US4131543A — Method of absorbing liquids using a preparation o…

Claim 1

Independent Claim 431 words

A method of absorbing a spill on land of hazardous, liquid materials chosen from the group consisting of nitric acid, hydrochloric acid, methyl ethyl ketone, other ketones, xylene, polychlorinated bis phenol, known as PCB, slurries thereof in gel form, crude petroleum oils, bunker fuel oil, gasoline, fuel oils, common solvents, and similar hazardous materials, consisting of taking an expanded insoluble light weight aggregate material formed by: (A) mixing, at a temperature less than boiling, an aqueous alkali metal silicate having an alkali metal oxide: silicon dioxide weight ratio of from about 1:3.0-7.0 with an essentially anhydrous alkali metal silicate within the same weight ratio range, the amount of anhydrous added being that quantity sufficient to give, in combination with the aqueous, a total alkali metal silicate solids content of from 80-40% by weight and the amount of alkali metal silicate solids being 40-90% by weight, dry basis, of the total resultant aggregate; (B) admixing, prior to the time when the anhydrous alkali metal silicate becomes substantially hydrated, two insolubilizing compounds as follows: (1) a primary insolubilizer capable of reacting with the alkali portion of the alkali metal silicate at temperatures less than boiling, the amount used being that sufficient to reduce hygroscopicity of the silicate to the point where caking of the composition prior to expansion but subsequent to grinding is prevented and (2) a secondary insolubilizer capable of reacting with the silicate portion of the alkali metal silicate at temperatures used in expanding same, the amount used being that sufficient to render the expanded aggregate water-insoluble, the total amount of insolubilizers used being less than the stoichiometric amount required for total reaction with the alkali metal silicate present; (C) continuing mixing until the components will not separate on standing at temperatures up to boiling; (D) curing the mixed composition at temperatures up to boiling until the anhydrous alkali metal silicate has become substantially hydrated and the primary insolubilizer reacted; (E) cooling the composition to a grindable solid; (F) grinding the composition into discrete nonadherent particles suitable for expansion and (G) rapidly expanding the particles and causing the secondary solubilizer to react by exposure to temperatures of from about 900°-1800° F., to provide an insoluble light weight aggregate which is free flowing in small clusters, having an average density in loose bulk of 2.5 to 3.5 pounds per cubic foot, and having a water absorption of 1.5 gallons per cubic foot, said insoluble light weight aggregate being sized at substantially 10 meshes per inch, then spread this light weight aggregate material over said spill thick enough to absorb said hazardous material.

Claim 2

Independent Claim 431 words

A method of absorbing a spill on land of hazardous, liquid materials chosen from the group consisting of nitric acid, hydrochloric acid, methyl ethyl ketone, other ketones, xylene, polychlorinated bis phenol, known as PCB, slurries thereof in gel form, crude petroleum oils, bunker fuel oil, gasoline, fuel oils, common solvents, and similar hazardous materials, consisting of taking an expanded insoluble light weight aggregate material formed by: (A) mixing, at a temperature less than boiling, an aqueous alkali metal silicate having an alkali metal oxide: silicon dioxide weight ratio of from about 1:3.0-7.0 with an essentially anhydrous alkali metal silicate within the same weight ratio range, the amount of anhydrous added being that quantity sufficient to give, in combination with the aqueous, a total alkali metal silicate solids content of from 80-40% by weight and the amount of alkali metal silicate solids being 40-90% by weight, dry basis, of the total resultant aggregate; (B) admixing, prior to the time when the anhydrous alkali metal silicate becomes substantially hydrated, two insolubilizing compounds as follows: (1) a primary insolubilizer capable of reacting with the alkali portion of the alkali metal silicate at temperatures less than boiling, the amount used being that sufficient to reduce hygroscopicity of the silicate to the point where caking of the composition prior to expansion but subsequent to grinding is prevented and (2) a secondary insolubilizer capable of reacting with the silicate portion of the alkali metal silicate at temperatures used in expanding same, the amount used being that sufficient to render the expanded aggregate water-insoluble, the total amount of insolubilizers used being less than the stoichiometric amount required for total reaction with the alkali metal silicate present; (C) continuing mixing until the components will not separate on standing at temperatures up to boiling; (D) curing the mixed composition at temperatures up to boiling until the anhydrous alkali metal silicate has become substantially hydrated and the primary insolubilizer reacted; (E) cooling the composition to a grindable solid; (F) grinding the composition into discrete nonadherent particles suitable for expansion and (G) rapidly expanding the particles and causing the secondary solubilizer to react by exposure to temperatures of from about 900°-1800° F., to provide an insoluble light weight aggregate which is free flowing in small clusters, having an average density in loose bulk of 2.5 to 3.5 pounds per cubic foot, and having a water absorption of 1.5 gallons per cubic foot, said insoluble light weight aggregate being sized at substantially 10 meshes per inch, then spread this light weight aggregate material over said spill thick enough to absorb said hazardous material.

Claim 3

Dependent Claim 152 words

The method as defined in claim 1, including the additional steps wherein said light weight aggregate material at any temperature up to 165° F. is then mixed with a binder consisting of 5% to 7% polyvinyl chloride dissolved in a solvent free of water and consisting of 15% dimethylsulfoxide and 85% methylethyl ketone at a temperature of about 150° F. to 165° F., until the saturated condition of the mixture turns it from white to gray, while mechanically stirring such mixture, thus forming a final mixture varying in thickness from that of a paint prepared for brush application to a thick paste, and then applying said final mixture to the hazardous liquid material to be absorbed, which absorption occurs in a matter of seconds after contact of the final mixture with the hazardous liquid, the final mixture absorbing said hazardous liquid materials at a rate about 10 to 15 times its weight.

Claim 4

Dependent Claim 105 words

The method of claim 1, wherein said final mixture of aggregate material with said binder is like a thick paste and is submitted to the following steps: (A) passing the said thick paste through contact with salt or fresh water at any temperature, whereby the contact with the water congeals or agglomerates the thick paste instantly into mats or blocks driving off the solvents, and (B) then heating or air drying the resulting mats and blocks at about 150° F. to 200° F. for 45 to 60 minutes, after which said mats and blocks are applied to spills of hazardous liquid materials to absorb same.

Claim 5

Dependent Claim 67 words

The method as defined in claim 1, including the additional steps wherein said light weight aggregate material is then mixed with between 20 percent and 40 percent of its weight of a slurry consisting of 5% to 7% of polyvinyl chloride dissolved in a solvent free of water and consisting of 15% dimethylsulfoxide and 85% methylethyl ketone at a temperature of about 150° F. to 165° F.

Claim 6

Dependent Claim 116 words

The method as defined in claim 1, including the additional steps wherein said light weight aggregate material at any temperature up to 165° F. is then mixed with a binder comprising waxes, or oils, or acrylic or other plastic polymers while mechanically stirring such mixture, thus forming a final mixture varying in thickness from that of a paint prepared for brush application to a thick paste, and then applying said final mixture to the hazardous liquid material to be absorbed, which absorption occurs in a matter of seconds after contact of the final mixture with the hazardous liquid, the final mixture absorbing said hazardous liquid materials at a rate about 10 to 15 times its weight.

Annuity Stage	Window Opens	Payment Deadline	Surcharge Period Until	Estimated Fee	Status
3.5 Years (Year 4)	1981-12-25	1982-06-26	1982-12-26	$2000.00	Window Closed / Lapsed
7.5 Years (Year 8)	1985-12-25	1986-06-26	1986-12-26	$3760.00	Window Closed / Lapsed
11.5 Years (Year 12)	1989-12-25	1990-06-26	1990-12-26	$7700.00	Window Closed / Lapsed

Method of absorbing liquids using a preparation of expanded silicate-based aggregates

Abstract

Inventors

Bibliographic Details

Claims Analysis

References Cited (Backward Citations)

USPTO Annuity & Maintenance Windows

Assigned Categories & Tags

Assign Category Tag