CN105332311B - Papermaking to zero discharge standard production line - Google Patents

Papermaking to zero discharge standard production line Download PDF

Info

Publication number
CN105332311B
CN105332311B CN201510844791.0A CN201510844791A CN105332311B CN 105332311 B CN105332311 B CN 105332311B CN 201510844791 A CN201510844791 A CN 201510844791A CN 105332311 B CN105332311 B CN 105332311B
Authority
CN
China
Prior art keywords
stock
water
pump
biological treatment
eddy flow
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201510844791.0A
Other languages
Chinese (zh)
Other versions
CN105332311A (en
Inventor
黄蒋元
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN201510844791.0A priority Critical patent/CN105332311B/en
Publication of CN105332311A publication Critical patent/CN105332311A/en
Application granted granted Critical
Publication of CN105332311B publication Critical patent/CN105332311B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The papermaking to zero discharge standard production line of the present invention, successively by hydrabrusher, conveying worm or stock pump, fiberizer, stock pump, defibrator, stock pump, two series connection stock tanks, stock pump, stock tank, stock pump, size-mixing tank, three stock pumps in parallel, three desanders in parallel, three cylinder moulds in parallel, be made up of vaccum dewatering box, squeezing rod, woollen blanket, carrying roller, drying cylinder, the paper machine formed into paper device, rewinding machine, cutting machine, baling press connection;Discharge waste water all to recycle, waste residue sludge carries out biological treatment and becomes organic fertilizer product;So as to realize zero-emission.

Description

Papermaking to zero discharge standard production line
Technical field
The invention belongs to a kind of papermaking to zero discharge standard and production line.
Background technology
Two production processes of slurrying and copy paper of paper waste in paper industry production.Slurrying is that plant is former Fiber separation in material comes out, and slurry is made, then can produce substantial amounts of paper waste through bleaching, this process;Copy paper is slurry Material dilution, shaping, squeezing, drying, are made paper, this process also easily produces paper waste.Paper waste is a kind of processing The larger industrial wastewater of difficulty, due to waste water, contained pollutant is sufficiently complex in itself, and papermaking to zero discharge standard is current trend.
The content of the invention
Present invention aims in view of the shortcomings of the prior art, propose a kind of papermaking to zero discharge standard production line.
The papermaking to zero discharge standard production line of the present invention, successively by hydrabrusher, conveying worm or stock pump, fiberizer, slurry Pump, defibrator, stock pump, two series connection 1#, 2# stock tanks, stock pump, 3# stock tanks, stock pump, size-mixing tank, three groups by stock pump, desanding Route that device and cylinder mould are composed in series is in parallel, by vaccum dewatering box, squeezing rod, woollen blanket, carrying roller, drying cylinder, form into paper device Paper machine, rewinding machine, cutting machine, baling press connection are formed;Waste water reclaiming device, Sewage treatment dress is arranged below in the paper machine Put and be connected to white water chest and emergent wastewater disposal basin, the white water chest is connected by pump with the eddy flow biological treatment tower of three series connection, end End eddy flow biological treatment tower is connected with regeneration cycle pond, and the regeneration cycle pond is provided with water pump and size-mixing tank, stock tank, waterpower Pulper, fiberizer, defibrator connection;The white water chest is connected provided with water pump with size-mixing tank;The rotation of three series connection The mud discharging pipe of stream biological treatment tower is connected with Treatment of Sludge organic fertilizer production device respectively;The drying cylinder connects with steam pipe Connect, the drying cylinder condensate pipe is connected with boiler;Sparge pipe, the hydrabrusher, fiber separation are provided with above the woollen blanket Sparge pipe, boiler above machine, woollen blanket are connected with running water pipe respectively.
The beneficial effect of the present invention compared with prior art:Discharge waste water all to recycle, waste residue sludge is carried out Biological treatment becomes organic fertilizer product;So as to realize zero-emission.
Brief description of the drawings
Fig. 1 --- papermaking to zero discharge standard production line flow process figure.
Fig. 2 --- the flow chart that papermaking to zero discharge standard production line numbering represents.
In figure:Hydrabrusher 1, conveying worm or stock pump 2, fiberizer 3, stock pump 4,6,8,10,12,14,15,16, Defibrator 5, stock tank 7,9, stock tank 11, size-mixing tank 13, desander 17,18,19, cylinder mould 20,21,22, vaccum dewatering box 23, Squeeze rod 24, woollen blanket 25, carrying roller 26, drying cylinder 27, into paper device 28, rewinding machine, cutting machine, baling press 29, eddy flow biological treatment Tower 30,31,32, regeneration cycle pond 33, water pump 34,36,38, Treatment of Sludge organic fertilizer production device 35, white water chest 37, meet an urgent need Wastewater disposal basin 39, paper pulp A1, waste paper A2, stone flour A3, paper product storehouse B1, fertilizer product storehouse B2, steam W, boiler P, running water pipe S, Condensate pipe S1, regeneration cycle water pipe S2, white water pipe S3.
Waste water reclaiming device is arranged below in the paper machine, and waste water reclaiming device is connected to white water chest and emergent wastewater disposal basin, The white water chest is connected by pump with the eddy flow biological treatment tower of three series connection, end eddy flow biological treatment tower and regeneration cycle water Pond connects, and the regeneration cycle pond is provided with water pump and connected with size-mixing tank, stock tank, hydrabrusher, fiberizer, defibrator Connect;The white water chest is connected provided with water pump with size-mixing tank;The mud discharging pipe point of the eddy flow biological treatment tower of three series connection It is not connected with Treatment of Sludge organic fertilizer production device;The drying cylinder is connected with steam pipe, and the drying cylinder condensate pipe connects with boiler Connect;Be provided with sparge pipe above the woollen blanket, the hydrabrusher, defibrator, the sparge pipe above woollen blanket, boiler are distinguished It is connected with running water pipe.
Embodiment
The invention will be further described below in conjunction with the accompanying drawings, but the implementation of the present invention is not limited to this.
As shown in the figure:The papermaking to zero discharge standard production line of the present invention, including hydrabrusher 1, conveying worm or stock pump 2, Fiberizer 3, stock pump 4,6,8,10,12,14,15,16, defibrator 5, stock tank 7,9, stock tank 11, size-mixing tank 13, desander 17th, 18,19, cylinder mould 20,21,22, vaccum dewatering box 23, squeezing rod 24, woollen blanket 25, carrying roller 26, drying cylinder 27, into paper device 28, Rewinding machine, cutting machine, baling press 29, eddy flow biological treatment tower 30,31,32, regeneration cycle pond 33, water pump 34,36,38 are dirty Mud processing organic fertilizer production device 35, white water chest 37, wastewater disposal basin 39 of meeting an urgent need, paper pulp A1, waste paper A2, stone flour A3, paper product storehouse B1, Fertilizer product storehouse B2, steam W, boiler P, running water pipe S, condensate pipe S1, regeneration cycle water pipe S2, white water pipe S3.
The papermaking to zero discharge standard production line of the present invention, successively by hydrabrusher, conveying worm or stock pump, fiberizer, slurry Pump, defibrator, stock pump, two series connection stock tanks, stock pump, stock tank, stock pump, size-mixing tank, three groups by stock pump, desander and cylinder mould The route that is composed in series is in parallel, by vaccum dewatering box, squeezing rod, woollen blanket, carrying roller, drying cylinder, the paper machine formed into paper device, multiple Volume machine, cutting machine, baling press connection are formed;Waste water reclaiming device is arranged below in the paper machine, and waste water reclaiming device is connected to White water chest and emergent wastewater disposal basin, the white water chest are connected with the eddy flow biological treatment tower of three series connection, end eddy flow biological treatment Tower is connected with regeneration cycle pond, the regeneration cycle pond be provided with water pump and size-mixing tank, stock tank, hydrabrusher, fiberizer, Defibrator connects;The white water chest is connected provided with water pump with size-mixing tank;The eddy flow biological treatment tower of three series connection Mud discharging pipe is connected with Treatment of Sludge organic fertilizer production device respectively;The drying cylinder is connected with steam pipe, the drying cylinder condensation Water pipe is connected with boiler;It is provided with sparge pipe above the woollen blanket, the hydrabrusher, defibrator, the spray above woollen blanket Water pipe, boiler are connected with running water pipe respectively.
The papermaking to zero discharge standard production line of the present invention, what well pumped has three places to use, and is domestic water respectively, makes Paper machine industrial water and boiler feed water.Domestic water is directly outer to be arranged;Industrial water is used for felt and cleans and produce cleaning etc., is produced Raw plain boiled water is pooled to white water chest;Boiler feed water supplies production and application for producing steam, and condensed water caused by industrial water returns Deliver to boiler recycling.Various production waste water are discharged into air by wastewater collection pond collection with boiler smoke heating evaporation.
White waste paper and wet pulp form paper pulp by hydrabrusher size degradation, and add talcum powder or starch, through fiber separation 1 is evacuated to after machine processing#Stock tank, through 2#、3#The stock tank of series connection, delivered into by stock pump and rush stock tank through 1#、2#Desander desanding, then by upper Slurry send 1#、2#Cylinder mould starching, paper pulp are transferred to woollen blanket through couch roll, are brought by woollen blanket to 1#、2#, vacuum tank be dehydrated, through pressure roller Cylinder dried is transferred into paper by carrying roller after squeezing, then through rewinding, cut, be packaged into finished product storage.
Mthod of white water from paper making main source has plain boiled water, felt washing water, vacuum tank plain boiled water and pressure caused by net filtration on paper pulp Plain boiled water caused by squeezing and carrying roller squeezing all flow to white water chest after collecting, the plain boiled water of white water chest is by being pumped to three eddy flows biologies Tower processing is managed, the plain boiled water treated through eddy flow biological treatment tower delivers to hydrabrusher, defibrator and rushes stock tank respectively to be made With.The afterbody waste water of sand cleaning machine is surfed the Net after desilting ditch flow to and rushes stock tank and paper pulp mixing certainly.
Eddy flow biological treatment tower:
Structure brief introduction:Volume 80m3, top is cylinder, and bottom is cone, and inside sets spiral to open sieve plate, plays water conservancy diversion And filtration, bottom interconnect, separate respective function with valve, can also pass through each own effect of switch complementary of valve.
Main working process:
Plain boiled water is from 1#The cylinder bottom of biological treatment tower enters, and helically sluggish flow rises to top from flowing to current 2#、3#Biological treatment tower, hydrabrusher size degradation slurry is delivered to respectively through treated plain boiled water, defibrator and punching slurry hole are dilute Release paper pulp use.Slurry is diluted to suitable concentration after size degradation and delivers to 1#、2#、3#Stock tank, so not having to typically in stock tank white Water.
(3), main operational principle:
The plain boiled water that paper machine is collected contains substantial amounts of aerobic bacteria, produced in plain boiled water using corruption value matter be main matter it is rotten starch, Rotten slurry, this is the main reason for hindering plain boiled water largely to reclaim use, and it can make smelly plain boiled water, fiber and other materials rot to become Matter;A large amount of chemicals accumulation can also hinder the recycling of plain boiled water in plain boiled water simultaneously.And the plain boiled water in Hunan and Guangxi paper mill is through eddy flow It can largely, for a long time be recycled after the processing of biological treatment tower, be because eddy flow biological treatment tower is water-tight equipment, completely cut off oxygen The entrance of gas, so that aerobic bacteria, dead without life condition, therefore largely recycle and be possibly realized for plain boiled water;Together When factory production fruit wrap to the less demanding of water quality, by simple processing, make bacterium in plain boiled water, fungi etc. aerobic Bacterium, which does not work, to meet the needs of production, and this is also that white water recycle can a large amount of reuse preconditions.
Containing large amount of organic matter cellulose and starch etc. in mthod of white water from paper making, while also have with talcum powder etc. for major auxiliary burden Material, be dissolved in after water and being formed using calcium ion as main cation.
Main function:
Suppress, kill aerobic bacteria, fungi grows, the white Organic substance in water is not sent out in eddy flow biological treatment tower Raw effect, so as to not produce rotten slurry, rotten slurry;Anaerobic bacteria, fungi are cultivated simultaneously, makes white Organic substance in water in eddy flow biological treatment Certain effect occurs in tower, anaerobic reaction to a certain degree occurs, carrying out mesophilic digestion obtains anion, sicker in plain boiled water Processing to a certain extent, also a certain degree of disinfective action.
When mthod of white water from paper making leaves eddy flow biological treatment tower because without or only a small amount of aerobic bacteria, fungi and certain Amount detests bacterium, therefore aerobe effect a small amount of effect without generation or only;And only a certain amount of anaerobic bacteria, that is, having It can not be acted under conditions of oxygen.
The formulation of process conditions:
Aerobic bacteria, the life condition of fungi be have abundant nutriment, sufficient oxygen and suitable temperature and PH value.And containing large amount of organic matter cellulose and suitable temperature in papermill whitewater, therefore plain boiled water eddy flow biological treatment tower Process conditions formulation, aerobic bacteria is not worked, in addition kill aerobic bacteria, its process conditions most important condition is scarce Oxygen processing environment, it is key factor to carry out eddy flow biological treatment tower encapsulation process, is secondly exactly the processing time for controlling plain boiled water, It is exactly the pH value and temperature for regulating plain boiled water again.Therefore with regard to the life condition and eddy flow biological treatment tower of aerobic bacteria the characteristics of Specially formulate following process conditions:
Oxygen content:Less than 5% or below 1mg/l.
Processing time:3h
Treatment temperature:30~40 DEG C
Plain boiled water pH value:6~8 (preferably no more than 8).

Claims (1)

  1. A kind of 1. papermaking to zero discharge standard production line, successively by hydrabrusher, conveying worm or stock pump, fiberizer, stock pump, fiber Seperator, stock pump, two series connection 1#, 2# stock tanks, stock pump, 3# stock tanks, stock pump, size-mixing tank, three groups by stock pump, desander and cylinder mould The route that is composed in series is in parallel, by vaccum dewatering box, squeezing rod, woollen blanket, carrying roller, drying cylinder, the paper machine formed into paper device, multiple Volume machine, cutting machine, baling press connection are formed;Waste water reclaiming device is arranged below in the paper machine, and waste water reclaiming device is connected to White water chest and emergent wastewater disposal basin, the white water chest are connected by pump with the eddy flow biological treatment tower of three series connection, the life of end eddy flow Thing treating column is connected with regeneration cycle pond, the regeneration cycle pond be provided with water pump and size-mixing tank, stock tank, hydrabrusher, Fiberizer, defibrator connection;The white water chest is connected provided with water pump with size-mixing tank;Three 1#, 2#, 3# rotations being sequentially connected in series The mud discharging pipe of stream biological treatment tower is connected with Treatment of Sludge organic fertilizer production device respectively;The drying cylinder connects with steam pipe Connect, the drying cylinder condensate pipe is connected with boiler;Sparge pipe, the hydrabrusher, fiber separation are provided with above the woollen blanket Sparge pipe, boiler above machine, woollen blanket are connected with running water pipe respectively;Main working process:Plain boiled water is successively from 1#Eddy flow biology The cylinder bottom for the treatment of column enters, and helically sluggish flow rises to top from flowing to 2 to current#、3#Eddy flow biological treatment tower, Hydrabrusher size degradation slurry is delivered to respectively through treated plain boiled water, and defibrator and punching slurry hole dilution paper pulp use;Slurry Suitable concentration is diluted to after size degradation and delivers to 1 for being connected to and being sequentially connected in series after defibrator respectively#、2#、3#Stock tank, so Stock tank does not have to plain boiled water;The formulation of process conditions:Aerobic bacteria, the life condition of fungi are that have abundant nutriment, abundance Oxygen and suitable temperature and pH value;And containing large amount of organic matter cellulose and suitable temperature in papermill whitewater, because The formulation of the process conditions of this plain boiled water eddy flow biological treatment tower, will make aerobic bacteria not work, or even kill aerobic bacteria, its The process conditions most important condition is anoxic treatment environment, and it is key factor to carry out eddy flow biological treatment tower encapsulation process, is secondly exactly The processing time of plain boiled water is controlled, is exactly the pH value and temperature for regulating plain boiled water again;Therefore with regard to the life condition of aerobic bacteria Following process conditions are specially formulated with the characteristics of eddy flow biological treatment tower:
    Oxygen content:Less than 5% or below 1mg/l;
    Processing time:3h
    Treatment temperature:30~40 DEG C
    Plain boiled water pH value:6~8.
CN201510844791.0A 2015-11-26 2015-11-26 Papermaking to zero discharge standard production line Active CN105332311B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510844791.0A CN105332311B (en) 2015-11-26 2015-11-26 Papermaking to zero discharge standard production line

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510844791.0A CN105332311B (en) 2015-11-26 2015-11-26 Papermaking to zero discharge standard production line

Publications (2)

Publication Number Publication Date
CN105332311A CN105332311A (en) 2016-02-17
CN105332311B true CN105332311B (en) 2017-12-15

Family

ID=55283054

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510844791.0A Active CN105332311B (en) 2015-11-26 2015-11-26 Papermaking to zero discharge standard production line

Country Status (1)

Country Link
CN (1) CN105332311B (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106248534A (en) * 2016-10-11 2016-12-21 广西大学 A kind of the change of temperature value in plain boiled water is utilized to carry out the system of early warning microstickies unstability
CN106939523B (en) * 2017-03-14 2019-01-25 傅承祖 A kind of waste paper regenerating process fundamentally solving waste paper regenerated pollution and equipment
CN112342827A (en) * 2020-10-29 2021-02-09 江苏理文造纸有限公司 Long net paper machine wire press portion spraying water-saving system
CN112811729A (en) * 2021-01-05 2021-05-18 玖龙纸业(太仓)有限公司 Water circulation system for pulping and papermaking

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3821073A (en) * 1971-10-15 1974-06-28 Karlstad Mekaniska Ab Multi-layer paper formation wherein outer layers are substantially free of bod substances
CN1710193A (en) * 2005-06-09 2005-12-21 西安交通大学 Process for realizing waste-water zero-discharge of papermaking from waste paper by anaerobic-aerobic treatment
CN1916273A (en) * 2005-08-17 2007-02-21 赵振平 Technique of zero discharge from closed circuit of white water for producing non-deinking regenerated paper
CN201261850Y (en) * 2008-05-07 2009-06-24 常州市英中电气有限公司 Equipment for producing high-density large insulating paperboard
CN101544452A (en) * 2009-05-05 2009-09-30 浙江省环境保护科学设计研究院 Composite anaerobic-aerobic process for treating waste paper making wastewater
CN205242169U (en) * 2015-11-26 2016-05-18 黄蒋元 Zero release papermaking production line

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN203229830U (en) * 2013-05-03 2013-10-09 连恩平 White-water recycling zero-discharge environmental papermaking equipment

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3821073A (en) * 1971-10-15 1974-06-28 Karlstad Mekaniska Ab Multi-layer paper formation wherein outer layers are substantially free of bod substances
CN1710193A (en) * 2005-06-09 2005-12-21 西安交通大学 Process for realizing waste-water zero-discharge of papermaking from waste paper by anaerobic-aerobic treatment
CN1916273A (en) * 2005-08-17 2007-02-21 赵振平 Technique of zero discharge from closed circuit of white water for producing non-deinking regenerated paper
CN201261850Y (en) * 2008-05-07 2009-06-24 常州市英中电气有限公司 Equipment for producing high-density large insulating paperboard
CN101544452A (en) * 2009-05-05 2009-09-30 浙江省环境保护科学设计研究院 Composite anaerobic-aerobic process for treating waste paper making wastewater
CN205242169U (en) * 2015-11-26 2016-05-18 黄蒋元 Zero release papermaking production line

Also Published As

Publication number Publication date
CN105332311A (en) 2016-02-17

Similar Documents

Publication Publication Date Title
CN105332311B (en) Papermaking to zero discharge standard production line
CN106283809B (en) A kind of OCC lines slurry high efficiente callback production method
CN104278594B (en) A kind of cop tube paper production technology
CN104818640B (en) Bioanalysis extracts Plant fiber's manufacturing technique method
CN1786340A (en) Corrugated paper produced by steam blasting straw to pulp and its production method
CN205242169U (en) Zero release papermaking production line
CN106219826B (en) Grading treatment and cascade recycling system and method for white water of paper-making reconstituted tobacco
CN106007230B (en) Treatment method for removing cellulose in papermaking wastewater
CN205668991U (en) A kind of multi-functional pressure filter
CN107604736A (en) A kind of plain boiled water step processing and reuse technology
CN112342819A (en) Method for preparing papermaking pulp
CN207877554U (en) A kind of sludge decompression dehydration drying device
CN1150365C (en) Pulping and paper-making process with palm shell as raw material
CN106968118B (en) A kind of fruit cultivating bag paper and its zero-emission production method of waste paper manufacture
CN206014569U (en) A kind of papermaking-method reconstituted tobaccos plain boiled water classification processes step reclaiming system
CN201553674U (en) Band-type sludge thickening and dewatering machine
CN202829740U (en) Paper machine white water recycling and disposal system
CN212833386U (en) Papermaking sludge resourceful treatment equipment
CN208562112U (en) A kind of energy-saving and environment-friendly sludge treatment equipment
CN113683280A (en) Efficient recycling method and recycling system for deposited sludge
CN204266049U (en) The circulating treating system of insulating board plain boiled water
CN206768487U (en) A kind of paper machine white water processing system
CN104609681A (en) System for recovering and monitoring papermaking wastewater
CN106007231B (en) Treatment system for removing cellulose in papermaking wastewater
CN110804891B (en) Combined treatment process for papermaking pulp

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant