Alternatives to Venting of Natural Gas ANG gas capture to reduce emissionsmembers.igu.org/old/IGU...
Transcript of Alternatives to Venting of Natural Gas ANG gas capture to reduce emissionsmembers.igu.org/old/IGU...
DNV GL © 2013 SAFER, SMARTER, GREENER DNV GL © 2013
Alternatives to Venting of Natural Gas –
ANG gas capture to reduce emissions
DNV GL © 2013
Categories of emission or venting
Natural gas emissions to the atmosphere result from several on-
shore gas industry processes and operations, but can be
categorised by four general types. These are:
− Fugitive emission (unplanned and uncontrolled)
− Process venting (planned, function of system operation)
− Venting from maintenance work (planned and controlled)
− Emergency vents (unplanned but controlled)
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Natural Gas Venting Reduction
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By design
Reduce Natural Gas Venting
By detection and repair
By reducing losses during operations
• Don’t vent gas in the first instance – design features and processes that prevent venting
• Ensure any new equipment installed does not vent gas
• Extend emission and leakage surveys • Take remedial actions to reduce leakage • Develop procedures to keep emissions low
through new systems and improved training/awareness
• Improve operational and/or maintenance practices and procedures
• Capture and re-use the vented gas (or flare it)
• Gas transfer by recompression
Approach
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Key objectives of this study
To find technological solutions to reduce the gas vented volumes : – Prevent the methane emission in the first place (new processes,
technologies or equipment)
– Capture the methane emission (and then use the gas somewhere else or return it to the network)
– Flare the gas to convert it to CO2
Feasibility Study to evaluate options, develop solutions and focus on cost and environmental benefit view-point. Three aspects highlighted: – Recompression – gas transfer from an isolated section to a “live section”
– Capture the gas that would be vented (using specific technology eg. ANG) then re-use it
– Flare the gas rather than vent it.
Main project: Undertake a series of field trials of selected technologies to raise awareness and provide validation data
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Concept of gas capture at a Compressor Station
P
Vent gas
compressor
control
Fuel gas
regulator
Process
compressor
Vent gas
compressor fuel
storage tank
Vent valve
(Normally closed)
Station Vent
Stack
Station Valves
(normally open)
Unit Valves
(normally closed)
Station
Inlet
Station
Outlet
Pressure
Measurement
Vent gas
compressor
Station emergency
shutdown protection
Method of re-compressing casing gas and valve leakage gas
Valve seal leakage
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Introduction to ANG Technology
Adsorption of natural gas onto adsorbent at low or intermediate pressure ranging from
5 to 50 bar.
Adsorbent has a high porosity to achieve maximum storage capacity.
Greater energy density than Compressed Natural Gas (CNG) at same pressure.
LARGE/SMALL GAS MOLECULES
MICROPORE MACROPORE
ACTIVATED CARBON
ADSORBENT
Methane Adsorbed in Micropores
Gas Density in Free Space
Gas Density
in Carbon
Vessel without Carbon
Vessel with Carbon
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ANG Process Overview
Simplified process flow diagram for ANG
Compressor
PackageSolids
Filter
Guard Bed
Vessel
Heater
Package
To existing
venting system
Vented Gas Supply
50 – 2 barg
ANG Vessel
30 barg
Gas Discharged
to be reused
~ 1 barg
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ANG Process Overview
Charging Phase
Compressor
PackageSolids
Filter
Guard Bed
Vessel
Heater
Package
To existing
venting system
Vented Gas Supply
50 – 2 barg
ANG Vessel
30 barg
Gas Discharged
to be reused
~ 1 barg
DNV GL © 2013
ANG Process Overview
Discharge Phase
Compressor
PackageSolids
Filter
Guard Bed
Vessel
Heater
Package
To existing
venting system
Vented Gas Supply
50 – 2 barg
ANG Vessel
30 barg
Gas Discharged
to be reused
~ 1 barg
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Layout of Test Facility
To capture approximately 400 kg of natural gas.
Footprint of test rig is 14 m x 22 m = Area of 308 m2
Gas Receiver Vessel
ANG Storage Vessel
Compressor
Package
Heater Package
Guard Bed
Vessel
Natural
Gas Feed Pressure
Reduction
Flow Control and
Metering
GasPT1
GasPT2
Solids
Filter
1m (Dia) x 11m (L)
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ANG Trial Objectives
To evaluate the performance and capabilities of the ANG storage technology and
carbon footprint.
– To replicate venting scenario at National Grid Compressor Site
– To evaluate and verify the capacity for the selected installation
– To optimise the control of gas quality
– To verify the carbon footprint reduction
– To determine the time taken to capture and store gas
– To demonstrate cyclic operation
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ANG Vessel Design
Thermocouple Locations
ANG Vessel Layout
Existing 42 Inch Diameter Vessel
Metal Framework
V = 9.8 m3 Diameter = 1.1 m Length = 11.0 m
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GAS CAPTURE FIELD TRIAL RESULTS
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Adsorption Process
Adsorption phase Adsorbent bed heats up
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Desorption Process
Desorption phase Adsorbent bed cools down
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Guard Bed Temperature Profile
08 05 07 10 11 09 06 04
Baffle plate
Guard Bed
Charging Direction
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Storage & Delivered Capacity
The results show that at full scale and a pressure of 30 barg, ANG
provides a 70% increase in working capacity compared to CNG.
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Gas Quality
The average WI of the charge and discharge phases were within the
range set by GS(M)R.
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Carbon Footprint Reductions
Figure below shows the comparison of carbon footprint using different
technologies as an alternatives to venting.
VENTING,
100.0%
FLARING,
22.9%
ANG, 0.1%CNG, 0.7%
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Achievements
“Full” scale demonstration of ANG technology.
The trial was successful and met all the objectives.
The trial and facility have been designed to mimic the expected venting
and capture process at a compressor site.
The system installation can capture close to 400 kg of natural gas and
showed the benefit of 70% storage enhancement compared to CNG.
For these scenarios, ANG technology gives the greatest carbon footprint
reduction compared to recompression and flaring.
During the discharge phase, the gas delivered meets the transmission
pipeline gas quality specification.
There is no evidence of carbon performance reduction from the cyclic
operations.
DNV GL © 2013
SAFER, SMARTER, GREENER
www.dnvgl.com
The DNV GL project team
Chiew Yen Law, You Van Lam, Robert Judd, Bill Walker,
Len Eastell and Martin Brown
Supported by Quentin Mabbutt and Tamsin Kashap from
National Grid
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Martin Brown
(01509) 282468