Novel absorbent for treating ammonia-containing wastewater or feed liquid by gaseous membrane method
A technology of absorbent and gaseous membrane, applied in water/sewage treatment, water/sludge/sewage treatment, osmosis/dialysis water/sewage treatment, etc.
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Embodiment 1
[0041] Feed liquid: a factory ternary precursor mother liquor wastewater, pH = 13.5, ammonia nitrogen concentration of about 6000mg / L, sulfate ion concentration of 70g / L, surface tension of 70mN / m, slightly turbid, passed through an ultrafiltration membrane with a molecular weight cut-off of 50000 After treatment, it enters the gaseous membrane deamination device. The ultrafiltration process is well known to those skilled in the art and will not be emphasized here.
[0042] Gaseous membrane deamination process: use polypropylene gaseous membrane modules to treat ammonia-containing solutions. The effective membrane area is 65m 2 , The parameters of the membrane silk are: outer diameter 0.53mm, inner diameter 0.40mm, average pore diameter 0.02μm, porosity 50%. The three components are used in series, the water inlet flow rate is 800L / h, the inlet operating pressure is 0.042MPa, and the operating temperature is 35°C.
[0043] Absorbing solution: Potassium dihydrogen phosphate ...
Embodiment 2
[0050] Feed liquid: wastewater from a non-ferrous metal smelter, ammonia nitrogen 1500-2000mg / L, temperature 30°C, pH=12.2, surface tension 72mN / m after pretreatment such as sand filtration and ultrafiltration; devices involved in the pretreatment process and steps are well known to those skilled in the art and will not be emphasized here.
[0051] Gas membrane deamination process: use polypropylene microporous hydrophobic hollow fiber gas membrane module for treatment. The effective membrane area is 65m 2 , The parameters of the membrane silk are: outer diameter 0.53mm, inner diameter 0.40mm, average pore diameter 0.02μm, porosity 50%. Three membrane modules are used in series, the water flow rate is 700L / h, and the inlet operating pressure is 0.04MPa.
[0052] Absorbing solution: Industrial grade sodium dihydrogen phosphate is used to prepare an aqueous solution with a mass fraction of 35%. The measured initial pH is about 3.49. It circulates in the shell side of the gaseo...
Embodiment 3
[0058] Feed liquid: Ammonia nitrogen wastewater from a pharmaceutical factory, yellow and slightly turbid, the concentration of ammonia nitrogen in the influent is 1460mg / L, pH=11.8, temperature 30°C, surface tension 62mN / m; treated by polysulfone ultrafiltration membrane with a molecular weight cut-off of 50,000 Enter the gaseous membrane deamination device. The ultrafiltration process is well known to those skilled in the art and will not be emphasized here.
[0059] Gas membrane deamination process: PTFE gaseous membrane modules are used to treat ammonia-containing solutions. The effective membrane area is 10.5m 2 , The parameters of the membrane are: outer diameter 1.2mm, inner diameter 0.60mm, average pore diameter 0.10μm, porosity 65%, three membrane modules are used in series, the flow rate is 300L / h.
[0060] Absorbing solution: Add methylamine solution dropwise to 30% phosphoric acid solution to make the pH reach 4.0, used as absorbent for gaseous membrane process; ...
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