CN218250037U - Feeding device of high viscosity nickel cobalt material - Google Patents
Feeding device of high viscosity nickel cobalt material Download PDFInfo
- Publication number
- CN218250037U CN218250037U CN202222293617.XU CN202222293617U CN218250037U CN 218250037 U CN218250037 U CN 218250037U CN 202222293617 U CN202222293617 U CN 202222293617U CN 218250037 U CN218250037 U CN 218250037U
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- Prior art keywords
- slurrying
- feeding
- nickel cobalt
- liquid
- squirt
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- 239000000463 material Substances 0.000 title claims abstract description 36
- QXZUUHYBWMWJHK-UHFFFAOYSA-N [Co].[Ni] Chemical compound [Co].[Ni] QXZUUHYBWMWJHK-UHFFFAOYSA-N 0.000 title claims abstract description 30
- 239000007788 liquid Substances 0.000 claims abstract description 65
- 239000002253 acid Substances 0.000 claims abstract description 41
- 238000003860 storage Methods 0.000 claims abstract description 37
- 230000001105 regulatory effect Effects 0.000 claims abstract description 15
- 239000012530 fluid Substances 0.000 claims abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 40
- 238000003756 stirring Methods 0.000 claims description 31
- 239000002893 slag Substances 0.000 claims description 7
- 230000003014 reinforcing effect Effects 0.000 claims description 4
- 239000007787 solid Substances 0.000 abstract description 6
- UUCGKVQSSPTLOY-UHFFFAOYSA-J cobalt(2+);nickel(2+);tetrahydroxide Chemical compound [OH-].[OH-].[OH-].[OH-].[Co+2].[Ni+2] UUCGKVQSSPTLOY-UHFFFAOYSA-J 0.000 abstract description 4
- 238000009854 hydrometallurgy Methods 0.000 abstract description 3
- 239000002699 waste material Substances 0.000 description 31
- 239000002002 slurry Substances 0.000 description 15
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 14
- 239000010941 cobalt Substances 0.000 description 14
- 229910017052 cobalt Inorganic materials 0.000 description 14
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 14
- 238000004537 pulping Methods 0.000 description 8
- 229910052759 nickel Inorganic materials 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 239000013049 sediment Substances 0.000 description 6
- 238000001514 detection method Methods 0.000 description 4
- 238000004090 dissolution Methods 0.000 description 4
- 239000002184 metal Substances 0.000 description 4
- 229910052751 metal Inorganic materials 0.000 description 4
- 230000001276 controlling effect Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000000746 purification Methods 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 229910021503 Cobalt(II) hydroxide Inorganic materials 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- -1 and particularly Chemical compound 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 150000001868 cobalt Chemical class 0.000 description 1
- GVPFVAHMJGGAJG-UHFFFAOYSA-L cobalt dichloride Chemical compound [Cl-].[Cl-].[Co+2] GVPFVAHMJGGAJG-UHFFFAOYSA-L 0.000 description 1
- 229910000361 cobalt sulfate Inorganic materials 0.000 description 1
- 229940044175 cobalt sulfate Drugs 0.000 description 1
- KTVIXTQDYHMGHF-UHFFFAOYSA-L cobalt(2+) sulfate Chemical compound [Co+2].[O-]S([O-])(=O)=O KTVIXTQDYHMGHF-UHFFFAOYSA-L 0.000 description 1
- ASKVAEGIVYSGNY-UHFFFAOYSA-L cobalt(ii) hydroxide Chemical compound [OH-].[OH-].[Co+2] ASKVAEGIVYSGNY-UHFFFAOYSA-L 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
- 230000003301 hydrolyzing effect Effects 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 150000002815 nickel Chemical class 0.000 description 1
- LGQLOGILCSXPEA-UHFFFAOYSA-L nickel sulfate Chemical compound [Ni+2].[O-]S([O-])(=O)=O LGQLOGILCSXPEA-UHFFFAOYSA-L 0.000 description 1
- 229910000008 nickel(II) carbonate Inorganic materials 0.000 description 1
- 229910000363 nickel(II) sulfate Inorganic materials 0.000 description 1
- ZULUUIKRFGGGTL-UHFFFAOYSA-L nickel(ii) carbonate Chemical compound [Ni+2].[O-]C([O-])=O ZULUUIKRFGGGTL-UHFFFAOYSA-L 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000033116 oxidation-reduction process Effects 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Images
Classifications
-
- 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
- Y02P10/20—Recycling
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- Manufacture And Refinement Of Metals (AREA)
Abstract
The utility model discloses a feeding device of high viscosity nickel cobalt material, relate to nickel cobalt hydrometallurgy equipment technical field, solved the problem that there is inefficiency in the feeding mode of current high viscosity nickel cobalt material, including the liquid sending pipe of being connected with the spent acid storage tank, be connected with the delivery pump on the liquid sending pipe, the flow meter, the automatically regulated valve, the liquid outlet of spent acid storage tank is connected to liquid sending pipe one end, the other end connects soft rubber tube, is connected with the feeding squirt on the soft rubber tube, the soft rubber tube is connected with the entry linkage of feeding squirt, the feeding squirt is connected on the removal structure, the acidizing fluid that the feeding squirt spouts enters into the slurrying dissolving tank from the feed inlet of slurrying dissolving tank; can make the nickel cobalt hydroxide material utilize mechanical equipment to add in the slurrying groove, not only improve and throw material efficiency, also avoided abominable operational environment to cause the harm to staff's health simultaneously, the control that level gauge and flow meter connected can be accurate moreover is thrown the dosage, and then the liquid-solid ratio of control slurrying liquid and the density of slurrying liquid.
Description
Technical Field
The utility model relates to a nickel cobalt hydrometallurgy equipment technical field, more specifically is the feeding device technical field who relates to high viscosity nickel cobalt material.
Background
In the nickel-cobalt hydrometallurgy industry, a soluble anode diaphragm electrolysis process comprises purification and electrolysis, wherein the purification process comprises three stages of purification including iron removal, copper removal and cobalt removal, the cobalt removal is to separate the nickel and the cobalt by utilizing the difference of oxidation-reduction potentials and hydrolysis pH values of the cobalt and the nickel, and particularly, chlorine is introduced to separate the cobalt and the nickel, so that the cobalt and the nickel are separated 2+ Oxidation to Co 3+ Adding nickel carbonate to neutralize, hydrolyzing cobalt into cobalt hydroxide to remove, and separating nickel from cobalt.
The cobalt slag is subjected to the working procedures of proportioning slurrying, reduction dissolving, nickel-cobalt separation and the like to produce pure solutions of cobalt sulfate, cobalt chloride, nickel sulfate and the like, and further produce electrodeposited cobalt, cobalt salt or nickel salt products, wherein in the raw materials of the cobalt slag, metals such as cobalt, nickel and the like mainly exist in a high-valence hydroxide form, have high viscosity and need to be slurried into a liquid-solid ratio of 4:1, sending the cobalt slag slurry into a dissolving tank, and introducing a reducing agent to ensure that high-price metals such as nickel and cobalt are selectively reduced into low-price entering solution.
In actual production, as the material viscosity is high, the bucket elevator, the grab bucket crane and other special equipment cannot be used, the high-viscosity nickel-cobalt material is added manually by using a shovel in different periods, the operation environment is poor, the labor efficiency is low, and the slurry solid ratio and the density are unstable.
SUMMERY OF THE UTILITY MODEL
The utility model aims to solve the problem that there is inefficiency in the feeding mode of current high viscidity nickel cobalt material, in order to solve above-mentioned technical problem, the utility model provides a feeding device of high viscidity nickel cobalt material.
The utility model discloses a realize above-mentioned purpose and specifically adopt following technical scheme:
the utility model provides a feeding device of high viscosity nickel cobalt material, includes the liquid delivery pipe of being connected with the spent acid storage tank, be connected with delivery pump, flow meter, automatically regulated valve on the liquid delivery pipe, the liquid outlet of spent acid storage tank is connected to liquid delivery pipe one end, and soft rubber tube is connected to the other end, be connected with reinforced squirt on the soft rubber tube, soft rubber tube with the entry linkage of reinforced squirt, reinforced squirt is connected in removing the structure, reinforced squirt spun acidizing fluid enters into the pulp dissolving tank from the feed inlet of pulp dissolving tank in.
When the feeding device for the high-viscosity nickel-cobalt material is used, waste acid and waste water generated in the production process are added into a waste acid storage tank, the liquid level does not exceed 80% of the waste acid storage tank, then a liquid level meter and a flow meter are regulated, an automatic regulating valve and a conveying pump are sequentially started, a feeding water gun is operated, the position of the feeding water gun is adjusted through a moving structure, the liquid in the waste acid storage tank is sprayed into a slurrying dissolving tank by the feeding water gun, the solid-liquid ratio of slurrying liquid is controlled to be 4:1 through the automatic regulating valve and the flow meter, and the density of the slurrying liquid is 1.2-1.3g/l; and stopping feeding after the liquid level of the slurrying dissolving tank reaches a certain height.
This application can make the nickel cobalt hydroxide material utilize mechanical equipment to add the slurrying groove in, has not only improved and has thrown material efficiency, has also avoided abominable operational environment to cause the harm to staff's health simultaneously, and the control that level gauge and the flow meter connected can be accurate moreover is thrown the dosage, and then the liquid-solid ratio of control slurrying liquid and the density of slurrying liquid.
Further, the top of the waste acid storage tank is connected with a liquid level detection meter, and the liquid level detection meter is in communication connection with the delivery pump; the automatic regulating valve is in communication connection with the flow meter.
The liquid level detector is in communication connection with the delivery pump, so that the delivery pump is started when the liquid level in the waste acid storage tank reaches 80% of the volume of the waste acid storage tank, and the delivery pump is automatically stopped when the liquid level in the waste acid storage tank is lower than 20% of the volume of the waste acid storage tank, so that the effect of automatically controlling the liquid amount in the waste acid storage tank is realized; meanwhile, the automatic regulating valve is in communication connection with the flow meter, so that the solid-to-liquid ratio of the slurry can be automatically controlled to be 4:1, the density of the slurry is 1.2-1.3g/l, the automatic control effect is achieved, and the accuracy of the density control of the slurry is improved.
Further, the moving structure comprises a bottom plate, the feeding water gun is connected to the bottom plate, supporting legs are connected to the lower portion of the bottom plate, reinforcing connecting rods are connected between the supporting legs, and idler wheels are connected to the bottoms of the supporting legs.
The feeding water gun is characterized in that a horizontal short shaft is connected to the bottom plate, the horizontal short shaft is connected to a horizontal rotating bearing, two side plates are connected to the horizontal rotating bearing, the feeding water gun is connected to the side plates through a vertical rotating structure, and a horizontal operating handle is connected to the side plates.
The vertical rotating structure comprises vertical rotating bearings which are connected to the side plates respectively, a vertical rotating shaft is connected to the vertical rotating bearings, the feeding water gun is connected to the vertical rotating shaft, and a vertical operating handle is connected to the feeding water gun.
When the distance between the feeding water gun and the slurrying dissolving tank needs to be adjusted, a worker holds the support legs to push the support legs, so that the feeding water gun can move back and forth; when the horizontal angle of the feeding water gun needs to be adjusted, a worker holds the horizontal operating handle to rotate the feeding water gun; when the vertical angle of the feeding water gun needs to be adjusted, a worker can hold the vertical operating handle, and then the adjustment of the vertical angle of the feeding water gun can be achieved.
This application can not only realize horizontal rotation 360 through connect removal structure, connect horizontal rotating-structure and vertical rotating-structure on the bottom plate in landing leg bottom, can also realize vertical rotation 180, make the staff more convenient when operating reinforced squirt, the accurate feed inlet department from the pulp dissolving tank of reinforced squirt spun water gets into when also can the time simultaneously.
Furthermore, a stirring structure is connected in the slurrying and dissolving tank.
The stirring structure comprises a stirring shaft connected in the slurrying dissolution tank, wherein a stirring blade is connected to the stirring shaft, and the stirring shaft extends to the outside of the slurrying dissolution tank and is connected with a motor for driving the stirring shaft to rotate.
When the liquid level in the slurrying dissolving tank reaches the lower stirring paddle, the stirring structure is started, and the feeding is stopped after the liquid level in the slurrying dissolving tank reaches the height of the upper stirring paddle.
This application is through connecting stirring structure in the pulp dissolving tank, can add the waste acid of spent acid storage tank at reinforced squirt and in the pulp dissolving tank after, carry out quick stirring with the material of pulp dissolving tank through stirring structure, further improved the efficiency of handling.
Furthermore, a feed inlet of the slurrying and dissolving tank is connected with a slag receiving mesh plate.
This application connects the sediment net dish through the feed inlet department connection at the slurrying dissolving tank, can hold back on connecing the sediment net dish with bold, harder nickel cobalt material, reuse after handling the bold that will filter out, harder nickel cobalt material.
The utility model has the advantages as follows:
(1) According to the method, the nickel-cobalt hydroxide material can be added into the pulping tank by using mechanical equipment, so that the feeding efficiency is improved, the damage of a severe working environment to the body of a worker is avoided, and the adding amount of the connected liquid level meter and the flow meter can be accurately controlled, so that the liquid-solid ratio of the pulping liquid and the density of the pulping liquid are controlled; the requirements of working conditions can be met, continuous, stable and uniform feeding can be realized, and meanwhile, mechanical operation and automatic control are realized;
(2) The liquid level detector is in communication connection with the delivery pump, so that the delivery pump is started when the liquid level in the waste acid storage tank reaches 80% of the volume of the waste acid storage tank, and the delivery pump is automatically stopped when the liquid level in the waste acid storage tank is lower than 20% of the volume of the waste acid storage tank, so that the effect of automatically controlling the liquid amount in the waste acid storage tank is realized; meanwhile, the automatic regulating valve is in communication connection with the flowmeter, so that the solid-to-liquid ratio of the slurry can be automatically controlled to be 4:1, the density of the slurry is 1.2-1.3g/l, the automatic control effect is achieved, and the accuracy of the density control of the slurry is improved;
(3) According to the water feeding gun, the moving structure is connected to the bottom of the supporting leg, and the horizontal rotating structure and the vertical rotating structure are connected to the bottom plate, so that not only can 360-degree horizontal rotation be realized, but also 180-degree vertical rotation can be realized, the water sprayed by the water feeding gun can accurately enter from a feed port of the slurrying dissolving tank, and is more convenient for workers to operate the water feeding gun;
(4) According to the pulping and dissolving tank, the stirring structure is connected in the pulping and dissolving tank, so that after waste acid in the waste acid storage tank is added into the pulping and dissolving tank by the feeding water gun, substances in the pulping and dissolving tank are quickly stirred by the stirring structure, and the treatment efficiency is further improved;
(5) This application connects the sediment net dish through the feed inlet department connection at the slurrying dissolving tank, can hold back on connecing the sediment net dish with bold, harder nickel cobalt material, reuse after handling the bold that will filter out, harder nickel cobalt material.
Drawings
FIG. 1 is a schematic structural diagram of an apparatus for extracting sulfur from a plurality of metal minerals according to the present invention;
fig. 2 is a top view of the device for extracting sulfur from various metal minerals in the utility model.
Reference numerals are as follows: 1-a waste acid storage tank, 2-a liquid level detector, 3-a delivery pump, 4-a flow meter, 5-an automatic regulating valve, 6-a soft rubber tube, 7-a feeding water gun, 8-a feeding port, 9-a slag receiving mesh disc, 10-a slurrying dissolving tank, 11-a stirring structure, 71-a vertical operating handle, 72-a barrel, 73-a horizontal operating handle, 74-a side plate, 75-a bottom plate, 76-a supporting leg, 77-a reinforcing connecting rod, 78-a roller, 79-a vertical rotating bearing, 710-a vertical rotating shaft, 711-a horizontal rotating bearing and 712-a horizontal short shaft.
Detailed Description
In order to make the objects, technical solutions and advantages of the embodiments of the present invention clearer, the drawings in the embodiments of the present invention are combined below to clearly and completely describe the technical solutions in the embodiments of the present invention.
Example 1
Referring to fig. 1 to 2, this embodiment provides a feeding device of high viscosity nickel cobalt material, including the liquid sending pipe of being connected with spent acid storage tank 1, be connected with delivery pump 3 on the liquid sending pipe, flow meter 4, automatically regulated valve 5, the liquid outlet of spent acid storage tank 1 is connected to liquid sending pipe one end, soft rubber tube 6 is connected to the other end, be connected with reinforced squirt 7 on the soft rubber tube 6, soft rubber tube 6 and the entry linkage of reinforced squirt 7, reinforced squirt 7 is connected on removing the structure, the acidizing fluid of reinforced squirt 7 spun enters into in the slurrying dissolving tank 10 from the feed inlet 8 of slurrying dissolving tank 10.
When the feeding device for the high-viscosity nickel-cobalt material is used, waste acid and waste water generated in the production process are added into a waste acid storage tank 1, the liquid level does not exceed 80% of that of the waste acid storage tank 1, then a liquid level meter and a flow meter 4 are adjusted, an automatic regulating valve 5 and a delivery pump 3 are sequentially opened, a feeding water gun 7 is operated, the position of the feeding water gun 7 is adjusted through a moving structure, the feeding water gun 7 sprays liquid in the waste acid storage tank 1 into a slurrying and dissolving tank 10, the slurry solid-liquid ratio of the slurry liquid is controlled to be 8978 zft 8978 through the automatic regulating valve 5 and the flow meter 4, and the density of the slurry liquid is 1.2-1.3g/l; and stopping feeding after the liquid level of the slurrying and dissolving tank 10 reaches a certain height.
This application can make the nickel cobalt hydroxide material utilize mechanical equipment to add the pulping groove in, has not only improved and has thrown material efficiency, has also avoided rugged operational environment to cause the harm to staff's health simultaneously, and the control that level gauge and flow meter 4 connected moreover can be accurate is thrown the volume of adding, and then the liquid-solid ratio of control pulp liquid and the density of pulp liquid.
Example 2
Referring to fig. 1-2, based on the embodiment 1, the top of the waste acid storage tank 1 of the embodiment is connected with a liquid level detection meter 2, and the liquid level detection meter 2 is in communication connection with a delivery pump 3; the self-regulating valve 5 is in communication connection with the flow meter 4.
According to the waste acid storage tank, the liquid level detector 2 is in communication connection with the delivery pump 3, so that when the liquid level in the waste acid storage tank 1 reaches 80% of the volume of the waste acid storage tank 1, the delivery pump 3 is started, and when the liquid level in the waste acid storage tank 1 is lower than 20% of the volume of the storage tank, the delivery pump 3 is automatically stopped, so that the effect of automatically controlling the liquid amount in the waste acid storage tank 1 is realized; meanwhile, the automatic regulating valve 5 is in communication connection with the flowmeter 4, so that the solid-to-liquid ratio of the slurry can be automatically controlled to be 4:1, the density of the slurry is 1.2-1.3g/l, the automatic control effect is achieved, and the accuracy of the density control of the slurry is improved.
Example 3
Referring to fig. 1 to 2, based on embodiment 1, the moving structure of this embodiment includes a bottom plate 75, a charging water gun 7 is connected to the bottom plate 75, legs 76 are connected below the bottom plate 75, a reinforcing link 77 is connected between the legs 76, and rollers 78 are connected to bottoms of the legs 76.
Wherein, the bottom plate 75 is connected with a horizontal short shaft 712, the horizontal short shaft 712 is connected with a horizontal rotating bearing 711, the horizontal rotating bearing 711 is connected with two side plates 74, the feeding water gun 7 is connected with the side plates 74 through a vertical rotating structure, and the side plates 74 are connected with a horizontal operating handle 73.
The vertical rotating structure comprises vertical rotating bearings 79 respectively connected to the two side plates 74, a vertical rotating shaft 710 is connected to each vertical rotating bearing 79, the feeding water gun 7 is connected to the vertical rotating shaft 710, and a vertical operating handle 71 is connected to the feeding water gun 7.
When the distance between the feeding water gun 7 and the slurrying and dissolving tank 10 needs to be adjusted, a worker holds the supporting legs 76 to push the feeding water gun 7 to move back and forth; when the horizontal angle of the feeding water gun 7 needs to be adjusted, a worker holds the horizontal operating handle 73 and rotates the feeding water gun 7; when the vertical angle of the feed water gun 7 needs to be adjusted, a worker can hold the vertical operating handle 71 by hand, so that the adjustment of the vertical angle of the feed water gun 7 can be realized.
This application can not only realize horizontal rotation 360 through connecting the removal structure in landing leg 76 bottom, connect horizontal rotating-structure and vertical rotating-structure on bottom plate 75, can also realize vertical rotation 180, make the staff more convenient when operating reinforced squirt 7, the accurate feed inlet 8 department from pulp dissolving tank 10 of reinforced squirt 7 spun water gets into when also can the time simultaneously.
Example 4
Referring to FIGS. 1 and 2, in example 1, a stirring structure 11 is connected to a slurry dissolution tank 10.
Wherein, stirring structure 11 is connected with stirring paddle including the (mixing) shaft of connection in slurrying dissolving tank 10 on the (mixing) shaft, and the (mixing) shaft extends to slurrying dissolving tank 10 outside and connects the pivoted motor of drive (mixing) shaft.
When the liquid level in the slurrying dissolving tank 10 reaches the lower-layer stirring blade, the stirring structure 11 is started, and the feeding is stopped after the liquid level in the slurrying dissolving tank 10 reaches the height of the upper-layer blade.
This application is through connecting stirring structure 11 in slurrying dissolving tank 10, can add the waste acid of waste acid storage tank 1 at reinforced squirt 7 and add the slurrying dissolving tank 10 in later, carry out quick stirring through stirring structure 11 with the material in the slurrying dissolving tank 10, further improved the efficiency of handling.
Example 5
Referring to FIGS. 1 and 2, in example 1, a slag receiving mesh plate 9 is connected to a feed port 8 of a pulp dissolution tank 10.
This application connects sediment net dish 9 through 8 connections of feed inlet at pulp dissolving tank 10, can hold back on receiving sediment net dish 9 with bold, harder nickel cobalt material, reuse after handling the bold that will filter out, harder nickel cobalt material.
Claims (8)
1. The utility model provides a feeding device of high viscosity nickel cobalt material, its characterized in that includes the liquid sending pipe of being connected with spent acid storage tank (1), be connected with delivery pump (3), flowmeter (4), automatically regulated valve (5) on the liquid sending pipe, the liquid outlet of spent acid storage tank (1) is connected to liquid sending pipe one end, and soft rubber tube (6) are connected to the other end, be connected with reinforced squirt (7) on soft rubber tube (6), soft rubber tube (6) with the entry linkage of reinforced squirt (7), reinforced squirt (7) are connected on removing the structure, reinforced squirt (7) spun acidizing fluid enters into in slurrying dissolving tank (10) from feed inlet (8) of slurrying dissolving tank (10).
2. The feeding device for high viscosity nickel cobalt material as claimed in claim 1, characterized in that a liquid level detecting meter (2) is connected to the top of the spent acid storage tank (1), and the liquid level detecting meter (2) is connected with the conveying pump (3) in communication; the automatic regulating valve (5) is in communication connection with the flow meter (4).
3. The charging device for high viscosity nickel cobalt material as claimed in claim 1, characterized in that the moving structure comprises a bottom plate (75), the charging water gun (7) is connected to the bottom plate (75), a leg (76) is connected below the bottom plate (75), a reinforcing connecting rod (77) is connected between the legs (76), and a roller (78) is connected to the bottom of the leg (76).
4. The feeding device for high viscosity nickel cobalt material as claimed in claim 3, characterized in that a horizontal short shaft (712) is connected to the bottom plate (75), the horizontal short shaft (712) is connected to a horizontal rotating bearing (711), two side plates (74) are connected to the horizontal rotating bearing (711), the feeding water gun (7) is connected to the side plates (74) through a vertical rotating structure, and a horizontal operating handle (73) is connected to the side plates (74).
5. The feeding device for high viscosity nickel cobalt material as claimed in claim 4, characterized in that the vertical rotation structure comprises vertical rotation bearings (79) respectively connected to the two side plates (74), a vertical rotation shaft (710) is connected to the vertical rotation bearings (79), the feeding water gun (7) is connected to the vertical rotation shaft (710), and a vertical operating handle (71) is connected to a barrel (72) of the feeding water gun (7).
6. The charging device for high viscosity nickel cobalt material as claimed in claim 1, characterized in that the slurrying and dissolving tank (10) is connected with a stirring structure (11).
7. The feeding device for high viscosity nickel cobalt material as claimed in claim 6, characterized in that the stirring structure (11) comprises a stirring shaft connected in the slurrying and dissolving tank (10), the stirring shaft is connected with a stirring blade, the stirring shaft extends to the outside of the slurrying and dissolving tank (10) and is connected with a motor for driving the stirring shaft to rotate.
8. The charging device for high-viscosity nickel cobalt materials according to claim 6, characterized in that a slag receiving mesh disc (9) is connected to the feeding port (8) of the slurrying and dissolving tank (10).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222293617.XU CN218250037U (en) | 2022-08-29 | 2022-08-29 | Feeding device of high viscosity nickel cobalt material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202222293617.XU CN218250037U (en) | 2022-08-29 | 2022-08-29 | Feeding device of high viscosity nickel cobalt material |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN218250037U true CN218250037U (en) | 2023-01-10 |
Family
ID=84710313
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202222293617.XU Active CN218250037U (en) | 2022-08-29 | 2022-08-29 | Feeding device of high viscosity nickel cobalt material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN218250037U (en) |
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2022
- 2022-08-29 CN CN202222293617.XU patent/CN218250037U/en active Active
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| TR01 | Transfer of patent right |
Effective date of registration: 20240202 Address after: 737100 No. 2 Lanzhou Road, Beijing Road Street, Jinchuan District, Jinchang City, Gansu Province Patentee after: Jinchuan Group Nickel Cobalt Co.,Ltd. Country or region after: China Address before: 737104 No. 98, Jinchuan Road, Jinchuan District, Jinchang City, Gansu Province Patentee before: JINCHUAN GROUP Co.,Ltd. Country or region before: China |