Critical Ethylene Level and Flow Applications and Case Studies

Similar documents
Steam Generation, Waste Heat and Condensate Recovery Level Applications

A Guide to Level Instrumentation for Onshore/Offshore Oil Processing

A Guide to Level Instrumentation for the Nuclear Power Industry

A Guide to Level Instrumentation for Power Generating Plants

A Guide to Level Instrumentation for Onshore/Offshore Oil Processing

LEVEL AND FLOW INSTRUMENTS FOR FLUE GAS DESULFURIZATION

Special Applications Series Heat Rate Awareness

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

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

1 S P E C I A L A P P L I C AT I O N S E R I E S. magnetrol

LEVEL AND FLOW INSTRUMENTS FOR MODULAR SKID SYSTEMS

Table of Contents. iii. vi Tables. Figures. viii Foreword. ix Acknowledgments

ABB MEASUREMENT & ANALYTICS ANALYTICAL MEASUREMENT. Ethylene plant production excels with the PGC1000

Natural Gas Processing Unit Modules Definitions

Transfer and Storage of Flammable Liquefied Hydrocarbon Gases

Bulk petrochemical manufacturing is a highly competitive

Chemistry Resource Kit

Chemistry of Petrochemical Processes

Coker Safety and Reliability Lessons Learned

Report No. 29 ETHYLENE. August A private report by the PROCESS ECONOMICS PROGRAM I STANFORD RESEARCH INSTITUTE MENLO PARK, CALIFORNIA

NEW RECYCLE PROCESS SCHEME FOR HIGH ETHANE RECOVERY NEW PROCESS SCHEME FOR HIGH NGL RECOVERY INTRODUCTION. Abstract PROCESS FUNDAMENTALS

PTAC PROCESS TECHNOLOGY II - SYSTEMS. Last Reviewed: Page 1 of 10

Enhanced Heat Transfer Solutions. Energy efficiency and compactness for the oil and gas industry

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

DryVAC Vapor Recovery Systems

On-Line Gas Analysis In Air Separation Plants

Taravosh Jam Design & Engineering Co.

ETHYLENE. Best Available Technology Burners Flares Thermal Oxidizers

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

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

Performance Evaluation of Deethanizer Column Using Real Time Optimization

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

TABLE OF CONTENT

Questions. Downdraft biomass gasifier. Air. Air. Blower. Air. Syngas line Filter VFD. Gas analyzer(s) (vent)

Magnetically Coupled Submerged Cryogenic Pumps and Expanders for Ammonia Applications

Polaris. Smart VOC Recovery Systems

Novel Method for Gas Separation By: Chris Wilson and Dr. Miguel Bagajewicz

TABLE OF CONTENT

The Separation and Liquefaction of Oxygenated CBM Yang Kejian and Zhang Wu

MB 1 Contribute to the safe operation of a ship subject to IGF Code

Valves for the Process Industries

H 2. Derivatives and Uses: Fuel Cells. ENERGY CRISIS: One of biggest issues in world today. Problem? Solution?

NATURAL GAS HYDRATES & DEHYDRATION

Optimizing a World-Scale Petrochemical Plant

Hydrogen Recovery by Pressure Swing Adsorption

Distillation DEPARTMENT OF CHEMICAL ENGINEERING

AFPM 2018 Operations & Process Technology Summit

Appendix 8.5 Equipment Summary & Specification Sheets

HYSYS WORKBOOK By: Eng. Ahmed Deyab Fares.

Nitrogen production plants HPN

UNIQUE DESIGN CHALLENGES IN THE AUX SABLE NGL RECOVERY PLANT

Minimize the Risk of Fire During Distillation Column Maintenance

Livia Tizzo, Process Control and Automation Engineer, Braskem. Case Study

Safer, More Efficient Combustion Control for Fired Heaters

Sentinel LNG. Panametrics Ultrasonic Flowmeter for Cryogenic Liquids. GE Sensing & Inspection Technologies. Benefits. Applications

PILLER INDUSTRIAL HEAT PUMP WE ARE WORKING ON THERMAL ENERGY

10/2/2013. Gas CHEMICAL PLANTS AMMONIA METHANOL UTILITIES TOWN GASS SUPPLIES ENERGY INTENSIVE INDUSTRIES. Power Generation

Fuel Sources. Gases Liquids/vapours Chemicals and Solids

Chemical Process Instrumentation Prof. Debasis Sarkar Department of Chemical Engineering Indian Institute of Technology, Kharagpur

COMPREHENSIVE MSW PROCESSING STEPS BIO COKE METHOD

NOVEL DISTILLATION CONCEPTS USING ONE-SHELL COLUMNS

SULFUR RECOVERY UNIT. Thermal Oxidizer

Effect of catalyst to oil weight ratio on gaseous product distribution during heavy oil catalytic pyrolysis

Wastewater Recycling Plants with Zero Effluent Discharge. Water Recycling Plants

COMBIMASS Thermal Gas Flow

Donald Hite, Business Development Manager Magnetrol International and Orion Instruments

Title slide. LNG Technology. Compiled by PD.Supriyadi

Optimization Based Approach for Managing Enterprise-Wide Business Planning in a Petrochemical Industry

Sentinel LNG. Panametrics Ultrasonic Flowmeter for Cryogenic Liquids. GE Sensing & Inspection Technologies. Benefits. Applications

CO₂ purification and liquefaction. Adding value through standardization and modularization.

Digital E3 Modulevel Liquid Level Displacer Transmitter

THERMATEL MASS FLOW MEASUREMENT

(12) Patent Application Publication (10) Pub. No.: US 2008/ A1

3M Dyneon Fluoropolymers. Dyneon solutions. for the Chemical Processing Industry

Polimeri Europa Olefin Plant Maximizes Benefits from Advanced Solutions

Qualitative Phase Behavior and Vapor Liquid Equilibrium Core

SURFACE PRODUCTION OPERATIONS

forming the on-line analysis and started conducting it in the laboratory.

THERMATEL MASS FLOW MEASUREMENT

Gas Dehydration Field Manual

Hydrocarbons contain the elements... and... only. (1) H 6. Draw a ring around the correct answer to complete the sentence.

Petrochemical Processing

PROCESSES IN ORGANIC CHEMICAL INDUSTRIES (BULK PRODUCTION) pr Activity

Tuffy II Liquid Level Controls with Electric Switches

Process Gas Monitoring In Petroleum Refineries

PRE-FEASIBILITY REPORT ON

Engineered Products for the Process Industries

Advanced Equipment Manufacturing

Propane Dehydrogenation Reactor and product recovery section applications

Specialty Chemical Measurement Solutions

Superior reliable performance. Niagara Wet Surface Air Coolers for fluid cooling and vapor condensing

Flash Zone Optimization of Benzene-Toluene-Xylene Fractionation Unit

Industrial Gases. Chapter 3 1. NITROGEN. 1.1 Manufacture

Modular Oil & Gas Equipment Onshore & Offshore

Sentinel LNG. Panametrics Ultrasonic Flowmeter for Cryogenic Liquids. GE Sensing & Inspection Technologies. Benefits. Applications

Design Characteristics of the Cold Neutron Source in HANARO Process System and Architecture Design

III.P. Recovery and utilization of waste gas in refinery facilities

Mach-RGA. The Fast Refinery Gas Analyzer. Analyzer

Downsizing a Claus Sulfur Recovery Unit

Transcription:

Special Applications Series: Critical Ethylene Level and Flow Applications and Case Studies Maintaining Safety, Reliability and Productivity In ethylene plants, balancing environment, health, and safety is essential while maximizing productivity. Level and flow instrumentation will assist in preventing loss of primary containment and maintaining a safe environment inside of the tank. That s critical, because incident consequences are significant, with the direct cost of a work-related death of $1M and indirect costs approximately 4 times greater.* In addition, there is the lasting damage to your brand reputation and the compromised safety of the local community. Instrumentation can also assist in maximizing productivity, including interface type measurement in some of the harshest environments. Today, conformance to IEC 61508 is the standard for reliability. Instruments with the appropriate SIL requirements are suitable for use in SIL 1, SIL 2 or SIL 3 safety loops as a single device or with redundancy. This brochure contains a wide spectrum of Magnetrol and Orion Instruments level and flow products that conform to the latest safety standards, including SIL requirements, to assist in the most critical applications in ethylene plants. *National Safety Council s Injury Facts via Chemical Processing Magazine

Ethylene Process Flow Diagram This diagram depicts a typical ethylene plant and indicates key applications. 1. Furnaces Quench Tower/Settler CGC Stages 1 4 CGC Stage 5 Acid Gas Removal (Scrubber) Drying Unit Cold Box 2. Demethanizer Column C2 Cut 2. Deethanizer Column Acetylene Reactor 5. Lubrication Fluids C2 Splitter 2. Depropanizer Column C3 Cut C3 Splitter 2. C4 Cut C5 Cut Ethylene Storage 3. Propylene Storage 3. Raw C4 Storage 3. Gasoline Storage 6. Power/Utilities Debutanizer Column 3. Key Applications 1. Quench Tower/Settler 2. Fractionation Towers 3. Liquefied Gas Storage/Cryogenic Tank Blanketing 5. Lubrication Fluids 6. Power/Utilities 2

1. Quench Tower/Settler Feedstock comes into the plant and goes through the ethylene furnaces (pyrolysis) Once cracked into a variety of hydrocarbons and hydrogen, it immediately begins to recombine into larger molecules To prevent these reactions, the cracked vapor goes through the quench towers to cool using oil or water The largest hydrocarbons are carried with the water into the quench settler or the quench water separation drum (QWSD) Loss of control of interface will reduce ethylene production due to inefficient quench tower operation As feedstock is increased, more cooling fluids are required The residence time in the settlers needs to be minimal to maintain composition and prevent secondary reactions A quench settler or QWSD that catches the hydrocarbon liquids and water from the quench tower creates an interface in the QWSD and possibly an emulsion layer if too much caustic is added The interface is important to recirculate the quench water from the settler to the tower and not recirculate the hydrocarbons which will reduce productivity and potentially cause fouling of equipment; also applies to quenching oil versus tars and other heavy hydrocarbons If fluid composition negatively changes in the quench tower, less ethylene is produced from the feedstock reducing efficiency and productivity. Regulating an interface level can also aid in using less caustic if quench water is used Eclipse Model 706 Guided Wave Radar Transmitter Jupiter Model JM4 Magnetostrictive Level Transmitter 3

2. Fractionation Towers TOWER Separating substances based on differences in volatilities/ boiling points Level measurement at the bottom of a distillation tower controls the bottoms product rate Poor level control could allow liquid to back up over the stripping trays causing damage and reduced yields Level that s too low may cause pump cavitation Instrumentation Solutions: Eclipse Model 706 Guided Wave Radar Transmitter Digital Displacer E3 Modulevel Liquid Level Transmitter REBOILER Provides heat to the bottom of a distillation tower to drive the separation process Excess reboiler liquids (bottoms or blow-down) overflow a baffle where level is controlled by means of a level controller When level becomes too low, it will affect the maximum flow rate of bottoms product that can be drawn off Inaccurate reboiler level can also degrade composition control for material balance Instrumentation Solutions: Eclipse Model 706 Guided Wave Radar Transmitter Digital Displacer E3 Modulevel Liquid Level Transmitter CONDENSER Changes a gas or vapor to a liquid; condensation is employed in the reflux process to improve the efficiency of distillation Tower vapors are condensed prior to entering an accumulator (reflux drum) where level can assist controlling tower pressure Instrumentation Solutions: Eclipse Model 706 Guided Wave Radar Transmitter REFLUX DRUM Uses reflux system to achieve a more complete product separation where condensate is cycled back to the tower to provide cooling and condensation of upward flowing vapors Condensed liquid leaves reflux drum under level control. Poor liquid level can cause expensive operating problems and product degradation if the proper amount is not returning to towers Instrumentation Solutions: Eclipse Model 706 Guided Wave Radar Transmitter Digital Displacer E3 Modulevel Liquid Level Transmitter 4

3. Liquified Gas Storage/Cryogenic Many liquids are cooled at normal atmospheric pressure while others require pressurization Feedstock to an ethylene plant s fractionation towers contains a liquid cryogenic hydrocarbon mixture as a result of going through compression and refrigeration trains after the quench tower Above or below-ground insulated storage tanks are built to specifically hold liquefied gases and minimize evaporation Instruments contend with pressurization, extreme low temperatures and low dielectric media Eclipse Model 706 Guided Wave Radar Transmitter Pulsar Model R86 Pulse Burst Radar Transmitter Echotel 961 and 962 Single and Dual Point Ultrasonic Level Switches Tank Blanketing Nitrogen is the ideal tank blanketing gas when injected into the vapor space of a storage tank to prevent ignition of flammable liquids, inhibit vapor loss, and possibly protect the products from oxygen degradation Extreme low flows and pressures Economical mass flow totalization Thermatel Model TA2 Thermal Mass Flow Meter 5

5. Lubricating Fluids Liquids used for barrier or buffer fluids are essential in maintaining proper operation of equipment requiring mechanical moving parts, such as pumps At a minimum, low level indication is required to ensure there is liquid in the vessel or seal pot Newer standards, such as API 682 Revision 4, are moving towards continuous measurement utilizing transmitters Eclipse Model 706 Guided Wave Radar Transmitter Echotel 961 and 962 Single and Dual Point Ultrasonic Level Switches 6. Power/Utilities Heat Recovery Steam Generator (HRSG) from cracked gases for additional steam and power generation Improving heat rate efficiency through feedwater heater level control Utilities steam and condensate recovery system Optimizing makeup water treatment, energy management, steam generation cycle, condensate and waste heat recovery Eclipse Model 706 Guided Wave Radar Transmitter 6

Case Studies Case Study 1 Company: One of the world s largest oil & gas and petrochemical companies headquartered in Europe Challenge: Problems occurred with multiphase applications involving hydrocarbon level with water bottoms and gas vapor space. Guided wave radar was being used, but it did not produce a reliable signal throughout the length of the probe and the interface made it difficult to distinguish between upper level and water below. This threatened LOPC due to error in measurement. Solution: ECLIPSE Model 706 was found to be best-in-class guided wave radar when tested side-byside. It tracked level up to the device s flanged process connection (above 100% level point), even with water bottoms. There were no dead zones or blind spots at top of probe. The ECLIPSE prevented LOPC and the superior signal strength went through the hydrocarbon level down to the water level. Case Study 2 Company: Ethylene plant in China requiring clear visual indication of level Challenge: Required clear visual indication of level from challenging cryogenic applications including methane, ethane, ethylene and propylene. SGs ranged from 0.3 0.8. Solution: The Orion Instruments Atlas Magnetic (MLI has physical floats in the MLI chamber that can simultaneously meet cryogenic and low SG requirements. The careful float design allows level to be tracked accurately even as temperature and SG shifts. Cryogenic visual flags or indicators (frost shield) prevent frosting to provide a clear visual indication of liquid level. Case Study 3 Company: Oil & gas and petrochemical company in China Challenge: The company required tank blanketing for their flammable liquid tanks to create an inert environment in the vapor space. Nitrogen was commonly utilized and required monitoring to account for leakage and verify flow. Users wanted to limit gas to an as-needed basis. They needed to monitor not only pressure, but the flow, in order to find balance of gas usage and cost savings. Solution: Thermatel TA2 thermal mass flow meters came fully calibrated and configured so the company could simply install and power up. THERMATEL TA2 is also effective in extreme low pressures. In addition, total cost of ownership was reduced with calibration verification procedures that could be performed in the field. Recalibrations can cost tens of thousands of dollars and cause process downtime or loss of measurement. Case Study 4 Company: Refinery and petrochemical facility in Canada that primarily produces ethylene Challenge: The facility s reliability and safety groups needed level devices that met SIL requirements for emergency shutdown (ESD) and safety systems. Both SIL 1 and SIL 2 applications exist at this site. The facility needed to implement proof test procedures for their instrumentation and control devices to meet safety loop requirements. One proof test requirement was for the ma output to be set below 4 ma and above 20 ma; this was the necessary output range to meet the NAMUR NE43 recommendation. Solution: The Orion Jupiter JM4 magnetostrictive transmitter was chosen. It allowed current output to be taken low or high per NAMUR NE43. The advanced diagnostics of the JM4 allowed users to pull echo curves from the transmitter display or access them externally using a PC by wiring into the current loop. 7

The Right Solutions for Every Application Radar Eclipse Model 706 Guided Wave Radar Transmitter Pulsar Model R86 (26 GHz) Pulse Burst Radar Transmitter Pulsar Model R96 (6 GHz) Pulse Burst Radar Transmitter Thermal Dispersion Thermatel Model TA2 Thermal Mass Flow Meter Thermatel Models TD1 and TD2 Flow/Level/Interface Switches Ultrasonic Echotel 961 Single Point Ultrasonic Level Switch Echotel 962 Dual Point Ultrasonic Level Switch Buoyancy Digital E3 Modulevel Liquid Level Displacer Transmitter Model A10 Single-Stage Displacer Switch Magnetostrictive Jupiter Model JM4 Magnetostrictive Level Transmitter Magnetic s Aurora Magnetic Atlas Magnetic CORPORATE HEADQUARTERS 705 Enterprise Street Aurora, Illinois 60504-8149 USA Phone: 630-969-4000 Fax: 630-969-9489 magnetrol.com info@magnetrol.com EUROPEAN HEADQUARTERS Heikensstraat 6 9240 Zele, Belgium Phone: 052 45.11.11 Fax: 052 45.09.93 PLEASE NOTE: The instruments recommended in these brochures are based on field experience with similar applications and are included as a general guide to level and flow control selection. Because all applications differ, however, customers should determine suitability for their own purposes. Magnetrol & Magnetrol logotype, Orion Instruments, Aurora, Echotel, Eclipse, Jupiter, Pulsar and Thermatel are registered trademarks of Magnetrol International, Incorporated. Copyright 2017 Magnetrol International, Incorporated. Bulletin: 41.191 Effective: April 2017