Cullet sorting using density variations

• US 6,464,082 B1
• Filed: 06/15/2000
• Issued: 10/15/2002
• Est. Priority Date: 08/20/1997
• Status: Expired due to Fees

• Current Assignee: Eftek Corp.
• Original Assignee: Eftek Corp.
• Inventors: Whitmore, Frank, Hawk, Neal A., Kimmel, Kevin S., Keller, Meredith A.
• Primary Examiner(s): Walsh, Donald P.
• Assistant Examiner(s): RODRIGUEZ, JOSEPH C
• Application Number:
  US09/594,384
• Time in Patent Office: 852 Days
• Field of Search: 209/3, 209/4, 209/7, 209/10, 209/12.1, 209/11, 209/21, 209/30, 209/38, 209/39, 209/930, 241/24.22, 241/24.14, 241/19
• US Class Current: 209/12.1
• CPC Class Codes: B03B 9/062 the refuse being glass
• CPC Class Codes: B07C 5/3427 by changing or intensifying the optical properties prior to scanning, e.g. by inducing fluorescence under UV or x-radiation, subjecting the material to a chemical reaction
• CPC Class Codes: Y02W 30/52 Mechanical processing of waste for the recovery of materials, e.g. crushing, shredding, separation or disassembly
• CPC Class Codes: Y02W 30/60 Glass recycling
• CPC Class Codes: Y10S 209/93 Municipal solid waste sorting

Abstract

Glass cullet such as recycled municipal waste is processed to substantially eliminate contaminants including light weight paper and polymer, ferrous and nonferrous metal and also ceramics, pyroceramics, tempered glass, stones and assorted silicates that have properties approximating those of glass. In a series of washing and sorting steps, different mechanical, chemical, electromagnetic, and thermal processes cause distinct materials in the cutlet to react differently, whereupon the contaminants are selectively removed and the glass is processed on. The cullet is crushed; ferrous and nonferrous metals are detected and diverted, a screening station sizes cullet particles and routes larger sizes back for additional crushing. An air blower entrains and removes light fractions and dust. A wash station entrains and removes dirt and soluble material. In a flow of sized particles, further metal and ceramic (non-glass silica) detection devices divert portions of the flow sensed to contain non-glass materials. The non-glass non-metallic contaminants are removed by processing to achieve distinct temperatures and also by sorting as a function of particle density. The respective steps are provided along a continuous series of conveyors between processing stations such that the cullet is processed directly through the steps from the raw to finished product. Clean, dry, sized glass particles, including fine glass powder, is produced and can be used for making new glass products.

Claims

1. A method for separating mixed particulates containing recycled glass, which comprises the steps of:

separating out ferrous metal from the mixed particulates by delivering the mixed particulates to a magnetic separator;

separating the mixed particulates into a magnetic fraction and a non-magnetic fraction and removing the magnetic fraction;

dividing the non-magnetic fraction into a coarse component and a fine component;

crushing particulates in the coarse component and admixing them with the fine component so as to render the non-magnetic fraction into components of a relatively uniform size;

separating out light and low density material by applying an air flow to the non-magnetic fraction after said crushing, to entrain and remove air-borne chaff;

separating out soluble fractions by washing the non-magnetic fraction in a washing solution after said separating by air flow, to entrain and remove soluble and water borne fractions; and

drying the washed particulates;

separating out non-magnetic metal particulates from the non-magnetic fraction;

wherein said separating and dividing steps produce a fraction substantially consisting of glass and non-glass contaminants having selective characteristics that resemble but are distinguishable from glass; and

,

lastly, separating out the non-glass contaminants having said selective characteristics, whereby the remaining fraction consists essentially of glass wherein said selective characteristics are substantially uniform.

2. A method as defined by claim 1, wherein the step of separating out light and low density material comprises applying air flow to the non-magnetic fraction to remove air-borne chaff using at least one overhead vacuum hood to draw said air flow through the non-magnetic fraction.

3. A method as defined by claim 1, wherein the step of separating non-magnetic metal particulates from the non-magnetic fraction is carried out by a non-ferrous metal detection station with at least one stage of detection.

4. A method as defined by claim 1, wherein at least part of the non-glass contaminants are distinguishable by density, and wherein the step of separating out the non-glass contaminants having said selective characteristics comprises screening the pulverized glass fraction in conjunction with a separating step wherein a density separation station utilizes a plurality of screen sizes for sorting and also subdivides the pulverized glass fraction into particles of distinct densities.

5. A system for separating mixed particulates of which a portion is recycled glass and is mixed with waste portions including non-glass contaminants having selective characteristics that resemble but are distinguishable from glass, the system comprising sequential operations and including:

means for delivering the mixed particulates to a magnetic separator;

at least one separating station operable to separate the mixed particulates into a magnetic fraction and a non-magnetic fraction;

a separating station which divides the non-magnetic fraction and divides it into a coarse component and a fine component wherein the separating station passes the coarse component through a crusher operable to receive and crush the coarse component and wherein the separating station admixes an output of the crusher with the fine component to provide material with a relatively uniform reduced particle size;

at least one air flow station positioned along a flow path of the non-magnetic fraction and which applies and air flow to said fraction to entrain and remove light and low density material as air-borne chaff;

a washing station which receives and washes the non-magnetic fraction in a washing solution, thereby separating out soluble fractions;

a non-magnetic metal separation station operable to remove remaining metal particulates;

wherein said separating, washing and separation stations pass material containing non-glass contaminants having selective characteristics that resemble but are distinguishable from glass; and

,

a further separating station disposed to operate on the material containing the non-glass contaminants after passing said separating, washing and separation stations, which separates out particulates having said selective characteristics, whereby a remaining fraction consists essentially of glass wherein said selective characteristics are substantially uniform.

6. A system as defined by claim 5, wherein the screening station which screens the pulverized glass fraction comprises a density separation station utilizing a plurality of screen sizes for separating the pulverized glass fraction into particles of uniform size, the density separation fluidizing the particles and applying a force to the particles whereby relatively dense particles including at least part of the non-glass contaminants are selectively removed.