Method for preparing chloraniliprole from Wille D as raw material

A technology for chloran and raw materials, which is applied in the field of direct synthesis of chloran by Ursi D as a raw material, can solve the problems of pollution, no batch production, and the inability of continuous recycling of mother liquor, etc., and achieve the effects of reducing production costs and improving efficiency.

Pending Publication Date: 2022-07-22
于欣然
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Problems solved by technology

Present domestic basically is to adopt the production technology that takes p-aminophenol as raw material to synthesize chlorinated, but because this technology fails to solve the influence that produces ammonium chloride in the reaction process to mother liquor, makes the mother liquor used in production can't be continuously recycled, Not only the processing cost of the mother liquor is high, but also new pollution and solid waste may be generated. In addition, the price of p-aminophenol is also rising sharply, so this production process is difficult to meet the needs of current production enterprises.
[0003] In addition, in recent years, there have been patents for re-using phenol as raw material to produce chlorine, but due to dangerous and heavily polluting processes such as nitrification and the use of concentrated flow acid, as well as problems such as low product content and high dioxin content, there is no such patent yet. Reports on mass production, etc.

Method used

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Examples

Experimental program
Comparison scheme
Effect test

Embodiment 01

[0020] Example 01: Take the mixed liquid (hereinafter referred to as mother liquor MY) of 50g+200g acetic acid ("specific organic solvent") with a concentration of 15% hydrochloric acid ("specific inorganic acid solution"), a total of 250g, and then 12g of Ursi D (content ≥ 98%) add in mother liquor and stir, be warming up to 60 ℃ and begin to pass into chlorine (the flow rate of chlorine flow is 3.3 × 12g per hour), maintain stirring and control the temperature of chlorination reaction between 60~80 ℃, time-sharing sampling is detected When the melting point of the target material chloran is ≥ 292°C (and the melting point does not continue to rise for 15 minutes in a row), stop the chlorination, filter, wash and dry to obtain the chloran finished product (yellow crystal powder), and recover the mother liquor MY01.

[0021] Result: 25.9g of chloran was obtained (content: 99.3%, acceptance rate: 97%, chemical concentration of dioxin: not tested); recovered mother liquor MY01 was...

Embodiment 02

[0022] Embodiment 02: The mother liquor MY01 (actual recovery is 220g) recovered in Example 01 is retained 200g+concentration 36% hydrochloric acid 600g and a total of 800g mother liquor is applied mechanically, then 120g Ursi D (content ≥ 98%) is added to the mother liquor to stir, When warming up to 110°C, start to feed chlorine gas (the flow rate of chlorine flow is 3.3×120g per hour), maintain stirring and control the chlorination reaction temperature to be between 90 and 110°C, and time-sharing sampling detects the melting point of the target material chloran ≧292 ℃ (the melting point does not continue to rise for 15 minutes), stop the chlorine flow, filter, wash and dry to obtain the finished product (yellow crystal powder) of chlorine, and recover the mother liquor MY02.

[0023]Results: The obtained chlorine ran was 258.2g (content: 99.1%, acceptance rate: 96%, dioxin chemical concentration: 66.80ppb); the recovered mother liquor MY02 was 820g (containing a small amount...

Embodiment 03

[0024] Embodiment 03: directly use the mother liquor MY02 (820g) that embodiment 02 reclaims to carry out mechanically, add 80g Urs D (content ≥ 98%) in the mother liquor and stir, be warming up to 80 ℃ and begin to pass into chlorine (the flow rate of chlorine is per 3.3 × 80 g per hour), maintain stirring and control the chlorination reaction temperature to be between 80 and 90 °C, time-sharing sampling stops when the melting point of the target material chlororan is ≥ 292 °C (the melting point does not continue to rise for 15 minutes). Chlorine, finally stabilize the temperature of the reactor to 95 ℃ and filter, and obtain the finished product (yellow crystal powder) of chloran through processes such as washing and drying, and cool the mother liquor to 30 ℃ and then filter out part of the ammonium chloride to obtain the mother liquor MY03.

[0025] Result: 170.6g of chloran was obtained (content: 98.9%, acceptance rate: 95%, chemical concentration of dioxin: not tested); re...

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Abstract

The invention relates to a method for preparing chloraniliprole from Uille silk D. The method comprises the following steps: stirring and dissolving a Uille silk D raw material or a mixed raw material of Uille silk D, hydroquinone and p-aminophenol in any proportion into a mixed liquid of a specific inorganic acid solution and a specific organic solvent, then introducing chlorine while stirring, carrying out a chlorination reaction at 60-110 DEG C, and separating the chloraniliprole from the chloraniliprole silk D to obtain chloraniliprole silk D, when the melting point of the target product chloraniliprole is detected to be greater than or equal to 292 DEG C and is maintained for more than 10 minutes and the melting point is not continuously increased, stopping introducing chlorine to obtain a chloraniliprole crystal, and filtering, washing and drying to obtain a chloraniliprole finished product; cooling, filtering and decolorizing ammonium chloride generated in the reaction to obtain an ammonium chloride finished product; hydrogen chloride gas generated by the reaction is absorbed by washing water to form a hydrochloric acid finished product; excessive chlorine in the reaction process is absorbed by liquid caustic soda to form a sodium hypochlorite finished product; and the filtered and recycled mother liquor can be infinitely used, so that zero emission is realized.

Description

technical field [0001] The technical scheme of the present invention belongs to the field of organic chemistry, and specifically takes Ursi D as a raw material to directly synthesize chloranil. Background technique [0002] Chloran is a yellow powder with a melting point above 292°C. It is used in the production of pharmaceutical intermediates and antioxidants, and is also one of the main raw materials for the production of permanent violet pigments (partly for export). Beginning in the 1980s, foreign countries began to limit the content of dioxins in chloran products and formulate relevant standards. Since the late 1990s, my country has generally adopted the hydroquinone method instead of the phenol method to produce chloran products to meet the requirements. The requirements of medium and high-end users for dioxin indicators. However, due to the high price of hydroquinone in recent years, this process has been basically eliminated in China. At present, the production proc...

Claims

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Application Information

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Patent Type & Authority Applications(China)
IPC IPC(8): C07C50/24C07C46/00C07C46/10C01C1/16C01B7/01C01B7/07C01B11/06
CPCC07C46/00C07C46/10C01C1/164C01B7/012C01B7/0706C01B11/062C07C50/24
Inventor 于欣然
Owner 于欣然
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