CN109517547A - Smoke removing method is gone using ultrasonic atomization technique - Google Patents
Smoke removing method is gone using ultrasonic atomization technique Download PDFInfo
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07D—HETEROCYCLIC COMPOUNDS
- C07D307/00—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom
- C07D307/02—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings
- C07D307/34—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members
- C07D307/38—Heterocyclic compounds containing five-membered rings having one oxygen atom as the only ring hetero atom not condensed with other rings having two or three double bonds between ring members or between ring members and non-ring members with substituted hydrocarbon radicals attached to ring carbon atoms
- C07D307/40—Radicals substituted by oxygen atoms
- C07D307/46—Doubly bound oxygen atoms, or two oxygen atoms singly bound to the same carbon atom
- C07D307/48—Furfural
- C07D307/50—Preparation from natural products
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B1/00—Preparatory treatment of cellulose for making derivatives thereof, e.g. pre-treatment, pre-soaking, activation
- C08B1/08—Alkali cellulose
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B11/00—Preparation of cellulose ethers
- C08B11/02—Alkyl or cycloalkyl ethers
- C08B11/04—Alkyl or cycloalkyl ethers with substituted hydrocarbon radicals
- C08B11/10—Alkyl or cycloalkyl ethers with substituted hydrocarbon radicals substituted with acid radicals
- C08B11/12—Alkyl or cycloalkyl ethers with substituted hydrocarbon radicals substituted with acid radicals substituted with carboxylic radicals, e.g. carboxymethylcellulose [CMC]
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G8/00—Condensation polymers of aldehydes or ketones with phenols only
- C08G8/04—Condensation polymers of aldehydes or ketones with phenols only of aldehydes
- C08G8/08—Condensation polymers of aldehydes or ketones with phenols only of aldehydes of formaldehyde, e.g. of formaldehyde formed in situ
- C08G8/10—Condensation polymers of aldehydes or ketones with phenols only of aldehydes of formaldehyde, e.g. of formaldehyde formed in situ with phenol
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
- C08G8/00—Condensation polymers of aldehydes or ketones with phenols only
- C08G8/28—Chemically modified polycondensates
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- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08H—DERIVATIVES OF NATURAL MACROMOLECULAR COMPOUNDS
- C08H6/00—Macromolecular compounds derived from lignin, e.g. tannins, humic acids
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- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J161/00—Adhesives based on condensation polymers of aldehydes or ketones; Adhesives based on derivatives of such polymers
- C09J161/04—Condensation polymers of aldehydes or ketones with phenols only
- C09J161/06—Condensation polymers of aldehydes or ketones with phenols only of aldehydes with phenols
- C09J161/14—Modified phenol-aldehyde condensates
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Abstract
The present invention goes smoke removing method using ultrasonic atomization technique, belongs to environmental protection technical field.Method of the invention be first with diluted acid catalyzing hydrolysis biomass half cellulose prepare xylose solution, concentrated acid catalysis xylose dehydration prepare furfural, then base catalysis extracts lignin and obtains alkali lignin solution, again using phenol as phenolate reagent, alkali is that catalyst is modified to alkali lignin progress phenolate, modified lignin fortified phenol in varing proportions, furfural replaces formaldehyde in varing proportions, and lignin, furfural, phenol, the collaboration copolymerization of formaldehyde quaternary prepare lignin-base phenolic resin adhesive.The present invention is using hydrolysis of hemicellulose, dehydration product furfural as crosslinking agent, it solves the ratio industrial applications problem that causes the bonding strength of adhesive decline for improving lignin fortified phenol in the prior art, improves chemicals derived from biomass to being derived from the phenol of fossil resource, total Replacement rate of formaldehyde.
Description
Technical field
The invention belongs to field of environment protection, and in particular to go smoke removing method using ultrasonic atomization technique.
Background technique
Biomass as resources comprehensive utilization, prepares biomass fuel and chemicals has caused the extensive pass of all circles, the world
Note.Xylose, furfural are produced using hemicellulose, industrialized production has been formed using cellulose production ethyl alcohol, papermaking, has come relatively
It says, lignin utilization rate is lower, has become the bottleneck of biomass as resources comprehensive utilization.Such as the annual by-product of pulping and papermaking industry
50000000 tons of lignin only 2% are utilized, and rest part is passively burnt.In organic constituent of biomass lignin account for 25%~
35%, and energy content is even more to reach 40%.Therefore research lignin is of great significance to using entire biomass.Lignin
Depolymerization be convert lignocellulosic rate-determining steps, effectively break the split hair lignocellulosic of paradigmatic structure of lignin again
It is of great significance for the raw energy.Currently, have 4 industrial process for separating Vinsol, in addition to sulfur-bearing and not sulfur-bearing
Outside difference, the purity of product, structure and molecular weight are also different, but belong to preliminary working, and application performance is poor, and added value is lower.
Researcher has carried out a large amount of research on deeply process work, is directed not only to efficiently separating for lignin, and be related to producing height
The phenol products of added value.Lignin structure differs greatly, source and separation process dependent on material, but all separation are wooden
Element all contains phenolic hydroxyl group and alcoholic extract hydroxyl group, handles by degradation modification, lignin by as monomer, for synthesis of polyurethane,
Polyester, epoxy resin and phenolic resin.But lignin degradation needs effective catalyst, whole process energy to phenol or alcohol monomer
Consumption is high, and price can not be with petroleum product competition, this is that current lignin cannot function as raw material production high value added product
One of the main reasons.
Phenolic resin is because of its unique cross-linked network molecular structure, with bonding strength height, water-tolerant, good weatherability
Advantage.Lignin is to pass through the highly cross-linked tridimensional network day of carbon-carbon bond and ehter bond using phenyl-propane as structural unit
Right aromatic compound.It is similar to phenolic resin structure due to having alcoholic extract hydroxyl group and phenolic hydroxyl group isoreactivity functional group on molecule, wood
Quality can partially substitute phenol and prepare the glutinous agent of modified phenol formaldehyde resin adhesive with pulping waste liquor, can both reduce cost, reach biomass resource height
The purpose utilized is imitated, and the toxic remnants such as glutinous agent free phenol of the modified phenol formaldehyde resin adhesive with pulping waste liquor prepared are lower, have environmental protection
Meaning.Domestic related biological Quality Research has been in first place in the world, has a large amount of articles to deliver and patent application every year.
CN101260283A discloses a kind of preparation method and applications of modified phenolic adhesive based on lignin phenolate liquid,
Acid catalyst is added under normal heating or condition of normal pressure, using phenol as liquefied reagent, be added lignin, be warming up to 90 DEG C~
150 DEG C, liquefaction reaction is kept the temperature, cooling obtains liquefying lignin product；Then basic catalyst is added and formaldehyde reaction prepares glue
Stick.Wherein acidic catalyst is phosphoric acid, hydrochloric acid or sulfuric acid.
CN101942068A discloses a kind of preparation method of lignin phenol formaldehyde resin, and phenol and liquid lignin are mixed
Then formaldehyde condensation polymer is added into lignin phenol formaldehyde resin in the phenolate under liquid alkaline.CN102516909A discloses a kind of pulping waste liquor
Pulping waste liquor is carried out phenolate modification and is polycondensed into phenolic resin gluing with aldehyde by the preparation method of adhesive under alkaline condition
Agent, wherein a certain amount of urea is added as formaldehyde catching agent.Wherein pulping waste liquor uses sulfate pulp-making waste liquid, soda pulping
One or more of waste liquid, CTMP effluents.CN103804618A discloses a kind of lignin-base environmental protection phenolic aldehyde
The preparation method of Resin adhesive includes: mixing lignin raw material and phenol, forms raw mixture, mixture and formaldehyde, alkali
Solution hybrid reaction prepares lignin-base Environmental protection phenol formaldehyde resin adhesive.CN105754527A discloses a kind of containing demethylation
Lignin phenol formaldehyde resin adhesive and preparation method thereof.Phenol, sodium hydroxide, water and formalin are added in container, added
For heat to 60 DEG C, stirring makes system be uniformly dispersed, and temperature is then risen to 90 DEG C, demethylation is then added in insulation reaction 1.5h
Lignin, and continue insulation reaction 2h, cooling discharging obtains demethylation lignin-base phenolic resin adhesive.
CN105111394A discloses a kind of lignin phenol formaldehyde resin adhesive of high activity.Using alkaline dispersing agent to lignin
Macromolecule raw material is dissolved and is degraded, and the methoxyl group on lignin is efficiently deviate from by piptonychia based composite catalyst, is adopted simultaneously
With reduction protectants without to generate more phenolic hydroxyl groups on phenyl ring under being passed through condition of nitrogen gas.CN102675570A is disclosed
A kind of preparation method of phenolic resin adhesive modified lignin resin and starch composite material.By lignin: starch: phenol is by matching
Catalyst reaction is added under conditions of arranging temperature than 1:0.3~0.6:2~4；After reaction synthesis, finished product is obtained, under average
Cost declining 20%~25%.CN105348460A discloses a kind of cellulosic ethanol lignin modification Phenolic resin wood adhesive
And preparation method thereof.Heretofore described preparation method the following steps are included: by cellulosic ethanol lignin, phenol, piece alkali,
Reaction kettle is added in water, then it is molten successively to add formalin, first liquid alkaline and second batch water, second batch formaldehyde for insulation reaction
Liquid and second batch liquid alkaline, and isothermal holding is carried out respectively, urea is then added, is obtained through cooling discharging.CN106590488A is public
A kind of manufacturing method of oxidative lignin's phenolic resin adhesive is opened.Solid powdery lignin is first made, then carries out wooden
Element degradation and adhesive preparation.
Above method is successfully prepared lignin phenol formaldehyde resin glue adhesive, is provided for the scientific and technological progress of the industry
Important reference.But up to the present, there are still problems, main cause to be for industrial applications: when lignin additive amount is few,
It increases to the bonding strength of adhesive, when lignin additive amount is high, the bonding strength of adhesive is decreased obviously, and reality is not achieved
It is required with changing.A kind of pervasive, energy-saving and environment-friendly new process is found, is the main problem for needing to solve at present.
Summary of the invention
Smoke removing method is gone using ultrasonic atomization technique the purpose of the present invention is to provide a kind of, is solved in the prior art
The ratio of lignin fortified phenol improves, and the decline of adhesive bonding strength cannot achieve the problem replaced at high proportion.
In order to achieve the above object, the invention proposes the following technical solutions:
Smoke removing method is gone using ultrasonic atomization technique, which is characterized in that the preparation method includes the following steps:
Step 1: prepared by xylose solution
1. biomass is mixed with the sulfuric acid solution that concentration is 2wt% by solid-to-liquid ratio 1Kg:10L, heating reflux reaction 2h~
4h, cooling filtering obtain the hydrolyzate and hydrolysis residue that xylose concentration is 6wt%~7wt%；
2. the sulfuric acid concentration in hydrolyzate in the sulfuric acid solution for being 3wt% with concentration adjustment 1. is 2wt%, by solid-to-liquid ratio
Biomass is added in 1Kg:10L, and heating reflux reaction 2h~4h, cooling filtering, obtaining xylose concentration is 9wt%~11wt%'s
Hydrolyzate and hydrolysis residue；
3. the sulfuric acid concentration in hydrolyzate in the sulfuric acid solution for being 3wt% with concentration adjustment 2. is 2wt%, by solid-to-liquid ratio
Biomass is added in 1Kg:10L, and heating reflux reaction 2h~4h, cooling filtering, obtaining xylose concentration is 15wt%~17wt%'s
Xylose solution and hydrolysis residue；
Step 2: prepared by furfural aqueous solution
The sulfuric acid catalysis agent solution that molar concentration is 2mol/L is added in reactor, sulfuric acid catalysis agent solution is heated to
Reflux adds co-catalyst sodium chloride to being saturated, and stirring forms the rotation with fixed concentration catalyst and co-catalyst
Turn liquid level, step 1 then is hydrolyzed to obtain the xylose solution that xylose concentration is 15wt%~17wt% and is added to by certain speed spray
In reactor, heated constant temperature reaction carries out xylose dehydration in liquid levels layer, generates furfural steam, prepares concentration through condensation
For 6wt%~8wt% furfuryl aldehyde solution, yield reaches 60wt%~75wt%；
Step 3: prepared by furfural modified lignin resin base phenolic resin adhesive
1. the hydrolysis residue in step 1 through 1., 2. and 3. obtaining is concentrated, washing to neutrality, by washing to neutral hydrolysis
Slag is mixed with the alkaline solution that concentration is 3wt%~8wt%, and heating reflux reaction 3h~6h is down to room temperature, and filtering obtains alkali
Lignin liquor and coarse product of cellulose；
The alkaline solution is sodium hydroxide solution or potassium hydroxide solution, is washed to neutral hydrolysis residue butt and alkali
Property solution solid-to-liquid ratio be 1Kg:(5L~8L)；
2. the alkali lignin solution 1. obtained, phenol and base catalyst are added in reaction unit, be warming up to 80 DEG C~
100 DEG C, flow back 0.5h~2h, obtains the modified alkali lignin solution of phenolate；
The quality of lignin accounts for the 10%~75% of lignin and phenol gross mass in the alkali lignin solution；
The base catalyst is sodium hydroxide solution, and the quality of effective component sodium hydroxide is wooden in sodium hydroxide solution
The 4%~6% of element and phenol gross mass；
3. the formalin that concentration is 37% is added portionwise in the alkali lignin solution modified to the phenolate 2. obtained, first
It criticizes and is added the 80% of formalin total amount, adjustment system temperature is 60 DEG C~70 DEG C, then addition reaction 0.5h~1.5h rises
Temperature to 75 DEG C~90 DEG C, be down to by the furfuryl aldehyde solution and remaining formalin, isothermal reaction 1h~2.5h that addition step 2 obtains
Room temperature, stop reaction, products therefrom is evaporated under reduced pressure at 50 DEG C~70 DEG C to the viscosity of solution 60.0mPas~
When 700mPas, discharging obtains lignin-base phenolic resin adhesive.
Further, the biomass in the step 1 is one of straw, wood-curing waste, bamboo processing waste material
Or it is a variety of.
Preferably, in the step 3 in furfuryl aldehyde solution the quality of furfural account for formaldehyde and furfural gross mass 5%~
20%.
The gross mass of formaldehyde is W in the formalin being added twice in the step 3F=[WP/MP×1.5 ×MF+WL×
10%] ÷ 37%, wherein WPFor the quality of phenol in step 3, MPFor the molal weight of phenol, MFFor the molal weight of formaldehyde,
WLFor the quality of the lignin in step 3 alkali lignin solution.
Preferably, the base catalyst is sodium hydroxide solution, the matter of effective component sodium hydroxide in sodium hydroxide solution
Amount is the 5% of lignin and phenol gross mass.
Preferably, in the step 3, the formalin that concentration is 37% is added portionwise, it is total that formalin is added in first
The 80% of amount, reaction temperature is 60 DEG C, reaction time 1h, after furfuryl aldehyde solution and remaining formalin is added, reaction temperature
It is 80 DEG C, reaction time 1.5h.
The further deep processing of coarse product of cellulose is obtained in step 3 prepares sodium carboxymethylcellulose, the specific steps are as follows:
1. coarse product of cellulose and hydrogenperoxide steam generator are added in reaction kettle by solid-to-liquid ratio 1Kg:10L, it is warming up to 80 DEG C
Constant temperature is stirred at reflux reaction 7h, cooling filtering, and filter residue is washed with distilled water to neutrality, and it is fine to obtain white straw for 60 DEG C of drying
Dimension；
2. by step 1. in obtain white rice-straw fibre 10Kg, dehydrated alcohol 100L, concentration be 25.6wt% sodium hydroxide
Aqueous solution 25L is added separately in reaction kettle, is warming up to 28 DEG C, quaternization 85min, adds the chlorine that concentration is 63.3wt%
The ethanol solution of acetic acid is warming up to 65 DEG C, etherification reaction 140min, and filters pressing recycling design, filter cake is washed three times with dehydrated alcohol, and 60
DEG C drying, obtain white sodium carboxymethylcellulose.
Through the above design, the present invention can be brought the following benefits:
1, furfural aqueous solution is prepared using diluted acid catalyzing hydrolysis hemicellulose, concentrated acid catalysis xylose dehydration, as crosslinking agent,
Polynary collaboration copolymerization in situ prepares biomass-based adhesive.
2, alkali soluble lignin, base catalysis degradation, base catalysis pre-polymerization, base catalysis, which gradually polymerize, carries out under base catalysis, system
One catalyst, simplifies technique, base catalyst is made to be fully used.
3, by dilute acid hydrolysis step, impurity is sufficiently removed, the alkali lignin purity is high that alkali soluble lignin obtains, solution
In only alkali and lignin exist, without other impurity, improve product purity.
4, expensive and toxic phenol is replaced to can achieve 70wt% with alkali lignin, the additive amount of formaldehyde is wooden
The 10% of quality amount considerably reduces the usage amount of formaldehyde.
5, using furfural as crosslinking agent, lignin Replacement rate height, bonding strength decline are solved the problems, such as, while further mentioning
High biomass resource replaces the ratio of fossil resource, realize reduce formaldehyde usage amount 60% and improve phenol substitution rate 80% with
On lignin-base phenolic resin adhesive.
6, formaldehyde is added portionwise using the phenolate pre-polymerization of lignin elder generation, again, the quaternary of furfural polymerization cooperates with the side being gradually copolymerized
Method improves the bonding strength of lignin adhesive.
7, coarse product of cellulose is dispersed in dehydrated alcohol through bleaching, anti-by alkalization and etherificate under alkaline condition
It answers, prepares sodium carboxymethylcellulose.
8, using furfural as crosslinking agent, the bonding strength of adhesive is not only increased, and is developed for furfural industry
The passive situation that furfural market depends on overseas market has been broken in new market.
The present invention produces furfural using hemicellulose, produces adhesive using lignin, produces carboxymethyl using cellulose
Sodium cellulosate makes full use of each component part in biomass, realizes biomass as resources comprehensive utilization.
Specific embodiment
The invention will be further described with reference to embodiments:
Embodiment 1
Step 1: prepared by xylose solution
1. biomass is mixed with the sulfuric acid solution that concentration is 2wt% by solid-to-liquid ratio 1Kg:10L, heating reflux reaction 2h~
4h, cooling filtering obtain the hydrolyzate and hydrolysis residue that xylose concentration is 6.5wt%；
2. the sulfuric acid concentration in hydrolyzate in the sulfuric acid solution for being 3wt% with concentration adjustment 1. is 2wt%, by solid-to-liquid ratio
Biomass, heating reflux reaction 3h is added in 1Kg:10L, and cooling filtering obtains the hydrolyzate and hydrolysis that xylose concentration is 10wt%
Slag；
3. the sulfuric acid concentration in hydrolyzate in the sulfuric acid solution for being 3wt% with concentration adjustment 2. is 2wt%, by solid-to-liquid ratio
Biomass is added in 1Kg:10L, and heating reflux reaction 2h~4h, cooling filtering, obtaining hydrolyzate xylose concentration is 15.6wt%'s
Xylose solution and hydrolysis residue；
Step 2: prepared by furfural aqueous solution
The sulfuric acid catalysis agent solution that molar concentration is 2mol/L is added in reactor, catalyst solution is heated to and returns
Stream adds co-catalyst sodium chloride to being saturated, and stirring forms the rotation with fixed concentration catalyst and co-catalyst
Then the xylose solution that step 1 hydrolyzes to obtain 15.6wt% is added in reactor, heated constant temperature by liquid level by certain speed spray
Reaction carries out xylose dehydration in liquid levels layer, generates furfural steam, and preparing concentration through condensation is that 7.33wt% furfural is molten
Liquid, yield reach 75wt%；
Embodiment 2
1. by hydrolysis residue is concentrated in step 1 in embodiment 1, washing to neutrality is 1Kg:8L by solid-to-liquid ratio, is with concentration
The sodium hydroxide solution of 5wt% mixes, and heating reflux reaction 4h is down to room temperature, filters, obtains alkali lignin solution and cellulose
Crude product；
2. the alkali lignin solution 1. obtained, phenol and base catalyst are added in reaction unit, be warming up to 80 DEG C~
100 DEG C, flow back 0.5h~2h, obtains the modified alkali lignin solution of phenolate；
The quality of lignin accounts for the 40% of lignin and phenol gross mass, the base catalyst in the alkali lignin solution
For sodium hydroxide solution, the quality of effective component is the 5% of lignin and phenol gross mass in base catalyst；
3. the formalin that concentration is 37% is added portionwise in the alkali lignin solution modified to the phenolate 2. obtained, first
It criticizes and is added the 80% of formalin total amount, adjustment system temperature is 65 DEG C, addition reaction 1.0h, is then warming up to 80 DEG C, is added
The furfuryl aldehyde solution and remaining formalin that step 2 obtains, isothermal reaction 1.0h cool down 70 DEG C, are evaporated under reduced pressure sticking to solution
In 600mPas, discharging obtains lignin-base phenolic resin adhesive, is denoted as LPF4005 degree.
The quality of furfural accounts for the 5% of furfural and formaldehyde gross mass in the furfuryl aldehyde solution, and remaining formaldehyde is 15%.
Embodiment 3
The quality of lignin accounts for the 40% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
10%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF4010.
Embodiment 4
The quality of lignin accounts for the 40% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
15%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF4015.
Embodiment 5
The quality of lignin accounts for the 40% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
20%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF4020.
Comparative example 1
The quality of lignin accounts for the 40% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
0%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF4000.
Embodiment 6
The quality of lignin accounts for the 50% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
5%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF5005.
Embodiment 7
The quality of lignin accounts for the 50% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
10%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF5010.
Embodiment 8
The quality of lignin accounts for the 50% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
15%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF5015.
Embodiment 9
The quality of lignin accounts for the 50% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
20%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF5020.
Comparative example 2
The quality of lignin accounts for the 50% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
0%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF5000.
Embodiment 10
The quality of lignin accounts for the 60% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
5%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF6005.
Embodiment 11
The quality of lignin accounts for the 60% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
10%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF6010.
Embodiment 12
The quality of lignin accounts for the 60% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
15%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF6015.
Embodiment 13
The quality of lignin accounts for the 60% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
20%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF6020.
Comparative example 3
The quality of lignin accounts for the 60% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
0%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF6000.
Embodiment 14
The quality of lignin accounts for the 70% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
5%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF7005.
Embodiment 15
The quality of lignin accounts for the 70% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
10%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF7010.
Embodiment 16
The quality of lignin accounts for the 70% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
15%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF7015.
Embodiment 17
The quality of lignin accounts for the 70% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
20%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF7020.
Comparative example 3
The quality of lignin accounts for the 70% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
0%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF7000.
Comparative example 4
The quality of lignin accounts for the 0% of lignin and phenol gross mass, and the quality of furfural accounts for furfural and formaldehyde gross mass
0%, other conditions and embodiment 2 are consistent, obtain lignin-base phenolic resin adhesive LPF0000.
Embodiment 18
The coarse product of cellulose that embodiment 2 obtains is dispersed in dehydrated alcohol, under alkaline condition by alkalization and etherificate
Reaction, prepares sodium carboxymethylcellulose.Specific step is as follows:
1. coarse product of cellulose and hydrogenperoxide steam generator are added in reaction kettle by solid-to-liquid ratio 1Kg:10L, it is warming up to 80 DEG C
Constant temperature is stirred at reflux reaction 7h, cooling filtering, and filter residue is washed with distilled water to neutrality, and it is fine to obtain white straw for 60 DEG C of drying
Dimension；
2. by step 1. in obtain white rice-straw fibre 10Kg, dehydrated alcohol 100L, concentration be 25.6wt% sodium hydroxide
Aqueous solution 25L is added separately in reaction kettle, is warming up to 28 DEG C, quaternization 85min, adds the chlorine that concentration is 63.3wt%
The ethanol solution of acetic acid is warming up to 65 DEG C, etherification reaction 140min, and filters pressing recycling design, filter cake is washed three times with dehydrated alcohol, and 60
DEG C drying, obtain white sodium carboxymethylcellulose.Carboxymethyl cellulose degree of substitution is 1.756 and whiteness is 88.4.
The foregoing is merely presently preferred embodiments of the present invention, non-to limit the scope of the patents of the invention, other are with this
The equivalence changes of the patent spirit of invention should all belong to the scope of the patents of the invention.
Claims (7)
1. a kind of go smoke removing method using ultrasonic atomization technique, which is characterized in that this method comprises the following steps:
Step 1: prepared by xylose solution
1. biomass is mixed with the sulfuric acid solution that concentration is 2wt% by solid-to-liquid ratio 1Kg:10L, heating reflux reaction 2h~4h,
Cooling filtering obtains the hydrolyzate and hydrolysis residue that xylose concentration is 6wt%~7wt%；
2. the sulfuric acid concentration in hydrolyzate in the sulfuric acid solution for being 3wt% with concentration adjustment 1. is 2wt%, by solid-to-liquid ratio 1Kg:
Biomass, heating reflux reaction 2h~4h is added in 10L, and cooling filtering obtains the hydrolyzate that xylose concentration is 9wt%~11wt%
And hydrolysis residue；
3. the sulfuric acid concentration in hydrolyzate in the sulfuric acid solution for being 3wt% with concentration adjustment 2. is 2wt%, by solid-to-liquid ratio 1Kg:
Biomass, heating reflux reaction 2h~4h is added in 10L, and cooling filtering obtains the xylose that xylose concentration is 15wt%~17wt%
Solution and hydrolysis residue；
Step 2: prepared by furfural aqueous solution
The sulfuric acid catalysis agent solution that molar concentration is 2mol/L is added in reactor, sulfuric acid catalysis agent solution is heated to and returns
Stream adds co-catalyst sodium chloride to being saturated, and stirring forms the rotation with fixed concentration catalyst and co-catalyst
Liquid level, then by step 1 hydrolyze to obtain xylose solution that xylose concentration is 15wt%~17wt% be added to by certain speed spray it is anti-
It answers in device, heated constant temperature reaction, carries out xylose dehydration in liquid levels layer, generate furfural steam, preparing concentration through condensation is
6wt%~8wt% furfuryl aldehyde solution, yield reach 60wt%~75wt%；
Step 3: prepared by furfural modified lignin resin base phenolic resin adhesive
1. the hydrolysis residue in step 1 through 1., 2. and 3. obtaining is concentrated, washing to neutrality, will washing to neutral hydrolysis residue with
The alkaline solution that concentration is 3wt%~8wt% mixes, and heating reflux reaction 3h~6h is down to room temperature, filters, it is wooden to obtain alkali
Plain solution and coarse product of cellulose；
The alkaline solution is sodium hydroxide solution or potassium hydroxide solution, is washed molten to neutral hydrolysis residue butt and alkalinity
The solid-to-liquid ratio of liquid is 1Kg:(5L~8L)；
2. the alkali lignin solution 1. obtained, phenol and base catalyst are added in reaction unit, it is warming up to 80 DEG C~100
DEG C, flow back 0.5h~2h, obtains the modified alkali lignin solution of phenolate；
The quality of lignin accounts for the 10%~75% of lignin and phenol gross mass in the alkali lignin solution；
The base catalyst is sodium hydroxide solution, in sodium hydroxide solution the quality of effective component sodium hydroxide be lignin and
The 4%~6% of phenol gross mass；
3. the formalin that concentration is 37% is added portionwise in the alkali lignin solution modified to the phenolate 2. obtained, first adds
Enter the 80% of formalin total amount, adjustment system temperature is 60 DEG C~70 DEG C, then addition reaction 0.5h~1.5h is warming up to 75
DEG C~90 DEG C, the furfuryl aldehyde solution and remaining formalin, isothermal reaction 1h~2.5h that addition step 2 obtains are down to room temperature,
Stop reaction, products therefrom is evaporated under reduced pressure to the viscosity to solution at 50 DEG C~70 DEG C in 60.0mPas~700mPas
When, discharging obtains lignin-base phenolic resin adhesive.
2. according to claim 1 go smoke removing method using ultrasonic atomization technique, it is characterised in that: the step 1
In biomass be one of straw, wood-curing waste, bamboo processing waste material or a variety of.
3. according to claim 1 go smoke removing method using ultrasonic atomization technique, it is characterised in that: the step 3
The quality of furfural accounts for the 5%~20% of formaldehyde and furfural gross mass in middle furfuryl aldehyde solution.
4. according to claim 1 go smoke removing method using ultrasonic atomization technique, it is characterised in that: the step 3
In in the formalin that is added twice the gross mass of formaldehyde be WF=[WP/MP×1.5×MF+WL× 10%] ÷ 37%, wherein WP
For the quality of phenol in step 3, MPFor the molal weight of phenol, MFFor the molal weight of formaldehyde, WLFor step 3 alkali lignin
The quality of lignin in solution.
5. according to claim 1 go smoke removing method using ultrasonic atomization technique, it is characterised in that: the base catalysis
Agent is sodium hydroxide solution, and the quality of effective component sodium hydroxide is lignin and phenol gross mass in sodium hydroxide solution
5%.
6. according to claim 1 go smoke removing method using ultrasonic atomization technique, it is characterised in that: the step 3
In, the formalin that concentration is 37% is added portionwise, the 80% of formalin total amount is added in first, and reaction temperature is 60 DEG C,
Reaction time is 1h, and after furfuryl aldehyde solution and remaining formalin is added, reaction temperature is 80 DEG C, reaction time 1.5h.
7. according to claim 1 go smoke removing method using ultrasonic atomization technique, it is characterised in that: in step 3
Sodium carboxymethylcellulose is prepared to the further deep processing of coarse product of cellulose, the specific steps are as follows:
1. coarse product of cellulose and hydrogenperoxide steam generator are added in reaction kettle by solid-to-liquid ratio 1Kg:10L, 80 DEG C of constant temperature are warming up to,
It is stirred at reflux reaction 7h, cooling filtering, filter residue is washed with distilled water to neutrality, and 60 DEG C of drying obtain white rice-straw fibre；
2. by step 1. in obtain white rice-straw fibre 10Kg, dehydrated alcohol 100L, concentration be 25.6wt% sodium hydroxide it is water-soluble
Liquid 25L is added separately in reaction kettle, is warming up to 28 DEG C, quaternization 85min, adds the monoxone that concentration is 63.3wt%
Ethanol solution, be warming up to 65 DEG C, etherification reaction 140min, filters pressing recycling design, filter cake is washed three times with dehydrated alcohol, 60 DEG C baking
It is dry, obtain the sodium carboxymethylcellulose of white.
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