CN205023995U - Portable cyanogen ore pulp processing apparatus that contains - Google Patents
Portable cyanogen ore pulp processing apparatus that contains Download PDFInfo
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- CN205023995U CN205023995U CN201520705289.7U CN201520705289U CN205023995U CN 205023995 U CN205023995 U CN 205023995U CN 201520705289 U CN201520705289 U CN 201520705289U CN 205023995 U CN205023995 U CN 205023995U
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- CN
- China
- Prior art keywords
- sizing mixing
- room
- wimble thickener
- deep wimble
- oxidation reaction
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- JMANVNJQNLATNU-UHFFFAOYSA-N oxalonitrile Chemical compound N#CC#N JMANVNJQNLATNU-UHFFFAOYSA-N 0.000 title claims abstract description 34
- 238000004513 sizing Methods 0.000 claims abstract description 52
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims abstract description 27
- 239000012445 acidic reagent Substances 0.000 claims abstract description 12
- 238000005276 aerator Methods 0.000 claims abstract description 12
- 229910001385 heavy metal Inorganic materials 0.000 claims abstract description 8
- 239000002562 thickening agent Substances 0.000 claims description 39
- 229910000831 Steel Inorganic materials 0.000 claims description 32
- 239000010959 steel Substances 0.000 claims description 32
- 238000011284 combination treatment Methods 0.000 claims description 29
- 238000007254 oxidation reaction Methods 0.000 claims description 29
- 238000006385 ozonation reaction Methods 0.000 claims description 29
- 238000003756 stirring Methods 0.000 claims description 29
- 239000000126 substance Substances 0.000 claims description 14
- 239000002002 slurry Substances 0.000 claims description 7
- 239000003795 chemical substances by application Substances 0.000 claims description 6
- 239000010935 stainless steel Substances 0.000 claims description 6
- 229910001220 stainless steel Inorganic materials 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 4
- 235000004443 Ricinus communis Nutrition 0.000 claims description 3
- 240000000528 Ricinus communis Species 0.000 claims description 3
- 229910001069 Ti alloy Inorganic materials 0.000 claims description 3
- 230000005540 biological transmission Effects 0.000 claims description 3
- 238000011282 treatment Methods 0.000 abstract description 8
- 238000000034 method Methods 0.000 abstract description 7
- 230000000694 effects Effects 0.000 abstract description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 3
- 238000010276 construction Methods 0.000 abstract description 2
- 238000005273 aeration Methods 0.000 abstract 2
- 230000001590 oxidative effect Effects 0.000 abstract 2
- 239000000834 fixative Substances 0.000 abstract 1
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 4
- 239000002699 waste material Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 3
- 239000010931 gold Substances 0.000 description 3
- 229910052737 gold Inorganic materials 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 239000010802 sludge Substances 0.000 description 3
- 238000004064 recycling Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000002920 hazardous waste Substances 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Landscapes
- Paper (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Abstract
The utility model discloses a portable cyanogen ore pulp processing apparatus that contains, it is by one section room of sizing mixing, oxidizing reaction chamber, the two -stage process room of sizing mixing, hybrid processing room and bore dense room deeply and constitute, one of them section is sized mixing room and the two -stage process room of sizing mixing and comprises two stirred tanks of sizing mixing that parallel respectively, it is equipped with acid reagent and adds the pencil to size mixing stirred tank top, oxidizing reaction chamber's bottom is equipped with ozone aeration main pipe, ozone aeration main pipe and ozone microporous aerator, the indoor portion of hybrid processing is equipped with a hybrid processing stirred tank, hybrid processing stirred tank top is equipped with the heavy metal fixative and adds the pencil. The utility model provides a portable cyanogen ore pulp processing apparatus that contains not only can realize containing the innocent treatment of cyanogen ore pulp, can realize the recycle 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.
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.
Shell of the present utility model is cuboid-type, below is provided with four castors, inside is provided with four baffle plates, shell is divided into five chambers, be respectively one section of room of sizing mixing, oxidation reaction chamber, two sections of rooms of sizing mixing, combination treatment room and the dense rooms of dark cone, wherein one section of room of 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 one section of room outlet pipe of sizing mixing near a upper lateral part of oxidation reaction chamber; Oxidation reaction chamber is a cuboid-type ozone oxidation reaction groove, ozone oxidation reaction trench bottom is provided with ozonation aerated supervisor, ozonation aerated arm and ozone micro-hole aerator, and the upper lateral part of ozone oxidation reaction groove near two sections of rooms of sizing mixing is provided with oxidation reaction chamber outlet pipe; Two sections of rooms of sizing mixing are 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 and stirs power set, stir below power set and connect stirring rake, the upper lateral part of steel basin near combination treatment room of sizing mixing is provided with two sections of room outlet pipes of sizing mixing; Combination treatment indoor arrange a cylindrical combination treatment steel basin, be provided with heavy metal fixing agent chemical feed pipe above combination treatment steel basin and stir power set, stir below power set and connect stirring rake, the upper lateral part of combination treatment steel basin near the dense room of dark cone is provided with combination treatment room outlet 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, deep wimble thickener inlet pipe is connected with combination treatment room outlet 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, be connected with transmission shaft below drive unit, bottom deep wimble thickener, be provided with deep wimble thickener underflow outlet pipe.
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 groove, 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.
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.
Wherein, 1-shell; 11-castor; 12-baffle plate; 13-one section of room of sizing mixing; 14-oxidation reaction chamber; 15-two sections of rooms of sizing mixing; 16-combination treatment 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-one section of room outlet pipe of sizing mixing; 3-ozone oxidation reaction groove; 31-ozonation aerated supervisor; 32-ozonation aerated arm; 33-ozone micro-hole aerator; 34-oxidation reaction chamber outlet pipe; 41-two sections of room outlet pipes of sizing mixing; 5-combination treatment steel basin; 51-combination treatment room outlet pipe; 52-heavy metal fixing agent chemical feed pipe; 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, shell 1 of the present utility model 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 one section of room 13 of sizing mixing, oxidation reaction chamber 14, two sections of rooms 15 of sizing mixing, combination treatment room 16 and the dense room 17 of dark cone, wherein one section of room 13 of 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 one section of room outlet pipe 24 of sizing mixing near a upper lateral part of oxidation reaction chamber 14, oxidation reaction chamber 14 is a cuboid-type ozone oxidation reaction groove 3, be provided with ozonation aerated supervisor 31, ozonation aerated arm 32 and ozone micro-hole aerator 33 bottom ozone oxidation reaction groove 3, the upper lateral part of ozone oxidation reaction groove 3 near two sections of rooms 15 of sizing mixing is provided with oxidation reaction chamber outlet pipe 34, two sections of rooms 15 of sizing mixing are 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 and stirs power set 23, stir below power set 23 and connect stirring rake 231, the upper lateral part of steel basin 2 near combination treatment room 16 of sizing mixing is provided with two sections of room outlet pipes 41 of sizing mixing, a cylindrical combination treatment steel basin 5 is set in combination treatment room 16, be provided with heavy metal fixing agent chemical feed pipe 52 above combination treatment steel basin 5 and stir power set 23, stir below power set 23 and connect stirring rake 231, the upper lateral part of combination treatment steel basin 5 near the dense room 17 of dark cone is provided with combination treatment room outlet pipe 51, 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, deep wimble thickener inlet pipe 61 is connected with combination treatment room outlet pipe 51, 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, deep wimble thickener underflow outlet pipe 63 is provided with bottom deep wimble thickener 6.
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 groove 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.
The utility model is when carrying out process containing cyanogen ore pulp, size mixing steel basin 2 containing cyanogen ore pulp from what enter that oar pipe 22 enters one section of room 13 of sizing mixing, adding a certain amount of acid reagent from acid reagent chemical feed pipe 21 regulates between pH value to 9 ~ 11 of ore pulp, ore pulp after sizing mixing enters into oxidation reaction chamber 14 from one section of room outlet pipe 24 of sizing mixing, oxide treatment is carried out under the ozone that ozone micro-hole aerator 33 bloats, what the ore pulp after ozone Oxidation Treatment flow into two sections of rooms 15 of sizing mixing sizes mixing in steel basin 2, adding a certain amount of acid reagent from acid reagent chemical feed pipe 21 regulates between pH value to 7 ~ 9 of ore pulp, ore pulp after sizing mixing enters into the combination treatment steel basin 5 of combination treatment room 16 from two sections of room outlet pipes 41 of sizing mixing, add heavy metal fixing agent by heavy metal fixing agent chemical feed pipe 52 to process, the deep wimble thickener 6 that ore pulp after process enters into the dense room 17 of dark cone 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 (3)
1. a movable type is containing cyanogen slurry processing unit, it is characterized in that: 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 one section of room of sizing mixing (13), oxidation reaction chamber (14), two sections of rooms of sizing mixing (15), combination treatment room (16) and the dense room of dark cone (17), wherein one section of room of sizing mixing (13) 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 one section of room outlet pipe (24) of sizing mixing near a upper lateral part of oxidation reaction chamber (14), oxidation reaction chamber (14) is a cuboid-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), and ozone oxidation reaction groove (3) is provided with oxidation reaction chamber outlet pipe (34) near a upper lateral part of two sections of rooms of sizing mixing (15), two sections of rooms of sizing mixing (15) are 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) and stirs power set (23), stir power set (23) below and connect stirring rake (231), the upper lateral part of steel basin of sizing mixing (2) near combination treatment room (16) is provided with two sections of room outlet pipes (41) of sizing mixing, a cylindrical combination treatment steel basin (5) is set in combination treatment room (16), combination treatment steel basin (5) top is provided with heavy metal fixing agent chemical feed pipe (52) and stirs power set (23), stir power set (23) below and connect stirring rake (231), combination treatment steel basin (5) is provided with combination treatment room outlet pipe (51) near a upper lateral part of the dense room of dark cone (17), 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), deep wimble thickener inlet pipe (61) is connected with combination treatment room outlet pipe (51), 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. movable type according to claim 1 is 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. movable type according to claim 1 is containing cyanogen slurry processing unit, it is characterized in that: described ozone oxidation reaction groove (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.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520705289.7U CN205023995U (en) | 2015-09-12 | 2015-09-12 | Portable cyanogen ore pulp processing apparatus that contains |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520705289.7U CN205023995U (en) | 2015-09-12 | 2015-09-12 | Portable cyanogen ore pulp processing apparatus that contains |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205023995U true CN205023995U (en) | 2016-02-10 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520705289.7U Active CN205023995U (en) | 2015-09-12 | 2015-09-12 | Portable cyanogen ore pulp processing apparatus that contains |
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| CN (1) | CN205023995U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109908825A (en) * | 2019-04-23 | 2019-06-21 | 陕西科技大学 | A kind of slurry stirring device and stirring method thereof |
-
2015
- 2015-09-12 CN CN201520705289.7U patent/CN205023995U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109908825A (en) * | 2019-04-23 | 2019-06-21 | 陕西科技大学 | A kind of slurry stirring device and stirring method thereof |
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| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |