Will never break down or deteriorate

Requires replacement after 10 years

Will deteriorate due to high temperatures

Will not burn

Class I, Division I

Class I, Division II

Class II, Division I

Class II, Division II

Allowing motors or conductors to stay dry, unless designed for wet locations

Prematurely replacing deteriorated wiring

Following too closely to the Electrical Code when installing electrical equipment

Replacing burned fuses with ones of a higher rating

Allowing the accumulation of dust on a motor since this buildup will prevent heat from escaping, thus keeping the motor warm in cold ambient conditions

Keeping electrical equipment dry unless designed for wet locations

Using the equipment designed for the application

Checking any aluminum connections frequently for tightness and presence of corrosion

need only make contact, they need not be tight

will create large amounts of heat if not tight

can cause an arc if too tight

may operate on overload for specified duration

the equipment may be left running if the fire is put out with a C type fire extinguisher

the equipment should be de-energized as quickly as possible

the equipment should be left running until a backup power supply is available

the equipment may be immediately restarted once the fire is extinguished

pressurized water extinguisher

dry chemical extinguisher

purple K extinguisher

carbon dioxide extinguisher

0 degrees C

-30 degrees C

-60 degrees C

-80 degrees C

all fuses in the electrical system be replaced

aluminium wiring be replaced

all electrical panels be checked for tightness and corrosion

all circuit breakers be disassembled and cleaned

the type of hazardous material involved.

the capacity of electrical equipment involved.

the type of fire extinguishers available

pressure

the air is dry.

any moisture is present.

it is directed at the base of the flame.

it is non-conductive.

installed in a sealed compartment.

be explosion proof.

electrically insulated.

of an ABSA approved design.

Closing an electrical breaker.

Shutting down a motor too quickly.

Low voltage at a generator.

A loose electrical connection.

Class 1, Division 1

Class 1, Division 2

Class 2, Division 2

Class 3, Division 1

Class 1, Division 1

Class 1, Division 2

Class 2, Division 2

Class 3, Division 1

Class 1, Division 1

Class 2, Division 1

Class 1, Division 2

Class 3, Division 1

Class 1, Division 1

Class 1, Division 2

Class 2, Division 2

Class 3, Division 2

Class 2, Division 2

Class 2, Division 1

Class 1, Division 2

Class 3, Division 1

Class 3, Division 1

Class 3, Division 2

Class 1, Division 2

Class 2, Division 2

I*R

R^2*I

I^2*R

I^2*R^2

Class A

Class B

Class C

Class A, B or a combination of both

2.2 to 9

2.1 to 9

2.2 to 10

2.1 to 10

1898

1951

1942

1899

1898

1952

1941

1899

1898

1951

1942

1899

1898

1951

1942

1899

1898

1951

1942

1899

15

30

60

22

103 kpa

30 psi

1034 kpa

121 psi

1100 kPa, 121 degrees C

103 kPa, 121 degrees C

1034 kPa, 130 degrees C

103 kPa, 230 degrees C

1000 kW

100 kW

5000 kW

10,000 kW

1000 kW

5000 kW

10,000 kW

500 kW

1000 kW

5000 kW

10,000 kW

100 kW

1000 kW

10,000 kW

5000 kW

200 kW

1000 kW

10,000 kW

5000 kW

500 kW

5000 kW, 140 kPa

1000 kW, 103 kPa

10,000 kW, 30 psi

500 kW, 15 psi

CSA B52

CSA B51

ASME Section II

ASME Section VI

CSA B52

CSA B51

ASME Section III

ASME Section VI

Section I

Section IV

Section VI

Section II

Section II

Section I

Section III

Section V

Section VI

Section III

Section IV

Section I

Section V

Section VII

Section IV

Section I

Section V

Section III

Section II

Section VI

Section VII

Section II

Section IV

Section VI

Section VII

Section XI

Section VIII

Section V

Section V

Section III

Section VIII

Section I

Section IX

Section X

Section II

Section VI

Boiler and Pressure Vessel Committee

ASME

ABSA

CRN

ASME

ABSA

CSA

CRN

The National Board of Boiler and Pressure Vessel Inspectors.

ASME

CRN

ISO

Quebec

Alberta

Ontario

Newfoundland

A, B and C

1, 2 and 3

L, A, J

None of the above

50 Deg C

100 Deg C

0 Deg C

-40 Deg C

compressed gas

flammable gas

flammable liquid

combustible liquid

flammable

toxic

oxidizing

all of the above

oxidizing

flammable

toxic

compressed gas

Oxidizing

Toxic

flammable

compressed gas

<37.8 Deg C

>37.8 Deg C

between 37.8 & 93.3 Deg C

None of the above

<37.8 Deg C

> 37.8 Deg C

between 37.8 and 93.3 Deg C

None of the above

corrosive

toxic

flammable

oxidizing

hazardously reactive

oxidizing

flammable

compressed gas

to protect the secrecy of a manufacturer's formula

safety for workers and employers

to set legal precedent on hazardous materials

all of the above

3 years

2 years

1 year

10 years

flaming

combustion

flameless

spontaneous

flameless

flaming

oxidizing

spontaneous

10%

5%

20%

15%

5%

15%

25%

10%

21%

20%

10%

100%

impaired motor coordination

death

possible unconsiousness

difficulty breathing

impaired judgement, fatigue

impaired motor coordination, difficulty breathing

loss of consciousness, death

all of the above

lose consciousness

die

become sick

lose sight

It is the ratio of the weight of a product's vapour to the weight of air.

It is the ratio of the weight of a product's vapour to the specifc gravity.

It is the ratio of the weight of a product's vapour to the molar mass.

It is the ratio of the weight of a product's vapour to oxygen.

It is the ratio of the evaporation rate of a product to the evaporation rate of normal air.

It is the ratio of the evaporation rate of a product to the evaporation rate of hydrogen.

It is the ratio of the evaporation rate of a product to the evaporation rate of normal Butyl acetate.

It is the ratio of the evaporation rate of a product to the evaporation rate of isopropol alcohol.

It is the ratio of the weight of a volume of a controlled product to the weight of an equal volume of air at a specified temperature.

It is the ratio of the weight of a volume of a controlled product to the weight of an equal volume of hydrogen at a specified temperature.

It is the ratio of the weight of a volume of a controlled product to the weight of an equal volume of oxygen at a specified temperature.

It is the ratio of the weight of a volume of a controlled product to the weight of air at a specified temperature.

1.6 (it falls in air)

1.6 (it rises in air)

0.8 (it falls in air)

0.8 (it rises in air)

7.5 (it will sink in water)

10 (it will sink in water)

0.75 (it will rise in water)

75 (it will sink in water)

0.8 (it will float on water)

8 (it will float on water)

80 (it will sink on water)

8 (it will sink on water)

31.03 MPa

5 MPa

103 MPa

62.06 MPa

efficiency

labour mobility

safety

pollution

foaming

filming

an interface

scaling

experts from the industry, professional and insurance
groups and all levels of government

only multi-National power corporations

one independent safety and standardisation board

only experts from the industry and government

Take charge of the general care and operation of a power
plant consisting of one or more coil type drumless boilers having an aggregate capacity not over 5,000 kW,when only in use for the purpose of subterranean thermal flooding in oil fields, as chief engineer.

Take charge of a shift in a power plant having a capacity
of MORE than 10,000 kW, as shift engineer.

Take charge of the general care and operation of a powerplant having a capacity of not more than 1,000 kW as
chief steam engineer, and to supervise the engineers in that plant.

Take charge of a shift in a power plant consisting of one or more coil type drumless boilers having an aggregate capacity of not more than 10,000 kW, when used only for underground thermal flooding in oil fields, as shift engineer.

au

lux

cd

lumen

1 joule

1 N/ m^2

1 kg/ cm^2

1 kg/ m^2

1 pascal/m2

1 N/m2

1 joule/second

1 kilojoule/minute

172.06 r/min

344 r/min

294 r/min

1.1 r/min

prevent injury to the worker

prevent massive condensation of the steam within the tank

flush the tank gradually

reduce the risk of static electricity spark

pyrophoric effect

static electric charge buildup

catalytic effect of the fresh metallic surface

temperature of the mixture

5.0 to 15.0 %

2.2 to 9.5 %

1.9 to 8.5 %

1.1 to 7.5 %

5.0 to 15.0 %

2.2 to 9.5 %

1.9 to 8.5 %

1.1 to 7.5 %

5.0 to 15.0 %

2.2 to 9.5 %

1.9 to 8.5 %

1.1 to 7.5 %

5.0 to 15.0 %

2.2 to 9.5 %

1.9 to 8.5 %

1.1 to 7.5 %

0.7 to 5.0 %

2.2 to 9.5 %

1.9 to 8.5 %

1.1 to 7.5 %

0.7 to 5.0 %

4.3 to 45.5 %

1.9 to 8.5 %

1.1 to 7.5 %

-60 Deg

-45 Deg

58 Deg

49 Deg

-60 Deg C

-45 Deg C

54 Deg C

49 Deg C

-60 Deg C

-45 Deg C

58 Deg C

49 Deg C

-60 Deg C

-45 Deg C

58 Deg C

49 Deg C

650 Deg C

480 Deg C

490 Deg C

295 Deg C

650 Deg C

490 Deg C

480 Deg C

295 Deg C

650 Deg C

490 Deg C

480 Deg C

295 Deg C

650 Deg C

490 Deg C

480 Deg C

295 Deg C

340 Deg C

490 Deg C

480 Deg C

295 Deg C

650 Deg C

260 Deg C

480 Deg C

295 Deg C

257 Deg C

210 Deg C

571 Deg C

500 Deg C

257 Deg C

210 Deg C

571 Deg C

500 Deg C

257 Deg C

210 Deg C

571 Deg C

500 Deg C

257 Deg C

210 Deg C

571 Deg C

500 Deg C

257 Deg C

210 Deg C

571 Deg C

500 Deg C

At equal temperatures

Bonded together

The same size

All of the above

High to low loading

Flash point loading

Switch loading

None of the above

Hand brake and wheels must be chocked on the railway car

Washing steam should enter the tank slowly to reduce the risk

Grounding connections must be in good condition

Trucks don't need to be grounded when the loading spout is inserted.

Compartments don't need to be inspected if the product being loaded is different from the previous load

To prevent switch loading compartments should be purged with carbon dioxide

Deflector should be installed on a loading spout

One minute before withdrawing the spout after loading a tank.

Deflector should be installed on a loading spout

At least five minutes after loading samples must not be obtained

One minute before withdrawing the spout after loading a tank.

Compartments need to be inspected if the product being loaded is different from the previous load

Truck or Tank car must contain air before being loaded

Containers must be designed for the right type of LPG product being transported

Before loading a check should be made to ensure liquids from a previous load are not present

LPG containers should never be filled completely.

Outages left in LPG containers must conform to local regulations.

Loading hoses must be hydro statically tested every two years.

Container must be not over pressured

Before loading LPG the correct type of product must be verified

It is easier to load and unload the LPG

Ensure relief valve connection is not flooded

Both of the above

None of the above

If hydrogen sulphide might be present, three workers should be assigned to the job

Tanks should not be gauged when thunderstorms are approaching

Defects in ladders and stairways should be reported

Thief ropes or cords, may be allowed in some situations

10 minutes

20 minutes

30 minutes

40 minutes

1 cm

1.5 cm

2 cm

2.5 cm

Liquid expands due to a temperature increase

Liquid explodes due to a temperature increase

Both of the above

None of the above

Read the rotary gauge on the side of the tank

Weighing the unit before and after filling

Using temperature - corrected meters

All of the above

Space left above the surface of the liquid

Amount of liquid left

Temperature of the liquid

None of the above

lethal dose which results in death of 50% of the test population

lethal concentration which resulted in death of 50% of the test population

lethal concentration diluted to half strength and supplied to the test population

legal exposure in which 50% of the test population survived

100 ppm

20 ppm

10 ppm

15 ppm

pre-accident safety record

attitude before and after the accident

lifestyle off the job

support received from the immediate family

management only

employees only

owners only

all persons in the workplace

26 to 35 years

16 to 25 years

36 to 45 years

46 to 55 years

principle contractor

general contractor

sub-contractor

building contractor

indefinitely

until the officer arrives at the scene

for a maximum of 48 hours

until any serious safety hazards are corrected

$150,000.00 fine

one year in jail

500,000.00 fine and/or one year in jail

$300,000.00 fine and one year in jail

too much noise to withstand

equipment being used to become a hazard

the worker to refuse to perform his job

moisture vapours to be released in the atmosphere

difficult place in which to maneuver

breeding ground for biohazardous infectious substances

life threatening environment

healthy environment

verify the operator's isolation points though the Plant Safety Committee

estimate how long you will be there

inform the Plant Manager of your whereabouts

plan the entry using a confounded entry space check list

Is the required oxygen level measured and assured (minimum level of 20% O2 by volume)?

Is the temperature in the space within tolerable working limits?

Is the confined space structurally safe to enter?

Has the head of the plant safety department been notified?

harmful gases, vapours, mist, or dust

no way out

limited room for tools and equipment

restricted entry and exit

ambient air temperatures

proper lighting

proper air ventilation

a simple means of entry

8%

10%

15%

20%

Occupational Health and Safety Act

Boiler and Pressure Vessels Regulation

Workers' Compensation Act

Provincial Firemans Regulation

a self-contained breathing apparatus

an approved fire extinguisher

permission from OH&S to be there

to be in communication with another worker nearby

to retrieve tools or equipment for the worker

only long enough to go to the washroom

only when properly relieved by another qualified person

for ten minutes every hour

wear approved respiratory protective equipment

wait until the gases dissipate

receive special permission from OH&S before entering

wear a safety belt and lifeline