Feasibility Study on DCA Microspheres for Deep Profile Control Technology in High Permeability of High Temperature and High salt Reservoirs Changchun Yang.

Slides:



Advertisements
Similar presentations
The influence of wettability and carbon dioxide injection on hydrocarbon recovery Saif Al Sayari Martin J. Blunt.
Advertisements

Outline of Presentation
Surfactant/Polymer Flood of Midland Farms Dolomite Core D6
Preformed Particle Gel (PPG) for Conformance Control
Pore-scale modelling of carbonates 1 Hiroshi Okabe Petroleum Engineering and Rock Mechanics Research Group Department of Earth Science and Engineering.
Petroleum & Natural Gas Eng. Dept.
Dr. Mohammed M. Amro Petroleum Engineering Dept. King Saud University Effect of Scale and Corrosion Inhibitors on Well Productivity in Reservoirs Containing.
CIPC Application of X-Ray CT for Investigation of CO 2 and WAG Injection in Fractured Reservoirs D. Chakravarthy, V. Muralidharan, E. Putra and.
BrightWater® – A Step Change in Sweep Improvement
Texas A&M UniversityFeb, 2004 Application of X-Ray CT to Investigate Effect of Rock Heterogeneity and Injection Rates During CO 2 Flood Process Deepak.
3D Images of residual oil in an Ottawa sand Congjiao Xie, Saif Ai-Sayari and Martin Blunt Earth Science and Engineering, Imperial College London.
Upscaling of Foam Mobility Control to Three Dimensions Busheng Li George Hirasaki Clarence Miller Rice University, Houston, TX.
Imperial College, PETROLEUM ENGINEERING AND ROCK MECHANICS GROUP 10 th January 2003 PETROLEUM ENGINEERING AND ROCK MECHANICS GROUP Pore Scale Modeling.
CO 2 Foam Mobility Control and Adsorption with Nonionic Surfactant Michael Guoqing Jian, Leyu Cui, Lisa Biswal, George Hirasaki 04/22/2015.
Classification: Internal Introduction to flow diversion technologies Force workshop, Stavanger, January
Rheology of Viscoelastic surfactants and foam in homogeneous porous media Aarthi Muthuswamy, Clarence Miller, Rafael Verduzco and George Hirasaki Chemical.
07/ This document is the property of SNF. It must not be reproduced or transfered without prior consent Enhanced Oil Recovery Optimizing Molecular.
Rhodia/Poweltec Visosifying Surfactant for Chemical EOR EOR Workshop “Mario Leschevich”, 3-5 Nov Mikel Morvan, Guillaume Degré, Rhodia Alain.
Modelling the field potential of in- depth waterflood diversion with Brightwater Mechanism of Brightwater activation and diversion Preferred modelling.
CBE 555: Chemical EngineeringConnections: Impact of Chemical Engineering on the Outside World Tertiary Oil Recovery Steve Ng Kim Hoong 16 October 2007.
CHROMATOGRAPHY Chromatography basically involves the separation of mixtures due to differences in the distribution coefficient.
 Completed slim-tube tests for MMP measurement.  Completed swelling tests.  Completed phase behavior model.  Completed preliminary geological model.
China University of Petroleum, Beijing In-depth Profile Control Property of Pre-crosslinked Polymer Dispersion Jiao Lu, Bo Peng, Mingyuan Li, Meiqin Lin,
Snorre in-depth water diversion using silicate Arne Stavland, Hilde Jonsbråten, Olav Vikane, IRIS Kjetil Skrettingland and Herbert Fischer, Statoil FORCE.
Ran Qi, Valcir T Beraldo, Tara C LaForce, Martin J Blunt Design of CO 2 storage in aquifers 17 th Jan Imperial College Consortium on Pore-Scale Modelling.
Adel Sharif University of Surrey
2015 International Perforating Symposium Europe 2015 International Perforating Symposium Europe 1 PENETRATION OF HIGH DENSITY TUNGSTEN BASE POROUS JETS.
Research Institute of Petroleum Industry
ENGINEERING MATERIALS Haseeb Ullah Khan Jatoi Department of Chemical Engineering UET Lahore.
Company “IDZHAT” Technologies for enhanced oil layer recovery by application of polymer dispersion systems (PDS) and their modification (MPDS) (PDS) and.
The Cell Membrane. Cell Environment Plasma membrane is the boundary that separates cells from their environment. Its function is to regulate what enters.
Anatoly Stoyanov UKOILSERVICE LIMITED. Water production is one of the major technical, environmental, and economical problems associated with oil and.
Critical Parameters of a Horizontal Well in a Bottom Water Reservoir Department: Southwest Petroleum University Address: No.8,
This study processes the optimization of heat extraction under the varied pressure and flow rate. Based on the validated model, two kinds of test tube.
Date of download: 11/12/2016 Copyright © ASME. All rights reserved. From: Characterization and Prediction of Gas Breakthrough With Cyclic Steam and Gas.
The Experimental study of supercritical CO 2 flow in the porous media for the heat transfer of EGS Reporter :Ming-Che Chung Date : 2014/07/01.
Fluid Sampling and Hydrates. Group Members:  Mohammad Afaq Akbar(23)  Nisar Ali(39)  Saif Ur Rehman(43)  Shahnawaz(46)  Uzair Ahmed Khan(49)
Idar Akervoll, SINTEF Petroleum, Trondheim
Understanding Liquids and Gases
Green Oil Recovery (GRO) UAE Innovation on Oil Recovery
Capillary End Effects during Core Flooding – Analytical Solutions and Capillary Numbers accounting for Saturation Functions Pål Østebø Andersen, Postdoc.
The Physical and Chemical Properties of the Ocean
Permeability analysis of influencing factors of tight reservoir cores with high pressure    Weiqing An Key Laboratory of Petroleum Engineering, Ministry.
SPE MS Experience of Microbial Enhanced Oil Recovery Methods
Gas Condensate PVT – What’s Really Important and Why?
超臨界CO2在增強型地熱系統儲集層中取熱之研究-子計畫三 CO2在增強型地熱系統取熱模型之建構及效能分析
Dual Mesh Method in Dynamic Upscaling
Wettability in reservoir engineering.
CO2 EOR and Sequestration Technologies in PetroChina
Pouyan Ebrahimi, Javier Vilcáez Abstract ID: GSA
Xiaomin Pang, Yanyan Chen, Xiaotao Wang, Wei Dai, Ercang Luo
Unconventional Reservoirs
on Petroleum and Refinery
SEDIMENTATION 9/11/2018.
By: Engr. Hassaan Bin Younis
Chapter Two Part 1 Classifying Matter Properties of Matter.
Enhanced Oil Recovery by Nitrogen and Carbon Dioxide Injection Followed by Low Salinity Water Flooding in Tight Carbonate Reservoir: A Laboratory Study.
Supercritical Fluid Chromatography and Extraction
Studies on the Impacts from Different Activators and Inorganic Components of Curing Agents on Performance of Solidifiable Plugging Fluid Author: Xiaoyang.
Refinery: Separation units
How are Elements, Compounds and Mixtures Similar? Different?
East China University of Science and Technology
Introduction to Effective Permeability and Relative Permeability
Heat Exchangers Heat Exchangers.
BASICS OF SUPERCRITICAL FLUID CHROMATOGRAPHY
Mohr Separations Research, Inc.
Classifying Matter Properties of Matter.
Condensate blockage is the build-up of liquid around the wellbore, reducing the effective gas permeability and lowering well deliverability.  Condensate.
Chapter Two Part 1 Classifying Matter Properties of Matter.
Presentation transcript:

Feasibility Study on DCA Microspheres for Deep Profile Control Technology in High Permeability of High Temperature and High salt Reservoirs Changchun Yang (doctoral supervisor:Xiang’an Yue) China University of Petroleum(Beijing) July 21, 2016 Brisbane

Laboratory of Enhanced Oil & Gas Recovery Basic Information Laboratory of Enhanced Oil & Gas Recovery in Complex Reservoir

Distribution of high temperature and high salt reservoirs of major oil and gas fields in China Tarim Oilfield Qinghai Oilfield Zhongyuan Oilfield

The problems in high-temperature and high-salt reservoirs development What are the main features? High-temperature and high-salt reservoirs What are the problems it brought about? What are the problems it brought about? High-temperature and high-salt Heterogeneous ● Serious channeling ● Low sweep efficiency ● Low production and production capacity. ● rapid rising of water cut ● Conventional agents of high temperature and salinity tolerance is poor. ● Cross-linking reaction time is difficult to control. ● The validity period of the operation measures is short. What should we do? Deep profile control

The challenges in high-temperature and high-salinity reservoirs deep profile control Better temperature resistance of profile control agent Profile control Good injection property Stronger plugging capability The permeability of the remaining oil area is much lower, for the purpose of flooding the remaining oil, the profile control agent must have stronger plugging capability Why?? Generally speaking, the profile agent used in high-temperature and high-salinity reservoirs must satisfy these three demands.

The commonly used deep profile control agents Weak cross-linked polymer gel Linked polymer solution (LPS) Colloidal dispersion gel (CDG) polymer concentration and cross-linking agent concentration New profile control agents are needed Because of low polymer concentration and low cross-linking agent concentration, the cross-linking reaction is easily influenced by formation conditions, such as salt, temperature, shearing degradation and chromatographic separation of cross-linking agent, thus can not suit the deep profile control in high-temperature and high-salinity reservoirs. Pre-cross-linked water swellable particles Solid polymer gel particles, with good injection property, but weak plugging capability and washing-out resistance, the validity period is short.

The elastic water swellable DCA microsphere The elastic water swellable DCA microspheres have been developed based on linked polymer solution for about more than eight years. (a) (b) Hydration layer Cross-linked polymer layer Gel core ● Like the gels, the elastic water swellable microspheres have cross-linked 3D networks structure. ● Unlike the gels, the cross-linked 3D networks structure is built by covalent bond not coordinate bond, so the microspheres have many advantages compared with other polymer type deep profile control agent. ●DCA microspheres have a three-layer structure which is the outer layer of the hydration, intermediate layer of cross-linked polymer, inner layer of gel core.

Plugging step by step, till the deep profile control is carried out. Plugging mechanism Plugging step by step, till the deep profile control is carried out. ● Temporarily plug the large pores and throats near wellbore, cause the water flow to divert and displace the remaining oil in the small pores and throats. ● When the pressure gradient is high enough, they will deform and traverse the pore throat, and recover to their original shape and size rapidly. ●Finally, they move into the deep area of oil formation and effectively plug the large pores and throats there, because of a relative low-pressure gradient. Thus, the water flow is diverted again and the remaining oil in the deep area of oil formation is also displaced.

Temperature Resistance of DCA microspheres Temperature performance of DCA microspheres and HPAM were measured in an oxygen environment by thermal gravimetric analyzer (TGA). HPAM DCA microspheres ● The temperature capability of HPAM and DCA microspheres were 193 ℃ and 300℃ respectively. ● According to relationship between viscosity and temperature, HPAM adapted to reservoir temperature from 70℃ to 80℃. ●According to decomposition temperature, DCA microspheres adapted to the target reservoir temperature above 130 ℃.

Plugging Ability of DCA microspheres Experimental temperature: 115℃ ; Particle size distribution :2-399 μm ; Salinity of formation water: 26.9×104mg/L ; Concentration of the microspheres: 1000ppm; Gas permeability : 1400mD; Length and diameter of the core : 30 cm and 2.5 cm respectively. The pressure distribution along the cylindrical core was monitored in real time. Microstructure of DCA microspheres in injection original liquid and recovery solution

Plugging Ability of DCA microspheres The plugging ability of DCA microspheres was characterized by residual resistance coefficient were calculated by the using of the is permeability of the core after injecting microspheres; is permeability of the core before injecting microspheres. ● the residual resistance coefficient along the cylindrical core was greater than 2. The highest value of residual resistance coefficient was 1777. ● The microspheres have a stable plugging ability to migrate into all the measure points of the core to achieve the deep plugging. ●DCA microspheres show high-strength deep plugging in reservoirs.

Effect of profile control and water shutoff of DCA microspheres Experimental temperature: 115℃ ; Experimental pressure: 20Mpa ; Particle size distribution :2-399 μm ; Concentration of the microspheres: 1000ppm; Length , width and height of the core : 30 cm, 4.5 cm, and 4.5 cm respectively; Gas measured permeability of low and high permeability : 220mD and1400mD. (a)model appearance before saturated oil (b)model appearance after DCA microspheres plugging and subsequent water flooding ● The rate of enhanced oil recovery reached 10.18% and the water cut dropped by 20.73% after injecting only the slug of the DCA microspheres. ● The low-permeability region of the model was a white color inside yellow circle in Figure(b). ●The remaining oil of the unswept regional, whose relative permeability was lower, was started.

Appearance of produced liquid of carbon dioxide flooding Method optimization of effect of profile control and water shutoff of DCA microspheres Experimental temperature: 115℃ ; Experimental pressure: 20Mpa ; Particle size distribution :2-399 μm ; Concentration of the microspheres: 1000ppm; Length , width and height of the core : 30 cm, 4.5 cm, and 4.5 cm respectively; Gas measured permeability of low and high permeability : 220mD and1400mD. Appearance of produced liquid of carbon dioxide flooding ● After subsequent water flooding, the further method was carbon dioxide flooding and the rate of enhanced oil recovery reached 19.64%. ● The crude displacement with carbon dioxide enhanced oil recovery and one important mechanism of carbon dioxide emulsified crude oil.

Conclusions ● DCA microsphere had a three-layer structure and have better suspension. The temperature capability of DCA microspheres was up to 300 ℃ and had better temperature resistance. ● The residual resistance coefficient along the cylindrical core was greater than 2. The microspheres have a stable plugging ability to migrate into all the measure points of the core to achieve the deep plugging. ●The rate of enhanced oil recovery reached 10.18% in stage of the subsequent water flooding. On the basis of the subsequent water flooding, the rate of enhanced oil recovery reached 19.64% in stage of carbon dioxide flooding. ●Feasibility methods which was the plugging of DCA microspheres and carbon dioxide flooding on deep profile control technology in high permeability of high temperature and high salt reservoirs have been proposed.

Acknowledgements ● Thanks to my co-authors for their contribution to synthesis and performance evaluation of high-temperature and high-salinity tolerance polymer microspheres: Changchun Yang, Xiang’an Yue, Jie He, Daiyu Zhou, Rui Xu, Ji Zhao, Chaoyue Li, Xuenan Zhang ●Xiang’an Yue, Ph.D, Professor (doctoral supervisor) Laboratory of Enhanced Oil & Gas Recovery in Complex Reservoir, College of Petroleum Engineering China University of Petroleum,Beijing No.18 Fuxue Road,Changping,Beijing 102249 Tel: 86-10-89733960 M: 86-13621210958 E-mail: yxa@cup.edu.cn

Thank You… Questions ??