生物质甘油在农药中间体合成中的应用研究
详细信息    本馆镜像全文|  推荐本文 |  |   获取CNKI官网全文
摘要
近年来石化资源日益短缺,推动了生物柴油产业的迅速发展,2011年全球生物柴油产量预计达到2050万吨。在生物柴油生产过程中约有10%的副产物甘油产生,从而导致市场上甘油产量过剩,价格下跌。合理利用甘油可以有效降低生物柴油生产成本,提高资源利用率。因此,甘油作为一种可再生资源在化工领域的应用受到了广泛关注。本论文对甘油的应用现状进行了概述,在此基础上,设计了三条路线,分别是以甘油为原料合成农药及中间体3-甲氧基丙醛、异丙甲草胺和1,3-丙二醇,这对解决甘油的应用问题具有重要意义。
     1. 3-甲氧基丙醛是合成高效低毒咪唑啉酮类除草剂甲氧咪草烟的重要原料之一。本论文以甘油为起始原料,经甲基化和脱水两步反应合成了3-甲氧基丙醛,发明了脱水反应所用的复合催化剂,在无水硫酸铜和PEG600共同催化作用下得到产物。与现有其它方法相比,本方法合成3-甲氧基丙醛具有原料易得、工艺简单、成本低等优势,具有应用潜力。
     2.异丙甲草胺是一种广谱高活性氯代酰胺类除草剂,其销量大,效果得到人们的广泛认可,是目前我国使用的主要除草剂品种之一。本论文以甘油为起始原料,先脱水生成羟基丙酮,再与2-甲基-6-乙基苯胺缩合、加氢得到中间体N-(1-甲基-2-羟基乙基)-2-甲基-6-乙基苯胺,然后用氯乙酰氯酰化,最后用甲醇醚化得到除草剂异丙甲草胺。本方法合成N-(1-甲基-2-羟基乙基)-2-甲基-6-乙基苯胺的步骤未见文献报道,研究表明以氯化锌为催化剂、二甲苯为带水剂、酮胺摩尔比为2、氢气压力为3.2MPa和反应温度为150℃时,效果最好。该方法为甘油的深加工利用提供了一条可行性路线。
     3.以甘油为起始原料,经缩醛保护、氯化、脱保护和脱氯加氢4步反应合成1,3-丙二醇。通过对醛的选择和处理方式的优化,可以得到高纯度的对甘油1,3-二羟基保护的缩醛——5-羟基-2-苯基-1,3-二氧六环,然后用双(三氯甲基)碳酸酯对未被保护的2-羟基进行氯化,最后脱保护和脱氯加氢,期望高选择性地得到1,3-丙二醇。然而,实验结果表明5-羟基-2-苯基-1,3-二氧六环在氯化时发生重排反应,最后得到的主要产物是1,2-丙二醇。本论文还考察了甘油缩合反应的催化剂和反应底物醛酮的类型对反应生成异构体比例的影响,为提高1,3-二羟基保护缩醛的选择性打下了基础。
     此外,在本论文研究初期阶段,还进行了含氟农药中间体4-氯-2-三氟甲基苯胺的研究,结果表明:以邻三氟甲基苯胺为原料,使用双氧水/盐酸氯化体系,并加入二水氯化铜做催化剂,可以使主产物的选择性大大提高,达到80%以上,转化率为95%。该方法不仅合成路线短,而且反应条件温和,适宜工业化生产。
     总之,本论文从甘油的利用角度出发,研究了其在精细化工中的应用,拓展了甘油的应用途径,为今后的工作打下了基础。
In recent years the shortage of fossil energy has promoted the the biodiesel industry developed rapidly, and global biodiesel production is expected to reach 20.5 million tons in 2011. Glycerol is the main by-product obtained and about 10wt% of glycerol is produced during the production of biodiesel. This is leading to excess output of glycerol on the market and price decline. The proper use of biomass glycerol can effectively reduce the cost of biodiesel and increase utilization rate of resourse. So it has attracted many researchers’interests. In this paper, the present applications of glycerol were reviewed and three new using strategies of glycerol were designed for the synthesis of pescitide and intermediates including 3-methoxypropanal, metolachlor and 1, 3-propanediol. This is important to solve application problems of glycerol.
     1. 3-methoxypropanal is the intermediate of imidazolinone herbicide imazamox which is high-effective and low-toxic. Using glycerol as the starting material, 3-methoxypropanal was obtained via two reaction steps of methylation and dehydration. A new complex catalyst, consisting of anhydrous copper sulfate and PEG600, was invented for the dehydration reaction. Compared with other existing preparing methods of 3-methoxypropanal, this method had such advantages as raw materials available readily, operation process simple and low cost. The method has application potential in the synthesis of 3-methoxypropanal.
     2. Metolachlor is a wide-spectrum, highly-active and chlorinated amide herbicide. The effect is widely recognized by the people. It is one of the main herbicide used in China at present. The herbicide metolachlor was synthesized using glycerol as the starting material, comprising five reaction steps. Firstly, acetol was produced by dehydration of glycerol. Then the intermediate N-(1'-methyl-2'-hydroxyethyl)-2-ethyl-6-methylaniline was obtained by condensation and hydrogenation reactions of acetol and 2-methyl-6-ethylaniline. Finally, through acylation with chloroacetyl chloride and etherification with methanol, metolachlor was ontained. The noval synthetic process of N-(1'-methyl-2'-hydroxyethyl) - 2-ethyl-6-methylaniline from glycerol has not been reported before. The optimized operation conditions were that using zinc chloride as catalyst, xylene as solvent, the mole ratio of acetol and 2-methyl-6-ethylaniline being 2, reaction pressure at 3.2 MPa and reaction temperature at 150℃. This method provided a feasible route for deep processing of glycerol.
     3. With glycerol as the starting material, 1, 3-propanediol was obtained via four reaction steps: protection as acetal, chlorination, hydrolysis and catalytic dechlorination-hydrogenation. Through the selection of aldehydes and the optimization of treatment, high purity 1, 3-protected product of 5-hydroxy-2-phenyl-1, 3-dioxane was obtained. Then the un-protected hydroxyl group was chlorinated with bis (trichloromethyl) carbonate, followed by deprotection and dechlorination-hydrogenation, 1, 3-propanediol was prospectively obtained with high selectivity. In our experimental results, however, a rearrangement reaction was conducted in the chlorination step, which causing the major product obtained was 1, 2-propanediol. This paper also examined the effect of catalysts and the types of substrate on the reaction of glycerol condensation, which laid a good foundation for improving the selectivity of 1, 3-protected product.
     In addition, in the early stage, the synthesis of a fluorine-contained pesticide intermediate of 4-chloro-2-trifluoromethyl aniline was researched. The results showed that 4-chloro-2-trifluoromethyl aniline was obtained in 95% conversion and 80% selectivity using o-(trifluoromethyl) aniline as raw material, hydrogen peroxide/hydrochloric acid as chlorination reagents and chloride copper as catalyst. This synthetic route is shorter and reaction condition is mild, which is suitable for industrial production.
     In summary, three new applications of glycerol in fine chemicals were developped, which expanded the application approaches of glycerol and laid a good foundation for the future work.
引文
[1]杨艳,卢滇楠,李春等.面向21世纪的生物能源[J].化工进展, 2003, 22(1): 8-12
    [2]苏畅,赵崇峰,岳莉等.生物柴油技术的进展[J].当代化工, 2004, 33(2): 79-82
    [3]黄忠水,纪威,李淑艳等.国外生物柴油的应用[J].节能与环保, 2003, 30(1): 34-35
    [4]朱建良,张冠杰.国内外生物柴油研究生产现状及发展趋势[J].化工时刊, 2004, 18(1): 23-27
    [5] Suppes G. J., Dasari M. A., Doskocil E. J. et al. Transesterification of soybean oil with zeolite and metal catalysts[J]. Applied Catalysis A: General, 2004, 257: 213-223
    [6]熊犍,宋炜,叶君.降低生物柴油生产成本的研究进展[J].化工进展, 2007, 26(6): 774-777
    [7] Zhou C. H., Beltramini J. N., Fan Y. X. et al. Chemoselective catalytic conversion of glycerol as a biorenewable source to valuable commodity chemicals[J]. Chem. Soc. Rev., 2008, 37: 527-549
    [8]宋国安.我国甘油生产亟待开发[J].陕西粮油科技, 1996, 21(1): 15-18
    [9]施春辉.国内甘油工业现状及展望[J].山东化工, 1997, 3: 42-43
    [10]张金廷,胡培强,施永诚等.甘油[M].北京:化学工业出版社, 2008, 7-10
    [11] Che T. M., Westfield. Production of propanediols[P]. US: 4642394, 1987-02-10
    [12] Dasari M. A., Kiatsimkul P. P., Sutterlin W. R. et al. Low-pressure hydrogenolysis of glycerol to propylene glycol[J]. Applied Catalysis A: General, 2005, 281: 225-231
    [13]石英华.丙二醇合成工艺[J].沈阳化工, 1996, 3: 35-37
    [14] Casale B., Gomez A. M. Method of hydrogenating glycerol[P]. US: 5214219, 1993-05-25
    [15] Casale B., Gomez A. M. Catalytic method of hydrogenating glycerol[P]. US: 5276181, 1994-01-04
    [16] Schuster L., Eggersdorfer M. Preparation of 1, 2-propanediol[P]. US: 5616817, 1997-04-01
    [17] Suppes G. J., Sutterlin W. R., Dasari M. Method of producing lower alcohols from glycerol[P]. US: 7663004, 2010-02-16
    [18]熊犍,宋臻善,叶君.第十一届美国总统绿色化学挑战奖介绍[J].精细化工, 2006, 23(12): 1145-1147
    [19]冯建,袁茂林,陈华等.甘油催化氢解的研究与应用[J].化工进展, 2007, 19(5): 651-658
    [20]杨菊群,王幸宜,戚蕴石. 1,3-丙二醇的合成新进展[J].石油化工, 2002, 31(11): 943-947
    [21] Haasa T, Jaegera B., Webera R., et al. New diol processes: 1, 3-propanediol and 1, 4-butanediol[J]. Applied Catalysis A: General, 2005, 280: 83–88
    [22] Drent E., Jager W. W. Hydrogenolysis of glycerol[P]. US: 6080898, 2000-06-27
    [23] Hass T., Neher A., Arntz D. et al. Process for the simultaneous production of 1, 2- and 1, 3-propanediol[P]. US: 5426249, 1995-06-20
    [24] (a)崔小明.国内外乙二醇生产技术及市场分析(上)[J].上海化工, 2004, 11: 43-46; (b)崔小明.国内外乙二醇生产技术及市场分析(下)[J].上海化工, 2004, 12: 41-44
    [25] (a)葛欣,张英.乙二醇的生产与制备[J].山东化工, 1997, 2: 41-46; (b)郑智,王建黎,计建炳. Ru催化剂氢解甘油制备二元醇的研究进展[J].现代化工, 2009, 29(2): 12-15
    [26] Tanikella M.S.S.R. Hydrogenolysis of polyols to ethylene glycol in nonaqueous solvents[P]. US: 4404411, 1983-09-13
    [27]金离尘.以生物柴油的副产品甘油为原料生产1,3-丙二醇[J].聚酯工业, 2006,19(5): 8-10
    [28]赵红英,程可可,向波涛等.微生物发酵法生产1,3-丙二醇[J].精细与专用化学品, 2002, 13: 21-23
    [29]邵敬伟,刘长江. 1,3-丙二醇发酵生产的研究进展[J].沈阳农业大学学报, 2001 02, 32(1): 57-60
    [30]向晓丽. 1,3-丙二醇的制备[J].化工纵横, 2003, 17(7): 22-24
    [31]陈宏文,洪其文,徐晶等.克雷伯杆菌有氧发酵利用甘油生产3-羟基丙醛的研究[J].现代化工, 2004, 24(11): 36-39
    [32]綦文涛,修志龙.甘油歧化生产1,3-丙二醇过程的代谢和基因调控机理研究进展[J].中国生物工程杂志, 2003, 23(2): 64-68
    [33] Gallezot P. Selective oxidation with air on metal catalysts[J]. Catalysis Today, 1997, 37: 405-418
    [34] Dimitratos N., Sanchez J. A. L., Anthonykutty J. M. et al. Oxidation of glycerol using gold-palladium alloy-supported nanocrystals[J]. Phys. Chem. Chem. Phys., 2009, 11: 4952–4961
    [35] Pagliaro M., Ciriminna R., Kimura H. et al. From glycerol to value-added products[J]. Angew. Chem. Int. Ed., 2007, 46: 4434-4440
    [36] Garcia R., Besson M., Gallezot P. Chemoselective catalytic oxidation of glycerol with air on platinum metals[J]. Applied Catalysis A: General, 1995, 127: 165-176
    [37] Demirel-Gulen S., Lucas M., Claus P. Liquid phase oxidation of glycerol over carbon supported gold catalysts[J]. Catalysis Today, 2005, 102-103: 166-172
    [38] Fordham P., Besson M., Gallezot P. Selective catalytic oxidation of glyceric acid to tartronic and hydroxypruvic acids[J]. Applied Catalysis A: General, 1995, 133: 179-184
    [39] Fordham P., Besson M., Gallezot P. Catalytic oxidation with air of tartronic acid to mesoxalic acid on bismuth-promoted platinum[J]. Catalysis Letters, 1997, 46: 195-199
    [40] Kimura H., Tsuto K., Wakisaka T. et al. Selective oxidation of glycerol on platinum-bismuth catalyst[J]. Applied Catalysis A: General, 1993, 96(2): 217-228
    [41] Besson M., Gallezot P. Selective oxidation of alcohols and aldehydes on metal catalysts[J]. Catalysis Today, 2000, 57: 127–141
    [42]王敬锋,陈先明,赵帆.金属催化剂选择性催化氧化甘油及其衍生物的研究[J].化工时刊, 2007, 21(8): 30-32
    [43] Ciriminna R., Palmisano G., Pina C. D. et al. One-pot electrocatalytic oxidation of glycerol to DHA[J]. Tetrahedron Letters, 2006, 47: 6993-6995
    [44] Ciriminna R., Pagliaro M. One-pot homogeneous and heterogeneous oxidation of glycerol to ketomalonic acid mediated by TEMPO[J]. Adv. Synth. Catal., 2003, 345(3): 383-388
    [45]严志远,徐常威,沈培康.甘油在氧化物钯复合催化剂上的电氧化研究[J].电化学, 2006, 12(4): 408-411
    [46]李明燕,周春晖, Beltramini J. N. et al.甘油的催化选择氧化[J].化学进展, 2008, 20(10): 1474-1486
    [47]章朝辉,胡忠策,郑裕国.生物转化生产二羟基丙酮的研究进展[J].化学与生物工程, 2007, 24(1): 1-3
    [48] G?tgens C., Degner U. Biotransformation of glycerol to dihydroxyacetone by recombinant Gluconobacter oxydans DSM 2343[J]. Appl Microbiol Biotechnol, 2007, 76: 553–559
    [49] (a)郑裕国,张霞,沈寅初.微生物转化甘油生产1,3-二羟基丙酮的菌株筛选[J].浙江工业大学学报, 2001, 29(2): 124-127;(b)郑裕国,胡忠策,柳志强等.地衣芽孢杆菌B-05571及其在制备1,3-二羟基丙酮中的应用[P]. CN: 101037659, 2007-09-19
    [50] Mcmorn P., Roberts G., Hutchings G. J. Oxidation of glycerol with hydrogen peroxide using silicalite and aluminophosphate catalysts[J]. Catalysis Letters, 1999, 63: 193–197
    [51]张月成,户秋义,韩建萍等.甘油三油酸酯的合成研究[J].精细石油化工, 2003, 6: 32-33
    [52]王漓江,张所信.葵花油醇酸树脂的合成及其应用[J].丹东纺专学报, 1997, 4: 27-29
    [53] Jér?me F., Kharchafi G., Adam I.“One pot”and selective synthesis of monoglycerides over homogeneous and heterogeneous guanidine catalysts[J]. Green Chem., 2004, 6: 72-74
    [54] Mequro S., Osaki N., Matsuo N. et al.Effect of diacylglycerol on the development of impaired glucose tolerance in sucrose-fed rats[J]. Lipids, 2006, 41(4): 347-355
    [55] Barrault J., Pouilloux Y., Clacens J. M. Catalysis and fine chemistry[J]. Catal.Today, 2002, 75: 177-181
    [56]陈福明,孙登文.双甘酯的生产及应用[J].中国油脂, 1997, 22(5): 49-51
    [57]刘书成,章超桦,洪鹏志等.有机溶剂中酶促酯化合成n-3PUFA甘油酯的研究[J].中国粮油学报, 2006, 21(3): 146-151
    [58]雷学军.三醋酸甘油酯的合成方法[J].中外技术情报, 1995, 1: 28-30
    [59] Bremus N., Dieckelmann G., Jeromin L. et al. Process for the continuous production of triacetin[P]. US:4381407, 1983-04-26
    [60] Goncalves V. L., Pinto B. P., Silva J. C. et al. Acetylation of glycerol catalyzed by different solid acids[J]. Catalysis Today, 2008, 133–135: 673–677
    [61] Bell J. B., Currier V. A., Malkemus J. D. Method for preparing glycerin carbonate[P]. US: 2915529, 1959-12-01
    [62] Teles J. H., Rieber N., Harder W. Preparation of glycerol carbonate[P]. US: 5359094, 1994-10-25
    [63] Claude S., Mouloungui Z., Yoo J. W. et al. Method for preparing glycerol carbonate[P]. US: 6025504, 2000-02-15
    [64] Okutsu M., Kitsuki T. Process for the preparation of glycerol carbonate[P]. US: 64957063, 2002-12-17
    [65] Behr A., Eilting J., Irawadi K. et al. Improved utilization of renewable resources: New important derivatives of glycerol[J]. Green Chem., 2008, 10: 13-30
    [66] Rokicki G., Rakoczy P., Parzuchowski P. et al. Hyperbranched aliphatic polyethers obtained from environmentally benign monomer: glycerol carbonate[J]. Green Chem., 2005, 7: 529-539
    [67] Takagaki A., Iwatani K., Nishimura S. Synthesis of glycerol carbonate from glycerol and dialkyl carbonates using hydrotalcite as a reusable heterogeneous base catalyst[J]. Green Chem., 2010, 12: 578–581
    [68]朱宝库,赵永红,孔力等.超支化聚缩水甘油醚研究进展[J].高分子通报, 2007, 4: 23-28
    [69] Clacens J. M., Pouilloux Y., Barrault J. Selective etherification of glycerol to polyglycerols over impregnated basic MCM-41 type mesoporous catalysts[J]. Applied Catalysis A: General, 2002, 227: 181–190
    [70]万新军,吴蓉,宋明友.改进从甘油制备丙烯醛实验方法的研究[J].巢湖学院学报, 2003, 5(3): 67-68
    [71]张跃,谢国红,刘建武等.生物甘油制备农药中间体丙烯醛的研究[J].安徽农业科学, 2009, 37(4): 1420-1422
    [72] Chai S. H., Wang H. P., Liang Y. et al. Sustainable production of acrolein: investigation of solid acid-base catalysts for gas-phase dehydration of glycerol[J]. Green Chem., 2007, 9(10): 1130-1136
    [73]宁丽丽,丁云杰,陈维苗等.活性炭负载硅钨酸催化甘油脱水制丙烯醛[J].催化学报, 2008, 29(3): 212-214
    [74] Chai S. H., Wang H. P., Liang Y. et al. Sustainable production of acrolein: Gas-phase dehydration of glycerol over Nb2O5 catalyst[J]. Journal of Catalysis, 2007, 250: 342–349
    [75] (a)Ott L., Bicker M., Vogel H. Catalytic dehydration of glycerol in sub- and supercritical water: a new chemical process for acrolein production[J]. Green Chem., 2006, 8: 214-220; (b)Watanabe M., Iida T., Aizawa Y.et al. Acrolein synthesis from glycerol in hot-compressed water[J]. Bioresource Technology, 2007, 98: 1285–1290
    [76] Chuang-Wei Chiu C. W., Dasari M. A., Suppes J. Dehydration of glycerol to acetol via catalytic reactive distillation[J]. AIChE journal, 2006, 52(10): 3543-3548
    [77] (a)Sato S., Akiyama M., Takahashi R. et al. Vapor-phase reaction of polyols over copper catalysts[J]. Appl. Catal. A: General, 2008, 347(2): 186-191; (b)Kinage A. K., Upare P. P., Kasinathna P. et al. Selective conversion of glycerol to acetol over sodium-doped metal oxide catalysts[J]. Catal. Commun., 2010, 11(7): 620-623; (c)赵静,于维强,李德财等.常压两步法催化丙三醇脱水-加氢制备1,2-丙二醇[J].催化学报, 2010, 31(2): 200-204; (d)牛莎莎,朱玉雷,郑洪岩等.铜基催化剂上甘油脱水制备羟基丙酮[J].催化学报, 2011, 32(2): 345-351
    [78]张金廷,施永诚.聚合甘油的性质及其应用[J].日用化学品科学, 2005, 28(10): 22-24
    [79] Axel K. Method for preparing polymers of glycerol with a saponite catalyst[P]. EP: 1316577, 2002-11-14
    [80]汪多仁.聚甘油脂肪酸酯的合成应用与市场开发[J].表面活性剂工业, 1998, 2: 1-2
    [81] Arno B., Heiko S., Christoph L. et al. Method of preparing polyol alkyl ethers[P]. DE: 4222183, 1992-07-06
    [82] Kesling H. S., Karas L. J., Liotta F. J. Diesel fuel[P]. US:5308365, 1994-05-03
    [83] Gupta V. P. Glycerine ditertlary butyl ether preparation[P]. US: 5476971, 1995-12-19
    [84] Klepacova K.; Mravec D.; Bajus M. Tert-butylation of glycerol catalysed by ion-exchange resins[J]. Appl. Catal. A, 2005, 294: 141-147
    [85] Pariente S., Tanchoux N., Fajula F. Etherification of glycerol with ethanol over solid acid catalysts[J]. Green Chem., 2008, 11: 1256–1261
    [86] Queste S., Bauduin P., Touraud D. Short chain glycerol 1-monoethers-a new class of green solvo-surfactants[J]. Green Chem., 2006, 8: 822–830
    [87] Garcia J., Hector G. M., Mayoral J. A. Green solvents from glycerol. Synthesis and physico-chemical properties of alkyl glycerol ethers[J]. Green Chem., 2010, 12: 426–434
    [88] Cortright R. D., Davda R. R., Dumesic J. A. Hydrogen from catalytic reforming of biomass-derived hydrocarbons in liquid water[J]. Nature, 2002, 418: 964-967
    [89] Hirai T., Ikenaga N., Miyake T. et al. Production of hydrogen by steam reforming of glycerin on ruthenium catalyst[J]. Energy Fuels, 2005, 19: 1761-1762
    [90] Davda R. R., Shabaker J.W, Huber G.W. et al A review of catalytic issues and process conditions for renewable hydrogen and alkanes by aqueous-phase reforming of oxygenated hydrocarbons over supported metal catalysts[J]. Applied Catalysis B: Environmental, 2005, 56: 171–186
    [91] Kersten S. R., Potic B., Prins W. et al. Gasification of model compounds and wood in hot compressed water[J]. Ind. Eng. Chem. Res. 2006, 45: 4169-4177
    [92] Soares R. R., Simonetti D. A., Dumesic J. A. Glycerol as a source for fuels and chemicals by low-temperature catalytic processing[J]. Angew .Chem. Int. Ed., 2006, 45: 3982-3985
    [93] Zhou C. H., Beltramini J. N., Fan Y. X. et al. Chemoselective catalytic conversion of glycerol as a biorenewable source to valuable commodity chemicals[J]. Chem. Soc. Rev., 2008, 37: 527–549
    [94]郑伟华,李辉,叶波等.环氧氯丙烷的制备工艺研究[J].广西轻工业, 2008, 6: 41-43
    [95]朱红军.环氧氯丙烷生产技术及市场消费[J].中国氯碱, 2003, 1: 27-29
    [96] (a)Freddy G. Solvay will make epichlorohydrin from glycerol[J]. Industrial Bioprocessing, 2006, 28(3): 8-9; (b)钱伯章.环氧氯丙烷生产的直接法路线[J].化学反应工程与工艺, 2006, 2: 6
    [97] (a)吴广铎,张建丽.甘油法环氧氯丙烷生产技术[J].氯碱工业, 2008, 44(2): 26-28; (b)许玉梅,丁克鸿,田宇等.一种甘油催化氢氯化制备二氯丙醇的方法[P]. CN: 101029000, 2007-09-05
    [98]赵学娟,柏子龙.甘油法制备环氧氯丙烷中间体二氯丙醇催化剂的研究[J].精细化工中间体, 2008, 37(7): 34-36
    [99]赵学娟,柏子龙.有机酸催化甘油法制备二氯丙醇的反应研究[J].化工中间体, 2008, 5: 19-22
    [100]蒋建兴,张培培,姚成.甘油生产环氧氯丙烷的发展概况[J].现代化工, 2006, 26(2): 71-73
    [101]王鸿显,赵红坤,张跃华.甘油金属配合物的合成、应用及发展前景[J].日用化学品科学, 2006, 29(1): 24-27
    [102] Radoslovich E. W., Raupach M., Slade P. G. et al. Crystalline cobalt zinc manganese and iron alkyoxides of glycerol[J]. Aust. J. Chem., 1970, 23: 1963-1971
    [103] David A. M., Dennis C. R., Anthony R. H. Zinc glycerolate manufacture[P]. US: 5646324, 1997-07-08
    [104]郑灵芝,舒万艮,申雄军等.甘油锌的合成及其光稳定作用研究[J].现代塑料加工应用, 2002, 13(4): 38-40
    [105] Razzak M.,韩景田, Tucker I. G.固体甘油铜制备[J].山东化工, 2001, 30(4): 5-6
    [1] (a)Doehner, Francls R. Novel 5 (and/ or 6) substituted 2-(2-imidazolin-2-yl) nicotinic acids, asters and salts, useful as herbicidal agents and novel intermediates for the preparation of said nicotinic acids, esters and salts[P]. EP:0254951, 1988-03-02; (b)毕强,王巍,程志明等.甲氧咪草烟的合成概述[J].现代农药, 2007, 6 (2): 10-14
    [2] Boot J. R., Boulet S. L., Clark B. P. et al. N-alkyl-N-arylmethylpiperidi-4-amines: Novel dual inhibitors of serotonin and norepinephrine reuptake[J]. Bioorg. Med. Chem. Lett., 2006, 16: 2714-2718
    [3] Chapuis C., Buchi G. H., Wuest H. Synthesis of cis-hedione and methyl jasmonate via cascade baylis-hillman reaction and claisen ortho ester rearrangement[J]. Helvetica Chimica Acta, 2005, 88: 3069-3088
    [4] (a)Poly W., Schomburg D., Hoffmann H. M. R. Stereoselective generation and facile dimerization of (E)-2-methylene-3-alkenoic acid esters[J]. J. Org. Chem., 1988, 53: 3701-3710; (b)Juric S., Kronja O. Reactivity of some tertiary chlorides with olefinic and methoxy neighboring groups. A case of extendedπ, n-participation[J]. J. Phys. Org. Chem., 2002, 15: 556-560
    [5] Alagona G., Ghio C., Lazzaroni R. et al. Olefin insertion into the rhodium-hydrogen bond as the step determining the regioselectivity of rhodium-catalyzed hydroformylation of vinyl substrates: Comparison between theoretical and experimental results[J]. Organometallics, 2001, 20: 5394-5404
    [6] Procopio A., Dalpozzo R., Nino A. D. et al. Erbium(III) triflate: A valuable catalyst for the rearrangement of epoxides to aldehydes and ketones[J]. Synlett, 2004, 14: 2633-2635
    [7] (a)Hiroshi K., Shunei Y. Production of beta-alkoxypropionaldehyde[P]. JP: 2000072708, 2000-03-07; (b)Tokuo K., Misako K., Hideji H. et al. Method of producing 3-alkoxy-1-propanals and 3-alkoxy-1-propanols[P]. JP: 2001247507, 2001-09-11; (c)Thorsten H., Mathias H., Christion R. et al. Production of 3-alkoxy-1-propanal, useful in the production of 3-alkoxy-1-propanol, comprises reaction of acrolein with a saturated alcohol in the presence of a base at low temperature[P]. DE: 10122268, 2002-11-14; (d)Thorsten H., Christian R., Rudolf V. et al. Production of 3-alkoxypropanols, comprises alkoxylating acrolein or an acrolein precursor with an alcohol in the presence of an acidic ion exchanger as catalyst and hydrogenating the product[P]. DE: 10138967, 2003-02-27; (e)Elderfield R. C., Pitt B. M., Wempen I. Synthesis of the branched chain 5-isopropylaminoamyl and 4-isopropylaminobutyl ethers and of the bromidesderived from them[J]. J. A. C. S., 1950, 72: 1334-1350; (f)Wang Z. Y., Jiang H. F., Qi C. R. et al. PS–BQ: an efficient polymer-supported cocatalyst for the wacker reaction in supercritical carbon dioxide[J]. Green Chem., 2005, 7: 582–585; (g) Wang Z. Y., Jiang H. F., Ouyang X. Y. et al. Pd (II)-catalyzed acetalization of terminal olefins with electron-withdrawing groups in supercritical carbon dioxide: selective control and mechanism[J]. Tetrahedron, 2006, 62: 9846–9854
    [8] Koshchii S. V. Optimization of synthesis of mono-o-methylglycerol isomers[J]. Russian Journal of Applied Chemistry, 2002, 75(9): 1434-1437
    [9]俞善信,熊士荣.对甲苯磺酸催化环己醇脱水制备环己烯[J].化学与生物工程, 2004, 2: 24-27
    [10]李肇凯,杜泽学.无机酸对二甘醇脱水环化反应的催化作用[J].金山油化纤, 2005, 1: 13-17
    [11]文瑞明,俞善信,雷存喜等.硫酸氢钠催化合成环己烯的研究[J].精细石油化工进展, 2001, 2(10): 21-22
    [12]蔡小华,陈学勇.催化剂硫酸氢钾的合成进展[J].应用化工, 2007, 36(12): 1229-1232
    [13]郭明林.硫酸铜催化制备1,4-二氧六环[J].精细化工, 1996, 13(4): 45-46
    [14]许建勋.咪唑类离子液体合成及其应用研究[J].化工技术与开发, 2004, 33(4): 15-21
    [15] Zhu H. P., Yang F., Tang J. et al. Br?nsted acidic ionic liquid 1-methylimidazolium tetrafluoroborate: a green catalyst and recyclable medium for esterification[J]. Green Chem., 2003, 5: 38-39
    [16] Wang Y. Y., Wang R., Wu L. C. et al. Preparation of fructone catalyzed by water-soluble br?nsted acid ionic liquids[J]. Chinese Chemical Letters, 2007, 18: 24-26
    [17]李红娟,于世涛,刘福胜等.酸性离子液体催化合成三醋酸甘油酯[J].工业催化, 2007, 15(9): 38-42
    [18] Chuang W. C., Mohanprasad A. D., Suppes G. J. Dehydration of glycerol to acetol via catalytic reactive distillation[J]. AIChE Journal, 2006, 52(10): 3543-3548
    [19]朱惠琴.聚乙二醇相转移催化合成2,4-二硝基苯酚[J].化学试剂, 2007, 29(3):177~178
    [20]吕小兰,麦曦,郭惠等.相转移催化合成邻硝基苯乙醚的研究[J].化学世界, 2007, 12: 744-747
    [21] Chen J., Spear S. K., Huddleston J. G. et al. Polyethylene glycol and solutions of polyethylene glycol as green reaction media[J]. Green Chemistry, 2005, 7: 64–82
    [22] Dickerson T. J., Reed N. N., Janda K. D. Soluble polymers as scaffolds for recoverable catalysts and reagents[J]. Chem. Rev., 2002, 102(10): 3325-3344
    [23]陈秋实.环糊精及其应用[J].化工时刊, 2007, 21(8): 49-53
    [1]刘长令.世界农药大全-除草剂卷[M].北京:化学工业出版社, 2002: 262-266
    [2] Moser H., Vogel C. Optically active N-(1'-methyl-2'-methoxyethyl) -N-chloroacetyl-2-ethyl-6-methylaniline as herbicide[P]. US: 5002606, 1991-03-26
    [3] Vogel C., Aebi R. Herbicidal and plant growth inhibiting agent[P]. US: 4324580, 1982-04-13
    [4] Vaclav K., Ludovic K., Emaneul B. et al. Repeated use of platinum hydrogenation catalyst in the preparation of 2,6-dialkyl-N-(1'-methoxy-2'-propyl)anilines by reductive alkylation of anilines[P]. CS: 266994, 1990-12-14
    [5] Vaclav K., Ludovic K., Emaneul B. et al. Method of preparing 2-ethyl-6-methyl-N (1-methoxy-2-propyl) chloroacetanilide[P]. CS: 272750, 1989-11
    [6] Degischer G., Angst W. Process for producing N-substituted-N-acetyl-2, 6-dialkyl-anilines[P]. US: 4317916, 1982-03-02
    [7] (a)张洪渊,万海清.生物化学[M].北京:化学工业出版社, 2001; (b)包文娟,吴永果,冯忖等.精异丙甲草胺的不对称催化合成研究进展[J].世界农药, 2007, 29(增): 26-34; (c)郑良玉,张锁秦,高贵等.酶催化拆分N-(2-甲基-6-乙基苯基)丙氨酸[J].有机化学, 2003, 23(增): 134
    [8] Chiu C. W., Dasari M. A., Suppes G. J. Dehydration of glycerol to acetol via catalytic reactive distillation[J]. AIChE Journal, 2006, 52(10): 3543-3548
    [9]洪伟良,刘剑洪,田德余等.纳米铜铬复合氧化物对XRD热分解的催化作用[J].推进技术, 2003, 24(1): 83-86
    [10]储伟,何川华,戴晓雁等.用于低温液相合成甲醇的铜铬铝催化剂的研制与表征[J].四川大学学报, 2003, 35(6): 1-4
    [11] Adkins, Kinsey, Folkers. The catalytic hydrogenation of organic compounds overcopper chromite[J]. Ind. Eng. Chem., 1931, 53: 1901-1905
    [12]赵峰,李国英,李能等. CuCrO2和CuCr2O4间相互作用对体系结构及催化性能的影响[J].催化学报, 2003, 24(1): 11-16
    [13] Kawamoto A. M., Pardini L. C., Rezende L. C. Synthesis of copper chromite catalyst[J]. Aerospace Science and Technology, 2004, 8: 591–598
    [14] Chaudhari R.V., Jaganathan R., Chaudhari S. T. et al. Process for the preparation of copper chromite catalyst[P]. US: 7037877, 2006-05-02
    [15]唐熏,杨新国,李筱芳等. N-苯基-2,2,6,6-四氯环己亚胺的催化合成[J].湖南大学学报, 2001, 28(4): 14-17
    [16] Bader R., Flatt P., Radimerski P. Process for the preparation of 2-alkyl-6-methyl-N-(1'-methoxy-2'-propyl)-aniline and a process for the preparation of their chloracetanilides[P]. US :5430188, 1995-07-04
    [17]陈芬儿,万江陵,管春生等.双氯芬酸钠合成工艺研究[J].中国医药工业杂志, 1995, 26(4): 145-148
    [1]孟翠敏,田华. 1,3-丙二醇的生产技术[J].天津化工, 2008, 22(1): 48-49
    [2]徐兆瑜. 1,3-丙二醇技术进展和市场[J].精细化工原料和中间体,2004, 2: 25-29
    [3]吉振坡,石相如,曲振峰. 1,3-丙二醇生产技术及成本分析[J].河南化工, 2005, 22(9): 4-6
    [4]金离尘.以生物柴油的副产品甘油为原料生产1,3-丙二醇[J].聚酯工业, 2006, 19(6): 8-10
    [5]赵洵,许张乔,曹发海.生物质甘油制备1,3-丙二醇的研究进展[J].合成技术及应用, 2007, 2(1): 29-32
    [6] Slaugh L. H., Weider P. R. Process for making 3-hydroxypropanal and 1, 3- propanediol[P]. US: 5256827, 1993-10-26
    [7] Powell J. B., Slaugh L. H., Forschner T. C. et al. Cobalt-catalyzed process for preparing 1, 3-propanidiol[P]. US: 5777182, 1998-07-07
    [8] Briggs J. R., Maher J. M., Harrison A. M. Catalysts and processes useful in producing 1, 3-diols and/or 3-hydroxyldehydes[P]. US: 5210318, 1993-05-11
    [9]谢家明,郭世卓,徐泽辉.丙烯醛制备1,3-丙二醇的中型试验研究[J].石油炼制与化工, 2006, 37(5): 39-44
    [10] Unruh J. D., Ryan D. A. Method for the manufacture of 1, 3-propanediol[P]. US: 5093537, 1992-03-03
    [11]赵红英,程可可,向波涛等.微生物发酵法生产1,3-丙二醇[J].精细与专用化学品, 2002, 13: 21-23
    [12]赵亚囡,陈国,姚善泾.若干因素对发酵法生产1,3-丙二醇的调控作用[J].化学反应工程与工艺, 2006, 22(3): 193-198
    [13] Chaminand J., Djakovitch L., Gallezot P. Glycerol hydrogenolysis on heterogeneous catalysts[J]. Green Chem., 2004, 6: 359-361
    [14] Unruh. Method for the manufacture of 1, 3-PDO[P]. US: 5093537, 1992-03-03
    [15]徐泽辉.丙烯醛水合加氢制1,3-PDO[J].石油炼制与化工, 2001, 12(32): 21-24
    [16] Wang K. Y., Hawley M. C., DeAthos S. J. Conversion of glycerol to 1,3-propanediol via selective dehydroxylation[J]. Ind. Eng. Chem. Res., 2003, 42(13): 2913-2923
    [17] Procopio A., Dalpozzo R., Nino A. Mild and efficient method for the cleavage of benzylidene acetals by using erbium (III) triflate[J]. Org. Biomol. Chem., 2005, 3: 4129-4133
    [18] Procopio A., Gaspari M., Nardi M. Simple and efficient MW-assisted cleavage of acetals and ketals in pure wate[J]. Tetrahedron Letters, 2007, 48: 8623–8627
    [19] Ikai K., Kameyama N., Furukawa Y. et al. Process for producing 1, 2-propanediol [P]. US: 6156941, 2000-12-05
    [20] Showler A. J., Darley P. A. Condensation products of glycerol with aldehydes and ketones. 2-Substituted m-dioxan-5-ols and 1, 3-dioxolane-4-methanols[J]. Chem. Rev., 1967, 67(4): 427-440
    [21] Jaeger D. A., Jamrozik J., Golich T. G. et al. Preparation and characterization of glycerol-based cleavable surfactants and derived vesicles[J]. J. Am. Chem. Soc., 1989, 111: 3001-300
    [22] Zey E. G., Christi C., Hoffmann W. A. Cyclic acetal acrylates or methacrylates and processes for preparing same[P]. US: 4076727, 1978-02-28
    [23] Hill H. S., Myron S. Whelen M. S., Hibbert H. Studies on the reactions relating tocarbohydrates and polysaccharides. XV. The isomeric benzylidene glycerols[J]. J. Am. Chem. Soc., 1928, 50(8): 2235-2242
    [24] Harold H., Carter N. M. Mechanism of organic reactions. I. The wandering of acyl groups in glycerol esters[J]. J. Am. Chem. Soc., 1929, 51: 1601-1613
    [25] Carlsen P. J., Sorbye K., Ulven T. et al. Synthesis of benzylidene–protected dihydroxyacetone[J]. Acta Chemica Scandinavica, 1996, 50: 185-187
    [26]王建黎,余建儿,计建炳.一种由甘油制备1,3-二羟基丙酮的新方法[P]. CN: 101412706, 2009-04-22
    [27]梁学正,高珊,于心玉等. KHSO4催化合成甘油类缩醛(酮)的研究[J].应用化工, 2006, 35(3): 180-182
    [28]陈晓梅,桂建舟,张晓彤等.功能化酸性离子液体催化缩醛(酮)的合成[J].应用化工, 2006, 35(2): 96-98
    [29]苏广均.阳离子交换树脂催化合成苯甲醛1,2-丙二醇缩醛的研究[J].日用化学工业, 2008, 38(3): 176-178
    [30]文瑞明,游沛清,罗新湘等.维生素C催化合成缩醛(酮)[J].石油化工, 2002, 31(5): 373-375
    [31]杨水金,童文龙.单质碘催化合成缩醛(酮)[J].香料香精化妆品, 2006, 4: 11-13
    [32]何淼,周海霞,刘春生等.碘掺杂聚苯胺催化合成环己酮1,2-丙二醇缩酮[J].合成化学, 2006, 14(1): 99-102
    [33] Fadnavis N. W., Reddipalli G. S., Ramakrishna G. et al. Highly regioselective preparation of 1, 3-dioxolane-4-methanol derivatives from glycerol using phosphomolybdic acid[J]. Synthesis, 2009, 4: 557–560
    [34] Deutsch J., Martin A., Lieske H. Investigations on heterogeneously catalysed condensations of glycerol to cyclic acetals[J]. Journal of Catalysis, 2007, 245: 428–435
    [35] Hill H. S., Whelen M. S., Hibbert H. Studies on the reactions relating to carbonydrates and polysaccharides. XV. The isomeric benzylidene glycerols[J]. J. Am. Chem. Soc., 1928, 50: 2235-2242
    [36]陈丽涛,肖鹤鸣.а-取代甲苯定向硝化的理论研究[J].化学学报, 2006, 64(1): 61-69
    [37]陈丽涛,肖鹤鸣,居学海等.苯硝化反应机理及其溶剂效应的理论研究[J].中国科学, 2003, 33(3): 192-200
    [38]奚强,唐杜陵,廖佳音.氯化亚砜在有机合成中的应用[J].荆州师专学报, 1997, 20(5): 69-72
    [39] Tesser R., Santacesaria E., Serio M. D. et al. Kinetics of glycerol chlorination with hydrochloric acid: A new route toα,γ-Dichlorohydrin[J]. Ind. Eng. Chem. Res., 2007, 46: 6456-6465
    [40]陈时忠. 2,4,6-三氯嘧啶的合成[J].科技通报, 2001, 17(5): 57-58
    [41] Aneja R., Davies A. P. Nucleophilic substitution in glycerol derivatives. Part VI. halogenodeoxygenation of 2-phenyl-l, 3-dioxan-5-ol to give 1, 3-dioxans and 1, 3-dioxolans[J]. J. Chem. Soc., Perkin Trans. 1, 1974: 141-145
    [1]谭成侠,徐瑶,曾仲武等.杀菌剂氟菌唑的合成及表征[J].农药, 2008, 47(7): 497-499
    [2] (a)金枫.三氟甲基苯胺生产与应用市场[J].精细化工原料及中间体, 2005, 8: 19-20; (b)蔡良珍. CI酸性红266的研究,华东理工大学研究生论文, 1998
    [3] Boudakian M. M. Preparation of 2-amino-5-halobenzotrifluoride[P]. US: 4008278, 1977-02-15
    [4]台立民,蔡良珍,沈永嘉. 4-氯-2-三氟甲基苯胺的合成[J].染料工业, 1998, 35(4): 31-33
    [5] Disdier C., Martinaud J. P., Sullivan J. W., et al. Method of preparing orthotrifluoromethyl aniline[P]. US: 4387246, 1983-06-07
    [6] Whalley W. B. Organic fluoro-compounds. Part I. Hydroxy-derivatives of benzotrifluoride[J]. J. Chem. Soc., 1949, 3016-3020
    [7] Forbes E. J., Stacey M., Tatlow J. C. et al. The synthesis of 1-, 2- and 3-trifluoromethylcarbazoles by the fischer-indole method[J]. Tetrahedron, 1960, 8, 1-2: 67-72
    [8] Junji S., Masayoshi F. Preparation of 4-chloro-α,α,α-ttrifluoro-o-toluidine[P]. JP: 2255643, 1990-10-16
    [9] (a)赵黔榕.正交法在化学试验中的应用[J].云南教育学院学报, 1998, 14(2): 51-57; (b)方开泰.均匀设计与均匀设计表[M].科学出版社: 1994; (c)郝拉娣,于化东.正交试验设计表的使用分析[J].编辑学报, 2005, 17(5): 334-335

© 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