1
Equipment Leading Spec
1.1
Emergency Shutdown Valve for Fuel Gas
Description
Unit
Minimum Value
Maximum Value
Design Value
Quantity
2)
Type
3)
Type of Actuator
4)
Location
5)
Line Size (inlet / outlet)
6)
Volumetric Flowrate of ESDV
m3/h
56.0
6,686.0
6,686.0
7)
Mass Flowrate of ESDV
kg/s
0.630
47.141
51.250
8)
ESDV Suction Pressure
barg
39.30
52.40
60.70
Double Block and Bleed, Full Bore, Ball Valve, Fire Safe with SIL3 Certificate
include equalizing valve
Pneumatic, Self media, Fail Close
Outdoor (Sunshade should supplied)
Not in Shelter
DN400 / DN400
DN
9)
ESDV Discharge Pressure
barg
39.10
52.40
60.70
10)
ESDV Suction Temperature
degC
37.222
54.444
60.000
11)
Closing time (Open to Close)
sec
5 sec (Max)
12)
Maximum Pressure Drop
bar
0.10
13)
Corrosion allowance
mm
14)
Explosion protection
15)
Material
1.2
Remark
Two (1) x 100% (with local push button)
1)
per Each
Hydro.Test 150% of
Design Pressure
1.5
Zone II
Refer to ITB requirement
ASTM A216 WCB / A105N
Coalescing Filter Separator
Description
Unit
Minimum Value
Maximum Value
Design Value
Quantity
2)
Type
3)
Location
4)
Line sizing (inlet / outlet)
5)
Volumetric Flowrate of Filter Separator
m3/h
56.0
6,686.0
6,686.0
6)
Mass Flowrate of Filter Separator
kg/s
0.630
47.141
51.250
7)
Filter Separator Suction Pressure
barg
39.10
52.40
60.70
8)
Filter Separator Discharge Pressure
barg
38.20
52.40
60.70
9)
Filter Separator Suction Temperature
degC
37.222
54.444
60.000
10)
Removal efficiency
Vertical Solid and Liquid Particle separator, Two Stage design
(1st stage with inertial separators, 2nd stage consisting of coalescing filters)
Outdoor
DN400 / DN400
DN
a) Dust Removal efficiency
%
99.99% > 0.3 microns
b) Droplets Removal efficiency
%
99.99% > 0.3 microns
11)
Maximum Pressure Drop
bar
12)
Corrosion allowance
mm
13)
Explosion protection
14)
Material
Hydro.Test 150% of
Design Pressure
0.70
Valve, piping, fitting: 1.5
Vessels: 2.5
Zone II
a) Shell
ASTM A106Gr B or eq.
b) Cover
ASTM A105 or eq.
ASTM A105 or eq.
c) Inlet / Outlet Flange
Fiber and Stainless or CS
d) Filter element
1.3
Remark
Two(2) x 100%
1)
Fuel Gas Pressure Reducing Station
Description
Unit
Minimum Value
Maximum Value
Design Value
Quantity
2)
No of PRVs per stream
3)
PRV Type
4)
Location
5)
Line sizing (inlet / outlet)
6)
Volumetric Flowrate of PRVS
m3/h
134.0
2314.0
7)
Mass Flowrate of PRVS
kg/s
1.50
15.71
17.08
8)
PRVS Suction Pressure
barg
37.77
52.40
60.70
One(1) PRV + One(1) Full Capacity PSV
Set
Self acting pilot operator.
Outdoor
DN200 / DN250
DN
2314.0
9)
PRVS Discharge Pressure
barg
32.700
32.700
36.000
10)
PRVS Suction Temperature
degC
37.222
54.444
60.000
11) PRVS Discharge Temperature
12) Pressure Drop at PRV wide open
13)
14)
Remark
Four(4) x 33.3%
1)
Noise emission
Corrosion allowance
degC
by supplier
bar
0.7
dBA
<85
mm
Hydro.Test 150% of
Design Pressure
Valve, piping, fitting: 1.5
Vessels: 2.5
15)
Explosion protection
Zone II
16)
Material (Valve Body)
A216 WCB or eq.
Refer to ITB requirement
1.4
Start-up Fuel Gas Pressure Reducing Station
Description
Unit
Minimum Value
Maximum Value
Design Value
Quantity
2)
No of PRVs per stream
3)
PRV Type
4)
Location
5)
Line sizing (inlet / outlet)
6)
Volumetric Flowrate of PRVS
m3/h
18.0
57.0
7)
Mass Flowrate of PRVS
kg/s
0.20
0.63
2.00
8)
PRVS Suction Pressure
barg
37.77
52.40
60.70
One(1) PRV + One(1) Full Capacity PSV
Set
Self acting pilot operator.
Outdoor
DN200 / DN250
DN
178.0
9)
PRVS Discharge Pressure
barg
32.700
32.700
36.000
10)
PRVS Suction Temperature
degC
37.222
54.444
60.000
11) PRVS Discharge Temperature
12) Pressure Drop at PRV wide open
13)
Noise emission
14)
Corrosion allowance
Hydro.Test 150% of
Design Pressure
by supplier
degC
bar
0.7
dBA
<85
Valve, piping, fitting: 1.5
mm
Vessels: 2.5
15)
Explosion protection
Zone II
16)
Material (Valve Body)
A216 WCB or eq.
1.5
Remark
Four(4) x 33.3%
1)
Refer to ITB requirement
Aux. Fuel Gas Pressure Reducing Station
Description
Unit
Minimum Value
Maximum Value
Design Value
Quantity
2)
No of PRVs per stream
3)
PRV Type
4)
Location
5)
Line sizing (inlet / outlet)
6)
Volumetric Flowrate of PRVS
m3/h
87.0
1781.0
7)
Mass Flowrate of PRVS
kg/s
0.63
5.05
5.60
8)
PRVS Suction Pressure
barg
32.30
32.70
32.70
9)
PRVS Discharge Pressure
barg
15.000
15.000
15.000
degC
15.000
54.444
60.000
10)
Outdoor
PRVS Suction Temperature
12) Pressure Drop at PRV wide open
Noise emission
14)
One(1) PRV + One(1) Full Capacity PSV
Set
Self acting pilot operator.
11) PRVS Discharge Temperature
13)
Corrosion allowance
DN200 / DN250
DN
1960.0
Hydro.Test 150% of
Design Pressure
by supplier
degC
bar
0.7
dBA
<85
Valve, piping, fitting: 1.5
mm
Vessels: 2.5
15)
Explosion protection
Zone II
16)
Material (Valve Body)
A216 WCB or eq.
1.6
Remark
Four(4) x 33.3%
1)
Fuel Gas Condensate Drain Tank
Description
Unit
Minimum Value
Maximum Value
Design Value
Remark
One(1) x 100%
1)
Quantity
2)
Type
3)
Location
4)
Operating Pressure
barg
1
5)
Operating Temperature
degC
28.2~ 135
6)
Size (W x L x H or OD x L)
m3/h
3.5
Set
Horizontal
Outdoor
Hydro.Test 130% of
Design Pressure