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API MPMS Chapter 19.2 Evaporative Loss from Floating-roof Tanks, Fourth Edition
Handbook / Manual / Guide by American Petroleum Institute, 08/01/2020
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MPMS CHAPTER 19.2
FOURTH EDITION, AUGUST 2020
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Copyright © 2020 American Petroleum Institute
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Page
Scope 1
Normative References 2
Symbols 2
Procedure for Estimating Loss 3
General 3
S
Standing Loss L 4
W
Working Loss L 22
Sample Problems 23
General 23
EFRT Sample Problem 23
IFRT Sample Problem 27
Domed EFRT Sample Problem 30
Equipment Descriptions 34
Components 34
Types of Floating-Roof Tanks 59
Loss Mechanisms 60
General 60
Standing Loss 61
Working Loss 63
Development of Estimation Methods 63
General 63
Standing Loss 63
Working Loss 68
Annex A (informative) Development of Rim-Seal Loss Factors 70
Annex B (informative) Development of Rim-Seal Relationship Between Airflow Rate and Wind Speed 74
Annex C (informative) Development of Diameter Function 76
Annex D (informative) Development of Deck-Fitting Loss Factors 78
Annex E (informative) Development of Vapor Pressure Function 85
Annex F (informative) Development of Product Factors 87
Annex G (informative) Development of Clingage Factors 89
Annex H (informative) Development of Fitting Wind-Speed Correction Factor 90
Annex I (informative) Development of Deck-Seam Loss Factors 93
Annex J (informative) Documentation Records 95
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Page
Annex K (informative) SI Units 96
Bibliography 97
EFRT with Pontoon Floating Roof 36
EFRT with Double-deck Floating Roof 37
IFRT with Noncontact Deck 38
Domed EFRT 39
Vapor-mounted Primary Seals 41
Liquid-mounted Primary Seals 43
Mechanical-shoe Primary Seals 44
Secondary Seals 46
Access Hatch 47
Fixed-roof Support Column 47
Gauge Float (Automatic Gauge) 48
Gauge Hatch Sample Ports 49
Vacuum Breaker 50
Deck Drains 51
Deck Leg 52
Rim Vent 53
Vertical Ladder 54
Unslotted (Unperforated) Guidepole 55
Slotted (Perforated) Guidepole 56
Ladder/Guidepole Combination 57
Symbols 2
Rim-Seal Loss Factors 6
fc
Typical Number of Columns N for Tanks with Column-Supported Roofs 15
Typical Number of Vacuum-Breakers N
fvb
fdd
and Deck Drains N
for API 650 Annex C Decks (EFRTs and
Domed EFRTs) 15
Typical Number of Deck Legs N
fdl
for API 650 Annex C Floating Roofs 16
d
Deck-Seam Length Factors S 18
L
Clingage Factors C for Steel Tanks (bbl/1000 ft2) 22
C
Effective Column Diameter D for Typical Column Construction 23
Summary of Deck Fittings Selected for Data Regression, and Associated Loss Factors for Each 81
Net Liquid Surface Area for a Ladder/Guidepole Combination 82
Emission Factors for IFRT Ladder Sleeves 83
vi
Page
IFRT Emission Factor Comparison for a Ladder/Guidepole Combination 84
Assumed Distribution of Time for a Floating Roof in Each Height Range 91
Assumed Floating Roof Height Distribution versus Survey Results 91
Noncontact Deck Seams 94
Contact Deck Seams 94
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Evaporative Loss from Floating-roof Tanks
This standard contains methodologies for estimating the total evaporative losses of hydrocarbons from external floating-roof tanks (EFRTs), freely vented internal floating-roof tanks (IFRTs), and domed external floating-roof tanks (domed EFRTs).
The methodologies provide loss estimates for general equipment types based on laboratory, test-tank, and field-
tank data.
Types of floating roofs, rim-seal systems, and deck fittings are described for information only.
The equations estimate average annual losses from floating-roof tanks for various types of tank construction, floating-roof construction, rim-seal systems, and deck fittings, as well as for various liquid stocks, stock vapor pressures, tank sizes, and wind speeds (EFRTs).
The equations were developed for:
stocks with a true vapor pressure greater than ~0.1 psia;
average wind speeds ranging from 0 miles per hour (mph) to 15 mph (EFRTs); and
tank diameters greater than 20 ft.
The estimation techniques become more approximate when these conditions are not met.
When this standard is used to estimate losses from non-freely vented (closed vent) internal or domed external floating-roof tanks (tanks vented only through a pressure-vacuum relief vent, blanketed with an inert gas, vented to a vapor processing unit, or otherwise restricted from being freely vented), refer to the methodology in API TR 2569 [7].
The equations are not intended to be used in the following applications.
a) to estimate losses from unstable or boiling stocks (i.e. stocks with a true vapor pressure greater than the atmospheric pressure at the tank location) or from petroleum liquids or petrochemicals for which the vapor pressure is not known or cannot readily be predicted;
to estimate losses from tanks in which the materials used in the rim seal, deck fittings, or deck seams have either deteriorated or been significantly permeated by the stored stock;
to estimate losses from storage tanks that do not have a floating roof (API MPMS 19.1[53] addresses this);
to estimate losses from landing floating roofs (API MPMS 19.6.1 [8] addresses this);
e) to estimate losses from cleaning storage tanks (API MPMS 19.6.2 [9] addresses this).
The estimation procedures were developed to provide estimates of typical losses from floating-roof tanks that are properly maintained and in normal working condition. Losses from poorly maintained tanks can be greater. Because the loss equations are based on equipment conditions that represent a large population of tanks, a loss estimate for a group of floating-roof tanks will be more accurate than a loss estimate for an individual tank. The estimation can be improved by using detailed field information, including climatic data and operational data for the appropriate time period.
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