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Producing long chain amino and dibasic acids

A technology of dodecanedicarboxylic acid and amino acid is applied in the production field of long-chain amino acids and dibasic acids, and achieves the effects of simplifying the separation process, good economy and stable process conditions

Pending Publication Date: 2022-01-14
VITAWORKS IP LLC
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

[0019] In order to solve the shortcomings of the existing industrialized production process, the invention discloses a process for the co-production of long-chain amino acid and dibasic acid

Method used

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  • Producing long chain amino and dibasic acids
  • Producing long chain amino and dibasic acids
  • Producing long chain amino and dibasic acids

Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0138] This example concerns the production of 11-aminoundecanoic acid and dodecanedioic acid.

[0139] 90 g of 12-ketostearic acid was mixed with 200 mL of water, and then an aqueous solution (about 8%) containing 14.5 g of hydroxylamine sulfate was added. The mixture was vigorously stirred at 70-85°C while adjusting the pH of the reaction solution with aqueous ammonia and maintaining the pH at 4.5-5.0. The reaction was tracked by HPLC. After 2 hours of reaction, the starting material was completely converted into 12-oximino stearic acid.

[0140] After the oximation reaction is completed, the mixture is allowed to stand for phase separation, the lower water phase is separated, and the upper oil phase is vacuum-dried. The obtained product was dissolved in 500 mL of 98% methanesulfonic acid and heated to 140° C., and the Beckmann rearrangement was completed after 4 hours of reaction. The reaction was quenched by adding 500 mL of water. Filtration and washing with deionized ...

Embodiment 2

[0147] This example relates to the production of 9-aminononanoic acid and sebacic acid.

[0148] 90 g of 10-ketostearic acid was mixed with 200 mL of water, and then an aqueous solution (about 8%) containing 12.5 g of hydroxylamine sulfate was added. The mixture was vigorously stirred at 70-80° C. for 2 h, while adjusting the pH of the reaction solution with aqueous ammonia and maintaining the pH at 4.5-5.0. HPLC followed the reaction, and the starting material was completely converted to 10-oximinostearic acid.

[0149] The water phase was separated, and the oil phase was vacuum-dried and dissolved in a mixture of 100 g of trifluoroacetic acid and 100 g of acetonitrile, and the reaction was heated to reflux for 8 hours to complete the Beckmann rearrangement. After the solvent was recovered by distillation, 300 mL of water was added to precipitate an off-white mixed amide fatty acid product.

[0150] The solid mixed amide fatty acid was dissolved in 200mL of acetic acid, and...

Embodiment 3

[0155] This example concerns the production of 13-aminotridecanoic acid and tetradecanedioic acid.

[0156] 100 g of 14-ketoarachidic acid was mixed with 200 mL of water, and then an aqueous solution (about 8%) containing 16.5 g of hydroxylamine sulfate was added. The mixture was vigorously stirred at 70-85° C. for 2 h, while adjusting the pH value of the reaction solution with aqueous ammonia and maintaining the pH value at 4.5-5.0. The reaction was followed by HPLC, and the starting material was completely converted to 14-oximinoarachidic acid.

[0157] The water phase was separated, and the oil phase was vacuum-dried to obtain a waxy solid. The waxy solid was slowly added to 300 mL of 98% sulfuric acid at 100 °C. After the solution was stirred at 100°C for 2 h, the Beckmann rearrangement was completed, and 800 g of ice was added to quench the reaction. Filter and wash with water to obtain a dark mixed amide fatty acid product.

[0158] Add the mixed amide fatty acid and...

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Abstract

There is disclosed a process for the production of dodecanedioic acid and 11- aminoundecanoic acid, comprising: (1) reacting castor oil with a primary or secondary amine to form a amide; (2) isomerizing the amide in the presence of a catalyst to form ketoamide; (3) reacting the ketoamide with hydroxylamine to form the oximeamide; (4) subjecting the oximeamide to Beckmann rearrangement to yield a mixture of two diamides; (5) hydrolyzing the mixed diamides to produce dodecanedioic acid, 11-aminoundecanoic acid, hexylamine and heptanoic acid.

Description

[0001] Cross References to Related Applications [0002] This application is a continuation-in-part of U.S. Patent Application U.S. 16 / 436,470 filed June 10, 2019, which is a continuation-in-part of U.S. Patent Application U.S. 15 / 880,293 filed January 25, 2018, now 2019 U.S. Patent U.S. 10,343,978, issued July 9, 2018, U.S. Patent Application 15 / 880,293 is a continuation-in-part of U.S. Patent Application U.S. 15 / 644,708, filed July 7, 2017 U.S. 10,065,921, the contents of each patent are incorporated by reference. technical field [0003] The present invention relates to a kind of production method of long-chain nylon monomer, more specifically, relate to a kind of production method of long-chain amino acid and dibasic acid. Background technique [0004] Long-chain saturated aliphatic amino acids, lactams and dibasic acids are important monomers for long-chain nylon and engineering plastics. Nylon is a class of long-chain polymers containing amide linkages in the backbon...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C51/06C07C51/42C07C55/21C07C227/04C07C227/40C07C229/08
CPCC07C51/06C07C51/42C07C227/28C07C227/20C07C231/00C07C231/12C07C55/21C07C229/08C07C237/22C07C235/74
Inventor 胡松洲宋真
Owner VITAWORKS IP LLC