uisng soap to revive mature oil field
TRANSCRIPT
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Academia
Most reservoirs in the US under
operation by smal l producers have
become mature due to extended
waterflooding. In fact, an estimated 80%
of the total number of oil wells in the
US are now classified as “marginal.”
The mature reservoirs accessed by
these wells usually have a high water
cut, in the range of 80% to 90%. Also,
the industry typically leaves about
65% of oil behind after many years ofwaterflooding because of reservoir
heterogeneity and incomplete sweep of
the formation.
Excessive water production
becomes a major problem as these oil
fields mature. High volumes of water
production result in increased levels
of corrosion and scale, increased
load on fluid-handling facilities,
increased environmental concerns,
and eventually well abandonment
(with associated workover costs).
Consequently, producing zones are
often abandoned in an attempt to
avoid water contact, even when the
intervals still retain large volumes of
recoverable hydrocarbons.
Controlling water production has
been a challenging goal for most
oil producers.
Reservoir heterogeneity severely
affects the flow of gas, oil, and water
in the reservoir and thus affects
the choice of production strategies,
reservoir management, and ultimate oil
recovery. Reservoir heterogeneity is
the single most important reason for low
oil recovery, early breakthrough, and
excess water production. To maintain
reservoir pressure, these reservoirs
have usually been developed bywaterflooding from an early stage
in their development. Many of them
have been hydraulically fractured,
intentionally or unintentionally, or have
channels due to mineral dissolution
and production during many years
of waterflooding.
Reservoirs with induced fractures
or high-permeability channels are
quite common in mature oil fields.
Resin, foam, polymer/gel treatments,
and/or polymer flooding are among
enhanced oil recovery (EOR)
techniques typically used to correct the
reservoir heterogeneity and improve
oil production. Chemical EOR (CEOR),
involving alkali, surfactant, and
polymer chemicals, is currently gaining
some attention in the oil industry to
mobilize and recover large amounts
of both unswept and residual oil from
mature oil fields.
Chemical EOR Challenges
and Recent Advancements
CEOR includes the injection of a
mixture of chemicals to improve sweep
efficiency and produce residual oil
saturation left behind in the swept
volume. T he follow ing are some of the
barriers to widespread implementation
of CEOR:
1. Uncertainties in reservoir
geology
2. Project logistics
3. High front-end investment and
delay in oil production and payout
4. Complex engineering and the
need for highly specialized staff
5. Some negative field experiences
dating back to the 1980s
However, there have been
several crucial improvements to
increase the widespread application
of CEOR processes. Examples of
these improvements include better
geological description of oil reservoirs;
Using Soap to Revive Mature Oil FieldsMojdeh Delshad, The University of Texas at Austin
Mojdeh Delshad is a research professor in the Department
of Petroleum and Geosystems Engineering at The Universityof Texas (UT) at Austin. She is also the assistant director for
the US Department of Energy-funded Center of Frontiers of
Subsurface Energy Security. Delshad holds a BS degree in
chemical engineering from Sharif University and MS and
PhD degrees in petroleum engineering from UT Aust in. She
has 27 years’ experience in modeling multiphase flow, fluid
property modeling, and reservoir simulation of enhanced oil recovery processes,
and is in charge of the UT Chemical Flooding reservoir simulator (known as
UTCHEM) development, user support, and tra ining. Delshad was awarded the SPE
rank of “A Peer Apart” for reviewing more than 100 technical papers in 2010. She is
currently a member of the SPE Books Development Committee.
Fig. 1— Example of surfactant
molecule.
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2Vol. 9 // No. 3 // 2013
improved reservoir simulation;
horizontal and multilateral wells; more
efficient and better quality polymer
and surfactant molecules that are stable
at higher temperatures and higher
salinities (Fig. 1); new cost-effective
CEOR processes, such as alkaline/
co-solvent/polymer, and the use of
surfactants for wettability alteration in
carbonate reservoirs; and extending
the application of CEOR floods to
higher temperatures and higher
salinities, higher viscosity oils, and
carbonate reservoirs.
Chemical EOR Working
Principles and Associated
Synergism
The way a chemical flood works is
through the synergist ic effect of a
polymer (to improve mobility by
slowing down the movement of thewater to match that of the oil [i.e.,
mobility ratio of 1]) and a sur factant
(with or without alka line) to reduce the
interfacial tension (IFT) between oil
and water and thereby displace the
discontinuous trapped oil remaining in
the reservoir after the waterflood. Using
a surfactant i nvolves the same concept
as using detergent/soap to remove oil.
The primary objective of surfactant/
polymer (SP) or alkal ine/surfactant /
polymer (ASP) flooding is to reduce the
IFT between oil and water to values on
the order of 0.001 dyne/cm or less in
order to displace the trapped oil from
rock pores.
The use of alkaline chemicals for
improving oil recovery dates back
to the 1920s. The alkaline flooding
process relies on chemical reactions
between alkali, such as sodium
carbonate, and organic acids in the
crude oil to produce in-situ surfactants
(soaps) that can reduce the IFT. Most
researchers of the process have
reported that the lowest IFT occurs
at very low alkali concentrations. On
the other hand, alkali consumption
by the reservoir demanded injection
of a higher alkali concentration. This
problem was resolved by Nelson
et al. (1984), who proposed a method
to enlarge the low-IFT region andthereby promote optimum salinity by
combining the alkali with a surfactant
which is more hydrophilic than the
in-situ–generated soap. The formation
of the in-situ surfactant also reduced
the need for a synthetic surfactant
in an ASP slug (typically 10) is an indication of ultralow IFT
(