초록 ▼

A process and apparatus for reducing the volume and mass of solid waste (A) by initially subjecting the solid waste to a digestive enzymatic solution (20) agitated by fluid jets (28) under conditions which convert substrate (12) into a liquid waste which is discharged through a conventional sewage s

A process and apparatus for reducing the volume and mass of solid waste (A) by initially subjecting the solid waste to a digestive enzymatic solution (20) agitated by fluid jets (28) under conditions which convert substrate (12) into a liquid waste which is discharged through a conventional sewage system (30). Non-biodegradable plastic shells (10) may be collected in a strainer basket (24) to be removed for further solid waste treatment such as shredding and the like.

대표청구항 ▼

[ What is claimed is:] [1.] A solid waste digestion process comprising reducing the mass and volume of substantially untreated solid waste having cellulose as its major component by subjecting the solid waste to a preliminary enzymatic digestive process, in the presence of an enzymatic solution at a

[ What is claimed is:] [1.] A solid waste digestion process comprising reducing the mass and volume of substantially untreated solid waste having cellulose as its major component by subjecting the solid waste to a preliminary enzymatic digestive process, in the presence of an enzymatic solution at a controlled temperature without appreciable bacterial fermentation from added microorganisms, to convert the solid waste into a liquefied waste and any residual solid waste; separating the resulting liquefied waste from said any residual solidified waste and discharging the resulting liquefied waste. [9.] A solid waste digestion process for reducing the mass and volume of substantially untreated solid waste having cellulose as its major component, the process consisting essentially of: subjecting solid waste having cellulose as its major component to a preliminary enzymatic digestive process, in the presence of an enzymatic solution at a controlled temperature, to convert the solid waste into a liquefied waste and any residual non-cellulose solid waste; separating the resulting liquefied waste from said any residual non-cellulose solid waste; and discharge the resulting liquefied waste. The process of claim 9 including agitating said solid waste in an enzymatic solution during said enzymatic digestive process which contains a cellulase enzyme. The process of claim 10 wherein endoglucanase is included in said enzymatic solution. The process of claim 10 wherein exoglucanase is included in said enzymatic solution. The process of claim 9 including agitating said solid waste in said enzymatic solution by using fluid agitation. The process of claim 9 including agitating said solid waste in said enzyme solution containing an enzyme in a range of about 0.01 to 1.0% by weight of the enzymatic solution and a volume of enzymatic solution of about 0.20 to 1.0 gallons per pound of waste; agitating said solid waste during an agitation period in a range of about 0.5 to 6 hours; and at a temperature range of about 32.degree. to 120.degree. F.; and maintaining the pH of said enzymatic solution at a pH in a range of about 3 to 9. The process of claim 14 including agitating said solid waste in said enzymatic solution containing from about 0.05% to about 0.2% of enzyme by weight and from about 0.25 to about 0.75 gallons of enzymatic solution per pound of waste, during an agitation period from about 0.5 hours to about 2 hours, at a temperature from about 90.degree. F. to about 120.degree. F., and a solution pH from about 3 to about 7. The process of claim 10 wherein said untreated solid waste having cellulose as its major component is selected from the group consisting of throw-away diapers, underpants, paper, and food products.