CN103321081A - ECF bleaching technology of fast growing poplar by sodium hydroxide anthraquinone pulp bio-chemical method - Google Patents

ECF bleaching technology of fast growing poplar by sodium hydroxide anthraquinone pulp bio-chemical method Download PDF

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CN103321081A
CN103321081A CN2013103001355A CN201310300135A CN103321081A CN 103321081 A CN103321081 A CN 103321081A CN 2013103001355 A CN2013103001355 A CN 2013103001355A CN 201310300135 A CN201310300135 A CN 201310300135A CN 103321081 A CN103321081 A CN 103321081A
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吉兴香
陈嘉川
田中建
杨桂花
庞志强
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Qilu University of Technology
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Abstract

The invention discloses an ECF bleaching technology of fast growing poplar by a sodium hydroxide anthraquinone pulp bio-chemical method. The ECF bleaching technology is characterized by comprising the following steps: (1) boiling: taking fast growing poplar chips, stewing the fast growing poplar chips in a digester to obtain virgin pulp, washing, and screening to obtain paper pulp; (2) xylanase pretreatment; and (3) ECF bleaching: bleaching the above paper pulp which has undergone enzyme treatment, wherein the bleaching process is one of three bleaching processes, namely ODQP, OPDQP or O1O2PDQP. According to the invention, xylanase is used to pretreat the paper pulp, and one of the three bleaching processes, namely ODQP, OPDQP or O1O2PDQP, is carried out for bleaching so as to obtain the paper pulp with higher whiteness and viscosity. In comparison with paper pulp which is directed bleached without xylanase pretreatment, the paper pulp produced by the ECF bleaching technology has the following advantages: beating whiteness loss is less, folding strength is averagely higher by 30 times, burst index is averagely higher by 0.35N.m.g<-1>, breaking length is averagely higher by 0.25KM, and tear index difference is basically unchanged or slightly reduced by a very small magnitude.

Description

The NaOH anthraquinone slurry biochemical process ECF bleaching process of a kind of fast-growing poplar
Technical field
The present invention relates to the NaOH anthraquinone slurry biochemical process ECF bleaching process of a kind of fast-growing poplar, belong to pulp technology for making paper.
Background technology
Owing to having produced the foul gas that hydrogen sulfide, methyl mercaptan, methyl sulfide and dimethyl sulphide etc. have peculiar smell in sulfate pulping and the alkali recovery process, atmosphere around the production unit is existed the problem of pollution and air peculiar smell, therefore in the open type slurrying production procedure of some medium-sized pulp mills, adopted take NaOH anthraquinone as main pulping technique.Because the chemicals of the anthraquinone slurrying of NaOH mainly is NaOH; also contain a small amount of anthraquinone as the boiling protective agent; these two kinds of chemicalss are nontoxic free from extraneous odour all; also do not produce the material of peculiar smell in the pulping digestion process, therefore this soda pulping process technology is used more at part batch (-type) pulping by cooking production line.
The fast-growing poplar is as a kind of good paper making raw material, its yield of producing NaOH anthraquinone slurry is higher, generally about 51%, and the own whiteness of fast-growing poplar is high, former pulp brightness after the anthraquinone slurrying of NaOH exceeds 3-5%ISO than the former pulp brightness of other leaf woods generally about 35%ISO.And the fast-growing poplar is as a kind of broad-leaved wood paper making raw material of high-quality, and the black liquor that produces in its alkaline cooking process has the treatment technology of comparative maturity, and environment is not polluted substantially.
At present, the application study of zytase in the broad-leaved wood sulphate pulp bleaching is a lot, and partly realizes industrialization abroad, and not yet realization is at home used on a large scale.Simultaneously, zytase is studied rarely seen report for technique and the mechanism of the bleaching of NaOH anthraquinone slurry.For this reason, the application has selected three kinds of novel commercial xylanase, adopts the biochemistry method for bleaching, has explored a kind of new technology of ECF bleaching of fast-growing poplar NaOH-AQ slurry, for the current pulp and paper industry of China fast, developing in a healthy way provides realistic basis.
Summary of the invention
For above-mentioned prior art, the objective of the invention is to change the technique of traditional pure chemistry method association with pulp bleaching, the technique that adopts bio-bleaching to combine with chemical bleaching, when reaching identical pulp brightness, thereby the chemical bleaching liquor that consumes still less further reduces bleaching waste liquor to the pollution of environment, when perhaps consuming identical chemical bleaching liquor, makes the more Gao Gengyi making beating of whiteness of paper pulp, further reduce the beating energy consumption of paper pulp, realize the low consumption high efficiency bleaching of fast-growing poplar NaOH anthraquinone slurry.
The present invention is achieved by the following technical solutions: the concentration of following related slurry is mass percent if no special instructions; Related reagent, the consumption of medicine if no special instructions, all are for oven dry stock.
The NaOH anthraquinone slurry biochemical process ECF bleaching process of a kind of fast-growing poplar, step is as follows:
(1) boiling: get the quick growth poplar wood sheet, put into the digester boiling, get magma, then wash fully, screen, get paper pulp, the Kappa number of paper pulp is 16～21;
(2) xylanase pretr eatment;
(3) ECF bleaching: the above-mentioned paper pulp of processing through enzyme is bleached, and bleaching process is ODQP, O PDQP or O 1O 2PThree kinds of DQP float one of order, and the step of bleaching process is: at first, the paper pulp of processing through enzyme is carried out the deoxidation lignin or strengthens the deoxidation lignin; Oxygen delignification washs paper pulp after finishing, and then carries out D section ClO 2 bleaching; D section ClO 2 bleaching washs paper pulp after finishing, and then carries out Q section chelation treatment; Q section chelation treatment is washed paper pulp after finishing, and then carries out P section H 2O 2Bleaching is finished.
Further, the concrete mode of described boiling is: get the quick growth poplar wood sheet of length 15～25mm, width 10～20mm, thickness 3～5mm, behind the natural air drying, in 15L electric heating rotating autoclave, carry out boiling, make fast-growing poplar NaOH anthraquinone magma, the condition of boiling is: alkali charge 22%(is to the over dry raw material, and NaOH counts), AQ consumption 0.05%, liquor ratio 1:4,165 ℃ of boiling maximum temperatures are carried out little venting 10-15min in the time of 105 ℃, heating-up time 90min, temperature retention time 90min; The boiling disposed slurry gets paper pulp, the Kappa number 16～21 of paper pulp through fully washing, screening.
Further, the concrete mode of described xylanase pretr eatment is: adjusting pulp density is 10%, then uses zytase X 1, X 2Or X 3Process, in processing procedure, every interval 10～15min rubs once, to guarantee that enzyme mixes with the even of paper pulp; Take out after processing, put into boiling water bath 10min, make zytase inactivation cessation reaction, with entering next step bleaching process behind the running water cleaning paper pulp.
Described zytase X 1Provide (the letter zytase Pulpzyme HC of trade name Novi, article number CKN00117 and CDN00429) by Novozymes Company, liquid state, the cellulose-less enzyme is lived; Zytase X 2, X 3Biological Co., Ltd provides (trade name zytase, article number LV-1 and LV-2) by the green little health in Shenzhen, is the white powder solid, and all cellulase is not lived.
Described zytase X 1, X 2Or X 3The concrete technology condition of processing is as follows: dextranase X 1Process conditions be: enzyme dosage 10IU/L(is for the cumulative volume of paper pulp), temperature 50 C, pH8-9, time 90-120min; Zytase X 2Process conditions be: enzyme dosage 8IU/g(is for the quality of exhausted paper pulp), 55 ℃ of temperature, pH8-9, time 90-120min; Zytase X 3Process conditions be: enzyme dosage 10IU/g(is for the quality of exhausted paper pulp), temperature 50 C, pH8-9, time 120min.
Further, the concrete mode of described ODQP bleaching process is: Oxygen Delignification of Fast-Growing is: starch dense 10%, NaOH consumption 2.5%, oxygen is pressed 0.6MPa, 100 ℃ of temperature, time 80min, MgSO 4Consumption 0.5%; D section: ClO 2Consumption is 0.6%, original ph 5, temperature 70 C, starch dense 10%, time 120min; The Q section: starch dense 8%, DTPA(Chinese diethylene triamine pentacetic acid (DTPA)) consumption 0.5%, temperature 70 C, time 60min, pH value 4-5; P section: H 2O 2Consumption is 3%, Na 2SiO 3Consumption 0.7%, MgSO 4Consumption 0.5%, original ph 12,90 ℃ of temperature, starch dense 10%, time 90min.
Further, described O PThe concrete mode of DQP bleaching process is: strengthening the Oxygen Delignification of Fast-Growing condition is: starch dense 10%, NaOH consumption 2.5%, oxygen is pressed 0.6MPa, 100 ℃ of temperature, MgSO 4Consumption 0.5%, Na 2SiO 3Consumption 0.7%, H 2O 2Consumption 3%, time 80min; D section: ClO 2Consumption is 0.4%, original ph 5, temperature 70 C, starch dense 10%, time 120min; The Q section: starch dense 8%, DTPA consumption 0.5%, temperature 70 C, time 60min, pH value 4-5; P section: H 2O 2Consumption is 2%, Na 2SiO 3Consumption 0.7%, MgSO 4Consumption 0.5%, original ph 12,90 ℃ of temperature, starch dense 10%, time 90min.
Further, described O 1O 2PThe concrete mode of DQP bleaching process is: first paragraph O 1: starch dense 10%, NaOH consumption 2%, oxygen is pressed 0.6MPa, 100 ℃ of temperature, time 20min, MgSO 4Consumption 0.5%; Second segment O 2P: replenish 0.5% NaOH, add 3% H 2O 2, Na 2SiO 3Consumption 0.7%, oxygen is pressed 0.5MPa, time 60min; D section: ClO 2Consumption is 0.4%, original ph 5, temperature 70 C, starch dense 10%, time 120min; The Q section: starch dense 8%, DTPA consumption 0.5%, temperature 70 C, time 60min, pH value 4-5; P section: H 2O 2Consumption is 2%, Na 2SiO 3Consumption 0.7%, MgSO 4Consumption 0.5%, original ph 12,90 ℃ of temperature, starch dense 10%, time 90min.
The present invention adopts zytase that paper pulp is carried out preliminary treatment, then by ODQP, O PDQP or O 1O 2PThree kinds of DQP float one of order and bleach, and have obtained the higher paper pulp of whiteness and viscosity, (X refers to xylanase pretr eatment) specific as follows:
Fast-growing poplar NaOH-AQ slurry XODQP floats order at ClO 2Total consumption 0.6%, H 2O 2In the situation of total consumption 3%, the whiteness of bleached pulp is up to 87.7%ISO, minimum 87.2%ISO; The whiteness of ODQP bleached pulp is 84.7%ISO, through enzyme process than not with enzyme process float after the whiteness of slurry exceed 2.5-3.0%ISO, and kept higher pulp viscosity and lower Kappa number;
Fast-growing poplar NaOH-AQ starches XO PDQP floats order at ClO 2Total consumption 0.4%, H 2O 2In the situation of total consumption 5%, the whiteness of bleached pulp is up to 88.5%ISO, minimum 88.1%ISO; XO PThe whiteness of DQP bleached pulp is 85.3%ISO, through enzyme process than not with enzyme process float after the whiteness of slurry exceed 2.8-3.2%ISO, and kept higher pulp viscosity and lower Kappa number; This floats the ClO of order 2Consumption further reduces, more environmental protection.
Fast-growing poplar NaOH-AQ starches XO 1O 2PDQP floats order at ClO 2Total consumption 0.4%, H 2O 2In the situation of total consumption 5%, the whiteness of bleached pulp is up to 88.2%ISO, minimum 87.8%ISO; O 1O 2PThe whiteness of DQP bleached pulp is 85.0%ISO, through enzyme process than not with enzyme process float after the whiteness of slurry exceed 2.8-3.2%ISO, and kept higher pulp viscosity and lower Kappa number; This floats the ClO of order 2Consumption further reduces, and more is conducive to environmental protection.
With respect to not using xylanase pretr eatment, directly bleach for the paper pulp that obtains, making beating loss of whiteness value of the present invention still less, folding strength on average exceeds 30 times, burst index on average exceeds 0.35Nmg -1, fracture length on average exceeds 0.25KM, and tear index is substantially constant or slightly descend but amplitude is very little.The present invention has also compared the correspondence of three kinds of xylanase treatment paper pulp and has floated the bleaching effect of order, and the effect of the pulp treatment of three kinds of enzymes is difference to some extent, from the initial effect that affects oxygen delignification, has influence on the bleaching results that ECF respectively floats order always.Wherein help float effect best be X 2, secondly be X 1And X 3Help that to float effect close.But on the whole, these three kinds of enzymes helps that to float effect all apparent in view.When reaching identical or close beating degree, the former required making beating revolution still less can be saved beating energy consumption about 17.8%.
Description of drawings
Fig. 1: NaOH-AQ magma fiber properties schematic diagram.
Fig. 2: NaOH-AQ magma is through zytase X 1The paper pulp fiber characteristic schematic diagram of processing.
Fig. 3: NaOH-AQ magma is through zytase X 2The paper pulp fiber characteristic schematic diagram of processing.
Fig. 4: NaOH-AQ magma is through zytase X 3The paper pulp fiber characteristic schematic diagram of processing.
Fig. 5: NaOH-AQ magma is through the paper pulp fiber characteristic schematic diagram of ODQP bleaching.
Fig. 6: NaOH-AQ magma is through X 1The paper pulp fiber characteristic schematic diagram of ODQP bleaching.
Fig. 7: NaOH-AQ magma is through X 2The paper pulp fiber characteristic schematic diagram of ODQP bleaching.
Fig. 8: NaOH-AQ magma is through X 3The paper pulp fiber characteristic schematic diagram of ODQP bleaching.
The specific embodiment
The present invention is further illustrated below in conjunction with embodiment.
The process optimization of embodiment 1 xylanase treatment fast-growing poplar NaOH-AQ slurry
The research and comparison of zytase aspect leaf wood KP slurry auxiliary bleaching is many, has also obtained good effect.According to pertinent literature, the principal element that affects xylanase treatment paper pulp has enzyme dosage, temperature, pH value and time etc., and these factors have in various degree impact to oxygen delignification effect and follow-up bleaching.At present, because the research rarely seen report of zytase in the bleaching of fast-growing poplar NaOH-AQ slurry, so inquire into the only preliminary treatment fast-growing of different xylanase preparations poplar NaOH-AQ sizing process condition, and utilize various modern Instrumental Analysis means, inquire into Novel xylanase helping of fast-growing poplar NaOH-AQ slurry floated mechanism, have important innovation and realistic meaning.
The below discusses different xylanase preparations in the impact of the factors such as consumption, temperature, pH value, time on fast-growing poplar NaOH-AQ slurry oxygen delignification effect.This experiment with reference to the Master's thesis of the lucky emerging perfume (or spice) of inventor, is formulated better oxygen delignification condition as follows when the Oxygen Delignification of Fast-Growing condition of selecting: starch dense 10%, NaOH consumption 2.5%, oxygen pressure 0.6MPa, 100 ℃ of temperature, time 80min, MgSO 4All drug dosages of consumption 0.5%(are all for oven dry stock, and are as follows).
The used raw material sources of this experiment are:
Experiment is to mix the quick growth poplar wood sheet with the quick growth poplar wood sheet, takes from Shandong sun Paper Co., Ltd.Chip dimensions length 15-25mm, width 10-20mm, thickness 3-5mm, the qualification rate of wood chip is more than 90%, and is after wood chip is fetched from the stock ground, for subsequent use behind the natural air drying equilibrium water conten.
Zytase X 1Provided by Novozymes Company, liquid state, the cellulose-less enzyme is lived; Zytase X 2, X 3All have Shenzhen biological Co., Ltd of green little health to provide, be the white powder solid, all cellulase is not lived.
During experiment, the fast-growing poplar is carried out boiling, obtain paper pulp after, carry out again xylanase pretr eatment.Digestion process is: carry out boiling in 15L electric heating rotating autoclave, make fast-growing poplar NaOH-AQ magma.The condition of boiling is: alkali charge 22%(is to the over dry raw material, and NaOH counts), AQ consumption 0.05%, liquor ratio 1:4,165 ℃ of boiling maximum temperatures are carried out little venting 10-15min, heating-up time 90min, temperature retention time 90min in the time of 105 ℃.The boiling disposed slurry is through fully washing, screening.Paper pulp yield 49.5%, the Kappa number 18.2 of paper pulp, viscosity 881.7mL/g, whiteness 36.0%ISO.
Behind the xylanase pretr eatment, carry out oxygen delignification, the oxygen delignification experiment is carried out in JF-DSTE polymerization reaction kettle (have and stir and the automatic constant-temperature function).Its Oxygen Delignification of Fast-Growing is: starch dense 10%, NaOH consumption 2.5%, oxygen is pressed 0.6MPa, 100 ℃ of temperature, time 80min, MgSO 4Consumption 0.5%.
1.1 the consumption of zytase is on the impact of fast-growing poplar NaOH-AQ slurry oxygen delignification
Because the content of different slurry kind of xylans is different, and is higher than the content of softwood pulp such as the xylan content of hardwood pulp, and xylan is easier and, so the consumption of enzyme is less.In the situation that pH value and temperature are suitable, the consumption with zytase of greater activity just lacks than common zytase consumption.So in order to obtain best enzyme treatment effect, must carry out optimum experimental to the consumption of xylanase treatment fast-growing poplar NaOH-AQ slurry.The present embodiment mainly is to inquire into three kinds of Novel xylanase consumptions to the impact of fast-growing poplar NaOH-AQ slurry oxygen delignification effect.Following table 1,2,3 is three kinds of Novel xylanase X 1, X 2, X 3Consumption to fast-growing poplar NaOH-AQ slurry oxygen delignification experimental studies results.
Table 1 zytase X 1Consumption is on the impact of the oxygen delignification performance of pretreating paper pulp
Figure BDA00003525588400041
Annotate: zytase X 1Other conditions of processing: temperature 50 C, time 120min, starch dense 10%, pH value 8-9.
As can be seen from Table 1, under identical xylanase treatment condition, along with zytase X 1Increase, weaken to some extent after the whiteness of the paper pulp behind the NaOH-AQ slurry oxygen delignification improves first, at X 1When consumption was 10IU/L, the whiteness of paper pulp reached peak 60.5%ISO; The Kappa number of paper pulp is along with X 1The increase of consumption no longer changes after progressively reducing first, at X 1During consumption 10-12IU/L, the Kappa number minimum of paper pulp is 7.6; The viscosity of paper pulp is along with X 1The increase of consumption tends towards stability after progressively raising first, at X 1During consumption 8-10IU/L, the viscosity maximum of paper pulp is 772mL/g.
Also can find out from table 1, be not the consumption that the increases zytase effect that just can always increase pulp oxygen delignification.The factors such as the whiteness of paper pulp, Kappa number, viscosity can draw behind the comprehensive oxygen delignification: zytase X 1The most suitable consumption of processing NaOH-AQ slurry be 10IU/L.
Table 2 zytase X 2Consumption is on the impact of the oxygen delignification performance of pretreating paper pulp
Figure BDA00003525588400042
Annotate: zytase X 2Other conditions of processing: temperature 50 C, time 120min, starch dense 10%, pH value 8-9.
As can be seen from Table 2, along with zytase X 2The increase of consumption slightly reduces after the whiteness of paper pulp increases first behind the NaOH-AQ slurry oxygen delignification and is tending towards gradually constant, and when the zytase consumption was 8IU/g, whiteness reached 60.6%ISO, did not use X 2The whiteness of the oxygen delignification paper pulp of processing improves 1.5%ISO; The viscosity of paper pulp rises first and tends towards stability afterwards or slightly reduction, at zytase X 2When consumption was 6IU/g, the viscosity of oxygen delignification paper pulp remained on 769mL/g, does not use X 2The viscosity of the oxygen delignification paper pulp of processing exceeds 26mL/g; The Kappa number of paper pulp reduces first and is tending towards afterwards constant or slightly rises, at zytase X 2When consumption is 8-10IU/g, paper pulp kappa number minimum 7.7.
Also can find out from table 2, the consumption that neither increase zytase just can increase the effect of pulp oxygen delignification always.Consider the experimental result of table 2, can draw zytase X 2When consumption was 8IU/g, the paper pulp that enzyme is processed was best to the effect of oxygen delignification.
Table 3 zytase X 3Consumption is on the impact of the oxygen delignification performance of pretreating paper pulp
Figure BDA00003525588400043
Annotate: zytase X 3Other conditions of processing: temperature 50, time 120min, starch dense 10%, pH value 8-9.
As can be seen from Table 3, along with zytase X 3The increase of consumption no longer increases on the contrary slightly decline, at X after the whiteness of paper pulp progressively increases behind the oxygen delignification 3When consumption was 10IU/g, the whiteness of paper pulp reached 60.5%ISO, does not use X 3The whiteness of the oxygen-delignified pulp of processing exceeds 1.4%ISO; The Kappa number of paper pulp descends first and is tending towards afterwards no longer changing, at X 3When consumption was 10-12IU/g, the Kappa number of paper pulp was minimum 7.7, and the oxygen-delignified pulp of more processing with enzyme reduces by 0.8 unit; The viscosity of paper pulp is tending towards slightly changing after keeping first rising, at X 3When consumption was 8IU/g, the viscosity of paper pulp reached maximum 762mL/g, and the viscosity of the oxygen-delignified pulp of more not processing with enzyme exceeds 19mL/g.
From the experimental data of table 3, can draw: at X 3When consumption was 8-10IU/g, the oxygen delignification effect of xylanase treatment paper pulp was comparatively desirable.
Can find out from table 1,2 and 3, oxygen-delignified pulp after three kinds of zytases are processed the NaOH-AQ slurry is all along with the increase of enzyme dosage, the whiteness of paper pulp and viscosity all increase first and is tending towards afterwards no longer changing, and is substantially constant after the Kappa number of paper pulp reduces first, just slightly variant on the general effect.Also can find out from top experimental data, the paper pulp of paper pulp behind oxygen delignification that three kinds of enzymes are processed has shown the common feature of higher whiteness, lower Kappa number and higher pulp viscosity, and this shows that also the preliminary treatment that zytase is used for before the NaOH-AQ anthraquinone slurry oxygen delignification is feasible.
In sum, the only consumption of three kinds of enzyme processing NaOH-AQ is: X 1Consumption is 10IU/L, X 2Consumption is 8IU/g, X 3Consumption is 8-10IU/g.
1.2 temperature is on the impact of fast-growing poplar NaOH-AQ slurry oxygen delignification
The activity of zytase is relevant with temperature, and temperature raises can fast reaction speed, Reaction time shorten.Therefore too high or too low for temperature, the relative activity of enzyme can reduce, and must control temperature well.Temperature mainly contains two aspects to the effect of zytase and paper pulp: the one, in the scope of zytase existence temperature, the activity of temperature rising enzyme improves, accelerate with the speed of paper pulp reaction, the 2nd, along with the rising enzyme of temperature loses activity gradually, so that the functioning efficiency of the reaction speed of enzyme and enzyme reduces.Therefore select suitable reaction temperature, the usefulness of giving full play to zytase has important practical significance.Table 4,5, the 6th, temperature is to three kinds of Novel xylanase X 1, X 2, X 3Process the result of study that affects of NaOH-AQ slurry oxygen delignification.
Table 4 temperature is to zytase X 1The impact of the oxygen delignification performance of pretreating paper pulp
Figure BDA00003525588400051
Annotate: enzyme dosage is 10IU/L, time 120min, starch dense 10%, pH value 8-9.
As can be seen from Table 4, along with the rising of temperature, zytase X 1Reduce gradually after the whiteness of the NaOH-AQ slurry oxygen-delignified pulp of processing raises first, when temperature was 55 ℃, pulp brightness reached maximum 60.5%ISO; The Kappa number of paper pulp reduces first rear rising, when temperature is 50-55 ℃, and the Kappa number of paper pulp minimum 7.6; The viscosity of paper pulp raises first and diminishes afterwards, when temperature is 55 ℃, and the highest 767mL/g of viscosity of paper pulp.
The experimental result of consolidated statement 4, zytase X 1Enzyme activity in the time of 50-55 ℃, be more satisfactory.But consider zytase X from actual production 1Select treatment temperature be 55 ℃ relatively good, both can save heat and reduce the water consumption, can reduce production costs and increase economic efficiency again.
Table 5 temperature is to zytase X 2The impact of the oxygen delignification performance of pretreating paper pulp
Figure BDA00003525588400052
Annotate: enzyme dosage is 8IU/g, time 120min, starch dense 10%, pH value 8-9.
As can be seen from Table 5, along with the rising of temperature, zytase X 2Increase afterwards first with the action effect of paper pulp and to weaken.As can be seen from Table 5, along with the rising of pretreatment temperature, the pulp brightness behind the oxygen delignification begins to improve, when 55 ℃ of temperature, and X 2The whiteness of the NaOH-AQ slurry oxygen-delignified pulp of processing reaches 60.6%ISO, and the whiteness of paper pulp begins to reduce behind the oxygen delignification subsequently; The Kappa number of paper pulp reduces along with the rising of temperature, and Kappa number is minimum to 7.7 when 55 ℃ of temperature; The viscosity of paper pulp becomes along with the rising of temperature greatly, but when temperature surpassed 55 ℃, the viscosity of paper pulp was up to 764mg/L; The viscosity of paper pulp descends apparent in viewly when temperature surpasses 60 ℃, shows that the usefulness of excess Temperature zytase performance reduces rapidly.
The experimental result of consolidated statement 5 draws: as zytase X 2The effect of preliminary treatment fast-growing poplar NaOH-AQ slurry is the most desirable when temperature is 55-60 ℃.
Table 6 temperature is to zytase X 3The impact of the oxygen delignification performance of pretreating paper pulp
Figure BDA00003525588400061
Annotate: enzyme dosage is 10IU/g, time 120min, starch dense 10%, pH value 8-9.
As can be seen from Table 6, along with the rising of temperature, zytase X 3The rear reduction that raises first of the whiteness of the oxygen-delignified pulp of processing, when temperature was 50 ℃, whiteness reached 60.5%ISO, and when temperature was 55 ℃, whiteness reached 60.4%ISO; The Kappa number of paper pulp is 7.7 when temperature is 50 ℃, and temperature is 7.8 when being 55 ℃; The rising first increases and then decreases of the viscosity with temperature of paper pulp is 760mg/L when temperature is 50 ℃, is 759mg/L when temperature is 55 ℃.Can draw thus zytase X 3Performance helps that to float performance ideal when temperature is 50 ℃.
Can find out from table 4,5,6, the temperature that three kinds of xylanase treatment fast-growing poplar NaOH-AQ slurry is fit to is all 50-55 ℃ of scope, temperature cross low too high all the action effect of enzyme and paper pulp can not be performed to best.But the temperature of three kinds of xylanase treatment effects preferably the time be difference to some extent also: zytase X 1And X 3The effect of enzyme pulp treatment is better when temperature is 50-55 ℃, zytase X 2Effect is better when being 55-60 ℃.
1.3pH value is on the impact of fast-growing poplar NaOH-AQ slurry oxygen delignification
Zytase has different activities under different pH values, thereby the hydrolyzed xylan ability is different.The activity of most of zytase need to competence exertion effect in certain pH value scope, and pH value is crossed to exceed to hang down all can affect the conformation of zymoprotein, even zytase is lost activity, thereby directly has influence on the effect of xylanase treatment paper pulp.Table 7,8, the 9th, the experimental data of the effect of the lower xylanase treatment fast-growing poplar NaOH-AQ slurry of different pH values oxygen delignification.
Table 7 pH value is to zytase X 1Pretreating paper pulp is on the impact of oxygen delignification effect
Figure BDA00003525588400062
Annotate: enzyme dosage is 10IU/L, temperature 50 C, and time 120min starches dense 10%.
As can be seen from Table 7, zytase X 1The whiteness of paper pulp is that 8 o'clock pulp brightness are up to 60.5%ISO along with the increase of pH value increases first rear reduction in the pH value behind the preliminary treatment fast-growing poplar NaOH-AQ slurry oxygen delignification, is that 9 o'clock pulp brightness reach 60.4%ISO in the pH value; The Kappa number of paper pulp is along with the rising of pH value reduces first rear increase, and pH value 8 and 9 o'clock, Kappa number is minimum all to reach 7.6; The viscosity of paper pulp becomes first with the rising of pH value and diminishes after large, and when pH value 8, the viscosity of paper pulp reaches maximum 767mg/L.Therefore, zytase X 1The optimal pH of pulp treatment is 8-9.
As can be seen from Table 8, along with the increase of pH value, X 2Slowly reducing after the whiteness of the fast-growing poplar NaOH-AQ slurry oxygen-delignified pulp of processing improves rapidly first, is 8 o'clock in the pH value, and pulp brightness reaches the highest 60.6%ISO, is 9 o'clock in the pH value, and pulp brightness reaches 60.5%ISO; The Kappa number of paper pulp is to reach 7.7 at 8 o'clock in the pH value, is to reach minimum 7.6 at 9 o'clock in the pH value; The viscosity of paper pulp is to reach 764mg/L at 8 o'clock in the pH value, is to reach maximum 766mg/L at 9 o'clock in the pH value.Can draw thus: X 2The optimal pH of the fast-growing poplar NaOH-AQ slurry of processing is 8-9.
Table 8 pH value is to zytase X 2Pretreating paper pulp is on the impact of oxygen delignification effect
Figure BDA00003525588400071
Annotate: enzyme dosage is 8IU/g, 55 ℃ of temperature, and time 120min starches dense 10%.
As can be seen from Table 9, zytase X 3The whiteness of paper pulp is along with the rising of pH value increases first rear reduction behind the preliminary treatment fast-growing poplar NaOH-AQ slurry oxygen delignification, and when pH value 9, the whiteness of paper pulp is up to 60.5%ISO; The Kappa number of paper pulp is along with the increase of pH value reduces first rear increase, and when pH value 8-9, Kappa number reaches minimum 7.7; The viscosity of paper pulp is along with the increase of pH value increases first rear reduction, and when pH value 8, the viscosity of paper pulp reaches maximum 763mL/g.When the treatment effect of pH value 8 and 9 is substantially suitable, gap is very little, can draw thus zytase X 3The better pH value of pretreating paper pulp is 8-9.
Table 9 pH value is to zytase X 3Pretreating paper pulp is on the impact of oxygen delignification effect
Figure BDA00003525588400072
Annotate: enzyme dosage is 10IU/g, temperature 50 C, and time 120min starches dense 10%.
Can find out from table 7,8,9, the pH value of three kinds of zytases treatment effect to paper pulp in the 8-10 scope is all more satisfactory.Zytase X 1, X 2And X 3Best pH value all is 8-9.It is different that this and three kinds of enzymes are used for the optimal pH of Aspen KP slurry, also there are differences with the zymologic property of three kinds of zytases.The most suitable pH value of the zymologic property test of these three kinds of zytases all is 8, optimal pH when processing fast-growing poplar NaOH-AQ slurry all is 8-9, this shows that the alkali resistance of three kinds of zytases when processing this slurry increases, and the enzyme that is conducive to after the soda pulping process is processed.
1.4 the time is on the impact of fast-growing poplar NaOH-AQ slurry oxygen delignification effect
There is certain influence time to xylanase treatment fast-growing poplar NaOH-AQ slurry.If the time is too short, the effect of zytase and paper pulp is abundant not, can not bring into play its usefulness.If overlong time is unfavorable for enhancing productivity.Based on this, in immobilized enzyme consumption, temperature, pH value with starch and studied the time under the dense condition to the impact of NaOH-AQ slurry pretreating effect.Experimental result sees Table 10,11,12.
Table 10 time is to zytase X 1Pretreating paper pulp is on the impact of oxygen delignification effect
Figure BDA00003525588400073
Annotate: enzyme dosage is 10IU/L, temperature 50 C, and pH value 8 starches dense 10%
As can be seen from Table 10, along with the prolongation of time, zytase X 1The NaOH-AQ slurry of processing is tending towards constant or slightly reduces after the pulp brightness behind the oxygen delignification progressively raises.When the processing time was 120min, the whiteness of paper pulp reached peak 60.5%ISO, and the paper pulp of more not processing with enzyme exceeds 1.4%ISO; The Kappa number of paper pulp is tending towards constant after progressively reducing first, and the processing time, the Kappa number of paper pulp was down to 7.6 when being 120min, and more untreated paper pulp hangs down 0.9 unit; The viscosity of paper pulp is along with the prolongation of time is tending towards substantially constant after progressively raising, and when the processing time was 120min, the viscosity of paper pulp reached maximum 767mL/g.Also can find out from table 10, the time of enzyme pulp treatment is when being 90min, and effect is not best but has kept higher whiteness, lower Kappa number and higher viscosity yet, meets the needs of production to a certain extent.Therefore, zytase X 1The time 90-120min of pulp treatment is advisable.
As can be seen from Table 11, along with the prolongation of time, zytase X 2Fast-growing poplar NaOH-AQ slurry after the processing is behind oxygen delignification, and the whiteness of paper pulp also is the rear reduction that raises first, and when the time was 120min, the whiteness of paper pulp reached the highest 60.6%ISO; After descending first, the Kappa number of paper pulp raises to some extent, when the time is 120min, and paper pulp kappa number minimum 7.7; After raising first, the viscosity of paper pulp descends to some extent, when the time is 90min, and the highest 765mL/g of viscosity of paper pulp.The experimental result of consolidated statement 11, zytase X 2The time of pulp treatment is that 90-120min is comparatively desirable.
Table 11 time is to zytase X 2Pretreating paper pulp is on the impact of oxygen delignification effect
Figure BDA00003525588400081
Annotate: enzyme dosage is 8IU/g, 55 ℃ of temperature, and pH value 8-9 starches dense 10%.
As can be seen from Table 12, along with the prolongation of time, zytase X 3Fast-growing poplar NaOH-AQ slurry after the processing is behind oxygen delignification, and the viscosity of paper pulp raises first and omits afterwards reduction, and when the processing time was 120min, the viscosity of paper pulp reached maximum 760mL/g; The whiteness of paper pulp also is the rear reduction that raises first, and when the processing time was 120min, the whiteness of paper pulp reached maximum 60.5%ISO; It is large that the Kappa number of paper pulp reduces first rear change, and when the processing time was 120min, the Kappa number of paper pulp was down to minimum 7.7.Also can find out zytase X from table 12 3The pulp treatment time, the whiteness of paper pulp was the highest, Kappa number is minimum, viscosity is the highest when being 120min, surpassed this time treatment effect and just began to weaken.
Table 12 time is to zytase X 3Pretreating paper pulp is on the impact of oxygen delignification effect
Figure BDA00003525588400082
Annotate: enzyme dosage is 10IU/g, temperature 50 C, and pH value 8-9 starches dense 10%.
Comprehensive above-mentioned experimental technique analysis result can draw the process conditions that three kinds of better processing fast-growing poplar NaOH-AQ of zytase starch: zytase X 1The preferred process condition be: enzyme dosage 10IU/L, temperature 50 C, pH8-9, time 90-120min; Zytase X 2The preferred process condition be: enzyme dosage 8IU/g, 55 ℃ of temperature, pH8-9, time 90-120min; Zytase X 3The preferred process condition be: enzyme dosage 10IU/g, temperature 50 C, pH8-9, time 120min.
The optimization of embodiment 2 bleaching conditions
2.1.1 raw material
Experiment is to mix the quick growth poplar wood sheet with the quick growth poplar wood sheet, takes from Shandong sun Paper Co., Ltd.Chip dimensions length 15-25mm, width 10-20mm, thickness 3-5mm, the qualification rate of wood chip is more than 90%, and is after wood chip is fetched from the stock ground, for subsequent use behind the natural air drying equilibrium water conten.
Zytase X 1Provided by Novozymes Company, liquid, the cellulose-less enzyme is lived; Zytase X 2, X 3All have Shenzhen biological Co., Ltd of green little health to provide, be the white powder solid, all cellulase is not lived.
2.1.2 boiling experiment
In 15L electric heating rotating autoclave, carry out boiling, make fast-growing poplar NaOH anthraquinone magma.The condition of boiling is: alkali charge 22%(is to the over dry raw material, and NaOH counts), AQ consumption 0.05%, liquor ratio 1:4,165 ℃ of boiling maximum temperatures are carried out little venting 10-15min, heating-up time 90min, temperature retention time 90min in the time of 105 ℃.The boiling disposed slurry is through fully washing, screening.Paper pulp yield 49.8%, the Kappa number 18.5 of paper pulp, viscosity 912ml/g, whiteness 36.1%ISO.
2.1.3 xylanase pretr eatment
Three kinds of xylanase pretr eatment experiments are all finished in polyethylene plastic bag.The fast-growing poplar NaOH-AQ slurry good washing after the boiling mixes in plastic bag with enzyme, enzyme treatment process condition and experimental procedure according to embodiment 1 optimization, regulate the pH value and starch zytase liquid that dense rear handle modulates put into bag and evenly mix after, put into the water-bath that sets temperature and carry out constant temperature and process.In processing procedure, every interval 10-15min rubs once with hand, to guarantee that enzyme mixes with the even of paper pulp.Slurry takes out after processing the stipulated time, then puts into boiling water bath 10min, makes zytase inactivation cessation reaction, with entering the following bleaching operation behind the running water cleaning paper pulp.
2.1.4 oxygen delignification and the experiment of reinforcement oxygen delignification
The experiment of fast-growing poplar NaOH-AQ slurry oxygen delignification is carried out in JF-DSTE polymerization reaction kettle (have and stir and the automatic constant-temperature function).Its Oxygen Delignification of Fast-Growing is: starch dense 10%, NaOH consumption 2.5%, oxygen is pressed 0.6MPa, 100 ℃ of temperature, time 80min, MgSO 4All drug dosages of consumption 0.5%(are all for oven dry stock, and are as follows).
The process conditions of two sections oxygen delignifications: first paragraph O 1: starch dense 10%, NaOH consumption 2%, oxygen is pressed 0.6MPa, 100 ℃ of temperature, time 20min, MgSO 4Consumption 0.5%; Second segment O 2: replenish 0.5% NaOH, oxygen is pressed 0.5MPa, time 60min.
Fast-growing poplar NaOH-AQ slurry is strengthened oxygen delignification O pProcess conditions be: starch dense 10%, NaOH consumption 2.5%, oxygen is pressed 0.6MPa, 100 ℃ of temperature, MgSO 4Consumption 0.5%, Na 2SiO 3Consumption 0.7%, H 2O 2Consumption 3%, time 80min.
First paragraph oxygen delignification and second segment are strengthened the process conditions of oxygen delignification: first paragraph O 1: starch dense 10%, NaOH consumption 2%, oxygen is pressed 0.6MPa, 100 ℃ of temperature, time 20min, MgSO 4Consumption 0.5%; Second segment O 2P: replenish 0.5% NaOH, add 3% H 2O 2, Na 2SiO 3Consumption 0.7%, oxygen is pressed 0.5MPa, time 60min.
Two sections process conditions of strengthening oxygen delignification: first paragraph O 1P: starch dense 10%, NaOH consumption 2%, H 2O 2Consumption 1%, oxygen is pressed 0.6MPa, 100 ℃ of temperature, time 20min, Na 2SiO 3Consumption 0.7%, MgSO 4Consumption 0.5%; Second segment O 2P: replenish 0.5% NaOH, add 2.5% H 2O 2, oxygen is pressed 0.5MPa, time 60min.
2.1.5 the bleaching experiment of paper pulp
The bleachings such as D, E, Q, P or processing section carry out in polyethylene plastic bag respectively.Get the 30g oven dry stock at every turn, according to the experimental procedure of drafting, pour in the plastic bag after required liquid evenly mixed, put into thermostat water bath after slurry and liquid are mixed and bleach or process.In the process of bleaching or processing, every interval 15min takes out and rubs even mixing once with hand, guarantees paper pulp and the even mixing of floating agent.
2.1.6 analytical method
The mensuration of viscosity: the method according to standard GB/T 1548-1989 regulations is carried out.
Kappa number must be measured: according to GB1546-1989 standard test
The mensuration of whiteness: paper pulp is discongested after device discongests through fiber, copies into the scraps of paper at Buchner funnel, and is air-dry rear with YQ-Z-48B
The whiteness instrument is measured
Folding number: domestic MIT folding strength tester is measured in using.
Burst index: use swedish company L﹠amp; The bursting strength tester that W produces is measured.
Fracture length: use swedish company L﹠amp; The anti-tester that W produces is measured.
Tear index: measure with the tearability tester that the TMI of u s company produces.
2.1.7 the mensuration of making beating and beating energy consumption
Slurry behind the defibrination adopts KRK company to produce the PFI mill and pulls an oar, and beating consistency is 10%, and beater roll(er) and beater chamber gap are 0.2mm, and beating pressure is 3.4Nmm -1The beating degree of making beating disposed slurry is measured and is adopted Xiao Baier-Rui Gele YQ-Z-13 beating degree analyzer to measure.
The revolution of making beating specific energy consumption: PFI mill is linear with beating energy consumption within the specific limits [119], this experiment required making beating revolution when reaching identical beating degree calculates can loss-rate.Bleached pulp making beating revolution * 100% of the beating energy consumption reduction rate in this experiment=(enzyme is processed the bleached pulp making beating revolution of after bleaching slurry making beating revolution-do not process with enzyme)/do not process with enzyme.
2.1.8 ESEM
To under the identical experiment condition of embodiment 1 " oxygen delignification experiment ", carry out respectively oxygen-delignified pulp from magma through the paper pulp that different enzymes are processed, carry out the different orders of floating subsequently and bleach gained paper pulp etc., after the running water washing, utilizing the quick handshcet former of triumphant match to copy the formulation amount is 60g/m 2The l Water Paper page or leaf then with l Water Paper page or leaf in vacuum drier dry 48 hours, after metal spraying is processed, is that the ESEM of QUANTA200 is observed and taken pictures in model, and accelerating potential is 10kV.
2.1.9 atomic force microscope observation
Getting slurry sample 0.1g to be measured is distributed in the distilled water of 200mL, break up with dispersing device, fiber is evenly distributed in the water, then getting a droplet with pipette is put on the mica sheet, so that single fiber is distributed on the mica sheet, then air-dry 24h under the room temperature uses MultiMode SPM model AFM (AFM) produced in USA to carry out scanning and photograph, and the model of probe is NP-20.
2.1.10 xylanase activity is measured
Adopt the DNS method to measure (being conventional determining method of the prior art).
2.1.11 enzyme preparation characteristic is determined
Zytase X 1, X 2, X 3Enzyme activity determination measure according to the DNS method, it the results are shown in Table 13 and table 14.
The characteristic of table 13 liquid xylanase preparation
The characteristic of table 14 solid xylanase preparation
Figure BDA00003525588400102
2.2 result and discussion
2.2.1 xylanase treatment is to the effect of fast-growing poplar NaOH-AQ slurry ECF bleaching
Zytase is used for the preliminary treatment before the association with pulp bleaching, and the consumption that reduces chlorine-containing bleaching is arranged, and further alleviates the pollution to environment, improve filterability and the fragility of paper pulp, increase fiber separating degree, improve the whiteness of floating rear paper pulp, reduce beating energy consumption, the advantage such as save production cost [155,156]For this reason, the present invention carries out bleaching research to the fast-growing poplar NaOH-AQ slurry that three kinds of Novel wooden glycan are used for different bleaching process, inquire into the whiteness of Xylanase-aided Bleaching paper pulp, the fibre morphology variation etc. that becomes the physical strength index of paper and float rear slurry, for novel commercial xylanase is already changed application and popularization provides theoretical foundation at fast-growing poplar NaOH-AQ pulp bleaching.
The present embodiment contains all bleaching process of oxygen delignification section bleaching, all carries out before oxygen delignification during xylanase treatment paper pulp, and its process conditions are the xylanase treatment process conditions of optimizing among the embodiment 1.
2.2.1.1 three kinds of xylanase pretr eatments are starched the impact of ODQP bleaching results on fast-growing poplar NaOH-AQ
Adopt zytase X 1, X 2And X 3Before fast-growing poplar NaOH-AQ slurry ODQP floats the order bleaching, carry out preliminary treatment, inquire into xylanase treatment to the impact of fast-growing poplar NaOH-AQ slurry bleachability.
Starch the process conditions of oxygen delignification best results according to three kinds of xylanase treatment fast-growing poplar NaOH-AQ of embodiment 1 optimization, carry out this experiment in conjunction with the ODQP bleaching conditions.Concrete process conditions are as follows: X 1The process conditions of processing: enzyme dosage 10IU/L, 55 ℃ of temperature, pH8-9, time 120min; X 2The process conditions of processing: enzyme dosage 8IU/g, temperature 60 C, pH9, time 120min; X 3The process conditions of processing: enzyme dosage 10IU/g, 55 ℃ of temperature, pH8-9, time 120min.
ODQP floats the process conditions of order bleaching: the process conditions of oxygen delignification section are seen 2.1.4.D section: ClO 2Consumption is 0.6%, original ph 5, temperature 70 C, starch dense 10%, time 120min; The Q section: starch dense 8%, DTPA consumption 0.5%, temperature 70 C, time 60min, pH value 4-5; P section: H 2O 2Consumption is 3%, Na 2SiO 3Consumption 0.7%, MgSO 4Consumption 0.5%, original ph 12,90 ℃ of temperature, starch dense 10%, time 90min.
Through and do not carry out simultaneously the ODQP bleaching through the fast-growing poplar NaOH-AQ of xylanase treatment slurry, to guarantee the comparativity of bleaching results, xylanase pretr eatment sees Table 15 to fast-growing poplar NaOH-AQ slurry ODQP bleaching results.Paper pulp after the bleaching is pulled an oar with the PFI mill, and the making beating revolution of controlling various slurries is controlled at about 41 ° of SR its beating degree, then copies and makes quantitative 60g/m 2Paper, then the physical properties such as its folding strength, bursting strength, tear index, fracture length are detected its result such as table 16.
As can be seen from Table 15, fast-growing poplar NaOH-AQ slurry floats bleaching results that order finishes through XODQP and is better than ODQP and floats order.X wherein 2The final bleaching whiteness that ODQP floats order is the highest, reaches 87.7%, and the final whiteness of floating order than ODQP exceeds 3.0%ISO, and floats the pulp viscosity 742mLg that has kept the highest in the order at these four kinds -1Next is X 3The bleaching results that ODQP floats order is comparatively desirable, and the final whiteness of paper pulp reaches 87.4%ISO, and the final whiteness of floating order than ODQP exceeds 2.7%ISO, and has kept higher pulp viscosity 737mLg -1That the enzyme action effect is relatively weak is X 1ODQP floats order, but the final whiteness of floating rear slurry has also reached 87.2%ISO, and the final whiteness that the ODQP that does not more process with enzyme floats order exceeds 2.5%ISO, and the viscosity of paper pulp also exceeds 13mLg than the viscosity of the paper pulp of not processing with enzyme -1
Table 15 xylanase pretr eatment is on the impact of fast-growing poplar NaOH-AQ slurry ODQP bleaching results
As can be seen from Table 15, through xylanase treatment and do not pass through the paper pulp of xylanase treatment, float the order bleaching through ODQP after, the final Kappa number of paper pulp is also different, X 2It is minimum 2.1 that ODQP floats the Kappa number of order, floats low 0.4 unit of Kappa number of order than ODQP, secondly is X 1ODQP and X 3The Kappa number that ODQP floats order is 2.2, floats low 0.3 unit of Kappa number of order than ODQP.These show, the NaOH-AQ slurry through enzyme is processed floats in the order bleaching process at ODQP, more is conducive to removing of lignin, further reduces the Kappa number of paper pulp, and have kept than the conventional higher pulp viscosity of order bleaching that floats.
Also can find out from table 15, after paper pulp process ODQP and the XODQP bleaching, copy the quantitative 60g/m of being that makes through making beating 2Paper, the whiteness of paper has decline in various degree.Wherein, it is at most 2.1%ISO that the whiteness of floating order through the ODQP of xylanase treatment reduces, the X that processes through enzyme 2The whiteness reduction minimum that ODQP floats order is 1.9%ISO, through X 1ODQP and X 3The loss of whiteness that ODQP floats order is 2.0%ISO, these show through the loss of whiteness of the paper pulp of three kinds of xylanase treatments paper pulp after making beating still less, this may be because the Kappa number of slurry is lower after the floating after processing through enzyme, lignin content still less, paper pulp is difficult for brightness reversion.
As can be seen from Table 16, the paper pulp of fast-growing poplar NaOH-AQ slurry after the paper pulp after the XODQP bleaching is than the ODQP bleaching is more easily pulled an oar.When reaching close 41 ° of SR of beating degree, required making beating revolution still less, the beating energy consumption reduction rate is greatly about about 17.8%, this may be because the processing of paper pulp process zytase, liquid soaks into more deep abundant to paper pulp ground, so that paper pulp fiber is softening, save beating energy consumption when more easily pulling an oar.
The comparison of table 16ODQP/XODQP bleached pulp physical properties of paper
Figure BDA00003525588400112
Figure BDA00003525588400121
The physical indexs such as the folding strength of the paper pulp after as can be seen from Table 16, the paper pulp after the XODQP bleaching is bleached than ODQP, bursting strength, fracture length are better.The bleached pulp that XODQP and ODQP float order is all copied and made quantitatively is 60g/m 2Paper, through X 2Physical property of pulp after the ODQP bleaching is best, and with exceeding 41 times that enzyme is processed, fracture length has not improved 0.37Km to the folding strength ratio, and burst index exceeds 0.4Nmg -1, several slurry tear indexes are very approaching, but X 2It also is that this severally floats rear slurry and copy the maximum 6.12mNm that makes paper that ODQP floats rear slurry 2G -1Through X 1ODQP and X 3ODQP floats the rear slurry of floating of order, has shown equally good physical property: these two kinds of bleached pulps are copied the paper folding strength of making than the ODQP bleached pulp and are improved respectively 28 times and 19, and fracture length improves respectively 0.24 and 0.3Km, and burst index exceeds respectively 0.3 and 0.2Nmg -1But through X 1ODQP and X 3The rear slurry that floats of ODQP slightly descends than the tear index that floats rear slurry of ODQP.
In sum, after fast-growing poplar NaOH-AQ slurry floats the order bleaching through XODQP, can improve the final whiteness 2.5-3.0%ISO of paper pulp, XODQP floats rear slurry and floats rear slurry than ODQP and kept higher pulp viscosity, keep better bleaching selectivity, improved more significantly the physical property of floating rear slurry.
2.2.1.2 three kinds of xylanase pretr eatments are to fast-growing poplar NaOH-AQ slurry O PThe impact of DQP bleaching results
Adopt zytase X 1, X 2And X 3At fast-growing poplar NaOH-AQ slurry O PDQP carries out preliminary treatment before floating the order bleaching, inquires into xylanase treatment to fast-growing poplar NaOH-AQ slurry O PDQP floats the impact of order bleachability.
The process conditions of three kinds of xylanase treatment fast-growing poplar NaOH-AQ oxygen delignification best results optimizing according to embodiment 1 are in conjunction with O PThe DQP bleaching conditions carry out this experiment.Concrete process conditions are as follows: X 1The process conditions of processing: enzyme dosage 10IU/L, 55 ℃ of temperature, pH8-9, time 120min; X 2The process conditions of processing: enzyme dosage 8IU/g, temperature 60 C, pH9, time 120min; X 3The process conditions of processing: enzyme dosage 10IU/g, 55 ℃ of temperature, pH8-9, time 120min.
O PDQP floats the process conditions of order bleaching: the process conditions of oxygen delignification section are seen 2.1.4.D section: ClO 2Consumption is 0.4%, original ph 5, temperature 70 C, starch dense 10%, time 120min; The Q section: starch dense 8%, DTPA consumption 0.5%, temperature 70 C, time 60min, pH value 4-5; P section: H 2O 2Consumption is 2%, Na 2SiO 3Consumption 0.7%, MgSO 4Consumption 0.5%, original ph 12,90 ℃ of temperature, starch dense 10%, time 90min.
The fast-growing poplar NaOH-AQ slurry that passes through and do not pass through xylanase treatment carries out O simultaneously PThe DQP bleaching, to guarantee the comparativity of bleaching results, xylanase pretr eatment is to fast-growing poplar NaOH-AQ slurry O PThe DQP bleaching results sees Table 17.Paper pulp after the bleaching is pulled an oar with the PFI mill, and the making beating revolution of controlling various slurries is controlled at about 44.2 ° of SR its beating degree, then copies and makes quantitative 60g/m 2Paper, then the physical properties such as its folding strength, bursting strength, tear index, fracture length are detected its result such as table 18.
Table 17 xylanase pretr eatment is to fast-growing poplar NaOH-AQ slurry O PThe impact of DQP bleaching results
Table 17 can find out, fast-growing poplar NaOH-AQ starches through O PDQP floats the bleaching results that order finishes and is better than O PDQP floats order.X wherein 2O PThe final bleaching whiteness that DQP floats order is the highest, reaches 88.5%ISO, than O PThe final whiteness that DQP floats order exceeds 3.2%ISO, and floats the pulp viscosity 728mL/g that has kept the highest in the order at these four kinds; X 3O PThe final whiteness that DQP floats the bleached pulp of order reaches 88.2%ISO, than O PThe final whiteness that DQP floats order exceeds 2.9%ISO, and has kept higher pulp viscosity 713mL/g, exceeds 12mL/g than the viscosity of the paper pulp of not processing with enzyme; X 1O PThe final whiteness of floating rear slurry that DQP floats order has also reached 88.1%ISO, the O that does not more process with enzyme PThe final whiteness that DQP floats order exceeds 2.8%ISO, and the viscosity of paper pulp is 714mL/g, exceeds 13mL/g than the viscosity of the paper pulp of not processing with enzyme.
As can be seen from Table 17, through xylanase treatment and not through the fast-growing poplar NaOH-AQ of xylanase treatment slurry, through O PAfter DQP floated order bleaching, the final Kappa number of paper pulp was also different, X 2O PIt is minimum 1.7 that DQP floats the Kappa number of order, than O PDQP floats low 0.4 unit of Kappa number of order, secondly is X 1O PDQP and X 3O PThe Kappa number that DQP floats order is 1.8, than O PDQP floats low 0.3 unit of Kappa number of order.These show, through the NaOH-AQ slurry of enzyme processing, at O PDQP floats in the order bleaching process, more is conducive to removing of lignin, further reduces the Kappa number of paper pulp, and has kept than the conventional higher pulp viscosity of order bleaching that floats.
Also can find out from table 17, fast-growing poplar NaOH-AQ slurry is through O PDQP and XO PAfter the DQP bleaching, copy the quantitative 60g/m of being that makes through making beating 2Paper, the whiteness of paper has decline in various degree.Wherein, do not pass through the O of xylanase treatment PThe whiteness reduction that DQP floats order is at most 2.0%ISO, through the X of enzyme processing 2O PThe whiteness reduction minimum that DQP floats order is 1.7%ISO, through X 1O PDQP and X 3O PThe loss of whiteness that DQP floats order is 1.8%ISO, these show through the loss of whiteness of the paper pulp of three kinds of xylanase treatments paper pulp after making beating still less, this may be because the Kappa number of slurry is lower after the floating after processing through enzyme, lignin content still less, paper pulp is difficult for brightness reversion.
Can find out from table 15 and 17, through XO PDQP and XODQP, O PDQP and ODQP float the paper pulp of order bleaching, and the former whiteness is higher, and the loss of viscosity is larger; Generally speaking, it is difficulty relatively that the whiteness of paper pulp reaches 88%ISO, but through processing and the O of three zytases PDQP floats the bleaching of order, has all reached more than the 88.0%ISO, and these experimental datas show that the preliminary treatment of zytase helps to solve the practical difficulty that the final whiteness of paper pulp is difficult to raising, and this will be conducive to the application of zytase in actual production.
Table 18 O PDQP/XO PThe comparison of DQP bleached pulp physical properties of paper
Figure BDA00003525588400131
As can be seen from Table 18, fast-growing poplar NaOH-AQ slurry is through XO PPaper pulp after the DQP bleaching compares O PPaper pulp after the DQP bleaching is more easily pulled an oar.When reaching close 44.2 ° of SR left and right sides of beating degree, required making beating revolution still less, the beating energy consumption reduction rate is greatly about about 17.8%.Contrast table 16 and 18 can find, under the identical making beating revolution of correspondence, and XO PDQP and O PDQP floats the beating degree of order and floats about the high 3 ° of SR of beating degree of order than XODQP and ODQP, the XO of fast-growing poplar NaOH-AQ slurry PDQP floats order and more easily pulls an oar and more save beating energy consumption.
As can be seen from Table 18, fast-growing poplar NaOH-AQ slurry is through XO PPaper pulp after the DQP bleaching compares O PThe physical indexs such as the folding strength of the paper pulp after the DQP bleaching, bursting strength, fracture length are better.XO PDQP and O PThe bleached pulp that DQP floats order is all copied and made quantitatively is 60g/m 2Paper, through X 2O PPhysical property of pulp after the DQP bleaching is best, and with exceeding 38 times that enzyme is processed, fracture length has not improved 0.35Km to the folding strength ratio, and burst index exceeds 0.5Nmg -1, several slurry tear indexes are very approaching, but X 2O PIt also is that this severally floats rear slurry and copy the maximum 5.73mNm that makes paper that DQP floats rear slurry 2G -1Through X 1O PDQP and X 3O PDQP floats the rear slurry of floating of order, has shown equally good physical property: these two kinds of bleached pulps are than O PThe DQP bleached pulp is copied the paper folding strength of making and is improved respectively 33 and 24 times, and fracture length improves respectively 0.18 and 0.27Km, and burst index improves respectively 0.2 and 0.3Nmg -1But through X 1O PDQP and X 3O PDQP floats rear slurry than O PThe tear index gap of floating rear slurry of DQP is very little.
In sum, fast-growing poplar NaOH-AQ slurry is through XO PAfter DQP floats the order bleaching, can improve the final whiteness 2.8-3.2%ISO of paper pulp, XO PDQP floats rear slurry than O PDQP floats rear slurry and has kept higher pulp viscosity, has kept better bleaching selectivity, has improved more significantly the physical property of floating rear slurry.
2.2.1.3 three kinds of xylanase pretr eatments are to fast-growing poplar NaOH-AQ slurry O 1O 2PThe impact of DQP bleaching results
Adopt zytase X 1, X 2And X 3At fast-growing poplar NaOH-AQ slurry O 1O 2PDQP carries out preliminary treatment before floating the order bleaching, inquires into xylanase treatment to fast-growing poplar NaOH-AQ slurry O 1O 2PDQP floats the impact of order bleachability.
The process conditions of three kinds of xylanase treatment fast-growing poplar NaOH-AQ oxygen delignification best results optimizing according to embodiment 1 are in conjunction with O 1O 2PThe DQP bleaching conditions carry out this experiment.Concrete process conditions are as follows: X 1The process conditions of processing: enzyme dosage 10IU/L, 55 ℃ of temperature, pH8-9, time 120min; X 2The process conditions of processing: enzyme dosage 8IU/g, temperature 60 C, pH9, time 120min; X 3The process conditions of processing: enzyme dosage 10IU/g, 55 ℃ of temperature, pH8-9, time 120min.
O 1O 2PDQP floats the process conditions of order bleaching: the process conditions of oxygen delignification section are seen 2.1.4.D section: ClO 2Consumption is 0.4%, original ph 5, temperature 70 C, starch dense 10%, time 120min; The Q section: starch dense 8%, DTPA consumption 0.5%, temperature 70 C, time 60min, pH value 4-5; P section: H 2O 2Consumption is 2%, Na 2SiO 3Consumption 0.7%, MgSO 4Consumption 0.5%, original ph 12,90 ℃ of temperature, starch dense 10%, time 90min.
The fast-growing poplar NaOH-AQ slurry that passes through and do not pass through xylanase treatment carries out O simultaneously 1O 2PThe DQP bleaching, to guarantee the comparativity of bleaching results, xylanase pretr eatment is to fast-growing poplar NaOH-AQ slurry O 1O 2PThe DQP bleaching results sees Table 19.Paper pulp after the bleaching is pulled an oar with the PFI mill, and the making beating revolution of controlling various slurries is controlled at about 45.2 ° of SR its beating degree, then copies and makes quantitative 60g/m 2Paper, then the physical properties such as its folding strength, bursting strength, tear index, fracture length are detected its result such as table 20.
Table 19 can find out, fast-growing poplar NaOH-AQ starches through XO 1O 2PDQP floats the bleaching results that order finishes and is better than O 1O 2PDQP floats order.X wherein 2O 1O 2PThe final bleaching whiteness that DQP floats order is the highest, reaches 88.2%ISO, than O 1O 2PThe final whiteness that DQP floats order exceeds 3.2%ISO, and floats the pulp viscosity 741mL/g that has kept the highest in the order at these four kinds; X 3O 1O 2PThe final whiteness that DQP floats the bleached pulp of order reaches 88.0%ISO, than O 1O 2PThe final whiteness that DQP floats order exceeds 3.0%ISO, and has kept higher pulp viscosity 729mL/g, exceeds 9mL/g than the viscosity of the paper pulp of not processing with enzyme; X 1O 1O 2PThe final whiteness of floating rear slurry that DQP floats order is 87.8%ISO, the O that does not more process with enzyme 1O 2PThe final whiteness that DQP floats order exceeds 2.8%ISO, and the viscosity of paper pulp is 729mL/g, exceeds 9mL/g than the viscosity of the paper pulp of not processing with enzyme.
Table 19 xylanase pretr eatment is to fast-growing poplar NaOH-AQ slurry O 1O 2PThe impact of DQP bleaching results
Figure BDA00003525588400141
As can be seen from Table 19, through xylanase treatment and not through the fast-growing poplar NaOH-AQ of xylanase treatment slurry, through O 1O 2PAfter DQP floated order bleaching, the final Kappa number of paper pulp was also different, X 2O 1O 2PDQP and X 3O 1O 2PIt is minimum 1.7 that DQP floats the Kappa number of order, than O 1O 2PDQP floats low 0.4 unit of Kappa number of order, X 1O 1O 2PThe Kappa number that DQP floats order is 1.8, than O 1O 2PDQP floats low 0.3 unit of Kappa number of order.These show, through the NaOH-AQ slurry of enzyme processing, at O 1O 2PDQP floats in the order bleaching process, more is conducive to removing of lignin, further reduces the Kappa number of paper pulp, and has kept than the conventional higher pulp viscosity of order bleaching that floats.
Also can find out from table 19, fast-growing poplar NaOH-AQ slurry is through O 1O 2PDQP and XO 1O 2PAfter the DQP bleaching, copy the quantitative 60g/m of being that makes through making beating 2Paper, the whiteness of paper has decline in various degree.Wherein, do not pass through the O of xylanase treatment 1O 2PThe whiteness reduction value that DQP floats order is 2.0%ISO, through the X of enzyme processing 2O 1O 2PDQP and X 3O 1O 2PThe whiteness that DQP floats order reduces the minimum 1.7%ISO of being, through X 1O 1O 2PThe loss of whiteness that DQP floats order is 1.8%ISO, these show through the loss of whiteness of the paper pulp of three kinds of xylanase treatments paper pulp after making beating still less, this may be because the Kappa number of slurry is lower after the floating after processing through enzyme, lignin content still less, paper pulp is difficult for brightness reversion.
Can find out from table 17 and 19, through XO PDQP and XO 1O 2PDQP, O PDQP and O 1O 2PDQP floats the paper pulp of order bleaching, and the former whiteness is slightly high, and the loss of viscosity is larger; These show that one section oxygen delignification strengthens oxygen delignification and strengthen oxygen delignification and compare with one section with one section, the pulp brightness that both are final close, but the former is conducive to the viscosity that keeps paper pulp higher.
Table 20 O 1O 2PDQP/XO 1O 2PThe comparison of DQP bleached pulp physical properties of paper
Figure BDA00003525588400151
As can be seen from Table 20, fast-growing poplar NaOH-AQ slurry is through XO 1O 2PPaper pulp after the DQP bleaching compares O 1O 2PPaper pulp after the DQP bleaching is more easily pulled an oar.When reaching close 44.2 ° of SR left and right sides of beating degree, required making beating revolution is still less saved beating energy consumption approximately 17.8%.Contrast table 18 and 20 can find, under the identical making beating revolution of correspondence, and XO PDQP and XO 1O 2PDQP, O PDQP and O 1O 2PDQP floats rear slurry making beating revolution when identical, and the former beating degree is about 44.2 ° of SR, and the latter's beating degree is about 43.8 ° of SR, and this is because one section oxygen delignification O 1With one section reinforcement oxygen delignification O 2PStrengthen oxygen delignification O than one section PAfter the DQP bleaching identical through postorder, when pulp brightness is identical with Kappa number or close, O 1O 2PCompare O PThe damage that the better effects if of oxygen delignification, fiber are subject to is less, and the viscosity of paper pulp is higher, and the fiber average degree of polymerization is larger.And XO 1O 2PDQP compares XO PDQP, O 1O 2PDQP compares O PIt is better that DQP floats the physical indexs such as rear folding strength of starching into paper, burst index, fracture length, tear index.
As can be seen from Table 20, fast-growing poplar NaOH-AQ slurry is through XO 1O 2PPaper pulp after the DQP bleaching compares O 1O 2PThe physical indexs such as the folding strength of the paper pulp after the DQP bleaching, bursting strength, fracture length are better.XO 1O 2PDQP and O 1O 2PThe bleached pulp that DQP floats order is all copied and made quantitatively is 60g/m 2Paper, through X 2O 1O 2PPhysical property of pulp after the DQP bleaching is best, and with exceeding 38 times that enzyme is processed, fracture length has not improved 0.3Km to the folding strength ratio, and burst index exceeds 0.4Nmg -1, several slurry tear indexes are very approaching, but X 2O 1O 2PIt also is that this severally floats rear slurry and copy the maximum 5.77mNm that makes paper that DQP floats rear slurry 2G -1Through X 1O 1O 2PDQP and X 3O 1O 2PDQP floats the rear slurry of floating of order, has shown equally good physical property: these two kinds of bleached pulps are than O 1O 2PThe DQP bleached pulp is copied the paper folding strength of making and is improved respectively 32 and 26 times, and fracture length improves respectively 0.12 and 0.24Km, and burst index improves respectively 0.2 and 0.3Nmg -1But through X 1O 1O 2PDQP and X 3O 1O 2PDQP floats rear slurry than O 1O 2PThe tear index that floats rear slurry of DQP descends a little, but gap is very little.
In sum, fast-growing poplar NaOH-AQ slurry is through XO 1O 2PAfter DQP floats the order bleaching, can improve the final whiteness 2.8-3.2%ISO of paper pulp, XO 1O 2PDQP floats rear slurry than O 1O 2PDQP floats rear slurry and has kept higher pulp viscosity, has kept better bleaching selectivity, has improved more significantly the physical property of floating rear slurry.
2.2.3 scanning electron microscope analysis
Be further to understand before and after three kinds of xylanase treatment fast-growing poplar NaOH-AQ slurries and bleaching finish after the variation of fiber exterior appearance, magma, enzyme are processed slurry and corresponding bleached pulp is observed with environmental scanning electronic microscope.
ECF bleached pulp scanning electron microscopic observation
Choose fast-growing poplar NaOH-AQ magma, process X 1The NaOH-AQ magma of processing, process X 2The NaOH-AQ magma of processing, process X 3The NaOH-AQ magma, ODQP bleached pulp, the X that process 1ODQP bleached pulp, X 2ODQP bleached pulp, X 3The ODQP bleached pulp, obtain Fig. 1～stereoscan photograph shown in Figure 8 according to the requirement of 2.1.8.
Under 3000 times environmental scanning electronic microscope, poplar NaOH-AQ magma is starched, X from Fig. 1,2,3,4 1The NaOH-AQ slurry, the X that process 2The NaOH-AQ slurry and the X that process 3The electromicroscopic photograph on the NaOH-AQ pulp fibres surface of processing can be found out significantly, does not pass through zytase X 1, X 2, X 3The fiber surface of the NaOH-AQ slurry of processing is smooth, and close structure exists without tiny or microfibre.Fiber surface through the NaOH-AQ of three kinds of xylanase treatments slurry seems loose, soft, and fiber surface fiber fines occurs like free state, and the surface area of fiber increases.
Under 3000 times environmental scanning electronic microscope, fast-growing poplar NaOH-AQ slurry is through ODQP bleaching, X from Fig. 5,6,7,8 1The NaOH-AQ slurry, the X that process 2The NaOH-AQ slurry and the X that process 3The NaOH-AQ that processes can find out through the electromicroscopic photograph of ODQP bleached pulp fiber surface, do not pass through xylanase treatment the ODQP bleached pulp fiber surface fiber fines seldom, but change to some extent the smooth but curling phenomenon of peripheral appearance of fiber surface than magma.The NaOH-AQ slurry of processing through enzyme is larger through the pulp freeness of ODQP bleached pulp, it is more loose, coarse and curling that fiber surface seems, it is more soft that fiber becomes, and what this can be interpreted as to a certain extent and more easily pull an oar through the bleached pulp of enzyme processing, more can reduce energy consumption.
2.3 the brief summary xylanase treatment is on the result that affects of fast-growing poplar NaOH-AQ slurry ECF bleaching
After bleaching through ECF with the fast-growing poplar NaOH-AQ slurry of not using xylanase treatment, the former whiteness and viscosity are higher, become the physical property of paper also to make moderate progress, and concrete outcome is as follows:
Fast-growing poplar NaOH-AQ slurry XODQP floats order at ClO 2Total consumption 0.6%, H 2O 2In the situation of total consumption 3%, the whiteness of bleached pulp is up to 87.7%ISO, minimum 87.2%ISO; The whiteness of ODQP bleached pulp is 84.7%ISO, through enzyme process than not with enzyme process float after the whiteness of slurry exceed 2.5-3.0%ISO, and kept higher pulp viscosity and lower Kappa number;
Fast-growing poplar NaOH-AQ starches XO PDQP floats order at ClO 2Total consumption 0.4%, H 2O 2In the situation of total consumption 5%, the whiteness of bleached pulp is up to 88.5%ISO, minimum 88.1%ISO; XO PThe whiteness of DQP bleached pulp is 85.3%ISO, through enzyme process than not with enzyme process float after the whiteness of slurry exceed 2.8-3.2%ISO, and kept higher pulp viscosity and lower Kappa number; This floats the ClO of order 2Consumption further reduces, more environmental protection.
Fast-growing poplar NaOH-AQ starches XO 1O 2PDQP floats order at ClO 2Total consumption 0.4%, H 2O 2In the situation of total consumption 5%, the whiteness of bleached pulp is up to 88.2%ISO, minimum 87.8%ISO; O 1O 2PThe whiteness of DQP bleached pulp is 85.0%ISO, through enzyme process than not with enzyme process float after the whiteness of slurry exceed 2.8-3.2%ISO, and kept higher pulp viscosity and lower Kappa number; This floats the ClO of order 2Consumption further reduces, and more is conducive to environmental protection.
Top XODQP and ODQP, XO PDQP and O PDQP, XO 1O 2PDQP and O 1O 2PThe ECF bleached pulp of DQP is copied through making beating and is made 60g/m 2Paper, the former making beating loss of whiteness value is than the latter still less; The former folding strength on average exceeds 30 times than the latter, and bursting strength on average exceeds 0.35Nmg -1, fracture length on average exceeds 0.25KM, and tear index is substantially constant or slightly descend but amplitude is very little.
Relatively the correspondence of three kinds of xylanase treatment fast-growing poplar NaOH-AQ slurries is floated the bleaching effect discovery of order: the effect of the pulp treatment of three kinds of enzymes is difference to some extent, from the initial effect that affects oxygen delignification, has influence on the bleaching results that ECF respectively floats order always.Wherein help float effect best be X 2, secondly be X 1And X 3Help that to float effect close.But on the whole, these three kinds of enzymes helps that to float effect all apparent in view.When reaching identical or close beating degree, the former required making beating revolution still less can be saved beating energy consumption about 17.8%.
The ESEM result
Under 3000 times environmental scanning electronic microscope, can be clearly seen that: through the fiber fines of the fiber surface of the fast-growing poplar NaOH-AQ of xylanase treatment slurry not seldom, but change to some extent the smooth but curling phenomenon of peripheral appearance of fiber surface than magma.The NaOH-AQ slurry of processing through enzyme is larger through the pulp freeness of ODQP bleached pulp, it is more loose, coarse and curling that fiber surface seems, it is more soft that fiber becomes, and what this can be interpreted as to a certain extent and more easily pull an oar through the bleached pulp of enzyme processing, more can reduce energy consumption.
Under 3000 times environmental scanning electronic microscope, from fast-growing poplar NaOH-AQ slurry O PQP bleached pulp, XO PThe electromicroscopic photograph of QP bleached pulp fiber surface can be found out, does not pass through the paper pulp of xylanase treatment through O PPulp fiber surface is smooth after the QP bleaching, and close structure is tiny or microfibre is considerably less.X through the enzyme processing 1O PQP, X 2O PQP and X 3O PThe specific area of the fiber of QP bleached pulp increases, and that fiber becomes is loose, microfibre increases, and it is more soft that fiber seems, more easily pulls an oar and reduces energy consumption.

Claims (7)

1. the NaOH anthraquinone of a fast-growing poplar is starched biochemical process ECF bleaching process, and it is characterized in that: step is as follows:
(1) boiling: get the quick growth poplar wood sheet, put into the digester boiling, get magma, the washing of then carrying out, screening get paper pulp;
(2) xylanase pretr eatment;
(3) ECF bleaching: the above-mentioned paper pulp of processing through enzyme is bleached, and bleaching process is ODQP, O PDQP or O 1O 2PThree kinds of DQP float one of order, and the step of bleaching process is: at first, the paper pulp of processing through enzyme is carried out the deoxidation lignin or strengthens the deoxidation lignin; Oxygen delignification washs paper pulp after finishing, and then carries out D section ClO 2 bleaching; D section ClO 2 bleaching washs paper pulp after finishing, and then carries out Q section chelation treatment; Q section chelation treatment is washed paper pulp after finishing, and then carries out P section H 2O 2Bleaching is finished.
2. the NaOH anthraquinone of a kind of fast-growing poplar according to claim 1 is starched biochemical process ECF bleaching process, it is characterized in that: the concrete mode of described boiling is: the quick growth poplar wood sheet of getting length 15～25mm, width 10～20mm, thickness 3～5mm, behind the natural air drying, carry out boiling, make fast-growing poplar NaOH anthraquinone magma, the condition of boiling is: alkali charge 22%, and to the over dry raw material, the NaOH meter; AQ consumption 0.05%, liquor ratio 1:4,165 ℃ of boiling maximum temperatures, the 10-15min that in the time of 105 ℃, exits, heating-up time 90min, temperature retention time 90min; The boiling disposed slurry gets paper pulp, the Kappa number 16～21 of paper pulp through washing, screening.
3. the NaOH anthraquinone of a kind of fast-growing poplar according to claim 1 is starched biochemical process ECF bleaching process, and it is characterized in that: the concrete mode of described xylanase pretr eatment is: adjusting pulp density is 10%, then uses zytase X 1, X 2Or X 3Process, in processing procedure, every interval 10～15min rubs once; Take out after processing, put into boiling water bath 10min, make zytase inactivation cessation reaction, clean paper pulp with running water.
4. the NaOH anthraquinone of a kind of fast-growing poplar according to claim 3 slurry biochemical process ECF bleaching process is characterized in that: described zytase X 1, X 2Or X 3The concrete technology condition of processing is as follows: dextranase X 1Process conditions be: enzyme dosage 10IU/L, temperature 50 C, pH8-9, time 90-120min; Zytase X 2Process conditions be: enzyme dosage 8IU/g, 55 ℃ of temperature, pH8-9, time 90-120min; Zytase X 3Process conditions be: enzyme dosage 10IU/g, temperature 50 C, pH8-9, time 120min.
5. the NaOH anthraquinone of a kind of fast-growing poplar according to claim 1 is starched biochemical process ECF bleaching process, it is characterized in that: the concrete mode of described ODQP bleaching process is: Oxygen Delignification of Fast-Growing is: starch dense 10%, NaOH consumption 2.5%, oxygen is pressed 0.6MPa, 100 ℃ of temperature, time 80min, MgSO 4Consumption 0.5%; D section: ClO 2Consumption is 0.6%, original ph 5, temperature 70 C, starch dense 10%, time 120min; The Q section: starch dense 8%, DTPA consumption 0.5%, temperature 70 C, time 60min, pH value 4-5; P section: H 2O 2Consumption is 3%, Na 2SiO 3Consumption 0.7%, MgSO 4Consumption 0.5%, original ph 12,90 ℃ of temperature, starch dense 10%, time 90min.
6. the NaOH anthraquinone of a kind of fast-growing poplar according to claim 1 slurry biochemical process ECF bleaching process is characterized in that: described O PThe concrete mode of DQP bleaching process is: strengthening the Oxygen Delignification of Fast-Growing condition is: starch dense 10%, NaOH consumption 2.5%, oxygen is pressed 0.6MPa, 100 ℃ of temperature, MgSO 4Consumption 0.5%, Na 2SiO 3Consumption 0.7%, H 2O 2Consumption 3%, time 80min; D section: ClO 2Consumption is 0.4%, original ph 5, temperature 70 C, starch dense 10%, time 120min; The Q section: starch dense 8%, DTPA consumption 0.5%, temperature 70 C, time 60min, pH value 4-5; P section: H 2O 2Consumption is 2%, Na 2SiO 3Consumption 0.7%, MgSO 4Consumption 0.5%, original ph 12,90 ℃ of temperature, starch dense 10%, time 90min.
7. the NaOH anthraquinone of a kind of fast-growing poplar according to claim 1 slurry biochemical process ECF bleaching process is characterized in that: described O 1O 2PThe concrete mode of DQP bleaching process is: first paragraph O 1: starch dense 10%, NaOH consumption 2%, oxygen is pressed 0.6MPa, 100 ℃ of temperature, time 20min, MgSO 4Consumption 0.5%; Second segment O 2P: replenish 0.5% NaOH, add 3% H 2O 2, Na 2SiO 3Consumption 0.7%, oxygen is pressed 0.5MPa, time 60min; D section: ClO 2Consumption is 0.4%, original ph 5, temperature 70 C, starch dense 10%, time 120min; The Q section: starch dense 8%, DTPA consumption 0.5%, temperature 70 C, time 60min, pH value 4-5; P section: H 2O 2Consumption is 2%, Na 2SiO 3Consumption 0.7%, MgSO 4Consumption 0.5%, original ph 12,90 ℃ of temperature, starch dense 10%, time 90min.
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CN114277599A (en) * 2021-12-17 2022-04-05 广西大学 Low-temperature neutral chlorine dioxide bleaching method

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