NaCl-Na2SO4-H2O system and process for producing NaHCO3, NH4Cl and NaCl from NH4HCO3
A nacl-na2so4-h2o, production process technology, applied in the directions of alkali metal chlorides, ammonium halides, carbonate preparations, etc., can solve the problems of waste of resources, environmental pollution, application, etc., and achieve no three-waste emissions and raw material adaptability. Strong and low energy consumption
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Embodiment 1
[0018] Embodiment 1: take 105.30m 3 NaCl-Na 2 SO 4 -H 2 O system Glauber's salt brine (NaCl 295g / l, Na 2 SO 4 18.27g / l) and 31.05 tons of ammonium bicarbonate (including NH 4 HCO 3 99.2%) as raw materials for metathesis reaction (reaction temperature 40°C) to separate and obtain 32.62 tons of sodium bicarbonate product and 116.38 m of soda-making mother liquor containing ammonium chloride, sodium sulfate and sodium chloride 3 (NaCl 71g / l, NaCl 2 SO 4 18.27g / l, NH 4 Cl 179g / l), high temperature (temperature 130°C) evaporation and separation of soda-making mother liquor to obtain 10.39 tons of mixed salt of sodium chloride and sodium sulfate and 75.09 tons of salt-making nitrate mother liquor 3 / h (NaCl 90g / l, NaCl 2 SO 4 19g / l, NH 4 Cl 437g / l), the salt-making nitric acid mother liquor was evaporated and separated at low temperature (temperature 50°C) to obtain 20.83 tons of ammonium chloride and 43.73m of ammonium-making mother liquor 3 / h (NaCl 133g / l, NaCl 2...
Embodiment 2
[0020] Embodiment 2: take 102.07m 3 NaCl-Na 2 SO 4 -H 2 O system Glauber's salt brine (NaCl 290g / l, Na 2 SO 4 20g / l) and 27.95 tons of ammonium bicarbonate (including NH 4 HCO 3 99.2%) as raw material for metathesis reaction (reaction temperature 45°C) to separate and obtain 29.36 tons of sodium bicarbonate product and 116.38 m of soda-making mother liquor containing ammonium chloride, sodium sulfate and sodium chloride 3 (NaCl 78g / l, NaCl 2 SO 4 20g / l, NH 4 Cl 161g / l), high temperature (temperature 130°C) evaporation and separation of soda-making mother liquor to obtain 11.41 tons of mixed salt of sodium chloride and sodium sulfate and 67.58m of salt-making nitrate mother liquor 3 / h(NaCl90g / l, NaCl 2 SO 4 19g / l, NH 4 Cl 437g / l), the salt-making nitric acid mother liquor was evaporated and separated at low temperature (temperature 50°C) to obtain 18.75 tons of ammonium chloride and 39.36m of ammonium-making mother liquor 3 / h (NaCl 133g / l, NaCl 2 SO 4 37g / ...
Embodiment 3
[0022] Embodiment 3: take 100.10m 3 NaCl-Na 2 SO 4 -H 2 O system Glauber's salt brine (NaCl 285g / l, Na 2 SO 4 30g / l) and 34.16 tons of ammonium bicarbonate (including NH 4 HCO 3 99.2%) as raw materials for metathesis reaction (reaction temperature 40°C) to separate and obtain 35.88 tons of sodium bicarbonate product and 116.38 m of soda-making mother liquor containing ammonium chloride, sodium sulfate and sodium chloride 3 (NaCl 70g / l, NaCl 2 SO 4 30g / l, NH 4 Cl 160g / l), high temperature (temperature 130°C) evaporation separation of soda-making mother liquor to obtain 11.64 tons of mixed salt of sodium chloride and sodium sulfate and 82.60m of salt-making nitrate mother liquor 3 / h(NaCl90g / l, NaCl 2 SO 4 19g / l, NH 4 Cl 437g / l), the salt-making nitric acid mother liquor was evaporated and separated at low temperature (temperature 50°C) to obtain 18.62 tons of ammonium chloride and 48.10m of ammonium-making mother liquor 3 / h (NaCl 133g / l, NaCl 2 SO 4 37g / l, NH...
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