CN204865114U - Concentrated quick -witted cloth mechanism - Google Patents

Concentrated quick -witted cloth mechanism Download PDF

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Publication number
CN204865114U
CN204865114U CN201520562805.5U CN201520562805U CN204865114U CN 204865114 U CN204865114 U CN 204865114U CN 201520562805 U CN201520562805 U CN 201520562805U CN 204865114 U CN204865114 U CN 204865114U
Authority
CN
China
Prior art keywords
feeder trough
choked flow
guiding gutter
thick bamboo
fixed
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201520562805.5U
Other languages
Chinese (zh)
Inventor
姚宝明
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Huaibei Sino-German Mining Machinery Co Ltd
Original Assignee
Huaibei Sino-German Mining Machinery Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Huaibei Sino-German Mining Machinery Co Ltd filed Critical Huaibei Sino-German Mining Machinery Co Ltd
Priority to CN201520562805.5U priority Critical patent/CN204865114U/en
Application granted granted Critical
Publication of CN204865114U publication Critical patent/CN204865114U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

The utility model relates to a concentrated quick -witted cloth mechanism, including increasing material mouth, feeder trough, a cloth section of thick bamboo, choked flow refraction board, harrow frame, organism, rotation post and guiding gutter, a cloth section of thick bamboo fix at the center of organism, the feeder trough is fixed and is surveyed in the organism, open on the one end of feeder trough surface has two the at least material mouthful of increasing of quantity, the other end surface of feeder trough is connected with the guiding gutter, the guiding gutter is fixed at a cloth section of thick bamboo inboardly, the welding of choked flow refraction board is on rotating the post, choked flow refraction board lies in the centre of a harrow frame and a cloth section of thick bamboo, harrows to put up and fixes on the rotation post, the initial stage construction investment and the manufacturing cost in later stage have been saved in the throughput reinforcing of concentrated machine, and the concentration effect of ore pulp and the clarity of overflow water are improved greatly.

Description

Thickener distribution mechanism
Technical field
The utility model relates to a kind of thickener distribution mechanism.
Background technology
At coal, metallurgical, chemical industry, in these links of industry-by-industry tail Slurry treatment such as environmental protection, one of thickener key equipment becoming extensive use of the concentrated and clarification be mainly used in, in thickener total, the mode that feeds of ore pulp is a very important link, traditional thickener feed, that feed pipe directly feeds in the stabilizing feed well in centre, and stabilizing feed well is more shallow, ore pulp enters into the flocbed of concentration basin, floc sedimentation dropping distance is large, time is long, flocculate and precipitate slower, ore pulp has also carried a large amount of air secretly in the process fed, a large amount of foams is created in thickener pond, directly affects the concentrated effect of ore pulp and the clarity of overflow water.
Summary of the invention
For above-mentioned prior art Problems existing, the utility model provides a kind of thickener distribution mechanism, the disposal ability of thickener strengthens, and save primary construction investment and the production cost in later stage, the concentrated effect of ore pulp and the clarity of overflow water are greatly enhanced.
To achieve these goals, the utility model is achieved through the following technical solutions: a kind of thickener distribution mechanism, comprise and increase material mouth, feeder trough, material distribution cartridge, choked flow deflecting plate, harrow frame, body, Rotational Cylindrical and guiding gutter, described material distribution cartridge is fixed on the center of body, feeder trough is fixed in body and surveys, the end surface of feeder trough has the increasing material mouth of quantity at least two, the other end surface of feeder trough is connected with guiding gutter, guiding gutter is fixed on inside material distribution cartridge, choked flow deflecting plate is welded in Rotational Cylindrical, choked flow deflecting plate is positioned at the centre of harrow frame and material distribution cartridge, harrow frame is fixed in Rotational Cylindrical.
Static mixing plate I and static mixing plate II are respectively welded in described feeder trough inwall both sides, can flocculant and ore pulp be mixed fully, and start to produce flocculation group.
Described choked flow deflecting plate is than cloth tube length 20 ~ 50cm, ensure that ore pulp out enters in thickener pond with spiral radiation shape level in material distribution cartridge, surrounding slowly to pond spreads, shortening floc sedimentation is down to the distance at the bottom of pond, add floc sedimentation to float and enter the resistance of overflow, most of material is directly entered at the bottom of pond, avoid current and the ore pulp of flocculation sediment is produced impact, make full use of effective desilting area of concentration basin, improve flocculation group to greatest extent and re-unite speed.
Described choked flow deflecting plate, than cloth tube length 40cm, finds in process of production, and when choked flow deflecting plate is than cloth tube length 40cm, the effect reached is best.
Find in production test, the disposal ability of thickener, by the every m of original concentration basin 2effective area process 0.2-0.7m 3ore pulp, bring up to the every m of concentration basin 2effective area maximum process 1.5-2.5m 3ore pulp, significantly improve the disposal ability of ore pulp, save primary construction investment and the production cost in later stage, improve nearly one times of production efficiency, and ore pulp can be avoided to enter into the flocbed of concentration basin, floc sedimentation dropping distance reduces, time shorten, flocculation and precipitation are accelerated, and can not be entrained with air, foam can not produce, and the concentrated effect of ore pulp and the clarity of overflow water are greatly enhanced.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the structural representation of guiding gutter;
Fig. 3 is the structural representation of static mixing plate I and static mixing plate II;
In figure: 1, increase material mouth, 2, feeder trough, 3, material distribution cartridge, 4, choked flow deflecting plate, 5, harrow frame, 6, body, 7, Rotational Cylindrical, 8, guiding gutter, 9, static mixing plate I, 10, static mixing plate II.
Detailed description of the invention
Below in conjunction with accompanying drawing, the utility model is described further.
As shown in Figure 1 to Figure 3, this thickener distribution mechanism, comprise and increase material mouth 1, feeder trough 2, material distribution cartridge 3, choked flow deflecting plate 4, harrow frame 5, body 6, Rotational Cylindrical 7 and guiding gutter 8, described material distribution cartridge 3 is fixed on the center of body 6, feeder trough 2 is fixed in body 6 and surveys, the end surface of feeder trough 2 has the increasing material mouth 1 of quantity at least two, flocculant injects in feeder trough by increasing material mouth 1, static mixing plate I 9 and static mixing plate II 10 are respectively welded in feeder trough 2 inwall both sides, , fully flocculant and ore pulp can be mixed, and start to produce flocculation group, the other end surface of feeder trough 2 is connected with guiding gutter 8, guiding gutter 8 is fixed on inside material distribution cartridge 3, choked flow deflecting plate 4 is welded in Rotational Cylindrical 7, choked flow deflecting plate 4 is positioned at the centre of harrow frame 5 and material distribution cartridge 3, harrow frame 5 is fixed in Rotational Cylindrical 7, described choked flow deflecting plate 4 20 ~ 50cm longer than material distribution cartridge 3, find in process of production, when choked flow deflecting plate is than cloth tube length 40cm, in material distribution cartridge 3, ore pulp out enters in thickener pond with spiral radiation shape level, surrounding slowly to pond spreads, shortening floc sedimentation is down to the distance at the bottom of pond, add the resistance that floc sedimentation floating enters overflow, most of material is directly entered at the bottom of pond, avoid current to produce the ore pulp of flocculation sediment and impact, make full use of effective desilting area of concentration basin, improve flocculation group to greatest extent and re-unite speed.

Claims (4)

1. a thickener distribution mechanism, comprise and increase material mouth (1), feeder trough (2), material distribution cartridge (3), choked flow deflecting plate (4), harrow frame (5), body (6), Rotational Cylindrical (7) and guiding gutter (8), it is characterized in that, described material distribution cartridge (3) is fixed on the center of body (6), feeder trough (2) is fixed in body (6) and surveys, the end surface of feeder trough (2) has the increasing material mouth (1) of quantity at least two, the other end surface of feeder trough (2) is connected with guiding gutter (8), guiding gutter (8) is fixed on material distribution cartridge (3) inner side, choked flow deflecting plate (4) is welded in Rotational Cylindrical (7), choked flow deflecting plate (4) is positioned at the centre of harrow frame (5) and material distribution cartridge (3), harrow frame (5) is fixed in Rotational Cylindrical (7).
2. thickener distribution mechanism according to claim 1, is characterized in that, static mixing plate I (9) and static mixing plate II (10) are respectively welded in described feeder trough (2) inwall both sides.
3. thickener distribution mechanism according to claim 1, is characterized in that, described choked flow deflecting plate (4) 20 ~ 50cm longer than material distribution cartridge (3).
4. thickener distribution mechanism according to claim 3, is characterized in that, described choked flow deflecting plate (4) 40cm longer than material distribution cartridge (3).
CN201520562805.5U 2015-07-30 2015-07-30 Concentrated quick -witted cloth mechanism Expired - Fee Related CN204865114U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520562805.5U CN204865114U (en) 2015-07-30 2015-07-30 Concentrated quick -witted cloth mechanism

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520562805.5U CN204865114U (en) 2015-07-30 2015-07-30 Concentrated quick -witted cloth mechanism

Publications (1)

Publication Number Publication Date
CN204865114U true CN204865114U (en) 2015-12-16

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201520562805.5U Expired - Fee Related CN204865114U (en) 2015-07-30 2015-07-30 Concentrated quick -witted cloth mechanism

Country Status (1)

Country Link
CN (1) CN204865114U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111604161A (en) * 2020-05-25 2020-09-01 中钢集团山东矿业有限公司 Tailing comprehensive utilization production line and method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN111604161A (en) * 2020-05-25 2020-09-01 中钢集团山东矿业有限公司 Tailing comprehensive utilization production line and method

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20151216

Termination date: 20170730