Influence of hydrothermal carbonized sewage sludge on coal water slurry performance
Asma Leghari1,2, Yao Xiao1,2, Lu Ding1,2(), Hammad Sadiq3, Abdul Raheem4, Guangsuo Yu1,2,5()
. Institute of Clean Coal Technology, East China University of Science and Technology, Shanghai 200237, China . Engineering Research Center of Resource Utilization of Carbon-containing Waste with Carbon Neutrality, Ministry of Education, Shanghai 200237, China . School of Mechanical and Power Engineering, East China University of Science and Technology, Shanghai 200237, China . Energy and Bioproducts Research Institute (EBRI), Aston University, Birmingham, B4 7ET, UK . State Key Laboratory of High-Efficiency Utilization of Coal and Green Chemical Engineering, Ningxia University, Yinchuan 750021, China
Coal utilization, as a major energy source, raises sustainability concerns and environmental impacts, prompting researchers to explore blending it with other feedstocks. This study discusses hydrochar coal-water slurry (HC-CWS) preparation conditions, emphasizing apparent viscosity and exploring the influence of high ash content on char reactivity. The study highlights that the presence of free water in sludge is moderately influential, while high amounts of free water in raw sewage sludge (SS) and its near absence during hydrothermal carbonization (HTC) of SS are both unfavorable for enhancing the overall performance of coal-water slurry (CWS). HTC reduces the concentration of hydroxyl functional group, enhancing slurry performance and reducing ash content in HC-CWS, indicating that coal complements hydrochar (HC). High-temperature HC preparation is unsuitable for HC-CWS due to increased viscosity and decreased stability. In terms of ash content, the optimal pH and HC ratio for CWS are determined at 30% HC. The gasification reactivity of HC, prepared at 180 °C with a 30% HC ratio in CWS at R0.5 is 6 × 10−3 and at R0.9 is 9 × 10−3. However, increasing HC to 50% diminishes reactivity under CO2 atmosphere. The inhibitory effect was observed with an increasing percentage of HC in CWS and the synergy factor decreased in the following order: 10% HC > 30% HC > 50% HC, i.e., from 1.04 to 0.35. The possible reason is the presence of high ash content and their similar initial gasification rates during its early stages.
Fig.1 Particle size of (a) raw SS and SH coal and (b) HC prepared at 180 °C at 30, 60, and 90 min.
Sample
Ultimate analysis/(wt %, d)
Proximate analysis/(wt %, d)
N
C
H
S
O
Ashd
VMd
FCd
SH coal
0.93
77.22
4.550
0.590
9.320
6.890
32.91
60.20
HC 180-30
1.58
20.54
2.461
0.353
9.116
65.95
27.24
6.81
HC 180-60
1.57
19.80
2.101
0.384
12.315
63.83
28.98
7.66
HC 180-90
1.56
19.61
2.025
0.424
12.951
63.43
30.80
9.37
Tab.1 Proximate and ultimate analysis of HCa)
Sample
SiO2
Al2O3
Fe2O3
P2O5
CaO
K2O
MgO
TiO2
SO3
Na2O
HC 180-30
47.59
18.11
13.02
12.90
2.42
1.68
1.69
0.984
0.772
0.580
HC 180-60
47.21
18.19
13.32
12.70
2.42
1.67
1.67
0.984
0.750
0.605
HC 180-90
47.03
18.09
13.33
13.23
2.35
1.65
1.62
0.985
0.648
0.559
Tab.2 Ash composition of HC
Fig.2 SEM images of HC prepared at different operating conditions: (a) raw SS, (b) 180 °C-30 min, (c) 180 °C-60 min, (d) 180 °C-90 min, (e) 200 °C-30 min, (f) 200 °C-60 min, (g) 200 °C-90 min, (h) 220 °C-30 min, (i) 220 °C-60 min, (j) 220 °C-90 min, (k) 240 °C-30 min, (l) 240 °C-60 min, and (m) 240 °C-90 min.
Fig.3 FTIR spectra of (a) raw SS and SH coal, (b) 180 °C at 30, 60 and 90 min, and (c–e) HC-CWS (30%) against different time at the same temperature.
Sample
SH coal
Raw SS
HC (180 °C-30 min)
HC (180 °C-60 min)
HC (180 °C-90 min)
Specific surface area/(m2·g–1)
4.5648
2.0645
19.1363
19.1399
22.2268
Adsorption average pore size/nm
7.3623
18.7025
16.5532
15.6029
14.1106
Desorption average pore size/nm
8.6057
24.0405
24.5947
22.5801
20.0721
Pore volume/(cm3·g–1)
0.008402
0.009653
0.079192
0.074660
0.078408
Tab.3 Specific surface area, pore size and pore volume of raw SS, HC and SH coal
Sample
Maximum contact angle/(° )
Minimum contact angle/(° )
HC 180 °C-30 min
89.51
49.07
HC 180 °C-60 min
89.17
56.97
HC 180 °C-90 min
87.11
56.90
SH coal
85.45
33.55
Tab.4 Contact angle measurements of HC and SH coal
Fig.4 Apparent viscosities of HC-CWS (a) at different ratios of 180 °C and 30 min HC, (b) at different ratios of 180 °C and 60 min HC, and (c) at different ratios of 180 °C and 90 min HC.
Samples
HC-CWS
Ash (air db)/%
VM
FC
pH
HC
10%
30%
50%
10%
30%
50%
10%
30%
50%
10%
30%
50%
180 °C-30 min
12.20
23.61
36.19
27.50
30.61
29.09
57.90
45.59
32.55
6.37
6.12
5.89
180 °C-60 min
11.76
23.91
34.09
29.90
30.80
29.50
56.97
45.48
36.59
6.20
5.96
5.79
180 °C-90 min
12.29
24.13
33.05
30.21
31.36
31.26
58.21
44.51
37.55
6.94
5.96
5.62
Tab.5 Proximate analysis of HC-CWS with different proportions of HC
Fig.5 (a) TGA and (b) DTG of HC at 180 °C at different holding times.
Fig.6 Carbon conversion curves against gasification time (min).
Sample
R0.5/min–1
R0.9/min–1
Initial gasification rate
Raw SS
3.508 × 10?2
2.230 × 10?2
0.018
SH coal
1.224 × 10?2
1.910 × 10?2
0.039
180-30
2.890 × 10?2
2.250 × 10?2
0.010
180-30-10%
1.233 × 10?2
1.937 × 10?2
0.016
180-30-30%
1.257 × 10?2
1.929 × 10?2
0.014
180-30-50%
6.527 × 10?3
9.950 × 10?3
0.014
Tab.6 Initial gasification rate and reactivity index at R0.5 and R0.9
Fig.7 Carbon conversion curves X against gasification reactivity (min–1) of (a) raw SS and SH coal, (b) 180 °C, 30, 60 and 90 min, (c) different ratios of HC-CWS and (d) synergy index A of HC-CWS.
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