Adsorption Capacity for Phosphorus Comparison among Activated Alumina, Silica Sand and Anthracite Coal
Junling WANG, Yajun ZHANG, Cuimin FENG, Junqi LI, Guibai LI
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DOI: 10.4236/jwarp.2009.14031   PDF    HTML     7,372 Downloads   14,476 Views   Citations

Abstract

Experimental researches on adsorptive capacity of activated alumina, silica sand and anthracite coal for phosphorus were conducted. Results showed that performances of three filter media were all in line with Langmuir isotherm, and activated alumina adsorptive performance was much better than silica sand and an-thracite coal for phosphorus removal. The adsorptive capacity of activated alumina, silica sand and anthracite coal for phosphorus was 3333μg/g, 49μg/g and 100μg/g respectively. Activated alumina displayed adsorp-tive function well for phosphorus, because its inner porosity, specific surface area and surface isoelectric pH value were all higher than those of other two filter media. While activated alumina was used as filter material in water treatment process, phosphorus would be removed strongly because of adsorptive characteristic of activated alumina.

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WANG, J. , ZHANG, Y. , FENG, C. , LI, J. and LI, G. (2009) Adsorption Capacity for Phosphorus Comparison among Activated Alumina, Silica Sand and Anthracite Coal. Journal of Water Resource and Protection, 1, 260-264. doi: 10.4236/jwarp.2009.14031.

1. Introduction

Generally the proportion of organic carbon, nitrogen and phosphorus is 100:10:1 for microorganism growing in pipe water, therefore, removal of phosphorus as a kind of nutrient in drinking water may be a method to restrain the regrowth of microorganism. Lehtola [1,2] reported that phosphorus could replace the organic matter as the limitation factor for microbial regrowth in drinking water with high organic matter concentration. In China, a great many surface water sources have been contaminated severely by organic matter, thus the phosphorus will be the limitation factor in drinking water and raw water there.

Many researchers have studied the removal technology for phosphorus in drinking water. Membrane treatment technology [3] and ozonation process [4] were two techniques that have been tested to remove phosphorus in drinking water, but removal rate did not get promoted. In addition, researchers [5,6] experimented and concluded that traditional water treatment process in water plant couldn’t achieve efficient performance for phosphorus removal. It is unknown whether traditional filter media hold strong adsorptive capacity for phosphorus or not. New technique and application of new filter media to improve the removal of phosphorus were creative and beneficial explored for keeping drinking water biological stability. Activated alumina was one unique media with high adsorptive capacity for many pollutants, but the character for phosphorus removal in drinking water has not been disclosed, so it is worth testing and confirming the efficiency to remove or adsorb phosphorus, at the same time, adsorptive capacity of traditional filter media silica sand and anthracite coal are tested to compare, moreover, application feasibility of activated alumina should be considered.

2. Experimental Materials and Methods

2.1. Experimental Materials

Three filter media including activated alumina, silica sand and anthracite coal were utilized in experiments. Silica sand and anthracite coal were mostly used in filtration process of water works. All materials purchased in local market showed the characteristics in Table 1.

The appliance used in experimentation included beaker flask, constant temperature oscillator, 0.45 μm

Table 1. Physical characteristics of filter media.

microporous membranes, and main chemical was KH2PO4.

2.2. Experimental Methods

Step one, KH2PO4 was dissolved into ultrapure water to form samples with various phosphorus concentration in five beaker flasks, and each volume was 1000mL. Phosphorus concentration of prepared water in beaker flasks were 500μg/L, 2000μg/L, 5000μg/L, 8000μg/L, 10000μg/L respectively. Step two, 5g activated alumina filter media was added to every beaker flask and put into constant temperature oscillator. After operating for 24h at 40 degree Celsius, samples in all beaker flasks were filtered through 0.45μm membrane, the phosphorus concentration in supernatant was examined and adsorptive capacity value was obtained.

Experimental procedure with silica sand and anthracite coal were as same as activated alumina, but phosphorus concentration varied. It was conjectured that adsorptive capacities of silica sand and anthracite coal were all lower than activated alumina, so experimental initial concentration was set at low level. Six water samples with phosphorus concentration 100μg/L, 200μg/L, 300μg/L, 500μg/L, 800μg/L, and 1000μg/L were prepared for silica sand experiment, and 50μg/L, 100μg/L, 200μg/L, 300μg/L, 500μg/L, and 1000μg/L for anthracite coal. Silica sand and anthracite coal were added by 5g respectively.

3. Results

3.1 Experiment on Phosphorus Adsorption by Activated Alumina

The formula is:

(1)

where x=quality of adsorbed adsorbate, μg m=quality of adsorbent, g V=volume of water sample, L Ci=the initial concentration of adsorbate, μg/L Ce=equilibrium concentration of adsorbate, μg/L qe=adsorptive capacity, μg/g Experimental result was presented in Table 2 and plotted in Figure 1.

In view of the variation of the isotherm, it seems to obey the Langmuir isotherm. The adsorption equations are:

(2)

(3)

where b=constant value

(qe)0=adsorptive capacity extreme value, μg/g Taking the Ce as x-axis and Ce/qe as y-axis, Langmuir formula was plotted in Figure 2. Then

Table 2. Adsorption experimental result for phosphorus by activated alumina.

Figure 1. Phosphorus adsorption isotherm of activated alumina.

Figure 2. Simulated line of activated alumina adsorption.

the adsorptive capacity extreme value and constant b value can be obtained from the line intercept and line slope.

In Figure 2, the coefficient of determination was 0.9979, and the adsorption isotherm was the type of Langmuir. Based on the isotherm, the process of adsorption for phosphorus was predominant by single molecule adsorption. Then result was obtained as followed:

=0.0003,=0.6059, b=0.0005, (qe)0=3333μg/g

(4)

Finally, the adsorptive capacity of activated alumina was 3333μg/g.

3.2. Experiment on Silica Sand

The result was shown in Table 3.

The result was obtained as followed:

, , b=0.0011, (qe)0=48.78μg/g

.(5)

The adsorptive capacity of silica sand for phosphorus was 49μg/g.

The result showed that silica sand could adsorb phosphorus weakly, but its adsorptive capacity was far less than activated alumina.

3.3. Experiment on Anthracite Coal

The adsorption experimental result was shown in Table 4.

Table 3. Adsorption experimental result for phosphorus by silica sand.

Table 4. Adsorption experimental result for phosphorus by anthracite coal.

Then result was obtained as followed:

(6)

Adsorptive capacity was 100μg/g.

More times of experiment for each filter media were conducted, results were similar to previous data respectively.

4. Discussion

4.1. Adsorption Mechanism of Activate Alumina

Experimental result demonstrated that activated alumina adsorption was consistent with the langmuir isotherm. Feng [7] reported that one type of activated alumina has large adsorptive capacity of 3950μg/g for soluble ortho-phosphorus and it was in agreement with result of this paper. Ning [8] reported that activated alumina adsorptive capacity was higher than activated carbon, and it was 3-9 times as high as activated carbon, in addition, optimum pH value was 3-4. The adsorptive capacity would increase when temperature was higher, but the adsorption for phosphorus was a type of reaction of thermal relief.

The Langmuir adsorption theory states that no solid surface is even and smooth absolutely, there are a great quantity of convex points which attract ions. The atom and ion on the convex point have unsaturated chemical bond, and creat surface activated centers, which can adsorb the adsorbate. Every center trap only one adsorbate molecule. When surface activated centers were occupied completely, the adsorptive capacity reach the highest, so generally there is one layer absorbate molecule on the surface of adsorbent. Hua [9] indicated that when activated alumina was saturated, all of surface of micropore was deposited by adsorbate particle closely and tightly. Almost all micropores were not in conjunction longer and activated alumina would lose activation after saturation. Comparison of new and used activated alumina showed that new activated alumina had much more micropores and surface area than used.

The order of activated alumina adsorptive force for anion in water is followed:

OH->PO43->F->SO3->Fe(CN)64->CrO42->SO42->Fe(CN)53->Cr2O72->I->Br->Cl->NO3->MnO4->ClO4->S2-

It is apparent that activated alumina adsorptive force for phosphate anion is stronger than other anions, such as SO42- and Cl-, so activated alumina adsorb phosphate anion in predominance.

4.2. Filter Media Comparison

According to adsorptive experiment, the adsorptive capacity of activated alumina, silica sand and anthracite coal were 3333μg/g, 49μg/g and 100μg/g respectively. Characteristic difference of three filter media are analyzed as follows, and represented in Table 5.

Porosity: It is different for every filter media. The porosity just represents the space between granules, not including inner micropore. It is micropore performing main adsorptive function instead of space between granules, so it is insignificant to compare the porosity of filter media to analyze the adsorptive capacity.

Micropore volume and pore size: The quantity of micropore decides the inner surface area, and pore size limit the dimension of attached molecules. Silica sand and anthracite coal have little inner micropore, therefore they don’t have inner adsorption efficiency for phosphorus.

Surface area: In Table 5, adsorptive capacity is correlative to surface area. The specific surface area of activated alumina was larger than that of silica sand and anthracite coal. Xie [10] reported that when specific surface area was large, the adsorptive capacity would be large. Additionally it was proved that even if absorbent was the

Table 5. Comparison of every adsorbent.

same species, the adsorptive capacity would differ because of specific surface area.

The adsorptive efficiency of silica sand or anthracite coal was very low for soluble ortho-phosphate, because they were all pure solid without micropore. The adsorptive property was only influenced by outer surface area for these two materials. Xie [11] reported that silica sand with diameter from 0.5mm to 1.2mm had a little surface area, and the surface was charged negatively. The outer surface of them was flat without micropore under the test of EM reported by Zhang [12], so the adsorptive function was not considered when they were applied to water treatment process.

Surface charge: Surface of mineral and clay was charged negatively, so they can not adsorb the anion in water. But activated alumina surface attach numerous anion OH-, so the surface isoelectric pH value is higher than 7, and it has capacity of ion exchange. The surface isoelectric pH value of silica sand is less than 7, reportedly it is 0.7~2.2 [13], so it is charged negatively. This is the part reason for these three filter media holding different adsorptive capacity for phosphorus.

5. Conclusions

Adsorptive experiments of activated alumina, silica sand and anthracite coal were conducted for phosphorus removal, and result showed that adsorptive capacity of activated alumina, silica sand and anthracite coal were 3333μg/g, 49μg/g and 100μg/g respectively.

Effective adsorptive property of activated alumina for phosphorus results from three factors, firstly there are many inner micropore that silica sand and anthracite coal do not have. The second factor is that surface area of activated alumina is approximate 300m2/g and much larger than that of silica sand and anthracite coal. Finally the surface isoelectric pH value is higher than 7, but those of silica sand and anthracite coal are far less than 7.

For the biological stabilization of tap water, in order to improve removal of phosphorus, the activated alumina could be considered as effective material to replace the traditional filter media, because in filtration process the activated alumina can remove more phosphorus relying on the adsorptive capacity. But undesirable factors exist for applicable feasibility of activated alumina, such as the frangibility, the difficulty of regeneration and high cost in running process.

6. Acknowledgement

This work was financed by National Key Technology R&D Program (2008BAJ08B13-04), Beijing Supreme Talents Supporting Project (20071D0501700240) and Major Projects on Control and Rectification of Water Body Pollution (2009ZX07317-005). We thank the laboratory staffs of the laboratories of School of Environment and Energy of BUCEA.

Conflicts of Interest

The authors declare no conflicts of interest.

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