Efficient Co-Production of Cyclohexanone and Phenol

Total Page:16

File Type:pdf, Size:1020Kb

Efficient Co-Production of Cyclohexanone and Phenol Efficient Co-production of Cyclohexanone and Phenol Dr. C. Morris Smith Project Chief Scientist ExxonMobil Chemical Company 10th China International Polyamide & Intermediates Forum Efficient Co-production of Cyclohexanone and Phenol C Morris Smith, Ph.D. ExxonMobil Chemical Company 1 Integrated Global Technology European Technology Center Brussels Clinton, NJ Baytown, TX Shanghai Baytown Technology Center Bangalore Shanghai Technology Center 2 47 10th China International Polyamide & Intermediates Forum Focused Strategic Effort Industry-leading technology creates innovative solutions Advantaged feeds • Feed flexibility Lower-cost manufacturing processes • Advanced process and catalysts • Improved energy efficiency and reliability Premium products • Higher performance • Higher value 3 Advanced Capabilities Expertise in catalysis and process, products, applications and manufacturing State-of-the-art capabilities • Fast catalyst discovery • Advanced chemical characterization • Scale-up World-class expertise • Catalyst discovery and scale-up • Process development and manufacturing • New products and applications Globally leveraged • Application development • Strong customer support 4 48 10th China International Polyamide & Intermediates Forum Hurdles to Cyclohexanone + Phenol Co-production First identified by Rhone-Poulenc in 1954, EP # 6B712264 Significant work in the patent literature by Texaco, Phillips and Phenolchemie over 50+ years did not lead to a commercial process Poor selectivity and low yield continued to limit commercial potential Cyclohexylbenzene (CHB) yield affected by over-alkylation to heavies and over-hydrogenation to lights Poor oxidation selectivity due to 10 secondary H’s that are also subject to oxidation, but don’t yield the desired products 5 ExxonMobil Advances Enable New Route Conventional Hock Process Alkylation Oxidation Cleavage + + Zeolite O2 H2SO4 Cumene Cumylhydroperoxide New Route OH In 1993, ExxonMobil introduced a new zeolite Cumene process that was rapidly commercialized worldwide New process greatly improves CHB selectivity using a new Hydroalkylation catalyst Selective oxidation of benzylic H achieved using N-Hydroxyphthalamide (NHPI) New EM Process Co-produces Cyclohexanone and Phenol at high yields Decouples the production of Phenol and Acetone All in a process with leading-edge energy efficiency 6 49 10th China International Polyamide & Intermediates Forum New EM Process Technology Development Research scoping from 2000 to 2005 Process development began in 2008 More than 100 patents filed Pilot plant demonstrating integrated process Integrated process design and model Seven reactive steps, multiple separations VLE data generation for non-ideal oxygenate species Detailed CFD modeling / design of critical mechanical systems New EM Process – Baytown, TX Pilot Plant Facility Scoping for commercial design underway 7 New EM Process: Hydroalkylation Hydroalkylation Oxidation Cleavage OH 2H2 + + Zeolite O2 NHPI H2SO4 Highly selective production of Yield ~ 97% Cyclohexylbenzene (CHB) No Propylene feed Transalkylation Cyclohexene generated in-situ and undergoes hydroalkylation over noble metal / zeolite catalyst Hydroalkylation 2H2 + + + Cyclohexane recovered using selective catalytic dehydrogenation Cyclohexylbenzene Heavies transalkylated to CHB Dehydrogenation Minimal yield loss from unrecoverable alkylation / isomerization products Enabled by proprietary catalysts 8 50 10th China International Polyamide & Intermediates Forum New EM Process: Oxidation Hydroalkylation Oxidation Cleavage OH 2H2 + + Zeolite O2 NHPI H2SO4 Thermal oxidation of CHB not Yield ~ 94% selective to desired PCH-HP Selectivity improved by NHPI, a Hydrogenation Dehydration chain propagating agent NHPI radical (PINO•) abstracts only the benzylic H, accelerating oxidation to desired PCH-HP Oxidation + Low levels of secondary NHPI hydroperoxides formed; some Phenyl Cyclohexyl Hydroperoxide (PCH-HP) recoverable to CHB Minor yield loss also occurs by Heavy PCH-HP decomposition Oxygenates High oxidation yield enabled by NHPI under optimized conditions 9 New EM Process: Cleavage Hydroalkylation Oxidation Cleavage OH 2H2 + + Zeolite O2 NHPI H2SO4 PCH-HP cleaved to Phenol and Yield ~ 99% Cyclohexanone Rates controlled to eliminate Cyclohexanone loss reactions 1-phenylcyclohexanol 1-phenylcyclohexene Cyclohexylbenzene 1-Phenylcyclohexene formed but O easily recovered Cleavage + β-scission can lead to the loss of Pheno Cyclohexanone PCH-HP by forming 6-Hydroxy- l hexaphenone (6HHP) When optimized, product O Heavy selectivity is nearly stoichiometric Oxygenates 6-hydroxyhexaphenone (6HHP) 10 51 10th China International Polyamide & Intermediates Forum New EM Process Flow Diagram Hydrocarbon Loop Overall Product Yield ~ 90% Oxygenates Separation Hydrogen Hydrogen Cyclohexane Purification Dehydrogenation Cyclohexanone Cleavage Cyclohexanone Product Phenol Fractionation Fractionation Benzene Benzene Hydroalkylation Purification Phenol Phenol Purification Hydrocarbon Fractionation Spent Air to Oxidation Scrubber Loop Transalkylation Hydrogenation Oxidation Cleavage Vent Air to Flare WO2009131769 11 Efficiency, Co-production Drive Advantage New EM Process Conversion 25% H2 50% Phenol Co-production of Phenol and Oxidation Hydroalkyation Separations Cleavage Cyclohexanone in one large-scale line Benzene 50% Cx-one CHB • 45% lower equipment count Higher conversion / yield process Phenol Conversion 25% C3= 62% Phenol • Smaller equipment Cumene Oxidation Alkylation Separations Cleavage • Reduced energy requirements Benzene 38% Acetone AMS De- Hydrogenation phenolization Avoids Acetone, no Propylene feed Cyclohexanone Conversion 4% Cyclohexane Cyclohexanol Products for highest quality Recovery Dehydration applications H2 Oxidation 100% Cx-one Hydrogenation Separations Cleavage Benzene Cyclohexane 12 52 10th China International Polyamide & Intermediates Forum Summary New EM Process produces two high value products in the Benzene derivative chain Breakthrough catalysis enables efficient co-production of Cyclohexanone and Phenol eliminating Acetone co-product and Propylene sourcing Leading-edge process design leads to substantial reduction in equipment count, increased scale, and improved capital utilization Significantly improved energy efficiency supports more sustainable production of petrochemical intermediates Commercial-scale facilities scoping is underway 13 53 .
Recommended publications
  • New Synthesis Routes for Production of Ε-Caprolactam by Beckmann
    New synthesis routes for production of ε-caprolactam by Beckmann rearrangement of cyclohexanone oxime and ammoximation of cyclohexanone over different metal incorporated molecular sieves and oxide catalysts Von der Fakultät für Mathematik, Informatik und Naturwissenschaften der RWTH Aachen University zur Erlangung des akademischen Grades eines Doktors der Naturwissenschaften genehmigte Dissertation vorgelegt von Anilkumar Mettu aus Guntur/Indien Berichter: Universitätprofessor Dr. Wolfgang F. Hölderich Universitätprofessor Dr. Carsten Bolm Tag der mündlichen Prüfung: 29.01.2009 Diese Dissertation ist auf den Internetseiten der Hochschulbibliothek online verfügbar. Dedicated to my Parents This work reported here has been carried out at the Institute for Chemical Technolgy and Heterogeneous Catalysis der Fakultät für Mathematik, Informatik und Naturwissenschaften in the University of Technology, RWTH Aachen under supervision of Prof. Dr. Wolfgang F. Hölderich between June 2005 and August 2008. ACKNOWLEDGEMENTS I would like to express my deepest sence of gratitude to my supervisor Prof. Dr. rer. nat. W. F. Hölderich for giving me the opportunity to do my doctoral study in his group. His guidance and teaching classes have allowed me to grow and learn my subject during my Ph.d. He has provided many opportunities for me to increase my abilities as a researcher and responsibilities as a team member. I am grateful for the financial support of this work from Sumitomo Chemicals Co., Ltd, Niihama, Japan (Part One) and Uhde Inventa-Fischer GmBH, Berlin (Part Two). Our collaborators at Sumitomo Chemicals Co., Ltd (Dr. C. Stoecker) and Uhde Inventa- Fischer GmBH (Dr. R. Schaller and Dr. A. Pawelski) provided thoughtful guidance and suggestions for each project.
    [Show full text]
  • Selective Hydrogenation of Phenol to Cyclohexanol Over Ni/CNT in the Absence of External Hydrogen
    energies Article Selective Hydrogenation of Phenol to Cyclohexanol over Ni/CNT in the Absence of External Hydrogen Changzhou Chen 1,2, Peng Liu 1,2, Minghao Zhou 1,2,3,*, Brajendra K. Sharma 3,* and Jianchun Jiang 1,2,* 1 Institute of Chemical Industry of Forest Products, Chinese Academy of Forestry, Key Laboratory of Biomass Energy and Material, Jiangsu Province, National Engineering Laboratory for Biomass Chemical Utilization, Key and Open Laboratory on Forest Chemical Engineering, SFA, Nanjing 210042, China; [email protected] (C.C.); [email protected] (P.L.) 2 Co-Innovation Center of Efficient Processing and Utilization of Forest Resources, Nanjing Forestry University, Nanjing 210037, China 3 Illinois Sustainable Technology Center, Prairie Research Institute, one Hazelwood Dr., Champaign, University of Illinois at Urbana-Champaign, Champaign, IL 61820, USA * Correspondence: [email protected] (M.Z.); [email protected] (B.K.S.); [email protected] (J.J.) Received: 7 January 2020; Accepted: 11 February 2020; Published: 14 February 2020 Abstract: Transfer hydrogenation is a novel and efficient method to realize the hydrogenation in different chemical reactions and exploring a simple heterogeneous catalyst with high activity is crucial. Ni/CNT was synthesized through a traditional impregnation method, and the detailed physicochemical properties were performed by means of XRD, TEM, XPS, BET, and ICP analysis. Through the screening of loading amounts, solvents, reaction temperature, and reaction time, 20% Ni/CNT achieves an almost complete conversion of phenol after 60 min at 220 ◦C in the absence of external hydrogen. Furthermore, the catalytic system is carried out on a variety of phenol derivatives for the generation of corresponding cyclohexanols with good to excellent results.
    [Show full text]
  • Photooxidation of Cyclohexane by Visible and Near-UV Light Catalyzed by Tetraethylammonium Tetrachloroferrate
    catalysts Article Photooxidation of Cyclohexane by Visible and Near-UV Light Catalyzed by Tetraethylammonium Tetrachloroferrate Kira M. Fahy , Adam C. Liu, Kelsie R. Barnard, Valerie R. Bright, Robert J. Enright and Patrick E. Hoggard * Department of Chemistry and Biochemistry, Santa Clara University, Santa Clara, CA 95053, USA; [email protected] (K.M.F.); [email protected] (A.C.L.); [email protected] (K.R.B.); [email protected] (V.R.B.); [email protected] (R.J.E.) * Correspondence: [email protected]; Tel.: +1-408-554-7810 Received: 2 August 2018; Accepted: 18 September 2018; Published: 19 September 2018 Abstract: Tetraethylammonium tetrachloroferrate catalyzes the photooxidation of cyclohexane heterogeneously, exhibiting significant photocatalysis even in the visible portion of the spectrum. The photoproducts, cyclohexanol and cyclohexanone, initially develop at constant rates, implying that the ketone and the alcohol are both primary products. The yield is improved by the inclusion of 1% acetic acid in the cyclohexane. With small amounts of catalyst, the reaction rate increases with the amount of catalyst employed, but then passes through a maximum and decreases, due to increased reflection of the incident light. The reaction rate also passes through a maximum as the percentage of dioxygen above the sample is increased. This behavior is due to quenching by oxygen, which at the same time is a reactant. Under one set of reaction conditions, the photonic efficiency at 365 nm was 0.018 mol/Einstein. Compared to TiO2 as a catalyst, Et4N[FeCl4] generates lower yields at wavelengths below about 380 nm, but higher yields at longer wavelengths. Selectivity for cyclohexanol is considerably greater with Et4N[FeCl4], and oxidation does not proceed past cyclohexanone.
    [Show full text]
  • Phenol Hydrogenation Over Pd/Zro2 Using Ethanol As Hydrogen Source
    4th International Conference on Sensors, Measurement and Intelligent Materials (ICSMIM 2015) Phenol hydrogenation over Pd/ZrO2 using ethanol as hydrogen source Yunjie Shi1, a, Bin Wang1,b, Junjun Shen1,c and Rongrong Miao1,d* 1Faculty of Environmental Science and Engineering, Kunming University of Science and Technology, Kunming 650500, China [email protected], [email protected], [email protected], d*[email protected] Keywords: Ethanol, Phenol, Hydrogenation, Pd/ZrO2 Abstract. Phenol hydrogenation over the Pd/ZrO2 catalyst has been carried out using ethanol as hydrogen source. The reaction temperature, catalyst and ethanol quantity are found to be influencing factors for effective phenol conversion. In all cases, low quantity (5%~10%) of ethanol and high temperature is efficient for a high phenol conversion. The results show that low quantity (5%~10%) of ethanol is efficient for high cyclohexanone selectivity at low temperature (573K). However, the selectivity of cyclohexanone, cyclohexanol and cyclohexane are insensitive to the ethanol quantity at high temperature (653K). It seems that ethanol plays an important dual role: as hydrogen source and as additive to control the phenol conversion and products selectivity. Introduction Cyclohexanone is the key raw material for the preparation of nylon 6 and adipic acid for nylon 66 [1,2]. The industrial production of cyclohexanone commonly involves the selective catalytic hydrogenation of phenol. On the other hand, phenol is an established environmental toxin and phenol-based waste originates form a variety of industrial sources including oil refineries, petrochemical units, polymeric resin manufacturing and plastic units [7]. Therefore, catalytic hydrogenation of phenol for cyclohexanone is an important chemical process, and has been widely studied [3-10].
    [Show full text]
  • Synthetic Turf Scientific Advisory Panel Meeting Materials
    California Environmental Protection Agency Office of Environmental Health Hazard Assessment Synthetic Turf Study Synthetic Turf Scientific Advisory Panel Meeting May 31, 2019 MEETING MATERIALS THIS PAGE LEFT BLANK INTENTIONALLY Office of Environmental Health Hazard Assessment California Environmental Protection Agency Agenda Synthetic Turf Scientific Advisory Panel Meeting May 31, 2019, 9:30 a.m. – 4:00 p.m. 1001 I Street, CalEPA Headquarters Building, Sacramento Byron Sher Auditorium The agenda for this meeting is given below. The order of items on the agenda is provided for general reference only. The order in which items are taken up by the Panel is subject to change. 1. Welcome and Opening Remarks 2. Synthetic Turf and Playground Studies Overview 4. Synthetic Turf Field Exposure Model Exposure Equations Exposure Parameters 3. Non-Targeted Chemical Analysis Volatile Organics on Synthetic Turf Fields Non-Polar Organics Constituents in Crumb Rubber Polar Organic Constituents in Crumb Rubber 5. Public Comments: For members of the public attending in-person: Comments will be limited to three minutes per commenter. For members of the public attending via the internet: Comments may be sent via email to [email protected]. Email comments will be read aloud, up to three minutes each, by staff of OEHHA during the public comment period, as time allows. 6. Further Panel Discussion and Closing Remarks 7. Wrap Up and Adjournment Agenda Synthetic Turf Advisory Panel Meeting May 31, 2019 THIS PAGE LEFT BLANK INTENTIONALLY Office of Environmental Health Hazard Assessment California Environmental Protection Agency DRAFT for Discussion at May 2019 SAP Meeting. Table of Contents Synthetic Turf and Playground Studies Overview May 2019 Update .....
    [Show full text]
  • Cyclohexanone
    CYCLOHEXANONE ALPHA CHEMICALS PTY LTD Chemwatch Hazard Alert Code: 2 Chemwatch: 1915 Issue Date: 05/09/2018 Version No: 6.1.7.7 Print Date: 21/06/2021 Safety Data Sheet according to WHS Regulations (Hazardous Chemicals) Amendment 2020 and ADG requirements S.GHS.AUS.EN SECTION 1 Identification of the substance / mixture and of the company / undertaking Product Identifier Product name CYCLOHEXANONE Chemical Name cyclohexanone C6-H10-O; Anon; anone; Hytrol o; ketohexamethylene; Nadone; pimelic pimelin ketone; pimelic ketone; cyclohexyl ketone; Hexanon; Sextone; Synonyms pennyroyal oil; Cat. No. 14033; Airex 930; Screen Opener Aerosol; OCD Thinner; Product Code: 8.22269 Proper shipping name CYCLOHEXANONE Chemical formula C6H10O Other means of identification Not Available CAS number 108-94-1 Relevant identified uses of the substance or mixture and uses advised against As a solvent for cellulose acetate, nitrocellulose, natural resins, vinyl resins, rubber, waxes, fats, shellac, and manufacture of ketone resins. In the production of adipic acid and caprolactam; production of polymers and resins. Reagent chemical. Used in wood stains; paint varnish and spot Relevant identified uses remover; degreasing of metals, polishes; textile dyeing and processing and in lubricating oil additives. Occurs naturally in the herb Pennyroyal and is responsible for the toxic effects in the misuse of Pennyroyal Oil in folk medicine, herbal teas. Details of the supplier of the safety data sheet Registered company name ALPHA CHEMICALS PTY LTD Address 4 ALLEN PLACE WETHERILL PARK NSW 2099 Australia Telephone 61 (0)2 9982 4622 Fax Not Available Website ~ Email [email protected] Emergency telephone number Association / Organisation ALPHA CHEMICALS PTY LTD Emergency telephone 61 (0)418 237 771 numbers Other emergency telephone Not Available numbers SECTION 2 Hazards identification Classification of the substance or mixture HAZARDOUS CHEMICAL.
    [Show full text]
  • Green Production Technology of Cyclohexanone
    N°456 / OC TOPIC(s) : Industrial chemistry / Alternative technologies Green Production Technology of Cyclohexanone AUTHORS Dongqiang MA / RESEARCH INSTITUTE OF PETROLEUM PROCESSING (RIPP),, SINOPEC, BEIJING 100083,, BEIJING Langyou WEN / SINOPEC, SINOPEC, BEIJING 100083, P. R., BEIJING Keyong YANG / SINOPEC, BEIJING 100083, P. R., BEIJING Baoning ZONG / SINOPEC, SINOPEC, BEIJING 100083, P. R. CHINA, BEIJING PURPOSE OF THE ABSTRACT 1 Introduction Cyclohexanone is an important organic chemical raw material and is the main intermediate for the manufacture of ?-caprolactam and adipic acid. It is also widely used as a solvent. Industrially, the production processes of cyclohexanone mainly include cyclohexane oxidation, phenol hydrogenation and cyclohexene hydration. Among the above processes, the application of the cyclohexane oxidation is most common. 2 Production technology of cyclohexanone The cyclohexane oxidation process uses an oxidizing agent (generally air) to oxidize cyclohexane to cyclohexyl hydroperoxide, and cyclohexyl hydroperoxide decomposes to a mixture of cyclohexanol and cyclohexanone (KA oil), and cyclohexanone obtained by dehydrogenation of cyclohexanol. The disadvantages of this process are: (1) the conversion of cyclohexane is low, only 3 to 5%, the yield of cyclohexanone is less than 80%; (2) a large amount of refractory waste alkali liquor is produced in the production process, so it is environment unfriendly; (3) intrinsic safety issues with oxidation processes. The phenol hydrogenation process is a relatively clean cyclohexanone production route, and the yield of cyclohexanone can reach 90% to 95%, which has the advantages of short process flow and high product purity. However, this process requires the vaporization of phenol and methanol, so the energy consumption is high; and the industrial application of the process is limited due to the shortage of phenol raw materials.
    [Show full text]
  • Interagency Committee on Chemical Management
    DECEMBER 14, 2018 INTERAGENCY COMMITTEE ON CHEMICAL MANAGEMENT EXECUTIVE ORDER NO. 13-17 REPORT TO THE GOVERNOR WALKE, PETER Table of Contents Executive Summary ...................................................................................................................... 2 I. Introduction .......................................................................................................................... 3 II. Recommended Statutory Amendments or Regulatory Changes to Existing Recordkeeping and Reporting Requirements that are Required to Facilitate Assessment of Risks to Human Health and the Environment Posed by Chemical Use in the State ............................................................................................................................ 5 III. Summary of Chemical Use in the State Based on Reported Chemical Inventories....... 8 IV. Summary of Identified Risks to Human Health and the Environment from Reported Chemical Inventories ........................................................................................................... 9 V. Summary of any change under Federal Statute or Rule affecting the Regulation of Chemicals in the State ....................................................................................................... 12 VI. Recommended Legislative or Regulatory Action to Reduce Risks to Human Health and the Environment from Regulated and Unregulated Chemicals of Emerging Concern ..............................................................................................................................
    [Show full text]
  • Adipic Acid Route: Oxidation of Cyclohexene Vs. Cyclohexane
    catalysts Article Adipic Acid Route: Oxidation of Cyclohexene vs. Cyclohexane Ana P. C. Ribeiro 1 , Elisa Spada 2, Roberta Bertani 2 and Luísa M. D. R. S. Martins 1,* 1 Centro de Química Estrutural and Departamento de Engenharia Química, Instituto Superior Técnico, Universidade de Lisboa, Av. Rovisco Pais, 1049-001 Lisboa, Portugal; [email protected] 2 Department of Industrial Engineering, University of Padova, 35122 Padova, Italy; [email protected] (E.S.); [email protected] (R.B.) * Correspondence: [email protected]; Tel.: +351-218-419-389 Received: 20 November 2020; Accepted: 8 December 2020; Published: 10 December 2020 Abstract: A cleaner alternative to the current inefficient oxidation of cyclohexane to adipic acid is presented. Direct oxidation of neat cyclohexene by aq. hydrogen peroxide to adipic acid is selectively achieved in good yield (46%), in the presence of the recyclable C-homoscorpionate iron(II) complex 3 [FeCl2{κ -HC(pz)3}] (pz = pyrazol-1-yl) and microwave irradiation, by a nitrous oxide-free protocol. Keywords: cyclohexene; adipic acid; oxidation; nitrous oxide; C-scorpionate; iron; microwave; ionic liquid; recyclable 1. Introduction Adipic acid (AA) is a highly relevant commodity produced at a large scale (over 3.5 mio metric tons/year and growing by ca. 5%/year) [1,2] worldwide, as it constitutes a building block for several industrial processes. It is mostly used for the synthesis of Nylon-6,6 polyamide; therefore, the rising demand for engineered plastics requires increased production of AA. Currently, adipic acid is mainly obtained by an inefficient and environmentally harmful two-step process [1,3] involving catalytic cyclohexane oxidation to cyclohexanol and cyclohexanone mixture followed by its oxidation with nitric acid.
    [Show full text]
  • ABSTRACT RUDD, HAYDEN. Assessing the Vulnerability Of
    ABSTRACT RUDD, HAYDEN. Assessing the Vulnerability of Coastal Plain Groundwater to Flood Water Intrusion using High Resolution Mass Spectrometry. (Under the direction of Dr. Elizabeth Guthrie Nichols). Communities in the North Carolina Coastal Plain (NCCP) depend on safe and reliable groundwater for private well use, agriculture, industry, and livelihoods. Although storm intensity and frequency are predicted to increase in coastal areas, the risk of surficial and confined aquifer contamination from extreme storms is not understood. In September 2018, Hurricane Florence caused extensive flooding across the NCCP for several weeks. The North Carolina Department of Environmental Quality (NCDEQ) Groundwater Management Branch had just completed sampling of some wells in their monitoring network when Hurricane Florence made landfall. NCDEQ returned to these wells, particularly those flooded by Hurricane Florence, for post-flood sampling. These groundwater samples were analyzed by NCDEQ for regulated semi-volatile organics with few to any detections of regulated organic contaminants. NCDEQ provided NC State the same sample extracts for analysis by high resolution mass spectrometry (HRMS). This research reports on the non-targeted and suspect-screening HRMS analyses of groundwater from nested monitoring wells. Some monitoring well sites experienced flooding during the study period, and some did not. The goal of this research was to advance our understanding of coastal aquifer susceptibility to flooding by producing the first comprehensive organic chemical profiles of coastal aquifers and by determining if aquifers have distinct organic chemical profiles that change after flooding events. This study used HRMS analyses to produce the first comprehensive organic chemical profiles of 11 aquifers in the coastal plain.
    [Show full text]
  • Liquid-Phase Hydrogenation of Phenol to Cyclohexanone Over Supported Palladium Catalysts
    CORE Metadata, citation and similar papers at core.ac.uk Provided by Universitas Diponegoro: Undip E-Journal System (UEJS) Portal Available online at BCREC Website: http://bcrec.undip.ac.id Bulletin of Chemical Reaction Engineering & Catalysis, 11 (3), 2016, 354-362 Research Article Liquid-phase Hydrogenation of Phenol to Cyclohexanone over Supported Palladium Catalysts Lihui Fan*, Luyang Zhang, Yanming Shen*, Dongbin Liu, Nasarul Wahab, Md Mahmud Hasan Department of Chemical Engineering, Shenyang University of Chemical Technology, China 110142 Received: 7th March 2016; Revised: 13rd May 2016; Accepted: 7th June 2016 Abstract The ZSM-5, -Al2O3, SiO2 and MgO supported Pd-catalysts were prepared for the phenol hydrogenation to cyclohexanone in liquid-phase. The natures of these catalysts were characterized by XRD, N2 adsorption-desorption analysis, H2-TPR, CO2-TPD and NH3-TPD. The catalytic performance of the supported Pd-catalyst for phenol hydrogenation to cyclohexanone is closely related to nature of the support and the size of Pd nanoparticles. The Pd/MgO catalyst which possesses higher basicity shows higher cyclohexanone selectivity, but lower phenol conversion owing to the lower specific surface area. The Pd/SiO2 catalyst prepared by precipitation gives higher cyclohexanone selectivity and phenol conversion, due to the moderate amount of Lewis acidic sites, and the smaller size and higher dispersion of Pd nanoparticles on the surface. Under the reaction temperature of 135 oC and H2 pressure of 1 MPa, after reacting for 3.5 h, the phenol conversion of 71.62% and the cyclohexanone selectivity of 90.77% can be obtained over 0.5 wt% Pd/SiO2 catalyst.
    [Show full text]
  • Modeling the Liquid Phase Autoxidation of Cyclohexylbenzene to Hydroperoxide
    chemical engineering research and design 1 2 4 ( 2 0 1 7 ) 202–210 Contents lists available at ScienceDirect Chemical Engineering Research and Design journal homepage: www.elsevier.com/locate/cherd Modeling the liquid phase autoxidation of cyclohexylbenzene to hydroperoxide a a a a a,b,∗ Weizhen Sun , Shenglu Zhang , Junfeng Qiu , Zhimei Xu , Ling Zhao a State Key Laboratory of Chemical Engineering, East China University of Science and Technology, Shanghai 200237, China b Engineering Research Center of Process System Engineering, East China University of Science and Technology, Ministry of Education, Shanghai 200237, China a r a t i c l e i n f o b s t r a c t Article history: The liquid phase autoxidation of cyclohexylbenzene (CHB) to CHB hydroperoxide (CHBHP) is Received 26 November 2016 the key step of green production of phenol. The CHB oxidation kinetics was originally inves- Received in revised form 3 April tigated by semibatch experiments under various oxygen partial pressures. Kinetic models 2017 to deal with oxygen-rich and oxygen-poor conditions were developed on the basis of free Accepted 17 June 2017 radical chain mechanism. It was found that the activation energy of the rupture of the bond Available online 24 June 2017 O O of molecule CHBHP was close to that of cumene hydroperoxide, while the activation energy of hydrogen abstraction from the tert-butyl carbon of CHB was reasonably larger than Keywords: that of cumene due to the steric effect. The kinetic model involving the oxygen addition to • Kinetic model R (Model II) can be used to deal with various oxygen partial pressure conditions.
    [Show full text]