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Synthesis method of DTPA (diethylene triamine pentacetic acid) penta-sodium salt

A synthesis method and sodium salt technology, applied in chemical instruments and methods, preparation of organic compounds, organic chemistry and other directions, can solve the problems of affecting the yield of DTPA, intensified hydrolysis of sodium chloroacetate, and inability to compete with similar products, and achieve a beneficial effect. The effect of later refining and purification, stable reaction and shortening of process time

Active Publication Date: 2014-02-12
YIXING FENGZE CHEM
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Problems solved by technology

[0003] The DTPA industrial production method has following two kinds at present: the first kind of method is the chloroacetic acid method, CN101607921A a kind of preparation method of diethylenetriaminepentaacetic acid, the research of pentasodium diethylenetriaminepentaacetic acid synthetic technique ("Chemical Industry and Engineering Technology" (2008.29. (1). 18-19)), DTPA chelating agent and its manufacture ("Paper and Paper" (2005.3.63-64)), DTPA synthesis process ("Paper Chemicals" (1997.9 ( 4) .7-10)), the synthesis of papermaking chemical DTPA ("China Paper" (1997.5.68-69)) and other documents have introduced this method, which uses chloroacetic acid, diethylenetriamine and hydrogen oxidation Synthesis of raw materials such as sodium or sodium carbonate has a relatively simple process, but a large amount of by-product sodium chloride will be produced during the production process, and the obtained DTPA crude product needs to be desalted and purified. In addition, chloroacetic acid is easy to hydrolyze during the production process, which seriously affects DTPA Yield
[0004] The second method is the sodium cyanide method, the research on the synthesis method of DTPA ("Leather Chemical Industry" (2002.19. (5). 26-28)), the synthesis of diethylenetriaminepentaacetic acid ("Chemical Industry and Engineering Technology" ( 2006.27.(6).24-25)) and other documents introduced this method, using sodium cyanide, formaldehyde and diethylenetriamine and other raw materials to synthesize. The advantages of this method are simple operation, low cost, good product quality, and no Sodium chloride is produced as a by-product, but this method uses highly toxic cyanide as a raw material, making production management difficult to control
[0005] At present, most domestic production of DTPA adopts the chloroacetic acid method, and the yield is low. The yield reported in the literature is mostly below 80%. In addition, the impurity content is high, the salt content is high, and the refining process is backward, so it cannot compete with similar foreign products in the market.
[0006] Above-mentioned chloroacetic acid method reaction equation is as follows, and wherein formula 1, 2 are target reaction equations, but in actual production, when lye is added dropwise, the local concentration of lye may be too large and easily cause the hydrolysis failure of sodium chloroacetate, formula 3 is Sodium chloroacetate is hydrolyzed under strong alkaline conditions to generate sodium glycolate and sodium chloride. As the pH value of the solution system rises further in the later stage, the hydrolysis of sodium chloroacetate may be intensified
Sodium carbonate can also be used in the chloroacetic acid neutralization step, but at a higher cost

Method used

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  • Synthesis method of DTPA (diethylene triamine pentacetic acid) penta-sodium salt
  • Synthesis method of DTPA (diethylene triamine pentacetic acid) penta-sodium salt
  • Synthesis method of DTPA (diethylene triamine pentacetic acid) penta-sodium salt

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Embodiment 1

[0064] Dissolve 240 kg of chloroacetic acid in 80 kg of deionized water to prepare a chloroacetic acid solution; slowly add 52 kg of diethylenetriamine, turn on the cooling device, and put ice water into the jacket to control the temperature of the reaction system at -10 to -5°C; Then slowly add 630 kg of 32-33% sodium hydroxide solution in two batches. When the first 315 kg is slowly added, the jacket is fed with ice water to control the reaction temperature at -10~-5°C; the last 315 kg of sodium hydroxide When the solution is slowly added, the temperature of the reaction system is controlled by feeding water into the jacket to be 55-60° C. After the sodium hydroxide solution is added, the temperature is kept for 3 hours; the pH value of the solution is adjusted to 11.5, and the temperature is lowered to room temperature, and the material is filtered out.

Embodiment 2

[0066] Dissolve 240 kg of chloroacetic acid in 80 kg of deionized water to prepare a chloroacetic acid solution; slowly add 52 kg of diethylenetriamine, open the cooling device, and put ice water into the jacket to control the temperature of the reaction system to be -5 to 0°C; then Slowly add 630 kg of 32-33% sodium hydroxide solution in two batches. When the first 315 kg is slowly added, the jacket is fed with ice water to control the reaction temperature at -5~0°C; the last 315 kg of sodium hydroxide solution is slowly added. When adding, the temperature of the reaction system is controlled by feeding water into the jacket to be 45-50° C. After adding the sodium hydroxide solution, it is kept warm for 4 hours; the pH value of the solution is adjusted to 11.5, cooled to room temperature, and filtered out.

Embodiment 3

[0068] Dissolve 240 kg of chloroacetic acid in 80 kg of deionized water to prepare a chloroacetic acid solution; slowly add 52 kg of diethylenetriamine, open the cooling device, and put ice water into the jacket to control the temperature of the reaction system to be 0-5°C; Slowly add 630 kg of 32-33% sodium hydroxide solution in 2 batches. When the first 315 kg is slowly added, the jacket is filled with ice water to control the reaction temperature at 0-5°C; when the last 315 kg of sodium hydroxide solution is slowly added , the temperature of the reaction system is controlled by feeding water into the jacket to be 50-55° C., and the sodium hydroxide solution is added and kept warm for 5 hours; the pH value of the solution is adjusted to 11.5, and the temperature is lowered to room temperature, and the material is filtered and discharged.

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Abstract

The invention discloses a synthesis method of a DTPA (diethylene triamine pentacetic acid) penta-sodium salt, and belongs to the field of chemical synthesis. The synthesis method comprises the following steps: dissolving chloroacetic acid into deionized water to obtain a chloroacetic acid solution; adding diethylene triamine into the chloroacetic acid solution for reaction, and maintaining the temperature of a solution reaction system at -20-30 DEG C; slowly adding 2 / 5 to 3 / 5 of sodium hydroxide into the solution reaction system, controlling the reaction temperature at -20-30 DEG C; slowly adding the remaining sodium hydroxide into the reaction system, and controlling the reaction temperature at 30-60 DEG C, and preserving heat and reacting for 2-5 hours after the sodium hydroxide is completely added; adjusting the pH of the reaction system in the step 4) to 11.5, cooling to room temperature, and filtering. According to the synthesis method, the yield of the DTPA penta-sodium salt is improved; in the synthesis process, the reaction is relatively stable and the reaction time is shortened by controlling the alkali dripping speed and the reaction temperature.

Description

Technical field: [0001] The invention relates to the field of chemical industry, in particular to a method for synthesizing DTPA pentasodium salt. Background technique: [0002] Diethylenetriaminepentaacetic acid (DTPA) is an important aminocarboxyl complexing agent, and its pentasodium salt is often used in practical applications. The effect of eliminating color-forming metal ions is very obvious, and it is widely used in textile, dyeing, chemical process control and other aspects. Since the stability and antioxidant capacity of the chelate formed by DTPA and transition metal ions are stronger than those of ethylenediaminetetraacetic acid (EDTA), it can chelate metal ions such as calcium, magnesium, iron, manganese in water, and reduce the impact of metal ions , so it is widely used in the bleaching process of wood pulp. [0003] The DTPA industrial production method has following two kinds at present: the first kind of method is the chloroacetic acid method, CN101607921A...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C229/16C07C227/18C07C227/08
Inventor 艾飞艾强陈强黄建平
Owner YIXING FENGZE CHEM
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