The document discusses kinetics of electrochemical reactions and mass transfer in electrochemical systems. It covers the following key points:
1) Chemical kinetics is the study of reaction rates and mechanisms. In industrial synthesis, reaction rates are as important as equilibrium constants. Kinetics answers how fast reactions occur, while thermodynamics addresses if they will occur.
2) Applying a potential increases the reaction rate by reducing the activation energy barrier. Current increases with increasing driving force from an applied potential. Catalysts also reduce the activation energy.
3) The rate of electrochemical reactions depends on parameters like materials, composition, and temperature. Increasing the reaction rate improves fuel cell performance. Reactions occur at electrode-elect
lecture slide on:
Gibbs free energy and Nernst Equation, Faradaic Processes and Factors Affecting Rates of Electrode Reactions, Potentials and Thermodynamics of Cells, Kinetics of Electrode Reactions, Kinetic controlled reactions,Essentials of Electrode Reactions,BUTLER-VOLMER MODEL FOR THE ONE-STEP, ONE-ELECTRON PROCESS,Current-overpotential curves for the system, Mass Transfer by Migration And Diffusion,MASS-TRANSFER-CONTROLLED REACTIONS,
ELECTRICAL DOUBLE LAYER-TYPES-DYNAMICS OF ELECTRON TRANSFER-MARCUS THEORY-TUNNELING - BUTLER VOLMER EQUATIONS-TAFEL EQUATIONS-POLARIZATION AND OVERVOLTAGE-CORROSION AND PASSIVITY-POURBAIX AND EVAN DIAGRAM-POWER STORAGE-FUEL CELLS
lecture slide on:
Gibbs free energy and Nernst Equation, Faradaic Processes and Factors Affecting Rates of Electrode Reactions, Potentials and Thermodynamics of Cells, Kinetics of Electrode Reactions, Kinetic controlled reactions,Essentials of Electrode Reactions,BUTLER-VOLMER MODEL FOR THE ONE-STEP, ONE-ELECTRON PROCESS,Current-overpotential curves for the system, Mass Transfer by Migration And Diffusion,MASS-TRANSFER-CONTROLLED REACTIONS,
ELECTRICAL DOUBLE LAYER-TYPES-DYNAMICS OF ELECTRON TRANSFER-MARCUS THEORY-TUNNELING - BUTLER VOLMER EQUATIONS-TAFEL EQUATIONS-POLARIZATION AND OVERVOLTAGE-CORROSION AND PASSIVITY-POURBAIX AND EVAN DIAGRAM-POWER STORAGE-FUEL CELLS
A ppt compiled by Yaseen Aziz Wani pursuing M.Sc Chemistry at University of Kashmir, J&K, India and Naveed Bashir Dar, a student of electrical engg. at NIT Srinagar.
Warm regards to Munnazir Bashir also for providing us with refreshing tea while we were compiling ppt.
A ppt compiled by Yaseen Aziz Wani pursuing M.Sc Chemistry at University of Kashmir, J&K, India and Naveed Bashir Dar, a student of electrical engg. at NIT Srinagar.
Warm regards to Munnazir Bashir also for providing us with refreshing tea while we were compiling ppt.
This is presentation is useful for the M. Sc. I students from Sant Gadge Baba Amravati University Amravati. It includes Collision Theory its Derivation and Limitations
Knocking Door of Cyclic Voltammetry - cv of CV by Monalin MishraMONALINMISHRA
This ppt presentation shares some short basic knowledge on the electroanalytical technique of Cyclic Voltammetry. It also covers the working of CV with some short videos and photos.It also provides general explanation on some relevent techniques
Chemical kinetics, also known as reaction kinetics, is the branch of physical chemistry that is concerned with understanding the rates of chemical reactions. It is to be contrasted with thermodynamics, which deals with the direction in which a process occurs but in itself tells nothing about its rate
This Perspective presents a personal overview of the current status of the theory of chemical kinetics and mechanisms for complex processes. We attempt to assess the status of the field for reactions in the gas phase, at gas–solid interfaces, in liquid solutions, in enzymes, and for protein folding. Some unifying concepts such as potential energy surfaces, free energy, master equations, and reaction coordinates occur in more than one area. We hope this Perspective will be useful for highlighting recent advances and for identifying important areas for future research.
Sachpazis:Terzaghi Bearing Capacity Estimation in simple terms with Calculati...Dr.Costas Sachpazis
Terzaghi's soil bearing capacity theory, developed by Karl Terzaghi, is a fundamental principle in geotechnical engineering used to determine the bearing capacity of shallow foundations. This theory provides a method to calculate the ultimate bearing capacity of soil, which is the maximum load per unit area that the soil can support without undergoing shear failure. The Calculation HTML Code included.
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Advancements in technology unveil a myriad of electrical and electronic breakthroughs geared towards efficiently harnessing limited resources to meet human energy demands. The optimization of hybrid solar PV panels and pumped hydro energy supply systems plays a pivotal role in utilizing natural resources effectively. This initiative not only benefits humanity but also fosters environmental sustainability. The study investigated the design optimization of these hybrid systems, focusing on understanding solar radiation patterns, identifying geographical influences on solar radiation, formulating a mathematical model for system optimization, and determining the optimal configuration of PV panels and pumped hydro storage. Through a comparative analysis approach and eight weeks of data collection, the study addressed key research questions related to solar radiation patterns and optimal system design. The findings highlighted regions with heightened solar radiation levels, showcasing substantial potential for power generation and emphasizing the system's efficiency. Optimizing system design significantly boosted power generation, promoted renewable energy utilization, and enhanced energy storage capacity. The study underscored the benefits of optimizing hybrid solar PV panels and pumped hydro energy supply systems for sustainable energy usage. Optimizing the design of solar PV panels and pumped hydro energy supply systems as examined across diverse climatic conditions in a developing country, not only enhances power generation but also improves the integration of renewable energy sources and boosts energy storage capacities, particularly beneficial for less economically prosperous regions. Additionally, the study provides valuable insights for advancing energy research in economically viable areas. Recommendations included conducting site-specific assessments, utilizing advanced modeling tools, implementing regular maintenance protocols, and enhancing communication among system components.
Saudi Arabia stands as a titan in the global energy landscape, renowned for its abundant oil and gas resources. It's the largest exporter of petroleum and holds some of the world's most significant reserves. Let's delve into the top 10 oil and gas projects shaping Saudi Arabia's energy future in 2024.
Welcome to WIPAC Monthly the magazine brought to you by the LinkedIn Group Water Industry Process Automation & Control.
In this month's edition, along with this month's industry news to celebrate the 13 years since the group was created we have articles including
A case study of the used of Advanced Process Control at the Wastewater Treatment works at Lleida in Spain
A look back on an article on smart wastewater networks in order to see how the industry has measured up in the interim around the adoption of Digital Transformation in the Water Industry.
CFD Simulation of By-pass Flow in a HRSG module by R&R Consult.pptxR&R Consult
CFD analysis is incredibly effective at solving mysteries and improving the performance of complex systems!
Here's a great example: At a large natural gas-fired power plant, where they use waste heat to generate steam and energy, they were puzzled that their boiler wasn't producing as much steam as expected.
R&R and Tetra Engineering Group Inc. were asked to solve the issue with reduced steam production.
An inspection had shown that a significant amount of hot flue gas was bypassing the boiler tubes, where the heat was supposed to be transferred.
R&R Consult conducted a CFD analysis, which revealed that 6.3% of the flue gas was bypassing the boiler tubes without transferring heat. The analysis also showed that the flue gas was instead being directed along the sides of the boiler and between the modules that were supposed to capture the heat. This was the cause of the reduced performance.
Based on our results, Tetra Engineering installed covering plates to reduce the bypass flow. This improved the boiler's performance and increased electricity production.
It is always satisfying when we can help solve complex challenges like this. Do your systems also need a check-up or optimization? Give us a call!
Work done in cooperation with James Malloy and David Moelling from Tetra Engineering.
More examples of our work https://www.r-r-consult.dk/en/cases-en/
Overview of the fundamental roles in Hydropower generation and the components involved in wider Electrical Engineering.
This paper presents the design and construction of hydroelectric dams from the hydrologist’s survey of the valley before construction, all aspects and involved disciplines, fluid dynamics, structural engineering, generation and mains frequency regulation to the very transmission of power through the network in the United Kingdom.
Author: Robbie Edward Sayers
Collaborators and co editors: Charlie Sims and Connor Healey.
(C) 2024 Robbie E. Sayers
About
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
• Remote control: Parallel or serial interface.
• Compatible with MAFI CCR system.
• Compatible with IDM8000 CCR.
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
• Easy in configuration using DIP switches.
Technical Specifications
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
Key Features
Indigenized remote control interface card suitable for MAFI system CCR equipment. Compatible for IDM8000 CCR. Backplane mounted serial and TCP/Ethernet communication module for CCR remote access. IDM 8000 CCR remote control on serial and TCP protocol.
• Remote control: Parallel or serial interface
• Compatible with MAFI CCR system
• Copatiable with IDM8000 CCR
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
Application
• Remote control: Parallel or serial interface.
• Compatible with MAFI CCR system.
• Compatible with IDM8000 CCR.
• Compatible with Backplane mount serial communication.
• Compatible with commercial and Defence aviation CCR system.
• Remote control system for accessing CCR and allied system over serial or TCP.
• Indigenized local Support/presence in India.
• Easy in configuration using DIP switches.
1. UNIT-ONE
1.2. Kinetics of Electrochemical Reactions
1.3. Mass transfer in electrochemical systems
BY Brhane Amha
Mekelle Institute of technology
MU
2. Reactions Kinetics
• Chemical kinetics, also called reaction kinetics, is the study of the rates and
mechanisms of chemical reactions.
• In the industrial synthesis of compounds, reaction rates are as important as
equilibrium constants.
• The thermodynamic equilibrium constant tells us the maximum possible yield of
NH3 obtainable at any given T and P from N2 and H2, but if the reaction rate
between N2 and H2 is too low, the reaction will not be economical to carry out.
• We can, from thermodynamics, address the question; Will the reaction occur?
• We need kinetics, however, answer the question: How fast will the reaction occur?
• In summary, to understand and predict the behavior of a chemical system, one
must consider both thermodynamics and kinetics.
3.
4.
5. Fuel Cell Reactions Kinetics
• Applying a potential to an electrode generates an electric field at the
electrode/electrolyte interface that reduces the magnitude of the
activation energy barrier increasing the ET reaction rate, Electrolysis
works on this principle.
• An applied potential acts as a driving force for the ET reaction.
• Expect that current should increase with increasing driving force
• Catalysts act to reduce the magnitude of the activation energy barrier .
6.
7.
8.
9.
10.
11. Fuel Cell Reactions Kinetics
• Each electrochemical reaction event results in the transfer of one or more electrons,
the current produced by a fuel cell (number of electrons per time) depends on the
rate of the electrochemical reaction (number of reactions per time).
• Rate of electrochemical reaction is dependent on various parameters electrode
material, electrolyte composition, temperature etc.
• Increasing the rate of the electrochemical reaction is therefore crucial to improve
fuel cell performance.
• Electrochemical processes are heterogeneous.
• Electrochemical reactions take place at the interface between an Electrode and an
electrolyte.
12.
13.
14. Fuel Cell Reactions Kinetics
• One of the fundamental laws of electrochemistry is
Faraday’s Law, which relates the charge passed in
an electrochemical experiment (Q) to the number of
moles of analyte electrolyzed (N): Q = nFN
15. O + ne- ⇄ R
(electrode reaction)
nFA
I
v
Electric current (I) measured at the
electrode is proportional to the rate (v)
of the electrode reaction!
(q – charge, t – time, F – Faraday constant; A –
electrode surface area; n – number of electrons, n(O)
– number of moles of the reactant O)
Rate of an electrode reaction: the flux
R (reduced species)
O (oxidized species)
- e
electrode|solution Interface
AnF
I
AnFt
q
v
tA
n
v
nFnq
t
q
I
1
d
d
d
)O(d
)O(
d
d Flux (the rate of the
heterogeneous electrode
reaction) is equal to the
amount of reacted
material per unit of time
per unit of electrode
surface area
(mol s -1 cm-2). This
chemical rate is equal to
the ratio of the electric
current, number of
exchanged electrons in a
unit reaction and
electrode surface area.