BP Letterhead]
Exhibit 10(s)
[BP Letterhead]
September 8, 2003
PCS Nitrogen Ohio, L.P.
Dear Xxx:
This letter amends the Manufacturing Support Agreement (“Support Agreement”) and the Operating Agreement (“Operating Agreement”) both between BP Chemicals Inc. (“BP”) and PCS Nitrogen Ohio, L.P., formerly Arcadian Ohio, L.P., (“PCS”), dated May 11, 1993 and each as previously amended. BP understands that both parties desire to modify the cost of Steam set forth in those Agreements, including the Boiler Feed Water component of the cost of Steam. Consequently, BP proposes that the two Agreements be modified, retroactive back to January 1, 2003, as follows:
| 1. | In the Support Agreement, the “Steam” portion of Exhibit D will be deleted in its entirety and replaced with “Exhibit D, 2003 Steam Calculation” attached hereto. |
| 2. | In the Operating Agreement, the handwritten page setting forth the calculation for Steam in Exhibit H will be deleted in its entirety and replaced with “Exhibit D, 2003 Steam” attached hereto. |
| 3. | Notwithstanding anything to the contrary in the Support Agreement, the Operating Agreement, or this Amendment, the parties agree that PCS will take as much of its requirements of 650 PSIG Steam from BP as PCS can consume at its Lima Nitrogen plant unless PCS’s cost of generating its own steam is less than the cost of Steam that BP provides to PCS pursuant to the Agreements. The parties acknowledge that, with the current Steam pipeline, BP can deliver up to approximately 80,000 pounds/hour of 650 PSIG superheated Steam to PCS. If, pursuant to the provisions of this paragraph, PCS generates its own steam rather than use the absorber offgas incinerator supplied (“AOGI”) Steam, PCS will (a) provide BP with boiler feed water for the portion of the AOGI Steam that PCS did not use because it generated its own steam free of charge to BP (and it will not be included when calculating the Steam cost in accordance with Exhibit D, 2003 Steam); and (b) provide BP with boiler feed water for the rest of the AOGI Steam and such will be included when calculating the Steam cost in accordance with Exhibit D, 2003 Steam. |
| 4. | Notwithstanding anything to the contrary in the Support Agreement, the Operating Agreement, or this Amendment, the parties intent is to work together, in good faith, to try to optimize the Steam usage across BP’s and PCS’s plants at the Lima site, realizing that PCS, pursuant to the Support Agreement, has the first right to take the Steam produced and that BP may choose to use the Steam internally for its benefit. Therefore, the parties agree that if, during any given period, BP elects not to provide some portion of the produced Steam to PCS, for any reason, BP can require PCS to continue to supply Boiler Feed Water to BP during such period, up to the boiler feed water production capability of PCS. If such occurs, BP must pay PCS for such Boiler Feed Water during that period pursuant to the cost calculations for Boiler Feed Water that are a part of Exhibit D, 2003 Steam attached hereto. |
2
All other terms and conditions of the Support Agreement and the Operating Agreement would remain the same.
If you are in agreement, please have an authorized representative sign below and return one fully executed original to BP.
BP CHEMICALS INC.
| By: | /s/ XXXXXXX X. XXXXXXX |
ACCEPTED AND AGREED:
| By: | /s/ X.X. XXXXX |
v
“EXHIBIT D, 2003 STEAM”
Addendum to the BP/PCS Operating Agreement for Calculating BP Export Steam
| Inputs: | ||||||||||
| Last Calculated On: 8-Jan-03 | ||||||||||
|
Items for BP to Enter:
|
||||||||||
|
Misc. Utility Costs
|
||||||||||
|
Electricity
|
33.3998 | $/MWh | Formula contained in Original PCS Operating Agreement — Conversion Cost Exhibit H 3400 | |||||||
|
Natural Gas
|
4.46 | $/MMBtu | PCS Actual Monthly cost to BP | |||||||
|
Refinery 125# Steam
|
4.24 | $/MMBtu | Premcor Actual Monthly cost to XX | |||||||
|
Xxxx Water to Zeolites
|
1.564 | $/MWh | Formula contained in Original PCS Operating Agreement — Conversion Cost Exhibit H 3500 | |||||||
Items for PCS to Enter:
Estimated PCS BFW Cost 18.4079 $/MGAL
|
*Misc. Costs Specific to PCS BFW
|
*To be calculated in the same manner PCS calculated such items prior to the date of this Amendment and using only those costs specifically and directly related to PCS generating Boiler Feed Water |
|
*Denim Water
|
3.1048 | $ | /MGAL | ||||||
|
*Xxxx HTP 73611
|
0.1281 | $ | /MGAL | ||||||
|
*Xxxx ADJ560
|
0.1002 | $ | /MGAL | ||||||
|
*Xxxx 778P
|
0 | $ | /MGAL | ||||||
|
*Fixed Cost
|
3.8304 | $ | /MGAL | ||||||
| 7.1635 | $ | /MGAL |
PCS/BP Steam Transfers
|
AOGI Steam to PCS
|
614950 | Mlbs | FQI-33228 | 75.00% | ||||||
|
Reactor Steam to PCS
|
204950 | Mlbs | FQI-50037 | 25.00% | ||||||
|
Steam From PCS to BP
|
0 | Mlbs | FQI-50036 | (steam to BP to be billed separately) |
PCS Steam Usages
|
Boiler Steam
|
473177 | tons | 40.74 | % | |||||||||||||
|
Steam Import from BP
|
409950 | tons | 35.29 | % | —> A | ||||||||||||
|
Ammonia Steam
|
135470 | tons | 11.66 | % | |||||||||||||
|
Nitric Acid Steam
|
142922 | tons | 12.30 | % | |||||||||||||
| 1161519 | tons | ||||||||||||||||
PCS/BP BFW Transfers
|
BFW to AOGI
|
167404 | MGALS | FQI-33281 | —> C |
vi
Outputs
|
Calculated BP Steam to PCS Price
|
14.1315 $/ton | —> B “See Page 2” | ||
|
Cost for Steam to be paid to BP
|
$5,793,200 | —> A x B | ||
| Takes the difference between these two to determine the net payout | ||||
|
Calculated PCS BFW to BP Price:
|
19.4362 $/MGAL | —> D “See Page 3” | ||
|
Cost to BFW to be paid to PCS:
|
$3,253,703 | —> C x D | ||
|
Net Cost for PCS to pay BP:
|
$2,539,497 |
vii
Addendum to the BP/PCS Operating Agreement for Calculating BP Export Steam Price to PCS & PCS BFW Price to BP
| Example — Based on 2003 Plan Values | Revised: 3-Apr-03 |
Heat Required to Make AOGI Steam
BFW Make-up from PCS Demin Plant to AOGI Economizer
|
Inlet Pressure:
|
1025 | psig | ||||||||||
|
Inlet Temperature:
|
283 | deg F | ||||||||||
|
Enthalpy @ Inlet Cond:
|
254.29 | Btu/lb | ||||||||||
|
Steam from AOGI Superheater
|
||||||||||||
|
Outlet Pressure:
|
731 | psig | ||||||||||
|
Outlet Temperature:
|
701 | deg F | ||||||||||
|
Enthalpy @ Outlet Cond:
|
1342.55 | Btu/lb | ||||||||||
|
Change in Enthalpy:
|
1088.21 | Btu/lb | —> B17 | |||||||||
|
Heat Required to Make Reactor Steam
|
||||||||||||
|
Steam from Reactors
|
||||||||||||
|
Outlet Pressure:
|
600 | psig | ||||||||||
|
Outlet Temperature:
|
489 | deg F | ||||||||||
|
Enthalpy @ Outlet Cond:
|
1203.3 | Btu/lb | —> B25 | |||||||||
| Cost to Make AOGI Steam (based on Nat Gas Fuel Value): | Cost to Steam | Comments | ||||||||||||
|
SH Stm Natural Gas Cost:
|
$ | 4.46 $/MMBtu | $ | 4.8534 | $ | /Mlb | Uses BTU value reqmt for AOGI steam from above | |||||||
|
BFW from PCS Cost:
|
$ | 19.4362 $/MGAL | $ | 2.6101 | $ | /Mlb | includes a 12% blowdown based on yearly averages | |||||||
| $ | 7.4636 | $ | /Mlb | |||||||||||
| $ | 14.9271 | / | ton | |||||||||||
viii
| Cost to Make Reactor Steam (based on Nat Gas Fuel Value): | Cost to Steam | |||||||||||||||||
|
Sat Stm Natural Gas Cost
|
$ | 4.46 | $/MMBtu | $ | 5.3667 | $/Mlb | Uses BTU value reqmt for Reactor steam from above | |||||||||||
|
City Water to Zeolites Cost:
|
$ | 1.56 | $/MGAL | $ | 0.2157 | $/Mlb | Includes bed regen water usage: 15% B/D | |||||||||||
|
50# Stm to DA
|
$ | 4.24 | $/Mlb | $ | 0.1632 | $/Mlb | Based on yearly averages | |||||||||||
|
Chemicals Cost:
|
$ | 0.0600 | $/Mlb | Based on yearly averages | ||||||||||||||
|
Electricity Cost:
|
$ | 0.03 | $/kWh | $ | 0.0665 | $/Mlb | Assumes (1) 500 hp Make-up Water pump and (2) 125 hp/each Circulating Water pumps | |||||||||||
| $ | 5.8721 | $/Mlb | ||||||||||||||||
| $ | 11.7442 | /ton | ||||||||||||||||
| AOGI Steam to PCS (add Daily Values for the Month): | FQI-33228 | 614950 | M lb | 75.00% | ||||||||||||||
| Reactor Steam to PCS (add Daily Values for the Month): | FQI-50037 | 204950 | M lb | 25.00% | ||||||||||||||
| Total Steam Export to PCS: | 819900 | M lb | ||||||||||||||||
| Average Steam Cost to PCS: —> B | $ | 14.1315 | $/ton | Weighted average | ||||||||||||||
| $ | 7.0657 | $/Mlb |
— for BP accounting purposes (PCS uses $/ton basis) |
|||||||||||||||
Formulas
Cost to Make AOGI Steam (based on Nat Gas Fuel Value):
SH Stm Natural Gas Cost = [Natural Gas Cost $/MMBtu] x [BTU rqmt for AOGI steam from above = B17] x [1000 lb/Mlb] / [1000000 Btu/MMBtu]
BFW from PCS Cost = [PCS BFW Cost $/Mgal] x [12% blowdown adjustment = 1.12] / [Density of water = 8.34 lb/gal]
Cost to Make Reactor Steam (based on Nat Gas Fuel Value):
Sat Stm Natural Gas Cost = [Natural Gas Cost $/MMBtu] x [BTU rqmt for Rxtr steam from above = B25] x [1000 lb/Mlb] / [1000000 Btu/MMBtu]
City Water to Zeolites Cost = [City Water Cost $/Mgal] x [15% softener regen blowdown adjustment = 1.15] / [Density of water = 8.34 lb/gal]
50# Stm to DA = [Refinery 50# Steam Cost $/Mlb] x [50# Steam Required to Dearate 1 lb of BFW used to Make Reactor Steam = 0.0385 lb]
Chemicals Cost = [Typical Yearly Cost of Chemicals to Treat BFW and Reactor Steam $] / [Typical Yearly Production of Reactor Steam Mlb]
Electricity Cost = [Electricity Cost $/kWH] x [Total Horsepower of the three pumps = 750 hp] / [Horsepower to Watt conversion = 0.00134 hp/W] x [1000 W/Kw] x [Average Reactor Steam Production = 281 Mlb/hr]
ix
Addendum to the BP/PCS Operating Agreement for Calculating BP Export Steam
| Iterative Calculation | 3-Apr-03 |
“The D” term is the calculated PCS BFW to BP Price determined through an Iterative Calculation to remove the spiraling effect of any increases or decreases to any variable used in both the Steam and BFW price calculations. An example of this calculation is set forth on this page. “BFW Cost ($/Mgal) column will be the “D” term used in the calculation set forth on page 1 of this Exhibit”
| Nitric Acid | ||||||||||||||||||||||||||||||||||||||||||||||||||
| BFW Cost | NG Cost to | AOGI | BFR Contribution | Credit — | ||||||||||||||||||||||||||||||||||||||||||||||
| Natural Gas | to AOGI | AOGI | Steam | AN to PCS | to PCS Steam | adjusted | Ammonia | Import | Steam | |||||||||||||||||||||||||||||||||||||||||
| Cost | BFW Cost | Steam | Steam | Price | Export Avg. | Variable Cost | for a H | Boiler | Credit | from BP | Average Price | |||||||||||||||||||||||||||||||||||||||
| Iteration | ($/MMBtu) | ($/MGAL) | ($/ton) | ($/ton) | ($/ton) | Price ($/ton) | $/ton | ($/ton) | ($/ton) | ($/ton) | ($/ton) | ($/ton) | ||||||||||||||||||||||||||||||||||||||
| 0 | $ | 4.46 | $ | 18.4079 | $ | 4.9441 | $ | 9.7068 | $ | 14.6509 | $ | 13.9243 | $ | 4.3733 | $ | 1.4003 | $ | 6.9758 | $ | 1.9971 | $ | 4.9145 | $ | 15.2874 | ||||||||||||||||||||||||||
| 1 | $ | 4.46 | $ | 19.2399 | $ | 5.1676 | $ | 9.7068 | $ | 14.8744 | $ | 14.0919 | $ | 4.6229 | $ | 1.4207 | $ | 7.0773 | $ | 2.0262 | $ | 4.9737 | $ | 15.4978 | ||||||||||||||||||||||||||
| 2 | $ | 4.46 | $ | 19.3988 | $ | 5.2102 | $ | 9.7068 | $ | 14.9171 | $ | 14.1239 | $ | 4.6705 | $ | 1.4246 | $ | 7.0967 | $ | 2.0318 | $ | 4.9849 | $ | 15.5380 | ||||||||||||||||||||||||||
| 3 | $ | 4.46 | $ | 19.4291 | $ | 5.2184 | $ | 9.7068 | $ | 14.9252 | $ | 14.1300 | $ | 4.6796 | $ | 1.4253 | $ | 7.1004 | $ | 2.0328 | $ | 4.9871 | $ | 15.5458 | ||||||||||||||||||||||||||
| 4 | $ | 4.46 | $ | 19.4349 | $ | 5.2199 | $ | 9.7068 | $ | 14.9267 | $ | 14.1312 | $ | 4.6813 | $ | 1.4254 | $ | 7.1011 | $ | 2.0330 | $ | 4.9875 | $ | 15.5471 | ||||||||||||||||||||||||||
| 5 | $ | 4.46 | $ | 19.4360 | $ | 5.2202 | $ | 9.7068 | $ | 14.9270 | $ | 14.1314 | $ | 4.6817 | $ | 1.4255 | $ | 7.1012 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 6 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 7 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 8 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 9 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 10 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 11 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 12 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 13 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 14 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 15 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 16 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 17 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 18 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 19 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 20 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 21 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 22 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 23 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 24 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 25 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 26 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 27 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 28 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 29 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 30 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 31 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 32 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 33 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 34 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 35 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 36 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 37 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 38 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 39 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 40 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 41 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 42 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 43 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 44 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 45 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 46 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 47 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 48 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 49 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
| 50 | $ | 4.46 | $ | 19.4362 | $ | 5.2203 | $ | 9.7068 | $ | 14.9271 | $ | 14.1315 | $ | 4.6817 | $ | 1.4255 | $ | 7.1013 | $ | 2.0331 | $ | 4.9876 | $ | 15.5474 | ||||||||||||||||||||||||||
x
