Products
ASP/SP
Alkaline Surfactant Polymer / Surfactant Polymer Technologies
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Overview
Primary and Secondary Recovery techniques together are able to recover only about 35-50% of oil form the reservoir. This leaves a significant amount of oil remaining in the reservoir. Chemical flooding (using surfactants) is one of the available technologies that can be used to recover up to an additional 35%.
Surfactant flooding is a well known concept that has been practiced in the field for many decades. Current technology is a progressive and gradual development of technologies and ideas that have existed for a long time. The key difference is the amount of surfactant used in projects today is much lower due to high purity.
SURFACTANT FLOODING
Surfactant flooding is usually carried out after a waterflood. There are two main types of surfactant flooding – Alkaline Surfactant Polymer or Surfactant Polymer Flooding. All components are injected together into the reservoir as an ASP “slug” and it is not a sequential injection. Typically, the (A)SP slug is injected at about 0.3-0.4 PV for effective performance. The alkaline component reacts with the acidic moieties that exist in the oil creating natural soap and also helps with reducing the adsorption of the surfactant on the rock. Surfactant component helps in releasing the oil from the rock and reducing the interfacial tension between water and oil, while the polymer (typically, partially hydrolyzed polyacrylamide or HPAM) acts as the viscosity modifier and helps mobilize the oil. Typically, a (A)SP flood is followed up with an equivalent pore volume injection of a polymer “push” solution. This helps reduce the slope of oil recovery decline and helps extend the production for a longer period of time.
The diagram (from: NETL) depicts a surfactant flooding process in a 5-spot well pattern. In an ideal situation, the ASP slug creates an oil bank as it moves through the reservoir.

Pre-work for (A)SP
Today, typical implementation of (A)SP in the field (pilot scale) take about 3-4 years. This is mainly because of the lab developmental work that goes into the choice of the various components. Additionally, implementation requires significant capital expenditure for polymer hydration equipment, blending equipment and specialty injection pumps.
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Fluid analysis (water and oil analysis)
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Fluid-fluid work (phase behavior work) to identify alkali and surfactants |
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Alkali identification |
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Alkali concentration |
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Surfactant concentration |
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Static adsorption of surfactant on reservoir rock |
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Core flood Work |
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Oil displacement efficiency |
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Adsorption studies |
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Simulation or modeling work |
The various aspects of implementation of a chemical EOR project are summarized below.
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Field Screening & Identification |
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Develop EOR Chemicals |
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Flood Design |
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Implement Flood |
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Oil Recovery |
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Field history and status
Field geology
Oil type
Available water / CO2
Polymer, SP, ASP
Existing equipment
Economic modeling |
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Feedstock supply
Capacity
Prove chemicals
IFT / Phase behavior
Core floods
Water TX plan |
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Flood pattern
Injection plan
Equipment design
Water TX plan
Develop capital cost
Refine economics
Modeling |
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Install capital
Train operators
Contract services
Purchase chemical
Manage chemical inventory
Monitor flood |
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Demulsify oil/water
Treat water |
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ASP vs. SP
ASP formulation typically consists of about 0.5-1% alkali, 0.1% surfactant and 0.1% polymer, while a SP formulation consist of 1% surfactant and 0.1% polymer. The choice between ASP or SP depends on a number of factors. |
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Acid value of the oil
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Quality of water – if divalent ion concentration is high, >100 ppm, SP may have to be used |
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Economics of project |
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Ability to carry out water softening or desalination (geographic location) |
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Alkaline-Surfactant-Polymer Flooding of the Cambridge Minnelusa Field
Jay Vargo , Jim Turner, Barrett Resources; Bob Vergnani, Coleman Oil and Gas; Malcolm J. Pitts , Kon Wyatt, Harry Surkalo, Surtek; David Patterson, Unichem
Journal: SPE Reservoir Evaluation & Engineering, 68285-PA
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Alkaline-Surfactant-Polymer Flood of the West Kiehl, Minnelusa Unit
Meyers, J.J., Pitts, M.J., Wyatt, Kon,
SPE/DOE Enhanced Oil Recovery Symposium, 22-24 April 1992, Tulsa, Oklahoma 24144-MS
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Alkaline/Surfactant/Polymer Pilot Performance of the West Central Saertu, Daqing Oil Field
Shutang, Gao, Huabin, Li, Zhenyu, Yang, Institute of Petroleum E&D, Daqing Oil Field; Pitts, M.J., Surkalo, Harry, Wyatt, Kon, Surtek, Inc.
SPE 35383-PA
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Development of High-Performance Surfactants for Difficult Oils
Ping Zhao, SPE, Adam C. Jackson, SPE, Chris Britton, Do Hoon Kim, Larry N. Britton, David B. Levitt, SPE, and Gary A. Pope, SPE, The University of Texas
SPE 113432-MS
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Chemical Flooding of Fractured Carbonates Using Wettability Modifiers
Najafabadi N.F.; Delshad M.; Sepehmoori K.; Nguyen Q.P.; Zhang J.
SPE - DOE Improved Oil Recovery Symposium Proceedings (16th SPE/DOE Improved Oil Recovery Symposium 2008 - "IOR: Now More Than Ever."
SPE 113369
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Field Chemical Flood Performance Comparison with Laboratory Displacement in Reservoir Core
Wyatt K.; Pitts M.J.; Surkalo H.
SPE - DOE Improved Oil Recovery Symposium Proceedings (Society of Petroleum Engineers, SPE 2004 SPE - DOE Fourteenth Inproved Symposium Oil Recovery Proceedings: Clean Sweep Strategies,
Paper No. 89385
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Polyacrylamide Vertical Conformance Process Improved Sweep Efficiency and Oil Recovery in the OK Field
H. Surkalo, M. J. Pitts, Surtek Inc. and B. Sloat and D. Larsen, Tiorco Inc.
SPE 14115
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Coupling the Alkaline-Surfactant Polymer Technology and The Gelation Technology to Maximize Oil Production
Malcolm Pitts, Jie Qi, Dan Wilson, David Stewart, Bill Jones, Surtek Inc.
October 2005
DOE Report # DE-FC26-03NT15411
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