CN105080737A - Three-product dense medium cyclone - Google Patents
Three-product dense medium cyclone Download PDFInfo
- Publication number
- CN105080737A CN105080737A CN201510647520.6A CN201510647520A CN105080737A CN 105080737 A CN105080737 A CN 105080737A CN 201510647520 A CN201510647520 A CN 201510647520A CN 105080737 A CN105080737 A CN 105080737A
- Authority
- CN
- China
- Prior art keywords
- section
- cyclone
- cone
- truncated cone
- sections
- 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.)
- Pending
Links
Landscapes
- Cyclones (AREA)
Abstract
A three-product dense medium cyclone comprises a one-section circular truncated cone cyclone and a two-section cone cyclone, wherein a heavy medium suspension liquid inlet and a tailing outlet are formed in one end of the one-section circular truncated cone cyclone, and a raw ore feed port is formed in the other end; an ore concentrate outlet is formed in one end of the two-section cone cyclone, and a middling outlet is formed in the other end; the one-section circular truncated cone cyclone and the one-section circular truncated cone cyclone are mounted in an involute manner; the two-section cone cyclone adopts a bipyramidal cyclone and comprises a small-cone-angle pyramid section and a large-cone-angle pyramid section which are connected to form an integrated structure through a flange. The cyclone is simple in production process, low in production cost and long in equipment service life, causes little environmental pollution, and the ore concentrate product has a high grade.
Description
Technical field
The present invention relates to a kind of ore dressing three products heavy medium cyclone, specifically a kind of realization applies the cyclone that low-density heavy-media suspension carrys out sorting high density non magnetic ore, belongs to sorting technology field.
Background technology
Three products heavy medium cyclone coal preparation technique and equipment is high with its sharpness of separation, structure simply, easily realizes the advantages such as Automated condtrol, becomes first-selected technique and the equipment of newly-built coal preparation plant of current China and the technological transformation of old factory.
Since 20 century 70s, heavy medium cyclone is developed rapidly in China.Particularly since the nineties, newly-built coal preparation plant and the old factory of the difficult choosing of nearly all raw coal genus all adopt three products heavy medium cyclone as main equipment, and the coal preparation plant that this technique and equipment belong to medium or more difficult choosing at some raw coal is also adopted.
Typical example is that Chinese patent application 02158903.8 discloses " a kind of heavy medium cyclone device, Recognition Applied in Coal Preparation System and coal preparation method ", the simplified heavy medium matter coal preparation technique of this to be a kind of large-scale pressureless fed three-product dense-medium cyclone be main equipment.This kind of heavy medium cyclone is composed in series by cylindrical cyclone and the conical cyclone of cylinder, and one section is cylindrical cyclone, and two sections is the conical cyclone of cylinder, and cone angle is 20 °.
The above-mentioned three products heavy medium cyclone adopted in coal production, sub-elects two kinds of products in a cylindrical section type cyclone, and provides high density suspensions for two cylindrical section pyramid type cyclones.But in actual production, because heavy-media suspension density used is many at 1.8 ㎏/below L, the density of suspending liquid after a cylindrical section type cyclone concentrates improves limited, and for two cylindrical section pyramid type cyclones, owing to adopting one section of cone, also limited to the concentrated effect of suspension; This three products heavy medium cyclone can not carry out effective sorting by the non magnetic ore high to separating density, and practical effect is poor, affects the efficiency of separation and quality.
Summary of the invention
Technical problem to be solved by this invention is to provide the three products heavy medium cyclone that a kind of non magnetic ore high to separating density can carry out effective sorting.
The technical scheme realizing above-mentioned purpose employing is: a kind of three products heavy medium cyclone, comprise the one section of truncated cone-shaped cyclone and two sections of conical cyclones that are connected in series, wherein one section of truncated cone-shaped cyclone one end is provided with heavy-media suspension entrance and mine tailing outlet, and the other end is provided with raw ore feeding mouth; One end of two sections of conical cyclones is provided with concentrate outlet, and the other end is provided with chats outlet; One section of truncated cone-shaped cyclone is connected by connecting pipe with between two sections of conical cyclones,
Installation form between described one section of truncated cone-shaped cyclone and heavy-media suspension entrance is involute mode;
Described two sections of conical cyclones are bicone cyclone, and it comprises the slender cone section of leading portion and the big-taper-angle taper body section of back segment, and it is into a single integrated structure that slender cone section and big-taper-angle taper body section pass through Flange joint;
The big-taper-angle taper body section of described one section of truncated cone-shaped cyclone and two sections of conical cyclones is connected with all adopting involute mode between connecting pipe.
Compared with prior art, the present invention can carry out sorting to high density mineral effectively, is specially adapted to the mineral that separating density is greater than 2.4 ㎏/L, is a kind of gravity beneficiation equipment that can realize high density sorting; In addition, this cyclone production technology disclosed in this invention is simple, production cost is low, service life of equipment is long, environmental pollution is little, gained concentrate product grade is high.
Preferably: the cone angle of one section of truncated cone-shaped cyclone is 0 ° ~ 20 °.
Preferably: two sections of conical cyclones, the tapering of its slender cone section is 0 ° ~ 20 °, and the tapering of its big-taper-angle taper body section is 20 ° ~ 180 °.
Preferably: connecting pipe is integral by Flange joint by multistage arc pipe.
Accompanying drawing explanation
Fig. 1 is the overall structure schematic diagram of type of the present invention.
Fig. 2 is that the A of New type cyclone is to schematic diagram.
Fig. 3 is that the B of New type cyclone is to schematic diagram.
Fig. 4 is that the C of New type cyclone is to schematic diagram.
In figure: heavy-media suspension entrance 1, one section of truncated cone-shaped cyclone 2, raw ore feeding mouth 3, two sections of cone cyclones 4, concentrate outlet 5, chats outlet 6, mine tailing outlet 7, connecting pipe 8.
Detailed description of the invention
Below in conjunction with drawings and Examples, the present invention will be further described.
See accompanying drawing 1-4, this three products heavy medium cyclone disclosed in this invention, comprises heavy-media suspension entrance 1, one section of truncated cone-shaped cyclone 2, raw ore feeding mouth 3, two sections of cone cyclones 4, concentrate outlet 5, chats outlet 6, mine tailing outlet 7, connecting pipe 8.
One section of truncated cone-shaped cyclone and two sections of conical cyclones are connected in series, and wherein one section of truncated cone-shaped cyclone one end is provided with heavy-media suspension entrance and mine tailing outlet, and the other end is provided with raw ore feeding mouth; One end of two sections of conical cyclones is provided with concentrate outlet, and the other end is provided with chats outlet.Installation form between one section of truncated cone-shaped cyclone and heavy-media suspension entrance is involute mode, as shown in Figure 2, heavy-media suspension entrance is arranged on the side of one section of truncated cone-shaped cyclone, its suspension pan feeding pipeline is arc shape pipeline, adopt involute mode to install setting between itself and one section of truncated cone-shaped cyclone, the cone angle of one section of truncated cone-shaped cyclone is defined between 0-20 degree.Tangent line pan feeding is had to change involute pan feeding into the enter material way of one section of feed cylindrical cyclone, rounder and more smooth relative to tangent line pan feeding, decrease turbulent phenomenon, thus the impact wear reduced medium inlet, also in a disguised form increase the volume of one section of circular platform type cyclone, angle of taper becomes 0 ° ~ 20 ° truncated cone-shaped cyclones, like this can when ensureing to enter two sections of cyclone overbottom pressure, improve the concentrated effect of cyclone one section, the density of suspending liquid entering two sections of cyclones is improved relatively.
Two sections of conical cyclones are bicone cyclone, and it comprises the slender cone section of leading portion and the big-taper-angle taper body section of back segment, and it is into a single integrated structure that slender cone section and big-taper-angle taper body section pass through Flange joint; The tapering of its slender cone section is between 0-20 degree, and the tapering of its big-taper-angle taper body section is between 20-180.Conical for two cylindrical sections cyclone is become two sections of bicone structures, and upper end conical section cone angle is 0 ° ~ 20 °, and lower end conical section is the large cone angle of 20 ° ~ 180 °.Due to adopt double tapered angle, be enter two sections suspension inspissation strengthen, substantially increase the separating density of two sections of cyclones, thus realize effective sorting of high density mineral.Also change involute by one section into the connected mode of two sections to be connected simultaneously, can be that the mixture of a section of remaining suspension, chats and concentrate enters two sections with rounder and more smooth form like this, realize two sections of sortings in advance, reduce the wearing and tearing to tube connector.
As shown in Figure 1: density is that in 1.8 ㎏/L ~ 2.4 ㎏/L heavy-media suspensions, low-density suspension is fed with involute in form with the edge of certain speed by truncated cone-shaped cyclone by heavy-media suspension entrance, and the non magnetic ore of high density is directly fed by gravity by raw ore feeding mouth.Ore, after one section of truncated cone-shaped cyclone and the sorting of two sections of cone cyclones, can realize the high density sorting of 2.4 ㎏/L ~ 3.2 ㎏/L, and the high density chats product obtained is exported by chats and discharges, and concentrate product is exported by concentrate and discharges.The concentrate of discharging, chats and mine tailing carry out the dehydration of product and the recycling of dense media by the method for dehydration and dielectric film filter.Each angle in the present invention includes two endpoint value.
As shown in Figure 2: the entrance of one section of circular platform type cyclone heavy-media suspension adopts the entry mode of involute, rounder and more smooth relative to tangent line pan feeding, decrease turbulent phenomenon, thus the impact wear reduced medium inlet, also in a disguised form increase the volume of one section of circular platform type cyclone, improve the disposal ability of equipment.
The big-taper-angle taper body section of one section of truncated cone-shaped cyclone and two sections of conical cyclones, all adopts involute mode to be connected between they with connecting pipe.Connecting pipe is integral by Flange joint by multistage arc pipe.
As shown in Figures 3 and 4: the connecting pipe of a section and two sections, adopting the pipeline of involute mode to connect, can be that material enters Pre-sorting before two sections of prerequisites, keep laminar stable, reduce the wearing and tearing to tube connector, increase the volume of two sections of bicone cyclones, improve the disposal ability of equipment.
Claims (4)
1. a three products heavy medium cyclone, comprises the one section of truncated cone-shaped cyclone and two sections of conical cyclones that are connected in series, and wherein one section of truncated cone-shaped cyclone one end is provided with heavy-media suspension entrance and mine tailing outlet, and the other end is provided with raw ore feeding mouth; One end of two sections of conical cyclones is provided with concentrate outlet, and the other end is provided with chats outlet; One section of truncated cone-shaped cyclone is connected by connecting pipe with between two sections of conical cyclones, it is characterized in that:
Installation form between described one section of truncated cone-shaped cyclone and heavy-media suspension entrance is involute mode;
Described two sections of conical cyclones are bicone cyclone, and it comprises the slender cone section of leading portion and the big-taper-angle taper body section of back segment, and it is into a single integrated structure that slender cone section and big-taper-angle taper body section pass through Flange joint;
The big-taper-angle taper body section of described one section of truncated cone-shaped cyclone and two sections of conical cyclones is connected with all adopting involute mode between connecting pipe.
2. three products heavy medium cyclone according to claim 1, is characterized in that, the cone angle of one section of described truncated cone-shaped cyclone is 0 ° ~ 20 °.
3. three products heavy medium cyclone according to claim 1, is characterized in that, two sections of described conical cyclones, and the tapering of its slender cone section is 0 ° ~ 20 °, and the tapering of its big-taper-angle taper body section is 20 ° ~ 180 °.
4. three products heavy medium cyclone according to claim 1, is characterized in that, described connecting pipe is integral by Flange joint by multistage arc pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510647520.6A CN105080737A (en) | 2015-10-09 | 2015-10-09 | Three-product dense medium cyclone |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201510647520.6A CN105080737A (en) | 2015-10-09 | 2015-10-09 | Three-product dense medium cyclone |
Publications (1)
Publication Number | Publication Date |
---|---|
CN105080737A true CN105080737A (en) | 2015-11-25 |
Family
ID=54562597
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201510647520.6A Pending CN105080737A (en) | 2015-10-09 | 2015-10-09 | Three-product dense medium cyclone |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN105080737A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112058479A (en) * | 2020-09-03 | 2020-12-11 | 中国矿业大学 | Two-section separation density regulating device and method for three-product heavy medium cyclone |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999022873A1 (en) * | 1997-11-04 | 1999-05-14 | B.H.R. Group Limited | Cyclone separator |
CN1418734A (en) * | 2002-12-26 | 2003-05-21 | 天地科技股份有限公司唐山分公司 | Heavy medium vortrap, coal separation system and method therefor |
CN201871429U (en) * | 2010-11-30 | 2011-06-22 | 三一重型装备有限公司 | Three-product heavy-medium swirler |
CN102764706A (en) * | 2011-05-06 | 2012-11-07 | 韦善兵 | Unpressurized feeding three-product dense medium cyclone for high-density separation |
CN203750714U (en) * | 2014-04-11 | 2014-08-06 | 中煤科工集团唐山研究院有限公司 | Three-product dense medium cyclone capable of carrying out online adjustment on two-stage separation density |
CN205074113U (en) * | 2015-10-09 | 2016-03-09 | 北京柯林柯矿业科技有限公司 | Three -product dense medium cyclone |
-
2015
- 2015-10-09 CN CN201510647520.6A patent/CN105080737A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO1999022873A1 (en) * | 1997-11-04 | 1999-05-14 | B.H.R. Group Limited | Cyclone separator |
CN1418734A (en) * | 2002-12-26 | 2003-05-21 | 天地科技股份有限公司唐山分公司 | Heavy medium vortrap, coal separation system and method therefor |
CN201871429U (en) * | 2010-11-30 | 2011-06-22 | 三一重型装备有限公司 | Three-product heavy-medium swirler |
CN102764706A (en) * | 2011-05-06 | 2012-11-07 | 韦善兵 | Unpressurized feeding three-product dense medium cyclone for high-density separation |
CN203750714U (en) * | 2014-04-11 | 2014-08-06 | 中煤科工集团唐山研究院有限公司 | Three-product dense medium cyclone capable of carrying out online adjustment on two-stage separation density |
CN205074113U (en) * | 2015-10-09 | 2016-03-09 | 北京柯林柯矿业科技有限公司 | Three -product dense medium cyclone |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112058479A (en) * | 2020-09-03 | 2020-12-11 | 中国矿业大学 | Two-section separation density regulating device and method for three-product heavy medium cyclone |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN202778747U (en) | Classifying cyclone | |
CN205074113U (en) | Three -product dense medium cyclone | |
CN105080737A (en) | Three-product dense medium cyclone | |
CN206286078U (en) | One kind has pressure three products heavy medium cyclone | |
CN205095977U (en) | Kaolinic sorting facilities of sulphur coal and coal measures | |
CN203916930U (en) | The hydrocyclone of embedded with conical screen cloth | |
CN206965950U (en) | A kind of concentration-type cyclone | |
CN202667016U (en) | Hydrocyclone | |
CN102764706A (en) | Unpressurized feeding three-product dense medium cyclone for high-density separation | |
CN103736602A (en) | High-density separation pressure dual-product heavy-medium cyclone | |
CN210304163U (en) | Three-product cyclone | |
CN204261806U (en) | The ore-dressing plant of a kind of natural rutile or zircon sand | |
CN202180009U (en) | Pressurized feeding three-product heavy-medium cyclone | |
CN203664038U (en) | High density separation pressurized two-product heavy medium cyclone | |
CN203648738U (en) | Two-stage high-density separation three-product swirler | |
CN206444756U (en) | Without pressure fluorite coarse fraction ore deposit sorting cyclone pipe | |
CN201552070U (en) | Concentric swirler | |
CN202199445U (en) | Double media feeding non-pressure feeding cyclone for separation at high density | |
CN201596576U (en) | High efficiency energy saving three-product heavy medium cyclone | |
CN206444755U (en) | There is pressure fluorite coarse fraction ore deposit cyclone separator | |
CN202129155U (en) | Pressurized feeding type three-product dense medium cyclone for realizing high density seperation | |
CN102764705A (en) | Pressure feeding three-product dense medium cyclone for high-density sorting | |
CN103418506A (en) | Dense medium vortex system for high density separation | |
CN202577028U (en) | Waste paper pulp impurity separating device | |
CN201524618U (en) | High-density sorting triadic product heavy medium cyclone with pressure |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20151125 |
|
RJ01 | Rejection of invention patent application after publication |