Method for circularly utilizing cooling capacity and method for increasing yield of synthesis ammonia
A technology for synthesizing ammonia and cooling capacity, which is applied in the preparation/separation of ammonia, etc. It can solve the problems affecting the production of ammonia and the air pumping volume of the compressor, and achieve the effects of reducing impurities, increasing the operating cycle, and increasing the air pumping volume
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Embodiment 1
[0026] Such as figure 1 As shown, by adding a cooling tower spray tower at the inlet of the first-stage compressor of synthetic ammonia (that is, before the first stage of compression), the spray nozzle adopts Φ50 volute-type atomizing nozzles, 48 nozzles, and is installed at the inlet of the chilled water pump Install an 80-mesh (70-90 mesh) filter (not shown in the figure), set the outlet pressure of the chilled water pump to 0.45MPa, and the 40°C semi-water gas from the energy section flows into the first-stage compressor before entering the cooling tower for spraying tower; the chilled water at 15°C in the ionic membrane caustic soda section is pumped to the top of the cooling tower spray tower to exchange heat with the semi-water gas through the chilled water pump, and the temperature of the semi-water gas drops below 33°C, and then enters the first-stage compressor for ammonia synthesis, and then Ammonia is synthesized according to the conventional ammonia synthesis pr...
Embodiment 2
[0028] Such as figure 1 As shown, by adding a cooling tower spray tower at the inlet of the first-stage compressor of synthetic ammonia (that is, before the first stage of compression), the spray nozzle adopts Φ50 volute-type atomizing nozzles, 45 nozzles, at the inlet of the chilled water pump Install a 90-mesh filter screen, set the outlet pressure of the chilled water pump to 0.35MPa, and enter the cooling tower spray tower before the 36°C semi-water gas from the energy section flows into the first-stage compressor (that is, the first stage of compression); the ionic membrane caustic soda section 20 The chilled water at about ℃ is pumped to the top of the cooling tower spray tower to exchange heat with the semi-water gas, the temperature of the semi-water gas drops below 31 °C, and then enters the first-stage compressor of synthetic ammonia; the bottom of the cooling tower spray tower comes out The chilled water is pumped through the water recovery pump to the ammonia coole...
Embodiment 3
[0030] Such as figure 1 As shown, by adding a cooling tower spray tower at the inlet of the first-stage compressor of synthetic ammonia, the spray nozzle adopts Φ50 volute type atomizing nozzle, 50 nozzles, and installs 70 mesh (70- 90 mesh) filter screen, the outlet pressure of the chilled water pump is set to 0.40MPa, and the 38°C semi-water gas from the energy section enters the cooling tower spray tower before entering the first-stage compressor (that is, the compression section); the ionic membrane caustic soda section The chilled water at about 12°C is pumped to the top of the cooling tower spray tower to exchange heat with the semi-water gas, the temperature of the semi-water gas drops below 30°C, and then enters the first-stage compressor of synthetic ammonia; the bottom of the cooling tower spray tower The chilled water that comes out is pumped through the water recovery pump to the ammonia cooler to cool down to 11°C, and is used for cooling the chlorine gas. The tem...
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