The Art of Heterogeneous Catalytic Hydrogenation Part 1
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Production of Cyclohexane Through Catalytic Hydrogenation of Benzene
Production of Cyclohexane through Catalytic Hydrogenation of Benzene Background Cyclohexane is industrially produced from Benzene as it is not a naturally available resource. Cyclohexane undergoes oxidation reactions yielding Cyclohexanone and Cyclohexanol which are precursors for the production of Adipic acid and Caprolactum. Caprolactum is the raw material used for producing polymer Nylon-6. Benzene reacts with a mixture of hydrogen and methane in contact with a Nickel based catalyst producing Cyclohexane. The conversion of this vapour phase reaction is almost 99%. Reaction involved: Benzene + Hydrogen Cyclohexane (Vapour Phase) Reactor Used: Catalytic Packed Bed Conversion Reactor Reactor conditions: Outlet Temperature = 497 K, Pressure Drop = 1.02 atm Catalyst Used: Nickel Based Process Description Fresh benzene (370 kmol/h) and excess hydrogen (1470 kmol/h) is preheated to a temperature of 422 K and sent to a packed bed reactor. A vapour phase reaction occurs in the reactor at 497 K which converts benzene to cyclohexane through catalytic hydrogenation of benzene. The conversion of this reaction is about 99%. The reactor products are cooled to 370 K and sent through a pressure reduction valve which reduces the pressure of the stream from 30 atm to 24 atm. A two stage separator separates the product cyclohexane from unreacted hydrogen and methane- first at a high pressure (24 atm) and then at a lower pressure (3 atm). The unreacted hydrogen-methane mixture is recovered from the top of the flash column and is sent to a splitter having a splittling ratio of 9:1. The smaller stream is sent as a recycle stream and mixes with fresh hydrogen, while the rest is drawn out as fuel gas for incinerators. -
Catalytic Transfer Hydrogenolysis Reactions for Lignin Valorization to Fuels and Chemicals
catalysts Review Catalytic Transfer Hydrogenolysis Reactions for Lignin Valorization to Fuels and Chemicals Antigoni Margellou 1 and Konstantinos S. Triantafyllidis 1,2,* 1 Department of Chemistry, Aristotle University of Thessaloniki, 54124 Thessaloniki, Greece; [email protected] 2 Chemical Process and Energy Resources Institute, Centre for Research and Technology Hellas, 57001 Thessaloniki, Greece * Correspondence: [email protected] Received: 31 October 2018; Accepted: 10 December 2018; Published: 4 January 2019 Abstract: Lignocellulosic biomass is an abundant renewable source of chemicals and fuels. Lignin, one of biomass main structural components being widely available as by-product in the pulp and paper industry and in the process of second generation bioethanol, can provide phenolic and aromatic compounds that can be utilized for the manufacture of a wide variety of polymers, fuels, and other high added value products. The effective depolymerisation of lignin into its primary building blocks remains a challenge with regard to conversion degree and monomers selectivity and stability. This review article focuses on the state of the art in the liquid phase reductive depolymerisation of lignin under relatively mild conditions via catalytic hydrogenolysis/hydrogenation reactions, discussing the effect of lignin type/origin, hydrogen donor solvents, and related transfer hydrogenation or reforming pathways, catalysts, and reaction conditions. Keywords: lignin; catalytic transfer hydrogenation; hydrogenolysis; liquid phase reductive depolymerization; hydrogen donors; phenolic and aromatic compounds 1. Introduction The projected depletion of fossil fuels and the deterioration of environment by their intensive use has fostered research and development efforts towards utilization of alternative sources of energy. Biomass from non-edible crops and agriculture/forestry wastes or by-products is considered as a promising feedstock for the replacement of petroleum, coal, and natural gas in the production of chemicals and fuels. -
Appendix F. Glossary
Appendix F. Glossary 2DEG 2-dimensional electron gas A/D Analog to digital AAAR American Association for Aerosol Research ADC Analog-digital converter AEM Analytical electron microscopy AFM Atomic force microscope/microscopy AFOSR Air Force Office of Scientific Research AIST (Japan) Agency of Industrial Science and Technology AIST (Japan, MITI) Agency of Industrial Science and Technology AMLCD Active matrix liquid crystal display AMM Amorphous microporous mixed (oxides) AMO Atomic, molecular, and optical AMR Anisotropic magnetoresistance ARO (U.S.) Army Research Office ARPES Angle-resolved photoelectron spectroscopy ASET (Japan) Association of Super-Advanced Electronics Technologies ASTC Australia Science and Technology Council ATP (Japan) Angstrom Technology Partnership ATP Adenosine triphosphate B Magnetic flux density B/H loop Closed figure showing B (magnetic flux density) compared to H (magnetic field strength) in a magnetizable material—also called hysteresis loop bcc Body-centered cubic BMBF (Germany) Ministry of Education, Science, Research, and Technology (formerly called BMFT) BOD-FF Bond-order-dependent force field BRITE/EURAM Basic Research of Industrial Technologies for Europe, European Research on Advanced Materials program CAD Computer-assisted design CAIBE Chemically assisted ion beam etching CBE Chemical beam epitaxy 327 328 Appendix F. Glossary CBED Convergent beam electron diffraction cermet Ceramic/metal composite CIP Cold isostatic press CMOS Complementary metal-oxide semiconductor CMP Chemical mechanical polishing -
Chapter 3 CHEMICAL MODIFICATION of OILS and FATS
Chapter 3 CHEMICAL MODIFICATION OF OILS AND FATS From the fats and oils obtained from natural resources, the majority of them are used directly or just after refinement. While the others are used after modification by chemical process. This chapter lists some typical modifications of fats and oils by chemical means. 3-1 Alkaline Hydrolysis Figure 3-1-1: Alkaline hydrolysis (saponification) of oil to make soaps. There are many methods for hydrolysis of triacylglycerol molecule. The most common method is alkaline hydrolysis. Heating (around 100˚C)triacylglycerols with aqueous solu- tion of sodium hydroxide results in glycerol and alkaline salt of fatty acid (i.e. soap) (Figure 3-1-1). This is called saponification, and used for production of soap. 3-2 Hydrogenation Number of double bonds in oils and fats affects physical property such as melting point, crystallinity. Generally, double bonds reduce the oil’s melting point. Therefore, oils rich in unsaturated fatty acids are liquid, while ones with small amount of unsaturated fatty acids are solid or semi-solid. Hydrogenation is a process to add hydrogen atoms into double bonds of unsaturated fatty acids (Figure 3-2-1). As the result of hydrogenation, liquid oil becomes solid or semi-solid. A typical example of hydrogenation is in the process of margarine and shortening production. Vegetable oil is hydrogenated with gaseous H2 in the presence of a metal catalyst (usually nickel catalyst). If the hydrogenation is completely performed, all the double bounds are 19 Figure 3-2-1: Hydrogenation. converted to the saturated ones with the same carbon number. -
Hydrogenation Reaction
SOP: How to Run an Atmospheric-Pressure Hydrogenation Reaction Hazards: Hydrogenation reactions pose a significant fire hazard due to the use of flammable reagents and solvents. Such reagents include palladium on carbon (Pd/C), which is highly flammable and can ignite solvents and hydrogen. It is especially dangerous after having been used for the hydrogenation. The presence of hydrogen gas increases the risk of explosion. Special Precautions: Remove any excess clutter and any flammable solvents that are not needed from your fume hood for the reaction. Be prepared for the possibility of a small fire. Do not panic if this occurs, but simply cover the flask or funnel in which there is a fire with a watch glass and it will go out. Have a suitable sized watch glass on hand. Recommended Apparatus: A three-necked flask equipped with a magnetic stirring bar, a nitrogen inlet adapter connected to a nitrogen/vacuum manifold, a glass stopper or rubber septum, and a gas inlet adapter with a stopcock and a balloon filled with hydrogen. Procedure: 1. Put a weighed quantity of the catalyst in the flask. 2. Evacuate and back-fill the flask with nitrogen 3 times. 3. Add your solvent under a countercurrent of nitrogen. CAUTION: Do not pour your solvent from a 4-liter bottle or a 1-liter bottle. Use a small Erlenmeyer flask (for example 125 mL) containing only the needed amount of solvent. 4. Add your substrate to be hydrogenated to the flask. 5. Evacuate and back-fill the flask with hydrogen. 6. If needed, you may replace the balloon with a full one as needed during the reaction. -
Catalytic Hydrogenation and Dehydrogenation Reactions of N-Alkyl-Bis(Carbazole)-Based Hydrogen Storage Materials
catalysts Article Catalytic Hydrogenation and Dehydrogenation Reactions of N-alkyl-bis(carbazole)-Based Hydrogen Storage Materials Joori Jung 1,2,†, Byeong Soo Shin 3,4,†, Jeong Won Kang 4,5,* and Won-Sik Han 1,* 1 Department of Chemistry, Seoul Women’s University, Seoul 01797, Korea; [email protected] 2 REYON Pharmaceutical, Co., Ltd., Anyang 01459, Korea 3 Hyundai Motor Company, Strategy & Technology Division, Ulwang 16082, Korea; [email protected] 4 Department of Chemical and Biological Engineering, Korea University, Seoul 02841, Korea 5 Graduate School of Energy and Environment, Korea University, Seoul 02841, Korea * Correspondence: [email protected] (J.W.K.); [email protected] (W.-S.H.) † These authors contributed equally. Abstract: Recently, there have been numerous efforts to develop hydrogen-rich organic materials because hydrogen energy is emerging as a renewable energy source. In this regard, we designed and prepared four new materials based on N-alkyl-bis(carbazole), 9,90-(2-methylpropane-1,3-diyl)bis(9H- carbazole) (MBC), 9,90-(2-ethylpropane-1,3-diyl)bis(9H-carbazole) (EBC), 9,90-(2-propylpropane-1,3- diyl)bis(9H-carbazole) (PBC), and 9,90-(2-butylpropane-1,3-diyl)bis(9H-carbazole) (BBC), to investi- gate their hydrogen adsorption/hydrogen desorption reactivity depending on the length of the alkyl chain. The gravimetric densities of MBC, EBC, PBC, and BBC were 5.86, 5.76, 5.49, and 5.31 H2 wt %, respectively, again depending on the alkyl chain length. All materials showed complete hydro- genation reactions under ruthenium on an alumina catalyst at 190 ◦C, and complete reverse reactions ◦ and dehydrogenation reactions were observed under palladium on an alumina catalyst at <280 C. -
Catalytic Hydrogenation Syringe Pump Application Note Using Teledyne Isco Syringe Pumps AN19
Catalytic Hydrogenation Syringe Pump Application Note Using Teledyne Isco Syringe Pumps AN19 Overview Methodology Hydrogenation is a chemical reaction of great impor- Molecular hydrogen does not readily react with tance to the petrochemical and fine chemical industries. organic molecules; a catalyst is always required. A cata- In its most elementary sense, the term hydrogenation lyst is a substance that controls a chemical reaction, but refers to the addition reaction of molecular hydrogen is not consumed or part of the final product. Catalysts with an unsaturated carbon-carbon double bond as work by lowering the activation energy needed for col- illustrated: liding molecules to reach the transition state. Therefore, catalysts can allow reactions to take place that would otherwise not be possible or allow them to happen at a HH HH much faster rate. A comparison of the effect catalysts can have in the + energy required can be seen in Figure 2: CC H2 CC HH energy Figure 1: Typical hydrogen reaction The first compound, called an alkene, is converted into the corresponding alkane. activation In addition to the example above, there are other energy ways in which molecular hydrogen can be reacted with activation other types of molecules. These include the incorpora- energy tion of hydrogen accompanied by cleavage of the starting molecule as in hydrodesulfurization and reac- tions in which the starting molecule undergoes rearrangement such as isomerization. uncatalysed reaction Hydrogenation in Practical Use catalysed reaction time For the petrochemical industry, many of the com- pounds found in crude oil are of little use since they Figure 2: Boltzman Energy Diagram for reaction contain multiple double bonds; they must be first con- pathway verted to saturated compounds before use as commodities such as gasoline. -
Kinetic Study of the Selective Hydrogenation of Acetylene Over Supported Palladium Under Tail-End Conditions
catalysts Article Kinetic Study of the Selective Hydrogenation of Acetylene over Supported Palladium under Tail-End Conditions Caroline Urmès 1,2, Jean-Marc Schweitzer 2, Amandine Cabiac 2 and Yves Schuurman 1,* 1 IRCELYON CNRS, UMR 5256, Univ Lyon, Université Claude Bernard Lyon 1, 2 avenue Albert Einstein, 69626 Villeurbanne Cedex, France; [email protected] 2 IFP Energies nouvelles, Etablissement de Lyon, Rond-point de l’échangeur de Solaize, BP3, 69360 Solaize, France; [email protected] (J.-M.S.); [email protected] (A.C.) * Correspondence: [email protected]; Tel.: +33-472445482 Received: 9 January 2019; Accepted: 31 January 2019; Published: 14 February 2019 Abstract: The kinetics of the selective hydrogenation of acetylene in the presence of an excess of ethylene has been studied over a 0.05 wt. % Pd/α-Al2O3 catalyst. The experimental reaction conditions were chosen to operate under intrinsic kinetic conditions, free from heat and mass transfer limitations. The data could be described adequately by a Langmuir–Hinshelwood rate-equation based on a series of sequential hydrogen additions according to the Horiuti–Polanyi mechanism. The mechanism involves a single active site on which both the conversion of acetylene and ethylene take place. Keywords: power-law; Langmuir–Hinshelwood; kinetic modeling; Pd/α-Al2O3 1. Introduction Ethylene is the largest of the basic chemical building blocks with a global market estimated at more than 140 million tons per year with an increasing growth rate. It is used mainly as precursor for polymers production, for instance polyethylene, vinyl chloride, ethylbenzene, or even ethylene oxide synthesis. -
Reactions of Alkenes and Alkynes
05 Reactions of Alkenes and Alkynes Polyethylene is the most widely used plastic, making up items such as packing foam, plastic bottles, and plastic utensils (top: © Jon Larson/iStockphoto; middle: GNL Media/Digital Vision/Getty Images, Inc.; bottom: © Lakhesis/iStockphoto). Inset: A model of ethylene. KEY QUESTIONS 5.1 What Are the Characteristic Reactions of Alkenes? 5.8 How Can Alkynes Be Reduced to Alkenes and 5.2 What Is a Reaction Mechanism? Alkanes? 5.3 What Are the Mechanisms of Electrophilic Additions HOW TO to Alkenes? 5.1 How to Draw Mechanisms 5.4 What Are Carbocation Rearrangements? 5.5 What Is Hydroboration–Oxidation of an Alkene? CHEMICAL CONNECTIONS 5.6 How Can an Alkene Be Reduced to an Alkane? 5A Catalytic Cracking and the Importance of Alkenes 5.7 How Can an Acetylide Anion Be Used to Create a New Carbon–Carbon Bond? IN THIS CHAPTER, we begin our systematic study of organic reactions and their mecha- nisms. Reaction mechanisms are step-by-step descriptions of how reactions proceed and are one of the most important unifying concepts in organic chemistry. We use the reactions of alkenes as the vehicle to introduce this concept. 129 130 CHAPTER 5 Reactions of Alkenes and Alkynes 5.1 What Are the Characteristic Reactions of Alkenes? The most characteristic reaction of alkenes is addition to the carbon–carbon double bond in such a way that the pi bond is broken and, in its place, sigma bonds are formed to two new atoms or groups of atoms. Several examples of reactions at the carbon–carbon double bond are shown in Table 5.1, along with the descriptive name(s) associated with each. -
Hydrodeoxygenation of Vegetable Oil in a Trickle Bed Reactor for Renewable Diesel Production
International Journal of Technology 11(7) 1292-1299 (2020) Received July 2020 / Revised November 2020 / Accepted December 2020 International Journal of Technology http://ijtech.eng.ui.ac.id Hydrodeoxygenation of Vegetable Oil in a Trickle Bed Reactor for Renewable Diesel Production Yuswan Muharam1*, Jessica Adeline Soedarsono1 1Department of Chemical Engineering, Faculty of Engineering, Universitas Indonesia, Kampus UI Depok, Depok 16424, Indonesia Abstract. The hydrodeoxygenation of vegetable oil in a trickle bed reactor for renewable diesel production was observed in this research. Vegetable oil was represented by triolein. The NiMo/Al2O3 catalyst with a composition of 6.13% w/w Ni, 12.49% w/w Mo, and 81.33% w/w Al2O3 was used. The reactions took place in the temperature range of 272–327.5°C and pressures of 5 and 15 bar. A trickle bed reactor of 2.01 cm in diameter and 24 cm in bed length was able to convert triolein into renewable diesel. C18 hydrocarbons became the dominant reacting compounds at temperatures above 310°C and a pressure of 15 bar, which reached more than 50% w/w. At 5 bar pressure, fatty acids with stearic acid as the acid with the highest concentration were the dominant reacting component, reaching more than 60% w/w at temperatures above 280°C. This led to double bond saturation once the reactants were mixed. Keywords: Hydrodeoxygenation; Renewable diesel; Trickle bed reactor 1. Introduction The Fuel is one of the basic needs for transportation and industry, which mostly comes from petroleum processing (fossil-based). Economic oil reserves are depleting, while energy demand continues to increase with population size and advancing technology. -
Catalytic Glycerol Hydrogenolysis to Produce 1,2-Propanediol with Molecular Hydrogen and in Situ Hydrogen Produced from Steam Reforming
Catalytic Glycerol Hydrogenolysis to Produce 1,2-propanediol with Molecular Hydrogen and in situ Hydrogen Produced from Steam Reforming by Yuanqing Liu A thesis presented to the University of Waterloo in fulfillment of the thesis requirement for the degree of Doctor of Philosophy in Chemical Engineering Waterloo, Ontario, Canada, 2014 ©Yuanqing Liu 2014 AUTHOR'S DECLARATION I hereby declare that I am the sole author of this thesis. This is a true copy of the thesis, including any required final revisions, as accepted by my examiners. I understand that my thesis may be made electronically available to the public. ii Abstract Biodiesel has shown great promise to supplement the fossil diesel since it is a renewable energy resource and is environmentally friendly. However, the major obstacle to biodiesel large scale commercialization is the high production cost; so converting glycerol, the by- product of a biodiesel process, into value-added products is an efficient way to promote biodiesel production. 1,2-propanediol (1,2PD), also known as propylene glycol, is an important commodity chemical used for many applications such as polyester resins, liquid detergents and anti-freeze. It can be produced via dehydration of glycerol into acetol followed by hydrogenation of acetol into 1,2PD using a bi-functional catalyst. Currently high pressure gaseous hydrogen added for hydrogenation causes safety issues as well as additional costs of hydrogen purchasing, transportation and storage. Therefore, the utilization of the in situ hydrogen produced by steam reforming of a hydrogen carrier could be a novel route for this process. In this work, processes of glycerol hydrogenolysis to produce 1,2PD have been developed using different hydrogen sources, i.e. -
Catalytic Hydrogenation, Hydrodeoxygenation, and Hydrocracking Processes of a Lignin Monomer Model Compound Eugenol Over Magneti
catalysts Article Catalytic Hydrogenation, Hydrodeoxygenation, and Hydrocracking Processes of a Lignin Monomer Model Compound Eugenol over Magnetic Ru/C–Fe2O3 and Mechanistic Reaction Microkinetics Ana Bjeli´c 1,2, Miha Grilc 1,* , Sašo Gyergyek 3, Andraž Kocjan 4 , Darko Makovec 3 and Blaž Likozar 1 1 Department of Catalysis and Chemical Reaction Engineering, National Institute of Chemistry, Hajdrihova 19, 1001 Ljubljana, Slovenia; [email protected] (A.B.); [email protected] (B.L.) 2 Faculty of Chemistry and Chemical Technology, University Ljubljana, Veˇcnapot 113, 1001 Ljubljana, Slovenia 3 Department of Synthesis of Materials, Jožef Stefan Institute, Jamova Cesta 39, 1001 Ljubljana, Slovenia; [email protected] (S.G.); [email protected] (D.M.) 4 Department of Nanostructured Materials, Jožef Stefan Institute, Jamova Cesta 39, 1001 Ljubljana, Slovenia; [email protected] * Correspondence: [email protected]; Tel.: +386-1-4760-283 Received: 13 September 2018; Accepted: 25 September 2018; Published: 28 September 2018 Abstract: Conversion of waste lignocellulosic (LC) biomass, a widely-available low-cost feedstock, into value-added biobased chemicals (and biofuels) has been gaining much attention recently. Therefore, the present lignin valorisation study was aimed at developing magnetically-separable highly-active catalysts for hydrodeoxygenation (HDO), also proposing surface chemical kinetics. Five carbonaceous substrate-deposited Ru were synthesised and tested for the HDO of monomer moiety eugenol. Their annealing temperatures differed, specifically between 300 and 750 ◦C, while one was not subjected to calcination. Experiments revealed the substantial influence of annealing temperature on the product distribution. Namely, fresh nonannealed nanocomposites were not active for hydrogenolysis. By further pretreatment increase, hydrogenation and, exclusively, the deoxygenation of saturated cyclic species, were enhanced, these being more promoted considering rates and yields than commercial carbon-supported ruthenium.