CN1884686A - Reed pulp prepared from wholly closed pollution-free biological oxidation method and its preparation method - Google Patents
Reed pulp prepared from wholly closed pollution-free biological oxidation method and its preparation method Download PDFInfo
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Abstract
The invention discloses a reed pulp and preparing method through full-sealing, self-circulating, zero-discharge and non-polluting biological or oxidizing method, which is characterized by the following: utilizing electron reducing reaction in the ion reaction of enzyme and oxygen molecular to produce free radical of active oxygen to transmit and separate lignin; making chromogenic gene change in the plant cell interlayer to obtain reed pulp. The invention changes chemical pulping technology without polluting acid, alkaline and anthraquinone, which saves boiling and bleaching procedures.
Description
Technical field
Totally-enclosed pollution-free biology/oxidizing process that it is pulping raw material that the present invention discloses a kind of non-timber grass family fiber reed is made reed pulp and preparation method thereof.The present invention more specifically relate to a kind of totally-enclosed, self-loopa, need not acid, without alkali, without chlorine, without anthraquinone, non-evaporatingly boil, exempt from bleaching, zero-emission, pollution-free green technology for making paper paste-making method.
Background of invention
Current paper industry is well-known, faces two big predicaments: the one, and raw material is in short supply, the 2nd, and seriously polluted, as solution as early as possible, paper-making industry will be flooded by green barrier in the ecological, environmental protective rules.
One, current paper making raw material is in short supply for a long time, is not some areas and be meant global paper industry.Forest is the lung of life on earth, removes water conservation, prevents erosion, regulate the climate wait act on outside, can also emit oxygen by absorbing carbon dioxide, forest not only has the ecological value and economic worth is arranged.Yet the world is just with per 700 * 10 at present
8m
2Decrease of speed, tropical rain forest is with per minute 50 * 10
4m
2Speed reduce, as not strictly control continue excessive and random lumbering, after 40 years, world population constantly increases, the mankind will face no oxygen for the predicament of breathing.
The China Forest statistical yearbook was compared the forest rate of descent in 1999 to 2000: ten big ecological projects related to the forestry industry-12.9%, natural forest reserve engineering-10.7%, the area of closing hillsides to facilitate afforestation-6.33%, shelter-forest+24.75%, economic forest-3.82%, timber stands-14.07%.
The plain raw material of non-wood-fiber divides in the string chemistry: 1. grass family fibrous raw material; 2. bast fiber raw material; 3. seed wool fibre raw material; 4. leaf fiber raw material four big classes are combined fiber content 48%～84% and are not waited, and grass fiber length majority is longer than lumber fibre, and cellulose is mainly used in papermaking.No matter be with wood, or, all can be used as framework material in the slurrying, all can make middle and high grade of paper pulp with the cellulose that grass extracts.Studies confirm that, reed, obtain about 8,000,000 mu of reed, hybrid giant napier, giantreed, about 4,600,000 mu of whole nation natural reed area, receive dried reed 500kg for every mu and count 2,300,000 t, in recent years, a kind of novel paper pulp raw material-hybrid giant napier, successively in Guangan, Sichuan, establishing in large scale such as Deyang, Pan Xi, Zhenjiang, Jiangsu, hybrid giant napier is received siccative 3.5-5.6t for every mu, becomes noticeable paper making raw material.Show according to the environmental protection data, reed pulp mainly concentrates on Xinjiang Bohu paper plant, long positive paper industry, golden river paper industry, Morning Ring Paper Indusrty etc., produce 20.2 ten thousand t altogether per year, about 500,000 t of year consumption raw material, account for 21.6%, all with strong acid and strong base and chlorine bleaching process, useful alkaline hydrogen peroxide method of reported in literature and bio-mechanical method pretreated feedstock are not feared the pollution of quinone to environment but thoroughly ban soda acid chlorine in the boiling, dipping, bleaching.
Table 1 is measured the integrated fiber cellulose content of each raw material with the sodium chlorite method
Unit: %
| Raw material | The place of production | Holocellulose | Raw material | The place of production | Holocellulose |
| The fish scale dragon spruce | The Xiaoxinanlin Mountains | 73.0 | Wheat straw | Hebei | 71.3 |
| Korean pine | Daxing'an Mountainrange | 69.6 | Bagasse | Guangdong | 75.6 |
| The high point poplar | Henan | 81.6 | Chinese alpine rush | Guangxi | 76.7 |
| Green bamboo | Zhejiang | 69.5 | The jowar stalk | Hebei | 66.4 |
| Red bamboo | Guangdong | 67.2 | Cornstalk | Hebei | 84.9 |
| Reed | Hubei | 75.4 | Splendid achnatherum | Ningxia | 79.8 |
| Chinese silvergrass | Hubei | 76.6 | Leaflet camphor | Heilungkiang | 74.9 |
| Cotton stalk | Jiangsu | 75.1 | Fragrant plant hair shell | Sichuan | 84.3 |
| Straw | Hebei | 64.0 |
Source resource: " pulping process and equipment ", China Light Industry Press, 2000
The various paper pulp raw material SiO of table 2
2Variation W% behind content and the alkaline boiling
| Material name | Needlebush | Reed | Sugarcane | Bamboo | Wheat Straw | The rye fringe | Straw |
| SiO 2 | 0.002～ 0.007 | 2～4 | 1～2 | 1～ 3.5 | 2～4 | 0.5～ 1.5 | 8～14 |
| Account for solid content behind the alkaline boiling and account for inorganic matter | Korean pine 0.21 0.75 | 2.6 8.83 | 2.36 7.44 | 4.71 5.44 | 7.48 23.90 |
Each layer thickness of table 3 reed fiber cell membrane relatively
Annotate: the first fiber type refers to the normal fiber of secondary wall layering, and thickness is single wall thickness.
The power spectrum peakedness ratio in the table 4 reed fiber cell membrane different levels
| Measuring point | The cell membrane position | Peak value | Measuring point | The cell membrane position | Peak value |
| 1 | S 2 | 29 | 5 | S 2 | 25 |
| 2 | S 1 | 62 | 6 | S 2 | 27 |
| 3 | SML | 94 | 7 | S 3 | 27 |
| 4 | S 1 | 73 |
Data source: table 2,3,4 derives from " string chemistry teaching material ", China Light Industry Press, 2001.
Two, seriously polluted, though trying one's best, paper-making industry improving the old technology of tradition, still use strong acid, highly basic, strong chlorine up to now without restraint, development in recent years is to using anthraquinone, because of anthracene is a condensed-nuclei aromatics in the aromatic hydrocarbon, all condensed-nuclei aromatics are had a carcinogen by universally acknowledged at present.
Use ClO 2 bleaching, Environmental Protection Agency was issued about ban use of the order of chloride chemicals in papermaking slurry bleaching in April, 2000, stipulated that simultaneously chloride paper forbids being used for packaging for foodstuff.At present 54% paper mill is invested chlorine dioxide to sight as bleaching agent again in the world, but the dioxane compound of chlorine dioxide 91% and other organic matter chemical combination, and 9% the chlorine of surplusing is discharged in the Nature, still the harm humans living environment.
The oxidizing process bleached pulp can be traced back to early 1950s; nineteen fifty-two Soviet Union wood woods chemist Nikieih and ARim find that first oxygen can bleach; after 12 years; people such as French scientist Rebeve in 1964; the discovery magnesium salts can be protected the not oxidated degraded of cellulose; cross 6 years 1970 U.S.s again; method; auspicious three states successively set up laboratory; the same year, South Africa Enstrd set up first ClO 2 bleaching workshop in the world; the U.S. set up daily output 12t ClO 2 bleaching workshop in 1972; and application chlorine-free bleaching patent, the back is big because of cellulose loss; power consumption; water consumption; factors such as cost height do not enter industrialization.After 27 years, French George's rood company in 1999, the calendar year 2001 U.S. general position Sai Er company successively begin again with chlorine dioxide, ozone and with bleaching.Retrieve the up-to-date patent documentation in countries in the world by in March, 2002, straw plant papermaking slurry does not have new technological break-through, still rest in the boiling and bleaching technology of strong acid before more than 100 year, highly basic, strong chlorine, still rest in the traditional idea of isolated lignin xylogen degradation.
Reed total fiber element 75.4%, minimum 55.5%, ash content 4.2%, lignin contains 21.2%, poly-pentose 21.1%, the hot water extract 5.5%, 1%NaOH extract 32.2%.From the morphological analysis of reed fiber, though reed fiber is long greater than wheat straw, straw, stalk, fibre wall thickness has only 3um, and the wall chamber is than 1.77um, and wheat straw wall chamber is than 4.16um, wall chamber 5.2um.For this reason; reed fiber cell water absorbing capacity when making beating is strong; swollen is fast; elasticity is strong; be difficult to features such as wire-dividing broom purification; biology/oxidative treatment reed raw material key technology is the pH value, and the degree of accuracy that the biological respinse condition provides, cellulose protective agent consumption and the active oxygen time of staying, the simple bioanalysis of evidence does not reach the requirement of medium and high-grade goods slurry.Optimal processes should be first biology, rear oxidation, and oxygen is pressed mix grinding again, thoroughly breaks away from the unique selection of environmental pollution for current paper-making pulping enterprise.
Summary of the invention
The invention provides a kind of totally-enclosed, self-loopa, zero-emission, pollution-free biology/oxidizing process and make reed pulp and preparation method thereof.This method is to generate active oxygen radical with biology/biology enzyme and molecular oxygen in electronic reduction reaction to transform isolated lignin, and the chromophore in the plant cell interbed is changed, and obtains news paper pulp.This method has fundamentally changed traditional handicraft with chemicals pulping process such as with serious pollution acid, alkali, chlorine, anthraquinones, use the present invention not only to remove with serious pollution boiling, bleaching two big workshop sections from, and utilize abundant year production-goods source, also can save energy water saving and reduce product cost.
Biology/oxidizing process of the present invention: be meant earlier and handle the reed raw material that sterilization treatment is in the presence of the cellulose of metal ion and metal ion match composition is protectant, with active oxygen A, B mix grinding pulping with microorganism and/or biology enzyme.
Described reed refers to reed and reed reed in the grass family fibrous raw material, comprises like the non-bamboo of bamboo, and like the giantreed of the non-reed of reed and hybrid giant napier etc., or their mixture.
Biology refers to white-rot fungi, Phanerochaete chrysosporium, soft-rot fungi and variegated manyzoned polypore bacteria, and their mixture, biology enzyme comprises: horseradish peroxidase (HRP), lignin peroxidase (LiP-H1, H2, H3 ...-H10), manganese peroxidase (MnP), glyoxal oxidizing ferment, laccase, hydrogen peroxide generate enzyme, third generation zytase, lignoenzyme, poly oxidation of phenol enzyme, catalase, lipoxidase and coenzyme, and their mixture, preferably horseradish peroxidase, hydrogen peroxide generate enzyme, soft-rot fungi.
The consumption of enzyme should make that usually its concentration in the processing material is 0.001-50umol/L, and preferred 0.1-20umol/L, biological consumption are not special the restrictions, are generally hundred million/ml of 10-10 material.
Active oxygen A of the present invention comprises the free radical of hydrogen peroxide and generation thereof, for example the free radical that generates with metal.The energy that molecular oxygen provides when the ionizing radiation device produces redox reaction generates water at last, accepts oxygen radical of an electron institute generation of every acceptance in 4 electronic processes altogether, is generically and collectively referred to as active oxygen A, comprises H
2O
2Free radical with metal ion generates generates ultra-oxygen anion free radical as an electron reduction---
Two-electron reduction generates hydrogen peroxide---
, three electron reductions generate hydroxyl radical free radical---
, the free radical that generates of ferrous iron and hydroperoxidation---
。
Active oxygen B of the present invention: comprise O
3And/or its free radical that in water, generates and microorganism or biology enzyme, the generation H that it does not stop with biological bacteria in water
2O
2Need use for decoloring reaction, comprise for example soft-rot fungi, white-rot fungi, soybean peel peroxidase (SHP), laccase and catalase also are used in the decoloring reaction that aqueous phase produces, as
, the H that glyoxal oxidizing ferment and horseradish peroxidase acting in conjunction produce down
2O
2Wherein said biology or biology enzyme can use as previously discussed those.
H
2O
2Consumption be not special restriction, the concentration in processing material (comprising WATER AS FLOW MEDIUM and raw material reed) is generally 0.0001-5%.
O
3Concentration in processing material (comprising WATER AS FLOW MEDIUM and raw material reed) is generally 0.1-0.15wt%.
Cellulose protective agent of the present invention: comprise metal ion and metallic ion coordination body, they and O
3In water, have in the presence of enzyme such as horseradish peroxidase or lipoxidase or catalase and the coenzyme, with ultra-oxygen anion free radical
Hydrogen peroxide (H
2O
2) the plain protection system of functional fiber formed of different component respectively.
Metal ion is selected from Mg
++, Fe
++, Mn
++, Cu
++, Cu
+, Zn
++, Al
+++Or their bond, these metal ions generally use with the form of salt, as sulfurous acid iron, magnesium carbonate etc.Their concentration in the processing material is generally 10-1000ppm.
The metallic ion coordination body comprise can with above-mentioned metalchelated compound, comprise dimethyl ethylene oxide (DMD), divinyl three ammonium pentaacetic acids (DTPA), b diammonium edta EDTA, sodium alkyl sulfonate, polyoxyethylene alkyl ether etc., or their mixture.Their consumption is 0.2-1.5wt%, based on the dry pulp amount.
Non-evaporating boiling of the present invention: refer to remove from cooking section, use active oxygen B, be added drop-wise to the rotation heat by grinding in the disc mill, the produce power transfer reaction makes cellulose dissolve from the transfer of cell interbed.
Of the present invention exempting from bleached: refer to that without bleachery the acting in conjunction with active oxygen A, B is converted into colourless group with the chromophore in the lignin, as α, alpha or beta-aldehyde ketone base class are changed into carboxylic acid or dicarboxylic acids class.
In preferred embodiments, technology of the present invention comprises:
Purification of raw materials system: be that raw material is removed to eradicate leaf; it is long that reed is cut into 20-40mm; with the removal of impurity of goat's horn deduster; after the purification of raw materials; input bioreactor (commercial bioreactor or fermentation tank commonly used); reaction temperature 10-40 ℃; pH value=1.5-4.5; add 0.1-10 μ mol/L horseradish peroxidase (HRP); add 0.2-12 μ mol/L soybean peel peroxidase (SHP); agitator speed 20-30/min; behind the 1h; leave standstill 4-6h; material pulled out to extract shake up; at oxygen automatically under the cycling condition, the capping of stacking canopy film, oxygen by the bottom toward cocycle; discharging in 6-10 days; carry out sterilization treatment, under temperature control 100-150 ℃, in the presence of 0.2%-1% active oxygen A; add the cellulose protective agent that 0.02-0.2% prepares in advance; speed of agitator 40-80/min, pH value=2.5, temperature 35-80 ℃; moisture 30-40%; discharging behind the 2h enters the oxygen grinding system, evenly sends into fiberizer with screw feeder; add 0.1-1.5% active oxygen A mix grinding; mill speed 600-1200/min, the grinding machine gap is 0.2-0.5mm, screenings changes kibbling mill over to and regrinds and rescreen after the scalping; enter centrifugal purifier; beating process making beating routinely for anti-oxidation, adds 0.03% food grade citric acid and 0.01% azanol in the slurry; the thick pulp brightness 48-52 of raw material °; the original thick slurry of over dry value, this workshop section can build the roughing production line in the township enterprise that the aboundresources raw material is concentrated, and is the assurance of supplying raw materials of center enterprise.
Original thick slurry evenly sent in the grinding machine with screw feeder finish grind, finish grind for the first time, in fine grinding technology, drip the active oxygen A for preparing earlier, dripping quantity and slurry than 1: 0.12 with the slurry mix grinding, mill speed 1200-1400/min, the grinding machine gap is 0.12-0.35mm, starch dense 15%-35%, pH value=2.5, the slurry flowing velocity is 1.5-2h, the observation pulp brightness is 60-75 ° and enters fine screen (ISO); The concentration of correct grinding dropping for the second time is 0.2-1% active oxygen B and slurry mix grinding, mill speed 1200-1400/min, the grinding machine gap transfers to 0.12-0.25mm, starch dense 20-35%, temperature 35-80 ℃, pressure 0.2-1.2MPa, pH value 2.5, during 75-86 ° of sampling Detection whiteness, enter conventional bolting house fine screen, screenings finish grindes till whole oxidation polymerizations repeatedly again.Correct grinding slurry input centrifugal purifier purification section enters that conventional cylinder concentrates, making beating, reserve pit, can be more repeatedly once as improving whiteness by precision grinding process, and technology of the present invention obtains slurry rate 61-78% (seeing process chart for details).
Totally-enclosed self-loopa zero-emission of the present invention: be after pretreatment of raw material, to send into bioreactor, all use moisture two parts backflow self-loopa in the technological process, the one, solid slag is transported after the centrifugal clarification, slurry is sent into conventional beater floor, the clear water that is produced is gone into the self-circulating water clarifier-tank, and the three basic Oxygen Generator (O of 0.1%-0.15% are housed in the clarifier-tank
3Generator), clear water is produced decoloring reaction, in the water and contain micro-superoxide anion, enter recirculated water using system (seeing process chart for details) by pump; The 2nd, handle with conventional thickener after the centrifugal clarification, slurry is sent into reserve pit and is advanced machine room, the water filtration that is produced enters the self-circulating water clarifier-tank, with purify waste water pumping purification of raw materials system, bioreactor, disinfection system, oxygen grinding system, the screening system after handling, self-loopa is used repeatedly.Technology of the present invention does not have the gas discharging, the discharging of no Heisui River, and discharging solid slag accounting 5%-12%, free from environmental pollution, this waste residue is sent into biological treatment tank and is used it for anything else in addition.See totally-enclosed self-loopa technique of zero discharge flow chart for details, for the feasibility that further specifies patent of the present invention sees embodiment for details.
Description of drawings
Fig. 1 is a process chart of the present invention.At first be purification of raw materials, in the presence of biology/biology enzyme, in bioreactor, handle then, then sterilization, oxygen mill in the presence of active oxygen A and B, screening, centrifugal clarification, making beating, waste water enters self-circulating water clarifier ozone treatment, water after the processing can enter above each procedure, and solid matter is rich in and enriches organic substance, does not contain harmful element, strong acid and strong base, can be used as his usefulness such as fertilizer, thereby realize self-loopa, zero-emission, pollution-free.
Embodiment one
It is long that reed 100 weight portions are cut into 20-40mm with shredding machine, with the removal of impurity of goat's horn deduster, after the purification of raw materials, input bioreactor, reaction temperature 10-40 ℃, pH value=1.5-4.5, add 0.1-10 μ mol/L horseradish peroxidase (HRP), add 0.2-12 μ mol/L soybean peel peroxidase (SHP), agitator speed 20-30/min, behind the 1h, leave standstill 4-6h, material is pulled out to extract shake up, at oxygen automatically under the cycling condition, the capping of stacking canopy film, toward cocycle, sterilization treatment is carried out in discharging in 6-10 days to oxygen by the bottom, under temperature control 100-150 ℃, at 0.2%-1%H
2O
2Exist down; add the cellulose protective agent (comprising magnesium carbonate 0.02 weight portion and dimethyl ethylene oxide 0.1 weight portion) for preparing in advance; speed of agitator 40-80/min; pH value=2.5, temperature 35-80 ℃, moisture 30-40%; discharging behind the 2h; enter the oxygen grinding system, evenly send into fiberizer, add 0.1-1.5%H with screw feeder
2O
2Mix grinding, mill speed 600-1200/min, the grinding machine gap is 0.2-0.5mm, screenings changes kibbling mill over to and regrinds and rescreen after the scalping, enter centrifugal purifier, beating process making beating routinely for anti-oxidation, adds 0.03% food grade citric acid and 0.01% azanol in the slurry, the thick pulp brightness 48-52 of raw material °, the original thick slurry of over dry value, this workshop section can build the roughing production line in the township enterprise that the aboundresources raw material is concentrated, and is the assurance of supplying raw materials of center enterprise.
Embodiment two
Get original thick slurry 100 weight portions among the embodiment one, evenly send into grinding machine continuously with screw feeder, correct grinding drips the 0.4%H for preparing earlier in fine grinding technology for the first time
2O
2, dripping quantity and slurry than 1: 0.12 with the slurry mix grinding, mill speed 1200-1400/min, 0.12-0.35mm is transferred in the grinding machine gap, temperature is 60-90 ℃, starch the dense 15%-35% that reaches, pH value 2.5, the slurry flowing velocity is 1.5-2h, the observation pulp brightness be 60-75 °; Correct grinding drips concentration 1umol/L ozone and 10umol/L horseradish peroxidase for the second time, mill speed 1200-1400/min, the grinding machine gap transfers to 0.12-0.25mm, starches dense 20-35%, temperature 35-80 ℃, pressure 0.2-1.2MPa, pH value 2.5,75-86 ° of sampling Detection whiteness enters that conventional fine screen, purification, cylinder concentrate, making beating, storage sizing process system (seeing production technology for details), can be more repeatedly once if need to improve whiteness by the correct grinding operating procedure, technology of the present invention obtains slurry rate 61-78%.
Embodiment three
Carry out the program identical, just generate enzyme and replace horseradish peroxidase with the hydrogen peroxide of same amount with embodiment one.
Embodiment four
Carry out the program identical, just replace horseradish peroxidase with the lignin peroxidase of 1umol/L and the manganese peroxidase of 1umol/L with embodiment two.Whiteness 75-86 °, obtain slurry rate 61-78%.
The present invention is non-evaporating to boil, exempts from bleaching, totally-enclosed self-loopa, and active oxygen mix grinding technology need not be added chemicalss such as strong acid, highly basic, chlorine again, and enterprise can make various dissimilar middle-grade paper pulp according to the market demand.
Claims (10)
1, biology/oxidizing process is made the reed pulp method; comprise earlier and handle the reed raw material that sterilization treatment is again under the protectant existence of being made up of metal ion and metallic ion coordination body of cellulose with microorganism and/or biology enzyme; with active oxygen A, B mix grinding pulping, described active oxygen A comprises H in aqueous medium
2O
2And the free radical that generates, described active oxygen B comprises O
3And/or its free radical that in water, generates and biology enzyme and/or microorganism, wherein in described method overall process, without strong acid, highly basic, strong chlorine and anthraquinone (comprising chlorine dioxide and chlorion compound).
2, the microorganism of claim 1 is selected from white-rot fungi, Phanerochaete chrysosporium, soft-rot fungi and variegated manyzoned polypore bacteria, and their mixture, described biology enzyme is selected from horseradish peroxidase (HRP), lignin peroxidase (LiP-H1, H2, H3, H4, H5, H6, H7, H8, H9, H10), manganese peroxidase (MnP), soybean peel peroxidase (SHP), laccase, hydrogen peroxide generation enzyme, third generation zytase, lignoenzyme, poly oxidation of phenol enzyme, catalase, lipoxidase and coenzyme, and their mixture.
3, according to the process of claim 1 wherein that the concentration of active oxygen A in the processing material is 0.01-5%, be generally 0.1-0.4wt%.
4, according to the O that the process of claim 1 wherein among the active oxygen B
3Concentration in the processing material is 1-15umol/L.
5, according to the process of claim 1 wherein that metal ion is selected from Mg
++, Fe
++, Mn
++, Cu
++, Cu
+, Zn
++, Al
+++Or their bond, these metal ions generally use with the form of salt, as ferrous sulfate, and magnesium carbonate etc., their concentration in the processing material is generally 10-1000ppm.
6, according to the method for claim 1, wherein the metallic ion coordination body comprise can with above-mentioned metalchelated compound, comprise dimethyl ethylene oxide (DMD), divinyl three ammonium pentaacetic acids (DTPA), b diammonium edta (EDTA), sodium alkyl sulfonate, polyoxyethylene alkyl ether, or their mixture, their consumption is 0.2-1.5wt%, based on the dry pulp amount.
7, according to the method for claim 1, described reed is selected from reed and reed reed in the grass family fibrous raw material, comprise like the non-bamboo of bamboo, like giantreed and the hybrid giant napier of the non-reed of reed, and their mixture.
8, according to the method for claim 1, described method feature is:
Non-evaporating boiling: refer to remove from cooking section, use active oxygen B, be added drop-wise to the rotation heat by grinding in the disc mill, the produce power transfer reaction makes cellulose dissolve from the transfer of cell interbed;
Exempt from bleaching: refer to that without bleachery the acting in conjunction with active oxygen A, B is converted into colourless group with the chromophore in the lignin, as α, alpha or beta-aldehyde ketone base class are changed into carboxylic acid or dicarboxylic acids class;
Self-loopa, zero-emission: be after pretreatment of raw material, to send into bioreactor, all use moisture two parts backflow self-loopa in the technological process, the one, solid slag is transported after the centrifugal clarification, slurry is sent into conventional beater floor, the clear water that is produced is gone into the self-circulating water clarifier-tank, and the three basic Oxygen Generator (O of 0.1%-0.15% are housed in the clarifier-tank
3Generator), clear water is produced decoloring reaction, in the water and contain micro-superoxide anion, enter the recirculated water using system by pump; The 2nd, handle with conventional thickener after the centrifugal clarification, slurry is sent into reserve pit and is advanced machine room, the water filtration that is produced enters the self-circulating water clarifier-tank, with purify waste water pumping purification of raw materials system, bioreactor, disinfection system, oxygen grinding system, the screening system after handling, self-loopa is used repeatedly.
9, according to the process of claim 1 wherein usefulness active oxygen A and B mix grinding pulping temperature, the pressure of 0.2-1.2Mpa at 35-150 ℃, 1.5-5.5pH under carried out 0.5-2 hour, starching dense is 12-38%, and the defibrination rotating speed is 1200-1400/min, and speed of agitator is 40-80/min.
10, according to the process of claim 1 wherein that the consumption of biology enzyme is 0.001-50umol/L, the consumption of microorganism is 10-1,000,000,000/ml.
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|---|---|---|---|
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|---|---|---|---|
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104179055A (en) * | 2014-07-18 | 2014-12-03 | 刘秀平 | Grass fiber bio-separation compound preparation and application method thereof |
| CN110158344A (en) * | 2019-05-24 | 2019-08-23 | 滕铁生 | The pulping process of non-wood fiber or grass kind plant fiber based on substep biology |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE69316988T2 (en) * | 1992-10-23 | 1998-07-30 | Mac Millan Bloedel Ltd | IMPROVED Ozone Bleaching |
| CN1055737C (en) * | 1996-01-15 | 2000-08-23 | 南京林业大学 | Prescription and process for intensively bleaching pulp using singlet state oxygen in alkali bleaching stage of multi-stage process |
| DE19612194A1 (en) * | 1996-03-27 | 1997-10-02 | Consortium Elektrochem Ind | Multi-component system for changing, breaking down or bleaching lignin, lignin-containing materials or similar substances as well as methods for their use |
| EP1101860A1 (en) * | 1999-11-19 | 2001-05-23 | Praxair Technology, Inc. | Method for bleaching pulp with activated ozone |
| DE10126988A1 (en) * | 2001-06-05 | 2002-12-12 | Call Krimhild | Systems for oxidation or bleaching, especially of pulp, comprise a component enzymatically generating peroxide, superoxide or other reactive oxygen species, and a precursor formed enzymatically, or is oxidizably reactive |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104179055A (en) * | 2014-07-18 | 2014-12-03 | 刘秀平 | Grass fiber bio-separation compound preparation and application method thereof |
| CN104179055B (en) * | 2014-07-18 | 2016-03-09 | 刘秀平 | Grass fiber bio-separation compound formulation |
| CN110158344A (en) * | 2019-05-24 | 2019-08-23 | 滕铁生 | The pulping process of non-wood fiber or grass kind plant fiber based on substep biology |
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