Gas Storage: Trends and Future Projections Compression Equipment Selection. Marybeth Nored Klaus Brun, Ph.D. Southwest Research Institute

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Gas Storage: Trends and Future Projections Compression Equipment Selection Marybeth Nored Klaus Brun, Ph.D. Southwest Research Institute

Gas Storage Ten Year Trend: Seasonal Variation on +/- 1400 BCF natural gas - Seasonal variation for United States on a level of approx. +/- 1400 BCF natural gas, compared to a base gas volume of 4300 BCF. - Aggregate peak capacity in 2009 estimated at 3890 BCF. - Last two years shows gas storage volumes on the high side of five year average, possibly due to lower prices for natural gas. May 2002-May 2004: Total Gas in Storage compared to storage capacity and base gas January 2009-January 2011: Last 2 yr comparison shows gas storage volume at high end of 5-year average Source: U.S. Energy Information Administration, http://www.eia.doe.gov/pub/oil_gas/natural_gas/analysis_pu blications/storagebasics/storagebasics.html

Gas Storage Planned Projects -INGAA study reports that more than half of future storage projects through 2030 will be development of salt caverns over depleted reservoirs. - INGAA pipeline efficiency study notes, Because it generally is more economical in providing short-term delivery storage has become an increasingly important way for pipeline companies to meet customers peak day capacity requirements and to accommodate outages. - Important Variable: Effect of new gas shale production of natural gas / storage sites if gas prices rise again. Magnum Gas Utah = 42 BCF Ryckman Creek - Wyoming = 35 BCF Pine Prairie - Louisiana = 32 BCF Natural Gas Pipeline and Storage Infrastructure Projections Through 2030, INGAA Foundation Report October 2009. FERC, Office of Energy Projects, November 2010

Potential Increase in Storage Needs through 2030 Storage compression has relied on seasonal demand swings (decreased summer residential demand) to build up the reservoir through compression for storage injection in the summer months. Depending upon power generation with natural gas forecast, this summer low demand compression availability could change. Source: Natural Gas Pipeline and Storage Infrastructure Projections Through 2030, INGAA Foundation Report October 2009.

Compression Equipment Selection Compression storage must meet low pressure ratio, high flow rates in beginning of cycle (initial injection or withdrawal) Must also meet high pressure ratio, low flow during end of cycle for injection or withdrawal. Centrifugal compressors will follow continuous curve to support storage cycle, to the left of max power line and to the right of the surge line. Reciprocating compressors will follow stair-stepped approach, using combinations of unloading and staged compression. End Withdrawal: High Compression ratio, since reservoir now depleted and must meet pipeline pressure End Injection: Reservoir Pressure is high, Flow rate required is low Steepness of curve (dh/dq) depends on pipeline pressures and reservoir volume Begin Withdrawal: Low Compression ratio, since reservoir pressure is high Begin Injection: High Flow, Low Pressure, Empty Reservoir Flow

Operation to Meet Storage Cycle Pressure Ratio and Flow Two Stage Region Reciprocating Compressor operation for storage End storage cycle Max power limit in red double acting all cylinders Centrifugal Compressor operation for storage End storage cycle May consider second stage of compression Yellow load step = all cylinders single acting Flow Begin storage cycle Flow Begin storage cycle Reciprocating compressor uses incremental load steps limits are amount of unloading and number of cylinders, effects on pulsations, and more narrow two stage region. As load steps and staging increases = complexity increases! Centrifugal compressor operating curve is continuous and limited only by max power limit of driver and surge region

Centrifugal Compressor Storage Curve Centrifugal compressors can meet the injection / withdrawal curve naturally by following a constant power line. Design can be either single stage or two stage. Need to match power requirements of compressor to operating map and storage reservoir capacity. ISENTROPIC HEAD 50,000 45,000 77% 80% 80% 40,000 77% 35,000 73% Constant Head 30,000 69% 25,000 20,000 15,000 Max. Power (Storage) 10,000 5,000 500 1,000 1,500 2,000 2,500 3,000 Surge Limit 10,000 rpm 15,000 rpm 11,000 rpm 15,500 rpm 14,000 rpm 13,000 rpm 12,000 rpm INLET VOLUME FLOW

Centrifugal Compressors: Use of Series and Parallel Operation to Accommodate Storage Needs - Most storage applications can be fit with a single centrifugal unit. - Adding option for using low pressure and high pressure stage in series will add flexibility. Source: Solar Turbines, Kurz and Brun, Assessment of Compressors in Gas Storage Applications, Turbomachinery Symposium 2009.

Pressure (psig) / Horsepower (hp) 1400 1200 1000 800 600 400 200 0 Reciprocating Compressors: Transmission vs Storage Compression Transmission Application: Discharge Pressure is constant. Loading and HP are varied to meet flow rate and suction pressure Suction Pressure Discharge Pressure Horsepower Required 0 20 40 60 Flow Rate (MMSCFD) Pressure (psig) 1400 1200 1000 800 600 Storage Application: Much more varied. Discharge and Suction pressure can vary, Staging and unloading used to match storage curve Two Stage 5000 4500 4000 3500 3000 2500 2000 400 1500 Single Stage - Single Stage - 1000 200 Suction Pressure Unloaded No unloading 500 Discharge Pressure 0 0 Horsepower 0 Required 100 200 300 400 Increasingly more complex pulsation study Flow Rate (MMSCFD) Simplified Pulsation Analysis Horsepower (hp)

Reciprocating Compressors: Use of Unloading and Single / Two Stage Designs - In beginning, a 6-cylinder reciprocating compressor can meet lower pressure ratio required with single unit operating at fixed speed and many load steps - to match flow rate. - Towards end of cycle, must switch to two stage operation to meet pressure ratio. - May need to add second unit to meet flow rate. - Unloading and staging will add more cost and complexity to pulsation filter bottles and station design. Pressure Ratio 2.60 2.40 2.20 2.00 1.80 1.60 1.40 1.20 End of storage cycle Two Stage May need second unit Single Stage Load steps with all cylinders provide more breadth in single stage operation Beginning of storage cycle 1.00 0 50 100 150 200 250 300 350 Flow Rate (MMSCFD)