Page 63 - 《精细化工》2023年第3期
P. 63

第 3 期                  杨文兵,等:  乙醇羰基化制丙酸及丙酸乙酯多相催化剂研究进展                                    ·519·


            该项技术于 1986 年被英国石油公司收购,并进一步                             2001, 8(1): 27-29, 22.
                                                               [3]   WU C H (吴翠红), WANG X Z (王喜正), LI W B (李文波), et al.
            扩展,目前甲醇均相羰基化合成醋酸及醋酸乙酯的                                 Production technology and market prospect of propionate[J]. Qilu
            Rh 基催化剂和 Ir 基催化剂已经实现工业化。然而,                            Petrochemical Technology (齐鲁石油化工), 2003, 31(2): 131-135
                                                               [4]   GAO P F (高鹏飞). Preparation of highly stable and highly dispersed
            相比于甲醇羰基化,乙醇均相羰基化反应条件苛刻,                                Ni-Cu based catalyst and its application in gas phase carbonylation of
            活性和选择性较低,美国杜邦公司进行初步的开发                                 ethanol[D]. Taiyuan: Taiyuan University of Technology (太原理工大
            研究后,并未进行规模化工业化应用                  [20,59-60] 。且均       学), 2021.
                                                               [5]   LIU L, ZHU Y F, LI J H, et al. Microbial production of propionic
            相反应存在产物与催化剂分离难的问题,而多相催                                 acid from propionibacteria: Current state, challenges and perspectives[J].
                                                                   Critical Reviews in Biotechnology, 2012, 32(4): 374-381.
            化剂则可以避免该问题,并且有利于节能和持续生                             [6]   WU X G (吴鑫干), LIU H M (刘含茂). Synthesis and applicaton of
            产 [61] 。目前,用于乙醇多相羰基化合成丙酸及丙酸                            propionic acid[J]. Speciality Petrochemicals (精细石油化工), 2003,
            乙酯的贵金属和非贵金属催化剂虽然均具有较高的                                 (2): 60-64.
                                                               [7]   FENG J X (冯景贤), WANG D W (王大为). Uses and production
            乙醇转化率,但是均存在选择性较低、稳定性差等                                 routes of propionic acid and ethyl propionate[J]. Guangdong
            问题,这也是制约该过程工业化的关键问题。                                   Chemical Industry (广东化工), 1997, (2): 15-17.
                                                               [8]   XUAN E F (玄恩锋). Production status and application of propionic
                                                                   acid at China and abroad[J]. Modern Chemical Industry (现代化工),
            4   结束语与展望                                             1999, 19(11): 33-35.
                                                               [9]   ROBERT Z J. Process and catalyst for carbonylating olefins:
                 目前,国内外主要集中在甲醇多相羰基化的研                              US005760284A[P]. 1998-06-02.
                                                               [10]  YAN T Z (颜廷昭), XU R (徐荣). Process and economic evalution of
            究,对乙醇多相羰基化催化剂研究较少。近年来乙                                 propionic acid produced by propionaldehyde oxidation method[J].
            醇羰基化制备丙酸技术受到广泛关注,目前研究的                                 Advances in Fine Petrochemicals (精细石油化工进展), 2001, 2(5):
                                                                   17-20, 16.
            贵金属和非贵金属催化剂体系均未实现工业化应                              [11]  SCHAFER M,  HOHN A, LIPPERT F. Process for selectively
            用,高选择性、高催化稳定性及低成本催化剂的开                                 preparing carboxylic acids by carbonylation  of  olefins:
                                                                   US005866716A[P]. 1999-02-02.
            发是该技术瓶颈突破和发展的关键。由于中国石油                             [12]  PAULIK F E, HERSHMAN  A, ROTH J F,  et al. Production of
            资源集中,以乙烯为原料的丙酸合成方法受到限制,                                propionic acid: US3944604A[P]. 1976-03-16.
                                                               [13]  SONG J (宋军). Study on nickel-based catalyst for wapor phase
            而相比于乙烯,乙醇来源丰富,且易于运输,因此,                                ethanol carbonylation[D]. Daqing: Northeast Petroleum University
            发展基于非石油途径的乙醇多相羰基化催化剂是重                                 (东北石油大学), 2013.
                                                               [14]  BAI L J (白丽军), WANG M  Y (王明义), DING C M (丁传敏),
            要的机遇和挑战。
                                                                   et al. Research progress of ethanol production from syngas[J].
                 今后的研究应集中在以下 3 个方面:(1)从活                           Modern Chemical Industry (现代化工), 2021, 41(12): 27-31, 37.
            性中心、载体、助剂及制备技术等角度出发,发展                             [15] MENG  Y  (孟迎),  BAI X Y (白晓宇), LI K (李凯),  et al. Ethanol
                                                                   production technologies and research progress of the coal chemical
            高效非贵金属卤化物体系。需要指出的是,碘化物                                 industry to ethanol technology in China[J]. Coal  and  Chemical
            作为传统醇羰基化体系中不可缺少的促进剂,具有                                 Industry (煤炭与化工), 2017, 40(8): 21-23.
                                                               [16]  TIAN M (田嫚), LUO B (罗冰), QIN H (秦虹). Research status and
            一定的腐蚀性和毒性,因此,发展无卤化物体系乙                                 prospect of ethanol production by fermentation[J]. Chemical
            醇多相羰基化是符合绿色化学且十分具有挑战性                                  Engineering Design Communications (化工设计通讯), 2019, 45(10):
                                                                   104-105.
            的。(2)随着现代原位表征技术及量化计算手段的                            [17]  SPIVEY J J, EGBEBI A, KIM S,  et al. Heterogeneous catalytic
            多样化,可为探究催化剂表界面在乙醇多相羰基化                                 synthesis of ethanol from biomass-derived syngas[J].  Chemical
                                                                   Society Reviews, 2007, 36(9): 1514-1528.
            合成丙酸及丙酸乙酯反应中的作用机制提供重要参
                                                               [18]  LAI C W (赖崇伟), ZENG J (曾健), YONG Y H (雍永祜),  et al.
            考,进而实现产物高选择性和催化稳定性,为开发                                 Study on homogeneous Rh complex catalyst for the carbonylation of
                                                                   ethanol to propionic acid[J]. Natural Gas Chemical Industry (天然气
            高效多相羰基化催化材料提供坚实的基础。(3)CO 2
                                                                   化工: C1 化学与化工), 2008, 33(4): 40-43.
            可直接作为羰基化试剂进行羰基化反应,而目前有                             [19]  BITSI G, JENNER G. Transition  metal catalysed carbonylation
            关直接采用 CO 2 作为羰基化试剂用于乙醇羰基化技                             reactions of primary alcohols[J]. Applied Catalysis, 1986, 21(1):
                                                                   201-203.
            术的研究还未见报道。因此,开发以 CO 2 直接作为                         [20]  LIAO L W (廖列文), CUI Y D (崔英德), ZHU X W (朱学文). The
            羰基化试剂的乙醇羰基化技术,即同时实现逆水汽                                 processs on preparation and application of  propionic acid and
                                                                   propionate[J]. Chemical Industry and Engineering Progress (化工进
            变换和乙醇羰基化耦合技术将是以后的发展方向,                                 展), 2001, (8): 38-41.
            也可为双碳战略目标的实现提供一定技术支撑。                              [21]  YUAN C M (袁传敏), ZHANG Y Z (张亚珍), HE Z X (何志祥).
                                                                   The preparation and performance of ethanol carbonylation catalyst in
            参考文献:                                                  propionic acid preparation[J]. Shanghai Chemical Industry (上海化
                                                                   工), 2011, 36(12): 4-7.
            [1]   DAKE S B, KOLHE D S,  CHAUDHARI R  V. Carbonylation of   [22]  SARKAR B R, CHAUDHARI  R  V. Carbonylation  of alkynes,
                 ethanol using homogeneous Rh complex catalyst: Kinetic study[J].   alkenes and alcohols using metal complex catalysts[J]. Catalysis
                 Journal of Molecular Catalysis, 1984, 24(1): 99-113.          Surveys from Asia, 2006, 9(29): 193-205.
            [2]   WANG B L (汪蓓蕾), ZHANG X B (张晓斌), SUN Z Y (孙志愿),   [23]  OUYANG H Y (欧阳华勇). Study on synthesis  of propionic acid
                 et al. Productive application and developing  peopect of propionic   with Ni-Pd/C bimetallic catalysit for carbonylation reaction[J].
                 acid[J]. Chemical Production and Technology (化工生产与技术),   Henan Chemical Industry (河南化工), 2009, 26(11): 34-36.
   58   59   60   61   62   63   64   65   66   67   68