John C. Grimberg Co. v. United States

32 Cont. Cas. Fed. 73,264, 7 Cl. Ct. 452, 1985 U.S. Claims LEXIS 1041
CourtUnited States Court of Claims
DecidedFebruary 26, 1985
DocketNo. 106-84C
StatusPublished
Cited by49 cases

This text of 32 Cont. Cas. Fed. 73,264 (John C. Grimberg Co. v. United States) is published on Counsel Stack Legal Research, covering United States Court of Claims primary law. Counsel Stack provides free access to over 12 million legal documents including statutes, case law, regulations, and constitutions.

Bluebook
John C. Grimberg Co. v. United States, 32 Cont. Cas. Fed. 73,264, 7 Cl. Ct. 452, 1985 U.S. Claims LEXIS 1041 (cc 1985).

Opinion

OPINION

NETTESHEIM, Judge.

This matter is before the court on cross-motions for summary judgment.

FACTS

An agreement modifying a contract entered into by plaintiff, John C. Grimberg Company, Inc. (“plaintiff”), and the General Services Administration (“GSA”) gives rise to this case. The original contract was for the design, manufacture, delivery, erection, start-up, and testing of modular type fabric filter dust collectors, known as “bag-houses,” and other associated equipment, designed to remove flyash from the flue gases discharged from two coal-fired boilers at the West Heating Plant in Washington, D.C.

The dust collectors or “baghouses,” whose malfunction engendered the subject agreement, contain honeycombs of teflon bags. The bags are mounted on wire cages and are divided among six modules in each baghouse. Flyash in the flue gases from the boilers accumulates on the outer surfaces of the bags as the gases pass through the fabric. When the “filter cake” of dust on the surface of the bags becomes excessive, impeding the flow of the gases through the fabric, a pulse of air is directed down into the bags, thereby flexing them and dislodging the ash, which falls into a hopper. This cleaning process is triggered automatically when the difference in pressure under which the gases enter and leave the baghouse (the “flange to flange pres[454]*454sure drop”) exceeds a certain level (measured in inches on a water gauge).

Section 5 of the contract’s specifications set forth “Performance Guarantee Parameters,” which, inter alia, called for each dust collector to operate under a steam output from each boiler of 220,000 pounds per hour (“pph”) and a gas flow of “126,-000 ACFM at 50% excess air.” At the same time it was required that “[t]he flange to flange pressure drop for each unit shall not exceed 6" W.G. [‘water gauge’].” Section 11 provided, inter alia, for certain acceptance tests to be conducted under the conditions specified by section 5, including “[i]nlet and outlet tests,” i.e., flange to flange. A “flange to flange” test of pressure differential would measure the pressure drop in an entire baghouse, which contained six modules. In addition, section 6 provided, inter alia, that “[e]ach module shall be equipped with a gage to indicate differential pressure across that module in inches of water.”

Plaintiff subcontracted with ResearchCottrell, Inc. (“Research-Cottrell”), to furnish the baghouses, but remained responsible for their erection and testing. The baghouses were fabricated, furnished, and installed by Research-Cottrell and plaintiff pursuant to the specifications.

From fall 1980 to spring 1981, one bag-house was operational, but a problem with high pressure drop arose that resulted in continuous cleaning of the bags and danger of damage to them. In a letter to plaintiff dated October 30, 1980, GSA complained that, in spite of efforts to correct the problem, “[T]he pressure differential across the bags ... rapidly builds up to the range of 6.0 to 7.0 inches water gauge at 50% boiler load____” and that “the boiler may not be able to be operated at any substantial load with the 4.0 inch pressure differential across the bags predicted by ResearchCottrell.” 1

An April 8, 1981 letter from GSA to plaintiff stated:

In the wake of the March 31 and April 1 stack tests conducted by Mogul Enviroservice, it is obvious to all concerned parties that the baghouse is performing below the specified design criteria.
The March 31 test was performed with a steam output of approximately 150,000 pph, differential pressures, measured across the bags, [of] 8.5 to 9.0 inches W.G., and air volume of less than 100,000 ACFM. Those conditions are in contrast to the specified 220,000 pph steam output, flange to flange pressure drop of 6.0 inches W.G., and 126,000 ACFM air flow____
The April 1 test, performed for information only by mutual agreement with Research-Cottrell and you, was performed with approximately 170,000 pph steam output, differential pressure across the bags of 13.5 to 15.0 inches W.G., and 128,000 to 132,000 ACFM air volume.
We deduce, from the foregoing data, that the permissible airflow and output of the boiler is being limited by the pressure drop being experienced across the bags____2

GSA contended that the primary problem was that plaintiff failed to allow for operationally caused “shrinkage” of the bags’ [455]*455felted teflon cloth and that, as a result, the bags fit too tightly over their wire cages, not flexing properly or providing the specified ratio of cloth to air. Plaintiff contended that the particle size of the flyash encountered was smaller than specified, thereby resulting in clogging of the fabric.

On July 1, 1981, the parties met to discuss solutions to the problem. After negotiation it was agreed that plaintiff would install enlarged bags. Tests would then be conducted to determine the pressure drop and the size of the flyash in the flue gases. If the particle size testing reflected that the sizes were not within the range provided in the specifications, then GSA would assume that this contributed to the pressure drop problem. Depending on the results of the bag enlargement program, the cost would be borne totally by one or the other party or shared equally by both: If the pressure drop testing yielded a pressure drop of less than 6 inches, plaintiff was to bear all costs; if the pressure drop exceeded 6 but not 10 inches, the parties would share the costs equally; and if the pressure drop still exceeded 10 inches, then GSA would bear the entire cost of enlarging the bags and the project would be discontinued.

As formally proposed by plaintiff and Research-Cottrell in a letter dated July 7, 1981, under the first contingency “[t]he baghouse meets guarantee and is accepted.” Under the second and third contingencies, acceptance would await further testing of “the unit” after improvement.

GSA drafted an integration of the agreement in the form of a letter to plaintiff dated July 24, 1981, which provided in part:

3. An operational test to establish that the baghouse will operate at 6" W.G. or less, at 126,000 ACFM, must be performed. After establishment of this position, a 30 day operational period will be initiated____
4. Upon expiration of the 30 day operational period, a test will be run to determine the pressure drop across the bags at a gas flow of 126,000 ACFM.

Division of costs based on testing results was as per plaintiffs proposal. No mention was made of conditions for acceptance of the baghouse.

Plaintiffs counsel responded to this proposal in a letter dated August 27, 1981, taking exception to a section of the proposal providing that, in any event, plaintiff would bear all costs if the results of the particle size testing disfavored plaintiff. Counsel objected because even if the particle sizes were within specifications, that would not necessarily mean either that “the bag house operation problem” was caused by undersizing of the bags “or that the enlargement of those bags ... will, in fact, bring the bag house into compliance with ...

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Bluebook (online)
32 Cont. Cas. Fed. 73,264, 7 Cl. Ct. 452, 1985 U.S. Claims LEXIS 1041, Counsel Stack Legal Research, https://law.counselstack.com/opinion/john-c-grimberg-co-v-united-states-cc-1985.