CN214032063U - Full-automatic electro-oxidation flocculation dye liquor recycling system - Google Patents
Full-automatic electro-oxidation flocculation dye liquor recycling system Download PDFInfo
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- CN214032063U CN214032063U CN202022579592.0U CN202022579592U CN214032063U CN 214032063 U CN214032063 U CN 214032063U CN 202022579592 U CN202022579592 U CN 202022579592U CN 214032063 U CN214032063 U CN 214032063U
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- 238000005189 flocculation Methods 0.000 title claims abstract description 54
- 230000016615 flocculation Effects 0.000 title claims abstract description 54
- 238000006056 electrooxidation reaction Methods 0.000 title claims abstract description 51
- 238000004064 recycling Methods 0.000 title claims description 41
- 239000012752 auxiliary agent Substances 0.000 claims abstract description 217
- 238000001914 filtration Methods 0.000 claims abstract description 135
- 238000003756 stirring Methods 0.000 claims abstract description 67
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 51
- 239000010865 sewage Substances 0.000 claims abstract description 40
- 238000011084 recovery Methods 0.000 claims abstract description 13
- 238000003860 storage Methods 0.000 claims description 14
- 238000007599 discharging Methods 0.000 claims description 11
- 238000011001 backwashing Methods 0.000 claims description 9
- 238000004140 cleaning Methods 0.000 claims description 4
- 239000000654 additive Substances 0.000 claims 1
- 230000000996 additive effect Effects 0.000 claims 1
- 239000004753 textile Substances 0.000 abstract description 7
- 238000004519 manufacturing process Methods 0.000 abstract description 4
- 239000003814 drug Substances 0.000 abstract description 3
- 239000004744 fabric Substances 0.000 abstract description 3
- 238000001514 detection method Methods 0.000 abstract description 2
- 230000005611 electricity Effects 0.000 abstract description 2
- 238000012544 monitoring process Methods 0.000 abstract description 2
- 238000005406 washing Methods 0.000 abstract description 2
- 239000000975 dye Substances 0.000 description 42
- 238000004043 dyeing Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 238000012545 processing Methods 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 238000009941 weaving Methods 0.000 description 3
- 239000002671 adjuvant Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 230000010354 integration Effects 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000004094 surface-active agent Substances 0.000 description 2
- 238000000108 ultra-filtration Methods 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 210000004209 hair Anatomy 0.000 description 1
- 239000010842 industrial wastewater Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 150000002632 lipids Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 229920002401 polyacrylamide Polymers 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 210000002268 wool Anatomy 0.000 description 1
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Abstract
The utility model discloses a full-automatic electrooxidation flocculation dye liquor circulation recovery system belongs to textile fabric production technical field, including electrooxidation flocculation dye liquor circulation recovery system body, agitator, filtration system assembly, row's clear water mouth, control box, agitator sewage inlet, auxiliary agent system assembly and PLC controller, the PLC controller is connected with filtration system assembly, control box and auxiliary agent system assembly electricity respectively. The utility model discloses a full-automatic electrooxidation flocculation dye liquor circulation recovery system, compact structure, degree of automation height, equipment commonality are strong, the play water quality is high. The utility model discloses a full-automatic electrooxidation flocculation dye liquor circulation recovery system can realize automatic feed, stirring, add medicine, filtration, automatic washing, accomplish water detection, on-line monitoring etc. automatically.
Description
Technical Field
The utility model relates to a full-automatic electrooxidation flocculation dye liquor recycling system belongs to textile fabric production technical field.
Background
China is a large country for textile production, annual water consumption of textile industry is in the forefront of all industrial industries, and the water consumption for dyeing accounts for 80 percent.
In the traditional dyeing industry, water is used as a medium to dye fabrics, and a large amount of chemical pollutants are contained in a water body due to the incompleteness of water phase reaction.
The difficulty of the wastewater treatment technology is high, the investment is large, and the bottleneck which troubles the sustainable development of the textile industry is formed, so that how to reduce the dyeing water and zero discharge of sewage is the future trend.
The textile industry sewage contains oil, lipid and cellulose eluted from cotton, wool and textiles, and various sizing agents, dyes, surfactants, auxiliaries and the like which are added in the processing process, so the components of the sewage are complex, the sewage is characterized by high organic matter concentration, deep and variable chromaticity, large change of pH value, large change of water quantity and water quality and the like, the sewage belongs to industrial waste water which is difficult to treat, and the traditional waste water treatment process is seriously challenged.
The patent name that 16 discloses in 2014 4 is "a weaving sewage treatment system", chinese utility model patent that patent application number is CN201320587985.3 discloses a weaving sewage treatment system, including sewage intake pond and sewage outlet basin, the sewage intake pond with be equipped with in proper order between the sewage outlet basin and drag for hair machine pond, equalizing basin, one-level materialization processing pond, biochemical treatment pond, decoloration processing pond. The disadvantages are that: the whole system has large floor area, discrete and unconcentrated devices, low automation degree, difficult recycling of treated clean water and the like.
Therefore, the full-automatic electro-oxidation flocculation dye liquor recycling system which is compact in structure, high in automation degree, strong in equipment universality and high in water outlet quality is provided, and the technical problem which needs to be solved urgently in the technical field is solved.
SUMMERY OF THE UTILITY MODEL
The utility model aims at solving the problems in the prior art and providing a full-automatic electro-oxidation flocculation dye liquor recycling system with compact structure, high automation degree, strong equipment universality and high water outlet quality.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
a full-automatic electro-oxidation flocculation dye liquor recycling system comprises an electro-oxidation flocculation dye liquor recycling system body, a stirring barrel, a filtering system assembly, a clear water discharging port, an operation box, a stirring barrel sewage inlet port and an auxiliary agent system assembly; the stirring barrel is positioned in the middle of the electrooxidation flocculation dye liquor recycling system body, the filtering system assembly is positioned on the right side of the electrooxidation flocculation dye liquor recycling system body, the auxiliary agent system assembly is positioned on the left side of the electrooxidation flocculation dye liquor recycling system body, the operation box is positioned on the front side of the electrooxidation flocculation dye liquor recycling system body, the clear water discharging port is positioned below the filtering system assembly, and the sewage inlet of the stirring barrel is positioned below the stirring barrel; the sewage inlet of the stirring barrel is connected with an auxiliary agent pump in the auxiliary agent system assembly through a pipeline; the clear water discharging port is connected with the clear water storage tank through a pipeline;
the auxiliary system assembly comprises: the auxiliary agent box comprises an auxiliary agent box A, an auxiliary agent box B, an auxiliary agent box C, an auxiliary agent box D, an auxiliary agent box A electromagnetic valve, an auxiliary agent box B electromagnetic valve, an auxiliary agent box C electromagnetic valve, an auxiliary agent box D electromagnetic valve, an auxiliary agent pump A, an auxiliary agent pump B, an auxiliary agent pump C and an auxiliary agent pump D; an electromagnetic valve of an auxiliary agent box A is fixed on the auxiliary agent box A, one end of an auxiliary agent pump A is connected with the auxiliary agent box A through the electromagnetic valve of the auxiliary agent box A, and the other end of the auxiliary agent pump A is connected with the stirring barrel; an electromagnetic valve of the auxiliary agent box B is fixed on the auxiliary agent box B, one end of an auxiliary agent pump B is connected with the auxiliary agent box B through the electromagnetic valve of the auxiliary agent box B, and the other end of the auxiliary agent pump B is connected with the stirring barrel; an electromagnetic valve of an auxiliary agent box C is fixed on the auxiliary agent box C, one end of an auxiliary agent pump C is connected with the auxiliary agent box C through the electromagnetic valve of the auxiliary agent box C, and the other end of the auxiliary agent pump C is connected with the stirring barrel; an electromagnetic valve of an auxiliary agent box D is fixed on the auxiliary agent box D, one end of an auxiliary agent pump D is connected with the auxiliary agent box D through the electromagnetic valve of the auxiliary agent box D, and the other end of the auxiliary agent pump D is connected with the stirring barrel; the operation box is connected with the master control operation platform and is connected with an auxiliary agent box A electromagnetic valve, an auxiliary agent box B electromagnetic valve, an auxiliary agent box C electromagnetic valve, an auxiliary agent box D electromagnetic valve, an auxiliary agent pump A, an auxiliary agent pump B, an auxiliary agent pump C and an auxiliary agent pump D in the auxiliary agent system; the filter system is connected with a filter electric control box, a deslagging motor, a first filter pneumatic valve, a second filter pneumatic valve, a third filter pneumatic valve, a filter pump, a fourth filter pneumatic valve, a fifth filter pneumatic valve and a sixth filter pneumatic valve in the filter system;
the filtration system assembly includes: the device comprises a filtering electric cabinet, an ultramicro filter barrel, a deslagging motor, a first filtering pneumatic valve, a residue barrel, a backwashing water storage tank, a second filtering pneumatic valve, a third filtering pneumatic valve, a filtering pump, a fourth filtering pneumatic valve, a fifth filtering pneumatic valve and a sixth filtering pneumatic valve; the filtering electric control box is positioned at the upper part of the filtering system body and is connected with each pump and the pneumatic valve, the filtering third pneumatic valve, the filtering pump, the filtering fourth pneumatic valve, the filtering fifth pneumatic valve and the filtering sixth pneumatic valve are positioned at the bottom of the filtering system body and are connected with each other through a pipeline, the filtering third pneumatic valve is connected with the backwashing water storage tank through a pipeline and a filtering second pneumatic valve, the residue barrel is positioned at the middle part of the filtering system body and is connected with the residue removing motor and the ultramicro filtering barrel through the filtering first pneumatic valve, and the ultramicro filtering barrel is respectively connected with the filtering fourth pneumatic valve, the filtering fifth pneumatic valve and the filtering sixth pneumatic valve through pipelines;
the electric oxidation flocculation dye liquor recycling system further comprises a PLC controller which is electrically connected with the filtering system assembly, the operation box and the auxiliary agent system assembly respectively.
Preferably, the operation box is electrically connected with a filtering electric control box, an ultramicro filtering barrel, a deslagging motor, a filtering first pneumatic valve, a filtering second pneumatic valve, a filtering third pneumatic valve, a filtering pump, a filtering fourth pneumatic valve, a filtering fifth pneumatic valve and a filtering sixth pneumatic valve in the filtering system assembly.
Preferably, the operation box is electrically connected with an auxiliary agent box A electromagnetic valve, an auxiliary agent box B electromagnetic valve, an auxiliary agent box C electromagnetic valve, an auxiliary agent box D electromagnetic valve, an auxiliary agent pump A, an auxiliary agent pump B, an auxiliary agent pump C and an auxiliary agent pump D in the auxiliary agent system assembly.
Preferably, two stirring barrels are provided.
Preferably, a view window of the mixing tank is arranged at the middle front part of the electro-oxidation flocculation dye liquor circulating and recycling system body.
Preferably, a filter is arranged in the ultramicro filter barrel.
Preferably, the filter is a laminated self-cleaning filter.
Has the advantages that:
the full-automatic electro-oxidation flocculation dye liquor recycling system has compact structure, high automation degree, strong equipment universality and high effluent quality; the sewage generated by the cleaning device during color changing of the dye liquor color matching crushing equipment and the dye liquor injection system can be treated, the treated clear water can be recycled, the discharge of the sewage is reduced, and the energy-saving and environment-friendly effects are achieved.
In order to make the objects, technical solutions and advantages of the present invention clearer, the following description of the present invention with reference to the accompanying drawings and specific embodiments is made for further details, but does not mean any limitation to the scope of the present invention.
Drawings
Fig. 1 is a schematic front sectional view of a full-automatic electro-oxidation flocculation dye liquor recycling system in embodiment 1 of the present invention.
Fig. 2 is a schematic diagram of a right-side view sectional structure of a full-automatic electro-oxidation flocculation dye liquor recycling system in embodiment 1 of the present invention.
Fig. 3 is a schematic view of a left-side view section structure of a full-automatic electro-oxidation flocculation dye liquor recycling system in embodiment 1 of the present invention.
Names of main parts:
1 electric oxidation flocculation dye liquor circulation recovery system body 2 agitator A
3 stirring barrel A window 4 stirring barrel B
5 stirring barrel B window 6 filtering system assembly
7 arrange clear water mouth 8 control boxes
9 agitator B advances sewage mouth 10 agitator A and advances sewage mouth
11 is an auxiliary agent system assembly
601 electric cabinet 602 ultramicro filter vat
603 deslagging motor 604 first pneumatic valve for filtering
605 residual slag barrel 606 backwashing water storage tank
607 Filtering the second pneumatic valve 608 Filtering the third pneumatic valve
609 filter pump 610 filters the fourth pneumatic valve
611 filter fifth pneumatic valve 612 filter sixth pneumatic valve
1101 auxiliary agent box A1102 auxiliary agent box B
1103 auxiliary agent tank C1104 auxiliary agent tank D
1105 auxiliary agent case A solenoid valve 1106 auxiliary agent case B solenoid valve
1107 auxiliary agent case C solenoid 1108 auxiliary agent case D solenoid valve
1109 adjuvant Pump A1110 adjuvant Pump B
1111 auxiliary agent pump C1112 auxiliary agent pump D
Detailed Description
Unless otherwise indicated, the apparatus and methods described in the embodiments of the present invention are all conventional in the art; unless otherwise indicated, the devices or components of the embodiments of the present invention are commercially available conventional devices or components, and their installation and connection are conventional in the art.
Example 1
As shown in fig. 1, is a schematic structural diagram of a front section of a full-automatic electro-oxidation flocculation dye liquor recycling system in embodiment 1 of the present invention; wherein, 1 is the body of the electro-oxidation flocculation dye liquor recycling system, 2 is a stirring barrel A, 3 is a window of the stirring barrel A, 4 is a stirring barrel B, 5 is a window of the stirring barrel B, 6 is a filtering system assembly, 7 is a clear water discharging port, 8 is an operation box, 9 is a sewage inlet of the stirring barrel B, 10 is a sewage inlet of the stirring barrel A, and 11 is an auxiliary agent system assembly;
as shown in fig. 2, is a schematic diagram of a right-view cross-sectional structure of a full-automatic electro-oxidation flocculation dye liquor recycling system in embodiment 1 of the present invention; the system comprises a tank body 601, an electric cabinet, an ultramicro filter barrel 602, a deslagging motor 603, a first filtering pneumatic valve 604, a residue barrel 605, a backwashing water storage tank 606, a second filtering pneumatic valve 607, a third filtering pneumatic valve 608, a filter pump 609, a fourth filtering pneumatic valve 610, a fifth filtering pneumatic valve 611 and a sixth filtering pneumatic valve 612, wherein the ultramicro filter barrel is arranged in the tank body;
as shown in fig. 3, is a schematic left-side sectional structure view of a full-automatic electro-oxidation flocculation dye liquor recycling system in embodiment 1 of the present invention; wherein 1101 is an auxiliary agent box A, 1102 is an auxiliary agent box B, 1103 is an auxiliary agent box C, 1104 is an auxiliary agent box D, 1105 is an auxiliary agent box A electromagnetic valve, 1106 is an auxiliary agent box B electromagnetic valve, 1107 is an auxiliary agent box C electromagnetic valve, 1108 is an auxiliary agent box D electromagnetic valve, 1109 is an auxiliary agent pump A, 1110 is an auxiliary agent pump B, 1111 is an auxiliary agent pump C, 1112 is an auxiliary agent pump D;
the utility model provides a full-automatic electrooxidation flocculation dye liquor circulation recovery system includes: the system comprises an electrooxidation flocculation dye liquor recycling system body 1, a stirring barrel A2, a stirring barrel A window 3, a stirring barrel B4, a stirring barrel B window 5 (or one stirring barrel), a filtering system assembly 6, a clear water discharging port 7, an operation box 8, a stirring barrel B sewage inlet and outlet port 9, a stirring barrel A sewage inlet and outlet port 10 and an auxiliary agent system assembly 11; the stirring barrel A2 and the stirring barrel B4 are located in the middle of the electrooxidation flocculation dye liquor recycling system body 1, the window 3 and the window 5 of the stirring barrel A are located in the middle front part of the middle of the electrooxidation flocculation dye liquor recycling system body 1, the filtering system assembly 6 is located on the right side of the electrooxidation flocculation dye liquor recycling system body 1, the auxiliary agent system assembly 11 is located on the left side of the electrooxidation flocculation dye liquor recycling system body 1, the operation box 8 is located on the front side of the electrooxidation flocculation dye liquor recycling system body 1, the clear water discharging port 7 is located below the filtering system assembly 6, the sewage inlet port 9 of the stirring barrel B is located below the stirring barrel B4, and the sewage inlet port 10 of the stirring barrel A is located below the stirring barrel A2; the sewage inlet 9 of the stirring barrel B and the sewage inlet 10 of the stirring barrel A are connected with an auxiliary agent pump A1109, an auxiliary agent pump B1110, an auxiliary agent pump C1111 and an auxiliary agent pump D1112 in an auxiliary agent system assembly 11 through pipelines; the clear water discharging port 7 is connected with a clear water storage tank through a pipeline;
the auxiliary system assembly 11 comprises: an auxiliary agent box A1101, an auxiliary agent box B1102, an auxiliary agent box C1103, an auxiliary agent box D1104, an auxiliary agent box A electromagnetic valve 1105, an auxiliary agent box B electromagnetic valve 1106, an auxiliary agent box C electromagnetic valve 1107, an auxiliary agent box D electromagnetic valve 1108, an auxiliary agent pump A1109, an auxiliary agent pump B1110, an auxiliary agent pump C1111 and an auxiliary agent pump D1112; an auxiliary agent box A electromagnetic valve 1105 is fixed on an auxiliary agent box A1101, one end of an auxiliary agent pump A1109 is connected with the auxiliary agent box A1101 through the auxiliary agent box A electromagnetic valve 1105, and the other end is connected with a stirring barrel A2 or a stirring barrel B4; an auxiliary agent box B electromagnetic valve 1106 is fixed on an auxiliary agent box B1102, one end of an auxiliary agent pump B1110 is connected with the auxiliary agent box B1102 through the auxiliary agent box B electromagnetic valve 1106, and the other end of the auxiliary agent pump B1110 is connected with a stirring barrel A2 or a stirring barrel B4; an auxiliary agent box C electromagnetic valve 1107 is fixed on an auxiliary agent box C1103, one end of an auxiliary agent pump C1111 is connected with the auxiliary agent box C1103 through the auxiliary agent box C electromagnetic valve 1107, and the other end is connected with a stirring barrel A2 or a stirring barrel B4; an auxiliary agent tank D solenoid valve 1108 is fixed on the auxiliary agent tank D1104, one end of an auxiliary agent pump D1112 is connected with the auxiliary agent tank D1104 through the auxiliary agent tank D solenoid valve 1108, and the other end is connected with a stirring barrel A2 or a stirring barrel B4; the operation box 8 is connected with the general control operation platform and is connected with an auxiliary agent box A electromagnetic valve 1105, an auxiliary agent box B electromagnetic valve 1106, an auxiliary agent box C electromagnetic valve 1107, an auxiliary agent box D electromagnetic valve 1108, an auxiliary agent pump A1109, an auxiliary agent pump B1110, an auxiliary agent pump C1111 and an auxiliary agent pump D1112 in the auxiliary agent system; the filter system is connected with a filter electric cabinet 601, a deslagging motor 603, a filter first pneumatic valve 604, a filter second pneumatic valve 607, a filter third pneumatic valve 608, a filter pump 609, a filter fourth pneumatic valve 610, a filter fifth pneumatic valve 611 and a filter sixth pneumatic valve 612 in the filter system;
the filter system assembly 6 includes: a filtering electric cabinet 601, an ultramicro filter barrel 602, a deslagging motor 603, a filtering first pneumatic valve 604, a residue barrel 605, a backwashing water storage tank 606, a filtering second pneumatic valve 607, a filtering third pneumatic valve 608, a filtering pump 609, a filtering fourth pneumatic valve 610, a filtering fifth pneumatic valve 611 and a filtering sixth pneumatic valve 612; the filtering electric control box 601 is positioned at the upper part of the filtering system body and is connected with each pump and pneumatic valve, the filtering third pneumatic valve 608, the filtering pump 609, the filtering fourth pneumatic valve 610, the filtering fifth pneumatic valve 611 and the filtering sixth pneumatic valve 612 are positioned at the bottom of the filtering system body and are connected with each other through pipelines, the filtering third pneumatic valve 608 is connected with the backwashing water storage tank 606 through a pipeline and a filtering second pneumatic valve 607, the residue barrel 605 is positioned at the middle part of the filtering system body and is connected with the residue removing motor 603 and the ultramicro filtering barrel 602 through the filtering first pneumatic valve 604, and the ultramicro filtering barrel 602 is respectively connected with the filtering fourth pneumatic valve 610, the filtering fifth pneumatic valve 611 and the filtering sixth pneumatic valve 612 through pipelines;
the operation process of the full-automatic electro-oxidation flocculation dye liquor recycling system is as follows: sewage flows from a sewage tank to a sewage inlet 10 of a stirring barrel A and a sewage inlet 9 of a stirring barrel B through pipelines, and then flows to the stirring barrel A2 or the stirring barrel B4 through a pump, the two stirring barrels can be used alternately, an auxiliary agent system assembly 11 adds an auxiliary agent into the stirring barrel A2 or the stirring barrel B4, the stirring barrel A2 or the stirring barrel B4 is stirred, electrically oxidized, flocculated and precipitated, and then flows to a filtering system assembly 6 through the pump, and after being filtered and separated by the filtering system assembly 6, clean water is discharged through a clean water discharging port 7 and enters a clean water storage tank, and residues are discharged to a residue barrel;
4 auxiliary agent boxes in the auxiliary agent system assembly 11 respectively add auxiliary agents to the stirring barrel A2 and the stirring barrel B4 through respective valves and pumps;
the mixed liquid reaches a filter pump 609 through a third pneumatic valve 608, is sent to an ultramicro filter barrel 602 through a fourth pneumatic valve 610, is filtered and separated, clean water is discharged through a sixth pneumatic valve 612, residues are discharged into a residue barrel 605 through a residue removing motor 603 and a first pneumatic valve 604, when the mixed liquid is cleaned, the clean water in a backwashing water storage tank 606 is sent to the filter pump 609 through a second pneumatic valve 607, and is sent to a fifth pneumatic valve 611 to reach the ultramicro filter barrel 602, a filter screen in the ultramicro filter barrel 602 is cleaned, and the treated clean water enters a clean water storage tank through the sixth pneumatic valve 612;
the auxiliary agent box A is filled with a surfactant, the auxiliary agent box B is filled with polyaluminium chloride, the auxiliary agent box C is filled with a flocculation decolorizing agent, and the auxiliary agent box D is filled with polyacrylamide; the addition amount is correspondingly adjusted according to the actual process.
The filter used in the ultramicro filter vat is a laminated self-cleaning filter.
The utility model provides a full-automatic electrooxidation flocculation dye liquor circulation recovery system in 1 still includes the PLC controller, is connected with 11 electricity of filtration system assembly 6, control box 8 and auxiliary agent system assembly respectively.
The operation box 8 is electrically connected with a filtering electric control box 601, an ultra-micro filtering barrel 602, a deslagging motor 603, a filtering first pneumatic valve 604, a filtering second pneumatic valve 607, a filtering third pneumatic valve 608, a filtering pump 609, a filtering fourth pneumatic valve 610, a filtering fifth pneumatic valve 611 and a filtering sixth pneumatic valve 612 in the filtering system assembly 6;
the operation box 8 is electrically connected with an auxiliary agent box A electromagnetic valve 1105, an auxiliary agent box B electromagnetic valve 1106, an auxiliary agent box C electromagnetic valve 1107, an auxiliary agent box D electromagnetic valve 1108, an auxiliary agent pump A1109, an auxiliary agent pump B1110, an auxiliary agent pump C1111 and an auxiliary agent pump D1112 in the auxiliary agent system assembly 11;
the utility model discloses an in the technology of electrooxidation flocculation dye liquor circulation recovery system, the sewage that produces when dyeing system and dye liquor color matching machine trade look and wash gets into and handles among the electrooxidation flocculation dye liquor circulation recovery system, through electrooxidation flocculation back, through ultrafiltration system, separates clear water and solid waste, but clear water cyclic utilization reaches the requirement of sewage zero release.
The utility model discloses a full-automatic electrooxidation flocculation dye liquor recycling system's advantage is: compact structure, high automation degree, strong equipment universality, high effluent quality, capability of recycling treated clean water and the like.
The utility model discloses a full-automatic electrooxidation flocculation dye liquor circulation recovery system compact structure mainly embodies and is in the whole integrated integration of parts such as agitator tank, auxiliary agent bucket (medicament addition bucket), pump package, ultrafiltration system.
The utility model discloses a full-automatic electrooxidation flocculation dye liquor circulation recovery system degree of automation is high, mainly embodies and puts complete machine operation control on the operation control screen, can realize automatic feed, stirring, add medicine, filter, automatic washing, accomplish water detection, on-line monitoring etc. automatically.
The utility model discloses a full-automatic electrooxidation flocculation dye liquor recycling system's commonality is strong, mainly embodies at this processing apparatus, can handle various sewage and other various industrial sewage that weaving low carbon dyeing and finishing integration production facility produced (different according to sewage kind composition, add the auxiliary agent according to the technological requirement in the auxiliary agent case).
The utility model discloses a full-automatic electrooxidation flocculation dye liquor circulation recovery system goes out water quality high quality, mainly reflects in the water after the device handles, can reach and be higher than each item national standard, the target of the zero release of the real realization sewage.
The above description is only the specific implementation manner of the preferred embodiment of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art can substitute or change the technical solution of the present invention and the design of the present invention within the technical scope of the present invention.
Claims (5)
1. The utility model provides a full-automatic electrooxidation flocculation dye liquor circulation recovery system which characterized in that: the system comprises an electrooxidation flocculation dye liquor recycling system body, a stirring barrel, a filtering system assembly, a clear water discharging port, an operation box, a stirring barrel sewage inlet port, an auxiliary agent system assembly and a PLC (programmable logic controller); the stirring barrel is positioned in the middle of the electrooxidation flocculation dye liquor recycling system body, the filtering system assembly is positioned on the right side of the electrooxidation flocculation dye liquor recycling system body, the auxiliary agent system assembly is positioned on the left side of the electrooxidation flocculation dye liquor recycling system body, the operation box is positioned on the front side of the electrooxidation flocculation dye liquor recycling system body, the clear water discharging port is positioned below the filtering system assembly, and the sewage inlet of the stirring barrel is positioned below the stirring barrel; the sewage inlet of the stirring barrel is connected with an auxiliary agent pump in the auxiliary agent system assembly through a pipeline; the clear water discharging port is connected with the clear water storage tank through a pipeline; the additive system assembly comprises: the auxiliary agent box comprises an auxiliary agent box A, an auxiliary agent box B, an auxiliary agent box C, an auxiliary agent box D, an auxiliary agent box A electromagnetic valve, an auxiliary agent box B electromagnetic valve, an auxiliary agent box C electromagnetic valve, an auxiliary agent box D electromagnetic valve, an auxiliary agent pump A, an auxiliary agent pump B, an auxiliary agent pump C and an auxiliary agent pump D; an electromagnetic valve of an auxiliary agent box A is fixed on the auxiliary agent box A, one end of an auxiliary agent pump A is connected with the auxiliary agent box A through the electromagnetic valve of the auxiliary agent box A, and the other end of the auxiliary agent pump A is connected with the stirring barrel; an electromagnetic valve of the auxiliary agent box B is fixed on the auxiliary agent box B, one end of an auxiliary agent pump B is connected with the auxiliary agent box B through the electromagnetic valve of the auxiliary agent box B, and the other end of the auxiliary agent pump B is connected with the stirring barrel; an electromagnetic valve of an auxiliary agent box C is fixed on the auxiliary agent box C, one end of an auxiliary agent pump C is connected with the auxiliary agent box C through the electromagnetic valve of the auxiliary agent box C, and the other end of the auxiliary agent pump C is connected with the stirring barrel; an electromagnetic valve of an auxiliary agent box D is fixed on the auxiliary agent box D, one end of an auxiliary agent pump D is connected with the auxiliary agent box D through the electromagnetic valve of the auxiliary agent box D, and the other end of the auxiliary agent pump D is connected with the stirring barrel; the operation box is connected with the master control operation platform and is connected with an auxiliary agent box A electromagnetic valve, an auxiliary agent box B electromagnetic valve, an auxiliary agent box C electromagnetic valve, an auxiliary agent box D electromagnetic valve, an auxiliary agent pump A, an auxiliary agent pump B, an auxiliary agent pump C and an auxiliary agent pump D in the auxiliary agent system; the filter system is connected with a filter electric control box, a deslagging motor, a first filter pneumatic valve, a second filter pneumatic valve, a third filter pneumatic valve, a filter pump, a fourth filter pneumatic valve, a fifth filter pneumatic valve and a sixth filter pneumatic valve in the filter system; the filtration system assembly includes: the device comprises a filtering electric cabinet, an ultramicro filter barrel, a deslagging motor, a first filtering pneumatic valve, a residue barrel, a backwashing water storage tank, a second filtering pneumatic valve, a third filtering pneumatic valve, a filtering pump, a fourth filtering pneumatic valve, a fifth filtering pneumatic valve and a sixth filtering pneumatic valve; the filtering electric control box is positioned at the upper part of the filtering system body and is connected with each pump and the pneumatic valve, the filtering third pneumatic valve, the filtering pump, the filtering fourth pneumatic valve, the filtering fifth pneumatic valve and the filtering sixth pneumatic valve are positioned at the bottom of the filtering system body and are connected with each other through a pipeline, the filtering third pneumatic valve is connected with the backwashing water storage tank through a pipeline and a filtering second pneumatic valve, the residue barrel is positioned at the middle part of the filtering system body and is connected with the residue removing motor and the ultramicro filtering barrel through the filtering first pneumatic valve, and the ultramicro filtering barrel is respectively connected with the filtering fourth pneumatic valve, the filtering fifth pneumatic valve and the filtering sixth pneumatic valve through pipelines; the PLC is respectively and electrically connected with the filtering system assembly, the operation box and the auxiliary agent system assembly.
2. The full-automatic electro-oxidation flocculation dye liquor recycling system of claim 1, characterized in that: the operation box is electrically connected with a filtering electric control box, an ultra-micro filtering barrel, a deslagging motor, a first filtering pneumatic valve, a second filtering pneumatic valve, a third filtering pneumatic valve, a filtering pump, a fourth filtering pneumatic valve, a fifth filtering pneumatic valve and a sixth filtering pneumatic valve in the filtering system assembly.
3. The full-automatic electro-oxidation flocculation dye liquor recycling system of claim 2, characterized in that: the operation box is electrically connected with an auxiliary agent box A electromagnetic valve, an auxiliary agent box B electromagnetic valve, an auxiliary agent box C electromagnetic valve, an auxiliary agent box D electromagnetic valve, an auxiliary agent pump A, an auxiliary agent pump B, an auxiliary agent pump C and an auxiliary agent pump D in the auxiliary agent system assembly.
4. The full-automatic electro-oxidation flocculation dye liquor recycling system of claim 3, characterized in that: a filter is arranged in the ultramicro filter barrel.
5. The full-automatic electro-oxidation flocculation dye liquor recycling system of claim 4, characterized in that: the filter is a laminated self-cleaning filter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022579592.0U CN214032063U (en) | 2020-11-10 | 2020-11-10 | Full-automatic electro-oxidation flocculation dye liquor recycling system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202022579592.0U CN214032063U (en) | 2020-11-10 | 2020-11-10 | Full-automatic electro-oxidation flocculation dye liquor recycling system |
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| Publication Number | Publication Date |
|---|---|
| CN214032063U true CN214032063U (en) | 2021-08-24 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202022579592.0U Expired - Fee Related CN214032063U (en) | 2020-11-10 | 2020-11-10 | Full-automatic electro-oxidation flocculation dye liquor recycling system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN214032063U (en) |
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2020
- 2020-11-10 CN CN202022579592.0U patent/CN214032063U/en not_active Expired - Fee Related
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Granted publication date: 20210824 |