CN2892283Y - Liquid dregs separator - Google Patents
Liquid dregs separator Download PDFInfo
- Publication number
- CN2892283Y CN2892283Y CN 200620006435 CN200620006435U CN2892283Y CN 2892283 Y CN2892283 Y CN 2892283Y CN 200620006435 CN200620006435 CN 200620006435 CN 200620006435 U CN200620006435 U CN 200620006435U CN 2892283 Y CN2892283 Y CN 2892283Y
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- CN
- China
- Prior art keywords
- cyclone dust
- dust collectors
- dust collector
- liquid
- pump
- 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
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Abstract
The utility model relates to a separation plant, a liquid and dregs separator in particular. The segregator comprises a pump and more than one cyclone dust collector and is characterized in that the cyclone dust collectors are connected in series, namely an outlet of the previous cyclone dust collector is connected with an inlet of the next cyclone dust collector, and the outlet of the last cyclone dust collector is connected with the pump. Discharge hole of each cyclone dust collector is equipped with a discharge seal control valve. By using such this separation plant, liquid and dregs can be quickly separated, and accordingly, production efficiency is improved on one side, worsening of product quality resulting from sand blown by northwester is effectively eliminated on the other hand and accordingly product quality is improved. In addition, in order to keep continuous production run, based on prior equipments, prior structure is simply reconstructed to achieve the purposes of high efficiency and continuous separation of liquid and dregs.
Description
Technical field
The utility model relates to a kind of separation equipment, particularly a kind of melt cinder separator.
Background technology
At present, in the production process of sodium humate, melt cinder separates the common sedimentation basin that adopts and precipitates, and adopt the shortcoming that sedimentation basin precipitates to be: the floor space of sedimentation basin is big on the one hand, makes the input of producing land used bigger; The production efficiency of natural sedimentation is low on the other hand, simultaneously because sedimentation basin is an open type, and sand and dust are easy to enter in the pond, causes product quality to descend, and also environment is caused very big pollution.And adopt the separating effect of existing solid-liquid separating equipment not very good.
Summary of the invention
The purpose of this utility model is to overcome above-mentioned the deficiencies in the prior art, provides a kind of and realizes carrying out continuously the melt cinder separation, and the high melt cinder separator of separative efficiency.
For realizing the purpose of this utility model, the technical scheme that is adopted is: a kind of melt cinder separator, comprise pump and more than one cyclone dust collectors, it is characterized in that being between the cyclone dust collectors series connection, the outlet that is previous cyclone dust collectors links to each other with the import of back cyclone dust collectors, is connected with pump in the exit of back cyclone dust collectors; The discharge seal control valve is installed on the discharge gate of each cyclone dust collectors.
Above-mentioned discharge seal control valve is by forming with the balancing weight that hinged valve plate, the vertical weight linear meter that links with valve plate and the slip of discharge gate is installed on the weight linear meter; The end face of above-mentioned discharge gate and horizontal plane form the angle greater than zero degree.
Characteristics of the present utility model are: 1, can carry out melt cinder fast by this melt cinder separator and separate, improved production efficiency on the one hand, can effectively solve the problem that the northwest dust storm causes product quality to descend on the other hand, improve product quality, simultaneously production process can be carried out continuously; 2, equipment is installed simple.This equipment is on the basis of existing device, simply transforms the purpose that the back just can realize that efficient, continuous melt cinder separates.
Description of drawings
The utility model is described in further detail below in conjunction with drawings and Examples.
Fig. 1 is a structural representation of the present utility model;
Fig. 2 is the structural representation of the utility model discharge seal control valve.
The specific embodiment
As shown in Figure 1, the melt cinder separator is to be in series by two cyclone dust collectors 4,6, and the outlet of cyclone dust collectors 6 links to each other with the import of cyclone dust collectors 4, is connected with underflow pump 2 at outlet 3 places of cyclone dust collectors 4, material by after the melt cinder separation is transported to subsequent processing by underflow pump 2.
The material that needs melt cinder to separate, feeding mouth 5 by cyclone dust collectors 6 is inhaled in the cyclone dust collectors 6, because the density of slag is bigger in the material, and the density of leachate is less, slag drops under the effect of gravity in the discharge gate 9 of cyclone dust collectors 6 in the material, and leachate is entered in the cyclone dust collectors 4 by the outlet of cyclone dust collectors 6, carries out melt cinder once more and separates, last leachate is squeezed into subsequent processing by the outlet 3 of cyclone dust collectors 4 by the outlet 1 of underflow pump 2.
On cyclone dust collectors discharge gate 9, discharge seal control valve 7,8 is installed, be deposited in the slag in the cyclone dust collectors discharge gate 9 because the effect of deadweight, be deposited in a certain amount of after, will push discharge open by the valve plate 12 that hinge 13 is connected with discharge gate 9.Vertical fixing is connected with weight linear meter 11 and balancing weight 10 on valve plate 12, and balancing weight 10 can slippage on weight linear meter 11, to adjust the amount of slags in the discharge gate 9.When the quantity of slag that need pile up in discharge gate 9 was big, as shown in Figure 2, the balancing weight 10 that moves right just can be realized.When the quantity of slag that need in discharge gate 9, pile up hour, reverse self-balanced upper rotary 10 then.The end face of above-mentioned discharge gate is vertical with horizontal plane, also can form certain angle, and the main cause of doing like this is to want balancing weight 10 to give valve plate 12 certain power of closing.
The above-mentioned power resources that need the melt cinder separation of material to flow are underflow pumps 2, outwards take out by underflow pump, can make to form negative pressure in the cyclone dust collectors, and in the discharge gate 9 of each cyclone dust collectors, because the accumulation of slag can guarantee that it is airtight.
Claims (2)
1, a kind of melt cinder separator, comprise pump and more than one cyclone dust collectors, it is characterized in that being between the cyclone dust collectors (4) (6) series connection, the outlet that is previous cyclone dust collectors (6) links to each other with the import of back cyclone dust collectors (4), is connected with pump (2) in the exit of back cyclone dust collectors (4); On the discharge gate (9) of each cyclone dust collectors, discharge seal control valve (7) (8) is installed.
2, a kind of melt cinder separator according to claim 1 is characterized in that being made up of the balancing weight (10) that the valve plate hinged with discharge gate (12), the vertical weight linear meter that links with valve plate (11) and slip are installed on the weight linear meter at above-mentioned discharge seal control valve; The end face of above-mentioned discharge gate (9) and horizontal plane form the angle greater than zero degree.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200620006435 CN2892283Y (en) | 2006-02-28 | 2006-02-28 | Liquid dregs separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 200620006435 CN2892283Y (en) | 2006-02-28 | 2006-02-28 | Liquid dregs separator |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2892283Y true CN2892283Y (en) | 2007-04-25 |
Family
ID=38060449
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 200620006435 Expired - Fee Related CN2892283Y (en) | 2006-02-28 | 2006-02-28 | Liquid dregs separator |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2892283Y (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110653660A (en) * | 2019-10-03 | 2020-01-07 | 王剑 | Leading high-efficient slagging-off protection device of digit control machine tool coolant liquid circulating pump |
-
2006
- 2006-02-28 CN CN 200620006435 patent/CN2892283Y/en not_active Expired - Fee Related
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110653660A (en) * | 2019-10-03 | 2020-01-07 | 王剑 | Leading high-efficient slagging-off protection device of digit control machine tool coolant liquid circulating pump |
CN110653660B (en) * | 2019-10-03 | 2021-02-19 | 大连元坤机械设备有限公司 | Leading high-efficient slagging-off protection device of digit control machine tool coolant liquid circulating pump |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |