Magnetic aluminum-based adsorbent and preparation method therefor
US-2024342688-A1 · Oct 17, 2024 · US
US9604859B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9604859-B2 |
| Application number | US-201314421904-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 17, 2013 |
| Priority date | Aug 17, 2012 |
| Publication date | Mar 28, 2017 |
| Grant date | Mar 28, 2017 |
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In the present invention nanotubes-based dye-adsorbent powder is used for adsorption and decomposition of synthetic dye under dark-condition without the use of any external power-source such as the applied potential-difference, microwave, ultrasonicator, and others to save the energy consumption, which results in a complete dye-decomposition on the powder-surface. The surface-cleaned dye-adsorbent powder has very high specific surface-area and dye-adsorption capacity comparable with those of the original dye-adsorbent powder and can be recycled for the next cycles of dye-adsorption and dye-decomposition under the dark-condition. In the present method, the nanotubes-based dye-adsorbent powder is stirred under the dark-condition in an aqueous dye solution containing a strong oxidizer to get simultaneous dye-adsorption and dye-decomposition on the powder-surface, or getting dye adsorption in one solution and dye decomposition in a separate solution by said adsorbent powder under dark condition.
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What is claimed is: 1. A process for decomposition of organic synthetic-dyes using semiconductor-oxides nanotubes via dark-catalysis which comprises the steps of: (i) suspending nanotubes-based dye-adsorbent powder in an aqueous solution of organic synthetic-dye, wherein the concentration of nanotubes-based dye-adsorbent powder is in the range of 0.1-3.0 g L −1 ; (ii) adding a strong oxidizer in the above solution of step (i), stirring the suspension, under the dark-condition, using a magnetic or overhead stirrer for 10-3600 min for simultaneous dye-adsorption and dye-decomposition on the powder-surface, designated as “one-step method”, wherein the net dye-removal rate is in the range of 1-100 mg g −1 h −1 ; (iii) separating the powder from the solution of step (ii) using a centrifuge operated at 2000-4000 rpm; (iv) drying the powder in an oven at 70-90° C. for 15-20 h; and (v) recycling the dried-powder to repeat step-(i) to step-(iv) for the next cycle of dye-decomposition under the dark-condition. 2. The process as claimed in claim 1 , wherein the nanotubes-based dye-adsorbent powder consists of high surface-area nanotubes selected from the group of H 2 Ti 3 O 7 and anatase-TiO 2 processed via hydrothermal. 3. The process as claimed in claim 1 , wherein the organic synthetic-dye is selected from the group consisting of basic, acidic, and reactive-dyes in an aqueous solution. 4. The process as claimed in claim 1 , wherein the strong oxidizer is selected from a group consisting of H 2 O 2 and any other material containing the OH′ group except water. 5. The process as claimed in claim 1 , wherein H 2 O 2 is used as the strong oxidizer in the concentration range of 0.5-15 M (3-50 wt. %). 6. The process as claimed in claim 1 , wherein the dried nanotubes powder obtained at step (iv) retains adsorbent capacity in the one-step method of dye decomposition. 7. The process as claimed in claim 1 , wherein the recycled dye-adsorbent powder is pale-yellow in color having the same capacity for the maximum dye-adsorption, under the dark-condition, as that of the original white-color dye-adsorbent powder. 8. The process as claimed in claim 1 , wherein the step (ii) is replaced by the step of: transferring the dye-adsorbent powder treated with the solution of organic synthetic dye in step (i) to another aqueous solution containing a strong oxidizer and stirring the suspension, under the dark-condition, designated as “two-step method”, using a magnetic or overhead stirrer for 10-3600 min for the complete dye-decomposition on the powder-surface. 9. The process as claimed in claim 8 , wherein the dried nanotubes powder obtained at step (iv) retains adsorbent capacity in the two-step method of dye decomposition. 10. The process as claimed in claim 8 , wherein the concentration of nanotubes-based dye-adsorbent powder with the surface-adsorbed organic synthetic-dye is in the range of 0.1-3.0 g L −1 and the net dye-removal rate, involving the dye-adsorption and dye-decomposition occurring in separate aqueous solutions under the dark-condition, designated as “two-step method”, is in the range of 0.1-10 mg g −1 h −1 .
Dyes; Colorants; Fluorescent agents · CPC title
by catalytic oxidation · CPC title
using solar energy · CPC title
using inorganic sorbents · CPC title
Removal of treatment agents after treatment · CPC title
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