United States
Environmental Protection
Agency
EPA-600/R-93-080b
May 1993
<&ER<\ Research and
Development
KRESS INDIRECT DRY COOLING
SYSTEM. BETHLEHEM STEEL'S
COKE PI.ANT DEMONSTRATION AT
SPARROWS POINT, MARYLAND
Volume 2. Appendices ON
Prepared for
Office of Environmental Engineering
and Technology Demonstration
Prepared by
Air and Energy Engineering Research
Laboratory
Research Triangle Park NC 27711

-------
EPA REVIEW NOTICE
This report has been reviewed by the U.S. Environmental Protection Agency, and
approved for publication. Approval does not signify that the contents necessarily
reflect the views and policy of the Agency, nor does mention of trade names or
commercial products constitute endorsement or recommendation for use.
This document is available to the public through the National Technical Informa-
tion Service. Springfield, Virginia 22161.

-------
TECHNICAL REPOHT DATA
	 	. (Please read Inurstctions on the reverse before compleir'%
	
¦ . REPORT NO.
EPA-600/R-93-080b
¦>
a i pb93
-19*310
)
4. TITLE ANC SUBTITLE
Kress Indirect Dry Cooling System, Bethlehem Steel's
S. REPORT DATE
May 1993
Coke Plant Demonstration at Sparrows Point,
Maryland
o. rcnronMiNG organization code
7. AUTHOFHSI
A. George Cssinan
8. PERFORMING ORGANIZATION REPORT NO.
9. PERFORMING OROANIZATION NAME AND ADDRESS
Bethlehem Steel Corporation
Bethlehem, Pennsylvania 18016-7699
10.	PROGRAM bLEMENT NO.
11.	CON TflACI/GHANT NO.
68-DC-0128
12. SPONSORING AGENCY NAME AND ADDRESS
EPA, Office of Research and Development
Air and Energy Engineering Research Laboratory
Research Triangle Park, NC 27711
13. TYPE OF REPORT AND PERIOD COVERED
Final; 2/90 - 2/92
14. SPONSORING ACFNCY OODE
EPA/600/13
is.supplementary notes project officer is Chester A. Vogel. Mail Drop 61, 919/
541-2827. Volume 1'consists of the Technical Report and Appendices_A-F.
i«. abstract The report evaluates the Kress Indirect Dry Cooling (KIDC) process, an
innovative system for handling and cooling coke produced from a slot-type by-product
coke oven battery. The report is based on the test work and demonstration of the sys-
tem at Bethlehem Steel Corporation's Sparrows Point (Maryland) facility in 1991. The
report covers both environmental and operational impacts of the KIDC process.
Areas covered in the report include opacity levels, quenching emissions, and the im-
pact of the KIDC coke on blast furnace operations. Also evaluated were various per-
formance characteristics of the KIDC system, including reliability, cycle time, coke
cooling requirements, and costs. Unfortunately, abbreviation of the test program,
caused by the idling of coke production at Sparrows Point, limited the experience
gained and data collected during the demonstration. The report data have not been
thoroughly audited, and the conclusions are neither approved nor endorsed by EPA.
Because of the sudden termination of the project and the associated quality assurance
effort, it was not possible to perform the detailed laboratory and data audits that had
been planned.
17.
KEY WORDS AND DOCUMENT ANALYSIS


a. DESCRIPTORS
b. IDENTIH ERS/OPEN ENDED TERMS
c. COSATI Field/Gioup
Pollution
Coke
Coking
Blast Furnaces
Pollution Control
Stationary Sources
Kress Indirect Dry Cool-
ing (KIDC) Process
13 B
21D
13H
11F
18. DISTRIBUTION STATEMENT

19. SECURITY CLASS (ThisRrport)
Unclassified
71. NO OF PAGFS
346
Release to Public

20. SECURITY CLASS (This page)
Unclassified
22. PRICE
CPA form 2220*1 <9»/3)

-------
Kl'A-600/R-93-080b
May 1993
KRESS INDIRECT DRY COOLING SYSTEM,
BETHLEHEM STEEL'S COKE PLANT DEMONSTRATION
AT
SPARROWS POINT, MARYLAND
Volume 2. Appendices G-N
By:
A. George Ossman
Bethlehem Steel Corporation
Bethlehem, PA 18016-7699
EPA Contract No. 68-DO-0128
Project Officer: Chester A. Vogel
U.S. Environmental Protection Agency
Air and Energy Engineering Research Laboratory
Research Triangle Park, NC 27711
Prepared For:
U.S. Environmental Protection Agency
Office of Research and Development
Washington, DC 20460

-------
ABSTRACT
&This report provides an evaluation of the Kress Indirect Dry Cooling (KIDC) process. The
KIDC process is an innovative system for the handling and cooling of coke produced from a slot
type by-product coke oven battery. The report is based on the test work and demonstration of
the system at Bethlehem Steel Corporation's Sparrows Point facility in 1991. The report covers
both environmental and operational impacts of the KIDC process.^Areas covered in the report
include opacity levels, quenching emissions, and the Impact of the klDC coke on blast furnace
operations. Also evaluated were various performance characteristics of the KIDC system.
These included reliability, cycle time, coke cooling requirements, and costs. Unfortunately, the
shortened duration of the test program as a result of the idling of coke production at Sparrows
Point limited the experience and data collected during the demonstration.
DISCLAIMER
The data presented in this report have not been thoroughly audited and the conclusions are not
approved or endorsed by the Agency. Because of the sudden termination of the project and the
associated Quality Assurance effort, it was not possible to perform the detailed laboratory and
data audits that had been planned.

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APPENDICES
Page
A.	Visible Emission Observation Data and Summary Tables -	A-1 *
Pushing Emissions
B.	Visible Emission Observation Data and Summary Tables -	B-1'
Pushside, Topside, and Discharge and Handling Emissions
C.	Keystone Consulting Engineers Report on KIDC Box Gas Sampling	C-1 *
D.	Area Monitoring Data Sheets and Analytical Results	D-1'
E.	Quench Tower Emissions and Water Analysis	E-1 *
F.	Kress Bulletin and Photographs of the KIDC Operation	F-1*
G.	Coke Quality Data	G-1
H.	Blast Furnace Balwax Model Report	H-1
I.	Report of KIDC Operating Costs and Maintenance Requirements	1-1
J. Kress Box Thickness Readings	J-1
K. KIDC Coke Discharge Temperature	K-1
L QA/QC Program	L-1
M. Door Leak Data	M-1
N. Coal Data	N-1
'In Volume 1

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Appendix G
Coke Quality Data- Summary Tables and Graphs
Table of Contents
Section	Page
1	Comparison Graphs of Coke Properties - KIDC vs.	G-2
Conventional Coke.
2	Graphs of KIDC Coke Properties.	G-14
3	Graphs of Conventionally Quenched Coke Properties.	G-22
4	Monthly Average & Standard Deviation Graphs of	G-29
Conventionally Quenched Coke Properties.
5	Conventionally Quenched Coke Properties Database.	G-40
6	KIDC Coke Properties Database.	G-62
7	Consolidation Coal Company Report of Coke Analysis.	G-67
G-l

-------
Section 1
Comparison Graphs of Coke Properties
KIDC vs. Conventional Coke.
G-2

-------
a
i
u>
T
* e
SEPTEMBER
1991
Comparison of Coke Stability
KIDC vs. Conventional Coke
Sparrows Point 11/12 Battery
September - November, 1991
1a \
V
> 60
55
55
Legend
• Conventional Cok
" KIDC Cokm
22	29	ft
OCTOBER
i	r	i
27	3	10
NOVEMBER
Date
JWP
2/21/92

-------
80
75
70
65
60
55
50
45
40
Comparison of Coke Hardness
KJDC vs. Conventional Coke
Sparrows Point 11/12 Battery
September - November, 1991
65 ~o
Legend
Conventional Coke
° KIDC Coke
MBER
91
"i i r
22	29	0
OCTOBER
i	r
27	3	10
NOVEMBER
60 cn
CD
Date
JWP
2/21/92

-------
20
18
16
14
12
10
8
6
4
2
0
Comparison of Coke Reactivity
KIDC vs. Conventional Coke
Sparrows Point 11/12 Battery
September - November, 1991
Legend
• Conventional Coke
KIDC Coke
MBER
91
t	r
29 e
OCTOBER
i	—r
27	3	10
NOVEMBER
>
O
CO
CD
CC
Date
JWP
2/21/02

-------
a
i
a\

100 n

90-

80

70-

-------
o
E
=3
u
CO
CD
JZ
u
c.
CM
+
100
Comparison of Coke Size, % +2 Inches
KIDC vs. Conventional Coke
Sparrows Point 11/12 Battery
September - November, 1991
vi
1
Legend
• Conventional Coke
° KIDC Coke
40
—	_T
1	8
SEPTEMBER
1991
~r~
16
~r~
22
	1	r~
OQ	A
OCTOBER
I	I	T	I	I	I
13 20 27	3	10 M
NOVEMBER
I
24
100
90
80
70
60
50
40
E
u
C/3
CD
O
CM
+
Date
JWP
2/21/92

-------
Comparison of Coke Volatile Matter
KIDC vs. Conventional Coke
Sparrows Point 11/12 Battery
September - November, 1991
-0.8
OC
LU
H 0.7-
DC
0.7
!Sc
5
0.6
-0 .6
-0.5
LU
0.5
< 0 4
-0.4 ^
O
> 0.3-
0.3 >
0 2
Legend
• Conventional Cok»
° KIDC Coke
¦—r"
22
	f	r
79 e
OCTOBER
70
27	3
NOVEMBER
to
24
SEPTEMBER
1991
JWP
Date

-------
1-
0.9-
0.8-
0.7-
QC
5 O-6 H
Z>
CO
0.5
0.4
0.3
0.2
0.1
0
i e
SEPTEMBER
1991
Comparison of Coke % Sulfur
KIDC vs. Conventional Coke
Sparrows Point 11/12 Battery
September - November, 1991

r
IB
I	1 "	1
22	29	6
OCTOBER
~r
13	20	27	3	10
NOVEMBER
Legend
• Conventional Coke
KIDC Coke
Date
JWP
2/21/92

-------
0
1
Comparison of Coke % Moisture
KIDC vs. Conventional Coke
Sparrows Point 11/12 Battery
September - November, 1991
Legend
• Conventional Coke
o KIDC Coke
K)
i
1	8
SEPTEMBER
1991
"i	r
29	6	13
OCTOBER
l	1	r
27	3 10
NOVEMBER
Date
JWP
2/21/02

-------
a
i
Comparison of Coke CRI (Hampton Roads)
KIDC vs. Conventional Coke
Sparrows Point 11/12 Battery
September - November, 1991
x
CD
"O
_C
>
¦4—'
>
o
CO
CD
cc
CD
o
o
¦
Legend
• Conventional Coke
» KIDC Coke
	T
1	8
SEPTEMBER
1991
22 29	6
OCTOBER




1 1 1 : 1 1 ' I 1 t 1 ' • 1 lit 1 ! II 1 '
u.




s
	A....






-



-
27	3	10
NOVEMBER
17
24
50
45
40 X
CD
35 ^
30
25
20
M5
10
5
0
_c
>*
+-¦
">
o
CD
CD
CC
CD
o
o
Date
JWP
2/21/02

-------
75
£ 70
65
60-
55
CD
® 50
45
40
Comparison of Coke CSR (Hampton Roads)
KIDC vs. Conventional Coke
Sparrows Point 11/12 Battery
September - November, 1991

Legend
• Conventional Coke
KIDC Coke
	r
1	8
SEPTEMBER
1991
~i		- i
OQ	A
OCTOBER
i	r
27	3	10
NOVEMBER
Date

-------
Comparison of Coke Size, % -0.5 Inches
KIDC vs. Conventional Coke
Sparrows Point 11/12 Battery
September - November, 1991
Legend
• Conventional Coke
° KIDC Coke
7-
co
a>
sz
o
c
LD
O
l
T	
e
1 6
27
1
22
13
20
3
10
I?
24
SEPTEMBER	OCTOBER	NOVEMBER
1991
Date

-------
Section 2
Graphs of KIDC Coke Properties
G-14

-------
80
75
X
CD
? 70
:= 65
JU
CD
CO 60
66
55
50
45
KIDC COKE PROPERTIES I
Hardness & Stability
Sparrows Point 11 Battery
09/07/90 - 11/26/91
40
i e
SEPTEMBER
1991
"T"
16
'/V\yS

V


"V

i - i 	r
22	29	6
OCTOBER
Legend
• HARDNESS
STABILITY
i	1	r	-	~	t	~i	1	r~
13	20	27	3	10	17	24
NOVEMBER
80
75
X


-------
20
18
16
14
12
10
8
6
4
2
0
KIDC COKE PROPERTIES II
Moisture & Ash
Sparrows Point 11 Battery
09/07/91 - 11/26/91
Legend
• Moisture
° Ash

MBER
91
i	1—	—r
22	28	6
OCTOBER
r

i~	r —	¦	r	-
20	27	3	10
NOVEMBER
M
f	"I
17	24
/
20
f- 18
16 _C
CO
14 <
12 ^
O
10 
-------
KIDC COKE PROPERTIES III
Sulfur & Volatile Matter
Sparrows Point 11 Battery
09/07/91 - 11/26/91
LL 0.9
0 .9 ~_
r 0.5-
Legend
• VOLATILE MATTER
<> SULFUR
i	r
1	8	16
SEPTEMBER
1991
i	1	r
22	29	0
OCTOBER
27	3	10
NOVEMBER
Date
l(|UP
2/20/02

-------
CO

-------
20
18
16
14
12
10
8
6
4
2
0
KIDC COKE PROPERTIES V
Reactivity
Sparrows Point 11 Battery
09/07/91 - 11/26/91
20
6
4
MBER
91
i	¦ i	i	i"
16	22 29	0
OCTOBER
i	1	1	1	1	1	r
13 20 27	3	10	17	24
NOVEMBER
Date
2
0
JWP
2/20/92

-------
c 75
O
70
o
to
£ 65
0 60
+-»
< 55
-C
O) 50
c
CD
2- 45
CO
00 40
.r 35
>
O 30
CD
® 25-
£ 20
O
° 15
KIDC COKE PROPERTIES VI
Hampton Roads CRI & CSR Data
Sparrows Point 11 Battery
09/06/91 - 11/26/91
¦A-
r
r-

\
'/J/V-'
1	8
SEPTEMBER
1991
16
—I	1	I"
22	29	0
OCTOBER
~r~
13
'V

Legend
• CSR	
° CRI

20	27	3	10
NOVEMBER
/¦
/
17
" I
24
75
70
c
o
o
CD
65 ®
CO
60 <5
55 <
_c
-50 o>
c

30 g
<0
25 £
20 £
O
15 U
Date
JWP
2/20/92

-------
a
i
_c
o
_c
CN
10
9
8 H
7
6
5
4
3
0
KIDC COKE PROPERTIES VII
% Passing 0.5 Inches
Sparrows Point 11 Battery
09/07/91 - 11/26/91
T
1	6
SEPTEMBER
1991
r	¦		r
22	29	6
OCTOBER
i	1	r
27	3	10
NOVEMBER
10
9
8
7
JZ
he g
5
i
4
3
2
1
0
Date
JWP
2/20/92

-------
Section 3
Graphs of Conventionally Quenched Coke Properties
G-22

-------
0
1
K>
X
CD
T3
_C
_Q
CO
+-»
GO
o3
CO
w
o
c
"O
L.
(0
COKE PROPERTIES I
Hardness & Stability
Sparrows Point 11/12 Battery
12/01/90 - 11/30/91
m
60 CO
Legend
• HARDNESS
" STABILITY
1	T	1	1	1	1	1 — n	n	"7
DEC JAN FEB MAR APR MAY JUN JUL AUG SEP OCT NOV
1990 1991
Date
I Ml P
2/13/B2

-------
0
1

20-

18

16-
c~
O)
-
<
14
\0

0s

v_
12-
O
-

-------
DC
3
Ll_
_l
3
CO
o
cc
LU
H
*
LU
£
o
>
COKE PROPERTIES III
Sulfur & Volatile Matter
Sparrows Point 11/12 Battery
12/01/90 - 11/30/91
0.8 CO

-0.5
Legend
• VOLATILE MATTER
SULFUR
DEC JAN FEB MAR APR MAY JUN JUL AUG SEP OCT NOV
1990 1991
Date
JWP
2/13/92

-------

o
+
E
D
(J
CO
(D
O
CN
+
100
COKE PROPERTIES IV
% +2 Inches (Cu) & % +4 Inches
Sparrows Point 11/12 Battery
12/01/90 - 11/30/91
100
80-
I

i M
I.
Legend
• % +2 INCHES
% +4 INCHES
DEC JAN FEB MAR APR MAY JUN JUL AUG SEP OCT NOV
1990 1991
Date
CO
CD
O
_c
+
o
1e
3
CO
CD
O
_c
CNI
+
JWP
2/13/B2

-------
20
18
16
14
12
10
8
6
4
2
0
>
^—'
>
o
CD
CD
cc
JWP
2/13/92

-------
0
1
K>
COKE PROPERTIES VI
Hampton Roads CRI & CSR Data
Sparrows Point 11/12 Battery
10/15/90 - 07/13/91
V 65-

0 60
60 m
U) 50
Legend
<* 40
• CSR
£ 35
A
Z 30
JAN
1991
FEB MAR APR
Date
J VII P
2/13/92

-------
Section 4
Monthly Average i Standard Deviation Graphs for
Conventionally Quenched Coke Properties
C-29

-------
a
i
COKE REACTIVITY INDEX
Monthly Avg, +/- 1 Std. Dev. (Hampton Roads Data)
Sparrows Point 11/12 Battery
October 90 to October 91
o 30
40
35
 S<& t>^	vNC> cS
Cr O0, ^	V*- ^ ^	& O
25
20
15
X

<
1990
1991
JWP
2/21/92

-------
, COKE STRENGTH AFTER REACTION
Monthly Avg, +/- 1 Std. Dev. (Hampton Roads Data)
Sparrows Point 11/12 Battery
October 90 to November 91
«
i
C
o
+->
o
CD

<
50 <->
o°V <#" / ^ £ o°V
1990	1991
JWP
2/21/92

-------
COKE MOISTURE
Monthly Avg, +/- 1 Std. Dev.
Sparrows Point 11/12 Battery
December 90 to November 91
0<-° ^
1990
1991

-------
0
1
75
X
CD
? 70
-Q 6*5
CD DO
¦»—1

<
50
COKE STABILITY INDEX
Monthly Avg, +/- 1 Std. Dev.
Sparrows Point 11/12 Battery
December 90 to November 91
55 
-------
Ci
I
COKE HARDNESS INDEX
Monthly Avg, +/- 1 Std. Dev.
Sparrows Point 11/12 Battery
December 90 to November 91
u 75 -
0 70

1990
1991
lUfP
2/25/92

-------
0
1
COKE REACTIVITY INDEX (Bethlehem)
Monthly Avg, +/- 1 Std. Dev.
Sparrows Point 11/12 Battery
December 90 to November 91
25
X
CD
T3
C 20
>
"G 15
CO
CD
CC
CD
o
(J
CD
D)
CO
v_
CD
>
<
10-
0.
o*-c ^	^
1990	1991
25

-
X

CD

"O
20
c

>*

•*-»

>

+-»
- 15
o

co

CD

DC

CD
-10
O


-
<
0


JWP
2/25/92

-------
COKE SIZE (% -1/2 Inch)
Monthly Avgr +/- 1 Std. Dev.
Sparrows Point 11/12 Battery
December 90 to November 91

1990
1991

-------
COKE SIZE (% +4 Inches)
Monthly Avg, +/- 1 Std. Dev.
Sparrows Point 11/12 Battery
December 90 to November 91
0
1
O 50

<
1990
1991
JWP
2/25/82

-------
COKE SIZE (Ciim. % +2 Inches)
Monthly Avg, +/- 1 Std. Dev.
Sparrows Point 11/12 Battery
December 90 to November 91
100
100

CO

<
1990
1991
JWP
2/25/92

-------
COKE SULFUR CONTENT, %
Monthly Avg, +/- 1 Std. Dev.
Sparrows Point 11/12 Battery
December 90 to November 9i
O 0.7 -

CO 0.2
-0.9
sP
0s
_
s.
4-»
: 0.8
c

. 0.4
a>
-
o
r 0.3
CJ

CD

O)
: 0.2
<0
1	
~

<
^	^	& 0c^ ^
0
1990
1991
JWP
2/25/92

-------
Section 5
Conventionally Quenched Coke Properties Database
G-40

-------
1
2
3
4
5
6
7
6
y
io
11
i 2
13
14
15
16
17
18
19
20
21
22
23
24
20
2b
27
28
29
30
31
32
33
34
35
36
37
38
39
40
4 1
42
43
44
45
46
47
48
49
bO
51
02
sn
40
54
54
63
63
72
72
71
20
96
96
17
17
69
69
07
07
31
3 t
54
54
20
28
17
1 7
23
23
57
57
17
1 7
C7
07
36
36
29
29
45
45
67
67
74
74
20
20
04
04
28
28
2D
90
90
37
COKE PROPERTIES FROM DAILY COKE REPORTS. 11/12 BATTERIES 11:30 Wednesday. April 1,
KIDC DEMONSTRATION PROJECT - BETHLEHEM STFFl CORPORATION
SPARROWS POINT. MARYLAND





COKE

SIZE




°/o
STAB 1L
DATF
RFI T
TURN
0N4"
C1N3 "
ON 2"
ONI 5
ON 1 "
(IN 75"
ON . 5"
THRU 5
H20
ITY
12/01/90
K-6
3-11
31 .3
30. 1
24. 1
8.2
3.2
1
1
0.5
1.5
2.63
58.2
12/02/90
K-6
7-3
34 .4
28.2
25.9
6.6
2 . 4
0
6
0.6
1 . 3
1 16
08 . 4
12/02/90
K-6
3- 1 1
35.9
19.2
30.3
8 .7
3 . 1
0
6
0 6
1 .6
111
59 . 1
12/03/90
K-6
7-3
22 . 3
30.9
34 5
8.2
2 .0
0
5
0 2
1 .4
12 21
61 .5
12/03/90
K-6
3- 11
27 .8
33.9
32.0
4 .0
1 . 1
0
1
0 1
I.O
3 68
62 . 5
12/04/90
K-6
7-3
20.4
36 1
30 9
8 9
2 4
0
6
0 3
0.4
1 04
59 6
12/04/90
K 0
3 11
1 1 .0
20.5
39.4
15.5
7.4
1
G
1 2
3.4
G 95
CO 4
12/05/90
K-6
3- 11
15.8
28.2
40.9
11.7
2 . 3
0
4
0 3
0.4
4 98
6 1.7
12/06/yo
K-6
3-11
26.9
33 .9
30.4
4 . 4
2 b
0
b
0.3
1 . 1
2 93
60. 1
12/07/SO
K-6
7-3
11.1
28.4
40.6
12.0
b . 1
0
9
0.4
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14.19
09.8
12/07/90
K-6
3- 1 1
30 . 7
20. 7
30 1
10. 4
4 e
1
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0.3
1 . 3
1 1 .43
60. 5
12/0R/90
K-6
7-3
20 1
22 9
25 6
20 2
9 1
0
R
O 5
1 O
2 44
60 1
12/08/90
K-6
3-11
35.2
211
29 8
7.0
5.0
0
8
0.3
0.8
2.03
58.9
12/09/9O
K-6
7-3
25.4
23.0
22 5
16 . 1
11.4
0
4
0.3
0.9
O 34
61.3
12/09/90
K C
3 11
31 .2
22.7
26.0
12.5
5.6
0
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0.3
1.5
5.88
GO.9
12/10/9O
K-6
7-3
2 1.4
32. 1
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1
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1 .7
2 . 4
2.34
60. 1
12/10/90
K-6
3- 1 1
2b . 3
26. 1
34 8
8 9
3. 1
0
6
O 6
0.6
2 82
60. 3
12/11/90
K-6
7-3
20.9
28.4
3? 3
10.4
3 . 7
1
2
O 9
2 . 2
4 63
60 . 9
12/X 1/90
K-6
3- 1 1
39.9
25.2
24.8
5 .8
1.7
0
7
0.2
1 . 7
1 1 97
6 1.3
12/12/90
K G
3-11
26 9
20.6
29 5
1 1 9
5 6
1
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1 2
2 8
ft 63
60 2
12/13/90
K-6
3-11
20. 1
26.5
37.6
7 2
4 . 4
1
9
0 8
15
0 61
59.0
12/14/90
K C
7-3
23 7
25 2
33 3
9 3
4 6
1
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0 7
2 1
8 44
6 1.7
1 2/14/90
K-6
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20.0
29.9
27 .9
7 . 3
5.5
1
7
1 .7
6.0
12. 16
57 .8
12/15/90
K-6
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28.4
26.4
29.9
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3.5
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1.9
3 75
59 . 7
12 / 10/30
K-6
3 1 1
22 . 4
28 . 4
30.9
0 . 2
4 . 4
1
2
1 . 2
3 . 3
3 74
58.8
12/16/90
K-6
7-3
19.7
29.5
35.6
9. 1
3.3
1
2
0.5
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2 37
61 .0
12/ 16/90
K-6
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31.7
31.4
27 . 4
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12/17/90
K-6
7-3
36.5
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20 3
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5 14
58 9
12/17/90
K-6
3- 1 1
4 12
23 . 8
24 0
6 1
2 1
0
2
0 6
2 0
2 64
58 4
12/18/90
K-6
7-3
10.9
25.4
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17.5
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1 1 52
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12/18/90
K-6
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412
30 . 9
2 11
3 . 7
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0 4
0.8
1 47
60 0
12/19/90
K-6
7-3
20 8
28 4
37 2
6 9
4 2
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1 . 1
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605
12/10/90
K-6
3-1 1
34 . 4
26 . 4
23 1
4 .4
3.8
3
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6 1.2
12/20/90
K G
7 3
14 1
22 . 7
30 7
12.4
7 . 8
1
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1 . 4
4 23
57 .6
12/20/90
K 6
3-11
22.9
20.2
44.6
G . 7
2.7
0
2
0.7
1 8
2.49
59.2
12/21/30
K-6
7-3
03.6
24 . 1
1 7.0
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0
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0.2
13.01
oy. r
12/21/90
K-6
3- 1 1
12 8
31.7
36 7
10.5
4 . 1
1
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2.0
8 2 1
60 . 4
12/22/90
K-6
7-3
44 .6
22 . 1
18 .8
10.5
3.3
0
3
0.2
0.2
8.99
60.2
12/22/90
K-6
3- 1 1
2 14
25.6
32 6
13 8
3.0
1
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0.8
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6 11
12/23/90
KG
7-3
32.5
25.8
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9.4
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GO. 0
12/23/90
K-6
3- 1 1
36. 4
23 .9
26.8
8 . 2
2.3
0
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0.2
2.0
2.6 1
59.6
12/24/90
K-6
7-3
17 3
14 . 4
47 .9
111
3 . 2
0
7
0.9
1.5
2 .92
60.4
12/24/90
K-6
3- 1 1
29 4
17.8
37 .4
10 1
3 . 4
0
6
0 4
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2 56
59.8
12/25/90
K-6
7-3
18.6
22.0
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10.0
4.2
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59.6
12/25/90
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3- 1 1
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23.6
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7.6
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1.9
15 .56
60.4
12/26/90
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20.4
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0.8
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5.84
60.2
12/26/90
K-6
3- 1 1
37 8
27 .4
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2.0
0
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1 .54
61 .6
12/27/90
K-6
7-3
24 .0
25 .0
34 3
8 7
6.5
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15.79
59.3
12/27/90
K-6
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16 4
23 . 5
39 6
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60 6
12/20/90
K 6
3 1 1
32 4
27 .4
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61 .0
12/29/90
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7-3
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23.3
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10. 71
60. 1
12/29/90
K-6
3- 1 1
14.0
25.9
31.5
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5 .62
6 1.2
12/30/90
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25 2
34 5
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68.	1
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COKfe PROPERTIES FROM DAILY COKE REPORTS, 11/12 8ATTERJES 11:30
KIDC DEMONSTRATION PROJECT - BETHLEHEM STCCl CORPQRAUUN
SPARROWS POINT. MARYLAND
Wednesday, April 1.
COKf	SIZE	%	S1AB1L	HARD	RtAC I
TURN 0N4"	0N3"	0N2"	ONI.5*	0N1"	ON.75"	ON.5"	THRU.5	H2U	ifY	N£Sb	JV1IY	SULFUR	VM
24.4	25 5	33.2	10 9	4 5	O 7	O.b	0.3	1 12	58.1	68 4	R 6	0.60	0 53
33.7	29.0	23.6	6 8	4 8	0.4	0.1	16	2.77	58.1	68.1	12.9	0.56	0 48
28.0	30.2	23 b	9 8	5 3	1.8	0.1	1.3	16.72	58 8	69.3	12 0	0.56	0 4ft
12.7	16 9	37.6	21.5	B.I	14	0.5	1 3	2 06	50.2	68.8	13.7	0 56	0 45
20.1	21.b	29.b	13.2	b 8	3.6	3.4	2.8	1 .34	60 2	69.6	13.7	0.56	0.45
17	b	lb 4	30 9	19.2	7.7	2.0	1.5	b 8	11.37	60.1	68.0	10.0	0.59	04?
30.5	36.5	28.3	2.2	11	0 3	0.2	0.9	1 72	61 5	67 4	10 0	0 50	0 42
29.6	27.3	24.6	10.1	b.8	0.8	0.3	1b	b.26	60.1	66 9	B 5	0 56	0 68
50.0	21.5	19.4	4.8	2.3	0.1	0.3	1.6	3.26	60. 4	66.6	85	056	068
18.6	12.0	31.5	26.3	8.2	1.9	0.6	0.9	3 79	Sfl.fi	70 1	9 7	0.58	0 54
21.3	11.1	41.4	1b.4	6.8	2.2	0.4	0.4	2 61	62 0	70 7	9.7	0 58	0 54
17.5	29 3	31.4	14 8	5 4	O 3	0 2	11	3.18	C1.1	G0 5	11.3	0.62	069
25.7	30.7	35.2	5 4	1 2	0 3	0 3	1.2	3.50	60.4	70.1	11.3	062	0 09
7.3	22.0	46 7	1? 8	4 9	1 G	11	2.7	0.62	00.8	08.6	7.8	0.61	O 9b
19.2	26.8	37.0	8.G	3 G	2.1	1.2	1.5	1.44	b9.9	60.2	7 8	0.61	0.96
30.9	37.9	25.1	3.b	1.4	O.b	0.4	0.3	4.00	66.4	68.9	9.7	0.63	0 59
50.4	24.6	22.6	1 3	0.3	0.3	0.2	0.3	2.82	60 3	69.0	13.0	0.67	O 64
27.0	38. b	28.3	4.b	0 8	0.3	0.2	0.3	2.74	61.7	70.5	9.0	0.6B	0 48
18.3	37.1	32.3	7.8	2.7	0.6	0.3	0.9	2.76	61.0	69.3	9.0	0.6R	O 48
41.7	32.4	21.8	30	07	01	O 1	0.2	11?	62 2	69.1	1O0	0 65	0G9
9.8	41.?	40.9	b 2	l.b	0.2	O 2	1.0	? 34	60.1	705	10.0	0.05	0.G9
19.4	41.0	29.7	7 4	1.0	0.4	0.3	O ft	7,33	67.3	69 1	11.1	0.G9	0.58
19 5	29.0	3? 8	10.7	4 3	10	O 7	2.0	9.21	G1.2	70.1	11.1	O 69	O 58
18.8	23.4	33.5	13 2	5 2	16	0.9	3.4	3.57	62.8	70.3	110	0.67	0.86
29.6	34 5	26 8	5 2	2 2	0 5	O 3	0.9	0 8?	60 O	fifl 3	11.0	0.67	0.86
19.1	33 2	31.4	10 2	2 9	11	0.6	1.5	4.61	62 5	69 9	11 1	O.G8	0.58
24.6	28 7	29 8	97	39	09	O 7	1.7	2 26	59 7	67 3	112	0 08	0.58
34	.2	28 b	2/ 7	4 R	3.2	O. 4	0.3	0..9	6.06	59 4	69 6	10 ft	O.G2	0.77
29.2	22 8	2b.0	11 7	8 1	2.1	0.1	1.0	0.76	60 6	6R 5	10 8	0.62	0.77
27 2	34 6	20.8	10.0	b.2	0.4	0 1	O 7	3 87	58 6	68 4	8 9	0 66	0.51
30	6	3b 3	2b.0	5.4	2.2	0.2	0.2	0 6	2.I9	60 0	69 I	fl.9	0 66	0.51
37.4	30 2	26 2	3 7	1.2	0 3	0 2	0.8	0 34	GO 4	6R 9	10.9	0.03	0.53
3b.9	33.0	22.1	4.8	2.6	O f	0.1	14	5 59	61.0	69 4	JO 9	0.6-1	0 53
35	6	32 4	23 5	5 ?	2 1	0 3	0 1	0.8	1 32	60 2	70 O	14.7	0.61	0.92
34 6	?9 7	27.0	7 9	4 7	0.3	0 1	0.7	2.25	59.9	GG 0	14.7	0.01	0.92
18	6	22.4	29.9	15 7	8.6	3 8	O 4	O 6	1 22	59 G	GG 2	15.0	0.64	O 72
211	25 G	32 3	99	49	f. O	04	O 8	1.05	59.9	GB 4	15 0	O.04	0.72
38.0	32.9	22 1	39	14	03	0.1	1.3	0.35	59 5	70-t	11.4	0.6b	0.56
34 8	20 ft	28 3	13.0	1ft	0 1	0.1	11	2.3 1	by.1	bB b	11.4	O.Ob	O.06
20.6	25 6	31.2	19.2	2 0	0.3	0.3	0.8	2.84	bO. 9	07.3	10.2	O. bb	0. 50
25 O	29.1	32 2	10 1	1.4	1.2	0.4	0.6	3.15	00. b	70.2	10.2	O.bb	0 bO
53 6	28 0	13 ft	17	0.4	0.8	O 5	0.4	3.30	00.3	08.7	9 8	0.67	O 55
31	7	31.2	22 2	6.6	2 9	13	0.9	3.2	4.41	61.6	67.4	9.8	0.67	0.55
13.8	43.0	37 9	2 0	1.4	0.6	0.4	0.3	2 44	59.8	69.2	9.b	O.bb	0.53
15.0	21.b	40 9	10./	5 *	1.2	1.8	2.b	9.29	60.4	70.2	9b	0.66	0.53
21.4	22.8	31.5	11.3	8.0	3.5	0.6	0.9	5 94	60.1	67.8	14.9	0 62	0 55
27.2	2b. ii	31.1	7.0	6.2	1.9	0.4	Ob	1.18	b7 . 3	65.0	14.9	0 62	0 55
32.2	3b 3	26 2	2 1	lb	0.8	0.5	0.4	0.00	5fl 9	6fl 2	11 G	0 65	0.29
23.5	2b 9	31 b	8 7	b.3	1.2	1.3	2 6	2 28	5ft 5	67 4	11.G	0.G5	0 29
3/3	28.4	27 b	3 b	1.7	0.4	0 1	0.7	<). 96	59 8	68 2	15 0	0.63	O 42
bG 3	27.b	12 b	1.7	Ob	0.2	0.3	10	1.52	60.2	68.6	15 O	O 63	O 42
33 7	35.7	25 3	2b	1.2	0.4	0.3	0.9	2.32	bO.9	68.1	8.6	0 67	0 55
39.O	2b.b	2 1.7	b 1	2.7	0.7	2 2	2.1	2 b6	6 1.4	67.5	8.6	0.6?	O 55

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COKF PRGPLH TIES FROM OAILY COKE REPORTS. 11/1? BATTERIES
KIDC DEMONSTRATION PROJECT - BETHLEHEM STEEL CORPORATION
SPARROWS POINT, MARYLAND
11:30 Wednesday, April 1.
BELT
TURN
0N4"
0N3 *
K"b
/-'J
JO. U
41.5
K-6
3- 1 1
39 . 5
29.4
K-6
7-3
33.2
34 .4
K-6
3- 1 1
27 ft
42 . 1
K-6
7-3
20.0
31.8
K-6
3-11
41.9
23. G
K"b
7 3
26 . 2
30 . 1
K-6
3- 1 1
40 7
31.6
K-6
7-3
25 9
37 . 7
K-6
3- 1 1
36 6
31.?
K-6
7-3
20. 1
35 4
K-6
3- 1 1
23 .5
30.8
K G
7-3
25.4
35 7
K C
3 11
27. G
29. G
K-6
7-3
34 7
39 . 2
K-6
3-1 1
35.4
31 7
K-ti
7-3
db. O
31 .4
K-6
3- 1 1
19 7
37 1
K-6
7-3
19 7
38 8
K-6
3-11
5 9
29 2
K C
7-3
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19.0
K-6
3- 1
12 . 3
17.4
K G
7 3
13 . 7
42 O
K-6
3 11
28 .a
4 1 .O
K-6
7-3
38.3
27 .9
K-6
3- 1 1
27 .0
37 2
K-6
7-3
36 .9
26 .8
K-6
3- 1 1
30 1
3b . 4
K-6
7-3
14 . 3
29 . 7
K-6
3- 1 1
35 7
35.4
K-6
7-3
17.2
30 7
K-6
3-11
22 . 5
39.6
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COKE PROPERTIES FROM DAILY COKE REPORTS. 11/12 BATTERIES
KIDC DCMONSTRA T ION PROJLC1 - BE I HI EHbM *> I t L L CUKPUHATION
SPARROWS POINT. MARYLAND
11:30 Wednesday, April 1
1992 B



COKE

SIZE


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0N1.5"
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~N.75"
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7-3
42 2
37 2
17 . 8
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27 3
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30 0
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2 3
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27 6
3 1 6
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79 n
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24 5
1 6
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SPARROWS POINT, MARYLAND
1 1 - no
WtuJnosri.'iy , Apr 1 1 I
1992 11
O
I
L"






COKE

SIZE



UBS
DATE
BELT
TURN
0N4"
0N3 "
UN2"
ON 1 .fa"
ONI "
ON.7b"
ON . b "
IHRU
531
09/00/91
K 0
3 11
28.7
31 .0
23.8
6 4
3 7
1 . 4
1 . 8
3 2
532
09/07/91
K-6
7-3
28 6
43.3
23. 1
2.9
0.7
0.4
0.2
0.8
533
09/07/91
K 0
3 11
299
35.8
25.2
4.8
2.0
0.7
0.7
0.9
534
09/O8/91
K-6
7-3
33 . 3
39 .0
22 .9
2 . 1
1 .0
0.4
0.3
0.4
535
09/OR/91
K-6
3- 1 1
35 0
41 6
2 1.1
1 t
O 6
0.3
0.2
0 1
536
09/O9/91
K-6
7-3
32 . 4
37.4
25 .8
2 5
0 6
0.4
0.6
0.3
537
09/09/91
K-6
3- 1 1
38 . 5
37.2
2 1.2
1 .3
04
0.7
0.4
0.3
538
09/10/91
K-6
7-3
46 9
30 0
16 ft
1 7
1 .4
0.9
0 4
1 9
539
09/10/91
K-6
3-11
31.1
4 1 .5
25.0
1 .0
0.2
0 2
0 2
08
540
09/11/91
K 0
7-3
43 0
3fl .0
16 . 2
1 0
0.7
0.5
0.0
O.b
541
09/11/91
K 0
3 1 1
32.5
3G . 3
28.2
2 1
0.2
0 3
0.2
0.2
542
09/12/91
K-6
7-3
25 2
43.2
28.0
2.0
O.B
0.4
0. 2
0.2
b43
09/12/91
K-6
3-1 1
310
43.0
24 . 2
0.8
0.4
0.2
0.2
O?
b44
09/13/9 1
K-6
7-3
10.0
27 .5
38.5
17 . 3
8.2
1 .5
1 . 3
1.7
545
09/13/91
K 6
3- 1 1
212
37 6
33 5
4 1
1 6
Oft
0. ft
0 4
540
09/14/91
k-G
7-3
17.3
34.5
32. 1
9. 1
4 . 3
0.9
0.7
1 . 1
547
03/14/91
K-b
3-11
27 .0
38.5
25.8
4.0
2.3
0.7
0.2
0.3
548
09/15/91
K-6
7-3
42 . 7
27 .5
24 . 3
3.2
1 O
0.2
0.3
0.8
549
09/15/91
K-6
3-11
38.2
35 B
15.8
4 7
1.6
0.9
1 .0
2 0
550
09/10/91
K-6
7-3
41.5
34.8
21 .6
1 . 5
0.2
0.2
0. 1
0. 1
bb 1
09/16/91
K 0
3-11
31.3
30.4
27 . 1
4 . 2
0.4
0.2
0.2
0 2
552
09/17/91
K-6
7 3
34 .8
34 0
?7. 1
? .O
1 ?
0 6
O 2
0 1
553
09/17/91
K-6
3-11
44 . 1
34 .4
17.9
1 .6
0.7
0.7
0 5
0 1
554
09/18/91
K -6
7-3
34 4
37 9
22 4
? 4
0 4
0 ?
0.4
1 .9
555
09/18/91
K-6
3-11
34.9
39.0
23. 1
2.3
0.2
0. 1
0. 1
0.3
550
09/19/91
K-6
7-3
42 .0
36 .9
16.6
2. 1
0.9
0.2
0.2
0.5
bb7
09/19/91
K 0
3 11
39. 1
34.7
2 1.1
2 . 4
1 . 7
0.0
O. 5
0 5
558
09/20/91
K-6
7-3
39.9
34 O
21 .2
2.9
0.7
0.3
0. 3
0.7
559
09/20/91
K 0
3-11
33 .8
39 5
2 1.7
2 4
O 8
0.8
0. 4
0 6
560
09/? i/m
K-6
7-3
40 6
37 6
19.4
1 . 3
0.4
0.2
0.2
0 3
56 }
09/21/91
K-6
3- 1 1
3ft 1
?9 4
?ft 6
3 O
0 2
0 1
0. 1
O.b
562
09/22/91
K-6
7-3
39 . 5
35 9
21.2
2 3
0 5
0 3
0 2
0 1
563
09/22/91
KG
3-11
38.9
37 3
19.0
2 . 9
1 .0
0.5
0.2
0.2
564
09/23/91
K-6
7-3
43.2
39 4
13.9
1.6
0 8
0 3
03
O.b
565
09/23/91
K-6
3-11
20.5
500
10. 7
0 5
2 4
0 4
0.2
1 .3
5G0
09/24/91
K-6
7-3
43.2
37.4
14.6
2.2
0 8
0.8
0.4
0.6
507
09/24/91
K-0
3- 1 1
20.3
39 . 1
25.8
4.9
1 . 8
0.5
0.5
1 1
568
09/25/91
K 6
7-3
37 .5
33 8
25 ?
? 0
0 5
0 3
0 3
0 4
569
09/25/91
K-6
3-11
35.0
38 7
20. 1
3.9
1 .0
0.5
0.4
0.4
570
09/20/91
K 0
7 3
30.0
40 2
21 .9
0.7
0.3
0 1
0 1
01
571
09/26/91
K-0
3-1 1
b0.3
30.9
10. 1
1 . 4
0.9
0. 1
0 1
0.2
b72
09/27/91
K-6
7-3
43.4
36 6
18 3
1 -O
0 4
0 1
0 1
O 1
573
09/27/91
K-6
3- 1 1
25. 3
4 1.8
2D 5
3.0
0 1
0 1
0 1
0 1
574
09/28/9 1
K-6
7-3
40 1
3R 4
1ft 6
1 4
0 4
0.3
0.3
0 5
575
09/28/9 1
K-6
3-1 1
17 2
23.6
33 5
16 3
5 6
1 4
0.8
1 6
576
09/29/91
K-6
7-3
43 O
32 .5
2 1.3
2 . 1
0 2
0 2
0.2
0 5
577
09/29/91
K-6
3-11
31.7
38.8
22 6
3 8
0 7
0 7
0.7
1 .0
578
09/30/91
K-0
7-3
30.5
28. 1
27.3
0.2
0.5
0.3
0.2
0.9
579
09/30/91
K 0
3- 1 1
43 . 7
32.5
21 0
0.7
0.2
0.2
0.3
i.A
580
1<)/01 / 9 1
K-6
7-3
32 .5
45.3
19.9
1.5
0.4
0. 1
0.1
0?
581
10/01/91
K-6
3- 1 1
25.8
40. 1
30 . 3
2 3
OR
0 2
0.2
0.3
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10/02/91
K-6
7-3
37 0
40 G
18 8
1 5
0.4
0.2
0.2
1 3
5fl3
10/02/91
K-6
3- 1 1
25 0
40 1
29.4
2.7
1 .0
0.4
0.5
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O.80
0.59
1 .26
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2. 15
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0.38
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0.00
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2.00
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COKE PROPERTIES FROM DAILY COKE REPORTS. 11/12 BATTERIES
KIDC DEMONSTRATION PROJECT BETHLEHEM STEEL CORPORATION
SPARROWS POINT. MARYLAND
11:30 Wednesday, April 1, 1992 14
COKE	S17F	%	STABIL	HARD	REACT
OBS DATE BELT TURN 0N4" ON.V' 0N2"	0N1 5"	0N1"	ON.75" ON S" THRU 5	H?0	ITY	NESS	IVITY	SULFUR	VM	ASH
690 11/30/91 K-6 7-3 39 O 3? 5 31.4	3.9	13	0 4	0.7	0.8	1.68	60.8	68 8	15.9	O.56	0.75	8.59
G91 M/30/91 K-6 3-11 32.8 40.2 21.1	3 3	0.9	0 4	0.3	1 0	1.36	60.6	68 5	15.9	0 56	0.75	8 59
0
1

-------
HAMPTON ROAUS LABS CUKE. DATA. 11 / Y2 BATTERIES & A RATTFRY 11:30 Wndncr.rtay. April 1. 1fl92 15
KIOC DEMONSTRATION PROJECT - BETHLEHEM STFFl. CORPORATION
SPARROWS POINT. MARYLAND


COKE
COKE REACTIVITr
COKE STR&NUfH
obs
HATE
BATTCRY
INDEX
AFTTR REACT ION

10/15/90
A
27 .0
bb . 2
2
10/16/90
A
28 .8
b4 . 9
3
10/16/90
11/12
28. 1
bb. 1
4
10/17/90
A
28 .2
58. 2
5
10/18/90
A
28.6
5b. /

-------
HAMPTON ROADS LABS COKE DATA, 11/12 BATTERltS & A BAlTtRY
KIDC DEMONSTRAlION PROJECT - RETHl EHEM STEEL CORPORATION
SPARROWS POINT, MARYLAND
11:30 WHflnnr»dnY. April 1, 1392 16


COKE
COKE REACTIVITY
CUKE SIRENGFH
OBS
DA T C
HA fILRY
INDEX
AFTER REACTION
54
1 1/ 18/90
1 1/1?
26 .6
t>8 O
55
11/19/90
A
24.3
65.6
56
11/20/90
A
26 .2
60. 2
57
11/20/90
11/12
28 6
54 4
58
11/21/90
A
2/ .0
59.9
59
11/22/90
A
26 .0
6 1.2
60
11/22/90
11/12
28 3
58 5
6 1
11/23/90
A
26 5
62 . 1
62
1 1/24/90
A
26 .9
58.4
63
11/24/90
11/12
27 2
59. 2
64
1 1/25/90
A
24.7
66.0
€5
11/25/90
11/12
27 .0
*9.0
60
11/26/90
A
28 . 4
63 . 5
67
11/27/90
A
24 . 1
64.9
68
1 1/27/90
11/1?
26 0
62 . 5
69
11/28/90
A
20.8
79. 1
70
11/29/90
A
24 . /
64 . 4
7 1
11/29/90
11/12
24 .9
68.8
72
11/30/90
A
26 . 2
61 5
73
12/01/90
A
24.8
64 3
74
I2/O1/90
11/1?
23 8
69.2
75
12/02/90
A
29.4
58.0
76
12/02/90
1 1/12
22.9
70. 1
77
12/03/90
A
22 9
6b . 2
78
12/04/90
A
26.8
60.7
79
12/O4/90
1 1/12
2b.5
i>a. 4
80
12/05/90
A
24 6
64 3
81
12/O6/90
A
24 .2
63 3
82
12/06/90
1 1/ 1?
24 3
6 19
83
12/07/90
A
30.8
51.3
84
12/08/90
A
27 1
58.0
85
12/08/90
11/12
22 .8
6b . 4
86
12/09/90
A
25 7
60 7
87
12/09/90
11/12
27 . 7
59 9
Aft
12/10/90
A
26.0
61 .9
89
12/11/90
A
24 4
64 . 8
90
12/11/90
11/12
26 0
62 8
91
12/ 12/90
A
26 5
63 3
9?
12/13/90
A
23 .8
65.5
93
12/1.1/90
11/1?
24 . 1
VO. 2
94
12/14/90
A
20.3
69 1
95
12/lb/90
A
22 . b
68 0
96
12/15/90
11/12
28 0
57 6
97
12/ 16/90
A
23 7
63 1
98
12/ 16/90
11/1?
77 . R
66 6
99
12/17/90
A
22 9
65 0
1O0
12/ 18/90
A
21 9
66 .6
101
12/18/90
11/1?
23 7
65.4
10?
12/19/90
A
27 . 1
59.2
103
12/20/90
A
23 9
64 .0
104
12/20/90
1 1/12
27 .4
57 .6
105
12/21/90
A
21 6
63 4
106
12/22/90
A
23 3
66.8

-------
HAMPIUN ROADS LABS COKE DATA. 11/12 BATTERIES & A BATTERY
KIDC DEMONSTRATION PROJECT - BETHLEHEM STEEL CORPORATION
SPARROWS POINT. MARYLAND
11:30 Wf*dne3dov. April 1. 1992 17


COKfc
COKF RFACTIVITY
COKE STRENGTH
OBS
DATF
RATTFGY
rNnrx
Af TFR RTACT ION
107
12/22/90
11/12
25.6
59 3
108
12/23/90
A -
2? 7
67 . 2
109
12/23/90
1 1/12
26 5
63.0
1 10
12/24/90
A
24 . 3
62 .G
1 1 1
12/25/90
A
24 .3
64 . 2
112
12/25/90
11/12
22 . /
6b .0
1 13
12/26/90
A
24 . 1
66 4
1 14
17/27/90
A
20 9
69.8
1 15
12/27/90
1 1/ 12
24 .9
62.9
1 1C
12/28/90
A
22.8
68.4
117
12/29/90
A
21.7
67.4
1 18
12/29/90
11/12
23 2
69 8
1 19
12/30/90
11/12
22. 1
G7 . 1
120
12/31/90
A
24 .6
6b . f
121
01/01/91
A
23.2
66 . 4
122
01/01/91
11/12
23.8
64 3
123
01/02/91
A
25.2
66.0
124
01/03/91
A
23.8
64 . 5
125
01/03/91
11/12
24 .6
64 . 1
126
01/04/91
A
23 . 3
63.9
127
01/Ob/91
A
26 .0
613
128
01/Oh/91
11/12
25 0
60 5
129
01/06/91
A
25 .0
G3 . 4
no
01/06/01
1 1/12
24 . 1
b'j . lJ
131
01/07/91
A
23.4
66.0
132
01/08/91
A
22. 7
66 . 2
133
01/08/91
1 1/12
22 9
58 1
134
01/09/91
A
24 3
64 2
1 35
01/10/91
A
22 1
£0 1
136
01/10/91
11/12
26 1
6 1.1
137
01/11/31
A
26 . 2
61 . 9
1 3d
01/ 12/9 1
A
23.8
05 1
1 in
01/12/91
11/12
2-1 .6
63 . 9
140
01/13/91
A
22.6
66 . B
14 1
01/13/91
11/12
2-1. 6
62 6
142
01/14/91
A
22 6
65 3
143
01/15/01
A
20.9
70.8
144
01/15/01
11/12
22 1
67.4
145
01/16/91
A
18.8
70. 7
14G
01/17/01
A
20.5
69.8
147
01/17/91
11/12
25.7
58 9
148
01/18/91
A
22.2
66 2
149
01/19/91
A
19 4
68 1
1 IjO
01/19/91
11/12
24 .5
50 3
VjI
01/2O/91
A
22 8
65 1
152
01/20/91
11/12
27 3
58 fi
153
01/21/31
A
20 3
69.9
154
01/22/01
A
24.5
61 .2
155
01/22/91
11/12
22.4
66.4
15G
01/23/91
A
23 . 1
63.6
157
01/24/91
A
22 .4
68. b
158
01/24/91
11/12
24 .3
60. 8
159
01/25/91
A
25.3
60. a

-------
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-------
HAMPTON ROADS LABS COKE DATA. 11/12 BATTERltS 5 A BATTERY 11:30 Wednesday, April 1, 199? 19
KIDC DEMONS1 HAT I ON PRDJECT - RFTHIFHFM STFFl. CORPORATION
SPARROWS POINT. MARYLAND


CflKF
COKF REACTIVITY
COKE STRENGTH
DBS
DATE
BATTERY
INDEX
AFTER REACTION
'213
02/28/91
11/1?
21 B
66 1
214
03/01/91
A
?3.0
63 3
515
03/02/91
A
22.3
00.7
216
03/02/91
11/12
24.9
62 .3
217
03/03/91
A
20. 7
62.9
216
03/03/91
11/12
?3 4
62 7
219
03/04/91
A
17.9
72 .9
2?0
03/05/91
A
? 1 P
68 . 3
221
03/05/91
~ 1/12
22 0
65 8
222
03/06/91
A
26 . 4
59.0
??3
0.1/07/0 1
A
2 18
66 .0
224
03/07/91
11/12
23.5
66 .3
225
03/08/91
A
20 0
€7 .0
226
03/09/91
A
2 1.3
67 . 3
227
03/09/91
11/12
25 G
61 . 1
228
03/10/91
A
20.9
68 .5
229
03/10/91
1 1/12
23 1
67 2
230
03/11/91
A
?0 9
68.2
231
03/12/91
A
2 12
07.9
232
03/12/91
1 1/ 12
24 6
63.3
233
03/13/91
A
22.0
65.2
234
03/14/91
A
22 .0
66.4
235
03/14/91
1 1/12
24 3
€2 1
236
03/15/91
A
24 .4
64. 1
237
03/16/91
A
2 1.1
68 . 1
238
03/17/91
t 1/12
25 4
r.O 3
73fl
03/22/91
11/12
24.5
04.4
240
03/23/91
1 1/12
24 7
63 .0
24 1
03/26/91
11/12
25.5
61 .5
242
03/28/91
11/12
26.3
59.2
243
03/30/91
1 1/12
25.8
€0.4
244
03/31/91
1 1/12
27 . 1
57 .0
245
O4/02/91
1 1/ 12
28.5
55 8
246
04/04/91
11/1?
26.4
59.2
247
04/06/91
1 1/12
25.0
61.1
248
04/07/91
1 1/12
2G.4
5U. 7
243
04/09/91
1 1/12
26 . 5
60.0
250
04/11/91
11/12
27.2
56 . 9
251
04/13/91
11/12
25.0
62 . 5
252
04/14/91
11/1?
27 . 2
59 0
253
04/16/91
1 1/ 12
27 1
56 8
254
04/ 18/9 1
11/1?
25 5
Oi 2
255
04/20/91
1 1/12
27 8
56.8
250
04/21/91
1 1/12
26 .0
60.6
25 7
04/23/91
1 1/12
25.5
61 .0
258
04/25/91
1 1/12
77 5
5« 1
259
04/27/91
11/12
27 .0
58 9
260
04/30/91
1 1/1?
?6 6
58.3
261
05/02/91
1 1/12
25.8
01.9
202
05/04/9 1
11/12
25 4
fcO. 7
263
05/05/91
11/12
28 0
55.3
264
05/07/91
11/12
2R 7
54 3
265
05/09/91
11/12
30 . G
50.4

-------
HAMPTON ROADS IAR5 COKF OATA, 11/12 BATTERIES & A BATTERY
KIDC OCMOMGTRAI ION PROJECT DETHLEHCM STEEL CORPORATION
SPARROWS POIN1. MARYLAND
11:3U Wednesday, April 1, 1992 20


COKF
COKE REACTIVITY
COKE STRENGTH
OBS
DATE
BATTERY
INDEX
AfTER REACTION
266
OS/1 1/91
11/12
26.5
60 8
267
05/12/91
1 1/1?
27 6
56.8
268
05/14/91
11/12
20.7
58 .6
269
05/16/91
11/12
26 2
62 .0
270
05/10/91
11/12
26 5
60.2
27 1
05/19/91
11/12
28 0
58.3
272
05/21/91
1 1/12
20 2
58.0
273
05/23/91
11/12
2fl 3
57 . 4
274
05/25/91
11/12
27 0
GO 7
275
05/26/91
11/12
30 3
51 .5
276
05/28/91
1 1/12
314
bO. 2
277
05/29/91
11/12
32 .0
48.3
278
06/01/91
11/12
34.4
44 . b
279
06/02/91
11/12
27 2
58 0
280
06/O4/91
1 1/12
29.3
54 2
281
06/04/91
BFTH
21 7
64 3
282
OG/Oh/9 1
BETH
21 .9
G3 8
283
06/C6/9'
11/12
27 . 3
58 . 8
284
06/00/91
11/12
26.8
5G.0
285
06/09/91
11/12
2b 3
62 . b
286
06/11/91
11/12
28. 1
57 0
287
06/1 1/91
KRFSS
26 1
61 4
288
06/13/91
1 1/12
29 1
btt.2
289
06/15/91
11/12
26.8
56 9
290
06/16/91
11/12
26 1
57.9
291
06/18/91
11/12
25.0
G3.G
?9?
06/20/91
1 1/12
26.0
59. G
293
00/22/91
11/12
27 .9
59. 1
294
06/23/91
11/12
29. 7
51 ?
295
06/25/91
1 1/12
25 3
61.2
206
OT./77/9 1
11/12
27 5
56.6
297
06/29/91
11/12
24 .8
63 9
298
06/30/91
11/12
29.O
bb.B
299
07/02/9 1
11/12
26 3
62 2
3O0
07/04/91
11/12
27 7
60 1
301
07/06/91
1 1/ 12
25 3
64 1
30?
07./07/9 1
11/12
27 .4
59 . b
303
07/09/91
11/12
20. G
61 . 9
304
07/1 */91
11/12
2b b
b9. b
305
07/13/91
1 1/1?
?8 .4
56 8
30b
08/14/91
KRFSS
? 7 3
57 1
307
08/15/91
KRFSS
27 2
59 0
308
08/23/91
KRESS
26 9
b9 /
309
08/29/91
KRESS
28.6
bb 7
y 10
09/O1/91
11/12
31 .0
49 6
311
09/02/91
11/1?
26 0
57 8
312
09/OJ/91
11/12
? 7 6
54 . 7
313
09/05/91
11/1?
? 7 q
55 4
314
09/06/91
KRESS
2G 9
59 9
31b
09/07/91
KRFSS
27 9
61.6
3 lf>
09/07/9 1
11/1?
28 3
56 4
317
09/08/91
11/12
25.2
59.7
318
09/ 10/91
1 1/12
25.8
6 1.1

-------
HAMPTON ROADS IARS COKF I1ATA. 11/1? RATTFRIES 8 A BATTERY 11:30 Wednesday, April 1. 1992 21
KIDC DEMONSTRATION PROJECT - BETHLEHCM STEEL CORPORATION
SPARROWS POINT. MAKYLAND


COKE
COKE REACTIVITY
CUKt 51 RfcNGTH
ODS
DATE
BATTERY
INDEX
AFTER RFACTION
319
09/11/91
KHbSS
27 3
59.8
320
09/12/91
KRESS
29.3
55 5
321
09/13/91
11/12
22.7
66.3
327
OH/14/31
11/12
24 6
€3 8
323
09/15/91
1 1/12
31 .3
54.9
324
09/17/91
1 1/12
25.8
59 .8
325
00/21/91
11/12
29.6
51 .0
326
09/22/91
11/12
29.4
53 1
327
09/24/91
11/12
27 3
58 5
328
09/26/91
KRF5S
27 9
57 4
329
09/27/91
11/12
24 5
01 .9
330
09/28/91
11/12
24 3
60 .9
331
09/29/91
11/12
27 4
54 1
332
10/01/91
1 1/12
28 &
•j8 . 7
333
10/02/91
KRESS
28 7
55 2
334
10/03/9 1
KRESS
25 2
60 2
335
10/04/9 I
1 1/12
26 7
59.4
336
10/05/9 1
11/12
27 7
57 . 7
337
10/00/91
11/12
20.0
55 9
3JU
10/07/91
KRESb
29.2
56 . 3
339
10/08/91
11/12
23 4
63 3
340
10/10/91
11/12
24.3
66. 1
34 1
10/11/9 1
1 1/12
26 6
57 3
342
10/12/91
11/12
23.2
65 .6
343
10/13/91
11/12
25.9
58 . 1
344
10/ 1 *j/9 1
11/12
29.6
51 .5
345
10/17/91
11/12
26.6
58 0
346
10/18/91
11/12
27 2
59 1
347
10/20/91
11/12
24 3
65 6
348
10/21/91
11/12
2G.6
C2 7
349
10/25/91
11/12
29 2
55.0
350
10/26/91
11/12
24 3
62 9
351
10/27/91
11/12
25.0
64 .0
352
10/29/91
11/12
24 8
6 19
353
1 1/01/91
11/12

6 1 3
354
1 1/02/91
11/12

61.6
355
1 1/03/91
11/12

59.3
356
1 1/05/91
11/12

59 .0
357
1 1/08/91
11/12

59.8
358
1 1/09/91
11/12

62 . 2
359
11/10/91
11/12

66 6
360
1 1/12/91
1 1/12

66.0
301
1 1/15/91
11/12

60.5
362
11/16/91
11/12

62 5
363
1 1/17/91
11/12

57 5
364
11/19/9 1
11/1?

61.1
365
11/21/91
1 1/12

63.8
366
11/23/91
1 1/12

60.0
367
11/21/91
11/12

64 6
368
11/26/91
1 1/ 12

56 0
369
11/28/9 1
1 1/12

58.4
370
11/30/91
11/12

57 .8

-------
Section 6
KiDC Coke Properties Database
G-62

-------
KIDC COKF PROPFRTIf S FROM DAILY COKE REPORTS. 11 BATTERY t I . 30 Wednesday. April 1 1992 22
KIOC DFMONSTRATZON PROJECT - BETHLEHEM STCCL CORPORATION
SPARROWS POINT. MARYLAND
0
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08/14/91



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08/15/91



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08/23/91



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08/23/91



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09/12/91



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09/20/91



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10/10/91
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10/10/91
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10/10/91
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10/11/91
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10/12/91
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10/12/91
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10/12/91
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10/13/91
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10/13/91
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10/13/91
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10/14/91
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10/14/91
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10/14/91
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10/15/91
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10/ 17/91
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10/18/91
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10/18/91
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10/19/91
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10/19/91
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10/19/91
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10/20/91
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10/20/91
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10/21/91
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10/21/91
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10/22/9 1
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10/22/91
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10/22/91
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10/23/91
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10/23/91
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10/23/91
1 153
1 149
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-------
OBS
54
55
56
57
58
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61
62
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64
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66
67
68
69
70
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72
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74
75
76
77
78
79
80
81
82
8 3
84
85
86
87
88
KIDC COKE PROPtKIlElS V RUM DAILY COKb WEPURIS. 11 BA1TERY 11:30 Wednesday. April 1. 199? 23
KIDC UEMUNSIRATION PKOOFCI - BEIHLEHFM STEEL CORPORATION
SPARROWS POINT, MARYI AND
DATE
0/23/91
0/29/91
0/29/91
0/30/91
0/30/91
0/31/91
0/31/91
0/31/91
1/05/91
1/05/91
l/0b/91
1/OB/9 1
1 /06/91
1/06/9 1
1/07/9 1
1/07/91
1/07/91
1/13/91
1/14/91
1/19/91
1/20/91
1/20/91
1/20/91
1/21/01
1/21/91
1/21/91
1/22/91
1/22/91
1/24/91
1/24/91
1/25/91
1/25/91
1/26/91
1/26/91
1/26/91
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-------
1
2
3
4
5
C
7
8
9
10
1 1
12
13
14
15
16
17
18
19
20
21
22
23
24
25
26
27
28
20
30
31
32
33
34
3b
36
37
38
39
40
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42
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44
45
46
47
48
40
50
51
'j2
53
HAMPTON ROADS I ARS COKF DATA. KIDC QIJFNCHFD COKE
KIDC DEMONSTRATION PROJECT - BETHLEHEM STEEL CORPORATION
SPARROWS POINT. MARYLAND
11:30 Wednesday. April I. 1902 24

OVEN
OVEN
OVEN
COKC REACTIVITY
COKE STRENGTH

DATE
1
7
3
INDEX
ArTER REACTION
COMMENTS
08/14/91



27 3
57 . 1
OVt-NS NO! 1 AREIED
08/15/91



27 2
59 .0
OVFNS NOT IARFIFO
08/23/91



26 9
59 .7
OVFNS NOT LABELED
08/23/01



27 5
58 8
NO OVFNS LISTED
08/29/01



28 6
55 7
NO OVFNS LISTED
09/0G/91



26 9
59.9
OVENS NOT LABELED
oy/of/91



27.9
y 1.0
OVLNS NOT LABfcLtU
09/11/91



27 3
U9.8
OVtNS NU! LABELED
09/12/91



29.3
55.5
OVENS NOT IARFIFD
0^/26/91



27 9
57 4
OVFNS NOT LABELED
10/02/91



20 . 7
55.2
OVENS MOT LABELED
10/03/91



25.2
60.2
UVENS NOT LABtLLU
10/04/91



29.8
48.0
OVENS NOT LABELED
10/07/91



20 2
56 3
OVFNS NOT LARFIFO
10/08/91



24.6
GO.7
KRESS I
10/08/91



22 .4
b7 . 7
KRfcSS ii
10/09/91



26 .9
bB.O
NUS
10/09/91



26 4
58 9
3- 1
10/IO/91



25 . 2
60.3
NOS
10/10/91
1 148
1151
1153
23 G
64 . 1

10/11/91
1 148
1 151

24 .7
02 .0

10/11/91
1 135
1 149
1 17 1
24 5
61 2

10/11/91
11 b'J


23.4
63 . 2

10/12/91
1 13b
1 1'j1
1 1 bl
2b .0
57 . ~

10/12/91
\ 149
1 lb 1
1 1 b3
29 .5
54 .8

10/12/91
1148
1171

2b.8
6 1.4

10/13/91
1 13b
1 148
117 1
25. 1
62. 2

10/14/91
1 149
1 151
1 153
26 0
60 0

10/14/91
1 135
117 1

26.0
60.3

10/14/91
1 134
1 148
1 152
20.8
61.4

10/16/91
1 13b
117 1

28.0
bH.H

10/18/91
1 148
1 1b1
1 153
27 . 2
62.8

10/18/91
1 149
1 1 b2
1 154
25.6
61 .0

10/19/9 1
1 135
1 147
117 1
24 . 3
62 . 9

10/19/91
1 148
1 151
1 153
24.O
61.3

10/IO/01
1 140
1 152

25 3
62 2

10/20/91
1 134
1 154
1 171
25 4
62 1

10/20/91
1 149
1 15?

25 ?
6 1 7

10/21/91
1 135
1 154
117 1
23.4
64 . 4

10/21/91
1 148
1 151
1 153
27 .5
58 5

10/21/91
1 149
1 1b2
1 1 72
24 . 3
K>4 . 1

10/22/91
1135
1 154
1171
24.8
62 S

10/22/91
1 149
1 172

2b. 6
61 .6

10/23/91
1 149
1 153
1 172
24 . 3
62 1

10/23/91
1 135
1 1 b2
1 159
23.3
67 7

10/23/01
1 148
115 1
1 153
23 . 2
66 1

10/23/91



20 2
57 4
NH flTHFI? I Of NT I T Y
10/23/91
1 148
1 151
1171
28.5
5G.G

10/24/91
1 135
1 154
1 171
2b . 4
62 . 2

10/24/91
1 149
1 152
1 172
27.0
59 2

10/24/91
1 148
1 1 b 1
1
27 . 5
59. 5

10/29/91
1 149
1 152

24 6
66. 9

10/20/0 t
1 148
1 1 b 1
1 1 53
25 5
60 8


-------
54
55
b6
57
\)8
5n
60
6 1
62
63
64
C5
CO
67
68
69
70
71
72
73
74
75
76
77
70
79
80
81
82
HAMPTON ROADS LABS COKE DATA. KIDC QUENCHED COKE	11:30 Wednesday, April 1. 1992 25
KIDC DEMONSTRATION PROJECT - BETHLEHEM STEEL CORPORATION
SPARROWS POINT. MARYLAND

OVEN
DVFN
OVFN
COKE REACTIVITY
COKE STRENGTH
DATE
1
2
3
1 NO FX
AM FR KF AC f ION
10/30/91
1 148
1 152
1 153
31 .0
51 . 3
io/3o/m
1 149
1 152
1 172
?4 6
62 .6
10/31/91
1 14Q
1 15 1
1 153
2G 7
60 5
10/31/91
1 135
1 154

25.6
61 .0
10/31/91
117 1


24. 3
61.8
1 l/05/fl1
1 14R
1 lb 1
1 1b3
2b 3
l>8 b
1 1/05/91
1 149
1 152
1 172
25 1
60 .6
1 1/06/91
1 135
1 154

25. 4
66 .0
1 1/06/91
1 141
1 15?
1 17?
23 2
65 6
1 1/06/91
1151
1 17 1

26.9
60 2
1 1/06/91
1148
1 153

23 7
67 3
11/08/91
1 135
1 154
117 1
22 6
66 3
11/13/91
1148
1151
1 153
23.9
62 .2
1 1/14/91



26 0
59 8
1 1/19/91
1 148
1 Hi 1
1 1b3
22 . 4
66 . b
1 1/20/01
1131
1 135
1 154
2? 6
65 0
1 1/20/91
1148
1 151
1 153
22.8
65.6
1 1/21/91
1149
1152
1 172
2G.2
58 8
1 1/21/91
1134
1 130
1 171
24 0
02 . 1
11/21/91
1 14B
1 151
1 153
27 4
b7 . b
t 1/22/91
1 149
1 152
1 172
22 . b
66.4
1 t/23/01
1148
1 15?
1 153
23 0
65 . 2
1 1/24/91
1152
1 154
1 172
24 5
63 5
11/24/91
1149
117 1

23 6
66 . 3
1 l/2b/91
1 171


24 3
6? \
1 l/2!i/91
1149
1 1b2
1 172
24.0
02 . 1
1 1/26/91
1149
1 152
1 172
27 b
59. b
1 1/26/91
1 148
1 15 1
1 153
2'j . 7
61.7
1 1/26/11
1 154


24 6
63 3
CDMMFNTS
NO OVCNS LISTED

-------
Section 7
Consolidation Coal Company Report of Coke Analysis
G-67

-------
I CON SOU
V
Consolidation Coal Company
Research & Development
Library, PA 15129
Cok« Laboratory Report
January 20, 1992
TO:
Alan D. Strauss - Bethlehem Steel
FROM: D. E. Lowenhaupt - Consol RID
SUBJECT: Physical, Chemical, and Reactive Properties
of Cokes Subjected to the Kress Process -
Coke Lab Report No. 4762
The tests you requested for the coke samples representing plant coke
subjected to the Kress process are complete. The data are in the attached
table, and an invoice has been issued to cover these costs. Also in the
invoice are costs for sample preparation and dumping.
0. E. lowenhaupt
cs

-------
TABLE 1
PHYSICAL AMD CKiHICAl PROPERTIES OF THE KRESS COKI SAKPIES
COKE
REGULAR
KRESS
KRESS
KRESS
KRESS
CRESS
BATE
10/28/91
10/28
10/28
10/29
10/29
10/29
TIHE
--
3:20pm
3:40pm
11:30am
12:15pm
12:15pm
CHEMISTRY






M
7.2
1.4
1.1
0.0
0.0
0.0
VM(dry)
1.06
0.94
1.13
0.94
1.21
1.28
FCCdry)
90.20
90.18
90.03
90.13
89.79
89.88
ASH(dry)
8.74
8.88
8.84
B.96
9.00
8.84
S(drv)
0.57
0.58
0.57
0.58
0.58
0.59
COKE SCREEN
ANAtYSlSteim X!
~4"
15.9
6.0
12.6
11.0
7.0
4.4
4X3
44.4
25.3
38.1
34.0
38.0
25.0
3X2
79.1
61.5
74,0
70.7
73.0
67.8
2 X 1.5
91.2
80.6
88.0
8V.8
86.8
84.4
1.5 X 1
85.7
93.0
95.2
97.4
95.0
92.2
1 X .5
97.5
96.9
97.3
98.6
98.0
95.1
-.5
100. u
100.0
100.0
100.0
100.0
100.0
AVERAGE
COKE SIZE
2.9C
2.40
2.75
2.72
2.56
2.41
COKE STABILITY
COKE HARDNESS
60.0
6?. 2
64.0
70.6
63.9
69. a
62.2
66.?
62.7
66.5
62.9
67.4
CXI
CSR
29.1
52.4
24.2
66.8
26.3
62.4
25.4
60.8
26.8
60.8
26.8
59.2
G-69

-------
Appendix H
Blast Furnace Baiwax Model Report
Table of Contents
Sect ion	Page
1	Description of the Primary Facilities (BALWAX) Model.	H-2
2	Report ot KIDC Coke Impact on Blast Furnace Pertormance.	H-5
! 1,-1 j

-------
Section 1
Description of the Primary Facilities (BALWAX) Mod

-------
Bethlehem's Computer Models
Primary Facilities (BALWAX) Model
The Primary Facilities Models (BaLUAX) is a heat and material balance
model for the blase furnace and associated processes: coke plane, sinter plane
and hoc blase stoves.
Tor a given case the key inputs eo che BALWAX nodal are:
o The coses, chemical composition, energy content, moisture level of all
ores, fluxes, coals and other fuels.
o The overall hoe metxl production requirement, che coke oven capacity an
utilization of purchased coke.
o The availability of all coala, ores, revere materials, fluxes except for
the "swing" material required to achieve specified product demand for each
process. Typically these swing materials could be: one coal type for the
coke ovens, one sintering ore fines type for the slater plant, one pellet
type and purchased coke for the blast furnace.
o For each blast furnace, the production, the blast conditions, slag 3/A,
hot aetal silicon, sulfur asd temperature, burden composition and coke
rate. The coke rate assumption is checked is the model via empirical coke
rate coefficients. Either the production rate or the wind rate may be
specified and the other calculated.
for each ease the key outputs from the BALWAX model are:
o Tor each blast furnace, a two stage maas and energy balance is produced
which indicates the quantities, chemical composition and temperature of
the furnace oueputs (hot metal, slag and top gas) and compleces che
specification of required inputs not already specified: ferrous
materials, purchased coke, fluxes, wind race.
•H-3.

-------
o Also, for the blue furnace, detailed heat balances and elemental material
balances and as analysis of coka race changes bassd on coka race
coefficients.
a Far the sinter plane, an overall aaterlal balance presents the required
ore fines and additional flux aeeded to satisfy alncar production and
chealstry (B/A) requireaants.
o The coke plant balances indicate coal, coka, and byproduct streams.
a the quantities, unit casts, and total casts and energy requirements for
each process and for tha overall process are presented on a sumary sheet.
H-4

-------
Section 2
Report of K1DC Coke Impact on Blast Furnace Performance

-------
BETHLEHEM STEEL
Bethlehem, PA
INTEROFFICE CORRESPONDENCE
Research Department
Primary Processes Research
February 3, 1992
ReF:
1004-18
563-691
From: J. J. Poveromo
To:
P. D. Stelts
Subject: PROJECTED BLAST FURNACE BENEFITS FROM COKE PRODUCED IN THE
KRESS INDIRECT COOLING (KIDC) SYSTEM AT SPARROWS POINT.
The KIDC Process otters potential benefits in the areas of environmental control, reduction of
coke breeze and improved coke properties due to dry quenching. The improved coke
properties have been projected as reduced moisture content and increased stability. These
improved coke properties would then project an improvement in blast furnace performance as
outlined in earlier letters on this topic.
The test program of the Kress System has just been completed at Sparrows Point. A
summary of key coke properties, on a daily average basis, comparing coke quenched by
standard methods with coke quenched by the Kress System for the same coke battery, is
attached. This summary was compiled by T. J. Strayer based on sampling and testing
conducted by Sparrows Point, Research and Corporate Environmental personnel.
The key differences between the Kress coke and coke quenched by the standard process,
designated as K6 coke, are that with Kress coke:
•	Coke sizing is adversely affected, with a decrease in +.2" coke of almost 5% and an
increase in coke breeze of 0.7%. This is contrary to expectations; however, Kress
personnel attribute this to the method used in discharging coke from the KIDC cooling
boxes following the coke cooling cycle. Originally the discharged coke was expected to
fall approximately five feet into a specially built receiving hopper that would remain full of
coke. During the trial period. Kress coke was not produced in sufficient quantity to keep
the receiving hopper full. Therefore, the coke discharged from the coaling box had a total
vertical drop of about 20 feet into an empty hopper which may have caused excessive
breakage compared to coke discharged onto the wharf.
•	Coke moisture is reduced by 1%. A reduction in coke moisture was expected with the
Kress dry quenching method
•	Coke stability is increased by 2.4%. This exceeds expectations but it is likely that a
portion of this increase may be attributed to the stabilization effect of the excessive drop
height which caused the adverse change in coke size.

-------
2
Coke reactivity increased by 0.8%; however, the CRI (Coke Reactivity Index) decreased
by 0.9% while the CSR (Coke Strength After Reaction) increased by 1.3%. The changes
in reactivity and CRI are normally expected to be in the same direction since both are
measures of coke reactivity. This contradiction along with the observation that the
standard deviations for all of these measurements exceeds the differences, lead us to
suspect that, as projected, there would be no change in these coke metallurgical
properties.
In addition to the large standard deviation for the coke metallurgical properties we observe the
same for coke sizing and moisture. Given the variability of the attached data and with the
presi.mption that coke sizing would be unaffected after design changes we estimate that the
Kress system would have negligible influence on coke sizing, reactivity and CSR. We
conclude that the Kress system would positively influence coke moisture and coke stability; to
be conservative we will project a 1% increase in coke stability and a moisture reduction of at
least 1%.
The blast furnace process benefit of reduced coke moisture is strongly dependent on overall
blast furnace top temperature level. If the top temperature is already at or near the lower
threshold value, then further increases in coke moisture will further suppress top temperature
and cause insufficiently pre-heated and pre-reduced burden materials to descend in the
. furnace. This will lower the furnace heat level and disturb hot metal quality. These conditions
will require an increase in furnace coke rate to restore stable operation. Based on past
analyses of blast furnace operating data we estimate this effect to be an increase of 7 lbs
coke/NTHM for every 1% increase in coke moisture.
Within Bethlehem Steel, the following coefficients are used tor estimating the benefit of
improved coke stability (ASTM Tumbler Strength):
Change	Decrease in Coke Rate, Increase in Wind Volume,
(%)	(Ibs/NTHM)	(%)
Coke Stability, +1%	5	1
The total increase in productivity would include the impact of operation at a higher wind
volume and also of operation at a lower coke rate. This increase would be calculated with the
Primary Facilities (BALWAX) Computer Model but could be estimated as follows:
Production
Gain, NTHM/d = Old Production x (% Increase in Wind Volume)/100
+ Old Production x (% Decrease in Coke Rate)/100
In order to illustrate the impact of improvements in coke stability ana coke moisture on blast
furnace energy requirements and productivity we have used Bethlehem's Primary Facility
(BALWAX) Computer Model. In the following table we show calculated results for a i%
improvement coke stability and then for an additional improvement with 1% reduction in coke
moisture. The calculations are based on Sparrows Point L furnace with a base production
level of 9000 NTHM/day.
H-7

-------
3
Case	Base	With KIDC Colte
Improved Stability, + 1%
Process Impact of
Reduced Moisture, -1%
Production, NTHM/d
Coke Rate, Ibs/NTHM
Natural Gas Rate, "
Total Fuel Rate, *
Blast,
90C0
660
70
530
9000
955
70
925
9146*
Net BF Gas, available
to plant after
stoves, MMBTU/XTHM	2.704	2.64C
Coke Consumed, MNT/yr	1414	1406
9000
S4S
70
913
9219*
Volume, Ir.c .02, CFM
221161
219935
218218
Natural Gas, CFM
9187
9237
9162
Oxygen Enr. , %
1.0
1.0
1.0
Flame Temperature,F
4000
4000
4000
:cp Gas



Temperature, F
282
278
280
BTU/CF
84.00
83.14
81.88
KCF/NTHK
52.30
52.46
52.00
KKBTC/NTHM
4 .44
4.36
4.26
llast Quantities, Annua
X


Steam, N'T
16620
16528
16399
Wind, MMCF
116338
115693
114790
Gas, MMCF
4886
4659
4821
Oxygen, NT
49062
48790
48409
2.550
1394
The above results are presented for a constant level of hot metal demand so that we could
calculate, (using the annual quantities) the reduction in hot metal cost due to coke rate
reductions with KIDC coke. We have also shown with an * ttie potential increase in hot metal
production due to these coke rate reductions and aiso due to the increased wind volume with
increased coke stability.
We emphasize that the coke rate reduction for reduced coke moisture is dependent upon
base case top temperature, indeed in the example above the base case top temperature of
272 F, in actual practice, would be high enough to drive off any small (e.g. 1-2%) additional
coke moisture and thereby minimize or eliminate the coke rate effect of this increase in coke
moisture. The above results in the final column are presented for illustrative purposes only.
The table above summarizes the key results; the complete of BALWAX output for the constant
level of hot metal demand are attached.
J. J. Poveromo
Research Fellow
JJPxnts
Attachment
cc: RWBouman (w/o Balwax attachments)
DKwasnoski
ADStrauss
RRGreenbaum
APBreen
:	H-8 ¦
TJStrayer (w Balwax attach.)
LMStuart
AGOssman

-------
KRE. 3 COKE DATA IHHOUUH NOVfcMflfcR 26.1901
I
vo ;

*CNf
%ON2*
% THRU 1/2*
MDBTlflE
STABHrtY
HMCNE9S
HEACTTVITY
ca
CSR
SHAntRTtSTCOEFr
kreascokE
l*AN
sn

88.5
Ts
	


	

80 9
¦ - 		

62.8
_25.7
20
21.6
12 2
t.4
89.1
137
2 7
10.4
1.8
11
14
13
1 0
3.S
0 6
N
86
8/
87
88
8S
85
88
92
92
73






















K800KE



2.8
IB
¥<
0 9


26.6"*
69.6:i
— 2 2
0 7
(CAN
SD
34.6
93 2
0.8
OB
89 2
12 9
13
TO
6 3
1 0
2.2
4 1
	N
"UAIA J-HCJM
43
!EPr. octobe
43
^NOVEMBER
43
43
CEDA1A.
43
43
42
35
53
39
- BLAST HIHNJ
	
— - 	

-------
SP PT I KIDC - IMPR STABILITY.MOISTURE
0PERA11NG
SUMMARY
AND FIE AT &
MA1EHIAL BALANCE
fON ICE
1


OI/3 1/97

1 H/NTHM
TON/DAY
TON/YEAR



NATURA1
ANALYSES.
"/.




3G5 OAVO
FE

S 102
Al 203
CAO
MGO
H20
HOT MFTAl PRODUCTION
?ooo
9(K><>
3287873
94 13






RUNNER LOSS 1 1*%
23
10b
38250
94 13






COKE-DRY 89 6%C
84 A
3H 16
1394 150
0 00

3 94
2.19
0 20
0.00
0 LMJ
SHAM
10
45
IG399







(JXYGtN tNH I CHMfcNI
29
133
46409







SLAG
492
22 lb
aoyibi







UttY HUE OUST 30 0%C
1
2
H22
32 CX>

6 60
? RO
3 HO
1 20
0 00
DRY Fill CAKf 35 0%C
()
(>
O
33 OO

6 60
1 70
6 20
2 20
0.00
RUROTN - MfTAI 1 ICS










CAROLPEL ( 31.2*)
999
4494
1G4I773
G3 83

4 Gl
0.31
0 44
0 15
3 OO
SINTER ( CO¦8%)
2200
990O
36 16605
57 50

5 4J
1 .05
7 46
3 40
O 00
GRAVEL
1 1
bO
1BO0J
2 4y

94 70
0 70
0 60
O 30
O OO
BURDEN - FLUX










SINF 1 MX ( lOO 0"/.)
1
t
2427
0 45

1 70
0.33
42 00
13.00
O.OO
INJICHD f Ut L










GAS
CF/NIHM
MCF/OAY
MMCr/YR
CO
C02
H2 H20 N2
UM
C2H6
NAI GAS
14fc6
13198
482 1
0 OO
o
OO (J
» OO 0
OO O 00
9? 00
3 00
~C
o
HUI HI AM
DRY CNR WIND. Cf M
CF/NTHM
OXYGCN.
MUlblURt.
%
GR/cr
1 EMPE RA 1 UKE . DKi F
PRE SSURF
COI n Bt AST .
PSIG
OFG F
PERCENT OPCRATiON
FLAME TEMP. OtG f

HOT
ME 1 AL
SLAG
IOP GAS

TWO'S 1 AGE OAfA
2 182 1B
FE
94 13
S 102
37 2
CO %
2 1.29
E1 ACQ 94 72
349 14
SI
O 60
Al 203
9 1
C02 %
72 15
ETAH2 107 72
22 0
P
0.056
TI02
0 ia
H? %
4 19
HEAT LOSS
a 0
MN
O. '37
CAO
34 7
N2 '/.
cyj. jo
MMUIU/M1N 1.20
22SO
S
0.025
MGO
15 5
C0/C02
O 96

36 O
T 1
O 03
MNO
O 7b
B1U/CF
81 88
HEAT REQUIRED
400
C
4 60
Sill FUR
1 0 1
MCF/NTHM
5? OO
(MMBTU/NTHU)
95 O
TEMP
2770
OTHER
1 50
MMBTU/NTIM
4 2G
ABOVE 77 13.85



B/S
1 349
TEMP DFG F
280
AROVF 180O 1 95
4000
SI
0 B4
0/A
1 080
PCWPOINT r
101


THfORE TICAL
TEMP
2870






Liocnjs
2492



HOT BLAST STOVF OPERATION (2747 HFC, DOME TEMP AT 5 07. FXCESS AIR)
HE A f CONTENI OF BLAST
HEA1 CONTENT DF COLO BLASI
PFQIJtRFO INPUT HFATINT, VAIUF
GASSING RAIL 30 STOVES (
STOVE FUEL ENRICHMENT
0 CFM MAX)
iG2G MBTU/NTHM
260 MBIU/NIHM
1708 M8TU/NTHM
12BI7 MAT Cf/NTHM
12.00 PCI
COKE GAS ENRICHMENT TO STOVES i 540.O BTU/CF) 1538 CF/NTHM
GO109 NAT CTM
96 13 CFM
CARBON (MOl/NTHM)
AT TUYCRES	42:70
ME IAlI 01 OS	1 44
HOT METAL	7.75
rLUC DUST	0.01
bULN LObb	1 it.'J I
TOTAL	67 77
DRY BLAST FURNACE GAS
GENERATED
USED IN STDVFS ( M779 WET CF/NIHM)
available io nrheh departments
5 1995 CF/NTHM
107 15 CF/NTHM
4 17A0 Cf /NHIM
3249ft? CFM
6697 1 CFM
7 5H010 CFM
(%S SI AG )/(%* HM)
BY MASS RAI 40 46
THFORF T I C Al 5A 77
A K BISWAS bU 91
Af <;TnVF FFFICIFNCV IIF AO O %

-------
^P PI L KIOC
imph s ratm 11 y .MuisTuut
SINTf.R Pi ANT OPIRAflONS

NAfUKAL
DRY


- -


- -

1*
NAME
MNT/YR
LB/T SI NT
•/
X H20
101
1 t
p
s
(02
CAROIPFI
14? 8
78 9
1 1
3
OO
1 00
6b
BO
O OIO
4
75
CARCII c
4bb 0
2b 1 b
13 4
0
(X)
» .00
66
. 10
o ooa
4
32
MUR
9O0 0
407 7
26 €
0
OO
0 45
68
18
O 027
O
8 1
T A 7 1 01 T
420 O
232 3
17 4
0
OO
0 70
63
9 1
O 03?
5
88
HAM PAO
650.O
359 5
19. 2
0
00
3 40
63
50
0.055
4
45
SAND
lb 0
B J
0.4
0
OO
0 00
7
40
O.OOO
94
70
MILL SCL
450.0
248 9
13.3
0
00
-5 00
7 1
95
0 OM
1
40
UNI L1 Ml
O O
o V
O.O
0
OO
O 00
O
OO
o ooo
0
00
OL1V1NF
1 to 0
GO 8
3 2
0
00
0 95
3
99
0 011
42
20
*> f l UK (a <»	164 4	00 9	4 9 O.OO	O OO	2! 86	0.450	11.50
PLTRCV	85 S	47 3	3 5 0 00	O OO	41 80	0-H5	1 1 AO
K IMIST	0 7	0 4	O O O.OO	30.00	32.OO	O.OOO	6.60
5INFIUX	432 9	239 4	0 (XJ	43. OO	O 45	O.OOO	1 . JO
COKC HIJ/	189 2	104 .6	/ .OO	9 I 7b	O O	O	3 94
lor FMO	401 b . b	2220 b	O 44	9 04	b2 38	O 043	4.94
URt F M ri	.1998 O	2210 D
I CM I 1 ION	-36 1 '4	199 8
*¦ iri r> i n«.s -?o o	ii«
j INTER 3GI6 ft 2000 0	O OO O 00 b/ b9 O 04 /
SINTFR FFO.	- I. bO
F F 203. %	74 . lO
BASICITY. ICAO+MCO)/S10? = 2 000
STONC FQlJf WAl FNT ( f > , IR/IOO LB "	8 73
DLSULFURIZATJON	• 78 09% = 1305.0 TOMS
(1) STONl LOUlVALtNl =	100 * ASfc OF SINItK / ASt 01 Of FLUX
WHFRF. ASF	CAO.03
0 27
0
73
O.OI
0
0 1
0.003
0 03
O 03
o
97
0 ? »
0
11
0 007
O 04
O 15
1
ft?
0 03
0
05
0.015
0.01
O.OO
o
70
0 GO
0
. :io
O OOO
O.OO
O 66
0
88
0 5G
0
.08
0.010
0.05
O 00
o
OO
too (JO
0
OO
O.OOO
O OO
0 08
0
88
0 88
47
40
0.030
0 01
3 50
1
20
4? OO
6
50
O l?0
0 50
U) 00
2
65
14 80
2
00
0 150
0 15
O.OO
2 .
80
3 50
1
20
O.OOO
O OO
0 OO
0.
33
42. OO
13
00
O (X)3
0.00
O.O
2
19
O . 20
0
O
O 613
O.O
Ob4
O
95
b /9
3
.09
O 04 2
O.Ob
O b9
1
Ob
/ . <16
3
40
0 01O
O Ob

-------
SP PI L KIUC IMPH Si AH I L 1 I Y .Mill SlURt
RFSUITS f)F TWO-STAGF MASS AND HEAT BAl ANCE FOR FCE L
RESULTS BA'jLU ON
PROUULIION 90U0 NIHM/PAY
RUNNER IOSS I 1 >C
CDKf RATF 848 tK/NIHM
NAT GAS	I166 CF/NIHM
DRY W1NO 2 18218	CFM
349 1 4	U/NIUM
OPEHA TION 9b 0	%
UlAST I|MP 2250	DLO I
RIAST H?0 A 0	CR/CF
BLAST 02 22.0	%
TOTAL MUX
St AG VOLUMC
SI AG B/A
B/S
1 LB/NTI#!
492 LU/NIIM
i oao
I 349
FRACTION CAC03 CALC1NE0 ABOVE
EQUILIBRIUM TEMP O.OO %
HF A1 RAIANCES
TUYERE 2ONE
(RTU / IOO MOl S TUYERE GAS)
DRY AIR <2250)	1235269
BLASI H2U (22'jO)	70453
COKE CARBON!3000)	448984
INJECT ANT 1 S}	0
PI AC TIONS AT 77
C ~ 1/2 02 * CO	1571425
H20 - H2 ~ y/'i. 02	• 2 18GU0
I N.lb C I ANH Nl 1 CV)	016*5
IHIAI	3 I !>9 1 I 4
I U«" L HI GAMS
CO ( 4? 7 MniS/NTHM)	1094454
H? ( 10 I MOIS/NTHM)	241469
N? ( 7 I A MOlS/NTllM)	1823179
TOTAI	3159102
HEAT ABOVE 1800 DEG F
IUIU / NII1M)
SFNS1H1F HF A I *	1917798
REACTION MIAT	1G132B3
IIJYLKE GASES A? 1800 1G04726
TOTAL 1946351
rc OX I DCS
M[7 ALL 01D
HOI MtlAt
SLAG
CAC03 ~ <:
MtAI LUSS
RLDUCIION
RCDUCTION
fLAMfc ItMP = 4000 OCG F
~ INCLUDES COKE CARBON AT 180O. DEG F
B9b4 17
143040
bJ24bb
I I] I 4 4 4
O
tvjyys
TOTAL 1946350
HEAT ABOVE 77 DEG	F
I SLAG	332078
LHLM ENERGY OF C IN HM	131181/
CULM LNLRGY Of C IN ID	2114
CHEM ENERGY OF DRY TG	4257610
SFNS & IAI HI (IF DRY FT.	2 15531
SFNS & IAI HT OF TG H20	19G439
HEAT LOSS	191993
TOTAi.	13854717

-------
SP PT L K1I)C - 1MPR SIAHIl I TY .M0IS1URE
HtbUllh Ul IWU STAtit MASS AND HI-AI BAL ANCL F OR fCfc L
Fl (MENTAL MATEfMAI RAtANCF (()
Mf ! Al I ICS
CAPO I I'tL
SINIE R
GRAVE I
NA tural
IONb/YW
IG4 1773
3010005
laoa-j
NATURAL %
l.H/NTIlM H20
F E
S 1 02 AL2U3
TONS / YEAR
CAD MGO
MN
099 J O 1047H7A 75645
2 200 O O 2002650 19G320
11 OO	434 1712b
b096 7 166 238') 2070 111	iby UbG
37022 269799 122859 2I1S2 364 1701 1918
127 U)B	04	O	0	O	O
FlUXES
SINF I UK
COKE (DRY |
2427
1394 150
1
848
1 1
O
4 I
54980
R
30490
1019
2765
:i 16
o
0
6539
3130971 344119 73543 20005ft 125617 23522
jQtJ
i
HUI METAL
320 fU2 J
200O
3094G04
42200(2)


10UO 1
022
1839
PlINNF R IOSS
3B250
23
36003
491(2)


2 16
10
2 1
SLAG
HOB 161
492

301374
73520
280829
1 2b607
<1704
8184
O
I'lUE DUS1
87 2
1
263
54
23
29
10
O
0
O
1ILIER CAKfc
0
0
0
0
0
0
0
0
0
0
TOP At


J »JU9GO
J44 1 19
73543
280858
1256 1/
23522
9015
t860
14 20( 2 )
17(2)
1437
O
O
20 / J
(1)	ANNUAL TONNAGES BASED ON 3fcb DAYS/YR AT 9b.O % OPtNAIlUN
(2)	CIf MFNTAl , RFPORTED AS flXTOE

CARGON
BALANCE (MOL/NIHM)

CHARGED

CONSUMED

COKT
NAT GAS
C3 290
3 807
ntJRNFO AT TUVrurs
OCOUCTION OF METALLOIDS
I10T MCIAL CARBON
F1UC DUST
FILTER CAKE
SOLUUUN LU'jS
4 2 705
1 4 3G
7 ND
0 012
0.000
lb 3/0
101 At
67 1(>J
TOTAL
.212

-------
SP PT L KI DC IMPR STADIL1TV.Mn!STURC
COKF PI ANT OPFRAT IONS

NATtJRAI
NAIlJRAt
ORY
ANAI YSI S


COAL NAML
PERCENT
MNT/YR
VOL MATTFR
SIJI FUR
ASH
S1 02
Ellsdlnd
0 00
0 <)
37 10
1 3 30
6 60
46 60
1OMING
30 40
G8G 4
34 75
0 700
5 50
46 ftO
PURCH HV
4b.bO
1U29.6
3 1 .00
O.OOO
G 2b
49 00
Cambria
16 00
36 1 3
18 50
O OOO
6 AO
46 2<)
PURCH LV
0.00
IftO 6
21 OO
0.710
7 20
47 70
HIGH VOl COAL 30.40
LOW VOL COAL 69.60
TOTAL COAL MIX
225ft.0
TOTAI DRV COAI USED
TOTAL OVCN COKE (DRY OASI^ > (D
COKI PURCHASED
r URNACt COKE
fOKF BRFF7F
COKi BRtEZf IISFP IN SINTERING
NET COKC BRCC7F FOR SAI F
20 35
0 77ft
COKC PRODUCED
2 133 7 MNl/YR
1GOO O MNT/YR
50 9 MNT/YR
139-1 . 1 MNf/YH
1 b4 9 MNT/YR
189 2 MNT/YR
34 2 MNT/YR
ANALYS1 b ."/.
C
SIU2
al2o:i»iio?
CAU + M(»0
S (2)
H2
N2
ASH
MO IS T IJRE
COKC OVtN BY PRODUCTS
COKE OVtN GAS:
TOTAI GFNE-RAT FD (3)
A1R-D11 UTED BASIS (4)
UNOERFIRING (5)
STOVC rilfl ENRICHMENT
AVAILABLE FOR OTHER OFPARTMFNTS
GROSS HCATING VALUE
1AR :
TOTAI GFNFRATFD
USED IN BlAST FURNACE
AVAILABLE FOR SALE
LIGHI OIL PROUUCLU
PRIMARY OIL HKOOUCLO
NAPHTHALENE RECOVERED
AMMONIUM SUL f Alt RLCOVLKtO
ElfMFfJTAI SULFUR RFCOVF RF 0
2446 1
MMCF/YR
23164
MMCF/YK
799B
MMCF/YR
5057
MMCF/YR
IO 109
MMCF/YR
540
GTU/Cr
IOG733
TONS/YR
O
TONS/YR
100733
TONS/YR
R3 IO
MGAL/YR
853
MGAL/yR
0
MGAL/YR
23 13(j
TONS/YR
1334
TONS/YR
(1)	PI ANT CAPAC I IY 1600 MNT RUN OF OVEN COKE PER YR.
(2)	DLSULfURIZATION - 40.09*/. = 6R0H 1 TONS
( J) 11464 SIO CU FT PFR !ON URY COAL CHARGED
(4)	RASfD ON ML ASUKL L) CALORIFIC VA| UE 01 ISIO O U1U/SCt
(5)	IN ADO ITI ON TO A40? MMCF/YR HI AST FURNACF GAS
A! 0 1.88 UIU/SCF TO PROVIDF 7 3hO MMRTII/TON OllY COAI
01/3 1/92
ASH ANAI YSIS
AI2n.1»Tin?	CAO«MGO	1120
35 40	1 HO	G *>0
25.40	3.90	GOO
29 30	1 43	U.OO
26 60	2 50	6 25
15.70	2.75	5.00
26 5 I	2 . 40	5 50
HOME
flf) 64
3.94
2 . 19
O 20
(>6 13
O OO
O 
O.OO
0.00
0 00
o 00
AVERAGE
A3 G4
3 94
2 19
O 20
0 613
O.OO
o 00
0 25
7 00
CUKL UVLN
GAS. DRY
CO
7 IO
C02
2 . IO
H2
52 .80
H>
ft 60
CH4
26 . 10
C2II6
3 1G
GHV	b40 OO BIU/CF
T HEORi I I CAl UNDfcNtlKlNG REQUIRED
BASED ON HEA? RALANCC
2 7G5 MMRTU/TON ORY COAI
9J09• MMCf/YR CUKL OVLN GAS
999 1. MMCF/YR HI AST FURNACF C.AS

-------
SP HI L K1UC 1MPR SIAU1LI IY,MOISTURE
SUMMARY OF- BIAS! FURNACE OPERATIONS
OI/3 1/02
0«L USED.
CAPOI PEL
CAROL C
MRP
T A 7 11>! 1
HAM PAU
SANI>
Milt SCI
OLIVINE
MNT/YR
1611 .8 (31 2%)
0 0 ( 0.0%)
0 0 ( O.0%)
O O < O 0%)
0 0 * 0 0%)
O.O ( 0 0%)
O O ( O 0%)
0 0(00%)
TOIAL ORC
PLANT SINTER
PI ANT REVEKIS
STFFlMAKING SIAil
GRAVEL
siwriUX
DRY LUKE ( 7 O*/• H20)
j DR * MUt DUSI
r 101 MMAI PRO.
LC
l
MNP/YR
NT/DAY
"/
%
¦/.
%
MNI/YK
Sll ln OPE RA I I l)N
y*o o
AO. UlSTMf NFS RD AT 1 Vf
CUKl RATE. LB/TON
WIND RAlt, PCI
TIIFORF r ICAI BASE
OG 0
O oo
SINTER
PI ANI
147 8
455 0
900 0
4 20 0
650 0
lb O
41*0 O
1 10 n
1784 b
4 55 0
900 O
420.0
650 0
15 O
4 SO O
I 10 f)
3 142 8
bS b
164 4
O O
43? 9
189 2
O 7
4784
36 16
85
164
18
4 US
1583
O
ANAl YSIS
5.43
1 . Ob
7 46
3 40
0	O IO
2 000
1	663
3287.d
9000
O.fcOO
O 056
O br.G
0.025
38 2
848
1466
1
492
229703
34914

-------
»
SP PI L KIOC - fMTff.SFAOIL!rv.MUISTUPL
LQMING	686.4
MIRCH HV	1029 6
CAMBRIA	36 I 3
PIJKCH LV	180.6
COKf PI ANT
lOl COKE
PUKCH.CUKt
bO 9
iwo.o
CAROtPtL
gRavci
SINTER
sinflux
r.OKF
MNT/YR LB/NNW
164 f 9
IB t
16 16 6
2.4
<394 r
999
I f
2200
t
048
fCE COKE
NUT COKE
CDKF BR?
V
1394 . 1
o.o
154 g
V
1AR lOO.'f'J
CUG 2a.16*
UNOERfIRI
ru siuvts
FOR SALE
8 .00*
5 Ob •
10.1!~
TO SINT PL F 169
FOR SALE -34
CAHULPEL
CAROL. C
MBR
TAiJUJ1
HAM-PAO
SAND
MJLL SCL
01IVINF
STLMKG S
PI TRFV
FI UUSI
SlNFIUX
COKL BRZ
142 .8
455 .0
900.0
420.0
650 O
IS 0
450.0
1 10
164
Ob
0
A'J'2
189
TOI FEED
SINTFR PLANT
JOT SIN!
B/A 1.66
96 16 6
B/S 2.00
NUT SIN? 1808.3
PEA SINI 1308.3
| NAT GAS
82. |-
	4
•>| BlASf FURNAC€$ |	> Ft DUST 0.74
FN 7 CM 0 00
B f GAS 170.95*
TO STOVES 35
CUKE OVENS B
FUR SALE 127
23*
49'
23 *
Hur
NLf
MfclAL
PROD
RNtf LOSS
SLAG
3326.1
J2B7 0
38 2
809 2
I 'JOOO NIIIM/UAV)
( » >b % Of GROSS>
( 492 L6/NTHM)
IN nil! ION SL*/yR. ALL OTHERS IN MNT/ YR

-------
SP PT I KIOC STUDY - IMPROVE STABILITY
OPERATING SUMMARY ANfl MFAT & MA TIRI ft! KAl ANCt M1K hilt L	1)1/30/92
lo/ntmm ton/day ton/yfar	natupai anai yses. %
305 DAYS	rc	$102 Al 303 CAO	MGO	*1?
HUI ME IAL PRODUCTION
2UOO
yooo
J2G7B33
94 13








runner toss 1 »S%
?n
K>5
38250
94 13








COKE DRY 89 6%C
855
3B4B
1405700
ooo
3
m
7
19
o
50
0 OO
0 00
STEAM
\o
45
16528









OXYGEN enrichment
JO
134
46790









SLAG
4»1
22 IO
007356









PRY FLUE DUST 30 0%C
1
2
022
32 OO
t>
00
2
no
3
50
1 ?o
0 OO
DRY Htl CAKE 3b OttC
0
0
0
33 OO
r.
GO
1
70
6
20
2 . 20
0 OO
BUROfN - METALLIC*












CAROiPEL { 31 2%)
999
4495
164 1856
fcJ BJ
4
6 1
0
3 1
O
4 4
O. 15
~ OO
SINTER ( 68 8*1
2?00
9900
36166 15
57 59
5
43
1
05
7
46
3.40
0 OO
GRAVEL
IO
•lb
164:13
2.4U
94
70
o
70
O
.60
O.JO
0.00
BURDEN - ^UX












SINFLUX < 100 0%l
O
2
655
n 45
1
70
0
33
42
00
13 00
O 00
INJLCllO TULL












GAS i
Lj /Hum
Mf.f/OAV
MMC.F/YR
c.n
CO?
H?
m?ii

N?
CH4
c?nr»
NAI GAS
147B
13302
4859
0.00
0 00
0
00
0 00

0 00
97.00
3 00
mil bias?

MOT
METAL
SI
AG

TOP GAS

TWO-STAGE DATA
DRY tNR WJND, CIM
219935
F E
94. 13
SJ02
37 2
CO
%
21 .63
ETAfn 92 83
C» /NIHM
30 188
s r
O GO
Al 203
9 1
C02
%
2 1 82
t T AH2 *0\i. H'J
OXYGEN, %
7? O
i»
0 056
T 102
0 IB
H2
%
4.24
HEAT LOSS
MOlSlURk, GK/Cl
8 O
MN
0 57
CAO
34 7
N2
%
52 . 32
MMkJlU/MlN I.20
T IMPt HA I URL .DIG T
2 2T.O
S
O 025
MGO
15 5
CO/CO?
0.99

PRFSSUMF PSIC;
3b O
f i
0.03
MNO
0 75
OTU/CF
83. 14
MEAT REQUIRED
cut II m AS! . 1J t G h
42 . 40
(MMtl IU/NIHM)
PERCENT OPERA 1 ION
95 0
TEMP
2770
OTHFR
1 50
MMBTU/NTHM
4 36
AROVF 77 13 97




B/S
1 350
Tf IIP
DEG F
278
ABOVE 1800 1,96
ri AMf TEMP, OFG F
4GQO
Si
0.84
IS/A
1 OOO
OEWPl)INT F
101



THEORETICAL
TEMP
2870








LIQDUS
2493




HUI BLAST STOVE OPERATION (575?) OEG DOME TEMP AT 5 0% EXCESS AIR)
HFAT CONTENT OF BLAST	1639 MGTU/NTmM
HEAT CONTENT DF COI I) BIAS I	262 MBTU/NTHM
REQUIRED INPUT HEATING VALUE *	1721 MiilU/NIHM
GASSING RATE TO STOVFS (	O CFM MAX J 17817 NAI CF/NTHM 80109 NAI CIM
STOVC FUEL ENRICHMENT	I? 00 PCI
COKC r.AS ENRICHMlNl 10 STOVES i 540.0 BIU/CFJI538 CF/NIi
-------
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-------
bP HI L KIOC STUDY 1MPROVC STABILITY
RESULIS UF T WO -ST AGL MASS AND HEAT BALANCE FOR fCf I
fif StM t S BASI L) UN
PKUUUCIi UN
RIINNFR I nc>s
COKE RATI
NAT GAS
yiXJU NIIIM/DAY
! I %
655 LO/NTMM
1478 Cr/NUIM
DRY WIND 2 19935 CfM
3bt B0 Cf/NIHM
OPFRA TION 95 0 %
BLAST 1EMP 2250 DEG F
BLASI M2U BO CJH/CF
Rl AST 02 7? O %
T01AL FLUX
SLAG V(JI UMF
SI AG R/A
6/S
U LU/NUW
49 I I B/NTHM
1 000
1 . 350
FKACIION CAC03 CAICINFO AfifWF
FQUI LIBRIUM TFMP O 00 %
P=
\D
TllYFRf /(INF
IOTU / 100 MOLS TIJYFRF GAS)
DRY AIR (2250)	1735269
ULAbl H2U (2250)	70453
COKF CARBON( 3000)	448984
INJECTANHS)	O
KLAC I IUNb A! 77
C 1/2 ()? CO	lii/142'j
H20 - H2 ~ 1/2 02	-216600
I N.JF C 1 AN 1 ( Nt- I CV)	blbbb
TOT Al	31591 14
TUYERE GASES
CO I 43.O MULb/NTllM)	1094454
H2 ( 10 I MUIS/N1HM)	2414b9
N2 i 72 3 MHl S/NTHM)	1823179
IOTAL	3159102
FLAMC TEMP » 4000 OCG T
HFAI
HAIANCF S


HFA1 ABOVE
IBOO DEG F
HF AI AROVF 77 DFG 1
F
(RTti /
NTHMJ

(ATM / NJIHM)

SENSIBI F HfAT'

1932R79
SFNSIBl E HEAT
16385183
REACT ION HF AT

1646 126
CHFM INFRCY OF COKE
10B03440
IUYIHI GASLS Al
IBOO
lb 1734b
CMLM INLNGY 01 AUX IULL
1525726

TOTAL
19ft 1660
TOTAL
139G0149
FE OXIDES REDUCTION
910742
FE OXIDES REDUCTION
5681055
MEIALLOID RLDUC11UN
143039
ML 1AILUIO RLUUC1ION
220420
HOT MFTAl

632456
C03 DFCOMPOS ITI ON
290
SI AG

131430
SFNS & I AT HT OF HM
1244674
C.AC03 • c - C AO
» ?r.o
O
SFNS & 1 AT HT OF SI AG
nmciG
HI AT LOSS

143994
CULM ENERGY Or C IN HM
131 1817



CHEM ENERGY OF C IN FD
2 114



CHFM FNFRGY OF DRY TG
4361677



SENS 8 LAT HT OF DRY TG
215055



SINS 6 LAI HI Ul Iti H2U
20/44O



HEAT LOSS
191992

TOTAL
196 1660
TOTAL
13968 148
• INCLUDES COKE CARBON AT IBOO DEG F

-------
SP PT I KIDC STUDY IMPROVE STARIIITV
RE5UL15 Of TWO-SfAGE MASS AND HE AT BALANCE FOP FCE L
ELEMENTAL MATERIAL BALANCE 11)
NATURAL NATURAL
IONS / YEAH
I
to
O

TONVYR
1R/N1NM
H20
FE
S 102
Al 203
CAO
mco
MN
S
r»
TI02
Mb r A1 1 ICS












CAROIPEL
1041856
999
3 O
1047931
75649
509G
7 1G7
2369
2070
1 1 1
159
956
SINTFR
36 166 lb
2 200
o o
208265 1
196331
37822
26980Y
122857
2 1451
361
!7<>l
1918
GRAVEL
IR439
1()
0 0
395
15568
1 15
99
49
0
0
0
0
TLUXFS












S1NF LU*
655
0
o o
3
1 1
2
275
85
0
0
0
0
COKE (DRY)
14O5700
855

0
5541fi
30743
2788
0
o
86 lO


TOTAL



3130978
342994
7 37 78
280135
125380
2352 1
0086
IRGO
2871
HOI MtlAL
328 /833
2 (XX)

J094 IK}J
42200U)


10U01
822
1839
1420(2)
R* INNER 1 OSS
38250
21

36003
491(2)


7 16
10
2 1
17(2)
SLAG
80735G
401


30024*1
7375b
280106
125370
4704
8254
0
4437
FLUL DUSI
822
1

203
54
23
20
10
0
0
0
0
F II TFP CAKF
()
O

0
0
0
0
O
CI
0
0
0
3130973 3-12991 737Y8 280135 125380 23021
(1) ANNUAL I0NNAGES OASCU UN 3G5 DAYS/YR AT 9b O % OPERATION
(7) ELEMENTAL. KEPORItU AS OXIOE

CARBON
BALANCE (M0L/NII1M)

CHARGED

COfrJSlJMFD

COKF
63 A?0
RIJRNED AT TUYERES
4 3 04 1
NAT GAS
3 837
REDUCTION OF METALLOIDS
1 . 436


140 T ML 1 AL CAR80N
7 . 749


FLUE OUST
0 012


HMER CAKE
0.000


SOLUTION LOSS
15 ^89
IOTA!
6/ t>57
101 AL
67 827

-------
SP PI t KIDC STUDY
IMPROVfc STABILITY
CGKL PLANT OPERATIONS
COAL NAME
NAIIIRAI
PTRCFNT
NA1UWAI
MNT/YR
. URY ANALYSIS
MAMtK Sill F OR
sin?
CLLSQIND
LOMING
PURCM HV
CAUBRIA
PURCM IV
O 00
30 40
45.60
16 OO
b oo
o o
6A6 4
1029 6
36 1.3
I BO C
37 IO
31 75
31 00
18 SO
2 I 00
i	:i:io
O	700
O	ft 00
O	900
O	710
6 60
5 50
>5
BO
20
4 6 HO
46 AO
49 00
46	20
47	70
HIGH VOI f.OAl
LOW VOL COAL
30 40
69 00
T01 AI COAL MIX
4 7 0O
COKfc PRODUCED
X
ro
TFITAI DRY COAl IJSFD
2 133
7
MNT/YR
ANALYSIS.%
TOT Al OVFN COKE (DRY KASISI 111
1600
0
MNI/YR
C
COKF PURCHASED
-3B
1
MNI/YR
S 102
rtlRNACt COKF
1405
7
MNT/YR
Al203+T102
LUKL URLC2E
i*r>
7
MNT/YR
C AO+MGf)




S (2)
COKF BREFZF IJSFD IN S1NIERING
191
2
MNT/YR
H2
NCT COKE OREC ?F FOR SAl F
-35
0
MNI/YR
N2
ASH
MOISTURE
COKE OVEN BY-PRODUCTS
COKfc OVEN GAS .
TOT Al GFNF RA11-0 131
AIR DILUTFO RAS1S (4)
UNOFRF I RING (5)
srovr riiri fnrichmfnt
AVAILABLE FOR OTHFR DEPARTMENTS
GROSS HFATING VALIJF
IAR .
TOTAL GENERATED
USfcL) IN BLAST TURNACE
AVAILABLE FOR SALE
I 1CHT OIL PROIHICMI
PRIMARY OIL PRODUCE 0
NAPHTHALENE RECOVfRH)
AMMONIUM SULFATE RECOVE RED
ELLMtNIAL SULIUH RLCOVERIO
21461	MMCF/YR
73 164	MMCF/YR
79B1	MMCF/YR
5057	MMCF/YR
10126	MMCF/YR
540	BTU/CF
100733	TONS/YR
O	IONS/YR
100733	IONS/YR
b'JIO	MGAL/YH
R53	MGAl/YR
O	MGAI /YR
23 136	TONS/YR
1JJ4	IONS/yR
<1) Pi ANT CAPACITY - I GOO MNI RUN OF OVLN COKt PL H YR
4^) OCSIII rilRl ?AT ION - 40 WJL = GfiOfl » TONS
4 3> 11464 StD CU FT PER TON DRY COAL CHARGED
(4> 0 A b C D ON MFASURFH CAlORIFIC VAl UF Ol S40 O BIU/SCF
<5* IN AUDI HON TO 0474 MMCF/YP RL AST FURNACE GAS
Al 63.14 BIU/SCF 10 PROVlOf 2.350 MMOTU/TON DRY COAL
O1/30/92
ASH ANALYSIS .
Al?03*nn?	CAO + MC.O	M20
2b 40	3 90	6.bO
?5 40	3 no	n oo
20 30 r43	5 00
?C, GO	2.50	G.aS
15 70	2.7b	5 00
5 RO
HOMF
PURCM
AVERAGE
89 . 64
o OO
89 64
3 <14
0 OO
3 94
2 19
o.oo
2 19
O 20
o oo
O 20
O.6 13
o.ooo
0.613
O 00
0 00
0 00
o OO
o.oo
o. oo
8 25
o.oo
8 25
0.00
o.oo
8.00
COKE OVEN	GAS. ORY %
CO	7 10
CO?	2 10
H2	52. AO
N?	B.GO
CM4	2C 10
C2H6	J . lb
GUV	54000 ttlU/Cf
THEORETICAL UNDERHR1NG RCQUIRFO
RASFD ON Hf AT HAl ANCF
? 764 UMBTIJ/TON DRV COAL
83H7 MMCF/YR l.UKf OVLN GAS
aoca UMCF/YR riAST furnace gas

-------
SP PI I K1UC SIUDY (MPROVt STABILITY	SUMMARY OF dLASI FURNACE GPkWAIIONS	01/30/9?


SINTFR

FURNACE
I
PLANT
TOTAL
OWF IJSFI), MNI/VW



CARCJl PEL
1641.9 (31.2%)
14? A
17R4 6
caroi r
0 0 1 r> o%)
455 0
455 O
MOP
0.0 ( 0 0%)
900.0
90O.0
IftilUI1
o o ( 0.0%)
420.0
420.O
MAM-PAO
O 0 ( O.OTL)
650 0
650 0
SAND
o o ( o. o%)
15.0
15 0
MIL! SCI
0 0(00%)
450 0
450 O
OLIVINE
o o ( o.o%>
1 10 O
1 10.O
TOT Al ORF
164 ! 0
1 14? R
47R4 6
PLANT SINTFR
3616 6 (68.8%)

3G16.G
PLAN! RCVLRTS

B'j 'j
Bb . *j
S1FFI MAKING SLAG
O 0 ( 0.0%)
164 4
164 . 4
GRAVFI
16.4, 10.0#/T
0 o
16 4
S1NFI IJX
0.7
432 9
433 6
DRY COKE ( 0 0% H70)
1405 7
191 7
159G 9
DRV FLUE DUST
0 0. 0.5#/T
0.7
OB
Htll MFIAl PKU. HNI/VR
32B8

328/ 8
N f/DAY
90CX)

9000
'ill ICON, %
0 60O

0 COO
PMUSPnORUS. %
0 05G

0.056
MAN(»ANfc SI . %
U 57

0 566
SIJIFUR. %
0 025

0 0?!S
RUNNER LOSS. MNT/YR
38 2

38 2
(JOKL KAIL. Lb/NTHM
655

855
NAT CAS CF/NTMM
1478

1477
ELUX RATE. LB/NTHM
0

0
SLAli VULUME. LB/NTHM
4H 1
ANALYSIS
49 1
S102. %
37 19
5 43

A1203, %
9 14
1 or>

CAO. %
.14 6ft
7 46

MGO. %
15.53
3.40

S. %
1 022
O.OIO
1 . 022
fi/S
1 . 3i;0
2 OOO

D/A
1 OBO
1 683

OPV ENR WIND. CFM
231511

7115 11
r.r/MTHM 35 1 flft

35iaa
1LMPLKAIURE. DEC F
2250


MOISTURE. Gfi/CF
0 O


UKVGLN. V.
77 n


(IXY(>LN AUUfeU. CFM
2 199


FLAME 1 IMP. UfcG F
4000


TOP CAS TFMF'FRATURf . OEG F 278


CARBON UTIL ETACO. %
0? fin


HYUKOOIN Ul 1 L LTAII2 .
*05 01


UPtPAl iNli days
Jb5

3b0
pci opfration
9b 0


AU JU'j 1MLNI RELATIVE TO A T HLORL T IC AL BASF
COKF RATE. IR/TON	•06 0
WIND RATF. PCT	0 00

-------
LOMING
PURCH HV
CAMBRIA
PURCH LV
686 4
1029 6
361.3
I8O.0
SP PI I KIDC SIUDY - IMPROVE STABILITY
TOT COAL 2258 0
I
V
COKF PLANT
IWT/YR Lfe/MTHM
CAROLPEL
GRAVEI
SINTER
SINFLUX
COKE
164 1
16
3fi Iff
0
1405
999
IQ
2200
O
855
PURCH COKE
•38 I - -
IAR
COG
FCt CUKC
NUT COKE
COKF RR2
TO SJNT PLT
FOR SALL
V
1405 7
O O
156 2
191
35
V
100 73
23 16*
UNUtRfIRE
TO STOVES
FOR SAl E
7 96»
b U6»
10 13*
CAROLPCL
142 8
CAROI C
4 Sili 0
MBR
900.0
T A 7 10 I T
420 0
MAM PAO
G50 0
SAND
15.0
MILL SCL
450 0
01IVINF
no o
STLMKG S
164 4
PLTREV
85 . 5
FL UUSI
00
SINFLUX
432 9
COKE BRZ
191.2
TOT FEED
S1NIEH PLANT
101 S1N1
R/A 1 66
J6 16.6
B/S 2 00
NUT
PEA
S INT
SIN?
I SOfl
1806
| NAT GAS
. 86 ~ |
>| OLAST FURNACES |-
FI OUST 0.74
rILT CK o 00
B . F GAS 172.49*
TO STOVES 3b
COKF HVFNS R
TOR SALE 128
23*
47*
7B*
MOT MFTA1
NET PROO
KNR LOSS
SI AG
3326
328 /
38
807
BOOH NIHM/UAYj
!IS % OF C.ROSS)
491 L8/NTIIM)
IN BILLION SCf/vR. AIL OTHfRS IN MNt/YR

-------
SP PT L K1 l)C S1UUY BASt CASE
0PLWA1ING 'jllMMARY
AND IIF A 1 ft MA
1 FR1 Al HAl ANCF F ON
! FC.F 1



0 1/30/92
1 B/NIHM
MJN/OAY
HIN/YFAR


NATilRAI ANAE VStS.
%



365 DAYS
FF SIO?

Al 203
CAO
MGO
1170
HOI MFTAI PRODUCTION 2 (XX)
9000
328/B20
94
13





RIINNFR I OSS 1 1 57. 23
105
38250
94
1 3





COKF-DRY 89 6VS. R60
38/0
14 13862
0.
00 3 94

2 . 19
0 20
0 OO
0 00
SVFAM 10
4 5
16620







OKYGFN INRICHMFMT 30
134
19062







SLAG 492
22 1J
808496







DRY FlUE OUST GO.O'/.C 1
2
822
32
OO 6 60

2 80
3 50
1 . 20
0 00
DRY F11T CAKF 35 0%C 0
0
0
33
OO 6.60

1 . 70
6 20
2. 20
0 00
BUROEN - MF FA1 LJCS









carolpii ( 3i 7%) nnn
4494
1641838
63 .
83 4 6 1

0 3 1
O 44
O 15
3 OO
SINTER ( GO.8%) 2200
<>f>00
3616601
57
59 5 43

1 Oh
7 46
3 40
0 00
GHAVLl 10
45
16433
2
40 94 70

0 70
0 r>0
0 30
0.00
BURDEN - MUX









S INF I OX ( 1 0% 1 1
5
1651
0
45 1 70

0 33
42 00
13.OO
0 00
INiltClLU FUtL









GAS CF/NIIIM
MCF/IMY
MMCF/YK
CO
CU2
112
H20
N2
CH4
C2I16
NAT GAS I486
1.WB
4RA6
OOO 0 00 0 OO 0 00 OOO
97 OO
n oo
HUl BIAS I
MOT MFTAI
SI AG
TOP GAS

TWO-
STAGE DATA
CHV ENK VINll. CIM 221161
TE 94 13
SI02
37 2
CO %

21 8G
tTACO
91
51
CF/NTfrM 353 84
SI O bU
Al JOJ
9 1
l02 y.

2 1 59
L 1 Al 12
104
51
OXYGFN, % 22 O
P 0 Obb
1 102
0 18
H2 %

4 2 7
HEAT
LOSS

MOISTURF. GR/CF BO
MN 0 5 t
C AO
34 7
N2

52.2/
MMUI
U/MIN 1.
20
TFMPFRATIJRF .DIG F 2250
S 0 02b
MGO
15. 5
C0/C02

1.01



PRC5SURE PS 1G 1G 0
11 0 03
MNO
0 7b
BTU/CF

84 OO
Ht A
1 REQUIRED
COLD BLAST. DFG F 400
C 4 60
SULFUR
1 03
MCI /NHM

52 80
(MHf'O/NIHM)

PFRCFNT OPERATION 9S.O
TEMP 2770
U1HER
1 50
MMltlll/NIF
W
4 44
ABOVL
7 7 11
05


B/S
1 35 1
TFMP DFG
r
282
ABOVE
1800 1
97
FlAME TEMP. DtG F 4000
SI 0 83
b/a
1 OHO
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1731	MBTU/NTHM
12B2Q	NAT Or/NTHM
12 00 PCT
COKF GAS INRICHMtfJI 10 S10VES ( 540.0 UTU/CFM530 Cf/NTMM
80126 NAT CFM
CARBON (Mfll /MTHU)
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BLAST IURNACE GAS
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USEIJ IN SIOVCS < 1 1?B I UCT CF /NTHM \
AVAJLAULE 10 OIHER DEPARTMENTS
52799 CF/NTHM
107 17 CF/NTHM
42082 Cf/NTHM
3JOOOV CFM
66985 CFM
263022 CFM
<7.b SLA6)/(/.S MM)
BY MASS BAL 41 09
IHtUKfcIICAL 58 35
A K BISWAS €9 21
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o
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to
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tn
(0
-J
BO
5>
20
9
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CD
CD
c
a>
to
o
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CJ
SJ
u
•o

ff! O ^
— a
U U Ki
oSocoooo
3>
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.20
79
00
ftO
50
»5J1ffOMOA
o
o
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Q CJ
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o o
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icoco
c
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i. b o L b

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o
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-

o
o
0
0
0
0
o
o c
—,
C O O C O
o
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to
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b c 3 8 ^
c
•J
o c
O CO OOd 0ooccoooo-
o oo O-u codccooooc
lp o O y> o	juckj

-------
SP PT I Kinc STUDY - BASE CASfc
ri suits Of two stac.f mass ano heat baian<;f for fcf i
WtSlJIIS BASEE) ON
PRODUCTION	900D NIHM/DAY
RUNNtH LOSS	I I /.
r.OKF RATF	060 I B/NTtIM
NAT OAS	I486 CF/NtHM
DRY WIND 22 1101 CrM
3'jJBI Cl/NOW
OPERATION 9b O t
Hi AST 1 tMP 22bO UbG F
BLAST H20 8 O GH/CF
Ul AST 02 22 O %
IOIAL >LUX
SLAG VULUHL
SLAG B/A
B/S
1 IR/Nlf
492 I H/NIF
I 000
1 .3b I
ItfAC 11 ON CAC03 CALCINED ABOVE
EQUILIBRIUM IEMP 0.00 %



H€AT
HALANCFS



1UYIWL /UNl

hf a r Annvr
1600 DCu F
MfAf AROVr 77 OCT, l
1
(HTU
/ 100 MOlS TUYERE GAS)
(RTll /
NTHM)

(BTU / NTI
-------
SP PI I KIOC STUDY - BASF CASE
RESULTS OF TWO-STAGE MASS AND HEAT BALANCE FOR FCI L




ELEMENTAL
MATERIA!
BAI ANCE ( 1 )







NATURAL
NATURAI
%



TONS /
VF AR






TONS/VR
1 G/NTHM
1120
Ft
S102 Al 203
CAO
MCO
MN
S
V
r iu2

MET Al I ICS













CAHOLPEL
1b4 1838
999
3 0
1047920
?Wi48
b096
7 lb /
2389
207O
1 1 1
159
956

SINTER
3616601
2200
0 0
2082649
19632ft
37822
269798
122059
2 1452
364
1701
vj 10

r.PAVFL
16439
10
O 0
395
15568
1 IfS
99
49
0
0
0
0

FLUXES













S1NH UX
Ibb 1
1
o.o
7
28
b
693
? 1 b
O
0
0
0

COKE (ORY)
14 11)862
860

O
5b7b8
30922
2BOb
0
0
8660



1UTAL



3 1JU9 70
J43329
rjnK* o
2ttOb&I
12bb 12
231)22
9136
I860
2R73

HUI Hi 1AL
328/820
2OU0

3094<>yb
42200(2>


iuoo i
822
1839
14 20<

RUNNER in^S
38250


36003
491(7)


? 16
10
21


SI AG
808496
49?


3O0584
73937
?8053?
125502
4 704
8304
0
143/
\
F1UF OUSI
fl?2
1

261
04
2 3
29
io
O
0
0
0
j
F II TFR CAKfr
0
0

O
0
O
0
0
0
0
0
0
1
TOTAI



313096?
343329
7 3960
280561
1255 1 \
23522
9 I3G
I860
2873
-J
(I) ANNUAL TONNAGFS BASED ON 3C.S DAYS/YR AT 95.0 X OPFRATION
12) ELEMENTAL. RCPORTED AS OXIDI
CARBON BALANCE (MOL/NTHM)
CHARGED	CONSUMED
CUKL 61191 BURNED Al IUYEKLS	43 281
NAT GAS 3.8b8 REDUCTION OF MtlAIIOIOS 1436
HOI ML I AL CARBON	7 749
FLUE OUST	0 01?
F 11 TER CAKE	0 000
SOLUTION LOSS	15 742
TOTAL
b8 049
TOTAL
69 220

-------
SP PI L KI DC SIUOY - HAS* CASF




CUKfr PIANI
OPERATIUNS


NAIURAL
NAIURAL
DRY
ANALYSIS



COAL NAME
PtPCENI
MNI/YR
VUL MAI ICR
SULFUR
ASM
SI
IU2
ELLSBLND
o.oo
0 0
37 . 10
1 330
6 60
4G
ao
L0M1NG
30.40
<>OG . 4
34 . 75
0. 700
5 SO
4G
BO
PIHICH HV
45 GO
1029.6
3 1 00
O BOO
6 25
49
oo
CAMBRIA
16.00
36 13
18 . bO
O.WX)
6 80
46
20
PURCH LV
8 OO
10O.6
2 1 .OO
0.710
7 . 20
4 7
70
HIGH VOL COAL 10 40






IOW V01 COAI 69.60






TOTAL COAL
MIX
225B 0
29 35
0 778
6 19
4 7
80
CUKE PRODUCEO
ANALYSIS.%
C
SI 02
ai ?u:im 10?
CAO+MGO
S (2)
H2
N2
ASH
M0IST1JRF
COKE OVEN BY-PRODUCTS
COKE UVfcN GAS.
TOTAI GENERA I CO (J)
AIR -f>| I IJT FD RASI<; H)
UNOLRf]RING (5)
STOVE fUfL ENRICHMENT
AVAILABLE FOR OTIICP DEPARTMENTS
GROSS HEATING VALUE
1 AR.
1UIAL GENtRAlEO
USH) IN HI AST FURNACE
avaiiAnt f rnp sair
LIGHT OIL PRODUCED
PRIMARY OIL PRUUUCLD
NAPHTHAlENF RECOVEREO
AMMONIUM Sill FATF RFCOVFRFD
ELEMENTAL SULFUR RCCOVCRLD
(1)	PLANT CAPACITY =• 1600 MNT RUN Ul OVtN
(2)	UL SULt UR 1IA I I UN - 40.99* =- 6008 1 IONS
(3)	I 1464 STD CM FT PFR TON DRY COAI CHARCFO
(4)	RASED ON MFASURFD CAIORIFIC VALUE OF 540 0 BTIJ/SCF

1UNS/YH
1007 3.1
10NS/YR
5310
MGAL/YR
853
MGAL/YR
O
MCAI/YR
23136
TONS/YR
1334
TONS/YR
:uke PIR
YR
O1/30/92
ASH ANALYSIS
AL201MTICJ2	CAO ~ MliU	1120
25.40	3 00	G 50
25 lO	3 *JO	6 OO
29 JO	1.43	b . 00
26.60	2.50	6.25
lb.ro	2.	b .00
5 50
HOME
PURCH
AVERAGE
89 .64
0.00
89 .64
3 . 94
0 00
3 94
7 19
0.00
2 19
0 20
0 OO
0 20
0 G 1 3
0 000
0 6 13
0 00
0 00
0 00
0.00
o.oo
0 OO
fl 25
o oo
fl 25
fl 00
0 00
8 00
COKE OVEN GAS. DRY %
co	r io
CO2	2 10
112	52 80
N2	0 CO
CI 14	26 IO
C2HC	3 10
GHV	540 00 BIU/CF
fHIURfr IK.AL UNULRI IR I NG REUUlREU
BASED UN HI A J UALANCt
2 7C,4 MMRTU/TON DRY COAI
9117 2 MMfF/YR CDKF OVFN CAS
91152 MMCI/vR HI AS I f UKNAi. L GA'j

-------
SP PT L KIDC STUDY - BASF CASE
SUMMARY Of HLASI f URNACE OPERAIIUNS
01/30/92


SINTER

rURNACt
I
PtANl
rciiAL
ORE USFD, MNI/VR



cahoi rfi
1641 8 (31 2%)
142 0
1 /B4.I>
c AllOt C
O.O ( o o%i
4D!> a
4bl». O
«0R
0 0 ( 0.0% J
MOO O
aoo.o
1A21D1T
O.O { 0.0%)
420 O
420.0
HAM PAO
a o ( ao%)
650.0
650 O
!>ANU
0 0 i 0 0%)
1?> 0
1fi O
MILL bCL
0 0 ( 0 0%J
450.0
4 f>0 O
01 1V 1 ML
0 O ( 0 0%)
1 IO o
1 10 o
10! *t- ORE
164 1 H
3142 8
4784 6
PI. AN I SINfCR
3616 6 (6B 11*4)

36 16 6
PLANT reverts

85 5
85 5
SI El I WAKING St AG
0.0 ( 0 0%)
164 4
164 4
GRAVLL
1G 4, 10 Oi/T
o n
16 4
SlNft-UX
1 7
4jj e
434 6
prv coke ( a o% ii20)
14 13 fl
191 2
l€Ob 1
or* flue dust
o a, o s*/i
o /
0 8
nor mtM pm, mmi/vs
J2BB

3287 8
HI/DAY
90CXJ

9000
SI 1 ICON. *
<1 €

O. OOO
PHOSPIHJOOS. %
0 056

0.056
MANGANESE. %
O 57


¦>ui i OH . "A
O O'/S

0.025
RtlNNtH IU*S. MNl/YR
38. 2

3ft 2
COKE RAIL. LB/NIHM
800

AGO
NAT GAS CI /NIHM
14 Bfa

Hftfi
FLUX RATE. Lti/NIHM
1

1
SI AU VOLUME. LB/Nf HM
4 {#2
ANAi V5IS
4D2
SIC12 , 7.
37 . 18
5 43

AL203, %
9. 11
1 .05

CAO, %
34. ;o
7 4&

MGO. %
1b 52
:i. 40

5. %
1 027
0 010
1 .028
D/S
t 3S 1
2 0

D/A
1 oao
1 Hb'j

l)«f ENR. WINO, CFM
2321101

232801
CE/NTHW rif%3«4

35384
1LMPfRaTURC. OEG E
2250


M0IS1URC, GR/Cf
8 O


OKfGtN.	%	O
IIXtftSEN AUDIO. CEM	2212
HAME JLMP. OLG E	40OO
10P GAS IEMTLRAIORE. ULG f 202
CARBON UTII ETAtO %	»1 b1
HvnKtHiFN 111 I L E 1 AK2,	104 .'jl
OPERAI IMG DAVS
i*(. f niMRAiiON
9'j O
36S
AlMU'ilMtNtti HtlAIIVfc 10 A H^UkMH.Al HASE
t. t)K I Rflf | , 1 n/ION	ft7 1
wind rah , pcr	o oo

-------
~
LOMING	686 4
PURCM MV	1029 C
CAMBRIA	30 1 J
PURCM I V	180.6
SP PI I KIDC S1UUY - BASl CASE
2256 O
COKE PLANT
I -
PIIWCH COKE
?o o - - -
FCF COKF
NUT COKE
COKE BRZ
1-1 13
0
157
TAR 10O.73
COG 23 16*
llNDERf 1RF
TO SIOVES
fOR SALE
9
0
1
IU SINI PLT 191
FOR SALE -34
MNT/YR IB/NTHM
CAROLPEL 1641 8 909
GRAVEL	16 4	10
SINTER 3616 6 2200
SINFLUX	17' 1
COKE	14 13.9 OGO
7 97*
5 06*
10 14*
CAROLPEL
142
B
CAROL C
45 5
0
MHR
9(X>
o
TAZiniT
4 20
0
HAM PAO
650
0
SANU
lb
o
MILL SCL
450
0
OLIVINE
110
0
STI MKG S
164
4
PLTREV
B5
5
FL OUST
0
8
SINFl IJX
432
9
COKE BRZ
19 1
2
lOT FEED 4017.6
I
V
| SINTER PLANT |
	I
V
IOT SINT 3616.6
R/A 1 Gf» R/S 7 OO
NUT 'J INI lUUD J
PFA SIMT IflOfl 1
| NAT GAS 4.89* |
>| BIAST FURNACES |*
FL UUSI O 14
FIL T CK O .OO
B F GAS 173 S9*
TO STOVES 35 24*
COKE OVENS 8 46*
rUR SALE 129.90*
HOT HETAL
NET PROD
RNH LOSS
SLAG
3126
3267
JO
BOB
9008 NTHM/OAY)
i »s y. or gross >
492 LB/NTHM)
~ IN BILLION SCI/YR. All OTHERS IN MNT/VR

-------
Appendix I
Report of KIDC Operating Costs and Maintenance Requirements
from the Kress Corporation.
1-1

-------
p g ¦ 01
DS
I1AINTEWAMuE COST [~ OR r .IL'i
.MRRiEfc
CHG EUERY

PN.
QTY

PRICE
250
ENGINE OIL FILTERS
oeec24


23. 60


088025


! 4 . RO
250
ENGINE OIL
1 5-40
12 5
Li AL
SB . 68
250
ENGINE FUEL FILTERS
OBS027
2

I 6 . 60
500
ENGINE COOLANT FILTERS
O8R033
t

7. 90
10O
HIGH PSI HYD FILTERS
027602
r>

12B.42
100
LOU PSI HYD FILTERS
085521
9

60.48
500
SUING DRIUE
SAE-40
11.7
GAL .
54.29
500
FRONT LEFT PlANETARY
SAE-40
I 6
GAL.
74 . 24
500
FRONT RIGHT PLANETARY
SAE-40
1 4
GAL.
G4 . 96
500
REAR LEFT PLANETARY
SAE-40
1 6
GAL.
74. 24
" 500
REAR RIGHT PLANETARY
SAE-40
14
GAL.
64.24
100
HYDROSTATIC DRIUE FILTERS
085176
4

I 32.00
AS REG
HYDROSTATIC OIL
039217
105
GAL .
1066.80
AS REQ
HYDRAULIC OIL
j05~3?
450
GAL .
3429.00
100
CAB AIR FILTERS
08 £-03 I
2

: 3. 96
250
ENGINE AIR FILTERS
;1 I 707
1

6 1 . 26
100
GEN. FILTERS
084262
1

5.24
1000
TWIN DISK DRIUE
SAF-30
1
GAL .
4 . 64
AS REQ
COOLING SYSTEPI H20
& ANTIFREEZE
38
GAL .
66. 1 2
AS REQ
FUEL 13 gal per hr (est)
DIESEL
346
GAL .
397.90
AS REQ
GREASE
0G73B7
40
LBS.
151.GO
COST PER 100 HRS	3>	340.10
COST PER 250 HRS	S- 521.24
COST PER 500 HRS	.«	2017.39
COST PER 1000 HRS	4039.42
THE COST LISTED ABOUE DOESN'T INCLUDE THE CC-ST OF HYDRAULIC
OIL OR HYDROSTATIC OIL LOST DURING- FILTER CHANGES OR GREASE
ESTIMATED COST FOR THIS WILL BE.
HYDROSTATIC OIL LOST 2 GAL. AT 10.16 FER GAL.= 	$	20.32
HYDRAULIC OIL LOST 6 GAL. AT 7.62 PER GAL.= 	S	45.72
GREASE EUERY 100 HOURS' 1 0 LBS." .... 				S	37.90
EUERY 100 HOUR FILTER CHANGE	TOTAL *	103.94
PER HOUR AT S 1.15 PER
			 £ ! 495 . 00

-------
pg - 02
DS
fl AII-4TCN ANCE C0£.T F 3R KIDC CARRIER
MAN HOURS TO CHANGE' ENGINE Oil. & FILTERS. ENGINE FUEL FILTERS
ENGINE COOLANT FILTERS. HIGH PST HYD. FILTERS. LOW PST HYD. FILT
ERS, HYDROSTATIC DRK'E FILTERS. CAP AJR FILTERS, ENGINE AIR FI! T
ERS, GEN. FILTERS WOULD TAKE R *!HN HOURS. TO GREASE AMD INSPEf"
THE CARRIER IT - WOULD TAKE 4 C"hN HOURS.
THE LABOR RATE USED IS $ I'^.OO PER MAM HOUR.
OIL AND F ILTER CHANGE 8 X S 25. CO = 	£ 200.0C
GREASE AND INSPECT 4 X $ . 00 = 	£ 100 .00
THE COST FOR ROUTINE MAINTENANCE AND FJEL PER 1 GO HOURS
ON THE KIDC CARRIER IS ^sS FOLLOWS.
$ 4039.42 / 1000 HRS = I 4.04 x ' OC HRS =	S	404.00
OIL LOST AND GREASE PER 100 HP.S	S	103.94
FUEL PER 100 HRS	S	1495.00
LABOR FOR OIL CHANGES AND GREASE	I	200.00
TOTAL J	2302.54
THE COST PER 100 HOURS OF SERUIC.E IS	4	2302.94
THE COST PER t HOUR OF SERVICE IS	£	23.03
(
! J-3 .7
:	i

-------
pa.03	MAINTENANCE COST FUR KiDC CARRIER
DS
THE FOLLOWING ITEMS WERE MAINTAINED FROM OCTOBER 1. 159! TC
NOUEMBER 26, 1991 ON THE KIDC CARRIhR. THESE ITEMS WERE NON
SCHEDULE MAINTENANCE ITEMS.
LABOR RATE USED IS 4 "5.00 PER MAM HOUR.
(01)
" " UIATER SHORTS OUT DIODE UNDER LOUER CAB IT ALSO TOOK
OUT A D/C OUTPUT CARD.
PARTS	$ 305.64
LABOR 2 HOURS	:	S 50. OO
T0TAL $ 355.6-4
02 )
HYDAULIC RETURN LINE A30UE ROTARY JOINT BROKE"AND
LOST 150 GAL. CF HYDAULIC OIL.
HOSE	S 75.00
OIL			$ 1 143.00
LABOR 3 HOURS	S 75.00
TO^AL % 1293.00
C 03)
CLEAN MOOG UALUE
LABOR 1 HOUR 	% 25 . 00
TOTAL S 25.00
C 04 )
REPLACE SEAL IN ROTARV jOINT HYDRAULIC MOTOR.
PARTS.	£ 35.40
LABOR 4 HOURS		£ 100. GO
CHANGED OIL AT THAT time IN SUING DRIUE	S 54.29
TOTAL $ !99 .£9
C 05 )
REPLACE STEERING SELECTOR SWITCH ON DRIUE BOX.
PARTS	£ 50.00
LABOR 1/2 HOUR	£ 12.50
TOTAL S 62.50
C OS)
CLEAN AIR CONDITIONER COILS AND CONDENSERS.
LABOR 1 HOUR X 3 TIMES		$ 75.00
' TOTAL $ 75.00
(07)
CLEAN CABS
LABOR 1 HOUR X 4 TIMES	$ 100. CO
TOTAL 9 100.00
COS)
READJUST PROXIMITY SWITCH FOR F IN ITES, FINE ALIGNMENT AND
AIR INTERLOCK.
LABOR 1 1.'2 HOUR		£ 37.50
'	TOTAL £ 37.50
(09)
CLEAN OUT UIATER TUBES ON TCP OP CARRIER.
LABOR 1/2 HOUR X 10 TIMES				$ " 125.00
TOTAL $ 125.00

-------
pg . 04
DS
MAINTENANCE COST FCR 
-------
MA i NTEN ANC E il'EMS ON CaRR'EP
*	= REGULAR MAINTENANCE ITEMS
*	I. POWER SUPPLIES FAILED J.V LOWER CAB AND UPPER CAB-
¦* z. w-mlt; shouts oi t diodf: on trakf swttc>;f:s uni.:-? : owvr
"A B .
*	.5. HYDRAULIC	RETURN LIN'7. ABOVE ROTARY JOINT LOST ISO :j.A •
OT L .
*	-i . HYDRAULIC	LOW PS I FILTER LINE FAILED — LOST 100 GAL .
7 |
: .	K*':-	f. f M f TS r.:!i GEOThlGN ICS •
1;.	". ''-FOTRC'N I CS jG\'.
»-.k.	ft EP LAC - H iCHl REAP. STEERING MCOC VALVE .
i .': .	-> '.)¦.) A'"'' . ; LATOrf 10 TILT ••' k A M .'• .
.!¦	REPLAt E HYDRAULIC TEMPERATURE GAUGE.
Ml.	REPLACE STEERING SWITCH ON DRIVE 30X.
*16.	REPLACE WINDOW IN UPPER CAB.
*17.	REPLACE WINDOW IN LCWER CAB.
16.	RELOCA!.-; DOOR CLEANER.
*19.	REPLACE FRONT RIGHT HEADLIGHT.
*20.	REPLACE SEAL IN FINE ALIGNMENT CYCLE END.
*2V.	CLEAN MOOG VALVE.
*22.	REPLACE SEAL IN ROTARY JOINT HYDRAULIC MOTOR.
23.	ADD AIR TANK TO SWING FRAME.
' 1-6 __ !
i 3U' \ rin<~\ m r \t rvs - ->c •.

-------
MAINTENANCE ITEMS ON CARRIER (Continued)
HL:'LACL HYDRAULIC SOCT 1V L N ES ON >1A1 N PUMP .
W:l'. STACK IGNITER.
H LI 'I.AC E E STOP.
CLEW AIR CONDITIONERS.
CLEAN C ABS .
REPLACE D/C OUTPUT CARD.
ADD GAUGES TO MAIN H\UKALL1C PUMP.
ADD "LOW METERS IN HYDRAULIC SYVIKM.
fvKi.oc\TE air cannon,
i MANGE OIL, FILTERS, AND GREASE.
REWORK RIGHT REAR CO'JNTER WEIGHT.
READJUST PHOXTMTTY SlvTTCH FOR FIXITES .
AD.icrvT ppo>:iv-.tv switch for fine alignment.
;< :¦ A. :J LS I r'R.uXrMITY SWITCH FOR Ala 1N I ER LO:. i\ .
•i r r \ ! k :n PA" I L.Afi RETURN ROLLER .
\i:t> SH r M PI.aTES UNDER TILT FRAME.
add shades to car.
ADD STOP TO DRAGON TON'GUE.
ADD DOOR OPEN DETECTION STUC7URE.
RELOCATE HOSES ON TILT FRAME SO THAT BOX SPATULA AMS
I- ILL NOT HIT THEM.
'.LEAN OUT WATER TUBE VALVES.
REP:.ACE TEMPOSCNIC IN STRUT.
REPLACE FINE ALIGNMENT CYLINDER ENDS.
REPLACE PROXTMTTY SWTTCH FOR FIVE ALIGNMENT AIR
CYLINDER ON TILT FRAME.
T-7-
I , ¦

-------
pg .01
D5
MAINTENANCE CD3T FGP KIDC BOXES
THIS REPORT IS ON THE ACTUAL MAINTENANCE PREFORMED GN
THE 3 KIDC BOXES FROM OCTOBER 1, 1931 THRU NOUEMBER 2G, 13™1.
LABOR RATE USED IS $ 25.00 PER HUUR.
BOX 8 1
(1)	INSTALL PINCH POINT ADJUSTMENT BARS.
PARTS (3 SETS).....	$ 139.75
LABOR 6 HOURS	£ 150.00
TOTAL $ ' 339.7S
(2)	INSTALL DRIP EDGE MATERIAL.
PARTS		S	105.00
LABOR 3 HOURS.:	."....		$	75.00
TOTAL S	180.00
(3)	INSPECT AND GREASE BOX.
PARTS	$	3 . 79
LABOR I 1^2 H0UR5	$	37.50
TOTAL S	-41 .29
TOTAL COST FOR BOX 8 1	S	561.04 «
BOX 3 2
<15 REPAIR JAMB SEALS BOTTOM LEFT 4 RIGHT.
PARTS 1 SEAL		S	77. OO
LA30R 1 HOUR	S	25.00
TOTAL S	102.00
(2)	REPLACE TOP JAMB SEAL.
PARTS	2=	98.00
LABOR 1 HOUR 		I	25 . 00
TOTAL £	121.00
(3)	BLOW LOOSE PAINT OFF SIDE BOX.
LABOR 1 HOUR		£	25 . 00
TClTA_ S	25.00
(4)	REPAIR BLAST DOOR SAFETY CHAIN.
LABOR 1 HOUR	$¦	25.00
TOTA'_ S	25 . 00
(55 REPLACE AIR DUCTS
PARTS (2 DUCTS)	S	134.00
LABOR 1 1/2 HOURS	$	37.50
TOTAL 5	171.50
(6) STRAIGHTEN BOTTOM LEFT & RIGHT JAMB SEALS.
LABOR 2 HOURS	s	50.00
TOTAL e	50.00
r
i
T-8

-------
pg .
DS
Mh INT ENANCt CUS1 Fuk K. DL BGXtb
C 7) INSPECT AND GREASE.
PARTS	S 3.79
LABOR 1 1/2 HOURS		£ 37.50
TOTAL $ 4 1.29
total cost for box n 2	s 535.79
BOX H 3
U) INSPECT AND GREASE.
P^RTS	. . . .S	3. 79
LABOR 1 1/2 HOURS	$	37 .SO
TOTAL $	41.29
TOTAL COST FOR BOX 0 3. . . 		 ... .&	41 .29
BOX a 4
(1) BLOUJ LOOSE PAINT OFF SIDE UF BOX.
LABOR 1 HOUR.	S	25 . OC
TOTAL a>	25.00
<.Z) clean out catch easim.
LABOR 1 '/2 HOURS		X	37. SO
TOTAL $	37.50
(3)	TOP LEFT SEAL NEED ADJUSTED.
LABOR 1 HOUR	S	25.00
TuTAI. £	ZS.OO
(4)	INSPECT AND GREASE.
PARTS		 . . .§¦	3.79
LABOR 1 1/2 HOURS	S	37.50
TOTAL S. -4 1 . 29
TOTAL COST FOR BOX tt 4	S	i 20 . 79
BOX » 5
CI) replace uater curtain.
PARTS	S	i 05 . 00
LABOR 3 HOURS. 			.£	75.00
TOTAL S	130.00
(2) INSPECT AND GREASE.
PARTS			S	3.79
LABOR 1 1/2 HOURS	i	37.50
- - ¦ TOTAL $	4 1 .29
TOTAL COST FOR BOX tt 5	S	221.29

-------
og. 03
DS
M«IN""£l\i«NCE CCiST FOr« - IDC BlaES
30X 8 6
(H REPAIR BROKEN UEL~ ON CABLE BRACKET ON EXHAUST
STACK DOOR.
LABOR 1 HOUR		4	75.00
~OTAL $	25.00
I2) REPLACE WATER CERTAIN.
PARTS	$	105-00
LABOR 3 HOURS	$	75.00
TOTAL S	;80-00
(3)	INSPECT AND GR="ASc -
PARTS	.S	3.79
LABOR 1 1/2 HOURS	. S	37. 50
TCTAL $	41.29
(4)	REPLACE AIR DUCTS.
PARTS (3 DUCTS)	S	201.CO
LABOR 3 1/4 HOURS	S	81.25
TOTAL S	232.25
TCTAL COST FOR BOX tt S		.*	S2S.S4
BOX tt 7
(1) ADJUST TOP JAMB SEAL.
LABOR 1 HOUR	I	15.00
TOTAL I	25.00
C2) REMOTE LOOSE PATN-.
LABOR 1 HOUR		 . .$	25.00
~QTA*_ $	25.00
C 3) INSPECT AND GREASE.
PARTS	3	3.79
LABOR 1 1/2 HOURS	£	37.50
TCTAL *	41 . 29
TOTAL COST FOR ECX a 7	$	21.29
BOX 8 3
(1) REPLACE AIR DUCTS
PARTS C 3 DUCTS)	S	201 . OO
LABOR 3 1/4 HOJRS	$	91.25
TCTAL S	262.25
i-:o

-------
79
50
29
00
00
00
oo
54
79-
50
"9
23
'1ft IN i LWftNLc. CJSi i- CK KI DC BLXEi
INSPECT HND GREASE.
PARTS	S
LABOR l 1/2 HOURS.	£
TOTAL S
REPAXR WELD SEAMS ON FLOUR INSIDE BOX.
LABOR 3 HOURS	S
TOTAL S
REWORK EXPLOSION DOOR HINGES.
LABOR 2 HOURS	S
TOTAL I
TOTAL COST FOR BOX 3 8.
B 9
INSPECT AND GREASE.
PARTS	$
LABOR i 1 '2 HOURS - - . 					S
TOTAL $
TOTAL COST FOR BOX a 9.	S
.1-11

-------
us	flHlNTFNHr;CF COST FOP <1";C BOxES
TGTAL COST PER BO*.
BOX a i	£	5'5 t . 04
BOX a 2	?	535.79
BOX 0 3		 ........ s	4 ; . 29
BOX » A	'	t	128.79
BOX tt 5	$	221 . 29
BOX a 6		S	528.5*
BOX H 7	$	9 1 . 29
BOX 0 8	 		.....I	448 . 54
BOX tt 9	S-	4 1 . 29
TOTAL. . .5	2597.36
THE T3TA_ COST FCP MAIMTENANCE CN ALL 9 BOXES 13
5 2597.86. THE AD'..'ER'-GE COST PEP ECX IS S 259. £5.
CS 2597.96 •• 9 = -5 133.65)
FROM OCTCBER : , 1991 ~0 NOVEMBER 26, 199: THE^E
WERE. 269 PUSHES TAKE!; WITH THE 9 BOXES- THE ADUERAGE
AMOUNT 0- P-SKES -EC" BOX IS 29.65.(269 ~ 9 = 29.88.'
THE COST ~ER PUSH IS £ 9. 36. '. S 2©S.65 ' 29. S3 - $ 9 . 6£ ;
THE ACTUA_ MAINTENANCE COST ON THE BOXES PER =USH IS 5 9.66.
12 ••19'-91
REPORT BY DAUE SHI=LEV
1-12

-------
MAINTENANCE 1 .nMS
*	-	REGULAR MAINTENANCE ITEMS
*	1.	R F P L \ C F JAMB SEALS.
*	2.	US: HAIR - A ML SEALS.
¦i .	REPLACE DOOR SEALS.
" I •	REPLACE WATER CVitTAlN .
5.	KV>V>r;:.r FLOOR OF BOX.
*	r	REPaTR - .\ P LOS I ON DOOR HINGES.
*	7 .	UEPAIR EXPLOSION DOOR SEALS.
*	8 .	vir P; Mr ; T ft DUCTS IV HO \' .
'I.	REP A I P SPATULA RETURN ARM .
•*	: SI^-i-CRTS ON SIDE ;>r bOX .
¦' ji. . ::-:a\	?a i nt c~? box.
*	! - . : :• C. ..'A :\.'H POL i .
*	. • R L-.C i*. ' a t! L L ON" EXHA'*_SI S I i- 11 'J ¦'1 v -
! -J . RE " :A I. r AX OX BOX .
V r- GUIDES TO REAR OF 30X.
! i; . h i-.MOV CORNER OF CATCH PAX FOR CLEAKNACE ON' < 4 i !..•
i T . REWORM SPATULA TRUN'TCNS .
i 8• REPAIR SPATULA TUBE.
S . RELOCATE LIFT EYES.
20. REPAIR CBAi\ ON EXPLOSION DOOR.
il. ¦JRLASE WHEELS AND ROLLER BEARINGS ON BOX 300R -t\r>
EXHALSi STACK DOOR, REACTION AKS! .
1-1 -l !
! r r>t.? \	\ \«

-------
Appendix J
KIDC Box Thickness Readings
Table of Contents
Sect ion	Page
1	Summary Table of KIDC Box Erosion/Corrosion	J-2
2	Graph of KIDC Box Wear vs. Pushes Accepted	J-4
3	Data Sheets of KIDC Box Thickness Readings	J-6
4	Report of Water Analysis and Estimated Treatment	J-17
Costs from Betz MetChem
J-L

-------
Section 1
Summary Table of KIDC Dox Erosion/Corrosion

-------
APPENDIX J - 1
PUSHCb ACCEPTCQ QV LACH K1 DC BOX AND RESULTS Of TltlCKNFSS MFASUHfcMtHTS
1 I
ho. o* pushns
Lfus'on/
(.ii r rot. i nn
na to hub
i
Ci 00(Vj
4B I
I \V
(1. 0 I I (toil I f» . i fin
0 .004
a. 01 o
NA - Not Avdi lab)**
» Tnase rciii* •» opr. are bason on t rw u' iyuiiil im> tiin.hni!sr, rt»n minus i eadnicit after tht:
Ueironst rat 1 c>i

-------
Section 2
Graph of KIDC Box Wear vs. Pushes Accepted
n;>4	-1
! - ' ' •' :
I

-------
Appendix J
BOX EROSION/CORROSION VS. KIDC PUSHES
Sparrows Point 11 Battery
0.016
0.015
0.014
0.013
0.012
0.011
0.009
0.008
0.007
0 006
0.005
0.004
0.003
0.002
0.001
0.001
0.002
0 003
0.004
0.005
0 20 30 40 50 60 70 80 90 100
No. of Pushes on Box

-------
Section 3
Data Sheets of KIDC Box Thickness Headings
J-5

-------
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-------
ThH 02 '92 14::
Kre"ss Box Th'ic/ne-ss Readings
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-------
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'T-rf hiz.

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-------
Section 4
Report of Water Analysis and Estimated Treatment
Costs from Betz Metchem

-------

Betz
MetChem
MO'fl1 "hemii:a a D.viS'C" C' Bo'r LatxiraiO"(>s Irv
Kress Corpnrat ion
2 27 Illinois Street
j Brimfield, Illinois 61bl/
Attention: Mr. Bill Huffman
jjJULs
'Vcr 7
/ 5
/?/
October 29, 19 9 1
P.E: Service Report
Dear Mr. Huffnan:
The i.ollowing water analysis was run on the indirect coke quench
system.
System:
PH
7. a
Conduct i v i ty
Phcsphoridte
2600 ramhos
<0.1 ppm
Industrial Water:
PH
7 . 3
Conductivity
600
JAOdrtjc :jousi O Mr\-t Olt>cc
46 Synijir nciti S j:'.u ?
iFores! H I. I.'C 2 05C
¦3Cl-39r> OSco
J-18

-------
B«ta
StetChvm
»iWu
Th i r. indicates that you are running 4.3 cycles ot concentration
which is the upper limit of control with treatnent. At this point
ycu have no treatment s •• nee the BFT7, 83K tank is empty.
i
The! conductivity control ir, not functional and needs to be
repa i re L1M1C1DL' C74 is aibu faulty and
in need-of repair.
git>V I
We ialso ran suspended solids on the industrial water and the
quench iater which were '>.2 and <5^.4 respectively.
•	idevtuZ	^
r
i
Sin^e this operation is qoinq to be shut down sometime in the
near future, we. need to decide if we are qoinq to treat the system
and how' it will be put into "r.to-aqo".
Pleaoe let us know how Betz MetChem can help duriny this
transition. If you have any questions, please not hesitate to
contact me at cur Bel An, Maryland. District Office (301 ) 893-0b5s.
S incerely,
BETZ METCHEM
Y	f	' * '¦
V	O (
c. E. Delss
District Manaqer
CED/tb
report

-------
Beta
MetChem
Trm Mtttal Chemicals Division of Betz Laboratories, Inc
February 19, 1992
Bethlehem Steel Corporation
Homer Research
Building C
Bethlehem, Pennsylvania 18016
Attention: Mr. Ge;orge Osnan
RE: KRESS INDIRECT COKE QUENCH PROJECT
Dear Mr. Osman:
The chemical ;treatment program which Betz recommended for the
Kress Indirect Coke Quench System was a two part program.
Corrosion and scale inhibition was provided by Betz 83K. The
annual cost for this program was estimated to be $23,000. This was
assuming 3 cycles of concentration of Industrial Water and running a
pH Of 7 to 8.
Microbiological control would be achieved by a liquid
non-oxidizing biocide, namely, Betz Slimicide C-74. We anticipate
the annual cost of microbiological control to be $5,000.
In summary anticipated annual treatment cost would be $28,000.
If you need any more information on this subject, please do not
hesitate to contact me at our Bel Air, Maryland, District office,
(410) 893-0555.
CED/sah
kress-icqp
Atlantic Coast District Office
346 Bynum Road, Suite 2
Forest Hill. MD 21050
301-893-0556
Sincerely
BETZ METCHEM
Charles E. Delss ^
District Manager
J-20

-------
Appendix K
KIDC Coke Discharge Temperature
Table of Contents
Section	Page
1	Calibration Report of the Ircon Temperature Sensors.	R-2
2	KIDC Coke Discharge Temperature Charts.	K-7
3	Three-Dimensional Beat Transfer Model	K-48
K-l

-------
Section 1
Calibration Report of the Ircon Temperature Sensors
""A
I K-2
!

-------
liEAH
~
SQUARE D COMPANY
INFRARED MEASUREMENT DIVISION .
7301 N. CALDWELL AVE., NILES. IL 60648 708-967-5151 AOMIN. FAX 708-647-0070
MANufACTuncn or IHOON MOOUCTS
October 11, 1991
Kress Corporation
C/O Bethlehem Steel
Truck Dock 321
Sparrows Point, MD 21219
Attn: Mr. Bill Hoffman
Dear Mr. Hoffman,
Enclosed is the Service Report which documents results
obtained during the calibration visit I completed at your
location on October 2nd.
If you have any questions, or if I may be of any assistance,
please do not hesitate to contact me.
Sincerely,
SQUARE D IMD
Brian J. Burke
Technical Services Engineer
encl.
cc: Commonwealth Controls Corp.
Michael Bailey
Eastern Regional Manager
Gedir.;ilt*j to Gf'jwth • Commi'tpd fn O'.&iitv
K-3


-------
Technical Service Report
cusroSe^SKSTP^^™™™
Bill Hoffman
Kress Corporation
PvOMcWX
301/477-6394
aoooess
C/O Bethlehem Steel
CITY/SrATMP
Sparrows Point, MD
6-06F15
CUSTOMER P.O. HQ.
96051
SERVICE OA W.O. NO.
15709
SEAM. NOJS)
See Report
USES (f OTVER THAN AAOVE)
CITY/STATE/aP
DATE(S) SERVICE PROVIOEO
' October 2, 1991
A call was received from Bill Hoffman requesting a field service
visit to check the calibration of their IRCON temperature sensors.
Kress is using 2 Modline Plus 6-06F15 temperature sensors to
measure the temperature of coke. A coke battery partially bums
coal to remove impurities, the result being coke. The coke is used
in making steel, both as a fuel and as an additive for making
carbon steel.
After the coal has been partially burned, it is allowed to cool in
its container before removal (this lowers pollution emissions),
when the coke has cooled down, it is dumped into a large hopper,
which empties onto a conveyor. The IRCON instruments measure the
temperature of the coke as it is dumped on the conveyor.
The target temperature is approximately 400"F. If the temperature
is too high, it can damage the conveyor belt. It takes a long time
for the coke to cool down, so the customer would like to keep this
wait to a minimum.
SERVICE ENGINEER Brian J. Burke
REPORT DATE
10-11-91
IRCON. INC.
7301 North Caldwell Ave. ¦
Phone (703) 967-5151
Toll Free (800) 323 7660
Niles. Illinois 60648
Fax (7C8) 647 0948
Tele* 72 4412
0
SQUARE D COMPANY
INFRARED MEASUREMENT OlVlSION
Dedicated to Growth • Committed to Quality

-------
Technical Service Report
Kress Corporation
Sparrows Point, MD
s£avc£ oRcen no. on wo.
15709
Page 2
The problem Kress was experiencing was that the IRCON instruments
were pegging at their maximum temperature of 600"P. Also, one of
the instruments seemed to be reading higher than the other. It was
decided to have an IRCON representative check the calibration.
When I arrived, I checked the installations and did not see any
initial problems. The sensing heads are about 2-3 feet apart, both
looking straight down on the conveyor about 9 feet below. The
target is relatively large, so focusing and alignment are not
critical. Due to space restrictions, it was not possible to sight
through the sensing heads. One of the heads was pointed at a small
angle, and it looked as though some reinforcing on the hopper might
interfere with the sight path of the instrument. This would tend
to lower the temperature indication, but Kress personnel said that
this instrument was reading higher than the other. The application
looks very straightforward, and I did not see any possible cause
for the instruments to read too high. If anything, dust and steam
in the area would tend to make the instruments read low. I did not
get a chance to view a run before calibrating the instruments.
Calibration consisted of checking the temperature indication at two
separate temperatures, using a portable Blackbody Calibration
System. The instrument was then adjusted to read correctly.
Results are as follows:
Location:
Initial:
Fire Switch #1
Model: 6-06F15
Blackbodv
250
601
Indication
LOW
582
Head V
.010
5.43
lOOmv
-1.2
94.3
Cal V
Final:
Blackbodv
250
600
Indication
250
600
Head V
.053
8.00
lOOmV
0.2
98.7
Cal V
1.443
IRCON. INC.
7301 North Caldwell Ave. ¦
Phone (708) 967-5151
Totl Free (800) 323-7660
Niles. Illinois 60548
Fax (706) 647-0948
Telex 72-4412
K-5
b
SQUARE D COMPANY
INFRARED MEASUREMENT DIVISION
OedicateO to Growth • Committed to Quality

-------
Technical Service Report
Kress Corporation
CITY/STATE
Sparrows Point, MD
SEflvcs onoen no. on wo.
15709
Page 3
Location:
Initial:
Blackbodv
250
600
Final:
Blackbody
250
601
Fire Switch §2
Indication
245
595
Indication
250
600
Head V
.040
6.84
Head V
.054
.8.01
Model:
IQOmV
-0.2
99.1
lOOmV
0.8
100.3
6-06F15
cal V
1.380
Cal V
1.555
As shown in the above calibration results, both instruments were
reading low. So after calibration, the instruments will read
higher than they did before. After calibration, I^viewed a
production run, and both instruments pegged at 600*F, with the
Emittance set to 0.999. There is no appreciable dust or steam, and
I found no problems with the installations.
In conclusion, the instruments are pegging at 600"F because the
temperature is actually above 600"F. There were no problems found
with the instruments, or their applications. The coke is a very
easy target to measure. I recommend either allowing the coke to
cool further before running, or have the temperature range of the
instruments changed to a higher range.
IRCON, INC.
7301 North Caldwell Ave.
Phone (708) 967-5151
Toll Free (800) 323-7660
Miles, Illinois 60648
Fax (708) 647-0948
Telex 72-4412

K-6
SQUARE ~ COMPANY
INFRARED MEASUREMENT DIVISION
Dedicated to Growth • Committed to Quality

-------
Section 2
KIDC Coke Discharge Temperature Charts

-------
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-------
Section 3
Three-Dinensional Heat Transfer Model
,K-48-

-------
CALCULATION OF THE THREE-DIMENSIONAL TRANSIENT TEMPERATURE FTELD WTTHIN
Part of the cokemaking process involves the cooling of a pile of
coka in a KIDC box because of environmental considerations. The XIDC box
is a thin and almost rectangular prism so as to enhance heat renoval.
After the coke is pushed in and the box is closed water is sprayed over
the top surface of the box and it cascades down the side walls. In the
meantime, the air trapped in the box is circulated by means of a fan.
The coke pile is assumed to form the shape shown in Figure 1. The walls
of the KIDC box are made of 1/4" thick steel plate.
For the purpose of modeling, the change in thickness along the
length of the box was neglected and a uniform thickness of 22.42" was
assumed. In addition, the temperature field in the coke pile was assumed
to be symmetric along the thickness and the length directions, hence
one quarter of the coke pile was modeled. Figure 2 shows the geometry of
the model. In Figures 1 and 2, X=0 and Z=0 define the two symmetry planes.
Heat transfer coefficient boundary conditions were imposed on the
remaining four planes. On the wide side, heat is transferred from the
coke to the water film through the steel plate. On the top and inclined
sides heat is removed by the recirculating air and transferred to the
spraying water over the top of the box through the steel plate. This
indirect nature of the process results in much less heat removal compared
to the wide side. On the bottom surface, heat transfer froo the steel
plate to the ambient air is through natural convection.
The numerical values used in the model are as follows:
Initial Temperature of the Coke = 1800 F
Specific Heat of Coke	=0.38 BTU/lb-F
Density of Coke	¦ 30 lb/ft3
Thermal Conductivity of Coke = 0.7 BTU/hr-ft-F
Heat Transfer Coefficients(BTU/hr-ft2-F)
THE COKE PILE COOLED IN THE KIDC BOX
Wide Side
Bottom Surface
Top and Inclined Surfaces
= 137
= 1.4
= 0.2
» 80 F
= 80 F
Ambient Air Temperature
Cooling Water Temperature
Initial Time Step Size
Maximum Time Step Size
Period of Cooling Calculated
Total Number of Time Steps
Finite Element Mesh
= 0.001 sec
= 60 sec
= 40,145 sec
= 883
= 27 x 13X 9 Nodes (Nonuniform)
K-49

-------
RESULTS
Results of the analysis ace summarized in Figures 3 through 8.
Figure 3 shows the variation of temperature along the line from point
A to point B (indicated in Figure 2) as a function of tine. Figures 4
through 6 show the isotherms at three different times on some portion of
the plane containing points A and B. It can be observed from Figures 3
through 6 that the heat transfer occurs predominantly in the thickness
direction as a result of the high convection coefficient on the outer
face of the wide side. In Figure 1, the arithmetic average of the nodal
temperatures is plotted as a function of the cooling time. The average
temperature drops to 400 F after about 6 hours of cooling. Figure 8 shows
the timewise variation of the fraction of nodes where the temperature is
greater than 400 F. This curve is not smooth because of the fact that as
the 400 F front moves inward along the thickness direction it reaches a
nodal plane and crosses a large number ot nodes at once.
KtSO

-------

-------
FORCED CONVECTION COOLING OF COKE
ELEMENT
EDGE PLOT
TIME 0.182Et04
PLANE COPFF.S
A	0. 100E + 01
B	0.000EK)0
C	0.000K+00
D	-.10QE+02
VIEW DIRECTION
VX 0 . 100E+01
VY 0 .100Ei01
ANG 0. OOOEi00
FIDAP 5.02
18-MAR-92
r",	2.

-------
FORCED CONVECTION COOLING OF COKE
1.80000
LL
1.4S60O
T
(X10 + 3)
1.11200 -
« 0.76800
L
O.
0.42400 -
0.08000
T
0.00000 G.1BG96
e~o
i	i	i	1—
0.37392 0.b6088 0.74784 0.93480
COORDINATE, {t
COORDINATE VS.
VARIABLE PLOT
TEMPERATURE
LTNE
DEFIMITICH
POINT
XO 0.1Q0E+02
Y0 0.bOOE+Ol
Z0 0.000E f-00
DIRECTION
X
Y
0.0000
0.0000
1.0000
FIDAP 5.02
16-APR-92
3

-------
FORCED CONVECTION COOLING OF COKE
f I ^. • r C 4
TEMPERATURE
CONTOUR PLOT
LEGEND
A -
0.1000E+03
R -
0.3000E+03
c -
O.bO0OF,+O3
D -
0.7000EI03
E -
0.9000E+03
F -
0.1 100E4 04
G -
0.1300E+04
H -
0.1500EI 04
I -
0.1700Et04
MINIMUM
0. 95122E•02
MAXIMUM
0.1817?E+ 04
TIME 0.180E+04
PLANE COEFF.S
A 0.100EI01
B O.OOOElOO
C 0.OOOE+OO
D -.1 OOF. tO?
VIEW DIRECTION
VX 0.]QOE+O1
VY 0.100EI01
VZ 0.100E401
ANG 0.OOOF. + OO
FIDAP 5.02
20-APR-92
09:30:39

-------
FORCED CONVECTION COOLING OF COKE
l~ A k.
; r, I» r C. fT.
TEMPERATURE
CONTOUR PLOT
LF.GF.ND
A - 0.1500E+03
B - 0.2b00E+03
C - 0.3500E+03
D - 0.4500E+03
E - 0.5500E+03
F - 0.6500Ft03
G - 0.7b00E+03
[1 - 0.8500E(03
I - 0.9500E+03
J - 0.1050E+04
MINIMUM
0 . 82855EI 02
MAXIMUM
0.11 009FHM
TIME O.H4E+Ulj
PLANK COEE'F.S
A 0.100E+01
B 0.000EI00
C 0.000E+00
D -.100E+02
VIEW DIRECTION
VX 0.100E+01
VY 0.100E t 01
VZ 0.100E+01
ANG O.OOOR+OO
FIDAP 5.02
20-APR-92
09:26:01

-------
FORCED CONVECTION COOLING OF COKE

L/i
i
f.-_ II J-.
I-; /)tA tt 6.
TEMPERATURE
CONTOUR PLOT
LEGEND
A - 0.9500R+02
R - 0.1300E+03
C - 0.1700Ei03
D - 0 . 2 10 0 E + 0 3
E - 0.2500EI03
F - 0 - 2 900E103
G - 0.3300E103
H - 0. 3850R+0.1
MTNTMUM
0.81007E+02
MAXIMUM
0.40153K+03
TIME 0.396EI 0b
PLANE (JOKt'F. S
A 0.100EI 01
B 0.000E+00
C 0.OOOE+OO
[) -. 1 QQE-t-02
VIEW DIRECTION
VX 0.100E+01
VY 0.100E+01
VZ O.IOOE+Oi
ANG O.OOOEtOU
FIDAP 5". 02
20-APR-92
09:37:46

-------
7s
I
i-n
FORCED CONVECTION COOLING OF COKE
TIME
HISTORY PLOT


1.80000 -

A NODE 1,F
1 . 4 f>6()() -


(X10+ 3)
ts
^ 1.11200 -
*
\

u
\

of
X 0.76800 -
h
<*:
Vu
Qi.


w 0.42400 -
h


7
oc
o
2.7 \/2 3 /W
¦r i	 i 	 ' i i 'i

0
.00000 0.90000 1.80000 2.70000 3.60000 4.50000
TIME, sec 
-------
FORCED CONVECTION COOLING OF COKE
1.00000 -
0.80506
- i
in
o

-------
Appendix L
QA/QC Program
Table of Contents
Sect ion	Page
1	Demonstration Project Organization Chart	L-2
2	internal Audit Reports	L-4
3	Monthly Progress Reports	L-46
4	Observer Method 9 Certifications	L-86
5	American Medical Laboratory Quality Assurance	L-92
6	Keystone Environmental Resources! Inc. Quality Assurance L-106
I-1

-------
Section 1
Demonstration Project Organization Chart
1,-2

-------

DEMONSTRATION PROJECT ORGANIZATION CHART
OPERATION/TESTING PHA8E
Attachment 4
EPA
C. Vogel
Pro|. Mtntfir
R. A. Fatilnger
Program Director
BSC
Operetlona Manager
lor KIDC Oemonitratlor
A. Baaoaka
Prolaot Englnaarlng
a. Sllvha
Baltary Operation*
A. Baaoaka
lull Contractor
KRESS. Inc
D. Farden
R. W. Reybuck
Qanaral Manager
Bparrowa Point plant
n.
B. C.Clement*
Senior Manager
X
Plant QA Deportment
Q. D. March
BBC - Corporata
OA Daparlmanl
D. Mongeon
R. Welnholfei
Supt.. Coke Omni
T
QA Manager
E. Fletcher
Protect Manager
C. Kelbal
Teat Coaaullant
C. R. Bymona
Sampling 1 Teetlng
Manager
A. Q. Oaaman
Data Manager
J. W. Paaquall
r
Coal I Coke
Quality
R. Qreenbaum
Hamptoa Roade
Taatlng Lab
II
BSC'a
Homer Raeearch
Laboratory
D. Fllnohbaugh
I
1
(Analy tlca
Sparrow* Point
Plant
Laboratory
F. T. Kowalciyk
BCM
Engineer*. Ins.
H. Alexander
and Teatlng Laboratoilea)
American
Medloai
Lab.
F. Grander
Door Emlaalon*
Monitoring
bem, INC
r-
k-
Quench Water
Monitoring
J. W. Paaquall
Area Monitoring
A. Q. Oeeman
BF Evaluation
J. Povaromo
Pualtlng Enlaa.
Monitoring
BCM. Inc.
Vldae Taping
R. T. Bewald
KRESS Bon
VOC
A. Q. Oairaan

-------
Section 2
Audit Reports
1,-4

-------
BETHLEHEM STEEL
SPARROWS POINT PLANT
Interoffice Correspondence
QUALITY ASSURANCE DEPAR'MENT
June 14, 1991
Ref:
from: G. D. Marsh, Superintendent, Quality Assurance
To:	R. J. Weirhoffer, Superintendent, Coke Oven
Subject: 1991 INTERNAL QUALITY SYSTEM AUDIT
In compliance with the Corporate Quality Assurance Program, an Internal
Quality Assurance Audit was conducted in the Coke Over, on May 2, 1991. The
audit team members were:
E. A. Fletcher - Mgr. - QA Systems and SPC, Lead Auditor
R. A. Boehm - SPC Engineer
R. Charles - SPC Engineer
Specific audit results are attached, detailed as	follows:
Category I
Audit Corrective Action Report (ACAR) - Audit	findings which detail
significant non-conformances and/or deficiencies	in the Quality system.
Category II
Audit Comments/Suggestions - Audit findings which would improve the
Quality System.
Category III
• Audit Isolated Significant Observation (Fix-It) - Audit findings which
appear to be isolated and generally reflect a deficiency in continued
adherence to established procedures.
Significant improvements have been made since the last Internal Audit
•n botn the documentation and implementation of the Quality System, a:so,
new control chart applications have been identified and implementec wni'e
the existing charts have undergone a complete review.
Primary areas of concern were identified as follows:
1.	Identification of training requirements for individual positions
and the establishment of a documentation method
2.	Documentation of product standards
3.	Calibration of scales
L-b

-------
June 14, 1991
1991 INTERNAL QUALITY SYSTEM AUDIT
The KVSOP's for "B" coal chemical plant have been revised but are still
under review, and the associated process audit cards have not been revised.
At this point, a decision should be made to either expedite the finalization
cf the KVSOP's and audit cards or discontinue the effort and concentrate on
the development of the process standards for the new coal chemical process.
It was also noted that several of the KVSOP's for the batteries are
primarily related to environmental controls. In most,cases, these process
standards do not meet the strict criteria for the selection of key
variables. Even though the KVSOP system is the most appropriate place to
maintain the environmental standards and provides an audit process, a method
to discretely distinguish the environmental standards from the process
standards should be considered.
Other items of concern varied from area to area and are detailed in the
attacned report. An action plan to address each of the findings will be
developed by the Audit Team in conjunction with Coke Oven Operating and
Quality Assurance Personnel. Progress will be tracked by the lead Auditor
which will include, at a minimum, a formal quarterly review of progress.
G. D. Marsh
Superi ntendent,
Qua!ity Assurance
cc: R.	W.	Raybuck
B.	R.	Clements
C.	W.	Johnson
S.	R.	Kinghorn (C. Schramm) ACAR C0-G03-91
A.	J.	Wi11iamson
I.	R.	Arnett
F.	W.	Kowalczyk
File
EAr/dee
'Sli'cisaco/EAF3
r	- '	¦ "1
L-0 I

-------
BETHLEHEM STEEL CORPORATION
AUDIT CORRECTIVE ACTION REPORT (ACAR)
FAciLfTV/DEPT.
ACAR NO.
: UATE AUDITED:
Sparrows Point / CoKe Ovens
CO-GO 1-91
: 05/02/91
AUUITOR:
AKfcA:

Fletcher, Bcenm, Charles
. General

ESCORT:
DISCUSSED WITH: ""

A. Williamson
Various

DCCUMENT/PROCEOURE NO.
VERIFIED WITH:

QAM 6.3.1.2.1, 6.3.2.1.1, 6.3.2.1.3
Various


Personnel shall be evaluated and qualified on the basis of education, training
and/or experience, as required. Records of training and qualification shall be
maintained.
Employees performing inspection, testing and laboratory functions shall be trained
to the extent necessary to permit them to acquire the necessary skills for the
position.
Qualification evaluations shall be reviewed against established criteria and the
results documented for an employee to be qualified.
OBSERVATION:
Training is handled differently throughout all areas of the Coke Oven. Even though
some documentation is maintained, results are fragmented and incomplete. Due to
lack of *ormal documentation, filling temporary vacancies would be very suspect and
vulnerable to error. Training scope and requirements have not been clearly
ider.ti fied.
RECOMMENDATION:
Develop and implement a specific training program and documentation met.nod. The
training program should identify position requirements and qualifications.
CORRECTIVE ACTION RESPONSE: (INCLUDE TIMETABLE}
acar-fcrm
F 5359000(5-89)
L-7
I

-------
BETHLEHEM STEEL CORPORATION
AUDIT CORRECTIVE ACTION REPORT (ACAR)
HACILITY/DEPT.
ACAft NO.
: DATE AUDITED:
Sparrows Point / Ccke Ovens
C0-G02-91
: 05/02/91
AUDITOR:
AKtA:

Fletcher, Boehm, Charles
General

iSCORT:
DISCUSSED WITH:

A. Williamson
Various

DOCUMENT/PROCEDURE NO.
VERIFIED WITH:

QAM 5.3.2
,Various

STATEMENT OF REQUIREMENTS:
A procedure for selection/verification of suppliers of critical materials and
services shall be established and documented which Includes one or more of the
following: Supplier evaluation and approval system (Supplier Excellence),
self-assessment, source evaluation, audits, quality performance measurements,
receipt inspection and objective evidence of process control and/or product
control.
OBSERVATION:	
A selection/verification procedure has not been established for suppliers of
critical services. For example, Console, Hampton Roads and Sampling Associates ail
supply a critical service to the Coke Oven.
RECOMMENDATION:
Establish and implement a selection/verification procedure *or the sjpplie'-s of
critical services.
c6rrecTIve action REsMnSE: (INCLUDE TIMETABLE)
acar-form
-5355000(5-89)
L-8

-------
BETHLEHEM STEEL CORPORATION
AUDIT CORRECTIVE ACTION REPORT (ACARJ
PACIL1TY/0CPT.
ACAR NO.
: DATE AUDITED:
Coke Ovens
C0-S03-91
: 05/C2/91
AUJITGR:
A^tA:

Fletcher, Boehm, Charles
Various

L5C0RT;
DISCUSSED WITH:

Arnett
Various

DOCUMENT/PROCEDURE NO.
vERifI£D WITH:

QAM 8.3.1
Various

STATEMENT OF REQUIREMENTS:
Calibration shall be performed on measuring and testing equipment used to evaluate
key process variables and specified product attributes in accordance with
MIL-STD-45662A.
OBSERVATION:
A significant amount of progress has. been made in the calibration program for
measuring and testing equipment used to evaluate key process variables and
specified product attributes. However, scales continue to be a weak part of the
program. Scales are maintained by bath the Local Electronics Unit (within the Coke
Oven) and the Plant Electronics Units (Ron Goetzke) dependent upon the age of the
scale. Local Electronics1 procedures are in compliance with plant calibration
requirements and test weight traceability has been established to the plant scale.
However, it was discovered that the procedures for initiating calibration of the
plant scale is very informal and the calibration is not consistently performed.
Awareness of the results of calibrations performed by Plant Electronics and the
frequency of calibrations has not been communicated well to the Coke Oven and has
not been incorporated into the overall Coke Oven calibration program. Test weight
traceability has not been established by Plant Electronics. Also, an outs'de
source is utilized to calibrate the scale at the Coal Moisture Test House.
RECOMMENDATION:	
In order for Coke Oven Personnel to effectively manage the scale calibration
program, better communication must be established between Plant Electronics and the
Coke Oven Electronics Group. Also, the Plant Electronics Group must review
calibration procedures and make any necessary changes to be in compliance with
plant requirements.
A procedure must be developed and implemented to routinely initiate calibration of
the plant scale.
CORRECTIVE ACTION RESPONSE: (INCLUDE TIMETABLE)
acar-form
F5359C00(5-89)

-------
BETHLEHEM STEEL CORPORATION
AUDIT CORRECTIVE ACTION REPORT {ACAR)
FACILITY/DEPT.
ACAR NO.
: CATE AUDITED:
Sparrows Point Plant
C0-6C4-S1
: 05/02/91
AUDITOR:
AREA:

Fletcher, 3oehm, Charles
Various

ESCORT:
DISCUSSED WITH:

A. Williamson
A. Williamson

COCuMENT/PftOCEDuAE NO.
VERIFIED WITH:

QAM 7.3.4
A. Williamson

STATEMENT OF ACQUIREMENTS:
Product standards shall be developed and documented to identify the critical
product characteristics and acceptance criteria at each major stage of the process.
CBSEmrnmi	
Appropriate standard practice instructions (product standards! have: not been
developed for Coal, Coke, and appropriate by-products.
RECOMMENDATION:
Develop the appropriate product standards to identify the critical product
characteristics and acceptance criteria.
JUKHLHIVE ACTION RfcSPONSt: (iNCLLl)e TIMtlABLk}
acar-forrr
F53 59000(5-89)
: L-K)

-------
BETHLEHEM STEEL CORPORATION
AUDIT - COMMENTS / SUGGESTIONS
FACILITY:
: DATE AlDJTED:
Sparrows Point Plant
: 05/02/91
DEPARTMENT:
: AUDIIUK:
Coke Ovens - General
: Fletcher, Boehm, Charles
C0-G05-91
The unloading and segregation of coal is a very important aspect of the Coal
Handling Process and several measures are taken to prevent mixing of coal types in
the Coal Field. However, when a mix does occur, it is recommended that the
investigation and corrective action for the mix be documented. Therefore, a
procedure should be developed detailing the appropriate actions to be taken to
investigate mixed coal.
comnents
F5359200(5-89)

-------
BETHLEHEM STEEL CORPORATION
AUDIT CORRECTIVE ACTION REPORT (ACAR)
"Ac'llTY/DEPT.
ACAR NO.
: DATE AUDITED:
Sparrows Point Plant
C0-BA01-91
: 05/02/91
AuOITOft:
AREA:

Fletcher, Boehm, Charles
"A" 3attery

ESCORT:
J1SCUSSED WITH:

T. Baird
Various

uocument/1 Procedure no.
VtKIMfcl) WITH:

QAM 7.3.6, 7.3.9
Various

STATEMENT OF REQUIREMENTS:
Process standards, procedures or practices shall be developed, documented and
Implemented to establish the specific requirements necessary for process ccntrol to
ensure consistency in product and service quality.
Standards, procedures and practices shall be periodically monitored to verify
compliance with requirements.
.OKeRVATION:	
Several KVSOP's require review and revision as follows:
1.	03.01.01 Pushing Schedule - 24 Hour Coke is not addressed
2.	03.02.02 Changing - Corrective Action does not address what is to be done if
the ovens are not charged in the proper sequence
3.	03.04.02	- Validity of current standard is questionable
4.	Corrective Action - Many of the Corrective Actions appear to be very general in
nature and their effectiveness may be questionable
RECOMMENDATION:	
1.	Develop a time table for the various pushing schedules to cover all operating
scenarios.
2.	Identify appropriate Corrective Action.
3.	Statistically review validity of current standard and adjust as required.
4.	Review all Corrective Actions to determine if more specific actions car. be
identified.
CORRECTIVE ACTION RESPONSE: (INCLuDt IIMUABUJ
acar-form
F5359000(5-89)
1-12

-------
BETHLEHEM STEEL CORPORATION
AUDIT - ISOLATED SIGNIFICANT OBSERVATION
(FIX IT REPORT)
DATE: May 2, 1991
PLANT:
Sparrows Point Plant
AUDITOR:
Fletcher, Boehm, Charles
DEPARTMENT:
Coke Ovens 11 & 12 Batteries
ACCOMPANIED BY:
A. Benoska
LOCATION &
REFERENCE
NUMBER:
OBSERVATION:
COMMENTS:
CORRECT ACTION RESPONSE:
(USE REVERSE IF NECESSARY)
C0-BA02-91
C0-BA03-91
02.06.02 Gas Tending - Standard
is addressed in degrees fahrenheit and
and should be expressed in degrees
centigrade
02.05.01 KVSOP contains a large
process table
Revise KVSOP 02.06.02
Eliminate Process Table from
KVSOP and develop a SPI to be
referenced from the KVSOP

isulated/DG

-------
BETHLEHEM STEEL CORPORATION
AUDIT CORRECTIVE ACTION REPORT (ACAR)
"ACILITV/bEPT.
ACAR NO.
: DATE AUDITED:
Sparrows Point / Coal Chemical
C0-CC01-91
: 05/02/91
AUDITOR:
AREA:

Fletcher, Boehm, Charles
Coal Chemical

SSCOrT:
DISCUSSED WITH:

D. Saul
D. Saul

DOCUMENT/PROCEDURE NO.
VERIFIED WITH:

QAM 4.3.3
D. Saul

SlAFiMENT OF REQUIREMENTS:
Documents shall be distributed to and maintained at required work 'ocaticns.
OBSERVATION:
KVSOP's are not available to Operators at their work locations.
Example: Area of Primary Coolers/Tar Processing: Operating Engineer -Z does not
have KVSOP's in their office. Distribution QCP lists only General Foreman,
Supervisor, and Leader as only recipients of KVSOP copies.
RECOMMENDATION:	
Broaden distrioution to include other locations for Operators including above
example.
CORRECTIVE ACTION RESPONSE: (INCLUDE TIMETABLE)
acar-form
F5359000(5-89)
1,-U

-------
BETHLEHEM STEEi. CORPORATION
AUDIT CORRECTIVE ACTION REPORT (ACAR)
"AciilTY/DEPT.
ACAR NO. : OATE AUDITED:
Sparrows Point / Coal Chemical
C0-CC02-91 : 05/C2/91
SufclTOft:
AREA:
Fletcher, Boehm, Charles
"B" Coal Chemical Plant
tSCORT:
DISCUSSED WITH:
D. Saul
D. Saul
UCCIjment/procedure no.
vtKiKLD WITH:
QAM 4.3.4
D. Saul
STATEMENT OF .REQUIREMENTS:
4.3.4 Documents shall periodically be reviewed for accuracy and correctness and be
revised as appropriate.
OBSERVATION:
Discrepancies exist between KVSOP Process Standards and Audit /Cards for 3 Coal
Chemical Plant. Standards exist	in following KVSOP's that are not included on
audit cards: (KVSOP's 07.01.02	07.10.01
07.06.01	07.10.05
07.07.01	07.11.01
07.07.03	07.13.01
07.08.01	07.13.02
RECOMMENDATION:
Complete revisions to B Coal Chemical Plant KVSOP's and ensure a'l Process
Standards are similarly included on Audit Cards. See suggestion C0-CC06-91
LUUHbCim ACTION RESPONSE: (INCLUUfc TIMETABLE)
acar-form
F5359000(5-39)
L-15

-------
BtTHLEHfM STEfL CORPORATION
AUDIT - I SOI ATE I) SIGNIFICANT OBSERVATION
(FIX IT REPORT)
DATE: May 2, 1991
TDtFTT
Sparrows Point Plant
TODTTOR:
K. Charles
DEPARTMENT:
Coke Ovens/ Coal Chemical
ACCOMPANIED BY:
I). Saul
LOCATION &
REFERENCE
NUMBER:
C0-CC03-91
"i
I
C0-CC04-91
C0-CC05-91
OBSERVATION:
COMMENTS:
KVSOP 06.02.01 indicates use of an
Individuals, Moving Range Chart
KVSOP 06.01.02 states, "Tar temp. 1n
full dehydrator must be maintained
between 80 and 90 degrees
Operator was reporting 90 degrees on
his report though temperature gauge,
after being wiped clean of grime,
read 100".
Q.A. Calibration -
Test Basin and Still PH:
Located in B Plant; acct.# N009 in
M1CS. Identity of instrument used to
perforin calibration is not made on
work order completed by technician.
Chart is actually an X-Bar,
R chart.
This incident underscores
implementation of Process
Standards that are valid and
Operators are familiar with.
See suggestions C0-CC06-91
Create a heading for instrument
serial # or 1.0. # oil work order
to be filled in by technician
CORRECT ACTION RESPONSE:
(USE REVERSE IF NECESSARY)
isolated/DG

-------
BETHLEHEM STEEL CORPORATION
AUDIT - COMMENTS / SUGGESTIONS
FACILITY:
: DATE AUDITED:
Sparrows Point Plant
: 05/02/91
DEPARTMENT:
: AUDI 10k:
Coke Ovens / Coal Chemical
: R. Charles
C0-CC06-91
The key Issue for the Coal Chemical Plant relative to the Quality System at the
present, is the effective development and implementation of Process Standards in
conjunction with the new plant scheduled to start up 1n September.
Recommendation:
While undergoing training on the new Foxboro process control system, Operators are
monitoring hypothetical system pressures, temperatures, flow rates, etc. that are
the same as those that will be identified in Process Standards. Ideally, alongside
this training, Operator input can be used to develop Process Standards for the new
operations. Expected benefits would be:
*	Development and review of Process Standards with Operators throughout
learning curve.
*	Implementation of valid Process Standards as a result of Operator's
familiarity, "buy-in", of well reviewed Process Standards and KVSOP's.
*	Quality System will be in place for start-up of the facility.
comments
F5359200(5-89)
1,-17
i

-------
BETHLEHEM STEEL CORPORATION
AUDIT - COMMENTS / SUGGESTIONS
FACILITY:
: DATE AUDITED:
Sparrows Point Plant
: 05/02/31
"DEPRRTMEfiT:
: AUDITOR:
Coke Ovens / Coal Chemical
: R. Charles
Recommendation;
C0-CC07-91
Training and documentation of training of employees in spill prevention, time spent
in various positions, and or new Foxboro system is thorough and well maintained.
Documentation of Operator's time spent in various positions will become cuirbersome
after some time and would lead itself well to routine input into a computerized
system (HRIS, LOTUS, etc.)
Recommendation:
C0-CCQ8-91
Control Dept. Has made much progress, in development of a calibration system thru
use of MICS. System, Identification of quality arid environmental related
calibration requirements is a good idea. The only gap in the program is that
Instruments used to make calibration are not identified on MICS work orders that
Technician completes and this limits traceabiHty.
comments
F5 359200(5—89)

-------
BETHLEHEM STEEL CORPORATION
AUDIT - ISOLATED SIGNIFICANT OBSERVATION
(FIX IT REPORT)
DATE: Hay 2, 1991
Kim	: AUOTTOft:	
Sparrows Point Plant	: Fletcher, Boehm, Charles
DEPARTMENT:	: ACCOMPANIED BY:
Coke Oven Lab.	: M. Gould, M. Saddler
LOCATION &	OBSERVATION:	:	COMMENTS:	: CORRECT ACTION RESPONSE:
REFERENCE	:	: (USE REVERSE IF NECESSARY)
NUMBER:	:	:
C0-LAB01-91 :	SKg NIST Class P weight was due for	: Calibrate as required per
	.	:	calibration on 11/22/90. Calibration	: procedure.
:	is significantly past due.	:
l- CO-LAB02-91 :	The Shelf Life of many of the	: Develop & implement a system to
^	:	chemicals used for analytical work	: control the shelf life of ALL
° ,	:	was questionable.	: materials used by the lab.
isoluted/DG

-------
SPARROWS POINT PLANT
CORRECTIVE ACTION REPLY
ch^ck appropriate step:



ACAR ( X ) C0-G01-91
FIX IT ( )

SUGGESTION ( )
PRELIMINARY ( )
FINAL (
)

AREA:



General



OBSERvATIOn/RECOMMENDATION:
Training is handled differently throughout all areas of the Coke Oven. Even
though some documentation is maintained, results are fragmented and
Incomplete. Due to lack of formal documentation, filling temporary vacancies
would be very suspect and vulnerable to error. Training scope and
requirements have not been clearly identified.
Develop and implement a specific training program and documentation method.
The training program should identify position requirements and
qualifications.
CORRECTIVE ACTION PLAN:
/tscoi &	
-------
SPARROWS POINT PLANT
CORRECTIVE ACTION REPLY
CHECk APPROPRIATE STEP:


ACAR ( X ) C0-G02-91
FIX IT ( )
SUGGESTION ( )
PRELIMINARY ( )
FINAL ( )

AREA:


General


ObStRVATIOh/RECOMHENDATION:
A selection/verification procedure has not been established for suppliers of
critical services. For example, Console, Hampton Roads and Sampling
Associates all supply a critical service to the Coke Oven.
Establish and Implement a selection/verification precedure for the suppliers
of critical services.
CORRECTIVE ACTION PLAN:
x s-zcecsr/F*^/t/
L-G /ZcTTL	cf- c/2.""
%£ frsrrtsc/sstt) a*jl
JTx-^ PCA l* /u-r /er^j J;*
T~I>	-4sS'Jr X^>	0*
«- J*M<" ff-f ¦ ffrr/e/?ss/yr'
iO'rrt 7#KJt /fit, 4.
mmmmMii: s_ ,ce7t,^ , c.
PROPOSED COMPLETION DATE:	'
// ,'2u If/
corr/act/reply-EAF3
¦ ~-I.-?l'

-------
BETHLEHEM STEEL CORPORATION
AUDIT CORRECTIVE ACTION REPORT (ACAR)
(¦AcIlITV/dEpt.
ACAR NO.
: DATE AUDITED:
Sparrows Point / Coke Ovens
CO-GO 1-91
: 05/02/91
Auditor:
AREA:

Fletcher, Boehm, Charles
. General

ESCORT:
DISCUSSED WITH:

A. Williamson
Various

DOCUMENT/PROCEDURE NO.
VERIFIED WITH:

QAM 6.3.1.2.1, 6.3.2.1.1',. 6.3.2.1.3
Various

Personnel shall be evaluated and qualified on the basis of education, training
and/or experience, as required. Records of training, and qualification shall be
maintained.
Employees performing inspection, testing and laboratory functions shall be trained
to the extent necessary to permit them to acquire the necessary skills for the
position-
Qualification evaluations shall be reviewed against established criteria and the
results documented for an employee to be qualified.
OBSERVATION:
Training is handled differently throughout all areas of the Coke Oven. Even though
some documentation is maintained, results are fragmented, and incomplete. Due to
lack of formal documentation, filling temporary vacancies would be very suspect and
vulnerable to error. Training scope- and requirements have not been clearly
identified.
RECOMMENDATION:
Develop and implement a specific training program and documentation method. The
training program should identify position requirements and qualifications.
CORRECTIVE ACTION RESPONSE: (INCLUDE TIMETABLE)
acar-form
F 5359000(5-89)
L-7

-------
BETHLEHEM STEEL CORPORATION
AUDIT CORRECTIVE ACTION REPORT (ACAR)
fAciliTy/depT.
ACAR NO.
:. DATE AUDITED:
Sparrows Point / Coke Ovens
C0-G02-91
: 05/02/91
AUUITOR:
AREA:

Fletcher, Boehm, Charles
General

h5C0RT:
DISCUSSED WITH:

A. Williamson
Various

document1/Procedure, no.
VERIFIED WITH:

QAM 5.3.2
,Various

STATEMENT OF REQUIREMENTS:
A procedure for selection/verification of suppliers of critical materials and
services shall be established and documented which includes one or more of the
following: Supplier evaluation and approval system (Supplier Excellence),
self-assessment, source evaluation, audits, quality performance measurements,
receipt inspection and objective evidence of process control and/or product
control.
OBSERVATION:	|
A selection/verification procedure has not been established for suppliers of
critical services. For example, Console, Hampton Roads and Sampling Associates all
supply a critical service to the Coke Oven.
RECOMMENDATION:
Establish and implement a selection/verification procedure for the suppliers of
critical services.
CORRECTIVE ACTION RESPONSE: (INCLUDE TIMETABLE)
acar-form
F5359000(5-89)

-------
BETHLEHEM 5TEEL CORPORATION
AUDIT CORRECTIVE ACTION REPORT (ACAR)
WCIII1WPT.
ACAR NO.
: DATE AUDITED:
Coke Ovens
C0-G03-91
: 05/02/91
AUDITOR:
AktA;

Fletcher, Boehm, Charles
Various

tSCORT:
DISCUSSED WITH:

Arnett
Various

DOCUMENT/PROCEDURE NO.
vEftlFll-O WITH:

QAM 8.3.1
Various

Statement of requirements:
Calibration shall be performed on measuring and testing equipment used to evaluate
key process variables and specified product attributes in accordance with
MIL-STD-45662A.
OBSERVATION:	:
A significant amount of progress has. been made in the calibration program for
measuring and testing equipment used to evaluate key process variables and
specified product attributes. However, scales continue to be a weak part of the
program.. Scales are maintained by both the Local Electronics Unit (within the Coke
Oven) and the Plant Electronics Units (Ron Goetzke) dependent upon the age of the
scale. Local Electronics1 procedures are in compliance with plant calibration
requirements and test weight traceability has been established to the plant scale.
However, it was discovered that the procedures for initiating calibration of the
plant scale is very informal and. the calibration is not consistently performed.
Awareness of the results of calibrations performed by Plant Electronics and the
frequency of calibrations has not been communicated well to the Coke Oven and has
not been incorporated into the overall Coke Oven calibration program. Test weight
traceability has not been established by Plant Electronics. Also, an outside
source is utilized to calibrate the scale at the Coal Moisture Test House.
RECOMMENDATION:	^
In order for Coke Oven Personnel to effectively manage the scale calibration
program, better communication must be established between Plant Electronics and the
Coke Oven Electronics Group. Also, the Plant Electronics Group must review
calibration procedures and make any necessary changes to be in compliance with
plant requirements.
A procedure must be developed and implemented to routinely initiate calibration of
the plant scale.
CORRECTIVE ACTION RESPONSE: (INCLUDE TIMETABLE)
acar-form
F5359000(5-89)
i
L-9

-------
BETHLEHEM STEEL CORPORATION
AUDIT CORRECTIVE ACTION REPORT (AGAR)
FACIL1TV/DEPT.
ACAR NO.
: DATE AUDITED:
Sparrows Point Plant
C0-604-91
: 05/02/91
AllDlTOft:
AREA:

Fletcher, 3oehm, Charles
Various

ESCORT:
DISCUSSED WITH:

A. Williamson
A. Williamson

DOCuMENT/PftOCEDuRg NO.
VERIFIED WITH:

QAM 7.3.4
A. Williamson

STATEMENT OF REQUIREMENTS:
Product standards shall be developed and documented to identify the critical
product characteristics and acceptance criteria at each major stage of the process.
(JURATION:	
Appropriate standard practice instructions (product standards) have: not been
developed for Coal, Coke, and appropriate by-products.
RECOMMENDATION:
Develop the appropriate product standards to identify the critical product
characteristics and acceptance criteria.
OJKKktlllVE ACTION RkMSt: (INCLUUfc TIMLI AfclLLj
acar-form
F5359000(5-89)
L-10

-------

BETHLEHEM STEEL CORPORATION

AUDIT - COMMENTS / SUGGESTIONS
FACILITY:
: DATE AUDITED:
Sparrows Point Plant
: 05/02/91
DEPARTMENT:
: AUliilUK:
Coke Ovens - General
: Fletcher, Boehm, Charles
CQ-GQ5-91
The unloading and. segregation of coal is a, very important aspect of the Coal
Handling Process and several measures are taken to prevent mixing of coal types in
the Coal Field. However, when a mix does occur, it is recommended that the
investigation and corrective action for the mix be documented. Therefore, a
procedure should be developed detailing the appropriate actions to be taken to
investigate mixed coal.
comments
F5359200(5-89)

-------
BETHLEHEM STEEL CORPORATION
AUDIT CORRECTIVE ACTION REPORT (ACAR)
FAClllTY/DEPT.
ACAR NO.
: DATE AUDITED:
Sparrows Point Plant
C0-BA01-91
: 05/02/91
auditor:
AREA:

Fletcher, Boehm, Charles
"A" Battery

ESCORT:
UISCUSSED WITH:

T. Baird
Various

DOCUMENT/PROCEDURE NO.
VtKlULU WITH:

QAM 7.3.6, 7.3.9
Various

STATEMENT 0F RECREMENTS:
Process standards, procedures or practices shall be developed, documented and
implemented to establish the specific requirements necessary for process control to
ensure consistency in product and service quality.
Standards, procedures and practices shall be periodically monitored to verify
compliance with requirements.
OBSERVATION:
Several KVSOP's require review and revision as follows:
1.	03.01.01 Pushing Schedule - 24 Hour Coke is not addressed
2.	03.02.02 Changing - Corrective Action does not address what is to be done-if
the ovens are not charged in the proper sequence
3.. 03.04.02	- Validity of current standard is questionable
4. Corrective Action - Many of the Corrective Actions appear to be very general in
nature- and their effectiveness may be questionable
RECOMMENDATION:	
1.	Develop a time table for the various pushing schedules to cover all operating
scenarios.
2.	Identify appropriate Corrective Action.
3.	Statistically review validity of current standard and adjust as required.
4.	Review all Corrective Actions to determine if more specific actions can be
identified.
CORRECTIVE ACT ION RESPONSE: (INCLUDE HMtlABLt)
acar-form
F5359C00{5-89)
L-12

-------
BETHLEHEM STEEL CORPORATION
AUDIT - ISOLATED SIGNIFICANT OBSERVATION
(FIX IT REPORT)
DATE: May 2, 1991
PLANT:
Sparrows Point Plant
AUDITOR:
Fletcher, Boehm, Charles
DEPARTMENT:
Coke Ovens 11 & 12 Batteries
ACCOMPANIED BY:
A. Benoska
LOCATION &
REFERENCE
NUMBER:
OBSERVATION;
COMMENTS:
CORRECT ACTION RESPONSE:
(USE REVERSE IF NECESSARY)
C0-BA02-91
C0-BAO3-91
02.06.02 Gas Tending - Standard
is addressed in degrees fahrenheit and
and should be expressed in degrees
centigrade
02.05.01 KVSOP contains a large
process table
Revise KVSOP 02.06.02
Eliminate Process Table from
KVSOP and develop a SPI to be
referenced from the KVSOP

isolated/UG

-------
BETHLEHEM STEEL CORPORATION
AUDIT CORRECTIVE ACTION REPORT (ACAR)
FAClLlTV/bEF'T.
ACAR NO.
: DATE AUDITED:
Sparrows Point / Coal Chemical
C0-CC01-91
: 05/02/91
AUDITOR:
AREA:

Fletcher, Boehm, Charles
Coal Chemical

SSCOrT:
DISCUSSED WITH:

D. Saul
D. Saul

DOCUMENT/PROCEDURE NO.
VERIFIED WITH:

QAM 4.3.3
D. Saul

STATEMENT OF REqulftEMEWS:
Documents shall be distributed to and maintained at required work locations.
OBSERVATION:
KVSOP's are not available to Operators at their work locations.
Example: Area of Primary Coolers/Tar Processing: Operating Engineer #2 does not
have KVSOP'S- in their office. Distribution QCP lists only General Foreman,
Supervisor, and Leader as only recipients of KVSOP copies.
kECOMHENDATIOto:	
Broaden distribution to include other locations for Operators including above
example.
CORRECTIVE ACTION RESPONSE: (INCLUDE TIMETABLE)
acar-form
F53590QQ(5-89)

-------
BETHLEHEM STEEL CORPORATION
AUDIT CORRECTIVE ACTION REPORT (ACAR)
kAciliTV/DEPT.
ACAR W). ;
DATE AUDITED:
Sparrows Point / Coal Chemical
C0-CC02-91 :
05/02/91
Auditor:
AREA:

Fletcher, Boehm, Charles
"B" Coal Chemical Plant

ESCORT:
DI5CU5SED WITH:

D. Saul
D. Saul

OUCUMEhT/Procedure no.
VtmHED WITH:

QAM 4.3.4
D. Saul

STATEMENT OF REQUIREMENTS:
4.3.4 Documents shall periodically be reviewed for accuracy and correctness and be
revised as appropriate.
OBSERVATION:
Discrepancies exist between KVSOP	Process Standards and Audit /Cards for B Coal
Chemical Plant. Standards exist	in following KVSOP's that are not included on
audit cards: (KVSOP's 07.01.02	07.10.01
07.06.01	07.10.05
07.07.01	07.11.01
07.07.03	07.13.01
07.08.01	07.13.02
RECOMMENDATION:
Complete revisions to B Coal Chemical Plant KVSOP's and ensure all Process
Standards are similarly included on Audit Cards. See suggestion C0-CC06-S1
lUMKbCUVfc ACTION HfcSPONSE: (INCLUDE TIMETABLE)
acar-form
F5359000(5-89]

-------
BETHLEHEM STEEL CORPORATION
AUDIT - ISOLATED SIGNIFICANT OBSERVATION
{FIX IT REPORT)
DATE: May 2, 1991
PLANT:
Sparrows Point Plant
AUDITOR:
R. Charles
DEPARTMENT:
Coke Ovens/ Coal Chemical
ACCOMPANIED BY:
D. Saul
LOCATION &
REFERENCE
NUMBER:
OBSERVATION:
COMMENTS:
CORRECT ACTION RESP0N5E:
(USE REVERSE IF NECESSARY)
C0-CC03-91
KVSOP 06.02.01 indicates use of an
Individuals, Moving Range Chart
Chart is actually an X-Bar,
R chart.

^ C0-CC04-91
i
KVSOP 06.01.02 states, "Tar temp, in
full dehydrator must be maintained
between 80 and 90 degrees ...
Operator was reporting 90 degrees on
his report though temperature gauge,
after being wiped clean of grime,
read 100°.
This incident underscores
implementation of Process
Standards that are valid and
Operators are familiar with.
See suggestions C0-CC06-91

C0-CC05-91
Q.A. Calibration -
Test Basin and Still PH:
Located in B Plant; acct.# N009 in
MICS. Identity of instrument used to
perforin calibration is not made on
work order completed by technician.
Create a heading for instrument
serial # or 1.0. # on work order
to be filled in by technician

isolated/DG

-------
BETHLEHEM STEEL CORPORATION
AUDIT - COMMENTS / SUGGESTIONS
FACILITY:
: uarfcl AUDITED:
Sparrows Point Plant
: 05/02/91
DEPARTMENT:
: AUUilUK:
Coke Ovens / Coal Chemical
: R. Charles
C0-CC06-91
The key issue for ttie Coal Chemical Plant relative to the Quality System at the
present, is the effective development and implementation of Process Standards in
conjunction with the new plant scheduled to start up in September.
Recommendation:
While undergoing training on the new Foxboro process control system, Operators are
monitoring hypothetical system pressures, temperatures, flow rates, etc. that are
the same as those that will be identified in Process Standards. Ideally, alongside
this training, Operator input can be used to develop Process Standards for the new
operations.. Expected benefits would be:
*	Development and review of Process Standards with Operators throughout
learning curve..
*	Implementation of valid Process Standards as a result of Operator's
familiarity, "buy-in", of well reviewed Process Standards and KVSOP's.
*	Quality System will be in place for start-up of the facility.
comments
F5359200( 5-89)		 —
L-ll
i

-------
BETHLEHEM STEEL CORPORATION
AUDIT - COMMENTS / SUGGESTIONS
FACILITY:
: DATE AUDITED:
Sparrows Point" Plant
: 05/02/91
DEPARTMENT:
: AUDITOR:
Coke Ovens / Coal Chemical
: R. Charles
Recommendation:
CG-CC07-91
Training and documentation of training of employees, in spill prevention, time- spent
in various positions, and or new Foxboro system is thorough and well maintained.
Documentation of Operator's, time spent in various positions will become cumbersome-
after some time and would lead itself well to routine input into a computerized
system (HRIS, LOTUS, etc.)
Recommendation;
C0-CCQ8-91
Control Dept. has made much progress, irr development of a- calibration system- thru
use- of MIC5 System. Identification of quality and environmental related
calibration requirements is a good idea. The only gap in the program is that
instruments used to make calibration are not identified on MICS work orders that
Technician completes and this limits traceablllty.
comments
F5359200(5-89)

-------
BETHLEHEM STEEL CORPORATION
AUDIT - ISOLATED SIGNIFICANT OBSERVATION
(FIX IT REPORT)
DATE: May 2, 1991
PLANT:	: AUDITOR:
Sparrows Point Plant	: Fletcher, Boehm, Charles
DEPARTMENT:	: ACCOMPANIED BY:
Coke Oven Lab.	: M. Gould, M. Saddler
LOCATION &	OBSERVATION:	:	COMMENTS:	: CORRECT ACTION RESPONSE:
REFERENCE	:	: (USE REVERSE IF NECESSARY)
NUMBER:	:	:	:
C0-LAB01-91 :	5Kg NIST Class P weight was due for	: Calibrate as required per
;—,	:	calibration on 11/22/90, Calibration	: procedure.
:	Is significantly past due.	:
t-1 CO-LAB02-91 :	The Shelf Life of many of the	: Develop & implement a system to
4"	:	chemicals used for analytical work	: control the shelf life of ALL
1X1 1	:	was questionable.	: materials used by the lab.
isoluted/DG

-------
SPARROWS POINT PLANT
CORRECTIVE ACTION REPLY
CheCK Appropriate step:


ACAR ( X } C0-G01-91
FIX IT { )
SUGGESTION ( }
PRELIMINARY ( )
FINAL ( )
AREA:


General


06$EhvATI0N/Rtt0hHENflATMh:
Training is handled differently throughout all areas of the Coke Oven. Even
though some documentation is maintained, results are fragmented and
incomplete. Due to lack of formal documentation, filling temporary vacancies
would be very suspect and vulnerable to error. Training scope and
requirements have not been clearly identified.
Develop and implement a specific training program and documentation method.
The training program should identify position requirements and
qualifications.
corrective action plan:
/tec#*, b* ^ q (MC/Ft	s
ujftc bg c>€vei
-------
SPARROWS POINT PLANT
CORRECTIVE ACTION REPLY
cHECk appropriate step:


ACAR ( X ) C0-G02-91
FIX IT ( )
SUGGESTION ( )
PRELIMINARY ( )
FINAL ( )

AREA:


General


Ob^LftVATIOh/ftECOWENDATIOH:
A selection/verification procedure has not been established for suppliers of
critical services. For example, Console, Hampton Roads and Sampling
Associates all supply a critical service to the Coke Oven.
Establish and. implement a selection/verification precedure for the suppliers
of critical services.
CORRECTIVE ACTION PLAN:
A CecT/^/iy rr/i
c.eby)rL	y4si'Sr	Juff •-<>-* j fir
^AiT-sft-T' S?" u' ¦ fSrr	^	1 I*-/^ rfss/jr'
iO'rf* 7a>KJI yfa/O, ¦ f//~s/<7 I
PERSON RESPONSIBLE:			" ~—~
G, 73/^^2. s c. L-<"K
PROPOSED COMPLETION DATE:	9
// !2u l)/
corr/act/reply-EAF3	~ — 	,

-------
SPARROWS POINT PLANT
CORRECTrVE ACTION REPLY
CHECK APPRUPRlATt STtP:

ACAR ( X ) C0-G03-91 FIX IT ( )
SUGGESTION ( )
PRELIMINARY ( ) FINAL ( )
AKtA:

Various

OBSI-RMTIOS/RECOMMENDATION:
A significant amount of progress has been made in the calibration program for
measuring and testing equipment used to evaluate key process variables and
specified product attributes. However, scales continue to be a weak part of
the program. Scales- are maintained by both the Local Electronics Unit
(within the Coke Oven) and the Plant Electronics Units (Ron Goetzke),
dependent upon the age of the scale. Local Electronics' procedures are in
compliance with plant calibration requirements and test weight traceability
has been established to the plant scale. However, it was discovered that the
procedures for initiating calibration of the plant scale is very informal and
the calibration is,not consistently performed. Awareness of the results of
calibrations performed by Plant Electronics and the frequency of calibrations
has not been communicated well to the Coke Oven and has not been incorporated
into the overall Coke Oven calibration program. Test weight traceability has
not been established by Plant Electronics. Also, an outside source is
utilized to calibrate the scale at the Coal Moisture Test House.
In order for Coke Oven Personnel to effectively manage the scale calibration
program, better conanunication must be established between Plant Electronics
and the Coke Oven Electronics Group. Also, the Plant Electronics Group must
review calibration procedures and make any necessary changes to be in
compliance with plant requirements.
A procedure must be developed and implemented to routinely initiate
calibration of the plant scale.
CUKKECTIVE ACTION PLAN:
PhRSUN RESPONSIBLE:
PROPOSED COMPLETION DATE:	
/ /
corr/act/reply-DG3
5.L«cj'jUnu>/c	_
! L-22 ;

-------
SPARROWS POINT PLANT
CORRECTIVE ACTION REPLY
CHECK APPROPRIATE STEP:


ACAR ( X ) C0-G04-91
FIX IT ( )
SUGGESTION ( )
PRELIMINARY ( )
FINAL ( )
AKfcA:


Various


OBSERVATION/RECOMMENDATION:
Appropriate standard practice instructions (product standards) have not been
developed for Coal, Coke, and appropriate by-products.
Develop the appropriate product standards to identify the critical product
characteristics and acceptance criteria.
CORRECTIVE Action PLAN:	
j>£X?b vcrr	6^.S" Uj'LL
!>$_o7>	h oc 'J m eAJ
PERSON RcSPONSISl£ :	7™^	J——	
HKUWJSKD COMPLETION DATE:	~
s?/Z 't 9/
corr/act/reply-0G3	/ "	C0t+/><'F7&
i L-23^ \

-------
SPARROWS POINT PLANT
CORRECTIVE ACTION REPLY
CHECK APPROPRIATE STEP:


ACAR { )
FIX IT ( )
SUGGESTION ( X ) C0-G05-91
PRELIMINARY (
)
FINAL { )
AREA:


Coke Ovens - General


OBSERVATION/RECOMMENDATION:
The unloading and segregation of coal is a very important aspect of the Coal
Handling Process and several measures are taken to prevent mixing of coal
types in the Coal Field. However, when a mix does occure, it is recommended
that the investigation and corrective actions for the mix be documented.
Therefore, a procedure should be developed detailing the appropriate actions
to be taken to investigate mixed coal.
CORRECTIVE ACTION PLAN:	
5 A. t? C O M E < \j CaJ	A T'&yJ*
PERSON RESPONSIBLE: !	7777
A. VjtLL'A" '
PROPOSED COMPLETION DATE:	
/ /
corr/act/reply-0G3
i. . L-24, • I

-------
SPARROWS POINT PLANT
CORRECTIVE ACTION REPLY
CHECK APPROPRIATE STEP:		
ACAR ( X ) C0-8A01-91 FIX IT ( )	SUGGESTION ( )
PRELIMINARY { )	FINAL ( )
mm	
"A" Battery
OBSERVATION/RECOMMENDATION:		
Seveal KVSOP's require review and revision as follows:
1.	03.01.01 Pushing Schedule - 24 Hour Coke is not addressed
2.	03.02,02 Chairging - Corrective Action does not address what is to be
done if the ovens are not charged in the proper
sequence
3.	03.04.02	- Validity of current standard is questionable
4.	Corrective Action - many of the Corrective Actions appear to.be very
general in nature and their effectiveness may be
questionable
1.	Develop a time table for the various pushing schedules to cover all
operating scenarios.
2.	Identify appropriate Corrective Action.
3.	Statistically review validity of current standard and adjust as
required..
4.	Review all Corrective Actions to determine if more specific actions can
be identified.
LUKKtCriVE ACTION PLAN:
T7rZ	Ki/FdPS uJ/a, fi 
-------
SPARROWS POINT PLANT
CORRECTIVE ACTION REPLY
CHECK APPROPRIATE STEP:


ACAR ( )
FIX IT ( X )C0-BA02-91
SUGGESTION ( )
PRELIMINARY (
) FINAL { )

AREA:


Coke Ovens 11 & 12 Batteries


OUSEfivATION/RttOMMMATION:
02.06.02 Gas Tending - Standard is addressed in degrees fahrenheit and should,
be- expressed in degrees centigrade.
Revise KVSOP 02.06.02
CORRECTIVE ACTION PLAN:	.
u_;,CC Z
-------
SPARROWS POINT PLANT
CORRECTIVE ACTION REPLY
CHECK. APPWJPhlATE STEP:


ACAR ( )
FIX IT ( X ) CQ-8A03-91
SUGGESTION ( )
PRELIMINARY (
) final ( )
AREA:


Coke Ovens II & 12 Batteries


observatiqn/riICOMMENDATIOn :
02.05.01 KVSOP contains a large process table.
Eliminate Process Table from KVSOP and develop a SPI to be referenced from
the- KVSOP.
CORRECTIVE AcTIOn PlAH:
JL£VrS€~C> A-*Jt r> £
b £ '1/&COPTQ ^
PERSON RESPONSIBLE: ^ ^ .	~—7T~7™~=r
A. ££aJ0S£-<^ B. A&A/&7T^
PROPOSE COMPLETION DATE:	'			
<3/3// 9/
corr/act/reply-0G3
C-OJUfiZT&>
L-27 j

-------
SPARROWS POINT PLANT
CORRECTIVE ACTION REPLY
CHECK APPROPRIATE STEP:			"""""		

ACAR { X ) C0-CC01-91 FIX IT ( )
SUGGESTION ( )
PRELIMINARY ( ) FINAL ( )
AKtA:

Coal Chemical

UKSERVATI0N/REC0MMENQAT10N:
KVSOP's are not available to Operators at their work locations.
Example: Area of Primary Coolers/Tar Processing: Operating Engineer #2 does
not have KVSOP's in their office. Distribution QCP lists only General
Foreman, Supervisor, and Leader as only recipients of KVSOP copies.
Broaden distribution to include other locations for Operators including above
example.
CORRECTIVE ACTION PLAN:	
K\ysotr uj/cu &€ bis?-#. iQoTZb
PLUiiON RESPONSIBLE:		—	
WUM5ED COMPLETION UAiL:	
corr/act/reply-DG3
UJ/LL	«us"s
\aJ1u7T&J
L-2.8

-------
SPARROWS POINT PLANT
CORRECTIVE ACTION REPLY
CHECK APPROPRIATE STEP:

ACAR ( X ) C0-CCO2-91 FIX IT ( }
SUGGESTION ( )
PRELIMINARY ( ) FINAL ( )
AKfcA:

"8" Coal Chemical Plant

OSServATIOn/AECCiMMENDATIOn :
Discrepancies exist between KVSOP Process	Standards and Audit/Cards for B
Coal Chemical Plant. Standards exist in	following KVSOP's that are not
included on audit cards: (KVSOP's 07.01.02	07.10.01
07.06.01	07.10.05
07.07.01	07.11.01
07.07.03	07.13.01
07.08.01	07.13.02
Complete revisions to B Coal Chemical Plant KVSOP's and ensure all Process
Standards are similarly included on Audit Cards. See suggestion C0-CC06-91
OTmvTAmm™	
/>CAx/-r	40hr7~
PERSON RESPONSIBLE: ^ S4VL , g. A/t
-------
SPARROWS.POINT FUWT
CORRECTIVE ACTION REPLY
CHECK APPROPRIATESTEP:


ACAR ( )
FIX IT ( X ) C0-CC03-91
SUGGESTION { )
PRELIMINARY (
) FINAL ( )
AREA:


Cake Ovens - Coal Chemical


KVSOP 06.02.01 indicates use of an Individuals, Moving Range Chart.
Chart iy actually an X-Bar, R chart.
COkRECTIVE ACTION PUN;	.
Aaj x, M/i cjtstfur wu- usee.
PC/1. KsjS&P Cf. 01,6 /.
™Nkts™: o-sw.r.^rTr
PH0WSE0 COMPLETION DATE: "	' , ^	
Mill/
corr/act/reply-EAF3

L-30

-------
SPARROWS POINT PLANT
CORRECTIVE ACTION REPLY
CHECK APPROPRIATE STEP:			
ACAR { )	FIX IT ( X ) CQ-CC04-91	SUGGESTION ( )
PRELIMINARY ( )	FINAL ( )
MZF.	
Coke Ovens / Coal Chemical
OBSERVATION/RECOMMENDATION:	~~	——
KVSOP 06.01.02 states, "Tar temp, in full dehydrator must be maintained
between 80 and 90 degrees	Operator was reporting 90 degrees on his
report though temperature gauge, after being wiped clean of grime, read. 100°.
This incident underscores implementation of Process Standards that are valid
and Operators are familiar with. See suggestions C0-CC06-91.
mterivE action plan:	;
p/LAC*nc.	r> -
PLkiUN ULSPUNSIBLE: ^	
PrOMSSD COMPLETION DATE:	
en I?/
corr/act/reply-EAF3
CM?c
-------
SPARROWS POINT PLANT
CORRECTIVE ACTION REPLY
CHECK APPROPftlATT STEP:

ACAR ( ) FIX IT ( )
SUGGESTION ( X ) C0-CC06-91
PRELIMINARY ( )
FINAL ( )
aREA:

Coke Ovens / Coal Chemical
. ' i i » '

UIJiSERVATION/RECOMMENDATION:
The key issue for the Coal Chemical Plant relative to the Quality System at
the present, is. the effective development and Implementation of Process
Standards in conjunction with the new- plant scheduled; to start up in
September.
While undergoing training on the new Foxboro process control system,.
Operators are monitoring hypothetical system pressures, temperatures, flow
rates, etc. that are the sane as those that will be identified, in Process
Standards. Ideally, alongside this training, Operator Input can be used to
develop Process Standards for the new operations. Expected benefits would
be:
*	Development and review of Process Standards with Operators
throughout learning curve.
*	Implementation of valid Process Standards as a result of Operator's
familiarity, "buy-in", of well reviewed Process Standards and
KYSOP's.
*	Quality System will be 1n place for start-up of the facility.
CORRECTIVE ACTION PUT:	
K\JS0 PS PO/L aJSUj &*€>'<-
HAC F- JF-	C/tC*t(CsfC f^CA^T
S\) CG T~/
PLkbON kt^MblBU: p-<5
-------
SPARROWS POINT PLANT
CORRECTIVE ACTION REPLY
CHECK APPROPRIATE STEP:	
ACAR ( )	FIX IT ( )	SUGGESTION ( X ) C0-CC07-91
PRELIMINARY ( )	FINAL ( )
MT7H	:		
Coke Ovens / Coal Chemical
OB$EftvATION/RECOMMENDATION:	
Training and documentation of training of employees in spill prevention, time
spent in various positions, and or new Foxboro system is thorough and well
maintained. Documentation of Operator's time spent in various positions will
become cumbersome after some time and would lend itself well to routine input
into a computerized system (HRIS, LOTUS, etc.)
CORRECTIVE ACTION PlAN:	
THfS Is ErtT&kek 715 TfC
& 7.Z~/VAft 5
(haTs-, ' PC.	t-Tlt)
PERSON RESPONSIBLE:
PROPOSED COMPLETION DATE:	:	
/ /
corr/act/reply-EAF3
c Of^fL FT £7)
i ; L-r33 ]

-------
a
x	COKE OVENS - INTERNAL AUDIT
STATUS AS OF 09/11/91
1989 CORPORATE INTERNAL AUDIT
8 FINDINGS
8 COMPLETE
1991 PLANT INTERNAL AUDIT
18 FINDINGS
10 COMPLETE
OUTSTANDING FINDINGS
DESCRIPTION
CORRECTIVE
ACTION PLAN
PERSON
1. TRAINING PROGRAM
2. SERVICE VENDOR
AUDITS
3. COAL CHEMICAL
KVSOP*S
4. CALIBRATION
5.	COAL MIX
PROCEDURE
6.	DEVELOP PRODUCT
STANDARDS
A.	DEVELOP RECORDS OF
QUALIFICATIONS
B.	ESTABLISH TRAINWG
REQUIREMENTS CHECKLIST
A. PERFORM AUDIT IF VENDOR
SUPPLYING CRITICAL
SERVICES (4 IDENTIFIED)
A. REVISE/COMBINE A * B
B» DEVELOP NEW
DISTRIBUTION
A. IDENTIFY STANDARD
INSTRUMENT BY SERIAL
NUMBER
A. DOCUMENT PROCEDURE
A.	COAL
B.	COKE
WILLIAMSON/
GEN FOREMAN
CORP QA/
FLETCHER
D. SAUL/
B. ARNETT
S. DOWNEY
WILLIAMSON
B. ARNETT
PROPOSED
COMPLETION
DATE
10/15/91
11/30/91
09/20/91
12/30/91
10/15/91
09/20/91
COMPLETE
L-34
" i

-------
COKE OVENS - INTERNAL AUDIT
STATUS AS OF 09/11/91
1989 CORPORATE INTERNAL AUDIT
8 FINDINGS
8 COMPLETE
1991 PLANT INTERNAL AUDIT
18 FINDINGS
10 COMPLETE
OUTSTANDING FINDINGS CONT
PROPOSED
CORRECTIVE	PERSON	COMPLETION
DESCRIPTION	ACTION PUN	RESPONSIBLE DATE
7.	PAST DUE
CALIBRATION OF
5Kg NIST
CLASS P WEIGHT
8.	SYSTEM TO
CONTROL SHELF
UFE OF ALL
CHEMICALS
CALIBRATE	KOWALCZYK 10/01/91
DEVELOP AND IMPLEMENT KOWALCZYK 10/01/91
SYSTEM
L-35

-------
/	I
oj
*,
Uhy
BY: -r.r./H^/K/cK
BADGE: 3/4 -IJ! €
CONTACT ( Ad)
ACCOMPANIED pf 05/M/KA
DISTRIBUTION
YES
NO
COMMENTS:
1. IS THERE A DISTRIBUTION QCP?
J


2. ARE THE QCP•S,KVSOP¦S AND SPI'S DISTRIBUTED PER THE
DISTRIBUTION QCP?
J


UNCONTROLLED DOCUMENTS
YES
NO
N/A
COMMENTS:
1. IS AREA VOID OF UNSIGNED OR UNDATED OP. INST.?
>/

XXX

2. ARE TEMPORARY SIGNED AND ORIGINAL DATE OF OP INST
LESS THAN 3 MONTHS OLD?


J

CHANGE LOG
YES
N/A
COMMENTS:
1. HAVE ANY CHANGES IN OPERATING PRACTICES, GRADES,
SUPPLIERS AND EQUIPMENT OCCURRED IN THE CURRENT QTR?
J
r

2. HAVE THE ABOVE CHANGES BEEN ENTERED INTO THE CHANGE
LOG SYSTEM?
YES
NO
N/A
COMMENTS:
y



DOCUMENT CONTROL
YES
NO
N/A
COMMENTS:
1. DO THE KVSOP'S HAVE THE APPROPRIATE SIGNATURES?
J



2. DO THE REVISION #'S AND EFFECTIVE DATES AGREE WITH THE
REVISION #«S AND EFFECTIVE DATES IN THE M.O. COPY?
•J



3. DO THE KVSOP'S REFERENCE THE SPI AND QCP'S WHEN
APPROPRIATE?


J

4. DO THE AUDIT CARDS AGREE WITH DOCUMENTS IN THE BOOK OR
IS THERE EVIDENCE A REVISION IS BEING PROCESSED?
J




-------
KVSOP'S
1.	Ol-.Ol.Dl
2.	dZ-.d*-- 03
3.	<»*-~ 
-------
SPC CHARTS

area: ////l
BY: J.fT. FMNni cK
badge: 3/4-/?/*"
DATE: fft-ijll

YES
NO
N/A
IS SPC REQUIRED FOR THE AREA?
IF NO, DO NOT CONTINUE.
J



1. ARE THE SPC CHARTS IN THE AREA VALID APPLICATIONS?
A.	CHARTS OF SINGLE MEASUREMENT THAT ARE X, MR OR
SPECS OR TOLERANCE CHARTS.
B.	X-BAR, R CHARTS
C.	ATTRIBUTE CHARTS (P CHART)
D.	OTHER:
J



2. ARE THE LIMITS APPLICABLE TO THE CONTROL CHART?
X-BAR, R CHARTS MUST HAVE CONTROL LIMITS
NOT SPECIFICATIONS.
J



3. ARE THE DATA POINTS PLOTTED CORRECTLY ON THE CHART
(X-BAR, INDIVIDUALS, RANGES)?
J



4. ARE OUT OF CONTROL POINTS DOCUMENTED ON THE CHART?
J

-j
MOTCI *HTlL Tttlt ^OfTH, 0*r OF ClMrKtJ-
WfAt fi 9 Vtl* 01* 1= •/ICAAA/'-f
5. IS THERE A REVISION # AND DATE ON THE CHART?
J


Hep'AX. 0*7 HfoT «v tw£ c>/a>h . J TAnrim 4-
tHij Jwt 014.IHHM
6. IS THE BASE PERIOD FOR CALCULATION OF THE CONTROL
LIMITS IDENTIFIED?
J


\_Tt> flfrcnAfny tN TWt WAfcr.
KVvfof 0 1,0*. Of ftEAT/Ati "" W TEf\fS.~
'-HAtfs IN All i\x" »<\TTCfV< CAHf-l /LoflAy
I
02/04/91

-------






P&ES THE UNIT/PROCESS
EQUIPMENT REQUIRE CALI-
BRATION MAINTENANCE?
VES
J
N/A
A
DOES THE SYSTEM HAVE
POSITIVE IDENTIFICATION t
CONTROL OF ALL MEASURING
DEVICES? Jt/U/U- NiS.
YES
NO
/
N/A
B
13 THERE AN ESTABLISHED
FREQUENCY OP CALIBRATION
FOR ALL EQUIPMENT?
YES
J
NO
N/A
C
ARK HE CORDS OF CALIBRATION
KEPT?
7
NO
N/A
D
DO CALIBRATION RECORDS
INCLUDE AS FOUND/AS LEFT
RESULTS?
YES
v/
NO
N/A
E
DO CALIBRATION RECORDS
IDENTIFY THE PIECE OF
EQUIPMENT USED TO HAKE THE
CALIBRATION?
YES
J
HO
N/A
PL
: K
u>
ARE STANDARDS TRACEABLE TO
N.I.S.T. OR OTHER
ACCEPTABLE SOURCE?
YES
J
NO
N/A
	
IS THERE A SYSTEM (LABELS
OR EQUIVALENT) TO INDICATE
DATE OF CALIBRATION, BY
WHOM AND NEXT DUE DATE?
YES
J
NO
N/A
H
ARE THERE DOCUMENTED
CALIBRATION PROCEDURES
(DO0.U8 GOVT.MFG.BSCO)?
YES
J
NO
N/A
I
OOES THE PROCEDURE INCLUDE
AN ACCEPTABLE TOLERANCE
(RANGE,PARAMETER) FOR THE
ACCURACY OP THE INSTRUMENT
CHARACTERISTIC BEING
CALIBRATED?
YES
J
NO
N/A
J
DOES THE PROCEDURE
ADDRESS CORRECTIVE ACTION
FOR THE PRODUCT PRODUCED
DURING THE OUT OF
CALIBRATION PERIOD?
YES
NO
N/A
comments
/,A ~ J"i:/UAL NOS. WKO Tt ȣ
f\rJ)tML9 To THJC f)r
-------
((^') °/')	/P.Yhdluu
QUALITY SYSTEM AUDIT ' IdATE: 7-8-91
DEPARTMENT: yX}/
AREA: CImL tMkidiiM
BY: #£M/llE£
BADGE: -aS2.
CONTACT: <7
ACCOMPANIED: jr
DISTRIBUTION
YES
NO
COMMENTS:
1- IS THERE A DISTRIBUTION QCP? CO¦ QAG -OOZ
t/


2. ARE THE QCP' S, KVSOP¦ S AND SPI'S DISTRIBUTED PER THE
DISTRIBUTION QCP?
~


UNCONTROLLED DOCUMENTS
YES
NO
N/A
COMMENTS:
1. IS AREA VOID OF UNSIGNED OR UNDATED OP. INST.?
/

XXX

2. ARE TEMPORARY SIGNED AND ORIGINAL DATE OF OP INST
LESS THAN 3 MONTHS OLD?


l/

CHANGE LOG
YES
N/A
COMMENTS:
1. HAVE ANY CHANGES IN OPERATING PRACTICES, GRADES,
SUPPLIERS AND EQUIPMENT OCCURRED IN THE CURREHT QTR?
/


2. HAVE THE ABOVE CHANGES BEEN ENTERED INTO THE CHANGE
LOG SYSTEM?
YES
NO
N/A
COMMENTS:
~



DOCUMENT CONTROL
YES
NO
N/A
COMMENTS:
1. DO THE KVSOP*S HAVE THE APPROPRIATE SIGNATURES?
~



2. DO THE REVISION #'S AND EFFECTIVE DATES AGREE WITH THE
REVISION #'S AND EFFECTIVE DATES IN THE M.O. COPY?
/



3. DO THE KVSOP'S REFERENCE THE SPI AND QCP'S WHEN
APPROPRIATE?


/

4. DO THE AUDIT CARDS AGREE WITH DOCUMENTS IN THE BOOK OR
IS THERE EVIDENCE A REVISION IS BEING PROCESSED?
/



ft/PTE .* /*f£W0l/T Jjurf/lt "a/01 iAZsrf /"PJo/l&f/
/flr S/)/j	yiv,

-------
SELECT AT RANDOM
KVSOP'S	REV # REV DATE YES NO
Q/. iS.Of	3	'o/"/s9	ill —
2. e>4,o!	S	to/u Js/ TedJouse	
~ N°3 Station	

-------
SPC CHARTS

AREA: doAi /Jah&ua/G
BY:
BADGE: -os2
DATE S ^ py

YES
NO
N/A
IS SPC REQUIRED FOR THE AREA?
IF NO, DO NOT CONTINUE.
/



1. ARE THE SPC CHARTS IN THE AREA VALID APPLICATIONS?
A.	CHARTS OF SINGLE MEASUREMENT THAT ARE X, MR OR
SPECS OR TOLERANCE CHARTS.
B.	X-BAR, R CHARTS
C- ATTRIBUTE CHARTS (P CHART)
D. OTHER:
/


ArrtfOf af,04 o/ stzs covr&>tr-
% Vf "or A"SS
Xvsop o/. os.o/ £>jr/a C0AS7XOL.
X. & Mi it /¦£/ .
2. ARE THE LIMITS APPLICABLE TO THE CONTROL CHART?
X-BAR, R CHARTS MUST HAVE CONTROL LIMITS
NOT SPECIFICATIONS.
/



3. ARE THE DATA POINTS PLOTTED CORRECTLY ON THE CHART
(X-BAR, INDIVIDUALS, RANGES)?
~



4. ARE OUT OF CONTROL POINTS DOCUMENTED ON THE CHART?



OUT-OP-court"'- flOtUrt W/fH/At SPBC 4A)B w
JH/s /Atxrjwca S£*>erir/At- ft Qcaa. a'.o*.af
5. IS THERE A REVISION # AND DATE ON THE CHART?
/



6. IS THE BASE PERIOD FOR CALCULATION OF THE CONTROL
LIMITS IDENTIFIED?
/



02/04/91

-------
calibration system audit
1.
DOES THE UNIT/PROCESS
EQUIPMENT REQUIRE CALI-
BRATION MAINTENANCE?

YES
/
N/A
A
DOES THE SYSTEH HAVE
POSITIVE IDENTIFICATION t
CONTROL OF ALL MEASURING
DEVICES?
YES
/
NO
N/A
B
IS THERE AN ESTABLISHED
FREQUENCY OF CALIBRATION
FOR ALL EQUIPMENT?
VES
~
NO
H/A
C
ARE RECORDS OF CALIBRATION
KEPT?
YES.
V
NO
N/A
D
DO CALIBRATION RECORDS
INCLUDE AS FOUND/AS LEFT
RESULTS?
YES
l/
NO
N/A
E
DO CALIBRATION RECORDS
IDENTIFY THE PIECE OF
EQUIPMENT USED TO HAKE THE
CALIBRATION?
YES
HO
l/
H/A
F
ARE STANDARDS TRACEABLE TO
N.I.S.T. OR OTHER
ACCEPTABLE SOURCE?
YES
NO
H/A
c/
I-1
IS THERE A SYSTEH (LABELS
OR EQUIVALENT) TO INDICATE
YES
NO
N/A
F--
DATE OF CALIBRATION. BY
./



Uj i
HHOH AND NEXT DUE DATE?









H
ARE THERE DOCUMENTED
CALIBRATION PROCEDURES
(DOD.US GOVT,HFC, BSCO) ?
YES
/
NO
N/A
I
DOES THE PROCEDURE INCLUDE
AM ACCEPTABLE TOLERANCE
(RAMCE,PARAMETER) FOR THE
ACCURACY OF THE INSTRUMENT
CHARACTERISTIC BEING
CALIBRATED?
YES
/
NO
N/A
J
DOES THE PROCEDURE
ADDRESS CORRECTIVE ACTION
FOR THE PRODUCT PRODUCED
DURING THE OUT OF
CALIBRATION PERIOD?
YES
NO
N/A
/
COHHENTS (SVS6P C/.OS.O/ SfA L£S
frecjiifncy (vvfftAA it und^rs-Jocd, 6"*
no /n-*/ tiuf da** appears On -/tirm
4kW ¦>/."'ir/?> cprrsfL/Pf	.
B
CALIBRATION SYSTEM AUDIT




I.
ARE HAND TOOLS (TAPES/
MICROMETERS) USED FOR
MEASURING AND TESTING OF
PRODUCT?

YES
N/A
/
A
IS THERE A CALIBRATION
SYSTEM?
YES
NO
N/A
B
DOES THE SYSTEH HAVE
POSITIVE IDENTIFICATION «
CONTROL OF ALL MEASURING
DEVICES?
YES
NO
N/A
C
IS THERe AN ESTABLISHED
FREQUENCY OF CALIBRATION
FOR ALL EQUIPMENT?
YES
NO
N/A
D
ARE RECORDS OF CALIBRATION
KEPT?
YES
NO
N/A
E
DO CALIBRATION RECORDS
INCLUDE AS POUND/AS LEFT
RESULTS?
YES
NO
N/A
F
DO CALIBRATION RECORDS
IDENTIFY THE PIECE OF
EQUIPMENT USED TO HAKE THE
CALIBRATION?
YES
HO
N/A
G
ARE STANDARDS TRACEABLE TO
N.I.S.T. OR OTHER
ACCEPTABLE SOURCE?
YES
NO
H/A
H
IS THERE A SYSTEM (LABELS
OR EQUIVALENT) TO INDICATE
DATE OF CALIBRATION, BY
HHOH AHD NEXT DDE DATE?
YES
NO
N/A
I
ARE THERE DOCUMENTED
CALIBRATION PROCEDURES
(DOD.US GOVT,HFG,BSCO)?
YES
NO
N/A
J
DOES THE PROCEDURE INCLUDE
AM ACCEPTABLE TOLERANCE
(RANGE, PARAMETER) FOR THE
ACCURACY OF THE INSTRUMENT
CHARACTERISTIC BEING
CALIBRATED?
YES
NO
N/A
K
DOES THE PROCEDURE
ADDRESS CORRECTIVE ACTION
FOR THE PRODUCT PRODUCED
DURING THE OUT OF
CALIBRATION PERIOD?
YES
NO
H/A
COMMENTS
C CALIDRATton SYSTEM AUDIT
. ARE INSTRUMENTS (ROCKWELL,
ROFILOMETER,TENSILE TESTER.LAB.
QUIPHENT ETC. ) USED TO DETERMINE
RODUCT ACCEPTANCE?
YES
N/A
IS THERE A CALIBRATION
SYSTEM?
YES
NO
N/A
B DOES THE SYSTEM HAVE
POSITIVE IDENTIFICATION t
CONTROL OF ALL MEASURING
DEVICES?
YES
NO
N/A
IS THERE AN ESTABLISHED
FREQUENCY OF CALIBRATION
FOR ALL EQUIPMENT?
YES
NO
H/A
ARE RECORDS OF CALIBRATION
KEPT?
NO
N/A
DO CALIBRATION RECORDS
INCLUDE AS FOUND/AS LEFT
RESULTS?
YES
NO
N/A
DO CALIBRATION RECORDS
IDENTIFY THE PIECE OF
EQUIPMENT USED TO HAKE THE
CALIBRATION?
YES
N/A
ARE STANDARDS TRACEABLE TO
N.I.S.T. OR OTHER
ACCEPTABLE SOURCE?
YES
NO
H/A
19 THERE A SYSTEM (LABELS
OR EQUIVALENT) TO INDICATE
DATE of CALIBRATION, BY
WHOM AND NEXT DUB DATE?
YES
NO
N/A
ARE THERE DOCUMENTED
CALIBRATION PROCEDURES
(DOD,US GOVT,HFC,BSCOJ?
N/A
DOES THE PROCEDURE INCUJDE
AN ACCEPTABLE TOLERANCE
(RANGE, PARAMETER) FOR THE
ACCURACY OF THE INSTRUMENT
CHARACTERISTIC BEING
CALIBRATED?
YES
N/A
DOES THE PROCEDURE
ADDRESS CORRECTIVE ACTION
FOR THE PHODUCT PRODUCED
DURING THE OUT OF
CALIBRATION PERIOD?
YES NO
N/A
COMMENTS

-------
AUDITS OF COKE OVENS PROCESS STANDARDS
11/12 BATTERIES % NON-COMPLIANCE
% NON-COMPLIANCE
10
9
0
7
6
5
4
3
2
1
0
mm
05/25 06/22 07/20 08/17 09/14 10/12 11/09 12/07 01/04
~ - 100% COMPLIANCE
COKE OVENS - 11/12 BATTERIES
KVSOP CHECKLIST CARD ANALYSIS - BIHEEK'E ll'25'9i
02.01 01A
TASK
DAMPER OUT. ARE DAMPERS DOWN SEAL INC OFF FOUL CAS FROH THE OVEN
S

-------
AUDITS OF COKE OVENS PROCESS STANDARDS
COAL HANDLING % NON-COMPLIANCE
NON-COMPLIANCE
05/25 06/22 07/20 08/17 09/14 10/12 11/09 12/07 01/04
• - 100% COMPLIANCE

-------
Section 3
Monthly Progress Reports
L-46

-------
KIDC DEMONSTRATION PROJECT
BETHLEHEM STEEL CORPORATION
SPARROWS POINT, MARYLAND
MONTHLY REPORT OF
SAMPLING AND TESTING PROGRAM ACTIVITIES
NOVEMBER, 1991
GENERAL OVERVIEW
The performance demonstration of the Kress system continued in November.
Visible emission observations continued to be performed during the month and
coke samples continued to be obtained. In addition, video recordings of both the
conventional pushes and Kress pushes were made. Other activities related to the
baseline sampling and analysis program continued during the month. Testing of
the Kress system ended on November 26 as a result of the idling of the coke
batteries in early December. Attachment 1 indicates the percent completion of
the various, aspects of the sampling and testing program through the end of
November. Compilation and analysis of all data collected during the testing
program will be performed during December and January.
Project Team Meetings
A. meeting was held on December 5 with all personnel involved in the testing
program to discuss the concent and format of the final report. A follow up
meeting will be scheduled for early January to evaluate progress on the data
analysis currently being performed.
Demonstration Program
The Kress system accepted a total of 112 pushes during the performance testing
in November. During Octobeti a total of 1S8 pushes were accepted rather than the
159 pushes reported last month. This gives a total of 321 pushes accepted by the
Kress system since start up in June. Visible emission observations continued in
November and samples of the Kress coke were obtained. Video recordings of both
the Kress and conventional pushes were made during this period as well.
QA/QC Activities
As a result of the audit performed by EPA's contractor in October, visible
emission observations were performed of five Kress pushes by three certified
observers at the same time. The results of this QA/QC activity are presented in
attachment 2.
L-47

-------
-2-
COflL AND COKE QUALITY
Coke Screening
One sample of Kress coke was obtained for every set of chree pushes taken by
Kress in November. These samples were in addition to the conventional quenched
coke samples which continued to be collected. These samples are being screened
to evaluate the size differential between this coke and conventional quenched
coke. This information will be used to evaluate the impact on blast furnace
performance.
Drop Shatter Test
Drop Shatter Testing of Kress coke- continued in November.
Hampton Roaos Testing Lab
Testing or Kress coke for coke reactivity index (CRI) and coke strength after
reaction (CSR) continued to be conducted by Hampton Roads Testing Lab in
November. These data will be compared to the CRI/CSR data for conventional
quenched coke over the same period.
BLAST FURNACE PERFORMANCE EVALUATION
Bethlehem's research department has begun	an evaluation of the Kress coke
quality data so that inputs to the Balwax	model can be developed. This model
will be used to determine cost advantages	or disadvantages of using Kress coke
vs. conventional quenched coke.
DOOR EMISSIONS MONITORING
Collection of jaily door emission data continued during the month.
PUSHING EMISSION MONITORING
Visible emission observations of Kress pushes continued to be performed by BCM,
Inc. throughout November.
QUENCH WATER MONITORING
Sampling of quench and makeup waters continued in November.
L-48. |

-------
-3-
Nov#mber, 1991
Monthly Report
VIDEO TAPING
Video taping of conventional and Kress pushes continued in November.
AREA MONITORING
Baseline samples not suspended particulate and benzene soluble matter in the
area of the coke door machine continued in November. In addition, samples were
obtained in November from the Kress carrier.
KRESS BOX VOC MEASUREMENTS.
Testing of the Kress boxes by Keystone Environmental Resources was conducted on
October 20 & 31. This testing was performed to determine a number of volatile i
semi-volatiie organics including polynuclear aromatics, phenols, cresols, and
phthalates held within the box during the cooling cycle. A report of the testing
results from Keystone is expected by the middle of December.
KRESS BOX HEAT TRANSFER CALCULATIONS
Bethlehem's Research Group has agreed to assist in performing heat transfer
calculations from the Kress box. These calculations were begun in November.
Prepared by: A. G. Ossman
December 10, 1991
L-49

-------
December 10, 1991
ATTACHMENT 1
KRESS TESTING - PERCENT COMPLETION OF BASELINE TEST PLAN THROUGH NOVEMBER
Coal Analyses
No. of Samples
Completed
262 days
No. of Samples
Needed
mo days
Percent
Complet ion
>100%
Coke Analyses
Hampton Roads
(CRI/CSR)
Drop Shatter Test
VEO Pushing/Travel
VEO Pushing
( from TS.- PS)
Video Pushing/
Travel/Discharge
Door Emissions.
Quench Water-TCLP
Makeup Water-TCLP
Quench Chem. Anal.
MaKeup Chen. Anal.
Area Samples
GC/MS
GC/MS-QA
SP
ESQ
SP/BSO-QA
Amb. Air
277 days.
152 days
35
580 pushes
528 pushes
23 days
180
3
3
19
18
3
0
53
46
4
2
180 days
180 days
40
260
260
13
180
3
3
25
25
6
1
50
50
5
3
>100%
84%
88%
>100%
>100%
>100%
100%.
100%
100%
76%
72%
50%
0
>100%
92%
8G%
S6 %
\ L-50

-------
-2-
December 10, 1991
KRESS TESTING - PEBCENT COMPLETION FOR DEMONSTRATION TEST PLAN
THROUGH NOVEMBER
Coke Analyses
Hampton Roads
(CRI/CSR)
Drop Shatter Test
VEO Pushing/Travel
VEO Pushing
(£rom Ts/PS)
VEO Cooling Cycle
VEO Kress Burner
Video Pushing/
Travel
No. of Samples
Completed
90
90
72
29
29
0
29
39
Video Ccoiing/Discharge 27
Video Burner
Door Emissions
Makeup Chem. Anal.
Area Samples
GC.'MS
GC.MS-QA
SP
BSO
SP/BSO-QA
Kress Box Test
34
SI
3
15
15
L»
1
No. of Samples
Needed
150
150
40
98 (days)
98 (days)
ISO (days)
98 (days)
46 (pushes)
30
30
180
3
S
1
50
50
5
1
Percent
Complet ion
60%
60%
>100%
30%
30%
0
30%
85%
90%
>100%
34%
100%
0
0
30%
30%
0
100%
¦1
Lr51 I
'"¦v	!

-------
ATTACHMENT 2
KRESS PUSHING EMISSION OBSERVATION QUALITY ASSURANCE DATA


NOVEMBER 25,
1991



OPACITY




Max. | Max.
| Max.



Stack | Stack
1 Opacity



Opacity|Opacity
I Box/Jamb



Before | After
1 Interface



Ignition|lgnition
1

OVEN NO.
OBSERVER 1
OBSERVER 2
OBSERVER 3
AVERAGE
1148
25/5/25
20/10/25
25/5/20
23.3/6.7/23.3
1151*
40/-/-
40/-/-
40/-/-
40/—/—
1153
20/10/10
15/10/10
10/10/15
15/10/11.7
1149
15/5/5
10/10/10
15/5/10
13.3/6.7/8.3
1172
20/10/10
15/15/10
15/10/10
16.7/11.7/10
AVERAGE
24/7.5/12.5
20/11.2/13.8
21/7.5/13.8
21.7/3.8/13.3
CUMULATIVE TIME OF EMISSIONS
Seconds|Seconds
During |Dur ing
Push (Travel
OVEN NO.
1148
1151
1153
1149
1172
AVERAGE
OBSERVER 1
60/-10
71/203
107/85
108/149
91/165
87.4/128.4
OBSERVER 2
66/43
75/200
110/85
79/152
83/175
82.6/131
OBSERVER 3
67/40
74/200
109/83
90/150
90/170
86/128.6
AVERAGE
54.3/41
73.3/201
108.7/04.3
92.3/150.3
88/170
85.3/129.33
* Note: On pusli 1151, no ignition of che stack'occur red and steam
interference prevented readings at the box/jamb interface.
L-52 j
)

-------
KIDC DEMONSTRATION PROJECT
BETHLEHEM STEEL CORPORATION
SPARROWS POINT, MARYLAND
MONTHLY REPORT OF
SAMPLING AND TESTING PROGRAM ACTIVITIES
OCTOBER, 1991
GENERAL OVERVIEW
The performance demonstration of the Kress system was conducted during October.
This demonstration consisted of nine pushes per day between the hours of 11am.
and 7pm. These pushes were accepted by the Kress system in groups o£ three with
a three hour cooling time between each group. During the demonstration, visible
emission observations were made and three coke samples per day were obtained. In
addition, video recordings of both the conventional pushes and kress pushes were
made. Extended testing of the Kress system will cont inue through November. Other
activities related to the baseline sampling and analysis program continued in
October. Attachment 1 indicates the percent completion of the various aspects of
the baseline sampling and testing program through the end of October.
Project Team Meetings
A visit by a number of personnel from EPA was made on October 17 to observe the
Kress operation. On this day, one successful push was observed but because of
power supply problems the remainder of pushes scheduled for Kress were
cancelled. These problems were corrected and the Kress system resumed operation
on October 16. An audit of the sampling and testing program was conducted on
October 29 to 31 by EPA•s contractor from Research Triangle Institute. In
addition, the Kress box testing conducted by Keystone Environmental Resources
during this period was observed.
Demonstration Program
The Kress system accepted a total of 15^ pushes during the performance testing
from October 1 to 31. During this period, visible emission observations were
made and samples of the Kress coke were obtained. Video recordings of both the
Kress and conventional pushes were made during this period as well.. This testing
will continue through November.
QA/QC Activities
An audii of the testing program was conducted by EPA's contractor from Research
Triangle Institute on October 29 to 31. This audit consisted of an extensive
review the data base collected to date and observation of the methods used by
Bethlehem's contractor, BCM Inc., in making visible emission observations.
Although not anticipated at this time, changes in the existing procedures will
made as the findings of the audit require and as they are reported co us.
L—53-

-------
-2-
October, 1991
Monthly Report
COAL AND COKE QUALITY
Coke Screening
One sample of Kress coke was obtained for every set of three pushes taken by
Kress in October. These samples were in add i t ion to the conventional quenched
coke samples which continued to be collected. These samples are being screened
to evaluate the size differential between this coke and conventional quenched
coke. This information will be used to evaluate the impact on blast furnace
performance.
Drop Shatter Test
Drop Shatter Testing of Kress coke was conducted in October and will continue
through November.
Hampton Roads Testing Lab
Testing of Kress coke for coke reactivity index (CRI) and coke strength after
reaction (CSR t were conducted by Hampton Roads Testing Lab in October. This test
will continue through November. These data will be compared to the CRl/CSR data
for conventional quenched coke over the same period.
BLAST FURNACE PERFORMANCE EVALUATION
No activities during the month.
DOOR EMISSIONS MONITORING
Collection of daily coke side and pusher side door emissions data are
cent inuing.
PUSHING EMISSION MONITORING
Visible emission observations of Kress pushes were performed five days per week,
by BCM, Inc. throughout October. In addition, observations of ten conventional
pushes per week continued in October. These observations will continue through
November.
QUENCH WATER MONITORING
Sampling of quench and makeup waters continued in October, A modification to the
CDS analytical procedure was initiated in October as recommended by Alliance
Corp. This change involves making the TDS determination at 103-105 C instead of
180 C as directed by the EPA method. This change should provide a better
estimate of particulate emissions when used with the emission formula developed
by Alliance Corp. Plans for obtaining water samples from the Kress cooling
system have been dropped from the program at EPA's request. This, is being done
so that efforts can be concentrated on other testing work which needs to be
completed before the batteries are idled. A sample of the makeup water to the
Kress cooling system was obtained, however, to ensure that this is essentially
the same as the conventional quench water makeup.
..Lr54

-------
-3-
October, 1991
Monthly Report
VIDEO TAPIMG
video taping of conventional and Kress pushes continued in October.
AREA MONITORING
Baseline samples for suspended particulate and benzene soluble matter in the
area of the coke door machine continued in October. In addition, samples were
obtained in October from the Kress carrier. This testing will continue through
November.
KRESS BOX VOC MEASUREMEMTS¦
Testing of che Kress boxes by Keystone Environmental Resources was conducted on
October 30 & 31. This testing was. performed to determine a number of volatile k
serai-volatile organics including polynuclaar aromatics, phenols, cresols, and
phthalates held within the box during the-cooling cycle. A report of the testing
results from Keystone is expected by the end of November or the beginning of
December.
KRESS BOX HEAT TRANSFER CALCULATIONS
Bethlehem's Research Group has agreed to assist in performing heat transfer
calculations from the Kress box. These calculations will be started in November.
Prepared by: A. G. Ossman
November 15, 1991
i
		\
L-55 |

-------
November 18, 1991
KRESS TESTING - PERCENT COMPLETION OF BASELINE TEST PLftN THROUGH OCTOBER
No. of Samples	No. of Samples
Completed	Heeded
Coal Analyses	262 days	180 days
Coke Analyses	277 days	180 days
Hampton Roads	152 days	180 days
(CRI/CSRJ
Drop Shatter Test	28	40
VEO Pushing/'Travel	542 pushes	260
VEO Pushing	528 pushes	260
(from TS/PS)
Video Pushing/	22 days	13
Travei/Di scharge¦
Door Emissions	180	180
Quench Water-TCLP	3	3
Makeup Water-TCLP	3	3
Quench Chera. Anal.	17	25
Makeup Cham. Anal.	16	25
Area Samples
GC, MS	1	6
GC/MS-QA	0	I
SP	53	50
BSO	4 6	50
SP/BSO-QA	4	5
Arab. Air	2	3
. L-56
Percent
Completion
>100% (continuing)
>100% (continuing)
84%
70%
>100% (continuing)
>100% (continuing)
>100% (continuing)
100% (continuing]
100%
100%
68%
64%
17%
0
>1001(cont inu ing)
92%
80%
6b*

-------
November 18, 1991
KRESS TESTING
PERCENT COMPLETION FOR DEMONSTRATION TEST PLAN
THROUGH OCTOBER
Coke Analyses
Hampton Roads
(CRI/CSR)
Drop Shatter Test
VEO Pushing/Travel
VEO Pushing
(from TS/PS)
VEO Cooling Cycle
VEO Kress Burner
Video Pushing/
Travel
No. of Samples
Completed
54
53
4Q
16
16
0
16
32
Video Cooling/Discharge 27
Video Burner
Door. Emissions
MaKeup Chem. Anal.
Area Samples
GC/MS
GC/MS-QA
SP
BSO
SP/BSO-QA
Kress Box Test
27
31
X
Q
0
5
5
0
1
No. o£ Samples
Needed
150
150
40
98 (days)
98 (daysJ
150 (days)
98 (days)
46 (pushes)
30
30
180
3
6
I
50
50
5
1
Percent
Complet ion
36%
35%
100%(cont inu ing)
16%
16%
0
16% •
70%
90%
90%
17%
a
0
0
10%
10%
0
100%
- L-57 1 !

-------
KIDC DEMONSTRATION PROJECT
BETHLEHEM STEEL CORPORATION
SPARROWS POINT, MARYLAND
MONTHLY REPORT OF
SAMPLING AND TESTING PROGRAM ACTIVITIES
SEPTEMBER, 1991
GENERAL OVERVIEW
Activities related to the baseline sampling and analysis program Cor the Kress
demonstration continued in September. We continued preliminary visible emission
observations and video recordings of Kcess pushes to monitor the progress of the
Kress start-up operations. Kress coke samples were obtained to establish a
baseline before the start of the performance demonstration. The performance
demonstration is currently scheduled for the month of October. Attachment 1
indicates the percent completion of the various aspects of the baseline sampling
and testing, program through the end' of September.
Project Team Meeting
A meeting to discuss the sampling and analysis program requirements during the
Kress performance test was- held on September 24. It was agreed that that the
performance test would be seven days a week and would Initially consist of nine
pushes each day between 11am and 7pm. The nine pushes would be taken in groups
of three with a three hour cooling time between each group. It was stated,
however, that Kress should maximize efforts to achieve a 24 hour operation. It
was also agreed that Kress should take pushes with or without the Kress door
machine functioning..
Demonstration Program
The Kress system has accepted a total of 51 pushes through the end of September.
The demonstration test program started on October 1. Preliminary Kress data
continued to be obtained during September to monitor the start-up progress and
to gain experience with visible emission observations and video taping of the
Kress sy-item prior to the October demonstration.
QA/OC Activities
An update of water sample QA/QC results are provided in Attachment 2. These
data indicate good precision and accuracy by the Homer Research Laboratory.
QA/QC samples for area monitoring data are provided in Attachment 3.
! i

-------
-2-
September, 1991
Monthly Report
COAL AND COKE QUALITY
Coke Screening
Ihe automatic coke screening equipment was installed in September. Starting in
October one sample of Kress coke will be obtained Cor every set of three pushes
taken by Kress in addition to the conventional quenched coke sample. The
screening device will allow the laboratory personnel to conduct these additional
sample screenings required.
Drop Shatter Test
Drop Shatter Testing of Kress coke will be initiated in October.
Hampton Roads Testing Lab
The representativeness of Kress coke samples continues to be problem e
because of water spayed on the coke at the receiver station to reduce
temperature. During October, some Of the Kress coke will be cooled overnight to
ensure that it is cool enough not to activate the receiver station water sprays.
BLAST FUBNACE PERFORMANCE EVALUATION
No activities during the month.
DOOR EMISSIONS MONITORING
Collection of daily coke side and pusher side door emissions data are
cont inuing.
PUSHING EMISSION MONITORING
Observation of baseline pushing emissions by BCM, Inc. continued in September.
Observation of Kress pushes initiated in August continued in September as well.
QUENCH WATER MONITORING
Sampling of quench and makeup waters continued in September. A second TCLP test
was performed on the quench and make-up waters in September. This test confirms
the earlier test result which indicated that the waters are not
characteristically hazardous. A modification to the TDS analytical procedure
will be initiated in. October as recommended by Alliance Corp. This change
involves making the TDS determination at 103-105 C instead of 105 C as directed
by the EPA method. This change should provide a better estimate of particulate
emissions when used with the emission formula developed by Alliance Corp. Plans
for obtaining water samples from the Kress cooling system have been dropped from
the program at EPA's request. This is being done so that efforts can be
concentrated on other testing work which needs to be completed before the
batteries are idled.
,L-59

-------
-3-
September, 1991
Monthly Report
VIDEO TAPING
Video taping of conventional and Kress pushes continued in September.
AREA MONITORING
Baseline samples for suspended particulate and benzene soluble natter in the
area of the coke door machine continued in September. Samples will be obtained
in October from the Kress carrier. Data from QA samples obtained are presented
in Attachment 3.
KRESS BOX VOC MEASUREMENTS.
A draft test protocol from Keystone Engineers has been reviewed by Bethlehem and
EPA. Keystone is currently revising the protocol to incorporate comments fro®
EPA and Bethlehem. This test work is currently scheduled for the end of October
or the first part of November.
Prepared! by: A. G. Ossman
October 11, 1991
¦- 1-60

-------
d'o-1
October 14, 1991
KRESS TESTING - PERCENT COMPLETION OF BASELINE TEST PLAN THROUGH SEPTEMBER
Coal Analyses
No. of Samples
Completed
261 days
No. of Samples
Needed
180 days
Percent
Complet ion
>100% (continuing)
Coke Analyses
Hampton Roads
(CRI/CSR)
Drop Shatter Test
VEO Pushing/Travel
VEO Pushing
(Erom TS/PS)
Video Pushing/
Travel/Discharge
Door Emissions-
Quench Water-TCLP
Makeup Water-TCLP
Quench Chem. Anal.
Makeup Chem. Anal.
Area Samples
GC/MS
GC/MS-QA
SP
BSO
SP/BSO-QA
Amb. Air
249 days
152 days
10
530 pushes
421 pushes
IS days
180
2
2
13
13
0
0
48
29
4
2
180 days
ISO days
40
260
260
13
180
3
3
25
25
50
50
5
3
>100% (continuing)
84%
25%
>100% (continuing)
>100% (continuing)
>100% (continuing)
100% (continuing)
66%
66%
52%
52%
0
0
96%
58%
30%
66%
L-61. i

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-2-
October 14, 1991
KRESS TESTING - PERCENT COMPLETION FOR DEMONSTRATION TEST PLAH
THROUGH SEPTEMBER
Coke Analyses
Hampton Roads
(CRI/CSR)
Drop Shatter Test
VEO Pushing/Travel
VEO Pushing
(from TS/PS)
VEO Cooling Cycle
VEO Kress Burner
Video Pushing/
Travel
Mo. of Samples
Completed
9
8
0
1
1
0
1
20
Video Cooling/Discharge 15
video Burner
Door Emissions
Makeup Chem. Anal.
Area Samples
GC/MS
GC/MS-QA
SP
BSD
SP/BSO-QA
Unflared Box
(End of push)
Unflared Box
(after cooling)
15
14
0
0
0
0
0
0
0
No. of Samples
Needed
150
150
40
98 (days)
98 (days)
150 (days)
98 (days)
45 (pushes)
30
30
180
3
6
1
50
50
5
2
Percent
Complet ion
6%
5%
0
II
1%
0
11
43%
50%
50%
8%
0
L-62 .

-------
No'
BETHLEHEM STEEL
Bethlehem, PA
INTEROFFICE CORRESPONDENCE
Research Department
Planning, Administration and
Technical Services
September 24, 1991
Ref:
1307
From: J. Y. Liu
To:
A. G. Gssman
Subject: KRESS PROJECT WATER SAMPLES FROM SPARROWS POINT
Reference: Project Plan for Kress Indirect Dry Cooling System, Jan. 10,1991
As requested, we have been analyzing the Kress Project water samples taken from the
Sparrows Point Coke Batteries 11 and 12 since March 1991. We follow EPA methods for
these analyses except for the Chloride determinations for which we use the Volhard titrimetric
method. As part of our quality assurance program and the project plan (Ref), we periodically
perform duplicate determinations and spike samples to check the precision and accuracy of
our results. Our most recent data are shown on the following pages. The concentration of
each determination, the agreement between the samples and the duplicates along with the
spike values and the % recoveries are reported. As you can see, the agreement between the
original samples and the duplicates are between 97% and 108% which are within the EPA
expectation of 90% and 110%. The spike recoveries are above 86% which are much better
than the EPA-accepted value, of 75%. Some analytes such as TDS, TSS, and oil/grease are
not appropriate to spike.
We have been discussing with you the possibility of having the EPA audit our laboratory. If
possible, please make the necessary contacts and then advise us who to contact to discuss
details of the audit. If you have any questions, contact me at x31 18.
J. Y. Uu
cc: WJRiley
LMStuart
PGCheplick
DAFLinchbaugh
" 	1
L-63 ;

-------
SPARROWS POINT COKE BATTERIES 11 & 12 MAKE-UP WATER AND SPIKES
Make-up
Sampling Make-up Water Spiked
Date	Water Spiked Value Recovery
CN, ppm
8-29-91
0.03
0.23
0.20
100
Hg, ppb
7-25-91
<5
9.3
10
93
Na, ppm
8-29-91
77
113
40
90
As, ppm
7-25-91
<0.02
0.096
0.10
96
Pb, ppm
7-25-91
<0.2
1.0
1.0
100
Ca, ppm
7-25-91
25
43
20
90
Hardness, ppm
7-25-91
134
188
50
108
TSS, ppm
7-25-91
7
NA
NA
NA
TDS, ppm
7-25-91
454
NA
NA
NA
S04, ppm
8-29-91
76
167
100
91
CI, ppm
8-29-91
92
135
50
86
Oil/Grease, ppm
7-25-91
14
NA
NA
NA
NH3-N, ppm
7-25-91
<1
10
10.6
92
Phenol, ppm
7-25-91
<0.05
0.39
0.40
97
NA: Sample is not spiked.
I 		*\
;	L-64

-------
SPARROWS POINT COKE BATTERIES 11 & 12 QUENCH WATER
Sampling Date
CN, ppm
8-29-91
Hg,ppb
7-25-91
Na, ppm
7-25-91
As, ppm
7-25-91
Pfc>, ppm
7-25-91
Ca, ppm
7-25-91
Hardness, ppm
7-25-91
TSS, ppm
7-25-91
TDS, ppm
7-25-91
S04, ppm
7-25-91
CI, ppm
7-25-91
Oil/Grease, ppm
9-10-91
NH3-N, ppm
7-25-91
Phenol, ppm
7-25-91
* Agreement = (Duplicate / Original) x 100%
Original	Duplicate Agreement*
%
0.12	0.13	108
<5	<5	100
124	123	99
0.07	0.07	100
<0.2	<0.2	100
62	60	97
269	269	100
560	590	105
793	805	101
172	176	102
189	186	98
<5	<5	100
1	<1	98
0.64?	0.68	106
L-65

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October 11, 1991
ATTACHMENT NO¦ 3
KRESS PROJECT COKE OVEN AREA SAMPLS QA
DATE	TOTAL PARTICULATE MATTER
(MG/M3)
5/13/91	13.90
5/13/91	8.22
BENZENE SOLUBLE ORGAHICS
(MG/M3)
5. 44
5. 00
7/31/91
7/31/91.
22.35
16.66
1.10
0.84
8/01/91
8/01/91
7.64
3.76.
1.28
1.67
9/13/91.
9/13/91
5 .68
3. 2 3
N. A.
N. A.
N.A.- Not available at the present time. Waiting on results from the lab.
L-66

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KIDC DEMONSTRATION PROJECT
BETHLEHEM STEEL CORPORATION
SPARROWS POINT, MARYLAND
MONTHLY REPORT OF
SAMPLING AND TESTING PROGRAM ACTIVITIES
AUGUST, 1991
GENERAL OVERVIEW
Activities related to the baseline sampling and analysis program for the Kress
demonstration continued in August. We continued preliminary visible emission
observations and video recordings of Kress pushes to monitor the progress of the
Kress start-up operations. Kress coke samples were obtained to establish a
baseline before the start oE the performance demonstration. The performance
demonstration is currently scheduled tor the month of October. Attachment 1
indicates the percent completion of the various aspects of the baseline sampling
and testing, program througn the end of August.
Project Team Meeting
A.pre-audit survey by EPA and their contractor from Research Triangle Institute
was held on August 12 - 14. During this visit, QA/QC procedures and sampling
methods were reviewed. EPA recommended during the visit that their consultant
from Alliance Corp visit Sparrows Point to observe the quench cower design and
operation to develop an estimate of quench tower emissions. Bethlehem agreed and
Alliance Corp's J. Jeffery visited Sparrows Point on August 29. as a'result of
this visit, the quench water sampling location was changed. J. Jeffery will
issue a letter report of his observations with his suggested empirical
correlations- for estimating the quench tower particulate emissions. The
correlation will be based on TDS concentration of the quench water used.
Demonstration Program
The Kress system has accepted a total of 33 pushes through the end of August.
The demonstration tesc program is currently scheduled to start in October.
Preliminary data will be obtained prior to the demonstration to monitor the
start-up progress and to gain experience with visible emission observations and
video tapping of the Kress system prior to the October demonstration.
QA/QC Activities
QA/QC results for water samples obtained during July are provided in Attachment
2. These data indicate good precision and accuracy by the Homer Research
Laboratory. Other QA/QC samples for area monitoring and visible emission
monitoring are planned for September. Bethlehem's corporate QA department has
agreed to take a lead role in the performance of audits for contracted services
related to this project. A meeting was held between the 'sampling and testing
manager and the plant QA department to discuss the development.of audit
checklists. These checklists are currently being developed.

-------
-2-
August, 1991
Monthly Report
COAL AND COKE QUALITY
Coke Screening
The automatic coke screening equipment has been delivered, installation by
plant personnel will occur in September. It is hoped that this installation can
be completed before the start of the performance test program in October. The
screening device will allow the laboratory personnel to conduct the extra number
of sample screenings required by the KIDC test plans. It will also provide more
consistent screening procedures than the manual screening method now being used.
Until this equipment is received and installed/ the laboratory will use overtime
to process the additional number of samples.
Drop Shatter Test
Drop Shatter Testing of Kress coke will be initiated in September. This testing
is planned over a 20 week period.
Hampton Roads Testing Lab
Preliminary testing of Kress coke samples for CSR and CHI was initiated in
August to monitor the start-up progress of the Kress process. The
representativeness of these samples is questionable because of water spayed on
the coke at the receiver station to reduce temperature. Methods will be used, on
future samples to obtain truly dry quenched coke samples.
BLAST FURNACE PERFORMANCE EVALUATION
No activities during the month.
DOOR EMISSIONS MONITORING
Collection of daily coke side and pusher side door emissions data are
continuing. Multiple readings of doors for QA/QC were obtained in August to
evaluate Che accuracy and- precision of the data being collected.
POSHING EMISSION MONITORING
Observation of baseline pushing emissions by BCM, Inc. continued in August.
Observations are currently scheduled for two days each week for 10 pushes each
day. Observation of Kress pushes was also initiated in August in preparation for
the performance demonstration.
QUENCH WATER MONITORING
Sampling of quench and makeup waters continued in August. The sampling location
for quench water was changed at the end of the month as recommended by EPA's
consultant from Alliance Corp. This new sampling location should provide a
better estimate of TDS in the quench water which will be used in developing an
estimate for particulate emissions. Results of TCLP analysis of quench and
makeup waters obtained in July indicate that the water is not hazardous. A
second TCLP test is planned for September.
L-68

-------
-3-
August, 1991
Monthly Report
VIDEO TAPING
Video taping of conventional pushes on 11 & 12 batteries continued in August.
Videos are currently being taken, once per week from two angles simultaneously.
This program will continue for the next several months. Additional videos of
pushes with the kress system have been initiated as well to monitor the start-up
progress.
Baseline samples for suspended particulate and benzene soluble matter in the
area of the coke door machine continued in August. Additional samples will be
obtained in the near future for volatiles and semi-volatiles as well as a number
of quality assurance samples and background ambient air samples.
A field survey with Keystone Environmental Resources, Inc. was conducted	in
August so that a testing protocol can be developed to perform this work.	We
have received a recommended test protocol from Keystone and will forward	it to
EPA for their comments, and approval.
AKEA MONITORING
KRESS BOX VQC MEASUREMENTS.
Prepared by: A. G. Ossjnan
September 13, 1991
L-69

-------
September 9, 1991
ATTACHMENT 1
KRESS TESTING - PERCENT COMPLETION OF BASELINE TEST PLAN THROUGH AUGUST
Coal Analyses
No. of Samples
Completed
241 days
No. of Samples
Needed-
180 days
Coke Analyses
Hampton Roads.
(CRI/CSR)
Drop shatter Test
VEO Pushing/Travel
VEO Pushing
(from TS/PS)
Video Pushing/
Travel/Discharge
Door Emissions
Quench Water-TCLP
Makeup Water-TCLP
Quench Chem. Anal.
Makeup Chem. Anal.
A tea Samples
GC/MS
GC/MS-QA
SP
BSD
SP/BSO-QA
Amb. Air
2 46 days
154 days
6
390 pushes
380 pushes
16 days
180
1
1
12
12
0
o
36
29
0
2
180 days
180 days
40
260
260
13
180
3
3
25
25
6
1
50
50
5
3
\
L-7,0
Percent
Completion
>100% (continuing)
>100% (continuing)
86%
15%
>100% (continuing)
>100% (continuing)
>100% (continuing)
100% (continuing)
33%
3 3%
48%
4S%
0
0
72%
58%
0
66%

-------
kress/M
09/13/91	12:01
Ali(\thmesrf X
Sparrows Point Coke Bit t er1 as 1 l&l 2 Quench and Make-up Watur
Submitted Date s 7/26/91	Reported Date i 8/16/91
Sample ID
CM	Hq	Na	As	Pb	Ca Hardness	T5S	TDS	S04
ppm	pph	ppm	ppm	ppm	ppm	ppm	ppm	ppm	ppm
Quench water	0. 12	<5	124	0.07	<.2	62	269	560	793	172
quench water	0.10	<5	123	0.07	<. 2	60	269	S90	S05	176
dup11 cats
make-up water	<.02	<5	72	<0.02	<. 2	25	134	7	454	81
* make-up water	<.02	9.3	101	0:096	1.0	43	166	NA	NA	551
splked
F4 , fipl ke value	NA	10	40	0. 10	1.0	20	50	NA	NA	500
-J !
HK! ;
recovery %	NA	93	73	66	100	90	108	NA	NA	102
«*NAj sample 1s not spiked

-------
kr ess/
~9/13
Sample ID
quench water
quench water
duplicate
mak«-up water
make-up water
I ~~"i spiked
!
•' spike va lue
¦i
j«V	recovery %
¦sj
fo
~*NA; sample 1s not spiked
CI	0/6	NHJ-N	Phanol
ppm	ppm	ppm	ppm
16&	20	1	0.64
166	25	<1	0.68
94	14	<1	< .05
138	NA	10	0.30
50	NA	10.6	0.4
98	NA	82	96

-------
KIDC DEMONSTRATION PROJECT
BETHLEHEM STEEL CORPORATION
SPARROWS POINT, MARYLAND
MONTHLY REPORT OF
SAMPLING AND TESTING PROGRAM ACTIVITIES
JULY, 1991
GENERAL OVERVIEW
Activities related to the baseline sampling and analysis program for the Kress
demonstration continued in July. In addition, we initiated preliminary visible
emission observations and video recordings of Kress pushes to monitor the
progress of the Kress start-up operations. Collection of Kress coke is planned
for mid-August to establish a baseline before the start of the performance
demonstration currently scheduled for September. Observation and video recording
of baseline pushing emissions also continued. The quench water sampling program
was restarted- in July.
Project Team Meeting
A pre-audit survey by EPA and their contractor from Research Triangle Institute
has been scheduled for August 12 - 14. The purpose of. this visit is to review
QA/QC procedures and sampling methods prior to the demonstration test program.
Demonstration Program
The Kress system has accepted a. total of 17 pushes through the end. of July. The
demonstration test program is currently scheduled to start in September.
Preliminary data will be obtained prior to the demonstration to monitor the
start-up progress and to gain experience with visible emission observations and
video tapping of the Kress system prior to the September demonstration.
QA/QC Activities
A meeting was held between the QA manager and the Sampling and Testing manager
to identify actions needed to update the OA and QC aspects of the testing
program. As a result of this meeting, a number of Quality Control Procedures and
quality system audit checklists are being developed. In addition, arrangements
are being made to audit outside laboratories involved in the testing program.
Additional quench water samples needed to perform spiked samples and multiple
runs on the same sample were obtained during the month to evaluate the accuracy
and precision of the analytical test methods being used by the Homer Research
Lab Chemical Analysis laboratory. Other QA/QC samples for area monitoring and
visible emission monitoring are planned for August.
i
i f 3-73 !

-------
-2-
July, 1991
Monthly Report
COAL AMD COKE QUALITY
Coke Screening
The automatic coke sample screening equipment should be delivered in August. It
will require installation by plant personnel. It is hoped that this installation
can be completed before the start of the performance test program in September.
The screening device will allow the laboratory personnel to conduct the extra
number of sample screenings required by the KIDC test plans. It will also
provide more consistent screening procedures than the manual screening method
now being used. Until this equipment is received and installed, the laboratory
will use overtime to process the additional number of samples.
Drop Shatter Test
Drop Shatter Testing of baseline coke samples continued during the month. This
testing will continue for a total of approximately 20 weeks. Additional testing
of Kress coke will be initiated as soon as samples of the Kress coke are
obtained. This testing is also planned over a 20 week period.
Hampton Roads Testing Lab
Testing of conventional coke for Coke Strength Reaction and Coke Reactivity
Index by the Hampton Roads Testing Laboratory was temporarily stopped in early
July because of delays in the start of steady operation of the Kress system.
Testing of preliminary Kress coke samples for CSR and CRI will be initiated in
August to monitor the start-up progress, of the Kress process.
BLAST FURNACE PERFORMANCE EVALUATION
No activities during the month.
DOOR EMISSIONS MONITORING
Collection of daily coke side and pusher side door emissions data are
continuing. BCM Inc., is collecting these data. We plan to begin entering all
of these data into a- computer data base. Multiple readings of doors for QA/QC
are planned for August to evaluate the accuracy and precision of the data being
collected.
PUSHING EMISSION MONITORING
Observation of baseline pushing emissions by BCM, Inc.	continued in July.
Observations are currently scheduled for two days each week for 10 pushes each
day.
QUENCH WATER MONITORING
Sampling of quench and makeup waters was restarted in July. Additional samples
were also obtained so that spiked samples and multiple runs on the same sample
can be made for QA/QC. Samples were also obtained for TCLP analysis in July.
r'
L-74,

-------
-3-
July, 1991
Monthly Report
VIDEO TAPING
Video taping of conventional pushes on 11 S> 12 batteries continued in July.
Videos ace currently being taken once per week from two angles simultaneously.
This program will continue for the next several months. Additional videos o£
pushes with the kress system have been initiated as well to monitor the start-up
progress.
AREA MONITORING
Baseline samples for suspended particulate and benzene soluble matter in the
area of the coke door machine continued in July. Additional samples will be
obtained in the near future for volatilea and semi-volatiles as well as a number
of quality assurance samples and background ambient air samples. Additional
personal sampling pumps and a calibrator to handle the increased number of
samples during the demonstration test program was received1 in July.
KRESS BOX VOC MEASUREMENTS.
No activities during the month.
Prepared by: A. G. Ossman
August 9, 1991
L-7-5

-------
KIDC DEMONSTRATION PROJECT
BETHLEHEM STEEL CORPORATION
SPARROWS POINT, MARYLAND
MONTHLY REPORT OF
SAMPLING AND TESTING PROGRAM ACTIVITIES
JUNE, 1991
GENERAL OVERVIEW
Activities related to the baseline sampling and analysis program Cor the Kress
demonstration continued in June. Collection of baseline data from 11 & 12
batteries relating to coal and coke properties continued. Observation and video
recording of baseline pushing emissions also continued. The quench water
sampling program was temporarily stopped in June because of a backlog at the
Homer Research laboratory. It is anticipated that this sampling will start again
in mid-July. The data base of the baseline data being collected continues to be
updated.
Project Team Meeting
Members, of the project team met with EPA on June 13 & 14 to review- data
collection procedures and to review the QA/QC plan for the program.
Demonstration Program
The Kress system accepted 6 pushes through the end of June. Collection of data
for the demonstration test program will begin once the system becomes fully
operational. Spot checks of coke quality and emission readings from the system
may be obtained on a periodic basis to monitor the start-up progress.
QA/QC Activities
It is anticipated that audits of the analytical and testing laboratories by BSC
and EPA will be scheduled at the start of the demonstration test program and
again halfway through the program.
COAL AND COKE QUALITY
Coke Screening
The Sparrows Point Plant Laboratory has initiated the purchase of automatic coke
sample screening equipment which will allow the laboratory personnel to conduct
the extra number of sample screenings required by the KIDC test plans. It will,
also provide more consistent screening procedures than the manual screening
method now being used. Until this equipment is received and installed, the
laboratory will use overtime to process the additional number of samples.
Delivery of this equipment is expected in early August.

-------
-2-
June, 1991
Monthly Report
Drop Shatter Test
Drop Shatter Testing of baseline coke sample* continued during the month. This
testing will continue for approximately 20 weeks. Additional testing o£ Kress
coke will be initiated as soon as steady operation of the Kress system is
attained. This testing is also planned over a 20 week period.
Hampton Roads Testing Lab
Testing of conventional coke for Coke Strength Reaction and Coke Reactivity
Index by the Hampton Roads Testing Laboratory continued in June. This testing
was temporarily stopped at the end of the month, however, because of delays in
the start of steady operation of the Kress system. This testing will continue
once steady operation of the Kress system is attained.
BLAST FURNACE PERFORMANCE EVALUATION
No activities during the month.
DOOR EMISSIONS MONITORING
Collection of daily coke side and pusher side door emissions data are
continuing. BCM Inc., is collecting these data. We plan to begin entering all
of these data into a computer data base.
PUSHING EMISSION MONITORING
Observation of baseline pushing emissions by BCM, Inc. continued' in June.
Observations are currently scheduled for two days each week for 10 pushes each
day.
QUENCH MATER MONITORING
Sampling of quench and makeup waters was stopped in June because of a backlog at
the Homer Research laboratory. Sampling is expected to start again in mid-July.
Sampling and analysis for TCLP constituents is also planned for July.
VIDEO TAPING
Video taping of pushes on 11 & 12 batteries continued in June. Videos are
currently being taken once per week from two angles simultaneously. This
program will continue for the next several months.
AREA MONITORING
Baseline samples for suspended particulate and benzene soluble matter in the
area of the coke door machine continued in June. Additional samples will be
obtained in the near future for volatiles and semi-volat iles as well as a number
of quality assurance samples and background ambient air samples. A purchase
order has been issued for additional personal sampling pumps and a calibrator to
handle the increased number of samples during the demonstration test program.
Delivery of this equipment is expected in early July.
KRESS BOX VOC MEASUREMENTS.
No activities during the month.
Prepared by: ft. G. Ossman [ • L-77-
July 5, 1991 ; C. , '

-------
KIDC DEMONSTRATION PROJECT
BETHLEHEM STEEL CORPORATION
SPARROWS POINT, MARYLAND
MONTHLY REPORT OF
SAMPLING AND TESTING PROGRAM ACTIVITIES
MAY, 1991
GENERAL OVERVIEW
Activities related to the baseline sampling and analysis program for the Kress
demonstration continued in May. Collection of baseline data fro® 11 & 12
batteries relating to coal and coke properties continued. Observation and video
recording of baseline pushing emissions also continued along with the quench
water sampling program during the month. All the baseline data collected is
being entered into a data base for comparison with data to be collected during
the Kress demonstration.
Proiect Team Meeting
A project team meeting was held on April 29 to review activities, data
collection, and schedules related to the test program. Minutes of this meeting
were issued. The next project team meeting will be scheduled as needed-.
Demonstration Proqram
Delays, in the start-up of the Kress system, relating to the construction of the
Kress carrier have delayed the start of the Demonstration Test Plan. Current
schedules indicate that start-up of the Kress system should occur in mid-June.
Initiation of the Demonstration Test Plan is planned to coincide with, this
start-up.
SPA Review of Test Program Reports
A response to EPA's comments- on the Baseline, Demonstration and Quality
Assurance Test reports has been completed and has been sent to EPA. A visit to
Sparrows Point by EPA is scheduled £or June 13 & 14 so that they can observe and
discuss data collection procedures.
COAL AND COKE QUALITY
Coke Screening
The Sparrows Point Plant Laboratory has initiated the purchase of automatic coke
sample screening equipment which will allow the laboratory personnel to conduct
the extra number of sample screenings required by the KIDC test plans. It will
also provide more consistent screening procedures than the manual screening
method now being used. Until this equipment is received and installed, the
laooratory will use overtime to process the additional number of samples.
Delivery of this equipment is expected in early August.
Lr7.8

-------
-2-
Hay, 1991
Monthly Report
Drop Shatter Test
Drop Shatter Testing of baseline coke samples was initiated during the month.
This testing will continue for approximately 20 weeks. Additional testing of
Kress coke will be initiated as soon as steady operation of Kress system is
attained. This testing is also planned over a 20 week period.
Hampton Roads Testing Lab
Testing of conventional coke for Coke Strength Reaction and Coke Reactivity
Index by the Hampton Roads Testing Laboratory continued in May.
BLAST FURNACE PERFORMANCE EVALUATION
Ho activities during the month.
POOR EMISSIONS MONITORING
Collection of daily coke side and pusher side door emissions data are
continuing. BCM Inc., is collecting these data. We plan to begin entering all
of these data into a computer data base.
PUSHING EMISSION MONITORING
Observation of baseline pushing emissions by BCM, Inc. continued in May.
Observations are currently scheduled for two days each week for 10 pushes each
day.
QUENCH WATER MONITORING
Sampling of quench and makeup waters continued in May. Samples are currently
being collected once per week. This program will continue for the next several
months. We are currently investigating other labs to perform the required
analyses because of a backlog at the Homer Research laboratory.
VIDEO TAPING
Video taping of pushes on 11 & 12 batteries continued in May. Videos are
currently being taken once- per week from two angles simultaneously. This
program will continue for the next several months.
AREA MONITORING
Baseline samples for suspended particulate and benzene soluble matter in the
area of the coke door machine continued in May. Additional samples will be
obtained in the near future for volatiles and semi-volatiles as well as a number
of quality assurance samples and background ambient air samples. He are
currently investigating the purchase of additional personal sampling pumps and a
calibrator to handle the increased number of samples which will need to be
obtained when the Kress system starts up.
KRESS BOX VOC MEASUREMENTS.
No activities during the month.
Prepared by: A. G. Ossman
June 7, 1991,
y L-79

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KIDC DEMONSTRATION PROJECT
BETHLEHEM STEEL CORPORATION
SPARROWS POINT, MARYLAND
MONTHLY REPORT OF
SAMPLING AMD TESTING PROGRAM ACTIVITIES
APRIL, 1991
GENERAL OVERVIEW
Activities related to the baseline sampling and analysis program for the Kress
demonstration continued in April. Collection of baseline data from 11 & 12
batteries relating to coal and coke properties continued. Observation and video
recording o£ baseline pushing emissions also continued along with the quench
water sampling program during the month. All the baseline data collected is
being, entered into a data base for comparison with data to be collected during
the Kress demonstration.
Project Team Meeting. A project team meeting was held on April 29 to review
activities/ data collection, and schedules related to the test program. Minutes
of this meeting have been issued. The next project team meeting will be
scheduled, as needed.
Demonstration Program. Delays in the start-up of the Kress system relating to
the construction of the Kress carrier have delayed the start of the
Demonstration Test Plan. Current schedules indicate that start-up of the Kress
system should occur in May. Initiation of the Demonstration Test Plan is. planned
to coincide with this start-up.
EPA Review of Test Program Reports. A response to EPA's comments on the
Baseline, Demonstration and Quality Assurance Test reports has been completed -
arid has been sent to EPA. A visit to Sparrows Point by EPA is scheduled for June
13 & 14 so that they can observe and discuss data collection procedures.
COAL AMD COKE QUALITY
Coke Screening. The Sparrows Point Plant Laboratory has initiated the purchase
of automatic coke sample screening equipment which will allow the laboratory
personnel to conduct the extra number of sample screenings required by the KIDC
test plans. It will also provide move consistent screening procedures than the
manual screening method now being used. Until this equipment is received and
installed, the laboratory will use overtime to process the additional number of
samples.
Drop shatter Test Equipment¦ Drop Shatter Test equipment which was constructed
by BSC'S Research Dept. has been, tested and delivered to Sparrows Point.
Training of Sparrows Point personnel will be performed in early May and
initiation of baseline Drop Shatter Tests should begin soon after.
Hampton Roads Testing Lab. Testing of conventional coke for Coke Strength
Reaction and Coke Reactivity Index by the Hampton Roads Testing Laboratory
continued in April.
L-80 -'J

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-2-
Apr11, 1991
Monthly Report
BLAST FURNACE PERFORMANCE EVALUATION.
No activities during the month.
DOOR EMISSIONS MONITORING
Collection of daily coke side and pusher side door emissions data are
continuing. BCM Inc., is collecting these data. We plan to begin entering all
of these data into a computer data base.
PUSHING EMISSION MONITORING
Observation of baseline pushing emissions by BCM, Inc. continued in April.
Observations are currently scheduled for two days each week for 10 pushes each
day.
QUENCH WATER MONITORING
Sampling o£ quench and makeup waters continued in April. Samples are currently
being collected once per week. This program will continue for the next several
months.
VIDEO TAPING
Video taping of pushes or, 11 & 12 batteries continued in April. Videos are
currently being taken once per week from two angles simultaneously. This
program will continue for the next several months.
AREA MONITORING
Baseline samples for suspended particulate and benzene soluble matter in the
area of the coke door machine was initiated in April. Additional samples will be
obtained in the near future for volatiles and s«mi-volat ilea as well as a number
of quality assurance samples and background ambient air samples.
KRESS BOX VOC MEASUREMENTS.
No activities during the month.
Prepared by: A. G. Ossman
May ID, 1991
L-81

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KIDC DEMONSTRATION PROJECT
BETHLEHH4 STEEL CORPORATION
SPARROWS POINT, MARYLAND
MONTHLY REPORT OF
SAMPLING AND TESTING PROGRAM ACTIVITIES
MARCH, 1991
GENERAL OVERVIEW
Activities related, to the baseline sampling, and analysis program for the Kress
demonstration continued i_n March. Collection of baseline data from 11 & 12
batteries relating to coal and coke properties continued. Observation and video
recording ofi baseline pushing amissions was initiated. The quench water sampling
program was. also initiated during the month. All the baseline data collected is
being entered into a data base for comparison with data to be collected during
the Kress demonstration.
Project Team Meeting. A project team meeting will be scheduled, for the end of
April to review activities> data collection, and schedules related to the test
program.
Demonstration Program. Delays in the start-up of the Kress system relating to
the construction of the Kress carrier have delayed the start of the
Demonstration Test Plan. Current schedules indicate that start-up of the Kress
system should occur in mid-May. Initiation of the Demonstration Test Plan is
planned to coincide with this, start-up.
EPA Review of Test Program Reports. A response to SPA's comments on the
Baseline, Demonstration and Quality Assurance Test reports has been completed
and will be sent to EPA..
COAL AND COKE QUALITY
Coke Screening. The Sparrows Point Plant Laboratory has initiated the purchase
of automatic coke sample screening equipment which will allow the Laboratory
personnel to conduct the extra number of sample screenings required by the KIDC
test plans. It will also provide more consistent screening, procedures than the
manual screening method now being used.
Drop Shatter Test Equipment. Drop Shatter Test equipment which was constructed
by BSC'S Research Dept. has been tested and delivered to Sparrows Point.
Initiation of baseline Drop Shatter Tests should begin in mid-April.
Hampton Roads Testing Lab. Testing of conventional coke for Coke Strength
Reaction and Coke Reactivity Index by the Hampton Roads Testing Laboratory was
initiated in March.
BLAST FURNACE PERFORMANCE EVALUATION.
No activities during the month.
L-8'2 I

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-2-
March, 1991
Monthly Report
DOOR EMISSIONS MONITORING
Collection of daily coke side and pusher side door emissions data are
continuing. BCM Inc., is collecting these data. He plan to begin entering all
of these data into a computer data base.
PUSHING EMISSION MONITORING
Observation of baseline pushing emissions by BQ1, Inc. was initiated in March.
Observations are currently scheduled for two days each week for 10 pushes each
day.
0UENC3 WATER MONITORING
Sampling of quench and makeup-waters was initiated in March. Samples ara
currently being collected once per week. This program will continue for the next
several months.
VIDEO TAPING
video taping of pushes on 11 s> 12 batteries was initiated in March. Videos are
currently being taken once per week from two angles simultaneously. This
program will continue for the next several months.
AREA MONITORING
We- expect to begin collecting baseline samples for suspended particulate and
benzene soluble matter in Che area of the coke door machine in April.
KRESS BOX VOC MEASUREMENTS.
No activities during the month.
Prepared by: A. G. Ossman
April 11, 1991
[ .L-83

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KIDC DEMONSTRATION PROJECT
BETHLEHEM STEEL CORPORATION
SPARROWS POINT, MARYLAND
MONTHLY REPORT OF
¦ SAMPLING AND TESTING PROGRAM ACTIVITIES
FEBRUARY, 1991
GENERAL OVERVIEW
During the month of February a number of activities were initiated or completed
to begin the collection of the information required by the Baseline and
Demonstration Test Programs. These are discussed in the following paragraphs.
Project Team Meeting. On February 6, 1991 a meeting was held at Sparrows Point
of the Sampling and Tasting project team to review the overall test programs
required, the test program schedules and personnel responsibilities. Several
followup actions were initiated as a result of this meeting.
Demonstration Program Delay. There has been an extended delay in the startup of
the-KIDC demonstration, project due to a number of factors relating to the
construction of the KRESS Carrier. This delay has delayed, the start of the
Demonstration Test Plan. However, we have begun collecting information related
to the Baseline Test Plan and have initiated training and practice programs for
several activities which will be helpful during the conduct of the Test Plans.
Revised test program schedules will be dveloped as soon as a new
contruction/startup schedule-has been established.
EPA Review of Test Program Reports. We have received EPA's comments on our
Baseline, Demonstration and Quality Assurance Test reports and have begun
preparing a response. In general, EPA's comments do not appear to be sufficient
to delay the test program activities. He expect to have a response to EPA's
comments, completed by the end of March.
DATA MANAGER
We have retained the services of J. W. Pasquali for the Data Manager position
and he has begun collecting and computer entry of several of the Baseline Data
for coal and conventional coke quality, coke battery operating, conditions.
COAL AND COKE QUALITY
Coke Screening. The Sparrows Point Plant Laboratory has initiated the purchase
of a automatic coke sample screening equipment which will allow the Laboratory
personnel to conduct the extra number of sample screenings required by the KIDC
test plans. It will also provide more consistent screening procedures than the
manual screening method now being used.
Drop Shatter Test Equipment. BSC'S Research Dept. has completed the
. construction of the Drop Shatter Test Equipment. This equipment will be shipped
to Sparrows Point for installation at the Sparrows point Laboratory in March.
I	L-84

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-2-
February, 1991
Monthly Report
Hampton Roads Testing Lab. We have retained tha Hampton Roads Testing
Laboratory to conduct the Coke Strength Reaction tests required of both
conventional and KIDC coke.
BLAST FURNACE PERFORMANCE EVALUATION.
Ho activities during the month.
DOOR EMISSIONS MONITORING
Collection of daily coke side and pusher side door emissions data are
continuing. 'BCM Inc., is collecting these data. He plan to begin entering all
of these data into a computer data base.
Ho activities during the month. We expect to begin collecting Baseline Pushing
Emissions observations in March.
QUENCH WATER MONITORING
No activities during the month.
VIDEO TAPING.
Two video cameras and tripods have been purchased and a few practice video
taping trials have.been conducted at Sparrows Point inorder to. locate the best
positions for filming.
No activities during the month. Me expect to begin collecting baseline samples
for suspended particulate and benzene soluble matter in April.
KRESS BOX VOC MEASUREMENTS.
No activities during the month.
Prepared by: L. M. Stuart
March 13, 1991
PUSHING EMISSION MONITORING
AREA MONITORING
I
L-S5

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Section 4
Observe! Method 9 Certifications
(.

-------
c
i
Oo
fesra (ttmromtmttj (Enllwje
an
award of completion
to
FRANK R . CflMPEGGI
For Completion of the Continuing Education Course
VISIBLE EMISSIONS KVIVI.nATTON TRAINING AND TESTING
Inclusive Dates of the Course 	—
Continuing Education Units Awarded
May 20. 21, fi 22, 1991
2.5
Donald J, Slowinski, President
Hay 23, 1991
Date
Andrew J. Snope, Dean of Instruction

-------
F'.
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fern* Gkmtmmtity QtaUfg?
presents an
award of completion
to
RONALD J - ABBAMOWSKI
For Completion of the Continuing Education Course
VTSIBI.E EMISSIONS EVALUATION TRAINING AND TESTING
. . . _	, , „	Hay 20, 2|, & 22, 1991
Inclusive Pates of the Course 		
2.5
Continuing Education Units Awarded 	
M.'iy 23, 1991
iDonanl J. Slowinski, President
Date	Andrew J. Snope, Dean of Instruction	[
t

-------
Easra (Eummmttty
presents an
award of completion
to
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:
I
EUGENE P - HARD
For Completion of the Continuing Education Course
VISIBLE EMISSIONS EVALUATION TRAINING AND TESTING
•j V; v"
.L.l. .
''i ••
': . :' '

May 23, 1991
Inclusive Dates of the Course 	
Continuing Education Units Awarded
May 20, 21, & 22, 1991
2.5

Donald J. Slowinski, President
Date
Andrew J. Snope, Dean of Instruction

-------
(Emmmttutu (Mlwje
presents an
award of completion
to
« r4
i

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£fflummmtttfj
presents an
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to
RICHARp E T ABRAMOWSKX
•tT'
For Completion of the Continuing Education Course
'! -v
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,>¦: >¦ V-" ,
VISIBLE EMISSIONS EVALUATION THATNTNG AND TESTING
f V '
Inclusive Dates of the Course 	
Continuing Education Units Awarded
Nay 20, 21, & 22, 1991
V V; V..Vv I'	' I.' ¦-
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Hay 23, 1991
n 11 ry
Donaid J. Slowinski, President
-I .^noFiP Dpan of Instriirtiori

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Section 5
American Medical Laboratory Quality Assurance

-------
AML
KJ industrial hygiene laboratory 9
A DIVISION OF AMERICAN MEDICAL LABORATORIES. INC,
11091 Main Street. Fairfax, Virginia 22030 . (703)691-9100
March 25, 1991
Mr. George Qssman
Homer Research Labs, C-Building
Bethlehem Steel Corporation
Bethlehem, PA 18Q16
Dear Mr- Ossman:
In response to your request I have enclosed copies of several
documents which demonstrate our commitment to quality including
several of our certifications and accreditations and a general quality
assurance statement. AML-Industrial Hygiene is accredited by the
American Industrial Hygiene Association (AIHA), the National Voluntary
Laboratory Accreditation program (NVLAP), and is certified by the
Commonwealth of Virginia and the State of Florida to perform analysis
of drinking water for inorganic parameters. The laboratory
participates in several voluntary proficiency programs including a
program for lead and arsenic in filters and one for the determination
of PCB's in biological materials.
For the analyses which we discussed, BSFTPM and total particulate the
following procedures are currently in place. Most of the samples that
we currently analyze for BSFTPM are OSHA related so the final extract
volume is too small for any type of repeat analysis. Filters are all
prewashed with benzene and upon return to the laboratory, a blank
sample is analyzed with every group of nine samples. This is in
addition to the blanks that may be submitted by the client. ¦ We keep a
record of these values and have established lower and upper control
levels, which, if exceeded, require investigation. If duplicate
samples could be obtained, we would be more than happy to compare
extracted values and' statistically monitor any significant changes.
With regard to total particulate, filters are preweighed and every
tenth filter is reweighed and compared with the original filter
weight. A record of this information is also kept. Before any filter
weights are taken, the electronic balance is calibrated with a class S
standard weight on a daily basis and a record of these weights is
monitored.
If you need any additonal information, please contact me.
Fred I. Grunder
ACCREIMEO BY" AMERICAN INDUSTRIAL HYGIENE ASSOCIATION

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American
INDUSTRIAL
HYGIENE
ASSOCIATION
Jkmerictut'^edicar
Virginia
haa fuHUM AIHA erMria for
Industrial Hyfiana Laboratory Aeeradiiatian

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United Slates Department of Commerce
National Institute ol Standards and Technology
Certificate of Accreditation
vO
AMERICAN MEDICAL LABORATORIES, INC.
FAIRFAX, VA
i-> in i'i/ui i iI itiiih i IIii' Niilii'/iiW Vo/iiiihuii I iibiiiiihufi	VrOijhini
/¦'J *iih--l(ii h'i ti it'fuf/jiiifi ¦* mill mli ilit i Lhil>li--lii'il in I ilh' I *» Pii/I 7 Ci'i/r of h'lli'hii Riyuhiltiiiii
Atitfilihihi'ii iMiitiKifri/ /<>i	M irini hiltil I'll llir Sii'i'i- (if Aicrftlil/iliiM. lor-.
ASBESTOS FIBER ANALYSIS
April 1. 1990
I (|n lit!' null!
S?ATES °f
I xt Ifcr Niilli'UiW liolifuli' i'l Sluinjiirilt iiniJ In Iiui'/imIii

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COMMONWEALTH of VIRQINIA
DEPARTMENT OF GENERAL SERVICES
DIVISION OF	1 NORTH 14TH STREET
CONSOLIDATED LABORATORY SERVICES	February 21, 1969	RICHMOND, VIRGINIA J3219
Mr. Fred I. Grunder
American Medical Laboratories
11091 Main Street
Fairfax, VA 22030
Enclosed is a copy of the on-site evaluation report for American Medical
Laboratories conducted on February 9, 1989 in accordance with the provisions
of the Regulations for the Certification of Laboratories Analyzing Drinking
Water in the Commonwealth of Virginia.
This report addresses itself to the deviations found in the area of Micro-
biology and Inorganic Chemistry. All deviations are included under the broad
headings: Laboratory Equipment and Supplies; Sample Collecting, Handling, and
Preservation; General Laboratory Practices; and Methodology and Analytical
Quality Control.
I
Comments' on specific deviations are listed under broad headings. If no
specific entries are made under such headings, this indicates that no devia-
tions were observed at the time of the on-site visit.
LABORATORY CERTIFICATION (BY SECTIONS)
MICROBIOLOGY - CERTIFIED
Total Coliform - MF Procedure
INORGANIC - CERTIFIED
Arsenic, Barium, Cadmium, Chromium, Copper, Iron, Lead, Manganese, Selenium,
Silver, Zinc, Fluoride, Nitrate, Chloride, Sulfate, pH
Your Laboratory I.D. Number is 00003.
Effective February 1989 through January 1992.
A letter to confirm and document the corrections of the listed deviations
must be received by this office within sixty (60) days after receipt of this
correspondence.
DOS
DIVISION OF ADMINISTRATIVE SERVICES • DIVISION OF ENGINEERING & BUILDINGS
DIVISION OF PURCHASES & SUPPLY - DIVISION OF CONSOLIDATED LABORATORY SERVICES • DIVISION OF RISK MANAGEMENT
" "I
! ,L-96 '
I	-» '	j

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i
SPttUe SFl&Uda
«j^ 3€eadt/i tvruj tSte/iafafoCati&e SReMtdceA
Office of Laboratory Services
Post Office Box 210
Jacksonville, Florida 32231
1990 • 1991
£T/ua to c&Uify. that tAe 4tt&ouUotop named delate,
c&tnfvtie*/ <&iCA tecHon 40%l)-44 ofi €Ae ttfilvucta
9&ot£e fiebfa*n4mj, fa tttafat £e&£*ng, m
^0&C4t>4n^	Inorganic-Primary****************
*a : *>;
EFFECTIVE:October 31, 1990 through June 30, 1991
Ne .90 253
HR5#87348
American Medical Laboratories
11091 Main Street
Fairfax, VA 22030
NON-TRANSFERABLE

Eldert C. Hartwig, Jr., ScD.. M.P.H.
Chief. Laboratory Service;
Office of Laboratory Services
HRS Form 1629, Apr 90
L-97

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EXPinES
QtKil-31
COMMONWEALTH O*" VIRGINIA
DEPARTMENT OF CL IEHCE
96W Wmi BrMd Siimi. Richmond. VA 2321*
TlUphoil*' 1 IBM) 367-aSOD
VIRGINIA ASBESTOS LICENCE
ASBESTOS ANALYTICAL LABORATORY LICENSE
NUMBER
QQotioa
AMERICAN MEDICAL LA1JOKATOK1 ELI, INC.
11091 MAIN STREET
FAIRFAX, VA 22030
ll	AlMUf.M HAMJI
Milton K. Brnwn, I**., Director
{PICKtl c2J)33000003	(OETACM HERE)
COMMONWEALTH OF VIRGINIA ~ DEPARTMENT OF COMMERCE - 3600 Weti Broad Sueti Richmond, Virginia 23230
VIRGINIA ASBESTOS LICENSE
ASBESTOS ANALYTICAL LABORATORY
NUMBLH
EXPIRES
000003
08-31-91
AMERICAN MEDICAL LABORATORIES, INC.
11091 MAIN STREET
FAIRFAX. VA 22030

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Industrial Hygiene QC Plan
Introduction:
To maintain high standards of quality established by the
management of American Medical Laboratories, Inc.® (AMI.®),
is essential that each employee of AML have full knowledge
of the Quality Assurance objectives, policies and programs
as published. This policy is required to maintain the
public confidence associated with the reliability of
results reported on constituents analyzed at AML.
Purpose:
To establish Quality Assurance guidelines, procedures and
control practices to assure the appropriate performance of
all departments of the laboratory..
Policy:
The Quality Assurance Program at AML is designed to require
the active involvement of all employees and to:
1 .. Assure satisfactory handling of specimens from
collectipn through analysis which will ensure an
acceptable level of integrity of the specimens.
2.	Provide instrument maintenance: schedules to include
both functional checks and preventive maintenance.
3.	Establish a protocol for the adequate evaluation of
methodologies prior to selection and implementation.
4.. Provide adequate space, equipment and stable control
materials and reagents to accomplish the- mission of the
laboratory.
5.	Ensure the competence of the personnel to perform the
tasks required.
6.	Enhance communication by providing a comprehensive
program followed by instruction in quality philosophy.
7.	Develop specific Quality Assurance objectives and a
system for monitoring the program to achieve the
performance required.
8.	Provide support, supervision and communication between
all levels of management and staff members.
Responsibility:
1. Director of Laboratories
It shall be the role of the Laboratory Director, or his
delegate, the Vice-President of Clinical Operations, to
I ' L-99: -

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Industrial Hygiene QC Plan
Page 2
set the objectives of the laboratory Quality Assurance
Program.
2.	Quality Assurance Supervisor
a.	It shall be the primary responsibility of the
Quality Assurance Department to design, execute,
monitor and evaluate all Quality Assurance programs
to ensure that the objectives set by the
¦» Laboratory Director are fulfilled.
b.	It shall be the responsibility of the Quality
Assurance Supervisor or delegate to manage the
required Proficiency Testing programs offered by:
T) College of American Pathology (CAP)
2)	Centers for Disease Control (CDC)
3)	National Institute for Occupational Safety and
Health (NIOSH)
4)	Commonwealth of Virginia
5)	Commonwealth of Pennsylvania
6)	Environmental Proection Agency Quality Control
Program
7)	State of New York.
Other Quality Control Programs which are not
mandatory are also managed by the Quality Assurance
Office. These include:
1)	Wellcome Immunoassay Quality Control Programs
(I and II)
2)	Wellcome Clinical Chemistry Quality Control
Programs
3} American Association of Clinical Chemistry -
Therapeutic Drug Monitoring Program (AACC-TDM)
4) American Association of Clinical Chemistry -
Endocrinology Program (AACC-ENDO).
3.	Technical Director or Technical Supervisor
a.	It shall be the responsibility of the Technical
Director or Technical Supervisor of each department
to assure that each technical member of the
department staff has read and signed the Quality
Assurance Statement written for the department.
The statement will be initialed and dated again at
the time of annual review.
b.	It shall be the responsibility of each Technical
Director or Technical Supervisor to monitor all
. L-100
j

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Industrial Hygiene QC Plan
Page 3
Quality Assurance procedures in their respective
departments and to assure that they are performed
properly and in a timely manner.
c. It shall be the responsibility of each Technical
Director or Technical Supervisor to: (1) respond
appropriately when notified of control or
instrument problems. (2) Institute corrective
action as. required. (3) Document action taken.
The Technical Director or Technical Supervisor
should inform the appropriate Vice-President of any
unresolved methodology problems.
d - It shall be the responsibility of each Technical
Director or Technical Supervisor to order and
maintain a sufficient supply of control materials
to assure availability of these controls at all
times. (When possible, at least a 12 month supply
should be ordered.)
e. It shall be the responsibility of each Technical
Director or Technical Supervisor to- assure the
parallel analysis of each new lot number of control
material introduced into the department. This will
assure that acceptable parameters for the' new
control' materials are established prior to its
being placed in use. In areas where control
material is not. available, other parameters will, be
assessed.
4 - Employees
a.	It shall be the responsibility of each employee of
AML to perform all Quality Assurance procedures as
published.
b.	It shall be the responsibility of each employee of
AML to report all Quality Assurance problems to the
appropriate supervisor immediately..
E. Analytical Procedures:
1.	All analytical procedures shall be approved by the
division Director/Supervisor.
2.	The procedures in each department shall be read by the
technical, staff. Any unauthorized changes in any
procedure are prohibited. Procedures are to be
followed as written unless otherwise instructed by the
Technical Director. Sample collection, storage,
processing and analysis information is included in each
method.
- - f
L-101 'j

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Industrial Hygiene QC Plan
Page 4
3. The following protocol will apply in all technical
areas;
a.	Quality control -specimens should be analyzed with
each set of specimens when control material is
available for that analyte.
b.	The results of all quality control specimens shall
be evaluated and recorded prior to the release of
results on any sample.
c.	When the results of quality control samples are not
acceptable, the problem shall be defined and no
results will be released until it is approved by
the Technical Director of his designate.
d.	The Quality Assurance Department shall be notified
by all departments of the following changes:
1)	Change in test methodology
2)	Change in manufacturer of reagents
3)	Change in control, material, lot number or
manufacturer
4)	Addition of a new-test procedure
e.	Temperature of all. water baths, refrigerators,
freezers, and ovens shall be recorded and evaluated
every day they are in. use.
f..	The speed of all centrifuges and rotators shall be
checked monthly. Repairs are to be accomplished as
required.
g.	All new thermometers shall be calibrated against an
NBS certified thermometer before being put into
service and at least annually thereafter.
h.	All micropipettes shall be calibrated every month.
i.	Bach deionized water outlet shall be examined for
bacterial growth on a scheduled monthly basis.
j. All instruments shall be calibrated and maintained
as described by manufacturer.
Maintenance records for all instruments will be
reviewed on a weekly basis. A written report of
this review will be submitted to the Quality
Assurance Office.
r
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06/to/ot :axva
xhvhd ssNiHNar-iAaa

-------
HONTH /WAR TEAK 9/
PROCEDURE:	TFq*)	INSTRUMENT I	&\
CONTROL!	3q ^ irff	j,OT t
MEAN	2SD	 C.V.	
2 S.O. RANGE	
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-------
Section 6
Keystone Environmental Resources< Inc. Quality Assurance
L-106

-------
KEYSTONE
ENVIRONMENTAL RKSOIRCKS. INC.
3000 Tech Center Drive
Monroeville, PA 15146
412 825-9600
FAX 412 825-9699
Ref. No. 395110-01
August 3, 1992
Mr. George Ossman
Bethlehem Steel Corporation
Homer Research Laboratories
Building C
Bethlehem, PA 18016
Dear Mr Ossman:
Re: Kress Box Report, Response to EPA Comments
In response to EPA's comments on the report summarizing the determination of concentrations
of volatile and semi-volatile compounds in the headspace of Kress Box #3, the quality
assurance/quality control procedures followed in the program are summarized in the attached
table. Details of each procedure are listed below.
	1	T^ps jnJferi&s
Two sorbent traps were connected in series in each sampling train to determine if all
constituents were captured in the primary sorbent trap. Both the primary and back-up
sorbent craps were analyzed separately to determine the capture efficiency.
	2	Field Blank
A separate sampling train was transported to the site to serve as a field blank. No process
gases were pumped through the field blanks. These samples were analyzed with the
regular samples.
2	Surrogates Added to Extracts
Excluding the VOC sampling trains, constituents were extracted from the sorbent traps
and concentrated, in a liquid sample. Surrogate compounds were added to the extracts
prior to analysis. The analyses of the surrogate compounds are expressed as percent
recovery.
A CHESTER EnYironrrental Comoany
L-107

-------
To: Mr. George Ossman
Re: Kress Box Report, Response to EPA Comments
August 3, 1992
Page 2
4	Frequency of Concurrent Calibration
An initial five point calibration curve was prepared and analyzed for each compound of
interest. A continuing calibration standard was reanalyzed either every tenth sample or
every twelfth hour. If the results between the initial and concurrent concentration
differed by more than 15 percent, then a new five point calibration curve was prepared.
Tentatively identified compounds (TIC's) were determined by comparison of the retention time
and mass spectral data of the TIC's to those in a NBS library resident in the data system.
If you have any questions regarding my response, please call me at (412) 825-9760.
Very truly yours,.
John P. Shimshock
Air Quality Scientist
Air Quality Engineering
JPS:mjt
Enclosures

\ KEYSTONE
\ ~xMKu>MKVf*iHKsniKn:s,i\t'.

-------
BETHLEHEM STEEL CORPORATION'
SPARROWS POINT. MARYLAND
DETERMINATION OF CONCENTRATIONS OF
VOLATILE AND SEMI-VOLATILE ORGANIC COMPOUNDS
IN THE HEABSPACE OF KRESS BOX #3
SUMMARY OF QAJQC PROCEDURES
Surrogates	Frequency of
Constituent
4 Sample
Trains
Sorbcnt Tiaps
in Series?
Field
Blank 7
Analytical
EPA Method
Added to
Extracts?
Concurrent
Calibration
VOC's
2
yes
yes
TG-1
(GC/ITD)
no
None -
Initial 3-point
calibration only
VOC's - scan
1
no
yes
TO-1
(GC/ITD)
no
None-
Imdat 3-pdnt
calibration only
PAH's
2
yes
yes
610 (HPLQ
yes-
banzo(e)pyiene &
2-Buorobipheny)
every
10th sample
PAH's - scan
1
no
yes:
623 (GC/M5)
yes-
rri trohenzene-d5 &
2-fl»o»otjipk«ityl
every
12th hour
Phenols
& Cresols
2
yes
yes
625 (GC/MS)
yes-
luUubeiiZBne-d5
every
12tti hour
Phenols &
CresoLs - scan
1
no
yes
625 (GC/MS)
no
every
12th hour
Phthalatcs
2
yes
yes
623 (GC/MS)
yes-
nifirobenzene-d5 &
2-fluoiobiphcnyl
every
12th hour
Phthalatcs
1
no
yes
625 (GC/MS)
no
every
12th hour
L-10,9, ¦ I
\ KEYSTONE
\ K.SVJhdNVIkSm. KkNOl RLES. INC.


-------
Appendix M
Door Leak Data
M-1'

-------
NO. 11 6, 12 BATTERY
DAILY PERCENT DOOR LEAKS FOR 1991
Pe rcen t
Inspector Door
DATE	Initials Leaks
01J AN 91
02JAN91
03JAN91 RA	6.5
04JAN91 RA	5.4
05JAN91-RA	7.1
06JAN91 RA	5.J
07JAN91
G8JAN91
09JAN91
10JAN91 RA	o.b
11JAN91 PC	7.2
12JAN91 FC	7.7
13JAN91 FC	7.7
14JAN91
15JAN91
laJAW91
17JAN91 RA	7.5
18JAN91 RA	6.3
19JAH91 RA	7.2
20JAN91
21JAN91
22JAN91 CH	8.1
23JAM91 FC	B.fi
24JAN91 RA	5.7
25JAN91 RA	6.3
26JAN91
27JAK91
28JAN9I
2 9JAN91 FC	7.4
30JAN91 FC	6.9
31JAN91 RA	5.1
01FEB91 RA	5.4
02FEB91
0 3FEB91
U4FEB91
05FEB91 FC	10.9
06FEB91 FC	6.1
07FEB91 RA	6.1
0SFEB91 RA	5.3
11FEB91 FC
12FEB91 FC	;.u
13FEB91 FC	7.5
14FEB91 RA	b-6
15FEB91 RA	3.9
16FEB91
17FEB91
M-2

-------
-2-
MO. II & 12 BATTER*.'
DAI Lif PERCENT DOOR LEAKS FOR 1991


ir^ I'Ci

Inspector
Dix.r
DATE
Init ials
~=ak.
18FEB9)
PC
7 . 3
19FE091


2 0FEB91
FC
4 . 7
21FEB9I
RA
S. >
22FEB91
RA
4 . G
23FEB91


24FEB91


2SFEB91


26FEB91
RA
6 . -1
27FEB91
FC
7 . 2
2BFEB91
RA
6 . 6
0 LMAR91
RA
1, 3
U2MAR91


D3MAR91


0 4MAR91


Q5MAR91
RA
s. :j
06MAR9 I
RA
5.a
U7MAR91
RA
6 .
08MAR91
RA
7.4
Q9MAR91


10MAR91


11MAR91


12MAR91
FC

13MAR91
FC
3 . 6
14MAR91
RA
i.
15MAR91
RA
8.4
16MAR91


17MAR91


18MAR91


J.9MAH91
FC
* . J.
20MAR91
FC
11.0
21MAR91
RA
6 . if
22MAR91
RA
5. b
2 3MAR91


24MAR91


2 5MAH9I


2GMAR91
RA
I. -j
2 7MAE91
RA
8.2
28MAH91
RA
9 . u
2 9MAH91
RA
6 . 1
3CMAR91


31MAR91


02APR91
FC
U . 3
0 3APR 91
FC
¦0.4
04APR91
RA
6.'3
05APR91
RA
7 .7
G9APR91
FC
7. J
1CAPR91
FC
b.Z
• >1-3 ,

-------
-3-
NO ¦ 11 £ 12 BATTKHV
PAILy PERCENT POOR LEAKS FOP 1.991


Perc:

Inspector
Do... L
DATE
Initials
Leak
11APR91
HA
5 . •-<
12APR91
RA
6 .
i 6A.PR91
FC
!j . i
17APB91
FC
e. h
18APR9I
FC
8 .
19APR91
FC
¦i . 1
23APR91
RA
9 . L
2 4APR91
FC
9 . -1
2&APR91
RA
5. 1
26APR91
RA
6 . 8
30APR91
FC
7 . 7
01MAY91
FC ¦
6 .2
0 2MAY91
RA
a. >,
0 3MAY91
FC
a. 5
Q7MAY91
RA
4 . 1
Q8MAY91
FC
r-
09MAX91
RA
. <>
10MAY'91
RA
3 . 2
t 4MAY91
PC
9.;
1SMAY91
FC
9.4
16MAY91
RA
i . 4
17MAY91
RA
6.9
21MAY91
FC
li'i.B
22MAY91
FC
8 . 5
2 3MAS91
RA
6 . 0
24MAY91
RA
5.2
28MAY91
FC
LO . S
2 9MAY91
FC
11, ¦;
3DMAY91
RA
s , 3
31MAY91
FC
6. a
01JUN91


02JUN91


CJJUN91


04JUN91
RA
6 . o
05JUN91
FC
lit . 2
06JUN91
RA
4 . I
07JUN91
RA
H . s
0SJUN91


C/9JUN91


10JUN91


L1JUN91
FC
a. r.
12JUN91
RA
1 . 4
13JUN91
RA
8.0
14JUN91
RA
7 . 1
1bJUN91


| -H-4 '
i * '*

-------
HO. 11- & 12 BATTERi'
DAILY PERCENT DOOR LEAKS FLR I.MO 1.
PerccJi c
Ieispecc or Dour
DATE	I nit ials Leaks
16JUN91


17JUN91


18JUN91
RA
1. 4
19JUN91
FC
; o. a
20JUN91
RA
i.j.
21JUN91
RA
8.1
2 2JUN91


2 3JUN91


24JUN91


25JUN91
FC
10.2
26JUN91
FC
6 . 3
2 7JUN91
RA
5. S
28JUN91
RA
a. a
29JUN91


3QJUN91


AUG90

9.4
SEP90

ii. 1
OCT 90

8.1
02JUL91
BA
5. A
03JUL91
FC
10.2
04JUL91
FC '
7.2
05JUL91
ISA
3 . 6
09JUL91
FC
8.0
10 JUL 9-1
FC
5.8
11JUL91
RA
6.6
12 JUL 91
RA
4.7
1SJUL91
KA
5 . 8
17JUL91
FC
8 . 3
18JUL91
RA
5.C
19JUL91
RA
i , G
23JULS1
FC
7.7
24JUL91
RA
6.3
2 5JUL91
RA
4.1
2 6JCL31
RA
6.3
30JUL91
RA
5.5
31JUL91
FC
3 . i
01AUG91
RA
LI .'J
0 2AUG91
RA
1.1
G6AUG91
FC
7 . i
07AUG91
FC
7
UKAUG91
FC
b. i.-
09AUH91
RA
i.i
13AUG91
RA
8.0'
14AUG91
FC
8.8
1SAUG91
RA
6. 3
>1-5
f .>»!

-------
MO. II it 12 BA'I'l'Ek i
DAI LV_ PERCENT DOOR LEAKS KOH I ;J-j


Perc

Inspector
Dog i'
DATE
Initials
k
16AUG91
FC
4 . ¦i
2 0AUC9I
FC
6 . 9
21AUG91
FC
b.'J
2 2AUG91
RA
8 . :
2 3AUG91
FC
n. ^ ¦
2 7AUG91
RA
6. o
28AUG91
FC
8.2
29AUG91
RA
4.9
30AUG91
HA
5.2
Q3SEP91
FC
7.5
04SEP91
FC
B.S
05SEP91
RA
3. j
06SEP91
RA
1. i
10SEP91
RA
4 . J
11SEP91
RA
7. i
12SEP91
RA
4."<
13SEP91
RA
4 .:
17SEP91
FC
b . ^
18SEP91
FC
6 .0
19SEP91
RA
3.0
20SEP91
FC
8.1
24SEP91
RA
6.6
2SSEP91
RA
3.8
26SEP91
RA
4.;
27SEP91
FC
a. ii
010CT91
FC
fi. 2
020CT91
FC
8. a
G3QCT91
FC
4 . 4
04OCT91
FC
5 . i
08OCT91
FC
7 fc
09OCT91
FC
b . 1
10OCT91
FC
6. 6
liocrai
HA
2 . 7
150CT91
FC
S . (j
	~'\
"i
•>

-------
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-------
Appendix N
Coal Data - Summary Tables and Graphs
Table of Contents
Section
1	Summary Table of Sparrows Point Coal Mix for 1991.
i 2	Summary Table of Sparrows Point Blended Coal Chemistry
for 1991.
3	Graphs of Sparrows Point Coal Properties.
4	Sparrows Point Coal Properties - Database.
| ¦ ' -N-l

-------
Section 1
Summary Table of Sparrows Point Coal Mix for 1991

-------
SPARROWS POINT COAL MIX 1991
Individual Coal Mix "fe 1991
Low Volatile:
Cambria
Jowei
Vu. Crewe
Total Low Volatile
High Volatile:
Moss
Lo Ming
Knox Creak
Total High Volatile
January	February	March
15.0	150	15.0
66	10.0	10.0
3,4
25.0	25.0	25.0
300	30 0	30.0
45.0	45.0	45.0
75.0	75.0	75.0
TABLE 1
April	May	June
15.0	15.0	15.0
10.D	10 0	10.0
25.0	25.0	25.0
IO.0	-	-
45.0	45.0	45.0
200	300	30.0
75 0	75.0	75.0
July	August	September	October November
15.0	15 0	15 0	15.0	15.0
10.0	100	10 0	10.0	10.0
25.0	25.0	25.0	25.0	25.0
45.0	45 0	45 0	45.0	51.0
30.0	30 0	30.0	30.0	24.0
75.0	75.0	75.0	75.0	75.0

-------
Section 2
Summary Table of Sparrows Point Blended Coal Chemistry for 1991.

-------
SPAR HOWS POINT BLENDED COAL CHEMISTRY
TABLE 2
Coal Blond Properties 1991
% Moisture
% Volalilas
% Ash
% Sullur
% Minus 1/B1
Bulk Density
January
7.9
29.4-
6.2
.79
78.8
48.0
February
7.0
28.8
6.2
82
78.9
48.0
March
?.fl
20.S
6.2
eo
?b a
47 9
April
?.a
90.2
6.2
79
78.7
48.0
May
7.6
20.6
6.3
.79
76.fi
47.S
June
71
29.2
6.2
.80
76.6
48.9
July	Auqum
7.0	7.2
2S.1	so.o
6 2	6 2
-AO	-79
79.0	76.9
48.5	48.5
September	October
7.1	7-7
29.B	2tt,7
6.3	6.3
.78	.79
78.9	78 8
46.5	48 5
November
7.6
30.3
6.2
77
78.0
48.5

-------
COAL PROPERTIES - 11/12 BATTERIES
OVERALL STATISTICS
VARIABLE	AVERAGE STANDARD MAXIMUM MINIMUM NUMBER OF
VALUE DEVIATION VALUE VALUE OBSERVATIONS
% SULFUR
0.79
0.03
1.26
0.73
703
% VOLATILE MATTER
29.61
0.87
33.00
27.10
703
% ASH
6.21
0.28
9.30
5.S0
703
% FIXED CARBON
64.17
0.90
66.90
60.20
703
% MINUS 100 MESH
15.63
1.61
22.00
9.70
698
% MINUS 1/8 INCH
78.84
0.24
79.80
78.09
364
% MOISTURE
7.42
0.67
9.B1
5.55
364
BULK DENSITY, LB/CU FT
43.21
0.27
48.66
47.79
364
N-6..


-------
COAL PROPERTIES - 11/12 BATTERIES
MONTHLY STATISTICS
VARIABLE	AVERAGE STANDARD MAXIMUM MINIMUM NUMBER OF
VALUE DEVIATION VALUE VALUE OBSERVATIONS
DEC90
% SULFUR
0.80
0.02
0.85
0.77
59
% VOLATILE MATTER
29.16
0.67
32.30
28.30
59
% ASH
6.20
0.23
6.80
5.70
59
% FIXED CARBON
64.64
0.70
65.60
61.60
59
% MINUS 100 MESH
16.54
0.83
18.10
14.60
59
% MINUS 1/8 INCH
78.83
0.14-
79.15
78.54
31
% MOISTURE
7.30
0.49
8.75
6.60
31
BULK DENSITY, LB/CU FT
48.00
0.05
48.10
47.90
31
JAN91





% SULFUR
0.79
0.02
0.82
0.76
62
% VOLATILE MATTER
29.41
0.75
31.00
27.70
62
% ASH
6.24
0.23
6.80
5.70
62
% FIXED CARBON
64.36
0.80
66.20
62.50
62
% MINUS 100 MESH
16.49
1.31
19.90
12.40
62
% MINUS 1/8 INCH
73.82
0.27
79.80
78.54
31
% MOISTURE
7.92.
0.59
9.29
6.93
31
BULK DENSITY, LB/CU FT,
47.96
0.10
48.38
47.85
31
FEB91





% SULFUR
0.82
0.03
0.88
0.75
55
% VOLATILE MATTER
29.19
0.82
31.80
27.10
55
% ASH
6.20
0.24
6.70
5.80
55
% FIXED CARBON
64.60
0.93
66.90
61.50
55
% MINUS 100 MESH
15.87
1.40
18.20
12.40
55
% MINUS 1/8 INCH
78'. 08
0.21
79.44
78.61
23
% MOISTURE
6.95
0.38
7.85
6.45
28
BULK DENSITY, LB/CU FT
47.97
0.08
48.22
47.86
28
MAR91





% SULFUR
0.80
0.02
0.-85
0.76
62
% VOLATILE MATTER
29.83
0.79
31.50
28.30
62
% ASH
6.17
0.17
6.60
5.90
62
% FIXED CARBON
63.98
0.83
65.60
62.20
62
% MINUS 100 MESH
17.02
1.18
21.70
14.80
62
% MINUS 1/8 INCH
78.81
0.21
79.22
78.56
31
% MOISTURE
7.80
0.92
9.81
6.65
31
BULK DENSITY, LB/CU FT
47.94
0..07
48.10
47.82
31
APR91





1 SULFUR
0.79
0.02
0.84
0.74
58
% VOLATILE MATTER
30.18
0.74
32.00
28.60
58
% ASH
6.20
0.21
7.20
5.90
58
% FIXED CARBON
63.62
0.83
65.40
61.60
58
% MINUS 100 MESH
15.81
1.29
18.80
12.70
57
% MINUS 1/8 INCH
78.70
0.26
79.70
78.57
27
% MOISTURE
7.75
Q.38
8.90
6.95
27
BULK DENSITY, LB/CU FT
47.97
0.07
r"™ k-7.
48.10
47. SI
27

-------
COAL PROPERTIES - 11/12 BATTERIES
MONTHLY STATISTICS
VARIABLE	AVERAGE STANDARD MAXIMUM MINIMUM NUMBER OF
VALUE DEVIATION VALUE VALUE OBSERVATIONS
MAY91
% SULFUR
0.79
0.02
0.87
0.75
58
% VOLATILE MATTER
29.57
0.68
31.20
28.20
58
% ASH
6.26
0.21
6.80
5.90
58
% FIXED CARBON
64.17
0.69
65.50
62.30
58
% MINUS 100 MESH
15.24
1.64
18.60
9.70
58
%. MINUS 1/8 INCH
78.82
0.16
79.47
78.65
31
% MOISTURE
7.60
0.42
8.39
6.74
31
BULK DENSITY, LB/CU FT
47.91
0.06
48.04
47.79
31
JUN9I





% SULFUR
0.80
0.02
0.87
0.74
59
% VOLATILE MATTER
29.18
0.69
31.50
27.70
59
% ASH
6.20
0.30
7.40
5.60
59
% FIXED CARBON
64.62
0.71
66.20
62.20
59
% MINUS 100 MESH
15.54
1.87
22.00
10.60
59'
V MINUS 1/8 INCH
78.84
0.26-
79.41
78.52
30
% MOISTURE
7.07
0.45
8.28
5.95
30
BULK DENSITY, LB/CU FT
48.33
0.20
48.58
47.84
30
JUL 91





% SULFUR
0.80
0.06
1.26'
0.75
61
% VOLATILE MATTER
29.13
0.52
30.20
27.70
61
%. ASH
6.20
0.26
¦ 7.20
5.SO
61
% FIXED CARBON
64.66
0.56
66.10
63.50
61
% MINUS 100 MESH
14.62
1..76
17.70
11.00
59
%¦ MINUS 1/8 INCH
78.95
0.32
79.35
78.09
31
% MOISTURE
6.95
0.59
8.25
5.55
31
BULK DENSITY, LB/CU FT
48-48
0.06
48.62
48-38
31
AUG91





% SULFUR
0.79
0.02
0.87
0.74
62
% VOLATILE MATTER
30.00
0.75
31.90
28.30
62
% ASH
6.15
0.31
6.80
5.60
62
% FIXED CARBON
63.83
0.81
65.60
62.00
62
% MINUS 100 MESH
15.27
1.52
18.30
10.60
62
% MINUS 1/8 INCH
78.91
0.28
79.44
78.51
31
% MOISTURE
7.17
0.55
8.14
6.22
31
BULK DENSITY, LB/CU FT
48.51
0.08
48.63
48.31
31
SEP91





% SULFUR
0.78
0.03
0.85
0.73
60
% VOLATILE MATTER
29.83
0.92
31.60
28.00
60
% ASH
6.27
- 0.52
9.30
5.50
60
% FIXED CARBON
63.90
1.00
65.60
60.20
60
% MINUS 100 MESH
14.67
1.23
17.90
11.20
60
% MINUS 1/8 INCH
78.55
0. 20
79.26
73.57
30
% MOISTURE
7.06
0. 46
8.06
6.44
30
BULK DENSITY, LB/CU FT
48.48
0.07
48.66
48.36
30

i.

i



1.
		
J



-------
COAL. PROPERTIES - 11/12 BATTERIES
MONTHLY STATISTICS
VARIABLE	AVERAGE STANDARD MAXIMUM MINIMUM NUMBER OF
VALUE DEVIATION VALUE VALUE OBSERVATIONS
OCT 91
% SULFUR
0.79
0.03
0.84
0.73
61
% VOLATILE MATTER
29.67
0.96
31.60
27.10
61
%¦ ASH
6.25
0.26
6.90
5.60
61
% FIXED CARBON
64.08
0.95
66.90
62.50
61
% MINUS 100 MESH
15.46
1.55
18.80
12.00
59
% MINUS 1/8 INCH
78.84
0.18
79.23
78.50
30
% MOISTURE
7.69
0.49
8.99
6.59
30
BULK DENSITY, LB/CU FT
48.49
0.07
48.64
48.35
30
NOV91





% SULFUR
0.77
0.02
0.81
0.74
46
% VOLATILE MATTER
30.34
0.99
33.00
27.80
46
% ASH
6.20
0.19
6.70
6.00
46
%: FIXED CARBON
63.49
0.99
65.80
61.00
46
% MINUS 100 MESH
14.78
1.36
17.60
12.10
¦ 46
% MINUS 1/0 INCH
78.86
0.23
79.33
78.50
30
% MOISTURE
7.63
0.80
9.21
6.14
30
BULK DENSITY, LB/CU FT
48.46
0.06
48.63
48.34
30

-------
Section 3
Graphs ot Sparrows Point Coal Properties.
r
< -Nrio

-------
I?
80
% 75
c
CD
Q
D
GQ
C
o
jO
k_
CO
o
u
Q>
X
70
65
60
55
50
45
40
COAL PROPERTIES I
Fixed Carbon & Bulk Density
Sparrows Point Coke Batteries
12/01/90 - 12/05/91












Leg
• FIX
° BU
end
ED CAf
LK DEN
tBON
SITY





















































80
75 "5
c

-------
Coal PROPERTIES II
Moisture & Ash
Sparrows Point Coke Batteries
12/01/90 - 12/05/91
Legend
• Moisture
° Ash
"i i i i i i	i i	r
DEC JAN FEB MAR APR MAY JUN JUL AUG SEP OCT NOV DEC
1990 1991
Date
JWP
2/24/02

-------
COAL PROPERTIES lit
% -1/8 inch & % -100 Mesh
Sparrows Point 11/12 Battery
12/01/90 * 12/05/91

























































Legend
~ % -1/8 Inch








0 %
-100 mc
lah























A0*





fMr












DEC JAN FEB MAR APR MAY JUN JUL AUG SEP OCT NOV DEC
1990 1991
Date
100
90
80
70
60
50
40
30
20
10
0
JWP
2/24/92

-------
COAL PROPERTIES IV
% Sulfur & Volatile Matter
Sparrows Point Coke Batteries
12/01/90 - 12/05/91
40

35-
30
25
20-
O
=5 15
13
CO
10
0
Legend
• Volatile Matter
° Sulfur
40
35
30
25
20
<1)
CD
O
>
O
15 5
10
CO
	1	1	1	T	1	
DEC JAN FEB MAR APR MAY JUN JUL AUG SEP OCT NOV DEC
1990 1991
Date
0
JWP
2/24/92

-------
Section 4
Sparrows Point Coal Properties - Database.
/-	

-------
COAL PROPERTIES FROM DAILY COAL MIX REPORTS
KIOC DEMONSTRATION PROJECT - BETHLEHEM STEEL CORPORATION
SPARROWS POINT. MARYLAND
16:22 Tuesday, March 31. 1992 1





VOLATILE
FIXED



PCT PASSING
OB 5
DATt
ROA
TURN
PLANT
MATTER
CARBON
ASH
SULFUR
FSI
100 MESH
1
12/02/90
1225
7-3
B
28.9
65.0
6. 1
0 St
7.5
18. 1
2
12/02/9O
1225
3- 11
B
29.0
64 .9
6. 1
0.79
7.5
17.4
3
1 2/03/90
1225
7-3
B
29. 1
64.4
6.5
0.81
7.5
14.6
4
12/03/90
1225
3- 11
B
28. a
65.3
5.9
o.ao
a.o
15.2
5
12/04/90
1225
7-3
B
2a. 7
65.5
5.8
0.80
7.5
16.7
6
12/04/90
1225
3- 11
B
20 . 4
64.8
6.8
0.80
7.5
17.2
7
12/05/9O
1225
7-3
B
29.2
64.8
6.2
0,77
7.5
16.4
B
1 2/05/90
1225
3- 1 1
e
28 . 7
€5.3
6.0
079
a.o
15.9
9
12/06/90
1225
7-3
B
26.6
65.2
6.2
0.80
8.0
17.3
10
12/06/9O
1225
3- 1 1
B
26.4
65.6
6 0
0.79
7.5
16 . 7
1 1
12/07/9O
1225
7-3
B
2B . 5
65 . 1
6.4
O. 79
7.5
17.4
12
12/07/90
1225
3- 1 1
B
28. 7
65. 1
6.2
0.83
7.5
16.8
13
12/08/90
1225
7-3
B
29.9
63.9
6.2
0.78
7.5
17.7
14
12/0B/90
(225
3- 11
B
29.9
63.6
6.3
0.78
7.5
16 . 9
15
12/09/9O
1227
7-3
B
2B.4
64 9
6.7
0.77
7.5
17.2
16
12/09/90
1227
3-11
B
28.3
64 .9
6.3
0 77
7.5
16.8
17
12/10/90
1227
7-3
B
29 . 3
64 1
6.6
o.ao
7.5
16.0
18
12/10/90
1227
3-11
B
20. 3
65.4
6.3
0 80
7.5
16 . 8
19
12/11/90
1227
7-3
a
29. 1
64 7
6.2
0.80
7.5
f6.5
20
12/11/90
1227
3- 1 1
B
29 . 2
64.8
6.0
0.79
a.o
17 . 2
2 1
12/12/90
1227
7-3
B
28.9
64.8
6.3
0.79
a.o
15.5
22
12/12/90
1227
3- 11
B
29.0
64 .8
6.2
0.82
7.5
16.8
23
12/13/90
1227
7-3
B
28.6
' 65.3
6. 1
0.82
7.5
16 . 2
24
12/13/90
1227
3-11
B
2a .4
6b. 2
6.4
0.79
7.5
17.6
25
12/14/90
1227
7-3
B
28.3
04 .9
ti. 2
0-81
7.5
16 ,0
26
12/14/90
1227
3- 1 1
B
28.6
65. 2
6.2
0.82
7.5
16 .8
27
12/15/90
1227
7-3
B
28. a
65. 1
6. 1
0.81
7.5
15. 3
28
12/15/90
1227
3- 11
B
28 . 9
65.O
6. 1
0-81
/. 5
16 .0
29
12/16/90
1230
7-3
B
29.3
64.7
6.0
o.ai
7.5
16 . a
30
12/16/90
1230
3-11
B
29. 2
€4.6
6.2
0.8 t
7.0
14 .a
3 1
12/17/90
1230
7-3
B
29 . 3
64.O
6 7
0 85
7.5
17 . 3
32
12/17/90
1230
3-11
B
28.6
64.9
6.5
0 84
7.5
17.0
33
12/18/90
12 30
3- 11
u
29. 2
64.2
6.6
0.83
7.5
18 0
34
12/19/90
1230
7-3
B
29 . 2
64 .5
6.3
0.80
7.5
15.5
35
12/19/90
1230
3- 11
B
29.5
64.3
6.2
0.80
7.5
16.6
3b
12/20/90
12 30
7-3
B
29. 1
64.8
6. 1
0.80
7.0
17. 2
37
12/20/90
1230
3- 1 1
B
28.S
65. 4
6.0
0.77
7.5
17 O
38
12/21/90
1230
7-3
B
29-2
64.7
6. 1
0.80
7.5
15.8
33
12/21/90
1230
3- 1 1
B
28.9
65.0
6. 1
0.81
7.5
16. 2
40
12/22/90
1230
7-3
B
28.6
65. 1
G. 3
0.81
7.5
16.0
41
12/22/90
1230
3-t^
B
28 .3
65. i
6. 1
0.84
a.o
16. 2
42
12/23/90
1232
7-3
B
29.5
64 4
6 . 1
0.82
7.0
16. 1
43
12/23/90
1232
3-11
B
30.5
63.5
6.0
0.80
7.5
17 . 2
44
12/24/90
1232
7-3
B
30.5
63.0
6.5
0 81
7.5
17.4
45
12/24/90
1232
3- ft 1
B
30. 3
63.7
6.0
0.73
7.5
16.4
46
12/25/90
1232
7-3
B
29.7
64 .3
6.0
0.78
7.5
16. 8
47
12/25/90
1232
3-11
B
29.5
64.3
6.2
0.82
a.o
17.6
4fi
12/2S/90
1232
7-3
B
32. 3
61.6
6. 1
0.82
7.5
14.9
49
12/26/90
1232
3-11
B
30. 1
63.8
6. 1
0.82
8.0
16. 1
50
12/27/90
1232
73
B
29 .9
63.8
6.3
0 82
a.o
15.5
51
12/27/00
1232
3 11
B
29 .6
63.8
6 6
0.79
a.o
16.3
52
12/28/90
1232
7-3
B
30.0
64 1
5.3
0 78
75
15.8
53
12/28/90
1232
3-M
B
29.0
64.8
6.2
0.78
a.o
15. 1

-------
CDAL PRDPtKTIES FROM DAILY COAL MIX REPORTS
K1UC DEMONSTRATION PROJECT ~ BETHLEHEM STEEL CORPORATION
SPARROWS POINT, MARYLAND
16:22 Tuesday, March 31, 1992 2
25
i






VOLATILE
FIXED



PCT PASSING
OBS
DATE
RQA
TURN
PLANT
MATTER
CARBON
ASH
SULFUR
FSI
100 MESH
54
12/29/90
123?
7-3
B
29. 1
G5.2
5.7
0.81
B.O
15.2
55
12/29/9O
1232
3-11
B
28.8
65.3
5.9
0.79
7.5
16. B
56
12/30/9O
1234
7-3
B
2B.B
65. 1
6.1
0.81
7.5
17.4
57
12/30/90
1234
3- 11
R
28. 7
£5.5
5.8
0.80
8.0
16.4
58
12/31/90
1234
7-3
B
29.2
64.4
6.4
0.80
7.5
18. 1
59
12/31/QO
1234
3- 11
B
29. 3
64 .5
6.2
o.ao
7.5
16 .6
60
01/O1/91
1234
7-3
B
29.7
63.9
6.4
0.79
7.5
17 . 1
61
01/CJ1/9 1
1234
3-11
B
30.0
63. B
6.2
0.79
6-0
15.9
62
01/02/91
1234
7-3
B
28 . 5
65.4
6. 1
0-S2
8 .0
16.3
63
01/02/91
1234
3-11
B
28.9
64.7
6-4
0.62
8.0
14.4
64
01/03/91
1234
7-3
B
28.9
65. 1
60
0.82
7.5
17.5
65
01/03/91
1234
3- 11
B
28.6
65.5
5.9
O.B2
7.5
16.2
66
01/04/91
1234
7-3
B
28.S
64 .a
6.3
0.81
8.0
16.3
67
01/04/91
1234
3- i 1
B
2S.2
65.5
6.3
o.ao
6.0
17.0
68
01/05/91
1234
7-3
B
30.0
63.4
6.6
0.76
7.0
15.8
69
01/05/&1
1234
3-11
B
29.6
64 .2
€.2
0.79
7.5
16.2
70
Ol/Ob/91
1236
7-3
B
31.0
62.5
6.5
0.78
8.0
17.5
7 t
O1/06/91
1236
3-11
B
29. 7
64.6
5.7
0.77
7.5
18.3
72
01/07/91
1236
7-3
B
28.5
65.2
6.3
O.S2
7.5
17. 1
73
- 01/07/91
1236
3-11
B
29. 1
64.6
6.3
0.79
B.O
16.4
74
01/OB/91
1236
7-3
B
27,7
66.2
6.1
0.79
8.0
15.8
75
0I/O8/S1
1236
3- 1 1
B
27.9
65.9
6.2
0.79
6.0
16. 1
76
01/O9/91
1 23€
7-3
B
26. 3
65 „ &
5 9
0.81
B.O
17.6
77
O1/09/91
1236
3-11
B
28.7
65.2
€.1
0.81
7.5
17.3
78
O1/10/91
1236
7-3
B
29. 4
63,8
6.8
0.79
7.5
18.8
7S
01/10/91
1236
3-1 i
B
30.0
63.7
6.3
0.8 1
7.5
1B.0
BO
01/11/91
1236
7-3
B
28.5
65.5
€.0
0.82
7.5
17.2
B1
01/11/91
1236
3- 1 1
B
29.5
64,0
6.5
0.80
8.0
16. b
B2
01/12/91
1 236
7-3
B
30.3
63.5
6.2
0.79
8.0
17.4
83
01/12/31
1236
3-11
B
29.6
64.3
6.1
0.82
8.0
16.8
B4
01/13/31
1238
7-3
B
30. 7
63. 1
6.2
0.79
B.O
17 .0
85
01/13/91
1 236
3-11
B
30.4
63:2
6.4
o.ai
7.5
16 . 3
86
01/14/91
1238
7-3
B
29. 5
' 64.4
6. 1
0.78
7 .5
15.8
87
01/14/91
1238
3-1 1
B
29.6
64.4
6.0
O. 79
7.5
16.8
8a
01/15/91
1238
7-3
B
30.8
63.3
5.9
0.79
7.5
16.7
89
01/15/91
1238
3-11
B
30.8
63.4
6.4
0-77
7 0
16. 1
9G
01/16/91
1238
7-3
B
29.6
64.2
6.2
0.82
7 .5
19 H
91
01/16/91
1238
3-11
B
30 . 4
63 8
5.8
0.77
7.5
14.8
92
01/17/91
1238
7-3
B
30.0
63.7
6.3
0.79
8.0
16.4
93
01/ t "7 / fi 1
1 2'J8
3-11
B
30 O
63 . 7
6.3
O- 78
8.0
IB . B
94
01/18/91
1238
7-3
B
30 1
63 9
6.0
O. 80
7 .5
16.4

01/ ia/91
12J6
3-lt
B
29 . 2
64 . 7
6. 1
0.80
7.5
17 .0
9&
01/19/9 I
1
7-3
B
29.8
64 . 2
6.2
0.82
7.0
16.S
97
01/19/91
1238
3- 1 1
B"
30. 1
64 . 1
5-8
0.78
8.0
16.5
98
01/20/91
1 240
7-3
B
29 . 4
64 ,5
6. 1
0.80
7 .b
15 .0
99
01/70/91
1240
3- 1 1
B
29 . 6
6.4.4
6.0
0.79
7.0
15. 9
100
01/21/91
1240
7-3
B
29.3
64.2
6.5
0.81
7.5
14.7
101
01/21/91
1240
3- 1 1
B
29 , 7
64.0
6.3
0.79
7.5
16 . B
102
01/22/91
1240
7-3
B
30 . G
62.9
6.5
0.76
8.0
15.6
(03
01/22/91
1240
3-1 1
B
30.0
63.4
6.6
0.77
8.0
16.0
104
01/23/91
1240
7-3
B
29 . 3
64 .5
6.2
0.78
7.5
15.2
105
01/23/91
1240
3- 1 1
B
28.6
65.4
6.0
0.80
7 .5
17.9
106
01/24/91
1240
7-3
B
28.6
65.2
6.2
0.8 1
8.0
15.9

-------
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-------
COAL PROPERTIES FROM DAILY COAL MIX REPORTS
Kinr: demonstration project - bethlehem steel corporation
SPARROWS POINT, MARYLAND
1G:22 Tuesday. Marcfi 31. 1992 4





VOLATILE
f IXE0



PCT PASSING
QQS
DATE
ROA
TURN
PLANT
MATTER
CARBON
ASH
SULFUR
F5I
100 MESH
160
02/20/91
1252
7-3
B
28.9
64-8
6.3
0.81
7.5
13.3
161
02/21/91
1252
11-7
B
28.9
65.4
6.3
0.83
7 . 5
66.8
162
02/21/91
1252
7-3
B
28,7
64 fi
6.5
0.83
7.5
16.6
163
02/22/91
1*252
11-7
B
29.0
64.9
6.1
0.84
7.5
15.3
164
02/22/91
1252
7-3
B
SB.8
64.9
6.3
0. 83
? . 5
17.7
165
02/23/91
1252
1 1-7
B
29.5
64.3
6.2
0.82
8.0
16.8
166
02/23/91
1252
7-3
B
29. 1
64.7
6.2
0.82
8.0
15.6
167
02/24/91
1254
11-7
B
28.3
65.6
6.1
0.84
a.o
15.3
168
02/24/91
1254
773
B
29.2
64 .9
5.9
0.84
8.0
16.3
169
02/25/91
1254
11-7.
B
28.4
65.4
62
0.82
8.0
16.O
170
02/25/91
1254
7-3
B
29.3
64.7
6.0
0.80
7.5
16.0
17 1
02/26/91
1254
1 1-7
B
27 , 1
66.9
6.0
0.83
7.5
17.7
172
02/26/91
1254
7-3
B
27 .6
£6.4
6.0
0.82
a.o
16 . 9
173
02/27/91
1254
11-7
B
30.6
62.8
6.6
0.83
? . 5
S6.5
174
02/27/91
1254
7-3
B
31.8
61.5
6.7
O.B2
7.5
16 8
175
02/28/91
1254
11 7
B
30.5
63.2
6.3
0.79
8.0
17. 1
176
02/28/91
1254
7-3
B
29.4
64.2
6.4
O. BO
7.5
16.8
177
03/01/91
1254
11-7
B
29.7
64. 1
6.2
0.78
7.0
17.0
		— 178
03/01/91
1254
7-3
B
29.3
64.5
6.2
0.80
7.0
16.8

179
03/02/91
1254
11-7
B
29.0
64.9
6.1
0.81
7.5
15.6

180
03/02/91
1254
7-3
B
29.3
64 5
6.2
0.80
7.0
16.6
*.v
181
03/03/91
1756
11-7
B
29.8
64. 2
6.0
0.80
7.5
16.0
J
182
03/03/91
1256
7-3
B
26.7
65.2
6- t
0.76
6.0
16.4
v-SS
183
03/04/91
1256
11-7
B
30. 9
62.9
6.2
0.79
8.0
17 . 1
8'
' l-li
184
03/04/91
1256
7-3
B
30.3
63.3
6.4
0. SO
7.5
16.3
sO
185
03/05/91
1256
11-7
B
30.7
62.7
6.6 '
0.76
7.5
16.8

186
03/05/91
1256
7-3
B
30,0
63.9
6. 1
0.79
8.0
16.2

1fi7
03/06/91
1256
11-7
B
28.9
65.2
&.9
O. 83
7.5
17 .5
i iaa
03/06/91
1256
7-3
B
29 .6
64 4
6.0
0-80
7.5
17 „ 1
~ 189
03/07/91
1256
11-7
B
29.0
64 .9
6. 1
0.78
7.5
17 .O
190
03/07/91
1256
7-3
B
28.9
64.9
6.2
o.ao
8.0
16 . 4
191
03/08/91
1256
1 1-7
B
29 .0
64.7
6.3
0.80
8.0
16 .4
192
03/08/91
1256
7-3
B
29.8
64 1
6. 1
0- 83
7.5
17 . 1
(93
03/09/91
1256
11-7
B
29.5
64. 1
6.4
0.80
8 .O
16.5
194
03/09/91
1256
7^3
B
29.5
64 3
6.2
0.&1
& .O
16.9
195
03/10/91
1258
11-7
B
28 . 9
64 .8
6.3
O. 79
7 .5
17 .3
196
03/10/91
1258
73
B
26 .7
64.9
6.4
0.81
7.5
17 . 1
197
03/11/91
1258
11-7
B
28 .3
65 .6
6 . 1
o.ai
8.0
16 . 8
198
03/1 1/91
1258
7 3
B
28 .7
65 .3
6.0
0. 79
7 . 5
16.fi
199
03/12/91
1258
1 1 -7
B
29.2
64 .5
6.3
0.80
7 . 5
17 .5
?oo
03/ 12/91
t25B
7-3
B
28 . 7
64 .9
6.4
0.3 I
7 . 5
17 . 4
201
03/13/9 1
1258
1 1-7
&
30.4
63.4
6.2
0.80
7.5
17.3
202
03/13/9 1
1258
7 3
B
30.3
63.3
6.4
0.77
7.5
16 .0
203
03/ 14/9 1
1258
117
B
30 . 4
63 3
6.3
O. 78
7 . 5
16 . 8
204
03/14/91
1258
7-3
B
30.0
63 .4
6.6
O. 78
7.0
16.3
205
03/15/91
1258
11-7
B
23.5
64 .4
6. 1
0.80
7.5
16.3
206
03/15/91
1258
7-3
B
28 .6
64 1
6.3
O. BO
7 . 5
16.0
207
03/16/91
1258
11-7
B
2B.3
65.4
6.3
0.83
8.0
15.9
206
03/10/91
1258
7-3
a
29.8
64.2
6.0
O . 8 1
7 . 5
16.6
" - 209
03/17/91
1 2 GO
1 1-7
a
28.9
65.0
6. 1
0.81
8.0
18.8
210
03/17/91
1260
7-3
B
29.0
64.9
6. 1
0.8I
7.0
19.3
2 1 !
03/18/91
120O
1 1-7
B
30.8
63 . 1
6 . 1
0.80
7 , 5
14 . 8
2 12
03/18/91
1260
7-3
B
SO. 6
63.5
5.9
0.79
7.5
16.9

-------
COAL PROPERTIES FROM DAILY COAL MIX REPORTS
KIDC DEMONSTRATION PROJECT - BETHLEHEM STEEL CORPORATION
5PAKWOVS PO/NT, MARYLAND





VOLATILE
FIXED


oes
DATE
ROA
TURN
HLANT
MAT 1tR
CARBON
ASH
SULFUR
2 13
03/19/91
1260
1 1-7
R
30.3
63.5
6.2
0.77
214
03/19/91
1260
7-3
B
30.6
63. 3
6 1
0.77
215
03/20/91
1260
11-7
B
30-3
63.7
6.0
0.8O
216
03/20/91
1260
7 3
a
29.7
64.3
6 O
o.so
217
03/21/91
f 260
1 1 -7
B
29.0
G5. 1
5.9
o.ao
2 18
03/21/91
1260
7-3
B
29.5
64.5
6 0
0. 79
219
03/22/91
1260
1 1-7
B
29.9
64. O
6 1
0.81
220
03/22/91
(260
7-3
a
30.5
63.5
SO
0.81
221
03/23/91
1260
1 1-7
B
30.8
63.0
6 2
0.79
222
03/23/91
1260
7-3
B
30.5
63. 3
6 . 2
O.SO
223
03/24/91
1262
1 1-7
a
30. 1
63. a
6. 1
O . 79
224
03/24/91
1262
7-3
B
30.3
63.4
6 3
0.82
225
03/25/91
1262
1 1-7
B
29 . 2
64 .8
SO
G.82
226
03/25/91
1262
7-3
B
29.4
64 . 4
6 2
0.85
227
03/26/91
1262
1 1-7
B
29 0
64 .4
6.6
0.80
228
03/26/91
1262
7-3
B
30.8
63. 1
6. 1
0.81
229
03/27/91
1262
11-7
B
31 . 3
62.6
6. 1
0.92
230
03/27/91
1262
7-3
a
31. 1
62.9
6.0
0.81
23 1
03/28/91
I2G2
1 1-7
B
3Q.6
63. 3
6 . 1
0.8 1
232
03/28/91
126?
7-3
B
30.5
62.2
6,3
0.82
233
03/29/91
1262
1 1-7
B
30 . 3
63 7
6 0
0.79
234
03/29/91
1262
7-3
B
30.5
63 4
6 1
O .80
235
03/30/91
1262
1 1-7
. B
31.5
62 4
6. 1
0. 76
236
03/30/91
1262
7-3
B
30.8
63 1
6 1
0. 77
237
03/31/91
1264
11-7
B
30. 3
63. 3
b 4
0.77
238
03/31/91
1264
7-3
a
30.5
63. 1
6.4
0.80
239
04/01/91
1264
1 1-7
B
so. a
63.2
6 0
O 78
240
04/01/91
1264
7-3
B
30.8
63.0
6 2
0 81
24 \
04/02/91
12G4
11-7
a
30.4
63.3
6.3
0.81
242
04/02/91
1264
7 3
~
29.6
64.3
6. 1
0.84
24a
04/03/91
1264
1 1-7
B
31.5
62 1
6 . 4
O.EI
244
04/03/91
1264
7-3
B
31.6
61 .8
6 . 6
0.7B
245
04/04/91
12G4
1 1-7
a
31 .O
62 .8
6.2
0.83
246
04/04/91
1264
7-3
B
30.4
63.5
6 . 1
0.78
217
04/05/9 1
1264
1 1-7
B
30. 1
63.6
6 3
0.77
248
04/05/91
1264
7-3
B
316
62. 3
6. 1
0.81
249
04/06/91
1264
1 1-7
B
30.7
63. 3
SO
0 81
250
04/06/91
1264
7-3
B
30.8
63. 1
6 . 1
0.79
251
04/07/91
1266
11-7
B
30. 4
63.3
6 . 3
0 .80
252
04/07/91
1266
7-3
a
31 2
62 .4
6.4
0 80
253
04/00/91
1266
11-7
u
29.4
64 .6
6 O
0 77
254
04/08/91
1266
7-3
B
29.5
64.6
5 3
0.79
255
04/09/91
1266
11-7
B
30.2
63. 7
6 . 1
0.76
256
04/09/01
1266
7-3
B
30.6
63 2
6 . 2
0.76
257
04/10/9 1
1266
1 1-7
B
30. 4
63.5
6 1
0.80
25b
04/ 10/91
1266
7-3
B
30-2
63.8
6 0
0.79
259
04/11/91
1266
1 1-7
B
30. 5
63. 3
6.2
0.77
260
04/1 1/91
1266
7-3
B
31 .0
62.5
6.5
0.77
26 1
04/12/91
1266
1 1-7
B
29 . 2
64.6
6 2
0,77
262
04/12/91
1266
7-3
B
2B. 7
65. 2
6 1
0.77
263
04/13/91
1266
11-7
B
31 . 1
62.8
6. 1
0.78
2fc>4
04/11/91
t 9 fifi
7-3
B
30. 7
63 3
6.0
0.75
265
04/14/91
1268
1 1-7
B
29 . 8
64 .0
6 2
0.77
16:22 Tuesday. March 31, 1992 5
PCT PASSING
FSI
100 MESH
7.5
15.5
7.5
16 .0
SO
16 . 7
7.0
15. 3
7.5
16.0
7.5
16.6
7.5
16.5
7.5
17 0
7.5
16.5
7.5
17. 1
7 a
ts.s
7.5
16.2
7.5
17.5
8 .O
16.8
7.5
21 . 7
8 .O
13 . 7
7.5
16.3
8.0
18. 1
7.5
20.5
7.5
16. b
8.0
13.0
7.5
17.4
7.5
18.5
7 . 5
17.3
7 . 5
17.2
8.0
15.6
7.5
15.2
7 O
14.8
7.5
16.3
7.5
15. 1
8.0
17. 1
8,0
15.2
7.0
16 . 1
7.b
16.7
7. 0
15.0
7 , 5
17.0
7.5
16.5
7 , 5
17. 1
8.0
17.4
7.0
16.6
7.5
18.2
a.o
17.6
7-5
16.5
7.5
17. 1
7.5
17.0
7.5
16.9
7.5
17.7
7.5
17. 1
a.o
16 . 4
a.o
18.6
7.5
15. 1
8 .O
14.7
7.5
14.2

-------
COAL PROPERTIES FROM DAILY COAL MIX REPORTS
KIDC DEMONSTRATION PROJECT - BETHLEHEM STEEL CORPORATION
SPARROWS POINT, MARYLAND





VOLATILE
FIXED


OB 5
DATE
ROA
TURN
PLANT
MATTER
CARBON
ASH
SULFUR
266
04/11/91
1268
7-37
B
30.2
63 .4
6 .4
O. 79
267
04/15/91
1268
11-7
B
29.6
64 .4
6.0
0.81
268
04/15/91
1268
7-3
B
29.5
64 .4
6 . 1
O. B4
269
04/16/91
1268
11-7
B
30.3
63.4
6.3
0.78
270
04/16/91
1268
7-3
B
30.5
63.0
6.5
0.79
271
04/17/91
1268
1 1-7
B
29 .2
64 .6
6.2
0 . 78
272
04/17/91
1268
7-3
B
29.7
64.0
6.3
0.79
273
04/ 18/91
1268
11-7
B
26 .6
65 .4
6.©
0.82
274
04/ 18/91
1268
7-3
B
29 . 5
64 3
6.2
0.82
275
04/19/91
1268
11-7
B
30.9
62 .9
6.2
0.80
276
04/19/91
1268
7-3
B
31.1
62 .5
6.4
0.83
277
04/20/91
1268
11-7
B
32.0
61.6
6.4
0.78
278
04/20/91
1268
7-3
B
30 -3
63.5
6.2
0.81
279
04/21/91
1270
1 1-7
a
30.4
63.3
6.3
0.77
280
04/22/91
1270
11-7
B
29.6
64.4
6.0
0.77
281
04/22/91
1270
7-3
B
30.0
63.6
6.4
0.82
262
04/23/91
1270
1 1-7
B
30. 4
63.5
.6.1
0.76
283
04/23/91
1270
7-3
B
30.4
63.2
6.4
0.77
284
04/24/91
1270
11-7
B
29.7
64 5
6.©
0.76
285
04/24/91
1270
7-3
B
30.4
63.5
6.3
0.76
286
OA/26/9 1
1270
11-7
B
29.5
64.6
5.9
0.75
287
04/25/9 1
1270
7-3
B
29 . a
64 .2
6.0
0 . 74
288
04/26/91
1270
11-7
B
29.6
64.2
6.©
0.77
289
04/26/91
1270
7-3
B
30. 1
62 .7
7.2
o.ao
2 SO
04/27/91
1270
11-7
B
30. 1
63 .7
6.2
0.76
291
04/27/91
1270
7-3
B
30.2
63.7
6.1
0.76
292
04/28/91
1272
11-7
B




saa
04/38/91
1272
7-3
B
29 . 2
64 .7
6. 1
0.77
294
©4/29/91
1272
11 7
B
29.5
64.4
6. 1
0.77
29b
©4/29/91
1272
7-3
B
29.4
64.7
5.9
0.78
29G
04/30/91
1272
1 1-7
B
29 . 4
64 2
6.4
0.78
297
04/30/91
1272
7-3
B
29.2
64.5
6.3
0.75
296
©5/01/91
1272
1 1 7
B
28 . 2
65.5
6.3
0.79
299
05/01/91
1272
7-3
B
28.9
64. B
6.3
0.77
300
05/02/91
1272
11 -7
B
28.3
65. 1
6.6
0. 78
301
05/02/91
1272
7-3
B
28.5
64.7
6.8
0.79
302
05/03/91
1272
11-7
B
30. 1
63.6
6.3
0.77
303
05/03/91
1272
7-3
B
30.0
63.5
6.5
0. 76
304
O5/04/91
1272
1 1 -7
B
29 .9
64 .0
6. 1
0.76
305
05/04/91
1272
7-3
B
29 .9
63.7
6.4
0.76
306
05/05/91
1282
1 1-7
B
23 .3
64. O
6.7
0.7B
307
05/05/91
1282
7-3
B
28 . 9
64.9
6.2
0,79
308
05/06/91
1282
11-7
B
29 . i
64 f
6.8
o.ao
309
05/06/91
1282
7-3
B
28.7
65 0
6.3
0.81
310
05/07/91
1282
1 1-7
B
29.4
64.5
6. 1
0. 79
31 1
05/07/91
1282
7-3
B
28.9
64.9
6.2
o.ao
3 1 2
05/08/91
1282
1 1-7
B
29 .4
64 .5
6 . 1
0.77
313
05/08/91
1282
7-3
B
29 .6
64 .5
5.9
0.77
314
05/09/91
1282
1 1-7
B
29.6
64. i
6.3
0. 76
315
05/09/91
1282
7-3
B
28 .7
65 .2
6. 1
0. 62
316
05/10/9 1
1282
11-7
B
20 .7
65 2
6.1
0.83
317
OS/10/91
1282
7-3
B
29.5
64.2
6.3
0.79
318
05/11/91
1282
t 1-7
B
29.4
64 .5
6. 1
0.78
16:22 Tuesday, March 31, 1992 €
PCT PASSING
FSI	100 MESH
7
5
12
7
7
0
15
3
7
5
16
3
7
5
15
5
7
5
15
2
7
5
13
6
7
5
14
4
8
0
14
3
7
5
15
4
7
5
14
2
a
0
15
4
B
0


8
0
16
8
8
0
14
2
7
5
14
4
7
5
15
1
7
5
18
8
7
O
14
0
7
0
14
7
7
5
15
8
7
0
15
5
7
O
14
7
7
5
16
0
7
5
15
2
S
0
1G
4
7
5
14
6
7
b
16
3
7
5
17
0
7
5
15
5
7
O
14
4
7
5
16
0
7
5
(4
S
8
0
15
5
7
5
17
1
8
0
16
2
7
5
15
0
7
5
16
1
7
0
14
a
7
5
15
6
7
5
16
9
7
5
16
5
8
0
16
3
8
0
15
9
7
5
15
6
8
0
16
1
8
0
14
2
8
0
16
1
8
0
16
4
8
0
16
4
7
5
13
2
7
5
15
4
8
O
17
1

-------
COAL PROPERTIES FROM DAILY COAL MIX
KI DC DEMONSTRATION PROJECT - BETHLEHEM STI
SPARROWS POINT. MARYLAND
VOLATILE FIXED
OBS
DATE
KQA
TUHN
PLANT
MATTER
CARBON
3 19
05/11/91
1282
7-3
B
28 .9
64 . a
320
05/12/91
1284
1 1-7
B


32 1
05/12/91
1264
7-3
B
28 . 7
65 .0
322
05/13/91
1284
11-7
B


323
05/13/91
1284
7-3
B
29.9
G4! 0
324
05/14/91
1284
11 -7
B
29.5
63 . 9
325
05/14/91
1284
7-3
B
29 .6
64 .0
326
05/15/91
1284
11-7
B
30.0
63.6
327
05/15/91
1284
7-3
B
31.1
62 .8
328
05/16/91
1284
11-7
B
29.6
63.6
329
05/16/91
1284
7-3
B
30.3
63.5
330
05/17/91
1284
1 1-7
B
30.7
63. i
331
05/17/91
1284 .
7-3
B
31 .2
62.3
332
05/18/91
1284
7-3
B
30.8
63 . 1
333
05/18/91
1284
3-11
B
30. i
63.7
334
05/19/91
1286
11-7
B
30.7
63.2
33b
05/19/91
1286
7-3
B
30.8
63 .0
336
05/20/91
1286
11-7
B
29.6
64 . 4
337
05/20/91
1286
7-3
B
29.4
64.5
338
05/21/91
128S
1 1-7
B
29.4
64.5
339
05/21/91
1286
7-3
B
29.0
64.9
340
05/22/91
1286
1 1-7
B
29.5
64 .3
34 1
05/22/91
1286
7-3
B
29 . 3
64 . 7
342
05/23/91
1286
1 1-7
B
29.5
64.3
343
05/23/91
1286
7-3
B
29.2
64.8
344
05/24/91
1286
11-7
B
29.4
64.4
345
05/24/91
1286
7-3
B
2 9.6
64. f
346
05/25/91
1286
1 1-7
B
29.6
64.2
347
05/26/91
1290
1 1-7
B
28.5
65.5
348
05/26/91
1290
7-3
B
29.7
64.2
349
05/27/91
129Q
7-3
B
29.6
64 .2
350
05/28/91
1 2 BO
11-7
B
30. 2
63 . 1
351
05/28/91
1290
7-3
B
29.9
63.8
352
05/29/91
1290
1 1-7
B
29 .2
64 .5
353
05/29/91
12 BO
7-3
B
3D 4
£3.2
354
05/30/91
1290
1 1-7
B
30.3
63.6
355
O5/30/91
12 SO
7-3
B
29.4
64.2
356
05/31/91
1290
1 1-7
B
29.6
64,3
357
05/31/91
1290
7-3
B
29. e
63 6
358
06/QI/91
1290
11-7
B
29.6
64 . 4
3b9
06/01/91
1 2 90
7-3
B
29.9
64.0
3GO
06/02/91
U92
11-7
B
29.6
64 . 4
36 1
06/02/9i
1292
7-3
8
30.0
64 .0
362
06/03/91
1292
11-7
B
29.6
63.6
363
06/03/91
1292
7-3
e
29.8
64 . 2
364
06/04/91
1292
11-7
B
29.5
64.7
365
06/04/91
1292
7-3
B
3O.0
64 . 3
366
06/05/91
1292
11-7
B
30. 1
63.9
3b7
06/05/91
1292
7-3
B
29 8
63. B
368
06/06/91
1292
11/
B
29.8
63 . 6
369
06/06/91
1292
7-3
B
29 .3
64 . 9
370
06/07/91
1292
11-7
6
29.7
63.7
37 1
0G/07/91
1232
7-3
B
29.9
64 .0
REPORTS
[EL CORPORATION
16:22 Tuesday, March 31, 1992
7
ASH
SULFUR
FSI
6 2
O 80
7.5
6.3
0.79
8.0
6.1
0.78
8 .0
6 . 6
0 . 79
8.Q
6.4
0.81
7.6
6.4
0.79
7.5
6.1-
0.78
8.0
6.6
0.83
7.5
6.2
0.80
8.0
6.2
0.75
8.0
6,5
0.80
7.5
6. i
0 . 76
S.O
6 2
0.78
8.0
6. 1
0.79
a.o
6.2
0.77
7.5
6.0
0.79
7.5
6. t
0. 79
7.5
6. 1
0. 79
7.5
6. 1
0.79
8.0
6.2
0.87
8.5
6.0
o.ao
8.0
6.2
0.79
8.0
6.0
O.S1
8.0
6.2
0.79
7.5
6.3
0.79
8.0
6 . 2
0.78
B.O
6.0
0.80
7.5
6 . 1
0.81
7.5
6 . 2
0.77
7.5
6.7
O. 79
7.5
6.3
0.80
B.O
6.3
0.82
7.5
6,4
0.79
8.0
6. 1
0.84
7.5
6 4
0.77
7.5
6. 1
0.77
7.5
6.4
0. 79
7.5
6.0
0.80
7.5
6. 1
0.80
7.0
GO
Q.82
a.o
6.0
0.80
7.5
6.8
0.77
7.5
6.0
o.ai
7.5
5.8
0.83
7.5
5 . 7
0.80
7.5
6.0
0. 79
7.5
6 4
0.79
7.0
6.6
O. 78
7 . 5
5.8
O.S1
7 .5
6.6
0.74
7.5
6. 1
0. 78
8.0
PCT PASSING
tOO MESH
15.2
16.6
15.4
16.8
14.7
16.2
15 .O
16.4
16.4
16.2
15.5
17.5
18.6
I7.fi
17.6
15.2
13.5
10.9
13.9
I I .9
13.5
1S.fi
9.7
15. 2
14.6
12.5
12.6
14.0
14 .9
16.8
15.0
14 .9
15.3
14.4
15.0
14.0
14	.O
14.8
15.5
14.6
16.2
10-6
19 . 1
15.2
13.7
15.0
12.9
13.2
15	a
13.2
14.0

-------
COAL PROPERTIES FROM DAILY COAL MIX REPORTS
KIDC DEMONSTRATION PROJECT - BETHLEHEM STEEL CORPORATION
SPARROWS POINT. MARYLAND





VOLATILE
FIXED


DBS
DATE
ROA
TURN
PLANT
MATTER
CARBON
ASH
SULFUR
372
06/06/91
1292
11-7
R
29.6
64 3
6. 1
0.83
373
06/06/91
1292
7-3
B
29.4
64.7
5.9
0.79
374
06/09/91
1296
11-7
B
29.5
63, 1
7.4
©. 79
375
06/O9/9!
1296
7-3
B
28.7
65.0
6.3
O. 78
376
06/10/91
1296
11-7
B
28.5
65 1
6.4
0.83
377
06/10/91
1296
7-3
B
28.7
65.0
€.3
0.81
378
06/11/91
1296
11-7
B
28.7
65.4
5.9
O. 82
379
06/11/91
1296
7-3
B
29. 1
65.0
5.9
O- 78
380
06/12/91
1296
11 7
B
28.7
64 .7
6.6
0.79
381
06/12/91
1296
7-3
B
28. 9
64 .7
6.4
0- 79
382
06/13/91
1296
11-7
B
29.0
64 .7
6.3
0.80
383
06/13/91
1296
7-3
B
28.7
64 .7
6.6
0.81
384
06/14/91
1296
11-7
B
28.9
64 ,9
6.2
0.78
385
06/14/91
1236
7-3
B
28.6
65 .0
6.4
0.83
388
06/15/91
1296
11-7
6
29 . 4
64 .3
6.3
0.79
387
06/15/91
1296
7-3
B
29.7
64 1
6.2
0.80
3BB
06/16/9 1
1298
i 1-7
B
30 .9
62.6
6 .0
0. 76
389
06/ 16/9 1
1298
7-3
B
31 .5
62 2
6.3
0. 74
390
06/17/9 1
1298
11-7
B
29.5
64.9
5.6
0. 76
39 I
06/17/91
1296
7 3
6
29.7
64.7
5.6
0.77
392
06/18/91
1298
11-7
B
30. 1
64 1
6.0
0.77
393
06/18/91
1290
7~3
B
29.7
64 .9
5.6
0. 75
394
06/19/91
1298
11-7
a
28.3
65 .3
6.4
O.BO
395
06/19/91
1298
7-3
B
28.7
64,9
6.4
0.85
396
06/20/91
1298
11-7
B
29.3
64.4
6.3
0. 79
397
06/2O/9I
1298
7-3
B
28.6
65.2
6.2
O.SO
39B
06/21/91
1298
11-7
B
28.8
65. 1
6. 1
0.80
399
06/21/91
1298
7-3
B
29.5
64. 3
6.2
O.BO
400
06/22/91
1298
11-7
B
28. 7
65.2
6. 1
O.SO
401
06/23/91
1302
11-7
6
29.3
64.5
6.2
0.79
402
06/23/91
1302
7-3
e
28.7
65. i
6.2
0.81
403
06/24/91
1302
11-7
B
28.6
65.0
6.4
0.80
404
06/24/91
1 3Q2
7-3
B
29.0
64.7
6.3
0.78
405
06/25/91
(302
" 11-7
B
28.3
65.4
6.3
0.62
406
06/25/91
1302
7-3
B
28.2
65.6
6.2
0.85
407
06/26/91
1302
11-7
B
29.0
64.8
6.2
0.78
408
06/26/91
1302
7-3
&
29.3
64.4
6.3
0.79
409
06/27/91
1302
11-7
B
28.7
65.0
K.3
0.79
4 10
06/27/91
1302
7-3
B
28 . 4
65.2
6.4
0. 79
4 11
06/28/91
1302
t 1 -7
B
28.5
65 .3
6.2
0-79
412
06/28/91
1302
7-3
B
28.4
65.3
6.3
0.79
4 13
06/29/91
1302
t 1-7
8
28. 5
65. 4
6. 1
0.81
4 14
06/29/91
1302
7-3
6
28.5
65 5
6.0
0.87
415
06/30/91
1304
11-7
B
28.6
65.2
6.2
0.77
4 Ifi
06/30/91
S304
7-3
B
27 . 7
66 2
6 1
O.SO
417
07/01/91
1304
11-7
e
28.4
65.5
6. 1
0.79
418
07/01/91
1304
7-3
B
27 . 7
66.0
6.3
0.81
4 19
07/02/91
1304
11-7
B
28. 7
65 3
6.0
0.81
420
07/03/91
1304
11-7
B
27.9
66. i
6.0
0.77
421
07/03/91
1304
7-3
B
28.8
64.8
6.4
0.80
422
07/04/91
1304
14-7
B
28.3
65. 3
6.4
0.79
423
07/04/91
1304
7-3
B
28.7
64.8
6.5
0.77
424
07/05/91
1304
11-7
B
28.2
65.7
6. 1
0.80
16:22 Tuesday, March 31. 1992 8
PCT PASSING
FSI	lOO MESH
7.5	13.3
7.5	12.9
7.5 . 13.7
a.O	14.6
a.o	is n
7.5	15.0
7.5	14.8
7.5	16.6
7.5	15.1
B.O	16.1
7.5	16.0
8.0	17.0
S.O	16.3
7.5	16.1
7.5	13.6
7.5	14.0
7.5	12.4
7.5	14.4
8.0	14.8
7.5	16.4
7.5	14.8
8.0	16.4
7.5	14 4
8.0	17.S
7.5	IG.t
7.5	IT.2
B.O	16.2
7.5	16.8
7.5	14 4
8.0	18.4
S.O	18.4
a.O	15.2
7.5	17.1
B.O	18.0
7.0	15.6
7.5	16.4
B.O	ISO
7.5	17 0
8.0	15 6
7.5	17.6
7.5	15.6
8.0	22.0
B.O	17.6
B.O	16.4
7.5	16.4
7.5	16.1
7.5	16.8
7.5	14.5
7.5	17.0
7.5	15 5
7.5	17.0
7.5	16,5
7.b	14.2

-------
COAL PROPERTIES FROM DAILY COAL MIX
K1UC DEMONSTRATION PROJECT - BETHLEHEM STI
SPARKUVS KU1NI, MARYLAND
QBS
DATE
425
07/05/91
426
07/06/91
427
07/06/91
428
07/07/91
429
07/07/91
430
07/08/91
431
07/08/91
432
07/09/91
433
07/09/91
434
07/10/91
435
07/10/91
436
07/11/91
437
07/<
-------
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-------
COAL PROPERTIES FROM DAILY COAL MIX REPORTS
KIDC DEMONSTRATION PROJECT - BETHLEHEM STEEL CORPORATION
SPARROWS POINT. MARYLAND





VOLATILE
FIXED


DBS
DATE
ROA
TURN
PLANT
MATTER
CARBON
ASH
SULFUR
531
08/27/91
1326
7-3
e
29.7
64. 1
6.2
0.78
532
Q8/2B/91
1326
11-7
6
29.8
64.5
5 , 7
0.79
633
08/28/91
1326
7-3
B
30.7
63.2
6 . i
0.76
534
08/29/91
1326
11-7
e
30.3
63.6
6. %
0.78
535
08/29/91
1326
7-3
8
30.5
63 2
6.3
0.77
536
08/30/91
1326
11-7
B
29.9
64. 2
5.9
0.78
b3?
08/30/91
1326
7-3
B
30-5
63. 4
6. 1
0-77
538
08/31/91
1326
11-7
B
30. 3
63. 2
6.5
O. 79
539
08/31/91
1326
7-3
B
29.7
63.5
6.8
0.79
540
09/01/91
1329
11-7
B
3Q.O
63.9
6.1
0.77
54 1
09/01/91
1329
7-3
B
30.2
63.7
6. 1
0.70
fa42
09/02/91
1329
1 1-7
B
29.9
63.6
6.5
0.76
543
09/02/91
1329
7-3
B
29.S
64.1
6. i
0.77
544
09/03/91
1329
S 1-7
B
31 .2
62 . S
G.O
0-76
545
09/03/91
1329
7-3
B
30.7
63.0
6.3
0.73
546
09/04/91
1329
11-7
B
31 .0
63. 1
5.9
0.77
547
09/04/91
1329
7-3
B
3C.2
03.6
6 . 2
0.80
548
• 09/05/91
1329
11-7
B
29.3
63. 9
6 . B
0.83
549
09/05/91
1329
7 3
B
30.3
63.6
6. 1
0.80
550
09/06/91
1329
11-7
B
29.2
64.5
6 , 3
0.76
551
09/06/91
1329
7-3
B
30.5
60.2
9.3
O. 78
552
03/07/91
1320
11-7
B
30.B
63. 1
6 . 1
0.75
553
09/07/91
1329
7-3
D
30.2
63.8
6.0
0.73
554
09/08/91
1331
11-7
B
29. 1
65.0
5.9
0.81
555
09/08/91
(33 t
7-3
B
30. 1
63.4
6.5
0. 78
556
09/09/91
1331
11-7
B
29.9
64.4
5.7
0.79
557
09/09/91
1331
7-3
B
30.4
64 .0
5.6
0,78
559
09/10/91
1331
11 -7
B
29.7
64-8
5.5
0 . 79
5b9
09/10/91
1331
7-3
B
30.8
62.9
6.3
0.79
560
09/11/91
1331
i 1-7
B
30. 1
64 .0
5.9
O. 76
561
09/11/91
1331
7- ?j
B
30.0
64.3
5.7
O. 77
562
09/12/91
1331
14-7
B
29.8
64.0
6.2
0.78
563
09/12/91
1331
7-3
B
29.9
64 .0
6 . 1
0.74
564
09/13/91
1331
11-7
B
26. 1
65.4
6.5
0.78
565
09/13/91
1331
7-3
B
26.5
65.0
6.5
O. 77
566
09/14/91
1331
11-7
B
30.7
62 .4
6.9
0.78
567
09/14/91
1331
7-3
B
31.4
62.5
6. 1
0.77
56B
09/15/9 1
1333
1 1-7
B
29.9
63.9
6.2
O. 80
569
09/15/91
1333
7-3
6
30.0
63.9
5- 1
0.80
570
09/16/91
1333
11-7
B
29.6
64 .5
5.9
0-79
hf 1
09/16/9 1
(333
7-3
6
29.6
64.3
ti. 1
O.V9
572
09/17/m

1 i -7
n
3D. 5
63.6
5.9
0.75
573
09/17/91
1333
7-3
B
30.2
63.9
5.9
0.76
574
09/18/91
1333
11-7
B
28.6
65.4
6.0
0.80
575
09/18/91
1333
7-3
B
29.3
64 .4
6.3
0.81
576
09/19/91
1333
11-7
B
29. 1
64,7
6 ; 2
0.79
577
09/19/91
1333
7-3
B
29.6
64.5
5.9
0.80
576
09/20/91
1333
1 1-7
B
28.2
65.6
6.2
0.78
579
09/20/91
1333
7-3
B
28.4
65.3
6.3
0.76
580
09/21/91
1333
11-7
B
28.5
65.5
6.0
0.79
581
09/21/91
1333
7-3
B
28. 9
64 .4
G. 7
0.75
562
09/22/91
1335
11-7
B
28.9
65.2
5.9
0.77
583
09/22/91
1335
7-3
B
29.8
63 .9
6.3
0.80
16:22 Tuesday, March 31, 1992 I!

POT PASSING
FS*
100 MESH
7.5
14.8
7.5
15.0
7.5
14.6
7.5
17.1
7.5
15. 1
7.0
15.6
7.5
, 15. 1
8.0
11 .8
7.5
16.6
7.5
13.6
7.5
15.5
7.5
14. 1
7.5
16. 1
8.0
12. B
7.5
13.9
7.5
14.4
7.5
15.8
7.5
15.2
7.5
14.6
7.5
15.4
7.5
15.6
7.5
12 .0
7.5
13. 1
8.0
14.6
7 . 5
15.0
7.5
16.0
7.5
15.2
7.5
11.2
7.5
16.0
7.5
14.0
7.5
14 . 9
7.5
13.3
7.0
14.2
7.5
14.6
7.5
15. 1
S.O
13.9
7.5
11.6
7.5
16.4
7.5
15.6
7.5
13. 1
7.5
15. 1
7.5
14 . 3
7.5
15.1
a.o
15.6
7.5
16.4
8.0
17.4
7.5 •
13.9
7.5
17.9
8.0
14.8
7.5
15.2
7.5
14.8
7.5
15.6
8.0
14.6

-------
COAL PROPERTIES FROM DAILY COAL MIX REPORTS
KIDC DEMONSTRATION PROJECT - BETHLEHEM STEEL CORPORATION
SPARROWS POINT. MARYLAND
16:22 Tuesday, March 31. 1992 12





VOLATILE
FIXED



PCT PASSING
OBS
DATE
RQA
TURN
PLANT -
MATTER
CARBON
ASH
SULFUR
FSI
100 MESH
584
09/23/91
1335
11-7
B
30.3
63.3
6 .4
O.B1
7,5
14 6
btib
09/23/91
1335
7-3
6
31.3
62.4
6.3
0.79
7.5
14.8
586
09/24/91
1335
1 1-7
B
29 .6
63.8
6 .6
0.75
7 ,5
14.6
587
09/24/91
1335
7-3
B
30.6
63.4
SO
0 , 74
8.0
13.9
58B
09/25/91
1335
1 1-7
B
31 .6
62.5
5.9
0,74
8.0
14.6
589
09/25/91
1335
7-3
B
30. a
63.3
5.9
0,74
8.0
15.3
590
09/26/91
1335
11-7
B
25 .3
64.0
6,7
0.79
7.0
15.6
59 1
09/26/91
1335
7-3
B
31 .0
62 .4
6.6
0 . 76
7 , 5
15.2
592
09/27/91
1335
11-7
B
30.3
62.8
6.9
0.74
7.5
15.2
593
09/27/91
1335
7-3
B
31.1
62.8
6. 1
0.76
7.5
15.0
594
<>9/28/91
1335
11-7
e
30.8
62.9
6.3
0.76
7 . 5
14 .O
595
09/28/91
1335
7-3
B
29.3
64 1
6.6
0.79
8.0
15.0
596
09/29/91
1337
11-7
B
28.0
65. 1
6.9
0.83
8.0
13.4
597
09/29/91
1337
7-3
B
28.3
65.2
6.5
0.85
6.0
14.6
596
00/30/91
1337
1 1-7
B
28.6
64 .9
6.9
0.77
7.5
12.6
599
09/30/91
1337
7-3
B
28.2
€5.2
6.6
0.82
8.0
14.7
600
10/01/91
1337
1 1 -7
B
30.0
63.e
6 . 2
0. 78
7 . 5
16.8
601
10/01/91
1337
7-3
B
29.9
63.8
6.3
0.79
8.0
15.2
602
10/02/91
1337
1 1 -7
B
30.0
63.9
6. 1
0.83
8 >0
14.3
603
10/02/91
1337
7-3
B
30.9
62.9
6.2
0.82
7.5
12. 1
	-v S04
10/03/91
1337
11-7
B
28.3
65.6
6. 1
0.82
8.0
17.6

605
10/03/91
1 337
7-3
B
29 .O
64 .9
6. 1
0.82
7.5
16.4

606
10/04/91
1 337
11 -7
B
29. 1
64.5
6.4
0.79
7.5
16.5
Jf
607
10/04/91
1337
7-3
B
29.7
64.0
6.3
0.82
B.O
17.2

608
10/05/91
1337
11-7
6
29.4
64. 2
6.4
0.81
8.0
16.4
!"0
609
10/05/91
1337
7-3
B
30.2
63.3
6.5
0.81
8.0
17. 1
>
610
10/06/91
1339
1 1 -7
B
29.5
64. 1
6.4
0.80
7.5
15.1

61 1
10/06/91
1339
7-3
B
28 . 2
65.5
6.2
0.76
7.5
18 .8

612
10/07/91
1339
11-7
B
30. 1
63.5
6.4
o.ai
7.5
17.2

613
10/07/91
1339
7-3
B
29.4
64.4
6.2
0.83
7.0
16.8
614
10/08/91
1339
11-7
B
29.8
63.5
6.7
0.79
8.0
17.6
G15
10/08/91
1339
7-3
B
30.8
62.9
6.3
0.76
7.5
18. 1
616
10/09/91
1339
1 1 7
B
29.2
64 .4
6.4
0.79
7.5
13.8
£ 17
10/09/91
1339
7-3
B
29 . 5
64 1
6.4
0.79
7.5
13.2
£18
10/10/91
1339
11-7
B
30.4
63.6
6 .O
0.74
8.0
13.5
619
10/10/91
1339
7 3
B
30.3
63. 8
5.9
O. 76
8.0
17.6
620
10/11/91
1339
11-7
B
30.9
63.4
5.7
0.74
7 . S
14 .6
621
10/11/91
1339
7-3
B
31 .6
62.5
5.9
0. 73
7.5
14.8
622
10/12/91
1339
1 1 -7
B
30.2
63.5
6 .3
0.79
7 5
15.3
623
10/12/9 I
1339
7-3
B
29 .1
63.7
6 .6
o.ao
8.0
14.8
62-4
10/13/91
13-44
1 1 7
b
30.4
64 .O
5.6
0. 78
7 . 5
17.3
62b
10/13/91
1344
7-3
B
30 B
63 6
5.6
0. 76
7 5
15 ,S
626
10/14/91
1344
11-7
B
29 .8
63 .6
6.6
0.78
7,5
15.8
627
10/14/91
1344
7-3
B
29.6
63.7
6.7
0. BO
7.5
14.4
€26
10/16/91
1344
7-3
B
28 .2
64 .9
6.9
G . BO
fl 0
13.2
629
10/10/91
134 4
11-7
B
2S .9
65 .2
5.9
0-B1
8,0
15.6
630
10/16/91
1344
7-3
U
2S .9
64 .9
6.2
0,81
8.0
15.9
631
10/17/91
134 4
1 1-7
B
30.6
63 4
6.0
0.77
7 . 5
14.8
632
10/17/91
1344
7-3
B
31 .3
62.7
6.0
0.78
8.0
14 .b
633
tO/18/91
1344
1 1-7
B
ao 7
63 . 1
6.2
0. 76
8.0
15.4
634
10/18/9 J
1344
7-3
B
29 .7
64 0
6.3
0.75
8.0
14 .8
635
10/19/91
134 4
11-7
B
29. 1
64.6
6.3
0.83
B.O
15. 1
636
10/19/9 1
1344
7-3
B
3 1.2
62.5
6.3
0.77
7 .5
15.4

-------
COAL PROPERTIES FROM DAILV CQAL MIX REPORTS
KIDC DEMONSTRATION PROJECT - BETHLEHEM STEEL CORPORA!1 OH
SPARROWS POINT, MARYLAND





VOLATILE
FIXED


OBS
DATE
ROA
TURN
PLANT
MATTER
CARBON
ASH
SULFUR
637
10/20/91
1346
1 1-7
B
29.9
64 . 1
6.0
0.79
638
10/20/91
1346
7-3
B
29.3
64.6
6. 1
0.79
639
10/21/91
1346
1 1 -7
0
30.2
63.3
6.5
0.80
640
10/21/91
1346
7-3
B
30.3
€3. 1
6.6
0.83
641
10/22/91
1346
11-7
B
28.4
64.9
6.7
0.84
642
10/22/91
1346
7-3
6
28. 8
64 8
6.4
O. 79
643
10/23/91
1346
11-7
8
27. 1
66.9
6.0
0.80
644
10/23/91
1346
7-3
B
27.4
66.3
6.3
0.79
645
10/24/91
1346
1 1-7
8
28.9
64.7
6.4
0-76
646
10/24/91
1346
7 3
B
30.4
63.2
6.3
0.74
647
10/25/91
1346
11-7
B
28.6
65.0
6.4
0.83
646
10/25/91
1346
7-3
B
29.9
63.8
6.3
0.75
649
10/26/91
1346
11-7
B
28. 1
65.9
6.0
0.78
650
10/26/91
1346
7-3
B
27.6
66.3
6.1
0.80
651
10/27/91
1348
1 1-7
B
30.6
62 .8
6.6
0.81
652
10/27/91
1348
7-3
B
30.5
63.5
6.0
0.79
6^3
10/28/91
1348
1 1 -7
B
28.6
65.3
6. 1
0.8 1
654
10/28/91
1348
7-3
B
30. 1
63.5
6.4
O. 78
655
10/29/91
1348
11-7
B
30.4
63.3
6.3
0. 78
€56
IO/29/9 i
1348
7-3
B
30.0
63.9
6. 1
0.80
657
10/30/91
1346
11-7
B
29.9
63.9
6.2
0.79
658
10/30/91
1348
7-3
B
29.4
64.5
6.1
0.78
659
10/31/91
1348
11-7
B
30.2
63.7
6.1
O. 76
660
10/31/91
1348
7-3
B
30.0
63.5
6.5
0.79
66
11/01/91
1348
11-7
B
27.8
65.8
6.4
O. BO
662
11/01/91
1348
7-3
B
29.8
64.8
6.4
O. 8 1
663
11/02/91
1348
11-7
B
26.7
64.9
6.4
0.79
664
11/02/91
1348
7-3
B
29. 9
63.7
6.4
O. 76
665
11/03/91
1350
11-7
B
29.6
63.7
6.7
0.77
6C£
11/03/91
1350
7-3
B
29.7
63.7
6.6
O. BO
667
11/04/91
1350
1 1-7
a
29.9
63.9
€.2
0.79
668
11/04/91
1 3 50
7-3
B
30.5
63.2
6.3
O. 78
669
11/05/91
1350
1 1 -7
B
29.8
64 .2
6.0
0.78
070
11/05/91
1350
7 3
B
30. 9
63 .2
6.0
0.79
671
11/06/91
1350
1 1 -7
B
30. 1
63.8
6. 1
0.75
672
11/06/91
1350
7-3
B
29.6
64.3
6. 1
0.78
673
1l/OV/91
13 bO
1 1 -7
fcJ
31.0
62 .9
6. 1
O. 76
674 '
11/07/91
1350
7-3
B
30.2
63 . 7
6 . 1
O. 76
675
11/08/91
1350
1 1-7
B
30. 1
63.5
6.4
0.78
€76
11/08/91
1350
7-3
B
30. t
63 . 7
6.2
0-78
677
t1/09/91
1350
11-7
B
31 .2
62 .7
6. 1
O. 75
676
11/09/91
1 350
7-3
B
30.5
63.4
€ . 1
O. 77
679
11/10/91
1352
11-7
B
33.0
61 .0
€.0
O. 76
6 DO
11/10/91
1352
7-3
B
31.5
62. 1
6.4
Q-.76
681
11/11/91
1352
1 1 -7
B
32.3
61 .6
6. 1
0.74
682
11/11/91
1352
7-3
8
32 . 4
61.2
€.4
O. 76
683
11/12/91
1352
117
B
29.9
63.4
6.7
0.77
604
11/12/91
1352
7-3
B
29 . 5
64 . 4
6. 1
O. 78
685
11/13/91
1352
11-7
B
31 .6
62.4
6.0
0.77
636
11/13/91
1352
7-3
B
30. 7
63. 1
6.2
0.77
68/
11/14/91
1352
1 1-7
B
29. 4
64 ,6
6.0
0.77
688
11/14/91
1352
7-3
B
29.0
65.0
6.0
0.75
689
11/15/91
1352
11-7
B
31 .6
62. 3
6 - 1
0.75
16:22 Tuesday. March 31. 1992 13
PCT PASSING
FSI
100 MESH
7.5
14.7
7.5
16.3
7 .5
17 . 3
7 .5
16.5
7.5

7 .0

7 .b
18.0
7.5
17 . 2
8.0
15.5
7 .
13.2
7.Si
16.7
7 .5
17.4
7.5
14. t
8.0
13. 1
8.0
14,5
7.5
14.7
7.5
12.0
7.5
13.3
7.0
15. 1
7.5
14.4
7.5
15.3
8.0
14.6
7.5
14.5
7.5
15.2
8.0
14. 1
8.0
15.2
7.5
15.0
8.0
16.9
7.5
16.0
7.5
16.6
8.0
16.9
7.5
15.2
8.0
15. 1
7.5
15 , 8
8.0
16 .0
8.0
15 , 7
8.0
14.9
8.0
14.4
7.5
14.4
8.0
13. B
7.5
15.6
7 .5
15 . 1
7 , 5
13.6
7.5
12 . I
8.0
12.4
8.0
12.3
8.0
13. 1
8.0
12.6
8.0
12.5
7.5
13.4
8.0
14 . 1
8,0
17.6
8.0
12 .8

-------
COAL PROPERTIES FROM DAILY COAL MIX REPORTS
KIDC DEMONSTRATION PROJECT - BETHLEHEM STEEL CORPORATION
SPARROWS POINT. MARYLAND
16:22 Tuesday, March 31, 1992 14
VOLATILE FIXED	PCT PASSING
OBS
DATE
BOA
TURN
PLANT
matter
CARBON
ASH
SULFUR
FSI
100 MESH
690
1 1/15/91
1352
7-3
B
29.4
64 4
6.2
o.eo
B.O
13.9
691
11/16/91
1352
11-7
B
30.7
63.0
6.3
0.74
7.5
14 . 1
692
11/16/91
1352
7-3
B
29.9
63.9
6.2
0.7S
7.5
15.2
693
t 1/17/91
1354
11-7
B
31 1
62.9
6.0
O. 74
tt.O
16 . 1
694
1 1/17/91
1354
7-3
B
30.6
63.4
6.0
0.75
B.O
13.8
695
1 1/18/91
1354
\ 1-7
B
31.7
62 2
G. 1
0.75
7.5
13.9
696
11/18/9 1
1354
7-3
B
30. 8
63 2
6.0
0.75
7.0
16.9
697
11/19/91
1354
11-7
B
29 5
64 3
6.2
O. 76
8.0
14 .9
698
11/19/91
1354
7-3
B
30.2
63.8
6.0
0.75
7.5
14.6
699
11/20/91
1354
1 1-7
B
29 .O
65.0
0 0
O , 75
0.0
15.6
700
11/20/91
1354
7-3
B
30.0
64.0
6.0
0.75
6 .O
15.0
701
11/21/91
1354
11-7
B
30.6
63.0
6.4
0.76
8.0
15.6
702
1 1/21/91
1354
7-3
B
30. 2
63.a
6.3
O 74
so
16.0
703
11/22/91
1354
11-7
B
30.0
64.0
6.0
0.77
a.o
16.2
704
11/22/91
1354
7-3
B
30 6
63. 1
6.3
0.77
7 .5
15.9
705
1 1/23/91
1354
1 1-7
B
30. 2
63.7
6. 1
0. 77
7.5
14. 3
706
1 1/23/91
1 354
7-3
B
31.0
62.7
6.3
0.75
7.5
14.7
• ro
-so I

-------
COAL PROPERTIES FROM QUALITY COAL HANDLING REPORTS
KIDC DEMONSTRATION PROJECT - BETHLEHEM STEEL CORPORATION
SPARROWS POINT, MARYLAND
16:22 Tuesday, March 31, 1992
15


BULK
PULV.
%
OBS
DATE
DENSITY
% -1/6"
H20
1
12/01/90
47.96
78.93
6.82
2
12/02/90
47.95
76.91
6 .60
3
12/03/90
47.94
76 68
6.87
4
12/04/90
4®.07
79.00
7.14
5
12/05/90
47 .97
78.67
7. 12
6
12/06/90
47.97
78.88
7.08
7
12/07/90
47.99
76.85
7 .07
a
I2/O8/90
4&.03
78.67
6.85
9
12/09/90
48. 10
78.92
7 . 13
1Q
12/10/90
4fl.07
78.71
6.79
11
12/11/90
47 .96
76 .96
7.35
12
12/12/90
47 . SB
78.83
7.07
13
12/13/90
47.99
78.99
7. 17
14
12/14/90
48.06
79.00
6.65
15
12/15/90
48.00
78.9!
€ .85
16
12/16/30
46.03
76.77
7 .20
17
12/17/90
46. 10
79.15
6.78
18
12/16/90
48.06
78.64
7.34
19
12/19/90
4a.Ob
78.84
7 .55
20
12/20/90
47.9a
78.67
7. 15
2 1
12/21/90
4a.01
78.88
7 .46
22
12/22/90
48 .01
78 . BO
7 .60
23
12/23/90
47.99
78.95
7.42
24
12/24/90
47 .91
78 . 74
7 .44
25
12/25/90
48. OS
78 .85
7.35
26
12/26/90
4B.09
7B.74
7.65
27
12/27/90
47.08
78.72
7.65
28
12/28/90
47.95
76.88
6. 14
29
12/29/90
47.94
78.90
8.75
30
12/30/90
47.90
78 .54
8.35
31
12/31/90
47.97
78.73
7 .93
32
01/01/91
47 .91
78.82
7.98
33
01/02/91
47 .91
78.75
7 .98
34
01/03/91
47.88
78.85
7 .84
35
01/04/91
47.92
78.72
7.52
36
01/05/91
47.91
79. 13
7 .35
37
01/06/91
47.67
79. 17
7.34
36
01/07/91
47.96
76.85
9.29
39
01/08/91
47.91
78 .6b
8 .50
40
01/09/91
47 .89
78.58
7.84
4 1
01/10/9 1
47 .93
78 .65
7 .64
42
01/11/91
47.98
78 .66
8 . 12
43
0 J / 12/91
4 7.95
78.81
9. 16
44
01/13/91
47 .99
78.58
a.35
45
01/14/91
48.05
78 .59
7.70
46
01/15/91
48.38
78.72
8.55
47
01/16/91
47.97
70.59
8.73
48
01/17/91
48.00
78.54
8.38
49
01/18/91
47,90
78.62
8.63
50
01/19/91
47.91
78.60
7.67
51
01/20/91
47.91
79. 15
7 .83
52
01/21/91
47.92
78.73
7.42
53
01/22/91
48.04
78.94
a. 70

-------
LUAL PRUPERTICS FROM QUALITY CUAL HANDLING REPORTS
KlDC DEMONSTRATION PROJECT BETHLEHEM STEEL CORPORATION
SPARROWS POINT, MARYLAND
16:22 Tuesday, March 31, 1992 16


BULK
PliLV.
%
OBS
DATE
DENSITY
% -1/8"
H20
54
01/23/9*
47.94
79.80
7 .77
55
O1/24/91
48 .00
79.09
7 ,88
56
01/25/91
47 .98
78 .95
6.94
57
01/26/9!
48 06
79. 12
7 .43
58
01/27/91
47.86
78.67
7.4 1
59
01/28/91
47 .98
78.64
7 .30
tiO
01/29/91
48.01
7H.7 1
7 .75
61
01/30/91
47 .85
79. 14
7.74
62
01/31/91
48.08
78.67
6.93
63
02/01/91
47 .98
78.85
7 .60
64
02/02/91
48.00
78.83
7 - 13
65
02/03/9 t
47 .93
78.85
7 .25
GG
02/04/91
47.89
78.6b
7 .SB
67
02/05/91
47.89
78.33
7.25
66
02/06/91
47.88
79. 13
7.25
69
02/07/91
48 .00
78 . 79
7 .53
70
02/08/91
47.95
78.66
7 .85
7 1
02/09/91
47.96
78.62
6.90
72
02/<0/91
48.02
78 .65
7.25
73
02/1t/St
48.04
78 61
6.93
74
02/12/91
47.96
78.70
6.80
75
02/13/91
47.90
78.63
6.58
76
02/14/91
47.94
78.62
7.04
77
02/15/91
48.00
79.44
7 .00
7B
02/16/91
47.89
79.20
6.45
79
02/17/9!
48. 10
78.89
6.80
80
02/18/91
47.90
78 . 83
6 . 75
ai
02/19/91
47.96
78 .92
6.63
82
02/20/91
47.90
78.92
6.57
as
02/21/91
47 .86
79 10
6.55
84
02/22/91
47.91
79 14
6.55
B5
02/23/91
47 .92
78.74
6.55
86
02/24/91
48 .00
78.85
6.58
87
02/25/91
47 .94
79. 10
6.55
66
02/26/91
48.22
79.06
6.76
89
02/27/91
48 . 16
79.01
6 .86
90
02/28/91
47.99
78.77
7 .01
91
03/01/91
47-92
78.79
6.97
92
03/02/91
47.ao
78.61
6.65
93
03/03/91
47.87
79.22
6.97
34
03/04/Q1
47.95
78 .81
7 .53
95
03/05/91
48.03
78.74
6.90
96
03/06/91
48.01
78.58
6.95
97
03/07/91
47 .96
76.86
6 .94
96
03/08/91
48.02
78.58
6.67
99
03/09/91
48.06
78.99
7 .48
100
03/10/91
47.84
78.70
6.83
101
03/11/91
47.96
78.90
6.92
102
03/12/91
47 .93
79.04
6.97
103
03/13/91
47.96
79. 11
6.99
104
03/14/91
48 05
79. 18
6.08
105
03/15/91
47.85
79. 11
7 .64
106
03/16/91
47.83
79.04
7 .34

-------
COAL PROPERTIES FROM QUALITY COAL HANDLING REPORTS
KIDC DEMONSTRATION PROJECT - BETHLEHEM STEEL CORPORATION
SPARROWS POINT, MARYLAND
16:22 Tuesday, March 31, 1992 17


BULK
PULV.
%
OBS
DATE
DENSITY
% -1/8H
H20
107
03/17/91
47.95
78.81
7 .40
108
03/18/91
47.97
78.70
7 .95
109
03/19/91
4 7 .93
78.72
a . 82
110
03/20/91
47 .99
76.89
7 .84
111
03/21/91
47 .86
79. 18
7 .77
112
03/22/91
47 ,90
78.66
7 .60
113
03/23/91
47 .91
78 .59
8.30
1 14
03/24/91
47.92
78.62
8. 70
115
03/25/91
48 . 10
78.71
9.46
116
03/26/91
47 .82
78.56
9.23
117
03/27/91
47 .84
76.85
9.81
118
03/28/91
47 .99
78.83
9.28
I IS
03/29/91
47 .94
78.58
8.68
120
03/30/91
47.89
78 .58
B .81
121
03/31/91
47.91
_ 78.57
9.01
122
04/01/91
47 .85
79.28
8.90
823
04/O2/91
4B.01
79.70
8 .05
124
04/03/91
47.93
78.85
7 .45
125
04/04/91
47.84
79 .03
8.67
126
04/07/91
47.89
78. 6B
7,55
127
04/08/91
47.88
78 . 76
7 .24
126
04/09/91
47 .83
78 . 79
7 .69
129
04/10/91
47.81
78.68
7 .47
13G
04/11/91
4? .90
78.72
6.95
131
04/12/91
47.97
78. 69
7 . 30
132
04/13/91



133
04/14/91
48.00
78 .57
7 . 74
134
04/15/91
48. OO
78 . 57
7 .74
135
04/16/91
48.00
78 , 57
7.74
136
04/17/91
48. OO
78.57
7.74
13?
04/18/91
48.OO
78 , 57
7.74
136
04/19/91
48. OO
78.57
7.74
139
04/20/91
48.00
78 . 57
7.74
140
04/21/91
48.OO
78.57
7.74
14 1
04/22/91
48.00
78.57
7.74
142
04/23/91
48.OO
78 .57
7.74
143
04/24/91
48.OO
78.57
7 .74
144
04/25/91
48.00
78.57
7 .74
145
04/26/91
48 .OO
78 .57
7.74
146
04/27/91
48.00
78 ,57
7.74
147
Q*J/2tt/91
48.00
78 . 57
7 . 74
148
04/29/91
4B 00
78 57
7 74
149
04/30/91
48. 10
78 .65
8.09
1bO
05/01/91
47.87
78.85
8 . 08
15 1
05/02/91
47 . 94
78 6G
7 .53
152
OD/03/91
47.92
78.73
7.50
153
05/04/91
4 7. 90
78.75
7.71
154
OS/OS/91
47.82
78.70
7 .92
155
05/06/91
47.79
78.88
8.39
156
05/07/91
47 . 85
7S .84
8.37
157
Ob/Ofl/91
47 . 88
78 , 79
8 .05
158
05/09/91
47.91
78.73
B.Ot
159
05/10/91
47 .84
78.71
7 . 99

-------
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-------
COAL PROPERTIES FROM QUALITY COAL HANDLTNG REPORTS
KIDC DEMQNSTRATION PROJECT - BETHLEHEM STEEL CORPORATION
SPARROWS POINT, MARYLAND
16:22 Tuesday, March 31, 1992 19


BULK
PULV.
%
DBS
DATE
DENSITY
% - l/B"
H20
213
07/03/S1
48.53
79.06
6.54
214
07/O4/91
48 . 49
79.06
7.20
215
07/05/91
46.43
78.88
7 .07
216
07/06/91
40 .49
79.33
6. 39
217
07/07/91
48.53
79.25
6.70
210
07/08/9!
48.46
78.58
6.48
2 19
07/09/9 I
46.45
76.61
6.46
220
07/10/91
48.52
78.77
7.04
221
07/ 11/91
48. 5G
78.74
7.23
222
07/12/91
48.53
78.32
6.48
223
07/13/91
4B.50
76.09
6.B5
224
07/14/91
48.48
76.8!
6 . 84
225
07/15/91
48.52
78 64
6.99
226
07/16/91
48.47
79 .01
6.70
227
07/17/91
48 . 43
78 .68
6.69
228
07/18/91
48.58
79.3b
7 .02
229
07/19/91
4B . 46
79. 16
6.70
230
07/20/91
48 . 43
7B . 72
6.42
231
07/21/91
48.46
79. 15
6.30
232
07/22/91
48.50
79.22
6. 45
233
07/23/91
48.46
78 .99
6.65
234
07/24/91
46.49
78.65
G. 79
235
07/25/91
48.39
79. 14
7 - 63
236
07/26/91
48.38
79.34
7,72
237
07/27/91
48.57
79.27
8.25
238
07/28/91
48.46
78.60
8. 15
239
07/29/91
48.39
79. 14
7.45
240
07/30/91
48.52
79. 14
7.92
241
07/31/91
46.62
79. 11
7.60
242
08/01/91
48.55
78.71
8. 14
243
00/02/91
48. 50
78.69
a. 11
244
OB/03/91
48.56
78. 6B
6 . 98
245
08/04/91
48.51
78.59
6.58
246
08/05/91
48.51
78.58
6.53
247
06/06/91
48.53
78 . 84
6.82
248
08/07/91
48.52
78.52
6.70
249
OB/Ofl/91
48.45
78. 5 1
6.22
250
08/09/91
48 .41
78 . 58
7.85
25 1
08/10/91
48.49
79, 20
7.99
252
08/ 1 1/91
48 . 56
78 . 83
7.45
253
OB/12/91
48.42
78 . 59
6.84
254
OB/13/91
48 . 47
79 . 16
7.93
255
08/14/91
4B .63
79 . 40
6.97
256
OB/15/91
48.35
79. 15
7.71
257
08/S6/91
48.55
79. 10
7 .09
258
08/17/91
48.43
79.35
6.74
259
oe/18/91
48.56
79. 12
6.94
260
08/19/91
48.43
79.44
7.25
261
08/20/91
48.51
78.92
8. 13
262
08/21/91
48.51
79. 14
7.72
263
08/22/91
48 53
78 90
7.22
264
Ofi/23/9f
48.50
79.38
6.53
265
08/24/91
48.45
76.76
7.G1

-------
COAL PROPERTIES FROM QUALITY COAL HANDLING REPORTS
KIDC DEMONS I RATION PROJECT - BETHLEHEM STEEL CORPORATION
SPARROWS POINT, MARYLAND
16:22 Tuesday, March 31, 1992 20



BULK
PULV.
%

OBS
DATE
DENSITY
% - 1 / B "
H20

266
OB/25/91
48 . 63
78 , 70
7 . 15

267
08/26/91
48.59
79. 15
6.79

266
03/27/91
48.60
78. 8B
7.00

269
00/26/9t
48. 51
78. 76
6.63

270
08/29/9f
48 . 31
78.72
7.02

27 1
08/30/91
48.60
78.81
6.71

212
OB/31/91
48 . 56
79.03
6 32

273
09/01/9 t
48.55
78.56
6.80

274
09/02/9t
48. 56
78.92
6,73

275
O9/03/91
48. 45
78.81
6 .85

276
09/04/9i
48.49
78.59
€.75

277
09/05/91
48. 44
79 . 2 6
7. 13

278
09/06/9t
48. 41
78.74
7 50

279
09/07/9 J
48.42
79. 10
6.44

280
09/O8/91
48. 41
78.62
6.45

281
09/09/9 t
48. 51
79.05
7 . 25

282
09/10/91
48.45
78.75
7.01

233
09/11/91
48. 51
79. 14
6.70

284
09/)2/91
48. 54
78.7B
6 90
1
285
09/13/91
48.44
79.09
6.67

286
09/14/91
48.66
78.83
6.59
i
287
09/15/91
48. 53
78 .75
6.99
- !
288
09/16/91
48. 38
78.81
6.90
289
09/l7/9t
48 50
79 .00
6.63
to 1
290
09/18/91
48. 59
79.05
7.06
- ui |
29 I
09/19/91
48. 47
79.01
7.06
i
292
09/20/91
48 43
78 65
7 .67
i
293
09/21/91
48. 43
78.80
7.40
294
09/22/91
48. 39
78.75
7.79

295
09/23/9t
48 55
78.57
€.45

296
09/24/91
48.38
78.58
7.25

297
09/25/91
48 60
78 .69
6 .97

298
09/26/9t
48.36
78 70
7 .89

299
09/27/91
48. 43
78.72
7 .04

300
09/28/91
48. 43
78.98
6.89

301
09/29/91
48.41
79 . 13
7 97

302
09/30/91
48. 54
79.04
a.oe

303
10/01/91
48. 48
79, 10
7.44

304
10/02/91
48 54
78 .69
7 .50

305
10/03/91
48. 35
79.OO
7.85

306
10/04/91
48 . 4 1
78 .72
7 . 76

307
10/05/91
48.41
78.72
7.86

308
10/06/31
48. 47
78.60
7 98

309
10/07/91
48 . 50
78.75
7.70

310
10/08/91
48.42
79.00
7,65

311
10/09/91
48. 44
78.50
8 99

312
10/10/91
48 42
78.68
7 ,69

313
10/11/91
48.47
78.76
7 .64

314
10/12/91
48. 47
7B 87
a 03

315
10/13/91
48 41
78 99
a. 40

316
10/14/91
4B , 50
78.81
6. 59

317
10/15/yi
48. 51
78 . 7 2
8 42

318
10/16/91
48 51
79.23
7 ,58

-------
COAL PROPERTIES FROM QUALI I V COAL HANDLING REPORTS
KIOC DCMDMSTRATION PROJECT - BETHLEHEM STEEL CORPORATION
SPARROWS POINT. MARYLAND
16: 22 Tuesday, March 31. 1992 21


SULK
PULV .
%
06 S
DATE
DENSITY
% -1/8"
H2Q
319
10/17/91
48.44
78 66
7.71
320
10/18/91
40 . 39
78.98
86O
321
10/19/91
48. 55
78. 61
7.62
322
10/20/91
40.60
78.65
7.45
323
1Q/21/91
48.52
78 . B3
7.29
324
10/22/91
48.47
78. 69
7.77
325
10/23/91
48.50
79.01
7.94
326
10/24/91
48. 46
78 . 70
7.45
327
10/25/91
48.62
78.72
6.93
326
10/26/91
48.57
76 94
7.70
329
tO/27/91
48. 57
79 OS
7. 44
330
10/28/91
48.50
78 B6
7.15
331
10/29/91
48.52
79.06
7.09
332
10/30/91
48.64
79 11
7. 36
333
11/01/91
48.42
78 . 94
7.40
334
1 1/02/91
48.52
78. BO
6.65
335
11/03/91
48 . 47
78 76
7.21
336
11/04/91
48 . 39
79.32
6. 14
337
11/05/91
48.56
79.22
7 . 20
338
11/06/91
48 52
79.01
6.99
339
11/07/91
48.47
79. 17
7.04
340
>1/08/91
48. 47
78. 94
7 . 10
341
11/09/91
48.50
78 . 71
6.37
342
11/10/91
48.46
78 . 66
6.67
343
11/11/91
48.57
79 . 00
7. 10
344
11/(2/91
48.46
78 . 72
7.60
345
1 1/13/91
48.47
78 79
7.40
346
1 1/14/91
48.49
79 . 12
7.55
347
11/15/91
48.46
76.75
7.32
348
1 1/16/91
43.42
70 . 60
8.35
349
1 1/17/91
48.47
78.55
7 .76
350
1 1/18/91
48.48
78. 70
7.43
351
1 1/19/91
48.51
70 . 92
7 . 38
352
11/20/91
48.54
78.69
7.55
353
1 1/21/91
48.56
79. 13
7.47
354
1 1/22/91
48.49
79.07
7.62
355
1 1/23/91
48.44
70.91
8.40
356
1 1/24/91
48.52
79. 33
6.60
357
11/25/91
48 . 52
7B 69
6 .49
358
11/26/91
48.40
78.88
8.80
3b9
11/27/91
48.34
76 .60
9.20
360
11/28/91
48 37
78.76
9.21
361
11/29/91
4a. 41
78 . 70
8.61
362
11/30/91
43.63
78.50
8. 35
363
12/01/91
46.62
78 .50
9. 10
364
12/02/91
48.47
70.72
8.B5
365
12/03/91
43.55
78.60
8 . 98
366
12/04/91



f
i
t

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