The present invention relates to a condenser assembly, which, in some applications, is part of an apparatus for removing liquid from a suspension.
Mixtures of liquids and solids, known as suspensions, present expensive disposal problems to the industries that generate them. Unprocessed suspensions typically cannot be disposed of in landfills due to regulations on water content. Even with more permissive regulations, it is much more expensive to transport and dispose of unprocessed suspensions as compared to solid components because transportation charges and landfill charges correspond to weight.
Additionally, the scope of potential uses of such suspensions is often substantially increased by removal of the liquid component from the solid component. Typically, the value of the dry solids arises from the decrease in weight occasioned by the removal of the liquid fraction, which leads to decreased disposal and transportation costs. The recovered dried solids may also be commercially valuable, such as if they are useable in other industrial and municipal applications (e.g., renewable fuel) or can be sold in secondary markets, such as in the case where the suspensions comprise paper, fiber, coal or mineral slurries.
Unfortunately, efforts to work around the suspension disposal problems often employ methods lacking environmental soundness. For example, many industries dump suspensions, such as waste products, into holding ponds, which are typically large concrete or plastic lined, man-made pools requiring acres of real estate. The suspensions then sit in these holding ponds while the solid materials settle at the bottom over time with the aid of only gravity. Aside from being a slow process, the potential for the pool lining to fail or result in contamination of the surrounding environment makes this a less-than-desirable solution in terms of both efficiency and environmental impact.
Industrial suspension ponds suffer from significant practical difficulties. For instance, holding ponds have a poor resulting yield (dry solid percentage content). Being passive, it also takes a long time to separate water from solids for a given volume of suspension, as compared to devices that rely on active separation. Keeping up with the output for any given suspension flow rate requires a greater area than if active separation systems are used. Two active separation systems, centrifuge processors and belt presses, each produce higher solid content yields than suspension ponds; however, they lack the ability to utilize thermodynamics to achieve 60-100% dry solid percentage yields. These active separation systems are also expensive to purchase and operate, and they are not readily scaled up or down to handle corresponding volumes of industrial suspension flow rates. The lack of portability and limitations on the amount of material which can be processed in a given time are also a significant limiting factor.
Certain drying technologies have been used to further remove water from suspensions processed by belt presses or screw presses. These drying technologies have focused on the use of thermal energy for removing water from the suspensions. For instance, drum dryers have been used; however, the technology is expensive in terms of both capital and operating costs. Belt dryers have also been used and promoted as a way of reducing footprint and costs. However, like drum dryers, belt dryers rely primarily on thermal energy to remove the water from a suspension by use of heat. Using heat to remove water requires large amounts of thermal energy to be available, which significantly adds to the operating costs of drying. In addition, both belt and drum dryers lack the ability of flexible throughputs, and also require large systems and high temperatures to operate.
In one attempt to address such limitations and disadvantages in the prior art, commonly assigned U.S. Pat. No. 9,341,410, which is incorporated herein by reference, describes an apparatus for removing liquid from a suspension. Such an apparatus comprises one or more drying chambers arranged in series. Each such drying chamber defines a substantially enclosed volume in which liquid is extracted from a suspension as it passes through the drying chamber. The apparatus further includes an internal conveyor system comprised of a conveyor belt and one or more rollers for driving the conveyor belt and transporting the suspension through the drying chambers at a substantially continuous speed. Such a conveyor belt is preferably manufactured from a material capable of withstanding the heat and pressure created within the drying chambers without significantly stretching, warping, tearing, or being otherwise rendered useless. Furthermore, the conveyor belt is preferably semi-permeable (i.e., perforated or porous), thus allowing liquids and gases to pass through the conveyor belt, while still supporting solids.
A suspension is loaded onto the conveyor belt at a first end of the conveyor belt. In each of the drying chambers, compressed and heated air is injected and applied in conjunction with a vacuum. In other words, air is pushed into and pulled from each of the drying chambers as the conveyor belt carries the suspension through the drying chambers.
With respect to the injection of air into each of the drying chambers, in some embodiments, air exits a blower and is routed via a hose to an air injection trunk line. Multiple air delivery hoses then connect the air injection trunk line to the lid of each of the drying chambers. In each drying chamber, air is then diffused by and distributed through one or more air distribution plates. The air contacts the suspension carried on the conveyor belt, and the air is then pulled through the suspension and the conveyor belt, exiting through a vacuum pipe. As a result of the application of the vacuum, the air further expands from its compressed state, through atmospheric conditions, into a negative pressure, such that the flow rate is significantly increased as the air passes through the suspension. In short, the positive-pressure injection of air into the drying chambers, combined with the vacuum pressure applied to the drying chambers, creates a pressure differential that causes rapid air expansion and increased air flow through the suspension. This facilitates efficient removal of liquid from the suspension, as there is an element of force drawing the liquid from the suspension, along with heat transfer. Thus, as the air passes through the suspension, the air becomes heavily saturated.
The heavily saturated air is then delivered to a condenser. In the condenser, the air reaches full saturation, and the liquid component (such as water) is drawn from the air as it cools and is collected in a water collection box associated with the condenser.
In some embodiments, the cooled air flows from the condenser back through the drying chambers via a series of pipes. The air is passed through the drying chambers in this manner to preheat and increase the temperature of the air. Such a preheating arrangement thus enables the use of heat that was not absorbed by the suspension to aid in the drying process.
The air is then returned to the blower. The blower again compresses and raises the temperature of the air, and the air is then again directed through the air injection trunk line to multiple air delivery hoses, and then directed into the respective drying chambers. Thus, the air is flowing through the apparatus in a closed loop (i.e., a recirculating air stream), such that the blower is also used to create the vacuum that draws air from each drying chamber.
In the present application, the focus is on the condenser (or condenser assembly) that may be used with such an apparatus for removing liquid from a suspension, or the condenser (or condenser assembly) may be used in other applications for removing a liquid component, such as water, from an air stream.
The present invention is a condenser assembly, which, in some applications, is part of an apparatus for removing liquid from a suspension.
An exemplary apparatus for removing liquid from a suspension made in accordance with the present invention comprises one or more drying chambers in which liquid is extracted from a suspension as it passes through the drying chamber. The apparatus also includes an internal conveyor system comprised of a continuous conveyor belt and one or more rollers for driving the conveyor belt and transporting the suspension continuously through the drying chambers.
In each of the drying chambers, compressed and heated air is injected and applied in conjunction with a vacuum. In other words, air is pushed into and pulled from each of the drying chambers, for example by a blower and vacuum pipe. The blower generates a positive pressure, which injects air into the respective drying chambers. The positive pressure generated by the blower acts to increase the temperature of the air, and it also acts to compress and decrease the volume of air that will be subsequently heated. The blower is also used to create the vacuum that draws air from each drying chamber, and thus, the vacuum pipe is operably connected to the intake of the blower. In other words, the air flows through the apparatus in a closed loop (i.e., a recirculating air stream).
In short, the positive-pressure injection of air into the drying chambers, combined with the vacuum pressure applied to the drying chambers, creates a pressure differential that causes rapid air expansion and acceleration of the air as it passes through the suspension. The expansion and acceleration of the air as it passes through the suspension enables moisture to be removed from the suspension by mass transfer. Accordingly, as the air passes through the suspension, the air becomes heavily saturated.
The heavily saturated air is then evacuated from the respective drying chambers and delivered to a condenser. The condenser assembly is designed to have a larger total volume (i.e., larger total diameter), such that the saturated air reduces its speed while in contact with the chilled surfaces of the condenser. Thus, in the condenser, the air reaches full saturation (100% relative humidity), and the liquid component (such as water) is drawn from the air as it cools. Cooled air then exits the condenser assembly with 100% relative humidity, but at a lower temperature (for example, 100° F.) under the vacuum pressure.
The cooled air flows from the condenser assembly to a blower filter box that provides filtration of the air prior to returning it to the blower. Again, as described above, the air is flowing through the apparatus in a closed loop (i.e., a recirculating air stream), such that the blower is also used to create the vacuum that draws air from each drying chamber. As a result, no exhausting of the air stream is necessary.
An exemplary condenser assembly for use with an apparatus for removing liquid from a suspension and made in accordance with the present invention generally comprises: a main cabinet; a filter frame and associated filters that are moveable between a first (operating) position within the main cabinet and a second (maintenance) position substantially outside of the main cabinet; and a condenser box that is similarly moveable between a first (operating) position within the main cabinet and a second (maintenance) position substantially outside of the main cabinet.
In some embodiments, the main cabinet includes a front wall which defines a first opening associated with the filter frame and a second opening associated with the condenser box. The main cabinet further defines a first interior cavity that is accessible via the first opening, which receives and houses the filter frame and associated filters in the first position. Similarly, the main cabinet also defines a second interior cavity that is accessible via the second opening, which receives and houses the condenser box in the first position.
In some embodiments, a first door selectively closes the first opening, and a second door selectively closes the second opening. In some embodiments, it is preferred that the first door and the second door each have a gasket or similar sealing means around its periphery to seal each door relative to the main cabinet when closed.
In some embodiments, an intermediate panel is positioned within the main cabinet between the first interior cavity and the second interior cavity, and the intermediate panel defines a passageway between the first interior cavity and the second interior cavity. Furthermore, a gasket is preferably positioned on the intermediate panel around the passageway and within the first interior cavity. The gasket is therefore positioned so as to seal the filter frame relative to the intermediate panel when the filter frame is in the first position. As such, in operation, all of the air entering the condenser assembly passes through the filters of the filter frame before entering the second interior cavity and contacting the condenser box.
To facilitate movement of the filter frame between the first position and the second position, in some embodiments, the filter frame includes a plurality of wheels located at the bottom of the filter frame and a guide plate located at the top of the filter frame. When the filter frame is in the first position within the first interior cavity of the main cabinet, the plurality of wheels of the filter frame engage a lower filter guide track located within the first interior cavity, and the guide plate engages an upper filter guide track located within the first interior cavity. However, after opening the door that selectively closes the first opening, a user can move the filter frame and associated filters from the first (operating) position within the first interior cavity of the main cabinet to the second (maintenance) position outside of the main cabinet, with the plurality of wheels facilitating such movement.
In some embodiments, the exemplary condenser assembly further includes a filter roller cart positioned outside of the main cabinet adjacent to the first opening. The filter roller cart includes a vertical support structure which is sized and configured to accept and maintain the filter frame in an upright position when outside of the main cabinet and multiple casters that engage the underlying ground surface.
The condenser box includes a frame and all of the coils and piping necessary for the condensing function and the removal of the liquid component (water) from the saturated air as it cools. In some embodiments, an inner roller conveyer is positioned within the second interior cavity of the main cabinet, which supports the condenser box in the first position. In some embodiments, an exterior roller conveyor extends from the second opening and is positioned outside of the main cabinet. The exterior roller conveyor supports the condenser box in the second position and is supported on multiple legs that engage the underlying ground surface. Thus, by opening the door that selectively closes the second opening, the condenser box can be withdrawn from the main cabinet of the condenser assembly, from the first (operating) position to the second (maintenance) position, over the respective first and second roller conveyors.
The present invention is a condenser assembly, which, in some applications, is part of an apparatus for removing liquid from a suspension.
A suspension is loaded onto the conveyor belt 30 at a first end of the conveyor belt 30, for example, by a sifter 31, which is positioned at the first end of the conveyor belt 30 and meters the suspension onto the conveyor belt 30 while breaking the suspension into small particles (e.g., 2 to 4 millimeters in diameter) to increase the exposed surface area of the suspension being dried and to increase the porosity of the suspension to enable better air flow through the suspension. However, various other means of loading the suspension onto the conveyor belt 30 may be incorporated into the apparatus 10.
In each of the drying chambers 20a, 20b, compressed and heated air is injected and applied in conjunction with a vacuum. In other words, air is pushed into and pulled from each of the drying chambers 20a, 20b. In this exemplary embodiment, air is injected by a blower 66 via a hose 68 and air injection trunk line 60 into each of the drying chambers 20a, 20b. A vacuum pipe 70 then runs along the length of the drying chambers 20a, 20b, with one or more vacuum pipe segments 71 extending from the vacuum pipe 70 into the bottom of each of the drying chambers 20a, 20b, drawing air from the respective drying chambers 20a, 20b.
Referring still to
Referring still to
As a result of the application of the vacuum, the air further expands from its compressed state, through atmospheric conditions, into a negative pressure, such that the actual flow rate is approximately 1101 ACFM as the air passes through the suspension. Such transition of the expanding air occurs in the short distance between the air distribution plate 80 and the conveyor belt 30. In short, the positive-pressure injection of air into the drying chambers 20a, 20b, combined with the vacuum pressure applied to the drying chambers 20a, 20b, creates a pressure differential that causes rapid air expansion and acceleration of the air as it passes through the suspension. The expansion and acceleration of the air as it passes through the suspension enables moisture to be removed from the suspension by mass transfer. By heating the air in a dense state (lower volume), the ideal heat transfer by the heating elements 24a, 24b is also conducted in an efficient manner. Thus, both mass transfer and heat transfer are utilized in an efficient form to remove liquid from the suspension. Accordingly, as the air passes through the suspension, the air becomes heavily saturated, and the relative humidity increases to approximately 84.5% (or higher).
Referring now to
Referring still to
Referring still to
Again, as described above, the air is flowing through the apparatus 10 in a closed loop (i.e., a recirculating air stream), such that the blower 66 is also used to create the vacuum that draws air from each drying chamber 20a, 20b. As a result, no exhausting of the air stream is necessary, which often requires some form of costly permitting. Furthermore, as described above, thermal energy is not wasted as the preheating arrangement enables the use of heat that was not absorbed by the suspension to aid in the drying process.
Although not shown in the Figures, it is, of course, contemplated that an apparatus for removing liquid from a suspension made in accordance with the present invention would include a control system. For example, with respect to the exemplary apparatus 10 described above, such a control system could include a microprocessor with a memory component. A motor associated with the conveyor belt 30 would be operably connected to and receive control signals from the microprocessor. Similarly, the blower 66 would be operably connected to and receive control signals from the microprocessor. The heating elements 24a, 24b, the material sifter 31, and the condenser assembly 100 also would be operably connected to and receive control signals from the microprocessor. Accordingly, each of these components could be operated in response to user input. Furthermore, preprogrammed routines could be stored in the memory component to automate the process. For example, the user may simply have to press a button to activate a preprogrammed routine that operates the components to initiate and carry out a drying process for a particular suspension.
As described above, the condenser assembly 100 included in an apparatus for removing liquid from a suspension has heavily saturated air delivered to the condenser assembly 100 from the drying chambers 20a, 20b. In the condenser assembly 100, the liquid component (such as water) is drawn from the air as it cools and is collected in a water collection box associated with the condenser assembly 100.
Referring now to
The condenser assembly 100 further includes an inlet 117 and an outlet 119 which are operably connected to the respective hoses 73, 75 described above with respect to
Referring still to
As also shown in
Referring now to
Referring now to
Referring now to
Referring now to
Referring now to
Referring now to
Of course, as the liquid component (water) is removed from the saturated air, the condensate falls under the force of gravity to the bottom of the main cabinet 110. Thus, the main cabinet 110 preferably includes a bottom panel 111 which is sloped to direct the condensate toward an outlet (not shown). Furthermore, although not shown in the Figures, the condenser assembly 100 may be equipped with a pumping system that is automatically activated for removal of the condensate, for example, when the condensate level reaches a certain threshold.
Referring now to
As a further refinement, although not shown in the Figures, it is also contemplated that the condenser assembly 100 could include a secondary filter box at or near the inlet 117 for dust and debris collection before saturated air enters the main cabinet 110. It is contemplated that such a secondary filter box could be positioned upstream or downstream of the diffuser 180 shown in
Although not shown in the Figures, as a further refinement, the condenser assembly 100 could also function as a heat exchanger, with heat absorbed from the saturated air passing through the condenser box 150 being used, for example, in combination with or in place of the heating elements 24a, 24b described with respect to
Although not shown in the Figures, as a further refinement, a wash system could be incorporated into the condenser box 150 to clean the filters 142, condenser coils, and/or other components.
Finally, as mentioned above, although the condenser assembly of the present invention is particularly useful as part of an apparatus for removing liquid from a suspension, the condenser assembly of the present invention may also be used in other applications for removing a liquid component, such as water, from an air stream, especially when it would be beneficial to provide ready access to the filters and/or condenser box for maintenance.
One of ordinary skill in the art will also recognize that additional embodiments are also possible without departing from the teachings of the present invention. This detailed description, and particularly the specific details of the exemplary embodiment disclosed therein, is given primarily for clarity of understanding, and no unnecessary limitations are to be understood therefrom, for modifications will become obvious to those skilled in the art upon reading this disclosure and may be made without departing from the spirit or scope of the present invention.
The present application claims priority to U.S. Patent Application Ser. No. 62/289,425 filed on Feb. 1, 2016, the entire disclosure of which is incorporated herein by reference.
Number | Name | Date | Kind |
---|---|---|---|
2742708 | McCormick | Apr 1956 | A |
3673822 | Fleissner | Jul 1972 | A |
3685167 | Loveday | Aug 1972 | A |
3693382 | Grantham | Sep 1972 | A |
3941425 | Reichl | Mar 1976 | A |
4991912 | Fox | Feb 1991 | A |
5565112 | Bratten | Oct 1996 | A |
5632097 | Snitchler | May 1997 | A |
6105273 | Johanson | Aug 2000 | A |
6233841 | Beach | May 2001 | B1 |
6901990 | Howard | Jun 2005 | B2 |
7600460 | Manders | Oct 2009 | B2 |
7644515 | Doh | Jan 2010 | B2 |
7694432 | Eriksson | Apr 2010 | B2 |
7749395 | Griffin | Jul 2010 | B2 |
7987616 | Bae | Aug 2011 | B2 |
8181359 | Bae | May 2012 | B2 |
8673156 | Griffin | Mar 2014 | B2 |
8726533 | Cai | May 2014 | B2 |
8789287 | Kim | Jul 2014 | B2 |
8806771 | Holmes | Aug 2014 | B2 |
8991140 | Dorn | Mar 2015 | B2 |
9341410 | Griffin | May 2016 | B1 |
20140161680 | Kantor | Jun 2014 | A1 |
20140263769 | Lakhmiri | Sep 2014 | A1 |
Number | Date | Country |
---|---|---|
84 37 357.1 | Mar 1985 | DE |
WO 2010039250 | Apr 2010 | WO |
Number | Date | Country | |
---|---|---|---|
62289425 | Feb 2016 | US |