CN107044063B - A kind of once pretreatment immersion liquid A and its application - Google Patents
A kind of once pretreatment immersion liquid A and its application Download PDFInfo
- Publication number
- CN107044063B CN107044063B CN201710358395.6A CN201710358395A CN107044063B CN 107044063 B CN107044063 B CN 107044063B CN 201710358395 A CN201710358395 A CN 201710358395A CN 107044063 B CN107044063 B CN 107044063B
- Authority
- CN
- China
- Prior art keywords
- parts
- immersion liquid
- paper pulp
- pretreatment immersion
- sinocalamus latiflorus
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Classifications
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C1/00—Pretreatment of the finely-divided materials before digesting
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21C—PRODUCTION OF CELLULOSE BY REMOVING NON-CELLULOSE SUBSTANCES FROM CELLULOSE-CONTAINING MATERIALS; REGENERATION OF PULPING LIQUORS; APPARATUS THEREFOR
- D21C9/00—After-treatment of cellulose pulp, e.g. of wood pulp, or cotton linters ; Treatment of dilute or dewatered pulp or process improvement taking place after obtaining the raw cellulosic material and not provided for elsewhere
- D21C9/18—De-watering; Elimination of cooking or pulp-treating liquors from the pulp
Abstract
The invention discloses a kind of primary pretreatment immersion liquid A and its application, belong to unbleached paper preparing technical field, the primary pretreatment immersion liquid A, as unit of parts by weight, including following raw material：48 parts of alkyl phenol polyoxyethylene ether, 0.3 0.6 parts of triethanolamine, 0.5 1 parts of stearic acid, 0.4 1.2 parts of oleic acid, 0.8 1.5 parts of lauric acid, 42 90 parts of water.The primary pretreatment immersion liquid A is applied to prepare in sinocalamus latiflorus true qualities paper pulp, gained paper pulp yield and whiteness are significantly higher than paper pulp yield made from the prior art and whiteness, in addition, paper pulp drainability is good, intensity is big, at low cost, low energy consumption for pulping process, and prepared paper pulp can be suitable for the true qualities paper pulp of paper mould manufacture, paper for daily use manufacture.
Description
【Technical field】
The invention belongs to unbleached paper preparing technical fields, and in particular to a kind of once pretreatment immersion liquid A and its application.
【Background technology】
The production method of paper pulp includes mainly the productions streams such as chemical method, semichemical method, Mechanical Method and chemical mechanical pulping at present
Journey.Wherein chemical pulping is occupied an leading position among current numerous pulping process.Claim by paper pulp made from chemical method boiling
For true qualities paper pulp, true qualities paper pulp limits its application since whiteness is relatively low, and true qualities paper pulp will could generally give birth to after bleaching
Produce the paper kind of higher level.If the whiteness of true qualities paper pulp can be improved in pulping process, the fiber crops of following bleaching can be saved
It is tired, simplify production procedure, reduces production cost, and improve the use value of true qualities paper pulp.
In the production process of true qualities paper pulp, for wood raw material, carried out using sodium hydroxide and vulcanized sodium in pulping process
The sulfate process of boiling is main pulping process, and small part uses sulfite pulping, but these use sulfur-bearing chemicals
The method of boiling there are the problem of be exactly can environmental danger.For non-wood material, soda processes or burning are mainly used at present
The problem of soda-AQ qulping, this pulping process is difficult to recycle presently, there are waste liquid.In addition, either sulfate process, caustic soda
Method or alkali-AQ pulping, since the lignin in raw material is condensed in digestion process, the true qualities pulp brightness of gained is all
It is relatively low, therefore development of the free of contamination novel high whiteness true qualities paper pulp manufacturing technique for paper industry is sought with important meaning
Justice.
A kind of patent document " true qualities method of manufcturing paper pulp (Authorization Notice No. improving pulp brightness：CN103924470B)”
A kind of production method for the true qualities paper pulp improving bamboo paper pulp brightness is disclosed, this method includes locating bamboo raw material SODIUM PERCARBONATE in advance
After reason, then with the mixed organic solvents of formic acid, acetic acid and acetone boiling is carried out, the paper pulp after boiling uses formic acid and hot water wash
It washs, finally prepares true qualities paper pulp, however gained bamboo paper pulp yield and whiteness are still relatively low.
With the continuous expansion of paper industry, constantly opening up for pulp applications is wide, originally the wood as main paper making raw material
Gradually supply falls short of demand for material, and forest is caused excessively to be cut down, and influences ecological environment, therefore, it is necessary to seek new raw material substituent.
Sinocalamus latiflorus (Dendrocalamus latiflorus Munro) is that south China cultivates most wide one of bamboo kind, is standing grain
Undergraduate course (Poaceae) Bambusoideae (Bambusoideae) Dendrocalamus (Dendrocalamus) large-scale sympodial bamboo kind, is distributed mainly on
The provinces and regions such as Fujian, Taiwan, Guangdong and Guangxi Provinces, Yunnan, Hainan, Sichuan, the Guizhou middle and south, for edible, timber-used, Ye Yong, water and soil conservation, greening
The multipurposes bamboo kind such as ornamental, to produce bamboo shoot or do based on pulpwood.Sinocalamus latiflorus growth is fast, the bamboo shoot phase is long, yield is high, bamboo shoot are of fine quality good, sinocalamus latiflorus
Fast growing, widely used, primary plant utilizes for many years, is that a kind of economic value is high, excellent calculation material profitable on ecology is dual-purpose
Bamboo kind, economic benefit, ecological benefits and social benefit Three benefits are notable.
Therefore be conducive to avoid result in forest and excessively cut down as substitution wood raw material using artificial growth sinocalamus latiflorus, influence
Ecological environment.
【Invention content】
A kind of primary pretreatment immersion liquid A provided by the invention and its application, with solve how to improve sinocalamus latiflorus paper pulp yield and
The problem of whiteness.
In order to solve the above technical problems, the present invention uses following technical matters：
A kind of primary pretreatment immersion liquid A, as unit of parts by weight, including following raw material：Alkyl phenol polyoxyethylene ether 4-8
Part, 0.3-0.6 parts of triethanolamine, 0.5-1 parts of stearic acid, 0.4-1.2 parts of oleic acid, 0.8-1.5 parts of lauric acid, 42-90 parts of water.
Preferably, as unit of parts by weight, including following raw material：6 parts of alkyl phenol polyoxyethylene ether, 0.5 part of triethanolamine,
0.8 part of stearic acid, 0.8 part of oleic acid, 1.2 parts of lauric acid, 66 parts of water.
The present invention also provides a kind of primary pretreatment immersion liquid A in the application for preparing sinocalamus latiflorus true qualities paper pulp, the sinocalamus latiflorus true qualities
The preparation method of paper pulp, includes the following steps：
S1：Sinocalamus latiflorus is cut into sinocalamus latiflorus piece, is delivered in primary pretreatment immersion liquid A, immersion 30- is carried out under ul-trasonic irradiation
45min is then filtered, and obtains leaching material A；
S2：Leaching material A made from step S1 is delivered in secondary pretreatment immersion liquid B, the secondary pretreatment immersion liquid B is with weight
Amount part is unit, including following raw material：10-20 parts of percarbamide, 4-6 parts of potassium hydroxide, 0.3-0.5 parts of amino carboxylic acid, five oxygen
Change 0.1-0.2 parts of two vanadium, 35-150 parts of water, immersion 20-40min is carried out under ul-trasonic irradiation, is then filtered, obtains leaching material B；
S3：Leaching material B made from step S2 is washed with hot water, is then dehydrated, dehydrated material C is made；
S4：Dehydrated material C made from step S3 is ground, thick slurry is made；
S5：It is washed slightly being starched made from step S4, uses screening concentration for 0.6%-2.5%, inlet outlet pressure differential is
The pressurized screen of 0.12-0.35MPa is screened, and press filtration, system are carried out using into the Double-screen filter press for starching a concentration of 2.4%-5.3%
Obtain sinocalamus latiflorus true qualities paper pulp.
Preferably, the size of sinocalamus latiflorus piece described in step S1 is 24-28 × 3-3.6mm × 1.4-2mm.
Preferably, the ratio between sinocalamus latiflorus weight described in step S1 and primary pretreatment immersion liquid A volumes are 1:2-4.
Preferably, ultrasonic power described in step S1 is 30-50W, and temperature is 43-48 DEG C.
Preferably, the ratio between the A weight and secondary pretreatment immersion liquid B volumes of leaching material described in step S2 are 1:6-13.
Preferably, ultrasonic power described in step S2 is 40-80W, and temperature is 85-92 DEG C.
Preferably, the temperature of hot water described in step S3 is 60-80 DEG C.
Preferably, washing described in step S3 to pH value is 6.8-7.2.
The invention has the advantages that：
(1) the primary alkyl phenol polyoxyethylene ether in pretreatment immersion liquid A, triethanolamine, stearic acid, oleic acid, lauric
Addition plays synergistic effect, improves paper pulp yield and whiteness；
(2) paper pulp yield made from preparation process of the invention and whiteness are significantly above paper pulp made from the prior art and obtain
Rate and whiteness；
(3) present invention process is simple, and gained paper pulp drainability is good, intensity is big, at low cost, and low energy consumption for pulping process, made
Standby paper pulp can be suitable for the true qualities paper pulp of paper mould manufacture, paper for daily use manufacture.
【Specific implementation mode】
It for ease of more fully understanding the present invention, is illustrated by following embodiment, these embodiments belong to the present invention's
Protection domain, but do not limit the scope of the invention.
In embodiment, the preparation method of the sinocalamus latiflorus true qualities paper pulp, includes the following steps：
S1：Sinocalamus latiflorus is cut into the sinocalamus latiflorus piece that size is 24-28 × 3-3.6mm × 1.4-2mm, is delivered to primary pretreatment leaching
In liquid A, the ratio between the sinocalamus latiflorus weight and primary pretreatment immersion liquid A volumes are 1:2-4, the primary pretreatment immersion liquid A is with weight
Part is unit, including following raw material：4-8 parts of alkyl phenol polyoxyethylene ether, 0.3-0.6 parts of triethanolamine, 0.5-1 parts of stearic acid,
0.4-1.2 parts of oleic acid, 0.8-1.5 parts of lauric acid, 42-90 parts of water are 30-50W in ultrasonic power, and temperature is at 43-48 DEG C
Immersion 30-45min is carried out, is then filtered, leaching material A is obtained；
S2：Leaching material A made from step S1 is delivered in secondary pretreatment immersion liquid B, the leaching material A weight and secondary pre- place
It is 1 to manage the ratio between immersion liquid B volumes:6-13, the secondary pretreatment immersion liquid B is as unit of parts by weight, including following raw material：Cross phosphinylidyne
10-20 parts of amine, 4-6 parts of potassium hydroxide, 0.3-0.5 parts of amino carboxylic acid, 0.1-0.2 parts of vanadic anhydride, 35-150 parts of water, super
Acoustic power is 40-80W, and temperature is to carry out immersion 20-40min at 85-92 DEG C, is then filtered, and leaching material B is obtained；
S3：It is 6.8-7.2 by leaching material B is washed with 60-80 DEG C of hot water to pH value made from step S2, then takes off
Dehydrated material C is made in water；
S4：Dehydrated material C made from step S3 is ground, thick slurry is made；
S5：It is washed slightly being starched made from step S4, uses screening concentration for 0.6%-2.5%, inlet outlet pressure differential is
The pressurized screen of 0.12-0.35MPa is screened, and press filtration, system are carried out using into the Double-screen filter press for starching a concentration of 2.4%-5.3%
Obtain sinocalamus latiflorus true qualities paper pulp.
Embodiment 1
A kind of preparation method of sinocalamus latiflorus true qualities paper pulp, includes the following steps：
S1：Sinocalamus latiflorus is cut into the sinocalamus latiflorus piece that size is 26 × 3.4mm × 1.8mm, is delivered in primary pretreatment immersion liquid A,
The ratio between the sinocalamus latiflorus weight and primary pretreatment immersion liquid A volumes are 1:2, the primary pretreatment immersion liquid A as unit of parts by weight,
Including following raw material：4.1 parts of alkyl phenol polyoxyethylene ether, 0.3 part of triethanolamine, 0.5 part of stearic acid, 0.4 part of oleic acid, lauric acid
0.8 part, 42 parts of water are 30W in ultrasonic power, and temperature is to carry out immersion 45min at 44 DEG C, is then filtered, and leaching material A is obtained；
S2：Leaching material A made from step S1 is delivered in secondary pretreatment immersion liquid B, the leaching material A weight and secondary pre- place
It is 1 to manage the ratio between immersion liquid B volumes:6, the secondary pretreatment immersion liquid B is as unit of parts by weight, including following raw material：Percarbamide
11 parts, 4 parts of potassium hydroxide, 0.3 part of amino carboxylic acid, 0.1 part of vanadic anhydride, 36 parts of water, ultrasonic power be 40W, temperature
It is to carry out immersion 40min at 85 DEG C, then filters, obtains leaching material B；
S3：It is 6.8 by leaching material B is washed with 60 DEG C of hot water to pH value made from step S2, is then dehydrated, is made de-
Water material C；
S4：Dehydrated material C made from step S3 is ground, thick slurry is made；
S5：By slightly slurry is washed made from step S4, use screening concentration for 0.7%, inlet outlet pressure differential 0.13MPa
Pressurized screen screened, press filtration is carried out using the Double-screen filter press into slurry a concentration of 2.5%, sinocalamus latiflorus true qualities paper pulp is made.
Embodiment 2
A kind of preparation method of sinocalamus latiflorus true qualities paper pulp, includes the following steps：
S1：Sinocalamus latiflorus is cut into the sinocalamus latiflorus piece that size is 24 × 3mm × 1.4mm, is delivered in primary pretreatment immersion liquid A, institute
It is 1 to state the ratio between sinocalamus latiflorus weight and primary pretreatment immersion liquid A volumes:4, the primary pretreatment immersion liquid A are as unit of parts by weight, packet
Include following raw material：8 parts of alkyl phenol polyoxyethylene ether, 0.6 part of triethanolamine, 1 part of stearic acid, 1.2 parts of oleic acid, 1.5 parts of lauric acid,
90 parts of water is 50W in ultrasonic power, and temperature is to carry out immersion 32min at 48 DEG C, is then filtered, and leaching material A is obtained；
S2：Leaching material A made from step S1 is delivered in secondary pretreatment immersion liquid B, the leaching material A weight and secondary pre- place
It is 1 to manage the ratio between immersion liquid B volumes:13, the secondary pretreatment immersion liquid B is as unit of parts by weight, including following raw material：Percarbamide
20 parts, 6 parts of potassium hydroxide, 0.5 part of amino carboxylic acid, 0.2 part of vanadic anhydride, 148 parts of water, ultrasonic power be 80W, temperature
It is to carry out immersion 20min at 90 DEG C, then filters, obtains leaching material B；
S3：It is 7.2 by leaching material B is washed with 60-80 DEG C of hot water to pH value made from step S2, is then dehydrated, makes
Obtain dehydrated material C；
S4：Dehydrated material C made from step S3 is ground, thick slurry is made；
S5：By slightly slurry is washed made from step S4, use screening concentration for 2.5%, inlet outlet pressure differential 0.35MPa
Pressurized screen screened, press filtration is carried out using the Double-screen filter press into slurry a concentration of 5.2%, sinocalamus latiflorus true qualities paper pulp is made.
Embodiment 3
A kind of preparation method of sinocalamus latiflorus true qualities paper pulp, includes the following steps：
S1：Sinocalamus latiflorus is cut into the sinocalamus latiflorus piece that size is 28 × 3.6mm × 2mm, is delivered in primary pretreatment immersion liquid A, institute
It is 1 to state the ratio between sinocalamus latiflorus weight and primary pretreatment immersion liquid A volumes:3.2, the primary pretreatment immersion liquid A as unit of parts by weight,
Including following raw material：6 parts of alkyl phenol polyoxyethylene ether, 0.5 part of triethanolamine, 0.8 part of stearic acid, 0.8 part of oleic acid, lauric acid
1.2 parts, 66 parts of water are 42W in ultrasonic power, and temperature is to carry out immersion 40min at 46 DEG C, is then filtered, and leaching material A is obtained；
S2：Leaching material A made from step S1 is delivered in secondary pretreatment immersion liquid B, the leaching material A weight and secondary pre- place
It is 1 to manage the ratio between immersion liquid B volumes:10, the secondary pretreatment immersion liquid B is as unit of parts by weight, including following raw material：Percarbamide
16 parts, 5 parts of potassium hydroxide, 0.4 part of amino carboxylic acid, 0.1 part of vanadic anhydride, 92 parts of water, ultrasonic power be 60W, temperature
It is to carry out immersion 32min at 88 DEG C, then filters, obtains leaching material B；
S3：It is 7 by leaching material B is washed with 60-80 DEG C of hot water to pH value made from step S2, is then dehydrated, is made
Dehydrated material C；
S4：Dehydrated material C made from step S3 is ground, thick slurry is made；
S5：By slightly slurry is washed made from step S4, use screening concentration for 1.5%, inlet outlet pressure differential 0.2MPa
Pressurized screen screened, press filtration is carried out using the Double-screen filter press into slurry a concentration of 4.2%, sinocalamus latiflorus true qualities paper pulp is made.
Comparative example 1
After sinocalamus latiflorus is cut into sinocalamus latiflorus piece, is impregnated without primary pretreatment immersion liquid A, but be fed directly to secondary pretreatment
Immersion liquid B impregnates, other preparation processes are identical as the preparation process of embodiment 3.
Comparative example 2
The secondary pretreatment immersion liquid B is as unit of parts by weight, including following raw material：5 parts of potassium hydroxide, amino carboxylic acid
0.4 part, 0.1 part of vanadic anhydride, 92 parts of water, other preparation processes are identical as the preparation process of comparative example 1.
Comparative example 3
The secondary pretreatment immersion liquid B is as unit of parts by weight, including following raw material：16 parts of percarbamide, potassium hydroxide 5
Part, 0.1 part of vanadic anhydride, 92 parts of water, other preparation processes are identical as the preparation process of comparative example 1.
Comparative example 4
The secondary pretreatment immersion liquid B is as unit of parts by weight, including following raw material：16 parts of percarbamide, potassium hydroxide 5
Part, 0.4 part of amino carboxylic acid, 92 parts of water, other preparation processes are identical as the preparation process of comparative example 1.
Comparative example 5
After sinocalamus latiflorus is cut into sinocalamus latiflorus piece, only impregnated by primary pretreatment immersion liquid A, and without secondary pretreatment immersion liquid B
It impregnates, the preparation process of other preparation processes and embodiment 3 are essentially identical.
Comparative example 6
The primary pretreatment immersion liquid A is as unit of parts by weight, including following raw material：6 parts of alkyl phenol polyoxyethylene ether, three
0.5 part of ethanol amine, 66 parts of water, other preparation processes are identical as the preparation process of comparative example 5.
Comparative example 7
The primary pretreatment immersion liquid A is as unit of parts by weight, including following raw material：0.8 part of stearic acid, 0.8 part of oleic acid,
1.2 parts of lauric acid, 66 parts of water, other preparation processes are identical as the preparation process of comparative example 5.
Comparative example 8
Using a kind of patent document " true qualities method of manufcturing paper pulp (Authorization Notice No. improving pulp brightness：
CN103924470B) " method of embodiment 2 prepares true qualities paper pulp.
True qualities paper pulp is prepared using the preparation process of embodiment 1-3 and comparative example 1-8, detects paper pulp yield and white respectively
Degree, the results are shown in table below.
| Experimental project | Paper pulp yield, % | Whiteness, %ISO |
| Embodiment 1 | 62.11 | 50.64 |
| Embodiment 2 | 63.58 | 51.43 |
| Embodiment 3 | 65.32 | 53.24 |
| Comparative example 1 | 57.36 | 46.65 |
| Comparative example 2 | 53.86 | 44.01 |
| Comparative example 3 | 56.31 | 45.86 |
| Comparative example 4 | 55.15 | 45.01 |
| Comparative example 5 | 50.38 | 41.05 |
| Comparative example 6 | 46.14 | 37.16 |
| Comparative example 7 | 47.61 | 37.82 |
| Comparative example 8 | 42.0 | 42.2 |
Can it is found that being not added with percarbamide, amino carboxylic acid, vanadic anhydride in secondary pretreatment immersion liquid B by comparative example 1-4
Paper pulp yield and whiteness are reduced, this is because percarbamide can slowly release hydrogen peroxide, the hydrogen peroxide released and wood
Element reaction is conducive to improve paper pulp yield and whiteness；Amino carboxylic acid can play chelation；Vanadic anhydride plays the work of catalysis
With；Understand that percarbamide, amino carboxylic acid, vanadic anhydride add by the paper pulp yield and whiteness of example 3 and comparative example 1-4 simultaneously
Add and play synergistic effect, improves paper pulp yield and whiteness.
By comparative example 5-7 it is found that being once not added with alkyl phenol polyoxyethylene ether, triethanolamine, tristearin in pretreatment immersion liquid A
Acid, oleic acid, lauric acid can reduce paper pulp yield and whiteness, this is because alkyl phenol polyoxyethylene ether, triethanolamine are moistening
Agent plays good humidification；Stearic acid, oleic acid, lauric acid play sinocalamus latiflorus piece surface-active action；Simultaneously by example 3
With the paper pulp yield and whiteness of comparative example 5-7 known to alkyl phenol polyoxyethylene ether, triethanolamine, stearic acid, oleic acid, lauric
Addition plays synergistic effect, improves paper pulp yield and whiteness.
In addition, by with upper table it is found that paper pulp yield and whiteness made from the preparation process of the present invention be significantly above it is existing
Paper pulp yield made from technology and whiteness.
The above content is a further detailed description of the present invention in conjunction with specific preferred embodiments, and it cannot be said that
The specific implementation of the present invention is confined to these explanations, for person of an ordinary skill in the technical field, is not departing from
Under the premise of present inventive concept, a number of simple deductions or replacements can also be made, all shall be regarded as belonging to the present invention by being submitted
Claims determine scope of patent protection.
Claims (10)
1. a kind of primary pretreatment immersion liquid A, it is characterised in that：As unit of parts by weight, including following raw material：Alkyl phenol polyoxy second
4-8 parts of alkene ether, 0.3-0.6 parts of triethanolamine, 0.5-1 parts of stearic acid, 0.4-1.2 parts of oleic acid, 0.8-1.5 parts of lauric acid, water 42-
90 parts.
2. primary pretreatment immersion liquid A according to claim 1, it is characterised in that：As unit of parts by weight, including following original
Material：6 parts of alkyl phenol polyoxyethylene ether, 0.5 part of triethanolamine, 0.8 part of stearic acid, 0.8 part of oleic acid, 1.2 parts of lauric acid, water 66
Part.
3. a kind of primary pretreatment immersion liquid A according to claim 1 or 2 is in the application for preparing sinocalamus latiflorus true qualities paper pulp, spy
Sign is：The preparation method of the sinocalamus latiflorus true qualities paper pulp, includes the following steps：
S1：Sinocalamus latiflorus is cut into sinocalamus latiflorus piece, is delivered in primary pretreatment immersion liquid A, immersion 30- is carried out under ul-trasonic irradiation
45min is then filtered, and obtains leaching material A；
S2：Leaching material A made from step S1 is delivered in secondary pretreatment immersion liquid B, the secondary pretreatment immersion liquid B is with parts by weight
For unit, including following raw material：10-20 parts of percarbamide, 4-6 parts of potassium hydroxide, 0.3-0.5 parts of amino carboxylic acid, five oxidations two
0.1-0.2 parts of vanadium, 35-150 parts of water, immersion 20-40min is carried out under ul-trasonic irradiation, is then filtered, and obtains leaching material B；
S3：Leaching material B made from step S2 is washed with hot water, is then dehydrated, dehydrated material C is made；
S4：Dehydrated material C made from step S3 is ground, thick slurry is made；
S5：It is washed slightly being starched made from step S4, uses screening concentration for 0.6%-2.5%, inlet outlet pressure differential 0.12-
The pressurized screen of 0.35MPa is screened, and carries out press filtration using into the Double-screen filter press for starching a concentration of 2.4%-5.3%, fiber crops are made
Bamboo true qualities paper pulp.
4. primary pretreatment immersion liquid A according to claim 3 is in the application for preparing sinocalamus latiflorus true qualities paper pulp, it is characterised in that：
The size of sinocalamus latiflorus piece described in step S1 is 24-28 × 3-3.6mm × 1.4-2mm.
5. primary pretreatment immersion liquid A according to claim 3 is in the application for preparing sinocalamus latiflorus true qualities paper pulp, it is characterised in that：
The ratio between sinocalamus latiflorus weight described in step S1 and primary pretreatment immersion liquid A volumes are 1:2-4.
6. primary pretreatment immersion liquid A according to claim 3 is in the application for preparing sinocalamus latiflorus true qualities paper pulp, it is characterised in that：
Ultrasonic power described in step S1 is 30-50W, and temperature is 43-48 DEG C.
7. primary pretreatment immersion liquid A according to claim 3 is in the application for preparing sinocalamus latiflorus true qualities paper pulp, it is characterised in that：
Leaching material described in step S2 the ratio between A weight and secondary pretreatment immersion liquid B volumes are 1:6-13.
8. primary pretreatment immersion liquid A according to claim 3 is in the application for preparing sinocalamus latiflorus true qualities paper pulp, it is characterised in that：
Ultrasonic power described in step S2 is 40-80W, and temperature is 85-92 DEG C.
9. primary pretreatment immersion liquid A according to claim 3 is in the application for preparing sinocalamus latiflorus true qualities paper pulp, it is characterised in that：
The temperature of hot water described in step S3 is 60-80 DEG C.
10. primary pretreatment immersion liquid A according to claim 3 is in the application for preparing sinocalamus latiflorus true qualities paper pulp, it is characterised in that：
Washing described in step S3 to pH value is 6.8-7.2.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710358395.6A CN107044063B (en) | 2017-05-19 | 2017-05-19 | A kind of once pretreatment immersion liquid A and its application |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710358395.6A CN107044063B (en) | 2017-05-19 | 2017-05-19 | A kind of once pretreatment immersion liquid A and its application |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN107044063A CN107044063A (en) | 2017-08-15 |
| CN107044063B true CN107044063B (en) | 2018-08-03 |
Family
ID=59546489
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710358395.6A Active CN107044063B (en) | 2017-05-19 | 2017-05-19 | A kind of once pretreatment immersion liquid A and its application |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107044063B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107858845A (en) * | 2017-09-30 | 2018-03-30 | 广西金荣纸业有限公司 | A kind of two stage treatment liquid and its application in production high-strength corrugated paper |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1916272A (en) * | 2006-09-02 | 2007-02-21 | 广西大学 | Method for blowing up pretreated APMP pulp by using bamboo as raw material |
| CN1974921A (en) * | 2006-12-18 | 2007-06-06 | 河北吉藁化纤有限责任公司 | Method for producing bamboo pomace |
| EP1084291B1 (en) * | 1998-05-05 | 2008-07-02 | Chempolis Oy | Process for producing pulp with a mixture of formic acid and acetic acid as cooking chemical |
| CN102174765A (en) * | 2010-12-01 | 2011-09-07 | 江西含珠实业有限公司 | Technological process for making Lian-si paper by using moso bamboo |
| CN102978993A (en) * | 2012-11-26 | 2013-03-20 | 四川银鸽竹浆纸业有限公司 | Bamboo fiber dissolving pulp and production technology thereof |
-
2017
- 2017-05-19 CN CN201710358395.6A patent/CN107044063B/en active Active
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1084291B1 (en) * | 1998-05-05 | 2008-07-02 | Chempolis Oy | Process for producing pulp with a mixture of formic acid and acetic acid as cooking chemical |
| CN1916272A (en) * | 2006-09-02 | 2007-02-21 | 广西大学 | Method for blowing up pretreated APMP pulp by using bamboo as raw material |
| CN1974921A (en) * | 2006-12-18 | 2007-06-06 | 河北吉藁化纤有限责任公司 | Method for producing bamboo pomace |
| CN102174765A (en) * | 2010-12-01 | 2011-09-07 | 江西含珠实业有限公司 | Technological process for making Lian-si paper by using moso bamboo |
| CN102978993A (en) * | 2012-11-26 | 2013-03-20 | 四川银鸽竹浆纸业有限公司 | Bamboo fiber dissolving pulp and production technology thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN107044063A (en) | 2017-08-15 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107184132B (en) | A kind of preparation method of finished product sinocalamus latiflorus toilet paper | |
| CN107119477B (en) | A kind of sinocalamus latiflorus true qualities paper pulp and its preparation process | |
| CN109577059B (en) | Method for preparing biomechanical unbleached pulp by wheat straw | |
| CN107174155B (en) | A kind of toilet paper prepared using bleaching process | |
| CN110644270B (en) | Process for producing dissolving pulp by TCF bleaching of poplar KP pulp | |
| CN107177996A (en) | A kind of preprocess method of bleached pulp | |
| CN107090730B (en) | A method of preparing true qualities paper pulp using sinocalamus latiflorus | |
| US9951476B2 (en) | Chemical pulping method | |
| CN103821022B (en) | The method of neutral cellulase preliminary treatment needle slurry and broad-leaved slurry | |
| CN1811055A (en) | Production process of bleached chemical pulp with hemp stalk core | |
| CN102121201A (en) | Preparation method of bamboo dissolving pulp | |
| CN112442922A (en) | Method for producing degradable mulching film paper by using bamboo pulp | |
| CN107044063B (en) | A kind of once pretreatment immersion liquid A and its application | |
| CN107700275A (en) | A kind of preparation method of high-strength corrugated paper | |
| CN107034717B (en) | A kind of preprocess method preparing sinocalamus latiflorus true qualities paper pulp | |
| CN102587185B (en) | Method for cleaning and bleaching eucalyptus dissolving pulp | |
| CN1970850A (en) | Method for making bamboo pulp for use in preparation of artificial fiber | |
| CN107034712B (en) | A kind of novel papermaking method | |
| CN107030817B (en) | A kind of secondary pretreatment immersion liquid B and its application in preparation sinocalamus latiflorus true qualities paper pulp | |
| CN104928958A (en) | Method of producing corrugated paper with straw | |
| CN107326714B (en) | A kind of preparation method of finished product sinocalamus latiflorus body paper | |
| CN102747636B (en) | The method preparing high bulk Eucalyptus APMP | |
| CN110593010A (en) | Preparation method of corrugated base paper | |
| CN107338666B (en) | A kind of method that sinocalamus latiflorus prepares bleached pulp | |
| CN108221470B (en) | Method for preparing semi-chemical pulp by using broadleaf wood board skin as raw material |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190107 Address after: 530103 Yiling Village, Shuangqiao Town, Wuming District, Nanning City, Guangxi Zhuang Autonomous Region Patentee after: GUANGXI JIANIAN AGRICULTURE CO.,LTD. Address before: Room 1602, Unit A, 10 Building No. 20-1 Dongge Road, Qingxiu District, Nanning City, Guangxi Zhuang Autonomous Region Patentee before: GUANGXI NANNING CHENGYUAN TECHNOLOGY CO.,LTD. Effective date of registration: 20190107 Address after: Room 1602, Unit A, 10 Building No. 20-1 Dongge Road, Qingxiu District, Nanning City, Guangxi Zhuang Autonomous Region Patentee after: GUANGXI NANNING CHENGYUAN TECHNOLOGY CO.,LTD. Address before: 531504 Twelve Bridges in Silin Town, Tiandong County, Baise City, Guangxi Zhuang Autonomous Region Patentee before: GUANGXI JIN RONG PAPER Co.,Ltd. |