Boiler Venting. Definitions, Theory and Applications. Presented by: Jason Geagan, National Sales Manager US Draft Co Fort Worth, TX

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Boiler Venting Definitions, Theory and Applications Presented by: Jason Geagan, National Sales Manager US Draft Co Fort Worth, TX

Gas Appliance Listings ANSI Z21 - Categorized Appliances Gas fired low pressure steam and hot water boilers UL795 - Building Heating Appliances Commercial-Industrial Gas Heating Appliances

Gas Appliance Listings Definitions 3.3.80* Gas Appliance Categories. Vented gas appliances are classified for venting purposes into four categories as follows: (1)Category I An appliance that operates with a non-positive vent static pressure and with a vent gas temperature that avoids excessive condensate production in the vent (2)Category II An appliance that operates with a non-positive vent static pressure and with a vent gas temperature that may cause excessive condensate production in the vent (3)Category III An appliance that operates with a positive vent static pressure and with a vent gas temperature that avoids excessive condensate production in the vent (4)Category IV An appliance that operates with a positive vent static pressure and with a vent gas temperature that may cause excessive condensate production in the vent. A.3.3.80 Gas Appliance Categories. For additional information on appliance categorization, see the appropriate Z21 and Z83 American National Standards.

ANSI Z223.1 - Venting Categories Non-Condensing ~80-84% Efficiency I III Negative Positive II IV 85%+ Efficiency Condensing

ANSI Z223.1 - Venting Categories Type B Gas Vent is the most common venting material for Category I Appliances Non-Condensing ~80-84% Efficiency Specification: UL-441 B-Vent I III Negative Positive II IV Double Wall Special Gas Vent is the most common venting material for Category II, III & IV Appliances 85%+ Efficiency Condensing Specification: UL-1738 Special Gas Vent

Using PVC to Vent Flue Gases

UL795 - NFPA 211 Appliances Definitions 3.3.3.6 Nonresidential Appliance, 1400 F. A commercial, industrial, or institutional appliance needing a chimney capable of withstanding a continuous flue gas temperature not exceeding 1400 F (760 C). 3.3.3.8 Nonresidential, Low-Heat Appliance. A commercial, industrial, or institutional appliance needing a chimney capable of withstanding a continuous flue gas temperature not exceeding 1000 F (538 C).

UL103 Pressure Tested Chimney 304SS or 316SS inner wall Galvalum/Aluminized, 304SS or 316SS outer wall Pressure tested up to 60 WC 1 air to 4 fiber insulation

Sizing Gas Appliance Vents

ASHRAE Chimney Design Equation The equations and design chart may be used to determine the vent or chimney size based on steady-state operating conditions I = 4.13x10 5 (d i 2/M)(ΔpT m /kb) 0.5 I = Input, Btu/h d i = Inside Diameter, in. M = Ratio of Mass Flow to Heat Input Δp = Pressure Loss, w.c. T m = Mean Flue Gas Temperature, R k = Resistance Coefficients B = Barometric Pressure, inhg

ASHRAE Chimney Design Equation The equations and design chart may be used to determine the vent or chimney size based on steady-state operating conditions I = 4.13x10 5 (d i 2/M)(ΔpT m /kb) 0.5 I = Input, Btu/h d i = Inside Diameter, in. M = Ratio of Mass Flow to Heat Input Δp = Pressure Loss, w.c. T m = Mean Flue Gas Temperature, R k = Resistance Coefficients B = Barometric Pressure, inhg Does not consider modulation, cycling, or time to achieve equilibrium flow conditions from a cold start

ASHRAE Equation Determine Pressure Loss Determine the Pressure Loss Δp = (k p m V 2 )/10.4g Δp = Pressure Loss, WC k = Total System Resistance p m = Gas Density, lb/ft 3 V = Gas Velocity, FPS g = gravity, 32.174 ft/s 2 Pressure losses are directly proportional to the resistance factor and to the square of the velocity.

ASHRAE Equation Determine Pressure Loss Determine the Theoretical Draft D t = 0.2554BH(1/T o - 1/T m ) D t = Theoretical Draft, WC B = Barometric Pressure, inhg T o = Ambient Temperature, R T m = Mean Flue Gas Temperature, R H = Height of the Chimney, ft Theoretical draft increases directly with height and the difference between ambient and flue gas temperatures

ASHRAE Equation Determine Pressure Loss Determine the Theoretical Draft 0.098 wc = 0.2554(29.92)(20)((1/520)-(1/780)) Determine the Theoretical Draft 0.079 wc = 0.2554(29.92)(20)((1/520)-(1/710)) Determine the Theoretical Draft 0.039 wc = 0.2554(29.92)(20)((1/520)-(1/600)) Theoretical draft increases directly with height and the difference between ambient and flue gas temperatures

Effect of Chimney Height vs Outdoor Temp Height 105 F 60 F 0 F 5 -.017 WC -.0233 WC -.032 WC 20 -.069 WC -.093 WC -.131 WC 50 -.17 WC -.233 WC -.320 WC @ 300 F Flue Gas Temp., 500 ASL

Barometric Dampers

Variations of Draft, Common Vent 0.25 0.20 0.15 0.10 0.05 0.00-0.05-0.10-0.15-0.20-0.25 Boiler 1 Boiler 2 Boiler 3 Boiler 4

Variations of Draft, Common Vent Category I 0.25 0.20 0.15 0.10 0.05 0.00-0.05-0.10-0.15-0.20-0.25 Boiler 1 Boiler 2 Boiler 3 Boiler 4

Variations of Draft, Common Vent Category II & IV Manufacturer A: -0.25 / +0.25 w.c. Manufacturer B: -0.25 / +0.50 w.c. Manufacturer C: -0.10 / +1.25 w.c. Manufacturer D: -0.10 / 0.00 w.c.

Typical Mechanical Draft System

Typical Mechanical Draft System

Typical Mechanical Draft System

Variations of Draft, Common Vent 0.25 0.20 0.15 0.10 0.05 0.00-0.05-0.10-0.15-0.20-0.25 Boiler 1 Boiler 2 Boiler 3 Boiler 4

EC Flow Technology

Common Code Violations 12.7.2 Gas Vent Termination. The termination of gas vents shall comply with the following requirements: (1)A gas vent shall terminate in accordance with one of the following: (a)gas vents that are 12 in. (300 mm) or less in size and located not less than 8 ft from a vertical wall or similar obstruction shall terminate above the roof in accordance with Figure 12.7.2 and Table 12.7.2. (b)gas vents that are over 12 in. in size or are located less than 8 ft from a vertical wall or similar obstruction shall terminate not less than 2 ft above the highest point where they pass through the roof and not less than 2 ft (0.6 m) above any portion of a building within 10 ft (3.0 m) horizontally.

Common Code Violations

Lower Terminations with Draft Inducer

Common Code Violations 13.1.9 Vertical Vent Upsizing/7 Rule. Where the vertical vent has a larger diameter than the vent connector, the vertical vent diameter shall be used to determine the minimum vent capacity, and the connector diameter shall be used to determine the maximum vent capacity. The flow area of the vertical vent shall not exceed seven times the flow area of the listed appliance categorized vent area, flue collar area, or draft hood outlet area unless designed in accordance with approved engineering methods.

Common Code Violations 12.4.3.3 Forced draft systems and all portions of induced draft systems under positive pressure during operation shall be designed and installed so as to prevent leakage of flue or vent gases into a building. 12.4.3.4 Vent connectors serving appliances vented by natural draft shall not be connected into any portion of mechanical draft systems operating under positive pressure.

Common Venting - Good Practices

Common Venting - Good Practices

Overdraft

Effect of Chimney Height vs Outdoor Temp Manufacturer A: -0.25 / +0.25 w.c. Manufacturer B: -0.25 / +0.50 w.c. Manufacturer C: -0.10 / +1.25 w.c. Manufacturer D: -0.10 / 0.00 w.c.

Typical Mechanical Draft System

Concerns of Mechanical Draft 1. Cost

Concerns of Mechanical Draft 1. Cost In most cases, equipment costs can be offset by less vent material and smaller diameters

Concerns of Mechanical Draft 1. Cost 2. Complication

Concerns of Mechanical Draft 1. Cost 2. Complication In most cases, equipment manufacturers work together to minimize complications

Concerns of Mechanical Draft 1. Cost 2. Complication 3. Single Point of Failure

Concerns of Mechanical Draft 1. Cost 2. Complication 3. Single Point of Failure Redundancy systems can be designed to prevent single failure point

Individual Connector Draft System

Thank You! Questions and Comments