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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

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2018 Impact Factor: 2.809

Front. Chem. Sci. Eng.    2025, Vol. 19 Issue (1) : 6    https://doi.org/10.1007/s11705-024-2508-z
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
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Abstract

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.

Keywords hydrochar coal water slurry      high ash content      slurry properties      gasification reactivity     
Corresponding Author(s): Lu Ding,Guangsuo Yu   
Just Accepted Date: 17 July 2024   Issue Date: 28 November 2024
 Cite this article:   
Asma Leghari,Yao Xiao,Lu Ding, et al. Influence of hydrothermal carbonized sewage sludge on coal water slurry performance[J]. Front. Chem. Sci. Eng., 2025, 19(1): 6.
 URL:  
https://academic.hep.com.cn/fcse/EN/10.1007/s11705-024-2508-z
https://academic.hep.com.cn/fcse/EN/Y2025/V19/I1/6
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).
SampleR0.5/min–1R0.9/min–1Initial gasification rate
Raw SS3.508 × 10?22.230 × 10?20.018
SH coal1.224 × 10?21.910 × 10?20.039
180-302.890 × 10?22.250 × 10?20.010
180-30-10%1.233 × 10?21.937 × 10?20.016
180-30-30%1.257 × 10?21.929 × 10?20.014
180-30-50%6.527 × 10?39.950 × 10?30.014
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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