Method for joint production of liquid ammonia and methane chloride
A monochloromethane and combined production technology, applied in the field of chemical technology, can solve the problems of material waste, low element utilization rate, and increased cost, and achieve the effect of recycling, high utilization rate, and increased cost
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Embodiment 1
[0030] Present embodiment provides a kind of method of joint production liquid ammonia and monochloromethane, as figure 1 The process flow chart is shown, and the specific steps are as follows:
[0031] (1) Add 5349g of ammonium chloride and 28392g of phosphoric acid solution with a concentration of 30wt% into the premixing tank with stirring and filter screen for normal pressure premixing. The ratio of phosphoric acid and ammonium chloride is 1:1.5, The premixing temperature is 15°C to obtain a suspension containing ammonium chloride;
[0032] (2) The suspension containing ammonium chloride premixed in step (1) is continuously sent into the tubular reactor with a steam jacket by a small pump, and a metathesis reaction occurs to generate diammonium hydrogen phosphate and hydrogen chloride, and the reaction For the endothermic reaction, the required heat is provided by the steam jacket of the tubular reactor, and the reaction is carried out at 60°C and 10KPa, and the reaction ...
Embodiment 2
[0046] Present embodiment provides a kind of method of joint production liquid ammonia and monochloromethane, specifically:
[0047] (1) Add 5349g of ammonium chloride and 4000g of concentrated phosphoric acid solution with a concentration of 98wt% into the premixing tank with stirring and filter screen for normal pressure premixing. The ratio of concentrated phosphoric acid and ammonium chloride is 1: 2.5, the premixing temperature is 45°C to obtain a suspension containing ammonium chloride;
[0048] (2) The suspension containing ammonium chloride pre-mixed in step (1) is continuously sent into a tubular reactor with a steam jacket with a small pump, and a metathesis reaction occurs to generate diammonium hydrogen phosphate and hydrogen chloride. React under the conditions of 100°C and 50KPa, and the reaction time is 50 minutes; the tubular reactor is followed by a steam-water separator, and the hydrogen chloride gas is continuously released from the top of the steam-water se...
Embodiment 3
[0061] Present embodiment provides a kind of method of joint production liquid ammonia and monochloromethane, specifically:
[0062] (1) Add 5349g of ammonium chloride and 6802g of concentrated phosphoric acid solution with a concentration of 80wt% into the premixing tank with stirring and filter screen for normal pressure premixing. The ratio of concentrated phosphoric acid and ammonium chloride is 1: 1.8, the premixing temperature is 30°C to obtain a suspension containing ammonium chloride;
[0063] (2) The suspension containing ammonium chloride pre-mixed in step (1) is continuously sent into a tubular reactor with a steam jacket with a small pump, and a metathesis reaction occurs to generate diammonium hydrogen phosphate and hydrogen chloride. React under the conditions of 70°C and 15KPa, and the reaction time is 25 minutes; the tubular reactor is followed by a steam-water separator, and the hydrogen chloride gas is continuously released from the top of the steam-water sep...
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