CN109265707A - A method of separation wood lignin - Google Patents

A method of separation wood lignin Download PDF

Info

Publication number
CN109265707A
CN109265707A CN201811129799.9A CN201811129799A CN109265707A CN 109265707 A CN109265707 A CN 109265707A CN 201811129799 A CN201811129799 A CN 201811129799A CN 109265707 A CN109265707 A CN 109265707A
Authority
CN
China
Prior art keywords
lignin
acid
formic acid
methyl benzenesulfonic
filter
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.)
Pending
Application number
CN201811129799.9A
Other languages
Chinese (zh)
Inventor
王松林
王飞
邢仁卫
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Qingdao University of Science and Technology
Original Assignee
Qingdao University of Science and Technology
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Qingdao University of Science and Technology filed Critical Qingdao University of Science and Technology
Priority to CN201811129799.9A priority Critical patent/CN109265707A/en
Publication of CN109265707A publication Critical patent/CN109265707A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08HDERIVATIVES OF NATURAL MACROMOLECULAR COMPOUNDS
    • C08H6/00Macromolecular compounds derived from lignin, e.g. tannins, humic acids

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Biochemistry (AREA)
  • Materials Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Compounds Of Unknown Constitution (AREA)

Abstract

The present invention provides a kind of method for separating wood lignin, can isolate lignin under conditions of protecting cellulose not oxidized;Solve the problems, such as that traditional slurrying isolated lignin process cycle is long, energy consumption is high, chemicals recycling is difficult.Compared with prior art, the present invention shortening reaction time, energy consumption is low in separation process, reaction condition is mild, and drug price is cheap and is easy to get, and p-methyl benzenesulfonic acid, formic acid are easily recycled, p-methyl benzenesulfonic acid, the formic acid of recycling can reuse, and save the cost belongs to environmentally friendly.

Description

A method of separation wood lignin
Technical field
The invention belongs to lignin separation technology fields in timber, and in particular to a kind of p-methyl benzenesulfonic acid-formic acid separation timber The method of lignin.
Background technique
Lignin as the most abundant organic matter of second (cellulose is first) in the world, be it is a kind of it is easy to use can Regenerated resources, separation is using as focus concerned by people in recent years.Lignin is that three kinds of benzene oxide units pass through ehter bond and carbon The boiomacromolecule with tridimensional network that carbon key is interconnected to form plays resistance to compression work between cellulose fibre With.Its purposes is very extensive, such as in the oil industry, can do heavy crude thinner, high temperature tune flux, grease coagulant etc..Except this Except can also do cement water reducing agent, urea-formaldehyde adhesive prepares surfactant, soil conditioner, prepares novel water-coal-slurry Additive etc..Lignin is also applied to rubber industry, is used as rubber reinforcing filler, gum filler etc..
But lignin is studied, first has to isolate lignin.Industrially, lignin products to be obtained mainly it is exactly by by alkali For black liquid separation obtained in method slurrying and sulfite pulping come what is obtained, the Lignin Molecular Weight obtained under this approach is past It is arrived between tens of thousands of toward hundreds of, they have the distribution of significant wide molecular weight, so as to cause industrial lignin without stabilization Thermal transition temperature the characteristics of, the lignin in addition to this obtained by this method is also unfavorable for deeper development and utilization. And traditional lignin separation method also can cause environmental pollution, and it is extremely urgent to develop new lignin separation method.
It is existing to use acid, alkali, overcritical, two water phases, the method for mitigating the means separating lignins such as hydrogenolysis, ionic liquid.Acid Lignin includes klason lignin, periodic acid lignin, phosphoric acid lignin etc., and Klason chemical modification of lignin is big, unfavorable In the utilization of lignin.Periodic acid lignin is aoxidized, and phosphoric acid lignin condition mitigates, and chemical modification is small, but has one Fixed polymerization.Alkali lignin is conducive to lignin dissolution in heating, and chemical modification occurs for lignin during this.Alkali soluble lignin oxygen Change serious, carbonyl and carboxyl increase.For organic solvent type lignin other than dioxacyclohexanes, organic solvent is pure in conjunction with lignin Degree is not high, is not easily recycled.
Summary of the invention
The present invention provides a kind of method for separating wood lignin, can divide under conditions of protecting cellulose not oxidized Separate out lignin;Solve the problems, such as that traditional slurrying isolated lignin process cycle is long, energy consumption is high, chemicals recycling is difficult.
The method of separation wood lignin of the invention, comprises the following steps that
1) wood powder is added in 60 DEG C -90 DEG C of toluenesulfonic acid-formic acid solution and is reacted;
Toluenesulfonic acid-the formic acid solution, wherein the volume ratio of toluenesulfonic acid and formic acid is 1-20:1;
Preferably, the volume ratio that wherein toluenesulfonic acid and formic acid are is 5:1,
The reaction is that revolving reaction or oscillating reactions are carried out under the conditions of water bath with thermostatic control;
2) after reaction, separating filtrate and filter residue;Filtrate is diluted with deionized water, precipitating is generated, will precipitate It filters out and obtains lignin and acid pickle;
The spent acid first passes through distillation, recycles formic acid, then pass through cooling concentration and recovery p-methyl benzenesulfonic acid again;
The wood powder, preferably cotton wood powder.
In the step 2), the usage amount of deionized water is the ph value 7.0-7.5 for making filtrate.
Compared with prior art, the beneficial effects of the invention are that:
The present invention handles timber using a kind of novel separation method p-methyl benzenesulfonic acid-formic acid, and then isolates in timber Various substances.Lignin can be isolated under the premise of protecting cellulose not oxidized.
Compared with prior art, the present invention this method can dissolve greatly in relatively low temperature, in the short time Measure lignin;And the condition that traditional handicraft reaches same effect needs is harsher.
Compared with prior art, the present invention shortening reaction time, energy consumption is low in separation process, and reaction condition is mild, Drug price is cheap and is easy to get, and p-methyl benzenesulfonic acid, formic acid are easily recycled, and p-methyl benzenesulfonic acid, the formic acid of recycling can reuse, Save the cost belongs to environmentally friendly.
The method and process simple possible and safety of isolated lignin of the present invention, convenient for operation.
It is the method and process route economy of isolated lignin of the present invention, environmentally protective, it is easy to realization of industrialization.
Detailed description of the invention
Fig. 1: the infrared analysis figure of the lignin extracted in the filtrate of embodiment 4.
Fig. 2: the filter residue in the product and embodiment 4 in embodiment 2 carries out X-ray diffraction (XRD) analysis chart.
Fig. 3: the sem analysis figure of poplar sawdust, fiber in embodiment 1 and embodiment 4.
Specific embodiment
The present invention separates the lignin in poplar, p-methyl benzenesulfonic acid-formic acid isolated lignin using p-methyl benzenesulfonic acid-formic acid A large amount of lignin can be isolated in the short time, and right at low temperature (traditional subtraction slurrying isolated lignin needs 140-160 DEG C) Toluenesulfonic acid and formic acid recovery process are extremely convenient, and lignin can be isolated under conditions of protecting cellulose not oxidized by reaching.
The affected step of the present invention is described in detail combined with specific embodiments below, but not as the limitation of the invention.
Embodiment 1: survey poplar in lignin content the following steps are included:
(a) ethyl alcohol and 113.33 milliliters of benzene for measuring 56.67 milliliter 72% are uniformly mixed, and have configured benzene-alcohol mixeding liquid It is spare.1.0023g poplar sawdust accurately is weighed, is wrapped with qualitative filter paper, is tied with line.It puts in people's Soxhlet extractor with benzene -ol Mixed liquor extracts six hours in boiling water, then takes out sample and air-dries.
(b) filter paper packet is unlocked, air-dried sample is carefully moved into people 250ml in the conical flask of ground glass stopper, adds people 15ml is pre-adjusted 72% sulfuric acid that temperature is 13 DEG C, sways 1min, impregnates sample by acid completely, then places it in Kept for two hours sway always in insulating process in 18 DEG C of water bath and at this temperature.
(c) after two hours, sample distillation is washed in one liter of conical flask, and the concentration of dilute acid is 3%, it is added Distilled water adds up to 560ml including flushing water.Reflux condenser is loaded on conical flask, boils 4h.
(d) heating finishes, and stands, insoluble matter is made to precipitate, the 1G3 then crossed with preparatory constant weight, mistake in glass filter Filter, reusable heat distills water washing residue, until washing lotion is no acidic, with the not aobvious muddiness of 10% barium chloride solution examination.It inhales Dry filtrate, takes out filter, and cleaned outside filter with distilled water, and filter and residue are placed in baking oven, are dried to perseverance at 105 DEG C Weight, obtains lignin.
Lignin content is 28.12% in poplar sawdust used in the present invention.
Embodiment 2: measurement poplar in content of cellulose the following steps are included:
(a) take 800ml chemistry straight alcohol (95%) in the 1000ml beaker of a clean dried with clean dried graduated cylinder, then It takes the pure nitric acid (relative density 1.42) of 200ml chemistry to be poured into ethyl alcohol by several times slowly with another clean dried graduated cylinder, is added every time About 10ml, and continuously added after being stirred evenly with glass bar.
(b) 1.0134g poplar sawdust accurately is weighed in the conical flask of 250ml clean dried, 25ml nitric acid ethyl alcohol is added Mixed solution loads onto reflux condenser, until heating 1h on boiling water bath, during heating, should sway conical flask at any time.
(c) condenser pipe is removed, conical flask is removed from water-bath, a moment is stood, uses gradient method after residue deposition The 1G of constant weight2.It is filtered in glass filter, flows out residue as far as possible.
(d) filtrate in filter is blotted with vacuum pump, then moves people's conical flask for the residue in filter is flowed into glass bar In.
(e) 25m nitric acid alcohol mixed solution is measured, the residue of filter and dimension shape bottleneck attachment is moved into conical flask, dress Upper condensation reflux device, then 1h is heated on boiling water bath.During heating.It should be noted that conical flask is swayed frequently,
(f) it is so repeated 3 times, until fiber bleaches.
(g) conical flask content is all finally moved into filter, washs residue with 10mI nitric acid alcohol mixed solution, then use Hot water washs until washing lotion methyl orange reagent is not in acidity.Finally twice with ethanol washing.
(h) washing lotion is blotted, filter is taken out, will be cleaned, moved in people's baking oven outside filter with distilled water, dried in (105 scholar 3) DEG C Drying to constant weight in case.
(i) weighing and calculating content of cellulose.
Content of cellulose is 58.3% in poplar sawdust used in the present invention.
Embodiment 3: the present embodiment isolated lignin method the following steps are included:
(a) according to p-methyl benzenesulfonic acid: formic acid volume ratio is the condition of 1:1, takes 37.5102 grams of p-methyl benzenesulfonic acid, quality dense Degree weighs 42.6023 grams for 88% formic acid, measures 50ml deionized water in the flask of 500ml, configures 60% mass concentration P-methyl benzenesulfonic acid-formic acid solution, p-methyl benzenesulfonic acid-formic acid solution is heated.
(b) 60 DEG C are heated to p-methyl benzenesulfonic acid-formic acid solution, 5 grams of poplar sawdusts, the size of poplar sawdust is then added For 30~50 mesh, flask is put into 100rpm thermostatic control oscillator vibration, 5 minute reaction time was set, starts to react.
(c) after to the preset reaction time, flask is taken out, and terminate reaction.
(d) it is cooled to room temperature to product in flask, vacuum filter is carried out to product, obtains filtrate and filter residue.
(e) filter residue obtained is cleaned with deionized water, and is detected with barium chloride, until liquid is no longer muddy, It washs to neutrality.Filter residue is subjected to constituent analysis, wherein lignin content is 16.9%.
(f) obtained filtrate being diluted, until being diluted to acid concentration is 10%, stands 30min, solution becomes cloudy, There is solid precipitation.Again with being filtered, solid is filtered out.And solid is dried, weighing and calculating is molten Produce rate is 48.33% out
Embodiment 4:
(a) according to p-methyl benzenesulfonic acid: formic acid is the condition of 5:1, takes 97.2365 grams of the p-methyl benzenesulfonic acid, mass concentration to be 88% formic acid weighs 22.1290 grams, measures 50ml deionized water in the flask of 500ml, configures pair of 70% mass concentration Toluenesulfonic acid-formic acid solution heats p-methyl benzenesulfonic acid-formic acid solution.
(b) 80 DEG C are heated to p-methyl benzenesulfonic acid-formic acid solution, 5 grams of poplar sawdusts, the size of poplar sawdust is then added For 30~50 mesh, flask is put into 100rpm thermostatic control oscillator vibration, 20 minute reaction time was set, starts to react.
(c) after to the preset reaction time, flask is taken out, and terminate reaction.
(d) it is cooled to room temperature to product in flask, vacuum filter is carried out to product, obtains filtrate and filter residue.
(e) filter residue obtained is cleaned with deionized water, and is detected with barium chloride, until liquid is no longer muddy, It washs to neutrality.Filter residue is subjected to constituent analysis, wherein lignin content is 11.47%.
(f) obtained filtrate being diluted, until being diluted to acid concentration is 10%, stands 30min, solution becomes cloudy, There is solid precipitation.Again with being filtered, solid is filtered out.And solid is dried, weighing and calculating is molten Object (lignin) yield is 83.15% out
Step (e) is diluted acid solution with deionized water, and dilute strength is that the mass concentration of p-methyl benzenesulfonic acid is 11% ~5%.Dilute strength is different, and lignin granular size is different, and granular size is 300 nanometers~3000 nanometers.Dilute strength is bigger, Particle is bigger.
Embodiment 5: the present embodiment isolated lignin method the following steps are included:
(a) according to p-methyl benzenesulfonic acid: formic acid is the condition of 10:1, takes 181.8236 grams of the p-methyl benzenesulfonic acid, mass concentration to be 88% formic acid weighs 20.7864 grams, measures 50ml deionized water in the flask of 500ml, configures pair of 80% mass concentration Toluenesulfonic acid-formic acid solution heats p-methyl benzenesulfonic acid-formic acid solution.
(b) 80 DEG C are heated to p-methyl benzenesulfonic acid-formic acid solution, 5 grams of poplar sawdusts, the size of poplar sawdust is then added For 30~50 mesh, flask is put into 100rpm thermostatic control oscillator vibration, 10 minute reaction time was set, starts to react.
(c) after to the preset reaction time, flask is taken out, and terminate reaction.
(d) it is cooled to room temperature to product in flask, vacuum filter is carried out to product, obtains filtrate and filter residue.
(e) filter residue obtained is cleaned with deionized water, and is detected with barium chloride, until liquid is no longer muddy, It washs to neutrality.Constituent analysis is carried out to filter residue, wherein lignin content is 19.42%.
(f) obtained filtrate being diluted, until being diluted to acid concentration is 10%, stands 30min, solution becomes cloudy, There is solid precipitation.Again with being filtered, solid is filtered out.And solid is dried, weighing and calculating is molten Object (lignin) yield is 68.93% out
Embodiment 6: the present embodiment isolated lignin method the following steps are included:
(a) according to p-methyl benzenesulfonic acid: formic acid is the condition of 20:1, takes 428.5422 grams of the p-methyl benzenesulfonic acid, mass concentration to be 88% formic acid weighs 24.3566 grams, measures 50ml deionized water in the flask of 500ml, configures pair of 90% mass concentration Toluenesulfonic acid-formic acid solution heats p-methyl benzenesulfonic acid-formic acid solution.
(b) 80 DEG C are heated to p-methyl benzenesulfonic acid-formic acid solution, 5 grams of poplar sawdusts, the size of poplar sawdust is then added For 30~50 mesh, flask is put into 100rpm thermostatic control oscillator vibration, 20 minute reaction time was set, starts to react.
(c) after to the preset reaction time, flask is taken out, and terminate reaction.
(d) it is cooled to room temperature to product in flask, vacuum filter is carried out to product, obtains filtrate and filter residue.
(e) filter residue obtained is cleaned with deionized water, and is detected with barium chloride, until liquid is no longer muddy, It washs to neutrality.Filter residue is subjected to constituent analysis, wherein lignin content is 18.19%.
(f) obtained filtrate being diluted, until being diluted to acid concentration is 10%, stands 30min, solution becomes cloudy, There is solid precipitation.Again with being filtered, solid is filtered out.And solid is dried, weighing and calculating is molten Object (lignin) yield is 60.16% out.
Embodiment 3-6 acquired results are available, when p-methyl benzenesulfonic acid and formic acid are 5:1, mass concentration 70%, temperature It is 80 DEG C, when the reaction time is 20 minutes, lignin the amount of dissolution is most, is optimal case.
Infrared analysis is carried out to the lignin extracted in filtrate in embodiment 4, as a result such as Fig. 1.The experimental results showed that toluene The lignin of sulfonic acid processing, 3417cm-1The stretching vibration enhancing for locating O-H key in phenolic hydroxyl group and alcoholic extract hydroxyl group, compared with acid-insoluble lignin, Peak position shifts, by 3422cm-1It is displaced to 3417cm-1.The C-H vibration of methyl, methylene increases in lignin at 2924cm-1 By force, peak position is displaced to 2924cm-1 by 2934cm-1.It is the C in non-conjugated ketone, carbonyls and ester group at 1714cm-1 The enhancing of=O stretching vibration bands of a spectrum.1400cm-1 to 1497cm-1 aromatic backbone vibrational band enhance.Lilac at 1327cm-1 C-O vibration disappearance in guaiacyl OCH at nuclear vibration and 1270cm-1.The ehter bond C-H vibration of S type lignin subtracts at 1231cm-1 It is weak, there is the C-O-C stretching vibration of 1180cm-1 absorption peak ehter bond.There is 567cm-1 to 814cm-1 absorption peak.
X-ray diffraction (XRD) analysis is carried out to the filter residue in the fiber and embodiment 4 in embodiment 2, it is real as a result such as Fig. 2 Test the result shows that, two kinds of cellulose peak positions are constant, and the cellulose peak value obtained after the processing of p-methyl benzenesulfonic acid-formic acid reduces very Few, crystallinity still keeps higher.
Scanning electron microscope is done to the filter residue fiber in poplar sawdust, 2 fiber of embodiment and embodiment 4, as a result such as Fig. 3.Comparison The form that two kinds of isolated lignins obtain fiber can be seen that by p-methyl benzenesulfonic acid-formic acid treated fiber filter residue structure more There is interformational sliding and peeling fluffiness, illustrate by first in Gabon pine, fibrocyte layer especially compound middle lamella Benzene sulfonic acid-formic acid treatment process can not only lignin between fast degradation fibrocyte, while can also effectively permeate and fibre of degrading Intracellular lignin is tieed up, delignification effect is higher.
Outside divided by above-described embodiment, the present invention can also have other embodiments.Above-described embodiment is only exemplary implementation Example, is not used in the limitation present invention, all technical solutions formed using equivalent substitute or equivalent transformation, the present invention claims Protection scope.

Claims (7)

1. a kind of method for separating wood lignin, which is characterized in that the method comprises the following steps that
1) wood powder is added in 60 DEG C -90 DEG C of toluenesulfonic acid-formic acid solution and is reacted;
2) after reaction, separating filtrate and filter residue;Filtrate is diluted with deionized water, generates precipitating, precipitating is filtered Lignin and acid pickle are obtained out.
2. the method as described in claim 1, which is characterized in that the toluenesulfonic acid-formic acid solution, wherein toluenesulfonic acid and The volume ratio of formic acid is 1-20:1.
3. the method as described in claim 1, which is characterized in that the toluenesulfonic acid-formic acid solution, wherein toluenesulfonic acid and The volume ratio of formic acid is 5:1.
4. the method as described in claim 1, which is characterized in that the reaction in the step 1) is under the conditions of water bath with thermostatic control Carry out revolving reaction or oscillating reactions.
5. the method as described in claim 1, which is characterized in that the wood powder is cotton wood powder.
6. the method as described in claim 1, which is characterized in that the spent acid first passes through distillation, recycles formic acid, then by cold But concentration and recovery p-methyl benzenesulfonic acid again.
7. the method as described in claim 1, which is characterized in that in the step 2), the usage amount of deionized water is to make to filter The ph value of liquid is 7.0-7.5.
CN201811129799.9A 2018-09-27 2018-09-27 A method of separation wood lignin Pending CN109265707A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811129799.9A CN109265707A (en) 2018-09-27 2018-09-27 A method of separation wood lignin

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811129799.9A CN109265707A (en) 2018-09-27 2018-09-27 A method of separation wood lignin

Publications (1)

Publication Number Publication Date
CN109265707A true CN109265707A (en) 2019-01-25

Family

ID=65198990

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811129799.9A Pending CN109265707A (en) 2018-09-27 2018-09-27 A method of separation wood lignin

Country Status (1)

Country Link
CN (1) CN109265707A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109929262A (en) * 2019-03-19 2019-06-25 福建农林大学 A method of preparing high-strength Wood-plastic material
CN110818912A (en) * 2019-10-23 2020-02-21 广东工业大学 Method for rapidly preparing nanoscale lignin
CN111286039A (en) * 2020-03-26 2020-06-16 齐鲁工业大学 Method for separating and extracting high-activity lignin by taking needle-leaved wood as raw material

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103998617A (en) * 2011-12-20 2014-08-20 花王株式会社 Method for producing lignin degradation product
CN104389216A (en) * 2014-10-21 2015-03-04 国际竹藤中心 Method for separating lignin and holocellulose from wood fiber raw materials and application thereof
US20180215774A1 (en) * 2017-01-30 2018-08-02 The United States Of America As Represented By The Secretary Of Agriculture Low Temperature and Efficient Fractionation of Lignocellulosic Biomass Using Recyclable Organic Solid Acids

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103998617A (en) * 2011-12-20 2014-08-20 花王株式会社 Method for producing lignin degradation product
CN104389216A (en) * 2014-10-21 2015-03-04 国际竹藤中心 Method for separating lignin and holocellulose from wood fiber raw materials and application thereof
US20180215774A1 (en) * 2017-01-30 2018-08-02 The United States Of America As Represented By The Secretary Of Agriculture Low Temperature and Efficient Fractionation of Lignocellulosic Biomass Using Recyclable Organic Solid Acids

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
贾玲等: "有机酸水溶液提取玉米芯木质素及其性质", 《精细化工》 *
路瑶等: "《稻壳和麦秆及其萃余物的逐级氧化》", 31 August 2017, 中国矿业大学出版社 *

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109929262A (en) * 2019-03-19 2019-06-25 福建农林大学 A method of preparing high-strength Wood-plastic material
CN109929262B (en) * 2019-03-19 2021-12-14 福建农林大学 Method for preparing high-strength wood-plastic material
CN110818912A (en) * 2019-10-23 2020-02-21 广东工业大学 Method for rapidly preparing nanoscale lignin
CN111286039A (en) * 2020-03-26 2020-06-16 齐鲁工业大学 Method for separating and extracting high-activity lignin by taking needle-leaved wood as raw material
CN111286039B (en) * 2020-03-26 2022-02-01 齐鲁工业大学 Method for separating and extracting high-activity lignin by taking needle-leaved wood as raw material

Similar Documents

Publication Publication Date Title
CN109265707A (en) A method of separation wood lignin
CN103711017B (en) A kind ofly prepare the method for cellulose and lignin as solvent normal pressure ultrasonic wave is auxiliary taking the height alcohol that boils
CN101649160B (en) Method for producing refined light-color rosin by using turpentine as raw material
CN106832757A (en) A kind of composite of Graphene phenol-formaldehyde resin modified and preparation method thereof, application
CN104142321A (en) Method for fast detecting surface enhancing Raman spectrums of pesticide residues in tea leaves
CN102321383A (en) The preparation method of vegatable tannin dye liquor and the application aspect silk fabric dyeing thereof
CN106854264A (en) A kind of rice husk sill quality modified phenolic resin adhesive preparation method
CN106633099A (en) Production method for high-activity lignin
CN110585933A (en) Preparation method of nano-iron-calcium alginate composite membrane for removing hexavalent chromium
Rietzler et al. Investigation of the decomplexation of polyamide/CaCl2 complex toward a green, nondestructive recovery of polyamide from textile waste
CN101665660B (en) A kind of method of refining and processing rosin
CN103290502B (en) The method for making of the native cellulose fibre of the resistance to combustion function of tool
CN104655580A (en) Method for quickly determining content of alpha-cellulose in dissolving pulp
CN105294883B (en) A kind of method that diluted acid-pressurization prepares beet pectin
CN106468032A (en) The method and device of lignin is extracted a kind of black liquor from sulfate pulping
CN110465271A (en) A kind of synthetic method and application of temperature control targeted capture material
CN109627348A (en) The method of microcrystalline cellulose is extracted from Taxus x media branch residue
KR101130647B1 (en) Natural dye, Method for manufacturing the same and Dyeing method using the same
US2423020A (en) Process for treatment of lumber and other forest products
CN110183621A (en) The synthesis of covalent organic polymer with ionic liquid and its application in Dye Adsorption
CN106317418A (en) Method for preparing sodium ligninsulfonate from corncob acidolysis residue soda-boiling black liquid
CN106632515A (en) Method for degrading lignin by ionic liquid catalyzed alcohol system
DE19844246B4 (en) Method for recovering waste heat during the polymer coagulation step by means of an absorption heat pump
Lehnen et al. Impact of pulping conditions on Formacell Aspen Lignin: Investigation of methoxyl and ester groups, carbohydrates, molar mass and glass transition temperatures
Wang et al. Liquefaction processes and characterization of liquefied products from waste woody materials in different acidic catalysts

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
RJ01 Rejection of invention patent application after publication

Application publication date: 20190125

RJ01 Rejection of invention patent application after publication