The present invention relates to waste disposal, and more particularly to the disposal of liquid waste containing toxic suspended or dissolved substances.
The disposal of liquid waste containing toxic suspended or dissolved substances requires the handling of large volumes and weights of liquid. Although all toxic waste can be treated with the system of the present invention wood treatment will be used as an example. In the case of wood treatment facility, for example, the treated wood liquid is classified as a dangerous waste. It is classified as a dangerous waste due to the toxicity associated with metals, primarily chromium, copper, and arsenic, tebuconazoles, with a second waste stream showing trace amounts of lead, barium, silver, and mercury. The liquid is not classified as corrosive, and has an anticipated pH range of between 3-9.8 The waste is not considered to be ignitable or reactive. The waste does contain a high percentage of suspended solids. The proper storage and disposal of large amounts of such liquid waste is time consuming and costly.
There are shown in the drawings embodiments that are presently preferred it being understood that the invention is not limited to the arrangements and instrumentalities shown, wherein:
A system for the disposal of liquid waste includes a portable container body having an open interior and a liquid waste inlet for receiving liquid waste containing solids. A liquid waste holding tank is provided within the open interior of the portable body for receiving the liquid waste from the liquid waste inlet. A liquid-solid separator within the open interior of the portable body produces a solid waste and a separated liquid waste. A solid waste removal system is provided for receiving the solid waste and placing the solid waste into disposal containers. A conduit directs the liquid waste from the liquid waste holding tank to the liquid-solid separator. An evaporator within the open interior of the portable body heats the separated liquid waste to evaporate and remove water from the separated liquid waste as water vapor, which can be at 0.001 Parts Per Million and can produce a minor residual amount of concentrated liquid waste.
A safety containment system can be provided for retaining overflow or leakage from escaping from the portable body. The safety containment system can include a primary containment apparatus such as a containment liner positioned under the system components. The containment liner has a floor portion and upwardly extending side portions so as to form a container for catching and retaining overflow and spillage. All components of the system can be positioned over the containment liner such that all liquid waste from the system will be captured. The safety containment system can include secondary safety containment apparatus such as a catchment container under the floor of the portable container body. An overflow conduit from the containment liner to the catchment container can be provided. The overflow conduit has an inlet distanced above the floor of the liner such that when liquid waste in the containment liner or primary containment system or apparatus reaches the height of the inlet the liquid waste will flow to the catchment container. The safety containment system can also include a tertiary safety containment apparatus as a berm container positioned under the portable body. The portable container body can be positioned over the tertiary container for additional protection in the event of small drips and overflows, for example during transfer of material to and from the portable container body. The tertiary berm container is positioned at or near the ground and has a liquid waste-impermeable floor and peripheral upwardly extending side portions to catch any liquid waste which might escape from the container body and/or primary and secondary containment systems. This tertiary berm container acts as the final defense in case the other containments systems fail.
The liquid-solid separator can be a screw press assembly. One of several manufacturers offer solutions based on the type of chemical makeup the portable containment body will be used for. Many types of liquid-solid separators are possible, such as filtration devices.
A flocculant treatment station can be provided for adding a flocculant to the liquid waste. The flocculant helps to agglomerate the solids in the liquid waste and to help the separation from the liquid. Many flocculants are known, and include polyacrylamides, chitosan and aluminum compounds such as aluminum sulfate, aluminum chloride and sodium aluminate.
The portable body can be part of or attached to a truck or other electric, fuel cell or combustion engine vehicle capable of moving the portable body. It is also possible to move the portable body by means of another mobile device such as a boat or a barge. The portable body can be a trailer having wheels and an attachment system for attaching the trailer to a motor vehicle. Other vehicles are possible, for example, the system can be provided in a portable container body such as a standard shipping container or a container similarly dimensioned, and then secured to a flatbed truck or other vehicle.
A method for the disposal of liquid waste includes the step of directing a vehicle having a portable container body that can have a liquid waste inlet for receiving liquid waste containing solids to a site with the liquid waste. The liquid waste is transferred into a liquid waste holding tank for receiving the liquid waste from the liquid waste inlet. The liquid waste is transferred from the liquid waste holding tank to a liquid-solid separator. The liquid-solid separator produces a solid waste and a separated liquid waste. The separated liquid waste is transferred to an evaporator and heated to evaporate and remove water from the separated liquid waste as water vapor and to produce a minor residual amount of concentrated liquid waste.
The method can include providing a safety containment system for retaining liquid waste overflow or leakage. A double lined inlet hose can extend from the customers holding tank to the main liquid waste holding tank of the invention. Liquid waste overflow or leakage can be retained by a primary safety containment apparatus such as a liner for the vehicle body. Overflow from the primary safety containment apparatus can be retained by a secondary safety containment apparatus, such as a catchment container positioned beneath the portable container body. The liquid waste overflow or leakage can be collected by a tertiary safety containment apparatus, such as a berm positioned underneath the vehicle, trailer, or other mobile system.
The system and method of the invention have particular utility for the disposal of liquid waste from environmental hazardous waste treatment facilities. These facilities generate large amounts of liquid wastewater containing metals, primarily chromium, copper, and arsenic, and also sometimes trace amounts of lead, barium, silver, and mercury. The metals will remain in the concentrated liquid of the evaporator. The water that is evaporated from the evaporator can be vented to the atmosphere without the risk of environmental contamination to 0.001 microns PPM lower than the current standard in the industry of 0.010 PPM. Also, the system components can be operated at or near atmospheric pressure, so risks associated with elevated pressures are reduced or eliminated.
The operating conditions of the system can vary. Typically, the system works in an ambient temperature. The only temperature variation from ambient is the introduction of the liquid stream is at the evaporation chamber. That temperature will be 213 to 220 degrees Fahrenheit. All plumbing pressures will be maximum rated at 250 PSI and typical operating pressures not to exceed 150 PSI. Flue gas from the evaporator will not exceed manufacturers safety parameters. All systems will be PLC controlled for additional protection. The system can be operated as a batch system or a continuous system.
There is shown in
A tertiary berm containment system 26 is provided for the catchment of liquid waste from overflow and drippings as will be described. A client waste storage container 30 has liquid waste to be treated. A liquid waste transfer conduit 34 is provided to transfer liquid waste to the system 10. A ramp 38 or other suitable structure can be provided for lifting barrels 42 into the portable container body 13 to receive solid sludge or removing the barrels 42 from the portable container body, or barrels 42 that can contain concentrated liquid waste. The ramp 38 can be retractable or removable. Electric, mechanical or pneumatic lifting structure is also possible to lift and lower the barrels 42.
There is shown in
As shown in
A screw press inlet conduit 96 directs the liquid waste that has been treated with the flocculant into a suitable screw press inlet storage container 98. Liquid waste 100 accumulates in the screw press inlet storage container 98 and is drawn into the screw press 90 by the action of shaft 102 driving screw blades 104.
The action of the screw press 90 is to remove liquid droplets 110 through suitable openings 106 in the screw press 90. The liquid effluent 112 from the screw press 90 is collected in a screw press storage outlet container 111. The accumulated liquid effluent 112 is removed from the screw press storage outlet container 111 through an outlet conduit 122 communicating with a valve 124 and through a connecting conduit 126 to a suitable pump 128. Solid waste 114 leaving the outlet 108 of the screw press 90 is deposited as collected solid waste 116 into disposal barrels 42.
Liquid effluent from the screw press 90 is directed through evaporator inlet conduit 132 into an evaporator 130 and accumulates as evaporator liquid 134. The evaporator liquid 134 is heated by a suitable heat source such as a burner 136 creating heated gas 138. The heated gas 138 travels through suitable heat transfer conduit such as pipes 140 and 142 as indicated by arrows 141 and 143. The generated water vapor and heated gas exhaust can be exhausted through an exhaust conduit 144 as shown by arrows 146 and escapes through a vent 148 as shown by arrow 150. When the evaporation process has been completed in a batch process, or in a continuous process, the minor residual amounts of concentrated liquid 134 can be removed from the evaporator through an outlet 152 controlled by valve 154. The concentrated liquid 134 can then be directed through a suitable conduit (not shown) to collection containers for proper disposal.
As the liquid waste contains toxic substances, control of spillage is essential. A primary containment system such as containment liner 72 (
An excess overflow outlet 77 can be provided in the catchment container 76. The inlet 81 of the overflow outlet 77 can be positioned approximately 2 inches below the top level of the containment wall from the surface of the catchment container 76, such that when the liquid reaches this height it will flow into the overflow outlet 77. When the excess liquid spillage 168 reaches the height of the inlet 81 of the excess overflow outlet 77 it will travel as an excess liquid waste stream 172. A valve 79 can be provided to permit the escape of this excess liquid into a suitable disposal container (not shown) as an excess liquid disposal stream 176. Any additional leakage or spillage 180 which falls from the system will be collected within the berm container 26 under the trailer 18 as shown in
Additional leak protection can be provided by securing the transfer of liquid from the customer container 32 the trailer 16. An outlet 204 from the customer container 30 can communicate with a valve 208 through a connecting bracket 206 (
The invention as shown in the drawings and described in detail herein disclose arrangements of elements of particular construction and configuration for illustrating preferred embodiments of structure and method of operation of the present invention. It is to be understood however, that elements of different construction and configuration and other arrangements thereof, other than those illustrated and described may be employed in accordance with the spirit of the invention, and such changes, alternations and modifications as would occur to those skilled in the art are considered to be within the scope of this invention as broadly defined in the appended claims. In addition, it is to be understood that the phraseology and terminology employed herein are for the purpose of description and should not be regarded as limiting.
This application claims priority to U.S. Provisional Patent Application No. 63/255,171 filed on Oct. 13, 2021, entitled “Hazardous WASTE DISPOSAL SYSTEM AND METHOD”, the entire disclosure of which is incorporated herein by reference.
Number | Date | Country | |
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63255171 | Oct 2021 | US |