CN1627991A - Milling method - Google Patents
Milling method Download PDFInfo
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- CN1627991A CN1627991A CN 03803378 CN03803378A CN1627991A CN 1627991 A CN1627991 A CN 1627991A CN 03803378 CN03803378 CN 03803378 CN 03803378 A CN03803378 A CN 03803378A CN 1627991 A CN1627991 A CN 1627991A
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- raw material
- vertical crusher
- pulverizing
- rotary table
- electric power
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C25/00—Control arrangements specially adapted for crushing or disintegrating
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C15/00—Disintegrating by milling members in the form of rollers or balls co-operating with rings or discs
- B02C15/04—Mills with pressed pendularly-mounted rollers, e.g. spring pressed
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C15/00—Disintegrating by milling members in the form of rollers or balls co-operating with rings or discs
- B02C2015/002—Disintegrating by milling members in the form of rollers or balls co-operating with rings or discs combined with a classifier
Abstract
A simple apparatus structure capable of milling with excellent efficiency without using a tube mill having poor milling efficiency. The milling method uses a mill apparatus provided with a vertical mill and a classifier. A raw material milled by the vertical mill is separated by the classifier into a coarse powder and a fine powder. The coarse powder is returned to the vertical mill to mill it again and the fine powder is taken out as a product. At least one of the following is adjusted so that a mill electric-power unit requirement of the vertical mill is controlled to a range between 1 and 30 kWh/t: the height of the dam ring of the vertical mill, the milling pressure of the milling roller, the number of revolutions of a rotary table, and the amount of raw material to be charged in the vertical mill.
Description
Technical field
The present invention relates to have vertical crusher (vertical crusher) and grading plant, and can carry out the breaking method that high efficiency is pulverized as raw material with mineral such as cement clinker (cement clinker), cement raw material, slag (slag), coal, calcium carbonate, pottery and chemical substances.
Background technology
In the past, as raw materials such as coal, lime stone, cement raw material, slag, cement clinker, pottery and chemical substance are carried out the broken reducing mechanism of fine powder, be to use two-stage reducing mechanism always, perhaps use the inner vertical crushing plant that rotary grader is housed with vertical crusher and tube mill (tube mill).
Above-mentioned two-stage reducing mechanism is the raw material after pulverizing with vertical crusher, re-uses tube mill these raw materials are carried out the broken reducing mechanism of fine powder.For example, disclosed technology in patent documentation 1 (spy opens flat 4-338244 communique), be in the raw material after pulverizing through vertical crusher, pulverize with vertical crusher and tube mill once more, raw material is carried out the broken reducing mechanism of fine powder with dispensing device for dispensing.Shown in Figure 15 is exactly an example of this reducing mechanism in the past.
In addition, the vertical crusher of grader is housed, for example, disclosed technology in the patent documentation 2 (spy opens clear 57-75156 communique) is arranged as above-mentioned inside.Reducing mechanism shown in Figure 16 is exactly an example of disclosed vertical crushing plant in this piece document, this device gas that imports from the rotary table below, above raw material after pulverizing between crushing rolls in pulverizer and the rotary table blowed to, carry out classification with the rotary grader that is arranged in the rotary table top, and when fine powder is discharged to the device outside, allow meal drop on the rotary table, pulverize once more, thereby it is broken to carry out fine powder to raw material with very high efficient.
, above-mentioned two-stage reducing mechanism in the past, owing to must have vertical crusher and two kinds of machines of tube mill in the formation of its device, therefore the structure of device is very complicated, wants to make various devices to turn round expeditiously, it is very complicated that the control method of running also becomes.
In addition, complicated apparatus also exists the labour that need expend maintenance (maintenance) etc. and the problem of time, and entire equipment is also very expensive.In addition, owing to used the low tube mill of crush efficiency, also exist the electric power consumption of whole device big, problem such as efficient is low.
Also have, the vertical crusher (air-sweeping type of being referred to as (airswept) vertical crusher is also arranged) of grader is equipped with in above-mentioned inside, need use the gas that imports from the rotary table below, above raw material after pulverizing between crushing rolls in pulverizer and the rotary table blowed to, thereby also have such problem, that is, and for the raw material after pulverizing is blowed to the top, just need a large amount of gas, and just need very big pressure fan power (power of fan) in order to discharge a large amount of gases.
Summary of the invention
The present invention puts forward in view of the above problems, its objective is provides a kind of have vertical crusher and grading plant, and as raw material, carry out the breaking method that high efficiency is pulverized with mineral such as cement clinker, cement raw material, slag, coal, calcium carbonate, pottery and chemical substances.
For achieving the above object, be according to breaking method of the present invention:
(1) a kind of breaking method that uses reducing mechanism, this reducing mechanism has vertical crusher and will be separated into the grader of meal and fine powder by the raw material after this vertical crusher pulverizing, roughly to make horizontal circle tabular and be provided with at peripheral part on the rotary table of back-up ring and be provided with the taper crushing rolls that a plurality of energy freely rotate on the surface thereon for above-mentioned vertical crusher, by means of the pulverizing pressure that applies regulation to this crushing rolls, the raw material that drops on this rotary table is pulverized, raw material after by means of this grader above-mentioned vertical crusher being pulverized is separated into meal and fine powder, and this meal is got back in this vertical crusher, pulverize once more, simultaneously, to eject as this fine powder of product, it is characterized in that, by adjusting at least a factor in the following various factors: the height of this back-up ring, the pulverizing pressure of this crushing rolls, the rotating speed of this rotary table, and the input amount of the raw material in the input vertical crusher, pulverizer unit's electric power consumption of this vertical crusher is controlled in the scope of 1～30kWh/ ton (ton).
(2) in the breaking method that (1) is put down in writing, the pulverizing pressure of the above-mentioned crushing rolls of crushing cement raw material is in the scope of 0.6～0.8MPa, and the unit electric power consumption of above-mentioned pulverizer is in the scope of 5～10kWh/ ton (ton).
(3) in the breaking method that (1) is put down in writing, the pulverizing pressure of the above-mentioned crushing rolls of crushing cement raw material is in the scope of 0.8～1.1MPa, and the unit electric power consumption of above-mentioned pulverizer is in the scope of 20～25kWh/ ton (ton).
(4) in the invention of the breaking method of being put down in writing in (1), the pulverizing pressure of above-mentioned crushing rolls of pulverizing slag is in the scope of 0.8～1.1MPa, and the unit electric power consumption of above-mentioned pulverizer is in the scope of 25～30kWh/ ton (ton).
(5) in (1)～(4) in the invention of any one breaking method of putting down in writing, the central diameter of crushing rolls relatively is in 1～10% the scope with the height setting of above-mentioned back-up ring.
(6) in (1)～(5) in the invention of any one breaking method of putting down in writing, mensuration is by the amount of the raw material that above-mentioned vertical crusher ejected, and adjust the amount that drops into the raw material this vertical crusher from the outside of above-mentioned reducing mechanism, so that the amount of the raw material of this discharge is constant.
Description of drawings
Fig. 1 is the overall structure figure that uses the reducing mechanism of vertical crusher in the embodiments of the invention.
Fig. 2 is vertical sectional drawing of the employed vertical crusher of embodiments of the invention.
Fig. 3 is the key diagram of the roller pressurization of employed vertical crusher in the explanation embodiments of the invention with oil gear and pulverizing pressure.
Fig. 4 is the key diagram of the pulverizing pressure of employed vertical crusher in the explanation embodiments of the invention;
Fig. 5 be the milling product particle mean size that obtains with employed breaking method in the embodiments of the invention than and system capability between the figure of proportionate relationship.
Fig. 6 is the figure with the proportionate relationship of resulting pulverizing pressure of employed breaking method in the embodiments of the invention and milling product particle mean size.
Fig. 7 is expression when being added in cement raw material on the sieve, the figure of the relation between sieve aperture and the throughput.
Fig. 8 is expression when slag is added in sieve, the figure of the relation between sieve aperture and the throughput.
Fig. 9 is expression when slag is added in sieve, the figure of the relation between sieve aperture and the throughput.
Figure 10 be expression use breaking method resulting pulverizer unit electric power consumption in the embodiments of the invention and system capability than between graph of a relation.
Figure 11 be expression use the resulting pulverizing pressure of breaking method in the embodiments of the invention and pulverizer unit's electric power consumption than between graph of a relation.
Figure 12 is that the resulting back-up ring aspect ratio of breaking method and the particle mean size ratio of milling product and the graph of a relation between pulverizer unit's consumption of power in the embodiments of the invention used in expression.
Figure 13 be the expression particle mean size of using the acceleration of raw material on the resulting workbench of breaking method in the embodiments of the invention and milling product than between graph of a relation.
Figure 14 be expression use the unit electric power consumption of the resulting pulverizer outlet of the breaking method conveyer in the embodiments of the invention and milling product particle mean size than etc. between graph of a relation.
Figure 15 is to use the overall structure figure of reducing mechanism of the pattern in the past of ball mill.
Figure 16 is to use the overall structure figure of reducing mechanism of the pattern in the past of air-sweeping type vertical crusher.
The specific embodiment
Below, with reference to the breaking method of accompanying drawing detailed description according to reducing mechanism of the present invention.Fig. 1～Fig. 4 is the example of a preferred embodiment of the present invention, and Fig. 1 is to use the overall structure figure of the reducing mechanism of vertical crusher; Fig. 2 is vertical sectional drawing of vertical crusher.Fig. 3 and Fig. 4 are the key diagram of the roller pressurization of explanation vertical crusher with oil gear and pulverizing pressure.Fig. 5～Figure 14 is the curve map of the test data used for the effect that breaking method of the present invention is described.Figure 15 and Figure 16 are the overall structure figure of reducing mechanism in the past.
Below, the preferred structure of employed vertical crusher 1 in the embodiments of the invention is described.In the present embodiment employed vertical crusher 1 as shown in Figure 2, it has: the housing (casing) that forms the outline of this vertical crusher; By being arranged on the reductor 2B of pulverizer bottom, by Motor Drive rotary table 2 rotation, the horizontal circle plate-like; Be arranged in locational a plurality of circular cones (conical) the shape crushing rolls 3 that the peripheral part of the top 2A of rotary table is along the circumferential direction carried out five equilibrium.
Crushing rolls 3 is by being installed on the lower case and upper arm 6 that can freely rotate and the underarm 6A that is made of one with above-mentioned upper arm (upper arm) 6 with axle 7, be connected on the piston rod (piston rod) 9 of oil hydraulic cylinder (oil hydrauliccylinder) 8, work by means of this oil hydraulic cylinder 8, press to the direction of rotary table 2A, by the drive of raw material, on rotary table, rotate on the 2A.
The central upper of 2A on the rotary table of above-mentioned housing, be provided with raw material input port 35 and raw material that raw material is thrown on the top 2A of rotary table and drop into chute 13, so as can with raw material from raw material input port 35 by raw material drop into chute 13 throw into (also can be referred to as supply) rotary table above on the 2A.The raw material of this input moves to be Vorticose track peripheral part of 2A above rotary table on the 2A on rotary table, between the top 2A of the rotary table of being nipped and the crushing rolls 3 and pulverize.
In addition, nipped between the top 2A of rotary table and the crushing rolls 3 and the raw material after pulverizing, cross the back-up ring (dam ring) 15 of the peripheral portion of the top 2A that is arranged on this rotary table, the peripheral part of 2A and the gap between the housing above rotary table, promptly, the direction of annular channel 30 (also can be referred to as the space 30 that changes the outfit) drops to the bottom of annular channel 30, from bottom outlet 34 it is discharged to the outside of vertical crusher 1 as milling product again.
In addition, on above-mentioned housing, below rotary table 2, be provided with the gas introduction port 33 that is used to import gas, and above rotary table, be provided with the top outlet 39 that is used to discharge this gas.In the running of vertical crusher 1, import gases (being air in the present embodiment) by means of this gas introduction port 33, produced in above-mentioned housing the air-flow of the gas that flows upward below the rotary table.
Like this, the fine powder that diameter is little in crossing the raw material of back-up ring rises in housing above just being blown to, and as fine powder, discharges from top outlet 39.
In addition, the amount of the fine powder of this discharge is seldom, in the present embodiment, through adjusting the gas flow of this importing, this fine powder amount is accounted for about 2～5% the raw material of discharging from bottom outlet 34.
In addition, in the vertical crusher 1 of present embodiment, the not pressure gauge of expression has been installed also among the figure,, thereby can have often been measured the thrust P1 of oil hydraulic cylinder 8 so that can measure the thrust P1 in the grease chamber of piston rod one side that is applied to oil hydraulic cylinder 8.
The value of being measured by above-mentioned pressure gauge is delivered to the pressure control device of crushing rolls, promptly in the control panel with after amplifier (amplifier) conversion.Control panel is made of calculator, comparator and setting apparatus etc., after the said determination value having been carried out calculating, compare with the setting value of in setting apparatus, setting in advance, according to result relatively, just can control and be sent to the pressure of crushing rolls pressurization with the pressure oil in the oil hydraulic cylinder 8 of oil gear 36.
In addition, the quantity of the crushing rolls of employed vertical crusher 1 is 3 in the present embodiment, and the rotating speed of workbench is 73RPM, and the central diameter D of crushing rolls is 0.4m, and workbench diameter T is 0.64m, the high about 20mm of the aspect ratio worktable upper surface 2A of back-up ring 15.
Then, the structure of employed reducing mechanism in the key diagram 1.In the preferred example of employed in an embodiment of the present invention reducing mechanism 100, have vertical crusher 1, grader 50 and gathering machine 60, in addition, for these mechanical connections are become structure described later, also have pressure fan 70 (also have be referred to as scavenger fan (exhaust fan) 70), bucket elevator (bucket elevator) 41 and belt conveyer (belt conveyer) 80 or the like.
Here, be connected with pipe arrangement, so that make the raw material of being supplied by belt conveyer 80 from the outside of reducing mechanism 100, after passing through double door 45,35 drop into the vertical crushers 1 from the raw material input port.
In addition, the major part of the raw material after being pulverized by vertical crusher 1 is the outside that is discharged to vertical crusher 1 by bottom outlet 34, and these raw materials that eject are transported by bucket elevator 41, drops in the grader 50.
Grader 50 in the present embodiment is grading plants of gravity classification formula,, uses its pipeline that absorbs is coupled together by catcher 60 (in the present embodiment, being sack cleaner (bag filter) 60) from pressure fan 70.
Then, start pressure fan 70, grader 50 just by gathering machine 60 will be attracted to its inside, particle diameter delivers in the catcher 60 together than desired littler fine powder and gas, and delivers to raw material beyond the gathering machine 60 as meal, discharge from the below of grader 50.
The raw material of discharging from grader 50 belows as meal 35 drops in the vertical crushers 1 from the raw material input port by the pipeline that connects.
In addition, the grader 50 in the present embodiment for input raw material is separated into meal and fine powder (product) all the time in certain proportion, has the structure that can adjust, is constant all the time so that make its classification efficiency.In the present embodiment,, service condition of gas flow of grader 50 and so on or the like is adjusted, just can be all the time 30% of input raw material be separated as meal according to the granularity of input raw material.
In addition, in the present embodiment, grader 50 has used the grading plant of gravity classification formula as mentioned above, yet, be not limited only to this, also can use as sieve formula, inertia-type, centrifugal force type etc. or other hierarchical approaches, still, just effectively fine powder is delivered to this point in the gatherer, preferably adopt gas flow to carry out the hierarchical approaches of classification.
And, in the present embodiment, in order to make the atmosphere gas generation control of dust in the vertical crusher 1, be connected with attraction pipeline from the top outlet 36 of pressure fan 70 by gathering machine 60 and grader 50 and vertical crusher 1, the dusty gas that swims in the vertical crusher 1 by means of 50 pairs in grader carries out classification, and the fine powder also littler than the requirement particle diameter delivered in the gathering machine 60, simultaneously with gas, with delivering to above-mentioned gathering machine 60 raw material in addition, discharge from the below of grader 50 as meal.
In addition, in the preferred example of the embodiment shown in Fig. 1, on each position of the air-supply route of sending from pressure fan 70,, just can regulate air quantity of flowing through the gas in vertical crusher 1 and the grader 50 or the like by flow rate regulating valve B2, B3 are set.
Below, a preferred embodiment that has the breaking method of the present embodiment that the reducing mechanism 100 of said structure implemented by means of use is described.
The raw material that is supplied to vertical crusher 1 by means of belt conveyer 80 from reducing mechanism 100 outsides, be (being cement clinker in the present embodiment) such as mineral, the raw material input port 35 of the central upper of 2A above the rotary table that is arranged on vertical crusher 1, drop into chute 13 by raw material, 2A drops into the top middle body of 2A above the rotary table above rotary table.Input raw material, by means of it is rotated on 2A on rotary table, and owing to rotating the centrifugal force that produces, on rotary table, draw out in the Vorticose track on the 2A, the peripheral part of 2A moves above rotary table, and 2A and be pressed in this above rotary table between the crushing rolls on the 2A 3 and pulverized nips above the rotary table.
Nipped above the rotary table in the raw material between the 2A and crushing rolls 3, the raw material of crossing back-up ring 15 is discharged in the outer peripheral face and the annular channel 30 between the housing inner peripheral surface of 2A above the rotary table, and fall from annular channel 30, be discharged to the outside of vertical crusher 1 from bottom outlet 34 as the product of pulverizing.In addition, blocked by back-up ring 15 and be trapped in above the rotary table raw material on the 2A and nipped once more above the rotary table among the 2A and crushing rolls 3, pulverize once more.
In addition, be discharged to the milling product of vertical crusher 1 outside, be transported in the grader 50 by bucket elevator 41 from bottom outlet 34.
In the raw material in being transported to grader 50, the fine powder that diameter is little is transported in the gathering machine 60 with gas, discharges as product there.In addition, the meal that diameter is big then returns in the vertical crusher 1 once more, pulverizes once more.
Below, the curve map that is documented in the test data among Fig. 5～Figure 14 is described.
The particle mean size of said milling product ratio, the unit electric power consumption of pulverizer and the unit electric power consumption (kWh/ton) of reducing mechanism are defined as follows in the present invention:
The particle mean size of milling product is represented with following formula 1 than the ratio that is particle mean size with the particle mean size of raw material of milling product:
Formula 1
In addition, the definition of particle mean size is, milling product is being placed on when sieving on the sieve, and its surplus ratio (dropping into the ratio that does not remain in the raw material on the sieve in the raw material behind the sieve by sieve) is the size of 36.8% o'clock sieve aperture.
The unit electric power consumption of pulverizer is the electric power (kWh) that consumes of pulverizer and the ratio of product weight (ton), represents with following formula 2:
The unit electric power consumption of reducing mechanism is the electric power (kWh) that consumes of device and the ratio of the product weight (ton) of raw material, represents with following formula 3:
In addition, the electric power that consumed of device is the summation of the electric power that consumed of vertical crusher 1, grader 50, pressure fan 70 and mill auxiliaries.
So-called device capability is that sieve that usefulness can allow the milling product of (under 90 μ m) below 90 microns pass through is when carrying out classification to milling product than (being also referred to as energy the force rate of reducing mechanism), with in above-mentioned particle mean size than being that sieve percent of pass under 0.15 the situation is benchmark (a reference value is 1), the ratio of the resulting percent of pass of comparing with the particle mean size of various milling products.Fig. 5 represents the reference curve of an example of the relation between milling product particle mean size ratio and the device capability ratio, and the energy force rate of device improves along with reducing of milling product particle mean size ratio.
As shown in Figure 5, along with raw material pulverizing must be thin more, device capability is than will improve thereupon.
Then, Fig. 6 represents the surface pressing (crushing rolls pressure) of vertical crusher and the relation of the particle mean size of milling product (when being cement clinker).
Can see too clearly from Fig. 6, even there is surface pressing to rise among the figure, the particle mean size of milling product but is difficult to the zone that reduces.(hence one can see that, and in the pulverizing characteristic of cement clinker, surface pressing can not improve the effect of pulverizing during greater than 1.1Mpa).
In addition, though not expression in the drawings, cement raw material and slag have also shown same tendency, and in the characteristic of cement raw material, what effect surface pressing does not have to improving degree of grinding during greater than 0.8MPa.In addition, slag also demonstrates same tendency, and what effect surface pressing does not have to improving degree of grinding during greater than 1.1MPa.
Also have, can see too clearly, under situation about repeatedly raw material being pulverized, when the number of times of pulverizing repeatedly is a lot, do not have what effect for the particle mean size that reduces milling product with vertical crusher from Fig. 7～Fig. 9.At this moment, so-called throughput is when being loaded in milling product on the sieve, and the amount by sieve aperture is with respect to the percentage that is loaded in the amount on the sieve (percentage).
In other words, when the device in making Fig. 1 turns round, select optimum surface pressing, carry out the pulverizing repeatedly of minimum number, reach the granularity of target milling product, be only most effective method.
, also has problem here.The number of times of Fen Suiing is the factor (factor) that changes along with the particle diameter of needed product repeatedly, and controlling raw material, need to carry out that how many times pulverizes repeatedly be very difficult.
Particularly, in the device of Fig. 1 because the raw material that drops into from belt conveyer 80, be with repeatedly pulverize repeatedly after raw material mix and drop in the vertical crusher, so just be difficult to correctly calculate (count) and control its number of times repeatedly.
The present inventor is conceived to the unit electric power consumption of vertical crusher, and this suitable factor of number of times of pulverizing repeatedly as control has been carried out wholwe-hearted research.That is, found the proportionate relationship of the number of times pulverized repeatedly and the unit electric power consumption of vertical crusher, that is, when pulverizing number of times and increase, the unit electric power consumption is increase just.
Owing to the unit electric power consumption of pulverizer is to change along with number of times that raw material is pulverized repeatedly, so selecting best surface pressure (pressure of crushing rolls) afterwards, just can make the raw material of being pulverized reach best pulverization conditions by control unit electric power consumption.
Here, please see expression Figure 10 (is example with the cement clinker) through the relation between the ability of the unit electric power consumption of pulverizer of investigation and reducing mechanism, be characterized in, has the very high zone of crush efficiency when 5～10kWh/ ton (ton), and increasing to 30kWh/ ton (ton) when above when the power of pulverizer, the efficient of device just descends.(but, Figure 10 is that what to be tried to achieve with cement clinker is 12% o'clock situation on product granularity is 90 microns sieve.)
This tendency of Figure 10, being not only cement clinker, for pulverizing different cement raw material, the slags of characteristic, roughly also is the same, when the unit electric power consumption of pulverizer being increased to 30 during more than or equal to kWh/ ton (ton), consequently the ability of reducing mechanism does not increase.This is the numerical value with feature for the reducing mechanism among Fig. 1.
From these facts as can be known, during reducing mechanism in control chart 1, for carrying out the needed precondition of good pulverizing is not waste the power of pulverizer, so will under condition, turn round smaller or equal to 30kWh/ ton (ton), in fact, owing to below 1kWh/ ton (ton), can not pulverize, so the unit electric power consumption of desirable pulverizer is in the scope of 1～30kWh/ ton (ton).
Below, different raw materials is described.
1. cement raw material
Because the product granularity of being tried to achieve is that 12% (referring to accompanying drawing) is just passable on 90 microns sieve, so do not need very strong pulverizing, reducing mechanism (just can carry out the very high pulverizing of efficient in the scope of surface pressing 0.6～0.8MPa) at 5～10kWh/ ton (ton).
Therefore, desirable scope is at 5～10kWh/ ton (ton) (surface pressing 0.6～0.8MPa).In other words, cement raw material is very suitable for the raw material pulverized with the device among Fig. 1.
2. cement clinker
The product granularity of being tried to achieve is that 3000～4000 cloth make (it is the unit of Japan's expression powder particle size that cloth makes (blaine), is documented among the R5201-1997 of JIS).Owing to recognize from the pulverizing characteristic of cement clinker, the pulverizing that surface pressing surpasses 1.1MPa does not have any effect, so utilize the pulverizing pressure in the scope of the 1.1MPa left and right sides, just can carry out high efficiency pulverizing repeatedly.Therefore, desirable scope is that the pulverizing pressure with above-mentioned crushing rolls fixes in the scope of 0.8～1.1MPa, carry out repeatedly pulverizing with this surface pressing, the unit electric power consumption that reaches the needed above-mentioned pulverizer of product granularity is in the scope of 20～25kWh/ ton (ton).
3. slag
For making that the product granularity tried to achieve is the orders of 4000～5000 cloth, just must be very carefully that raw material is carried out fine powder is broken.And, also must in not wasting the scope of pulverizing power, in the highest zone of degradation rate, pulverize.Therefore, desirable scope is, the pulverizing pressure of above-mentioned crushing rolls is in the scope of 0.8～1.1MPa, for the granularity that the higher limit in not wasting the scope of pulverizing power and this surface pressing are issued to product, the scope of the desirable unit electric power consumption of above-mentioned pulverizer is 25～30kWh.
In addition, as shown in Figure 10, making that under the situation that pulverizer unit's electric power consumption of vertical crusher 1 rises gradually, the energy force rate of device has the tendency that upwards improves gradually.The unit electric power consumption of pulverizer can be controlled by at least one factor of regulating in the following various factors: the pulverizing pressure of crushing rolls, the height of back-up ring, the rotating speed of rotary table, and the input amount that drops into the raw material in the vertical crusher.
Below, illustrate by regulating at least one factor in the following various factors: the pulverizing pressure L of crushing rolls 3, the height of back-up ring 15, the rotating speed of rotary table 2, and the input amount that drops into the raw material in the vertical crusher 1, control the technology of pulverizer unit's consumption of power.
At first, explanation is pulverized the technology that pressure L controls pulverizer unit's electric power consumption by adjustment with reference to Figure 11.Figure 11 is the curve map of the relation of the expression roller surfaces pressure of pulverizer and pulverizer unit's consumption of power.In addition, the roller surfaces pressure of being put down in writing among Figure 11 is illustrated pulverizing pressure L among the present invention.
Can be seen too clearly by Figure 11, along with the increase of the pulverizing pressure of vertical crusher 1, the unit electric power consumption of pulverizer just rises.
This be because, the pulverizing pressure of pulverizing the raw material of 2A above the rotary table is high more, the power that vertical crusher 1 is consumed is also many more.Therefore, pulverize pressure L, just can control the unit electric power consumption of pulverizer by adjusting.
Here, as shown in Figure 3, crushing rolls 3 is pressed in the pulverizing pressure L on the 2A above the above-mentioned rotary table, be that central diameter when crushing rolls 3 is D, the width of crushing rolls is W, in vertical direction crushing rolls 3 is pressed in the strength on the 2A above the rotary table, and promptly pulverizing pressure is F, and the angle of inclination of the center line of the width of crushing rolls 3 and vertical axis is pulverized pressure L and is defined by following formula 4 when being θ.
In the formula 4, the unit of employed pulverizing pressure F is newton (N) among Fig. 3, and the unit of the central diameter D of crushing rolls and the width W of crushing rolls is m.
In addition, when the pulling force of the piston rod of oil hydraulic cylinder 8 (also have be referred to as oil hydraulic cylinder pressure) is F1, lever ratio (lever rate) from oil hydraulic cylinder 8 to crushing rolls till 3 is that (in the present embodiment, in the time of R=L1/L2), the pulverizing pressure F in the present embodiment is R: F=F1 * R+M.(M is the crush force that deadweight produced by crushing rolls 3 grades)
Below, utilize Figure 12 that the unit electric power consumption of controlling pulverizer by the height of adjusting back-up ring 15 is described.Figure 12 represents the aspect ratio and the milling product particle mean size ratio of back-up ring, and the relation between pulverizer unit's consumption of power.The aspect ratio of back-up ring is the ratio of the height of the back-up ring 15 represented with percentage (%) with respect to the central diameter dimension D of crushing rolls 3, along with the height of back-up ring 15 with respect to the increasing of the central diameter D of crushing rolls 3, this ratio just increases.
Seen too clearly by Figure 12, along with the increase of back-up ring aspect ratio, the unit electric power consumption of pulverizer just rises.This be because, the height of the back-up ring 15 that is provided with along with the outer edge of the top 2A of rotary table increases, the raw material on the top 2A of rotary table just is difficult to cross back-up ring 15, the number of times of pulverizing repeatedly on rotary table increases and causes.And along with the rising of pulverizer unit's electric power consumption, the particle mean size of milling product is than the tendency that reduces is arranged thereupon.Therefore, change the aspect ratio of back-up ring, just can control the unit electric power consumption of pulverizer by means of the height of adjusting back-up ring 15.
Then, the result to Figure 12 is described further.Surpass 10% from the aspect ratio of back-up ring, the ascending curve of the unit electric power consumption of pulverizer just sharply rises, but as can be seen, the particle mean size of milling product reduces accordingly than the rapid rising of unit electric power consumption that does not but have with pulverizer.In addition, less than 1% o'clock, the unit electric power consumption of pulverizer rose slowly in the aspect ratio of back-up ring, and is very little for the influence of the unit electric power consumption of pulverizer as can be known.
According to above these reasons, so it is desirable to, being in ratio with the central diameter D of crushing rolls 3 by means of the height that makes above-mentioned back-up ring 15 is in 1～10% the scope, just can obtain the milling product that the particle mean size of milling product conforms to the rising of the unit electric power consumption of pulverizer, thereby can carry out high efficiency running with waste seldom.
In addition,, therefore, reducing mechanism is turned round in this scope because the aspect ratio of back-up ring can make the particle mean size ratio of milling product reduce in 3～8% scope effectively, so just can be to produce the fine powder product effectively.
Then, the problem of controlling the unit electric power consumption of pulverizer by means of the rotating speed of adjusting rotary table 2 is described.When the rotating speed of rotary table 2 rises, the power that vertical crusher 1 is consumed will rise, and this is self-explantory, so by adjusting the rotating speed of rotary table 2, just can control the unit electric power consumption of pulverizer.
Furtherly, as shown in figure 13, using the contemplated reducing mechanism of the present invention for example to pulverize, under the situation of cement clinker, changing the rotating speed of workbench, making raw material acceleration on the workbench at 12～15 radian per seconds
2(rad/sec
2) scope in the time, find that the particle mean size ratio of milling product has diminished.
In addition, drop into the raw material of 2A above the rotary table, be that the centrifugal force that utilizes the rotation owing to rotary table 2 to produce is dispersed in above the rotary table on the 2A, thereby pulverized by crushing rolls 3, still, under the slow situation of the rotary speed of rotary table 2, because raw material has been trapped in above the rotary table time lengthening on the 2A, the thickness of the raw material layer on rotary table on the 2A is blocked up, not only can not pulverize, and also can produce the problem of the power increase of pulverizer waste; Otherwise, under the fast situation of the rotary speed of rotary table 2, because it is short that raw material is trapped in above the rotary table time on the 2A, therefore the thickness of the raw material layer on the 2A is thin excessively on rotary table, can produce the problem that can not stably pulverize or the like again.Estimate the sort of result shown in Figure 13, just because of what these reasons caused.
In other words, the rotating speed of adjusting workbench can be controlled the unit electric power consumption of pulverizer, but the rotating speed of workbench has suitable scope, means if exceeding this scope makes under the situation that rotating speed of table changes, and then can not make the ability of device bring up to the height of expection.
Therefore, control at the rotating speed that changes workbench under the situation of unit electric power consumption of pulverizer, make the acceleration of the raw material on the workbench be in 12～15 radian per seconds
2(rad/sec
2) in the suitable like this scope, be very desirable then for carrying out fine powder effectively broken.
Below, illustrate among the present invention the amount of the raw material that ejects from vertical crusher 1 is measured, adjust and the amount of the raw material that control drops into from the outside, so that the constant method of the amount of the raw material of above-mentioned discharge.
Figure 14 represents the relation of the vibration of the unit electric power consumption of particle mean size, pulverizer of the unit electric power consumption of outlet conveyer of pulverizer and milling product and pulverizer.
Here, the unit electric power consumption of the outlet conveyer of so-called pulverizer, be meant the unit electric power consumption of the conveyer of the feedstock delivery of being pulverized with vertical crusher 1 to the grader 50, in the contemplated reducing mechanism of the present invention shown in Figure 1, it is the ratio of the weight (ton) of bucket elevator 41 electric power (kWh) that is consumed and the product that transports.
In addition, in the present embodiment, be by measuring the electric power that bucket elevator 41 is consumed, measure the raw material discharge rate of vertical crusher 1.
Can see too clearly from Figure 14, under the situation that the unit electric power consumption of the outlet conveyer of pulverizer increases, though the unit electric power consumption of pulverizer has improved, the particle mean size that milling product occurred is pulverized the not tendency of progress than also increasing.
In addition, under the situation that the unit electric power consumption of the outlet conveyer of pulverizer reduces, vibration occurred and increased gradually, the vibration of pulverizer is than the tendency that increases.This just means, in the unit interval, under the many situation of the raw material of being discharged by vertical crusher 1, because the amount of the raw material on the 2A has increased on rotary table, pulverizing can't be carried out, and under the few situation of the raw material of being discharged by vertical crusher 1 in the unit interval, because the amount of the raw material on the 2A has reduced on rotary table, can carry out though pulverize, the vibration of vertical crusher 1 has strengthened.
Therefore, the amount of the raw material that mensuration is discharged by vertical crusher 1 is adjusted from the above-mentioned reducing mechanism 100 outside amounts that drop into the raw material these vertical crushers 1, so that the amount of the raw material of above-mentioned discharge is constant, just can prevent vibration effectively, improve the efficient of pulverizing.
Below, a desirable method in this method is described: by measuring the electric power that bucket elevator 41 is consumed, the amount of the raw material that mensuration ejects from vertical crusher 1, control is from the input amount of belt conveyor 80 input raw materials, so that the outlet conveyer of pulverizer, promptly the unit electric power consumption of bucket elevator 41 is not vibrating and can stably carry out keeping certain in the scope of 0.3～0.7kWh/ton of high efficiency pulverizing.
According to breaking method of the present invention as explained above, because the tube mill that does not need in the previous methods to be put down in writing, can carry out high efficiency pulverizing with device simple in structure, in addition, owing to needn't all blow to the top to the whole raw materials after pulverizing with gas, therefore also not need very big pressure fan power.
And, according to breaking method of the present invention, by means of at least a factor of adjusting in the following various factors: the pulverizing pressure of the height of back-up ring, crushing rolls, the rotating speed of rotary table and the input amount that drops into the raw material in the vertical crusher, by making the unit electric power consumption of above-mentioned pulverizer be in the scope of 1～30kWh/ ton (ton), just can make it waste seldom the running that efficient is very high.
In addition, in second invention, the pulverizing pressure by making crushing rolls is in the scope of 0.6～0.8MPa, and the unit electric power consumption that makes pulverizer just can effectively be pulverized cement raw material in the scope of 5～10kWh/ ton (ton).
In the 3rd invention, the pulverizing pressure by making crushing rolls is in the scope of 0.8～1.1MPa, and the unit electric power consumption that makes pulverizer just can effectively be pulverized the cement clinker raw material in the scope of 20～25kWh ton (ton).
In the 4th invention, the pulverizing pressure by making crushing rolls is in the scope of 0.8～1.1MPa, and the unit electric power consumption that makes pulverizer just can effectively be pulverized raw materials of slag in the scope of 25～30kWh/ ton (ton).
In the 5th invention, by selecting the suitable height of back-up ring, the height that makes back-up ring, with regard to the problem of the waste power that can not take place to take place owing to the aspect ratio of back-up ring is excessive, just can stably be pulverized in 1～10% scope with respect to the ratio of the central diameter of crushing rolls.
In the 6th invention, mensuration is by the amount of the raw material that vertical crusher ejected, and adjusts the amount that drops into the raw material this vertical crusher from the outside of reducing mechanism, so that the amount of the raw material of being discharged is constant, just can prevent that vertical crusher from vibrating, and effectively pulverizes.
Claims (6)
1. breaking method, it uses reducing mechanism, this reducing mechanism has: vertical crusher and will pulverize by this vertical crusher after raw material be separated into the grader of meal and fine powder, this vertical crusher is provided with a plurality of taper crushing rolls that can freely rotate on its rotary table, by apply the pulverizing pressure of regulation to this crushing rolls, with the raw material pulverizing that drops on this rotary table, wherein the upper surface of this rotary table is roughly made the tabular and peripheral part this rotary table of horizontal circle and is provided with back-up ring along circumference; Raw material after this grader is pulverized this vertical crusher is separated into meal and fine powder, and this meal is got back in this vertical crusher, pulverize once more, and, to eject as this fine powder of product, it is characterized in that, by adjusting at least a factor in the following various factors: the pulverizing pressure of the height of this back-up ring, this crushing rolls, the rotating speed of this rotary table and the input amount that drops into the raw material in the vertical crusher are controlled at pulverizer unit's electric power consumption of this vertical crusher in the scope of 1～30kWh/ ton.
2. breaking method as claimed in claim 1 is characterized in that, the pulverizing pressure of above-mentioned crushing rolls is set in the scope of 0.6～0.8MPa, and above-mentioned pulverizer unit electric power consumption is set in the scope of 5～10kWh/ ton, carries out the pulverizing of cement raw material.
3. breaking method as claimed in claim 1, it is characterized in that, the pulverizing pressure of above-mentioned crushing rolls is set in the scope of 0.8～1.1MPa, and above-mentioned pulverizer unit electric power consumption is set in the scope of 20～25kWh/ ton, carries out the pulverizing of cement clinker.
4. breaking method as claimed in claim 1 is characterized in that, the pulverizing pressure of above-mentioned crushing rolls is set in the scope of 0.8～1.1MPa, and the unit electric power consumption of above-mentioned pulverizer is set in the scope of 25～30kWh/ ton, carries out the pulverizing of slag.
5. as the described breaking method of any one claim in the claim 1～4, it is characterized in that the height setting of above-mentioned back-up ring is in 1～10% scope of the central diameter of crushing rolls.
6. as the described breaking method of any one claim in the claim 1～5, it is characterized in that, the amount of the raw material that mensuration is discharged by above-mentioned vertical crusher, and adjust the amount that drops into the raw material this vertical crusher from the outside of above-mentioned reducing mechanism, so that the amount of the raw material of this discharge is constant.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP30473/2002 | 2002-02-07 | ||
| JP2002030473 | 2002-02-07 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1627991A true CN1627991A (en) | 2005-06-15 |
| CN100368092C CN100368092C (en) | 2008-02-13 |
Family
ID=27677905
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB03803378XA Expired - Lifetime CN100368092C (en) | 2002-02-07 | 2003-02-07 | Milling method |
Country Status (3)
| Country | Link |
|---|---|
| JP (1) | JPWO2003066220A1 (en) |
| CN (1) | CN100368092C (en) |
| WO (1) | WO2003066220A1 (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102872958A (en) * | 2012-09-26 | 2013-01-16 | 佛山市博晖机电有限公司 | Grinding process of ceramic raw material and ceramic raw material grinding production line |
| CN101664707B (en) * | 2008-09-02 | 2013-01-30 | 浙江明峰水泥有限公司 | Slag micropowder superfine open-circuit production line |
| CN102985185A (en) * | 2010-05-07 | 2013-03-20 | 明宇微米系统有限公司 | Device for pulverizing and distribution transferring for coal |
| CN107737642A (en) * | 2017-11-20 | 2018-02-27 | 重庆嘉韵实业有限公司 | The production line and its technique of a kind of flyash |
| CN109926164A (en) * | 2019-04-27 | 2019-06-25 | 南京凯盛国际工程有限公司 | A kind of Novel rocker arm grinding roller structure |
Families Citing this family (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AU2010347572B8 (en) * | 2010-03-05 | 2014-12-18 | Loesche Gmbh | Preparation method for stainless steel slags and steelmaking slags for recovering metal |
| JP5906782B2 (en) * | 2012-02-13 | 2016-04-20 | 宇部興産機械株式会社 | Vertical crusher |
| CN105080698B (en) * | 2014-05-14 | 2018-10-12 | 天津水泥工业设计研究院有限公司 | Use the grinding process of vertical roller grinder system |
| CN104437757B (en) * | 2014-09-23 | 2016-06-01 | 南京凯盛国际工程有限公司 | A kind of pre-grinding vertical |
| JP6492690B2 (en) * | 2015-01-23 | 2019-04-03 | 宇部興産機械株式会社 | How to operate the vertical crusher |
| US10646877B2 (en) * | 2017-03-13 | 2020-05-12 | General Electric Technology Gmbh | System and method for adjusting a material bed depth in a pulverizer mill |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN85106642B (en) * | 1985-09-03 | 1988-12-14 | 川崎重工业株式会社 | Classifier and controller for vertical roller mill |
| US4714202A (en) * | 1986-02-12 | 1987-12-22 | Combustion Engineering, Inc. | Pulverized solid control system |
| JP2817859B2 (en) * | 1991-09-03 | 1998-10-30 | 宇部興産株式会社 | Vertical crusher |
| JP3074656B2 (en) * | 1992-01-21 | 2000-08-07 | 宇部興産株式会社 | Crushing equipment |
| JP3422932B2 (en) * | 1998-05-29 | 2003-07-07 | 株式会社神戸製鋼所 | Aggregate production method and apparatus |
| JP2001224973A (en) * | 2000-02-16 | 2001-08-21 | Ube Ind Ltd | Vertical type pulverizing machine for manufacturing crushed sand |
-
2003
- 2003-02-07 JP JP2003565638A patent/JPWO2003066220A1/en active Pending
- 2003-02-07 WO PCT/JP2003/001315 patent/WO2003066220A1/en active Application Filing
- 2003-02-07 CN CNB03803378XA patent/CN100368092C/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101664707B (en) * | 2008-09-02 | 2013-01-30 | 浙江明峰水泥有限公司 | Slag micropowder superfine open-circuit production line |
| CN102985185A (en) * | 2010-05-07 | 2013-03-20 | 明宇微米系统有限公司 | Device for pulverizing and distribution transferring for coal |
| CN102872958A (en) * | 2012-09-26 | 2013-01-16 | 佛山市博晖机电有限公司 | Grinding process of ceramic raw material and ceramic raw material grinding production line |
| CN107737642A (en) * | 2017-11-20 | 2018-02-27 | 重庆嘉韵实业有限公司 | The production line and its technique of a kind of flyash |
| CN109926164A (en) * | 2019-04-27 | 2019-06-25 | 南京凯盛国际工程有限公司 | A kind of Novel rocker arm grinding roller structure |
Also Published As
| Publication number | Publication date |
|---|---|
| WO2003066220A1 (en) | 2003-08-14 |
| JPWO2003066220A1 (en) | 2005-05-26 |
| CN100368092C (en) | 2008-02-13 |
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