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US3856672A Expired / Lapsed US ⏱️ 0.0 years remaining

Continuous wet oxidation system for the home

Assignee: Whirlpool Corp
•
Filing: 1972-12-04
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Granted: 1974-12-24
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Expires: 1992-12-04
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Abstract

Abstract A continuous wet oxidation system for the home handles virtually all wastes arising out of normal habitation of a domestic dwelling place. Bathroom, toilet and organic kitchen wastes are collected in a common receptor, macerated to form an influent which is pumped through a hydraulic system including a reactor means to which thermal energy and compressed air may be selectively supplied to oxidize the wastes, thereby producing harmless gases, sterile residual ash, and clarified reusable water. The reactor means may be used in conjunction with a reverse osmosis filter to preliminarily remove water from the influent and/or a combined reactor-filter unit may be utilized whereby activated carbon acts as a filter which is selectively reactivated by oxidation of the retained waste.

Inventors

  • 👤 G Boswinkle
  • 👤 R Wheaton

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-30 10:32
CPC Classifications
B; B01; B01D; B01D61/00; B01D61/02; B01D61/025; C; C02; C02F; C02F1/00; C02F1/28; C02F1/283; C02F11/00; C02F11/06; C02F11/08; C02F2103/00; C02F2103/002; C02F2103/005

Claims Analysis

Total Claims: 14
Claim 1
Independent Claim 262 words
THE METHOD OF HANDLING WASTE, ORGANIC TRASH AND GARBAGE IN A HOME, WHICH INCLUDES THE STEPS OF: FLUSHING GARBAGE DISPOSERS, TOILETS AND OTHER HOUSEHOULD APPLIANCES FOR RECEIVING AND GATHERING ORGANIC REFUSE, GARBAGE AND TRASH THROUGH A COMMON HYDRAULIC SYSTEM FORMED BY SUITABLE PLUMBING MEANS, THEREBY TO COLLECT THE WASTE GENERATED IN THE HOME AS FLUSHED MATERIAL CONTAINING SOLID AND LIQUID CONTENTS; AT ONE POINT IN THE SYSTEM COLLECTING THE FLUSHED MATERIAL INTO A COMMON RECEIVING TANK; MACERATING AND MIXING THE SOLID AND LIQUID CONTENTS OF THE TANK TO FORM AN INFLUENT WHICH CAN BE CIRCULTED THROUGH THE SYSTEM; AT A SECOND POINT IN THE SYSTEM METERING A SUPPLY OF PRESSURIZED AIR TO SUPPORT OXIDATION OF THE INFLUENT; AT A THIRD POINT IN THE SYSTEM PRESSURIZING THE INFLUENT BY PUMPING TO DRIVE THE INFLUENT IN THE FORM OF A STREAM; AT A FOURTH POINT IN THE SYSTEM CONFINING THE STREAM TOGETHER WITH THE AIR SUPPLIED THERETO TO FLOW THROUGH A HEAT TRANSFER COIL OF SUBSTANTIAL LENGTH AND NUMEROUS LOOPS IN A REACTING ZONE WHILE ADDING RADIANT ELECTRICAL THERMAL ENERGY TO THE STREAM THROUGH THE COIL THROUGHOUT THE ENTIRE EFFECTIVE FLOW PATH LENGTH OF THE COIL WITHIN THE REACTING ZONE SUCH THAT A TEMPERATURE IN THE ORDER OF 550*-560*F. IS MAINTAINED THROUGHT TRAVEL OF THE STREAM THROUGH THE COIL IN THE REACTING ZONE AND THEREBY OXIDIZING THE SOLIDS DURING THE RESIDENCE OF THE STREAM IN THE REACTING ZONE AND FORMING A COMPLETELY OXIDIZED EFFLUENT WITHIN THE REACTING ZONE; AND SEPARATING EFFLUENT LEAVING THE REACTING ZONE INTO HARMLESS GAS, STERILE RESIDUAL ASH AND CLARIFIED WATER.
Claim 2
Independent Claim 262 words
THE METHOD OF HANDLING WASTE, ORGANIC TRASH AND GARBAGE IN A HOME, WHICH INCLUDES THE STEPS OF: FLUSHING GARBAGE DISPOSERS, TOILETS AND OTHER HOUSEHOULD APPLIANCES FOR RECEIVING AND GATHERING ORGANIC REFUSE, GARBAGE AND TRASH THROUGH A COMMON HYDRAULIC SYSTEM FORMED BY SUITABLE PLUMBING MEANS, THEREBY TO COLLECT THE WASTE GENERATED IN THE HOME AS FLUSHED MATERIAL CONTAINING SOLID AND LIQUID CONTENTS; AT ONE POINT IN THE SYSTEM COLLECTING THE FLUSHED MATERIAL INTO A COMMON RECEIVING TANK; MACERATING AND MIXING THE SOLID AND LIQUID CONTENTS OF THE TANK TO FORM AN INFLUENT WHICH CAN BE CIRCULTED THROUGH THE SYSTEM; AT A SECOND POINT IN THE SYSTEM METERING A SUPPLY OF PRESSURIZED AIR TO SUPPORT OXIDATION OF THE INFLUENT; AT A THIRD POINT IN THE SYSTEM PRESSURIZING THE INFLUENT BY PUMPING TO DRIVE THE INFLUENT IN THE FORM OF A STREAM; AT A FOURTH POINT IN THE SYSTEM CONFINING THE STREAM TOGETHER WITH THE AIR SUPPLIED THERETO TO FLOW THROUGH A HEAT TRANSFER COIL OF SUBSTANTIAL LENGTH AND NUMEROUS LOOPS IN A REACTING ZONE WHILE ADDING RADIANT ELECTRICAL THERMAL ENERGY TO THE STREAM THROUGH THE COIL THROUGHOUT THE ENTIRE EFFECTIVE FLOW PATH LENGTH OF THE COIL WITHIN THE REACTING ZONE SUCH THAT A TEMPERATURE IN THE ORDER OF 550*-560*F. IS MAINTAINED THROUGHT TRAVEL OF THE STREAM THROUGH THE COIL IN THE REACTING ZONE AND THEREBY OXIDIZING THE SOLIDS DURING THE RESIDENCE OF THE STREAM IN THE REACTING ZONE AND FORMING A COMPLETELY OXIDIZED EFFLUENT WITHIN THE REACTING ZONE; AND SEPARATING EFFLUENT LEAVING THE REACTING ZONE INTO HARMLESS GAS, STERILE RESIDUAL ASH AND CLARIFIED WATER.
Claim 3
Dependent Claim 38 words
The method of claim 1, including the step of introducing the pressurized air into the stream of inluent after preheating the influent in a heat exchanger and before introducing the influent into the coil in the reacting zone.
Claim 4
Dependent Claim 51 words
The method of handling waste, organic trash and garbage in a home as defined in claim 1 and further characterized by the additional step of directing the hot effluent through a heat exchanger through which the influent is directed prior to supplying the air for oxidation, thereby to preheat the influent.
Claim 5
Dependent Claim 41 words
The method of claim 1 and further characterized by the step of passing the influent through a reverse osmosis filter to remove approximately 80 percent of the water from the stream prior to oxidation of the influent in the reacting zone.
Claim 6
Independent Claim 259 words
A system for handling waste, organic trash and garbage in a home, comprising: means for receiving and gathering organic refuse, garbage and trash such as flushings from garbage disposers, toilets and other household applicances and comprising a common hydraulic system provided by plumbing means; means in the system for collecting the flushed material as solid and liquid contents and including a common receiving tank; means for macerating and mixing the solid and liquid contents of the tank to form an influent which can be circulated through the system; means for supplying pressurized air into the system after said macerating and mixing means to support oxidation of the influent; means in the system for pressurizing the influent and pumping the influent to flow as a stream; means providing a reacting zone having therein a heat transfer coil of substantial length and numerous loops through which the pressurized stream of influent together with the air supplied thereto is confined to flow; means for supplying radiant electrical energy through the coil to the stream flowing therethrough throughout the entire effective flow path length of the coil within the reacting zone to heat the stream to a temperature in the order of 550* to 560* F. throughout the travel of the stream through the coil in the reacting zone for oxidizing the solids during the residence of the stream in the reacting zone to form a completely oxidized effluent within the reacting zone; and means for separating the effluent after leaving the reacting zone into harmless gas, sterile residual ash and clarified water.
Claim 7
Independent Claim 259 words
A system for handling waste, organic trash and garbage in a home, comprising: means for receiving and gathering organic refuse, garbage and trash such as flushings from garbage disposers, toilets and other household applicances and comprising a common hydraulic system provided by plumbing means; means in the system for collecting the flushed material as solid and liquid contents and including a common receiving tank; means for macerating and mixing the solid and liquid contents of the tank to form an influent which can be circulated through the system; means for supplying pressurized air into the system after said macerating and mixing means to support oxidation of the influent; means in the system for pressurizing the influent and pumping the influent to flow as a stream; means providing a reacting zone having therein a heat transfer coil of substantial length and numerous loops through which the pressurized stream of influent together with the air supplied thereto is confined to flow; means for supplying radiant electrical energy through the coil to the stream flowing therethrough throughout the entire effective flow path length of the coil within the reacting zone to heat the stream to a temperature in the order of 550* to 560* F. throughout the travel of the stream through the coil in the reacting zone for oxidizing the solids during the residence of the stream in the reacting zone to form a completely oxidized effluent within the reacting zone; and means for separating the effluent after leaving the reacting zone into harmless gas, sterile residual ash and clarified water.
Claim 8
Dependent Claim 37 words
A system according to claim 5, including a heat exchanger through which the influent is directed prior to supplying air to the influent by said means for supplying pressurized air for oxidation, whereby to preheat the influent.
Claim 9
Dependent Claim 28 words
A system according to claim 5, including a reverse osmosis filter for removing approximately 80 percent of water from the stream and located downstream from the reacting zone.
Claim 10
Dependent Claim 38 words
A system according to claim 5, including a heat exchanger through which the influent stream is directed and which is located in the system before said pressurized air supplying means introduces the air into the stream of influent.
Claim 11
Dependent Claim 102 words
A system according to claim 5, including a tube-in-tube heat exchanger having an inner tube connected in said system between said pumping means and said coil to receive the influent on its way to the coil, and an outer tube surrounding the inner tube connected with outlet from the coil and leading to said separating means, and conducting the effluent in the heat exchanger in counter-current flow relationship to the influent stream in the inner tube, whereby the inflUent is efficiently heated by the effluent from the reacting means coil and the effluent is correspondingly cooled by the heat exchange thus effected.
Claim 12
Dependent Claim 280 words
Apparatus for handling waste, organic trash and garbage in a home, and comprising: a conduit system provided with a common receiving tank in the system for collecting flushed material waste generated in the home and containing solid and liquid contents; means for macerating and mixing the solid and liquid contents of the tank to form an influent which can be circulated through the system; means for metering a supply of pressurized air to a point in the system for oxidation of the influent; means in the system for pumping the influent to drive the influent as a stream through the system; means providing a reacting zone comprising a pair of reactor filter units each having an elongated vertical bed of activated carbon for retaining solid waste material by filtration and disolved organic materials, colors and odors by adsorption; switching means for alternately switching the stream of influent to one or the other of the filter units to flow in one direction therethrough and in the opposite direction through the other of the filter units, selectively; means extending longitudinally through the bed of activated carbon in each of said filter units for heating the influent passing through the respective filter units by radiant electrical thermal energy throughout the entire effective flow path length through the units to a temperature in the order of 550* F. and operating to maintain such tmeperature throughout the travel of the influent through the units to oxidize solids during residence of the influent stream in the units to form a completely oxidized effluent before leaving the units; and means for separating the effluent after leaving the units into harmless gas, sterile residual ash and clarified water.
Claim 13
Dependent Claim 280 words
Apparatus for handling waste, organic trash and garbage in a home, and comprising: a conduit system provided with a common receiving tank in the system for collecting flushed material waste generated in the home and containing solid and liquid contents; means for macerating and mixing the solid and liquid contents of the tank to form an influent which can be circulated through the system; means for metering a supply of pressurized air to a point in the system for oxidation of the influent; means in the system for pumping the influent to drive the influent as a stream through the system; means providing a reacting zone comprising a pair of reactor filter units each having an elongated vertical bed of activated carbon for retaining solid waste material by filtration and disolved organic materials, colors and odors by adsorption; switching means for alternately switching the stream of influent to one or the other of the filter units to flow in one direction therethrough and in the opposite direction through the other of the filter units, selectively; means extending longitudinally through the bed of activated carbon in each of said filter units for heating the influent passing through the respective filter units by radiant electrical thermal energy throughout the entire effective flow path length through the units to a temperature in the order of 550* F. and operating to maintain such tmeperature throughout the travel of the influent through the units to oxidize solids during residence of the influent stream in the units to form a completely oxidized effluent before leaving the units; and means for separating the effluent after leaving the units into harmless gas, sterile residual ash and clarified water.
Claim 14
Dependent Claim 53 words
Apparatus according to claim 10, wherein said means for metering a supply of pressurized air to the influent is located to introduce the air to the influent in passing from one of said units alternately to the other unit in either direction of flow of the influent from one unit to the other.

References Cited (Backward Citations)

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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1977-12-23 1978-06-24 1978-12-24 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1981-12-23 1982-06-24 1982-12-24 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1985-12-23 1986-06-24 1986-12-24 $7700.00 Window Closed / Lapsed

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