Method for recovering triethylamine from industrial waste water
A technology for industrial wastewater and triethylamine, which is applied in chemical instruments and methods, natural water treatment, water/sewage treatment, etc., can solve the problems of triethylamine being unable to be obviously stratified, high steam energy consumption, and large amount of wastewater, etc. To achieve the effect of reducing energy consumption, reducing sewage pressure, and reducing recovery costs
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Embodiment 1
[0032] Get the waste water with low content of triethylamine produced in the production of ceftriaxone sodium, wherein triethylamine content is 0.8wt%, pH value is 5.7, COD is 960mg / L, and ammonia nitrogen is 145mg / L. Regulate the pH value of this waste water to 10 with 32wt% sodium hydroxide solution, pass through macroporous adsorption resin column bed (resin model DM700, wet packing, loading capacity 1.0L, aspect ratio is 8.0 with the flow rate of 2.0L / h ), when the detection column outlet effluent detected triethylamine, it stopped entering the waste water (waste water intake: 10L), and collected the adsorption residual liquid flowing through the resin column bed simultaneously, and in this adsorption residual liquid, COD was 80mg / L, The ammonia nitrogen is 15mg / L, which is discharged into the general sewage treatment system of the factory for unified biochemical treatment; then, 1.5L of purified water is used to pass through the macroporous adsorption resin column bed (flo...
Embodiment 2
[0036] Get the waste water with low content of triethylamine produced in the production of ceftriaxone sodium, wherein the content of triethylamine is 0.5wt%, the pH value is 5.3, the COD is 890mg / L, and the ammonia nitrogen is 131mg / L. Regulate the pH value of this waste water to 10 with 32wt% sodium hydroxide solution, pass through macroporous adsorption resin column bed (resin model DM700, wet packing, loading capacity 1.0L, aspect ratio is 8.0 with the flow rate of 2.5L / h ), when the detection column outlet effluent detected triethylamine, it stopped entering the waste water (waste water intake: 16.5L), and collected the adsorption residual liquid flowing through the resin column bed simultaneously, and the COD in the adsorption residual liquid was 68mg / L , ammonia nitrogen is 18mg / L, and it is discharged into the general sewage treatment system of the factory for unified biochemical treatment; then, 1.5L of purified water is used to pass through the macroporous adsorption ...
Embodiment 3
[0040] Get the waste water with low content of triethylamine produced in the production of ceftriaxone sodium, wherein the content of triethylamine is 1.0wt%, the pH value is 4.6, the COD is 915mg / L, and the ammonia nitrogen is 113mg / L. Regulate the pH value of this waste water to 11 with 32wt% sodium hydroxide solution, pass through macroporous adsorption resin column bed (resin model LX033, wet packing, loading capacity 1.0L, aspect ratio is 8.0 with the flow velocity of 1.5L / h ), when the detection column outlet effluent detected triethylamine, it stopped entering waste water (waste water intake: 8L), and collected the adsorption residual liquid flowing through the resin column bed simultaneously, and in this adsorption residual liquid, COD was 62mg / L, The ammonia nitrogen is 14mg / L, which is discharged into the general sewage treatment system of the factory for unified biochemical treatment; then, 1.5L of purified water is used to pass through the macroporous adsorption res...
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