API MPMS Chapter 19.1
- Handbook / Manual / Guide by American Petroleum Institute, 10/01/2012
- Evaporative Loss Measurement, Section 1-Evaporative Loss from Fixed-Roof Tanks, Fourth Edition
- Category: API
$157.00
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Full Description
This standard contains methodologies for estimating the total evaporative losses of hydrocarbons from fixed-roof tanks. The methodologies provide loss estimates for general equipment types based on laboratory, test-tank and field-tank data.
Types of fixed-roof tanks and roof fittings described are for information only.
The equations estimate average annual losses from uninsulated fixed-roof tanks for various liquid stocks, stock vapor pressures, tank sizes, meteorological conditions, and operating conditions.
The following special cases are addressed:
a) Horizontal tanks.
b) Higher volatility stocks (true vapor pressure greater than 0.1 psia).
c) Vent settings higher than 0.03 psia (0.5 oz/in2).
The estimation may be improved by using detailed field information, including climatic data and operational data for the appropriate time period.
The equations are not intended to be used in the following applications:
a) To estimate losses from unstable or boiling stocks or from petroleum liquids or petrochemicals for which the vapor pressure is not known or cannot readily be predicted (to calculate emissions from tanks that contain material at or above their boiling point or the point at which material starts to flash, the API model E&P Tank (API Publication 4697) can be used).
b) To estimate losses from fixed-roof tanks which have an internal floating roof. API MPMS Ch. 19.2 and API TR 2569 address these.
c) To estimate losses from fixed-roof tanks which have either roof or shell insulation.
d) To estimate losses from cleaning fixed-roof tanks. API TR 2568 addresses this.
Types of fixed-roof tanks and roof fittings described are for information only.
The equations estimate average annual losses from uninsulated fixed-roof tanks for various liquid stocks, stock vapor pressures, tank sizes, meteorological conditions, and operating conditions.
The following special cases are addressed:
a) Horizontal tanks.
b) Higher volatility stocks (true vapor pressure greater than 0.1 psia).
c) Vent settings higher than 0.03 psia (0.5 oz/in2).
The estimation may be improved by using detailed field information, including climatic data and operational data for the appropriate time period.
The equations are not intended to be used in the following applications:
a) To estimate losses from unstable or boiling stocks or from petroleum liquids or petrochemicals for which the vapor pressure is not known or cannot readily be predicted (to calculate emissions from tanks that contain material at or above their boiling point or the point at which material starts to flash, the API model E&P Tank (API Publication 4697) can be used).
b) To estimate losses from fixed-roof tanks which have an internal floating roof. API MPMS Ch. 19.2 and API TR 2569 address these.
c) To estimate losses from fixed-roof tanks which have either roof or shell insulation.
d) To estimate losses from cleaning fixed-roof tanks. API TR 2568 addresses this.
Product Details
- Edition:
- 4th
- Published:
- 10/01/2012
- Number of Pages:
- 38
- File Size:
- 1 file , 510 KB
- Product Code(s):
- H190104, H190104, H190104
- Note:
- This product is unavailable in Russia, Cuba, Syria, North Korea, Ukraine, Belarus, Iran
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