CN1141912A - Preparation aromatic amine compound - Google Patents
Preparation aromatic amine compound Download PDFInfo
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- CN1141912A CN1141912A CN 96107507 CN96107507A CN1141912A CN 1141912 A CN1141912 A CN 1141912A CN 96107507 CN96107507 CN 96107507 CN 96107507 A CN96107507 A CN 96107507A CN 1141912 A CN1141912 A CN 1141912A
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- aromatic amine
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- synthesis gas
- amine compound
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Abstract
The present invention discloses an aromatic amine compound and its preparation mehod. It uses aromatic nitro-compound as raw material, ammonia synthesis gas as hydrogen source. Under the action of skeletal nickel, load type nickel, palladium and platinum it makes the above-mentioned material pass through the process of catalytic cracking reaction to prepare the correspondent aromatic amine. The dosage of the catalyst is 0.5-3.0% of weight of aromatic nitro-compound, its reaction temp. is 50-150 deg.C and reaction pressure is 50-100 kg/sq.cm.
Description
The present invention relates to a kind of preparation method of aromatic amine compounds, relate in particular to a kind of preparation method who utilizes aromatic nitro compound reduction preparation aromatic amine compounds.
Aromatic amine compounds is main Organic Chemicals, is widely used in to produce dyestuff, pigment, spices, medicine etc., and traditional production method has two classes, and a class is a catalytic hydrogenating reduction, and a class is a chemical reduction method.Chemical reduction method is a reductive agent with iron powder or sodium sulphite, as document Y, ogata, and etal, J, Am, Chem, Soc, 82,2459 (1960) promptly is reduction legal system aromatic amine, though this method safety is easily gone, cost is low, it exists the serious environmental pollution problem.Document M, Freifekder, Catalytic Hydrogenation in organic synthesis (1978) has introduced the method that shortening prepares aromatic amine, though this kind method has solved environmental pollution problems, but the pure hydrogen material purity height that this method is used, preparation need electrolysis or pressure-swing absorption apparatus, high pressure storage device, so cost is higher, transportation is also inconvenient.
The purpose of this invention is to provide a kind of environmental pollution that do not produce, the preparation method of the aromatic amine compound that facility investment is few and product cost is lower.
Technical scheme of the present invention realizes in the following manner:
A kind of preparation method of aromatic amine compound, it is to be raw material with the aromatic nitro compound, with the ammonia synthesis gas is hydrogen source, under the effect of skeleton nickel, load-type nickel, palladium, platinum, carry out catalytic ammoniation prepared in reaction corresponding aroma amine, catalyst levels is the 0.5-3.0% of aromatic nitro compound weight, temperature of reaction is 50-150 ℃, and reaction pressure is the 5-100 kilograms per centimeter.
Aromatic nitro compound is meant nitrobenzene derivative, and the substituting group on the phenyl ring can have one or more alkyl, hydroxyl, alkoxyl group, amido, halogen except that nitro.
Ammonia synthesis gas is meant hydrogen richness 〉=35% of synthesis ammonia plant, is mixed with the ammonia synthesis gas or the off-gas of nitrogen, ammonia, methane, hydrogen.
Positively effect of the present invention is:
1, opens up the new way of aromatic amine compound preparation, utilized ammonia synthesis gas to replace determined hydrogen source problem of pure hydrogenolysis, reduced the production cost of aromatic amine compound.
2, eliminate the severe contamination that is caused by iron powder or sodium sulphite reduction method, protected environment.
3, increased new product to synthesis ammonia plant, ammonia synthesis gas can be fully utilized.
Be described further below in conjunction with embodiment:
Embodiment one:
At a volume is 1000 milliliters, be equipped with in the autoclave of agitator, electric heater, airway, blow-off valve, pressure and temperature indicating instrument, pack into 306.3 the gram (2.0 moles) o-Nitrophenyl methyl ethers, 4 gram skeletal nickel catalysts, reactive system is vacuumized inflated with nitrogen displacement, three times so repeatedly, then charge into ammonia synthesis gas, start agitator in 140 ℃ and 50 kilograms per centimeter
2Pressure reaction is down extremely obviously absorbing hydrogen, (seeing that from gauge outfit pointer is motionless), stopped reaction, cooling, exhaust, suction filtration is removed catalyzer, in separating funnel, divide oil-yielding stratum, the water layer of draining, underpressure distillation is collected 117-120 ℃/2.67kpa cut and is got Ortho Anisidine 230.0 grams, yield 93.8%, gas chromatographic analysis product purity are 99.21%
Embodiment two:
In with the autoclave of embodiment one, add 167.2 gram (1.0 moles) p-Nitrophenetoles, 83.8 gram p-phenetidines, 2 gram (weight in wet base) skeletal nickel catalysts vacuumize reactive system, inflated with nitrogen displacement, three times so repeatedly.Then charge into ammonia synthesis gas, start agitator, in 130 ℃, 80 kilograms per centimeter
2Pressure reacts stopped reaction when extremely no longer obviously absorbing hydrogen down, cooling, exhaust, suction filtration is removed catalyzer, in separating funnel, divide oil-yielding stratum, underpressure distillation is collected 130-132 ℃/2.67kpa cut and is got p-phenetidine 216.0 grams, deduction feeds intake, and yield is 96.3% after the p-phenetidine that adds, and the gas chromatographic analysis product purity is 99.06%.
Embodiment 3
Add 139.1 gram (1.0 moles) p-NPs at autoclave, the solution of 100 grams, 10% sodium hydroxide, 2 gram 5%pd/c catalyzer with embodiment one, reactive system is vacuumized inflated with nitrogen displacement, three times so repeatedly, then fill ammonia synthesis gas, start agitator in 85 ℃ of .15 kilograms per centimeter
2Pressure reacts stopped reaction when extremely no longer obviously absorbing chlorine down.Cooling, exhaust, suction filtration are removed catalyzer, add 3 gram S-WATs in the filtrate, transfer PH-7 with 25% sulfuric acid, are cooled to 5-10 ℃, and suction filtration is separated out crystallization, and 60 ℃ of vacuum-dryings get 104.5 gram p-aminophenol (m.p187-189 ℃).
Embodiment four
In with the autoclave of embodiment one, add 138.1 gram (1.0 moles) o-Nitranilines, 1.2 gram sodium hydroxide, 174 Ke Shui and two gram (weight in wet base) skeletal nickel catalysts vacuumize reactive system.The inflated with nitrogen displacement, three times so repeatedly, then charge into ammonia synthesis gas, start stirring, in 95 ℃ and 30 kilograms per centimeter
2Pressure reacts stopped reaction when extremely no longer obviously absorbing hydrogen down, and cooling, exhaust, suction filtration are removed catalyzer.The filtrate air distillation removes and anhydrates, and underpressure distillation is collected 115-118 ℃/0.8kpa cut and got O-Phenylene Diamine 100.0 grams then, yield 93.0%, and the gas chromatographic analysis product purity is 99.33%.
Embodiment five
In with the autoclave of embodiment one, add 157.6 gram (1.0 moles) p-Nitrophenyl chlorides.237 grams, 95% ethanol, 2 gram 5%pa/c catalyzer vacuumize reactive system, and logical nitrogen replacement three times so repeatedly, then charges into ammonia synthesis gas, in 70 ℃ and 80 kilograms per centimeter
2Pressure reaction is down lowered the temperature to no longer obviously absorbing hydrogen, exhaust, and suction filtration is removed catalyzer.Filtrate is distilled under normal pressure and is reclaimed ethanol, and 105-108 ℃/1.1kpa cut is collected in underpressure distillation then, gets p-Chlorobenzoic acid amide 120.5 grams, yield 94.4%, and the gas chromatographic analysis product purity is 99.8%.
Claims (3)
1, a kind of preparation method of aromatic amine compound, it is characterized in that with the aromatic nitro compound being raw material, with the ammonia synthesis gas is the chlorine source, under the effect of skeleton nickel, load-type nickel, palladium, platinum, carry out catalytic hydrogenation and prepare corresponding aroma amine, catalyst levels is the 0.5-3.0% of aromatic nitro compound weight, temperature of reaction is 50-150 ℃, and reaction pressure is the 5-100 kilograms per centimeter
2
2, the preparation method of aromatic amine compound according to claim 1 is characterized in that aromatic nitro compound is meant nitrobenzene derivative, and the substituting group on the phenyl ring can have one or more alkyl except that nitro, hydroxyl, alkoxyl group, amido, halogen.
3, the preparation method of aromatic amine compound according to claim 2 is characterized in that ammonia synthesis gas is meant hydrogen richness 〉=35% of synthesis ammonia plant, is mixed with the ammonia synthesis gas or the off-gas of nitrogen, ammonia, methane, hydrogen.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96107507A CN1059432C (en) | 1996-05-09 | 1996-05-09 | Preparation aromatic amine compound |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN96107507A CN1059432C (en) | 1996-05-09 | 1996-05-09 | Preparation aromatic amine compound |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1141912A true CN1141912A (en) | 1997-02-05 |
| CN1059432C CN1059432C (en) | 2000-12-13 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN96107507A Expired - Fee Related CN1059432C (en) | 1996-05-09 | 1996-05-09 | Preparation aromatic amine compound |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1059432C (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101434548B (en) * | 2008-11-07 | 2012-03-21 | 甘肃中科药源生物工程有限公司 | Method for preparing diaminobenzene from dinitro benzene |
| CN102816074A (en) * | 2012-08-27 | 2012-12-12 | 万隆化工有限公司 | Synthesis method of p-n-butylaniline |
| CN103467302A (en) * | 2013-09-18 | 2013-12-25 | 葫芦岛天启晟业化工有限公司 | Application of antioxidant in distillation reaction of p-chloroaniline |
| CN103977833A (en) * | 2014-05-20 | 2014-08-13 | 中国科学院福建物质结构研究所 | Preparation method and application of coordination polymer platinum-loaded nano-catalyst |
| CN108218719A (en) * | 2017-12-23 | 2018-06-29 | 杨向党 | A kind of method for being not added with antioxidant continuous rectification parachloroanilinum |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE3928329A1 (en) * | 1989-08-26 | 1991-02-28 | Bayer Ag | METHOD FOR PRODUCING CHLORINE-SUBSTITUTED AROMATIC AMINES |
| DE4023056A1 (en) * | 1990-07-20 | 1992-01-23 | Bayer Ag | METHOD FOR THE PRODUCTION OF AROMATIC AMINES IN THE P POSITION BY C (ARROW DOWN) 1 (ARROW DOWN) -C (ARROW DOWN) 4 (ARROW DOWN) 4 (ARROW DOWN) |
| DE4404342C2 (en) * | 1994-02-11 | 1996-09-19 | Hoechst Ag | Process for the preparation of aminofluoroaromatics (fluoroanilines) or aminofluoroheteroaromatics |
| DE4428017A1 (en) * | 1994-08-08 | 1996-02-15 | Bayer Ag | Process for the preparation of aromatic amines |
-
1996
- 1996-05-09 CN CN96107507A patent/CN1059432C/en not_active Expired - Fee Related
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101434548B (en) * | 2008-11-07 | 2012-03-21 | 甘肃中科药源生物工程有限公司 | Method for preparing diaminobenzene from dinitro benzene |
| CN102816074A (en) * | 2012-08-27 | 2012-12-12 | 万隆化工有限公司 | Synthesis method of p-n-butylaniline |
| CN103467302A (en) * | 2013-09-18 | 2013-12-25 | 葫芦岛天启晟业化工有限公司 | Application of antioxidant in distillation reaction of p-chloroaniline |
| CN103467302B (en) * | 2013-09-18 | 2015-08-26 | 葫芦岛天启晟业化工有限公司 | The application of a kind of antioxidant in p-Chlorobenzoic acid amide distillation reaction |
| CN103977833A (en) * | 2014-05-20 | 2014-08-13 | 中国科学院福建物质结构研究所 | Preparation method and application of coordination polymer platinum-loaded nano-catalyst |
| CN108218719A (en) * | 2017-12-23 | 2018-06-29 | 杨向党 | A kind of method for being not added with antioxidant continuous rectification parachloroanilinum |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1059432C (en) | 2000-12-13 |
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