CN2113824U - Slurry concentrating chamber - Google Patents
Slurry concentrating chamber Download PDFInfo
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- CN2113824U CN2113824U CN 91232835 CN91232835U CN2113824U CN 2113824 U CN2113824 U CN 2113824U CN 91232835 CN91232835 CN 91232835 CN 91232835 U CN91232835 U CN 91232835U CN 2113824 U CN2113824 U CN 2113824U
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Abstract
The utility model relates to a settling tank for separating suspended solid microparticle from liquid with deposition method, particularly a slurry concentrating chamber used in the slurry for separating the solid from liquid, concentrating and draining the concentrating slurry, and mainly solves the problems of nonmotile running, large processing ability, favoring draining, etc. The utility model comprises a vertical chamber body (1), a chute purification plant (2), a supplying slurry device (3) and a draining device of fluidize inverted U-tube (4), and has the advantages that the chamber does not need scraping mud device, power drive device thereof and flocculating reagent, has large processing ability and stockpiling capacity, can drain slurry automatically and adjust production, and is suitable for the selecting and smelting field of slurry concentration and the water processing field of turbid water clarification.
Description
The utility model relate to a kind of with sedimentation with the subsider that separates in the suspended solid particles from liquid, especially slurry carried out Separation of Solid and Liquid, concentrate and will concentrate the concentrated storehouse that slurry is discharged, the ore pulp concentrator that generally uses both at home and abroad mainly is the concentrator of peripheral transmission or center transmission at present.This legacy equipment not only consumes electric power and flocculant, and floor space is big, and disposal ability is low, also needs mud-scraping apparatus, complex structure.Patents such as CN86201178U, CN2030107U and CN2045324U, though traditional concentrator has been done improvement, still need mud-scraping apparatus and actuating unit thereof, still needing to use flocculant, disposal ability is still not high.
The muddy water clarification equipment that uses both at home and abroad at present mainly is preliminary sedimentation tank.This legacy equipment exists also that floor space is big, cost is high, inefficient shortcoming.Patent such as CN2043130U, CN2045667U, though traditional preliminary sedimentation tank has been done improvement, but only be applicable to that the clarification sand content is less than 6% muddy water, and also need to add flocculant when handling, special public clear 61-47562, special public clear 63-44402 have announced a kind of precipitation separation device, though warehouse is rational in infrastructure, disposal ability is little, can not adapt to the requirement that ore pulp concentrates.
The purpose of this utility model is to overcome the weak point of above-mentioned known technology and a kind of mud-scraping apparatus and actuating unit thereof of not needing is provided, and does not generally need to add flocculant, and floor space is little, and disposal ability is big, the efficient storehouse that concentrates that underflow density is high.
Another purpose of the present utility model also is to provide a kind of not only can satisfy above-mentioned requirements, but also can regulate underflow density as required, in case the plasma discharge difficulty, the efficient storehouse that concentrates that can remove obstacles rapidly.
The purpose of this utility model can reach by following scheme:
The scheme of adopt a kind of vertical warehouse, inclined tube purifier, combining for proportioning device and slurry-discharging equipment.The vertical warehouse of this scheme is made up of dark cone, cylindrical shell, overflow launder and trestle that many pillars, bottom have the plasma discharge mouth.Comprise that to proportioning device the center gives slurry pipe, with the center give that the slurry pipe fuses join the slurry pipe, with join buffer that the slurry pipe end all is connected, the center given starched pipe and be fixed on straight tube bearing on the trestle.
The purpose of this utility model can also reach by following scheme:
Dark cone lower end at such scheme is provided with a slurry-discharging equipment, and this device also can add fluidization equipment.
The accompanying drawing drawing is described as follows:
Fig. 1 concentrates the storehouse front view for ore pulp.
Fig. 2 is vertical warehouse front view.
Fig. 3 is the A-A cutaway view of Fig. 1.
Fig. 4 is a fluidization inverted-loop tube device front view.
Fig. 5 is the B-B cutaway view of Fig. 4.
Fig. 6 is the C-C cutaway view of Fig. 4.
The utility model is described in further detail below in conjunction with accompanying drawing:
The utility model ore pulp concentrates chamber structure as shown in Figure 1.Mainly comprise vertical warehouse (1), give proportioning device (2), inclined tube purifier (3), fluidization inverted-loop tube slurry-discharging equipment (4).
The structure of vertical warehouse (1) as shown in Figure 2.Mainly comprise many pillars (1-a), dark cone (1-b), cylindrical shell (1-c), bearing (1-d), overflow launder (1-e), trestle (1-f).Whole vertical warehouse can be welded into one by steel part, also can be watered by armored concrete and be integral.The cylindrical shell section can be circle, also can be polygon.Overflow launder can be the single annular groove, also can be the combination slot of cannelure and radius.
Can be single-point to proportioning device and joined the slurry mode, also can be multiple spot and give the slurry mode of joining.This example is at 3 and gives the slurry mode of joining.Its structure as shown in figures 1 and 3.It comprises that the center joins slurry pipe (7), 3 buffers (8) for slurry pipe (6), 3.It is fixed on the trestle (1-f) with straight tube bearing (5).Join slurry Guan Zaiyong erecting by overhang for every and be hung on the crossbeam (9), its arrangement mode is: at vertical plane, joining the slurry pipe has certain inclination angle, at horizontal plane, joins the slurry pipe and is mutually 120 °.Buffer (8) is fixed on joins slurry pipe (7) end, mainly is made up of umbrella shape plate and fixture thereof.
The inclined tube purifier is made up of frp honeycomb inclined tube and bracing or strutting arrangement thereof.The inclined tube purifier as shown in figures 1 and 3 in this example.It mainly comprises frp honeycomb inclined tube (12), the crossbeam (9) of support glass steel honeycomb inclined-tube (12), the rack (10) and the wire netting (11) of reinforcing frp honeycomb inclined tube (12).
The structure of fluidization inverted-loop tube slurry-discharging equipment such as Fig. 4 are to shown in Figure 6.
The structure of slurry-discharging equipment as shown in Figure 4.It mainly comprises center discharge pipe (16), inverted U-shaped discharge pipe (25), bottom discharge pipe (18), hose valve (19), fluidised form bag (24).Wherein, manage (16) and be contained in top, fluidised form bag (24) center, it and inverted U-shaped discharge pipe (25) are the main pipe of using of normal discharge pipe together; Pipe (18) is contained in fluidised form bag (24) central lower, is the bottom-dump discharge pipe, mainly is as emptying usefulness, also can be used as the standby pipes of normal discharge pipe.
Fluidization equipment is to regulate underflow density or plasma discharge just use at need at needs.It comprises umbrella shape fluidization equipment and annular fluidization equipment.The umbrella shape fluidization equipment comprises pressure water supply pipe (12-a), umbrella hat (13), pressurized tank (14), nozzle (15-a), blow-down pipe (22-a).Nozzle quantity is determined according to concentrated phase layer concentration being become requirement transportation concentration time institute amount of water.Nozzle in this example (15-a) has 8, is welded on pressurized tank (14) circumference, as shown in Figure 4 and Figure 5 by pseudo-tilted radiation shape is uniform.The annular fluidization equipment comprises pressure water supply pipe (12-b), annular pressure pipe (23), nozzle (15-b), blow-down pipe (22-b).Nozzle (15-b) has 8, is welded on the annular pressure pipe (23) its welding position and angle such as Fig. 4 and shown in Figure 6, uniform 4 of inner ring, injection direction points to center discharge pipe (16), uniform 4 of outer ring, and injection direction points to fluidised form bag (24) upper inside wall position.
Fluidization inverted-loop tube slurry-discharging equipment is welding and bolt fastening structure, and it is fixed, installation method is: the umbrella hat of umbrella shape fluidization equipment (13) is welded on the column upper end of bracing frame (17); The annular pressure pipe (23) of annular fluidization equipment is fixed on the column bottom of bracing frame (17) with angle steel clip (21) and bolt, nut; Column is made by steel pipe, and it is enclosed within on the backstay (20); On backstay (20) is welded at the bottom of the awl of fluidised form bag (24).
The utility model ore pulp concentrates, discharge process can be summarized as follows: low concentration slurry (thin pulp) enters for slurry pipe (6) by the center, after joining slurry pipe (7), buffer (8) deceleration, break-in, at first carry out Separation of Solid and Liquid, it is the higher slurry of solid content, dependence is from resedimentation, to dark cone (1-b); Contain the less liquid of particulate and rise,, become supernatant, come together in overflow launder (1-e), discharge outside the storehouse by overflow pipe through the further post precipitation of inclined tube purifier (2).
After the solid-liquid separation on ore pulp, promptly begin to concentrate, discharge.After the higher concentration slurry is reduced to dark cone (1-b), it is close to carry out three axial compressions, forms the high concentration concentrated phase layer (underflow) of a densification at this, and this underflow glides swimmingly along awl base slope angle, and be pressed into center discharge pipe (16), discharge smoothly through inverted-loop tube (25).
During in the ordinary course of things with normal operation, do not need to use fluidization equipment, just when needs are regulated underflow density and eliminated the plasma discharge obstacle, just use, and service time is very short, gets final product in about 10~20 minutes.
Utilize above-mentioned ore pulp to concentrate the storehouse, carried out iron raw ore slurry, iron ore concentrate slurry, three kinds of slurries of uranium raw ore slurry industry concentration test, experimental condition, result are as shown in the table.
The utility model has following advantage and good effect compared to existing technology:
1. the saving energy. Should concentrate the storehouse did not need power in the ordinary course of things, and no power consumption is just regulated underflow density and underflow discharge at need at needs, just need short time startup fluidization equipment.
2. saving material. When concentrating general particle slurry, do not need to use flocculant, only when concentrating special Fine Particle Slurry, just need to use a small amount of flocculant.
3. floor space is little, disposal ability is big. The big several times of the more traditional concentrator of unit are disposal ability.
4. plasma discharge is smooth. By the inverted-loop tube slurry-discharging equipment, generally can both successfully discharge underflow, even discharging is obstructed, utilize fluidization equipment, just can in time discharge obstacle.
5. maneuverability. Should concentrate the storehouse have certain storage slurry ability, and when operation or rear operation generation short duration failure, the unlikely system that affects stops production, and has kept the continuity of localized production before concentrating the storehouse.
Claims (9)
1, a kind of ore pulp concentrates the storehouse, it has vertical warehouse (1), with the inclined tube purifier (2) that is contained in vertical warehouse (1) lining, wherein vertical warehouse (1) comprises many pillars (1-a) again, and dark cone (1-b) and the cylindrical shell (1-c) supported by its, dark cone (1-b) bottom has the plasma discharge mouth, and the interior accent of cylindrical shell (1-c) has overflow launder (1-e); Inclined tube purifier (2) comprises the frp honeycomb inclined tube (12) that is contained in overflow launder (1-e) bottom again, and the crossbeam (9) of support glass steel honeycomb inclined-tube and bearing (1-d) thereof, it is characterized in that vertical warehouse (1) inner chamber is equipped with to proportioning device (3), it is positioned at below the inclined tube purifier (2), and slurry-discharging equipment (4) is equipped with in dark cone (1-b) bottom.
2, concentrate the storehouse by the described ore pulp of claim 1, it is characterized in that giving proportioning device for multiple spot to proportioning device (3), it comprises that the center gives slurry pipe (6), the slurry of joining of giving slurry pipe (6) lower end at the center and fusing with it is managed (7), at the buffer (8) of joining slurry pipe (7) lower end and fusing with it, be fixed on straight tube bearing (5) on the trestle (1-f) for slurry pipe (6) at the center, trestle (1-f) is contained in cylindrical shell (1-c) top.
3, concentrate the storehouse by claim 1 or 2 described ore pulps, it is characterized in that slurry-discharging equipment (4) is the inverted-loop tube slurry-discharging equipment, it comprises the fluidised form bag (24) that links to each other with dark cone (1-b) bottom, be positioned at the center discharge pipe (16) at fluidised form bag (24) center, the inverted U-shaped discharge pipe (25) that is positioned at center discharge pipe (16) top and fuses with it.
4, concentrate the storehouse by claim 1 or 2 described ore pulps, it is characterized in that slurry-discharging equipment (4) is the bottom slurry-discharging equipment, it comprises the fluidised form bag (24) that links to each other with dark cone (1-b) bottom, the bottom discharge pipe (18) that links to each other with fluidised form bag (24) bottom and be contained in hose valve (19) on the bottom discharge pipe (18).
5, concentrate the storehouse by the described ore pulp of claim 4, it is characterized in that slurry-discharging equipment (4) installs an inverted-loop tube slurry-discharging equipment additional, it comprises center discharge pipe (16) and inverted U-shaped discharge pipe (25).
6, concentrate the storehouse by the described ore pulp of claim 5, it is characterized in that fluidised form bag (24) inner chamber top is equipped with the umbrella shape fluidization equipment, it comprises pressure water supply pipe (12-a), the umbrella hat (13) of encirclement center discharge pipe (16), communicate with pressure water supply pipe (12-a) and surround the pressurized tank (14) of center discharge pipe (16), with the peripheral nozzle (15-a) that links to each other of pressurized tank (14), the blow-down pipe (22-a) that links to each other with the pressurized tank bottom.
7, concentrate the storehouse by the described ore pulp of claim 5, it is characterized in that fluidised form bag (24) inner chamber bottom is equipped with annular fluidization equipment, it comprises pressure water supply pipe (12-b), the annular pressure pipe (23) that links to each other with pressure water supply pipe (12-b), nozzle (15-b) that links to each other with annular pressure pipe (23) and blow-down pipe (22-b).
8, concentrate the storehouse by the described ore pulp of claim 7, it is characterized in that fluidised form bag (24) inner chamber top is equipped with the umbrella shape fluidization equipment, it comprises pressure water supply pipe (12-a), the umbrella hat (13) of encirclement center discharge pipe (16), communicate with pressure water supply pipe (12-a) and surround the pressurized tank (14) of center discharge pipe (16), with the nozzle (15-a) that pressurized tank (14) periphery links to each other, the blow-down pipe (22-a) that links to each other with the pressurized tank bottom.
9, concentrate the storehouse by the described ore pulp of claim 8, it is characterized in that fluidised form bag (24) lining is equipped with bracing or strutting arrangement, it comprises the bracing frame (17) that fuses with umbrella shape fluidization equipment and annular fluidization equipment, the backstay (20) of fixing support rack (17), the angle steel clip (21) that connects annular force pipe (23), backstay (20) are welded in fluidised form bag (24) intracavity bottom.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 91232835 CN2113824U (en) | 1991-12-28 | 1991-12-28 | Slurry concentrating chamber |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 91232835 CN2113824U (en) | 1991-12-28 | 1991-12-28 | Slurry concentrating chamber |
Publications (1)
Publication Number | Publication Date |
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CN2113824U true CN2113824U (en) | 1992-08-26 |
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ID=4937793
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN 91232835 Granted CN2113824U (en) | 1991-12-28 | 1991-12-28 | Slurry concentrating chamber |
Country Status (1)
Country | Link |
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CN (1) | CN2113824U (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103252115A (en) * | 2013-05-31 | 2013-08-21 | 云南大红山管道有限公司 | Dehydrating device for improving concentration of slurry |
CN103830940A (en) * | 2014-03-19 | 2014-06-04 | 常州神力热喷涂技术有限公司 | Non-turbulence sediment box |
CN111643932A (en) * | 2020-06-15 | 2020-09-11 | 泉州台商投资区双艺商贸有限公司 | Sedimentation tank for sewage treatment |
-
1991
- 1991-12-28 CN CN 91232835 patent/CN2113824U/en active Granted
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103252115A (en) * | 2013-05-31 | 2013-08-21 | 云南大红山管道有限公司 | Dehydrating device for improving concentration of slurry |
CN103252115B (en) * | 2013-05-31 | 2015-04-01 | 云南大红山管道有限公司 | Dehydrating device for improving concentration of slurry |
CN103830940A (en) * | 2014-03-19 | 2014-06-04 | 常州神力热喷涂技术有限公司 | Non-turbulence sediment box |
CN103830940B (en) * | 2014-03-19 | 2016-02-03 | 常州神力热喷涂技术有限公司 | Without turbulent settling tank |
CN111643932A (en) * | 2020-06-15 | 2020-09-11 | 泉州台商投资区双艺商贸有限公司 | Sedimentation tank for sewage treatment |
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C06 | Publication | ||
PB01 | Publication | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |