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Other investment costs catalyst

All other operating costs (catalyst and chemicals, utilities at typical rates fixed charges at 18%/yr. of investment operating labor at 2 men/shift overhead, etc. at 100% of operating labor)... [Pg.175]

In hybrid systems different processes are coupled, for example, reaction and separation by membranes, adsorption, or distillation. This could lead to a reduction of the investment costs as two different functions are combined in one vessel, and one process step is eliminated. For example, a reactor with a catalyst and a membrane may be used or a distillation column with a catalytic packing, which could also lead to an optimal heat integration. Other benefits depend on the specific reaction. For example, equilibrium-limited reactions would benefit if a product is continuously removed in situ, which leads to an enhanced yield beyond the equilibrium. ... [Pg.370]

The operating costs for the manufacture of fuels and chemicals consist of the variable costs such as feed, catalysts, and energy, which depend on the actual consumption and on the price of the various streams needed for production. The fixed costs include labor, maintenance, overhead, and above all the provision for recovering the investment in the plant and lost interest (capital expenditure, i.e., provision for recovering the investment, maintenance, insurance, etc.). The total production costs are the sum of the variable and fixed costs, and depend on the plant complexity and capital-related expenditures. A simple rule is that the annual fixed costs are 35% of the total investment, 25% of which accounts for the capital-related expenditures and 10% for the other fixed costs. The utilization degree where the production costs reach the revenues is the break-even point. [Pg.524]

The total working capital must be added to this estimate of fixed capital to obtain the full composite figure for the capital cost. The working capital represents an investment in storage of feed ammonia for one week, product acid for one week, stores (e.g. catalyst) and others. Table E.3 in Appendix E summarizes these incurred costs. [Pg.101]

We will now look at some other important industrial applications of the chemical principles studied so far. Each of these processes involves at least one step that reaches equilibrium, and so the position of the equilibrium has to be altered in order to make the process economically viable. Although both raising the temperature and increasing the concentration of reactants can speed up reactions, the latter method is costly and the former may destroy some substances in the process. The use of a suitable catalyst is generally more efficient and economical in the long run. A considerable amount of time and money is invested in the development of catalysts. The detailed composition of an industrial catalyst is often a well-guarded secret. [Pg.247]

Alkyllithium initiators offer some peculiarities in contrast to the coordination catalysts [41]. Alkyllithium initiation can tolerate very high temperatures. As expensive cooling facilities are not needed, the polymerization can proceed at high reaction rates with low investment and operating costs. Since the polymerization runs without termination or other side reactions under formation of living polymers , the preparation of block polymers by sequential addition of monomers is possible. It also permits the introduction of functional groups on the end of each chain. Because the initiation step is fast relative to the pro-... [Pg.307]

A fixed bed reactor has many unique and valuable advantages relative to other reactor types. One of its prime attributes is its simplicity, with the attendant consequences of low costs for construction, operation, and maintenance relative to moving bed or fluidized bed operation. Fixed bed reactors require a minimum of auxiliary equipment and are particularly appropriate for use in small commercial units when investments of large sums for control, catalyst handling, and supporting facilities would be economically prohibitive. Another major advantage of this mode of operation is implicit in the use of the term fixed bed reactor (i.e., there are no problems in separating the catalyst from the reactor effluent stream). (In many fluidized bed systems, catalyst recovery can be quite troublesome and require substantial equipment costs.) Another important attribute of fixed bed reactors is the wide variation in... [Pg.372]


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