Gestão de Sistemas Energéticos 2017/2018

Similar documents
Lecture 11 Combustion Processes

Exergy Analysis of a Power Plant in Abu Dhabi (UAE)

Thermodynamic analysis of a regenerative gas turbine cogeneration plant

High-efficiency low LCOE combined cycles for sour gas oxy-combustion with CO[subscript 2] capture

CO 2 capture processes: Novel approach to benchmarking and evaluation of improvement potentials

CONTROL VOLUME ANALYSIS USING ENERGY. By Ertanto Vetra

Heat Engines and Refrigerators

Principles of Engineering Thermodynamics. 8th Edition SI Version

Energy & Power Unit 5, Lesson 1 Explanation

Energy Balances and Numerical Methods Design Project. Production of Methyl Tertiary-Butyl Ether

Introduction to Energy Economics. Basic Concepts and Global Energy Picture

ENERGY AND EXERGY ANALYSIS OF SNØHVIT - AN LNG PROCESSING PLANT IN NORWAY

Potential of a Chemical Heat Storage as a Heat for a Catalytic Converter

DESIGN ANALYSIS OF A REFRIGERATED WAREHOUSE USING LNG COLD ENERGY

Carpet Waste Gasification:

Energy And Exergy Analysis Of Fully Condensing Steam Turbine At Various Steam Load Condition

Exergy Based Analysis of an Open Cycle Gas Turbine Power Plant

Hydrogen production via catalytic water splitting. Prospects of reducing greenhouse emission by hydrogen powered energy technologies

Thermodynamic analysis on post combustion CO 2 capture of natural gas fired power plant

Reduction of Energy Consumption in Investment Casting Process by application of a New Casting Facility

Chemistry CH1HP. (Jan13CH1Hp01) General Certificate of Secondary Education Higher Tier January Unit Chemistry C1. Unit Chemistry C1 TOTAL

Performance and Efficiency of a Biogas CHP System Utilizing a Stirling Engine

An Approach towards Thermal Power Plants Efficiency Analysis by Use of Exergy Method

Solid Waste to Energy

Conversion of Hydrocarbons into Syn-Gas Stimulated by Non-thermal Atmospheric Pressure Plasma

Energy Sector March 2016, Maseru, Lesotho Pavel Shermanau, IPCC TFI TSU

Theory Comparison between Propane and Methane Combustion inside the Furnace

Life cycle analysis of thermosyphon solar water heaters

MCG THERMODYNAMICS II. 22 April 2008 Page 1 of 7 Prof. W. Hallett

Your Family s Carbon Footprint

PRODUCTION OF SYNGAS BY METHANE AND COAL CO-CONVERSION IN FLUIDIZED BED REACTOR

OUTCOME 2 TUTORIAL 2 STEADY FLOW PLANT

S.E. (Chemical) (First Semester) EXAMINATION, 2012 PROCESS CALCULATIONS (2008 PATTERN) Time : Three Hours Maximum Marks : 100

Synergistic Energy Conversion Processes Using Nuclear Energy and Fossil Fuels

EXERGY ANALYSIS OF GAS-TURBINE COMBINED CYCLE WITH CO 2 CAPTURE USING PRE-COMBUSTION DECARBONIZATION OF NATURAL GAS

Plastic to Fuel Technologies

World Energy Sources & Fossil Fuel Power Production. Josh Barnes, Cyrus Hughlett...and Karl. SL/AP Physics Hour 2

Performance of CLOU process in the combustion of different types of coal with CO 2 capture

Mechanical energy describes the sum of potential energy and kinetic energy present in the components of a mechanical system.

Hydrogen oxygen steam generator integrating with renewable energy resource for electricity generation

Smart CHP from Biomass and Waste

Gasification of Woodchips from the San Rossore natural Reserve Maintenance for CHP Application: a Case Study Analysis. 1.

Organic Rankine Cycle Configurations

Modeling and simulations of methane steam reforming in thermally coupled plate type membrane reactor

Efficiency improvement of steam power plants in Kuwait

Chapter 2.7: Cogeneration

Chapter 6 THE SECOND LAW OF THERMODYNAMICS

Exergy & Environmental Based Comparison of Hydrogen Production from Natural gas, Carbon and Nuclear energy

ES Hydrogen Production via the Iron/Iron Oxide Looping Cycle. Copyright 2011 by ASME

ABOUT AVA-CO2 ENERGY OF THE FUTURE

4.1 Introduction 4.2 Kiln System. 4.3 Kiln System Analysis 4.4 Results and Discussion 4.5 Conclusion

Q1. The diagrams show what happens to each 100 joules of energy from burning coal on an open fire and in a stove.

Technical Description Package Micro Auto Gasification System (MAGS )

Syngas Makes any Vehicle Green

Environmental Science and Engineering Toolbox

POLLUTION FROM MOTOR VEHICLES

Environmental Science. Physics and Applications

MultiZon incinerator for batch operation

Techno-Economic Analysis for Ethylene and Oxygenates Products from the Oxidative Coupling of Methane Process

Christian Ohler, ABB Switzerland Corporate Research Efficiency versus Cost - a Fundamental Design Conflict in Energy Science

Development of 1MW high efficiency gas engine cogeneration system

Combined use of coal mine gases for efficient energy generation

Technical Analysis of the Natural Gas to Hydrocarbon Liquid Process

BIOGAS SPECIFIC HEAT CAPACITY VARIATIONS DURING UPGRADING

Chapter 2 ENERGY, ENERGY TRANSFER, AND GENERAL ENERGY ANALYSIS

with Physical Absorption

Environmental Life Cycle Assessment PSE 476/FB 576

Heat and Power Integration Opportunities in Methane Reforming based Hydrogen Production with PSA separation

4. If the Earth is to continue to use oil its current rate, what must happen for us to sustain this rate?

NATURAL GAS STEAM REFORMING FOR HYDROGEN PRODUCTION. AN ENERGETIC APPROACH

Michigan State University DEPARTMENT OF CHEMICAL ENGINEERING AND MATERIALS SCIENCE. ChE 321: Thermodynamics Spring 2017

Fast Analysis of Extended Natural Gas using the New Transportable INFICON Micro GC Fusion

REDUCTION OF CO 2 EMISSION TO METHANE USING HYDROGENATION WITH NICKEL (110) SURFACE CATALYST

Status and Trends for Stationary Fuel Cell Power Systems

Energy Efficient Process Heating: Managing Air Flow

Lecture 14 Modern trends in BOF steelmaking

FactSage Independent Study

Chemical kinetics study of combustion characteristics of ammonia-air mixtures under high pressure lean conditions

Lignite oxidative desulphurization. Notice 2: effects of process parameters

Exergoeconomic Analysis of A 100MW Unit GE Frame 9 Gas Turbine Plant in Ughelli, Nigeria.

Performance of a Gas Turbine Power Plant

Critical exergy analysis of counterflow reversibly used cooling towers

2 nd M2M Partnership Expo,

A student investigated the efficiency of a motor using the equipment in Figure 1. Figure 1

SUPERCRITICAL COAL FIRED POWER PLANT

HEAT TRANSFER IN MINI HEAT EXCHANGER USING NANOFLUIDS. L.B. Mapa 1, Sana Mazhar 2 ABSTRACT

Maximizing the Efficiency of a Heat Recovery Steam Generator for Solid Oxide Fuel Cell-Based Trigeneration Systems

Best Practices Learned from Greenhouse Gas Reporting

Lecture No.3. The Ideal Reheat Rankine Cycle

Energy Balances and Numerical Methods Design Project. Production of Cumene

COMBUSTION PROCESS ANALYSIS IN BOILER OP-650K BASED ON ACOUSTIC GAS TEMPERATURE MEASURING SYSTEM

Urban Environmental Excursions

Thermo-Chemical Recuperation as an Efficient Way of Engine's Waste Heat Recovery

Legrand's environmental commitments

Chapter 11: Energy Flow and Power

WESTINGHOUSE PLASMA GASIFICATION

a. The power required to drive the compressor; b. The inlet and output pipe cross-sectional area. [Ans: kw, m 2 ] [3.34, R. K.

EFFECT OF AMBIENT TEMPERATURE, GAS TURBINE INLET TEMPERATURE AND COMPRESSOR PRESSURE RATIO ON PERFORMANCE OF COMBINED CYCLE POWER PLANT

Thermodynamic Analysis of Coal to Synthetic Natural Gas Process

Transcription:

Gestão de Sistemas Energéticos 2017/2018 Exergy Analysis Prof. Tânia Sousa taniasousa@tecnico.ulisboa.pt

Conceptualizing Chemical Exergy The logarithmic term typically contributes only a few percent to the chemical exergy magnitude

Total Exergy Total exergy is: First evaluate thermomechanical exergy (the system goes from T, P to T 0, P 0 ) and then evaluate the chemical exergy (at constant T 0, P 0 the system goes to the reference chemical composition of the environment)

Example What about an ideal mixture of gases present in the environment when T 0 = 298.15 K, p 0 = 1 atm?

Example What about an ideal mixture of gases present in the environment when T 0 = 298.15 K, p 0 = 1 atm?

Example Methane gas enters a reactor and burns completely with 140% theoretical air. Combustion products exit as a mixture at temperature T and a pressure of 1 atm. For T 480 and 1560 K, evaluate the flow exergy of the combustion products, in kj per kmol of fuel.

Example Methane gas enters a reactor and burns completely with 140% theoretical air. Combustion products exit as a mixture at temperature T and a pressure of 1 atm. For T 480 and 1560 K, evaluate the flow exergy of the combustion products, in kj per kmol of fuel. Combustion Products yp 0 480K Combustion Products yp 0 25ºC Combustion Products at y e P 0 25ºC

Exergetic efficiency of an internal combustion engine Liquid octane enters an internal combustion engine operating at steady state with a mass flow rate of 1.8 10-3 kg/s and is mixed with the theoretical amount of air. Determine the exergetic efficiency. Substance Model for HHV LHV e ch Liquid octane Gasoline 47,900 44,430 47,390 a b

Fuel Cells Fuel (H 2 ) and oxidizer (O 2 ) 40 a 60 % efficiency

Exergy Balances to Reacting Systems What is the exergy balance to the reversible steadystate combustion of C a H b?

Chemical Exergy The exergy value of C a H b is

Primary, Final, Useful Energy & Energy Services

Forms of Energy - Primary energy

Forms of Energy - Final energy

Forms of Energy Useful Energy Other Electrical Uses Light Mechanical power Heat Muscle work Heat/Cooling

Forms of Energy Primary energy embodied in resources as it is found in nature (coal, oil, natural gas in the ground) Final energy sold to final consumers such as households or firms (electricity, diesel, processed natural gas) Useful energy in the form that is used: light, heat, cooling and mechanical power (stationary or transport) Productive energy the fraction of useful energy that we actually use

Energy Services

From Primary Energy to Energy Services

From Primary Energy to Energy Services Energy Supply energy flows driven by resource availability and conversion technologies IAASA - Global Energy Assessment 2012

From Primary Energy to Energy Services Energy Demand Energy system is service driven IAASA - Global Energy Assessment 2012

From Primary Energy to Energy Services Quality and cost of energy services IAASA - Global Energy Assessment 2012

Sankey Diagrams & First Law Efficiency

Sankey Diagrams Sankey Diagrams: a flow diagram used to represent flows of mass (water, CO2, etc) or energy or money or... by arrows where the thickness of arrows are proportional to the amount Miguel Águas (2009)

Example? Sankey Diagram

Sankey Diagram Schematic representation of the energy flow (natural gas electricity light reading) Natural gas 50% E E final primary W Q out in Electricity 50% E E useful final Light 20% E productive E useful What is the aggregate efficiency?

Sankey Diagram Schematic representation of the energy flow (natural gas electricity light reading) Natural gas 50% E E final primary W Q out in Electricity 50% E E useful final Light 20% E productive E useful What is the aggregate efficiency? 5%

World Sankey Diagram in 2005 E final? Eprimary E E useful final? US 94 EJ Portugal 1.1 EJ 1st law efficiencies from primary to final energy and primary to useful are 66 % and 34% IAASA Global Energy Assessment 2012

Typical values of 1 st law efficiencies 1 st Law efficiencies from primary to final energy 1 st Law efficiencies from final to useful energy

First vs. Second Law energy efficiencies IAASA - Global Energy Assessment 2012 Overall 2 nd law efficiency in converting primary to final is 76% and primary to useful energy is 10%

First vs. Second Law energy efficiencies Second law efficiencies provide information on how much you can improve your efficiency Rosen and Dincer, 1997

World Sankey Diagram in 2005 IAASA Global Energy Assessment 2012

World Sankey Diagram in 2005 IAASA Global Energy Assessment 2012

World Sankey Diagram in 2005 IAASA Global Energy Assessment 2012

World Sankey Diagram in 2005 IAASA Global Energy Assessment 2012

World Sankey Diagram in 2005 IAASA Global Energy Assessment 2012

World Sankey Diagram in 2005 IAASA Global Energy Assessment 2012

World Sankey Diagram in 2005 IAASA Global Energy Assessment 2012

From useful energy to energy services Passive systems: where useful energy is delivered into and mostly lost as unwanted heat, in exchange for energy services such as thermal comfort, illumination and transport (Cullen et al., 2011).

From useful energy to energy services Human behaviour & quality

kahoot