Dehydrogenation by Heterogeneous Catalysts
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De Novo Biosynthesis of Terminal Alkyne-Labeled Natural Products
De novo biosynthesis of terminal alkyne-labeled natural products Xuejun Zhu1,2, Joyce Liu2,3, Wenjun Zhang1,2,4* 1Department of Chemical and Biomolecular Engineering, 2Energy Biosciences Institute, 3Department of Bioengineering, University of California, Berkeley, CA 94720, USA. 4Physical Biosciences Division, Lawrence Berkeley National Laboratory, Berkeley, CA 94720, USA. *e-mail:[email protected] 1 Abstract: The terminal alkyne is a functionality widely used in organic synthesis, pharmaceutical science, material science, and bioorthogonal chemistry. This functionality is also found in acetylenic natural products, but the underlying biosynthetic pathways for its formation are not well understood. Here we report the characterization of the first carrier protein- dependent terminal alkyne biosynthetic machinery in microbes. We further demonstrate that this enzymatic machinery can be exploited for the in situ generation and incorporation of terminal alkynes into two natural product scaffolds in E. coli. These results highlight the prospect for tagging major classes of natural products, including polyketides and polyketide/non-ribosomal peptide hybrids, using biosynthetic pathway engineering. 2 Natural products are important small molecules widely used as drugs, pesticides, herbicides, and biological probes. Tagging natural products with a unique chemical handle enables the visualization, enrichment, quantification, and mode of action study of natural products through bioorthogonal chemistry1-4. One prevalent bioorthogonal reaction is -
Opportunities for Catalysis in the 21St Century
Opportunities for Catalysis in The 21st Century A Report from the Basic Energy Sciences Advisory Committee BASIC ENERGY SCIENCES ADVISORY COMMITTEE SUBPANEL WORKSHOP REPORT Opportunities for Catalysis in the 21st Century May 14-16, 2002 Workshop Chair Professor J. M. White University of Texas Writing Group Chair Professor John Bercaw California Institute of Technology This page is intentionally left blank. Contents Executive Summary........................................................................................... v A Grand Challenge....................................................................................................... v The Present Opportunity .............................................................................................. v The Importance of Catalysis Science to DOE.............................................................. vi A Recommendation for Increased Federal Investment in Catalysis Research............. vi I. Introduction................................................................................................ 1 A. Background, Structure, and Organization of the Workshop .................................. 1 B. Recent Advances in Experimental and Theoretical Methods ................................ 1 C. The Grand Challenge ............................................................................................. 2 D. Enabling Approaches for Progress in Catalysis ..................................................... 3 E. Consensus Observations and Recommendations.................................................. -
1 Refinery and Petrochemical Processes
3 1 Refinery and Petrochemical Processes 1.1 Introduction The combination of high demand for electric cars and higher automobile engine effi- ciency in the future will mean less conversion of petroleum into fuels. However, the demand for petrochemicals is forecast to rise due to the increase in world popula- tion. With this, it is expected that modern and more innovative technologies will be developed to serve the growth of the petrochemical market. In a refinery process, petroleum is converted into petroleum intermediate prod- ucts, including gases, light/heavy naphtha, kerosene, diesel, light gas oil, heavy gas oil, and residue. From these intermediate refinery product streams, several fuels such as fuel gas, liquefied petroleum gas, gasoline, jet fuel, kerosene, auto diesel, and other heavy products such as lubricants, bunker oil, asphalt, and coke are obtained. In addition, these petroleum intermediates can be further processed and separated into products for petrochemical applications. In this chapter, petroleum will be introduced first. Petrochemicals will be intro- duced in the second part of the chapter. Petrochemicals – the main subject of this book – will address three major areas, (i) the production of the seven cornerstone petrochemicals: methane and synthesis gas, ethylene, propylene, butene, benzene, toluene, and xylenes; (ii) the uses of the seven cornerstone petrochemicals, and (iii) the technology to separate petrochemicals into individual components. 1.2 Petroleum Petroleum is derived from the Latin words “petra” and “oleum,” which means “rock” and “oil,” respectively. Petroleum also is known as crude oil or fossil fuel. It is a thick, flammable, yellow-to-black mixture of gaseous, liquid, and solid hydrocarbons formed from the remains of plants and animals. -
Production of Pure Hydrogen by Ethanol Dehydrogenation Abstract
The Future Role of Hydrogen in Petrochemistry and Energy Supply DGMK Conference October 4-6, 2010, Berlin, Germany Production of Pure Hydrogen by Ethanol Dehydrogenation E. Santacesaria, G. Carotenuto, R. Tesser, M. Di Serio University of Naples “Federico II”, Department of Chemistry, Naples, Italy Abstract Hydrogen production from bio-ethanol is one of the most promising renewable processes to generate electricity using fuel cells. In this work, we have studied the production of pure hydrogen as by product of ethanol dehydrogenation reaction. This reaction is promoted by copper based catalysts and according to the catalyst used and the operative conditions gives place to acetaldehyde or ethyl acetate as main products. We studied in particular the performance of a commercial copper/copper chromite catalyst, supported on alumina and containing barium chromate as promoter that has given the best results. By operating at low pressure and temperature with short residence times, acetaldehyde is more selectively produced, while, by increasing the pressure (10-30 bars), the temperature (200-260°C) and the residence time (about 100 (grams hour/mol) of ethanol contact time) the selectivity is shifted to the production of ethyl acetate. However, in both cases pure hydrogen is obtained, as by product, that can easily be separated. Hydrogen obtained in this way is exempt of CO and can be directly fed to fuel cells without any inconvenience. In this work, runs performed in different operative conditions have been reported with the scope to individuate the best conditions. A carrier of H2 6% in N2 has been used. The studied catalyst has also shown a good thermal stability with respect to sintering phenomena, that generally occurs during the -1 -1 dehydrogenation on other copper catalysts. -
Sustainable Catalysis
Green Process Synth 2016; 5: 231–232 Book review Sustainable catalysis DOI 10.1515/gps-2016-0016 Sustainable catalysis provides an excellent in-depth over- view of the applications of non-endangered elements in Michael North (Ed.) all aspects of catalysis from heterogeneous to homogene- Sustainable catalysis: with non-endangered metals ous, from catalyst supports to ligands. The Royal Society of Chemistry, 2015 Four volumes of the book series are divided into RSC Green Chemistry series nos. 38–41 two sub-topics devoted to (i) metal-based catalysts and Part 1 (ii) catalysts without metals or other endangered ele- Print ISBN: 978-1-78262-638-1 ments. Each sub-topic comprises of two books due to the PDF eISBN: 978-1-78262-211-6 detailed analysis of catalytic applications described. All Part 2 chapters are written by the world-leading researchers in Print ISBN: 978-1-78262-639-8 the area; however, covering far beyond the scope of their PDF eISBN: 978-1-78262-642-8 immediate research interests, which makes the book par- ticularly valuable for a wide range of readers. Sustainable catalysis: without metals or other Sustainable catalysis: with non-endangered metals endangered elements begins with a very brief chapter which describes the Part 1 concept of elemental sustainability, overviewing the Print ISBN: 978-1-78262-640-4 abundance of the critical elements and perspectives on PDF eISBN: 978-1-78262-209-3 sustainable catalysts. The chapters follow the groups of EPUB eISBN: 978-1-78262-752-4 the periodic table from left to right, from alkaline metals to Part 2 lead spanning 22 chapters. -
The Pennsylvania State University
The Pennsylvania State University The Graduate School Energy and Geo-environmental Engineering ROLES OF ZEOLITE SUPPORT AND NOBLE METAL IN SULFUR-TOLERANT CATALYST FOR LOW TEMPERATURE HYDROGENATION OF AROMATICS A Dissertation in Energy and Geo-environmental Engineering by Hyun Jae Kim 2011 Hyun Jae Kim Submitted in Partial Fulfillment of the Requirements for the Degree of Doctor of Philosophy August 2011 The dissertation of Hyun Jae Kim was reviewed and approved* by the following: Chunshan Song Distinguished Professor of Fuel Science and Professor of Chemical Engineering Dissertation Advisor Chair of Committee Yaw D. Yeboah Professor of Energy and Mineral Engineering Department Head of Energy and Mineral Engineering Yongsheng Chen Assistant Professor of Energy and Mineral Engineering Adri van Duin Associate Professor of Mechanical Engineering *Signatures are on file in the Graduate School iii ABSTRACT This dissertation focuses on fundamental understanding of the roles of supports and noble metals in the sulfur-tolerant catalysts for low-temperature hydrogenation of aromatics in the presence of sulfur. Emphasis was placed on investigating the effect of supports and supported metals for high sulfur tolerance and verifying a catalyst design concept for the sulfur-tolerant noble metal catalyst based on shape selective exclusion of sulfur and hydrogen spillover for low- temperature hydrogenation of aromatics [C.S. Song, Chemtech, 29 (1999) 26-30]. The effect of supports was explored for sulfur tolerance of the supported Pd catalyst on tetralin hydrogenation in the presence of benzothiophene by varying the Pd catalysts on different supports (mordenite, zeolite Y, zeolite A, amorphous silica-alumina). The pore structures and pore sizes were both found to be the important factors in determining the catalytic activity of sulfur-tolerant metal catalyst. -
The Early History of Catalysis
The Early History of Catalysis By Professor A. J. B. Robertson Department of Chemistry, King’s College, London One hundred and forty years ago it was Berzelius proceeded to propose the exist- possible for one man to prepare an annual ence of a new force which he called the report on the progress of the whole of “catalytic force” and he called “catalysis” the chemistry, and for many years this task was decomposition of bodies by this force. This undertaken by the noted Swedish chemist is probably the first recognition of catalysis J. J. Berzelius for the Stockholm Academy of as a wide-ranging natural phenomenon. Sciences. In his report submitted in 1835 and Metallic catalysts had in fact been used in published in 1836 Berzelius reviewed a num- the laboratory before 1800 by Joseph Priestley, ber of earlier findings on chemical change in the discoverer of oxygen, and by the Dutch both homogeneous and heterogeneous sys- chemist Martinus van Marum, both of whom tems, and showed that these findings could be made observations on the dehydrogenation of rationally co-ordinated by the introduction alcohol on metal catalysts. However, it seems of the concept of catalysis. In a short paper likely that these investigators regarded the summarising his ideas on catalysis as a new metal merely as a source of heat. In 1813, force, he wrote (I): Louis Jacques Thenard discovered that ammonia is decomposed into nitrogen and “It is, then, proved that several simple or compound bodies, soluble and insoluble, have hydrogen when passed over various red-hot the property of exercising on other bodies an metals, and ten years later, with Pierre action very different from chemical affinity. -
Physical Organic Chemistry
CHM 8304 Physical Organic Chemistry Catalysis Outline: General principles of catalysis • see section 9.1 of A&D – principles of catalysis – differential bonding 2 Catalysis 1 CHM 8304 General principles • a catalyst accelerates a reaction without being consumed • the rate of catalysis is given by the turnover number • a reaction may alternatively be “promoted” (accelerated, rather than catalysed) by an additive that is consumed • a heterogeneous catalyst is not dissolved in solution; catalysis typically takes place on its surface • a homogeneous catalyst is dissolved in solution, where catalysis takes place • all catalysis is due to a decrease in the activation barrier, ΔG‡ 3 Catalysts • efficient at low concentrations -5 -4 -5 – e.g. [Enz]cell << 10 M; [Substrates]cell < 10 - 10 M • not consumed during the reaction – e.g. each enzyme molecule can catalyse the transformation of 20 - 36 x 106 molecules of substrate per minute • do not affect the equilibrium of reversible chemical reactions – only accelerate the rate of approach to equilibrium end point • most chemical catalysts operate in extreme reaction conditions while enzymes generally operate under mild conditions (10° - 50 °C, neutral pH) • enzymes are specific to a reaction and to substrates; chemical catalysts are far less selective 4 Catalysis 2 CHM 8304 Catalysis and free energy • catalysis accelerates a reaction by stabilising a TS relative to the ground state ‡ – free energy of activation, ΔG , decreases – rate constant, k, increases • catalysis does not affect the end point -
Process Technologies and Projects for Biolpg
energies Review Process Technologies and Projects for BioLPG Eric Johnson Atlantic Consulting, 8136 Gattikon, Switzerland; [email protected]; Tel.: +41-44-772-1079 Received: 8 December 2018; Accepted: 9 January 2019; Published: 15 January 2019 Abstract: Liquified petroleum gas (LPG)—currently consumed at some 300 million tonnes per year—consists of propane, butane, or a mixture of the two. Most of the world’s LPG is fossil, but recently, BioLPG has been commercialized as well. This paper reviews all possible synthesis routes to BioLPG: conventional chemical processes, biological processes, advanced chemical processes, and other. Processes are described, and projects are documented as of early 2018. The paper was compiled through an extensive literature review and a series of interviews with participants and stakeholders. Only one process is already commercial: hydrotreatment of bio-oils. Another, fermentation of sugars, has reached demonstration scale. The process with the largest potential for volume is gaseous conversion and synthesis of two feedstocks, cellulosics or organic wastes. In most cases, BioLPG is produced as a byproduct, i.e., a minor output of a multi-product process. BioLPG’s proportion of output varies according to detailed process design: for example, the advanced chemical processes can produce BioLPG at anywhere from 0–10% of output. All these processes and projects will be of interest to researchers, developers and LPG producers/marketers. Keywords: Liquified petroleum gas (LPG); BioLPG; biofuels; process technologies; alternative fuels 1. Introduction Liquified petroleum gas (LPG) is a major fuel for heating and transport, with a current global market of around 300 million tonnes per year. -
Concepts and Tools for Mechanism and Selectivity Analysis in Synthetic Organic Electrochemistry
Concepts and tools for mechanism and selectivity analysis in synthetic organic electrochemistry Cyrille Costentina,1,2 and Jean-Michel Savéanta,1 aUniversité Paris Diderot, Sorbonne Paris Cité, Laboratoire d’Electrochimie Moléculaire, Unité Mixte de Recherche Université–CNRS 7591, 75205 Paris Cedex 13, France Contributed by Jean-Michel Savéant, April 2, 2019 (sent for review March 19, 2019; reviewed by Robert Francke and R. Daniel Little) As an accompaniment to the current renaissance of synthetic organic sufficient to record a current-potential response but small electrochemistry, the heterogeneous and space-dependent nature of enough to leave the substrates and cosubstrates (of the order of electrochemical reactions is analyzed in detail. The reactions that follow one part per million) almost untouched. Competition of the the initial electron transfer step and yield the products are intimately electrochemical/chemical events with diffusional transport under coupled with reactant transport. Depiction of the ensuing reactions precisely mastered conditions allows analysis of the kinetics profiles is the key to the mechanism and selectivity parameters. within extended time windows (from minutes to submicroseconds). Analysis is eased by the steady state resulting from coupling of However, for irreversible processes, these approaches are blind on diffusion with convection forced by solution stirring or circulation. reaction bifurcations occurring beyond the kinetically determining Homogeneous molecular catalysis of organic electrochemical reactions step, which are precisely those governing the selectivity of the re- of the redox or chemical type may be treated in the same manner. The same benchmarking procedures recently developed for the activation action. This is not the case of preparative-scale electrolysis accom- of small molecules in the context of modern energy challenges lead to panied by identification and quantitation of products. -
Thermal Conductivity Correlations for Minor Constituent Fluids in Natural
Fluid Phase Equilibria 227 (2005) 47–55 Thermal conductivity correlations for minor constituent fluids in natural gas: n-octane, n-nonane and n-decaneଝ M.L. Huber∗, R.A. Perkins Physical and Chemical Properties Division, National Institute of Standards and Technology, Boulder, CO 80305, USA Received 21 July 2004; received in revised form 29 October 2004; accepted 29 October 2004 Abstract Natural gas, although predominantly comprised of methane, often contains small amounts of heavier hydrocarbons that contribute to its thermodynamic and transport properties. In this manuscript, we review the current literature and present new correlations for the thermal conductivity of the pure fluids n-octane, n-nonane, and n-decane that are valid over a wide range of fluid states, from the dilute-gas to the dense liquid, and include an enhancement in the critical region. The new correlations represent the thermal conductivity to within the uncertainty of the best experimental data and will be useful for researchers working on thermal conductivity models for natural gas and other hydrocarbon mixtures. © 2004 Elsevier B.V. All rights reserved. Keywords: Alkanes; Decane; Natural gas constituents; Nonane; Octane; Thermal conductivity 1. Introduction 2. Thermal conductivity correlation Natural gas is a mixture of many components. Wide- We represent the thermal conductivity λ of a pure fluid as ranging correlations for the thermal conductivity of the lower a sum of three contributions: alkanes, such as methane, ethane, propane, butane and isobu- λ ρ, T = λ T + λ ρ, T + λ ρ, T tane, have already been developed and are available in the lit- ( ) 0( ) r( ) c( ) (1) erature [1–6]. -
Measurements of Higher Alkanes Using NO Chemical Ionization in PTR-Tof-MS
Atmos. Chem. Phys., 20, 14123–14138, 2020 https://doi.org/10.5194/acp-20-14123-2020 © Author(s) 2020. This work is distributed under the Creative Commons Attribution 4.0 License. Measurements of higher alkanes using NOC chemical ionization in PTR-ToF-MS: important contributions of higher alkanes to secondary organic aerosols in China Chaomin Wang1,2, Bin Yuan1,2, Caihong Wu1,2, Sihang Wang1,2, Jipeng Qi1,2, Baolin Wang3, Zelong Wang1,2, Weiwei Hu4, Wei Chen4, Chenshuo Ye5, Wenjie Wang5, Yele Sun6, Chen Wang3, Shan Huang1,2, Wei Song4, Xinming Wang4, Suxia Yang1,2, Shenyang Zhang1,2, Wanyun Xu7, Nan Ma1,2, Zhanyi Zhang1,2, Bin Jiang1,2, Hang Su8, Yafang Cheng8, Xuemei Wang1,2, and Min Shao1,2 1Institute for Environmental and Climate Research, Jinan University, 511443 Guangzhou, China 2Guangdong-Hongkong-Macau Joint Laboratory of Collaborative Innovation for Environmental Quality, 511443 Guangzhou, China 3School of Environmental Science and Engineering, Qilu University of Technology (Shandong Academy of Sciences), 250353 Jinan, China 4State Key Laboratory of Organic Geochemistry and Guangdong Key Laboratory of Environmental Protection and Resources Utilization, Guangzhou Institute of Geochemistry, Chinese Academy of Sciences, 510640 Guangzhou, China 5State Joint Key Laboratory of Environmental Simulation and Pollution Control, College of Environmental Sciences and Engineering, Peking University, 100871 Beijing, China 6State Key Laboratory of Atmospheric Boundary Physics and Atmospheric Chemistry, Institute of Atmospheric Physics, Chinese