CN207294534U - A kind of textile waste processing system - Google Patents

A kind of textile waste processing system Download PDF

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Publication number
CN207294534U
CN207294534U CN201721314199.0U CN201721314199U CN207294534U CN 207294534 U CN207294534 U CN 207294534U CN 201721314199 U CN201721314199 U CN 201721314199U CN 207294534 U CN207294534 U CN 207294534U
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CN
China
Prior art keywords
sedimentation basin
reaction tank
tank
processing system
waste processing
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.)
Expired - Fee Related
Application number
CN201721314199.0U
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Chinese (zh)
Inventor
丁秋红
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Philip (zhangjiagang) Special Textile Co Ltd
Original Assignee
Philip (zhangjiagang) Special Textile Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Philip (zhangjiagang) Special Textile Co Ltd filed Critical Philip (zhangjiagang) Special Textile Co Ltd
Priority to CN201721314199.0U priority Critical patent/CN207294534U/en
Application granted granted Critical
Publication of CN207294534U publication Critical patent/CN207294534U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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Abstract

This application discloses a kind of textile waste processing system, including the grille well being sequentially communicated by pipeline, regulating reservoir, first reaction tank, first sedimentation basin, hydrolytic tank, aerobic tank, second sedimentation basin, second reaction tank and the 3rd sedimentation basin, first sedimentation basin, the sludge outlet of second sedimentation basin and the 3rd sedimentation basin has been respectively communicated with a mud-collecting well, the mud-collecting well has been sequentially communicated sludge concentration tank and belt filter press by sludge pump, belt filter press is connected with air compressor machine, heat exchanging pipe is arranged with the outside of first reaction tank and the second reaction tank, heat exchanger is provided between the floss hole of the heat exchanging pipe and the 3rd sedimentation basin, sewage pump is provided between the regulating reservoir and the first reaction tank.The utility model system heats the first reaction tank and the second reaction tank by the waste water after heating, improves reaction efficiency, and after the first reaction tank and the heat exchange of the second reaction tank, waste water obtains certain cooling, then can directly discharge or secondary heat recovery and utilization.

Description

A kind of textile waste processing system
Technical field
This application involves environmental protection and textile technology field, more particularly to a kind of textile waste processing system.
Background technology
In process of textile production, containing organic matters such as hairiness, surfactants in its waste water produced, if the waste water is straight Run in and put, it will environment is caused greatly to destroy.
Utility model content
The purpose of this utility model is to provide a kind of textile waste processing system, to overcome deficiency of the prior art.
To achieve the above object, the utility model provides following technical solution:
The embodiment of the present application discloses a kind of textile waste processing system, including grille well, the tune being sequentially communicated by pipeline Save pond, the first reaction tank, the first sedimentation basin, hydrolytic tank, aerobic tank, the second sedimentation basin, the second reaction tank and the 3rd sedimentation basin, institute The sludge outlet for stating the first sedimentation basin, the second sedimentation basin and the 3rd sedimentation basin has been respectively communicated with a mud-collecting well, which passes through Sludge pump has been sequentially communicated sludge concentration tank and belt filter press, and the belt filter press is connected with air compressor machine, and described first is anti- Heat exchanging pipe is arranged with the outside of Ying Chi and the second reaction tank, is set between the heat exchanging pipe and the floss hole of the 3rd sedimentation basin There is heat exchanger, sewage pump is provided between the regulating reservoir and the first reaction tank.
Preferably, in above-mentioned textile waste processing system, the bottom of the regulating reservoir is provided with gas distribution pipe, the cloth Multiple stomatas are distributed with tracheae.
Preferably, in above-mentioned textile waste processing system, first sedimentation basin, the second sedimentation basin and the 3rd precipitation Pond includes a cavity with taper bottom surface and the mud scraper being provided with cavity respectively.
Preferably, in above-mentioned textile waste processing system, first reaction tank and the second reaction tank include respectively One mixer and explosive-feeding processing device.
Preferably, in above-mentioned textile waste processing system, the bottom of the hydrolytic tank and aerobic tank is distributed with respectively Snorkel, is distributed with multiple stomatas on the snorkel.
Preferably, in above-mentioned textile waste processing system, set between the sludge concentration tank and belt filter press There is screw pump.
Compared with prior art, the utility model has the advantage of:The utility model system can be efficient by three sedimentation basins Ground handles textile waste, and the waste water after processing meets direct discharge standard, in order to further improve treatment effeciency, passes through Waste water after heating heats the first reaction tank and the second reaction tank, improves reaction efficiency, by the first reaction tank and the After the heat exchange of two reaction tanks, waste water obtains certain cooling, then can directly discharge or secondary heat recovery and utilization.
Brief description of the drawings
In order to illustrate the technical solutions in the embodiments of the present application or in the prior art more clearly, below will be to embodiment or existing There is attached drawing needed in technology description to be briefly described, it should be apparent that, drawings in the following description are only this Some embodiments described in application, for those of ordinary skill in the art, without creative efforts, Other attached drawings can also be obtained according to these attached drawings.
Fig. 1 show the principle schematic of textile waste processing system in the utility model specific embodiment.
Embodiment
The following is a combination of the drawings in the embodiments of the present utility model, and the technical scheme in the embodiment of the utility model is carried out Detailed description, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole implementation Example.Based on the embodiment in the utility model, those of ordinary skill in the art institute on the premise of creative work is not made The every other embodiment obtained, shall fall within the protection scope of the present invention.
With reference to shown in Fig. 1, textile waste processing system, including be sequentially communicated by pipeline grille well 1, regulating reservoir 2, One reaction tank 3, the first sedimentation basin 4, hydrolytic tank 5, aerobic tank 6, the second sedimentation basin 7, the second reaction tank 8 and the 3rd sedimentation basin 9, the The sludge outlet of one sedimentation basin 4, the second sedimentation basin 7 and the 3rd sedimentation basin 9 has been respectively communicated with a mud-collecting well 10, and the mud-collecting well 10 is logical To cross sludge pump 11 and be sequentially communicated sludge concentration tank 12 and belt filter press 13, belt filter press 13 is connected with air compressor machine 14, the The outside of one reaction tank 3 and the second reaction tank 8 is arranged with heat exchanging pipe, is set between heat exchanging pipe and the floss hole of the 3rd sedimentation basin Heat exchanger 15 is equipped with, sewage pump 16 is provided between 2 and first reaction tank 3 of regulating reservoir.
In the technical solution, system efficiently can be handled textile waste by three sedimentation basins, after processing Waste water meets direct discharge standard, in order to further improve treatment effeciency, by the waste water after heating to the first reaction tank and Two reaction tanks are heated, and improve reaction efficiency, and after the first reaction tank and the heat exchange of the second reaction tank, waste water obtains certain Cooling, then can directly discharge or secondary heat recovery and utilization.
In this case, grille well is for intercepting bulk slag in sewage, ensureing the normal operation of pump;Sewage passes through grille well Afterwards, the visible foreign in water and hair etc. can generally be disposed.
In this case, the influence of water and water quality variation to waste water treatment process process can be reduced by regulating reservoir, in addition The subsequent treatment structures inflow that interior energy is equalized during operation and the water quality stablized can also be made by regulating reservoir, and Reach preferable treatment effect.
In this case, hydrolytic tank processing method is a kind of between the aerobic method between Anaerobic Treatment method, and other techniques Combination can reduce processing cost and improve treatment effeciency.Hydrolysis acidification technique is according to methanogen and the hydrolysis acid-producing bacteria speed of growth Difference, by Anaerobic Treatment control in shorter the first and second stage of Anaerobic Treatment in reaction time, i.e., in a large amount of hydrolytic bacterias, acid It by insoluble hydrolysis of organic matter is dissolved organic matter to change under bacterium effect, and the macromolecular substances of difficult for biological degradation are converted into easy life The process of the small-molecule substance of thing degraded, so as to improve the biodegradability of waste water, good basis is established for subsequent treatment.
In the technical solution, oxidation pond processing method is a kind of biomembrane between activated sludge process and biofilter Method technique, its main feature is that setting filler in pond, bottom of pond aeration is oxygenated sewage, and sewage in pond body is in flowing shape State, to ensure that sewage comes into full contact with the filler in sewage, avoids contacting not with filler there are sewage in biological contact oxidation pond The defects of equal.The basic principle of its purification waste water is identical with general biofilm, and the organic matter in waste water is adsorbed with biomembrane, Under conditions of aerobic, organic matter is decomposed by microbiological oxidation, and waste water is purified.
Further, the bottom of regulating reservoir 2 is provided with gas distribution pipe 17, and multiple stomatas are distributed with gas distribution pipe.
Further, the first sedimentation basin 4, the second sedimentation basin 7 and the 3rd sedimentation basin 9 include one respectively has taper bottom surface Cavity 18 and the mud scraper 19 being provided with cavity.
Further, the first reaction tank 3 and the second reaction tank 8 include a mixer 20 and explosive-feeding processing device respectively.
Further, snorkel 21 is distributed with the bottom of hydrolytic tank 5 and aerobic tank 6 respectively, is distributed with snorkel 21 more A stomata.
Further, screw pump 22 is provided between sludge concentration tank 12 and belt filter press 13.
In the technical solution, belt filter press is in quiet, dynamic by the sludge by concentration with certain density flocculant After being sufficiently mixed in mixer, the minute solid particles coacervation in sludge is isolated at the same time into the larger cotton-shaped agglomerate of volume Free water, the sludge after flocculation are transported on the strainer of concentration gravity dehydration, and Free water is separated under gravity, shape Into the sludge of not flow regime, be then clamped between two guipures up and down, by wedge-shaped precompressed zone, low-pressure area and higher-pressure region by It is small to arrive under big extruding force, shearing force, sludge is progressively extruded, to reach maximum mud, water separates, and eventually forms filter Cake is discharged.
It should be noted that herein, relational terms such as first and second and the like are used merely to a reality Body or operation are distinguished with another entity or operation, are deposited without necessarily requiring or implying between these entities or operation In any this actual relation or order.Moreover, term " comprising ", "comprising" or its any other variant are intended to Non-exclusive inclusion, so that process, method, article or equipment including a series of elements not only will including those Element, but also including other elements that are not explicitly listed, or further include as this process, method, article or equipment Intrinsic key element.In the absence of more restrictions, the key element limited by sentence "including a ...", it is not excluded that Also there are other identical element in process, method, article or equipment including the key element.
The above is only the embodiment of the application, it is noted that for the ordinary skill people of the art For member, on the premise of the application principle is not departed from, some improvements and modifications can also be made, these improvements and modifications also should It is considered as the protection domain of the application.

Claims (6)

  1. A kind of 1. textile waste processing system, it is characterised in that including be sequentially communicated by pipeline grille well, regulating reservoir, One reaction tank, the first sedimentation basin, hydrolytic tank, aerobic tank, the second sedimentation basin, the second reaction tank and the 3rd sedimentation basin, described first The sludge outlet of sedimentation basin, the second sedimentation basin and the 3rd sedimentation basin has been respectively communicated with a mud-collecting well, which passes through sludge pump Be sequentially communicated sludge concentration tank and belt filter press, the belt filter press is connected with air compressor machine, first reaction tank and Heat exchanging pipe is arranged with the outside of second reaction tank, heat exchange is provided between the heat exchanging pipe and the floss hole of the 3rd sedimentation basin Device, sewage pump is provided between the regulating reservoir and the first reaction tank.
  2. 2. textile waste processing system according to claim 1, it is characterised in that:The bottom of the regulating reservoir is provided with cloth Tracheae, is distributed with multiple stomatas on the gas distribution pipe.
  3. 3. textile waste processing system according to claim 1, it is characterised in that:First sedimentation basin, the second precipitation Pond and the 3rd sedimentation basin include a cavity with taper bottom surface and the mud scraper being provided with cavity respectively.
  4. 4. textile waste processing system according to claim 1, it is characterised in that:First reaction tank and the second reaction Pond includes a mixer and explosive-feeding processing device respectively.
  5. 5. textile waste processing system according to claim 1, it is characterised in that:The bottom of the hydrolytic tank and aerobic tank Snorkel is distributed with respectively, multiple stomatas are distributed with the snorkel.
  6. 6. textile waste processing system according to claim 1, it is characterised in that:The sludge concentration tank and belt press filtration Screw pump is provided between machine.
CN201721314199.0U 2017-10-12 2017-10-12 A kind of textile waste processing system Expired - Fee Related CN207294534U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721314199.0U CN207294534U (en) 2017-10-12 2017-10-12 A kind of textile waste processing system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721314199.0U CN207294534U (en) 2017-10-12 2017-10-12 A kind of textile waste processing system

Publications (1)

Publication Number Publication Date
CN207294534U true CN207294534U (en) 2018-05-01

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721314199.0U Expired - Fee Related CN207294534U (en) 2017-10-12 2017-10-12 A kind of textile waste processing system

Country Status (1)

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CN (1) CN207294534U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI715110B (en) * 2018-07-19 2021-01-01 德商艾瑞岡研究發展公司 Vorrichtung und verfahren zur reinigung von mit elektrolyten und farbstoffen verunreinigtem abwasser

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI715110B (en) * 2018-07-19 2021-01-01 德商艾瑞岡研究發展公司 Vorrichtung und verfahren zur reinigung von mit elektrolyten und farbstoffen verunreinigtem abwasser

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CF01 Termination of patent right due to non-payment of annual fee
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Granted publication date: 20180501

Termination date: 20201012