Category Archives: CE Mark - Page 2

Reader Question: Multiple E-​​Stops and Resets

This entry is part 7 of 9 in the series Emergency Stop

Control Panel with Emergency Stop Button.I had an inter­est­ing ques­tion come in from a reader today that is rel­e­vant to many situations:

When you have mul­ti­ple E-​​Stop but­tons I have often got­ten into an argu­ment that says you can have a reset beside each one. I was taught that you were required to have a sin­gle point of reset. Who is correct?”

— Michael Barb, Sr. Electrical Engineer

The Short Answer

There is noth­ing in the EU, US or Canadian reg­u­la­tions that would for­bid hav­ing mul­ti­ple reset but­tons. However, you must under­stand the over­lap­ping require­ments for emer­gency stop and pre­ven­tion of unex­pected start-​​up.

The Long Answer:

First I need to define two dif­fer­ent types of reset for clarity:

  1. Emergency Stop Device Reset: Each e-​​stop device, i.e. but­ton, pull cord, foot switch, etc., is required to latch in the acti­vated state and must be indi­vid­u­ally reset. Resetting the e-​​stop device is NOT per­mit­ted to re-​​start the machin­ery, only to per­mit restart­ing. (NFPA 79, CSA Z432, ISO 14118).
  2. Restarting the machine is a sep­a­rate delib­er­ate action from reset­ting the emer­gency stop device(s).

ANSI B11-​​2008 pro­vides some direct guid­ance on this topic:

7.2.2 Zones

A machine or an assem­bly of machines may be divided into sev­eral con­trol zones (e.g., for emer­gency stop­ping, stop­ping as a result of safe­guard­ing devices, start-​​up, iso­la­tion or energy dis­si­pa­tion). The machine and con­trols in dif­fer­ent zones shall be defined and iden­ti­fied. Controls for machines in zones can be local for each machine, across sev­eral machines in a zone, or glob­ally for machines across zones. The con­trol require­ments shall be based on the oper­a­tional require­ments and on the risk assess­ment.The inter­faces between zones, includ­ing syn­chro­niza­tion and inde­pen­dent oper­a­tion, shall be designed such that no func­tion in one zone cre­ates a haz­ard(s) /​ haz­ardous sit­u­a­tion in another zone.

CSA Z432-​​04 has sim­i­lar wording:

6.2.1.8.4

When zones can be deter­mined, their delim­i­ta­tions shall be evi­dent (includ­ing the effect of the asso­ci­ated emer­gency stop device). This shall also apply to the effect of iso­la­tion and energy dissipation.

Let’s take a case with a sin­gle e-​​stop but­ton first. The same require­ments apply for all e-​​stop devices. The require­ments include:

  1. Button must be in ‘easy-​​reach’ of the nor­mal oper­a­tor posi­tion. I con­sider ‘easy-​​reach’ to be the range I can touch while sit­ting or stand­ing at the nor­mal oper­a­tor posi­tion. This posi­tion is not nec­es­sar­ily in front of the con­trol panel. This is the posi­tion where the oper­a­tor is expected to be while car­ry­ing out the tasks expected of them when the machine is oper­at­ing. This is the require­ment that dri­ves hav­ing mul­ti­ple but­tons in most cases.
  2. E-​​stop devices can­not be located so that the oper­a­tor must reach over or past a haz­ard to acti­vate them.
  3. The but­ton must latch in the oper­ated position.
  4. The but­ton must be robust enough to han­dle the mechan­i­cal and elec­tri­cal stresses that will be placed on it when used. i.e. rugged but­tons are required.
  5. When the e-​​stop device is reset — i.e returned to the ‘RUN’ posi­tion — the machine is NOT per­mit­ted to restart. It is only PERMITTED to restart. It must be restarted through another delib­er­ate action, like press­ing a ‘Power On’ button.

So what do you do with the ‘POWER ON’ or safety cir­cuit reset but­ton? The first ques­tion to ask is: ‘What hap­pens when I reset this cir­cuit, apply­ing power to the con­trol circuits?”

Case A: If it is impos­si­ble to see the entire machine from the loca­tion of the reset but­ton, then I would rec­om­mend a sin­gle reset but­ton located at the HMI or main con­sole. The oper­a­tor must check to make sure the machine is clear before re-​​applying power. Where the machine is too big to be com­pletely vis­i­ble from the main oper­a­tor con­sole, then I would also recommend:

  • warn­ing horn,
  • warn­ing lights, and
  • a start-​​up delay that is long enough to allow a per­son to get clear of the machine before it starts moving.

Case B: If the machine is sim­ply ‘enabled’ at this point, but no motion occurs, then mul­ti­ple ‘reset’ or ‘power on’ but­tons may be accept­able, depend­ing on the out­come of the risk assess­ment and start/​stop analy­sis. Having said that, the oper­a­tor will likely have to return to a main con­sole to reset the machine and restart oper­a­tion, and chances are there is only one HMI screen on the machine, so there may not be any advan­tage to hav­ing mul­ti­ple reset buttons.

I would rec­om­mend doing two things to get a good han­dle on this: Conduct a detailed risk assess­ment and include all nor­mal oper­a­tions and all main­te­nance oper­a­tions. Then con­duct a start/​stop analy­sis to look at all of the start­ing and stop­ping con­di­tions that you can rea­son­ably fore­see. Combine the results of these two analy­ses to find the start­ing and stop­ping con­di­tions with the high­est risk, and then deter­mine if hav­ing mul­ti­ple reset but­tons will con­tribute to the risk or not. You may also want to look at the con­trol reli­a­bil­ity require­ments for the emer­gency stop sys­tem based on the out­come of the risk assess­ment and the start/​stop analysis.

In a case where there are mul­ti­ple emer­gency stop devices, loca­tions are impor­tant. There must be one at each nor­mal work­sta­tion to meet the reg­u­la­tory require­ments in most juris­dic­tions, and within ‘easy reach’. You may also want some inside the machine if it is pos­si­ble to gain full body access inside the machin­ery. i.e. inside a robot work cell. Make sure that the but­tons or other devices are located so that a per­son exposed to the hazard(s) inside the machine is not required to reach over or past the haz­ard to get to the button.

Michael, I hope that set­tles the argument!

Understanding the Hierarchy of Controls

Effectiveness of the Hierarchy of Controls
This entry is part 2 of 3 in the series Hierarchy of Controls

Risk assess­ment is the first step in reduc­ing the risk that your cus­tomers and users are exposed to when they use your prod­ucts. The sec­ond step is Risk Reduction, some­times called Risk Control or Risk Mitigation. This arti­cle looks at the ways that risk can be con­trolled using the Hierarchy of Controls. Figure 2 from ISO 12100–1 (shown below) illus­trates this point.

The sys­tem is called a hier­ar­chy because you must apply each level in the order that they fall in the list. In terms of effec­tive­ness at reduc­ing risk, the first level in the hier­ar­chy, elim­i­na­tion, is the most effec­tive, down to the last, PPE*, which has the least effectiveness.

It’s impor­tant to under­stand that ques­tions must be asked after each step in the hier­ar­chy is imple­mented, and that is “Is the risk reduced as much as pos­si­ble? Is the resid­ual risk a) in com­pli­ance with legal require­ments, and b) accept­able to the user or worker?”. When you can answer ‘YES’ to all of these ques­tions, the last step is to ensure that you have warned the user of the resid­ual risks, have iden­ti­fied the required train­ing needed and finally have made rec­om­men­da­tions for any needed PPE.

*PPE — Personal Protective Equipment. e.g. Protective eye wear, safety boots, bump caps, hard hats, cloth­ing, gloves, res­pi­ra­tors, etc. CSA Z1002 includes ‘…any­thing designed to be worn, held, or car­ried by an indi­vid­ual for pro­tec­tion against one or more haz­ards.’  in this definition.

Risk Reduction from the Designer's Viewpoint

ISO 12100:2010 — Figure 2

 

Introducing the Hierarchy of Controls

The Hierarchy of Controls was devel­oped in a num­ber of dif­fer­ent stan­dards over the last 20 years or so. The idea was to pro­vide a com­mon struc­ture that would pro­vide guid­ance to design­ers when con­trol­ling risk.

Typically, the first three lev­els of the hier­ar­chy may be con­sid­ered to be ‘engi­neer­ing con­trols’ because they are part of the design process for a prod­uct. This does not mean that they must be done by engineers!

We’ll look at each level in the hier­ar­chy in detail. First, let’s take a look at what is included in the Hierarchy.

The Hierarchy of Controls includes:

1)    Hazard Elimination or Substitution (Design)
2)    Engineering Controls (see [1, 2, 8, 9, 10, and 11])

a)    Barriers

b)    Guards (Fixed, Movable w/​interlocks)

c)    Safeguarding Devices

d)    Complementary Protective Measures

3)    Information for Use (see [1, 2, 4, 7, 8, 12, and 13])

a)    Hazard Warnings

b)    Manuals

c)    HMI* & Awareness Devices (lights, horns)

4)    Administrative Controls (see [1, 2, 4, 5, 7, and 8])

a)    Training

b)    SOP’s,

c)    Hazardous Energy Control Procedures (see [5, 14])

d)    Authorization

5)    Personal Protective Equipment

a)    Specification

b)    Fitting

c)    Training in use

d)    Maintenance

*HMIHuman-​​Machine Interface. Also called the ‘con­sole’ or ‘oper­a­tor sta­tion’. The loca­tion on the machine where the oper­a­tor con­trols are located. Often includes a pro­gram­ma­ble screen or oper­a­tor dis­play, but can be a sim­ple array of but­tons, switches and indi­ca­tor lights.

The man­u­fac­turer, devel­oper or inte­gra­tor of the sys­tem should pro­vide the first three lev­els of the hier­ar­chy. Where they have not been pro­vided, the work­place or user should pro­vide them.

The last two lev­els must be pro­vided by the work­place or user.

Effectiveness

Each layer in the hier­ar­chy has a level of effec­tive­ness that is related to the fail­ure modes asso­ci­ated with the con­trol mea­sures and the rel­a­tive effec­tive­ness in reduc­ing risk in that layer. As you go down the hier­ar­chy, the reli­a­bil­ity and effec­tive­ness decrease as shown below.

Effectiveness of the Hierarchy of ControlsThere is no way to mea­sure or specif­i­cally quan­tify the reli­a­bil­ity or effec­tive­ness of each layer of the hier­ar­chy — that must wait until you make some selec­tions from each level, and even then it can be very hard to do. The impor­tant thing to under­stand is that Elimination is more effec­tive than Guarding (engi­neer­ing con­trols), which is more effec­tive than Awareness Means, etc.

1. Hazard Elimination or Substitution

Hazard Elimination

Hazard elim­i­na­tion is the most effec­tive means of reduc­ing risk from a par­tic­u­lar haz­ard, for the sim­ple rea­son that once the haz­ard has been elim­i­nated there is no remain­ing risk. Remember that risk is a func­tion of sever­ity and prob­a­bil­ity. Since both sever­ity and prob­a­bil­ity are affected by the exis­tence of the haz­ard, elim­i­nat­ing the haz­ard reduces the risk from that par­tic­u­lar haz­ard to zero. Some prac­ti­tion­ers con­sider this to mean the elim­i­na­tion is 100% effec­tive, how­ever it’s my opin­ion that this is not the case because even elim­i­na­tion has fail­ure modes that can re-​​introduce the hazard.

Failure Modes:

Hazard elim­i­na­tion can fail if the haz­ard is rein­tro­duced into the design. With machin­ery this isn’t that likely to occur, but in processes, ser­vices and work­places it can occur.

Substitution

Substitution requires the designer to sub­sti­tute a less haz­ardous mate­r­ial or process for the orig­i­nal mate­r­ial or process. For exam­ple, beryl­lium is a highly toxic metal that is used in some high tech appli­ca­tions. Inhalation or skin con­tact with beryl­lium dust can do seri­ous harm to a per­son very quickly, caus­ing acute beryl­lium dis­ease. Long term expo­sure can cause chronic beryl­lium dis­ease. Substituting a less toxic mate­r­ial with sim­i­lar prop­er­ties in place of the beryl­lium in the process  could reduce or elim­i­nate the pos­si­bil­ity of beryl­lium dis­ease, depend­ing on the exact con­tent of the sub­sti­tute mate­r­ial. If the sub­sti­tute mate­r­ial includes any amount of beryl­lium, then the risk is only reduced. If it con­tains no beryl­lium, the risk is elim­i­nated. Note that the risk can also be reduced by ensur­ing that the beryl­lium dust is not cre­ated by the process, since beryl­lium is not toxic unless ingested.

Alternatively, using processes to han­dle the beryl­lium with­out cre­at­ing dust or par­ti­cles could reduce the expo­sure to the mate­r­ial in forms that are likely to cause beryl­lium dis­ease. An exam­ple of this could be sub­sti­tu­tion of water-​​jet cut­ting instead of mechan­i­cal saw­ing of the material.

Failure Modes:

Reintroduction of the sub­sti­tuted mate­r­ial into a process is the pri­mary fail­ure mode, how­ever there may be oth­ers that are spe­cific to the haz­ard and the cir­cum­stances. In the above exam­ple, pre– and post-​​cutting han­dling of the mate­r­ial could still cre­ate dust or small par­ti­cles, result­ing in expo­sure to beryl­lium. A sub­sti­tuted mate­r­ial might intro­duce other, new haz­ards, or might cre­ate fail­ure modes in the final prod­uct that would result in risks to the end user. Careful con­sid­er­a­tion is required!

If nei­ther elim­i­na­tion or sub­sti­tu­tion is pos­si­ble, we move to the next level in the hierarchy.

2. Engineering Controls

Engineering con­trols typ­i­cally include var­i­ous types of mechan­i­cal guards [16, 17, & 18], inter­lock­ing sys­tems [9, 10, 11, & 15], and safe­guard­ing devices like light cur­tains or fences, area scan­ners, safety mats and two-​​hand con­trols [19]. These sys­tems are proac­tive in nature, act­ing auto­mat­i­cally to pre­vent access to a haz­ard and there­fore pre­vent­ing injury. These sys­tems are designed to act before a per­son can reach the dan­ger zone and be exposed to the hazard.

Control reli­a­bil­ity

Barrier guards and fixed guards are not eval­u­ated for reli­a­bil­ity because they do not rely on a con­trol sys­tem for their effec­tive­ness. As long as they are placed cor­rectly in the first place, and are oth­er­wise prop­erly designed to con­tain the haz­ards they are pro­tect­ing, then noth­ing more is required. On the other hand, safe­guard­ing devices, like inter­locked guards, light fences, light cur­tains, area scan­ners, safety mats, two-​​hand con­trols and safety edges, all rely on a con­trol sys­tem for their effec­tive­ness. Correct appli­ca­tion of these devices requires cor­rect place­ment based on the stop­ping per­for­mance of the haz­ard and cor­rect inte­gra­tion of the safety device into the safety related parts of the con­trol sys­tem [19]. The degree of reli­a­bil­ity is based on the amount of risk reduc­tion that is being required of the safe­guard­ing device and the degree of risk present in the unguarded state [9, 10].

There are many detailed tech­ni­cal require­ments for engi­neer­ing con­trols that I can’t get into in this arti­cle, but you can learn more by check­ing out the ref­er­ences at the end of this arti­cle and other arti­cles on this blog.

Failure Modes

Failure modes for engi­neer­ing con­trols are as many and as var­ied as the devices used and the meth­ods of inte­gra­tion cho­sen. This dis­cus­sion will have to wait for another article!

Awareness Devices

Of spe­cial note are ‘aware­ness devices’. This group includes warn­ing lights, horns, buzzers, bells, etc. These devices have some aspects that are sim­i­lar to engi­neer­ing con­trols, in that they are usu­ally part of the machine con­trol sys­tem, but they are also some­times classed as ‘infor­ma­tion for use’, par­tic­u­larly when you con­sider indi­ca­tor or warn­ing lights and HMI screens. In addi­tion to these ‘active’ types of devices, aware­ness devices may also include lines painted or taped on the floor or on the edge of a step or ele­va­tion change, warn­ing chains, sig­nage, etc. Signage may also be included in the class of ‘infor­ma­tion for use’, along with HMI screens.

Failure Modes

Failure modes for Awareness Devices include:

  • Ignoring the warn­ings (Complacency or Failure to com­pre­hend the mean­ing of the warning);
  • Failure to main­tain the device (warn­ing lights burned out or removed);
  • Defeat of the device (silenc­ing an audi­ble warn­ing device);
  • Inappropriate selec­tion of the device (invis­i­ble or inaudi­ble in the pre­dom­i­nat­ing conditions).

Complementary Protective Measures

Complementary Protective mea­sures are a class of con­trols that are sep­a­rate from the var­i­ous types of safe­guard­ing because they gen­er­ally can­not pre­vent injury, but may reduce the sever­ity of injury or the prob­a­bil­ity of the injury occur­ring. Complementary pro­tec­tive mea­sures are reac­tive in nature, mean­ing that they are not auto­matic. They must be man­u­ally acti­vated by a user before any­thing will occur, e.g. press­ing an emer­gency stop but­ton. They can only com­ple­ment the pro­tec­tion pro­vided by the auto­matic systems.

A good exam­ple of this is the Emergency Stop sys­tem that is designed into many machines. On its own, the emer­gency stop sys­tem will do noth­ing to pre­vent an injury. The sys­tem must be acti­vated man­u­ally by press­ing a but­ton or pulling a cable. This relies on some­one detect­ing a prob­lem and real­iz­ing that the machine needs to be stopped to avoid or reduce the sever­ity of an injury that is about to occur or is occur­ring. Emergency stop can only ever be a back-​​up mea­sure to the auto­matic inter­locks and safe­guard­ing devices used on the machine. In many cases, the next step in emer­gency response after press­ing the emer­gency stop is to call 911.

Failure Modes:

The fail­ure modes for these kinds of con­trols are too numer­ous to list here, how­ever they range from sim­ple fail­ure to replace a fixed guard or bar­rier fence, to fail­ure of elec­tri­cal, pneu­matic or hydraulic con­trols. These fail­ure modes are enough of a con­cern that a new field of safety engi­neer­ing called ‘Functional Safety Engineering’ has grown up around the need to be able to ana­lyze the prob­a­bil­ity of fail­ure of these sys­tems and to use addi­tional design ele­ments to reduce the prob­a­bil­ity of fail­ure to a level we can tol­er­ate. For more on this, see [9, 10, 11].

Once you have exhausted all the pos­si­bil­i­ties in Engineering Controls, you can move to the next level down in the hierarchy.

3. Information for Use

This is a very broad topic, includ­ing man­u­als, instruc­tion sheets, infor­ma­tion labels on the prod­uct, haz­ard warn­ing signs and labels, HMI screens, indi­ca­tor and warn­ing lights, train­ing mate­ri­als, video, pho­tographs, draw­ings, bills of mate­ri­als, etc. There are some excel­lent stan­dards now avail­able that can guide you in devel­op­ing these mate­ri­als [1, 12 and 13].

Failure Modes:

The major fail­ure modes in this level include:

  • Poorly writ­ten or incom­plete materials;
  • Provision of the mate­ri­als in a lan­guage that is not under­stood by the user;
  • Failure by the user to read and under­stand the materials;
  • Inability to access the mate­ri­als when needed;
  • Etcetera.

When all pos­si­bil­i­ties for inform­ing the user have been cov­ered, you can move to the next level down in the hier­ar­chy. Note that this is the usual sep­a­ra­tion point between the man­u­fac­turer and the user of a prod­uct. This is nicely illus­trated in Fig 2 from ISO 12100 above. It is impor­tant to under­stand at this point that the resid­ual risk posed by the prod­uct to the user may not yet be tol­er­a­ble. The user is respon­si­ble for imple­ment­ing the next two lev­els in the hier­ar­chy in most cases. The man­u­fac­turer can make rec­om­men­da­tions that the user may want to fol­low, but typ­i­cally that is the extent of influ­ence that the man­u­fac­turer will have on the user.

4. Administrative Controls

This level in the hier­ar­chy includes:

  • Training;
  • Standard Operating Procedures (SOP’s);
  • Safe work­ing pro­ce­dures e.g. Hazardous Energy Control, Lockout, Tagout (where per­mit­ted by law), etc.;
  • Authorization; and
  • Supervision.

Training is the method used to get the infor­ma­tion pro­vided by the man­u­fac­turer to the worker or end user. This can be pro­vided by the man­u­fac­turer, by a third party, or self-​​taught by the user or worker.
SOP’s can include any kind of pro­ce­dure insti­tuted by the work­place to reduce risk. For exam­ple, requir­ing work­ers who drive vehi­cles to do a walk-​​around inspec­tion of the vehi­cle before use, and log­ging of any prob­lems found dur­ing the inspec­tion is an exam­ple of an SOP to reduce risk while dri­ving.
Safe work­ing pro­ce­dures can be strongly influ­enced by the man­u­fac­turer through the infor­ma­tion for use pro­vided. Maintenance pro­ce­dures for haz­ardous tasks pro­vided in the main­te­nance man­ual are an exam­ple of this.
Authorization is the pro­ce­dure that an employer uses to autho­rize a worker to carry out a par­tic­u­lar task. For exam­ple, an employer might put a pol­icy in place that only per­mits licensed elec­tri­cians to access elec­tri­cal enclo­sures and carry out work with the enclo­sure live. The employer might require that work­ers who may need to use lad­ders in their work take a lad­der safety and a fall pro­tec­tion train­ing course. Once the pre­req­ui­sites for autho­riza­tion are com­pleted, the worker is ‘autho­rized’ by the employer to carry out the task.
Supervision is one of the most crit­i­cal of the Administrative Controls. Sound super­vi­sion can make all of the above work. Failure to prop­erly super­vise work can cause all of these mea­sures to fail.

Failure Modes

Administrative con­trols have many fail­ure modes. Here are some of the most common:

  • Failure to train;
  • Failure to inform work­ers regard­ing the haz­ards present and the related risks;
  • Failure to cre­ate and imple­ment SOP’s;
  • Failure to pro­vide and main­tain spe­cial equip­ment needed to imple­ment SOP’s;
  • No for­mal means of autho­riza­tion — i.e. How do you KNOW that Joe has his lift truck license?;
  • Failure to super­vise adequately.

I’m sure you can think of MANY other ways that Administrative Controls can go wrong!

5. Personal Protective Equipment (PPE)

PPE includes every­thing from safety glasses, to hard­hats and bump caps, to fire-​​retardant cloth­ing, hear­ing defend­ers, and work boots. Some stan­dards even include warn­ing devices that are worn by the user, such as gas detec­tors and person-​​down detec­tors, in this group.
PPE is prob­a­bly the sin­gle most over-​​used and least under­stood risk con­trol mea­sure. It falls at the bot­tom of the hier­ar­chy for a num­ber of reasons:

  1. It is a mea­sure of last resort;
  2. It per­mits the haz­ard to come as close to the per­son as their clothing;
  3. It is often incor­rectly specified;
  4. It is often poorly fitted;
  5. It is often poorly main­tained; and
  6. It is often improp­erly used.

The prob­lems with PPE are hard to deal with. You can­not glue or screw a set of safety glasses to a person’s face, so ensur­ing the the pro­tec­tive equip­ment is used is a big prob­lem that goes back to supervision.

Many small and medium sized enter­prises do not have the exper­tise in the orga­ni­za­tion to prop­erly spec­ify, fit and main­tain the equipment.

User com­fort is extremely impor­tant. Uncomfortable equip­ment won’t be used for long.

Finally, by the time that prop­erly spec­i­fied, fit­ted and used equip­ment can do it’s job, the haz­ard is as close to the per­son as it can get. The prob­a­bil­ity of fail­ure at this point is very high, which is what makes PPE a mea­sure of last resort, com­ple­men­tary to the more effec­tive mea­sures that can be pro­vided in the first three lev­els of the hierarchy.

If work­ers are not prop­erly trained and ade­quately informed about the haz­ards they face and the rea­sons behind the use of PPE, they are deprived of the oppor­tu­nity to make safe choices, even if that choice is to refuse the work.

Failure Modes

Failure modes for PPE include:

  • Incorrect spec­i­fi­ca­tion (not suit­able for the hazard);
  • Incorrect fit (allows haz­ard to bypass PPE);
  • Poor main­te­nance (pre­vents or restricts vision or move­ment, increas­ing the risk; causes PPE fail­ure under stress or allows haz­ard to bypass PPE);
  • Incorrect usage (fail­ure to train and inform users, incor­rect selec­tion or spec­i­fi­ca­tion of PPE).

Time to Apply the Hierarchy

So now you know some­thing about the ‘hier­ar­chy of con­trols’. Each layer has its own intri­ca­cies and nuances that can only be learned by train­ing and expe­ri­ence. With a doc­u­mented risk assess­ment in hand, you can begin to apply the hier­ar­chy to con­trol the risks. Don’t for­get to iter­ate the assess­ment post-​​control to doc­u­ment the degree of risk reduc­tion achieved. You may cre­ate new haz­ards when con­trol mea­sures are applied, and you may need to add addi­tional con­trol mea­sures to achieve effec­tive risk reduction.

The doc­u­ments ref­er­enced below should give you a good start in under­stand­ing some of these challenges.

References

5% Discount on All Standards with code: CC2011

[1]             Safety of machin­ery – Basic con­cepts, gen­eral prin­ci­ples for design – Part 1: Basic ter­mi­nol­ogy and method­ol­ogy, ISO Standard 12100–1, 2003.
[2]            Safety of machin­ery – Basic con­cepts, gen­eral prin­ci­ples for design – Basic ter­mi­nol­ogy and method­ol­ogy, Part 2: Technical prin­ci­ples, ISO Standard 12100–2, 2003.
[3]            Safety of Machinery – Risk Assessment – Part 1: Principles, ISO Standard 14121–1, 2007.
[4]            Safety of machin­ery — Prevention of unex­pected start-​​up, ISO 14118, 2000
[5]            Control of haz­ardous energy – Lockout and other meth­ods, CSA Z460, 2005
[6]            Fluid power sys­tems and com­po­nents – Graphic sym­bols and cir­cuit dia­grams – Part 1: Graphic sym­bols for con­ven­tional use and data-​​processing appli­ca­tions, ISO Standard 1219–1, 2006
[7]            Pneumatic fluid power — General rules and safety require­ments for sys­tems and their com­po­nents, ISO Standard 4414, 1998
[8]            American National Standard for Industrial Robots and Robot Systems — Safety Requirements, ANSI/​RIA R15.06, 1999.
[9]            Safety of machin­ery — Safety-​​related parts of con­trol sys­tems — Part 1: General prin­ci­ples for design, ISO Standard 13849–1, 2006
[10]          Safety of machin­ery – Functional safety of safety-​​related elec­tri­cal, elec­tronic and pro­gram­ma­ble elec­tronic con­trol sys­tems, IEC Standard 62061, 2005
[11]           Functional safety of electrical/​electronic/​programmable elec­tronic safety-​​related sys­tems, IEC Standard 61508-​​X, seven parts.
[12]          Preparation of Instructions — Structuring, Content and Presentation, IEC Standard 62079, 2001
[13]          American National Standard For Product Safety Information in Product Manuals, Instructions, and Other Collateral Materials, ANSI Standard Z535.6, 2010.
[14]          Control of Hazardous Energy Lockout/​Tagout and Alternative Methods, ANSI Standard Z244.1, 2003.
[15]          Safety of Machinery — Interlocking devices asso­ci­ated with guards — prin­ci­ples for design and selec­tion, EN 1088+A1:2008.
[16]          Safety of Machinery — Guards — General require­ments for the design and con­struc­tion of fixed and mov­able guards, EN 953+A1:2009.
[17]          Safety of machin­ery — Guards — General require­ments for the design and con­struc­tion of fixed and mov­able guards, ISO 14120.
[18]         Safety of machin­ery — Safety dis­tances to pre­vent haz­ard zones being reached by upper and lower limbs, ISO 13857:2008.
[19]         Safety of machin­ery — Positioning of safe­guards with respect to the approach speeds of parts of the human body, ISO 13855:2010.

5% Discount on All Standards with code: CC2011

Understanding Risk Assessment

When peo­ple dis­cuss ‘Risk’ there are a lot of dif­fer­ent assump­tions made about what that means. For me, the study of risk and risk assess­ment tech­niques started in 1995. As a tech­nol­o­gist and con­trols designer, I had to some­how wrap my head around the whole con­cept in ways I’d never con­sid­ered. If you’re try­ing to fig­ure out risk and risk assess­ment this is a good place to get started!

What is risk?

From a machin­ery per­spec­tive, ISO 12100:2010 defines risk as:

com­bi­na­tion of the prob­a­bil­ity of occur­rence of harm and the sever­ity of that harm”

Risk can have pos­i­tive or neg­a­tive out­comes, but when con­sid­er­ing safety, we only con­sider neg­a­tive risk, or events that result in neg­a­tive health effects for the peo­ple exposed.

The risk rela­tion­ship is illus­trated in ISO 12100:2010 Figure 3:


ISO 12100-2010 Figure 3

ISO 12100–2010 Figure 3


Where

R = Risk

S = Severity of Harm

P = Probability of Occurrence of Harm

The Probability of Occurrence of Harm fac­tor is often fur­ther bro­ken down into three sub-​​factors:

  • Probability of Exposure to the haz­ard
  • Probability of Occurrence of the Hazardous Event
  • Probability of Limiting or Avoiding the Harm

How is risk measured?

In order to esti­mate risk a scor­ing tool is needed. There is no one ‘cor­rect’ scor­ing tool, and there are flaws in most scales that can result in blind-​​spots where risks may be over or under-​​estimated.

At the sim­plest level are ‘screen­ing’ tools. These tools use very sim­ple scales like ‘High, Medium, Low’, or ‘A, B, C’. These tools are often used when doing a shop-​​floor inspec­tion and are intended to pro­vide a quick method of cap­tur­ing obser­va­tions and giv­ing a gut-​​feel assess­ment of the risk involved. These tools should be used as a way to iden­tify risks that need addi­tional, detailed assess­ment. To get an idea of what a good screen­ing tool can look like, have a look at the SOBANE Déparis sys­tem.

Every scor­ing tool requires a scale for each risk para­me­ter included in the tool. For instance, con­sider the CSA tool described in CSA Z434:

CSA Z434-03 Table 1As you can see, each para­me­ter (Severity, Exposure and Avoidance) has a scale, with two pos­si­ble selec­tions for each parameter.

When con­sid­er­ing selec­tion of a scor­ing tool, it’s impor­tant to take some time to really exam­ine the scales for each fac­tor. The scale shown above has a glar­ing hole in one scale. See if you can spot it and I’ll tell you what I think a bit later in this post.

There are more than 350 dif­fer­ent scales and method­olo­gies avail­able for assess­ing risk. You can find a good review of some of them in Bruce Main’s text­book “Risk Assessment: Basics and Benchmarks” avail­able from DSE online.

A sim­i­lar, although dif­fer­ent, tool is found in Annex 1 of ISO 13849–1. Note that this tool is pro­vided in an Informative Annex. This means that it is not part of the body of the stan­dard and is NOT manda­tory. In fact, this tool was pro­vided as an exam­ple of how a user could link the out­put of a risk assess­ment tool to the Performance Levels described in the nor­ma­tive text (the manda­tory part) of the standard.

Consider cre­at­ing your own scales. There is noth­ing wrong with deter­min­ing what char­ac­ter­is­tics (para­me­ters) you want to include in your risk assess­ment, and then assign­ing each para­me­ter a numeric scale that you think is suit­able; 1–10, 0–5, etc. Some scales may be inverted to oth­ers, for exam­ple: If the Severity scale runs from 0–10, the Avoidability scale might run from 10–0 (Unavoidable to Entirely Avoidable).

Once the scales in your tool have been defined, doc­u­ment the def­i­n­i­tions as part of your assessment.

Who should con­duct risk assessments?

Lake YogaIn many orga­ni­za­tions, I find that risk assess­ment has been del­e­gated to one per­son. This is a major mis­take for a num­ber of rea­sons. Risk assess­ment is not a solo activ­ity for a ‘guru’ in a lonely office somewhere!

Risk assess­ment is not a lot of fun to do, and since risk assess­ments can get to be quite involved, it rep­re­sents a sig­nif­i­cant amount of work to put on one per­son. Also, leav­ing it to one per­son means that the assess­ment will nec­es­sar­ily be biased to what that per­son knows, and may miss sig­nif­i­cant haz­ards because the asses­sor doesn’t know enough about that haz­ard to spot it and assess it properly.

Risk assess­ment requires mul­ti­ple view­points from par­tic­i­pants with var­ied exper­tise. This includes users, design­ers, engi­neers, lawyers and those who may have spe­cial­ized knowl­edge of a par­tic­u­lar haz­ard, like a Laser Safety Officer or a Radiation Safety Officer. The var­ied exper­tise of the peo­ple involved will allow the com­mit­tee to bal­ance the opin­ion of each haz­ard, and develop a more rea­soned assess­ment of the risk.

I rec­om­mend that risk assess­ment com­mit­tees never be less than three mem­bers. Five is fre­quently a good num­ber. Once you get beyond five, it becomes increas­ingly dif­fi­cult to obtain con­sen­sus on each haz­ard. Also, con­sider the cost. As each com­mit­tee mem­ber is added to the team, the cost of the assess­ment can esca­late exponentially.

Training in risk assess­ment is cru­cial to suc­cess. Ensure that the indi­vid­u­als involved are trained, and that at least one has some pre­vi­ous expe­ri­ence in the prac­tice so that they may guide the com­mit­tee as needed.

When should a risk assess­ment be conducted?


Risk Assessment Lifetime Flow Chart

Risk Assessment in the Lifetime of a Product


Risk assess­ment should begin at the begin­ning of a project, whether it’s the design of a prod­uct, the devel­op­ment of a process or ser­vice, or the design of a new build­ing. Understanding risk is crit­i­cal to the design process. Cost for changes made at the begin­ning of a project are min­i­mal com­pared to those that will be incurred to cor­rect prob­lems that might have been fore­seen at the start. Risk assess­ment should start at the con­cept stage and be included at each sub­se­quent stage in the devel­op­ment process. The accom­pa­ny­ing graphic illus­trates this idea.

Essentially, risk assess­ment is never fin­ished until the prod­uct, process or ser­vice ceases to exist.

What tools are available?

As men­tioned ear­lier in this post, the book ‘Risk Assessment: Basics and Benchmarks” pro­vides an overview of roughly 350 dif­fer­ent scor­ing tools. You can search the Internet and turn up quite a few as well. The key thing with all of these sys­tems is that you will need to develop any soft­ware based tools your­self. Depending on your com­fort with soft­ware, this might be a spread­sheet for­mat, a word pro­cess­ing doc­u­ment a data­base, or some other for­mat that works for your application.

There are a num­ber of risk assess­ment soft­ware tools avail­able as well, includ­ing ISI’s CIRSMA and DSE’s DesignSafe. As with the scor­ing tools, you need to be care­ful when eval­u­at­ing tools. Some have sig­nif­i­cant blind spots that may trip you up if you are not aware of their limitations.

Remember too that the out­put from the soft­ware can only be as good as the input data. The old saw “Garbage In, Garbage Out” holds true with risk assessment.

Where can you get training?

There are a few places to get train­ing. Compliance InSight Consulting pro­vides train­ing to cor­po­rate clients and will be launch­ing a series of web-​​based train­ing ser­vices in 2011 that will allow indi­vid­ual learn­ers to get train­ing too.

The IEEE PSES oper­ates a Risk Assessment Technical Committee that is open to the pub­lic as well. See the RATC web site.

The Answer to the Scale Question

The Exposure Scale in the CSA tool has a gap between E1 and E2. Looking at the def­i­n­i­tions for each choice, notice that E1 is less than once per day or shift, while E2 is more than once per hour. Exposures that occur once per hour or less, but more than once per day can­not be scored effec­tively using this scale.

Also, notice the Severity scale: S1 encom­passes injuries requir­ing not more than basic first aid. One com­mon ques­tion I get is “Does that include CPR*?”. This ques­tion comes up because most basic first aid courses taught in Canada include CPR as part of the course. There is no clear answer for this in the stan­dard. The S2 fac­tor extends from injuries requir­ing more than basic first aid, like a bro­ken fin­ger for instance, all the way to a fatal­ity. Does it make sense to group this broad range of injuries together? This def­i­n­i­tion doesn’t quite match with the Province of Ontario’s def­i­n­i­tion of a Critical Injury found in Regulation 834 either.

All of this points to the need to care­fully assess the scales that you choose before you start the process. Choosing the wrong tool can skew your results in ways that you may not be very happy about.

*Cardio-​​Pulmonary Resuscitation

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