MS and MD Information

MD, MS Manual Man ifold Sys tems
M anualm anifolds are designed to regulate
com pressed gases in high pressure cylinders
(up to 3,000 psig)and are idealform anifold
applications not requiring autom atic changeover
from the service to the secondary bank.The M D
Series duplex m anifold is designed form anual
changeoverof2 banks ofcylinders.The M S
series sim plex m anifold system allow s m anifolding
ofan unlim ited num berofcylinders in a single
bank.This system is often used as a high
pressure reserve forbulk,portable bulk and
gas generatorsystem s.
specifications
MD,MS s e r i e s
tManual Systems
tMaximum w orking pressure: 3 0 0 0 psig
tManifold O utlet:1/2 ” N PT male
t2 4 ” flexible stainless steel braided pigtails w ith check valves.
C heck valve is at header end of pigtail for all gases except
O xygen. N ote: H elium and H ydrogen manifolds shipped w ith
synthetic fiber braided pigtails
M D – 4– 4
Ex am ple: M D–4–4 = C O 2 (4=C G A–320)
M anifold for4 C ylinders
tIndividual header valves at each cylinder location (units w ith 4
cylinders or larger-all gases except O xygen)
tH eaders constructed of 1/2 ” brass pipe and tees
tA cetylene manifolds shipped complete w ith dry flashback
arrestor, relief valve and connecting piping. H ydraulic Flashback
arrestors are available as an option for an additional charge
M S– 9– 4
tO ptional safety kits, flash arrestor and relief valve available for
Liquefied Fuel gases
Ex am ple: M S–9–4 = O xygen (9=C G A–540)
M anifold for4 cylinders
tH eater Kits available for C arbon D ioxide and
N itrous O xide gases
tModel RM regulator included for most gas services.
Note: RD M Series used for O xygen
tA n alarm can be added to non fuel gas MD systems to signal
changeover from service to reserve banks by adding items
W ME-4 -9 pressure sw itch,W MS-1 -9 7 adaptor, W MS-9 -2 5 C
pow er source and BIA -3 remote A / V alarm.
HO W
TO O R DER
Specify: Control Type (V)–Service (W)–Number of Cy
Exam ple 1:MD –9–12V represents MD w ith oxygen gas service and a vert
Exam ple 2:MSH P–7–6 represents MSH P w ith nitrogen gas service w ith a st
C O N TRO L TYPE (V)
G A S SERVIC E (W )
MD / MS
Most gases: 2 0 –16 0 psig
A cetylene: (0 –15 psig)
LPG : (0 –4 5 psig)
(1 )
(1 A )
(2 )
(3 )
(4 )
(5 )
(6 )
(6 A )
(7 )
(7 A )
(8 )
(9 )
(1 0 )
MD H P / MSH P
(only available for non–fuel
gas services)
Most gases:14 0 –3 0 0 psig
O xygen:14 0 –4 5 0 psig
A cetylene (PO L)
A cetylene (C ommercial)
C ompressed A ir
A rgon
C arbon D ioxide
H elium
H ydrogen
A rgon/ Methane Mixtures
N itrogen
Industrial A ir/ N itrogen O P
N itrous O xide
O xygen
Liquefied Fuel G ases (LPG )
# O F C YL’S (X)
CG
CG
CG
CG
CG
CG
CG
CG
CG
CG
CG
CG
CG
A –5 1 0
A –3 0 0
A –3 4 6
A –5 8 0
A –3 2 0
A –5 8 0
A –3 5 0
A –3 5 0
A –5 8 0
A –5 9 0
A –3 2 6
A –5 4 0
A –5 1 0
N ote: Different regulators m ay be substituted to achieve
higherdelivery pressures on allcontroltypes.
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For m ore inform ation, callW estern C ustom er Service at1-800 -783 -7890
D es ig n Len g t h s
TO TA L N O . O F C Y LIN DE R S
2
3
4
5
6
7
8
MS-Standard (1 0 ” C enters)
O verall Manifold Length
2 ’–9 ”
(.8 4 m)
3 ’–7 ”
(1 .0 9 m)
4 ’–5 ”
(1 .3 5 m)
5 ’–3 ”
(1 .6 0 m)
6 ’–1 ”
(1 .8 5 m)
7 ’–0 ”
(2 .1 3 m)
7 ’–1 0 ”
(2 .3 9 m)
MS-Staggered D esign (5 ” C enters)
O verall Manifold Length
2 ’–4 ”
(.7 4 m)
2 ’–9 ”
(.8 4 m)
3 ’–2 ”
(.9 7 m)
3 ’–7 ”
(1 .0 9 m)
4 ’–0 ”
(1 .2 2 m)
4 ’–5 ”
(1 .3 5 m)
4 ’–1 0 ”
(1 .4 7 m)
MS-Vertical C rossover and C rossover
(1 0 ” C enters)O verall Manifold Length
1 ’–1 1 ”
(.5 8 m)
N /A
2 ’–9 ”
(.8 4 m)
N /A
3 ’–7 ”
(1 .0 9 m)
N /A
4 ’–5
(1 .3 5 m)
MS-Standard (1 3 ” C enters)
O verall Manifold Length
3 ’–0 ”
(.9 1 m)
4 ’–1 ”
(1 .2 2 m)
5 ’–2 ”
(1 .5 7 m)
6 ’–3 ”
(1 .9 1 m)
7 ’–4 ”
(2 .2 4 m)
8 ’–5 ”
(2 .5 7 m)
9 ’–6 ”
(2 .9 0 m)
MS-Staggered D esign (6 .5 ” C enters)
O verall Manifold Length
2 ’–5 .5 ”
(.7 5 m)
3 ’–0 ”
(.9 1 m)
3 ’–6 .5 ”
(1 .0 8 m)
4 ’–1 ”
(1 .2 5 m)
4 ’–7 .5 ”
(1 .4 1 m)
5 ’–2 ”
(1 .5 7 m)
5 ’–8 .5 ”
(1 .7 4 m)
MS-Vertical C rossover and C rossover
(1 3 ” C enters) O verall Manifold Length
1 ’–1 1 ”
(.5 8 m)
N /A
3 ’–0 ”
(.9 1 m)
N /A
4 ’–1 ”
(1 .2 5 m)
N /A
5 ’–2 ”
(1 .5 7 m)
2
4
6
8
12
14
MD -Standard (1 0 ” C enters)
O verall Manifold Length
2 ’–4 ”
(.7 1 m)
4 ’–4 ”
(1 .3 2 m)
6 ’–0 ”
(1 .8 3 m)
7 ’–8 ”
(2 .3 4 m)
9 ’–4 ”
(2 .8 5 m)
1 1 ’–0 ”
(3 .3 5 m)
1 2 ’–8 ”
(3 .8 6 m)
MD -Staggered D esign (5 ” C enters)
O verall Manifold Length
2 ’–4 ”
(.7 1 m)
3 ’–6 ”
(1 .0 7 m)
4 ’–4 ”
(1 .3 2 m)
5 ’–2 ”
(1 .5 7 m)
6 ’–0 ”
(1 .8 3 m)
6 ’–1 0 ”
(2 .0 8 m)
7 ’–8 ”
(2 .3 4 m)
N /A
2 ’–8 ”
(.8 1 m)
N /A
4 ’–4 ”
(1 .3 2 m)
N /A
6 ’–0 ”
(1 .8 3 m)
N /A
MD -Standard (1 3 ” C enters)
O verall Manifold Length
2 ’–4 ”
(.7 1 m)
4 ’–9 ”
(1 .4 7 1 m)
7 ’–0 ”
(2 .1 3 m)
9 ’–2 ”
(2 .7 9 m)
1 1 ’–4 ”
(3 .4 5 m)
1 3 ’–6 ”
(4 .1 1 m)
1 5 ’–8 ”
(4 .7 7 m)
MD -Staggered D esign (6 .5 ” C enters)
O verall Manifold Length
2 ’–4 ”
(.7 1 m)
3 ’–9 ”
(1 .1 4 m)
4 ’–1 0 ”
(1 .4 7 m)
5 ’–1 1 ”
(1 .8 0 m)
7 ’–0 ”
(2 .1 3 m)
8 ’–1 ”
(2 .4 6 m)
9 ’–2 ”
(2 .7 9 m)
N /A
2 ’–8 ”
(.8 1 m)
N /A
4 ’–1 0 ”
(1 .4 7 m)
N /A
7 ’–0 ”
(2 .1 3 m)
N /A
TO TA L N O . O F C Y LIN DE R
MD -Vertical C rossover and C rossover
(1 0 ” C enters)O verall Manifold Length
MD -Vertical C rossover and C rossover
(1 3 ” C enters) O verall Manifold Length
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ylinders (X)–Header Configuration (Y)–Mounting (Z)
rticalcrossover bank of 6 cylinders per side w hich is m ounted on the w all.
standard header configuration of 6 cylinders w hich is m ounted on the w all.
H EA D ER C O N FIG U RATIO N (Y)
MO U N TIN G (Z)
B LA NK –Standard 10” on C enter
13 ” on C enter for A cetylene & LPG
S–Staggered 5 ” on C enter
6 .5 ” on C enter for A cetylene & LPG
V–Vertical C rossover
1 0 ” on C enter or 1 3 ” on C enter for
A cetylene & LPG
C–C rossover (Floor Mount O nly)
1 0 ” on C enter or 1 3 ” on C enter for
A cetylene & LPG
B LA NK = W all mount
F = Floor mounted
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