Wah Chang Smelting & R. Co. v. Commissioner

30 T.C. 838, 1958 U.S. Tax Ct. LEXIS 141
CourtUnited States Tax Court
DecidedJune 30, 1958
DocketDocket No. 61013
StatusPublished
Cited by4 cases

This text of 30 T.C. 838 (Wah Chang Smelting & R. 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
Wah Chang Smelting & R. Co. v. Commissioner, 30 T.C. 838, 1958 U.S. Tax Ct. LEXIS 141 (tax 1958).

Opinion

Pierce, Judge:

An income tax deficiency of $18,488.75 for the calendar year 1952 was determined against the petitioner by the respondent.

The sole issue for decision is: Where petitioner constructed and installed a hydrogen-producing facility for its ore-reducing plant, which facility when operated proved to be inefficient and had to be changed in some respects through reconstruction, may that portion of its construction and installment costs prior to the reconstruction, which is allocable to expenditures for labor and materials in respect of certain piping and fittings that were torn out and scrapped during the reconstruction work, be deducted as an abandonment loss under section 23 (f) of the 1939 Code; or should the same be regarded as part of the overall capital cost of the facility as ultimately completed?

FINDINGS OF FACT.

Part of the facts have been stipulated. The stipulation of facta is incorporated herein by this reference.

Petitioner is a New York corporation with its principal office in New York City. Its return for 1952, the taxable year involved, was filed with the collector of internal revenue for the second district of New York.

Petitioner at all times here material was principally engaged in the production of tungsten concentrates and the manufacture of tungstic acids and tungstic powders, rods, and wires. It also refined other metals, such as tin, antimony, and molybdenum. Its principal manufacturing plant was located at Glen Cove, New York.

In October 1951, petitioner commenced the erection of a building at Glen Cove for the primary purpose of housing equipment for the production of metallic tungsten powder. Such production required the use of reduction furnaces wherein tungsten oxides were heat treated. These furnaces could have been fueled either by carbon, natural gas, manufactured gas supplied by a local utility (called city gas), or hydrogen gas. Petitioner’s management decided to use hydrogen gas, because this fuel was the most efficient. Hydrogen gas could have been purchased from an outside supplier; but petitioner decided, prior to commencement of the construction of the above-mentioned building, to manufacture its own hydrogen gas, for reasons of convenience and also to assure the necessary quality.

The process of producing, treating, and feeding hydrogen gas to reduction furnaces, in a facility of the type decided upon by petitioner’s management, may be briefly described as follows: The hydrogen is first generated in banks of cells by a process known as electrolysis. Electrolysis involves passing electric current from a generator through water in a series of cells, thus causing the water to be separated into its component elements of hydrogen and oxygen. The oxygen is passed off as waste. The hydrogen is then forced by pressure of an air compressor through various stages, so that it is cooled and dried preparatory to being introduced into the reduction furnaces. This process of producing hydrogen has been known for more than 20 years, and there are numerous plants throughout the country which employ it. The hydrogen-generating cells are similar in all installations which employ the process; but there are many variations in other phases of the process, owing to the differing uses to which the hydrogen may be put, and to the consequent need for varying degrees of dryness, purity, rate of flow, and the like. Petitioner’s officers were confident at all times that a hydrogen-producing facility of the type above described could be installed in-petitioner’s plant, and that such facility would yield hydrogen in the quantity and quality desired.

After petitioner had begun construction of the building which was to house its reduction furnaces and hydrogen-producing facility, it retained an individual named Benbow on a part-time basis, to develop an overall plan or scheme for the facility. Benbow had theretofore invented the hydrogen-generating cells which petitioner had decided to use in its facility, and he also was the founder of the company from which such cells were purchased. Another engineering employee of the petitioner, named Noel, was charged with the duty of consulting with Benbow, drawing up the plans, and supervising the construction and installation work. Noel left petitioner’s employment sometime prior to June 1952, before he had finished his work; and he was replaced by another engineering employee named Walter Habeck.

I-Tabeck thereafter drew up detailed plans for the hydrogen-producing facility, and was in charge of supervising the work incident to constructing and installing the necessary fixtures and equipment. The actual construction commenced in July 1952 and continued for about 3y2 months until approximately October 15, 1952, when a complete hydrogen-producing facility was achieved. Up to October 15, 1952, petitioner expended $21,008.93 for the following items pertaining to the construction and installation of equipment for the facility: $3,312.06 for piping, $5,413.22 for fittings, and $12,283.65 for contractors’ labor. The record does not disclose the cost of various equipment installed, such as the hydrogen-generating cells, an electric generator, hydrogen storage tanks, and several compressors.

After the facility had been connected with the reduction furnaces and put into operation, it proved to be unsatisfactory, because it did not produce hydrogen in sufficient quantity or with requisite dryness. This failure was due to several errors in ITabeck’s design, which could not have been anticipated or discovered while the construction work was in progress. Thereupon, petitioner’s officers decided to make changes in the hydrogen-producing facility; and one of its engineering employees, Alfred O. Wu, drew up plans embodying certain changes and eliminations which were aimed toward correction of the existing errors in design. The names of Benbow and Wu appear on the drawings for such changes, as the designers.

The reconstruction work for giving effect to such changes was commenced in November 1952, and was completed prior to December 31, 1952. The changes and eliminations made may be summarized as follows:

As regards the cell room, the electrolytic cells had functioned properly; but owing to the discovery that the facility was losing slightly more hydrogen gas than had been anticipated, 10 cells were added to each of the 2 then existing 20-cell banks. Also, 2 of the 3 hydrogen traps were eliminated; and the remaining hydrogen trap plus an oxygen trap were moved to another part of the same room, apparently to allow space for the added electrolytic cells.

In an adjoining room-called the compressor room, the generator which was used to supply electric current to the electrolytic cells, was moved to a spot just outside the cell room; and the control panel used in connection with such generator was replaced by a new one. Also, there were added a new electric device called an exciter, and a control panel therefor; and these were placed adjacent to the relocated generator and panel. In addition, a second air compressor was installed to supplement the existing one which was retained. An existing blower was turned halfway around, and two new blowers were installed. A cooling tower was moved from the compressor room to a point outside.

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Related

Clayton v. Commissioner
1981 T.C. Memo. 433 (U.S. Tax Court, 1981)
Haspel v. Commissioner
62 T.C. No. 8 (U.S. Tax Court, 1974)
Wah Chang Smelting & R. Co. v. Commissioner
30 T.C. 838 (U.S. Tax Court, 1958)

Cite This Page — Counsel Stack

Bluebook (online)
30 T.C. 838, 1958 U.S. Tax Ct. LEXIS 141, Counsel Stack Legal Research, https://law.counselstack.com/opinion/wah-chang-smelting-r-co-v-commissioner-tax-1958.