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Cereals processing technology

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Breadmaking 207<br />

The development of no-time (i.e. no resting time in bulk before dividing)<br />

dough making processes changed traditional bread making. Foremost amongst the<br />

process changes was the development and commercialisation of the Chorleywood<br />

Bread Process (CBP). In the CBP the development of optimum dough qualities<br />

was achieved in the mixer by transferring a defined energy input to the dough<br />

(Cauvain, 1998a). The result of the introduction of the CBP was to eliminate the<br />

need for bulk fermentation periods with considerable raw material and time<br />

savings, as well as to initiate changes in ingredient and <strong>processing</strong> technologies<br />

which are still evolving today. The principles of the CBP were adopted in many<br />

countries around the world (Gould, 1998). Even in those bakeries which did not<br />

adopt the CBP there has been a similar trend away from long periods of bulk<br />

fermentation to shorter <strong>processing</strong> times and the use of more functional<br />

ingredients to achieve more consistent bread quality (Cauvain, 1998a).<br />

10.3.1 The Chorleywood Bread Process<br />

The basic principles involved in the production of bread and fermented goods by<br />

the CBP remain the same as those first published by the Chorleywood team in<br />

1961 though the practices have changed with changes in ingredients and mixing<br />

equipment. The essential features of the CBP are:<br />

• Mixing and dough development in a single operation lasting between 2 and 5<br />

minutes to a fixed energy input.<br />

• The addition of an oxidising improver above that added in the flour mill.<br />

• The inclusion of a high melting point fat, emulsifier or fat and emulsifier<br />

combination.<br />

• The addition of extra water to adjust dough consistency to be comparable<br />

with those from bulk fermentation.<br />

• The addition of extra yeast to maintain final proof times comparable with that<br />

seen with bulk fermentation.<br />

• The control of mixer headspace atmosphere to achieve given bread cell<br />

structures.<br />

As the level of energy per kg dough in the mixer increases bread volume<br />

increases and with the increase in bread volume comes a reduction in cell size,<br />

increased cell uniformity and improved crumb softness. The role of energy<br />

during CBP mixing has yet to be fully explained but may be likened to the<br />

effects of natural or chemical reduction and, as such, will increase the available<br />

sites for oxidation. Chamberlain (1985) considered that only about 5% of the<br />

available energy was required to break the disulphide bonds with the rest being<br />

consumed by mixing of the ingredients and the breaking of weaker bonds. The<br />

input of energy during mixing causes a considerable temperature rise to occur<br />

and typically final dough temperatures fall in the region of 27 to 32ºC.<br />

The cell structure in the final bread does not become finer (smaller average<br />

cell size) as the result of <strong>processing</strong> CBP doughs. In the case of CBP doughs<br />

final bread crumb cell structure is almost exclusively based on an expanded

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