Methanol Dehydration for Dimethyl Ether. Production for Transportation

Slides:



Advertisements
Similar presentations
Mathieu Lucquiaud, Hannah Chalmers, Jon Gibbins
Advertisements

A First-year Introduction to Life Cycle Analysis Stephanie FarrellRowan University Eduardo CavanaghGlassboro, NJ USA Mariano Savelski.
Module 2: Production and Manufacturing. 2 Objective Upon the successful completion of this module, participants will be able to describe the process involved.
From Fryer to Fuel Tank rinnova Renewable Energy.
AN-NAJAH NATIONAL UNIVERSITY FACULTY OF ENGINEERING DEPARTMENT OF MECHANICAL ENGINEERING Prepared by: Wajdi abu-muhsen Khaled aamer Ahmad Al-Hunate Nabeel.
Life Cycle Inventory of Methyl Methacrylate Yong Li, Evan Griffing, Celia Ponder, Michael Overcash Department of Chemical & Biomolecular Engineering North.
Capture of Heat Energy From Diesel Engine After Cooler Circuit (2006 Annual Report) Mark Teitzel Alaska Village Energy Corporation
Liquid-Phase Methanol Process (LPMeOH) Jill DeTroye, Brandon Hurn, Kyle Ludwig, and Isaac Zaydens.
Direct manufacture from methane (natural gas) without syn-gas, chemical recycling of carbon dioxide of industrial exhausts and eventually.
Hydrogen Fuel Cell Technology and Its Environmental Benefits Wendy Estela PACE university school of law November 29, 2001.
Method of Apparatus for making Biofuel July 1st 2009 Eco Energy International Co., Ltd. Yokohama Japan.
Tennesse Technological University
Chemical Engineering Department
From Left: Joshua Harbert, Christian Ocier, Mitch Kenyon, Fred Thielke, Adebo Alao Calvin College.
Hydrogen from Renewable Fuels by Autothermal Reforming: Alcohols, Carbohydrates, and Biodiesel Lanny D. Schmidt Department of Chemical Engineering and.
1 Hydrogen Economy Ryan Morrison ChE /20/2006 Methanol Economy vs.
New Frontiers in Biofuel Production Fernando Robelo Daniel Bowser.
1 Department of Chemical Engineering Faculty of Engineering, Chulalongkorn University Bangkok 10330, Thailand Plantwide control structure design for an.
Economic Analysis Introduction Motivation Process Flow Diagram Design Basis/Block Flow Diagram Environmental Analysis We have taken advantage of the arbitrage.
DIMETHYL ETHER- AN ALTERNATIVE FUEL INTRODUCTION World present oil resources may be wiped out in 42 years World present oil resources may be wiped out.
BALIKESİR ETHANOL PLANT
1. Introduction Basis of Design Process Structure Process Flow Diagram Equipment Design Process Control Waste, Environment, Safety Economy Conclusion.
AIR POLLUTION PREVENTION AND CONTROL
Desulphurisation Hemant Pandit, Ranjan agrawal. DTU Chemical Engineering Technical University of Denmark The wet FGD process CaCO 3 (s) + SO 2 (g) + 2H.
Breaking Bad Fuel: Biodiesel as an alternative energy source.
Senior Design Project Chapter 22. Project Overview –Feed Pre- conditioners –Reactor(s) –Separator(s) –Product Conditioners –Recycle –Heat Integration.
FISCHER-TROPSCH LIQUIDS REFINING PLANT Team Foxtrot Presentation #5 – April 23, 2013 Mentor: Dan Rusinak, PE Team: Mudassir Ali Stephen Drake Kevin Meaux.
Friction Factors, Pumping and You Understanding how friction affects your bottom line.
Khalid Aldhahri Omar Alrajeh Daniel Marken Thomas White CLEAN AIR POWER ASU with Oxy-fuel Combustion for Zero Emission Energy University of Wyoming College.
H 2 Technology and Policy: Fuel Cells as an Alternative Energy Source John McLees 9/27/05 ChE 384 Dr. Edgar.
Short Design Report Terry Ring CH EN 5253 Process Design II.
Lead Pipe Disposal. Overview Background and Project Requirements Top 5 Designs Detailed Final Design Social and Environmental Factors Testing of Design.
PROCESS DESIGN DEVELOPMENT
SWOT analysis of dry toilets
Production of Nylon 66 Using Bio-Based Feedstock
References Abstract Conclusion The process of biodiesel production
Manufacturing Facility for Nylon 6,6 Mass Flow Rate (kg/batch)
Che 451 chemical engineering design PIPELINE DESIGN
Nylon 6,6 from HMDA and Adipic Acid
Semi-batch Processing of Nylon 66 Chips Ryan Doherty, Meissy Fakhoury, Madeline Frattaroli, Abby Koczera Chemical Engineering, University of New Hampshire,
Continuous Production of Nylon-6,6
Biodiesel Seminar On Submitted To: Submitted By:
Hazard Mitigation.
Manufacturing Facility for Nylon 6,6 Mass Flow Rate (kg/batch)
Date of download: 12/31/2017 Copyright © ASME. All rights reserved.
An-Najah National University
Critical to Quality Variables
ChE 473K Plant Design R. Bruce Eldridge.
Syngas to Liquids (SGTL) Plant
Manufacturing Nylon 66 from the Ground Up
Terry Ring CH EN 5253 Process Design II
Safe Manufacture of Nylon 66
Icelandic Transport Authority
Electric Power Generation
Progress Presentation on: Production Cost Analysis By
Production of Propylene from Methanol
Batch Production of Monoclonal Antibodies
Equipment Cost Summary
Process Flow Diagram & Material Balances
U.S. Citizens Affected by Macular Degeneration
Methanol Dehydration for Dimethyl Ether. Production for Transportation
Natural Circulation in Heat Exchangers Chit Eaindray Thant, Jonathan Thomas, & Shadi Zamani Chemical Engineering Department, University of New Hampshire,
Production of Propylene from Methanol
Production of Monoclonal Antibodies
Production of Dimethyl Ether from Methanol ROLO Engineers Serge Boucher, MaKenzie Marshall, Jia Mo, Joseph Verro Chemical Engineering, University of New.
DME Aerosol LLC – a new producer in the propellant market
Introduction and Background
Renewable Power to Fuels Symposium
Process Flow Diagram and Safety and Other Considerations
Presentation transcript:

Methanol Dehydration for Dimethyl Ether. Production for Transportation Methanol Dehydration for Dimethyl Ether Production for Transportation Thomas Higgins, Adam McCoy, Brandon Musitano Department of Chemical Engineering, University of New Hampshire Introduction Process Flow Diagram and Material Balance 250,000 gal/day DME production rate MeOH  DME + Water No side reactions or byproducts Quality: 99.92 wt% DME Low T acid catalyst (Amberlyst 35) Market Analysis Jie, L., et.al., “Regulated and non-regulated Emissions from a DME Powered Compression Ignition Engine” Safety Considerations Economic Analysis Conclusions and Recommendations DME Sell Price: $0.93/kg or $2.33/gal Recommend motivating transportation users to switch from low sulfur diesel to DME fuel There are enough engineered protections to build a safe plant Recommended to move on for further design analysis Minimize Unit size & storage inventory Substitute Water as coolant Mechanical seals & welded pipes Moderate T & P drops Simplify Use of same equipment 20 year operation Total capital investment of $10M DCFRR: 198% . Acknowledgements We would like to thank Dr. McLarnon as well as the entire Chemical Engineering department for guidance and assistance