Two examples of steady state simulation with HYSYS at GALPenergia Sines Refinery

Size: px
Start display at page:

Download "Two examples of steady state simulation with HYSYS at GALPenergia Sines Refinery"

Transcription

1 Two examples of steady state simulation with HYSYS at GALPenergia Sines Refinery José Egídio Fernandes Inverno 1*, Eurico Correia 2, Pablo Jiménez-Asenjo 3 and Josep A. Feliu 3 1 Galpenergia, Refinaria de Sines, Sines, Portugal 2 Intituto Superior Técnico, Lisboa, Portugal 3 Aspentech Inc, Passeig de Gràcia 56, Barcelona, Spain Abstract This document shows two examples of aplication of a simulation software, in this case HYSYS, to a real situation in an oil refinery: a crude destillation model and a sour water stripper model. Keywords: simulation software, oil refining, crude destillation, sour water stripping 1. Introduction The purpose of this paper is to present the work developed at Sines Refinery in cooperation with the University (Instituto Superior Técnico, Lisbon) regarding the development of models of some process units of GALPenergia SINES Refinery. The work was done during six months and HYSYS was used as simulation tool. Sines Refinery has been using this software for the last 4-5 years with success in solving some small operational problems. The chalenge here was to model a complete process unit in order to allow the optimization of the operation. 2. Crude destillation Unit The crude destillation unit at Sines Refinery is the process unit where the crude oil is first processed in the refinery and is composed by the following equipment: 2 pre-heat trains (each one composed by several heat exchangers, a desalter and a furnace) 1 pre-flash drum 1 main destilation column (a very complex column with several pumparounds and side strippers) 4 secundary fraccionation columns (Deetanizer, debutanizer, naphta splitter and a deisopentanizer) * Author to whom correspondence should be adressed: josé.inverno@galpenergia.com

2 The original model was initially developed in close collaboration with Hyprotech (now Aspentech) some years ago. The objective of the present works was to validate the model, checking all the settings and calibrations, to verify the answer of the model to real operating conditions. The first step for a successfull simulation is a correct choose of the thermodynamic method that will be used in the calculations of the state variables and the physical properties. For the family of compounds that are present in the crude distillation unit process streams, the Peng-Robinson equation of state is normally accepted as adequate. The second step is to correctly characterize the feed composition. Refineries can be feeded with a multiplicity of crude oils and usuallly the feed is not a crude of only one origin but a crude mix that can vary from 3 to 10 diferent crude types. Simulation packages are able to properly characterize petroleum fluids if data from laboratory assays (distillation curves, light end analysis, bulk properties, etc.) is available. How to do it if we don t have this type of data available? Ready-to-use characterized oil crudes from a BP crudes database are available in another commercial software (KBC s Petrofine with CAMS) leased by GALPenergia. This software doesn t use rigorous thermodynamic models but is used to simulate all the refinery for schedulling and blending proposes.the results of generating a crude slate with this software is a huge table with all types of data (SG, S, V, Ni, UOPK, viscosities, etc.) for 75 different components (22 pure light components and 53 heavier pseudo components separated trough different cut points). All this data can be used to feed the model developed in HYSYS and check the correct characterization of the quality of the feed. However, using a database and not current crude data, has the inherent problem of ignoring the properties variability of the real crude extracted from fields. When observing mismatches between simulated and real plant data there will always remain the doubt if the cause is a modelization mistake in the process or a wrong (outdated) feed characterization. A back-blending procedure would have been as well possible in case assays from the distillation column products whould have been available. Using the distillation curves, the bulk properties and the light end analysis obtained from the column products, HYSYS could have back-generated the original crude entering the column by leveraging the properties as a function of the products flows leaving the column. In any case, using the crude database, we have obtained a good agreement between the crude column simulation and the real data obtained from the process. At the end of the paper, the Figure 1 shows the general arrangement of the unit operations in the simulation of this unit. In the Table 1 we can compare the results of the simulation with the real data obtained. For the case study we have used the 10 of June 2003 operating data. In this day the refinery treated a crude mix composed by 4 different crudes (Es Sider, Qua Iboe, Sahran Blend and Marlin). We can compare the column temperature profile and also some products properties (SG Specific gravity and 5 an 95 v/v % ASTM D86 distillation temperatures). From the table we can see that we have obtained a good agreement between the crude column simulation and the real data obtained from the process.

3 Table 1 Differences between the real operation and the simulation. Real Simulation Units (1) (2) (1)-(2) Column temperature profile Overhead Temp ºC % Tray 03 Temp ºC % Tray 15 Temp ºC % Tray 19 Temp ºC % Tray 26 Temp ºC % Tray 30 Temp ºC % Tray 35 Temp ºC % Tray 39 Temp ºC % Tray 43 Temp ºC % Bottoms Temp ºC % T Pumparound Naphtha ºC % T Pumparound LGO ºC % T Pumparound HGO ºC % Products properties Naphtha 95% ºC % Naphtha SG kg/m % Light Gasoil 95% ºC % Light Gasoil 5% ºC % Light Gasoil SG kg/m % Heavy Gasoil 95% ºC % Heavy Gasoil 5% ºC % Heavy Gasoil SG kg/m % Atmospheric Residue 5% ºC % Atmospheric Residue SG kg/m % 3. Sour Water stripper In many refinery units water or steam is injected to facilitate the process. This water is usually separated and collected in the boots of the overhead receivers of the destillation columns or in other type of receivers where the separation between water and hydrocarbons can be enhanced.the drawback of injecting water into the refinery processes is that it strips the acid soluble gases, NH 3 and H 2 S, generating sour water streams The objective of the sour water stripper is to reuse the recovered water in other refinery processes and to remove almost all the H 2 S and NH 3 present, mainly because environmental reasons.

4 If by any reason the water cannot be reused, and these two gases are not substantially removed the sour water needs to be sent to a wastewater treatment plant where the treatment to remove this type of contaminants can be finally performed but with a very high cost. With the information that in the existing installation the NH 3 removal was not effective, we used the simulation software to simulate the column (Sour Water Stripper) to find out what would be the best operating conditions in terms of column temperature, pressure, and stripping steam in order to maximize the removal of NH 3 from water. For this simulation, and because the type of compounds present is not the same than in the crude distillation column, it is necessary to use another thermodynamic method. For sour systems, due to the presence of H 2 S and NH 3 there are some adequate thermodynamic methods present in HYSYS database (the Sour options of the SRK and PR equations of state as well as the Stryjek Vera modification of the PR). Finally, for data availability, it was decided to use the Peng Robinson Stryjek Vera [PRSV] equation of state The tests performed using the column model in HYSYS have concluded that to have a better NH 3 removal the operating temperatures should be increased, pressures decreased and the stripping steam flow optimised. Graphs 1 and 2 show the relationship between the pressure, temperature and steam flow in the level of NH 3 in the stripped water Overhead P: 2bar Overhead P: 2.5bar Ammonia (ppm) Steam flow (t/h) Graph 1- Ammonia in stripped water as a function of stripping steam flow

5 Overhead P: 2bar Overhead P: 2.5bar 84 Ammonia (ppm) Column overhead temperature (ºC) Graph 2 - Ammonia in treated water as a function of the overhead temperature The real plant column has been adjusted using the results obtained trough HYSYS simulation. The increase in column performance obtained has supposed company savings both in raw water consumption and in the waste water treatment plant. Figure 2 shows the general arrangement of the unit operations in the simulation of this unit 4. Conclusions Simulation software is a very good tool for the process industry, not only at the level of conceptual design but also during the entire lifecycle of the equipment, were it can be very useful for performance, debottlenecking and process studies. The presented results have been obtained using the steady state version of the software, but all the simulations done in steady state can have an evolution to a dynamic simulation (for example to build process simulators for operator training or to study the behaviour of the process units in transient conditions), or to a real time optimisation system where, together with the advanced process control tools, can be very profitable in the optimisation of the operation in real time.

6 Figure 1 Crude distillation column diagram Figure 2 Sour water stripper diagram

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

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

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

Aspen HYSYS Property Packages

Aspen HYSYS Property Packages Aspen HYSYS Property Packages Overview and Best Practices for Optimum Simulations Aspen Process Engineering Webinar October 17, 2006 Aspen HYSYS Property Packages Maria Jesus Guerra, PhD Director, Business

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

FAQ: Modeling Heavy Oils Using Aspen HYSYS

FAQ: Modeling Heavy Oils Using Aspen HYSYS FAQ: Modeling Heavy Oils Using Aspen HYSYS 2010 Aspen Technology, Inc. AspenTech, aspenone, and the Aspen leaf logo are trademarks or registered trademarks of Aspen Technology, Inc. All rights reserved.

More information

A crude oil refinery is an industrial process plant where crude oil is processed and refined into different petroleum products (i.e.

A crude oil refinery is an industrial process plant where crude oil is processed and refined into different petroleum products (i.e. A crude oil refinery is an industrial process plant where crude oil is processed and refined into different petroleum products (i.e. gasoline, diesel, kerosene, jet fuel) This figure shows a typical refinery

More information

Heat Exchanger Network Optimization using integrated specialized software from ASPENTECH and GAMS Technology.

Heat Exchanger Network Optimization using integrated specialized software from ASPENTECH and GAMS Technology. EngOpt 2012 3 rd International Conference on Engineering Optimization Rio de Janeiro, Brazil, 01-05 July 2012. Heat Exchanger Network Optimization using integrated specialized software from ASPENTECH and

More information

ProMax. Use It. Love It. Bryan Research & Engineering, Inc. BR&E. with TSWEET & PROSIM Process Simulation Software

ProMax. Use It. Love It. Bryan Research & Engineering, Inc. BR&E. with TSWEET & PROSIM Process Simulation Software ProMax with TSWEET & PROSIM Process Simulation Software Use It. Love It. ProMax is a powerful Microsoft Windows based process simulation package for use in gas processing, oil refining and chemical facilities.

More information

Sulsim Sulfur Recovery in Aspen HYSYS V9 A Brief Tutorial for Using and Optimizing Your Sulfur Recovery Unit in Aspen HYSYS

Sulsim Sulfur Recovery in Aspen HYSYS V9 A Brief Tutorial for Using and Optimizing Your Sulfur Recovery Unit in Aspen HYSYS Sulsim Sulfur Recovery in Aspen HYSYS V9 A Brief Tutorial for Using and Optimizing Your Sulfur Recovery Unit in Aspen HYSYS Jump Start Guide Chad Mondor, Product Management, Aspen Technology, Inc. Jennifer

More information

USING OLI TO DESIGN SOLUTION TO MINIMIZE THE CORROSION OF CRUDE DISTILLATION TOWERS

USING OLI TO DESIGN SOLUTION TO MINIMIZE THE CORROSION OF CRUDE DISTILLATION TOWERS USING OLI TO DESIGN SOLUTION TO MINIMIZE THE CORROSION OF CRUDE DISTILLATION TOWERS Benoit ALBINET TOTAL, Belgium Sheyla Camperos TOTAL, France Rasika Nimkar OLI THE ISSUE More and more crude oil contains

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

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

CONTROL OF CRUDE FRACTIONATOR PRODUCT QUALITIES DURING FEEDSTOCK CHANGES BY USE OF A SIMPLIFIED HEAT BALANCE

CONTROL OF CRUDE FRACTIONATOR PRODUCT QUALITIES DURING FEEDSTOCK CHANGES BY USE OF A SIMPLIFIED HEAT BALANCE Petrocontrol Advanced Control & Optimization CONTROL OF CRUDE FRACTIONATOR PRODUCT QUALITIES DURING FEEDSTOCK CHANGES BY USE OF A SIMPLIFIED HEAT BALANCE Y. Zak Friedman, PhD Principal Consultant Paper

More information

Mass Transfer Rate Modeling Basics. Nathan A. Hatcher, P.E. AIChE South Texas Section Dinner Pellazio Banquet Hall, Houston TX September 11, 2014

Mass Transfer Rate Modeling Basics. Nathan A. Hatcher, P.E. AIChE South Texas Section Dinner Pellazio Banquet Hall, Houston TX September 11, 2014 Mass Transfer Rate Modeling Basics Nathan A. Hatcher, P.E. AIChE South Texas Section Dinner Pellazio Banquet Hall, Houston TX September 11, 2014 Outline History of Process Simulation Briefly about the

More information

Model and Optimisation of a Multi-Effect Evaporator of Sugarcane Juice: Energy Consumption and Inversion Losses

Model and Optimisation of a Multi-Effect Evaporator of Sugarcane Juice: Energy Consumption and Inversion Losses Model and Optimisation of a Multi-Effect Evaporator of Sugarcane Juice: Energy Consumption and Inversion Losses Daniela Galatro*, Elisa Verruschi, Roberto Guillen Universidad Nacional Experimental Politécnica

More information

CN4205R Pinch Analysis and Process Integration

CN4205R Pinch Analysis and Process Integration CN4205R Pinch Analysis and Process Integration Sachin V JANGAM Department of Chemical and Biomolecular Engineering National University of Singapore Singapore Email: chejsv@nus.edu.sg Office location: E4-05-46

More information

Challenges for Processing Oil and Gas from Kazakhstan

Challenges for Processing Oil and Gas from Kazakhstan Challenges for Processing Oil and Gas from Kazakhstan Paul Roberts, Les Armstrong WorleyParsons Parkview Great West Road Brentford Middlesex, TW8 9AZ, UK ABSTRACT In recent years WorleyParsons has been

More information

Claus plants. SURE oxygen enrichment portfolio for sulfur recovery in

Claus plants. SURE oxygen enrichment portfolio for sulfur recovery in Refining SURE oxygen enrichment portfolio for sulfur recovery in Claus plants. Covering the full oxygen enrichment range for increased capacity, flexibility and reliability. APPLICATION TECHNOLOGIES O₂

More information

Researcher, 1(2), 2009, Energy Integration Of Crude Distillation Unit Using Pinch Analysis

Researcher, 1(2), 2009,  Energy Integration Of Crude Distillation Unit Using Pinch Analysis Energy Integration Of Crude Distillation Unit Using Pinch Analysis K.R. AJAO (Ph.D) Department of Mechanical Engineering, University of Ilorin, Ilorin, Nigeria e-mail: ajaomech@unilorin.edu.ng H. F. Akande

More information

Integrating Risk-Based Inspection Recommendations with Inspection Programs and Integrity Operating Windows

Integrating Risk-Based Inspection Recommendations with Inspection Programs and Integrity Operating Windows Integrating Risk-Based Inspection Recommendations with Inspection Programs and Integrity Operating Windows Lynne Kaley, PE Principal Trinity Bridge, LLC Savannah, GA W. Clay White Fixed Equipment Network

More information

HIGH PUITY CARBON MONOXIDE FROM A FEED GAS ARNOLD KELLER AND RONALD SCHENDEL KINETICS TECHNOLOGY INTERNATIONAL CORPORATION MONROVIA, CALIFORNIA

HIGH PUITY CARBON MONOXIDE FROM A FEED GAS ARNOLD KELLER AND RONALD SCHENDEL KINETICS TECHNOLOGY INTERNATIONAL CORPORATION MONROVIA, CALIFORNIA THE USE OF COSORB R II TO RECOVER HIGH PUITY CARBON MONOXIDE FROM A FEED GAS BY ARNOLD KELLER AND RONALD SCHENDEL KINETICS TECHNOLOGY INTERNATIONAL CORPORATION MONROVIA, CALIFORNIA PRESENTED AT AICHE SUMMER

More information

Heavy Oil and Bitumen Analytical. Understanding Their Capabilities

Heavy Oil and Bitumen Analytical. Understanding Their Capabilities Heavy Oil and Bitumen Analytical Methods: Understanding Their Capabilities and dlimitationsi i Project Review & Update /COQG Meeting Calgary, Alberta June 24 th, 2008 Project Manager: Bryan Fuhr, ARC (fuhr@arc.ab.ca)

More information

FOULING MONITORING AND CLEANING OPTIMISATION IN A HEAT EXCHANGER NETWORK OF A CRUDE DISTILLATION UNIT

FOULING MONITORING AND CLEANING OPTIMISATION IN A HEAT EXCHANGER NETWORK OF A CRUDE DISTILLATION UNIT FOULING MONITORING AND CLEANING OPTIMISATION IN A HEAT EXCHANGER NETWORK OF A CRUDE DISTILLATION UNIT Andrea Heins 1, Ramón Veiga 1, Carlos Ruiz 2, Andrés Riera 2 1 Argentinean Technology Center (CTA)

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

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

Delayed coking remains the

Delayed coking remains the Delayed coking advances New technologies and procedures for building and upgrading delayed coking facilities are enhancing health, safety and the environment while increasing economic viability Rick Wodnik

More information

Qualitative Phase Behavior and Vapor Liquid Equilibrium Core

Qualitative Phase Behavior and Vapor Liquid Equilibrium Core 2/22/2017 Qualitative Phase Behavior and Qualitative Phase Behavior Introduction There are three different phases: solid, liquid, and gas (vapor) Energy must be added to melt a solid to form liquid If

More information

EXPERIENCE WITH GDS A FIRST PRINCIPLES INFERENTIAL MODEL FOR DISTILLATION COLUMNS

EXPERIENCE WITH GDS A FIRST PRINCIPLES INFERENTIAL MODEL FOR DISTILLATION COLUMNS PETROCONTROL Advanced Control and Optimization EXPERIENCE WITH GDS A FIRST PRINCIPLES INFERENAL MODEL FOR DISLLAON COLUMNS By: Y. Zak Friedman, PhD, New York, NY pertocontrol@earthlink.net Gwilym T. Reedy

More information

Chemistry of Petrochemical Processes

Chemistry of Petrochemical Processes Chemistry of Petrochemical Processes ChE 464 Instructor: Dr. Ahmed Arafat, PhD Office: building 45 room 106 E-mail: akhamis@kau.edu.sa www.kau.edu.sa.akhamis files Book Chemistry of Petrochemical Processes

More information

TKP4170 PROCESS DESIGN. PROJECT

TKP4170 PROCESS DESIGN. PROJECT NTNU Norwegian University of Science and Technology Faculty of Natural Sciences and Technology Department of Chemical Engineering TKP4170 PROCESS DESIGN. PROJECT - Title: Process Design and Economic Investigation

More information

Sridhar Srinivasan June 20, 2017 REAL TIME PREDICTIVE ANALYTICS AND CORROSION MANAGEMENT WITH PREDICT -RT

Sridhar Srinivasan June 20, 2017 REAL TIME PREDICTIVE ANALYTICS AND CORROSION MANAGEMENT WITH PREDICT -RT Sridhar Srinivasan June 20, 2017 REAL TIME PREDICTIVE ANALYTICS AND CORROSION MANAGEMENT WITH PREDICT -RT Speaker Bio Global Business Leader Corrosion Asset Integrity Solutions Honeywell International

More information

Corrosion Potential - Refinery Overhead Systems

Corrosion Potential - Refinery Overhead Systems Corrosion Potential - Refinery Overhead Systems Amit Patel Bartlesville, Oklahoma OLI Simulation Conference November 16-18, 2010 Whippany, NJ Corrosivity Amine Hydrochlorides Impact of overhead corrosion

More information

APPLICATION NOTE. UOP : Analysis of Trace CO and CO 2 in bulk H 2 and Light Gaseous Hydrocarbons by GC

APPLICATION NOTE. UOP : Analysis of Trace CO and CO 2 in bulk H 2 and Light Gaseous Hydrocarbons by GC UOP 63-13: Analysis of Trace CO and CO 2 in bulk H 2 and Light Gaseous Hydrocarbons by GC Fast Analysis in

More information

Conception of a Pulverized Coal Fired Power Plant with Carbon Capture around a Supercritical Carbon Dioxide Brayton Cycle

Conception of a Pulverized Coal Fired Power Plant with Carbon Capture around a Supercritical Carbon Dioxide Brayton Cycle Available online at www.sciencedirect.com Energy Procedia 37 (2013 ) 1180 1186 GHGT-11 Conception of a Pulverized Coal Fired Power Plant with Carbon Capture around a Supercritical Carbon Dioxide Brayton

More information

Steam balance optimisation strategies

Steam balance optimisation strategies Steam balance optimisation strategies Publicado en Chemical Engineering, Noviembre 2002 Background Optimising a steam balance in a plant with several steam mains pressures is not always a simple intuitive

More information

Facilities Cost Estimates Drivers in the Oil and Gas Field Development. By Ruby Aka. Independent Oil and Gas Consultant

Facilities Cost Estimates Drivers in the Oil and Gas Field Development. By Ruby Aka. Independent Oil and Gas Consultant Facilities Cost Estimates Drivers in the Oil and Gas Field Development. By Ruby Aka Independent Oil and Gas Consultant rubyaka@me.com Abstract The paper reviews the drivers of oil and gas cost estimate

More information

Overview. Challenges in Opportunity Crude Processing 16 th April 2012

Overview. Challenges in Opportunity Crude Processing 16 th April 2012 1 Challenges in Opportunity Crude Processing 16 th April 2012 Thomas Lu Industry Development Manager Asia Pacific Overview Opportunity Crude Trends (High TAN Crude) and its challenges Overview of Factors

More information

Stephen M. Patera, Sales Manager, LHI Metals. October 6-9, 2013 Caesars Palace, Las Vegas, Nevada, USA

Stephen M. Patera, Sales Manager, LHI Metals. October 6-9, 2013 Caesars Palace, Las Vegas, Nevada, USA TITANIUM USED IN REFINERIES Presented by Stephen M. Patera LHI Metals Titanium Grades Most Commonly Grade 2 Grade 7 Grade 12 Grade 16 Used in Refineries Corrosive Environments HCl Hydrochloric acid NH₄Cl

More information

Problems at the Cumene Production Facility, Unit 800

Problems at the Cumene Production Facility, Unit 800 Problems at the Cumene Production Facility, Unit 800 Background Cumene (isopropyl benzene) is produced by reacting propylene with benzene. During World War II, cumene was used as an octane enhancer for

More information

PROCESSING NATURAL GAS Leontev A.A. Vladimirskiy State University named after the Stoletov brothers Vladimir, Russia

PROCESSING NATURAL GAS Leontev A.A. Vladimirskiy State University named after the Stoletov brothers Vladimir, Russia PROCESSING NATURAL GAS Leontev A.A. Vladimirskiy State University named after the Stoletov brothers Vladimir, Russia ПЕРЕРАБОТКА ПРИРОДНОГО ГАЗА Леонтьев А.А. Владимирский государственный университет имени

More information

Estimation of Boil-off-Gas BOG from Refrigerated Vessels in Liquefied Natural Gas Plant

Estimation of Boil-off-Gas BOG from Refrigerated Vessels in Liquefied Natural Gas Plant International Journal of Engineering and Technology Volume 3 No. 1, January, 2013 Estimation of Boil-off-Gas BOG from Refrigerated Vessels in Liquefied Natural Gas Plant Wordu, A. A, Peterside, B Department

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

Bitumen Upgrader Residue Conversion to Incremental Synthetic Fuels Products

Bitumen Upgrader Residue Conversion to Incremental Synthetic Fuels Products Bitumen Upgrader Residue Conversion to Incremental Synthetic Fuels Products Technical Paper Expander Energy Inc. Jan Wagner, P.Eng. Steve Kresnyak, P.Eng. Final Issue June 19, 2013 Introduction During

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

APPLYING THE HEAT INTEGRATION IN ORDER TO ENVIRONMENTAL POLLUTANTS MINIMIZATION IN DISTILLATION COLUMNS

APPLYING THE HEAT INTEGRATION IN ORDER TO ENVIRONMENTAL POLLUTANTS MINIMIZATION IN DISTILLATION COLUMNS Iran. J. Environ. Health. Sci. Eng., 6, Vol. 3, No. 4, pp. 73-84 APPLYING THE HEAT INTEGRATION IN ORDER TO ENVIRONMENTAL POLLUTANTS MINIMIZATION IN DISTILLATION COLUMNS * A. H. Javid, A. Emamzadeh, 3 A.

More information

Fluid Mechanics, Heat Transfer, Fluid Mechanics Design Project. Production of Ethanol

Fluid Mechanics, Heat Transfer, Fluid Mechanics Design Project. Production of Ethanol Fluid Mechanics, Heat Transfer, Fluid Mechanics Design Project Production of Ethanol Your assignment is to continue evaluating the details of a process to produce 30,000 tonne/y of ethanol from ethylene.

More information

REAL-TIME PREDICTIVE ANALYTICS AND CORROSION MONITORING WITH PREDICT -RT

REAL-TIME PREDICTIVE ANALYTICS AND CORROSION MONITORING WITH PREDICT -RT Honeywell Technology Summit Kuwait Dr. Slawomir Kus; Ahmed Lofty 4 October 2017 REAL-TIME PREDICTIVE ANALYTICS AND CORROSION MONITORING WITH PREDICT -RT Outlines 1. Corrosion in Refining Industry costs,

More information

Emission-Reductive and Multi-Objective Coordinative Optimization of Binary Feed for Atmospheric and Vacuum Distillation Unit

Emission-Reductive and Multi-Objective Coordinative Optimization of Binary Feed for Atmospheric and Vacuum Distillation Unit Simulation and Optimization China Petroleum Processing and Petrochemical Technology 2017, Vol. 19, No. 4, pp 101-112 December 30, 2017 Emission-Reductive and Multi-Objective Coordinative Optimization of

More information

Top 10 Questions About Aspen Operator Training FAQ

Top 10 Questions About Aspen Operator Training FAQ Top 10 Questions About Aspen Operator Training FAQ 1. What is Aspen Operator Training? In April 2017, AspenTech acquired a copy of the rights to Inprocess Group s operator training simulator (OTS) software.

More information

The Rectisol Process. Lurgi s leading technology for purification and conditioning of synthesis gas

The Rectisol Process. Lurgi s leading technology for purification and conditioning of synthesis gas The Rectisol Process Lurgi s leading technology for purification and conditioning of synthesis gas Capacity installed and operating (in MM Nm3/day) 350 300 250 200 150 100 50 Today, Rectisol purifies 75

More information

OPTIONS FOR REVAMP OF UREA PLANTS

OPTIONS FOR REVAMP OF UREA PLANTS OPTIONS FOR REVAMP OF UREA PLANTS by Federico Zardi, P. Silva UREA CASALE S.A. - Lugano, Switzerland Presented at The Scientific and Practical Conference on the subject of GPO GRODNO-AZOT, Grodno, Republic

More information

Fluid Mechanics, Heat Transfer, Thermodynamics. Design Project. Production of Ammonia

Fluid Mechanics, Heat Transfer, Thermodynamics. Design Project. Production of Ammonia Fluid Mechanics, Heat Transfer, Thermodynamics Design Project Production of Ammonia Your assignment is to continue evaluating the details of a process to produce 50,000 tonne/y of ammonia from a syngas

More information

Separations and Reactors. Acrylic Acid Production via the Catalytic Partial Oxidation of Propylene

Separations and Reactors. Acrylic Acid Production via the Catalytic Partial Oxidation of Propylene Separations and Reactors Acrylic Acid Production via the Catalytic Partial Oxidation of Propylene Process Information Background Acrylic acid (AA) is used as a precursor for a wide variety of chemicals

More information

Modelling of liquid-vapor-solid equilibria in the NH 3 -CO 2 -H 2 O system. Maria G. Lioliou, Statoil ASA

Modelling of liquid-vapor-solid equilibria in the NH 3 -CO 2 -H 2 O system. Maria G. Lioliou, Statoil ASA Modelling of liquid-vapor-solid equilibria in the -CO 2 -H 2 O system Maria G. Lioliou, Statoil ASA Introduction CO 2 capture by amines is state-of-the-art technology Characteristics of a desired technology

More information

Technical Analysis of the Natural Gas to Hydrocarbon Liquid Process

Technical Analysis of the Natural Gas to Hydrocarbon Liquid Process American Journal of Chemical Engineering 2015; 3(2-1): 25-40 Published online May 6, 2015 (http://www.sciencepublishinggroup.com/j/ajche) doi: 10.11648/j.ajche.s.2015030201.14 ISSN: 2330-8605 (Print);

More information

Hydrocarbon processing Separation processes - distillation. English version based on the presentation of István Rabi, held on

Hydrocarbon processing Separation processes - distillation. English version based on the presentation of István Rabi, held on Hydrocarbon processing Separation processes - distillation English version based on the presentation of István Rabi, held on 18.09.2013. Agenda Introduction Distillation Crude oil distillation Goal of

More information

The Use of Reduced Models in the Optimisation of Energy Integrated Processes

The Use of Reduced Models in the Optimisation of Energy Integrated Processes A publication of CHEMICAL ENGINEERING TRANSACTIONS VOL. 35, 2013 Guest Editors: Petar Varbanov, Jiří Klemeš, Panos Seferlis, Athanasios I. Papadopoulos, Spyros Voutetakis Copyright 2013, AIDIC Servizi

More information

Flare minimisation via dynamic simulation. Amarnath Singh, Kuyen Li*, Helen H. Lou, J.R. Hopper, Hardik B. Golwala and Sandesh Ghumare

Flare minimisation via dynamic simulation. Amarnath Singh, Kuyen Li*, Helen H. Lou, J.R. Hopper, Hardik B. Golwala and Sandesh Ghumare Int. J. Environment and Pollution, Vol. 29, Nos. 1/2/3, 2007 19 Flare minimisation via dynamic simulation Amarnath Singh, Kuyen Li*, Helen H. Lou, J.R. Hopper, Hardik B. Golwala and Sandesh Ghumare Chemical

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

Safer, More Efficient Combustion Control for Fired Heaters

Safer, More Efficient Combustion Control for Fired Heaters Safer, More Efficient Combustion Control for Fired Heaters By Julie Valentine, Emerson Electric, Inc. Introduction Fired Heaters are devices used for high-temperature heating. A fired heater is used in

More information

Delayed Coker Blowdown System Water Reuse

Delayed Coker Blowdown System Water Reuse Delayed Coker Blowdown System Water Reuse Presented by Mitch Moloney of ExxonMobil Research & Engineering mitchell.j.moloney@exxonmobil.com Budapest Hungary coking.com October-2017 a This material is not

More information

Material Balances Design Project Manufacture of Diethyl Ether

Material Balances Design Project Manufacture of Diethyl Ether Material Balances Design Project Manufacture of Diethyl Ether Diethyl ether (DEE) is a colorless, highly volatile, flammable liquid with a characteristic odor. It is an important solvent in the production

More information

PROCESS ECONOMICS PROGRAM. Report No by NICK KORENS ROBERT W. VAN SCOY. January private report by the PARK, CALIFORNIA

PROCESS ECONOMICS PROGRAM. Report No by NICK KORENS ROBERT W. VAN SCOY. January private report by the PARK, CALIFORNIA Report No. 110 SYNTHESIS GAS PRODUCTION by NICK KORENS and ROBERT W. VAN SCOY January 1977 A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I MENLO PARK, CALIFORNIA For detailed

More information

Removal of CO2 and H2S using Aqueous Alkanolamine Solusions

Removal of CO2 and H2S using Aqueous Alkanolamine Solusions Removal of CO2 and H2S using Aqueous Alkanolamine Solusions Zare Aliabad, H., and Mirzaei, S. Abstract This work presents a theoretical investigation of the simultaneous absorption of CO 2 and H 2 S into

More information

Nufarm DNBP as a Styrene Polymerization Retarder

Nufarm DNBP as a Styrene Polymerization Retarder Nufarm DNBP as a Styrene Polymerization Retarder DNBP (2,4-dnitro-6-sec butyl phenol) is the most commonly used polymerisation control additive in the distillation of styrene monomer. It is used similarly

More information

Special Report. Plant Design and Engineering

Special Report. Plant Design and Engineering Originally appeared in: December 2012, pgs 38-42. Used with permission. Special Report Plant Design and Engineering In the high-priced, fast-paced capital project environment, failure is costly, while

More information

A Study on Re-liquefaction Process of Boil-off Gas of LCO 2 Transfer Ship

A Study on Re-liquefaction Process of Boil-off Gas of LCO 2 Transfer Ship A Study on Re-liquefaction Process of Boil-off Gas of LCO 2 Transfer Ship Yeongbeom Lee, Sanggyu Lee, Youngsoon Sohn, Kyusang Cha Korea Gas Corporation R&D Division 364, SongDo-Dong, Yeonsu-Gu, Incheon-City,

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

WinSim Inc. Advanced Process Simulation Solutions. NEW! Dynamic Simulation Capability FREE TWO WEEK TRIAL

WinSim Inc. Advanced Process Simulation Solutions. NEW! Dynamic Simulation Capability FREE TWO WEEK TRIAL WinSim Inc. NEW! Dynamic Simulation Capability FREE TWO WEEK TRIAL Advanced Process Simulation Solutions TABLE OF CONTENTS The Value of WinSim 3 Process Simulator Comparison 4 DESIGN II for Windows 5 How

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

REQUIREMENTS OF PIPEUNE SIMULATION: ACCURATELY MODELING TRANSIENT PIPELINE OPERATION

REQUIREMENTS OF PIPEUNE SIMULATION: ACCURATELY MODELING TRANSIENT PIPELINE OPERATION REQUIREMENTS OF PIPEUNE SIMULATION: ACCURATELY MODELING TRANSIENT PIPELINE OPERATION International Pipeline Conference Volume II ASME 1998 IPC1998-2098 Kenneth H. Hanks Director of Marketing, Oil & Gas

More information

Options for Removing Methanol from NGL in an Amine Treater Abstract. Submitted to SOGAT 2017 by:

Options for Removing Methanol from NGL in an Amine Treater Abstract. Submitted to SOGAT 2017 by: Options for Removing Methanol from NGL in an Amine Treater Abstract Methanol is commonly injected into hydrocarbon fluids to inhibit hydrate formation. Bulk methanol removal from a hydrocarbon fluid often

More information

Modelling of CO 2 capture using Aspen Plus for EDF power plant, Krakow, Poland

Modelling of CO 2 capture using Aspen Plus for EDF power plant, Krakow, Poland Modelling of CO 2 capture using Aspen Plus for EDF power plant, Krakow, Poland Vipul Gupta vipul.gupta@tecnico.ulisboa.pt Instituto Superior Técnico,Lisboa, Portugal October 2016 Abstract This work describes

More information

MEASUREMENT AND MODELING METHODOLOGY FOR HEAVY OIL VAPOR PRESSURE. O. Castellanos-Díaz, W. Y. Svrcek, H. W. Yarranton, and M. A.

MEASUREMENT AND MODELING METHODOLOGY FOR HEAVY OIL VAPOR PRESSURE. O. Castellanos-Díaz, W. Y. Svrcek, H. W. Yarranton, and M. A. MEASUREMENT AND MODELING METHODOLOGY FOR HEAVY OIL VAPOR PRESSURE O. Castellanos-Díaz, W. Y. Svrcek, H. W. Yarranton, and M. A. Satyro Department of Chemical and Petroleum Engineering, University of Calgary,

More information

SIMULATION AND SENSITIVITY ANALYSIS OF A MIXED FLUID CASCADE LNG PLANT IN A TROPICAL CLIMATE USING A COMMERCIAL SIMULATOR

SIMULATION AND SENSITIVITY ANALYSIS OF A MIXED FLUID CASCADE LNG PLANT IN A TROPICAL CLIMATE USING A COMMERCIAL SIMULATOR SIMULATION AND SENSITIVITY ANALYSIS OF A MIXED FLUID CASCADE LNG PLANT IN A TROPICAL CLIMATE USING A COMMERCIAL SIMULATOR Gianfranco Rodríguez 1, Fabiana Arias 1, Maria G. Quintas 1, Alessandro Trigilio

More information

THE ROLE OF STAINLESS STEELS IN PETROLEUM REFINING

THE ROLE OF STAINLESS STEELS IN PETROLEUM REFINING THE ROLE OF STAINLESS STEELS IN PETROLEUM REFINING 1 TABLE OF CONTENTS Introduction... 3 Petroleum Refining... 4 Applications for Stainless Steels... 6 Crude Distillation... 6 Fluid Catalytic Cracking...

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

GUIDANCE DOCUMENT April 6, Guidance on Estimating Condensate and Crude Oil Loading Losses from Tank Trucks

GUIDANCE DOCUMENT April 6, Guidance on Estimating Condensate and Crude Oil Loading Losses from Tank Trucks OKLAHOMA DEPARTMENT OF ENVIRONMENTAL QUALITY AIR QUALITY DIVISION GUIDANCE DOCUMENT April 6, 207 SUBJECT: Guidance on Estimating Condensate and Crude Oil Loading Losses from Tank Trucks SECTION I. INTRODUCTION

More information

Simplify APC Tuning and Configuration

Simplify APC Tuning and Configuration WHITE PAPER Simplify APC Tuning and Configuration Advanced Process Control Tushar Singh, APC Product Marketing, Aspen Technology, Inc. Lucas Reis, APC Product Management, Aspen Technology, Inc. Introduction

More information

Determination of Corrosion rates and remaining life of piping using API and ASME standards in oil and gas industries

Determination of Corrosion rates and remaining life of piping using API and ASME standards in oil and gas industries Determination of Corrosion rates and remaining life of using API and ASME standards in oil and gas industries Nibin V Baby 1, Mr. Bibhudatta Paricha 2, Dr. Shailendra J. Naik 3 1ME 2 nd year, Department

More information

Sour Water Stripper Performance in the Presence of Heat Stable Salts

Sour Water Stripper Performance in the Presence of Heat Stable Salts Sour Water Stripper Performance in the Presence of Heat Stable Salts Nathan A. Hatcher Optimized Gas Treating, Inc. 142 Cimarron Park Loop, Suite C Buda, TX 78610 (512) 970-5019 nate.hatcher@ogtrt.com

More information

ReservoirSimulationModelsImpactonProductionForecastsandPerformanceofShaleVolatileOilReservoirs

ReservoirSimulationModelsImpactonProductionForecastsandPerformanceofShaleVolatileOilReservoirs Global Journal of Researches in Engineering: J General Engineering Volume 16 Issue 4 Version 1.0 Type: Double Blind Peer Reviewed International Research Journal Publisher: Global Journals Inc. (USA) Online

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

Latest Development of Lurgi s MPG-technology Update on Hydrogen Unit for NWU Project

Latest Development of Lurgi s MPG-technology Update on Hydrogen Unit for NWU Project Latest Development of Lurgi s MPG-technology Update on Unit for NWU Project U. Wolf, H. Schlichting, S. Walter, Lurgi AG J. Quinn, North West Upgrading Inc. Gasification Technologies Conference 2007 October

More information

Keywords: GTL, Fisher-Tropsch, natural gas, synthesis gas, steam reforming NCPO, auto-thermal reforming. UNESCO EOLSS

Keywords: GTL, Fisher-Tropsch, natural gas, synthesis gas, steam reforming NCPO, auto-thermal reforming. UNESCO EOLSS GASES TO LIQUIDS (GTL) H. K. Abdel-Aal NRC, Cairo, Egypt Keywords: GTL, Fisher-Tropsch, natural gas, synthesis gas, steam reforming NCPO, auto-thermal reforming. Contents 1. Introduction 2. Exploitation

More information

VALUE ENGINEERING IN AN ESCALATING BUSINESS ENVIRONMENT

VALUE ENGINEERING IN AN ESCALATING BUSINESS ENVIRONMENT David Nash, CB&I 3102 East Fifth Street Tyler, Texas 75701 www.cbi.com Prepared for presentation at the NPRA Annual Meeting San Diego, Calif., March 2008 CB&I, March 2008 NPRA shall not be responsible

More information

UniSim Design Suite Release Bulletin

UniSim Design Suite Release Bulletin Connected Plant UniSim Design Suite Release Bulletin Honeywell unveiled UniSim Design Suite R450, the latest major release of Honeywell s process simulation technology. UniSim Design Suite is part of Honeywell

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

4.0 HYDROGEN GENERATION UNIT (PREP) 4.1 INTRODUCTION

4.0 HYDROGEN GENERATION UNIT (PREP) 4.1 INTRODUCTION 4.0 HYDROGEN GENERATION UNIT (PREP) 4.1 INTRODUCTION 4.1.1 PURPOSE The objective of the unit is to produce hydrogen by steam reforming of full range naphtha i.e. C 5-140 O C SR naphtha & coker naphtha

More information

Process Simulation an efficient and capable tool in environmental technology

Process Simulation an efficient and capable tool in environmental technology Process Simulation an efficient and capable tool in environmental technology Author Dipl.-Ing. Wolfgang Schmidt Chemstations Deutschland GmbH Augustastr. 12 D 46483 Wesel Tel. 0281-33991-0, Fax 0281-33991-33

More information

Advanced models in industrial praxis - from process design to process optimization

Advanced models in industrial praxis - from process design to process optimization Advanced models in industrial praxis - from process design to process optimization Georgios K. Folas 1-2011-12-26 Introduction to Statoil We are headquartered in Norway with 30,300 employees worldwide

More information

ARE PRODUCED WATER EMISSION FACTORS ACCURATE?

ARE PRODUCED WATER EMISSION FACTORS ACCURATE? ARE PRODUCED WATER EMISSION FACTORS ACCURATE? Kyle Ross, PhD, PE Bryan Research & Engineering, Inc. Bryan, TX, U.S.A. Abstract Rules of thumb are often used for estimating emissions from Produced Water

More information

Keys to Excellence in the Practice of Process Engineering. An overview by Scott D. Love, P.E. October 2016

Keys to Excellence in the Practice of Process Engineering. An overview by Scott D. Love, P.E. October 2016 Keys to Excellence in the Practice of Process Engineering An overview by Scott D. Love, P.E. October 2016 Outline What is excellence? How do I learn about my process? Learning examples Summary Questions?

More information

Oxygen Enrichment of Sulfur Recovery Units to Boost Capacity, Conserve Capital, and Improve Environmental Performance

Oxygen Enrichment of Sulfur Recovery Units to Boost Capacity, Conserve Capital, and Improve Environmental Performance Oxygen Enrichment of Sulfur Recovery Units to Boost Capacity, Conserve Capital, and Improve Environmental Performance By: Elmo Nasato Uday Parekh Goar Allison Ltd. Air Products and Chemicals, Inc. 2301

More information

Inland Technologies Inc

Inland Technologies Inc Inc Evaluation of the Mono-ethylene Glycol [MEG] Concentrator to Recycle MEG used in Hydrate Prevention March 2007 Document Nr 0035_INL-OPT-REP-001 Client : Inland Technologies Inc Project : Evaluation

More information

Optimisation of Heat-integrated Distillation Schemes Based on Shortcut Analysis, Pinch Analysis and Rigorous Simulation. Abstract

Optimisation of Heat-integrated Distillation Schemes Based on Shortcut Analysis, Pinch Analysis and Rigorous Simulation. Abstract Optimisation of Heat-integrated Distillation Schemes Based on Shortcut Analysis, Pinch Analysis and Rigorous Simulation Mansour Emtir* and Mansour Khalifa Libyan Petroleum Institute, P.O. Box 6431 Tripoli,

More information

Fluid Mechanics, Heat Transfer, Thermodynamics Design Project. Production of Ethylbenzene

Fluid Mechanics, Heat Transfer, Thermodynamics Design Project. Production of Ethylbenzene Fluid Mechanics, Heat Transfer, Thermodynamics Design Project Production of Ethylbenzene We continue to investigate the feasibility of constructing a new, grass-roots, 80,000 tonne/y, ethylbenzene facility.

More information

Filtration Applications for the Refining & Petrochemical Industries

Filtration Applications for the Refining & Petrochemical Industries Refining Petrochemicals Filtration Applications for the Refining & Petrochemical Industries Process Proven Performance Quality Filtration Made Simple Filtration Applications for the Refinery & Petrochemical

More information

Improving H 2 O Measurement in Catalytic Reformer Hydrogen Recycle Streams

Improving H 2 O Measurement in Catalytic Reformer Hydrogen Recycle Streams Improving H 2 O Measurement in Catalytic Reformer Hydrogen Recycle Streams On-line, real-time moisture measurements in catalytic reformer hydrogen recycle gas streams help refineries assess catalyst condition

More information