states that nitrocellulose for use in the manufacture of artificial leather should have a nitrogen content between II. 5 per cent. and 13 per cent., with an average of I2 per cent. Its ash content should not exceed 0.4 per cent. The nitrocellulose is applied to the cloth base as a solution. The chie
Kinetics of the thermal decomposition of oil shale from Puertollano (Spain)
✍ Scribed by M.C Torrente; M.A Galán
- Publisher
- Elsevier Science
- Year
- 2001
- Tongue
- English
- Weight
- 190 KB
- Volume
- 80
- Category
- Article
- ISSN
- 0016-2361
No coin nor oath required. For personal study only.
✦ Synopsis
The kinetics of the thermal decomposition of Spanish oil shale was studied using isothermal and non-isothermal thermogravimetric analyses (TGA). The isothermal TG data were studied at different particle sizes (0.250 £ 10 23 , 0.505 £ 10 23 and 0.925 £ 10 23 m) and three temperature plateaux (703, 688 and 673 K). For the kinetic analysis, the Integral Method was used.
The non-isothermal weight-loss data was analysed at different heating rates (5, 10, 15, 20 and 50 K/min) up to 1173 K and for a particle size of 0.250 £ 10 23 m. Three methods were applied for the determination of the kinetic parameters: the Direct Arrhenius Plot Method, the Integral Method and the Differential Method.
From an engineering point of view, the rate of the thermal decomposition of Spanish oil shale can be suitably described by overall ®rstorder kinetics. We also found that transport effect problems affected the observed rate when the heating rates were higher than 10 K/min; additionally, no mass and heat transfer resistance was observed for the different particle sizes studied.
The results obtained from the isothermal method give an apparent activation energy of 150 kJ/mol and a frequency factor of 2.11 £ 10 8 s 21 , while for the non-isothermal method these results were: E 167 kJ=mol and A 2:16 £ 10 9 s 21 : The pyrolysis rates of Spanish shale are compared with those of Anvil Points, Clear Creek and Moroccan shale.
📜 SIMILAR VOLUMES
The thermal decomposition behavior of polypropylene, oil shale and a 1:3 mixture of the two was investigated in a thermogravimetric analyzer (TGA) reaction system in an argon atmosphere, with a view to comparing the process of the mixture with those of the individual components. Experiments were con
methods
Befs Technologies designed the benzene plant in Rautaruukki Raahe Steel, which commenced operation in 1992. The analyses of coke oven gas and crude benzene have reached the targets and the operation and maintenance costs have been low.
Isothermal and nonisothermal methods have been used to investigate the kinetics of oil generation during decomposition of 91.7 ml/kg (22 US. gal/short ton) Colorado oil shale. The result from the nonisothermal method gives an apparent activation energy of 219.4 kJ/mol and a frequency factor of 2.81