This invention relates to a pulveriser or mill used to crush or grind raw material such as coal, for example, into fine particles suitable for combustion in steam-generating furnaces of fossil fuel power plants. More particularly, this invention relates to a classifier used in conjunction with such a pulveriser for classifying crushed particulate material received from the pulveriser into a sufficiently fine fraction which is suitable for combustion and a coarse fraction which is rejected and returned to the pulveriser.
Pulverisers are commonly used for crushing large coal or other raw material into small particles. An airstream entering the pulveriser sweeps the particles into a classifier which separates coarse particles from the airstream for regrinding and allows the finer particles to exit the classifier and to be used in a process or burned in a furnace (in the case of coal). Prior art classifiers in some cases are not as effective in returning the coarse particles or are less efficient owing to increased flow resistance caused by turbulence in certain areas within the classifier. Increased turbulence is undesirable as the classifier parts are subjected to increased wear. These inefficiencies limit the capacity of the pulveriser and negatively affect the output of boilers fed by the pulveriser (in the case of coal). Latest boiler requirements for NOx reduction require a finer product than previous type classifiers were designed for. The Inventors desire an improved static classifier which can provide the fineness required in these boilers for low NOx design burners whilst maintaining throughput of these mills.
The Inventors desire a classifier which addresses the above drawbacks.
In accordance with a first aspect of the invention, there is provided a classifier for use with a pulveriser which is configured to crush raw material, the classifier being configured to classify air-entrained, crushed particulate material received from the pulveriser into a fine fraction which is expelled from the classifier and a coarse fraction which is returned to the pulveriser for further crushing, the classifier including:
wherein at least part of the upstream portion of each adjustable blade is inclined with respect to the downstream portion of the blade body, the adjustable blades collectively being configured to induce swirl and to direct the entrained particulate material through the inlet into the classification zone.
The size of the area around the blades will be such as to supply a desired air/particle velocity. The Inventors believe the velocity will typically be between 4.5 and 5.5 m/s. However, this may vary depending on operating conditions. In general a velocity of about 4.5 m/s may be used where a high throughput classifier is desired and a velocity of about 5.5 m/s may be used where a high fineness product is required. The length of the adjustable blades may affect the velocity at the outlet of the blades and is therefore adjusted to meet operational requirements.
The classifier may be a static classifier and a corner of the upstream portion of each blade may be inclined at an angle of between 20° and 40° with respect to the downstream portion of the blade body when viewed edge-on from a bottom of the blade body.
The corner of the upstream portion may be separated from a remainder of the blade body by a fold line or bend line which is substantially perpendicular to a diagonal extending between a pair of opposing corners of the blade body. Each adjustable blade may include a mounting formation whereby the blade is mounted to the housing. Accordingly, the blade may be bent corner-to-corner. A remainder of the upstream portion and the downstream portion may be planar. A selection of the inclination of the angle of between 20° and 40° may depend on an expected turbulence behind the adjustable blades.
The classifier may include an inlet blade adjustment mechanism which is connected to the mounting formations of each of the blades in a configuration in which an angle of each blade body relative to the housing is adjustable in order to regulate air flow through the inlet, by adjusting the blade adjustment mechanism. In use, an air/particle velocity through the blades may be between 4.5 and 5.5 m/s.
The classifier may further include a plurality of angularly spaced apart, inclined pre-swirl vanes which are disposed upstream of the inlet blades, wherein each pre-swirl vane comprises a multi-planar body.
In accordance with a further aspect of the invention, there is provided a classifier for use with a pulveriser which is configured to crush raw material, the classifier being configured to classify air-entrained, crushed particulate material received from the pulveriser into a fine fraction which is expelled from the classifier and a coarse fraction which is returned to the pulveriser for further crushing, the classifier including:
The pre-swirl vanes may be disposed around an upper region of an outer periphery of walls of the housing defining the classification zone. The body of each vane may include an operatively upstream portion and an operatively downstream portion, the upstream and downstream portions being joined by a middle, wherein the upstream portion is downwardly inclined with respect to the middle such that the upstream portion is substantially parallel to an incoming air stream in order to minimise air flow resistance and wear; and at least part of the downstream portion is upwardly and inwardly inclined with respect to the middle and configured to direct fluid flow inward and to induce a centrifugal swirl. The upstream portion of each vane may be downwardly inclined at an angle of between 20° and 40° relative to the middle of the vane body and a fold line or bend line representing a start of the upstream portion may be parallel with a lower edge of the upstream portion. The size of an area around the pre-swirl vanes may be designed to match the air/particle velocity selected for the adjustable blades.
An outer corner of the downstream portion of each vane may be inclined at an angle between 20° and 40° with respect to the middle of the vane body. The selection of a bend angle of between 20° and 40° may be determined by analysing turbulence on a surface of the pre-swirl vanes. The middle of each vane body may be inclined at between 30° and 60° with respect to the vertical. Preferably each vane is inclined at 45° with respect to the vertical but this may depend on flow conditions within the classifier. The angle of the vanes with respect to the vertical may be calculated and modelled using fluid dynamics. Inner and outer edges of each vane may match profiles of neighbouring walls of the classifier and a gap may be defined between the outer edges of the vanes and a mill body, the gap being smaller than or equal to half a width of a pre-swirl vane. There may be at least one blade for every two pre-swirl vanes. The pre-swirl vanes may have vane-to-vane overlap of one third of at least a vane breadth.
A lower edge of the housing defining the upper exit may have an aerofoil or teardrop cross-sectional profile which is configured to reduce turbulence and flow resistance at the exit of the classifier.
The invention also extends to a classifier for use with a pulveriser which is configured to crush raw material, the classifier being configured to classify air-entrained, crushed particulate material received from the pulveriser into a fine fraction which is expelled from the classifier and a coarse fraction which is returned to the pulveriser for further crushing, the classifier including:
The classifier may include an open ended depending member which is at least partially disposed within the classification zone, the member having a narrow upper end and a lower end, the member diverging from the upper end toward the lower end, the upper end defining a mouth having a reduced cross-sectional area when compared with a cross-sectional area of the upper exit, wherein the upper end of the depending member is arranged within or below the upper exit.
In accordance with yet another aspect of the invention, there is provided a classifier for use with a pulveriser which is configured to crush raw material, the classifier being configured to classify air-entrained, crushed particulate material received from the pulveriser into a fine fraction which is expelled from the classifier and a coarse fraction which is returned to the pulveriser for further crushing, the classifier including:
The depending member may be supported by a plurality of adjustable struts which permits a position of the depending member within the classification zone to be adjusted. The depending member may be in the form of a cone and the mouth of the depending member may be concentric with the upper exit such that the upper end is positioned in the middle of the upper exit. A length of the depending member, and hence the extent to which the depending member extends downwardly into the classification zone, may be adjustable.
The invention also extends to a method of modifying a classifier for use with a pulveriser, the classifier being configured to classify air-entrained, crushed particulate material received from the pulveriser into a fine fraction which is expelled from the classifier and a coarse fraction which is returned to the pulveriser for further crushing, the classifier including:
An angular position of the inlet blades with respect to the housing may be adjustable.
The method may include retrofitting a plurality of pre-swirl vanes to the upper region of the classifier such that the vanes are arranged below the classifier inlet blades, each pre-swirl vane comprising a multi-planar body which includes an operatively upstream portion and an operatively downstream portion, the upstream and downstream portions being joined by a middle, the upstream portion being downwardly inclined with respect to the middle such that the upstream portion is substantially parallel to an incoming air stream in order to minimise air flow resistance and at least part of the downstream portion of each vane is upwardly and inwardly inclined with respect to the middle of the vane body to direct fluid flow inward and to induce a centrifugal swirl.
The method may further include retrofitting an appendage to an operatively lower edge of a member defining the upper exit of the classifier, the appendage having an aerofoil or teardrop cross-sectional profile.
The invention will now be further described, by way of example, with reference to the accompanying drawings.
In the drawings:
In the figures, reference numeral 10 refers generally to a classifier in accordance with the invention. The classifier 10 is configured to classify air-entrained, crushed particulate material received from a pulveriser below (not shown) into a fine fraction which is expelled from the classifier 10 and a coarse fraction which is returned to the pulveriser for further crushing. The classifier 10 includes an outer body 12 which comprises an upper part 13 and a partially cone-shaped lower part 14. The classifier 10 further includes an inner housing 15 which is concentrically arranged within the outer body 12, the inner housing 15 defining an inward classification zone 19. The inner housing 15 comprises an operatively upper cylindrical wall 17, an upper periphery of which defines an inlet 20 which leads into the classification zone 19 and an operatively lower cone or grit funnel 21. The classifier 10 further includes a cylindrical feed pipe 22 which extends lengthwise through the middle of the classifier 10 and defines a feed inlet 24 toward an operatively upper end of the pipe 22. Raw material, for example coal, received into the feed pipe 22 via the feed inlet 24 is passed through the classifier 10 along an inlet axis X to the pulveriser (not shown) positioned below the classifier 10.
The inner housing 15 is radially inwardly spaced from the outer body 12 and held fast by braces 26 which extend between the inner housing 15 and the outer body 12. An airflow pathway 27 is defined between the inner housing 15 and the outer body 12 through which air-entrained crushed particulate material from the pulveriser is conveyed into the classification zone 19 via the inlet 20. The classifier 10 further includes a cylindrical vortex finder or exit pipe 30 which is concentrically arranged about the feed pipe 22 and extends axially upward from the classification zone 19. The feed pipe 22 and exit pipe 30 together define an annular exit passageway 31 whereby fine particulate material is transported to a desired location, e.g. in the case of coal to a furnace (not shown) for combustion.
Toward a lower end of the grit funnel 21 the classifier 10 has an annular rejection outlet 33 defined between an inner wall of the funnel 21 and a downwardly depending skirt 35 which is secured around a lower periphery of the feed pipe 22. Coarse material, unsuitable for combustion, which has been separated owing to the classification action of the classifier 10, is returned to the pulveriser via the rejection outlet 33 for regrinding.
The classifier 10 further includes a plurality of angularly spaced apart classifier inlet blades 37 which are arranged at least partially above the inlet 20 leading into the classification zone 19, within an annular space defined by an inner surface of the upper part 13 of the outer body 12, an outer surface of the exit pipe 30 and the upper periphery of the cylindrical wall 17. The classifier 10 further includes a blade adjustment mechanism 39 in the form of a mechanical linkage which comprises a plurality of downwardly depending arms 42 (see
Each inlet blade 37 comprises a generally planar body which is divided into an operatively upstream portion 43 which is outwardly disposed away from the inlet 20 (see
In addition to the classifier inlet blades 37, the classifier 10 further includes a plurality of pre-swirl vanes 47 (
Still referring to
Referring now to
A further embodiment of a classifier in accordance with the invention is illustrated in
A height of the conical member 102 with respect to the vortex finder 30 is adjustable by increasing/decreasing a length of adjustable struts 109 secured to an upper part of the cone 103. The conical member 102 is also supported by external struts 110 connecting the cone 103 to the inner housing 15. A pair of three angularly spaced apart inclined braces 112, each of which is connected to the feed pipe 22, support the conical member 102 from the inside (see
An alternative embodiment of the classifier in accordance with the invention is illustrated in
In use, air-entrained, crushed particulate material received from the pulveriser is directed along the airflow pathway 27 and passes through the pre-swirl vanes 47. The upstream portion 53 of each vane 47 is downwardly directed in the direction of the airflow such that it is substantially parallel with the flow direction of the incident particles in order to minimise flow resistance and wear. The particles then encounter the inclined middle 55 of the vane 47 which induces a vortex. Finally, as the particles pass the downstream portion 54, the upwardly and inwardly inclined outer corner 51 or upper kink forces the particles inward toward the classifier inlet blades 37 above.
The adjustable inlet blades 37 receive the airflow from the vanes 47 below in an upward and inward direction. The lower corner 45 of each blade 37 is angled or kinked to allow smooth inlet flow conditions into the blades 37. The angle of the blades 37 is adjustable by manipulating the blade adjustment mechanism 39 in order to regulate swirl and product fineness. The blade length is determined using velocity requirements at the blade outlet to set swirl conditions to suit fineness adjustability. The airstream is then directed into the classification zone 19 via the inlet 20 where it is subjected to classification action. The lower edge of the exit pipe or vortex finder 30 which has a teardrop or aerofoil profile 57 then receives the fine particles entrained in an upward airflow flowing along the exit passageway 31. In previous designs, this lower edge was plain or manufactured from two inverted cones and produced turbulence around its lower periphery which resulted in resistance losses. The teardrop or aerofoil profile 57 reduces flow separation and resultant resistance losses.
In respect of the classifiers 100, 200, the conical members 102, 202 improve efficiency of the classifier and hence product fineness. If it is desirable to increase particle size, the length of the conical member 102 can be reduced, hence increasing a gap between the grit funnel 21 and the lower periphery 107. Also, by lowering the position of the conical member 102 with respect to the vortex finder 30, the resultant particle size will be increased. The performance of the classifiers 100, 200 can therefore be fine tuned by adjusting the position and length of the conical members 102, 202.
The Inventors believe that by introducing the above design modifications, the throughput of the classifier 10, 100, 200 can be improved by a significant percentage (e.g. 15%) or product fineness improved at similar resistances over existing designs. The inlet blades 37, pre-swirl vanes 47, modified vortex finder 57 and conical members 102/202 serve to improve efficiency and reduce resistance to flow throughout the classifier 10 hence improving throughput capabilities or product fineness at similar resistances which suits low NOx requirements of present boilers.
Number | Date | Country | Kind |
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2013/06762 | Sep 2013 | ZA | national |
Filing Document | Filing Date | Country | Kind |
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PCT/IB2014/064310 | 9/8/2014 | WO | 00 |