专利摘要:
A CENTRIFUGAL SEPARATOR, containing a drum mounted on a vertical shaft, containing a base with sludge outlet openings, a cover, a plate holder with a stack of plates, placed on the base of a cone-shaped piston and a device for moving the latter, having two communicating with each other using vertical channels of the working chamber liquids having channels for the inlet and outlet of the latter, one of which is located under the cone-shaped piston, and the other at the base of the drum, and the locking ring piston With seals for closing said vertical channels, over which a distribution chamber with throttling openings is located, characterized in that, in order to accelerate the movement of the cone-shaped piston to close the orifice openings and to discharge the sediment, the outer surface of the closure ring piston is the inner wall of the the working fluid located at the base of the drum, while to (L the outer surface of this piston under each vertical channel is attached to the disk lottery, and in the base under the piston there is an additional distribution chamber of the working fluid with inlet and outlet channels. | gp 9 U1
公开号:SU1175351A3
申请号:SU833561945
申请日:1983-03-04
公开日:1985-08-23
发明作者:Кольштетте Вернер
申请人:Вестфалиа Сепаратор Аг (Фирма);
IPC主号:
专利说明:

 one
The invention relates to equipment for the separation of liquids in the field of centrifugal forces.
The purpose of the invention is to accelerate the movement of the cone-shaped piston to close the outlet openings and to accelerate the discharge of sediment.
The drawing schematically shows a part of a separator drum with a longitudinal section.
The centrifugal separator includes a drum mounted on a vertical shaft 1, containing a base 2 with outlets 3 for sludge, a cap 4, a plate holder 5 with a stack of plates 6, a cone-shaped piston 7 placed at the base and a device for moving the latter, including two communicating with each other using the vertical channels 8 of the chamber 9 10 for the working fluid, one of which is located under the conical piston and the other at the base of the drum, and the locking ring piston 11 with seals 12 for closing the decree nnyh vertical channels over which the distribution chamber 13 is located with throttling apertures 14.
The outer surface of the locking ring piston 11 is the inner wall of the working fluid chamber 10 located at the base of the drum, while a disk 15 is attached to the outer surface of this piston under each vertical channel to accommodate the seal 12,
At the base 2 under the piston 11 there is an additional distribution chamber 16 of the working fluid with inlet 17 and outlet 18 channels. Krshka 4 drum attached to the base 2 by means of a locking ring 19 (not shown). The base of the drum has a guide ring 20, which is rigidly connected to its lower part with screws.
The chamber 10 has throttled outlets 21.
The distribution chambers 13 and 16 are hermetically separated from the distribution chamber 10 and communicated with the channels 22 and 23 for the working fluid.
753512
The distribution chamber 9 is connected through channel 24 with cavity 25.
The separator works as follows.
5 Before applying the slurry to the separation, the rotary annular piston 11 is in the closed position. The chamber 9 through the openings 26 of the cavity 25 and the channels 24 is supplied with the working fluid, by means of which the cone-shaped piston 7 is moved to the closed position. The initial suspension enters the cavity of the plate holders 5 and then into the inter-plate gaps.
As a result of separation, the sediment accumulates in cavity 27, after which it is partially discharged. To accomplish the latter, the working fluid is supplied to the distribution chambers 13 and 16 of the locking ring piston 11 through the openings 28, the cavity 25 and the channels 17 and 22. Since the pressure of the liquid
25 in the distribution chamber 13
Much more than in the distribution chamber 16, the locking ring piston 11 moves in the direction of the opening position so that the working fluid, under the action of centrifugal force, flows from the chamber 9 through the vertical channels 8 into the chamber 10 in a fraction of a second.
After filling this chamber, the working fluid closes the vertical channels 8. The cone-shaped piston 7 thus moves to the closed position as soon as in the cavity
, Q 29 due to the removal of a certain amount of sediment, the pressure will drop so much that the pressure developed in chamber 9 by the remaining working fluid there will overcome it.
g. With continued supply of working fluid, its division in chamber 9 very quickly reaches its full value, which keeps the cone-shaped piston 7 in the closed position of the cover.
When the sediment is partially unloaded, the feed of the initial suspension does not stop and after closing the outlet openings 3 the pressure inside the drum
jr increases again.
After unloading sediment at the termination of the supply of working fluid through,. holes 28 and channels 22 in the chamber
权利要求:
Claims (1)
[1]
CENTRIFUGAL SEPARATOR, containing a drum mounted on a vertical shaft, containing a base with sludge outlet openings, a lid, and a plate holder with a package of plates placed in. a conical piston and a device for moving the latter, having two chambers for working fluid communicating with each other using vertical channels, having channels for supplying and discharging the latter, one of which is located under the conical piston, and the other at the base of the drum, and a locking annular piston with seals for closing said vertical channels, over which there is a distribution chamber with throttling holes, characterized in that, in order to accelerate the movement of the cone of the corresponding piston for closing the outlet openings and discharging the sediment, the outer surface of the locking annular piston is the inner wall of the working fluid chamber located at the base of the drum, and a disk is attached to the outer surface of this piston under each vertical channel to accommodate the seal, with the base underneath an additional distribution chamber of the working fluid with inlet and outlet channels is located by the piston.
类似技术:
公开号 | 公开日 | 专利标题
SU1175351A3|1985-08-23|Centrifugal separator
US3448919A|1969-06-10|Automatic desludging apparatus
SU1743339A3|1992-06-23|Centrifugal separator
KR920006647B1|1992-08-14|Centrifugal separator
US3550843A|1970-12-29|Sludge centrifuge
EP0332639B1|1998-01-28|Operating system for centrifugal separator
US4103822A|1978-08-01|Centrifugal separator
US3765599A|1973-10-16|Self cleaning centrifuge drum with stepwise variable closing pressure
CA1131599A|1982-09-14|Operating system for centrifuges
US4149668A|1979-04-17|Centrifugal separator with outlet valves
US3494545A|1970-02-10|Sludge level indicating device for centrifugal separators
US4410319A|1983-10-18|Self-discharging centrifugal drum
US4044945A|1977-08-30|Self-cleaning centrifugal separator having a main piston valve defining one side of the separating chamber and connected to at least one auxiliary piston valve
SU1422986A4|1988-09-07|Centrifugal separator
US2906449A|1959-09-29|Flushing of centrifugal separators of the hermetic type
GB1506628A|1978-04-05|Centrifugal separators
US3871575A|1975-03-18|Centrifugal separator having valve in passageway beneath distributor foot
KR920010883B1|1992-12-21|Maintaining closing-liquid level in centrifuges for operating slide valves
US4643708A|1987-02-17|Centrifuge operating system
US4193537A|1980-03-18|Centrifugal separator with presedimentation means
SE500622C2|1994-07-25|Centrifuge with self-emptying centrifuge drum
US3985292A|1976-10-12|Self-cleaning centrifuge drum with a piston valve defining one side of the sludge chamber
US3648926A|1972-03-14|Liquid-solid separator
SU1667934A1|1991-08-07|Centrifugal liquid separator
US3445062A|1969-05-20|Centrifugal separator apparatus
同族专利:
公开号 | 公开日
FR2522989B1|1987-03-20|
SE458748B|1989-05-08|
DE3208808C2|1984-11-22|
JPS58166950A|1983-10-03|
DE3208808A1|1983-09-22|
DD206943A5|1984-02-15|
SE8301311L|1983-09-12|
SE8301311D0|1983-03-10|
JPS6239013B2|1987-08-20|
GB8306608D0|1983-04-13|
GB2116080B|1985-07-31|
FR2522989A1|1983-09-16|
GB2116080A|1983-09-21|
US4514183A|1985-04-30|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题

DK117207B|1960-04-20|1970-03-23|Separator Ab|Sludge centrifuge.|
SE321896B|1968-02-29|1970-03-16|Alfa Laval Ab|
JPS5730559A|1980-07-29|1982-02-18|Mitsubishi Kakoki Kaisha Ltd|Centrifugal separator|DE3240093C2|1982-10-29|1986-03-27|Westfalia Separator Ag, 4740 Oelde|Centrifuge with a self-cleaning centrifugal drum|
DE3509139C1|1985-03-14|1986-04-17|Westfalia Separator Ag, 4740 Oelde|Centrifuge with a self-draining centrifuge|
DE3621074C1|1986-06-24|1987-08-13|Westfalia Separator Ag|Self-draining centrifugal drum|
SE457856B|1986-11-17|1989-02-06|Alfa Laval Separation Ab|Centrifugal separator with an axially movable annular wear|
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US7320750B2|2003-03-11|2008-01-22|Phase Inc.|Centrifuge with controlled discharge of dense material|
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US7371322B2|2003-07-30|2008-05-13|Phase Inc.|Filtration system and dynamic fluid separation method|
EP1663461A4|2003-07-30|2009-01-14|Phase Inc|Filtration system with enhanced cleaning and dynamic fluid separation|
US7282147B2|2003-10-07|2007-10-16|Phase Inc.|Cleaning hollow core membrane fibers using vibration|
DE102008048934A1|2008-09-25|2010-04-01|Gea Westfalia Separator Gmbh|Centrifuge with a self-cleaning centrifugal drum|
EP2774684B1|2013-03-06|2018-10-17|Alfa Laval Corporate AB|A centrifugal separator|
ES2812749T3|2016-02-22|2021-03-18|Alfa Laval Corp Ab|Centrifugal separator with intermittent discharge system|
法律状态:
优先权:
申请号 | 申请日 | 专利标题
DE3208808A|DE3208808C2|1982-03-11|1982-03-11|Centrifuge with a self-cleaning centrifugal drum|
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