When Chemical Reactors Were Admitted and Earlier Roots of Chemical Engineering
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Metallurgical Engineering
ENSURING THE EXPERTISE TO GROW SOUTH AFRICA Discipline-specific Training Guideline for Candidate Engineers in Metallurgical Engineering R-05-MET-PE Revision No.: 2: 25 July 2019 ENGINEERING COUNCIL OF SOUTH AFRICA Tel: 011 6079500 | Fax: 011 6229295 Email: [email protected] | Website: www.ecsa.co.za ENSURING THE Document No.: Effective Date: Revision No.: 2 R-05-MET-PE 25/07/2019 Subject: Discipline-specific Training Guideline for Candidate Engineers in Metallurgical Engineering Compiler: Approving Officer: Next Review Date: Page 2 of 46 MB Mtshali EL Nxumalo 25/07/2023 TABLE OF CONTENTS DEFINITIONS ............................................................................................................................ 3 BACKGROUND ......................................................................................................................... 5 1. PURPOSE OF THIS DOCUMENT ......................................................................................... 5 2. AUDIENCE............................................................................................................................. 6 3. PERSONS NOT REGISTERED AS CANDIDATES OR NOT BEING TRAINED UNDER COMMITMENT AND UNDERTAKING (C&U) ..................................................... 7 4. ORGANISING FRAMEWORK FOR OCCUPATIONS ............................................................. 7 4.1 Extractive Metallurgical Engineering ..................................................................................... 8 4.2 Mineral Processing Engineering .......................................................................................... -
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.................................................. -
The Great War, the Russian Civil War, and the Invention of Big Science
Science in Context 15(2), 239–275 (2002). Copyright © Cambridge University Press DOI: 10.1017/S0269889702000443 Printed in the United Kingdom The Great War, the Russian Civil War, and the Invention of Big Science Alexei Kojevnikov Department of History, University of Georgia, Athens, Georgia. Institute of the History of Science and Technology of the Academy of Sciences, Moscow. E-mail: [email protected] Argument The revolutionary transformation in Russian science toward the Soviet model of research started even before the revolution of 1917. It was triggered by the crisis of World War I, in response to which Russian academics proposed radical changes in the goals and infrastructure of the country’s scientific effort. Their drafts envisioned the recognition of science as a profession separate from teaching, the creation of research institutes, and the turn toward practical, applied research linked to the military and industrial needs of the nation. The political revolution and especially the Bolshevik government that shared or appropriated many of the same views on science, helped these reforms materialize during the subsequent Civil War. By 1921, the foundation of a novel system of research and development became established, which in its most essential characteristics was similar to the U.S. later phenomenon known as “big science.” Those who watched Russian industry perform during the first months of the Great European War could not escape the conclusion that the country’s degree of economic, industrial, and scientific dependence upon Germany was intolerable and bordered on the colonial. This situation should not have been surprising in high technology fields, such as machines and chemicals, where less than 50 per cent of the needed products were manufactured in Russia (Grinevetskiy 1922, 33). -
Process Intensification in the Synthesis of Organic Esters : Kinetics
PROCESS INTENSIFICATION IN THE SYNTHESIS OF ORGANIC ESTERS: KINETICS, SIMULATIONS AND PILOT PLANT EXPERIMENTS By Venkata Krishna Sai Pappu A DISSERTATION Submitted to Michigan State University in partial fulfillment of the requirements for the degree of DOCTOR OF PHILOSOPHY Chemical Engineering 2012 ABSTRACT PROCESS INTENSIFICATION IN THE SYNTHESIS OF ORGANIC ESTERS: KINETICS, SIMULATIONS AND PILOT PLANT EXPERIMENTS By Venkata Krishna Sai Pappu Organic esters are commercially important bulk chemicals used in a gamut of industrial applications. Traditional routes for the synthesis of esters are energy intensive, involving repeated steps of reaction typically followed by distillation, signifying the need for process intensification (PI). This study focuses on the evaluation of PI concepts such as reactive distillation (RD) and distillation with external side reactors in the production of organic acid ester via esterification or transesterification reactions catalyzed by solid acid catalysts. Integration of reaction and separation in one column using RD is a classic example of PI in chemical process development. Indirect hydration of cyclohexene to produce cyclohexanol via esterification with acetic acid was chosen to demonstrate the benefits of applying PI principles in RD. In this work, chemical equilibrium and reaction kinetics were measured using batch reactors for Amberlyst 70 catalyzed esterification of acetic acid with cyclohexene to give cyclohexyl acetate. A kinetic model that can be used in modeling reactive distillation processes was developed. The kinetic equations are written in terms of activities, with activity coefficients calculated using the NRTL model. Heat of reaction obtained from experiments is compared to predicted heat which is calculated using standard thermodynamic data. The effect of cyclohexene dimerization and initial water concentration on the activity of heterogeneous catalyst is also discussed. -
Chemical Process Modeling in Modelica
Chemical Process Modeling in Modelica Ali Baharev Arnold Neumaier Fakultät für Mathematik, Universität Wien Nordbergstraße 15, A-1090 Wien, Austria Abstract model creation involves only high-level operations on a GUI; low-level coding is not required. This is the Chemical process models are highly structured. Infor- desired way of input. Not surprisingly, this is also mation on how the hierarchical components are con- how it is implemented in commercial chemical process nected helps to solve the model efficiently. Our ulti- simulators such as Aspen PlusR , Aspen HYSYSR or mate goal is to develop structure-driven optimization CHEMCAD R . methods for solving nonlinear programming problems Nonlinear system of equations are generally solved (NLP). The structural information retrieved from the using optimization techniques. AMPL (FOURER et al. JModelica environment will play an important role in [12]) is the de facto standard for model representation the development of our novel optimization methods. and exchange in the optimization community. Many Foundations of a Modelica library for general-purpose solvers for solving nonlinear programming (NLP) chemical process modeling have been built. Multi- problems are interfaced with the AMPL environment. ple steady-states in ideal two-product distillation were We are aiming to create a ‘Modelica to AMPL’ con- computed as a proof of concept. The Modelica source verter. One could use the Modelica toolchain to create code is available at the project homepage. The issues the models conveniently on a GUI. After exporting the encountered during modeling may be valuable to the Modelica model in AMPL format, the already existing Modelica language designers. software environments (solvers with AMPL interface, Keywords: separation, distillation column, tearing AMPL scripts) can be used. -
The Role of Nanotechnology in Chemical Substitution
EUROPEAN PARLIAMENT Scientific Technology Options Assessment S T O A The role of Nanotechnology in Chemical Substitution STUDY IPOL/A/STOA/ST/2006-029 PE 383.212 This project was commissioned by STOA under Framework Contract IP/A/STOA/FWC/2005-28). The associated workshop, "The Role of Nanotechnology in Chemical Substitution" was organised by the European Parliament in Brussels on 13 September 2006. Only published in English. Authors: ETAG European Technology Assessment Group Institute for Technology Assessment and Systems Analysis (ITAS), Karlsruhe Danish Board of Technology (DBT), Copenhagen Flemish Institute for Science and Technology Assessment (viWTA), Brussels Parliamentary Office of Science and Technology (POST), London Rathenau Institute, The Hague Dr. Ulrich Fiedeler, ITAS E-mail: [email protected] Administrator: Mr. Miklos Györffi Policy Department A: Economic and Scientific Policy DG Internal Policies European Parliament Rue Wiertz 60 - ATR 00K076 B-1047 Brussels Tel: +32 (0)2 283 25 05 Fax: +32 (0)2 284 49 84 E-mail: [email protected] Manuscript completed in April 2007. The opinions expressed in this document do not necessarily represent the official position of the European Parliament. Reproduction and translation for non-commercial purposes are authorised provided the source is acknowledged and the publisher is given prior notice and receives a copy. E-mail: poldep- [email protected]. IP/A/STOA/ST/2006-029 PE 383.212 TABLE OF CONTENTS 1 EXECUTIVE SUMMARY..............................................................................................................ii -
Chemical Engineering Curriculum
CHEMICAL ENGINEERING CURRICULUM Fall Term Spring Term First Year EGGG 101 Introduction to Engineering (FYE) 2 CHEG 112 Introduction to Chemical Engineering 3 CHEM 111 General Chemistry 3 CHEM 112 General Chemistry 3 MATH 242 Analytic Geometry & Calculus B 4 MATH 243 Analytic Geometry & Calculus C 4 CISC 106 General Computer Science for Engineers 3 PHYS 207 Fundamentals of Physics I 4 ENGL 110 Critical Reading and Writing 3 Breadth Requirement Elective 1 3 15 17 Second Year CHEG 231 Chemical Engineering Thermodynamics 3 CHEG 325 Chemical Engineering Thermodynamics 3 CHEM 220 Quantitative Analysis 3 CHEG 304 Random Variability in Chemical Processes 3 CHEM 221 Quantitative Analysis Laboratory 1 CHEM 444 Physical Chemistry 3 PHYS 208 Fundamentals of Physics II 4 CHEM 445 Physical Chemistry Laboratory ( a ) 0/1 MSEG 302 Materials Science for Engineers 3 MATH 305 Applied Math for Chemical Engineering 3 Breadth Requirement Elective 2 3 Breadth Requirement Elective 3 3 17 15/16 Third Year CHEG 332 Chemical Engineering Kinetics 3 CHEG 342 Heat and Mass Transfer 3 CHEG 341 Fluid Mechanics 3 CHEG 345 Chemical Engineering Laboratory I 3 CHEM 331 Organic Chemistry I 3 CHEM 332 Organic Chemistry ( b ) or 3 CHEM 333 Organic Chemistry Laboratory 1/2 CHEM 527 Introduction to Biochemistry Technical Elective 1 3 Breadth Requirement Elective 4 3 Technical Elective 2 3 CHEG Elective 1 3 16/17 15 Fourth Year CHEG 431 Chemical Process Design 1 3 CHEG 432 Chemical Process Design 2 (DLE) 3 CHEG 401 Chemical Process Dynamics and Control 3 CHEG Elective 3 3 CHEG 445 Chemical Engineering Laboratory II 3 Technical Elective 3 3 CHEG Elective 2 3 Technical Elective 4 or CHEG Elective 4 3 Breadth Requirement Elective 5 3 Breadth Requirement Elective 6 3 15 15 Total Credit Hours 126 ( a ) If CHEM 333 is taken for two credits, CHEM 445 is not required. -
Chemical Process Modeling in Modelica
Chemical Process Modeling in Modelica Ali Baharev Arnold Neumaier Fakultät für Mathematik, Universität Wien Nordbergstraße 15, A-1090 Wien, Austria Abstract model creation involves only high-level operations on a GUI; low-level coding is not required. This is the Chemical process models are highly structured. Infor- desired way of input. Not surprisingly, this is also mation on how the hierarchical components are con- how it is implemented in commercial chemical process nected helps to solve the model efficiently. Our ulti- simulators such as Aspen PlusR , Aspen HYSYSR or mate goal is to develop structure-driven optimization CHEMCAD R . methods for solving nonlinear programming problems Nonlinear system of equations are generally solved (NLP). The structural information retrieved from the using optimization techniques. AMPL (FOURER et al. JModelica environment will play an important role in [12]) is the de facto standard for model representation the development of our novel optimization methods. and exchange in the optimization community. Many Foundations of a Modelica library for general-purpose solvers for solving nonlinear programming (NLP) chemical process modeling have been built. Multi- problems are interfaced with the AMPL environment. ple steady-states in ideal two-product distillation were We are aiming to create a ‘Modelica to AMPL’ con- computed as a proof of concept. The Modelica source verter. One could use the Modelica toolchain to create code is available at the project homepage. The issues the models conveniently on a GUI. After exporting the encountered during modeling may be valuable to the Modelica model in AMPL format, the already existing Modelica language designers. software environments (solvers with AMPL interface, Keywords: separation, distillation column, tearing AMPL scripts) can be used. -
Taking Reactive Distillation to the Next Level of Process Intensification, Chemical Engineering Transactions, 69, 553-558 DOI: 10.3303/CET1869093 554
553 A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 69, 2018 The Italian Association of Chemical Engineering Online at www.aidic.it/cet Guest Editors: Elisabetta Brunazzi, Eva Sorensen Copyright © 2018, AIDIC Servizi S.r.l. ISBN 978-88-95608-66-2; ISSN 2283-9216 DOI: 10.3303/CET1869093 Taking Reactive Distillation to the Next Level of Process Intensification Anton A. Kissa,b,*, Megan Jobsona a The University of Manchester, School of Chemical Engineering and Analytical Science, Centre for Process Integration, Sackville Street, The Mill, Manchester M13 9PL, United Kingdom b University of Twente, Sustainable Process Technology, PO Box 217, 7500 AE Enschede, The Netherlands [email protected] Reactive distillation (RD) is an efficient process intensification technique that integrates catalytic chemical reaction and distillation in a single apparatus. The process is also known as catalytic distillation when a solid catalyst is used. RD technology has many key advantages such as reduced capital investment and significant energy savings, as it can surpass equilibrium limitations, simplify complex processes, increase product selectivity and improve the separation efficiency. But RD is also constrained by thermodynamic requirements (related to volatility differences and heat of reaction), overlapping of the reaction and distillation operating conditions, and the availability of catalysts that are active, selective and with sufficient longevity. This paper is the first to provide insights into novel reactive distillation technologies that combine RD principles with other intensified distillation technologies – e.g. dividing-wall columns, cyclic distillation, HiGee distillation, and heat integrated distillation column – potentially leading to new processes and applications. 1. Introduction Reactive distillation (RD) is one of the best success stories of process intensification technology – developed since the early 1920s – that made a strong positive impact in the chemical process industry (CPI). -
“…I Want to Have Freedom of Research; Otherwise, I Will Be Limited in My Work”
A Good Journal for Inquisitive People Th ere is no room 1 (48) scfh.ru/en/ in ancient history 1 2018 so far for the army of stone horsemen pertifi ed SCIENCE on the slopes First Hand of the Pir Panjal THE LIFE mountain range, OF A CHEMIST Himalayas № 1 (48) 2018 RIDERS LOST IN THE HIMALAYAS SELECTION In June 2017, this was the site OF THE BEST of a Russian-Indian FRIEND archaeological expedition launched to find and describe stone horses, enigmatic statues “…I want to have A GARDEN BORN lost in these remote areas BY INSPIRATION of the western Lesser Himalayas freedom of research; otherwise, I will be limited in my work” 9 772310 3000024 78 2018 1. popular science journal IN THIS ISSUE: Vladimir Ipatieff, the inventor of technology for the production of polyethylene and high-octane gasoline, was called in 1937 the Man of the Year in the USA and deprived of academic title and citizenship in the USSR There is no room in ancient history so far for the army of stone horsemen pertified on the slopes of the Pir Panjal mountain range, Himalayas The publisher of Science will donate several thousand copies of the book about the Siberian experiment on fox domestication as a gift to the American schools Meditation prevents the shortening of the telomeres which protect the chromosomes from damage during cell division Even a trivial dandelion from the Bonsai Park has an extraordinary story to tell: the creator of this living collection found it at the other end of the world – up in the Andes! A Journal for Inquisitive People “The natural desire Editorial -
CHEMICAL REACTION ENGINEERING* Current Status and Future Directions
[eJij9iviews and opinions CHEMICAL REACTION ENGINEERING* Current Status and Future Directions M. P. DUDUKOVIC and petrochemical industry provided a fertile ground Washington University for further development of reaction engineering con St. Louis, MO 63130 cepts. The final cornerstone of this new discipline was laid in 1957 by the First Symposium on Chemical HEMICAL REACTIONS have been used by man Reaction Engineering [3] which brought together and C kind since time immemorial to produce useful synthesized the European point of view. The Amer products such as wine, metals, etc. Nevertheless, the ican and European schools of thought were not identi unifying principles that today we call chemical reac cal, but in time they converged into the subject matter tion engineering were not developed until relatively a that we know today as chemical reaction engineering, short time ago. During the decade of the 1940's (not or CRE. The above chronology led to the establish even half a century ago!) a transition was made from ment of CRE as an accepted discipline over the span descriptive industrial chemistry to the conceptual un of a decade and a half. This does not imply that all the ification of reaction processes and reactor types. The principles important in CRE were discovered then. pioneering work in this area of industrial practice was The foundation for CRE had already been established done by Denbigh [1] in England. Then in 1947, by the early work of Frank-Kamenteski, Damkohler, Hougen and Watson [2] published the first textbook Zeldovitch, etc., but at that time they represented in the U.S. -
Development of a Pedagogical Model to Help Engineering Faculty Design Interdisciplinary Curricula
International Journal of Teaching and Learning in Higher Education 2016, Volume 28, Number 3, 372-384 http://www.isetl.org/ijtlhe/ ISSN 1812-9129 Development of a Pedagogical Model to Help Engineering Faculty Design Interdisciplinary Curricula Maria Navarro, Timothy Foutz, Kerri Patrick Singer and Sidney Thompson Ray International Group University of Georgia The purpose of this study was to develop a model to help engineering faculty overcome the challenges they face when asked to design and implement interdisciplinary curricula. Researchers at a U.S. University worked with an Interdisciplinary Consultant Team and prepared a steering document with Guiding Principles and Essential Elements for the design, implementation, and evaluation of integrative curricula in engineering education. The team also developed exemplar materials (Integrative Learning Module) to provide a practical example and demonstrate how the tools provided could be used in the development of new curricula. The Guiding Principles, Essential Elements, and Integrative Learning Module were evaluated by faculty and students who provided feedback for their improvement. Faculty indicated that the tools provided were appropriate guidelines for faculty, but they indicated that the Integrative Learning Module was too long to be a manageable example. Students agreed about the need for more interactive, real-world applications of engineering concepts, but they expressed differences of opinion regarding how humanities and social sciences topics should be addressed in the engineering curriculum. Students who participated in a course modeling the Integrative Learning Module were satisfied with its use and learning outcomes. After the course, these students were able to explain the importance of problem definition, process, and disciplinary integration in engineering work.