CN105085187B - The method of preparing ethyl glycol by hydrolysis of ethylene carbonate - Google Patents

The method of preparing ethyl glycol by hydrolysis of ethylene carbonate Download PDF

Info

Publication number
CN105085187B
CN105085187B CN201410202046.1A CN201410202046A CN105085187B CN 105085187 B CN105085187 B CN 105085187B CN 201410202046 A CN201410202046 A CN 201410202046A CN 105085187 B CN105085187 B CN 105085187B
Authority
CN
China
Prior art keywords
ethylene carbonate
hydrolysis
catalyst
quaternary ammonium
consumption
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201410202046.1A
Other languages
Chinese (zh)
Other versions
CN105085187A (en
Inventor
陈梁锋
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 CN201410202046.1A priority Critical patent/CN105085187B/en
Publication of CN105085187A publication Critical patent/CN105085187A/en
Application granted granted Critical
Publication of CN105085187B publication Critical patent/CN105085187B/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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/50Improvements relating to the production of bulk chemicals
    • Y02P20/52Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts

Landscapes

  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The present invention relates to a kind of method of preparing ethyl glycol by hydrolysis of ethylene carbonate, mainly solve prior art and there is resin to be easily swelled, the problem of activity decrease is fast.The present invention is by using using ethylene carbonate and water as reaction raw materials, it it is 60~180 DEG C in reaction temperature, the mol ratio of water and ethylene carbonate is 1~10, and the weight ratio of catalyst and ethylene carbonate is that under conditions of 0.005~1, raw material obtains ethylene glycol in 1~8 hour with catalyst haptoreaction;Wherein, the catalyst preferably solves the problem for the technical scheme of the nano combined quaternary ammonium resin of strong base, available in the industrial production of preparing ethyl glycol by hydrolysis of ethylene carbonate.

Description

The method of preparing ethyl glycol by hydrolysis of ethylene carbonate
Technical field
The present invention relates to a kind of method of preparing ethyl glycol by hydrolysis of ethylene carbonate.
Background technology
The hydrolysis of esters is a kind of important chemical reaction, is widely used in the every field of petrochemical iy produced, its middle ring Shape carbonic ester, such as ethylene carbonate (EC), the hydrolysis of propene carbonate are even more to have very important fundamental position.
EC hydrolysis is the important step that ethylene glycol (EG) is produced by oxirane (EO) catalysis hydration two-step method.EG is one Important Organic Chemicals is planted, is mainly used to production polyester fiber, antifreezing agent, unsaturated polyester resin, non-ionic surface and lives Property agent, monoethanolamine and explosive etc..EG production technology is broadly divided into petrochemical industry route and non-petrochemical industry route.Have in petrochemical industry route EO direct hydration methods and EO catalytic hydrations, direct hydration method need higher water ratio (being more than 20) just to can guarantee that higher EG Yield, and it is higher to be consumed energy during purifying EG.EO catalytic hydrations include direct catalytic hydration and EC routes again.Directly urge Change hydration method water than relatively low (about 5 or so), but still need evaporation and remove substantial amounts of water, and EC routes are then first with second Alkene aoxidizes the CO2 discharged during EO processed and EC is generated in the presence of catalyst with EO for raw material, is then catalyzed by intermediate product of EC Hydrolysis generation EG, the process water ratio, close to stoichiometric proportion 1, is the industrialization direction of EO EG from now on.
Having been used for the catalyst of annular carbonic acid esters hydrolysis at present mainly has:Alkali (soil) metal carbonate (hydrogen) salt (US4524224,1985), Mo and W compound (JP822106631,1982;WO2009071651,2009), quaternary ammonium salt, season Ammonium salt and ion exchange resin (EP0133763,1989;US6080897,2000;US20090156867,2009) etc..But these More or less there is difficult, the active low, stability of catalyst separation not in catalyst system and catalyzing.
Activity and selectivity is all preferable when strong base ion exchange resin is for annular carbonic acid esters hydrolysis, but is due to that its is resistance to Gentle swelling resistance poor performance, activity decrease very fast (Yu FP, Cai H, the He WJ, et in catalytic reaction process al.J.Appl.Polym.Sci.,2010,115:2946~2954), this is to cause the catalyst to fail industrialized main original Cause.
The content of the invention
The technical problems to be solved by the invention are that prior art has resin catalyst and is easily swelled, activity decrease asking soon There is provided a kind of method of new preparing ethyl glycol by hydrolysis of ethylene carbonate for topic.This method has heatproof, swelling resistance, activity decrease Slow the characteristics of.
In order to solve the above technical problems, the technical solution adopted by the present invention is as follows:A kind of ethylene carbonate ester hydrolysis prepares second The method of glycol, is 60~180 DEG C in reaction temperature using ethylene carbonate and water as reaction raw materials, water and ethylene carbonate Mol ratio is 1~10, and the weight ratio of catalyst and ethylene carbonate is that under conditions of 0.005~1, raw material is contacted instead with catalyst Answer 1~8 hour and obtain ethylene glycol;Wherein, the catalyst is the nano combined quaternary ammonium resin of strong base.
In above-mentioned technical proposal, it is preferable that the preparation method of the nano combined quaternary ammonium resin of strong base includes following Step:
A) auxiliary agent one is made into the water solution A that weight percent concentration is 0.5~2%, by monomer, comonomer, nanometer Material, initiator and the wiring solution-forming B of auxiliary agent two;
Wherein, the monomer is selected from methyl methacrylate, butyl acrylate, styrene, α-methylstyrene, 4- butyl At least one of styrene or acrylonitrile;
The comonomer is selected from ethyleneglycol dimethyacrylate, diallyl benzene, divinyl phenylmethane or two At least one of vinyl benzene;
The nano material is selected from least one of multi-walled carbon nanotube, single-walled carbon nanotube, C60 or C70 fullerenes;
The initiator is selected from benzoyl peroxide, azodiisobutyronitrile, lauroyl peroxide or isopropyl benzene hydroperoxide At least one of;
The auxiliary agent one in polyvinyl alcohol, gelatin, starch, methylcellulose, bentonite or calcium carbonate at least one Kind;
The auxiliary agent two is selected from least one of aliphatic hydrocarbon, polystyrene, gasoline, aliphatic acid or paraffin;
By weight percentage, the consumption of monomer is 85~95%, and the consumption of comonomer is 2~5%, nano material Consumption is 0.1~3%, and the consumption of initiator is 0.1~10%;The consumption of auxiliary agent one is the 150~400% of monomer consumption, is helped The consumption of agent two is the 50~100% of monomer consumption;
B) then solution B is mixed in 60~75 DEG C of prepolymerizations 0.5~2.5 hour, is warming up to 70 by solution B with solution A ~90 DEG C react 5~15 hours, then be warming up to 90~100 DEG C react 5~15 hours;After reaction terminates, through extracting, washing, mistake Filter, dry, sieving, obtain the complex microsphere of 0.35~0.60 millimeter of particle size range;
C) chloromethylation reagents equivalent to complex microsphere weight 200~500% are added into complex microsphere, and quite In the zinc chloride catalyst of complex microsphere weight 20~70%, reacted 8~30 hours at 30~60 DEG C, through filtering, washing To compound chlorine ball, drying to constant weight;The chloromethylation reagents in chloromethyl ether or 1,4- dichloro methyl butyl ethers at least It is a kind of;
D) organic solvent equivalent to complex microsphere weight 200~700%, 200~500% are added into compound chlorine ball Tertiary amine NR1R2R3, react 4~30 hours under reflux state, the nano combined quaternary ammonium salt tree of the chlorine type obtained after scrubbed, drying Fat;Wherein, the organic solvent in cyanophenyl, toluene, tetrahydrofuran, dimethylformamide, chloroform or dichloroethanes extremely Few one kind;PR1R2R3In, R1、R2、R3For methyl, ethyl, propyl group, normal-butyl, phenyl or aryl;
E) the nano combined quaternary ammonium salt tree of the strong base is obtained after the nano combined quaternary ammonium resin of chlorine type is exchanged with highly basic Fat.
In above-mentioned technical proposal, it is preferable that the monomer is selected from styrene.
In above-mentioned technical proposal, it is preferable that the comonomer is selected from divinylbenzene.
In above-mentioned technical proposal, it is preferable that the nano material is selected from multi-walled carbon nanotube.
In above-mentioned technical proposal, it is preferable that the initiator is selected from benzoyl peroxide.
In above-mentioned technical proposal, it is preferable that the auxiliary agent one is selected from polyvinyl alcohol.
In above-mentioned technical proposal, it is preferable that the auxiliary agent two is selected from polystyrene.
In above-mentioned technical proposal, it is preferable that the highly basic is selected from NaOH, KOH, LiOH, Ca (OH)2、Sr(OH)2Or Ba (OH)2At least one of.
In above-mentioned technical proposal, it is preferable that reaction temperature is 80~160 DEG C, the mol ratio of water and ethylene carbonate for 1~ 8, the weight ratio of catalyst and ethylene carbonate is 0.01~0.5, and the reaction time is 1~6 hour.
In the inventive method, the method that the nano combined quaternary ammonium resin of chlorine type is exchanged with highly basic is for those skilled in the art Known.Usually, it can be added into the nano combined quaternary ammonium resin of chlorine type equivalent to the nano combined quaternary ammonium salt tree of chlorine type The highly basic of fat weight 20~200%, 200~2000% deionized water, are stirred at room temperature 1~20 hour, through filtering, washing Afterwards, repeat said process 2 times, then through filtering, washing and dry.
The inventive method is mixed due to using the nano combined quaternary ammonium resin of strong base for catalyst in resin base material The nano material of high intensity is entered, so as to enhance the resistance to gentle resistance to swelling energy of resin.Using the inventive method, in reaction temperature 100 DEG C of degree, the mol ratio of water and ethylene carbonate is 1.5, and the weight ratio of catalyst and ethylene carbonate is under the conditions of 0.05, instead Answer 2 hours, the conversion ratio of ethylene carbonate is up to 99.4%, and the selectivity of ethylene glycol is up to 99.6%, and catalyst reuses 5 After secondary, activity decrease is less than 5%, achieves preferable technique effect.
Below by embodiment, the invention will be further elaborated.It is necessarily pointed out that following examples are only used Further illustrated in the present invention, it is impossible to be interpreted as limiting the scope of the invention.
Embodiment
【Embodiment 1】
58.0 grams of styrene, 0.6 gram of divinylbenzene, 30 grams of polystyrene and 0.6 are added in 500 milliliters of three-necked flasks Gram benzoyl peroxide initiator, in being stirred 2.0 hours at 60 DEG C;Then 2.8 grams of multi-walled carbon nanotubes are added, continue to stir 1 Hour carries out prepolymerization.Add the 260 ml deionized water solution for being dissolved with 2.5 grams of polyvinyl alcohol.Mixing speed is adjusted, together When be progressively warming up to 80 DEG C, react 5 hours;90 DEG C are warming up to again, is reacted 5 hours, 98 DEG C are finally warming up to, and are reacted 6 hours.Instead After should terminating, supernatant liquid is poured out, washs, then filters with 85 DEG C of hot washes, then with cold water, 80 DEG C of bakings in baking oven are put into It is dry, sieving, complex microsphere A of the collection cut size in the range of 0.35~0.60 millimeter.
The chloromethylation of complex microsphere:In 500 milliliters of three-necked flask, 50 grams of complex microsphere A and 250 milliliters of chlorine are added Methyl ether, is stored at room temperature 4 hours, starts stirring, and it is catalyst to add 15 grams of zinc chloride, is warming up to 50 DEG C and reacts 8 hours, chlorination knot Room temperature is cooled to after beam, chlorination mother solution is filtered out, methanol cyclic washing is used, dried 8 hours at 100 DEG C, compound chlorine ball A is obtained.
The quaternization of compound chlorine ball:In 500 milliliters of there-necked flasks, 20 grams of compound chlorine ball A, 100 milliliters of tetrahydrochysene furans are added Mutter, 20.0 grams of Trimethylamines, stirring reaction 12 hours, react and mother liquor are filtered to remove after terminating, respectively successively at reflux With dichloromethane, acetone and water washing, the nano combined quaternary ammonium resin A1 of chlorine type is dried to obtain under vacuo.
The transition of the nano combined quaternary ammonium resin of chlorine type:In 200 milliliters of beakers, 10 grams of nano combined quaternary ammoniums of chlorine type are added Salt resin A1,3 grams of NaOH and 180 gram of deionized waters, were stirred at room temperature after 2 hours, filtering, after being washed with deionized, in repetition State process 2 times, filter, be washed with deionized, drying under vacuo obtains the nano combined quaternary ammonium resin A2 of strong base.
【Embodiment 2】
In 500 milliliters of there-necked flasks, 20 grams are added【Embodiment 1】The compound chlorine ball A of gained, 150 milliliters of tetrahydrofurans, 35.0 grams of tri-butylamines, stirring reaction 30 hours, react and mother liquor are filtered to remove after terminating, respectively successively with two at reflux Chloromethanes, acetone and water washing, dry to obtain the nano combined quaternary ammonium resin A3 of chlorine type under vacuo.
The transition of the nano combined quaternary ammonium resin of chlorine type:In 200 milliliters of beakers, 10 grams of nano combined quaternary ammoniums of chlorine type are added Salt resin A3,20 grams of Ba (OH)2With 40 grams of deionized waters, it is stirred at room temperature after 18 hours, filters, after being washed with deionized, weight Said process 2 times, filtering, are washed with deionized again, and drying under vacuo obtains the nano combined quaternary ammonium resin A4 of strong base.
【Embodiment 3】
Monomer mixture solution (60.0 grams of styrene, 1.7 grams containing initiator are added in 500 milliliters of three-necked flasks Divinylbenzene, 60 grams of polystyrene, 1.6 grams of multi-walled carbon nanotubes and 1.0 grams of benzoyl peroxides, the solution are stirred prior to 70 DEG C Mix reaction 0.5 hour), agitator is started, the mixed solution of 200 ml deionized waters and 5 grams of gelatin is added, is warming up to 85 DEG C, Reaction 3 hours, then it is warming up to 90 DEG C, react 9 hours, be finally warming up to 100 DEG C, react 10 hours.After reaction terminates, pour out Supernatant liquid, is washed with 85 DEG C of hot washes, then with cold water, then filters, and is put into 80 DEG C of drying in baking oven, and grain is collected in sieving Complex microsphere B of the footpath in the range of 0.35~0.60 millimeter.
The chloromethylation of complex microsphere:In 500 milliliters of three-necked flask, 50 grams of complex microsphere B and 150 milliliters of chlorine are added Methyl ether, is stored at room temperature 6 hours, starts stirring, and it is catalyst to add 30 grams of zinc chloride, is warming up to 50 DEG C and reacts 24 hours, chlorination Room temperature is cooled to after end, chlorination mother solution is filtered out, methanol cyclic washing is used, dried 8 hours at 100 DEG C, compound chlorine ball is obtained B。
The quaternization of compound chlorine ball:In 500 milliliters of there-necked flasks, 20 grams of compound chlorine ball B, 150 milliliters of tetrahydrochysene furans are added Mutter, 30.0 grams of tri-butylamines, stirring reaction 24 hours, react and mother liquor are filtered to remove after terminating, respectively successively at reflux With dichloromethane, acetone and water washing, the nano combined quaternary ammonium resin B1 of chlorine type is dried to obtain under vacuo.
The nano combined quaternary ammonium resin B1 of chlorine type is used【Embodiment 2】Described method is made the transition, and is obtained strong base and is received Rice compound quaternary ammonium salt resin B 2.
【Embodiment 4】
In 500 milliliters of there-necked flasks, 15 grams are added【Embodiment 3】The compound chlorine ball B of gained, 150 milliliters of tetrahydrofurans, 35.0 grams of triethylamines, stirring reaction 10 hours, react and mother liquor are filtered to remove after terminating, respectively successively with two at reflux Chloromethanes, acetone and water washing, dry to obtain the nano combined quaternary ammonium resin B3 of chlorine type under vacuo.
The nano combined quaternary ammonium resin B3 of chlorine type will be used【Embodiment 2】Described method is made the transition, and obtains strong base Nano combined quaternary ammonium resin B4.
【Embodiment 5】
Change【Embodiment 3】In monomer mixture solution (76.0 grams of α-methylstyrenes, 3.5 grams of divinylbenzenes, 75 Gram gasoline, 2.4 grams of multi-walled carbon nanotubes and 1.4 grams of benzoyl peroxides), remaining preparation condition with【Embodiment 3】It is identical, obtain Complex microsphere C.
The chloromethylation of complex microsphere:In 500 milliliters of three-necked flask, 40 grams of complex microsphere C and 150 milliliter 1 are added, 4- dichloro methyl butyl ethers, are stored at room temperature 6 hours, start stirring, and it is catalyst to add 25 grams of zinc chloride, is warming up to 50 DEG C of reactions 24 hours, chlorination was cooled to room temperature after terminating, and filters out chlorination mother solution, used methanol cyclic washing, dries 8 hours, obtains at 100 DEG C To compound chlorine ball C.
The quaternization of compound chlorine ball:In 500 milliliters of there-necked flasks, 30 grams of compound chlorine ball A, 150 milliliters of tetrahydrochysene furans are added Mutter, 20.0 grams of triethylamines, stirring reaction 12 hours, react and mother liquor are filtered to remove after terminating, respectively successively at reflux With dichloromethane, acetone and water washing, the nano combined quaternary ammonium resin C1 of chlorine type is dried to obtain under vacuo.
The nano combined quaternary ammonium resin C1 of chlorine type is used【Embodiment 2】Described method is made the transition, and is obtained strong base and is received Rice compound quaternary ammonium salt resin C2.
【Embodiment 6】
According to【Embodiment 4】The step of quaternization reaction is carried out to compound chlorine ball C, obtain nano combined quaternary ammonium resin C3。
The nano combined quaternary ammonium resin C3 of chlorine type is used【Embodiment 2】Described method is made the transition, and is obtained strong base and is received Rice compound quaternary ammonium salt resin C4.
【Embodiment 7】
Will【Embodiment 1】The nano combined quaternary ammonium resin A2 of prepared strong base prepares carbon for ethylene carbonate ester hydrolysis In the reaction of vinyl acetate.By 44.0 grams of ethylene carbonates, 13.5 grams of deionized waters and 2.2 grams【Embodiment 1~9】What is prepared urges Agent is placed in 100 milliliters of autoclaves that (mol ratio of water and ethylene carbonate is 1.5, the quality of catalyst and ethylene carbonate Than for 0.05), 100 DEG C are reacted 2 hours.After reaction terminates, autoclave is cooled to room temperature, is vented.Liquid product is taken to enter promoting the circulation of qi Analysis of hplc, the conversion ratio for measuring ethylene carbonate is 99.4%, and the selectivity of ethylene glycol is 99.6%, resin catalyst Swellbility is SSWELLFor 3.9%.
【Embodiment 8~12】
Strong base nano combined quaternary ammonium resin species used in changing, remaining condition with【Embodiment 7】Described phase Together, the result obtained is as shown in table 1.
Table 1
【Embodiment 13】
Together【Embodiment 7】, simply reaction temperature is 120 DEG C.The conversion ratio for obtaining ethylene carbonate is 99.8%, ethylene glycol Selectivity be 99.1%, the selectivity of many ethylene glycol is 0.9%.
【Embodiment 14】
Together【Embodiment 7】, simply reaction temperature is 140 DEG C.The conversion ratio for obtaining ethylene carbonate is 99.5%, ethylene glycol Selectivity be 98.8%, the selectivity of many ethylene glycol is 1.2%.
【Embodiment 15】
Together【Embodiment 7】, simply reaction temperature is 80 DEG C.The conversion ratio for obtaining ethylene carbonate is 67.8%, ethylene glycol Selectivity be 99.1%, the selectivity of many ethylene glycol is 0.9%.
【Embodiment 16】
Together【Embodiment 7】, simply the consumption of deionized water is 27.0 grams (mol ratio of water and ethylene carbonate is 3). It is 99.5% to ethylene carbonate ester conversion rate, the selectivity of ethylene glycol is 99.3%, the selectivity of many ethylene glycol is 0.7%.
【Embodiment 17】
Together【Embodiment 7】, simply the consumption of deionized water is 72.0 grams (mol ratio of water and ethylene carbonate is 8). It is 99.4% to ethylene carbonate ester conversion rate, the selectivity of ethylene glycol is 99.5%, the selectivity of many ethylene glycol is 0.5%.
【Embodiment 18】
Together【Embodiment 7】, simply the consumption of catalyst is 1.1 grams (ratio of catalyst and ethylene carbonate is 0.025). It is 66.8% to obtain ethylene carbonate ester conversion rate, and the selectivity of ethylene glycol is 99.3%, and the selectivity of many ethylene glycol is 0.7%.
【Embodiment 19】
Together【Embodiment 7】, simply catalyst amount is 8.8 grams (ratio of catalyst and ethylene carbonate is 0.2).Obtain Ethylene carbonate ester conversion rate is 99.3%, and the selectivity of ethylene glycol is 98.0%, and the selectivity of many ethylene glycol is 2.0%.
【Embodiment 20】
Together【Embodiment 7】, simply the consumption of catalyst be 17.6 grams (the weight ratio of catalyst and ethylene carbonate be 0.4).It is 99.4% to obtain ethylene carbonate ester conversion rate, and the selectivity of ethylene glycol is 96.1%, and the selectivity of many ethylene glycol is 3.9%.
【Embodiment 21】
Will【Embodiment 7】Catalyst after reaction terminates is applied mechanically 5 times by same reaction conditions, and activity is not decreased obviously. Reaction result is shown in Table 3.
Table 2
【Comparative example 1】
Together【Embodiment 1】, be simply added without multi-walled carbon nanotube, obtain microballoon D, chlorine ball D, chlorine type quaternary ammonium resin D1 and Strong base quaternary ammonium resin D2.D2 is used into ethylene carbonate and water hydrolysis to prepare in the reaction of ethylene glycol, reaction condition with【It is real Apply example 7】Identical, the conversion ratio for obtaining ethylene carbonate is 98.9%, and the selectivity of ethylene glycol is 99.1%, the swelling ratio of resin SSWELLFor 16.7%.The catalyst reacted after terminating is applied mechanically 5 times by same reaction conditions, activity is decreased obviously.Reaction result It is shown in Table 3.
Table 3

Claims (8)

1. a kind of method of preparing ethyl glycol by hydrolysis of ethylene carbonate, using ethylene carbonate and water as reaction raw materials, in reaction temperature Spend for 60~180 DEG C, the mol ratio of water and ethylene carbonate is 1~10, the weight ratio of catalyst and ethylene carbonate is 0.005 Under conditions of~1, raw material obtains ethylene glycol in 1~8 hour with catalyst haptoreaction;Wherein, the catalyst is received for strong base Rice compound quaternary ammonium salt resin;
The preparation method of the nano combined quaternary ammonium resin of strong base comprises the following steps:
A) by auxiliary agent one be made into weight percent concentration be 0.5~2% water solution A, by monomer, comonomer, nano material, Initiator and the wiring solution-forming B of auxiliary agent two;
Wherein, the monomer is selected from methyl methacrylate, butyl acrylate, styrene, α-methylstyrene, 4- butyl benzene second At least one of alkene or acrylonitrile;
The comonomer is selected from ethyleneglycol dimethyacrylate, diallyl benzene, divinyl phenylmethane or divinyl At least one of base benzene;
The nano material is selected from multi-walled carbon nanotube;
The initiator is in benzoyl peroxide, azodiisobutyronitrile, lauroyl peroxide or isopropyl benzene hydroperoxide It is at least one;
The auxiliary agent one is selected from least one of polyvinyl alcohol, gelatin, starch, methylcellulose, bentonite or calcium carbonate;
The auxiliary agent two is selected from least one of aliphatic hydrocarbon, polystyrene, gasoline, aliphatic acid or paraffin;
By weight percentage, the consumption of monomer is 85~95%, and the consumption of comonomer is 2~5%, the consumption of nano material For 0.1~3%, the consumption of initiator is 0.1~10%;The consumption of auxiliary agent one is the 150~400% of monomer consumption, auxiliary agent two Consumption be monomer consumption 50~100%;
B) then solution B is mixed in 60~75 DEG C of prepolymerizations 0.5~2.5 hour, is warming up to 70~90 by solution B with solution A DEG C reaction 5~15 hours, then be warming up to 90~100 DEG C react 5~15 hours;After reaction terminates, through extracting, washing, filter, do Dry, sieving, obtains the complex microsphere of 0.35~0.60 millimeter of particle size range;
C) chloromethylation reagents equivalent to complex microsphere weight 200~500% are added into complex microsphere, and equivalent to multiple The zinc chloride catalyst of microspheres weight 20~70% is closed, is reacted 8~30 hours at 30~60 DEG C, is answered through filtering, washing Close chlorine ball, drying to constant weight;The chloromethylation reagents are selected from least one of chloromethyl ether or 1,4- dichloro methyl butyl ethers;
D) organic solvent, 200~500% tertiary amine equivalent to complex microsphere weight 200~700% are added into compound chlorine ball NR1R2R3, react 4~30 hours under reflux state, the nano combined quaternary ammonium resin of the chlorine type obtained after scrubbed, drying;Its In, the organic solvent in cyanophenyl, toluene, tetrahydrofuran, dimethylformamide, chloroform or dichloroethanes at least one Kind;NR1R2R3In, R1、R2、R3For methyl, ethyl, propyl group, normal-butyl or phenyl;
E) the nano combined quaternary ammonium resin of the strong base is obtained after the nano combined quaternary ammonium resin of chlorine type is exchanged with highly basic.
2. the method for preparing ethyl glycol by hydrolysis of ethylene carbonate according to claim 1, it is characterised in that monomer is selected from benzene second Alkene.
3. the method for preparing ethyl glycol by hydrolysis of ethylene carbonate according to claim 1, it is characterised in that comonomer is selected from Divinylbenzene.
4. the method for preparing ethyl glycol by hydrolysis of ethylene carbonate according to claim 1, it is characterised in that initiator was selected from BP.
5. the method for preparing ethyl glycol by hydrolysis of ethylene carbonate according to claim 1, it is characterised in that auxiliary agent one is selected from poly- Vinyl alcohol.
6. the method for preparing ethyl glycol by hydrolysis of ethylene carbonate according to claim 1, it is characterised in that auxiliary agent two is selected from poly- Styrene.
7. the method for preparing ethyl glycol by hydrolysis of ethylene carbonate according to claim 1, it is characterised in that the highly basic is selected from NaOH、KOH、LiOH、Ca(OH)2、Sr(OH)2Or Ba (OH)2At least one of.
8. the method for preparing ethyl glycol by hydrolysis of ethylene carbonate according to claim 1, it is characterised in that reaction temperature is 80 ~160 DEG C, the mol ratio of water and ethylene carbonate is 1~8, and the weight ratio of catalyst and ethylene carbonate is 0.01~0.5, instead It is 1~6 hour between seasonable.
CN201410202046.1A 2014-05-14 2014-05-14 The method of preparing ethyl glycol by hydrolysis of ethylene carbonate Active CN105085187B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410202046.1A CN105085187B (en) 2014-05-14 2014-05-14 The method of preparing ethyl glycol by hydrolysis of ethylene carbonate

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410202046.1A CN105085187B (en) 2014-05-14 2014-05-14 The method of preparing ethyl glycol by hydrolysis of ethylene carbonate

Publications (2)

Publication Number Publication Date
CN105085187A CN105085187A (en) 2015-11-25
CN105085187B true CN105085187B (en) 2017-08-11

Family

ID=54566625

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410202046.1A Active CN105085187B (en) 2014-05-14 2014-05-14 The method of preparing ethyl glycol by hydrolysis of ethylene carbonate

Country Status (1)

Country Link
CN (1) CN105085187B (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107915578B (en) * 2016-10-08 2021-02-09 中国石油化工股份有限公司 Method for producing ethylene glycol by ethylene carbonate hydrolysis
CN107353225A (en) * 2017-05-04 2017-11-17 南京齐正化学有限公司 A kind of preparation method of 2 isopropylidene amino ethoxy-ethanol

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101121642A (en) * 2006-08-10 2008-02-13 中国科学院过程工程研究所 Catalytic method used for cyclic carbonates hydrolysis
CN101528649A (en) * 2006-09-07 2009-09-09 国际壳牌研究有限公司 Process for the preparation of alkylene glycol
CN103122045A (en) * 2011-11-18 2013-05-29 中国石油化工股份有限公司 Nano composite quaternary phosphonium salt resin

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101121642A (en) * 2006-08-10 2008-02-13 中国科学院过程工程研究所 Catalytic method used for cyclic carbonates hydrolysis
CN101528649A (en) * 2006-09-07 2009-09-09 国际壳牌研究有限公司 Process for the preparation of alkylene glycol
CN103122045A (en) * 2011-11-18 2013-05-29 中国石油化工股份有限公司 Nano composite quaternary phosphonium salt resin

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
Synthesis and Characterization of a Polymer/Multiwalled Carbon Nanotube Composite and Its Application in the Hydration of Ethylene Oxide;Fengping Yu et al.;《Journal ofAppliedPolymer Science》;20091026;第115卷;2946-2954 *

Also Published As

Publication number Publication date
CN105085187A (en) 2015-11-25

Similar Documents

Publication Publication Date Title
CN105503811B (en) The method for preparing ethylene carbonate
CN103121987B (en) Method for preparing alkylene carbonate
CN103122045B (en) Nano composite quaternary phosphonium salt resin
CN105440007B (en) The method of synthesizing ethylene carbonate
CN106391112A (en) Immobilized ionic liquid catalyst and application thereof
CN104525260B (en) Polymeric solid acid catalyst for esterification reaction and preparation method thereof
CN105439866B (en) The method that ester exchange prepares dimethyl carbonate
CN105085187B (en) The method of preparing ethyl glycol by hydrolysis of ethylene carbonate
CN106391113A (en) Immobilized ionic liquid catalyst and application thereof
CN105272858B (en) The production method of dimethyl carbonate
CN105503529B (en) Method for preparing ethyl glycol by hydrolysis of ethylene carbonate
CN112619705B (en) Alkylene oxide addition reaction catalyst and application thereof
CN105503528B (en) The method that ethylene carbonate ester hydrolysis produces ethylene glycol
CN106391114A (en) Immobilized ionic liquid catalyst and application thereof
CN105272822B (en) Method used for preparation of ethylene glycol by hydrolyzation of ethylene carbonate
CN105503520B (en) The method of preparing ethyl glycol by hydrolysis of ethylene carbonate
CN105503608B (en) The method for producing ethylene carbonate
CN106824283A (en) A kind of attapulgite reinforced resin solid acid catalyst and preparation method thereof
CN103709010B (en) A kind of by tetrahydrobenzene, carboxylic acid and water Reactive Synthesis hexalin method
CN105503607B (en) The method for preparing dimethyl carbonate
CN105503519B (en) The production method of dimethyl carbonate
CN102757406B (en) Styrene epoxidation method for preparing styrene oxide
CN105503609B (en) The method for producing dimethyl carbonate
CN102049305B (en) Method for preparing titanium silicon molecular sieve catalyst
CN102049304A (en) Titanium-silicon molecular sieve and resin composite catalyst and preparation method thereof

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant