Experimental study on air-stream gasification of biomass micron fuel (BMF) in a cyclone gasifier

Based on biomass micron fuel (BMF) with particle size of less than 250 microm, a cyclone gasifier concept has been considered in our laboratory for biomass gasification. The concept combines and integrates partial oxidation, fast pyrolysis, gasification, and tar cracking, as well as a shift reaction, with the purpose of producing a high quality of gas. In this paper, experiments of BMF air-stream gasification were carried out by the gasifier, with energy for BMF gasification produced by partial combustion of BMF within the gasifier using a hypostoichiometric amount of air. The effects of ER (0.22-0.37) and S/B (0.15-0.59) and biomass particle size on the performances of BMF gasification and the gasification temperature were studied. Under the experimental conditions, the temperature, gas yields, LHV of the gas fuel, carbon conversion efficiency, stream decomposition and gasification efficiency varied in the range of 586-845 degrees C, 1.42-2.21 N m(3)/kg biomass, 3806-4921 kJ/m(3), 54.44%-85.45%, 37.98%-70.72%, and 36.35%-56.55%, respectively. The experimental results showed that the gasification performance was best with ER being 3.7 and S/B being 0.31 and smaller particle, as well as H(2)-content. And the BMF gasification by air and low temperature stream in the cyclone gasifier with the energy self-sufficiency is reliable.     

Gasification of biomass/high density polyethylene mixtures in a downdraft gasifier

In this work, an experimental study of the thermal decomposition of mixtures of wood particles and high density polyethylene in different atmospheres has been carried out in a downdraft gasifier with a nominal processing capacity of 50 kg/h. The main objective was to study the feasibility of the operation of the gasification plant using mixtures and to investigate the characteristics of the gas obtained. In order to do so, experiments with biomass only and with mixtures with up to 15% HDPE have been carried out. The main components of the gas generated are N₂ (50%), H₂ (14%), CO (9–22%) and CO₂ (7–17%) and its relatively high calorific value was adequate for using it in an internal combustion engine generator consisting of a modified diesel engine coupled with a 25 kV A alternator.     

Biomass gasification: Development cooperation in Belgium

Development cooperation in the field of biomass gasification between Belgium and the Developing Countries, Indonesia and Zaire is discussed. Results from the fluidized-bed gasification of Eucalyptus deglupta wood in Indonesia and the testing of a moving-bed gasifier in a remote location in Zaire are presented. The impact of these technologies on the rural communities is analyzed.     

Fermentation of biomass-generated producer gas to ethanol

The development of low-cost, sustainable, and renewable energy sources has been a major focus since the 1970s. Fuel-grade ethanol is one energy source that has great potential for being generated from biomass. The demonstration of the fermentation of biomass-generated producer gas to ethanol is the major focus of this article in addition to assessing the effects of producer gas on the fermentation process. In this work, producer gas (primarily CO, CO(2), CH(4), H(2), and N(2)) was generated from switchgrass via gasification. The fluidized-bed gasifier generated gas with a composition of 56.8% N(2), 14.7% CO, 16.5% CO(2), 4.4% H(2), and 4.2% CH(4). The producer gas was utilized in a 4-L bioreactor to generate ethanol and other products via fermentation using a novel clostridial bacterium. The effects of biomass-generated producer gas on cell concentration, hydrogen uptake, and acid/alcohol production are shown in comparison with "clean" bottled gases of similar compositions for CO, CO(2), and H(2). The successful implementation of generating producer gas from biomass and then fermenting the producer gas to ethanol was demonstrated. Several key findings following the introduction of producer gas included: (1) the cells stopped growing but were still viable, (2) ethanol was primarily produced once the cells stopped growing (ethanol is nongrowth associated), (3) H(2) utilization stopped, and (4) cells began growing again if "clean" bottled gases were introduced following exposure to the producer gas.     

Influence of switchgrass generated producer gas pre-adaptation on growth and product distribution of Clostridium ragsdalei

Gasification-fermentation is a thermo chemical-biological process for the production of fuels and chemicals. Producer gas cleanup is a major issue that must be addressed for integration of these platforms. Pre-adaptation of producer gas fermenting microbes to gas impurities has improved tolerances to impurities and production of alcohols in certain bacteria. In this research, the effect of switchgrass generated producer gas was studied with adapted and unadapted cultures of C. ragsdalei and compared to fermentations with a control of clean custom producer gas. Results indicated no inhibition to microbial growth with unadapted cells and final cell mass concentrations were 22% higher when cells were exposed to switchgrass-based producer gas compared to control. The ethanol productivity with adapted cells was 1.9 and 2.8 times higher than unadapted and control treatments, respectively. Similarly, the ethanol yield (Y_ETOH/X) of C. ragsdalei adapted to producer gas was 119% more than the control and 35% greater than the unadapted cells used in this study. The presence of switchgrass-based producer gas also induced metabolic shifts resulting in reduction of acetic acid to ethanol that increased ethanol to acetate ratios from 0.7 g/g in control to 4.9 g/g with unadapted cells and 13.7 g/g with adapted cells. Isopropanol was also observed as a product when switchgrass generated producer gas was used. We conclude that cultural adaptation of C. ragsdalei to biomass generated producer gas during preculture stages could be used as an important strategy to enhance ethanol yields for integrating gasification and fermentation platforms using C. ragsdalei.     

Italian activities in biomass gasification

The role of ENEA (Italian Commission for Nuclear and Alternative Energy Sources) in supporting and promoting technological research in biomass gasification is illustrated. The main interests are: (a) biomass (wood and agricultural residues) gasificaiton for its application in the Developing Countries and/or in specific industrial applications and (b) RDF gasification as an energy supply for some industrial sectors. The more active Italian firms involved in manufacturing gasifiers are indicated. The performance of several producer gas systems has been examined and experimental tests have been carried out for long-term operation in field trials.Standards and procedures for the evaluation of technical performance and safety requirements of wood gasifiers have been developed and tested.     

Simulation of biomass gasification with a hybrid neural network model

Gasification of several types of biomass has been conducted in a fluidized bed gasifier at atmospheric pressure with steam as the fluidizing medium. In order to obtain the gasification profiles for each type of biomass, an artificial neural network model has been developed to simulate this gasification processes. Model-predicted gas production rates in this biomass gasification processes were consistent with the experimental data. Therefore, the gasification profiles generated by neural networks are considered to have properly reflected the real gasification process of a biomass. Gasification profiles identified by neural network suggest that gasification behavior of arboreal types of biomass is significantly different from that of herbaceous ones.     

Fluidized-bed steam gasification of rice hull

Steam gasification of grain by-products can be a significant biomass conversion technology because of the need to utilize agricultural waste for non-food applications including energy resources. The most obvious beneficiary will be the developing countries whose economies are often tied to agricultural produce and are lacking in conventional fuels. One agricultural by-product that shows promise is the rice hull; it is found in abundance in the rice mills of producer countries and is considered as a waste material. Although gasification of rice hull has been proposed as a potential waste disposal and energy recovery method, little has been done to fully realize this proposition. In the present work, data were obtained for steam gasification of rice hull in a bench-scale fluidized-bed gasifier, a technology which has proven to be feasible for other grain by-products. The produced gas, which is rich in hydrogen, has been found to have a heating value ranging between 12.1 and 11.1 MJ m⁻³ at the respective reactor temperatures of 700 and 800°C; energy recovery varies between 35 and 59%.     

Energy production from biomass (Part 3): Gasification technologies

The conversion of biomass by gasification into a fuel suitable for use in a gas engine increases greatly the potential usefulness of biomass as a renewable resource. Gasification is a robust proven technology that can be operated either as a simple, low technology system based on a fixed-bed gasifier, or as a more sophisticated system using fluidized-bed technology. The properties of the biomass feedstock and its preparation are key design parameters when selecting the gasifier system. Electricity generation using a gas engine operating on gas produced by the gasification of biomass is applicable equally to both the developed world (as a means of reducing greenhouse gas emissions by replacing fossil fuel) and to the developing world (by providing electricity in rural areas derived from traditional biomass).     

Status of peat and biomass gasification in Finland

Research and development into the gasification of solid fuels in Finland are focused on the utilization of indigenous fuels: peat and biomass. Development work is concentrated on the production of low-Btu gas. The Bioneer fixed-bed gasifier and the Pyroflow circulating fluidized-bed gasifier offer flexible and reliable operation coupled to boilers, dryers and lime kilns in the range 1–10 MW and 5–100 MW thermal effect, respectively.     

Biomass gasification research and field developments by the Prince of Songkla University,Thailand

Studies on the production and utilization of producer gas from charcoal, wood and several types of crop residues have been undertaken at the Department of Mechanical Engineering, Prince of Songkla University. Details of the gasification systems suitable for operation on various types of fuels together with their performance are presented. Based on the results from the tests carried out at the University and data from the field trials, the technical and economic feasibility of biomass gasification technology is discussed. In addition, some practical aspects and problems concerning the performance, operation and maintenance of the gasification systems operating on difficult fuels are also discussed.     

Operational characteristics of a 1.2-MW biomass gasification and power generation plant

In this study, we analyzed the operational characteristics of a 1.2-MW rice husk gasification and power generation plant located in Changxing, Zhejiang province, China. The influences of gasification temperature, equivalence ratio (ER), feeding rate and rice husk water content on the gasification characteristics in a fluidized bed gasifier were investigated. The axial temperature profile in the dense phase of the gasifier showed that inadequate fluidization occurred inside the bed, and that the temperature was closely related to changes in ER and feeding rate. The bed temperature increased linearly with increasing ER when the feeding rate was kept constant, while a higher feeding rate corresponded to a lower bed temperature at fixed ER. The gas heating value decreased with increasing temperature, while the feeding rate had little effect. When the gasification temperature was 700–800 °C, the gas heating value ranged from 5450–6400 kJ/Nm³. The water content of the rice husk had an obvious influence on the operation of the gasifier: increases in water content up to 15% resulted in increasing ER and gas yield, while water contents above 15% caused aberrant temperature fluctuations. The problems in this plant are discussed in the light of operational experience of MW-scale biomass gasification and power generation plants.     

Experimental study on cyclone air gasification of wood powder

In this paper, effects of the equivalence ratio (ER) and the secondary air on the gasification system were studied. The results indicate that as the ER varies in the range of 0.20–0.26, the low heating value (LHV) of the producer gas is in the range of 3.64–5.76 MJ/Nm³, the carbon conversion is 55%–67% and the cold gas efficiency of the gasification system is 33%–47%. In contrast to the gasification without the secondary air, air staged process is a gasification method capable of increasing the LHV of the producer gas from 4.63 to 5.67 MJ/Nm³, the carbon conversion from 65.5% to 81.2%, and the cold gas efficiency of the gasifier from 42.5% to 56.87%, while the tar content of the producer gas decreases from 13.96 to 5.6 g/Nm³. There exists an optimum ratio of the secondary air.     

Energy and exergy analyses of a biomass-based hydrogen production system

In this paper, a novel biomass-based hydrogen production plant is investigated. The system uses oil palm shell as a feedstock. The main plant processes are biomass gasification, steam methane reforming and shift reaction. The modeling of the gasifier uses the Gibbs free energy minimization approach and chemical equilibrium considerations. The plant, with modifications, is simulated and analyzed thermodynamically using the Aspen Plus process simulation code (version 11.1). Exergy analysis, a useful tool for understanding and improving efficiency, is used throughout the investigation, in addition to energy analysis. The overall performance of the system is evaluated, and its efficiencies become 19% for exergy efficiency and 22% energy efficiency while the gasifier cold gas efficiency is 18%.     

Biomass–oxygen gasification in a high-temperature entrained-flow gasifier

The technology associated with indirect biomass liquefaction is currently arousing increased attention, as it could ensure a supply of transportation fuels and reduce the use of petroleum. The characteristics of biomass–oxygen gasification in a bench-scale laminar entrained-flow gasifier were studied in the paper. Experiments were carried out to investigate the influence of some key factors, including reaction temperature, residence time and oxygen/biomass ratio, on the gasification. The results indicated that higher temperature favored H₂ and CO production. Cold gas efficiency was improved by > 10% when the temperature was increased from 1000 to 1400 °C. The carbon conversion increased and the syngas quality was improved with increasing residence time. A shorter residence resulted in incomplete gasification. An optimal residence time of 1.6 s was identified in this study. The introduction of oxygen to the gasifier strengthened the gasification and improved the carbon conversion, but lowered the lower heating value and the H₂/CO ratio of the syngas. The optimal oxygen/biomass ratio in this study was 0.4. The results of this study will help to improve our understanding of syngas production by biomass high-temperature gasification.     

Influence of operation conditions and additives on the development of producer gas and tar reduction in air gasification of construction woody wastes using a two-stage gasifier

Air gasification was conducted with fractions of construction woody wastes in a two-stage gasifier, consisting of a fluidized bed zone and a tar cracking zone. The aim of this work is to investigate the influence of reaction conditions and additives on the composition of producer gas and tar content in producer gas.A producer gas obtained with activated carbon of 540 g at an ER of 0.26 was mainly composed of H₂ (25 vol.%), CO (22 vol.%) and CH₄ (5 vol.%). Regarding tar removal efficiency, activated carbon was better than olivine. The tar removal rate with virgin activated carbon reached up to 80%. The reuse of spent activated carbon caused an efficiency loss in tar removal to some extent. Overall, it seems that the strong need for intensive downstream tar removal measurements can be removed with the use of a two-stage gasifier and the application of activated carbon.     

Experimental study of wood downdraft gasification for an improved producer gas quality through an innovative two-stage air and premixed air/gas supply approach

This study conducted experiments on three different downdraft gasification approaches: single stage, conventional two-stage, and an innovative two-stage air and premixed air/gas supply approach. The innovative two-stage approach has two nozzle locations, one for air supply at combustion zone and the other located at the pyrolysis zone for supplying the premixed gas (air and producer gas). The producer gas is partially bypassed to mix with air and supplied to burn at the pyrolysis zone. The result shows that producer gas quality generated by the innovative two-stage approach improved as compared to conventional two-stage. The higher heating value (HHV) increased from 5.4 to 6.5 MJ/Nm³. Tar content in producer gas reduced to less than 45 mg/Nm³. With this approach, gas can be fed directly to an internal combustion engine. Furthermore, the gasification thermal efficiency also improved by approximately 14%. The approach gave double benefits on gas qualities and energy savings.     

生态设计家具的碳足迹核算与减排效果分析——以木质家具为例

我国的木质家具不仅产量大,而且碳排放强度也相对较高,利用生态设计理念可以降低木质家具的碳足迹。为了定量化生态设计所带来的减排效果,按照减少资源消耗和环境污染、节省住宅空间等木质家具生态设计原则,通过在一款多功能家具的框架内安装不同面板,形成了4种不同材质和结构的设计方案,利用生命周期分析方法核算了4种方案的碳足迹,并进一步量化了改进方案的减排效果。结果表明:4种家具设计的碳足迹从小到大为三聚氰胺板家具、木皮板家具、拼板家具、嵌条板家具,其中,实木类家具原材料碳排放较低,人造板类家具加工过程电力碳排放较低(主要来源于喷涂工段,占电力排放的83%—92%);通过各种减排方案的减排效果分析,发现采用"可拆卸无胶连接方式"改进方案减排效果显为明显;同时发现,合理的"低碳设计"(采用以实木板为基板,以三聚氰胺纸为贴面制作面板),可以避免中纤板喷涂过程的碳排放,从而减少产品整体碳足迹。     

A novel reforming method for hydrogen production from biomass steam gasification

In this work, an experimental study of biomass gasification in different operation conditions has been carried out in an updraft gasifier combined with a porous ceramic reformer. The effects of gasifier temperature, steam to biomass ratio (S/B), and reforming temperature on the gas characteristic parameters were investigated with and without porous ceramic filled in reformer. The results indicated that considerable synergistics effects were observed as the porous ceramic was filled in reformer leading to an increase in the hydrogen production. With the increasing gasifier temperature varying from 800 to 950 °C, hydrogen yield increased from 49.97 to 79.91 g H₂/kg biomass. Steam/biomass ratio of 2.05 seemed to be optimal in all steam-gasification runs. The effect of reforming temperature for water-soluble tar produced in porous ceramic reforming was also investigated, and it was found that the conversion ratio of total organic carbon (TOC) contents is between 71.08% and 75.74%.     

Biomass downdraft gasifier with internal cyclonic combustion chamber: design, construction, and experimental results

An exploratory downdraft gasifier design with unique biomass pyrolysis and tar cracking mechanism is evolved at Oklahoma State University. This design has an internal separate combustion section where turbulent, swirling high-temperature combustion flows are generated. A series of research trials were conducted using wood shavings as the gasifier feedstock. Maximum tar cracking temperatures were above 1100°C. Average volumetric concentration levels of major combustible components in the product gas were 22% CO and 11% H(2). Hot and cold gas efficiencies were 72% and 66%, respectively.