CN1205375A - Method for bleaching medium thick paper pulp by for hydrogen peroxide for medium-small paper mill - Google Patents
Method for bleaching medium thick paper pulp by for hydrogen peroxide for medium-small paper mill Download PDFInfo
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- CN1205375A CN1205375A CN 98113209 CN98113209A CN1205375A CN 1205375 A CN1205375 A CN 1205375A CN 98113209 CN98113209 CN 98113209 CN 98113209 A CN98113209 A CN 98113209A CN 1205375 A CN1205375 A CN 1205375A
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- paper pulp
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- pulp
- hydrogen peroxide
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- 229920001131 Pulp (paper) Polymers 0.000 title claims abstract description 75
- 238000004061 bleaching Methods 0.000 title claims abstract description 55
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 title claims abstract description 38
- 238000000034 method Methods 0.000 title claims description 29
- 238000009897 hydrogen peroxide bleaching Methods 0.000 claims abstract description 16
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 12
- KCXVZYZYPLLWCC-UHFFFAOYSA-N EDTA Chemical compound OC(=O)CN(CC(O)=O)CCN(CC(O)=O)CC(O)=O KCXVZYZYPLLWCC-UHFFFAOYSA-N 0.000 claims abstract description 8
- 229960002163 hydrogen peroxide Drugs 0.000 claims description 17
- 238000005406 washing Methods 0.000 claims description 17
- 239000000463 material Substances 0.000 claims description 14
- 239000002002 slurry Substances 0.000 claims description 13
- 239000002562 thickening agent Substances 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 9
- 239000000126 substance Substances 0.000 claims description 8
- 238000010297 mechanical methods and process Methods 0.000 claims description 5
- 238000004537 pulping Methods 0.000 claims description 5
- 230000035484 reaction time Effects 0.000 claims description 4
- 239000010893 paper waste Substances 0.000 claims description 2
- MMBMIVSDYYPRHH-UHFFFAOYSA-N hydrogen peroxide Chemical compound OO.OO MMBMIVSDYYPRHH-UHFFFAOYSA-N 0.000 claims 1
- 239000002351 wastewater Substances 0.000 abstract description 9
- CSNNHWWHGAXBCP-UHFFFAOYSA-L Magnesium sulfate Chemical compound [Mg+2].[O-][S+2]([O-])([O-])[O-] CSNNHWWHGAXBCP-UHFFFAOYSA-L 0.000 abstract 2
- 238000007865 diluting Methods 0.000 abstract 1
- 238000007599 discharging Methods 0.000 abstract 1
- 229910052943 magnesium sulfate Inorganic materials 0.000 abstract 1
- 235000019341 magnesium sulphate Nutrition 0.000 abstract 1
- 235000019795 sodium metasilicate Nutrition 0.000 abstract 1
- 229910052911 sodium silicate Inorganic materials 0.000 abstract 1
- 241000196324 Embryophyta Species 0.000 description 8
- 238000004076 pulp bleaching Methods 0.000 description 6
- 244000025254 Cannabis sativa Species 0.000 description 5
- 239000000835 fiber Substances 0.000 description 5
- 239000002761 deinking Substances 0.000 description 4
- 238000005265 energy consumption Methods 0.000 description 4
- 238000010790 dilution Methods 0.000 description 3
- 239000012895 dilution Substances 0.000 description 3
- 239000003245 coal Substances 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- WQYVRQLZKVEZGA-UHFFFAOYSA-N hypochlorite Chemical compound Cl[O-] WQYVRQLZKVEZGA-UHFFFAOYSA-N 0.000 description 2
- 231100000252 nontoxic Toxicity 0.000 description 2
- 230000003000 nontoxic effect Effects 0.000 description 2
- 241000202567 Fatsia japonica Species 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 229960004601 aliskiren Drugs 0.000 description 1
- KLRSDBSKUSSCGU-KRQUFFFQSA-N aliskiren fumarate Chemical compound OC(=O)\C=C\C(O)=O.COCCCOC1=CC(C[C@@H](C[C@H](N)[C@@H](O)C[C@@H](C(C)C)C(=O)NCC(C)(C)C(N)=O)C(C)C)=CC=C1OC.COCCCOC1=CC(C[C@@H](C[C@H](N)[C@@H](O)C[C@@H](C(C)C)C(=O)NCC(C)(C)C(N)=O)C(C)C)=CC=C1OC KLRSDBSKUSSCGU-KRQUFFFQSA-N 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 239000007844 bleaching agent Substances 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 238000011109 contamination Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000011143 downstream manufacturing Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000013467 fragmentation Methods 0.000 description 1
- 238000006062 fragmentation reaction Methods 0.000 description 1
- 230000008676 import Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 230000002035 prolonged effect Effects 0.000 description 1
- 238000009418 renovation Methods 0.000 description 1
- 239000010902 straw Substances 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Landscapes
- Paper (AREA)
Abstract
A hydrogen peroxide bleaching method for middle-concentration paper pulp in middle-scale or small paper mill NaOH (1-2 wt.%), Na2SiO3 (2-4), EDTA (0.2-0.4), MgSO4 (0-0.4) and hydrogen peroxide (1.5-2.5) to paper pulp (12-17% in concentration), fully mixing through pulp pump and mixer, bleaching in downflow bleaching tower at 65-90 deg.C for 90-120 min, diluting to 4-6 wt.% of concentration at tower bottom and discharging the bleached pulp with centrifugal pump. The whiteness of pulp is increased by 10-20% GE. Its drained waste water does not pollute environment.
Description
The present invention relates to the dioxde pulp bleaching process of pulp and paper industry.More particularly relate to the method for bleaching that not only is applicable to careless class paper pulp but also is applicable to the hydrogen peroxide of wooden class paper pulp and deinking paper pulp.
China's 20～100 tons of association with pulp bleaching of existing daily output mainly are to utilize chlorination bleaching and hypochlorite bleaching method, and the wastewater toxicity that this method is discharged is very big, and wastewater flow rate is many, thereby makes pulp and paper industry have three big problems:
(1) serious environment pollution makes pulp and paper industry become one of three the most serious big industries of China's environmental pollution;
(2) severe contamination pulping and papermaking equipments, thus need equipment and materials is proposed too high requirement, damage otherwise will speed up ageing equipment;
(3) have a strong impact on the healthy of operator.
Though in the external prior art middle concentration paper pulp hydrogen peroxide bleaching method is arranged, but there is the limitation of all many-sides in this method, at first it only is applicable to wood type paper pulp, be not suitable for careless class paper pulp, this is because grass fiber is shorter than wood pulp fibre, fibre strength is lower, and careless class paper pulp the ash content of coal height, thereby has increased the difficulty of bleaching.So the middle concentration paper pulp hydrogen peroxide bleaching method of wood pulp can not be indiscriminately imitated the middle concentration paper pulp hydrogen peroxide bleaching method that is used for straw pulp.Secondly this method only is applicable to the large and medium-sized factory of daily output more than 150 tons, and the most of paper mill of China is the medium and small factory of daily output below 100 tons as direct introducing equipment expense costliness, energy consumption height, thereby to be not suitable for China's national situation.
The objective of the invention is to overcome the deficiencies in the prior art part, provide that a kind of operating flexibility is big, cost of equipment is relative with energy consumption low, can be widely used in careless class paper pulp, wooden class paper pulp and deinking paper pulp, the hydrogen peroxide bleaching method of concentration grass class paper pulp in being particularly suitable for.This method will make discharge waste water reach environmental requirement, and is pollution-free to paper pulp papermaking equipment, do not influence the healthy of workman.
For being fit to China's national situation, concentration paper pulp hydrogen peroxide bleaching method during the present invention studies emphatically and produces 20～100 tons daily.
The objective of the invention is to realize by the following method:
The middle concentration paper pulp hydrogen peroxide bleaching method of 20～100 tons of oven dry stocks of daily output of the present invention comprises the steps and process conditions:
Following % content is all by oven dry stock weight
(1) washing concentrating
With the low-consistency stock of 3～6% (weight), by being pumped into thickener, the pulp density after washing concentrating is brought up to 12～17% (weight), falls in the defeated material spiral that is installed on the thickener bottom;
(2) add bleaching assistant
With consumption is the NaoH of 1～2% (weight), the EDTA of 0.2～0.4% (weight), the Na of 2～4% (weight)
2SiO
3And the MgSO of 0～0.4% (weight)
4Add in the defeated material spiral, being transported to the range of speeds with paper pulp is 200～400 rev/mins mixing screw, feeding steam pressure in mixing the process of carrying is that 0.4～0.6Mpa, temperature are 110～120 ℃ low-pressure steam, make temperature of charge reach 65～90 ℃, concentration remains in 10～14% (weight) scope, through the range of speeds be 1500～2500 rev/mins middle underflow pump send into the range of speeds be 950～1460 rev/mins in dense blender, the outlet pressure of middle underflow pump is 0.3～0.6Mpa;
(3) paper pulp mixes with hydrogen peroxide
Hydrogen peroxide inlet before the therefrom dense blender feeds the hydrogenperoxide steam generator of pressure a little more than the middle underflow pump outlet pressure, use amount is 1.5～2.5% (weight), in fully mix with paper pulp in the dense blender, mixture homogeneity reaches 94%, enter then and fall the stream bleaching tower, this moment, the paper pulp temperature still remained in 65～90 ℃ of scopes, and pulp density still remains in 10～14% (weight) scope;
(4) bleaching
Entering the paper pulp that falls the stream bleaching tower bleaches in bleaching tower, 65～90 ℃ of bleaching tower temperature, pressure is normal pressure, the material stop reaction time must guarantee 90～120 minutes in bleaching tower, at the bottom of tower, paper pulp is diluted to 4～6% (weight), pump to rinsing maching by centrifugal low-consistency, after washing, get bleached pulp.
The used equipment component of said method adapts to the whole system operation to reach the purpose that satisfies technological requirement and cut down the consumption of energy by the Frequency Converter Control range of speeds.This law branch multistage that can combine with other method for bleaching is connected into whole bleaching system, can obtain being applicable to producing cultural paper, paper for daily use, industrial or agricultural with needed bleached pulps such as paper.
The equipment that the present invention uses can be commercially available, also can self design.
The present invention compared with prior art has following advantage:
(1) this law solved short because of grass fiber, intensity is low and the high bleaching process that brings of the ash content of coal on technical barrier, make this law operating flexibility big, applied widely, both go for careless class Mechanical Method slurry, careless class chemical method slurry, also gone for the hydrogen peroxide bleaching of wooden class chemical method slurry, wooden class Mechanical Method slurry and deinking paper pulp; The whiteness increment 10%GE～20%GE of paper pulp before the paper pulp contrast of adopting this law to produce is not bleached.
(2) this process route tallies with the national condition, and meets the medium and small factory of China and uses, and 50% of this law device therefor can be saved equipment investment greatly by former bleaching process all devices renovation and utilization.Compare with similar factory introducing equipment, cost of equipment reduces more than 50～80%.
(3) this law device therefor energy consumption only is 60～80% of the same category of device energy consumption introduced.
(4) waste water that the association with pulp bleaching of paper industry is discharged meets state specified standards, and environment is not brought pollution.
(5) equipment in association with pulp bleaching workshop and the equipment of downstream process workshop section are not produced any pollution, so just prolonged the service life of equipment, reduced the running cost of pulping and paper-making factory.
(6) make the discharge waste water environmental pollution degree of pulping and paper-making factory reduce half, make pulp and paper industry stride forward major step to clean industry.
(7), thereby operator's healthy nothing is influenced because bleaching agent and bleaching assistant are nontoxic, and bleaching effluent is also nontoxic.
(8) owing to operating system automation and serialization degree height, thereby make association with pulp bleaching quality height, more can not damage quality of fibre in the paper pulp.
Below by embodiment the present invention is further described below.
Embodiment 1
Produce 20 tons wooden class Mechanical Method middle concentration paper pulp hydrogen peroxide bleaching method daily, its step and process conditions are as follows:
(1) washing concentrating:
With stock pump the low-consistency stock of concentration 3% (weight), whiteness 35%GE is sent into washing thickener, the pulp density after washing concentrating is brought up to 16% (weight), and 30 ℃ of temperature are fallen into fragmentation, the mixing of rinsing maching bottom and failed in the material spiral;
(2) add NaOH, Na
2SiO
3, MgSO
4Reach bleaching assistants such as EDTA:
The NaoH that in defeated material spiral, adds 2% (weight), the MgSO of 0.2% (weight)
4, the Na of the EDTA of 0.4% (weight) and 2% (weight)
2SiO
3Being transported to rotating speed with paper pulp is 200 rev/mins mixing screw, in the process of mix carrying, feed the low-pressure steam of 110 ℃ of pressure 0.4Mpa, temperature simultaneously, make temperature of charge reach 65 ℃, to be admitted to by Frequency Converter Control, rotating speed be 2500 rev/mins middle underflow pump to paper pulp then, the input mixing screw through middle underflow pump send into rotating speed be 1460 rev/mins in dense blender, the input mixing screw steam heat be 3.5 * 10
5(kilocalorie/hour), this moment, pulp density was 14% (weight);
(3) paper pulp mixes with hydrogen peroxide:
Paper pulp is dense blender during the middle underflow pump of 0.5MPa enters through outlet pressure, import hydrogen peroxide bleaching and steam simultaneously a little more than 0.5Mpa pressure, the hydrogen peroxide input quantity is 1.5～2.5% (weight), the paper pulp temperature reaches 85 ℃～90 ℃, concentration still keeps 14% (weight), and hydrogen peroxide and paper pulp mixture homogeneity reach 94%;
(4) bleaching:
Paper pulp falls the stream bleaching tower with entering after hydrogen peroxide mixes.After paper pulp entered bleaching tower, the time of staying was 90 minutes, and the tower internal pressure is a normal pressure, 85 ℃～90 ℃ of temperature, and the bleaching tower lower end is provided with the dilution runner, is the paper pulp dilution 4% (weight), pumps rinsing maching by centrifugal low-consistency.The flowing time of paper pulp at the bottom of from the bleaching tower top to tower is exactly the reaction time, is 90 minutes.Therefore, the definite of the height of tower and diameter must satisfy association with pulp bleaching stop reaction time and permissible velocity of flow value, and present embodiment is tower height 10m, and diameter is 1.7m, and paper pulp just becomes bleached pulp after washing, and whiteness reaches 50%GE.BOD in the waste water is discharged in the bleaching back
5Be 100mg/L, COD
CrBe 200mg/L, be lower than national grade ii standard.
The capital equipment that present embodiment is selected for use is as follows:
The rinsing maching that step 4 is used all adopts model to be ZHK
4Suction washer, Anyang machinery plant of the light machine parent company of China product; The thickener that step 1 is used is SLX20 inclined screw press master, and SPP20 defeated material screw machine and SMP20 mixing screw are Fujian Machinery Plant of Light Industry and make; Turbulence type middle underflow pump ZBJ31-20, the light machine in Tianjin factory makes; Dense blender in the ZH-8 type, South China Science ﹠ Engineering University makes; MPB-20 slurry stream bleaching tower, Fujian Machinery Plant of Light Industry makes.
Embodiment 2
The hydrogen peroxide bleaching method of 100 tons of deinking paper pulp of daily output, its step and process conditions are as follows:
(1) washing concentrating;
The low dense pulp from decoloured waste paper of concentration 6% (weight) is by being pumped into thickener, and the pulp density after washing concentrating reaches 12% (weight), 30 ℃ of temperature, and whiteness 45%GE falls in the defeated material spiral of thickener bottom;
(2) add NaoH, Na
2SiO
3, MgSO
4Reach bleaching assistants such as EDTA;
The NaoH that adds 1% (weight), the Na of the EDTA of 0.2% (weight) and 4% (weight)
2SiO
3Add in the defeated material spiral, sending into rotating speed with paper pulp is 300 rev/mins mixing screw, and in mixing screw, feed pressure 0.5Mpa, the low-pressure steam that temperature is 120 ℃, make temperature of charge reach 90 ℃, paper pulp is dense blender during 2000 rev/mins middle underflow pump is sent into by high frequency device control rotating speed then, and the vapour heat that adds mixing screw is 20 * 10
5(kilocalorie/hour), this moment, pulp density was reduced to 10% (weight);
(3) paper pulp mixes with hydrogen peroxide:
Paper pulp through outlet pressure be the middle underflow pump of 0.6Mpa enter rotating speed be 1150 rev/mins in dense blender, in hydrogen peroxide inlet before the dense blender feed the hydrogen peroxide of 2.5% (weight), hydrogen peroxide mixes with paper pulp, and mixture homogeneity reached 94%, temperature keeps 90 ℃ paper pulp to be admitted to falling the stream bleaching tower;
(4) bleaching:
The temperature of falling in the stream bleaching tower is 90 ℃, and pressure is normal pressure, and concentration still keeps 10% (weight), and the time of paper pulp from overhead streams to the dilution zone, bottom is exactly bleaching time, promptly 120 minutes.The bleaching tower height of present embodiment is 16m, and diameter is 2.5m.Paper pulp is diluted as concentration 4% (weight) at the bottom of tower, pump to wash engine by stock pump and wash.Paper pulp contrast after the washing not whiteness increment of the preceding paper pulp of bleaching is 12%GE, and whiteness reaches 57%GE, BoD in the bleaching back discharge waste water
5Be 100mg/L, COD
CrBe 200mg/L, be lower than national grade ii standard.
The capital equipment that present embodiment is selected for use is as follows:
The rinsing maching model that step 4 is used is the ZNK10 vacuum pulp washing machine, and Anyang Machinery Plant of Light Industry makes; Conveyor screw machine SPP100 and mixing screw SMP100, and the thickener that step 1 is used is the manufacturing of the light machinery plant in Fujian as inclined screw press master SLX100; Turbulence type middle underflow pump ZBJ31-100, the light machine in Tianjin factory makes; In dense blender ZH-10, South China Science ﹠ Engineering University makes; The bleaching tower model is MPB100, and the light machine in Fujian factory makes.
Embodiment 3
Produce concentration grass class paper pulp hydrogen peroxide bleaching method in 50 tons of chemical methods daily, its step and process are as follows:
(1) washing concentrating:
The low dense chemical method grass class paper pulp of concentration 4% (weight) is by being pumped into thickener, and the pulp density after washing concentrating reaches 14% (weight), 32 ℃ of temperature, and whiteness 34%GE falls in the defeated material spiral of pulp thickener bottom;
(2) add bleaching assistant:
The NaoH that in defeated material spiral, adds 1.5% (weight), the EDTA of 0.3% (weight), the Na of 3% (weight)
2SiO
3And the MgSO of 0.3% (weight)
4, sending into rotating speed with paper pulp is in 400 rev/mins the mixing screw, and feeding pressure in mixing screw is 0.4Mpa, and temperature is 110 ℃ a low-pressure steam, and temperature of charge reaches 80 ℃ after mixing.The heat that adds mixing screw is 10 * 10
5(kilocalorie/hour), this moment, pulp density was reduced to 12% (weight), dense blender in middle underflow pump is sent into;
(3) paper pulp mixes with hydrogen peroxide:
Mix back paper pulp with bleaching assistant and send into middle underflow pump, and by rotating speed be 1500 rev/mins middle underflow pump pump to rotating speed be 950 rev/mins in dense blender, the middle underflow pump outlet pressure is 0.5Mpa, the hydrogen peroxide of dense blender in the feeding, input quantity is 2% (weight), the mixture homogeneity of hydrogen peroxide and paper pulp is reached 94%, and the paper pulp that the temperature maintenance is 80 ℃ is admitted to and falls stream bleaching pipe;
(4) bleaching:
Paper pulp enters slurry stream bleaching tower from the bleaching tower top, temperature is 80 ℃ in the slurry stream bleaching tower, pressure is normal pressure, pulp density still keeps 12% (weight), and bleaching time is 100 minutes, tower height 14m, diameter is 2.0m, paper pulp is diluted as 5% (weight) concentration at the bottom of tower, pump to rinsing maching by low-consistency and wash, and just becomes bleached pulp.
The paper pulp contrast of washing back is the pulp brightness 16%GE that rised in value before the bleaching, reaches 50%GE.Bleaching process is discharged BoD in the waste water
5Be 10mg/L, CoD
CrBe 200mg/L, be lower than national grade ii standard.
The capital equipment that present embodiment is selected for use is:
Step 1 and 4 two suction washer ZNKZ that use
10, Anyang Machinery Plant of Light Industry makes; Conveyor screw machine SPP50 and mixing screw SMP50 are Fujian Machinery Plant of Light Industry and make; Turbulence type middle underflow pump ZBJ31-50, Tianjin Machinery Plant of Light Industry makes; In dense blender AHLMIX-50, South China Science ﹠ Engineering University makes; Bleaching tower MPB-50, the light machine in Fujian factory makes.
Claims (3)
1, the middle concentration paper pulp hydrogen peroxide bleaching method of 20～100 tons of oven dry stocks of daily output is characterized in that comprising the steps and process conditions:
Following % content is all by oven dry stock weight
(1) washing concentrating
With the low-consistency stock of 3～6% (weight), by being pumped into thickener, the pulp density after washing concentrating is brought up to 12～17% (weight), falls in the defeated material spiral that is installed on the thickener bottom;
(2) add bleaching assistant
With consumption the Na of EDTA, 2～4% (weight) of the NaoH, 0.2～0.4% (weight) of 1～2% (weight)
2SiO
3And the MgSO of 0～0.4% (weight)
4Add in the defeated material spiral, be transported to mixing screw with paper pulp, feeding steam pressure in mixing the process of carrying is that 0.4～0.6Mpa, temperature are 110～120 ℃ low-pressure steam, make temperature of charge reach 65～90 ℃, concentration remains in 10～14% (weight) scope, dense blender in middle underflow pump is sent into, the outlet pressure of middle underflow pump are 0.3～0.6Mpa;
(3) paper pulp mixes with hydrogen peroxide
Hydrogen peroxide inlet before the therefrom dense blender feeds the hydrogenperoxide steam generator of pressure a little more than middle underflow outlet pressure, the hydrogen peroxide use amount is 1.5～2.5% (weight), in fully mix with paper pulp in the dense blender, mixture homogeneity reaches 94%, enter then and fall the stream bleaching tower, this moment, the paper pulp temperature still remained in 65～90 ℃ of scopes, and pulp density still remains in 10～14% (weight) scope;
(4) bleaching
Entering the paper pulp that falls the stream bleaching tower bleaches in bleaching tower, 65～90 ℃ of bleaching tower temperature, pressure is normal pressure, the material stop reaction time is 90～120 minutes in bleaching tower, at the bottom of tower, paper pulp is diluted to 4～6% (weight), pump to rinsing maching by centrifugal low-consistency, after washing, get bleached pulp.
2,20～100 tons of middle concentration paper pulp hydrogen peroxide bleaching methods of daily output according to claim 1 is characterized in that the paper pulp of being bleached can be careless class Mechanical Method slurry, careless class chemical method slurry, careless class chemical mechanical pulping slurry, wooden class Mechanical Method slurry, wooden class chemical method slurry, wooden class chemical mechanical pulping slurry and pulp from decoloured waste paper.
3, according to concentration paper pulp hydrogen peroxide bleaching method in 20～100 tons of the claims 1,2 described daily outputs, it is characterized in that mixing screw, middle underflow pump and in equipment such as dense blender by frequency converter timing, wherein the range of speeds of mixing screw is 200～400 rev/mins; The range of speeds of middle underflow pump is 1500～2500 rev/mins; In the dense blender range of speeds be 950～1460 rev/mins.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN98113209A CN1107140C (en) | 1998-05-14 | 1998-05-14 | Method for bleaching medium thick paper pulp by for hydrogen peroxide for medium-small paper mill |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN98113209A CN1107140C (en) | 1998-05-14 | 1998-05-14 | Method for bleaching medium thick paper pulp by for hydrogen peroxide for medium-small paper mill |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1205375A true CN1205375A (en) | 1999-01-20 |
| CN1107140C CN1107140C (en) | 2003-04-30 |
Family
ID=5222967
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN98113209A Expired - Fee Related CN1107140C (en) | 1998-05-14 | 1998-05-14 | Method for bleaching medium thick paper pulp by for hydrogen peroxide for medium-small paper mill |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1107140C (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102677536A (en) * | 2012-05-15 | 2012-09-19 | 山东轻工业学院 | Modifying agent used for improving properties of tissue paper manufactured with poplar chemical pulp and modification method |
| CN104389223A (en) * | 2014-10-10 | 2015-03-04 | 天津科技大学 | Use method of novel chelating agent in hydrogen peroxide bleaching of deinked pulp |
| CN106012627A (en) * | 2016-05-24 | 2016-10-12 | 中国林业科学研究院林产化学工业研究所 | Method for preparing high-brightness bleached mechanical pulp of bamboo by utilizing alcohol solvent |
| CN110747682A (en) * | 2019-10-08 | 2020-02-04 | 中国宣纸股份有限公司 | Chlorine-free bleaching method for rice paper straw pulp |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100412267C (en) * | 2006-04-30 | 2008-08-20 | 华南理工大学 | A double-tower hydrogen peroxide bleaching method for medium-consistency pulp |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR2712313B1 (en) * | 1993-11-10 | 1995-12-15 | Atochem Elf Sa | Process for bleaching a high-yield paper pulp with hydrogen peroxide. |
| CN1154729A (en) * | 1994-07-11 | 1997-07-16 | 贝洛特工艺技术公司 | Method for bleaching wood pulp using hydrogen peroxide |
| CN1050642C (en) * | 1996-06-25 | 2000-03-22 | 华南理工大学 | Everyday production 30-150 ton high concentration paper pulp bleaching method by using hydrogen peroxide |
-
1998
- 1998-05-14 CN CN98113209A patent/CN1107140C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102677536A (en) * | 2012-05-15 | 2012-09-19 | 山东轻工业学院 | Modifying agent used for improving properties of tissue paper manufactured with poplar chemical pulp and modification method |
| CN104389223A (en) * | 2014-10-10 | 2015-03-04 | 天津科技大学 | Use method of novel chelating agent in hydrogen peroxide bleaching of deinked pulp |
| CN106012627A (en) * | 2016-05-24 | 2016-10-12 | 中国林业科学研究院林产化学工业研究所 | Method for preparing high-brightness bleached mechanical pulp of bamboo by utilizing alcohol solvent |
| CN106012627B (en) * | 2016-05-24 | 2018-05-04 | 中国林业科学研究院林产化学工业研究所 | A kind of method that bamboo wood High brightenss bleach reducing rules are prepared using alcohols solvent |
| CN110747682A (en) * | 2019-10-08 | 2020-02-04 | 中国宣纸股份有限公司 | Chlorine-free bleaching method for rice paper straw pulp |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1107140C (en) | 2003-04-30 |
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