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Bends in piping, pipe expansions and/or contractions, 

valves orifice plates or flow obstructing devices of any kind 

cause turbulent flow. Turbulent flow enhances mixing of the 

combustible gases, greatly increasing the combustion intensity. 

This can result in increased flame speeds, higher flame 

temperatures and higher flame front pressures than would 

occur in normal flow conditions. Obstructions in protected side 

piping can cause pressure buildup that might inhibit the effective 

performance of the DFA Series under certain conditions.

Installation

WARNING

!

Always make sure that the system is at 

atmospheric pressure and that there is no 

ignitable gas that could flash when either 

installing or maintaining the unit.

Lifting

DFA Series arrestors are not designed for single point lifting. An 

appropriately designed spreader bar must be used when lifting 

or moving the unit. The angle of the lift lines should be no more 

than 5° from the vertical (refer to Figure 4). Recommended 

shackles are Crosby 1-3/4" 25t-G-2130 (Stock No. 1019659) 

or equivalent.

Connection

DFA Series arrestors are normally provided with CL150 

raised or flat faced flanges. Other flanges such as CL300 

are sometimes provided on special request. Make sure the 

companion flanges installed in adjacent piping match the 

flanges on the detonation flame arrestor.
Standard compressed fiber gaskets that withstands 

temperatures of 450°F / 232°C or higher are normally used, 

but other materials of equal or higher temperature capability 

may be used at the customer’s discretion.

Positioning

CAUTION

The detonation flame arrestor element 

is fitted with lugs for lifting the element 

assembly during servicing operations. These 

lugs are not intended for lifting the entire 

unit. Damage to the detonation flame arrestor 

may result from improper lifting. The unit 

should be lifted using the lugs located on 

each end-section or with appropriately rated 

Nylon (PA) straps rigged on the outside 

of the tension studs. Detonation flame 

arrestors fitted with temperature sensors 

are directional dependent if the temperature 

sensor is only installed on one side of the 

arrestor. The sensor must be located on the 

unprotected side of the arrestor in that case.

The arrestor should be positioned such that the entire 

arrestor is accessible for removal. Install the unit such that 

the flow arrow located on the unit points in the direction 

travelling with the vapor flow. Models that have drain 

plugs are designed for horizontal installation and should 

be installed with the drain ports aligned at the bottom of 

the unit. Models that have pressure taps are designed to 

allow pressure gauges to be installed on both sides of the 

flame cell assembly to determine blockage. The pressure 

taps should be aligned at the top to allow easy viewing of 

the gauges. Units that are equipped with optional internal 

cleaning systems should be connected to a source of 

cleaning media such as water, steam or other suitable 

solvent. Observe recommended installation practice as 

detailed bends and/or flow obstruction section.

Flow Direction 

The DFA Series is not bi-directional when temperature 

sensors are installed unless a sensor is installed on both 

sides of the arrestor element assembly. All arrestors covered 

in this manual can be installed either vertically or horizontally. 

Consideration should be given to non-symmetrical assemblies 

that include features such as clean-out ports, temperature 

monitoring device or other options that might have a preferred 

installation direction to suit the needs of the customer.

Piping Expansions and Reductions 

Adjacent to Detonation Flame Arrestor

WARNING

!

No instrument, tubing or other device 

whatsoever shall circumvent the detonation 

flame arrestor in such a manner to allow a 

flame path to exist around the flame element 

of the arrestor. When instrumentation is 

installed in such a manner that it creates 

a path circumventing the flame element 

of an arrestor, measures must be taken 

to prevent passage of flame through the 

instrumentation device and/or system. 

Instrumentation must be capable of 

withstanding the maximum and minimum 

pressures and temperatures to which the 

device may be exposed and at a minimum 

be capable of withstanding a hydrostatic 

pressure test of 350 psig / 24 bar.

DFA Series detonation flame arrestors may be installed in 

any vapor control line that is smaller than or equal to the 

nominal pipe diameter of the arrestor’s connection flanges. 

When it is necessary to increase the diameter of the piping 

on the downstream side (unprotected) of the detonation 

flame arrestor, a length of pipe at least 120 pipe diameters 

must be installed between the detonation flame arrestor 

and the expansion. A pipe diameter is considered as the 

inside diameter of pipe having a nominal size equal to the 

detonation flame arrestor’s connecting flanges.

4

Model DFA 7236

North America 

Only

Summary of Contents for Enardo DFA 7236

Page 1: ... arrestor provides protection against flame propagation in piping systems that are manifolded or have long run up distances These are typically used for extended pipe length or multiple pipe bend configurations to stop high pressures and flame velocities with detonations and overdriven detonations It also stops confined and unconfined low and high pressure deflagration The design is unique in the ...

Page 2: ...e Arrestor Performance Gas Group WARNING Methanol is classified as a Group D IIA vapor However our lab tests indicate that methanol exhibits characteristics unlike other Group D IIA vapors under certain conditions We therefore recommend that an arrestor rated for Group C IIB3 vapors be specified for methanol service The type of gas in the system determines its gas grouping and therefore predetermi...

Page 3: ...ssure is the pressure of the system at or near static flow conditions High pressure deflagration and detonations can occur more easily at higher system operating pressures than at pressures near atmospheric Elevated pressures condense the ignitable gas giving the flame more matter and energy to release thereby boosting the flame heat intensity Unstable over driven detonations exist during a deflag...

Page 4: ...w located on the unit points in the direction travelling with the vapor flow Models that have drain plugs are designed for horizontal installation and should be installed with the drain ports aligned at the bottom of the unit Models that have pressure taps are designed to allow pressure gauges to be installed on both sides of the flame cell assembly to determine blockage The pressure taps should b...

Page 5: ...Figure 4 Lifting Diagram CENTER OF GRAVITY CENTER OF GRAVITY 5 Model DFA 7236 North America Only ...

Page 6: ...ssembly Following Flame Propagation Event 1 Inspect the outboard flame cells for damage immediately following a deflagration detonation and or stabilized burn 2 Carefully remove the element assembly from the arrestor with the entire flame arrestor out of the line 3 Inspect the flame cells and the screens visually for any signs of corrosion or other damage and inspect the flame cells with a calibra...

Page 7: ...le the nuts to the studs such that the amount of thread extending outboard beyond the nut is approximately equal on both ends 4 Tighten the nuts to the torque values shown in Table 1 following the designated sequence repeating the sequence as shown Flange pattern tightening sequences are shown in Figure 5 Bolt Lubrication Lubrication affects required torque of clean fasteners in good condition mor...

Page 8: ...sented for informational purposes only and while every effort has been made to ensure their accuracy they are not to be construed as warranties or guarantees express or implied regarding the products or services described herein or their use or applicability We reserve the right to modify or improve the designs or specifications of such products at any time without notice Emerson Process Managemen...

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