Hazardous areas can contain flammable gases, vapors, or dusts that could cause fires or explosions. These areas are classified based on the type of hazard and likelihood of a hazardous atmosphere being present. The Class/Division system used in North America categorizes areas based on whether hazardous materials are likely to be present continuously or occasionally. The international Zone system defines three zones based on the probability and duration of hazardous atmospheres. Equipment used in hazardous areas must use explosion-proof techniques to prevent ignition, such as flame-proofing or intrinsic safety.
Hazardous area classification and Elecrtical, Instrument and Process Engineer...Kathiresan Nadar
This presentation explains the Hazardous gas Classification and area Classification, and the responsibility of Electrical, Instrument and Process Engineer Responsibility.
Hazardous Area Location Presentation
• What is a Hazardous Location?
• What causes an explosion?
• Potential ignition sources
• Protection concepts 101
• Classification Schemes (ATEX/IEC vs. NEC)
• Designing/Certification for HazLoc
Ex D, Ex E, Ex DE, Ex ED, Ex np, Ex I
Hazardous area classification and Elecrtical, Instrument and Process Engineer...Kathiresan Nadar
This presentation explains the Hazardous gas Classification and area Classification, and the responsibility of Electrical, Instrument and Process Engineer Responsibility.
Hazardous Area Location Presentation
• What is a Hazardous Location?
• What causes an explosion?
• Potential ignition sources
• Protection concepts 101
• Classification Schemes (ATEX/IEC vs. NEC)
• Designing/Certification for HazLoc
Ex D, Ex E, Ex DE, Ex ED, Ex np, Ex I
Hazardous area module- Zones, Method of Determination of Hazardous area Radiu...Aniruddha Kulkarni
The explosion properties of our fuel like gasses, vapors, combustible dusts have been studied and organized by their flammability limits and ignition temp etc in order to suitably assess the potential of an explosion and to take appropriate preventative measures to avoid an explosion.
Hazardous location protection methods e book by pepperl+ fuchsKristen_Barbour_PF
Hazardous Location Protection Methods Explained.
By definition, a hazardous (classified) location is an area in an industrial complex where the atmosphere contains flammable concentrations of gases or vapors by leakage, or ignitable concentrations of dust or fibers by suspension or dispersion.
The treatment of dangerous substances, where the risk of explosion or fire exists that can be caused by an electrical spark, arc, or hot temperatures, requires specifically defined instrumentation located in a hazardous location. It also requires that interfacing signals coming from a hazardous location be unable to create the necessary conditions to ignite and propagate an explosion.
Fundamental training on Fire Detection & Alarm SystemSabrul Jamil
This is a basic training on Fire Detection and Alarm System, created to give my colleagues from non-engineering divisions a comprehensive brief on the system. This is most suitable for individuals with little or no technical knowledge. This training introduces the devices and the system in a whole, not how to design it.
Hazardous area module- Zones, Method of Determination of Hazardous area Radiu...Aniruddha Kulkarni
The explosion properties of our fuel like gasses, vapors, combustible dusts have been studied and organized by their flammability limits and ignition temp etc in order to suitably assess the potential of an explosion and to take appropriate preventative measures to avoid an explosion.
Hazardous location protection methods e book by pepperl+ fuchsKristen_Barbour_PF
Hazardous Location Protection Methods Explained.
By definition, a hazardous (classified) location is an area in an industrial complex where the atmosphere contains flammable concentrations of gases or vapors by leakage, or ignitable concentrations of dust or fibers by suspension or dispersion.
The treatment of dangerous substances, where the risk of explosion or fire exists that can be caused by an electrical spark, arc, or hot temperatures, requires specifically defined instrumentation located in a hazardous location. It also requires that interfacing signals coming from a hazardous location be unable to create the necessary conditions to ignite and propagate an explosion.
Fundamental training on Fire Detection & Alarm SystemSabrul Jamil
This is a basic training on Fire Detection and Alarm System, created to give my colleagues from non-engineering divisions a comprehensive brief on the system. This is most suitable for individuals with little or no technical knowledge. This training introduces the devices and the system in a whole, not how to design it.
Learn more on hazardous locations illustrated, ATEX and IECEx zonesAMETEK STC
Overview of the different zones in gas stations or dry/powder storage such as grain silos. Learn the similarities of the safety certifications, the explanations are based on level measurement
Dated 2/2/2009 - Overview for the kinds of industries where Combustible Dust Hazards are an issue. Also, recommendations for prevention and mitigation along with how to test to see if a specific manufacturing facility has a problem with either their raw ingredients, byproducts/scrap, and/or finished goods.
Also available going to following url:
http://sache.org/links.asp
Albert V. Condello III
Univ of Houston Downtown
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.
Explore the innovative world of trenchless pipe repair with our comprehensive guide, "The Benefits and Techniques of Trenchless Pipe Repair." This document delves into the modern methods of repairing underground pipes without the need for extensive excavation, highlighting the numerous advantages and the latest techniques used in the industry.
Learn about the cost savings, reduced environmental impact, and minimal disruption associated with trenchless technology. Discover detailed explanations of popular techniques such as pipe bursting, cured-in-place pipe (CIPP) lining, and directional drilling. Understand how these methods can be applied to various types of infrastructure, from residential plumbing to large-scale municipal systems.
Ideal for homeowners, contractors, engineers, and anyone interested in modern plumbing solutions, this guide provides valuable insights into why trenchless pipe repair is becoming the preferred choice for pipe rehabilitation. Stay informed about the latest advancements and best practices in the field.
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.
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/
Immunizing Image Classifiers Against Localized Adversary Attacksgerogepatton
This paper addresses the vulnerability of deep learning models, particularly convolutional neural networks
(CNN)s, to adversarial attacks and presents a proactive training technique designed to counter them. We
introduce a novel volumization algorithm, which transforms 2D images into 3D volumetric representations.
When combined with 3D convolution and deep curriculum learning optimization (CLO), itsignificantly improves
the immunity of models against localized universal attacks by up to 40%. We evaluate our proposed approach
using contemporary CNN architectures and the modified Canadian Institute for Advanced Research (CIFAR-10
and CIFAR-100) and ImageNet Large Scale Visual Recognition Challenge (ILSVRC12) datasets, showcasing
accuracy improvements over previous techniques. The results indicate that the combination of the volumetric
input and curriculum learning holds significant promise for mitigating adversarial attacks without necessitating
adversary training.
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.
2. Hazardous Areas
A “Hazardous area” can be
defined as an area or location where
the atmosphere contains, or may
contain the quantities of flammable
or explosive gases, dusts or
vapours. In such an atmosphere a
fire or explosion is possible.
3. Classification of Hazardous area
• Presently there are two systems
used for classification of these
hazardous areas;
– The Class/Division system,
– The Zone system
• The Class/Division system is used in
the United States and Canada,
whereas the rest of the world
generally uses the Zone system.
Referred Std - BS EN 60079/10; BS EN 61241/3
4. Classification
• Class I—Locations in which
flammable gases or vapors
may or may not be in
sufficient quantities to produce
explosive or ignitable
mixtures.
• Class II—Locations in which
combustible dusts (either in
suspension, intermittently, or
periodically) may or may not
be in sufficient quantities to
produce explosive or ignitable
mixtures.
• Class III—Locations in which
ignitable fibers may or may
not be in sufficient quantities
to produce explosive or
ignitable mixtures
• Division 1 - indicates that the
hazardous material has a high
probability of producing an
explosive or ignitable mixture
due to it being present
continuously, intermittently, or
Periodically or from the
equipment itself under normal
operating conditions.
• Division 2 - indicates that the
hazardous material has a low
probability of producing an
explosive or ignitable mixture
and is present only during
abnormal conditions for a short
period of time.
5. Group-The Group defines the type of hazardous material in the
surrounding atmosphere.
– Group A—Atmospheres containing acetylene.
– Group B—Atmospheres containing a flammable gas, flammable liquid-produced vapor,
or combustible liquid-produced vapor whose MESG is less than 0.45 mm or MIC ratio is
less than 0.40. Typical gases include hydrogen, butadiene, ethylene oxide, propylene
oxide, and acrolein
– Group C—Atmospheres containing a flammable gas, flammable liquid-produced vapor,
or combustible liquid-produced vapor whose MESG is greater than 0.45 mm but less
than 0.75 mm or MIC ratio is greater than 0.40 but less than 0.80. Typical gases
include ethyl either, ethylene, acetaldehyde, and cyclopropane.
– Group D—Atmospheres containing a flammable gas, flammable liquid-produced vapor,
or combustible liquid-produced vapor whose MESE is greater than 0.75 mm or MIC
ration is greater than 0.80. Typical gases include acetone, ammonia, benzene, butane,
ethanol, gasoline, methane, natural gas, naphtha, and propane.
– Group E—Atmospheres containing combustible metal dusts such as aluminum,
magnesium, and their commercial alloys.
– Group F—Atmospheres containing combustible carbonaceous dusts with 8% or more
trapped volatiles such as carbon black, coal, or coke dust.
– Group G—Atmospheres containing combustible dusts not included in Group E or Group
F. Typical dusts include flour, starch, grain, wood, plastic, and chemicals
6. Zone System
Zone—The Zone defines the probability of the hazardous material, gas or dust, being
present in sufficient quantities to produce explosive or ignitable mixtures.
Gas
Zone 0—Ignitable
concentrations of flammable
gases or vapors which are
present continuously or for long
periods of time.
Zone 1—Ignitable
concentrations of flammable
gases or vapors which are likely
to occur under normal operating
conditions.
Zone 2—Ignitable
concentrations of flammable
gases or vapors which are not
likely to occur under normal
operating conditions and do so
only for a short period of time.
Dust
Zone 20—An area where
combustible dusts or ignitable
fibers and flyings are present
continuously or for long periods
of time.
Zone 21—An area where
combustible dusts or ignitable
fibers and flyings are likely to
occur under normal operating
conditions.
Zone 22—An area where
combustible dusts or ignitable
fibers and flyings are not likely to
occur under normal operating
conditions and do so only for a
short period of time.
7. Group I
Equipment used
in mines with
atmospheres
containing
methane or
gases and vapors
of equivalent
hazard
Group II
IIA - Atmospheres containing
propane, or gases and
vapors of equivalent hazard.
IIB -Atmospheres containing
ethylene, or gases and
vapors of equivalent hazard.
IIC - Atmospheres
containing acetylene or
hydrogen, or gases and
vapors of equivalent hazard.
Sub Division of Gas Group
8. Temperature Code (T Code)
A mixture of hazardous gases and air may be ignited by
coming into contact with a hot surface. The conditions under
which a hot surface will ignite a gas depends on surface area,
temperature, and the concentration of the gas. The same can
be said about combustible dusts.
Group II Temperature Class
T Code Maximum Surface Temperature Ignition temperature
T1 450 0C > 450 0C
T2 300 0C > 3000C ≤ 450 0C
T3 200 0C > 200 0C ≤ 300 0C
T4 130 0C > 130 0C ≤ 200 0C
T5 100 0C > 100 0C ≤ 135 0C
T6 85 0C > 85 0C ≤ 100 0C
The T code of a product denotes the maximum surface temperature that
a given product will not exceed under a specified ambient temperature.
For example, a product with a T code of T3 means that its maximum
surface temperature will not exceed 2000C provided it is operated in a
ambient temperature defined by the manufacturer
9. Protection Techniques and Methods
• Class/Division system
– Explosion-proof
– Intrinsically Safe
– Dust Ignition-proof
• Zone system
– Flame-proof
– Intrinsically Safe
10. Gas Dust Hazardous Area Characteristics
Zone 0 Zone 20
A hazardous atmosphere is highly likely
to be present and may be present for
long periods of time (>1000 hours per
year) or even continuously
Zone 1 Zone 21
A hazardous atmosphere is possible but
unlikely to be present for long periods
of time (>10 <1000 hours per year
Zone 2 Zone 22
A hazardous atmosphere is not likely to
be present in normal operation or
infrequently and for short periods of
time (<10 hours per year)
Hazardous Area Characteristics