Centrifugation device with adjustable vanes

Abstract

The invention relates to a device for drawing off fluid of a centrifugation device, particularly for separating at least one fluid, with a disk (10) with channels (12, 12). It is characterized by adjustable vanes. This allows to change the property of the disk and thus treat liquids with different properties without disassembling the separator. Therefore there is no dead time during working time and an easy adjustment of the disk.

Claims

1. A separator with a device for separating specific liquids from each other and drawing off fluid in centrifugation separation equipment, comprising a rotor with a series of conical separation disks inside a separation chamber, a distributor, a top disk and a main separation disk defining a radius of separation with a plurality of fluid flow channels defined by a plurality of vanes that have an adjustable outer diameter.

2. The device according to claim 1, wherein each vane is rotatable about a respective axis.

3. The device of claim 1, wherein each vane includes a slot that defines a minimum and a maximum outer diameter.

4. The device of claim 3, including a second disk having a plurality of pins that respectively engage said slots in the vanes.

5. The device of claim 4, wherein said second disk is rotatable.

6. The device of claim 3, wherein a second disk is cooperatively associated with said main separation disk, said second disk has a plurality of pins respectively guided in said slots in the vanes, and said second disk is rotatable whereby said pins rotate and thereby adjust the outer diameter of said vanes.

7. A centripetal discharge pump of a centrifugal fluid phase separator, comprising: a rotor defining pump axis, the rotor having a series of conical separation disks positioned inside a separation chamber; a distributor; a top disk; a circular chamber for the discharge of one phase; a discharge disk for separating specific liquids from each other, the disk defining a radius of separation having an inner diameter and an outer diameter, situated within the discharge chamber, coaxial with and rotated by the rotor, with a discharge channel between the inner diameter of the disk and the rotor; wherein the discharge disk has a plurality of vanes extending from the outer diameter to the inner diameter, said vanes defining a plurality of channels running from the outside diameter to the discharge channel; and wherein the vanes have an adjustable outer diameter.

8. The centripetal discharge pump of claim 7, wherein each vane is rotatable about a respective axis.

9. The centripetal discharge pump of claim 7, wherein each vane includes a slot that defines a minimum and a maximum outer diameter.

10. The centripetal discharge pump of claim 9, including a second disk having a plurality of pins that respectively engage said slots in the vanes.

11. The centripetal discharge pump of claim 10, wherein said second disk is rotatable.

12. The centripetal discharge pump of claim 11, wherein each vane is rotatable about a respective axis.

13. The centripetal discharge pump of claim 9, wherein a second disk is cooperatively associated with said discharge disk, said second disk has a plurality of pins respectively guided in said slots in the vanes, and said second disk is rotatable whereby said pins rotate and thereby adjust the outer diameter of said vanes.

Description

BRIEF DESCRIPTION OF THE DRAWING

(1) The invention is now described in more detail with reference to the accompanying drawings, where

(2) FIG. 1 shows a separator including the invention,

(3) FIG. 2 shows a portion of the separator with two separating disks,

(4) FIG. 3 shows a sketch with the different outer radii of the vanes,

(5) FIG. 4 shows the position of the various vanes, and

(6) FIG. 5 shows a possible variant of the invention to adjust the vanes.

DETAILED DESCRIPTION

(7) FIG. 1 shows a separator 1 with a rotor 2 comprising a series of conical separation disks 3 inside a separation chamber 4, a distributor 5 and a top disk 6. In the example shown in FIG. 1 the rotor 2 is mounted on a hollow shaft, through which the liquid to be centrifugally treated is supplied to the rotor. The mixture to be separated is fed into the hollow shaft on top at 8. Drive 7, which may be a belt drive, is connected to a spindle to rotate rotor 2.

(8) The separation quality is based on the location of the liquid particles according to the following equation:
.sub.l(R.sub.iR.sub.l)=.sub.p(R.sub.iR.sub.x)

(9) If the specific weight of the liquid(s) change the separation radius R.sub.i can only be changed by adapting the radius R.sub.x of the centripetal pump 9.

(10) Here .sub.l is the specific weight of the lighter phase

(11) .sub.p is the specific weight of the heavier phase

(12) R.sub.i is the radius of separation

(13) R.sub.l is the inner radius of the shaft and

(14) R.sub.x is the outer radius of the centripetal pump.

(15) With the change of R.sub.i many different kinds of products can be separated with the same separator and it may be easily modified also during operation to allow an easy setting of the separation radius for an optimal result of the separation of the liquids. Different combinations of liquids as oil and water, oil and soap, oil and gums can be separated. Also the same separator can remove water from oil in different kind of oils due to different specific weight of oil.

(16) FIG. 2 shows the area of the separating disk 10, which is situated in a circular channel 9 for the discharge of one phase. The separated liquid passes through a channel 11 upward to a separate discharge. For the separation of three different liquids a second disk 10, which is not adjustable, is situated below the first adjustable separating or gravity disk 10.

(17) FIG. 3 shows a section of the separating disk 10 with the inner channel 11. The liquid is drawn though channels 12 limited by vanes 13, 13 to the inner channel 11. In this figure the vanes 13, 13 are at the minimum position of the outer radius R.sub.x of the centripetal pump. It is also shown the maximum position of the outer radius R.sub.x. It can be seen that the difference is very small, however the effect of this different position is enormous.

(18) In FIG. 4 the separating disk 10 is shown around the hollow rotor shaft 2 and the discharge channel 11. The lighter liquid is drawn through the channels 12, 12 in direction of the arrows 18, 18 to the discharge channel 11 and directed by the edges (in position 14, 15, 14, 15) of the vanes 12, 12. In case of the minimum separation radius the channels 12, 12 are limited by the edges of the vanes 12, 12 in position 14, 14. In case of the maximum separation radius the channels 12, 12 are limited by the edges of the vanes 12, 12 in position 15, 15. The vanes 12, 12 are pivotal around axes (preferably in form of pins) 16, 16 and guided by pins fixed at a second disk in slots 17, 17 situated in the vanes 12, 12 of the separation disk 10. Thus the way of the vanes 12, 12 is defined and limited.

(19) FIG. 5 shows a side view of the top of a separator 1 with the top opening 8 to feed the liquid. Further the discharge opening 19 for the lighter phase and 20 for the heavier phase can be seen. In addition screw 21 is shown with which the vanes can be moved and thus the separation radius be changed even during operation and without dismantling of any part of the separator 1.

(20) FIG. 2 shows that a second disk 22 is situated immediately below main disk 10. The top of the second disk forms the bottom of channels 12 shown in FIG. 4. Pins 23 fixed to the second disk 22 are guided in the adjustment slots 17 of disk 10 for adjusting the outer diameter of the vanes. The pins 23 can move within slots 17 because the second disk 22 can be rotated relative to the main disk 10, by means of, e.g., screw 21.