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Frontiers in Energy

ISSN 2095-1701

ISSN 2095-1698(Online)

CN 11-6017/TK

邮发代号 80-972

2019 Impact Factor: 2.657

Frontiers in Energy  2020, Vol. 14 Issue (3): 578-589   https://doi.org/10.1007/s11708-020-0808-7
  本期目录
A comprehensive study of hydrogen production from ammonia borane via PdCoAg/AC nanoparticles and anodic current in alkaline medium: experimental design with response surface methodology
Hilal ÇELİK KAZICI(), Şakir YILMAZ, Tekin ŞAHAN(), Fikret YILDIZ, Ömer Faruk ER, Hilal KIVRAK
Department of Chemical Engineering, Faculty of Engineering, Van Yüzüncü Yıl University, 65080 Van, Turkey
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Abstract

In this paper, the optimization of hydrogen (H2) production by ammonia borane (NH3BH3) over PdCoAg/AC was investigated using the response surface methodology. Besides, the electro-oxidation of NH3BH3 was determined and optimized using the same method to measure its potential use in the direct ammonium boran fuel cells. Moreover, the ternary alloyed catalyst was synthesized using the chemical reduction method. The synergistic effect between Pd, Co and Ag plays an important role in enhancement of NH3BH3 hydrolysis. In addition, the support effect could also efficiently improve the catalytic performance. Furthermore, the effects of NH3BH3 concentration (0.1–50 mmol/5 mL), catalyst amount (1–30 mg) and temperature (20°C–50°C) on the rate of H2 production and the effects of temperature (20°C–50°C), NH3BH3 concentration (0.05–1 mol/L) and catalyst amount (0.5–5 µL) on the electro-oxidation reaction of NH3BH3 were investigated using the central composite design experimental design. The implementation of the response surface methodology resulted in the formulation of four models out of which the quadratic model was adjudged to efficiently appropriate the experimental data. A further statistical analysis of the quadratic model demonstrated the significance of the model with a p-value far less than 0.05 for each model and coefficient of determination (R2) of 0.85 and 0.95 for H2 production rate and NH3BH3 electrroxidation peak current, respectively.

Key wordsammonia borane    hydrogen production    fuel cell    response surface methodology
收稿日期: 2019-10-31      出版日期: 2020-09-14
Corresponding Author(s): Hilal ÇELİK KAZICI,Tekin ŞAHAN   
 引用本文:   
. [J]. Frontiers in Energy, 2020, 14(3): 578-589.
Hilal ÇELİK KAZICI, Şakir YILMAZ, Tekin ŞAHAN, Fikret YILDIZ, Ömer Faruk ER, Hilal KIVRAK. A comprehensive study of hydrogen production from ammonia borane via PdCoAg/AC nanoparticles and anodic current in alkaline medium: experimental design with response surface methodology. Front. Energy, 2020, 14(3): 578-589.
 链接本文:  
https://academic.hep.com.cn/fie/CN/10.1007/s11708-020-0808-7
https://academic.hep.com.cn/fie/CN/Y2020/V14/I3/578
Fig.1  
Independent parameters Coded and un-coded values
–1 0 + 1
H2 production rate /(mL·(g·min)–1) NH3BH3 conc./mmol/5 mL) (X1) 0.1 2.55 5
Catalyst amount/mg (X2) 1 15.5 30
Temperature/°C (X3) 20 35 50
Temperature/°C (A) 20 35 50
Current/mA NH3BH3 conc./M (B) 0.05 0.525 1
Catalyst amount/mL (C) 0.5 2.75 5
Tab.1  
Run NH3BH3 conc. (X1, mmol/5 mL) Catalyst amount (X2, mg) Temperature (X3, °C) H2 production rate /(mL·(g·min)–1)
1 2.55 (0) 1 (–1) 35 (0) 5263.16
2 0.1 (–1) 30 ( + 1) 50 ( + 1) 2000
3 2.55 (0) 15.5 (0) 35 (0) 8513.6
4 0.1 (–1) 1 (–1) 50 ( + 1) 6481.48
5 5 ( + 1) 15.5 (0) 35 (0) 4950.72
6 5 ( + 1) 1 (–1) 20 (–1) 1190.48
7 2.55 (0) 15.5 (0) 35 (0) 8513.6
8 2.55 (0) 15.5 (0) 35 (0) 8513.6
9 2.55 (0) 15.5 (0) 35 (0) 8513.6
10 2.55 (0) 15.5 (0) 20 (–1) 2150.54
11 2.55 (0) 15.5 (0) 50 ( + 1) 11414.4
12 5 ( + 1) 1 (–1) 50 ( + 1) 5133.61
13 0.1 (–1) 15.5 (0) 35 (0) 3154.12
14 2.55 (0) 15.5 (0) 35 (0) 8513.6
15 0.1 (–1) 1 (–1) 20 (–1) 2982.46
16 5 ( + 1) 30 ( + 1) 50 ( + 1) 6637.43
17 5 ( + 1) 30 ( + 1) 20 (–1) 1750
18 2.55 (0) 15.5 (0) 35 (0) 8513.6
19 2.55 (0) 30 ( + 1) 35 (0) 4851.85
20 0.1 (–1) 30 ( + 1) 20 (–1) 1666.67
Run Temperature (A, °C) NH3BH3 conc. (B, M) Catalyst amount (C, mL) Current/mA
1 50 ( + 1) 0.05 (–1) 5 ( + 1) 0.078
2 20 (–1) 0.05 (–1) 0.5 (–1) 0.268
3 35 (0) 1 ( + 1) 2.75 (0) 2.369
4 35 (0) 0.525 (0) 2.75 (0) 2.686
5 20 (–1) 0.525 (0) 2.75 (0) 2.028
6 35 (0) 0.525 (0) 2.75 (0) 2.686
7 20 (–1) 1 ( + 1) 5 ( + 1) 2.895
8 35 (0) 0.525 (0) 5 ( + 1) 2.487
9 35 (0) 0.525 (0) 2.75 (0) 2.686
10 50 ( + 1) 0.525 (0) 2.75 (0) 1.34
11 50 ( + 1) 0.05 (–1) 0.5 (–1) 0.649
12 35 (0) 0.05 (–1) 2.75 (0) 0.489
13 20 (–1) 0.05 (–1) 5 ( + 1) 0.881
14 50 ( + 1) 1 ( + 1) 5 ( + 1) 0.603
15 35 (0) 0.525 (0) 2.75 (0) 2.686
16 35 (0) 0.525 (0) 2.75 (0) 2.686
17 35 (0) 0.525 (0) 0.5 (–1) 1.897
18 35 (0) 0.525 (0) 2.75 (0) 2.686
19 50 ( + 1) 1 ( + 1) 0.5 (–1) 1.65
20 20 (–1) 1 ( + 1) 0.5 (–1) 2.151
Tab.2  
Sum of squares df Mean square F value p-value
H2 production rate Model (significant) 1.481E+ 008 9 1.645E+ 007 6.05 0.0447
X1-NH3BH3 conc. 1.141E+ 006 1 1.141E+ 006 0.42 0.5316
X2-Catalyst amount 1.718E+ 006 1 1.718E+ 006 0.63 0.4450
X3-Temperature 4.808E+ 007 1 4.808E+ 007 17.69 0.0018
X1X2 7.724E+ 006 1 7.724E+ 006 2.84 0.1227
X1X3 3.123E+ 006 1 3.123E+ 006 1.15 0.3089
X2X3 6.168E+ 005 1 6.168E+ 005 0.23 0.6440
X12 2.130E+ 007 1 2.130E+ 007 7.84 0.0188
X22 8.692E+ 006 1 8.692E+ 006 3.20 0.1040
X32 7702.90 1 7702.90 2.835E-003 0.9586
Current Model (significant) 16.78 9 1.86 19.10 <0.0001
A-Temperature 1.52 1 1.52 15.61 0.0027
B-NH3BH3 conc. 5.33 1 5.33 54.64 <0.0001
C-Catalyst amount 0.011 1 0.011 0.11 0.7460
AB 0.70 1 0.70 7.20 0.0230
AC 1.11 1 1.11 11.33 0.0072
BC 0.015 1 0.015 0.15 0.7044
A2 0.86 1 0.86 8.85 0.0139
B2 1.83 1 1.83 18.74 0.0015
C2 7.606E-003 1 7.606E-003 0.078 0.7858
Tab.3  
Fig.2  
Fig.3  
Fig.4  
Parameters Optimum value H2 production rate/(mL·(g·min)–1) Current/mA
Predicted Experimental Predicted Experimental
X1/(mmol/5 mL) 2.91 10105.6 9459.92
X2/mg 13.26
X3/°C 50
A/°C 28.21 2.77984 2.51799
B/M 2.5
C/mL 0.78
Tab.4  
Fig.5  
Fig.6  
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