Production process and preparation method of ultrapure ammonia
A production process, a technology for ultra-pure ammonia, which is applied in the preparation/separation of ammonia, chemical industry, sustainable manufacturing/processing, etc., can solve the problems of long-term stability of ammonia purity, low energy utilization rate, and high power consumption, and achieve energy efficiency. Reduced power consumption, high degree of automation and good safety performance
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Embodiment 1
[0023] A kind of ultrapure ammonia production technique, is characterized in that:
[0024] The raw material ammonia is pumped into the rectification tower. The pressure of the rectification tower is controlled at 1.3-1.5Pa, and the rectification temperature is controlled at about 60°C. Light components and some impurities such as water are removed. ≦100ppm, when the total content of light components is less than 10ppb, recover the cooling capacity, and then enter the oil and water remover after recovering the cooling capacity, control the temperature at 50-55°C, and the pressure within the range of 1.2-1.3 Pa. , when the water content is ≦100ppb, it enters the terminal purification device. The temperature in the control device is within the range of 40-50°C and the pressure is within the range of 1.0-1.2 Pa. After deep removal of water and impurities, the gas ammonia is condensed and then enters the product ammonia tank. Obtain ultra-pure ammonia product.
[0025] A kind of ...
Embodiment 2
[0028] see figure 1 , in this process, the raw material ammonia tank (1), liquid ammonia pump (2), rectification tower (3), oil and water remover (4) are connected with 304 stainless steel pipes and valves, and the terminal purification device ( 5), Condenser (6), product ammonia tank (7) are connected with 316L stainless steel (inner wall electropolished) pipes and valves. The system adopts DCS automatic control. After the rectification tower (3), the total content of light components is less than 10ppb; the water content after the oil and water remover (4) is less than 100ppb; the water content after the terminal purification device (5) is less than 1ppb, and the ammonia content is greater than 7N.
[0029] The process flow of the present invention: the liquefied ammonia in the raw material ammonia tank (1) is pressurized by the pump (2) and enters the rectification tower (3), removes light components and part of the water, enters the oil and water remover (4), and further...
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