• 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:
    Grinder housing of a pressure chamber grinder, which said grinder housing comprises a substantially cylindrical outer mantle (1), end walls (2, 3), at least two accelerating nozzles (4) passing radially through the outer mantle (1), between which said nozzles there is an obtuse angle, as well as a discharge opening (5) made into one of the end walls (3) for the ground product. The invention is characterized in that the grinder housing is provided with a substantially cylindrical partition wall (6), which is in itself known, centrally located, and which surrounds the grinding chamber (7) proper and is provided with an inlet opening (9) facing the orifice of each accelerating nozzle, preferably terminating at the plane of the inner face of the outer mantle (1), that the annular space surrounding the partition wall (6) is a gas removing chamber (8) to which an exhaust duct (10) passing through the outer mantle is connected for the removal of the excess quantity of working gas discharged out of the solids-working-gas jets of the accelerating nozzles (4) into the gas removing chamber (8).
    公开号:SU1627077A3
    申请号:SU874202732
    申请日:1987-05-15
    公开日:1991-02-07
    发明作者:Ниеми Йоуко
    申请人:Ой Финнпулва Аб (Фирма)；
    IPC主号:
    专利说明:

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    The invention relates to the design of jet mills and can be used in the construction, mining and other industries.
    The purpose of the invention is to increase the efficiency of the grinding
    ma figure 1 shows a jet mill, top view; FIG. 2 is a section A-A in FIG.
    The jet mill contains a cylindrical body 1, end walls 2 and 3, preferably two accelerator nozzles 4, passing radially through the body 1, the nozzles forming an obtuse angle between them, and an outlet 5 for a crushed product made in the end wall 3 In the mill housing there is a cylindrical separation wall 6 in the center, which divides the housing into a grinding chamber 7 and a gas removal chamber 8 surrounding the chamber 7 Acceleration nozzles 4
    preferably terminated precisely in the plane of the inner surface of the housing 1. In the dividing wall 6 there is an outlet 9 facing the jet of each accelerating nozzle 4. An outlet 10 for the working gas to the outer surface of the housing 1 is attached to the chamber 8 to remove the gas from gas jets moving rapidly through accelerator nozzles 4
    Jet mill works as follows.
    A pre-crushing gas jet consisting of a pressurized pre-crushing chamber is divided into equivalent jet components, the number of which is equal to the number of accelerator nozzles 4. These consist of separate components. The guns are passed into the accelerator nozzles 4 in which speed
    jets rise to supersonic level under the action of pressure of the working gas. Most of the quantity of working gas in the stream from the gas material is separated from the indicated stream in the gap between the nozzles of the accelerator nozzle 4 and the inlet 9 located in the separation wall 6, and flows through the gap into the chamber 8 to remove the gas, while Some of the small fractions in the stream from the gas material also follow. Only the rougher particles continue their movement directly into the crushing chamber 7, where in the first crushing zone A formed in the middle of chamber 7, these particles collide with particles of material coming out of another accelerator nozzle and are crushed. Those particles that randomly pass through crushing zone A without coming into contact with any material particles that are rapidly moving in the opposite direction continue to pass them straight ahead and ultimately hit the partition wall 6 in the second crushing zone, formed on the opposite side of the grinding chamber 7. This method is possible, since the larger Particles of material that are to be crushed move along a linear path, following along the longitudinal axis of the accelerator nozzles 4, and fine particles of the material, which correspond to the size of the finished product, move closer to the inner walls of the accelerator nozzles. To ensure that the solid particles still have the kinetic energy required to ensure crushing even in the second crushing zone B, the pressure of the working gas in the conical part of the accelerator nozzles 4 should be kept positive and be at least 0.3 bar.
    The size and shape of the inlet openings 9 in the separation wall 6, as well as the size of the crushing chamber 7 itself, are chosen in accordance with the properties and composition of the material to be crushed, as well as in accordance with the properties of the desired finished product.
    In the outlet channel 10, there is preferably a control valve (not shown) whereby the amount of gas removed from the jets of the gas-material of the accelerator nozzles 4 through the chamber 8 to remove the gas is regulated.
    In order to prevent abrasion of the inner surface of the dividing wall 6 as a result of crushing, the inner side of the wall 6 is lined with wear-resistant material, for example, ceramic tiles or plates made of hard metal. Tiles or plates should be installed so that the particles of the material intended for grinding - nor, they collided with their surfaces virtually perpendicularly.
    In order to enhance the removal of the working gas, the chamber 8 for the removal of gas in the crusher body can advantageously be provided with an inlet pipe 11 for a rapid flow of air provided by the control valve 12. In this case, the control valve located in the exhaust channel 10 can not installed The inlet pipe 11 for the rapid flow of air and the outlet channel 10 for the working gas are preferably installed on opposite sides of the crusher body in the central part between the accelerator nozzles 4 so that the inlet pipe 11 is located on the side of the largest angle between the accelerator nozzles 4. In this case, the jet
    the gas material, which is rapidly moving from the accelerator nozzles 4, under the action of the inflowing air, to a greater degree turn towards each other so that the crushing resulting from the collision is intensified.
    If, in addition to the working gas, it is also assumed that particles of material smaller than a certain size are removed from the material-gas streams, nozzles 13 can be installed for rapid air flow between the nozzles of the accelerator nozzles 4 and the corresponding inlet holes 9 in the separation wall 6, and the nozzles 13 contain the first channel
    13a, which actually monitors the shape of the flow channels in the acceleration nozzles 4 and is intended for a jet of material-gas rapidly moving from the acceleration nozzle 4, and the second channel 13b,
    having the shape of a venturi and passing through the first channel, for a rapid flow of air at the side.
    Since most of the working gas contained in the streams of the material gas,
    leaves the crusher body through the outlet 10, the outlet 5 for the crushed product, which is located in the crusher body, can be directly connected to the receiving and storage
    a container (not shown) for the crushed product, in which the rest of the working gas, if any, can be separated from the crushed product.
    To eliminate the possibility that a particle in a jet of material is rapidly
    Moving from one of the accelerating nozzles 4 can penetrate the opposite accelerating nozzle 4, which is very disadvantageous in terms of energy saving and besides destroys the end part in this accelerating nozzle 4, the obtuse angle between the accelerating nozzles 4 should preferably be less than 170 °.
    权利要求:
    Claims (4)
    [1]
    1. A jet mill comprising a body, end walls, preferably two accelerator nozzles, forming a mutual obtuse angle, as well as a discharge opening in one of the end walls, in order to increase the efficiency of the crushing process, the mill provided with a cylindrical dividing wall with an inlet orifice located coaxially with the housing, in the form of a crushing chamber, said wall has openings coaxial with the nozzles, preferably in the plane of the inner front surface of the housing th space between the wall and the housing ob- forms a gas removal chamber, wherein
    An outlet channel through the housing is connected to remove excess working gas discharged from the jets of particles of the working gas of the accelerator nozzles into the chamber to remove the gas.
    [2]
    2. The mill according to claim 1, in which it is provided that the exhaust gas channel of the working gas is provided with a control valve.
    [3]
    3. Mill on the PP. 1 and 2, characterized in that the air inlet and the working gas outlet are on opposite sides of the body in the central plane between the two acceleration nozzles, and the inlet is made on the side of the body where the mutual angle between the accelerator nozzles is larger.
    [4]
    4. Mill on PP. 1-3, characterized in that air flushing nozzles opposing the accelerator nozzles are mounted in the gas removal chamber, the air flushing nozzles have a first channel that repeats the channel shape in the accelerating nozzles, and a second channel having the shape of a venturi tube passing through first channel.
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    类似技术:
    公开号 | 公开日 | 专利标题
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    同族专利:
    公开号 | 公开日
    NO871940D0|1987-05-11|
    FI74222C|1988-01-11|
    JPH0374138B2|1991-11-26|
    DK247087A|1987-05-14|
    JPS63501695A|1988-07-14|
    DE3663338D1|1989-06-22|
    WO1987001617A1|1987-03-26|
    NO165430B|1990-11-05|
    DK247087D0|1987-05-14|
    AT43076T|1989-06-15|
    EP0236469A1|1987-09-16|
    AU582280B2|1989-03-16|
    US4768721A|1988-09-06|
    FI853592A0|1985-09-18|
    NO165430C|1991-02-13|
    FI853592L|1987-03-19|
    EP0236469B1|1989-05-17|
    FI74222B|1987-09-30|
    AU6401986A|1987-04-07|
    NO871940L|1987-05-11|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    EA000001B1|1996-03-12|1997-03-31|Владимир Иванович Размаитов|The equipment for grinding of materials|US2588945A|1948-06-29|1952-03-11|Micronizer Company|Means inhibiting escape of oversize particles from circulatory pulverizing mills|
    US3559895A|1968-02-20|1971-02-02|Edwin F Fay|Apparatus for and method of comminuting solid materials|
    US4502641A|1981-04-29|1985-03-05|E. I. Du Pont De Nemours And Company|Fluid energy mill with differential pressure means|
    FI63869C|1981-11-27|1983-09-12|Jouko Niemi|TRYCKKAMMARKVARN|FI86514C|1990-12-19|1992-09-10|Finnpulva Ab Oy|Mill chamber for a counter-jet mill|
    JP2527297B2|1993-10-01|1996-08-21|ナノマイザー株式会社|Material atomizer|
    US5683039A|1996-03-28|1997-11-04|Xerox Corporation|Laval nozzle with central feed tube and particle comminution processes thereof|
    GB2339709B|1998-07-27|2002-05-29|Xerox Corp|Apparatus for grinding particulate material|
    US6138931A|1999-07-27|2000-10-31|Xerox Corporation|Apparatus and method for grinding particulate material|
    US6230995B1|1999-10-21|2001-05-15|Micropulva Ltd Oy|Micronizing device and method for micronizing solid particles|
    WO2005028115A1|2003-09-19|2005-03-31|Micropulva Ltd Oy|Improved acceleration nozzle for gas-solids suspension|
    ES2355967T3|2008-04-02|2011-04-01|Evonik Degussa Gmbh|DEVICE AND PROCEDURE TO CARRY OUT CHEMICAL AND PHYSICAL CONVERSIONS OF MATERIALS.|
    JP6621370B2|2016-05-16|2019-12-18|中越パルプ工業株式会社|Opposing collision processing device|
    FR3072307B1|2017-10-12|2019-11-15|Commissariat A L'energie Atomique Et Aux Energies Alternatives|CRYOGENIC MILLING DEVICE AND METHOD WITH CONFLUENT JETS|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FI853592A|FI74222C|1985-09-18|1985-09-18|KVARNHUS FOER TRYCKAMMARKVARN.|
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