Performance of a global congestion measure for CDMA networks
cdmp p级题库

cdmp p级题库The problem at hand is related to the CDMP P-level question bank. To address this issue, it is important to consider various perspectives and provide a comprehensive response.From an educational standpoint, having a well-designed and comprehensive question bank is crucial for the success of any certification program. The CDMP P-level question bank plays a significant role in assessing the knowledge and skills of individuals seeking certification in data management. It is essential that the question bank covers a wide range of topics, including data governance, data quality, data modeling, and data integration, among others. By ensuring a diverse and comprehensive set of questions, the question bank can effectively evaluate the proficiency of candidates in various areas of data management.Moreover, the quality of the question bank is of utmost importance. The questions should be carefully crafted totest not only the candidates' theoretical knowledge but also their practical understanding and application of concepts. Each question should be clear, concise, and unambiguous to avoid any confusion or misinterpretation. Furthermore, the question bank should be regularly updated to keep up with the evolving field of data management. This can include incorporating new technologies, industry best practices, and emerging trends in data management.In addition to the educational perspective, it is crucial to consider the perspective of the candidates. The CDMP P-level certification is a significant milestone for individuals in their data management careers. Therefore, the question bank should provide a fair and accurate representation of the knowledge and skills required at this level. Candidates should feel confident that the questions are relevant, challenging, and aligned with the expectations of the industry. This will ensure that the certification holds value and serves as a credible recognition of their expertise in data management.Furthermore, it is important to address the emotionalaspect of the problem. Candidates invest significant time, effort, and resources in preparing for the CDMP P-level certification. They may experience various emotions, such as anxiety, stress, and excitement, throughout the preparation process. The question bank should be designedin a way that supports candidates' emotional well-being and motivates them to succeed. This can be achieved by providing clear instructions, offering practice questions, and providing feedback on performance. Additionally, the question bank should be accessible and user-friendly, allowing candidates to navigate through the questions easily.From a practical standpoint, the CDMP P-level question bank should be easily accessible to candidates. It should be available in various formats, such as online platforms or downloadable resources, to cater to different learning preferences. The question bank should also be accompanied by detailed explanations and references to relevant study materials. This will enable candidates to understand the rationale behind the correct answers and further enhance their knowledge in specific areas. Moreover, the questionbank should include a sufficient number of questions to adequately assess the candidates' proficiency level.In conclusion, the CDMP P-level question bank plays a crucial role in evaluating the knowledge and skills of individuals seeking certification in data management. It is essential to ensure that the question bank is comprehensive, of high quality, and regularly updated. Additionally, it should be designed to support candidates' emotional well-being and provide a fair representation of the knowledgeand skills required at the P-level. By considering these perspectives and addressing the various aspects of the problem, the CDMP P-level question bank can effectively serve its purpose and contribute to the success of data management professionals.。
performance evaluation理工英语4

performance evaluation理工英语4 Performance EvaluationIntroductionPerformance evaluation is a crucial process in assessing the effectiveness and efficiency of individuals, teams, or organizations. It involves the systematic assessment and measurement of performance against predetermined goals, objectives, and standards. This article aims to explore the concept of performance evaluation, its significance in various contexts, and the different methods used for evaluation.Defining Performance EvaluationPerformance evaluation is defined as the systematic process of assessing and reviewing an individual's or organization's performance in relation to established goals and objectives. It involves analyzing the quality, quantity, and timeliness of work, as well as the overall contribution towards achieving desired outcomes.Significance of Performance EvaluationPerformance evaluation plays a critical role in various contexts, including:1. Employee Performance Evaluation: In organizations, performance evaluation helps assess employees' job performance, identify areas for improvement, and determine reward and promotion opportunities. It provides valuable feedback and helps create a performance-driven culture.2. Team Performance Evaluation: Evaluating team performance is essential for identifying strengths and weaknesses, enhancing collaboration, and optimizing resources. It enables organizations to allocate tasks effectively, promote teamwork, and achieve collective goals.3. Organizational Performance Evaluation: Assessing the overall performance of an organization is essential for strategic planning, decision-making, and performance improvement. It helps identify areas requiring attention and enables organizations to align their objectives with key performance indicators (KPIs).Methods of Performance EvaluationThere are several methods used for performance evaluation, depending on the nature and context of evaluation:1. Rating Scales: This method involves using predefined scales to rate employees' performance against specific criteria. It provides a structured approach and simplifies the evaluation process. However, it can be subjective and may not capture the full extent of performance.2. 360-Degree Feedback: This method involves obtaining feedback from multiple sources, including supervisors, subordinates, peers, and customers. It provides a holistic view of an individual's performance and promotes a comprehensive understanding of strengths and areas for improvement.3. Objective Measurements: Objective measurements involve quantifying performance based on quantifiable data, such as sales figures, production output, or customer satisfaction ratings. This method provides a precise assessment of performance but may not capture qualitative aspects.4. Self-Assessment: Self-assessment encourages individuals to reflect on their performance and identify areas for improvement. It promotes self-awareness, accountability, and personal development. However, it may be biased and influenced by individuals' perceptions.5. Behavioral Observation: This method involves directly observing individuals' behavior in specific work-related situations. It provides valuable insights into work habits, interpersonal skills, and adherence to organizational values. However, it can be time-consuming and may not capture performance in all areas.ConclusionPerformance evaluation is a vital process for assessing and improving individual, team, and organizational performance. It helps organizations align their objectives, motivate employees, and ensure efficient resource allocation. By using appropriate evaluation methods, organizations can drive continuous improvement and achieve long-term success. It is essential for organizations to establish clear evaluation criteria, provide constructive feedback, and support employee development to maximize the benefits of performance evaluation.。
performance evaluation理工英语4 -回复

performance evaluation理工英语4 -回复Performance evaluation is a crucial process for organizations to assess and measure the performance of their employees. It is a systematic and objective review of an individual's job performance, focusing on their accomplishments, strengths, areas of improvement, and goals for the future. In this article, we will explore the steps involved in conducting an effective performance evaluation.Step 1: Establishing clear performance expectationsThe first step in conducting a performance evaluation is to establish clear performance expectations for the employee. This involves setting clear goals and objectives that are specific, measurable, achievable, relevant, and time-bound (SMART). By establishing clear expectations, both the employee and the evaluator have a common understanding of what is expected and can work towards achieving those goals.Step 2: Collecting performance dataOnce the performance expectations are set, the next step is to collect data on the employee's performance. This can be done through various methods, such as self-assessment, supervisorfeedback, peer feedback, customer feedback, and objective performance metrics. Gathering data from multiple sources provides a comprehensive perspective on the employee's performance and reduces bias.Step 3: Conducting a performance review meetingAfter collecting the necessary data, the evaluator conducts a performance review meeting with the employee. This meeting provides an opportunity to discuss the employee's performance, strengths, areas for improvement, and future goals. It is important to approach the meeting with a constructive and non-biased mindset, focusing on providing feedback and guidance rather than criticism.Step 4: Providing constructive feedbackDuring the performance review meeting, the evaluator provides constructive feedback to the employee. This feedback should be specific, accurate, and focused on behavior and results rather than personal traits. The evaluator should highlight the employee's achievements and strengths, while also addressing areas where improvement is needed. It is essential to maintain a balanced approach, recognizing the employee's hard work while alsoencouraging growth and development.Step 5: Developing a performance improvement planIf there are areas for improvement identified during the performance review, it is important to develop a performance improvement plan. This plan outlines specific actions and steps the employee can take to improve their performance in the identified areas. The plan should be collaborative and mutually agreed upon, with clear objectives, timelines, and support mechanisms in place to help the employee succeed.Step 6: Monitoring and reviewing progressAfter the performance improvement plan is implemented, it is crucial to monitor and review the employee's progress regularly. This may involve periodic check-ins, coaching sessions, orfollow-up meetings to track the employee's improvement and provide ongoing support. Regular communication and feedback are essential to ensure that the employee stays on track towards achieving their goals and making necessary improvements.Step 7: Rewarding and recognizing good performanceFinally, it is important to recognize and reward good performance.Acknowledging and appreciating the employee's achievements and efforts boosts morale and motivation. Rewards and recognition can come in various forms, such as salary adjustments, bonuses, promotions, or simply verbal praise and public acknowledgment. This step helps create a positive work environment, encourages continued excellence, and reinforces the value of performance evaluation.In conclusion, conducting a performance evaluation involves several important steps, from establishing clear performance expectations to providing constructive feedback and implementing a performance improvement plan. It is a comprehensive and ongoing process that aims to assess, motivate, and develop employees, ultimately contributing to the overall success of the organization.。
GMAT作文题目翻译

所有作文题目的中文翻译Analysis of Issue Questions1. 有些国家里,电视和广播节目被仔细审查着不让出现带攻击性的语言和行为。
在另一些国家里,基本上没有审查制度。
在你的观点里,政府或其他任何团体应该在何种程度上审查电视或广播节目?解释,给出相关的原因and/or例子来支持你的观点。
2. “指望单个国家独立地作出必要的牺牲来保存能源是不现实的。
如果我们希望为下一代保护世界的能源资源,国际领导力量和全球性的公司是基本的。
”讨论你在何种程度上赞成或不赞成上述观点。
从你自身的经验,观察和阅读给出相关的原因and/or例子来支持你的观点。
3. “有限公司和其他商业机构应该尽力消除根据员工经验和技术划分员工的许多职称和工资等级。
一个扁平的组织结构更可能鼓励员工间的共同掌权和共同合作。
”讨论你在何种程度上赞成或不赞成上述观点。
从你自身的经验,观察和阅读给出相关的原因and/or例子来支持你的观点。
4. “权力的所有表现之中,对使用权力的克制是最令人影响深刻的。
”阐述你认为这段引语是什么意思,讨论你在何种程度上赞成或不赞成上述观点。
使用来自历史,时事或你自身经验,观察,阅读的原因and/or特定的例子来展开你的立场。
5. “所有的团体和组织都应该作为一个每个人都参与决定,分享责任和义务的团队来运作。
给予一个人关于一个项目和行动的集中的权威和责任不是完成工作的有效方式。
”讨论你在何种程度上赞成或不赞成上述观点。
从你自身的工作或学习经验,观察和阅读给出相关的原因and/or例子来支持你的观点。
6. “成功的定义只有一种:可以按你自己的方式过你的人生。
”讨论你在何种程度上赞成或不赞成上述观点。
从你自身的经验,观察和阅读给出相关的原因and/or例子来支持你的观点。
7. “最好的给别人提建议的方法是发现他们想要的东西然后告诉他们如何去得到。
”讨论你在何种程度上赞成或不赞成上述观点。
从你自身的经验,观察和阅读给出相关的原因and/or例子来支持你的观点。
世界强人力资源管理绩效管理培训教程中英文

第十二页,共八十八页。
12
Recommended Don’ts for Performance Discussions
● Stereotyping ● “Since one thing is bad, therefore everything is bad〞 ● Mirroring – just like me ● Salary discussions – leave for a separate time ● Do not promise what you can not deliver ● Saying “I think I can get you a promotion〞 is DANGEROUS!
Nov.-Jan.
Phase 3: Performance Appraisal
• Set Business Goals
• Set Dev. Goals
• Complete Appropriate Sections of Performance Form
•Review Progress Against Goals
● How have you developed personally over the year?
● What new competencies have you developed?
● What have you learned that can be applied in the future? ● What feedback have you received from others about your
Seek and receive performance feedback
Facilitate developing skills & capabilities Get work done ● Differentiate Performance
Measuring the CHP performance of a PEMFC

Identifying and quantifying energy savings on fired plant using low cost modelling techniquesRobert Tucker a ,⇑,John Ward ba Zerontec Energy Consultancy,Stratford-upon-Avon CV376PQ,United KingdombFaculty of Advanced Technology,University of Glamorgan,Pontypridd CF371DL,United Kingdoma r t i c l e i n f o Article history:Received 21July 2010Received in revised form 17September 2010Accepted 27January 2011Available online xxxx Keywords:Heat transfer Modelling Radiation Combustion Furnacesa b s t r a c tCombustion in fired heaters,boilers and furnaces often accounts for the major energy consumption on industrial processes.Small improvements in efficiency can result in large reductions in energy consump-tion,CO 2emissions,and operating costs.This paper will describe some useful low cost modelling tech-niques based on the zone method to help identify energy saving opportunities on high temperature fuel-fired process plant.The zone method has for many decades,been successfully applied to small batch furnaces through to large steel-reheating furnaces,glass tanks,boilers and fired heaters on petrochemical plant.Zone models can simulate both steady-state furnace operation and more complex transient operation typical of a pro-duction environment.These models can be used to predict thermal efficiency and performance,and more importantly,to assist in identifying and predicting energy saving opportunities from such measures as: Improving air/fuel ratio and temperature controls. Improved insulation.Use of oxygen or oxygen enrichment. Air preheating via flue gas heat recovery.Modification to furnace geometry and hearth loading.There is also increasing interest in the application of refractory coatings for increasing surface radia-tion in fired plant.All of the techniques can yield savings ranging from a few percent upwards and can deliver rapid financial payback,but their evaluation often requires robust and reliable models in order to increase confidence in making financial investment decisions.This paper gives examples of how low cost modelling techniques can be applied to improve confidence in implementing energy efficiency improvements whilst safeguarding manufacturing output and quality.Ó2011Elsevier Ltd.All rights reserved.1.IntroductionModelling is applied in many fields ranging from climate and weather forecasting to predicting the performance of the stock market.In the field of energy conservation on industrial processes,modelling can provide reliable assessments of the losses and the potential for improved efficiency and performance.Unfortunately,the benefits afforded by modelling are often ignored on the basis that models are too expensive or complex to apply,and that it is often simpler and quicker to rely on engineering experience and simple ‘‘rules-of-thumb’’.For example,application of large compu-tational fluid dynamic programmes can involve prohibitively large expense in expertise and computing resources.However,simpler mathematical models can provide an alternative approach,which can be equally powerful when evaluating a number of alternative options for improving plant performance.Rhine and Tucker [1],Mullinger and Jenkins [2]and Baukal and Schwartz [3]all describe techniques for mathematical modelling of industrial combustion plant.Many of the techniques described are based on the zone method first originally developed by Hottel and Sarofim [4].The energy efficiency of high temperature plant can have a ma-jor impact on the unit cost of production.Often the fuel burnt in a furnace or fired heater accounts for the major source of energy consumption within a manufacturing process.Measures such as flue stack heat recovery and improvements to the insulation and controls,have to be carefully applied to ensure that product quality and productivity are not adversely affected.The potential risk to production is often used as a reason for not investing in improved energy saving measures.This paper gives examples of how low cost modelling techniques can be applied to improve confi-dence in implementing energy efficiency improvements,whilst0306-2619/$-see front matter Ó2011Elsevier Ltd.All rights reserved.doi:10.1016/j.apenergy.2011.01.061Corresponding author.Tel./fax:+44(0)1789298659.E-mail address:robertjtucker@ (R.Tucker).safeguarding manufacturing output and quality.A general descrip-tion of the zone modelling technique willfirst be described.This will then be followed by description of its application to examples of industrial furnaces andfired heaters.2.Background to the zone methodTo improve thermal efficiency,a furnace should be designed to ensure maximum heat is transferred to the load surface and that the heat losses through the walls and in the gases leaving the process are minimised.Thermal radiation is usually the dominant mode of heat transfer in high temperature industrial combustion equipment.Radiation is emitted from the hot com-bustion products on account of the CO2and H2O in the combus-tion products,and this radiation is transmitted,reflected and absorbed within the furnace chamber.The complex interchange of radiation in a furnace can be modelled using the zone method.In the zone method,the radiating enclosure is subdivided into a number of isothermal surface and volume elements(zones).A total energy balance is formulated around each surface or volume zone (i)which includes terms for:radiation leaving i,radiation arriving at i from all other zones j in the enclosure, enthalpyflow in and out of volume zone i due toflow of the combustion products,heat release due to combustion in volume zone i,convection to and from contiguous surface and volume zones.The radiation interchange is written in terms of radiation ex-change factors.The net radiationflux between any two zones is proportional to these factors and to the absolute temperatures to the fourth power.The factors are a function of the geometric orien-tation and radiative properties(emissivities)of the zones.The radi-ation from the hot combustion products is a function of their emissivity.These gases are not grey and include spectrally absorb-ing(and emitting)bands interspersed with clear non-participating bands or‘windows’in the spectrum.In the zone models described in this paper,the gases are represented by the weighted-sum-of-grey-gases modelfirst introduced by Hottel and Sarofim[4].In its simplest form,a single gas zone can be used to represent the furnace chamber.This is often referred to as the single well-stir-red zone(WSZ)model.The radiation interchange factors between a single gas zone and a load and a wall surface can be derived from simple algebraic expressions.This simple model,involves only three temperatures(combustion products,wall and load surface) and can provide a very powerful technique for evaluating energy savings.If there is a significant temperature gradient through the fur-nace,such as within a continuous steel-reheating furnace,then a long furnace(LF)model can be applied.This entails a series of linked well-stirred zones with for example a wall surface and a load sur-face surrounding each gas zone.A typical configuration of a long furnace model is shown in Fig.1.The long furnace model simulates the temperature profile of the load as it moves through the furnace in counter-currentflow to the hot combustion products.Such models are able to predict:The specific fuel consumption.Theflue gas temperature and losses.The heat losses to the refractory walls and hearth.The internal and surface load temperatures at discharge and during the heating process.The internal wall temperatures.Both the WSZ and LF models can provide a complete heat bal-ance on a furnace,which is often the crucialfirst step in identifying opportunities for fuel saving.In larger furnaces there may be con-siderable variations in temperature across the length,width and height of the system and in these situations multi-zone two and three-dimensional zone models may be appropriate as described by Correia et al.[5].Some simple examples of applications will now be described starting with the WSZ model,followed by the LF model applied to both steady-state and transient furnace applications.3.Application of the WSZ modelThe single well-stirred gas zone model provides a valuablefirst step to evaluate energy saving options on fuel-fired furnaces and heaters.A version has been developed in Visual Basic,which re-quires negligible computing resources.The model only requires the wall and load surface areas and the chamber volume to be specified.The radiation interchange between the gases and load plus any convective heat transfer is calculated,and the fuel input rate is derived which satisfies the following energy balance equa-tion on the furnace:Heat in fuelþHeat in air¼Heat to loadþHeat loss in flue gasesþHeat loss through walls3.1.A small continuous furnacePredictions for a natural gas furnace of hearth area5Â5m and height2m were prepared.The base case assumed an excess air level of25%with an exhaust gas temperature of1250°C,and a load surface temperature of900°C.The model predicts a ther-mal efficiency of29.6%net.This may be representative of a stea-dy-state metal heat treatment or metal melting application.The WSZ model was applied to evaluate a number of energy saving opportunities.The results are shown in Table1.The priority should be to reduce the excess air level,if this can be done without detriment to the safe operation of the plant,emis-sions or to product quality.Controlling excess air may be achieved though better burner air–fuel ratio control,or by preventing air in-gress into the furnace by pressure control and sealing of gaps and doors.The fuel saving achieved,then reduces the cost of subse-quent measures.For example if recuperation is applied,the size and installed cost of the equipment is reduced because smaller heat exchangers can be used.On high temperature plant,whereflue losses are significant, oxygen enrichment or oxy-gasfiring can achieve substantial sav-ings.The cost savings in reduced fuel consumption has to be greater than the cost of supplying the oxygen.Hence,it is important to minimise fuel consumption before applying oxygen. In this example,oxygen has been supplied at a rate that gives the sameflue gas oxygen concentration(1.1%).The level has to be set to ensure safe operation of the plant.In the oxy/gas case above,a total of0.049kg/s of natural gas is saved by supplying 0.177kg/s oxygen.To break even,the cost/kg of oxygen must be less than27%of the cost/kg of natural gas.The same break even cost ratio applies for the oxygen enriched combustion case.In the case of reducing excess air or applying oxygen,the pre-dictedflue gas temperature is reduced because the radiant emis-sivity of the gases is improved(owing to the high concentrations of CO2and H2O).2R.Tucker,J.Ward/Applied Energy xxx(2011)xxx–xxx3.2.Afired heaterFired heaters account for the major energy consumption and carbon emissions on refineries and petrochemical plant.They usu-ally comprise a high temperature radiant box in which combustion occurs.The hot gases radiate to a series of tubes containing high-pressure hydrocarbonfluids.On most largefired heaters,the hot flue gases leaving the radiant section are passed across a convec-tive tube bank to further heat the hydrocarbonfluids.On modern plant the heat in theflue gases may then be further recovered to preheat the combustion air or to generate steam.Safety is critical in these applications because of the serious consequences in the event of a release of high-pressure feedstock. The temperature at the top of the radiant section is often referred to as the bridge wall temperature(BWT).During operation,this must be maintained below a certain value to avoid overheating and potential failure of the tubes.A schematic of a typicalfired heater with convective tube bank and air preheater is shown in Fig.2.Over the last three decades,there has been a considerable inter-est in the application of coatings on the refractory walls of fuel-fired furnaces for energy savings.It is claimed that these special coatings raise the emissivity of the surface and improve the radia-tive heat transfer and hence the thermal efficiency of the process. Products under various brand names are commercially available and can be applied by trowel or spray gun to the surface of hard face refractory or ceramicfibre walls.However,energy savings claims resulting from these products are often difficult to verify because of the variable nature of plant operation.It has also been difficult to forecast the savings on different applications be-cause most thermal design models for heat transfer in furnaces fail to show any influence of wall emissivity.This is due to the limita-tions of most models rather than the capability of the coating products.Docherty and Tucker[6]and Elliston et al.[7]independently showed that if the combustion products are assumed to be grey, then changing the wall emissivity in an enclosed furnace,has no effect on overall predicted heat transfer.This is because in general, for an adiabatic wall,these simple models do not distinguish be-tween radiation that is absorbed and re-radiated,and radiation that is reflected at the wall surface.By introducing a non-grey gas to represent more realistically the combustion products in the furnace,both authors identified improvements when emissiv-ity was raised.The radiation model used in the zone method uses a non-grey gas combustion model(the weighted-sum-of-grey-gas model)and is therefore able to predict the increase in radiant heat transfer with surface emissivity.A WSZ model has been applied to simulate the heat transfer enhancement in the radiant section of a typicalfired heater.The heater parameters are:Fig.1.A long furnace model representation of a small-scale steel-reheating furnace.Table1Prediction of fuel saving opportunities on a small continuous furnace.Flue gas O2%dry O2conc.v/v%Air preheat,T(°C)Exhaust gas,T(°C)Fuel input kW net Efficiency(%net)Fuel saving(%)Base case a 4.621151*********.6_ Reduced xsa b 1.121151243457839.124.3 Recuperator b 1.1213831243342752.343.3 Regenerator b 1.1218751243251271.458.5 Oxy-enriched 1.125151236372948.138.4 Oxy/gas 1.195151216222480.763.2a Excess air=25%.b Excess air reduced to5%.Fuel type Natural gas Excess air20%Thermal input 6907kW net Tube area110m 2Exposed wall area 152m 2section load 3187Convection section load 3098gas temperature downstream of the convection and flue losses represent just 7.1%of the net emissivity in the model wasthen changed simulate application of a high emissivity coating.shown in Table 2.In Case 1,the total process and the model predicts the fuel saving.A negligible predicted.This is because the heater is already net thermal efficiency,and so there is little available to extract from the combustion products.model is able to predict a potential increase in version of the LF model can be very useful since most furnaces operate under non-steady-state conditions with variable through-put,changes in load size and scheduled and unscheduled breaks in production.In these models,which are described in detail by Rhine and Tucker [1],the transient conduction into both the steel billets and the refractory hearth and walls are calculated.The approach has been validated against operating data from a Fig.2.A schematic arrangement of a typical fired heater.Fig. 3.Predicted and measured energy consumption on a continuous steel-reheating furnace.4.1.A small forging furnaceFig.4is an example of a small forging furnace used to reheat 150mm diameter steel bars to1150°C.There are many similar furnaces used in industry for reheating steel and non-ferrous met-als for rolling,forging or heat treatment applications.This study is based on a small furnace in Belarus.The original specification is de-tailed in Table3.Since this furnace is used in a semi-continuous manner,with repeated cold starts every day,a transient long fur-nace model was applied[1].This model simulates the start-up of the furnace from cold.Under such conditions the heat stored in the refractory walls can represent a significant energy loss.The furnace was represented by an11-zone LF model with zones of length0.36m.A time step of5s was applied to simulate the operation from cold.After150min,production is simulated with billets leaving from the hot zone1and cold billets entering zone11.The thermal input is modulated to simulate temperature control to maintain furnace roof temperature in zone1.To main-tain desired output,a roof set point temperature of1220°C was required.Six simulations were carried out as follows:(1)A base case simulation according to the current furnace.Unfortunately,there was no metered data so it was not pos-sible to establish the reliability of the predictions.(2)Simulation with the walls and roof replaced with light-weight ceramicfibre.(3)Repeat of Case1with an improvedflue gas recuperator(heatrecovery effectiveness increased to50%).(4)Repeat of Case2with improvedflue gas recuperator.(5)Base case but with a single recuperative burner installed athot end(replacing all existing burners).Flue gas pull back to recuperator=60%and40%of combustion products go onto the existingflue.As can be seen from these predictions,the largest single fuel saving($15%)is achieved by installing an improvedflue stack recuperator(Case3).Replacing the walls with ceramicfibre gives a fuel saving of around11%.Combining these options(Case4)gives a saving of$23%.The preferred optionfinancially is dependent on the cost of installation.However,the model provides reliable pre-diction of the running cost savings,which can be used to derive the financial payback of each option.The model has also shown that in this application,installing a recuperative burner,although giving a12.5%fuel saving,may lead to excessive temperature differences in the billets,which may seri-ously reduce forging quality.This results from the change in heat flux profile along the hearth.Also,the furnace throughput is re-duced.This demonstrates how a model can help avoid bad invest-ment decisions.4.2.Application of heat recovery on a steel-reheating furnaceThe above application demonstrated how a recuperative burner could lead to poor performance.There are many applications where recuperative and regenerative burners can yield very signif-icant performance benefiing a steady-state LF model,a simple study was carried out to compare different options forflue gas heat recovery on a continuous natural-gasfired steel-reheating furnace, against performance with no heat recovery.These options were: Use of aflue stack recuperator(40%effective).Use of regenerative burners with an effectiveness of70%.The furnace is18.6m in length and heats steel bars of thickness 88mm to1100°C with a throughput of70Te/h.The furnace was modelled using a10-zone LF model.Burners are distributed along the length of the furnace in order to ensure that the steel is ade-quately‘soaked’before discharge.The originalfiring profile as shown in thefirst row in Table5was applied in the model and this predicted a steel temperature distribution through the furnace as shown in Fig.5resulting in a(top to bottom)temperature differ-ence in the steel at discharge of56°C.The model was then applied to predict the performance benefits of the different heat recovery options.In the regenerative burner case,80%of theflue gases are pulled back into the burner to preheat the air.The remaining 20%of products travel to the mainflue stack.Thefiring profile and burner locations had to be adjusted as shown in Table5toFig.4.A schematic of the small forge furnace.Table3Specification of the small forging furnace.Load details Size15mm diaÂ280mm lengthWeight38.6kgMaterial Carbon steelOutput temperature1150°CNo.of billets infurnace22(850kg)Throughput1000kg/hFurnace construction Length 4.1mWidth093mHearth Dense refractory brick2600kg/m3Walls and roof Insulatingfirebrick860kg/m3 Burner Number3Total max thermalinput54m3(s)/hExcess air5%Air preheat285°CProduction schedule 2.5h to start of forging16h production Table4Predicted results for the forge furnace.Case Condition OverallSFC(GJ/Te net)Saving(%)Steady-state SFCGJ/Te netT b(°C)D T(°C)kg/heff%net(%) 1Base case 1.728– 1.3911547098253.75 2CF walls 1.53910.94 1.2911517198357.89 3Recup50% 1.46715.10 1.1911567198262.71 4CFwalls+recup50%1.3322.92 1.191154739S262.715Recuperativeburner1.5112.50 1.29115115083657.89ensure that billet temperature difference at discharge was not ad-versely affected.The predicted efficiencies and steel temperature differences are given in Table 6.This final choice depends on the installed cost of an end recu-perator compared to installing regenerative burners.5.ConclusionsThis paper has shown how low cost mathematical models based on the zone method for computation of radiation exchange in enclosures can be applied to evaluate fuel saving opportunities on a range of high temperature plant.In many applications there are often several opportunities that could be applied.It is impor-tant to identify low cost,fast pay-back options that should be given priority.These can then reduce the cost of more expensive solu-tions.This is demonstrated on a simple furnace where reducing the excess air is given priority.This then reduces the cost of more expensive measures such as flue gas heat recovery or application of oxygen to the combustion process.In certain situations,fuel saving measures may lead to unex-pected reduction in throughput or product quality.When heating thick material such as steel billets or slabs,any impact on the heat flux profile and temperature distribution in the steel has to be carefully evaluated before investment is made.Steady-state anddimensional problems.A 3-dimensional zone model has recently been applied to simulate different low NO x firing strategies on a glass-melting furnace [9].Data on the complex flow and combus-tion fields were provided by computational fluid dynamic simula-tions and by the use of physical models –in this case using the acid-alkali technique to simulate fuel/air mixing.References[1]Rhine JM,Tucker RJ.Modelling of gas-fired furnaces and boilers.McGraw-Hill;1990.[2]Mullinger P,Jenkins B.Industrial and process furnaces.Elsevier;2008.[3]Baukal CE,Schwartz R.The John Zink combustion handbook.CRC Press;2001.[4]Hottel HC,Sarofim AF.Radiative transfer.McGraw Hill;1967.[5]Correia SAC,Ward J,Sousa JLVA.Numerical prediction of the transient operationof a gas-fired reheating furnace.In:Proc ASME heat transfer division,HTD,vol 367;2000.p.87–94.[6]Docherty P,Tucker RJ.The influence of wall emissivity on furnace performance.J Inst Energy 1985;59:35–7.[7]Elliston DG,Gray WA,Hibberd DF,Ho T-Y,Williams A.The effects of surfaceemissivity on furnace performance.J Inst Energy 1987;60:155–67.[8]Ward J,Tan CK,Tucker RJ.Development of a spectral radiation model to predictthe transient performance of a metal reheating furnace.Proc ASME Int Mech Eng Cong 2009.[9]Fricker N et al.A multimode modelling approach for NO x reduction on gas-firedglass melters through flame/furnace matching.In:Proc 16th IFRF members conference,–combustion and sustainability:new technologies,new fuels,new challenges.Boston (USA);June 2009.p.13.Table 56R.Tucker,J.Ward /Applied Energy xxx (2011)xxx–xxx。
国际物流学知到章节答案智慧树2023年山东财经大学

国际物流学知到章节测试答案智慧树2023年最新山东财经大学第一章测试1.Internationalization and globalization give birth to the development ofinternational trade.()参考答案:对2.Supply Chain Management integrates supply and demand managementwithin and across companies. ()参考答案:对3.Which of the following belongs to non-trade logistics? ()参考答案:international postal logistics;international logistics of foreign aid project;international exhibition logistics;international ammunition logistics4.In international logistics, transport facilities, storage facilities and otherinfrastructures need standardized. ()参考答案:对5.国际物流系统的主要参与者包括哪些?()参考答案:customs;international freight agent;Consignor;Consignee;carrier第二章测试1.采购是指为保障企业物资供应而对企业的整个采购活动进行的计划、组织、指挥、协调和控制活动。
( )参考答案:错2.What are the differences between international procurement and domesticprocurement?()参考答案:Different cost involved.;Different ways of payment;;Different customers and different ways of communication;;Different procedures of shipping and transport mode;3.Seeking access to talented human resources, and process and producttechnologies belongs to Skill & knowledge strategy. ()参考答案:对4.下面哪些因素是做离岸运作选址时考虑的因素?()参考答案:Quality of infrastructure;Logistics;Risk profile;Factor cost;Market potential5.Offer and Acceptance are the necessary procedures in business negotiation.()参考答案:对第三章测试1.国际贸易的增长可以归因于多个因素,包括()。
高二英语全球安全意识广阔视野单选题40题

高二英语全球安全意识广阔视野单选题40题1. The ______ of global warming on food security is a major concern.A. impactB. effectC. influenceD. result答案:A。
本题考查名词辨析。
“impact”强调强烈的冲击和影响;“effect”侧重于结果、效果;“influence”多指潜移默化的影响;“result”是结果。
全球变暖对粮食安全的强烈影响,用“impact”更恰当。
2. We need to take ______ measures to protect the environment from further damage.A. effectiveB. efficientC. affectiveD. effectual答案:A。
“effective”表示能产生预期效果的;“efficient”侧重效率高;“affective”指情感方面的;“effectual”有效的,但不如“effective”常用。
保护环境采取能产生效果的措施,用“effective”。
3. The international community is making ______ efforts to address the issue of global terrorism.A. considerableB. considerateC. regardedD. regarding答案:A。
“considerable”大量的、相当多的;“considerate”体贴的;“regarded”被认为;“regarding”关于。
国际社会为解决全球恐怖主义问题付出大量努力,用“considerable”。
4. The ______ of natural disasters has increased in recent years due to climate change.A. frequencyB. frequentC. frequentlyD. infrequency答案:A。
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Performance of a Global Congestion Measure for CDMA NetworksLachlan L.H.Andrew and Stephen V.HanlyElectrical and Electronic EngineeringUniversity of Melbourne,Parkville,Vic3052,AUSTRALIAPh+61393449208Fax+61393449188L.Andrew,S.Hanly@ee.mu.oz.auAbstract—A recently proposed global congestion measure for CDMA networks is applied to call ad-mission control,call dropping,and band allocation in multi-carrier CDMA networks.It is shown to perform comparably with existing techniques for call dropping, and better than existing techniques for admission con-trol and band allocation.Difficulties arising in the measurement of this parameter are also investigated.I.I NTRODUCTIONEffective management of any communications system requires an accurate real-time measure of how“congested”the system is.In a simple cir-cuit switched network,the congestion is easily mea-sured by counting the number of available circuits on each link.In packet switched networks,it can be assessed by measuring the queue sizes at all of the nodes.Code division multiple access(CDMA)net-works,with their soft capacity,require a new concept of capacity.In[1],a global congestion measure for CDMA networks was proposed,based on the dom-inant eigenvalue,,of a matrix determined by the path gains of the mobile stations to the base stations. This measure was shown to have useful mathemati-cal properties,such as being below a threshold if and only if the system is“feasible”,and always increas-ing when a new user is added.However,no empiri-cal evidence was presented that it can be successfully used for network management tasks.In this paper, we demonstrate that using in strategies for call ad-mission control and for band allocation in multiband CDMA systems can provide better performance than traditional local congestion measures.The congestion measure will be defined formally in Section II,and Section III investigates the correla-tion between outage events and being high.Sec-tions IV to VI determine how effective is in deter-mining which calls to drop or accept,and in which This work was funded in part by the Australian Research Council(ARC).band of a multiband system new calls should beplaced.Finally Section VII considers how can bemeasured in a real system without eigenvalue calcu-lations.II.M EASURING CONGESTION—This paper will examine the congestion of a sys-tem working with an optimal power control schemeproposed in[2].Under this power control algorithm,users iteratively update their transmit powers to thelevel which would give them exactly their desiredsignal to interference ratio(SIR)if the interferenceremained the same as at the previous iteration.Thatis,,where is the power trans-mitted by user at iteration,is the effectiveinterference(after despreading)at the base station towhich user is connected at iteration,and is theSIR requirement of user.It was shown in[2]that the rate of convergenceof this algorithm is governed by the dominant eigen-value of the matrix,given bywhere is the SIR required by user,is the pro-cessing gain,is the base station to which user isconnected,and is the path gain from user to base station.If,the Perron-Frobenius eigen-value of,is less than1,the algorithm converges.If,then no allocation of powers to users canachieve all of the users’SIR requirements.It wasconjectured in[3]that may be a useful measure ofcongestion.For a given network state,it can easily bemeasured in a decentralised manner by observing therate of convergence of the power control algorithm.It also provides a measure of the global congestion,rather than the specific congestion of a single cell.00.20.40.60.811.20102030405060rtime (call holding times)outagerFig.1.and system-wide outages (divided by 8)vs time.0.10.20.30.40.50.60.70.80.9105101520253035rtime (call holding times)128512Fig.2.vs time for small (processing gain 128)and large(512)system.III.VARIATION OFA new measure of congestion should be corre-lated with existing measures.Figure 1shows the changes in over time,and also periods of high out-age.Clearly outage is higher when is high.How-ever can be measured by any base station,whereas outage can only be measured at the connected base stations.Detecting congestion before users go into outage is important for good network management.In particular,techniques such as handoff and admis-sion control,which work to prevent outage,should be triggered before outage occurs to maintain suffi-cient quality of service.Figure 1indicates that can be useful in predicting outage events.Figure 2,showing for systems with spreading gain 128and 512,shows that fluctuations in de-crease for “larger”systems.IV.D ROPPINGWhen a CDMA system is overloaded,some or all calls will be unable to attain their required signal to interference ratio (SIR)and go into outage.In order to ensure sufficient quality of service for the major-ity of users,some users must be dropped.The sim-ple scheme of dropping users when they have been in outage for longer than a threshold time has proved to be quite effective.However it may not be optimal.If the aim of dropping users is to drop the fewest users required to make the system feasible,this can be achieved by dropping the users which have the great-est impact on ,which need not be those currently in outage.To determine the effectiveness of as a congestion measure,three dropping strategies weretested by simulation.In all cases,atoroidal hexagonal grid of base stations was used,and there was no admission ers did not move,but mobility was simulated by recalculating the shadow-ing occasionally.When outage occurs (i.e.,the SIR drops below 6dB),the first strategy simply drops all of the users currently in outage.The second strat-egy drops a randomly selected user which is cur-rently in outage.The third drops the user which makes the largest contribution to .Figure 3clearly shows that the most aggressive strategy,which drops all users currently in outage,performs substantially worse than the either scheme which drops one user at a time,but that there is little difference between the other two schemes.This shows that correctly iden-tifies users which are contributing to the poor per-formance of the system.These results also highlight the importance of a conservative dropping algorithm.When a strong interferer connects to a neighbouring cell,several users may go into outage.Typically all of these are dropped simultaneously (say after a con-stant timeout).However if one user is dropped and the power control is allowed to stabilise,the reduc-tion in transmit power of all of the other users may be sufficient for the other users to return from outage.This could be achieved in practice by using a random timeout for dropping.The drawback of this strategy is that it is difficult to assess the impact of a single user on .The most obvious method is tentatively dropping the user,and measuring the change in rate of convergence of the power control algorithm.Not only is this very time-consuming,but each user will briefly go into outage while its impact is being measured,even if only a sin-gle user is initially in outage.However,these results support as a measure of network congestion,which can in principle be used for network management.Investigation is continuing into whether users which contribute highly to can be characterised by more measurable parameters (like relative position or sig-nal strength)which may be able to be used for prac-tical dropping algorithms.0.0010.010.11101414.51515.51616.517d r o p p i n g (%)load (erlangs)all in outage one in outage congestion basedFig.3.Dropping probability vs.arrival rate for outage-based and congestion-based dropping.V.A DMISSION C ONTROLWhen a system is becoming congestion,it is bet-ter to block incoming calls than to allow new users to connect to the system and cause existing users to re-ceive inadequate service.This is commonly done by simply limiting the number of users who may con-nect to each base station,which entirely ignores the (often substantial)impact of other-cell interference.A more sophisticated approach considers the inter-ference from neighbouring cells and blocks new calls when the total received interference at the target base station is excessive These methods are compared in [4].A further enhancement would be to consider the interference caused to neighbouring cells.For example,new calls could also be blocked when the interference at neighbouring base stations would be-come excessive if the new call were accepted.How-ever this requires communication between the base stations,and it is not clear how many tiers of neigh-bours should be consulted.An alternative approach would be to use to determine whether or not a call should be admitted.Because is a global measure of congestion,ad-mission should not be based simply on the current value of .This would cause congestion in one part of the network to prohibit access in a very distant,lightly loaded part.Instead,admission should be based on the impact of the new user,that is,the change in .This can be measured in terms of the “spare capacity”,defined as .A maximum limit can be place on the allowable proportional decreasein spare capacity,.It is not clear that this is the optimal criterion,but it is nonetheless effective.The effectiveness of an admission control scheme is best measured by considering how well it can0.10.20.30.40.50.60.70.80.911.100.51 1.52 2.53o u t a g e (%)Blocking probabilty (%)SIRchange in rFig.4.Outage vs.blocking for -based admission con-trol,and conventional SIR-based admission control.trade blocking for outage,the aim being to min-imise the blocking for a given outage rate.Fig-ure 4shows the tradeoff possible with the pro-posed scheme for a load of 17Erlangs.The acceptance criterion was thatfor,.There is a lowerlimit to the blocking performance of this approach,because it will never allow a call into the system if that makes the system infeasible,but analogous schemes could be developed to consider the case al-lowing negative spare capacity.For comparison Figure 4also shows the results of blocking based on the interference measured at the target base station.The proposed algorithm based on the reduction in spare capacity outperforms the algo-rithm based solely on the SIR of the target base sta-tion over a wide range of operating conditions,most notably for lower blocking probabilities.Note how-ever that blocking based on local measurements can allow the entire system to become infeasible occa-sionally,which can reduce the blocking arbitrarily much,at the expense of increased outage.While the improvement in performance offered by the proposed approach may not in practice justify the extra compu-tational complexity,these results show that the pro-posed scheme can be used as a benchmark against which other less optimal admission algorithms can be compared.VI.B ANDALLOCATIONIn some CDMA systems,multiple non-interfering bands are used to increase capacity [5,6].The per-formance of such systems depends on how new users are allocated to bands.This is typically done by allo-cating new users to the band with the fewest current users in the cell of interest (“least load”)[6].An ob-0.010.11101515.51616.51717.518o u t a g e (%)traffic intensity (Erlangs)least load lowest r least impactFig.5.Outage probabilities using least load,lowest ,and least impact strategies.vious extension is to allocate users to the least con-gested band (with the smallest ).A better strategy is to allocate users to the band where they contribute least to the congestion.The user can be added to the band in which it causes the smallest proportional decrease in spare capacity.Figure 5shows the total outage probability when calls were allocated using the least load,lowest ,and decrease in spare capac-ity strategies.Clearly the latter approach is ing directly for band selection is more feasible than for dropping.The network only needs to try the new user in each of the bands,of which there are typically less than ten,rather than disrupt all users in the network,of which there may be thousands.VII.M EASUREMENTISSUESThis section will investigate the feasibility of mea-suring from changes in the received power level.This will be done by considering the dynamics ofthe system,which converges to the feasible power allocation (if one exists).Hereis the vector of powers received at each base station,and is a matrix whose eigenvalues are the same as those of [1].The total power at a given base station in such a system has the solution.Letfor some constants and .For sufficiently large (i.e.,once the lower order terms have died out),and ignoring the effect of measurement errors,can be determined from(1)The main sources of error are the term,thermal noise,nonlinearity of the measuring device,fast fading,voice activity and quantisation of the power control.Because measurements are being made almost at equilibrium,the changes in received power will be small,and quantisation of the power control signals will be particularly important.Two important issues arise here.The sampling instants (governed by and )must be deter-mined,and the accuracy with which the measure-ments should be made must be determined.Each of these involves a tradeoff.If is made too small,the terms due to non-dominant eigenvalues will be significant.However,if is too large,the system will almost have converged before the measurements are taken,and the changes will be small compared to the measurement errors.Furthermore,the larger is,the longer the measurement process takes.If is too small then the factorin the relative error becomes large,but if is toolarge the same problems occur as fortoo large.Clearly if the accuracy with which the measurements are taken is too low,the resulting estimate of will be bad.However increasing the accuracy requires increasing the averaging period to reduce the quanti-sation noise,which places a lower bound on .More-over this may actually decrease the accuracy because the ideal received power will change over the averag-ing period.Of these problems,the most fundamental is the impact of the decaying term caused by the non-dominant eigenvalues.Even in the absence of measurement errors,this can cause the estimateto be anywhere in the range by caus-ing the difference (or )to be ap-proximately zero,and possibly of the wrong sign.This is illustrated in Figure 6,which shows a phaseportrait of the system,,which is a possible trajec-tory for the total received powers at each base station of a two-cell system.If measurements are taken atpointsand then either the numerator or de-nominator ofcould be zero.However,for purposes such as admission control,the measurements will only be made by the base sta-tion,,to which the new mobile is connected.It is to be expected that the largest change in received power will occur at base station ,and hence the chance of00.20.40.60.811.21.400.10.20.30.40.5B a s e s t a t i o n 2Base station 1P0P1Fig.6.Possible phase portrait of received powers at basestations of a two-cell system.the received power at this base station “overshoot-ing”is low.(That is,it is expected that,if the received power vector is resolved into the eigenvectors,com-ponent of each of these resolved vectors will have the same sign.)This would mean that and (and and )are clearly distinct,and the above problem would not occur.To test this intuition,a simulation was performed with no admission control,and the impact of the call arrivals was measured.Propagation conditions were assumed to be constant and the load was 17Erlangs.For every arriving call,the change in the total (equilibrium)received power at each base sta-tion,,was recorded,along with the matrix de-scribing the system with the new call and the num-ber of the base station,,to which the new call ar-rived.Then was decomposed as whereare the eigenvectors of and are co-efficients.If the eigenvalues,,of are dis-tinct,the solution of the linearised system is then,with derivative.Assuming that no softhandoff occurs,a sufficient condition for the th com-ponent of to be monotonic for time is that,whereand is the th component of .How-ever,for the measurement to be meaningful,it is nec-essary for the dominant term to be an order of mag-nitude larger than the sum of the other terms.Theproportion of call arrivals for which is mono-tonic after time and the proportion for which the dominant term is an order of magnitude larger than the others after time are both shown in Figure 7.If the update interval is assumed to be 1.25ms,as in the IS-95standard,then acceptable accuracy is generally achieved after 60ms.This is faster than the timescale at which other factors cause the power0.20.40.60.81010203040506070p r o p o r t i o n o f c a l l sPower control iterationsmonotonic dominantFig.7.Proportions of calls such that is monotonicand after which the dominant term is clearly dominant after time .level to change,such as shadowing or the admission of new calls in neighbouring cells.(In a large,multi-cellular system,the arrival of a call in any cell has a slight impact on the power control,but new calls in distant cells can generally be ignored.Quantifying their effect is a future research topic.)VIII.C ONCLUSIONThis paper has investigated the effectiveness of a simple global congestion measure for CDMA net-works.It has been shown that the measure agrees well with existing measures of congestion,and can be used for admission control or band allocation in a multi-band system.It can in principle also be used to guide dropping of excess calls.The strengths of the global congestion measure are that it can be mea-sured at any point in the network and that it can pre-dict congestion before problems occur.R EFERENCES[1]S.V .Hanly,“Congestion measures in DS-CDMA net-works,”IEEE mun.,vol.47,pp.426–437,Mar.1999.[2]S.V .Hanly,Information Capacity of Radio Networks .PhD thesis,King’s College,Cambridge University,http://www.ee.mu.oz.au/staff/hanly/publications.html ,1993.[3]S.V .Hanly,“An algorithm for combined cell-site selectionand power control to maximize cellular spread spectrum ca-pacity,”IEEE J.Select.Areas Commun.,vol.13,pp.1332–1340,Sept.1995.[4]Y .Ishikawa and N.Umeda,“Capacity design and perfor-mance of call admission control in cellular CDMA systems,”IEEE J.Select.Areas Commun.,vol.15,pp.1627–1635,Oct.1997.[5]L.L.H.Andrew,“Measurement-based band allocation inmultiband CDMA,”in com ’99,(New York),1999,pp.1536–1543.[6]T.Dean,P.Fleming,and A.Stolyar,“Estimates of multi-carrier CDMA system capacity,”in Proc.Winter Sim.Conf.,(Washington,DC),1998,pp.1615–1622.。