CN204817436U - Contain cyanogen waste residue recycling processed system - Google Patents
Contain cyanogen waste residue recycling processed system Download PDFInfo
- Publication number
- CN204817436U CN204817436U CN201520485199.1U CN201520485199U CN204817436U CN 204817436 U CN204817436 U CN 204817436U CN 201520485199 U CN201520485199 U CN 201520485199U CN 204817436 U CN204817436 U CN 204817436U
- Authority
- CN
- China
- Prior art keywords
- pipe
- level
- wimble thickener
- deep wimble
- rinsing maching
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/82—Recycling of waste of electrical or electronic equipment [WEEE]
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
The utility model discloses a contain cyanogen waste residue recycling processed system, it is by the screening machine, the batcher, the one -level washing machine, one -level deep -cone thickener, the second grade washing machine, second grade deep -cone thickener, the pressure filter, the sedimentation tank, the acidizing is blown and is taken off the groove and become with the oxidation bank of cells, wherein, the washing machine top is equipped with the filler pipe and the detergent adds the pencil, the acidizing is blown and is taken off the inslot and be equipped with with the acid tube, heating rod and aeration systems, oxidation groove upper end is equipped with the alkaline reagents and adds the pencil, the oxidant adds the pencil and the precipitating agent adds the pencil, oxidation inslot portion is equipped with agitating unit. The utility model discloses not only can realize containing the innocent treatment of cyanogen waste residue, can realize having the recovery of valence resource and the cyclic utilization of washing water resource in the waste residue moreover, have advantages such as the treatment effect is good, the treatment effeciency is high, system's operation is stable, the running cost is low, the construction investment is few, have wide application prospect.
Description
Technical field
The utility model relates to Industrial Solid Waste processing technology field, and particularly a kind of gold industry is containing cyanogen Solid state fermentation system.
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 cyanide and heavy metal, become the ubiquitous hazardous waste 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 cyanide 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 controlling waste residue aspect, the application of also administering containing the industrialization of cyanogen waste residue so far.
Summary of the invention
The purpose of this utility model is exactly for the problems referred to above, and provide that a kind for the treatment of effect is good, treatment effeciency is high containing cyanogen waste residue recovery and processing system.
The utility model is made up of screening machine, batcher, one-level rinsing maching, one-level deep wimble thickener, secondary rinsing maching, secondary deep wimble thickener, filter press, sedimentation basin, acidifying blow-off groove and oxidation trough, wherein be provided with charging aperture at the upper side of screening machine, sieve lower discharge port is provided with below opposite side, sieve lower discharge port is connected with the belt transmission system of batcher, be placed in above belt transmission system, screening machine inside is provided with screen cloth and electric device, batcher is made up of support and belt transmission system, and prop up and be placed on bottom belt transmission system, belt transmission system lower end is placed in below sifted lower discharge port, and upper end is placed in one-level rinsing maching charging aperture, one-level rinsing maching profile is cylindrical, one-level rinsing maching charging aperture, one-level rinsing maching filler pipe and washing agent chemical feed pipe is provided with above one-level rinsing maching, one-level rinsing maching is provided with one-level rinsing maching grout outlet bottom leaning to one side, one-level rinsing maching grout outlet is connected by Pulp pump with one-level deep wimble thickener pulp-inlet pipe, and one-level rinsing maching inside is provided with agitating device, the profile of one-level deep wimble thickener is the assembly of cylinder with cone, one-level deep wimble thickener top of leaning to one side is provided with one-level deep wimble thickener pulp-inlet pipe and one-level deep wimble thickener outlet pipe, one-level deep wimble thickener outlet pipe is connected with sedimentation basin water inlet pipe, the center upper portion of one-level deep wimble thickener is provided with into pulp bin, one-level deep wimble thickener pulp-inlet pipe with enter pulp bin and be connected, bottom in one-level deep wimble thickener is provided with harrow frame, the upper center position of one-level deep wimble thickener is provided with drive unit, be connected with power transmission shaft below drive unit, one-level deep wimble thickener underflow grout outlet is provided with bottom one-level deep wimble thickener, one-level deep wimble thickener underflow grout outlet is connected with secondary rinsing maching pulp-inlet pipe by Pulp pump, secondary rinsing maching profile is cylindrical, secondary rinsing maching is provided with secondary rinsing maching pulp-inlet pipe bottom leaning to one side, secondary rinsing maching top of leaning to one side is provided with secondary rinsing maching grout outlet, secondary rinsing maching grout outlet is connected by Pulp pump with secondary deep wimble thickener pulp-inlet pipe, be provided with secondary rinsing maching filler pipe and washing agent chemical feed pipe above secondary rinsing maching, secondary rinsing maching inside is provided with agitating device, the profile of secondary deep wimble thickener is the assembly of cylinder with cone, secondary deep wimble thickener top of leaning to one side is provided with secondary deep wimble thickener pulp-inlet pipe and secondary deep wimble thickener outlet pipe, secondary deep wimble thickener outlet pipe is connected with sedimentation basin water inlet pipe, the center upper portion of secondary deep wimble thickener is provided with into pulp bin, secondary deep wimble thickener pulp-inlet pipe with enter pulp bin and be connected, bottom in secondary deep wimble thickener is provided with harrow frame, the upper center position of secondary deep wimble thickener is provided with drive unit, be connected with power transmission shaft below drive unit, secondary deep wimble thickener underflow grout outlet is provided with bottom secondary deep wimble thickener, secondary deep wimble thickener underflow grout outlet is connected with filter press pulp-inlet pipe by Pulp pump, filter press is plate and frame filter press, and top is provided with filter press pulp-inlet pipe and press filteration system, is provided with collecting tank below press filteration system, and collecting tank front end is provided with drain pipe, and drain pipe is connected with sedimentation basin water inlet pipe, sedimentation basin is rectangle or round pool, sedimentation basin water inlet pipe and sedimentation basin drinking-water pipe is respectively equipped with in sedimentation basin, sedimentation basin water inlet pipe is connected with filter press drain pipe with one-level deep wimble thickener outlet pipe, secondary deep wimble thickener outlet pipe, and sedimentation basin drinking-water pipe is connected with acidifying blow-off groove feed tube by water pump, acidifying blow-off groove shell is cylindrical, top adopts hemispherical head sealing, acidifying blow-off groove top and the bottom of leaning to one side are respectively equipped with acidifying blow-off groove feed tube and acidifying blow-off groove drain pipe, acidifying blow-off groove drain pipe is connected with oxidation trough water inlet pipe by water pump, top in acidifying blow-off groove is provided with and adds acid tube, and middle part is provided with heating rod, and bottom is provided with aerating system, the top of acidifying blow-off groove is provided with escape pipe, and escape pipe end is connected with the micro-hole aerator of Alkali absorption trench bottom, Alkali absorption groove is leaned to one side as cylindrical, and bottom is conical, and NaOH absorbing liquid and absorption tower filler are equipped with in Alkali absorption groove inside, and bottom is provided with micro-hole aerator, oxidation trough is cylindrical tank diameter, oxidation trough upper and lower of leaning to one side is respectively equipped with oxidation trough water inlet pipe and oxidation trough outlet pipe, oxidation trough outlet pipe is connected by water pump with one-level rinsing maching filler pipe, oxidation trough upper end is provided with alkaline reagent chemical feed pipe, oxidant chemical feed pipe and precipitating reagent chemical feed pipe, and oxidation trough inside is provided with agitating device.
The circular array of described heating rod, in the inside of acidifying blow-off groove, is evenly distributed in same level.
Described absorption tower filler is the fillers such as Pall ring, cascade ring, arc saddle, square saddle.
Described aerating system is made up of blower fan, aeration tube, aeration branch pipe and micro-hole aerator, the end of aeration tube is connected with blower fan, the both sides, front end of aeration tube are equidistantly vertically provided with each aeration branch pipe, each aeration branch pipe is equidistantly provided with micro-hole aerator, and all micro-hole aerators are evenly distributed in the bottom in acidifying blow-off groove.
The beneficial effects of the utility model:
The utility model is to containing after twice washing of cyanogen waste residue and Separation of Solid and Liquid, the recovery of acidifying stripping and oxidation precipitation process are carried out to cleaning solution, not only can realize the harmless treatment containing cyanogen waste residue, and the recovery of valuable resource in waste residue and recycling of washings resource can be realized, there is the advantages such as process treatment effect is good, treatment effeciency is high, system run all right, operating cost are low, construction investment is few, have broad application prospects.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Fig. 2 is that schematic diagram laid by heating rod of the present utility model.
Fig. 3 is aeration tube of the present utility model, aeration branch pipe and micro-hole aerator structural representation.
Wherein, 1-screening machine; 11-screening machine charging aperture; 12-sieve lower discharge port; 13-screen cloth; 14-electric device; 2-batcher; 21-support; 22-belt transmission system; 3-one-level rinsing maching; 31-one-level rinsing maching charging aperture; 32-one-level rinsing maching grout outlet; 33-one-level rinsing maching filler pipe; 34-washing agent chemical feed pipe; 35-agitating device; 36-Pulp pump; 4-one-level deep wimble thickener; 41-one-level deep wimble thickener pulp-inlet pipe; 411-enter pulp bin; 42-one-level deep wimble thickener outlet pipe; 43-one-level deep wimble thickener underflow grout outlet; 44-harrow frame; 45-drive unit; 46-power transmission shaft; 5-secondary rinsing maching; 51-secondary rinsing maching pulp-inlet pipe; 52-secondary rinsing maching grout outlet; 53-secondary rinsing maching filler pipe; 6-secondary deep wimble thickener; 61-secondary deep wimble thickener pulp-inlet pipe; 62-secondary deep wimble thickener outlet pipe; 63-secondary deep wimble thickener underflow grout outlet; 7-filter press; 71-filter press pulp-inlet pipe; 72-press filteration system; 73-collecting tank; 74-drain pipe; 8-sedimentation basin; 81-sedimentation basin water inlet pipe; 82-sedimentation basin drinking-water pipe; 83-water pump; 9-acidifying blow-off groove; 91-acidifying blow-off groove feed tube; 92-acidifying blow-off groove drain pipe; 93-add acid tube; 94-heating rod; 95-aeration tube; 951-blower fan; 96-aeration branch pipe; 97-micro-hole aerator; 98-escape pipe; 99-Alkali absorption groove; 10-oxidation trough; 101-oxidation trough water inlet pipe; 102-oxidation trough outlet pipe; 103-alkaline reagent chemical feed pipe; 104-oxidant chemical feed pipe; 105-precipitating reagent chemical feed pipe.
Detailed description of the invention
Refer to shown in Fig. 1, the present embodiment is made up of screening machine 1, batcher 2, one-level rinsing maching 3, one-level deep wimble thickener 4, secondary rinsing maching 5, secondary deep wimble thickener 6, filter press 7, sedimentation basin 8, resin absorbing column 9 and oxidation trough 10, wherein be provided with charging aperture 11 at the upper side of screening machine 1, sieve lower discharge port 12 is provided with below opposite side, sieve lower discharge port 12 is connected with the belt transmission system 22 of batcher 2, be placed in above belt transmission system 22, screening machine 1 inside is provided with screen cloth 13 and electric device 14, batcher 2 is made up of support 21 and belt transmission system 22, and support 21 is placed in bottom belt transmission system 22, and belt transmission system 22 lower end is placed in screening machine 1 and sieves below lower discharge port 12, and upper end is placed in one-level rinsing maching charging aperture 31, one-level rinsing maching 3 profile is cylindrical, one-level rinsing maching charging aperture 31, one-level rinsing maching filler pipe 33 and washing agent chemical feed pipe 34 is provided with above one-level rinsing maching 3, one-level rinsing maching 3 is provided with one-level rinsing maching grout outlet 32 bottom leaning to one side, one-level rinsing maching grout outlet 32 is connected by Pulp pump 36 with one-level deep wimble thickener pulp-inlet pipe 41, and one-level rinsing maching 3 inside is provided with agitating device 35, the profile of one-level deep wimble thickener 4 is the assembly of cylinder with cone, one-level deep wimble thickener 4 top of leaning to one side is provided with one-level deep wimble thickener pulp-inlet pipe 41 and one-level deep wimble thickener outlet pipe 42, one-level deep wimble thickener outlet pipe 42 is connected with sedimentation basin water inlet pipe 81, the center upper portion of one-level deep wimble thickener 4 is provided with into pulp bin 411, one-level deep wimble thickener pulp-inlet pipe 41 with enter pulp bin 411 and be connected, bottom in one-level deep wimble thickener 4 is provided with harrow frame 44, the upper center position of one-level deep wimble thickener 4 is provided with drive unit 45, be connected with power transmission shaft 46 below drive unit 45, one-level deep wimble thickener underflow grout outlet 43 is provided with bottom one-level deep wimble thickener 4, one-level deep wimble thickener underflow grout outlet 43 is connected with secondary rinsing maching pulp-inlet pipe 51 by Pulp pump 36, secondary rinsing maching 5 profile is cylindrical, secondary rinsing maching 5 is provided with secondary rinsing maching pulp-inlet pipe 51 bottom leaning to one side, secondary rinsing maching 5 top of leaning to one side is provided with secondary rinsing maching grout outlet 52, secondary rinsing maching grout outlet 52 is connected by Pulp pump 36 with secondary deep wimble thickener pulp-inlet pipe 61, be provided with secondary rinsing maching filler pipe 53 and washing agent chemical feed pipe 34 above secondary rinsing maching 5, secondary rinsing maching 5 inside is provided with agitating device 35, the profile of secondary deep wimble thickener 6 is the assembly of cylinder with cone, secondary deep wimble thickener 6 top of leaning to one side is provided with secondary deep wimble thickener pulp-inlet pipe 61 and secondary deep wimble thickener outlet pipe 62, secondary deep wimble thickener outlet pipe 62 is connected with sedimentation basin water inlet pipe 81, the center upper portion of secondary deep wimble thickener 6 is provided with into pulp bin 411, secondary deep wimble thickener pulp-inlet pipe 61 with enter pulp bin 411 and be connected, bottom in secondary deep wimble thickener 6 is provided with harrow frame 44, the upper center position of secondary deep wimble thickener 6 is provided with drive unit 45, be connected with power transmission shaft 46 below drive unit 45, secondary deep wimble thickener underflow grout outlet 63 is provided with bottom secondary deep wimble thickener 6, secondary deep wimble thickener underflow grout outlet 63 is connected with filter press pulp-inlet pipe 71 by Pulp pump 36, filter press 7 is plate and frame filter press, and top is provided with filter press pulp-inlet pipe 71 and press filteration system 72, is provided with collecting tank 73 below press filteration system 72, and collecting tank 73 front end is provided with drain pipe 74, and drain pipe 74 is connected with sedimentation basin water inlet pipe 81, sedimentation basin 8 is rectangle or round pool, sedimentation basin water inlet pipe 81 and sedimentation basin drinking-water pipe 82 is respectively equipped with in sedimentation basin 8, sedimentation basin water inlet pipe 81 is connected with filter press drain pipe 74 with one-level deep wimble thickener outlet pipe 42, secondary deep wimble thickener outlet pipe 62, and sedimentation basin drinking-water pipe 82 is connected with acidifying blow-off groove feed tube 91 by water pump 83, acidifying blow-off groove 9 shell is cylindrical, top adopts hemispherical head sealing, acidifying blow-off groove 9 upper and lower of leaning to one side is respectively equipped with acidifying blow-off groove feed tube 91 and acidifying blow-off groove drain pipe 92, acidifying blow-off groove drain pipe 92 is connected with oxidation trough feed tube 101 by water pump 83, top in acidifying blow-off groove 9 is provided with and adds acid tube 93, middle part is provided with heating rod 94, bottom is provided with aerating system, the top of acidifying blow-off groove 9 is provided with escape pipe 98, and escape pipe 98 end is connected with the micro-hole aerator 97 bottom Alkali absorption groove 99, Alkali absorption groove 99 is leaned to one side as cylindrical, and bottom is conical, and NaOH absorbing liquid and absorption tower filler are equipped with in Alkali absorption groove 99 inside, and bottom is provided with micro-hole aerator 97, oxidation trough 10 is cylindrical tank diameter, oxidation trough 10 upper and lower of leaning to one side is respectively equipped with oxidation trough water inlet pipe 101 and oxidation trough outlet pipe 102, oxidation trough outlet pipe 102 is connected by water pump 83 with one-level rinsing maching filler pipe 33, oxidation trough 10 upper end is provided with alkaline reagent chemical feed pipe 103, oxidant chemical feed pipe 104 and precipitating reagent chemical feed pipe 105, and oxidation trough 10 inside is provided with agitating device 35.
As shown in Figure 2, the circular array of heating rod 94, in the inside of acidifying blow-off groove 9, is evenly distributed in same level.
Described absorption tower filler is the fillers such as Pall ring, cascade ring, arc saddle, square saddle.
As shown in Figure 3, aerating system is made up of blower fan 951, aeration tube 95, aeration branch pipe 96 and micro-hole aerator 97, the end of aeration tube 95 is connected with blower fan 951, the both sides, front end of aeration tube 95 are equidistantly vertically provided with each aeration branch pipe 96, each aeration branch pipe 96 is equidistantly provided with micro-hole aerator 97, and all micro-hole aerators 97 are evenly distributed in the bottom in acidifying blow-off groove 9.
The course of work of the present utility model:
The utility model is when carrying out process containing cyanogen waste residue, first sieve in screening machine 1 containing cyanogen waste residue, lower part of screen divide from sieve lower discharge port 13 enter into belt transmission system 22, be delivered in one-level rinsing maching 3 by belt transmission system 22, the water added by one-level rinsing maching filler pipe 33 and washing agent chemical feed pipe 34 and washing agent are washed ore pulp, ore pulp after washing enters into one-level deep wimble thickener 4 and carries out dense, upper reaches flows into sedimentation basin 8 from one-level deep wimble thickener outlet pipe 42, underflow pumps into secondary rinsing maching 5 from one-level deep wimble thickener underflow grout outlet 43 and carries out secondary washing, ore pulp after washing enters into secondary deep wimble thickener 6 and carries out dense, upper reaches flows into sedimentation basin 8 from secondary deep wimble thickener outlet pipe 62, underflow pumps into filter press 7 from secondary deep wimble thickener underflow grout outlet 63 and carries out press filtration, filter residue is delivered to slag field and stores up, filtrate enters into sedimentation basin 8, then by water pump 83 cleaning solution in sedimentation basin 8 and filtrate be pumped in acidifying blow-off groove 9 and carry out acidifying stripping, through adding between sulfuric acid adjustment pH to 2 ~ 3 in acid tube 93, heating rod is heated to 30 ~ 40 DEG C, under aerating system stripping bottom acidifying blow-off groove 9, cyanide in waste liquid by stripping out, enter in Alkali absorption groove 99 and absorbed by the NaOH in Alkali absorption groove, acid solution after stripping enters into oxidation trough 10, by alkaline reagent chemical feed pipe 103, the alkaline reagent that oxidant chemical feed pipe 104 and precipitating reagent chemical feed pipe 105 add, oxidant and precipitating reagent carry out pH adjustment to waste liquid, oxidation processes is carried out to amounts of residual contamination and precipitation process is fixed to the heavy metal of remnants, waste liquid after process is pumped in one-level rinsing maching filler pipe 33 by water pump 83 and washs waste residue.
Claims (3)
1. one kind contains cyanogen waste residue recovery and processing system, it is characterized in that: be by screening machine (1), batcher (2), one-level rinsing maching (3), one-level deep wimble thickener (4), secondary rinsing maching (5), secondary deep wimble thickener (6), filter press (7), sedimentation basin (8), resin absorbing column (9) and oxidation trough (10) composition, wherein screening machine (1) upper side is provided with charging aperture (11), sieve lower discharge port (12) is provided with below opposite side, sieve lower discharge port (12) is connected with the belt transmission system (22) of batcher (2), be placed in belt transmission system (22) top, screening machine (1) inside is provided with screen cloth (13) and electric device (14), batcher (2) is made up of support (21) and belt transmission system (22), support (21) is placed in belt transmission system (22) bottom, belt transmission system (22) lower end is placed in screening machine (1) sieve lower discharge port (12) below, and upper end is placed in one-level rinsing maching charging aperture (31), one-level rinsing maching (3) profile is cylindrical, one-level rinsing maching (3) top is provided with one-level rinsing maching charging aperture (31), one-level rinsing maching filler pipe (33) and washing agent chemical feed pipe (34), one-level rinsing maching (3) is provided with one-level rinsing maching grout outlet (32) bottom leaning to one side, one-level rinsing maching grout outlet (32) is connected by Pulp pump (36) with one-level deep wimble thickener pulp-inlet pipe (41), and one-level rinsing maching (3) inside is provided with agitating device (35), the profile of one-level deep wimble thickener (4) is the assembly of cylinder with cone, one-level deep wimble thickener (4) top of leaning to one side is provided with one-level deep wimble thickener pulp-inlet pipe (41) and one-level deep wimble thickener outlet pipe (42), one-level deep wimble thickener outlet pipe (42) is connected with sedimentation basin water inlet pipe (81), the center upper portion of one-level deep wimble thickener (4) is provided with into pulp bin (411), one-level deep wimble thickener pulp-inlet pipe (41) with enter pulp bin (411) and be connected, bottom in one-level deep wimble thickener (4) is provided with harrow frame (44), the upper center position of one-level deep wimble thickener (4) is provided with drive unit (45), drive unit (45) below is connected with power transmission shaft (46), one-level deep wimble thickener (4) bottom is provided with one-level deep wimble thickener underflow grout outlet (43), one-level deep wimble thickener underflow grout outlet (43) is connected with secondary rinsing maching pulp-inlet pipe (51) by Pulp pump (36), secondary rinsing maching (5) profile is cylindrical, secondary rinsing maching (5) is provided with secondary rinsing maching pulp-inlet pipe (51) bottom leaning to one side, secondary rinsing maching (5) top of leaning to one side is provided with secondary rinsing maching grout outlet (52), secondary rinsing maching grout outlet (52) is connected by Pulp pump (36) with secondary deep wimble thickener pulp-inlet pipe (61), secondary rinsing maching (5) top is provided with secondary rinsing maching filler pipe (53) and washing agent chemical feed pipe (34), and secondary rinsing maching (5) inside is provided with agitating device (35), the profile of secondary deep wimble thickener (6) is the assembly of cylinder with cone, secondary deep wimble thickener (6) top of leaning to one side is provided with secondary deep wimble thickener pulp-inlet pipe (61) and secondary deep wimble thickener outlet pipe (62), secondary deep wimble thickener outlet pipe (62) is connected with sedimentation basin water inlet pipe (81), the center upper portion of secondary deep wimble thickener (6) is provided with into pulp bin (411), secondary deep wimble thickener pulp-inlet pipe (61) with enter pulp bin (411) and be connected, bottom in secondary deep wimble thickener (6) is provided with harrow frame (44), the upper center position of secondary deep wimble thickener (6) is provided with drive unit (45), drive unit (45) below is connected with power transmission shaft (46), secondary deep wimble thickener (6) bottom is provided with secondary deep wimble thickener underflow grout outlet (63), secondary deep wimble thickener underflow grout outlet (63) is connected with filter press pulp-inlet pipe (71) by Pulp pump (36), filter press (7) is plate and frame filter press, top is provided with filter press pulp-inlet pipe (71) and press filteration system (72), press filteration system (72) below is provided with collecting tank (73), collecting tank (73) front end is provided with drain pipe (74), and drain pipe (74) is connected with sedimentation basin water inlet pipe (81), sedimentation basin (8) is rectangle or round pool, sedimentation basin water inlet pipe (81) and sedimentation basin drinking-water pipe (82) is respectively equipped with in sedimentation basin (8), sedimentation basin water inlet pipe (81) is connected with filter press drain pipe (74) with one-level deep wimble thickener outlet pipe (42), secondary deep wimble thickener outlet pipe (62), and sedimentation basin drinking-water pipe (82) is connected with acidifying blow-off groove feed tube (91) by water pump (83), acidifying blow-off groove (9) shell is cylindrical, top adopts hemispherical head sealing, acidifying blow-off groove (9) upper and lower of leaning to one side is respectively equipped with acidifying blow-off groove feed tube (91) and acidifying blow-off groove drain pipe (92), acidifying blow-off groove drain pipe (92) is connected with oxidation trough feed tube (101) by water pump (83), top in acidifying blow-off groove (9) is provided with and adds acid tube (93), middle part is provided with heating rod (94), bottom is provided with aerating system, the top of acidifying blow-off groove (9) is provided with escape pipe (98), escape pipe (98) end is connected with the micro-hole aerator (97) of Alkali absorption groove (99) bottom, Alkali absorption groove (99) is leaned to one side as cylindrical, and bottom is conical, and NaOH absorbing liquid and absorption tower filler are equipped with in Alkali absorption groove (99) inside, and bottom is provided with micro-hole aerator (97), oxidation trough (10) is cylindrical tank diameter, oxidation trough (10) upper and lower of leaning to one side is respectively equipped with oxidation trough water inlet pipe (101) and oxidation trough outlet pipe (102), oxidation trough outlet pipe (102) is connected by water pump (83) with one-level rinsing maching filler pipe (33), oxidation trough (10) upper end is provided with alkaline reagent chemical feed pipe (103), oxidant chemical feed pipe (104) and precipitating reagent chemical feed pipe (105), and oxidation trough (10) inside is provided with agitating device (35).
2. one according to claim 1 is containing cyanogen waste residue recovery and processing system, it is characterized in that: described heating rod (94) circular array, in the inside of acidifying blow-off groove (9), is evenly distributed in same level.
3. one according to claim 1 is containing cyanogen waste residue recovery and processing system, it is characterized in that: described aerating system is by blower fan (951), aeration tube (95), aeration branch pipe (96) and micro-hole aerator (97) composition, the end of aeration tube (95) is connected with blower fan (951), the both sides, front end of aeration tube (95) are equidistantly vertically provided with each aeration branch pipe (96), each aeration branch pipe (96) is equidistantly provided with micro-hole aerator (97), all micro-hole aerators (97) are evenly distributed in the bottom in acidifying blow-off groove (9).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520485199.1U CN204817436U (en) | 2015-07-08 | 2015-07-08 | Contain cyanogen waste residue recycling processed system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201520485199.1U CN204817436U (en) | 2015-07-08 | 2015-07-08 | Contain cyanogen waste residue recycling processed system |
Publications (1)
Publication Number | Publication Date |
---|---|
CN204817436U true CN204817436U (en) | 2015-12-02 |
Family
ID=54675078
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201520485199.1U Active CN204817436U (en) | 2015-07-08 | 2015-07-08 | Contain cyanogen waste residue recycling processed system |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN204817436U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110902894A (en) * | 2019-12-16 | 2020-03-24 | 广州市真爱环保科技有限公司 | Cyanide-containing wastewater treatment system and method |
-
2015
- 2015-07-08 CN CN201520485199.1U patent/CN204817436U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110902894A (en) * | 2019-12-16 | 2020-03-24 | 广州市真爱环保科技有限公司 | Cyanide-containing wastewater treatment system and method |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN207210130U (en) | One kind spraying wastewater treatment circulation recycling system | |
CN205133262U (en) | Water purification treatment device | |
CN204700030U (en) | A kind of containing cyanogen waste residue total system | |
CN204817436U (en) | Contain cyanogen waste residue recycling processed system | |
CN204769846U (en) | Contain cyanogen waste residue recycling processed system | |
CN204918227U (en) | It synthesizes processing system to contain cyanogen mine tailings | |
CN104086011A (en) | Zero discharge process suitable for waste water of viscose fiber industrial acid station | |
CN204700029U (en) | A kind of containing cyanogen Solid state fermentation system | |
CN204735530U (en) | Contain cyanogen mine tailings processing system | |
CN203540183U (en) | Dyeing wastewater fiber treatment system | |
CN206680550U (en) | Heavy metal waste recovery soaks reactor with alkali | |
CN205949455U (en) | Contain cyanogen waste residue processing system | |
CN204910590U (en) | Contain cyanogen waste residue processing system | |
CN205023995U (en) | Portable cyanogen ore pulp processing apparatus that contains | |
CN204918229U (en) | Contain cyanogen ore pulp treatment system | |
CN205949454U (en) | Contain cyanogen waste slag recycling processing system | |
CN204939137U (en) | A kind of portable cyaniding tailing slurry treatment system | |
CN208995320U (en) | Environment friendly washing Intergration system | |
CN204939156U (en) | A kind of portable containing cyanogen slurry processing unit | |
CN204897569U (en) | It synthesizes processing system to contain cyanogen ore pulp | |
CN204934190U (en) | A kind of containing cyanogen waste residue integrated processing system | |
CN205821051U (en) | Rhodanate recovery and processing system in a kind of sludge containing cyanogens | |
CN204918245U (en) | Portable cyanogen ore pulp processing system that contains | |
CN205391938U (en) | Organic solvent waste water recycling device | |
CN204932696U (en) | A kind of portable containing cyanogen Solid state fermentation system |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant |