专利摘要:
1. A DEVICE FOR TREATING PULP OF SUSPENSION OF SOLID SUBSTANCES, for example, paper pulp, containing a pretreatment station with an inlet and an outlet connected to the inlet of the squeezing means, characterized in that, with an increase in productivity when energy costs are reduced, a pretreatment station is processed, which is characterized by the fact that, with an increase in productivity when energy costs are reduced, a pretreatment station, which is used for preprocessing, is a pretreatment station that has been processed. the form of perforated containers made of tin installed in the holes of the receiving turntable is equipped with a fixed disk with eccentric located vertices corresponding to the shape of the surface of the bottom of the perforated tank and the inlet opening of the squeezing means, while the tanks are made in the form of a cylinder, a cone, an oval or a rectangle, 2. The device according to claim 1, which is perforated the tank is provided on the inner surface with a mesh or filter cloth. 3. The device according to claim 1, wherein it is equipped with a funnel-shaped catch tank or annular channel located under the fixed disc and connected to its outlet opening. .four. A device according to claim 1, characterized in that it is provided with a seal placed between (U) a fixed disk and a perforated reservoir in the opening of the swivel plate, and made in the form of a receiving ring with a collar facing the fixed disk, and an elastic ring extending for the lower edge of the collar and located wok | tN3 rug it. CO 5. The device according to p. 3, which is shaped so that the seal is provided with an elastic sliding ring located between the bottom surface of the swivel plate and the elastic ring located on the fixed disk. Priority points: 12.05.81 on PP. 1-3, 10.10.81 on PP. 4-5.
公开号:SU1123536A3
申请号:SU823430747
申请日:1982-04-27
公开日:1984-11-07
发明作者:Кох Клаус;Шеффер Ханс-Йоахим;Сюрбиус Герхард
申请人:Херманн Бершторфф Машиненбау,Гмбх (Фирма);
IPC主号:
专利说明:

J The invention relates to a device for treating a pulp-like suspension of solids, in particular for the preliminary dewatering of clarifying sludge, paper pulp, etc., COMPOSITION 1; from a preprocessing station with an outlet connected to an inlet of a squeezing device. A press with a pretreatment station is known, consisting of two press augers located in one housing. With this device, a pulp suspension of solids is pressed and fed to a screw press for subsequent pressing of C13. However, this device is uneconomical when working with a suspension with a high water content, for example, 95%. The closest to the technical issue of the technical essence and the achieved result is a device containing a pretreatment station with an inlet opening and an outlet opening connected to the inlet opening of the squeezing means 2. A disadvantage of the known device is low productivity. The purpose of the invention is to increase productivity while reducing energy costs. The goal is achieved by the fact that in the device containing. The pretreatment station with the inlet and the outlet connected to the inlet of the squeezing means, the pretreatment station is made in the form of rotary receiving plates - perforated oeaeDBvaDOB made of tin, installed in the holes; it is equipped with a fixed squeak with eccentrically located openings corresponding to the outer surface The first perpendicular reservoir and the inlet opening of the squeeze tube are in the form of a cylinder, cone, oval or rectangle. It is advisable to provide a perforated tank on the inner surface with a mesh or filter cloth .. 6 .2 - It is preferable to provide devices with a funnel-shaped catch tank or an annular channel located under the fixed disc and connected to its outlet. . It is advisable to provide the device with a seal placed between the fixed disk and the perforated tank in the opening of the swivel receiving plate, and made in the form of a receiving ring with a collar facing the stationary disk and the elastic ring going out. the lower edge of the collar and located around it. Preferably, the seal is provided with an elastic sliding ring located between the bottom surface of the swivel plate and the elastic ring located on the fixed disk. In FIG. 1 is a view of the SI1 “common device, general VID5 in FIG. 2 a filling nozzle with a filtering sleeve in the form of a stocking attached thereto; a general view5 of FIG. 3 fixed disk with eccentrically located holes, type of xy; in fig. 4 shows a swiveling receiving plate, top view; in FIG. 5, a cone-shaped container of perforated tin, general view; in fig. 6 — rectangular container of perforated tin; in fig. 7. The pressing device with a receiving swivel plate, made in the form of a cylindrical container, cut in FIG. 8 - fixed disk, top view; in fig. 9 base plate of the swivel receiving plate, top view; in fig. 10 - sealing the container from perforated tin; in fig. 11 another embodiment of the seal 5 in FIG. 12 — node I in FIG. 7. The device consists of a pretreatment station 1 and a wring-out screw press 2. The device has a filling nozzle 3 for filling the containers 4-6 from perforated tin. The containers are installed with the possibility of EO rotation. And by means of the receiving rotary plate 7 in the direction of the arrow 8. The tanks have openings 9 through which they are connected to a stationary disk 10. The pressing screw-2 is equipped with a receiving chamber 11. The device is equipped with 311 catching means 12. Through the opening 13 in the receiving swivel plate and the hole 14 in the fixed disk 10, the liquid enters the closed discharge channel 15. The screw 16 of the screw press 2 rotates in the direction of arrow 17 and transports a mixture of liquid and solids in the direction of and arrows 18. The inlet part 19 of the screw press has holes 20 through which liquid is pressed in it. There are radial drills 21 in the auger turn, which are connected to axial drilling 22 along the auger, due to which the dry content is achievable depending on the type of material. substance up to 90%. The device is equipped with a punch 23. It can also be made in the form of a brush and can be operated mainly by means of pneumatics. Using a drive gear 24, which drives a rotation from a drive assembly (not shown) and engages with an internal gear 25 of the swivel receiving plate 7, the corresponding perforated tin receptacle on the swiveling receiving plate 7 alternately passes through the opening 9 of the fixed disk 10 therefore, it can be emptied. In chamber 26, ten receptacles 27-36 of perforated tin are placed. The perforated sheet container 27 is in the emptying position through the opening 37 of the base plate 38. With the downward movement of the punch 39, the process of pushing out and simultaneously cleaning the walls of the container from perforated sheet can be carried out. The released fluid exits through the central tapping hole 40 or through the longitudinal hole 41 in the base plate 38 and through the central hole 42 or the longitudinal hole 43 of the fixed disk 44. Then the liquid is collected in the collecting funnel 45 located under the fixed disk 44, and discharged. If the contents of the perforated sheet container 27 are emptied into the receiving chamber 46 of the screw press, the pre-dried mixture is in the screw press 2. Through the opening 20, LIQUID released in the screw press is withdrawn. In order to avoid accumulations of the pressed mixture in the support of the screw press, the latter is made with a reverse thread 47, which creates a counteraction, and therefore excludes contamination on the auger supports. The cylindrical container is alternately driven in the direction of the arrow 49 (FIG. 9) by means of a drive device with gear wheels 48 (FIG. 9), respectively, through the holes 37 of one of the containers from perforated sheet 27-36 so that the contents of the container from perforated sheet are previously drained to the receiving chamber 46 The containers of perforated sheet (Fig. 7) are made removable, they can be freely removed to be cleaned or repaired without stopping the work of the pretreatment station. Only further connection of the swiveling receiving plate to the removable container is required. The filling nozzle 3 is equipped with a filtering sleeve 50 in the form of a stocking. FIG. 5 shows a cone-shaped container 51 of perforated tin, which is made with an OKOTit 5 taper angle and expands downwards. Such a design is advantageous because the solid particles in the upper part of the container, when the level of the contents of the container decreases, under the action of gravity, are separated from the wall of the container towards the bottom, due to which this container spontaneously clears. FIG. 6 shows a rectangular container 52 of perforated sheet metal with an average line 53. Since the fixed disk 44 and the base plate 38 are made of metal with high sliding properties, energy costs are reduced by alternately moving containers or turning the receiving plate 7 from the drive. A seal 54 is fixed on the lower edge of the perforated sheet container 32 (FIG. 10), which slides over the fixed disk 44 during the alternate rotation of the base plate 38. The receiving ring 56 is shown in the passage 55 (FIG. 11) of the base plate 38, welded to the base plate 38 and having a shoulder 57. Around
the protruding shoulder is elastic ynnotKeHne 56 from a Material with good sliding properties. The elastic seal 58 protrudes through the lower lip 59 of the receiving ring 56, thereby eliminating friction of the receiving ring 56. b fixed disc 44.
. The preferred form of embodiment shown in FIG. 12 also has a receiving ring 56, around which lower edge 59 there is an elastic sliding ring 60, which presses the plastic seal 61 relative to the fixed disk 44,
The device works as follows.
Subject to a dehydrated mixture, for example, a fiber-containing cadium sludge clarified with a dry substance content of about 5%, through a filling tube 3 fills a container 4 of perforated sheet metal. The liquid flows through the perforated walls of the container so that in a very short time the forage cover is reduced. With the help of the swivel receiving plate 7, the three containers 4-6 from perforated tin are rotated in the direction of the arrow 8 so T6. the container 6 is installed under the sealing pipe 3, and the container 5 is installed above the hole 9 of the non-mounted disk 10. The liquid escaping from the envelope of the container from the Perfop Orbit of its tin is captured by means of the catching means 12 which is rigidly connected to the fixed disc 10, and is directed through the opening 13 in the receiving swivel plate 7 and open 14 in the disk 10 in the closed bypass passage 15 finds schiIs above the disk 10 and is rigidly connected with it, № | ek 16
The press 2 rotates in the direction of the arrow .17 and, therefore, captures the mixture of liquid and solids and transports it in the arrow 18 direction. With the help of the screw auger 16, the mixture is further compressed so that a further spin effect is achieved. Through the openings 20, liquid released in the inlet of the screw press is withdrawn. Further drying in the front of the screw press 2 occurs through radial drills 21 in the auger turn, which are connected to axial drilling -22 along the screw, thereby becoming achievable, depending on the type of material, to bring the substance to the bitch to 90%, using a punch 39, respectively under it a container made of perforated tin is emptied, cleared, or the contents of the container is precompacted. With the help of a drive gear 24, engaged with an internal gear 25, the receiving gear hydrochloric plates 7, sootvetstvunzscha capacity of perforated sheet metal or receiving the rotary plate 7 alternately pass through the aperture of the stationary disc 9 and emptied.
If, for pre-drying, a larger number of tanks from perforating (tinned and tin) are provided, moving around the circumference of the swivel plate one after the other, passing to the eccentric flaps in the fixed disk, empty and immediately filled with the initial mixture, then continuous pre-dewatering is obtained with very high throughput at low energy costs.
The proposed device is also reliable because of its low sensitivity to interference and provides continuous high-quality preliminary dewatering of, for example, sludge from 4 to 10% of the dry substance content.
FIG. 2
3
13
.I
.f °: nz: ir ::.
j.t
/ 5f
/
i / o
I 6S
.
.6
n
Ft7
J
FIG. eight
Fig.Z
 g
and
38
59 60 61
Fig. / 2
权利要求:
Claims (6)
[1]
1. DEVICE FOR PROCESSING PULPHOUS SUSPENSION OF SOLIDS, for example, paper pulp, containing a pre-treatment station with an inlet and an outlet connected to the inlet of the squeezing means, characterized in that, in order to increase productivity while reducing energy consumption, the pre-treatment station in the form of perforated tanks and tins installed in the holes of the receiving rotary plate, equipped with a fixed disk with eccentrically located holes holes corresponding to the shape of the surface of the bottom of the perforated reservoir and the inlet of the squeezing means, while the reservoirs are made in the form of a cylinder, cone, oval or rectangle.
[2]
2. The device according to π. 1, about t l and -. characterized in that the perforated tank is provided on the inner surface with a mesh or filter cloth.
[3]
3. The device according to claim 1, characterized in that it is equipped with a funnel-like catching tank or an annular channel located under the fixed disk and connected to its outlet.
[4]
4. The device according to claim 1, characterized in that it is equipped with a seal located between the fixed disk and the perforated reservoir in the opening of the receiving rotary plate, and made in the form of a receiving ring with a shoulder facing the stationary the disk, and an elastic ring extending beyond the lower edge of the shoulder and located around it.
[5]
5. The device according to claim 3, characterized in that the seal is provided with an elastic sliding ring located between the lower surface of the receiving turntable and an elastic ring located on the fixed disk.
Priority on points: 12.05.81 on points. 1-3,
[6]
10.10.81 in claims 4-5.
类似技术:
公开号 | 公开日 | 专利标题
US3190449A|1965-06-22|Filter apparatus
EP0674930B1|1999-12-22|Filtration apparatus for solid-liquid separation from a sludge, corresponding filtration process and use of said apparatus for liquid manure treatment
SU1123536A3|1984-11-07|Apparatus for treating pulp-like suspension of solids
US3966607A|1976-06-29|Solid-liquid separator
US3375776A|1968-04-02|Disintegrating material in a liquid carrier and separating the same
US4525275A|1985-06-25|Concentric filter elements
US3936378A|1976-02-03|Rotary strainer
US2321885A|1943-06-15|Material handling system
US3966617A|1976-06-29|Sludge elevator for fluid clarification system
US4774008A|1988-09-27|Apparatus for separating a mixture into solid and liquid components
US2909286A|1959-10-20|Separator for filtering out solids
US6077425A|2000-06-20|Method of separating a medium into a solids-containing component and a liquid component
DE19839846B4|2007-01-04|centrifuge
CN109293198A|2019-02-01|A kind of sludge floc remove device
US5458775A|1995-10-17|Filtration apparatus for separating solids from liquid containing same
KR100437552B1|2004-07-16|Process and device for separating a medium into a sold mattter-containing component and a liquid component
GB2085750A|1982-05-06|Vacuum apparatus for liquid extraction of solids
US3438503A|1969-04-15|Rotary vacuum filter
CN212370392U|2021-01-19|Horizontal spiral sedimentation centrifuge
CN209646745U|2019-11-19|A kind of centrifuge to maintain equipment
WO1996030102A1|1996-10-03|Dewatering device
CN211937440U|2020-11-17|Discharging structure of portable material pushing centrifugal machine
CN211678275U|2020-10-16|Clean top-suspension bottom-discharge plate centrifuge
CN210796410U|2020-06-19|Boke white beer fine brewing beer centrifugal device
CA2173658A1|1996-10-09|Apparatus for separating liquid from a material
同族专利:
公开号 | 公开日
BR8202722A|1983-04-19|
FR2505728A1|1982-11-19|
IT1150912B|1986-12-17|
FI821659L|1982-11-13|
FI821659A0|1982-05-11|
GB2099324A|1982-12-08|
SE8202926L|1982-11-13|
FR2505728B3|1984-02-17|
US4404101A|1983-09-13|
NO821553L|1982-11-15|
IT8221158D0|1982-05-10|
引用文献:
公开号 | 申请日 | 公开日 | 申请人 | 专利标题

US2452638A|1945-02-07|1948-11-02|Smith Drum & Company|Package extractor|
US3176606A|1963-03-06|1965-04-06|Zoffmann Paul|Apparatus for separating hop leaves from wort|
US3460466A|1965-12-14|1969-08-12|Bauer Bros Co|Press structure|
SE379647B|1970-02-18|1975-10-20|A J Walker|
SE371657B|1973-04-05|1974-11-25|Wallen & Co Ab Lennart|
FR2354293B2|1975-08-19|1983-01-21|Alsthom Atlantique|
DE3043194A1|1980-11-15|1982-07-01|Hermann Berstorff Maschinenbau Gmbh, 3000 Hannover|DEVICE FOR MECHANICALLY SEPARATING LIQUIDS FROM LIQUIDS-SOLIDS MIXTURES IN A SCREW PRESS|AT385429B|1985-03-05|1988-03-25|Scheriau Robert Dipl Ing Dr Te|Automatic dewatering appliance|
US4707277A|1985-03-20|1987-11-17|Uddo Mims International, Inc.|Method and apparatus for removing granular material from an aeration basin|
US5167841A|1985-03-20|1992-12-01|Uddo-Mims-International|Removing material debris from body of water|
US4775487A|1986-12-22|1988-10-04|Consolidation Coal Company|Rotating continuous separation system|
US5221469A|1991-12-09|1993-06-22|Hydroflow, Inc.|Filtration system|
US7410569B1|2005-11-18|2008-08-12|Turhan A. Tilev|Filtration system for metalworking fluids|
US8017021B1|2006-02-01|2011-09-13|Staples Wesley A|Sludge processing apparatus and method|
AT507837B1|2008-12-29|2010-10-15|Andritz Ag Maschf|METHOD AND DEVICE FOR DRAINING AND DISPERSING A FIBROUS MATERIAL|
法律状态:
优先权:
申请号 | 申请日 | 专利标题
DE19813118715|DE3118715A1|1981-05-12|1981-05-12|Pressing-out device for handling a pulpy solids suspension|
DE19813140341|DE3140341A1|1981-10-10|1981-10-10|Pressing device for treating a pasty solids suspension|
[返回顶部]