CN102677501B - Material preparation process suitable for preparing dissolving pulp by modifying natural color unblenched needlebush and broadleaf wood composite paper pulp - Google Patents
Material preparation process suitable for preparing dissolving pulp by modifying natural color unblenched needlebush and broadleaf wood composite paper pulp Download PDFInfo
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- CN102677501B CN102677501B CN201210170737.9A CN201210170737A CN102677501B CN 102677501 B CN102677501 B CN 102677501B CN 201210170737 A CN201210170737 A CN 201210170737A CN 102677501 B CN102677501 B CN 102677501B
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Abstract
The invention discloses a material preparation process suitable for preparing dissolving pulp by modifying natural color unblenched needlebush and broadleaf wood composite paper pulp. The process comprises the processes of preparing raw materials, dispersing, slicing, impregnating and the like. Aiming at the natural color unblenched needlebush and broadleaf wood composite paper pulp raw materials, the special process steps and process control parameters thereof are adopted; the aims of improving the quality of the finished product, saving energy and reducing emission can be fulfilled; the content of alpha cellulose, the yield and the whiteness of the finished product are improved; the ash content is reduced; the material preparation process is beneficial to the cost control of chemical industrial liquid medicine; a subsequent cooking and heating curve is stable; the concentration is uniformly reduced; and the prepared semi-finished product can be suitable for various cooking modes and has wide application range.
Description
Technical field
The present invention relates to a kind of material preparation technology for the preparation of dissolving pulp, more particularly, the present invention relates to and be a kind ofly applicable to the material preparation technology that true qualities do not float needlebush, dissolving pulp is prepared in the modification of leaf wood using compound pulp, belong to viscose fiber raw material-pulp preparing technical field.
Background technology
Along with the development of China's viscose industry, the raw materials for production of Cotton Pulp as viscose are prepared mainly with cotton linter by domestic enterprise.It is high that cotton linter has content of cellulose, fiber is long, intensity good, can be used for the advantage of producing multiple product, but the resource of raw material cotton linter is day by day shortage by the restriction of cultivated area and growth cycle, because the outstanding of ground contradiction striven by grain and cotton, the impact of long period and the ecological balance thereof, seriously constrains the development of China's viscose industry.Wood, bamboo dissolved pulp are used for viscose glue and produce by existing enterprise for this reason, but the price of import dissolving pulp is high, fluctuation large, have impact on the normal operation of enterprise.
Prepare dissolving pulp can adopt bleaching bamboo and wood paper pulp or not float true qualities bamboo and wood paper pulp, its preparation process comprise select materials, get the raw materials ready, boiling, bleaching, operation of washing and to manufacture paper with pulp etc., wherein select materials, source part that procedure for preparation is whole technique, the design of its technological process, the selection of technological parameter, can affect the carrying out of subsequent technique and the quality of final product to a great extent.
It is 200710050472.8 that State Intellectual Property Office discloses an application number in 2008.3.26, name is called " paper-making-stage bamboo wood pulp plate denaturalization producing technique ", this invention provides a kind of modified production process of papermaking level bamboo wood-pulp board, solves that existing sex change wood pulps production technology also exists that wood-pulp board dipping is uneven, hemicellulose stripping slow, falls poly-difficulty, half steaming is even, boiling method is single, method for bleaching is single and the deficiency such as condition is violent.Step comprises wood-pulp board paging, alkali steeping, squeezes, discongests dispersion, boiling, washing, removal of impurities, bleaching, secondary washing, copies the dregs of rice; Wherein, described wood-pulp board paging, alkali steeping, squeezing discongest be by papermaking level bamboo wood-pulp board through paging device one by one separately after, sending into concentration is in the alkali steeping bucket of 6% ~ 18%, and flooding into concentration is after the slurry congee of 2.5% ~ 5%, is pumped into squeezer extrudes and discongest loosen collagen fibre with slurry congee.Adopt the present invention to make the quality of dissolving grade viscose wood pulps more excellent, more stable, raw material choose is wider.
It is 201110049038.4 that State Intellectual Property Office discloses an application number in 2011.09.14, name is called " compound pulp of a kind of paper pulp and cotton linter and preparation method thereof ", the invention provides a kind of method of paper pulp and cotton linter compound Making viscose fiber pulp, employing the method can by bamboo, wood, fiber crops, the special performance of the fibers such as bagasse combines with cotton excellent properties, can be other two or more paper pulp or bamboo arbitrarily, wood, cotton, fiber crops wait the boiling of raw material independence, after series of process process, dissolving pulp is prepared in bleaching section compound.The kind of the present invention's paper pulp used is not subject to the restriction of production method and raw material, it can be natural color pulp, also can be bleached pulp, by alkali steeping process, reduce pulp cooking difficulty, obtained dissolving pulp content of alphacellulose is high, maceration extract reusable edible, adopt in the method pulping process and pollute less, the recycle of alkali lye can be realized.
In above-mentioned two sections of documents select materials and material preparation technology mainly contain following problem:
1, wayward in producing, semi-manufactured goods quality is uneven, and end product quality is unstable; Greatly, cost is high for chemical industry soup, energy resource consumption;
2, in alkali steeping, fiber pervasion is uneven, and the stripping of non-fiber impurity is few, falls poly-unstable, uneven.
It is 201110217636.8 that State Intellectual Property Office discloses an application number in 2011.12.14, name is called " production process for modified papermaking grade wood pulp ", a kind of production process for modified papermaking grade wood pulp of this disclosure of the invention, it comprises suddenly following: (1) gets the raw materials ready, by papermaking grade wood pulp plate conveying feeding hydrabrusher, discongest dispersion through alkali spray and agitator, send into after squeezer carries out extrusion dehydration, feeding rotary spherical digester; (2) boiling, the slurry flooded enters rotary spherical digester and carries out boiling, adds caustic soda; (3) chlorination, carries out chlorination by boiling disposed slurry, adds hydrochloric acid, liquid chlorine, caustic soda; (4) bleach, the slurry after chlorination is sent into Bellmer and bleaches; (5) acid treatment, adds hydrochloric acid and carries out acid treatment, enters drift pond, manufacture paper with pulp, be packaged as wood pulps through paper machine through spray.The present invention fully discongests dispersion by utilizing hydrabrusher to slurry, makes xylon and soda-dip more even, increases substantially cooking homogeneities.By cooking process, non-cellulosic impurity content can be reduced, reduce the cotton fiber degree of polymerization.By chloride process, part foreign pigment can be removed, the fine content of corresponding raising first.By bleaching process, cellulose whiteness can be improved, and maintenance falls poly-, remove impurity.By acid treatment, can ash, irony be removed, improve reactivity worth.The modified papermaking grade wood pulp adopting the present invention to produce can reach the index request of dissolving pulp, meets the production requirement of viscose.
Selecting materials in above-mentioned document, the semi-finished product that material preparation technology is produced can only be applicable to minority boiling mode, have significant limitation, and labour intensity is large, cost is high, and single pulp property is dull, can not possess simultaneously antibacterial, antibacterial, be easy to the functions such as nursing, health environment-friendly.
It is 200910263443.9 that State Intellectual Property Office discloses an application number in 2010.9.1, the patent of invention that name is called " method of preparing wood dissolving pulp by modifying true color unbleached wood slurry ", the production method that this disclosure of the invention is a kind of to be utilized true qualities not float wood pulp modification to prepare wooden dissolving pulp, solves the drawback that alkali refining method preparing product reactivity worth is not good.Step does not float true qualities wood pulp after discongesting, double screwy roller grinded-paste machine is sent into after thickening, dehydration is continued in machine, and add liquid, slurry completes in machine that continuation concentrates, rubs, liquid mixed processes, then by slurry transferring to boiling vessel, enter the subsequent handling comprising washing, bleach after boiling, until manufacture paper with pulp.The present invention reduces preparation cost, improves the quality of products, and expands resource provisioning source.The wood pulps of this law manufacture is higher except having alpha-cellulose content, has more good reactivity worth, is applicable to long or short filament fiber.
Production in technique scheme is wayward, semi-manufactured goods quality is uneven, end product quality is unstable, in alkali steeping, fiber pervasion is uneven, the stripping of non-fiber impurity is few, fall poly-unstable, uneven, and single pulp property is dull, can not possess simultaneously antibacterial, antibacterial, be easy to the functions such as nursing, health environment-friendly.
Summary of the invention
The present invention is intended to solve in above-mentioned prior art, pulp by modifying true color unbleached is the material preparation technology of dissolving pulp, semi-finished product and end product dissolving pulp of low quality, cost is high, be only applicable to minority boiling mode, and be not suitable for the problem of not floating using compound pulp with true qualities, the material preparation technology that a kind of true qualities do not float needlebush, dissolving pulp is prepared in the modification of leaf wood using compound pulp is provided.The present invention can improve get the raw materials ready after the quality of semi-finished product and last dissolving pulp finished product, reduce costs, its semi-finished product are applicable to all boiling modes.
In order to realize foregoing invention object, its concrete technical scheme is:
True qualities do not float the material preparation technology that dissolving pulp is prepared in needlebush and the modification of leaf wood using compound pulp, it is characterized in that: comprise following processing step:
A, raw material prepare
Not floating needlebush paper pulp and true qualities according to true qualities, not float leaf wood paper pulp gross weight with the ratio of boiling vessel volume be 100 ~ 250kg:1m
3get the raw materials ready, choose true qualities and do not float needlebush paper pulp and true qualities do not float leaf wood paper pulp;
True qualities described in step do not float needlebush paper pulp and true qualities, and not float leaf wood paper pulp be content of alphacellulose >=88%, the degree of polymerization 700 ~ 1500DP, content of ashes≤0.90%.
It is content of alphacellulose 88 ~ 94% that above-mentioned true qualities do not float needlebush paper pulp, the degree of polymerization 1000 ~ 1400DP, content of ashes 0.2 ~ 0.8%; It is content of alphacellulose 90 ~ 96% that described true qualities do not float leaf wood paper pulp, the degree of polymerization 1000 ~ 1400DP, content of ashes 0.2 ~ 0.8%.
It is that true qualities do not float needlebush paper pulp that true qualities described in step do not float the combined weight ratio that needlebush paper pulp and true qualities do not float leaf wood paper pulp: true qualities do not float leaf wood paper pulp=4:6 ~ 6:4.
B, dispersion and pulping
True qualities are not floated needlebush paper pulp not float leaf wood paper pulp dispersion treatment with true qualities and become pulp board, then true qualities are not floated needlebush pulp board and true qualities not float leaf wood pulp board and mix with water, carry out pulping process, obtain the mixture that true qualities do not float needlebush paper pulp, true qualities do not float leaf wood paper pulp and water and namely starch congee, carry out the de-liquid process of next step squeezing again, the slurry concentration of the described slurry congee obtained through pulping process is 3 ~ 5%;
Slurry concentration is this area technical term, refers to that true qualities do not float the percentage that needlebush paper pulp and true qualities do not float mixture (namely the starching congee) weight that fiber over dry gross weight and true qualities in leaf wood paper pulp do not float needlebush paper pulp, true qualities do not float leaf wood paper pulp and water.
Described needlebush pulp board and the true qualities of true qualities not floated are not floated leaf wood pulp board and are mixed with water in stepb, carry out pulping process and refer to that true qualities not being floated needlebush pulp board and true qualities does not float leaf wood pulp board and be delivered to hydrabrusher with the transporting velocity of 85 ~ 200kg/min, add water simultaneously and carry out pulping process, and the discharging speed after pulping process is 2.8 ~ 6m
3/ min.
The above-mentioned speed adding water is 2.8 ~ 6m
3/ min.
The electric machine frequency of above-mentioned hydrabrusher is 30 ~ 60Hz.
C, the de-liquid of squeezing
Undertaken squeezing de-liquid process by through the slurry congee of dispersion with pulping, the de-liquid of squeezing is 20 ~ 35% to slurry congee mass dryness fraction;
Mass dryness fraction is this area technical term, refers to the percentage of the weight of all liq in the liquid weight sloughed and the mixture (namely starching congee) that true qualities do not float needlebush paper pulp, true qualities do not float leaf wood paper pulp and water.
The Stress control that squeezing described in step C takes off liquid is 0.4 ~ 0.5MPa.
D, dipping
Slurry congee through de-liquid is mixed with sodium hydroxide solution, carry out impregnation process, obtain the mixture that true qualities do not float needlebush paper pulp, true qualities do not float leaf wood paper pulp and sodium hydroxide solution, control liquor ratio is 1:3 ~ 4, and it is 17 ~ 22% that sodium hydrate solid weight and true qualities do not float the percentage that needlebush paper pulp and true qualities do not float fiber over dry gross weight in leaf wood paper pulp;
Liquor ratio (or being called bath raio) is this area technical term, refers to that true qualities do not float the ratio that needlebush paper pulp and true qualities do not float fiber over dry gross weight and sodium hydroxide solution volume in leaf wood paper pulp.
The alkalinity that true qualities do not float needlebush paper pulp, true qualities do not float the mixture of leaf wood paper pulp and sodium hydroxide solution described is in step D 3.0 ~ 5.1%, and methylcellulose content is 20 ~ 25%.
E, flooded after enter boiling vessel and carry out next step cooking process.
This technique device therefor:
1, the boiling vessel in steps A and step e is rotary spherical digester, steamer or continuous steamer, and continuous steamer comprises horizontal continuous cooking device or tower continuous steamer;
2, being delivered to hydrabrusher in step B is adopt belt conveyor, and pulping complete after slurry congee by delivery pump discharging, be delivered to the de-liquid equipment of squeezing;
3, it is squeezer or acroll press washer that the squeezing in step D takes off liquid equipment;
4, the impregnating equipment in step C is treating tank, gives dipping machine or double helix kneading machine;
The said equipment is this area conventional equipment.
The Advantageous Effects that the present invention brings:
1, the viscose produced of single paper pulp pulp, performance is dull, performance is different, have their own characteristics each, as deflection, antibacterial bacteriostatic function, fiber soft feeling, deodorization, gas permeability, coloring, least, the humidity absorption and release of skin affinity, fiber, but using compound pulp of the present invention can possess above-mentioned multifrequency nature simultaneously;
2, true qualities do not float needlebush, true qualities do not float leaf wood using compound pulp fibre morphology evenly, finished product first fibre is higher containing height, viscous consistency, reactivity worth, there is antibacterial bacteriostatic function, fiber soft feeling be good, deodorization is good;
3, true qualities are not floated needlebush pulp board and true qualities and are not floated leaf wood pulp board and send in hydrabrusher and carry out the process of water pulping by the present invention, what add when pulping is water, follow-up employing double helix kneader is coordinated to carry out impregnation process, the use amount of NaOH can be reduced, save cost, and soda recovery unit and salkali waste process, tapping equipment can be saved, energy-saving and emission-reduction, reduce environmental protection pressure;
4, material preparation technology process of the present invention is easy to control, and the semi-manufactured goods quality before boiling is even, and the ash content of end product is easy to control, and can save chemical industry soup well, shortens washing flow, saves water, electric consumption, reduces cost and the pollution to environment;
5, material preparation technology equipment investment of the present invention is few, and cost is low, and productivity ratio is high, and single machine production ability is large, and control stability is good;
6, the present invention is by the optimization of material preparation technology parameter system, reaches following effect:
(1) owing to making optimization to inventory and digesting apparatus volume ratio, the semi-finished product that making gets the raw materials ready obtains can load digesting apparatus well, medium density, be conducive to semi-finished product boiling where varus boilingly to rise, evenly soak into, produce easy to control, improve cooking quality, be conducive to evenly soaking into and to fiber homogeneous heating, having taken into account utilization rate and the economy of equipment simultaneously of liquid;
(2) using compound pulp modification of the prior art or sex change are prepared in the technique of dissolving pulp, its production of getting the raw materials ready is wayward, cause the poor quality of final product, and the present invention is by optimizing the standard of selecting materials, whole dissolving pulp production process is made to be easy to control, end product quality is stablized, and content of alphacellulose is high, yield is high;
(3) adopt raw material pulping of the present invention, dipping and squeezing to take off liquid technological parameter system, paper pulp fiber soaks into evenly, and non-cellulosic impurity stripping is many, can remove most of non-cellulosic impurity like this, falls poly-stable, is conducive to the cost control of chemical industry soup;
(4) raw material pulping of the present invention, dipping and squeezing is adopted to take off liquid technological parameter system, be conducive to fiber fully to soak into, make follow-up boiling heating curve steady, fall evenly poly-, obtained semi-finished product are applicable to and various boiling mode, applied range, solve existing true qualities and do not float the large problem of paper pulp following bleaching pressure, finally obtained viscose pulp lighter color, alleviates bleaching pressure, little to the damage of first fibre, environmental protection pressure is little;
(5) adopt technique and the parameter of impregnation steps of the present invention, evenly, every root fiber is all soaked into by alkali lye dipping, with fiber after NaOH hybrid infusion containing alkali >=3.0%, and first fibre >=20.0%, be conducive to boiling and fall evenly poly-, non-cellulosic impurity stripping is many;
(6) adopt pulping of the present invention, dipping and squeezing to take off technique and the parameter of liquid step, fiber can be made to occur expanded, longitudinal contraction, diameter increases, and can improve the chemical activity of fiber, its result can make fiber moisture absorption, and chemical reaction ability and dye uptake strengthen; The a large amount of stripping of non-cellulosic impurity can also be made, in and the organic acid that produces in digestion process, saponification, grease, wax etc. contained by emulsification fiber, with reactions such as lignin, in addition, after getting the raw materials ready, mass dryness fraction is moderate, can reduce liquor ratio, and liquid is mixed;
(7) adopt the transporting velocity parameter system of conveying equipment of the present invention, the dynamic equilibrium that efficiency and quality in integrated artistic flow process can be made to reach best, farthest can avoid the waste of material, liquid;
7, the present invention is directed to true qualities and do not float needlebush paper pulp and true qualities do not float leaf wood paper pulp compound material, take above-mentioned specific processing step and process control parameter thereof, thus technical scheme integrally, the object improving end product quality, energy-saving and emission-reduction can be realized, improve first fine content, yield and the whiteness of finished product, reduce ash content, be conducive to the cost control of chemical industry soup, make follow-up boiling heating curve steady, fall evenly poly-, obtained semi-finished product are applicable to and various boiling mode, applied range.
Detailed description of the invention
embodiment 1
True qualities do not float the material preparation technology that dissolving pulp is prepared in needlebush and the modification of leaf wood using compound pulp, comprise following processing step:
A, raw material prepare
Not floating needlebush paper pulp and true qualities according to true qualities, not float leaf wood paper pulp gross weight with the ratio of boiling vessel volume be 100kg:1m
3get the raw materials ready, choose true qualities and do not float needlebush paper pulp and true qualities do not float leaf wood paper pulp;
B, dispersion and pulping
True qualities are not floated needlebush paper pulp not float leaf wood paper pulp dispersion treatment with true qualities and become pulp board, then true qualities are not floated needlebush pulp board and true qualities not float leaf wood pulp board and mix with water, carry out pulping process, obtain the mixture that true qualities do not float needlebush paper pulp, true qualities do not float leaf wood paper pulp and water and namely starch congee, carry out the de-liquid process of next step squeezing again, the slurry concentration of the described slurry congee obtained through pulping process is 3%;
C, the de-liquid of squeezing
Undertaken squeezing de-liquid process by through the slurry congee of dispersion with pulping, the de-liquid of squeezing is 20% to slurry congee mass dryness fraction;
D, dipping
Slurry congee through de-liquid is mixed with sodium hydroxide solution, carry out impregnation process, obtain the mixture that true qualities do not float needlebush paper pulp, true qualities do not float leaf wood paper pulp and sodium hydroxide solution, control liquor ratio is 1:3, and it is 17% that sodium hydrate solid weight and true qualities do not float the percentage that needlebush paper pulp and true qualities do not float fiber over dry gross weight in leaf wood paper pulp;
E, flooded after enter boiling vessel and carry out next step cooking process.
embodiment 2
True qualities do not float the material preparation technology that dissolving pulp is prepared in needlebush and the modification of leaf wood using compound pulp, comprise following processing step:
A, raw material prepare
Not floating needlebush paper pulp and true qualities according to true qualities, not float leaf wood paper pulp gross weight with the ratio of boiling vessel volume be 250kg:1m
3get the raw materials ready, choose true qualities and do not float needlebush paper pulp and true qualities do not float leaf wood paper pulp;
B, dispersion and pulping
True qualities are not floated needlebush paper pulp not float leaf wood paper pulp dispersion treatment with true qualities and become pulp board, then true qualities are not floated needlebush pulp board and true qualities not float leaf wood pulp board and mix with water, carry out pulping process, obtain the mixture that true qualities do not float needlebush paper pulp, true qualities do not float leaf wood paper pulp and water and namely starch congee, carry out the de-liquid process of next step squeezing again, the slurry concentration of the described slurry congee obtained through pulping process is 5%;
C, the de-liquid of squeezing
Undertaken squeezing de-liquid process by through the slurry congee of dispersion with pulping, the de-liquid of squeezing is 35% to slurry congee mass dryness fraction;
D, dipping
Slurry congee through de-liquid is mixed with sodium hydroxide solution, carry out impregnation process, obtain the mixture that true qualities do not float needlebush paper pulp, true qualities do not float leaf wood paper pulp and sodium hydroxide solution, control liquor ratio is 1:4, and it is 22% that sodium hydrate solid weight and true qualities do not float the percentage that needlebush paper pulp and true qualities do not float fiber over dry gross weight in leaf wood paper pulp;
E, flooded after enter boiling vessel and carry out next step cooking process.
embodiment 3
True qualities do not float the material preparation technology that dissolving pulp is prepared in needlebush and the modification of leaf wood using compound pulp, comprise following processing step:
A, raw material prepare
Not floating needlebush paper pulp and true qualities according to true qualities, not float leaf wood paper pulp gross weight with the ratio of boiling vessel volume be 175kg:1m
3get the raw materials ready, choose true qualities and do not float needlebush paper pulp and true qualities do not float leaf wood paper pulp;
B, dispersion and pulping
True qualities are not floated needlebush paper pulp not float leaf wood paper pulp dispersion treatment with true qualities and become pulp board, then true qualities are not floated needlebush pulp board and true qualities not float leaf wood pulp board and mix with water, carry out pulping process, obtain the mixture that true qualities do not float needlebush paper pulp, true qualities do not float leaf wood paper pulp and water and namely starch congee, carry out the de-liquid process of next step squeezing again, the slurry concentration of the described slurry congee obtained through pulping process is 4%;
C, the de-liquid of squeezing
Undertaken squeezing de-liquid process by through the slurry congee of dispersion with pulping, the de-liquid of squeezing is 27.5% to slurry congee mass dryness fraction;
D, dipping
Slurry congee through de-liquid is mixed with sodium hydroxide solution, carry out impregnation process, obtain the mixture that true qualities do not float needlebush paper pulp, true qualities do not float leaf wood paper pulp and sodium hydroxide solution, control liquor ratio is 1:3.5, and it is 19.5% that sodium hydrate solid weight and true qualities do not float the percentage that needlebush paper pulp and true qualities do not float fiber over dry gross weight in leaf wood paper pulp;
E, flooded after enter boiling vessel and carry out next step cooking process.
embodiment 4
True qualities do not float the material preparation technology that dissolving pulp is prepared in needlebush and the modification of leaf wood using compound pulp, comprise following processing step:
A, raw material prepare
Not floating needlebush paper pulp and true qualities according to true qualities, not float leaf wood paper pulp gross weight with the ratio of boiling vessel volume be 120kg:1m
3get the raw materials ready, choose true qualities and do not float needlebush paper pulp and true qualities do not float leaf wood paper pulp;
B, dispersion and pulping
True qualities are not floated needlebush paper pulp not float leaf wood paper pulp dispersion treatment with true qualities and become pulp board, then true qualities are not floated needlebush pulp board and true qualities not float leaf wood pulp board and mix with water, carry out pulping process, obtain the mixture that true qualities do not float needlebush paper pulp, true qualities do not float leaf wood paper pulp and water and namely starch congee, carry out the de-liquid process of next step squeezing again, the slurry concentration of the described slurry congee obtained through pulping process is 4.2%;
C, the de-liquid of squeezing
Undertaken squeezing de-liquid process by through the slurry congee of dispersion with pulping, the de-liquid of squeezing is 23% to slurry congee mass dryness fraction;
D, dipping
Slurry congee through de-liquid is mixed with sodium hydroxide solution, carry out impregnation process, obtain the mixture that true qualities do not float needlebush paper pulp, true qualities do not float leaf wood paper pulp and sodium hydroxide solution, control liquor ratio is 1:3.8, and it is 21% that sodium hydrate solid weight and true qualities do not float the percentage that needlebush paper pulp and true qualities do not float fiber over dry gross weight in leaf wood paper pulp;
E, flooded after enter boiling vessel and carry out next step cooking process.
embodiment 5
On the basis of embodiment 1 ~ 4, preferred:
True qualities described in step do not float needlebush paper pulp and true qualities, and not float leaf wood paper pulp be content of alphacellulose 88%, degree of polymerization 700DP, content of ashes 0.10%.
It is content of alphacellulose 88% that above-mentioned true qualities do not float needlebush paper pulp, degree of polymerization 1000DP, content of ashes 0.2%; It is content of alphacellulose 90% that described true qualities do not float leaf wood paper pulp, degree of polymerization 1000DP, content of ashes 0.2%.
It is that true qualities do not float needlebush paper pulp that true qualities described in step do not float the combined weight ratio that needlebush paper pulp and true qualities do not float leaf wood paper pulp: true qualities do not float leaf wood paper pulp=6:4.
Described needlebush pulp board and the true qualities of true qualities not floated are not floated leaf wood pulp board and are mixed with water in stepb, carry out pulping process and refer to that true qualities not being floated needlebush pulp board and true qualities does not float leaf wood pulp board and be delivered to hydrabrusher with the transporting velocity of 85kg/min, add water simultaneously and carry out pulping process, and the discharging speed after pulping process is 2.8m
3/ min.
The described speed adding water is 2.8m
3/ min.
The electric machine frequency of described hydrabrusher is 30Hz.
The Stress control that squeezing described in step C takes off liquid is 0.4MPa.
The alkalinity that true qualities do not float needlebush paper pulp, true qualities do not float the mixture of leaf wood paper pulp and sodium hydroxide solution described is in step D 3.0%, and methylcellulose content is 20%.
embodiment 6
On the basis of embodiment 1 ~ 4, preferred:
True qualities described in step do not float needlebush paper pulp and true qualities, and not float leaf wood paper pulp be content of alphacellulose 98, degree of polymerization 1500DP, content of ashes 0.90%.
It is content of alphacellulose 94% that above-mentioned true qualities do not float needlebush paper pulp, degree of polymerization 1400DP, content of ashes 0.8%; It is content of alphacellulose 96% that described true qualities do not float leaf wood paper pulp, degree of polymerization 1400DP, content of ashes 0.8%.
It is that true qualities do not float needlebush paper pulp that true qualities described in step do not float the combined weight ratio that needlebush paper pulp and true qualities do not float leaf wood paper pulp: true qualities do not float leaf wood paper pulp=4:6.
Described needlebush pulp board and the true qualities of true qualities not floated are not floated leaf wood pulp board and are mixed with water in stepb, carry out pulping process and refer to that true qualities not being floated needlebush pulp board and true qualities does not float leaf wood pulp board and be delivered to hydrabrusher with the transporting velocity of 200kg/min, add water simultaneously and carry out pulping process, and the discharging speed after pulping process is 6m
3/ min.
The described speed adding water is 6m
3/ min.
The electric machine frequency of described hydrabrusher is 60Hz.
The Stress control that squeezing described in step C takes off liquid is 0.5MPa.
The alkalinity that true qualities do not float needlebush paper pulp, true qualities do not float the mixture of leaf wood paper pulp and sodium hydroxide solution described is in step D 5.1%, and methylcellulose content is 25%.
embodiment 7
On the basis of embodiment 1 ~ 4, preferred:
True qualities described in step do not float needlebush paper pulp and true qualities, and not float leaf wood paper pulp be content of alphacellulose 93%, degree of polymerization 1100DP, content of ashes 0.50%.
It is content of alphacellulose 91% that above-mentioned true qualities do not float needlebush paper pulp, degree of polymerization 1200DP, content of ashes 0.5%; It is content of alphacellulose 93% that described true qualities do not float leaf wood paper pulp, degree of polymerization 1200DP, content of ashes 0.5%.
It is that true qualities do not float needlebush paper pulp that true qualities described in step do not float the combined weight ratio that needlebush paper pulp and true qualities do not float leaf wood paper pulp: true qualities do not float leaf wood paper pulp=12:13.
Described needlebush pulp board and the true qualities of true qualities not floated are not floated leaf wood pulp board and are mixed with water in stepb, carry out pulping process and refer to that true qualities not being floated needlebush pulp board and true qualities does not float leaf wood pulp board and be delivered to hydrabrusher with the transporting velocity of 142.5kg/min, add water simultaneously and carry out pulping process, and the discharging speed after pulping process is 4.4m
3/ min.
The described speed adding water is 4.4m
3/ min.
The electric machine frequency of described hydrabrusher is 45Hz.
The Stress control that squeezing described in step C takes off liquid is 0.45MPa.
The alkalinity that true qualities do not float needlebush paper pulp, true qualities do not float the mixture of leaf wood paper pulp and sodium hydroxide solution described is in step D 4.05%, and methylcellulose content is 22.5%.
embodiment 8
On the basis of embodiment 1 ~ 4, preferred:
True qualities described in step do not float needlebush paper pulp and true qualities, and not float leaf wood paper pulp be content of alphacellulose 92%, degree of polymerization 1400DP, content of ashes 0.52%.
It is content of alphacellulose 93% that above-mentioned true qualities do not float needlebush paper pulp, degree of polymerization 1100DP, content of ashes 0.3%; It is content of alphacellulose 95.5% that described true qualities do not float leaf wood paper pulp, degree of polymerization 1100DP, content of ashes 0.3%.
It is that true qualities do not float needlebush paper pulp that true qualities described in step do not float the combined weight ratio that needlebush paper pulp and true qualities do not float leaf wood paper pulp: true qualities do not float leaf wood paper pulp=6:7.
Described needlebush pulp board and the true qualities of true qualities not floated are not floated leaf wood pulp board and are mixed with water in stepb, carry out pulping process and refer to that true qualities not being floated needlebush pulp board and true qualities does not float leaf wood pulp board and be delivered to hydrabrusher with the transporting velocity of 186kg/min, add water simultaneously and carry out pulping process, and the discharging speed after pulping process is 3.9m
3/ min.
The described speed adding water is 3.9m
3/ min.
The electric machine frequency of described hydrabrusher is 49Hz.
The Stress control that squeezing described in step C takes off liquid is 0.41MPa.
The alkalinity that true qualities do not float needlebush paper pulp, true qualities do not float the mixture of leaf wood paper pulp and sodium hydroxide solution described is in step D 5%, and methylcellulose content is 23%.
embodiment 9
True qualities do not float the material preparation technology that dissolving pulp is prepared in needlebush and the modification of leaf wood using compound pulp, comprise following processing step:
A, raw material prepare
Not floating needlebush paper pulp and true qualities according to true qualities, not float leaf wood paper pulp gross weight with the ratio of boiling vessel volume be 100 ~ 250kg:1m
3get the raw materials ready, choose true qualities and do not float needlebush paper pulp and true qualities do not float leaf wood paper pulp; Get the raw materials ready according to aforementioned proportion, make the medium density in boiling vessel;
True qualities described in step do not float needlebush paper pulp and true qualities, and not float leaf wood paper pulp be content of alphacellulose >=88%, the degree of polymerization 700 ~ 1500DP, content of ashes≤0.90%.
Be more preferably, reach the balance of material quality and economy, it is content of alphacellulose 88 ~ 94% that above-mentioned true qualities do not float needlebush paper pulp, the degree of polymerization 1000 ~ 1400DP, content of ashes 0.2 ~ 0.8%; It is content of alphacellulose 90 ~ 96% that described true qualities do not float leaf wood paper pulp, the degree of polymerization 1000 ~ 1400DP, content of ashes 0.2 ~ 0.8%.
It is that true qualities do not float needlebush paper pulp that true qualities described in step do not float the combined weight ratio that needlebush paper pulp and true qualities do not float leaf wood paper pulp: true qualities do not float leaf wood paper pulp=4:6 ~ 6:4.
B, dispersion and pulping
True qualities are not floated needlebush paper pulp not float leaf wood paper pulp dispersion treatment with true qualities and become pulp board, then true qualities are not floated needlebush pulp board and true qualities not float leaf wood pulp board and mix with water, carry out pulping process, obtain the mixture that true qualities do not float needlebush paper pulp, true qualities do not float leaf wood paper pulp and water and namely starch congee, carry out the de-liquid process of next step squeezing again, the slurry concentration of the described slurry congee obtained through pulping process is 3 ~ 5%;
The starting pulps bought back one to wrap, and dispersion adopts bale opener packaging to be opened, and re-uses paging cutter and raw material is divided into pulp board one by one, finally uses the belt conveyor conveying pulp board of feeding dregs of rice machine to hydrabrusher;
Slurry concentration is this area technical term, refers to that true qualities do not float the percentage that needlebush paper pulp and true qualities do not float mixture (namely the starching congee) weight that fiber over dry gross weight and true qualities in leaf wood paper pulp do not float needlebush paper pulp, true qualities do not float leaf wood paper pulp and water.
Described needlebush pulp board and the true qualities of true qualities not floated are not floated leaf wood pulp board and are mixed with water in stepb, carry out pulping process and refer to that true qualities not being floated needlebush pulp board and true qualities does not float leaf wood pulp board and be delivered to hydrabrusher with the transporting velocity of 85 ~ 200kg/min, add water simultaneously and carry out pulping process, and the discharging speed after pulping process is 2.8 ~ 6m
3/ min.
The above-mentioned speed adding water is 2.8 ~ 6m
3/ min.
The electric machine frequency of above-mentioned hydrabrusher is 30 ~ 60Hz.
C, the de-liquid of squeezing
Undertaken squeezing de-liquid process by through the slurry congee of dispersion with pulping, the de-liquid of squeezing is 20 ~ 35% to slurry congee mass dryness fraction;
Mass dryness fraction is this area technical term, refers to the percentage of the weight of all liq in the liquid weight sloughed and the mixture (namely starching congee) that true qualities do not float needlebush paper pulp, true qualities do not float leaf wood paper pulp and water.
The Stress control that squeezing described in step C takes off liquid is 0.4 ~ 0.5MPa.
D, dipping
Slurry congee through de-liquid is mixed with sodium hydroxide solution, carry out impregnation process, obtain the mixture that true qualities do not float needlebush paper pulp, true qualities do not float leaf wood paper pulp and sodium hydroxide solution, control liquor ratio is 1:3 ~ 4, and it is 17 ~ 22% that sodium hydrate solid weight and true qualities do not float the percentage that needlebush paper pulp and true qualities do not float fiber over dry gross weight in leaf wood paper pulp;
Liquor ratio (or being called bath raio) is this area technical term, refers to that true qualities do not float the ratio that needlebush paper pulp and true qualities do not float fiber over dry gross weight and sodium hydroxide solution volume in leaf wood paper pulp.
The alkalinity that true qualities do not float needlebush paper pulp, true qualities do not float the mixture of leaf wood paper pulp and sodium hydroxide solution described is in step D 3.0 ~ 5.1%, and methylcellulose content is 20 ~ 25%.
E, flooded after enter boiling vessel and carry out next step cooking process.
This technique device therefor:
1, the boiling vessel in steps A and step e is rotary spherical digester, steamer or continuous steamer, and continuous steamer comprises horizontal continuous cooking device or tower continuous steamer;
2, being delivered to hydrabrusher in step B is adopt belt conveyor, and pulping complete after slurry congee by delivery pump discharging, be delivered to the de-liquid equipment of squeezing;
3, it is squeezer or acroll press washer that the squeezing in step D takes off liquid equipment;
4, the impregnating equipment in step C is treating tank, gives dipping machine or double helix kneading machine;
The said equipment is this area conventional equipment.
embodiment 10
Digesting technoloy:
The semi-finished product obtained getting the raw materials ready carry out boiling, the steam pipe of described continuous steamer is set to 3 sections, one section that is connected with pre-reaction feed bin is provided with the T-shaped pipe adding alkali lye and the steam pipe adding steam, and other two sections are equipped with the steam pipe adding steam, and its digesting technoloy requires as follows:
Liquor ratio: 1:2.0 ~ 4.0;
Cooking liquor is added by 17 ~ 30% of oven dry weight;
The vapor (steam) temperature of one section be connected with pre-reaction feed bin of described steam pipe is 105 ± 5 DEG C;
The vapor (steam) temperature of middle one section is 140 ± 5 DEG C;
The vapor (steam) temperature of one section that is connected with cold spraying device is 150 DEG C ~ 175 DEG C;
Compression ratio: 1:2 ~ 3.0.
Described digestant is NaOH and Na
2sO
3mixed solution, mixed proportion is NaOH:Na
2sO
3=90 ~ 98%:2 ~ 10%.
embodiment 11
Aftertreatment technology:
Bellmer after the pulp of boiling sends into alkali tune is carried out sodium hypochlorite bleaching 18 ~ 25 minutes, and after dechlorination, acid treatment, namely complete bleaching, technological parameter is as follows:
Alkali tune amount: 20 ~ 200g/m
3;
Clorox consumption: 0.1 ~ 0.6g/l;
Hypo consumption: 1.8 ~ 2 times of residual chlorine;
Acid treatment: hydrochloric acid consumption 1 ~ 4%, processes 30 ~ 60 minutes;
Calgon consumption 0.5 ~ 2%;
Consumption of oxalic acid 0.5 ~ 2%;
Bleaching temperature 30 ~ 60 DEG C;
Process flow of manufacturing paper with pulp is: compound stock tank-copy forebay-stuff box-desander-pulp machine-cut paper stacker-weighing balance-baling press-warehouse-in, and technological parameter comprises:
To manufacture paper with pulp desanding concentration: 0.6 ~ 1.5%;
Manufacture paper with pulp desanding pressure: 0.15 ~ 0.32MPa;
Size mixing with water: clear water, plain boiled water;
Online concentration: 0.6 ~ 1.5%;
One squeeze pressure: 0.1 ~ 0.3MPa;
Second press pressure: 0.2 ~ 0.5MPa;
Three road squeeze pressure: 0.3 ~ 0.7MPa;
Drying cylinder steam pressure: 0.15 ~ 0.35MPa;
Cut paper specification: 600*800;
Gauge: 100 ~ 250Kg/ wraps.
embodiment 12
The dissolving pulp that the semi-finished product that material preparation technology of the present invention obtains adopt conventional digesting technoloy and aftertreatment technology to obtain with do not adopt material preparation technology of the present invention to obtain the Indexes Comparison of the semi-finished product dissolving pulp that adopts conventional digesting technoloy and aftertreatment technology to obtain:
After material preparation technology of the present invention, under the prerequisite of the degree of polymerization ensureing finished product, first fine content, yield and the whiteness of finished product dissolving pulp all have lifting, play remarkable effect especially to reduction ash content.
Claims (1)
1. true qualities do not float the material preparation technology that dissolving pulp is prepared in needlebush and the modification of leaf wood using compound pulp, it is characterized in that: comprise following processing step:
A, raw material prepare
Not floating needlebush paper pulp and true qualities according to true qualities, not float leaf wood paper pulp gross weight with the ratio of boiling vessel volume be 100kg:1m
3get the raw materials ready, choose true qualities and do not float needlebush paper pulp and true qualities do not float leaf wood paper pulp; It is that true qualities do not float needlebush paper pulp that described true qualities do not float the combined weight ratio that needlebush paper pulp and true qualities do not float leaf wood paper pulp: true qualities do not float leaf wood paper pulp=4:6 ~ 6:4; It is content of alphacellulose 88 ~ 94% that described true qualities do not float needlebush paper pulp, the degree of polymerization 1000 ~ 1400DP, content of ashes 0.2 ~ 0.8%; It is content of alphacellulose 90 ~ 96% that described true qualities do not float leaf wood paper pulp, the degree of polymerization 1000 ~ 1400DP, content of ashes 0.2 ~ 0.8%;
B, dispersion and pulping
True qualities are not floated needlebush paper pulp not float leaf wood paper pulp dispersion treatment with true qualities and become pulp board, then true qualities are not floated needlebush pulp board and true qualities not float leaf wood pulp board and mix with water, carry out pulping process, true qualities are not floated needlebush pulp board and true qualities not float leaf wood pulp board and be delivered to the transporting velocity of 85 ~ 200kg/min the hydrabrusher that electric machine frequency is 30 ~ 60Hz, add water simultaneously and carry out pulping process, and the discharging speed after pulping process is 2.8 ~ 6m
3/ min, the speed adding water is 2.8 ~ 6m
3/ min, obtains the mixture that true qualities do not float needlebush paper pulp, true qualities do not float leaf wood paper pulp and water and namely starches congee, then carries out the de-liquid process of next step squeezing, and the slurry concentration of the described slurry congee obtained through pulping process is 3%;
C, the de-liquid of squeezing
Undertaken squeezing de-liquid process by through the slurry congee of dispersion with pulping, the de-liquid of squeezing is 20% to slurry congee mass dryness fraction; The Stress control of the de-liquid of squeezing is 0.4 ~ 0.5MPa;
D, dipping
Slurry congee through de-liquid is mixed with sodium hydroxide solution, carry out impregnation process, obtaining alkalinity is 3.0 ~ 5.1%, methylcellulose content is the mixture that true qualities do not float needlebush paper pulp, true qualities do not float leaf wood paper pulp and sodium hydroxide solution of 20 ~ 25%, control liquor ratio is 1:3, and described liquor ratio is volume ratio; It is 17% that sodium hydrate solid weight and true qualities do not float the percentage that needlebush paper pulp and true qualities do not float fiber over dry gross weight in leaf wood paper pulp;
E, flooded after enter boiling vessel and carry out next step cooking process.
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|---|---|---|---|
| CN201210170737.9A CN102677501B (en) | 2012-05-29 | 2012-05-29 | Material preparation process suitable for preparing dissolving pulp by modifying natural color unblenched needlebush and broadleaf wood composite paper pulp |
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|---|---|---|---|
| CN201210170737.9A CN102677501B (en) | 2012-05-29 | 2012-05-29 | Material preparation process suitable for preparing dissolving pulp by modifying natural color unblenched needlebush and broadleaf wood composite paper pulp |
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Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0639434A1 (en) * | 1993-08-18 | 1995-02-22 | Fraunhofer-Gesellschaft Zur Förderung Der Angewandten Forschung E.V. | Method for the manufacture of medium density wood fibre boards (MDF) |
| CN101818460A (en) * | 2009-12-17 | 2010-09-01 | 宜宾长毅浆粕有限责任公司 | Method for preparing wood dissolving pulp by modifying true color unbleached wood pulp |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101532185B (en) * | 2009-04-22 | 2011-07-20 | 宜宾长毅浆粕有限责任公司 | Method for producing cotton pulp for acetate fibre |
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2012
- 2012-05-29 CN CN201210170737.9A patent/CN102677501B/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0639434A1 (en) * | 1993-08-18 | 1995-02-22 | Fraunhofer-Gesellschaft Zur Förderung Der Angewandten Forschung E.V. | Method for the manufacture of medium density wood fibre boards (MDF) |
| CN101818460A (en) * | 2009-12-17 | 2010-09-01 | 宜宾长毅浆粕有限责任公司 | Method for preparing wood dissolving pulp by modifying true color unbleached wood pulp |
Non-Patent Citations (3)
| Title |
|---|
| 国内外溶解浆的原料、技术及市场发展(一);邱有龙;《纺织导报》;20110731(第7期);60-64 * |
| 国内外溶解浆的原料、技术及市场发展(二);邱有龙;《纺织导报》;20110831(第8期);60-64 * |
| 针叶木、阔叶木混合蒸煮以及连续蒸煮系统的选型;齐秀乐等;《中华纸业》;20090803;第30卷(第16期);68-70 * |
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