CN109777630A - The method of preparing biodiesel by ester interchange - Google Patents

The method of preparing biodiesel by ester interchange Download PDF

Info

Publication number
CN109777630A
CN109777630A CN201711111543.0A CN201711111543A CN109777630A CN 109777630 A CN109777630 A CN 109777630A CN 201711111543 A CN201711111543 A CN 201711111543A CN 109777630 A CN109777630 A CN 109777630A
Authority
CN
China
Prior art keywords
ion
hours
grams
ester interchange
preparing biodiesel
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.)
Granted
Application number
CN201711111543.0A
Other languages
Chinese (zh)
Other versions
CN109777630B (en
Inventor
俞峰萍
谢同
何文军
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.)
China Petroleum and Chemical Corp
Sinopec Shanghai Research Institute of Petrochemical Technology
Original Assignee
China Petroleum and Chemical Corp
Sinopec Shanghai Research Institute of Petrochemical 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 China Petroleum and Chemical Corp, Sinopec Shanghai Research Institute of Petrochemical Technology filed Critical China Petroleum and Chemical Corp
Priority to CN201711111543.0A priority Critical patent/CN109777630B/en
Publication of CN109777630A publication Critical patent/CN109777630A/en
Application granted granted Critical
Publication of CN109777630B publication Critical patent/CN109777630B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel

Landscapes

  • Catalysts (AREA)

Abstract

The step of the present invention relates to a kind of methods of preparing biodiesel by ester interchange, are included under the conditions of ester exchange reaction, and grease and short chain alcohol and ion-exchange resin catalyst contact;The ion-exchange resin catalyst has following structure general formula:Wherein,For gel-type nanocomposite resin matrix;MFor anion, it is selected from trifluoromethanesulfonic acid radical ion, hydrogen sulfate ion, phosphoric acid hydrogen radical ion, tetrafluoroborate ion or hexafluorophosphoricacid acid ions;POSS is cage-type silsesquioxane unit;

Description

The method of preparing biodiesel by ester interchange
Technical field
The present invention relates to a kind of methods of preparing biodiesel by ester interchange.
Background technique
With the continuous consumption of traditional fossil energy, people are for researching and developing environmentally protective, renewable new energy demand day It is beneficial urgent.Conventional fossil fuel can generate sulfur dioxide, nitrogen oxides and other a large amount of dust in combustion, to ecology Environment causes great damage.And biodiesel is as a kind of green energy resource, compared with petrifaction diesel, have it is renewable, can biology Degradation, waste discharge is low, Cetane number is high, flash-point is high, using it is safe the features such as.
The preparation method of biodiesel, which mainly has, directly to be used method, is used in mixed way method, microemulsion method, high-temperature cracking method and ester Exchange process.At present industrially using it is more be ester-interchange method, it be with oil crops such as soybean, rape, cotton, palm etc., it is wild The water plants such as oil generation tannin plant and engineering microalgae grease and animal fat, food garbage oil etc. are feedstock oil, with short chain alcohol Fatty acid methyl Ester is made by transesterification or thermochemical processes, to replace petrifaction diesel.
Method used by preparing biodiesel by ester interchange is more, such as homogeneous acid-base method, Lipids Enzymatic, supercritical methanol technology and Heterogeneous acid-base method etc..Traditional homogeneous acid-base catalysis method post-processes cumbersome, a large amount of three wastes of generation etc. there are equipment burn into and asks Topic;Enzyme catalyst is since its is environmental-friendly by numerous concerns in Lipids Enzymatic, but the reaction time needed for enzymatic is longer, is easy Inactivation, while its usage amount is larger, limits the extensive use of enzyme catalyst;Preparation of Biodiesel by Supercritical Method high conversion rate, But high-temperature and high-pressure conditions are needed, equipment requirement is high and energy consumption is high;Although heterogeneous acid-base catalysis method catalyst recycling is convenient, also deposit It is low in reactivity, there is certain limitation.Therefore environmental-friendly effective catalyst is developed as current research hotspot.
Acidic ion liquid is provided simultaneously with traditional liquid as a kind of novel environmentally friendly solvent and effective catalyst The high density reaction active site of acid catalyst and the fixedness of solid acid, and because its molecular structure and acidity have and can design Property, it is considered to be one of most promising green catalyst.But acidic ion liquid there is also viscosity big, at high cost, product/urge Agent separation is inconvenient, makes it in the process of industrialization of catalysis biological diesel oil by biggish limitation.
Document CN201410442179.6 discloses a kind of preparation side of N- Methyl-N-alkyl film type ionic liquid Method, catalyst of the ionic liquid as bio-oil and methanol preparing biodiesel by ester exchange, activity is high, and dosage is few, performance Also more stable.It is 40 in methanol/soybean oil alcohol oil rate, temperature is 60 degree reaction 1 hour lower, and the yield of biodiesel is reachable 93.7%.
It is excellent that immobilized ionic liquid combines high activity and the easily separated, recycling of heterogeneous catalysis of homogeneous catalyst etc. Point is a kind of novel green catalyst, has huge application potential in biodiesel synthesis field.
Document CN201510064336.9 discloses a kind of acidic ion liquid of biodiesel synthesis cultivation property catalyst admittedly, The patent is solid by ionic liquid [2-MPYR-BS] [HSO4], [HMIM-BS] [HSO4] or [PYR-BS] [HSO4] using infusion process It plants to introducing on the mesopore molecular sieve Al-MCM-41 of Al, solid cultivationization ionic-liquid catalyst is prepared, be used for transesterification legal system Standby biodiesel.Using Al-MCM-41- [2-MPYR-BS] [HSO4] as catalyst, under certain alcohol oil rate, reacted at 150 DEG C 6 hours, the yield of biodiesel was up to 97.0%.Biodiesel is environmentally friendly without neutralizing washing, and catalyst is with excellent Different catalytic activity, Yi Huishou.But by the type of cultivation admittedly ionic-liquid catalyst prepared by infusion process, there are still certain activity Center losing issue, after which uses 5 times, the yield of biodiesel has fallen to 91.5%, and repeat performance is poor.
Document CN201710337145.4 discloses a kind of preparation method of biodiesel special solid base catalyst, utilizes Polymer emulsion adsorbs saleratus, calcines through two steps, forms spongy porosu solid base catalyst, carrier is equal with effective component For porous structure, although solving the easy blockage problem in catalyst duct made from traditional infusion process.But the repetition of the catalyst Service performance is poor, and after 5 times are reused, the yield of biodiesel is reduced to 88.9% via 94.6%.
Admittedly the catalytic activity of cultivation type ionic-liquid catalyst depends not only on the performance of ionic liquid itself, load is additionally depended on The various performances of body, such as heat resistance, solvent resistance, porosity etc..It can be seen that designing a kind of with high activity, repetition The excellent biodiesel preparation of utility is of crucial importance with ester exchange catalyst.
Summary of the invention
The present invention provides a kind of method of preparing biodiesel by ester interchange.The method includes in ester exchange reaction condition Under, the step of grease and short chain alcohol and ion-exchange resin catalyst contact;The ion-exchange resin catalyst has following General structure:
Wherein,For gel-type nanocomposite resin matrix;
M-For anion, it is selected from trifluoromethanesulfonic acid radical ion, hydrogen sulfate ion, phosphoric acid hydrogen radical ion, tetrafluoroborate Ion or hexafluorophosphoricacid acid ions;
POSS is cage-type silsesquioxane unit, and general formula is (- SiO1.5)m;M is 6,8,10 or 12;
For glyoxaline cation unit;
Linking group of the R between POSS unit and glyoxaline cation unit, R are alkylidene or arylene;
The gel-type nanocomposite resin matrix is styrene monomer, comonomer and nano material through in-situ copolymerization Obtained nanogel type copolymer;The nano material is selected from single-layer graphene, multi-layer graphene, graphene oxide, graphite At least one of alkynes.
According to an aspect of the present invention, content of the POSS unit in the ion exchange resin is 5~15 weight %.
According to an aspect of the present invention, M-For trifluoromethanesulfonic acid radical ion.
According to an aspect of the present invention, alkylidene is selected from methylene, ethylidene or propylidene;Arylene is selected from sub- benzene Base, naphthylene or sub- benzyl.
According to an aspect of the present invention, the styrene monomer is selected from styrene, α-methylstyrene or 4- butyl At least one of styrene, optimization styrene.
According to an aspect of the present invention, the comonomer be selected from ethyleneglycol dimethyacrylate, diallyl benzene, At least one of divinyl phenylmethane or divinylbenzene, preferably divinylbenzene.
According to an aspect of the present invention, the preferred multi-layer graphene of the nano material.
According to an aspect of the present invention, the dosage of styrene monomer is 85~95 parts, the dosage of comonomer is 2~ 5 parts, the dosage of nano material is 0.1~3 part.
According to an aspect of the present invention, the grease is selected from any one of the vegetable and animals oils of fatty glyceride. Such as the vegetable oil such as soybean oil, rapeseed oil, cottonseed oil or palm oil, the water plants grease such as wild plant oil plant, engineering microalgae, And animal fat, food garbage oil etc..
According to an aspect of the present invention, the short chain alcohol is any in methanol, ethyl alcohol, propyl alcohol or butanol.
According to an aspect of the present invention, it is (10 that the ester exchange reaction condition, which includes: the molar ratio of short chain alcohol and grease, ~50): 1, catalyst amount is the 1~15% of raw oil material quality, and 40~180 DEG C of reaction temperature, the reaction time 1~24 is small When.
The preparation method of heretofore described ion-exchange resin catalyst, comprising the following steps:
A) auxiliary agent is made into the water solution A that weight percent concentration is 0.5~2%, styrene monomer, copolymerization is single Body, nano material, initiator wiring solution-forming B;Wherein, the styrene monomer is selected from styrene, α-methylstyrene or 4- At least one of butylstyrene;The comonomer is selected from ethyleneglycol dimethyacrylate, diallyl benzene, divinyl At least one of base phenylmethane or divinylbenzene;The nano material is selected from single-layer graphene, multi-layer graphene, oxidation At least one of graphene, graphite alkene;The initiator is selected from benzoyl peroxide, azodiisobutyronitrile, peroxidating laurel At least one of acyl or isopropyl benzene hydroperoxide;The auxiliary agent is selected from polyvinyl alcohol, gelatin, starch, methylcellulose, swelling At least one of soil or calcium carbonate;Based on parts by weight, the dosage of styrene monomer is 85~95 parts, the dosage of comonomer It is 2~5 parts, the dosage of nano material is 0.1~3 part, and the dosage of initiator is 0.1~10 part;The dosage of auxiliary agent is monomer use The 150~400% of amount;
B) by solution B 60~75 DEG C prepolymerization 0.5~2.5 hour, solution B is mixed with solution A then, is warming up to 70 ~90 DEG C are reacted 5~15 hours, then are warming up to 90~100 DEG C and are reacted 5~15 hours;After reaction, through extracting, washing, mistake Filter, dry, sieving, obtain 0.35~0.60 millimeter of particle size range of composite gel microsphere;
C) make the composite gel microsphere chloromethylation: being added in composite gel microsphere and be equivalent to composite gel microsphere weight The chloromethylation reagents of amount 200~500%, and it is equivalent to the zinc chloride catalyst of composite gel microsphere weight 20~70%, It is reacted 8~30 hours at 30~60 DEG C, is filtered, washed to obtain plural gel chlorine ball;The chloromethylation reagents are selected from chlorine At least one of methyl ether, dichloroethyl ether or Isosorbide-5-Nitrae-dichloro methyl butyl ether;
D) it by the plural gel chlorine ball, the mixture of imidazoles and acetonitrile, is reacted at 60~90 DEG C, obtains compound imidazoles Microballoon;In the mixture, the molar ratio of plural gel chlorine ball, imidazoles and acetonitrile is 1:(1~2): (30~150);
E) by the POSS compound of the compound imidazoles microballoon and halogenated alkyl according to imidazole functionalities and halogenated functional group Equimolar mixing, is dissolved in tetrahydrofuran, 24~72 hours at 100 DEG C, filters after reaction, and washing obtains compound miaow Azoles/POSS microballoon;The POSS compound of the halogenated alkyl is selected from eight chloromethyl POSS, eight chloroethyl POSS, eight chloropropyls At least one of POSS;
F) the compound imidazoles/POSS microballoon brine, wherein compound imidazoles/POSS microballoon and salting liquid rub You are than being (1:1)~(1:10);The concentration of salting liquid is 0.1~1mol/L;It is washed with deionized after washing to pH= 7, obtain the ion exchange resin.The salting liquid is selected from trifluoromethanesulfonic acid (salt), disulfate, hydrophosphate, tetrafluoro boron At least one of hydrochlorate or hexafluorophosphoric acid salting liquid.
Beneficial effects of the present invention: the ion-exchange resin catalyst in the present invention contains two different nano materials: receiving Rice carbon material and cage-type silsesquioxane (Polyhedral oligomeric silsesquioxanes, abbreviation POSS).Nanometer Carbon material and monomer, comonomer are introduced into resin matrix by in-situ polymerization under initiator effect, improve resin base The glass transition temperature of body;Simultaneously because the introducing of nano-carbon material, increases the resistance to swelling energy of resin matrix.And POSS Comprising the inorganic supporting structure being made of Si and O, the good heat resistance of ion exchange resin is imparted, thermal stability significantly mentions It is high.
The preferred solution of the invention is total for the situ-gel type of the styrene of chloromethylation, divinylbenzene and multi-layer graphene Copolymer resin matrix is reacted with imidazoles, obtains compound imidazoles microballoon, then passes through the POSS chemical combination of imidazole group and halogenated alkyl Object reaction, finally carries out ion-exchange reactions with salting liquid again, and the gel type ionic containing two kinds of different nano materials is prepared Exchanger resin.It is reacted by the in-situ copolymerization between graphene and monomer, comonomer and realizes graphene and polymeric matrix Covalent bond, and realized between POSS and resin matrix by the chemical reaction of halogenated alkyl POSS compound and imidazole group Combination.
The gel-type ion-exchange resin catalyst containing two kinds of different nano materials in the present invention is for grease and short chain The ester exchange reaction of alcohol, has the advantage that
(1) catalyst prepared by is used for preparing biodiesel by ester interchange, and catalytic activity is high;
(2) catalyst easily recycles, and stability is good, reusable.
The present invention will be further described below by way of examples, it should be noted however that protection model of the invention It encloses not that this is limited by this, but is determined by the appended claims.
It should be strongly noted that two or more aspects (or embodiment) disclosed in the context of the present specification Any combination, the technical solution formed therefrom it can belong to a part of this specification original disclosure each other, while It falls under the scope of the present invention.
Specific embodiment
The preparation of [embodiment 1] ion-exchange resin catalyst
47.0 grams of styrene, 2.3 grams of divinylbenzenes and 1.6 grams of benzoyl peroxide first are added in 500 milliliters of three-necked flasks Acyl initiator is stirred to react 2.0 hours at 60 DEG C;Then 0.6 gram of multi-layer graphene is added, continues to carry out for stirring 1 hour pre- Polymerization.The 260 ml deionized water solution for being dissolved with 2.0 grams of gelatin are added.Mixing speed is adjusted, while being gradually warming up to 80 DEG C, it reacts 5 hours;It is warming up to 90 DEG C again, reacts 5 hours, is finally warming up to 98 DEG C, reacts 6 hours.After reaction, topple over Supernatant liquid out is washed with 85 DEG C of hot water, then is washed with cold water, is then filtered, and is put into 80 DEG C of drying in baking oven, is sieved, collects Composite gel microsphere A1 of the partial size within the scope of 0.35~0.60mm.
Composite gel microsphere chloromethylation: in the three-necked flask of 500ml, be added 40 grams of composite gel microsphere A1 and 250ml chloromethyl ether is stored at room temperature 3 hours, starts to stir, and it is catalyst that 10 grams of zinc chloride, which are added, and it is small to be warming up to 60 DEG C of reactions 10 When, it is cooled to room temperature after chloromethylation, filters out chlorination mother solution, washed repeatedly with methanol, dry 8 hours, obtain at 100 DEG C To plural gel chlorine ball A1.
30 grams of plural gel chlorine ball A1 (chlorinity is 3.4mmol Cl/g), imidazoles are added in 500ml there-necked flask (102.0mmol) and 200ml acetonitrile, reacts 24 hours at 60 DEG C, are cooled to room temperature, and filter, successively use ethyl acetate, The HCl of 0.1mol/L, deionized water, methanol washing, then 60 DEG C of vacuum bakings obtain compound imidazoles microballoon A1 in 24 hours.
In 500ml three-necked flask, the compound imidazoles microballoon A1 of 30 grams of addition (imidazole group content is 3.1mmol/g), 9.8 Gram eight chloromethyl silsesquioxanes and 300ml tetrahydrofuran filter after reaction 24 hours at 100 DEG C, with tetrahydro furan Mutter, deionized water is successively washed, obtain compound imidazoles/POSS microballoon A1.
In 1000ml three-necked flask, it is 0.1mol/L's that 30 grams of compound imidazoles/POSS microballoon A1,500ml concentration, which is added, Progress ion-exchange reactions 24 hours is stirred at room temperature in the deionized water solution of trifluoromethanesulfonic acid lithium;Then it is washed with deionized water It washs until washing lotion pH=7, obtains the ion-exchange resin catalyst of the different nano materials of of the invention two kinds, note after vacuum drying For Cat-A1, wherein POSS unit content is 9.6%, and structural formula is as follows:
The preparation of [embodiment 2] ion-exchange resin catalyst
In 500 milliliters of three-necked flasks be added containing initiator monomer mixture solution (60.0 grams of styrene, 1.0 grams Divinylbenzene, 1.6 grams of multi-layer graphenes and 1.0 grams of benzoyl peroxides, the solution are stirred to react 0.5 hour prior to 70 DEG C), Blender is started, the mixed solution of 200 ml deionized waters and 4 grams of polyvinyl alcohol is added, is warming up to 85 DEG C, is reacted 3 hours, then 90 DEG C are warming up to, is reacted 9 hours, is finally warming up to 100 DEG C, is reacted 10 hours.After reaction, supernatant liquid is poured out, uses 85 DEG C of hot water washing, then washed with cold water, is then filtered, and is put into 80 DEG C of drying in baking oven, sieving, collection cut size 0.35~ Composite gel microsphere B1 within the scope of 0.60 millimeter.
The chloromethylation of complex microsphere: in 500 milliliters of three-necked flask, 50 grams of complex microsphere B1 and 200 milliliters are added Dichloroethyl ether is stored at room temperature 6 hours, and it is catalyst that 30 grams of zinc chloride, which are added, starts to stir, and is warming up to 50 DEG C and is reacted 30 hours, chlorine It is cooled to room temperature after methylation, filters out chlorination mother solution, washed repeatedly with methanol, dried 8 hours, answered at 100 DEG C Close gel chlorine ball B1.
50 grams of plural gel chlorine ball B1 (chlorinity is 4.6mmol Cl/g), imidazoles are added in 500ml there-necked flask (230.0mmol) and 300ml acetonitrile, reacts 16 hours at 80 DEG C, are cooled to room temperature, and filter, successively use ethyl acetate, The HCl of 0.1mol/L, deionized water, methanol washing, then 60 DEG C of vacuum bakings obtain compound imidazoles microballoon B1 in 24 hours.
In 1000ml three-necked flask, 50 grams of compound imidazoles microballoon B1 (imidazole group content is 4.0mmol/g) are added, 21.0 gram of eight chloromethyl silsesquioxane and 500ml tetrahydrofuran filter after reaction 72 hours at 100 DEG C, with four Hydrogen furans, deionized water are successively washed, and compound imidazoles/POSS microballoon B1 is obtained.
In 1000ml three-necked flask, it is 1.0mol/L's that 40 grams of compound imidazoles/POSS microballoon B1,400ml concentration, which is added, Progress ion-exchange reactions 24 hours is stirred at room temperature in the deionized water solution of trifluoromethanesulfonic acid lithium;Then it is washed with deionized water It washs until washing lotion pH=7, obtains the ion-exchange resin catalyst of the different nano materials of of the invention two kinds, note after vacuum drying For Cat-B1, wherein POSS unit content is 11.2%, and structural formula is as follows:
The preparation of [embodiment 3] ion-exchange resin catalyst
In 500 milliliters of three-necked flasks be added containing initiator monomer mixture solution (42.5 grams of styrene, 2.5 grams Divinylbenzene, 0.1 gram of multi-layer graphene and 2.0 grams of benzoyl peroxides, the solution are stirred to react 1.5 hours prior to 70 DEG C), The mixed solution of 200 ml deionized waters and 4 grams of polyvinyl alcohol is added, is warming up to 85 DEG C, reacts 3 hours, then be warming up to 90 DEG C, Reaction 9 hours is finally warming up to 100 DEG C, reacts 10 hours.After reaction, supernatant liquid is poured out, with 85 DEG C of hot water wash It washs, then is washed with cold water, then filtered, be put into 80 DEG C of drying in baking oven, sieving, collection cut size is in 0.35~0.60 millimeter of range Interior composite gel microsphere C1.
The chloromethylation of complex microsphere: in 250 milliliters of three-necked flask, 20 grams of complex microsphere C1 and 100 milliliters are added Isosorbide-5-Nitrae-dichloro methyl butyl ether is stored at room temperature 6 hours, and it is catalyst that 8 grams of zinc chloride, which are added, starts to stir, and is warming up to 30 DEG C instead It answers 24 hours, is cooled to room temperature after chloromethylation, filters out chlorination mother solution, washed repeatedly with methanol, dry 8 at 100 DEG C Hour, obtain plural gel chlorine ball C1.
20 grams of plural gel chlorine ball C1 (chlorinity is 1.5mmol Cl/g), imidazoles are added in 250ml there-necked flask (30.0mmol) and 150ml acetonitrile, reacts 16 hours at 90 DEG C, are cooled to room temperature, and filter, successively use ethyl acetate, The HCl of 0.1mol/L, deionized water, methanol washing, then 60 DEG C of vacuum bakings obtain compound imidazoles microballoon C1 in 24 hours.
In 250ml three-necked flask, the compound imidazoles microballoon C1 of 20 grams of addition (imidazole group content is 1.4mmol/g), 3.4 Gram eight chloroethyl silsesquioxanes and 150ml tetrahydrofuran filter after reaction 72 hours at 100 DEG C, with tetrahydro furan Mutter, deionized water is successively washed, obtain compound imidazoles/POSS microballoon C1.
In 500ml three-necked flask, three that 20 grams of compound imidazoles/POSS microballoon C1,300ml concentration is 0.5mol/L are added Progress ion-exchange reactions 24 hours is stirred at room temperature in the deionized water solution of fluorine methanesulfonic acid lithium;Then it is washed with deionized Until washing lotion pH=7, obtains the ion-exchange resin catalyst of the different nano materials of of the invention two kinds, is denoted as after vacuum drying Cat-C1, wherein POSS unit content is 5.6%, and structural formula is as follows:
The preparation of [embodiment 4] ion-exchange resin catalyst
47.0 grams of styrene, 2.3 grams of divinylbenzenes and 1.6 grams of benzoyl peroxide first are added in 500 milliliters of three-necked flasks Acyl initiator is stirred to react 2.0 hours at 60 DEG C;Then 0.6 gram of single-layer graphene is added, continues to carry out for stirring 1 hour pre- Polymerization.The 260 ml deionized water solution for being dissolved with 2.0 grams of gelatin are added.Mixing speed is adjusted, while being gradually warming up to 80 DEG C, it reacts 5 hours;It is warming up to 90 DEG C again, reacts 5 hours, is finally warming up to 98 DEG C, reacts 6 hours.After reaction, topple over Supernatant liquid out is washed with 85 DEG C of hot water, then is washed with cold water, is then filtered, and is put into 80 DEG C of drying in baking oven, is sieved, collects Composite gel microsphere A2 of the partial size within the scope of 0.35~0.60mm.
Composite gel microsphere chloromethylation: in the three-necked flask of 500ml, be added 40 grams of composite gel microsphere A2 and 250ml chloromethyl ether is stored at room temperature 3 hours, starts to stir, and it is catalyst that 10 grams of zinc chloride, which are added, and it is small to be warming up to 60 DEG C of reactions 10 When, it is cooled to room temperature after chloromethylation, filters out chlorination mother solution, washed repeatedly with methanol, dry 8 hours, obtain at 100 DEG C To plural gel chlorine ball A2.
30 grams of plural gel chlorine ball A2 (chlorinity is 3.6mmol Cl/g), imidazoles are added in 500ml there-necked flask (108.0mmol) and 200ml acetonitrile, reacts 24 hours at 60 DEG C, are cooled to room temperature, and filter, successively use ethyl acetate, The HCl of 0.1mol/L, deionized water, methanol washing, then 60 DEG C of vacuum bakings obtain compound imidazoles microballoon A2 in 24 hours.
In 500ml three-necked flask, 30 grams of compound imidazoles microballoon A2 (imidazole group content is 3.2mmol/g) are added, 10.1 gram of eight chloromethyl silsesquioxane and 300ml tetrahydrofuran filter after reaction 24 hours at 100 DEG C, with four Hydrogen furans, deionized water are successively washed, and compound imidazoles/POSS microballoon A2 is obtained.
In 1000ml three-necked flask, it is 0.1mol/L's that 30 grams of compound imidazoles/POSS microballoon A2,500ml concentration, which is added, Progress ion-exchange reactions 24 hours is stirred at room temperature in the deionized water solution of trifluoromethanesulfonic acid lithium;Then it is washed with deionized water It washs until washing lotion pH=7, obtains the ion-exchange resin catalyst of the different nano materials of of the invention two kinds, note after vacuum drying For Cat-A2, wherein POSS unit content is 9.9%, and structural formula is as follows:
The preparation of [embodiment 5] ion-exchange resin catalyst
In 500 milliliters of three-necked flasks be added containing initiator monomer mixture solution (60.0 grams of styrene, 1.0 grams Divinylbenzene, 1.6 grams of single-layer graphenes and 1.0 grams of benzoyl peroxides, the solution are stirred to react 0.5 hour prior to 70 DEG C), Blender is started, the mixed solution of 200 ml deionized waters and 4 grams of polyvinyl alcohol is added, is warming up to 85 DEG C, is reacted 3 hours, then 90 DEG C are warming up to, is reacted 9 hours, is finally warming up to 100 DEG C, is reacted 10 hours.After reaction, supernatant liquid is poured out, uses 85 DEG C of hot water washing, then washed with cold water, is then filtered, and is put into 80 DEG C of drying in baking oven, sieving, collection cut size 0.35~ Composite gel microsphere B2 within the scope of 0.60 millimeter.
The chloromethylation of complex microsphere: in 500 milliliters of three-necked flask, 50 grams of complex microsphere B2 and 200 milliliters are added Dichloroethyl ether is stored at room temperature 6 hours, and it is catalyst that 30 grams of zinc chloride, which are added, starts to stir, and is warming up to 50 DEG C and is reacted 30 hours, chlorine It is cooled to room temperature after methylation, filters out chlorination mother solution, washed repeatedly with methanol, dried 8 hours, answered at 100 DEG C Close gel chlorine ball B2.
50 grams of plural gel chlorine ball B2 (chlorinity is 4.7mmol Cl/g), imidazoles are added in 500ml there-necked flask (235.0mmol) and 300ml acetonitrile, reacts 16 hours at 80 DEG C, are cooled to room temperature, and filter, successively use ethyl acetate, The HCl of 0.1mol/L, deionized water, methanol washing, then 60 DEG C of vacuum bakings obtain compound imidazoles microballoon B2 in 24 hours.
In 1000ml three-necked flask, 50 grams of compound imidazoles microballoon B2 (imidazole group content is 4.1mmol/g) are added, 21.6 gram of eight chloromethyl silsesquioxane and 500ml tetrahydrofuran filter after reaction 72 hours at 100 DEG C, with four Hydrogen furans, deionized water are successively washed, and compound imidazoles/POSS microballoon B2 is obtained.
In 1000ml three-necked flask, it is 1.0mol/L's that 40 grams of compound imidazoles/POSS microballoon B2,400ml concentration, which is added, Progress ion-exchange reactions 24 hours is stirred at room temperature in the deionized water solution of trifluoromethanesulfonic acid lithium;Then it is washed with deionized water It washs until washing lotion pH=7, obtains the ion-exchange resin catalyst of the different nano materials of of the invention two kinds, note after vacuum drying For Cat-B2, wherein POSS unit content is 11.3%, and structural formula is as follows:
The preparation of [embodiment 6] ion-exchange resin catalyst
In 500 milliliters of three-necked flasks be added containing initiator monomer mixture solution (42.5 grams of styrene, 2.5 grams Divinylbenzene, 0.1 gram of single-layer graphene and 2.0 grams of benzoyl peroxides, the solution are stirred to react 1.5 hours prior to 70 DEG C), The mixed solution of 200 ml deionized waters and 4 grams of polyvinyl alcohol is added, is warming up to 85 DEG C, reacts 3 hours, then be warming up to 90 DEG C, Reaction 9 hours is finally warming up to 100 DEG C, reacts 10 hours.After reaction, supernatant liquid is poured out, with 85 DEG C of hot water wash It washs, then is washed with cold water, then filtered, be put into 80 DEG C of drying in baking oven, sieving, collection cut size is in 0.35~0.60 millimeter of range Interior composite gel microsphere C2.
The chloromethylation of complex microsphere: in 250 milliliters of three-necked flask, 20 grams of complex microsphere C2 and 100 milliliters are added Isosorbide-5-Nitrae-dichloro methyl butyl ether is stored at room temperature 6 hours, and it is catalyst that 8 grams of zinc chloride, which are added, starts to stir, and is warming up to 30 DEG C instead It answers 24 hours, is cooled to room temperature after chloromethylation, filters out chlorination mother solution, washed repeatedly with methanol, dry 8 at 100 DEG C Hour, obtain plural gel chlorine ball C2.
20 grams of plural gel chlorine ball C2 (chlorinity is 1.6mmol Cl/g), imidazoles are added in 250ml there-necked flask (32.0mmol) and 150ml acetonitrile, reacts 16 hours at 90 DEG C, are cooled to room temperature, and filter, successively use ethyl acetate, The HCl of 0.1mol/L, deionized water, methanol washing, then 60 DEG C of vacuum bakings obtain compound imidazoles microballoon C2 in 24 hours.
In 250ml three-necked flask, the compound imidazoles microballoon C2 of 20 grams of addition (imidazole group content is 1.5mmol/g), 3.6 Gram eight chloroethyl silsesquioxanes and 150ml tetrahydrofuran filter after reaction 72 hours at 100 DEG C, with tetrahydro furan Mutter, deionized water is successively washed, obtain compound imidazoles/POSS microballoon C2.
In 500ml three-necked flask, three that 20 grams of compound imidazoles/POSS microballoon C2,300ml concentration is 0.5mol/L are added Progress ion-exchange reactions 24 hours is stirred at room temperature in the deionized water solution of fluorine methanesulfonic acid lithium;Then it is washed with deionized Until washing lotion pH=7, obtains the ion-exchange resin catalyst of the different nano materials of of the invention two kinds, is denoted as after vacuum drying Cat-C2, wherein POSS unit content is 5.9%, and structural formula is as follows:
The preparation of [comparative example 1] comparative catalyst
Nano material is not added prepares gel micro-ball: 47.0 grams of styrene of addition in 500 milliliters of three-necked flasks, 2.3 grams Divinylbenzene and 1.6 grams of benzoyl peroxide initiators.260 ml deionized waters that addition has been dissolved with 2.0 grams of gelatin are molten Liquid.Mixing speed is adjusted, is stirred 2 hours.It is stirred to react at 60 DEG C 2.0 hours, is then gradually warming up to 80 DEG C, reaction 5 is small When;It is warming up to 90 DEG C again, reacts 5 hours, is finally warming up to 98 DEG C, reacts 6 hours.After reaction, supernatant liquid is poured out, Washed with 85 DEG C of hot water, then washed with cold water, then filtered, be put into baking oven 80 DEG C of drying, sieving, collection cut size 0.35~ Gel micro-ball DZ-1 within the scope of 0.60mm.
Gel micro-ball chloromethylation: in the three-necked flask of 500ml, 40 grams of gel micro-ball DZ-1 and 250ml chloromethanes are added Ether is stored at room temperature 3 hours, starts to stir, and it is catalyst that 10 grams of zinc chloride, which are added, is warming up to 60 DEG C and reacts 10 hours, chloromethyl It is cooled to room temperature after change, filters out chlorination mother solution, washed repeatedly with methanol, dried 8 hours at 100 DEG C, obtain gel chlorine Ball DZ-1.
Halogenated alkyl POSS compound is not used: 30 grams of gel chlorine ball DZ-1 (chlorinities being added in 500ml there-necked flask For 3.3mmol Cl/g), N- methylimidazole (99.0mmol) and 200ml acetonitrile, is reacted 24 hours at 60 DEG C, be cooled to room Temperature, filtering, is successively washed with ethyl acetate, the HCl of 0.1mol/L, deionized water, methanol, is then dried 24 hours for 60 DEG C of vacuum To imidazoles microballoon DZ-1.
In 1000ml three-necked flask, the trifluoro methylsulphur that 30 grams of imidazoles microballoon DZ-1,500ml concentration are 0.1mol/L is added Progress ion-exchange reactions 24 hours is stirred at room temperature in the deionized water solution of sour lithium;It is then washed with deionized until washing Liquid pH=7 obtains ion-exchange resin catalyst after vacuum drying, is denoted as Cat-DZ-1:
The preparation of [comparative example 2] comparative catalyst
47.0 grams of styrene, 2.3 grams of divinylbenzenes and 1.6 grams of benzoyl peroxide first are added in 500 milliliters of three-necked flasks Acyl initiator is stirred to react 2.0 hours at 60 DEG C;Then 0.6 gram of multi-layer graphene is added, continues to carry out for stirring 1 hour pre- Polymerization.The 260 ml deionized water solution for being dissolved with 2.0 grams of gelatin are added.Mixing speed is adjusted, while being gradually warming up to 80 DEG C, it reacts 5 hours;It is warming up to 90 DEG C again, reacts 5 hours, is finally warming up to 98 DEG C, reacts 6 hours.After reaction, topple over Supernatant liquid out is washed with 85 DEG C of hot water, then is washed with cold water, is then filtered, and is put into 80 DEG C of drying in baking oven, is sieved, collects Composite gel microsphere DZ-2 of the partial size within the scope of 0.35~0.60mm.
Composite gel microsphere chloromethylation: in the three-necked flask of 500ml, be added 40 grams of composite gel microsphere DZ-2 and 250ml chloromethyl ether is stored at room temperature 3 hours, starts to stir, and it is catalyst that 10 grams of zinc chloride, which are added, and it is small to be warming up to 60 DEG C of reactions 10 When, it is cooled to room temperature after chloromethylation, filters out chlorination mother solution, washed repeatedly with methanol, dry 8 hours, obtain at 100 DEG C To plural gel chlorine ball DZ-2.
Halogenated alkyl POSS compound is not used: 30 grams of plural gel chlorine ball DZ-2 (chlorine being added in 500ml there-necked flask Content is 3.4mmol Cl/g), N- methylimidazole (102.0mmol) and 200ml acetonitrile, is reacted 24 hours at 60 DEG C, cooling To room temperature, filtering is successively washed with ethyl acetate, the HCl of 0.1mol/L, deionized water, methanol, and then 60 DEG C of vacuum bakings 24 are small When obtain compound imidazoles microballoon DZ-2.
In 1000ml three-necked flask, the trifluoro that 30 grams of compound imidazoles microballoon DZ-2,500ml concentration are 0.1mol/L is added Progress ion-exchange reactions 24 hours is stirred at room temperature in the deionized water solution of methanesulfonic acid lithium;It is then washed with deionized straight To washing lotion pH=7, ion-exchange resin catalyst is obtained after vacuum drying, is denoted as Cat-DZ-2:
The preparation of [comparative example 3] comparative catalyst
Nano material is not added prepares gel micro-ball: 47.0 grams of styrene of addition in 500 milliliters of three-necked flasks, 2.3 grams Divinylbenzene and 1.6 grams of benzoyl peroxide initiators.260 ml deionized waters that addition has been dissolved with 2.0 grams of gelatin are molten Liquid.Mixing speed is adjusted, is stirred 2 hours.It is stirred to react at 60 DEG C 2.0 hours, is then gradually warming up to 80 DEG C, reaction 5 is small When;It is warming up to 90 DEG C again, reacts 5 hours, is finally warming up to 98 DEG C, reacts 6 hours.After reaction, supernatant liquid is poured out, Washed with 85 DEG C of hot water, then washed with cold water, then filtered, be put into baking oven 80 DEG C of drying, sieving, collection cut size 0.35~ Gel micro-ball DZ-3 within the scope of 0.60mm.
Gel micro-ball chloromethylation: in the three-necked flask of 500ml, 40 grams of gel micro-ball DZ-3 and 250ml chloromethanes are added Ether is stored at room temperature 3 hours, starts to stir, and it is catalyst that 10 grams of zinc chloride, which are added, is warming up to 60 DEG C and reacts 10 hours, chloromethyl It is cooled to room temperature after change, filters out chlorination mother solution, washed repeatedly with methanol, dried 8 hours at 100 DEG C, obtain gel chlorine Ball DZ-3.
30 grams of gel chlorine ball DZ-3 (chlorinity is 3.3mmol Cl/g), imidazoles are added in 500ml there-necked flask (99.0mmol) and 200ml acetonitrile, reacts 24 hours at 60 DEG C, are cooled to room temperature, and filter, successively use ethyl acetate, The HCl of 0.1mol/L, deionized water, methanol washing, then 60 DEG C of vacuum bakings obtain imidazoles microballoon DZ-3 in 24 hours.
In 500ml three-necked flask, it is added 30 grams of imidazoles microballoon DZ-3 (imidazole group content is 3.1mmol/g), 9.8 grams Eight chloromethyl silsesquioxanes and 300ml tetrahydrofuran filter after reaction 24 hours at 100 DEG C, with tetrahydro furan Mutter, deionized water is successively washed, obtain imidazoles/POSS microballoon DZ-3.
In 1000ml three-necked flask, three that 30 grams of imidazoles/POSS microballoon DZ-3,500ml concentration is 0.1mol/L are added Progress ion-exchange reactions 24 hours is stirred at room temperature in the deionized water solution of fluorine methanesulfonic acid lithium;Then it is washed with deionized Until washing lotion pH=7, obtains ion-exchange resin catalyst after vacuum drying, is denoted as Cat-DZ-3:
[embodiment 7] catalytic applications
The ion-exchange resin catalyst of [embodiment 1] preparation is used for the ester exchange reaction of grease and short chain alcohol, reaction Condition is as follows: under inert gas protection, soybean oil and methanol being added in autoclave according to the molar ratio of 40:1, then The 5% catalyst Cat-A1 that quality is soybean oil quality is added, 100 DEG C of reaction temperature are reacted 6 hours.It samples after reaction Analysis measurement is carried out, the yield for measuring biodiesel is 94.2% (using the yield of fatty acid methyl ester as index).
[embodiment 8~14] catalytic applications
Change used in resin catalyst, and reaction temperature and time, remaining reaction condition all with [embodiment 7] It is identical, the ester exchange reaction of grease and short chain alcohol is carried out, obtained reaction result is shown in Table 1.
Table 1
[embodiment 15] catalytic applications
Catalyst Cat-A1 used in [embodiment 7] is filtered, is washed, it is dry, then according to the anti-of [embodiment 7] Step and reaction condition are answered, the ester exchange reaction of grease and short chain alcohol is catalyzed, obtains catalyst circulation using 2 times as a result, seeing Table 2.The rest may be inferred, carries out the catalysis that cycle-index is 3~5 times respectively and reacts, the results are shown in Table 2.
Table 2
Cycle-index 2 3 4 5
Biodiesel yield/% 94.1 94.2 94.0 94.1
[comparative example 4-6] catalytic applications
The ion-exchange resin catalyst of [comparative example 1-3] preparation is used for the ester exchange reaction of grease and short chain alcohol.Instead It answers condition as follows: under inert gas protection, soybean oil and methanol being added in autoclave according to the molar ratio of 40:1, with 5% comparative catalyst that quality is soybean oil quality is added afterwards, 100 DEG C of reaction temperature are reacted 6 hours.It samples after reaction Analysis measurement is carried out, reaction result is as shown in table 3.
Table 3
[comparative example 7] catalytic applications
By catalyst filtration used in [comparative example 4-6], wash, it is dry, then according to the reaction of [comparative example 4-6] Step and reaction condition are catalyzed the ester exchange reaction of grease and short chain alcohol, obtain catalyst circulation using 2 times as a result, being shown in Table 4.The rest may be inferred, carries out the catalysis that cycle-index is 3~5 times respectively and reacts, the results are shown in Table 4.
Table 4

Claims (10)

1. a kind of method of preparing biodiesel by ester interchange, is included under the conditions of ester exchange reaction, grease and short chain alcohol with from The step of sub-exchange resin catalyst contacts;The ion-exchange resin catalyst has following structure general formula:
Wherein,For gel-type nanocomposite resin matrix;
M-For anion, selected from trifluoromethanesulfonic acid radical ion, hydrogen sulfate ion, phosphoric acid hydrogen radical ion, tetrafluoroborate ion or Hexafluorophosphoricacid acid ions;
POSS is cage-type silsesquioxane unit, and general formula is (- SiO1.5)m;M is 6,8,10 or 12;
For glyoxaline cation unit;
Linking group of the R between POSS unit and glyoxaline cation unit, R are alkylidene or arylene;
The gel-type nanocomposite resin matrix is that styrene monomer, comonomer and nano material are obtained through in-situ copolymerization Nanogel type copolymer;The nano material is in single-layer graphene, multi-layer graphene, graphene oxide, graphite alkene At least one.
2. the method for preparing biodiesel by ester interchange according to claim 1, which is characterized in that POSS unit it is described from Content in sub-exchange resin catalyst is 5~15 weight %.
3. the method for preparing biodiesel by ester interchange according to claim 1, which is characterized in that M- is trifluoromethanesulfonic acid root Ion.
4. the method for preparing biodiesel by ester interchange according to claim 1, which is characterized in that alkylidene is selected from methylene Base, ethylidene or propylidene;Arylene is selected from phenylene, naphthylene or sub- benzyl.
5. the method for preparing biodiesel by ester interchange according to claim 1, which is characterized in that the styrene monomer Selected from least one of styrene, α-methylstyrene or 4- butylstyrene;
The comonomer is selected from ethyleneglycol dimethyacrylate, diallyl benzene, divinyl phenylmethane or divinyl At least one of base benzene.
6. the method for preparing biodiesel by ester interchange according to claim 5, which is characterized in that the styrene monomer Selected from styrene;The comonomer is selected from divinylbenzene.
7. the method for preparing biodiesel by ester interchange according to claim 1, which is characterized in that the nano material is selected from Multi-layer graphene.
8. the method for preparing biodiesel by ester interchange according to claim 1, which is characterized in that the use of styrene monomer Amount is 85~95 parts, and the dosage of comonomer is 2~5 parts, and the dosage of nano material is 0.1~3 part.
9. the method for preparing biodiesel by ester interchange according to claim 1, which is characterized in that the grease is selected from fat Any one of vegetable and animals oils of acid glyceride;The short chain alcohol is any in methanol, ethyl alcohol, propyl alcohol or butanol.
10. the method for preparing biodiesel by ester interchange according to claim 1, which is characterized in that the ester exchange reaction Condition includes: that the molar ratio of short chain alcohol and grease is (10~50): 1, catalyst amount is the 1~15% of raw oil material quality, 40~180 DEG C of reaction temperature, the reaction time 1~24 hour.
CN201711111543.0A 2017-11-13 2017-11-13 Method for preparing biodiesel by ester exchange method Active CN109777630B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711111543.0A CN109777630B (en) 2017-11-13 2017-11-13 Method for preparing biodiesel by ester exchange method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711111543.0A CN109777630B (en) 2017-11-13 2017-11-13 Method for preparing biodiesel by ester exchange method

Publications (2)

Publication Number Publication Date
CN109777630A true CN109777630A (en) 2019-05-21
CN109777630B CN109777630B (en) 2022-10-11

Family

ID=66484833

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711111543.0A Active CN109777630B (en) 2017-11-13 2017-11-13 Method for preparing biodiesel by ester exchange method

Country Status (1)

Country Link
CN (1) CN109777630B (en)

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101418225A (en) * 2007-10-23 2009-04-29 北京化工大学 Method for preparing biodiesel by using supported solid acid combining cosolvent
CN103664583A (en) * 2013-12-04 2014-03-26 河北工程大学 Method for preparing biodiesel by gemini ionic liquid catalyst
CN105924464A (en) * 2016-05-18 2016-09-07 上海大学 Octa-imidazolyl POSS room temperature ionic liquid and preparation method thereof
CN106391113A (en) * 2015-08-03 2017-02-15 中国石油化工股份有限公司 Immobilized ionic liquid catalyst and application thereof

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101418225A (en) * 2007-10-23 2009-04-29 北京化工大学 Method for preparing biodiesel by using supported solid acid combining cosolvent
CN103664583A (en) * 2013-12-04 2014-03-26 河北工程大学 Method for preparing biodiesel by gemini ionic liquid catalyst
CN106391113A (en) * 2015-08-03 2017-02-15 中国石油化工股份有限公司 Immobilized ionic liquid catalyst and application thereof
CN105924464A (en) * 2016-05-18 2016-09-07 上海大学 Octa-imidazolyl POSS room temperature ionic liquid and preparation method thereof

Also Published As

Publication number Publication date
CN109777630B (en) 2022-10-11

Similar Documents

Publication Publication Date Title
Yang et al. Biodiesel production from rubber seed oil using poly (sodium acrylate) supporting NaOH as a water-resistant catalyst
CN103588190B (en) A kind of method being prepared carbosphere by lignocellulose
Chen et al. Bifunctional acid-activated montmorillonite catalyzed biodiesel production from non-food oil: Characterization, optimization, kinetic and thermodynamic studies
Suresh et al. Esterification of free fatty acids in non-edible oils using partially sulfonated polystyrene for biodiesel feedstock
CN102963898A (en) Preparation method of dual-functional group organically modified montmorillonite
CN104815690B (en) A kind of more sulfonic acid funtionalized mesoporous polymer solid acid catalysts and its preparation method and application
CN103638973A (en) Preparation method of sulfoacid-type cation exchange resin catalyst
Gómez-Trejo-López et al. Waste cooking oil transesterification by sulfonated polyphenylsulfone catalytic membrane: Characterization and biodiesel production yield
CN103242914A (en) Method for rapidly producing biodiesel from kitchen garbage and produced biodiesel
CN109574807A (en) The method of epoxyalkane catalysis hydration preparing ethylene glycol
Wang et al. Efficient production of methyl oleate using a biomass-based solid polymeric catalyst with high acid density
CN109569717A (en) Ion exchange resin and purposes
Li et al. Catalytic hydrothermal saccharification of rice straw using mesoporous silica-based solid acid catalysts
CN109777630A (en) The method of preparing biodiesel by ester interchange
CN100375780C (en) Production of biological diesel oil with solid alkali
CN109777628A (en) The method for preparing biodiesel
CN109777466A (en) The method of transesterification legal system biodiesel
CN109777624A (en) The method of preparing biodiesel by ester exchange
CN109777629A (en) The preparation method of biodiesel
CN109777627A (en) The method of transesterification biodiesel
CN109777626A (en) The production method of biodiesel
CN109776264A (en) The method of olefine aldehyde condensation reaction
CN109777625A (en) The synthetic method of biodiesel
CN102492559A (en) Method for preparing biodiesel in novel alkaline ionic liquid
CN102321489A (en) Method for catalyzing and liquefying agricultural wastes by using ion liquid

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