LIQUID FUEL PRODUCTION AT THE BOEHLEN PLANT

• Document Type: CREST
• Collection: General CIA Records
• Document Number (FOIA) /ESDN (CREST): CIA-RDP80-00810A002800550006-8
• Release Decision: RIPPUB
• Original Classification: S
• Document Page Count: 4
• Document Creation Date: December 27, 2016
• Document Release Date: June 6, 2013
• Sequence Number: 6
• Publication Date: February 10, 1954
• Content Type: REPORT

CLASSIFICATION SEC,:iT
Declassified in Part - Sanitized Copy Approved for Release 2013/06/06: CIA-RDP80-00810A002800550006-8
WELLOFAX 28 L.1-11.1L.M.4.-..Pli...1C.1`41/4/ I VALCV11
INFOR TPON RPORT? CD NO.
COUNTRY
SUBJECT
PLACE
ACQUIRED
DATE OF
INFO.
East Germany
DATE DISTR. 10 February 1954
Liquid Fuel Production at the Boehlen Plant N 50X1 -HUMO. OF PAGES it
V.M.7-4;7106M-01.?:ti
1141$ OCCOLIEEIRCOOTAMS ttiVORRATION RPercanno TU RATIORAL.OEVERSM
ft or no um= STATER. raram rut Immo or mut U. SECTIORS
ROD V94. Or TRR O. S. CORR. AS ARWOOD. TINzs1ofl OR RRVRL-
AT= or VTR COZ1EXIT3 TO OR eas'7.1301 t.Oit413TRORTTSR PRREOR
PROMITEIT BY If& TREI RGPRODUCTIOR OP MS VOW IS PROIROITED.
c.
NO. OF ENCLS.
(LISTED BELOW)
SUPPLEMENT TO .
REPORT NO.
THIS IS UNEVALUATED INFORMATION
t. . The fcliowine abie indicates the fulfillment of quality n.ms
for products fabricated in VIM Oti;o Grotewohl Boehlen during
the second c:uartor of 1955. The cuality. norm is listed together
with the measurement unit used for it and the actual value
. attdined, The table contains exz-sct technical ata on some of the
most lui.dortant items jroduced in the enter,2rise.
FulX111111E1.9.g..alaal-V?ZEMP.t
IZezis4rement c.uality Actual
No. Item Unit ? Norm ? Value.
1. Raw Goal .
Water content `X )., rz;
54.1
e.
Ashes I- 5,5 to 6.5 57
Combustible content (.; 38..,0 to 40.5 .1J02
(-'?7.0 to 8.0 E33
Tar P
e
Volatile sulfur /- 07 to 0.9 1,00
Heating value
kca.
2200, to
2,300
2,409
21 Dlaillallalint22A
?15 3 15 9
;iater content
.,
Ashes
Combustible content
Tar
Pressure resista.ace
Heatink value
Lair
ARMY
CLASSIFICATION .STIeRET
NAVY 1NSRS I CHSTRffiliTION
MP JJJ
?
10,0 to 12,0 10,8
? 740 to 76.0 73.3
14a0 to 15.0 15.2
kg per sq cm 50 to 75 42
kcal 4O00 to
5,000
4i860
50X1 -HUM
?
50X1 -HUM
im Declassified in Part - Sanitized Copy Approved for Release 2013/06/06: CIA-RDP80-00810A002800550006-8
Declassified in Part - Sanitized Copy Approved for Release 2013/06/06: CIA-RDP80-00810A002800556066:8"
A
Water content
Ashes
Combustible content
Pressure resistance
Heating value
4. Distillation coke
Water content
5?
Ashes
Tar
Combustible content
Heating value
Li5nite distillation tar
Specific gra4ITirep.gro)
at 50 centigrades
later content
Solidification temperature
Percentage boiling at 320c0
centigrade
Li,.;ht distillation oil .
Lpogro at 200 centigrade
Flash point
Percentage up to 100?
centigrade
Percentage up to 150?
centigalo
7? Plajlas
Maximum heating valve
Density
02 not exceeding
a. Phenolate lye
w acid-
1 8
16.6
11
.10.7
72.5 to 75.0
72.7.
kg .c,e1-
sq, cm
70 to CO
kcal
4,700 to
4,830
4 845
2.1
22.0 to 240
24.1
"1.0
1.0
kcal
73.0 to 7600
5,900 to
6,100
. 0.930 to-
tons.?per cubic, --_
aster
1.0 -.
degrees
centigrade. 35 to 35
26 to 30
tons per cu.
met or
0.835 to
.00850
6,035
00943
0,66
7.J.Z..
0.858
? degrees .
oonticie 6 to 7 0
0 to -5.0 24
32,0 to 40.0 26.6
LC,:a 4,250 tO
? 450
? of
SECRET
A ..A/A0
0.45 to 0.50 0.475
0.3 0.2
22.0 to 25.0 23.82
.
,
LDeclassified in Part - Sanitized Copy Approved for Release 2013/06/06: CIA-RDP80-00810A002800550006-8
Declassified in Part - Sanitized Copy Approved for Release 2913/06/06 : CIA-RDP80-00810A0028666-50006:8
SECT
uto b9nzine (without lead
addition).
5i,tot. at 15(4centigrades
Boiling sterte
Boiling ende,
tons per s4.
meter.
?degrees
centigraUe
degrees
cenuigrude:,; 205
Steam pressure mrn H (380
centigrade ) '500
Octane. number - --
10. Sceciel Benzine 0
Spogro, tons per cu.
meter 0,740.
degrees ?
Boiling startz, contlgrade 46 46 '
degrees
-13eil.i., ends centigrade 180. ? 163
Steam 7)rossure mm, lig (380
centigrade.)
11.
327 ,
58.4
563
Octane number 95
LT Benzine
Spoor.?
-Boilina start
Boiling ends
-3team pressure
338
96.5
tons per cu.
meter 0.692
degrees
eentirsde 4L 44.
degrees
centicrde , 180 179.
mm. Hg (300
centigrade 360
Oetne number 91
mittel Benzine-
Boiling start
BosLt.n' end
flas1[.. point
Solidifying point ?
Visen_sity at 20/ centigrade.
'2esin test
341
92.3
tons per Cu
meter = 0,800. to
0.850 . .0.810
degrees
centigrade ? .150 147
centigrv.de- 280 243
degrees
centigrade . plus 30 plus 3405.
degrees
centigrade minus 56 ' minus 61.5_
?
contistokes 1 5
mg per 100
cuo cm
sEc
Declassified in Part - Sanitized Copy Approved for Release 2013/06/06: CIA-RDP80-00810A002800550006-8
Declassified in Part - Sanitized Copy Approved for Release 2013/06/06: CIA-RDP80-00810A002800550006-8
SECRET
G. 0
4
15. Diesel .Fuel
Spgr tons per cu-.
meter 0.837
degrees
Boiling starts ? centigrade 3,83
degrees ?
Boiling ends centigrade. 330 317
degrees
Flesh 7;oint centigrade plus 61
degrees
Solidifying point centigrade minus 15 minus 21
14. Prooane
C3
Organic sulfur
15?. Iso-octane 224
Octane -number
Spogro
Refractive index
Boiling point
mg per cu
, meter
95 , ? 96.7 ,
250
2300
100 100.0
tons per cu. 0.6018 to
meter 0.6923 .
1.3914 to
degrees 1.3915
centigrade 99.1 to 99,5
0,69185
1.3915
99.16
_achstoff S
Oc number 99 99.6
(gr
'Refractive index
? Boiling point,
tons per. cu.
meter 0.6835 to
0.6923
degrees
ceptir:rade
105915 to
' 1.3922
' 0.6919
1.3915
50X1 -HUM
98,4 to 100,0 98.62 50X1 -HUM
comments on some of the items listed above:
a. Items 2. and 3: Fulfillment of the quality, norms is not possible for
the briquette factory? if the high production plan is to be fulfilled.
b. -tem ?4: The increase in the ash content is caused by the low quality
of the briquette.
C. Item 6. The decreese of the ?light parts in light oil is to be
considered as a result ofinsifficient distillation capacity.
im Declassified in Part - Sanitized Copy Approved for Release 2013/06/06: CIA-RDP80-00810A002800550006-8