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1910.110(b)(11)(i)
Indirect fired vaporizers utilizing steam, water, or other heating medium shall be constructed and installed as follows:
1910.110(b)(11)(i)(a)
Vaporizers shall be constructed in accordance with the requirements of paragraph (b)(3) (i)-(iii) of this section and shall be permanently marked as follows:
1910.110(b)(11)(i)(a)(1)
With the code marking signifying the specifications to which the vaporizer is constructed.
1910.110(b)(11)(i)(a)(2)
With the allowable working pressure and temperature for which the vaporizer is designed.
1910.110(b)(11)(i)(a)(3)
With the sum of the outside surface area and the inside heat exchange surface area expressed in square feet.
1910.110(b)(11)(i)(a)(4)
With the name or symbol of the manufacturer.
1910.110(b)(11)(i)(b)
Vaporizers having an inside diameter of 6 inches or less exempted by the ASME Unfired Pressure Vessel Code, Section VIII of the ASME Boiler and Pressure Vessel Code - 1968 shall have a design pressure not less than 250 p.s.i.g. and need not be permanently marked.
1910.110(b)(11)(i)(c)
Heating or cooling coils shall not be installed inside a storage container.
1910.110(b)(11)(i)(d)
Vaporizers may be installed in buildings, rooms, sheds, or lean-tos used exclusively for gas manufacturing or distribution, or in other structures of light, noncombustible construction or equivalent, well ventilated near the floor line and roof.

When vaporizing and/or mixing equipment is located in a structure or building not used exclusively for gas manufacturing or distribution, either attached to or within such a building, such structure or room shall be separated from the remainder of the building by a wall designed to withstand a static pressure of at least 100 pounds per square foot. This wall shall have no openings or pipe or conduit passing through it. Such structure or room shall be provided with adequate ventilation and shall have a roof or at least one exterior wall of lightweight construction.
1910.110(b)(11)(i)(e)
Vaporizers shall have, at or near the discharge, a safety relief valve providing an effective rate of discharge in accordance with paragraph (b)(10)(iii) of this section, except as provided in paragraph (d)(4)(v)(a), of this section.
1910.110(b)(11)(i)(f)
The heating medium lines into and leaving the vaporizer shall be provided with suitable means for preventing the flow of gas into the heat systems in the event of tube rupture in the vaporizer. Vaporizers shall be provided with suitable automatic means to prevent liquid passing through the vaporizers to the gas discharge piping.
1910.110(b)(11)(i)(g)
The device that supplies the necessary heat for producing steam, hot water, or other heating medium may be installed in a building, compartment, room, or lean-to which shall be ventilated near the floorline and roof to the outside. The device location shall be separated from all compartments or rooms containing liquefied petroleum gas vaporizers, pumps, and central gas mixing devices by a wall designed to withstand a static pressure of at least 100 pounds per square foot. This wall shall have no openings or pipes or conduit passing through it. This requirement does not apply to the domestic water heaters which may supply heat for a vaporizer in a domestic system.
1910.110(b)(11)(i)(h)
Gas-fired heating systems supplying heat exclusively for vaporization purposes shall be equipped with automatic safety devices to shut off the flow of gas to main burners, if the pilot light should fail.
1910.110(b)(11)(i)(i)
Vaporizers may be an integral part of a fuel storage container directly connected to the liquid section or gas section or both.
1910.110(b)(11)(i)(j)
Vaporizers shall not be equipped with fusible plugs.
1910.110(b)(11)(i)(k)
Vaporizer houses shall not have unprotected drains to sewers or sump pits.
1910.110(b)(11)(iii)
Direct gas-fired vaporizers shall be constructed, marked, and installed as follows:
1910.110(b)(11)(iii)(a)(1)
In accordance with the requirements of the American Society of Mechanical Engineers Boiler and Pressure Vessel Code-1968 that are applicable to the maximum working conditions for which the vaporizer is designed.
1910.110(b)(11)(iii)(a)(2)
With the name of the manufacturer; rated BTU input to the burner; the area of the heat exchange surface in square feet; the outside surface of the vaporizer in square feet; and the maximum vaporizing capacity in gallons per hour.
1910.110(b)(11)(iii)(b)(1)
Vaporizers may be connected to the liquid section or the gas section of the storage container, or both; but in any case there shall be at the container a manually operated valve in each connection to permit completely shutting off when desired, of all flow of gas or liquid from container to vaporizer.
1910.110(b)(11)(iii)(b)(2)
Vaporizers with capacity not exceeding 35 gallons per hour shall be located at least 5 feet from container shutoff valves. Vaporizers having capacity of more than 35 gallons but not exceeding 100 gallons per hour shall be located at least 10 feet from the container shutoff valves. Vaporizers having a capacity greater than 100 gallons per hour shall be located at least 15 feet from container shutoff valves.
1910.110(b)(11)(iii)(c)
Vaporizers may be installed in buildings, rooms, housings, sheds, or lean-tos used exclusively for vaporizing or mixing of liquefied petroleum gas. Vaporizing housing structures shall be of noncombustible construction, well ventilated near the floorline and the highest point of the roof. When vaporizer and/or mixing equipment is located in a structure or room attached to or within a building, such structure or room shall be separated from the remainder of the building by a wall designed to withstand a static pressure of at least 100 pounds per square foot. This wall shall have no openings or pipes or conduit passing through it. Such structure or room shall be provided with adequate ventilation, and shall have a roof or at least one exterior wall of lightweight construction.
1910.110(b)(11)(iii)(d)
Vaporizers shall have at or near the discharge, a safety relief valve providing an effective rate of discharge in accordance with paragraph (b)(10)(iii) of this section. The relief valve shall be so located as not to be subjected to temperatures in excess of 140 deg. F.
1910.110(b)(11)(iii)(e)
Vaporizers shall be provided with suitable automatic means to prevent liquid passing from the vaporizer to the gas discharge piping of the vaporizer.
1910.110(b)(11)(iii)(f)
Vaporizers shall be provided with means for manually turning off the gas to the main burner and pilot.
1910.110(b)(11)(iii)(g)
Vaporizers shall be equipped with automatic safety devices to shut off the flow of gas to main burners if the pilot light should fail. When the flow through the pilot exceeds 2,000 B.t.u. per hour, the pilot also shall be equipped with an automatic safety device to shut off the flow of gas to the pilot should the pilot flame be extinguished.
1910.110(b)(11)(iii)(h)
Pressure regulating and pressure reducing equipment if located within 10 feet of a direct fire vaporizer shall be separated from the open flame by a substantially airtight noncombustible partition or partitions.
1910.110(b)(11)(iii)(i)
Except as provided in (c) of this subdivision, the following minimum distances shall be maintained between direct fired vaporizers and the nearest important building or group of buildings:

Ten feet for vaporizers having a capacity of 15 gallons per hour or less vaporizing capacity.

Twenty-five feet for vaporizers having a vaporizing capacity of 16 to 100 gallons per hour.

Fifty feet for vaporizers having a vaporizing capacity exceeding 100 gallons per hour.
1910.110(b)(11)(iii)(j)
Direct fired vaporizers shall not raise the product pressure above the design pressure of the vaporizer equipment nor shall they raise the product pressure within the storage container above the pressure shown in the second column of Table H-31.

TABLE H-31
Container type For gases with vapor press. Not to exceed lb. per sq. in. gage at 100 deg. F (37.8 deg C.) Minimum design pressure of container, lb. per sq. in. gage
1949 and earlier editions of ASME Code (Par. U-68, U-69) 1949 edition of ASME Code. (Par. U-200, U-201); 1950, 1952, 1956, 1959, 1962, 1965, and 1968 (Division 1)editions of ASME Code; All editions of API-ASME Code(3)
(1)80 (1)80 (1)80 (1)100
100 100 100 125
125 125 125 156
150 150 150 187
175 175 175 219
(2)200 215 200 250
   Footnote(1) New storage containers of the 80 type have not been authorized since Dec. 31, 1947.

   Footnote(2) Container type may be increased by increments of 25. The minimum design pressure of containers shall be 100% of the container type designation when constructed under 1949 or earlier editions of the ASME Code (Par. U-68 and U-69). The minimum design pressure of containers shall be 125% of the container type designation when constructed under: (1) the 1949 ASME Code (Par. U-200 and U-201), (2) 1950, 1952, 1956, 1959, 1962, 1965, and 1968 (Division 1) editions of the ASME Code, and (3) all editions of the API-ASME Code.

   Footnote(3) Construction of containers under the API-ASME Code is not authorized after July 1, 1961.
1910.110(b)(11)(iii)(k)
Vaporizers shall not be provided with fusible plugs.
1910.110(b)(11)(iii)(l)
Vaporizers shall not have unprotected drains to sewers or sump pits.
1910.110(b)(11)(iv)
Direct gas-fired tank heaters shall be constructed and installed as follows:
1910.110(b)(11)(iv)(a)
Direct gas-fired tank heaters, and tanks to which they are applied, shall only be installed above ground.
1910.110(b)(11)(iv)(b)
Tank heaters shall be permanently marked with the name of the manufacturer, the rated B.t.u. input to the burner, and the maximum vaporizing capacity in gallons per hour.
1910.110(b)(11)(iv)(c)
Tank heaters may be an integral part of a fuel storage container directly connected to the container liquid section, or vapor section, or both.
1910.110(b)(11)(iv)(d)
Tank heaters shall be provided with a means for manually turning off the gas to the main burner and pilot.
1910.110(b)(11)(iv)(e)
Tank heaters shall be equipped with an automatic safety device to shut off the flow of gas to main burners, if the pilot light should fail. When flow through pilot exceeds 2,000 B.t.u. per hour, the pilot also shall be equipped with an automatic safety device to shut off the flow of gas to the pilot should the pilot flame be extinguished.
1910.110(b)(11)(iv)(f)
Pressure regulating and pressure reducing equipment if located within 10 feet of a direct fired tank heater shall be separated from the open flame by a substantially airtight noncombustible partition.
1910.110(b)(11)(iv)(g)
The following minimum distances shall be maintained between a storage tank heated by a direct fired tank heater and the nearest important building or group of buildings:

Ten feet for storage containers of less than 500 gallons water capacity.

Twenty-five feet for storage containers of 500 to 1,200 gallons water capacity.

Fifty feet for storage containers of over 1,200 gallons water capacity.
1910.110(b)(11)(iv)(h)
No direct fired tank heater shall raise the product pressure within the storage container over 75 percent of the pressure set out in the second column of Table H-31.
1910.110(b)(11)(v)
The vaporizer section of vaporizer-burners used for dehydrators or dryers shall be located outside of buildings; they shall be constructed and installed as follows:
1910.110(b)(11)(v)(a)
Vaporizer-burners shall have a minimum design pressure of 250 p.s.i.g. with a factor of safety of five.
1910.110(b)(11)(v)(b)
Manually operated positive shut-off valves shall be located at the containers to shut off all flow to the vaporizer-burners.
1910.110(b)(11)(v)(c)
Minimum distances between storage containers and vaporizer-burners shall be as follows:

Water capacity per container (gallons) Minimum
distances
(feet)
Less than 501 10
501 to 2,000 25
Over 2,000 50
1910.110(b)(11)(v)(d)
The vaporizer section of vaporizer-burners shall be protected by a hydrostatic relief valve. The relief valve shall be located so as not to be subjected to temperatures in excess of 140 deg. F. The start-to-discharge pressure setting shall be such as to protect the components involved, but not less than 250 p.s.i.g. The discharge shall be directed upward and away from component parts of the equipment and away from operating personnel.
1910.110(b)(11)(v)(e)
Vaporizer-burners shall be provided with means for manually turning off the gas to the main burner and pilot.
1910.110(b)(11)(v)(f)
Vaporizer-burners shall be equipped with automatic safety devices to shut off the flow of gas to the main burner and pilot in the event the pilot is extinguished.
1910.110(b)(11)(v)(g)
Pressure regulating and control equipment shall be located or protected so that the temperatures surrounding this equipment shall not exceed 140 deg. F. except that equipment components may be used at higher temperatures if designed to withstand such temperatures.
1910.110(b)(11)(v)(h)
Pressure regulating and control equipment when located downstream of the vaporizer shall be designed to withstand the maximum discharge temperature of the vapor.
1910.110(b)(11)(v)(i)
The vaporizer section of vaporizer-burners shall not be provided with fusible plugs.
1910.110(b)(11)(v)(j)
Vaporizer coils or jackets shall be made of ferrous metal or high temperature alloys.
1910.110(b)(11)(v)(k)
Equipment utilizing vaporizer-burners shall be equipped with automatic shutoff devices upstream and downstream of the vaporizer section connected so as to operate in the event of excessive temperature, flame failure, and, if applicable, insufficient airflow.
1910.110(b)(11)(ii)
Atmospheric vaporizers employing heat from the ground or surrounding air shall be installed as follows:
1910.110(b)(11)(ii)(a)
Buried underground, or
1910.110(b)(11)(ii)(b)
Located inside the building close to a point at which pipe enters the building provided the capacity of the unit does not exceed 1 quart.
1910.110(b)(11)(ii)(c)
Vaporizers of less than 1 quart capacity heated by the ground or surrounding air, need not be equipped with safety relief valves provided that adequate tests demonstrate that the assembly is safe without safety relief valves.
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