scholarly journals Investigation of Low Rank Coal Gasification in a Two-Stage Downdraft Entrained-Flow Gasifier

2014 ◽  
Vol 03 (01) ◽  
pp. 1-12 ◽  
Author(s):  
Xijia Lu ◽  
Ting Wang
Keyword(s):  
Coal Gasification ◽  
Low Rank ◽  
Low Rank Coal ◽  
Two Stage ◽  
Entrained Flow ◽  
Entrained Flow Gasifier

scholarly journals Investigation of the Coal Gasification Process Under Various Operating Conditions Inside a Two-Stage Entrained Flow Gasifier

2012 ◽  
Vol 4 (2) ◽  
Author(s):  
Armin Silaen ◽  
Ting Wang
Keyword(s):  
Coal Gasification ◽  
Operating Conditions ◽  
Coal Slurry ◽  
Two Stage ◽  
Heating Value ◽  
Fuel Distribution ◽  
Entrained Flow ◽  
One Stage ◽  
Gasification Process ◽  
Entrained Flow Gasifier

Numerical simulations of the coal gasification process inside a generic 2-stage entrained-flow gasifier fed with Indonesian coal at approximately 2000 metric ton/day are carried out. The 3D Navier–Stokes equations and eight species transport equations are solved with three heterogeneous global reactions, three homogeneous reactions, and two-step thermal cracking equation of volatiles. The chemical percolation devolatilization (CPD) model is used for the devolatilization process. This study is conducted to investigate the effects of different operation parameters on the gasification process including coal mixture (dry versus slurry), oxidant (oxygen-blown versus air-blown), and different coal distribution between two stages. In the two-stage coal-slurry feed operation, the dominant reactions are intense char combustion in the first stage and enhanced gasification reactions in the second stage. The gas temperature in the first stage for the dry-fed case is about 800 K higher than the slurry-fed case. This calls for attention of additional refractory maintenance in the dry-fed case. One-stage operation yields higher H2, CO and CH4 combined than if a two-stage operation is used, but with a lower syngas heating value. The higher heating value (HHV) of syngas for the one-stage operation is 7.68 MJ/kg, compared with 8.24 MJ/kg for two-stage operation with 75%–25% fuel distribution and 9.03 MJ/kg for two-stage operation with 50%–50% fuel distribution. Carbon conversion efficiency of the air-blown case is 77.3%, which is much lower than that of the oxygen-blown case (99.4%). The syngas heating value for the air-blown case is 4.40 MJ/kg, which is almost half of the heating value of the oxygen-blown case (8.24 MJ/kg).

scholarly journals Experimental Study on Coal Gasification in a Full-Scale Two-Stage Entrained-Flow Gasifier

Energies ◽  
2020 ◽  
Vol 13 (18) ◽  
pp. 4937
Author(s):  
Guangyu Li ◽  
Luping Wang ◽  
Chaowei Wang ◽  
Chang’an Wang ◽  
Ping Wu ◽  
...  
Keyword(s):  
Experimental Study ◽  
Coal Gasification ◽  
Full Scale ◽  
Input Rate ◽  
Two Stage ◽  
Entrained Flow ◽  
Operation Period ◽  
Entrained Flow Gasifier ◽  
Coal Resource ◽  
First Time

In this paper, coal gasification characteristics in the reductor were investigated in a full-scale two-stage pressurized entrained-flow gasifier, which has been seldom conducted previously. The present study aimed at elucidating the effects of gasifying agent concentration, coal input rate, and operation period under full reductor load on the performance of a utility two-stage pressurized entrained-flow gasifier for the first time. When the steam input in the combustor was raised from 3318 kg/h to 5722 kg/h, the total outputs of H2, CO, and CO2 were increased by 1765 Nm3/h and 2063 Nm3/h, respectively, while the CH4 output was decreased by 49 Nm3/h. The coal conversion rate was minimal at low steam input. In addition, more coal gasified in the reductor could increase the output of CH4, while CH4 could reach 1.24% with the coal input in the range of 8000–10,000 kg/h. The present work can offer a further understanding of the gasification performance in the reductor of the full-scale two-stage pressurized entrained-flow gasifier, and motivates the potential for clean utilization of coal resource.

Numerical analysis on the influential factors of coal gasification performance in two-stage entrained flow gasifier

2017 ◽  
Vol 112 ◽  
pp. 1601-1611 ◽  
Author(s):  
Lijun Wang ◽  
YiJun Jia ◽  
Sunel Kumar ◽  
Rundong Li ◽  
Rasool Bux Mahar ◽  
...  
Keyword(s):  
Numerical Analysis ◽  
Coal Gasification ◽  
Influential Factors ◽  
Two Stage ◽  
Entrained Flow ◽  
Entrained Flow Gasifier

Improvement of ash flow properties of low-rank coal for entrained flow gasifier

Fuel ◽  
2014 ◽  
Vol 120 ◽  
pp. 122-129 ◽  
Author(s):  
Lingxue Kong ◽  
Jin Bai ◽  
Zongqing Bai ◽  
Zhenxing Guo ◽  
Wen Li
Keyword(s):  
Low Rank ◽  
Low Rank Coal ◽  
Flow Properties ◽  
Entrained Flow ◽  
Entrained Flow Gasifier

Numerical Simulation of Coal Gasification in a 1 t/h Two-Stage Entrained Flow Gasifier

2007 ◽  
Author(s):  
Min Du ◽  
Yingli Hao ◽  
Yan Wang
Keyword(s):  
Particle Size ◽  
Coal Particle ◽  
Particle Deposition ◽  
Coal Gasification ◽  
Volatile Component ◽  
Operating Conditions ◽  
Two Stage ◽  
Entrained Flow ◽  
Second Stage ◽  
Entrained Flow Gasifier

Coal gasification has received increasing attention in the past two decades due to the growing demand for clean gaseous fuels. Numerical simulations of the coal gasification process inside a two-stage dry feed entrained flow gasifier were carried out using the commercial CFD solver FLUENT. The predicted main product gas components and carbon conversion were in well agreement with the measured data, which verified the validity of the model. A series of calculations were carried out to investigate the effects of operating parameters on the performance of gasifier, including the coal particle size, coal type and coal feeding ratio between the first and the second stages. The flow field, coal particle deposition on the wall, gas temperature and mole fraction inside of the gasifier were analyzed. And the simulation results indicated that the performance of gasifier is improved with decreasing particle size. The low volatile component fraction or high ash content in coal is not propitious to the gasification performance. And the performance of gasifier of the case with coal distribution with 75% (first stage) vs. 25% (second stage) is better than the case with 50% (first stage) vs. 50% (second stage) and the case with 100% for the first stage. The calculation is helpful for designing the operating conditions of the gasifier.

scholarly journals Study on coal gasification with soot formation in two-stage entrained-flow gasifier

2015 ◽  
Vol 6 (3) ◽  
pp. 255-265 ◽  
Author(s):  
Md. Saiful Alam ◽  
Agung Tri Wijayanta ◽  
Koichi Nakaso ◽  
Jun Fukai
Keyword(s):  
Coal Gasification ◽  
Soot Formation ◽  
Two Stage ◽  
Entrained Flow ◽  
Entrained Flow Gasifier

Catalytic effects of ash components in low rank coal gasification

Fuel ◽  
1990 ◽  
Vol 69 (3) ◽  
pp. 275-281 ◽  
Author(s):  
Ralf Köpsel ◽  
Henryk Zabawski
Keyword(s):  
Coal Gasification ◽  
Low Rank ◽  
Low Rank Coal ◽  
Catalytic Effects
Sign in / Sign up

Export Citation Format

Share Document