• 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:
    The invention relates to a method for dispersing the two liquid phases of a solvent extraction process well together, for controlling the desired type of dispersion and for raising the created dispersion to a level essentially higher than the liquid surface in the mixing tank. In the apparatus of the invention, to the circulation cylinder (6) of the mixer there is connected the heavy phase return conduit (27) and the light phase return conduit (29) entering from the settler of the same extraction step. In the top part of the mixer, coaxially with the turbine pump (9), there is installed the dispersion pump (12) where the dispersion rises to above the liquid surface (8) of the mixer through 2-24 rising pipes (15). The top ends of the rising pipes (15) are connected to the circular pipe (18), wherefrom the dispersion flow is conducted to the next stage through the collecting trough (22).
    公开号:SU1531840A3
    申请号:SU864028550
    申请日:1986-11-27
    公开日:1989-12-23
    发明作者:Геран Ниман Брор；Халтхольм Стиг-Эрик；Лео Лилья Лауно；Йоханнес Мякитало Валто
    申请人:Оутокумпу Ой (Фирма)；
    IPC主号:
    专利说明:

    I
    (21) 4028550 / 23-26
    (22) 11/27/86
    (31) 854725
    (32) 11/28/85
    (33) FI
    (46) 12.23.89, Bull. Number 47
    (71) Outokumpu Oi (FI)
    (72) Bror Gyo niman, Stig-Zrik Haltholm, Launo Leo Lil
    and Valto Johannes M Kitalo (FI) (53) 66.061.5.05 (088.8) (56) CMA Patent N 4628391, cl. On 01 D 11/04, 1980.
    U.S. Patent 4,235,602, cl. 23-293, 1978.
    Patent of Great Britain N 2024645, cl. On 01 D 11/04, 1980.
    (54) DEVICE FOR L11SPERGING
    TWO GASKY FAZ
    (57) The invention relates to a device for dispersing two liquid phases in a solvent extraction process, for adjusting a desired type of dispersion, and for raising the resulting dispersion to a level that is much higher than the surface of the liquid in the mixer. The purpose of the invention is to obtain a dispersion, improve the quality and create a double contour. In the proposed device, a return pipe of a heavy phase 27 and a return pipe are connected to the circulating cylinder 6 of the mixer 5.
    about s
    (L
    ate
    with kx)
     cm
    skins (. i ibi, which depart from the single bed) and the same extra-extra stage. 1-1, the upper part of the mixer coaxially with the turbopump 9 is installed, the dispersion pump 12 is MI, when gay, it is set at the point where, and 1sporci rises above the surface, 1 (m-8 from the press There are vertical tubes 15. The upper horses, 1 raising vertical tubes 15, are connected to the Kpyi onoi i tube 18, from which the flow of dispersion passes to the next processing stage through the collecting tray 22.
    The circular pipe 18 is provided with at least one horizontal slot located inside the circular pipe at an angle of 20-40 ° from the highest point of the pipe. The circular tube is provided with a downward sloping element mounted on its outer edge. The pipe is also provided with an annular plate. The outer surface of the collecting tray is provided with an inclined surface 25 directed towards the inside of the mixer and continues as an inwardly curved brake surface 26,
    15
    5 3.p. f-ly, 3 ill.
    The invention is poured to a device for dispersing two liquid phases in the process of extracting the solvents with the help of an intensified Hoii ne ;; that is (1st circulation).
    The aim of the invention is to obtain a dispersion of improved quality and a Ci -creation of double-curved circulation,
    On ibiir. 1 is given a mixer, a front and an orciofiHHK installed around the GMS C1 1 e and, a cross-section on (lig. 2 - dispersion c.1 pump, axonometric; on () ig. 3 - perhn part of the mixer, g. 1G1 inter1: Full incision.
    Arrangement:; goal neigh mixer 1,
    before cTcn ii-and :: 2 and sump 3, pipe-6on; i (.iu..in 6. T, cylindrical cylinder 3, co gpr (, 1st is located n the bottom (bottom) Mt iCTn C. month Tapering the upper part 6 of the circulating G: frndra 5 and prod 7, HanpaiUiCHiihifi to the upper part of the mixer, i.e. to the liquid surface 8. The dispersion of the liquid phases occurs through the circulation cylinder and using a turbine pump (turbo pump) 9 Installed in relation to ciiecHTCjiio in the center of the center or at the upper part of the mixer. Inside the mixer there is a divided elm, ring 10, cree-m it is set at the same height as the 6oHacoc tube so that the separating whip 10 directs the turbopump and mainly up, thanks to chego in case it is formed1, with circulation of the dispersion in the form of dropspoints (loop
    the dispersion circulation in FIG. 1 is shown by arrows.
    In order for this mixer to work efficiently even in the case of processing a high flow volume of the solution while ensuring a more uniform mixing intensity, but which on average will be lower than usual (intensity), a dispersion pump 12 is installed in the upper part of the mixer and on the same axis 11 with the turbopump 9. The main and main function of the dispersion pump is to ensure that the dispersion flow rises to a level that will be much higher than the surface of the liquid in the mixer, since in this case the surface Bytes predotstoynike be liquid sump 2 and 3 will also be above the surface comprised within the fluid mixer. Dispersion pump 12 rotates at the same speed as the turbopump. The suction inlet 13 of the suction cylinder 14 of the dispersion pump 12 is located quite close to the turbopump, slightly above its midpoint, but necessarily below the surface of the liquid. Serving dispersion pump and upward tubes (vertical, tubes) 1 are installed with their lower ends in the suction lindra, which is hermetically closed from above. These vertical tubes are installed in such a way that they form an expanding cone. Around the vertical tubes in the bottom of them m.ch ti (in particular below the top
    liquid) the conical plates 16 and 17 are installed. At the top, these conical plates are lengthened at least to the same level as the surface of the mixer 8 of the mixer. These conical vorus plates (ayuts with the same speed as the vertical tubes.
    The elevation or elevation angle of the vertical tubes is selected depending on the size of the hole and the speed of rotation of the tubes themselves in the range of 30 - 60 °. The number of vertical tubes may be in the range of 2-24. The diameter of the vertical tubes is chosen in such a way that the flow velocity inside the tubes remains relatively low 0.1 - 0.5 m / s.
    The turbulence formed by the flow inside this area is usually insignificant, so that the work of the pump or pumps will not reduce the size of the medium droplets.
    In the proposed device, the vertical tubes are straight, however, they may have a different shape, but with the obligatory condition that this shape will not impart an impulse force intended for pumping dispersion, which will be either too weak or too strong. dispersion pump must be such that it keeps the mixer surface at such a low level (raising the dispersion flow to such a high level) so that a light phase of the liquid from the collecting tray of the adjacent The cells passed freely to the surface of the mixer without the individual actuation of the pump and that the heavy phase of the liquid passed into the circulation cylinder directly under the turbopump.
    Vertical tubes 15 bring the dispersion flow directly to a circular tube 18 that connects all vertical tubes. The circular tube performs the centrifuge functor, the section of the solution phase, and in the annular or circular tube itself, the flow is somewhat damped only because of the partial collision of substream flowing from the vertical tubes. The dispersion flow leaves the circular pipe 18 (Fig. 2 and 3) through horizon 8406
    The taller slot 19, which is located inside the circular tube at an angle of about 20-40 ° with respect to the highest point of the tube. It is not necessary to make a horizontal notch 19 uniform: instead of one uniform notch you can make and use several small large cuts made in that part of the pipe, which is always in the interval between the vertical tubes.
    An annular plate 20, which surrounds the circular pipe and forces the dispersion flow coming out of the circular pipe, to flow in the interval between the annular plate, is inclined above the circular pipe.
    20 20 and the most circular pipe. Along the outer edge of the circular pipe 18, an element 21 is tilted downward, the outer surface of which is parallel to the annular
    5 layer ine. The main function of this element 21 is to cause the dispersion flow to depart from the circular pipe. would. The ring-shaped plate and the element 21 are matched and positioned relative to each other so that they direct the dispersion current, which comes out of the circular pipe, downwards at an angle of about- but at 45 °.
    From the circular pipe 18, the dispersion stream passes to the upper part of the mixer and further to the 1st tray 22 for dispersion, which surrounds the upper part of the mixer. Low or extra
    The .Q surface of the collecting tray is above the level of the surface of the liquid 8, located in the mixer. The outer surface 23 of the collecting tray simultaneously performs the function of the 1C1 cylinder surface of the mixer itself. The inner surface 24 of the collecting tray can be made, for example, so that in its lower part it is parallel to the outer
    l of the surface, and in its upper part parallel to the vertical tubes 15 of the dispersion pump. In addition, in accordance with an embodiment of the present invention, a surface 25 is formed, which is inclined from the - the outer surface of the collecting tray towards the inside to receive a dispersion flow, with the lower part of the inclined surface
    five
    five
    five
    25 continues as an inward curved brake surface 26.
    Flexible or gentle dispersion treatment is a very important factor in reducing the likelihood of emulsification or the occurrence of emulsification. That is why the design of the device guides the inclined surface 25, against which the dispersion flow coming out of the circular pipe strikes under a very small fragrance. The brake surface 26 is used to slow down the dispersion flow, since the dispersion flow passing along this surface is forced to overcome the resistance with all of the active centrifugal force. If the intrusion reaction proceeds slowly, then this braking surface can not be used, and in this case the collecting tray will function as an element of the continuation of the mixer itself, since the dispersion already in the collecting tray still vortexes. The device works as follows. From the collecting tray, the dispersion stream passes into the pre-settler and then into the sump.
    The dispersing device (Fig. 1) is also provided with return pipelines from the same ethane extraction sump: a return pipe 27 for a heavier phase, which is equipped with valves 28, and a return pipe 29 for an easier phase, which is equipped with a valve 30 The return flow passes to the conical part of the 6th circulation cylinder. The return pipe of the heavy phase 27 is also used in equipment preparation operations for commissioning. The return pipe of the heavy phase, connected to the working dispersion pump, ensures the start of the double loop circulation, which is an important aspect of the normal operation of the entire mixer. Differences in the specific gravity of the solutions used can lead to a situation in which a part of the light phase will be in the upper part of the mixer, and a part of the heavy phase in the lower part of the mixer as obstacles to normal circulation of the mixer. Thus, the dispersion pump will raise
    five
    0
    five
    0
    five
    0
    five
    0
    five
    A relatively large part of the light phase goes directly to a settling tank, from where a part of the heavy phase will return via a return line to the mixer. After a short period of operation of the device, a sufficient amount of the heavy solution phase will flow into the turbopump of the mixer through the circulation cylinder, so that there are all conditions for the normal start up of the double loop circulation operation. It is recommended by valve 28 to continuously support the return of a slightly heavy phase.
    The return pipe 29 of the light phase can be used if it is necessary or desirable to disperse the heavy phase into droplets. If the lifting height of the dispersion pump 12 and its performance are quite sufficient and satisfactory, then the surface of the liquid in the mixer decreases so much that it is possible to easily and successfully also return the light phase. Another limiting factor in this case is the constriction due to the cone-shaped upper part 6 of the circulation cylinder, this constriction sometimes leads to the formation of low pressure inside the circulation cylinder. That is why it is recommended to introduce all portions of the solution into the upper part of the circulation cylinder. The cross-sectional area of the cylinder-circulation should be 0.2-0.6 times the cross-sectional area of the mixer itself. If the dispersion flow passes downward into the double loop circulation, then this dispersion flow enters the circulation cylinder 5 through openings 31 located in close proximity to the lower part of the circulation cylinder.
    If neutralizing additives are introduced directly into the mixer, then it is recommended to place the necessary measuring and reading devices 32, for example, to measure the PH value, and some other electrodes in the upper part of the mixer, they are constantly affected by the jet of the turbopump. Consequently, the electrodes installed at the limits of the main jet will always be in a clean state and provide more
    high degree of accuracy of conductive measurements.
    权利要求:
    Claims (6)
    [1]
    Invention Formula
    1, Device For dispersing two liquid phases, containing a mixer, a circulation cylinder located in its lower part, a turbine pump installed above a circulation cylinder, a separating ring, a preliminary sump, surrounding the mixer and a sump connected to the mixer, return channel heavy a phase and a light phase channel from a settling tank, characterized in that, in order to obtain an improved quality dispersion and create a double-circuit circulation, the heavy phase return channel and the light phase channel are connected with the upper part of the circulation cylinder, the mixer is equipped with a dispersion pump mounted above the turbine pump, the suction nozzle of which is located above the middle part of the turbine pump, suction 1TS1LINDROM, closed at the top and equipped with at least two lifting pipes, conical plates that are on the lower end passes below the surface of the fluid, and
    “/ 7/5 /; f9js
    IS
    0
    five
    0
    five
    0
    at the upper end - at least to the same level as the surface of the liquid in the mixer, while the lifting pipes are equipped with a connecting circular pipe with a collecting tray 1.
    [2]
    2. The device according to claim 1, about tl and - it is because the circular pipe is provided with at least one horizontal slot, which is located inside the circular pipe at an angle of 20-40 ° from the highest point of the pipe.
    [3]
    3. The device according to claim 1, characterized in that the circular tube is provided with a downwardly inclined element mounted on its outer edge.
    [4]
    A. The device according to claim 1, about tl and the fact that the circular pipe is provided with an annular plate installed in an inclined plane.
    [5]
    5. The device according to claim 1, about tl and - the fact that the outer surface of the collecting tray is provided with an inclined surface directed inside the mixer.
    [6]
    6. The device according to claim 1, about tl and - the fact that the lower part of the inclined surface continues in the form of a bent inward brake surface.
    W.
    24
    29
    28
    Fig.Z
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    同族专利:
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    CN1005961B|1989-12-06|
    DE3640791C2|1990-05-17|
    FR2590496B1|1990-07-20|
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    引用文献:
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    US2729545A|1950-09-20|1956-01-03|Shell Dev|Contact apparatus with rotating discs|
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    DE2710241C2|1976-03-11|1989-08-03|Krebs & Cie., Paris, Fr|
    FI57059C|1978-06-28|1980-06-10|Outokumpu Oy|EXTRAKTIONSENHET FOER VAETSKE-VAETSKE-EXTRAKTION|
    CA1125989A|1978-06-28|1982-06-22|Erco Industries Limited|Modular chlorine dioxide generation systems|
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    法律状态:
    优先权:
    申请号 | 申请日 | 专利标题
    FI854725A|FI73146C|1985-11-28|1985-11-28|SAETT ATT DISPERGERA TVAO FASER VID VAETSKA-VAETSKA-EXTRAKTION SAMT PUMPMIXER FOER GENOMFOERANDE AV SAETTET.|
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