Understanding of Interactions Between Pyrolysis Gases and Liquid Aluminum and Their Impact on Dross Formation

Author(s):  
R. Dittrich ◽  
B. Friedrich ◽  
G. Rombach ◽  
J. Steglich ◽  
A. Pichat
1980 ◽  
Vol 41 (C8) ◽  
pp. C8-226-C8-229 ◽  
Author(s):  
O. J. Eder ◽  
B. Kunsch ◽  
J. B. Suck ◽  
M. Suda
Keyword(s):  

Author(s):  
N. I. Chernova ◽  
S. V. Kiseleva ◽  
O. M. Larina ◽  
G. A. Sytchev

Algae biomass is considered as an alternative raw material for the production of biofuels. The search for new types of raw materials, including high-energy types of microalgae, remains relevant, since the share of motor fuels in the structure of the global fuel and energy balance remains consistently high (about 35%), and the price of oil is characterized by high volatility. The authors have considered the advantages of microalgae as sources of raw materials for fuel production. Biochemical and thermochemical conversion are proposed as technologies for their processing. This paper presents the results of the study of the pyrolysis of the biomass of clonal culture of blue-green microalgae / cyanobacteriumArthrospira platensis rsemsu 1/02-Pfrom the collection of the Research Laboratory of Renewable Energy Sources of the Lomonosov Moscow State University. An experiment to study the process of pyrolysis of microalgae biomass was carried out at the experimental facility of the Institute of High Temperatures RAS in pure nitrogen grade 6.0 to create an oxygen-free environment with a linear heating rate of 10 ºС / min from room temperature to 1000 ºС. The whole process of pyrolysis proceeded in the field of endothermy. The specific amounts of solid residue, pyrolysis liquid and gaseous products were experimentally determined. As a result of the pyrolysis of microalgae biomass weighing 15 g, the following products were obtained: 1) coal has the mass of the solid residue is 2.68 g, or 17.7% of the initial mass of the microalgae (while 9.3% of the initial mass of the microalgae remained in the reactor); 2) pyrolysis liquid – weight 3.3 g, or 21.9% of the initial weight; 3) non-condensable pyrolysis gases – weight 1.15 l. The specific volumetric gas yield (the amount of gas released from 1 kg of the starting material) was 0.076 Nm3/ kg. The analysis of the composition and specific volume yield of non-condensable pyrolysis gases formed in the process of pyrolysis, depending on temperature. It is shown that with increasing temperature, the proportion of highcalorie components of the gas mixture (hydrogen, methane and carbon monoxide) increases. The calorific value of the mixture of these gases has been estimated.


1974 ◽  
Vol 60 (1) ◽  
pp. 96-103 ◽  
Author(s):  
Hiroshi YAMAGUCHI ◽  
Yoshihiro HISAMATSU
Keyword(s):  

2011 ◽  
Vol 42 (3) ◽  
pp. 441-450 ◽  
Author(s):  
Yurii Kolesnikov ◽  
Christian Karcher ◽  
André Thess

2021 ◽  
pp. 103424
Author(s):  
Sahand Rasoulipour ◽  
Charles Fleischmann ◽  
Luke Merciec ◽  
Nicole Adams

1989 ◽  
Vol 20 (3) ◽  
pp. 533-541 ◽  
Author(s):  
S. Y. Oh ◽  
J. A. Cornie ◽  
K. C. Russell

2006 ◽  
Vol 42 (4) ◽  
pp. 560-562
Author(s):  
V. A. Borysenko ◽  
O. H. Arkhypov ◽  
H. V. Lipko
Keyword(s):  

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