CN205949453U - Contain cyanogen waste residue integration treatment device - Google Patents
Contain cyanogen waste residue integration treatment device Download PDFInfo
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- CN205949453U CN205949453U CN201620786676.2U CN201620786676U CN205949453U CN 205949453 U CN205949453 U CN 205949453U CN 201620786676 U CN201620786676 U CN 201620786676U CN 205949453 U CN205949453 U CN 205949453U
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- oxidation reaction
- waste residue
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Abstract
The utility model discloses a contain cyanogen waste residue integration treatment device belongs to industry processing technique field useless admittedly. The utility model provides a still not have at present a problem to the facility including the advanced and mature processing of cyanogen waste residue. The utility model discloses a being sized mixing by one section room of sizing mixing, oxidizing reaction chamber, two -stage process, five cavities of room, hybrid processing room and filter pressing chamber constitute, five cavities accomplish in proper order add water size mixing, the oxidation of ozone aeration, acid reagent are sized mixing, the heavy metal is fixed and the whole process flow of filter -pressing, has realized containing the integration of cyanogen waste residue and has handled. The device not only can realize containing the innocent treatment of cyanogen waste residue, can realize the cyclic utilization of water resource in the ore pulp in addition, has advantages such as the processing speed is fast, the treatment effect good, the running cost is low, the construction investment is few, has wide application prospect.
Description
Technical field
This utility model is related to Industrial Solid Waste processing technology field, particularly to a kind of gold industry Solid state fermentation containing cyanogen dress
Put.
Background technology
Because the most of gold mine of China has been used up Cyanide Process, produce during golden production and contain in a large number
Cyanogen Tailings Slurry, these sludge containing cyanogenses are deposited in Tailings Dam in the way of dry row or wet row, with the expansion of golden production scale
The prolongation of big and production history, the accumulating amount containing cyanogen waste residue is increasing year by year, a large amount of soils of occupancy, and these waste residues are due to containing cyanogen
Compound and heavy metal, become the hazardous waste of gold mine enterprise generally existing, Tailings Dam Anti-seeping technology improper or safeguard
Management not in time when, in waste residue containing cyanogen, cyanide will ooze because drenching with rain down and produce pollution to surrounding enviroment and subsoil water, near
Resident cause health to cause huge threat, there is presently no the facility for the advanced and mature process of waste residue containing cyanogen, particularly
Integrated equipment for wastewater treatment.
Content of the invention
Provide the high integration of waste residue containing cyanogen of a kind of high treating effect, treatment effeciency for the problems referred to above this utility model
Processing meanss.
The technical scheme that this utility model is adopted is specific as follows：
The integrated treatment unit of waste residue containing cyanogen is sized mixing room 14, mixed by one section of room 12 of sizing mixing, oxidation reaction chamber 13, two-stage nitration successively
Close process chamber 15 and filter pressing room 16, totally five chambers, between connected and composed by pipeline.
Wherein one section room 12 of sizing mixing is made up of the multiple arranged side by side first agitator tanks 2 of sizing mixing, be provided with above agitator tank 2 of sizing mixing plus
Water pipe 21, feed pipe 22 and agitating device, the first agitator tank 2 of sizing mixing is provided with outlet near a upper lateral part of oxidation reaction chamber 13,
This outlet is connected with oxidation reaction chamber 13 by pipeline；
It is provided with ozone oxidation reaction groove 3, ozone oxidation reaction groove 3 bottom is provided with ozonation aerated supervisor in oxidation reaction chamber 13
31st, ozonation aerated arm 32 and several ozone micro-hole aerators 33, ozonation aerated supervisor 31 one end are connected with ozonator,
Ozonation aerated supervisor 31 other ends are communicated to each ozone micro-hole aerator 33 by ozonation aerated arm 32；Oxidation reaction chamber 13
It is provided with outlet near a size mixing upper lateral part of room 14 of two-stage nitration, this outlet is connected by pipeline and two-stage nitration room 14 of sizing mixing；
Two-stage nitration room 14 of sizing mixing is made up of the multiple arranged side by side second agitator tanks of sizing mixing, and second sizes mixing is provided with acidity above agitator tank
Reagent chemical feed pipe 42 and agitating device, the second upper lateral part near mixed processing room for the agitator tank of sizing mixing is provided with outlet, this outlet
It is connected with mixed processing room 15 by pipeline；
It is provided with mixed processing agitator tank 5 in mixed processing room 15, above mixed processing agitator tank 5, be provided with heavy metal fixative
Chemical feed pipe 52 and agitating device, a upper lateral part near filter pressing room for the mixed processing agitator tank 5 is provided with outlet, and pipeline is passed through in this outlet
It is connected with filter pressing room 16；
It is provided with filter press 6, filter press 6 top is provided with pressure filter pulp-inlet pipe 61 and pressure filtration mechanism in filter pressing room 16
62, pressure filter pulp-inlet pipe 61 is connected with the pipeline between mixed processing room 15 and grout outlet filter pressing room 16, pressure filtration mechanism 62 side
It is provided with sludge outlet 64, below pressure filtration mechanism 62, is provided with collecting tank 63, liquid collecting front of the slot is provided with drain pipe 65.
In ozone oxidation reaction groove 3, each ozonation aerated arm 32 is preferably equidistantly arranged in parallel, each ozonation aerated arm 32
On be equidistantly provided with ozone micro-hole aerator 33.
Described ozone oxidation reaction groove 3, ozonation aerated supervisor 31 and the preferred stainless steel of ozonation aerated arm 32, ozone
The material preferred 316L rustless steel of micro-hole aerator, titanium alloy or pottery.
The beneficial effects of the utility model：
This utility model provides a kind of integrated treatment unit of waste residue containing cyanogen, not only can realize harmless containing cyanogen waste residue
Change is processed, and can realize recycling of water resource in ore pulp, has that processing speed is fast, high treating effect, operating cost
The advantages of low, construction investment is few, has broad application prospects.
Brief description
Fig. 1 is the front view of this utility model structure.
Fig. 2 is the top view of this utility model structure.
Using labelling in the figures above：1 shell；11 baffle plates；12 1 sections of rooms of sizing mixing；13 oxidation reaction chambers；
14 two-stage nitration are sized mixing room；15 mixed processing rooms；16 filter pressing rooms；2 size mixing agitator tank；21 filler pipes；22 feed pipes；
23 stirring power devices；231 stirring paddles；24 1 sections of room grout outlets of sizing mixing；3 ozone oxidation reaction grooves；31 ozone
Aeration is responsible for；32 ozonation aerated arms；33 ozone micro-hole aerators；34 oxidation reaction chamber grout outlets；41 two-stage nitration are adjusted
Slurry room grout outlet；42 acid reagent chemical feed pipes；5 mixed processing agitator tanks；51 mixed processing room grout outlets；52 huge sum of moneys
Belong to fixative chemical feed pipe；6 filter press；61 filter pressing room pulp-inlet pipes；62 pressure filtration mechanisms；63 collecting tanks；64 filters
Slag exports；65 drain pipes.
Specific embodiment
Refer to shown in Fig. 1 and Fig. 2, this utility model shell 1 is cuboid-type, inside is provided with four baffle plates 11, will be outer
Shell 1 is divided into five chambers, sizes mixing room 14, mixed processing room 15 and pressure in respectively one section room 12 of sizing mixing, oxidation reaction chamber 13, two-stage nitration
Filter chamber 16, wherein one section room 12 of sizing mixing is made up of two arranged side by side agitator tanks 2 of sizing mixing, and agitator tank 2 of sizing mixing is cylindrical structure, on
Side is provided with filler pipe 21, pulp-inlet pipe 22 and stirring power device 23, and stirring power device 23 lower section connects stirring paddle 231, sizes mixing
Agitator tank 2 is provided with one section of room grout outlet 24 of sizing mixing near a upper lateral part of oxidation reaction chamber 13；Oxidation reaction chamber 13 is long for one
Cube type ozone oxidation reaction groove 3, ozone oxidation reaction groove 3 bottom is provided with ozonation aerated supervisor 31, ozonation aerated arm 32 and
Ozone micro-hole aerator 33, ozone oxidation reaction groove 3 is provided with oxidation reaction chamber pulp near a size mixing upper lateral part of room 14 of two-stage nitration
Pipe 34；Two-stage nitration room 14 of sizing mixing is made up of two arranged side by side agitator tanks 2 of sizing mixing, and agitator tank 2 of sizing mixing is cylindrical structure, and top is provided with
Acid reagent chemical feed pipe 42 and stirring power device 23, stirring power device 23 lower section connects stirring paddle 231, agitator tank 2 of sizing mixing
A upper lateral part near mixed processing room 15 is provided with two-stage nitration and sizes mixing room grout outlet 41；One cylinder of setting in mixed processing room 15
Mixed processing agitator tank 5, is provided with heavy metal fixative chemical feed pipe 52 and stirring power device 23 above mixed processing agitator tank 5,
Stirring power device 23 lower section connects stirring paddle 231, and a upper lateral part near filter pressing room 16 for the mixed processing agitator tank 5 is provided with mixing
Process chamber grout outlet 51；It is provided with a filter press 6, pressure filter 6 top is provided with pressure filter pulp-inlet pipe 61 He in filter pressing room 16
Pressure filtration mechanism 62, pressure filtration mechanism 62 side is provided with sludge outlet 64, is provided with collecting tank 63, before collecting tank 63 below pressure filtration mechanism 62
End is provided with drain pipe 65.
The end of described ozonation aerated supervisor 31 is connected with ozonator, and the front end of ozonation aerated supervisor 31 and ozone expose
Gas branch pipe 32 is connected, 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 groove 3, ozonation aerated supervisor 31 and ozonation aerated arm 32 are stainless steel, and ozone is micro-
The material of hole aerator 33 is 316L rustless steel, titanium alloy or pottery.
When carrying out processing waste residue containing cyanogen, waste residue containing cyanogen enters the tune of one section of room 12 of sizing mixing from feed pipe 22 to this utility model
In slurry agitator tank 2, add a certain amount of water from filler pipe 21 simultaneously, open stirring and carry out process of sizing mixing, the ore pulp after sizing mixing from
One section of room grout outlet 24 of sizing mixing enters in oxidation reaction chamber 13, is aoxidized under the ozone that ozone micro-hole aerator 33 bloats
Process, what the ore pulp after ozone Oxidation Treatment was flowed into that two-stage nitration sizes mixing room 14 sizes mixing in agitator tank 2, from acid reagent chemical feed pipe 42
A certain amount of acid reagent is added to adjust the pH value of ore pulp between 7～9, the ore pulp after sizing mixing is sized mixing room grout outlet 41 from two-stage nitration
Enter in the mixed processing agitator tank 5 in mixed processing room 15, add heavy metal solid by heavy metal fixative chemical feed pipe 52
Determine agent to be processed, the ore pulp after process enters in the filter press 6 of filter pressing room 16 and carries out filter pressing, and filtering residue is from sludge outlet
64 exit into slag field stores up, and filtrate exits back to size mixing agitator tank 2 from drain pipe 65.
Claims (3)
1. the integrated treatment unit of waste residue containing cyanogen is it is characterised in that this device is successively by one section of room of sizing mixing (12), oxidation reaction chamber
(13), two-stage nitration is sized mixing room (14), mixed processing room (15) and filter pressing room (16), totally five chambers, between structure is connected by pipeline
Become；
Wherein one section room of sizing mixing (12) is made up of the multiple arranged side by side first agitator tanks (2) of sizing mixing, and agitator tank of sizing mixing is provided with above (2)
Filler pipe (21), feed pipe (22) and agitating device, first size mixing agitator tank (2) near oxidation reaction chamber (13) a upper lateral part
It is provided with outlet, this outlet is connected with oxidation reaction chamber (13) by pipeline；
It is provided with ozone oxidation reaction groove (3), ozone oxidation reaction groove (3) bottom is provided with ozonation aerated master in oxidation reaction chamber (13)
Pipe (31), ozonation aerated arm (32) and several ozone micro-hole aerators (33), ozonation aerated supervisor (31) one end and ozone
Generator is connected, and ozonation aerated supervisor (31) other end is communicated to each ozone micro-hole aerator by ozonation aerated arm (32)
(33)；Oxidation reaction chamber (13) is provided with outlet near a size mixing upper lateral part of room (14) of two-stage nitration, and pipeline and two-stage nitration are passed through in this outlet
Size mixing room (14) connect；
Two-stage nitration room (14) of sizing mixing is made up of the multiple arranged side by side second agitator tanks of sizing mixing, and second sizes mixing is provided with acid examination above agitator tank
Agent chemical feed pipe (42) and agitating device, the second upper lateral part near mixed processing room for the agitator tank of sizing mixing is provided with outlet, this outlet
It is connected with mixed processing room (15) by pipeline；
It is provided with mixed processing agitator tank (5) in mixed processing room (15), be provided with heavy metal above mixed processing agitator tank (5) and fix
Agent chemical feed pipe (52) and agitating device, a upper lateral part near filter pressing room for the mixed processing agitator tank (5) is provided with outlet, and this outlet is led to
Piping is connected with filter pressing room (16)；
It is provided with filter press (6), filter press (6) top is provided with pressure filter pulp-inlet pipe (61) and filter pressing in filter pressing room (16)
Mechanism (62), pressure filter pulp-inlet pipe (61) is connected with the pipeline between mixed processing room (15) and grout outlet filter pressing room (16), pressure
Filter structure (62) side is provided with sludge outlet (64), is provided with collecting tank (63) below pressure filtration mechanism (62), and liquid collecting front of the slot is provided with
Drain pipe (65).
2. the integrated treatment unit of waste residue containing cyanogen according to claim 1 is it is characterised in that ozone oxidation reaction groove (3)
In each ozonation aerated arm (32) be equidistantly arranged in parallel, each ozonation aerated arm (32) is equidistantly provided with ozone micropore expose
Gas device (33).
3. the integrated treatment unit of waste residue containing cyanogen according to claim 1 and 2 is it is characterised in that described ozone oxidation is anti-
Groove (3), ozonation aerated supervisor (31) and ozonation aerated arm (32) is answered to be stainless steel, the material of ozone micro-hole aerator is excellent
Select 316L rustless steel, titanium alloy or pottery.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620786676.2U CN205949453U (en) | 2016-07-25 | 2016-07-25 | Contain cyanogen waste residue integration treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620786676.2U CN205949453U (en) | 2016-07-25 | 2016-07-25 | Contain cyanogen waste residue integration treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205949453U true CN205949453U (en) | 2017-02-15 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
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| CN201620786676.2U Active CN205949453U (en) | 2016-07-25 | 2016-07-25 | Contain cyanogen waste residue integration treatment device |
Country Status (1)
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| CN (1) | CN205949453U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111732223A (en) * | 2020-06-26 | 2020-10-02 | 长春黄金研究院有限公司 | Harmless treatment and backfill utilization method of high-arsenic cyanided tailings |
-
2016
- 2016-07-25 CN CN201620786676.2U patent/CN205949453U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111732223A (en) * | 2020-06-26 | 2020-10-02 | 长春黄金研究院有限公司 | Harmless treatment and backfill utilization method of high-arsenic cyanided tailings |
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