Amino naphthalene sulphonic acids prepn. from corresp. nitro cpds. - using mostly used Raney nickel under specified conditions
A process for prepg. aminonaphthalene sulphonic acids by catalytic hydrogenation of the salts of nitronaphtalene sulphonic acids comprises the following. A mixture of used Raney nickel catalyst and fresh Raney nickel catalyst is suspended in water and/or an aq. soln. of the hydrogenation product. Th...
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Main Authors | , , , , , |
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Format | Patent |
Language | English German |
Published |
26.04.1979
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Edition | 2 |
Subjects | |
Online Access | Get full text |
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Abstract | A process for prepg. aminonaphthalene sulphonic acids by catalytic hydrogenation of the salts of nitronaphtalene sulphonic acids comprises the following. A mixture of used Raney nickel catalyst and fresh Raney nickel catalyst is suspended in water and/or an aq. soln. of the hydrogenation product. The suspension under 100-300 bars hydrogen pressure is heated to 100-180 degrees C. At this temp. a soln. or suspension of the nitronaphthalene sulphonic acid at pH 6-9 is added in amt. such that the content of the nitro cpd. in the reaction mixture is not above 5% of the total weight and the final concn. of aminonaphthalene sulphonic acid is 5-40% of the total reaction mixture. The products are intermediates in the prepn. of dyes. The process gives a 10% yield increase compared with previous processes (95-99% and a space/time yield of 1-3 kg. amino cpd./l. capacity/hr.); also the bulk of the catalyst may be recycled and a faster reaction rate is obtained. |
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AbstractList | A process for prepg. aminonaphthalene sulphonic acids by catalytic hydrogenation of the salts of nitronaphtalene sulphonic acids comprises the following. A mixture of used Raney nickel catalyst and fresh Raney nickel catalyst is suspended in water and/or an aq. soln. of the hydrogenation product. The suspension under 100-300 bars hydrogen pressure is heated to 100-180 degrees C. At this temp. a soln. or suspension of the nitronaphthalene sulphonic acid at pH 6-9 is added in amt. such that the content of the nitro cpd. in the reaction mixture is not above 5% of the total weight and the final concn. of aminonaphthalene sulphonic acid is 5-40% of the total reaction mixture. The products are intermediates in the prepn. of dyes. The process gives a 10% yield increase compared with previous processes (95-99% and a space/time yield of 1-3 kg. amino cpd./l. capacity/hr.); also the bulk of the catalyst may be recycled and a faster reaction rate is obtained. |
Author | KAISER,REINHARD,.DR ZANDER,JUERGEN,.DR BEHRE,HORST,.DR BECKER,HANS-JOACHIM,.DR STEFFAN,GUIDO,.DR BARTH,OTTO |
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DocumentTitleAlternate | VERFAHREN ZUR HERSTELLUNG VON AMINONAPHTHALINSULFONSAEUREN |
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Snippet | A process for prepg. aminonaphthalene sulphonic acids by catalytic hydrogenation of the salts of nitronaphtalene sulphonic acids comprises the following. A... |
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SubjectTerms | CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION ORPROCESSING OF GOODS GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINSTCLIMATE CHANGE |
Title | Amino naphthalene sulphonic acids prepn. from corresp. nitro cpds. - using mostly used Raney nickel under specified conditions |
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