SUMMARY 
The Sulzer Chemtech MVGT
TM
 tray was tested at Fractionation Research Inc. (FRI) under the Category 1 
test program.  The results showed that the MVGT tray had the highest useful capacity of any tray tested at 
FRI in the Butane System 100 psia. 
 
 
This Topical Report presents the test results of the Sulzer Chemtech MVGT
TM 
tray.  The tray was tested 
in  the  4  ft  (1.22  m)  diameter  high  pressure  column  of  the  F.R.I.  distillation  unit  with  the  iso-
butane/normal-butane (iC4/nC4) system at 100 and 165 psia (6.9 and 11.4 bar).  The experimental results 
of  the  MVGT  tray  were  compared  to  those  of  the  standard  F.R.I.  Type  2  valve  tray
(1)
.  The  capacity, 
efficiency and the pressure drop were also compared to experimental results of the sieve tray tested by 
F.R.I. in 1987
(2)
, with 0.5 in (12.7 mm) hole diameter and similar percent hole area to the MVGT tray. 
  
For both pressures, the MVGT tray showed substantially higher capacity than the sieve tray and type 2 
valve tray. The efficiency of the MVGT tray was about 3 to 4 percent higher than the type 2 valve tray at 
low to medium vapor rates, but substantially higher at high vapor rates due to the higher capacity. At total 
reflux the pressure drop of the MVGT tray was significantly lower than both the sieve tray and type 2 
valve tray. 
 
The comparison of gamma scan results shows that the MVGT tray has less material entrained above the 
tray floor than the F.R.I. type 2 valve tray.  The MVGT tray has lower tray liquid holdup and downcomer 
backup than the type 2 valve tray. There is good agreement between the downcomer backups measured 
from the gamma scan and those from the bubblers, except at extreme conditions.  
 
 
INTRODUCTION 
 
This test was conducted as the 2001 Category 1, F.R.I. paid, proprietary tray test.  The MVGT tray was 
selected  under  the  tray  category.  The  test  was  conducted  under  the  proprietary  device  test  procedures 
amended at the May, 2001 TAC meeting
(3)
.   
 
The tray was tested for capacity, efficiency and pressure drop using the iC
4
/nC
4
 system at 100 and 165 
psia (6.9 and 11.4 bar) column pressures.  To measure the tray liquid holdup and the downcomer backup, 
the tray was gamma scanned and the results were compared to the measurements from bubblers installed 
inside downcomers. 
 
 
DESCRIPTION OF EQUIPMENT 
 
Trays 
 
 
The  Sulzer  Chemtech  MVGT  tray,  as  shown  in 
Figure  1,  is  a  fixed  valve  tray  with  a  truncated 
downcomer. The tray deck consisted of MVG (Mini V-Grid) valves to reduce the pressure drop of the 
tray deck and lower the froth height on the tray deck.  An inlet weir with directional baffles was installed 
on the inlet of the tray deck.    A sloped truncated downcomer was used in the MVGT tray to maximize 
the effective bubbling area.   The trays used in these tests were made of 304 stainless steel with a 0.0747 
in  (1.897  mm)  thickness.  The  downcomers  had  an  area  of  approximately  17.5%  of  the  column  cross 
sectional  area  at  top  and  10%  at  the  bottom.  The  bottom  plate  of  the  downcomer  was  5  in  (127  mm) 
above the tray deck.  A sweptback outlet weir with  2.36 in height (60 mm) was installed for each tray.  
The chord length at the downcomer was 39 in (991 mm).  The bubbling area of the tray was about 8.93 ft
2