Method for preparing ortho-nitroaniline by kettle-type continuous operation
A technology of o-nitroaniline and o-nitrobenzene, which is applied in the field of o-nitrochlorobenzene to prepare o-nitrobenzene, can solve the problems of many side reactions, more washing water, and high operating intensity, and achieve product quality and yield Stabilization, reduction of production costs, and reduction of water consumption
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example 1
[0020] Three 50L high-pressure stainless steel reactors are connected in series, each with an effective volume of 35L, 36L, and 36L, and the total effective volume is 107L. According to the molar ratio of 1:10, o-nitrochlorobenzene (hereinafter referred to as ONCB) and ammonia water are pumped into the first-stage reaction kettle, and the flow rates are V ONCB =6.1L / hr, V NH3 = 11.73 L / hr. The stirring speed is 500rpm, the temperature in the reactor is raised to 170°C-175°C, the pressure is 3MPa-6MPa, and the reaction residence time is 6hr. The reaction liquid overflows sequentially from the first-stage reactor to the next-stage reactor.
[0021] After the reaction, oil-water separation was carried out.
[0022] The water layer is cooled to normal temperature, o-nitroaniline (hereinafter referred to as ONBA) is precipitated in solid form, the filter cake is filtered out and put into the o-nitroaniline tank, and the filtrate is heated to recover ammonia.
[0023] The oil la...
example 2
[0026] Three 50L high-pressure stainless steel reaction kettles are connected in series, and the effective volume of each kettle is 35L, 36L, and 36L respectively, and the total effective volume is 107L. Ortho-nitrochlorobenzene and example 1 recovery preparation concentration are that 42% ammoniacal liquor is squeezed in the first stage reactor by pump, and flow rate is V ONCB =6.1L / hr, V NH3 = 11.73 L / hr. The stirring speed is 500rpm, the temperature is raised and the pressure is increased until the temperature is 160°C-200°C, the pressure is 3MPa-7MPa, and the residence time is 6hr. The reaction liquid overflows sequentially from the top of the first-stage reactor to the next-stage reactor.
[0027] After the reaction, oil-water separation was carried out.
[0028] The water layer is cooled to normal temperature, o-nitroaniline (hereinafter referred to as ONBA) is precipitated in solid form, the filter cake is filtered out and put into the o-nitroaniline tank, and the fi...
example 3
[0033] Three 50L high-pressure stainless steel reaction kettles are connected in series, and the effective volume of each kettle is 35L, 36L, and 36L respectively, and the total effective volume is 107L. The o-nitrochlorobenzene and ammonia water with a concentration of 42% are metered and pumped into the first-stage reaction kettle respectively. The stirring speed is 500rpm, the temperature is raised and the pressure is increased until the temperature is 170°C-175°C, the pressure is 4MPa-5MPa, and the residence time is 6hr. The reaction liquid overflows sequentially from the top of the first-stage reactor to the next-stage reactor.
[0034] After the reaction, oil-water separation was carried out.
[0035] The water layer is cooled to normal temperature, o-nitroaniline (hereinafter referred to as ONBA) is precipitated in solid form, the filter cake is filtered out and put into the o-nitroaniline tank, and the filtrate is heated to recover ammonia.
[0036] The oil layer con...
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