CN1837458A - Chemical and machinery pulping process using complete white mulberry branch as raw material - Google Patents
Chemical and machinery pulping process using complete white mulberry branch as raw material Download PDFInfo
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Abstract
This invention discloses a pulping process with mulberry bough as raw material, which comprises the following steps: slicing, steaming before scouring, scouring, steaming after scouring, first squeeze, second squeeze, steeping, reaction, post-treatment, and these steps are sequential. The invention improves percent of pass of slicing mulberry bough and availability ratio of pulp in the core, and has good dust collection efficiency. With mixing pulping of mulberry bough, the bore rod with short fibre and large content can be used fully, and the finished pulp can be used in top grade paper. With fully using resource is, the process settles said technical matters, and it is suit for use in commercial manufacture.
Description
Technical field
The present invention relates to a kind of paper-making pulping process, particularly a kind of pulping process that utilizes mulberry branch for the chemi-mechanical pulp of raw material.
Background technology
Along with the technological progress of paper industry and the increase of paper consumption figure, the raw material mix of papermaking is also constantly developing.As the papermaking technology of one of China's " four inventions ", be born in the Cai Lun epoch of the Eastern Han Dynasty, the raw material of papermaking at that time is based on rag of fiber crops and fishing net; To in the period of the Tang and Song Dynasty, raw materials such as fiber crops, bark, straw are brought into use in papermaking; It is found that subsequently, timber is better than other raw material because of its fibre morphology, and, easily produce various high-quality products, the production efficiency height, be easy to pollution control, volume is intensive, is convenient to transportation, preservation is more suitable for producing greatly in modernization than other raw material, but in China, because the attribute understanding to the paper industry is not enough after the founding of the state, add that the Chinese forest resource is very poor, has hindered the development of Chinese paper industry, now, in conjunction with the abundant actual conditions of China's bamboo resource, though successfully it is used as paper making raw material,, still can not satisfy the needs of paper making raw material far away, domestic each research institutions and scientific research institution are all in the exploitation of carrying out various paper making raw materials energetically at present, and mulberry twigs pulping is exactly one of them.
Mulberry tree is a herbaceos perennial, has growth soon, branch output advantages of higher, and its phloem fiber accounts for the 26%-30% of full bar total amount simultaneously, and long fiber content accounts for 40%-50%, is a kind of paper making raw material of high-quality.Utilizing mulberry twigs pulping papermaking, can alleviate the contradiction of current China paper industry long fibered raw material deficiency, is a good thing of benefiting the nation and the people.China produces the rice paper record with regard to the bast of useful ramulus mori very many years ago, has been the achievement that obtains in the China recent years research with the core bar production true qualities wrapping paper of ramulus mori, and still, discovery utilizes the report of the full bar mixed pulp of mulberry shoot.
Patent Office of the People's Republic of China discloses a kind of " mulberry shoot; tobacco rod cold soda pulping paper technology " with publication number CN107092A, it is to adopt caustic soda that material piece is flooded at normal temperatures and pressures, wash routinely behind the pulping, making beating, papermaking, utilize this method can make cigarette paper, imitative rice paper, the high-grade paper of offering a sacrifice to gods or ancestors, grease proofing and waterproof body paper (food wrapper) etc., this technology is typical chemical pulping process, a kind of technology of cold soda pulping specifically, from its technology contents, though it carries out mixed pulp after with the bast of ramulus mori and core bar section, but do not provide the technical clarification of the high-grade paper such as paper of can framing news yet, its reason is that the mulberry shoot cold soda pulping only adopts the pulping process that removes lignin in a large number, do not bleach and the technical process of high consistency refining, whiteness and fiber properties etc. can not reach the requirement of making high-grade paper.
Do not utilize the full bar of mulberry shoot to carry out the instruction that mixed pulp prepares high-grade paper in the above-mentioned background technology, the reason of searching to the bottom, be not fully realize the characteristic of mulberry branch itself and, certainly, also do not find the way that addresses these problems with the technical barrier that is run in its pulping process.
Through fully experiment, research, the applicant finds that the full bar of mulberry branch has following characteristic:
Table one: mulberry branch is fibrous
| Bast | Core bar | ||
| Fibre length | Fiber content | Fibre length | Fiber content |
| 1-10mm | About 60% | 0.5-0.7mm | About 40% |
Table two: bast institutional framework
| Ash content | Solution extract (%) | Poly-the eleventh of the twelve Earthly Branches sugar (%) | Protein (%) | Lignin (%) | Pectin (%) | Cellulose (%) | ||
| Hot water | Ether | 1%NaOH solution | ||||||
| 4.40 | 2.39 | 3.37 | 35.47 | 10.42 | 6.13 | 8.74 | 8.84 | 54.81 |
Bast and core bar ratio in table three, the mulberry branch
| Bast | Core bar |
| 26％ | 77％ |
From above three tables as can be known, the technological difficulties of the full bar mixed pulp of mulberry branch mainly show following several aspect:
(1) since ramulus mori bast and core bar chemical composition have than big-difference, in the mixed pulp process, particularly in dipping process, to reach fully very difficult simultaneously to the alkalization of bast and core bar, be not easy to find suitable maceration extract and impregnation technology condition, cause the inadequate phenomenon of fibre swelling easily, influence effects on slurry making;
(2) because ramulus mori bast and core bar fibre morphology are also very inequality, fiber length has a long way to go, in the mixed pulp process, oversize as fruit fiber, hold poly-during papermaking easily, too short as fruit fiber, made strength of paper is not enough, therefore, and in pulping process, must solve made paper pulp and meet the requirement of producing high-grade paper, but still unresolved so far;
Exactly because above-mentioned difficult point, the employing mulberry branch is a pulping raw material, prior art can only be separated bast and distinguished slurrying with core bar, but bast and core bar separation process difficulty, the general requirement fully soaked mulberry branch before separation, and soak time must be grown, the ramulus mori moisture should be high, and adopt artificial the separation, the needs that at all can not adapt to industrialized production, therefore with bast and core bar respectively the method for slurrying generally only limit to handicraft workshop, copying high-grade paper in China with bast system chemical pulp has long history, as rice paper, lens wiping paper, filter paper etc., because the restriction that raw material and slurrying require, production scale is very little, if only adopt bast as pulping raw material, because its ratio shared in whole mulberry branch is little, as carrying out pulping and paper-making with bast entirely, then other positions are lost and are decreased greatly, and how the cost height makes full use of the high-grade paper of core bar manufacturing and become to need to be resolved hurrily and also unsolved so far technical problem;
The second, bast appearance dust is difficult to remove:
The very thin dust of one deck is arranged on the outer surface of bast, and this dust and bast are closely linked, as do not remove totally will cause have on the paper pierce, paper defects such as scar, will influence quality of finished paper and output.Unique chemical method that adopts is specially to the slurrying of bast part.By the dosage that strengthens chemical liquid bast is carried out boiling, adopts several sections washings can remove dust voluntarily then, adopt the method production exactly as the pulping process of rice paper, lens wiping paper, filter paper etc.But this pulping process exists the yield of slurry very low, the high defective of production cost, and can't be used for big production requirement, economy is relatively poor.
Full bar is adopted chemical pulping,, as adopt identical chemical liquid to occur because of there is not dust problems in core bar: or the excessive core bar fiber of soup is impaired serious, and the yield of slurry and intensity are low excessively; Or soup causes dust to eradicate with quantity not sufficient, and bast fibre bundle is more, and therefore the poor quality of slurry is difficult to amount of liquid medicine is controlled accurately.
Summary of the invention
The objective of the invention is to overcome the shortcoming of above-mentioned prior art and provide a kind of is chemistry, the mechanical type pulping process of raw material with the full bar of mulberry branch, this technology not only is suitable for industrialized production, and can adopt the full bar mixed pulp of mulberry branch, made full use of resource, can solve the removal problem of bast appearance dust, made paper pulp meets the quality requirement of producing high-grade paper.
Consider that with the full bar of mulberry branch be raw material, will run into many insoluble technical barriers as routinely chemical pulping, the present invention has improved the pulping process of existing chemi-mechanical pulp according to the self character of the full bar of mulberry branch, reaches purpose of the present invention.
A kind of is the pulping process of the chemi-mechanical pulp of raw material with the mulberry branch, carries out as follows:
(1) section: mulberry branch is cut into the vertical cut sheet that length is 10～18mm;
(2) decatize before the washing: above-mentioned vertical cut sheet is sent into the decatize storehouse, and (concentration is 50～100g/l) to add the sodium hydroxide solution of vertical cut sheet weight (net weight) 2-3% in the decatize storehouse, be under 40～60 ℃ the condition at the decatize exhaust temperature, steaming time 20-40 minute;
(3) washing: the vertical cut sheet after the decatize is washed in 40～70 ℃ water;
(4) washing back decatize: the vertical cut sheet after will washing is sent into the decatize storehouse, is under 35～70 ℃ the condition, about steaming time 20-30 minute at the decatize exhaust temperature;
(5) one sections squeezings: the vertical cut sheet after the decatize is sent into to squeeze in first section screw extruder to grind to tear under 1～2 kilogram of pressure and is processed into the compression material once more, and the compression ratio of this section vertical cut sheet is 1: 4;
(6) two sections squeezings: the compression material is sent into to squeeze in second section screw extruder to grind to tear under 1.5～2 kilograms of pressure and is processed into the second-compressed material after will squeezing, and the compression ratio of this section compression material is 1: 4;
(7) dipping: will send in the macerator through the material after two sections squeezings, and (concentration is 70～130g/l), 2～5% hydrogen peroxide, 3～5% sodium metasilicate (being commonly called as waterglass) and 0.2～0.4% DTPA (chemical name: diethylene triamine pentacetic acid (DTPA), its molecular formula: C to add the NaOH of weight of material (net weight) 3～5% in macerator
14H
23N
3O
10), the material dipping was got final product in 2～5 minutes;
(8) reaction: the material after will flooding is sent into the reaction warehouse internal reaction, and the time of staying is 30～50 minutes, and temperature is 50～80 ℃;
(9) post processing: reacted material is sent into two sections defibrination workshop sections, and disappearing behind the defibrination dives handles, and screening then purifies, and is concentrated into pulping.Post-processing step is a conventional steps
Physicochemical characteristic such as following table by the made pulping of above-mentioned chemi-mechanical pulp pulping process meet the quality requirement of making high-grade paper.
Table four: the physicochemical characteristic of pulping:
| Physical name | Whiteness | Beating degree | Fracture length | Tear index | Dust |
| Unit | ％ISO | °SR | m | mN·m 2/g | A dust/gram slurry (0.5～2.5mm) |
| Size of data | 60～64 | 50～55 | 2400～2600 | 5～6 | 10～18 |
The present invention has following advantage than prior art:
(1) improved the section qualification rate: getting the raw materials ready in pulp and paper production is the key link, and what material was equipped with is good with bad, is directly connected to the unimpeded of blanking.Wood chip or bamboo chip that the slicer of conventional usefulness cuts out are the sheet of cutting sth. askew, and can effectively increase specific area like this, and the overlapping putty phenomenon that causes when having certain gradient can reduce the tablet blanking.Carry out the mulberry branch blank with the method for routine and bigger difficulty then occurred, its reason is that the bast of mulberry branch has certain toughness, between the upper and lower cutter of slicer of usefulness certain clearance is arranged owing to get the raw materials ready, cause bast to be difficult to cut off, can't blanking, the present invention breaks the intrinsic section pattern of papermaking feed-preparing process, change original blank mode, courageously adopt the unused blank mode of papermaking circle, change the vertical cut sheet into by the original sheet of cutting sth. askew, mulberry bar bast is thoroughly cut off, thereby improved the section qualification rate;
(2) change APP decatize mode, it is effective to remove dust: the decatize of general APP tablet is that directly logical steam gets final product, consider that bast has a large amount of dust, these dust will directly influence the quality of slurry as not removing, cause to have on the paper and pierce or scar, but these dust generally can not remove easily, according to the experience of the tough latex of laboratory chemistry legal system ramulus mori, in decatize, increase a certain amount of soup, can reach the purpose that removes dust comparatively fully; Dipping effect is good: in impregnation stage mainly is to control institute well to add amount of liquid medicine, should guarantee that ramulus mori epidermis dust can remove as far as possible, can make the abundant swollen of fiber again, the cutting of fiber length is even when being convenient to high consistency refining, wire-dividing broom purification is good, add the relevant treatment of screening stage, the fiber length of pulping can reach good uniformity, can guarantee into the bulk of paper, neat and well spaced degree like this, can also satisfy the adaptability of printing paper.The purpose of dipping mainly is to be softening lignin, be convenient to defibrination, particularity at the mulberry branch structure, it is many than broadleaf to be that bast contains the pectin amount, and the surface has one deck dust to adhere to, because the ramulus mori water imbibition is stronger, dipping, squeezing effect are better, infiltration such as alkali lye is very fast, alkali absorbs many, easily skids, and it is not smooth that this just causes material for making clothes to carry in screw machine, the normal obstruction, so have only one section dipping to get final product, in order to guarantee pulping intensity, the alkali number of one section dipping is bigger, the hydrogen peroxide addition is also bigger, has fully guaranteed dipping effect; This kind mulberry twigs pulping technology pulp yield is higher, and the chemical industry medicine that is consumed and APMP production line system poplar, masson s pine pulp relatively have certain superiority.
Process conditions when (3) changing the squeezing conquassation: press the APP normal mode, the general employing of squeezing conquassation of tablet is carried out for two sections, two sections pressure is identical.Because the particularity of mulberry branch structure, the length that is bast fiber is oversize too short with the core bar fibre length, as still being undertaken by former method, the situation that impaired serious (pressure is excessive) two-stage differentiation of long fiber bundle more (pressure is not enough) and staple fibre then may occur, such slurry is used for papermaking, to cause paper-forming evenness very poor, intensity does not reach requirement, can't satisfy production requirement at all.By repeatedly medium and small experiment, find one, two section suitable squeeze pressure respectively promptly: one section pressure is slight, two sections pressure are heavy slightly, one section squeezing is mainly used in the effect to epidermis, two sections squeezings are mainly used in the effect to full bar, and the pressure by alleviating first section squeezing is further removed dust to the reaction time that prolongs epidermis, the effect of protection sandwich layer fiber, thus effectively raise the yield that sandwich layer is starched;
(4) this technology can adopt the full bar mixed pulp of mulberry branch, short but the high material of content of this fiber of core bar has been given utilizing fully, and made pulping has reached the requirement of making high-grade paper, made full use of resource, simultaneously, this technology is suitable for industrialized production because of having solved above-mentioned technical problem.
Description of drawings
Fig. 1 is a process chart of the present invention.
The specific embodiment
Below in conjunction with drawings and Examples the present invention is described in further detail, but the present invention has more than and is limited to these examples:
Embodiment 1: a kind of is the pulping process of the chemi-mechanical pulp of raw material with the mulberry branch, carries out as follows:
(1) section: mulberry branch is cut into the vertical cut sheet that length is 10mm;
(2) decatize before the washing: above-mentioned vertical cut sheet being sent into the decatize storehouse, and add the sodium hydroxide solution (concentration is 100g/l) of vertical cut sheet weight (net weight) 2% in the decatize storehouse, is under 60 ℃ the condition at the decatize exhaust temperature, steaming time 20 minutes;
(3) washing: the vertical cut sheet after the decatize is washed in 70 ℃ water;
(4) washing back decatize: the vertical cut sheet after will washing is sent into the decatize storehouse, is that steaming time is about 20 minutes under 70 ℃ the condition at the decatize exhaust temperature;
(5) one sections squeezings: the vertical cut sheet after the decatize is sent into to squeeze in first section screw extruder to grind to tear under 1 kilogram of pressure and is processed into the compression material once more, and the compression ratio of this section vertical cut sheet is 1: 4;
(6) two sections squeezings: the compression material is sent into to squeeze in second section screw extruder to grind to tear under 1.5 kilograms of pressure and is processed into the second-compressed material after will squeezing, and the compression ratio of this section compression material is 1: 4;
(7) dipping: will send in the macerator through the material after two sections squeezings, and in macerator, add NaOH (concentration is 130g/l), 2% hydrogen peroxide, 3% sodium metasilicate (being commonly called as waterglass) and 0.2% the DTPA (chemical name: diethylene triamine pentacetic acid (DTPA), its molecular formula: C of weight of material (net weight) 3%
14H
23N
3O
10), the material dipping was got final product in 2 minutes;
(8) reaction: the material after will flooding is sent into the reaction warehouse internal reaction, and the time of staying is 50 minutes, and temperature is 50 ℃;
(9) post processing: reacted material is sent into two sections defibrination workshop sections, and disappearing behind the defibrination dives handles, and screening then purifies, and is concentrated into pulping.
Embodiment 2: a kind of is the pulping process of the chemi-mechanical pulp of raw material with the mulberry branch, carries out as follows:
(1) section: mulberry branch is cut into the vertical cut sheet that length is 18mm;
(2) decatize before the washing: above-mentioned vertical cut sheet being sent into the decatize storehouse, and add the sodium hydroxide solution (concentration is 50g/l) of vertical cut sheet weight (net weight) 3% in the decatize storehouse, is under 40 ℃ the condition at the decatize exhaust temperature, steaming time 40 minutes;
(3) washing: the vertical cut sheet after the decatize is washed in 40 ℃ water;
(4) washing back decatize: the vertical cut sheet after will washing is sent into the decatize storehouse, is that steaming time is about 30 minutes under 35 ℃ the condition at the decatize exhaust temperature;
(5) one sections squeezings: the vertical cut sheet after the decatize is sent into to squeeze in first section screw extruder to grind to tear under 1.9 kilograms of pressure and is processed into the compression material once more, and the compression ratio of this section vertical cut sheet is 1: 4;
(6) two sections squeezings: the compression material is sent into to squeeze in second section screw extruder to grind to tear under 2 kilograms of pressure and is processed into the second-compressed material after will squeezing, and the compression ratio of this section compression material is 1: 4;
(7) dipping: will send in the macerator through the material after two sections squeezings, and in macerator, add NaOH (concentration is 70g/1), 5% hydrogen peroxide, 5% sodium metasilicate (being commonly called as waterglass) and 0.4% the DTPA (chemical name: diethylene triamine pentacetic acid (DTPA), its molecular formula: C of weight of material (net weight) 5%
14H
23N
3O
10), the material dipping was got final product in 5 minutes;
(8) reaction: the material after will flooding is sent into the reaction warehouse internal reaction, and the time of staying is 30 minutes, and temperature is 80 ℃;
(9) post processing: reacted material is sent into two sections defibrination workshop sections, and disappearing behind the defibrination dives handles, and screening then purifies, and is concentrated into pulping.
Claims (1)
1, a kind of is the pulping process of the chemi-mechanical pulp of raw material with the full bar of mulberry branch, carries out as follows:
(1) section: mulberry branch is cut into the vertical cut sheet that length is 10～18mm;
(2) decatize before the washing: above-mentioned vertical cut sheet is sent into the decatize storehouse, and (concentration is 50～100g/l) to add the sodium hydroxide solution of vertical cut sheet weight (net weight) 2-3% in the decatize storehouse, be under 40～60 ℃ the condition at the decatize exhaust temperature, steaming time 20-40 minute;
(3) washing: the vertical cut sheet after the decatize is washed in 40～70 ℃ water;
(4) washing back decatize: the vertical cut sheet after will washing is sent into the decatize storehouse, is under 35～70 ℃ the condition, about steaming time 20-30 minute at the decatize exhaust temperature;
(5) one sections squeezings: the vertical cut sheet after the decatize is sent into to squeeze in first section screw extruder to grind to tear under 1～2 kilogram of pressure and is processed into the compression material once more, and the compression ratio of this section vertical cut sheet is 1: 4;
(6) two sections squeezings: the compression material is sent into to squeeze in second section screw extruder to grind to tear under 1.5～2 kilograms of pressure and is processed into the second-compressed material after will squeezing, and the compression ratio of this section compression material is 1: 4;
(7) dipping: will send in the macerator through the material after two sections squeezings, and (concentration is 70～130g/l), 2～5% hydrogen peroxide, 3～5% sodium metasilicate and 0.2～0.4% DTPA, and the material dipping was got final product in 2～5 minutes to add the NaOH of weight of material (net weight) 3～5% in macerator;
(8) reaction: the material after will flooding is sent into the reaction warehouse internal reaction, and the time of staying is 30～50 minutes, and temperature is 50～80 ℃;
(9) post processing: reacted material is sent into two sections defibrination workshop sections, and disappearing behind the defibrination dives handles, and screening then purifies, and is concentrated into pulping.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100209101A CN100398745C (en) | 2006-04-25 | 2006-04-25 | Chemical and machinery pulping process using complete white mulberry branch as raw material |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100209101A CN100398745C (en) | 2006-04-25 | 2006-04-25 | Chemical and machinery pulping process using complete white mulberry branch as raw material |
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| Publication Number | Publication Date |
|---|---|
| CN1837458A true CN1837458A (en) | 2006-09-27 |
| CN100398745C CN100398745C (en) | 2008-07-02 |
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|---|---|---|---|
| CNB2006100209101A Expired - Fee Related CN100398745C (en) | 2006-04-25 | 2006-04-25 | Chemical and machinery pulping process using complete white mulberry branch as raw material |
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Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102154887A (en) * | 2011-02-22 | 2011-08-17 | 杨和荣 | Method for producing high-whiteness bleached ramulus mori pulp by caustic soda-anthraquinone continuous stewing technology |
| CN102108644B (en) * | 2009-12-24 | 2012-08-08 | 深圳市美中现代科技发展有限公司 | Pollution-free production process of plant fiber pulp |
| CN102943409A (en) * | 2012-11-14 | 2013-02-27 | 常州亚当生物技术有限公司 | Method for making paper by utilizing aquilaria sinensis branches and leaves |
| CN103266516A (en) * | 2013-05-09 | 2013-08-28 | 祁建生 | Cotton stalk unbleached pulp making technology |
| CN105735030A (en) * | 2016-02-25 | 2016-07-06 | 杭州特种纸业有限公司 | Lens wiping paper and preparing method thereof |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1385580A (en) * | 2001-05-11 | 2002-12-18 | 张志芬 | Pulping using bark of artificial quickly-grown Common Papermulberry (HAP method) and trunk (APMP method) |
-
2006
- 2006-04-25 CN CNB2006100209101A patent/CN100398745C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102108644B (en) * | 2009-12-24 | 2012-08-08 | 深圳市美中现代科技发展有限公司 | Pollution-free production process of plant fiber pulp |
| CN102154887A (en) * | 2011-02-22 | 2011-08-17 | 杨和荣 | Method for producing high-whiteness bleached ramulus mori pulp by caustic soda-anthraquinone continuous stewing technology |
| CN102943409A (en) * | 2012-11-14 | 2013-02-27 | 常州亚当生物技术有限公司 | Method for making paper by utilizing aquilaria sinensis branches and leaves |
| CN103266516A (en) * | 2013-05-09 | 2013-08-28 | 祁建生 | Cotton stalk unbleached pulp making technology |
| CN103266516B (en) * | 2013-05-09 | 2016-01-20 | 祁建生 | A kind of cotton stalk natural color pulp manufacturing technique |
| CN105735030A (en) * | 2016-02-25 | 2016-07-06 | 杭州特种纸业有限公司 | Lens wiping paper and preparing method thereof |
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| Publication number | Publication date |
|---|---|
| CN100398745C (en) | 2008-07-02 |
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