PROCESS ECONOMICS PROGRAM SRI INTERNATIONAL Menlo Park, California

Similar documents
PROCESS ECONOMICS PROGRAM

PROCESS ECONOMICS PROGRAM

PEP Review ON-PURPOSE BUTADIENE PRODUCTION By Richard Nielsen with a Contribution by Russell Heinen (June 2011)

Abstract Process Economics Program Report No. 158A OCTANE IMPROVERS FOR GASOLINE (February 1992)

IHS CHEMICAL PEP Report 29J. Steam Cracking of Crude Oil. Steam Cracking of Crude Oil. PEP Report 29J. Gajendra Khare Principal Analyst

CONTENTS 1 INTRODUCTION SUMMARY 2-1 TECHNICAL ASPECTS 2-1 ECONOMIC ASPECTS 2-2

Abstract Process Economics Program Report 222 PETROLEUM INDUSTRY OUTLOOK (July 1999)

THE OIL & GAS SUPPLY CHAIN: FROM THE GROUND TO THE PUMP ON REFINING

Abstract Process Economics Program Report No. 203 ALKANE DEHYDROGENATION AND AROMATIZATION (September 1992)

OCTANE THE NEW ECONOMICS OF. What Drives the Cost of Octane and Why Octane Costs Have Risen Since 2012 T. J. HIGGINS. A Report By:

Study on Relative CO2 Savings Comparing Ethanol and TAEE as a Gasoline Component

Investment Planning of an Integrated Petrochemicals Complex & Refinery A Best Practice Approach

Maximizing Refinery Margins by Petrochemical Integration

Consulting and Training Services Available to the Petroleum Industry

Process Economics Program

Conversion Processes 1. THERMAL PROCESSES 2. CATALYTIC PROCESSES

ETHYLENE-PROPYLENE PROCESS ECONOMICS PROGRAM. Report No. 29A. Supplement A. by SHIGEYOSHI TAKAOKA With contributions by KIICHIRO OHYA.

Changes to America s Gasoline Pool. Charles Kemp. May 17, Baker & O Brien, Inc. All rights reserved.

CHEMSYSTEMS. Report Abstract. Petrochemical Market Dynamics Feedstocks

Renewable Liquids as Steam Cracker Feedstocks

Petroleum Refining Fourth Year Dr.Aysar T. Jarullah

Abstract PEP Review PROCESS ECONOMICS OF COAL-BASED OLEFINS PRODUCTION IN CHINA By R. J. Chang and Jamie Lacson (May 2012)

Process Economics Program

ACO TM, The Advanced Catalytic Olefins Process

CHAPTER 2 REFINERY FEED STREAMS: STREAMS FROM THE ATMOSPHERIC AND VACUUM TOWERS

REFINING PETROCHEMICALS INTEGRATION

IHS CHEMICAL Light Hydrocarbon and Light Naphtha Utilization. Process Economics Program Report 297. Light Hydrocarbon and Light Naphtha Utilization

Report No. 35 BUTADIENE. March A private report by the PROCESS ECONOMICS PROGRAM STANFORD RESEARCH INSTITUTE I PARK, CALIFORNIA

Acombination. winning

On-Line Process Analyzers: Potential Uses and Applications

Abstract Process Economics Program Report 21F NEW GENERATION OXO ALCOHOLS (October 2012)

Refining/Petrochemical Integration A New Paradigm. Anil Khatri, GTC Technology Coking and CatCracking Conference New Delhi - October 2013

Seeing is believing:

Challenges and Opportunities in Managing CO 2 in Petroleum Refining

Abstract Process Economics Program Report 195A ADVANCES IN FLUID CATALYTIC CRACKING (November 2005)

Refinery / Petrochemical. Integration. Gildas Rolland

PEP Review METHYL TERTIARY BUTYL ETHER PRODUCTION FROM STEAM CRACKER C 4 STREAM By Syed N. Naqvi (December 2012)

Bottom of Barrel Processing. Chapters 5 & 8

Light Olefins Market Review. Bill Hyde, Senior Director Olefins and Elastomers Foro Pemex Petroquimica June 7, 2012

Enhance Naphtha Value and Gasoline Reformer Performance Using UOP s MaxEne TM Process

Fischer-Tropsch Refining

A new simple and robust process FT-NIR Spectrometer with small footprint and extended maintenance interval

Using Pyrolysis Tar to meet Fuel Specifications in Coal-to-Liquids Plants

Abstract Process Economics Program Report 43D MEGA METHANOL PLANTS (December 2003)

Refining/Petrochemical Integration-A New Paradigm Joseph C. Gentry, Director - Global Licensing Engineered to Innovate

Schwechat Refinery Visit

PCE154. Refinery Process and Products. H.H. Sheikh Sultan Tower (0) Floor Corniche Street Abu Dhabi U.A.E

Refining/Petrochemical Integration-A New Paradigm

REFINING SOLUTIONS IN A CHANGING WORLD RFG, RFS, SULFUR, BENZENE, TIER 3 AND BEYOND

GULFTRONIC SEPARATOR SYSTEMS

Alkylation & Polymerization Chapter 11

GTC TECHNOLOGY WHITE PAPER

Fig:1.1[15] Fig.1.2 Distribution of world energy resources. (From World Energy Outlook 2005, International Energy Agency.)[16,17]

MERTC 23 rd 24 th January, 2017 Manama, Kingdom of Bahrain

Supporting Information for: Economic and Environmental Benefits of Higher-Octane Gasoline

AN ECONOMIC ASSESSMENT OF THE INTERNATIONAL MARITIME ORGANIZATION SULPHUR REGULATIONS

KBR Technology Business

Mr. Joseph C. Gentry. Director, Global Licensing GTC Technology US, LLC USA

A New Proxy for Coking Margins Forget the Crack Spread

Potential Environmental and Economic Benefit s of Higher-Oct ane Gasoline

Crude Distillation Chapter 4

Boron-Based Technology: An Innovative Solution for Resid FCC Unit Performance Improvement

SOLVENT DEASPHALTING OPTIONS How SDA can increase residue upgrading margins

Fundamentals of Petroleum Refining Refinery Products. Lecturers: assistant teachers Kirgina Maria Vladimirovna Belinskaya Natalia Sergeevna

ON-PURPOSE PROPYLENE FROM OLEFINIC STREAMS

Abu Dhabi International Downstream Summit 2017 Downstream optimization: role of technology, integration and industrial gases. Dr.Ch.

Ethylene US Margin Report Methodology

Challenges for proper implementation of residue upgrading processes within oil refineries

Preface... xii. 1. Refinery Distillation... 1

GCC CATALYST MARKET. (Saudi Arabia, UAE, Kuwait, Qatar, Bahrain) Prepared for XXXX

Catalytic Reforming for Aromatics Production. Topsoe Catalysis Forum Munkerupgaard, Denmark August 27 28, 2015 Greg Marshall GAM Engineering LLC 1

Eni Slurry Technology:

FUTURE SUPPLIES OF PARAXYLENE FEEDSTOCK

Roles of Emerging FCC-based Technologies in Shifting to Petrochemicals Production

Middle East DownStream Weak May 2013 ABU DHABI, UAE

Modernization of Libyan Oil Refineries and Petrochemical Plants

Changing Refinery Configuration for Heavy and Synthetic Crude Processing

The Petrochemical Industry From Middle Eastern Perspective?

Replacing the Volume & Octane Loss of Removing MTBE From Reformulated Gasoline Ethanol RFG vs. All Hydrocarbon RFG. May 2004

PILOT PLANT DESIGN, INSTALLATION & OPERATION Training Duration 5 days

HOW OIL REFINERIES WORK

Coking and Thermal Process, Delayed Coking

HOW OIL REFINERIES WORK

Converting Visbreakers to Delayed Cokers - An Opportunity for European Refiners

Petroleum Refining-Production Planning, Scheduling and Yield Optimization

Unit 1. Naphtha Catalytic Reforming. Assistant lecturers Belinskaya Nataliya Sergeevna Kirgina Maria Vladimirovna

Innovative Solutions for Optimizing Refining & Petrochemicals Synergies. Jean-Paul Margotin

Implications Across the Supply Chain. Prepared for Sustainableshipping Conference San Francisco 30 September 2009

exactly the same savings in investment cost much faster overall construction profitability

THE CHANGING WORLD OF RAW MATERIALS: IMPACT OF ADHESIVES AND COATINGS. Ingrid Brase

Molecular Sieves Application Guide for the Natural Gas Industry Molecular Sieve Molecular Sieve Recommendations

The Greener FCC Moving from Fuels to Petrochemicals

Crude to Chemicals. Opportunities and Challenges of an Industry Game-Changer. MERTC, Bahrain. January 23, 2017

Impact of a changing global landscape

UTILIZING CHEAP GAS TO MAXIMIZE REFINERY PROFITS IN NORTH AMERICA. Daniel B Gillis and Ujjal K Mukherjee, Chevron Lummus Global Gary M Sieli, CB&I

REFORMATE Crude Condensate Naphtha Ethane Reformate

GTC TECHNOLOGY. GT-BTX PluS Reduce Sulfur Preserve Octane Value - Produce Petrochemicals. Engineered to Innovate WHITE PAPER

HOW OIL REFINERIES WORK

REFINING ECONOMICS OF A SINGLE OCTANE. For. The Alliance of Automobile Manufacturers. MathPro Inc. P.O. Box West Bethesda, Maryland

Refinery Maze Student Guide

Transcription:

PROCESS ECONOMICS PROGRAM SRI INTERNATIONAL Menlo Park, California Abstract Process Economics Program Report No. 169 REFINERY/CHEMICALS INTERFACE (January 1985) Demand for most major refinery products is declining throughout the industrialized world, and refining capacity, particularly that upstream, is already underutilized. At the same time, crude slates are becoming progressively heavier and there is a general trend toward removal of lead from the gasoline pool. In contrast with the demand in the refining industry, the demand for the major olefins--ethylene and propylene--will increase significantly over the next decade. At the same time, In the United States in particular, availability of natural gas liquids--currently the predominant olefins source--will decline or at best remain static. To some extent these trends conflict. The first purpose of this study, therefore, is their quantification. Of particular interest to the hydrocarbons Industry is the effect these trends will have on refinery capacity utilization and on the availability, production cost, and transfer price of petrochemical feedstocks and coproducts. The tendency In the United States toward heavier feedstocks suggests possible economic advantages In integrating new olefins production into existing underutilized refineries. This study examines all of these topics in depth. PEP'83 DG

Report No. 169 REFINERY/CHEMICALS INTERFACE by DONALD GREENAWAY I I f-z 0 m A private report by the January 1985 PROCESS ECONOMICS PROGRAM Menlo Park, California 94025

For detailed marketing data and information, the reader is referred to one of the SRI programs specializing in marketing research. The CHEMICAL ECONOMICS HANDBOOK Program covers most major chemicals and chemical products produced in the United States and the WORLD PETROCHEMICALS Program covers major hydrocarbons and their derivatives on a worldwide basis. In addition, the SRI DIRECTORY OF CHEMICAL PRODUCERS services provide detailed lists of chemical producers by company, product, and plant for the United States and Western Europe.

CONTENTS 1 INTRODUCTION........................ 2 MAJOR CONCLUSIONS AND SUMMARY............... 3 The Problem... 4 The Products--Major Refinery Trends... 4 The Products --Ethylene and Propylene... 5 The Feedstocks... 6 The Existing Operable Conversion Refineries... 8 Refining Trends... 9 Producing Petrochemical Feedstock in 1993... :t Feedstock Comparisons--Existing Flexible Plants... Feedstock Comparisons--New Plants... 16 Integrated Facilities... 18 Variable Cost Analysis... '1; New Units... Logistics of Integration... 21 3 INSTALLED CAPACITY..................... 23 U.S. Refining Capacity... 23 U.S. Ethylene Capacity... 25 4 SUPPLY AND DEMAND TRENDS................. 29 Major Refinery Products........ 29 Gasoline............... 29 Middle Distillates.......... 32 Residual Fuel Oil and Coke...... 33 Summary of Product Slate Changes... 33 Crude Oil Supply and Price....... 34 Major Olefins............. 38 Ethylene.............. 38 Propylene.............. 39 Butadiene.............. 41 Olefins Feedstocks........... 43 5 REFINING OPERATIONS... 53 Refinery Processes... 55 Primary Fractionation... 55 Conversion Processing... 57 Fluid Catalytic Cracking... 57 Alkylation... 58 Hydrocracking... 59 1 iii

CONTENTS 5 REFINING OPERATIONS (continued) Catalytic Reforming... Isomerization... Use of Butanes in Gasoline... Thermal Processes... Refinery Operations in 1993... Operations in General... Sensitivity to Octane... Sensitivity to Additives... Sensitivity to Heavier Crudes... Refinery Propylene... Refinery Economics... Petrochemical Feedstock Production... 6 OLEFINS OPERATIONS... Process Background... Pyrolysis and Cooling... Compression and Acid Gases Removal... Subcooling and Products Separation... Refrigeration Pyrolysis Gasoline Hydrotreating... Butadiene Recovery... Feedstock Comparisons... Medium Severity Operations--Feeds and Products... Medium Severity Operations--Economic Comparisons... High Severity Operations... New Plant Operations... Single-Feedstock Plants... Flexible-Feedstock Plants... Seasonal Effects... Benefits of Integration... Existing Units... Integrated Facilities (New Units)... Logistics of Integration... Factors Influencing Future Olefins Prices... 59 60 61 61 62 64 68 70 74 77 79 86 95 97 97 99 99 100 100 101 101 101 102 106 107 107 112 114 118 118 122 125 134 iv

ILLUSTRATIONS 4.1 Historical U.S. Refining Trends... 30 4.2 Historic and Forecast U.S. Refining Trends... 31 4.3 1993 Olefins Production Feedstock Sensitivity... 50 5.1 Block Flow Diagram of Refinery Flow Sheet... 141 5.2 Projected Effect of Isomerization Throughput on Reforming Severity in 1993... 66 5.3 1982/1993 Refinery Operations Flow Sheet... 143 5.4 Projected Effect of Crude Oil Gravity on Flexicoking Requirement in 1993... 76 6.1 Block Flow Diagram of Ethylene Unit... 98 6.2 Feed Comparison New Feed-Specific Olefins Units... 113 6.3 Feed Comparison New Feed-Flexible Olefins Units... 115 6.4 1993 Integrated Operations (Refinery) Flow Sheet... 145 6.5 1993 Integrated Operations (Olefins Production) Flow Sheet... 147 6.6 Economics of New-Built Olefins Units Integrated vs. Independent Facilities... 126 6.7 1993 Ethylene Price Sensitivity... 139

TABLES 2.1 Highlights of Projected 1993 Refinery Operations... 10 2.2 Medium Severity Operations Highlights of Olefins Feedstock Comparison... 12 2.3 High Severity Operations Main Effects of Supplementary Feedstock... 15 2.4 Comparison of Projected 1993 Olefin Feedstock Values and Prices.... 17 2.5 Highlights of 1993 Integrated Operations... 19 3.1 Total Refinery Capacity in the United States, End-1982... 24 3.2 Conversion Refinery Capacity in the United States, End-1982... 26 3.3 Ethylene Olefins Capacity in the United States, End-1982... 27 4.1 Major U.S. Refinery Products, 1993 versus 1982... 33 4.2 U.S. Crude Imports by Source, 1983 versus 1979... 34 4.3 Free World Oil Reserves and Current Production... 36 4.4 Projected Spot Prices for Saudi Arabian Light Crude, F.O.B. Saudi Arabia... 37 4.5 Breakdown of Ethylene Demand, 1993 versus 1982... 39 4.6 Feeds and Product Trends, U.S. Olefins Units, 1993 versus 1982... 48 5.1 Projected Refinery Operations in 1993... 65 5.2 Projected Effect of Octane of Premium Gasoline on 1993 Refinery Operations... 69 5.3 Projected Effect of Additions of 500 BPCD each of Ethanol, MTBE, and Oxinol on 1993 Refinery Operations... 73 5.4 Projected Effect of Heavier Crude Oil Slate on 1993 Refinery Operations... 75 5.5 Projected Effect of Propylene Production on 1993 Refinery Operations... 78 5.6 Prices of Major Refinery Products on U.S. Gulf Coast... 80 5.7 Profitability of Hypothetical U.S. Refinery in 1982... 82 Vii

TABLES 5.8 Profitability of Hypothetical U.S. Refinery in 1993... 84 5.9 Incremental Petrochemical Feedstock Production in 1982.. 88 5.10 Incremental Petrochemical Feedstock Production in 1993.. 89 6.1 Typical Pyrolysis Yields... 96 6.2 Medium Severity Operations Olefins Feedstock Comparison... 103 6.3 Medium Severity Operations Feedstock Break-Even Values... 105 6.4 High Severity Operations Effect of Supplementary Feedstock... 108 6.5 High Severity and Medium Operations Feedstock Break-Even Values... 109 6.6 Economics of New Feedstock Specific Olefins Units... 111 6.7 Economics of Feed-Specific Versus Feed-Flexible Olefins Units... 117 6.8 1993 Integrated Operations... 119 6.9 Major U.S. Refineries... 127 6.10 Louisiana and Texas Refineries... 128 6.11 Operating Parameters for Integrated Refinery/Olefins Plants... 130 6.12 Economics of Integrated Refinery/Olefins Units... 132 6.13 Economics of New Naphtha Crackers... 135 6.14 Propylene Production Cost by Catalytic Dehydrogenation of Propane... 137 viii