CN107803387A - Viscose waste residue processing system - Google Patents

Viscose waste residue processing system Download PDF

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Publication number
CN107803387A
CN107803387A CN201711086427.8A CN201711086427A CN107803387A CN 107803387 A CN107803387 A CN 107803387A CN 201711086427 A CN201711086427 A CN 201711086427A CN 107803387 A CN107803387 A CN 107803387A
Authority
CN
China
Prior art keywords
waste residue
storage tank
controller
retort
viscose glue
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.)
Pending
Application number
CN201711086427.8A
Other languages
Chinese (zh)
Inventor
胡小东
廖廷高
官磊
刘潘
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.)
Yibin Grace Group Co Ltd
Original Assignee
Yibin Grace Group 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 Yibin Grace Group Co Ltd filed Critical Yibin Grace Group Co Ltd
Priority to CN201711086427.8A priority Critical patent/CN107803387A/en
Publication of CN107803387A publication Critical patent/CN107803387A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/80Destroying solid waste or transforming solid waste into something useful or harmless involving an extraction step
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B09DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09BDISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B5/00Operations not covered by a single other subclass or by a single other group in this subclass

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  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Separation Of Suspended Particles By Flocculating Agents (AREA)

Abstract

The invention discloses a viscose waste residue treatment system, which comprises a waste glue storage tank and is characterized in that: the outlet end of the waste rubber storage tank is sequentially connected with a butterfly separator, a waste residue reaction tank, a filter press and an incinerator through pipelines; the waste residue reaction tank is also connected with a concentrated sulfuric acid storage tank, a coagulant aid storage tank and a flocculating agent storage tank through pipelines; a PH sensor and a controller are arranged on the waste residue reaction tank, the input end of the controller is connected with the PH sensor, and the output end of the controller is connected with an electromagnetic valve; the invention can separate the waste residue in the viscose glue and finally treat the waste residue in a burning way, thereby realizing the harmless treatment of the viscose glue waste residue and having the advantages of small environmental pollution, good treatment effect and the like.

Description

A kind of viscose glue Solid state fermentation system
Technical field
The present invention relates to viscose glue production technical field, and in particular to a kind of viscose glue Solid state fermentation system.
Background technology
Viscose rayon be pulp first and alkali reaction generation alkali cellulose, then alkali cellulose again in xanthating machine with curing Carbon reaction generation cellulose sulfonate, cellulose sulfonate are re-dissolved in sig water and rayon spinning stoste are made, and then viscose glue is spun Silk stock solution is filtered by filtration system, and substantial amounts of scrap rubber can be produced in filter process, and its main component is:Cellulose sulfonic acid Ester, hemicellulose, weathering alkali cellulose, alkali and carbon disulfide etc.;In the prior art be usually scrap rubber is diluted, separate after obtain Clean dilution fly glue be used for configure yellow lysate, realize the recycling to scrap rubber, but scrap rubber is through diluting and separating Certain waste residue can be produced afterwards, for this part waste residue prior art is directly discharged in trench, and it is dirty to there is larger environment Dye problem, it is therefore desirable to which harmless treatment is carried out to reduce the pollution to environment to the part waste residue.
The content of the invention
For the defects of environmental pollution is larger present in prior art, the invention discloses a kind of viscose glue Solid state fermentation system System, the system can be thoroughly handled viscose glue, effectively reduce pollution of the scrap rubber processing procedure to environment.
The present invention is achieved through the following technical solutions above-mentioned purpose:
A kind of viscose glue Solid state fermentation system, including scrap rubber storage tank, it is characterised in that:The scrap rubber storage tank port of export passes through pipe Road is connected with butterfly seperator, waste residue retort, filter press and incinerator in turn;The waste residue retort is also connected by pipeline There are concentrated sulfuric acid storage tank, flocculation aid storage tank and flocculant storage tank;PH sensor and control are provided with the waste residue retort Device processed, the controller input are connected with Ph sensors, and controller output end is connected with magnetic valve.
Agitating paddle is provided with the waste residue retort, the agitating paddle is connected with stirring motor;Stirring motor passes through change Frequency device is connected with controller.
Liquid level gauge and alkali densimeter, the liquid level gauge and alkali densimeter and controller are additionally provided with the waste residue retort It is connected.
Surge tank is additionally provided between the waste residue retort and filter press, centrifugal pump is provided with the surge tank.
On the concentrated sulfuric acid storage tank, flocculation aid storage tank and flocculant storage tank and the connecting pipe of waste residue retort Electromagnetic flow valve is provided with, the electromagnetic flow valve is connected with controller.
The main component of the flocculation aid is polyacrylamide.
The main polymerisation aluminium chloride of the flocculant.
Compared with prior art, the invention has the advantages that:
1st, scrap rubber retort of the invention is connected with concentrated sulfuric acid storage tank, flocculation aid storage tank and flocculant storage tank, by dense Sulfuric acid, flocculation aid and flocculant etc. are reacted with viscose glue waste residue, so that can not recoverer by weathering cellulose in scrap rubber etc. Burned after analyzing, so as to thoroughly be handled the major pollutants in viscose glue, avoid viscose glue waste residue to environment Pollution.
2nd, agitating paddle is provided with waste residue retort of the invention, the agitating paddle passes through motor and frequency converter and controller It is connected, the mixing velocity of various materials is on the one hand accelerated by agitating paddle and makes its mixing more uniform, between various materials Reaction can be carried out fully;On the other hand the speed of stirring can be easily adjusted by frequency converter, both ensure that the matter of stirring Amount, while energy consumption is reduced, so as to reduce production cost.
3rd, be provided with liquid level gauge and alkali densimeter in waste residue retort of the invention, the liquid level gauge and alkali densimeter with Controller is connected, and the convenient concentration of lye for gathering the content of mixture in alkaline reaction tank, is provided substantially for the control of controller Data supporting, improve the automaticity of system.
4th, the present invention is provided with surge tank between waste residue retort and filter press, ensures the continuity of filter press work, So as to improve operating efficiency.
5th, the present invention is in concentrated sulfuric acid storage tank, flocculation aid storage tank and flocculant storage tank and the connecting tube of waste residue retort Electronic flow valve is provided with road, the electromagnetic flow valve is connected with controller, is advantageous to control the concentrated sulfuric acid, flocculation aid in real time With the addition of flocculant, enough additions of various reactants were both ensure that, turn avoid unnecessary waste, reduction is produced into This.
Brief description of the drawings
Fig. 1 is schematic structural view of the invention;
Reference:1st, scrap rubber storage tank, 2, butterfly seperator, 3, waste residue retort, 4, filter press, 5, incinerator, 6, dense sulphur Sour storage tank, 7, flocculation aid storage tank, 8, flocculant storage tank, 9, PH sensor, 10, controller, 11, electromagnetic flow valve, 12, Agitating paddle, 13, stirring motor, 14, frequency converter, 15, liquid level gauge, 16, alkali densimeter, 17, surge tank, 18, centrifugal pump.
Embodiment
It will be described further below by the way that specific embodiment is new to this practicality
Embodiment 1
The present embodiment is as highly preferred embodiment of the present invention, and it discloses a kind of viscose glue Solid state fermentation system, concrete structure such as Fig. 1 Shown, including scrap rubber storage tank 1, the port of export of the scrap rubber storage tank 1 is connected with butterfly seperator 2, useless in turn by pipeline Slag retort 3, filter press 4 and incinerator 5;The waste residue retort 3 also by pipeline be connected with concentrated sulfuric acid storage tank 6, help it is solidifying Agent storage tank 7 and flocculant storage tank 8;PH sensor 9 is provided with the scrap rubber retort 3, is provided with scrap rubber retort 3 Controller 10, the input of controller 10 are connected with PH sensor 9, and the port of export of the scrap rubber retort 3 is provided with electromagnetism Flow valve 11, the electromagnetic flow valve 11 are connected with controller 10;The concentrated sulfuric acid storage tank 6, flocculation aid storage tank 7 and flocculation Agent storage tank 8 is with being provided with electromagnetic flow valve 11, the electromagnetic flow valve 11 and control on the connecting pipe of waste residue retort 3 Device 10 is connected.
Agitating paddle 12 is provided with the waste residue retort 3, the agitating paddle 12 is connected with stirring motor 13;Stirring motor 13 are connected by frequency converter 14 with controller 10.
Liquid level gauge 15 and alkali densimeter 16, the liquid level gauge 15 and alkali densimeter are additionally provided with the waste residue retort 3 16 are connected with controller 10.
Surge tank 17 is additionally provided between the waste residue retort 3 and filter press 4, centrifugation is provided with the surge tank 17 Pump 18.
The main component of the flocculation aid is polyacrylamide.
The main polymerisation aluminium chloride of the flocculant.
The present invention is by the way that the concentrated sulfuric acid, flocculation aid and flocculant are mixed with viscose glue waste residue, by the weathering cellulose in viscose glue The like waste separates out, then is separated weathering cellulose and viscose liquid by filter press, the side for finally burning weathering cellulose Formula is thoroughly handled the waste residue in viscose glue, and it has the advantages that high treating effect, environmental pollution is small.

Claims (7)

1. a kind of viscose glue Solid state fermentation system, including scrap rubber storage tank(1), it is characterised in that:The scrap rubber storage tank(1)Outlet End is connected with butterfly seperator in turn by pipeline(2), waste residue retort(3), filter press(4)And incinerator(5);The waste residue Retort(1)Concentrated sulfuric acid storage tank is also connected with by pipeline(6), flocculation aid storage tank(7)With flocculant storage tank(8);Institute State waste residue retort(3)On be provided with PH sensor(9)And controller(10), the controller(10)Input and PH sensor (9)It is connected, controller(10)Output end is connected with electromagnetic flow valve(11).
A kind of 2. viscose glue Solid state fermentation system according to claim 1, it is characterised in that:The waste residue retort(3)It is interior It is provided with agitating paddle(12), the agitating paddle(12)It is connected with stirring motor(13);Stirring motor(13)Pass through frequency converter(14) With controller(10)It is connected.
A kind of 3. viscose glue Solid state fermentation system according to claim 1, it is characterised in that:The waste residue retort(3)It is interior It is additionally provided with liquid level gauge(15)And alkali densimeter(16), the liquid level gauge(15)With alkali densimeter(16)With controller(10)Phase Even.
A kind of 4. viscose glue Solid state fermentation system according to claim 1, it is characterised in that:The waste residue retort(3)With Filter press(4)Between be additionally provided with surge tank(17), the surge tank(17)Inside it is provided with centrifugal pump(18).
A kind of 5. viscose glue Solid state fermentation system according to claim 1, it is characterised in that:The concentrated sulfuric acid storage tank(6)、 Flocculation aid storage tank(7)With flocculant storage tank(8)With waste residue retort(3)Connecting pipe on be provided with electromagnetic flow valve (11), the electromagnetic flow valve(11)With controller(10)It is connected.
A kind of 6. viscose glue Solid state fermentation system according to claim 1, it is characterised in that:The main component of the flocculation aid For polyacrylamide.
A kind of 7. viscose glue Solid state fermentation system according to claim 1, it is characterised in that:The main polymerisation of the flocculant Aluminium chloride.
CN201711086427.8A 2017-11-07 2017-11-07 Viscose waste residue processing system Pending CN107803387A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711086427.8A CN107803387A (en) 2017-11-07 2017-11-07 Viscose waste residue processing system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711086427.8A CN107803387A (en) 2017-11-07 2017-11-07 Viscose waste residue processing system

Publications (1)

Publication Number Publication Date
CN107803387A true CN107803387A (en) 2018-03-16

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CN201711086427.8A Pending CN107803387A (en) 2017-11-07 2017-11-07 Viscose waste residue processing system

Country Status (1)

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CN (1) CN107803387A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109133447A (en) * 2018-11-06 2019-01-04 宜宾海丝特纤维有限责任公司 A kind of on-line monitoring system and method for viscose glue waste liquid
CN111001651A (en) * 2019-12-20 2020-04-14 宜宾丝丽雅股份有限公司 Waste residue treatment method and system in viscose fiber production

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201192589Y (en) * 2008-03-19 2009-02-11 大庆市乾晟机械制造有限公司 Slime water separation device
CN205146863U (en) * 2015-10-29 2016-04-13 郑州经纬科技实业有限公司 Electrolytic aluminum slot liner innocent treatment device that gives up
CN205874100U (en) * 2016-07-11 2017-01-11 无锡蓝海工程设计有限公司 High -efficient materialization pretreatment systems of viscose staple fibre dimension waste water
CN206188530U (en) * 2016-10-26 2017-05-24 北京华福环境工程科技有限公司 Viscose fiber wastewater advanced treatment device
CN206232640U (en) * 2016-11-28 2017-06-09 宜宾海丝特纤维有限责任公司 A kind of processing unit suitable for the fibre of high concentration half
CN206232531U (en) * 2016-11-28 2017-06-09 宜宾海丝特纤维有限责任公司 A kind of processing unit suitable for highly concentrated half fibre
CN207756594U (en) * 2017-11-07 2018-08-24 宜宾丝丽雅股份有限公司 Viscose waste residue processing system

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN201192589Y (en) * 2008-03-19 2009-02-11 大庆市乾晟机械制造有限公司 Slime water separation device
CN205146863U (en) * 2015-10-29 2016-04-13 郑州经纬科技实业有限公司 Electrolytic aluminum slot liner innocent treatment device that gives up
CN205874100U (en) * 2016-07-11 2017-01-11 无锡蓝海工程设计有限公司 High -efficient materialization pretreatment systems of viscose staple fibre dimension waste water
CN206188530U (en) * 2016-10-26 2017-05-24 北京华福环境工程科技有限公司 Viscose fiber wastewater advanced treatment device
CN206232640U (en) * 2016-11-28 2017-06-09 宜宾海丝特纤维有限责任公司 A kind of processing unit suitable for the fibre of high concentration half
CN206232531U (en) * 2016-11-28 2017-06-09 宜宾海丝特纤维有限责任公司 A kind of processing unit suitable for highly concentrated half fibre
CN207756594U (en) * 2017-11-07 2018-08-24 宜宾丝丽雅股份有限公司 Viscose waste residue processing system

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
邓晨野;张爽;: "DBP-50型离心机在废胶回收中的应用", 人造纤维, vol. 1, no. 01, pages 177 - 178 *
邬国铭: "《高分子材料加工工艺》", vol. 1, 中国纺织出版社, pages: 230 - 231 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109133447A (en) * 2018-11-06 2019-01-04 宜宾海丝特纤维有限责任公司 A kind of on-line monitoring system and method for viscose glue waste liquid
CN111001651A (en) * 2019-12-20 2020-04-14 宜宾丝丽雅股份有限公司 Waste residue treatment method and system in viscose fiber production

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Application publication date: 20180316

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