The effect of psychrometry on the performance of a solar collector.

The investigation of a solar collector is based on the thermal behaviour of a carrier fluid and the degradation of energy across a flat plate collector. The exergy analysis of a thermal system includes the change in the exergy function of a carrier fluid while transferring solar radiation across an air gap. The cell cast acrylic glass was used to transmit the incident solar radiation to the absorber plate, and to safeguard the absorber plate from the outside environment. With the help of the steady flow energy equation, the enthalpy of the carrier fluid (moist air) was calculated. The specific humidity of the incoming air was calculated at an average dry bulb temperature of 299.4 K. The stagnation temperature at a limiting condition was also estimated to find out the maximum permissible limit for a given thermal design. The mass flow rate of air was assumed to be 5.2 g-s-1. The efficiency of the solar collector was found to vary from 40 to 42%, whereas the thermal energy available for drying was 15-59% of the exergy of the carrier fluid. The net entropy generation rate due to the collector plate was calculated to be 0.12 W-K-1.

Physico-chemical assessment of torrefied Eurasian pinecones.

BACKGROUND: Biomass pre-treatment is gaining attention as a standalone process to improve the qualitative aspect of the lignocellulosic material. It has been gaining ground in the power station by replacing the coal with the pre-treated biomass. In this context, this paper enlightens the operating condition of carrying out the torrefaction so that the process can be made relatively more effective. The influence of physico-chemical characteristics on the heat of reaction of pyrolysis reactions, mass loss and temperature regimes are evaluated by thermogravimetry of the pre-treated samples of the pinecone; whereas, the structural transformation in the basic constituents is determined via knowing the fractional change in cellulose, hemicellulose and acid-insoluble lignin contents of the pine cone. The thermogravimetric (TGA) and differential thermal analysis (DTA) were performed to determine the physical as well as the thermal behaviour of the thermally processed biomass. The samples had undergone thermal decomposition at heating rates of 5 °C min-1, 10 °C min-1 and 15 °C min-1. Nitrogen gas was used as a purge gas for the pyrolysis of the pre-treated samples. The volumetric rate of 200 ml min-1 was pre-set for the thermal decomposition of the samples at 600 °C; whereas, the selected torrefaction temperature range varied from 210 to 250 °C. RESULTS: The heat of reaction for the pre-treated samples was found to vary from 1.04 to 1.52 MJ kg-1; whereas, it was 0.91-1.54 MJ kg-1 for the raw samples. The total annual production cost of processing 3.6 Mg of fuel in a year at a pilot scale was $ 36.72; whereas, the fiscal burden per kilogram of fuel during thermal degradation of the processed fuel was reduced by 0.08-1.5ȼ. The entropy of the system decreased with an increasing ramp rate. The exergetic gain in the system increased by 1-2%. The loss of energy during the energy-intensive processing of the pre-treated fuel was relatively low at a heating rate of 5 °C min-1. CONCLUSION: By the physico-chemical assessment, it was determined that pinecones required the highest torrefaction temperature and time to provide the upgraded pinecones. It was concluded that the duration of the torrefaction should be at least 15 min for a temperature of 250 °C so that the chemical exergy of the system, energy yield and the energy density of the processed material are qualitatively improved. The volatile and ash contents were noticed to decrease during the torrefaction process. The least fractional change in the volatile content was estimated at 210 °C for a torrefaction time of 15 min; whereas, the ash content was minimum at 210 °C for a torrefaction time of 5 min.

Thermo-kinetics of Forest Waste Using Model-Free Methods / Termocinética de residuos de bosque usando los métodos de modelo libre / Termocinética de resíduos de bosque usando métodos de modelo livre

Abstract Thermal behaviour of pine needles (Pinus Roxburghii) is examined through a thermogravimetry technique. The dried samples of pine needles undergo the non-isothermal decomposition at temperature range of 308-1173 K. The heating rates used for experimental purposes are: 5 ◦ C min-1, 10 ◦ C min-1 and 15 ◦ C min-1. Kinetic parameters of thermal decomposition reactions of pine needles are obtained through the model-free schemes. The estimated values of activation energy and frequency factor derived from Kissinger method are 132.77 kJ mol-1 and 13.15 x 107 min-1, respectively. Furthermore, the averaged values of the same kinetics parameters retrieved from the isoconversional methods are 82.38 kJ mol-1 and 74.833 kJ mol-1, 25.42 x 1013 min-1 and 13.449 x 1010 min-1, respectively. Instead of the Flynn-Wall- Ozawa (FWO) and Kissinger- Akahira- Sunrose (KAS) schemes, the kinetic parameters derived from the Kissinger method are relatively promising for the thermal decomposition process, since the kinetic parameters are highly affected by intermediate stages and overlapping of the concurrent reaction occurred during pyrolysis.

Resumen Se examina el comportamiento térmico de las agujas de pino (Pinus roxburghii) a través de la técnica de termogravimetría. Las muestras secas de las agujas de pino se someten a una descomposición no isotérmica en un rango de temperatura de 308-1173 K. Las tasas de calentamiento usadas para los propósitos experimentales son: 5 °C min-1, 10 °C min-1 y 15 °C min-1. Los parámetros cinéticos de las reacciones de descomposición térmica de las agujas de pino se obtuvieron a través de esquemas de modelo libre. Los valores estimados de la energía de activación y el factor de frecuencia derivado del método Kissinger son: 132.77 kJ mol-1 y 13.15 x 107 min-1, respectivamente. Por otra parte, los valores promediados de los mismos parámetros cinéticos recuperados por los métodos isoconversionales son 82.38 kJ mol-1 y 74.833 kJ mol-1, 25.42 x 1013 min-1 y 13.449 x 1010 min-1, respectivamente. A diferencia de los esquemas Flynn-Wall-Ozawa (FWO) y Kissinger-Akahira-Sunrose (KAS), los parámetros cinéticos derivados del método Kissinger son relativamente promisorios para los procesos de descomposición térmica, ya que estos parámetros se afectan grandemente por los estados intermedios y la superposición de la reacción concurrente que ocurre durante la pirólisis.

Resumo O comportamento térmico de agulhas de pinheiro (Pinus roxburghii) foi examinado por meio da técnica de gravimetria. As amostras secas das agulhas de pinheiro se submeteram a uma decomposição não-isotérmica em uma faixa de temperatura de 308-1173 K. As taxas de aquecimento usadas para propósitos experimentais foram: 5 °C min-1, 10 °C min-1 e 15 °C min-1. Os parâmetros cinéticos das reações de decomposição térmica das agulhas de pinheiro se obtiveram por meio de esquemas de modelo livre. Os valores estimados da energia de ativação e o fator de frequência derivado do método Kissinger são: 132.77 kJ mol-1 e 13.15 x 107 min-1, respectivamente. Adicionalmente, os valores médios dos mesmos parâmetros cinéticos recuperados pelos métodos isoconversionais são 82.38 kJ mol-1 e 74.833 kJ mol-1, 25.42 x 1013 min-1 y 13.449 x 1010 min-1, respectivamente. Diferentemente dos esquemas Flynn-Wall-Ozawa (FWO) e Kissinger-Akahira-Sunrose (KAS), os parâmetros cine'ticos derivados do método Kissinger são relativamente promissórios para os processos de decomposição térmica, já que estes parâmetros são altamente afetados pelos estados intermediários e sobreposição da reação concorrente que ocorre durante a pirólise.

Asymptotic Approximations to the Isothermal Pyrolysis of Deodara Leaves using Gamma Distribution / Aproximaciones asintóticas a la pirólisis isotérmica de hojas de deodara usando la distribución gamma / Aproximações assintóticas à pirólise isotérmica de folhas de deodara com a distribuição gamma

Abstract The main aim of this paper pivoted around the influence of some parameters relevant to biomass pyrolysis on the numerical solutions of the nth order distributed activation energy model (DAEM) using the Gamma distribution. The upper limit of 'dE' integral, frequency factor, reaction order, and the shape and rate parameters of the Gamma distribution are investigated. Analysis of the mathematical model is done with the help of asymptotic expansion.

Resumen El propósito principal de este artículo gira en torno de la influencia que tienen ciertos parámetros relacionados con la pirólisis de biomasa sobre las soluciones numéricas del modelo de energía de activación distribuida (MEAD) de orden n, usando la distribución Gamma. Se estudian el límite superior de la integral 'dE', el factor de frecuencia, el orden de reacción, y los parámetros de forma y velocidad de la distribución Gamma. El análisis del modelo matemático es realizado con ayuda de una expansión asintótica.

Resumo O objetivo principal deste artigo gira em torno da influencia de certos parâmetros relacionados à pirólise de biomassa nas soluções numéricas do modelo de energia de ativação distribuída (MEAD) de orden n, usando a distribuição Gamma. São estudados o limite superior da integral 'dE', o fator de frequência, a ordem da reação, e os parâmetros de forma e velocidade da distribuição Gamma. A análise do modelo matemático é realizada com a ajuda de uma expansão assintótica.