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Frontiers of Agricultural Science and Engineering

ISSN 2095-7505

ISSN 2095-977X(Online)

CN 10-1204/S

Postal Subscription Code 80-906

Front. Agr. Sci. Eng.    2023, Vol. 10 Issue (3) : 492-502    https://doi.org/10.15302/J-FASE-2023503
RESEARCH ARTICLE
DEGRADATION OF ORGANIC POLLUTANTS IN FLOCCULATED LIQUID DIGESTATE USING PHOTOCATALYTIC TITANATE NANOFIBERS: MECHANISM AND RESPONSE SURFACE OPTIMIZATION
Yiting XIAO1(), Yang TIAN2, Yuanhang ZHAN1, Jun ZHU1
1. Department of Biological and Agricultural Engineering, University of Arkansas, Fayetteville, AR 72701, USA
2. Material Science and Engineering Programs, University of Arkansas, Fayetteville, AR 72701, USA
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Abstract

● Titanate NFs were synthesized and photodegraded liquid digestate for the first time.

● The long titanate NFs (bandgap of 3.16 eV) have a high VFA removal rate of 72.9%.

● RSM has been used to optimize the VFA, COD, and color removal rate.

● The quadratic model and the effects of photocatalytic dosage were significant.

Titanate nanofibers (TNFs) were synthesized using a hydrothermal method and were employed for the first time in this study to photocatalytically degrade organic pollutants found in flocculated liquid digestate of poultry litter. The photocatalytic performance of TNFs, with a bandgap of 3.16 eV, was tested based on degradation of organic pollutants and removal of color. Five combinations of pollutant concentration and pH were examined (0.2 to 1.3 g·L−1 at pH 4 to 10). Central composite design (CCD) and response surface methodology (RSM) were applied in order to optimize the removal rates of volatile fatty acids (VFA) and chemical oxygen demand (COD), and the decolorization rate. There were no significant differences between the regression models generated by the CCD/RSM and the experimental data. It was found that the optimal values for pH, dosage, VFA removal rate, COD removal rate and decolorization rate were 6.752, 0.767 g·L−1, 72.9%, 59.1% and 66.8%, respectively. These findings indicates that photocatalytic TNFs have potential for the posttreatment of anaerobic digestion effluent, as well as other types of wastewater.

Keywords titanate nanofibers      photocatalysis      poultry litter liquid digestate     
Corresponding Author(s): Yiting XIAO   
Just Accepted Date: 28 April 2023   Online First Date: 01 June 2023    Issue Date: 20 September 2023
 Cite this article:   
Yiting XIAO,Yang TIAN,Yuanhang ZHAN, et al. DEGRADATION OF ORGANIC POLLUTANTS IN FLOCCULATED LIQUID DIGESTATE USING PHOTOCATALYTIC TITANATE NANOFIBERS: MECHANISM AND RESPONSE SURFACE OPTIMIZATION[J]. Front. Agr. Sci. Eng. , 2023, 10(3): 492-502.
 URL:  
https://academic.hep.com.cn/fase/EN/10.15302/J-FASE-2023503
https://academic.hep.com.cn/fase/EN/Y2023/V10/I3/492
Fig.1  Schematic of the photocatalytic reactor system.
Run pH Concentration (mg·L−1) VFA removal rate (%) COD removal rate (%) Decolorization rate (%)
1 7.00 0.75 68.0 53.2 59.9
2 7.00 1.30 51.6 10.4 18.7
3 10.0 0.75 33.1 20.7 48.1
4 9.12 0.36 30.5 18.3 54.9
5 7.00 0.75 67.4 57.8 70.8
6 4.00 0.75 38.1 37.4 42.6
7 7.00 0.75 75.6 66.3 74.3
8 4.88 1.14 57.3 39.6 42.6
9 7.00 0.20 20.9 12.8 32.8
10 4.88 0.36 47.8 38.4 49.4
11 9.12 1.14 53.1 32.3 40.2
12 7.00 0.75 74.3 59.7 60.6
13 7.00 0.75 76.4 55.7 71.1
Tab.1  Central composite design matrix of the two independent variables with experimental responses for volatile fatty acid (VFA) removal rate, chemical oxygen demand (COD) removal rate and decolorization rate
Fig.2  X-ray diffraction pattern for TiO2 nanoparticles and Titanate nanofibers (Na2TiO5 NFs) at different synthesis time from 1 day to 5 days (from bottom to top).
Fig.3  Scanning electron microscope image of (a) TiO2 nanoparticles; (b) titanate (as Na2TiO5) nanofiber synthesized by hydrothermal method from TiO2 nanoparticles.
Fig.4  Transformed reflectance spectrum plot of Titanate nanofibers to determine the band gap energy (Eg). x-axis data (Eg) was extrapolated from linear plots of the plot. Absorption spectrum of titanate nanofibers is shown in the inset plot.
Pollutant Nanoparticle photocatalyst Initial COD* (mg·L–1) pH Concentration(g·L–1) UV intensity (W) Removal efficiency (%) Reference
Refinery wastewater TiO2 immobilized on white concrete 1200 9 0.05 24 60 [17]
Coffee processing wastewater TiO2 (addition of H2O2 oxidants) 28,800 4 0.5 64 84 [16]
Refinery wastewater TiO2 200–240 4 1.2 88 41 [18]
Metronidazolein aqueous solutions TiO2 126 10 3 125 34 [19]
Petroleum refinery wastewater TiO2 220 4 0.1 400 83 [20]
Tab.2  Comparisons with previous studies
ANOVA parameter Response variable
VFA removal rate COD removal rate Decolorization rate
Sum of squares 0.378 0.390 0.274
Mean squares 0.0755 0.0780 0.0548
R2 0.911 0.902 0.865
Adjusted R2 0.848 0.832 0.768
Mean 0.534 0.387 0.512
Standard deviations 0.0725 0.0779 0.0783
Coefficient of variation (%) 13.6 20.17 15.3
Adequate precision 9.56 8.19 8.14
SSE* 0.0368 0.0424 0.0429
F 14.4 12.9 8.94
P 0.0015 0.0020 0.0060
(Lack of fit)
F 5.24 4.36 1.94
P 0.0717 0.0943 0.2650
Tab.3  ANOVA analysis for fitting models for volatile fatty acids (VFA) and chemical oxygen demand (COD) removal rate, and Decolorization rate
Fig.5  Linear correlations between the observed and predicted data for volatile fatty acids (VFA) removal rate (a), chemical oxygen demand (COD) removal rate (b) and decolorization rate (c).
ANOVA parameters Response variables
pH Concentration pH by concentration pH2 Concentration2
VFA removal rate
 Sum of squares 0.0102 0.0713 0.0043 0.168 0.162
 Mean squares 0.0102 0.0713 0.0043 0.168 0.162
 F 1.94 13.6 0.821 32.0 30.7
 P 0.207 0.0078a 0.395 0.0008a 0.0009a
COD removal rate
 Sum of squares 0.0325 0.0018 0.0040 0.0968 0.292
 Mean squares 0.0325 0.0018 0.0040 0.0968 0.292
 F 5.35 0.291 0.664 16.0 48.3
 P 0.0539 0.606 0.4420 0.0052a 0.0002a
Decolorization rate
 Sum of squares 0.0015 0.0214 0.0016 0.0466 0.226
 Mean squares 0.0015 0.0214 0.0016 0.0466 0.226
 F 0.244 3.49 0.256 7. 60 36.8
 P 0.637 0.104 0.628 0.0282a 0.0005a
Tab.4  ANOVA for model variables and their interactions for volatile fatty acids (VFA) removal rate, chemical oxygen demand (COD) removal rate, and decolorization rate
Fig.6  Response surface plots of volatile fatty acid (VFA) removal rate (a) chemical oxygen demand (COD) removal rate (b), and decolorization rate (c) with respect to pH and concentration.
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