scholarly journals Accelerator Operations

2020 ◽  
pp. 519-583
Author(s):  
M. Lamont ◽  
J. Wenninger ◽  
R. Steinhagen ◽  
R. Tomás García ◽  
R. Garoby ◽  
...  
Keyword(s):  
Capital Investment ◽  
Particle Accelerator ◽  
Machine Availability ◽  
The Cost ◽  
Measures Of Performance ◽  
Integrated Luminosity

AbstractThe cost of building a particle accelerator is a major capital investment. Commissioning should be swift and the subsequent exploitation of a facility must provide an effective return. This return may be difficult to quantify unambiguously but generally acceptable measures of performance can be established. These measures might include: machine availability; integrated luminosity; protons on target; beam hours to users and so on.

Exergoeconomic analysis of renewable multi-generation system

2020 ◽  
pp. 99-111
Author(s):  
Vontas Alfenny Nahan ◽  
Audrius Bagdanavicius ◽  
Andrew McMullan
Keyword(s):  
Capital Investment ◽  
Combined Cycle ◽  
Asian Countries ◽  
Generation System ◽  
Integrated Gasification Combined Cycle ◽  
Heating And Cooling ◽  
Integrated Gasification ◽  
Exergoeconomic Analysis ◽  
Main Components ◽  
The Cost

In this study a new multi-generation system which generates power (electricity), thermal energy (heating and cooling) and ash for agricultural needs has been developed and analysed. The system consists of a Biomass Integrated Gasification Combined Cycle (BIGCC) and an absorption chiller system. The system generates about 3.4 MW electricity, 4.9 MW of heat, 88 kW of cooling and 90 kg/h of ash. The multi-generation system has been modelled using Cycle Tempo and EES. Energy, exergy and exergoeconomic analysis of this system had been conducted and exergy costs have been calculated. The exergoeconomic study shows that gasifier, combustor, and Heat Recovery Steam Generator are the main components where the total cost rates are the highest. Exergoeconomic variables such as relative cost difference (r) and exergoeconomic factor (f) have also been calculated. Exergoeconomic factor of evaporator, combustor and condenser are 1.3%, 0.7% and 0.9%, respectively, which is considered very low, indicates that the capital cost rates are much lower than the exergy destruction cost rates. It implies that the improvement of these components could be achieved by increasing the capital investment. The exergy cost of electricity produced in the gas turbine and steam turbine is 0.1050 £/kWh and 0.1627 £/kWh, respectively. The cost of ash is 0.0031 £/kg. In some Asian countries, such as Indonesia, ash could be used as fertilizer for agriculture. Heat exergy cost is 0.0619 £/kWh for gasifier and 0.3972 £/kWh for condenser in the BIGCC system. In the AC system, the exergy cost of the heat in the condenser and absorber is about 0.2956 £/kWh and 0.5636 £/kWh, respectively. The exergy cost of cooling in the AC system is 0.4706 £/kWh. This study shows that exergoeconomic analysis is powerful tool for assessing the costs of products.

What Drives a Successful Technology Implementation?

2013 ◽  
pp. 340-357
Author(s):  
Kawal Kapoor ◽  
Yogesh K. Dwivedi ◽  
Michael D. Williams ◽  
Mohini Singh ◽  
Mark J. Hughes
Keyword(s):  
Public Sector ◽  
Radio Frequency Identification ◽  
Technology Implementation ◽  
Capital Investment ◽  
Stock Management ◽  
Implementation Team ◽  
Public Sector Organizations ◽  
Self Service ◽  
The Individual ◽  
The Cost

Radio Frequency Identification (RFID) is revolutionizing item identification and tracking. The technology demonstrates complexities in terms of (a) huge initial capital investment, (b) validating the need for RFID followed by its implementation decisions, (c) risks associated with consumer acceptance and consequences of incorrect implementation, and (d) capability to support enhancements and upgrades in cordial agreement with the individual implementer organizations. This paper explores the extent of RFID implementation at the Swansea University Library, examining the Social, Technological, Economic, and Managerial (STEM) aspects directly associated with implementation. A focused interview approach was resorted to, for data collection purposes. The core implementation team for RFID at Swansea University was interviewed to gain insights into the study’s areas of interest. It was found that self service is the most sought after benefit. It simplifies stock management and enhances security at the libraries. Although the cost of the system remains a concern, varying on the basis of the scale of implementation, vandalism also continues to exist but to a reduced degree. University libraries are public sector organizations, consequently leading these findings to have an insinuation for RFID implementations in other public sector organizations as well.

Distillation-based Separation Systems Synthesis

1995 ◽  
Author(s):  
Christodoulos A. Floudas
Keyword(s):  
Capital Investment ◽  
Optimal Configuration ◽  
Synthesis Problem ◽  
Total Annual Cost ◽  
Separation Processes ◽  
Distillation Columns ◽  
Separation Systems ◽  
Total Capital ◽  
Separation Sequence ◽  
The Cost

This chapter presents two applications of MINLP methods in the area of separations. Section 9.1 provides an overall introduction to the synthesis of separation systems. Section 9.2 focuses on sharp heat-integrated distillation sequencing. Section 9.3 presents an application of nonsharp separation synthesis. The synthesis of distillation-based separation sequences has been one of the most important subjects of investigation in the area of process synthesis. This is attributed to the significant contribution of separation processes to the total capital investment and operating expenses of a chemical plant. As a result, a lot of interest has been generated in the development of systematic approaches that select optimal sequences of distillation columns. Westerberg (1985) provided a comprehensive review of the distillation-based separation synthesis approaches, as well as presented a classification of different types of separation problems along with their associated challenges. Nishida et al. (1981) and Smith and Linnhoff (1988) reviewed the general separation synthesis problem (i.e., not only distillation-based) and presented the progress made. To illustrate the nature of the distillation-based separation system synthesis problem, let us consider its generic definition shown in Figure 9.1, which is as follows: . . . Given a number of input multicomponent streams which have specified amounts for each component, create a cost-optimal configuration of distillation columns, mixers, and splitters that produces a number of multicomponent products with specified composition of their components. . . The products feature components that exist in the input streams and can be obtained by redistributing the components existing in the input streams, while the cost-optimal configuration corresponds to the least total annual cost one. Most of distillation columns or sequences can be classified as (i) Sharp, (ii) Nonsharp, (iii) Simple, (iv) Complex, (v) Heat-integrated, and (vi) Thermally coupled. In (i), a column separates its feed into products without overlap in the components. An example is the separation of a stream consisting of four components A, B, (C, and D via a distillation column, into one product consisting of only A and another product featuring B, C, and D. If all columns are sharp, then the separation sequence is termed as sharp sequence.

Techno-Economic Feasibility Analysis of Pumped Storage Hydroelectricity in Abandoned Underground Coal Mines

2020 ◽  
Vol 142 (12) ◽  
Author(s):  
Dacheng Shang ◽  
Peng Pei ◽  
Yujun Zuo
Keyword(s):  
Coal Seam ◽  
Capital Investment ◽  
Economic Feasibility ◽  
Abandoned Mines ◽  
Cost Of Energy ◽  
Calculation Results ◽  
Pumped Storage ◽  
Geological Constraints ◽  
The Cost ◽  
Cycle Efficiency

Abstract It is anticipated that utilizing the underground space in abandoned mines to build and operate pumped-storage hydroelectricity (PSH) plants can reduce capital investment and geological constraints. However, there are currently few detailed investigations into techno-economic feasibility except for conceptual studies. In this paper, an underground coal mine in Guizhou, China was used as a reference, and the PSH layout was designed; in addition, the head loss, plant efficiency, and major cost components were investigated. The calculation results show that the capital investment of mine-based PSH was 33–50% less than that of conventional PSH. Sensitivity analysis found a clear influence of coal seam inclination on the performance of the mine-based PSH. Under the assumed conditions, the plant cycle efficiency increased from 62.7% to 71.5% when the coal seam dip varied from 5 deg to 25 deg. Depending on different price scenarios, when the coal seam inclination was steep enough, the cost of energy storage of a mine-based PSH plant was competitive compared with conventional PSH, and the plant could even become profitable. The influence of the dip of coal seam was more pronounced when in the lower range (5–15 deg) than the higher range (15–25 deg).

scholarly journals COMPARAÇÃO ENTRE OS TRATAMENTOS COM TANASE E COM GELATINA PARA CLARIFICAÇÃO DO SUCO DE CAJU ( Anacardium occidentale L.)

2002 ◽  
Vol 20 (1) ◽  
Author(s):  
SONIA COURI ◽  
LUCIANE FERREIRA DE MENEZES ◽  
GUSTAVO ADOLFO SAAVEDRA PINTO ◽  
MARIA DE LOURDES M. SOUZA ◽  
SUELY PEREIRA FREITAS
Keyword(s):  
Economic Analysis ◽  
Capital Investment ◽  
Apple Juice ◽  
Anacardium Occidentale ◽  
Tannin Content ◽  
Cashew Apple Juice ◽  
Hydrolysable Tannin ◽  
Juice Clarification ◽  
Cashew Apple ◽  
The Cost

Comparou-se o tratamento da polpa do caju com tanase e com gelatina, visando à redução da turbidez e do teor de taninos. Os resultados indicaram que a redução das concentrações de taninos totais, hidrolisáveis, proantocianidinas e turbidez ficaram em 39%, 50%, 32% e 94% para sucos tratados com gelatina e 46%, 88%, 2% e 88% para a polpa tratada com tanase, respectivamente. Deste modo, o tratamento com gelatina foi eficiente para remoção de proantocianidinas, enquanto que o tratamento enzimático foi mais eficiente na redução de taninos hidrolisáveis. Os produtos obtidos não apresentaram diferenças visuais. Estudo comparativo de pré-viabilidade econômica mostrou que o investimento de capital para obtenção do suco de caju clarificado com enzima é menor que para o suco clarificado com gelatina. Entretanto, o custo de produção do suco de caju clarificado com gelatina é menor devido ao preço elevado da enzima tanase. COMPARISION OF THE CASHEW APPLE (Anacardium occidentale L.) JUICE CLARIFICATION WITH TANNASE AND GELATIN Abstract Tannase and gelatin were compared for treatment of cashew apple pulp aiming to reduce turbidity and tannin content. The results indicated that the decrease in concentrations of total tannin, hydrolysable tannin, proanthocyanidin, and turbidity was 39%, 50%, 32% and 94% for juices treated with gelatin and 46%, 88%, 2% and 88% for pulp treated with tannase, respectively. In this way the treatment with gelatin was more efficient to remove proanthocyanidin, whereas enzymatic ones was better for hydrolysable tannin decrease. The obtained products didn’t present visual differences. The comparative economic analysis for the cashew-apple juice production showed that the capital investment for the enzymatic clarification is lower than for the conventional clarification process, using gelatin. Although, the cost of clarified cashew apple juice using gelatin is lower due to the high cost of the enzyme tannase.

Hotel and Dependency Costs of Residents in Old People's Homes

1978 ◽  
Vol 7 (1) ◽  
pp. 1-22 ◽  
Author(s):  
Bleddyn Davies ◽  
Martin R. J. Knapp
Keyword(s):  
Residential Care ◽  
Capital Investment ◽  
Self Care ◽  
Marginal Costs ◽  
Unit Costs ◽  
Long Run ◽  
Average Unit ◽  
Short Run ◽  
The Cost ◽  
Old People's Homes

AbstractA comparison of costs to the organization of alternative forms of care requires estimates for similar types of client. The degree of dependency is the main characteristic in which comparability is necessary with regard to services for the aged. This paper presents estimates of the costs incurred in providing residential care for clients of four degrees of incapacity for self-care – the capacity implicit in Bevan's residential hotel model of the old people's home, and three progressively more severe states of dependency. The estimates are for two cost concepts – average (unit) costs and marginal costs (the cost of caring for an additional person). The paper also estimates both long-run costs (costs that it is appropriate to take into account in decisions in which capital investment in new plant is being considered), and short-run costs (costs that it is appropriate to consider when the issue is the allocation of existing capacity between client groups). It also examines the consequences of the size of the home with regard to costs. Inter alia the paper shows:(a) that the size of home beyond which costs do not fall with scale provides for as many as fifty places (equivalent to an average daily census of forty-six residents); and(b) that, although the dependency components of costs are much smaller than the hotel components, dependency costs are large enough for it to be important to base comparisons of alternative forms of care on estimates of costs for clients which are comparable with respect to dependency.

Paper 8: Maintenance Planning Applied to Plant Auxiliaries in the Central Electricity Generating Board

1966 ◽  
Vol 181 (14) ◽  
pp. 87-118
Author(s):  
V. J. Wright ◽  
R. E. Seymour ◽  
N. D. Norris
Keyword(s):  
Capital Investment ◽  
Critical Path ◽  
Effective Control ◽  
Service Experience ◽  
Technical Data ◽  
Design Engineers ◽  
Power Stations ◽  
Economic Methods ◽  
Minimum Requirements ◽  
The Cost

The C.E.G.B. operates 230 power stations of various ages and output capacities representing a total capital investment of some £2400 million. The steam conditions, sizes of generating units, and complexity of the installed plant reflect the stage of technical development at the time of their construction. These factors influence the cost of production at individual stations as also do the nature and cost of fuel. The economic level of maintenance at each station is thus dependent upon a number of factors and must generally be established locally. This places an obligation on the maintenance engineer to collect and consider economic, in addition to technical, data. Also, service experience must be fed back to the design engineer so that future plant designs may be improved. Unless a simple and effective control system is employed paper work can become an intolerable burden. Power station maintenance can be broadly divided between: (1) work which can only be carried out while a generating unit is shut down; (2) work which can be carried out with the main plant on load. The first category has received the greatest attention, since the cost of keeping a modern generator out of service can be substantial. Planning of this work is based on Critical Path Analysis techniques which are now well known and widely practised. However, the day-to-day maintenance of a large variety of auxiliary plant also presents a heavy planning burden upon the maintenance department. The basic minimum requirements for the effective local control of this work have been examined, while the most economic methods of: (a) co-ordinating maintenance in a number of stations in the best national interest, and (b) ensuring that service experience is fed back to design engineers are also receiving attention.

Thermoeconomic Optimization of COOLCEP-S: A Novel Zero-CO2-Emission Power Cycle Using LNG (Liquified Natural Gas) Coldness

2008 ◽  
Author(s):  
Meng Liu ◽  
Noam Lior ◽  
Na Zhang ◽  
Wei Han
Keyword(s):  
Natural Gas ◽  
Capital Investment ◽  
Power Plants ◽  
High Efficiency ◽  
Pressure Ratio ◽  
Payback Period ◽  
Inlet Temperature ◽  
Pinch Point ◽  
Cost Of Electricity ◽  
The Cost

This paper presents a thermoeconomic optimization of a novel zero-CO2 and other emissions and high efficiency power and refrigeration cogeneration system, COOLCEP-S† which uses the liquefied natural gas (LNG) coldness during its revaporization. It was predicted that at the turbine inlet temperature (TIT) of 900°C, the energy efficiency of the COOLCEP-S system reaches 59%. The thermoeconomic optimization determines the specific cost, the cost of electricity, and the system payback period. The optimization started by performing a thermodynamic sensitivity analysis, which has shown that for a fixed TIT and pressure ratio, the pinch point temperature difference in the recuperator, ΔTp1, and that in the condenser, ΔTp2, are the most significant unconstrained variables to have a significant effect on the thermal performance of this novel cycle. The thermoeconomic analysis of the cycle (with fixed net power output of 20 MW and plant life of 40 years) shows that the payback period with the revenue from electricity and CO2 mitigation was ∼5.9 years, and would be reduced to ∼3.1 years when there is a market for the refrigeration byproduct. The capital investment cost of the economically optimized plant is estimated to be about $1,000/kWe, and the cost of electricity is estimated to be 0.34–0.37 CNY/kWh (∼0.04 $/kWh). These values are much lower than those of conventional coal power plants being installed at this time in China, which, in contrast to COOLCEP-S, do produce CO2 emissions at that.

Paper 4: Gas-Turbine Cycles and Associated Problems

1968 ◽  
Vol 183 (14) ◽  
pp. 28-36
Author(s):  
R. H. Burdett ◽  
D. W. Thomas
Keyword(s):  
Great Britain ◽  
Gas Turbine ◽  
Capital Investment ◽  
Nuclear Reactors ◽  
Electricity Supply ◽  
Operating Parameters ◽  
Reactor Technology ◽  
The Cost ◽  
Cycle Efficiency ◽  
The Given

The practical value of cycle efficiency is influenced by the extent of the capital investment necessary to achieve that efficiency and also by the quality, and hence the cost, of the fuel necessary for the successful attainment of the operating parameters necessary to the given efficiency level. This paper shows how such considerations have led to proposals for combined gas/steam cycles. The gas turbine in electricity supply has been severely limited in its extent of application because of the considerable problems and implied limitations of cheap fuels. In the future the coolant of gas-cooled nuclear reactors could offer greatly widened scope for the application of gas turbine technology. This paper explores the prospects in the context of the developments which may be expected in advanced gas-cooled reactor technology as it is evolving in Great Britain.

Relation of Corrosion to Business Costs★

CORROSION ◽  
1954 ◽  
Vol 10 (9) ◽  
pp. 273-278
Author(s):  
AARON WACHTER
Keyword(s):  
Indirect Effects ◽  
Capital Investment ◽  
Corrosion Damage ◽  
Operating Costs ◽  
Competitive Condition ◽  
Maintenance Costs ◽  
Doing Business ◽  
Functional Aspects ◽  
Product Sales ◽  
The Cost

Abstract Every business can benefit from reduction of its losses due to corrosion. Awareness of all possible sources of such losses is essential. Unnecessary acceptance of losses is common from chronic corrosion which is tolerated as established custom, and from hidden or indirect effects of corrosion. The importance of corrosion damage is not always proportional to the volume of metal affected. The functional aspects of corrosion are listed. Analysis is made of the ways in which corrosion enters into the cost of doing business. Explanations are given of the direct and indirect ways corrosion may effect capital investment, operating costs, product sales, maintenance costs, overhead costs and market competitive condition of and company.

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