1. No category

D ie fle x ib le n V e r te ile r s y s te m e a u s K u n s ts to ff fü r S a n itä r u n d H e iz u n g
2 0 1 4 /0 0 1
-U n iv e r s a lv e r te ile r 5 0 0 0 K S T 1 ¼ ”
E n d p la tte w a h lw e is e :
-o h n e B o h ru n g
-m it ½ ” IG
-¾ ” IG
-1 ” IG
8 2
1 6 0
v o n W P
2 0 0
w a h lw e is e
IG 1 ¼ ” o d e r IG 1 ½ ”
z u W P
w a h lw e is e
IG 1 ¼ ” o d e r IG 1 ½ ”
IG
7 3
1 "
9 0
1 0 0
G e s a m tlä n g e L
2 9 2
A n z a h l d e r A b g ä n g e
2
3
4
5
6
7
8
9
1 0
G e s a m tlä n g e L (m m )
2 6 3
3 6 3
4 6 3
5 6 3
6 6 3
7 6 3
8 6 3
9 6 3
1 0 6 3
L ä n g e d e r G e w in d e s ta n g e n (m m )
2 3 0
3 3 0
4 3 0
5 3 0
6 3 0
7 3 5
8 3 5
9 3 5
1 0 3 5
-U n iv e r s a lv e r te ile r 5 0 0 0 K S T 1 ¼ ” - D u r c h flu s s k e n n lin ie
M e s s s tre c k e :
Z u la u f = G 1 ½ ” , A b la u f = G 1 ½ ” ,
V e r b in d u n g z w is c h e n V o r la u f- u n d
R ü c k la u fv e r te ile r : g e r a d e R o h r s tü c k e G 1 ” ,
c a . 1 0 0 m m la n g
0 8 -fa c h
0 2 -fa c h
1 0 .0 0 0
V e n tile im V o r la u f u n d D u r c h flu s s m e s s e r im
R ü c k la u f m a x . g e ö ffn e t
(l/h )
D u r c h flu s s Q
m a x
= 1 3 .9 5 0 l/h b e i d p = 1 b a r
5 .0 0 0
A n z a h l V e r te ile r k r e is e
W a s s e r 1 8 °C
D u r c h flu s s Q
M e d iu m
0 1 -fa c h
1 .0 0 0
5 0 0
0 ,0 1
S ie g fr ie d B ö h n is c h
K u n s ts to ffte c h n ik G m b H
M a y b a c h s tra ß e 1
D -7 4 6 3 2 N e u e n s te in
0 ,1
D r u c k v e r lu s t d p (b a r )
T e le fo n : + 4 9 ( 0 ) 7 9 4 2 - 9 4 4 9 2 6 0
T e le fa x : + 4 9 ( 0 ) 7 9 4 2 - 9 4 4 9 2 6 9 9
1 ,0
in fo @ s b k - n e u e n s te in .d e
w w w . s b k - n e u e n s t e in . d e
S e ite 1 7