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The minimum production

SAQ 8.7 The product value at 100% capadty will now be (total cost of production + 7 to 15% ROD, ie 16.04 to 1654 + 1.12 to 2.48. So the minimum product value will be 17.16 per kg of L-phenylalanine and the maximum product value 19.02 per kg of L-phenylalanine. It is rattier difficult to say whether this fictitious process would survive or could compete. Actual data are absolutely necessary. On the other hand this exercise gives us a better understanding of process economics and can also be used to compare a fermentative process for the production of amino adds with, for example, a chemo-enzymatic process. Calculate the return on investment over a 15 year period for an amino add fermentation, based on the following data and assumptions. Production capadty = 500 tonnes per annum Selling price of product = 50 kg Cost price of product = 24.5 kg 1 Capital = 40 million Taxes = 50%. Assumptions Cost of dealer discount, distribution and freight = 20% total sales Startup costs = 10% of capital Working capital = 25% of net sales Administration plus R and D costs = 12.5% of net sales. [Pg.262]

Ortho-xylene (A) is oxidised to phthalic anhydride (B) in an ideal, continuous flow tubular reactor. The reaction proceeds via the complex consecutive parallel reaction sequence, shown below. The aim of the reaction is to produce the maximum yield of phthalic anhydride and the minimum production of waste gaseous products (C), which are CO2 and CO. [Pg.393]

For some processes, though they would not be classified as batch processes, the period of continuous production will be limited by gradual changes in process conditions such as, the deactivation of catalysts or the fouling of heat-exchange surfaces. Production will be lost during the periods when the plant is shut down for catalyst renewal or equipment clean-up, and, as with batch process, there will be an optimum cycle time to give the minimum production cost. [Pg.30]

The constraints considered so far are concerned with the physical nature of the plant. Constraints are also needed to define the availability of raw materials and product requirements over a time period. For this example, there are no restrictions on crude oil availability or the minimum production required. The maximum production requirement constraints, in t/day, are as follows ... [Pg.47]

Figure 2.13 Influence of moisture content on the temperature of powder in a spray dryer (tp), dryer outlet temperature (f0) and sticking temperature (rs). The minimum product tempera-tured required to avoid problems with sticking is at TPC with the corresponding dryer outlet temperature TOC. (Modified from Hynd, 1980.)... Figure 2.13 Influence of moisture content on the temperature of powder in a spray dryer (tp), dryer outlet temperature (f0) and sticking temperature (rs). The minimum product tempera-tured required to avoid problems with sticking is at TPC with the corresponding dryer outlet temperature TOC. (Modified from Hynd, 1980.)...
Derivation of the expression for the minimum production of S in the systems with constant T and V (volume) differs from the one above only by replacement of enthalpy by internal energy (U) and the Gibbs energy by the Helmholtz energy in the equations. When we set S and P or S and V dissipation turns out to be zero according to the problem statement. In the case of constant U and V or H and P, the interaction with the environment does not hinder the relaxation of the open subsystem toward the state max Sos. [Pg.13]

Cpm)min = the minimum product of stream heat capacity and mass flowrate. [Pg.11]

Breaking out of this situation requires an internal discontinuity - a real step change in performance, characterized by improvement targets of inconceivable proportions. The concept of core costs has proved to be highly successful here over the last 10 to 15 years, particularly in production environments. Core costs are the minimum production costs that would be required if all types of costs... [Pg.157]

How these constraints are formulated is exemplified with the minimum product transport constraint. The qtp c.pr transported quantity of product pr from plant p to customer c either has to be equal to zero or not smaller than a minimum transport quantity QTMINp py. In the GDP formulation of this constraint, logical variable ztp ppyE. true, false denotes whether there is product transport on the given route ... [Pg.208]

Preparative chromatography is widely used for the purification of different compounds, but this procedure needs to be optimized to achieve the minimum production costs. This can be done by computer-assisted modeling. However, this approach requires a priori determination of accurate competitive adsorption isotherm parameters. The methods to determine this competitive information are poorly developed and hence often a time limiting step or even the reason why the computer-assisted optimization is still seldom used. In this thesis in papers IV-VI, a new injection method was developed that makes it possible to determine these competitive adsorption isotherm parameters more easily and faster than before. The use of this new... [Pg.75]

The TPP is often expressed primarily in clinical terms, but should also include the pharmaceutical, technical, regulatory and commercial/marketing attributes required of the product. The TPP is based on the ideal product characteristics which are considered to be desirable, whereas the minimum product profile is based on the minimum product requirements which must be met for the product to be viable and worth developing. For example, the TPP may stipulate an ideal dosing regimen of once daily. However, the minimum product profile may state that the dosing regimen must be no more than twice daily for the product to be competitive. [Pg.159]

If the ROK lime has a top size in excess of (say) 45 mm, it is reduced in size with the minimum production of fines. Jaw and roll crushers are widely used for this duty. [Pg.192]

The Ausmelt system is extremely well suited for the processing of lead secondary and other materials with the minimum production of dioxins and fiirans, because of ... [Pg.160]

The method of precutting or postcutting to length has an effect on roll design. In most cases, sheet-fed products are more prone to flair and the minimum product... [Pg.467]

As with any system of differential equations boundary conditions are necessary to determine a unique solution. The assumptions made concerning the expected profit function, G n, n, k wi), imply that the productivity parameter, p, increases both profit and the optimal level of safety. Thus, the zero profit constraint endogenously determines the minimum productivity of safety equipment in the production of goods... [Pg.99]

A target area is most closely defined by sharp changes in pH and Eh (or dissolved oxygen) and by dissolved radon and radium. The latter two elements may be used to calculate the minimum product of grade times thickne.ss that could produce the anomaly. The most conservative assumption is that the well penetrates the centre of the mineralization. The farther the water travels to the well, the larger is the uranium source for a measured concentration of radon. [Pg.40]

The minimum production and cumulative need values naturally refer to an extensive use of fast reactors the maximum values to the use of open-cycle LWR reactors alone. These data, related to the economically exploitable uranium resources, show that no problems of uranium supply should exist before the year 2000 thereafter the choice of an adequate strategy (including, if possible, a non-marginal use of FBR) becomes fundamental in providing a satisfactory answer to the problems of fuel supply. [Pg.166]

It is easily shown that, if Onsager s reciprocity relations = L i are valid, Eq. 117 is deduced from the condition of the minimum production of entropy. Indeed, the forces remain... [Pg.294]

When the boundary values are left free for the whole boundary surface, the minimum production of entropy leads to the equilibrium state for which the entropy production vanishes. [Pg.303]

Rather lately, an attempt to generalize this principle to a nonlinear irreversible process has been made by Klein, based on a statistical method for a simplified model. He demonstrated that the minimum production properties are also a useful approximation criterion for the stationary state even when the latter is very far from equilibrium. According to a simple example of an irreversible process given in his calculation, it has been found that the entropy production does not decrease monotonically, but passes through its minimum en route to the stationary state. We have already mentioned these results in connection with the variational principle in nonlinear irreversible processes. [Pg.311]

Equation 7.28 ensures that the quantity of product / produced at plant m meets the minimum production requirement and does not exceed its capacity ... [Pg.207]

These operations have to be carried out so as to minimize occupational dose rates, in the minimum time (setting up. actual cutting, cleaning up, packing up, maintenance, etc. ) and with the minimum production of technological and secondary wastes. The following criteria thus apply to the tools ... [Pg.52]


See other pages where The minimum production is mentioned: [Pg.290]    [Pg.120]    [Pg.185]    [Pg.136]    [Pg.262]    [Pg.39]    [Pg.220]    [Pg.210]    [Pg.364]    [Pg.165]    [Pg.386]    [Pg.262]    [Pg.154]    [Pg.353]    [Pg.75]    [Pg.81]    [Pg.132]   
See also in sourсe #XX -- [ Pg.307 ]




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