SimSci APC and Offsites Updates. Rujun Li SimSci by Schneider Electric

Similar documents
The Advantage of Real Atmospheric Distillation using D7345 Test Method. Presented by Jonathan Cole, PAC

Refinery Crude Unit Advanced Control What? Why? How?

On-Line Process Analyzers: Potential Uses and Applications

Richard Salliss & Rakesh Mehta New Approach to Refinery Crude Switch Optimization using Profit Suite and Unisim

Optimal Gasoline Blending

New Residue Up-grading Complex at European Refinery Achieves Euro 5 Specifications

Pre-Owned OIL REFINERY 280,000 bpd FOR SALE AND RELOCATION

Jagdish Rachh, TSC EMEA, 4 th October UniSim Design New Refining Reactors Deep Dive

Mini refinery feasibility study

1. Introduction. 2. Challenges. APC Implementation Case Study Implementing Advanced Process Control on Hydrocracker Unit 1

CRUDE DISTILLATION. Overview. Purpose To recover light materials. Fractionate into sharp light fractions.

Converting Visbreakers to Delayed Cokers - An Opportunity for European Refiners

ARA TT Market Projections

Indian Oil Corporation Limited Mathura Refinery

The Chevron Pembroke oil

Crude Evaluation Best Practices

MEG/WRI s Partial Bitumen Upgrader Project Adding Value to MEG and Alberta

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

White Paper.

FEASIBILITY REPORT 100% BS-V AUTO FUEL PRODUCTION AT 13.7 MMTPA

OEGEW Conference presentation Challenges in Oil Movements in a globalising world

Upgrade Bottom of the Barrel to Improve Your Margins

The Asphalt Oil Binder Business A Necessary Evil or a Godsend From a Refiner s Perspective

20,000 bpd CRUDE OIL REFINERY FOR SALE AND RELOCATION

High speed, closed loop frequency control using PMU measurements for power grids

Changing Crude Qualities and Their Impacts on U.S. Refinery Operations AM-14-42

Introduction of S-OIL

Maximizing Refinery Margins by Petrochemical Integration

Inverter Advancements in UL1741 and UL 62109

2015 Interim Results Announcement

Refinery / Petrochemical. Integration. Gildas Rolland

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

TYPES OF BLENDING PROCESS

North American Storage and Transportation Trends

Remote Process Analysis for Process Analysis and Optimization

Results Certified by Core Labs for Conoco Canada Ltd. Executive summary. Introduction

breakthrough versatility

Residue Upgrading Technologies Key Technologies, Considerations & Options for your Refinery Russia BBTC 2015 MOSCOW

Crude Distillation Chapter 4

IMPLEMENTATION OF FOUNDATION FIELDBUS (FF) TECHNOLOGY IN IOCL REFINERIES

Energy Performance Information Request Timeline

Canadian Bitumen and Synthetic Crudes

Refining & Marketing. Mario Taraborrelli COO

Russia's downstream: Old Problems and New Reality

ALBERTA CARBON LEVY. Impact of Producers, Marketers and Users of Fuel. December 15, 2016 Craig McDougall, QC / Peter Mitchell, CA Felesky Flynn LLP

A Theoretical Study in Maximizing Crude Unit Kerosene

LC-FINING Options for Heavy Oil Upgrading

Defining the Debate: Crude Oil Exports

Acombination. winning

Testing Catalyst Additives for Sulfur Reduction in Cat-Naphtha

Changing Refinery Configuration for Heavy and Synthetic Crude Processing

TechnipFMC RFCC Technology converts bunker fuels into high value products for African refiners

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

Refining at NIS, Bottom of the Barrel Project

9M 2003 Financial Results (US GAAP)

Optimizing Distillate Yields and Product Qualities. Srini Srivatsan, Director - Coking Technology

Stronger than the others

Cosmo Oil Co., Ltd. Presentation on Results for First Quarter of Fiscal 2012 August 2, 2012 Director: Satoshi Miyamoto

Q Analyst Teleconference. 9 August 2018

CHALLENGES = OPPORTUNITIES

Axens CCR Reforming Technology

Crude Export and the New Dynamics

US biofuel Indicators and a changing market dynamic

Methodology. Supply. Demand

PowerFlex 755T Drive Solutions New Solutions for Low Harmonic, Regenerative & Common Bus Applications

ERGMed Coastal. Refining

A summary of national and global energy indicators. FEDERAL RESERVE BANK of KANSAS CITY

Schwechat Refinery Visit

Optimize Energy Recovery in Refineries. Copyright : Evae Andersson

EURONAV TALKS IMO 2020 FROM THE VIEW OF A SHIPOWNER JUNE

Refining Outlook: elements for a modern industrial culture in Italy

Modernization of Afipsky Refinery. The Russia and CIS Project & Equipment Forum RPEF 2015 April 21-22, 2015, Moscow

Technology for Producing Clean Diesel Utilizing Moderate Pressure Hydrocracking With Hydroisomerization

DHEYAA JAAFAR HAJAM AL - MUSAUI Deputy Minister for Refining Affairs Ministry of Oil, Iraq

Challenges for proper implementation of residue upgrading processes within oil refineries

Global Overview of Middle Distillates Supply and Demand ICE Market Forum Rotterdam, November 2012

Used Oil Refinery for Sale and Relocation, 80,000 bpd.

Updated: April 1, Releases Reported by Trans Mountain February 2017 (Updated: April 1, 2017)

2010 Interim Results Presentation. August 23, 2010 Hong Kong

William Piel

Diesel Maximization: Putting a Straw on the FCC Feed AM Annual Meeting March 22-24, 2015 Marriott Rivercenter San Antonio, TX.

Pre U.S. Crude Boom (~2007/2008)

Shunt reactors Proven history for future success

PRISM TM Refining and Marketing Industry Analysis

Crude Tower Simulation Aspen Plus v8.6. The feedstock to the crude system will be an equal mix of Light, Medium, & Heavy Crude oils.

GULFTRONIC SEPARATOR SYSTEMS

Electronic Control Valves

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

Modernization of Libyan Oil Refineries and Petrochemical Plants

2012 Honeywell Users Group EMEA

Solvent Deasphalting Conversion Enabler

Wheat Marketing Situation

BEFORE IT ALL BEGAN. Osagyefo unveils the plaque to mark the opening of GHAIP

SOLVENT DEASPHALTING OPTIONS How SDA can increase residue upgrading margins

Increased recovery of straight-run

UPGRADER FOR HEAVY, EXTRA-HEAVY CRUDE/BITUMEN AND RESIDUAL FRACTIONS

Modernizing a Vintage Cat Cracker. Don Leigh HFC Rahul Pillai KBR Steve Tragesser KBR

FSR on Expansion and Modernization of the MOIN Refinery Project

Advantages of Using Raman. Spectroscopy to Monitor Key. Gasoline Blending Parameters

UPGRADER FOR HEAVY, EXTRA-HEAVY CRUDE/BITUMEN AND RESIDUAL FRACTIONS

Transcription:

SimSci APC and Offsites Updates Rujun Li SimSci by Schneider Electric

SimSci APC SimSci APC is the next-gen APC to replace Connoisseur Updated, intuitive UI Streamlined workflow New functions and features SimSci APC release history 2014 2015 Will be released every 9-12 months

Director IronPython based script language Automation of control actions and tasks Pre- and post-process the data going in and out of the controller Turn on and off controller Switch controller modelset during transition

Subcontroller Improved operator ease of use while switching in & out of control point groups

Enhanced Trending Ability to deal with large gaps in data Improved ease of use due to synchronizing all trends during analysis Faster analysis by allowing complete flexibility of intermixed process variables and modeling residuals Enhanced future prediction

Easier and Faster Data Selection Model data selector Zooming and dragging data slice edge for fine tuning of the start/end point

Enhanced Import and Export Can import multiple and export Connoisseur and SimSci APC data files Can export tag data to csv files Can import and export controller modelsets Can import and export Connoisseur and SimSci APC controller files

SimSci APC Crude/Vacuum Unit APC Tom Kinney, Schneider Electric

Crude Unit Description & Operation Mid-continent US refinery 60,000 BPD Unit produces naphtha, kerosene, diesel, AGO/LVGO, and HVGO Operators face challenges keeping the unit stable with products on spec due to crude switches, and especially addition of various slop oils as charge every few days Atmospheric tower overhead condenser duty frequently limited Control engineering staff is limited to 2 engineers covering the entire refinery, which includes an FCC and a hydrocracker

Day 1 Diesel Control

Before and After: Naphtha 450 Lab Naphtha Endpoint 430 410 390 370 Deg F 350 330 Before After 310 290 270 250 25-Feb-15 7-Mar-15 17-Mar-15 27-Mar-15 6-Apr-15 16-Apr-15 26-Apr-15 6-May-15 16-May-15 26-May-15 5-Jun-15

Product Improvements Before Commission Benefit is about $875K per year After Commission Change Naphtha Lab EP (F) 347.5 366.2 N/A Std Dev (F) 8.5 6.3-26% Kero Lab Freeze Pt (F) -57.4-56.9 +0.5 Std Dev (%) 4.84 4.07-16% Diesel Lab T90 (F) 645.5 645.7 Std Dev (F) 4.4 3.4-23% Diesel Yield (%) 6.01 6.75 +0.74% Std Dev (%) 0.82 0.71-13%

Total Refinery Antwerp Upgrade Refinery Off-sites Cor Swart, Schneider Electric

Estimate Sizing of the TRA Tank Farm TANKS 200 Motor Operated Valves (MOV) 1500 Hand Operated Valves (with feedback) (OZV) 400 Hand Operated Valves (HOV) 5000 Control Valves 200 PUMPS 200 LINES 3200 LINE SEGMENTS 12000 LOADING ARMs (shiploading) 20 PIPELINES (External movements) 3

Off-sites Application at TRA 1 Oil Movement Management; 3000 Source/destinations, 30,000 line-ups and 200 movements active 2 Movement Automation System including TRA functions 3 Thermal Relieve and Anti-Contamination 4 Non-registered movements in the field 5 Key valve selection 6 Pump protection valve (PBV) 7 Dynamic isolation 8 Line-up generation and management 9 Blenders control (10 blenders : 2 crude, 2 gasoline, 2 Diesel, 1 fuel 3 Bitumen) 10 Jetty loading control 11 Tank Information System 12 Aspentech/Infoplus interface (bitumen blender and supervisory control for other blenders) 13 OPC with DCS 14 ODBC with ROMSS 15 Hand Held Terminal system interface 16 Business application interface (MPRO, SAP, ROLLS) 17 Order handling 18 Inventory control 19 Equipment management and traceability 20 Line-up maintenance

Reason to Execute Project Legacy Yokogawa not supported anymore Legacy system had no expansion capabilities anymore for near future refinery expansion DCS and off-sites were integrated and therefore both to be upgraded Requirement to have the migration to future system during normal operations with minimum disturbance Request for upgrade was put on the market Project awarded to SimSci by Schneider Electric in summer 2011

End Results System startup was smooth, without unexpected impact on the operation of the refinery Target of change over one day achieved Operators are happy with the delivered functionality, which is better than the previous system.