Minimizing Transmix With FuellCheck

Similar documents
Systems. In-line Blending. Solutions you can trust

On-Line Process Analyzers: Potential Uses and Applications

LIQUID MEASUREMENT STATION DESIGN Class No

White Paper.

Systems. In-line Blending

Chapter 2. The Vehicle-Tank Metering System

Monitor Chlorine in Crude at Sub-ppm Levels

FAME The Saga Continues

DESIGN, OPERATION & MAINTENANCE OF L.A.C.T. UNITS

Northville Product Services and Colonial Pipeline B5 Soy Test Data and Report February Soy blended low sulfur diesel

POWER PROFET A simpler solution with integrated protection for switching high-current applications efficiently & reliably

Are You Prepared For Tier 3 Gasoline Standards? Presented by: Shaun Spiro and Leslie Johnson

FLUXUS HPI Series. Non-Intrusive Ultrasonic Flow Measurement for the Hydrocarbon Processing Industries. External Measurement of Internal Flow FLEXIM

Flammability of Bakken Crude Oil: Dangerous. Rail Cargo Even When Empty. (by Dr. Gerard Macri, Expert Witness)

Application Note. Case study Early fault detection of unique pump bearing faults at a major US refinery

Temperature sensors: Make the right choice, RTD vs. TC

Phase-Two Water Detector

Environmental Expenditures. by the U.S. Oil and Natural Gas Industry

Understanding the benefits of using a digital valve controller. Mark Buzzell Business Manager, Metso Flow Control

Non-Invasive Hydrocarbon Products Mass Flow Measurement, Media Identification and Leak Detection

Guidance on Changes to ASTM D1655 and Def Stan to Increase Allowable FAME Limits to 50 mg/kg

Worldwide Demand for Crude Oil & Refined Products: Refinery Business Objectives: Fundamental Qualities of Oil:

FUNDAMENTALS OF ORIFICE METERING Ken Embry FMC Measurement Solutions

This presentation focuses on Biodiesel, scientifically called FAME (Fatty Acid Methyl Ester); a fuel different in either perspective.

LACT MEASUREMENT. Total Head = Or PSI = S.G. 2.31

U.S. GASOLINE AND DISTILLATE FUELS UPDATE - DECEMBER 20, 2017

TERMINAL BLENDING AS AN ULTIMATE SOLUTION FOR PETROLEUM PRODUCTS ANTI-THEFT SECURITY

1 Faculty advisor: Roland Geyer

Once a waste of lamp oil production

better analysis counts

10 S Naphtha - Isomerized Not Diluent Minimum RVP of S Naphtha Mix Not Diluent Minimum RVP of 4.5

PECTEN MIDSTREAM LLC

Fast Gas Chromatography in the Refinery Quality Control Laboratory. Carl Rechsteiner CRechsteiner Consulting, LLC (Chevron retired)

breakthrough versatility

Fuel Focus. Understanding Gasoline Markets in Canada and Economic Drivers Influencing Prices. Issue 20, Volume 8

On-Line NIR Analysis for Blending

Remote Process Analysis for Process Analysis and Optimization

Department of Energy Analyses in Support of the EPA Evaluation of Waivers of the Renewable Fuel Standard November 2012

The Cost of Banning No. 6 Oil in New York City

Fuel Focus. Understanding Gasoline Markets in Canada and Economic Drivers Influencing Prices. Volume 10, Issue 4

1. Introduction and Summary

Flow Measurement SITRANS F S Clamp-on

Thermal Management: Key-Off & Soak

MthSc 810 Mathematical Programming Case Study: The Global Oil Company


EI HMC Report Spring API Committee on Petroleum Measurement Standards Meeting

PETE 203: Properties of oil

Elemental Analysis Advanced

Permanent Multipath Clamp-On Transit Time Flow Meter

BULLETIN August 2009 PERMASEAL PLUG VALVE. ISO 9001:2008 Certified QMS. SMG Valves A Unit of Southern Manufacturing Group, Inc.

KNOWLEDGE

Oxidative Desulfurization. IAEE Houston Chapter June 11, 2009

NJK Precision Product NJK-02 Sensor Installation Guide

9M 2003 Financial Results (US GAAP)

LIQUID MEASUREMENT STATION DESIGN with NGL CONSIDERATIONS

Product Quality Bulletin

SUMMARY OF THE IMPACT ASSESSMENT

VALVOLINE HYDRAULIC OILS PEOPLE WHO KNOW USE VALVOLINE

Detection of Volatile Organic Compounds in Gasoline and Diesel Using the znose Edward J. Staples, Electronic Sensor Technology

White Paper. Improving Accuracy and Precision in Crude Oil Boiling Point Distribution Analysis. Introduction. Background Information

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

GTC TECHNOLOGY WHITE PAPER

Transitioning from Commercial Pilot to Mass Production 2 IUT s skid mounted 15,000 barrel per day Processing Unit

Lease Automatic Custody Transfer

Mini refinery feasibility study

400/230 Volt 60Hz UPS Power

Estimation Procedure for Following Vapor Pressure Changes

Submission to Select Committee on Electric Vehicles - inquiry into the use and manufacture of electric vehicles in Australia

Internal Revenue Service

KAM CHA COLORIMETER/HAZE ANALYZER. User Manual API COMPLIANT PTB 04 ATEX 1027

IGE Business Model Presentation. FOYSON RESOURCES LIMITED EXTRAORDINARY GENERAL MEETING 31 st March 2015

OIL Driver Information Getting the best from your car

A Performance Balance. The First Time, Every Time.

Ultrasonic Transit Time Flow Measurement for Coker Furnace Feed

PETROLEUM PRODUCTS INSPECTION OPERATIONS MANUAL

Design Considerations for Pressure Sensing Integration

Advanced Biolubricants and Used Oil Re-refining

FLUXUS HPI Series External Measurement of Internal Flow

HARDWIRE VS. WIRELESS FAILSAFE CONTROL SYSTEM. The answer is No.

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

Jet Fuel Conductivity Analysers & Additive Management systems

R-MAG Vacuum Circuit Breaker with Magnetic Actuator Mechanism 15.5 kv - 27 kv; 1200 A A

Co-Processing of Green Crude in Existing Petroleum Refineries. Algae Biomass Summit 1 October

Plug Valve Solutions for the Upstream Exploration and Production Pipelines Production manifolds, test manifolds and other dirty services

Made in Texas Plan to Create a Million New Jobs. Oil Sign Policy

PPTS OPERATOR ADVISORY: FACILITIES PIPING AND EQUIPMENT: FOCUS ON ITEMS INVOLVED AND CAUSES OF INCIDENTS

Exceeding Expectations

Challenges to Ethanol Blending in the Southeast

Desulphurizing Marine Fuel/HFO Utilizing IUT Technology. November 19, 2017 International Ultrasonic Technologies Inc.

SITRANS F flowmeters SITRANS F US. SITRANS FUT1010 Ultrasonic flowmeter. Overview. Application

BIG DEAL. cylinders are still a. compact air. inside: Digital Ebook A Design World Resource. Compact Air Cylinders: 101

PROTECT. Building a New Category of Opportunity for your Business

SHELL PIPELINE COMPANY LP ZYDECO PIPELINE COMPANY LLC

Grid Services From Plug-In Hybrid Electric Vehicles: A Key To Economic Viability?

Weekly Statistical Bulletin

Flo-Way. Measure Granular or Powdered Material. Stand Alone or Connect to Other Devices for Blending. Used by Successful Producers World-Wide

Refining/Petrochemical Integration-A New Paradigm

FUNDAMENTALS OF INSERTION TURBINE METERS Les Bottoms Thermo Electron Corporation, Flow Systems

FURTHER TECHNICAL AND OPERATIONAL MEASURES FOR ENHANCING ENERGY EFFICIENCY OF INTERNATIONAL SHIPPING

TYPES OF BLENDING PROCESS

Transcription:

Minimizing Transmix With FuellCheck What is Transmix? Those who have to deal with transmix best answer this question. Below are 2 different perspectives, the first from an engineering consulting firm, and the second from a trans-mix refiner. Figure 1 Figure 2 any of a number of products. For example, a pipeline branch linking two major cities may move aviation fuel in the morning, gasoline in the afternoon, and fuel oil in the evening. The question that immediately arises is, how can you transport two dissimilar products in succession without blending the two? The fact is, some blending will occur. However, if plug flow conditions can be maintained between origination and destination points, blended product can be minimized. Undesirable product blending which occurs during transport is commonly referred to as transmix. A certain amount of transmixing is inevitable. It represents a problem that can cost the pipeline company and the American consumer millions of dollars per year. Transmixing erodes the margin that exists between a premium product and a lower grade and less expensive product. Frequently, a transmixed section of fuels must either be blended into lower grade product streams, or trucked out at a loss to be recycled (re-refined) back into individual product streams. In the case of one South Texas pipeline, transmixing was responsible for approximately $1 MM/month in lost revenues. 1 Millions of barrels of motor gasoline, diesel fuel and jet fuel move daily in batches through pipelines connecting refineries to terminals in major population and distribution centers across the country. Each refiner and marketer shipping these products through the pipelines is responsible for disposing of the interface between batches of the individual products. The interface between different refined petroleum products is a product known as transmix. Transmix has been handled in a variety of ways in the past but recent changes in the laws regarding the environment, diesel desulfurization regulations and mandatory oxygen-based additives in motor gasoline have made disposal of this product more troublesome for shippers. The volume of transmix is expected to increase as more kinds of products are shipped as a result of additional regulations. The major refining companies need someone capable of physically removing and paying for large volumes on short notice so that pipeline shipments 1

are not interrupted. Another concern of the shippers is that the transmix be handled by a safe and legal operation and not simply blended back into conventional products sold in the local marketplace. 2 What IS FuellCheck? Fueel lcheecckk is a completely fiberoptic process refractometer used to perform accurate batch cuts in shared product pipelines. Fueel lcheecckk is comprised of 3 major components; namely, the probe, the fiberoptic interconnect, and the controller. The probe is installed into the pipeline through a 1-inch (or larger) full-opening valve. The probe is normally inserted only until flush with the inside wall of the pipeline so that pigging can be conducted without removing Figure 2 or retracting the probe. The fiberoptic interconnect is used to convey light energy to and from the probe, and consists of a pair of optical fibers packaged in various cable configurations which are selected based on application environment. The controller supplies the light energy to the probe and measures the light intensity returning from the probe, which is then converted into an electrical signal. The controller can be located up to 2 km away from the probes, enabling cost-effective upstream placement of probes without the need for 2

power or special piping. Because the probes are completely fiberoptic, they are immune to lightning and other EMR and are also inherently safe devices. How does FuellCheck work? The Fueel lcheecckk sensor (U.S. patent number 5,946,084) is a dual surface critical angle refractometer. Light enters the 5 mm diameter hemispherical sapphire lens through one of the attached optical fibers, reflects twice inside the lens, and leaves the lens via the other optical fiber. Some light is refracted out of the lens into the fluid wetting the lens. The amount of refraction (or loss) is proportional to the refractive index of the fluid. Refractive index is defined as the ratio of the speed of light in a fluid to the speed of light in air; Figure 3 hence, the refractive index of air is 1.0000. Since light travels ⅓ faster in water than in air, its refractive index is 1.3333. Refined products' refractive indices run from about 1.38 to 1.5. With refined products containing no dditives, there is an excellent correlation between refractive index and density. If the fluid temperature correction algorithm (described in the Fueel lcheecckk Installation & Operation Manual) is applied to the Fueel lcheecckk output, the system can be calibrated very closely to API gravity or specific gravity. Fueel lcheecckk is an extraordinarily robust sensing system. The dynamic range between air (η = 1.0000) and heavy hydrocarbons (η = 1.5000) is over 40 db optical. This results in extremely high sensitivity and SNR, enabling easy differentiation of similar products. The charts shown below demonstrate the sensitivity of the Fueel lcheecckk system. How are transmix volumes minimized using FuellCheck? Too often, terminal operators are forced to rely on little more than experience and intuition when making batch cuts on incoming product streams. Indeed, most batch cuts are per- 3

formed using sight (color), smell, or a barrel counter. Almost every terminal has a densitometer located somewhere in the terminal; however, these are of little use in conducting batch cuts because of their location and speed. Because most batch cuts are seat-of-thepants operations, unnecessarily large volumes of perfectly good product are diverted to the transmix tank to minimize the risk of contamination. Figure 4 In order to significantly reduce transmix volume, one must be able to perform very accurate batch cuts during pipeline receipt. For example, when switching tanks from diesel to gasoline, one must have the ability to perform the batch cut at the beginning of the interface. A very small amount of low-sulfur diesel contamination in the gasoline tank generally will not cause an out-of-spec condition; however, a small amount of gasoline in a diesel tank will almost certainly cause unacceptable contamination. In order for accomplish highly accurate cuts on incoming batches of products, early detection and definition of the interface is necessary. The best way to accomplish this is to place interface detectors several minutes upstream of the tank manifolds. Because product interfaces are rarely normal, early detection and a definition of the interface is critical. In order to do this, an interface sensor must be located sufficiently upstream of the tank manifold so 4

as to allow the operators enough time to identify the interface and decide where within it the batch cut should be performed. Figure 5 Figure 5 shows the tandem Fueel lcheecckk sensor arrangement frequently implemented to conduct high-accuracy batch cuts in refined product pipelines. In this simplified example, diesel is being delivered to the tank on the left, followed by a batch of gasoline. Because of irregular valve operation at the originating pipeline terminal, or disruption of batch integrity in transit, abnormalities in interfaces such as the one shown in the example are extremely common. When making a batch cut from diesel to gasoline, it is necessary to make the cut early in the interface so as to prevent introducing gasoline into the diesel tank. If, however, only a single sensor located close to the incoming tank manifold is used, it is likely that the batch cut would be performed too early because of the anomalous blip just ahead of the actual interface. This could result in the sulfur content of the gasoline being increased above acceptable limits. When tandem sensors are employed as shown in this example, Probe A would provide sufficient time for the operator to properly assess the interface and decide where the batch cut should be conducted when it arrived at Probe B. 5

Figure 6 Additional benefits to this system configuration include the ability to save the data onto a computer or data logger and thus provide documentation of the batch changes. Certainly, identical response at 2 identical probes will assure high confidence in sensor integrity. Also, by placing a sensor sufficiently upstream of the terminal, the line could be shut down and samples obtained before the interface arrived at the manifold should an extremely anomalous event be observed. References 1 Tru Tec Services, Inc., Pipeline Transmix Study, World Wide Web, http://www.tru-tec.com/html/body_q2art31998.html 2 Petro Source Corporation, Tonopah Nevada Refinery, Transmix, World Wide Web, http://www.petrosourcecorp.com/asphalt_tonopah.htm#transmix 6