CN101691709B - Natural-color straw pulp with improved freeness, air permeability and tensile index, and stable performance - Google Patents
Natural-color straw pulp with improved freeness, air permeability and tensile index, and stable performance Download PDFInfo
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Abstract
The invention relates to natural-color straw pulp with improved freeness, air permeability and tensile index, and stable performance, in particular to natural-color straw pulp and application thereof in mixed pulp and paper products. The straw pulp has the advantages that: color phase or whiteness of the straw pulp is remarkably improved; the bulk and freeness are high; and the acquired data of the sizing agent of the natural-color straw pulp is more stable because of small quality fluctuation of sizing agent.
Description
Technical field
What the present invention relates to is a kind of freedom, air permeability and the tensile index of improvement and the natural-color straw pulp of stable performance, and concretely, what the present invention relates to is a kind of described natural-color straw pulp, and their application in mixed pulp, paper products.
Background technology
In the daily life, paper can be divided into cultural paper, industrial paper, paper for daily use and the special paper of using according to purposes, and wherein cultural paper can be divided into uncoated paper and coated paper simply.Paper without coating processing is referred to as uncoated paper, as newsprint, offset paper, electro-photographic paper and writing paper etc.; Paper through coating processing is referred to as coated paper, as art paper, wall calendar paper, inferior machine-glazed paper, glass paperboard etc.Their manufacturing comprises following several links: the slurrying section: material choice → boiling defibre → washing → bleaching → washing and screening → concentrate or copy into lodicule → store for future use;
Copy the paper section: the stream of the mixing → paper stock of the slurry → removal of impurity of loosing → refining → various additive → paper stocks of pulling an oar → prepare send → case → wet end → press section → drying section → top sizing → drying → press polish → coil into paper;
Coating section: the volume → supercalendering of bodystock paper → coating machine coating → drying → batch → again;
Processing sections: rewinding → cutting flat board (or reel) → sorted and packaged → warehouse-in finishes;
What the present invention related generally to is pulping process and the paper pulp that makes, and existing pulping process comprises chemistry, machinery or both combinations, and the mode that is preferred for slurrying of the present invention is the combination of chemistry, machinery pulping mode.
In the prior art, paper pulp is divided into wood pulp and straw pulp usually, and described wood pulp is meant softwood pulp (as masson pine, larch, Korean pine, dragon spruce etc.) and hardwood pulp (as birch, poplar, linden, Eucalyptus, maple etc.).Described straw pulp is meant standing grain section fiber pulp (as straw, wheat straw, reed, bamboo, bagasse etc.), bast fiber slurry (as hemp, bluish dogbane, flax, mulberry skin, cotton stalk bark etc.) and seed hair fiber slurry (as cotton fiber etc.).
Prior art thinks that later paper pulp is separated, washs, screens and bleached to boiling or machinery mill, can't directly be used for copying paper.In order to satisfy the different serviceabilities of paper, also need be in the preparation process of paper, in paper pulp or preparation process, add various auxiliary agents or auxiliary material, described auxiliary agent or auxiliary material comprise filler, sizing material, colorant and other chemical assistants, in printing, add the printability that filler can improve paper, as increasing paper of whiteness, smoothness, opacity, deflection, simultaneously, can improve affinity, pliability and the stability of paper, thereby help the raising of print quality printing ink.
But, paper pulp is basic to the influence of paper, in the prior art, the general every physical index that adopts bleached pulp or mixed pulp is estimated the various performances of paper, and stable by a period of time is fixed up the relation of paper pulp and paper, this production for paper pulp is useful, specific to straw pulp, it is very big that the physical and chemical index of straw pulp is subject to processing condition effect, for example:
At open source literature, the multiple factor that influences paper performance is disclosed in the literary composition that " influences the factor of paper physical property ", wherein relate to processing technology to the factor of paper because not in discussion scope of the present invention, factor is omitted at this, what be introduced in the present invention is the influence of beating degree to paper physical property, can learn from the document, the fracture length of paper the initial beating-up period rise very fast, gradually slowly get off later on, produce decline on the contrary after having arrived certain numerical value, folding strength, bursting strength, tearability also are like this; The air permeability of paper reduces along with the increase of beating degree; Making beating can reduce whiteness, and the low more whiteness of freedom is just fallen, and the high more whiteness of freedom also increases.
Usually, the paper pulp that those skilled in the art will make through methods such as chemical method or Mechanical Method is called natural color pulp, and described natural color pulp is generally yellow or brown.Prior art is thought, satisfy the instructions for use of paper, must bleach processing to paper pulp, makes paper have higher whiteness.Bleached pulp method commonly used has two kinds: a kind of is oxidative bleaching method, and another kind is the reducing bleach method, slurry can not be floated to the whiteness of appointment when a kind of method of use in the bleaching practice, can also adopt multiple method for bleaching, that is, multistage bleaching, as three sections float, five sections float etc.But bleaching changes the physical and chemical parameter of paper pulp, referring to accompanying drawing 11, causes prepared paper pulp can't carry out the contrast of stable physical and chemical parameter.
The characteristic of Straw Pulp points out the influence (2000.4. gansu science and technology .17) that becomes paper character with water retention value, and straw pulp in use generally need not be pulled an oar or light beating gets final product.In conjunction with the open source literature of aforesaid prior art, making beating also is tangible to the influence of the physical and chemical parameter of paper pulp.
(free freeness) can be used for representing the degree of dehydration of Paper material on diddle-net to freedom, and high freedom shows that drainability is good, is fit to high-speed paper machine and uses, and the principal element that influences this index comprises kinds of fibers, fibre property, making beating degree or state etc.Beating degree is meant the fibre length after the making beating, and the big more then fiber of the long more beating degree value of beating time is short more. the beating degree measuring method is the slurry of accomplishing fluently to be put into the container of a band funnel, and the capacity of the water that leaks down is big more, shows that then fiber is short more, and beating degree is high more.
Air permeability is meant the page venting capability, paper machine speed when this index can influence the detersive efficiency of slurry and copy paper, and high air permeability can effectively improve the slurry washing effect, reduces pollutant emission; Described straw pulp is also applicable to high-speed paper machine." papermaking straw pulp applied research " (" International Paper ", the 13rd the 5th phase of volume of October in 1994: point out that 23-25) air permeability and the bulk of Straw Pulp are lower, opacity is relatively poor, and drainability is poor.Fiber is elongated, and the paper tightness of copying is bigger, and the space is less, and general bulk of paper and air permeability are all relatively poor (referring to " fibre detaching apparatus with high shearing is to the influence of bleached wheat straw pulp physical property ".
In sum, straw pulp has shortcomings such as air permeability, freedom and tensile index are lower, the stock quality fluctuation is big; Simultaneously, bleaching and making beating have tangible influence to the physicochemical property of straw pulp, cause straw pulp can't have stable performance.In view of this, special proposition the present invention.
Summary of the invention
Main purpose of the present invention is to provide a kind of air permeability, tensile index and the freedom of improvement and the natural-color straw pulp of stable performance;
Another object of the present invention is to provide the application of a kind of described straw pulp in mixed pulp;
Another object of the present invention is to provide the application of a kind of described straw pulp in paper products.
In order clearly to define the difference between prior art and the present invention, the present invention is made to give a definition, promptly, natural-color straw pulp of the present invention is meant, only be meant, the paper pulp that adopts straw, wheat straw, reed, giantreed, bagasse, cotton stalk and their mixture to make as raw material comprises the slurry that obtains after boiling, shove, the washing; Perhaps boiling, shove, wash and discongest the slurry that obtains; Perhaps boiling, shove, wash, discongest the slurry that obtains with oxygen delignification.
Natural-color straw pulp of the present invention is meant, only is meant, the paper pulp that preferably adopts straw, wheat straw, reed and their mixture to make as raw material comprises the slurry that obtains after boiling, shove, the washing; Perhaps boiling, shove, wash and discongest the slurry that obtains; Perhaps boiling, shove, wash, discongest the slurry that obtains with oxygen delignification.
Purpose of the present invention can be achieved in the following manner:
Be applicable to that preferably pulping process of the present invention comprises boiling, shove, washs, discongests and oxygen delignification.Be applicable to that boiling method of the present invention comprises any in ammonium sulfite boiling, anthraquinone-soda cooking, kraft cooking or the boiling of alkaline sodium sulfite method.
Concrete, if adopt the concrete parameter of boiling in batch (-type) spherical boiler or the continuous steamer as follows:
When adopting the ammonium sulfite boiling, add cooking liquor in the grass kind plant raw material, wherein the ammonium sulfite consumption is the 9-13% to the over dry material quantity, and liquor ratio is 1: 2-4.Feed the Steam Heating temperature to 165-173 ℃, then little venting, insulation, omnidistance time 160-210 minute.
When adopting anthraquinone-soda cooking, in the grass kind plant raw material, add cooking liquor, wherein alkali charge in NaOH to over dry material quantity 9-15%, liquor ratio is 1: 2-4, the anthraquinone addition is the 0.5-0.8 ‰ of over dry material quantity.Feed Steam Heating and be warming up to 160-165 ℃, then little venting, insulation, omnidistance time 140-190 minute.
When adopting kraft cooking, in the grass kind plant raw material, add cooking liquor, wherein alkali charge be the NaOH meter to over dry material quantity 8-11%, liquor ratio is 1: 2-4, sulphidity are 5-8%.Feed Steam Heating and be warming up to 165-173 ℃, then little venting, insulation, omnidistance time 150-200 minute.
When adopting the boiling of alkaline sodium sulfite method, add steaming preparation in the dogstail raw material, wherein sodium hydroxide concentration is counted 11-15% with the over dry raw material weight, and the sodium sulfite consumption is the 2-6% of over dry raw material weight, the consumption of anthraquinone is the 0.02-0.08% of over dry raw material weight, and the cooking liquor ratio is 1: 3-4.Feed Steam Heating then and be warming up to 160-165 ℃, then little venting, insulation, omnidistance time 140-190 minute.
Concrete, if adopt the concrete parameter of vertical digester boiling as follows:
When adopting the ammonium sulfite boiling, add cooking liquor in the grass kind plant raw material, wherein the ammonium sulfite consumption is the 9-15% to the over dry material quantity, and liquor ratio is 1: 6-10.Described grass kind plant raw material is packed in the digester by packer by hot black liquor, after the dress pot is full, close pot cover, replenishing temperature in the digester is 130-145 ℃ of steaming preparation, discharge the air in the pot simultaneously and boost to 0.6-0.75MPa, cooking liquor is warming up to 156-173 ℃, heats up, is incubated and be replaced into 220 minutes; Put with pump at last slurry is delivered to spraying pot.
When adopting anthraquinone-soda cooking, in the grass kind plant raw material, add cooking liquor, wherein alkali charge in NaOH to over dry material quantity 9-17%, liquor ratio is 1: 6-10, the anthraquinone addition is the 0.5-0.8 ‰ of over dry material quantity.Described grass kind plant raw material is packed in the digester by packer by hot black liquor, after the dress pot is full, close pot cover, replenishing temperature in the digester is 130-145 ℃ of steaming preparation, discharge the air in the pot simultaneously and boost to 0.4-0.6MPa, cooking liquor is warming up to 147-165 ℃, heat up, be incubated and be replaced into 170-200 minute, put with pump at last slurry is delivered to spraying pot.
When adopting kraft cooking, in the grass kind plant raw material, add cooking liquor, wherein alkali charge be the NaOH meter to over dry material quantity 8-13%, liquor ratio is 1: 6-10, sulphidity are 5-9%.Described grass kind plant raw material is packed in the digester by packer by hot black liquor, after the dress pot is full, close pot cover, replenishing temperature in the digester is 130-145 ℃ of steaming preparation, discharge the air in the pot simultaneously and boost to 0.5-0.65MPa, cooking liquor is warming up to 155-168 ℃, heat up, be incubated and be replaced into 180-220 minute, put with pump at last slurry is delivered to spraying pot.
When adopting the boiling of alkaline sodium sulfite method, add steaming preparation in the dogstail raw material, wherein, sodium hydroxide concentration is counted 9-17% with the over dry raw material weight, and sodium sulfite is 4-8%, and anthraquinone is 0.04-0.08%, and the cooking liquor ratio is 1: 6-10.The dogstail raw material is packed in the digester by packer by hot black liquor, after the dress pot is full, close pot cover, replenishing temperature in the digester is 145 ℃ of steaming preparations, discharge the air in the pot simultaneously and boost to 0.45-0.6MPa, cooking liquor is warming up to 152-165 ℃, heat up, be incubated and be replaced into 180-220 minute, put with pump at last slurry is delivered to spraying pot.
The permanganate number 16-28 of the slurry that obtains after the above-mentioned boiling of process, beating degree is 10-24 ° of SR, belongs to high-hardness pulp; Permanganate number 16-23 preferably, beating degree is 10-24 ° of SR.
Through shove, slurry after washing, discongesting, change oxygen delignification over to, promptly, described high-hardness pulp is delivered to the oxygen delignification reaction tower, and add NaOH and oxygen carries out the oxygen delignification reaction, obtaining hardness is permanganate number 7-16K, preferred 8-15K, the more preferably slurry of 8-14K.Preferred oxygen delignification is the single hop oxygen delignification, uses an oxygen delignification reaction tower; Described high-hardness pulp is 90-100 ℃ in the temperature of this reaction tower import department, and pressure is 0.9-1.2MPa; The temperature in exit is 95-105 ℃, and pressure is 0.2-0.4MPa; Alkali charge is that the addition of oxygen is a 20-40kg slurry per ton in the 2-4% of NaOH to the oven dry stock amount in the described oxygen delignification; The reaction time of described high-hardness pulp in this reaction tower is 60-90 minute.
The straw pulp of described method preparation has freedom, air permeability and the tensile index of improvement, the air permeability 50-1200ml/min of described natural-color straw pulp; Tensile index 35-70N.m/g, freedom 505-350ml.The preferred 60-900ml/min of the air permeability of described natural-color straw pulp; The preferred 38-68N.m/g of tensile index, the preferred 485-375ml of freedom.The air permeability of described natural-color straw pulp is 70-800ml/min more preferably, and tensile index is 40-65N.m/g more preferably, and freedom 480-500 is 460-400ml more preferably.The whiteness of described natural-color straw pulp is 28-54%, preferred 32-50%, more preferably 33-45%.The hardness 7-16K of natural-color straw pulp, preferred 8-15K more preferably can add known paper making additive in the described natural-color straw pulp of 8-14K..
The invention has the advantages that:
1, air permeability is significantly improved;
2, tear index is higher;
3, freedom is higher;
4, stock quality fluctuation is little, the natural-color straw pulp that obtains therefrom the slurry data more stable.
Description of drawings
Below be description of drawings of the present invention, can better understand the present invention by the following description
Fig. 1 is the opacity comparative parameter of contrast with natural-color straw pulp and natural-color straw pulp of the present invention;
Fig. 2 is the bulk comparative parameter of contrast with natural-color straw pulp and natural-color straw pulp of the present invention;
Fig. 3 is the air permeability comparative parameter of contrast with natural-color straw pulp and natural-color straw pulp of the present invention;
Fig. 4 is the tensile index comparative parameter of contrast with natural-color straw pulp and natural-color straw pulp of the present invention;
Fig. 5 is the tear index comparative parameter of contrast with natural-color straw pulp and natural-color straw pulp of the present invention;
Fig. 6 is the folding strength comparative parameter of contrast with natural-color straw pulp and natural-color straw pulp of the present invention;
Fig. 7 is the freedom comparative parameter of contrast with natural-color straw pulp and natural-color straw pulp of the present invention;
Fig. 8 is the whiteness comparative parameter of contrast with bleaching straw pulp and natural-color straw pulp of the present invention;
Fig. 9 is the form and aspect comparative parameter of contrast with bleaching straw pulp and natural-color straw pulp of the present invention;
Figure 10 is the hardness comparative parameter of contrast with natural-color straw pulp and natural-color straw pulp of the present invention;
Figure 11 be prior art with the otherness of various parameters between the straw pulp of different modes bleaching and the natural-color straw pulp relatively.
The specific embodiment
Below be the specific embodiment of the present invention and comparative example, the description by following can better understand the present invention.
Experiment method
This experiment method is meant, data of Ce Dinging in the present invention, described natural-color straw pulp is meant, only be meant, the paper pulp that adopts straw, wheat straw, reed, giantreed, bagasse, cotton stalk and their mixture to make as raw material, preferably, described raw material is straw, wheat straw, reed, giantreed and their mixture.
Using this case applicant's technology in early stage, is in the slurrying section, carries out material choice → boiling defibre → washing according to above-mentioned definition; Resulting paper pulp is referred to as the contrast natural-color straw pulp in the present invention.Certainly, this case applicant's of the present invention technology in early stage can be thought the part of prior art.
Adopting technology of the present invention, also is in the slurrying section, carries out material choice → boiling defibre → washing according to above-mentioned definition; Perhaps
Adopt researcher of the present invention at the pulping process of applying for before this, for example: CN200710143130.0 (a kind of oxygen delignify treating method of grass group unbleached chemical pulp), CN 200710143131.5 (washing process in a kind of grass pulping process), CN200710143133.4 (a kind of method of the grass kind plant raw material being carried out the high-hardness pulp extruding black liquor of gained after the boiling), CN200710129635.1 (a kind of is the high-hardness pulp and preparation method thereof of feedstock production with the grass kind plant), CN200710143129.8 (a kind of is the bleach chemical pulp and preparation method thereof of feedstock production with the grass kind plant), CN200710143132.X (a kind of is paper pulp of raw material and preparation method thereof with straw and wheat straw), CN200710129634.7 (a kind of carding process that is used for dogstail raw material production bleach chemical pulp) also is introduced at this.Specifically: carry out material choice → get the raw materials ready → boiling → shove → wash → discongest → oxygen delignification → washing according to above-mentioned definition; The paper pulp that this mode obtains is referred to as natural-color straw pulp of the present invention in the present invention.
After obtaining described natural-color straw pulp, under laboratory condition, it is washed to pH value 6.5-7.5, preferred washing is to neutral; Becoming on the page or leaf machine to become page or leaf, carry out the detection of described index again according to the mode of prior art then.Then, test, perhaps test according to relevant criterion according to following standard.
| Standard No. | Standard name |
| GB/T?457-2008 | The mensuration of paper and cardboard folding strength |
| GB/T?458-2008 | The mensuration of paper and cardboard air permeability |
| GB/T?12660-2008 | The mensuration of Pulp Drainage Properties " Canadian standard " freedom method |
| GB/T?12914-2008 | The mensuration of paper and cardboard tensile strength |
| GB/T?1545.1-2003 | The mensuration of paper, cardboard and pulp-water extract pH |
| GB/T?1545.2-2003 | The mensuration of paper, cardboard and pulp-water extract acidity or alkalinity |
| GB/T?10739-2002 | The standard atmosphere condition that paper, cardboard and paper pulp sample are handled and tested |
| GB/T?7975-2005 | The mensuration of paper and cardboard color (diffuse reflection method) |
| GB/T?7974-2002 | Mensuration diffusion/the normal beam technique of paper, cardboard and brightness of pulp (whiteness) |
| GB/T?1546-1989 | The determination method of paper pulp kappa number |
Point out that as, " characteristic of Straw Pulp with water retention value to becoming the influence of paper character " (2000.4. gansu science and technology .1 7) straw pulp in use generally need not be pulled an oar or light beating gets final product.
Be meant with bleaching straw pulp in the contrast described in specification of the present invention or the accompanying drawing, adopt the straw pulp of prior art or the present patent application people's early stage technology preparation, after the common process bleaching, be referred to as the contrast bleaching straw pulp.
Researcher of the present invention finds, the physicochemical property of straw pulp is subjected to the influence of various factors very big, even natural-color straw pulp with a collection of taking-up, the otherness of the data of the different detections that detect batch is very big, perhaps, place the regular hour, the otherness of the various parameters of sample is also very big, even technology is identical, because the raw material different batches that different time drops into, detected data also have very big otherness, but in the detection of natural-color straw pulp of the present invention, the trend of various data is consistent, therefore can assert that natural-color straw pulp of the present invention has stronger stability.
Many indexs of natural-color straw pulp of the present invention, it all is a kind of trend scope, under the influence of irregular raw material, almost be difficult to obtain absolute value, therefore, on trend, the present invention has the terrible various indexs of improvement than prior art, therefore, natural-color straw pulp of the present invention is creative.
Embodiment
Present embodiment is the conditions of cooking among the preparation technology of described natural-color straw pulp of the present invention, and described embodiment is in order to further describe the present invention, rather than restriction the present invention.Wherein:
Embodiment 1-6 adopts the ammonium sulfite boiling
Table ten one, ammonium sulfite boiling parameter
| |
1 | 2 | 3 | 4 | 5 | 6 | |
| Raw material | Wheat straw | Straw | Reed | Giantreed | Cotton | Wheat straw | 50 |
| Alkali number (NaOH meter) % | 0 | 5％ | 2％ | 8％ | 6％ | 3％ | |
| |
9％ | 10％ | 14％ | 15％ | 12％ | 13 | |
| Liquor ratio | |||||||
| 1∶6 | 1∶10 | 1∶8 | 1∶9 | 1∶7 | 1∶3 | ||
| Temperature ℃ | 156 | 162 | 173 | 167 | 158 | 171 | |
| Pressure MPa | 0.6 | 0.62 | 0.75 | 0.68 | 0.64 | 0.72 | |
| Digestion time min | 180 | 190 | 220 | 210 | 200 | 195 |
Embodiment 7-13 adopts the caustic soda-anthraquinone method boiling
Table ten two, caustic soda-anthraquinone boiling parameter
| |
7 | 8 | 9 | 10 | 11 | 12 | 13 |
| Raw material | Wheat straw | Straw | Wheat straw: giantreed 70: 30 | Straw: reed 70: 30 | Straw: wheat straw 60: 40 | Straw: wheat straw 70: 30 | Wheat straw: reed 40: 60 |
| Alkali number (NaOH meter) | 10％ | 12％ | 13％ | 16％ | 9％ | 7％ | 11％ |
| Anthraquinone consumption (%) | 0.06％ | 0.075％ | 0.065％ | 0.08％ | 0.08％ | 0.055％ | 0.05 |
| Liquor ratio | |||||||
| 1∶2 | 1∶3 | 1∶5 | 1∶10 | 1∶4 | 1∶8 | 1∶6 | |
| Idle running (min) | 30 | 20 | 15 | 25 | 40 | 35 | 30 |
| Pressure (kPa) | 460 | 350 | 400 | 450 | 430 | 370 | 470 |
| Temperature (℃) | 175 | 130 | 140 | 175 | 160 | 130 | 175 |
| Heating-up time (min) | 80 | 70 | 90 | 50 | 70 | 90 | 100 |
| Temperature retention time (min) | 170 | 30 | 50 | 60 | 60 | 100 | 120 |
| Digestion time (min) | 250 | 100 | 140 | 110 | 130 | 190 | 220 |
Embodiment 14-21 adopts kraft cooking
Table ten three, kraft cooking parameter
Embodiment 22-26 adopts the boiling of alkaline sodium sulfite method
Table ten four, alkaline sodium sulfite method boiling parameter
The permanganate number 16-28 of the slurry that obtains after the above-mentioned boiling of process, beating degree is 10-24 ° of SR, belongs to high-hardness pulp; Permanganate number 16-23 preferably, beating degree is 10-24 ° of SR.
Through shove, slurry after washing, discongesting, change oxygen delignification over to, oxygen delignification mainly is meant oxygen delignification itself and does not comprise the possible bleaching factor that it contains in the present invention, according to description of the invention, even adopt described oxygen delignification, still need wash and bleach, therefore can distinguish with traditional bleaching.Described high-hardness pulp is delivered to the oxygen delignification reaction tower, and add NaOH and oxygen carries out the oxygen delignification reaction, obtain the slurry that hardness is permanganate number 8.7-13.2.Preferred oxygen delignification is the single hop oxygen delignification, uses an oxygen delignification reaction tower; Described high-hardness pulp is 90-100 ℃ in the temperature of this reaction tower import department, and pressure is 0.9-1.2MPa; The temperature in exit is 95-105 ℃, and pressure is 0.2-0.4MPa; Alkali charge is that the addition of oxygen is a 20-40kg/ slurry per ton in the 2-4% of NaOH to the oven dry stock amount in the described oxygen delignification; The reaction time of described high-hardness pulp in this reaction tower is 60-90 minute.
Embodiment 27
Present embodiment is the further additional embodiment to the pulp-making test of straw
1, test raw material
Straw: raw material section sampling
The sampling of caustic soda (400g/l) workshop
The sampling of anthraquinone derivative workshop
Hydrogen peroxide (30%) laboratory sample
2, digesting technoloy and data:
3, oxygen delignification technology and result
Utilize 15 liters of digesters to carry out oxygen delignification in the laboratory.Oxygen delignification technology sees Table:
Index sees Table behind the oxygen delignification:
4, screening:
Utilize the laboratory slotted screen to screen, sieve seam is 0.3mm, respectively to the slurry behind the oxygen delignification and not the slurry of oxygen delignification directly screen.
5, the sheet data are copied in the making beating of the slurry behind the straw oxygen delignification:
6, form and aspect numerical value:
Embodiment 28
Present embodiment is the further additional embodiment to the reed pulp-making test.
1, test raw material
Reed: raw material section sampling
The sampling of caustic soda (400g/l) workshop
The sampling of anthraquinone derivative workshop
Hydrogen peroxide (30%) laboratory sample
2, digesting technoloy and data:
3, oxygen delignification technology and result
Utilize 15 liters of digesters to carry out oxygen delignification in the laboratory.Oxygen delignification technology sees the following form:
Index sees Table before and after the oxygen delignification:
4, screening:
Utilize the laboratory slotted screen to screen, sieve seam is 0.3mm, respectively to slurry behind the oxygen delignification and not oxygen-delignified pulp directly screen.
5, the sheet data are copied in the slurry making beating making beating of crossing of reed oxygen delignification:
| Beating degree ° SR | 17°SR | 23°SR | 28°SR | 36° |
| Freedom CFS | ||||
| 600 | 520 | 470 | 410 | |
| Weight in wet base g | 3.0 | 2.6 | 2.2 | 2.0 |
| Quantitative g/ |
60 | 60 | 60 | 60 |
| Whiteness %IS0 | 37.25 | 37.25 | 37.25 | 37.25 |
| Bulk cm 3/g | 2.585 | 2.370 | 2.469 | 2.174 |
| Air permeability ml/min | 7289 | 3038 | 2764 | 4728 |
| Fracture length Km | 3.510 | 4.119 | 4.337 | 5.628 |
| Tearability mN | 397.8 | 507.1 | 481.4 | 472.8 |
| Folding strength (inferior) | 14 | 35 | 23 | 151 |
| Tensile index N.m/g | 34.398 | 40.366 | 42.502 | 55.154 |
| Tear index mN.m2/g | 6.60 | 8.40 | 8.00 | 7.88 |
6, reed not the slurry making beating of oxygen delignification copy the sheet data:
| Beating degree ° SR | 17°SR | 23°SR | 28°SR | 36°SR |
| Freedom CFS | 640 | 550 | 480 | 430 |
| Weight in wet base g | 3.1 | 3.1 | 2.8 | 2.0 |
| Quantitative g/ |
60 | 60 | 60 | 60 |
| Whiteness %ISO | 29.6 | 29.6 | 29.6 | 29.6 |
| Bulk cm 3/g | 2.732 | 2.573 | 2.577 | 2.256 |
| Air permeability ml/min | 8409 | 3685 | 6359 | 1415 |
| Fracture length Km | 2.349 | 4.247 | 4.623 | 5.964 |
| Tearability mN | 452.2 | 459.9 | 443.1 | 511 |
| Folding strength (inferior) | 9 | 20 | 13 | 220 |
| Tensile index N.m/g | 23.020 | 41.621 | 45.305 | 58.447 |
| Tear index mN.m2/g | 7.54 | 7.67 | 7.39 | 8.52 |
7, form and aspect:
Embodiment 29
Present embodiment is the further additional embodiment to the cotton stalk pulp-making test
1, test raw material
Cotton stalk: provide raw material for oneself, carry out craft and get the raw materials ready.
The sampling of caustic soda (400g/l) workshop
The sampling of anthraquinone derivative workshop
Hydrogen peroxide (30%) laboratory sample
2, digesting technoloy and data:
3, oxygen delignification technology and result
Utilize 15 liters of digesters to carry out oxygen delignification in the laboratory, oxygen delignification technology sees Table:
Index sees Table before and after the oxygen delignification:
4, screening:
Utilize the laboratory slotted screen to screen, sieve seam is 0.3mm, respectively to the slurry behind the oxygen delignification and not the slurry of oxygen delignification directly screen.
5, the cotton stalk pulp behind the oxygen delignification is copied the sheet data:
6, the sheet data are not copied in the making beating of the cotton stalk pulp of oxygen delignification:
7, form and aspect:
Comparative example one
What this comparative example detected is the opacity of natural-color straw pulp, and the mode of sample acquisition process and test is carried out according to aforesaid test method, and in this comparative example, described opacity can adopt aforesaid test method that the opacity of the above is detected.
The opacity actual measurement parameter of table one contrast natural-color straw pulp and natural-color straw pulp of the present invention
| Contrast natural-color straw pulp (%) (sample obtains with random order according to the present invention's definition, and records following parameter) | The following data of natural-color straw pulp of the present invention (%) in order, |
| ?85.6 | 90 |
| ?86 | 91.1 |
| ?86.4 | 97.1 |
| ?85.5 | 93 |
| ?82.9 | 93.9 |
| ?85.9 | 94.1 |
| ?86 | 100 |
| ?83.8 | 92.4 |
| ?86.1 | 99.9 |
| ?84.5 | 95 |
Comparative example two
What this comparative example detected is the bulk index of natural-color straw pulp of the present invention, and in this comparative example, described opacity can adopt aforesaid test method that described opacity is detected.
The bulk actual measurement parameter of table two contrast natural-color straw pulp and natural-color straw pulp of the present invention
| Contrast natural-color straw pulp (cm 3/ g) (sample obtains with random order according to the present invention's definition, and records following parameter) | Natural-color straw pulp (cm of the present invention
3/ g) following data in order, |
| ?1.4 | 1.4 |
| ?1.3 | 1.5 |
| ?1.7 | 1.6 |
| ?2 | 2.572 |
| ?1.7 | 2.623 |
| ?1.94 | 2.631 |
| ?1.941 | 2.65 |
| ?1.4 | 3 |
| ?1.5 | 2.5 |
| ?1.5 | 2.1 |
Comparative example three
What this comparative example detected is the air permeability index of natural-color straw pulp of the present invention, and in this comparative example, described air permeability can adopt aforesaid test method that described air permeability is detected.
The air permeability actual measurement parameter of table three contrast natural-color straw pulp and natural-color straw pulp of the present invention
| Contrast natural-color straw pulp (ml/min) (sample obtains with random order according to the present invention's definition, and records following parameter) | The following data of natural-color straw pulp of the present invention (ml/min) in order, |
| ?30 | 350 |
| 452 | 60 |
| 37 | 110 |
| 550 | 150 |
| 55 | 1200 |
| 170 | 760 |
| 330 | 900 |
| 33 | 70 |
| 500 | 800 |
| 41 | 50 |
Comparative example four
What this comparative example detected is the tensile index index of natural-color straw pulp of the present invention, and in this comparative example, described tensile index can adopt aforesaid test method that described tensile index is detected.
Table four contrast is surveyed parameter with the tensile index of natural-color straw pulp and natural-color straw pulp of the present invention
| Contrast with natural-color straw pulp (N.m/g) (sample obtains with random order according to the present invention's definition, and records following parameter) | The following data of natural-color straw pulp of the present invention (N.m/g) in order, |
| ?28.15 | 56 |
| ?29.78 | 38 |
| ?31.42 | 40 |
| ?36.75 | 50 |
| ?37 | 68 |
| ?27 | 70 |
| ?39 | 49 |
| ?38 | 65 |
| ?39 | 53 |
| ?29 | 35 |
Comparative example five
What this comparative example detected is the tear index index of natural-color straw pulp of the present invention, and in this comparative example, described tear index can adopt aforesaid test method that described tear index is detected.
Table five contrast is surveyed parameter with the tear index of natural-color straw pulp and natural-color straw pulp of the present invention
| Contrast natural-color straw pulp (mN.m 2/ g) (sample obtains with random order according to the present invention's definition, and records following parameter) | Natural-color straw pulp (mN.m of the present invention
2/ g) following data in order, |
| 3.77 | 5.5 |
| 2.3 | 4.97 |
| 4.4 | 2.9 |
| 2.5 | 3.098 |
| 4.16 | 4.107 |
| 2.2 | 3.3 |
| 3.811 | 4.616 |
| 2.7 | 4.735 |
| 3.867 | 4.809 |
| 4.142 | 3.8 |
| 2.6 | 4.862 |
| 2.9 | 2.7 |
| 4.244 | 4.3 |
| 2.4 | 5.2 |
| 4.714 | 5.4 |
| 2.2 | 2.5 |
Comparative example six
What this comparative example detected is the folding strength index of natural-color straw pulp of the present invention, and in this comparative example, described folding strength can adopt aforesaid test method that described folding strength is detected.
Table six contrast is surveyed parameter with the folding strength of natural-color straw pulp and natural-color straw pulp of the present invention
| Contrast with natural-color straw pulp (inferior) (sample obtains with random order according to the present invention's definition, and records following parameter) | The following data of natural-color straw pulp of the present invention (inferior) in order, |
| ?10 | 36 |
| ?17 | 70 |
| ?8 | 22 |
| ?14 | 30 |
| ?9 | 10 |
| ?10 | 57 |
| ?7 | 50 |
| ?11 | 43 |
| ?9 | 60 |
| ?7 | 20 |
Comparative example seven
What this comparative example detected is the freedom index of natural-color straw pulp of the present invention, and in this comparative example, described freedom can adopt aforesaid test method that described freedom is detected.
Table seven contrast is surveyed parameter with the freedom of natural-color straw pulp and natural-color straw pulp of the present invention
| Contrast with natural-color straw pulp (ml) (sample obtains with random order according to the present invention's definition, and records following parameter) | The following data of natural-color straw pulp of the present invention (ml) in order, |
| 370 | 350 |
| 380 | 485 |
| 330 | 400 |
| 420 | 505 |
| 330 | 470 |
| 450 | 480 |
| 360 | 490 |
| 330 | 460 |
| 320 | 375 |
| 450 | 450 |
Comparative example eight
What this comparative example detected is the whiteness index of natural-color straw pulp of the present invention, and in this comparative example, described whiteness can adopt aforesaid test method that described whiteness is detected.
The whiteness of paper or cardboard be meant white or near the paper of white or paperboard surface to the reflectivity of blue light, and recently represent with the reflectivity on blue light illumination magnesia on-gauge plate surface is relative.
Table eight contrast is surveyed parameter with the whiteness of bleaching straw pulp and natural-color straw pulp of the present invention
| Contrast with bleaching straw pulp (%) (sample obtains with random order according to the present invention's definition, and records following parameter) | The following data of natural-color straw pulp of the present invention (%) in order, |
| ?66.7 | 46.3 |
| ?79.2 | 45 |
| ?77.3 | 52 |
| ?74.9 | 40.8 |
| ?77.2 | 42.7 |
| ?77.2 | 30 |
| ?73.1 | 51.3 |
| ?78 | 50 |
| ?78.7 | 33 |
| ?68.4 | 54 |
Comparative example nine
What this comparative example detected is the form and aspect index of natural-color straw pulp of the present invention, and in this comparative example, described form and aspect can adopt aforesaid test method that described form and aspect are detected.
Form and aspect are the absolute color that are used for representing paper, L, a, b value that a certain particular color is corresponding concrete.This index can be expressed the impression of human eye dialogue degree and form and aspect more exactly, it is to use datumization to describe the system of form and aspect (color), in Hunter Lab system, L, a, b are calculated by above tristimulus values, L (L=10Y015) is the measurement unit of lightness, (a=1715's (1102X-Y)/Y015) is red on the occasion of representing, and negative value is represented green for a; (b=710's (Y-01847 Z)/Y015) is yellow on the occasion of representing, and negative value is represented blue for b.
Table nine contrast is surveyed parameter with the form and aspect of bleaching straw pulp and natural-color straw pulp of the present invention
| Contrast with bleaching straw pulp L (sample obtains with random order according to the present invention's definition, and records following parameter) | Contrast bleaching straw pulp a | Contrast bleaching straw pulp b | The following data of natural-color straw pulp L of the present invention in order, |
Natural-color straw pulp a of the present invention | Natural-color straw pulp b of the present invention |
| 90.34 | 0.03 | 5.47 | 85 | 3.14 | 19 |
| 90.77 | 0.11 | 5.68 | 84 | 1.33 | 11 |
| 91.16 | 0.19 | 5.86 | 77 | 2.9 | 10.44 |
| 92.1 | 0.23 | 6.19 | 82 | 1.5 | 10 |
| 92.46 | 0.31 | 6.34 | 74.72 | 3 | 18.52 |
| 93.34 | 0.47 | 6.5 | 75 | 2.61 | 14.13 |
| 93.82 | 0.56 | 6.83 | 77.18 | 1.6 | 18 |
| 94.01 | 0.61 | 7.1 | 79.72 | 1.9 | 20 |
| 94.27 | 0.79 | 7.56 | 72 | 3.14 | 12 |
| 94.47 | 0.86 | 7.98 | 87 | 3.2 | 19.11 |
Comparative example ten
What this comparative example detected is the hardness number of natural-color straw pulp of the present invention, and in this comparative example, described hardness can adopt aforesaid test method that described hardness is detected.
Pulp hardness (hardness of pulp) is one of quality index of chemical pulp, the degree that non-fibrous material (mainly being lignin) is removed in the expression paper pulp.Commonly used have card primary (Kappa) valency and two kinds of methods of permanganate number, and the both is based on the oxidation of the sour potassium of permanganic acid to non-fibrous material.The former is the 1 gram oven dry stock consumption (in milliliter) of (25 ℃ time 10 minutes) 0.02 rubbing of being consumed/rising potassium manganate standard liquid under certain condition, how in order to the hardness of expression true qualities wood pulp.The latter is the 1 gram oven dry stock consumption (in milliliter) of (25 ℃ time 5 minutes) 0.02 rubbing of being consumed/rising potassium manganate standard liquid under certain condition, how needs the hardness of the non-wood-fiber paper pulp (as straw pulp) of bleaching in order to expression.
Pulp hardness is higher, and then by the material of potassium permanganate oxidation the more, the consumption of the outer solution of permanganic acid is bigger, and bleaching more is not easy, but the mechanical strength of paper pulp is also higher.The permanganate number that generally can float straw pulp is 9～14, and semi-chemical pulp is 15～18, and the true qualities hard stock is then more than 20.
The hardness actual measurement parameter of table ten natural-color straw pulp of the present invention
| The following data of natural-color straw pulp hardness of the present invention (K) in order, |
| 16 |
| 7 |
| 9.6 |
| 8 |
| 10.7 |
| 11.1 |
| 14 |
| 12.4 |
| 13 |
| 15 |
Claims (8)
1. the natural-color straw pulp of the freedom of an improvement, air permeability and tensile index and stable performance is characterized in that the air permeability 70-800ml/min of described natural-color straw pulp; Tensile index 40-65N.m/g, freedom 460-400ml, whiteness is 33-45%, the hardness of natural-color straw pulp is 8-14K.
2. natural-color straw pulp according to claim 1 is characterized in that the raw material of described natural-color straw pulp is meant straw, wheat straw, reed, giantreed, bagasse, cotton stalk and their mixture.
3. natural-color straw pulp according to claim 1 and 2 is characterized in that the raw material of described natural-color straw pulp is meant straw, wheat straw and their mixture.
4. natural-color straw pulp according to claim 3 is characterized in that the raw material of described natural-color straw pulp is meant wheat straw.
5. according to claim 1-2 or 4 described natural-color straw pulps, it is characterized in that adding in the described natural-color straw pulp known paper making additive.
6. natural-color straw pulp according to claim 3 is characterized in that adding in the described natural-color straw pulp known paper making additive.
7. any application of described natural-color straw pulp in paper products of claim 1-6.
8. any application of described natural-color straw pulp in mixed pulp of claim 1-6.
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|---|---|---|---|---|
| CN1432687A (en) * | 2002-01-16 | 2003-07-30 | 邓州市老廷实业有限公司 | Straw pulping process |
| CN101353872A (en) * | 2007-12-05 | 2009-01-28 | 山东福荫造纸环保科技有限公司 | Duplicating paper made from grass pulp and preparation thereof |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1432687A (en) * | 2002-01-16 | 2003-07-30 | 邓州市老廷实业有限公司 | Straw pulping process |
| CN101353872A (en) * | 2007-12-05 | 2009-01-28 | 山东福荫造纸环保科技有限公司 | Duplicating paper made from grass pulp and preparation thereof |
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