CN1186124C - Composite base catalyst and its preparing method - Google Patents
Composite base catalyst and its preparing method Download PDFInfo
- Publication number
- CN1186124C CN1186124C CNB031485669A CN03148566A CN1186124C CN 1186124 C CN1186124 C CN 1186124C CN B031485669 A CNB031485669 A CN B031485669A CN 03148566 A CN03148566 A CN 03148566A CN 1186124 C CN1186124 C CN 1186124C
- Authority
- CN
- China
- Prior art keywords
- hydroxide
- base catalyst
- alkali metal
- compound base
- tetraalkylammonium
- 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.)
- Expired - Lifetime
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- 239000003054 catalyst Substances 0.000 title claims abstract description 58
- 239000002131 composite material Substances 0.000 title abstract description 10
- 238000000034 method Methods 0.000 title description 3
- 150000005621 tetraalkylammonium salts Chemical class 0.000 claims abstract description 17
- 150000008044 alkali metal hydroxides Chemical class 0.000 claims abstract description 16
- 238000006243 chemical reaction Methods 0.000 claims abstract description 13
- 238000002360 preparation method Methods 0.000 claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 12
- 229910044991 metal oxide Inorganic materials 0.000 claims abstract description 8
- 150000004706 metal oxides Chemical class 0.000 claims abstract description 8
- 238000003756 stirring Methods 0.000 claims abstract description 8
- 150000001875 compounds Chemical class 0.000 claims description 35
- 239000002585 base Substances 0.000 claims description 34
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 18
- 150000005622 tetraalkylammonium hydroxides Chemical class 0.000 claims description 14
- WGTYBPLFGIVFAS-UHFFFAOYSA-M tetramethylammonium hydroxide Chemical group [OH-].C[N+](C)(C)C WGTYBPLFGIVFAS-UHFFFAOYSA-M 0.000 claims description 14
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 9
- 229910000272 alkali metal oxide Inorganic materials 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 claims description 7
- 125000000217 alkyl group Chemical group 0.000 claims description 4
- 229910052799 carbon Inorganic materials 0.000 claims description 4
- 125000004432 carbon atom Chemical group C* 0.000 claims description 4
- JKQOBWVOAYFWKG-UHFFFAOYSA-N molybdenum trioxide Chemical compound O=[Mo](=O)=O JKQOBWVOAYFWKG-UHFFFAOYSA-N 0.000 claims description 4
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 claims description 4
- 229910001948 sodium oxide Inorganic materials 0.000 claims description 4
- WJZPIORVERXPPR-UHFFFAOYSA-L tetramethylazanium;carbonate Chemical compound [O-]C([O-])=O.C[N+](C)(C)C.C[N+](C)(C)C WJZPIORVERXPPR-UHFFFAOYSA-L 0.000 claims description 4
- 229940073455 tetraethylammonium hydroxide Drugs 0.000 claims description 3
- LRGJRHZIDJQFCL-UHFFFAOYSA-M tetraethylazanium;hydroxide Chemical compound [OH-].CC[N+](CC)(CC)CC LRGJRHZIDJQFCL-UHFFFAOYSA-M 0.000 claims description 3
- 150000005324 oxide salts Chemical class 0.000 claims description 2
- CHWRSCGUEQEHOH-UHFFFAOYSA-N potassium oxide Chemical compound [O-2].[K+].[K+] CHWRSCGUEQEHOH-UHFFFAOYSA-N 0.000 claims description 2
- 229910001950 potassium oxide Inorganic materials 0.000 claims description 2
- DZLFLBLQUQXARW-UHFFFAOYSA-N tetrabutylammonium Chemical compound CCCC[N+](CCCC)(CCCC)CCCC DZLFLBLQUQXARW-UHFFFAOYSA-N 0.000 claims description 2
- KJFVITRRNTVAPC-UHFFFAOYSA-L tetramethylazanium;sulfate Chemical group C[N+](C)(C)C.C[N+](C)(C)C.[O-]S([O-])(=O)=O KJFVITRRNTVAPC-UHFFFAOYSA-L 0.000 claims description 2
- LPSKDVINWQNWFE-UHFFFAOYSA-M tetrapropylazanium;hydroxide Chemical compound [OH-].CCC[N+](CCC)(CCC)CCC LPSKDVINWQNWFE-UHFFFAOYSA-M 0.000 claims description 2
- 239000007864 aqueous solution Substances 0.000 claims 1
- LQNUZADURLCDLV-UHFFFAOYSA-N nitrobenzene Chemical compound [O-][N+](=O)C1=CC=CC=C1 LQNUZADURLCDLV-UHFFFAOYSA-N 0.000 abstract description 31
- PAYRUJLWNCNPSJ-UHFFFAOYSA-N N-phenyl amine Natural products NC1=CC=CC=C1 PAYRUJLWNCNPSJ-UHFFFAOYSA-N 0.000 abstract description 21
- 239000003513 alkali Substances 0.000 abstract description 5
- 238000006482 condensation reaction Methods 0.000 abstract description 3
- 238000004519 manufacturing process Methods 0.000 abstract description 3
- 238000006467 substitution reaction Methods 0.000 abstract description 3
- 125000003118 aryl group Chemical group 0.000 abstract description 2
- 230000000269 nucleophilic effect Effects 0.000 abstract description 2
- 125000005207 tetraalkylammonium group Chemical group 0.000 abstract 3
- 150000001448 anilines Chemical class 0.000 abstract 1
- 239000006227 byproduct Substances 0.000 abstract 1
- 229910052739 hydrogen Inorganic materials 0.000 abstract 1
- 239000001257 hydrogen Substances 0.000 abstract 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 abstract 1
- 239000000047 product Substances 0.000 abstract 1
- -1 cerium hydroxide tetramethyl-ammonium Chemical compound 0.000 description 5
- 238000002156 mixing Methods 0.000 description 5
- 150000003839 salts Chemical class 0.000 description 5
- XXYMSQQCBUKFHE-UHFFFAOYSA-N 4-nitro-n-phenylaniline Chemical compound C1=CC([N+](=O)[O-])=CC=C1NC1=CC=CC=C1 XXYMSQQCBUKFHE-UHFFFAOYSA-N 0.000 description 4
- OIJHFHYPXWSVPF-UHFFFAOYSA-N para-Nitrosodiphenylamine Chemical compound C1=CC(N=O)=CC=C1NC1=CC=CC=C1 OIJHFHYPXWSVPF-UHFFFAOYSA-N 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- OKIZCWYLBDKLSU-UHFFFAOYSA-M N,N,N-Trimethylmethanaminium chloride Chemical compound [Cl-].C[N+](C)(C)C OKIZCWYLBDKLSU-UHFFFAOYSA-M 0.000 description 2
- 238000004587 chromatography analysis Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- RUKISNQKOIKZGT-UHFFFAOYSA-N 2-nitrodiphenylamine Chemical compound [O-][N+](=O)C1=CC=CC=C1NC1=CC=CC=C1 RUKISNQKOIKZGT-UHFFFAOYSA-N 0.000 description 1
- GNGCALKASVBYMT-UHFFFAOYSA-N 2-nitroso-n-phenylaniline Chemical compound O=NC1=CC=CC=C1NC1=CC=CC=C1 GNGCALKASVBYMT-UHFFFAOYSA-N 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 239000011552 falling film Substances 0.000 description 1
- 150000007529 inorganic bases Chemical class 0.000 description 1
- LQNUZADURLCDLV-IDEBNGHGSA-N nitrobenzene Chemical group [O-][N+](=O)[13C]1=[13CH][13CH]=[13CH][13CH]=[13CH]1 LQNUZADURLCDLV-IDEBNGHGSA-N 0.000 description 1
- ATGUVEKSASEFFO-UHFFFAOYSA-N p-aminodiphenylamine Chemical compound C1=CC(N)=CC=C1NC1=CC=CC=C1 ATGUVEKSASEFFO-UHFFFAOYSA-N 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- APBDREXAUGXCCV-UHFFFAOYSA-L tetraethylazanium;carbonate Chemical compound [O-]C([O-])=O.CC[N+](CC)(CC)CC.CC[N+](CC)(CC)CC APBDREXAUGXCCV-UHFFFAOYSA-L 0.000 description 1
- 230000008542 thermal sensitivity Effects 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
Abstract
The present invention discloses a composite alkali catalyst and a preparation method thereof. The catalyst is a water solution composed of tetra-alkyl ammonium hydroxid, alkali metal hydroxide or oxide and tetra-alkyl ammonium salts. The preparation method of the composite alkali catalyst comprises: the tetra-alkyl ammonium hydroxid, the alkali metal hydroxide or oxide and tetra-alkyl ammonium salts are proportionally added to water; a temperature of the water is controlled; the composite alkali catalyst is obtained by homogeneously stirring the water, the tetra-alkyl ammonium hydroxid, the alkali metal hydroxide or oxide and tetra-alkyl ammonium salts. Cheap alkali metal hydroxide or oxide and tetra-alkyl ammonium salts are adopted by the present invention, so the production cost is substantially reduced. Meanwhile, byproducts of nitrobenzene adjacent substitution of aniline are reduced in the reaction of hydrogen substitution by nucleophilic aromaticring, and consequently, the purity of the product can be improved. The composite alkali catalyst is used for the condensation reaction of nitrobenzene and aniline. A conversion rate of nitrobenzene is larger than 99%, and the selectivity is larger than 97%.
Description
Technical field
The present invention relates to a kind of compound base catalyst and preparation method thereof, particularly a kind ofly carry out the synthetic 4 nitrodiphenyl amine of condensation reaction and 4-nitrosodiphenylamine or/and compound base catalyst of their salt and preparation method thereof with nitrobenzene and aniline.
Background technology
In the technical process of preparation 4-aminodiphenylamine, contract and react synthetic 4 nitrodiphenyl amine and 4-nitrosodiphenylamine or/and in the technology of their salt, selection of catalysts is a key by aniline and nitrobenzene.
Be used for aniline and nitrobenzene at present and contract and catalyst for reaction, mainly contain two kinds: one, use inorganic base (as NaOH, KOH etc.) or inorganic salts (as K
2CO
3) make catalyst, but adopt the reaction temperature height of this catalyst, conversion ratio is low, and selectivity is low poor, the post processing difficulty, and the more alkali waste water that contains is arranged, catalyst can not reclaim, and is difficult to handle.Two, utilize tetraalkylammonium hydroxide to make catalyst (referring to CN1307556A), though this method can overcome the problems referred to above, but catalyst costs an arm and a leg, aniline carries out substitution reaction at the ortho position of nitrobenzene easily, generation as the 2-nitrodiphenylamine of accessory substance or/and 2-nitrosodiphenylamine and replace azophenlyene, thereby reduced degree of purity of production.
Summary of the invention
The technical issues that need to address of the present invention are that development is a kind of cheap, and the compound base catalyst that catalytic activity is high improves the conversion ratio that aniline and nitrobenzene contract and reacts, and increases selectivity.
Compound base catalyst of the present invention is made up of tetraalkylammonium hydroxide, alkali metal hydroxide or oxide and tetraalkylammonium salt.
The structural formula of tetraalkylammonium hydroxide is:
In the formula, each R represents to contain the alkyl of 1-4 carbon atom independently.Wherein preferred tetramethyl ammonium hydroxide, tetraethyl ammonium hydroxide, tetrapropylammonium hydroxide, tetrabutylammonium, most preferably tetramethyl ammonium hydroxide.
Alkali metal hydroxide or oxide comprise NaOH or sodium oxide molybdena, potassium hydroxide or potassium oxide.
The structural formula of tetraalkylammonium salt is:
In the formula, each R represents to contain the alkyl of 1-4 carbon atom, X independently
N-Be Cl
-, Br
-, I
-, HCO
3 -, CO
3 2-, HSO
4 -, SO
4 2-, n=1-2 preferably adopts tetramethyl ammonium sulfate, tetramethyl ammonium carbonate.
Tetraalkylammonium hydroxide in the compound base catalyst that the present invention adopts: alkali metal hydroxide: tetraalkylammonium salt=(2-9): (0.5-3): (0.5-3) (mole), if adopt alkali metal oxide, then its ratio in catalyst can convert by corresponding hydroxide and get.
The preparation method of the compound base catalyst that the present invention adopts, with tetraalkylammonium hydroxide, alkali metal hydroxide, tetraalkylammonium salt is (2-9) in molar ratio: (0.5-3): (0.5-3), be added in certain water gaging the control temperature, stir, promptly make this compound base catalyst.If adopt alkali metal oxide, then its ratio in catalyst can convert by corresponding hydroxide and get.
In the compound base catalyst that the present invention adopts, tetraalkylammonium hydroxide, alkali metal hydroxide, tetraalkylammonium salt three concentration sum are 15-50 (weight %), preferred 25-38 (weight %), and determine the consumption of water with this.Adopt alkali metal oxide, should be converted into corresponding hydroxide and calculate.
The preparation of the compound base catalyst that the present invention adopts because catalyst is a thermal sensitivity, is decomposed with regard to producing above 90 ℃, and therefore the temperature of controlling is no more than 90 ℃.
The compound base catalyst that the present invention adopts can recycle and reuse.Help the stream falling film evaporator to concentrate by an effect or multiple-effect gas.Compound base catalyst after the recovery directly or after adding a spot of fresh compound base catalyst recycles, and income effect does not have significant difference with the effect of using fresh compound base catalyst.
Be that synthetic 4 nitrodiphenyl amine of raw material and 4-nitrosodiphenylamine are or/and in the reaction of their salt with aniline and nitrobenzene, adopt this compound base catalyst, control certain reaction condition, reaction finishes, by the liquid-phase chromatographic analysis products therefrom, the nitrobenzene conversion ratio is greater than 99%, and selectivity is greater than 97%.
The present invention has adopted cheap alkali metal hydroxide or its oxide and tetraalkylammonium salt, make compound base catalyst with tetraalkylammonium hydroxide is compound, make production cost significantly reduce, replace the accessory substance that aniline replaces at the nitrobenzene ortho position in the H-H reaction at the nucleophilic aromatic ring simultaneously and reduce, improved the purity of product.
The specific embodiment
Below utilize specific embodiment to describe the present invention in detail.
Embodiment 1
In being furnished with 500 milliliters of three-neck flasks of condenser and agitator, add entry 230 grams, (containing the pure cerium hydroxide tetramethyl-ammonium is 50% not to be sequentially added into tetramethyl ammonium hydroxide 91 grams, 0.50 mole, all the other are water), NaOH 20 gram (0.5 mole), tetramethyl ammonium carbonate 52 grams (0.25 mole), 75 ± 2 ℃ of control mixing temperatures stir, make composite catalyst, concentration 29.9 (weight %).
Embodiment 2
In being furnished with 500 milliliters of three-neck flasks of condenser and agitator, add entry 230 grams, be not sequentially added into tetramethyl ammonium hydroxide 91 grams and (contain pure cerium hydroxide tetramethyl-ammonium 50%, 0.50 mole, all the other are water), NaOH 20 gram (0.5 mole), tetramethyl ammonium chloride 55 grams (0.5 mole), 75 ± 2 ℃ of control mixing temperatures stir, make composite catalyst, concentration 30.4 (weight %).
Embodiment 3
In being furnished with 500 milliliters of three-neck flasks of condenser and agitator, add entry 230 grams, be not sequentially added into tetramethyl ammonium hydroxide 91 grams and (contain pure cerium hydroxide tetramethyl-ammonium 50%, 0.50 mole, all the other are water), sodium oxide molybdena 15.5 gram (0.25 mole), tetramethyl ammonium chloride 55 grams (0.5 mole), 75 ± 2 ℃ of control mixing temperatures stir, make composite catalyst, concentration 30.4 (weight %).
Embodiment 4
In being furnished with 500 milliliters of three-neck flasks of condenser and agitator, add entry 290 grams, be not sequentially added into tetraethyl ammonium hydroxide 147 grams and (contain pure cerium hydroxide tetraethyl ammonium 50%, 0.50 mole, all the other are water), NaOH 20 gram (0.5 mole), tetraethyl ammonium carbonate 80 grams (0.25 mole), 75 ± 2 ℃ of control mixing temperatures stir, make composite catalyst, concentration 32.3 (weight %).
Embodiment 5
In being furnished with 500 milliliters of three-neck flasks of condenser and agitator, add entry 230g, be not sequentially added into tetramethyl ammonium hydroxide 91 grams and (contain pure cerium hydroxide tetramethyl-ammonium 50%, 0.50 mole, all the other are water), sodium oxide molybdena 15.5 gram (0.25 mole), tetramethyl ammonium carbonate 52 grams (0.25 mole), control mixing temperature 75 ± 2 (℃), stir, make composite catalyst, concentration 30.2 (weight %).
Application Example
Use the compound base catalyst of embodiment 1-5 preparation, synthetic 4 nitrodiphenyl amine of the condensation reaction of catalysis aniline and nitrobenzene and 4-nitrosodiphenylamine are or/and their salt.
In being furnished with 500 milliliters of three-neck flasks of condenser, agitator and vacuum plant, drop into above-mentioned compound base catalyst successively, aniline 615 grams (6.61 moles), drip nitrobenzene 123 down in 70 ℃-75 ℃ and restrain (1 mole), the limit adds nitrobenzene sideband vacuum, and control nitrobenzene dripped time 1-1.5 hour, stirred 4 hours down in 70 ℃-75 ℃ then, by the liquid-phase chromatographic analysis products therefrom, the nitrobenzene conversion ratio reaches 99.5%, selectivity 98%.
Claims (12)
1, a kind of compound base catalyst is characterized in that the aqueous solution that this catalyst is made up of tetraalkylammonium hydroxide, alkali metal hydroxide or its oxide and tetraalkylammonium salt.
2, compound base catalyst according to claim 1 is characterized in that the structural formula of described tetraalkylammonium hydroxide is:
In the formula, each R represents to contain the alkyl of 1-4 carbon atom independently.
3, compound base catalyst according to claim 1 and 2 is characterized in that described tetraalkylammonium hydroxide is tetramethyl ammonium hydroxide or tetraethyl ammonium hydroxide or tetrapropylammonium hydroxide or tetrabutylammonium.
4, compound base catalyst according to claim 1 is characterized in that described alkali metal hydroxide or oxide comprise NaOH or sodium oxide molybdena, potassium hydroxide or potassium oxide.
5, compound base catalyst according to claim 1 is characterized in that the structural formula of described tetraalkylammonium salt is:
In the formula, each R represents to contain the alkyl of 1-4 carbon atom, X independently
N-Be Cl
-, Br
-, I
-, HCO
3 -, CO
3 2-, HSO
4 -, SO
4 2-, n=1-2.
6, compound according to claim 1 or 5 base catalyst is characterized in that described tetraalkylammonium salt is tetramethyl ammonium sulfate or tetramethyl ammonium carbonate.
7, compound base catalyst according to claim 1, it is characterized in that tetraalkylammonium hydroxide: alkali metal hydroxide: tetraalkylammonium salt=(2-9): (0.5-3): (0.5-3) (mole), the ratio of alkali metal oxide in its catalyst can convert by corresponding hydroxide and get.
8, according to the preparation method of claim 1 or 7 described compound base catalysts, it is characterized in that according to the above ratio tetraalkylammonium hydroxide, alkali metal hydroxide, tetraalkylammonium salt, be added in certain water gaging, the control temperature, stir, promptly get this compound base catalyst, if adopt alkali metal oxide, then its consumption in catalyst can convert by corresponding hydroxide and get.
9, the preparation method of compound base catalyst according to claim 8, it is characterized in that in the compound base catalyst, tetraalkylammonium hydroxide, alkali metal hydroxide, tetraalkylammonium salt three concentration expressed in percentage by weight summation are 15%-50%, if adopt alkali metal oxide, then its consumption can convert by corresponding hydroxide and get.
10, the preparation method of compound base catalyst according to claim 8, it is characterized in that in the compound base catalyst, tetraalkylammonium hydroxide, alkali metal hydroxide or oxide, tetraalkylammonium salt three concentration expressed in percentage by weight summation are 25%-38%, if adopt alkali metal oxide, then its consumption can convert by corresponding hydroxide and get.
11, the preparation method of compound base catalyst according to claim 8 is characterized in that controlling reaction temperature and is no more than 90 ℃.
12, compound base catalyst according to claim 1 is characterized in that compound base catalyst can reclaim recycled.
Priority Applications (31)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB031485669A CN1186124C (en) | 2003-07-04 | 2003-07-04 | Composite base catalyst and its preparing method |
| BRPI0412101-5A BRPI0412101A (en) | 2003-07-04 | 2004-07-02 | process for the preparation of 4-aminodiphenylamine |
| EP04738332A EP1645555B1 (en) | 2003-07-04 | 2004-07-02 | A method for producing 4-aminodiphenylamine |
| US10/882,677 US7176333B2 (en) | 2003-07-04 | 2004-07-02 | Process for preparing 4-aminodiphenylamine |
| EA200501647A EA009395B1 (en) | 2003-07-04 | 2004-07-02 | A process for preparing 4-aminodiphenylamine |
| JP2006517937A JP4546958B2 (en) | 2003-07-04 | 2004-07-02 | Method for producing 4-aminodiphenylamine |
| DE602004010234T DE602004010234T2 (en) | 2003-07-04 | 2004-07-02 | PROCESS FOR THE PREPARATION OF 4-AMINODIPHENYLAMINE |
| JP2006500463A JP4500302B2 (en) | 2003-07-04 | 2004-07-02 | Method for producing 4-aminodiphenylamine |
| ES04738332T ES2373720T3 (en) | 2003-07-04 | 2004-07-02 | METHOD FOR THE PRODUCTION OF 4-AMINODYPHENYLAMINE. |
| CA2515238A CA2515238C (en) | 2003-07-04 | 2004-07-02 | Process for preparing 4-aminodiphenylamine |
| EP04738331A EP1591438B1 (en) | 2003-07-04 | 2004-07-02 | A process for preparing 4-aminodiphenylamine |
| AT04738332T ATE526305T1 (en) | 2003-07-04 | 2004-07-02 | METHOD FOR PRODUCING 4-AMINODIPHENYLAMINE |
| EA200600052A EA009396B1 (en) | 2003-07-04 | 2004-07-02 | A method for producing 4-aminodiphenylamine |
| MXPA05013788A MXPA05013788A (en) | 2003-07-04 | 2004-07-02 | A process for preparing 4-aminodiphenylamine. |
| PCT/CN2004/000734 WO2005003079A1 (en) | 2003-07-04 | 2004-07-02 | A method for producing 4-aminodiphenylamine |
| PL04738332T PL1645555T3 (en) | 2003-07-04 | 2004-07-02 | A method for producing 4-aminodiphenylamine |
| US10/883,042 US7084302B2 (en) | 2003-07-04 | 2004-07-02 | Process for preparing 4-aminodiphenylamine |
| PCT/CN2004/000733 WO2005003078A1 (en) | 2003-07-04 | 2004-07-02 | A process for preparing 4-aminodiphenylamine |
| KR1020040051541A KR100612922B1 (en) | 2003-07-04 | 2004-07-02 | A process for producing 4-aminodiphenylamine |
| PT04738332T PT1645555E (en) | 2003-07-04 | 2004-07-02 | A method for producing 4-aminodiphenylamine |
| ES04738331T ES2298762T3 (en) | 2003-07-04 | 2004-07-02 | PROCESS TO PREPARE 4-AMINODYPHENYLAMINE. |
| CA2531074A CA2531074C (en) | 2003-07-04 | 2004-07-02 | Process for preparing 4-aminodiphenylamine |
| KR1020040051932A KR100612923B1 (en) | 2003-07-04 | 2004-07-05 | A process for preparing 4-aminodiphenylamine |
| US11/477,954 US7235694B2 (en) | 2003-07-04 | 2006-06-30 | Process for preparing 4-aminodiphenylamine |
| US11/757,277 US20080039657A1 (en) | 2003-07-04 | 2007-06-01 | Process for preparing 4-aminodiphenylamine |
| US11/759,897 US8293673B2 (en) | 2003-07-04 | 2007-06-07 | Process for preparing 4-aminodiphenylamine |
| US11/759,901 US20070227675A1 (en) | 2003-07-04 | 2007-06-07 | Process for preparing 4-aminodiphenylamine |
| US12/195,371 US7989662B2 (en) | 2003-07-04 | 2008-08-20 | Process for preparing 4-aminodiphenylamine |
| US12/900,459 US8486223B2 (en) | 2003-07-04 | 2010-10-07 | Falling film evaporator |
| US13/104,900 US8686188B2 (en) | 2003-07-04 | 2011-05-10 | Process for preparing 4-aminodiphenylamine |
| US13/620,588 US9029603B2 (en) | 2003-07-04 | 2012-09-14 | Process for preparing alkylated p-phenylenediamines |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB031485669A CN1186124C (en) | 2003-07-04 | 2003-07-04 | Composite base catalyst and its preparing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1470330A CN1470330A (en) | 2004-01-28 |
| CN1186124C true CN1186124C (en) | 2005-01-26 |
Family
ID=34156271
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB031485669A Expired - Lifetime CN1186124C (en) | 2003-07-04 | 2003-07-04 | Composite base catalyst and its preparing method |
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| Country | Link |
|---|---|
| CN (1) | CN1186124C (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100336796C (en) * | 2004-07-15 | 2007-09-12 | 王农跃 | Process for preparing 4-amino diphenylamine |
| CN100453525C (en) * | 2004-07-15 | 2009-01-21 | 江苏圣奥化学科技有限公司 | Process for preparing 4-amino diphenylamine |
| CN108558675A (en) * | 2018-04-25 | 2018-09-21 | 南通理工学院 | A kind of synthetic method of 4-ADPA |
-
2003
- 2003-07-04 CN CNB031485669A patent/CN1186124C/en not_active Expired - Lifetime
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| Publication number | Publication date |
|---|---|
| CN1470330A (en) | 2004-01-28 |
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Owner name: SHANDONG SHENG AO CHEMICAL CO., LTD. Free format text: FORMER OWNER: GUO ZHANGYU Effective date: 20080118 |
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Effective date of registration: 20080118 Address after: 1#, North Ring Road, Heze, Shandong, Caoxian Patentee after: Shandong Sinorgchem chemical Limited by Share Ltd. Address before: 1#, North Ring Road, Heze, Shandong, Caoxian Patentee before: Guo Changyu |
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Owner name: JIANGSU SHENG AO CHEMICAL TECHNOLOGY CO., LTD. Free format text: FORMER OWNER: SHANDONG SHENG AO CHEMICAL CO., LTD. Effective date: 20080711 |
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Effective date of registration: 20080711 Address after: Room 1, No. 212, drug City Avenue, Jiangsu, Taizhou Patentee after: Jiangsu Sinorgchem Technology Co.,Ltd. Address before: No. 1, North Ring Road, Heze, Shandong, Caoxian Patentee before: Shandong Sinorgchem chemical Limited by Share Ltd. |
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Address after: Room 1, building 606, medicine City Avenue, Jiangsu, Taizhou, China, 225316 Patentee after: SENNICS Co.,Ltd. Address before: 225300 Jiangsu City, Taizhou Province medicine city road, room 1, No. 212 Patentee before: Jiangsu Sinorgchem Technology Co.,Ltd. |
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Address after: 200120 Shanghai, China (Shanghai) free trade zone, 2304 Pudong Avenue, 2304. Patentee after: SENNICS Co.,Ltd. Address before: 225316 Room 606, medicine City Avenue, Taizhou, Taizhou, Jiangsu Patentee before: SENNICS Co.,Ltd. |
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Granted publication date: 20050126 |
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