CN204939156U - A kind of portable containing cyanogen slurry processing unit - Google Patents
A kind of portable containing cyanogen slurry processing unit Download PDFInfo
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- CN204939156U CN204939156U CN201520678577.8U CN201520678577U CN204939156U CN 204939156 U CN204939156 U CN 204939156U CN 201520678577 U CN201520678577 U CN 201520678577U CN 204939156 U CN204939156 U CN 204939156U
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- ozone oxidation
- ultrasonic
- oxidation reaction
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Abstract
The utility model discloses a kind of portable containing cyanogen slurry processing unit, it is made up of teeter column of sizing mixing, ozone oxidation reaction room, combination treatment room, ultrasonic/ozone oxidation reaction 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 ozone oxidation reaction room is provided with ozonation aerated system, ultrasonic/ozone oxidation reaction indoor are provided with ozonation aerated system and ultrasonic wave generation systems, be provided with heavy metal fixing agent chemical feed pipe, hydrogen peroxide chemical feed pipe and stir power set above combination treatment room.The one movable type that the utility model provides is containing cyanogen slurry processing unit, not only can realize the harmless treatment containing cyanogen ore pulp, and the recycling of water resources 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, and particularly a kind of gold industry is containing cyanogen slurry processing unit.
Background technology
Because the most of gold mine of China adopts Cyanide Process always, a large amount of sludge containing cyanogens is produced in golden production process, these sludge containing cyanogenses 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, accumulating amount containing cyanogen waste residue 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, will ooze because drenching with rain down containing prussiate in cyanogen waste residue and pollution is produced to surrounding enviroment and underground water.At present, the documents and materials of administering for cyanide wastewater both at home and abroad and Engineering Projects more, to less containing the research of cyanogen ore pulp improvement aspect.If sludge containing cyanogens 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 movable type that a kind for the treatment of effect is good, processing efficiency is high to contain cyanogen slurry processing unit.
The utility model shell is cuboid-type, below is provided with four castors, inside is provided with four baffle plates, shell is divided into five chambers, be respectively teeter column of sizing mixing, ozone oxidation reaction room, combination treatment room, ultrasonic/ozone oxidation reaction 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, the upper lateral part of steel basin near ozone oxidation reaction room of sizing mixing is provided with steel basin outlet pipe of sizing mixing, ozone oxidation reaction room is a cuboid-type ozone oxidation reaction device, be provided with ozonation aerated supervisor, ozonation aerated arm and ozone micro-hole aerator bottom ozone oxidation reaction device, the upper lateral part of ozone oxidation reaction device near combination treatment room is provided with ozone oxidation reaction room outlet pipe, combination treatment room is made up of two combination treatment steel basins arranged side by side, combination treatment steel basin is cylindrical structure, top is provided with heavy metal fixing agent chemical feed pipe, hydrogen peroxide chemical feed pipe and stirs power set, stir below power set and connect stirring rake, the upper lateral part of combination treatment room near ultrasonic/ozone oxidation reaction room is provided with combination treatment steel basin outlet pipe, ultrasonic/ozone oxidation reaction room be cuboid-type ultrasonic/ozone oxidation groove, ultrasonic/ozone oxidation groove inside is provided with ultrasonic amplitude transformer probe, ultrasonic amplitude transformer probe is connected with the ultrasonic transducer above ultrasonic/ozone oxidation groove, ultrasonic transducer is connected with ultra-sonic generator, ultrasonic/ozone oxidation trench bottom is provided with ozonation aerated supervisor, ozonation aerated arm and ozone micro-hole aerator, the upper lateral part of ultrasonic/ozone oxidation groove near adsorption treatment room is provided with ultrasonic/ozone oxidation reaction room outlet pipe, ultrasonic/ozone oxidation reaction room outlet pipe with deeply bore dense room inlet pipe and be connected, 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, ultrasonic/ozone oxidation groove, ultrasonic amplitude transformer probe, ozonation aerated supervisor and ozonation aerated arm are stainless steel, and the material of ozone micro-hole aerator is 316L stainless steel, titanium alloy or pottery.
Described ultrasonic/ozone oxidation groove in ultrasonic amplitude transformer probe diameter adjustable, ultrasonic amplitude transformer probe quantity be more than or equal to one, be evenly distributed on below mineral syrup liquid 30mm place.
The beneficial effects of the utility model:
The utility model provides a kind of portable containing cyanogen slurry processing unit, not only can realize the harmless treatment containing cyanogen ore pulp, and the recycling of water resources 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.
Fig. 3 is the ozonation aerated supervisor of the utility model, ozonation aerated arm and ozone micro-hole aerator structure iron.
Wherein, 1-shell; 11-castor; 12-baffle plate; 13-teeter column of sizing mixing; 14-ozone oxidation reaction room; 15-combination treatment room; 16-ultrasonic/ozone oxidation reaction room; The dense room of 17-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-ozone oxidation reaction room outlet pipe; 4-combination treatment steel basin; 41-heavy metal fixing agent chemical feed pipe; 42-hydrogen peroxide chemical feed pipe; 43-combination treatment steel basin outlet pipe; 5-ultrasonic/ozone oxidation groove; 51-ultrasonic/ozone oxidation reaction room outlet pipe; 52-ultrasonic amplitude transformer is popped one's head in; 53-ultrasonic transducer; 54-ultra-sonic generator; 6-deep wimble thickener; 61-deep wimble thickener inlet pipe; 611-enter pulp bin; 62-deep wimble thickener upper reaches drain pipe; 63-deep wimble thickener underflow outlet pipe; 64-harrow frame; 65-drive unit; 66-transmission shaft.
Embodiment
Refer to shown in Fig. 1 and Fig. 2, the utility model shell 1 is cuboid-type, below is provided with four castors 11, inside is provided with four baffle plates 12, shell 1 is divided into five chambers, be respectively teeter column 13 of sizing mixing, ozone oxidation reaction room 14, combination treatment room 15, ultrasonic/ozone oxidation reaction room 16 and the dense room 17 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, the upper lateral part of steel basin 2 near ozone oxidation reaction room 14 of sizing mixing is provided with steel basin outlet pipe 24 of sizing mixing, ozone oxidation reaction room 14 is a cuboid-type ozone oxidation reaction device 3, be provided with ozonation aerated supervisor 31, ozonation aerated arm 32 and ozone micro-hole aerator 33 bottom ozone oxidation reaction device 3, the upper lateral part of ozone oxidation reaction device 3 near combination treatment room 15 is provided with ozone oxidation reaction room outlet pipe 34, combination treatment room 15 is made up of two combination treatment steel basins 4 arranged side by side, combination treatment steel basin 4 is cylindrical structure, top is provided with heavy metal fixing agent chemical feed pipe 41, hydrogen peroxide chemical feed pipe 42 and stirs power set 23, stir below power set 23 and connect stirring rake 231, the upper lateral part of combination treatment room 15 near ultrasonic/ozone oxidation reaction room 16 is provided with combination treatment steel basin outlet pipe 43, ultrasonic/ozone oxidation reaction room 16 be cuboid-type ultrasonic/ozone oxidation groove 5, ultrasonic/ozone oxidation groove 5 inside is provided with ultrasonic amplitude transformer probe 52, ultrasonic amplitude transformer probe 52 is connected with the ultrasonic transducer 53 above ultrasonic/ozone oxidation groove 5, ultrasonic transducer 53 is connected with ultra-sonic generator 54, ozonation aerated supervisor 31 is provided with bottom ultrasonic/ozone oxidation groove 5, ozonation aerated arm 32 and ozone micro-hole aerator 33, the upper lateral part of ultrasonic/ozone oxidation groove 5 near the dense room 17 of dark cone is provided with ultrasonic/ozone oxidation reaction room outlet pipe 51, ultrasonic/ozone oxidation reaction room outlet pipe 51 with deeply bore dense room inlet pipe 61 and be connected, inside, dark cone dense room 17 is provided with a deep wimble thickener 6, deep wimble thickener 6 top of leaning to one side is provided with deep wimble thickener inlet pipe 61 and deep wimble thickener upper reaches drain pipe 62, the center upper portion of deep wimble thickener 6 is provided with into pulp bin 611, deep wimble thickener inlet pipe 61 with enter pulp bin 611 and be connected, bottom in deep wimble thickener 6 is provided with harrow frame 64, the upper center position of deep wimble thickener 6 is provided with drive unit 65, be connected with transmission shaft 66 below drive unit 65, bottom deep wimble thickener 6, be provided with deep wimble thickener underflow outlet pipe 63.
As shown in Figure 3, the end of ozonation aerated supervisor 31 is connected with ozonizer, 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, ultrasonic/ozone oxidation groove 5, ultrasonic amplitude transformer probe 52, 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.
Described ultrasonic/ozone oxidation groove 5 in ultrasonic amplitude transformer probe 52 diameter adjustable, ultrasonic amplitude transformer probe 52 quantity be more than or equal to one, be evenly distributed on below mineral syrup liquid 30mm place.
The utility model is when carrying out process containing cyanogen ore pulp, enter containing cyanogen ore pulp 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 ozone oxidation reaction room 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 combination treatment room 15, heavy metal fixing agent is added by heavy metal fixing agent chemical feed pipe 41, add hydrogen peroxide by hydrogen peroxide chemical feed pipe 42 to stir, ore pulp after stirring enters into ultrasonic/ozone oxidation reaction room 16, co-oxidation process is carried out under the Ultrasonic Conditions sent with ultrasonic amplitude transformer probe 52 under the ozone that ozone micro-hole aerator 33 bloats, ore pulp after oxide treatment enters into the dense room 17 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 63.
Claims (4)
1. a movable type is containing cyanogen slurry processing unit, 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 four baffle plates (12), shell (1) is divided into five chambers, be respectively teeter column of sizing mixing (13), ozone oxidation reaction room (14), combination treatment room (15), ultrasonic/ozone oxidation reaction room (16) and the dense room of dark cone (17), 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), the upper lateral part of steel basin (2) near ozone oxidation reaction room (14) of sizing mixing is provided with steel basin outlet pipe (24) of sizing mixing, ozone oxidation reaction room (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), and the upper lateral part of ozone oxidation reaction device (3) near combination treatment room (15) is provided with ozone oxidation reaction room outlet pipe (34), combination treatment room (15) is made up of two combination treatment steel basins (4) arranged side by side, combination treatment steel basin (4) is cylindrical structure, top is provided with heavy metal fixing agent chemical feed pipe (41), hydrogen peroxide chemical feed pipe (42) and stirs power set (23), stir power set (23) below and connect stirring rake (231), combination treatment room (15) upper lateral part near ultrasonic/ozone oxidation reaction room (16) is provided with combination treatment steel basin outlet pipe (43), ultrasonic/ozone oxidation reaction room (16) be cuboid-type ultrasonic/ozone oxidation groove (5), ultrasonic/ozone oxidation groove (5) inside is provided with ultrasonic amplitude transformer probe (52), ultrasonic amplitude transformer probe (52) is connected with the ultrasonic transducer (53) of ultrasonic/ozone oxidation groove (5) top, ultrasonic transducer (53) is connected with ultra-sonic generator (54), ultrasonic/ozone oxidation groove (5) bottom is provided with ozonation aerated supervisor (31), ozonation aerated arm (32) and ozone micro-hole aerator (33), ultrasonic/ozone oxidation groove (5) is provided with ultrasonic/ozone oxidation reaction room outlet pipe (51) near a upper lateral part of the dense room of dark cone (17), ultrasonic/ozone oxidation reaction room outlet pipe (51) with deeply bore dense room inlet pipe (61) and be connected, the dense room of dark cone (17) inside is provided with a deep wimble thickener (6), deep wimble thickener (6) top of leaning to one side is provided with deep wimble thickener inlet pipe (61) and deep wimble thickener upper reaches drain pipe (62), the center upper portion of deep wimble thickener (6) is provided with into pulp bin (611), deep wimble thickener inlet pipe (61) with enter pulp bin (611) and be connected, bottom in deep wimble thickener (6) is provided with harrow frame (64), the upper center position of deep wimble thickener (6) is provided with drive unit (65), drive unit (65) below is connected with transmission shaft (66), deep wimble thickener (6) bottom is provided with deep wimble thickener underflow outlet pipe (63).
2. according to claim 1 a kind of portable containing cyanogen slurry processing unit, 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. according to claim 1 a kind of portable containing cyanogen slurry processing unit, it is characterized in that: described ozone oxidation reaction device (3), ultrasonic/ozone oxidation groove (5), ultrasonic amplitude transformer probe (52), 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.
4. according to claim 1 a kind of portable containing cyanogen slurry processing unit, it is characterized in that: described ultrasonic/ozone oxidation groove (5) in ultrasonic amplitude transformer probe (52) diameter adjustable, the quantity of ultrasonic amplitude transformer probe (52) is more than or equal to one, is evenly distributed on below mineral syrup liquid 30mm place.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520678577.8U CN204939156U (en) | 2015-09-04 | 2015-09-04 | A kind of portable containing cyanogen slurry processing unit |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520678577.8U CN204939156U (en) | 2015-09-04 | 2015-09-04 | A kind of portable containing cyanogen slurry processing unit |
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| Publication Number | Publication Date |
|---|---|
| CN204939156U true CN204939156U (en) | 2016-01-06 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201520678577.8U Active CN204939156U (en) | 2015-09-04 | 2015-09-04 | A kind of portable containing cyanogen slurry processing unit |
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| CN (1) | CN204939156U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113354065A (en) * | 2021-06-18 | 2021-09-07 | 无锡普力环保科技有限公司 | AOP oxidation sewage treatment system |
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2015
- 2015-09-04 CN CN201520678577.8U patent/CN204939156U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113354065A (en) * | 2021-06-18 | 2021-09-07 | 无锡普力环保科技有限公司 | AOP oxidation sewage treatment system |
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| GR01 | Patent grant |