Magnesium Corp. of America v. Air Quality Board

941 P.2d 653, 321 Utah Adv. Rep. 13, 1997 Utah App. LEXIS 80, 1997 WL 377847
CourtCourt of Appeals of Utah
DecidedJuly 10, 1997
DocketNo. 960354-CA
StatusPublished
Cited by1 cases

This text of 941 P.2d 653 (Magnesium Corp. of America v. Air Quality Board) is published on Counsel Stack Legal Research, covering Court of Appeals of Utah primary law. Counsel Stack provides free access to over 12 million legal documents including statutes, case law, regulations, and constitutions.

Bluebook
Magnesium Corp. of America v. Air Quality Board, 941 P.2d 653, 321 Utah Adv. Rep. 13, 1997 Utah App. LEXIS 80, 1997 WL 377847 (Utah Ct. App. 1997).

Opinion

OPINION

ORME, Judge:

Petitioner Magnesium Corporation of America (MagCorp) seeks review of an Air Quality Board order upholding the Division of Air Quality’s administrative determination that MagCorp violated the terms of the Approval Order governing its magnesium production plant west of Salt Lake City. The Board ruled that MagCorp exceeded its chlorine emission limitation from June 1992 through April 1994. In reaching its conclusion, the Board determined that the Approval Order governing the plant’s emissions contemplated that MagCorp’s emission limitation included emissions from all sources, including those due to unavoidable breakdowns. We conclude the Board’s reading of the Approval Order is incorrect and reverse.

FACTS

MagCorp produces magnesium metal at a facility located on the edge of the Great Salt Lake. MagCorp operates its plant under an Approval Order issued by the Executive Secretary of the Division of Air Quality, Department of Environmental Quality, State of Utah. The Approval Order limits the chlorine emissions from MagCorp’s magnesium production process.

A. MagCorp’s Production Process

MagCorp produces primary magnesium metal from anhydrous magnesium chloride powder derived from concentrated brine solutions drawn from the Great Salt Lake.1 This magnesium chloride powder is melted in a melf/reactor and then continuously fed in batches to electrolytic cells that separate chlorine from magnesium metal.

The magnesium chloride powder contains a certain amount of magnesium oxide and must first be purified by converting all the magnesium oxide to magnesium chloride before introducing it to the electrolytic process. Purification is accomplished in the melt/reactor by melting the magnesium chloride and then charging it with chlorine gas and other additives to convert the magnesium oxide to magnesium chloride.

The purified molten magnesium chloride from the melt/reactor is sent to electrolytic cells which separate the magnesium from the chlorine using electrolysis. The molten magnesium is then conveyed to MagCorp’s foundry for casting. Not all of the chlorine is consumed in this process. Chlorine from the melt/reactor passes through particulate scrubbers and then is transported to the chlorine reduction burner, which converts chlorine to hydrogen chloride (HC1).2 From the burner, the HCl-rieh gas passes through a series of scrubbers that remove much of the HC1 before the emission stream passes through the melt/reactor stack.

The electrolytic cells cannot be turned on and off and must be continuously operated and fed batches of molten magnesium chloride from the melt/reactor. MagCorp operates approximately 100 electrolytic cells. If the cells are not continuously fed, they will cool and be destroyed. Replacement of a single cell costs about $70,000 and takes about two weeks. Thus, even if the chlorine reduction burner is not operating, MagCorp must still produce the molten material for the electrolytic cells to remain operational. The heavy price paid pending repair of the chlorine reduction burner is that dangerous chlorine gas is emitted, uncontrolled, directly into the atmosphere.

Most of the chlorine separated in the electrolytic process is sent to a chlorine plant, which generates chlorine for resale and for charging the melt/reactor. The remainder passes through scrubbers before the final emission stream vents through the cathode stack, which is distinct from the melt/reactor stack.

[655]*655B. The Chlorine Reduction Burner and the Approval Order Conditions

The chlorine reduction burner is a unique piece of equipment specially designed for the MagCorp facility. It was constructed pursuant to a Notice of Intent dated June 12,1989, and an Approval Order3 issued by the Bureau of Air Quality, now known as the Division of Air Quality, dated June 30, 1990, and subsequently amended and reissued a month later. That Approval Order was superseded by an Approval Order dated April 16, 1992.

The chlorine reduction burner is a custom-built, natural gas-fired burner that originally contained a pyroflex liner separating refractory brick on the inside from a steel shell on the outside. A pyroflex liner was recommended by the engineering experts who designed the burner and was approved by the Division. The burner was installed at a cost of more than $5.5 million.

The 1990 and 1992 Approval Orders set new chlorine emission limits for both the melVreactor stack and the cathode stack.4 The Division drafted the melVreactor stack emissions limits in condition l.B(3) to read, in part, as follows:

CI2 — emissions shall be determined as follows:

a)The short term Cl2[, i.e., chlorine gas,] limit in the [melVreactor] stack during the operation of the [chlorine reduction burner] shall not exceed 400 lb/hr as determined by appropriate stack testing procedures submitted by Magcorp on May 9, 1990 or as specified by the Executive Secretary.
b) The first 12 months of operation — conversion of no less than 50% of the chlorine gas to HC1 for the 12-month period, in accordance with the chlorine balance procedure required in Condition 16.D — In no case shall the chlorine gas emissions exceed 12,000 tons for the first 12 months of operation of the chlorine burner [.]
c) All subsequent operation — conversion of no less than 80% of the chlorine gas to HC1 in any 12-month period, in accordance with the chlorine balance procedure plan as required in Condition 16.D — In no case shall the chlorine gas emissions exceed ⅛,800 tons per 12-month period in any subsequent 12-mnonth period of operation.

There was no mention in condition l.B(3) of emissions attributable to unavoidable breakdowns.

The Division also drafted a limit for the cathode stack in condition l.C(3), immediately following the melVreactor stack limits in the Approval Order. Unlike condition l.B(3), the limits applicable to the cathode stack explicitly included emissions attributable to unavoidable breakdowns. The cathode stack emission limit was set forth as follows:

(3) CI2 — 3,100 tons per 30-day period based on a rolling sum of successive operating days — 28,950 tons per 12-month period. The Cl2 limits shall be increased by 8.3 ton per day for the number of days during 30-day period the [m]elV[r]eactor chlorine burner is out of service. These limits are for all emissions from the cathode stack including emissions from unavoidable breakdowns.

[656]*656Finally, condition 24 of the Approval Order stated, in pertinent part, as follows: “All installations and facilities authorized by this [Approval Order] shall be adequately and properly maintained. The owner/operator shall comply with [Utah Code of Administrative Procedure] R307-1-3.5 and 4.7.... R307-1-4.7 ... addresses unavoidable breakdown reporting requirements.”

C. Emissions from the Melt/Reactor Stack

Total chlorine emissions from the melt/reactor stack without pollution control equipment would be 24,000 tons annually. In order to allow MagCorp to “shake down” the chlorine reduction burner, the initial limitation was set at 12,000 tons.

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941 P.2d 653, 321 Utah Adv. Rep. 13, 1997 Utah App. LEXIS 80, 1997 WL 377847, Counsel Stack Legal Research, https://law.counselstack.com/opinion/magnesium-corp-of-america-v-air-quality-board-utahctapp-1997.