Effects of different operating parameters on the syngas composition in a two-stage gasification process

2017 ◽  
Vol 109 ◽  
pp. 135-143 ◽  
Author(s):  
Chiou-Liang Lin ◽  
Wang-Chang Weng
Author(s):  
Armin Silaen ◽  
Ting Wang

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).


Author(s):  
Maurizio De Lucia ◽  
Carlo Lanfranchi ◽  
Antonio Matucci

A cogeneration plant with a small gas turbine was installed in a pharmaceutical factory and instrumented for acquiring all the values necessary to appraise both its energetic and cost advantages. The plant was designed and built as a demonstrative project under a program for energy use improvement in industry, partially financed by the European Union. The system comprises as its main components: 1) a gas turbine cogeneration plant for production of power and thermal energy under the form of hot water, superheated water, and steam; 2) a two-stage absorption unit, fueled by the steam produced in the cogeneration plant, for production of cooling thermal energy. The plant was provided with an automatized control system for the acquisition of plant operating parameters. The large amount of data thus provided made it possible to compare the new plant, under actual operating conditions, with the previously existing cooling power station with compression units, and with a traditional power plant. This comparative analysis was based on measurements of the plant operating parameters over nine months, and made it possible to compare actual plant performance with that expected and ISO values. The analysis results reveal that gas turbine performance is greatly affected by part-load as well as ambient temperature conditions. Two-stage absorber performance, moreover, turned out to decrease sharply and more than expected in off-design operating conditions.


2004 ◽  
Vol 27 (3) ◽  
pp. 247-252 ◽  
Author(s):  
Paolo De Filippis ◽  
Carlo Borgianni ◽  
Martino Paolucci ◽  
Fausto Pochetti

1981 ◽  
Vol 11 (6) ◽  
pp. 335-345 ◽  
Author(s):  
JUN-ICHI KAWABATA ◽  
MIDORI YUMIYAMA ◽  
YONESHIRO TAZAKI ◽  
SENJI HONMA ◽  
SHOHEI TAKEDA ◽  
...  

BioResources ◽  
2021 ◽  
Vol 16 (3) ◽  
pp. 5964-5984
Author(s):  
Bin Yang ◽  
Ming Chen

The disposal of automotive shredder residue (ASR) directly affects China’s goal of achieving a 95% recycling rate for end-of-life vehicles. Pyrolysis and gasification have gradually become the most commonly used thermochemical technologies for ASR recycling. To obtain more hydrogen-rich syngas, it is necessary to determine the optimal process parameters of the ASR pyrolysis and gasification process. The main process parameters of the two-stage ASR pyrolysis and gasification process were studied using the established Aspen Plus model. Through analyzing the effects of process parameters, such as the temperature, equivalence ratio, and mass ratio of steam to ASR feedstock, on the product distribution and product characteristics of ASR pyrolysis and gasification, the optimal process parameters were determined. A series of comparative experiments under different conditions were conducted. The experimental results verified the accuracy and reliability of the Aspen Plus simulation model for the ASR pyrolysis and gasification processes and verified the practical feasibility of the process parameters obtained from the simulation analysis.


2017 ◽  
Vol 115 ◽  
pp. 03008
Author(s):  
Viktor Kuznetsov ◽  
Mikhail Chernetskiy ◽  
Nikolay Abaimov ◽  
Alexandr Ryzhkov

2014 ◽  
Vol 53 (18) ◽  
pp. 7611-7621 ◽  
Author(s):  
Yifei Wang ◽  
Weilong Jin ◽  
Longchu Zhu ◽  
Guangsuo Yu ◽  
Zhenghua Dai ◽  
...  

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