CN203184123U - Kaolin cyclone separation device - Google Patents
Kaolin cyclone separation device Download PDFInfo
- Publication number
- CN203184123U CN203184123U CN 201320195246 CN201320195246U CN203184123U CN 203184123 U CN203184123 U CN 203184123U CN 201320195246 CN201320195246 CN 201320195246 CN 201320195246 U CN201320195246 U CN 201320195246U CN 203184123 U CN203184123 U CN 203184123U
- Authority
- CN
- China
- Prior art keywords
- pipe
- cylinder section
- kaolin
- long
- separation device
- 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 - Lifetime
Links
- 239000005995 Aluminium silicate Substances 0.000 title claims abstract description 20
- 235000012211 aluminium silicate Nutrition 0.000 title claims abstract description 20
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 title claims abstract description 20
- 238000000926 separation method Methods 0.000 title claims abstract description 19
- 239000007788 liquid Substances 0.000 claims abstract description 12
- 238000009434 installation Methods 0.000 claims description 3
- 230000000694 effects Effects 0.000 abstract description 6
- 239000002734 clay mineral Substances 0.000 abstract description 3
- 238000003754 machining Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 description 5
- 239000007787 solid Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 2
- 238000004061 bleaching Methods 0.000 description 2
- 239000003814 drug Substances 0.000 description 2
- 238000007885 magnetic separation Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000000047 product Substances 0.000 description 2
- 239000013049 sediment Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000010433 feldspar Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 238000005188 flotation Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 229910001608 iron mineral Inorganic materials 0.000 description 1
- 238000005272 metallurgy Methods 0.000 description 1
- 239000010445 mica Substances 0.000 description 1
- 229910052618 mica group Inorganic materials 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- -1 papermaking Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 229910001773 titanium mineral Inorganic materials 0.000 description 1
- 238000011282 treatment Methods 0.000 description 1
Images
Abstract
The utility model provides a kaolin cyclone separation device and relates to kaolin machining equipment. The utility model provides a high-pressure type kaolin cyclone separation device which can efficiently separate clay minerals and organic matters in kaolin. The kaolin cyclone separation device is provided with a cyclone cylinder section, a tangential feeding pipe, a cone section, a bottom flowing pipe, a long overflowing pipe and an overflowing groove; the cyclone cylinder section is arranged above the cone section and is connected with a large bottom of the cone section; the bottom flow pipe is arranged below the cone section and is connected with a small bottom of the cone section; the tangential feeding pipe is arranged at the upper part of the cyclone cylinder section and enables a feeding direction to be tangential to the circumference of the cylinder section; the long overflowing pipe and the cyclone cylinder section are coaxially mounted and the long overflowing pipe stretches into 1/3 length of the cyclone cylinder section; and the overflowing groove is mounted on the top of the long overflowing pipe and is used for accepting overflowing liquid. Through a test, the solid-liquid separation effect is very obvious along the increasing of inlet pressure of a hydrocyclone or a centrifuge.
Description
Technical field
The utility model relates to the kaolin process equipment, especially relates to the kaolin cyclone separation device.
Background technology
Kaolin is metallurgy, light industry, chemical industry, raise a mouthful stemming, auxiliary material or the functional material of the primary raw material of pottery and plastics, rubber, papermaking, coating, daily-use chemical industry, also can be used for producing aluminum sulfate, aluminium chloride, sial white carbon etc.
In order to separate non-clay mineral and organic matters such as quartz in the kaolin, feldspar, mica, iron mineral, titanium mineral, produce the kaolin product that can satisfy each industrial circle demand, except adopting gravity treatment, flotation, magnetic separation etc. that kaolin is purified the removal of impurities, also to adopt chemical bleaching sometimes, ultra-finely delaminate, deep working methods such as calcining, surface modification handle kaolin.Kaolinic ore dressing processing is divided into dry method and two kinds of technologies of wet method.Wet method processing technology is generally with behind the crushing raw ore, through smashing slurry, desanding, cyclone classification, delaminate, centrifuge classification, magnetic separation (or bleaching), concentrate, press filtration, dry getting final product, the product that obtains like this can be used for pottery or papermaking paint.Cyclone classification and centrifuge classification are the kaolinic master operations of wet separation.
Summary of the invention
The purpose of this utility model is to provide a kind of non-clay mineral and organic high-pressure type kaolin cyclone separation device that can efficiently separate in the kaolin.
The utility model is provided with whirl cylinder section, tangential feed pipe, cone segments, underflow pipe, long overflow pipe and overflow launder; Described whirl cylinder section is located at the top of cone segments and is connected with the big end of cone segments; Underflow pipe is located at the below of cone segments and is connected with the handle of cone segments; Tangential feed pipe is located at the top of whirl cylinder section and is made feedstock direction tangent with tube section circumference; Long overflow pipe puts in 1/3rd length of whirl cylinder section with the coaxial installation of whirl cylinder section, long overflow pipe; Overflow launder is installed in the top of long overflow pipe, is used for accepting overflow liquid.
The length of described long overflow pipe can be more than 3 times of whirl cylinder section.The water column of long overflow pipe can improve the intake pressure of feed pipe, and can stablize intake pressure.
The internal diameter of described long overflow pipe can be identical with the internal diameter of underflow pipe, is about 50% of whirl cylinder section internal diameter.
The utlity model has following outstanding advantage:
1, the ore pulp for preparing medicament enters the whirl cylinder section from tangential feed pipe, tangentially enters cylindrical shell, and rotates in cylindrical shell.Utilize centrifugal force field, accelerate the solid particles sediment in the liquid, strengthen and separate, separate the solid in the ore pulp.
2, utilize the pressure of the increase whirl cylinder section of long overflow pipe, keep the high pressure of whirl cylinder section, the tangential feed pipe ore removal is steady, improves solid-liquid separation effect.
3, the long overflow pipe of utilization increases the pressure of whirl cylinder section, improves the inlet pressure of feed pump, and ore pulp is loose shape and enters the whirl cylinder section, so the more big solid-liquid separation effect of pressure is more good.
4, through test, along with the inlet pressure increase of cyclone or centrifuge, solid-liquid separation effect is also remarkable.
Description of drawings
Fig. 1 is that the structure of the utility model embodiment is formed schematic diagram.
Fig. 2 is the A-A generalized section of Fig. 1.
In Fig. 1 and 2, respectively be labeled as: 1 tangential feed pipe, 2 whirl cylinder sections, 3 cone segments, 4 underflow pipes, 5 long overflow pipes, 6 overflow launders.
The specific embodiment
Below in conjunction with accompanying drawing embodiment of the present utility model is further described.
Referring to Fig. 1 and 2, the cyclone separation device of present embodiment is provided with whirl cylinder section 2, tangential feed pipe 1, cone segments 3, underflow pipe 4, long overflow pipe 5 and overflow launder 6.
In the present embodiment, whirl cylinder section 2 is located at the top of cone segments 3 and is connected with the big end of cone segments 3; Underflow pipe 4 is located at the below of cone segments 3 and is connected with the handle of cone segments 3; Tangential feed pipe 1 is located at the top of whirl cylinder section 2 and is made feedstock direction tangent with tube section circumference; Long overflow pipe 5 and the 2 coaxial installations of whirl cylinder section, long overflow pipe 5 puts in 1/3rd length of whirl cylinder section 2; Overflow launder 6 is installed in the top of long overflow pipe 5, is used for accepting overflow liquid.
The length of the long overflow pipe 5 of present embodiment is 3 times of whirl cylinder section 2.The water column of long overflow pipe 5 can improve the intake pressure of feed pipe, and can stablize intake pressure.
The internal diameter of the long overflow pipe 5 of present embodiment is consistent with the internal diameter of underflow pipe 4, and is 50% of whirl cylinder section 2 internal diameters.
In the present embodiment, the ore pulp for preparing medicament enters whirl cylinder section 2 from tangential feed pipe 1, tangentially enters cylindrical shell, and rotates in cylindrical shell.Utilize centrifugal force field, accelerate the solid particles sediment in the liquid, strengthen and separate, separate the solid in the ore pulp.And the pressure of the increase whirl cylinder section 2 of long overflow pipe 5, keep the high pressure of whirl cylinder section 2, guaranteed that tangential feed pipe 1 ore removal is steady, improve solid-liquid separation effect; And utilize long overflow pipe 5 to increase the pressure of whirl cylinder section 2, and the inlet pressure of raising feed pump, ore pulp is loose shape and enters the whirl cylinder section, so the more big solid-liquid separation effect of pressure is more good.
Claims (4)
1. the kaolin cyclone separation device is characterized in that being provided with whirl cylinder section, tangential feed pipe, cone segments, underflow pipe, long overflow pipe and overflow launder; Described whirl cylinder section is located at the top of cone segments and is connected with the big end of cone segments; Underflow pipe is located at the below of cone segments and is connected with the handle of cone segments; Tangential feed pipe is located at the top of whirl cylinder section and is made feedstock direction tangent with tube section circumference; Long overflow pipe puts in 1/3rd length of whirl cylinder section with the coaxial installation of whirl cylinder section, long overflow pipe; Overflow launder is installed in the top of long overflow pipe, is used for accepting overflow liquid.
2. kaolin cyclone separation device according to claim 1, the length that it is characterized in that described long overflow pipe is more than 3 times of whirl cylinder section.
3. kaolin cyclone separation device according to claim 1 is characterized in that the internal diameter of described long overflow pipe is identical with the internal diameter of underflow pipe.
4. as kaolin cyclone separation device as described in claim 1 or 3, the internal diameter that it is characterized in that described long overflow pipe is 50% of whirl cylinder section internal diameter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320195246 CN203184123U (en) | 2013-04-17 | 2013-04-17 | Kaolin cyclone separation device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201320195246 CN203184123U (en) | 2013-04-17 | 2013-04-17 | Kaolin cyclone separation device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203184123U true CN203184123U (en) | 2013-09-11 |
Family
ID=49101023
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201320195246 Expired - Lifetime CN203184123U (en) | 2013-04-17 | 2013-04-17 | Kaolin cyclone separation device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203184123U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108819323A (en) * | 2018-07-31 | 2018-11-16 | 王政 | A kind of screw extruding type solid-liquid separator |
-
2013
- 2013-04-17 CN CN 201320195246 patent/CN203184123U/en not_active Expired - Lifetime
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108819323A (en) * | 2018-07-31 | 2018-11-16 | 王政 | A kind of screw extruding type solid-liquid separator |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN200942363Y (en) | Hydrocyclone | |
| CN103816992A (en) | Coarse slime dense medium sorting technology and system | |
| CN203791036U (en) | Coarse slime dense medium separation system | |
| CN203184123U (en) | Kaolin cyclone separation device | |
| CN202460212U (en) | Settling tank with feeding device | |
| CN102399028A (en) | Technology for treating coal slime water through secondary flow and settlement filtering centrifuge | |
| CN205361690U (en) | Hydraulic classification desliming cylinder for bauxite | |
| CN2782219Y (en) | Hydraulic power separator | |
| CN103357492A (en) | High speed rotating ore separating equipment | |
| CN203609932U (en) | Flow stabilizer for thickener | |
| CN206965950U (en) | A kind of concentration-type cyclone | |
| CN207042655U (en) | A kind of coal slime classification, deslimer | |
| CN109225687A (en) | A kind of hydrocyclone of cone slotting structure | |
| CN205796736U (en) | Ball milling mine tailing directly sieves dewatering system | |
| CN204261797U (en) | Ore dressing high-effective classifying deslimer | |
| CN104174484A (en) | Desiliconization processing method for bauxite flotation tailings | |
| CN204395547U (en) | Rotational-flow high-efficient deep cone thickener | |
| CN107344140A (en) | A kind of coal slime classification, deslimer | |
| CN105709945A (en) | Multifunctional whirlcone | |
| CN101856637A (en) | Hydraulic cyclone deslimer with washing function | |
| CN201249138Y (en) | Hydraulic cyclone classifier | |
| CN202577028U (en) | Waste paper pulp impurity separating device | |
| CN107999288A (en) | A kind of hydrocyclone of new export structure | |
| CN204475038U (en) | A kind of device of paper mill high efficiente callback fiber | |
| CN204981470U (en) | Whirlwind isolating construction of mud -water separation system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Kaolin cyclone separation device Effective date of registration: 20190319 Granted publication date: 20130911 Pledgee: Xiamen finance Company limited by guarantee Pledgor: XIAMEN XINYISHENG NONMETAL MATERIAL SCIENCE & TECHNOLOGY Co.,Ltd. Registration number: 2019990000239 |
|
| CP01 | Change in the name or title of a patent holder | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 361100 No. 681 Xinmin Road, Xinmin Town, Tongan District, Fujian, Xiamen Patentee after: Xiamen xinyisheng New Material Technology Co.,Ltd. Address before: 361100 No. 681 Xinmin Road, Xinmin Town, Tongan District, Fujian, Xiamen Patentee before: XIAMEN XINYISHENG NONMETAL MATERIAL SCIENCE & TECHNOLOGY Co.,Ltd. |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20200422 Granted publication date: 20130911 Pledgee: Xiamen finance Company limited by guarantee Pledgor: Xiamen xinyisheng New Material Technology Co.,Ltd. Registration number: 2019990000239 |
|
| PM01 | Change of the registration of the contract for pledge of patent right |
Change date: 20200422 Registration number: 2019990000239 Pledgor after: Xiamen xinyisheng New Material Technology Co.,Ltd. Pledgor before: XIAMEN XINYISHENG NONMETAL MATERIAL SCIENCE & TECHNOLOGY Co.,Ltd. |
|
| PM01 | Change of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right | ||
| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Kaolin cyclone separation device Effective date of registration: 20200424 Granted publication date: 20130911 Pledgee: Xiamen finance Company limited by guarantee Pledgor: Xiamen xinyisheng New Material Technology Co.,Ltd. Registration number: Y2020990000368 |
|
| PC01 | Cancellation of the registration of the contract for pledge of patent right | ||
| PC01 | Cancellation of the registration of the contract for pledge of patent right |
Date of cancellation: 20210428 Granted publication date: 20130911 Pledgee: Xiamen finance Company limited by guarantee Pledgor: Xiamen xinyisheng New Material Technology Co.,Ltd. Registration number: Y2020990000368 |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130911 |