Subpart H Hazardous Materials

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Presentation transcript:

Subpart H Hazardous Materials 1910.101-126 2-hour Lesson Sam Mason, CMfgT, CSTM Authorized OSHA Trainer Morehead State University

Subpart H - Hazardous Materials (1910.101 - 126) Class I liquids - Dispensing * Compressed gases - Handling, storage and use * Spray booth - Air velocity * Standard: 1910. Spray areas – Free from combustible residue * Sources of ignition - Precautions * *Average number of Federal OSHA citations issued

1910.101(a) Compressed gases Inspection of compressed gas cylinders: Employer shall determine that compressed gas cylinders under his control are in a safe condition to the extent that this can be determined by visual inspection Use Department of Transportation 49 CFR parts 171-179 where applicable, or Compressed Gas Association Pamphlets C-6-1968 and C-8-1962 Applicable to suppliers & distributors filling compressed gas cylinders

. Compressed gas cylinder types High Pressure Cryogenic Low Pressure Acetylene . Porous Mass Fusable Plug Very Cold Liquid AR O2 H2 N2 CO2 CL2 NO2 Acetone Solvent 42% Volume P>900psig P<900psig

Gas suppliers advise users to: Check cylinders as they are received Verify labels, tags and shipping papers Reject and return cylinders with obvious damage Determine required caps & plugs in place

Bulged - cylinder wall failure CGA C-6 1968 3.2.6 - Bulges: Cylinders are manufactured with reasonably symmetrical shape Cylinder which have definite bulges shall be removed from service Bulged - cylinder wall failure

Cylinder burst after fire exposure CGA C-6 1968 Cylinder burst after fire exposure 5.3.7 - Fire Damage: Cylinders shall be carefully inspected for evidence of exposure to fire Evidence includes: Charring or burning of paint Burning or scarfing of the metal Distortion of the cylinder Burning or melting of a valve

Gouge with deposit of weld metal Burn Cut Gouge Gouge with deposit of weld metal

General corrosion with pitting - reducing cylinder strength

1910.101(b) Compressed gases The in-plant handling, storage, and utilization of all compressed gases in cylinders, portable tanks, rail tankcars, or motor vehicle cargo tanks shall be in accordance with Compressed Gas Association (CGA) Pamphlet P-1-1965

CGA P-1 1965 Section 3.1; General 3.1.14 Never tamper with the safety relief devices in valves or cylinders 3.1.15 Never attempt to repair or to alter cylinders, valves, or safety relief devices

CGA P-1 1965 Section 3.1; General 3.1.16 Never use cylinders as rollers, supports, or for any other purpose than to contain the contents as received Big & heavy

CGA P-1 1965 Section 3.1; General 3.1.17 Keep cylinder valve closed at all times, except when cylinder is in active use 3.1.18 Notify owner of cylinder if any condition has occurred which might permit any foreign substance to enter the cylinder or valve: Provide details of incident Provide the cylinder serial number

CGA P-1 1965 Section 3.1; General 3.1.19 Do not place cylinders where they might become part of an electric circuit When cylinders are used in conjunction with electric welding, precautions must be taken against accidentally grounding cylinders and allowing them to be burned by electric welding arc

P-1 Section 3.2 Moving cylinders 3.2.2 Do not lift cylinders by the cap 3.2.3 Never drop cylinders nor permit them to strike against each other or against other surfaces violently

P-1 Section 3.2 Moving cylinders Lifting magnet 3.2.4 Never handle a cylinder with a lifting magnet 3.2.5 Avoid dragging or sliding cylinders

P-1 Section 3.2 Moving cylinders 3.2.6 Use suitable hand truck, fork truck, roll platform or similar device with cylinder firmly secured for transporting and unloading

Fire is a threat to containment! P-1 3.3 Storing cylinders 3.3.6 Do not store cylinders near highly flammable substances such as oil, gasoline or combustible waste Fire is a threat to containment! MEK

P-1 3.3 Storing cylinders 3.3.8 Do not store cylinders near elevators or gangways, or in locations where heavy moving objects may strike or fall on them LP gas stored near exit

P-1 3.4 Withdrawing cylinder content 3.4.2 If cylinder content is not identified by marking, return cylinder to the supplier without using I’m not labeled!! ACME Cylinder Co

P-1 3.4 Withdrawing cylinder content 3.4.4 Before using a cylinder, be sure it is properly supported to prevent it from being knocked over

P-1 3.4 Withdrawing cylinder content 3.4.5 Suitable pressure regulating devices must be used 3.4.6 Never force connections 3.4.7 Where compressed gas cylinders are connected to a manifold, all related equipment, such as regulators, must be of proper design

P-1 3.4 Withdrawing cylinder content 3.4.8 Do not mix regulators, gages, hoses and other appliances provided for use with a particular gas or group of gases with incompatible materials/gases

P-1 3.4.9 Safe work practices Open cylinder slowly Point valve opening away from yourself & others Never use wrenches or tools except those provided by the supplier or approved by the gas manufacturer Avoid the use of a wrench on a valve equipped with a handwheel

P-1 3.4.9 Safe work practices Never hammer on the valve wheel Frozen, corroded valves; contact the supplier Use check valves if cylinder is apt to be contaminated by feedback of materials Before removing a regulator, close the cylinder valve and release all the pressure from the regulator

Twenty feet from flammable or combustible materials P-1 3.5 Flammable gases Indoor cylinder storage Well protected Well insulated Dry Twenty feet from flammable or combustible materials Oxygen Fuel Gas 20 Feet

P-1 3.5 Flammable gases 3.5.1 Do not store cylinders near highly flammable solvents, combustible waste material and similar substances, or near unprotected electrical connections, gas flames or other sources of ignition 3.5.2 Never use a flame to detect flammable gas leaks; use soapy water

P-1 Section 3.6 Poison Gases 3.6.1 Personnel handling and using poison gases should have available for immediate use gas masks or self- contained breathing apparatus approved by U.S. Bureau of Mines* for the particular service desired *NOTE: This approval for respirators has been up-dated to the requirements of NIOSH (CGA P-1 2000)

1910.102 Acetylene "Cylinders." The in-plant transfer, handling, storage, and utilization of acetylene in cylinders shall be in accordance with Compressed Gas Association Pamphlet G-1-1966

1910.103 (b) Gaseous hydrogen systems (1)(i)(c) Each portable container shall be legibly marked with the name "Hydrogen" in accordance with "Marking Portable Compressed Gas Containers to Identify the Material Contained" ANSI Z48.1-1954 (1)(iv)(b) Installation of hydrogen systems shall be supervised by personnel familiar with proper practices with reference to their construction and use.

1910.103 (b) Gaseous hydrogen systems "Marking." The hydrogen storage location shall be permanently placarded as follows: Or equivalent "HYDROGEN - FLAMMABLE GAS - NO SMOKING - NO OPEN FLAMES,"

Flammable and Combustible Liquids CFR 1910.106

Purpose of Standard This standard applies to the handling, storage, and use of flammable and combustible liquids with a flash point (FP) below 200oF FP<200ºF

Purpose of Standard There are two primary hazards associated with flammable and combustible liquids: explosion and fire In order to prevent these hazards, this standard addresses the primary concerns of: Design and construction, Ventilation, Ignition sources, and Storage

Definitions 1910.106 (a)

Flash Point The minimum temperature at which a liquid gives off vapor within a test vessel in sufficient concentration to form an ignitable mixture with air near the surface of the liquid Flash point is normally an indication of susceptibility to ignition

Combustible Liquid Combustible liquid means any liquid having a flash point at or above 100oF (37.8oC) Combustible liquids are divided into two classes as follows: Class II liquids shall include those with flash points at or above 100oF (37.8oC) and below 140oF Class III liquids shall include those with flash points at or above 140oF Class IIIA liquids shall include those with flash points at or above 140oF (60oC) and below 200oF Class IIIB liquids shall include those with flash points at or above 200oF

Flammable Liquid Flammable liquid means any liquid having a flash point below 100oF Flammable liquids are known as Class I liquids

Flammable Liquid Class I liquids are divided into three classes as follows: Class IA shall include liquids having flash points below 73oF and having a boiling point below 100oF Class IB shall include liquids having flash points below 73oF and having a boiling point at or above 100oF Class IC shall include liquids having flash points at or above 73oF and below 100oF 100ºF

200 Fº III 140 Fº Combustible II Flash Point Fº 100 Fº Flammable IC IA IB IC II III 140 Fº Combustible Flash point > 100 Fº Flash Point Fº 100 Fº Flammable Flash point < 100 Fº 73 Fº 100 Fº Boiling Point Fº

Safety Can Safety can means an approved container, of not more than 5 gallons capacity, having a spring-closing lid and spout cover and so designed that it will safely relieve internal pressure when subjected to fire exposure

Ventilation Ventilation as specified in this section is for the prevention of fire and explosion It is considered adequate if it is sufficient to prevent accumulation of significant quantities of vapor-air mixtures in concentration over one- fourth of the lower flammable limit

Flammable (Explosive) Limits When vapors of a flammable or combustible liquid are mixed with air in the proper proportions in the presence of a source of ignition, rapid combustion or an explosion can occur The proper proportion is called the flammable range and is also often referred to as the explosive range.

Flammable (Explosive) Limits The flammable range includes all concentrations of flammable vapor or gas in air, in which a flash will occur or a flame will travel if the mixture is ignited + =

Flammable Range Explosion Pressure LEL UEL Vapor/Gas Concentration in Air (%)

1910.106(b)(2)(vi) Tank storage Where vent pipe outlets for tanks storing Class I liquids are adjacent to buildings or public ways: Located vapors are released at a safe point outside not less than 12 feet above the adjacent ground level. To aid dispersion, vapors discharged upward or horizontally away from adjacent walls Vent outlets located so vapors will not be trapped by eaves or other obstructions At least five feet from building openings

1910.106(b)(4) Tanks inside buildings Emergency venting by the use of weak roof seams on tanks not permitted Vents shall discharge vapors outside the buildings Connections for all tank openings shall be vapor or liquid tight

1910.106(b)(4) Tanks inside buildings Each connection to a tank inside of buildings through which liquid can normally flow shall be provided with an internal or an external valve located as close as practical to the shell of the tank

1910.106(b)(4) Tanks inside buildings Flammable/combustible tanks inside buildings provided with an automatic-closing heat-actuated valve on each withdrawal connection below the liquid level, except for connections used for emergency disposal, to prevent continued flow in the event of fire in the vicinity of the tank Inside tank Outlet opening

1910.106(c) Piping, valves & fittings Piping systems shall contain a sufficient number of valves to operate the system properly and to protect the plant

1910.106(d) Container and portable tank storage Applies only to the storage of flammable or combustible liquids: Drums or other containers (including flammable aerosols) not exceeding 60 gallons individual capacity and Portable tanks not exceeding 660 gallons individual capacity

1910.106(d) Container and portable tank storage Only approved containers and portable tanks shall be used Metal containers and portable tanks meeting the requirements of and containing products authorized by chapter I, title 49 of the Code of Federal Regulations (regulations issued by the Hazardous Materials Regulations Board, Department of Transportation)

1910.106(d)(3) Flammable Storage Cabinets Not more than 60 gallons of Class I and/or Class II liquids, or not more than 120 gallons of Class III liquids may be stored in an individual cabinet Storage cabinets shall be designed and constructed to limit the internal temperature to not more than 325oF when subjected to a standardized 10-minute fire test.

1910.106(d)(3) Flammable Storage Cabinets Cabinets shall be labeled in conspicuous lettering, "Flammable - Keep Fire Away" Storage cabinets shall be designed and constructed to limit the internal temperature to not more than 325oF when subjected to a standardized 10-minute fire test. Flammable Keep Fire Away

1910.106(d)(4)(iv) Ventilation Inside storage room shall be provided with either a gravity or a mechanical exhaust ventilation Complete change of air within the room at least six times per hour

1910.106(d)(5) Egress Flammable or combustible liquids, including stock for sale, shall not be stored so as to limit use of exits, stairways, or areas normally used for the safe egress of people

1910.106(d)(7) Open flames and smoking Open flames and smoking shall not be permitted in flammable or combustible liquid storage areas

Industrial Plants 1910.106(e)

1910.106(e) Industrial Plants Use and handling of flammable or combustible liquids is only incidental to the principal business, such as: Paint thinner storage in an automobile assembly plant; Solvents used in the construction of electronic equipment,and; Flammable finishing materials used in furniture manufacturing

1910.106(e)(2)(i) Containers Flammable or combustible liquids shall be stored in tanks or closed containers Flammable liquid stored in an open drum

1910.106(e)(2) Containers (ii)(b) The quantity of liquid that may be located outside of an inside storage room or storage cabinet in a building or in any one fire area of a building shall not exceed: 25 gallons of Class IA liquids in containers 120 gallons of Class IB, IC, II, or III liquids in containers 660 gallons of Class IB, IC, II, or III liquids in a single portable tank

1910.106(e)(2)(iv) Handling liquids at point of final use Flammable liquids shall be kept in covered containers when not actually in use

1910.106(e)(2(iv) Handling liquids at point of final use Where flammable or combustible liquids are used or handled, except in closed containers, means shall be provided to dispose promptly and safely of leakage or spills

1910.106(e)(6) Sources of ignition Adequate precautions shall be taken to prevent the ignition of flammable vapors

1910.106(e)(6) Sources of ignition Sources of ignition may include: Open flames, Lightning, Smoking, Cutting and welding, Hot surfaces, frictional heat, Sparks (static, electrical, and mechanical), Spontaneous ignition, Chemical and physical-chemical reactions, and Radiant heat

1910.106(e)(6) Sources of ignition "Grounding." Class I liquids shall not be dispensed into containers unless the nozzle and container are electrically interconnected Grounding and bonding wires, for dispensing flammables

Process Safety Management of Highly Hazardous Chemicals 1910.119

1910.119(a) Purpose This section contains requirements for preventing or minimizing the consequences of catastrophic releases of: Toxic, Reactive, Flammable, or Explosive chemicals These releases may result in toxic, fire or explosion hazards

1910.119(a)(1)Application A process which involves a chemical at or above the specified threshold quantities listed in Appendix A A process which involves a flammable liquid or gas (as defined in 1910.1200(c) of this part) on site in one location, in a quantity of 10,000 pounds (4535.9 kg) or more

Appendix A (example)

1910.119(a)(ii) Exceptions Hydrocarbon fuels used solely for workplace consumption as a fuel (e.g., propane used for comfort heating, gasoline for vehicle refueling), If such fuels are not a part of a process containing another highly hazardous chemical covered by this standard; Flammable liquids stored in atmospheric tanks or transferred which are kept below their normal boiling point without benefit of chilling or refrigeration

1910.119(a)(2) Exemptions Retail facilities; Oil or gas well drilling or servicing operations; or, Normally unoccupied remote facilities

1910.119(c) Employee Participation Written plan requires employee participation: consult with employees and their representatives on the development of process hazards analyses provide to employees and their representatives access to process hazard analyses

1910.119(d) Process safety information Complete a compilation of written process safety information before conducting any process hazard analysis: Enables the employer and the employees involved in operating the process to identify and understand the hazards posed by those processes

1910.119(d) Process safety information Pertaining to the hazards of the highly hazardous chemicals: Hazards of the process Technology of the process; and, The equipment in the process

1910.119(d) Process safety information Toxicity information*; Permissible exposure limits; Physical data; Reactivity data: Corrosivity data; Thermal and chemical stability data; and Hazardous effects of inadvertent mixing of different materials that could foreseeably occur *Note: Material Safety Data Sheets may be used to comply with this requirement to the extent they contain the information required

1910.119(e) Process hazard analysis Must conduct a process hazard analysis (hazard evaluation): What-If; Checklist; What-If/Checklist; Hazard and Operability Study (HAZOP); Failure Mode and Effects Analysis (FMEA); Fault Tree Analysis

1910.119(e) Process hazard analysis The process hazard analysis shall address: The identification of any previous incident which had a likely potential for catastrophic consequences in the workplace;

1910.119(e) Process hazard analysis The process hazard analysis shall address: Engineering and administrative controls applicable to the hazards such as detection of early warning of releases* *Acceptable detection methods might include process monitoring and control instrumentation with alarms, and detection hardware such as hydrocarbon sensors

1910.119(e) Process hazard analysis (PHA) PSA must be performed by a team with expertise in engineering and process operations Includes at least one employee who has experience and knowledge specific to the process being evaluated Also, one member of the team must be knowledgeable in the specific process hazard analysis methodology being used

1910.119(e) Process hazard analysis (PHA) Promptly address the team's findings and recommendations and document resolution of findings Document what actions are to be taken; Complete actions as soon as possible; Develop a written schedule of when these actions are to be completed; Communicate the actions to operating, maintenance and other employees whose work assignments are in the process

1910.119(f) Operating procedures Develop and implement written operating procedures* consistent with the process safety information and addresses at least the following elements: Initial start-up, normal and temporary operations Normal and emergency shut-down procedures Operating limits and consequences of deviation Hazards presented by the process *Readily accessible to employees

1910.119(f) Operating procedures Develop and implement safe work practices* to provide for the control of hazards during operations such as: Lockout/tagout; Confined space entry; Opening process equipment or piping; and Control over entrance into a facility by maintenance, contractor, laboratory, or other support personnel *These safe work practices apply to contractor employees as well

1910.119(g) Training Emphasis on the specific safety and health hazards of the process Emergency operations including shutdown, and Safe work practices applicable to the employee's job tasks Refresher training at least every three years Prepare a record which contains: The identity of the employee, The date of training, and The means used to verify that the employee understood the training

1910.119(h) Contractors* Applies to contractors performing maintenance or repair, turnaround, major renovation, or specialty work on or adjacent to a covered process Employer responsibilities: Obtain and evaluate information regarding the contract employer's safety performance and programs Inform contract employers of the known potential fire, explosion, or toxic release hazards related to the contractor's work and the process *Does not apply to contractors providing incidental services which do not influence process safety, such as janitorial work, food and drink services...

1910.123 Dipping and coating operations: Coverage and definitions (a)(1) This rule (§§1910.123 through 1910.126) applies when you use a dip tank containing a liquid other than water. It applies when you use the liquid in the tank or its vapor to: Clean an object Coat an object Alter the surface of an object, or Change the character of an object

1910.124 General requirements for dipping and coating operations (a)What construction requirements apply to dip tanks? Any container that you use as a dip tank must be strong enough to withstand any expected load. (b) What ventilation requirements apply to vapor areas? (b)(1)The ventilation that you provide to a vapor area must keep the airborne concentration of any substance below 25% of its LFL.

1910.124 General requirements for dipping and coating operations (e) What requirements must I follow when an employee enters a dip tank? When an employee enters a dip tank, you must meet the entry requirements of §1910.146, OSHA's standard for Permit- Required Confined Spaces, as applicable.

1910.124 General requirements for dipping and coating operations (f) What first-aid procedures must my employees know? Your employees must know the first-aid procedures that are appropriate to the dipping or coating hazards to which they are exposed.

1910.124 General requirements for dipping and coating operations (i) What must I do before an employee cleans a dip tank? Before permitting an employee to clean the interior of a dip tank, you must: (1) Drain the contents of the tank and open the cleanout doors; and (2) Ventilate and clear any pockets where hazardous vapors may have accumulated.

1910.125 Additional requirements for dipping and coating operations that use flammable or combustible liquids If you use flammable or combustible liquids, you must comply with the requirements of this section as well as the requirements of sections 1910.123, 1910.124, and 1910.126, as applicable.

You must comply with this section if: 1910.125 Additional requirements for dipping and coating operations that use flammable or combustible liquids You must comply with this section if: The flashpoint of the flammable or combustible liquid is 200° F or above And: The liquid is heated as part of the process, or A heated object is placed in the liquid