Louisiana Land & Exploration Co. v. Commissioner

90 T.C. No. 38, 90 T.C. 630, 1988 U.S. Tax Ct. LEXIS 39, 100 Oil & Gas Rep. 610
CourtUnited States Tax Court
DecidedApril 7, 1988
DocketDocket Nos. 30292-85, 37799-85, 47753-86
StatusPublished
Cited by15 cases

This text of 90 T.C. No. 38 (Louisiana Land & Exploration Co. v. Commissioner) is published on Counsel Stack Legal Research, covering United States Tax Court primary law. Counsel Stack provides free access to over 12 million legal documents including statutes, case law, regulations, and constitutions.

Bluebook
Louisiana Land & Exploration Co. v. Commissioner, 90 T.C. No. 38, 90 T.C. 630, 1988 U.S. Tax Ct. LEXIS 39, 100 Oil & Gas Rep. 610 (tax 1988).

Opinion

WILLIAMS, Judge:

In these consolidated cases, the Commissioner determined deficiencies in petitioners’ Federal corporate income tax for the taxable years 1979, 1981, and 1982 as follows:

Docket No. Year Deficiency
30292-85 1979 $30,693,922
37799-85 1981 29,618,171
47753-86 1982 1,130,372

The sole issue remaining for our decision is whether petitioners are entitled to percentage depletion pursuant to section 6131 on income from sulphur chemically converted from hydrogen sulfide produced from an oil and gas well. Respondent has stipulated that if we find petitioners are entitled to percentage depletion deductions, they correctly computed the amount of the depletion deductions on their Federal income tax returns.

FINDINGS OF FACT

Petitioners, the Louisiana Land & Exploration Co. (LL&E) and Subsidiaries, are an affiliated group of corporations whose common parent is LL&E. LL&E is a Maryland corporation having its principal office at New Orleans, Louisiana. Petitioners are calendar year, accrual method taxpayers.

During the years in issue, petitioners were engaged primarily in exploration for and development, production, refining, and sale of crude oil and natural gas and exploration for, production and mining of other minerals such as sulphur, gold, silver, copper, and coal in the United States and several foreign countries. Petitioners owned a working or operating interest in leases of oil wells in the Jay-Little Escambia Creek Field (Jay Field) in Escambia County, Alabama, and Santa Rosa and Escambia Counties, Florida. Petitioners extracted four categories of products from the Jay Field wells: liquid hydrocarbons, gaseous hydrocarbons, nonhydrocarbon gases, and nonhydrocarbon liquids.2

Hydrocarbons are organic compounds containing only hydrogen and carbon and Eire most commonly used as fuels. The liquid hydroceirbon produced from the Jay Field wells is crude oil, which consists of hydrocarbon compounds that are in a liquid phase at ambient temperature and pressure. Crude oil is processed into various types of fuels and oils, including diesel fuel and lubricating oil. The gaseous hydrocarbons, or natural gases, exist in a gaseous state at ambient temperature and pressure and consist primarily of methane, ethane, propane, and butane.

The nonhydrocarbon gases extracted from the Jay Field wells are primarily hydrogen sulfide and carbon dioxide.The typical well stream in the Jay Field contains approximately 8.5 percent hydrogen sulfide and 2.2 percent carbon dioxide.

Brine water, water with a high mineral content, is the nonhydrocarbon liquid extracted from the Jay Field wells. The minerals in the water are not developed for commercial use, and the brine water is reinjected into the well reservoir to maintain pressure.

When brought to the surface, all of the items in the wells are physically mixed. The gaseous effluent, or raw outflow, from the Jay Field wells is referred to as a “sour gas” stream, meaning a stream consisting of both natural gas and hydrogen sulfide with more than one grain of hydrogen sulfide per 100 standard cubic feet of the gaseous mixture.

Hydrogen sulfide and carbon dioxide are contaminants of natural gas.3 Sour gas cannot be used as fuel; the hydrogen sulfide and carbon dioxide must first be removed. Hydrogen sulfide is a poisonous, highly corrosive gas which cannot be vented into the atmosphere in large quantities without serious deleterious effects. In addition, natural gas contaminated by hydrogen sulfide cannot be burned or transported through pipelines because its corrosive nature would damage the combustion equipment and the pipelines. Hydrogen sulfide, alone, or in combination with natural gas is also unsuitable for use as a fuel because the combustion of hydrogen sulfide produces sulphur dioxide, a toxic substance subject to control under Federal pollution standards. Sulphur dioxide is a gas with an objectionable odor and which can damage both animals and plants.

The well effluent from the Jay Field wells is treated in facilities adjacent to the wells. Hydrogen sulfide is not transported far from the well because of the hazards involved. The well effluent is initially treated in a separation system which uses gravity to separate the effluent into brine water, sour crude oil, and a sour gas stream containing natural gas, hydrogen sulfide, and carbon dioxide. The brine water is reinjected into the well.

The separated sour crude oil undergoes further treatment within the oil stabilization system, a pressurized vessel in which heat vaporizes and removes more of the dissolved sour gas (i.e., hydrogen sulfide, carbon dioxide, and natural gas). The oil stabilization system also reduces the vapor pressure of the crude oil to a low enough level that it can be stored and transported in atmospheric tanks and tank trucks. After processing, the crude oil is classified as sweet rather than sour oil.

The sour gas streams from the separation system and the oil stabilization system, containing both natural gas and hydrogen sulfide, are combined and further treated in the acid gas removal system. The acid gases (hydrogen sulfide and carbon dioxide) are separated from the natural gas through an absorption process. In a vessel called a contactor, an amine solution such as sulfinal is added to the sour gas. The amine solution absorbs the hydrogen sulfide and carbon dioxide and natural gas flow out of the top of the contactor. The separated natural gas is processed further in another contactor which removes water vapor from the gas stream. The natural gas is then transported through natural gas pipelines for use by petitioner or sale to Florida Gas Transmission Co. pursuant to a long-term gas purchase contract dated November 15, 1971.

The acid gas next is separated from the amine solution and passed into a multistage Claus sulphur recovery system, where hydrogen sulfide is converted into molten elemental sulphur by controlled combustion with air. The carbon dioxide is vented to the atmosphere. The Claus system chemically converts more than 96 percent of the hydrogen sulfide into elemental sulphur. The sulphur is then condensed and stored until sold. At all relevant times, petitioner sold the sulphur it produced to Freeport Minerals Co.

The diagram on the facing page summarizes the sour production processing system used at the Jay Field Wells.

The primary products from the Jay Field wells and processing facilities have been oil and natural gas. Sulphur has been recovered from hydrogen sulfide and sold as a byproduct of the processing facilities since the facilities were placed in operation.

The basic Claus sulphur recovery process was developed in England around 1890, but did not become economically feasible until modified by work in Germany in 1937. The first commercial plant in the United States to use the modified Claus process was placed in operation in 1944. Claus sulphur recovery plants, however, were not economically attractive investments until the value of sulphur began to rise significantly in the 1960’s.

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Bluebook (online)
90 T.C. No. 38, 90 T.C. 630, 1988 U.S. Tax Ct. LEXIS 39, 100 Oil & Gas Rep. 610, Counsel Stack Legal Research, https://law.counselstack.com/opinion/louisiana-land-exploration-co-v-commissioner-tax-1988.