Richard L. Smith Vanalco, Inc. v. Commissioner of Internal Revenue

300 F.3d 1023, 2002 Daily Journal DAR 9179, 2002 Cal. Daily Op. Serv. 7304, 2002 U.S. App. LEXIS 16162, 2002 WL 1831997
CourtCourt of Appeals for the Ninth Circuit
DecidedAugust 12, 2002
Docket00-70124
StatusPublished
Cited by25 cases

This text of 300 F.3d 1023 (Richard L. Smith Vanalco, Inc. v. Commissioner of Internal Revenue) is published on Counsel Stack Legal Research, covering Court of Appeals for the Ninth Circuit primary law. Counsel Stack provides free access to over 12 million legal documents including statutes, case law, regulations, and constitutions.

Bluebook
Richard L. Smith Vanalco, Inc. v. Commissioner of Internal Revenue, 300 F.3d 1023, 2002 Daily Journal DAR 9179, 2002 Cal. Daily Op. Serv. 7304, 2002 U.S. App. LEXIS 16162, 2002 WL 1831997 (9th Cir. 2002).

Opinion

*1025 OPINION

TASHIMA, Circuit Judge.

The Commissioner of the Internal Revenue Service (“Commissioner”) disallowed deductions taken by appellant Vanalco, Inc. (“Vanalco”) in 1992 and 1993 for expenses related to replacing the lining of aluminum smelting machines and portions of its facility’s floors. The Commissioner determined that these items were capital expenditures depreciable under 26 U.S.C. § 263, rather than ordinary and necessary business expenses currently deductible under 26 U.S.C. § 162(a). The tax court upheld the Commissioner’s determination on Vanalco’s appeal. See Vanalco v. Comm’r, 78 T.C.M. (CCH) 251 (1999) (“Va-nalco I ”). We have jurisdiction over appeals from the tax court pursuant to 26 U.S.C. § 7482(a), and we affirm.

I. BACKGROUND 1

A. Vanalco’s Smelting Operations

During 1992 and 1993, Vanalco was in the business of smelting aluminum. Va-nalco operated a smelting facility in Vancouver, Washington, that it purchased in 1987 from ALCOA, which had owned the facility since 1940.

Aluminum is made from bauxite, an ore that contains large amounts of aluminum hydroxide. Bauxite is refined to make aluminum oxide, also known as alumina. Aluminum is produced by use of the chemical process electrolysis, which involves the decomposition of a chemical compound into ions by passage of electricity through an electrolytic solution. During the smelting process, large buckets carried by overhead cranes dump alumina into hoppers attached on top of reduction cells (“cells”). 2 The hoppers feed the alumina down the center of each cell, where it is dissolved in a bath of molten cryolite solution. An anode, which is a cubical carbon block attached to a copper rod, is then introduced into the cell, and an electrical current is passed from the anode, through the alumina/cryolite solution, and into a cathode, which is a carbon block that lines the bottom of each cell.

The electrical current separates the alumina into molten aluminum, which accumulates on top of the cathode at the bottom of the cell, and oxygen, which combines with the carbon anode at the top to produce carbon dioxide. This process produces aluminum continuously. At the Vanalco plant, the molten aluminum is removed from the cell every other day and transferred to a casting area called the ingot plant. In the ingot plant, the molten aluminum is poured into molds or combined with other alloys to be cast into pig or log shapes.

Vanalco used 636 low current density (“LCD”) cells and fourteen “N-40” cells. The LCD cells were oblong steel shells approximately 22 feet long, 76 inches wide, and 36 inches high. The N-40 cells were the same in all material respects, except that they were shorter in length by about three feet. The shells sat on steel “cradles” over which anodes hung from a large steel superstructure.

Vanalco’s 650 cells were divided equally into ten rooms, where the cells were spaced an average of 24 to 28 inches apart. Two rooms of cells were connected together in a cell line consisting of 130 cells, which were connected by busbars that allowed the cells to share the same electrical current. 3 The cells were arranged in such a way that a particular cell *1026 could be bypassed when necessary. A cell was bypassed or “shunted” from the line by disconnecting the riser from the superstructure and redirecting the flow of electricity. On average, eight to 10 cells were taken out of the line for replacement of their linings at any one time; however, without substantial modifications to its electrical system, Yanalco required a minimum of 112 functioning cells in order to operate its system on a sustained basis.

B. Cell Relining

The lining of the cell is located in the cell shell and consisted of cathode blocks made of carbon materials, collector bars, refractory brick made of a lightweight silicate material, castable refractory, steel plate, insulation board, carbon sidewall blocks, carbon lining paste, and various nuts and bolts. The cell lining of each LCD cell consisted of eight cathode blocks that were 60 inches x 18 inches x 14 inches; two that were 60 inches x 15 inches x 14 inches; one that was 60 inches x 17 inches x 14 inches; two that were 30 inches x 18 inches x 14 inches; and two that were 30 inches x 17 inches x 14 inches. The average life of the cell lining was three years. 4

Cells were monitored by Vanalco in two ways. One involved measuring the iron content of the molten aluminum within each cell twice a week. If the iron content increased above a certain level, it was a sign that the cell lining had eroded to expose the steel collector bars or the shell. Failure to replace the cell lining in this circumstance would cause the cell to eventually rupture, spilling molten metal onto the floor. In addition, the voltage of the cells was monitored to ensure that the cells were running efficiently. If the voltage could not be maintained at a designated level or within a specified range, it was an indication that there was something wrong with the cell lining. In this situation, if all other attempts to improve the operation of the cell failed, the cell would be bypassed and removed from service for relining.

Once the cell was shunted, the relining process involved removing the carbon anodes, cooling the cell for 20 hours, then adding water to further cool the cell and soften the lining materials. The superstructure and shields were then removed, and the superstructure was taken to the potlining area for any necessary repairs. The cell lining crew then removed the cooled, solidified electrolyte and solid aluminum metal from the cell cavity, and the cell was dug with pot diggers to extract the remaining cell lining. The shell and cradle of the cell were removed and taken to the shell repair area with a crane and wagon. In the shell repair area, the shell and cradle were straightened and necessary welding repairs were made. The repaired shell and cradle were put in a vacant spot in the cell line, which was usually different from their original location.

The replacement lining was installed in layers. First, the bottom of each cell was fined with two layers of insulating block cemented together. The cell fining crew then placed a layer of sheet metal on top of the insulating block, which formed a vapor barrier. Two layers of heavy refractory fire brick were added on top of the vapor barrier and the cathode blocks with embedded collector bars were placed in rows on top of the refractory fire brick. The cell fining crew then installed the carbon sidewall blocks around the sides of the shell to cover the area from the top of the *1027 cathode blocks to the top of the shell.

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300 F.3d 1023, 2002 Daily Journal DAR 9179, 2002 Cal. Daily Op. Serv. 7304, 2002 U.S. App. LEXIS 16162, 2002 WL 1831997, Counsel Stack Legal Research, https://law.counselstack.com/opinion/richard-l-smith-vanalco-inc-v-commissioner-of-internal-revenue-ca9-2002.