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.
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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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