M. Bugge, N. Haugen, Tian Li, Jingyuan Zhang, Ø. Skreiberg
{"title":"格栅燃烧装置生物质热分解行为数值模拟方法的验证","authors":"M. Bugge, N. Haugen, Tian Li, Jingyuan Zhang, Ø. Skreiberg","doi":"10.3303/CET2186013","DOIUrl":null,"url":null,"abstract":"The overall objective of the modelling work is to develop CFD aided design tools for optimum grate fired biomass-to-energy (BtE) and waste-to-energy (WtE) plants. An important part of this work has been to develop a flexible detailed transient fuel-bed model taking into account drying, pyrolysis, and char combustion/gasification, for different fuels (i.e. MSW fractions, and softwood and hardwood, including their bark and GROT (branches and treetops)). The fuel-bed model has been implemented in a CFD tool, ANSYS Fluent.The fuel bed consists of a large number of thermally thick particles. In this work, the fuel bed model is made up of representative particles, and the motion of every representative particle is individually tracked (Lagrangian tracking through Fluent's Discrete Phase Model). Thermochemical degradation and conversion of the representative particles are calculated by a thermally thick single particle model (SPM), with boundary conditions obtained from the solutions of the gas phase equations. The SPM model then provides sources to the gas-phase equations. In the modelling approach, the gas phase is solved using the Reynolds Averaged Navier-Stokes (RANS) equations. Under the given conditions, the gas flow in the bed is laminar.The developed model was validated against detailed experimental results from pyrolysis of dried spruce wood pellets in an electrically heated fixed bed reactor, with varying final pyrolysis temperature (600-800°C), heating rate (5-20 K/min) and purge gas composition (none, 100% N2 and 90/10% N2/O2). The experimental results included transient temperature measurements in different locations in the reactor and inside the pellets bed throughout the thermal decomposition process, as well as gas measurements of permanent gases.Through the CFD simulations, the main experimental trends could be reproduced, verifying the validity of the detailed modelling approach. This work is a step towards detailed modelling of biomass grate combustion units, which is required to improve their environmental and energetic performance.","PeriodicalId":9695,"journal":{"name":"Chemical engineering transactions","volume":"65 1","pages":"73-78"},"PeriodicalIF":0.0000,"publicationDate":"2021-06-15","publicationTypes":"Journal Article","fieldsOfStudy":null,"isOpenAccess":false,"openAccessPdf":"","citationCount":"0","resultStr":"{\"title\":\"Validation of a Numerical Approach for Simulation of the Thermal Decomposition Behaviour of Biomass in Grate Combustion Plants\",\"authors\":\"M. Bugge, N. Haugen, Tian Li, Jingyuan Zhang, Ø. Skreiberg\",\"doi\":\"10.3303/CET2186013\",\"DOIUrl\":null,\"url\":null,\"abstract\":\"The overall objective of the modelling work is to develop CFD aided design tools for optimum grate fired biomass-to-energy (BtE) and waste-to-energy (WtE) plants. An important part of this work has been to develop a flexible detailed transient fuel-bed model taking into account drying, pyrolysis, and char combustion/gasification, for different fuels (i.e. MSW fractions, and softwood and hardwood, including their bark and GROT (branches and treetops)). The fuel-bed model has been implemented in a CFD tool, ANSYS Fluent.The fuel bed consists of a large number of thermally thick particles. In this work, the fuel bed model is made up of representative particles, and the motion of every representative particle is individually tracked (Lagrangian tracking through Fluent's Discrete Phase Model). Thermochemical degradation and conversion of the representative particles are calculated by a thermally thick single particle model (SPM), with boundary conditions obtained from the solutions of the gas phase equations. The SPM model then provides sources to the gas-phase equations. In the modelling approach, the gas phase is solved using the Reynolds Averaged Navier-Stokes (RANS) equations. Under the given conditions, the gas flow in the bed is laminar.The developed model was validated against detailed experimental results from pyrolysis of dried spruce wood pellets in an electrically heated fixed bed reactor, with varying final pyrolysis temperature (600-800°C), heating rate (5-20 K/min) and purge gas composition (none, 100% N2 and 90/10% N2/O2). The experimental results included transient temperature measurements in different locations in the reactor and inside the pellets bed throughout the thermal decomposition process, as well as gas measurements of permanent gases.Through the CFD simulations, the main experimental trends could be reproduced, verifying the validity of the detailed modelling approach. This work is a step towards detailed modelling of biomass grate combustion units, which is required to improve their environmental and energetic performance.\",\"PeriodicalId\":9695,\"journal\":{\"name\":\"Chemical engineering transactions\",\"volume\":\"65 1\",\"pages\":\"73-78\"},\"PeriodicalIF\":0.0000,\"publicationDate\":\"2021-06-15\",\"publicationTypes\":\"Journal Article\",\"fieldsOfStudy\":null,\"isOpenAccess\":false,\"openAccessPdf\":\"\",\"citationCount\":\"0\",\"resultStr\":null,\"platform\":\"Semanticscholar\",\"paperid\":null,\"PeriodicalName\":\"Chemical engineering transactions\",\"FirstCategoryId\":\"1085\",\"ListUrlMain\":\"https://doi.org/10.3303/CET2186013\",\"RegionNum\":0,\"RegionCategory\":null,\"ArticlePicture\":[],\"TitleCN\":null,\"AbstractTextCN\":null,\"PMCID\":null,\"EPubDate\":\"\",\"PubModel\":\"\",\"JCR\":\"Q3\",\"JCRName\":\"Chemical Engineering\",\"Score\":null,\"Total\":0}","platform":"Semanticscholar","paperid":null,"PeriodicalName":"Chemical engineering transactions","FirstCategoryId":"1085","ListUrlMain":"https://doi.org/10.3303/CET2186013","RegionNum":0,"RegionCategory":null,"ArticlePicture":[],"TitleCN":null,"AbstractTextCN":null,"PMCID":null,"EPubDate":"","PubModel":"","JCR":"Q3","JCRName":"Chemical Engineering","Score":null,"Total":0}
Validation of a Numerical Approach for Simulation of the Thermal Decomposition Behaviour of Biomass in Grate Combustion Plants
The overall objective of the modelling work is to develop CFD aided design tools for optimum grate fired biomass-to-energy (BtE) and waste-to-energy (WtE) plants. An important part of this work has been to develop a flexible detailed transient fuel-bed model taking into account drying, pyrolysis, and char combustion/gasification, for different fuels (i.e. MSW fractions, and softwood and hardwood, including their bark and GROT (branches and treetops)). The fuel-bed model has been implemented in a CFD tool, ANSYS Fluent.The fuel bed consists of a large number of thermally thick particles. In this work, the fuel bed model is made up of representative particles, and the motion of every representative particle is individually tracked (Lagrangian tracking through Fluent's Discrete Phase Model). Thermochemical degradation and conversion of the representative particles are calculated by a thermally thick single particle model (SPM), with boundary conditions obtained from the solutions of the gas phase equations. The SPM model then provides sources to the gas-phase equations. In the modelling approach, the gas phase is solved using the Reynolds Averaged Navier-Stokes (RANS) equations. Under the given conditions, the gas flow in the bed is laminar.The developed model was validated against detailed experimental results from pyrolysis of dried spruce wood pellets in an electrically heated fixed bed reactor, with varying final pyrolysis temperature (600-800°C), heating rate (5-20 K/min) and purge gas composition (none, 100% N2 and 90/10% N2/O2). The experimental results included transient temperature measurements in different locations in the reactor and inside the pellets bed throughout the thermal decomposition process, as well as gas measurements of permanent gases.Through the CFD simulations, the main experimental trends could be reproduced, verifying the validity of the detailed modelling approach. This work is a step towards detailed modelling of biomass grate combustion units, which is required to improve their environmental and energetic performance.
期刊介绍:
Chemical Engineering Transactions (CET) aims to be a leading international journal for publication of original research and review articles in chemical, process, and environmental engineering. CET begin in 2002 as a vehicle for publication of high-quality papers in chemical engineering, connected with leading international conferences. In 2014, CET opened a new era as an internationally-recognised journal. Articles containing original research results, covering any aspect from molecular phenomena through to industrial case studies and design, with a strong influence of chemical engineering methodologies and ethos are particularly welcome. We encourage state-of-the-art contributions relating to the future of industrial processing, sustainable design, as well as transdisciplinary research that goes beyond the conventional bounds of chemical engineering. Short reviews on hot topics, emerging technologies, and other areas of high interest should highlight unsolved challenges and provide clear directions for future research. The journal publishes periodically with approximately 6 volumes per year. Core topic areas: -Batch processing- Biotechnology- Circular economy and integration- Environmental engineering- Fluid flow and fluid mechanics- Green materials and processing- Heat and mass transfer- Innovation engineering- Life cycle analysis and optimisation- Modelling and simulation- Operations and supply chain management- Particle technology- Process dynamics, flexibility, and control- Process integration and design- Process intensification and optimisation- Process safety- Product development- Reaction engineering- Renewable energy- Separation processes- Smart industry, city, and agriculture- Sustainability- Systems engineering- Thermodynamic- Waste minimisation, processing and management- Water and wastewater engineering