Method for treating arsenic-containing aqueous solution
View Patent ↗Provided is a method for treating an arsenic-containing aqueous solution by water treatment employing a titanium dioxide photocatalyst that is excellent in both photocatalytic activity and solid-liquid separation performance. The method according to the present disclosure includes the steps: of adding catalyst particles to the aqueous solution; oxidizing trivalent arsenic by irradiating the aqueous solution with light having a wavelength of 200 nanometers or more and 400 nanometers or less while stirring the catalyst particles in the aqueous solution; and stopping the stirring and separating the catalyst particles from the aqueous solution by sedimentation. Each catalyst particle is composed only of a titanium dioxide particle and a zeolite particle, the titanium dioxide particle is adsorbed on the outer surface of the zeolite particle, the zeolite particle has a silica/alumina molar ratio of 10 or more, and the catalyst particles are contained in the aqueous solution at a concentration of 0.4 grams/liter or more and 16 grams/liter or less.
1. A method for treating an arsenic-containing aqueous solution, comprising:
a step (a) of adding catalyst particles to the aqueous solution containing trivalent arsenic;
a step (b) of oxidizing trivalent arsenic by irradiating the aqueous solution with light having a wavelength of 200 nanometers or more and 400 nanometers or less while stirring the catalyst particles in the aqueous solution; and
a step (c) of stopping the stirring in the step (b) and separating the catalyst particles from the aqueous solution by sedimentation,
wherein each catalyst particle is composed only of a titanium dioxide particle and a zeolite particle, the titanium dioxide particle is adsorbed on an outer surface of the zeolite particle, the zeolite particle has a silica/alumina molar ratio of 10 or more, and the catalyst particles are contained in the aqueous solution at a concentration of 0.4 grams/liter or more and 16 grams/liter or less.
2. The method according to claim 1 , comprising a step (d) of adding again the catalyst particles separated by sedimentation in the step (c) to the aqueous solution after the step (c),
wherein the step (b) and the step (c) are performed again after the step (d).
3. The method according to claim 1 , wherein
the catalyst particles are separated by sedimentation by using a solid-liquid separation vessel so that the catalyst particles are sedimented in the solid-liquid separation vessel in the step (c), the solid-liquid separation vessel including a filtration membrane element,
the filtration membrane element comprises a plate-shaped frame and sheets of filter paper made of resin and attached to both faces of the frame, and is arranged parallel to a direction in which the catalyst particles are sedimented, and
the method further comprises a step (d) of passing the aqueous solution through one of the sheets of filter paper to produce treated water from the aqueous solution.
4. The method according to claim 3 , comprising a step (e) of adding again the catalyst particles separated by sedimentation in the step (c) to the aqueous solution after the step (c), wherein the step (b), the step (c) and the step (d) are performed again after the step (e).
5. The method according to claim 1 , wherein pentavalent arsenic produced in the step (b) is removed by a coagulating sedimentation process, an adsorption process, or a reverse osmosis membrane process.
6. The method according to claim 1 , wherein the zeolite particle is a zeolite particle subjected to a process in which an alumina portion is dissolved by treatment with an acid aqueous solution to introduce an active site for direct adsorption of the titanium dioxide particle, and then the acid aqueous solution adhered to the surface of the zeolite particle is removed by washing with water.
7. The method according to claim 1 , wherein the step (a) of adding catalyst particles to the aqueous solution includes adding a slurry containing the catalyst particles to the aqueous solution in a tank reactor.
8. The method according to claim 1 , wherein the catalyst particles have an average particle diameter of 5.5 μm.
9. The method according to claim 1 , further comprising mixing titanium dioxide particles and zeolite particles in water, thereby forming the catalyst particles.
10. The method according to claim 9 , the mixing comprises applying ultrasonic dispersion treatment to allow the titanium dioxide particles to be adsorbed on surfaces of the zeolite particles.