METHOD OF TREATMENT USING A SOLID PARTICULATE MATERIAL AND APPARATUS THEREFOR

Abstract

A method of treating a substrate with a solid particulate material and a treatment liquor comprising: agitating the substrate with said solid particulate material and said treatment liquor; and (a) separating the substrate from effluent comprising solid waste fragments derived from the substrate, said solid particulate material and the treatment liquor; (b) transferring said effluent to a hydrocyclone separator comprising an inlet, a first outlet and a second outlet, wherein the effluent is fed into the hydrocyclone separator via the inlet; (c) separating the effluent in the hydrocyclone separator to produce a first stream and a second stream, wherein the first stream comprises said solid particulate material and exits the hydrocyclone separator via the first outlet and wherein the second stream comprises treatment liquor and solid waste fragments and exits the hydrocyclone separator via the second outlet; and (d) collecting the first stream after it exits the hydrocyclone separator via the first outlet.

Claims

1. A method of treating a substrate with a solid particulate material and a treatment liquor comprising: agitating the substrate with said solid particulate material and said treatment liquor; and (a) separating the substrate from effluent comprising solid waste fragments derived from the substrate, said solid particulate material and the treatment liquor; (b) transferring said effluent to a hydrocyclone separator comprising an inlet, a first outlet and a second outlet, wherein the effluent is fed into the hydrocyclone separator via the inlet; (c) separating the effluent in the hydrocyclone separator to produce a first stream and a second stream, wherein the first stream comprises said solid particulate material and exits the hydrocyclone separator via the first outlet and wherein the second stream comprises treatment liquor and solid waste fragments and exits the hydrocyclone separator via the second outlet; and (d) collecting the first stream after it exits the hydrocyclone separator via the first outlet.

2. The method of claim 1 wherein said first stream comprises said solid particulate material as a major fraction and further comprises a minor fraction which is treatment liquor, preferably wherein the first stream comprises at least 70% wt, preferably at least 80% wt, preferably at least 90% wt, preferably at least 95% wt of said solid particulate material by total weight of the first stream.

3. The method of claim 1 or 2 wherein said first stream comprises said solid particulate material as a major fraction and further comprises a minor fraction which is residual solid waste fragments derived from the substrate, preferably wherein the first stream comprises at least 70% wt, preferably at least 80% wt, preferably at least 90% wt, preferably at least 95% wt of said solid particulate material by total weight of the first stream.

4. The method of any of claims 1 to 3, further comprising re-using the collected first stream in a method of treating a substrate with solid particulate material and a treatment liquor.

5. The method of any of claims 1 to 3, further comprising recirculating the collected first stream into the hydrocyclone separator and repeating steps (c) and (d) one or more times, optionally wherein said first stream is combined with a liquid diluent prior to introduction of the first stream into the hydrocyclone separator such that where the recirculating of the first stream is conducted a plurality of times said first stream may be combined with said liquid diluent in each recirculation step or in only one or some of said recirculation steps, preferably wherein said liquid diluent is or comprises a recycled liquid stream derived from said second stream exiting the hydrocyclone separator and/or wherein said liquid diluent is or comprises a recycled liquid stream derived from a cleaning liquid effluent exiting a further cleaning stage of the solid particulate material, and wherein said recirculation provides cleaned solid particulate material and said method further comprises re-using the cleaned solid particulate material in a method of treating a substrate with solid particulate material and a treatment liquor

6. The method of any of claims 1 to 3, further comprising transferring the collected first stream to a secondary cleaning apparatus for further cleaning of the solid particulate material, wherein said cleaning removes from said solid particulate material some or substantially all of the residual solid waste fragments derived from the substrate.

7. The method of claim 6, wherein the secondary cleaning apparatus comprises a secondary separator configured to allow water, said residual solid waste fragments and any treatment liquor and/or any liquid cleaning formulation to pass through the secondary separator, and wherein cleaning of said solid particulate material comprises retaining said solid particulate material on the surface of said secondary separator and: (i) directing a liquid cleaning formulation onto said solid particulate material whilst it is retained on the surface of said secondary separator; and/or (ii) agitating said solid particulate material whilst it is retained on the surface of said secondary separator.

8. The method of claim 7, wherein the secondary separator is planar and comprises multiple apertures therein, the apertures of the secondary separator being sized such that the apertures are smaller than the smallest dimension of the solid particulate material, preferably wherein the apertures have a smooth perimeter, preferably wherein the secondary separator is a non-woven mesh or perforated sheet.

9. The method of claim 7 or 8, wherein the liquid cleaning formulation is an aqueous cleaning formulation, optionally comprising a cleaning agent.

10. The method of claim 7, 8 or 9, said agitating of the solid particulate material on the secondary separator comprises vibrating the secondary separator or rotating the secondary separator or subjecting the secondary separator to a reciprocating motion or linear motion in a single direction, preferably wherein said agitating comprises vibrating the secondary separator, and preferably wherein the secondary cleaning apparatus comprises a vibratory separator.

11. The method of any of claims 7 to 10 wherein the secondary separator is substantially circular or elliptical, preferably substantially circular.

12. The method of any of claims 7 to 11 wherein the secondary separator is associated with an access means configured to remove the solid particulate material which is unable to pass through the secondary separator.

13. The method of any of claims 6 to 12, wherein the secondary cleaning apparatus provides cleaned solid particulate material and a secondary cleaning effluent and wherein the secondary cleaning effluent is a secondary cleaning liquid effluent the method further comprises the step of recycling said secondary cleaning liquid effluent to the hydrocyclone separator and/or to the secondary cleaning apparatus to further treat said solid particulate material, wherein said secondary cleaning liquid effluent may comprise any treatment liquor present in the first stream and/or any liquid cleaning formulation used in the secondary cleaning apparatus.

14. A method according to claim 13 wherein the step of recycling said secondary cleaning liquid effluent is effected after removal of some or all residual solid waste fragments from the secondary cleaning liquid effluent by passing the secondary cleaning liquid effluent through a first fine grading separator to remove some or all of the residual solid waste fragments from the secondary cleaning liquid effluent to provide a secondary cleaning filtrate stream, such that the secondary cleaning liquid effluent is recycled as the secondary cleaning filtrate stream.

15. A method according to claim 14 wherein the first fine grading separator has apertures sized to allow liquid to pass through but prevents substantially all of said residual solid waste fragments from passing through.

16. A method according to claim 14 or 15 wherein the secondary separator and the first fine grading separator are comprised in a multilayer separating apparatus, wherein the multilayer separating apparatus is configured so that any material to be separated is exposed to the secondary separator before it is exposed to the first fine grading separator.

17. The method of any of claims 6 to 16, further comprising re-using the cleaned solid particulate material in a method of treating a substrate with solid particulate material and a treatment liquor.

18. The method of any preceding claim, further comprising collecting the second stream after it exits the hydrocyclone separator via the second outlet and transferring the second stream to a filtration apparatus that allows treatment liquor to pass through the filtration apparatus but which prevents said solid waste fragments from passing through the filtration apparatus, providing a first filtrate stream comprising treatment liquor and a first residue comprising said solid waste fragments.

19. The method of claim 15, further comprising recycling the first filtrate stream to the feed stream introduced to the hydrocyclone separator wherein the first filtrate stream is added to the feed stream prior to introduction of the feed stream into the hydrocyclone separator.

20. The method of claim 18 or 19 wherein said filtration apparatus has a single filtration layer or has a plurality of filtration layers, and is preferably selected from single layered or multi-layered sieves and filters, and from self-cleaning filters.

21. The method of any of the preceding claims, further comprising a step of pre-treating the effluent prior to transferring the effluent to the hydrocyclone separator, wherein the pre-treating of the effluent comprises removing solid waste fragments of a size substantially larger than said solid particulate material.

22. The method of claim 21 wherein said pre-treating is performed in a coarse grading separator configured to allow the solid particulate material to pass through but to prevent material of a size substantially larger than said solid particulate material from passing through.

23. The method of any preceding claim further comprising the step of controlling the ratio of solid particulate material:liquid in the hydrocyclone, preferably wherein the stream fed into the hydrocyclone has a solid particulate material:liquid ratio in the range of from about 1.0:0.1 to about 1.0:10, preferably wherein said ratio is in the range of from about 1.0:0.5 to about 1.0:5.0.

24. The method of claim 23 wherein the ratio of solid particulate material:liquid is controlled by a flow regulator and/or by addition of a liquid diluent to the hydrocyclone and preferably by the addition of a liquid diluent to the stream fed into the hydrocyclone.

25. The method of claim 24 wherein said liquid diluent is or comprises one or more recycled liquid stream(s) derived from said first stream and/or said second stream and/or wherein said liquid diluent is or comprises one or more recycled liquid stream(s) derived from any cleaning of the solid particulate material downstream of the hydrocyclone separator.

26. The method of any of the preceding claims, wherein the first outlet is an underflow of the hydrocyclone separator and the second outlet is an overflow of the hydrocyclone separator.

27. The method of any of preceding claim, wherein the substrate is an animal skin substrate or a textile fibre or fabric.

28. The method of any of claims 1 to 27, which is a method of cleaning the substrate.

29. The method of any of claims 1 to 26, wherein the substrate is an animal skin substrate, preferably a hide or pelt.

30. The method of claim 29 wherein the method of treating the substrate is a tannery process, preferably selected from colouring,curing, beamhouse treatments, pre-tanning tanning, re-tanning, fat liquoring, enzyme treatment, tawing, crusting, dyeing and dye fixing, preferably wherein said beamhouse treatments are selected from soaking, liming, deliming, reliming, unhairing, fleshing, bating, degreasing, scudding, bating, pickling and depickling.

31. The method of any of the preceding claims, wherein the solid waste fragments derived from the substrate are fibrous and/or particulate.

32. The method of any preceding claim, wherein the solid particulate material comprises polymeric particles having a density of at least about 1.0 g/cm.sup.3 and no more than about 8.0 g/cm.sup.3, preferably in the range of from about 1.5 to about 2.5 g/cm.sup.3.

33. The method of any preceding claim, wherein the particles of the solid particulate material exhibit an average mass of from about 1 mg to about 3000 mg, and/or a surface area of from about 10 mm.sup.2 to about 1000 mm.sup.2, and/or an average volume in the range of from about 5 to about 500 mm.sup.3, and/or an average particle diameter of from about 1 mm to about 200 mm, and/or a length of from about 1 mm to about 200 mm wherein said length is the maximum two-dimensional length of each three-dimensional solid particle.

34. The method of any of the preceding claims, wherein said effluent from step (a) is pumped from a collection vessel to the hydrocyclone separator.

35. A method of cleaning solid particulate material recovered from a substrate treatment process, preferably an animal skin substrate treatment process, in which said substrate had been treated with said solid particulate material and a treatment liquor, the method of cleaning the recovered solid particulate material comprising (a) transferring effluent comprising solid waste fragments derived from the substrate, said solid particulate material and the treatment liquor to a hydrocyclone separator comprising an inlet, a first outlet and a second outlet, wherein the effluent is fed into the hydrocyclone separator via the inlet; (b) separating the effluent in the hydrocyclone separator to produce a first stream and a second stream, wherein the first stream comprises said solid particulate material and exits the hydrocyclone separator via the first outlet and wherein the second stream comprises treatment liquor and solid waste fragments and exits the hydrocyclone separator via the second outlet; and (c) collecting the first stream after it exits the hydrocyclone separator via the first outlet.

36. The method of claim 35 wherein said method is performed as defined in any of claims 2 to 34.

37. An apparatus for treating a substrate with a solid particulate material and a treatment liquor, the apparatus comprising: a rotatably mounted drum for containing the substrate, the solid particulate material and the treatment liquor; an opening in the rotatably mounted drum; a closure movable between a closed position at which the closure prevents the substrate, the solid particulate material, the treatment liquor and solid waste fragments derived from said substrate passing through the opening and an open position at which the substrate, the solid particulate material, the treatment liquor and the solid waste fragments can pass through the opening; a collection vessel configured to capture the substrate, the solid particulate material, the treatment liquor and the solid waste fragments that pass through the opening; a hydrocyclone separator comprising an inlet, a first outlet and a second outlet; a first flow pathway between the collection vessel and the hydrocyclone separator, wherein the substrate is unable to exit the collection vessel along the first flow pathway; a conveying means configured to convey effluent comprising the solid particulate material, the treatment liquor and the solid waste fragments along the first flow pathway to the inlet of the hydrocyclone separator; wherein the hydrocyclone separator is configured to separate the effluent to produce a first stream and a second stream, wherein the first stream comprises said solid particulate material and exits the hydrocyclone separator via the first outlet and wherein the second stream comprises treatment liquor and solid waste fragments and exits the hydrocyclone separator via the second outlet.

38. The apparatus of claim 37 wherein said conveying means is a pump configured to convey said effluent along the first flow pathway to the inlet of the hydrocyclone separator.

39. The apparatus of claim 37 or 38 wherein said first stream comprises said solid particulate material as a major fraction and further comprises a minor fraction which is treatment liquor and/or a minor fraction which is residual solid waste fragments derived from the substrate.

40. The apparatus of any of claims 37 to 39 further comprising a re-use pathway configured to return the first stream to a rotatably mounted drum in an apparatus for treating a substrate with a solid particulate material and a treatment liquor, said apparatus comprising said rotatably mounted drum for containing the substrate, the solid particulate material and the treatment liquor.

41. The apparatus of any of claims 37 to 39, further comprising a recirculation pathway configured to recirculate the first stream into the hydrocyclone separator.

42. The apparatus of claim 41 further comprising means for combining said first stream with a liquid diluent prior to introduction of said first stream into the hydrocyclone separator, preferably wherein said liquid diluent is or comprises a recycled liquid stream derived from said second stream exiting the hydrocyclone separator and/or wherein said liquid diluent is or comprises a recycled liquid stream derived from a liquid effluent exiting a further cleaning stage of the solid particulate material.

43. The apparatus of claim 41 or 42 further comprising collecting means configured to collect solid particulate material which has been recirculated at least once via said recirculation pathway, wherein said apparatus further comprises a re-use pathway configured to return said cleaned solid particulate material to a rotatably mounted drum in an apparatus for treating a substrate with a solid particulate material and a treatment liquor, said apparatus comprising said rotatably mounted drum for containing the substrate, the solid particulate material and the treatment liquor.

44. The apparatus of any of claims 37 to 39, further comprising a first stream transfer pathway configured to transfer the first stream to a secondary cleaning apparatus which is configured to remove from said solid particulate material some or substantially all of the residual solid waste fragments derived from the substrate.

45. The apparatus of claim 44, wherein the secondary cleaning apparatus comprises a secondary separator configured to allow water, said residual solid waste fragments and any treatment liquor and/or any liquid cleaning formulation to pass through the secondary separator, and wherein said secondary separator is configured to retain said solid particulate material on the surface of said secondary separator and further configured to: (i) direct a liquid cleaning formulation onto said solid particulate material whilst it is retained on the surface of said secondary separator; and/or (ii) agitate said solid particulate material whilst it is retained on the surface of said secondary separator.

46. The apparatus of claim 45, wherein the secondary separator is planar and comprises multiple apertures therein, the apertures of the secondary separator being sized such that the apertures are smaller than the smallest dimension of the solid particulate material, preferably wherein the apertures have a smooth perimeter, preferably wherein the secondary separator is a non-woven mesh or perforated sheet, preferably wherein the secondary separator is substantially circular or elliptical, preferably substantially circular.

47. The apparatus of claim 45 or 46 configured to agitate the solid particulate material on the secondary separator by vibrating the secondary separator or rotating the secondary separator or subjecting the secondary separator to a reciprocating motion or linear motion in a single direction, preferably wherein the secondary cleaning apparatus comprises a vibratory separator.

48. The apparatus of claim 45, 46 or 47 wherein the secondary separator is associated with an access means configured to remove the solid particulate material which is unable to pass through the secondary separator.

49. The apparatus of any of claims 44 to 48, wherein the apparatus comprises a first recycle pathway configured to recycle secondary cleaning liquid effluent from the secondary cleaning apparatus to the hydrocyclone separator and/or to the secondary cleaning apparatus to further treat said solid particulate material.

50. The apparatus of claim 49 further comprising a first fine grading separator to remove some or all of the residual solid waste fragments from the secondary cleaning liquid effluent to provide a secondary cleaning filtrate stream, wherein the first fine grading separator is configured such that recycling of said secondary cleaning liquid effluent is effected after removal of some or all residual solid waste fragments from the secondary cleaning liquid effluent, such that the secondary cleaning liquid effluent is recycled as the secondary cleaning filtrate stream.

51. The apparatus of claim 50 wherein the first fine grading separator has apertures sized to allow liquid to pass through but prevents substantially all of said residual solid waste fragments from passing through.

52. The apparatus of claim 50 or 51 wherein the secondary separator and the first fine grading separator are comprised in a multilayer separating apparatus, wherein the multilayer separating apparatus is configured so that any material to be separated is exposed to the secondary separator before it is exposed to the first fine grading separator.

53. The apparatus of any of claims 44 to 52, wherein said apparatus further comprises a re-use pathway configured to return said cleaned solid particulate material to a rotatably mounted drum in an apparatus for treating a substrate with a solid particulate material and a treatment liquor, said apparatus comprising said rotatably mounted drum for containing the substrate, the solid particulate material and the treatment liquor.

54. The apparatus of any of claims 37 to 53, further comprising a second stream transfer pathway to transfer the second stream to a filtration apparatus that allows treatment liquor to pass through the filtration apparatus but which prevents said solid waste fragments from passing through the filtration apparatus, providing a first filtrate stream comprising treatment liquor and a first residue comprising said solid waste fragments.

55. The apparatus of claim 54, further comprising a first filtrate recycle pathway to recycle the first filtrate stream to the hydrocyclone separator, preferably via said inlet.

56. The apparatus of claim 54 or 55 wherein said filtration apparatus is selected from single layered or multi-layered sieves or filters, optionally wherein the filtration apparatus is or comprises a self-cleaning filter.

57. The apparatus of any of claims 37 to 56, further comprising a pre-treatment means to pre-treat the effluent prior to transferring the effluent to the hydrocyclone separator, wherein the pre-treatment means removes solid waste fragments of a size substantially larger than said solid particulate material.

58. The apparatus of claim 57, wherein said pre-treatment means is a coarse grading separator configured to allow said solid particulate material to pass through said coarse grading separator but to prevent material of a size substantially larger than said solid particulate material from passing through.

59. The apparatus of any of claims 37 to 58 further comprising controlling means for controlling the ratio of solid particulate material:liquid in the stream fed into the hydrocyclone.

60. The apparatus of claim 59 wherein the controlling means comprises a flow regulator.

61. The apparatus of claim 59 or 60 wherein the controlling means comprises ducting to introduce a predetermined amount of a liquid diluent to the stream fed into the hydrocyclone, preferably wherein said liquid diluent is or comprises one or more recycled liquid stream(s) derived from said first stream and/or said second stream and/or wherein said liquid diluent is or comprises one or more recycled liquid stream(s) derived from any cleaning of the solid particulate material downstream of the hydrocyclone separator.

62. The apparatus of any of claims 37 to 61, wherein the first outlet is an underflow of the hydrocyclone separator and the second outlet is an overflow of the hydrocyclone separator.

63. The apparatus of any of claims 37 to 62 suitable for treating a substrate which is an animal skin substrate, preferably a hide or pelt, and wherein said treating of the substrate is a tannery process, preferably selected from curing, beamhouse treatments, pre-tanning tanning, re-tanning, fat liquoring, enzyme treatment, tawing, crusting, dyeing and dye fixing, preferably wherein said beamhouse treatments are selected from soaking, liming, deliming, reliming, unhairing, fleshing, bating, degreasing, scudding, bating, pickling and depickling.

64. The apparatus of any of claims 37 to 63 which is configured to separate said solid particulate material from solid waste fragments wherein the solid waste fragments derived from the substrate are fibrous and/or particulate.

65. The apparatus of any of claims 37 to 64 which is suitable for treating a substrate with a solid particulate material comprising polymeric particles having a density of at least about 1.0 g/cm.sup.3 and no more than about 8.0 g/cm.sup.3, preferably in the range of from about 1.5 to about 2.5 g/cm.sup.3.

Description

[0177] The disclosure is further illustrated by reference to the Figures:

[0178] FIG. 1 illustrates the geometry and dimensions of a hydrocyclone separator, and is described hereinabove.

[0179] FIG. 2 is a further illustration of a hydrocyclone separator (1), wherein stream (A) is the effluent stream comprising solid particulate material, solid waste fragments and treatment liquor; and stream (B) is the second stream comprising solid waste fragments and treatment liquor; and stream (C) is the first stream comprising solid particulate material and typically also treatment liquor and/or residual solid waste fragments

[0180] FIG. 3 illustrates a self-cleaning helical filter (10) comprising a helical cleaning element (11) and filter (12), wherein stream (D) is a stream (for instance the second stream) comprising solid waste fragments and liquid (for instance treatment liquor); stream (E) is a liquid filtrate stream (for instance the first filtrate stream) comprising liquid (for instance treatment liquor); and stream (F) is residue (for instance the first residue) comprising solid waste fragments.