阳,曾晓燕.磷钨酸季铵盐催化环己烯氧化的研究[J].海南师范学院学报(自然科学版),2093,16(4):37-39.
    [54] 贾琦,欧玲,马红,王向宇.磷钨酸催化环己烯合成己二酸的研究[J].河南化工,2004,21(4):18-20.
    [55] 阎松,姜恒,宫红,王锐.三氧化钨催化氧化环己烯合成己二酸[J].中国钨业,2005,20(2):33-36.
    [56] 庞晓华.国内外己二酸生产消费现状与前景分析[J].中国石油和化工经济分析,2005,3(12):48-49.
    [57] 杨学萍.己二酸生产技术现状及发展动向[J].精细石油化工进展,2004,5(9):??15-19.
    [58] Charvel A, Delmon B, Holderich W F. New catalytic processes developed in Europe during the 1980s[J]. Applied Catalysis A: Gmeral, 1994, 115(2):173-176.
    [59] 高鸿宾主编.有机化学M].北京:高等教育出版社,1999,268-283.
    [60] 柳士忠,王恩波.杂多化合物的酸性[J].大学化学,1995,10(1):28-30.
    [61] 胡长文,高丽娟,王恩波.杂多化合物的酸催化特性及其在有机合成反应中的应用[J].化学研究与应用,1995,7(4):341.350.
    [62] 陈霞.相转移催化H_2O_2环氧化环己烯合成环氧环己烷的研究[D].郑州:郑州大学.2004.
    [63] Gao Jin-bo, Chen Yang-ying, Han Bo, Feng Zhao-chi, Li Can, Zhou Ning, Gao Shuang; Xi Zu-wei. A spectroscopic study on the reaction-controlled phase transfer catalyst in the epoxidation of cyclohexene [J]. Journal of Molecular Catalysis A: Chemical, 2004, 210(1-2): 197-204.
    [64] 宫为民.分析化学[M].大连:大连理工大学出版社,2000,151.197.
    [65] 蒋永生,傅敏,高宇.超声相转移催化氧化环己醇合成己二酸的研究[J].包装工程,2005,26(1):65-67.
    [66] 陈亚春,刘镇江,朱子强.重结晶法在己二酸生产中的应用[J].浙江化工,2004,35(8):20-22.
    [67] 刘光启,马连湘,刘杰.化学化工物性数据手册[M].北京:化学工业出版社,2002.3-5
    [68] 宫红,杨中华,姜恒,孙兆林,张晓彤.清洁催化氧化环己烯合成己二酸反应中酸性配体的作用[J].催化学报,2002,33(2):182-184.
    [69] 王向宇,苗永霞,贾琦,苏运来,曹书霞,戴新民.己二酸绿色合成中溶液酸性的影响[J].石油化工,2003,33(32):608-610.
    [70] 王恩波,胡长文,许林.多酸化学导论[M].北京:化学工业出版社,1998,32-56.
    [71] 高金波.磷钨杂多化合物及其烯烃催化环氧化反应的光谱研究[D].哈尔滨:哈尔滨工程大学,2003,38-45

© 2004-2018 中国地质图书馆版权所有 京ICP备05064691号 京公网安备11010802017129号

地址:北京市海淀区学院路29号 邮编:100083

电话:办公室:(+86 10)66554848;文献借阅、咨询服务、科技查新:66554700