Safety Instrumented Systems
Instrumented Protective Functions and Emergency Shutdown (ESD) and Process Shutdown (PSD) Systems
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Have
a question on or need to purchase quality Safety Instrumented Systems? Our
Sponsors Triconex are Experts in this area! Invensys is the only automation company with the experience and track record in Safety and Critical Control as demonstrated by its 27 years of experience in safety systems, in excess of 8,000 installed systems, the only approved Nuclear Regulatory Commission Commercial Off-The-Shelf controller for Nuclear 1E Applications, large number of TÜV Certified Functional Safety Engineers deployed worldwide and patented TMR technology. Invensys' safety and critical control Tricon™ and Trident™ platforms have the ability to provide a wide variety of critical applications including Emergency Shutdown, NFPA85 certified for Burner Management, NFPA72 and EN54 certified for Fire and Gas and Turbomachinery Control and Protection Systems. Triconex Systems have been installed on many Onshore / Offshore Oil and Gas Facilities and Power Industries. |
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Tricon
- The Tricon is a State-of -the-Art Fault Tolerant Controller based on a
Triple-Modular Redundant (TMR) Architecture - It was the first
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system. The system uses two-out-of-three voting to provide high integrity,
error-free, uninterrupted process operation with no single point of failure. For
details on key benefits and capabilities click
here.
Trident
- Based on proven Triconex Triple Modular Redundant (TMR) technology, Trident is
designed to fit small applications where, until now, price concerns had kept
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Trident breaks through the budget barrier and provides customers with a
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on applications, key benefits and capabilities click
here.
SIS Articles, Technical Papers, Multimedia and Applications from Triconex
The Hidden Costs of Successful Safety
- Luis Duran - This article describes many of the hidden costs
and side effects associated with safety instrumented systems (SISs), especially
those embedded with distributed control systems (DCSs). It covers some of the
safety-related questions users need to ask their DCS vendors, even though many
suppliers don’t want to answer them. Thanks to www.controlglobal.com
Ten
Truths of Safety Instrumented Systems - Selection and
design of safety systems is not trivial, and it never has been. Operating
companies in the process industries must face compliance with new safety
standards such as IEC61508 and IEC61511, while implementing safeguards that
provide asset protection without disrupting asset utilization or compromising
production targets. What are the fundamental selection criteria for safety and
critical control equipment? What key principles must be clarified in order to
ensure successful selection and implementation of the system?
When
a SIL Rating is not Enough - Robin McCrea-Steele, TÜV
FSExp Invensys-Premier Consulting Services - SIL rating is a measure of the risk
reduction capability and probability of failure-on-demand. It measures only the
"Fail Safe" nature of the device and should not be the primary or sole
measurement considered when selecting a safety system.
Quality
of a SIS has a Direct Impact on Plant Performance -
Quality isn't always implemented the same way by every company. Quality
Assurance procedures differ between vendors, regardless of product compliance
with safety standards and certifications. Nevertheless, a vendor must make sure
that their SIS performs to the intended specification.
Many
Companies will sell you a Safety System, but few are able to Address Your Specific
Needs - Operating companies in the process industries
that are pursuing regulatory compliance represent tremendous potential for any
manufacturer that offers some form of process control technology or automation.
Many such manufacturers are scrambling to ensure their products offer some level
of compliance for use in safety applications. Unfortunately, while most of these
"new" products offer solutions for the fail safe side, only a few of
them can address the need for safety and process uptime simultaneously.
IEC61511
states that SIS Users must show Competence in Functional Safety -
When it comes to Safety Instrumented Systems (SIS) logic solvers, the process
industry reached a consensus in specifying that the equipment be third party
certified to meet IEC 61508 parts 2 and 3. Most Process plant require that SIS
certification be issued by TÜV, recognizing this lab as the safety systems
"Mark," even when safety standards don't mandate certification of SIS
equipment by any specific testing lab.What should be the process industry
consensus around the personnel responsible for the design and implementation?
Your
SIS should Protect Your Plant for its Lifecycle -
Production assets are built to last, and even when the investment is planned for
a 20-year lifetime, additional investments frequently extend their life beyond
the original design specification. Few safety systems can extend their lifecycle
and enhance their capabilities over the complete lifetime of the production
asset. A Safety Instrumented system should quietly provide year after year of
safe and extremely reliable performance in mission critical applications. Its
performance should be consistent and the user should not have to think about
them very often.
Integrating
Control and Safety - Where to Draw the Line - Robin
McCrea-Steele, TÜV FSExpert - New digital technology now makes it feasible to
integrate process control and safety instrumented functions within a common
automation infrastructure. While this can provide productivity and asset
management benefits, if not done correctly, it can also compromise the safety
and security of an industrial operation. This makes it critically important for
process industry users to understand where to draw the line. Cyber-security and
sabotage vulnerability further accentuate the need for securing the Safety
Instrumented System (SIS).
Dual
SIS Technologies do not cost less than TMR; They almost always Cost More
-Many companies advertise their Dual SIS technology (1oo2D
(Dual), 1oo2DR (Dual Redundant), 2oo4D) as a lower-cost alternative to Triple
Modular Redundant (TMR) systems. This is an unfortunate misrepresentation of the
capabilities of Dual SIS architectures. Dual PLCs in a 1oo2 (1 out of 2)
configuration were the initial solution of choice for "fail safe"
applications, but they cannot overcome an inherent problem with false trips.
Is
a TÜV Certificate Enough? - Robin McCrea-Steele, TÜV
FSExp - SIS vendors advertise their TÜV certification, but rarely tell you
about their implementation and operational restrictions - Most safety system
vendors focus on how the system performs when it is healthy, but don't talk much
about what happens when an internal failure is diagnosed; worst case, the entire
system shuts down. Each SIS vendor must provide clear information on factors
that might impair system performance, such as the system's implementation,
specific programming or configuration requirements, module or architecture
choices, and operational restrictions.
Given
a Choice, the Implementation and Installation of your SIS should not be
Entrusted to Strangers - Choosing an SIS implementer can
be as important as choosing the product itself. No matter how well the system is
designed or manufactured, failures are likely to occur if the implementation
team is not following proper procedures, is not experienced, or lacks adequate
technical qualification for the tasks they must perform.
What
is the Importance of Third Party Certification and SIL rating of SIS
devices? - Luis Duran - Based on the growing number of
safety certified devices or systems in the automation marketplace, these are the
times of Functional Safety Certification, especially in the process industries.
However as basic as it might sound, is there a “one-size-fits-all”
certification process? Or how useful is that “certified equipment” for your
application? From the reasons that gave birth to third party certification
agencies through the remaining fundamental need for their work today, the
questions to answer are: what is the end user getting with the certification?;
how can the end user benefit by utilizing certified equipment?; why this might
be better than using “proven in use” equipment as defined by IEC61511? This
paper presents a practical perspective to understanding certification and
selecting and applying certified devices or systems while deploying a safety
instrumented system, and highlights what else remains to be done by the
implementation team and end users to fulfil the requirements of current safety
standards as IEC61511 and best engineering practices.
Why
is Conforming to Safety Standards Important? - Compliance
to National and International safety standards is enforceable if the standards
are listed or referenced in the country's legislation. These references are
sometimes called "good engineering practices." The Occupational Safety
and Health Administration (OSHA) USA law and the Australian Occupational Health
and Safety (OHS) are examples of this legislation. Other countries e.g. Germany
and the UK are required to adopt IEC-61508 /61511 when applying safety
instrumented systems to process hazards.
Why
should Process Safety Engineers be Certified? - The
typical answer to this question is initially very defensive. Certified to what?
By whom? Who mandates certification of plant personnel? Why? What does this buy
me?
Duke
Power Upgrades Oconee Nuclear Station Turbine with a Digital Control System from
Invensys Operation Management - Safe operation is the top
concern of nuclear plants and reliability is a cornerstone of safety. Over
thirty years ago, when most of the nation’s nuclear plants were commissioned,
analog control systems were state of the art and ensured plant reliability.
Analog control systems presented certain constraints, if a component failed
under normal wear and tear, the entire system would be shut down. This would add
risk and cost hundreds of thousands of dollars a day in downtime. Marlon
Dempsey, Instruments and Controls Engineer, said, "We found that our analog
turbine control system was one of the top three causes of trips and transients,
primarily because its components presented a single point of failure. We knew
that introducing more redundancy at key points would enhance reliability
considerably and found that digital technology could provide that redundancy
while at the same time reducing the cost of downtime."After evaluating
alternative turbomachinery control solutions, Duke Energy began implementing a
fault-tolerant control system from Invensys Operations Management, contributing
to safe and reliable plant operations.
Tofino
for the Triconex Safety System - Walt Boyes of Control
magazine talks with Eric Byres of Byres Security and Joe Scalia from Invensys
Operations Management about the introduction of a custom Tofino for the Triconex
Safety System.
High
Security Integration Using OPC
- OPC Classic, the popular industrial integration
standard based on DCOM, has made the interfacing of different industrial control
products significantly easy. Unfortunately, it also brought with it a number of
serious security concerns for the designers of control, SCADA and safety
systems. This White Paper looks at these issues and reviews the solutions
proposed over the past decade from researchers and academics. It looks at new
technologies in advanced firewall port management and embedded OPC servers that
offer true defense-in-depth and read-only security for better reliability and
security of all control systems, but especially for safety integrated systems.
You will need to register to obtain this white paper.
TÜV FSEng Training
The Invensys Premier Functional Safety Engineering course, in cooperation with TÜV Industrie Service GmbH provides the training your organization needs to meet compliance requirements. Dates for courses can be found here.
Other Safety Instrumented Systems Links
The following links are
compliments of Emerson Process Management
Selecting
Transmitters for Safety Instrumented Systems
SIS/IEC
61508 Frequently Asked Questions
If
you go to the following SIS
link you can register and download the following very useful documents
which cover;
Basic safety concepts
What is risk? / Reducing risk/ Safety standards
Building your SIS
Physical design/Functional design/ Verification &
validation/ Installation & commissioning
Using your SIS
Operations & maintenance/ Modifications/
Decommissioning
The intelligent advantage
Smart SIS
The following Links are compliments of Pilz
Guide
to Programmable Safety Systems - A
comprehensive guide from Pilz
How
functional safety helps to save lives
-In this article Ron Bell explains functional safety
and looks ahead to the revision of the IEC 61508standard that is due for
publication in 2010.This article by Jeanne Erdmann was first published
in the January 2008 edition of the IEC's E-TECH. http://www.iec.ch
The
Golden Rules of Risk Assessment - Frank Schrever
- At its worst, the risk assessment is a bureaucratic time-waster that
does nothing to make workplaces safer. On the other hand, following five
golden rules mean risk assessments can be both functional and
lifesaving. From Pilz and Manufacturers Monthly.
The following Links are compliments of Moore
Industries-Pacific, Inc.
The
Ups and Downs of Alarms
-read about alarms in a Safety Instrumented Systems
environment -Garry Prentice-Moore
Industries International -Intech Magazine
Safety
Instrumented Systems: The "Logic" of Single Loop Logic
Solvers - What can the "new generation" of
safety-certified Single Loop Logic Solvers do for you?
Networked
Safety- Mainstream or Marketing? Discussing the
advantages and potential caveats of networked safety systems, and
specifically the Fieldbus Foundation’s FF-SIF safety protocol, this
article offers expert testimony and answers key questions about the
technologies. Moore Industries’ Director of Technology, Charles
Larson, contributes to the debate noting the considerable benefits of
networked safety - from Automation World
Emphasis
on Safety - Rob Stockham, Moore
Industries-Europe General Manager and safety expert, looks at the
latest method being employed by the UK nuclear industry to access
control systems in safety-related and safety-critical applications in
power stations
7.10
Using
HART To Improve Safe Failure Fraction in Protective Measures - Peter
Russell - Evaluation International (EI) is a technology club for large
scale users of instruments for measurement and control, their Members wished to
show, by the use of simulation testing (and other reliability data not part of
this testing), that the combination of a Moore Industries HIM converter, a Moore
Industries STA trip-amplifier and a Yokogawa EJX110A pressure transmitter would
be suitable for use up to Safety Integrity Level 2 (SIL2). The key to this is
the use of diagnostics via HART.
The following excellent papers have been generously
provided to ICEWeb with the permission of World Renowned SIS expert Dr Angela
E. Summers, Ph.D. President, SIS-TECH Solutions, LLC, 12621
Featherwood Dr., Suite 120, Houston, TX 77034 USA Phone: 281-922-8324
, Fax: 281-922-4362. For more papers and excellent links etc go to http://www.SIS-TECH.com
6.10
Glossary
of Terms for Safety Insrumented. Systems - This is a useful Glossary
of terms - from SISTech and flowcontrolnetwork.com.
3.10
SIF
Proof Testing Yields Process Sector Reliability Data - William H. Hearn,
Patrick Skweres, A. D. Arnold, and Angela E. Summers, Ph.D. - ANSI/ISA 84
requires periodic proof testing of SIFs to demonstrate the correct operation of
the loop elements along with sufficient historical documentation to support
analysis of discrepancies and validation of the SIF integrity and reliability.
The analysis of proof test records is an important element of the quality
assurance process necessary to support continued use of installed equipment. The
CCPS Process Equipment Reliability Database (PERD) project has developed failure
data taxonomies which provide a structure to capture data to support chemical
process data collection and analysis. SIS-TECH® has been distributing a device
failure rate database for more than 10 years. This paper describes how
SIS-TECH® will collect device performance data under a quality plan during
periodic SIF proof testing. This data will be contributed to PERD for review and
analysis so that SIL Solver® failure rates can be validated against operating
environment data.
3.10
Overfill
Protective Systems - Complex Problem, Simple Solution - Angela E. Summers,
Ph.D - Overfills have resulted in significant process safety incidents. Longford
(Australia, 1998), Texas City (United States, 2005), and Buncefield (United
Kingdom, 2005) can be traced to loss of level control leading to high level and
ultimately to loss of containment. A tower at Longford and a fractionating
column at Texas City were overfilled, allowing liquid to pass to downstream
equipment that was not designed to receive it. The Buncefield incident occurred
when a terminal tank was overfilled releasing hydrocarbons through its
conservation vents. The causes of overfill are easy to identify; however, the
risk analysis is complicated by the combination of manual and automated actions
often necessary to control level and to respond to abnormal level events. This
paper provides a summary of the Longford, Texas City, and Buncefield incidents
from an overfill perspective and highlights 5 common factors that contributed to
making these incidents possible. Fortunately, while overfill can be a complex
problem, the risk reduction strategy is surprisingly simple.
3.10
Lessons
Learned While Auditing Automation Systems for PSM Compliance - Angela
E. Summers, Ph.D - While reliance on instrumentation has
increased at an incredible pace, resources allocated to design and manage the
equipment have declined in many companies, leading to more burden and
expectations being placed on fewer and fewer people. Quality instrumented system
performance relies on a rigorous management system that minimizes human error
and equipment failure potential. This paper focuses on safety instrumented
systems and applicable process safety management requirements. Observations from
assessments and audits are provided, illustrating poor performing instrumented
systems, inadequate operating and maintenance procedures, recordkeeping and
retention practices, and out-of-date documentation.
3.10
Consistent
Consequence Severity Estimation -Angela Summers, PhD,
PE William Vogtmann and Steven Smolen - Most risk analysis methods rely on a
qualitative judgment of consequence severity, overstatement creates excessive
risk reduction requirements, understatement results in inadequate risk
reduction. This paper provides justification for developing semi-quantitative
look-up tables to support a LOPA team's assessment of consequence severity.
3.10
Safety
Management is a Virtue - Angela E. Summers, Ph.D - This paper discusses
various challenges to sustaining safe operation of process equipment. Each
challenge is introduced using a Chinese fortune cookie to remind the reader that
the barriers against progress are not new but have existed from many years. In
most cases, the solutions are also well known and generally require deployment
of robust equipment, proven techniques, and competent resources.
IEC
61508 Product Approvals - Veering Off Course - Upon
close examination it appears that the product approval process of IEC
61508(1) has veered seriously off course, possibly rendering many
safety instrumented system (SIS) applications less reliable than
expected or required.
A
Process Engineering View of Safe Automation -This
step-by-step procedure applies instrumented safety systems (ISS) to
continuously reduce process risk.
Quality
Assurance in Safe Automation - A
perfect process would have no hazards, but perfection is impossible in
the real world. Nearly all process units have inherent risk associated
with their design and operation. Safe operation is maintained with a
risk reduction strategy relying on a wide variety of safety systems.
This article focuses on the most common safety systems for managing
process deviations during planned operating modes – instrumented
safety systems (ISSs), such as safety alarms, safety controls, and
safety instrumented systems (SIS). Rigorous quality assurance is
necessary to achieve real-world risk reduction, so this article
follows the Plan, Do, Check, and Act process to discuss quality
assurance and its application to ISS.
Guidelines
for Safe and Reliable Instrumented Protective Systems (IPS) -
Written with guidance from members of the
CCPS’s Guidelines for Safe and
Reliable Instrumented Protective Systems subcommittee, author
and safety standards expert Dr. Angela Summers explores the decision
making processes necessary for the management of the protection
systems commonly applied throughout the process industry. Based
on the framework defined in the harmonized ANSI/ISA 84.01/IEC 61511
standards, this book provides readers with much-requested guidance in
an easy to understand discussion that addresses IPS planning, risk
assessment, design, engineering, installation, commissioning,
validation, operation, and maintenance activities.
Achieve
Continuous Safety Improvement
- This technical paper gives an insight of how to achieve
continuous safety improvement.
Continuous
Improvement in SIS - Discusses safety culture,
Protective Management Systems and how to achieve continuous improvement.
The
Evolution of Plant Automation
- Most
owner/operators continue the practice of implementing separate, and
often diverse, platforms for the BPCS and SIS, this paper discusses
the reasons behind this.
IEC
61511 and the Capital Project Process - A
Protective Management Systems Approach
Random,
Systematic, and Common Cause Failure: How do you manage them? - This paper provides an overview of random,
systematic, and common cause failures and clarifies the differences in
their management within IEC 61511.
Partial
Stroke Testing of Block Valves - Chapter, “Partial Stroke Testing of Block
Valves”, Instrument Engineers Handbook, Volume 4, Chapter 6.9 - For many operating companies, one of the most
difficult parts of complying with the standards is the testing
interval often required for final elements, such as emergency
isolation valves or emergency block valves, this excellent chapter
covers this in detail.
Safety
Instrumented Systems
- Published in Perry’s
Handbook of Chemical Engineering 2007 - Covers Hazard and Risk Analysis,
Design Basis, Requirements Specifications, Engineering,
Installation, Commissioning and Validation along with Operating Basis.
The
Evolution of the Cookbook - This paper provides
examples of simple “cookbook” approaches and illustrates how
architectures must evolve when addressing higher integrity levels
and/or process reliability.
User
Approval of SIS Device -This
paper explains the concept of user approval as documented in ANSI/ISA
84.00.01-2004, ANSI/ISA TR84.00.04, and the Center for ChemicalProcess
Safety book, Guidelines for Safe and Reliable Instrumented Protective
Systems.
Software
Implemented Safety Logic - This paper discusses some of the requirements
for implementing safety logic via software based systems.
Bridging
the Safe Automation Gap Part 1 - Part 1 discusses safe automation on a broad
perspective examining safety culture, organization and hazards
analysis issues.
Bridging the Safe Automation Gap Part 2 -Part 2 focuses on instrumented systems and
discusses specification, implementation, operation, maintenance, and
management of change.
To
Err is Human -It must be recognized in our designs that given the
right conditions that all things succumb to human error.
Fault
Management Analysis - Examining a device based on repairable or replaceable
components may be your best bet for designing failure out of your SIS
Partial-Stroke
Testing of Block Valves - This paper discusses the various ways that you can
partial stroke test block valves and illustrates the probability of
failure on demand calculations.
Common
Cause and Common Sense Designing Failure Out of Your SIS -Angela E. Summers, Ph.D. and Glenn Raney-
The paper will focus on how to identify potential common cause events
through the application of industry or internal design standards or
through the use of qualitative assessment techniques.
Improve
Facility SIS Performance and Reliability - Angela E. Summers, Ph.D., P.E, President, SIS-TECH
Solutions, LP and Bryan A. Zachary, Operations Manager
Introduction
to Layer of Protection Analysis -This paper provides an overview of the LOPA
process, highlighting the key considerations
High
Integrity Protective Systems for Reactive Processes - This paper discusses how to assess, design, and
implement HIPS to effectively manage potential overpressure of
equipment used for reactive processes.
Perspectives
on ANSI/ISA 84.00.01-2004 (IEC61511)-An Emerging International
Consensus Standard - Angela E. Summers, Ph.D., P.E., President, SIS-TECH
Solutions, LP
Bhopal:
Could it Happen Again? - Angela E. Summers, Ph.D., P.E., President, SIS-TECH Solutions, LP
Estimation
and evaluation of common cause failures in SIS - Angela E. Summers, Ph.D., Kimberly A. Ford, and
Glenn Raney
Safety
requirements specification in a capital project environment
Is
your SIS "grandfathered" under ANSI/ISA S84.01-2004? -
Kimberly A. Ford and Angela E. Summers, Ph.D., P.E.
Avoid
bad engineering practices in safety instrumented system design - Angela E. Summers, Ph.D., P.E., President, SIS-TECH
Solutions, LLC - As industry races toward compliance, it must work
hard to prevent the creation and acceptance of bad engineering
practices, which threaten the economics of plant operation and erode
the effectiveness of SIS designs.
Techniques
for assigning a target integrity level - Angela E. Summers, Ph.D.
Using
instrumented systems for overpressure protection - Dr. Angela E. Summers, PE, SIS-TECH Solutions, LLC
Viewpoint
on ISA TR84.0.02 - simplified methods and fault tree analysis -
Angela E. Summers, Ph.D., P.E.- Simplified
equations and fault tree analysis are two techniques that can be used
to verify safety integrity level. The two methods do yield different
results but both provide acceptable approximations.
The following Links are from Exida
Statistical
Signature Analysis: Modeling Complex λD(t) from Proof Test Data
and the Effects on Computing PFDavg - Julia V. Bukowski - To
compute PFDavg, we must first have a model for λD(t), the failure
rate of the equipment in the dangerous failure mode. A dangerous
failure occurs when equipment designed for prevention or mitigation of
an unsafe condition cannot properly respond to the unsafe condition,
i.e., the equipment fails on demand. For example, consider a PRV,
which, in normal operation, is closed. Should it fail in the
"stuck-shut" mode, it would be in a state of dangerous
failure as it would be unable to respond to an overpressure event if
one occurred.
Final
Elements and the IEC 61508 and IEC 61511 Functional Safety Standards
Book - This book reviews and explains the
application of the IEC 61508 and IEC 61511 functional safety standards
as they apply to final control elements. The overall safety lifecycle
and reliability requirements are reviewed with special focus on the
challenges encountered when dealing with complex electro-mechanical
subsystems. Throughout the book requirements for designing and
implementing reliable and effective safety instrumented functions are
covered in a clear step by step manner.
61508
and 61511; What Is an Operations Company Supposed to Do? - Eric
Scharpf - The typical first reaction from the process operations side
of the table when confronted with a new standard is, "How much
will this cost and how much extra paperwork will it involve?"....
IEC 61508 and 61511, the standards covering the design and use of a
safety instrumented system to reduce process plant accidents, are no
exception to this initial reaction.
Accurate Failure Metrics for Mechanical Instruments
-Dr. William M. Goble -Probabilistic calculations done to verify the
integrity of a Safety Instrumented System design require failure rate
data and failure mode data of all equipment including the mechanical
devices.
Assessment Levels for
Safety Equipment - Dr. William M. Goble - The end user must
carefully choose all instrumentation equipment used in Safety
Instrumented System (SIS) applications. All such equipment must be
carefully justified... IEC 61511, Functional Safety for the Process
Industries, requires that equipment used in safety instrumented
systems be chosen based on either IEC 61507 certification to the
appropriate SIL level or justification based on "prior use"
criteria.
Common Cause Simulation
- Dr. William M. Goble - Fault tolerant systems have been designed
for safety critical applications including the protection of
potentially dangerous industrial processes.
Development
of a Mechanical Component Failure Database -Dr. William Goble
& Julia Bukowski - In this paper, they present a methodology to
derive component failure rate data for mechanical components used in
automation systems based on warranty and field failure rate data as
well as expert opinion.
Estimating The Beta Factor
- Dr. William M. Goble - A Safety Instrumented System (SIS) is
often designed to help protect an industrial process against
potentially dangerous hazards. These systems often use redundant
equipment to achieve the needed levels of protection. If the design
was done to meet requirements of IEC 61511 or IEC 61508, probabilistic
evaluation is done to verify that the design achieves risk reduction
goals.
Evolution
of European Standards - Rainer Faller - Slide show presentation of
his Rockwell Automation 2002 speech
FMEDA
- Accurate Product Failure Metrics - John C. Grebe and Dr. William
Goble - The letters FMEDA form an acronym for "Failure Modes
Effects and Diagnostic Analysis." The name was given by one of
the authors in 1994 to describe a systematic analysis technique that
had been in development since 1998 to obtain subsystem / product level
failure rates, failure modes and diagnostic capability.
Functional
Safety Terms and Acronyms Glossary - exida - This list of
functional safety terms and acronyms has been compiled from a number
of sources listed at the end including the IEC 61508, IEC 61511
(ISA84.01) standards. It is meant to provide a general reference for
engineers practicing safety lifecycle engineering in the process
industry. As such it provides both safety and related non-safety term
definitions in a clear useable form. It specifically highlights the
most important terms and acronyms from the safety lifecycle standards
with working level definitions. The reader is encouraged to pursue IEC
61508 or IEC 61511 for additional definitions and for additional
information on applying the safety lifecycle to the process industry.
Getting
Failure Rate Data - Dr. William M. Goble - Safety verification
calculations for each safety instrumented function are a key concept
in functional safety standards like ISA 84.01 and IEC 61511.
IEC 61508 Overview
- exida - IEC 61508 is an international standard for the
“functional safety” of electrical, electronic, and programmable
electronic equipment. This standard started in the mid 1980s when the
International Electrotechnical Committee Advisory Committee of Safety
(IEC ACOS) set up a task force to consider standardization issues
raised by the use of programmable electronic systems (PES). At that
time, many regulatory bodies forbade the use of any software-based
equipment in safety critical applications. Work began within IEC
SC65A/Working Group 10 on a standard for PES used in safety-related
systems. This group merged with Working Group 9 where a standard on
software safety was in progress. The combined group treated safety as
a system issue.
IEC61511 Standard For Functional Safety
- exida - IEC 61511 has been developed as a Process Sector
implementation of the international standard IEC 61508:
"Functional safety of electrical / electronic / programmable
electronic safety-related systems."
Implementing
IEC61508 In The Process Industries - Dr. Eric W. Scharpf & Dr.
William M. Goble - IEC 61508 and its process-specific companion IEC
61511 are providing new codification to safety instrumented systems
and their application to the process industry.
Mechanical
Database Verification Report -Julia Bukowski - The purpose of this
document is to report on exida's successful efforts to validate
statistically certain random equipment failure rate data used in a
mechanical parts failure rate and failure mode database and, by
extension, to validate the techniques used to derive the data. To
accomplish this, a Failure Modes, Effects, and Diagnostic Analysis
(FMEDA) is initially used to predict the useful- life failure rate for
the fail-to-open condition of a particular pressure relief valve (PRV)
using the failure rates from the mechanical parts database. Next, this
prediction is statistically tested against three independent data sets
consisting of proof test data for PRV provided by Fortune 500
operating companies. The data sets all meet the intent of the quality
assurance of proof test data as documented by the Center for Chemical
Process Safety (CCPS) Process Equipment Reliability Database (PERD)
initiative.
Mechanical
Failure Rate Data for Low Demand Applications - exida - The use of
IEC 61508 [1] and IEC 61511 [2] has increased rapidly in the past
several years. Along with the adoption of the standards has come an
increase in the need for accurate reliability data for devices used in
Safety Instrumented Systems (SIS), both electronic and mechanical.
While the methodology of determining failure rates for electronic
equipment is fairly well accepted and applied, the same can not be
said for mechanical equipment. Several methods are currently being
utilized for generating failure rates for mechanical components. These
methods vary in their approach and often lead to dramatically
different failure rates which can lead to significant differences when
calculating the reliability of a safety instrumented function (SIF).
Some methods can result in dangerously optimistic failure rate
numbers.
Mechanical
FMEDA Presentation - Slide show presentation by Dr. William M.
Goble
Modeling & Analyzing The Effects Of Periodic Inspection On The
Performance Of Safety-Critical Systems - Julia V. Bukowski - This
paper presents a method for incorporating into Markov models of
safety-critical systems, periodic inspections and repairs which occur
deterministically in time.
Open
IEC 61508 Certification of Products -Rainer Faller & Dr.
William Goble -IEC 61508 has been in use for several years since the
final parts were released in 2000. Although written from the
perspective of a bespoke system, it is more commonly used to certify
products for a given SIL level. Valid product certification schemes
must involve the assessment of specific product design details as well
as an assessment of the safety management system of the product
manufacturer and the personnel competency of those professionals
involved in the product creation.
Partial Valve Stroke Testing
- Iwan van Beurden - The objective of a Safety Instrumented System
(SIS) is to reduce the risk associated with a particular process to a
level lower than or equal to the tolerable risk level.
PFDavg Calculations For Redundant Systems With Incomplete Testing
- Harry Cheddie - A common definition of a Safety Instrumented
Function (SIF) as defined in Functional Safety Standards is
"Function to be implemented by a Safety Instrumented System (SIS)
to mitigate or prevent a specific hazardous event."
PLC
vs Safety PLC - Dr. William M. Goble - Safety Programmable Logic
Controllers (PLCs) are special purpose machines that are used to
provide critical control and safety applications for automation users.
These controllers are normally an integral part of a safety
instrumented system (SIS) which are used to detect potentially
dangerous process situations.
Project
Experience with IEC 61508 and its Consequence - Rainer Faller
- This paper reports on the experiences with implementation of
IEC 61508 in recent projects with European, North American and
Japanese system vendors. The paper describes problems identified in
implementing the standard and proposes a knowledge tool and a
combination of software verification methods to mitigate these issues.
Real
Time Operating Systems for IEC 61508 - Mike Medoff - In today’s
world many potentially dangerous pieces of equipment are controlled by
embedded software. This equipment includes cars, trains, airplanes,
oil refineries, chemical processing plants, nuclear power plants and
medical devices. As embedded software becomes more pervasive so too do
the risks associated with it. As a result, the issue of software
safety has become a very hot topic in recent years. The leading
international standard in this area is IEC 61508: Functional safety of
electrical/electronic/ programmable electronic safety-related systems.
This standard is generic and not specific to any industry, but has
already spun off a number of industry specific derived standards, and
can be applied to any industry that does not have its own standard in
place. Several industry specific standards such as EN50128 (Railway),
DO-178B (Aerospace), IEC 60880 (Nuclear) and IEC 601-1-4 (Medical
Equipment), are already in place. Debra Herrmann (Herrmann, 1999) has
found a total of 19 standards related to software safety and
reliability cut across industrial sectors and technologies. These
standards’ popularity is on the rise, and more and more embedded
products are being developed that conform to these standards. Since an
increasing number of embedded products also use an embedded real time
operating system (RTOS), it has become inevitable that products with
an RTOS are being designed to conform to such standards. This creates
an important question for designers: how is my RTOS going to effect my
certification? This article will attempt to explore the challenges and
advantages of using an RTOS in products that will undergo
certification.
SIL Verification
- Dr. William M. Goble - The safety lifecycle (SLC) is one of the
fundamental concepts presented in the ANSI/ISA 84.01 and IEC 61508
functional safety standards.
Software - Stress Vs. Strength
- Dr. William M. Goble - Considering the components used in the
current control systems, hardware failure cause have been widely
studied.
Software Safety Technique
- Dr. William M. Goble - There is a strong trend toward the use of
programmable electronics in safety instrumented systems. yet some
users still avoid software-based systems.
State-Of-The-Art Safety Verification
- Dr. Eric W. Scharpf & Dr. William M. Goble -The past few
years have brought significant changes to the control safety field in
both technology (i.e., fieldbus) and regulation (i.e., IEC 61508).
What Does Proven In Use Imply?
- Rachel Amkreutz & Iwan van Beurden - The functional safety
standards, IEC 61508, IEC 61511, and ANSI/ISA 84.01 each specify the
Safety Integrity Level performance parameter of Safety Instrumented
Functions.
What
is PFDavg.? - Dr. William M. Goble - IEC 61508 requires
probabilistic evaluation of each set of equipment used to reduce risk
in a safety related system.
The
Grandfather Clause and existing equipment - Dr. William Goble -
International safety standards permit users to utilise a ‘Proven in
Prior Use’ methodology to justify SIS equipment ie., A
Grandfather Clause ; but can users take on the responsibility? -
Following a recent internally initiated audit of your facility’s
SIS, you realized your systems do not meet the “grandfather
clause” requirements described in ANSI/ISA 84.01.00. Now you face
the task of bringing those systems into conformance with international
safety standards. One of the questions your SIS team raised is, “Do
our installed transmitters meet the ‘prior use’ requirements
described in Section 11.5.3 of IEC 61511-1 – Requirements for the
selection of components and subsystems based on prior use?” From
the ISA and InTech.
The following Links are from
HIMA Australia
3.10
Integration
today - Integration solutions - For years people have been discussing the
subject of “integration” in automation technology. There are a variety of
solutions available for the integration of safety and control systems. Provided
the right decision is made you can take advantage of all the opportunities and
potential synergies of integration, long-term.
3.10
Summary
of Offshore Health and Safety Performance Report 2007-08 - The Offshore
Health and Safety Performance Report 2007-08 was produced by the National
Offshore Petroleum Safety Authority (NOPSA), with the aim to "move beyond
the view of safety as compliance with codes and standards and towards an overall
improved safety culture within an organisation. The report contains statistics,
trends and observations of health and safety within the Australian offshore
petroleum industry for the financial year 2007-08. Areas of concern highlighted
include equipment design, risk awareness and management, procedures, ageing
equipment, supervision and a shortage of skilled personnel.
Next
Generation Safety Controller Maximizes Availability for Demanding Process Applications
- The nemesis of all continuous processes is unplanned stoppage resulting from
controls malfunction, equipment failure, or operator error. System availability
can be improved significantly through the use of redundant control architectures
– especially those that allow hot-swapping or on-the-fly program changes.
Modern process safety solutions provide comprehensive diagnostics that help
users to recognize safety-critical situations and act quickly and accordingly to
avoid unnecessary system shutdowns. This paper from ARC highlights why companies
should invest in process safety.
NOPSA
competence findings in line with AS61511 - The Australian National Offshore
Petroleum Safety Authority recently recommended that oil and gas facility
operators implement formal staff competency management systems to ensure that
basic skills requirements for safe plant operation are met.
Functional
Safety: A Practical Approach for
End-Users and System Integrators- Tino Vande Capelle,Dr. M.J.M.
Houtermans - The object of this paper is to demonstrate through a practical
example how an end-user should deal with functional safety while designing a
safety instrumented function and implementing it in a safety instrumented
system.
Modern
2oo4-Processing Architecture for Safety Systems-Prof. Dr.-Ing. habil. Josef
Börcsök -This paper provides an overview of two out of four system
architecture and associated considerations.
Safety
Bus Systems -Prof. Dr.-Ing. habil. Josef Börcsök - Modern distributed
control systems are connected via bus systems, which need effective and
uninterrupted communication between all subscribers. Therefore it is necessary
for these communications to be fault tolerant and safe. For safety related
systems, additional safety layers are required to fulfil these requirements.
Introduction
in Safety Bus Systems-Prof. Dr.-Ing. habil. Josef Börcsök - This paper
discusses how modern distributed control systems are connected via bus systems,
and need effective and uninterrupted communication between all bus stations.
Therefore it is necessary that these communications are fault tolerant and
safe.
Safety
Critical Software-Prof. Dr.-Ing. habil. Josef Börcsök -This paper
discusses the methodical analysis of hardware architectures used in
safety-related applications. It provides an excursus on a safe computer system’s
software technology and specifies the overview in greater detail.
Safety
Systems -Prof. Dr.-Ing. habil. Josef Börcsök - This technical paper gives
an excellent overview of Safety Systems covering development history, the
fundamental considerations required, fault avoidance basis and measurement,
fault control basis, along with external influences such as environmental
demands, electromagnetic, mechanical and climatic considerations.
Comparison
of PFD calculation -Prof. Dr.-Ing. habil. Josef Börcsök - This paper
discusses the compares calculation methods.
Sharing
Control & Safety Instruments-Are your Layers Overlapping?-Dirk Schreier
- Since its release as an Australian standard in July of 2004, AS61511 is
rapidly being accepted and applied on Safety Instrumented Systems throughout the
process industry. Principles such as independence between control and protective
instruments have existed for many years; however they continue to often be
overlooked even with the introduction of this standard.
Risk
Prevention and Mitigation-Where does gas detection fit in?-Dirk Schreier -
It is quite common in today's process industry to see the terms fire and gas
(F&G). These terms have been used hand in hand for many years and are also
combined when referring to applications involving safety-instrumented systems.
This article challenges the thinking behind this concept and demonstrates that
although fire systems and gas detection systems both reduce risk; their methods
are actually quite different.
Legal
Implications in Australia for Companies and Individuals under “Industrial
Manslaughter”-Dean McNair - There has been a lot of discussion in
Australia recently over proposed new occupational health and safety (OH&S)
legislation which will include the provision to prosecute corporations and
individuals under industrial manslaughter laws. State and territory governments
are enacting these new laws in response to workplace deaths in the hope that it
will force company directors and senior executives to improve the safety
cultures within their organisations.
Safety
standard IEC 61508 - Consequences for automation technology and implementation
at HIMA -This white paper provides an overview of IEC 61508 and how HIMA
have addressed it's requirements.
SIL
Assessments -Identification of Safety Instrumented Functions-Dirk Schreier -
Since its release as an Australian standard in July of 2004, AS61511 is rapidly
being accepted and applied on Safety Instrumented Systems throughout the process
industry. AS61511 is a performance based standard with a risk-based approach to
safety. Performance based standards are by nature very open to interpretation,
and therefore allow for more than just one analysis technique. Some of the
techniques currently applied in industry have some shortfalls in achieving the
objective of the standard. This article looks at some common problems
encountered during the analysis phase of the AS61511 safety lifecycle.
Communication
with SafeEthernet -Franz Handermann- The application of SafeEthernet paves
the way for the open automation- and network systems of the future.
Safety
Considerations
Dr. Josef Börcsök,-Statistical
evaluation of HIMA systems in the context of IEC 61508. This
article contains the first comprehensive description of IEC 61508-compliant
calculation of errors in safety-related systems in general and describes how
relevant values for the H41q/H51q systems currently available from HIMA can be
calculated.
Critical
Aspects of Safety, Availability and Communication in the control of a subsea gas
pipeline- Requirements and Solutions - This is a large zipped file of 2.5
Meg so will take a while to download, however it is worth it as shows
safety related satellite communication.
Transporting
gas - with safety first!-Automation of an ethylene pipeline.
Complete
Burner Automation with Safety Controllers-A new solution for simple single
and multi burner arrangements through to complex BMS applications, e.g. for
power plants, waste incineration plants or processing plants. - Looking for more
on Burner
Management Systems? ICEweb's comprehensive BMS page has it!
Integrated
safety controllers with safeethernet - By combining the world's fastest
safety controllers "HIMatrix" with the world's fastest safety bus
"safeethernet", HIMA is creating a hitherto unknown level of
flexibility for safety-related automation. This flexibility is the basis for the
development of new potential. The current system limits of safety-related
automation concepts are disappearing, paving the way for truly application-based
safety solutions. This creates new potential for increasing productivity and
reducing the total costs for safety technology.
Comprehensive
safety solutions for the South Pars gasfield exploration-ESD, F&G and
HIPPS systems from HIMA ensure maximum safety and plant availability.
The following Links are from ACM
Automation
HAZOP
Budgeting Tool - How long will my HAZOP take?
Achieving High SIL
Ratings with Partial Stroke Testing of Valves
SIL Determination Techniques Report, this excellent document covers;
6.10
The following are from www.fabig.com
Fire
& Explosion Hazard Management - The aim of
the fire and explosion hazard management strategy is to reduce the
risks from fires and explosions to as low as reasonably practicable (ALARP).
The Oil and Gas UK guidance [1] and COMAH regulations [2] identify the
following aims:
• Identify, analyse and understand all fire and explosion hazards
and associated effects.
• The risk corresponding to fire and explosion hazards identified
above should be as low as reasonably practicable.
• A suitable order of priority, and a suitable combination, of
prevention, detection, control and mitigation systems for fire and
explosion hazards should be implemented and supported throughout the
life cycle of the offshore platform. In other words risks should be
reduced to ALARP using inherently safe design principles.
• The above prevention, detection, control and mitigation systems
should have performance measures proportionate to the required risk
reduction.
• The design, operation and maintenance of the above prevention,
detection, control and mitigation systems should be carried out by
competent staff.
• Any changes that may occur throughout the lifecycle of the
installation, and that may affect the likelihood and / or consequence
of any fire or explosion hazard event (and therefore may make the risk
on the installation deviate from an ALARP state) should be identified
and assessed. The prevention, detection, control and mitigation
systems should be modified and updated as necessary to take into
account any such changes.
Fire
& Explosion Hazard Management - Technical How-To-Do
Guidance - This useful list details references to many useful
documents.
Fire
& Explosion Hazard Management - Standards & Approved Codes of
Practice - A comprehensive list of standards
11.09
The following links are from the 61508
Association
Toolbox
Talks - This excellent link gives you the essential toolbox tips in just a few
sheets that will help your team to all be “singing from the same
hymn sheet” which covers:
• Directors
• Senior
Management
• Purchaser
• Project
Manager
• Project
Engineer
• Inspection
and QA
• Operations
• Maintenance
• Service
Engineer
• What
is Functional Safety Management
• Proven in use / Prior use claims
• Functional
Safety Management cross-reference
between IEC61508 and IEC61511
What
is a Functional Safety System? A short description.
What
is Conformity assessment? - Conformity Assessment is defined as
"activity that provides demonstration that specified requirements
relating to a product, process, system, person or body are
fulfilled."
What
is CASS? - Accredited Certification for Safety Systems - to IEC
61508 and Related Standards - CASS is a scheme for assessing the
compliance of safety related systems with the requirements of IEC
61508 and associated standards. It provides a systematic approach to
be used by certification bodies and others when assessing compliance
at all stages from the specification of safety requirements through
the design, development and manufacture of system components to
integration, commissioning, operation and maintenance. At each stage
CASS takes the conformity assessor through the logical steps of
defining the scope of the assessment, the target of evaluation, the
requirements to be met and the process of demonstrating and recording
conformity.
Legacy
Systems - Basic Principles for Safety - Engineered systems are
relied upon for safety in a wide range of work environments. There is
however, a general lack of awareness of the exact role played by such
systems, and whether adequate safety is, in fact, being achieved. This
is particularly true of systems that have been in place for many
years. This document describes how to assess the capability of so
called Legacy Systems, focussing on how electrical, electronic, or
programmable devices achieve adequate safety in conjunction with other
technologies such as mechanical systems and operational expectations.
SIL-Loops
to the Rescue - Poor Process Design shouldn’t have to Hide behind
Safety Loops - Clive de Salis -You’ve probably never thought of
it this way but it really is true: To have an SIL-rated loop is a
failure. An SIL-3 safety loop means that the layers of safety that we
as chemical engineers have put in place in the process design are
inadequate to such an extent that the risk of the fatality is 1000
timesthe wrong side of tolerable. The failure, herefore, is a failure
of the chemical engineer to design a process that has sufficient
layers of safety to not require an SIL-rated loop.
SIL
Certs can Seriously Impair Plant Safety - Clive de Salis -
Process operators are investing in certificates and experts - that the
IEC standards do not require - at the expense of actual functional
safety management. IEC61508 and particularly the process industry
application of it in IEC61511 is gaining ground strongly for high
integrity safety instrumented systems. However, the majority of
industry is still naively asking for certification that the standard
does not require, and has never needed, whilst ignoring its basic
essentials. How long can this really go on for?
The
61508 Association provides additional articles to promote the
benefits of IEC 61508 and accredited certification.
Other Very Useful Links
Fire
Safe Actuators - A paper detailing an innovative concept from valued
sponsor Samson
Controls Pty Ltd
Recommendations
on the Design and Operation of Fuel Storage Sites -This
52 page report sets out recommendations to improve safety in the
design and operation of fuel storage sites.
SIS
Links -TUV provides links to more Safety Instrumented Systems
Information
Safety
Users Group - An independent, professional community dedicated to
instrumented safety matters related to the oil, gas, petrochemical and
chemical industries. Lots of information here!
8.10
IEC
61511 – An Aid to COMAH and Safety Case Regulations Compliance -
CliveTimms - The paper focuses on the relationship between hazards and Safety
Instrumented Systems (SIS) that automatically shut down processes operations,
when an abnormal situation is encountered, to prevent a hazardous event or
mitigate the consequences of a hazardous event if it occurs (see section -
Safety Instrumented Systems). Thus a SIS will represent an integral part of an
SMS to reduce the risk of major accident hazards or mitigate the consequences -
from Asset Integrity Management Ltd.
8.10
Replacement
of SIS Logic Solvers Whilst the Process Remains Operational - Clive Timms -
With increasing global demand for oil and gas driving prices higher and higher,
the focus of oil and gas producers is to maintain and maximise production from
every available facility. Older unreliable facilities are being upgraded and
this often includes the replacement of Safety Instrumented Systems (SIS) such as
emergency shutdown (ESD) systems, process shutdown (PSD) systems, Emergency
Depressurisation (EDP) systems and fire and gas (F&G) systems due to
obsolescence or reliability issues. Traditionally, the replacement of such
safety critical systems is undertaken during a plant shutdown opportunity to
ensure that process integrity was maintained and the replacement systems could
be fully commissioned and validated without the presence of the process hazards.
However, in this era of high oil and gas demand we are now seeing more and more
SIS replacement projects being undertaken whilst the process is still fully
operational, and thiscan lead to potential compromises during commissioning and
validation of functionality - from C&C Technical Support Services and silsupport.com
8.10
Integrating
Control and Safety – Where to Draw the Line? - Robin McCrea-Steele - New
digital technology now makes it feasible to integrate process control and safety
instrumented functions within a common automation infrastructure. While this can
provide productivity and asset management benefits, if not done correctly, it
can also compromise the safety and security of an industrial operation.
Cyber-security and sabotage vulnerability further accentuate the need for
securing the Safety Instrumented System (SIS) - From the Safety Users Group.
8.10
Selecting
Transmitters for Safety Instrumented Systems - Stephen R. Brown and Mark
Menezes - Users design safety systems to mitigate the risk of identified
process hazards within tolerable levels, using application-specific risk models,
defined user inspection schedules, and safety data for the devices under
consideration. Some suppliers provide safety data for their devices. However,
supplier data, even when validated by a third party, reflects laboratory
results, and can be an order of magnitude too aggressive for field devices. “Proven-in-use”
data includes real-world failure causes; however it tends to be conservative,
since it must cover the whole range of the category, from 20-year-old pneumatics
to the latest smart technology. Moreover, proven-in-use data is often aggregated
for a given technology: for example, “pressure transmitter = dangerous failure
rate of once in 50 years”. This aggregate data often does not isolate failure
causes, so it does not allow users to take credit for improvements in technology
or user practices intended to minimize the impact of specific failures. The net
result to the user can be over design, over-testing, increased spurious trips
and needless capital expenditures - from IDC
3.10
SafetyBase.com
is a site that is full of some excellent information about Boiler
Management Systems, Machine and Process Safety. You’ll be able to
share ideas with colleagues across the country, stay current with
compliance requirements, and read the latest case studies, white
papers, and articles that can help you keep your people safe and your
process moving.
3.10
Center
for Chemical Process Safety - The
Global Community Committed to Process Safety - CCPS is a
not-for-profit, corporate membership organization within AIChE that
identifies and addresses process safety needs within the chemical,
pharmaceutical, and petroleum industries. CCPS brings together
manufacturers, government agencies, consultants, academia and insurers
to lead the way in improving industrial process safety.
3.10
An
Introduction to Inherently Safer Design - Inherently safer design
(ISD) is a philosophy for addressing safety issues in the design
and operation of chemical processes and manufacturing
plants. When considering ISD, the designer tries
to manage process risk by eliminating or significantly reducing
hazards. Thanks to Centre for
Chemical Process Safety.
Recommended
Guidelines for the application of IEC 61508 and IEC 61511 in the
petroleum activities on the Norwegian
Continental Shelf -
This very comprehensive 55 page guideline from the Norwegian Oil
Industry association is very useful.
Introduction
& background to IEC 61508 - Ron Bell - Over the past 25
years there have been a number of initiatives worldwide to develop
guidelines and standards to enable the safe exploitation of
programmable electronic systems used for safety applications. In the
context of industrial applications (to distinguish from aerospace and
military applications) a major initiative has been focussed on IEC
61508 and this standard is emerging as a key international standard in
many industrial sectors. This paper looks at the background to the
development of IEC 61508, considers some of the key features and
indicates some of the issues that are being considered in the current
revision of the standard. Thanks to the Safety Users group.
PDS
Method Handbook, 2003 Edition - Reliability Prediction Method
for Safety Instrumented Systems
8.10
Equipment,
Don't Fail Me Now - Calculating failure probabilities
works better with systematic approach - Peter Morgan - Specialists
in control and instrumentation were once confident to rely on their own
experience and good design practice to design protection systems. Now they must
adhere to a quantitative approach to designing systems deemed safety systems.
Even the ubiquitous burner management system (BMS) is by virtue of its function,
a safety instrumented system (SIS), and you should design it according to ISA
84.01 as well as the applicable National Fire Protection Agency standard.
One step in this approach is calculating the target probability
of failure on demand (PFD) for the system - From ISA and InTech
An
Integrated Approach to Safety: Defense in Depth - Ensuring
safety requires reducing the risk of incidents, faults and failures
that can disrupt normal operations. This effort goes far beyond simply
installing fail-safe controllers or a safety instrumented system. In
fact, to mitigate the risk of serious incidents that can cause injury
to personnel, equipment and the environment, it is important to
consider safety from all aspects of a plant’s operation - From
Honeywell
Certified
Functional Safety Expert Governance Board -The CFSE is now administered by the CFSE Governance
Board which is in turn supported by a broad consortium of companies
including Honeywell, Pilz, Siemens, TUV, exida and other leading
safety related firms.
Partial
Closing of Shutdown/Blowdown Valves - Useful news release from ICS Triplex
Safety
and related Acronyms From the Laboratory
Safety Institute
Functional
Safety and Safety Integrity Levels - An application note from Bentley
Nevada
Valve
system controls for safety - A matrix that substantially increases
the level of safety in the process industries while significantly
reducing the number of nuisance trips - Improved safety brings more
nuisance trips, which means lost production.The single block valve is
the weak point of the 2oo2D architecture and Parallel valve technology
can provide 95% diagnostic coverage- G. Paul Baker and ISA InTech
PDS
Data Handbook, 2003 Edition - PDS is a
method used to quantify and balance the safety and production loss of
Safety Instrumented Systems (SIS). The method accounts for all types
of failure categories; technical, software, human, etc.- The 2006
edition of the PDS Method Handbook gives an updated version of the PDS
method, including the mathematical details.
Converting
relay-based logic solver to triple modular redundancy means safer
plants at less cost - Keyur Vora and Ranjan Bhattacharya - When a
leading Indian petrochemical plant noticed interlock operations and
actuation happening six times a year due to shutdowns, they knew it
was time for a change. Problems with trips in the oxidation reactor
lead to huge costs in production and quality losses. Finally plant
officials looked at upgrading the relay-based interlock system with
triple modular redundancy (TMR) to enhance reliability and
availability and reduce nuisance trips. From ISA and InTech.
Process
Safety what are the Odds? - Enhancing a safety system's ability to perform
on demand requires improved diagnostic coverage, maintenance, and regular
testing. From controleng.com
How
to Specify Solenoid Valves for a Particular Safety Integrity Level
- S.A. Nagy - Selection must be done with care and understanding of
safety and reliability standards to avoid the risks associated with an
operational failure of a critical plant system - thanks to chem.info
Smart Instruments in Safety Instrumented Systems - Tom Nobes -
The U.K.'s largest nuclear site operator implements IEC61508 and finds
the quality of instrument firmware to be variable, but improving.
Thanks to ISA.
Vessel overflow protection systems seem so simple, so straightforward—that
is until one of them fails to work properly and your plant is the six
o’clock news - The underlying concept required of an automated
overfill protection system seems so simple: If the level of a vessel
reaches a pre-determined maximum, then stop the flow of liquid filling
the vessel. Satisfying such a simple requirement occurs in toilets,
clothes washers, and dishwashers every day, so what is the big deal?
The big deal is the liquid in toilets, washers, and dishwashers is
water, not a highly flammable, possibly toxic, fuel or chemical. In
addition, remember if the overfill protection system fails and there
is even a minor incident, government investigators are going to want
to see evidence you applied the principles of IEC 61511. Thanks to
InTech.
Equipment,
don't fail me now - Calculating failure probabilities works better
with systematic approach - Peter Morgan - One step in this
approach is calculating the target probability of failure on demand
(PFD) for the system. Because calculating PFDs for repairable systems
commonly seems complicated, the approach does not curry favor with the
average control and instrumentation specialist; some manufacturers
defer the design analysis to others or they do not do it at all. But
there is benefit in the approach for designing general protective
systems in addition to meeting the mandatory requirements for a SIS.
From the ISA and InTech.
HSE (UK) documents
'The Strategy for Workplace Health and Safety in Great Britain to 2010 and beyond' http://www.hse.gov.uk/aboutus/hsc/strategy.htm
6.10
Development
of a Business Excellence Model of Safety Culture - Michael S Wright,
Philip Brabazon, Alison Tipping and Medha Talwalkar - This report
gives the results of a study carried out by Entec UK Ltd to provide a
comprehensive review of research on how to assess and develop safety
culture, and thereafter produce a safety culture improvement matrix (SCIM).
6.10
Root
Causes Analysis - Literature review - This report contains the
findings of a literature search, outlining the principles, structure and
method of application of each identified root causes analysis technique.
6.10
Best
Practice for Risk Based Inspection as a part of Plant Integrity
Management - J B Wintle, B W Kenzie Mr G J Amphlett and S Smalley
-This report discusses the best practice for the application of Risk
Based Inspection (RBI) as part of plant integrity
management, and its inspection strategy for the inspection of pressure
equipment and systems that are subject to the
requirements for in-service examination under the Pressure Systems
Safety Regulations 2000 (PSSR). It can also apply to
equipment and systems containing hazardous materials
that are inspected as a means to comply with the Control of Major
Accident Hazards Regulations (COMAH).
6.10
A
Review of Experience from Two Offshore Design Projects - D Piper
- This report describes the outcome of a review of experience from
two recent offshore design projects, primarily from a safety
perspective, to identify key issues and any lessons that may be learnt
for future projects.
6.10
Application
of QRA in Operational Safety Issues - Andrew Franks, Richard
Whitehead, Phil Crossthwaite and Louise Smail - This study has performed
research into the use of risk in Health and Safety Executive's (HSE)
operational decisions in the context of the COMAH regulation 4. The
research focussed on the use of regulatory guidance, risk matrices and
Quantitative Risk Analysis (QRA) to demonstrate compliance with the
ALARP principle. Each approach has its strengths and weaknesses, for any
particular situation. Cost Benefit Analysis (CBA) when used in
conjunction with QRA is able to provide an economic justification as to
whether risk reduction measures should be implemented.
6.10
A
Methodology for the Assignment of Safety Integrity Levels (SILs) to
Safety-Related Control functions Implemented by Safety-Related
Electrical, Electronic and Programmable Electronic Control Systems of
Machines - Mark Charlwood, Shane Turner and Nicola Worsell -
This contract research report describes the development by the authors,
with funding from HSE, of a methodology for the assignment of required
Safety Integrity Levels (SILs) of safety related electrical control
systems of machinery. The rationale behind the methodology and how to
use it in practice are also explained in some detail. The methodology
has been developed and accepted for inclusion in an informative annex of
the International Electrotechnical Committee standard IEC 62061:
"Safety of Machinery Functional Safety of Electrical, Electronic
and Programmable Electronic Control Systems for Machinery"
6.10
Risk
Based Inspection -
A Case Study Evaluation of Onshore Process Plant
- W Geary - A survey of approximately 50 UK organisations
carried out by HSL in 1999 showed that approximately
half were using an approach to plant inspection based on risk. It was
clear however, that a wide range of systems were
in use including commercial software packages and
in-house systems specific to individual plants. Given the disparate
nature of some of these systems and the likelihood
that RBI assessments might produce very different results depending
on which methodology was used, HSE took the view that a study should be
undertaken using a number of example cases to tease out
the differences between the systems. This is the
subject of the current investigation.
INDG218, 'A Guide to Risk Assessment Requirements' http://www.hse.gov.uk/pubns/raindex.htm
INDG163, 'Five Steps to Risk Assessment'
http://www.hse.gov.uk/pubns/raindex.htm
RR216, 'A methodology for the assignment of
safety integrity levels (SILs) to safety-related control functions
implemented by safety-related electrical, electronic and programmable
electronic control systems of machines'
http://www.hse.gov.uk/research/rrhtm/rr216.htm
INDG316, 'Procedures for daily inspection and
testing of mechanical power presses and press brakes'
http://www.hse.gov.uk/pubns/engindex.htm
INDG375, 'Power presses: a summary of guidance
on maintenance and thorough examination'
http://www.hse.gov.uk/pubns/puwerind.htm
INDG229, 'Using work equipment safely'
http://www.hse.gov.uk/pubns/puwerind.htm
INDG270, 'Supplying New Machinery: a Short
Guide'
http://www.hse.gov.uk/pubns/puwerind.htm
INDG271, 'Buying New Machinery: a Short Guide'
http://www.hse.gov.uk/pubns/puwerind.htm
INDG291, 'Simple guide to the Provision and use
of Work Equipment Regulations 1998'
http://www.hse.gov.uk/pubns/puwerind.htm
RR125, 'Evaluation of the implementation of the
use of work equipment directive and the amending directive to the use of
work equipment directive in the UK'
http://www.hse.gov.uk/research/rrhtm/rr125.htm
HSC13, 'Health and Safety Regulation: a Short
Guide'
http://www.hse.gov.uk/pubns/regindex.htm
INDG275, 'Managing Health and Safety: Five
Steps to Success'
http://www.hse.gov.uk/pubns/manindex.htm
INDG343, 'Directors' Responsibilities for
Health and Safety'
http://www.hse.gov.uk/pubns/manindex.htm
'Directors' Responsibilities for Health and Safety (INDG343):
Frequently Asked Questions'
http://www.hse.gov.uk/pubns/manindex.htm
Training
6.10
E-learning course from Abhisam
Software on Safety
Instrumented Systems - This course covers ALL aspects of Safety
Instrumented Systems in seven modules covering the following;
* Introduction to SIS
* Hazards, Risks and their analysis
* Failures and Reliability
* Safety Integrity Level (SIL)
* SIS Standards
* SIS in Practice
* SIS Testing and Maintenance
This course is a blend of Flash based
animations/videos, graphics, real-life photos and and text that explain key
concepts in a easy to understand method. Take the Self Assessment test at the
end to gauge your understanding.
The Safety Users Group offers the following self training - Hardware Safety System Constraints Made Easy - An in-depth training course on IEC 61508 and IEC 61511 key hardware design concepts. This training course features hardware safety concepts as intended by IEC 61508 and IEC 61511 standards in an easy-to-understand format and at the viewer’s own pace. Topics covered are:
HIMA Australia offer a number of training courses in Australia - Details can be found here.
Wish to learn more about Manufacturing and Automation Safety or Burner Management? ICEweb has these topics well covered on our MAS and BM pages.