New process for producing high-purity iminodiacetonitrile

A technology of iminodiacetonitrile and a new process, which is applied in the field of producing high-purity iminodiacetonitrile, can solve the problems of sharp decline in product quality, increase in three waste treatment costs, high impurity content in mother liquor, etc., and achieve good product quality, high conversion rate, The effect of simple ingredients

Active Publication Date: 2010-12-15
SICHUAN LUTIANHUA
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

However, at present, the content of industrial iminodiacetonitrile is mostly about 92%. After neutralization of the reaction solution, the content of the primary acid (IDA) obtained after solid-liquid separation of iminodiacetic acid (IDA) can only guarantee 97%, and the color is relatively dark. Poor, needs to be decolorized
Moreover, the mother liquor has high impurity content and cannot be applied mechanically (the product quality drops sharply after application), so the secondary acid and the tertiary acid can only be processed in stages to obtain the secondary acid (IDA, content 90%), the tertiary acid (IDA, content 70%), four or more acids (IDA, content below 50%), and two or more acids (accounting for 20% of IDA) must be refined to more than 97% before they can enter the synthesis of diglyphosate, the process is extremely cumbersome ; Repeated refining, the impurities in the mother liquor continue to accumulate, and the mother liquor is finally withdrawn. On the one hand, the final mother liquor contains iminodiacetic acid (about 20%), which causes a loss of yield after withdrawal, and on the other hand increases the treatment cost of the three wastes

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 1

[0069] A 20,000-ton / year iminodiacetonitrile industrial plant. Run according to the scheme provided by the present invention, its operation parameter and index control are as follows:

[0070] The flash condenser 18, the first evaporator condenser 19, and the condensed water produced by the second evaporator condenser 20 total 5660kg / h, wherein 1639kg / h condensed water is pumped to the ammonia preparation tank 1, and 555kg / h The liquid ammonia with a purity of 99.5% is mixed to generate 2194kg / h of dilute ammonia water, and the concentration of the ammonia water is 25.3% after testing. After being metered by the ammonia water metering pump 3, it enters the ammonia water preheater 4 and is preheated to 90~120°C with a pressure of 0.8MPa. 50% raw material hydroxyacetonitrile with a pH of 2.0~3.0 adjusted by ammonium phosphate buffer solution or ammonium sulfate buffer solution 7407kg / h Hydroxyacetonitrile metering pump controlled by automatic feeding system 4 According to hydro...

Embodiment 2

[0081] In the same set of equipment, the reaction liquid purification and decolorization process is changed to activated carbon adsorption decolorization, and the other processes remain unchanged. Assess the output in 1 hour:

[0082]The white iminodiacetonitrile product with a purity of 99% is 2718kg / h, calculated in terms of hydroxyacetonitrile, and the total yield is 87.2%.

[0083] Send 4880kg / h of dilute waste liquid for biochemical treatment.

[0084] The concentrated waste liquid sent to the incinerator for treatment is 175kg / h in total.

[0085] Consumption specific surface area 600m2 / g activated carbon 100kg / h.

Embodiment 3

[0087] In the same set of equipment, the reaction solution purification and decolorization process is changed to ion exchange resin decolorization, and other processes remain unchanged. Assess the output in 1 hour:

[0088] The white iminodiacetonitrile product with a purity of 99% is 2685kg / h, and the total yield is 86.0% based on hydroxyacetonitrile.

[0089] Send 4980kg / h of dilute waste liquid for biochemical treatment.

[0090] A total of 165kg / h of concentrated waste liquid will be sent to the incinerator for treatment.

[0091] Consumption of waste water treatment resin 500kg / h.

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Abstract

The invention relates to a new process for producing high-purity iminodiacetonitrile. The new process is characterized in that: high-purity reaction liquid is obtained by using a process for synthesizing iminodiacetonitrile at high conversion rate; and white or pale yellow high-purity iminodiacetonitrile with iminodiacetonitrile content of over 99 percent is produced by using a synthesis reaction liquid decolorizing process, an impurity removal process and three crystallization processes, wherein a part of thin waste liquid produced during the production is returned to a raw material preparation system, the rest part of waste liquid is conveyed to a biochemical device for processing, and the produced thick waste liquid is directly conveyed to an incinerator for processing, so that pollution-free production of the entire process is realized. The new process has the advantages of high product quality, white color, purity of over 99 percent high product yield, iminodiacetonitrile yield of about 90 percent during the entire production process and low three-waste treatment difficulty.

Description

technical field [0001] The invention relates to a new process for producing high-purity iminodiacetonitrile. Background technique [0002] Iminodiacetonitrile (IDAN) is an important raw material for the production of glyphosate, and its development momentum has been strong in recent years. [0003] The production of iminodiacetonitrile is divided into raw material route, which is divided into hydrocyanic acid method and hydroxyacetonitrile method. [0004] U.S. patents disclose a large number of processes for producing iminodiacetonitrile by hydrocyanic acid method, such as: US2794044, US3167580, US3412137, US3886198, US3904668, US3988360, US4307037, etc. The disadvantages of the above process are: [0005] First, the raw material hydrocyanic acid is not easy to preserve, and it is easy to leak and cause danger during the production process; second, the conditions are harsh and the time required is long; third, the yield of iminodiacetonitrile is low and the economy is poo...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C255/24C07C253/30C07C253/34
Inventor 宁忠培何兴川李辑超李庆王诚林朝阳罗光碧戴志谦张爱民何惠基刘勤蔡雅娟
Owner SICHUAN LUTIANHUA
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