GAS-PRODUCTION BY ALMOND SHELL PYROLYSIS AT HIGH-TEMPERATURE

被引:19
作者
FONT, R
MARCILLA, A
DEVESA, J
VERDU, E
机构
[1] División de Ingeniería Química, Universidad de Alicante, Alicante
关键词
ALMOND SHELLS; FLUIDIZED BED; PYROLYSIS; PYROPROBE;
D O I
10.1016/0165-2370(93)00760-K
中图分类号
O65 [分析化学];
学科分类号
070302 ; 081704 ;
摘要
The production of gases from almond shell pyrolysis at high nominal temperatures (700-900-degrees-C) is discussed, taking into consideration the gaseous products formed by the primary and secondary reactions respectively. Two types of experimental apparatus have been used: (a) an analytical Pyroprobe 100, where the primary reactions take, place and in which the cracking of the primary tars evolved can be considered negligible; (b) a fluidized sand bed reactor, where the biomass is decomposed inside the sand bed and the tars formed are cracked in the upper part of the reactor over the sand bed. Both reactors have proved to be suitable for studying the primary and secondary pyrolysis reactions, respectively. The evolution of the primary hydrocarbons and primary carbon monoxide is suggested to take place by very temperature-sensitive mechanisms, whereby the other oxygenated compounds, carbon dioxide, water, acetic acid and methanol + formaldehyde, are formed by mechanisms involving depolymerizations. On considering the formation of the secondary products, correlations between the yields of carbon oxides and hydrogen as well as between methane and ethylene were observed.
引用
收藏
页码:13 / 27
页数:15
相关论文
共 14 条
[1]   EFFECTS OF REACTOR SEVERITY ON THE GAS-PHASE PYROLYSIS OF CELULOSE-DERIVED AND KRAFT LIGNIN-DERIVED VOLATILE MATTER [J].
ANTAL, MJ .
INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT, 1983, 22 (02) :366-375
[2]   PRODUCT YIELDS AND KINETICS FROM THE VAPOR-PHASE CRACKING OF WOOD PYROLYSIS TARS [J].
BOROSON, ML ;
HOWARD, JB ;
LONGWELL, JP ;
PETERS, WA .
AICHE JOURNAL, 1989, 35 (01) :120-128
[3]  
BROWNING BL, 1965, METHODS WOOD CHEM
[4]  
DIEBOLD JP, 1980, GASOLINE SOLID WASTE, P209
[5]   KINETIC-STUDY OF THE FLASH PYROLYSIS OF ALMOND SHELLS IN A FLUIDIZED-BED REACTOR AT HIGH-TEMPERATURES [J].
FONT, R ;
MARCILLA, A ;
DEVESA, J ;
VERDU, E .
JOURNAL OF ANALYTICAL AND APPLIED PYROLYSIS, 1993, 27 (02) :245-273
[6]   FLUIDIZED-BED FLASH PYROLYSIS OF ALMOND SHELLS - TEMPERATURE INFLUENCE AND CATALYSTS SCREENING [J].
FONT, R ;
MARCILLA, A ;
VERDU, E ;
DEVESA, J .
INDUSTRIAL & ENGINEERING CHEMISTRY PRODUCT RESEARCH AND DEVELOPMENT, 1986, 25 (03) :491-496
[7]   KINETICS OF THE PYROLYSIS OF ALMOND SHELLS AND ALMOND SHELLS IMPREGNATED WITH COCL2 IN A FLUIDIZED-BED REACTOR AND IN A PYROPROBE 100 [J].
FONT, R ;
MARCILLA, A ;
VERDU, E ;
DEVESA, J .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1990, 29 (09) :1846-1855
[8]   CATALYTIC PYROLYSIS OF ALMOND SHELLS - INFLUENCE OF TEMPERATURE AND COCL2 TO ALMOND SHELL RATIO [J].
FONT, R ;
MARCILLA, A ;
VERDU, E ;
DEVESA, J .
CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1990, 68 (02) :312-318
[9]   GASEOUS HYDROCARBONS FROM FLASH PYROLYSIS OF ALMOND SHELLS [J].
FONT, R ;
MARCILLA, A ;
DEVESA, J ;
VERDU, E .
INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1988, 27 (07) :1143-1149
[10]   CORRELATION OF VOLATILE PRODUCTS FROM FAST CELLULOSE PYROLYSIS [J].
FUNAZUKURI, T ;
HUDGINS, RR ;
SILVESTON, PL .
INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1986, 25 (01) :172-181