Cyclohexanone oxime serves as a crucial intermediate in the synthesis of caprolactam,which is an essential precursor for manufacturing nylonfibers,high-performance engineering plastics,and specialized plasticfilms.Cat...Cyclohexanone oxime serves as a crucial intermediate in the synthesis of caprolactam,which is an essential precursor for manufacturing nylonfibers,high-performance engineering plastics,and specialized plasticfilms.Catalytic hydrogenation of nitrocyclohexane to cyclohexanone oxime has been documented to be an atom-economical,green and environmentally friendly process.In this review,wefirst introduce the current design rules of catalysts for catalytic hydrogenation of nitrocyclohexane in terms of both active metals and supports.Secondly,we discuss the influence of solvent effects on the cyclohexanone oxime from the nitrocyclohexane conversion.In addition,we concisely discuss typically proposed reaction pathways for the hydrogenation of nitrocyclohexane to produce cyclohexanone oxime.Finally,we provide our perspectives on some issues for catalytic conversion of nitrocyclohexane to cyclohexanone oxime in the future.展开更多
An innovative green process of producing ε-caprolactam was proposed by integrating ammoximation and Beckmann rearrangement effectively. As a first part of the new process, TS-1 molecular sieve-catalyzed synthesis of ...An innovative green process of producing ε-caprolactam was proposed by integrating ammoximation and Beckmann rearrangement effectively. As a first part of the new process, TS-1 molecular sieve-catalyzed synthesis of cyclohexanone oxime from cyclohexanone, ammonia and hydrogen peroxide was carried out in a batch plant. Cyclohexane was used as the solvent in the three-phase reaction system. The influences of essential process parameters on ammoximation were investigated. Under the reaction conditions as catalyst content of 2.5% (by mass); H 2 O 2 /yclohexanone molar ratio of 1.10; NH 3 /cyclohexanone molar ratio of 2.20; reaction temperature of 343 K; reaction time of 5 h, high conversion of cyclohexanone and selectivity to oxime (both>99%) were obtained. Thus, the three-phase ammoximation process showed equal catalytic activity as TS-1 but much more convenient and simpler for the separation of catalyst in comparison to the industrial two-phase system with t-butanol used as solvent.展开更多
The addition of platinum over the B2O3/TiO2-ZrO2 remarkably enhanced its catalytic stability in the vapor phase Beckmann rearrangement of cyclohexanone oxime under the carder gas of H2. The content of coke deposited ...The addition of platinum over the B2O3/TiO2-ZrO2 remarkably enhanced its catalytic stability in the vapor phase Beckmann rearrangement of cyclohexanone oxime under the carder gas of H2. The content of coke deposited on catalyst surface was decreased from 1.92% over the B2O3/TiO2-ZrO2 to 1.14% over the platinum promoted B2O3/TiO2-ZrO2 after reaction of six hours. This result indicates that the platinum added on the B2O3/TiO2-ZrO2 catalyst plays an important role in reducing the coke formation on the catalyst surface.展开更多
The liquid phase Beckmann rearrangement of cyclohexanone oxime (CHO) using fuming sulfuric acid as a catalyst is a traditional method for preparing ε-caprolactam (CPL). This process has drawbacks, such as environment...The liquid phase Beckmann rearrangement of cyclohexanone oxime (CHO) using fuming sulfuric acid as a catalyst is a traditional method for preparing ε-caprolactam (CPL). This process has drawbacks, such as environmental pollution, corrosion of equipment, and low added value of by-product ammonium sulfate. This article designed and prepared a green silica gel-supported trifluoromethanesulfonic acid catalyst for the liquid-phase Beckmann rearrangement of CHO to prepare (CPL). The influencing factors of catalyst preparation and the optimal reaction conditions for Beckmann rearrangement were investigated. It was found that the optimal conditions for catalyst preparation were as follows: raw material silica gel:trifluoromethanesulfonic acid = 1:0.2 (mass ratio), room temperature, stirring time of 2.5 hours, and solvent of acetonitrile, silica gel mesh size is 100 - 200. The optimal reaction conditions for Beckmann rearrangement are CHO: catalyst = 1:2 (mass ratio), temperature of 130˚C, solvent of benzonitrile, volume of 30 mL/g CHO, and reaction time of 4 hours. Under the above conditions, the conversion of CHO is 90%, and the selectivity of CPL is 90%.展开更多
An intrinsic kinetics of cyclohexanone ammoximation in the liquid phase over titanium silicate molecular sieves is investigated in an isothermal slurry reactor at different initial reactant concentrations, catalyst lo...An intrinsic kinetics of cyclohexanone ammoximation in the liquid phase over titanium silicate molecular sieves is investigated in an isothermal slurry reactor at different initial reactant concentrations, catalyst loading, and reaction temperature. The rate equations are developed by analyzing data of kinetic measurements. More than 10 side reactions were found. H2O2 decomposition reaction must be considered and other side reactions can be neglected in the kinetic modeling. The predicted values of reaction rates based on the kinetic models are almost consistent with experimental ones. The models have guidance to the selection of reactor types and they are useful to the design and operation of reactor used.展开更多
A selective reaction of cyclohexanone oxime-blocked tolylene-2,4-diisocyanate（2,4-TDI）with amino siloxane was observed,in which amines were capable of discriminating two reactive groups in the 2,4-TDI molecule.Thus,...A selective reaction of cyclohexanone oxime-blocked tolylene-2,4-diisocyanate（2,4-TDI）with amino siloxane was observed,in which amines were capable of discriminating two reactive groups in the 2,4-TDI molecule.Thus,tolylene-2-tert-butyldimethylsilyloxyethyl carbamide-4-cyclohexanone oxime carbamate was synthesized and its precise structure was determined by single-crystal X-ray diffraction.Moreover,it was found that oxime-blocked isocyanate could react selectively with the–NH2group with the–OH group unprotected in ethanolamine.展开更多
环己酮肟气相Beckmann重排反应RBS-1催化剂在高温反应时易失活,导致催化剂费用居高不下。为提高技术经济性,实现失活催化剂性能的高效恢复,系统研究RBS-1催化剂失活机理、再生手段及催化性能。采用N_(2)物理吸附-脱附技术考察催化剂失...环己酮肟气相Beckmann重排反应RBS-1催化剂在高温反应时易失活,导致催化剂费用居高不下。为提高技术经济性,实现失活催化剂性能的高效恢复,系统研究RBS-1催化剂失活机理、再生手段及催化性能。采用N_(2)物理吸附-脱附技术考察催化剂失活前后与再生前后的比表面积及孔结构变化,并结合XRD、FT-IR和^(29)Si MAS NMR表征技术探讨了RBS-1催化剂在失活与再生过程中活性中心的演变规律。研究发现,失活RBS-1催化剂物相结构保持完好,但BET比表面积和孔体积均有明显降低,说明催化剂失活主要为积炭覆盖催化剂活性位点并堵塞孔道所致。针对积炭堵孔导致的催化剂失活问题,采用烧炭、含氮化合物改性处理构建巢式硅羟基活性位点等手段对失活催化剂进行再生研究。结果表明,在530℃下烧炭能将催化剂表面及孔道内的大部分积炭烧除,催化剂性能可恢复90%以上;对脱炭后的催化剂进一步改性处理,最优催化剂性能可恢复98%以上。展开更多
基金financial support from the National Natural Science Foundation of China(22125202,92461312,U24A20487,92361201)Natural Science Foundation of Jiangsu Province(BK20220033).
文摘Cyclohexanone oxime serves as a crucial intermediate in the synthesis of caprolactam,which is an essential precursor for manufacturing nylonfibers,high-performance engineering plastics,and specialized plasticfilms.Catalytic hydrogenation of nitrocyclohexane to cyclohexanone oxime has been documented to be an atom-economical,green and environmentally friendly process.In this review,wefirst introduce the current design rules of catalysts for catalytic hydrogenation of nitrocyclohexane in terms of both active metals and supports.Secondly,we discuss the influence of solvent effects on the cyclohexanone oxime from the nitrocyclohexane conversion.In addition,we concisely discuss typically proposed reaction pathways for the hydrogenation of nitrocyclohexane to produce cyclohexanone oxime.Finally,we provide our perspectives on some issues for catalytic conversion of nitrocyclohexane to cyclohexanone oxime in the future.
基金Supported by the National Natural Science Foundation of China and Sinopec (20736009)
文摘An innovative green process of producing ε-caprolactam was proposed by integrating ammoximation and Beckmann rearrangement effectively. As a first part of the new process, TS-1 molecular sieve-catalyzed synthesis of cyclohexanone oxime from cyclohexanone, ammonia and hydrogen peroxide was carried out in a batch plant. Cyclohexane was used as the solvent in the three-phase reaction system. The influences of essential process parameters on ammoximation were investigated. Under the reaction conditions as catalyst content of 2.5% (by mass); H 2 O 2 /yclohexanone molar ratio of 1.10; NH 3 /cyclohexanone molar ratio of 2.20; reaction temperature of 343 K; reaction time of 5 h, high conversion of cyclohexanone and selectivity to oxime (both>99%) were obtained. Thus, the three-phase ammoximation process showed equal catalytic activity as TS-1 but much more convenient and simpler for the separation of catalyst in comparison to the industrial two-phase system with t-butanol used as solvent.
文摘The addition of platinum over the B2O3/TiO2-ZrO2 remarkably enhanced its catalytic stability in the vapor phase Beckmann rearrangement of cyclohexanone oxime under the carder gas of H2. The content of coke deposited on catalyst surface was decreased from 1.92% over the B2O3/TiO2-ZrO2 to 1.14% over the platinum promoted B2O3/TiO2-ZrO2 after reaction of six hours. This result indicates that the platinum added on the B2O3/TiO2-ZrO2 catalyst plays an important role in reducing the coke formation on the catalyst surface.
文摘The liquid phase Beckmann rearrangement of cyclohexanone oxime (CHO) using fuming sulfuric acid as a catalyst is a traditional method for preparing ε-caprolactam (CPL). This process has drawbacks, such as environmental pollution, corrosion of equipment, and low added value of by-product ammonium sulfate. This article designed and prepared a green silica gel-supported trifluoromethanesulfonic acid catalyst for the liquid-phase Beckmann rearrangement of CHO to prepare (CPL). The influencing factors of catalyst preparation and the optimal reaction conditions for Beckmann rearrangement were investigated. It was found that the optimal conditions for catalyst preparation were as follows: raw material silica gel:trifluoromethanesulfonic acid = 1:0.2 (mass ratio), room temperature, stirring time of 2.5 hours, and solvent of acetonitrile, silica gel mesh size is 100 - 200. The optimal reaction conditions for Beckmann rearrangement are CHO: catalyst = 1:2 (mass ratio), temperature of 130˚C, solvent of benzonitrile, volume of 30 mL/g CHO, and reaction time of 4 hours. Under the above conditions, the conversion of CHO is 90%, and the selectivity of CPL is 90%.
文摘An intrinsic kinetics of cyclohexanone ammoximation in the liquid phase over titanium silicate molecular sieves is investigated in an isothermal slurry reactor at different initial reactant concentrations, catalyst loading, and reaction temperature. The rate equations are developed by analyzing data of kinetic measurements. More than 10 side reactions were found. H2O2 decomposition reaction must be considered and other side reactions can be neglected in the kinetic modeling. The predicted values of reaction rates based on the kinetic models are almost consistent with experimental ones. The models have guidance to the selection of reactor types and they are useful to the design and operation of reactor used.
基金financially supported by the National Natural Science Foundation of China (Nos. 21176147, 21276149 and 21204044)Program for Scientifc Research Innovation Team in Colleges and Universities of Shandong Province
文摘A selective reaction of cyclohexanone oxime-blocked tolylene-2,4-diisocyanate（2,4-TDI）with amino siloxane was observed,in which amines were capable of discriminating two reactive groups in the 2,4-TDI molecule.Thus,tolylene-2-tert-butyldimethylsilyloxyethyl carbamide-4-cyclohexanone oxime carbamate was synthesized and its precise structure was determined by single-crystal X-ray diffraction.Moreover,it was found that oxime-blocked isocyanate could react selectively with the–NH2group with the–OH group unprotected in ethanolamine.
基金was supported by the National Basic Research Program of China(‘‘973’’Program,No.G2000048005)the National Natural Science Foundation of China(No.21276183)
文摘环己酮肟气相Beckmann重排反应RBS-1催化剂在高温反应时易失活,导致催化剂费用居高不下。为提高技术经济性,实现失活催化剂性能的高效恢复,系统研究RBS-1催化剂失活机理、再生手段及催化性能。采用N_(2)物理吸附-脱附技术考察催化剂失活前后与再生前后的比表面积及孔结构变化,并结合XRD、FT-IR和^(29)Si MAS NMR表征技术探讨了RBS-1催化剂在失活与再生过程中活性中心的演变规律。研究发现,失活RBS-1催化剂物相结构保持完好,但BET比表面积和孔体积均有明显降低,说明催化剂失活主要为积炭覆盖催化剂活性位点并堵塞孔道所致。针对积炭堵孔导致的催化剂失活问题,采用烧炭、含氮化合物改性处理构建巢式硅羟基活性位点等手段对失活催化剂进行再生研究。结果表明,在530℃下烧炭能将催化剂表面及孔道内的大部分积炭烧除,催化剂性能可恢复90%以上;对脱炭后的催化剂进一步改性处理,最优催化剂性能可恢复98%以上。
