Distillation Column Flooding Predictor Texas Technology Showcase

Size: px
Start display at page:

Download "Distillation Column Flooding Predictor Texas Technology Showcase"

Transcription

1 Distillation Column Flooding Predictor Texas Techlogy Showcase Galveston, Texas 2006 George E. Dzyacky 2ndpoint LLC

2 Developer George E. Dzyacky (da ZA key) Background in Refining Operations 28 years Petroleum Refining FCC and Vapor Recovery Received Amoco Whiting Refinery highest recognition award three times for advanced process control invations, totaling $6.8MM (US) /year Patent holder Twice awarded U. S. Department of Energy grant on Flooding Predictor

3 Techlogy description Flooding Predictor was developed as a diagstic tool to predict and avoid chronic flooding in FCC absorber columns evolved into A/C strategy Exploits patterns of behavior that column variables undergo as liquid begins to hold-up Highly repeatable patterns were discovered to precede flooding events When pre-flood conditions are detected, the strategy generates a warning of impending flood or a discrete output to temporarily reduce operating severity 98%-plus accuracy increased confidence in the methodology and Flooding Predictor evolved from advisory to closed-loop application The Flooding Predictor integrates with Multivariable Predictive Control (MPC) or can be commissioned as a stand-alone application

4 Techlogy benefits Inexpensive software alternative for diagsing flooding problems and increasing column throughput by 3-7% Estimated ROI for original Amoco project in 2006 dollars; $0,000,000/year for $80,000 investment 00% payback in 3 days Virtually eliminates flooding events and the negative consequences associated with them: Throughput reduction Environmental excursions Equipment damage Risk to personal safety Increase energy efficiency Low installation and maintenance costs

5 Techlogy basis Flooding Predictor recognizes unique patterns of behavior among process variables as the column approaches flood Patterns are based on derivative values (rate of change) of column variables: reboiler temperature, levels, flows, delta temperature, and delta pressure Variables are chosen based on observation and analysis of their derivative values as the column approaches and enters flood When enabled, the Flooding Predictor compares current derivative values against critical derivative limits identified during step-tests When the critical limits are met, the Flooding Predictor warns of imminent flood or in closed-loop form momentarily reduces column operating severity by a predetermined value

6 Pre-flood patterns Comprised of changes in column variables, which occur well within rmal alarm limits. Temporary change in Overhead Flow 40 MSQFD 0 MSQFD 0 Temporary change in Delta Pressure 00 psig 0 psig Temporary change in Bottom Temperature 400 deg 0 0 deg 0 Temporary change in Level or Bottom Flow 00% 0% 0

7 Pre-flood pattern identification Changes are subtle, transient and simultaneous Changes in raw variables are virtually indistinguishable from rmal process ise Pre-flood patterns are well within rmal alarm limits Individual derivatives exceed their critical values frequently Simultaneous behavior present only at pre-flood conditions Pre-flood patterns occur up to 60 minutes in advance of flood event Temporary change in Overhead Flow 40 MSQFD 0 MSQFD 0 Temporary change in Delta Pressure 00 psig 0 psig 400 deg 0 deg 0 Temporary change in Bottom Temperature Temporary change in Level or Bottom Flow 00% 0% 0 0

8 Motiva commercial demonstration Motiva Enterprise Inc., Norco, Louisiana Actual test data of flood prediction on Motiva depropanizer; Norco, Louisiana USA

9 Pre-flood modeling 400 deg 00 psig Temporary increase in Delta Pressure, 0 psig deg 0 deg Change in engineering units/time, i.e., 0.56 degrees F/minute 0 Temporary increase in Bottom Temp. 0 deg 00% Temporary decrease in Level or Flow, 0% 0

10 Original closed-loop applications FCC Vapor recovery Feed Target Feed Rate Effect of flooding events on unit throughput Effect of eliminating flooding and operating column at or near its hydraulic limit

11 Why is this technique beneficial? Shifts control objective from conventional delta-pressure to the true hydraulic limit Hydraulic limit Column dp Capacity Upper dp limit 6%+ capacity increase proven in research at the University of Texas at Austin

12 University of Texas finite reflux test DISTILLATION COLUMN 8" TRAY SPACING Conventional distillation column operated at finite reflux, serviced by a kettle reboiler and horizontal condenser FC203 condenser T2070 accumulator Overhead reflux in top tray temperature control FC200 LT203 T2073 PDT25 feed tank FC204 Steam reboiler in pressure compensated temperature control FC20 LT600 T207 Independent feed flow control reboiler Bottoms level control Column pressure control with N2 Condensate LT204 reflux pump bottoms pump feed pump

13 University of Texas finite reflux test runs COMPOSITION (C6) RUN PREDICTOR FLOOD FEED RATE PRESS DRP REFLUX RATIO (gpm) (in H2O) FEED TOP BOT (%) (%) (%)

14 University of Texas finite reflux test runs COMPOSITION (C6) RUN PREDICTOR FLOOD FEED RATE PRESS DRP REFLUX RATIO (gpm) (in H2O) FEED TOP BOT (%) (%) (%)

15 Conclusions; Separation Research Program, University of Texas at Austin The Flooding Predictor works on a variety of columns. The Flooding Predictor controls the column very close to the flood point, where the highest efficiency and highest capacity occur. The Flooding Predictor can be installed on nearly any process control computer. Thorough testing at the SRP conclusively indicate DCFP can increase throughput and prevent flooding while maintaining efficiency. This equates to a 6.22% improvement in sustainable feed rate.

16 Typical demonstration plan Favorable licensing agreement for commercial-scale demonstration site Identification criteria for demonstration column Establish consensus on measure of success Meet with unit personal Conduct a preliminary assessment of column Determine demonstration test objectives Early analysis point building and derivative data collection Pre-commission phase Commissioning phase Post-commissioning and Performance data collection

J. Christopher Lewis Distillation Column Flooding Predictor INTRODUCTION

J. Christopher Lewis Distillation Column Flooding Predictor INTRODUCTION STS-AIChE Energy Forum March 3, 2005 J. Christopher Lewis, UT Austin George E. Dzyacky, 2ndpoint L.L.C. 3/05 INTRODUCTION Background Technology Results Conclusions Acknowledgements BACKGROUND -The Inventor

More information

GTC TECHNOLOGY. GT-UWC SM How a Uniting Wall Column Maximizes LPG Recovery. Engineered to Innovate WHITE PAPER

GTC TECHNOLOGY. GT-UWC SM How a Uniting Wall Column Maximizes LPG Recovery. Engineered to Innovate WHITE PAPER GTC TECHNOLOGY GT-UWC SM How a Uniting Wall Column Maximizes LPG Recovery WHITE PAPER Engineered to Innovate Maximizing LPG Recovery from Fuel Using a Uniting Wall Column Refiners have a challenge to recover

More information

GT-LPG Max SM. Maximizing LPG Recovery from Fuel Gas Using a Dividing Wall Column. Engineered to Innovate

GT-LPG Max SM. Maximizing LPG Recovery from Fuel Gas Using a Dividing Wall Column. Engineered to Innovate GTC Technology White Paper GT-LPG Max SM Maximizing LPG Recovery from Fuel Using a Dividing Wall Column Engineered to Innovate GT-LPG Max SM Maximizing LPG Recovery from Fuel Using a Dividing Wall Column

More information

Dynamic Simulation for APC projects A case study on a Reformate Splitter with side draw. Dr Sebastien OSTA TOTAL Jose Maria FERRER Inprocess

Dynamic Simulation for APC projects A case study on a Reformate Splitter with side draw. Dr Sebastien OSTA TOTAL Jose Maria FERRER Inprocess Dynamic Simulation for APC projects A case study on a Reformate Splitter with side draw Dr Sebastien OSTA TOTAL Jose Maria FERRER Inprocess Introduction Steady-state simulation is used traditionally for

More information

Synergies between process energy efficiency and relief loads

Synergies between process energy efficiency and relief loads Synergies between process energy efficiency and relief loads Mary Kay O Connor Process Safety Center 2008 Symposium Rob Brendel Jacobs Consultancy Inc. (Chicago) Petroleum, Chemicals & Energy Practice

More information

On-line Parameter Estimation and Control for a Pilot Scale Distillation Column

On-line Parameter Estimation and Control for a Pilot Scale Distillation Column On-line Parameter Estimation and Control for a Pilot Scale Distillation Column Lina Rueda, Thomas F. Edgar and R. Bruce Eldridge Department of Chemical Engineering University of Texas at Austin Prepared

More information

Advanced Process Control: Quick and Easy Energy Savings

Advanced Process Control: Quick and Easy Energy Savings Advanced Process Control: Quick and Easy Energy Savings Paul Kesseler Manager, Advanced Process Control Practice Global Consulting Group Invensys Operations Management Energy Management vs. Spot Energy

More information

The Engineer s Energy Toolbox: Practices, Technologies and Management Dec. 6-7, 2006 in Galveston, Texas Sabine Brueske, Energetics Inc.

The Engineer s Energy Toolbox: Practices, Technologies and Management Dec. 6-7, 2006 in Galveston, Texas Sabine Brueske, Energetics Inc. E-News Article The Engineer s Energy Toolbox: Practices, Technologies and Management Dec. 6-7, 2006 in Galveston, Texas Sabine Brueske, Energetics Inc. Learn how energy management, technologies, and practices

More information

Distillation Experiment--Flooding

Distillation Experiment--Flooding Lab Report Distillation Experiment--Flooding by Andrew Yu-Hao Chang Karri Lynn Crawford David Marion Genna [NOTE: The report has been minimally edited for clarity and consistency.] Submitted to Dr. C.

More information

Applying Dynamic Process Simulations Toward Flaring Reduction

Applying Dynamic Process Simulations Toward Flaring Reduction Applying Dynamic Process Simulations Toward Flaring Reduction White Paper Siemens AG 2018, All rights reserved 1 Dynamic process simulation has traditionally been a tool of process engineers and process

More information

Saving Energy in Fractionation Operation. Texas Technology Showcase 2006

Saving Energy in Fractionation Operation. Texas Technology Showcase 2006 Saving Energy in Fractionation Operation Texas Technology Showcase 2006 Presenter Doug White Principal Consultant and Vice President, APC Services Process Systems and Solutions Emerson Process Management

More information

Advanced Diagnostics: 4 Steps to Better Decision Making

Advanced Diagnostics: 4 Steps to Better Decision Making Advanced Diagnostics: 4 Steps to Better Decision Making Presenters Bill Zhou Product Marketing Engineer bill.zhou@emerson.com Andrew Klosinski Principle Engineer andrew.klosinski@emerson.com 27-Jun-01,

More information

Texas Petrochemicals LP

Texas Petrochemicals LP Texas Petrochemicals LP The Leading Producer of C 4 Based Chemicals Butene-1 Distillation Control Project Tom Ellerbrock Optimization Engineer Texas Petrochemicals L.P. Texas Technology Showcase December

More information

Coker Safety and Reliability Lessons Learned

Coker Safety and Reliability Lessons Learned Coker Safety and Reliability Lessons Learned Dale Wilborn 2015 Coking.com Conference COKER SAFETY & RELIABILITY Current Situation The Delayed Coker industry has had many incidents with severe consequences,

More information

Guidelines for Dynamic Modeling of Column Startup Chemstations, Inc.

Guidelines for Dynamic Modeling of Column Startup Chemstations, Inc. Guidelines for Dynamic Modeling of Column Startup Chemstations, Inc. Authors: Wendy Young Reed & Stuart Schwab www.chemstations.com Abstract Advances in computing speed continue to enable dynamic modeling

More information

Salt deposition in FCC gas concentration

Salt deposition in FCC gas concentration Salt Deposition in FCC Gas Concentration Units Michel Melin Director Technical Service Grace Davison Refining Technologies Europe, Middle East and Africa Colin Baillie Marketing Manager Grace Davison Refining

More information

WHITE PAPER Achieving Operational Excellence in the Chemicals Industry Using APC

WHITE PAPER Achieving Operational Excellence in the Chemicals Industry Using APC WHITE PAPER Achieving Operational Excellence in the Chemicals Industry Using APC Tushar Singh, Product Marketing Manager, Aspen Technology, Inc. Kate Kulik, Sr. Principal Business Consultant, Aspen Technology,

More information

A Better Approach To Energy Performance Benchmarking

A Better Approach To Energy Performance Benchmarking A Better Approach To Energy Performance Benchmarking John Walter KBC Advanced Technologies, Inc Texas Technology Showcase 2006 Galveston, TX Current Industry Challenges High energy costs driving need for

More information

Industrial Waste Heat Recovery

Industrial Waste Heat Recovery Industrial Waste Heat Recovery Industrial Energy RoundTable Kathey Ferland Project Manager Texas Industries of the Future kferland@mail.utexas.edu Riyaz Papar, PE, CEM Director, Energy Assets & Optimization

More information

OMNI-FIT Revamp of a Texas C3 Splitter

OMNI-FIT Revamp of a Texas C3 Splitter OMNI-FIT Revamp of a Texas C3 Splitter Eric T. Cole Koch-Glitsch LP Douglas J. Little Koch Hydrocarbon SW LLC Scott Schingen Koch Hydrocarbon SW LLC Veada Colic Process Consulting Services, Inc. Presented

More information

Coping With Rejection DCP Midstream s Operator Decision Support System

Coping With Rejection DCP Midstream s Operator Decision Support System Texas A&M University-kingsville Society Of Petroleum Engineers Student Chapter Student Driven Research Symposium For Oil And Gas Operations Coping With Rejection DCP Midstream s Operator Decision Support

More information

ENERGY EFFICIENT SYNTHESIS AND DESIGN FOR CARBON CAPTURE

ENERGY EFFICIENT SYNTHESIS AND DESIGN FOR CARBON CAPTURE Distillation Absorption 2010 A.B. de Haan, H. Kooijman and A. Górak (Editors) All rights reserved by authors as per DA2010 copyright notice ENERGY EFFICIENT SYNTHESIS AND DESIGN FOR CARBON CAPTURE Angelo

More information

Hydrate Formation in Chevron Mabee Unit for NGL Recovery and CO 2 Purification for EOR. Abstract

Hydrate Formation in Chevron Mabee Unit for NGL Recovery and CO 2 Purification for EOR. Abstract Hydrate Formation in Chevron Mabee Unit for NGL Recovery and CO 2 Purification for EOR Abstract In the early 199 s, Chevron installed a new process to recover natural gas liquids (NGLs) from recycled CO

More information

IMPACT OF CONTROL SYSTEM IMPROVEMENTS WITHIN AN ETHYLBENZENE & STYRENE MONOMER PLANT

IMPACT OF CONTROL SYSTEM IMPROVEMENTS WITHIN AN ETHYLBENZENE & STYRENE MONOMER PLANT IMPACT OF CONTROL SYSTEM IMPROVEMENTS WITHIN AN ETHYLBENZENE & STYRENE MONOMER PLANT Dong Eon Lee a, Donald L. Snowden b, Stephen G. Finlayson c a Samsung Total Chemicals Manager Production & Technology

More information

HYSYS WORKBOOK By: Eng. Ahmed Deyab Fares.

HYSYS WORKBOOK By: Eng. Ahmed Deyab Fares. HYSYS WORKBOOK 2013 By: Eng. Ahmed Deyab Fares eng.a.deab@gmail.com adeyab@adeyab.com Mobile: 002-01227549943 - Email: adeyab@adeyab.com 1 Flash Separation We have a stream containing 15% ethane, 20% propane,

More information

WWT Two-Stage Sour Water Stripping

WWT Two-Stage Sour Water Stripping WWT Two-Stage Sour Water Stripping Improve performance of sulfur recovery units ben efits The Chevron WWT Process is a two-stage stripping process which separates ammonia and hydrogen sulfide from sour

More information

In 1965, while working as a

In 1965, while working as a Sour strippers: design and operation Simpler, more cost-effective sour stripper designs can outperform more generally accepted designs in the refining industry NORMAN LIEBERMAN Process Improvement Engineering

More information

FIRST-PRINCIPLES INFERENCE MODEL IMPROVES DEISOBUTANIZER COLUMN CONTROL

FIRST-PRINCIPLES INFERENCE MODEL IMPROVES DEISOBUTANIZER COLUMN CONTROL PETROCONTROL Advanced Control and Optimization FIRST-PRINCIPLES INFERENCE MODEL IMPROVES DEISOBUTANIZER COLUMN CONTROL By: Y. Zak Friedman, PhD Petrocontrol, New York, NY, USA Mark Schuler United Refining

More information

A New Optimisation Based Retrofit Approach for Revamping an Egyptian Crude Oil Distillation Unit

A New Optimisation Based Retrofit Approach for Revamping an Egyptian Crude Oil Distillation Unit Available online at www.sciencedirect.com ScienceDirect Energy Procedia 36 (2013 ) 454 464 TerraGreen 13 International Conference 2013 - Advancements in Renewable Energy and Clean Environment A New Optimisation

More information

ALKYLATION OPTIONS FOR ISOBUTYLENE AND ISOPENTANE. Presented By. David C. Graves Senior Research Engineer

ALKYLATION OPTIONS FOR ISOBUTYLENE AND ISOPENTANE. Presented By. David C. Graves Senior Research Engineer ALKYLATION OPTIONS FOR ISOBUTYLENE AND ISOPENTANE Presented By David C. Graves Senior Research Engineer STRATCO, Inc. 11350 Tomahawk Creek Parkway Suite 200 Leawood, KS 66211 November, 2001 Copyright 2001

More information

DESIGN AND OPERATING EXPERIENCE FOR ANADARKO S LANCASTER FACILITY

DESIGN AND OPERATING EXPERIENCE FOR ANADARKO S LANCASTER FACILITY DESIGN AND OPERATING EXPERIENCE FOR ANADARKO S LANCASTER FACILITY Presented at the 95 th Annual Convention of the Processors Association April 11, 2016 New Orleans, Louisiana Joe T. Lynch, P.E. Ortloff

More information

ENHANCED V-GRID TRAYS INCREASE COLUMN PERFORMANCE

ENHANCED V-GRID TRAYS INCREASE COLUMN PERFORMANCE Distillation Honors Session ENHANCED V-GRID TRAYS INCREASE COLUMN PERFORMANCE by Daniel R. Summers, P.E. - Darcy Ehmann - AGP Corn Processors November 4, 2002 Background Ethanol already plays an an important

More information

OPTIMISATION OF EXISTING HEAT-INTEGRATED REFINERY DISTILLATION SYSTEMS

OPTIMISATION OF EXISTING HEAT-INTEGRATED REFINERY DISTILLATION SYSTEMS OPTIMISATION OF EXISTING HEAT-INTEGRATED REFINERY DISTILLATION SYSTEMS Mamdouh Gadalla, Megan Jobson and Robin Smith Department of Process Integration, UMIST, Manchester, UK ABSTRACT Existing refinery

More information

Distillation DEPARTMENT OF CHEMICAL ENGINEERING

Distillation DEPARTMENT OF CHEMICAL ENGINEERING Distillation DEPARTMENT OF CHEMICAL ENGINEERING 2 3 Weeping in distillation column 4 Distillation. Introduction Unit operation Separation process A feed mixture of two or more components is separated into

More information

Fundamentals of Distillation Column Control

Fundamentals of Distillation Column Control Fundamentals of Distillation Column Control by Terry Tolliver Standards Certification Education & Training Publishing Conferences & Exhibits ISA Automation Week 2011 PRESENTER Terry Tolliver Terry is a

More information

Challenges in Industrial Waste Heat Recovery. Texas Technology 2006 Showcase Tony Dafft December 6 & 7, 2006

Challenges in Industrial Waste Heat Recovery. Texas Technology 2006 Showcase Tony Dafft December 6 & 7, 2006 Challenges in Industrial Waste Heat Recovery Texas Technology 2006 Showcase Tony Dafft December 6 & 7, 2006 Outline Plant Statistics and Energy History Tools Used to Identify Projects Sample of Projects

More information

Improvement of distillation column efficiency by integration with organic Rankine power generation cycle. Introduction

Improvement of distillation column efficiency by integration with organic Rankine power generation cycle. Introduction Improvement of distillation column efficiency by integration with organic Rankine power generation cycle Dmitriy A. Sladkovskiy, St.Petersburg State Institute of Technology (technical university), Saint-

More information

DIVIDING WALL COLUMN REVAMP OPTIMISES MIXED XYLENES PRODUCTION

DIVIDING WALL COLUMN REVAMP OPTIMISES MIXED XYLENES PRODUCTION DIVIDING WALL COLUMN REVAMP OPTIMISES MIXED XYLENES PRODUCTION Bernie Slade 1, Berne Stober 1 and Dave Simpson 2 1 ExxonMobil, E-mail: bernie.slade@exxonmobil.com/berne.k.stober@exxonmobil.com 2 Koch-Glitsch,

More information

Application of Ultra High Capacity ConSep Trays for Debottlenecking of Gas and Ethylene Plant Fractionation Trains

Application of Ultra High Capacity ConSep Trays for Debottlenecking of Gas and Ethylene Plant Fractionation Trains Application of Ultra High Capacity ConSep Trays for Debottlenecking of Gas and Ethylene Plant Fractionation Trains by Waldo de Villiers, Shell Global Solutions (US), Inc. Peter Wilkinson, Shell Global

More information

Introduction to Distillation. Binous - Introd. to Distillation

Introduction to Distillation. Binous - Introd. to Distillation Introduction to Distillation 1 Exploits differences in boiling point, or volatility Requires the input of energy Handles a wide range of feed flow rates Separates a wide range of feed concentrations Produce

More information

Study of the Control Systems of a Distillation Process Equipped with Heat Pump

Study of the Control Systems of a Distillation Process Equipped with Heat Pump Study of the Control Systems of a Distillation Process Equipped with Heat Pump CRISTIAN PATRASCIOIU*, MARIAN POPESCU Petroleum-Gas University of Ploiesti, Automatic Control, Computers and Electronics Department,

More information

Expansion Power Cryostripping:

Expansion Power Cryostripping: EXPANSION POWER INC. Expansion Power Cryostripping: LOW-COST FRACTIONS RECOVERY FROM REFINERY FUEL-GAS SYSTEMS 1 WHO WE ARE Expansion Power Inc. (EPI) Edmonton, Alberta-based company formed in 2006 to

More information

Module 2: Solid Fossil Fuel (Coal) Lecture 12: Combustion of coal and coke making

Module 2: Solid Fossil Fuel (Coal) Lecture 12: Combustion of coal and coke making 1 P age Module 2: Solid Fossil Fuel (Coal) Lecture 12: Combustion of coal and coke making 2 P age Keywords: Coal tar, distillation, caustic washing, deoiling 2.4 Combustion of coal and coke making 2.4.3

More information

Agenda. 1. Introduction. 2. History of Distillation. 3. Types of Stages. 4. Tray Fundamentals. 5. Tray Efficiencies

Agenda. 1. Introduction. 2. History of Distillation. 3. Types of Stages. 4. Tray Fundamentals. 5. Tray Efficiencies Agenda 1. Introduction 2. History of Distillation 3. Types of Stages 4. Tray Fundamentals 5. Tray Efficiencies Introduction Distillation Distillation is the separation of key components by the difference

More information

FCC Spent Catalyst Stripper Technology

FCC Spent Catalyst Stripper Technology FCC Spent Catalyst Stripper Technology Paul D. Wendt FCC Technology Manager CB&I Coking and CatCracking Conference New Delhi, October 2013 Spent Catalyst Stripper Technology Big Picture Overview Process

More information

Using Petro-SIM to Optimize an FCCU with Integrated Product Separation. Gregory Tragitt Senior Staff Consultant

Using Petro-SIM to Optimize an FCCU with Integrated Product Separation. Gregory Tragitt Senior Staff Consultant Using Petro-SIM to Optimize an FCCU with Integrated Product Separation Gregory Tragitt Senior Staff Consultant 2014 KBC Advanced PROPRIETARY Technologies plc. INFORMATION All Rights Reserved. May 2014

More information

Influence of Process Operations on VOC and BTEX Emissions from Glycol Dehydration Units

Influence of Process Operations on VOC and BTEX Emissions from Glycol Dehydration Units Page 1 of 12 Influence of Process Operations on VOC and BTEX Emissions from Glycol Dehydration Units MICHAEL W. HLAVINKA, VICENTE N. HERNANDEZ-VALENCIA, JERRY A. BULLIN, Bryan Research & Engineering, Inc.,

More information

Waste Generation and Release Estimation from Chemical Processes - Chapter 8.3. David R. Shonnard Department of Chemical Engineering

Waste Generation and Release Estimation from Chemical Processes - Chapter 8.3. David R. Shonnard Department of Chemical Engineering Waste Generation and Release Estimation from Chemical Processes - Chapter 8.3 David R. Shonnard Department of Chemical Engineering 1 Outline After screening out a number of environmentally and economically

More information

Retrofit for a Gas Separation Plant by Pinch Technology

Retrofit for a Gas Separation Plant by Pinch Technology Retrofit for a Gas Separation Plant by Pinch Technology Napredakul, D. a, Siemanond, K.a, Sornchamni, T.b, Laorrattanasak, S.b a The Petroleum and Petrochemical College, Chulalongkorn University, Bangkok,

More information

HOW TO SELECT BEST MEG RECOVERY UNIT s CONFIGURATION?

HOW TO SELECT BEST MEG RECOVERY UNIT s CONFIGURATION? HOW TO SELECT BEST MEG RECOVERY UNIT s CONFIGURATION? PAPER PRESENTED AT GPA EUROPE Madrid, 17 th - 19 th September, 2014 Jérémie ESQUIER PROSERNAT Paris, France PROSERNAT Mr Jérémie ESQUIER - Business

More information

FOAMING EFFECT ON RANDOM PACKING PERFORMANCE

FOAMING EFFECT ON RANDOM PACKING PERFORMANCE FOAMING EFFECT ON RANDOM PACKING PERFORMANCE G. X. Chen, T. J. Cai, K. T. Chuang 2 and A. Afacan 2 Fractionation Research, Inc., P.O. Box 208, Stillwater, OK 7407, USA 2 Department of Chemical and Materials

More information

TABLE OF CONTENT

TABLE OF CONTENT Page : 1 of 12 Project Engineering Standard www.klmtechgroup.com KLM Technology #03-12 Block Aronia, Jalan Sri Perkasa 2 Taman Tampoi Utama 81200 Johor Bahru Malaysia RECOVERY AND SPLITTER TABLE OF CONTENT

More information

Nathan A. Hatcher and Ralph H. Weiland, Optimized Gas Treating Inc., USA, discuss the fate of ammonia in refinery amine systems.

Nathan A. Hatcher and Ralph H. Weiland, Optimized Gas Treating Inc., USA, discuss the fate of ammonia in refinery amine systems. Special treatment T he corrosion that results from ammonia ingress and accumulation in refinery and biogas amine systems is a problem that may be exacerbated by the increasing utilisation of advantaged

More information

Fate of Ammonia in Refinery Amine Systems

Fate of Ammonia in Refinery Amine Systems Fate of Ammonia in Refinery Amine Systems Nathan A. Hatcher and Ralph H. Weiland Optimized Gas Treating, Inc. Sugar Land, TX INTRODUCTION Ammonia ingress and accumulation in refinery and bio-gas amine

More information

Dynamics and Control Simulation of a Debutanizer Column using Aspen HYSYS

Dynamics and Control Simulation of a Debutanizer Column using Aspen HYSYS Dynamics and Control Simulation of a Debutanizer Column using Aspen HYSYS S. Karacan 1, F. Karacan 2 1 Ankara University, Engineering Faculty, Department of Chemical Engineering, Tandogan 06100, Ankara,

More information

Development and Cost Estimation of Green Gas Reduction Process for Power Plant

Development and Cost Estimation of Green Gas Reduction Process for Power Plant Development and Cost Estimation of Green Gas Reduction Process for Power Plant Jiyong Kim, Dongwoon Kim and Il Moon Department of Chemical Engineering, Yonsei University, 134 Shinchodong Seodaemoonku,

More information

Reactors and Separations Design Project. Phthalic Anhydride Production

Reactors and Separations Design Project. Phthalic Anhydride Production Reactors and Separations Design Project Phthalic Anhydride Production We are continuing our evaluation of process alternatives for the production of Phthalic Anhydride via the catalytic oxidation of o-xylene.

More information

Example SPC-2: Effect of Increasing Column P on a C3 splitter

Example SPC-2: Effect of Increasing Column P on a C3 splitter Example SPC-2: Effect of Increasing Column P on a C3 splitter Consider the separation of a mixture of 50 mol/hr of propane C 3 H 8 (1) and 50 mol/hr propene, C 3 H 6 (2) at a pressure of 1.1 bar and a

More information

Energy Balances and Numerical Methods Design Project. Production of Methyl Tertiary-Butyl Ether

Energy Balances and Numerical Methods Design Project. Production of Methyl Tertiary-Butyl Ether Energy Balances and Numerical Methods Design Project Production of Methyl Tertiary-Butyl Ether Methyl Tertiary-Butyl Ether () is a gasoline additive used to increase octane number that is produced from

More information

MTBE Production. Process Description. Possibility of Changing Process Feed Conditions

MTBE Production. Process Description. Possibility of Changing Process Feed Conditions Production You work in a facility that produces about 100,000 tonne/y of methyl tertiary butyl ether (). is an oxygenated fuel additive that is blended with gasoline to promote CO 2 formation over CO formation

More information

Water Conservation Initiatives Burnaby Refinery

Water Conservation Initiatives Burnaby Refinery Water Conservation Initiatives Burnaby Refinery CAP Meeting May 11 th, 2016 Mack Atkinson Process Engineer Kel Coulson Lead Process Engineer Outline Photo credit: waterbucket.ca 1. General Refinery Water

More information

Advanced Process and Chemical Complex Analysis Systems

Advanced Process and Chemical Complex Analysis Systems 157g Advanced Process and Chemical Complex Analysis Systems Derya Ozyurt b, Aimin Xu b, Thomas A Hertwig a, Janardhana R Punuru b, Ralph W Pike b, F. Carl Knopf b, Jack R Hopper c, and Carl L Yaws c a

More information

Equipment Sizing and Capital Cost Estimation

Equipment Sizing and Capital Cost Estimation Equipment Sizing and Capital Cost Estimation Warren D. Seider University of Pennsylvania Philadelphia, Pennsylvania Selection of Topics - depends on previous exposure to process economics Can begin with

More information

Optimization of Energy Consumption during Natural Gas Dehydration

Optimization of Energy Consumption during Natural Gas Dehydration Abdul Qadeer 1*, Adnan Aftab 2, Imran Nazir 3 1 Department of Chemical Engineering, 2 Department of Petroleum and Gas Engineering, Balochistan University of Information Technology Engineering & Management

More information

Overview of Distillation Techniques and Process in Recovery and Reuse of Volatile Liquids

Overview of Distillation Techniques and Process in Recovery and Reuse of Volatile Liquids Overview of Distillation Techniques and Process in Recovery and Reuse of Volatile Liquids Syed Abdul Jilani Dept. of Chemical Engineering, Vignan University Abstract: Distillation is a process in which

More information

Dynamic degrees of freedom for tighter bottleneck control

Dynamic degrees of freedom for tighter bottleneck control 10th International Symposium on Process Systems Engineering - PSE2009 Rita Maria de Brito Alves, Claudio Augusto Oller do Nascimento and Evaristo Chalbaud Biscaia Jr. (Editors) 2009 Elsevier B.V. All rights

More information

Econamine FG Plus SM Technology for Post- Combustion CO 2 Capture

Econamine FG Plus SM Technology for Post- Combustion CO 2 Capture Econamine FG Plus SM Technology for Post- Combustion CO 2 Capture Satish Reddy Presented at: 11 th Meeting of the International Post-Combustion CO2 Capture Network May 20 th -21 th, 2008, Vienna, Austria

More information

RETROFIT OF THE AMERADA HESS SEA ROBIN PLANT FOR VERY HIGH ETHANE RECOVERY ABSTRACT

RETROFIT OF THE AMERADA HESS SEA ROBIN PLANT FOR VERY HIGH ETHANE RECOVERY ABSTRACT RTROFIT OF TH AMRADA HSS SA ROBIN PLANT FOR VRY HIGH THAN RCOVRY Joe T. Lynch, P.. Ortloff ngineers, Ltd. Midland, Texas USA J. Pat McCann and Paul Carmody, P.. Amerada Hess Corporation Houston, Texas

More information

Evaluation of Water Curtailment on Energy Use and Plant Net Profitability

Evaluation of Water Curtailment on Energy Use and Plant Net Profitability Evaluation of Water Curtailment on Energy Use and Plant Net Profitability Kathey Ferland Nov. 5, 2015 Texas Industrial Water Management Forum Texas Industries of the Future The University of Texas at Austin

More information

Non-Intrusive Corrosion and Erosion Monitoring Solutions and Case Studies. Dr. Jake Davies, ICorr Aberdeen meeting, 28th Feb 2017

Non-Intrusive Corrosion and Erosion Monitoring Solutions and Case Studies. Dr. Jake Davies, ICorr Aberdeen meeting, 28th Feb 2017 Non-Intrusive Corrosion and Erosion Monitoring Solutions and Case Studies Dr. Jake Davies, ICorr Aberdeen meeting, 28th Feb 2017 Presentation Contents Company History Drivers to monitor for corrosion and/or

More information

Performance Evaluation of Deethanizer Column Using Real Time Optimization

Performance Evaluation of Deethanizer Column Using Real Time Optimization Performance Evaluation of Deethanizer Column Using Real Time Optimization Renanto Handogo, Indra Darmawan, Fadillah Akhbar Marsha, Juwari Department of Chemical Engineering Institut Teknologi Sepuluh Nopember

More information

Minimize Sulfur Pit Vent Contribution to Stack Emissions

Minimize Sulfur Pit Vent Contribution to Stack Emissions Minimize ulfur Pit Vent Contribution to tack Emissions Grant Qui, P.E. Excel Paralubes - ConocoPhillips 2800 Old panish Trail 3008 MO Westlake, LA 70609 Houston, TX 77079 Al Keller Refining Technical ervices

More information

Alkylating Refinery Grade Propylene

Alkylating Refinery Grade Propylene Alkylating Refinery Grade Propylene By Julian igliavacca Process Engineering anager, Downstream Process Engineering Process Plants & Industrial - Wood Group ustang Introduction Refinery grade propylene

More information

THE EFFECT OF PRESSURE ON DYNAMICS AND CONTROL OF SIDESTREAM DISTILLATION COLUMNS

THE EFFECT OF PRESSURE ON DYNAMICS AND CONTROL OF SIDESTREAM DISTILLATION COLUMNS Vol-2, Issue-3 PP. 63-612 ISSN: 2394-5788 THE EFFECT OF PRESSURE ON DYNAMICS AND CONTROL OF SIDESTREAM DISTILLATION COLUMNS S.R.Dantas, R.M.L.Oliveira, W.B.Ramos, G.W. Farias Neto & R. P. Brito Federal

More information

Journal of Emerging Trends in Engineering and Applied Sciences (JETEAS) 4(5): (ISSN: )

Journal of Emerging Trends in Engineering and Applied Sciences (JETEAS) 4(5): (ISSN: ) Journal of Emerging Trends in Engineering and Applied Sciences (JETEAS) 4(5): 731-736 Scholarlink Research Institute Journals, 2013 (ISSN: 2141-7016) jeteas.scholarlinkresearch.org Journal of Emerging

More information

Fluor s Econamine FG Plus SM Technology

Fluor s Econamine FG Plus SM Technology Flue Gas Fluor s Econamine FG Plus SM Technology An Enhanced Amine-Based CO 2 Capture Process NETL Carbon Sequestration Conference May 2003 to Atmos Reflux Condenser 1 Amine Filter Package FI W CW Stripper

More information

Optimize your Process with Advanced Process Control

Optimize your Process with Advanced Process Control Honeywell.com 1 Document control number 2014 Honeywell Users Group Europe, Middle East and Africa Optimize your Process with Advanced Process Control Richard Salliss, Honeywell Honeywell Proprietary Agenda

More information

The Use of MDEA and Mixtures of Amines for Bulk CO 2. Removal

The Use of MDEA and Mixtures of Amines for Bulk CO 2. Removal Page 1 of 9 The Use of MDEA and Mixtures of Amines for Bulk Removal JERRY A. BULLIN, JOHN C. POLASEK, Bryan Research & Engineering, Inc., Bryan, Texas STEPHEN T. DONNELLY, Propak Systems, Inc., Lakewood,

More information

Crude Vacuum Tower Wash Bed Optimization

Crude Vacuum Tower Wash Bed Optimization A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 69, 2018 Guest Editors: Elisabetta Brunazzi, Eva Sorensen Copyright 2018, AIDIC Servizi S.r.l. ISBN 978-88-95608-66-2; ISSN 2283-9216 The Italian

More information

Removal of Heat Stable Salts A Solution to Amine Plant Operational Problems

Removal of Heat Stable Salts A Solution to Amine Plant Operational Problems Removal of Heat Stable Salts A Solution to Amine Plant Operational Problems Chemical Engineering in Petroleum & Natural Gas Journal, China, December 2002 J. Shao, Technical Marketing Specialist, Eco-Tec

More information

ADVANCED PROCESS CONTROL

ADVANCED PROCESS CONTROL CHAPTER-11 ADVANCED PROCESS CONTROL Chapter No 11 Page No 1 INTRODUCTION The traditional control philosophy, what is called instrumentation in the chemical industries, is based on single loop control (sometimes

More information

Design of Extraction Column Methanol Recovery System for the TAME Reactive Distillation Process

Design of Extraction Column Methanol Recovery System for the TAME Reactive Distillation Process Design of Extraction Column Methanol Recovery System for the TAME Reactive Distillation Process Muhammad A. Al-Arfaj * Chemical Engineering Department King Fahd University of Petroleum and Minerals, Dhahran,

More information

Simple Dew Point Control HYSYS v10. When the simulation is set up the overall PFD should look like the following figure.

Simple Dew Point Control HYSYS v10. When the simulation is set up the overall PFD should look like the following figure. Simple Dew Point Control HYSYS v10 Steps to set up a simulation in HYSYS v10 to model a simple dew point control system consisting of: Gas chiller Flash separator Liquid stabilizer with gas recycle & compression

More information

OPERATION SKILLS ENHANCEMENT-MEASUREMENT & INSTRUMENT FOR PROCESS VARIABLES

OPERATION SKILLS ENHANCEMENT-MEASUREMENT & INSTRUMENT FOR PROCESS VARIABLES Training Title OPERATION SKILLS ENHANCEMENT-MEASUREMENT & INSTRUMENT FOR PROCESS VARIABLES Training Duration 5 days Training Venue and Dates REF PE015 Operation Skills Enhancement -Measurement & Instrument

More information

Identification of the Internal Condition of Crude Oil Distillation Unit Using Gamma Column Scanning Technique

Identification of the Internal Condition of Crude Oil Distillation Unit Using Gamma Column Scanning Technique Identification of the Internal Condition of Crude Oil Distillation Unit Using Gamma Column Scanning Technique ID-34, B13-05 Moe Phyu Hlaing, Khin Ye Lwin Division of Atomic Energy Department of Research

More information

Separations and Reaction Engineering Spring Design Project. Production of Acetone

Separations and Reaction Engineering Spring Design Project. Production of Acetone Process Objective Function Separations and Reaction Engineering Spring 2000 Design Project Production of Acetone We would like to complete our investigation of the economic feasibility of producing 15,000

More information

PE013: Advanced Distillation- Column, Operation, Control and Troubleshooting

PE013: Advanced Distillation- Column, Operation, Control and Troubleshooting PE013: Advanced Distillation- Column, Operation, Control and Troubleshooting PE013 Rev.001 CMCT COURSE OUTLINE Page 1 of 6 Training Description: The success of every company depends of each employee's

More information

Spring 2010 ENCH446 Project 1

Spring 2010 ENCH446 Project 1 Spring 2010 ENCH446 Project 1 Raymond A. Adomaitis March 8, 2010 To be covered: Class syllabus (http://www.isr.umd.edu/ adomaiti/ench446), grading Team selection (4 members per team) Initial project description

More information

A Case Study in Refinery Energy Improvement

A Case Study in Refinery Energy Improvement A Case Study in Refinery Energy Improvement Chevron El Segundo Refinery John Walter KBC Advanced Technologies, Inc Texas Technology Showcase 2006 Galveston, TX El Segundo Energy Goals & Objectives Current

More information

When Pressure Becomes a Reliable Energy Source:

When Pressure Becomes a Reliable Energy Source: SERVICE REGION North America ERI PRODUCT DIVISION Oil & Gas When Pressure Becomes a Reliable Energy Source: A white paper on how a South Texas gas plant saves energy using IsoBoost Energy Recovery System.

More information

Simple Dew Point Control HYSYS v8.6

Simple Dew Point Control HYSYS v8.6 Simple Dew Point Control HYSYS v8.6 Steps to set up a simulation in HYSYS v8.6 to model a simple dew point control system consisting of: Gas chiller Flash separator Liquid stabilizer with gas recycle &

More information

The influence of rectification sharpness on the quality of motor fuels

The influence of rectification sharpness on the quality of motor fuels Energy Production and Management in the 21st Century, Vol. 2 833 The influence of rectification sharpness on the quality of motor fuels M. S. Rogalev & R. Z. Magaril Department of Oil and Gas Processing,

More information

Steam System Asset Management. for the Oil, Petrochemical, and Chemical Industries

Steam System Asset Management. for the Oil, Petrochemical, and Chemical Industries Steam System Asset Management for the Oil, Petrochemical, and Chemical Industries In the oil, petrochemical and chemical (OPC) industries, steam system reliability is critical. The huge array of processing

More information

IMPLEMENTATION OF MPC ON A DEETHANIZER AT KÅRSTØ GAS PLANT. Elvira Marie B. Aske,, Stig Strand Sigurd Skogestad,1

IMPLEMENTATION OF MPC ON A DEETHANIZER AT KÅRSTØ GAS PLANT. Elvira Marie B. Aske,, Stig Strand Sigurd Skogestad,1 IMPLEMENTATION OF MPC ON A EETHANIZER AT KÅRSTØ GAS PLANT Elvira Marie. Aske,, Stig Strand Sigurd Skogestad, epartment of Chemical Engineering, Norwegian University of Science and Technology, N-749 Trondheim,

More information

Studying Effect of Feed Vapor Fraction on Consumption Energy in Distillation Process

Studying Effect of Feed Vapor Fraction on Consumption Energy in Distillation Process Studying Effect of Feed Vapor Fraction on Consumption Energy in Distillation Process Shymma Kadhem Rahem School of Chemical engineering, Babylon University, Hilla, Iraq. * E-mail of the corresponding author:

More information

Distillation Operation, Control, Design and Troubleshooting Course for Maintenance Personnel

Distillation Operation, Control, Design and Troubleshooting Course for Maintenance Personnel Page 1 of 8 Distillation Operation, Control, Design and Troubleshooting Course for Maintenance Personnel Introduction The success of every company depends of each employee's understanding of the business's

More information

Crude scheduling in refinery operations

Crude scheduling in refinery operations Crude scheduling in refinery operations Srinivasan R. 1, Karimi I.A. 2, Adhitya A. 3 Department of Chemical and Environmental Engineering, National University of Singapore 10 Kent Ridge Crescent, Singapore

More information

CCR MEG RECLAIMING TECHNOLOGY: FROM MOBILE UNITS TO THE LARGEST RECLAIMING UNIT IN THE WORLD

CCR MEG RECLAIMING TECHNOLOGY: FROM MOBILE UNITS TO THE LARGEST RECLAIMING UNIT IN THE WORLD CCR MEG RECLAIMING TECHNOLOGY: FROM MOBILE UNITS TO THE LARGEST RECLAIMING UNIT IN THE WORLD Jérémie Esquier, Terry Trofimuk & Steven Ayres PROSERNAT Paris, France PROSERNAT Mr Jérémie Esquier - Business

More information

Bulk petrochemical manufacturing is a highly competitive

Bulk petrochemical manufacturing is a highly competitive Originally appeared in: April 2012, pgs 1-5. Used with permission. Optimize olefin operations This operating company used process models to find solutions to poor separation performance K. Romero, Pequiven

More information

Cost-Effective Refinery Expansion Enables Lighter Crude While Maximizing ULSD

Cost-Effective Refinery Expansion Enables Lighter Crude While Maximizing ULSD Cost-Effective Refinery Expansion Enables Lighter Crude While Maximizing ULSD Presented to: AFPM 2015 Annual Meeting March 24, 2015 By James W. Jones Page 1 Introduction Delek Refining is on the verge

More information