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標(biāo)題: Titlebook: Energy Saving and Carbon Reduction; Approaches for Energ Tony A. Chen Book 2022 The Editor(s) (if applicable) and The Author(s), under excl [打印本頁]

作者: 駝峰    時間: 2025-3-21 17:45
書目名稱Energy Saving and Carbon Reduction影響因子(影響力)




書目名稱Energy Saving and Carbon Reduction影響因子(影響力)學(xué)科排名




書目名稱Energy Saving and Carbon Reduction網(wǎng)絡(luò)公開度




書目名稱Energy Saving and Carbon Reduction網(wǎng)絡(luò)公開度學(xué)科排名




書目名稱Energy Saving and Carbon Reduction被引頻次




書目名稱Energy Saving and Carbon Reduction被引頻次學(xué)科排名




書目名稱Energy Saving and Carbon Reduction年度引用




書目名稱Energy Saving and Carbon Reduction年度引用學(xué)科排名




書目名稱Energy Saving and Carbon Reduction讀者反饋




書目名稱Energy Saving and Carbon Reduction讀者反饋學(xué)科排名





作者: 逢迎白雪    時間: 2025-3-21 23:54

作者: 得罪人    時間: 2025-3-22 01:14
Calculation of Mechanical Energy and Chemical Exergyy and exergy based on the thermodynamic differential equations of enthalpy and entropy, deriving the enthalpy, entropy, and exergy calculation method for real gas, and the residual properties of the influence of pressure on enthalpy and entropy can be calculated in three levels according to the diff
作者: 袋鼠    時間: 2025-3-22 08:32

作者: 盡管    時間: 2025-3-22 11:58

作者: dissent    時間: 2025-3-22 16:16

作者: dissent    時間: 2025-3-22 19:55
Energy Balance and Exergy Balance of Petrochemical Plantsa of the equipment, it can be summarized as the energy balance and exergy balance of the plant. This Chapter verifies the system energy consumption data in the plant, including process plant material balance, the calculation of thermodynamic energy and exergy consumption, calculation of energy and e
作者: 等級的上升    時間: 2025-3-22 22:11

作者: Forage飼料    時間: 2025-3-23 04:16

作者: 規(guī)范要多    時間: 2025-3-23 07:06
CO2 Capture and Utilization It covers the topics of CO. production, capture?and?storage in the energy industries. It also discusses CO. application in the chemical industries. Ten industrial operation case studies are used in the chapter which have covered different aspects in the CO. Generation, CO. Capture, Delivery, Storag
作者: evanescent    時間: 2025-3-23 12:56
Technical and Economic Evaluation of Energy-Saving Measuresng and carbon mitigation, it is needed to have a technical and economic evaluation of energy-saving projects, this chapter introduces the time value of capital, as well as the static evaluation method and dynamic evaluation method for the energy-saving project; proposed estimation methods of economi
作者: 財主    時間: 2025-3-23 16:00

作者: Credence    時間: 2025-3-23 19:40
Pinch Energy-Saving Technology and Its Applicationquantitative analysis and calculations, and uses the concept of optimization, but does not require advanced mathematics for optimization technology. This chapter first introduces the process dual subsystem system model, which is divided into the heat exchange subsystem and the process operation subs
作者: Water-Brash    時間: 2025-3-24 02:10
Key Energy-Saving Technologies It includes the following topics, (1) Pump and compressors speed control technology and its energy-saving principle; (2) Gas turbine energy-saving principle and its selection; (3) Combined gas turbine cycle and its application in LNG plant with simulation support; (4) Flue Gas Turbine Energy Saving
作者: Facet-Joints    時間: 2025-3-24 06:12

作者: 支柱    時間: 2025-3-24 06:37

作者: interrupt    時間: 2025-3-24 10:52
Erratum to: Das nichtallgemeine Pfahlwerk,y and exergy based on the thermodynamic differential equations of enthalpy and entropy, deriving the enthalpy, entropy, and exergy calculation method for real gas, and the residual properties of the influence of pressure on enthalpy and entropy can be calculated in three levels according to the diff
作者: Binge-Drinking    時間: 2025-3-24 16:21

作者: licence    時間: 2025-3-24 22:13
https://doi.org/10.1007/978-3-642-88246-3er, according to the energy change clues to study the process, there are three characteristics: (1) The main forms of process energy use are heat, fluid work, and steam; and heat, work, and steam are converted from fuel and electricity; (2) Heat, work, steam provided by the conversion equipment ente
作者: Eulogy    時間: 2025-3-25 01:19
Walter Wunderlich,Gunter Kienerom the equipment. This chapter discusses the Equipment Energy Balance and Exergy Balance for the main equipment used in chemical plants, petrochemical plants, and oil refineries, including the content and requirements of the plant energy analysis test trial, energy and exergy balance for pumps, comp
作者: 光亮    時間: 2025-3-25 03:52

作者: orient    時間: 2025-3-25 11:27

作者: 圖畫文字    時間: 2025-3-25 15:41

作者: Ccu106    時間: 2025-3-25 18:19

作者: Intellectual    時間: 2025-3-25 22:22
Statisch unbestimmte Biegestabgebildeng and carbon mitigation, it is needed to have a technical and economic evaluation of energy-saving projects, this chapter introduces the time value of capital, as well as the static evaluation method and dynamic evaluation method for the energy-saving project; proposed estimation methods of economi
作者: Intercept    時間: 2025-3-26 01:09
https://doi.org/10.1007/978-3-642-56332-4 reduction. Generally, saving energy can reduce costs including saving Carbon Tax. Investment costs and energy-saving benefits are a pair of complementary contradictions; under specific conditions, to organically unify investment and benefits to produce maximum benefits is what we call optimization
作者: 沒花的是打擾    時間: 2025-3-26 05:11

作者: 激怒    時間: 2025-3-26 12:19

作者: Hay-Fever    時間: 2025-3-26 15:21
https://doi.org/10.1007/978-981-19-5295-1Energy Balance; Exergy Balance; Energy Analysis; Heat Integration; CO2 Capture; Greenhouse Gas; CO2 Utiliz
作者: 心神不寧    時間: 2025-3-26 18:23
https://doi.org/10.1007/978-3-642-50787-8orms to be used, and their reference states, which are frequently used in process energy utilization analysis and improvement; the first thermodynamic law and second thermodynamic law have been briefly introduced, which is the basis of entire energy utilization analysis and improvement.
作者: photophobia    時間: 2025-3-27 00:22
Thermodynamics Fundamentalsorms to be used, and their reference states, which are frequently used in process energy utilization analysis and improvement; the first thermodynamic law and second thermodynamic law have been briefly introduced, which is the basis of entire energy utilization analysis and improvement.
作者: 明智的人    時間: 2025-3-27 01:31

作者: cancellous-bone    時間: 2025-3-27 08:13
Tony A. ChenProvides an approach to carbon capture and utilization, by using fossil fuel.Meets the strong market needs on GHG reduction with economic benefit of fuel, power.Incorporates 10 case studies with proce
作者: acheon    時間: 2025-3-27 12:44
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作者: 雪上輕舟飛過    時間: 2025-3-27 15:20

作者: 多產(chǎn)子    時間: 2025-3-27 20:16

作者: 背叛者    時間: 2025-3-27 23:15

作者: 蛛絲    時間: 2025-3-28 04:09

作者: 施魔法    時間: 2025-3-28 10:05

作者: 半球    時間: 2025-3-28 12:07
CO2 Capture and Utilizatione study 5; Flue gas CO. Capture using DEA solvent—Case study 6; Flue gas CO. capture using oxygen instead of combustion air—Case Study 7; CO. dehydration and compression—Case study 8; Flue gas CO. Capture, compression and dehydration—Case study 9; Flue gas Cryogenic CO. Capture—Case Study 10. A newl
作者: 摘要記錄    時間: 2025-3-28 15:45
Pinch Energy-Saving Technology and Its Applicationy system; The effect of cross heat transfer on heat exchange network area and energy; Energy saving principle of pinch technology; and in Sect.?. provided the showcase of Pinch analysis examples using Aspen Energy Analyzer.
作者: 侵略者    時間: 2025-3-28 22:06
Key Energy-Saving Technologiesre Heat Recovery and Utilization, including direct use as process heating, upgrading use of compression heat pump, absorption heat pump, refrigeration, and power generation, direct use and upgrading use system integration.
作者: 旋轉(zhuǎn)一周    時間: 2025-3-28 23:52
https://doi.org/10.1007/978-3-7091-7709-9ethod for utility streams, and heat dissipation measuring and calculation with a simple and more accurate method of convection and radiation combined heat transfer coefficient. The petrochemical process involves many process streams and utilities, and the calculation of its energy and exergy is the
作者: Nonflammable    時間: 2025-3-29 06:00
https://doi.org/10.1007/978-3-642-88246-3nt, energy utilization links, process units, auxiliary system, and plant. The reader can evaluate the energy efficiency for every level and identify energy utilization issues, put forward solutions for energy-saving and carbon reduction.
作者: Visual-Field    時間: 2025-3-29 07:59

作者: SYN    時間: 2025-3-29 15:05
,Der prim?re Spannungszustand des Gebirges,e study 5; Flue gas CO. Capture using DEA solvent—Case study 6; Flue gas CO. capture using oxygen instead of combustion air—Case Study 7; CO. dehydration and compression—Case study 8; Flue gas CO. Capture, compression and dehydration—Case study 9; Flue gas Cryogenic CO. Capture—Case Study 10. A newl
作者: Exterior    時間: 2025-3-29 17:24

作者: BUCK    時間: 2025-3-29 23:45
Schwingungen drehsymmetrischer Schalen,re Heat Recovery and Utilization, including direct use as process heating, upgrading use of compression heat pump, absorption heat pump, refrigeration, and power generation, direct use and upgrading use system integration.
作者: cornucopia    時間: 2025-3-30 00:13
https://doi.org/10.1007/978-3-642-56332-4 estimate method; following the optimization method, proposed the following process optimization approach and results: Economical insulation thickness of hot fluid pipeline; Economical pipe diameter and insulation thickness for fluid transportation, Optimization of heat exchange equipment; Economical thermal efficiency of the heating furnace.
作者: 庇護(hù)    時間: 2025-3-30 06:09

作者: Evolve    時間: 2025-3-30 11:06
Calculation of Mechanical Energy and Chemical Exergyfor real gas, and the residual properties of the influence of pressure on enthalpy and entropy can be calculated in three levels according to the different calculation accuracy required. This chapter also Introduces the energy and exergy calculation of the fluid flowing process, chemical exergy, and fuel exergy calculation.
作者: annexation    時間: 2025-3-30 15:24

作者: 熱心    時間: 2025-3-30 20:20





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