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GEA vent terminals, are designed to ensure good safe dispersion of venting gases whilst ensuring minimal water and material ingress.

 The stainless steel SVT model comes in ½” bsp, 1” bsp (also for use on 1 ½” lines), 2” bsp and 3” flanged sizes and is suitable for terminal pressures up to 20 bar.

The smaller SVT15 vent terminal has been designed to meet National Grid E28 and IGEM/GM/8 Part 1 Breathers requirements. This is of stainless steel construction and the flow rate can be adjusted to meet flow rates of 2.5, 10 or 15 m3/h by changing the internal jet bore. It is available with a ½" bsp threaded connection.

The SVT15 terminal has been tested by one of UK's larger gas suppliers and confirmed to be ideally suitable for Medium Pressure domestic type meter installations. The limitation of vent flows with the SVT15 assists in reducing emissions and any hazardous area as required by IGEM/SR/25 and DSEAR.

 

 

 
                    TECHNICAL DATA FOR GEA VENT TERMINALS

 

 

 

 

 

 

 

 

              

SVT 50v1.JPGCIMG0589.JPGsmall vent terminal v3.jpg

 

 

 

 

 

 

 STV 50                                                           STV 25                                                              STV 15

 

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Model

Flow Rate

m3/h

Cross wind condition

Vertical distance    m

Horizontal  radius      m 

Downwash radius       m

XH

XR

XK

50% LEL

100 % LEL

50% LEL

100 % LEL

 

SVT 15

2.5

2 m/s

NA

NA

NA

NA

0.75

5 m/s

0.6

0.4

1

NA

SVT 25

10

2 m/s

2

0.18

0.16

0.11

1.00

5 m/s

0.16

0.11

4

2.4

SVT 50

15

2 m/s

0.31

0.22

2.2

1.3

3.00

5 m/s

2.2

1.3

4.4

2.6

 

 

 

 

 

 

 

Predicted Zoning areas for GEA Terminals ( For guidance only)

 

VT 15 conforms to “ideal” venting parameters and therefore cross wind conditions are

only quoted for the worst condition.

The flow rates are those achieved under low pressure flow conditions. At higher pressures

where higher pressure drops may be acceptable, a smaller terminal will provide better dispersion.

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

 

Downwash Considerations.

 

Vent pipe terminations are subject to some downward dispersion.

 

For momentum-driven dispersion,

Downward dispersion exists only when the duration of venting duration exceeds 1 minute

XL   =  1 m or 0.2 hs (m) whichever is the greater

hs   =  height of vent tip above ground level (m)

 

XL should not exceed Xr

 

Wind-driven dispersion

This may occur at start-up and shut-down where the radial dispersion distance is represented by Xk

 

Xk should not exceed Xr

 

The downward dispersion distance is  is the smaller of

XL + 3d (m), where d = nominal diameter of vent (m).

                    Or XK

Addition downwash due to nearby structures

Vent pipe terminations which are located close to a structure may be subject to additional downward

dispersion due to downwash. 

 

The criteria determining whether or not downwash exists is:

 

D < X, or D < 10 m, whichever is the smaller.

 

D    =    distance from the vent to a structure (m)

Xr    =    horizontal radius of the momentum-driven hazardous area (m).

 

Additional downward dispersion should be of extent (radius) Xk  and a height = 0.25Xk.

                   

(XL + 3d + 0.25 Xk) should not exceed Xk  as given in Table 12 of SR/25..