Oxford Paper Co. v. Commissioner

33 T.C. 943, 1960 U.S. Tax Ct. LEXIS 197
CourtUnited States Tax Court
DecidedFebruary 24, 1960
DocketDocket No. 63464
StatusPublished
Cited by4 cases

This text of 33 T.C. 943 (Oxford Paper 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
Oxford Paper Co. v. Commissioner, 33 T.C. 943, 1960 U.S. Tax Ct. LEXIS 197 (tax 1960).

Opinion

Train, Judge:

The respondent determined deficiencies in petitioner’s income and excess profits taxes for 1950 and 1951 in the respective amounts of $153,959.75 and $402,847.03.

The issue for decision is whether respondent erred in disallowing the claim for excess profits tax relief asserted by petitioner under section 442 of the Internal Revenue Code of 1939,1 relating to abnormalities during the base period.

FINDINGS OF FACT.

Some of the facts are stipulated and are hereby found as stipulated.

Petitioner, Oxford Paper Company, hereinafter referred to as Oxford, is a corporation organized and existing under the laws of the State of Maine, with its principal offices at 230 Park Avenue, New York, New York. Its returns for the taxable years 1950 and 1951 were filed with the director of internal revenue, Upper Manhattan District of New York. Oxford keeps its books and files its returns on the calendar year accrual basis of accounting.

Oxford owned and operated, at all times material herein, a fully integrated mill on the Androscoggin River at Rumford, Maine, the principal products of which are paper and woodpulp. The mill and the equipment contained therein were operated primarily by electric power, although some hydromechanical power was utilized.

Oxford’s mill operation is complete from wood to finished paper and includes the production of pulps and chemicals required in its papermaking processes. Although principally devoted to the production of book and printing papers, the mill’s normal operations at all times material herein included the production of its requirements of groundwood, sulphite and soda pulps. Pulp was also produced for sale to customers. In addition, the mill includes one of the largest electrochemical plants in the industry for the production of substantially all of the mill’s requirements of caustic soda and chlorine.

During 1947 and 1948, the mill’s papermaking operations were based upon three pulp making processes: (a) The semi-Kraft pulp process which replaced the soda pulp process on November 1, 1948, (b) the sulphite pulp process and (c) the groundwood pulp process. The basic difference between these was the method of breaking down the wood fibers into pulp. In the semi-Kraft, soda pulp and sulphite processes, logs are placed in drum barkers, where the bark is worked off the logs, then conveyed to chippers to be cut into approximately 1-inch pieces and from there to digesters where the chips are cooked with chemicals to separate the cellulose fibers from the lignin binder. In the semi-Kraft process sulphur is an ingredient in the cooking liquor. This permits a greater yield of pulp per pound and a stronger fiber than any of the other processes and permits the recovery of a substantial part of the chemicals. The sulphite process is an acid process in which there is no recovery of the chemicals. After the cooking has broken down the fibers into a pulp, the separate pulps are carried through washers, rifflers, screens, and deckers before being bleached. After bleaching, the pulps are separately stored.

In the groundwood pulp process logs are forced against grinders, operated primarily by hydromechanical power from water wheels, which grind the logs into fibers, thus avoiding cooking. The fibers are then screened and mixed with a thickener before being stored as pulp.

After storage the pulps are blended according to formulae determined by the type and grade of paper ordered and put through beaters and j or dans where they are refined by mechanical disintegration of the fibers for the paper machines.

As the pulp is carried onto the paper machine, the water is drained off and the fibers adhere to one another, becoming paper as it is dried and pressed. As the paper comes off the dry end of the paper machine, it is rolled on to bars and sometimes conveyed to super-calenders where it is pressed at high speeds to give the paper added finish. The paper is either rewound to be shipped in rolls or cut for shipment in flat packages.

During 1947 and 1948 the mill relied chiefly upon the following major pieces of equipment which were operated primarily by hydroelectric power for the production of paper, pulp, and chemicals:

(a) An electrochemical plant consisting of 288 electrolytic cells which required 1,900 kilowatts of electric power for normal operations.

(b) Two drum barkers, each requiring about 190 kilowatts of electricity.

(c) Sixty-eight pulp beaters, each requiring approximately 50 kilowatts of electricity.

(d) Thirteen jordans, each requiring about 75 kilowatts.

(e) Twelve paper machines until April 18, 1948, when the 13th, a new paper machine (No. 12), started up, varying in size and power requirements from 120 kilowatts on the smallest machine to 2,990 kilowatts on the larger machines.

(f) Eighteen supercalenders each requiring up to 375 kilowatts of electric power for their operation.

In addition, the mill contained a complete groundwood pulpmill, a bleaching plant, a chemical recovery system, and many other pieces of machinery and equipment necessary for the production of pulps and finished paper, all of which were operated primarily by electric power.

From 1941 to 1945, Oxford operated under War Production Board restrictions. During the post-World War II period following 1945, the demand for its products, particularly the demand for book and printing paper, exceeded the capacity of Oxford. Upon the lifting of World War II controls, Oxford began capital improvements to meet the increased demand for paper. This program, to the extent completed by the end of 1948, consisted primarily of the following major improvements:

(a) No. 11 paper machine, originally built in 1921, was rebuilt over the period 1945-1948, inclusive, to produce “on-the-machine” coating and to increase its speed and its capacity from 450 feet per minute to 900 feet per minute. During 1945 and 1946, the machine had produced 10,681 and 12,709 tons of paper, respectively. The “start-up” date of the rebuilt machine was February 1, 1947. In 1947, it produced 25,471 tons and in 1948, it produced 34,149 tons. The capital expenditure for No. 11 paper machine from 1945 through 1948 was $2,361,865.

(b) No. 12 paper machine was purchased and installed during the years 1946, 1947, and 1948. Its “start-up” date was April 18, 1948. This new machine, designed for 1,200 feet per minute operating speed, produced 21,853 tons of paper in 1948 and 37,998 tons in 1949, its first complete year of operation. The capital expenditure for No. 12 paper machine from 1945 through 1948, inclusive, was $4,137,653.

(c) A new boiler (No. 3) was installed during 1947 and 1948 to provide additional steam for use in the mill. Its “start-up” date was April 4, 1948. The capital expenditure for this equipment was $1,159,116 and it provided additional steam of 1,021 million pounds per year in 1948 and 1,242 million pounds in 1949.

(d) A new 8,000-kilowatt back-pressure turbine was installed and started up on June 1, 1948, at a cost from 1946 through 1948 of $592,076 and produced, during 1948, 22.3 million kilowatt-hours of electricity.

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Related

United States Steel Corp. v. United States
316 F. Supp. 990 (S.D. New York, 1970)
New York Shipbuilding Corp. v. United States
237 F. Supp. 995 (D. New Jersey, 1965)
Oxford Paper Co. v. Commissioner
33 T.C. 943 (U.S. Tax Court, 1960)

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Bluebook (online)
33 T.C. 943, 1960 U.S. Tax Ct. LEXIS 197, Counsel Stack Legal Research, https://law.counselstack.com/opinion/oxford-paper-co-v-commissioner-tax-1960.