• 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 continuous, completely jacketed countercurrent centrifugal extractor of the type utilized to mix and separate two liquids that have different specific gravities and enter through separate inlets. The extractor has at least one overflow weir in a mixing zone between the inlet for the specifically lighter and the inlet for the specifically heavier liquid phase and a division of the mixing zone into mixing-and-separation compartments. Access channels empty into the vicinity of the inner surface of a drum jacket and into that of the heavier phase, to conduct the lighter phase out of the compartment inside the hub of a conveyor worm into the initial mixing-and-separation compartment. One or more overflow channels also empty into the vicinity of the heavier phase, in the overflow weir to divert the lighter phase separated in the initial mixing-and-separation compartment into another and subsequent mixing-and-separation compartment. The design creates several highly efficient contact points in the vicinity of the mixing zone that enhance the extracting action.
    公开号:SU1218920A3
    申请号:SU833535718
    申请日:1983-01-07
    公开日:1986-03-15
    发明作者:Осткамп Вилли；Бруннер Карлхайнц；Виббельт Фридрих
    申请人:Вестфалия-Сепаратор Аг (Фирма)；
    IPC主号:
    专利说明:

    f12
    This invention relates to a continuous continuous centrifugal extractor with a solid drum for mixing and separating two separately supplied liquids of different specific gravities.
    The aim of the invention is to increase efficiency.
    FIG. I shows a countercurrent centrifugal extractor, a longitudinal section; in fig. 2 - zone nepcMeiuH- vani extractor.
    The countercurrent centrifugal extractor consists of a tssh1indro-conical drum 1 with body 2, in which a transport screw 3 is located, which is rotated at a speed different from the speed of rotation of the body 2 of the drum; the transport screw has turns 4, which correspond to the inner walls of the drum; the regulation of the speed difference between the transport screw and the drum is carried out by means of a pulley connected to the transport belt and the drum casing of the cyclotransfer mechanism 5; the drum rotates in the housing 6, which consists of a casing 7 and a claw 8. The drum and the transport w-drive are driven through a cycling gear, for example, from an electric motor (not shown), which by means of V-belts 9 and 10 of the cyclic drive drives the drum to rotate at a set speed and transport pimp.
    In the separation cavity, in the area of turns 4 of the screw shaft 11 of the screw and the drum body 2, there are separating disks 12 and 13, which divide the separation cavity into a zone of clarification 14 and 15 and a mixing zone 16. Inside the mixing zone 16 there is an overflow partition 17: which forms an annular gap with the inner wall of the drum body 2, adjoins the auger shaft and is angled. The dividing wall 17 divides the mixing zone into the first and second mixing and separating chambers 18 and 19. In the part of the dividing section passing along the axis, an overflow cat is provided, 20, the outlet of which is located in the zone of a heavier liquid phase in the second mixing and separation chamber 19 and which serves to divert the divided in the first mixing-section of the elite chamber 18 more easily.
    9202
    ISIK for supplying a lighter liquid phase is provided by a supply pipe 21, which enters the chamber 22, located inside the junction box.
    shaft 11. The chamber 22 exits one or more supply channels 23, which pass into the zone of the heavy liquid phase in the first mixing and separation chamber 18 to the internal
    Q her body wall 2 of the drum. The pipe 21 is enclosed in the pipe 24; .u1I of the supply of the heavy phase, which enters the chamber 25 from the chamber 22 and has one or several
    outlet holes 26 into the second mixing and separating chamber 19.
    While the light liquid phase is withdrawn through the upper discharge device 27, which
    Q is located in the discharge chamber 28 inside the lid 8, and the discharge chamber is separated from the lightening zone 15 by the overflow partition 29, diverting a heavy liquid phase from the lightening zone
    5 nor 14 of the drum is produced by means of an overflow pipe 30 that flows into the annular channel 31, from which the liquid passes through the outlet channel 32 from the drum to the
    JQu 8, from which the hard liquid phase is led out through exit 33.
    The solid phase separated in the drum by coils 4, mounted on the screw 3, located in the conical part of the drum, is transported to the discharge opening 34 in the housing: the drum 35 and unloaded through the discharge casing 7. The extractor works as follows
    iO i ---- 1iloc; jie, when the drum reaches the extractor of the working speed through pipe 24 to chamber 25 inside the screw shaft 11, it is supplied more heavy. } k.1 pin containing a solid phase
    from there, the liquid enters through the holes 26 into the mixing zone 16. As soon as the drum is filled with a certain amount of more liquid, it flows in the direction to the conical part of the drum and through the overflow pipe 30, the annular drip 31 and channel 32 without pressure come out of the rotating drum. At the same time, the solid phase separated out from the drum and deposited on the inner wall of the body.a 2 is captured by the turns 4 of the auger 3 and is shifted to the discharge opening.
    five
    0
    five
    3
    34 in the drum housing, through which it is discharged in a relatively dry form.
    After filling the drum with heavy liquid through conduit 21, a light liquid is supplied to the drum in countercurrent with a heavy liquid, for example an extracting agent, which first enters the chamber 22 inside the screw shaft 11 and from there through channels 23 due to With this, the pressure drops in the area of the solid liquid phase inside the mixing zone 16 into the mixing and separation chamber 18 between the turns 4 of the transport screw. Since at the same time all the light liquid flows through the heavy liquid phase and between the rotating screw 3 and the liquid drum housing 2 rotating with a different speed, an additional turbulence is obtained, intensive mixing of the liquids occurs in the mixing-separation chamber 18
    Depending on the difference in the specific gravity of both liquids and depending on. the duration of the stay of the liquids in the drum between the coils 4, with a counter-current of the liquids, there is again some separation between them, therefore at least partly light liquid 189204
    Each phase in the first mixing and separating chamber 18 can be used for further intensive mixing with the heavy liquid 5 phase, since this light liquid separated from the first mixing and separation chamber 18 passes through the overflow wall 17, which separates the mixing and separation 10 the separating chambers 18 and 19, and through the channel 20, are introduced into the heavy liquid phase in the second mixing and separating chamber 19, and again intensive mixing of the liquids occurs. On the way to the discharge side to the clarification zone 15, a light liquid phase flows in countercurrent through the heavy liquid phase coming from the holes 26,
    20, whereby the third intensive mixing of liquids occurs in this place. The light liquid then flows through the zone of clarification 15 into the discharge chamber 28, into which it is discharged under pressure from the drum using the device 27,
    The invention is also applicable to countercurrent centrifugal extraction
    30 solid drum drum out of which the extracted solid liquid phase is discharged together with the solid phase.
    / "
    J4
    - S4 f77fP-S 30 22 I 1 25 FIG. one
    eight
    28
    four
    Compiled by A.Mironov Editor M.Tsitkina Tehred Z.Palne Corrector I.Erdeyi
    Order 141/63 - Draw 663 Subscription
    VNIIPI USSR State Committee
    for inventions and discoveries 113035, Moscow, Zh-35, Raushsk nab., d.A / 3
    Branch PIP Patent, Uzhgorod, Proektna St., 4
    权利要求:
    Claims (6)
    [1]
    1. A continuous counterflow centrifugal extractor, comprising a continuous partially conical drum with clarification zones and a mixing zone, mounted for rotation around a horizontal axis, chambers for supplying liquids to the mixing zone located inside the drum, a transport auger installed in the drum for rotation around horizontal axis with a rotational speed different from the rotational speed of the drum, screw turns are made corresponding to the inner walls of the drum, unloaded a solid phase device made in the conical part of the drum, an unloading chamber with a top unloading device for draining one liquid phase, a drain chamber for a second liquid phase, separated from the separation cavity by an overflow partition and closed relative to the unloading chamber, characterized in that, in order to increase efficiency, it is equipped with at least one additional overflow partition located inside the mixing zone between the inlets of the liquid phases, which divides the mixing zone into a mixer but - separation chambers, a pipe for supplying the light phase to the first mixing separation chamber to the inner wall of the drum body, and at least one bypass pipe for draining the light liquid phase from the first mixing and separation chamber into the heavy phase zone of the next chamber located in the additional overflow partition.
    [2]
    2. An extractor according to π.
    [3]
    3. The extractor according to claims 1 and 2, characterized in that it is equipped with separation discs located between the mixing zone and the clarification zones.
    [4]
    4. The extractor according to claim 1, characterized in that the additional overflow partition has an annular gap with the drum body and is connected to the screw shaft.
    [5]
    5. The extractor according to paragraphs. 1 and 4, characterized in that the additional overflow partition has an angular shape.
    [6]
    6. The extractor according to paragraphs. 1-5, characterized in that the bypass pipes are located in the axially extending part of the overflow partition.
    SU „„ 1218920>
    f 121
    类似技术:
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    同族专利:
    公开号 | 公开日
    IT8367083D0|1983-01-25|
    SE459559B|1989-07-17|
    JPS6045921B2|1985-10-12|
    FR2520258A1|1983-07-29|
    US4451247A|1984-05-29|
    DE3202294C1|1983-04-21|
    GB2113576B|1985-10-09|
    FR2520258B1|1985-12-13|
    SE8300096L|1983-07-27|
    BR8202797A|1983-11-22|
    UA5565A1|1994-12-28|
    IT1161471B|1987-03-18|
    JPS58180202A|1983-10-21|
    SE8300096D0|1983-01-11|
    GB8301329D0|1983-02-16|
    GB2113576A|1983-08-10|
    引用文献:
    公开号 | 申请日 | 公开日 | 申请人 | 专利标题
    FR1360383A|1963-03-29|1964-05-08|Saint Gobain Nucleaire Soc|Apparatus for bringing two normally immiscible liquids into contact|
    US3228594A|1965-02-05|1966-01-11|Clifford L Amero|Centrifugal separator|
    FR1459134A|1965-02-08|1966-04-29|Dresser Ind|Centrifugal device with axial rotor|
    US3405866A|1966-11-09|1968-10-15|Bird Machine Co|Centrifuge|
    US3501346A|1966-12-22|1970-03-17|Sugar Cane Growers Coop|Treatment of sugar mill clarifier mud|
    US3782623A|1970-06-11|1974-01-01|Krueger As I|Decanting centrifuge for draining off water from sewage sludge|
    DE2627265A1|1976-06-18|1977-12-29|Krauss Maffei Ag|Decanter type centrifuge with cake washing - having inserts inside bowl to cause break up of cake|
    DE2701763C3|1977-01-18|1979-11-15|Westfalia Separator Ag, 4740 Oelde|Continuous full bowl countercurrent centrifugal extractor|
    US4190194A|1978-07-28|1980-02-26|Bird Machine Company, Inc.|Solids liquid separating centrifuge with solids classification|
    DE2901607C2|1979-01-17|1981-03-12|Westfalia Separator Ag, 4740 Oelde|Solid bowl screw centrifuge|DE3326310C2|1983-07-21|1986-02-20|Westfalia Separator Ag, 4740 Oelde|Solid bowl centrifuge with a screw conveyor|
    GB8328894D0|1983-10-28|1983-11-30|Broadbent & Sons Ltd Thomas|Decanting type centrifuges|
    DE3518885A1|1985-05-25|1986-11-27|Bayer Ag, 5090 Leverkusen|FULL-COVERED SCREW CENTRIFUGE WITH RECHARGEING DEVICE|
    WO1992005877A1|1990-09-27|1992-04-16|Conoco Specialty Products Inc.|Countercurrent washing of solids in a decanter centrifuge|
    US5151079A|1990-09-27|1992-09-29|Conoco Specialty Products Inc.|Method and apparatus for reduction of particle disintegration|
    JP3032283B2|1990-11-27|2000-04-10|月島機械株式会社|Decanter centrifuge|
    DE4132593A1|1991-09-30|1993-04-01|Linde Kca Dresden Gmbh|REACTOR FOR COUNTERFLOW TREATMENT OF SOLID AND LIQUID|
    WO1993010905A1|1991-11-27|1993-06-10|Baker Hughes Incorporated|Feed accelerator system including feed slurry accelerating nozzle apparatus|
    US5403486A|1991-12-31|1995-04-04|Baker Hughes Incorporated|Accelerator system in a centrifuge|
    DE4201427A1|1992-01-21|1993-07-22|Westfalia Separator Ag|FULL-COVERED SNAIL CENTRIFUGE|
    ES2158477T3|1996-01-18|2001-09-01|Rapanelli Fioravante Spa|HORIZONTAL CENTRIFUGE MACHINE FOR AN OPTIMAL OIL EXTRACTION.|
    IT1285052B1|1996-10-18|1998-06-03|Gennaretti S P A|HORIZONTAL CENTRIFUGE FOR THE EXTRACTION OF OIL FROM AN OIL MIXTURE|
    US6780147B2|2000-08-31|2004-08-24|Varco I/P, Inc.|Centrifuge with open conveyor having an accelerating impeller and flow enhancer|
    US6790169B2|2000-08-31|2004-09-14|Varco I/P, Inc.|Centrifuge with feed tube adapter|
    US7018326B2|2000-08-31|2006-03-28|Varco I/P, Inc.|Centrifuge with impellers and beach feed|
    DE10223802B4|2002-05-29|2005-06-09|Westfalia Separator Ag|Solid bowl centrifuge|
    DE10336350B4|2003-08-08|2007-10-31|Westfalia Separator Ag|Solid bowl centrifuge, with paring disc|
    CN100425315C|2007-02-02|2008-10-15|浦华控股有限公司|Down-transmission type centrifugal extractor for the chemical industry operation|
    US8961381B2|2008-06-06|2015-02-24|M-I L.L.C.|Dual feed centrifuge|
    DK177710B1|2012-09-14|2014-03-31|Alfa Laval Corp Ab|Snegletransportør til en centrifugal separator, navnlig en dekantercentrifuge, og en centrifugal separator|
    JP5667724B1|2014-08-20|2015-02-12|巴工業株式会社|Decanter centrifuge and operation method of decanter centrifuge|
    CN110479502B|2019-08-21|2020-05-12|四川宝石机械石油钻头有限责任公司|High-speed vertical centrifuge|
    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    DE3202294A|DE3202294C1|1982-01-26|1982-01-26|Continuously working full-jacket countercurrent centrifugal extractor|
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