Document Rawe7yObGDDGKBDV8Be15B2qB
ARBA Coot 218 3 6 0-1 008
CABLE AOBRESS-JETOiVilZER-LANSOALE
E I. DuPont 0 Nemours & Co. Copper Phthalocyanins Blue
Of f ic *!--300-302 W. Ma in St r e e t LANBOALE. PENNA. 19446
PLANTr-0OX A, 2620 PENN AVENUE HATFIELP, Pa . 18440
February 1, 196?
45$ Solids 20$ .Kerosene 35$ H2O
Our. analysis shows 56,8$ volatiles
wax. 0.5$' volatiles
The above material was test dried and milled in our model 0405F Jet-0Mizer using steam at 190 - 200 psig. The results of the test run are at follows*
FED #3637"1i
Manifold Pressure : 190 psig
Manifold Temp.
; 590F
Feed Rate
% 470#/hr.
Moisture
% 0.5$
Microscopically -
+5*4 , 5~2*i / 2-1*4 "1*4
Tr. 7 1-2$ 7 2-3$ 7 95-97$
Manifold Pressure 190 psig
Manifold Temp.
650 F
Feed Rat
765#/hr.
Moisture
0,3$
Microscopically -
15-lgu / lO-bjU. / 5-2*4 2-1*4 -iju
2-3$ 7 3-4$ 7 4-5$ 7 86-90$
needles
mjafiazs.a*
Manifold Pressure s 190 psig
Manifold Temp
: 650F
Feed Rat Moisture
j 203.80$#/hr,
Microscopically -
10-5/it / 5-2*4 / 2-4t / -1M tr*-l$ 7 1-2$ 7 3-5$ 7 92-96$
A repeat of run -3 was mad due to problems with the feeder. The rerun analysis is as follows:
N33712
WHEELER-STEPHANOFF FLUID ENERGY JET MULLS DUST COLLECTORS CUSTOM GRINDING
auiD m mmmrn m am
2Page
B. I. Qy&mt H Nwur & Co. tfUaiagten, Del; 19898
February X, 1967
'Mt
Manifold Pressure : 200 psig
Manifold Temp.
* 650F
Feed Eat*
i 31o#/hr*
!4oi $iii:wt
l 0,3%
y y ,Mlcc@pieally ~
4'5|i. 5-2*4. 2-Ip.
-1m
Tr. 7- 1-2% 7
7 95-97%
i ' \.i,
*Manifold pressure i 200 psig
Manifold Ttiap*.
i 660*F
Feed Hat#
* 900#/hr,
Moisture
* 1,3%
Mier&seopioally -
y 2-1m / * 1/j. Ir, 7 3 -2% 7 2 3/53 7 95-97%
The products, th balance of file raw feed, and two empty
steal drum:
returned to you vie North Penn Transfer
Co, an January .3 9=. 1967*
5 :
WST/ralc
CCi Juu9;3 VC foyy Jr,
Mr, d,
Sf.uber
>vy, s* ws; A* V'? * * -i Plant Manager
2
DUP050027641