CN1231278A - Process for preparing anthraquinone - Google Patents
Process for preparing anthraquinone Download PDFInfo
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- CN1231278A CN1231278A CN 99103274 CN99103274A CN1231278A CN 1231278 A CN1231278 A CN 1231278A CN 99103274 CN99103274 CN 99103274 CN 99103274 A CN99103274 A CN 99103274A CN 1231278 A CN1231278 A CN 1231278A
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C46/00—Preparation of quinones
- C07C46/02—Preparation of quinones by oxidation giving rise to quinoid structures
- C07C46/04—Preparation of quinones by oxidation giving rise to quinoid structures of unsubstituted ring carbon atoms in six-membered aromatic rings
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- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
The preparation method of anthraquinone is characterized by that in the mixed solvent of aromatic halohydrocarbon and organic acid, in the condition of a certain pressure and temp. and under the catalysis of metal salt and bromide, the oxygen-contained gas is used to oxidize anthracene to obtain anthraquinone. Said invented preparation method uses the composite catalyst with high catalytic activity and oxidation selectivity so as to effectively raise conversion rate of anthracene, and uses low-pressure reaction in low-pressure container to obtain high output rate. Its raw materials are easily available, cost is low, reaction temp. is low, conversion rate is 100%, output rate can be up to 93.7%, and its reaction liquor can be repeatedly used after it is decoloured by active clay or treated by distillation process.
Description
The present invention relates to a kind of chemical synthesis process, particularly produce the method for anthraquinone about catalysis oxygen-containing gas oxidation anthracene in liquid phase.
Anthraquinone is broad-spectrum industrial chemicals, is important organic intermediate, can be used for the manufacturing of dyestuff, medicine, agricultural chemicals.The anthraquinone dye that with the anthraquinone is the raw material manufacturing is a big class of organic dye, its kind and next in number only to azoic dyestuff.Anthraquinone is used as the catalyzer of paper pulp and cotton fiber delignification in paper industry and textile industry.Anthraquinone and derivative thereof have restraining effect to tumour, studies show that wherein some can be used as human cancer therapy drug.
At present industrially produce anthraquinone by anthracene six kinds of methods are arranged.Vapour phase oxidation process temperature of reaction height (330-360 ℃), per pass conversion low (50-60%), tarring is serious, reacts wayward.This respect report Poland Patent PL139 591 (1988) arranged, Czechoslovakia patent CS 273 726 (1992), Japanese Patent JP 8,610 0543 (1986).The report that uses high-valency metal salt or nitric acid to carry out oxidation in liquid phase has Poland Patent PL 140 054 (1987), German patent DE 3,207 572 (1982) etc.This method is serious to equipment corrosion, produces a large amount of waste water.Utilize superoxide, resemble hydrogen peroxide, tertbutyl peroxide and ammonium persulphate oxidation anthracene and produce anthraquinone, the cost height is dangerous big.This respect report Tetrahedron Lett.1983 24 (49): 5499-5500, Synth.Commun.1989 19 (11-12): 2061-67 arranged.It is big that electrochemical oxidation process is produced anthraquinone current consumption, and the oxidation selectivity is not high.Brazilian patent BR 9,162 011 (1992) has the report of this respect.Chinese patent CN 1,030 569 (1989) has reported that ozone oxidation anthracene in liquid phase produces the method for anthraquinone.The transformation efficiency 90%-100% of anthracene, yield 82%, purity 72% counts productive rate 59%.Ozone has severe toxicity, ozone takes place want special device, expends a large amount of electric energy.The oxygen catalytic oxidation anthracene is produced anthraquinone in liquid phase, is a kind of natural resources that utilizes, and energy consumption is low, is beneficial to the method for environment protection, has development prospect.German Patent Ger offen 2,422 461 (1974), the report spent glycol is made solvent, and mantoquita is made catalyzer, and the dioxygen oxidation anthracene is produced anthraquinone.U.S. Pat 4,446 070 (1984) and Beijing University of Technology's journal 1,990 16 (3): 94-5 have reported the method for being produced anthraquinone in acetate by ceric ammonium nitrate or ammonium meta-vanadate oxygen catalytic oxidation anthracene.Because research is not mature enough, productive rate is lower than 80%, and efficient has much room for improvement.
The object of the present invention is to provide a kind of catalysis oxygen-containing gas oxidation anthracene in liquid phase and obtain the method for anthraquinone.
The preparation method of anthraquinone of the present invention is included under the normal pressure anthracene in 100-150 ℃ temperature of reaction, composite catalyst and the organic acid of forming at cobalt salt, manganese salt or nickel salt and bromide or to add organic acid inert liq organism be under the reaction conditions of solvent, react with oxygen-containing gas, when the pressure of reaction system no longer descends, can obtain anthraquinone.
The preparation method of anthraquinone of the present invention can also comprise that reaction can carry out under the pressure of 0.5-0.8MPa; When under normal pressure, reacting, can adopt Bubbling method that oxygen-containing gas is pressed in the reactor.
Wherein, cobalt salt is a Primary Catalysts in the described composite catalyst, and manganese salt or nickel salt are promotor, and bromide is an initiator.Cobalt salt can be capric acid cobalt, cobalt naphthenate, cobaltous acetate, cobaltous bromide or cobalt chloride; Manganese salt can be manganous acetate, manganous sulfate or Manganous chloride tetrahydrate; Nickel salt can be nickelous acetate, single nickel salt or nickelous chloride; Bromide can be Sodium Bromide, Potassium Bromide, cobaltous bromide or Hydrogen bromide.The consumption of composite catalyst is the 1%-l0% of anthracene quality, and the proportioning of cobalt salt and manganese salt (or nickel salt) can be 1: 0.02-1.20 (mol), preferably 1: 0.3-0.8 (mol); The proportioning of cobalt salt and bromide can be 1: 0.05-1.00 (mol).If the amount of carbazole increases in the raw material anthracene, the amount of catalyzer also will increase.
Described as solvent organic acid or add the organic boiling spread of organic acid inert liq at 110-180 ℃, and the content 8-l00% of organic acid in solvent; Described organic acid can be acetate, propionic acid, butyric acid, isopropylformic acid, valeric acid or caproic acid; Described inert liq organism can be the aromaticity halohydrocarbon, as chlorobenzene, bromobenzene, orthodichlorobenzene, ortho-chlorotolu'ene, m-chlorotoluene or parachlorotoluene.When using the mixed solvent of aromaticity halohydrocarbon and butyric acid or valeric acid, if organic acid content≤20% is very little to the corrosive nature of reactor, and this mixed solvent helps product and separates out with crystal, and it is easy to separate, and purity is up to 99.2%.
Described oxygen-containing gas can be air, oxygen-rich air or oxygen, and content 〉=25% of oxygen in the gas.
Described temperature of reaction optimum control is at 110-120 ℃.
Chemical reaction of the present invention can be represented with following formula:
The preparation method of anthraquinone of the present invention uses catalytic activity height, composite catalyst that the oxidation selectivity is good, has improved the transformation efficiency of anthracene effectively, and under low pressure reaction, the just productive rate that can obtain; Characteristics such as have raw material and be easy to get, cost is low, can carry out in low pressure vessel, and facility investment is few; Compare with catalytic gas phase oxidation, temperature of reaction is low, less energy consumption, and transformation efficiency l00%, productive rate can reach 93.7%; Particularly reaction solution is handled and can be reused through activated decoloration or distillation, and is therefore free from environmental pollution, is a kind of method of suitable suitability for industrialized production.
With indefiniteness embodiment the present invention is described below.
Embodiment 1
In the reactor that magnetic stirrer, temperature regulator and gas duct are housed, add aromaticity halohydrocarbon 250ml, butyric acid 50ml, cobaltous acetate 500mg, manganous acetate 260mg, Hydrogen bromide 50mg, anthracene 9g stirs, heats; Aerating oxygen makes the still internal pressure be controlled at 0.5-0.8MPa, and temperature is controlled at 110-120 ℃; React to pressure and only do not reduce to, cooling, filtration, oven dry obtain rib shape crystal 9.5g, fusing point 283-284 ℃, productive rate 93.7%.
Embodiment 2
Solvent in the example 1 is all used butyric acid instead, and the Hydrogen bromide in the catalyzer is used Sodium Bromide 120mg instead, pressure 1.2MPa, and other conditions are constant, productive rate 86.8%.
Embodiment 3
Butyric acid in the example 1 changes valeric acid into, and other conditions are constant, reaction yield 84.6%.
Embodiment 4
The reaction system of example 1 does not add manganous acetate, control pressure 1.2MPa, and other condition is constant, reacts 7 hours postcooling, the productive rate 32.6% of anthraquinone.
Claims (10)
1, a kind of preparation method of anthraquinone, it is characterized in that being included under the normal pressure anthracene in 100-150 ℃ temperature of reaction, composite catalyst and the organic acid of forming at cobalt salt, manganese salt or nickel salt and bromide or to add organic acid inert liq organism be under the reaction conditions of solvent, react with oxygen-containing gas, when the pressure of reaction system no longer descends, can obtain anthraquinone.
2, preparation method as claimed in claim 1 is characterized in that also comprising under the pressure that is reflected at 0.5-0.8MPa and carries out.
3, preparation method as claimed in claim 1 when it is characterized in that reacting under normal pressure, adopts Bubbling method that oxygen-containing gas is pressed in the reactor.
4, preparation method as claimed in claim 1 is characterized in that cobalt salt is capric acid cobalt, cobalt naphthenate, cobaltous acetate, cobaltous bromide or cobalt chloride; Manganese salt is manganous acetate, manganous sulfate or Manganous chloride tetrahydrate; Nickel salt is nickelous acetate, single nickel salt or nickelous chloride; Bromide is Sodium Bromide, Potassium Bromide, cobaltous bromide or Hydrogen bromide.
5, preparation method as claimed in claim 1, the consumption that it is characterized in that composite catalyst is the 1%-10% of anthracene quality, the proportioning of cobalt salt and manganese salt or nickel salt is 1: 0.02-1.20 (mol), the proportioning of cobalt salt and bromide is 1: 0.05-1.00 (mol).
6, preparation method as claimed in claim 1 is characterized in that the proportioning of cobalt salt and manganese salt (or nickel salt) is 1: 03-0.8 (mol).
7, preparation method as claimed in claim 1, it is characterized in that described as solvent organic acid or add the organic boiling spread of organic acid inert liq at 110-180 ℃, and the content 8-100% of organic acid in solvent; Described organic acid is acetate, propionic acid, butyric acid, isopropylformic acid, valeric acid or caproic acid; Described inert liq organism is the aromaticity halohydrocarbon, as chlorobenzene, bromobenzene, orthodichlorobenzene, ortho-chlorotolu'ene, m-chlorotoluene or parachlorotoluene.
8, preparation method as claimed in claim 1 is characterized in that described oxygen-containing gas is air, oxygen-rich air or oxygen, and content 〉=25% of oxygen in the gas.
9, preparation method as claimed in claim 1 is characterized in that mixed solvent is aromaticity halohydrocarbon and butyric acid or valeric acid, and organic acid content≤20%.
10, preparation method as claimed in claim 1 is characterized in that described temperature of reaction is controlled at 110-120 ℃.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99103274A CN1095458C (en) | 1999-03-30 | 1999-03-30 | Process for preparing anthraquinone |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN99103274A CN1095458C (en) | 1999-03-30 | 1999-03-30 | Process for preparing anthraquinone |
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| Publication Number | Publication Date |
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| CN1231278A true CN1231278A (en) | 1999-10-13 |
| CN1095458C CN1095458C (en) | 2002-12-04 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN99103274A Expired - Fee Related CN1095458C (en) | 1999-03-30 | 1999-03-30 | Process for preparing anthraquinone |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110590527A (en) * | 2019-08-19 | 2019-12-20 | 浙江工业大学 | Process for continuously synthesizing anthraquinone by liquid phase method and synthesis system thereof |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE2218316C3 (en) * | 1972-04-15 | 1980-10-09 | Bayer Ag, 5090 Leverkusen | Process for the production of anthraquinone |
| DE2532242A1 (en) * | 1975-07-18 | 1977-02-10 | Gerhard Seeh | Suturing needle with thread feed and release - has sliding plunger in sealed needle shaft |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110590527A (en) * | 2019-08-19 | 2019-12-20 | 浙江工业大学 | Process for continuously synthesizing anthraquinone by liquid phase method and synthesis system thereof |
| CN110590527B (en) * | 2019-08-19 | 2022-07-12 | 浙江工业大学 | Process for continuously synthesizing anthraquinone by liquid phase method and synthesis system thereof |
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| CN1095458C (en) | 2002-12-04 |
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