• 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:
    A method and apparatus for conveying particulate material of the type wherein it is desired that the material be simultaneously pre-compacted from a generally loose state to a more or less solid "plug" state. A screw conveyor is arranged to deliver loose particulate material to an intermediate chamber at the end of the screw conveyor means wherein the material is pre-compacted by the action of the screw conveyor. Following the intermediate chamber, a piston reciprocating coaxially with the screw conveyor further urges the material in a direction coaxial with the centerline of the screw conveyor to further advance the material through a straight coaxial conduit within which the material becomes compacted to an increased degree of compactness, solely by the action of the reciprocating piston. The reciprocating piston has preferably an annular face, whose outside diagram is generally the same as that of the Industrial Design of the conduit. The second, high degree of compactness is thus achieved solely by the action of the piston. Accordingly, the mounting of the screw conveyor is not subjected to extreme forces. The device is capable of compacting, for instance, fibrous material of a relatively low fibre shear strength to an extremely high compactness without exceeding the fibre shear limit in the area of the screw conveyor. Frictional drag in the conduit following the apparatus may be increased by vanes protruding inside of the conveyor. The depth of the friction increasing vanes may be selectively adjustable.
    公开号:SU929004A3
    申请号:SU782587605
    申请日:1978-01-23
    公开日:1982-05-15
    发明作者:Буртхам Браун Дуглас
    申请人:Стейк Текнолоджи Лтд(Фирма)；
    IPC主号:
    专利说明:

    The invention relates to hoisting machinery, namely, to screw conveyors for transporting loose, loose, fibrous material into the pipeline.
    A known method of transporting material, comprising feeding the material with a screw conveyor into the chamber under pressure, where then the material is sealed with a piston 11].
    The disadvantage of this method is that it cannot be used for transporting loose, fibrous material.
    The closest technical solution to the proposed method of transporting material is a method of transporting material, which consists in the fact that the material from the output of the feed hopper to the processing zone of the material is transported by an auger in the axial direction and the material is compacted with it in the first zone [2).
    A disadvantage of this method is that this method but nevozmozh2 compacted material to a degree of compaction needed for further processing of the material, and a low efficiency, 6 NOSTA transportation.
    The closest technical solution to the proposed device is a device for transporting material, including a cylindrical housing with a feed hopper and an unloading hole, a screw placed in the housing, a pipeline fixed coaxially to the housing ”and drive Г2].
    .
    The purpose of the invention is to increase the efficiency of transportation.
    This goal is achieved by the fact that the material is discharged into the second .-. 20th zone, located coaxially with the first and immediately behind it, and behind. > m it is additionally compacted by means of a coaxial pulsating force in the second zone and further 25 ’further translational movement is carried out
    929004 4 materials coaxially with the longitudinal axis of the screw.
    This method is carried out, for example, by one embodiment of a device for transporting material $ in the form of particles.
    The specified device for transportation in the form of particles, including a cylindrical housing with a feed hopper and an unloading hole, a screw placed in the housing, a pipeline fixed coaxially to the housing, and the drive, is equipped with an annular piston and an intermediate chamber located at the end of the piston and is 15 'with the частью the diameter of the cylindrical body.
    The transportation method can be carried out by the second embodiment 25 of the device for transporting material in the form of particles.
    A device for transporting material in the form of particles, including a cylindrical housing with a feed hopper and an unloading hole, a screw located in the housing, a pipeline fixed coaxially to the housing and the pipeline, equipped with a piston and an intermediate chamber made in the form of a truncated housing located coaxially with the screw, the larger base of which is facing to the screw and corresponds to its diameter, and the smaller to the pipeline and correspond to its internal diameter, while the front surface of the piston is made in the form of a continuous circle new surface.
    In FIG. 1 shows a device for transporting material in the form of particles, a General view, the first option; FIG. 2 - the same, top view; FIG. 3 ~ same side view; FIG. 4 node 1 in figure 1; FIG. 5 schematically shows the movement of material from one zone to another; FIG. 6 - shows a device, General view, the second option; FIG. .7 - the same, a top view; FIG. 8 is the same side view.
    A device for transporting material (the first option) consists of a feed hopper 1, a cylindrical housing 2, an unloading hole 3. In the housing 2 there is a screw 4. The pipe 5 is fixed 1 to the housing 2. Outside of the cylindrical housing, a hollow piston 6 is installed the possibility of reciprocating movement in the intermediate chamber 7. The outer diameter of the piston 6 corresponds to the inner diameter of the pipe 5. In the latter, through holes 8 are made in the axial direction, in which the plates 9 are placed, having a horizontal surface protruding above the surface of the pipeline and an inclined surface located inside the pipeline. The height | of the inclined surface increases towards the transportation of the material. To adjust the plates 9 in height, a regulation mechanism is used
    10.
    A device for transporting material in the form of particles works as follows.
    When the drive 11 is turned on, the auger 4 starts to rotate and feed material from the hopper 1 in the direction of the breach chamber 7, which at that time is the first sealing zone, since it is compacted with the auger while transporting the material. When the material completely fills the entire cross section at the inlet of the pipeline, then it translationally moves using the reciprocating motion of the hollow piston 6, the end of which pushes the accumulated mass in the direction of the second zone 12, which leads to further compaction of the material forming the briquette, the density of which increases significantly by compared with the density in the chamber 7, in which the material leaves the area of the screw.
    Thus, the translational movement of the compacted mass through the pipeline 5 is carried out only under the influence of the reciprocating movement of the hollow piston 6, and the material is continuously fed to the pipeline by the screw 4. The action of the piston 6 of the reciprocating movement is shown schematically in Fig. 5 "where zone A shows fibrous material in the state of pre-compaction, translationally moving under the action of the screw 4 into the pipe 5 · Reciprocating moving piston 6 is additionally compacted the material to a high degree of compactness, which is achieved in zone B of the pipeline 5 · Due to the annular shape of the front of the piston 6 and the translational movement of the material through the pipe 5, stresses within the compacted mass are considered to have an arcuate shape, which contributes to the longitudinal strength of the formed compact briquette in zone B.
    To achieve even greater compaction in the area of the pipeline 5, the material is subjected to a force that frictionally slows down the surface of the specified mass of material. This force is regulated by installing the plates 9 by the control mechanism 10 at a certain depth of penetration into the material. The deeper the penetration of the plates 9, the greater the friction force of braking, respectively, of the plate. They can control the degree of compaction of the material.
    I Transport device 25 (second option) consists of a cylindrical housing 13 with a feed hopper 14 and an unloading hole 15 · Inside the housing 13, a screw 16 is placed. Coaxially to the housing 13, a pipe 3Q wire 17 is fixed, the drive is indicated by 18. The screw is fixed on the hollow shaft 19 which is rotatably supported by bearings 20, housed in support 21 and sprocket 22. unloading 35 otvers- term 15 is connected to an intermediate chamber 23 formed as a truncated cone, the larger base turned towards the screw 16 and respectively tstvuet its diameter, and the minimal - 40 to the conduit 17 and corresponds to its inner diameter. The hollow shaft 19 is arranged for rotation on the core sleeve 24, inside of which a piston 25 with a rod 45 of 26 is placed, the piston rod 26 being slidably mounted relative to the gasket 27. A recess is made in the front surface of the piston 25 to provide an annular front part 28,
    A device for transporting material works as follows. 55
    The drive sprocket 22 from its own drive (not shown) drives the screw 16. At the same time, thanks to the drive 18, begin.
    929004 6 The piston moves reciprocally. The material comes from the feed hopper 14 to the surface of the screw 16, which begins to move 5 and the cylindrical body 13 and further to the intermediate chamber 23, where it is additionally sealed with a piston 25. At the entrance to the pipe 17, the material is already preliminarily densified and then moves forward only under the action of the return - progressively moving piston 25.
    In the second version of the transportation device, as in the first), even greater compaction can be achieved by using only the friction of the material on the inner walls of the pipeline, which provides the adequate braking force required for compaction.
    权利要求:
    Claims (3)
    [1]
    9 material coaxially to the longitudinal axis of the screw. This method is carried out, for example, by one embodiment of an apparatus for transporting material in the form of particles. The specified device for transporting in the form of particles, including a cylindrical body with a feed hopper and a discharge hole, housed in the screw body, a pipeline fixed coaxially with the housing, and an actuator equipped with an annular piston and an intermediate chamber placed at the end of the piston and constituting part of the pipeline In this case, the piston is mounted outside the cylindrical housing coaxially with the screw with the possibility of reciprocating movement in the intermediate chamber, and the inner diameter of the piston corresponds to the outer diameter cylindrical housing. The method of transporting can also be carried out by a second variant of the device for transporting material in the form of particles. A device for transporting material in the form of particles, comprising a cylindrical body with a feed hopper and a discharge hole, housed in the screw body, a pipeline fixed coaxially with the body, and a pipeline equipped with a piston and an intermediate chamber made in the form of a truncated body aligned with the screw coaxially, the larger base of which faces to the screw and corresponds to its diameter, and the smaller to the pipeline and correspond to its internal diameter, while the piston surface is made in the form of a continuous circle oic surfaces Fig. 1 shows a device for transporting material in the form of particles, a general view, the first variant j of FIG. 2 is the same, top view of FIG. 3 is the same side view of FIG. k node 1 in FIG. FIG. 5 - schematically shows the movement of material from one zone to another; FIG. 6 shows a device, a general view, a second variant} of FIG., 7 is the same, top view, FIG. 8 - the same, side view. The device for transporting the material (first variant) consists of a feed hopper 1, a cylindrical body 2, a discharge opening 3. A 4 screw is placed in the body 2, Pipe 5 is fixed coaxially to the body 2. The hollow piston 6 is mounted coaxially to the screw 4 outside the cylindrical body reciprocating movement in the intermediate chamber 7. The outer diameter of the piston 6 corresponds to the internal diameter of the pipeline 5. In the latter in the axial direction there are through holes 8 in which the plates 9 are placed, Commercially horizontal surface projecting from the surface of the pipeline, and an inclined surface disposed within the conduit. The height 1 of the inclined surface increases in the direction of transporting the material. An adjustment mechanism 10 was used to adjust the plates 9 for trotting. A device for transporting material in the form of particles works as follows. When the actuator 11 is turned on, the screw l begins to rotate and feeds material from the hopper 1 in the direction of the sweep chamber 7, which is also the first sealing zone at that time, since simultaneously with the material being transported by the screw it is compacted. When the material completely fills all the cross section at the entrance of the pipeline, then it progressively moves using the reciprocating movement of the hollow piston 6, the end of which pushes the accumulated mass in the direction of the second zone 12, which leads to further compaction of the mother ala forming into a briquette, the density of which increases significantly as compared with the density in chamber 7 in which the material leaves the auger zone. Thus, the translational movement of the compacted mass through the pipe 5 is carried out only under the action of the reciprocating movement of the hollow piston 6, and The material is continuously supplied to the pipeline by screw a. The action of the piston 6 of reciprocating movement is shown schematically in Fig. 5 where zone A shows the fibrous material in a state of preliminary plating. of the protrusion moving progressively under the action of the screw t in the pipeline 5. The reciprocating moving piston 6 additionally compresses the material to a high degree of compactness, which is achieved in zone B of the pipeline 5 - Due to the circular shape of the front part of the piston 6 and the progressive movement of material The conduit 5; Line voltage within the compacted mass is considered to be arcuate, which contributes to the longitudinal strength of the compact briquette formed in Zone B. To achieve Olsha Neny flattening in zone 5 materi pipe is subjected to a force of frictions tionally moderating surface Set hydrochloric mass of material. This force is controlled by mounting the plates 9 by the adjustment mechanism 10 to a certain depth of penetration into the material. The deeper the penetration of the plates 9, the greater the friction braking force, respectively, the plates can control the degree of compaction of the material. I A device for transportation (the second option) consists of a cylindrical body 13 with a feed bunker k and an discharge opening 15. Inside the housing 13 is placed a screw 16. A pipe 17 is fixed coaxially to the housing 13. The drive is indicated by the positioning conductor 18. The screw is fixed on the hollow shaft 19 which is rotatably mounted by bearings 20 placed in the support 21 and sprocket 22. The discharge opening 15 is connected to an intermediate chamber 23, made in the form of a truncated cone, the larger base of which is facing screw 16 and corresponds to its diameter, and smaller to the pipeline 17 and corresponds to its internal diameter. A hollow shaft 19 is arranged to rotate on a core bushing 2k inside which a piston 25 with a rod 26 is housed, the piston rod 26 being slidably mounted with respect to a gasket 27. A recess is provided in the front surface of the piston 25 to provide an annular front part 28 The material works as follows. Driving sprocket 22. from its own drive (not shown) drives the auger 16. At the same time, thanks to the drive 18, first. The piston moves back and forth. The material flows from the feed hopper to the surface of the screw 16, which begins to move into the cylindrical body 13 and further into the intermediate chamber 23, where the piston 25 is further compacted. At the entrance to the pipe 17, the material is already pre-compacted and then moves forward only under the action of reciprocating piston 25 In the second version of the device for transporting MG both in TiepsoM), even greater compaction can be achieved using only material friction against the inner walls of the pipeline a, which provides sufficient braking force for sealing. Claim 1. The method of transporting material in the form of particles, in which the material from the outlet of the feed hopper into the processing zone of the material is transported by the screw in the axial direction and compresses the material in the first zone, characterized in that, in order to increase the efficiency of transportation, the material is unloaded into the second the zone located by SOOSNO first and immediately behind it, and then it is additionally compacted by means of coaxial pulsating force in the second zone and further translational movement material coaxially with the longitudinal axis of the screw.
    [2]
    2. A device for transporting material as a part, including a cylindrical body with a feed hopper and a discharge opening, housed in the body of the screw, a pipeline that is fixed coaxially with the body, an actuator characterized in that it is equipped with an annular horn and an intermediate chamber the end face of the piston and part of the pipeline, while the orishen is installed outside the cylindrical body coaxially with the auger with the possibility of reciprocating in the intermediate chamber, the inner diameter of the piston corresponds to outer diameter of the cylindrical housing.
    [3]
    3. The device according to claim 2, characterized in that the outer diameter of the piston corresponds to the internal diameter of the pipeline, which is made with through holes in the axial direction and is provided with installed with the possibility of reciprocating movement by means of an adjustment mechanism plates with a horizontal surface located outside the pipeline, and an inclined surface located inside the pipeline, with the height of the inclined surface increasing towards the transport of the material.
    C A device for transporting material in the form of particles, including a cylindrical body with a feed hopper and a discharge opening, housed in the screw body,
    a pipeline fixed coaxially to the housing, and an actuator, characterized in that it is provided with a piston and an intermediate chamber made in the form of
    coaxially to the screw of a truncated cone, the larger base of which is facing the screw and corresponds to its diameter, and the smaller to the pipeline and corresponds to its internal diameter, while the front surface of the piston is made in the form of a continuous circular surface.
    Information sources,
    taken into account in the examination
    1. Grigoriev A.M. Screw conveyors, M., Mashinostroenie, 1972, p. 6-7, fig. 7
    2. The author's certificate of the USSR 1 365313, cl. B 65 G 33/00, 1969
    (prototype).
    Y ////////////.
    i
    one
    c
    // Z // 7 ///
    // //// yZ
    Ш1
    U
    /at
    fe.
    类似技术:
    公开号 | 公开日 | 专利标题
    SU929004A3|1982-05-15|Method and apparatus for conveying particulate material |
    US4186658A|1980-02-05|Apparatus for conveying particulate material
    US5356280A|1994-10-18|Pump for particulate solids
    US7252120B2|2007-08-07|Powder feed apparatus, system and method
    JP2571962B2|1997-01-16|Apparatus for supplying lumps of particulate or fibrous substances
    CA2339002C|2009-04-07|Method and apparatus for feeding a mass of particulate or fibrous material
    CN1200097A|1998-11-25|Auger drive and method of driving an auger
    JPH07206140A|1995-08-08|Supply device of cylindrical body
    CN1743253B|2010-05-05|Vibrating bunker
    US3858759A|1975-01-07|Apparatus for volumeric feeding of fibrous material
    US2122874A|1938-07-05|Apparatus for compressing finely divided substances
    US5219468A|1993-06-15|Method for dewatering using addition of water to facilitate material movement
    GB2071065A|1981-09-16|Hopper feed out mechanism
    EP2558257B1|2014-12-31|Method and apparatus for feeding and compacting concrete and a feeding screw
    US3704917A|1972-12-05|Pulverulent material conveying apparatus
    CN215354496U|2021-12-31|Screening device
    RU2250050C2|2005-04-20|Extruder
    RU2214708C1|2003-10-27|Feed grinder-mixer-dispenser
    CN215152189U|2021-12-14|High-efficient biomass fuel make-up machine
    CN210914057U|2020-07-03|Powder feeding device for stone processing
    SU1071556A1|1984-02-07|Apparatus for feeding loose materials into pneumatic transport pipeline
    US2569969A|1951-10-02|Coal metering and cleanout block for stokers
    SU676514A1|1979-07-30|V.i.efimchev's conveyer screw pump for transporting loose materials
    CN110357748B|2021-06-15|Internal spiral quantitative feeding device
    SU1139565A1|1985-02-15|Arrangment for shaping long-size articles
    同族专利:
    公开号 | 公开日
    DE2714994C2|1984-01-12|
    US4119025A|1978-10-10|
    CA1070646A|1980-01-29|
    SE435609B|1984-10-08|
    BE863158A|1978-05-16|
    ES466295A1|1978-10-01|
    DK32978A|1978-07-25|
    AU511577B2|1980-08-28|
    AU3269378A|1979-08-02|
    SE7800729L|1978-07-25|
    JPS6014732B2|1985-04-15|
    CH629153A5|1982-04-15|
    FR2377953B1|1985-04-19|
    GB1599093A|1981-09-30|
    DE2714994A1|1978-07-27|
    FR2377953A1|1978-08-18|
    JPS53111982A|1978-09-29|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    GB191116309A|1911-07-14|1911-10-19|Henry Samuel Dean|Improved Construction of Apparatus for Packing or Stuffing Articles.|
    DE446268C|1924-05-24|1927-06-27|Bergin Akt Ges Fuer Kohle Und|Method for pressing paste-like masses into high pressure rooms|
    DE445107C|1924-11-08|1930-04-09|I G Farbenindustrie Akt Ges|Process for the introduction of solid bodies into reaction vessels under pressure|
    DK61101C|1940-11-22|1943-07-05|Niels Laurits Hansen|Press for liquid, especially oily Material.|
    US2540670A|1947-07-21|1951-02-06|Walter J Hoenecke|Backflow retarder|
    US2554082A|1948-02-20|1951-05-22|Anderson Co V D|Discharge means for cookers|
    DE1065266B|1954-05-28|1959-09-10|Pandia Inc., New York, N. Y. |Device for the continuous production of paper stock from cellulosic material|
    US3054343A|1959-06-26|1962-09-18|Sperry Rand Corp|Compressing apparatus|
    US3323444A|1963-06-12|1967-06-06|Massey Ferguson Inc|Hay wafering method and apparatus|
    FR1404177A|1964-08-11|1965-06-25|Koppers Gmbh Heinrich|Device for the continuous transfer of a finely divided solid substance from a chamber at normal pressure into a chamber placed under high pressure|
    US3621775A|1969-07-31|1971-11-23|Waterbury Hydraulic & Pollutio|Compacting mechanism|
    US3752066A|1971-04-05|1973-08-14|R Charles|Solid waste compactor operable on low pressure fluid|
    DE2165855C3|1971-12-31|1976-01-02|Hoechst Ag, 6000 Frankfurt|Sealing conveyor|
    US3865528A|1973-11-01|1975-02-11|Moog Inc|Extrusion apparatus having electronic interpolator|
    DE2714993C3|1977-01-24|1979-08-16|Stake Technology Ltd., Ottawa|Method for introducing a fiber material into a pressure vessel|US2546860A|1939-09-05|1951-03-27|Klagsbrunn Josef|Centrifugal mill|
    US4211163A|1978-11-07|1980-07-08|Robert Bender|Apparatus for discharge of pressure cooked particulate or fibrous material|
    DE2856097A1|1978-12-23|1980-07-03|Berstorff Gmbh Masch Hermann|SCREW EXTRUSION PRESS FOR THE PROCESSING OF PLASTIC, RUBBER OR THE LIKE.|
    CA1138708A|1980-03-27|1983-01-04|Douglas B. Brown|Press for expressing liquid from a mass|
    FI850837A0|1985-03-01|1985-03-01|Kt Suunnittelu Oy|GLIDGJUTMASKIN FOER FRAMSTAELLNING AV BETONGELEMENT.|
    US5012731A|1985-06-26|1991-05-07|Yves Maisonneuve|Device for pressing heterogeneous mixtures with regulated pressing force for separating liquid and solid fractions thereof, in particular fruit juices|
    CA1230208A|1987-03-24|1987-12-15|Bohuslav V. Kokta|Process for preparing pulp for paper making|
    DE3772991D1|1987-08-21|1991-10-17|Schumacher Walter|DEVICE FOR EXTRUDING, EXPANDING AND / OR THERMALLY TREATING SUBSTANCES AND SUBSTANCE MIXTURES.|
    US4834777A|1988-01-28|1989-05-30|Hydraulic Services, Inc.|Fuel pelletizing apparatus and method|
    CA1295179C|1988-02-19|1992-02-04|Douglas B. Brown|Apparatus for feeding a mass of particulate or fibrous material|
    SE469536B|1991-12-05|1993-07-19|Vattenfall Energisyst Ab|SEAT AND DEVICE FOR INPUT OF FRAGMENTED MATERIAL TO PRESSURE CONTAINERS|
    JPH0611527U|1992-04-06|1994-02-15|政▲いち▼ 大畑|toothbrush|
    US5377481A|1993-03-17|1995-01-03|Sibley; Duane L.|Apparatus for baling bulk fibrous material|
    CA2339002C|1998-08-03|2009-04-07|Stake Technology Ltd.|Method and apparatus for feeding a mass of particulate or fibrous material|
    KR20010100017A|1998-12-30|2001-11-09|로날드 디. 맥크레이|Steam Explosion Treatment with Addition of Chemicals|
    US6413362B1|1999-11-24|2002-07-02|Kimberly-Clark Worldwide, Inc.|Method of steam treating low yield papermaking fibers to produce a permanent curl|
    CA2383279A1|2002-05-06|2003-11-06|Sylvain Cloutier|Reactor|
    US8915644B2|2008-07-24|2014-12-23|Abengoa Bioenergy New Technologies, Llc.|Method and apparatus for conveying a cellulosic feedstock|
    CA2638152C|2008-07-24|2013-07-16|Sunopta Bioprocess Inc.|Method and apparatus for treating a cellulosic feedstock|
    CA2638159C|2008-07-24|2012-09-11|Sunopta Bioprocess Inc.|Method and apparatus for treating a cellulosic feedstock|
    CA2638160C|2008-07-24|2015-02-17|Sunopta Bioprocess Inc.|Method and apparatus for conveying a cellulosic feedstock|
    US9127325B2|2008-07-24|2015-09-08|Abengoa Bioenergy New Technologies, Llc.|Method and apparatus for treating a cellulosic feedstock|
    CA2638157C|2008-07-24|2013-05-28|Sunopta Bioprocess Inc.|Method and apparatus for conveying a cellulosic feedstock|
    CA2638150C|2008-07-24|2012-03-27|Sunopta Bioprocess Inc.|Method and apparatus for conveying a cellulosic feedstock|
    CA2650919C|2009-01-23|2014-04-22|Sunopta Bioprocess Inc.|Method and apparatus for conveying a cellulosic feedstock|
    CA2650913C|2009-01-23|2013-10-15|Sunopta Bioprocess Inc.|Method and apparatus for conveying a cellulosic feedstock|
    CA2672675A1|2009-07-17|2011-01-17|Murray J. Burke|Feeder with active flow modulator and method|
    CA2672674A1|2009-07-17|2011-01-17|Murray J. Burke|Compression apparatus with variable speed screw and method|
    CA2673134A1|2009-07-17|2011-01-17|Murray J. Burke|Method and apparatus for the heat treatment of a cellulosic feedstock upstream of hydrolysis|
    CA2672659A1|2009-07-17|2011-01-17|Murray J. Burke|Process apparatus with output valve and operation thereof|
    CA2672584A1|2009-07-17|2011-01-17|Murray J. Burke|Compression apparatus and method|
    WO2011028554A1|2009-08-24|2011-03-10|Abengoa Bioenergy New Technologies, Inc.|Method for producing ethanol and co-products from cellulosic biomass|
    JP5686572B2|2010-11-02|2015-03-18|株式会社大林組|Multi-stage soil feeder|
    BE1020599A3|2012-03-30|2014-01-07|Cnh Belgium Nv|MOVEABLE FRICTION BLOCKS FOR A RECTANGULAR BALL PRESS.|
    BE1020598A3|2012-03-30|2014-01-07|Cnh Belgium Nv|FRICTION BLOCKS FOR A RECTANGULAR BALL PRESS.|
    UA112793C2|2012-04-05|2016-10-25|Ґрінфілд Спешелті Елкоголз Інк.|TWO-SCREW PRESS EXTRUDER FOR SEPARATION OF SOLID MATERIALS FROM LIQUID|
    CN103015245B|2012-12-17|2015-04-22|吴玲鲜|Plant fiber continuous evaporation piston-type screw feeder|
    JP2017501876A|2013-12-05|2017-01-19|グリーンフィールド スペシャリティー アルコホールズ インコーポレイテッドＧｒｅｅｎＦｉｅｌｄ Ｓｐｅｃｉａｌｔｙ Ａｌｃｏｈｏｌｓ Ｉｎｃ．|Back pressure control of solid / fluid separator|
    WO2017190229A1|2016-05-02|2017-11-09|Greenfield Specialty Alcohols Inc.|Filter for extruder press|
    RU2698644C1|2018-07-26|2019-08-28|федеральное государственное бюджетное образовательное учреждение высшего образования "Ставропольский государственный аграрный университет"|Screw conveyor connecting assembly|
    CN112046067A|2020-08-26|2020-12-08|孔霞|Adjustable biomass fuel forming machine|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    US05/762,093|US4119025A|1977-01-24|1977-01-24|Method and apparatus for conveying particulate material|
    [返回顶部]