Preparation method and device of aromatic chloride
A chloride and aromatic technology, which is applied in the field of devices for realizing the above-mentioned aromatic chloride preparation method, can solve the problems of shrinkage, high safety risk, poor heat transfer, etc.
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[0088] Example 1
[0089] This tubular reaction device, such as figure 1 As shown, it contains: raw material storage tanks 2, 3, 4, crystallization tanks 5, 6, feed pumps 11, 12, 13, tubular reactor 15, liquid storage tank 7, heat exchanger 8, circulating pump 9 , Heat exchange liquid tank 14, raw material dissolving tank 1, transfer pump 10.
[0090] The number of raw material storage tanks, feed pumps and corresponding material inlets can be set according to needs. Such as figure 2 As shown, when two materials are first added to the tubular reactor during the reaction, and then reacted with another material added later in the tubular reactor 15, ports 16, 17, 20 and ports 18, 19, 21 They are the ports of two three-way hollow pipes; port 21 is connected to tubular reactor 15; ports 16, 17 and 18 are the material inlets of tubular reactor 15; material inlets 16, 17 and 18 are respectively connected to feed pump 11 , 12 and 13 are connected in a sealed connection; the feed pumps ...
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[0097] Example 2
[0098]
[0099] 1. Preparation of raw materials: compound A-1 and acetic acid are stirred at 60°C for 30 minutes to form a solution (35.7% by mass) placed in raw material tank 2, hydrogen peroxide (50% by mass) is placed in raw material tank 3, hydrochloric acid (mass fraction) 36%) placed in the raw material tank 4.
[0100] 2. Using the tubular reactor of Example 1, the reactor pipe inner diameter is 4mm and the pipe length is 40m, according to the following steps: (1) Controlled by a metering pump, the flow rate of compound A-1 solution is 76ml / min, and the flow rate of hydrogen peroxide is 10ml / min mixed first, with a residence time of 2s; (2) then mixed with 28ml / min hydrochloric acid controlled by a metering pump, reacted at an external temperature of 70℃, with a residence time of 4.3min; (3) added the effluent of the tubular reactor into water, Adjust to non-oxidizing with sodium sulfite, filter, wash the filter cake with water, and dry to obtain product...
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[0102] Example 3
[0103] 1. Preparation of raw materials: compound A-1 and acetic acid are stirred at 60°C for 30 minutes to form a solution (35.7% by mass) placed in raw material tank 2, hydrogen peroxide (35% by mass) is placed in raw material tank 3, hydrochloric acid (mass fraction) 36%) placed in the raw material tank 4.
[0104] 2. Using the tubular reactor of Example 1, the inner diameter of the reactor pipe is 4mm and the pipe length is 32m, according to the following steps: (1) Controlled by a metering pump, the flow rate of compound A-1 solution is 51ml / min, and the flow rate of hydrogen peroxide is 9.7 Mix ml / min first, with a residence time of 2s; (2) mix with 19ml / min hydrochloric acid controlled by a metering pump, react at an external temperature of 70°C, with a residence time of 5min; (3) add the effluent from the tubular reactor to water, Adjust to non-oxidizing with sodium sulfite, filter, wash the filter cake with water, and dry to obtain product B-1.
[0105] 3...
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