Fluidized Bed Gasifier Research Articles

Performance analysis of a novel biomass gasification system coupled to a coal-fired power plant based on heat and water recovery

Biomass gasification co-firing is a technology that can be implemented instantly in almost all coal-fired power plants in a relatively short period to reduce the consumption of fossil fuel. Most studies have focused on improving the system according to variations in the gasification conditions, biomass types, co-firing ratio, and boiler loads. However, the whole system process analysis and structural improvement based on the matter and energy of the co-firing system require further investigation. In this study, a novel biomass air–steam circulating fluidized bed gasification co-firing system based on waste heat and flue gas water recovery with different co-firing ratios (approximately 10 %–40 %) was simulated and compared with the original air gasification co-firing system using Aspen Plus software. The impacts of recovered water participate in gasification process and the optimal steam to biomass ratio (S/B) when it varied from 0.5 to 2, on the syngas quality, thermal characteristics of flue gas, recovered water, coal consumption, exergy loss, and efficiency of the system were analyzed. Compared with the air gasification co-firing system, the results showed that the N2 content in syngas reduced from 41.14 % to 28.92 %, and the heat yield of syngas increased by 7.73 %, along with a 110 t/h recovered water surplus at a 40 % co-firing ratio when steam to biomass ratio was equal to 1. The maximum coal saving amount was 2.26–9.11 t/h and the volume of atmospheric pollutants emissions, such as carbon dioxide (CO2), sulfur oxides (SOx) and nitrogen oxides (NOx), reduced by 0.95 %–6.02 %, 0.91 %–0.95 %, and 11.38 %–36.47 % at a co-firing ratio of approximately 10 %–40 %. Furthermore, the exergy loss can be reduced by 4.35 %–10 % with a 1.72 %–3.96 % increase in exergy efficiency, indicating that the new system mode improves the comprehensive performance of the co-firing system.

Catalytic Gasification and Reforming of Residual Biomass in a Bench Scale System with Low Cost Catalysts.

This paper demonstrates the effectiveness of using of different catalysts for reforming tars contained in the syngas of biomass gasifiers. The conversion of the tar content allows to obtain high quality syngas and to maximize the gas fraction. A bench scale equipment consisting of an autothermal fluidized bed gasifier and a downstream packed bed reformer was used. Pine sawdust was selected as the feedstock for gasification. TGA analysis showed that the temperature must be above 350 °C to ensure the ignition of the biomass and maintain the process in an autothermal steady-state. Dolomite and pyrolysis char were used to test of the fluidized bed catalysts. In the reformer, dolomite, pyrolysis char, iron doped activated carbon and spent HDS catalyst were used. All catalysts decreased the CO2 concentration in the product gas and increased H2 , CH4 and CO. When iron doped activated carbon is used, tar contents below 60 g/Nm3 in the product gas could be obtained, reaching less than 1 g/Nm3 . The best value of LHV (lower heating value) was obtained with pyrolysis char as a catalyst (4.8 MJ/Nm3 ). The results demonstrate that catalytic biomass gasification with downstream tar reforming with low-cost catalysts is a promising solution for energy applications.

Enrichment of fuel properties of biomass using non-oxidative torrefaction for gasification

The abundance and replenishment nature of solid biomass prompt fuel substitution for gasification and thermal power plants. However, many challenges are encountered while utilizing raw biomass, such as seasonality, strong hydrophilicity, low bulk and energy density, excess oxygen content, less compositional homogeneity, and poor grindability. It is, therefore, indispensable to augment the thermo-chemical properties of the solid biomass by performing suitable pretreatment. Among the various pretreatment techniques, non-oxidative torrefaction effectively upgrades solid biomass to coal-like fuel altering its physico-chemical properties. Therefore, in this work, torrefaction of rice husk and sugarcane bagasse have been performed in a fixed bed reactor by varying temperatures from 210–330 °C and residence time from 30–60 min under a non-oxidative environment. The experimental investigation illustrates a decrease in mass and energy yield of the biomass with a rise in temperature and residence time. Conversely, the higher heating value of rice husk and sugarcane bagasse has improved by 119.4% and 128.9%, respectively. The hydrogen-to-carbon (H/C) and oxygen-to-carbon (O/C) ratio of the torrefied biomass has reduced to enriched fuel variety as indicated by the van Krevelen plot. The decomposition and structural modifications were assessed using Fourier transform infrared spectroscopy, x-ray diffraction, and morphology analysis. Based on the experimental observations, it has been found that torrefaction of rice husk at 290 °C and 30 min and sugarcane bagasse at 270 °C and 30 min would generate enriched syngas using a dual fluidized bed gasification system. Furthermore, water gas shift reactions will be promoted to enhance the percentage of hydrogen in the gas mixture.

Gasification characteristics of refuse derived fuels in a fluidized bed: Effect of process parameters and catalytic reforming

Managing municipal solid waste and providing sustainable energy are major challenges faced globally. Although the gasification of solid waste into syngas is a viable solution, the presence of high tar content and low quality syngas hinder technological advancements. In this study, the gasification of refuse derived fuels was performed on a fluidized bed and the impact of temperature, oxygen concentration (OP), steam/RDF ratio (S/R), equivalence ratio (ER), and catalytic reforming on the quality of syngas was investigated. The results indicate that the optimal gasification efficiency and the highest lower heat value of syngas occur at 850 °C. The gasification process is most efficient when the ER = 0.23. Gasification with enriched oxygen significantly improves the syngas quality. OP increased from 21 % to 40 %, syngas lower heat value increased by 112 %, and H2 increased by 76.4 %. The addition of water vapor under oxygen enriched conditions (OP = 40 %) promotes the generation of hydrogen-rich syngas. At an S/R of 0.73, the H2 reached a notable 21.3 %. Finally, the reformation of syngas is catalyzed using a Ni-based catalyst co-modified with Ce and La. The findings showed that the H2 increased by 3.27 % following catalytic reforming. Additionally, the syngas yield increased by 13 %, and the tar removal rate of 91.5 %. This study's findings apply to optimizing the fluidized bed gasification of refuse derived fuels.

Influence of distributor plate design on mixing characteristics of rice husk biomass in a bubbling fluidized bed gasifier: An experimental and CFD study

This study investigates the mixing characteristics of rice husk biomass in a bubbling fluidized bed gasifier (BFBG) using different distributor plates: perforated, 45° slotted, and hybrid plates. The study explores the fluidization characteristics of a biomass/sand mixture using three distributor plates, observing the maximum difference in initial minimum fluidization velocity (Umf,i) and final minimum fluidization velocity (Umf,f) for perforated plate, indicating axial mixing and segregation, while the 45° slotted plate represents uniform bed expansion and fluidization, and the hybrid plate exhibits an intermediate behavior. Axial and lateral biomass distribution is also studied, and it is found that with the 45° slotted plate the highest axial distribution of rice husk is observed at the lower portion due to lateral and swirling flow whereas perforated plate causes the highest deviation at the lower portion but approaches ideal mixing at the mid and upper sections due to axial dominant flow. The hybrid plate exhibits a blend of axial and lateral flows, resulting in intermediate axial distribution at lower and upper section of gasifier. Radially, the perforated plate has the highest concentration of biomass at maximum height whereas the 45° slotted plate has concentration near the walls, and the hybrid plate has optimal mixing throughout. The hybrid plate also achieves the highest mixing index at all air velocities. Overall, the study provides insights into biomass mixing in BFBGs and highlights the superior performance of the hybrid distributor plate.The CFD study also carried out to complement the experimental results in terms of pressure drop and mixing behavior by employing different distributor plats. Multiphase two fluid model (TFM) with kinetic theory of granular flow has been employed for CFD simulations with the engagement of k-epsilon turbulence model. The simulation results are in good agreement with experimental results in terms of bed pressure drop quantitatively and mixing characteristics of rice husk biomass qualitatively.

Flow regimes and transitions in an ultra-high temperature gas-solid fluidized bed

Gas-solid fluidized bed reactors are widely used in industrial operations and thus have led to a significant amount of fundamental research over decades. For better design and operation of fluidized bed systems, it is essential to understand the fluidization regime and the related transition conditions. Dr. John R. Grace, a prominent figure and pioneer in fluidization science and technology, has made significant contributions to understanding fluidized bed systems, including fluidization regimes and their transitions. This study is a tribute to his extraordinary legacy, focusing on investigations of fluidization regimes and transitions in a laboratory-scale gas-fluidized bed operating from ambient to 1600 °C. The results indicate that the fluidization regime transitions follow three distinct pathways across different temperature ranges: below 300 °C, from 300 to 1400 °C, and above 1400 °C. These distinctive transitions arise as a result of the varying significances of hydrodynamic and interparticle forces in the fluidized bed of particles investigated.

Energetic Assessment of SCWG Experiments with Reed Canary Grass and Ethanol Solution on Laboratory and Pilot Scale

The energetic assessment of biomass conversion processes is important for evaluating their application potential. Process energy efficiency is often evaluated based on simulation results for processes under idealized conditions. The present work uses data from a laboratory plant to perform an evaluation of the supercritical water gasification (SCWG). For this purpose, experiments were conducted with two types of feedstock, Reed Canary Grass and ethanol. Under the present lab-plant configuration, a cold gas efficiency of up to 79% could be reached, which is comparable to the gasification of biomass in fluidized-bed gasifiers or entrained-flow gasifiers. Based on the obtained data on the produced substances and their distribution, a scale up to pilot plant size was conducted. A model was derived from the available data to energetically assess different SCWG plant sizes based on real laboratory results. This model can be transferred to other feedstocks and other process designs to approximate the optimal size for the used biomass feedstock. The importance of heat recuperation in this process is described in detail based on pilot-scale data.

Bubbling fluidized bed co-combustion and co-gasification of sewage sludge with agricultural residues with a focus on the fate of phosphorus

In this work, the fate of the ash-forming elements during bubbling fluidized bed combustion and gasification of P-rich sewage sludge (SS) and mixtures with either Si-K-rich wheat straw (WS) or K-Ca-rich sunflower husks (SH) were investigated. The focus of the study was assessing the feasibility of using fuel blends in fluidized bed systems and potential P recovery from the resulting ashes. The used fuels were pure SS and mixtures including 90 wt.% WS (WSS) and 85 wt.% SH (SHS). The analyzed operating conditions were combustion (930–960 °C, λ: 1.2–1.5) and gasification (780–810 °C, λ: 0.4–0.7) in a 5 kW bench-scale reactor. Residual ash and char fractions were collected from different parts of the 5 kW bubbling fluidized bed (bed, cyclone, filter) and analyzed by CHN, SEM/EDS, XRD, and ICP-AES.The conversion of the fuel mixtures achieved a steady state under the used process conditions except for the combustion of WSS, which led to the formation of large bed agglomerates with the bed material. The morphology of ash samples after combustion showed that SS fuel pellets mostly maintained their integrity during the experiment. In contrast, the ash and char particles from fuel mixtures were fragmented, and larger quantities were found in the cyclone, the filter, or on interior reactor surfaces. The fate of P was dominated by crystalline Ca-dominated whitlockites in all ash fractions, partially including K for the fuel mixtures SHS and WSS. 76–81 % of ingoing P was found in the bed residue after combustion and gasification of the SS-fuel. After conversion of the fuel mixtures SHS and WSS, the share was lower at 22–48 %, with larger shares of P in the entrained fractions (25–34 %). The quantity of identified crystalline compounds was lower after gasification than combustion, likely due to the limited interaction of ash-forming elements in the residual CHN matrix. Altogether, the results show that fuel mixtures of sewage sludge with agricultural residues could expand the fuel feedstock and enable P recovery. This may be used in the fuel and process design of upscaled fluidized bed processes or systems employing both combustion and gasification.

Development of a multiphase chemical reactor network method as a tool for simulating biomass gasification in fluidized beds

In the near future, biomass is expected to be a key resource for fulfilling clean energy requirements. The predictive modeling of biomass conversion in industrial systems is still challenging due to the multi-scale nature of the processes involved, including complex chemical reactions. To provide a detailed description and analysis of these reactions and their coupling to transport phenomena in large-scale systems, this work introduces a multiphase reactor network method incorporating efficient solution algorithms for engineering reacting systems. The method developed includes a novel multiphase solid–gas perfectly stirred reactor (sPSR) model capable of handling solid- and gas-phase reactions as well as heterogeneous reactions, in a fully coupled way. The sPSR approach, which is included in reactor networks with various levels of complexity, improves the analysis and understanding of physical and chemical phenomena occurring in gasifiers. Steam and air gasification experiments are analyzed using the new approach and fundamental differences and effects are revealed. Major findings include the importance of solid–gas coupling, char conversion reactions, and water–gas shift (WGS) reaction catalysis due to bio-ash. In addition, increasing the complexity of the reactor network achieves a better reproduction of the mixing behavior. The capability of handling complex reactor networks with detailed kinetics paves the way for efficient designs and improved reactors.

Numerical investigation on the influence of immersed tube bundles on biomass gasification in industrial-scale dual fluidized bed gasifier

Immersed tubes play a pivotal role in enhancing fluidization quality within fluidized beds by effectively disrupting bubbles. However, the effect of such internals within a large-scale gasification apparatus remains unclear. Consequently, this study focuses on numerically simulating biomass steam gasification within an industrial-scale dual fluidized bed gasifier that features immersed tube bundles using the multiphase particle-in-cell method. In this method, particles with identical properties are grouped, and the interparticle collisions are model via the solid stress to improve computational efficiency. The numerical model has been well verified with experiment in terms of bed pressure drop, solid recirculation and chemical reactions. Some main conclusions are shown as follows. Immersed tubes significantly alter the motion of gas and particles in the gasifier. The presence of immersed tubes can ameliorate solid entrainment and avoid excess particles escaping from the gasifier. The asymmetrical structure of the gasifier results in asymmetrical distribution of gas temperature and gas species. Increasing the number of immersed tubes slightly enhances particle temperature near the loop seal outlet. The radial biomass dispersion coefficient and axial sand dispersion coefficient decrease about 40.9 % and 28.9 % when increasing the immersed tube number from three to nine. The results provide enhanced understanding of the role of immersed tubes in altering gas-particle interactions and fluidization dynamics in industrial-scale fluidized bed gasifier.

Prediction of syngas properties of biomass steam gasification in fluidized bed based on machine learning method

Steam gasification of biomass is a promising technology to produce hydrogen-rich syngas. While the complex correlation between gasification process and syngas properties has not been effectively explained. In this study, 222 relevant experimental data from peer-reviewed publications was collected to predict the syngas properties in fluidized bed reactors by machine learning (ML) method. Five algorithms were adopted and the Extreme Gradient Boosting regression (XGBoost) showed the most consistent predictive performance with the testing R2 of 0.89–0.92. The equivalent ratio (ER) and steam to biomass ratio (S/B) were the most significant determinants of H2 concentration. Optimal H2 production (around 45%) was achieved by favorably choosing operating conditions characterized by the range of ER < 0.08 and 1 < S/B < 2.5. The valuable insights provided by ML models may contribute to the better understanding of biomass steam gasification process for the H2-rich syngas production.

Full-Loop Study of a Pilot-Scale Dual Fluidized Bed Cold Flow System: Hydrodynamic Simulation

Computational particle fluid dynamics (CPFD) simulations of three-dimensional cold-flow gas-solid flow were performed for a pilot-scale dual-circulating fluidized bed (DCFB) using Barracuda Virtual Reactor® 17.4.0. This DCFB system is a fluidized bed gasifier used in a calcium-loop gasification process to produce a hydrogen-rich gas with CO2 capture. The effects of different bubble bed inlet airflow rates and different solid inventories on the full-loop pressure distribution and particle concentration distribution were compared. The increase in the bubble bed inlet airflow rate significantly increases the pressure in the bubble bed and lift pipe, and the increase in the solids inventory significantly increases the pressure where the solids are tightly packed. For long-term operation, the appropriate combination of parameters should be found to maintain a stable particle seal at the loopseals.

A techno-economic study on the co-production of syngas and activated carbon from waste tyre gasification process

Waste tyre gasification offers a variety of benefits amongst which include the production of syngas—an alternate source of energy generation and activated carbon (AC)—a very good adsorbent used in industrial purification processes. In this study, a conceptual design of an industrial production plant design process and economic analysis of waste tyre gasification process for the co-production of syngas and AC were evaluated. Three reactor configurations namely: fluidized bed, fixed bed, and rotary kiln gasifiers were investigated in the design process. The design process put into consideration the total plant cost (TPC), total capital investment (TCI), the cost of raw materials, waste disposal cost, amongst other vital economic parameters. The fixed bed reactor has the highest syngas and AC production with 10,130 kg/h and 214.61 kg/h, respectively when compared to the other gasifiers. The minimum selling price (MSP) of syngas was set as 1$/kg and AC was set at $2/kg. The result obtained shows that the fixed bed production route was the most economical amongst the three reactor configurations considered. The fixed bed route has a net present value (NPV) of 435 M$, return on investment (ROI) of 56%, internal rate of return (IRR) of 54%, and a payback period (PBP) of 4.86 years. Finally, a sensitivity analysis considering a pm 20% variation in key economic parameters such as the syngas MSP, inflation rate, interest rate, tax rate, operating expenditure (OPEX), and capital expenditure (CAPEX) amongst others was investigated. The analysis shows that the syngas MSP, OPEX, inflation rate, and CAPEX have the most effect on the NPV of the waste tyre gasification process.

Catalytic steam gasification of soy hull pellets in a fluidized bed gasifier

The catalytic effects of inherent alkali-based metal catalysts present in biomass residues on biomass pellets were explored in this work. Gasification experiments were carried out in a pilot scale fluidized bed gasifier in the presence of alkali metal catalysts. By using a response surface methodology experimental design technique, soy hull biomass pellets were subjected to steam gasification within a temperature range of 750–950 °C. Additionally, the effects of steam-to-biomass (S/B) ratio and the catalyst loading on the gas and tar yields, and gaseous compositions were investigated. It was found that lower temperature resulted in the formation of more tar residue since the temperature was insufficient to crack the tar formed. Lower S/B ratio led to increased tar yield. Addition of catalyst significantly reduced the tar residue produced during the gasification experiments. An increase in the catalyst loading led to a steady decrease in the tar yield with up to 52% reduction at 950 °C. Further increasing catalyst loading beyond 5% had no significant effect on tar reduction. Gas yield increased slightly with catalytic gasification of the biomass pellets compared to the non-catalyzed reactions earlier studied. The reaction mechanism of the catalyzed reactions and effect on tar decomposition were discussed. Catalytic effects on tar composition were also investigated. The results from these experiments provide further insight into considering co-pelletization of catalysts during production of pellets for better gasification performance in terms of increased yields of the major gaseous components.

Optimizing Design and Operational Parameters for Enhanced Mixing and Hydrodynamics in Bubbling Fluidized Bed Gasifiers: An Experimental and CFD-Based Approach

An experimental investigation of hydrodynamics of gas-solid flow is carried out by engaging different designs of air distributor plates. An analysis of three different plates, i.e., perforated, 45° slotted and novel hybrid plate, revealed the difference in pressure drop and minimum fluidization velocities (Umf) for varying input operational variables. Umf is found to be lowest for perforated and highest for 45° slotted plate, whereas pressure drop is found to be highest for 45° slotted plate and lowest for novel hybrid distributor plate. The bubbles rise velocity ratio (Umf,b/Umf,f) is noticed minimum for 45° slotted plate due to relatively larger bubbles originating from the bigger slot openings and maximum for perforated distributor plate owing to smaller bubbles with dominant axial rise. Furthermore, the bed height rise ratio (h/L) is observed as a minimum for perforated distributor and maximum for 45° slotted plate due to larger bubbles through 45° slots rupturing the bed surface, causing more bed expansion. Furthermore, CFD analysis is also carried out to observe the insight flow dynamics using the distributor plates. The simulations use a two-fluid model (TFM) and K-Epsilon turbulence models. CFD model shows promising results in agreement with the experimental results. CFD results revealed that the lower portion enhanced lateral dispersion/mixing of solid particles due to 45° angular openings of an air inlet. In contrast, the perforated plate exhibited a straight upward motion of small air bubbles, causing no radial/lateral mixing. CFD results for the hybrid plate show the mixed axial as well as lateral mixing of solids by revealing velocity distribution; therefore, the novel hybrid plate is found to be an optimum distributor plate due to its lowest pressure drop, adequate Umf, intermediary bed height rise ratio and moderate bubble rise velocity ratio across the bed.

Synergistic effect of coal and biomass gasification and organo-inorganic elemental impact on gasification performance and product gas

The current study demonstrates the synergistic effect of co-gasification of high-ash Indian coal and biomass (press mud and sawdust) blends in varying proportions in a pilot-scale bubbling fluidized bed gasifier (BFBG) with a capacity of 20 kg/h. The effect of blending on product gas yield, composition and heating value, carbon conversion, and cold gas efficiency was critically analyzed. Mineralogical transformations and catalytic effects were investigated during co-gasification, wherein minerals in ash residue, such as hematite, sylvite, chlorite, K-feldspar, CaO, and MgO, showed a catalytic role in co-gasification, increasing the product gas compositions, and reverse the trend for kaolinite and phosphate minerals. Blending coal with biomass enhances the porosity and reactivity of blends, surface morphology, gasification performance, and product gas yield. So, high ash coal and biomass are suitable for gasification. The high ash coal gasification comprises the volumetric product gas composition (%) of CO (9.79), CO2 (8.75), H2(13.6), and CH4(1.12) with the maximum blends (40%) of biomass, the volumetric composition (%) is enhanced comprising CO (17.71), CO2 (14.8), H2(19.9) and CH4(2.05) for press mud blend, and CO(15.84), CO2(14.2), H2(18.3) and CH4(2.29) for sawdust blend, respectively, and HHV increases from 3.42 (MJ/Nm3) to 5.59(MJ/Nm3).

Influence of bed material on biomass gasification in fluidized beds via a TFM-DEM hybrid model

In the biomass gasification process, mixing and segregation behaviors of fuel particles and bed materials greatly influence the performance. In this work, the Two-Fluid Model-Discrete Element Method (TFM-DEM) hybrid model is employed to evaluate the impact of bed material on biomass gasification in a fluidized bed reactor, where fuel particles and bed material particles are described by the Lagrangian method and Eulerian method respectively. The biomass particle size distribution is taken into consideration. The kinetic theory of rough sphere (KTRS) is employed to consider the rotation impact of bed materials. Flow behaviors of binary mixture and gas composition distribution are analyzed. The results reveal that the bed materials with greater size can hinder the particle mixing behaviors and make the biomass particles concentrate on the bed surface so as to increase the non-uniformity of temperature distribution in the bed. A good fluidization with smaller bed material particles is beneficial to hydrogen production.

Thermal gasification of biomass in fluidized bed

Chemicals, heat, and electricity can all be made with biomass, a renewable energy source. Biomass gasification is more environment friendly than biomass combustion because it produces less carbon dioxide (CO2) and other polluting gases (NOx and SO2). Present paper is focused on biomass gasification using fluidized bed. CFD analysis are performed in a cylindrical fluidized bed gasification chamber with a diameter of 6.6 cm and static bed height of 100 cm. The biomass inlet is located at a height of 0.73 cm with diameter of 0.75 cm; unstructured grid is chosen for the analysis. In this study 39,250 cells and 40,086 nodes are used to perform the simulations. CFD simulations are carried out to investigate the devolatization behavior of biomass. Fluent model of volatile material is modified according to the ultimate and proximate analysis of biomass. To know the effect on conversion efficiency of biomass a different equivalence ratio is considered as a process parameter in the range of 0.2 to 0.3. The stoichiometric ratio considered as 0.4 for biomass gasification. Mass fraction of species generated from partial combustion i.e. gasification.

Experimental investigation and optimization of the gasification parameters of macadamia nutshells in a batch-fed bubbling fluidized bed gasifier with air preheating

Gasification of biomass waste has a significant potential to reduce environmental impact and promote sustainability by producing syngas, which is considered as renewable energy. This work investigated the gasification of macadamia nutshells in air-preheated, batch-fed fluidized bed gasifier. The study conducted a parametric analysis to assess the effect of equivalence ratio (ER) and air temperature on the gasifier temperature profile and its performance based on gas composition, higher heating value (HHV), and gas yield. The research was conducted within the range of 0.15–0.35 for the ER and 25–825 °C for the air temperature. Multi-objective numerical optimization was conducted using response surface methodology (RSM). From the parametric study, a distinct temperature profile was observed along the gasifier height, with the peak temperature near the top of the fluidized bed section and the lowest temperature at the top of the gasifier. Air preheating mostly favored gasification temperature at the lower part of the gasifier and showed rare significance at the top. No improvement in gasifier performance was observed beyond an air temperature of 620 °C, which was identified as the ideal air-preheating temperature. Analysis of variance (ANOVA) revealed that the ER was the most influential parameter in the production of combustible gasses, syngas HHV and gas yield. Air preheating did not have a significant effect on methane production and gas yield. The most optimal values for ER and air temperature were obtained as 0.195 °C and 620 °C, respectively, producing optimal values of 9.54, 14.65%, 2.03, 4.02 MJ·Nm−3, and 1.82 Nm3·kg−1 for hydrogen, carbon monoxide, methane, HHV, and gas yield, respectively.

Design and Simulation Study of Production of Syngas from Rice Husk

Energy relationship in global politics has become a vital determinant. Biomass especially the rice husk is a very potential source of energy, which can be utilized in a number of ways. In India, there is an abundance of rice production as a result more of the rice husk is easily available and has a higher potential in order to fulfillments the energy requirements. Rice husk can be used to produce the syngas which is an alternative source of energy generation as compared to natural gas. As compared to natural gas, the syngas produced by the rice husk contains lesser amount of sulfur contents. We have worked out at a plant design for the synthesis of kg/h of syngas via 1000 kg/h of rice husk using fluidized bed gasification and we get 820.4kg/hr of Syngas. We have designed gasifier of length 5.94m and 1.32 m diameter having a volume of 8.115 m3. we have designed one shell pass and two tube pass heat exchanger and cyclone separator. We have done simulation of our project using Aspen Plus