KR101672234B1 - Chitosan-melamine composite of eliminating posphorus and manufacturing method thereof - Google Patents

Abstract

The present invention relates to a chitosan-melamine complex for phosphorus removal and a method for producing the chitosan-melamine complex. More particularly, the present invention relates to a chitosan-melamine complex for preparing a chitosan-melamine solution by mixing melamine and chitosan powder in an acid solution. Preparing chitosan-melamine beads by titrating the chitosan-melamine solution; And mixing the chitosan-melamine beads with a transition metal aqueous solution to induce a chelate bond between the amine group and the transition metal ion of the chitosan-melamine bead, whereby the polymer and the transition metal in the chitosan- Melamine complex which is capable of selectively removing phosphorus regardless of the presence or absence of competitive ions in the water and which has excellent durability, and a method for producing the phosphorus-removing chitosan- .

Description

[0001] CHITOSAN-MELAMINE COMPOSITE OF ELIMINATING POSPHORUS AND MANUFACTURING METHOD THEREOF [0002]

The present invention relates to a phosphorus-removing chitosan-melamine complex having excellent selectivity to phosphorus and durability, and a method for producing the same.

Phosphorus (P) is known to be a factor that causes eutrophication of lakes, reservoirs and rivers even at low concentrations.

Methods for removing such phosphorus include physical methods such as electrodialysis, reverse osmosis membrane, filtration, adsorption and crystallization; Biological methods using activated sludge process, A2O and SBR; And physico-chemical methods such as coagulation-sedimentation. Biological methods and coagulation-precipitation methods are widely used.

The above physical methods have disadvantages of excessive facility cost and high operating cost.

Such biological methods are difficult to adapt to the required water quality due to high operating conditions such as adaptation time of microorganisms, anaerobic and aerobic conditions, and high water quality after treatment of several mg-P / L (Korean Patent No. 422,211).

Despite the advantages of simplicity of process and high removal efficiency, the coagulation-precipitation method has a disadvantage in that a large amount of chemicals are required for a water containing phosphorus at a low concentration and an additional cost is required for treatment of the generated sludge. There is also a limit to meeting the tolerance standards of a person who is constantly being strengthened.

Therefore, a method of using an ion exchange resin to remove phosphorus at a low concentration has been proposed.

Ion exchange resin has advantages such as ease of operation, ease of ion removal and regeneration at a low concentration, and is widely used for removing specific pollutants (Korean Patent No. 967,587).

However, since the selectivity to the resin is determined by the electrostatic force of the anions present in the water, the selectivity of the sulfate is the most excellent. That is, when the concentration of sulfate in water is high, the removal efficiency of phosphorus is lowered. Conversely, when the concentration of sulfate is low, the removal efficiency of phosphorus is increased.

Therefore, frequent regeneration of the anion exchange resin is required and, as a result, phosphorus removal efficiency is deteriorated due to short operating time.

It is an object of the present invention to provide a phosphorus-removing chitosan-melamine complex capable of effectively removing phosphorus regardless of the presence or absence of competitive ions in the water by increasing the selectivity to phosphorus.

It is another object of the present invention to provide a method for producing the chitosan-melamine complex for removing phosphorus.

In order to accomplish the above object, the present invention provides a method for producing a chitosan-melamine solution, which comprises mixing an acid solution with melamine and chitosan powder to prepare a chitosan-melamine solution; Preparing chitosan-melamine beads by titrating the chitosan-melamine solution; And mixing the chitosan-melamine beads with a transition metal aqueous solution to induce a chelate bond between the amine group and the transition metal ion of the chitosan-melamine bead. to provide.

The chelate bond may cross-link the polymer and the transition metal ion in the chitosan-melamine bead, and the transition metal ion may function as a functional group capable of ligand bonding.

The acid solution may be an aqueous hydrochloric acid solution.

The chitosan-melamine mixture may contain 1 to 3% by weight of chitosan powder and 1 to 3% by weight of melamine powder.

The transition metal aqueous solution may contain cupric chloride (CuCl ₂ .2H ₂ O), nickel chloride hydrate (NiCl ₂ .6H ₂ O), or a mixture thereof.

The aqueous solution containing the cupric chloride hydrate may have a pH of 4 to 5 and a concentration of 1 to 2% by weight.

The aqueous solution containing the nickel chloride hydrate (NiCl ₂ .6H ₂ O) may have a pH of 5 to 7 and a concentration of 0.2 to 0.6 wt%.

The present invention also relates to a composite in which an amine group and a transition metal ion of chitosan-melamine beads are chelated, wherein the polymer and the transition metal ion in the chitosan-melamine bead are crosslinked by the chelate bond and the transition metal ion is capable of ligand bonding Wherein the chitosan-melamine complex acts as a group.

The chitosan-melamine complex for phosphorus removal according to the present invention is excellent in selectivity to phosphorus and has an advantage that phosphorus can be selectively removed irrespective of presence or absence of competitive ions in the water.

In addition, the chitosan-melamine complex for phosphorus removal according to the present invention is advantageous in that the polymer and transition metal ion in the chitosan-melamine bead are crosslinked to have excellent physical strength and durability.

In addition, the chitosan-melamine complex for phosphorus removal according to the present invention has an advantage of being easily applied to a continuous process of sewage or wastewater treatment for phosphorus removal.

1 shows results of adsorption experiments of respective anions in water using the beads of Example 1 and Comparative Example 1 according to the present invention.

The present invention relates to a phosphorus-removing chitosan-melamine complex having excellent selectivity to phosphorus and durability, and a method for producing the same.

Hereinafter, the present invention will be described in detail.

The method for preparing a chitosan-melamine complex for removing phosphorus according to the present invention comprises the steps of: preparing a chitosan-melamine solution by mixing melamine and chitosan powder with an acid solution; Preparing chitosan-melamine beads by titrating the chitosan-melamine solution; And mixing the chitosan-melamine bead with a transition metal aqueous solution to induce a chelate bond between the amine group of the chitosan-melamine bead and the transition metal ion.

The chelate bond cross-links the polymer and the transition metal ion in the chitosan-melamine bead, and the transition metal ion acts as a functional group capable of ligand bonding.

In the present invention, the amine group (-NH ₂ ) of the chitosan-melamine bead is chelated with the transition metal ion to fix the transition metal ion to the chitosan-melamine bead. The fixed transition metal ion functions as a phosphate-adsorbing functional group and is ligand-bonded to a phosphate in water.

That is, in order to increase the adsorption amount of the phosphate, the amount of the transition metal ions fixed to the chitosan-melamine beads must be increased, and in order to increase the amount of the transition metal ions to be fixed, the number of the amine groups in the beads must be increased.

The present invention is characterized in that transition metal ions are fixed by using beads mixed with melamine together with chitosan to increase the number of amine groups in the beads.

In addition, since the polymer in the chitosan-melamine bead is crosslinked by the chelate bond with the transition metal, the physical strength is improved compared to the bead containing the chitosan alone.

The process for preparing the chitosan-melamine complex for removing phosphorus according to the present invention will be described below.

First, melamine and chitosan powder are mixed with an acid solution to prepare a chitosan-melamine solution.

The chitosan powder is a deacetylation substance of chitin, a linear structure of the glucosamine unit, and has an amine group (-NH ₂ ) on its surface.

The melamine is an organic base of a heterocyclic amine and is a trimer of cyanamide.

In order to improve the solubility of such melamine, it is preferable to add an appropriate amount of sulfoxide compound. The sulfoxide compound is generally used in the art and is not particularly limited. For example, dimethylsulfoxide may be used.

The sulfoxide compound is used for dissolving melamine, and it is preferable to use the sulfoxide compound in a certain amount within a range that does not deviate from the intended effect of the present invention.

The acid solution is preferably an aqueous hydrochloric acid solution.

In this case, the chitosan-melamine solution may contain 1 to 3% by weight of chitosan powder. If the content is less than 1% by weight, the formation of beads may not be easy. If the content is more than 3% by weight, .

If the content of the melamine powder is less than 1% by weight, the amount of the melamine powder may be insufficient and the effect of containing melamine may not be obtained. If the content of the melamine powder is more than 3% by weight, It is not possible to obtain an increase in economic efficiency.

In the present invention, the transition metal is immobilized on the amine group contained in the chitosan and melamine.

Next, the chitosan-melamine beads are prepared by titrating the chitosan-melamine solution.

The titration is performed by using a basic solution in which a chitosan-melamine solution, which is an acidic solution, is cured to form a bead.

The basic solution is generally used in the art and is not particularly limited. For example, a sodium hydroxide solution may be used. At this time, it is preferable that the sodium hydroxide solution has the same concentration as the acidic solution.

Next, the chitosan-melamine beads are mixed with a transition metal aqueous solution to induce a chelate bond between the amine group of the chitosan-melamine bead and the transition metal ion.

The nitrogen (N) of the amine group (-NH ₂ ), which is a functional group of the chitosan-melamine bead, and the transition metal ion of the transition metal aqueous solution form a chelate bond through a Lewis acid base reaction. Further, the polymer inside the bead is crosslinked through the transition metal ion.

That is, the transition metal ion acts as a cross-linking agent between the polymers in the bead and functions as a ligand binding with the phosphate.

The transition metal hydrate contains a transition metal hydrate. The transition metal hydrate includes, for example, cupric chloride (CuCl ₂ .2H ₂ O), nickel chloride hydrate (NiCl ₂ .6H ₂ O) And a cupric chloride hydrate is preferable in consideration of adsorbability with a phosphate and the like.

Also, the concentration and the pH are different depending on the kind of the transition metal hydrate.

The aqueous solution containing the cupric chloride hydrate preferably has a pH of 4 to 5 and a concentration of 1 to 2% by weight. If the pH is less than 4, the hydrogen ion (H ⁺ ) increases in the aqueous solution, and the bonding strength of the amine group (-NH ₂ ) to the hydrogen ion (H ⁺ ) instead of the copper ion (Cu ²⁺ ) the protonation is promoted, which can weaken the chelate bond between the amine group and the copper ion. On the other hand, when the pH exceeds 5, OH ^- is increased in the aqueous solution, and the resulting OH ^- reacts with copper ions (Cu ²⁺ ), and copper precipitation may occur.

Furthermore, the copper ion concentration is less than 1% by weight, unreacted amine group (-NH ₂₎ is increased to indicate a low removal efficiency when it exceeds 2 weight%, forming a chelate bond with an amine group (-NH ₂₎ (Cu ^{2 +} ) Is maintained at a constant level, so that it is preferably 2% by weight or less in terms of economy.

The aqueous solution containing the nickel chloride hydrate preferably has a pH of 5 to 7 and a concentration of 0.2 to 0.6% by weight. The pH and the concentration of the aqueous solution containing the nickel chloride hydrate are optimized in consideration of the same problems as the aqueous solution containing the cupric chloride hydrate.

According to the above-mentioned method, the present invention is a complex in which an amine group and a transition metal ion of chitosan-melamine beads are chelate-bonded, the polymer and the transition metal ion in the chitosan-melamine bead are crosslinked by the chelate bond and the transition metal ion is a ligand A chitosan-melamine complex for phosphorus removal acting as a functional group capable of binding can be obtained.

The chitosan-melamine complex may be in the form of a bead having a size of 3 to 4 mm, and the removal rate of phosphate may be 80% or more.

It will be apparent to those skilled in the art that various modifications and variations can be made in the present invention without departing from the spirit or scope of the present invention. Such variations and modifications are intended to be within the scope of the appended claims.

Example  One

To 200 mL of 1 wt% HCl solution, 29.4 g of dimethyl sulfoxide and 3 g of melamine were mixed for about 3 hours or more to prepare a melamine solution of 1.5 wt%. To 200 mL of the melamine solution, 5 g of chitosan powder was mixed for 12 hours to prepare a 2.5 wt% chitosan-melamine solution. Thereafter, 2.5 wt% chitosan solution was titrated in 200 mL of 1 M sodium hydroxide aqueous solution to prepare chitosan-melamine beads. At this time, the sodium hydroxide aqueous solution of the chitosan-melamine solution was slowly stirred (80 to 100 rpm) to maintain the concentration of the aqueous sodium hydroxide solution constant, to prevent the synthesized chitosan-melamine beads from entangling, The mixture was slowly stirred for 3 hours. The chitosan-melamine beads synthesized thereafter were washed several times with distilled water.

Thereafter, 3 g of cupric chloride hydrate (CuCl ₂ ? 2H ₂ O) was dissolved in 200 mL of distilled water to prepare a 1.5 wt% aqueous cupric chloride hydrate solution. Thereafter, the washed chitosan-melamine beads were mixed in the aqueous cupric chloride hydrate solution and stirred slowly for 24 hours. When there was a change in pH during the mixing process, the pH of the cupric chloride aqueous solution was maintained at 5 using 0.1 M HCl or 0.1 M NaOH solution. After 24 hours of mixing, the chitosan-melamine chitosan beads were washed with distilled water, some were stored in distilled water in gel form, and some were dried at the laboratory temperature.

Example  2

An aqueous solution (concentration 0.5 wt%, pH 6) containing nickel chloride hydrate was used in place of the cupric chloride hydrate.

Example  3

Each of the chitosan-melamine complexes was prepared in the same manner as in Example 1 except that the content of melamine was 1 wt% and 3 wt%, respectively.

Example  4

Each of the chitosan-melamine complexes was prepared in the same manner as in Example 1 except that the content of chitosan was 1.5 wt% and 3 wt%, respectively.

Example  5

Each of the chitosan beads was prepared in the same manner as in Example 1 except that 1.0 wt% and 2.5 wt% of copper ions were used.

Comparative Example  One

The procedure of Example 1 was repeated except that the chitosan powder was used alone except for the melamine powder.

Experimental Example

Batch adsorption experiments were carried out using Example 1 and Comparative Example 1.

A plurality of 50 ml of PO ₄ ^3- aqueous solution were prepared, and the phosphate removal experiments were repeatedly carried out by introducing Example 1 and Comparative Example 1 into each PO ₄ ^3- aqueous solution. PO ₄ ^{3- The} aqueous solution contains nitrate and sulfate in a certain concentration in addition to phosphate (PO ₄ ^3- ).

As a result, as shown in Fig. 1, the removal amount of phosphate of Comparative Example 1 (containing no melamine) was 18 mg / g, while the removal amount of phosphate of Example 1 (containing melamine) was 22 mg / g (1.25%) and 23 mg / g (2.5%), respectively.

In addition, Example 3 in which the content of melamine was different, Example 4 in which the content of chitosan was different and Example 5 in which the concentration of the transition metal was different showed a phosphate removal efficiency similar to that in Example 1, The phosphate removal efficiency was much higher than that of the phosphate removal.

These results indicate that CBM-Cu according to the present invention has an amine group increased by melamine in comparison with CB-Cu, which suggests that the chelate bond of the immobilized transition metal (Cu) is improved.

Claims (8)

Mixing 1% by weight HCl solution with dimethyl sulfoxide and melamine to prepare a melamine solution of 1.5% by weight;
Mixing the melamine solution with chitosan powder to prepare a 2.5 wt% chitosan-melamine solution;
Preparing a chitosan-melamine bead by titrating a 2.5 wt% chitosan solution into an aqueous solution of sodium hydroxide;
Washing the prepared chitosan-melamine beads with distilled water; And
The chitosan-melamine beads are mixed with an aqueous solution of cupric chloride (CuCl22H2O) containing 1.5% by weight of a pH of 4 to crosslink the polymer and the transition metal ion in the chitosan-melamine beads, and the transition metal ion is ligated Wherein the step of inducing the function of the functional group is carried out in the presence of a functional group capable of dissolving the chitosan-melamine complex. delete delete delete delete delete delete A phosphorus removal chitosan-melamine composite produced by the method of claim 1.

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