Fla. Admin. Code R. 62-730.182
(1) This section applies only to transfer facilities which store shipments of hazardous waste that are required to be manifested and to facilities, including federal facilities, which treat, store, or dispose of shipments of hazardous waste generated off-site that are required to be manifested. This section does not apply to:
(4) A substantial modification under this subsection means any change in operations, structures, or permit conditions, at a permitted TSD, or any changes to the transfer facility notification submitted to the Department in accordance with subsection 62-730.171(2), F.A.C., which is reasonably expected to lead to a substantial increase in the potential impact, or risk of impact, from a release at that facility, as follows:
(5) (a) In the demonstration required by subsection 62-730.182(3), F.A.C., the owner or operator shall analyze and report:
1. One worst-case release scenario that is estimated to create the greatest distance in any direction to an inhalation toxic endpoint determined in accordance with the hierarchy referenced in sub-subparagraph 62-730.182(5)(g)1.a., F.A.C.; and,
2. One worst-case release scenario that is estimated to create the greatest distance in any direction to a flammable endpoint defined in sub-subparagraph 62-730.182(5)(g)1.b., F.A.C., resulting from the release of regulated flammable substances under worst-case conditions defined in paragraph 62-730.182(5)(g), F.A.C.
(b) The worst-case release quantity shall be the greater of the following:
1. For substances in a tank (for example, a reactor, vat, kettle, boiler, or cylinder) or other container (for example, a drum or barrel), the greatest amount potentially held in a single tank or container, taking into account administrative controls that limit the maximum quantity, or
2. For substances in pipes, the greatest amount potentially in a pipe, taking into account administrative controls that limit the maximum quantity.
(c) 1. For toxic substances that are normally gases at ambient temperature and handled as a gas or as a liquid under pressure, the owner or operator shall assume that the quantity in the vessel or pipe, as determined under paragraph 62-730.182(5)(b), F.A.C., is released as a gas over 10 minutes. The release rate (in minutes) shall be assumed to be the total quantity divided by 10 unless passive mitigation systems are in place.
2. For gases handled as refrigerated liquids at ambient pressure:
a. If the released substance is not contained by passive mitigation systems or if the contained pool would have a depth of one centimeter, the owner or operator shall assume that the substance is released as a gas in 10 minutes,
b. If the released substance is contained by passive mitigation systems in a pool with a depth greater than one centimeter, the owner or operator may assume that the quantity in the vessel or pipe, as determined under paragraph 62-730.182(5)(b), F.A.C., is spilled instantaneously to form a liquid pool. The volatilization rate (release rate) shall be calculated at the boiling point of the substance and at the conditions specified in paragraph 62-730.182(5)(d), F.A.C.
(d) 1. For toxic substances that are normally liquids at ambient temperature, the owner or operator shall assume that the quantity in the vessel or pipe, as determined under paragraph 62-730.182(5)(b), F.A,C., is spilled instantaneously to form a liquid pool.
a. The surface area of the pool shall be determined by assuming that the liquid spreads to one centimeter deep unless passive mitigation systems are in place that serve to contain the spill and limit the surface area. Where passive mitigation is in place, the surface area of the contained liquid shall be used to calculate the volatilization rate.
b. The owner or operator may take into account the actual surface characteristics when analyzing the volatilization rate.
2. The volatilization rate shall account for the highest daily maximum temperature occurring in the past three years and the temperature of the substance in the vessel.
3. The rate of release to air shall be determined from the volatilization rate of the liquid pool. The owner or operator may use any publicly available technique or methodology that accounts for the modeling conditions and are recognized by industry as applicable as part of current practices. Proprietary models that account for the modeling conditions may be used provided the owner or operator allows the implementing agency access to the model and describes model features and differences from publicly available models upon request.
(e) For flammable gases, the owner or operator shall assume that the quantity of the substance, as determined under paragraph 62-730.182(5)(b), F.A.C., and the provisions in subparagraphs 62-730,182(5)(e)1. and 2., F.A.C., vaporizes resulting in a vapor cloud explosion. A yield factor of 10 percent of the available energy released in the explosion shall be used to determine the distance to the explosion endpoint if the model used is based on trinitrotoluene (TNT) equivalent methods.
1. For flammable substances that are normally gases at ambient temperature and handled as a gas or as a liquid under pressure, the owner or operator shall assume that the quantity in the vessel or pipe, as determined under paragraph 62-730.182(5)(b), F.A.C., is released as a gas over 10 minutes. The total quantity shall be assumed to be involved in the vapor cloud explosion.
2. For flammable gases handled as refrigerated liquids at ambient pressure:
a. If the released substance is not contained by passive mitigation systems or if the contained pool would have a depth of one centimeter or less, the owner or operator shall assume that the total quantity of the substance is released as a gas in 10 minutes, and the total quantity will be involved in the vapor cloud explosion.
b. If the released substance is contained by passive mitigation systems in a pool with a depth greater than one centimeter, the owner or operator may assume that the quantity in the vessel or pipe, as determined under paragraph 62-730.182(5)(b), F.A.C., is spilled instantaneously to form a liquid pool. The volatilization rate (release rate) shall be calculated at the boiling point of the substance and at the conditions specified in paragraph 62-730.182(5)(d), F.A.C. The owner or operator shall assume that the quantity which becomes vapor in the first 10 minutes is involved in the vapor cloud explosion.
(f) For flammable liquids, the owner or operator shall assume that the quantity of the substance, as determined under paragraph 62-730.182(5)(b), F.A.C., and the provisions in subparagraphs 62-730.182(5)(b)1. and 2., F.A.C., vaporizes resulting in a vapor cloud explosion. A yield factor of 10 percent of the available energy released in the explosion shall be used to determine the distance to the explosion endpoint if the model used is based on TNT equivalent methods.
1. For regulated flammable substances that are normally liquids at ambient temperature, the owner or operator shall assume that the entire quantity in the vessel or pipe, as determined under paragraph 62-730.182(5)(b), F.A.C., is spilled instantaneously to form a liquid pool. For liquids at temperatures below their atmospheric boiling point, the volatilization rate shall be calculated at the conditions specified in paragraph 62-730.182(5)(d), F.A.C.
2. The owner or operator shall assume that the quantity which becomes vapor in the first 10 minutes is involved in the vapor cloud explosion.
(g) The owner or operator may use any commercially or publicly available air dispersion modeling techniques, provided the techniques account for the modeling conditions and are recognized by industry as applicable as part of current practices. Proprietary models that account for the modeling conditions may be used provided the owner or operator allows the implementing agency access to the model and describes model features and differences from publicly available models upon request. The chosen model shall use the following parameters:
(III) For lower flammability limit, concentration of flammable constituent in air that exceeds 25 percent of their lower flammability limit.
2. The owner or operator shall use a wind speed of 1.5 meters per second and F atmospheric stability class (Pasquill-Gifford system).
3. The owner or operator shall use the highest daily maximum temperature in the previous three years and average humidity for the site, based on temperature/humidity data gathered at the stationary source or at a local meteorological station.
4. The worst-case release of a toxic substance shall be analyzed assuming a ground level (0 feet) release.
5. The owner or operator shall use either urban or rural topography, as appropriate. Urban means that there are many obstacles in the immediate area; obstacles include buildings or trees. Rural means there are no buildings in the immediate area and the terrain is generally flat and unobstructed.
6. The owner or operator shall ensure that tables or models used for dispersion analysis of toxic substances appropriately account for gas density.
7. For worst case, liquids other than gases liquefied by refrigeration only shall be considered to be released at the highest daily maximum temperature, based on data for the previous three years appropriate for the stationary source, or at process temperature, whichever is higher.
1. The following endpoints shall be used:
a. The inhalation toxic endpoints shall be determined in accordance with the hierarchy provided in the “Technical Report for the Substantial Modification Rule for 62-730, F.A.C.” dated August 1, 2008, which is hereby adopted and incorporated by reference.
b. The endpoints for flammables vary according to the scenarios studied:
(i) Factors in selecting a worst-case scenario. Notwithstanding the provisions of paragraph 62-730.182(5)(b), F.A.C., of this section, the owner or operator shall select as the worst case for flammable substances or the worst case for toxic substances, a scenario based on the following factors if such a scenario would result in a greater distance to an endpoint defined in subparagraph 62-730.182(5)(g)1., F.A.C., beyond the stationary source boundary than the scenario provided under paragraph 62-730.182(5)(b), F.A.C., of this section:
1. Smaller quantities handled at higher process temperature or pressure; and,
2. Proximity to the boundary of the stationary source.
(6) In the demonstration required by subsection 62-730.182(3), F.A.C., the owner or operator shall analyze and report:
(7) The modifications listed in paragraph 62-730.182(4)(b), F.A.C., shall not be considered to substantially increase the risk of impact if, evaluated on a unit by unit basis, the applicable criteria within the following conditions are met:
(a) Any additional units or expanded areas are:
1. Separated from adjoining hazardous waste storage, treatment, or disposal units or areas by 4-hour fire rated walls, or
2. Separated from the existing hazardous waste storage, treatment, disposal units, or areas by a sufficient distance (to be specified in the site-specific permit or other authorization based upon the flammability and explosive potential of the permitted waste types at their maximum permitted mass or volume; the types of containers and building materials; the available data on wind speed and relative humidity; any passive fire suppression systems; and the presence of natural or manmade features between the existing and proposed units) such that a spill, fire, or other accidental release will not result in the spread of a fire, spill, or other accidental release to the new unit or units.
(d) Secondary containment is provided for all loading and unloading areas, as follows:
1. The secondary containment system has sufficient capacity to contain the total volume of the largest container or 10% of the total volume of the maximum number of containers managed in the loading and unloading area, whichever is greater.
2. If the secondary containment system is not sheltered from precipitation, the secondary containment system has the additional capacity necessary to contain precipitation at the loading and unloading area from a 25-year, 24-hour storm event.
3. For attended transfer to a tank, the tank is installed with a spill containment system at each tank fill connection. This spill containment system is designed to prevent a discharge of regulated substances when the transfer hose or pipe is detached from the tank fill pipe and meets the requirements of paragraph 62-761.500(1)(e), F.A.C.
Rulemaking Authority 403.0877, 403.7211 FS. Law Implemented 403.0877, 403.7211 FS. History–New 10-28-08.