Nitric acid production technology with double-pressurized method
A production process, double pressurization technology, applied in the direction of nitric acid, sustainable manufacturing/processing, chemical industry, etc., can solve the problems of not reducing the NOx content in the tail gas, low output, high production cost, etc., and achieve heat recovery The effect of good utilization, low NOx content, and lower absorption temperature
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Embodiment 1
[0019] (1) Mixing of raw materials: liquid ammonia is pressurized to 0.52MPa by the ammonia evaporator, then heated to 100°C by the heater, enters the ammonia filter, removes oil and other impurities, and adjusts the system and air through the ammonia air ratio Mixing, the air used for mixing should enter the air filter and air compressor in advance, pressurize to 0.45MPa, and control the temperature at 236°C;
[0020] (2) Ammoxidation reaction process: Ammonia-air mixed gas is evenly distributed on the platinum grid through the distributor on the top of the ammonia oxidation furnace, and the oxidation reaction of ammonia is carried out. The reaction temperature is controlled at 860°C and the pressure is controlled at 0.45MPa;
[0021] (3) Heat recovery and cooling process: the NOx-containing gas after the above reaction passes through the steam superheater, waste heat boiler, high-temperature gas-gas heat exchanger, and economizer to recover heat, and then passes through the l...
Embodiment 2
[0025] Example 2: The rest is the same as in Example 1, the difference is that the ammonia oxygen reaction temperature in step (2) is controlled at 880°C, the bleaching tower top pressure in step (5) is -25KPa, and the temperature is 43°C, and the step ( 6) The medium tail gas is heated to 365°C.
[0026]
Example 1 Example 2 Example 3 Total Ammonia Utilization 93.2% 96.5% 91.3% NOx removal rate in bleaching tower 97.2% 98.1% 94.5% NOx content in exhaust gas 20ppm 15ppm 25ppm
[0027] Through the above three examples, it can be seen from the three sets of data in the above table that the ammonia oxygen reaction temperature is controlled at 880°C, the top pressure of the bleaching tower is controlled at -25KPa, the temperature is 43°C, and the tail gas is gradually heated to 365°C before entering the tail gas expander. At this time, the total utilization rate of nitrogen and the NOx removal rate in the bleaching tower are the highe...
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