Exhibit No. ATC-610
`Page 1 of 50
`
`N\
`Mfingfiw
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`Alyeska Pipeline Service Company
`900 E. Benson Blvd.
`Anchorage, AK 99519
`
`Pump Station 4 Equipment Replacement
`Cost Estimate Report
`(Final)
`
`April 29, 2011
`
`SUBMITTED BY
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`Stantec Consulting Inc.
`10160-112 Street
`
`370 North Wiget Lane, Suite 210
`Walnut Creek Edmonton, Alberta
`
`CA 94598 T5K 2L6
`
`USA Canada
`Phone: (925) 941-1400 Phone: (780) 917-T000
`FAX: (925) 941-1401 FAX: (780) 917-8580
`
`WHWW.SIaniec.com
`Stantec Project No.: 2010790000 FEDERAL ENERGY REGULATORY COMMISSION
`Docket Mo. 1509-348-004
`Hearing Exhibibs, T ¢ = bi0
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`Diate kst -
`Drate Admitind I ST
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`PUMP STATION 4 EQUIPMENT REPLACEMENT
`COST EBTIMATE REPORT (FINAL)
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`APRIL 29, 2011
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`TABLE OF CONTENTS
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`L SCOPE SUMMARY'.
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`1.1. Background
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`1.2. Project Description
`13 Cost Basis and Details
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`2. COST SUMMARY ...
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`l'!!4
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`3. APPENDICES
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`wnd
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`Exhibit Mo, ATC-810
`Page 2 of 50
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`Exhibit Mo, ATC-810
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`Page 3 of 50
`PUMP STATION 4 EQUIPMENT REPLACEMENT
`COST ESTIMATE REPORT (FINAL) %
`APRIL 23, 2011
`e Stantec
`1. SCOPE SUMMARY
`1.1. Background
`
`Alyeska Pipeline Service Company and Trans-Alaska Pipeline System (TAPS) Owners are
`involved in a pipeline tariff case with the Federal Energy Regulatory Commission (FERC)
`and the Regulatory Commission of Alaska (RCA). One element of the tariff case involves
`costs of pump station reconfigurations.
`
`Alyeska requested Stantec to develop a rough order of magnitude (ROM) cost estimate 1o
`renovate a typical pump station with new pumps, drivers, and electrical generation and
`distribution equipment, suitable for present operating requirements.
`
`1.2. Project Description
`The ROM cost to renovate a typical pump station is based on Pump Station No. 4.
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`Three mainline pumps are included, each with gas turbine drivers. The combination of
`pump and drives is referred to as a mainline unit (MLU). The arrangement allows for
`regular operation with two MLUs and the third as a rotational spare. Pump and turbine
`equipment will be located in the existing pump/turbine building. Total pumping capacity is
`based on pipeline throughput of nominally 750,000 barrels per day (bpd). The gas turbine
`drivers for the pumps are to have capacity of approximately 6,500 horsepower, plus an
`allowance for end-of-curve capacity or future increase in crude oil viscosity.
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`A recirculation piping system is included to allow the MLUs to operate up to full capacity
`even when the pipeline throughput is a lesser amount. This amangement allows for some
`crude oil heating, which is advantageous at lower throughputs.
`
`Crude oil piping systems which are presently buried are relocated to allow for inspection.
`The general arrangement 15 for above ground piping. 1f above ground 15 impractical, the
`below ground sections are placed in utilidors to provide accessibility.
`
`The electrical power generation and distribution equipment involves engine/generator units
`and 480 volt switchgear. Multiple generator units are provided to allow for availability to
`meet the load requirements during maintenance rotations and unplanned down time. In
`addition to diesel generators a natural gas lifeline system backup generator is provided.
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`The gas turbine units are provided with cumrent technology control systems and
`communications protocol for remote operation.
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`The remainder of the pump station continues with the present equipment, facilities, and
`arrangement.
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`Exhibit No. ATC-610
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`Page 4 of 50
`PUMP STATION 4 EQUIPMENT REPLACEMENT
`APRIL 28, 2011
`EEseme e re— m
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`1.3 Cost Basis and Details
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`The cost estimate is developed using a factored approach. This involves gathering cost
`information for major equipment and applying a factor to armive at an estimate for the total
`project cost. The factor is based on cost relationships that have been developed for past
`prajects in the US Northwest/Alaska geographic region.
`
`Preliminary sizing data was provided to prospective vendors who were asked to submit
`budgetary pricing. For the solicited major equipment pricing was requested to be within a
`+/- 25% band.
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`Each pump is nominally sized for 375,000 bpd capacity using the same head pressure as
`the pre-SR pumps. Crude oil viscosity was chosen as 20 centipoise, which comesponds to
`an oil temperature of 30°F. Proposals were received from two pump manufacturers, Sulzer
`and Flowserve. The Sulzer pumps pricing is used in the estimate, as Sulzer pumps have
`been used more commonly by Alyeska.
`
`The gas turbines were sized for the pump duty and an additional 15% capacity factor was
`included to allow for pump operation in excess of the rated capacity. Price quoles were
`received from Solar Turbines and from Siemens. These unils are mechanical drivers for the
`pumps, with gearboxes for speed reduction to the pump speed of 3600 rpm. Operating
`parameters were for a maximum ambiént temperature of 90°F at an altitude of 3000 feet,
`Of the two prices received Solar Turbine’s proposal was determined to be the better
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`selection as the sizing was closer to the requested rating and low temperature operation
`features were included.
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`The pump station electrical single line drawing was used as the basis for the swiltchgear
`scope. Six busses were identified for replacement. Contact was made with Schoeider
`Electric for Square D equipment and with Rockwell Automation who worked with
`Westburne, for what developed into Alpha equipment. The Westburne proposal was
`selected. The proposal included custom switchgear and motor control assemblies including
`protective relaying and data communications. Extra spaces were included for future
`cXpansion.
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`Electrical generators were sized based on replacing the existing units with 10% larger units.
`The existing generators consist of three 450 kW diesel units and a 900 kW natural gas unit.
`The replacement generators are 500 kW diesel fueled continuous rated and a 1.3 MW
`natural gas fueled prime rated unit. The requested generator size was 1000 kW but
`Caterpillar does not have this size rating so the next standard size was priced. Cummins
`were also contacted and did provide what would be considered ballpark pricing for the
`generators. However, NC Power Systems, whom we have had much discussion with on
`previous work, submitted a better quality and more detailed response, The Caterpillar units
`included for current emissions standards compliance to tier 4 interim using exhaust after-
`treatment systems. These systems increase the basic generator cost by approximately 15%
`for the natural gas generator and by 30% for the diesel generators.
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`Exhibit Mo. ATC-810
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`Page 5 of 50
`PUMP STATIOM 4 EQUIPMENT REPLACEMENT
`COST ESTIMATE REPORT (FIMUAL)
`APRIL 28, 2011 %
`e T Stantee
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`The station recirculation scheme and replacement of the buried station piping with
`aboveground piping was not priced out for this report. Instead, cost data was taken from a
`study on station re-moding thal was done for pump station 4 under Stantec projects
`201010890204, The design case for this study was 1.4 MM bpd throughput. Mo scaling of
`capacity is made and the detailed cost is imported directly as a summary line item. An
`escalation factor of 5% was applied to adjust the 2009 costs 1o present 2011 costs. Since
`this estimate separately detailed all pertinent cost categories the IPA Lang factor is not
`applied.
`
`Alyeska shared Independent Project Analysis (IPA) subscriber data with Stantec for the
`purpose of factoring the major equipment costs to a final project cost. The composite factor
`approach includes for preliminary and detailed engineering design, project and construction
`management, direct field labor, construction indirect costs, associated bulk materials cost,
`and others. The factor recognized the cost of renovation of an existing facility is greater
`than for constructing & new facility of similar capacity. A location adjustment is included to
`account for the greater cost of remote and cold climate conditions of the pump station.
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`This approach is a convenient method of estimating project costs at an early stage.
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`The major equipment multiplying factor adopted by Alyeska and used in this cost study is
`5.7, Since there can be variability with this factor and since the major equipment prices are
`class IV quality, the resulting scope cost should not be considered to be close to definitive.
`It will however, meet the intended purpose in the project definition.
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`Exhibit No. ATC-610
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`Page & of 50
`PUMP STATION 4 EQUIPMENT REPLACEMENT
`COST ESTIMATE REPORT (FINAL) ;
`APRIL 28, 2011 %
`e ———————— Stantec
`2. COST SUMMARY
`Item Description Cost
`(Smillions)
`1 Pumps (1) 1.6
`2 Gas Turbine Drivers (3) 15.9
`3 Engine/Generators (3-500 kW diesel) 0.98
`4 Engine/Generators (1-1.3 MW natural gas) 1.76
`5 Electrical Switchgear & MCC 0.90
`Major Equipment Subtotal 21.14
`IPA Lang Factor Multiplier 3.7
`Subtotal 120.50
`1] Spare parts and tools (6.67% of items 1, 2 & 3, 20% of items 4 & 5) 1.76
`Freight costs (12% of items 1-6) 2,75
`Crude Qil Piping Reroute (from conceptual study F655) with escalation 25.00
`TOTAL £150.0
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`Exchibit Mo. ATC-E10
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`Page 7 of 50
`PUMP STATION 4 EQUIPMENT REPLACEMENT
`COST ESTIMATE REPORT (FINAL) %
`APRIL 29, 20411
`— Stavtes
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`3. APPENDICES
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`Appendix 1 — Pumps
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`Appendix 2 = Gas Turbines
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`Appendix 3 — Electrical Generators
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`Appendix 4 — Electrical Switchgear
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`Appendix 5 — Crude Oil Piping Reroute Cost Estimate (Project F&55)
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`Exhibit Mo, ATC-810
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`Fage 8 of 50
`PUNP STATION 4 EQUIPMENT REPLACEMENT
`COST ESTIMATE REPORT (FINAL) %
`APRIL 29, 2011 -
`Sharher
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`APPENDIX 1
`Pumps
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`Exhibit Mo. ATC-810
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`Page 8 of 50
`From: Bennett, Stephen
`Sent: Thursday, Aprl 21, 2011 8:01 AM
`Ta: Hoppaer, Dave
`Cc: Crieux, Gilles; Shivjl, Riyaz; Rain, David
`Subject: 2010790000 FW: Alyeska Pipeline Crude Pump Budget Quotation
`Attachments: CAN. 3076-MN0OG.11.0166-P0 MSD-D Apr 20.pdf
`Tracking: Recipiont Ruad
`Hoppar, D
`Orieus, Gilles Read: 42172011 3:56 PM
`Stini, Riyac Read: 42172011 G607 AM
`Rin, David
`
`Budgetary pricing for Sulzer maindine pumps (MSD-D 14x14x18.5C) for station 4 is $532,867 USD/ea. Quantity is (3)
`purmps. Comparison pricing from Flowserve later loday.
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`Sent: Thursday, Apri 21, 2011 43 AM
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`To: Bennett, Staphien
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`Subject: RE: Alyeska Pipeline Crude Pump Budget Quotation
`
`Good moming Stephen,
`
`You are cofrect in that taking $350,000 off the top will give you the package cost less drive. You probably only requine
`half the bage and the cost of the lube system will also be less. The budget price of my quote is getling less accurate -
`within 20% and on the high side is my best guess at this point.
`
`Bast Regards
`
`John Whittaker
`Sales Representative
`
`Sutrer Pumps Canada
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`Calgary, Alberta
`Tal: 403-233-T105
`Call: 403-870-6179
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`%
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`mmmlay 21. A;uilzuumqa
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`To: Whittaker, John
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`Subject: RE: Alyeska Pipeline Crude Pump Budget Quotation
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`Since thess pumps would be driven by gas turbine mechanical drivers | presume we can estimate the pump cost 8s
`#BB2 BET-$350,000 = §532 BET USD/ea. Please confirm.
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`Sent: Wednesday, Aprl 20, 2011 10:41 PM
`
`Ta: Bennelt, Stephen
`
`Subject: FW: Alyeska Pipeline Crude Pump Budget Quotation
`1
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`Exhibit No. ATC-E10
`Page 10 of 50
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`Stephan,
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`Please find attached the parformance data for our sslection for a pump suited to the pipeline application describad in your
`communication dated Apedl 18.
`Please also find attached a sultable GA drawing and brochure.
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`The MSD-D 14x14x18.5C 2 stage is the best selection for the application as described. I've included a ballpark price for a
`7000 HP 3960 rpm molor - about $350,000. It's very common for the end user to purchase their own motor for installation
`at site to help reduce costs, The pump and motor will require a pressurized lube system which has also been included in
`our price along with vibration transducers and RTDs. NDE, hydrostatic testing and performance testing is also included.
`
`A full detall descriplion can be provided on requast.
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`MED-D 14x14x18.5C 2 sig, 5-1 construction, pump package complete with T000 HP molor, pressure lube system for
`purmp and molor, vibratlon ransducers, pump RTS, and mounted on a fabricated sieel base sulted for 2xAP] table 4
`nozzle loads,
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`Estimated $882 867.00 USD,
`Current ship date afler raceipt of order is approximaltely 56 weeks. FCA Portland, Oragon.
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`A couple of other notes:
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`- The M3D i& an angieered product and Is commonly subject 1o fine luning to oplimize the efficiency or 1o intrease the
`operating range. When it comes time o reguest a firm quotation please allow 4 weaks to ensure we are able to provide &
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`= Consideration should be made for cold slars or handling a more viscous product.
`
`- Thara are always different philosophies regarding what typa of pump to handia what type of product. The MSD is
`commonly usad 1o handle dean, light, product with a low viscosity which seems to be whal you have describad sois
`@ good match,
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`If you have any questions or requirs additional information pleasa do not hesitate to call.
`
`Best Regards
`
`John Whittaker
`
`Sales Reprasentative
`Sulzer Pumps Canada
`Calgary, Alberia
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`Tek 403-233-T105
`Call; 403-870-5178
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`CONFIDENTIALITY ROTICE
`
`T irderennlice i this el mipy B confidential sndicr privilegod,
`Thim am! ks mlonded 1 b rrviawed by oy B addmessels] namsd
`nboven, if you are nol the intendad recipient, you e hareby notiled
`thal any review, dissamicalion. copying, uSe or siorage of this amail
`and ity aEechments, il any, or the information containgd herwin i
`profibited. IF v Ferves received this small in smor, plass
`immiedistely notify the: sender by i emall sl delctn this emad
`froem your wysbam. Thank you.
`
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`Exhibit Mo. ATC-810
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`FPage 11 of 50
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`Camtormet Sartec Consulting Lid. | Sulzer Referarce I-IJ___ nmmm—m.nmm
`Projoct Marmg Alyesica Bocster Pump Irsgquiry Db
`Inguiry MumbaeriiD waibal Bid Sxtbrited Digte
`I rurmbar Crude Pump #3 Dt Last Saved 21 Apr 2011 5:28 AM
`Servicn Crudha Ofl Trpnsler Sizes | Tlaghs 12
`Pump speed 3,560 rpm
`Description
`MED-0 14x14x18,5C / 2 &g
`
`Dirhver dirmanaions and waight 1o ba manualy enlersd 1o enmme comedt coulphing and basapiate soloction
`BARESHAFT PLMP.
`Material Class: 5-1 { Mod)
`SctionTalvary Flange Rating: Clies 500
`Dirains Flangs Ripting: Class 800
`Bawring Luba: Prossure Feed
`Isolator Typa: Inpro - Bronea |Solibor
`Oushoard Far: Nona
`Bearing Housing Drain: Pluggesd
`0_FirstStage: Double
`Balanca Spec: B_WIN
`PACKAGING ACCESSDRIES:
`Bi standard base size found - Refer io Advenca Englnearing for GA
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`Basapiats suppliod by: Customer | Othars
`Primary Sead Flush Plan: Plan 11 0,75 System
`
`Primary Seal Flush Cormsénadiion: 316 Tuba
`BLYDLIT COMPONENTS:
`Modor Tarmanal Box Position: RHS viewed from bishind mobod eiics (g
`Db Dimaansicna
`Diriver dimnsions and waight 10 be manuslly omonod ko ersuns sofmsc! coulipling and basaplals soloction
`Coupling Solection: Coupling Not Provided
`Saal Salecion: Spocial Mechanical Saal Ouotation Per Chambar
`Wiring _Syeam: Galv Conduit
`TRAKNEPORT AND PACKING:
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`TESTING, INSPECTION, PROCEDURES AND DOCUMENTATION;
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`Fump Performance Datasheoct
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`10,8375 USgeen
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`- 2,070.4 t
`: 000 /. 0.00 psig
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`20836 ft
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`+ Ampla
`:H-
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`: 3,560 mm
`
`12
`CLFVE: Fiksar : MISD-841.088-81-11-00
`: pr 2011 52289 AM
`
`s AT.08 i
`Imipssiee digematir, macimum tT.4d in
`Iimpsdiesr dsemoher, minimum {448 in
`tHE R MEdmum cosingibow] working pressisrs - 91808 psig
`NPSH mouired / mespin mdquinsd tBLAT00 N Maximurn allowable working prodswe @ 1 008 pai g
`I3 Fmp. fya Row) [ e (imp. e fow) S 14451 9,370 LS Units | Madmum afiowable suclion presssrs © G082 paig
`: 4,538.1 USgpm ol :1,B05.7 peig
`Haend, Faimim, rated diamiotee 238421
`Hizgdl risd fo shoicH 148 % ¢ IBKHTILET) Fecier
`Ficw, bast off, point (BEF) : 11,389.0 USgpm S 000 %
`Flow' ratio (reied § BEF) 19585 % = 1.00
`Dégenator ratio (raried [ ) ETET % 5179 hp
`Head mtic rmted dia /| max dia) 2% 18,124 hp
`Co/ChiCa |ANEIHI BB T-2004) ¢ 1007 1,00/ 0.57 tE,T9T hp
`| Spinction status. : Acrapinbia ¢ 7,000 hp § 5220 kW
`080 .
`2800 - :
`e L o
`245 - |
`1T : ! ;
`bt
`i 2000
`1,800 -
`16 e
`14,48 in
`1,400 p
`1,200 —p s
`100
`188
`-
`g 8
`" ]
`1]
`2 -]
`I 4,000 =
`2030 i
`a
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`0 1000 ;OO0 A0 4000 D000 4000 TOO0 A000 RO00 000 fig0d TRON TLDE 4000 BRO0G 10000
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`Page 2 ol 4
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`Exhibit No. ATC-810
`Page 13 of 50
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`SULZER
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`CENTRIFUGAL PU P DATA SHEET
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`Cushomer, Sinntec Cormulting LE, Bulpar Tander 107 CAN.OTE-NOG. 11.0188-P0
`Priect Narmac Abpwacn Bociler Pump ey Lok
`Irscpeiny MumbeniD: warhal Bl Suibwrired Dike:
`Cuminemer fmm Muamba: Cruda Pamp K3 Dimber Laes] Sorwndd: 0 A 2011
`Servion Crude Of Transisr Cusnidty: i
`b { Gl ) Pumg Tygei
`Tampor purg, Rated b 88,00 deg F 60.00 deg F Product Line: NS0
`Fugid) Dmsrradty, Fisbisci e 0888 53 ) 0.800 856 Pysp Sina I No. of Bages: NS00 14xidniBSC 1 2
`Viaper Prossum, Roisd: 5400 pula Faplstion {vissesd from drive end): S
`Vinofiity, Plabad: .00 ek Suction Impelar Typs {Lngks or doubln)r Doutls
`Ak Conpet = Casing Spit: s St
`Dischurgy Fiom, Ristec: 10,9575 Uiigpm Caming Type: Doubis Viskss
`Discharge Head, Fated: LOBABRTZOTHA R hecuerie Zire Futing F Fea'n
`Sueson Pramsune, nibodsmao: 0.00 pal.g /0,00 peig Bucticn 14 BOON RF Sida
`BPEH Mmintin: Amphs Discharge: 14 O RF Gide
`Podcemanes Curva Mo (8l eSO 1. 0eg-01-11-00 Baafng Typa, Fadis: Elsirne
`Pure Sgae: 4580 rpen e
`Frequency: B He Daariag Typa, Thrust Phvot Show
`FloncVarlabin Speed: Corgtant Sooed Bt Labication: Prassus Seed
`Imipaler Dignatnr, Faled: 17.080n
`Impeier et Wimam: 17,440
`irmpaler Dinrmatn, Winimem: t4.480n
`EMcianey: BAEDY,
`mwm”w BIARIDOR G | Bowwis: Carbon Steel WCB
`1 A48 LES: b [z oy o) [ ban
`K ! Nits: fimg, dyn Bow) /9,370 US: M {mp. | Column:
`ey B} [ s (i e i)
`Faind, Maxismum, Faks Dl PRI R Descharge Hoad
`Hoad R i Shutelt: BN il Carton Sies WCE
`Fiow, st EN Poant (BEPY 11,358 .0 USgom Coatryrniber Wes! Fings -
`Cmerinr Rado | Rated | Max} T eT% EFarft Aoy whewl (4140
`Haead Rstia (Rested Dia ! ax Diac): B4IIN D e -
`Viadni Cosloiesis (GO JCHICEE 100701007087
`Working Prassurs; RS palg Seal Coda:
`Working Pressurn Lismitc V2008 maly Sad Llaredscner -
`Baon Prossurs Lint: B0D.2 paig Seal Faush Piping, Primary, 11
`m“‘lm 1,805 7 palg Saal Flusn Piping, Sarmndery: :
`EaaTt0N P, reelirr L ot g F O Do et Coolng Wster Piping: =
`Chachargn Pressu, Rt 8005 psig A L
`BOD.S pelig -1.34 hp
`TRk Vol uPramsT miguesy, 0.8 130580 Hs
`; 10728 Servich Facion i
`Dirhoir: .00 B Pevte, Flsle: B,1Z2 hp
`Burneimte 1006 Pressps, Mankeum, Fialed Diseagten & 787 hp
`Tote! Fackage: 1BITEE TEFG
`Ciriwat; o Praferetcs TypicXPConsinsciionCastiron DesignHEMA
`Coupling: -
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`Exhibit No. ATC-610
`
`Pags 15 of 50
`SULZER ke R s
`DIMEMSIONAL DATA - TYPE MSD DIMENSIONS us
`Pump and Base - CCW Rotation - Double Suction Nowamiber - 06 D66
`CCW _ROTATION _ : T PAX -
`CSTANDARD) |—— 3.8 % T
`
`r.00 0.8.5.E. F
`
`' L0
`
`{ofyay ¢ o
`prepem— |
`
`14.5 1
`“'I"l. .....
`C
`] ...... P
`75 D) ARETER HOLES
`- FOR MOLD OOWM BOLTS
`o T T Pttt s il |
`Pump is counterdockwise rotation (CCW) as HH - Number of Base Hold Down Holes Each side equally spaced
`standard pump Fotation as vewsd from HF - Distance babseen Hold Down Holas
`wwflmififiunflw CHmensions based on ANSI Class D008 RF flanges
`for Clockwise rotation {CW).
`
`Size: 14 x 14 x 18.5 Double Suction
`
`[ Wo.of X Y w HR c Hk HE = HE HEF
`# fifimmlfim 140 2] 23575 280 | 330
`
`an | Pume W | Base
`[}
`
`=
`
`(1} Abowve diminisions s soonmie for mounting of besepkais, provided drivers DO BOT EXCEED width [P MAX) ond 'C WA dimansions.
`
`(2] For basegiate descripsons and sizing procodurss, or when additional egulpement must b sccommodsied, Ses Saction F,,
`mumahifl-.flnh—mfihufi.mmm
`meflumflhflnfllflfldm
`
`(5} Sl pipdeyd OF Sscman rrary roguine cunging s G
`
`H}mmflm“flmm oy et 1 304 8 mm) st acieneion standasd.
`
`(71 ADD 81, 35 rren (1.5 in.) o dmensions & HE for fan.
`
`LT
`
`(B} ADD 2694 mem {1155 i) e dimersion Y & HE' for Sleevahaot bearings with shalt driven LOF or T4,12 mm (28 In ) e THE for Sleeva'Pheot baarings wio shall
`
`drtvmn LOP.
`
`TR0} ADD 50U men (2 ) o this dimansion for B008 fangs.
`{11) Base Pisin weight s besed on ble sbow. AddiSonal infrmation on base plates in Saction F, lass Piste pages. For Skid add 800 LES (EXT Kg)
`
`
`
`
`
`
`
`
`
`Exhibit Mo. ATC-610
`
`Page 16 of 50
`Ben Ste
`From: Bannett, Stephen
`Sant: Monday, April 18, 2011 1:38 PM
`Tox “Whilttaker, John'
`Subject: Stantec Edmonton - new pumps budgel price
`Attachmants: PS-4 Mainline Pump Sizing Sulzer (vendor).pdf
`Hi Johin,
`
`We're on a naw estimate job for Alyeska Pipeline Sarvices Company. These are larger pumps for mainkine crude ol
`service. | ran the process conditions through the online software application and came up with a MSD-D 14x14x18A. The
`datasheet and curve are attached. This ks a 5-1 materials selection.
`
`mummfimfl#mnmmmmmmnhfinpflmhnmflfin{mw | will need this
`as 500n as practical for you, but bafore end-of-business this Thursday. Please advise ET.
`
`Call or emall with any questions.
`
`stantsccom
`
`The conbant of this email & the confidential propary of Stantec and should not be copled, modifiad, retransmifted, or usad for any
`purposa except with Stantec's written suthorization. i you are not the intended reciplent, pleass dalete all copies and notify us
`immediataly.
`
`P Piease consider the emviconment bafare printing this emal,
`
`
`
`
`
`
`
`
`p Performance
`
`Pom
`
`MORTH ELOPE CRUDE OiL
`
`i M08, 058-51-11-00
`
`; MSD-D 1l din B
`DAMER011 841 P
`
`+ 10,0837 5 (5,833.0)
`
`LEgpm
`
`Fiow, rated
`
`D (LEBE /0.0 BG
`
`- 80.00 deg F
`+ 920,00 P
`
`d hypa
`Adcitional Bguid description
`PN
`
`Siclicln
`
`T (Mod)
`
`AP B
`
`K
`
`10278 pal.g
`11,2038 pal.g
`
`_m
`m
`m
`m
`
`P ZOB3E N
`000/ 0,00 pslg
`
`Cifprantial head ! preddun, raled [reguested) | 20800 (2.557.0) ®
`Cearantial hesnd ! prossune, raled (Schusl)
`
`Suction pressuna, frked [
`MPSH mvaliable, rabed
`
`s;.ud.r-ud
`
`WPSH required | margin e
`
`i (iemp. ey flow] 1 5 (imp. eye flow)
`
`Irnpallar diamsier, raled
`Ienipadiar diarmeler, mersrmm
`MCSF
`
`Ienpelar diamter,
`
`Haad, maximum, rated diamster
`Haad riss fo shuof
`
`| 26.62 (260) %
`
`: 9,641.8 USgom
`
`Flow, baest off. point (BEF)
`Flow ratio (rated ! BEP)
`
`£ 113,44 (B0.50) %
`
`m.m.m
`5%
`1503
`mmmm
`
`o131 %
`B30 %
`
`Hameter ratie (rated /max)}
`
`Hoad rato (rated dia / max dia)
`
`1,007 1.00 1 0,64
`
`Co/ChCa [ANSUH| B.8.7-2004]
`Selocton status
`
`ALYVESKA FUMP BTATHOM 4
`
`g
`:
`?
`g
`2
`g
`. g
`i £
`b g
`g i g
`3 b :
`e :
`{8t : 1
`: g8 8 °
`- i
`
`Figrwr - LiBggem
`
`
`
`
`
`
`
`
`
`Exhibit Mo. ATC-E10
`
`Page 18 of 50
`PUMP STATION 4 EQUIPMENT REPLACEMENT
`COST ESTIMATE REPORT (FINAL)
`APRIL 28, 2011 %
`
` ———
`
`APPENDIX 2
`
`Gas Turbines
`
`
`
`
`
`
`
`
`Exchibit No. ATC-810
`
`Page 19 of 50
`From; James A. Raeside [Raeside_James A@solarturbines.com]
`Bent: Wednesday, April 20, 2011 10:44 AM
`To: Bannatt, Stephan
`Ce: Miks E. Clay; Greg B. Mittanck; Anthony X, Tsai
`Subjact: RE: Stantec inquiry - Solar Turbines Taurus T0S MD - Budget prcing - Alyeska Pipaling
`Altachments: dsTOmd. paf
`Dear Stephen,
`
`Further to our telephone conversation yesterday, please see below price and delivery for gty (3) Taurus 708 Mechanical
`Drives for the Alyeska Pipaline per your request.
`
`Solar Turbines Budget Pricing
`Base Package includes the following:
`
`- Taurys 70 Mechanical Drive
`
`- NEC, Class 1, Group D, Division 2
`
`- BoLoNOx Gas Fuel System w/ 25 ppm NOx emissions
`= Direct Drive AC Motor Driven Starting Systam
`
`- Gas Fuyel System with AluminumValve Body
`
`- On-Skid Controds System
`
`= Etfvesrmiat nestwork interface
`
`- Engine Parformance Map Display
`
`- Vibration Analysis — Torsional & Lateral Analysis
`
`- Portable Engine Claaning Sysiem
`
`- Cleaning Tank -~ ASME certified
`
`- Short term praservation
`
`= Alighment Tool
`
`- Factory Emissions Testing
`
`- Customer Participation of Testing - Observe only
`
`- Donalgson Carbon Steel Self Cleaning Inlet Air Fiter
`= Inlet Air Sllencer wi carbon steel ducting components
`- Exhaust Silancer, Floor Standing, Carbon Stesl
`
`= Exhaust System Ducting — includes silencer and stack rain profection
`
`PHOB[BECH]. . ..evvererenssrenssssscassmemssssssssssemsnssssenssenenssneeee U Be $5,300,000,00
`
`Pricing Is in U.5. Dollars, exclusive of all Sales Taxes, Ex-Works.
`Delivary: 12 months from receipt of order
`
`it should be noted that the above package Is based upon an On-Shore Ol & Gas Package and does not include a Driver
`Enclosure. Also, il is important 1o note that we have worked with Sulzer before on similar type applications.
`
`| trust that the information provided in this e-mail is sufficient for your FEED study, howsver, please contact me should you
`
`For your consideration.
`
`
`
`
`
`
`
`
`Exhibit No. ATC-810
`Page 20 of 50
`
`Regards,
`
`Jirn Raesida, P.Eng,
`Salar Turbines Canada Lid,
`Calgary Field Office
`
`Tel: 403-261-2640
`Cell: 403-874-6800
`Fax: 403-261-2757
`
`e-mail: fim_rasside@solarturbines, com
`
`“Hannett. dtephen” uphen, Bennathifstantes coms To “Jamas A. Reoside” <Aaeside_James_Aglsolarhurtings. com>
`=
`AHAZTY 0245 PM Subect RE: Stantac inguiny - indusinial gas lurbine budget pricng - Alyeska Pipsling
`
`Calerpilar: Conbdentinl Grsan Fetisn Uniil: 0SH2011
`
`Based on the high ambient temperature case I'd say the T80 is undersized while the T70 is close to bang-on for shaft HP
`(considaring a 15% overdesign). Preference would therefore be the Taurus 70.
`
`From: James A. Raeside [mailto:Raeside_James_ARsolarturbines.com]
`
`Sent: Tuesday, April 19, 2011 3:08 PM
`
`To: Bennett, Stephen
`
`Ce: Mike E. Clay; Dave J. Phaneuf; Greg B. Mittanck
`
`Subject: Re: Stantec inquiry - industrial gas turbine budget pricing - Alyeska Pipaline
`
`Dear Stephen,
`Thank you for contacting us regarding this opportunity.
`Solar will provide you budget price & delivary on / bafore Thursday April 215t par your request.
`
`Attached please find Tawms 60 & Tawus 7O Gas Turbine performanca al your site conditions for your review and
`Comment.
`
`Please advisa your preference.
`Best Regards,
`
`Jim Raeside, P.Eng.
`Solar Turbines Canada Lid.
`Calgary Flald Offica
`
`Tel: 403-261-2640
`Cell: 403-874-6800
`
`
`
`
`
`
`
`
`Solar Turbines
`A Catorpitisr Company
`
`+ Bearings
`- Joumal and Thrust: TIR Pad
`
`Coatings
`= Compressor Stators and Drums:
`
`TAURUS ?0
`
`stbine Mechenieal-Dii
`
`Key Package Features
`
`* Driver Skid with Drip Pans
`
`» 316L Stainless Steel Piping
`£102mm i47)
`
`» Compression-Type Tube Fittings
`
`+ Digital Display Panel
`
`+ Electrical System Oplions
`~ NEC Ciass |, Group D, Div. 1or2
`- CENELEC Zone 1072
`
`v Thrbotronc™ Microprocessor
`Controd System
`— Offskid or Onskid ControfNet 1.5
`
`- Predictive Emissions Monitomng
`» CE/ATEX Zona 2 Certification
`
`- Swart Systems
`
`= Pneumatic
`= Direct Drive AC
`* Fuel System: Natural Gas
`
`. w?_gmummmm
`— Turbine-Driven AcCessories
`- I0il Tank Vert Separator
`= i Tank Vent Flame Trap
`* Lube Qi System Options
`= Ol Cooler
`— Odl Heater
`* Compressor Cleaning System Options
`= On-Crank
`= Cn-Crank/On-Ling
`= Certified Cleaning Tank
`* Gaarbox (if applicabie)
`« Ajr infet and Exhaust System Options
`« Encicsune and Assockyied Oplions
`» Factory Testing of Turbine
`and Package
`« Documentation
`— Machanical and Blectrical Drawings
`— Quaiity Control Data Book
`= [nspachon and Test Plan
`- Test Repoits
`
`
`
`
`
`
`
`
`Solar Turbines TAURUS 70
`
`A M‘H w Geas Turbire Mechanieal-Drive FG:L..-DE:!.'.-
`
`Performance Available Power
`DUF L Tows” TERD N 1714012 .5
`10213 by (JENF-3 | 1912
`Hean Rae 13 M RIAW-hr _
`7213 Bewhps=hr) =
`= HBI ne =
`Exnnusl Flow BS B30 ke £ SFRFET 1FF Py T
`{210,830 e z =
`Erhaysl Termp 495 E Oulpud Pow %
`B2 =] 5 W00 1405
`7 (R [EL f
`Noména! Rabng — (150 5 :l_l
`e T S asa i B
`m@wwmum = et lmfiffi
`Relatyve humaiy 60% Haal Ralu e
`Natural gas kel widh
`LHW = 35 M.’ (840 Bhuisaf) i 84
`Dptmum power fusbing speed 70N 18715}
`; o P T ] 15,0 2.4 15.0 0.0 L]
`AL -drTren SCOPSS0NET i %) 133 L0 T.19] [113)
`Engine sficincy: 34.8% NLETAIR TEMPERATURE. °C |'F) N
`Package Dimensions
`Length: 7.7 m {35 37)
`Wih: 27 m {85
`Heabght 3.3 m (100 9°)
`Typical Welght: 24 550 kg (54,000 Ih)
`PO, Box BERT0 T FORMATION el
`RO Box BEATH FOR MORE IN
`San Dlago. CA 621588378 Taluphona: i+ 1) BT6A44-A 302 w
`e Poain FabiAe s 50 Rinbarte e e e T s gt IFaEmat. W SOLMTUIDINS. com
`i M o Rl W A e wiles Pl B
`8 T T e il B ol et DV
`B s gu]
`
`
`
`
`
`
`
`
`
`Exchibit No. ATC-610
`
`Page 23 of 50
`
`Benn hen
`
`CE T
`From: Bannatt, Stephen
`Sent: Tussday, April 18, 2011 247 PM
`Te: 1im_rasside@solarturbines.com’
`Subject: Stantec inquiry - industrial gas turbine budge! pricing
`Hi Jim,
`
`As mentionad during our phone conversalion we ane submitting this emad request for sizing and budget price for industrial
`gas urbines on behalf of our client Alyeska Pipeling.
`
`Stantec has bean contracted for a cost estimate study on an altemative pump station configuration which involves in part
`the provision of (3) new gas turbines. These turbines would be mechanical drivars for lange mainline crude ofl pumps.
`These pumps are praliminarily selected as Sulzer MSD-D 14x14:x18A or Flowsene equivalent.
`
`Each of the three pumps is identically sized at 6500 brake horsepower, with a speed of 3600 rpm. The gas turbines
`should be rated for this power with an additional 15% capacity available for overdesign flowrate or fulure changes fo the
`
`crude oll propertias.
`
`Location conditions for the gas turbines is at an altitude of approximatety 3000 ft above sea leved, indoor placement, with
`intake combustion air mimimum temperatune of -60F and 8 maximum temperature of +B0F, This location is in a seismic
`zone rated at 7.5 on the Richier scale,
`
`The gas turbines would be fueled with natural gas.
`
`Please indicate the lurmdown rangs for the selected turbine model. The scope is for complate tumkey units. Incuda
`manufacturer arector services for commissioning and starlup, Emissions complience to curment EPA end DEC [Alaska)
`
`regquiraments,
`
`¥ou are requested 1o provide +/- 25% quality budget pricing in USD for this proposal. Due to dient needs we require your
`response before 4:00 PM Thursday Aprl 21.
`
`Call or email if you have any questions.
`Thiank yodl.
`
`Stephen Banneti, P.Eng.
`Senior Mechanical Enginsar
`Stantec
`
`Thie contant of this email is the confidential property of Stamec and should nol ba copled, modified, retrensmitted, or used for any
`purpose axcept with Stantec’s weitlen authorization. i you are nol the intended reciplent, pleass delete sl coples and notify ws
`iFrimisdEatedy,
`
`“® Please consider the environmant before printing this emal,
`
`
`
`
`
`
`
`
`PUMP STATION 4 EQUIPMENT REPLACEMENT
`COST ESTIMATE REPORT (FINAL)
`
`APRIL 29, 2011
`
`Exhibit No. ATC-610
`Page 24 of 50
`
`&
`
`Lo G T
`
`APPENDIX 3
`Electrical Generators
`
`
`
`
`
`
`
`
`Exhibit No, ATC-510
`
`Page 25 of 50
`From: Bennett, Stephen
`Sent: Monday, Apdl 25, 2011 10:22 AM
`To: Hopper, Dave
`Cc: Oriewx, Gillas; Shivii, Riyaz: Rein, David
`Subject: FW: 2010790000 Stantec-Alyeska Budgetarys.doc
`Attachments: Stantec-Alyeska Budgetarys.doc
`
`Tha 900 kKW unit below turng out 1o be dissel fueled. This unit should be natural gas fueled. However the closest size that
`Caterpillar sells is the 1.3 MW unit. This is oversized but will have lo do for the eslimate. Therefore, use the 51,540,000
`plus $225,00 price and show the size as 1.3 MW backup Lifeline genarator.
`
`From: Bennett, Stephen
`
`Sent: Monday, April 25, 2011 7:39 AM
`
`To: Hopper, Dave
`
`Ce: Orieys, Gllles; Shivii, Riyaz; Rein, David
`
`Subject: 2010790000 Stantec-Alyeska Budgetarys.doc
`
`This pricing for P3-4 gensets was received after business on Friday.
`
`These prices can be considerad better quality than the Cummins price estimales sent previously. Uise these "Caterpillar®
`pricas for our estimate.
`
`The (3) 500 kW continuous rated gensets are listed at $325,000/ea plus an additional $100,000/ea for exhaust aftes-
`freatment (for EPA tier 4 complianca). Thess units would be instelled indocrs.
`
`The single lifefine backup gensel shown as 910 kW prime rated is priced at $900,000 phus an additional $250,000 for
`exhaust afler-treatment (for EFPA tier 4 complianca). This unit is in an Arctic Pack package for ouldoor standalone
`installation.
`
`Steve
`
`
`
`
`
`
`
`
`Exchibit Mo, ATC-510
`
`Page 26 of 50
`IR N ¢ POWER sYSTEMS co.
`April 22, 2011
`
`Stantec
`
`10160 - 112 Street
`
`Edmonton AB TSK 2LE
`
`Reference: Budgetary Estimate for Alyeska Pipeline Service Company
`Generators
`
`Mr. Bennett;
`
`The following will provide a summarized list of budgetary cost for generator sets we
`recently have been discussing. Each of these generator sets has all the major
`equipment to assemble a functional package with the addition of piping and electrical
`conduct