System and method for processing waste material

• US 8,425,857 B2
• Filed: 05/02/2011
• Issued: 04/23/2013
• Est. Priority Date: 05/01/2010
• Status: Active Grant

• Current Assignee: Red Bag Solutions
• Original Assignee: Red Bag Solutions
• Inventors: Glazer, Sanford A., Norton, William D.
• Primary Examiner(s): CONLEY, SEAN EVERETT
• Application Number:
  US13/099,073
• Publication Number:
  US 20110268606A1
• Time in Patent Office: 722 Days
• Field of Search: 422/292, 422/22
• US Class Current: 422/292
• CPC Class Codes: A61L 11/00 Methods specially adapted for refuse disintegrating medical waste B02C19/0075; disposal of medical waste B09B3/00
• CPC Class Codes: A61L 2/183 Ozone dissolved in a liquid
• CPC Class Codes: A61L 2/202 Ozone
• CPC Class Codes: B02C 18/0092 for waste water or for garbage
• CPC Class Codes: B02C 19/0075 specially adapted for disintegrating medical waste sterilisation of refuse A61L11/00; disposal of medical waste B09B3/00

Abstract

A system for ozone sterilization of waste material, includes a tank configured to receive waste material, ozonated water, and ozone gas. The system further includes a pump coupled to the tank to receive the waste material and the ozonated water from the tank and form a slurry. The pump includes a cutter assembly to reduce a particle size of the slurry through cutting. Additionally, the system includes a circulation loop coupled between the tank and the pump to receive the slurry from the pump and re-circulate the slurry to the tank until the slurry is sterilized. A method for ozone sterilization of waste material is also disclosed.

Claims

1. A system for ozone sterilization of waste material, comprising:

a tank including a top surface, a bottom surface and a substantially cylindrical side wall that define a substantially hollow chamber configured to receive waste material, ozonated water, and ozone gas, wherein the tank includes a first inlet to receive the waste material, a second inlet to receive ozonated water and ozone gas, a third inlet to receive the re-circulated slurry, and an outlet to discharge the slurry to the pump, wherein the first, second and third inlets are positioned within the substantially cylindrical side wall and the outlet is positioned within the bottom surface;

an ozone system to generate the ozonated water and coupled to the second inlet;

a pump coupled to the tank to receive the waste material and the ozonated water from the tank and form a slurry, the pump comprising a cutter assembly to reduce a particle size of the slurry through cutting;

a circulation loop coupled between the tank and the pump to receive the slurry from the pump and re-circulate the slurry to the tank until the slurry is sterilized; and

a deflector plate positioned on the bottom surface of the tank at an angle and height to allow recirculation and deflection to guide the slurry from the third inlet to the outlet after re-circulation, wherein the third inlet is positioned behind the deflector plate with respect to the outlet at a height and position to allow recirculation for the circumference of the tank wall.

2. The system of claim 1, further comprising a filter separator to receive the sterilized slurry from the pump and separate a solid portion of disposable waste and a liquid portion of disposable waste from the slurry.

3. The system of claim 1, wherein the pump comprises cartridge device including a cutter, a cutter bar plate and an impeller having cutting surfaces in a stacked formation.

4. The system of claim 3, wherein the cutter bar plate includes fingers to cut on both top and bottom surfaces.

5. The system of claim 3, wherein the cutter bar plate has a surface for vertical cutting with the cutter.

6. The system of claim 3, wherein the cutter includes at least one carbon insert for increased strength durability while cutting the slurry.

7. The system of claim 1, wherein the ozone system includes an ozone generator to generate the ozonated water and ozone gas, and an ozone injection device to inject the ozonated water and ozone gas into the tank via the second inlet.

8. The system of claim 1, wherein the ozonated water has an ozone concentration between approximately 5% and 50%.

9. The system of claim 1, wherein the circulation loop continuously re-circulates the slurry for an amount of time determined based on at least one of the amount of waste material, the type of waste material, the ozone concentration of the slurry, or the temperature of the slurry.