CN2897430Y - Accelerating crusher of circulating air-flow impeller - Google Patents

Accelerating crusher of circulating air-flow impeller Download PDF

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Publication number
CN2897430Y
CN2897430Y CN 200620090504 CN200620090504U CN2897430Y CN 2897430 Y CN2897430 Y CN 2897430Y CN 200620090504 CN200620090504 CN 200620090504 CN 200620090504 U CN200620090504 U CN 200620090504U CN 2897430 Y CN2897430 Y CN 2897430Y
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China
Prior art keywords
impeller
separator
cabinet
case
accelerating
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Expired - Fee Related
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CN 200620090504
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Chinese (zh)
Inventor
张歌今
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Individual
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Individual
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Priority to CN 200620090504 priority Critical patent/CN2897430Y/en
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Abstract

An impeller accelerating crusher with airflow circulation is to solve problems such as much energy consumption, low efficiency, influence to purity and fineness in prior technology. The utility model frame is fixed with a machine box and a power device with features as: a semi-enclosed impeller in the case is to form an accelerating crushing device with impeller; an inlet and an outlet of the case are connected with a separation device respectively; the separation device is a separator, a tangential inlet stays at upside profile of such separator, and the tangential inlet is connected to the outlet of the case by means of connect pipe and the low part of the separator is connected with the inlet of the case by means of connect piping to form an airflow circulation separation system, which is characterized in that strong crushing capacity to crush grain to nanometer level with high utilization rate of valid energy. The separation device gives circulating separation to stuff and super-fine powder escape from the outlet and uncrushed powder enters crusher again until total crushing.

Description

The air-flow circulation impeller is quickened pulverizer
Technical field
The utility model belongs to a kind of disintegrating apparatus, and particularly a kind of air-flow circulation impeller is quickened pulverizer.
Background technology
At present, superfine communication technique extensive use in the every field of national economy, and become enhance product performance, the effective ways of quality, class and economic value added, caused the attention and the concern of various circles of society, various micron ultra shifters also arise at the historic moment.At present, ultramicro grinding equipment mainly contains ball mill, Raymond machine, eddy mill, high pressure homogenizer, colloid mill or the like.Because therefore the crushing process more complicated, does not set up complete crushing mechanism in the pulverizing field, ubiquity two hang-ups, the one, and the effective energy utilization rate that is used to pulverize is extremely low, pulverizes the energy consumption height, and the 2nd, the fiber-like material is difficult to ultramicro grinding.In addition, material is subjected to strong extruding, the shearing that is listed as, grinds, cuts mechanisms such as stranding, turbulence in the process of pulverizing, though reached the purpose of comminuting matter, but material appearance heavy metal break flour particulate in various degree in the process of accepting the metal material grinding is peeled off to be disengaged, as disengaging of heavy metals such as chromium, nickel, cadmium, titanium, iron, copper, lead, aluminium, arsenic, make the material of ultramicro grinding be subjected to severe contamination.As colloid mill, this micron ultra shifter is pulverized material in the mode of extruding and grinding.It mainly is made of the stator that has the truncated cone chamber that rotor and of support, casing, actuating unit and a truncated cone shape cooperates with rotor.On the conical surface of rotor and stator, have the tooth lapping that to shear each other respectively, the awl chamber of its stator is respectively different taperings with the cone of rotor, thereby between the feed end stator of bistrique and rotor, form the certain included angle gap, utilize this gap coarse fodder particle of nipping, and relatively rotating along with rotor and stator, the minimum clearance place that the coarse fodder particle is ground gradually cooperate with rotor into stator is broken into fine particles with its grounds travel.In the process that material is pulverized; the surface of stator and rotor also can be ground; the metal particle that comes off on stator and the rotor can enter into material; material is polluted; or purity is affected; especially bigger for the harm of pharmaceutical, foodstuff material, particularly when being crushed to 5 microns left and right sides, further pulverize very difficult.
Summary of the invention
The technical problems to be solved in the utility model is, problems such as energy consumption height, the efficient that overcomes above-mentioned prior art existence is low, purity is influenced, fineness is restricted provide a kind of output height, energy consumption air-flow circulation impeller low, pollution-free, that can carry out the nanoscale pulverizing to quicken pulverizer.
The utility model has a frame, cabinet and power set are housed on frame, its special character is, semiclosed impeller is housed in cabinet, constitute impeller and quicken reducing mechanism, the feeding end of cabinet is connected with separator respectively with discharge end, described separator has a separator, upper side at separator has a tangential feeding mouth, tangential feeding mouth is connected with the discharge end of cabinet by tube connector, the lower end of separator is connected with the feeding end of cabinet by tube connector, constitutes air-flow circulation piece-rate system.
Described semiclosed impeller level or vertical the setting are to satisfy different needs.
Advantage of the present utility model is:
1, adopt semiclosed impeller as reducing mechanism, material is carried out high-speed impact, the centrifugal air draught effect of impeller makes the directed acceleration of material, strike again on the inwall of cabinet and separator, make material carry out multiple irregular bump and friction, simultaneously at impeller and cabinet inwall, also frictional impact between the material, thereby grindability of the present utility model is strong, effective energy utilization rate height, and material can be crushed to nanoscale.
2, separator is installed on reducing mechanism, reducing mechanism is pulverized material, material is quickened, form the high velocity air that carries material, circular flow in separator, and in the process of operation, material is separated, to reach the ultra micro powder of pulverizing requirement and discharge from outlet, the material of Fen Suiing does not then reenter in the reducing mechanism, pulverizes once more, and circulation repeatedly, up to pulverizing fully.
3, in the process of pulverizing, impeller does not contact, does not grind with cabinet and other parts, and can determine the material of semiclosed impeller according to the difference of comminuting matter material, thereby, pollution-free to material, be particularly suitable for foodstuff, drug class or high-purity rare mineral matter material grinding.
Description of drawings
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the left view of Fig. 1;
Fig. 3 is the vertical view of Fig. 1;
Fig. 4 is that the A of Fig. 1 is to view;
Fig. 5 is the structural representation of the semiclosed impeller of the utility model;
Fig. 6 is the vertical view of Fig. 5;
Fig. 7 is the structural representation of another embodiment of the utility model;
Fig. 8 is the vertical view of Fig. 7.
The specific embodiment
Embodiment 1:
As Fig. 1, Fig. 2, Fig. 3, Fig. 4, Fig. 5 and shown in Figure 6, the utility model has a frame 1, and the welding of frame 1 usefulness section bar is made; Cabinet 17 and power set are housed on frame 1, and described cabinet 17 is horizontally disposed with, and the casing of cabinet 17 is an involute shape, and two discharging openings are arranged, so that produce the air-flow of friction speed; Described power set are made of motor 6, belt pulley 2, belt pulley 4 and driving belt 3, motor 6 is installed on the frame 1, belt pulley 4 is installed on the output shaft of motor 6, belt pulley 2 is installed on the turning cylinder 7, driving belt 3 is installed on belt pulley 2 and the belt pulley 4, drives turning cylinder 7 rotations; Described turning cylinder 7 is installed on the bearing block 5, and bearing block 5 is installed on the frame 1; Semiclosed impeller 8 is housed in cabinet 17, and described semiclosed impeller 8 is horizontally disposed with, and semiclosed impeller 8 is fixed on the turning cylinder 7, constitutes impeller and quickens reducing mechanism; Described semiclosed impeller 8 has a wheel hub 21, a circular bottom plate 20 is arranged on wheel hub 21, several blades 19 are arranged on circular bottom plate 20, blade 19 is uniform on circular bottom plate 20, wheel hub 21, circular bottom plate 20 and blade 19 threes weld together, constitute an integral body, the material of blade 19 and circular bottom plate 20 can be determined according to the difference of comminuting matter material, when pulverizing plant material, blade 19 and circular bottom plate 20 will be passed through Wear-resistant Treatment, when comminution of minerals pledge material need keep purity, the material of manufacturing blade 19 and circular bottom plate 20 was identical with the material of institute's comminuting matter; On blade 19, also has an annular side plate 18, to improve the bulk strength of semiclosed impeller 8; The feeding end of cabinet 17 is connected with separator respectively with discharge end, and described separator has a separator 12, and separator 12 is conical, its upper end is big, the lower end is little, has a ultra micro powder to go out 13 at its top, reaches the ultra micro powder of pulverizing requirement and goes out 13 to discharge from the ultra micro powder; Upper side at separator 12 has a tangential feeding mouth, makes the air-flow that carries material enter separator 12 backs and produces rotation, forms the cyclone type air-flow; Described tangential feeding mouth is connected by tube connector 14, tube connector 15 and the discharging opening of tube connector 16 with cabinet 17, described tube connector 16 is three trouble shapes, wherein, two is feeding mouth, one is discharging opening, two feeding mouths are connected with two discharging openings of cabinet 17, and a discharging opening is connected with tube connector 15; The lower end of separator 12 is connected by the feeding mouth of tube connector 9 with cabinet 17, and impeller quickens to pulverize, cyclone type air-flow circulation piece-rate system thereby constituted, and material is progressively pulverized in circulation, separating process; Also have a wind-supplying mouth 10 and a feeding mouth 11 on tube connector 9, material enters into cabinet 17 by feeding mouth 11, and the effect of wind-supplying mouth 10 is constantly to replenish a part of wind in cabinet 17, to accelerate flowing of air-flow.
Embodiment 2:
As shown in Figure 7 and Figure 8, its structure such as embodiment 1, difference is, described power set are a motor 6, and semiclosed impeller 8 is directly installed on the output shaft of motor 6, and motor 6 is installed on the frame 23, one end height of frame 23, an end is low, to save material; Described cabinet 22 and semiclosed impeller 8 vertical settings are to satisfy different needs; The casing of cabinet 22 is an involute shape, and its discharging opening is one, and the tangential feeding mouth of separator 12 is connected with the discharging opening of tube connector 24 with cabinet 22 by tube connector 25; The lower end of separator 12 is connected by the feeding mouth of tube connector 26 with cabinet 22, and impeller quickens to pulverize, cyclone type air-flow circulation piece-rate system thereby constituted, and wind-supplying mouth 10 and feeding mouth 11 are arranged on the tube connector 26.

Claims (2)

1, a kind of air-flow circulation impeller is quickened pulverizer, it has a frame, cabinet and power set are housed on frame, it is characterized in that, semiclosed impeller is housed in cabinet, constitute impeller and quicken reducing mechanism, the feeding end of cabinet is connected with separator respectively with discharge end, described separator has a separator, upper side at separator has a tangential feeding mouth, tangential feeding mouth is connected with the discharge end of cabinet by tube connector, and the lower end of separator is connected with the feeding end of cabinet by tube connector.
2, air-flow circulation impeller according to claim 1 is quickened pulverizer, it is characterized in that described semiclosed impeller level or vertical the setting.
CN 200620090504 2006-04-21 2006-04-21 Accelerating crusher of circulating air-flow impeller Expired - Fee Related CN2897430Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 200620090504 CN2897430Y (en) 2006-04-21 2006-04-21 Accelerating crusher of circulating air-flow impeller

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 200620090504 CN2897430Y (en) 2006-04-21 2006-04-21 Accelerating crusher of circulating air-flow impeller

Publications (1)

Publication Number Publication Date
CN2897430Y true CN2897430Y (en) 2007-05-09

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101678402A (en) * 2007-05-15 2010-03-24 株式会社理光 Pulverizing and coarse powder classifying apparatus and fine powder classifying apparatus
CN103743198A (en) * 2013-12-31 2014-04-23 夏跃金 Circulating fluidized bed device with drying and crushing functions
CN103743197A (en) * 2013-12-31 2014-04-23 昆明特康科技有限公司 Circulating fluidized bed jet mill
CN104729269A (en) * 2013-12-31 2015-06-24 昆明特康科技有限公司 Medicine and edible material processing device

Cited By (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101678402A (en) * 2007-05-15 2010-03-24 株式会社理光 Pulverizing and coarse powder classifying apparatus and fine powder classifying apparatus
CN101678402B (en) * 2007-05-15 2014-05-07 株式会社理光 Pulverizing and coarse powder classifying apparatus and fine powder classifying apparatus
CN103743198A (en) * 2013-12-31 2014-04-23 夏跃金 Circulating fluidized bed device with drying and crushing functions
CN103743197A (en) * 2013-12-31 2014-04-23 昆明特康科技有限公司 Circulating fluidized bed jet mill
CN104729269A (en) * 2013-12-31 2015-06-24 昆明特康科技有限公司 Medicine and edible material processing device
CN104764298A (en) * 2013-12-31 2015-07-08 昆明特康科技有限公司 Circulating fluidized bed equipment
CN103743198B (en) * 2013-12-31 2015-10-21 楚雄博杉科技有限公司 There is circulating fluidised bed apparatus that is dry and crushing function
CN104729269B (en) * 2013-12-31 2019-05-24 云南崔三七药业股份有限公司 Medicine, edible materiel machining equipment
CN104764298B (en) * 2013-12-31 2019-05-28 昆明特康科技有限公司 Circulating fluidised bed apparatus

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C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20070509

Termination date: 20100421