High-temperature gasification kinetics of biomass pyrolysis

The rate of gas formation from wood pyrolysis has been experimentally measured at temperatures from 300°C to 1000°C. The formation rate of specific product gases has been measured rather than the rate of solid weight loss. Even for very fine particles, the rate becomes heat transfer limited a: high temperatures. The product gases also approach thermodynamic equilibrium rapidly at high temperatures. The results are corrected using the experimental residence time distribution.     

On the mechanism of the rapid pyrolysis of cellulose

Experimental yields and liquid product analyses obtained from the fast pyrolysis of biomass and cellulose in a fluidized bed reactor have been used to demonstrate that the decomposition of cellulose to liquid products proceeds to a major degree by a single mechanism. At temperatures over about 450°C and at vapor residence times of one second or less, it is proposed that the monomer unit of cellulose decomposes preferentially to a two-carbon and a four-carbon fragment, with the two-carbon fragment rearranging to give a yield of hydroxyacetaldehyde (glycolaldehyde) which is 75% or more of that theoretically probable. The most likely route for decomposition or rearrangement of the four-carbon moiety is suggested. The formation of carbonyl or hydroxycarbonyl compounds with two to four carbon atoms is favored. Experimental results from the fast pyrolysis of poplar wood indicate that the cellulose decomposition in wood follows the same path as that of pure cellulose in the production of liquid products.     

Simulation of the fast pyrolysis of Tunisian biomass feedstocks for bio-fuel production

An optimized model is developed for the production of bio-fuels from biomass using a SuperPro Designer tool. Four types of Tunisian biomass feedstocks including date palm rachis, olive stones, vine stems and almond shells were selected for the fast pyrolysis process simulation. Simulation tests were performed at different temperatures ranging from 450 to 650 °C, and residence times ranging from 0.1 to 10 s and the products yield were determined. The obtained results indicate that a temperature of 575 °C and 0.25 s vapor residence time are the optimum parameters to maximize the bio-oil yield. Comparison between the different feedstocks indicates that a higher bio-oil fraction was obtained from the date palm rachis and vine stem. However, the difference between the samples is not significant and further investigations on the bio-oil properties are requested to select the suitable biomass for bio-oil production in Tunisia.     

High Xylose Yields from Dilute Acid Pretreatment of Corn Stover Under Process-Relevant Conditions

Pretreatment experiments were carried out to demonstrate high xylose yields at high solids loadings in two different batch pretreatment reactors under process-relevant conditions. Corn stover was pretreated with dilute sulfuric acid using a 4-l Steam Digester and a 4-l stirred ZipperClave® reactor. Solids were loaded at 45% dry matter (wt/wt) after sulfuric acid catalyst impregnation using nominal particle sizes of either 6 or 18 mm. Pretreatment was carried out at temperatures between 180 and 200 °C at residence times of either 90 or 105 s. Results demonstrate an ability to achieve high xylose yields (>80%) over a range of pretreatment conditions, with performance showing little dependence on particle size or pretreatment reactor type. The high xylose yields are attributed to effective catalyst impregnation and rapid rates of heat transfer during pretreatment.     

Product distribution in pyrolysis of cellulose in a microfluidized bed

A study of flash pyrolysis of cellulose was carried out in the temperature range from 313 to 770°C in a microfluidized bed. Chemical analysis was done for gaseous and liquid products using gas chromatography. Levoglucosan was measured after silylation of the tar fraction. In the fluidized bed, residence times were of the order of 1 s, while heating rates were estimated at higher than 100,000°C/s for cellulose particles of 60 μm diameter and about 1000°C/s for cellulose particles having about 0.6 mm mean particle diameter. No pronounced effects of particle size were observed. Logarithms of product yields as wt.% of sample correlate linearly with bed temperature. Transitions in these curves are observed between 500 and 600°C corresponding roughly to decomposition of levoglucosan. Effects of atmosphere were also studied by comparing the effect of various atmospheres (CO, CO₂, H₂ + N₂) with pure N₂. Only a slight effect was noted on the product distribution. It appears that levoglucosan, a major product obtained from the slow pyrolysis of cellulose, is not a primary product under flash pyrolysis conditions.     

生物质组分及温度对闪速热解挥发分的影响

生物质是一种可再生、污染小的自然资源，它可以直接燃烧产生热能，也可以转化为气体、液体燃料或化工原料。生物质热转化技术近年来受到国内外学者的广泛重视。而热转化过程中，热解是第一步，与生物质组分、热解温度、滞留时间等因素有关。热重仪（TGA）是一种研究热解机理常用的方法，它适用于慢速程序升温的热解研究。研究发现，热解条件及生物质种类对反应表观活化能与表观频率因子等动力学参数有很大影响。层流炉闪速加热设备，已经用于煤的热解研究。本文利用自己设计的以热等离子体为热源的层流炉系统，对椰子壳、棉花秆和稻壳粉末进行了闪速热解实验研究及模型理论分析，探讨了生物质化学组分、热解温度和滞留时间对挥发分的影响，为生物质闪速热解提供了一定的基础数据。     

A comparative study on characterizations of biomass derived activated carbons prepared by both normal and inert atmospheric heating conditions

In the present study, cost effective activated carbon from wasteland biomass of Calotropis gigantea stem was prepared at 400 °C, 600 °C, 750 °C and 900 °C carbonization temperatures in normal atmosphere (NA) and at 600 °C, 750 °C in inert atmosphere (IA) of nitrogen by using Potassium Carbonate (K₂CO₃) as chemical activating agent in the impregnation ratios of 0.5, 1 and 2. Activated carbons prepared under NA and IA were characterized and compared. Field Emission Scanning Electron Microscopy (FESEM) study confirmed presence of micropores and mesopores. While Xray Diffraction (XRD) analysis confirmed presence of both disordered amorphous carbon humps and graphitic crystallite peaks. Presences of functional groups were more prominent in NAC; found from Fourier Transform Infra-Red Spectroscopy (FTIR) analysis. BET surface area at 750 °C at chemical impregnation ratio 1 under NA was recorded highest containing both micropores and mesopores. Disordered carbon structure was confirmed from RAMAN spectroscopic analysis and nanoporous structure of activated carbon was confirmed from HRTEM analysis. NA activated carbons processed from wasteland weed can be preferred for different adsorption related applications as they are reasonable with improved properties.     

Micro-pyrolysis of technical lignins in a new modular rig and product analysis by GC–MS/FID and GC × GC–TOFMS/FID

A new offline-pyrolysis rig has been designed to allow multifunctional experiments for preparative and analytical purposes. The system conditions can be set and monitored, e.g. temperature, its gradients and heat flux. Some special features include (1) high heating rates up to 120 °C/s with pyrolysis temperatures up to 850 °C at variable pyrolysis times and (2) the selection of different atmospheres during pyrolysis. A complete mass balance of products and reactants (gas, liquids and solids) by gravimetric methods and sequential chromatographic analyses was obtained.The pyrolytic behaviour and the decomposition products of lignin-related compounds were studied under different conditions: heating rates (from 2.6 °C/s up to 120 °C/s), pyrolysis temperatures at 500 °C and 800 °C in different atmospheres (N₂, H₂, and mixtures of N₂ and acetylene). Kraft lignin, soda lignin, organosolv lignin, pyrolytic lignin from pine bio-oil, residues from biomass hydrolysis and fermentation were studied.The obtained pyrolysis products were classified into three general groups: coke, liquid phase and gas phase (volatile organic compounds (VOC) and permanent gases). The liquid fraction was analysed by GC–MS/FID. In addition, comprehensive two-dimensional GC was applied to further characterise the liquid fraction. VOCs were semi-quantified by a modified headspace technique using GC–MS/FID analysis. The micro-pyrolysis rig proved to be an efficient and useful device for complex pyrolysis applications.     

Ethanol production from olive oil extraction residue pretreated with hot water

The olive pulp fraction contained in the residue generated in olive oil extraction by a two-step centrifugation process can be upgraded by using the cellulose fraction to produce ethanol and recovering high value phenols (tyrosol and hydroxytyrosol). Olive pulp was pretreated in a laboratory scale stirred autoclave at different temperatures (150–250°C). Pretreatment was evaluated regarding cellulose recovery, enzymatic hydrolysis effectiveness ethanol production by a simultaneous saccharification and fermentation process (SSF), and phenols recovery in the filtrate. The pretreatment of olive pulp using water at temperatures between 200°C and 250°C enhanced enzymatic hydrolysis. Maximum ethanol production (11.9 g/L) was obtained after pretreating pulp at 210°C in a SSF fed-batch procedure. Maximum hydroxytyrosol recovery was obtained in the liquid fraction when pretreated at 230°C.     

Particle size limitations due to heat transfer in determining pyrolysis kinetics of biomass

A simplified heat transfer model is analyzed in order to determine an upper bound for biomass particle size in conducting experimental pyrolysis kinetics. In determining intrinsic kinetic rates, it is desirable that the entire particle be at reactor temperature for the duration of the chemical reaction. By comparing characteristic times for reaction rates versus heat-up rates, an approximate boundary for particle size can be constructed as a function of temperature; above this boundary, the reaction rate is strongly heat transfer dominated, and below the boundary the reaction rate is kinetically controlled. Using parameters for cellulose pyrolysis, it is estimated that a 200 μm particle will be heat transfer limited due to internal heat transfer at temperatures above 500°C. This boundary applies for conditions where the surface of the particle is brought to reactor temperature instantaneously. Using our specific experimental conditions, it is found that the limitations imposed by external transfer are reached before those predicted by assuming that only internal heat transfer is limiting. In examining wood pyrolysis, where a global reaction rate approximation is insufficient, it is experimentally shown that the decomposition for hemicellulose can be transport limited, while cellulose remains in the kinetic controlled regime.     

Kinetic study of wood chips decomposition by TGA

Pyrolysis of a wood chips mixture and main wood compounds such as hemicellulose, cellulose and lignin was investigated by thermogravimetry. The investigation was carried out in inert nitrogen atmosphere with temperatures ranging from 20°C to 900°C for four heating rates: 2 K min⁻¹, 5 K min⁻¹, 10 K min⁻¹, and 15 K min⁻¹. Hemicellulose, cellulose, and lignin were used as the main compounds of biomass. TGA and DTG temperature dependencies were evaluated. Decomposition processes proceed in three main stages: water evaporation, and active and passive pyrolysis. The decomposition of hemicellulose and cellulose takes place in the temperature range of 200–380°C and 250–380°C, while lignin decomposition seems to be ranging from 180°C up to 900°C. The isoconversional method was used to determine kinetic parameters such as activation energy and pre-exponential factor mainly in the stage of active pyrolysis and partially in the passive stage. It was found that, at the end of the decomposition process, the value of activation energy decreases. Reaction order does not have a significant influence on the process because of the high value of the pre-exponential factor. Obtained kinetic parameters were used to calculate simulated decompositions at different heating rates. Experimental data compared with the simulation ones were in good accordance at all heating rates. From the pyrolysis of hemicellulose, cellulose, and lignin it is clear that the decomposition process of wood is dependent on the composition and concentration of the main compounds.     

Effects of doping with CeO2 and calcination temperature on physicochemical properties of the NiO/Al2O3 system

The effects of doping with CeO₂ and calcination temperature on the physicochemical properties of the NiO/Al₂O₃ system have been investigated using DTA, XRD, nitrogen adsorption measurements at −196°C and decomposition of H₂O₂ at 30–50°C. The pure and variously doped solids were subjected to heat treatment at 300, 400, 700, 900 and 1000°C. The results revealed that the specific surface areas increased with increasing calcination temperature from 300 to 400°C and with doping of the system with CeO₂. The pure and variously doped solids calcined at 300 and 400°C consisted of poorly crystalline NiO dispersed on γ-Al₂O₃. Heating at 700°C resulted in formation of well crystalline NiO and γ-Al₂O₃ phases beside CeO₂ for the doped solids. Crystalline NiAl₂O₄ phase was formed starting from 900°C. The degree of crystallinity of NiAl₂O₄ increased with increasing the calcination temperature from 900 to 1000°C. An opposite effect was observed upon doping with CeO₂. The NiO/Al₂O₃ system calcined at 300 and 400°C has catalytic activity higher than individual NiO obtained at the same calcination temperatures. The catalytic activity of NiO/Al₂O₃ system increased, progressively, with increasing the amount of CeO₂ dopant and decreased with increasing the calcination temperature.     

Biomass valorisation by staged degasification: A new pyrolysis-based thermochemical conversion option to produce value-added chemicals from lignocellulosic biomass

Pyrolysis of lignocellulosic biomass leads to an array of useful solid, liquid and gaseous products. Staged degasification is a pyrolysis-based conversion route to generate value-added chemicals from biomass. Because of different thermal stabilities of the main biomass constituents hemicellulose, cellulose and lignin, different temperatures may be applied for a step-wise degradation into valuable chemicals. Staged degasification experiments were conducted with deciduous (beech, poplar), coniferous (spruce) and herbaceous (straw) biomass. Thermogravimetry was used to estimate appropriate temperatures for a two-stage degradation process that was subsequently evaluated on bench-scale by moving bed and bubbling fluidised bed pyrolysis experiments. Degasification in two consecutive stages at 250–300 °C and 350–400 °C leads to mixtures of degradation products that originate from the whole biomass. The mixtures that were generated at 250–300 °C, predominantly contain hemicellulose degradation products, while the composition of the mixtures that were obtained at 350–400 °C, is more representative for cellulose. Lignin-derived fragments are found in both mixtures. Yields up to 5 wt% of the dry feedstock are obtained for chemicals like acetic acid, furfural, acetol and levoglucosan. Certain groups of thermal degradation products like C₂–C₄ oxygenates and phenols are formed in yields up to 3 wt%. Highest yields have been obtained for beech wood. Staged degasification is a promising pyrolysis-based route to valorise lignocellulosic biomass. Clear opportunities exist to increase product yields and selectivities by optimisation of reactor conditions, application of catalysts and specific biomass pretreatments like demineralisation and pre-hydrolysis.     

Wide-angle X-ray diffraction study of the effect of periodate oxidation and thermal treatment on the structure of cellulose powder

Cellulose and periodate oxidised cellulose powders were investigated for any structural changes occurring when subjected to thermal treatment, since their use as fillers in composites involves prolonged exposure to high temperatures. The wide-angle X-ray diffraction peak at 2θ = 22·9° for the oxidised cellulose samples was found to decrease almost proportionately to the degree of oxidation of the starting cellulose. Whereas heat treatment of cellulose powder at 120°, 180° and 240°C for three hours also produces a continual decrease in the crystallinity of the cellulose, heat treatment of periodate oxidised cellulose at 120°, 180° and 240°C for three hours produces drastic changes in the crystallinity of the resultant products. For 16% oxidised cellulose heated at 240°C for three hours, almost total crystallinity is lost. This is also seen from the increase in line broadening of the X-ray diffractogram. An interesting feature in the above cases was the appearance of an additional peak at 2θ ≈ 12°. In DTG studies the temperature at which the major loss in weight (～ 62%) occurred was ～ 290°C for most samples. The final weight loss (～ 85%) generally occurred at 430–450°C. The 16% oxidised cellulose behaved somewhat differently, and reasons for this are explained.     

Kinetics of Lime Pretreatment of Sugarcane Bagasse to Enhance Enzymatic Hydrolysis

The objective of this work was to determine the optimum conditions of sugarcane bagasse pretreatment with lime to increase the enzymatic hydrolysis of the polysaccharide component and to study the delignification kinetics. The first stage was an evaluation of the influence of temperature, reaction time, and lime concentration in the pretreatment performance measured as glucose release after hydrolysis using a 2³ central composite design and response surface methodology. The maximum glucose yield was 228.45 mg/g raw biomass, corresponding to 409.9 mg/g raw biomass of total reducing sugars, with the pretreatment performed at 90°C, for 90 h, and with a lime loading of 0.4 g/g dry biomass. The enzymes loading was 5.0 FPU/dry pretreated biomass of cellulase and 1.0 CBU/dry pretreated biomass of β-glucosidase. Kinetic data of the pretreatment were evaluated at different temperatures (60°C, 70°C, 80°C, and 90°C), and a kinetic model for bagasse delignification with lime as a function of temperature was determined. Bagasse composition (cellulose, hemicellulose, and lignin) was measured, and the study has shown that 50% of the original material was solubilized, lignin and hemicellulose were selectively removed, but cellulose was not affected by lime pretreatment in mild temperatures (60–90°C). The delignification was highly dependent on temperature and duration of pretreatment.     

Lanthanum zirconate nanoparticles and ceramics produced using a nitrate-modified alkoxide synthesis route

Fine lanthanum zirconate powder was prepared by thermally decomposing a nitrate-alkoxide-based precursor derived from dehydrated lanthanum nitrate, zirconium n-butoxide and 2-methoxyethanol. Upon heating, the decomposition of the organic groups was promoted by the nitrate groups, yielding a porous powder that crystallized into a pyrochlore phase at 800 °C. The powder that was heat treated at 900 °C for 1 h was composed of friable agglomerates of approximately 60-nm-sized nanoparticles. The ceramics obtained from the powder heat treated at 900 °C and milled for 30 min reached a relative density of 97.9 % after sintering at 1,400 °C for 10 h, which is at least 100 °C lower than the typically reported temperatures for this material.     

Investigation of rapid thermally annealed GaP(001) surfaces in vacuum

Morphology of rapid thermally annealed GaP(001) surfaces has been investigated using spectroscopic ellipsometry (SE), optical microscopy, ex situ atomic force microscopy, electron probe microanalysis (EPMA) and X‐ray photoelectron spectroscopy (XPS). The samples were annealed in vacuum for t = 2 s at temperatures T = 20–900 °C. The SE, optical microscopy and XPS spectra suggest that thermal annealing causes little influence on the GaP surface at T ≤ 600 °C; however, micro‐ and macroscopic roughening occur at T > 600 °C and T ≥ 750 °C, respectively, with a generation of Ga droplets at T ≥ 750 °C. The presence of the Ga droplets is confirmed by the EPMA measurements. The droplet density can be expressed as N_Ga ∝ exp (E_a/k_BT) with an activation energy of E_a ～ 2.3 eV. The XPS data indicate the change in the surface oxide composition from the native oxide to the Ga oxide (Ga₂O₃ and Ga₂O) after annealing at T ≥ 750 °C. Possible annealing‐induced degradation steps are proposed to provide as complete a picture as possible. Copyright © 2010 John Wiley & Sons, Ltd.     

Pyrolytic Chemistry of Benzyl Benzoate

Flash vacuum pyrolysis of benzyl benzoate ( 3 ) at temperatures in the range 750–900 °C and at 10² torr gave diphcnylmethane ( 5 ) as the major product with toluene ( 6 ) and eight other trace products, namely bipbenyl ( 7 ), dibenzyl ( 8 ), 2-, 3-, 4-phenyltoluenes ( 9,10,11 , respectively), fluorcne ( 12 ), benzyl alcohol ( 4 ) and benzaldehyde ( 13 ). The mechanism of formation of these products is proposed to involve benzyl and phenyl radicals.     

Production of bio-oil via fast pyrolysis of agricultural residues from cassava plantations in a fluidised-bed reactor with a hot vapour filtration unit

This article reports experimental results on fast pyrolysis of agricultural residues from cassava plantations, namely cassava rhizome (CR) and cassava stalk (CS), in a fluidised-bed fast pyrolysis reactor unit incorporated with a hot vapour filter. The objective of this research was to investigate the effects of reaction temperatures, biomass particle size and the use of simple hot vapour filtration on pyrolysis product yields and properties. Results showed that the optimum pyrolysis temperatures for CR and CS were 475 °C and 469 °C, which gave maximum bio-oil yields of 69.1 wt% and 61.4 wt% on dry biomass basis, respectively. The optimum particle size for bio-oil production in this study was 250–425 μm. The use of the hot filter led to a reduction of 6–7 wt% of bio-oil yield. Nevertheless, the filtered bio-oils appeared to have a better quality in terms of initial viscosity, solids content, ash content and stability.     

Vanadium Nitride Films Formed by Rapid Thermal Processing (RTP): Depth Profiles and Interface Reactions Studied by Complementary Analytical Techniques

The nitridation of vanadium films in molecular nitrogen and ammonia using a RTP‐system was investigated. The V films were deposited on silicon substrates covered by 100 nm thermal SiO₂. For a few experiments sapphire substrates were used. Nitride formation at high temperatures (900 and 1100 °C) and interface reactions and diffusion of oxygen out of the SiO₂‐layer into the metal lattice at moderate temperatures (600 and 700 °C) were studied. For characterisation complementary analytical methods were used: X‐ray diffraction (XRD) for phase analysis, secondary neutral mass spectrometry (SNMS) and Rutherford Backscattering (RBS) for acquisition of depth profiles of V, N, O, C and Si, transmission electron microscopy (TEM) in combination with electron energy filtering for imaging element distributions (EFTEM) and recording electron energy loss spectra (EELS) to obtain detailed information about the initial stages of nitride, oxide and oxynitride formation, respectively, and the microstructure and element distributions of the films. In these experiments the SiO₂‐layer acts as diffusion barrier for nitrogen and source for oxygen causing the formation of substoichiometric vanadium oxides and oxynitrides near the V/SiO₂‐interface primarily at temperatures ≤ 900 °C. At a temperature of 1100 °C just a small amount of oxynitride forms near the interface because rapid diffusion of nitrogen and fast formation of VN (diffusion barrier for oxygen) inhibit the outdiffusion of oxygen into the metal layer. In the 600 °C regime, in argon atmosphere oxynitride phases observed in the surface region of these films originate from reaction of residual oxygen in the argon gas, whereas NH₃ as process gas does not lead to oxide or oxynitride formation at the surface (apart from the oxidation caused by storage). NH₃ seems to support the diffusion of oxygen out of the SiO₂‐layer. During the decomposition of ammonia at higher temperatures hydrogen is formed, which could attack the SiO₂. In contrast, sapphire substrates do not act as oxygen source in the 600 °C regime and change the nitridation behaviour of the vanadium films.