METHOD FOR DEGRADING ANTIBIOTICS BY AQUEOUS PHASE TRANSFER CATALYSIS USING AN ANIONIC LIQUID AND HYDROGEN PEROXIDE

Abstract

Disclosed is a method for degrading antibiotics by aqueous phase transfer catalysis using an anionic liquid and hydrogen peroxide, including: adding hydrogen peroxide to a wastewater containing the antibiotics to obtain a first mixture, and adjusting a pH of the first mixture to 3-4 to form an aqueous phase, and adding a catalyst to a water-insoluble ionic liquid to obtain a second mixture, and stirring the second mixture to form an ionic liquid phase, wherein the catalyst is selected from the group consisting of ferrocene, iron dodecyl sulfonate, ferrous dodecyl sulfonate, and copper dodecyl sulfonate; and mixing the aqueous phase and the ionic liquid phase in a volume ratio of (8-11):1 to obtain a mixed phase, and stirring the mixed phase to degrade the antibiotics.

Claims

1. A method for degrading antibiotics by aqueous phase transfer catalysis using an anionic liquid and hydrogen peroxide, comprising: step 1, adding hydrogen peroxide to a wastewater containing the antibiotics to obtain a first mixture, and adjusting a pH of the first mixture to 3-4 to form an aqueous phase; and adding a catalyst to a water-insoluble ionic liquid to obtain a second mixture, and stirring the second mixture to form an ionic liquid phase, wherein the catalyst is selected from the group consisting of ferrocene, iron dodecyl sulfonate, ferrous dodecyl sulfonate and copper dodecyl sulfonate; and step 2, mixing the aqueous phase and the ionic liquid phase obtained in step 1 in a volume ratio of (8-11):1 to obtain a mixed phase, and stirring the mixed phase to degrade the antibiotics.

2. The method of claim 1, wherein a concentration of the antibiotics in the aqueous phase is in a range of 0.05-0.2 mmol/L, a concentration of hydrogen peroxide in the aqueous phase is in a range of 10-30 mmol/L, and a concentration of the catalyst in the ionic liquid phase is in a range of 25-50 mmol/L.

3. The method of claim 1, wherein, in step 1, the stirring is performed at ambient temperature for 30-60 min.

4. The method of claim 1, wherein, in step 2, the stirring is performed for 0.5-5 hours.

5. The method of claim 1, wherein the ionic liquid is an ionic compound composed of anions and cations, and the ionic liquid is insoluble in water and compatible with catalysts.

Description

DETAILED DESCRIPTION OF THE EMBODIMENTS

[0015] The present disclosure is further described below in conjunction with examples, and does not be limited in any way. Any variations or replacement made based on the teachings of the present disclosure should fall within the protection scope of the present disclosure.

[0016] The present disclosure provides a method for degrading antibiotics by aqueous phase transfer catalysis using an anionic liquid and hydrogen peroxide, comprising:

[0017] step 1, adding hydrogen peroxide to the wastewater containing the antibiotics to obtain a first mixture, and adjusting a pH of the first mixture to 3-4 to form an aqueous phase, wherein the pH of the first mixture may be adjusted by a pH regulator well known to those skilled in the art, such as sulfuric acid and sodium hydroxide; and

[0018] adding a catalyst to a water-insoluble ionic liquid to obtain a second mixture, and stirring the second mixture to form an ionic liquid phase, wherein the catalyst is selected from the group consisting of ferrocene, iron dodecyl sulfonate, ferrous dodecyl sulfonate and copper dodecyl sulfonate; and

[0019] step 2, mixing the aqueous phase and the ionic liquid phase obtained in step 1 in a volume ratio of (8-11):1 to obtain a mixed phase, and stirring the mixed phase to degrade the antibiotics.

[0020] In some embodiments, a concentration of the antibiotics in the aqueous phase is in a range of 0.05-0.2 mmol/L, a concentration of hydrogen peroxide in the aqueous phase is in a range of 10-30 mmol/L, and a concentration of the catalyst in the ionic liquid phase is in a range of 25-50 mmol/L.

[0021] In some embodiments, in step 1, stirring the second mixture is performed at ambient temperature for 30-60 min.

[0022] In some embodiments, in step 2, the stirring is performed for 0.5-5 hours.

[0023] In some embodiments, the ionic liquid is an ionic compound composed of an anion and a cation, and is insoluble in water and compatible with catalysts, wherein the cation is an alkyl imidazolium cation, such as EMIM.sup.+ and BMIM.sup.+, and the anion is BF.sub.4.sup.− or PF.sub.6.sup.−. For example, the ionic liquid may be 1-octyl-3-methylimidazolium hexafluorophosphate (OMImPF.sub.6).

[0024] The present disclosure will be further described with reference to Examples 1-9.

Example 1

[0025] 1-octyl-3-methylimidazolium hexafluorophosphate (OMImPF.sub.6) was selected as an ionic liquid (IL) and poured into a quartz tube. Ferrocene was selected as a catalyst and added into the quartz tube. The resulting mixture in the quartz tube was magnetically stirred at ambient temperature for 30 minutes to obtain an ionic liquid phase, wherein a concentration of the catalyst in the ionic liquid phase is 25 mmol/L. A wastewater containing sulfamethoxazole (SMX) and a H.sub.2O.sub.2 solution with a concentration of 3% (i.e. a solution of 3 g hydrogen peroxide in 100 g water) were poured into a volumetric flask, deionized water was added to make a volume constant, and a pH of the resulting solution was adjusted to 3 to form an aqueous phase, wherein a concentration of sulfamethoxazole in the aqueous phase is 0.05 mmol/L, and a concentration of H.sub.2O.sub.2 in the aqueous phase is 10 mmol/L. 50 mL of the aqueous phase and 5 mL of the ionic liquid phase were mixed and stirred at ambient temperature for 30 minutes. The resulting mixture was then stood for 10 minutes to collect an upper aqueous phase, and the upper aqueous phase was subjected to a chromatographic analysis. The results show that a degradation efficiency of sulfamethoxazole in the aqueous phase is 97.2%.

Example 2

[0026] 1-octyl-3-methylimidazolium hexafluorophosphate (OMImPF.sub.6) was selected as an ionic liquid (IL) and poured into a quartz tube. Ferrocene was selected as a catalyst and added into the quartz tube. The resulting mixture in the quartz tube was magnetically stirred at ambient temperature for 30 minutes to obtain an ionic liquid phase, wherein the ionic liquid phase has a concentration of the catalyst of 50 mmol/L. A wastewater containing sulfamethoxazole (SMX) and a H.sub.2O.sub.2 solution with a concentration of 3% were poured into a volumetric flask, deionized water was added to make a volume constant, and a pH of the resulting solution was adjusted to 5 to form an aqueous phase, wherein the aqueous phase has a concentration of sulfamethoxazole of 0.2 mmol/L, and a concentration of H.sub.2O.sub.2 of 30 mmol/L. 50 mL of the aqueous phase and 5 mL of the ionic liquid phase were mixed and stirred at ambient temperature for 5 hours. The resulting mixture was then stood for 10 minutes to collect an upper aqueous phase, and the upper aqueous phase was subjected to a chromatographic analysis. The results show that a degradation efficiency of sulfamethoxazole in the aqueous phase is 84.6%.

Example 3

[0027] 1-octyl-3-methylimidazolium hexafluorophosphate (OMImPF.sub.6) was selected as an ionic liquid (IL) and poured into a quartz tube. Ferrocene was selected as a catalyst and added into the quartz tube. The resulting mixture in the quartz tube was magnetically stirred at ambient temperature for 30 minutes to obtain an ionic liquid phase, wherein the ionic liquid phase has a concentration of the catalyst of 35 mmol/L. A wastewater containing sulfamethoxazole (SMX) and a H.sub.2O.sub.2 solution with a concentration of 3% were poured into a volumetric flask, deionized water was added to make a volume constant, and a pH of the resulting solution was adjusted to 4 to form an aqueous phase, wherein the aqueous phase has a concentration of sulfamethoxazole of 0.125 mmol/L, and a concentration of H.sub.2O.sub.2 of 20 mmol/L. 50 mL of the aqueous phase and 5 mL of the ionic liquid phase were mixed and stirred at ambient temperature for 5 hours. The resulting mixture was then stood for 10 minutes to collect an upper aqueous phase, and the upper aqueous phase was subjected to a chromatographic analysis. The results show that a degradation efficiency of sulfamethoxazole in the aqueous phase is 91.6%.

Example 4

[0028] 1-octyl-3-methylimidazolium hexafluorophosphate (OMImPF.sub.6) was selected as an ionic liquid (IL) and poured into a quartz tube. Ferrocene was selected as a catalyst and added into the quartz tube. The resulting mixture in the quartz tube was magnetically stirred at ambient temperature for 30 minutes to obtain an ionic liquid phase, wherein the ionic liquid phase has a concentration of the catalyst of 25 mmol/L. A wastewater containing sulfamethazine (SMZ) and a H.sub.2O.sub.2 solution with a concentration of 3% were poured into a volumetric flask, deionized water was added to make a volume constant, and a pH of the resulting solution was adjusted to 3 to form an aqueous phase, wherein the aqueous phase has a concentration of sulfamethazine of 0.05 mmol/L, and a concentration of H.sub.2O.sub.2 of 10 mmol/L. 50 mL of the aqueous phase and 5 mL of the ionic liquid phase were mixed and stirred at ambient temperature for 5 hours. The resulting mixture was then stood for 10 minutes to collect an upper aqueous phase, and the upper aqueous phase was subjected to a chromatographic analysis. The results show that a degradation efficiency of sulfamethazine in the aqueous phase is 96.4%.

Example 5

[0029] 1-octyl-3-methylimidazolium hexafluorophosphate (OMImPF.sub.6) was selected as an ionic liquid (IL) and poured into a quartz tube. Iron dodecyl sulfonate was selected as a catalyst and added into the quartz tube. The resulting mixture in the quartz tube was magnetically stirred at ambient temperature for 30 minutes to obtain an ionic liquid phase, wherein a concentration of the catalyst in the ionic liquid phase is 30 mmol/L. Iron dodecyl sulfonate was prepared by the following steps: a solution of sodium dodecyl sulfonate and a solution of ferric chloride were heated to a temperature of 70° C. and then mixed to obtain a mixed solution. The mixed solution was naturally cooled to ambient temperature to generate a precipitate. The precipitate was filtered by a water-based filter membrane, washed 3 times by water, and dried by a freeze dryer to obtain iron dodecyl sulfonate. A wastewater containing sulfamethazine (SMZ) and a H.sub.2O.sub.2 solution with a concentration of 3% were poured into a volumetric flask, deionized water was added thereto to make a volume constant, and a pH of the resulting solution was adjusted to 3 to form an aqueous phase, wherein a concentration of sulfamethazine in the aqueous phase is 0.1 mmol/L, and a concentration of H.sub.2O.sub.2 in the aqueous phase is 20 mmol/L. 50 mL of the aqueous phase and 5 mL of the ionic liquid phase were mixed and stirred at ambient temperature for 1 hour. The resulting mixture was then stood for 10 minutes, to collect an upper aqueous phase, and the upper aqueous phase was then subjected to a chromatographic analysis. The results show that a degradation efficiency of sulfamethazine in the aqueous phase is 92.3%.

Example 6

[0030] 1-octyl-3-methylimidazolium hexafluorophosphate (OMImPF.sub.6) was selected as an ionic liquid (IL) and poured into a quartz tube. Iron dodecyl sulfonate was selected as a catalyst and added into the quartz tube. The resulting mixture in the quartz tube was magnetically stirred at ambient temperature for 30 minutes to obtain an ionic liquid phase, wherein the ionic liquid phase has a concentration of the catalyst of 50 mmol/L. Iron dodecyl sulfonate was prepared by the following steps: a solution of sodium dodecyl sulfonate and a solution of ferric chloride were heated to a temperature of 70° C. and then mixed to obtain a mixed solution. The mixed solution was naturally cooled to ambient temperature to generate a precipitate. The precipitate was filtered by a water-based filter membrane, washed 3 times by water, and dried by a freeze dryer to obtain iron dodecyl sulfonate. A wastewater containing sulfamethazine (SMZ) and a H.sub.2O.sub.2 solution with a concentration of 3% were poured into a volumetric flask, deionized water was added thereto to make a volume constant, and a pH of the resulting solution was adjusted to 3.5 to form an aqueous phase, wherein the aqueous phase has a concentration of sulfamethazine of 0.2 mmol/L, and a concentration of H.sub.2O.sub.2 of 30 mmol/L. 50 mL of the aqueous phase and 5 mL of the ionic liquid phase were mixed and stirred at ambient temperature for 2.5 hours. The resulting mixture was then stood for 10 minutes, to collect an upper aqueous phase, and the upper aqueous phase was then subjected to a chromatographic analysis. The results show that a degradation efficiency of sulfamethazine in the aqueous phase is 93.4%.

Example 7

[0031] 1-octyl-3-methylimidazolium hexafluorophosphate (OMImPF.sub.6) was selected as an ionic liquid (IL) and poured into a quartz tube. Copper dodecyl sulfonate was selected as a catalyst and added into the quartz tube. The resulting mixture in the quartz tube was magnetically stirred at ambient temperature for 30 minutes to obtain an ionic liquid phase, wherein the ionic liquid phase has a concentration of the catalyst of 40 mmol/L. Copper dodecyl sulfonate was prepared by the following steps: a solution of sodium dodecyl sulfonate and a solution of copper chloride were heated to a temperature of 70° C. and then mixed to obtain a mixed solution. The mixed solution was naturally cooled to ambient temperature to generate a precipitate. The precipitate was filtered by a water-based filter membrane, washed 3 times by water, and dried by a freeze dryer to obtain copper dodecyl sulfonate. A wastewater containing sulfamethazine (SMZ) and a H.sub.2O.sub.2 solution with a concentration of 3% were poured into a volumetric flask, deionized water was added thereto to make a volume constant, and a pH of the resulting solution was adjusted to 3 to form an aqueous phase, wherein the aqueous phase has a concentration of sulfamethazine of 0.05 mmol/L, and a concentration of H.sub.2O.sub.2 of 15 mmol/L. 50 mL of the aqueous phase and 5 mL of the ionic liquid phase were mixed and stirred at ambient temperature for 3 hours. The resulting mixture was then stood for 10 minutes, to collect an upper aqueous phase, and the upper aqueous phase was then subjected to a chromatographic analysis. The results show that a degradation efficiency of sulfamethazine in the aqueous phase is 94.1%.

Example 8

[0032] 1-octyl-3-methylimidazolium hexafluorophosphate (OMImPF.sub.6) was selected as an ionic liquid (IL) and poured into a quartz tube. Ferrocene was selected as a catalyst and added into the quartz tube. The resulting mixture in the quartz tube was magnetically stirred at ambient temperature for 45 minutes to obtain an ionic liquid phase, wherein the ionic liquid phase has a concentration of the catalyst of 37.5 mmol/L. A wastewater containing sulfamethazine (SMZ) and a H.sub.2O.sub.2 solution with a concentration of 3% were poured into a volumetric flask, deionized water was added thereto to make a volume constant, and a pH of the resulting solution was adjusted to 3 to form an aqueous phase, wherein the aqueous phase has a concentration of sulfamethazine of 0.125 mmol/L, and a concentration of H.sub.2O.sub.2 of 20 mmol/L. 40 mL of the aqueous phase and 5 mL of the ionic liquid phase were mixed and stirred at ambient temperature for 2.75 hours.

Example 9

[0033] 1-octyl-3-methylimidazolium hexafluorophosphate (OMImPF.sub.6) was selected as a ionic liquid (IL) and poured into a quartz tube. Ferrous dodecyl sulfonate was selected as a catalyst and added into the quartz tube. The resulting mixture in the quartz tube was magnetically stirred at ambient temperature for 60 minutes to obtain an ionic liquid phase, wherein the ionic liquid phase has a concentration of the catalyst of 40 mmol/L. Ferrous dodecyl sulfonate was prepared by the following steps: a solution of sodium dodecyl sulfonate and a solution of ferrous chloride were heated to a temperature of 70° C. and then mixed to obtain a mixed solution. The mixed solution was naturally cooled to ambient temperature to generate a precipitate. The precipitate was filtered by a water-based filter membrane, washed 3 times by water, and dried by a freeze dryer to obtain ferrous dodecyl sulfonate. A wastewater containing sulfamethazine (SMZ) and a H.sub.2O.sub.2 solution with a concentration of 3% were poured into a volumetric flask, deionized water was added thereto to make a volume constant, and a pH of the resulting solution was adjusted to 4 to form an aqueous phase, wherein the aqueous phase has a concentration of sulfamethazine of 0.15 mmol/L, and a concentration of H.sub.2O.sub.2 of 25 mmol/L. 55 mL of the aqueous phase and 5 mL of the ionic liquid phase were mixed and stirred at ambient temperature for 2 hours.