| INTRODUCTION
This manual provides information
for reducing the risks associated with the handling and storage
of acetone. While it is not intended to be a comprehensive
examination of all possible acetone safety issues, it does
provide direction to enable individuals who manufacture, use,
store, transport, dispose, recycle and/or reclaim this chemical
to do so properly.
Acetone is an oxygenated
hydrocarbon belonging to the ketone family. Its primary uses are
as an industrial solvent and as an intermediate in the
production of methyl methacrylate, methylisobutyl ketone, and
methylisobutyl carbinol. Acetone is not known to have chronic or
cumulative effects on humans. It is considered extremely
flammable and its vapors may become explosive when mixed with
air.
USE
OF THIS DOCUMENT
This technical guidance manual for handling
acetone is offered solely for your information, consideration, and investigation. This manual is for general informational purposes only. Since every situation is unique, and
acetone is hazardous if not handled appropriately, you must consult qualified technical and engineering personnel to evaluate your specific situation and answer any specific questions you may have. Sunoco disclaims all warranties, either expressed or implied, assumes no responsibility for the accuracy or completeness of the data contained herein, and will not be liable for any personal injury, property damage, environmental harm or legal noncompliance that may result from reliance upon this document or your management of
acetone.
SAFETY
Acetone should always be handled,
stored, and used with precautions against fire and explosion.
Acetone is a flammable liquid with flammable limits of 2.6 to
12.8 vol% at 25°C. Solutions of acetone and water can be
flammable. Since
acetone vapors travel with air currents, they can be ignited by
flames and sparks at locations remote from the site at which the
material is being handled. Smoking should be prohibited since
prolonged exposure to acetone may cause the chemical to remain
on clothing.
Appropriate safety gear should
always be worn when handling acetone. This includes safety
glasses with cup-type side shields or chemical goggles, safety
shoes, natural rubber, or neoprene gloves, and hard hat. In
unusual or emergency situations when contact with the liquid is
necessary or likely, the handler should wear full protective
equipment and clothing. All contaminated clothing must be washed
before reuse. Protective equipment and clothing should be
decontaminated or disposed of according to the manufacturers
instructions.
In case of eye contact with
acetone, wash with copious amounts of water for at least 15
minutes, occasionally lifting the lower and upper lids. Obtain
medical attention promptly. In case of skin contact, wash with
water for at least 15 minutes. If inhaled, remove the patient
from contaminated atmosphere to fresh air. If not breathing,
give artificial respiration, preferably mouth-to-mouth. If
breathing is difficult, give oxygen which is administered only
by trained personnel. Get prompt medical attention.
For more detailed information on
first aid and the safe handling of acetone, refer to the
Material Safety Data Sheet which can be provided to you by
Sunoco in compliance with OSHA hazard communication regulations.
EMERGENCY
PROCEDURES
SPILL OR
LEAK: Eliminate all sources of ignition in the
vicinity of a spill or released vapors. Isolate the area. Permit
only trained personnel wearing full protective clothing and
equipment to enter the spill area. Terminate the leak
immediately, if possible. Collect the contaminated soil, debris,
clothing, etc., into a waste container for disposal. Flush the
spill area thoroughly with water and wash all contaminated
equipment. All flushing and wash water must be contained and
prevented from entering a waterway. Ventilate the area to
disperse vapors.
Spills of acetone in excess of
its Reportable Quantity (RQ) should be reported to the
appropriate federal, state, and local environmental agencies,
including The National Response Center (800-424-8802). Consult
Material Safety Data Sheet for the Reportable Quantity.
FIRE
EXTINGUISHING AGENTS
|
Small Fires:
|
Use carbon
dioxide or dry chemical..
|
| Large
Fires:
|
Use
polar solvent (alcohol) type foam. The normal fire
fighting foams that are suitable for gasoline or
hydrocarbon fires will break down and will not
extinguish acetone fires. Use water spray to reduce
intensity of flames.
|
SPECIAL
FIRE FIGHTING PRECAUTIONS
Handle acetone as a very
flammable liquid. Use water spray to keep fire-exposed tanks and
containers cool. Do not enter
the fire area without proper personal protective equipment,
including a self-contained breathing apparatus.
RECOMMENDATIONS
FOR STORAGE SYSTEMS
For the safe storage of acetone,
portable tanks not exceeding 660 gallons and containers not
exceeding 60 gallons must comply with National Fire Protection
Association (NFPA) Code 30, Chapter 4 and the Occupational
Safety and Health Administration (OSHA) regulation 1910.106.
Leaks are difficult to detect in underground tanks but if it is
necessary to use such tanks, they must also conform to the above
mentioned codes and all federal, state and local regulations.
Acetone is a Class 1 flammable
liquid. Bulk storage tanks are not to be located inside
buildings unless built in accordance with the process tank
provisions of the NFPA code.
The design of storage tanks must
conform to the principles of good engineering practice. Tanks
can be either horizontal or vertical and in any shape consistent
with good design principles. Acetone can be stored in tanks
designed for the following pressure ranges and standard:
|
TYPE |
PRESSURE
RANGE |
STANDARD |
|
|
Atmospheric |
0 - 0.5 PSIG |
API 650 |
|
Low Pressure |
0.5 - 15 PSIG |
API 620 |
|
Pressure Vessel
|
>15 PSIG |
ASME Boiler & Pressure
Vessel Code for Unfired Pressure Vessels
Sec. VIII, Div. 1
|
|
Floating Roof |
|
API 650 |
|
Pressure tanks built according to
ASME code are preferred over atmospheric tanks if acetone is to
be stored at or near its boiling point (56.2°C). In the case of
atmospheric tanks, provisions must be made for inbreathing
(vacuum relief) and outbreathing (pressure relief) in the form
of a combination pressure/vacuum relief valve whose size is
based on the vent rates established by NFPA 30, Flammable &
Combustible Liquids Code. Tanks should not have steam coils.
Open vents should not be used
with acetone since its flash point is below 100°F. When
designing vents, the minimum for venting that should be used is
contained in NFPA 30, Flammable & Combustible Liquid Code.
For inbreathing, vacuum relief API 2000 should be used.
Note: The inbreathing sizing as
called for in API 2000 is not adequate for the situation where a
steam tank is subject to sudden cooling. For most tanks,
emergency vents are required to protect against fire exposure.
Although protection can be achieved by the use of additional P/V
valves, a gauge hatch or manhole cover
that lifts when exposed to abnormal pressure is normally used.
Again, tanks used for acetone storage will not usually have
steam coils.
It is recommended that tanks
larger than 10,000 gallons be equipped with either an internal
or an external floating roof to prevent the accumulation and
loss of vapor.
Because of the high vapor
pressure of acetone (2.5 PSIA at 20°C) federal regulations
require that tanks larger than 20,000 gallons which were
constructed, reconstructed or modified after July 23, 1984 have
a floating roof or have a vapor recovery system to minimize
emissions.
NOTE:
Floating roof tanks need a double closure seal to eliminate the
space between the roof edge and wall. The design of floating
roof tanks is covered by API Standard 650.
Acetone storage tanks may be
painted white to minimize radiational heating by sunlight. Tanks
should also not be filled to the top as acetone will expand as
temperatures rise in warmer weather.
NOTE:
Check for any additional requirements mandated by State or Local
regulations.
AUXILIARY
EQUIPMENT AND INSTRUMENTATION
All storage tank systems should
be equipped with instrumentation to monitor temperature and
level, as well as a high-level alarm if possible. Centrifugal
pumps are preferred for transferring acetone. Avoid using
positive displacement type pumps since acetone provides minimum
lubrication to the internal parts. Fire safe valves, which can
be plug, gate, ball, or other types capable of providing tight
shut-off consistent with ANSI Standard B31.3 or ANSI B31.4l,
could be used. Plastic valves should not be used since they
typically do not provide adequate fire protection and may not be
compatible with acetone. Sufficient valves are required to
control flow into and discharge from the tank under normal and
emergency conditions.
A water spray system may be
installed consistent with NFPA 12 since acetone/water mixtures
are flammable. All tanks should have connections for the
introduction of polar solvent (alcohol) type foam. Floating roof
tanks need connections near the seal area.
Electrical equipment used should
meet the requirements of the NEC (NFPA 70) Class I, Group D.
Additional information can be found in NFPA 30, The Flammable
& Combustible Liquids Code and NFPA 497A Recommended
Locations for Electrical Installations in Chemical Process
Areas, which give the minimum requirements for proper
classification.
In dealing with static
electricity problems refer to NFPA 77, Recommended Practice on
Static Electricity, and NFPA 780, Lighting Protection Code.
In order to minimize problems
from static electricity arising from the loading and unloading
of acetone, grounding and bonding procedures should be used.
(Refer to NFPA 77).
Location of tanks with respect to
each other and property lines need to conform with NFPA Standard
30.
Provisions for containment of
spills from tanks must also be made in accordance with this
standard. An approved fire alarm system is required and a public
alarm box is recommended. The number of portable fire
extinguishers on hand should be consistent with the particular
hazard.
MATERIALS
FOR CONSTRUCTION
Carbon steel or stainless steel
are the preferred materials for construction of tanks, pumps,
and piping components. If diacetone alcohol or mesityl oxide are
of concern, stainless steel is preferred. Gaskets may be made of
expanded TFE or TFE-gylon 3510. Aluminum can be used as the
floating roof material. TFE wrapped urethane foam inserted with
polypropylene fingers that bolt to the floating roof provide an
effective perimeter seal for the roof.
NOTE:
Acetone is a solvent for many elastomers. Therefore, the sealing
material for a floatiang roof closure must be selected
carefully. It is recommended that all construction materials
used for equipment or containers be checked for acetone
compatibility.
TRANSPORTATION
INFORMATION
| US
DOT Hazardous Class: |
Class
3 - Flammable Liquid, Appendix A (171.101) |
| US
DOT ID Number: |
UN
1090 |
| Proper
Shipping Description: |
Acetone,
3, UN 1090, PG II, (RQ 5000) |
|
|
|
|
HANDLING
BULK DELIVERIES
Guidelines for loading and
unloading bulk deliveries are covered in NFPA 30, Chapter 5.
Systems must also comply with DOT Regulation 49 CFR 172.312 and
172.402.
Loading and unloading facilities
should be at least 25 feet from other buildings and warehouses.
When using compressed gas for transferring, refer to NFPA 30,
Paragraph 5-4.1.4, which allows the use of inert gas for Class 1
flammable liquids. When loading acetone into rail cars or tank
cars, install a vapor recovery system to minimize emissions. In
addition, provide grounding and bonding facilities for
protection from static sparks while loading and unloading.
Before loading or unloading a
bulk delivery always check the storage tank to insure that it
has sufficient available space. Monitor the tank level at all
times during filling and be prepared to stop the flow
immediately if necessary. High level alarms and shutdown may be
installed.
Samples should not be taken
through the dome immediately after filling (Refer to NFPA 77).
MAINTENANCE
AND INSPECTIONS
The volatile properties of
acetone make maintenance and inspection procedures especially
critical. Personnel should routinely observe for possible leaks
from valves, pump fittings, and storage tanks. Inspect all
atmospheric tanks internally every 10 years or when operational
problems arise. Floating roofs should be inspected every 5
years. Annually compare ultrasonic measurements or tank material
thickness to monitor the corrosion rate of the tank walls. It is
instructive to conduct a visual inspection of all welds at this
time as well. If potential problem areas are observed, tests
and/or an X-ray inspection should follow with repairs made
accordingly.
Specific maintenance procedures
for other equipment are available from its manufacturer. Testing
of all systems must be in accordance with applicable codes,
including ANSI B#1 as defined in NFPA 30.
Piping specifications can be
found in NFPA 30, Section 3-3, (ANSI B31 & B31.4).
|
REFERENCES
|
|
| 1. |
American Petroleum Institute, Recommended Rules for
the Design and Construction of Large, Welded, Low
Pressure Storage Tanks, Standard No 620. |
| 2. |
American Petroleum Institute, Welded Steel Storage for
Oil Storage, Standard No. 620. |
| 3. |
American Petroleum Institute, Venting Atmospheric and
Low Pressure Storage Tanks, Standard No. 2000. |
| 4. |
American Society of Mechanical Engineers, ASME
Boiler and Pressure Vessel Code, Code for Unfired
Pressure Vessels, Sec.VIII,
Div. 1. |
| 5. |
National Fire Protection Association, NFPA 13,
Installation of Sprinkler System. |
| 6. |
National Fire Protection Association, NFPA 15,
Standard for Water Spray Fixed System. |
| 7. |
National Fire Protection Association, NFPA 30,
Flammable and Combustible Liquid Code. |
| 8. |
National Fire Protection Association, NFPA 69,
Explosion Prevention Systems. |
| 9. |
National
Fire Protection Association, NFPA 77, Recommended
Practice on Static Electricity. |
| 10. |
National
Fire Protection Association, NFPA 780, Lighting
Protection Code. |
| 11. |
National
Fire Protection Association, NFPA 704, Identification
of Fire Hazards of Materials. |
| 12. |
Occupational
Safety and Health Administration, OSHA Regulation 29
CFR 1910.106. |
| 13. |
Department
of Transportation, DOT Regulations: 49 CFR 172.312 and
49 CFR 172.402. |
| 14. |
American
National Standard Institute, ANSI B31, Code for
Pressure Piping. |
| 15. |
Underwriters
Laboratories Inc., Standard for Steel Aboveground
Tanks for Flammable Liquids. |
|
|
|
NOTE: The latest editions of all listed references should
be checked.
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