Smith Engineering Co. v. Rice

102 F.2d 492, 1938 U.S. App. LEXIS 2440
CourtCourt of Appeals for the Ninth Circuit
DecidedDecember 17, 1938
Docket8400, 8401
StatusPublished
Cited by32 cases

This text of 102 F.2d 492 (Smith Engineering Co. v. Rice) 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
Smith Engineering Co. v. Rice, 102 F.2d 492, 1938 U.S. App. LEXIS 2440 (9th Cir. 1938).

Opinion

HANEY, Circuit Judge.

Appeal has been taken from a decree dismissing a suit brought by Smith Engineering Company, a Pennsylvania corporation, hereinafter referred to as the company, to foreclose a mechanics lien on real property in Montana, and from a judgment for plaintiff in an action brought by Laurel Oil and Refining Company, hereinafter called the refiner, against the company and American Surety Company of New York, hereinafter called the surety, to recover damages for breach of two contracts, hereafter called the contract and the supplemental contract, made and entered into by the company and one Will F. Lipman on August 2, 1929.

Because of the conclusion we have reached it is unnecessary to relate evidence and facts pertaining to a number of the questions raised.

Prior to 1910, gasoline was obtained from crude oil by what is known as the “topping process” exclusively. By that process, vapors arising from the crude oil when heat is applied to the same were condensed at atmospheric pressure, and the condensed vapors are referred to as “straight-run” gasoline. Thereafter, a process known as “cracking” was perfected, by which the yield of gasoline from a given crude oil is increased. By that process the part of the crude oil remaining after the straight-run gasoline is separated, is subjected to operations, including a time-temperature and pressure treatment, by which the molecules are broken down and rearranged, resulting in a so-called “synthetic” crude, which also produces gasoline.

It is apparent that vapors arise from the crude oil at low and high temperatures. It became necessary to designate an arbitrary temperature up to which gasoline was obtained by condensation of the vapors arising from the crude oil and temperatures up to the one arbitrarily fixed, called the “end-point”. The standard commonly accepted is the one promulgated by the Bureau of Mines, Department of Commerce of the United States. The first specification was issued October 2, 1918, and contained no provision regarding the sulphur content of gasoline. There were many revisions of such specification. A revision in 1924 first contained a provision regarding the sulphur content in gasoline. The specification as revised in 1927 stated that “Gasoline purchased under this specification shall be described as ‘U. S. Govern *494 ment Motor Gasoline’ * * *” Part of the specification provided:

“6. Distillation .Range. Method 100.13. When the first drop falls from the end of the condenser, the thermometer shall not read more than 55 degrees C. (131 degrees R). '

“When 20 per cent has been recovered in the receiver, the thermometer shall not read more than 105 degrees C. (221 degrees F.)

“When 50 per cent has been recovered in the receiver, the thermometer shall not read more than 140 degrees C. (284 degrees F.)

“When 90 per cent has been recovered in the receiver, the thermometer shall not read more than 200 (degrees) C. (392 degrees F.)

“The end point shall not be higher than 225 degrees C. (437 degrees F.)

“At least 95 per cent shall be recovered as distillate in the receiver from the distillation.

“7. Sulphur. Method 52.0.11. Sulphur shall not exceed 0.10 per cent.”

One Will F. Lipman of Portland, Oregon, being engaged in .the production of oil, in 1927 and 1928 became interested in the 'refining of Oregon Basin crude oil. After various inquiries and negotiations he entered into a contract' with the company, which was engaged in the business of designing and constructing oil refineries.

The contract was signed on August 2, 1929, by Lipman as trastee for the refiner, which had not then been organized, and by the company’s president. It consisted of a contract and a supplemental contract.

By the contract, the company agrees to construct “a complete operating oil refinery to process Oregon Basin crude, otherwise designated as charging stock, for the production of products as specified” therein, near Billings, Montana, for the total sum of $433,845, payable in installments.

The contract provided that' the company should “assume all responsibility for the design, construction and operation of the refinery”; that the capacity of the refinery would be: “ * * * to handle Fifteen Hundred (1500) barrels (42 gallons) per day of twenty-four (24) hours of the above mentioned charging stock, when operating on a cyclic time efficiency of' 90%, it being assumed that the normal charge stock fed to the refinery will be 70° F. or higher, as taken from storage.”

•It was provided that the yields from the crude oil would be:

“Anti-knock Gasoline, U. S. Motor Specifications, 65%. • (This will consist of the natural gasoline contained in the crude, plus the cracked gasoline produced from the topped crude.)

“Residuum of heavy fuel oil — 25%. “Fixed gas loss and fuel oil to operate refinery — 10%.”

It was also provided that “all material and equipment will be of the best quality and that the entire refinery” would “be designed and constructed in a sound workmanlike manner”; that the complete distillation and cracking unit was of the company’s individual design and would be engineered and constructed for its particular service to meet Lipman’s requirements, that “ * * * the distillation and cracking unit will be built in accordance with the best engineering practice known to the industry and that the remaining units will be built in an entirely sound and satisfactory manner for the character and the work contemplated, and will be so constructed that the routine maintenance and repairs will be maintained at lowest level.”

With respect to time, the contract provided that the company “ * * * estimates that the complete refinery can be made ready for initial operation in from 150 to 175 working days from the date on which the Purchaser turns over the refinery site clear and ready for the erection of the equipment.

“In the event that during the initial operating period [the company] finds it necessary to make changes or alterations, * * * it is agreed that [the company] shall have a period from 30 to 60 days in order to make the aforesaid alterations and an additional 30 days in which to produce the expected results, if so required by the Purchaser. The cost of any alterations and changes, however, will be borne entirely by [the company] * * * ” ,

It was further 'provided that Lipman “ * * * shall furnish the following items ■ of materials, labor and services: * * * “ * * * All necessary routine operating labor, as well as charging stock and other material required during initial and test runs * * * ”

The company guaranteed the following: “ * * * that the capacity of the unit will be 1500 barrels (42 gallons) of clean Oregon Basin crude oil per day of twenty- *495 four (24) hours, * * * as stipulated [above] * * *

“ * * * the yields of the products will be as stipulated [above] * * *

“ * * * to produce the yields of products * * * as shown [above], the [company] being permitted a tolerance of plus or minus 5 (five) percent of each product, the percentage being based upon the product as 100%.

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Bluebook (online)
102 F.2d 492, 1938 U.S. App. LEXIS 2440, Counsel Stack Legal Research, https://law.counselstack.com/opinion/smith-engineering-co-v-rice-ca9-1938.