CN206463550U - A kind of thickener - Google Patents

A kind of thickener Download PDF

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Publication number
CN206463550U
CN206463550U CN201720147165.0U CN201720147165U CN206463550U CN 206463550 U CN206463550 U CN 206463550U CN 201720147165 U CN201720147165 U CN 201720147165U CN 206463550 U CN206463550 U CN 206463550U
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CN
China
Prior art keywords
pond body
current stabilization
rotational flow
feeding device
thickener
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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
CN201720147165.0U
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Chinese (zh)
Inventor
张永安
杨宇
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.)
Holy Finlay Coal Preparation Engineering Technology (tianjin) Co Ltd
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Holy Finlay Coal Preparation Engineering Technology (tianjin) Co Ltd
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Priority to CN201720147165.0U priority Critical patent/CN206463550U/en
Application granted granted Critical
Publication of CN206463550U publication Critical patent/CN206463550U/en
Expired - Fee Related legal-status Critical Current
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Abstract

This application discloses a kind of thickener, including:Pond body, bottom centre is provided with underflow opening;Crane span structure, is fixed in pond body;Drive device, is fixed on crane span structure;Harrow frame, one end is connected with drive device, and other end movable supporting is in pond body;Scraper plate, is arranged in harrow frame;Rotational flow feeding device, is fixed in pond body vertically, and its tangential direction is provided with feeding mouth;Current stabilization distributor is provided with and respectively communicated with the top and bottom of current stabilization distributor, rotational flow feeding device, current stabilization distributor is enclosed construction, radially offers multiple cloth holes.This thickener carries out multiple eddy flow concentration by least two cyclones, and the material of various concentrations, granularity is passed through into the current stabilization distributor radial discharge positioned at different height to the decanting zone of pond body, compressional zone or underflow discharge area.While improving the treating capacity of thickener, material is reduced by current stabilization distributor and delivers kinetic energy, so that material will not disturb settled material bed, concentration and settlement effect is improved.

Description

A kind of thickener
Technical field
The utility model is related to ore dressing or coal preparation technology field, more particularly to a kind of thickener.
Background technology
Thickener is mainly used in coal separation or ore dressing process concentrating floating tail-coal or cleaned coal, passes through the nature of particle Flocculating setting after sedimentation or addition medicament, makes most solid particles sediment to motor spindle is concentrated, is driven and scraped by harrow frame Plate makes the material after sedimentation assemble to thickener bottom centre discharge gate, realizes the sedimentation and concentration of solid material.And after clarifying Clear water from thickener upper strata overfall discharge, return production system recycle.
Conventional thickener pan feeding mode is fairly simple at present, is fed mostly by center to barrel in waterfall mode.By Unreasonable in feed-type, all materials have fed the decanting zone of thickener, at the same pan feeding ore pulp to thickener inside The material bed disturbance for settling layering is larger, often results in that thickener unit area treating capacity is small, overflow thin mud concentration high, reduces dense The treatment effect of contracting machine.
Utility model content
In view of this, the purpose of this utility model is to provide a kind of thickener, to reduce to having been settled in thickener The material bed disturbance of layering, improves thickening efficiency.
To reach above-mentioned purpose, the utility model provides following technical scheme:
A kind of thickener, including:
Pond body, the bottom of the pond body is taper, and the bottom centre of the pond body is provided with underflow opening;
Crane span structure, is fixed in the pond body;
Drive device, is fixed on the crane span structure;
Harrow frame, one end is connected with the drive device, and other end movable supporting is in the pond body, in the pond body The heart is rotated;
Scraper plate, is arranged in the harrow frame, for by the deposition material scraper of the pond body bottom to the underflow opening;
Rotational flow feeding device, is fixed in the pond body vertically, and the rotational flow feeding device is provided with along its tangential direction Feeding mouth;
The current stabilization distributor is provided with and respectively communicated with the top and bottom of current stabilization distributor, the rotational flow feeding device, The current stabilization distributor is enclosed construction, and the radial direction of the current stabilization distributor offers multiple cloth holes.
It is preferred that, in above-mentioned thickener, the rotational flow feeding device includes at least two be arranged in series above and below vertical Individual cyclone, the top of each cyclone is provided with and communicated with the current stabilization distributor, two eddy flows being in series The bottom discharge mouthful of the cyclone above in device is connected with the feeding mouth of the underlying cyclone, is located at The bottom of the cyclone of bottom is provided with and communicated with the current stabilization distributor.
It is preferred that, in above-mentioned thickener, the top of the cyclone is cylindrical shape, and bottom is cone.
It is preferred that, in above-mentioned thickener, the quantity in the cloth hole on each current stabilization distributor is 8~16 It is individual.
It is preferred that, in above-mentioned thickener, the cloth hole on each current stabilization distributor is along the circumferential direction equal Even distribution.
It is preferred that, in above-mentioned thickener, the quantity of the feeding mouth of the rotational flow feeding device is 2~4.
It is preferred that, in above-mentioned thickener, the feeding mouth of the rotational flow feeding device along the circumferential direction uniformly divides Cloth.
It is preferred that, in above-mentioned thickener, the rotational flow feeding device is fixed in the pond body by support.
It is preferred that, in above-mentioned thickener, the top edge of the pond body is provided with overflow launder.
It is preferred that, in above-mentioned thickener, the harrow frame is supported in the pond body by pulley rolling.
Compared with prior art, the beneficial effects of the utility model are:
In the thickener that the utility model is provided, including pond body, crane span structure, drive device, harrow frame, scraper plate, eddy flow pan feeding dress Put and drive harrow frame with respect to the center rotating of pond body with current stabilization distributor, drive device, and then drive scraper plate by the heavy of pond body bottom Underflow opening of the product material scraper to pond body.Ore pulp enters rotational flow feeding device by the feeding mouth of rotational flow feeding device with tangential way In, eddy flow concentration is carried out in rotational flow feeding device, the fine granular materials of low concentration enter steady from the top of rotational flow feeding device In flow distributor, in the presence of current stabilization distributor, the kinetic energy of most of ore pulp is eliminated, and then passes through current stabilization distributor bottom Cloth hole radially into pond body upper strata decanting zone, after further settling, clear water is discharged above the pond body, returns to production system System is recycled;And the coarse granule material of the high concentration in rotational flow feeding device enters another current stabilization distributor from bottom In, high concentration coarse granule material is entered traveling one radially into the lower floor decanting zone of pond body by the cloth hole of the current stabilization distributor Step sedimentation compression is directly entered pond body bottom discharge area, shortens settling height, reduces the inventory into decanting zone, carries High thickener treating capacity, and kinetic energy is eliminated by current stabilization distributor, static pan feeding is realized, again will not be in vertical direction Particle sedimentation is impacted, thus, either low concentration fine granular materials or high concentration coarse granule material are in respective material Layer is settled, and will not disturb deposited good material bed, improves thickening efficiency.
Brief description of the drawings
, below will be to embodiment in order to illustrate more clearly of the utility model embodiment or technical scheme of the prior art Or the accompanying drawing used required in description of the prior art is briefly described, it should be apparent that, drawings in the following description are only It is embodiment of the present utility model, for those of ordinary skill in the art, on the premise of not paying creative work, also Other accompanying drawings can be obtained according to the accompanying drawing of offer.
A kind of structural representation for thickener that Fig. 1 provides for the utility model embodiment;
Fig. 2 be Fig. 1 in pulley partial enlarged drawing.
Wherein, 1 it is pond body, 101 be overflow launder, 102 be underflow opening, 2 be crane span structure, 3 be drive device, 4 be harrow frame, 5 is Pulley, 6 be scraper plate, 7 be rotational flow feeding device, 71 be forward spin flow device, 72 be lower cyclone, 701 be feeding mouth, 8 be current stabilization point Cloth device, 9 are support.
Embodiment
Core of the present utility model there is provided a kind of thickener, reduce the material to having settled layering in thickener The disturbance of layer, improves thickening efficiency and treating capacity.
Below in conjunction with the accompanying drawing in the utility model embodiment, the technical scheme in the utility model embodiment is carried out Clearly and completely describe, it is clear that described embodiment is only a part of embodiment of the utility model, rather than whole Embodiment.Based on the embodiment in the utility model, those of ordinary skill in the art are not under the premise of creative work is made The every other embodiment obtained, belongs to the scope of the utility model protection.
Refer to Fig. 1, the utility model embodiment provides a kind of thickener, including pond body 1, crane span structure 2, drive device 3, Harrow frame 4, scraper plate 6, rotational flow feeding device 7 and current stabilization distributor 8.Wherein, the bottom of pond body 1 is taper, the bottom centre of pond body 1 It is material decanting zone around discharge region, discharge region that region, which is, and the bottom centre of pond body 1 is provided with underflow opening 102;Crane span structure 2 is consolidated It is scheduled in pond body 1, one end of crane span structure 2 is fixed on the edge of pond body 1, and one end is suspended in the overcentre region of pond body 1, for propping up Drive device 3 and harrow frame 4 are installed in support;Drive device 3 is fixed on crane span structure 2, is preferably placed at the overcentre region of pond body 1, is driven Dynamic device 3 can be motor or current collecting equipment etc.;One end of harrow frame 4 is connected with drive device 3, and other end movable supporting is in pond body On 1, drive device 3 drives harrow frame 4 around the center rotating of pond body 1;Scraper plate 6 is arranged in harrow frame 4, scraper plate 6 and the bottom of pond body 1 Laminating is close, for by the deposition material scraper of the bottom of pond body 1 to underflow opening 102;Rotational flow feeding device 7 is fixed on pond body 1 vertically Interior, rotational flow feeding device 7 is provided with feeding mouth 701 along its tangential direction;The top and bottom of rotational flow feeding device 7 are respectively communicated with A current stabilization distributor 8 is provided with, specifically, the top of rotational flow feeding device 7 passes through the bottom of overflow pipe and current stabilization distributor 8 Center is connected, and the bottom of rotational flow feeding device 7 is connected by the central upper portion position of underflow pipe and another current stabilization distributor 8 Logical, current stabilization distributor 8 is enclosed construction, preferably cylinder enclosed structure, and the radial direction of current stabilization distributor 9 offers multiple cloth holes 801。
The operation principle and the course of work of the thickener be:Ore pulp is by the feeding mouth 701 of rotational flow feeding device 7 with tangent line Mode enters in rotational flow feeding device 7, carries out eddy flow concentration in the rotational flow feeding device 7, and the fine granular materials of low concentration are from rotation The top for flowing feeding device 7 enters in current stabilization distributor 8, and in the presence of current stabilization distributor 8, the kinetic energy of most of ore pulp is disappeared Remove, then by the cloth hole 801 of current stabilization distributor 8 radially into the upper strata decanting zone of pond body 1, after further sedimentation, clearly Water is discharged from the top of pond body 1, is returned to production system and is recycled;And the high concentration that eddy flow is concentrated in rotational flow feeding device 7 is thick Granule materials enter in another current stabilization distributor 8 from bottom, make high concentration thick by the cloth hole 801 of the current stabilization distributor 8 Granule materials carry out further sedimentation radially into the lower floor decanting zone of pond body 1 and compress or be directly entered the bottom discharge area of pond body 1, Settling height is shortened, the inventory into decanting zone is reduced, improves thickener treating capacity, and pass through current stabilization distributor 8 Kinetic energy is eliminated, static pan feeding is realized, the particle sedimentation in vertical direction will not be impacted again.Thus, it is either low dense Degree fine granular materials or high concentration coarse granule material are settled each material bed, will not disturb deposited good thing The bed of material, improves thickening efficiency.
As shown in figure 1, present embodiments providing a kind of specific rotational flow feeding device 7, the rotational flow feeding device 7 includes perpendicular Straight at least two cyclones being arranged in series up and down, the top of each cyclone is provided with and communicated with current stabilization distributor 8, is in series Each two cyclone in, the bottom discharge mouthful and the pan feeding of a underlying cyclone of a cyclone above Mouth connection, and the bottom of a cyclone positioned at bottom is provided with and communicated with current stabilization distributor 8.
The operation principle of the rotational flow feeding device 7 is:Said so that rotational flow feeding device 7 includes two cyclones as an example Bright, i.e., rotational flow feeding device 7 includes the forward spin flow device 71 and lower cyclone 72 of vertical series connection up and down, and ore pulp first passes through forward spin flow device Feeding mouth 701 on 71 tangentially enters in forward spin flow device 71, and eddy flow concentration, the fine grained of low concentration are carried out in forward spin flow device 71 Material enters in the current stabilization distributor 8 at top from the top of forward spin flow device 71, and current stabilization is carried out in the current stabilization distributor 8 at top Afterwards, most of kinetic energy is eliminated, material is from upper strata decanting zone of the cloth hole 801 radially into pond body 1, the fine particle of low concentration After material continues to settle in upper strata decanting zone, clear water is discharged from the top of pond body 1;And the higher concentration of the inward eddy of forward spin flow device 71 concentration Material enter the feeding mouth of lower cyclone 72 from the discharging opening of forward spin flow device 71, and carry out in lower cyclone 72 swirl flow Concentration, obtains the material and high concentration coarse granule material of intermediate concentration granularity, and the material of intermediate concentration is from the top of lower cyclone 72 Portion enters another current stabilization distributor 8, is compressed by the cloth hole 801 of the current stabilization distributor 8 radially into the lower floor of pond body 1 Area, further settle and compress after dehydration, the scraper plate 6 driven through harrow frame 4, which is scraped to the underflow opening 102 of pond body 1, discharges, highly concentrated Spend coarse granule material then to enter in the current stabilization distributor 8 of bottom of lower cyclone 72, the current stabilization distributor 8 through bottom is directly entered Bottom discharge area, is directly discharged by underflow opening 102.
It can be seen that, eddy flow twice is carried out by the vertical forward spin flow device 71 being arranged in series up and down and lower cyclone 72 and concentrated, will Various concentrations, the material of granularity pass through the heavy of the radial discharge of current stabilization distributor 8 positioned at different height to the different height of pond body Area, compressional zone and bottom discharge area drop.So as to shorten settling height, while improving the treating capacity of thickener, pass through Current stabilization distributor 8 reduces material and delivers kinetic energy, so that the material delivered will not disturb material bed, the improvement settled Concentration and settlement effect.
For the rotational flow feeding device being composed in series above and below more cyclones such as three cyclones, four cyclones, It is identical when operation principle is with two cyclones, it will not be repeated here, cyclone is determined according to the size and material handling capacity of pond body 1 Quantity.
As optimization, the top of cyclone is cylindrical shape, and bottom is cone, and feeding mouth is tangentially disposed in along columnar Top, material carries out eddy flow concentration in conical lower, adds swirl velocity.Certainly, cyclone can also be other knots Structure, such as generally cylindrical shape or cone.
In the present embodiment, the quantity of the feeding mouth 701 of rotational flow feeding device 7 is 2~4, and is tangentially set On rotational flow feeding device 7.Specifically, the top of forward spin flow device 71 is provided with 2~4 feeding mouths 701.
Further, feeding mouth 701 is evenly distributed in the circumferential direction on rotational flow feeding device 7, improves pan feeding uniformity.
In the present embodiment, the quantity in the cloth hole 801 on each current stabilization distributor 8 is 8~16, it is highly preferred that often Cloth hole 801 on individual current stabilization distributor 8 is distributed uniformly and circumferentially, so that material is evenly into pond body 1.
In the present embodiment, rotational flow feeding device 7 is fixed in pond body 1 by support 9, and pond body 1 is suspended in by support 9 Inside, support 9 does not hinder the sedimentation of material.
The clear water of pond body 1 is reclaimed for convenience, in the present embodiment, the top edge of pond body 1 is provided with overflow Groove 101, clear water is recycled to production system by overflow launder 101 and recycled.
As shown in Fig. 2 in the present embodiment, harrow frame 4 by the rolling support of pulley 5 in pond body 1, one end of harrow frame 4 with Drive device 3 is connected, and the other end is provided with pulley 5, and pulley 5 is rolled in pond body 1 along upper, facilitates harrow frame 4 around the center of pond body 1 Rotate.Certainly, harrow frame 4 can also be supported with coordinating in pond body 1 along slide rail.
The embodiment of each in this specification is described by the way of progressive, and what each embodiment was stressed is and other Between the difference of embodiment, each embodiment identical similar portion mutually referring to.
The foregoing description of the disclosed embodiments, enables professional and technical personnel in the field to realize or new using this practicality Type.A variety of modifications to these embodiments will be apparent for those skilled in the art, determine herein The General Principle of justice can in other embodiments be realized in the case where not departing from spirit or scope of the present utility model.Cause This, the utility model is not intended to be limited to the embodiments shown herein, and is to fit to and principles disclosed herein The most wide scope consistent with features of novelty.

Claims (10)

1. a kind of thickener, it is characterised in that including:
Pond body (1), the bottom of the pond body (1) is taper, and the bottom centre of the pond body (1) is provided with underflow opening (102);
Crane span structure (2), is fixed in the pond body (1);
Drive device (3), is fixed on the crane span structure (2);
Harrow frame (4), one end is connected with the drive device (3), and other end movable supporting is in the pond body (1), around the pond The center rotating of body (1);
Scraper plate (6), is arranged in the harrow frame (4), for by the deposition material scraper of the pond body (1) bottom to the underflow opening (102);
Rotational flow feeding device (7), is fixed in the pond body (1), the rotational flow feeding device (7) sets along its tangential direction vertically It is equipped with feeding mouth (701);
The current stabilization distributor is provided with and respectively communicated with the top and bottom of current stabilization distributor (8), the rotational flow feeding device (7) (8), the current stabilization distributor (8) is enclosed construction, and the radial direction of the current stabilization distributor (8) offers multiple cloth holes (801).
2. thickener according to claim 1, it is characterised in that the rotational flow feeding device (7) includes vertical string up and down Join at least two cyclones set, the top of each cyclone is provided with and communicated with the current stabilization distributor (8), mutually gone here and there Bottom discharge mouthful and the underlying cyclone of the cyclone above in two cyclones of connection Feeding mouth connection, be provided with and communicated with the current stabilization distributor (8) positioned at the bottom of the cyclone of bottom.
3. thickener according to claim 2, it is characterised in that the top of the cyclone is cylindrical shape, bottom is circle Taper.
4. thickener according to claim 1, it is characterised in that the cloth on each current stabilization distributor (8) The quantity in hole (801) is 8~16.
5. thickener according to claim 1, it is characterised in that the cloth on each current stabilization distributor (8) Hole (801) is distributed uniformly and circumferentially.
6. thickener according to claim 1, it is characterised in that the feeding mouth of the rotational flow feeding device (7) (701) quantity is 2~4.
7. thickener according to claim 6, it is characterised in that the feeding mouth of the rotational flow feeding device (7) (701) it is distributed uniformly and circumferentially.
8. thickener according to claim 1, it is characterised in that the rotational flow feeding device (7) is fixed by support (9) In the pond body (1).
9. thickener according to claim 1, it is characterised in that the top edge of the pond body (1) is provided with overflow launder (101)。
10. thickener according to claim 1, it is characterised in that the harrow frame (4) by pulley (5) rolling support in On the pond body (1).
CN201720147165.0U 2017-02-17 2017-02-17 A kind of thickener Expired - Fee Related CN206463550U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720147165.0U CN206463550U (en) 2017-02-17 2017-02-17 A kind of thickener

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Application Number Priority Date Filing Date Title
CN201720147165.0U CN206463550U (en) 2017-02-17 2017-02-17 A kind of thickener

Publications (1)

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CN206463550U true CN206463550U (en) 2017-09-05

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107961568A (en) * 2017-11-30 2018-04-27 重庆市沃利克环保设备有限公司 A kind of lifting center drive mud-scraper
CN113786651A (en) * 2021-08-23 2021-12-14 淮北市中芬矿山机器有限责任公司 Efficient flow stabilizing barrel with flow guide mechanism and working method thereof

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107961568A (en) * 2017-11-30 2018-04-27 重庆市沃利克环保设备有限公司 A kind of lifting center drive mud-scraper
CN107961568B (en) * 2017-11-30 2024-01-19 重庆市沃利克环保设备有限公司 Center transmission mud scraper
CN113786651A (en) * 2021-08-23 2021-12-14 淮北市中芬矿山机器有限责任公司 Efficient flow stabilizing barrel with flow guide mechanism and working method thereof

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GR01 Patent grant
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CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20170905

Termination date: 20190217

CF01 Termination of patent right due to non-payment of annual fee