By D. L. Pyle (auth.), P. J. Fryer, D. L. Pyle, C. D. Rielly (eds.)
Industrial nutrients processing includes the construction of additional worth meals on a wide scale; those meals are made via blending and processing varied parts in a prescribed means. The meals undefined, traditionally, has now not designed its strategies in an engineering feel, i.e. by way of realizing the actual and chemical ideas which govern the operation of the plant after which utilizing these rules to increase a technique. relatively, techniques were 'designed' by means of buying gear from various providers after which connecting that gear jointly to shape a whole strategy. whilst the method being run has basically been scaled up from the kitchen then this won't topic. although, there are limits to the technique. • because the turns into extra subtle, and economies of scale are exploited, then the dimensions of plant reaches a scale the place systematic layout concepts are wanted. • the diversity of procedures and items made by way of the nutrition has elevated to incorporate meals that have no kitchen counterpart, similar to low-fat spreads. • it is important to make sure the standard and security of the product. • Plant has to be versatile and ready to deal with the necessity to make various items from a number of elements. this can be in particular very important as markets evolve with time. • the normal layout technique can't effectively deal with multi-product and multi-stream operations. • techniques needs to be energetically effective and meet glossy environmen tal standards.
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Extra info for Chemical Engineering for the Food Industry
The reaction products are at equilibrium. The chromatograph is assumed to achieve perfect separation of the fructose and glucose: that is, the product stream is glucose-free; the recycle is fructose-free; al/ the oligosaccharide leaves the separator in the glucose stream. We now consider how the process yield varies with recycle, R. Basis: 100 kg fresh feed At steady state, there is no change in any composition or flow; then an overall balance (see Fig. 20) where x is the fraction of glucose in stream P.
The signs associated with the E-values are important. A negative sign corresponds to an object whose energy level is below the datum. Provided the datum levels are defined unambiguously, the calculation of energy levels with respect to other datum levels is a trivial matter. Moreover, the route by which the object reaches its stationary level A or B is irrelevant: energy is a function of state and not of path. This brief discussion has been in terms of the very familiar concept of potential energy, whose application to many thermal problems in process engineering is relatively limited.
This can be represented graphically (Fig. 18). 04 - is not surprising, as the reaction here is only weakly endothermic, and there would be little loss of accuracy in assuming that the system was isothermal and adiabatic. 42 INTRODUCTION TO PROCESS DESIGN Exit temperature Temperature, T --------. Fig. 10: mass and energy balance solution. 10 illustrates the fact that mass and energy balances cannot always be carried out independently, by computing first a mass balance and then an energy balance.