aupschool.org
RSS

May 21, 2025

Top 10 people who changed the whole world – The Engineering Concepts

maximios Engineering

1. Bill Gates  : Full name is William Henry Gates III (born October 28, 1955) ;  Founder of  Microsoft

Bill Gate Famous Quotes

Your most unhappy customers are your greatest source of learning.

Success is a lousy teacher. It seduces smart people into thinking they can’t lose.

It’s fine to celebrate success but it is more important to heed the lessons of failure.

2. Nelson Mandela : ( 18 July 1918-5 December 2013) ; first President of democratic South Africa in 1994.

Education is the most powerful weapon which you can use to change the world.

It always seems impossible until it’s done.

There is no passion to be found playing small – in settling for a life that is less than the one you are capable of living.

3.   Abraham Lincoln  : (12 February 1809- April 15, 1865)

Abraham Lincoln Famous Quotes

All that I am, or hope to be, I owe to my angel mother.

Character is like a tree and reputation like a shadow. The shadow is what we think of it; the tree is the real thing.
Don’t worry when you are not recognized, but strive to be worthy of recognition.

4.  Jesus Christ  : (c. 4 BC – c. AD 30 / 33)

Let the one among you who is without sin be the first to cast a stone. Blessed are the merciful, for they will be shown mercy.

But I say to you, Love your enemies and pray for those who persecute you, so that you may be sons of your Father who is in heaven; for he makes his sun rise on the evil and on the good, and sends rain on the just and on the unjust.

5.  Lord Buddha : (circa 563 BCE – 483 BCE)

Lord Buddha  Famous Quotes

Do not dwell in the past, do not dream of the future, concentrate the mind on the present moment.

You yourself, as much as anybody in the entire universe, deserve your love and affection.

Peace comes from within. Do not seek it without.

6.  Mahatma Gandhi :  Mohandas Karamchand Gandhi (1869 – 1948)

Where there is love there is life.

Happiness is when what you think, what you say, and what you do are in harmony.

The weak can never forgive. Forgiveness is the attribute of the strong.

7.  Karl Marx  : (1818 – 1883)

 Karl Marx Famous Quote

The philosophers have only interpreted the world, in various ways. The point, however, is to change it.

Men make their own history, but they do not make it as they please.

History repeats itself, first as tragedy, second as farce.

8.  Adolf Hitler : (20 April 1889 – 30 April 1945)

Adolf Hitler  Famous Quote

If you tell a big enough lie and tell it frequently enough, it will be believed.

Make the lie big, make it simple, keep saying it, and eventually they will believe it.

He alone, who owns the youth, gains the future.

9.  Albert Einstein : ( 14 March 1879 – 18 April 1955)

albert-einstein-9285408-1-402-6905406

Albert Einstein

Albert Einstein Famous Quote

Imagination is more important than knowledge.

Life is like riding a bicycle. To keep your balance you must keep moving.

Two things are infinite: the universe and human stupidity; and I’m not sure about the universe.

10. Alexander the Great : (356 BCE –323 BCE)

Alexander the Great Famous Quote

There is nothing impossible to him who will try.

I am indebted to my father for living, but to my teacher for living well.

Remember upon the conduct of each depends the fate of all.

May 21, 2025

P&ID Symbols and Notation – By TheEngineeringConcepts.com

maximios Engineering

As we all know that the industrial P&ID diagram  comprised of specific symobols (P&ID Symbols) having specific shape special notation .

In this article we will see different symbol and notations used to create a P&ID  diagram  as per industrial process . A  huge variety of symbols is used to craete a standard P&ID diagram.

Here in this article we will go through these topic of contents  which will give you a good idea regarding P&ID creation.

Topic of Contents

  • About P&ID symbols
  • Equipment symbols
  • Piping symbols
  • Vessel symbols
  • Heat exchanger symbols
  • Pump symbols
  • Instrument symbols
  • Valve symbols

About P&ID symbols

Piping and Instrumentation Diagram Standard Symbols Detailed Documentation provides a standard set of shapes & symbols for documenting P&ID and PFD, including standard shapes for instrument, valves, pump, heating exchanges, mixers, crushers, vessels, compressors, filters, motors and connecting shapes.

An equipment is comprised of miscellaneous P&ID units that don’t fit into the other categories. This group includes various individual components  like compressors, conveyors, motors, pumps, turbines, pneumatic controllers,  vacuums, and other mechanical devices.

Various symbols are used to indicate piping components, instrumentation, equipments in engineering drawings such as Piping and Instrumentation Diagram (P&ID), Isometric Drawings, Plot Plan, Equipment Layout, Welding drawings etc. Checkout list of such symbols given below.

Piping can be made of various materials, including metal and plastic. The piping group is made up of one-to-many pipes, multi-line pipes, separators, and other types of piping devices.

Pump symbols

Valve Symbols 

Static Equipment and Distillation column

Line Symbols for PFD and P&ID

pipeline-pid-symbols-4081998

SourceArticle : Lucidchart

Read Also :  

Piping and Instrumentation Diagram – P&ID

Process Flow Diagram (PFD)

Piping Systems Codes and Standards

Also Read Another Content:

What is Boiler ?

Venturi Flow Meter

Pitot Tube 

Coriolis Mass Flow Meter

May 21, 2025

What is SCADA ? How does SCADA Works? – The Engineering Concepts

maximios Engineering

SCADA stands for Supervisory Control and Data Acquisition but it is a term often used for data collection and presentation.

SCADA is normally a software package designed to display information, log data and show alarms.

This can be graphical and tabular and can involve words and pictures (or mimics).

The software would normally be installed on a computer and all the various signals would be wired back to the central point (CPU), or marshalled and gathered using some form of bus system or direct wired.

SCADA can be used to monitor and control plant or equipment. The control may be automatic, or initiated by operator commands. The data acquisition is accomplished firstly by the RTU’s (remote Terminal Units).

The central host will scan the RTU’s or the RTU’s will report in Data can be of three main types.

Analogue data (i.e. real numbers) will be trended (ie placed in graphs). Digital data (on/off) may have alarms attached to one state or the other. Pulse data (e.g. counting revolutions of a meter) is normally accumulated or counted

Supervisory control and data acquisition – SCADA refers to ICS (industrial control systems) used to control infrastructure processes (Utilities, water treatment, wastewater treatment, gas pipelines, wind farms, etc), facility-based processes (airports, space stations, ships, etc,) or industrial processes (production, manufacturing, refining, power generation, etc).

The following subsystems are usually present in SCADA systems:

  • The apparatus used by a human operator; all the processed data are presented to the operator
  • A supervisory system that gathers all the required data about the process
  • Remote Terminal Units (RTUs) connected to the sensors of the process, which helps to convert the sensor signals to the digital data and send the data to supervisory stream.
  • Programmable Logic Controller (PLCs) used as field devices
  • Communication infrastructure connects the Remote Terminal Units to supervisory system.

Generally, a SCADA system does not control the processes in real time – it usually refers to the system that coordinates the processes in real time.

SCADA refers to the centralized systems that control and monitor the entire sites, or they are the complex systems spread out over large areas.

Nearly all the control actions are automatically performed by the remote terminal units (RTUs) or by the programmable logic controllers (PLCs).

The restrictions to the host control functions are supervisory level intervention or basic overriding.

For example, the PLC (in an industrial process) controls the flow of cooling water, the SCADA system allows any changes related to the alarm conditions and set points for the flow (such as high temperature, loss of flow, etc) to be recorded and displayed.

Data acquisition starts at the PLC or RTU level, which includes the equipment status reports, and meter readings. Data is then formatted in such way that the operator of the control room can make the supervisory decisions to override or adjust normal PLC (RTU) controls, by using the HMI.

SCADA systems mostly implement the distributed databases known as tag databases, containing data elements called points or tags. A point is a single output or input value controlled or monitored by the system. Points are either ‘soft’ or ‘hard’.

The actual output or input of a system is represented by a hard point, whereas the soft point is a result of different math and logic operations applied to other points.

These points are usually stored as timestamp-value pairs. Series of the timestamp-value pairs gives history of the particular point.

Storing additional metadata with the tags is common (these additional data can include comments on the design time, alarm information, path to the field device or the PLC register).

The HMI, or Human Machine Interface, is an apparatus that gives the processed data to the human operator. A human operator uses HMI to control processes.

The HMI is linked to the SCADA system’s databases, to provide the diagnostic data, management information and trending information such as logistic information, detailed schematics for a certain machine or sensor, maintenance procedures and troubleshooting guides.

The information provided by the HMI to the operating personnel is graphical, in the form of mimic diagrams.

This means the schematic representation of the plant that is being controlled is available to the operator.

For example, the picture of the pump that is connected to the pipe shows that this pump is running and it also shows the amount of fluid pumping through the pipe at the particular moment.

The pump can then be switched off by the operator. The software of the HMI shows the decrease in the flow rate of fluid in the pipe in the real time.

Mimic diagrams either consist of digital photographs of process equipment with animated symbols, or schematic symbols and line graphics that represent various process elements.

HMI package of the SCADA systems consist of a drawing program used by the system maintenance personnel or operators to change the representation of these points in the interface.

These representations can be as simple as on-screen traffic light that represents the state of the actual traffic light in the area, or complex, like the multi-projector display that represents the position of all the trains on railway or elevators in skyscraper.

SCADA systems are commonly used in alarm systems. The alarm has only two digital status points with values ALARM or NORMAL. When the requirements of the Alarm are met, the activation will start.

For example, when the fuel tank of a car is empty, the alarm is activated and the light signal is on. To alert the SCADA operators and  managers, text messages and emails are sent along with alarm activation.

SCADA system may have the components of the Distributed Control System. Execution of easy logic processes without involving the master computer is possible because ‘smart’ PLCs or RTUs.IEC61131-39(Ladder Logic) is used, (this is a functional block programming language, commonly used in creating programs running on PLCs and RTUs.)

IEC 61131-3 has very few training requirements, unlike procedural languages like FORTRAN and C programming language.

The SCADA system engineers can perform implementation and design of programs being executed on PLC or RTU. The compact controller, Programmable automation controller (PAC), combines the capabilities and features of a PC-based control system with a typical PLC.

’Distributed RTUs’, in various electrical substation SCADA applications, use station computers or information processors for communicating with PACs, protective relays, and other I/O devices.

Almost all big PLC manufacturers offer integrated HMI/SCADA systems, since 1998.

Many of them are using non-proprietary and open communication protocols. Many skilled third party HMI/SCADA packages have stepped into the market, offering in-built compatibility with several major PLCs, which allows electrical engineers, mechanical engineers or technicians to configure HMIs on their own, without requiring software-developer-written custom-made program.

The RTU is connected to the physical equipment. Often, the RTU converts all electrical signals coming from the equipment into digital values like the status- open/closed – from a valve or switch, or the measurements like flow, pressure, current or voltage.

By converting and sending the electrical signals to the equipment, RTU may control the equipment, like closing or opening a valve or a switch, or setting the speed of the pump.

A ‘supervisory Station’ refers to the software and servers responsible for communication with the field equipment (PLCs, RTUs etc), and after that, to HMI software running on the workstations in the control room, or somewhere else.

A master station can be composed of only one PC (in small SCADA systems). Master station can have multiple servers, disaster recovery sites and distributed software applications in larger SCADA systems.

For increasing the system integrity, multiple servers are occasionally configured in hot-standby or dual-redundant formation, providing monitoring and continuous control during server failures.

The costs resulting from control system failures are very high. Even lives may be lost. For a few SCADA systems, hardware is ruggedized, to withstand temperature, voltage and vibration extremes, and reliability is increased, in many critical installations, by including communications channels and redundant hardware.

A part which is failing can be identified and the functionality taken over automatically through backup hardware. It can be replaced without any interruption of the process.

SCADA systems initially used modem connections or combinations of direct and radio serial to meet communication requirements, even though IP and Ethernet over SONET/SDH can also be used at larger sites like power stations and railways. The monitoring function or remote management of the SCADA system is called telemetry.

SCADA protocols have been designed to be extremely compact and to send information to the master station only when the RTU is polled by the master station. Typically, the legacy of SCADA protocols consists of Conitel, Profibus, Modbus RTU and RP-570.

These protocols of communication are specifically SCADA-vendor. Standard protocols are IEC 61850, DNP3 and IEC 60870-5-101 or 104. These protocols are recognized and standardized by all big SCADA vendors. Several of these protocols have extensions for operating through the TCP/IP.

The development of many automatic controller devices and RTUs had started before the advent of industry standards for the interoperability.

For better communication between different software and hardware, PLE for Process Control is a widely accepted solution that allows communication between the devices that originally weren’t intended to be part of the industrial network.

In the first generation, mainframe systems were used for computing. At the time SCADA was developed, networks did not exist.

Therefore, the SCADA systems did not have any connectivity to other systems, meaning they were independent systems. Later on, RTU vendors designed the Wide Area Networks that helped in communication with RTU.

The usage of communication protocols at that time was proprietary. If the mainframe system failed, there was a back-up mainframe, connected at the bus level.

The information between multiple stations was shared in real time through LAN and the processing was distributed between various multiple stations.

The cost and size of the stations were reduced in comparison to the ones used in the first generation. The protocols used for the networks were still proprietary, which caused many security issues for SCADA systems.

Due to the proprietary nature of the protocols, very few people actually knew how secure the SCADA installation was.

Modern SCADA systems allow real-time data from the plant floor to be accessed from anywhere in the world. This access to real-time information allows governments, businesses, and individuals to make data-driven decisions about how to improve their processes. Without SCADA software, it would be extremely difficult if not impossible to gather sufficient data for consistently well-informed decisions.

Also, most modern SCADA designer applications have rapid application development (RAD) capabilities that allow users to design applications relatively easily, even if they don’t have extensive knowledge of software development.

The introduction of modern IT standards and practices such as SQL and web-based applications into SCADA software has greatly improved the efficiency, security, productivity, and reliability of SCADA systems.

SCADA software that utilizes the power of SQL databases provides huge advantages over antiquated SCADA software. One big advantage of using SQL databases with a SCADA system is that it makes it easier to integrate into existing MES and ERP systems, allowing data to flow seamlessly through an entire organization.

Historical data from a SCADA system can also be logged in a SQL database, which allows for easier data analysis through data trending.

The SCADA system used today belong to this generation. The communication between the system and the master station is done through the WAN protocols like the Internet Protocols (IP).

Since the standard protocols used and the networked SCADA systems can be accessed through the internet, the vulnerability of the system is increased.

However, the usage of security techniques and standard protocols means that security improvements can be applied in SCADA systems.

In the late 1990s instead of using the RS-485, manufacturers used open message structures like Modbus ASCII and Modbus RTU (both developed by Modicon). By 2000, almost all I O makers offered fully open interfacing like Modbus TCP instead of the IP and Ethernet.

SCADA systems are now in line with the standard networking technologies. The old proprietary standards are being replaced by the TCP/IP and Ethernet protocols. However, due to certain characteristics of frame-based network communication technology, Ethernet networks have been accepted by the majority of markets for HMI SCADA.

The ‘Next Generation’ protocols using XML web services and other modern web technologies, make themselves more IT supportable. A few examples of these protocols include Wonderware’s SuiteLink, GE Fanuc’s Proficy, I Gear’s Data Transport Utility, Rockwell Automation’s FactoryTalk and OPC-UA.

Some vendors have started offering application-specific SCADA systems that are hosted on remote platforms all over the Internet. Hence, there is no need to install systems at the user-end facility. Major concerns are related to the Internet connection reliability, security and latency.

The SCADA systems are becoming omnipresent day by day. However, there are still some security issues.

Security of SCADA-based systems is being questioned, as they are potential targets to cyberterrorism/cyberwarfare attacks.

There is an erroneous belief that SCADA networks are safe enough because they are secured physically. It is also wrongly believed that SCADA networks are safe enough because they are disconnected from the Internet.

SCADA systems also are used for monitoring and controlling physical processes, like distribution of water, traffic lights, electricity transmissions, gas transportation and oil pipelines and other systems used in the modern society. Security is extremely important because destruction of the systems would have very bad consequences.

There are two major threats. The first one is unauthorized access to software, be it human access or intentionally induced changes, virus infections or other problems that can affect the control host machine. The second threat is related to the packet access to network segments that host SCADA devices.

In numerous cases, there remains less or no security on actual packet control protocol; therefore, any person sending packets to SCADA device is in position to control it.

Often, SCADA users infer that VPN is sufficient protection, and remain oblivious to the fact that physical access to network switches and jacks related to SCADA provides the capacity to bypass the security on control software and control SCADA networks.

SCADA vendors are addressing these risks by developing specialized industrial VPN and firewall solutions for SCADA networks that are based on TCP/IP. Also, white-listing solutions have been implemented due to their ability to prevent unauthorized application changes.

A group of Hydro and Gas generation plants when the load demand exceeds the generating capacity, These plants are considered as peak load plants because these plants can start in no time and deliver power to the grid.

These plants are located in the romote locations. These plants are controlled by opening and closing the valves of turbines so that they can deliver the power in peak conditions and can be kept on standby during normal load conditions.

Many process control parameters, motors, pumps, valves are spread over the wide area in the field.

Control and monitoring applications include turning on and off motors, pumps, valves and gathering information of process parameters(like flow rate, pressure, temperature) continuously and taking certain decisions can be done through SCADA systems.

Pipelines carrying oil, gas, chemicals and water which are located at varying distances from the plant needs continuous monitoring and control.

Control includes opening and closing the valves, starting and stopping the pumps. Monitoring the flowrate and other parameters to avoid leakage in the pipelines by acquiring the data and carrying out suitable controls is done through SCADA systems.

Electrical power transmission which is spread over thousands of kilometers can be controlled by opening and closing the circuit breakers and other functions, This is done in master control substation which can control the other substations through SCADA systems.

Irrigation systems which are spread over wide area can be controlled by closing and opening the valves, gathering the meter values of amount of water supplied and taking the control actions can be done through SCADA systems.

Arcticle Source : Inst Tools

Image Source : Inst Tools

May 21, 2025

Deareator Working Principle, Types & Controls – The Engineering Concepts

maximios Engineering

Deaerators are normally used in any Chemical Process Industry or in Power Plants where boiler is employed for steam production from boiler feed water.  Deaerator solves the purpose of removal of unwanted dissolved gases and dissolved oxygen from the boiler feed water before entering into boilers. Most of the deaerators are designed in such a way that the dissolved oxygen content in the outlet water is about 7 ppb by wt%

Dearator normally works based on the following principles.

Henrys Law

The solubility of the gas in a liquid is directly proportional to the partial pressure. Therefore if we decrease the partial pressure of the dissolved gas by adding steam in Deaerator, its solubility decreases and the gas is removed from water.

When the temperature of water is increased, the dissolved oxygen content in the water is decreases. Therefore the water temperature is increased by adding steam in Deaerator, the dissolved gas solubility is decreased and the gases are removed from water.

Types of Deaerators

Tray type Deaerator

1) Tray Type Deareator

Tray type deaerators contain perforated trays in the top of the Deaeration section. The bottom section acts as storage for boiler feed water. Feed water to deaerator enters into the perforated trays where the surface area and residence time is increased to contact with steam. Then the water goes to the horizontal storage section where steam is passed in sparger pipe to remove the remaining traces of dissolved gases and keep the stored water at its saturation temperature.

Spray Type Deaerator

Spray type deaerator contains spray nozzle in feed water entry area. It is then preheated and deaerated and sent to storage section. In storage section also steam is added to keep the water at its saturation temperature.

Process Control system in Deaerator

Steam Pressure Control

Deaerator uses Low pressure steam from the process plant at a pressure range between 0.5 to 1.5 bar. The low pressure steam sources may be any one of the following: Extraction from back pressure turbines, Flash steam recovered from Boiler blow down or Letdown steam from High pressure steam header through pressure reducing valve. Steam pressure inside the deaerator has to be maintained to facilitate the removal of dissolved gases from water and also to provide adequate NPSH to boiler feed water pump. Deaerators are normally installed at high elevation in order to provide enough NPSH in the event of failure in steam pressure control also. Pressure Relief valve is also fitted to avoid pressurization of deaerator due to malfunctioning of pressure control valve.

Water Level Control

Main sources of water to deaerator are Treated water from water treatment plant and steam condensate from the condensing type turbines. During the stable plant operation the water balance is maintained and during any upset in the above said sources water level fluctuates and control is essential. High level and low level alarms are provided. Low level may lead to starvation of feed water in Centrifugal Pump and High level leads to water entry into steam header. Therefore overflow drain is installed to drain the water if very high level is reached.

Other Advantages of Deaerator

Dearator acts as an additional storage device which provides reserve quantity of boiler feed water during upstream water supply failure for momentary periods normally for about 20 minutes.

In some of the Plants, Deaerator is also used for dosing oxygen scavenging chemicals like Hydrazine or Hydroquinone.

Chemical Engineering Site

Video Source : POWER PLANT GURU

Also Read:

Venturi Flow Meter

Pitot Tube 

Coriolis Mass Flow Meter

Design of Centrifugal Pump

Valve & Its Types

Cavitation

Piping and Instrumentation Diagram – P&ID

Refrence Books :

Practical Boiler Operation Engineering and Power Plant

Boiler Operators Handbook 

Boiler Operators Handbook

May 21, 2025

The Engineering Concepts – Page 8 of 21 – Learn All Your Chemical & Mechanical Engineering Concepts

maximios Engineering

Sulphuric Acid, also known as Vitriol…

Pump Sign Symbols Few more schematic…

Basic Process of Cement Manufacturing Cement…

Urea was first produced industrially by…

Flow sheet of production of ethylene…

Also Read Another Content: What is…

Gear Pump : What is Gear…

Cooling Tower : What is Cooling…

Chemical reactors The reactors, in which…

May 21, 2025

All Objective Questions – The Engineering Concepts

maximios Engineering

Here, you can read all important objective aptitude questions and answers for your interview and entrance exams preparation.

Engineering

  • Chemical Engineering
  • Mechanical Engineering
  • Civil Engineering
  • ECE, EEE, CSE

Verbal and Reasoning

  • Verbal Ability
  • Logical Reasoning
  • Verbal Reasoning
  • Non Verbal Reasoning

Current Affairs & GK

  • Current Affairs
  • Basic General Knowledge
  • General Science
  • Inventions
  • World Geography

Medical / Science

  • Microbiology
  • Biochemistry
  • Biotechnology
  • Biochemical Engineering

General Aptitude

  • Arithmetic Aptitude
  • Data Interpretation
  • Online Aptitude Test
  • Data Interpretation Test

Interview

  • Placement Papers
  • Group Discussion
  • HR Interview
  • Technical Interview
  • Body Language     

May 21, 2025

The Engineering Concepts – Page 3 of 21 – Learn All Your Chemical & Mechanical Engineering Concepts

maximios Engineering

Thermowell Thermowell is a cylindrical fitting…

Distillation: Distillation columns work on the…

Pump: Pump is a most commonly…

What is Coking Process in Refinery?…

What is MES? MES is often…

Thermosyphon Reboiler A reboiler is nothing…

Compressor : A Compressor  is one…

There are many names for ejectors…

Aricle written By : Pallavi Wankhede…

Aricle written By : Pallavi Wankhede…

May 21, 2025

Thermodynamic Cycle – The Engineering Concepts

maximios Engineering

The Thermodynamic cycle is a system which involves sequential thermodynamic processes, transfer of heat, work expansion or compression during varying pressure, temperature and other state variable and at the end, the system comes to its initial state.

Aricle written By : Pallavi Wankhede

During the cycle, the various types of thermodynamic processes involved are:

  1. Adiabatic: there is no energy transfer outside the system.
  2. Isothermal: the temperature remains constant where the reaction takes place in a cycle.
  3. Isobaric: the pressure remains constant in a cycle where the reaction takes place.
  4. Isochoric: reaction takes place at constant volume in a cycle.
  5. Isentropic: the entropy remains constant in a part of the cycle where the reaction takes place.
  6. Isenthalpic: the enthalpy or change in enthalpy remains constant where the reaction takes place.
  7. Polytropic: It involves multiple expansion and compression processes during heat transfer.
  8. Reversible: the entropy production is zero.

The thermodynamic cycle is primarily divided into two main cycles, power cycles and heat pump cycles, Where Power cycle convert heat input into mechanical work output, while heat cycle transfer heat from low temperature to high temperatures with the help of input as the mechanical work.

Thermodynamic Power Cycles are used to model the various types of heat engines. The cycle has two parts internal combustion engines and external combustion engines.

The internal combustion engine involves the Otto cycle and diesel cycle.

1. Otto Cycle: This cycle is used to model the gasoline engine. It also describes the function of a typical spark ignition piston engine. It involves the changes in the mass of gas with respect to change in pressure, temperature, volume, the addition of heat, and the removal of heat. The mass of gas is usually fluid within the cylinder and it is also called a system in this cycle. It considers both the changes, the changes in the system due to thermodynamic properties and the changes on the environment due to the system’s effect. The Otto cycle describes how much effect needs to be produced to get enough work from the system that needs to propel an automobile and its respected holder.

The sequence of operation for the Otto cycle is:

Part 1-2: isentropic

Part 2-3: isochoric

Part 3-4: isentropic

Part 4-1: isochoric

t-s-diagram-for-otto-cycle-1937402 Figure 1 : T-S Diagram for Otto Cycle

2. Diesel Cycle: This cycle is used to model the diesel engine. The diesel cycle is in complete contrast to the Otto cycle. It describes the combustion process of a reciprocating internal combustion engine. The fuel is ignited with the help of heat generated during the compression of air in the combustion chamber where then fuel is injected. The Diesel engine is used in aircraft, automobiles, power generation, diesel-electric locomotives and both surfaces of ships and submarines.

The sequence of operation for the diesel cycle is:

Part 1-2: Adiabatic

Part 2-3: Isobaric

Part 3-4: Adiabatic

Part 4-1: Isochoric

Figure 2 : TS and PV Diagram for Diesel Cycle

3. Dual Cycle: This cycle is a combination of two cycles, the Otto cycle, and the diesel cycle. It involves the addition of heat partly at the isochoric and isobaric reaction. This gives more time to fuel for complete combustion. This cycle is used only for diesel and hot spot engines due to the lagging characteristics of fuel.

The sequence of operation for the dual cycle is:

Part 1-2: Isentropic Compression

Part 2-3: Addition of heat at Constant Volume

Part 3-4: Isentropic expansion

Part 4-5: Rejection of heat at constant volume

Part 5-1: Isochoric

Figure 3 : T-S Diagram of Dual Cycle

4. Atkinson Cycle: It is a type of internal combustion engine. The cycle is designed to provide efficiency at the expense of power density. Its application has been used in modern automobiles such as hybrid electric cars, Toyota Prius. Analysis in the Atkinson cycle gives the idea of a good economy for the engine.

The sequence of operation for the Atkinson cycle is:

Part 1-2: Isentropic (adiabatic compression)

Part 2-3: Isochoric heating

Part 3-4: Isobaric heating

Part 4-5: Isentropic Expansion

Part 5-6: Isochoric cooling

Part 6-1: Isobaric Cooling

Figure 4 : PV diagram for Atkinson Cycle Figure 5 : PV and TS diagram for Atkinson Cycle

The external combustion engine involves the Brayton cycle, Rankine cycle, Stirling cycle, and Ericsson cycle.

5. Brayton Cycle: This cycle is used to model the gas turbines and jet engines. It describes the working of a constant pressure heat engine. The engine formed with the help of Brayton cycle is also called a Brayton engine which uses piston compressor and piston expander. This cycle is usually run as an open system, while exhaust gases are further reused in the intake and enabling the analysis of a closed system. On the other hand, Brayton cycle is open to atmosphere and used in IC (internal combustion) chamber and a closed type cycle is used in heat exchanger.

The sequence of operation for Brayton cycle is:

Part 1-2: Adiabatic (compression)

Part 2-3: Isobaric (heat addition)

Part 3-4: Adiabatic (expansion)

Part 4-1: Isobaric (heat rejection)

Figure 6 : P-V and T-S Diagram for Brayton Cycle

6. Rankine Cycle: This cycle is used to model the steam turbines. It is also used to study the performance of the reciprocating systems. This is an idealized thermodynamic cycle of heat engine that converts heat into mechanical work during phase change reaction where friction losses are neglected. The heat is supplied externally to a closed loop of a cycle, where water is used as a working fluid. The Rankine cycle is mostly found in the thermal power generation plants which generate the power.

The sequence of operation for the Rankine cycle is:

Part 1-2: Adiabatic

Part 2-3: Isobaric

Part 3-4: Adiabatic

Part 4-1: Isobaric

steam-turbine-pv-and-ts-diagram-for-rankine-cycle-5453785 Figure 7 : Steam Turbine PV and TS Diagram for Rankine Cycle

7. Ericsson Cycle: This cycle is used to model the hot air engines. Ericsson engine is based on this cycle; the engine is also known as an external combustion engine as it is heated externally. The Ericsson engine has a regenerator between the compressor and expander to improve efficiency. The cycle can be run in an open or closed cycle. The expansion takes place simultaneously with compression, on the opposite side of the piston.

The sequence of operation for the Ericsson cycle is:

Part 1-2: Isothermal

Part 2-3: Isobaric

Part 3-4: Isothermal

Part 4-1: Isobaric

Figure 8 : PV and TS Ericsson Cycle

8. Stirling Cycle: This cycle is used to model hot air engines. The cycle is reversible which states that if it is supplied with mechanical power, it can work as a heat pump for heating or cooling and for cryogenic cooling as well. It is also called a closed regenerative cycle with a working fluid as gas.

The sequence of operation for the Stirling cycle is:

Part 1-2: Isothermal

Part 2-3: Isochoric

Part 3-4: Isothermal

Part 4-1: Isochoric

Figure 9 : PV and T-S Diagram for Stirling Cycle

The heat pump cycle involves Carnot Cycle.

9. Carnot Cycle (Ideal Cycle): This cycle is used to model the Carnot heat engine. This is an ideal cycle that provides an upper limit on the efficiency that any classical thermodynamic engine can achieve during the conversion of heat into work, or conversely the efficiency of a refrigeration system in creating a temperature difference by the application of work to the system.

The sequence of operation for the Carnot cycle is:

Part 1-2: Isothermal Expansion

Part 2-3: Isentropic Expansion

Part 3-4: Isothermal Compression

Part 4-1: Isentropic Compression

Figure 10 : PV and TS Diagram for Carnot Cycle

Content Source:

https://en.wikipedia.org/; https://chem.libretexts.org/;

Image Source:

https://en.wikipedia.org/; http://web.mit.edu/; https://www.sciencedirect.com/; https://www.electrical4u.com/; https://www.mechanicaltutorial.com/;

Also Read:

Thermosyphon Reboiler

Piping and Instrumentation Diagram – P&ID

How to choose betwwen PLC and DCS systems for process industries ?

Cement Manufacturing Process

Vinyl Chloride from Ethylene

Cooling Tower

Psychrometric Chart

What is Boiler ?

Venturi Flow Meter

Pitot Tube 

Coriolis Mass Flow Meter

RECIPROCATING PUMP

Design of Centrifugal Pump

Valve & Its Types

Cavitation

P&ID Symbols and Notation

What is the Difference Between HMI and SCADA?

What is SCADA ? How does SCADA Works?

What is Programmable Logic Controller / PLC ?

What is Distributed Control Systems (DCS) ?

Heat Exchanger Temperature Control

What is Compressor Surge ?

Ejectors & Its Working Principle 

Desuperheater

Three Phase Seperator

May 21, 2025

Difference between Boiling & Evaporation. – The Engineering Concepts

maximios Engineering

In common; both boiling and evaporation is the process in which liquid is getting converted into gas (vapor). Both the processes are direct function of temperature & pressure.

Boiling Vs Evaporation

Boiling and evaporation is the process of a liquid becoming a vapor. This process is highly dependent on temperature. The higher the temperature of the liquid, the faster is the rate of evaporation. The maximum temperature at which (vapor pressure of the liquid is equal to the surrounding atmospheric pressure) a liquid changes into a vapor is called the boiling point. 

Figure 1 : Phase Change Diagram

In general boiling and evaporation is a highly confusing terms. Many times persons gets confused between both terms. Hence in this article let’s clear the difference between both of the terms.

Boiling :

  • It’s a bulk phenomenon. It takes place throughout the liquid.
  • Here the conversion of liquid to vapor takes place at the boiling point (at specific temperature and pressure).
  • Its a rapid process.
  • Boiling occurs when vapor pressure of the liquid is equal to the surrounding atmospheric pressure.
  • Boiling is a dynamic equilibrium condition at which both; the rate of vaporization is equal to rate of condensation.
  • Here bubbles of vapor forms in the liquid.
  • During boiling liquid temperature remains constant throughout the liquid.
  • Here in boiling rate of evaporation is independent of ambient Air RH (Relative Humidity).
  • It’s a surface phenomenon and doesn’t happen in a bulk.
  • Here the conversion of liquid to vapor takes place below the boiling point. No specific temperature is needed for this, as it can occur on any temperature.
  • Its a slow process.
  • In case of evaporation as the vapor pressure increases evaporation occurs (at any temperature). Here the vapor pressure of the liquid is a fraction of the overhead pressure.
  • Here no bubble forms / exists over the surface.
  • Liquid temperature drops during evaporation.
  • Rate of evaporation is a function of Ambient Air RH. As the RH of ambient air decreases evaporation decreases.

ImageSource : Wikipedia

Also Read:

Piping and Instrumentation Diagram – P&ID

How to choose betwwen PLC and DCS systems for process industries ?

Cement Manufacturing Process

Vinyl Chloride from Ethylene

Cooling Tower

Psychrometric Chart

What is Boiler ?

Venturi Flow Meter

Pitot Tube 

Coriolis Mass Flow Meter

RECIPROCATING PUMP

Design of Centrifugal Pump

Valve & Its Types

Cavitation

P&ID Symbols and Notation

What is the Difference Between HMI and SCADA?

What is SCADA ? How does SCADA Works?

What is Programmable Logic Controller / PLC ?

What is Distributed Control Systems (DCS) ?

Heat Exchanger Temperature Control

May 21, 2025

Fluid Coking and Flexi Coking – The Engineering Concepts

maximios Engineering

Aricle written By : Pramod Yadav

The crude oil after being processed through physical separation processes especially Vacuum Distillation Unit (VDU)  is left with heavier residual fuel oils in the bottom of a distillation unit which are undesirable for any refining unit.

Coking involves conversion of these heavier fractions into solid coke and lower boiling point hydrocarbons, generally liquid , using various thermal and chemical processes.

Also Read : Heat Exchanger Design

The liquid fractions so produced is highly olefinic and aromatic as well as contain high sulfur content.These liquid products can prove to be a feedstock for other refinery units by converting into a high value fuel using reforming , desalting ,hydrodesulfurization (HDS),etc. 

Coking is a carbon rejection process of converting heavier residues ,rich in sulfur content, at the bottom of VDU into lower molecular fractions like gases, naptha,  Light gas oil (LGO ) and heavy gas oil (HGO ) and solid product Petroleum Coke or Pet Coke (Carbon).

The sulfur content in the products from coking is relatively lower than the feed because much of the sulfur remains in the pet coke.

These conversions are processed in units known as Coking Drums or Coker.

Also Read : What is Pump Head and Shut-off Head ?

Important : Generally Coking is carried out at  high pressure and high temperature as high pressure allows decomposition of heavier hydrocarbons into lighter ones like naptha, gases , LGO (Light Gas Oil) etc. in contrast to VDUs where operation is carried out at very low pressure due to which Atmospheric Distillation Unit (ADU)  residue does not decompose, and therefore we get LGOs and HGOs along with vacuum residue as products from VDU.

There are various types of coking processes depending upon the product requirements and feed properties :

  1. Flexi-Coking and Fluid Coking
  2. Delayed Coking 
  3. Visbreaking

In this article ,we are going to discuss fluid coking and flexi-coking processes.

Flexi-Coking Process Diagram  (Image Credit: Springer Link)

Flexi coking is one of the most important processes in a refinery as only 2% of  coke is produced from the residue.

In Flexi-Coking process, feed after preheated to 315-350oC enters into the reactor fluid bed of hot coke  at a temperature of 510-540oC .The hot coke is recycled from the heater at a rate enough to maintain the desired temperature. This recycled coke from the heater provides the heat of evaporation and sensible heat to the feed and enables the cracking process. Vapors and lighter fractions are obtained at the upper end which are passed through separators to separate the coke particles from the products and somee high boiling cracked vapors are condensed and recycled to the feed.

The coke produced is deposited as thin films in the bottom of the reactor bed and is stripped off with steam.

Also Read : Design of Cooling Tower

The coke stripped off at bottom is sent to the heater where it is heated at around 590oCand the hot coke is sent back to the reactor and the excess coke ,also known as purge coke, is withdrawn at the bottom of the heater. The gases at top of the heater are sent to tertiary cyclones and venturi scrubbers to separate out fine coke particles and then it is treated to remove the sulfur content.

The coke then moves to gasifier where it reacts with steam and air to produce a fuel gas consisting  of H2,N2,CO and CO2  .This gas from the top of the gasifier is sent back to the bottom of the heater to fluidize the heater bed and provide necessary heating to the coke and send it back to the reactor.

Thus, it can be concluded that the major part of coke is used to heat the feed with the help of a gasifier which produces fuel gas which heats the coke in the heater.

Also, the main purpose of the heater is to transfer the heat from the gasifier back to the reactor bed.

b) Fluid Coking :

Image Credit : Vidya-mitra

It is a much simpler version of flexi-coking process consisting of a reactor bed and a burner.It does not consist of a gasifier.

In fluid coking, feed is first preheated to 260oC and then sent to a scrubber unit located above the reactor bed for recovering fine particles of coke from overhead vapours.The fine particles are recycled with heavy compounds and are entered into the reactor bed and the coking process takes place.

The lighter products from the reactor are withdrawn as overhead vapours and the remaining coke at the bottom is separated continuously . 

The cold coke at the bottom of the reactor is fed into the burner in a layering manner , and a scrubber is also present there to scrub any heavier hydrocarbons on coke, where it is fluidized with the help of steam. Some part of coke (15-30%) is sent to burner for combustion along with injected air and the coke is heated up and the rest is separated out.

The hot coke is sent back to the reactor bed and combustion of coke in the burner produces flue gases of lower calorific value which is processed with the help of separators,scrubbers etc. and can be used in steam generation , power generation etc.

The pet coke so obtained out of burner is used as cement industry fuel and partial oxidation feed.

So, it can be analyzed that both fluid and flexi-coking processes involve separation of lighter materials from the VDU residue and reduction of coke as plenty of coke is used in heating up the coke. Therefore, much of the residue is converted to fuel gases during combustion to heat up the coke and lighter fractions at the top of reactor bed  and the remaining is left up as pet coke.Also,the amount of coke left in case of flexi-coking is less than that of fluid coking.

ImageSource : John A. Dutton e-education Institute

1 2 3 4›»

Recent Posts

  • Top 10 people who changed the whole world – The Engineering Concepts
  • P&ID Symbols and Notation – By TheEngineeringConcepts.com
  • What is SCADA ? How does SCADA Works? – The Engineering Concepts
  • Deareator Working Principle, Types & Controls – The Engineering Concepts
  • The Engineering Concepts – Page 8 of 21 – Learn All Your Chemical & Mechanical Engineering Concepts

Recent Comments

No comments to show.

Archives

  • May 2025
  • April 2025
  • March 2025
  • February 2025
  • January 2025
  • December 2024
  • November 2024
  • September 2024
  • June 2024
  • May 2024
  • April 2024
  • June 2023
  • March 2023
  • December 2022
  • September 2022
  • August 2022
  • July 2022
  • October 2021
  • May 2021
  • January 2021
  • November 2020
  • October 2020
  • September 2020
  • August 2020
  • June 2020
  • July 2018
  • June 2018

Categories

  • Engineering

Back to Top

© aupschool.org 2025
Powered by WordPress • Themify WordPress Themes