Question
ConocoPhillipss (COP) Natural Gas and Gas Products Department (NG&GP) manages all of the companys activities relating to the gathering, purchasing, processing, and sale of natural
ConocoPhillipss (COP) Natural Gas and Gas Products Department (NG&GP) manages all of the companys activities relating to the gathering, purchasing, processing, and sale of natural gas and gas liquids. Chris Simpkins, a recent graduate, was recently hired as a financial analyst to support the NG&GP department. One of Chriss first assignments was to review the projections for a proposed gas purchase project that were made by one of the firms field engineers. The cash flow projections for the ten-year project are found in Exhibit P3-12.1 and are based on the following assumptions and projections:
The investment required for the project consists of two components: First, there is the cost to lay the natural gas pipeline of $1,200,000. The project is expected to have a ten-year life and is depreciated over seven years using a seven-year modified accelerated cost recovery system (MACRS).20 Second, the project will require a $145,000 increase in net working capital that is assumed to be recovered at the termination of the project.
20 Modified accelerated cost recovery system (MACRS) uses a shorter depreciable life for assets, thus giving businesses larger tax deductions and cash flows in the earlier years of the project life relative to those of straight-line depreciation.
The well is expected to produce 900,000 cubic feet (900 MCF) per day of natural gas during year 1 and then decline over the remaining nine-year period (365 operating days per year). The natural gas production is expected to decline at a rate of 20% per year after year 1.
In addition to the initial expenditures for the pipeline and additional working capital, two more sets of expenses will be incurred. First, a fee consisting of 50% of the wellhead natural gas market price must be paid to the producer. In other words, if the wellhead market price is $6.00 per MCF, 50% (or $3.00 per MCF) is paid to the producer. Second, gas processing and compression costs of $0.65 per MCF will be incurred.
There is no salvage value for the equipment at the end of the natural gas lease.
The natural gas price at the wellhead is currently $6.00 per MCF.
The cost of capital for this project is 15%.
Answer the following questions.
What are the NPV and IRR for the proposed project, based on the forecasts made above? Should Chris recommend that the project be undertaken? Explain your answer. What reservations, if any, should Chris have about recommending the project to his boss?
Perform a sensitivity analysis of the proposed project to determine the impact on NPV and IRR for each of the following scenarios:
Best case: a natural gas price of $8.00 and a year 1 production rate of 1,200 MCF per day that declines by 20% per year after that.
Most likely case: a natural gas price of $6.00 and a year 1 production rate of 900 MCF per day that declines by 20% per year after that.
Worst case: a natural gas price of $3.00 and a year 1 production rate of 700 MCF per day that declines by 20% per year after that.
Do breakeven sensitivity analysis to find each of the following:
Breakeven natural gas price for an NPV = 0
Breakeven natural gas volume in year 1 for an NPV = 0
Breakeven investment for an NPV = 0
Given the results of your risk analysis in parts b and c, would you recommend this project? Explain your answer.
Alternate View
Year | 0 | 1 | 2 | 3 |
---|---|---|---|---|
Investment | $ 1,200,000 | |||
Increase in NWC | 145,000 | |||
MACRS depreciation rate ?(7 years) | 0.1429 | 0.2449 | 0.1749 | |
Natural gas wellhead price ?(per MCF) | $ ???? 6.00 | $ ???? 6.00 | $ ????6.00 | |
Volume (MCF/day) | 900 | 720 | 576 | |
Days per year | 365 | |||
Fee to producer of natural gas (per MCF) | $ ???? 3.00 | $ ???? 3.00 | $ ????3.00 | |
Compression and processing? costs (per MCF) | 0.65 | 0.65 | 0.65 | |
Cash Flow Calculations | ||||
Natural gas wellhead price revenue | $ 1,971,000 | $ 1,576,800 | $1,261,400 | |
Lease fee expense | 985,500 | 788,400 | 630,720 | |
Compression and processing costs | 213,525 | 170,820 | 136,656 | |
Depreciation expenses | 171,480 | 293,880 | 209,880 | |
Net operating profit | 600,495 | 323,700 | 284,184 | |
Less taxes (40%) | (240,198) | (129,480) | (113,674) | |
Net operating profit after tax (NOPAT) | 360,297 | 194,220 | 170,510 | |
Plus depreciation | 171,480 | 293,880 | 209,880 | |
Return of net working capital | ||||
Project free cash flow | $(1,345,000) | $ 531,777 | $ 488,100 | $ 380,390 |
Alternate View
4 | 5 | 6 | 7 | 8 | 9 | 10 |
---|---|---|---|---|---|---|
0.1249 | 0.0893 | 0.0893 | 0.0893 | 0.0445 | ||
$ ????6.00 | $ 6.00 | $ 6.00 | $ 6.00 | $ 6.00 | $ 6.00 | $ 6.00 |
461 | 369 | 295 | 236 | 189 | 151 | 121 |
$ ????3.00 | $ 3.00 | $ 3.00 | $ 3.00 | $ 3.00 | $ 3.00 | $ 3.00 |
0.65 | 0.65 | 0.65 | 0.65 | 0.65 | 0.65 | 0.65 |
$1,009,152 | $807,322 | $645,857 | $516,686 | $413,349 | $330,679 | $264,543 |
504,576 | 403,661 | 322,929 | 258,343 | 206,674 | 165,339 | 132,272 |
109,325 | 87,460 | 69,968 | 55,974 | 44,779 | 35,824 | 28,659 |
149,880 | 107,160 | 107,160 | 107,160 | 53,400 | ||
245,371 | 209,041 | 145,801 | 95,209 | 108,495 | 129,516 | 103,613 |
(98,148) | (83,616) | (58,320) | (38,083) | (43,398) | (51,806) | (41,445) |
147,223 | 125,425 | 87,480 | 57,125 | 65,097 | 77,710 | 62,168 |
149,880 | 107,160 | 107,160 | 107,160 | 53,400 | ||
145,000 | ||||||
$ 297,103 | $232,585 | $194,640 | $164,285 | $118,497 | $ 77,710 | $207,168 |
Exhibit P3-12.1 Analysis of the ConocoPhillips Gas Purchase Project
ConocoPhillips Natural Gas Wellhead Project | |||||||||||
Given | |||||||||||
ConocoPhillips's Cost of Capital for project | |||||||||||
Project life | |||||||||||
Solution | |||||||||||
1. | Years | ||||||||||
0 | 1 | 2 | 3 | 4 | 5 | 6 | 7 | 8 | 9 | 10 | |
Investment | |||||||||||
Increase in NWC | |||||||||||
MACRS Depr Rate (7 year) | 0.1429 | 0.2449 | 0.1749 | 0.1249 | 0.0893 | 0.0893 | 0.0893 | 0.0445 | |||
Natural Gas Wellhead Price (per MCF) | |||||||||||
Volume (MCF/day) | |||||||||||
Days per year | |||||||||||
Fee to Producer of Natural Gas | |||||||||||
Compression & processing costs (per MCF) | |||||||||||
Cash Flow Calculations | |||||||||||
Natural Gas Wellhead Price Revenue | |||||||||||
Lease fee expense | |||||||||||
Compression & processing costs | |||||||||||
Depreciation expense | |||||||||||
Net operating Profit | |||||||||||
Less: Taxes (40%) | |||||||||||
Net operating profit after tax (NOPAT) | |||||||||||
Plus: Depreciation expense | |||||||||||
Return of net working capital | |||||||||||
Project Free Cash Flow | |||||||||||
NPV | |||||||||||
IRR | |||||||||||
2a-c. Scenario Summary | |||||||||||
Current Values | Best Case | Most Likely Case | Worst Case | ||||||||
Changing Cells | |||||||||||
NG Price | |||||||||||
Production Rate | |||||||||||
Result Cells | |||||||||||
NPV | |||||||||||
IRR | |||||||||||
Notes: Current Values column represents values of changing cells at time Scenario Summary Report was created. | |||||||||||
3. Breakeven Sensitivity Analsyis Students should use Goal Seek in Excel to answer this question. | |||||||||||
a. | |||||||||||
Breakeven nautral gas price for an NPV = 0 | |||||||||||
b. | |||||||||||
Breakeven natural gas volume in Year 1 for an NPV = 0 | |||||||||||
c. | |||||||||||
Breakeven investment for an NPV = 0 | |||||||||||
4. Analysis | |||||||||||
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