Waste Management System
20220203378 ยท 2022-06-30
Inventors
Cpc classification
B29B17/02
PERFORMING OPERATIONS; TRANSPORTING
B02C23/38
PERFORMING OPERATIONS; TRANSPORTING
B02C18/142
PERFORMING OPERATIONS; TRANSPORTING
C02F2303/24
CHEMISTRY; METALLURGY
B29B2017/0094
PERFORMING OPERATIONS; TRANSPORTING
B03C2201/20
PERFORMING OPERATIONS; TRANSPORTING
B29B2017/0416
PERFORMING OPERATIONS; TRANSPORTING
B03C1/035
PERFORMING OPERATIONS; TRANSPORTING
Y02W30/62
GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
B02C19/18
PERFORMING OPERATIONS; TRANSPORTING
C02F2103/007
CHEMISTRY; METALLURGY
C02F2201/008
CHEMISTRY; METALLURGY
C02F2303/26
CHEMISTRY; METALLURGY
B63B35/32
PERFORMING OPERATIONS; TRANSPORTING
C02F9/20
CHEMISTRY; METALLURGY
B02C19/186
PERFORMING OPERATIONS; TRANSPORTING
B09B3/70
PERFORMING OPERATIONS; TRANSPORTING
B02C18/143
PERFORMING OPERATIONS; TRANSPORTING
B03C1/30
PERFORMING OPERATIONS; TRANSPORTING
B09B3/40
PERFORMING OPERATIONS; TRANSPORTING
International classification
B02C19/18
PERFORMING OPERATIONS; TRANSPORTING
B02C21/02
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A waste management system for plastic or other material floating on the surface and in the subsurface of a body of water. A shredding device will reduce the size of the particles of waste. Ocean water is removed by a drying device. The dried waste material is frozen to a temperature at or below minus fifty degrees Fahrenheit, using liquid nitrogen or other suitable means. The frozen waste material is then pulverized and ground into a powder. The powder may then be sprayed into a gas-filled chamber and heated. Temperature, pressure and humidity are maintained within the chamber for more than one minute. Microwave or other radiation and catalysts may be used to enhance the process of extraction. The processed material is then removed from the chamber. Carbon may be recycled or used as fuel by the ship. Water may be used by the ship or returned to the ocean.
Claims
1. A process of waste management comprising: collecting material from the surface and subsurface of a body of water, using one or more nets that are sunk to a depth of no more than five meters; the one or more nets are closed slowly; the one or more nets are raised slowly to allow fish to escape, while capturing material that is floating; shredding the material; drying the material; freezing the material to a temperature at or below minus fifty degrees Fahrenheit in one or more chambers; pulverizing to maximize the ratio of the surface area to volume, and the ratio of surface area to mass; and reacting the material with one or more carbon oxide gases at a temperature at or above four hundred degrees Fahrenheit.
2. The process of waste management according to claim 1, wherein the material is waste material.
3. The process of waste management according to claim 1, wherein the material is plastic.
4. The process of waste management according to claim 1, wherein: each of the one or more nets has larger mesh sizes at its top, and smaller mesh sizes at its bottom; as the nets are closed, the top of each of the nets closes faster than its bottom, because of the difference in mesh sizes; and the nets are then raised.
5. The process of waste management according to claim 4, wherein: the net is angled at no more than twenty-five degrees from top to bottom, whereby marine life can exit, but material is retained.
6. The process of waste management according to claim 1, wherein: plastic is separated from heavier material with a vertical vacuum.
7. The process of waste management according to claim 1, further comprising: storing the material that has been processed.
8. The process of waste management according to claim 1, wherein: interacting screws are used to pulverize the material; and the interacting screws extend, retract, and rotate.
9. The process of waste management according to claim 1, wherein: the material is pulverized using sound waves; and sound is used to mix particles of the material.
10. The process of waste management according to claim 1, wherein: the material is pulverized using metal objects moved by electromagnets that are turned on and off.
11. The process of waste management according to claim 1, further comprising: separation of metal from the material using one or more magnets.
12. The process of waste management according to claim 1, wherein: the material is pulverized using knife-edged screens, with multiple horizontal knife edges and multiple vertical knife edges at right angles.
13. The process of waste management according to claim 4, wherein: there are a plurality of the nets, having varying mesh sizes, arranged vertically in order of mesh size, with the net having the largest mesh size at the top, and the net having the smallest net size at the bottom; wherein the nets are closed and then raised.
14. The process of waste management according to claim 13, wherein: the nets having larger mesh sizes are closed faster than nets having smaller mesh sizes.
15. The process of waste management according to claim 13, wherein: there are a plurality of sets of vertically arranged nets spaced horizontally.
16. The process of waste management according to claim 1, wherein: after the material is pulverized, it is mixed with one or more fluids to form a mixture, and it is then reacted with the one or more carbon oxide gases.
17. The process of waste management according to claim 16, wherein: the one or more fluids include water.
18. The process of waste management according to claim 16, wherein: the one or more fluids include one or more chemicals.
19. The process of waste management according to claim 16, wherein: the mixture is formed using means selected from the group comprising mechanical mixing, screw turning, vibration, centrifuging, and sound waves.
20. The process of waste management according to claim 16, wherein: carbonates are used to produce carbon dioxide.
21. The process of waste management according to claim 16, wherein: formates are used to produce carbon monoxide.
22. The process of waste management according to claim 16, wherein: one or more catalysts are added to the mixture.
23. The process of waste management according to claim 22, wherein: the one or more catalysts include ceric sulfate.
24. The process of waste management according to claim 22, wherein: the one or more catalysts include one or more elements from the platinum group.
25. The process of waste management according to claim 22, wherein: one or more of the one or more catalysts are coated.
26. The process of waste management according to claim 22, wherein: one or more of the one or more catalysts are uncoated.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
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[0093] Similar reference characters denote corresponding features consistently throughout the attached drawings.
DETAILED DESCRIPTION OF THE PREFERRED EM ODIMENT
[0094] The present invention is a waste management system.
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[0096] collecting waste material 10;
[0097] shredding the waste material 12;
[0098] drying the waste material 14;
[0099] freezing the waste material 16 to a temperature at or below minus fifty degrees Fahrenheit;
[0100] pulverizing the waste material, to maximize the ratio of the surface area to volume, and maximize the ration of surface area to mass, of particles of the waste material 18;
[0101] recovering useful material from the waste material 20;
[0102] recycling the recovered useful material 22; and
[0103] storing the recovered useful material 24.
[0104] The waste material should be frozen to a temperature, preferably at or below minus fifty degrees Fahrenheit. Liquid nitrogen, a solution of dry ice and ethanol, or other suitable means of cryogenic freezing may be used. Material that is cryogenically frozen tends to crystallize and become brittle, and therefore easier to pulverize into small particles. (Cryogenic means very cold, e.g., below minus fifty degrees Fahrenheit.) The ratio of the surface area to volume (and mass) increases as particles become small, due to the square-cube law, which states: When an object undergoes a proportional increase (or decrease) in size, it new surface area is proportional to the square of the multiplier, and its new volume is proportional to the cube of the multiplier. (In the case of a decrease, the multiplier will be a fraction.) As smaller particles have a relatively larger surface area on which chemical reactions can take place, they may be more easily converted by chemical reactions into a useful fowl.
[0105] A gas is used in the recovery of the useful material that reacts with the waste material. The gas is preferably a carbon oxide gas, such as carbon monoxide or carbon dioxide. A catalyst such as eerie sulphate, or platinum group metals, coated or uncoated, may be used, in the presence of steam, at a pressure of one atmosphere for a time greater than ten minutes. The waste material may include plastic or any carbon containing material. The waste material may be collected from land or from water. It may be collected from the surface or the subsurface of a body of water, such as an ocean, sea, lake or river.
[0106] The waste material may be collected using a ship, boat or other vessel. The vessel may have a bow that can open up to a greater width than the vessel's beam.
[0107] The waste material may be collected using pumps 30 in
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[0115] Where metal may be present in the waste material, it should be removed before the waste material is shredded or further processed. First, the waste material is passed under a series of magnets, preferably electromagnets. The magnets gather and release magnetic material (metal that can be magnetically attracted) into a size reducer. The size reducer includes grinders and/or shredders. The magnetic material is reduced in size, preferably to an average diameter of one centimeter or less. It is then stored and recycled.
[0116] Particles of the waste material are shredded to a size of no more than one meter at their longest dimension. Pulverization then reduces the average diameter of particles of the waste material to one centimeter or less, preferably one millimeter or less, most preferably one-tenth of a millimeter or less. After it is pulverized, the waste material is placed in a chamber at a temperature greater than thirty-two degrees Fahrenheit, preferably between 212 and 3,000 degrees Fahrenheit.
[0117] The pressure in the chamber is between 0.25 and 500 times the average pressure of air at sea level. The humidity in the chamber is kept greater than one percent but less than one hundred percent. Radiation and/or catalysts are used in the chamber to enhance the process of discovery. Carbon and water are collected from the chamber and recycled. The carbon may be used as fuel by the vessel or elsewhere. The water is purified, and may be used for drinking, washing, irrigating crops, industrial processes, etc. Where toxic substances are present in the waste material, after it has been processed the first time, it is processed again one or more times, to remove the toxic substances. Chemicals that neutralize or remove the toxic substances may be added to the waste material. After the waste material in a chamber has been completely processed, the chamber is purged (by washing, vacuuming, sweeping, air pressure, agitation, or other suitable means) of all remnants of the waste material, before more waste material is placed in the chamber.
[0118] Besides a method for waste management, the invention also includes apparatus for carrying out the method, including:
[0119] one or more chambers, within which waste material is:
[0120] frozen to a temperature at or below minus fifty degrees Fahrenheit;
[0121] pulverized to maximize the ratio of the surface area to volume (and mass) of particles of the waste material; and
[0122] processed to recover useful material.
[0123] The waste material is frozen using freezers, which may be inside or outside of the chambers. The waste material is pulverized using pulverizers, which may be inside or outside of the chambers. The waste material is processed using processors, which may be inside or outside of the chambers. The freezing, pulverization, and processing of the waste material may take place in separate chambers or other spaces.
[0124] There can be a plurality of the chambers, that are rotated to enable continuous processing of the waste material. As shown in
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[0127] Robotically controlled collection systems may control ships, boats, barges, submarines, jet skis, trains, trucks, cars, etc.
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[0130] There may be a plurality of the nets, having varying mesh sizes, arranged vertically in order of mesh size, with the net having the largest mesh size at the top, and the net having the smallest net size at the bottom. The nets are closed and then raised. The larges mesh size may be five centimeters and the smallest net size may be twenty micrometers. Nets having larger mesh sizes are closed faster than nets having smaller net sizes. The edges of the nets have an angle of inclination from the top to the bottom of the nets of not more than twenty-five degrees before they are closed, whereby allowing fish and other marine life to exit from the nets through the larger mesh at the top, while retaining plastic or other material in the smaller mesh at the bottom. There may be a plurality of sets of vertically arranged nets spaced horizontally.
[0131] Each of the one or more nets may have larger net sizes at its top, and smaller net sizes at its bottom. As the nets are closed, the top of each net may close faster than its bottom, because of the difference in mesh sizes. The nets are then raised.
[0132] After the waste material is pulverized, but before it is reacted with carbon oxide gas, it may be mixed with one or more fluids to form a slurry or other mixture. The fluid may be water or one or more chemicals. The slurry may be mixed using mechanical mixing, screw turning, vibration, centrifuging, or sound waves. Carbonates may be added to the mixture to produce carbon dioxide. Formates may be added to the mixture to produce carbon monoxide. Catalysts, such as ceric sulfate and/or a gas reactor, may be added to the mixture. One or more metallic elements from the platinum group (which includes platinum, palladium, rhodium, ruthenium, iridium, and osmium) may be added to the mixture as catalysts. The catalysts may be coated or uncoated.
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[0138] It is to be understood that the present invention is not limited to the embodiment described above, but encompasses any and all embodiments within the scope of the following claims.