CN211199359U - Zinc oxide recovery refining equipment - Google Patents
Zinc oxide recovery refining equipment Download PDFInfo
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- CN211199359U CN211199359U CN202020080740.1U CN202020080740U CN211199359U CN 211199359 U CN211199359 U CN 211199359U CN 202020080740 U CN202020080740 U CN 202020080740U CN 211199359 U CN211199359 U CN 211199359U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
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Abstract
The utility model discloses a zinc oxide retrieves refining equipment, which comprises an outer shell, shell one side outer wall welding has the heating chamber, the bottom outer wall welding of heating chamber has the heating chamber, there is the second door one side outer wall of heating chamber through hinged joint, one side outer wall of heating chamber has the second display through the fix with screw, one side outer wall of heating chamber has second shift knob through the fix with screw, one side outer wall of heating chamber has third adjust knob through the fix with screw, the bottom inner wall of heating chamber has the heating wire through the fix with screw, one side outer wall welding of shell has the support, the top outer wall of support has the thermostat through the fix with screw, the inside of shell is provided with the process chamber. The utility model discloses a place zinc cigarette ash in the heating chamber, third adjust knob adjusting temperature, the heating chamber passes through the electric heat wire and provides the heat to the heating chamber to fluorine and chlorine in the zinc cigarette ash carry out the desorption, can desorption arsenic and antimony in the zinc cigarette ash simultaneously, and need not carry out the desorption in the solution.
Description
Technical Field
The utility model relates to a zinc oxide retrieves technical field, especially relates to a zinc oxide retrieves refining equipment.
Background
The zinc oxide-containing material comprises zinc oxide ore and zinc ash, the zinc ash mainly comes from a zinc ash recovery system of a steel plant and a slag fuming furnace of a copper and lead smelting plant, and generally contains higher fluorine and chlorine, and when the leaching is directly carried out, almost all fluorine and chlorine enter a zinc sulfate solution, so that the fluorine and chlorine content in the zinc electrolyte exceeds the standard. Therefore, fluorine and chlorine in the zinc oxide must be removed before leaching.
Through retrieval, the Chinese patent with the application number of CN207317575U discloses a zinc oxide finished product recovery device, which comprises a cooling box, wherein the cooling box comprises an outer layer and an inner layer, and a side air cavity and a bottom air cavity are formed between the outer layer and the inner layer; the side air cavity is internally provided with a baffle and is divided into an upper air cavity and a lower air cavity, and the lower air cavity is obliquely provided with an air outlet along the inner wall of the cooling box; the bottom air cavity is connected with an air compressor in sequence. The recovery device generates a fluidization effect through gas, and adopts a condensation system condensation circulation system to carry out double cooling while carrying out fluidization stirring cooling, so that the cooling effect is improved; the driving device nut and the hollow screw are adopted to compress the inner space of the cooling box, so that the zinc oxide powder is directly extruded out of the discharge port, the settling time is reduced, and the production efficiency is improved.
The zinc oxide recovery device in the above patent has the following disadvantages: the method only considers that cooling is needed when the zinc oxide finished product is recovered and produced, and does not consider that chlorine and fluorine are needed to be separated in the treatment process before the zinc oxide finished product, but in reality, copper slag and silver salt are added into the solution to be removed, but the method has low efficiency and poor effect, and has influence on the solution.
SUMMERY OF THE UTILITY MODEL
The utility model aims at solving the defects existing in the prior art and providing zinc oxide recovery refining equipment.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
the utility model provides a zinc oxide retrieves refining equipment, includes the shell, shell one side outer wall welding has the heating chamber, and the bottom outer wall welding of heating chamber has the heating chamber, and there is the second door of one side outer wall of heating chamber through hinged joint, and one side outer wall of heating chamber has the second display through the fix with screw, and one side outer wall of heating chamber has second shift knob through the fix with screw, and one side outer wall of heating chamber has third adjust knob through the fix with screw, and the bottom inner wall of heating chamber has the heating wire through the fix with screw.
As a further aspect of the present invention: the inside of shell is provided with the process chamber, and the inner wall of process chamber top is opened there is the feed opening, and the top of shell is passed through the fix with screw and is had the dilute sulfuric acid fluid reservoir, and the circumference outer wall of dilute sulfuric acid fluid reservoir has first pipeline through threaded connection, and the other end of first pipeline has first self priming pump through threaded connection, and first self priming pump passes through the fix with screw top outer wall of shell, and the delivery outlet of first self priming pump is connected with the process chamber.
As a further aspect of the present invention: the outer wall of one side of shell has the second self priming pump through the fix with screw, and there is the second pipeline one side outer wall of second self priming pump through threaded connection, and there is zinc sulfate solution tank the other end of second pipeline through threaded connection.
As a further aspect of the present invention: the outer wall of one side of shell has the third self priming pump through the fix with screw, and the outer wall of one side of third self priming pump has the third pipeline through threaded connection, and the other end of third pipeline has the copper sulfate fluid reservoir through threaded connection.
As a further aspect of the present invention: the outer wall of one side of shell is fixed with the fourth from the suction pump through the screw, and the outer wall of one side of fourth from the suction pump has the fourth pipeline through threaded connection, and the other end of fourth pipeline has the oxidant jar through threaded connection.
As a further aspect of the present invention: the outer wall welding of one side of shell has the support, and the top outer wall of support has the thermostat through the fix with screw, and one side outer wall of thermostat has first display through the fix with screw, and one side outer wall of thermostat has first adjust knob through the fix with screw.
As a further aspect of the present invention: the outer wall of one side of shell has the control cabinet through the fix with screw, and the outer wall of one side of control cabinet has control panel through the fix with screw, and the outer wall of one side of control cabinet has first shift knob through the fix with screw, and the outer wall of one side of control cabinet has second adjust knob through the fix with screw.
As a further aspect of the present invention: the bottom inner wall of treatment chamber has the swash plate through the fix with screw, and the bottom inner wall of treatment chamber is provided with unloading door, and the bottom outer wall of unloading door is provided with the motor, and one side inner wall of treatment chamber has the filtration jube through the fix with screw, and one side inner wall of treatment chamber has the metal sheet through the fix with screw, and there is the apron at the top outer wall of shell through hinged joint, and there is first door one side outer wall of shell through hinged joint.
The utility model has the advantages that:
1. by placing the zinc ash in the heating chamber, adjusting the temperature by the third adjusting knob, the heating chamber supplies heat to the heating chamber through the electric heating wire, thereby removing fluorine and chlorine in the zinc ash, simultaneously removing arsenic and antimony in the zinc ash, and not needing to remove in solution.
2. Through first self priming pump, can make the dilute sulphuric acid of dilute sulphuric acid fluid reservoir flow into the treatment chamber in, leach the processing to zinc cigarette ash, get rid of the iron ion in the zinc cigarette ash, obtain zinc sulfate solution, the third self priming pump can make the copper sulfate in the copper sulfate fluid reservoir flow into the treatment chamber, get rid of the copper ion in the zinc sulfate solution, the fourth self priming pump can make the oxidant in the oxidant jar flow into the treatment chamber, further get rid of the iron ion, reach and carry out deep purification's effect to zinc sulfate solution.
3. Can make the required temperature of indoor maintenance of treatment through the thermostat, the steerable temperature size of first adjust knob, control panel can carry out parameter setting and controlgear to equipment, and unloading door can make the leaching sediment that obtains after leaching get into in first door, filters the jube and can make the leaching sediment not get into in the zinc sulfate solution jar to reach control and convenient operation's effect.
Drawings
FIG. 1 is a schematic view of a zinc oxide recovery and refining apparatus according to the present invention;
FIG. 2 is a schematic diagram of a right-view structure of a zinc oxide recovery and refining apparatus provided by the present invention;
FIG. 3 is a left side view schematic structural diagram of a zinc oxide recovery refining device provided by the utility model;
fig. 4 is a schematic view of a sectional structure of a zinc oxide recovery refining device provided by the utility model.
In the figure: 1 shell, 2 apron, 3 first pipeline, 4 dilute sulphuric acid liquid tank, 5 first self priming pumps, 6 thermostats, 7 supports, 8 zinc sulfate solution tank, 9 second pipeline, 10 first door, 11 second door, 12 heat supply chamber, 13 heating chamber, 14 first display, 15 first adjusting knob, 16 first shift knob, 17 second self priming pumps, 18 third self priming pumps, 19 third pipeline, 20 copper sulfate liquid tank, 21 oxidant jar, 22 fourth pipeline, 23 fourth self priming pumps, 24 second adjusting knob, 25 control cabinet, 26 control panel, 27 second display, 28 second shift knob, 29 third adjusting knob, 30 heating wire, 31 swash plate, 32 unloading door, 33 filtration jube, 34 metal sheets, 35 unloading mouth.
Detailed Description
The technical solution of the present patent will be described in further detail with reference to the following embodiments.
Reference will now be made in detail to embodiments of the present patent, examples of which are illustrated in the accompanying drawings, wherein like or similar reference numerals refer to the same or similar elements or elements having the same or similar function throughout. The embodiments described below with reference to the drawings are exemplary only for the purpose of explaining the present patent and are not to be construed as limiting the present patent.
In the description of this patent, it is to be understood that the terms "center," "upper," "lower," "front," "rear," "left," "right," "vertical," "horizontal," "top," "bottom," "inner," "outer," and the like are used in the orientations and positional relationships indicated in the drawings for the convenience of describing the patent and for the simplicity of description, and are not intended to indicate or imply that the referenced devices or elements must have a particular orientation, be constructed and operated in a particular orientation, and are not to be considered limiting of the patent.
In the description of this patent, it is noted that unless otherwise specifically stated or limited, the terms "mounted," "connected," and "disposed" are to be construed broadly and can include, for example, fixedly connected, disposed, detachably connected, disposed, or integrally connected and disposed. The specific meaning of the above terms in this patent may be understood by those of ordinary skill in the art as appropriate.
A zinc oxide recovery refining device is shown in figures 1, 3 and 4 and comprises a shell 1, wherein a heating chamber 13 is welded on the outer wall of one side of the shell 1, a heating chamber 12 is welded on the outer wall of the bottom of the heating chamber 13, a second bin door 11 is connected on the outer wall of one side of the heating chamber 13 through a hinge, a second display 27 is fixed on the outer wall of one side of the heating chamber 13 through a screw, a second switch button 28 is fixed on the outer wall of one side of the heating chamber 13 through a screw, a third adjusting knob 29 is fixed on the outer wall of one side of the heating chamber 13 through a screw, and a heating wire 30 is fixed on the inner wall of the bottom of the; by placing the zinc ash in the heating chamber 13 and adjusting the temperature by the third adjusting knob 29, the heating chamber 12 supplies heat to the heating chamber 13 through the heating wire 30, so that the fluorine and chlorine in the zinc ash can be removed, the arsenic and antimony in the zinc ash can be removed at the same time, and the removal in the solution is not needed.
In order to solve the problem of zinc soot leaching; as shown in fig. 1, 2 and 4, a treatment chamber is arranged inside a housing 1, a feed opening 35 is formed in the inner wall of the top of the treatment chamber, a dilute sulfuric acid liquid tank 4 is fixed at the top of the housing 1 through screws, a first pipeline 3 is connected to the circumferential outer wall of the dilute sulfuric acid liquid tank 4 through screws, a first self-priming pump 5 is connected to the other end of the first pipeline 3 through screws, the first self-priming pump 5 is fixed to the top outer wall of the housing 1 through screws, an output port of the first self-priming pump 5 is connected to the treatment chamber, a second self-priming pump 17 is fixed to the outer wall of one side of the housing 1 through screws, a second pipeline 9 is connected to the outer wall of one side of the second self-priming pump 17 through screws, a zinc sulfate solution tank 8 is connected to the other end of the second pipeline 9 through screws, a third self-priming pump 18 is fixed to the outer wall of one side of the housing 1 through, the other end of the third pipeline 19 is connected with a copper sulfate liquid tank 20 through threads, the outer wall of one side of the shell 1 is fixed with a fourth self-suction pump 23 through screws, the outer wall of one side of the fourth self-suction pump 23 is connected with a fourth pipeline 22 through threads, and the other end of the fourth pipeline 22 is connected with an oxidant tank 21 through threads; through first self priming pump 5, can make the dilute sulfuric acid of dilute sulfuric acid fluid reservoir 4 flow into the treatment chamber in, leach the processing to zinc cigarette ash, get rid of the iron ion in the zinc cigarette ash, obtain zinc sulfate solution, third self priming pump 18 can make the copper sulfate in the copper sulfate fluid reservoir 20 flow into the treatment chamber, get rid of the copper ion in the zinc sulfate solution, fourth self priming pump 23 can make the oxidant in the oxidant jar 21 flow into the treatment chamber, further get rid of the iron ion, reach and carry out deep purification's effect to zinc sulfate solution.
In order to solve the problem of controlling equipment; as shown in fig. 1, 2 and 4, a bracket 7 is welded on the outer wall of one side of the housing 1, a thermostat 6 is fixed on the outer wall of the top of the bracket 7 through screws, a first display 14 is fixed on the outer wall of one side of the thermostat 6 through screws, a first adjusting knob 15 is fixed on the outer wall of one side of the thermostat 6 through screws, a console 25 is fixed on the outer wall of one side of the housing 1 through screws, a control panel 26 is fixed on the outer wall of one side of the console 25 through screws, a first switch button 16 is fixed on the outer wall of one side of the console 25 through screws, a second adjusting knob 24 is fixed on the outer wall of one side of the console 25 through screws, a sloping plate 31 is fixed on the inner wall of the bottom of the processing chamber through screws, a discharging bin gate 32 is arranged on the inner wall of the bottom of the processing chamber, a motor is arranged on the outer wall of the bottom of the discharging bin, a metal plate 34 is fixed on the inner wall of one side of the treatment chamber through screws, the outer wall of the top of the shell 1 is connected with a cover plate 2 through a hinge, and the outer wall of one side of the shell 1 is connected with a first bin gate 10 through a hinge; can make the required temperature of indoor maintenance of treatment through thermostat 6, the steerable temperature size of first adjust knob 15, control panel 26 can carry out parameter setting and controlgear to equipment, and unloading door 32 can make the sediment of leaching that obtains after leaching get into first door 10 in, filter in the jube 33 can make the sediment of leaching not get into zinc sulfate solution tank 8 to reach control and convenient operation's effect.
The working principle is as follows: when in use, the power supply is connected, zinc ash is placed in the heating chamber 13, the second bin door 11 is closed, the second switch button 28 is pressed, the temperature of the heating chamber 13 is adjusted through the third adjusting knob 29, the second display 27 displays the temperature in the heating chamber 13, the heating wire 30 in the heating chamber 12 works to provide heat for the heating chamber 13, after heating is finished, the heating chamber is taken out and poured into the processing chamber from the discharging opening 35, the first switch button 16 is opened, the cover plate 2 is closed, parameters and control equipment are arranged on the control panel 26 in the control console 25, the first adjusting knob 15 is rotated to adjust the temperature of the thermostat 6, the beginning is confirmed in the control panel 26, the first self-priming pump 5 enables the dilute sulfuric acid in the dilute sulfuric acid liquid tank 4 to flow into the processing chamber to obtain zinc sulfate solution, the second self-priming pump 17 sucks the zinc sulfate solution into the zinc sulfate solution tank 8, the motor is controlled in the control panel 26 to enable the discharging bin door 32, the leached slag falls into the first bin gate 10, the zinc sulfate solution is discharged into the treatment chamber by the second self-priming pump 17, the copper sulfate in the copper sulfate liquid tank 20 can flow into the treatment chamber by the third self-priming pump 18, the oxidant in the oxidant tank 21 can flow into the treatment chamber by the fourth self-priming pump 23, and finally, the solution after deep purification is electrolyzed by electrifying the metal plate 34.
The above, only be the concrete implementation of the preferred embodiment of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art is in the technical scope of the present invention, according to the technical solution of the present invention and the utility model, the concept of which is equivalent to replace or change, should be covered within the protection scope of the present invention.
Claims (8)
1. The utility model provides a refining equipment is retrieved to zinc oxide, includes shell (1), a serial communication port, shell (1) one side outer wall welding has heating chamber (13), the bottom outer wall welding of heating chamber (13) has heat supply chamber (12), one side outer wall of heating chamber (13) has second door (11) through hinged joint, one side outer wall of heating chamber (13) has second display (27) through the fix with screw, one side outer wall of heating chamber (13) has second shift knob (28) through the fix with screw, one side outer wall of heating chamber (13) has third adjust knob (29) through the fix with screw, the bottom inner wall of heat supply chamber (12) has heating wire (30) through the fix with screw.
2. The zinc oxide recycling and refining equipment according to claim 1, characterized in that a treatment chamber is arranged inside the casing (1), a feed opening (35) is formed in the inner wall of the top of the treatment chamber, a dilute sulfuric acid liquid tank (4) is fixed to the top of the casing (1) through screws, a first pipeline (3) is connected to the outer wall of the circumference of the dilute sulfuric acid liquid tank (4) through threads, a first self-sucking pump (5) is connected to the other end of the first pipeline (3) through threads, the first self-sucking pump (5) is fixed to the outer wall of the top of the casing (1) through screws, and an output port of the first self-sucking pump (5) is connected with the treatment chamber.
3. The zinc oxide recovery refining equipment according to claim 2, characterized in that a second self-sucking pump (17) is fixed on the outer wall of one side of the casing (1) through screws, a second pipeline (9) is connected on the outer wall of one side of the second self-sucking pump (17) through threads, and a zinc sulfate solution tank (8) is connected on the other end of the second pipeline (9) through threads.
4. The zinc oxide recovery refining equipment according to claim 3, characterized in that a third self-sucking pump (18) is fixed on the outer wall of one side of the outer shell (1) through screws, a third pipeline (19) is connected on the outer wall of one side of the third self-sucking pump (18) through threads, and a copper sulfate liquid tank (20) is connected on the other end of the third pipeline (19) through threads.
5. The zinc oxide recovery refining equipment according to claim 4, characterized in that a fourth self-sucking pump (23) is fixed on the outer wall of one side of the shell (1) through screws, a fourth pipeline (22) is connected on the outer wall of one side of the fourth self-sucking pump (23) through threads, and an oxidant tank (21) is connected on the other end of the fourth pipeline (22) through threads.
6. The zinc oxide recovery refining equipment according to claim 5, characterized in that a support (7) is welded on the outer wall of one side of the casing (1), a thermostat (6) is fixed on the outer wall of the top of the support (7) through screws, a first display (14) is fixed on the outer wall of one side of the thermostat (6) through screws, and a first adjusting knob (15) is fixed on the outer wall of one side of the thermostat (6) through screws.
7. The zinc oxide recovery refining equipment according to claim 6, wherein a control console (25) is fixed on the outer wall of one side of the casing (1) through screws, a control panel (26) is fixed on the outer wall of one side of the control console (25) through screws, a first switch button (16) is fixed on the outer wall of one side of the control console (25) through screws, and a second adjusting knob (24) is fixed on the outer wall of one side of the control console (25) through screws.
8. The zinc oxide recovery refining equipment according to claim 7, wherein an inclined plate (31) is fixed on the inner wall of the bottom of the treatment chamber through screws, a blanking bin door (32) is arranged on the inner wall of the bottom of the treatment chamber, a motor is arranged on the outer wall of the bottom of the blanking bin door (32), a filtering barrier (33) is fixed on the inner wall of one side of the treatment chamber through screws, a metal plate (34) is fixed on the inner wall of one side of the treatment chamber through screws, a cover plate (2) is connected on the outer wall of the top of the shell (1) through hinges, and a first bin door (10) is connected on the outer wall of one side of the shell (1) through hinges.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020080740.1U CN211199359U (en) | 2020-01-15 | 2020-01-15 | Zinc oxide recovery refining equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020080740.1U CN211199359U (en) | 2020-01-15 | 2020-01-15 | Zinc oxide recovery refining equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN211199359U true CN211199359U (en) | 2020-08-07 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202020080740.1U Active CN211199359U (en) | 2020-01-15 | 2020-01-15 | Zinc oxide recovery refining equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN211199359U (en) |
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2020
- 2020-01-15 CN CN202020080740.1U patent/CN211199359U/en active Active
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