CN204939137U - A kind of portable cyaniding tailing slurry treatment system - Google Patents
A kind of portable cyaniding tailing slurry treatment system Download PDFInfo
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- CN204939137U CN204939137U CN201520678481.1U CN201520678481U CN204939137U CN 204939137 U CN204939137 U CN 204939137U CN 201520678481 U CN201520678481 U CN 201520678481U CN 204939137 U CN204939137 U CN 204939137U
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- oxidation reaction
- agitation tank
- wimble thickener
- deep wimble
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Abstract
The utility model discloses a kind of portable cyaniding tailing slurry treatment system, it is made up of teeter column of sizing mixing, oxidation reaction chamber, adsorption treatment room and the dense room of dark cone, teeter column of wherein sizing mixing is made up of two arranged side by side steel basins of sizing mixing, the bottom of oxidation reaction chamber is provided with ozonation aerated supervisor, ozonation aerated arm and ozone micro-hole aerator, adsorption treatment indoor arrange a telescopic adsorbing agitation tank, and adsorption stuffing is filled in adsorbing agitation tank inside.The utility model provides a kind of portable cyaniding tailing slurry treatment system, not only can realize the harmless treatment of cyaniding tailing slurry, and the recycling of valuable resource in ore pulp can be realized, there is the advantages such as processing speed is fast, treatment effect good, running cost is low, construction investment is few.
Description
Technical field
The utility model relates to Industrial Solid Waste processing technology field, particularly a kind of gold industry cyaniding tailing slurry treatment system.
Background technology
Because the most of gold mine of China adopts Cyanide Process always, a large amount of cyaniding tailing slurry is produced in golden production process, these cyaniding tailing slurries are deposited in Tailings Dam in the mode of dry row or wet row, along with the expansion of golden production scale and the prolongation of production history, the accumulating amount of cyaniding tailing slag is increasing year by year, take a large amount of soil, these waste residues are due to containing prussiate and heavy metal, become the ubiquitous Hazardous wastes of gold mine enterprise, at Tailings Dam Anti-seeping technology improper or maintenance management not in time time, in cyaniding tailing slag, prussiate will ooze because drenching with rain down and produce pollution to surrounding enviroment and underground water.At present, both at home and abroad for cyanide wastewater administer documents and materials and Engineering Projects more, less to the research of cyaniding tailing slurry improvement aspect.If cyaniding tailing slurry can realize harmless treatment before being delivered to Tailings Dam, the cyaniding waste residue leaching liquor formed because of rainfall can not only be avoided to pollute, and and then mine tailings recycling can be realized.
Summary of the invention
The purpose of this utility model is exactly for the problems referred to above, and provides the portable cyaniding tailing slurry treatment system that a kind for the treatment of effect is good, processing efficiency is high.
The utility model shell is cuboid-type, below is provided with four castors, inside is provided with three baffle plates, shell is divided into four chambers, be respectively teeter column of sizing mixing, oxidation reaction chamber, adsorption treatment room and the dense room of dark cone, teeter column of wherein sizing mixing is made up of two arranged side by side steel basins of sizing mixing, steel basin of sizing mixing is cylindrical structure, top is provided with acid reagent chemical feed pipe, inlet pipe and stirring power set, stir below power set and connect stirring rake, steel basin of sizing mixing is provided with near a upper lateral part of oxidation reaction chamber steel basin outlet pipe of sizing mixing, oxidation reaction chamber is a cuboid-type ozone oxidation reaction device, ozonation aerated supervisor, ozonation aerated arm and ozone micro-hole aerator is provided with bottom ozone oxidation reaction device, the upper lateral part of ozone oxidation reaction device near adsorption treatment room is provided with oxidation reaction chamber outlet pipe, and oxidation reaction chamber outlet pipe is connected with adsorption treatment room inlet pipe, adsorption treatment chamber interior is provided with a telescopic adsorbing agitation tank, adsorbing agitation tank is cylindrical structure, top is provided with stirring power set, stir power set to be connected with the stirring rake of adsorbing agitation tank inside, circle tube leaching net is provided with between stirring rake and adsorbing agitation tank inwall, adsorption stuffing is filled between filter screen and adsorbing agitation tank inwall, adsorbing agitation tank is provided with adsorption treatment room inlet pipe near oxidation reaction chamber one upper lateral part, adsorption treatment room inlet pipe is through filter screen, adsorbing agitation tank is provided with circular arc backstop near dark cone dense room one upper lateral part, adsorbing agitation tank inwall above circular arc backstop is provided with adsorption treatment room outlet pipe, adsorption treatment room outlet pipe is connected with deep wimble thickener inlet pipe, the dense chamber interior of dark cone is provided with a deep wimble thickener, deep wimble thickener top of leaning to one side is provided with deep wimble thickener inlet pipe and deep wimble thickener upper reaches drain pipe, the center upper portion of deep wimble thickener is provided with into pulp bin, deep wimble thickener inlet pipe with enter pulp bin and be connected, bottom in deep wimble thickener is provided with harrow frame, the upper center position of deep wimble thickener is provided with drive unit, is connected below drive unit with transmission shaft, is provided with deep wimble thickener underflow outlet pipe bottom deep wimble thickener.
The end of described ozonation aerated supervisor is connected with ozonizer, and the front end of ozonation aerated supervisor is connected with ozonation aerated arm, and each ozonation aerated arm is equidistantly arranged in parallel, and each ozonation aerated arm is equidistantly provided with ozone micro-hole aerator.
Described ozone oxidation reaction device, ozonation aerated pipe and ozonation aerated arm are stainless steel, and the material of ozone micro-hole aerator is 316L stainless steel, titanium alloy or pottery.
In described adsorbing agitation tank, the aperture of filter screen is less than the particle diameter of adsorption stuffing, is greater than the particle diameter of slag in ore pulp, and adsorption stuffing is gac or resin, and adsorption stuffing loadings accounts for 1/20 ~ 1/3 of adsorbing agitation tank volume.
The beneficial effects of the utility model:
The utility model provides a kind of portable cyaniding tailing slurry treatment system, not only can realize the harmless treatment of cyaniding tailing slurry, and the recycling of valuable resource in ore pulp can be realized, there is the advantages such as processing speed is fast, treatment effect good, running cost is low, construction investment is few, have broad application prospects.
Accompanying drawing explanation
Fig. 1 is the front view of the utility model structure.
Fig. 2 is the vertical view of the utility model structure.
Wherein, 1-shell; 11-castor; 12-baffle plate; 13-teeter column of sizing mixing; 14-oxidation reaction chamber; 15-adsorption treatment room; The dense room of 16-dark cone; 2-steel basin of sizing mixing; 21-acid reagent chemical feed pipe; 22-inlet pipe; 23-stir power set; 231-stirring rake; 24-steel basin outlet pipe of sizing mixing; 3-ozone oxidation reaction device; 31-ozonation aerated supervisor; 32-ozonation aerated arm; 33-ozone micro-hole aerator; 34-oxidation reaction chamber outlet pipe; 4-adsorbing agitation tank; 41-adsorption treatment room inlet pipe; 42-adsorption treatment room outlet pipe; 43-filter screen; 44-circular arc backstop; 45-adsorption stuffing; 5-deep wimble thickener; 51-deep wimble thickener inlet pipe; 511-enter pulp bin; 52-deep wimble thickener upper reaches drain pipe; 53-deep wimble thickener underflow outlet pipe; 54-harrow frame; 55-drive unit; 56-transmission shaft.
Embodiment
Refer to shown in Fig. 1 and Fig. 2, shell 1 of the present utility model is cuboid-type, four castors 11 are provided with below shell 1, shell 1 inside is provided with three baffle plates 12, shell 1 is divided into four chambers, be respectively teeter column 13 of sizing mixing, oxidation reaction chamber 14, adsorption treatment room 15 and the dense room 16 of dark cone, teeter column 13 of wherein sizing mixing is made up of two arranged side by side steel basins 2 of sizing mixing, size mixing steel basin 2 for cylindrical structure, top is provided with acid reagent chemical feed pipe 21, inlet pipe 22 and stirring power set 23, stir below power set 23 and connect stirring rake 231, steel basin 2 of sizing mixing is provided with near a upper lateral part of oxidation reaction chamber 14 steel basin outlet pipe 24 of sizing mixing, oxidation reaction chamber 14 is a cuboid-type ozone oxidation reaction device 3, ozonation aerated supervisor 31, ozonation aerated arm 32 and ozone micro-hole aerator 33 is provided with bottom ozone oxidation reaction device 3, the upper lateral part of ozone oxidation reaction device 3 near adsorption treatment room 15 is provided with oxidation reaction chamber outlet pipe 34, and oxidation reaction chamber outlet pipe 34 is connected with adsorption treatment room inlet pipe 41, inside, adsorption treatment room 15 is provided with a telescopic adsorbing agitation tank 4, adsorbing agitation tank 4 is cylindrical structure, top is provided with stirs power set 23, stir power set 23 to be connected with the stirring rake 231 of adsorbing agitation tank 4 inside, circle tube leaching net 43 is provided with between stirring rake 231 and adsorbing agitation tank 4 inwall, adsorption stuffing 45 is filled between filter screen 43 and adsorbing agitation tank 4 inwall, adsorbing agitation tank 4 is provided with adsorption treatment room inlet pipe 41 near oxidation reaction chamber 14 1 upper lateral part, adsorption treatment room inlet pipe 41 is through filter screen 43, adsorbing agitation tank 4 is provided with circular arc backstop 44 near dark cone dense room 16 1 upper lateral part, adsorbing agitation tank 4 inwall above circular arc backstop 44 is provided with adsorption treatment room outlet pipe 42, adsorption treatment room outlet pipe 42 is connected with deep wimble thickener inlet pipe 51, inside, dark cone dense room 16 is provided with a deep wimble thickener 5, deep wimble thickener 5 top of leaning to one side is provided with deep wimble thickener inlet pipe 51 and deep wimble thickener upper reaches drain pipe 52, the center upper portion of deep wimble thickener 5 is provided with into pulp bin 511, deep wimble thickener inlet pipe 51 with enter pulp bin 511 and be connected, bottom in deep wimble thickener 5 is provided with harrow frame 54, the upper center position of deep wimble thickener 5 is provided with drive unit 55, be connected with transmission shaft 56 below drive unit 55, bottom deep wimble thickener 5, be provided with deep wimble thickener underflow outlet pipe 53.
The end of described ozonation aerated supervisor 31 is connected with ozonizer, and the front end of ozonation aerated supervisor 31 is connected with ozonation aerated arm 32, and each ozonation aerated arm 32 is equidistantly arranged in parallel, and each ozonation aerated arm 32 is equidistantly provided with ozone micro-hole aerator 33.
Described ozone oxidation reaction device 3, ozonation aerated supervisor 31 and ozonation aerated arm 32 are stainless steel, and the material of ozone micro-hole aerator 33 is 316L stainless steel, titanium alloy or pottery.
In described adsorbing agitation tank 4, the aperture of filter screen 43 is less than the particle diameter of adsorption stuffing 45, is greater than the particle diameter of slag in ore pulp, and adsorption stuffing 45 is gac or resin, and adsorption stuffing 45 loadings accounts for 1/20 ~ 1/3 of adsorbing agitation tank 4 volume.
The utility model is when carrying out process cyaniding tailing slurry, cyaniding tailing slurry enters size mixing steel basin 2 from entering oar pipe 22, add a certain amount of acid reagent from acid reagent chemical feed pipe 21 regulates between pH value to 9 ~ 10 of ore pulp simultaneously, ore pulp after sizing mixing enters into oxidation reaction chamber 14 from steel basin outlet pipe 24 of sizing mixing, oxide treatment is carried out under the ozone that ozone micro-hole aerator 33 bloats, ore pulp after ozone Oxidation Treatment flow in the adsorbing agitation tank 4 in adsorption treatment room 15, gac or resin is filled between the inwall of adsorbing agitation tank 4 and filter screen 43, by gac or resin, the valuable metal element in ore pulp is adsorbed, ore pulp after adsorption treatment enters into the dense room 16 of dark cone and carries out dense, upper flow liquid returns in technical process, underflow flows out to Tailings Dam from deep wimble thickener underflow outlet pipe 53.
Claims (4)
1. a portable cyaniding tailing slurry treatment system, it is characterized in that: its shell (1) is cuboid-type, shell (1) below is provided with four castors (11), shell (1) inside is provided with three baffle plates (12), shell (1) is divided into four chambers, be respectively teeter column of sizing mixing (13), oxidation reaction chamber (14), adsorption treatment room (15) and the dense room of dark cone (16), teeter column (13) of wherein sizing mixing is made up of two steel basins of sizing mixing (2) arranged side by side, steel basin (2) of sizing mixing is cylindrical structure, top is provided with acid reagent chemical feed pipe (21), inlet pipe (22) and stirring power set (23), stir power set (23) below and connect stirring rake (231), steel basin (2) of sizing mixing is provided with near a upper lateral part of oxidation reaction chamber (14) steel basin outlet pipe (24) of sizing mixing, oxidation reaction chamber (14) is a cuboid-type ozone oxidation reaction device (3), ozone oxidation reaction device (3) bottom is provided with ozonation aerated supervisor (31), ozonation aerated arm (32) and ozone micro-hole aerator (33), the upper lateral part of ozone oxidation reaction device (3) near adsorption treatment room (15) is provided with oxidation reaction chamber outlet pipe (34), and oxidation reaction chamber outlet pipe (34) is connected with adsorption treatment room inlet pipe (41), adsorption treatment room (15) inside is provided with a telescopic adsorbing agitation tank (4), adsorbing agitation tank (4) is cylindrical structure, top is provided with stirs power set (23), the stirring rake (231) stirring power set (23) inner with adsorbing agitation tank (4) is connected, circle tube leaching net (43) is provided with between stirring rake (231) and adsorbing agitation tank (4) inwall, adsorption stuffing (45) is filled between filter screen (43) and adsorbing agitation tank (4) inwall, adsorbing agitation tank (4) is provided with adsorption treatment room inlet pipe (41) near oxidation reaction chamber (14) upper lateral part, adsorption treatment room inlet pipe (41) is through filter screen (43), adsorbing agitation tank (4) is provided with circular arc backstop (44) near dark cone dense room (16) upper lateral part, adsorbing agitation tank (4) inwall of circular arc backstop (44) top is provided with adsorption treatment room outlet pipe (42), adsorption treatment room outlet pipe (42) is connected with deep wimble thickener inlet pipe (51), the dense room of dark cone (16) inside is provided with a deep wimble thickener (5), deep wimble thickener (5) top of leaning to one side is provided with deep wimble thickener inlet pipe (51) and deep wimble thickener upper reaches drain pipe (52), the center upper portion of deep wimble thickener (5) is provided with into pulp bin (511), deep wimble thickener inlet pipe (51) with enter pulp bin (511) and be connected, bottom in deep wimble thickener (5) is provided with harrow frame (54), the upper center position of deep wimble thickener (5) is provided with drive unit (55), drive unit (55) below is connected with transmission shaft (56), deep wimble thickener (5) bottom is provided with deep wimble thickener underflow outlet pipe (53).
2. the portable cyaniding tailing slurry treatment system of one according to claim 1, it is characterized in that: the end of described ozonation aerated supervisor (31) is connected with ozonizer, the front end of ozonation aerated supervisor (31) is connected with ozonation aerated arm (32), each ozonation aerated arm (32) is equidistantly arranged in parallel, and each ozonation aerated arm (32) is equidistantly provided with ozone micro-hole aerator (33).
3. the portable cyaniding tailing slurry treatment system of one according to claim 1, it is characterized in that: described ozone oxidation reaction device (3), ozonation aerated supervisor (31) and ozonation aerated arm (32) are stainless steel, the material of ozone micro-hole aerator (33) is 316L stainless steel, titanium alloy or pottery.
4. the portable cyaniding tailing slurry treatment system of one according to claim 1, it is characterized in that: in described adsorbing agitation tank (4), the aperture of filter screen (43) is less than the particle diameter of adsorption stuffing (45), be greater than the particle diameter of slag in ore pulp, adsorption stuffing (45) is gac or resin, and adsorption stuffing (45) loadings accounts for 1/20 ~ 1/3 of adsorbing agitation tank (4) volume.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520678481.1U CN204939137U (en) | 2015-09-04 | 2015-09-04 | A kind of portable cyaniding tailing slurry treatment system |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520678481.1U CN204939137U (en) | 2015-09-04 | 2015-09-04 | A kind of portable cyaniding tailing slurry treatment system |
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| Publication Number | Publication Date |
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| CN204939137U true CN204939137U (en) | 2016-01-06 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520678481.1U Active CN204939137U (en) | 2015-09-04 | 2015-09-04 | A kind of portable cyaniding tailing slurry treatment system |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115874065A (en) * | 2022-11-22 | 2023-03-31 | 云南驰宏锌锗股份有限公司 | Method for deeply purifying middle and upper clear solution by deep cone system |
-
2015
- 2015-09-04 CN CN201520678481.1U patent/CN204939137U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115874065A (en) * | 2022-11-22 | 2023-03-31 | 云南驰宏锌锗股份有限公司 | Method for deeply purifying middle and upper clear solution by deep cone system |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20180206 Address after: 130012 nanhu road, Chaoyang District, Changchun, Jilin Province, No. 6760 Patentee after: Changchun Gold Research Institute Co., Ltd. Address before: 130012 nanhu road, Jilin, Changchun, No. 6760 Patentee before: Changchun Gold Research Institute |
|
| TR01 | Transfer of patent right |