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                RAVVA
    Celebrating 16 Years of Technical Excellence

          Operation | Produced Water Reinjection
Ravva | Production
Operation

Produced Water Reinjection

Increasing water production is a major environmental, as well as an economic issue for the oil and gas
producers. It’s also an issue for the regulators who are responsible for ensuring produced water discharge
requirements around the globe. Most oil and gas reservoirs have a natural water layer called formation
water beneath the hydrocarbon layer.
Also to achieve maximum oil recovery,
additional water is usually injected into the
reservoir, which may be associated with
hydrocarbons in the production. In the
case of some gas production, produced
water can be condensed water. Thus, the
liquid that comes out of the reservoir is
not just hydrocarbons, but is frequently
accompanied by water. The liquid
production is in the form of a mixture of
free water, an oil/water emulsion and oil.
Furthermore, as an oil field matures, the
amount of produced water increases. This
is because after some time, the formation
waters out due to the water injection
process. The water-oil ratio varies from reservoir to reservoir. It also varies with time for a particular
reservoir. Worldwide 75% of the production is water, but in some places this percentage may increase to
as high as 98%.

Ravva field started production in March 1993, and in year 1997 water injection in the field was started to
maintain the reservoir pressure above saturation pressure to maximise the recovery.

Cairn introduced PWRI at Ravva, which was a first in the country. The Ravva fields are in a mature phase
of operation, resulting in increased water cut or produced water. This coupled with other factors like
effluent discharged from plant limit as prescribed by the Andhra Pradesh Pollution Control Board
(APPCB), also presented challenges in meeting effluent specifications to be disposed in the sea. The
PWRI also has other environmental significance like helping reduce oil sludge through higher oil recovery
from produced water and helping reduce consumption of ground water with the treated produced water for
water injection purpose. Usually, the fluids that are removed from the reservoir by the producing well are
brought to the surface and separated into an oil stream, a gas stream and a water stream. The main
components of the water stream that is separated are:

       Water
       Suspended oil
       Dissolved oil
       Suspended solids (scale, corrosion products, sand, etc.)
       Dissolved solids
       Dissolved gases (CO2, H2S, O2)
       Bacteriological matter
       Added materials (treating chemicals, kill fluids, acids, etc.)
Ravva | Production
Operation

Before setting up the project, a detailed study was conducted to understand the feasibility of the PWRI
application. In this process various tests were conducted to understand the compatibility of the existing
source of water at various ratios and stages of the cycle. Also it was ensured that the design be feasible
for the treatment facility to be compatible with the reservoir requirements for the complete lifecycle of the
field.

Based on the available data and test samples, a high level study led to the design of a model, which had
the following objectives:

       to include reservoir behaviour, facilities modelling for scaling and to understand the effects on
        permeability due to oil presence
       to study the effects of change in temperature
       to determine specification for produced water for re-injection
       to identify and mitigate associated risks like injectivity decline, scaling, souring, corrosion issues,
        etc.
       to carry out basic engineering and provide specifications and make qualified cost estimates
       to examine various processes which are economically viable for treating produced water in
        consideration of the lifecycle of the field

The produced water to be reinjected originates from the FWKOD, HP and MP crude oil three phase
separators. The water from all these sources is degassed in the Produced Water Degasser vessel and
then routed to the Produced Water Surge tank for initial oil-water separation. Separated water from the
Crude Oil Wash Tank is pumped directly to the Surge Tank. The pump speed is varied by a variable
frequency drive (VFD) in response to an interface level control signal from the crude oil wash tank.

The Produced Water Surge Tank is provided with new internals allowing gas and slugs of oil to separate.
Sufficient residence time is provided to allow oil droplets to coalesce to form a separate oil layer, which
can be drained to Recovered Oil Sump manually. The water flows out from the Surge Tank via a hydraulic
loop, which would maintain a minimum level in the tank. From the Surge Tank the produced water then
flows into two parallel Induced Gas Flotation (IGF) units, each handling up to 50% of the design flow

Each IGF is designed for 100% of design flow and thus can be used as a standalone unit. In case of any
problem in PWRI facilities, the produced water in excess to ETP capacity is stored in one of the storage
tanks by pumping water from the API separator. Once PWRI is online, water is routed to ETP for
treatment and disposal. This situation is envisaged at high water cut condition. The water from the IGF
units is pumped into the mixing tank using low shear positive cavity screw pumps. The level in the IGFs is
maintained at its normal operating level by a level control loop modulating the transfer pump speed using
a variable frequency drive (VFD).

At present, the bore well water is collected in the supply header. The number of bore well pumps online
depends on the makeup demand of injection water to oil wells. The water is filtered in the existing auto-
back-flushing coarse filters, and then routed to the Mixing Tank. The number of bore wells online depends
on the injection water quantity required for the reservoir.

The produced water is commingled with the bore well water in the Mixing Tank and then fed to the
Produced Water Dual Media Fine Filter package. The existing water injection feed pumps are provided
sufficient head to overcome the pressure drop through the produced water dual media fine filter and also
to ensure the required net positive suction head (NPSH) at the Water Injection Pumps located
downstream of the fine filters.

Each new filter is provided with a dedicated flow control loop located downstream of the filter vessel The
injection pump discharge pressure is controlled by a split range pressure controller deriving signals from
Ravva | Production
Operation

two pressure transmitters – one on each side of the pressure control valve in the injection line. All
atmospheric tanks are fuel gas blanketed to prevent air from precipitating the dissolved iron.

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Ravva Produced Water Reinjection

  • 1.                           RAVVA Celebrating 16 Years of Technical Excellence Operation | Produced Water Reinjection
  • 2. Ravva | Production Operation Produced Water Reinjection Increasing water production is a major environmental, as well as an economic issue for the oil and gas producers. It’s also an issue for the regulators who are responsible for ensuring produced water discharge requirements around the globe. Most oil and gas reservoirs have a natural water layer called formation water beneath the hydrocarbon layer. Also to achieve maximum oil recovery, additional water is usually injected into the reservoir, which may be associated with hydrocarbons in the production. In the case of some gas production, produced water can be condensed water. Thus, the liquid that comes out of the reservoir is not just hydrocarbons, but is frequently accompanied by water. The liquid production is in the form of a mixture of free water, an oil/water emulsion and oil. Furthermore, as an oil field matures, the amount of produced water increases. This is because after some time, the formation waters out due to the water injection process. The water-oil ratio varies from reservoir to reservoir. It also varies with time for a particular reservoir. Worldwide 75% of the production is water, but in some places this percentage may increase to as high as 98%. Ravva field started production in March 1993, and in year 1997 water injection in the field was started to maintain the reservoir pressure above saturation pressure to maximise the recovery. Cairn introduced PWRI at Ravva, which was a first in the country. The Ravva fields are in a mature phase of operation, resulting in increased water cut or produced water. This coupled with other factors like effluent discharged from plant limit as prescribed by the Andhra Pradesh Pollution Control Board (APPCB), also presented challenges in meeting effluent specifications to be disposed in the sea. The PWRI also has other environmental significance like helping reduce oil sludge through higher oil recovery from produced water and helping reduce consumption of ground water with the treated produced water for water injection purpose. Usually, the fluids that are removed from the reservoir by the producing well are brought to the surface and separated into an oil stream, a gas stream and a water stream. The main components of the water stream that is separated are:  Water  Suspended oil  Dissolved oil  Suspended solids (scale, corrosion products, sand, etc.)  Dissolved solids  Dissolved gases (CO2, H2S, O2)  Bacteriological matter  Added materials (treating chemicals, kill fluids, acids, etc.)
  • 3. Ravva | Production Operation Before setting up the project, a detailed study was conducted to understand the feasibility of the PWRI application. In this process various tests were conducted to understand the compatibility of the existing source of water at various ratios and stages of the cycle. Also it was ensured that the design be feasible for the treatment facility to be compatible with the reservoir requirements for the complete lifecycle of the field. Based on the available data and test samples, a high level study led to the design of a model, which had the following objectives:  to include reservoir behaviour, facilities modelling for scaling and to understand the effects on permeability due to oil presence  to study the effects of change in temperature  to determine specification for produced water for re-injection  to identify and mitigate associated risks like injectivity decline, scaling, souring, corrosion issues, etc.  to carry out basic engineering and provide specifications and make qualified cost estimates  to examine various processes which are economically viable for treating produced water in consideration of the lifecycle of the field The produced water to be reinjected originates from the FWKOD, HP and MP crude oil three phase separators. The water from all these sources is degassed in the Produced Water Degasser vessel and then routed to the Produced Water Surge tank for initial oil-water separation. Separated water from the Crude Oil Wash Tank is pumped directly to the Surge Tank. The pump speed is varied by a variable frequency drive (VFD) in response to an interface level control signal from the crude oil wash tank. The Produced Water Surge Tank is provided with new internals allowing gas and slugs of oil to separate. Sufficient residence time is provided to allow oil droplets to coalesce to form a separate oil layer, which can be drained to Recovered Oil Sump manually. The water flows out from the Surge Tank via a hydraulic loop, which would maintain a minimum level in the tank. From the Surge Tank the produced water then flows into two parallel Induced Gas Flotation (IGF) units, each handling up to 50% of the design flow Each IGF is designed for 100% of design flow and thus can be used as a standalone unit. In case of any problem in PWRI facilities, the produced water in excess to ETP capacity is stored in one of the storage tanks by pumping water from the API separator. Once PWRI is online, water is routed to ETP for treatment and disposal. This situation is envisaged at high water cut condition. The water from the IGF units is pumped into the mixing tank using low shear positive cavity screw pumps. The level in the IGFs is maintained at its normal operating level by a level control loop modulating the transfer pump speed using a variable frequency drive (VFD). At present, the bore well water is collected in the supply header. The number of bore well pumps online depends on the makeup demand of injection water to oil wells. The water is filtered in the existing auto- back-flushing coarse filters, and then routed to the Mixing Tank. The number of bore wells online depends on the injection water quantity required for the reservoir. The produced water is commingled with the bore well water in the Mixing Tank and then fed to the Produced Water Dual Media Fine Filter package. The existing water injection feed pumps are provided sufficient head to overcome the pressure drop through the produced water dual media fine filter and also to ensure the required net positive suction head (NPSH) at the Water Injection Pumps located downstream of the fine filters. Each new filter is provided with a dedicated flow control loop located downstream of the filter vessel The injection pump discharge pressure is controlled by a split range pressure controller deriving signals from
  • 4. Ravva | Production Operation two pressure transmitters – one on each side of the pressure control valve in the injection line. All atmospheric tanks are fuel gas blanketed to prevent air from precipitating the dissolved iron.