Multi-effect energy-saving ammonia recovery process and device
An ammonia recovery and process technology, applied in the field of chemical engineering, can solve the problem of high comprehensive cost of ammonia recovery
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Embodiment 1
[0016] Example 1, the coke oven riser gas with a temperature of 750C uses heat-conducting oil to obtain heat in the waste heat exchanger, and the heat-conducting oil is heated to 200C and then sent to the first-effect heater as a heating source. The waste water containing ammonia of 0.4% (wt%) is sent to the first-effect separator, the pressure of the first-effect separator is 120kPa, and the temperature is 104C; The ammonia content in the liquid phase passing through the first-effect separator is 0.08% (wt%) and sent to the second-effect separator, and the second-effect heater adopts the steam from the first-effect heater as a heating heat source. The pressure of the second-effect separator is 75kPa and the temperature is 78C; the pressure of the second-effect heater is 85kPa and the temperature is 84C. The ammonia content in the liquid phase passing through the second-effect separator is 0.009% (wt%), which is sent to biochemical treatment. The ammonia gas at the top of the...
Embodiment 2
[0018] Example 2, the temperature is 560 ° C tube furnace flue gas with reclaimed water from biochemical treatment in the waste heat heat exchanger, after the reclaimed water is heated to 110 ° C (pressure 300kPa) sent to the first effect heater as Heating heat source. Wastewater containing ammonia of 0.36% (wt%) is sent to the first-effect separator, the pressure of the first-effect separator is 85kPa, and the temperature is 88°C; the first-effect heater is heated by reclaimed water, the pressure is 80kPa, and the temperature is 84°C. The ammonia content in the liquid phase passing through the first-effect separator is 0.06% (wt%) and sent to the second-effect separator, and the second-effect heater adopts the steam from the first-effect heater as a heating heat source. The pressure of the second-effect separator is 65kPa, and the temperature is 72°C; the pressure of the second-effect heater is 75kPa, and the temperature is 74°C. The ammonia content in the liquid phase passi...
Embodiment 3
[0020] Embodiment 3, the equipment used in the multi-effect energy-saving ammonia recovery process, including a waste heat recovery device heated by waste heat gas, 2 sets of ammonia recovery units connected in series and composed of heaters and ammonia separation tower ammonia, the waste heat recovery device 1 The primary heat medium channel is connected with the waste heat gas inlet 7 and the waste heat gas outlet 8, the secondary heat medium channel is connected with the primary heat medium channel of the first-effect heater 3 through the circulation pump 2, and the first-effect ammonia separation tower is equipped with an ammonia-containing Wastewater inlet 9, the secondary heat medium channel of one-effect heater is connected with the ammoniacal waste water channel of one-effect ammonia separation tower 4, namely the ammoniacal waste water outlet 42 at the bottom of one-effect ammonia separation tower is connected with the secondary heat of one-effect heater. The inlet of ...
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