A continuous, farm-scale, solid-phase fermentation process for fuel ethanol and protein feed production from fodder beets

1984 ◽  
Vol 26 (9) ◽  
pp. 1098-1107 ◽  
Author(s):  
William R. Gibbons ◽  
Carl A. Westby ◽  
Thomas L. Dobbs
1988 ◽  
Vol 31 (7) ◽  
pp. 696-704 ◽  
Author(s):  
William R. Gibbons ◽  
Carl A. Westby ◽  
Eugene Arnold

2008 ◽  
Vol 35 (9) ◽  
pp. 967-973 ◽  
Author(s):  
Carolina Elsztein ◽  
João Assis Scavuzzi de Menezes ◽  
Marcos Antonio de Morais

2009 ◽  
Vol 108 (6) ◽  
pp. 508-512 ◽  
Author(s):  
Yoji Koike ◽  
Ming-Zhe An ◽  
Yue-Qin Tang ◽  
Tomohiro Syo ◽  
Noriko Osaka ◽  
...  

2017 ◽  
Vol 2017 ◽  
pp. 1-9 ◽  
Author(s):  
Songming Luo ◽  
Qiang Li ◽  
Anjun Chen ◽  
Xingyan Liu ◽  
Biao Pu

The purpose of this study was to analyze the volatile compounds in baby ginger paocai and the fresh baby ginger and identify the key aroma components that contribute to the flavor of baby ginger paocai. A total of 86 volatile compounds from the two baby ginger samples were quantified; these compounds were extracted by headspace solid-phase microextraction (HS-SPME) and analyzed by gas chromatography–mass spectrometry (GC-MS). The aroma composition of baby ginger paocai was different from that of fresh baby ginger. Baby ginger paocai was characterized by the presence of aroma-active compounds which varied in concentration from 0.03 to 28.14%. Geranyl acetate was the aroma component with the highest relative content in baby ginger paocai. β-myrcene, eucalyptol, trans-β-ocimene, Z-ocimene, linalool, decanal, cis-citral, geraniol, geranyl acetate, curcumene, and β-bisabolene contributed to the overall aroma of the product of baby ginger paocai which had gone through a moderate fermentation process.


1980 ◽  
Vol 22 (11) ◽  
pp. 2425-2427 ◽  
Author(s):  
K. D. Kirby ◽  
C. J. Mardon
Keyword(s):  

1985 ◽  
Vol 107 (3) ◽  
pp. 402-405 ◽  
Author(s):  
S. Ghosh

This paper presents the development of a novel solid-phase methane fermentation process involving acidic bioleachate production from an organic bed and biomethanation of the bed-liquefaction products in an external methane digester. Process operation with municipal solid waste showed that about 81 percent of the biodegradable volatile solids (VS) could be stabilized during three months of batch operation to afford a methane yield of 0.21 std m3 / kg VS added under ambient (∼25°C) conditions; this compares favorably with an ultimate mesophilic (35°C) methane yield of 0.26 std m3 / kg VS added.


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