The present disclosure relates to a hydrocyclone for separating a fiber pulp suspension containing relatively heavy contaminants.
Hydrocyclones are used in the pulp and paper making industry for cleaning fiber pulp suspensions from contaminants, in particular, but not exclusively, from contaminants that differ from fibers in density.
Disclosed is a hydrocyclone having a mid-section having a longitudinal axis and a radius, and a fluid injection member having at least one dilution port therethrough, the dilution port causing fluid to enter with both tangential and radial velocity components
In one embodiment, the hydrocyclone has a mid-section having a longitudinal axis and a radius, and a fluid injection member releasably connected to the mid-section. The fluid injection member has a dilution passage therethrough and at least one spaced apart dilution ports, at least one dilution port being at an angle of between 5 and 75 degrees relative to the mid-section radius. The injection member comprises a nozzle housing releasably connected to the mid-section, the nozzle housing having a dilution passage therethrough, and a nozzle adapted to be connected to the nozzle housing, the nozzle being planar and having at least one dilution port therethrough, the nozzle being receivable within the dilution passage.
In one embodiment, one dilution port injects fluid into the mid-section in one direction and another dilution port injects fluid into the mid-section in a different direction.
Before one embodiment of the disclosure is explained in detail, it is to be understood that the disclosure is not limited in its application to the details of the construction and the arrangements of components set forth in the following description or illustrated in the drawings. The disclosure is capable of other embodiments and of being practiced or being carried out in various ways. Also, it is to be understood that the phraseology and terminology used herein is for the purpose of description and should not be regarded as limiting. Use of “including” and “comprising” and variations thereof as used herein is meant to encompass the items listed thereafter and equivalents thereof as well as additional items. Use of “consisting of” and variations thereof as used herein is meant to encompass only the items listed thereafter and equivalents thereof. Further, it is to be understood that such terms as “forward”, “rearward”, “left”, “right”, “upward” and “downward”, etc., are words of convenience and are not to be construed as limiting terms.
Conventional Hydrocyclone
Referring to the drawing Figures, like reference numerals designate identical or corresponding elements throughout the several Figures.
In operation, a pump 10 pumps a fiber suspension containing heavy contaminants through a conduit 11 to the inlet member 6, which feeds the suspension tangentially into the separation chamber 3. The incoming suspension forms a vortex, in which the heavy contaminants are pulled by centrifugal forces radially outwardly and the fibers are pushed by drag forces radially inwardly. As a result, a central fraction of the suspension substantially containing fibers is created centrally in the vortex and a reject fraction containing heavy contaminants and some fibers is created radially outwardly in the separation chamber. The created reject fraction is discharged through the reject fraction outlet 7 and the created central fraction is discharged through the central accept fraction outlet 8.
The housing 2 forms a first elongate generally tapering chamber section 3a of the separation chamber 3 extending from the base end 4 of the separation chamber 3 to an apex end 12 of the first chamber section 3a having an axial opening 13 and a second elongate generally tapering chamber mid-section 3b of the separation chamber 3 extending from a base end 14 thereof to the apex end 5 of the separation chamber 3. The axial opening 13 of the apex end 12 of the first chamber section 3a also forms an opening to the second chamber section 3b at the base end 14 thereof. The first and second chamber sections 3a, 3b are aligned with each other, so that their central symmetry axes form a common central symmetry axis 15. The vortex formed in the separation chamber 3 during operation extends from the first chamber section 3a through the axial opening 13 of the apex end 12 of the first chamber section 3a into the second chamber section 3b.
An injection member 16 is provided on the housing 2 to inject a liquid tangentially into the separation chamber 3 at a distance from the apex end 5 of the separation chamber 3, which is at least 40% of the length of the separation chamber 3. In the embodiment of
The fluid injection member may inject a liquid, or a mixture of liquid and gas. An advantage of injecting a mixture of liquid and gas is that the gas mechanically dissolves fiber network occurring in the second chamber section. Advantageously, the injected fluid may be a fiber suspension having a fiber concentration lower than that of the fiber suspension to be fed by the inlet member.
In operation, a pump 17 pumps liquid through a conduit 18 to the injection member 16, which injects the liquid tangentially into the second chamber section 3b so that the injected liquid increases the rotational speed of a portion of the vortex in the chamber section 3b, thereby increasing the separation efficiency with respect to fibers existing in said vortex portion. As indicated in a broken line 19 in
In one embodiment, the length L1 of the first chamber section 3a is about 60 cm and the length L2 of the second chamber section is about 50 cm. The width of the second chamber section 3b measured where the liquid is injected is about 6 cm and the width of the first chamber section 3a where the suspension is fed is about 8 cm.
Generally, the length L1 of the first chamber section 3a should be 5 to 9 times the width of the first chamber section 3a also measured where the suspension is fed into the first chamber section. The width of the second chamber section 3b measured where the liquid is injected should be equal to or smaller than the width of the first chamber section, preferably 65 to 100% of the width of the first chamber section, measured where the suspension is fed into the first chamber section. The width of the first chamber section at the apex should be 50 to 75% of the width of the first chamber section measured where the suspension is fed into the first chamber section.
Improved Fluid Injection Member
Illustrated in
Illustrated in
The mid-section 29 comprises an outer shell 23 and an inner shell 25 spaced apart from the outer shell 23, as shown in
More particularly, the nozzle housing 38 is positioned prior to engaging the mid-section 29 with the nozzle housing 38 extending upwardly, as shown in
In the illustrated embodiment the fluid injection member 28 comprises the nozzle housing 38 releasably connected to the mid-section 29, the nozzle housing having a dilution passage 43 therethrough, as shown in
In one embodiment, the nozzle 40 has the at least one dilution port 50 through the nozzle 40, the dilution port 40 being at an angle 27 (see
More particularly, in the illustrated embodiment, the injection member 28 has two spaced apart dilution ports 50 and 52 through the injection member 28 in the form of angled openings 50 and 52 in the nozzle 40. In other embodiments (not shown), there can be a single dilution port through the nozzle 40. In the illustrated embodiments, the dilution ports 50 and 52 are cylindrical, but in other embodiments (not shown), other port shapes can be used, such as slots, squares, diamonds, and so on. Further, in the illustrated embodiment the open area of each nozzle port is between 10 and 500 square millimeters, preferably between 10 and 300 square millimeters, and most preferably between 10 and 200 square millimeters. The open area is the area of the port when a cross section is taken through the port perpendicular to the longitudinal axis of the port. In a preferred embodiment, the total relative open area of the nozzle ports divided by the cross-sectional area of the inner shell where the nozzle port is located is between 0.1 and 10 percent.
In the illustrated embodiment, the injection member 28 is located at least at position about 30% of total length of chamber up from apex 5, and preferable greater than 40% up. In other embodiments (now shown), other positions can be used. The injection fluid amount from a nozzle port totals about 2% to 10% of the fluid at the hydrocyclone inlet, and preferably about 5% in the illustrated embodiment. With additional nozzle ports, higher injection fluid amounts are possible. In other embodiments (not shown) the hydrocyclone can include additional fluid injection members spaced apart around the hydrocyclone periphery or along the hydrocyclone axis 15.
The nozzle 40 is adapted to be attached to the nozzle housing 38 so that the injection direction of the dilutions ports 50 and 52 is in a direction perpendicular to the longitudinal axis 15 of the hydrocyclone 26. This results in the injection fluid entering the mid-section 29 oriented circumstantially around the inside of the mid-section 29.
Illustrated in
In still another embodiment of the nozzle 40″, as shown in
The improved fluid injection member 28 of this disclosure provides greater flexibility to allow for injection of fluid into the hydrocyclone in different directions. The improved fluid injection member 28 with two spaced apart dilution ports allow for fluid injection into the hydrocyclone in more than one direction, and the two dilution ports help ensure fluid injection if one port gets clogged. The planar nozzle 40 allows for a dilution port selection to be made at the hydrocyclone depending on what materials are being separated in the hydrocyclone, thus allowing more ready tuning of the injection member 28 to the particular hydrocyclone needs. The bayonet style connection allows for a secure and quick connection of the fluid injection member 28 to the mid-section 29.
Various other features and advantages of the disclosure will be apparent from the following claims.
Filing Document | Filing Date | Country | Kind |
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PCT/US2020/040825 | 7/3/2020 | WO |
Publishing Document | Publishing Date | Country | Kind |
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WO2022/005490 | 1/6/2022 | WO | A |
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Number | Date | Country | |
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20230211359 A1 | Jul 2023 | US |