By K.A. Jacques, T.P. Lyons, D. R. Kelsall
Gains the total content material of the broadcast ebook in PDF structure, in a CD-ROM layout.
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This approach to enzyme addition is able to increase yield to higher levels than normally seen with single activity liquid glucoamylase. 1 gallons/bushel (122 gallons or 456 liters per tonne). Table 5. Advantages of Rhizozyme™ over conventional glucoamylase. 0 None 50,000 None None 2500 5000 Saccharification: should we have high levels of sugar going into the fermentor? IF A SACCHARIFICATION STEP IS USED Saccharification of distillery mashes is a somewhat controversial subject. Over the last 10 years many distillers have changed from saccharifying mash in a dedicated saccharification vessel (or ‘sacc’ tank) to adding the saccharifying enzyme directly to the fermentor in a process referred to as Simultaneous Saccharification and Fermentation (SSF).
These enzymes satisfy the requirement to saccharify dextrins to glucose but have the additional activities required to attack, for example, ß-linked glucose polymers, if present. sources such as Aspergillus niger and Rhizopus sp. 5. These conditions of temperature and pH can cause significant problems in plants using dedicated saccharification tanks because they are quite conducive to the growth of certain bacterial contaminants. The claimed benefit of pre-saccharification of mash prior to fermentation is that a high level of glucose is made available at the start of fermentation.
Also varies within each category (Tables 1 and 2). In spite of these differences, the major components of all lignocellulosics are cellulose, hemicellulose, lignin and extraneous materials (Singh and Mishra, 1995). Of these, cellulose is by far the most abundant organic substrate. Cellulose is a linear homopolymer of anhydroglucose residues that are linked via ßO-1, 4-glycosidic bonds. Different forms of cellulose exist with varying degrees of polymerization and molecular weight (Singh and Mishra, 1995).