CN108440255A - A kind of synthetic method of high-purity methyl tertbutyl ether - Google Patents

A kind of synthetic method of high-purity methyl tertbutyl ether Download PDF

Info

Publication number
CN108440255A
CN108440255A CN201810378751.5A CN201810378751A CN108440255A CN 108440255 A CN108440255 A CN 108440255A CN 201810378751 A CN201810378751 A CN 201810378751A CN 108440255 A CN108440255 A CN 108440255A
Authority
CN
China
Prior art keywords
parts
added
mixed
mtbe
butyl ether
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201810378751.5A
Other languages
Chinese (zh)
Inventor
陈久仓
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to CN201810378751.5A priority Critical patent/CN108440255A/en
Publication of CN108440255A publication Critical patent/CN108440255A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C41/00Preparation of ethers; Preparation of compounds having groups, groups or groups
    • C07C41/01Preparation of ethers
    • C07C41/05Preparation of ethers by addition of compounds to unsaturated compounds
    • C07C41/06Preparation of ethers by addition of compounds to unsaturated compounds by addition of organic compounds only
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/06Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides containing polymers
    • B01J31/08Ion-exchange resins
    • B01J31/10Ion-exchange resins sulfonated
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C41/00Preparation of ethers; Preparation of compounds having groups, groups or groups
    • C07C41/01Preparation of ethers
    • C07C41/34Separation; Purification; Stabilisation; Use of additives
    • C07C41/40Separation; Purification; Stabilisation; Use of additives by change of physical state, e.g. by crystallisation
    • C07C41/42Separation; Purification; Stabilisation; Use of additives by change of physical state, e.g. by crystallisation by distillation

Abstract

The invention discloses a kind of synthetic methods of high-purity methyl tertbutyl ether, are related to chemical raw material synthesis field;It is raw material, the obtained thick methyl tertiary butyl ether(MTBE) of catalyst reaction by isobutene and methanol, thick methyl tertiary butyl ether(MTBE) sum aggregate sulphur agent is uniformly mixed, baking is stirred in vacuum drying oven, mixed liquor after baking is sent into destilling tower, the sulfur-containing mixture of collection is flowed out from bottom of tower, and methyl tertiary butyl ether(MTBE) after purification is flowed out from tower top;Sulfur impurity is absorbed with collection sulphur agent; it is simple for process controllable; good impurity removing effect, in collecting sulphur agent ingredient, part ferrous oxalate can be by potassium permanganate oxidation at ferric oxalate; carbon nanotube is sintered through special atmosphere oven, after reaction kettle processing; surface will produce rough shape, and subregion can form crackle, increase the adsorption activity and adsorption surface area of carbon nanotube; silver chlorate and cobalt nitrate, silica gel are used cooperatively, and desulfurization can be made more thorough.

Description

A kind of synthetic method of high-purity methyl tertbutyl ether
Technical field:
The present invention relates to chemical raw material synthesis fields, and in particular to a kind of synthetic method of high-purity methyl tertbutyl ether.
Background technology:
Methyl tertiary butyl ether(MTBE) (MTBE) is a kind of high-octane rating (research octane number (RON) 115) gasoline additive, and chemistry is oxygen-containing Amount is much lower compared with methanol, is conducive to warming up and saves fuel, evaporation latent heat is low, advantageous to cold start-up, is usually used in unleaded gas and low The blending of lead oil.Methyl tertiary butyl ether(MTBE) can also be cracked into isobutene again, as rubber and the raw material of other chemical products.Matter Best methyl tertiary butyl ether(MTBE) is measured, medicine is may be used as, is medicine intermediate.
Octane enhancing additives of the MTBE as gasoline may additionally facilitate cleaning burning, reduce in addition to it can increase gasoline oxygen content Automobile hazardous emission pollutes.MTBE has certain solubility in water, therefore, mainly due to letting out for underground and aboveground gasoline basin Leakage, the U.S. is found that MTBE more and more in underground drinking water body.Even if MTBE will also result in water quality in very low concentrations and dislike It is smelly.MTBE is classified as the possible carcinogen of the mankind by U.S.EPA.
The methyl tertiary butyl ether(MTBE) impurity content produced at present is more, needs by multiple tracks removal of impurities process so that production cost Height, low production efficiency, especially sulfide content are more, seriously affect the use of methyl tertiary butyl ether(MTBE).
Invention content:
Technical problem to be solved by the present invention lies in a kind of synthetic method of high-purity methyl tertbutyl ether is provided, prepare Methyl tertiary butyl ether(MTBE) impurity content it is few, purity is high, simple production process, controllable.
The technical problems to be solved by the invention are realized using technical solution below:
A kind of synthetic method of high-purity methyl tertbutyl ether, includes the following steps:
(1) thick methyl tertiary butyl ether(MTBE) sum aggregate sulphur agent is uniformly mixed, the stirring baking 1-2h in 50-60 DEG C of vacuum drying oven;
(2) mixed liquor after toasting step (1) is sent into destilling tower, and control column bottom temperature is 85-125 DEG C, tower top temperature Degree is 130-150 DEG C, and the sulfur-containing mixture of collection is flowed out from bottom of tower, and methyl tertiary butyl ether(MTBE) after purification is flowed out from tower top;
The collection sulphur agent is made of the raw material of following parts by weight:30-50 parts of ferrous oxalate, 26-42 parts of cobalt nitrate, potassium chloride 23-25 parts, 12-14 parts of silver chlorate, 6-8 parts of copper sulphate, 10-12 parts of silica gel, 20-30 parts of potassium permanganate, 50-70 parts of hexamethylene, 30-40 parts of acetophenone, 3-5 parts of carbon nanotube, 35-55 parts of ethyl alcohol.
Preferably, the preparation method of the collection sulphur agent is:
(1) ferrous oxalate, cobalt nitrate, potassium chloride, silver chlorate, copper sulphate are dissolved in deionized water, magnetic agitation 30min;
(2) silica gel and potassium permanganate are added in the mixed solution of step (1) preparation, react 1-2h at 45-55 DEG C;
(3) carbon nanotube is put into hydrogen atmosphere stove and is sintered 2-3h at 300-400 DEG C, natural cooling is added to 2- In the hydrochloric acid solution of 4% mass concentration, the processing 10h at 120-150 DEG C is put into reaction kettle;
(4) hexamethylene, acetophenone and ethyl alcohol are uniformly mixed, sequentially add step (2), (3) prepare mixed solution and Carbon nanotube stirs evenly, and the collection sulphur agent is made.
Preferably, the preparation method of the thick methyl tertiary butyl ether(MTBE) includes the following steps:
(1) isobutene decompression is cooled to liquid, is mixed with methanol, then mixed liquor is sent into expanded bed and reacts 2-3h;
(2) catalyst is added in the expanded bed after being reacted to step (1) and carries out catalysis reaction;
(3) product after reacting step (2) is sent into distillation column distillation, controls destilling tower temperature, is received at the top of destilling tower Collect unreacted methanol, destilling tower bottom collection catalyst, methyl tertiary butyl ether(MTBE) is collected in destilling tower side.
Preferably, the preparation method of catalyst includes the following steps in the step (2):
(1) mix 50-80 parts of styrene, 50-80 parts of divinylbenzenes, 60-100 parts of ethyl alcohol and 40-60 parts of deionized waters, It is heated to 45-55 DEG C and stirs 20min, it is very fast to be cooled to 15-20 DEG C;
(2) 25-35 parts of sodium ethoxides, 20-30 parts of benzoyls and 35-50 parts of acetone, mixing are added into step (1) mixture Uniformly, it is warming up to 80-85 DEG C of reaction 6-8h, polystyrene is made in washing, dry, filtering;
(3) 10-15 parts of catalysis sulfonating agents are added in the polystyrene prepared to step (2) and react 3-5h, polyphenyl second is made Alkene ion exchange resin;
(4) polystyrene ion-exchange resin prepared by step (3) is added in the salpeter solution of 20% concentration and is stirred 20min, then 5-10 parts of hydrofluoric acid, 3-5 parts of potassium chloride, 5-8 parts of ammonium acetates are added into mixed liquor and are uniformly mixed, it is put into reaction kettle In 5-7h is reacted at 120-130 DEG C, it is cooling, wash, it is dry, the catalyst is made.
Preferably, the catalysis sulfonating agent is made of the raw material of following parts by weight:20-30 parts of deionized waters, 12-15 parts of Asias Sodium sulphate, 30-40 part ethyl alcohol, 18-20 parts of bromines, 13-15 parts of sulfuric acid, 16-20 parts of n-hexanes, 30-50 parts of dimethylformamides;Its Preparation method is:
(1) deionized water and bromine are uniformly mixed, are put at -2 DEG C~-3 DEG C and freeze 2-3h;
(2) step (1) ice cube is thawed rapidly and is warming up to 55-60 DEG C, n-hexane and dimethyl formyl are added while stirring Amine, after mixing, it is 6-8% to be warming up to 120-130 DEG C of heat preservation to mixture water content, cooling;
(3) sodium sulfite, ethyl alcohol, sulfuric acid are uniformly mixed, step (2) system is added drop-wise to dropwise using No. 10 needle applicators It in standby mixture, is stirred when being added dropwise, rate of addition is 120 drops/minute, and 20min is stirred after being added dropwise, and is made described and urges Change sulfonating agent.
The beneficial effects of the invention are as follows:The present invention provides a kind of synthetic methods of high-purity methyl tertbutyl ether, use In destilling tower distillation process, sulfur impurity is absorbed with collection sulphur agent, simple for process controllable, good impurity removing effect, in collection sulphur agent In ingredient, part ferrous oxalate can be by potassium permanganate oxidation at ferric oxalate, and carbon nanotube is sintered through special atmosphere oven, at reaction kettle After reason, surface will produce rough shape, and subregion can form crackle, increase adsorption activity and the suction of carbon nanotube Surface area, silver chlorate and cobalt nitrate, silica gel are used cooperatively, and can make the desulfurization more thorough.
Isobutene and the catalyst of methanol reaction select styrene in divinylbenzene, ethyl alcohol, deionized water, sodium ethoxide, benzene Polystyrene is made in the mixed solution of formyl and acetone, polystyrene and catalysis sulfonating agent reaction are made polystyrene ion and hand over Resin is changed, polystyrene ion-exchange resin is added in nitric acid, hydrofluoric acid, potassium chloride, ammonium acetate solution and is modified, is made Isobutene and methanol can be reacted more thorough, product by the catalyst of isobutene and methanol reaction, the method for preparing catalyst Impurity content is few, and purity is high, and polystyrene ion-exchange resin prepared by used catalysis sulfonating agent is catalyzed work after modified Property increase so that final product methyl tertiary butyl ether(MTBE) purity is high, and by-product is few.
Specific implementation mode:
In order to make the technical means, the creative features, the aims and the efficiencies achieved by the present invention be easy to understand, tie below Specific embodiment is closed, the present invention is further explained.
Embodiment 1:
A kind of synthetic method of high-purity methyl tertbutyl ether, includes the following steps:
(1) thick methyl tertiary butyl ether(MTBE) sum aggregate sulphur agent is uniformly mixed, the stirring baking 1h in 50 DEG C of vacuum drying ovens;
(2) mixed liquor after toasting step (1) is sent into destilling tower, and control column bottom temperature is 125 DEG C, and tower top temperature is 140 DEG C, the sulfur-containing mixture of collection is flowed out from bottom of tower, and methyl tertiary butyl ether(MTBE) after purification is flowed out from tower top;
The collection sulphur agent is made of the raw material of following parts by weight:50 parts of ferrous oxalate, 26 parts of cobalt nitrate, 25 parts of potassium chloride, 13 parts of silver chlorate, 8 parts of copper sulphate, 11 parts of silica gel, 30 parts of potassium permanganate, 50 parts of hexamethylene, 40 parts of acetophenone, 4 parts of carbon nanotube, 55 parts of ethyl alcohol.
It is described collection sulphur agent preparation method be:
(1) ferrous oxalate, cobalt nitrate, potassium chloride, silver chlorate, copper sulphate are dissolved in deionized water, magnetic agitation 30min;
(2) silica gel and potassium permanganate are added in the mixed solution of step (1) preparation, react 1h at 45 DEG C;
(3) carbon nanotube is put into hydrogen atmosphere stove and is sintered 3h at 300 DEG C, it is dense to be added to 2% mass for natural cooling In the hydrochloric acid solution of degree, the processing 10h at 135 DEG C is put into reaction kettle;
(4) hexamethylene, acetophenone and ethyl alcohol are uniformly mixed, sequentially add step (2), (3) prepare mixed solution and Carbon nanotube stirs evenly, and the collection sulphur agent is made.
The preparation method of the thick methyl tertiary butyl ether(MTBE) includes the following steps:
(1) isobutene decompression is cooled to liquid, is mixed with methanol, then mixed liquor is sent into expanded bed and reacts 2h;
(2) catalyst is added in the expanded bed after being reacted to step (1) and carries out catalysis reaction;
(3) product after reacting step (2) is sent into distillation column distillation, controls destilling tower temperature, is received at the top of destilling tower Collect unreacted methanol, destilling tower bottom collection catalyst, methyl tertiary butyl ether(MTBE) is collected in destilling tower side.
The preparation method of catalyst includes the following steps in the step (2):
(1) 75 parts of styrene, 75 parts of divinylbenzenes, 100 parts of ethyl alcohol and 50 parts of deionized waters mixed, be heated to 50 DEG C and stir 20min is mixed, it is very fast to be cooled to 15 DEG C;
(2) 35 parts of sodium ethoxides, 20 parts of benzoyls and 40 parts of acetone are added into step (1) mixture, are uniformly mixed, heating To 80 DEG C of reaction 8h, polystyrene is made in washing, dry, filtering;
(3) 10 parts of catalysis sulfonating agents are added in the polystyrene prepared to step (2) and react 5h, polystyrene ion is made Exchanger resin;
(4) polystyrene ion-exchange resin prepared by step (3) is added in the salpeter solution of 20% concentration and is stirred 20min, then 5 parts of hydrofluoric acid, 5 parts of potassium chloride, 6 parts of ammonium acetates are added into mixed liquor and are uniformly mixed, it is put into reaction kettle 125 5h is reacted at DEG C, it is cooling, it washs, it is dry, the catalyst is made.
The catalysis sulfonating agent is made of the raw material of following parts by weight:25 parts of deionized waters, 13 parts of sodium sulfites, 35 parts of second Alcohol, 19 parts of bromines, 14 parts of sulfuric acid, 18 parts of n-hexanes, 40 parts of dimethylformamides;Preparation method is:
(1) deionized water and bromine are uniformly mixed, are put at -2 DEG C and freeze 3h;
(2) step (1) ice cube is thawed rapidly and is warming up to 55 DEG C, n-hexane and dimethylformamide are added while stirring, After mixing, it is 6% to be warming up to 125 DEG C of heat preservations to mixture water content, cooling;
(3) sodium sulfite, ethyl alcohol, sulfuric acid are uniformly mixed, step (2) system is added drop-wise to dropwise using No. 10 needle applicators It in standby mixture, is stirred when being added dropwise, rate of addition is 120 drops/minute, and 20min is stirred after being added dropwise, and is made described and urges Change sulfonating agent.
Embodiment 2:
A kind of synthetic method of high-purity methyl tertbutyl ether, includes the following steps:
(1) thick methyl tertiary butyl ether(MTBE) sum aggregate sulphur agent is uniformly mixed, the stirring baking 2h in 55 DEG C of vacuum drying ovens;
(2) mixed liquor after toasting step (1) is sent into destilling tower, and control column bottom temperature is 85 DEG C, and tower top temperature is 130 DEG C, the sulfur-containing mixture of collection is flowed out from bottom of tower, and methyl tertiary butyl ether(MTBE) after purification is flowed out from tower top;
The collection sulphur agent is made of the raw material of following parts by weight:40 parts of ferrous oxalate, 42 parts of cobalt nitrate, 24 parts of potassium chloride, 12 parts of silver chlorate, 7 parts of copper sulphate, 10 parts of silica gel, 20 parts of potassium permanganate, 60 parts of hexamethylene, 35 parts of acetophenone, 3 parts of carbon nanotube, 45 parts of ethyl alcohol.
It is described collection sulphur agent preparation method be:
(1) ferrous oxalate, cobalt nitrate, potassium chloride, silver chlorate, copper sulphate are dissolved in deionized water, magnetic agitation 30min;
(2) silica gel and potassium permanganate are added in the mixed solution of step (1) preparation, react 2h at 55 DEG C;
(3) carbon nanotube is put into hydrogen atmosphere stove and is sintered 2h at 400 DEG C, it is dense to be added to 3% mass for natural cooling In the hydrochloric acid solution of degree, the processing 10h at 150 DEG C is put into reaction kettle;
(4) hexamethylene, acetophenone and ethyl alcohol are uniformly mixed, sequentially add step (2), (3) prepare mixed solution and Carbon nanotube stirs evenly, and the collection sulphur agent is made.
The preparation method of the thick methyl tertiary butyl ether(MTBE) includes the following steps:
(1) isobutene decompression is cooled to liquid, is mixed with methanol, then mixed liquor is sent into expanded bed and reacts 2h;
(2) catalyst is added in the expanded bed after being reacted to step (1) and carries out catalysis reaction;
(3) product after reacting step (2) is sent into distillation column distillation, controls destilling tower temperature, is received at the top of destilling tower Collect unreacted methanol, destilling tower bottom collection catalyst, methyl tertiary butyl ether(MTBE) is collected in destilling tower side.
The preparation method of catalyst includes the following steps in the step (2):
(1) 80 parts of styrene, 80 parts of divinylbenzenes, 80 parts of ethyl alcohol and 40 parts of deionized waters mixed, be heated to 55 DEG C and stir 20min is mixed, it is very fast to be cooled to 20 DEG C;
(2) 30 parts of sodium ethoxides, 25 parts of benzoyls and 50 parts of acetone are added into step (1) mixture, are uniformly mixed, heating To 85 DEG C of reaction 7h, polystyrene is made in washing, dry, filtering;
(3) 10 parts of catalysis sulfonating agents are added in the polystyrene prepared to step (2) and react 4h, polystyrene ion is made Exchanger resin;
(4) polystyrene ion-exchange resin prepared by step (3) is added in the salpeter solution of 20% concentration and is stirred 20min, then 8 parts of hydrofluoric acid, 3 parts of potassium chloride, 5 parts of ammonium acetates are added into mixed liquor and are uniformly mixed, it is put into reaction kettle 130 6h is reacted at DEG C, it is cooling, it washs, it is dry, the catalyst is made.
The catalysis sulfonating agent is made of the raw material of following parts by weight:30 parts of deionized waters, 15 parts of sodium sulfites, 40 parts of second Alcohol, 20 parts of bromines, 15 parts of sulfuric acid, 20 parts of n-hexanes, 50 parts of dimethylformamides;Preparation method is:
(1) deionized water and bromine are uniformly mixed, are put at -3 DEG C and freeze 2h;
(2) step (1) ice cube is thawed rapidly and is warming up to 60 DEG C, n-hexane and dimethylformamide are added while stirring, After mixing, it is 7% to be warming up to 120 DEG C of heat preservations to mixture water content, cooling;
(3) sodium sulfite, ethyl alcohol, sulfuric acid are uniformly mixed, step (2) system is added drop-wise to dropwise using No. 10 needle applicators It in standby mixture, is stirred when being added dropwise, rate of addition is 120 drops/minute, and 20min is stirred after being added dropwise, and is made described and urges Change sulfonating agent.
Embodiment 3:
A kind of synthetic method of high-purity methyl tertbutyl ether, includes the following steps:
(1) thick methyl tertiary butyl ether(MTBE) sum aggregate sulphur agent is uniformly mixed, the stirring baking 1h in 60 DEG C of vacuum drying ovens;
(2) mixed liquor after toasting step (1) is sent into destilling tower, and control column bottom temperature is 105 DEG C, and tower top temperature is 150 DEG C, the sulfur-containing mixture of collection is flowed out from bottom of tower, and methyl tertiary butyl ether(MTBE) after purification is flowed out from tower top;
The collection sulphur agent is made of the raw material of following parts by weight:30 parts of ferrous oxalate, 34 parts of cobalt nitrate, 23 parts of potassium chloride, 14 parts of silver chlorate, 6 parts of copper sulphate, 12 parts of silica gel, 25 parts of potassium permanganate, 70 parts of hexamethylene, 30 parts of acetophenone, 5 parts of carbon nanotube, 35 parts of ethyl alcohol.
It is described collection sulphur agent preparation method be:
(1) ferrous oxalate, cobalt nitrate, potassium chloride, silver chlorate, copper sulphate are dissolved in deionized water, magnetic agitation 30min;
(2) silica gel and potassium permanganate are added in the mixed solution of step (1) preparation, react 1h at 50 DEG C;
(3) carbon nanotube is put into hydrogen atmosphere stove and is sintered 2h at 350 DEG C, it is dense to be added to 4% mass for natural cooling In the hydrochloric acid solution of degree, the processing 10h at 120 DEG C is put into reaction kettle;
(4) hexamethylene, acetophenone and ethyl alcohol are uniformly mixed, sequentially add step (2), (3) prepare mixed solution and Carbon nanotube stirs evenly, and the collection sulphur agent is made.
The preparation method of the thick methyl tertiary butyl ether(MTBE) includes the following steps:
(1) isobutene decompression is cooled to liquid, is mixed with methanol, then mixed liquor is sent into expanded bed and reacts 3h;
(2) catalyst is added in the expanded bed after being reacted to step (1) and carries out catalysis reaction;
(3) product after reacting step (2) is sent into distillation column distillation, controls destilling tower temperature, is received at the top of destilling tower Collect unreacted methanol, destilling tower bottom collection catalyst, methyl tertiary butyl ether(MTBE) is collected in destilling tower side.
The preparation method of catalyst includes the following steps in the step (2):
(1) 50 parts of styrene, 50 parts of divinylbenzenes, 60 parts of ethyl alcohol and 60 parts of deionized waters mixed, be heated to 45 DEG C and stir 20min is mixed, it is very fast to be cooled to 18 DEG C;
(2) 25 parts of sodium ethoxides, 30 parts of benzoyls and 35 parts of acetone are added into step (1) mixture, are uniformly mixed, heating To 80 DEG C of reaction 6h, polystyrene is made in washing, dry, filtering;
(3) 12 parts of catalysis sulfonating agents are added in the polystyrene prepared to step (2) and react 3h, polystyrene ion is made Exchanger resin;
(4) polystyrene ion-exchange resin prepared by step (3) is added in the salpeter solution of 20% concentration and is stirred 20min, then 10 parts of hydrofluoric acid, 4 parts of potassium chloride, 8 parts of ammonium acetates are added into mixed liquor and are uniformly mixed, it is put into reaction kettle 7h is reacted at 120 DEG C, it is cooling, it washs, it is dry, the catalyst is made.
The catalysis sulfonating agent is made of the raw material of following parts by weight:20 parts of deionized waters, 12 parts of sodium sulfites, 30 parts of second Alcohol, 18 parts of bromines, 13 parts of sulfuric acid, 16 parts of n-hexanes, 30 parts of dimethylformamides;Preparation method is:
(1) deionized water and bromine are uniformly mixed, are put at -2 DEG C and freeze 2h;
(2) step (1) ice cube is thawed rapidly and is warming up to 55 DEG C, n-hexane and dimethylformamide are added while stirring, After mixing, it is 8% to be warming up to 130 DEG C of heat preservations to mixture water content, cooling;
(3) sodium sulfite, ethyl alcohol, sulfuric acid are uniformly mixed, step (2) system is added drop-wise to dropwise using No. 10 needle applicators It in standby mixture, is stirred when being added dropwise, rate of addition is 120 drops/minute, and 20min is stirred after being added dropwise, and is made described and urges Change sulfonating agent.
Comparative example:
The 3kg tert-butyl alcohols are weighed, 3g p-methyl benzenesulfonic acid (TsOH), 3kgCaO is added in the reaction vessel of 5L, is warming up to 100 DEG C start that 1.5kg methanol is added dropwise, time for adding keep the temperature 4 hours open steams and distills, obtains at 100-105 DEG C after 2 hours 3.35kg crude products, stratification, upper layer ether further obtain 3.2kg methyl tertiary butyl ether(MTBE)s by rectification and purification.
Composition detection is carried out to methyl tertiary butyl ether(MTBE) prepared by the above various embodiments and comparative example, it is as a result as follows:
By above table it is found that the impurity content that contains of methyl tertiary butyl ether(MTBE) prepared by the present invention is few, purity is high, yield It is high.
The above shows and describes the basic principles and main features of the present invention and the advantages of the present invention.The technology of the industry Personnel are it should be appreciated that the present invention is not limited to the above embodiments, and the above embodiments and description only describe this The principle of invention, without departing from the spirit and scope of the present invention, various changes and improvements may be made to the invention, these changes Change and improvement all fall within the protetion scope of the claimed invention.The claimed scope of the invention by appended claims and its Equivalent thereof.

Claims (5)

1. a kind of synthetic method of high-purity methyl tertbutyl ether, which is characterized in that include the following steps:
(1) thick methyl tertiary butyl ether(MTBE) sum aggregate sulphur agent is uniformly mixed, the stirring baking 1-2h in 50-60 DEG C of vacuum drying oven;
(2) mixed liquor after toasting step (1) is sent into destilling tower, and control column bottom temperature is 85-125 DEG C, and tower top temperature is 130-150 DEG C, the sulfur-containing mixture of collection is flowed out from bottom of tower, and methyl tertiary butyl ether(MTBE) after purification is flowed out from tower top;
The collection sulphur agent is made of the raw material of following parts by weight:30-50 parts of ferrous oxalate, 26-42 parts of cobalt nitrate, potassium chloride 23- 25 parts, 12-14 parts of silver chlorate, 6-8 parts of copper sulphate, 10-12 parts of silica gel, 20-30 parts of potassium permanganate, 50-70 parts of hexamethylene, benzene second 30-40 parts of ketone, 3-5 parts of carbon nanotube, 35-55 parts of ethyl alcohol.
2. the synthetic method of high-purity methyl tertbutyl ether according to claim 1, which is characterized in that the collection sulphur agent Preparation method is:
(1) ferrous oxalate, cobalt nitrate, potassium chloride, silver chlorate, copper sulphate are dissolved in deionized water, magnetic agitation 30min;
(2) silica gel and potassium permanganate are added in the mixed solution of step (1) preparation, react 1-2h at 45-55 DEG C;
(3) carbon nanotube is put into hydrogen atmosphere stove and is sintered 2-3h at 300-400 DEG C, natural cooling is added to 2-4% matter In the hydrochloric acid solution for measuring concentration, the processing 10h at 120-150 DEG C is put into reaction kettle;
(4) hexamethylene, acetophenone and ethyl alcohol are uniformly mixed, sequentially add step (2), mixed solution prepared by (3) and carbon and receives Mitron stirs evenly, and the collection sulphur agent is made.
3. the synthetic method of high-purity methyl tertbutyl ether according to claim 1, which is characterized in that the thick methyl- tert The preparation method of butyl ether includes the following steps:
(1) isobutene decompression is cooled to liquid, is mixed with methanol, then mixed liquor is sent into expanded bed and reacts 2-3h;
(2) catalyst is added in the expanded bed after being reacted to step (1) and carries out catalysis reaction;
(3) by step (2) react after product be sent into distillation column distillation, control destilling tower temperature, destilling tower collected overhead not Methyl tertiary butyl ether(MTBE) is collected in the methanol of reaction, destilling tower bottom collection catalyst, destilling tower side.
4. the synthetic method of high-purity methyl tertbutyl ether according to claim 3, which is characterized in that the step (2) The preparation method of middle catalyst includes the following steps:
(1) 50-80 parts of styrene, 50-80 parts of divinylbenzenes, 60-100 parts of ethyl alcohol and 40-60 parts of deionized waters are mixed, heating 20min is stirred to 45-55 DEG C, it is very fast to be cooled to 15-20 DEG C;
(2) 25-35 parts of sodium ethoxides, 20-30 parts of benzoyls and 35-50 parts of acetone are added into step (1) mixture, mixing is equal It is even, it is warming up to 80-85 DEG C of reaction 6-8h, polystyrene is made in washing, dry, filtering;
(3) 10-15 part catalysis sulfonating agents are added in the polystyrene prepared to step (2) and react 3-5h, obtained polystyrene from Sub-exchange resin;
(4) polystyrene ion-exchange resin prepared by step (3) is added in the salpeter solution of 20% concentration and stirs 20min, 5-10 parts of hydrofluoric acid, 3-5 parts of potassium chloride, 5-8 parts of ammonium acetates are added into mixed liquor again to be uniformly mixed, are put into reaction kettle 5-7h is reacted at 120-130 DEG C, it is cooling, it washs, it is dry, the catalyst is made.
5. the synthetic method of high-purity methyl tertbutyl ether according to claim 4, which is characterized in that the catalysis sulfonation Agent is made of the raw material of following parts by weight:20-30 parts of deionized waters, 12-15 parts of sodium sulfites, 30-40 parts of ethyl alcohol, 18-20 parts Bromine, 13-15 part sulfuric acid, 16-20 parts of n-hexanes, 30-50 parts of dimethylformamides;Preparation method is:
(1) deionized water and bromine are uniformly mixed, are put at -2 DEG C~-3 DEG C and freeze 2-3h;
(2) step (1) ice cube is thawed rapidly and is warming up to 55-60 DEG C, n-hexane and dimethylformamide are added while stirring, mixed After closing uniformly, it is 6-8% to be warming up to 120-130 DEG C of heat preservation to mixture water content, cooling;
(3) sodium sulfite, ethyl alcohol, sulfuric acid are uniformly mixed, step (2) preparation is added drop-wise to dropwise using No. 10 needle applicators It in mixture, is stirred when being added dropwise, rate of addition is 120 drops/minute, and 20min is stirred after being added dropwise, and the catalysis sulphur is made Agent.
CN201810378751.5A 2018-04-25 2018-04-25 A kind of synthetic method of high-purity methyl tertbutyl ether Pending CN108440255A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810378751.5A CN108440255A (en) 2018-04-25 2018-04-25 A kind of synthetic method of high-purity methyl tertbutyl ether

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810378751.5A CN108440255A (en) 2018-04-25 2018-04-25 A kind of synthetic method of high-purity methyl tertbutyl ether

Publications (1)

Publication Number Publication Date
CN108440255A true CN108440255A (en) 2018-08-24

Family

ID=63200904

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810378751.5A Pending CN108440255A (en) 2018-04-25 2018-04-25 A kind of synthetic method of high-purity methyl tertbutyl ether

Country Status (1)

Country Link
CN (1) CN108440255A (en)

Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1724614A (en) * 2005-06-21 2006-01-25 大连理工大学 Deep oxidation desulfurization catalyst
CN102898286A (en) * 2012-08-21 2013-01-30 九江齐鑫化工有限公司 Method for removing sulfides in MTBE by adsorptive distillation
CN103145534A (en) * 2013-03-26 2013-06-12 南开大学 Method for deeply removing sulfides in gasoline additive, namely methyl tert-butyl ether
CN103333056A (en) * 2013-07-17 2013-10-02 凯瑞化工股份有限公司 Method and device for deeply removing sulfide in MTBE
CN103360221A (en) * 2013-07-17 2013-10-23 凯瑞化工股份有限公司 Method for deeply removing sulfides in MTBE
CN104014377A (en) * 2014-06-12 2014-09-03 大连理工大学 Preparation method of metal-free catalyst for room-temperature efficient catalytic oxidation desulfurization
CN104370708A (en) * 2013-08-14 2015-02-25 北京安耐吉能源工程技术有限公司 Methyl tert-butyl ether crude product purification method and methyl tert-butyl ether production method
CN104370707A (en) * 2013-08-14 2015-02-25 北京安耐吉能源工程技术有限公司 Methyl tert-butyl ether crude product purification method and methyl tert-butyl ether production method
CN104525136A (en) * 2014-10-27 2015-04-22 湖北工程学院 Composite material, and preparation method and application thereof
CN105218724A (en) * 2015-09-21 2016-01-06 安徽皖东化工有限公司 A kind of preparation method of strong-acid cation-exchange resin
CN105572248A (en) * 2015-12-15 2016-05-11 中国石油天然气股份有限公司 Method for determining sulfides in gasoline additive, i.e., methyl tert-butyl ether
CN106542974A (en) * 2015-09-17 2017-03-29 中国石油天然气股份有限公司 A kind of method of sulfide in enrichment methyl tertiary-butyl ether

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1724614A (en) * 2005-06-21 2006-01-25 大连理工大学 Deep oxidation desulfurization catalyst
CN102898286A (en) * 2012-08-21 2013-01-30 九江齐鑫化工有限公司 Method for removing sulfides in MTBE by adsorptive distillation
CN103145534A (en) * 2013-03-26 2013-06-12 南开大学 Method for deeply removing sulfides in gasoline additive, namely methyl tert-butyl ether
CN103333056A (en) * 2013-07-17 2013-10-02 凯瑞化工股份有限公司 Method and device for deeply removing sulfide in MTBE
CN103360221A (en) * 2013-07-17 2013-10-23 凯瑞化工股份有限公司 Method for deeply removing sulfides in MTBE
CN104370708A (en) * 2013-08-14 2015-02-25 北京安耐吉能源工程技术有限公司 Methyl tert-butyl ether crude product purification method and methyl tert-butyl ether production method
CN104370707A (en) * 2013-08-14 2015-02-25 北京安耐吉能源工程技术有限公司 Methyl tert-butyl ether crude product purification method and methyl tert-butyl ether production method
CN104014377A (en) * 2014-06-12 2014-09-03 大连理工大学 Preparation method of metal-free catalyst for room-temperature efficient catalytic oxidation desulfurization
CN104525136A (en) * 2014-10-27 2015-04-22 湖北工程学院 Composite material, and preparation method and application thereof
CN106542974A (en) * 2015-09-17 2017-03-29 中国石油天然气股份有限公司 A kind of method of sulfide in enrichment methyl tertiary-butyl ether
CN105218724A (en) * 2015-09-21 2016-01-06 安徽皖东化工有限公司 A kind of preparation method of strong-acid cation-exchange resin
CN105572248A (en) * 2015-12-15 2016-05-11 中国石油天然气股份有限公司 Method for determining sulfides in gasoline additive, i.e., methyl tert-butyl ether

Non-Patent Citations (11)

* Cited by examiner, † Cited by third party
Title
《化工百科全书》编辑委员会: "《化工百科全书 第8卷 计算机控制***-聚硅氧烷 ji-ju》", 30 September 1994 *
何铁林: "《水处理化学品手册》", 31 May 2000 *
卢衍楠: "MTBE选择性吸附脱硫的研究", 《石油与天然气化工》 *
卢衍楠: "吸附法降低甲基叔丁基醚中有机硫化物含量的研究", 《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》 *
岳昌海: "MTBE脱硫技术研究进展", 《天然气化工(C1化学与化工)》 *
张巧玲: "《化工工艺学》", 31 July 2015 *
李顺德: "凹凸棒脱硫剂脱除MTBE和汽油馏分中硫化物的研究", 《中国优秀硕士学位论文全文数据库 工程科技Ⅰ辑》 *
田铁牛: "《磺化工艺作业》", 31 March 2013 *
谭世荣: "甲(乙)基叔丁基醚的合成", 《合成橡胶工业》 *
谭世荣: "甲(乙)基叔丁醚的合成研究", 《湖南化工》 *
陈一萍: "碳纳米管对水中硫化物吸附性能的研究", 《皮革与化工》 *

Similar Documents

Publication Publication Date Title
CN100509726C (en) Preparation method of dichloro propanol from glycerin
CN101213168A (en) Method of making fluorinated vinyl ethers
CN106631684A (en) Method for preparing SBA(sec-butyl alcohol) through hydrolysis with sec-butyl acetate
CN106748763B (en) The method of two kettles joint phase-transfer Wittig reaction methyl benzoate
CN114805288B (en) Method for preparing 2, 4-butane sultone
CN108440255A (en) A kind of synthetic method of high-purity methyl tertbutyl ether
CN101704723A (en) Preparation method of hydroxymethyl substitutent o-alkyl biphenyl and intermediate thereof
CN108772070A (en) The preparation method of iron-based composite catalyst for the online upgrading of bio oil
CN106518620B (en) A kind of method and device preparing sec-butyl alcohol
CN111116327B (en) Synthesis process of ethylene glycol mono-tert-butyl ether
CN105777540A (en) Energy-saving efficient isopropenyl acetate synthesis method
CN114470826B (en) Purification device and method of bis (trifluoromethanesulfonyl) imide
CN101074187A (en) Production of o-phenylphenol
CN111072464A (en) Method for directly introducing aldehyde group on aromatic ring
CN109678647A (en) A kind of preparation method of high-purity 1- chlorine normal butane
CN102814193B (en) Copper-composite molecular sieve catalyst used for synthesis of diethyl carbonate through gas-phase oxidative carbonylation and its preparation method
CN108558612A (en) A kind of preparation method of methyl tertiary butyl ether(MTBE)
CN109776281A (en) A kind of synthetic method of ethyl isobutyl perfume (or spice) phenol
CN108586193A (en) A method of preparing 1,3-PD using 3- methoxy methyl propionates
CN104250204B (en) A kind of complex etherified technique
CN108774155A (en) A kind of preparation method of the fluoro- 4- cyanophenols of 3-
CN1190398C (en) Process for preparing bromo-n-dodecane
CN217450108U (en) Methyl chloride production system
CN109942420A (en) A kind of method of reaction rectification method preparation high-purity propionic ester
CN110668920A (en) Method for preparing ethanol and co-producing cyclohexanol by using reactive distillation method

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
WD01 Invention patent application deemed withdrawn after publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20180824