1 Direct Reduction Iron Plant Group Golf Selimos, Blake A. Arrington, Deisy C. Sink, Brandon Ciarlette, Dominic F. (Scribe) Advisor : Orest Romaniuk.

Slides:



Advertisements
Similar presentations
Direct Reduction Iron Plant Group Golf Selimos, Blake A. Arrington, Deisy C. Sink, Brandon Ciarlette, Dominic F. (Scribe) Advisor: Orest Romaniuk 1.
Advertisements

Cairo University Faculty of Engineering Petrochemicals Engineering Plant Layout May 2010.
Professor: Jeffery Perl Mentor: Dennis O’Brien Team Members: Jinrong Chen, Kei Simmel, Hantao Wang, Marzena Zarycki Scribe: Kei Simmel.
1 Direct Reduction Iron Plant Group Golf Selimos, Blake A. Arrington, Deisy C. Sink, Brandon Ciarlette, Dominic F. (Scribe) Advisor : Orest Romaniuk.
Senior Design Presentation Direct Fe Reduction Iron Plant Group Golf Selimos, Blake A. Arrington, Deisy C. Sink, Brandon Ciarlette, Dominic F. (Scribe)
Production of Gasoline Components from Synthesis Gas ChE 397 Senior Design Group Alpha Ayesha Rizvi Bernard Hsu Jeff Tyska Mohammad Shehadeh Yacoub Awwad.
King Saud University- College of Engineering- Dept of Chemical Engineering GUIDELINES AND RECOMMANDATIONS FOR THE PREPARATION OF GRADUATE PROJECT I AND.
Contemporary Engineering Economics, 4 th edition, © 2007 Initial Project Screening Method - Payback Period Lecture No.15 Chapter 5 Contemporary Engineering.
Raccoon Mountain Team Hydrogen Production Proposal
Economics – Why Today? Collecting data Additional information for request –Single vs multiple units –Quantity –Quality Future decisions Economic analysis.
KHABAROVSK REFINERY HYDROPROCESSING PROJECT BASIS OF DESIGN APRIL 29th – MAY 3rd 2013, MADRID, SPAIN TRAINING COURSE.
Summer Time Value of Money Session 2 07/02/2015.
Team Hotel: Russel Cabral, Tomi Damo, Ryan Kosak, Vijeta Patel, Lipi Vahanwala Advisors: Bill Keesom – Jacobs Consultancy Jeffery Perl, PhD – UIC Dept.
Given a P&ID, the learner will be able to identify the purpose of that P&ID according to their student guide. – Given a P&ID, locate the title block and.
Senior Design Presentation Direct Fe Reduction Iron Plant
RAO “UES of Russia” Action Plan on Reliability Improvement of Unified Power System of Russia August 29, 2005.
4/27/2010 Team Bravo: Presentation 5 1 Production of Dimethyl Sulfoxide from Lignin Team Bravo is: Stan Das, Jeff Umbach, Russ Boyer, Krista Sutton, Mike.
Office Layout Techniques and Space Requirements
State University of New York WARNING All rights reserved. No part of the course materials used in the instruction of this course may be reproduced in any.
Profitability Analysis Our client is evaluating a number of scenarios How does our process compare with the others?
Direct Reduction Iron Plant Group Golf Selimos, Blake A. Arrington, Deisy C. Sink, Brandon Ciarlette, Dominic F. (Scribe) Advisor: Orest Romaniuk 1.
Ethylene Production From Tennessee Fracked Natural Gas University of Tennessee at Chattanooga ENGR 5910/ENCH /26/2012 Brandon Dodd Valentine Mbamalu.
FLOW-SHEETING What we will cover here? PFD?
Energy Economics A synthetic methane plant from coal is to be constructed at a cost of $4 billion dollars. It requires 14,000 tons/day of coal (10,000.
Direct Reduction Iron Plant Group Golf Selimos, Blake A. Arrington, Deisy C. Sink, Brandon Ciarlette, Dominic F. (Scribe) Advisor : Orest Romaniuk.
1 Direct Reduction Iron Plant Group Golf Selimos, Blake A. Arrington, Deisy C. Sink, Brandon Ciarlette, Dominic F. (Scribe) Advisor : Orest Romaniuk.
FROM RUST TO IRON Deisy C. Arrington, Dominic Ciarlette, Blake Selimos & Brandon Sink Mentor: Orest J. Romaniuk of Ambitech University of Illinois at Chicago.
Syngas Production from Petroleum Coke Gasification
Team Hotel: Russel Cabral, Tomi Damo, Ryan Kosak, Vijeta Patel, Lipi Vahanwala Advisors: Bill Keesom – Jacobs Consultancy Jeffery Perl, PhD – UIC Dept.
Team Hotel: Russel Cabral, Tomi Damo, Ryan Kosak, Vijeta Patel, Lipi Vahanwala Advisors: Bill Keesom – Jacobs Consultancy Jeffery Perl, PhD – UIC Dept.
Production of Ammonia Plant Feedstock From Natural Gas Team Charlie Michael Gardiner - Scribe Rami Qafisheh Alexandria Rinella – Team Leader Advisor: Orest.
Senior Design Presentation Direct Fe Reduction Iron Plant Group Golf Selimos, Blake A. Arrington, Deisy C. Sink, Brandon Ciarlette, Dominic F. Advisor.
1 Improved Nitric Acid Production via Cobalt Oxide Catalysis for use in Ammonia-based Fertilizers University of Illinois at Chicago Department of Chemical.
Senior Design Presentation Direct Fe Reduction Iron Plant Group Golf Selimos, Blake A. Arrington, Deisy C. Sink, Brandon Ciarlette, Dominic F. Advisor.
Convert Gas Pneumatic Controls to Instrument Air Lessons Learned from Natural Gas STAR Partners EPA’s Natural Gas STAR Program, Pioneer Natural Resources.
Direct Reduction Iron Plant Group Golf Selimos, Blake A. Arrington, Deisy C. Sink, Brandon Ciarlette, Dominic F. (Scribe) Advisor: Orest Romaniuk 1.
Direct Reduction Iron Plant Group Golf Selimos, Blake A. Arrington, Deisy C. Sink, Brandon Ciarlette, Dominic F. (Scribe) Advisor : Orest Romaniuk.
Indirect Gasification of Municipal Solid Waste Team Bravo EleftheriosAvtzis David Garcia Bryan Isles Zack Labaschin Alena Nguyen Mentor Dan Rusinak Che.
Senior Design Project Chapter 22. Project Overview –Feed Pre- conditioners –Reactor(s) –Separator(s) –Product Conditioners –Recycle –Heat Integration.
+ Example processes P1. sterilizing ketchup. + Problem statement Heinz Ketchup is made in just a few plants in North America, one of which is in Fremont,
Team Hotel: Russell Cabral, Tomi Damo, Ryan Kosak, Vijeta Patel, Lipi Vahanwala Advisors: Bill Keesom – Jacobs Consultancy Jeffery Perl, PhD – UIC Dept.
Kyle Thorpe BOT Intern.
Confidential & Proprietary Internal Kaplan Use Only. CAPITAL PROJECT ANALYSIS Unit 7.
1 Direct Reduction Iron Plant Group Golf Selimos, Blake A. Arrington, Deisy C. Sink, Brandon Ciarlette, Dominic F. (Scribe) Advisor : Orest Romaniuk.
Optimization & Fleshing Out the Design Optimizing for capital and/or operating costs More detailed look at specific equipment.
Chapter 1: Diagrams for Understanding Chemical Processes
Short Design Report Terry Ring CH EN 5253 Process Design II.
04/06/2010 Production of Dimethyl Sulfoxide from Lignin Team Bravo is: Stan Das, Jeff Umbach, Russ Boyer, Krista Sutton, Mike Czepizak Project Lead: Jake.
Water Supply System And Other Plumbing Fittings
Biotechnology Plant Design:
Potential Energy Diagrams
Date of download: 10/14/2017 Copyright © ASME. All rights reserved.
3E Plus Program Software Insulation Thickness Calculator
Section 1.0 — Fundamentals and General
Syngas to Liquids (SGTL) Plant
Introduction to Chemical Process Design
AIChE Contest Organization
Heat Transfer Equations Based on the conservation equation Conservation of energy applies whether we are considering a whole plant, a single item.
Types of Managers.
Energy Balance Ex3 : A 1000 MW coal-burning power plant is burning bituminous coal with 8% ash content. The power plant is 33% efficient with 35% of.
CHAPTER 21: BUDGETARY PLANNING
Cash Flows for a New Project
Financial Appraisal of Project
Terry Ring CH EN 5253 Process Design II
Methanol Dehydration for Dimethyl Ether. Production for Transportation
Volume 2, Issue 2, Pages (February 2018)
Terry A. Ring Chemical Engineering University of Utah
Methanol Dehydration for Dimethyl Ether. Production for Transportation
Balanced scales and equations
Presentation transcript:

1 Direct Reduction Iron Plant Group Golf Selimos, Blake A. Arrington, Deisy C. Sink, Brandon Ciarlette, Dominic F. (Scribe) Advisor : Orest Romaniuk

Table of Contents » 3-4 Design Basis / Block Flow Diagram » 5 – Process Flow Diagram » 6 – Initial Control Scheme » 7-8 – Plant Layout » 9-11 – Calculations » – Convection Section » – Economics » – Report » 23 - Summary 2

Block Flow/Design Basis 3

Design Basis 4

Process Flow Diagram 5

Initial Control Scheme 6

Plant Layout (1) Ejector 2.HX -1 3.HX -2 4.Reformer 5.Oxy booster 6.Furnace 7.Storage 8.Tankage 9.Building Road Railroad Wind

8 Plant Layout (2)

Energy Balance Data and Equations 9

Calculation Summary 10

Heat Exchanger Calculations 11

Convection Section Issues 12

Convection Section Recommendations 13

Convection Section Recommendations 14

Equipment 15

Catalysts 16

Personnel EmployeesMan hours per day worked 7 Operators56 5 Engineers (shared with 3 plants)40/3 1 Complex manager (shared with whole plant)8/9 20 Administration (shared with whole plant)160/9 3 Safety (shared with whole plant)24/9 4 Medical staff (shared with plant)32/9 1 Maintenance (shared with plant)8/9 3 Supervisor24 Total120 17

Expenses 18

Revenue 19

Profit 20

Payback Period 21

Report 22

Report

Summary 24

Questions 25

References 26