scholarly journals Thermal Decomposition of n-Heptane in Fluidized Bed Reactor

1964 ◽  
Vol 28 (4) ◽  
pp. 305-308,a1
Author(s):  
Hiroshi Harada ◽  
Koichiro Kusunoki ◽  
Wataru Sakai
2015 ◽  
Vol 106 ◽  
pp. 721-727 ◽  
Author(s):  
Chao Gai ◽  
Yuping Dong ◽  
Pengfei Fan ◽  
Zhaoling Zhang ◽  
Jingcui Liang ◽  
...  

RSC Advances ◽  
2016 ◽  
Vol 6 (86) ◽  
pp. 83154-83162 ◽  
Author(s):  
Chao Gai ◽  
Yuping Dong ◽  
Shuai Yang ◽  
Zhaoling Zhang ◽  
Jingcui Liang ◽  
...  

Thermal decomposition of the two light polycyclic aromatic hydrocarbons (PAHs) naphthalene and anthracene as tar model compounds was investigated with a lab-scale fluidized bed reactor.


2019 ◽  
Vol 26 (1) ◽  
pp. 69-80
Author(s):  
Małgorzata Olek ◽  
Witold Żukowski ◽  
Jerzy Baron

Abstract Combustion of fuels, including renewable fuels and thermal treatment of waste (CFCs, pesticides), is associated with emissions of pollutants including halogens. The reversible process of sorption/desorption of HCl, in a fluidized (bubbling) bed reactor (BFB), during co-combustion of Cl-materials, was carried out. The thermal decomposition of methylene chloride (DCM, CH2Cl2) in an inert sand bed with the addition of the hydroxyapatite sorbent (HAp, Ca5(PO4)3(OH)) was investigated. The process parameters were as follows: temperature - 930 °C, the air excess - 1.3, stream rate of CH2Cl2 - 50 cm3/h. The concentration of HCl, CCl4, CHCl3, CH2Cl2, CH3Cl, COCl2 in the exhaust gases were monitored online with FTIR spectroscopy. The main chlorine product was hydrogen chloride. Samples of unprocessed HAp, taken from the bed during the process, and solid apatite residues were analyzed by X-ray diffraction (XRD). The content of chlorapatite (Ca5(PO4)3Cl) in the analyzed samples was respectively 11, 53 and 19 %. X-ray fluorescence (XRF) analysis showed the molar ratio of Ca:P:Cl was: 1.00:0.36:0.01, 1.00:0.36:0.09, 1.00:0.37:0.04 respectively. The HAp could be used as an sorbent of the HCl(g) during combustion of materials containing chlorine.


1996 ◽  
Vol 238 (1-2) ◽  
pp. 18-22 ◽  
Author(s):  
S.P. Chakraborty ◽  
P.K. Tripathy ◽  
I.G. Sharma ◽  
D.K. Bose

2019 ◽  
Vol 23 (Suppl. 4) ◽  
pp. 1231-1240
Author(s):  
Gabriela Berkowicz ◽  
Jan Wrona ◽  
Jerzy Baron ◽  
Dariusz Bradlo ◽  
Witold Zukowski

The process of oxidation of gaseous CH3OH by N2O was carried out over an Ag-Fe2O3-cenosphere catalyst whose structure can be defined as double shell-core catalyst. Preparation of the catalyst was carried out in two stages: thermal decomposition of Fe(CO)5 at above 160?C and then electroless Ag plating. The process of methanol degradation by N2O was carried out in a fluidized bed reactor. The study confirms that it is possible to achieve complete degradation of N2O and CH3OH for the obtained catalyst at above 450?C when the contact time of the reactants with the catalyst is approximately 6 second and when the substrates are used in stoichiometric ratios. More than 60% of the hydrogen contained in CH3OH can be converted to molecular hydrogen at 500?C with a ratio of N2O/CH3OH not greater than 0.6 and with a contact time of reactants with the catalyst of approx. 6 seconds.


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