Patent Application
20220289609
This invention relates generally to nuclear waste remediation, specifically a mobile processing system for the removal of radioactive contaminants from nuclear process wastewater. The mobile system is fully scalable, able to accommodate massive-scope industrial nuclear wastewater cleanup projects worldwide, and transportable on conventional national and international transportation infrastructure.
With a worldwide need for abundant and inexpensive energy production, nuclear generated power is increasing exponentially along with world population growth. The first commercial nuclear power stations started operation in June 1954. Since then, nuclear power generation has increased such that there are over 443 commercial nuclear power reactors operable in 31 countries, with over 375,000 MWe total capacity. Currently, as of 2015, there are about 66 more reactors under construction. Increased nuclear power production requires an increase in nuclear waste-water remediation.
With the present state of the art, nuclear wastewater is typically containerized and stored indefinitely at specialized storage facilities. What is needed in the art is a mobile, modular, and scalable wastewater treatment system designed to be both transported and operated from an intermodal shipping container for increased mobility, modularity, and scalability between sites and on-site, further increasing the speed, flexibility, and ease with which the system may be deployed. Additionally, a complete modular wastewater treatment system is needed wherein various different modules for performing different forms of wastewater remediation may be connected in parallel and/or in series in order to perform all of the wastewater remediation requirements and process time requirements for any given site. It would also be advantageous for additional modules to be available for further processing of the contaminants removed from the water during the wastewater remediation process(es) such that the contaminants do not need to be transported from the site for further processing prior to final disposition. An all-in-one mobile, modular, and scalable wastewater remediation and contaminant post-processing system as described in this disclosure would be advantageous for providing a complete solution for any given site, reducing transportation of hazardous materials, reducing implementation costs, and diminishing overall complexity of standard existing practices.
Mobile water processing is well known in the art. However, most existing mobile water processing systems are comprised of merely one specific process, or multiple processes within a single transportable module. Sites requiring wastewater remediation are diverse in their specific requirements, topography, and the location. Natural disaster, terrorist attacks, and malfunctions often require rapid deployment of aid to mitigate overall damage to the environment and adverse effect to people living in the region surrounding the site. Current water remediation systems are not sufficient to perform this task. What is needed is a highly mobile, easily transportable, scalable, modular system that can be deployed quickly (often within 24 hours depending on site location, topography, and remediation requirements) and cost-effectively. The system should be highly adaptable to differing remediation requirements, scalable to maximize efficiency, and modular to perform all remediation needs including outputting water within safety standards as well as processing the removed contaminants to final disposition standards.
In a discussion of prior art, CN. Patent No. 101229949 issued Sep. 7, 2011, titled MOBILE RADIOACTIVE LIQUID WASTE TREATMENT EQUIPMENT generally describes a movable treatment device for radioactive wastewater, which comprises a protecting vehicle, a heat preservation cabin, a treatment system of wastewater, a PLC controlling system and an external connecting pipeline, wherein, the treatment system of wastewater consists of a liquid and solid separator, a pre-filter, an ultra-filter, a security filter, a reverse osmosis filter of two levels and a combined adsorption device; the PLC system consists of a PLC, a flow meter, a conductivity meter, a radioactivity detector and a pressure controlling device. The invention solves the contradiction between the low interception and adsorption efficiency of nuclide and small size under the condition of large flow, meanwhile, which solves the problems of integration of a plurality of techniques and protection of the movable treatment device of radioactive wastewater and realizes automatic operation, safety and reliability in the overall process. What this patent does not disclose is a mobile treatment system designed to be both transported and operated from a standard sized intermodal container for increased mobility between sites and on-site, modularity in the ability to perform multiple different wastewater remediation processes within separate modules, and system scalability of adding multiple process-specific modules for quicker system process times required for a given project.
In a discussion of prior art, U.S. Pat. No. 5,972,216 issued Oct. 26, 1999, titled PORTABLE MULTI-FUNCTIONAL MODULAR WATER FILTRATION UNIT generally describes a portable multi-functional modular water filtration unit having configurable modules that can be adapted to render environmental water potable or to isolate contaminants from groundwater or water from other sources such as backwash from reverse osmosis water purification units (ROWPU) or shower and laundry water (“gray water”) such that the water may be recycled or discharged in full compliance with applicable laws. Plural treatment tanks as well as inlet and outlet filters may be coupled via pressure gauge bearing quick connect fittings in series and parallel arrangements, to allow changes of filter elements (for replacement or substitution of a different active material) and to accommodate flow in filtration arrays. The water purification system specifically addresses the changing water purifying needs that arise during troop deployment, training and maneuvers, disaster relief and environmental cleanup. What this patent does not disclose is a mobile treatment system designed to be both transported and operated from a standard sized intermodal container for increased mobility between sites and on-site, modularity in the ability to perform multiple different wastewater remediation processes within separate modules, and system scalability of adding multiple process-specific modules for quicker system process times required for a given project.
In a discussion of prior art, U.S. patent application Ser. No. 14/041,474 filed Sep. 30, 2013, titled MOBILE WATER FILTRATION UNIT AND CONTROL SYSTEM, AND RELATED DEVICES, COMPONENTS, SYSTEMS AND METHODS generally describes a standardized, modular mobile water purification unit for the production of safe potable water and for treatment of wastewater is disclosed to fulfill the water need for humans, animals and households. In one embodiment, the unit can be based on a standardized climate-controlled container that is robust both physically and functionally, can be easily transported and quickly set up in remote regions and disaster areas. The unit may work for purification of water of brackish, sea or polluted surface water, and of wastewater, and can be customized to the given water type based on easy changeable treatment modules. The unit includes a rigid frame that can be removed from the container, and also includes a control system for remote monitoring and control of the unit. This application teaches away from operating a water treatment system from within an intermodal container.
Although the best understanding of the present invention will be had from a thorough reading of the specification and claims presented below, this summary is provided to acquaint the reader with some of the new and useful features of the present invention. Of course, this summary is not intended to be a complete litany of all the features of the present invention, nor is it intended in any way to limit the breadth of the claims, which are presented at the end of the description of this application.
The mobile processing system as disclosed is designed to be both transported and operated from standard sized intermodal containers or custom designed enclosures for increased mobility between sites and on-site, further increasing the speed and ease with which the system may be deployed. Additionally, the system is completely modular wherein the various different modules perform different forms of wastewater remediation and may be connected in parallel and/or in series in order to perform all of the remediation requirements for any given site. A further advantage of the mobile processing system is the availability of additional modules for further processing of the contaminants removed from the water during the wastewater remediation process(es) such that the contaminants do not need to be transported from the site for further processing prior to final disposition. An all-in-one mobile, modular wastewater remediation and contaminant post-processing system is extremely advantageous for providing a complete solution for any given site, reducing transportation of hazardous materials, implementation costs, and overall complexity of standard existing practices.
The mobile processing system encompasses multiple forms of wastewater processing. Depending on the needs of the particular site, one or more different processes may be used. In some embodiments, one or more of the same modules may be used in the same operation. For instance, two or more separate ISM modules may be used in series wherein each module is operative to remove a specific isotope from the waste stream. Another example is placing two of the same modules in parallel to handle an increased flow capacity or to bring one module online while another is brought offline for maintenance. For processes that take more time, such as feed/blend, it may be advantageous to place one or more modules in parallel to reduce overall processing time.
In an embodiment, systems and methods are disclosed for a Mobile Processing System (MPS) (alternatively referred to a mobile nuclear waste processing system) water treatment process to remove radioactive contaminants from nuclear process wastewater and contaminated groundwater.
In an embodiment, systems and methods are disclosed for utilizing modified transportable intermodal containers (one example: ISO containers) or custom designed containers (hereinafter all enclosure containers are referred to as skids unless otherwise specified) which contain components of various sub-systems of the processing system. Skids may remain on and be operated from the trailers that were used for transporting the system to the treatment site, or they may be offloaded and placed adjacent each other or stacked. An example of an intermodal container for use with the system is a modified ISO shipping container; however, other containers that comply with regulations for conventional intermodal freight transport may be used.
In an embodiment, systems and methods are disclosed where the skids can be connected in a variety of configurations to provide different operating modes or capacities as required to process a particular nuclear process wastewater. As mentioned, each skid consists of an enclosed, modified intermodal container, which is further configured with a drip pan and leak detection. Process lines between skids may consist of hoses with double containment for the prevention of spills to the environment.
In an embodiment, a system and method are provided for in situ (on-site) removal of radioactive material from nuclear facility process water using a fully scalable, portable, and modular system. In general, the design of the system and method can prevent the radioactive material from leaking to the environment. Should the radioactive material be leaked from a train, dam installation, leak detector installation, or piping installed in or outside the reactor building, etc., the system will have a design that can prevent the radioactive material from diffusing, such as leak protection of the joints, etc. The design can prevent the retention of flammable gas, such as hydrogen gas, if such retention is a matter of concern. The process system is designed for ease of transfer from one site to another with flexibility for operating in different modes of filtration and ion removal.
In an embodiment, systems and methods are disclosed for modularity and scalability of the system. Skids (process-specific modules) may be added or removed allowing for a phased approach to site remediation. Quicker process times may be achieved by adding multiples of specific skids, depending on deadline requirements.
Aspects and applications of the invention presented here are described below in the attachments and description of the invention. Unless specifically noted, it is intended that the words and phrases in the specification and the claims be given their plain, ordinary, and accustomed meaning to those of ordinary skill in the applicable arts. The inventors are fully aware that they can be their own lexicographers if desired. The inventors expressly elect, as their own lexicographers, to use only the plain and ordinary meaning of terms in the specification and claims unless they clearly state otherwise and then further, expressly set forth the “special” definition of that term and explain how it differs from the plain and ordinary meaning. Absent such clear statements of intent to apply a “special” definition, it is the inventors' intent and desire that the simple, plain and ordinary meaning to the terms be applied to the interpretation of the specification and claims.
The inventors are also aware of the normal precepts of English grammar. Thus, if a noun, term, or phrase is intended to be further characterized, specified, or narrowed in some way, then such noun, term, or phrase will expressly include additional adjectives, descriptive terms, or other modifiers in accordance with the normal precepts of English grammar. Absent the use of such adjectives, descriptive terms, or modifiers, it is the intent that such nouns, terms, or phrases be given their plain, and ordinary English meaning to those skilled in the applicable arts as set forth above.
Further, the inventors are fully informed of the standards and application of the special provisions of 35 U.S.C. § 112, ¶6. Thus, the use of the words “function,” “means” or “step” in the Detailed Description or Description of the Drawings or claims is not intended to somehow indicate a desire to invoke the special provisions of 35 U.S.C. § 112, ¶6, to define the invention. To the contrary, if the provisions of 35 U.S.C. § 112, ¶6 are sought to be invoked to define the inventions, the claims will specifically and expressly state the exact phrases “means for” or “step for, and will also recite the word “function” (i.e., will state “means for performing the function of . . . ”, without also reciting in such phrases any structure, material or act in support of the function. Thus, even when the claims recite a “means for performing the function of . . . ” or “step for performing the function of . . . ”, if the claims also recite any structure, material or acts in support of that means or step, or that perform the recited function, then it is the clear intention of the inventors not to invoke the provisions of 35 U.S.C. § 112, ¶6. Moreover, even if the provisions of 35 U.S.C. § 112, ¶6 are invoked to define the claimed inventions, it is intended that the inventions not be limited only to the specific structure, material or acts that are described in the preferred embodiments, but in addition, include any and all structures, materials or acts that perform the claimed function as described in alternative embodiments or forms of the invention, or that are well known present or later-developed, equivalent structures, material or acts for performing the claimed function.
A more complete understanding of the present invention may be derived by referring to the detailed description when considered in connection with the following illustrative figures. In the figures, like reference numbers refer to like elements or acts throughout the figures.
Elements and acts in the figures are illustrated for simplicity and have not necessarily been rendered according to any particular sequence or embodiment.
In the following description, and for the purposes of explanation, numerous specific details, process durations, and/or specific formula values are set forth in order to provide a thorough understanding of the various aspects of exemplary embodiments. It will be understood, however, by those skilled in the relevant arts, that the apparatus, systems, and methods herein may be practiced without these specific details, process durations, and/or specific formula values. It is to be understood that other embodiments may be utilized and structural and functional changes may be made without departing from the scope of the apparatus, systems, and methods herein. In other instances, known structures and devices are shown or discussed more generally to avoid obscuring the exemplary embodiments. In many cases, a description of the operation is sufficient to enable one to implement the various forms, particularly when the operation is to be implemented in software. It should be noted that there are many different and alternative configurations, devices, and technologies to which the disclosed embodiments may be applied. The full scope of the embodiments is not limited to the examples that are described below.
In the following examples of the embodiments, references are made to the various embodiments in which the invention may be practiced. It is to be understood that other embodiments may be utilized and structural and functional changes may be made without departing from the scope of the invention.
System Overview
As previously discussed, the MPS equipment is contained in intermodal containers or skids. Example containers are ISO shipping containers, which are widely used standardized containers that can be quickly and easily transported to sites around the world, as needed, on existing infrastructure including truck, rail, ship, plane, and other conventional industrial transportation mediums. Additionally, custom designed enclosures may be used. For purposes of this disclosure, the MPS container(s) is (are) hereinafter referred to as a skid or skids.
Each skid is modified or customized to hold the process equipment, allow for connection of interconnecting hoses, power and signal cables, and allow for removal of lids for filter and ISM vessels replacement. The skids may be operated while mounted on transport trailers. Elevated access platforms may be installed to allow disconnect of filters and ISM vessels for replacements, hydrogen venting, sampling, access to the control room, and placement of interconnecting hoses. Crane access will be required for routine operational replacement of solids removal filters, ultra-filters, and ISM vessels (alternatively referred to as ion exchange vessels). Alternatively, openings in the sidewalls of skids, with or without doors, may be provided to afford forklift, or equivalent, access to filters and ISM vessels for the purpose of routine operational replacement. Additionally, these skids can be mounted on, and operated from, trailers on site to be easily moved around, or rearranged, as needed. If custom designed containers are used, the resulting skid may have integral wheels and towing fixtures, thereby not relying on transport trailers for mobility. In addition to integral wheels, a custom designed skid may include a built-in transport-power-source and vehicle operating controls, i.e., a skid that is drivable under its own power for purposes of mobility to and around the site. In some embodiments, the system will be implemented as a permanent installation on the site.
Modularity
Modularity is a key aspect to effective, efficient, flexible, deployable remediation systems. Containing separate processes within separate modules allows for better remediation customization—allowing only the necessary processes to be brought on-site thus reducing shipping and process costs. At any time, processes may be added or removed allowing for a phased approach to site remediation. Mobile processing modules are simpler to transport, setup, and are more cost-efficient. Standard shipping sizes, such as intermodal containers, allow easy stacking for simple cost-effective transport. Modularity also allows for simpler setup, as processes may be set up in any configuration as required by the topography of the region, including stacking. Modularity also allows for easy skid replacement or simple phase out for skid maintenance. Each module is equipped with standard sized quick disconnects for quick and simple connection/disconnection between any skids in any configuration.
Scalability
Size of Module:
Scalability is another key aspect to effective, efficient, deployable remediation systems. Using scaled modules that are appropriate for the needs of a specific remediation site reduces costs of transport, setup, and operation. The modules in the depicted embodiment have been designed to fit in 6.1 m (20 ft) intermodal containers; however, other container sizes are possible.
Number of Modules in Operation:
Some waste remediation sites may have tighter process time requirements to meet deadlines. Sometimes, the scope of a given remediation project may be so massive that conventional configurations will not be capable of meeting the time constraints. In these situations, it would be beneficial to bring in additional modules. It may even be beneficial to bring in more than one complete system to be used in unison either entirely separately or in parallel to increase processing rates and meet remediation deadlines.
Another distinguishing aspect of the mobile processing system is that it can be used as a complete remediation solution. The mobile processing system isn't just for water remediation—it also includes the capability of processing the contaminants that are removed from the water during the remediation process. There are many technologies available for preparing the removed contaminants for final disposition that are described in the incorporated documents.
One such technology is vitrification. With vitrification, or glassification, frit is added to the contaminant or contaminant laden slurry that is output from the water remediation process, as described in U.S. patent application Ser. No. 12/985,862 (the '862 application) and U.S. patent application Ser. No. 13/036,809 (the '809 application), which are included in the incorporated documents.
Another technology for further processing of contaminants removed from wastewater is volume reduction by separating ions from an ion exchange resin with an elution agent and running through an inorganic ISM column, as disclosed in U.S. patent application Ser. No. 13/850,908 (the '908 application), which is included in the incorporated documents.
For purposes of the present disclosure, the systems and methods disclosed in the '862 application, the '809 application, and the '908 application could be included in one or more intermodal containers or skids as described and used in combination with skids disclosed herein.
For the following discussions, normal operations are termed “Mode D” as identified in Table 1. In an embodiment, this mode has all five of the treatment skids installed and operational.
In an embodiment, the five skids depicted in
In the configuration depicted in an embodiment of
The mixed process water is then passed to the Solids Removal Filter skid where it is filtered through a solids removal filter (SRF) (alternatively referred to as a solids removal filter module) that collects all the sorbent solids and part of the waste solids. The filtered water is then passed to the Ultra Filter skid where it is filtered again through an ultra-filter that collects the remainder of the colloidal suspended solids. Finally, the ultra-filtered water is sent to the ISM skid where it is passed through ISM vessels that remove specific ions from the feed water. After the water has been treated, it is returned to the storage tanks.
In an embodiment, a specialized ion exchange media or sorbent additive is used to control the chemical properties of the process water entering the ISM vessels. In some embodiments the additive is in powder form. The chemical properties of process water can vary significantly between different batches entering the system. The underlying chemical process in the ISM vessels is reliant on equilibrium therefore when the chemical properties of the influent to the ISM vessels changes, the column efficiency could fluctuate. The quantity and type of sorbent additive can be adjusted to normalize the concentration of an ion (Sr or Ca, for example) such that the chemical conditions in the ISM vessels remain stable. In some embodiments, the chemical properties of the solution going into the ISM vessels is monitored, automatically and/or manually, and the amount of sorbent additive is adjusted incrementally to stabilize any fluctuations. In alternative embodiments, to minimize the system adjustment response time, the chemical properties of the influent process water are monitored, automatically and/or manually, and the amount of sorbent additive is adjusted stoichiometrically. The chemical properties in the ISM vessels may also be monitored to confirm/fine tune the effect of the sorbent additive adjustment.
In an example embodiment, the MPS is used to treat reverse osmosis (RO) reject water containing strontium (Sr-90). A powdered sorbent (or other ion exchange material in powder form) is fed from the Control/Solids Feed skid 140 into the Feed/Blend skid 130. The additive is mixed into the process water and given time to absorb a particular isotope from the solution. The sorption time is dependent on the ISM used and the targeted isotope to be removed. In the example embodiment, to remove Sr-90 from the RO reject water, the sorption time is about forty minutes. In an alternative embodiment, other nuclear waste components besides Sr-90 can be removed, and other wastewater besides RO reject water can be treated.
In some embodiments, each skid includes climate control and shock absorption to prevent damage to the hardware during transport, setup, and usage.
The depicted embodiment is an example of the preferred skid arrangement wherein the skids are situated proximately on a level surface in a single layer (i.e., not stacked). For certain sites, the topography of the region may render the preferred skid arrangement unfeasible, therefore elevation, distance, and system footprint need to be considered. At these certain sites, the skids may need to be placed at one or more of different elevations, farther distances apart, or stacked. In some embodiments additional pumps may be situated between the skids, hose diameters may be increased or decreased, and/or other system component settings may be altered to achieve the desired pressure and flow conditions. In some embodiments, differences in elevation may be used as a gravitational advantage to reduce pumping requirements and thus save on energy costs.
In one embodiment, for skids containing pumps, two or more pumps may be placed in parallel at each pump location wherein each pump is configured for a differing range of pressures. Depending on the skid arrangement at the particular site, the appropriate pump will be utilized. Placing two or more pumps in parallel allows for a more highly mobile and modular system allowing the system to function at appropriate flow conditions for a wider range of differing site topographies and skid arrangements.
In an embodiment, a first tank T-100 and second tank T-101 tank are connected in series. A pre-determined quantity of the sorbent and a pre-determined quantity of the contaminated water are combined in the first feed/blend tank T-100 and remain in first feed/blend tank T-100, with or without agitation, for a pre-determined period of time calculated to allow the contaminant to be sorbed by the sorbent. To convert this batch process into a continuous process, the contents of first feed/blend tank T-100 are transferred to the second feed/blend tank T-101 providing the source of a continuous flow of treated water to be pumped from the Feed/Blend skid 130 through pump P-152 into the Solids Removal Filter skid 120. Alternatively, the treated water may be transferred directly into the Solids Removal Filter skid 120 through pump P-152 while the second feed/blend tank T-101 is being processed in parallel. In an alternative embodiment (not shown), feed/blend tanks T-100 and T-101 are connected in parallel. A pre-determined quantity of the sorbent and a pre-determined quantity of the contaminated water are combined in the first feed/blend tank T-100 and remain in first feed/blend tank T-100, with or without agitation, for a pre-determined period of time calculated to allow the contaminant to be sorbed by the sorbent. The treated water in first feed/blend tank T-100 is pumped at a rate calculated to provide a continuous flow from the Feed/Blend skid 130 into the Solids Removal Filter skid 120. At the time the treated water starts to flow from first feed/blend tank T-100, the filling process is started for second feed/blend tank T-101. The alternating use of feed/blend tanks T-100 and T-101 provides a steady and continuous flow of treated water to the Solids Removal Filter skid 120. Regardless of whether the tanks are configured in parallel or in series, the treated water delivered to the Solids Removal Filter skid 120 passes through a first solids removal filter FLT-200 or a second solids removal filter FLT-201 (depending on which filter is online) to remove the sorbent and any other solids. Next the treated water is pumped through pump P-350 into the Ultra Filter skid 110 where it is further filtered by a first ultra-filter FLT-300 or a second ultra-filter FLT-301 (depending on which filter is online).
Continuing with an embodiment description, from the Ultra Filter skid 110 the process water is pumped through pump P-450 into the Ion Specific Media skid 100 where it is passed through one or more ion specific media (ISM) vessels containing ion exchange media specific to the removal requirements of the site. The depicted embodiment shows four ISM vessels VSL-460, VSL-461, VSL-462, and VSL-463, where three are online at a time and the fourth is in standby. Every five days, or on a different pre-determined maintenance schedule, the next vessel down the line is taken offline and the standby vessel is put online. After passing through one or more of the ISM vessels VSL-460, VSL-461, VSL-462, and VSL-463 the water is either returned to the storage tanks for further disposition or run through the system continuously until it meets purity standards.
The sorbent and the water are combined in a first feed/blend tank T-100 and then in a second feed/blend tank T-101. Next, the treated water is pumped P-152 from the tanks to pass through a first solids removal filter FLT-200 or a second solids removal filter FLT-201 (depending on which is online) to remove the sorbent and any other solids. Next the treated water is pumped P-350 (of
From the ultra-filters the water is pumped P-450 through one or more ion specific media (ISM) vessels containing ion exchange media specific to the removal requirements of the site. In some embodiments the ISM vessels are loaded with a titanosilicate synthetic product, which is a very stable granular material with a high strontium distribution coefficient KdSr, even in high competition (e.g., seawater, Ca and Mg) making it an excellent choice for removal of strontium in column/vessel applications. The depicted embodiment shows four ISM vessels VSL-460, VSL-461, VSL-462, and VSL-463, three of which are online and one which is in standby. After passing through one or more of the ISM vessels the water is either returned to the storage tanks or run through the system continuously until it meets purity standards. In some embodiments, the clean water may be used for system flushing operations.
In an embodiment, powdered sorbents or ion exchange materials are delivered in approximately 800 kg Super Sacks® or similar industrial sacks, hereinafter referred to as industrial sacks. The industrial sacks are unloaded through filter FLT-502 into the hopper T-502. Two mechanical vibrators VIB-503 and VIB-504 on either side of the hopper T-502 are used to aid the solid material in traveling to the base of the hopper T-502. At the base of the hopper T-502 a rotary valve RV-502 controls the rate of flow of the solids through a flex coupling into second smaller hopper. The second hopper has a discharge at the inlet which allows excess solids to flow out of the hopper in the event the hopper is overfilled. From the small hopper the solids travel into a solids feeder FDR-501 which uses an auger to control the feed rate of the solids. After the solids feeder FDR-501 stage, the sorbent is joined by air and sent through a flex hose out of the Control and Solids Feed skid 140 to the Feed/Blend skid 130.
In an embodiment, the Feed/Blend skid 130,
At a second inlet RO reject water (or other nuclear process waste feed water) is gravity fed into the system from the wastewater storage tanks through double contained transfer hose H-001. The feed water is passed through a disconnect valve DV-100. Most or all the feed water will continue through the primary piping, through ball valve V-106 (normally locked open) and into a first feed/blend pump P-150, which is variable speed. A portion of the feed water may travel through secondary piping if ball valve V-108 (normally locked closed) is opened, and then travel through check valve CV-103 to bypass the first feed/blend pump P-150 and join the primary flow. The first feed/blend pump P-150 has two additional outlets with ball valves V-109 (normally closed) and V-107 (normally locked closed) which direct excess water to the sump when one or both valves are opened.
Water exits the first feed/blend pump P-150 where it passes through check valve CV-104 and ball valve V-110 (normally locked open). The feed water continues down the pipeline to a split where one path is normally closed, and the other is open. On the normally open path, the feed water passes through ball valve V-123, is strained at basket strainer STR-100 to remove particulates, and through ball valve V-124. If the normally closed path is opened, the feed water passes through ball valve V-125, basket strainer STR-101, and ball valve V-126. The normally open and the normally closed paths converge prior to joining the powdered sorbent or ion exchange material flow into the eductor ED-102. Three alternative paths are provided for water flow to the sump which is blocked by valves that are normally locked closed. Ball valve V-128 controls flow on the alternative path from the normally closed primary line, ball valve V-129 controls flow on the alternative path from the normally open primary line, and ball valve V-127 controls flow on the alternative path just after the convergence of the normally open and normally closed primary lines.
Continuing with an embodiment description, at a third inlet powdered sorbent or ion exchange material is provided from the Control and Solids Feed skid 140 of
The process water leaves the second feed/blend tank T-101 through the bottom and through ball valve V-114 (normally locked open). Most or all the process water will continue through the primary piping, through ball valve V-116 (normally locked open) and into a second feed/blend pump P-152, which is variable speed. The speed of the second feed/blend pump P-152 (
Continuing with the example embodiment of
In an example embodiment, the Solids Removal Filter skid 120, depicted in
Hydrogen and other gases may be vented from the filtering system just before each filter. The hydrogen or other gases may pass through ball valve V-A (normally closed), through flex hose, through ball valve V-219 (normally locked closed), and then either to the sump through ball valve V-200 (normally closed) or to the environment outside the skid through filter FLT-210. Alternatively, the hydrogen or other gases may travel through ball valve V-B (normally closed) and check valve CV-D to the environment. Nitrogen may be purged at either ball valve V-222 (normally locked closed) or ball valve V-225 (normally locked closed) depending on which filter is currently in use.
At a second inlet, process water travels via double contained transfer hose H-002 from the Feed/Blend skid 130 of
If ball valve V-203 (normally locked closed) is opened, all or a portion of the process water will travel through secondary piping to the solids removal filter pump P-250. The solids removal filter pump P-250 has an additional outlet with ball valve V-205 (normally closed) which allows excess process water to flow to the sump when it is opened. Additionally, just after the primary outlet, excess process water may flow to the sump if ball valve V-226 (normally closed) is opened. However, most of the water will proceed through ball valve V-207 (normally open) and check valve CV-202 back to the primary piping.
Along the primary pipeline, before the filters FLT-200 and FLT-201, there is a pressure relief valve PRV-200 which will relieve any pressure over 0.48 MPA (70 PSIG), or any pressure deemed crucial for proper system operation. There is also a surge suppressor T-200 preceded by ball valve V-216 (normally locked open) on a secondary line. The pressure relief valve PRV-200 dumps process water to the sump when the maximum pressure is exceeded. The process water may either proceed through the first filter FLT-200 or the second filter FLT-201 depending on which one is online. The filters FLT-200 and FLT-201 remove most of the contaminant-bearing powdered sorbent or ion exchange material and small particulates containing contaminants from the process water. Two filters are provided with one online and one in standby or going through a replacement or maintenance procedure. The online filter remains online until the high differential pressure limit is reached. The standby filter is then placed online, and the loaded filter can be replaced.
Continuing with an embodiment in
In an embodiment, the Ultra Filter skid 110,
In an embodiment, the Ultra Filter skid 110 as shown in
Hydrogen and other gases may be vented from the filtering system just after each filter placement in the process line. The hydrogen or other gases may pass through ball valve V-A (normally closed), through flex hose, through ball valve V-315 (normally closed), and then either to the sump through ball valve V-300 (normally closed) or to the environment outside the skid through filter FLT-310. Alternatively, the hydrogen or other gases may travel through ball valve V-B (normally closed) and check valve CV-D to the environment. Nitrogen may be purged at either ball valve V-320 (normally closed) or ball valve V-323 (normally closed) depending on which filter is currently in use.
At a second inlet, process water travels via double contained transfer hose H-003 from the Solids Removal Filter skid 120 of
Along the primary pipeline, before the filters FLT-300 and FLT-301, there is a pressure relief valve PRV-300 which will relieve any pressure over 1.03 MPA (150 PSIG), or any pressure deemed crucial for proper system operation. There is also a surge suppressor T-300 preceded by ball valve V-307 (normally locked open) on a secondary line. The pressure relief valve PRV-300 dumps process water to the sump when the pressure is exceeded. The process water may either proceed through the first filter FLT-300 or the second filter FLT-301 depending on which one is online. The filters FLT-300 and FLT-301 remove most of the remaining contaminant bearing solids and small particulate containing contaminants from the process water. Two filters are provided with one online and one in standby or being replaced. The online filter remains online until the high differential pressure limit is reached. The standby filter is then placed online, and the loaded filter can be replaced.
Further with an embodiment of
The Ion Specific Media skid 100, depicted in an embodiment in
At a second inlet, filtered process water travels via double contained transfer hose H-004 from the Ultra Filter skid 110 of
The ISM feed pump P-450 is a constant speed pump, with variable speed capability, sized for transfer through the ISM vessels and for return to the storage tanks. The speed of the ISM feed pump P-450 will be adjusted manually from the control system to ensure sufficient head is available for the transfer function. Variable speed capability allows for flexibility of operation in different modes or for different transfer lengths. The pressure differential through the ISM vessels and back to the feed tanks does not generally change significantly, therefore setting the ISM feed pump P-450 at a constant speed reduces the complexity of the control system. Sufficient pressure and flow instrumentation is included to provide proportional feedback control on the ISM feed pump P-450, if desired based on operating experience.
Along the primary pipeline, before the ISM vessels, there is a pressure relief valve PRV-400 which will relieve any pressure over 0.90 MPA (130 PSIG), or any pressure deemed crucial for proper system operation. There is also a surge suppressor T-400 on a secondary line. The pressure relief valve PRV-300 dumps filtered process water to the sump when the pressure is exceeded. The filtered process water proceeds to the ISM vessels (
In an embodiment,
Continuing with an embodiment of
Filtered process water is pumped into the ISM vessel system from ISM feed pump P-450. The filtered process water flows into each ISM vessel. After each ISM vessel the filtered process water flows either to the next ISM vessel or out of the ISM vessel system to
Continuing with an embodiment of
Controls/Instrumentation
In an embodiment, the Control and Solids Feed skid 140 (
General Instrumentation
Sump Instrumentation
In an embodiment, every skid has a sump, and every sump has at least one leak detection transmitter which transmits to a leak detection alarm in the event a leak is detected. Each leak detection data line has at least one interlock. In an embodiment, the Control and Solids Feed skid 140 (
Environmental Monitoring Instrumentation
In an embodiment, every skid is also equipped with at least one temperature transmitter and at least one radiation detection transmitter. The Control and Solids Feed skid 140 (
In an embodiment, the Solids Removal Filter skid 120 (
In an embodiment, the Ultra Filter skid 110 (
In an embodiment, ambient skid temperature for the Ion Specific Media skid 100 (
Flow Controls
In an embodiment, all the skids except the Control and Solids Feed skid 140 (
In an embodiment, the Feed/Blend skid 130 (
In an embodiment, the Solids Removal Filter skid 120 (
In an embodiment, the Ultra Filter skid 110 (
In an embodiment, the Ion Specific Media skid (
In an embodiment, downstream from the first pump on each skid a magnetic flow meter is used to monitor flow out of the pump. In the Feed Blend skid 130 (
Pressure Indicators and Controls
In an embodiment, pressure is monitored at critical points in all of the skids.
In the Feed/Blend skid 130 (
In the Solids Removal Filter skid 120 (
In the Ultra Filter skid 110 (
In the Ion Specific Media skid 100 (
Pump Controls
In an embodiment, he Feed/Blend skid 130 (
The second feed/blend pump P-152 is connected to variable frequency drive VFD-152, equipped with interlocks I1 and I3. Variable frequency drive VFD-152 is connected to event controllers YC-152A and YC-152B, event indicators YI-152A and YI-152B, and speed controller SC-152. The second feed/blend pump P-152 controls are connected via data link to the pressure indicating controller PIC-300 (
In an embodiment, the speed of the second feed/blend pump P-152 is modulated to maintain a constant pressure at the inlet to the ultra-filter pump P-350 (
In an embodiment, within the Solids Removal Filter skid 120 (
In an embodiment, the Ultra Filter skid 110 (
In an embodiment, within the Ion Specific Media skid 100 (
Other Instrumentation
The level in each of the feed/blend tanks T-100 and T-101 is monitored by a pressure indicating transmitter PIT-103 and PIT-107 (respectively), each connected to a diaphragm. PIT-103 is connected to level switch indicator LSI-103, level switch high LSH-103, and level indicating controller LIC-103. LIC-103 is further connected to the first feed/blend pump P-150 controls. PIT-107 is connected to level indicator LI-107.
Downstream of the magnetic flow meter pH and turbidity are monitored by analyzer sensor AE-100, conductivity sensor CE-100, and analyzer sensor AE-101. Analyzer sensor AE-100 and conductivity sensor CE-100 are connected to conductivity transmitter CT-100 which is connected to analyzer indicator AI-100, temperature indicator TI-100, and conductivity indicator CI-100. Analyzer sensor AE-101 is connected to analyzer transmitter AT-101 which is connected to analyzer indicator AI-101.
Startup/Nominal Values
In an embodiment of a startup procedure, the piping system will be filled and vented by clean water injected through the flush connections. RO reject feed flow is started with second feed/blend pump P-152 and the powdered sorbent or ion exchange material feed is initiated. The first feed/blend tank T-100 is allowed to fill to its normal operating level. When the tank reaches the high level, the downstream pumps P-152, P-350, and P-450 are started in sequence. Second feed/blend pump P-152 is started initially with a permissive from a second feed/blend tank T-101 level set point and positive pressure at its suction. Ultra-filter pump P-350 will then start when its suction pressure reaches a positive value through a permissive on its suction side pressure transmitter. ISM feed pump P-450 will then start when its suction pressure reaches a positive value through a permissive on its suction side pressure transmitter. Variable speed drives will be set for slow pump ramp up to a fixed speed. Once all pumps are up to speed, the system is transferred to automatic control and the normal operation sequence described above takes over.
Optimal System Operation
With consideration now for the projected number of filters and ISM vessels to be generated in the spent SRF, UF, and ISM vessels. The number of SRFs generated is related to how much powdered sorbent or ion exchange material is used. The baseline operation is to use 400 kg sorbent per 1,000 m3 of water with the expectation of generating five spent SRFs per 5,000 m3 of water. The sorbent usage could be as low 100 kg per 1,000 m3, in which case there would be one or two spent SRFs. The UF loads only with the colloidal material that passes through the SRF. The expectation is that one spent UF is generated per 5,000 m3 of water. ISM vessels are expected to be spent after five days of operation, thus generating 3.33 spent ISM vessels per 5,000 m3 of water.
The MPS has been optimally designed to operate at an operational flow rate of 300 m3/day (55 gpm) (flow rate when system is operating, excludes downtime for filter and media changes, for reconfiguration or repositioning, for scheduled and unscheduled maintenance, etc.) with a strontium decontamination factor (DF) of greater than 10. The optimized goal is a DF of 1,000 which will be achieved under a continuous improvement program following further operation, assessment, and adjustment.
The process system is designed for ease of transfer to from one site to another with flexibility for operating in different modes of filtration and ion removal. Top level process requirements for the inlet water specifications are assumed as shown in Table 2.
Top level process requirements for the inlet water specifications are assumed as shown in Table 2.
In an embodiment, the Control/Solids Feed skid 140 (
In an embodiment, the Solids Removal Filter skid 120 (
In an embodiment, the Ultra Filter skid 110 (
Water Remediation
Reverse osmosis (RO) is a water purification technology that uses a semipermeable membrane to remove larger particles from drinking water. In reverse osmosis, an applied pressure is used to overcome osmotic pressure. Reverse osmosis can remove many types of molecules and ions from solutions, including bacteria, and is used in both industrial processes and the production of potable water. The result is that the solute is retained on the pressurized side of the membrane and the pure solvent is allowed to pass to the other side. Reverse osmosis is most commonly known for its use in drinking water purification from seawater, removing the salt and other effluent materials from the water molecules. Reverse Osmosis is well-known in the art of water remediation, both as an overall process and a highly mobile one. Thus, the RO process could be included as a skid within the mobile processing system.
Another remediation process is isotope separation via helical screw conveyer. The helical screw ion exchange (HSIX) system transports media in either a parallel flow or counter-flow configurations wherein the contaminated water is mixed with ion exchange media to facilitate transfer of contaminants from the contaminated water yielding clean water and a contaminant laden slurry to be processed for further disposition. The HSIX system is detailed in U.S. Prov. Pat. App. 62/152,521, which is included in the incorporated documents. The HSIX system may be used in place of, or in combination with, the ISM module, and may be contained in a skid for mobile, modular, and scalable operation similar to other skid system components as previously discussed in the disclosure.
The following is a detail system description of a Pilot skid embodiment comprising:
The Pilot embodiment utilizes a site interface power is 460 V, 3 phase, 50 Hz that is provided to a location near the MPS. Non-potable clean water is provided to the MPS site via hoses for system flushing. Alternatively, clean water output from the system may be rerouted back through for routine flushing of the system. The flush volume will be approximately 1900 L (500 gallons). Mobile cranes will be used in routine production operations to remove and replace filters and ISMs. Process equipment and piping can be arranged to mitigate risk of damage due to incidental contact during these operations and guard rails and/or structures shall be provided if indicated.
The clean water exiting the MPS is sampled at various points throughout the separate modules to ensure that it meets environmental and health standards at the final outlet. Water may be sampled by at least one of manually and automatically. In some embodiments, the clean water is stored in storage tanks on site to await further disposition. In some embodiments the clean water is rerouted back through the system for system flushing operations.
The Mobile Processing System (MPS) design incorporates applicable codes and standards for the real-time processing of radioactive waste. Considerations for the systems design and equipment will meet or exceed:
With a discussion now on materials selection and corrosion resistance, dual certified 316/316L stainless steel was selected for tanks and 316L for piping that will provide containment of tank water being processed. The quick letter water chemistry specification was used to evaluate anticipated bounding levels of chloride, conductivity and ionic content in tank water. 316L was selected because it is rated for use in this environment and is readily available. To further reduce the risk of corrosion the material will be passivated with nitric acid prior to delivery. Pipe spools will have welds cleaned and then the entire pipe spool will be passivated again after fabrication. Tank welds will be individually cleaned and passivated after fabrication.
Pumps will be made from 316L with impellers having a smooth finish that will reduce corrosion. Valve bodies will be composed of CF8M steel that is rated for seawater use. Kamvalok connectors will be composed of CF3M steel that is rated for seawater use.
304L stainless steel will be used for drip pans and structural steel that will not contact tank water. This material provides general environmental corrosion resistance, is readily available and has lower cost than 316/316L.
Considerations for radiation resistance have been incorporated by selecting polymer materials for use in the MPS, these are shown below with published radiation damage thresholds identified. Soft seats are preferred in valves to ensure leak tightness. Hoses were selected for pressure rating, bend radius, weight, and ease of handling. These properties are important to the process, but radiation resistance was emphasized in material selection. Fluoroelastomers (e.g., PTFE, Teflon) are common valve seat materials but were avoided due to their recognized low tolerance to radiation exposure.
Further, structural strength and seismic safety are included in Tables 5, 6, and 7 below.
Since radiation protection is of paramount importance, filters and ISM vessels that accumulate radioactive material are enclosed in shielding. The SRF and UF filters are enclosed in 51 mm of shielding carbon steel and the ISM vessels have 25 mm of carbon steel shielding. Dose rate calculations have been performed and the goal is to limit on-contact dose rates to 5 mSv/hr. Dose calculations were based on a source term two standard deviations above the average source term from characterization data and fully loaded filter cartridges. Calculated dose rates are shown in the table below. Each vessel will have a radiation monitoring probe and operating areas will have general area radiation monitors. Radiation detection will be monitored at both the local control skid and remote monitoring station.
Temperature control for spent SRFs, UFs, and ISM vessels caused by self-heating due to captured Sr-90 along with the result of MPS operation have been considered. The self-heating from the Sr-90 collected in an SRF filter (21.5 watts), the Ultra Filter (249.4 watts), and the ISM vessel (1.3 watts) has been evaluated. When ambient temperature is 40° C., the following results are obtained for the temperature of shielding exposed to ambient air, and for the internal filter canisters in wet and dry storage, and for ISM vessels in dry storage:
When spent filters and ISM vessels are stored in the sun, there is potential for additional heating of external surfaces due to solar radiation. Heating by solar radiation was not included in the above calculations. The precise amount of heating from solar radiation is difficult to assess because it is highly dependent on weather conditions. When incident solar radiation is 700 watts per m2, and there is a moderate wind of 5 m/s, plate metal can heat to 19° C. above ambient temperature. When the wind is 1 m/s, plate metal may heat to 37° C. above ambient air temperature. Similar increases in canister centerline temperature can be expected since the internal heating must now dissipate through the shielding that is solar heated as well as being heated from inside. These temperatures will not compromise the containment boundary provided by the filter canisters or the ISM vessel. The heat from all the Sr-90 stored in the process when water is flowing at 208 L/min will raise the temperature of the water by 0.019° C. When flow is interrupted, the UF canisters heat at 13° C./day and SRF canisters heat at a rate of 0.89° C./day.
Leak Prevention/Environmental Considerations/Safety
The system is designed to prevent leaks, damage to the environment, and injury to on-site operators.
In an embodiment, the system design includes a local control room and communication for remote operations during normal run time and interconnections between MPS units that are integrated into the control system allowing all system operations to be performed by the central control station. Further this allows immediate response to conditions with pump shutdown or failure guaranteeing unit isolation as needed to satisfy leak and radiological protection requirements.
Additional considerations for the pilot embodiment can be made to reduce the radioactive operator dose by installing shield, maintenance frequency reduction, radiation monitoring, and installation of the remote operation.
The design prevents the radioactive material from leaking to the environment; however, should any radioactive material be released from the train, the dam installation, leak detector installation, and piping installed outside the building, etc. has been designed to prevent any leaked radioactive material from defusing, to include leak protection of the joints etc. All process lines between skids consist of hoses with secondary containment for the prevention of spills to the environment. All filter vessels are provided with adequate shielding.
Check valves are used through the system to prevent flow from flowing backwards. Many of the valves are motor operated to allow for quick shutoff or open as necessary to prevent leaks or reduce pressure. All pressure gauges in the system display locally and most display in the control room as well for careful monitoring of system pressure. Pressure relief valves are located in each skid to automatically release pressure when the system pressure exceeds a predetermined value. The motor operated valves are designed to fail as-is, open, or closed depending on their location in the system to minimize damage and environmental hazards in the event of failure. Redundant valves are used throughout the system to provide additional control and increase the factor of safety of the system, again reducing the possibility of leakage to the environment in the event of a failure. Instrument interlocks are used to prevent operators and/or machinery from being harmed in the event of a leak or other failure.
In an embodiment, process equipment and piping can be arranged to mitigate risk of damage due to incidental contact during these operations and guard rails and/or structures shall be provided if indicated. Additionally, seismic resistance is consistent with the full scale MPS system.
Further, the design prevents the retention of flammable gas if such retention is a matter of concern. Hydrogen control is a concern from an explosion hazard; therefore, a hydrogen venting capability is provided. The approach to controlling hydrogen in the MPS is based on dilution to prevent a hydrogen concentration in air from exceeding a lower flammability limit (LFL). When connected to the process system the filters will have vent line with inert gas purge capability to safely vent hydrogen out of the ISO container. For filters in storage calculations and testing of filter characteristics needed to demonstrate that passive venting of the filters will effectively control hydrogen have not been completed. Active venting by forced air circulation similar to the vacuum pumping initially used on the cesium ISM vessels may be required until effectiveness of passive venting is demonstrated.
In an embodiment, the instrumentation and control systems are designed to provide for fully automatic normal operations of the system through the use of fully redundant fault tolerant programmable logic controllers (PLC); any off-normal operations are not automatically controlled, however the system implements a “graceful” shut down with provision for manual intervention at any point in the process cycle. The system design includes a local control room and communication for remote operations during normal run time and interconnections between MPS units that are integrated into the control system allowing all system operations to be performed by the central control station. Further this allows immediate response to conditions with pump shutdown or failure guaranteeing unit isolation as needed to satisfy leak and radiological protection requirements.
Stacking
In some embodiments skids may be stacked on top of other skids to reduce system footprint. The depicted configurations,
Elevated access platforms may be installed to allow disconnect of filters and ISM vessels for replacements, hydrogen venting, sampling, access to the control room, and placement of interconnecting hoses. Crane access may be required for routine operational replacement of solids removal filters, ultra-filters, and ISM vessels. Alternatively, openings in the sidewalls, roofs, and/or floors of the skids, with or without doors, may be provided to afford access to filters and ISM vessels for the purpose of routine operational replacement.
P1. A mobile nuclear waste processing system, the system comprising: a first intermodal shipping container including a main enclosure, an inlet leading into the main enclosure, and an outlet leading out of the main enclosure; a solids removal module disposed within the main enclosure, the solids removal module including a filter configured to receive a flow of fluid and remove at least some solids from the fluid; a first conduit extending through the inlet of the main enclosure and configured to direct the fluid from a fluid supply tank to the solids removal module; a second conduit extending through the outlet of the main enclosure and configured to direct the fluid from the solids removal module out of the main enclosure; and a control system configured to monitor flow of the fluid through solids removal module.
P2. The mobile nuclear waste processing system of paragraph P1, wherein the control system is housed in a second intermodal shipping container.
P3. The mobile nuclear waste processing system of paragraph P1, further comprising an ion specific media module including an ion specific media vessel, the ion specific media module positioned downstream of the solids removal module and configured to receive fluid from the solids removal module.
P4. The mobile nuclear waste processing system of paragraph P3, wherein the ion specific media module is housed in a second intermodal shipping container, and wherein the second conduit extends out of the first intermodal shipping container to direct fluid outside of the first intermodal shipping container and into the second intermodal shipping container.
P5. The mobile nuclear waste processing system of paragraph P3, wherein the first intermodal shipping container includes a secondary enclosure, and wherein the ion specific media module is housed in the second enclosure.
P6. The mobile nuclear waste processing system of paragraph P1, further comprising a feed blend module positioned upstream of the solids removal module, the feed blend module including a feed blend tank configured to receive the fluid and at least one of powdered sorbent and an ion exchange material capable of sorbing at least some contaminants from the fluid.
P7. The mobile nuclear waste processing system of paragraph P6, wherein the feed blend module is housed in a second intermodal shipping container, and wherein the second conduit extends out of the first intermodal shipping container to direct fluid outside of the first intermodal shipping container and into the second intermodal shipping container.
P8. The mobile nuclear waste processing system of paragraph P6, wherein the first intermodal shipping container includes a secondary enclosure, and wherein the feed blend module is housed in the second enclosure.
P9. The mobile nuclear waste processing system of paragraph P1, further comprising a second intermodal shipping container operatively connected to the first intermodal shipping container, the second intermodal shipping container including at least a portion of a wastewater treatment system.
P10. The mobile nuclear waste processing system of paragraph P1, wherein the first intermodal shipping container further includes a pump configured to pump the fluid through at least one of the first conduit and the second conduit.
P11. The mobile nuclear waste processing system of paragraph P1, wherein the first intermodal shipping container further includes at least one of a drain, piping, and a fluid control valve.
P12. The mobile nuclear waste processing system of paragraph P1, wherein the first intermodal shipping container further includes a ventilation system.
P13. The mobile nuclear waste processing system of paragraph P1, wherein the first intermodal shipping container further includes a climate control system for monitoring or regulating the climate inside of the first intermodal shipping container.
P14. The mobile nuclear waste processing system of paragraph P1, wherein the first intermodal shipping container further includes an access platform.
P15. The mobile nuclear waste processing system of paragraph P1, wherein the first intermodal shipping container further includes wheels.
P16. A mobile nuclear waste processing system for removing contaminants from a flow of fluid, the fluid including at least some solid particles, the system comprising: a first mobile container defining a first enclosure; a first filter disposed within the first enclosure of the first mobile container, the first filter configured to receive a flow of fluid and remove at least some solids from the fluid; a second mobile container defining a second enclosure; a second filter disposed within the second enclosure of the second mobile container, the second filter configured to receive the flow of fluid exiting the first filter and remove at least some solids from the fluid, the second filter providing finer filtration than the first filter; a conduit extending between the first mobile container and the second mobile container to transfer fluid from the first mobile container to the second mobile container, the conduit directing the flow of fluid exiting the first filter towards the second filter; and a control system configured to monitor flow of the fluid through the first and second filters.
P17. The mobile nuclear waste processing system of paragraph P16, wherein the first mobile container and the second mobile container are selectively disengagable from one another.
P18. The mobile nuclear waste processing system of paragraph P16, wherein at least one of the first mobile container and the second mobile container is a custom designed enclosure.
P19. The mobile nuclear waste processing system of paragraph P16, wherein at least one of the first mobile container and the second mobile container includes an integral transport power source and wheels to allow the mobile container to be self-transportable.
P20. The mobile nuclear waste processing system of paragraph P16, further comprising a third mobile container, wherein the first, second, and third mobile containers are each selectively couplable to the others of the first, second, and third mobile containers.
P21. The mobile nuclear waste processing system of paragraph P20, wherein the first, second, and third mobile containers are arrangeable into different configurations relative to one another to operate the mobile nuclear waste processing system according to different operational configurations.
P22. The mobile nuclear waste processing system of paragraph P16, further comprising a third mobile container defining a third enclosure and an ion specific media system disposed within the third enclosure, the ion specific media system including an ion specific media vessel.
P23. The mobile nuclear waste processing system of paragraph P16, further comprising a feed blend system positioned upstream of the first filter, the feed blend system including a feed blend tank configured to receive the flow of fluid and at least one of powdered sorbent and an ion exchange material capable of sorbing at least some contaminants from the fluid.
For the sake of convenience, the operations are described as various interconnected functional blocks or distinct software modules. This is not necessary, however, and there may be cases where these functional blocks or modules are equivalently aggregated into a single logic device, program or operation with unclear boundaries. In any event, the functional blocks and software modules or described features can be implemented by themselves, or in combination with other operations in either hardware or software.
Having described and illustrated the principles of the invention in a preferred embodiment thereof, it should be apparent that the invention may be modified in arrangement and detail without departing from such principles. Claim is made to all modifications and variation coming within the spirit and scope of the invention as claimed.
The entire content of each document listed below is incorporated by reference into this document (the documents below are collectively referred to as the “incorporated documents”).
Priority patent documents incorporated by reference:
Additional documents incorporated by reference:
| Number | Date | Country | |
|---|---|---|---|
| 62016517 | Jun 2014 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 16534764 | Aug 2019 | US |
| Child | 17662219 | US | |
| Parent | 14748535 | Jun 2015 | US |
| Child | 15950519 | US |
| Number | Date | Country | |
|---|---|---|---|
| Parent | 15950519 | Apr 2018 | US |
| Child | 16534764 | US |
