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US 12,121,638 B2Granted
Method and device for controlling odor and vapor
OwnerGary Homaninventor
Life of this patent
Estimating the term…
Abstract
A method of controlling vapor emissions using a liquid vapor trap containing an effective amount of a barrier fluid that will greatly reduce the volume of noxious and/or other gases emitted from a containment (natural or man-made) into the atmosphere. Examples of containment include, but are not limited to septic, fossil fuels and landfills.
Claims5
A trap to control gas and vapor emissions, said trap comprising:
- A) a first housing, said first housing having an entry port for gases and vapors, a top, sides, and bottom;
- B) a secondary housing mounted in an interior of said first housing, said secondary housing having partial vertical walls that do not rest on a bottom of said first housing;
- C) a water trap located in a bottom of said first housing;
- D) an exit port through said top of said first housing;
- E) a siphon tube extending from said water trap to said exit of said first housing;
- F) a barrier fluid contained in said first housing wherein the volume of said barrier fluid exceeds a bottom edge of said partial walls of said secondary housing wherein said barrier fluid is selected from the group consisting of:
- a) an organic fluid composition selected from the group consisting of:
- i) hydrocarbon oil,
- ii) polyglycol oil,
- iii) paraffinic oil,
- iv) aromatic oil, and
- v) poly-alfa-olefinic oil;
- b) polysiloxane fluid polymer compositions having the average formula
- RMe2SiO(Me2SiO)x(MeRSiO)y(R*SiO3/2)zOSiMe2R
- wherein Me denotes a methyl radical and R denotes a methyl radical, a hydroxyl radical, a phenyl radical, an alkyl radical with 2-6 carbon atoms, an alkenyl radical with 2-6 carbon atoms, a halogenated alkyl radical with 1 to 6 carbon atoms, or a silacyclopentene radical;
- R* is the same as R, or represent a siloxane branch represented by the formula RMe2SiO(Me2SiO)x-;
- the average value of x and y varies from 1 to 250, and the value of z is from 0-10;
- wherein said barrier fluids have a Melt Transition Temperature (Tm) less than −25 degrees centigrade, a Vapor Pressure (Vp) of less than 20 mm Mercury (Hg) at 40 degrees centigrade, a viscosity of 1 to 10,000 centipoise at 25 degrees centigrade, a Specific Gravity (SG) of less than 1 at 25 degrees centigrade and a goniometric static surface water contact angle of greater than 100 degrees.
15 more elements
Dependencies are inferred from the claim text.