Lewis v. VERMONT GAS CORPORATION

151 A.2d 297, 121 Vt. 168, 1959 Vt. LEXIS 105
CourtSupreme Court of Vermont
DecidedMay 5, 1959
Docket174
StatusPublished
Cited by22 cases

This text of 151 A.2d 297 (Lewis v. VERMONT GAS CORPORATION) is published on Counsel Stack Legal Research, covering Supreme Court of Vermont primary law. Counsel Stack provides free access to over 12 million legal documents including statutes, case law, regulations, and constitutions.

Bluebook
Lewis v. VERMONT GAS CORPORATION, 151 A.2d 297, 121 Vt. 168, 1959 Vt. LEXIS 105 (Vt. 1959).

Opinion

Shan¿raw, J.

This is an action of tort for personal injuries arising out of a propane air gas explosion. Trial was by jury and resulted in a verdict and judgment for the plaintiff. At the close of plaintiff’s case the defendant moved for a directed verdict, which motion was renewed at the close of all the evidence. After verdict and before judgment the defendant also moved to set aside the verdict. The defendant was allowed exceptions to the action of the court in denying all three motions. By proceeding with the trial, after the denial of its first motion, the defendant waived its exceptions to the overruling of that motion. Croteau v. Allbee, 117 Vt 332, 334, 91 A2d 803, and cases cited. Our consideration is therefore confined to the motion for a directed verdict made at the close of all the evidence and the motion to set aside the verdict.

In passing upon the defendant’s motions the evidence must be taken in the light most favorable to the plaintiff, and if there is any substantial evidence fairly and reasonably tending to support the plaintiff’s claim the question is for the jury. Wakefield v. Levin, 118 Vt 392, 395, 110 A2d 712. The effect of modifying evidence is to be excluded. Contradictions and contradictory inferences are for the jury to resolve. The tendency of the evidence and not its weight is to be considered. Campbell v. Howard National Bank, 118 Vt 182, 183, 184, 103 A2d 96; Fletcher v. Manning, 118 Vt 240, 241-242, 105 A2d 264; Ready v. Peters, 119 Vt 10, 11-12, 117 A2d 374. The defendant assigns and briefs three grounds of error on the part *171 of the court in denying its motions: (1) Plaintiff failed to prove any actionable negligence on the part of the defendant; (2) plaintiff had not discharged his burden of proof; and (3) that plaintiff by his own conduct was contributorily negligent, and must be presumed to have assumed the risk.

Viewed in the light most favorable to the plaintiff the evidence fairly and reasonably tended to show the following facts:

The explosion occurred in Bennington, Vermont on August 25, 1955 at the residence occupied by the plaintiff and his family since 1945 or 1946. The property is owned by plaintiff’s father and mother. A side-arm gas water heater was installed by the plaintiff’s father in 1946 by a private plumber and was being used by the plaintiff at the time of the accident. The defendant acquired the gas distribution system in the Bennington area from the Central Vermont Public Service Corporation in April, 1949, at which time the latter corporation was distributing manufactured water gas. In June of the same year the defendant changed or converted to propane air gas. At the time of the conversion burners on hot water heaters were adjusted and spuds changed if necessary.

Propane is a by-product of gasoline. It is received by the defendant in liquid form, placed in mixers and air added. As delivered by defendant to its customers it is considered a highly inflammable commodity and, when further diluted with air, explosive. Propane air gas being considered an inherently dangerous instrumentality, for detection and precautionary purposes it is also mixed with an unpleasant smelling odorant. Propane gas until mixed with air has a net heating value of about 2360 British Thermal Units per cubic foot at normal temperature and pressure. The propane air gas being furnished the plaintiff at the time of the explosion had a heating value of 750 British Thermal Units, (B.T.U.). Natural gas propane of 750 B.T.U. per cubic foot results in a mixture of 32 per cent propane and about 68 per cent air. This mixture is about 16 or 17 per cent heavier or more dense than air and contrary to popular opinion does not have a tendency to rise. If exposed to air it has a tendency to settle or accumulate in low areas.

*172 On August 25,1955, in the lighting of a match preparatory to igniting the hot water heater located in the cellar, gas ignited, an explosion occurred and the plaintiff sustained first, second and third degree burns involving the face, the neck, both upper extremeties, his chest, back and portions of the lower extremeties. The house was also damaged particularly on the first floor.

We now refer to details of the installation: the service line, Bristol Recorder, meter, valves, burner, pilot light, thermostat, etc., and the function of each. The defendant maintained a Bristol Recorder on its line located about 500 feet from the plaintiff’s premises, which recorded on a circular chart the gas pressure in the service line up to the meter located on plaintiff’s premises. The recorder would not reflect any leaks or irregularities beyond the meter. This pressure was constant and normal during the months of July and August, 1955. The pressure on August 25, 1955 was also normal, running from 6.2 to 6.4, varying only one tenth of an inch of water column. The defendant’s gas service line entered the cellar leading to a meter. Between the curbing and the meter there was a manual shutoff valve, which, for identification purposes, we shall refer to as a master shut-off valve. This valve was located about three feet from the meter. The defendant admits ownership, control and responsibility of the service line up to and including the meter — but not beyond. The purpose of the meter was to record the number of cubic feet of gas which passed through it. An annual inspection was made by an outside concern of the entire distribution system of the defendant’s commercial and residential accounts. Its own service department made an inspection from time to time of its lines. Such inspections, however, were limited up to and including the meter. No inspections were made by the company beyond the meter unless requested. No such specific request was made by the plaintiff. Beyond the meter, on the so-called downstream side, a distance of 16 to 20 feet was a burner to which gas was permitted to flow through a pipe leading from the meter. The burner was attached to a hot water tank and was located near a chimney through which fumes were permitted to escape.

The proper functioning of this burner depended on flame *173 stabilization. Stabilization occurs when the flow of gas is relatively constant and is entirely consumed by the flame. If the flow rate of gas through the port and into the flame front is increased too greatly what is known as "blow off” will occur and the flame will be extinguished completely by being lifted off the port. If the flow of gas through the burner port and into the flame front is too low a "flash back” occurs and in most cases the flame will go out.

William Paul Jensen, Research Associate at the Massachusetts Institute of Technology, qualified as an expert on propane air gas. This witness was familiar with the type of burner in question and testified as follows:

Q. This blowout which you mentioned with reference to a gas flame, would that be analogous to the flooding of an oil burner pilot light, an excess of oil would have the same effect as excess of gas?
A.

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Bluebook (online)
151 A.2d 297, 121 Vt. 168, 1959 Vt. LEXIS 105, Counsel Stack Legal Research, https://law.counselstack.com/opinion/lewis-v-vermont-gas-corporation-vt-1959.