A pickling waste liquor regeneration system and method for removing free acid in advance
A technology for pickling waste liquid and free acid, applied in combustion methods, chemical instruments and methods, combustion types, etc., can solve the problems of large investment and large land occupation, and achieve reduction of natural gas consumption, operation cost and process energy consumption The effect of reducing and improving the waste liquid treatment capacity
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Embodiment 1
[0075] A method for regenerating pickling waste liquor that removes free acid in advance, said method comprising:
[0076] (1) The pickling waste liquid is contacted with high-temperature flue gas and pre-concentrated at 95°C. The composition of the pickling waste liquid is:
[0077] Element g / L kg / h Remark FeCl 3
38.3 122.57 Fe 3+ =13.2g / L
FeCl 2
272.36 872.56 Fe 2+ =120.0g / L
HCl 43.4 138.88 h 2 o
927.84 2969.1 total 1243.60 3979.54
[0078] The volume of waste liquid treated per hour is 3.2m 3 ;
[0079] The pickling waste liquid after pre-concentration is composed of:
[0080] Element g / L kg / h Remark FeCl 3
51.11 122.68 Fe 3+ =17.6g / L
FeCl 2
363.15 871.56 Fe 2+ =160g / L
HCl 101.01 244.83 h 2 o
862.96 2071.11 total 1379.24 3310.18
[0081] (2) Preheat the pre-concentrated pickling waste liquid to 115°C at ...
Embodiment 2
[0090] A method for regenerating pickling waste liquor that removes free acid in advance, said method comprising:
[0091] (1) The pickling waste liquid is contacted with high-temperature flue gas and pre-concentrated at 90°C. The composition of the pickling waste liquid is:
[0092] Element g / L kg / h Remark FeCl 3
32.5 104.0 Fe 3+ =11.2g / L
FeCl 2
294.82 943.43 Fe 2+ =130.0g / L
HCl 35.7 114.24 h 2 o
930.10 2976.7 total 1293.2 4138.37
[0093] Waste liquid treatment per hour: 3.2m 3 ;
[0094] The pickling waste liquid after pre-concentration is composed of:
[0095]
[0096]
[0097] (2) Preheat the pre-concentrated pickling waste liquid to 113°C at 0.4MPa, and then perform negative pressure flash evaporation at -0.09MPa. The gas phase after flash evaporation is condensed at 30°C to obtain a mass fraction of 20.3%. Hydrochloric acid solution, the mass flow rate of hydrochloric acid solu...
Embodiment 3
[0107] A method for regenerating pickling waste liquor that removes free acid in advance, said method comprising:
[0108] (1) The pickling waste liquid is contacted with high-temperature flue gas and pre-concentrated at 92°C. The composition of the pickling waste liquid is:
[0109]
[0110]
[0111] Waste liquid treatment per hour: 3.2m 3 ;
[0112] The pickling waste liquid after pre-concentration is composed of:
[0113] Element g / L kg / h Remark FeCl 3
51.11 122.57 Fe 3+ =14.74g / L
FeCl 2
453.57 1088.57 Fe 2+ =173.3g / L
HCl 99.46 238.7 h 2 o
786 1886.4 total 1390.14 3336.24
[0114] (2) Preheat the pre-concentrated pickling waste liquid to 116°C at 0.6MPa, and then perform negative pressure flash evaporation at -0.095MPa. The gas phase after flash evaporation is condensed at 33°C to obtain a mass fraction of 23.5%. Hydrochloric acid solution, the mass fraction of hydrochloric acid so...
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