期刊文献+

Co/Mn/Br催化体系中CO_2协助氧化对二甲苯制对苯二甲酸 被引量:3

CO_2-Aided Aerial Oxidation of p-Xylene to Terephthalic Acid with Co/Mn/Br Catalyst
下载PDF
导出
摘要 以对二甲苯(PX)为原料、醋酸和水为溶剂,在Co/Mn/Br催化体系作用下,用N_2/O_2/CO_2混合气氧化PX制备了对苯二甲酸(TA)。考察了混合气中CO_2含量对氧化反应速率、氧化反应中间产物含量和TA收率的影响。同时,分析了PX液相氧化条件下CO_2的作用机理。实验结果表明,CO_2加快了PX的氧化反应进程,使氧化过程的耗氧速率明显加快。在反应液中w(Co)=0.030%、w(Mn)=0.060%、w(Br)=0.075%(相当于反应液的质量)和反应温度195℃的条件下,使用V(CO_2)∶V(O_2)∶V(N_2)=40∶21∶39的混合气氧化时,CO_2的协助氧化作用最为明显,与用空气氧化PX制备TA相比,反应时间缩短了4~5min,此时固体产物TA中中间产物的含量最低。紫外可见光谱分析表明,在PX液相催化氧化体系下加入CO_2,形成了一种活性组分,它促进了金属离子价位的转换。 CO2-aided aerial oxidation of p-xylene to terephthalic acid using Co/Mn/Br catalyst in liquid media of acetic acid and water was studied. The influence of CO2 content in feed gas on reaction rate, intermediate product concentration and yield of terephthalic acid was investigated. Possible mechanism of CO2-aided oxidations was discussed. Experimental results showed that oxidation was accelerated in the presence of COz. The optimal reaction conditions were: temperature 195℃, gas mixture rate V( CO2 ) : V( O2) : V( N2 ) 40 : 21 : 39, and concentration of Co/Mn/Br catalyst based on total liquid mixture : Co mass fraction 0. 030%, Mn mass fraction 0.060% and Br mass fraction 0. 075%. In comparing with ordinary aerial oxidation of p-xylene to terephthalic acid without CO2, reaction time reduced by 4 -5 min, and impurity content in solid product terephthalic acid was the minimum. UV-Vis investigation demonstrated that a new active species formed with addition of CO2 as a co-oxidant in p-xylene oxidation, which promoted the conversion of metallic ion valence, so promoted the reaction rate.
出处 《石油化工》 CAS CSCD 北大核心 2009年第10期1054-1058,共5页 Petrochemical Technology
关键词 对二甲苯 对苯二甲酸 二氧化碳 协助氧化 钴/锰/溴催化剂 p-xylene terephthalic acid carbon dioxide aided oxidation cobalt/manganese/ bromine catalyst
  • 相关文献

参考文献10

  • 1Samsung General Chemicals Co. Ltd. Method of Producing Aromatic Carboxylic Acids by Oxidizing Alkyl Aromatic Hydrocarbons or Partially Oxidized Intermediates Thereof. US Pat Appl,US 6194607. 2001.
  • 2Yoo J S, Lin P S, Elfline S D. Gas-Phase Oxygen Oxidations of Alkylaromatics over CVD Fe/Mo/Borosilicate Molecular Sieve. II. The Role of Carbon Dioxide as a Co-Oxidant. Appl Catal, A, 1993,106(2) :259 -273.
  • 3Amoco Corp. Catalytic Oxidation and Oxidative Dehydrogenation Using Metal-Compound-Loaded, Deboronated Hams-1 b Crystalline Borosilicate Molecular Sieve Compositions. US Pat Appl, US 5324702. 1994.
  • 4Choi Min-Ho, Baek Seung-Chan, Chavan S A. CO2-Assisted Aerial Oxidation of para-Methyl Anisole with Co/Mn Catalytic System. Appl Catal,A, 2003,247 ( 3 ) : 303 - 308.
  • 5Baeka Seung-Chan, Roha Hyun-Seog, Chavan S A. The Promotional Effect of CO2 in Ethylbenzene Oxidation with MC-Type Catalytic System. Appl Catal,A, 2003,244( 1 ) : 19 -25.
  • 6刘建新,邢跃军,徐彦,王丽军,王勤波.对二甲苯氧化过程模拟及热稳定性分析[J].聚酯工业,2004,17(5):27-30. 被引量:2
  • 7尤侯平,刘建新,邢跃军.富氧条件下对二甲苯氧化反应的研究[J].石油化工,2005,34(9):870-874. 被引量:5
  • 8盖旭东.乙酸—对二甲苯体系催化氧化动力学研究[J].石油化工,1993,22(11):715-719. 被引量:7
  • 9Fujita E, Creutz C, Sutin N,et al. Carbon Dioxide Activation by Cobalt Macrocycles: Factors Affecting CO2 and CO Binding. J Am Chem Soc, 1991,113( 1 ) :343 -353.
  • 10Sheldon R A, van Santen R A. Catalytic Oxidations: Principles and Applications. Singapore : World Scientific, 1995. 30 - 50.

二级参考文献11

  • 1盖旭东.乙酸—对二甲苯体系催化氧化动力学研究[J].石油化工,1993,22(11):715-719. 被引量:7
  • 2Sridhar T, Potter O E.Interfacial areas in gas- liquid stirred vessels[J]. Chemical Engineering Science. 1980,35:683-695.
  • 3Sridhar T, Potter O E. Gas Holdup and Bubble Diameters in Pressurized Gas-Liquid Stirred Vessels[J]. Ind Eng Chem Fundam,1980,19:21-26.
  • 4盖旭东,1987年
  • 5盖旭东.[D].天津: 天津大学,1987.
  • 6.精对苯二甲酸生产工艺技术规程[C].[S].南京:扬子石油化工公司化工厂,1989..
  • 7卢焕章.石油化工基础数据手册[M].北京:化学工业出版社,1994..
  • 8普拉塞尔技术有限公司.对苯二甲酸的生产[P].中国:CN95105714.2001.
  • 9Kingsley J P, Roby A K. Terephthalic Acid Production. US Pat Appl,US 5371283. 1994.
  • 10金斯利JP 罗比AK 里兹LM.对苯二甲酸的生产[P].中国:CN 941 17004.1999.

共引文献11

同被引文献54

引证文献3

二级引证文献3

相关作者

内容加载中请稍等...

相关机构

内容加载中请稍等...

相关主题

内容加载中请稍等...

浏览历史

内容加载中请稍等...
;
使用帮助 返回顶部