LIQUEFIED NATURAL GAS (LNG) BY Team supercooLNG Dhari Alotaibi Andrew Arambel Bhagya Gunatilleke Chris Robinson Sarah Scott.

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Presentation transcript:

LIQUEFIED NATURAL GAS (LNG) BY Team supercooLNG Dhari Alotaibi Andrew Arambel Bhagya Gunatilleke Chris Robinson Sarah Scott

Business Opportunity There is an excess of natural gas to be exported Large scale offshore plant located in the Gulf of Mexico Byproducts are ethane, propane, and butane

Plant Information Pipeline natural gas feed Feed contains 77 mol% methane Plant capacity: 531 MMSCF/day of natural gas Product capacity: 21.8 MMlb/day of LNG Operation: 344 operating days (8256 hr/year)

Overall Process

Pretreatment No dehydration unit Purchased commercially Offshore sulfur treatment unit

De-Methanizer Important characteristics: No condenser on de- methanizer since distillate is -120 F Liquid feed enters in top tray and acts as reflux stream

Important characteristics: Adiabatic expansion always for temperatures to reach -245 F without cooling. Heat integration minimizes the need for refrigeration. Nitrogen Rejection Unit

Important characteristics: Multiple compressors reduces required work in the system. Refrigeration

Important characteristics: Multiple heat exchangers will be incorporated into a cold box design

Fractionation

Economic Analysis 20 year plant life All costs of feed or product streams were analyzed using flow units of SCF/day or 1000 SCF/day (MSCF/D) MACRS 5 depreciation

Capital Costs Total fixed capital investment of plant: 2.83 MMM$ (85% of the total capital investment) o ISBL: 2.57 MMM$ o OSBL: MMM$ Working capital: MMM$ (15% of the total capital investment)

Revenue and Expenses Total cost of feed: MMM$/yr Total revenue from LNG: MMM$/yr Total revenue from byproducts: MMM$/yr Total variable and fixed costs: MMM$/yr Profit: 1.20 MMM$/yr

NPV Results NPV0: MMM$ NPV10: 3.69 MMM$ IRR: 21.7% Payback period: approximately 5.5 years

Sensitivity Analysis Profitable for all four cases Case 3 very close to MARR

Environmental Impact Wastewater will not be produced during operation Greenhouse gas emissions are low in comparison to a typical natural gas processing plant LNG is less hazardous to the environment where processing and transportation are concerned LNG is a less attractive alternative to natural gas where energy consumption is concerned

Safety LNG industry has strict requirements determined by federal and international agencies LNG as a product is much safer than natural gas in the gas phase Not an explosive substance by nature Not stored under pressure Tankers are designed to a high standard of safety General HAZOPS study for our plant was performed

Conclusion LNG product sold to the European market Process byproducts sold to the United States market Total Capital Investment: 3.33 MMM$ Profit: 1.20 MMM$/yr Payback Period: 5.5 years LNG is an efficient, economical, and safe way to process and sell natural gas

Thank you to our group mentors John Myers, David Bell, and Joseph Holles.

Plate-Fin Heat Exchanger Cold Box