Natural Gas Properties Analysis of Bangladesh: A Case Study of Titas Gas Field

Save this PDF as:
 WORD  PNG  TXT  JPG

Size: px
Start display at page:

Download "Natural Gas Properties Analysis of Bangladesh: A Case Study of Titas Gas Field"

Transcription

1 SUST Journal of Science and Technology, Vol. 16, No.2, 2012; P:26-31 Natural Gas Properties Analysis of Bangladesh: A Case Study of Titas Gas Field (Submitted: April 13, 2011; Accepted for Publication: December 13, 2011) Mohammad Islam Miah and M. Farhad Howladar 1 Dept. of Petroleum and Mining Engineering, Shahjalal University of Science and Technology, Sylhet, Bangladesh 1 Abstract Titas is the largest gas field in Bangladesh and the highest gas producer in the country at present which was discovered in 1962 by Shell Oil Company, Pakistan. In designing gas production, processing, transport and handling systems, a complete knowledge of natural gas properties is crucial. For this reason, a detailed research has been done for the measurement and prediction of hydrocarbon fluid properties. This research shows the reservoir of natural gas properties analysis of Titas gas field from gas composition. Based on the studied composition, it is shown that the Titas gas is a sweet gas. The specific gravity and apparent molecular weight of gas are and , respectively. The gas compressibility factor, super-compressibility factor, real gas density and gas formation volume factor are 0.94, 1.031, 9.48 lb m /ft 3, res ft 3 /scf, respectively. The Isothermal compressibility and viscosity of the gas are per psia and cp at reservoir formation temperature F and pressure 3689 psia. The estimated fluid properties are indicates that reservoir fluid type is semi-dry gas and these results are reliable for reserve estimation and well test analysis. Key Words: Composition, Specific Gravity, Formation Volume Factor, Isothermal Compressibility and Viscosity. 1. Introduction The Titas gas field was discovered by Shell Oil Company, Pakistan in 1962.This field is located (Figure-1) in Brahmanbaria district far from about 96 km E-N-E of Dhaka. The Titas field lies in the south central part of the Surma Basin and on the western margin of the Tripura high. The maximum flank dip to the east is 12 0 and that to the west is 6 0. The dip is much gentler in the north-south direction at 3 0 and indicates stronger compression and uplift. The structure was first mapped by Shell in 1960 with a single fold seismic grid. No faults were observed from the 2D seismic data over the Titas gas field and its vicinity. The stratigraphy of the field is related to the stratigraphy of the Surma Basin and is based on lithological correlation with rocks in the Assam oil fields. The formations that have been reached by wells in the Surma Basin are Dupi-Tila, Tipam, Bokabil and Bhuban Formation. Sediments deposited in the later stages of the Indian Plate collision include the Upper Bhuban and Bokabil units which are overlain by Tipam and Dupi-Tila. The reservoir sands in the area are composed of stacked sands which are divided into three groups A, B and C Sands (Figure-1). The most prolific are those of the Group-A Sands which are the dominated constituent of the reservoirs in the Titas Field [1]. In designing gas production, processing, transport, and handling systems a complete knowledge of petroleum properties is crucial. For this reason, the present research has been performed for the measurement and prediction of hydrocarbon fluid properties. The area of property prediction continues to attract significant attention from researchers who seek to optimize design and control of gas systems [2]. Knowledge of pressure-volume-temperature (PVT) relationships and other physical and chemical properties of gases are essential for prediction and solving problems in natural gas reservoir engineering. The physical properties of a natural gas may be obtained directly either by laboratory measurements or by prediction from the known chemical composition of the gas [3]. The type of the gas is sweet or sour; it can be identified mainly based on non-hydrocarbon gases percentages.

2 Natural Gas Properties Analysis of Bangladesh: A Case Study of Titas Gas Field 27 Drilled wells Gas sand A- Group sand B- Group sand C- Group sand West Eas Figure-1: Sub surface location of Titas field and gas bearing sands (Petrel software, Petrobangla) The properties of natural gases are apparent molecular weight, specific gravity and API gravity of gas, gas compressibility factor, super-compressibility factor, gas density, formation volume factor, isothermal compressibility and viscosity of gas. Interkomp Kanata Management studied about initial gas formation volume factor and viscosity at initial pressure and temperature conditions [4]. The objectives of this study are to identify the type of gas reservoir (sweet or sour) and natural gas properties analysis of Titas gas field. 2. Materials and Methods Brief Out Line about the Gas Composition and Used Different Charts Hydrocarbon molecular weight, pseudo-critical temperature and pressure for each component (Economides, 1994) and gas composition of A-Group sand [5] have been used for fluid properties estimation which is listed in Table-1. Reservoir formation temperature (T rf ) and pressure (P rf ) are F and 3689 psia have been used for reservoir fluid properties analysis of Titas gas field [4]. In the present research to complete the analysis properly, some well recognized charts have been used [6]. Table-1: Gas composition of A-group sand (IKM, 1991b) Gas composition Mole fraction (Y j ) C C C i- C n-c i-c n-c C C N H 2 S CO

3 28 Mohammad Islam Miah and M. Farhad Howladar Methodology of Gas Properties Analysis: How to Calculate the Molecular Weight and Gas Specific Gravity: The Apparent molecular weight (M a ) has been estimated from the product of each gas component (Y j ) and molecular weight (M j ) i.e. M a = Y j* M j [2]. The specific gravity of a gas is defined as the ratio of the density of the gas to the density of dry air with both measured at the same temperature and pressure [7]. The specific gravity (γ g ) is calculated from apparent molecular weight i.e. γ g = M a /28.97 [7]. Process of Estimating Gas Formation Volume Factor and Gas Density: The gas formation volume factor (B g ) is defined as the volume of gas at reservoir conditions required to produce one standard cubic foot of gas at the surface. The gas formation volume factor has been estimated as the following steps [2&7]: Step 1: Calculation the pseudo-critical temperature T pc and pseudo- critical pressure P pc, Step 2: Determination of the pseudo-reduced temperature T pr and pseudo-reduced pressure P pr, Step 3: Estimation of the gas compressibility factor (Z) from Standing and Katz chart [8] in Figure-2, Step 4: Calculation of gas formation volume factor. The real gas density (ρ g ) has been calculated as following equation [2]: ρ g = (PM/ZRT) where R is the universal gas constant. Figure-2: Gas compressibility factor (Z) chart (Standing et al, 1942) Steps of Estimating the Gas Compressibility and Viscosity: Isothermal gas compressibility is defined as the fractional change of volume as pressure is changed at constant temperature which has been calculated as the following steps:

4 Natural Gas Properties Analysis of Bangladesh: A Case Study of Titas Gas Field 29 Step-1: Estimation of the product of C pr (Pseudoreduced compressibility) and T pr from Pseudoreduced compressibilities chart for gases, Step-2: Estimation of C pr and gas isothermal compressibility [7] i.e. C g = (C pr /P pc ). The coefficient of viscosity is a measure of the resistance to flow exerted by a fluid. Usually, viscosity is given in units of centipoise (cp). The viscosity of a mixture of gases (µ g ) has been estimated as the following steps: Step-1: Calculation of the viscosity from chart [9] at 1 atmospheric (atm) pressure in Figure-3. Step-2: To take into account the effect of the presence of non-hydrocarbon gases using Figure-3. Step-3: Estimation of the viscosity of gas at elevated temperature-pressure from chart [9] in Figure-4. Figure-3: Viscosity chart at 1 atmospheric pressure (Carr et al, 1954 and Economides et al, 1994) Figure-4: Viscosity chart at elevated temperature-pressure (Carr et al, 1954 and Economides et al, 1994)

5 30 Mohammad Islam Miah and M. Farhad Howladar 3. Results and Discussions In Titas field, the gas composition of methane (mole fraction) is and H 2 S mole fraction is 0 (zero). Since methane is the predominant component of natural gases above 96% which indicate a sweet gas reservoir [10]. The gas composition is known and Kay s mixing rule has been used to calculate the pseudo-critical temperature & pressure. From the data analysis, a detailed reservoir gas properties results are shown in Table-2, 3 and 4. Table-2: Estimated gas compressibility factor (Z) and Formation volume factor of Titas gas field Reservoir Temperature Reservoir pressure Z-factor Gas formation volume factor, B g ( 0 R) (psia) (Dimensionless) ( res ft 3 /scf) Table-3: Apparent molecular weight and density of gas Specific gravity Molecular weight Real gas density, ρ g (Dimensionless) (Dimensionless) (lb m /ft 3 ) Pseudo-reduced Temperature, T pr (Dimensionless) Table-4: Estimated compressibility and viscosity of natural gases Pseudo-critical Pressure, P pr (psia) Product of C pr & T pr (Dimensionless) Gas compressibility, C g (per psia) Viscosity of gases, µ g (cp) The estimated pseudo-critical temperature and pressure are R and psia, respectively. The apparent molecular weight is The gas specific gravity is and API gravity is The gas Z-factor has been estimated from Standing and Katz chart (Figure-2) of 0.94 for sweet gas reservoir. This chart is generally more reliable for sweet natural gases with minor amounts of non-hydrocarbons such as N 2 and CO 2 [2] and supercompressibility factor is Gas compressibility factor may be changed if it is estimated by others methods and correlations. The estimated real gas density is lb m /ft 3 ( gm/cm 3 ) using universal gas constant (R) of The formation volume factor and expansion factor (1/B g ) are res ft 3 /scf and scf/ft 3 at reservoir formation temperature R and pressure 3689 psia, respectively. The real gas density, formation volume factor and isothermal gas compressibilities mainly depend on reservoir pressure, temperature as well as Z-factor. The Isothermal compressibility has been found of per psia using pseudo-reduced compressibility value ( per psia) and estimated Pseudo-critical pressure. The viscosity of hydrocarbon gases is cp at 1 atmosphere. The viscosity of all gases is cp including the effect of the presence of non-hydrocarbon gases at 1 atmosphere. The viscosity of A-group sand is cp at mentioned reservoir temperature and pressure. The effect of each of the non-hydrocarbon gases is to increase the viscosity of the gas mixture. Gas viscosity decreases with reservoir pressure decreases and vice versa. Viscosity of natural gases depends among reservoir temperature, pressure and gas compositions [7]. During gas production history of Titas gas field, some hydrocarbon liquid as condensate and water is produced [5] at the surface condition. The estimated fluid properties indicate that it is a semi-dry gas reservoir. 4. Conclusions Titas gas field is the largest gas producer in Bangladesh which is a sweet gas reservoir. The reservoir fluid type is semi-dry gas. The gas specific gravity is The gas compressibility factor, real gas density, formation volume factor and gas expansion factor are 0.94, lb m /ft 3, res ft 3 /scf and scf/ft 3, respectively. The Isothermal compressibility and viscosity of the gas are per psia and cp at reservoir formation temperature F and pressure 3689 psia. The estimated fluid properties are reliable and can be used for reserve estimation and well test analysis of Titas gas field.

6 Natural Gas Properties Analysis of Bangladesh: A Case Study of Titas Gas Field 31 Acknowledgement We are very much grateful to Mr. Md. Jakaria, Assistant professor, Department of Petroleum and Mining Engineering, Shahjalal University of Science and Technology, Sylhet and Mr. Mijanur Rahman, Deputy General Manager, Reservoir Engineering Department, BGFCL, Bangladesh, for their constructive criticism and overall advice regarding data processing and interpretation. References [1] Reservoir Management Project (RMP)-2, Titas Geological Study, Petrobangla, Bangladesh, p. 36, (2009). [2] Kumar, S., Gas Production Engineering, Gulf publishing Co. V. 4, Houston, Texas, p. 646, (1987). [3] Ahmed, Tarek, Hydrocarbon Phase Behavior, Volume 7, Gulf Publishing Company, Houston, Texas, p. 423, (1989). [4] Interkomp Kanata Management (IKM), Gas Field Appraisal Project: Reservoir Engineering Report, Titas Gas Field, Petrobangla, Bangladesh, p. 92, (1991b). [5] Interkomp Kanata Management (IKM), Gas Field Appraisal Project: Geological, Geophysical and Petrophysical Report, Titas Gas Field, Petrobangla, Bangladesh, p. 88, (1991a). [6] Economides, J. M. et al., Petroleum Production System, Prentice-Hall PTR, p. 611, (1994). [7] McCain, W. D. Jr., The Properties of Petroleum Fluids, second edition, Penn Well Publishing Co., Tulsa, Oklahoma, p. 548, (1990). [8] Standing, M. B. and Katz, D. L., Density of Natural Gases, Trans., AIME, 146, p , (1942). [9] Carr, N. L., Kobayashi, R. and Burrows, D. B., Viscosity of Hydrocarbon Gases under Pressure, Trans., AIME, 201, p , (1954). [10] Imam, B., Energy Resources of Bangladesh, First Edition, University Grants Commission Publication No. 89, Bangladesh, p. 280, (2005).

Optimization of Separator Train in Oil Industry

Optimization of Separator Train in Oil Industry Optimization of Separator Train in Oil Industry Pawan jain a M.E. Petroleum Engineering, Maharashtra Institute of Technology, Pune-411038 ---------------------------------------------------------------------***---------------------------------------------------------------------

More information

Abstract Introduction

Abstract Introduction SPE 7571 Simplified Correlations for Hydrocarbon Gas Viscosity and Gas Density Validation and Correlation of Behavior Using a Large-Scale Database F.E. Londono, R.A. Archer, and T. A. Blasingame, Texas

More information

Figure Vapor-liquid equilibrium for a binary mixture. The dashed lines show the equilibrium compositions.

Figure Vapor-liquid equilibrium for a binary mixture. The dashed lines show the equilibrium compositions. Another way to view this problem is to say that the final volume contains V m 3 of alcohol at 5.93 kpa and 20 C V m 3 of air at 94.07 kpa and 20 C V m 3 of air plus alcohol at 100 kpa and 20 C Thus, the

More information

Chapter 13 Gases, Vapors, Liquids, and Solids

Chapter 13 Gases, Vapors, Liquids, and Solids Chapter 13 Gases, Vapors, Liquids, and Solids Property is meaning any measurable characteristic of a substance, such as pressure, volume, or temperature, or a characteristic that can be calculated or deduced,

More information

CHAPTER 6: PERMEABILITY MEASUREMENT

CHAPTER 6: PERMEABILITY MEASUREMENT CHAPTER 6: PERMEABILITY MEASUREMENT Objective To measure the permeability of rock samples using a gas permeameter and to apply Klinkenberg effect corrections to obtain the liquid permeability. Introduction

More information

PVT analysis of. bottom hole sample from Well by Otto Rogne. STAT01 L EXPLORATION 81 PRODUCTlON LABORATORY

PVT analysis of. bottom hole sample from Well by Otto Rogne. STAT01 L EXPLORATION 81 PRODUCTlON LABORATORY PVT analysis of bottom hole sample from Well 3411 0-1 7 STAT01 L EXPLORATION 81 PRODUCTlON LABORATORY by Otto Rogne stcrtoil Den norske stats oljeselskap as Classification I Requested by J,Hanstveit, LET

More information

INVESTIGATION OF THE EFFECT OF STIMULATION TREATMENT AND CERTAIN PARAMETERS ON GAS WELL DELIVERABILIITY BY USING DIFFERENT ANALYSIS APPROACHES

INVESTIGATION OF THE EFFECT OF STIMULATION TREATMENT AND CERTAIN PARAMETERS ON GAS WELL DELIVERABILIITY BY USING DIFFERENT ANALYSIS APPROACHES ISSN 2394 7799 IJAETCS (214) Vol.1, No.1, 1-19 Research Article International Journal of Advancement in Engineering, Technology and Computer Sciences INVESTIGATION OF THE EFFECT OF STIMULATION TREATMENT

More information

CALCULATING THE SPEED OF SOUND IN NATURAL GAS USING AGA REPORT NO Walnut Lake Rd th Street Houston TX Garner, IA 50438

CALCULATING THE SPEED OF SOUND IN NATURAL GAS USING AGA REPORT NO Walnut Lake Rd th Street Houston TX Garner, IA 50438 CALCULATING THE SPEED OF SOUND IN NATURAL GAS USING AGA REPORT NO. 10 Jerry Paul Smith Joel Clancy JPS Measurement Consultants, Inc Colorado Engineering Experiment Station, Inc (CEESI) 13002 Walnut Lake

More information

CP Chapter 13/14 Notes The Property of Gases Kinetic Molecular Theory

CP Chapter 13/14 Notes The Property of Gases Kinetic Molecular Theory CP Chapter 13/14 Notes The Property of Gases Kinetic Molecular Theory Kinetic Molecular Theory of Gases The word kinetic refers to. Kinetic energy is the an object has because of its motion. Kinetic Molecular

More information

The Application of Temperature and/or Pressure Correction Factors in Gas Measurement

The Application of Temperature and/or Pressure Correction Factors in Gas Measurement The Application of Temperature and/or Pressure Correction Factors in Gas Measurement COMBINED BOYLE S CHARLES GAS LAWS To convert measured volume at metered pressure and temperature to selling volume at

More information

Petroleum Reservoir Rock and Fluid Properties

Petroleum Reservoir Rock and Fluid Properties second edition Petroleum Reservoir Rock and Fluid Properties Abhijit Y. Dandekar CRC Press Taylor & Francis Croup Boca Raton London NewYork CRC Press is an imprint of the Taylor & Francis an Croup, informa

More information

Calculation of Gas Density and Viscosity

Calculation of Gas Density and Viscosity Calculation of Gas Density and Viscosity Course No: H02-008 Credit: 2 PDH Harlan H. Bengtson, PhD, P.E. Continuing Education and Development, Inc. 9 Greyridge Farm Court Stony Point, NY 10980 P: (877)

More information

Chapter 13 Gases and Pressure. Pressure and Force. Pressure is the force per unit area on a surface. Force Area. Pressure =

Chapter 13 Gases and Pressure. Pressure and Force. Pressure is the force per unit area on a surface. Force Area. Pressure = Chapter 13 Gas Laws Chapter 13 Gases and Pressure Pressure and Force Pressure is the force per unit area on a surface. Pressure = Force Area Chapter 13 Gases and Pressure Gases in the Atmosphere The atmosphere

More information

LOW PRESSURE EFFUSION OF GASES revised by Igor Bolotin 03/05/12

LOW PRESSURE EFFUSION OF GASES revised by Igor Bolotin 03/05/12 LOW PRESSURE EFFUSION OF GASES revised by Igor Bolotin 03/05/ This experiment will introduce you to the kinetic properties of low-pressure gases. You will make observations on the rates with which selected

More information

ACOUSTIC VELOCITY FOR NATURAL GAS

ACOUSTIC VELOCITY FOR NATURAL GAS ACOUSTIC VELOCITY FOR NATURAL GAS Introduction Acoustic velocity data for natural gas is useful for determining liquid levels in oil or gas wells and locating obstructions in gas lines. Application of

More information

Control Valve Sizing. Sizing & Selection 3 P 1. P 2 (Outlet Pressure) P V P VC. CONTENTS Introduction Nomenclature Calculating C v

Control Valve Sizing. Sizing & Selection 3 P 1. P 2 (Outlet Pressure) P V P VC. CONTENTS Introduction Nomenclature Calculating C v Sizing & Selection 3 Control Valve Sizing CONTENTS Introduction 3-1 Nomenclature 3-1 Calculating for Liquids 3-3 Liquid Sizing Examples 3-7 Calculating for Gases 3-10 Gas Sizing Examples 3-13 Calculating

More information

Optimizing Effective Absorption during Wet Natural Gas Dehydration by Tri Ethylene Glycol

Optimizing Effective Absorption during Wet Natural Gas Dehydration by Tri Ethylene Glycol IOSR Journal of Applied Chemistry (IOSRJAC) ISSN : 2278-5736 Volume 2, Issue 2 (Sep-Oct. 212), PP 1-6 Optimizing Effective Absorption during Wet Natural Gas Dehydration by Tri Ethylene Glycol Khan, Mohd

More information

LOW PRESSURE EFFUSION OF GASES adapted by Luke Hanley and Mike Trenary

LOW PRESSURE EFFUSION OF GASES adapted by Luke Hanley and Mike Trenary ADH 1/7/014 LOW PRESSURE EFFUSION OF GASES adapted by Luke Hanley and Mike Trenary This experiment will introduce you to the kinetic properties of low-pressure gases. You will make observations on the

More information

Gases Day 12. Phases of Matter

Gases Day 12. Phases of Matter Phases of Matter Gases Day 12 Kinetic Molecular Theory ( Ideal Gases ) 1) The molecules of a gas are in continual, and random, motion of varying speeds. 2) The average kinetic energy of the gas molecules

More information

Figure 1 Schematic of opposing air bearing concept

Figure 1 Schematic of opposing air bearing concept Theoretical Analysis of Opposing Air Bearing Concept This concept utilizes air bearings to constrain five degrees of freedom of the optic as shown in the figure below. Three pairs of inherently compensated

More information

Modeling a Pressure Safety Valve

Modeling a Pressure Safety Valve Modeling a Pressure Safety Valve Pressure Safety Valves (PSV), Pressure Relief Valves (PRV), and other pressure relieving devices offer protection against overpressure in many types of hydraulic systems.

More information

Limitations of ASME PTC 10 in Accurately Evaluating Centrifugal Compressor Thermodynamic Performance ABSTRACT

Limitations of ASME PTC 10 in Accurately Evaluating Centrifugal Compressor Thermodynamic Performance ABSTRACT Proceedings of the Forty-Second Turbomachinery Symposium October 1-3, 2013, Houston, Texas Limitations of ASME PTC 10 in Accurately Evaluating Centrifugal Compressor Thermodynamic Performance Mark R. Sandberg,

More information

Kinetic Molecular Theory

Kinetic Molecular Theory Kinetic Molecular Theory Name Period Unit 7 HW 1 Worksheet (Goals 1 & 2) 1. Describe how gases, liquids, and solids compare using the following table. Volume (definite or indefinite) Molecular Motion (high,

More information

Natural Gas Desulfurization Process By MEA Amine: The preferable Engineering Design Procedure

Natural Gas Desulfurization Process By MEA Amine: The preferable Engineering Design Procedure Natural Gas Desulfurization Process By MEA Amine: The preferable Engineering Design Procedure Ribwar Abdulrahman 1, Ibtisam Kamal 2, Jagar Ali 3 1 Faculty of Engineering, KoyaUniversity, Kurdistan region,

More information

DISTILLATION POINTS TO REMEMBER

DISTILLATION POINTS TO REMEMBER DISTILLATION POINTS TO REMEMBER 1. Distillation columns carry out physical separation of liquid chemical components from a mixture by a. A combination of transfer of heat energy (to vaporize lighter components)

More information

Operating Parameters of Electrical Submersible Pump Simulation Using Excel

Operating Parameters of Electrical Submersible Pump Simulation Using Excel Operating Parameters of Electrical Submersible Pump Simulation Using Excel SUELEM SÁ DELA FONTE, GEORGE SIMONELLI Petroleum Engineer, Federal University of Bahia, Salvador/Ba, Brazil Federal University

More information

Gas Gathering System Modeling The Pipeline Pressure Loss Match

Gas Gathering System Modeling The Pipeline Pressure Loss Match PETROLEUM SOCIETY CANADIAN INSTITUTE OF MINING, METALLURGY & PETROLEUM PAPER 2005-230 Gas Gathering System Modeling The Pipeline Pressure Loss Match R.G. MCNEIL, P.ENG. Fekete Associates Inc. D.R. LILLICO,

More information

Optimized Gas Injection Rate for Underground Gas Storage; Sensitivity Analysis of Reservoir and Well Properties

Optimized Gas Injection Rate for Underground Gas Storage; Sensitivity Analysis of Reservoir and Well Properties Optimized Gas Injection Rate for Underground Gas Storage; Sensitivity Analysis of Reservoir and Well Properties Hadise Baghooee 1, Farhad Varzandeh 1, Masood Riazi 2,* 1. Chemical Engineering Department,

More information

Chapter 13. Gases. Copyright Cengage Learning. All rights reserved 1

Chapter 13. Gases. Copyright Cengage Learning. All rights reserved 1 Chapter 13 Gases Copyright Cengage Learning. All rights reserved 1 Section 13.1 Pressure Why study gases? An understanding of real world phenomena. An understanding of how science works. Copyright Cengage

More information

4.) There are no forces of attraction or repulsion between gas particles. This means that

4.) There are no forces of attraction or repulsion between gas particles. This means that KINETIC MOLECULAR (K-M) THEORY OF MATTER NOTES - based on the idea that particles of matter are always in motion - assumptions of the K-M Theory 1.) Gases consist of large numbers of tiny particles that

More information

Equipment Productivity

Equipment Productivity Arab Academy for Science, Technology & Maritime Transport College of Engineering & Technology Construction & Building Engineering CB 524 Methods and Equipment for Construction 2 Equipment Productivity

More information

PSI Chemistry: Gases Multiple Choice Review

PSI Chemistry: Gases Multiple Choice Review PSI Chemistry: Gases Multiple Choice Review Name Kinetic Molecular Theory 1. According to the kinetic-molecular theory, particles of matterare in constant motion (A) have different shapes (B) have different

More information

Pressure Data Analysis and Multilayer Modeling of a Gas-Condansate Reservoir

Pressure Data Analysis and Multilayer Modeling of a Gas-Condansate Reservoir Pressure Data Analysis and Multilayer Modeling of a Gas-Condansate Reservoir Fatema Akter Happy, Mohammad Shahedul Hossain, Arifur Rahman Department of Petroleum & Mining Engineering, Shahjalal University

More information

Petrophysical information (Verlo and Hatland, 2008)

Petrophysical information (Verlo and Hatland, 2008) Petrophysical information (Verlo and Hatland, 2008) The petrophysics of the Norne main field is based on data from the two exploration wells 6608/10 2 and 6608/10 3. In 1994 the exploration well 6608/10

More information

Enter your parameter set number (1-27)

Enter your parameter set number (1-27) 1- Helium balloons fly and balloons with air sink. Assume that we want to get a balloon that is just floating in the air, neither rising nor falling, when a small weight is placed hanging in the balloon.

More information

Pressure of the atmosphere varies with elevation and weather conditions. Barometer- device used to measure atmospheric pressure.

Pressure of the atmosphere varies with elevation and weather conditions. Barometer- device used to measure atmospheric pressure. Chapter 12 Section 1 Pressure A gas exerts pressure on its surroundings. Blow up a balloon. The gas we are most familiar with is the atmosphere, a mixture of mostly elemental nitrogen and oxygen. Pressure

More information

PMI Pulse Decay Permeameter for Shale Rock Characterization Yang Yu, Scientist Porous Materials Inc., 20 Dutch Mill Road, Ithaca NY 14850

PMI Pulse Decay Permeameter for Shale Rock Characterization Yang Yu, Scientist Porous Materials Inc., 20 Dutch Mill Road, Ithaca NY 14850 PMI Pulse Decay Permeameter for Shale Rock Characterization Yang Yu, Scientist Porous Materials Inc., 20 Dutch Mill Road, Ithaca NY 14850 This document describes the application of Pulse Decay Permeameter

More information

. In an elevator accelerating upward (A) both the elevator accelerating upward (B) the first is equations are valid

. In an elevator accelerating upward (A) both the elevator accelerating upward (B) the first is equations are valid IIT JEE Achiever 2014 Ist Year Physics-2: Worksheet-1 Date: 2014-06-26 Hydrostatics 1. A liquid can easily change its shape but a solid cannot because (A) the density of a liquid is smaller than that of

More information

Characteristics of Decompression Tank Internally Pressurized With Water Using OpenFOAM Syamsuri 1, a

Characteristics of Decompression Tank Internally Pressurized With Water Using OpenFOAM Syamsuri 1, a Applied Mechanics and Materials Submitted: 2015-11-26 ISSN: 1662-7482, Vol. 836, pp 3-8 Accepted: 2016-01-27 doi:10.4028/www.scientific.net/amm.836.3 Online: 2016-06-01 2016 Trans Tech Publications, Switzerland

More information

Chapter 13: The Behavior of Gases

Chapter 13: The Behavior of Gases Chapter 13: The Behavior of Gases I. First Concepts a. The 3 states of matter most important to us: solids, liquids, and gases. b. Real Gases and Ideal Gases i. Real gases exist, ideal gases do not ii.

More information

Introduction to Natural Gas Processing

Introduction to Natural Gas Processing Introduction to Natural Gas Processing John Jechura Professor of Practice Chemical & Biological Engineering Colorado School of Mines Course Objective Acquaint the student with the engineering & business

More information

What parameters do we use to describe gases? pressure: force/unit area 1 atm = 101 kpa; volume: liters (L) Temperature: K Amount of gas: moles

What parameters do we use to describe gases? pressure: force/unit area 1 atm = 101 kpa; volume: liters (L) Temperature: K Amount of gas: moles Gases Chapter 9 What parameters do we use to describe gases? pressure: force/unit area 1 atm = 101 kpa; volume: liters (L) Temperature: K Amount of gas: moles A gas consists of small particles that move

More information

Viscosity of Natural Gases

Viscosity of Natural Gases AMERICAS ISSTITUTE 01' MINIS(> AN11 METAI,I,UR(;ICAI, ENGISREIIS Technical Publication No. 1599 (CLASS G, PETROLEUM DIVISION, KO. IYI) DISCUSSION OF THIS PAPER IS INVITED. Discussion in writing (z copies)

More information

Critical Velocity/ Nodal Stability Gas Well Predictions

Critical Velocity/ Nodal Stability Gas Well Predictions Originally Presented at: Gas Well De-Liquification Workshop Adams Mark Hotel, Denver, Colorado March 5-7, 2007 European Conference Gas Well Deliquification 25-2626 September 2007 Critical Velocity/ Nodal

More information

10.4 Buoyancy is a force

10.4 Buoyancy is a force Chapter 10.4 Learning Goals Define buoyancy. Explain the relationship between density and buoyancy. Discuss applications of Archimedes principle. 10.4 Buoyancy is a force Buoyancy is a measure of the upward

More information

Yuan-Yun Lin 1 and Michael T. Myers 1 Search and Discovery Article #70299 (2017)** Abstract. References Cited

Yuan-Yun Lin 1 and Michael T. Myers 1 Search and Discovery Article #70299 (2017)** Abstract. References Cited PS Impact of Non-Linear Transport Properties on Low Permeability Measurements* Yuan-Yun Lin and Michael T. Myers Search and Discovery Article #799 (7)** Posted October 3, 7 *Adapted from poster presentation

More information

Drilling Efficiency Utilizing Coriolis Flow Technology

Drilling Efficiency Utilizing Coriolis Flow Technology Session 12: Drilling Efficiency Utilizing Coriolis Flow Technology Clement Cabanayan Emerson Process Management Abstract Continuous, accurate and reliable measurement of drilling fluid volumes and densities

More information

Date: Period: Gas Laws Worksheet #1 - Boyle s, Charles, Gay-Lussac s, and Combined Gas Law

Date: Period: Gas Laws Worksheet #1 - Boyle s, Charles, Gay-Lussac s, and Combined Gas Law Name: Date: Period: Gas Laws Worksheet #1 - Boyle s, Charles, Gay-Lussac s, and Combined Gas Law Boyle s Law: V1P1 = V2P2 1. A gas sample contained in a cylinder equipped with a moveable piston occupied

More information

Gases and Pressure SECTION 11.1

Gases and Pressure SECTION 11.1 SECTION 11.1 Gases and In the chapter States of Matter, you read about the kineticmolecular theory of matter. You were also introduced to how this theory explains some of the properties of ideal gases.

More information

Reservoir Simulator Practical

Reservoir Simulator Practical Reservoir Simulator Practical Course Notes 2012 Philipp Lang IZR Room 403 Tel 3004 philipp.lang@unileoben.ac.at for further information please refer to the accompanying document Info Sheet & Course Logistics

More information

CEE 452/652. Week 9, Lecture 2 Absorption. Dr. Dave DuBois Division of Atmospheric Sciences, Desert Research Institute

CEE 452/652. Week 9, Lecture 2 Absorption. Dr. Dave DuBois Division of Atmospheric Sciences, Desert Research Institute CEE 452/652 Week 9, Lecture 2 Absorption Dr. Dave DuBois Division of Atmospheric Sciences, Desert Research Institute Today s topics Today s topic: chapter 13 on absorption Cover odor control on Tuesday,

More information

To play movie you must be in Slide Show Mode CLICK HERE EXERCISE! EXERCISE! To play movie you must be in Slide Show Mode CLICK HERE

To play movie you must be in Slide Show Mode CLICK HERE EXERCISE! EXERCISE! To play movie you must be in Slide Show Mode CLICK HERE Boyle s Law Boyle s law Pressure and volume are inversely related (constant T, temperature, and n, # of moles of gas). PV k (kis a constant for a given sample of air at a specific temperature) P V P V

More information

Elements that exist as gases at 25 o C and 1 atmosphere H 2, N 2, O 2, F 2, Cl 2, He, Ne, Ar, Kr, Xe, Rn

Elements that exist as gases at 25 o C and 1 atmosphere H 2, N 2, O 2, F 2, Cl 2, He, Ne, Ar, Kr, Xe, Rn AP Chemistry Chapter 5 Sections 5. 5.9 Note Organizer Pressure, The Gas Laws of Boyle, Charles, and Avogadro, The Ideal Gas Law, Gas Stoichiometry, Dalton s Law of Partial Pressure, The Kinetic olecular

More information

PTRT 2470: Petroleum Data Management 3 - Facilities Test 4 (Spring 2017)

PTRT 2470: Petroleum Data Management 3 - Facilities Test 4 (Spring 2017) Use scantron to answer all questions PTRT 2470: Petroleum Data Management 3 - Facilities Test 4 (Spring 2017) 1. The term dehydration of natural gas means A. addition of water vapor B. removal of water

More information

Situated 250km from Muscat in

Situated 250km from Muscat in CYAN MAGENTA YELLOW BLACK GRAVITY GAINS A novel method of determining gas saturation has proved successful in Oman s Natih Field where conventional methods were giving anomalous results in difficult conditions.

More information

ResLab RESERVOIR LABORATORIES AS

ResLab RESERVOIR LABORATORIES AS , Laboratories AS Fabrikkvn 35-37 P.O.Box 291 N-4066 Stavanger Norway Telephone: + 47 51 81 66 00 Telefax: +4751816610 Internett: http://www.reslab.com RESERVOIR LABORATORIES AS Final Report Transfer and

More information

UNIT 10 - GASES. Notes & Worksheets - Honors

UNIT 10 - GASES. Notes & Worksheets - Honors Ideal Gas Equation 1 WKSHT 1.) What is the pressure exerted by 2.0 moles of an ideal gas when it occupies a volume of 12.0 L at 373 K? 2.) A flashbulb of volume 2.6 cm 3 contains O 2 gas at a pressure

More information

Numerical Simulation of Instability of Geothermal Production Well

Numerical Simulation of Instability of Geothermal Production Well GRC Transactions, Vol. 37, 2013 Numerical Simulation of Instability of Geothermal Production Well Ryuichi Itoi 1, Yasunari Katayama 3, Toshiaki Tanaka 1, Naoto Kumagai 2, and Takaichi Iwasaki 3 1 Department

More information

Deep water plume models - What s special about deep water

Deep water plume models - What s special about deep water Deep water plume models - What s special about deep water Øistein Johansen Senior scientist SINTEF Marine Environmental Technology Deep water blowouts - knowledge basis Present knowledge based on General

More information

Process Nature of Process

Process Nature of Process AP Physics Free Response Practice Thermodynamics 1983B4. The pv-diagram above represents the states of an ideal gas during one cycle of operation of a reversible heat engine. The cycle consists of the

More information

1. Add a new Annex B.8 to read as follows:

1. Add a new Annex B.8 to read as follows: NFPA 69-2014 Edition Standard on Explosion Prevention Systems TIA Log No.: 1212 Reference: Annex B.8 (new) Comment Closing Date: February 19, 2016 Submitter: Martin Clouthier, Clouthier Risk Engineering,

More information

Lecture Presentation. Chapter 10. Gases. John D. Bookstaver St. Charles Community College Cottleville, MO Pearson Education, Inc.

Lecture Presentation. Chapter 10. Gases. John D. Bookstaver St. Charles Community College Cottleville, MO Pearson Education, Inc. Lecture Presentation Chapter 10 John D. Bookstaver St. Charles Community College Cottleville, MO Characteristics of Unlike liquids and solids, gases Expand to fill their containers. Are highly compressible.

More information

INTRODUCTION Porosity, permeability, and pore size distribution are three closely related concepts important to filter design and filter performance.

INTRODUCTION Porosity, permeability, and pore size distribution are three closely related concepts important to filter design and filter performance. Measurement of Filter Porosity using a Custom-Made Pycnometer George Chase The University of Akron INTRODUCTION Porosity, permeability, and pore size distribution are three closely related concepts important

More information

Enbridge G & P (East Texas) LP EXAMINER S REPORT AND PROPOSAL FOR DECISION STATEMENT OF THE CASE

Enbridge G & P (East Texas) LP EXAMINER S REPORT AND PROPOSAL FOR DECISION STATEMENT OF THE CASE OIL AND GAS DOCKET NO. 05-0263914 THE APPLICATION OF ENBRIDGE G & P (EAST TEXAS) LP FOR AUTHORITY PURSUANT TO STATEWIDE RULES 9 AND 36 TO DISPOSE OF OIL AND GAS WASTE CONTAINING HYDROGEN SULFIDE INTO ITS

More information

Frequently Asked Questions (FAQ s)

Frequently Asked Questions (FAQ s) NTL No. 2015-N01 Information Requirements for Exploration Plans, Development and Production Plans, and Development Operations Coordination Documents on the OCS for Worst Case Discharge and Blowout Scenarios

More information

Name: Chapter 13: Gases

Name: Chapter 13: Gases Name: Chapter 13: Gases Gases and gas behavior is one of the most important and most fun things to learn during your year in chemistry. Here are all of the gas notes and worksheets in two packets. We will

More information

Experimental Study of an Air Lift Pump

Experimental Study of an Air Lift Pump Engineering, Technology & Applied Science Research Vol. 7, No. 3, 217, 1676-168 1676 Experimental Study of an Air Lift Pump Fawzy Sh. Abou Taleb Mechanical Engineering Department Engineering College Northern

More information

An Investigation of Liquid Injection in Refrigeration Screw Compressors

An Investigation of Liquid Injection in Refrigeration Screw Compressors An Investigation of Liquid Injection in Refrigeration Screw Compressors Nikola Stosic, Ahmed Kovacevic and Ian K. Smith Centre for Positive Displacement Compressor Technology, City University, London EC1V

More information

Operating Guidelines for PermSelect Modules Liquid Contacting

Operating Guidelines for PermSelect Modules Liquid Contacting Operating Guidelines for PermSelect Modules Liquid Contacting PermSelect PDMSXA-2500 (0.25m 2 ) PermSelect PDMSXA-7500 (0.75m 2 ) PermSelect PDMSXA-1.0 (1m 2 ) PermSelect PDMSXA-2.1 (2.1m 2 ) PermSelect

More information

Colorado Oil and Gas Conservation Commission

Colorado Oil and Gas Conservation Commission Colorado Oil and Gas Conservation Commission http://cogcc.state.co.us/ FORM 5A Completed Interval Report INDUSTRY TRAINING Denver, Colorado November 27, 2012 Form 5A Completed Interval Report Introduction

More information

Single & Headered Relief Vent Piping Analysis

Single & Headered Relief Vent Piping Analysis Single & Headered Relief Vent Piping Analysis Todd Jekel, Ph.D., P.E. Industrial Refrigeration Consortium 2005 Research & Technology Forum January 21, 2005 Madison, WI 1 Purpose Vent piping requirements

More information

Influence of Fly Ash Content on Compaction Characteristics of Fly Ash Clay Mixture

Influence of Fly Ash Content on Compaction Characteristics of Fly Ash Clay Mixture Jordan Journal of Civil Engineering, Volume, No. 1, 16 Influence of Fly Ash Content on Compaction Characteristics of Fly Ash Clay Mixture Ashis Kumar Bera 1)* and Sayan Kundu 2) 1) Associate Professor

More information

Guidance for Complying with BOEM NTL No N06 on Worst Case Discharge for Offshore Wells

Guidance for Complying with BOEM NTL No N06 on Worst Case Discharge for Offshore Wells Guidance for Complying with BOEM NTL No. 2010- N06 on Worst Case Discharge for Offshore Wells Society of Petroleum Engineers August 26, 2010 Chair: Tim Magner, Chevron Committee Members Jonathan Harris,

More information

Name: Class: Date: SHORT ANSWER Answer the following questions in the space provided.

Name: Class: Date: SHORT ANSWER Answer the following questions in the space provided. CHAPTER 11 REVIEW Gases SECTION 1 SHORT ANSWER Answer the following questions in the space provided. 1. Pressure =. For a constant force, when the surface area is tripled the pressure is (a) doubled. (b)

More information

To convert to millimeters of mercury, we derive a unit factor related to the equivalent relationship 29.9 in. Hg = 760 mm Hg.

To convert to millimeters of mercury, we derive a unit factor related to the equivalent relationship 29.9 in. Hg = 760 mm Hg. Example Exercise 11.1 Gas Pressure Conversion Meteorologists state that a falling barometer indicates an approaching storm. Given a barometric pressure of 27.5 in. Hg, express the pressure in each of the

More information

Lawrence Berkeley National Laboratory Lawrence Berkeley National Laboratory

Lawrence Berkeley National Laboratory Lawrence Berkeley National Laboratory Lawrence Berkeley National Laboratory Lawrence Berkeley National Laboratory Title Mixing of and in gas reservoirs: Code comparison studies Permalink https://escholarship.org/uc/item/879394qk Authors Oldenburg,

More information

and its weight (in newtons) when located on a planet with an acceleration of gravity equal to 4.0 ft/s 2.

and its weight (in newtons) when located on a planet with an acceleration of gravity equal to 4.0 ft/s 2. 1.26. A certain object weighs 300 N at the earth's surface. Determine the mass of the object (in kilograms) and its weight (in newtons) when located on a planet with an acceleration of gravity equal to

More information

Application of Expansive Soil Geotechnical Procedures

Application of Expansive Soil Geotechnical Procedures Application of Expansive Soil Geotechnical Procedures FPA PRESENTATION John T. Bryant, Ph.D., P.G., P.E with Robert L. Lytton, Ph.D., PE. And Mr. Dean Read HOUSTON, TEXAS WEDNESDAY DECEMBER 10, 2008 2008

More information

New power in production logging

New power in production logging New power in production logging Locating the zones where fluids enter the wellbore in a producing or injecting well is an important aspect of production logging. It is relatively straightforward to establish

More information

TSUNAMI IMPACT ON FUEL STORAGE CONTAINERS

TSUNAMI IMPACT ON FUEL STORAGE CONTAINERS TSUNAMI IMPACT ON FUEL STORAGE CONTAINERS Hillary Brooker Lehigh University Project PI: Clay Naito Lehigh University NEES REU Program August, 2011 Abstract The Tohoku Japan tsunami in 2011 caused many

More information

Increase in Evaporation Caused by Running Spa Jets swhim.com

Increase in Evaporation Caused by Running Spa Jets swhim.com Increase in Evaporation Caused by Running Spa Jets swhim.com Nomenclature A pipe cross-section area, m D water inlet diameter of the venturi tube nozzle, mm diameter of small end of the throat of the venturi

More information

SPE Combining Absorption and AVO Seismic Attributes Using Neural Networks to High-Grade Gas Prospects

SPE Combining Absorption and AVO Seismic Attributes Using Neural Networks to High-Grade Gas Prospects SPE-154215 Combining Absorption and AVO Seismic Attributes Using Neural Networks to High-Grade Gas Prospects A. Rahimi Zeynal, University of Southern California F. Aminzadeh, University of Southern California

More information

Case Study Results on Natural Gas Custody Transfer Measurement with Coriolis Meters in Saudi Arabia

Case Study Results on Natural Gas Custody Transfer Measurement with Coriolis Meters in Saudi Arabia Case Study Results on Natural Gas Custody Transfer Measurement with Coriolis Meters in Saudi Arabia Introduction Mohammed Al-Torairi: Saudi Aramco mohammed.torairi@aramco.com WC-1337, Al-Midra Tower Dhahran

More information

Vortex flowmeters. Product family introduction Principle of operation Product review Applications Key product features

Vortex flowmeters. Product family introduction Principle of operation Product review Applications Key product features Vortex flowmeters introduction Product review s Key product features This document should not be duplicated, used, distributed, or disclosed for any purpose unless authorized by Siemens. Page 1 Vortex

More information

Modeling air mass flow into a football and resulting pressure after cooling

Modeling air mass flow into a football and resulting pressure after cooling Modeling air mass flow into a foot and resulting pressure after cooling Dr. Joseph S. Jewell www.joejewell.com 1 February 2015 Abstract: Realistic modeling of the rapid filling process for a foot, neglected

More information

Temperature Influence on the Flammability Limits of Heat Treating Atmospheres

Temperature Influence on the Flammability Limits of Heat Treating Atmospheres Temperature Influence on the Flammability Limits of Heat Treating Atmospheres John Dwyer, Jr., James G. Hansel, Tom Philips Air Products and Chemicals, Inc., Allentown, PA Abstract The flammability limits

More information

Assistant Lecturer Anees Kadhum AL Saadi

Assistant Lecturer Anees Kadhum AL Saadi Pressure Variation with Depth Pressure in a static fluid does not change in the horizontal direction as the horizontal forces balance each other out. However, pressure in a static fluid does change with

More information

TABLE OF CONTENTS LIST OF FIGURES

TABLE OF CONTENTS LIST OF FIGURES CG39AGA-1 CONTENTS TABLE OF CONTENTS SECTION AND TITLE PAGE 1.0 INTRODUCTION... 1-1 1.1 PRODUCT DESCRIPTION... 1-1 1.2 PRODUCT SUPPORT... 1-8 1.3 RELATED LITERATURE... 1-9 2.0 AGA3... 2-1 3.0 TURBINE_METER...

More information

Simposium Nasional dan Kongres X Jakarta, November 2008 Makalah Profesional IATMI

Simposium Nasional dan Kongres X Jakarta, November 2008 Makalah Profesional IATMI Simposium Nasional dan Kongres X Jakarta, 12 14 November 2008 Makalah Profesional IATMI 08 018 Experimental Treatments for Fluid-Blocked Gas Wells By Melvin Devadass, Technical Manager, 3M Oil & Gas Markets,

More information

A GAS CORRECTION FOR THE SEPARATOR METHOD USED IN GEOTHERMAL WELL TESTING

A GAS CORRECTION FOR THE SEPARATOR METHOD USED IN GEOTHERMAL WELL TESTING 13thNew Zealand Geothermal Workshop 1991 99 A GAS CORRECTION FOR THE SEPARATOR METHOD USED IN GEOTHERMAL WELL TESTING SUWANA Pertamina EP-Divisi Panasbumi,Jakarta, Indonesia geothermal well can be tested

More information

By: Eng. Ahmed Deyab Fares - Mobile:

By: Eng. Ahmed Deyab Fares -  Mobile: Distillation Column 1 Workshop Separation of light products is present in any Hydrocarbons operations. In this module, a column will be modeled to separate Light and heavy components from each other using

More information

Moyno ERT Power Sections. Operational Guidelines

Moyno ERT Power Sections. Operational Guidelines Moyno ERT Power Sections Operational Guidelines Moyno ERT Power Section Operational Guidelines Index 1. Introduction... 3 2. ERT Performance Graph Interpretation... 3 3. Elastomer Compression (Fit) Recommendations...

More information

Comprehensive Analysis To Assess And Remove Causes Of Decline Flow In An Offshore Compression Module.

Comprehensive Analysis To Assess And Remove Causes Of Decline Flow In An Offshore Compression Module. Comprehensive Analysis To Assess And Remove Causes Of Decline Flow In An Offshore Compression Module. Vladimir Alexis Neri Quezadas, Abstract: In a three stages compression module, at an offshore installation,

More information

MODELLING PIPELINE DECOMPRESSION DURING THE PROPAGATION OF A DUCTILE FRACTURE

MODELLING PIPELINE DECOMPRESSION DURING THE PROPAGATION OF A DUCTILE FRACTURE MODELLING PIPELINE DECOMPRESSION DURING THE PROPAGATION OF A DUCTILE FRACTURE R.P. Cleaver and P.S. Cumber BG Technology Gas Research and Technology Centre Ashby Road, Loughborough, LE11 3GR There is considerable

More information

Lecture Outline Chapter 15. Physics, 4 th Edition James S. Walker. Copyright 2010 Pearson Education, Inc.

Lecture Outline Chapter 15. Physics, 4 th Edition James S. Walker. Copyright 2010 Pearson Education, Inc. Lecture Outline Chapter 15 Physics, 4 th Edition James S. Walker Chapter 15 Fluids Density Units of Chapter 15 Pressure Static Equilibrium in Fluids: Pressure and Depth Archimedes Principle and Buoyancy

More information

THE SIGNIFICANCE OF HAZARD ENDPOINTS IN QUANTITATIVE RISK ANALYSIS

THE SIGNIFICANCE OF HAZARD ENDPOINTS IN QUANTITATIVE RISK ANALYSIS THE SIGNIFICANCE OF HAZARD ENDPOINTS IN QUANTITATIVE RISK ANALYSIS John B. Cornwell and Jeffrey D. Marx Presented At 6 Process Plant Safety Symposium Houston, Texas April -2, 6 Presented By Quest Consultants

More information

TWO PHASE FLOW METER UTILIZING A SLOTTED PLATE. Acadiana Flow Measurement Society

TWO PHASE FLOW METER UTILIZING A SLOTTED PLATE. Acadiana Flow Measurement Society TWO PHASE FLOW METER UTILIZING A SLOTTED PLATE Acadiana Flow Measurement Society Gerald L. Morrison Presented by: Mechanical Engineering Department Daniel J. Rudroff 323 Texas A&M University Flowline Meters

More information

EXAMINER S REPORT AND RECOMMENDATION STATEMENT OF THE CASE

EXAMINER S REPORT AND RECOMMENDATION STATEMENT OF THE CASE OIL AND GAS DO0KET NO. 01-0249550 THE APPLICATION OF REGENCY FS LP UNDER RULE 36 AND RULE 46 TO DISPOSE OF OIL AND WASTE CONTAINING HYDROGEN SULFIDE GAS INTO ITS TILDEN GPI WELL NO. 1, TILDEN, S. (WILCOX

More information

New low temperature technologies of natural gas processing

New low temperature technologies of natural gas processing New low temperature technologies of natural gas processing Salavat Imaev, Vasily Borisov, Sergey Bordachev, ENGO Engineering, Ltd. Abstract Over the past 10 years a number of companies have been working

More information

USE OF MULTIPHASE METERS IN PROCESS CONTROL FOR OIL FIELD WELL TESTING: PERFORMANCE ENHANCEMENT THROUGH GVF CONTROL

USE OF MULTIPHASE METERS IN PROCESS CONTROL FOR OIL FIELD WELL TESTING: PERFORMANCE ENHANCEMENT THROUGH GVF CONTROL Proceedings of ETCE22 ASME Engineering Technology Conference on Energy February 4-6, 22, Houston, TX ETCE22/MANU-292 USE OF MULTIPHASE METERS IN PROCESS CONTROL FOR OIL FIELD WELL TESTING: PERFORMANCE

More information