CN115726118B - Waste liquid recovery treatment device after dyeing of vulcanized black coloring agent - Google Patents
Waste liquid recovery treatment device after dyeing of vulcanized black coloring agent Download PDFInfo
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- CN115726118B CN115726118B CN202211502799.5A CN202211502799A CN115726118B CN 115726118 B CN115726118 B CN 115726118B CN 202211502799 A CN202211502799 A CN 202211502799A CN 115726118 B CN115726118 B CN 115726118B
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- 239000007788 liquid Substances 0.000 title claims abstract description 216
- 239000002699 waste material Substances 0.000 title claims abstract description 203
- 238000004043 dyeing Methods 0.000 title claims abstract description 85
- 238000011084 recovery Methods 0.000 title claims abstract description 75
- 239000003086 colorant Substances 0.000 title claims description 16
- 238000004062 sedimentation Methods 0.000 claims abstract description 114
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 claims abstract description 73
- 238000010438 heat treatment Methods 0.000 claims abstract description 42
- 239000000975 dye Substances 0.000 claims abstract description 20
- 238000004064 recycling Methods 0.000 claims abstract description 4
- 238000000605 extraction Methods 0.000 claims description 16
- 238000001125 extrusion Methods 0.000 claims description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 11
- 230000002776 aggregation Effects 0.000 claims description 9
- 238000004220 aggregation Methods 0.000 claims description 9
- 238000004073 vulcanization Methods 0.000 claims description 9
- 239000002912 waste gas Substances 0.000 claims description 7
- PGYZAKRTYUHXRA-UHFFFAOYSA-N 2,10-dinitro-12h-[1,4]benzothiazino[3,2-b]phenothiazin-3-one Chemical compound S1C2=CC(=O)C([N+]([O-])=O)=CC2=NC2=C1C=C1SC3=CC=C([N+](=O)[O-])C=C3NC1=C2 PGYZAKRTYUHXRA-UHFFFAOYSA-N 0.000 claims description 5
- 230000000694 effects Effects 0.000 abstract description 19
- 239000010919 dye waste Substances 0.000 description 15
- 230000009471 action Effects 0.000 description 14
- 244000144992 flock Species 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 239000012535 impurity Substances 0.000 description 4
- 229920001021 polysulfide Polymers 0.000 description 4
- 239000005077 polysulfide Substances 0.000 description 4
- 150000008117 polysulfides Polymers 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 230000000740 bleeding effect Effects 0.000 description 3
- 230000002688 persistence Effects 0.000 description 3
- 230000008569 process Effects 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000004040 coloring Methods 0.000 description 2
- TXKMVPPZCYKFAC-UHFFFAOYSA-N disulfur monoxide Inorganic materials O=S=S TXKMVPPZCYKFAC-UHFFFAOYSA-N 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 229920002521 macromolecule Polymers 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical compound S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 2
- 239000002341 toxic gas Substances 0.000 description 2
- 229920000742 Cotton Polymers 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 238000005189 flocculation Methods 0.000 description 1
- 230000016615 flocculation Effects 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 230000001360 synchronised effect Effects 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
Classifications
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- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/50—Manufacturing or production processes characterised by the final manufactured product
- Y02P70/62—Manufacturing or production processes characterised by the final manufactured product related technologies for production or treatment of textile or flexible materials or products thereof, including footwear
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- Ink Jet (AREA)
- Treatment Of Fiber Materials (AREA)
Abstract
The invention discloses a waste liquid recovery treatment device after dyeing with a black sulfide dyeing agent, which relates to the technical field of black sulfide dyeing waste liquid recovery, and comprises a recovery box and an air pump, wherein the recovery box is used for temporarily storing black sulfide dyeing waste liquid, a heating part, a liquid supply part, a sedimentation part and a driving part are arranged in the recovery box, the heating part is positioned below the liquid level of the black sulfide dyeing waste liquid, the output direction of the liquid supply part is the side where a sedimentation belt is positioned, the sedimentation part is used for collecting waste batting in the black sulfide dyeing waste liquid, and the driving part provides power required by movement for the sedimentation belt. According to the invention, the content of the waste liquid of the vulcanized black dye in the waste batting layer is reduced through the driving part, the sedimentation part and the waste liquid outlet improve the recycling effect of the waste batting in the waste liquid of the vulcanized black dye, and the heating part and the liquid supply part improve the sedimentation effect of the waste batting in the waste liquid of the vulcanized black dye and reduce the continuous adhesion of the waste batting on the sedimentation belt.
Description
Technical Field
The invention relates to the technical field of vulcanized black dyeing waste liquid recovery, in particular to a waste liquid recovery treatment device after vulcanized black dyeing agent dyeing.
Background
The sulfur black is a black scale-shaped solid, is mainly used for dyeing cotton textiles, is a macromolecular compound containing more sulfur, contains disulfide bonds and polysulfide bonds in the structure, and is very unstable. In particular, the polysulfide bond can be oxidized into sulfur oxide by oxygen in the air under certain temperature and humidity conditions, and further reacts with water molecules in the air to generate sulfuric acid, so that the yarn strength is reduced, the fiber is fragile, and when serious, all the fiber is fragile into powder, therefore, when the sulfur black is used as dye, the dosage of the sulfur black should be controlled.
During the application period of the black sulfide serving as a dyeing agent, after the black sulfide dyeing agent is used for dyeing cloth, the waste liquid of the black sulfide dyeing agent needs to be recovered and treated, a large amount of waste batting exists in the waste liquid after the dyeing of the existing black sulfide dyeing agent, the existence of the waste batting influences the recovery effect of the waste liquid after the dyeing of the black sulfide dyeing agent, the existing waste liquid recovery treatment device mainly utilizes a sedimentation tank to realize waste batting sedimentation, the efficiency is slower, continuous work cannot be carried out, and the efficiency of the existing waste liquid recovery treatment device is lower.
Disclosure of Invention
The invention aims to provide a waste liquid recovery treatment device after dyeing of a vulcanized black coloring agent, so as to solve the problems in the background technology.
In order to solve the technical problems, the invention provides the following technical scheme: the waste liquid recovery treatment device after the black sulfide coloring agent is dyed comprises a recovery box and an air pump, wherein the recovery box is used for temporarily storing black sulfide coloring waste liquid, and a heating part, a liquid supply part, a sedimentation part and a driving part are arranged in the recovery box;
the heating component is positioned below the liquid level of the black sulfide dyeing waste liquid, the heating component is used for heating the black sulfide dyeing waste liquid, a sedimentation belt is arranged on one side of the liquid supply component, the liquid supply component is used for continuously outputting the black sulfide dyeing waste liquid, the output direction of the liquid supply component is the side where the sedimentation belt is positioned, the sedimentation component is used for collecting waste batting in the black sulfide dyeing waste liquid, and the driving component provides power required by movement for the sedimentation belt;
the protruding piece is installed to one side of recovery case, the subsider slides along the outer wall of recovery case and protruding piece, the cross section of recovery case is triangle-shaped, protruding piece is used for useless batting and subsider separation.
Further, the inside power pack, extrusion subassembly and the subassembly of bleeding that is including of sedimentation part, the subassembly of bleeding is connected with the air pump, power pack is used for realizing that the sedimentation belt is along the outer wall motion of collection box, extrusion subassembly is used for extruding the sedimentation belt, the subassembly of bleeding is used for absorbing the waste gas that produces after the heating of black dyeing waste liquid of sulphide, and the sedimentation belt carries waste wadding layer and can pass through the region that the protruding piece is located after leaving the collection box, and the sedimentation belt carries waste wadding layer during protruding piece, and the sedimentation belt forms the same dog-ear with protruding piece with the region that the protruding piece contacted, leads to the effort between the waste wadding layer of protruding piece protruding part and the sedimentation belt to reduce, separates between waste wadding and the sedimentation belt.
Further, the power pack is located the black dyeing waste liquid level top of vulcanizing, the power pack is including installing at the inside driving shaft of collection box, the driving shaft is connected with the bleed subassembly, the outer wall of driving shaft is provided with a plurality of deflector, the driving shaft is connected with the extrusion subassembly, the driving shaft is connected with the deflector through the spring shaft, and the deflector passes through the spring shaft increase to the effort of sedimentation belt, because the limiting roller is installed to the both sides of driving shaft, and sedimentation belt pass through with the clearance between the limiting roller for the deflector that contacts with the sedimentation belt is under the effect of pressure, and the deflector is hugged closely the outer wall of driving shaft.
Further, the extrusion assembly comprises limit rollers arranged on two sides of the driving shaft, the sedimentation belt passes through gaps between the driving shaft and the two limit rollers, a plurality of triangular blocks are arranged on the outer wall of the deflection plate, partial areas on the outer side of the deflection plate are contacted with the sedimentation belt through the triangular blocks, the deflection plate and the triangular blocks continuously extrude waste wadding layers attached to the surface of the sedimentation belt during the contact of the sedimentation belt with the deflection plate and the triangular blocks, and the waste wadding layers internally contain vulcanized black dyeing waste liquid during the contact of the sedimentation belt with the deflection plate and the triangular blocks, and a plurality of broken waste wadding layer strips are formed on the continuous waste wadding layers under the further extrusion of the triangular blocks so as to reduce the adhesion effect between the waste wadding layers.
Further, the air extraction assembly comprises an arc plate arranged in the driving shaft, an opening of the arc plate faces downwards, an inner shaft is arranged in the middle of the arc plate, a through hole is formed in the middle of the inner shaft, the inner shaft is connected with the air pump, the driving shaft is rotationally connected with the inner shaft, the inner shaft is connected with the arc plate, the opening of the arc plate is always downward, the deflection plate above the driving shaft is in an open state under the action of the spring shaft due to the fact that the sedimentation belt passes through the lower portion of the driving shaft, steam and waste gas in the recovery box enter the driving shaft through gaps of the deflection plate, and the steam and the waste gas enter the inner shaft under the guidance of the arc plate and the closed deflection plate and finally leave the recovery box under the action of the air pump.
Further, subside the part including installing at the inside gathering subassembly and the waste liquid export of collection box, gather vertical distribution between subassembly and the waste liquid export, the subside area passes from gathering between subassembly and the waste liquid export, gather the inside deflector that is provided with of subassembly, the lower extreme surface of deflector is laminated with the upper end surface of subsider, the longitudinal section of deflector is triangle-shaped, and the inside waste batting of black dyeing waste sulfide subsides under the effect of gravity, until the waste batting moves to the region at deflector place, and the waste batting drops to the top surface of subsider under the effect of deflector, because the subsider moves along the outer wall of collection box under the effect of driving shaft for the waste batting synchronous follow the motion of subsider, and the waste liquid export is located the decline of subsider part, and the waste liquid export is provided with the subsider between deflector, and the subsider under the motion state from the clearance process between waste liquid export and the deflector, and the waste liquid export is used for constantly exporting the inside black dyeing that sulfide of heat of guide box, because the export is located the below of deflector, makes the inside of sulfide dyeing to the effect of deflector and the waste batting and the waste liquid that the effect of subsider is arranged in the subsider to the main waste liquid that the subsider is arranged in the subsider to the guide box to the outside surface of the waste liquid, and the waste liquid is arranged in the subsider to the waste stream to the outside surface of the guide box, and the waste dyeing structure.
Further, the liquid supply part comprises a liquid supply pipe arranged on one side of the sedimentation belt, the liquid supply pipe is obliquely upwards arranged, an inclined notch is formed in one side of the liquid supply pipe, the inclined notch of the liquid supply pipe is attached to one side surface of the sedimentation belt, a water outlet of the liquid supply pipe is higher than the liquid level of the black sulfide dyeing waste liquid, a water outlet of the liquid supply pipe is obliquely upwards so as to reduce the impact of the black sulfide dyeing waste liquid after leaving the liquid supply pipe, and part of impact force of the black sulfide dyeing waste liquid acts on the surface of the sedimentation belt to impact waste flocks attached to the surface of the sedimentation belt all the time.
Further, the heating element is including installing at the inside hot plate of collection box, the transversal rectangle of hot plate, and the hot plate is vertical placing in the collection box under the idle state to the kinetic energy that the effectual absorption waste liquid lateral motion carried, the hot plate is connected with the collection box through the pivot, and the hot plate is heating the black dyeing waste liquid of sulphide, and secondly the hot plate is used for keeping the inside black dyeing waste liquid of sulphide of collection box stable, and the hot plate constantly absorbs the inside kinetic energy of black dyeing waste liquid of sulphide through the pivot, avoids supplying black dyeing waste liquid of sulphide because of the liquid pipe persistence, leads to the inside black dyeing waste liquid of sulphide of collection box horizontal kinetic energy great, and then influences the inside waste wadding subsides of black dyeing waste liquid of sulphide.
Compared with the prior art, the invention has the following beneficial effects:
1. according to the waste liquid recovery treatment device after the black sulfide dyeing agent is dyed, through the arrangement of the driving component, the power component provides power required by movement for the sedimentation belt, the black sulfide dyeing agent waste liquid leaving along with the waste wadding layer is reduced, the influence of impurities on the purity of the black sulfide dyeing agent waste liquid is reduced, the air extraction component is used for recovering toxic gas generated by the black sulfide dyeing waste liquid after heating, reducing the content of black sulfide in the black sulfide dyeing waste liquid, improving the purifying effect on the black sulfide dyeing waste liquid, enabling the chemical property of the purified black sulfide dyeing waste liquid to be more stable, and the air extraction component guides the air flow leaving the recovery box, so that the heat carried in the air flow is used for further drying the extruded waste wadding layer, the content of the black sulfide dyeing agent waste liquid in the waste wadding layer is reduced again, and the purifying effect of the driving component on the black sulfide dyeing waste liquid is improved;
2. according to the waste liquid recovery treatment device after the black sulfide dyeing agent is dyed, through the arrangement of the sedimentation part and the waste liquid outlet, the waste liquid outlet is positioned below the guide plate, so that waste flocks in the black sulfide dyeing waste liquid move to the position where the waste liquid outlet is positioned under the action of water flow, the sedimentation part and the waste liquid outlet are matched with the sedimentation belt, the content of waste flocks in the black sulfide dyeing waste liquid is reduced, various impurities in the black sulfide dyeing waste liquid are further separated, the recovery efficiency of the black sulfide dyeing waste liquid is improved, the outer surface structure of the guide plate is mainly used for guiding the waste flocks, the position of the guide plate is arranged to prevent the black sulfide dyeing waste liquid from entering the waste liquid outlet through a gap between the sedimentation belt and the recovery box, and the matching effect between the sedimentation belt and the guide plate is improved;
3. this waste liquid recovery processing device after vulcanization black dye dyeing, through the setting of heating element and liquid feed unit, heating element decomposes vulcanization black dye waste liquid through heating, reduce the dangerous degree of vulcanization black dye waste liquid after handling, with the recovery risk of reduction vulcanization black dye waste liquid, wherein the structure setting and the connected mode of hot plate, improve the sedimentation effect of the inside waste wadding of vulcanization black dye waste liquid, accelerate the inside waste wadding subsides of vulcanization black dye waste liquid, improve heating element to vulcanization black dye waste liquid treatment effeciency, secondly, the delivery port of liquid feed pipe is upwards to the slope, through absorbing the stirring that leaves the inside of collection box of waste liquid that gets into, realize that waste liquid recovery processing device carries out persistence processing to vulcanization black dye waste liquid.
Drawings
The accompanying drawings are included to provide a further understanding of the invention and are incorporated in and constitute a part of this specification, illustrate the invention and together with the embodiments of the invention, serve to explain the invention. In the drawings:
FIG. 1 is a schematic view of the present invention in front elevational view in full section;
FIG. 2 is a schematic view of the right side view of the guide plate of the present invention in full section;
FIG. 3 is a schematic top view in full section of the guide plate of the present invention;
FIG. 4 is a schematic view of the drive member of the present invention in front elevational view in full section;
FIG. 5 is a schematic top view of a structural liquid supply tube of the present invention;
FIG. 6 is an enlarged schematic view of the structure of FIG. 1A in accordance with the present invention;
fig. 7 is an enlarged schematic view of the structure of fig. 1B according to the present invention.
In the figure: 1. a recovery box; 2. a sedimentation belt; 3. a power assembly; 301. a driving shaft; 302. a deflector plate; 4. an extrusion assembly; 401. a limit roller; 402. triangular blocks; 5. an air extraction assembly; 501. an arc-shaped plate; 502. an inner shaft; 6. a protruding block; 7. an aggregation component; 701. a guide plate; 8. a waste liquid outlet; 9. a liquid supply pipe; 10. and (5) heating the plate.
Detailed Description
The following description of the embodiments of the present invention will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present invention, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
Referring to fig. 1 to 7, the present invention provides the following technical solutions: the waste liquid recovery treatment device after the black sulfide coloring agent is dyed comprises a recovery box 1 and an air pump, wherein the recovery box 1 is used for temporarily storing black sulfide coloring waste liquid, and a heating part, a liquid supply part, a sedimentation part and a driving part are arranged in the recovery box 1;
the heating component is positioned below the liquid level of the vulcanized black dyeing waste liquid, the heating component is used for heating the vulcanized black dyeing waste liquid, the sedimentation belt 2 is arranged on one side of the liquid supply component, the liquid supply component is used for continuously outputting the vulcanized black dyeing waste liquid, the output direction of the liquid supply component is the side where the sedimentation belt 2 is positioned, the sedimentation component is used for collecting waste batting in the vulcanized black dyeing waste liquid, and the driving component provides power required by movement for the sedimentation belt 2;
a protruding block 6 is arranged on one side of the recovery box 1, the sedimentation belt 2 slides along the outer walls of the recovery box 1 and the protruding block 6, the cross section of the recovery box 1 is triangular, and the protruding block 6 is used for separating waste batting from the sedimentation belt 2;
the inside of the sedimentation component comprises a power component 3, an extrusion component 4 and an air extraction component 5, the air extraction component 5 is connected with an air pump, the power component 3 is used for realizing the movement of the sedimentation belt 2 along the outer wall of the recovery box 1, the extrusion component 4 is used for extruding the sedimentation belt 2, and the air extraction component 5 is used for absorbing waste gas generated after the heating of the vulcanized black dyeing waste liquid;
the power assembly 3 is positioned above the liquid level of the vulcanized black dyeing waste liquid, the power assembly 3 comprises a driving shaft 301 arranged in the recovery box 1, the driving shaft 301 is connected with the air extraction assembly 5, a plurality of deflection plates 302 are arranged on the outer wall of the driving shaft 301, the driving shaft 301 is connected with the extrusion assembly 4, and the driving shaft 301 is connected with the deflection plates 302 through a spring shaft;
the extrusion assembly 4 comprises limit rollers 401 arranged on two sides of the driving shaft 301, the sedimentation belt 2 passes through a gap between the driving shaft 301 and the two limit rollers 401, and a plurality of triangular blocks 402 are arranged on the outer wall of the deflection plate 302;
the air extraction assembly 5 comprises an arc plate 501 arranged in the driving shaft 301, the opening of the arc plate 501 is downward, the middle part of the arc plate 501 is provided with an inner shaft 502, the middle part of the inner shaft 502 is provided with a through hole, the inner shaft 502 is connected with an air pump, the power assembly 3 provides power required by movement for the sedimentation belt 2, reduces the waste liquid of the vulcanized black colorant leaving along with the waste wadding layer, reduces the influence of impurities on the purity of the waste liquid of the vulcanized black colorant, the air extraction assembly 5 is used for recycling toxic gas generated by the heated vulcanized black colorant, reducing the content of vulcanized black in the vulcanized black colorant, improving the purifying effect on the vulcanized black colorant, enabling the chemical property of the purified vulcanized black colorant to be more stable, and the air extraction assembly 5 guides the air flow leaving the recovery box 1, so as to realize the further drying of the extruded waste wadding layer by the heat carried in the air flow, reduce the content of the vulcanized black colorant in the waste wadding layer again, and improve the purifying effect of the driving part on the vulcanized black colorant;
the sedimentation component comprises an aggregation component 7 and a waste liquid outlet 8 which are arranged in the recovery box 1, the aggregation component 7 and the waste liquid outlet 8 are vertically distributed, the sedimentation belt 2 passes through the aggregation component 7 and the waste liquid outlet 8, a guide plate 701 is arranged in the aggregation component 7, the lower end surface of the guide plate 701 is attached to the upper end surface of the sedimentation belt 2, the longitudinal section of the guide plate 701 is triangular, the waste liquid outlet 8 is positioned below the guide plate 701, so that waste batting in the vulcanized black dyeing waste liquid moves to the position of the waste liquid outlet 8 under the action of water flow, the sedimentation component and the waste liquid outlet 8 are matched with the sedimentation belt 2, so that the content of the waste batting in the vulcanized black dyeing waste liquid is reduced, various impurities in the vulcanized black dyeing waste liquid are separated, the vulcanized black dyeing waste liquid recovery efficiency is improved, the outer surface structure of the guide plate 701 is mainly used for guiding the waste batting, the position of the guide plate 701 is set to avoid the vulcanized black dyeing waste liquid from entering the waste liquid outlet 8 through a gap between the sedimentation belt 2 and the recovery box 1, and the matching effect between the sedimentation belt 2 and the guide plate 701 is improved;
the liquid supply component comprises a liquid supply pipe 9 arranged on one side of the sedimentation belt 2, wherein the liquid supply pipe 9 is obliquely upwards arranged, an inclined notch is formed in one side of the liquid supply pipe 9, the inclined notch of the liquid supply pipe 9 is attached to the surface of one side of the sedimentation belt 2, and the water outlet of the liquid supply pipe 9 is higher than the liquid level of the vulcanized black dyeing waste liquid;
the heating element is including installing at the inside hot plate 10 of collection box 1, the cross-section of hot plate 10 is the rectangle, hot plate 10 is connected with collection box 1 through the pivot, the heating element decomposes the black dye waste liquid of sulphur through heating, reduce the dangerous degree of the black dye waste liquid of sulphide after handling, in order to reduce the recovery risk of black dye waste liquid of sulphide, wherein the structure setting and the connected mode of hot plate 10 improve the inside waste wadding's of black dye waste liquid sedimentation effect of sulphide, accelerate the inside waste wadding sedimentation of black dye waste liquid of sulphide, improve the heating element to the black dye waste liquid treatment effeciency of sulphide, the delivery port of second feed pipe 9 is upwards to the slope, through absorbing the kinetic energy of black dye waste liquid of sulphide after leaving feed pipe 9, avoid the waste liquid that gets into to the inside disturbance that causes of collection box 1, realize that waste liquid recovery processing device carries out persistence to the black dye waste liquid of sulphide.
The working principle of the invention is as follows: the upper end of the interior of the recovery box 1 is provided with a liquid supply pipe 9, one end of the liquid supply pipe 9 is connected with a supply device of the black sulfide dyeing waste liquid, the black sulfide dyeing waste liquid is continuously supplied to the interior of the recovery box 1 through the supply device, the supply device is continuously supplied until the liquid level of the black sulfide dyeing waste liquid in the interior of the recovery box 1 is slightly lower than the water outlet of the liquid supply pipe 9, and then the heating plate 10 and the driving shaft 301 in the interior of the recovery box 1 can be started;
the outer wall of the recovery box 1 is surrounded by a sedimentation belt 2, the driving shaft 301 is in direct contact with the sedimentation belt 2, so that the driving shaft 301 drives the sedimentation belt 2 to move along the outer wall of the recovery box 1, the cross section of the recovery box 1 is triangular, the driving part is positioned above one side of the inside of the triangle, the sedimentation part is positioned at the lower included angle of the inside of the recovery box 1, and the liquid supply part is positioned at one side far away from the sedimentation part, namely, the liquid supply part is positioned above the other side of the inside of the triangle;
the waste vulcanized black dyeing liquid enters the waste vulcanized black dyeing liquid in the recovery box 1 after leaving the liquid supply pipe 9, and the waste batting in the waste vulcanized black dyeing liquid is settled under the action of gravity until the waste batting moves to the area where the guide plate 701 is positioned, and the waste batting falls onto the upper surface of the sedimentation belt 2 under the action of the guide plate 701, and the sedimentation belt 2 moves along the outer wall of the recovery box 1 under the action of the driving shaft 301, so that the waste batting above the sedimentation belt 2 synchronously follows the movement;
the waste liquid outlet 8 is positioned at the descending of the sedimentation part, the waste liquid outlet 8 is positioned below the guide plate 701, a sedimentation belt 2 is arranged between the waste liquid outlet 8 and the guide plate 701, the sedimentation belt 2 in a moving state passes through a gap between the waste liquid outlet 8 and the guide plate 701, the waste liquid outlet 8 is used for continuously guiding out the heated black sulfide dyeing waste liquid in the recovery box 1, the waste flock in the black sulfide dyeing waste liquid moves to the position of the waste liquid outlet 8 under the action of water flow due to the fact that the waste liquid outlet 8 is positioned below the guide plate 701, and the sedimentation belt 2 is arranged between the waste liquid outlet 8 and the guide plate 701, so that the waste flock in the black sulfide dyeing waste liquid is limited at one side of the sedimentation belt 2;
the heating plate 10 is positioned in the area between the liquid supply pipe 9 and the sedimentation component, the cross section of the heating plate 10 is rectangular, the heating plate 10 is connected with the recovery box 1 through a rotating shaft, and during the heating of the black sulfide dyeing waste liquid, the heating plate 10 contains disulfide bonds and polysulfide bonds in the structure of the black sulfide dye because the black sulfide dye is a macromolecular compound containing more sulfur, and is unstable, wherein the polysulfide bonds can be contacted and oxidized into sulfur oxide by oxygen in the air under certain temperature and humidity conditions, and further react with water molecules in the air to generate sulfuric acid, and the heating plate 10 is used for keeping the black sulfide dyeing waste liquid in the recovery box 1 stable, and the heating plate 10 continuously absorbs the kinetic energy in the black sulfide dyeing waste liquid through the rotating shaft, so that the black sulfide dyeing waste liquid in the recovery box 1 is prevented from being continuously supplemented by the liquid supply pipe 9, the transverse kinetic energy of the black sulfide dyeing waste liquid is large, and further the waste flocculation in the black sulfide dyeing waste liquid is prevented from being influenced;
the driving shaft 301 drives the sedimentation belt 2 through the deflection plates 302 to realize the movement of the sedimentation belt 2 along the outer wall of the recovery box 1, the driving shaft 301 is connected with the deflection plates 302 through a spring shaft, the deflection plates 302 increase the acting force on the sedimentation belt 2 through the spring shaft, and as the limit rollers 401 are arranged on two sides of the driving shaft 301, the sedimentation belt 2 passes through the gaps between the driving shaft 301 and the two limit rollers 401, the deflection plates 302 contacted with the sedimentation belt 2 are tightly attached to the outer wall of the driving shaft 301 under the action of pressure;
the deflection plate 302 is provided with a plurality of triangular blocks 402, a part of the area outside the deflection plate 302 is contacted with the sedimentation belt 2 through the triangular blocks 402, the deflection plate 302 and the triangular blocks 402 continuously squeeze a waste wadding layer attached to the surface of the sedimentation belt 2 during the contact of the sedimentation belt 2 with the deflection plate 302 and the triangular blocks 402, the waste wadding layer contains vulcanized black dyeing waste liquid during the contact of the sedimentation belt 2 with the deflection plate 302 and the triangular blocks 402, and under the further extrusion of the triangular blocks 402, the continuous waste wadding layer forms a plurality of broken waste wadding layer strips so as to reduce the adhesion effect between the waste waddings;
the driving shaft 301 and the inner shaft 502 are rotationally connected, the inner shaft 502 is connected with the arc plate 501, so that the opening of the arc plate 501 is always downward, the deflection plate 302 above the driving shaft 301 is in an open state under the action of a spring shaft due to the fact that the sedimentation belt 2 passes below the driving shaft 301, steam and waste gas in the recovery box 1 enter the driving shaft 301 through the gap of the deflection plate 302, the steam and the waste gas enter the inner shaft 502 under the guidance of the arc plate 501 and the closed deflection plate 302, and finally leave the recovery box 1 under the action of a gas pump;
the sedimentation belt 2 carries the waste wadding layer to leave the recovery box 1 and then passes through the area where the protruding block 6 is located, and during the period that the sedimentation belt 2 carries the waste wadding layer to pass through the protruding block 6, the area where the sedimentation belt 2 contacts with the protruding block 6 forms the same bending angle with the protruding block 6, so that the acting force between the waste wadding layer at the protruding part of the protruding block 6 and the sedimentation belt 2 is reduced, and the waste wadding is separated from the sedimentation belt 2;
the liquid supply pipe 9 is obliquely upwards arranged, an oblique notch is formed in one side of the liquid supply pipe 9, the oblique notch of the liquid supply pipe 9 is attached to one side surface of the sedimentation belt 2, and a water outlet of the liquid supply pipe 9 is obliquely upwards so as to reduce the impact of the vulcanized black dyeing waste liquid after leaving the liquid supply pipe 9, and part of the impact force of the vulcanized black dyeing waste liquid acts on the surface of the sedimentation belt 2 to impact the waste batting attached to the surface of the sedimentation belt 2 all the time.
It is noted that relational terms such as first and second, and the like are used solely to distinguish one entity or action from another entity or action without necessarily requiring or implying any actual such relationship or order between such entities or actions. Moreover, the terms "comprises," "comprising," or any other variation thereof, are intended to cover a non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements does not include only those elements but may include other elements not expressly listed or inherent to such process, method, article, or apparatus.
Finally, it should be noted that: the foregoing description is only a preferred embodiment of the present invention, and the present invention is not limited thereto, but it is to be understood that modifications and equivalents of some of the technical features described in the foregoing embodiments may be made by those skilled in the art, although the present invention has been described in detail with reference to the foregoing embodiments. Any modification, equivalent replacement, improvement, etc. made within the spirit and principle of the present invention should be included in the protection scope of the present invention.
Claims (3)
1. The utility model provides a waste liquid recovery processing device after vulcanization black coloring agent dyes, includes collection box (1) and air pump, its characterized in that: the recovery box (1) is used for temporarily storing the vulcanized black dyeing waste liquid, and a heating part, a liquid supply part, a sedimentation part and a driving part are arranged in the recovery box (1);
the heating component is positioned below the liquid level of the black sulfide dyeing waste liquid, the heating component is used for heating the black sulfide dyeing waste liquid, one side of the liquid supply component is provided with the sedimentation belt (2), the liquid supply component is used for continuously outputting the black sulfide dyeing waste liquid, the output direction of the liquid supply component is the side where the sedimentation belt (2) is positioned, the sedimentation component is used for collecting waste batting in the black sulfide dyeing waste liquid, and the driving component provides power required by movement for the sedimentation belt (2);
a protruding block (6) is arranged on one side of the recovery box (1), the sedimentation belt (2) slides along the outer walls of the recovery box (1) and the protruding block (6), the cross section of the recovery box (1) is triangular, and the protruding block (6) is used for separating waste batting from the sedimentation belt (2);
the sedimentation component comprises a power component (3), an extrusion component (4) and an air extraction component (5), wherein the air extraction component (5) is connected with an air pump, the power component (3) is used for realizing the movement of the sedimentation belt (2) along the outer wall of the recovery box (1), the extrusion component (4) is used for extruding the sedimentation belt (2), and the air extraction component (5) is used for absorbing waste gas generated after heating the vulcanized black dyeing waste liquid;
the power assembly (3) is positioned above the liquid level of the vulcanized black dyeing waste liquid, the power assembly (3) comprises a driving shaft (301) arranged in the recovery box (1), the driving shaft (301) is connected with the air extraction assembly (5), a plurality of deflection plates (302) are arranged on the outer wall of the driving shaft (301), the driving shaft (301) is connected with the extrusion assembly (4), and the driving shaft (301) is connected with the deflection plates (302) through a spring shaft;
the extrusion assembly (4) comprises limit rollers (401) arranged on two sides of the driving shaft (301), the sedimentation belt (2) penetrates through a gap between the driving shaft (301) and the two limit rollers (401) in an S shape, and a plurality of triangular blocks (402) are arranged on the outer wall of the deflection plate (302);
the air extraction assembly (5) comprises an arc-shaped plate (501) arranged in the driving shaft (301), an opening of the arc-shaped plate (501) faces downwards, an inner shaft (502) is arranged in the middle of the arc-shaped plate (501), a through hole is formed in the middle of the inner shaft (502), and the inner shaft (502) is connected with the air pump;
the sedimentation component comprises an aggregation component (7) and a waste liquid outlet (8) which are arranged in the recovery box (1), wherein the aggregation component (7) and the waste liquid outlet (8) are vertically distributed, the sedimentation belt (2) passes through the aggregation component (7) and the waste liquid outlet (8), a guide plate (701) is arranged in the aggregation component (7), the lower end surface of the guide plate (701) is attached to the upper end surface of the sedimentation belt (2), and the longitudinal section of the guide plate (701) is triangular.
2. The device for recycling waste liquid after dyeing with a sulfur black coloring agent according to claim 1, wherein the device comprises: the liquid supply part comprises a liquid supply pipe (9) arranged on one side of the sedimentation belt (2), the liquid supply pipe (9) is obliquely upwards arranged, an inclined notch is formed in one side of the liquid supply pipe (9), the inclined notch of the liquid supply pipe (9) is attached to the surface of one side of the sedimentation belt (2), and the water outlet of the liquid supply pipe (9) is higher than the liquid level of the black sulfide dyeing waste liquid.
3. The device for recycling waste liquid after dyeing with a sulfur black coloring agent according to claim 1, wherein the device comprises: the heating component comprises a heating plate (10) arranged in the recovery box (1), the cross section of the heating plate (10) is rectangular, and the heating plate (10) is connected with the recovery box (1) through a rotating shaft.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202211502799.5A CN115726118B (en) | 2022-11-28 | 2022-11-28 | Waste liquid recovery treatment device after dyeing of vulcanized black coloring agent |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202211502799.5A CN115726118B (en) | 2022-11-28 | 2022-11-28 | Waste liquid recovery treatment device after dyeing of vulcanized black coloring agent |
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| CN115726118A CN115726118A (en) | 2023-03-03 |
| CN115726118B true CN115726118B (en) | 2024-03-19 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN202211502799.5A Active CN115726118B (en) | 2022-11-28 | 2022-11-28 | Waste liquid recovery treatment device after dyeing of vulcanized black coloring agent |
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| CN117485973B (en) * | 2023-12-29 | 2024-03-15 | 常州市春晖纺织染整有限公司 | Textile winding device with drying and wrinkle removing functions |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1049545A (en) * | 1964-04-06 | 1966-11-30 | Fleissner Gerold | Apparatus for the treatment of textile material |
| EP0353963A1 (en) * | 1988-08-01 | 1990-02-07 | Milliken Research Corporation | Cleaning aid for dyeing apparatus |
| CN107879503A (en) * | 2017-10-30 | 2018-04-06 | 张�浩 | A kind of garbage, waste-water filter |
| CN217511322U (en) * | 2022-04-29 | 2022-09-30 | 重庆鑫科新型建筑材料有限责任公司 | Stirring station waste water recovery device |
-
2022
- 2022-11-28 CN CN202211502799.5A patent/CN115726118B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1049545A (en) * | 1964-04-06 | 1966-11-30 | Fleissner Gerold | Apparatus for the treatment of textile material |
| EP0353963A1 (en) * | 1988-08-01 | 1990-02-07 | Milliken Research Corporation | Cleaning aid for dyeing apparatus |
| CN107879503A (en) * | 2017-10-30 | 2018-04-06 | 张�浩 | A kind of garbage, waste-water filter |
| CN217511322U (en) * | 2022-04-29 | 2022-09-30 | 重庆鑫科新型建筑材料有限责任公司 | Stirring station waste water recovery device |
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| CN115726118A (en) | 2023-03-03 |
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