Big Chemical Encyclopedia

Chemical substances, components, reactions, process design ...

Articles Figures Tables About

Costs energy

Having established that there is apparently a mechanism whereby the problems of sequencing and heat integration can be decoupled for simple columns on the basis of energy costs, it is interesting to consider whether there is any conflict with capital cost. A column sequence that handles a large amount of heat must have a high capital cost for two reasons ... [Pg.146]

Hence the gas turbine is the most profitable in terms of energy costs. However,... [Pg.200]

The energy cost of the process can be set without having to design the heat exchanger network and utility system. These energy targets cam be calculated directly from the material and energy balance. Thus... [Pg.210]

In addition to being able to predict the energy costs of the heat exchanger network and utilities directly from the material and energy balance, it would be useful to be able to calculate the capital cost, if this is possible. The principal components that contribute to the capital cost of the heat exchanger network are... [Pg.213]

EP = value of products - raw materials costs - annualized capital cost - energy cost... [Pg.241]

It must be emphasi2ed that any energy costs for the separation in the tradeoffs shown in Fig. 10.7 must be taken within the context of the overall heat integration problem. The separation might after all be driven by heat recovery. [Pg.288]

The Tradeoffs Between Process Changes, Utility Selection, Energy Cost, and Capital Cost... [Pg.323]

Distillation capital costs. The classic optimization in distillation is to tradeoff capital cost of the column against energy cost for the distillation, as shown in Fig. 3.7. This wpuld be carried out with distillation columns operating on utilities and not integrated with the rest of the process. Typically, the optimal ratio of actual to minimum reflux ratio lies in the range 1.05 to 1.1. Practical considerations often prevent a ratio of less than 1.1 being used, as discussed in Chap. 3. [Pg.349]

Most characteristics of amphiphilic systems are associated with the alteration of the interfacial stnicture by the amphiphile. Addition of amphiphiles might reduce the free-energy costs by a dramatic factor (up to 10 dyn cm in the oil/water/amphiphile mixture). Adding amphiphiles to a solution or a mixture often leads to the fomiation of a microenuilsion or spatially ordered phases. In many aspects these systems can be conceived as an assembly of internal interfaces. The interfaces might separate oil and water in a ternary mixture or they might be amphiphilic bilayers in... [Pg.2381]

Conformations m which the torsion angles between adjacent bonds are other than 60° are said to have torsional strain Eclipsed bonds produce the most torsional strain staggered bonds none Because three pairs of eclipsed bonds are responsible for 12 kJ/mol (2 9 kcal/mol) of torsional strain m ethane it is reasonable to assign an energy cost of 4 kJ/mol (1 kcal/mol) to each pair In this chapter we 11 learn of additional sources of strain m molecules which together with torsional strain comprise steric strain... [Pg.107]

About 85% of U.S. adipic acid production is used captively by the producer, almost totally ia the manufacture of nylon-6,6 (194). The remaining 15% is sold ia the merchant market for a large number of appHcations. These have been developed as a result of the large scale availabihty of this synthetic petrochemical commodity. Prices for 1960—1989 for standard resia-grade material have parahed raw material and energy costs (petroleum and natural gas)... [Pg.246]

Life cycle cost analysis is the proper tool for evaluation of alternative systems (11,12). The total cost of a system, including energy cost, maintenance cost, interest, cash flow, equipment replacement and/or salvage value, taxes, inflation, and energy cost escalation, can be estimated over the useflE life of each alternative system. A Hst of life cycle cost items which may be considered for each system is presented in Tables 3 and 4. Reference 14 presents a cash flow analysis which also includes factors such as energy cost escalation. [Pg.363]

A.nnual energy and fuel costs electric energy costs chiller or compressor pumps chilled water heating water condenser or tower water weE water... [Pg.363]


See other pages where Costs energy is mentioned: [Pg.76]    [Pg.87]    [Pg.160]    [Pg.166]    [Pg.172]    [Pg.211]    [Pg.236]    [Pg.242]    [Pg.242]    [Pg.349]    [Pg.362]    [Pg.363]    [Pg.401]    [Pg.402]    [Pg.737]    [Pg.754]    [Pg.901]    [Pg.2370]    [Pg.2380]    [Pg.2382]    [Pg.2833]    [Pg.2833]    [Pg.119]    [Pg.258]    [Pg.127]    [Pg.155]    [Pg.88]    [Pg.88]    [Pg.229]    [Pg.419]    [Pg.69]    [Pg.76]    [Pg.78]    [Pg.96]    [Pg.171]    [Pg.358]    [Pg.364]   
See also in sourсe #XX -- [ Pg.686 , Pg.1376 ]

See also in sourсe #XX -- [ Pg.7 ]

See also in sourсe #XX -- [ Pg.204 ]

See also in sourсe #XX -- [ Pg.56 ]

See also in sourсe #XX -- [ Pg.84 , Pg.85 ]

See also in sourсe #XX -- [ Pg.232 , Pg.235 , Pg.308 ]

See also in sourсe #XX -- [ Pg.433 , Pg.434 , Pg.435 ]

See also in sourсe #XX -- [ Pg.420 , Pg.421 ]

See also in sourсe #XX -- [ Pg.100 ]




SEARCH



© 2026 chempedia.info