. .
Y
REPORT ON
GEOTHERMAL POWER PLANT COST AND
COMPARATtVE COST OF
GEOTHERMAL At!D COAL F I R E D STEAM POWER PLANTS
Prepared for
UTAH POWER AND L I G H T COMPANY
Y
Y
DISCLAIMER
DISCLAIMER
...
4-L .
TABLE OF CONTENTS.
I
tern Page-
Sect ion I ,- 1.0 INTRODUCTION 1.1 Purpose 1.2 Scope1.3
Format and Parameters1.4
Two Unit InstallationsL
1-1 1-1 1-1 1-1L
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2.0 2- 1 .1 Geothermal Power Plant Criteria2.2 Geothermal Power Plant Cost Estimate 2-1 ,
2.3
2-2 2.4
2-2
2.5 Plant Capacity Factor 2-3
2.6 Appendix lnformation 2-3
Geothermal Power Plant Operating and Maintenance Cost Comparisons, Geothermal and Coal Fired
Requirements Power Plants
3.0
GEOTHERMAL POWER
PLANTCRITERIA
3-
13.1
Weather3.2 Geothermal Well Data
3-
13.3
Power Cycle3-3
3.4
Slte Preparation and Building Construction3-4
.3-5
3-7
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3.5
Mechanical Design3.6
Electrical Design.Environmental Protection Considerations 3-10
Instrumentation a
3-1
14.0
GEOTHERMAL
POWER PLANT COST ESTIMATE4.1
Building4
.
2 Mechan 1 ca 14.3
Electrical 4- 1 4-2 4-24-3
4-3
1
4-4
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5.05-
15-
15.3
Expected Plant 5-2L
6.06-
16-
1 6.2 Coal Plant Costs by Accounts6.3
Cost Comparisons, Goethermal and Coal Fired Power. Plants
6-1
.e
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TABLE
OF CONTENTS (Cont'd)Appendix A
A- 1 Steam Gathering and Waste Water Reinjection Systems - Description
A-2 A-3
A-4 Equipment Quotat ions
Steam Gathering and Water Reinjection Systems Cost Estimate Gathering and Reinjection System Economics
&pendix C
Two Unit Estimates and Comparison Two Unit Geothermal Plant Estimate
Two Unit Coal Fired Plant Estimate
Cost Comparison, Geothermal vs Coal Fired
c-
1
Introduction c-2c-3
c-4
c-5
Cash Flow AppendixD
Back Up Information, Cash
Flow
and Interest During ConstructionDrawing No. Lil A-02- 102 8-02- 10 1 B-04-101
A-08-
1 0 1 €-Of-1
0 1 B-80-101 B-80- 102B-80.-
103 8-80- 104 .B-80-105 Table No.4-
1 4-2 6-1
6-2 C- 1 c-2c-3
c-4
i.
I FigureNo.
6.4-16.4.-2
INDEX
OF DRAWINGS 1 DescriptionNoncondensable Gas Purification "S tretf ord Process''
Power Plant Process Flow Diagram
4
-Plot Plan
Power Single Line Diagram
Page
3-15
3-1
4
3-16
3-2 1 Construction and Engineering Schedule
4-1
1Ground and Mezzanine Floor Plan
3-17
Operating Floor Plan
3-18
Side Elevation
3-19
Cross Sect ion ' 3-20
Ground and Operating Floor Plans, 2 Units APP.
c
INDEX OF
TABLES DescriptionSummary
-
55
MW
(Gross) Geothermal Power Plant Cost Estimate-
June1977
Cash Flow Estlma Power Plant
-
55
E.1W (Gross) Geothermalred Steam Power Piant
-
ate-
Hay1977
Geothermal v 1 Cost Estimate Comparison Summary
-
2XCost Est ima t
2X 400 MW Co
fmery #l and 62 Estimate
-
May1977
Geothermal vs Coal Cost Estimate Comparison
(Grossf Geothermal Power Plant
rn Power Plant
brass
f
Geotherma 1Engineering E; Construction Schedule for
400 HW Coal Fired Plant
Engineering E; Construction Schedule for
- -
1.0 INTRODUCTION
iil
ngineering was reque (gross) geothermal p
d to prepare a cost estimate for r plant at Roosevel t Hot Springs power plant cost in ollars per net kilowatt is to
be compared th that for Utah ower and Light Company's Emery No.
1
400M
et) coal-f ired eam power plant now under con- s t ruct ion.i
id
the Phillips Petroleum Company's discovery. The1.1 Purpose
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. i i 1.2This report is to be used by Utah Power and Light Company In making studies of geothermal plants. The dollars per kilowatt comparison between ermal plant and a UP &
L
coal-fired plan s to be developed. Geothermal gathering
system costs an eturn to owner are to be developed for in- format ion.
I
Scope
Prepare a detailed conceptual cost estimate for a
55 MW
gross(32
MW
net) geothermal power plant using Phil 1 ips Petroleum Company's resource characteristics.Prepare preliminary pr cess flow diagram to size major equipment Letter quotations on major items are included
Provlde an estimate of cash ftow during the engineering and con- struction period.
t
. fey;
er letter quotations stating price, delivery, and nt.
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1.3
Format and ParametersThe cost e s t i m a t e detail i s to follow U
P
S L's format for Emery No. 1: Man-hours, Material and Equipment, and Direct Labor costs.u
P &
L ' s mos e to be used in the geothermlntal costs are to be shown
ey could sup- The resourte are those in ROGERS previous report 'for
'UP &
L
"Evaluation of Geothermal Fluids from We1 1 No.54-3" December
1975.
t
1.4
n i t Jnstallatlonsconomy inherent in constructing twofunits at one plant site, thus
utilizing
certain c m n facilities, cost esti- mates and comparisons are provided for a 2X 52MW
geothe-mal powei plant and a 2X 400MW
coal fired plant.I '
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2.0 SUMMARYThe information in this report is to aid Utah Power and Light in their economic studies related to geothermal electric power gene- ration from the Roosevelt Hot Sprtngs resource. The report in- cludes development of the geothermal plant design basts, power plant cycle, process flow diagram, and the electrical power single l i n e diagram on which the estimated capital cost is based. The coal plant data was furnished by Utah Power and Light for its
Emery Plant, Unit No. 1, being constructed and due for operation
in
1978.
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1
2. i
, - urnished the resource data at
downhole conditions with enthalpy of
493.3
Btu per pound.power plant destgn which maximizes the energy extraction per .
pound of resource i s the double flash system.
tlons'are favorable to the double flashed system which utilizes a turbine with two entry steam pressures.
Informatton available to date, indicates that the noncondensable gas content o f the flashed steam has a low hydrogen sulfid, e con-
lant incorporates a minimum amount of hydrogen sulfide Added costs are specified in Section
3.3
i f hydrogenThe Resource condi-
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ulfide abatement i s necessary.
ant as conce l l y designed uses 3,926,600 pounds per hour available after [down hole basis) of the resource.
the production fluids are to be re rated 55,000 kW gross with an estima station power i s subtracted.
chanical and electrical design criteria are discussed by equipment i'tems and overall characteristics.
n should be noted concerning equipment and material con- er hour, of
plant is
Special at- struction.
units, Is designed on a unit basis.
The plant, In the future to hold a total of two The electrical single line
d selected accordingly. is assumed always avail-
small diesel generator
2.2
ection
4.
ItIs
istration area.
It has been general practice to include only two
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The bullding i s laid out to accommodate a future additional 52 MW unit.units
per plant to minimize trmsporting the geothermal fluids and steam great distances.one plant the geothermal wells would probably be several miles from the power plant.
I f more units were installed in
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tah Power and Light's subaccounts and the Federal Power Commission ccounts were utilize n detailing the plant cost estimate. Major
equipment cost and de Utah.
Power. and Light's Emery No. 1 power plant labor rates were used in. the cost estimate. The total construction cost including substa- tlon 1s estimated to be $23,640,400 or
455
dollars per net ktlo- watt.ery time were solicited from vendors-
The engineering and construction time required is estimated to be
34
months based on similar plants. Section4.5
contains a schedule for engineering and construction of a 52 MU geothermal power plant.This time excludes permit and utility comission times, if required, before engineering.
accounts in Section
4.4.
Geothermal Power Plant Operating and Maintenance Requirements The operation staffing and 'maintenance requirements are direct in- puts to developing cost of energy sold.
staffing requirements for normal operation and maintenance. plant is planned to be base loaded and operate three shifts per day.
tepor t
.
+The plant is schedule
year. The maintenance crew is listed in Section 5.2.
The d ailed estimate is provided by the sub-
This report discusses The .
Operation and maintenance expenses are not shown in this
or maintenance approximately two weeks per
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The Emery comparison plant because the labor costs are the No.1
coal fired steam power plant was selected to most recent. be the summary by FPC account category is included in Section 6.2.labor rates were used in t
Emery costs are from the
M
A These geothermal plant cost estimate. The
1977
monthly cost forecast.geothermal power p l a n t and t h e
ollow. Both single unit and tional detail and backup for
e found in Tables
6-1,
Geothermal Coal Fired Tota
1
Cost [substation excluded) $22,482,700 $252,000,000Dollar per Net Kilowatt 432 -630
Net Capacity 52,000 kW 400,000 kU
Engineering E Constructi
34
months 60 months. .
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-_TWO Unit Plants
Geotherma 1 Item
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Total Cost Csubstation excluded1 $39,142,000Net Capacity 104,000 kW
Engineering and Construction Time 40 months
Base Load Yes
Dollars per Net Kilowatt .
376
2.5 Coal Fired $449,933,000 562 800,000 kW Yes
--
Plant Capacity Factor
paclty factor i s estimated to be
85%.
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I Four appendices are included with the report. The first (Appendix
A) develops cost and investment return ranges for the geothermal resource production and reinject ion system.
B)
cont,ains letters from manufacturers relating to cost and deliveryof the major equipment pieces in the geothermal power plant.
geothermal cost estimate reflects these manufacturers' data.
' third (Appendix
C)
gives estimated costs for two unit geothermal andcoal fired plants. The fourth (Appendix D) includes back up informa-
t i o n for calculations of cash flow and IDC.
The second (Appendix The' The
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3.9
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e
-GEOTHERMAL POWER PLANT DESJGN CRITERIA
This Section presents the geothermal power plant design criteria and the operating conditions the design i s based on. Main areas
of discusslon presented here are as follows:
1)
Weather conditions21 Geothermal well data
3)
Power cycle4)
5 )
Site preparation and building constuction Mechan
I
ca 1 des i g nrotection considerations Weather Data
Basis for design for cooling tower and ventilating and air con- ditioning design:
Summer: 96°F Dry Bulb 67°F Wet Bulb Winter: 920°F Dry Bulb
Haximum Wind Velocity: 60 mph Design wind loading:
I
Below 30 feet
Above 30 and Below 50 feet Above 50 and Below 100 feet
-
15
lbs. per square foot-
20 lbs. per square foot-
25 lbs. per square foot Geothermal Well Data \Downhole 1 iqu4d temperature: Downhole l i q u i d enthalpy:
Noncondensable gas composition:
Gas
-
0.02 Hydrogen 0 -75
He1 ium Net hane 0.004 Nitrogen0.8
Carbon Dioxide93.34
Carbon Monoxide e10 PPm
0.1 Argon
Noncondensable gas quantlt): 2% by weight
in
the fyrst- -
bd Chemical Content o f Resource per Lab Report 0323-75
PPM
Boron,B
31
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Calcium, Ca Magnesium, Mg b 10 0.01 Potassium, K 470 iu Sodium, Na 2,200 tu .145
.
Chloride,CL
.3,900
k Nitrate, ~ 0 3 ) Nitrite, NO21 '75.1
520 bd . Silica, Si02 Ir nate, CO ) bonate, kO3)173
ki PH7.58
.Y Gas Composition o f Resoure per Well Data, Handwritten-Well
54-3
Sample #4 Gas From Wellhead 9/17/75
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3.3 Power CycleL
55 MW GENERATION UNIT (GROSS) CYCLE DATAResource Flow lb./hr. (Downhole Basis)
Flash Steam Flow lb./hr. (100% Steam B a s i s )
To Generator Turbine
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F i r s t Flash Steam Pressure (psia) Second Flash Steam Pressure (psia)
1 s t E n t r y
-
Temperature, "F/Case Pressure, p s i aNoncondensable Gas % W t . o f 1st Entry Steam
2nd Entry
-
Temperature, "F/Case Pressure, p s i aHain 'Condenser I n l e t , Inches Hg Absolute Turbine Steam I n l e t Conditions
. Pressu
Temperature
Steam Enthalpy, Btu/lb. I n l e t a t Flange l s t / 2 n d Turbine Drop l s t / 2 n d
Turbine Exhaust S a t u r a t i o n Temperature
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. Condenser Type: Condensing Water Flow 1b.rVlr. GPM (60°F) Temperature "F/Pressure, p s i g f'L
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Cold Return \e a t Transfer Duty, Btu/hr. ( m i l 1 ion)
a t Generator Terminals Cooling Water C i r c u l a t i o n Pumps
Cooling Tower Fans
Mlscellaneous A u x i l i a r y Loads
TOTAL POWER PLANT AUXILIARY POWER
DESIGN NET GENERATION
- -
3.4
Site Preparation and Building ConstructionThis Section describes the site and power plant building aspects of the project.
3.4.1
Site PreparationDrawing B-04-101, included at the end of this Section, indicates the layout
of
the power plant site relative to the power plant building, cooling tower and substation.of these three components for the additional Second 52 MW unit are also shown.
The future development The substation is shown fully entlosed by a e and gates. The power plant building shows the cess door central to the turbine'units in the ent. Front access to the administration area is shown in relationship to a proposed parking lot, landscaping and paved area, with direct roadway access.
For
the initial phase (one 52 MW unit), the drawing shows the main transformer connected via a bus duct to the13.8
kV switch- gear inside the power plant, and connected to the high voltage substation bus having three oil circuit breakers and associated disconnect switches; the first terminal point i s for the main step-up transformer; 2nd and 3rd terminal points are for the138
kV 1 ine takeoffs. Future arrangement provides for expansion of the ring bus to five(5)
terminal points, i. e., two points for step-up transformers, and three points for138
kV line take-offs.
3.4.2 Building Design Criteria
Structural Frame Steel columns and bracing Mezzanine Floor and Operating floor
Roof
Truss Steel, long-spanSteel frame, with concrete filled steel decking
r
I Exterior Wal Is Steel "Gal bestos" panels
insulated, with inside liner. Exterior and
interior faces pre-finished. (lrU" Value 0.13).
Steel "Galbestos panels, as
above. ,
3,000 psi concrete 4,000 ps f concrete
Zone
3
-
Importance Factor1.5
Zone 20
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,,Roof i ng
Foundation, Ground Floor Slab Turbine Pedestal
Selsrntc Design Wind Load
Assumed Live Loads
. Operating Floor 125 psf
Reinforcing Steel . ASTM A-615, 60,000 psi
. Structrual Steel ASTM
A-36
Assumed Soi 1 Pressure 3,000 p s f
Roof 20 psf (snow load
-
202Mezzanine
75
psfThird
Floors75
psfAdministrative Bay
-
Second andlu
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3.4.3
' Building Types Considered:L
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a) Poured in place reinforced concrete frame, exterior walls .and floors (mezzanine and operating floors); a steel roof
framing system with steel roof siding.
b) A structural steel frame with steel bracing and steel wall siding; structural steel floor framing (mezzanine and
operating floors) with concrete fill steel decking, a steel roof framing system with steel roof siding.
[Reinforced concrete foundations, ground floor slab and tur- uld be common to both types a and b).
selected on the basis of suitability for archi- . tectural requirements and economy. The dimensions indi- cated for the power plant building provide for optimum operating efficiency in both the vertical and horizonal directions.
Long span trusses over the operating floor provide the clear span required for the flexibility of overall bridge
ors for the performance of the operations are included to facilitate a logical flow to and from the building. The main service access to the power plant will be via a large rolling steel door, motor operated, planned central to the
-
two 52 MW units (2nd 52 MW unit-future) and contiguous with the machine shop., The main control room will be located on the third level of the administrative bay, level with the operating floor. By means of an observation window, the control room will have
the visual control for the entire operating floor area. Reference sketches of floor plans, building side elevation and
ss section are shown on Drawing Nos. 8-80-101, 102, 103 and
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3.4.4
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t the end of Section
3.
1
b
3.53-50 1
equipment are shown on the process
t the plant, plot limit on the econd stage separators and b
f l o w diagram 8-02-101. The power plant
from
the mechanical 'viewpoint is considered to startdownstream side of the first and
finish at the coollng tower and vent silencer discharges.
4
-The first and second separators and the reinjection pumps are thering and reinjection system, and ower plant components.
t;
Main Turbine
1 '
. 3.5.2
' b
The main turbine is a double flow, mixed pressure condensing turbine. The high pressure stage inlet pressure is approxi- mately 110 psia and the low pressure stage inlet pressure is approximately 25 p a with a rated gross output f r o m the generator of 55 MW The turbine output shaft is coupled directly to the ge rator shaft. The turbine exhausts into
condenser at e back pressure of
89
m m hg.(3.5
inches) absolute. The steam flow is controlled on the high pressure and low pressure inlet lines by means of control valvesuated through the hydraulic governor system on the turbine.
The material of construction of the turbine is as follows: a) Top and bottom outer shells are cast steel
b) Steam path is stainless steel
c) Blades and rotor are stainless steel.
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3.5.3
CondenserL
The main condenser i s located immediately below the main turbine and accepts and condenses steam discharged from the turbine primary and secondary exhaust stages. The coneenser is a direct contact spray condenser in which exhaust steam from the turbine i s directly mixed with and condensed by the cooling water from the cooling towers. The condensate then becomes part of the make-up cooling water in the cooling tower. The condenser is constructed of a carbon steel outer shell clad with
316L
stainless steel for theinner shell.
The condenser i s operated at a vacuum o f
89
mm (3.5 inches1 Hgwhich is produced by the steam jet ejector system. The condensate i s removed from the condenser by means of the hot well pumps and pumped directly to ere Noncondensabte gases are removed from a spe sectlon ? n the condenser by means of a two stage steam jet ejector.
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3.5.4
Hot Well Pumps.i
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cEach hot well pump i s
pumps are located adjacent to the condenser and are the "canned" type vertical contrifugal pumps,
low net positive suction head available from the condenser.
pump is sited to handle
55%
of the total flow though the. condenser.The flow
to
the cooling tower from the condenser via' the hot, wells pumps i s controlled by means of flow control valves which areintegrated with the water level control system on the condenser. ted 1,000 horsepower. The hot well
This type is used because of Each
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3-6
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3.5.5
Cooling TowersH:
The c o o l i n g tower i s a mechanical induced d r a f t type having s i n g l e speed reversing e l e c t r i c motor d r i v e n fans.
fans have t h e reversing c a p a b i l i t y t o insure proper operation d u r i n g w i n t e r conditions.
through t h e towers thereby inducing t h e d r a f t .
The c o o l i n g tower f u n c t i o n i s t o cool t h e water r e t u r n i n g from
t h e condensers v i a the h o t w e l l pumps, and-provide it c o l d water
d a l l water using equip-
ment as w e l l as a t e r t o the p l a n t f i r e
The c o o l i n g tower
The fans a r e operated t o d r a w * a i r
.
.
storage s u f f i c i e n tt h e . cool i ng tower bas i n
The water i s drawn i n t o
. (cold w e l l ) v i a l a r g e diameter piping.
the condenser under t h e e f f e c t o f a vacuum produced by the e j e c t o r sys tem.
The c o o l i n g tower i s konstructed mainly from wooden members
forming the superstructure and louver sides.
c e l l s a r e separated by f i r e proof s i d i n g which i s a l s o used
t o cover the o u t s i d e un-louvered areas.
The i n d i v i d u a l P-
3.5-
6 P i p i n g SystemsLi
The p i p i n g i s b a s i c a l l t h e o t h e r water. The scarbon s t e e l p i p e and the
from s t a i n l e s s s t e e l pipe.
n o t e x h i b i t the same tendencies as geothermal water t o cause
c o r r o s i o n a t an accelerated rate. . -
separated i n t o two areas, one steam and am system p i p i n g i s constructed from
t e r system p i p i n g i s constructed
The d i s t i n c t i o n i s made because of
Geother-1 steam does
. t h e c o r r o s i v e nature o f geothermal water.
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3.6 E l e c t r i cat Des i gn'k;i
3.6.1 'Genera 1 1 3. a t i e c t r i c a i uesign Y 3.6.1 'Genera 1 1proposed Utah Power and
n "Power Single L i n e
ev. A, included a t t h e end of
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t
.i t h a gross output o f 55
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b l Generator a i r c i r c u i t breaker switchgear w i t h c i r c u i t
breakers r a t e d 13.8 kV and 1,000 MVA i n t e r r u p t i n g capacity.
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-step-up transformer from
13.8
kV to138
kV served from the.8
kV generator swi tshgear by 3000A nonsegregated enclosed s duct and connected on the 1 ine sfde to the138
kV switch-i
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yard ring bus.d) el
Three
138
kV oil circuit breakers in a ring bus arrangement.A
13.8
kV to4.16
kV
transformer and associated draw-out motorstarters to serve two I000 H.
P.
hot well pumps and space forV bus tie circuit breaker.
0 volt transformer and associated swi tchgear rbine-generator auxiliaries, cooling tower fans
lding service loads, including space for a future
480
V bus tie circuit breaker.An
auxiliary diesel generator rated 200 kW at 0.8 powe'r factor to serve emergency lighting and other essential loads under emergency conditions.9)
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3.6.2
. Main Turbine GeneratorThe generator supplied with the steam turbine will be totally en- closed for recirculating hydrogen cooling with hydrogen-to-water heat exchangers and brushless excitation.
watts gross,
61.1
MVA continuous at 60 Hertz and13.8
kV.It will be rated
55
mega-. 3
Generator Swi tchgearThe generator switchgear will be rated
13.8
kV with 1000 MVA inter- rupting capacity and will be of the metal-clad, drawout type, for location Indoors, with a generator circuit breaker and two feeder circuit breakers to serve the4.16
kV and480
volt auxiliary trans-I '
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S '
formers.
3.6.4
Step-up TransformerThe ste transformer will be located outdoors in the
138
kV be oil-f i1
led rated 37.5/50/62.5MVA, OA/FA/FA,
VA,
OA/FA/FA, at65°C
rise, 13.8/138 kV, nsformer will be served from the 13.8 kVct. The trans- s. The transformer
1 ightning
tandard accessories for this class of transformer ipped with standard high voltage taps:
ormal, with a man
i
3-6-5
3.6.6
4
-Oil Circuit Breakers
-
138
KV
The three oil circuit breakers for the ring bus will be Fated
138
kV, 1200A, 5000MVA
interrupting capacity, and will each be provided with two gang-operated air disconnect switches for cir- cuit breaker isolation.Air Disconnect and Ground Switches
-
138
kVIn addition to the circuit breaker isolation air disconnect switches, each line will be provided with a gang-operated air disconnect
switch and ground switch, and a gang-operated air ground switch will be provided on the section o f the 138 kV ring bus which is connected to the step-up transformer. Air disconnect switches will be rated
138
kV, 1200A..
.
3-6.7
138
kV
Swl tchyard ArrangementThe ring bus arrangement of the
138
kV switchyard will facilitgte the addition of a fourth oil circuit breaker in the ring bus in the future when the second turbine generator and step-up transformer are instal led.3.6.8
4.16
kV Transformer and Swi tchgearI
The
4.16
kV transformer and associated swi tchgear wi 1 1 be locatedindoors.
OA/FA,
at55°C
rise and 2800/3500 kVA, OA/FA, at 65°C rise, 13.8/4.16 kV, 3-phase, 60 Hertz.the metal-clad drawout type and will include a drawout motor starter to serve each o f the 1000 H.
P.
hot well pumps and space for a future4.16
kV bus tie circuit breaker.480
Volt Transformer and Swi tchgearThe 480 volt transformer and associated switchgear will be located indoors. The transformer will be silicon-filled rated 2500/3125 kVA, OA/FA, at
55°C
rise and 2800/3500 kVA,OA/FA,
at 65°C rise,13.8
kV/The transformer wi 1 1 be si 1 icon-f i 1 led rated 2500/3125 kVA, The
4.16
kV switchgear will be of3.609
rtz.
ype and wi,ll include an air circuit breaker to ree plant auxiliary building service motor con-
mps. symmetrical.
The 480 volt switchgear will be of the
trol centers
breaker.
Ai
uit breakers will have a minimum interruptingpace for a future 480 volt bus tie circuit
3.6.10 Auxf 1 iary Diesel Generator The auxiliary diesel ge failure of normal power
loads.
tor will provide emergency power upon emergency lighting and other essential
a
-factor,
480
volts, 3-phase, 60 Hertz, and will supply power to vice motor control center.t '
.h;
-3.6.11
Plant Start-up'3.6.12
h j .
The plant design is based on connection to two incoming lines on a
138
kV grid system.can be started by energizing the
13.8
kV switchgear bus from the line through the step-up transformer. This permits operation of all turbine/generator auxiliaries and the hot well pumps, and when the generator is u p to speed and voltage, it can be synchronizedWith both or either lirie in service, the plant
generator circuit breaker.
/generator to provide cold starting The added of the plant independent of the
138
kV Vines is 1,300 kW.expense of approximately $7.00 per kW based on 52,000 kW net, or $364,000, does not seem to be justified economical l y with power available from two incoming lines.
Corrosion Protection
There is an inherent hydrogen sulfide atmosphere in geothermal power plants which i s corrosive to copper.
given to the protection of all electrical facilities. 6
Special attention must be Vulnerable
opper connections and contacts are to be tinned or plated with a rotective coating which will protect them against the harmful ef-
rogen sulfide. Since hydrogen sulfide does not aluminum bus, tubing and cable will be used for
. application above ground throughout the outdoor substation.
For added protection from the hydrogen sulfide atmosphere, switch- gear, motor control centers and main control boards will be located
ln charcoal filtered clean air pressurized rooms to prevent adverse
i
effects on electrical contacts.3.7
c'
L
ii
Environmental Protection Considerations
Information available to date, indicates that the noncondensable gas content of the flash steam has a low content of hydrogen sul- f4de.
lfti,es for hydrogen sulfide abatement. tndicat
to requ
ments, the following plant design changes and equipment additions would be required:
On
this basis, plant design and costs include minimum faci- Should further Information gen sulfide content increasing to values high enough or abatement facilities based on air quality require-L
a) Change main turbine condenser design from direct contact to surface type.
.
W
L.
- *
b) Change intercondenser design from direct contact to surface type. lntercondenser condensate to be separately collected and transferred to the'sulfur recovery system.
Add a Stretford type sulfer recovery unit to treat the exhaust gas from the turbine condenser vacuum system and the gas cool- ing and jet condensate.
c)
Drawing A-02-102, included et the end of this section, indicates the sulfur recovery equipment required by the installation of the "Stretford Process" noncondensable gas purification system. The increased cost for surface type heat exchangers for main steam condensing, gas cooling and intercondenser above that for a direct contact system is as follows:
Surface Condenser Installed Cost $ 800,000
Stretford Untt Installed Cost
(Including Paid Up Royalttes) $2,000,000 H2S Abatement Total Estimated
. .
- *
trol is supplemented by a bypass valve to return a portion of the discharge water from the hot well pump to the main condenser. bypass valve operates during conditlons of extreme low level in the condenser such as during plant start up.
The
I +
b
3.8.2.3 Condenser Pressure Control .
The pressure in the main condenser is regulated by a valve which controls the flow of cooling water to the sprays in the main con-
L
1
i:
L
Anti-Surge Control
Control is provided to admit ambient air to the suction side of duced load operation.
Lube Oil Warm Up System
Control i s provided to turn off the cooling water to the lube o i l heat exchanger to provide a fast warm u p of lube oil after a cold start.
.the noncondensable gas ejectors to prevent surging during re-
. .
1;
3.8.2.53.8.2.6 Compressed Air System
Compressed air is provided by two compressors.
pressors normally supplies instrument and control air and one compressor normally supplies utility air to the station.
One of the com-
The control air system.draws air from the charcoal filtered air
supply to the air conditioning system. provide air with a
-45°C
dewpoint.through a filter-regulator at each point of use.
In the event of the failure of the control air compressor, manual
valves are provided so that air from the utility air compressor may be introduced to the control air system ahead o f the dryers.
A dryer is provided to Instrument air is provided
~
Y I
fire pump sys pressure switc
s maintalned by a jockey pump
In the event the pressure con- inues to drop with the jockey pump running, a second contact of the pressure switch will start the main fire pump and open the automatic discharge valve.
operate a third pressure switch contact to start the No. 2 main fire pump and open its dfscharge valve. As the pressure In the system i s restored, the pumps will be stopped in the reverse order.
I '
u .
A continued drop in pressure will
.
3.8,3
3.8.3.1
3.8.3.23.8.3.3
'3,8.3.4
3.8.3.5
3.8.3.6
3.8.3.7
3.8.3.8
3.8.3.9
3.8.3.10
3.8.3.11
. . 4 -AlarmsAlarms are provided to the control room annunciator to alert the operator to imminent problems, The most important of these in- cl ude:
Main condenser low level Main condenser high pressure Main condenser low pressure
lntercondenser high pressure rcondenser high level Low f I re water pressure
Lube oil centrifuge breakover Low control air pressure Hotwell pump low flow alarm
erflow S u m p Level Control
oat switch i s provided in the sump of the cool- p the excess condensate to the blowdown area.
Air Compressor Cooling System Surge Tank
1-
I
t
REVlj
DATE R E V I S I O N
DETAtLS
ENG. APPR.UTAH
POWER & LIGHT 5 5 M W GEOTHERMAL PROJECT
I
JOB NO. S 74002-02 REV
Rogers
POWER -SINGLEA-
E DIAGRAM
.A-08-101-
A
P A G E - 3 - 2 1 __
. .
d
_ -
. .
id 4.0 GEOTHERMAL
POWER
PLANT COST ESTIMATEThe cost estimate is based upon the criteria, features and ratings of the equipment in Section
3.
of the cost estimate are discussed in this section.
The cost estimate was developed using the Federal Power Commission
(FPC)
"Electric Plant Accountsii with the Utah Power and Light ap- plicable Emery No. 1 sub-account numbering and descriptions. The geothermal plant cost estimate is presented in Section4.4
in accordancewith
the above accounts.The site and architectural features
L
1
L
4.1
Building 1 ,L
lkd. This section describes the power plant building aspects of the project with particular emphasis on the size and relationship parameters needed to prepare the conceptual cost estimate.
4.1.1
Power Plant BuildingL
The cost estimate for the proposed building represents a designof the following components:
A power plant building to house one 52 MW unit, with appropriate administration and ancillary services to effect a complete self-
I contained operation. The degree of administrative and ancillary
services included in the initial phase will be sufficient to serve a future second 52 MW unit.
The initial building, 158 feet X
78
feet, will consist of six bays at 22 feet,8
inches each for a total dimension of136
feet in the power plant proper, with a n additional bay of 22 feet,
8
inches to accommodate administrative and ancillary services, for an overall length of158
feet., the power plant will be approximately
75
feet above the groundfloor.
The power plant will have three (3) floors, namely, ground floor,
* mezzanine f-loor, and operating floor, The vertical heights be-
tween the respective floors will be approximately
14
feet-
0 The administrative and ancillary service areas comprising three(3)
floors in a lower level connected structure will contain the following:b
1?
Eave helght in , Iii
b
inches.4.1.1.3
Change and Locker Room4.1.1.4
Electrical Shop4.1.1.5
Instrument ShopL
L
il
4.1.1.6
-Chemical Laboratory4.1.1.7
General Office, including Mechanicaland Electrical Supervisors
Machine Shop with crane and parts
(will
occupy a n area in the powert
4.1.1.8
storage,
plant, ground floor 1 eve1 )
L
i
i 4.2 400 sq. ft. 520 sq. ft. 500 sq. ft. 1,500 sq. ft.A 50-ton'rfidge crane, operable throughout the power plant, wi 1 1 be mounted approximately
35
feet above the operating floor level. NechanicalThe estimate was prepared on the basis of construction man-hours, and equipment and material estimated costs.
h
4.2.1 The basis of the cost estimate for mechanical equipment and materials comes from two sources.
a) Prices quoted by manufacturers to a written summary
Id
Y specification.
b) Prices established by current or previous projects of the
lb
same nature and size.
4.2.2 The mechanical equipment duties shown on the Process Flow diagram
8-02-101, Rev. A, are the basis for the cost estimate. The equip-
ment items for which quotations were obtained are as follows: 1) Turbine Generator Package
3) Hot Well Pumps
4)
Cool ing Tower5)
Main Bridge CraneThe installation manhours are based on a combination of (a)
previous actual manhours for this type o f project (b) Richardson's Estimating Data Book information and (c) in-house experience
in estimating manhours
in
similar type installations.~ 2) Condensers
iu
4.2.3b
t4*3
.
Flectrical , -*4.3.1
Electrical Equipment RatingsL
4-2
4.3.1
Electrical Equipment Ratingsi
I
4
-The Power Single Line Drawing A-08-101, Rev. A, shows the major electrical equipment elements and ratings.
based on the single line equipment and the electrical design
Electrical Equipment and Material Costs
Electrical equipment + criteria in Section
3.5.
4.3.21
I IThe electrical equipment and material costs in the estimate are cur- rent, June
1977.
-
L
4.3.3
Electrical Constructlon Man-hoursThe electrical construction man-hours in the construction cost esti- mate are based, in general, on Richardson Engineering Services, Inc.
-
"General Construction Estimating Standards-
Mechanical and Electrical"-
1976-77
Edition.lJ
1
t
ii
Labor man-hours not included in the above Estimating Standards are based on man-hours for similar work from experience on previous power plant installations.
4.4
Cost Estimate By AccountsThe geothermal power plant cost estimate is presented by Utah Power and Light's accounts and subaccounts. In preparing the estimate, a
major factor in its presentation was keeping it similar in format to
other
UP &
L power plant projects for ease in comparing costs.The summary cost estimate for the 55 MU gross geothermal power plant is presented in Table
4-1
in this Section.table is a detailed listing by Utah Power and Light accounts and subaccounts of the geothermal p\ant cost estimate details.
All
equipment and material purchases for the project are under Mate- r i a l and Equipment. The man-ho'urs are the estimated construction man-hours required. The labor rates used are those given i n theUP &
L
January1977
report on Emery No. 1 costs escalated to June1977.
at the middle of a 40 month construction period per recommendation o f the
UP &
L
engineering department. the middle of construction was taken as October1976
and therefore7
months of escalation(0.05264 at
8%
labor per year Utah Power and Light figure) i s ap- plied to the Emery rates to get those used in the geothermal esti-The geothermal power plant total construction cost including substa- tlon i s estimated to be $23,640,400 or
$455
per net kilowatt.L -
Succeeding the summary
These construction labor rates are assumed to be the average
r
d
mate, Table4.1.
' >,
rd
4.5 Engineering-Construction Schedule
The engineering and construction schedule is graphically represented by Drawing E-07-101, Rev. A.
experience by Rogers in implementing geothermal power plant design, procurement of a1 1 major equipment, and construction management o f
the plant.
This schedule i s the resul-; o f past
i i -
i;
i
ii
C '4.6
_ cThe schedule presumes the resource is sufficiently defined to be able to proceed with the plant design based on the resource characteristics and well locations. This schedule includes an allowance for bids for all major equipment to be requested and evaluated according to detail specifications. The construction
i s separated into mjor areas: site, civil/structural, mechani- cal, etc. to show the allowed times and major interrelation- ships. The longest delivery item, the Turbine-Generator package, Is the item which governs delivery and construction schedules. Delivery to the site i s quoted by manufacturer to be 20 months. With delivery time of the turbine-generator package being 20
months, the shortest design and construction schedule achievable Is
34
months. This schedule i s based upon the increased time of delivery schedules recently proposed by manufacturers of turbine- genera tor packages.The engineering includes all design engineering of construction drawings inside the power plant boundary fence, procurement of all equipment and major construction contracts, and on-site super- vision by engineers as the construction progresses.
tion of the manufacturers' and construction personnel is maintained by the design engineering group.
Permits for building the power plant or acquirlng permits for site construction and transmission line rights-of-way have not been in- cluded in the schedule. The schedule represents only engineering, procurement and construction since the Stearns-Roger construction schedule, as provided by Utah Power and Light Company for the 400 MW coal fired plant, does not provide for acquisition of plant permits or transmission line rights-of-way. A comparison of the geothermal schedule with a coal plant schedule is included in Section
6.3.
Estimated Cash Flow
Close coordina-
An
estimated cash flow for the engineering and construction period, taken as 34 months, has been prepared at the request of UP & L (seePCN
No. 21 of July15,
1977),
and i s shown in Table 4-2. Back up information may be found in Appendix D.‘.TABLE
4-1
29,800 4,300 SUMMARY
55 MW [GROSS) GEOTHERMAL POWER PLANT
COST ESTIMATE JUNE
1977
. Mater I a 1 s . . andI‘
u
1.
AccountNumber Description Equ i pmen t Labor Cost
31
1 Structures and Improvements $. 1,186,000 $ 597,4001:
, 312 Boiler [Steam Piping Only) 171,000 92,400-
314
Turbogenera tors.7,85O,OOO
1,091,900315
Accessory Electrical Equipment 740,000 198,900( 1
316
. Miscellaneous Power Plant353
~ C b s ta t ion Equ i pmen t1;
443,000 258,500 ,738,000 255,200-
-
-
Refund Taxes t Sub Totals $1 1,128,000 $2,493,400 Man-hoursI
12,700 17,600 9,900147
,
500 31Q Land $ 8,000399
Contractor Overhead andProfit 2,100,OQO
Plant Instal led $15,729,400
399
UP
dL
Charges.
475,000399
Engineering 2,000,000L
$ 1
1w
399
lnterest During Construction 2,352,500Sub Total $20,556,900
L
Con t i ng ency3
,
083,5OO\iI ,
TOTAL
CONSTRUCTION COST $23,640,400P ’
k *
-
Power Plant Construction CostL
C$/Net kW1 $455
4 ’
4-5
i
si
. .
1 4
-TABLE 4-1 [Cont'd)
55
MW (GROSS) GEOTHERMAL POWER PLANTCOST ESTIMATE
JUNE 1977
L
Account
Number D e s c r i p t i o n Man- hou r s
IJ
310 LAND AND LAND RIGHTS
-
! 310.1
31 0.2 Land and Easements
Wa t e r R i g h t s
I;
I
SUB TOTAL DIRECTw
31 1 STRUCTURES AND IMPROVEMENTSI 311.1 Improvements t o S i t e
-
hl 311.12 Plant Si%e
5
,
79931 1
.
14 Sewage Treatment Faci 1 i t i e s 438311.15 Domestic Water System 266
31 1.3 Power B u i l d i n g
-
31 1.31 Substructure 8,092
311.32 Superstructures 12,190
311.33 B u i l d i n g Services 2,700
311.51 Fuel O i l Tanks (Including
Foundat ions) 250
311.52 Fuel O i l P i p i n g (Yard Only
-
B u i l d i n g 312.191) , 61 311.7 Administration B u i l d i n g and Lr, id
311.5 Fuel O i l System-
ibi
M a t e r i a l & Labor Equipment Dollars-
216,430-
8,732-
22,
823 11 1,057 726,805 86,
340-
-
186,058 5,552 3,405 90,120 263,
404 42,
746-
-
10,000 4,916 3,
493 1,199 -Main Warehouse and Shop Included i n Account 311.3
311.8 Other Structures None
1oJ
Sub T o t a l 29,796 1,185,680 597,400 Use As 29,800 1,186,000 597,400 . .L
7312 BOILER PLANT EQUIPMENT
312*5 B o i l e r P l a n t P i p i n g
G .
f 32,540
312.51 Steam Piping 2,349 . 85,374
312.56 Miscel laneous Process Piping 250 3
,
480 3,684i I n s u l a t i o n Here) 1,008 53
,
060 46,
624(Material Only) 646 28,530 '9,552
I 92,400
312.57
312.59 P i p i n g & Valve Suspense
. .
..
e c
Account Material & Labor
Man-hours Equipment Dollars Number Descri pt ion
31
4
TURBO-GENERATOR
UI4IT
314.1
Turbine-
Generator314.11
Turbine Pedestal 314.12 Turbine314.13
Generator 314.14 Turnincr Gear8,671
125,14591,457
17,0004
,
479,000 290,7921
Included in Account 314.121
314.
IS
Governing Control Sys-em)314.16
Control and Stop Valve )314.17
Gland Seal and Piping1
314.18
Supervisory Instrumenta-)tlon (Local Front
1
Standard)
1
314.19
(Lump All Process Instru-314.2 Mlscel laneous Turbine- Included in Account 314.12
mentat ion Here) 4,800 154,500 82,106 Generator Equipment
{Supplied by Turbine- Genera tor Package)
314.3
Condenser and Auxll i-aries
314.31
Main Condenser CSur-face Type Including
1 n tercondensers) 11,000 gO0,OOO 162,686
314.-33
Ejectors Included in Acct.314.31
314.34
Condensate PumpsCSurface Type Cond) 2,300 500,000
34,016
314.36
Circulating Water Pipe(Within Bui lding) 4,706
146,811
69,600314.4
Coot ing Tower andEqu I pmen t
314.41
Cooling Tower Basin andFoundations 2,355 32,434 38,425
314.42 Cooling Tower 7,000
1
,000,000 98,222314.43
Circulating Water Pump .St ruct ure NONE
314.45
Circulating Water Piping(!Outside Building)
7,384
261,114 109,5553i4.46
Water Treating System(For Circulating Water) NONE
314.47
Cathodic Protection Included in Acct. No.314.45
{C. W. Piping)
314.6
Lube Oil System{Including a1 1 equipment which is not furnished as
an integral part
of other equipment
314.35
Circulating Water Pumps185
30,215 2,7374-7
*t
- c . .
i
%'
Account Material E LaborNumber Description Man- hours Equipment Dollars
Equ i pmen t
61
4
. 56,790 9,0485,841
63,321 86,079H2 and C02 System
(On
1 y equ i pmen twhich i s not fur- nished as an integ- ral part of other
equ i pmen t) 730 81,200 10,758
314.9
Auxlliary Generator314.91
Diesel Engine DrivenGenera tor
346
20,6305,463
314.61
Tanks, Pumps and314.62 Lube Oil Piping
.
L
c
L
. 314.7
/ I - -f lu
Sub Total 73,190 7,851,160 1,091,000 UseAs
73,200 7,850,000 1,091,000 r '315
. ACCESSORY ELECTRICAL EQUIPMENTb
315.1
Main Power ControlEquipment
(13.8
kV)' I
i.
315.11
Cubicles 240 .127,3973
,
790u
315.14
Load Frequency Control Included in Account315.41
315.15
315.16
Cooling Tower Control315.2 Start-up Power
13,800 Volt Bus Duct and
u
Termi na1
s 180 58,812 2,8421 Equ i pmen t
315.22 Start-up Swi tchgear 30
3,576
.474
li
- 1 r
315.3
Other Station ServiceControl Equipment
-
d
4160 Voltd
and Receptacles315.31
Cubicles 250 40,808 4,158315.32 Local Control Stations Included in Account 315.42
315.35
4160 Volt Bus Duct315.4
Other Station Service315.41
Electrical Control Board315.42 Local Control Stations
1
315.34
4160 Vo1 t Transformers160
35
,
878
2,526' (1200
A)
806,969
1,263J,
1 Control
J & Supervisory Control 1,200
67,417
18,063and Receptacles 470 10,000 7,075
d
315.43
Motor Control Centers 200 68,000 3,011I