NOVA Gas Transmission Ltd. December 2008 Annual Plan

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Transcription:

NOVA Gas Transmission Ltd. December 2008 Annual Plan APPENDIX 3 FLOW SCHEMATICS Flow schematics for each of the design areas where additional facilities are required for the Planning Period. The flow schematics may differ from the design flow requirements shown in Appendix 2. This is because the detailed flow schematic information is taken directly from the hydraulic simulations whereas design flow requirements are estimated for the entire design area. 1

NORTH OF DESIGN AREA WINTER CAPABILITY WITHOUT PROPOSED FACILITIES FIELD HANMORE PELICAN LK LK B,C LK A LK B LK C,D LK D LK P sct (kpa g ) 5925 6036 6896 6896 6323 6473 5392 P dis (kpa g ) 7949 6961 8188 8193 6952 6472 8441 Flow (10 6 m 3 /d) 14.2 31.9 0.0 10.6 42.6-31.8 3.7 Fuel (10 3 m 3 /d) 55.4 59.9 0.0 27.9 65.1 0.0 23.2 Power Avail (MW) 6.3 6.6 3.5 3.2 7.4 15.2 3.2 Power Req (MW) 6.0 6.6 0.0 3.1 7.4 0.0 2.4 Compression Ratio 1.3 1.2 N/A 1.2 1.1 N/A 1.6 T sct ( C) 4.5 6.0 5.0 23.0 13.0 10.0 5.0 T dis ( C) 30.5 18.5 5.0 40.0 23.0 10.0 44.0 T amb ( C) 2.0 2.0 2.0 2.0 2.0 2.0 2.0 PAUL WOODENHOUSE BUFFALO WAND. SLAVE LK B2 #1 #2 NORTH RIVER LEISMER LK P sct (kpa g ) 5798 4993 4981 7606 5457 5510 5000 P dis (kpa g ) 7614 7783 7784 7602 7657 5509 6179 Flow (10 6 m 3 /d) 19.0 0.0 22.8 13.3 4.8 1.7 2.8 Fuel (10 3 m 3 /d) 54.2 0.0 87.5 0.0 29.3 0.0 10.2 Power Avail (MW) 14.5 10.6 14.7 5.0 2.9 0.9 3.8 Power Req (MW) 6.3 0.0 12.5 0.0 2.3 0.0 0.9 Compression Ratio 1.3 N/A 1.6 N/A 1.4 N/A 1.2 T sct ( C) 3.0 1.0 1.0 10.0 2.0 5.0 10.0 T dis ( C) 24.0 1.0 35.0 10.0 32.0 5.0 31.0 T amb ( C) 2.0 2.0 2.0 2.0 2.0 2.0 3.0 EXISTING RECEIPT POINTS INTERCHANGES AND PIPELINE LOOPS ARE SHOWN HERE EXISTING DELIVERY POINTS - FLOW AND FUEL IS @ STP (101.325 kpa AND 15 C) - COMPRESSOR CONDITIONS FOR COMPRESSION AT PAUL, EXISITING CONTROL VALVE A, HANMORE A, AND BEHAN NOT SHOWN OTHER PIPELINE SYSTEMS From Hunt Creek Q = 3.6 PAUL Marten Hills From Beaver Creek SLAVE Liege WOODENHOUSE Paul Lake Crossover Redwater PELICAN BUFFALO CREEK NORTH WANDERING RIVER Logan River HANMORE A LEISMER FIELD BEHAN D Fort McMurray Area Delivery Flow Q= 30.1 Conklin Graham/Chard Caribou Leming Lake Crossover Cold Lake Border

NORTH OF DESIGN AREA WINTER DESIGN WITH PROPOSED FACILITIES FIELD HANMORE PELICAN LK LK B,C LK A LK B LK C,D LK D LK P sct (kpa g ) 7102 7830 6969 6969 6962 7384 7029 P dis (kpa g ) 8271 8271 6969 7860 7894 8276 9930 Flow (10 6 m 3 /d) 13.5 22.6 0.0 0.0 36.9 35.8 4.7 Fuel (10 3 m 3 /d) 31.6 26.0 0.0 0.0 64.1 73.0 21.9 Power Avail (MW) 6.3 6.6 3.5 3.2 7.4 15.2 3.2 Power Req (MW) 2.9 1.1 0.0 0.0 7.4 5.6 2.2 Compression Ratio 1.2 1.1 N/A N/A 1.1 1.1 1.4 T sct ( C) 4.5 13.0 5.0 5.0 13.0 11.0 5.0 T dis ( C) 17.5 18.5 11.0 5.0 25.0 21.0 34.0 T amb ( C) 2.0 2.0 2.0 2.0 2.0 2.0 2.0 PAUL WOODENHOUSE BUFFALO WAND. SLAVE LK B2 #1 #2 NORTH RIVER LEISMER LK P sct (kpa g ) 6716 5530 5526 8794 6367 7185 5000 P dis (kpa g ) 8800 9000 9000 9504 9650 7184 6179 Flow (10 6 m 3 /d) 22.8 10.5 15.8 39.6 5.8 1.7 2.8 Fuel (10 3 m 3 /d) 60.9 55.2 72.0 20.6 36.2 0.0 10.2 Power Avail (MW) 14.5 10.6 14.7 5.0 2.9 0.9 3.8 Power Req (MW) 7.5 6.4 9.8 1.8 3.3 0.0 0.9 Compression Ratio 1.3 1.6 1.6 1.1 1.5 N/A 1.2 T sct ( C) 6.0 2.0 1.0 13.0 1.0 5.0 10.0 T dis ( C) 26.0 39.0 39.0 22.9 36.0 5.0 31.0 T amb ( C) 2.0 2.0 2.0 2.0 2.0 2.0 3.0 EXISTING RECEIPT POINTS INTERCHANGES AND PIPELINE LOOPS ARE SHOWN HERE EXISTING DELIVERY POINTS - FLOW AND FUEL IS @ STP (101.325 kpa AND 15 C) - COMPRESSOR CONDITIONS FOR COMPRESSION AT PAUL, EXISITING CONTROL VALVE A, HANMORE A, AND BEHAN NOT SHOWN OTHER PIPELINE SYSTEMS From Hunt Creek Q = 3.5 PAUL Marten Hills From Beaver Creek SLAVE Liege WOODENHOUSE Paul Lake Crossover Redwater PELICAN BUFFALO CREEK NORTH WANDERING RIVER Logan River FIELD HANMORE A LEISMER D BEHAN Fort McMurray Area Delivery Flow Q= 34.7 Conklin Caribou Graham/Chard Leming Lake Crossover Cold Lake Border

SOUTH OF DESIGN AREA WINTER CAPABILITY WITHOUT PROPOSED FACILITIES GADSBY OAKLAND P sct (kpa g ) 5547 6993 5292 5053 P dis (kpa g ) 8227 6992 7797 6128 Flow (10 6 m 3 /d) 41.3-37.2 35.4 34.7 Fuel (10 3 m 3 /d) 177.6 0.0 163.2 82.7 Power Avail (MW) 29.0 28.8 27.6 13.8 Power Req (MW) 21.6 0.0 19.0 12.2 Compression Ratio 1.5 N/A 1.5 1.2 T sct ( C) 9.0 5.0 9.0 7.0 T dis ( C) 41.0 5.0 42.0 28.0 T amb ( C) 2.0 3.0 4.0 4.0 PRINCESS A CAVENDISH P sct (kpa g ) 5000 4399 P dis (kpa g ) 5695 5045 Flow (10 6 m 3 /d) 29.6 4.0 Fuel (10 3 m 3 /d) 29.8 7.1 Power Avail (MW) 17.0 4.5 Power Req (MW) 6.2 0.8 Compression Ratio 1.1 1.1 T sct ( C) 5.6 4.0 T dis ( C) 23.0 17.0 T amb ( C) 6.0 5.0 NEVIS-GADSBY CROSSOVER Q= 4.0 GADSBY OAKLAND WAINWRIGHT UNITY BORDER EXISTING DELIVERY POINTS EXISTING CONTROL VALVE INTERCHANGES AND PIPELINE LOOPS ARE SHOWN HERE - FLOW AND FUEL @ STP (101.325 kpa AND 15 C) - COMPRESSOR CONDITIONS FOR LATERAL COMPRESSION AT WAINWRIGHT NOT SHOWN PRINCESS A Eastern Alberta Mainline CAVENDISH

SOUTH OF DESIGN AREA WINTER DESIGN WITH PROPOSED FACILITIES GADSBY OAKLAND P sct (kpa g ) 6871 6229 5033 4828 P dis (kpa g ) 8364 8450 7389 6147 Flow (10 6 m 3 /d) 46.0 41.8 40.7 39.7 Fuel (10 3 m 3 /d) 130.0 161.6 174.0 90.4 Power Avail (MW) 29.0 28.8 27.6 13.8 Power Req (MW) 12.4 18.7 21.3 13.8 Compression Ratio 1.2 1.4 1.5 1.3 T sct ( C) 21.0 19.0 9.0 7.0 T dis ( C) 38.0 45.0 41.0 28.0 T amb ( C) 2.0 3.0 4.0 4.0 PRINCESS A CAVENDISH P sct (kpa g ) 5000 4399 P dis (kpa g ) 5695 5045 Flow (10 6 m 3 /d) 34.6 4.0 Fuel (10 3 m 3 /d) 33.9 7.1 Power Avail (MW) 17.0 4.5 Power Req (MW) 7.2 0.8 Compression Ratio 1.1 1.1 T sct ( C) 5.6 4.0 T dis ( C) 23.0 17.0 T amb ( C) 6.0 5.0 NEVIS-GADSBY CROSSOVER Q= 4.0 GADSBY OAKLAND WAINWRIGHT UNITY BORDER EXISTING DELIVERY POINTS EXISTING CONTROL VALVE INTERCHANGES AND PIPELINE LOOPS ARE SHOWN HERE - FLOW AND FUEL @ STP (101.325 kpa AND 15 C) - COMPRESSOR CONDITIONS FOR LATERAL COMPRESSION AT WAINWRIGHT NOT SHOWN PRINCESS A Eastern Alberta Mainline CAVENDISH