CN1231633C - Method for combining living-paper using collagenous fiber and vegetable fiber - Google Patents

Method for combining living-paper using collagenous fiber and vegetable fiber Download PDF

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Publication number
CN1231633C
CN1231633C CN 200410026132 CN200410026132A CN1231633C CN 1231633 C CN1231633 C CN 1231633C CN 200410026132 CN200410026132 CN 200410026132 CN 200410026132 A CN200410026132 A CN 200410026132A CN 1231633 C CN1231633 C CN 1231633C
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pulp
paper
slurry
mass concentration
stock tank
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Expired - Fee Related
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CN 200410026132
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Chinese (zh)
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CN1580387A (en
Inventor
侯小东
蔡祥
章川波
王志杰
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Shaanxi University of Science and Technology
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Shaanxi University of Science and Technology
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Publication of CN1231633C publication Critical patent/CN1231633C/en
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Abstract

The present invention relates to a method for combining living paper by utilizing collagen fiber and vegetable fiber. Firstly, lime leftovers are washed by water, degreased and added into a masher to be mashed, and after magnesium oxide is added, water is added for dilution and hydrolysis, and collagen fiber pulp is obtained. Secondly, hexadecyl trimethyl ammonium bromide and phosphate ester are mixed to react to generate softening agents. Thirdly, bleached needle leaf (broad leaf) wood pulp and wheat straw pulp are conditioned to make the mass concentration of the pulp reaches 1% to 4%, the bleached needle leaf (broad leaf) wood pulp, the wheat straw pulp and the collagen fiber pulp are mixed, and the softening agents are added into a pulping tank. Finally, after being mixed, the prepared pulp is delivered to a paper machine net, and wet paper is squeezed, dried, coiled and processed into finished products. Collagen fiber extracted from lime leftovers in solid waste of tanning is used as raw material for making paper, so that raw wood pulp can be saved, the dosage of paper additives is reduced, the production processes are simplified, and the pollution of paper making is reduced. Due to the content of the collagen fiber, the living paper has the advantages of favorable affinity with human bodies, high intensity and favorable flexibility.

Description

A kind of method of utilizing collagenous fibres and the compound paper for daily use of string
Technical field
The present invention relates to a kind of method of compound paper for daily use, particularly a kind of method of utilizing collagenous fibres and the compound paper for daily use of string.
Background technology
Utilizing compound this one side of sheet of copying of collagenous fibres and string, only there is Sichuan University to pay the beautiful red correlative study of once doing at present, and the patent of applying for " preparation method of collagen protein face paper ", but she extracts collagen to do raw material in the chrome leather scrap that directly adopts in the tanning waste, need take off chromium, its complex manufacturing, the cost height.
Summary of the invention
The object of the present invention is to provide a kind of chromium that need not to take off, and can reduce production process, the cost-effective method of utilizing collagenous fibres and the compound paper for daily use of string.
For achieving the above object, the method that the present invention adopts is: at first slurrying, be sent to paper machine net after the slurry mixing with system then, l Water Paper is through squeezing, dry, batch, get product after the processing, be characterized in, said slurrying comprises: at first the graywall leftover bits and pieces in the solid leather wastes is washed, conventional degreasing agent degreasing with graywall weight 1%-5%, be cut into 2mm * 2mm to 5mm * 5mm fritter, add in the bruisher, smash to pieces 0.5-2 minute * 2-4 time, dilute with quality multiple 50-100 water doubly behind the magnesia of adding graywall weight 5%-10%, at 45 ℃ of-60 ℃ of following hydrolysis 1-3 hours, be dispersed in the hydrolyzate with refiner, promptly get collagen fiber pulp; Softex kw and the mass concentration that with mass concentration is 20%-40% is that the phosphate of 20%-40% mixes by mass ratio at 1: 1, normal-temperature reaction 30-60 minute, makes softener; To bleach pin wood and/or wealthy wooden leaf wood pulp, Straw Pulp then respectively through the hydrabrusher pulping and in stock tank, size mixing respectively and make the mass concentration of slurries reach 1%-4%, and behind paste mill grinding, enter respectively and kowtow the back stock tank; Bleaching pin wood and/or wealthy wooden leaf wood pulp with mass percent 15%-30%, the Straw Pulp of 50%-78% and the collagen fiber pulp of 5%-20% mix to be placed in the same stock proportioner joins slurry, join behind the slurry through joining stock tank and machine chest, adding mass percent in machine chest is the softener of 0.5%-1.0%.
Because the present invention can save former wood pulp consumption with the collagenous fibres that the graywall leftover bits and pieces in the solid leather wastes extracts as the paper grade (stock) raw material, reduce the use of paper making additive, and simplified production process, reduce paper-making pollution.Owing to contain collagenous fibres, this type of paper for daily use and human body affinity are good, the intensity height, and flexibility is good.
The specific embodiment
Embodiment 1: at first the graywall leftover bits and pieces in the solid leather wastes is washed, conventional degreasing agent OP-10 degreasing with graywall weight 1%, be cut into 2mm * 2mmm fritter, add in the bruisher, smash to pieces 2 minutes * 2 times, the water with 50 times of quality multiples behind adding graywall weight 5% magnesia diluted, 45 ℃ of following hydrolysis 3 hours, being dispersed to refiner does not have bulky grain in the hydrolyzate, promptly get collagen fiber pulp; Be 20% softex kw with mass concentration with mass concentration be that 20% phosphate mixes by mass ratio at 1: 1, normal-temperature reaction 60 minutes makes softener; To bleach pin wood and/or wealthy wooden leaf wood pulp, Straw Pulp then respectively through the hydrabrusher pulping and in stock tank, size mixing respectively and make the mass concentration of slurries reach 4%, and behind paste mill grinding, enter respectively and kowtow the back stock tank; The collagen fiber pulp of the bleaching pin of mass percent 15% wood and/or wealthy wooden leaf wood pulp, 78% Straw Pulp and 6.5% mixed to be placed in the same stock proportioner join slurry, join behind the slurry through joining stock tank and machine chest, in machine chest, add mass percent and be 0.5% softener; At last the slurry for preparing is sent to web part of paper machine, l Water Paper gets product through press section, drying section, reeling end, after adding the Ministry of worker.
Embodiment 2: at first the graywall leftover bits and pieces in the solid leather wastes is washed, conventional degreasing agent peregal degreasing with graywall weight 5%, be cut into 5mm * 5mm fritter, add in the bruisher, smash to pieces 0.5 minute * 3 times, the water with 80 times of quality multiples behind adding graywall weight 7% magnesia diluted, 55 ℃ of following hydrolysis 2 hours, being dispersed to refiner does not have bulky grain in the hydrolyzate, promptly get collagen fiber pulp; Be 40% softex kw with mass concentration with mass concentration be that 40% phosphate mixes by mass ratio at 1: 1, normal-temperature reaction 45 minutes makes softener; To bleach pin wood and/or wealthy wooden leaf wood pulp, Straw Pulp then respectively through the hydrabrusher pulping and in stock tank, size mixing respectively and make the mass concentration of slurries reach 3%, and behind paste mill grinding, enter respectively and kowtow the back stock tank; The collagen fiber pulp of the bleaching pin of mass percent 30% wood and/or wealthy wooden leaf wood pulp, 50% Straw Pulp and 19% mixed to be placed in the same stock proportioner join slurry, join behind the slurry through joining stock tank and machine chest, in machine chest, add mass percent and be 1.0% softener; At last the slurry for preparing is sent to web part of paper machine, l Water Paper gets product through press section, drying section, reeling end, after adding the Ministry of worker.
Embodiment 3: at first the graywall leftover bits and pieces in the solid leather wastes is washed, conventional degreasing agent peregal degreasing with graywall weight 3%, be cut into 2mm * 3mm fritter, add in the bruisher, smash to pieces 1 minute * 4 times, the water with 100 times of quality multiples behind adding graywall weight 10% magnesia diluted, 60 ℃ of following hydrolysis 1.5 hours, being dispersed to refiner does not have bulky grain in the hydrolyzate, promptly get collagen fiber pulp; Be 35% softex kw with mass concentration with mass concentration be that 35% phosphate mixes by mass ratio at 1: 1, normal-temperature reaction 30 minutes makes softener; To bleach pin wood and/or wealthy wooden leaf wood pulp, Straw Pulp then respectively through the hydrabrusher pulping and in stock tank, size mixing respectively and make the mass concentration of slurries reach 1%, and behind paste mill grinding, enter respectively and kowtow the back stock tank; The collagen fiber pulp of the bleaching pin of mass percent 25% wood and/or wealthy wooden leaf wood pulp, 69.2% Straw Pulp and 5% mixed to be placed in the same stock proportioner join slurry, join behind the slurry through joining stock tank and machine chest, in machine chest, add mass percent and be 0.8% softener; At last the slurry for preparing is sent to web part of paper machine, l Water Paper gets product through press section, drying section, reeling end, after adding the Ministry of worker.
Embodiment 4: at first the graywall leftover bits and pieces in the solid leather wastes is washed, conventional degreasing agent OP-10 degreasing with graywall weight 4%, be cut into 5mm * 4mm fritter, add in the bruisher, smash to pieces 1.6 minutes * 2 times, the water with 90 times of quality multiples behind adding graywall weight 6% magnesia diluted, 50 ℃ of following hydrolysis 2.5 hours, being dispersed to refiner does not have bulky grain in the hydrolyzate, promptly get collagen fiber pulp; Be 25% softex kw with mass concentration with mass concentration be that 25% phosphate mixes by mass ratio at 1: 1, normal-temperature reaction 50 minutes makes softener; To bleach pin wood and/or wealthy wooden leaf wood pulp, Straw Pulp then respectively through the hydrabrusher pulping and in stock tank, size mixing respectively and make the mass concentration of slurries reach 2%, and behind paste mill grinding, enter respectively and kowtow the back stock tank; The collagen fiber pulp of the bleaching pin of mass percent 20% wood and/or wealthy wooden leaf wood pulp, 59% Straw Pulp and 20% mixed to be placed in the same stock proportioner join slurry, join behind the slurry through joining stock tank and machine chest, in machine chest, add mass percent and be 1% softener; At last the slurry for preparing is sent to web part of paper machine, l Water Paper gets product through press section, drying section, reeling end, after adding the Ministry of worker.
Embodiment 5: at first the graywall leftover bits and pieces in the solid leather wastes is washed, conventional degreasing agent OP-10 degreasing with graywall weight 2%, be cut into 2mm * 5mm fritter, add in the bruisher, smash to pieces 1.3 minutes * 3 times, the water with 75 times of quality multiples behind adding graywall weight 8% magnesia diluted, 53 ℃ of following hydrolysis 1 hour, being dispersed to refiner does not have bulky grain in the hydrolyzate, promptly get collagen fiber pulp; Be 30% softex kw with mass concentration with mass concentration be that 30% phosphate mixes by mass ratio at 1: 1, normal-temperature reaction 40 minutes makes softener; To bleach pin wood and/or wealthy wooden leaf wood pulp, Straw Pulp then respectively through the hydrabrusher pulping and in stock tank, size mixing respectively and make the mass concentration of slurries reach 2.6%, and behind paste mill grinding, enter respectively and kowtow the back stock tank; The collagen fiber pulp of the bleaching pin of mass percent 28% wood and/or wealthy wooden leaf wood pulp, 61.5% Straw Pulp and 10% mixed to be placed in the same stock proportioner join slurry, join behind the slurry through joining stock tank and machine chest, in machine chest, add mass percent and be 0.5% softener; At last the slurry for preparing is sent to web part of paper machine, l Water Paper gets product through press section, drying section, reeling end, after adding the Ministry of worker.

Claims (6)

1, a kind of method of utilizing collagenous fibres and the compound paper for daily use of string, at first slurrying is sent to paper machine net after slurry that then will system mixes, l Water Paper through squeezing, dry, get product after batching, processing, it is characterized in that:
Said slurrying comprises
1) at first the graywall leftover bits and pieces in the solid leather wastes is washed, conventional degreasing agent degreasing with graywall weight 1%-5%, be cut into 2mm * 2mm to 5mm * 5mm fritter, add in the bruisher, smash to pieces 0.5-2 minute * 2-4 time, dilute with quality multiple 50-100 water doubly behind the magnesia of adding graywall weight 5%-10%, at 45 ℃ of-60 ℃ of following hydrolysis 1-3 hours, be dispersed in the hydrolyzate with refiner, promptly get collagen fiber pulp;
2) be that softex kw and the mass concentration of 20%-40% is that the phosphate of 20%-40% mixes by mass ratio at 1: 1 with mass concentration, normal-temperature reaction 30-60 minute, make softener;
3) will bleach pin wood and/or wealthy wooden leaf wood pulp, Straw Pulp then respectively through the hydrabrusher pulping and in stock tank, size mixing respectively and make the mass concentration of slurries reach 1%-4%, and behind paste mill grinding, enter respectively and kowtow the back stock tank;
4) the wooden and/or wealthy wooden leaf wood pulp with the bleaching pin of mass percent 15%-30%, the Straw Pulp of 50%-78% and the collagen fiber pulp of 5%-20% mix to be placed in the same stock proportioner joins slurry, join behind the slurry through joining stock tank and machine chest, adding mass percent in machine chest is the softener of 0.5%-1.0%.
2, the method for utilizing collagenous fibres and the compound paper for daily use of string according to claim 1, it is characterized in that: at first the graywall leftover bits and pieces in the solid leather wastes is washed, conventional degreasing agent OP-10 degreasing with graywall weight 1%, be cut into 2mm * 2mmm fritter, add in the bruisher, smash to pieces 2 minutes * 2 times, use the water of 50 times of quality multiples to dilute after adding graywall weight 5% magnesia, 45 ℃ of following hydrolysis 3 hours, being dispersed to refiner does not have bulky grain in the hydrolyzate, promptly get collagen fiber pulp; Be 20% softex kw with mass concentration with mass concentration be that 20% phosphate mixes by mass ratio at 1: 1, normal-temperature reaction 60 minutes makes softener; To bleach pin wood and/or wealthy wooden leaf wood pulp, Straw Pulp then respectively through the hydrabrusher pulping and in stock tank, size mixing respectively and make the mass concentration of slurries reach 4%, and behind paste mill grinding, enter respectively and kowtow the back stock tank; The collagen fiber pulp of the bleaching pin of mass percent 15% wood and/or wealthy wooden leaf wood pulp, 78% Straw Pulp and 6.5% mixed to be placed in the same stock proportioner join slurry, join behind the slurry through joining stock tank and machine chest, in machine chest, add mass percent and be 0.5% softener; At last the slurry for preparing is sent to web part of paper machine, l Water Paper gets product through press section, drying section, reeling end, after adding the Ministry of worker.
3, the method for utilizing collagenous fibres and the compound paper for daily use of string according to claim 1, it is characterized in that: at first the graywall leftover bits and pieces in the solid leather wastes is washed, conventional degreasing agent peregal degreasing with graywall weight 5%, be cut into 5mm * 5mm fritter, add in the bruisher, smash to pieces 0.5 minute * 3 times, use the water of 80 times of quality multiples to dilute after adding graywall weight 7% magnesia, 55 ℃ of following hydrolysis 2 hours, being dispersed to refiner does not have bulky grain in the hydrolyzate, promptly get collagen fiber pulp; Be 40% softex kw with mass concentration with mass concentration be that 40% phosphate mixes by mass ratio at 1: 1, normal-temperature reaction 45 minutes makes softener; To bleach pin wood and/or wealthy wooden leaf wood pulp, Straw Pulp then respectively through the hydrabrusher pulping and in stock tank, size mixing respectively and make the mass concentration of slurries reach 3%, and behind paste mill grinding, enter respectively and kowtow the back stock tank; The collagen fiber pulp of the bleaching pin of mass percent 30% wood and/or wealthy wooden leaf wood pulp, 50% Straw Pulp and 19% mixed to be placed in the same stock proportioner join slurry, join behind the slurry through joining stock tank and machine chest, in machine chest, add mass percent and be 1.0% softener; At last the slurry for preparing is sent to web part of paper machine, l Water Paper gets product through press section, drying section, reeling end, after adding the Ministry of worker.
4, the method for utilizing collagenous fibres and the compound paper for daily use of string according to claim 1, it is characterized in that: at first the graywall leftover bits and pieces in the solid leather wastes is washed, conventional degreasing agent peregal degreasing with graywall weight 3%, be cut into 2mm * 3mm fritter, add in the bruisher, smash to pieces 1 minute * 4 times, use the water of 100 times of quality multiples to dilute after adding graywall weight 10% magnesia, 60 ℃ of following hydrolysis 1.5 hours, being dispersed to refiner does not have bulky grain in the hydrolyzate, promptly get collagen fiber pulp; Be 35% softex kw with mass concentration with mass concentration be that 35% phosphate mixes by mass ratio at 1: 1, normal-temperature reaction 30 minutes makes softener; To bleach pin wood and/or wealthy wooden leaf wood pulp, Straw Pulp then respectively through the hydrabrusher pulping and in stock tank, size mixing respectively and make the mass concentration of slurries reach 1%, and behind paste mill grinding, enter respectively and kowtow the back stock tank; The collagen fiber pulp of the bleaching pin of mass percent 25% wood and/or wealthy wooden leaf wood pulp, 69.2% Straw Pulp and 5% mixed to be placed in the same stock proportioner join slurry, join behind the slurry through joining stock tank and machine chest, in machine chest, add mass percent and be 0.8% softener; At last the slurry for preparing is sent to web part of paper machine, l Water Paper gets product through press section, drying section, reeling end, after adding the Ministry of worker.
5, the method for utilizing collagenous fibres and the compound paper for daily use of string according to claim 1, it is characterized in that: at first the graywall leftover bits and pieces in the solid leather wastes is washed, conventional degreasing agent OP-10 degreasing with graywall weight 4%, be cut into 5mm * 4mm fritter, add in the bruisher, smash to pieces 1.6 minutes * 2 times, use the water of 90 times of quality multiples to dilute after adding graywall weight 6% magnesia, 50 ℃ of following hydrolysis 2.5 hours, being dispersed to refiner does not have bulky grain in the hydrolyzate, promptly get collagen fiber pulp; Be 25% softex kw with mass concentration with mass concentration be that 25% phosphate mixes by mass ratio at 1: 1, normal-temperature reaction 50 minutes makes softener; To bleach pin wood and/or wealthy wooden leaf wood pulp, Straw Pulp then respectively through the hydrabrusher pulping and in stock tank, size mixing respectively and make the mass concentration of slurries reach 2%, and behind paste mill grinding, enter respectively and kowtow the back stock tank; The collagen fiber pulp of the bleaching pin of mass percent 20% wood and/or wealthy wooden leaf wood pulp, 59% Straw Pulp and 20% mixed to be placed in the same stock proportioner join slurry, join behind the slurry through joining stock tank and machine chest, in machine chest, add mass percent and be 1% softener; At last the slurry for preparing is sent to web part of paper machine, l Water Paper gets product through press section, drying section, reeling end, after adding the Ministry of worker.
6, the method for utilizing collagenous fibres and the compound paper for daily use of string according to claim 1, it is characterized in that: at first the graywall leftover bits and pieces in the solid leather wastes is washed, conventional degreasing agent OP-10 degreasing with graywall weight 2%, be cut into 2mm * 5mm fritter, add in the bruisher, smash to pieces 1.3 minutes * 3 times, use the water of 75 times of quality multiples to dilute after adding graywall weight 8% magnesia, 53 ℃ of following hydrolysis 1 hour, being dispersed to refiner does not have bulky grain in the hydrolyzate, promptly get collagen fiber pulp; Be 30% softex kw with mass concentration with mass concentration be that 30% phosphate mixes by mass ratio at 1: 1, normal-temperature reaction 40 minutes makes softener; To bleach pin wood and/or wealthy wooden leaf wood pulp, Straw Pulp then respectively through the hydrabrusher pulping and in stock tank, size mixing respectively and make the mass concentration of slurries reach 2.6%, and behind paste mill grinding, enter respectively and kowtow the back stock tank; The collagen fiber pulp of the bleaching pin of mass percent 28% wood and/or wealthy wooden leaf wood pulp, 61.5% Straw Pulp and 10% mixed to be placed in the same stock proportioner join slurry, join behind the slurry through joining stock tank and machine chest, in machine chest, add mass percent and be 0.5% softener; At last the slurry for preparing is sent to web part of paper machine, l Water Paper gets product through press section, drying section, reeling end, after adding the Ministry of worker.
CN 200410026132 2004-05-17 2004-05-17 Method for combining living-paper using collagenous fiber and vegetable fiber Expired - Fee Related CN1231633C (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101265675B (en) * 2007-03-12 2011-12-07 福建农林大学 Environment friendly-type amortizing packaging material and method for making same

Families Citing this family (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100336971C (en) * 2005-07-18 2007-09-12 广东省造纸研究所 Paper maked from pulp of animal and plant fiber and its preparation technology
CN101760987B (en) * 2008-11-28 2012-10-03 山东福荫造纸环保科技有限公司 High-air-permeability mixed pulp and household paper made thereof
EP2854735B1 (en) 2012-05-24 2019-02-13 Takeda AS Apparatus and process for providing a coiled collagen carrier
CN102877379A (en) * 2012-09-27 2013-01-16 吉林大学 Preparation method of food paper packaging material containing rana chensinensis skin micropowder
CN106256953B (en) * 2016-07-15 2017-09-29 东莞顺裕纸业有限公司 A kind of leather waste matches somebody with somebody the method that OCC waste paper produces high-strength corrugating medium of copying
CN115652694B (en) * 2022-12-14 2023-04-07 山东海奥斯生物科技股份有限公司 Preparation process of collagen fiber composite paper

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101265675B (en) * 2007-03-12 2011-12-07 福建农林大学 Environment friendly-type amortizing packaging material and method for making same

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