MATERIAL RECYCLING APPARTUS
20210101192 · 2021-04-08
Inventors
Cpc classification
F23J15/04
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F23J15/022
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F23J2700/001
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B01D50/40
PERFORMING OPERATIONS; TRANSPORTING
F23J2900/13004
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B01D46/0027
PERFORMING OPERATIONS; TRANSPORTING
B09B3/00
PERFORMING OPERATIONS; TRANSPORTING
F23G5/027
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
B09B3/40
PERFORMING OPERATIONS; TRANSPORTING
F23J2217/50
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
F23J2217/20
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
International classification
B09B3/00
PERFORMING OPERATIONS; TRANSPORTING
B01D46/00
PERFORMING OPERATIONS; TRANSPORTING
B01D50/00
PERFORMING OPERATIONS; TRANSPORTING
F23J15/02
MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
Abstract
Thermal treatment techniques for recycling are generally very clean but their byproducts include a fine ash that may become entrained in the exhaust air plume as smoke. We therefore disclose a materials recycling apparatus comprising a heat treatment chamber for processing the material at an elevated temperature, the chamber having a vent leading via a heat exchanger to a scrubber comprising a disrupted flow path, at least one spray nozzle directed towards the disrupted flow path, and a supply of liquid (ideally water with a little detergent) to the or each spray nozzle. In this way, the entrained ash can be efficiently removed from the air flow, allowing it to be vented, and the captured ash disposed of via a waste water outlet together with the ash washed from the chamber. The flow path can be disrupted by at least one baffle plate, ideally with the spray nozzle located ahead of the baffle plate(s). Thermal treatment techniques for recycling are generally very clean but their byproducts include a fine ash that may become entrained in the exhaust air plume as smoke. We therefore disclose a materials recycling apparatus comprising a heat treatment chamber for processing the material at an elevated temperature, the chamber having a vent leading via a heat exchanger to a scrubber comprising a disrupted flow path, at least one spray nozzle directed towards the disrupted flow path, and a supply of liquid (ideally water with a little detergent) to the or each spray nozzle. In this way, the entrained ash can be efficiently removed from the air flow, allowing it to be vented, and the captured ash disposed of via a waste water outlet together with the ash washed from the chamber. The flow path can be disrupted by at least one baffle plate, ideally with the spray nozzle located ahead of the baffle plate(s).
Claims
1. A materials recycling apparatus comprising a heat treatment chamber for processing the material at an elevated temperature, the chamber having a vent leading via a heat exchanger to a scrubber comprising a disrupted flow path, at least one spray nozzle directed towards the disrupted flow path, and a supply of liquid to the or each spray nozzle.
2. The materials recycling apparatus according to claim 1 in which the flow path is disrupted by at least one baffle plate.
3. The materials recycling apparatus according to claim 2 in which the spray nozzle is located ahead of the baffle plate.
4. The materials recycling apparatus according to claim 2 in which the spray nozzle is located above and in front of the baffle plate.
5. The materials recycling apparatus according to claim 2 in which the flow path is disrupted by two or three baffle plates.
6. The materials recycling apparatus according to claim 5 in which a spray nozzle is located ahead of each baffle plate.
7. The materials recycling apparatus according to claim 5 in which a spray nozzle is located above and in front of each baffle plate.
8. The materials recycling apparatus according to claim 2 in which the scrubber includes a floor section below the flow path, and the lower edge of each baffle is spaced from the floor section along at least a part of that edge.
9. The materials recycling apparatus according to claim 8, further comprising a drain allowing escape of the liquid from the scrubber from a level which is a preset distance above the internal level of the floor, wherein the lower edges of the baffles are spaced from the floor by distances that are alternately greater than and less than the preset distance, and the baffles whose lower edges are spaced from the floor by less than the preset distance have an upper edge that is spaced from a roof section of the scrubber along at least a part of that upper edge.
10. The materials recycling apparatus according to claim 9 in which the drain comprises a conduit that extends upwardly through the floor with an open end standing proud of the floor by the preset distance.
11. The materials recycling apparatus according to claim 1 in which the flow path of the scrubber is generally upwards from a scrubber inlet toward a scrubber outlet.
12. The materials recycling apparatus according to claim 2 in which the flow path of the scrubber is generally upwards from a scrubber inlet toward a scrubber outlet, and the at least one baffle plates are located above the scrubber inlet.
13. The materials recycling apparatus according to claim 12 in which the baffle plates comprise apertures defining a flow path that is non-aligned with the scrubber inlet.
14. The materials recycling apparatus according to claim 12 in which the spray nozzles are provided on an underside of the or each baffle plate.
15. The materials recycling apparatus according to claim 11 in which the spray nozzles are directed in a downwards direction.
16. The materials recycling apparatus according to claim 1 in which the liquid is water or water-based.
17. The materials recycling apparatus according to claim 1 in which the liquid is water containing a detergent composition.
18. The materials recycling apparatus according to claim 1 in which the flow path is disrupted in that it does not comprise a straight line path.
19. The materials recycling apparatus according to claim 1 in which the flow path includes at least one filter.
20. The materials recycling apparatus according to claim 19 in which the filter is located after the spray nozzle or nozzles.
21. The materials recycling apparatus according to claim 20 in which the scrubber comprises a housing divided longitudinally by a dividing wall, the housing having an inlet located on one side of the dividing wall, and an aperture in the dividing wall, wherein the inlet receives gas flow from the vent, the disrupted flow path leads from the inlet to the aperture, and the filter is located on the opposite side of the dividing wall.
Description
BRIEF DESCRIPTION OF THE DRAWINGS
[0017] An embodiment of the present invention will now be described by way of example, with reference to the accompanying figures in which;
[0018]
[0019]
[0020]
[0021]
[0022]
[0023]
[0024]
[0025]
[0026]
[0027]
[0028]
[0029]
[0030]
[0031]
[0032]
[0033]
[0034]
[0035]
[0036]
DETAILED DESCRIPTION OF THE EMBODIMENTS
[0037]
[0038] Towards the upper end of the chamber 14, a selectively-openable exhaust port 24 allows the interior of the chamber 14 to be vented after a heat treatment. A corresponding inlet (not shown) allows cool air in to displace the hot atmosphere within the chamber 14. After leaving via the exhaust 24, the hot air enters a heat exchanger 26 which transfers the heat of the exhaust gas to water from a hot water storage tank (not shown) which is pumped to the heat exchanger via an inlet pipe 28 and back to the hot water tank via an outlet pipe 30. Thus, the process heat is reclaimed and is available subsequently in the form of a hot water supply to the premises. A condensate drain 32 for water collected within the heat exchanger from the exhaust gas is provided, and connects to the drain hose 22 via pipework 34. The cooled exhaust gases released by the heat exchanger 26 are then passed to a scrubber 36 before being released via a suitable flue.
[0039] The scrubber 36 is shown in
[0040] Within the first interior space there are three internal baffle plates 48, 50, 52. The first internal baffle plate 48 extends downwardly from the upper roof section of the first interior space, proximate the inlet aperture 40, but ends short of the lower floor section of the interior space. Thus, gases entering the first interior space via the inlet aperture 40 (at the upper end of the housing 38) must first travel downward in order to pass under the first baffle plate 48. The second baffle plate 50 is located after the first baffle plate 48 and also extends generally vertically, but has a space between it and both the roof and floor sections. The gap between the second baffle plate 50 and the roof section is generally the same as that between the first baffle plate 48 and the floor section and allows gases to flow past. The gap between the second baffle plate 50 and the floor section is less than that between the first baffle plate 48 and the floor section, and is sealed against gas flow as will be described later.
[0041] Finally, the third internal baffle plate 52 lies behind the second internal baffle plate 50 and, like the first internal baffle plate 48 it extends downwardly from the roof section towards the floor but with a gap between it and the floor section. The gap is similar to that that between the first internal baffle plate 48 and the floor, and more than that between the second internal baffle plate 50 and the floor. Thus, in use a gas must flow downwardly to pass below the first internal baffle plate 48, then upwardly to pass above the second internal baffle plate 50, then downwardly to pass below the third internal baffle plate 52, then upwardly to reach the internal aperture 46 and enter the second interior space.
[0042] A total of four spray nozzles 54, 56, 58, 60 are set into the roof section of the housing 38 and create a downwardly-directed fine spray within the first interior space. They are supplied with liquid by a supply pipe 62. The first nozzle 54 is located above and in front of the first internal baffle plate 48, and thus creates a spray between it and the inlet aperture 40. The second nozzle 56 is located above and between the first internal baffle plate 48 and the second internal baffle plate 50, and thus creates a spray between the two baffle plates. The third nozzle 58 is likewise located above and between the second internal baffle plate 50 and the third internal baffle plate 52. Finally, the fourth nozzle 60 is located above and behind the third internal baffle plate 52. As a result, gas flowing along the circuitous path around the baffle plates is thoroughly doused with the spray, removing smoke particulates.
[0043] Alternatively, the spray nozzles may be provided in a side section of the housing to provide a horizontally-directed fine spray.
[0044] A scrubber drain 64 is provided in the floor section of the housing 38 and allows liquid from the nozzles to escape. This takes the form of a drain pipe leading to a U-bend formation 66. The drain pipe passes through the floor section of the housing 38 and has an open end 70 that is spaced from the floor section, i.e. the pipe 64 stands proud of the floor within the first interior space. Thus, the liquid must collect to a preset depth before it can escape via the drain 64. This preset depth, determined by the amount that the drain pipe 64 stands proud of the floor section, is set as being slightly greater than the spacing between the second internal baffle plate 50 and the floor but less than the spacing between the first and third internal baffle plates 48, 52 and the floor. Thus, the liquid in the base of the first interior space seals the lower end as the second internal baffle plate 50 as noted above, but allows gas flow past the first and third internal baffle plates 48, 52.
[0045] In practice, as will be illustrated, a larger or smaller number of nozzles and/or baffle plates can be provided, as necessary in view of the characteristics of the thermal treatment process in question.
[0046] The liquid supplied to the nozzles should be one that is compatible with a domestic waste water drain, so that it can be safely and legally flushed away. Water is a convenient choice, so water or a water-based composition will be ideal. We have found that a solution of a detergent composition is ideal. This reduces the surface tension in the liquid thereby allowing a finer spray that is more apt for collecting entrained particulates. It also assists in mixing the oily residues entrained in the exhaust gases with the water base, leaving an outflow that is easy to flush and which has less odour.
[0047] A suitable composition for this purpose is up to about 50m1 of a domestic washing composition such as Persil® Bio Washing Powder (available from Unilever NV) per litre of water. We prefer a weak solution, however, as a concentration of around 20 ml per litre or less is still effective and will consume less detergent. Higher concentrations will generally work, but are unnecessary and therefore wasteful. Other detergent compositions can be expected to work, but we especially prefer household detergents as they are tested and accepted in the home as a known product.
[0048]
[0049]
[0050]
[0051]
[0052] In other variants, the scrubber unit can be mounted in other orientations. The above embodiments share a horizontal orientation but a vertical orientation is also possible and can be advantageous in slowing the passage of the smoke through the unit, giving the spray nozzles more time to work. In a vertical orientation, the drain is still located at the base but need not be designed so as to cover the base of any baffle plates.
[0053]
[0054] The upwardly-moving air must then pass through a series of three baffle plates 108, 110, 112. A greater or lesser number of baffle plates (for example one, two or four) could be provided but we find that three is a convenient number. Each contains a plurality of apertures, as will be explained below. The apertures can be located in the baffle plates so that they are not aligned with each other, thus forcing the airflow to adopt a disrupted path.
[0055] Each baffle plate 108, 110, 112 contains a fluid conduit 114 which is supplied by a fluid supply 116. The fluid conduit 114 leads to a spray nozzle 118 located on the underside of the baffle plate. This is directed downwards towards the airflow passing through the baffle plate. Thus, fluid from the supply 116 passes through the conduit and is sprayed into the oncoming airflow. The fluid may be as described above, i.e. water or water-based, such as a mild detergent solution.
[0056] In an alternative arrangement, the spray nozzles and/or the fluid supply and conduits may be separate from the baffle plates and mounted in the airflow.
[0057] After passing through the baffle plates, the airflow meets a collector plate 120. This has a single through-aperture 122 allowing the airflow to pass through upwards into an optional cyclone structure that is intended to remove entrained water and oils from the airflow. The through-aperture 122 leads to an upwardly-directed exhaust conduit 123 which ends with a nozzle 124 which directs the airflow tangentially around a central outlet pipe 126. This leads from a point just above the collector plate 120, upwards substantially concentrically within the main body 100, through the upper end cap 102 and away. It defines, together with the main body 100, an into which the airflow is directed, at an elevated flow rate due to the nozzle 124, in a tangential direction. This forces the airflow to adopt a helical flow path around the pipe 128 and downwardly along the annular passage 128. Eventually it reaches the base of the outlet pipe 126 just above the collector plate 120, from where it can escape via the pipe 126. The helical nature of the path will fling entrained water and oils out of the airflow, allowing them to drop into the collector plate, from which they can escape via a drain 130.
[0058] The cyclone structure, i.e. the collector plate 120 and the parts above it, is optional in that it can be omitted in favour of a cyclone located elsewhere, or an alternative structure, or a simple vent. Omitting this form of cyclone will reduce the overall height of the scrubber 100 and may therefore be advantageous, depending on the packaging limitations under which the overall apparatus needs to be designed. If omitted, a simple end cap with an exhaust aperture or conduit can be provided instead.
[0059]
[0060] Finally,
[0061] The exhaust conduit 123 extends from the floor of the collector plate 120 and upwardly so as to sit within the annular passage 128. It communicates with the space below the collector plate 120, to allow the airflow past the collector plate 120 but prevent fluid in the collector plate from draining downwardly. The upper end of the conduit 123 ends with a series of bends to direct the output substantially tangentially within the annular space 128; ideally it also directs the airflow roughly horizontally. A nozzle 124 at the end of the conduit 123 serves to accelerate the airflow and establish a cyclone effect within the annular space.
[0062] Also, the drains 64, 130 can direct liquid into a storage tank for the scrubber unit, with a pump that pumps the liquid (e.g. water with detergent) to the spray nozzles creating a closed circuit during use. When the scrubber cycle is complete, for example after one or more heat treatment cycles, the liquid can be disposed of. It can be released or pumped out of the tank and into the waste water outlet, or the storage tank can be manually removed and emptied. The tank can then be refilled with fresh liquid, either made up ex tempore or from a supply of premixed fluid.
[0063] It will of course be understood that many other variations may be made to the above-described embodiment without departing from the scope of the present invention.