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LiNE Noa
1
2.
3
4
5
6
'7
8
9
' 10
11
12
13
14
15
16
17
18
19
20
21
22
23
24
25,
26
271
28
29,
30
31
32
33
34
35
36
37
38
39
`40
A l .
42
43
44
45 ^
46
47
4849.
WASTE
EOU.
SUMP
TO
E®U.
AER TK
CLAR S
CLAR#1
CLAR#1
CLAR#1
CLAR#2
CLAR#2
CLAR#2
TO
1
CLAR S
OAF
RECYCL
DAF
DAF
DAF
DIGEST
DIGEST
PRE-TK
_
PRE TK
PRE-TKII
PRE-TK
PRESS
PRESS
PRESS
PRESS
DRYERS
DRYER
DRYER
DRYER
#1
DRYER
#1
DRYER
SCR #1
SCR #1
SCR #1
SCR #1
DRYER
DRYER
#2
DRYER
#2
DRYER
#2
DRYER
#2
SCR #2
SCR #2
SCR #2
RECYC
SCR #2
TO
LAND
PROCESS MATERIAL,',
AREA
SUMP
TANK
FEED
EOU
TANK
AN
EFFLUE
FEED
FEED
FEED
EFFLUE
RECYCL
FEED
EFFLUE
RECYCL
RIVER
RECYCL
FEED
TO
AER TK
COAGUL
FLUSH
WATER
TO
SUMP
FEED
EFFLUE
COAGUL
FEED
FLUSH
WATER
'IFILTRA
FEED
FLUSH
WATER
F�LTRA
STEAM
FEED
#1
FEED
#1
AIR IN
STEAM
RODUCT
#1
VENT
VENT
MU H2O
RECYC
H2O
TO
SUMP
#
FEED
AIRIIN
STEAM
PRODUCT
VENT
VENT
MU H2O
H2O
SUMP
FILL
A
LOW, LB/HR-AV
377,103
377.103
41,711
418,813
418.813
700.290
280.116
162,733
117,383
420.174
44,099
176,875
06,832
293,458
12,047
281.411
567
24.152
34.317
2,450
2.450
60
3,109
1,252
2,868
,493
1,669 ,
2,515
150
797
399 ''
10,268
366
124
10.543
10,539
1,001
3 004
1,006
399 ;
10,268
366
124
18,543
10,539
1,001
3,004 '
1,02G
247
8
FLOW. LB/DAY-AVG
9,050.461
.050.4611.001.06110.051,52310.051,52316.806,96
,
6,722.78
.905.5189
.817.19710,084,18®
.859.384
4,225.796
,763.91
7,042.99
289.125
.753.86
13,608
579.653
23.597
58,789
8,789
15.835
74.624
30,043
a8,830
5,836
0,057
60,362
,600
19,132
,566
46,431
.779
2.965
253,037
252.935
24,034
72.103
24,136
9,566
246,437
8,779
2.965 r
253.037
252,935
24,034
72,103
24.136,
5,931
C
W, LB/DAY-MAX
16,824.07716,824.01
,162.66418,025A3818,025,A3835.514,72110,504.354
.EO3.5784'0495.53425.010,36
5A21,44G9.990,075
1,030,02414A85.6082.312.99714A85,608
241,151
1.738.9GO
1.021.328
118,950
118,950
41,050
300,000
180,259
238,439
9,421
40,344
265,401
,000
25.200
12 600
84,697
11,881
3.906
284.697
293,606
72,103
120,172
63,194
12.66�0
2841697
11,881
3,906
284,697
8,910
72 103
120,172
63,194
7.812
D
E
TEMPERATURE C
28
28
28
8
28
8
28
9
8
28
a
28
28
8
5
5
8
28
25
5
25
'�5
25
5
5,
30
130
5
0
AMB
130
5
35
35 '
25
35 .
35
20 1
AMB
130
25
35
35
25
35
35
AMB
F
PRESSURE PSIS
ATM
ATM
17
ATM
15
ATM
ATM
ATM
ATM
TM
ATM
ATM
TM
30
30
30
5
0
25
30
ATM
5
ATM
TM
5 .
ATM
0
ATM
ATM
TM
0
AMB
AMB
AMB
30
15
10
ATM i
ATM ,
20
ATM
ATM
ATM
30
15
10
ATM
G
I
yI
ii
SPECIFIC GRAVITY
1.0a0
1.000
1.000,
1.000
1.000
.999
0.999
1.0010
0.999
.999
1.000
0.999
1.000
0.998
0.998
.998
1.000
1.000
1.000
0.990
0.990
0.999
.992
1.000
0.999
.995
1.003 3
1.000
1.000
0.973
.973
.991
1.009
0.913
0.967
0.967
1.000
1.003
1.000
0.973
0.991
0.000
0.913
0.967
0.967
1.003
1.020
1.000
0.913
I
I
r
,J
COMPOSTITION, LB/HR-AVG
r
I
I
K
TOTAL SOLIDS
0
0
589
589
589
0,421'
20 168
9
20,129
30,253
9
30,194
8
50,323
2,066
8,257
16
18
1,764
1.764
38
1.801
'180
.621
91
1,531
765
765
0
0
0
0
0
765
0
0
765
0
0
0
0
0
1.531
L
DATER
9,050,4619,050,4611.000,4
10,050P3
10,050�3416,75654
6,702,61
.905,5502.797.06
10,Orj3�2
5.858.
4.195,602,.763,8
6,992.671287.059
6.705,61
13.592
579.653
23,279
7,025
7,025
15 79.7
72,822
30.043
P38,650
4,215'
0,057
60,271
17.601
,801
1411
2,200
9.011
8,910
24,034
72.103
24.136
8.80
2.411
0
2.203
9,011
8.910
24,034
72.103
24,136
4.400
PJ
AIR
44,026
244.026
,�
244,026
0
244.026
N
STEAM
3,600
,779
8.779
D
P
TOTAL
9.053.4619,050,4611.091.06110,051.52
10,051=1
GROG XG6.722.78
3.905.
.917.19
IOR841805.858.38
4.225.79G9.763.9
7.042,99
289.125
6,753.86
13.608
579,653
823,597
59.789
8,789
15,835
74,623
30,043
1�8.63fl
5 836
0 ®51
60362
3,60fl
19.132
,566
46.437
779
,965
9.011
252,935
24,034
12,103
24.136
9,56�
246 431
8.779
2.965
253.037
8.910
24 034
72 103
24,136
5 931
a
I
,
I
,
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T
U
i
AA
Ba
GC
r
.
DD
T1
III
i
COAGULANT
SUMP
PUMPS
I
I
17
NOTES
1
1. RETENTION TANK USED FOR PROCESS SPILL CONTAINMENT, AND GRADUAL
; WORKOFF
TFIRODUH THE WASTE.TREATM�'NT FACILITIES.
2
i
DAF
r
.
'
1
2. 1575 LB/DAY OF DRY EXCESS SLUDGE SOLIDS ARE GENERATED IN I
I
H 20 18
THE AERATION TANK. r r
19
1
.I
I 3. MAXIMUM
I,
P F T P CAPACITY EQUIPMENT, GENERALLY P E
RATES ARE GE ERALL DESIGN CA CI 0 EQUI
FROM BLDG.
I
, .
RETENTION
EQUALIZATION SUMP
�•
PUMP
4. EQUALIZATION TANK BLOWER CAPACITY IS 700 SCFM, I
TANK
TANK
I
i
TO
SUMP
I I
5. AERATION TANK BLOWERS AVERAGE IS 4000 SCFM. WITH A
4r
T
MA . MUM
CAPACITY 0 KI SCFM
r
BLOWER
.w:ram_—_—wwrw—.r-----_wr-----r•--- r--w.__rl_Iw•_wr_---_—_-----_—_-----_—_---_—_I
K..
..
4
61. AVERAGE
FLOWS ARE BASED ON A 24 HOUR OPERATING 'DAY.
i
UMPS
1
'
�
JF
0
I
1
DIGESTER
I
1
AERATION
i
PUMP
.'
TANK
1
BLOWER,
I
1
21
16
i COAGULANT 22
6
'
23 PRE --THICKENER
10
i
FEED
7 14
i
TANK
STEAM
PUMPS
1
�
H2O
SCREW PRESS
3
45 VENT
40 � ''-
9 12
I
24
,�
;;
r I
I
i
H 0
_
%i
31
VENT
TO I
TO I
1
1
FROM 2
DAF
?
2
�--�
ip� R
HOLD U P
SUMF� SUMP
# 3 4
CLARIFIER CLARIFIER
I
�
FROM
30
Q
� �J
TANK
/��
32
c
3�
#
39 44 48
#
TANK 1 TANK
#2
1
T 0
SCRUBBERS
28
--► p
G,
A
DRYER cn
#1 �
41 DRYER
r I
A #1 �
1
EQUALIZATION
3
,w:•
+
c
r
u H2O
f
4Q`
H2O
r
TANK
-'L
1
PUMPS
�
34 3`
42 43 n 46 �� SLUDGE 'WASTE
I
'
BLDG SUMP
H2O
�
STEAM H2O ,.��' CONTAINER
1
1
1
-
STEAM 33
t,Q�A
I
8 11
i
--------�..-------.. �..----..
.—.. a ,�_..r_...-... ._.-.-.—.. r
i
EXISTING 1 NEW
4
FLUME
EQUIPMENT I EQUIPMENT
I
s
II TU LANDFILL
13
I
1
I
SLUDGE HANDLING
1
I
I,I I ,
r
,
DRYING
RIVER
1
i
THICKENING
OEWATERING
APPROVED
1
r.o' t. Carolina
FAYETTEVIL.LE"WORKS
BOO REMOVAL
i
r�4 n' n rlt �.
Divi ,on of c.;vii,onma�ial Managemenw ASTE TRPATMENT,
I
�
y
1r ti
IL-5-1 1 .^y
pale_ ACT I �"�'��
/7 I
Permit # �L (� c3J` % �� c
OW � �+ 1989
I I
PRE—THICKNER
SCREW PRESS
I
DRYER
SCRUBBER
CONVEYORS ' � �
�
OAF
�
HOLD UP TANK
;�"
I t'��✓d°r` ,�r r P Pis-dri��± frr«,, : ti '.I
MODEI_ NO . HL,-DS-918
MODEL NO HL-R-300X3500
MODEL N0. ED-30
�"
MODEL NO 125
� CT I ZOC 18-BELT
MODEL NO.
ELEV.
MODEL N0.20
MODEL NO. 30�3
I
% III „I ,
REFERENCE DRAWINGS PR�JJECTw�.,.�_.�,�,.�-.r_..�.:�r_,�
ROTATING DRUM PRETHTCKNER
FULL ROTATING FILTER
ENVTRO-DRI STEAM OPERATED
INPINJET SCRUBBER
MODEL N,O. CTIHQC�-12 REVERSING
DISSOLVED AIR
SIDE DELIVERY SPREADER
f
� r �
WITH INTERNAL HELICAL
SCREEN SCREW PRESS.
SLUDGE DRYER
SHUTTLE BELT CONVEYOR
FLOATATION THICKENER
NONE DATE
SCALE--r_-_----_ TI�_�
NG SHOWER.
SCREW AND FACE CLEANING
SCMANUFACTURER
MANUFACTURER
MANUFACTURER
ANQREWS ►^11-fl-89
__-__- _ _
DRAWN____ - _-.�
-- —�--
MANUFACTURER
MANUFACTURER
SLY MANUFACTURING,
MA TUBER
M
MANUFACTURER
NEW HOLLAND
'/. VAUSE EQUIP. CO.
CHECKED__,-__��
��.
MANUFACTUR ER
WORKS CO. LTD.
HOILIN IRON WORKS CO. LTD.
907-5 HOGAE-DONE
THE DURIRON COMPANY
9542 DEADPAN ROAD
21945 DRAKE ROAD'
STRONGSVILLE, OHIO 441.36
``.
BUCK -EL,, INC.
564 CENTRAL AVE.
.
_ _
ENVIREX
1901 SOUTH PRAIRIE AVE.
P.O. P 0 BOX 718
J
APPROVED- 1 ��_
aEslcnt REt,EASE ;
�
HOILIN`IRON
FAYETTEVILL,F N.C.28302
�� n
�— ----�,___.. .. _r_—�.,.
—r
907 5 HOGAE —DONG
ANYAYG-SI , KYUNGKI --DO ,
ANGOLA , NEW YOUK , 14006
MURRA`+' I HILL , NEW JERSEY
1573
,
WAUKSHA , WI
53186
.
I�
jj
APPROVED -- J �C ;H�LLAN i 11 -E1-89
Ar�YANG-SI ,KYUNGKI-DO,'1.
KOREA
MAT L CONSTRUCTION
07974—
I
__
_ - _ ------ � -
7
KOREA
MAT L CONSTRUCTION
INTERNALS - 304 ST. STL.
--_---r,.�4-- �_..� _,._.---- .__ �.,.._.. ,
MAT'L CONSTRUCTION
WETTED SURFACES: CARBON STEEL
SHELL - CARBON STL.
MAT'L CONSTRUCTION
THIS,tRAWING S
NEMO RS CCU=�`?1HE
EYEEN FURNISHED BY.E.I. DU PONT DE
I NFQRMAT I ON AND KNOW—HOW , THEREON E. 1. DU PANT DE . NEMOURS & CO , INC.
' CONSTRUCTION
MAT L CO
WETTED PARTS, 304'STAINLESS
STEEL
WETTED PARTS: 304 STAINLESS
ROTATION SPEED: TO 3.8RPM
STEEL
INCLUDES STEAM JACKET.RIBBON BLENDER,
AND INTERIOR VESSEL ASSEMBLIES.
CARBONISTEELaBLACK RMA
RUBBER (COVERED 2-PLY POLYESTER
GRADE
II
MAY T E US�
THE VRITNE SSION
NOR THE DRAWING REPRODUCED WITHOUT FAYETTEVILLE WORKS
OF DU PONT..ALL REPRODUCTIONS IN
.64RPM
WHOLE OFF I P
INCLUDING FAYETTEVILLE N C
FILTER MEDIA: WIRE CLOTH 24
M ' TO 3fRPM
MESH
CARCASS BELT
r
SHALE. 8E94RR
VENC�OR'S SHOP DRAWINGS.'
FER TO THIS STAMP.
- .""�3 -2�36
1
a
ROTATION SPEED 6RP
ANTE GR H M ER DRAWING PLOTTED r I
,I .
r r
r
II r
r
rr
DEQ-CFW 00077352
D: \DGN\JGH,DGN Nov. 08, 1989 13: 38:34