CN103741558A - Method for making archaistic art paper - Google Patents
Method for making archaistic art paper Download PDFInfo
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- CN103741558A CN103741558A CN201310751596.4A CN201310751596A CN103741558A CN 103741558 A CN103741558 A CN 103741558A CN 201310751596 A CN201310751596 A CN 201310751596A CN 103741558 A CN103741558 A CN 103741558A
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- 238000000034 method Methods 0.000 title claims abstract description 31
- 239000000835 fiber Substances 0.000 claims abstract description 59
- 238000004513 sizing Methods 0.000 claims abstract description 28
- 239000002002 slurry Substances 0.000 claims description 28
- 239000003795 chemical substances by application Substances 0.000 claims description 24
- 229920001131 Pulp (paper) Polymers 0.000 claims description 23
- 239000000463 material Substances 0.000 claims description 22
- 238000001035 drying Methods 0.000 claims description 21
- 239000003292 glue Substances 0.000 claims description 16
- 238000010009 beating Methods 0.000 claims description 14
- 238000004519 manufacturing process Methods 0.000 claims description 14
- 238000004043 dyeing Methods 0.000 claims description 12
- 239000000975 dye Substances 0.000 claims description 11
- 238000002360 preparation method Methods 0.000 claims description 11
- 239000007788 liquid Substances 0.000 claims description 9
- 239000002994 raw material Substances 0.000 claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 9
- 238000012856 packing Methods 0.000 claims description 7
- 239000011347 resin Substances 0.000 claims description 7
- 229920005989 resin Polymers 0.000 claims description 7
- 230000015572 biosynthetic process Effects 0.000 claims description 6
- 238000001816 cooling Methods 0.000 claims description 6
- 230000018044 dehydration Effects 0.000 claims description 6
- 238000006297 dehydration reaction Methods 0.000 claims description 6
- 239000011121 hardwood Substances 0.000 claims description 6
- 239000011122 softwood Substances 0.000 claims description 6
- 238000010025 steaming Methods 0.000 claims description 6
- 238000005406 washing Methods 0.000 claims description 6
- 239000012744 reinforcing agent Substances 0.000 claims description 5
- 239000000126 substance Substances 0.000 claims description 5
- 229920002472 Starch Polymers 0.000 claims description 4
- 235000019698 starch Nutrition 0.000 claims description 4
- 239000008107 starch Substances 0.000 claims description 4
- 241001343274 Dichrostachys spicata Species 0.000 claims description 3
- 235000011609 Pinus massoniana Nutrition 0.000 claims description 3
- 241000018650 Pinus massoniana Species 0.000 claims description 3
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 claims description 3
- 238000005520 cutting process Methods 0.000 claims description 3
- 230000002950 deficient Effects 0.000 claims description 3
- 239000004816 latex Substances 0.000 claims description 3
- 229920000126 latex Polymers 0.000 claims description 3
- 238000007670 refining Methods 0.000 claims description 3
- 230000002787 reinforcement Effects 0.000 claims description 3
- 238000005096 rolling process Methods 0.000 claims description 3
- 238000010186 staining Methods 0.000 claims description 3
- 238000009966 trimming Methods 0.000 claims description 3
- 239000002023 wood Substances 0.000 claims description 3
- 238000007639 printing Methods 0.000 abstract description 3
- 230000000704 physical effect Effects 0.000 abstract description 2
- 206010016322 Feeling abnormal Diseases 0.000 abstract 1
- 238000010422 painting Methods 0.000 abstract 1
- 238000004537 pulping Methods 0.000 abstract 1
- 238000003860 storage Methods 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 3
- 238000012545 processing Methods 0.000 description 2
- 239000004576 sand Substances 0.000 description 2
- 238000012216 screening Methods 0.000 description 2
- 239000000725 suspension Substances 0.000 description 2
- 230000007547 defect Effects 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004049 embossing Methods 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 230000035807 sensation Effects 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
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Abstract
The invention provides a method for making archaistic art paper. The method comprises the steps of making paper, carrying out surface sizing and completing. The method has the main characteristics that fiber bundles are added into pulp. Due to the adoption of a fiber bundle adding method, the paper can be more distinctive and eye-catching, the fiber bundles show soft feeling through pulping, and through adding the fiber bundles into excellent pulp, the archaistic art paper can have the high-quality performance of modern art paper and can be endowed with a bit of charm of rough ancient paper; in addition, two forward-flow pulp-overflow circular meshes are selected as paper page formers, so that the method has the characteristic that the forming zone is relatively large, meshing can be achieved at low concentration, the tissue of copied paper is uniform, and the physical properties are good. Therefore, the archaistic art paper made by the method can be used for printing ancient books and periodicals, painting albums, packages of special and local products, business cards and the like.
Description
Technical field
The invention belongs to the speciality paper manufacture field that culture and arts are used, relate to particularly a kind of manufacture method of antique artistic paper.
Background technology
The artistic paper using all too perfection of producing in modern paper technology, paper is careful, smooth has no time, bright-colored brilliant, but blemish in an otherwise perfect thing, paper is too dull, so people carry out embossing processing to paper, suppresses three-dimensional pattern, but too regularization.So add again colorful chemical fiber or plastics sand point in dyestuff.They,, in paper random distribution, have overcome regularization, but chemical fibre is into single state, and fiber is very thin, not eye-catching, and the profile of chemical fibre and sand point is all more stiff.
Summary of the invention
In order to solve the existing defect of artistic paper using of mentioning in background technology, the invention provides a kind of manufacture method of antique artistic paper.The manufacture method of antique artistic paper of the present invention focuses on manufacturing paper with pulp of page, in the process of manufacturing paper with pulp, is equipped with the most key again with slurry.Wherein the type selecting of fibre bundle is also crucial especially with preparation.The fibre bundle that adopts separate sources in order to reach different effects, forms a series of antique artistic paper products with the paper of different color light.The concrete technical scheme of the manufacture method of antique artistic paper of the present invention is as follows:
A manufacture method for antique artistic paper, it comprises: papermaking part, top sizing and complete part, wherein
1. papermaking part
1.1 get the raw materials ready
1.1.1 auxiliary material liquid is prepared: auxiliary material comprises dyestuff, color-fixing agent, sizing agent, determining agent and reinforcing agent, accurately takes auxiliary material and in the dissolvers of appointment, dissolves stand-byly completely, and wherein dyestuff must and be incubated stored for future use with 90-95 ℃ of hot water dissolving;
1.1.2 the preparation of fibre bundle: the raw material of fibre bundle is to be selected from the not steaming fresh material in boil house in sulfate pulp-making factory (being screening reject); According to different shape requirement, select the not steaming solution thing of dogstail, needlebush, leaf wood or bast fiber as raw material; The concrete preparation flow of fibre bundle is: 1. break into pieces; 2. making beating: adopt small-sized beater to process, beating consistency 1-2wt%, making beating terminal control maximum fibre bundle by no more than 20 fibrous; 3. washing: carry out in beater; 4. dewater standby: adopt centrifugal dehydrator dehydration, after dehydration, measure fibre bundle mass dryness fraction, so that metering drops into; Preferably, for improve the colourity of fibre bundle make more eye-catching step 3. and step add the washing step after staining procedure and dyeing between 4.; Fibre bundle mass dryness fraction: 23-30wt%(fibre bundle is suspension state in water still has large water gaging to be present in the middle of fibre bundle after processed, i.e. fibre bundle mass dryness fraction=dry fibre bundle weight/(dry fibre bundle weight+water weight))
1.1.3 the preparation of wood pulp: select masson pine, this wood pulp comprises softwood pulp and hardwood pulp, softwood pulp is 1:1 with the operating weight ratio of hardwood pulp, after hydrabrusher fibration, by conical refiner, process, beating degree is 22-24 ° of SR, and wood pulp refining concentration is 3.5-4.0wt%;
1.1.4 prepare burden: batching is carried out in pond with slurry, in pond with slurry, is provided with propeller, can make wood pulp and auxiliary material fully merge, and concentration with slurry is 3-3.5wt%, and batching program is that dyeing, applying glue, reinforcement finally add fibre bundle, wherein
Dyeing: at room temperature dyeing, to wood pulp meter, dye dosage is 0-1wt%, color-fixing agent is 0-1wt%;
To wood pulp meter, other auxiliary materials (be sizing agent, determining agent and reinforcing agent) consumption is 0.2-3.0wt%, and all auxiliary material liquid must be filtered by 200 mesh sieves before entering pond with slurry;
Fibre bundle: to wood pulp meter, fibre bundle consumption is 1-10wt%;
1.2 pulp flows: flow apperach comprises consistencyregulator, flow control valve, fan pump and slurry-stablizing case, flow apperach is diluted to 0.06-0.20wt% by the slurry of step 1.1.4 gained from 3.0-3.5wt%, with constant concentration, constant slurry amount, fluidised form is sent into copy paper system stably;
1.3 paper makings: carry out in two cylinder multi-cylinder paper machines;
1.3.1 sheet forming: select the following current slurry formula cylinder that overflows, online concentration 0.06-0.2wt%;
1.3.2 squeezing: squeezing is gentle, goes out to squeeze moisture 60-65wt%;
1.3.3 dry: to use many drying cylinders (being no less than 3 drying cylinders) dry, control surface temperature of drier curve, gently dried guarantees that page two sides is poor little: according to paper feed direction, 80～85 ℃ of the surface temperatures of first drying cylinder, since second drying cylinder, the surface temperature of each drying cylinder raises gradually until the drying cylinder at middle part reaches 100～105 ℃ of maximum surface temperatures, and after this surface temperature of each drying cylinder reduces gradually, until 95 ℃ of last surface temperature of drier, becoming paper moisture is 3-6wt%;
1.3.4 cooling cylinder: use 2 cooling cylinders to carry out ornamenting to paper, make paper level and smooth, paper formation.
1.3.5 coil paper: copy into product and send next part to process with reel form;
2. top sizing
Sizing agent is water-soluble substances, and preferably sizing agent is starch, PVA or synthetic latex.Applying glue concentration is 4-6wt%, and resin added is one side 0.3-0.5g/m
2, top sizing idiographic flow: applying glue liquid is prepared, unreeled, two-sided applying glue, oven dry, rolling; Preferably, applying glue concentration is 5wt%, and resin added is one side 0.4g/m
2.
3. complete part
Roll product is processed into sheet product.
3.1 cutting systems: in paper cutter, carry out, idiographic flow comprise unreel, trimming, cut paper, paper feeding, stacking.
3.2 selections: reject defective products.
3.3 packings: pack by specification.
3.4 packings: packaged paper part is packed with clamping plate.
3.5 product warehousing.
The preparation method's of antique artistic paper of the present invention main feature is to add fibre bundle in slurry, employing adds the method for fibre bundle to make paper more distinct brilliant, and these fibre bundles present Rejoice sensation through making beating, in good paper pulp, drop into fibre bundle and can make antique artistic paper have the high-quality performance of modern art paper, make again it add the graceful bearing of rough ancient paper somewhat.In addition, the present invention selects the excessive slurry formula cylinder of two following currents to have larger shaping area as page shaper feature, and it is even that the online of energy low concentration is ferreted out formation of sheet, has good physical property.Because antique artistic paper adds fibre bundle, it and paper fibre adhesion are poor, and easy hair and powder dropping during printing, so the present invention carries out top sizing to antique artistic paper.Therefore antique artistic paper of the present invention can be used in the packing, business card of printing ancient books books and periodicals, picture album, local and special products etc.
Accompanying drawing explanation
Fig. 1 is papermaking part flow chart;
Fig. 2 is top sizing and completes part flow chart.
The specific embodiment
Below provide a specific embodiment of the present invention thereby the present invention be more fully described, but this and do not mean that the restriction to the scope of claimed claim of the present invention.
Embodiment 1
A manufacture method for antique artistic paper, it comprises: papermaking part, top sizing and complete part, wherein
1. papermaking part
1.1 get the raw materials ready
1.1.1 auxiliary material liquid is prepared: auxiliary material comprises dyestuff, color-fixing agent, sizing agent, determining agent and reinforcing agent, accurately takes auxiliary material and in the dissolvers of appointment, dissolves stand-byly completely, and wherein dyestuff must and be incubated stored for future use with 90-95 ℃ of hot water dissolving;
1.1.2 the preparation of fibre bundle: the raw material of fibre bundle is to be selected from the not steaming fresh material in boil house in sulfate pulp-making factory (being screening reject); According to different shape requirement, the not steaming fresh material of selecting dogstail, needlebush, leaf wood or strangling hide fiber is as raw material; The concrete preparation flow of fibre bundle is: 1. break into pieces; 2. making beating: adopt small-sized beater to process, beating consistency 1-2wt%, making beating terminal control maximum fibre bundle by no more than 20 fibrous; 3. washing: carry out in beater; 4. dewater standby: adopt centrifugal dehydrator dehydration, after dehydration, measure fibre bundle mass dryness fraction, so that metering drops into; Preferably, for improve the colourity of fibre bundle make more eye-catching step 3. and step add the washing step after staining procedure and dyeing between 4.; Fibre bundle mass dryness fraction: 23-30wt%(fibre bundle is suspension state in water still has large water gaging to be present in the middle of fibre bundle after processed, i.e. fibre bundle mass dryness fraction=dry fibre bundle weight/(dry fibre bundle weight+water weight))
1.1.3 the preparation of wood pulp: select masson pine, this wood pulp comprises softwood pulp and hardwood pulp, softwood pulp is 1:1 with the operating weight ratio of hardwood pulp, accurately take wood pulp and in hydrabrusher, carry out fibration, then deliver to the upper storage of 1# stock tank, when making beating, put into lower storage stock tank, again with being pumped into conical refiner, slurry after processing is delivered to the upper storage of 2# stock tank, utilize slurry position transfer valve to put into lower storage stock tank and carry out defibrination for the second time, so through the circulation of defibrination repeatedly until send the upper storage of 2# stock tank stand-by after meeting the requirements of beating degree (22-24 ° of SR), wood pulp refining concentration is 3.5-4.0wt%,
1.1.4 prepare burden: batching is carried out in pond with slurry, in pond with slurry, is provided with propeller, can make wood pulp and auxiliary material fully merge, concentration with slurry is 3-3.5wt%, batching program is that dyeing, applying glue, reinforcement finally add fibre bundle, the slurry preparing is delivered to 1# and destroy forebay to 2#, to destroy forebay more stand-by, wherein
Dyeing: at room temperature dyeing, to wood pulp meter, dye dosage is 0-1wt%, color-fixing agent is 0-1wt%;
To wood pulp meter, other auxiliary materials (be sizing agent, determining agent and reinforcing agent) consumption is 0.2-3.0wt%, and all auxiliary material liquid must be filtered by 200 mesh sieves before entering pond with slurry;
Fibre bundle: to wood pulp meter, fibre bundle consumption is 1-10wt%;
1.2 pulp flows: flow apperach comprises consistencyregulator, flow control valve, fan pump and slurry-stablizing case, wherein:
1.2.1 consistencyregulator: the slurry that 2# is destroyed to forebay dilutes and is stabilized in 1.5wt%;
1.2.2 flow control valve: the slurry of steady concentration is sent in fan pump by setting constant magnitude;
1.2.3 fan pump: the slurry of constant flow rate is diluted to the required concentration 0.06-0.20wt% of paper sheet formation net;
1.2.4 slurry-stablizing case: eliminate the powerful impulsive force of fan pump and deliver to paper sheet formation net to starch stably stream;
1.3 paper makings: carry out in two cylinder multi-cylinder paper machines;
1.3.1 sheet forming: select the following current slurry formula cylinder that overflows, online concentration 0.06-0.2wt%;
1.3.2 squeezing: squeezing is gentle, goes out to squeeze moisture 60-65wt%;
1.3.3 dry: to use many drying cylinders (being no less than 3 drying cylinders) dry, control surface temperature of drier curve, gently dried guarantees that page two sides is poor little: according to paper feed direction, 80～85 ℃ of the surface temperatures of first drying cylinder, since second drying cylinder, the surface temperature of each drying cylinder raises gradually until the drying cylinder at middle part reaches 100～105 ℃ of maximum surface temperatures, and after this surface temperature of each drying cylinder reduces gradually, until 95 ℃ of last surface temperature of drier, becoming paper moisture is 3-6wt%;
1.3.4 cooling cylinder: use 2 cooling cylinders to carry out ornamenting to paper, make paper level and smooth, paper formation.
1.3.5 coil paper: copy into product and send next part to process with reel form;
2. top sizing
Sizing agent is starch.Applying glue concentration is 4wt%, and resin added is one side 0.3g/m
2, top sizing idiographic flow: applying glue liquid is prepared, unreeled, two-sided applying glue, oven dry, rolling;
3. complete part
Roll product is processed into sheet product.
3.1 cutting systems: in paper cutter, carry out, idiographic flow comprise unreel, trimming, cut paper, paper feeding, stacking.
3.2 selections: reject defective products.
3.3 packings: pack by specification.
3.4 packings: packaged paper part is packed with clamping plate.
3.5 product warehousing.
Embodiment 2
Other parts are with embodiment 1, and difference is: in top sizing part, sizing agent is PVA.Applying glue concentration is 5wt%, and resin added is one side 0.4g/m
2.
Embodiment 3
Other parts are with embodiment 1, and difference is: in top sizing part, sizing agent is synthetic latex.Applying glue concentration is 6wt%, and resin added is one side 0.5g/m
2.
Claims (4)
1. a manufacture method for antique artistic paper, it comprises: papermaking part, top sizing and complete part, wherein
1. papermaking part
1.1 get the raw materials ready
1.1.1 auxiliary material liquid is prepared: auxiliary material comprises dyestuff, color-fixing agent, sizing agent, determining agent and reinforcing agent, accurately takes auxiliary material and in the dissolvers of appointment, dissolves stand-byly completely, and wherein dyestuff must and be incubated stored for future use with 90-95 ℃ of hot water dissolving;
1.1.2 the preparation of fibre bundle: the raw material of fibre bundle is to be selected from the not steaming fresh material in boil house in sulfate pulp-making factory; According to different shape requirement, the not steaming fresh material of selecting dogstail, needlebush, leaf wood or strangling hide fiber is as raw material; The concrete preparation flow of fibre bundle is: 1. break into pieces; 2. making beating: adopt small-sized beater to process, beating consistency 1-2wt%, making beating terminal control maximum fibre bundle by no more than 20 fibrous; 3. washing: carry out in beater; 4. dewater standby: adopt centrifugal dehydrator dehydration, after dehydration, measure fibre bundle mass dryness fraction, so that metering drops into; Fibre bundle mass dryness fraction: 23-30wt%;
1.1.3 the preparation of wood pulp: select masson pine, this wood pulp comprises softwood pulp and hardwood pulp, softwood pulp is 1:1 with the operating weight ratio of hardwood pulp, after hydrabrusher fibration, by conical refiner, process, beating degree is 22-24 ° of SR, and wood pulp refining concentration is 3.5-4.0wt%;
1.1.4 prepare burden: batching is carried out in pond with slurry, in pond with slurry, is provided with propeller, can make wood pulp and auxiliary material fully merge, and concentration with slurry is 3-3.5wt%, and batching program is the fibre bundle that dyeing, applying glue, reinforcement finally add step 1.1.2 to obtain, wherein
Dyeing: at room temperature dyeing, to wood pulp meter, dye dosage is 0-1wt%, color-fixing agent is 0-1wt%;
To wood pulp meter, removing dyestuff and color-fixing agent other supplementary product consumptions is in addition 0.2-3.0%, and all auxiliary material liquid must be filtered by 200 mesh sieves before entering pond with slurry;
Fibre bundle: to wood pulp meter, fibre bundle consumption is 1-10wt%;
1.2 pulp flows: flow apperach comprises consistencyregulator, flow control valve, fan pump and slurry-stablizing case, flow apperach is diluted to 0.06-0.20wt% by the slurry of step 1.1.4 gained from 3.0-3.5wt%, with constant concentration, constant slurry amount, fluidised form is sent into copy paper system stably;
1.3 paper makings: carry out in two cylinder multi-cylinder paper machines;
1.3.1 sheet forming: select the following current slurry formula cylinder that overflows, online concentration 0.06-0.2wt%;
1.3.2 squeezing: squeezing is gentle, goes out to squeeze moisture 60-65wt%;
1.3.3 dry: to use many drying cylinders (being no less than 3 drying cylinders) dry, control surface temperature of drier curve, gently dried guarantees that page two sides is poor little: according to paper feed direction, 80～85 ℃ of the surface temperatures of first drying cylinder, since second drying cylinder, the surface temperature of each drying cylinder raises gradually until the drying cylinder at middle part reaches 100～105 ℃ of maximum surface temperatures, and after this surface temperature of each drying cylinder reduces gradually, until 95 ℃ of last surface temperature of drier, becoming paper moisture is 3-6wt%;
1.3.4 cooling cylinder: use 2 cooling cylinders to carry out ornamenting to paper, make paper level and smooth, paper formation;
1.3.5 coil paper: copy into product and send next part to process with reel form;
2. top sizing
Sizing agent is water-soluble substances, and applying glue concentration is 4-6wt%, and resin added is one side 0.3-0.5g/m
2, top sizing idiographic flow: applying glue liquid is prepared, unreeled, two-sided applying glue, oven dry, rolling;
3. complete part
Roll product is processed into sheet product;
3.1 cutting systems: in paper cutter, carry out, idiographic flow comprise unreel, trimming, cut paper, paper feeding, stacking;
3.2 selections: reject defective products;
3.3 packings: pack by specification;
3.4 packings: packaged paper part is packed with clamping plate;
3.5 product warehousing.
2. the manufacture method of antique artistic paper according to claim 1, wherein in order to improve that 3. the colourity of fibre bundle make more eye-catching step in step 1.1.2 and step adds the washing step after staining procedure and dyeing between 4..
3. the manufacture method of antique artistic paper according to claim 1, wherein in top sizing, sizing agent is starch, PVA or synthetic latex.
4. the manufacture method of antique artistic paper according to claim 3, wherein in top sizing, applying glue concentration is 5wt%, resin added is one side 0.4g/m
2.
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Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN104746385A (en) * | 2015-02-05 | 2015-07-01 | 上海骏源实业股份有限公司 | Manufacture method of pearl double-sided color card |
| CN105821709A (en) * | 2016-05-09 | 2016-08-03 | 蚌埠昆仑彩印包装有限公司 | Dip-dyeing method for retro books |
| CN105821708A (en) * | 2016-05-09 | 2016-08-03 | 蚌埠昆仑彩印包装有限公司 | Carbonization treatment method for increasing time sense of books |
| CN106368077A (en) * | 2016-10-17 | 2017-02-01 | 长沙理工大学 | Manufacturing method for acid-free lined paper used in cultural relic protection |
| CN106436437A (en) * | 2016-10-17 | 2017-02-22 | 长沙理工大学 | Method for making acid-free lining paper for historic preservation |
| CN107059483A (en) * | 2017-04-27 | 2017-08-18 | 浙江省普瑞科技有限公司 | A kind of manufacture method of manual copperplate etching art paper |
| CN108894056A (en) * | 2018-07-17 | 2018-11-27 | 泾县道旺环保科技有限公司 | A kind of preparation method of the high-quality advertisement consumptive material paper of environmental protection |
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| CN104746385A (en) * | 2015-02-05 | 2015-07-01 | 上海骏源实业股份有限公司 | Manufacture method of pearl double-sided color card |
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| CN105821708A (en) * | 2016-05-09 | 2016-08-03 | 蚌埠昆仑彩印包装有限公司 | Carbonization treatment method for increasing time sense of books |
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