TREATMENT METHOD FOR INDIGO-CONTAINING WASTEWATER BY COMBINED ADSORPTION AND REGENERATION PROCESS

Abstract

An integrative approach combines a process of adsorption and ozonation which are used for removing the indigo dye from textile wastewater and the regeneration of adsorbent materials. Metal oxide modified adsorbents are efficient dye adsorbent materials for indigo dye wastewater and are used have been developed for adsorption process and regenerated by ozonation process. Upon the regeneration process, the adsorption capacity has been recovered. The synergistic effect of adsorption and ozonation benefit for the efficient dye removal from wastewater and the adsorbent regeneration achieved in an environmentally friendly and cost effective way.

Claims

1. A method of treating indigo-containing wastewater to remove indigo from said wastewater comprising the steps of: 1) exposing the wastewater to an adsorbent capable of adsorbing the indigo for a sufficient period of time for the indigo to be adsorbed; and 2) regenerating the indigo-saturated adsorbent of step 1 by exposing to ozone for a sufficient period of time for the decomposition of the indigo dye adsorbed.

2. The method for adsorption process for indigo-containing wastewater according to claim 1, wherein the adsorbent in adsorption process is a metal oxide modified adsorbent carrier.

3. The method for adsorption process for indigo-containing wastewater according to claim 1, wherein the adsorbent carrier is formed from silica, alumina, clays, titanium oxide, boron oxide or zirconia.

4. The method for adsorption process for indigo-containing wastewater according to claim 1, wherein the metal oxide in adsorbent carrier is selected from the group consisting of iron oxide, aluminium oxide, manganese oxide, titanium oxide and copper oxide, or mixtures thereof.

5. The method for adsorption process for indigo-containing wastewater according to claim 1, wherein the adsorbent carrier has an average particle size of 1 mm to 10 mm, and has a micro-mesoporous structure with an adsorption capacity average 30 mg/g to 100 mg/g.

6. The method for regeneration process for indigo-containing wastewater according to claim 1, wherein the regeneration process is an ozone-based technology.

7. The method for regeneration process for indigo-containing wastewater according to claim 1, wherein the ozonated water is generated by ozone generator and micro-nano bubbler device.

8. A system for treating indigo-containing wastewater, comprising: a peristaltic pump which pumps out indigo-containing wastewater; an adsorption column filling with an adsorbent, to remove indigo dyes in wastewater; and outputs effluent; an ozone generator; a micro-nano bubbler; a flow controller; an ozone analyzer; and an ozone destructor for the removal of residual gaseous ozone from regeneration process; wherein the metal oxide modified adsorbent carrier is added to the indigo-containing wastewater in the reaction column, indigo in the wastewater is adsorbed on the metal oxide modified adsorbent, and the metal oxide modified adsorbent having indigo adsorbed thereon is treated and regenerated with the ozone micro-nano bubbler.

9. The system of claim 8 wherein the adsorbent is Fe alumina.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0009] These and/or other aspects and advantages of the invention will become apparent and more readily appreciated from the following description of the embodiments, taken in conjunction with the accompanying drawings of which:

[0010] FIG. 1 is a schematic diagram of an adsorption and regeneration system that is used to treat indigo-containing wastewater.

[0011] FIG. 2 shows Brunauer-Emmett-Teller (BET) surface analysis results of alumina (Al.sub.2O.sub.3) and iron-doped alumina (Fe-alumina, from alumina impregnated in 0.1M Fe(NO.sub.3).sub.3 solution).

[0012] FIG. 3A is an SEM (scanning electron microscope) image of alumina and FIG. 3B is an SEM image of Fe-alumina.

[0013] FIG. 4 is an XRF spectrum for 0.1M Fe-alumina.

[0014] FIGS. 5A to 5D show a column adsorption process with respect to time, from left to right.

[0015] FIG. 6 shows a breakthrough curve of Fe-alumina with a 2000 ppm indigo solution.

[0016] FIG. 7 shows an ozone regeneration process of indigo dye-saturated Fe-alumina in a glass adsorption column.

[0017] FIG. 8 is a chart of regeneration efficiency of Fe-alumina.

[0018] FIG. 9 is a chart of regeneration time of Fe-alumina.

DETAILED DESCRIPTION OF THE EMBODIMENTS

[0019] Reference will now be made in detail to the present embodiments of the present invention, examples of which are illustrated in the accompanying drawings, wherein like reference numerals refer to the like elements throughout. The embodiments are described below in order to explain the present invention by referring to the figures.

[0020] Aspects of the invention relate to a treatment process for the indigo-containing wastewater by a combined adsorption and ozonation process. Indigo-containing wastewater is first treated by primary process (for example, screening and/or sedimentation) and secondary process (for example, aerobic or anaerobic digestion, coagulation, flocculation). The combined adsorption and ozonation treatment process provides a tertiary treatment process using a combined adsorption and regeneration treatment process as a solution. An integrative approach is provided in which combined process of adsorption and ozonation coupled with a micro-nano-bubbler are used for removing the indigo dye from textile wastewater and the adsorbent materials with regeneration properties have been developed. As a result, an adsorption capacity of adsorbent materials is restored. Coupled with the micro-nano-bubbler device, prolonging the retention of the ozone in the aqueous phase has resulted in better regeneration efficiency.

[0021] In the adsorption treatment process disclosed herein, a metal-oxide modified adsorbent is modified with metal catalysts by impregnation-calcination procedures. The metal supported adsorbent could act as both an adsorbent and a catalyst. The indigo dye is adsorbed onto micro- and/or mesopores of the adsorbent while a neighbor metal catalyst facilitates ozone to generate hydroxyl radicals. This is a highly efficient method and system for degradation of indigo dye and regenerates the adsorbent for reuse. In an embodiment of the regeneration process, ozonated water produced by dissolving ozone in water is used to degrade indigo in adsorbent and regenerate the adsorbent. The regeneration cycle could be retained at least 80% for 10 cycles. While coupled with a micro-nano-bubbler device, the prolonged retention of ozone in an aqueous phase has resulted in better regeneration efficiency. The overall process provides a more cost-effective and environmentally friendly way for treating the indigo-containing wastewater. It is to be noted that the disclosed combined adsorption and regeneration process is also suitable for the treatment of other types of dye wastewater.

[0022] Schematic diagram of adsorption and regeneration system.

[0023] Preparation of Fe-alumina.

[0024] Commercial alumina (Al.sub.2 has been used for the development of the modified alumina. Alumina (size: 1.4-1.8 mm, by Sasol) modified with iron metal are prepared by impregnation-calcination method. Alumina is first soaked in 0.1M of iron (III) nitrate (Fe(NO.sub.3).sub.3) solution for 18 hours under room temperature and pressure. The impregnated alumina is then filtered under room temperature and pressure, dried in oven at 100 to 105 deg. C. for 24 hours, and subsequently calcinated at 400 deg. C. for 4 hours.

[0025] FIG. 1 is a schematic illustration of an adsorption and regeneration system, which is numbered 02 and 04, respectively, according to an embodiment of the present invention. Adsorption system 02 includes one adsorption column 14 packed with adsorbent, which is Fe-Alumina. It also includes a wastewater feed 10 and a peristaltic pump 12 in flow communication with, adsorption column 14. In an adsorption treatment process 2, wastewater 10 is fed to a peristaltic pump 12. Dye-containing wastewater 10 is then fed to an adsorption column 14 which outputs effluent 16.

[0026] For adsorbent regeneration process 04, it includes an ozone generator 20, which generates ozone from an oxygen source 18, an ozonation chamber 26, an ozone analyser 28 and an ozone destructor 30. In a regeneration treatment process 04, oxygen 18 is provided to an ozone generator to generate ozone, which subsequently mixes with water at a micro-nano bubbler 22 where ozone stream is sheared and break into a number of micro- and nano-sized bubbles through turbulence induced by flowing water. The flow to the ozonation chamber 26, which is in fact the same adsorption column 14, is regulated by a flow controller 24. Residual ozone from the ozonation chamber 26 is directed to an ozone analyser 28 and further to an ozone destructor 30. Filling with metal catalyst, the ozone destructor 30 converts ozone gas to oxygen before releasing in the atmosphere.

[0027] The regeneration efficiency (RE %) is defined as ratio of the amount of dye (mg) removed per gram of regenerated adsorbent after one adsorption-regeneration cycle (q.sub.reg), to the amount of dye (mg) removed per gram of fresh adsorbent (q.sub.fresh). It is defined as below:

[00001]$RE\%=\left(q_{\mathrm{reg}}/q_{\mathrm{fresh}}\right)100$

[0028] FIG. 2 shows Brunauer-Emmett-Teller (BET) surface area analysis results of Alumina (Al.sub.2O.sub.3). The alumina after impregnated with 0.1M iron (III) nitrate (Fe(NO.sub.3).sub.3) aqueous solution and calcination is known as Fe-alumina. The decrease in pore volume after impregnation-calcination suggests some pores over Fe-alumina surface area occupied by iron oxides.

[0029] FIGS. 3A and 3B are SEM images of alumina (Al.sub.2O.sub.3) and iron-doped alumina (Fe-alumina). In FIG. 3B, the light-coloured, small-size deposits over Fe-alumina surface and at the edge of pore openings indicate the presence of iron oxides.

[0030] FIG. 4 is an XRF spectrum for 0.1M Fe-alumina. Major emission peaks in the range of 5 to 10 keV indicate the presence of iron metal.

[0031] FIGS. 5A to 5D show a column adsorption process with respect to time, from left to right. (5A) Dye effluent enters the column in the down-flow manner. Dye is adsorbed effectively by the upper few layers of the fresh Fe-alumina. (5B) When more dye is adsorbed, some are readily escaped in the lower strata of the bed. The upper layer of Fe-alumina is gradually saturated. (5C) Fe-alumina continues to adsorb dye. The lower layer of Fe-alumina starts to turn blue. (5D) The adsorbent is close to completely saturated.

[0032] FIG. 6 shows a breakthrough curve of Fe-alumina with a 2000 ppm indigo solution. Breakthrough curve is a plot of the dye concentration in the column effluent as a function of time. At adsorption time (t) is zero, indigo-containing effluent enters the column at the top at concentration C.sub.0. The effluent dye concentration (C) increases with time, and eventually attains equilibrium (C/C.sub.0 closes to 1) when most adsorbent is saturated with dye. The breakthrough time, which is defined as C/C.sub.0 over 0.05, is about 36 minutes. Experimental data is fitted with Thomas model which the expression for an adsorption column is shown as below (Selambakkannu S. et al., SN Applied Sciences (2019) 1:175):

[00002]$\ln \left(\frac{C_o}{C}-1\right)=\frac{k_{\mathrm{Th}}{q}_{o}w}{Q}-k_{\mathrm{Th}}{C}_{o}t$ [0033] where C.sub.0 is the influent dye concentration (mg/L), C is the effluent dye concentration (mg/L), K.sub.Th represents Thomas model constant (mL/(min. mg)), q.sub.o is the equilibrium adsorption amount of dye, indigo on Fe-alumina (mg/g), w is the mass of the Fe-alumina (g) and Q is the flow rate (mL/min).

[0034] FIGS. 7A and 7B show an ozone regeneration process of dye-saturated Fe-alumina packed in a glass adsorption column, from left to right. FIG. 7A) is the dye-saturated Fe-alumina before ozone regeneration. FIG. 7B) shows that, after exposed to ozonated water for 2 hours, dye adsorbed onto Fe-alumina are decomposed by ozone and hydroxyl radicals from ozone. The Fe-alumina shows brown colour similar to the colour before adsorption, indicating the recovery of adsorption capacity.

[0035] FIG. 8 is a chart of regeneration efficiency of Fe-alumina. After 10 adsorption and regeneration cycles, the regeneration efficiency is retained at over 90%. For each regeneration, it takes about 40 minutes to regenerate about 3 grams of dye-saturated Fe-alumina.

[0036] FIG. 9 is a chart showing regeneration time of Fe-alumina. The regeneration efficiency is found to increase with time. At the ozone dosage of about 6 to 7 mg/min, the regeneration efficiency attains about 60% after 20 minutes of continuous exposure of ozonated water, and further increases to over 90% after 40 minutes.

[0037] Many of the commonly used adsorbent for dye removal from wastewater, for example, activated carbon, are difficult to recover and recycle, and suffer from high activation and regeneration costs. The disposal of spent adsorbent is rather costly but is also hazardous to the environment.

[0038] The adsorbent in the present invention, which is, Fe-alumina, offers a unique advantage because of its effectiveness on removing organic compounds (e.g., dyes) from wastewater and also the ease of reusability. By ozonation, dyes adsorbed are decomposed either by direct oxidation in the presence of molecular ozone, or by indirect oxidation with hydroxyl radicals (OH*) that are generated from the decomposition of ozone which is catalyzed by Fe.sup.2+ on the surface of Fe-alumina. After ozone regeneration, the adsorption capacity of Fe-alumina is recovered as dyes adsorbed are already decomposed. Compared with conventional regeneration techniques, such as thermal and chemical (e.g., solvent washing) regeneration, one advantage of the present invention is that on-site regeneration of spent adsorbents and destruction of adsorbed organic material (e.g., dye) is provided. Another advantage of the present invention is that the adsorbed organic material (e.g., dye) is destroyed or decomposed to non-toxic forms such as carbon dioxide (CO.sub.2) and water (H.sub.2O). As no residue (e.g., sludge containing metal ions) is generated at the end of wastewater process, the present invention will not incur secondary pollution due to discharge of sludge or used solvent. Still another advantage of the present invention is that the adsorbents can be used and reused for multiple adsorption/regeneration cycles. The examples which follow are merely illustrative, and should not be construed to be any sort of limitation on the Scope of the claimed invention.

Example 1 In-Situ Regeneration of Spent Adsorbent Using Ozonation

[0039] In this example, spent adsorbent was prepared. More specifically, in this example, approximately 25 to 30 grams of Fe-alumina was loaded to a glass column having a diameter pf 2 cm and a height of 16 cm. The bed height was approximately 10 cm. Indigo dye solution at a concentration of about 90 to 110 mg/L, was directed to the column in downflow manner, by a peristatic pump, at a flow rate of about 3 to 5 mL/min for approximately 30 to 40 minutes at a room temperature (approximately 21 to 26 C.). After loaded with indigo until exhausted, the Fe-alumina was regenerated in the same column where ozonated water (gaseous ozone concentration: approximately 10 to 20 g/m3) was directed through the column in an upflow manner at conditions at a flow rate of about 200 to about 400 mL/min for approximately 2 hours.

Example 2 Reuse of Regenerated Fe-Alumina

[0040] The adsorbent (e.g., Fe-alumina) would have to be reused several times in order to enhance the economic benefits of the above-described processes. A set of tests was conducted in which the same Fe-alumina was used for about 10 cycles. A full cycle includes an adsorption step and a regeneration step. Each test was completed in the same column.

[0041] FIG. 8 plots the amount of regeneration efficiency of Fe-alumina through ten sequential, adsorption-regeneration cycles. Ozonation was effective at decomposing the adsorbates from the spent Fe-alumina, whereas the regeneration efficiency was restored to over 92% of its initial capacity.

[0042] Although a few embodiments of the present invention have been shown and described, it would be appreciated by those skilled in the art that changes may be made in this embodiment without departing from the principles and spirit of the invention, the scope of which is defined in the claims and their equivalents.