EFFECTS OF FORMATION DAMAGE ON OIL WELL PRODUCTIVITY

EFFECTS OF FORMATION DAMAGE ON OIL WELL PRODUCTIVITY

ABSTRACT

Formation damage has been a constant headache to the oil producing industries as it is considered an impairment of the permeability of petroleum bearing formation with an expensive remediation procedure. Although, the prevention of formation damage is impracticable since every single operation embarked upon in petroleum production is a potential source of damage, it could be controlled. In this project, a well was studied and BHP survey was used from BHP analysis in addition to the information of the well history and reservoir data available. The well was observed to have been damaged with a skin of 115 and a damage ratio indicating the well should have been flowing about two times its present production rate. There are two major stimulation procedures which are the hydraulic fracturing and the matrix acidization in which the latter was used in the case of the damaged well. Well 57XX had a production rate which was initially 1550bbl/day at its peak before undergoing a decline, increased to 2100bbl/day and then continued to flow at an average of 2000bbl/day before a sharp decline and subsequent gradual declination of production rate showing the effect formation damage had on the well 57XX. This in conclusion proved that the matrix acidization technique used to stimulate the well was effective as it led to an increase in the well permeability and hence, increased the oil production rate.

CHAPTER ONE/INTRODUCTION

1.1. General Background
Formation damage is generally considered as the impairment of the unseen by the inevitable, causing an unknown reduction in the unquantifiable (Petrowiki, 2015). Also, it is a condition which occurs when barriers to flow develop in the near-wellbore region to give rise to a lower than expected production rate from or injection rate into a hydrocarbon bearing reservoir rock and it requires interdisciplinary knowledge and expertise (Amaefule et al, 1988). It can also be referred to as an impairment to reservoir (reduced production) permeability caused by wellbore fluids used during drilling, completion and work over operations (Petrowiki, 2015).
Oil well productivity on the other hand, is generally considered as the ability of a reservoir to produce hydrocarbons after the well has been drilled and made ready for production. The production stage of oil is the most important stage of a well’s life because it determines if the aim of drilling such well has been achieved or not, and this can be measured by the quantity of crude oil derived or quantity of crude oil which is producible. Formation damage is one of the major causes of decrease in oil production as a result of damage to the formation by reducing its porosity and permeability which also leads to flow restrictions. Flow restrictions into the wellbore create additional pressure drops known as ‘skin’ and reduce well productivity.
Formation damage is known to occur during any stage of a well’s life; from initial exploration, through appraisal, through production and through secondary or tertiary recovery and all these have their various roles which they play in the reduction of oil well productivity. Formation damage indicators include, among others, permeability impairment, skin damage and decrease of well performance. Formation damage according to Porter (1989) is considered not necessarily reversible and what gets into the porous media does not necessarily come out. It is, therefore, better to avoid the occurrence of formation damage rather than trying to restore it. Models for formation damages which have been proven to be verified can be used to avoid or minimize it (Faruk, 2011). Carefully planned laboratory and field tests can also help in providing scientific guidance as well as develop strategies for minimizing the damage. It will, therefore, cause considerable cost for remediation and deferred production. Accurately designed experimental and analytical techniques with the modelling and simulation approaches can be used to understand the evaluation, prevention, remediation and the control of formation damage that leads to low oil productivity.
Formation damage can occur as a result of fluid/rock incompatibility; particle migration and deposition may occur as a function of the chemistry of the clay minerals and the chemical and electrochemical nature of both the natural formation fluid and the drilling fluid. Changes in the pore fluid can also induce clay swelling which in turn reduces the pore spaces in the reservoir and this is considered a form of damage to the formation as it reduces the productivity of the formation.

The occurrence of the fluid/rock incompatibility is not as a result of only swelling of the clay and particle migration and deposition. Formation damage can also occur as a result of the fluid/fluid incompatibility. The incompatibility of the introduced fluid (drilling fluid) and the reservoir pore-fluid which creates emulsion blocks can only be controlled by stimulation techniques that include pre-flush or after flush techniques. Formation damage caused by various fluids introduced into the well is remediated by careful treatment design and quality control. The departure from radial flow in a homogenous and isotropic medium can also be a cause of formation damage. A positive skin may arise from a reduction of the area available to flow and/or a departure from purely radial flow (Harper and Buller, 1986).

Formation damage also has other causes such as the mechanical deformation around a borehole or perforation tunnel, reduction of fluid pressure during production, etc. Thorough understanding of the formation damage mechanism’s stringent measures for its control and prevention, and effective and efficient treatments are the keys for optimum production strategies for oil and gas fields.
The consequences of formation damage are the reduction of the oil and gas productivity of reservoirs and noneconomic operation. Hence, once formation damage has occurred, it is necessary that proper assessment, planning and treatment will require the cooperative efforts and knowledge of the geologists, reservoir engineer and production engineer both in the field and in the laboratory. This combined effort and approach will therefore help to develop effective solutions to the damage. A wide knowledge of the mechanism of formation damage is necessary in order for the engineers and geologists to develop effective, preventive and mitigating procedures.
With recent improvements in technology, laboratory, geology and engineering, it is easier to achieve accurate measurements which can provide the necessary insights into the mechanism, prevention and effective treatment of formation damage (Amaefule et al., 1988). Confidence in formation damage prediction using models cannot be achieved without undergoing field testing as they are necessary for the verification of the models. After the verification of the model, it can then be applied for accurate simulation of the reservoir formation damage and designing effective measures for formation damage (Faruk, 2011).

Formation has varying characteristics and a formation damage model can be used to incorporate these variations into a history matching process for the characterization of reservoir systems which can also be used for accurate prediction of future performance. Recent literature surveys have had various arguments and debate about if formation damage is considered more detrimental for the vertical wells or for the horizontal ones. However, the fact still remains that in both cases, the production loss due to formation damage is significant.

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MODELLING, SIMULATION AND CONTROL OF A REACTIVE DISTILLATION PROCESS FOR FUEL ADDITIVE PRODUCTION

MODELLING, SIMULATION AND CONTROL OF A REACTIVE DISTILLATION PROCESS FOR FUEL ADDITIVE PRODUCTION

ABSTRACT
In this work, a reactive distillation process for the production of a fuel additive has been modelled, simulated and controlled using proportional-integral-derivative (PID) control method. The fuel additive considered was isopropyl alcohol that was produced from the reaction occurring between propylene and water, with diisopropyl ether as a side product. In accomplishing the work, the ChemCAD model of the process was first developed using SCDS Distillation Column #1 and the fluid package employed was UNIFAC property model. The ChemCAD column had 15 stages where the feed stream for water was the 6th stage and the one propylene was the 10th stage; the section of the column between the two feed streams was the reaction section of the column. After simulating the developed ChemCAD model to convergence, it was converted to dynamic type from which the dynamic responses of the system were generated and used with the aid of MATLAB to develop transfer function model having the reboiler duty, the reflux ratio and the temperature of the bottom product as the input variable, the disturbance and the output variables of the process, respectively. The obtained transfer function of the model was used to develop both open-loop and closed-loop Simulink models for the process that were used to carry out the open-loop and the closed-loop simulations of the process. The closed-loop simulation was carried out with the desire of achieving a fuel additive product with a mole fraction of 0.97. This was accomplished using a PID controller applied inferentially via the product temperature and tuned by trial-and-error technique. It was observed from the results obtained that isopropyl alcohol could be produced successfully from a reaction between propylene and water using reactive distillation suppressing the associated side reaction. It was also found out that it is possible to control the mole fraction of isopropyl alcohol inferentially using bottom temperature because temperature and mole fraction have been found to be dependent on each other. Finally, it has has been shown that a reactive distillation has been controlled to give high purity of isopropyl alcohol of approximately 0.97 mole fraction as the bottom product in the developed reactive distillation column using the PID controller with trial-and-error tuning technique.

TABLE OF CONTENTS
1.0 INTRODUCTION
1.1 Background of Study
1.2 Problem statement
1.3 Aim and Objectives
1.6 Significant of Study
CHAPTER TWO
2.0 THEORETICAL BACKGROUND AND LITERATURE REVIEW
2.1 Isopropyl Alcohol (IPA)
2.2 Properties of Isopropyl alcohol
2.2.1 Physical properties of IPA
2.2.2 Chemical properties of IPA
2.3 Uses of isopropyl alcohol
2.4 Concept of Reactive Distillation Process
2.5 Previous Study on Reactive Distillation of IPA
CHAPTER THREE
3.0 METHODOLOGY
3.1 Procedures for Model Development and Steady State simulation
3.2 Procedures for Dynamics Simulation
3.3 Procedures for Open loop Simulation of the Process
3.4 Procedures for Process Controller Tuning
3.5 Procedures for Simulink Modelling and Closed Loop Simulation of the Process
CHAPTER FOUR
4.0 RESULTS AND DISCUSSION
4.1 Process Steady State Results
4.2 Process Dynamics results
4.3 Open-Loop Response
4.4 Closed Loop Response
4.4.1 Servo closed-loop response

  • 4.4.2 Regulatory closed-loop response
    CHAPTER FIVE
    5.0 CONCLUSION AND RECOMMENDATION
    5.1 Conclusion
    5.2 Recommendation
    REFERENCES
    APPENDICES
    APPENDIX A
    APPENDIX B
    APPENDIX C
    APPENDIX D
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INTRODUCTION

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ENGINEERING DESIGN AND PREDICTION OF HYDRATE FORMATION FOR A GAS PIPELINE

ENGINEERING DESIGN AND PREDICTION OF HYDRATE FORMATION FOR A GAS PIPELINE

ABSTRACT

This research is focused on the difficulties that gas producers usually face with Hydrate formation during transportation. Hydrate build up in gas transportation flowlines is one of the major tasks for gas operators to deal with as it may cease gas flow through the pipeline, reduce well head measured flow rate, equipment damages e.t.c Two kinds of Engineering designs were developed to help transport gases of different pressures to an extension facility whose inlet pressures was designed at 8 barg. HYSYS VERSION 2006 was used for the simulation of these designs to check for the possibilities of Hydrate formation and recommendations were made based on the outputs.
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  • TABLE OF CONTENTS

  • CERTIFICATION ii

  • DEDICATION iii

  • ACKNOWLEDGEMENT iv

  • ABSTRACT v

  • LIST OF TABLES viii

  • LIST OF FIGURES ix

  • CHAPTER ONE 1

  • 1.0 INTRODUCTION 1

  • 1.1 Background Knowledge 2

  • 1.2 Aims and Objectives of the Project 3

  • 1.3 Justification 3

  • 1.4 Scope of work 4

  • 1.5 Problem Statement 4

  • 1.6 Facilities Schematics 5

  • CHAPTER TWO 7

  • 2.0 LITERATURE REVIEW 7

  • 2.1 Natural Gas Transportation through Pipelines 7

  • 2.2 Single Phase Pipe Flow 8

  • 2.2.1 General Pressure Drop Equations in Gas Flow 8

  • 2.2.2 Simplified Equation 9

  • 2.2.4 Panhandle Equation 11

  • 2.2.5 The Spitzglass Equation 12

  • 2.3 Flow Assurance 12

  • 2.4 Natural Gas Hydrates 14

  • 2.4.1 History of Natural Gas Hydrates 14

  • 2.4.2 Structure of Natural Gas Hydrate 15

  • 2.5 Flow Assurance Challenges and Control 18

  • CHAPTER THREE 21

  • 3.0 METHODOLOGY 21

  • 3.1 System Description and Simulation Model 21

  • 3.2 Basis of Design 23

  • 3.2.1 Design Basis Feed Composition 23

  • 3.2.2 Basis of Analysis 24

  • 3.2.3 Bulkline 24 vii

  • 3.2.4 Pipeline Hydraulic Profile 24

  • 3.3 HYSYS Simulation Modelling 24

  • 3.3.1 Hysys Compositional Modelling 25

  • 3.4 PIPESIM Simulation Modelling 25

  • 3.4.1 Pipesim Compositional Modelling 26

  • 3.5 Pipe Flow Models and Flowsheets 27

  • CHAPTER FOUR 30

  • 4.0 Analysis of Results 30

  • 4.1 Results achieved with the HYSYS simulation 30

  • 4.1.1 HYSYS simulation results for design A 30

  • 4.1.2 HYSYS simulation results for design B 33

  • 4.1.3 Comparison of Designs A and B from HYSYS Outputs 35

  • 4.2 Results achieved with the PIPESIM simulation 36

  • 4.2.1 Suitability of pipe various pipe sizes 36

  • 4.2.2 Outlet pressure analysis for design A & B 37

  • 4.2.3 Fluid Mean Velocity for 10 inches sch 40 pipe size 38

  • 4.2.4 Fluid Mean Velocity for 8 and 24 inches sch 40 pipe size 39

  • 5.0 CONCLUSION AND RECOMMENDATION 41

  • 5.1 Conclusion 41

  • 5.2 Recommendation 43

  • REFERENCES

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