System Cost Considerations

Economic Considerations. The principal economic consideration is, of course, total installed system cost, including the initial cost of the flow primary, flow secondary, and related ancillary equipment as well as material and labor required for installation. Other typical considerations are operating costs and the requirements for scheduled maintenance. An economic factor of increasing importance is the cost of disposal at the end of normal flow meter service life. This may involve meter decontamination if hazardous fluids have been measured. 

Conceptual Design of MHD Repowered Plant. The first step toward MHD plant commercialization is a pilot-scale demonstration plant. Repowering of existing plants, actively under study both in the United States and elsewhere (65), allows use of existing systems at considerable cost savings compared to building a new plant from the ground up. It also ensures that the pilot scale demonstration occurs in a reaHstic utiHty environment and... 

Heat pumps are particularly suitable for recycling heat energy in the chemical-process industries. For the outlay of an additional fixed-capital expenditure Cec on a heat-pump system, a considerable reduction in the annual heating cost can be effected. 

The size and therefore the cost of a conventionally wound voltage transformer will be almost proportional to the system voltage for which it is wound. As a cost consideration, therefore, a more economical alternative is found in a Capacitor Voltage Transformer (CVT) (Figure 15.6(a)). 

The foregoing comparison of different valve arrangements for both full main air blower trains and TPG trains emphasizes its importance. The range of desired regenerator control, expected modes of operation, and system constraints all influence the choice of valve aiTangements. The selected arrangement depends on safety consciousness, cost considerations, and desired process flexibility. 

Commercial spectrometers are usually bakeable, can reach ultrahigh-vacuum pressures of better than 10" Torr, and have fast-entry load-lock systems for inserting samples. The reason for the ultrahigh-vacuum design, which increases cost considerably, is that reactive surfaces, e.g., clean metals, contaminate rapidly in poor vacuum (1 atomic layer in 1 s at 10 Torr). If the purpose of the spectrometer is to always look at as-inserted samples, which are already contaminated, or to examine rather unreactive surfaces (e.g., polymers) vacuum conditions can be relaxed considerably. 

The use of canopy hoods or remote capture of fume is usually considered only after the rejection of source or local hood capture concepts. The common reasons for rejecting source or local hood capture are usually operating interference problems or layout constraints. In almost all cases, a canopy hood system represents an expensive fume collection approach from both capital and opetating cost considerations. Remote capture depends on buoyant ait curtents to carry the contaminated gas to a canopy hood. The rising fume on its way to the hood is often subjected to cross-drafts within the ptocess buildings or deflected away from the hood by objects such as cranes. For many of these canopy systems, the capture efficiency of fume may be as low as 30-50%. 

Auditing the quality system (internal) Economics - Quality-related cost considerations V... 

The fatty adds commonly encountered in biological systems are straight chained alkanoic or alkenoic adds, containing an even number of carbon atoms (usually Ch-Ch). natural n Senera / these fatty adds can be produced readily by extraction of the lipids from sources natural sources and saponifying the neutral triglycerides. This is satisfactory providing a mixture of fatty acids is acceptable. Purification of spedfic fatty adds from the saponification mixture increases the costs considerably. 

For making compatible blends, the polymers should have comparable polarities and viscosities. The oil needs to be selected properly so that its solubility parameter is close to those for blend components. The cure system should be efficient for all constituent rubbers and the filler system needs to be appropriate. Finally, cost consideration should be taken into account to provide a commercially viable product. 

The feasibility of detection-based defensive strategies also depends on how the detectors are deployed and how they are actually used. Deployment considerations include the number and placement of detectors, whether in open spaces or in HVAC ductwork. In this respect, airport terminals are likely to be more difficult to protect by this strategy than are aircraft, owing to the vastly greater air volume and necessarily greater physical spacing between detectors in terminals. To the extent that more than one type of independent detection or verification system is needed to achieve acceptable POD and PFA, the system costs are multiplied. 

Maher et al. [26] describe the successful implementation of pico hydro (<5 kW) systems in two communities in Kenya. Costs for these systems were considerably less than comparable PV or auto battery systems. The systems were constructed locally using available materials and community labor. 

Cost considerations based on the low total system price for a household appliance did not allow for the customer-specific development of semiconductor components. The high development cost would either have to be split over a sufficiently large production volume or result in an unacceptably high unit price. Both are not given in the European market. 

These cost considerations have to rely on some risk analysis if the risks of producing smaller series for stationary markets, which can absorb fuel-cell systems at a specific cost of some 500/kWel are smaller, it seems likely that stationary fuel cells will enter the market earlier than mobile fuel cells in cars at a specific cost of 50 to 80/kWel, but with much larger production series. 

There are many variables associated with estimating the cost of perchlorate contamination. For many commercially available systems, cost data is estimated based on pilot- or bench-scale tests. These estimates may not include secondary contaminant disposal costs or other costs of operation. Costs are also likely to vary considerably based on site-specific conditions such as contaminant concentrations, additional contamination, treatment volumes, and treatment rates. 

The estimated capital cost of using a SAREX CFP system to treat contaminated sediment is 1,000,000 (D12618B, p. 7). The operating cost for a closed system application of this technology ranges from 65 to 85 (1996 dollars) per metric ton. The cost to operate this technology as an open system is considerably lower (personal communication Christopher Hebble, SRS, 1997). 

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