• Codes
  • Features

    Features Overview

    Go to features
    Reference

    Reference.

    A reliable and up-to-date source of codes.
    Research

    Research.

    Rapidly and efficiently calculate project parameters.
    Collaboration

    Collaboration.

    Get everyone on the same page and streamline code research.
    Workflows
    Architects
    Architects
    General Contractors
    General Contractors
    Building Official & Plans Examiners
    Building Official & Plans Examiners
    Inspectors
    Inspectors
    Owners
    Owners
    Subcontractors
    Subcontractors
    Code Consultants
    Code Consultants
  • Pricing
  • Login
  • Sign Up
Sign Up
Login
  • Code Library
  • Features
  • Pricing
  • About
  • Careers
  • Help
  • Contact
  • Terms
  • Privacy
Sign Up
Upgrade to Premium
Code calculators: Code Calculators automatically generates a detailed list of requirements.
REFERENCE
Amendment Styling
Industry-leading search
Code diagrams
RESEARCH
Code calculators
Filter by topic
Code compare
Code sheet exports
COLLABORATION
Team projects
Bookmarks
Comments
START 2 WEEK FREE TRIAL
Have an account? Sign in
// CODE SNIPPET

1926.57(i) Open Surface Tanks

OSHA 1926 Construction > D Occupational Health and Environmental Controls > 1926.57 Ventilation > 1926.57(i) Open Surface Tanks
JUMP TO FULL CODE CHAPTER
-

1926.57(i)(1) General

1926.57(i)(1)(i)

This paragraph applies to all operations involving the immersion of materials in liquids, or in the vapors of such liquids, for the purpose of cleaning or altering the surface or adding to or imparting a finish thereto or changing the character of the materials, and their subsequent removal from the liquid or vapor, draining, and drying. These operating include washing, electroplating, anodizing, pickling, quenching, dying, dipping, tanning, dressing, bleaching, degreasing, alkaline cleaning, stripping, rinsing, digesting, and other similar operation.

1926.57(i)(1)(ii)

Except where specific construction specifications are prescribed in this section, hoods, ducts, elbows, fans, blowers, and all other exhaust system parts, components, and supports thereof shall be so constructed as to meet conditions of service and to facilitate maintenance and shall conform in construction to the specifications contained in American National Standard Fundamentals Governing the Design and Operation of Local Exhaust Systems, Z9.2-1960.

1926.57(i)(2) Classification of Open-Surface Tank Operations

1926.57(i)(2)(i)

Open-surface tank operations shall be classified into 16 classes, numbered A-1 to D-4, inclusive.

1926.57(i)(2)(iii)

Hazard potential is an index, on a scale of from A to D, inclusive, of the severity of the hazard associated with the substance contained in the tank because of the toxic, flammable, or explosive nature of the vapor, gas, or mist produced there from. The toxic hazard is determined from the concentration, measured in parts by volume of a gas or vapor, per million parts by volume of contaminated air (p.p.m.), or in milligrams of mist per cubic meter of air (mg./m(3)), below which ill effects are unlikely to occur to the exposed worker. The concentrations shall be those in 1926.55 or other pertinent sections of this part.

1926.57(i)(2)(iv)

The relative fire or explosion hazard is measured in degrees Fahrenheit in terms of the closed-cup flash point of the substance in the tank. Detailed information on the prevention of fire hazards in dip tanks may be found in Dip Tanks Containing Flammable or Combustible Liquids, NFPA No. 34-1966, National Fire Protection Association. Where the tank contains a mixture of liquids, other than organic solvents, whose effects are additive, the hygienic standard of the most toxic component (for example, the one having the lowest p.p.m. or mg/m(3)) shall be used, except where such substance constitutes an insignificantly small faction of the mixture. For mixtures of organic solvents, their combined effect, rather than that of either individually, shall determine the hazard potential. In the absence of information to the contrary, the effects shall be considered as additive. If the sum of the ratios of the airborne concentration of each contaminant to the toxic concentration of that contaminant exceeds unity, the toxic concentration shall be considered to have been exceeded. (See Note A to paragraph (i)(2)(v) of this section.)

1926.57(i)(2)(v)

Hazard potential shall be determined from Table D-57.9, with the value indicating greater hazard being used. When the hazardous material may be either a vapor with a threshold limit value (TLV) in p.p.m. or a mist with a TLV in mg/m(3), the TLV indicating the greater hazard shall be used (for example, A takes precedence over B or C; B over C; C over D).

Note A:

(c1 ÷ TLV1) ÷ (c2 ÷ TLV2)+(c3 ÷ TLV3;... (cN ÷ TLVN)1

where:

c = Concentration measured at the operation in p.p.m.

TABLE D-57.9 - DETERMINATION OF HAZARD POTENTIAL

Hazard potential Toxicity group
Gas or
vapor
(p.p.m.)
Mist
(mg./m3
Flash point in
degrees F. (C.)
A 0-10 0-0.1
B 11-100 0.11-1.0 Under 100
(37.77)
C 101-500 1.1-10 100,200
(37.77-93.33)
D Over 500 Over 10 Over 200
(93.33)

1926.57(i)(2)(vi)

Rate of gas, vapor, or mist evolution is a numerical index, on a scale of from 1 to 4, inclusive, both of the relative capacity of the tank to produce gas, vapor, or mist and of the relative energy with which it is projected or carried upwards from the tank. Rate is evaluated in terms of

1926.57(i)(2)(vi)(A)

The temperature of the liquid in the tank in degrees Fahrenheit;

1926.57(i)(2)(vi)(B)

The number of degrees Fahrenheit that this temperature is below the boiling point of the liquid in degrees Fahrenheit;

1926.57(i)(2)(vi)(C)

The relative evaporation of the liquid in still air at room temperature in an arbitrary scale -- fast, medium, slow, or nil; and

1926.57(i)(2)(vi)(D)

The extent that the tank gases or produces mist in an arbitrary scale -- high, medium, low, and nil. (See Table D-57.10, Note 2.) Gassing depends upon electrochemical or mechanical processes, the effects of which have to be individually evaluated for each installation (see Table D-57.10, Note 3).

1926.57(i)(2)(vii)

Rate of evolution shall be determined from Table D-57.10. When evaporation and gassing yield different rates, the lowest numerical value shall be used.


TABLE D-57.10 - DETERMINATION OF RATE OF GAS, VAPOR, OR MIST EVOLUTION(1)
Rate Liquid temperature,
deg. F (C)
Degrees below
boiling point
Relative
evaporation(2)
Gassing(3)
1 Over 200 (93.33) 0-20 Fast High.
2 150-200 (65.55-93.33) 21-50 Medium Medium
3 94-149 (34.44-65) 51-100 Slow Low.
4 Under 94 (34.44) Over 100 Nil Nil.

     Footnote(1) In certain classes of equipment, specifically vapor degreasers, an internal condenser or vapor level thermostat is used to prevent the vapor from leaving the tank during normal operation. In such cases, rate of vapor evolution from the tank into the workroom is not dependent upon the factors listed in the table, but rather upon abnormalities of operating procedure, such as carryout of vapors from excessively fast action, dragout of liquid by entrainment in parts, contamination of solvent by water and other materials, or improper heat balance. When operating procedure is excellent, effective rate of evolution may be taken as 4. When operating procedure is average, the effective rate of evolution may be taken as 3.
     Footnote(2) Relative evaporation rate is determined according to the methods described by A. K. Doolittle in Industrial and Engineering Chemistry, vol. 27 p. 1169, (3) where time for 100-percent evaporation is as follows: Fast: 0-3 hours; Medium: 3-12 hours; Slow: 12-50 hours; Nil: more than 50 hours.
     Footnote(3) Gassing means the formation by chemical or electrochemical action of minute bubbles of gas under the surface of the liquid in the tank and is generally limited to aqueous solutions.

1926.57(i)(2)(ii) Determination of Class

Class is determined by two factors, hazard potential designated by a letter from A to D, inclusive, and rate of gas, vapor, or mist evolution designated by a number from 1 to 4, inclusive (for example, B.3).

1926.57(i)(3) Ventilation

Where ventilation is used to control potential exposures to workers as defined in paragraph (i)(2)(iii) of this section, it shall be adequate to reduce the concentration of the air contaminant to the degree that a hazard to the worker does not exist. Methods of ventilation are discussed in American National Standard Fundamentals Governing the Design and Operation of Local Exhaust Systems, Z9.2-1960.

1926.57(i)(4) Control Requirements

1926.57(i)(4)(i)

Control velocities shall conform to Table D-57.11 in all cases where the flow of air past the breathing or working zone of the operator and into the hoods is undisturbed by local environmental conditions, such as open windows, wall fans, unit heaters, or moving machinery.

1926.57(i)(4)(iii)

All tanks exhausted by means of hoods which do not project over the entire tank, and in which the direction of air movement into the hood or hoods is substantially horizontal, shall be considered to be laterally exhausted. The quantity of air in cubic feet per minute necessary to be laterally exhausted per square foot of tank area in order to maintain the required control velocity shall be determined from Table D-57.12 for all variations in ratio of tank width (W) to tank length (L). The total quantity of air in cubic feet per minute required to be exhausted per tank shall be not less than the product of the area of tank surface times the cubic feet per minute per square foot of tank area, determined from Table D-57.12.

1926.57(i)(4)(iii)(A)

For lateral exhaust hoods over 42 inches (1.06 m) wide, or where it is desirable to reduce the amount of air removed from the workroom, air supply slots or orifices shall be provided along the side or the center of the tank opposite from the exhaust slots. The design of such systems shall meet the following criteria:

1926.57(i)(4)(iii)(A)(1)

The supply air volume plus the entrained air shall not exceed 50 percent of the exhaust volume.

1926.57(i)(4)(iii)(A)(2)

The velocity of the supply airstream as it reaches the effective control area of the exhaust slot shall be less than the effective velocity over the exhaust slot area.


TABLE D-57.12 - MINIMUM VENTILATION RATE IN CUBIC FEET OF AIR PER MINUTE PER SQUARE FOOT OF TANK AREA FOR LATERAL EXHAUST
Required minimum
control velocity,
f.p.m. (from
Table D-57.11)
C.f.m. per sq. ft. to maintain required minimum
velocities at following ratios (tank width (W)/
tank length (L)(1),(2)
0.0-0.09 0.1-0.24 0.25-0.49 0.5-0.99 1.0-2.0
Hood along one side or two parallel sides of tank when one hood is
against a wall or baffle(2).
Also for a manifold along tank centerline(3).
50 50 60 75 90 100
75 75 90 110 130 150
100 100 125 150 175 200
150 150 190 225 260 300
Hood along one side or two parallel sides of free standing tank not
against wall or baffle.
50 75 90 100 110 125
75 110 130 150 170 190
100 150 175 200 225 250
150 225 260 300 340 375

   Footnote(1) It is not practicable to ventilate across the long
dimension of a tank whose ratio W/L exceeds 2.0.
   It is undesirable to do so when W/L exceeds 1.0. For circular tanks
with lateral exhaust along up to 1/2 the circumference, use W/L=1.0; for over one-half the circumference use W/L=0.5.
    Footnote(2) Baffle is a vertical plate the same length as the tank,
and with the top of the plate as high as the tank is wide. If the exhaust hood is on the side of a tank against a building wall or close to it, it is perfectly baffled.
   Footnote(3) Use W/2 as tank width in computing when manifold is along centerline, or when hoods are used on two parallel sides of a tank.
   Tank Width (W) means the effective width over which the hood must
pull air to operate (for example, where the hood face is set back from the edge of the tank, this set back must be added in measuring tank width). The surface area of tanks can frequently be reduced and better control obtained (particularly on conveyorized systems) by using covers extending from the upper edges of the slots toward the center of the tank.

1926.57(i)(4)(iii)(A)(3)

The vertical height of the receiving exhaust hood, including any baffle, shall not be less than one-quarter the width of the tank.

1926.57(i)(4)(iii)(A)(4)

The supply airstream shall not be allowed to impinge on obstructions between it and the exhaust slot in such a manner as to significantly interfere with the performance of the exhaust hood.

1926.57(i)(4)(iii)(A)(5)

Since most failure of push-pull systems result from excessive supply air volumes and pressures, methods of measuring and adjusting the supply air shall be provided. When satisfactory control has been achieved, the adjustable features of the hood shall be fixed so that they will not be altered.

1926.57(i)(4)(iv)

All tanks exhausted by means of hoods which project over the entire tank, and which do not conform to the definition of enclosing hoods, shall be considered to be overhead canopy hoods. The quantity of air in cubic feet per minute necessary to be exhausted through a canopy hood shall be not less than the product of the control velocity times the net area of all openings between the bottom edges of the hood and the top edges of the tank.

1926.57(i)(4)(v)

The rate of vapor evolution (including steam or products of combustion) from the process shall be estimated. If the rate of vapor evolution is equal to or greater than 10 percent of the calculated exhaust volume required, the exhaust volume shall be increased in equal amount.

1926.57(i)(4)(ii)

All tanks exhausted by means of hoods which

1926.57(i)(4)(ii)(A)

Project over the entire tank;

1926.57(i)(4)(ii)(B)

Are fixed in position in such a location that the head of the workman, in all his normal operating positions while working at the tank, is in front of all hood openings; and

1926.57(i)(4)(ii)(C)

Are completely enclosed on at least two sides, shall be considered to be exhausted through an enclosing hood.
SEE MORE

Related Code Sections


1926.57(i) Occupational Health and Environmental Controls, Open Surface Tanks
above an open-surface tank, control must be provided for the airborne spray. Such operations shall be enclosed as completely as possible. The inward air ...
OSHA 1926 Construction > D Occupational Health and Environmental Controls > 1926.57 Ventilation > 1926.57(i) Open Surface Tanks
1926.57(i)(2)(v) Occupational Health and Environmental Controls,
Hazard potential shall be determined from Table D-57.9, with the value indicating greater hazard being used. When the hazardous material may be either ...
OSHA 1926 Construction > D Occupational Health and Environmental Controls > 1926.57 Ventilation > 1926.57(i) Open Surface Tanks > 1926.57(i)(2) Classification of Open-Surface Tank Operations > 1926.57(i)(2)(v)
1926.57(i)(2)(vi) Occupational Health and Environmental Controls,
Rate of gas, vapor, or mist evolution is a numerical index, on a scale of from 1 to 4, inclusive, both of the relative capacity of the tank ...
OSHA 1926 Construction > D Occupational Health and Environmental Controls > 1926.57 Ventilation > 1926.57(i) Open Surface Tanks > 1926.57(i)(2) Classification of Open-Surface Tank Operations > 1926.57(i)(2)(vi)
1926.57(i)(2)(vi)(A) Occupational Health and Environmental Controls,
The temperature of the liquid in the tank in degrees Fahrenheit; ...
OSHA 1926 Construction > D Occupational Health and Environmental Controls > 1926.57 Ventilation > 1926.57(i) Open Surface Tanks > 1926.57(i)(2) Classification of Open-Surface Tank Operations > 1926.57(i)(2)(vi) > 1926.57(i)(2)(vi)(A)
1926.57(i)(2)(vi)(B) Occupational Health and Environmental Controls,
The number of degrees Fahrenheit that this temperature is below the boiling point of the liquid in degrees Fahrenheit ...
OSHA 1926 Construction > D Occupational Health and Environmental Controls > 1926.57 Ventilation > 1926.57(i) Open Surface Tanks > 1926.57(i)(2) Classification of Open-Surface Tank Operations > 1926.57(i)(2)(vi) > 1926.57(i)(2)(vi)(B)
Help Contact Us Privacy Terms
Code Compare
Code Compare
Highlight differences between any two building codes.
Code diagrams
Code diagrams
Unpack the code through illustrations and descriptions.
Code sheet exports
Code sheet exports
Generate a code sheet that integrates with your drawing set.
Search
Search
Don't miss relevant code. Quickly locate sections across your jurisdiction.
Shared projects
Shared projects
Projects provide a dedicated space to collaborate on code research.
Code Calculators
Code Calculators
Code calculators automatically generate a detailed list of requirements.
UpCodes Premium
Leverage the most sophisticated code compliance platform.
VISIT PRICING
UpCodes Premium
Leverage the full code compliance platform.
START 2 WEEK FREE TRIAL PRICING