CN208561709U - Beryllium oxide New Type of Separator - Google Patents
Beryllium oxide New Type of Separator Download PDFInfo
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- CN208561709U CN208561709U CN201821047792.8U CN201821047792U CN208561709U CN 208561709 U CN208561709 U CN 208561709U CN 201821047792 U CN201821047792 U CN 201821047792U CN 208561709 U CN208561709 U CN 208561709U
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Abstract
The utility model discloses a kind of beryllium oxide New Type of Separator, including raw material reactor tank, separating barrel and two siphon pipes, raw material reactor tank two sides are provided with support column, raw material reactor tank is rotatably arranged between two support columns, and the side of raw material reactor tank rotation direction is provided with secondary sampler, the first microfiltration tube is installed in the raw material reactor tank, first microfiltration tube bottom and top seal, and first is provided with the second microfiltration tube in microfiltration tube, second microfiltration tube sealed bottom, the siphon pipe has two, a piece siphon pipe is connected between the first microfiltration tube and separating barrel, another siphon pipe is connected between the second microfiltration tube and separating barrel.The mixed solution of reaction is sucked into screen pipe by the utility model using siphon principle, can filter the precipitating of different-grain diameter to separating barrel, and the separating technology is simple and at low cost, and is not in clogging in deslagging.
Description
Technical field
The utility model relates to beryllium oxide production equipment technologies, and in particular to a kind of beryllium oxide New Type of Separator.
Background technique
Sulfuric acid process is one of widely applied method in current beryllium oxide or beryllium hydroxide production, and principle is to utilize prebake
The structure and crystal form for destroying beryl are burnt, then uses sulfuric acid solution berryllium mineral, the acid soluble metals such as beryllium, aluminium, iron is made to enter solution
Phase, with the gangue minerals initial gross separation such as silicon, then solution containing beryllium is purified, is cleaned, and finally obtains qualified beryllium oxide or hydrogen
Beryllium oxide product.
Since a large amount of precipitating can be generated in the production technology, need to separate beryllium hydroxide from mixed precipitation,
Traditional separation method is that ammonium hydroxide is added to separate the impurity such as iron, and re-evaporation crystallizes out aluminium impurity, the separate process steps
It is various and complicated, considerably increase production cost.In addition, all leakage fluid dram or slag-drip opening can be arranged in bottom in most of reactor tanks,
Since solid reactant is more, when bottom deslagging, is often caused blockages, to influence residue collection work.
Summary of the invention
The purpose of this utility model is to provide a kind of beryllium oxide New Type of Separator, which will be anti-using siphon principle
The mixed solution answered is sucked into screen pipe, can filter the precipitating of different-grain diameter to the different holding region of separating barrel, should
Separating technology is simple and at low cost, and is not in clogging in deslagging.
The purpose of this utility model is achieved through the following technical solutions: beryllium oxide New Type of Separator, including raw material are anti-
Tank and separating barrel are answered, at least one siphon pipe is connected between raw material reactor tank and separating barrel, is set at the top of the raw material reactor tank
It is equipped with feed pipe and exhaust pipe, raw material reactor tank lower part is provided with drain pipe, is mounted on control valve on exhaust pipe and drain pipe,
Raw material reactor tank two sides are provided with support column, and raw material reactor tank is rotatably arranged between two support columns, and former
The side of material reactor tank rotation direction is provided with secondary sampler, and secondary sampler includes lifting cylinder, trapezoid block and cross bar, institute
It states trapezoid block to be fixed on the outer wall of raw material reactor tank, slideway is provided on trapezoid block, the lifting cylinder is located at trapezoid block one
Side, the cross bar are fixed on the end of lifting cylinder piston rod, and cross bar is equipped with and slideway cooperation close to one end of trapezoid block
Idler wheel is equipped with the first microfiltration tube in the raw material reactor tank, and the first microfiltration tube bottom and top seal, and
The second microfiltration tube, the second microfiltration tube sealed bottom, the top of the second microfiltration tube are provided in one microfiltration tube
Portion stretches out the top surface of the first microfiltration tube and is connected with air blowing packet, blows and is equipped with electromagnetism between packet and the second microfiltration tube
Pulse valve, the siphon pipe have two, wherein a siphon pipe is connected between the first microfiltration tube and separating barrel, Ling Yigen
Siphon pipe is connected between the second microfiltration tube extension end and separating barrel, and partition is provided in the separating barrel, and partition will divide
Two holding regions are divided into from barrel cavity, are communicated at the top of two holding regions, two siphon pipes, which are respectively protruding into two, to be held
In region.
Further, the separating barrel side is provided with air intake duct, is equipped with aspiration pump on air intake duct.
Further, the inner cavity top of the raw material reactor tank is fixed with protective shell, the air blowing packet and electromagnetic impulse valve
In protective shell, anti-corrosion pipe is connected between the delivery outlet of electromagnetic impulse valve and the second microfiltration tube top.
Further, the siphon pipe is made of ethylene propylene diene monomer (EPDM) material.
The utility model has the beneficial effect that
It 1, will be in raw material reactor tank using siphon principle by the first microfiltration tube of setting and the second microfiltration tube
Mixed solution is sucked into separating barrel, and the pore size filter of the first microfiltration tube is greater than the pore size filter of the second microfiltration tube,
The precipitating of different-grain diameter can be filtered to the different holding region of separating barrel, to realize precipitating point using simple technique
From；
2, by setting secondary sampler, lifting cylinder is controlled to push raw material reactor tank to rotate, the mixed solution in tank
It can slowly be flowed out by the drain pipe of tank body lower part, can avoid causing blockages；
3, by setting aspiration pump, it can will be evacuated to negative pressure in device, to improve the filter efficiency of mixed solution.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model；
Fig. 2 is the schematic diagram of internal structure of the utility model.
Marked in the figure: 1- raw material reactor tank；2- support column；3- secondary sampler；4- drain pipe；5- exhaust pipe；6- first
Microfiltration tube；The second microfiltration tube of 7-；8- protective shell；9- electromagnetic impulse valve；The first siphon pipe of 10-；The second siphon of 11-
Pipe；12- strut；13- control valve；14-, which blows, to be wrapped；15- trapezoid block；16- slideway；17- separating barrel；18- partition；19- air intake duct；
20- aspiration pump；21- feed pipe；31- lifting cylinder；32- cross bar；33- idler wheel.
Specific embodiment
As depicted in figs. 1 and 2, beryllium oxide New Type of Separator provided in this embodiment include upper raw material reactor tank 1,
Under separating barrel 17 and the first siphon pipe 10 and the second siphon pipe 11 that are connected between raw material reactor tank 1 and separating barrel 17,
The top of the raw material reactor tank 1 is provided with feed pipe 21 and exhaust pipe 5, and the lower part of raw material reactor tank 1 is provided with drain pipe
4, control valve 13 is mounted on the exhaust pipe 5 and drain pipe 4.The two sides of the reaction raw materials tank 1 are respectively provided with support column 2,
Reaction raw materials tank 1 is rotatably arranged between two support columns 2 by strut 12, and the one of 1 rotation direction of raw material reactor tank
Side is provided with secondary sampler 3, and secondary sampler 3 includes lifting cylinder 31, trapezoid block 15 and cross bar 32, and trapezoid block 15 is fixed on
On the outer wall of raw material reactor tank 1, in the present embodiment, the longitudinal section of trapezoid block 15 is right-angled trapezium, and the bottom surface of trapezoid block 15
Downward, the drain pipe 4 is located at the underface of trapezoid block 15, is provided with slideway 16 on the inclined-plane of trapezoid block 15.The lifting oil
Cylinder 31 is located at 15 side of trapezoid block, and the cross bar 32 is fixed on the end of 31 piston rod of lifting cylinder, and cross bar 32 is close to trapezoidal
One end of block 15 is provided with idler wheel 33, and idler wheel 33 is slidably matched with slideway 16, and by controlling lifting cylinder 31, idler wheel 33 is in slideway
It is rolled on 16, to drive raw material reactor tank 1 in the rotation in surface of lifting cylinder 31, when lifting cylinder 31 drops to certain journey
When spending, the mixed solution in raw material reactor tank 1 can be flowed out along drain pipe 4, can avoid the phenomenon that drain pipe 4 blocks, together
When raw material reactor tank 1 rotation amplitude it is bigger, the flow rate of mixed solution is faster.
First microfiltration tube 6 and the second microfiltration tube 7, the first micro porous filtration are installed in the raw material reactor tank 1
The filter opening diameter of pipe 6 is 300~600um, and the filter opening diameter of the second microfiltration tube 7 is 70~200um, and mixed precipitation is through first
Microfiltration tube 6 is filtered through the second microfiltration tube 7 again after filtering, according to the size of partial size can by beryllium hydroxide and ferric sulfate and
The filtering of the precipitation and separations such as aluminium hydroxide.First microfiltration tube 6 is fixed on vertically on the bottom surface in raw material reactor tank 1,
And first the bottom and top of microfiltration tube 6 seal, the sealed bottom of second microfiltration tube 7, the second micropore mistake
Chimney filter 7 is inserted into the first microfiltration tube 6, and the top surface of the first microfiltration tube 6 is stretched out on the top of the second microfiltration tube 7
And chain is connected to air blowing packet 14, the top surface of the first microfiltration tube 6 is provided with sealing ring 12 to improve airtightness, the air blowing packet 14
Electromagnetic impulse valve 9 is installed between the second microfiltration tube 7, the delivery outlet of electromagnetic impulse valve 9 and the second microfiltration tube 7
It is connected between top by anti-corrosion pipe, when the first microfiltration tube 6 and 7 adsorption of the second microfiltration tube have a large amount of filter cakes
When, electromagnetic impulse valve 9 is opened, gas is blown into the first microfiltration tube 6 and the second microfiltration tube 7 in the packet 14 that will blow,
And the filter cake on its surface is blown off.Protective shell 8, the air blowing packet 14 and electricity are fixed at the top of 1 inner cavity of raw material reactor tank
Magnetic field impulse valve 9 is located in protective shell 8.
First siphon pipe 10 is all made of ethylene propylene diene rubber just to make with the second siphon pipe 11, not only has soft
Property, also there is preferable antiseptic property.Second siphon pipe 11 is connected between the first microfiltration tube 6 and separating barrel 17, and first
Siphon pipe 10 is connected between the second microfiltration tube 7 and separating barrel 17, is filled in the first siphon pipe 10 and the second siphon pipe 11
Reaction solution filters the reaction solution of raw material reactor tank 1 to separating barrel 17 using siphon principle.In the separating barrel 17
It is provided with partition 18,17 inner cavity of separating barrel is divided into two holding regions, communicated at the top of two holding regions, first by partition 18
Siphon pipe 10 and the second siphon pipe 11 are respectively protruding into two holding regions, and the side of separating barrel 17 is provided with air intake duct 19,
Aspiration pump 20 is installed on air intake duct 19, by controlling the sucking rate of aspiration pump 20, the filtering rate of reaction solution is adjusted.
The above is only the utility model preferred embodiment, but the protection scope of the utility model is not limited to
This, any transformation carried out based on technical solution provided by the utility model and inventive concept and replacement should all be covered in this reality
With in novel protection scope.
Claims (4)
1. beryllium oxide New Type of Separator, including raw material reactor tank and separating barrel, be connected between raw material reactor tank and separating barrel to
A few siphon pipe, it is characterised in that: be provided with feed pipe and exhaust pipe, raw material reactor tank lower part at the top of the raw material reactor tank
It is provided with drain pipe, control valve is mounted on exhaust pipe and drain pipe, raw material reactor tank two sides are provided with support column,
Raw material reactor tank is rotatably arranged between two support columns, and the side of raw material reactor tank rotation direction is provided with auxiliary and takes
Sample device, secondary sampler include lifting cylinder, trapezoid block and cross bar, and the trapezoid block is fixed on the outer wall of raw material reactor tank,
Slideway is provided on trapezoid block, the lifting cylinder is located at trapezoid block side, and the cross bar is fixed on lifting cylinder piston rod
End, cross bar are equipped with the idler wheel with slideway cooperation close to one end of trapezoid block, and it is micro- to be equipped with first in the raw material reactor tank
Hole screen pipe, the first microfiltration tube bottom and top seal, and the second micro porous filtration is provided in the first microfiltration tube
Top surface and the connection of the first microfiltration tube are stretched out in the top of pipe, the second microfiltration tube sealed bottom, the second microfiltration tube
There is air blowing to wrap, blows and electromagnetic impulse valve is installed between packet and the second microfiltration tube, the siphon pipe there are two, wherein one
Siphon pipe is connected between the first microfiltration tube and separating barrel, and another siphon pipe is connected to the second microfiltration tube extension end
Between separating barrel, partition is provided in the separating barrel, partition will separate barrel cavity and be divided into two holding regions, two Shengs
It puts and is communicated at the top of region, two siphon pipes are respectively protruding into two holding regions.
2. beryllium oxide New Type of Separator according to claim 1, it is characterised in that: the separating barrel side is provided with air-breathing
It manages, aspiration pump is installed on air intake duct.
3. beryllium oxide New Type of Separator according to claim 1, it is characterised in that: the inner cavity top of the raw material reactor tank
It is fixed with protective shell, the air blowing packet and electromagnetic impulse valve are located in protective shell, the delivery outlet of electromagnetic impulse valve and the second micropore
Screen pipe is connected with anti-corrosion pipe between top.
4. beryllium oxide New Type of Separator according to claim 1, it is characterised in that: the siphon pipe uses ethylene-propylene-diene monomer
Glue material production.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821047792.8U CN208561709U (en) | 2018-07-04 | 2018-07-04 | Beryllium oxide New Type of Separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821047792.8U CN208561709U (en) | 2018-07-04 | 2018-07-04 | Beryllium oxide New Type of Separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN208561709U true CN208561709U (en) | 2019-03-01 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821047792.8U Active CN208561709U (en) | 2018-07-04 | 2018-07-04 | Beryllium oxide New Type of Separator |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111467873A (en) * | 2020-05-26 | 2020-07-31 | 唐山三友硅业有限责任公司 | Methylsiloxane dewatering and impurity removing process and device |
-
2018
- 2018-07-04 CN CN201821047792.8U patent/CN208561709U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111467873A (en) * | 2020-05-26 | 2020-07-31 | 唐山三友硅业有限责任公司 | Methylsiloxane dewatering and impurity removing process and device |
| CN111467873B (en) * | 2020-05-26 | 2024-05-24 | 唐山三友硅业股份有限公司 | Methyl siloxane dehydration and impurity removal process and equipment |
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