CN209507613U - A kind of zinc sulfate dissolution of raw material impurity removed system - Google Patents
A kind of zinc sulfate dissolution of raw material impurity removed system Download PDFInfo
- Publication number
- CN209507613U CN209507613U CN201920105093.2U CN201920105093U CN209507613U CN 209507613 U CN209507613 U CN 209507613U CN 201920105093 U CN201920105093 U CN 201920105093U CN 209507613 U CN209507613 U CN 209507613U
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- tank body
- zinc sulfate
- valve
- raw material
- exclusion device
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- Removal Of Specific Substances (AREA)
Abstract
The utility model discloses a kind of zinc sulfate dissolution of raw material impurity removed systems, including dissolver, exclusion device and filter device, the discharge port of the dissolver is connected to the feed inlet of the exclusion device, and the first valve is equipped in the two connectivity part, the discharge port of the exclusion device is connected to the feed inlet of the filter device, and the discharge outlet of the exclusion device is equipped with the second valve.Its structure is simple, and zinc sulfate raw material is adequately dissolved in dissolver, carries out that solution of zinc sulfate is obtained by filtration after then being cleaned by exclusion device, solution of zinc sulfate is then dried to obtain zinc sulfate finished product by subsequent handling condensing crystallizing.
Description
Technical field
The utility model belongs to field of chemical equipment more particularly to a kind of zinc sulfate dissolution of raw material impurity removed system.
Background technique
Zinc sulfate need to dissolve its raw material in production, and hydrogen peroxide, bleaching powder and potassium permanganate are added after dissolution and is come
The ferrous ion and divalent manganesetion in raw material are removed, while will form sediment, and zinc sulfate dissolution is in the solution, it is existing
Dissolution impurity removed system rate of dissolution influences production efficiency slowly, while impurity content is high in its zinc sulfate for producing.
Utility model content
In order to solve the above-mentioned technical problem, the purpose of this utility model is to provide a kind of high production efficiency, impurity-eliminating effects
It is good, zinc sulfate dissolution of raw material impurity removed system easy to use.
To achieve the goals above, the technical solution of the utility model is as follows: a kind of zinc sulfate dissolution of raw material impurity removed system,
Including dissolver, exclusion device and filter device, the feed inlet of the discharge port of the dissolver and the exclusion device connects
It is logical, and it is equipped with the first valve in the two connectivity part, the discharge port of the exclusion device is connected to the feed inlet of the filter device,
And the discharge outlet of the exclusion device is equipped with the second valve.
The beneficial effect of above-mentioned technical proposal is: its structure is simple, and zinc sulfate raw material is filled in dissolver
The dissolution divided, carries out that solution of zinc sulfate is obtained by filtration after then being cleaned by exclusion device, then by solution of zinc sulfate by rear
Continuous process condensing crystallizing is dried to obtain zinc sulfate finished product.
Dissolver described in above-mentioned technical proposal includes the first tank body and the first water pump, and first tank body is set vertically
It sets, the upper end is open, and middle part is vertically arranged with a partition in first tank body, and the partition divides first tank body
At two vertical groove bodies, the through-hole for running through it at least provided with one on the partition and two groove bodies being interconnected,
And at least one described through-hole is located at the lower end of the partition, two groove body lower ends are respectively equipped with a pipe joint, institute
The inlet and outlet for stating the first water pump are connected to two pipe joints respectively, and the water outlet of first water pump with
The connectivity part of the corresponding pipe joint is equipped with a threeway, and the connectivity part of the threeway and the pipe joint is equipped with one the
Three valves, the remaining interface of threeway constitute the water outlet of the dissolver.
The beneficial effect of above-mentioned technical proposal is: its structure is simple, closes the first valve in dissolution, opens third valve
Door and the first water pump enable zinc sulfate raw material rapid so that the intracorporal solution of the first tank is constantly recycled by the first water pump
Carry out solution, the solute effect than existing agitating paddle is good, and required time is shorter, and is needing the intracorporal solution of the first tank
When being emitted into the second tank body, then the first valve of either on or off, opens the first water pump and third valve, the first tank is intracorporal at this time
Solution is pumped into the second tank body, can so save equipment cost investment.
Exclusion device described in above-mentioned technical proposal includes the second tank body, and second tank body is vertically arranged, and the upper end is spacious
Mouthful, lower end is equipped with slag-drip opening, and the 4th valve is equipped at the slag-drip opening, between the upper and lower every setting on the side wall of second tank body
There are multiple leakage fluid drams, second valve is multiple, and multiple second valves and multiple leakage fluid drams correspond, often
A second valve is mounted at the corresponding leakage fluid dram, and multiple second valve remainder interfaces connect with a conduit
Logical, the upper end closure of the conduit, lower end opening constitutes the discharge port of the exclusion device.
The beneficial effect of above-mentioned technical proposal is: its structure is simple, adds hydrogen peroxide, bleaching due to being added in the second tank body
Powder and potassium permanganate will form sediment, for preliminary scavenger precipitation object, need to first settle, and settle to sediment, are then turned on position
In sediment layer and close to the second valve of settled layer upper end, supernatant is expelled to filter device and is filtered by filter device
Clear liquid is solution of zinc sulfate, and then openable 4th valve is discharged the sediment in the second tank body by slag-drip opening, and slag is discharged in gained
Clear liquid can be obtained after being centrifuged.
Exclusion device described in above-mentioned technical proposal further includes liquid level tube, and the liquid level tube is transparent pipe, is vertically arranged
In the outside of second tank body, and its lower end connect with the lower end of second tank wall and with second tank interior
Connection, the upper end of the liquid level tube is flushed with second tank body upper end.
The beneficial effect of above-mentioned technical proposal is: can observe level condition in the second tank body by liquid level tube.
Second tank body lower end described in above-mentioned technical proposal is the tapered end conical surface directed downwardly or downward projection of spherical surface, the row
Cinder notch is arranged in second tank body lower end level height lowest part.
The beneficial effect of above-mentioned technical proposal is: being convenient for slag-drip opening deslagging.
Detailed description of the invention
Fig. 1 is the structure diagram that zinc sulfate described in the utility model embodiment dissolves impurity removed system.
In figure: 1 dissolver, 11 first tank bodies, 111 first valves, 12 first water pumps, 13 partitions, 131 through-holes, 14 3
Logical, 15 third valves, 2 exclusion devices, 21 second tank bodies, 211 the 4th valves, 212 leakage fluid drams, 213 second valves, 214 conduits,
22 liquid level tubes, 3 filter devices.
Specific embodiment
The principles of the present invention and feature are described below in conjunction with attached drawing, example is served only for explaining that this is practical
It is novel, it is not intended to limit the scope of the utility model.
As shown in Figure 1, present embodiments providing a kind of zinc sulfate dissolution of raw material impurity removed system, including dissolver 1, removal of impurities
Device 2 and filter device 3, the discharge port of the dissolver 1 are connected to the feed inlet of the exclusion device 2, and are connected in the two
Logical place is equipped with the first valve 111, and the discharge port of the exclusion device 2 is connected to the feed inlet of the filter device 3, and described removes
The discharge outlet of miscellaneous device 2 is equipped with the second valve 213.Its structure is simple, zinc sulfate raw material is carried out in dissolver sufficiently
Dissolution, carry out that solution of zinc sulfate is obtained by filtration after then being cleaned by exclusion device, then by solution of zinc sulfate by subsequent
Process condensing crystallizing is dried to obtain zinc sulfate finished product.
Dissolver 1 described in above-mentioned technical proposal includes the first tank body 11 and the first water pump 12, first tank body 11
It is vertically arranged, the upper end is open, and middle part is vertically arranged with a partition 13 in first tank body 11, and the partition 13 will be described
First tank body 11 is divided into two vertical groove bodies, at least provided with one through it and by two groove bodies on the partition 13
Interconnected through-hole 131, and at least one described through-hole is located at the lower end of the partition 13, two groove body lower end difference
Equipped with a pipe joint, the inlet and outlet of first water pump 12 are connected to two pipe joints respectively, and
The water outlet of first water pump 12 is equipped with a threeway 14, the threeway 14 and institute with the connectivity part of the corresponding pipe joint
The connectivity part for stating pipe joint is equipped with a third valve 15, and the remaining interface of the threeway 14 constitutes going out for the dissolver
The mouth of a river.Its structure is simple, closes the first valve in dissolution, third valve and the first water pump is opened, so that the first tank is intracorporal
Solution is constantly recycled by the first water pump, enables the carry out solution that zinc sulfate raw material is rapid, more molten than existing agitating paddle
Solve that effect is good, and required time is shorter, and when needing the intracorporal solution discharge of the first tank into the second tank body, then either on or off
First valve opens the first water pump and third valve, and the intracorporal solution of the first tank is pumped into the second tank body at this time, so may be used
Save equipment cost investment.
Exclusion device described in above-mentioned technical proposal includes the second tank body 21, and second tank body 21 is vertically arranged, thereon
End is open, and lower end is equipped with slag-drip opening, and the 4th valve 211 is equipped at the slag-drip opening, on the side wall of second tank body 21
It is equipped at intervals with multiple leakage fluid drams 212 up and down, second valve 213 is multiple, and multiple second valves 213 and multiple institutes
The one-to-one correspondence of leakage fluid dram 212 is stated, each second valve 213 is mounted at the corresponding leakage fluid dram 212, and multiple described second
The remaining interface of valve 213 is connected to a conduit 214, the upper end closure of the conduit 214, is removed described in lower end opening composition
The discharge port of miscellaneous device 2, structure is simple, adds hydrogen peroxide, bleaching powder and potassium permanganate will form due to being added in the second tank body
Sediment need to be settled first for preliminary scavenger precipitation object, be settled to sediment, be then turned on positioned at sediment layer and close to heavy
Drop layer upper end the second valve, by supernatant be expelled to filter device by filter device filter supernatant be solution of zinc sulfate,
And then openable 4th valve is discharged the sediment in the second tank body by slag-drip opening, slag is discharged in gained can obtain clear liquid after being centrifuged.
Exclusion device 2 described in above-mentioned technical proposal further includes liquid level tube 22, and the liquid level tube 22 is transparent pipe, vertical
The outside of second tank body 21 is set, and its lower end is connect and with described second with the lower end of 21 side wall of the second tank body
It is connected to inside tank body 21, the upper end of the liquid level tube 22 is flushed with 21 upper end of the second tank body, can observe the by liquid level tube
Level condition in two tank bodies.
Second tank body, 21 lower end described in above-mentioned technical proposal be the tapered end conical surface directed downwardly or downward projection of spherical surface, it is described
Slag-drip opening setting is convenient for slag-drip opening deslagging in the 21 lower end level height lowest part of the second tank body.
Wherein, the filter device preferably uses negative pressure filtration device, and can refer to document number such as is CN104028026B
Patent of invention document " a kind of belt negative pressure filtration device and its wiper mechanism " or document number be the practical of CN206823287U
A kind of structure of new patent document " negative pressure filtration device " is similar.
The above is only the preferred embodiment of the present invention, is not intended to limit the utility model, all practical at this
Within novel spirit and principle, any modification, equivalent replacement, improvement and so on should be included in the guarantor of the utility model
Within the scope of shield.
Claims (5)
1. a kind of zinc sulfate dissolution of raw material impurity removed system, which is characterized in that including dissolver (1), exclusion device (2) and filtering
The discharge port of device (3), the dissolver (1) is connected to the feed inlet of the exclusion device (2), and is set in the two connectivity part
Have the first valve (111), the discharge port of the exclusion device (2) is connected to the feed inlet of the filter device (3), and described is removed
The discharge outlet of miscellaneous device (2) is equipped with the second valve (213).
2. zinc sulfate dissolution of raw material impurity removed system according to claim 1, which is characterized in that dissolver (1) packet
The first tank body (11) and the first water pump (12) are included, first tank body (11) is vertically arranged, and the upper end is open, first tank body
(11) middle part is vertically arranged with a partition (13) in, the partition (13) will first tank body (11) be divided into two it is mutual
Groove body arranged side by side, at least provided with one through itself and through-hole that two groove bodies are interconnected on the partition (13)
(131), and at least one described through-hole (131) is located at the lower end of the partition (13), and two groove body lower ends are respectively equipped with
The inlet and outlet of one pipe joint, first water pump (12) are connected to two pipe joints respectively, described
The water outlet of first water pump (12) and the connectivity part of the corresponding pipe joint are equipped with a threeway (14), the threeway (14) with
The connectivity part of the pipe joint is equipped with a third valve (15), and the remaining interface of threeway (14) constitutes the dissolution dress
The water outlet set.
3. zinc sulfate dissolution of raw material impurity removed system according to claim 1, which is characterized in that the exclusion device includes the
Two tank bodies (21), second tank body (21) are vertically arranged, and the upper end is open, and lower end is equipped with slag-drip opening, at the slag-drip opening
Equipped with the 4th valve (211), on the side wall of second tank body (21) between the upper and lower every be equipped with multiple leakage fluid drams (212), it is described
Second valve (213) is equipped with multiple, and multiple second valves (213) and multiple leakage fluid drams (212) correspond, often
A second valve (213), which is connected to, to be mounted at the corresponding leakage fluid dram (212), multiple second valves (213)
Remaining interface be connected to a conduit (214), the upper end closure of the conduit (214), lower end opening constitute described in remove
The discharge port of miscellaneous device (2).
4. zinc sulfate dissolution of raw material impurity removed system according to claim 3, which is characterized in that the exclusion device (2) is also
Including liquid level tube (22), the liquid level tube (22) is transparent pipe, is vertically arranged in the outside of second tank body (21), and its
Lower end is connect with the lower end of the second tank body (21) side wall, and is connected to the second tank body (21) inside, the liquid level tube
(22) upper end is flushed with the second tank body (21) upper end end.
5. zinc sulfate dissolution of raw material impurity removed system according to claim 4, which is characterized in that under second tank body (21)
End is the tapered end conical surface directed downwardly or downward projection of spherical surface, and the slag-drip opening setting is horizontal high in the second tank body (21) lower end
Spend lowest part.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920105093.2U CN209507613U (en) | 2019-01-22 | 2019-01-22 | A kind of zinc sulfate dissolution of raw material impurity removed system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920105093.2U CN209507613U (en) | 2019-01-22 | 2019-01-22 | A kind of zinc sulfate dissolution of raw material impurity removed system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209507613U true CN209507613U (en) | 2019-10-18 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201920105093.2U Expired - Fee Related CN209507613U (en) | 2019-01-22 | 2019-01-22 | A kind of zinc sulfate dissolution of raw material impurity removed system |
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| CN (1) | CN209507613U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111533175A (en) * | 2020-06-12 | 2020-08-14 | 福建常青新能源科技有限公司 | Multi-stage type manganese sulfate solution oil and impurity removing device and control method thereof |
-
2019
- 2019-01-22 CN CN201920105093.2U patent/CN209507613U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111533175A (en) * | 2020-06-12 | 2020-08-14 | 福建常青新能源科技有限公司 | Multi-stage type manganese sulfate solution oil and impurity removing device and control method thereof |
| CN111533175B (en) * | 2020-06-12 | 2022-06-21 | 福建常青新能源科技有限公司 | Multi-stage type manganese sulfate solution oil and impurity removing device and control method thereof |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20191018 Termination date: 20220122 |