29 C.F.R. § 1910.94
(2) Dust hazards from abrasive blasting.
(3) Blast-cleaning enclosures.
(i) Blast-cleaning enclosures shall be exhaust ventilated in such a way that a continuous inward flow of air will be maintained at all openings in the enclosure during the blasting operation.
(a) All air inlets and access openings shall be baffled or so arranged that by the combination of inward air flow and baffling the escape of abrasive or dust particules into an adjacent work area will be minimized and visible spurts of dust will not be observed.
(b) The rate of exhaust shall be sufficient to provide prompt clearance of the dust-laden air within the enclosure after the cessation of blasting.
(c) Before the enclosure is opened, the blast shall be turned off and the exhaust system shall be run for a sufficient period of time to remove the dusty air within the enclosure.
(d) Safety glass protected by screening shall be used in observation windows, where hard deep-cutting abrasives are used.
(e) Slit abrasive-resistant baffles shall be installed in multiple sets at all small access openings where dust might escape, and shall be inspected regularly and replaced when needed.
(1) Doors shall be flanged and tight when closed.
(2) Doors on blast-cleaning rooms shall be operable from both inside and outside, except that where there is a small operator access door, the large work access door may be closed or opened from the outside only.
(4) Exhaust ventilation systems.
(i) The construction, installation, inspection, and maintenance of exhaust systems shall conform to the principles and requirements set forth in American National Standard Fundamentals Governing the Design and Operation of Local Exhaust Systems, Z9.2-1960, and ANSI Z33.1-1961, which is incorporated by reference as specified in § 1910.6.
(a) When dust leaks are noted, repairs shall be made as soon as possible.
(b) The static pressure drop at the exhaust ducts leading from the equipment shall be checked when the installation is completed and periodically thereafter to assure continued satisfactory operation. Whenever an appreciable change in the pressure drop indicates a partial blockage, the system shall be cleaned and returned to normal operating condition.
(5) Personal protective equipment.
(ii) Abrasive-blasting respirators shall be worn by all abrasive-blasting operators:
(a) When working inside of blast-cleaning rooms, or
(b) When using silica sand in manual blasting operations where the nozzle and blast are not physically separated from the operator in an exhaust ventilated enclosure, or
(c) Where concentrations of toxic dust dispersed by the abrasive blasting may exceed the limits set in § 1910.1000 and the nozzle and blast are not physically separated from the operator in an exhaust-ventilated enclosure.
(iii) Properly fitted particulate-filter respirators, commonly referred to as dust-filter respirators, may be used for short, intermittent, or occasional dust exposures such as cleanup, dumping of dust collectors, or unloading shipments of sand at a receiving point when it is not feasible to control the dust by enclosure, exhaust ventilation, or other means. The respirators used must be approved by NIOSH under 42 CFR part 84 for protection against the specific type of dust encountered.
(a) Dust-filter respirators may be used to protect the operator of outside abrasive-blasting operations where nonsilica abrasives are used on materials having low toxicities.
(b) Dust-filter respirators shall not be used for continuous protection where silica sand is used as the blasting abrasive, or toxic materials are blasted.
(v) Operators shall be equipped with heavy canvas or leather gloves and aprons or equivalent protection to protect them from the impact of abrasives. Safety shoes shall be worn to protect against foot injury where heavy pieces of work are handled.
(a) Protective footwear must comply with the requirements specified by 29 CFR 1910.136(b)(1).
(b) Equipment for protection of the eyes and face shall be supplied to the operator when the respirator design does not provide such protection and to any other personnel working in the vicinity of abrasive blasting operations. This equipment shall conform to the requirements of § 1910.133.
(3) Hood and branch pipe requirements.
(ii) Grinding wheels on floor stands, pedestals, benches, and special-purpose grinding machines and abrasive cutting-off wheels shall have not less than the minimum exhaust volumes shown in Table G-4 with a recommended minimum duct velocity of 4,500 feet per minute in the branch and 3,500 feet per minute in the main. The entry losses from all hoods except the vertical-spindle disc grinder hood, shall equal 0.65 velocity pressure for a straight takeoff and 0.45 velocity pressure for a tapered takeoff. The entry loss for the vertical-spindle disc grinder hood is shown in figure G-1 (following § 1910.94(b)).
| Wheel diameter (inches) | Wheel width (inches) | Minimum exhaust volume (feet3/min.) |
|---|---|---|
| To 9 | 11⁄2 | 220 |
| Over 9 to 16 | 2 | 390 |
| Over 16 to 19 | 3 | 500 |
| Over 19 to 24 | 4 | 610 |
| Over 24 to 30 | 5 | 880 |
| Over 30 to 36 | 6 | 1,200 |
For any wheel wider than wheel diameters shown in Table G-4, increase the exhaust volume by the ratio of the new width to the width shown.
Example:If wheel width = 4 1/2 inches, then 4.5 ÷ 4 × 610 = 686 (rounded to 690).
(iii) Scratch-brush wheels and all buffing and polishing wheels mounted on floor stands, pedestals, benches, or special-purpose machines shall have not less than the minimum exhaust volume shown in Table G-5.
| Wheel diameter (inches) | Wheel width (inches) | Minimum exhaust volume (feet3/min.) |
|---|---|---|
| To 9 | 2 | 300 |
| Over 9 to 16 | 3 | 500 |
| Over 16 to 19 | 4 | 610 |
| Over 19 to 24 | 5 | 740 |
| Over 24 to 30 | 6 | 1,040 |
| Over 30 to 36 | 6 | 1,200 |
(iv) Grinding wheels or discs for horizontal single-spindle disc grinders shall be hooded to collect the dust or dirt generated by the grinding operation and the hoods shall be connected to branch pipes having exhaust volumes as shown in Table G-6.
| Disc diameter (inches) | Exhaust volume (ft.3/min.) |
|---|---|
| Up to 12 | 220 |
| Over 12 to 19 | 390 |
| Over 19 to 30 | 610 |
| Over 30 to 36 | 880 |
(v) Grinding wheels or discs for horizontal double-spindle disc grinders shall have a hood enclosing the grinding chamber and the hood shall be connected to one or more branch pipes having exhaust volumes as shown in Table G-7.
| Disc diameter (inches) | Exhaust volume (ft.3/min.) |
|---|---|
| Up to 19 | 610 |
| Over 19 to 25 | 880 |
| Over 25 to 30 | 1,200 |
| Over 30 to 53 | 1,770 |
| Over 53 to 72 | 6,280 |
(vi) Grinding wheels or discs for vertical single-spindle disc grinders shall be encircled with hoods to remove the dust generated in the operation. The hoods shall be connected to one or more branch pipes having exhaust volumes as shown in Table G-8.
| Disc diameter (inches) | One-half or more of disc covered | Disc not covered | ||
|---|---|---|---|---|
| Number 1 | Exhaust foot3/min.) | Number 1 | Exhaust foot3/min. | |
| Up to 20 | 1 | 500 | 2 | 780 |
| Over 20 to 30 | 2 | 780 | 2 | 1,480 |
| Over 30 to 53 | 2 | 1,770 | 4 | 3,530 |
| Over 53 to 72 | 2 | 3,140 | 5 | 6,010 |
| 1 Number of exhaust outlets around periphery of hood, or equal distribution provided by other means. |
(vii) Grinding and polishing belts shall be provided with hoods to remove dust and dirt generated in the operations and the hoods shall be connected to branch pipes having exhaust volumes as shown in Table G-9.
| Belts width (inches) | Exhaust volume (ft.3/min.) |
|---|---|
| Up to 3 | 220 |
| Over 3 to 5 | 300 |
| Over 5 to 7 | 390 |
| Over 7 to 9 | 500 |
| Over 9 to 11 | 610 |
| Over 11 to 13 | 740 |
(4) Exhaust systems.
(5) Hood and enclosure design.
(i) (a) It is the dual function of grinding and abrasive cutting-off wheel hoods to protect the operator from the hazards of bursting wheels, as well as to provide a means for the removal of dust and dirt generated. All hoods shall be not less in structural strength than specified in Tables O-1 and O-9 of § 1910.215.
(b) Due to the variety of work and types of grinding machines employed, it is necessary to develop hoods adaptable to the particular machine in question, and such hoods shall be located as close as possible to the operation.
(x) Grinding and polishing belt hoods shall be constructed as close to the operation as possible. The hood should extend almost to the belt, and 1-inch wide openings should be provided on either side. Figure G-8 shows a typical hood for a belt operation.

| Dia D. inches | Exhaust E | Volume Exhausted at 4,500 ft/min ft3/min | Note | ||
|---|---|---|---|---|---|
| Min. | Max. | No Pipes | Dia. | ||
| 20 | 1 | 41⁄4 | 500 | When one-half or more of the disc can be hooded, use exhaust ducts as shown at the left. | |
| Over 20 | 30 | 2 | 4 | 780 | |
| Over 30 | 72 | 2 | 6 | 1,770 | |
| Over 53 | 72 | 2 | 8 | 3,140 | |
| 20 | 2 | 4 | 780 | When no hood can be used over disc, use exhaust ducts as shown at left. | |
| Over 20 | 20 | 2 | 4 | 780 | |
| Over 30 | 30 | 2 | 51⁄2 | 1,480 | |
| Over 53 | 53 | 4 | 6 | 3,530 | |
| 72 | 5 | 7 | 6,010 | ||
| Entry loss = 1.0 slot velocity pressure + 0.5 branch velocity pressure. | |||||
| Minimum slot velocity = 2,000 ft/min—1⁄2-inch slot width. |

| Wheel dimension, inches | Exhaust outlet, inches E | Volume of air at 4,500 ft/min | ||
|---|---|---|---|---|
| Diameter | Width, Max | |||
| Min=d | Max=D | |||
| 9 | 11⁄2 | 3 | 220 | |
| Over 9 | 16 | 2 | 4 | 390 |
| Over 16 | 19 | 3 | 41⁄2 | 500 |
| Over 19 | 24 | 4 | 5 | 610 |
| Over 24 | 30 | 5 | 6 | 880 |
| Over 30 | 36 | 6 | 7 | 1,200 |
| Entry loss = 0.45 velocity pressure for tapered takeoff 0.65 velocity pressure for straight takeoff. |


| Wheel dimension, inches | Exhaust outlet, inches E | Volume of air at 4,500 ft/min | ||
|---|---|---|---|---|
| Diameter | Width, Max | |||
| Min=d | Max=D | |||
| 9 | 2 | 31⁄2 | 300 | |
| Over 9 | 16 | 3 | 4 | 500 |
| Over 16 | 19 | 4 | 5 | 610 |
| Over 19 | 24 | 5 | 51⁄2 | 740 |
| Over 24 | 30 | 6 | 61⁄2 | 1.040 |
| Over 30 | 36 | 6 | 7 | 1.200 |
| Entry loss = 0.15 velocity pressure for tapered takeoff; 0.65 velocity pressure for straight takeoff. |


| Dia D, inches | Exhaust E, dia. inches | Volume exhausted at 4,500 ft/min ft3/min | |
|---|---|---|---|
| Min. | Max. | ||
| 12 | 3 | 220 | |
| Over 12 | 19 | 4 | 390 |
| Over 19 | 30 | 5 | 610 |
| Over 30 | 36 | 6 | 880 |
| Note: If grinding wheels are used for disc grinding purposes, hoods must conform to structural strength and materials as described in 9.1. | |||
| Entry loss = 0.45 velocity pressure for tapered takeoff. |

| Disc dia. inches | Exhaust E | Volume exhaust at 4,500 ft/min. ft3/min | Note | ||
|---|---|---|---|---|---|
| Min. | Max. | No Pipes | Dia. | ||
| 19 | 1 | 5 | 610 | ||
| Over 19 | 25 | 1 | 6 | 880 | When width “W” permits, exhaust ducts should be as near heaviest grinding as possible. |
| Over 25 | 30 | 1 | 7 | 1,200 | |
| Over 30 | 53 | 2 | 6 | 1,770 | |
| Over 53 | 72 | 4 | 8 | 6,280 | |
| Entry loss = 0.45 velocity pressure for tapered takeoff. |

| Belt width W. Inches | Exhaust volume. ft.1/min |
|---|---|
| Up to 3 | 220 |
| 3 to 5 | 300 |
| 5 to 7 | 390 |
| 7 to 9 | 500 |
| 9 to 11 | 610 |
| 11 to 13 | 740 |
| Minimum duct velocity = 4,500 ft/min branch, 3,500 ft/min main. | |
| Entry loss = 0.45 velocity pressure for tapered takeoff; 0.65 velocity pressure for straight takeoff. |
(3) Design and construction of spray booths.
(i) Spray booths shall be designed and constructed in accordance with § 1910.107(b)(1) through (b)(4) and (b)(6) through (b)(10). For a more detailed discussion of fundamentals relating to this subject, see ANSI Z9.2-1960, which is incorporated by reference as specified in § 1910.6.
(a) Lights, motors, electrical equipment, and other sources of ignition shall conform to the requirements of § 1910.107(b)(10) and (c).
(b) In no case shall combustible material be used in the construction of a spray booth and supply or exhaust duct connected to it.
(iii) Baffles, distribution plates, and dry-type overspray collectors shall conform to the requirements of § 1910.107(b)(4) and (b)(5).
(a) Overspray filters shall be installed and maintained in accordance with the requirements of § 1910.107(b)(5), and shall only be in a location easily accessible for inspection, cleaning, or replacement.
(b) Where effective means, independent of the overspray filters, are installed which will result in design air distribution across the booth cross section, it is permissible to operate the booth without the filters in place.
(iv) (a) For wet or water-wash spray booths, the water-chamber enclosure, within which intimate contact of contaminated air and cleaning water or other cleaning medium is maintained, if made of steel, shall be 18 gage or heavier and adequately protected against corrosion.
(b) Chambers may include scrubber spray nozzles, headers, troughs, or other devices. Chambers shall be provided with adequate means for creating and maintaining scrubbing action for removal of particulate matter from the exhaust air stream.
(v) Collecting tanks shall be of welded steel construction or other suitable non-combustible material. If pits are used as collecting tanks, they shall be concrete, masonry, or other material having similar properties.
(a) Tanks shall be provided with weirs, skimmer plates, or screens to prevent sludge and floating paint from entering the pump suction box. Means for automatically maintaining the proper water level shall also be provided. Fresh water inlets shall not be submerged. They shall terminate at least one pipe diameter above the safety overflow level of the tank.
(b) Tanks shall be so constructed as to discourage accumulation of hazardous deposits.
(4) Design and construction of spray rooms.
(5) Ventilation.
(i) Ventilation shall be provided in accordance with provisions of § 1910.107(d), and in accordance with the following:
(a) Where a fan plenum is used to equalize or control the distribution of exhaust air movement through the booth, it shall be of sufficient strength or rigidity to withstand the differential air pressure or other superficially imposed loads for which the equipment is designed and also to facilitate cleaning. Construction specifications shall be at least equivalent to those of paragraph (c)(5)(iii) of this section.
(b) [Reserved]
(ii) Inlet or supply ductwork used to transport makeup air to spray booths or surrounding areas shall be constructed of noncombustible materials.
(a) If negative pressure exists within inlet ductwork, all seams and joints shall be sealed if there is a possibility of infiltration of harmful quantities of noxious gases, fumes, or mists from areas through which ductwork passes.
(b) Inlet ductwork shall be sized in accordance with volume flow requirements and provide design air requirements at the spray booth.
(c) Inlet ductwork shall be adequately supported throughout its length to sustain at least its own weight plus any negative pressure which is exerted upon it under normal operating conditions.
(iii) (a) Exhaust ductwork shall be adequately supported throughout its length to sustain its weight plus any normal accumulation in interior during normal operating conditions and any negative pressure exerted upon it.
(b) Exhaust ductwork shall be sized in accordance with good design practice which shall include consideration of fan capacity, length of duct, number of turns and elbows, variation in size, volume, and character of materials being exhausted. See American National Standard Z9.2-1960 for further details and explanation concerning elements of design.
(c) Longitudinal joints in sheet steel ductwork shall be either lock-seamed, riveted, or welded. For other than steel construction, equivalent securing of joints shall be provided.
(d) Circumferential joints in ductwork shall be substantially fastened together and lapped in the direction of airflow. At least every fourth joint shall be provided with connecting flanges, bolted together, or of equivalent fastening security.
(e) Inspection or clean-out doors shall be provided for every 9 to 12 feet of running length for ducts up to 12 inches in diameter, but the distance between cleanout doors may be greater for larger pipes. A clean-out door or doors shall be provided for servicing the fan, and where necessary, a drain shall be provided.
(f) Where ductwork passes through a combustible roof or wall, the roof or wall shall be protected at the point of penetration by open space or fire-resistive material between the duct and the roof or wall. When ducts pass through firewalls, they shall be provided with automatic fire dampers on both sides of the wall, except that three-eighth-inch steel plates may be used in lieu of automatic fire dampers for ducts not exceeding 18 inches in diameter.
(g) Ductwork used for ventilating any process covered in this standard shall not be connected to ducts ventilating any other process or any chimney or flue used for conveying any products of combustion.
(6) Velocity and air flow requirements.
(i) Except where a spray booth has an adequate air replacement system, the velocity of air into all openings of a spray booth shall be not less than that specified in Table G-10 for the operating conditions specified. An adequate air replacement system is one which introduces replacement air upstream or above the object being sprayed and is so designed that the velocity of air in the booth cross section is not less than that specified in Table G-10 when measured upstream or above the object being sprayed.
| Operating conditions for objects completely inside booth | Crossdraft, f.p.m. | Airflow velocities, f.p.m. | |
|---|---|---|---|
| Design | Range | ||
| Electrostatic and automatic airless operation contained in booth without operator | Negligible | 50 large booth | 50-75 |
| 100 small booth | 75-125 | ||
| Air-operated guns, manual or automatic | Up to 50 | 100 large booth | 75-125 |
| 150 small booth | 125-175 | ||
| Air-operated guns, manual or automatic | Up to 100 | 150 large booth | 125-175 |
| 200 small booth | 150-250 | ||
| Notes: | |||
| (1) Attention is invited to the fact that the effectiveness of the spray booth is dependent upon the relationship of the depth of the booth to its height and width. | |||
| (2) Crossdrafts can be eliminated through proper design and such design should be sought. Crossdrafts in excess of 100fpm (feet per minute) should not be permitted. | |||
| (3) Excessive air pressures result in loss of both efficiency and material waste in addition to creating a backlash that may carry overspray and fumes into adjacent work areas. | |||
| (4) Booths should be designed with velocities shown in the column headed “Design.” However, booths operating with velocities shown in the column headed “Range” are in compliance with this standard. |
(ii) In addition to the requirements in paragraph (c)(6)(i) of this section the total air volume exhausted through a spray booth shall be such as to dilute solvent vapor to at least 25 percent of the lower explosive limit of the solvent being sprayed. An example of the method of calculating this volume is given below.
Example:To determine the lower explosive limits of the most common solvents used in spray finishing, see Table G-11. Column 1 gives the number of cubic feet of vapor per gallon of solvent and column 2 gives the lower explosive limit (LEL) in percentage by volume of air. Note that the quantity of solvent will be diminished by the quantity of solids and nonflammables contained in the finish. To determine the volume of air in cubic feet necessary to dilute the vapor from 1 gallon of solvent to 25 percent of the lower explosive limit, apply the following formula: Dilution volume required per gallon of solvent = 4 (100−LEL) (cubic feet of vapor per gallon) ÷ LEL Using toluene as the solvent. (1) LEL of toluene from Table G-11, column 2, is 1.4 percent. (2) Cubic feet of vapor per gallon from Table G-11, column 1, is 30.4 cubic feet per gallon.(3) Dilution volume required= 4 (100−1.4) 30.4 ÷ 1.4 = 8,564 cubic feet. (4) To convert to cubic feet per minute of required ventilation, multiply the dilution volume required per gallon of solvent by the number of gallons of solvent evaporated per minute.
| Solvent | Cubic feet per gallon of vapor of liquid at 70 °F. | Lower explosive limit in percent by volume of air at 70 °F |
|---|---|---|
| Column 1 | Column 2 | |
| Acetone | 44.0 | 2.6 |
| Amyl Acetate (iso) | 21.6 | 1 1.0 |
| Amyl Alcohol (n) | 29.6 | 1.2 |
| Amyl Alcohol (iso) | 29.6 | 1.2 |
| Benzene | 36.8 | 1 1.4 |
| Butyl Acetate (n) | 24.8 | 1.7 |
| Butyl Alcohol (n) | 35.2 | 1.4 |
| Butyl Cellosolve | 24.8 | 1.1 |
| Cellosolve | 33.6 | 1.8 |
| Cellosolve Acetate | 23.2 | 1.7 |
| Cyclohexanone | 31.2 | 1 1.1 |
| 1,1 Dichloroethylene | 42.4 | 5.9 |
| 1,2 Dichloroethylene | 42.4 | 9.7 |
| Ethyl Acetate | 32.8 | 2.5 |
| Ethyl Alcohol | 55.2 | 4.3 |
| Ethyl Lactate | 28.0 | 1 1.5 |
| Methyl Acetate | 40.0 | 3.1 |
| Methyl Alcohol | 80.8 | 7.3 |
| Methyl Cellosolve | 40.8 | 2.5 |
| Methyl Ethyl Ketone | 36.0 | 1.8 |
| Methyl n-Propyl Ketone | 30.4 | 1.5 |
| Naphtha (VM&P) (76° Naphtha) | 22.4 | 0.9 |
| Naphtha (100 °Flash) Safety Solvent—Stoddard Solvent | 23.2 | 1.0 |
| Propyl Acetate (n) | 27.2 | 2.8 |
| Propyl Acetate (iso) | 28.0 | 1.1 |
| Propyl Alcohol (n) | 44.8 | 2.1 |
| Propyl Alcohol (iso) | 44.0 | 2.0 |
| Toluene | 30.4 | 1.4 |
| Turpentine | 20.8 | 0.8 |
| Xylene (o) | 26.4 | 1.0 |
| 1 At 212 °F. |
(iii) (a) When an operator is in a booth downstream from the object being sprayed, an air-supplied respirator or other type of respirator must be used by employees that has been approved by NIOSH under 42 CFR part 84 for the material being sprayed.
(b) Where downdraft booths are provided with doors, such doors shall be closed when spray painting.
(7) Make-up air.
(iii) (a) Where the air supply to a spray booth or room is filtered, the fan static pressure shall be calculated on the assumption that the filters are dirty to the extent that they require cleaning or replacement.
(b) The rating of filters shall be governed by test data supplied by the manufacturer of the filter. A pressure gage shall be installed to show the pressure drop across the filters. This gage shall be marked to show the pressure drop at which the filters require cleaning or replacement. Filters shall be replaced or cleaned whenever the pressure drop across them becomes excessive or whenever the air flow through the face of the booth falls below that specified in Table G-10.
(iv) (a) Means for heating make-up air to any spray booth or room, before or at the time spraying is normally performed, shall be provided in all places where the outdoor temperature may be expected to remain below 55 °F. for appreciable periods of time during the operation of the booth except where adequate and safe means of radiant heating for all operating personnel affected is provided. The replacement air during the heating seasons shall be maintained at not less than 65 °F. at the point of entry into the spray booth or spray room. When otherwise unheated make-up air would be at a temperature of more than 10 °F. below room temperature, its temperature shall be regulated as provided in section 3.6.3 of ANSI Z9.2-1960.
(b) As an alternative to an air replacement system complying with the preceding section, general heating of the building in which the spray room or booth is located may be employed provided that all occupied parts of the building are maintained at not less than 65 °F. when the exhaust system is in operation or the general heating system supplemented by other sources of heat may be employed to meet this requirement.
(c) No means of heating make-up air shall be located in a spray booth.
(d) Where make-up air is heated by coal or oil, the products of combustion shall not be allowed to mix with the make-up air, and the products of combustion shall be conducted outside the building through a flue terminating at a point remote from all points where make-up air enters the building.
(e) Where make-up air is heated by gas, and the products of combustion are not mixed with the make-up air but are conducted through an independent flue to a point outside the building remote from all points where make-up air enters the building, it is not necessary to comply with paragraph (c)(7)(iv)(f) of this section.
(f) Where make-up air to any manually operated spray booth or room is heated by gas and the products of combustion are allowed to mix with the supply air, the following precautions must be taken:
(1) The gas must have a distinctive and strong enough odor to warn workmen in a spray booth or room of its presence if in an unburned state in the make-up air.
(2) The maximum rate of gas supply to the make-up air heater burners must not exceed that which would yield in excess of 200 p.p.m. (parts per million) of carbon monoxide or 2,000 p.p.m. of total combustible gases in the mixture if the unburned gas upon the occurrence of flame failure were mixed with all of the make-up air supplied.
(3) A fan must be provided to deliver the mixture of heated air and products of combustion from the plenum chamber housing the gas burners to the spray booth or room.
[39 FR 23502, June 27, 1974, as amended at 40 FR 23073, May 28, 1975; 40 FR 24522, June 9, 1975; 43 FR 49746, Oct. 24, 1978; 49 FR 5322, Feb. 10, 1984; 55 FR 32015, Aug. 6, 1990; 58 FR 35308, June 30, 1993; 61 FR 9236, Mar. 7, 1996; 63 FR 1269, Jan. 8, 1998; 64 FR 13909, Mar. 23, 1999; 72 FR 71069, Dec. 14, 2007; 74 FR 46356, Sept. 9, 2009]