CN108585343A - The recycle device and processing method of papermaking enriched water - Google Patents

The recycle device and processing method of papermaking enriched water Download PDF

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CN108585343A
CN108585343A CN201810111710.XA CN201810111710A CN108585343A CN 108585343 A CN108585343 A CN 108585343A CN 201810111710 A CN201810111710 A CN 201810111710A CN 108585343 A CN108585343 A CN 108585343A
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water
tower body
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attapulgite
enriched
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王建玲
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    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
    • C02F3/342—Biological treatment of water, waste water, or sewage characterised by the microorganisms used characterised by the enzymes used
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/04—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising compounds of alkali metals, alkaline earth metals or magnesium
    • B01J20/041—Oxides or hydroxides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/06—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
    • B01J20/08—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04 comprising aluminium oxide or hydroxide; comprising bauxite
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
    • B01J20/16—Alumino-silicates
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/28—Treatment of water, waste water, or sewage by sorption
    • C02F1/281—Treatment of water, waste water, or sewage by sorption using inorganic sorbents
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/42—Treatment of water, waste water, or sewage by ion-exchange
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
    • C02F3/341—Consortia of bacteria
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F3/00—Biological treatment of water, waste water, or sewage
    • C02F3/34—Biological treatment of water, waste water, or sewage characterised by the microorganisms used
    • C02F3/347—Use of yeasts or fungi
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
    • C02F2103/26—Nature of the water, waste water, sewage or sludge to be treated from the processing of plants or parts thereof
    • C02F2103/28—Nature of the water, waste water, sewage or sludge to be treated from the processing of plants or parts thereof from the paper or cellulose industry

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  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Organic Chemistry (AREA)
  • Microbiology (AREA)
  • Environmental & Geological Engineering (AREA)
  • Engineering & Computer Science (AREA)
  • Hydrology & Water Resources (AREA)
  • Water Supply & Treatment (AREA)
  • Inorganic Chemistry (AREA)
  • Biodiversity & Conservation Biology (AREA)
  • Analytical Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Mycology (AREA)
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Abstract

The invention belongs to papermaking and environmental technology field, more particularly to a kind of recycle device of papermaking enriched water, including tower body, enzymatic treatment layer and adsorption layer, the enzymatic treatment layer is arranged in the middle part of tower body, to be inoculated with the culture medium of Mixed Microbes, the Mixed Microbes are that viable bacteria number ratio is 1:1.2~1.5 aspergillus niger and saccharomycete, aspergillus niger and saccharomycete can carry out growth metabolism by the nutriment in enriched water, pectase, chitosan enzyme and cellulase etc. be generated, for decomposing colloidal substance；The adsorption layer is arranged in tower body lower part, includes the hydrotalcite of the attapulgite of 20~30wt% and 70~80wt%, for adsorbing coloured contaminant and anionic trash.The invention also discloses its processing methods, can prevent the phenomenon that anionic trash is enriched with, and improve the chemical environment copied in technique processed, significantly reduce production cost, effectively reduce environmental pollution.

Description

The recycle device and processing method of papermaking enriched water
Technical field
The invention belongs to papermaking and environmental technology field, and in particular to a kind of recycle device of papermaking enriched water and place Reason method.
Background technology
Speciality paper is by the paper with particular function made of the different fiber utilization paper machines system of copying, and speciality paper is in life Produce manufacturing process（The system of copying）In, a large amount of enriched waters are will produce, wherein containing a large amount of fiber fines and chemical filler, if the row of being allowed to It puts, it will cause great physical waste and environmental pollutions.Therefore, the recycling of enriched water is that collection is energy saving, lowers consumption, subtracts It arranges in the important measures of one.
Currently, the multipair enriched water of papermaking enterprise carries out closed circulation, to reduce fiber waste and environmental pollution, however, with The continuous recycling of plain boiled water, anionic trash therein is constantly enriched with, and enables the chemical environment copied in technique processed deteriorate, not only It can react, result in waste of resources and economic loss with expensive cationic chemical auxiliary agent, can also interfere the phase between Fiber-Fiber Interaction reduces paper product quality（Such as whiteness, intensity）, and be attached on paper and cause the paper defects such as stain, cavity, it is deposited on net Production efficiency is influenced on portion's pipeline.This causes long-term technology to papermaker and perplexs, it would be highly desirable to solve.
Invention content
The problem of for speciality paper manufacturing process, the present invention provide a kind of enriched water recycle device and its Method can prevent the phenomenon that anionic trash is enriched with, and improve the chemical environment copied in technique processed, significantly reduce production cost, have Effect reduces environmental pollution.
To solve the above problems, the invention is realized by the following technical scheme：
A kind of recycle device of papermaking enriched water, including tower body, enzymatic treatment layer and adsorption layer, the enzymatic treatment layer setting exist In the middle part of tower body, to be inoculated with the culture medium of Mixed Microbes, the Mixed Microbes are that viable bacteria number ratio is 1:1.2~1.5 aspergillus niger and Saccharomycete, aspergillus niger and saccharomycete can carry out growth metabolism by the nutriment in enriched water, and it is poly- to generate pectase, shell Carbohydrase and cellulase etc., for decomposing colloidal substance；The adsorption layer is arranged in tower body lower part, including 20~30wt%'s is recessed The hydrotalcite of convex stick stone and 70~80wt%, for adsorbing coloured contaminant and anionic trash.
For above-mentioned recycle device, there is strainer package outside the enzymatic treatment layer and adsorption layer, and at the enzyme It manages layer lower part and is equipped with enzymatic treatment frame, to support enzymatic treatment layer, the adsorption layer lower part is equipped with adsorptive racks, to support adsorption layer.
For above-mentioned recycle device, it is located at the tower body inner wall at the enzymatic treatment layer and is equipped with temperature control list Member.
For above-mentioned recycle device, enriched water entrance is equipped at the top of the tower body, side wall upper part is equipped with upper layer Clear water output, bottom are equipped with the outlet of lower layer's concentrated water；The enriched water entrance is equipped with enriched water pipeline, which goes out Mouth is located at upper layer clear water output lower part, and is located at adsorption layer top.
For above-mentioned recycle device, the culture medium is sabouraud culture medium, the viable bacteria inoculum concentration of the Mixed Microbes For（1.5~1.6）×106A/g.
For above-mentioned recycle device, the attapulgite grain size is 50~80 μm, and the hydrotalcite grain size is 100 ~150 μm.
For above-mentioned recycle device, the hydrotalcite is synthetic hydrotalcite, is made of following steps：
（1）Weigh a certain amount of Al (NO3)3•9H2O and Mg (NO3)2•6H2O is separately added into distilled water and fully dissolves, each to prepare At a concentration of 1.0mol L-1Solution；
（2）By acquired solution by volume 1:2 are added to the container mixing, and after carrying out ultrasonic disperse 5min, obtain mixed solution A；
（3）Mixed solution A is persistently stirred with ultrasonic disperse 30min, while aqueous slkali is added dropwise, adjusts mixed solution pH value To 10~11, mixed solution B is obtained；The aqueous slkali is KOH or K2CO3Solution；
（4）5min is centrifuged in mixed solution B to be precipitated, distilled water is added in gained precipitation and carries out ultrasound point 10min is dissipated, 3min is then centrifuged again, is repeated according to this step aforementioned operation, until cleaning solution is neutrality, is obtained Precipitate C；
（5）Ethyl alcohol is added in gained precipitate C, and carries out ultrasonic disperse 10min, 5min is then centrifuged again, according to this Step aforementioned operation 3 times repeatedly obtains precipitation D；
（6）Precipitation D is dried into 18h under the conditions of 100 DEG C, then, drying object is broken into graininess to get hydrotalcite precursor E；
（7）Presoma E is placed in heating device, with 10 DEG C of min-1Heating rate be heated to 400 DEG C of heat preservation 2h, then with 6 ℃•min-1Heating rate continue to be heated to 900 DEG C of heat preservation 5h, then, cooled to room temperature is to get synthetic hydrotalcite；It should Method is with short production cycle, efficient, at low cost, and gained synthetic hydrotalcite purity is high, and grain size is average.
For above-mentioned recycle device, the attapulgite is modified attapulgite, is made of following steps：
Attapulgite is submerged with deionized water, and suitable NaCl is added, after mixing, be ultrasonically treated 5 minutes, surpasses Frequency of sound wave is 65KHz, then filters, dries, obtains modified attapulgite；Between the attapulgite, deionized water, NaCl Weight ratio be 1：5：0.04.
The method for handling papermaking enriched water using above-mentioned recycle device, includes the following steps：
（1）The enriched water that papermaking generates is slowly injected into tower body, condition is 40~43 DEG C, pH value 5~6 in adjusting tower, and setting stops It is 15 hours to stay the time；
（2）Upper layer clear water is used for washing felt and forming net；Bottom concentrated water is sent to slurrying and is beaten；Upper layer clear water and bottom are dense Flow-rate ratio between water is 1.5:1.
For above-mentioned processing method, the Mixed Microbes viable bacteria amount is per mL enriched waters（3.2~4.0）×104It is a；It is described Adsorption layer dosage is 15% of enriched water weight in tower body.
The positive beneficial effect of the present invention：
The present invention has complementary advantages, is carried out continuously using adsorbing and decomposing two kinds of approach；And the sustainable use of its raw material, at This cheap, high treating effect.According to current 5.5 yuan/ton of calculating of wastewater treatment price, after the technology of the present invention, upper rule Simile paper enterprise can save 1,000,000 yuan or more every year, along in enriched water fiber and industrial chemicals recycle, make to make Paper production cost reduces, and production target significantly improves.From after transformation use, dropped to by original 15 cubic metres of ton paper water consumption present Ton paper is no more than 3 cubic metres.
（1）Modified attapulgite used in the present invention has layer structure, internal gather parallel chain and channel, part Particle can be adsorbed directly into duct；The present invention in attapulgite modifying process by the cavitation of high-frequency ultrasonic, Violent energy is generated, sodium ion can not only be sent into the inner passage of attapulgite（Sodium ion）, moreover it is possible to remove attapulgite Adhesive surface ingredient avoids subsequent operations to bringing new impurity in plain boiled water into；Attapulgite is after sodium salt activation modification, sodium ion The effect for having functioned simultaneously as negative electrical charge on balance oxygen-octahedron, since sodium ion electricity price is low, radius is big, between structural unit Active force it is weaker, to make cation between attapulgite layer structure that there is interchangeability, additionally, due in interlayer volume Under the action of easily disperse, remove, and make attapulgite that there is the surface area of bigger, this charging property and huge specific surface area make Modified attapulgite has stronger adsorption capacity and cation exchange capacity (CEC), is remarkably improved to coloured dirt in enriched water Contaminate object（Metal ion）Adsorption capacity improves the whiteness of recycled fiber.
（2）Modified attapulgite of the present invention derives from physical absorption as a kind of molecular sieve, to the absorption of substance（Fan De Hua Li）, have very strong polarity and Coulombian field inside crystal hole, to polar molecule（Such as water）Go out by force with unsaturated molecule displays Strong adsorption capacity；In addition, since pore-size distribution is very uniform, make it that screening function be presented, only molecular diameter is less than its hole The substance of diameter is likely to enter inside its bug hole, and only molecular diameter is slightly less than the substance in its aperture and could more steadily retain in Inside its bug hole, the water smaller as molecular diameter cannot stablize the organic pollution retained, and significantly greater（As azo system, Phthalein blueness based dye）Molecule build matches, and forms stable absorption, that is, reaches the matched of mass exchange and bug hole aperture.
（3）In addition, the fiber fines of enriched water can be contaminated in closed circulation, quality can constantly deteriorate, the process quilt The fiber fines color of the referred to as aging of fiber fines, cycle gradually darkens, and is into the reduction of paper Paper White Degree, is generated relative to new Fiber fines for, repeatedly cycle after fine fiber strength contribution it is small, this process is mainly the absorption of coloured contaminant Caused by.And modified attapulgite of the present invention can increase the friction effect with fiber fines（Due to attapulgite porous surface cave, And it is uneven）, so that colored particle is further diverged from fiber surface, improve fiber fines whiteness and intensity contribution degree.
（4）Attapulgite used in the present invention is repeatable to be recycled, together with synthetic hydrotalcite periodic cleaning recycling go forward side by side After row screening, ultrasonic disperse cleaning, by modification, abandon its grain size differ, surface-fragile, easy colloidization etc. it is unfavorable because Element, forms a kind of good special sorbing material of load, the decoloration of specific aim matching enriched water, return it is white.
（5）Anionic trash in enriched water is mainly by negatively charged dissolving substance（DS）And colloidal substance（CS）Group At wherein it includes hemicellulose, pectic acid, oxylignin, viscoloid to endanger maximum, the present invention uses aspergillus niger culture side Formula had not only consumed the COD nutrients in enriched water, but also has produced a variety of metabolic enzymes, anionic trash of degrading.
（6）Hydrotalcite is by positively charged layer and interlayer negatively charged anion and the molecular layer structure chemical combination of moisture Object, interlayer main body are mostly made of two kinds of metal hydroxides, also known as layered double hydroxide；The artificial water of the present invention Talcum be hydrotalcite precursor through calcining, laminate metal ion therein have isomorphous replacement, can be to extraordinary pollutant Specific aim absorption is carried out, interlayer anion is with interchangeability, the anionic trash that adsorbable valence state is low, ionic radius is big, To restore its layer structure, hydrotalcite after recovery is after periodic cleaning is recycled and sieved together with modified attapulgite, again Recyclable calcining, circulation absorption.
（7）The aspergillus niger and saccharomycete of enzymatic treatment layer of the present invention can utilize the different nutriments in mthod of white water from paper making（Nothing Machine salt, fats, oligosaccharide pectic substance）It is metabolized out pectase, zytase and cellulase, and containing a large amount of in plain boiled water Fiber fines and colloidal substance are the significant contributors of COD, after multi strain co cultivation of the present invention processing, the biological enzyme energy of generation Unsaturated fatty acid, oligosaccharide pectic substance are effectively decomposed, the continuous enrichment of anionic trash can be blocked, prevent chemical environment Deteriorate, improves product quality.
Description of the drawings
Fig. 1 is the structural schematic diagram of papermaking enriched water recycle device of the present invention；
1 is tower body in figure, and 2 be enriched water entrance, and 3 be the outlet of lower layer's concentrated water, and 4 be upper layer clear water output, and 5 be adsorptive racks, and 6 are Adsorption layer, 7 be enzymatic treatment frame, and 8 be enzymatic treatment layer, and 9 be temperature control unit.
Specific implementation mode
Illustrate the specific implementation mode of the present invention with reference to specific embodiment, but following embodiment is used only in detail Illustrate the present invention, does not limit the scope of the invention in any way.Involved raw material are as without especially in following embodiments Explanation is that commercially available, involved detection method is conventional method unless otherwise instructed.
Embodiment 1
A kind of recycle device of papermaking enriched water, including tower body, enzymatic treatment layer and adsorption layer, the enzymatic treatment layer setting exist In the middle part of tower body, to be inoculated with the culture medium of Mixed Microbes, the Mixed Microbes are that viable bacteria number ratio is 1:1.2 aspergillus niger and yeast Bacterium；The adsorption layer is arranged in tower body lower part, includes the hydrotalcite of the attapulgite of 20wt% and 80wt%.The enzymatic treatment layer and There is strainer package outside adsorption layer, and enzymatic treatment layer lower part is equipped with enzymatic treatment frame, to support enzymatic treatment layer, the adsorption layer Lower part is equipped with adsorptive racks, to support adsorption layer.Tower body inner wall at the enzymatic treatment layer is equipped with temperature control unit.Institute It states and is equipped with enriched water entrance at the top of tower body, side wall upper part is equipped with upper layer clear water output, and bottom is equipped with the outlet of lower layer's concentrated water；Institute It states enriched water entrance and is equipped with enriched water pipeline, the outlet of the enriched water pipeline is located at upper layer clear water output lower part, and positioned at absorption Layer top.The culture medium is sabouraud culture medium, and the viable bacteria inoculum concentration of the Mixed Microbes is（1.5~1.6）×106A/g.It is described Attapulgite grain size is 50~80 μm, and the hydrotalcite grain size is 100~150 μm.
Embodiment 2
It is same as Example 1 other than the recycle device divided by lower part of a kind of papermaking enriched water：
The hydrotalcite is synthetic hydrotalcite, is made of following steps：
（1）Weigh a certain amount of Al (NO3)3•9H2O and Mg (NO3)2•6H2O is separately added into distilled water and fully dissolves, each to prepare At a concentration of 1.0mol L-1Solution；
（2）By acquired solution by volume 1:2 are added to the container mixing, and after carrying out ultrasonic disperse 5min, obtain mixed solution A；
（3）Mixed solution A is persistently stirred with ultrasonic disperse 30min, while aqueous slkali is added dropwise, adjusts mixed solution pH value To 10~11, mixed solution B is obtained；The aqueous slkali is KOH or K2CO3Solution；
（4）5min is centrifuged in mixed solution B to be precipitated, distilled water is added in gained precipitation and carries out ultrasound point 10min is dissipated, 3min is then centrifuged again, is repeated according to this step aforementioned operation, until cleaning solution is neutrality, is obtained Precipitate C；
（5）Ethyl alcohol is added in gained precipitate C, and carries out ultrasonic disperse 10min, 5min is then centrifuged again, according to this Step aforementioned operation 3 times repeatedly obtains precipitation D；
（6）Precipitation D is dried into 18h under the conditions of 100 DEG C, then, drying object is broken into graininess to get hydrotalcite precursor E；
（7）Presoma E is placed in heating device, with 10 DEG C of min-1Heating rate be heated to 400 DEG C of heat preservation 2h, then with 6 ℃•min-1Heating rate continue to be heated to 900 DEG C of heat preservation 5h, then, cooled to room temperature is to get synthetic hydrotalcite；It should Method is with short production cycle, efficient, at low cost, and gained synthetic hydrotalcite purity is high, and grain size is average, is distributed 100~150 μm.
Embodiment 3
It is same as Example 1 other than the recycle device divided by lower part of a kind of papermaking enriched water：
The attapulgite is modified attapulgite, is made of following steps：
Attapulgite is submerged with deionized water, and suitable NaCl is added, after mixing, be ultrasonically treated 5 minutes, surpasses Frequency of sound wave is 65KHz, then filters, dries, obtains modified attapulgite；Between the attapulgite, deionized water, NaCl Weight ratio be 1：5：0.04.
Embodiment 4
It is same as Example 2 other than the recycle device divided by lower part of a kind of papermaking enriched water：
The attapulgite is modified attapulgite, is made of following steps：
Attapulgite is submerged with deionized water, and suitable NaCl is added, after mixing, be ultrasonically treated 5 minutes, surpasses Frequency of sound wave is 65KHz, then filters, dries, obtains modified attapulgite；Between the attapulgite, deionized water, NaCl Weight ratio be 1：5：0.04.
Embodiment 5
It is same as Example 4 other than the recycle device divided by lower part of a kind of papermaking enriched water：
The Mixed Microbes are that viable bacteria number ratio is 1:1.5 aspergillus niger and saccharomycete, the adsorption layer setting is in tower body lower part, packet Include the attapulgite of 30wt% and the hydrotalcite of 70wt%.
Embodiment 6
The method for handling papermaking enriched water using 1 recycle device of embodiment, includes the following steps：
（1）The enriched water that papermaking generates is slowly injected into tower body, condition is 40~43 DEG C, pH value 5~6 in adjusting tower, and setting stops It is 15 hours to stay the time；
（2）Upper layer clear water is used for washing felt and forming net；Bottom concentrated water is sent to slurrying and is beaten；Upper layer clear water and bottom are dense Flow-rate ratio between water is 1.5:1.The Mixed Microbes viable bacteria amount is per mL enriched waters 3.5 × 104It is a；The adsorption layer dosage is The 15% of enriched water weight in tower body.Enriched water treatment effect is shown in Table 1.
1 embodiment of table, 6 enriched water treatment effect
。
Embodiment 7
The method for handling papermaking enriched water using embodiment 2, specific steps are same as Example 6.Enriched water treatment effect is shown in Table 2。
2 embodiment of table, 7 enriched water treatment effect
。
Embodiment 8
The method for handling papermaking enriched water using embodiment 3, specific steps are same as Example 6.Enriched water treatment effect is shown in Table 3。
3 embodiment of table, 8 enriched water treatment effect
。
Embodiment 9
The method for handling papermaking enriched water using embodiment 4, specific steps are same as Example 6.Enriched water treatment effect is shown in Table 4。
4 embodiment of table, 9 enriched water treatment effect
。
Embodiment 10
The method for handling papermaking enriched water using embodiment 5, specific steps are same as Example 6.Enriched water treatment effect is shown in Table 5。
5 embodiment of table, 10 enriched water treatment effect
。
6~10 plain boiled water treatment effect of above example is analyzed：Mixed Microbes are constantly grown in enriched water, and consumption is therein Organic nutrient substance makes COD be remarkably decreased, while being metabolized the various enzymes of generation and being degraded into the anionic trash in plain boiled water Small molecule, small molecule are mixed bacterium growth and utilize again, are thusly-formed benign cycle.With the culture of Mixed Microbes, colloid substance Small-molecule substance is constantly resolved by pectase etc., is the significant contributor of anionic trash, anion in colloid substance Rubbish is constantly reduced, while its cationic demand constantly declines, and reduces the consumption to expensive cationic chemical auxiliary agent.
Continue embodiment 6~10 being used for enriched water closed circulation respectively, and by gained paper pulp in standard sheet forming apparatus Upper handsheet (quantification of 200g/m2), survey whiteness and tear index, burst index.Whiteness is adopted according to standard GB/T 8940.1 It is measured with digital whiteness instrument YQ-Z-48B, fracture length is tested using brisement length tester ZB-WL100, and tensile index uses Tensile strength tester RH-K300 is tested, and tear index is tested using tearability instrument ZSE-1000, burst index It is tested using bursting strength instrument RH-P1200.Specific test result is shown in Table 6：
6 each embodiment dependence test Comparative result of table
。
The invention is not limited in above-mentioned specific implementation mode, those skilled in the art can also make a variety of variations accordingly, But it is any all to cover within the scope of the claims with equivalent or similar variation of the invention.

Claims (8)

1. a kind of recycle device of papermaking enriched water, it is characterised in that：It is described including tower body, enzymatic treatment layer and adsorption layer Enzymatic treatment layer is arranged in the middle part of tower body, and to be inoculated with the culture medium of Mixed Microbes, the Mixed Microbes are that viable bacteria number ratio is 1:1.2~ 1.5 aspergillus niger and saccharomycete；Adsorption layer setting in tower body lower part, including the attapulgite of 20~30wt% and 70~ The hydrotalcite of 80wt%；
The attapulgite is modified attapulgite, is made of following steps：Attapulgite is submerged with deionized water, and is added Suitable NaCl be ultrasonically treated 5 minutes, ultrasonic frequency 65KHz after mixing, is then filtered, dries, obtain Modified attapulgite；Weight ratio between the attapulgite, deionized water, NaCl is 1：5：0.04.
2. recycle device according to claim 1, it is characterised in that：There is filter outside the enzymatic treatment layer and adsorption layer Net package, and enzymatic treatment layer lower part is equipped with enzymatic treatment frame, to support enzymatic treatment layer, the adsorption layer lower part to be equipped with absorption Frame, to support adsorption layer.
3. recycle device according to claim 1, it is characterised in that：Tower body inner wall at the enzymatic treatment layer It is equipped with temperature control unit.
4. recycle device according to claim 1, it is characterised in that：Enriched water entrance is equipped at the top of the tower body, Its side wall upper part is equipped with upper layer clear water output, and bottom is equipped with the outlet of lower layer's concentrated water；The enriched water entrance is equipped with enriched water pipe The outlet in road, the enriched water pipeline is located at upper layer clear water output lower part, and is located at adsorption layer top.
5. recycle device according to claim 1, it is characterised in that：The culture medium is sabouraud culture medium, described The viable bacteria inoculum concentration of Mixed Microbes is（1.5~1.6）×106A/g.
6. recycle device according to claim 1, it is characterised in that：The attapulgite grain size is 50~80 μm, The hydrotalcite grain size is 100~150 μm.
7. a kind of method handling papermaking enriched water using any one of claim 1~6 recycle device, feature exist In including the following steps：
（1）The enriched water that papermaking generates is slowly injected into tower body, condition is 40~43 DEG C, pH value 5~6 in adjusting tower, and setting stops It is 15 hours to stay the time；
（2）Upper layer clear water is used for washing felt and forming net；Bottom concentrated water is sent to slurrying and is beaten；Upper layer clear water and bottom are dense Flow-rate ratio between water is 1.5:1.
8. processing method according to claim 7, it is characterised in that：The Mixed Microbes viable bacteria amount is per mL enriched waters（3.2 ~4.0）×104It is a；The adsorption layer dosage is 15% of enriched water weight in tower body.
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