Process for catalytic hydrogenation of halonitroaromatics
US-11820725-B2 · Nov 21, 2023 · US
US9988333B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9988333-B2 |
| Application number | US-201515311951-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 18, 2015 |
| Priority date | May 19, 2014 |
| Publication date | Jun 5, 2018 |
| Grant date | Jun 5, 2018 |
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The present invention relates to a process for reacting chemical compounds comprising the step of reacting a compound of formula (IV) wherein Hal is independently selected from Cl or Br, and X − is a monovalent anion, in the presence of an inorganic acid, wherein the aqueous inorganic acid has a concentration of at least about 60%, at a temperature of about 140° C. to about 250° C., to obtain a compound of formula (V) wherein Hal is as defined above.
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The invention claimed is: 1. A process for reacting chemical compounds comprising the step of hydrolysing a compound of formula (IV) wherein Hal is independently selected from the group consisting of Cl and Br, and X − is HSO 4 − , in the presence of an aqueous inorganic acid, wherein the aqueous inorganic is H 2 SO 4 , which has a concentration of at least 60% by weight, at a temperature of 140° C. to 250° C., to obtain a compound of formula (V) wherein Hal is as defined above; and wherein the compound of formula (IV) is provided by diazotating a compound of formula (III) wherein Hal is as defined above; and wherein the step of diazotating the compound of formula (III) to obtain the compound of formula (IV) is carried out in H 2 SO 4 having a concentration of at least 40% by weight in the presence of NOHSO 4 , and wherein the temperature is from 45° C. to 65° C. 2. The process of claim 1 , wherein product of formula (V) is continuously removed from the reaction system using steam distillation. 3. The process of claim 1 , wherein the concentration of the H 2 SO 4 in the hydrolysis step is at least 70% by weight. 4. The process of claim 3 , wherein at least part of the H 2 SO 4 used in the hydrolysis step is recycled. 5. The process of claim 1 , wherein the hydrolysis step is carried out at a temperature of at least 160° C. 6. The process of claim 1 , wherein NO H SO 4 is obtained by feeding NO x gas to sulfuric acid having a concentration of at least about 60% by weight, and wherein the NO x gas is a mixture of NO and NO 2 in a molar ratio of about 1:1. 7. The process of claim 1 , wherein the water used for steam distillation is recycled in a closed water loop. 8. The process of claim 1 , wherein the compound of formula (III) is obtained by reducing a compound of formula (II) wherein Hal is independently selected from the group consisting of Cl and Br. 9. The process of claim 8 , wherein the compound of formula (II) is obtained by nitrating a compound of formula (I) wherein Hal is independently selected from the group consisting of Cl and Br. 10. The process of claim 1 , further comprising the step of reacting the compound of formula (V) to obtain a compound of formula (VI) wherein Hal is independently selected from the group consisting of Cl and Br, and R 1 is an alkali metal. 11. The process of claim 10 , wherein the step of reacting the compound of formula (V) to obtain a compound of formula (VI) is carried out in the presence of an alkali metal hydroxide and carbon dioxide. 12. The process of claim 10 , further comprising the step of reacting the compound of formula (VI) to obtain a compound of formula (VII) wherein R 2 is —(C 1 -C 4 )alkyl, R 1′ is an alkali metal or —(C 1 -C 4 )alkyl, and Hal is independently selected from the group consisting of Cl and Br. 13. The process of claim 12 , further comprising the step of reacting the compound of formula (VII) to obtain a compound of formula (VIII) wherein R 2 and Hal are as defined in claim 12 . 14. The process of claim 12 , wherein (a) Hal is Cl; and/or (c) R 1′ is selected from the group consisting of sodium and potassium, or R 1′ is selected from the group consisting of ethyl and methyl; and/or (d) R 2 is selected from the group consisting of ethyl and methyl. 15. The process of claim 13 , wherein the compound of formula (VIII) is
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