• 专利附录
  • 专利说明
  • 权利要求
  • 类似技术
  • 同族专利
  • 引用文献
  • 法律状态
  • 优先权
    • 专利摘要:

    公开号:SU1776199A3
    申请号:SU4742694
    申请日:1989-12-15
    公开日:1992-11-15
    发明作者:Tarchisio Orlandi
    申请人:Snam Progetti；
    IPC主号:
    专利说明:

    The invention relates to a high-performance tube mill for the finest grinding, operating in a continuous cycle.
    The aim of the invention is to improve the efficiency of the mill.
    Nafig. 1 is a longitudinal section of the mill; in fig. 2 - separator partition; in fig. 3 - technological installation for wet grinding; in fig. 4 - technological unit for dry grinding.
    The mill is made in the form of a rotor drum 1 with a high ratio of length to inner diameter, and this ratio is at least five, and preferably six or more, while its inner volume is divided by separator baffles 2 into a large number of cylindrical grinding chambers 3, in which are located crushing weights, the components of which have successively decreasing dimensions from the falling chamber to the dispensing chamber. The shape of the separator baffles 2 is shown in more detail in FIG. 2. The feeding is carried out by means of a hopper device 4 with a rotary screw feeder 5 known in the art. The rotational speed of the screw feeder 5 determines its performance.
    Inside the cylindrical chambers 3, crushing bodies are located, consisting of metal, for example, steel balls or rods.
    The components of crushing bodies have sequentially decreasing sizes from
    1776199 AZ of the initial chamber, which receives the feed, to the final chamber, from which the finest grinding product is discharged. According to the present invention, it has been found that optimal efficiency is obtained by placing in each chamber, and especially in the initial chamber, crushing bodies consisting of bodies, not all of which are of the same size, while the size distribution is such as to obtain the maximum number of possible collisions between the product and crushing bodies, and having a kinetic energy, at least part of the crushing weight, which is sufficient for crushing large granules.
    The size distribution of the crushing bodies must be corrected with the particle size distribution of the feed particles.
    The walls of the grinding chambers 3 are provided with a grooved armored coating
    6, which not only provides the necessary protection, but also determines the mixing and advancement of the material to be ground and rotates the grinding bodies, which rise in a circular direction along the grooved wall to a certain height directly related to the rotation speed, and then fall down in a parabolic trajectory onto the bed of granules to grind them.
    According to a preferred embodiment of the invention, the rotor drum 1 is divided into three cylindrical chambers 3, of which the central chamber is considerably longer than the other two.
    The purpose of the first grinding chamber is to reduce the particle size of the largest portion of the feed, with the largest central chamber doing the most work and the last chamber completing the grinding.
    The finest product is discharged from the last cylindrical chamber by means of baffle blades and transported to the storage site through the hopper
    7 that is known in the industry. One of the essential components of the finest grinding mill according to the invention is the separator baffle, which acts both as a wall between the different chambers 3 and as a device for controlling the product level (FIG. 1).
    The separator partition consists of an outer ring 8, intended for its rigid attachment to the tubular wall of the rotor drum 1, and two round flat front walls 9 and 10. The surface of which adjoins the grinding chambers 3, between which the product moves, passing from left to right.
    In the wall 9 facing the downstream grinding chamber, circular slots 11 are formed through the inner circular belt, while the peripheral circular belt is made without slots. At the center of the baffle is an outwardly projecting solid, such as a truncated cone 12, with its smaller base facing the downstream grinding chamber. In the wall 10 facing the downstream grinding chamber, there is a central circular hole coaxial with the cone 12 to allow material to be discharged.
    On the inner side of the hollow disc formed by the walls 9 and 10, in addition to the cone 12, there is a large number of blades 13 that move the product between the grinding chambers. The operation of the mill according to the invention is essentially the same for dry and wet grinding, with the solid material in concentrated suspension in the liquid phase.
    When the mill rotates, the circular slots 11 in the circular sectors, which are moved to the lower position, allow the passage of a turbid liquid in the case of wet grinding or powder in the case of dry grinding from the downstream grinding chamber into the inner recess of the partition formed by walls 9 and 10 and the ring 8. and containing the blades 13, where they are assembled according to the arrows. The sectors containing the turbid liquid or powder accumulated in the recesses continue to rotate and pass from the lower position to the upper position, while the turbid liquid or powder retained by the blades 13 falls under the action of gravity onto the cone 12 and passes through the central circular hole in the wall 10 into the grinding chamber downstream. The protruding body 12 can also be made in the form of a truncated regular pyramid with a regular polygonal base.
    The blade 13 can be formed with flat walls from a C-shaped profile or with curved shovel-shaped walls. It can pass completely between the ring 8 and the protruding cone 12 to isolate the circular sectors from each other, or it can leave openings in the central zone, as shown in Figure 28, or in the peripheral zone near the ring 8. thereby reducing the degree of movement efficiency per revolution from one chamber to the next.
    In this respect, it should be noted that the required mill capacity is usually significantly less than the conveying capacity of the blades 13. if the circular sectors are completely isolated from each other.
    The performance of the mill can be changed by changing a certain number of parameters.
    This is mainly the number, size and position of the slots 11, and, in particular, the height of the uncut peripheral strip of the wall 9, and the number, shape and size of the blades 13 and their radial position in relation to the proportion of the departure path, and hence their transmission capacity.
    In a preferred embodiment of the invention, the last chamber of the finest grinding mill is separated from the discharge by a separator baffle provided with a wall 9, in which the uncut peripheral belt is actually lower in height than in the other baffles, so that the ground product has a lower level and is all contained within the grinding weight. which acts as a filter and prevents the discharge of particles outside the size range.
    In order to illustrate the advantages obtained by the present invention, some tests in wet grinding of coal carried out on a control microfine mill constructed according to the present invention are described.
    Example 1. The product to be ground was coal, and grinding was carried out with separate feeds of dry coal and water with a weight ratio of the order of 1: 1.
    The control mill contained 3 chambers with a useful inner diameter, excluding armor plating, of the order of 550 m, and a total useful length, excluding partitions, of the order of 3300 mm. divided as follows: the first chamber is 760 mm, the second chamber is 1780 mm, and the third, final chamber is 760 mm.
    The separator baffles have been shaped as shown in FIG. 2, and had the following characteristics;
    1st partition: The ratio of the passage area to the total area 3%:
    slot height 8 mm: uncut circular band height 86 mm;
    number of blades 4, C-shaped:
    2nd partition: The ratio of the passage area to the total area is 2%;
    the height of the slots is 5 mm; * height of uncut circular tape 86 mm;
    number of blades 4; C-shaped;
    3rd partition (unloading): The ratio of the passage area to the total area is 2.9%;
    the height of the slots is 5 mm;
    height of uncut circular tape 69 mm;
    number of blades 4, C-shaped. Rotation speed: 37 rpm - equivalent to 65% of critical speed.
    The grinding weight was as follows: 1st chamber. Steel balls with the following weight distribution; diameter 30 mm 13% mm - 25% mm - 25% --15 mm-37%
    2nd camera. Steel balls with the following weight distribution;
    diameter 15 mm - 24% mm-76% '
    3rd camera. Steel balls with a diameter of 8 mm or rods 8 x 8 mm.
    The degree of filling retained in the grinding chamber was: Grinding weight,% Product,%
    1st chamber 3629
    2nd chamber 3635
    3rd chamber 3428
    The obtained performance indicators are as follows: Particle size of the supplied coal
    Connection index Dry outlet Maximum product size Power consumption
    0-6 mm
    KWh / t kg / h micron 100 kWh / t dry basis.
    Example 2: The same mill was also used to grind coal into smaller particles, fed in a slurry.
    The first divider has been removed. The grinding weight and the degree of filling were the same as 55 in the second and third stages of the previous example.
    The obtained performance indicators were as follows:
    Particle size of the supplied coal 0-350 micron
    Compound index 21 KWh / t
    Output of 110 kg / h of turbid liquid Maximum size of ground product <20 microns Power consumption 60 kWh / t, dry base Rotation speed 37 rpm, equivalent to 65% of critical speed.
    Tests were also performed with a different control mill to determine the effect of the L / D ratio on the ground product by reducing the effective length of the device. Tests were performed using separate dry material and water feeds.
    Example 3.
    Tsbsh) = 4
    Inner diameter 600 mm
    Useful length 2400 mm
    Number of chambers 2
    Effective length of 1st chamber 560 mm
    Tsbsh) = 6
    600 mm
    3600 mm
    830 mm
    Grinding bodies of the 1st chamber, as in
    0-6 mm
    1st chamber example 1 Useful length 2nd chamber 1840 mm 2770 mm
    Grinding bodies of the 2nd chamber, as in the 2nd chamber of example 1
    Coal feed Particle size 0-6 mm Compound index (kWh / t) 21
    Yield, dry basis (kg / h) 20.8
    Max, product size <20 μm
    Energy consumption (kWh / t) 225
    Productivity (kg / m 3 h) 30.8
    Rotational speed (rpm) Example 4.
    <20 μm
    180
    38.3
    35.5 35.5
    Inner diameter Usable length
    Tsbsh) = 4
    600 mm
    2400 mm
    Tsbsh) = 6
    600 mm
    3600 mm
    Number of chambers 3 3
    Effective length of 1st chamber 560 mm 830 mm
    Useful length of the 2nd chamber 1280 mm 1940 mm
    Useful length of the 3rd chamber 560 mm 830 mm
    Shredding bodies as in example 1
    The degree of filling is the same as in example 1 Coal feed
    Particle sizeCompound index 0-6 mm 0-6 mm five (KWh / t) 21 21Yield, dry basis (kg / h) 27 65 'Max, product size <20 μm <20 μm ten Energy consumption (kWh / t), dry basis 160 100Productivity (kg / m 3 h) 39.8 64 fifteen Rotation speed (rpm) 35.5 35.5
    From Examples 3 and 4 it can be seen that the unexpected increase in the production of small particle sizes (<20 μm) obtained by the increased length is significantly superior to the resulting increase in usable volume.
    In addition, with an increase in the number of grinding chambers, energy consumption is significantly reduced.
    During the tests, it was also found that the maximum energy efficiency for the finest grinding of materials and the maximum size less than 20 microns is obtained with a range of 30 speed zones, which is 60-70% of the critical speed, and this range during testing was 40-80%.
    The finest grinding mill according to the invention can be used in industry for both dry and wet grinding. FIG. 3 shows a flow diagram for wet grinding. The granular coal is fed by a conveyor belt 14 to a stirrer 15, into which water for the suspension is supplied by a pump 16 and a line 17. The resulting suspension is fed to the finest grinding mill 1 according to the invention. It is discharged 45 by an unloading device 18, consisting of a rotating structure with a perforated wall 19, which allows the suspension with the finely divided product and 50 to be removed through the line 20, while any unwanted grinding bodies that have passed through the separator walls 2 are discharged from its end. They are collected in bunker 21 and periodically 55 are removed from it.
    The energy consumed during grinding results in an increase in the temperature of the aqueous slurry and some steam generation. Steam removal rate and ___ temperature of the suspension with the product cont
    They are rotated by a control valve 22 connected between the extractor fan 23 and the unloading device 18.
    FIG. 4 is a flow diagram for dry micronizing associated with a cyclone classifier. The granular feed and recirculated coarse product are fed to a feed hopper 24 and sucked into the micronizing mill 1 according to the invention. It is held under vacuum and, if necessary, under a controlled atmosphere, the latter occurring when the material to be comminuted can generate dust or volatile products that are dangerous in the presence of air, such as coal. This atmosphere can consist of air and mixtures of inert gases, the composition of which is outside the explosion limits.
    Under the action of suction, the very finely ground product is liquefied at the discharge point and is fed through the line 25 to the first cyclone separator 26, which separates the coarse fraction of the product, while it is recirculated to the hopper 24 through the line 27. The finer fraction remains liquefied and is fed through the line 28 to a second, higher efficiency cyclone separator 29 that separates the product fines. The conveying fluid leaves the top of the separator 29 and is recirculated to the hopper 24 by means of the suction fan 30, which compensates for the pressure drop across the entire circuit and line 31.
    Part of the liquefying gas is discharged to the atmosphere through line 31 after the final removal of dust in the filter 33. The product is discharged through line 34. A part of the liquefying transport gas must be released in order to keep its composition within safety limits, since a certain infiltration of external air from the feeders is inevitable and through swivel joints. Air is supplied via line 34, and inert gas via line 35. Carrying out the grinding process under the influence of vacuum prevents dust from escaping into the atmosphere. In order to more clearly show the industrial advantages of the present invention, the following are the structural and operational data of a finer mill according to the invention for wet grinding of coal, in this case for the treatment of granular fossil coal and petroleum coke according to the scheme shown in FIG. 3.
    Innings
    Type Fossil coal Petroleum coke Feed rate (t / h, dry
    substance) 20 20 Moisture content (wt%) 5-10 6-11 Density (kg / dm 3 ) 1.35 1.4 GrindabilityH.C.I. (hardness index) 52 55 g Compound index (kWh / t) 21 Not specified
    Particle size distribution Same in both cases
    The size cells, mm Total retention% by weight 2 on average 2 maximum 5 1.5 --5 fourteen 1 15 34 0.7 30 45 0.6 - ”- 45 56 0.35 - 60 65 0.25 73Middle 75 diameter (mm) - to - 0.6 Injected liquid (added water) Velocity 0.65 chenie (t / h)Temperature (° C) 20-24 pH 9-10Derivedliquid Slurry flow rate (t / h) 42.1Steam flow rate (t / h) 1.7Temperature (° C) 69Concentration,% by weight 49-50Viscosity (cps) 80-180pH 7 22.7
    Suspended solid material 99.5% pass microns, all pass 32 microns
    Mill characteristics
    Inner diameter without armor coating 3.1m
    Total cylinder length 19.0 m
    Effective length of 1st chamber 4.0 m Effective length of 2nd chamber 9.5 m
    Useful length of the 3rd chamber 4.3 m Shredding weight:
    1st chamber 51 t
    2nd chamber 119 t
    3rd chamber 50 t
    Type, distribution and degree of filling as in example 1
    Construction power 2700 kW
    Separator baffles: Total thickness of 1st and
    2nd partition 500 mm
    The total thickness of the 3rd partition is 250 mm
    Number of sectors and blades 14 Slot height as in example 1
    Total area of the slot
    1st chamber 0.252m
    2nd chamber 0.154m
    3rd chamber 0.232m
    Operational data
    Dwell time (minutes) 36
    Rotational speed (rpm) 15.5% critical speed 65
    Absorbed power (kW) 2200
    Energy consumption (kWh / t, dry) 110
    权利要求:
    Claims (4)
    [1]
    Claim
    1. A cylindrical multi-chamber continuous mill for grinding coal, containing a rotating drum, divided into chambers containing crushing bodies such as balls or rods, and each chamber is separated from adjacent chambers by separator baffles and communicated with adjacent chambers through a central hole in which an open body in the form of a truncated cone, characterized in that, in order to increase efficiency in work, at least two adjacent grinding chambers 5 contain crushing bodies of at least two sizes, and the remaining chamber contains crushing bodies of the same size, while the separator baffles consist of two parallel walls 10 with central holes, and the wall adjacent to the previous chamber, in the direction of advancement of the material to be crushed, has a plurality of holes adapted to provide additional communication between two adjacent grinding chambers, and the opposite wall is solid, while on the peripheral wall of the mill mounted at one end, a set of 20 blades mounted for rotation in the space bounded by the walls of the grinding chamber.
    [2]
    2. Mill pop. 1, characterized in that the crushing bodies contained in the first grinding chamber 25 have the following distribution by weight,%: <
    diameter 30 mm-13 diameter 25 mm - 25 diameter 20 mm-25
    30 diameter 15 mm - 37.
    Z. Melnitsa 1, characterized in that the crushing bodies in the second grinding chamber have the following weight distribution,%:
    35 diameter 15 mm - 24 diameter 10 mm -76.
    [3]
    4. The mill according to claim 1, characterized in that the crushing bodies of the third chamber are steel balls of dia-
    40 meters 8 mm or steel rods 8 x 8 mm.
    [4]
    5. A method of fine grinding of coal using a mill, characterized in that the rotation speed of the mill is 60-67% of the critical speed
    45 rotation of the mill. ‘Fig. /
    类似技术:
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    RU2694313C1|2019-07-11|Dismembrator
    同族专利:
    公开号 | 公开日
    AU619369B2|1992-01-23|
    GB2229940A|1990-10-10|
    GB8927959D0|1990-02-14|
    CN1025292C|1994-07-06|
    IT1228049B|1991-05-27|
    CN1044419A|1990-08-08|
    DE8914652U1|1990-03-22|
    GB2229940B|1992-10-21|
    IT8822989D0|1988-12-16|
    AU4684089A|1990-06-21|
    DE3940906A1|1990-06-21|
    引用文献:
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    DE1285277B|1965-04-15|1968-12-12|Basf Ag|Process and device for the continuous wet grinding of solids in tubular mills|
    DE2207484C3|1971-02-18|1988-07-07|Pierre Bruessel/Bruxelles Be Slegten|
    US4498634A|1983-09-01|1985-02-12|Fuller Company|Division head for grinding mill|WO1992006725A1|1990-10-12|1992-04-30|Habley Medical Technology Corporation|Disposal module with sleeve for prefilled cartridges|
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    CN102002266B|2010-10-28|2013-03-13|长沙族兴新材料股份有限公司|Preparation method of silver dollar-shaped aluminum pigment|
    CN106238155B|2016-08-21|2018-06-08|横店集团东磁股份有限公司|A kind of material breaking mixing apparatus|
    法律状态:
    2010-09-20| REG| Reference to a code of a succession state|Ref country code: RU Ref legal event code: MM4A Effective date: 20071216 |
    优先权:
    申请号 | 申请日 | 专利标题
    IT8822989A|IT1228049B|1988-12-16|1988-12-16|GRINDING PROCEDURE AND CONTINUOUS HIGH CAPACITY MICRONIZER MILL FOR ITS REALIZATION|
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