NC0078158_Wasteload Allocation_19951213

NPDES WASTE LOAD ALLOCATION
PERMIT NO.: NCO078158
PERNU= NAME: O. B. G. P. Company
FACILITY NAME: Olde Beau Golf Club
Facility Status: Existing
Permit Status: Renewal
Major
Pipe No.: 001
Design Capacity:
Minor �1
0.04 MGD
Domestic (% of Flow):
Industrial (% of Flow):
100 %
1
Comments:
STREAM INDEX: 10-9-10-2
RECEIVING STREAM: an unnamed tributary to Laurel Branch
Class: C-Trout
Sub -Basin: 05-07-03
Reference USGS Quad: B 15NW (please attach)
County: Alleghany
Regional Office: Winston-Salem Regional Office
Previous Exp. Date: 12/31/95 Treatment Plant Class: H
Classification changes within three miles:
Requested by: n Susan Robson
Prepared by:
Reviewed M
D 53,SS 76
Wall i✓L —�--
Date: 10/9/95
Date: /z 8 9'J--
' Date: 3 �5
1i1� l31 ��
Modeler
Date Rec.
#
r
Drainage Area (mi ) 0. /3 Avg. Streamflow (cfs): 0.26
7Q10 (cfs) 0.079 Winter 7Q10 (cfs) o. /o 30Q2 (cfs) 6,13
Toxicity Limits: IWC % Acute/Chronic
Instream Monitoring:
Upstream y / Location
Downstream y Location
Effluent
Characteristics
Summer
Winter
BOD5 (m )
'20
30
NH3-N (mg/1)
-3
6,9
D.O. (mg/1)
n✓
TSS (mg/1)
3u
36
F. Col. (/100 ml)
Zoo
2a6
PH (SU)
6 - y
6-7
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Zg
7R
t (3//C tma
306 ��a�� w/x
30 ' G 6 �i(Ai� ,»a
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Comments: 4 26 OC,

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41de Beau Golf Clubt '��� \�''•-
NCO078158
Receiving Stream: UT to ��- =' °��;r
Laurel Branch C Trout
USGS Quad No.: B15NW =_ ��-
�\ . USGS Quad Name: Roaring Gap
County: Al leghany�;`'��
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apped, edited, and published by the Geological Stw--ey \ '�
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intro) by I ISC;C and I V;rRr;C * --

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i
A. (). EFFLUENT LIMITATIONS AND MONITORING REQUIREMENTS SUMMER (April 1 - October 31) Permit No. NCO078158
During the period beginning on the effective date of the permit and lastinguntil expiration, '
outfall(s) serial number 001. Such discharges shall be limited and monitred b the permittee as ecified below: to discharge from
Y P p o
Effluent Characterlstics
Flow
BOD, 5 day, 20°C
Total Suspended Residue
NH3 as N
Dissolved Oxygen"
Fecal Coliform (geometric mean)
Total Residual Chlorine
Temperature
Conductivity
Oil and Grease
Discharge Limitations
Monthly
0.020 MGD
20.0 mg/I
30.0 mg/l
3.0 mg/I
200.0 /100 ml
30.0 mg/l
Weekly Avg,,
Monitoring Requirements
Measurement
Sample
*Sample
Daily Max
Frequency
Type
Location
Continuous
Recorder
I or E
30.0 mg/I
2/Month
Grab
E
45.0 mg/i
2/Month
Grab
E
2/Month
Grab
E
Weekly
Grab
E, U, D
400.0 /100 ml
2/Month
Grab
E, U, D
28.0 ug/I
Daily
Grab
E
i
Weekly
Grab
E, U, D
Weekly
Grab
U, D
60.0 mg/l
2/Month
Grab
E
* Sample locations: E - Effluent, I -'Influent, U - Upstream , D - Downstream at mouth of the unnamed tributary
** The daily average dissolved oxygen effluent concentration shall not be less than 5.0 mg/l.
*** The temperature of the effluent shall be such as to not cause an increase in the temperature of the receiving stream of more than 0.5°C and
in no case cause the ambient water temperature to exceed 20°C.
The pH shall not be less than 6.0 standard units nor greater than 9.0 standard units and shall be monitored 2/month at the E, U, D by grab
sample.
There shall be no discharge of floating solids or visible foam in other than trace amounts.

A. (). EFFLUENT LIMITATIONS AND MONITORING REQUIREMENTS WINTER (November 1 - March 31) Permit No. NCO078158 ,
During the period beginning
on the effective date of the permit and lasting until expiration, the Permittee is authorized to discharge from
outfall(s) serial number 001.
Such discharges shall be limited and monitored by the permittee as specified below:
Effluent Characteristics
Discharge Llmitatlons
Monitoring
Requirements
Measurement
Sample
*Sample
Monthly Avg.Weekly Avg. Daily Max
Frequency
Type
Location
Flow
0.020 MGD
Continuous
Recorder
I or E
BOD, 5 day, 200C
30.0 mg/1 45.0 mg/1
2/Month
Grab
E
Total Suspended Residue
30.0 m g/ I 45.0 m g/ I
2/Month
Grab
E
NH3 as N
6.9 mg/1
2/Month
Grab
E
Dissolved Oxygen
Weekly
Grab
E, U, D
Fecal Coliform (geometric mean)
200.0 /100 ml 400.0 /100 ml
2/Month
Grab
E, U, D
Total Residual Chlorine
28.0 ug/I
Daily
Grab
E
Temperature
* '
Weekly
Grab
E, U, D
Conductivity
Weekly
Grab
U, D
Oil and Grease
30.0 mg/l 60.0 mg/l
2/Month
Grab
E
* Sample locations: E - Effluent, I - Influent, U - Upstream , D - Downstream at mouth of the unnamed tributary
*** The temperature of the effluent shall be such as to not cause an increase in the temperature of the receiving stream of more than 0.5°C and
in no case cause the ambient water temperature to exceed 20°C.
The pH shall not be less than 6.0 standard units nor greater than 9.0 standardi units and shall be monitored 2/month at the E, U, D by grab
sample.
There shall be no discharge of floating solids or visible foam in other than trace amounts.

GKEX88/MP
10/09/95
COMPLIANCE EVALUATION ANALYSIS REPORT
PAGE 1
• PERMIT--NC0078158
PIPE--001 REPORT PERIOD:
9209-9308
LOC ---
E
' FACILITY--O.
B.
G. P. COMPANY
DESIGN FLOW--
.0200
CLASS --
LOCATION --ROARING
GAP
REGION/COUNTY--04 ALLEGHANY
50050
00310
00530
00610
31616
50060
00300
00010
MONTH
Q/MGD
BOD
RES/TSS
NH3-N
FEC COLI
CHLORINE
DO
TEMP
LIMIT F
.0200
F 20.00
F 30.0
F 3.00
F 200.0
NOL
NOL
92/09
.0019
LESSTHAN
14.5
.30
LESSTHAN
.000
7.00
19.00
92/10
.0006
2.35
2.0
LESSTHAN
LESSTHAN
.000
7.20
12.80
LIMIT F
.0200
F 30.00
F 30.0
F 6.90
F 200.0
NOL
NOL
92/11
.0079
5.00
11.0
.30
LESSTHAN
.000
7.00
9.60
92/12
.0002
2.30
LESSTHAN
LESSTHAN
LESSTHAN
.000
7.70
4.80
93/01
.0001
1.90
3.0
.25
LESSTHAN
.000
9.50
8.00
LIMIT F
.0200
F 30.00
F 30.0
F 6.90
F 200.0
F
5.00
NOL
93/02
93/03
LIMIT F
.0200
F 20.00
F 30.0
F 3.00
F 200.0
F
5.00
NOL
93/04
LIMIT F
.0200
F 20.00
F 30.0
F 3.00
F 200.0
NOL
NOL
93/05
.0080
2.20
10.7
.40
34.0
.000
7.00
16.00
93/06
.0028
.90
3.5
.15
14.0
.000
6.80
20.00
93/07
.0015
2.90
7.7
.10
10.0
.000
6.50
22.60
93/08
.0002
1.90
5.5
.15
10.0
.000
6.30
24.80
AVERAGE
.0025
2.43
7.2
.23
17.0
.000
7.22
15.28
MAXIMUM
.0080
5.00
14.5
.40
34.0
9.50
24.80
MINIMUM
.0001
LESSTHAN
LESSTHAN
LESSTHAN
LESSTHAN
.000
6.30
4.80
UNIT
MGD
MG/L
MG/L
MG/L
#/100ML
UG/L
MG/L
DEG.0

GKEX88/MP 10/09/95
COMPLIANCE EVALUATION ANALYSIS REPORT PAGE 2
PERMIT--NC0078158 PIPE--001 REPORT PERIOD: 9209-9308 LOC---E
FACILITY--O. B. G. P. COMPANY DESIGN FLOW-- .0200 CLASS --
LOCATION --ROARING GAP REGION/COUNTY--04 ALLEGHANY
00400 00556
MONTH PH OIL-GRSE
LIMIT 9.0 6.0 F 30.000
92/09 7.4-6.9 LESSTHAN
92/10 7.4-6.9 26.300
LIMIT 9.0 6.0 F 30.000
92/11 7.1-7.0 3.550
92/12 7.1-6.9 4.000
93/01 7.1-6.9 LESSTHAN
LIMIT 9.0 6.0 F 30.000
93/02
93/03
LIMIT 9.0 6.0 F 30.000
93/04
LIMIT 9.0 6.0 F 30.000
93/05 8.2-8.1 1.000
93/06 8.0-7.8 LESSTHAN
93/07 7.8-6.4 1.300
93/08 6.6-6.3 1.350
AVERAGE 6.250
MAXIMUM 8.200 26.300
MINIMUM 6.300 1.000
UNIT SU MG/L

•GKEX88/MP
10/09/95
•
COMPLIANCE EVALUATION ANALYSIS REPORT
PAGE 1
PERMIT--NC0078158
PIPE--001 REPORT PERIOD:
9309-9408
LOC---E
' FACILITY--O. B. G.
P. COMPANY
DESIGN FLOW--
.0200
CLASS --
LOCATION --ROARING
GAP
REGION/COUNTY--04 ALLEGHANY
50050
00310
00530
00610
31616
50060
00300
00010
MONTH
Q/MGD
BOD
RES/TSS
NH3-N
FEC COLI
CHLORINE
DO
TEMP
LIMIT F
.0200 F
20.00
F 30.0
F 3.00
F 200.0
NOL
NOL
93/09
.0020
1.20
5.0
.10
LESSTHAN
.000
6.50
18.60
93/10
.0013
3.92
5.0
LESSTHAN
LESSTHAN
9.00
15.00
LIMIT F
.0200 F
30.00
F 30.0
F 6.90
F 200.0
NOL
NOL
93/11
.0008
6.53
13.0
LESSTHAN
3.8
.000
9.90
8.00
93/12
.0016
3.80
8.5
LESSTHAN
3.8
.000
12.10
4.00
LIMIT F
.0200 F
30.00
F 30.0
F 6.90
F 200.0
F
5.00
NOL
94/01
94/02
LIMIT F
.0200 F
30.00
F 30.0
F 6.90
F 200.0
NOL
NOL
94/03
.0007
4.30
12.0
LESSTHAN
LESSTHAN
.000
11.10
6.00
LIMIT F
.0200 F
20.00
F 30.0
F 3.00
F 200.0
NOL
NOL
94/04
.0017
7.80
8.0
LESSTHAN
2.2
.000
8.90
15.00
94/05
.0024
8.87
9.0
LESSTHAN
32.0
13.000
7.60
14.00
94/06
.0019
17.70
22.0
.79
46.0
6.60
21.00
94/07
.0026
4.16
LESSTHAN
LESSTHAN
LESSTHAN
6.20
22.00
94/08
.0032
5.30
12.0
LESSTHAN
LESSTHAN
5.40
21.00
AVERAGE
.0018
6.35
10.5
.44
17.5
2.166
8.33
14.46
MAXIMUM
.0032
17.70
22.0
.79
46.0
13.000
12.10
22.00
MINIMUM
.0007
1.20
LESSTHAN
LESSTHAN
LESSTHAN
.000
5.40
4.00
UNIT
MGD
MG/L
MG/L
MG/L
#/100ML
UG/L
MG/L
DEG.0

r r
GKEX88/MP 10/09/95
COMPLIANCE EVALUATION ANALYSIS REPORT PAGE 2
PERMIT--NC0078158 PIPE--001 REPORT PERIOD: 9309-9408 LOC---E
FACILITY--O. B. G. P. COMPANY DESIGN FLOW-- .0200 CLASS --
LOCATION --ROARING GAP REGION/COUNTY--04 ALLEGHANY
00400 00556
MONTH PH OIL-GRSE
LIMIT 9.0 6.0 F 30.000
93/09 7.2-6.7
93/10 7.2-6.5 4.600
LIMIT 9.0 6.0 F 30.000
93/11 7.6-7.1 LESSTHAN
93/12 7.1-6.3 3.660
LIMIT 9.0 6.0 F 30.000
94/01
94/02
LIMIT 9.0 6.0 F 30.000
94/03 6.8-6.5
LIMIT 9.0 6.0 F 30.000
94/04 6.7-6.1 LESSTHAN
94/05 6.9-6.8 LESSTHAN
94/06 7.1-6.0 6.700
94/07 6.9-6.6 3.300
94/08 6.2-6.2 4.700
AVERAGE 4.592
MAXIMUM 7.600 6.700
MINIMUM 6.000 3.300
UNIT SU MG/L

v •
DF93650I
SESSION READY FOR INPUTGKEX88/MP
COMPLIANCE EVALUATION ANALYSIS REPORT
PAGE 1
PERMIT--NC0078158
PIPE--001 REPORT PERIOD:
9409-9508
LOC ---
E
• FACILITY--O.
B. G.
P. COMPANY
DESIGN FLOW--
.0200
CLASS --
LOCATION --ROARING
GAP
REGION/COUNTY--04 ALLEGHANY
50050
00310
00530
00610
31616
50060
00300
00010
MONTH
Q/MGD
BOD
RES/TSS
NH3-N
FEC COLI
CHLORINE
DO
TEMP
LIMIT F
.0200 F
20.00
F 30.0
F 3.00
F 200.0
NOL
NOL
94/09
.0022
2.52
6.5
LESSTHAN
27.0
7.60
17.00
94/10
.0067
5.40
6.5
LESSTHAN
LESSTHAN
.000
7.10
12.00
LIMIT F
.0200 F
30.00
F 30.0
F 6.90
F 200.0
NOL
NOL
94/11
.0039
12.80
18.0
2.30
4.4
.000
8.50
12.00
94/12
.0037
1.22
14.0
LESSTHAN
LESSTHAN
.000
10.90
4.00
LIMIT F
.0200 F
30.00
F 30.0
F 6.90
F 200.0
F
5.00
NOL
95/01
95/02
LIMIT F
.0200 F
30.00
F 30.0
F 6.90
F 200.0
NOL
NOL
95/03
.0014
3.58
10.5
LESSTHAN
LESSTHAN
.000
11.60
7.00
LIMIT F
.0200 F
20.00
F 30.0
F 3.00
F 200.0
NOL
NOL
95/04
.0023
5.12
40.5FLESSTHAN
2.1
.000
10.10
11.00
95/05
.0043
13.40
20.0
1.08
14.0
.000
9.30
15.00
95/06
.0061
5.52
9.5
LESSTHAN
LESSTHAN
.000
9.30
18.00
95/07
.0025
3.75
LESSTHAN
LESSTHAN
LESSTHAN
.000
7.80
21.00
AVERAGE
.0036
5.92
15.6
1.69
11.8
.000
9.13
13.00
MAXIMUM
.0067
13.40
40.5
2.30
27.0
11.60
21.00
MINIMUM
.0014
1.22
LESSTHAN
LESSTHAN
LESSTHAN
.000
7.10
4.00
UNIT
MGD
MG/L
MG/L
MG/L
#/100ML
UG/L
MG/L
DEG.0

GKEX88/MP 10/09/95
COMPLIANCE EVALUATION ANALYSIS REPORT PAGE 2
PERMIT--NC0078158 PIPE--001 REPORT PERIOD: 9409-9508 LOC---E
FACILITY--O. B. G. P. COMPANY DESIGN FLOW-- .0200 CLASS --
LOCATION --ROARING GAP REGION/COUNTY--04 ALLEGHANY
00400 00556
MONTH
PH
OIL-GRSE
LIMIT
9.0 6.0
F 30.000
94/09
6.9-6.9
LESSTHAN
94/10
7.0-6.7
LESSTHAN
LIMIT
9.0 6.0
F 30.000
94/11
6.9-6.9
LESSTHAN
94/12 6.8-6.7 LESSTHAN
LIMIT 9.0 6.0 F 30.000
95/01
95/02
LIMIT 9.0 6.0 F 30.000
95/03 6.1-6.1 LESSTHAN
LIMIT 9.0 6.0 F 30.000
95/04 6.4-6.0 LESSTHAN
95/05 6.7-6.1 LESSTHAN
95/06 7.7-6.1 LESSTHAN
95/07 6.9-6.0 LESSTHAN
AVERAGE
MAXIMUM 7.700
MINIMUM 6.000
UNIT SU MG/L

RECEIVED
N.C. Dept. of EHNR
Facility Name:
NPDES No.:
Type of Waste:
Facility Status:
Permit Status:
Receiving Stream:
Stream Classification:
Subbasin:
County:
Regional Office:
Requestor:
Date of Request:
Topo Quad:
FACT SHEET FOR WASTELOAD ALLOCATION
Olde Beau Golf Club
NCO078158
Domestic - 100010
Existing
Renewal
UT Laurel Branch
C-Trout
050703
Alleghany
Winston-Salem
Robson
10/9/95
B15NW
Request #
NOV 21 1995
8362Winston-Salem
m�egional Office
Stream Characteristic:
USGS #
Date:
Drainage Area (mi2):
0.13
Summer 7Q10 (cfs):
0.078
Winter 7Q10 (cfs):
0.10
Average Flow (cfs):
0.26
30Q2 (cfs):
0.13
IWC (%):
Wasteload Allocation Summary
(approach taken, correspondence with region, EPA, etc.)
Facility requesting renewal of existing permit with no modifications. Review of compliance data
shows no problems with the discharge. Some problems reported because of high turbidity
downstream after a dam breach, but overall the facility appears to be well operated. Recommend
renewal of all existing limits.
Special Schedule Requirements and additional comments from Reviewers:
Recommended
Reviewed by
Instream Assessmer
Regional Supervisor
Pemrits & Engineeri
RETURN TO TECHNICAL SERVICES BY:

tzdatinLimi •
Wasteflow (MGD):
BODS (mgft
NH3N (mg/1):
DO (mg/1):
TSS (mg/1):
Fecal Col. (/100 ml):
pH (SU):
Residual Chlorine (µg/1):
Oil & Grease (mg/1):
Temperature (C):
CONVENTIONAL PARAMETERS
Monthly Average
Summer Winter
0.020 0.020
20
30
3
6.9
5
nr
30
30
200
200
6-9
6-9
28
28
30; 60 (da. 30; 60 (da.
monitor* monitor*
*The temperature of the effluent shall be such as not to cause an increase in the temperature of the receivi
stream of more than 0.5 C and in no case cause the ambient water temperature to exceed 20 C.
Wasteflow (MGD):
-BODS (mg/1):
NH3N (mg/l):
DO (mg/1):
TSS (mgft
Fecal Col. (1100 ml):
pH (SU):
Residual Chlorine (µg/l):
Oil & Grease (mg/1):
Temperature (C):
Monthly Average
Summer Winter WQ or EL
0.020 0.020
20
30
3
6.9
5
nr
30
30
200
200
6-9
6-9
28
28
30; 60 (da. 30; 60 (da.
max.)
max.)
monitor*
monitor*
*The temperature of the effluent shall be such as not to cause an increase in the temperature of the receivi
stream of more than 0.5 C and in no case cause the ambient water temperature to exceed 20 C.
Limits Changes Due To:
Change in 7Q10 data
Change in stream classification
Relocation of discharge
dhange in wasteflow
Other (onsite toxicity study, interaction, etc.)
Instream data
New regulations/standards/procedures
New facility information
X Parameter(s) are water quality limited. For some parameters, the available load capacity of
the immediate receiving water will be consumed. This may affect future water quality based
effluent limitations for additional dischargers within this portion of the watershed.
OR
No parameters are water quality limited, but this discharge may affect future allocations.

INSTREAM MONITORING REQUIREMENTS
Upstream Location: 50 ft upstream of discharge
Downstream Location: At the mouth of the unnamed tributary
Parameters: Dissolved Oxygen, Temperature, Fecal Coliform, Conductivity
Special instream monitoring locations or monitoring frequencies:
MISCELLANEOUS INFORMATION & SPECIAL CONDITIONS
Adgquacy. of Existing Treatment
Has the facility derlaonstrated the ability to meet the proposed new limits with existing treatment
facilities? Yes / No
If no, which parameters cannot be met?
Would a "phasing in" of the new limits be appropriate? Yes _ No
If yes, please provide a schedule (and basis for that schedule) with the regional
office recommendations:
If no, why not?
Wasteload sent to EPA? (Major) _ (Y or N)
(If yes, then attach schematic, toxics spreadsheet, copy of model, or, if not modeled, then old
assumptions that were made, and description of how it fits into basinwide plan)
Additional Information attached? (Y or N) If yes, explain with attachments.

Olde Beau Golf Club JMN
UT Laurel Branch 10/25/95
050703
Facility requesting renewal of existing permit. Extremely controversial discharger with
much debate about its initial permit issuance in 1990. Permit finally issued after meeting
(9/12/90) where officials of DEM, DEH, and other agencies determined that there were no
non- discharge alternatives. Model was run to develop limits for the NPDES permit.
Current limits are:
Summer Winter
BOD5 20 30
NH3 3 6.9
DO 5 NR
TS S 30 30
Fecal 200 200
Cl 28 28
O&G 30 30
Special Note: Previous WLA done by C. Sanderson in 10/90, gave summer/winter limits
of BOD5=30, NH3 = 3 and 6.9. Cannot find any documentation showing when the
summer BOD5 limit was reduced to 20 mg/l. These limits of BOD5=20 & 30 mg/l,
respectively, are the ones that are recorded in the the permit and compliance system but the
origin, as far as WLA documentation, is unknown. Per telecon with Allan Smith of
WSRO: 1) Qw of 40,000 GPD on his staff report was taken from previous
staff report and is incorrect. The design capacity of the plant is 20,000
GPD. 2) The reason for the change of the BOD limit to 20 mg/l, is because
of the two lakes up above the discharge, that are used during the summer
for irrigation.(?). Therefore, the summer BOD limit was reduced from 30
• mg/l to 20 mg/l.
WSRO has previously recommended denial of permit because of alternatives to discharge
. that are available. WSRO staff report reports that spray irrigation, subsurface disposal, and
wastewater reuse on the golf course are all alternatives that need to addressed. (These
concerns were addressed in the 1990 meeting) Also indicated that the quality of the effluent
has improved since Old Beau changed labs.
10/4/94 memo from the WSRO about the breach of a dam (due to heavy rainfall) @ Olde
Beau on their lower pond. This breach occurred on 8/17/94. Downstream turbidity and
suspended solids values were very high after this accident. Several complaints received
about these problems in the stream.
Recommendation: Facility appears to be well operated with no permit
exceedances.Plant seems somewhat underutilized with an average flow of
3600 GPD. In lieu of downstream turbidity problems due to the dam
breach, the effluent discharged by Old Beau doesn't appear to be causing
any problems downstream. Recommend renewal of all existing limits.

OLDE BEAU GOLF CLUB
s
UPSTREAM DOWNSTREAM
MONTH Temp DO Saturation Fecal Conductivity Temp DO Saturation Fecal Conductivity
Sep-95
14
9.2
89%
<1
254
13
9.2
87%
<1
180
Aug-95
16
9.8
99%
17
348
16
9.9
100%
17
308
Jul-95
15
9.2
91 %
16
444
15
9.3
92%
16
373
Jun-95
13
10.4
99%
16
666
14
10.5
102%
11
411
May-95
12
10.1
94%
>300
186
12
10.2
95%
81
201
Apr-95
10
10.5
93%
61
150
9
10.7
92%
7.8
294
Oct-94
11
9.4
85%
110
42
11
9.1
83%
17
61
Sep-94
14
8
78%
212
105
16
8.6
87%
17
33
Aug-94
16
6.8
69%
<2
33
19
6.5
70%
6.6
38
Jul-94
18
8.2
87%
<2
49
21
6.8
76%
<2
121
Jun-94
16
8.9
90%
84
56
19
8.2
88%
24
75
May-94
13
1 9.7
1 92%
97
1 39
11 14
1 9.3
1 90%
26
1 44
Apr-94
14
1 9.5
1 920/6
<2
111
15
1 9.4
1 93%
47
1 51
Notes ups-100 ft above discharge ar pond
dwn-200 ft below outfall
NCO078158 1 1 /9/95

1
OLDS BEAU GOLF CLUB '
UPSTREAM DOWNSTREAM
Temp DO Saturation Fecal Conductivity Temp DO Saturation Fecal Conductivity
10
9.6
85%
49.6
10
10.1
90%
4
r
16
9.6
97%
66
49.4
16
9.8
99%
35
49.6
15
8.9
88%
63
43
16
'9.1
92%
49
43
17
9.3
960/0
106
46
19
9.6
1040/6
100
46
May-93
10
9.8
87%
<14
44
10
10.7
95%
20
49
Apr-93
0
0
0%
0
0
0
0
0%
0
0
Oct-94
0
0
0%
0
0
0
0
0%
0
0
Sep-94
0
0
0%
0
0
0
0
010/0
0
0
Aug-94
0
0
0%
0
0
0
0
0%
0
0
Jul-94
0
0
0%
0
0
0
0
0%
0
0
Jun-94
0
0
0%
0
0
0
0
00/0
0
0
May-94
0
0
0%
0
0
0
0
0%
0
0
0%
0%
Apr-94
0
0
0
0
0
0
0
0
Notes ups-100 ft above discharge @ pond
dwn-200 ft below outfall
F
NCO078158
1 1 /9/95

Facility: olde beau golf
NPDES#: nc0078158
Receiving Stream: ut laurel branch
Comment(s):
Low Flow Record Station Number.
Hydrologic Area Number:
Drainage Area Low Flow Record Station:
Gave Low Flow Record Station:
s7010 Low Flow Record Station:
w7010 Low Flow Record Station:
30G2 Low Flow Record Station:
nuumur not avmmou
HA10
must be < 4W sq. miles
Drainage Area New Site:
0.13 sq. miles
MAR New Site:
2.0 cfs/miles squared
Gave per Report Equation:
0 cis
s7010 per Report Equation:
0.04 do
w7010 per Report Equation:
0.07 afs
3002 per Report Equation:
0.09 cfs
Unuseable Drainage Area
Drainage Area Ratio: #DIV/01
[ new DA / Da at gage ] #DIV/01
Weighted Ratio: #DIV/Ol
Over -ride inappropriate Site ( y ):I I
Drainage Area New Site: 0.13 miles squared
MAR New Site: 2.0 cfs/miles squared
Weighted Oave per Report Equation: #DIV/01
Weighted 0010 per Report Equation: no Input from above
Weighted w7010 per Report Equation: no input from above
Weighted 3002 per Report Equation: no input from above

0a(r cxP,r V 10 = 0' 07(4 c&
�c(5frk! (vt"���J
Nit)
� �5IU,4 Qw = 0, o fo 1,10
SUMMER
---------- MODEL RESULTS -------_------
Discharger : OLDE BEAU GOLF CLUB
Receiving Stream : UT LAUREL BRANCH
-__..-__..__-__w.._______________________________________________________
The End D.O. is 0.00 mg/1.
The End CBOD is 0.00 mg/1.
The End NBOD is 0.00 mg/1.
_-..-_......_..-..-_-_____W-_-w-____.._________-____.._-_-------_________---___-
WLA
WLA
WLA
DO Min CBOD
NBOD
DO
Waste Flow
(mg/1) Mi1epoint Reach # (mg/1)
(mg/1)
(mg/1)
(mgd)
Segment 1 6.51 0.00 1
Reach 1 45.00
9.00
5.00
0.04000
Reach 2 0.00
0.00
0.00
0.00000

*** MODEL SUMMARY DATA ***
Discharger : OLDE BEAU GOLF CLUB
Receiving Stream : UT LAUREL BRANCH
Summer 7Q10 : 0.078
Design Temperature: 23.0
Subbasin : 050703
Stream Class: C TR
Winter 7Q10 : 0.1
ILEi1GTHI
SLOPEI
VELOCITY
I DEPTHI Kd I Kd
I Ka I Ka I Kil I KN
I Ki1R I KNR
I SOD I SOD I
-------------------------------------------------------------------------------------------------------------------
I mile I
ft/mil
fps
I ft Idesign) @201
Idesign) @20° Idesign) @20°
Idesign) @20°
Idesign) @20° 1
Segment i
I I
1 0.171
I
70.001
0.160
I I I
1 0.26 1 0.59 1 0.57
I I I I
117.62 1 20.121 0.63 1 0.50
I I
1 0.63 1 0.00
I I I
1 0.00 1 0.00 1
Reach 1
-------------------------------------------------------------------------------------------------------------------
I I
I
I I I
I I i I
I I
I
Segment 1
I I
1 1.001
I
70.001
0.355
I I I
1 0.57 1 0.65 1 0.58
I I I I
147.00 1 44.771 0.63 1 0.50
I I
1 0.63 1 0.00
I I I
1 0.00 1 0.00 1
Reach 2
-----------------------------------------------------------------------------------------------------
1 1
1
1 1 1
1 1 1 1
1 1
1
I Flow (
CBOD 1
1 cfs I
mg/l I
Segment 1
Reach 1
Waste
1 0.062 1
45.000 1
Headwatersl 0.078 1
2.000 1
Tributary
( 0.000 (
2.000
* Runoff
1 0.280 1
2.000 1
Segment 1
Reach 2
Waste
1 0.000 I
0.000 1
Tributary
1 1.430 1
2.000 I
* Runoff
1 0.200 (
2.000 1
* Runoff flow is in cfs/mil e
NBOD 1 D.O. I
mg/l I mg/l I
9.000 (
5.000
1.000 1
7.720
1.000 I
7.720
1.000 I
7.720
0.000 i 0.000
1.000 ( 7.720
1.000 1 7.720

SUMMER
Seg #
Reach #
Seg Mi
D.O.
CBOD
NBOD
Flow
1
1
0.00
6.52
21.04
4.54
0.14
1
1
0.01
6.64
20.62
4.46
0.14
1
1
0.02
6.75
20.21
4.39
0.15
1
1
0.03
6.86
19.82
4.31
0.15
1
1
0.04
6.95
19.44
4.24
0.15
1
1
0.05
7.04
19.07
4.17
0.15
1
1
0.06
7.12
18.72
4.10
0.16
1
1
0.07
7.19
18.38
4.04
0.16
1
1
0.08
7.25
18.06
3.98
0.16
1
1
0.09
7.31
17.74
3.92
0.17
1
1
0.10
7.37
17.43
3.86
0.17
1
1
0.11
7.42
17.14
3.80
0.17
1
1
0.12
7.47
16.85
3.75
0.17
1
1
0.13
7.51
16.57
3.70
0.18
1
1
0.14
7.55
16.31
3.65
0.18
1
1
0.15
7.59
16.05
3.60
0.18
1
1
0.16
7.62
15.79
3.55
0.18
1
1
0.17
7.65
15.55
3.50
0.19
1
2
0.17
7.71
3.57
1.29
1.62
1
2
0.27
8.16
3.51
1.27
1.64
1
2
0.37
8.36
3.45
1.26
1.66
1
2
0.47
8.44
3.40
1.24
1.68
1
2
0.57
8.48
3.34
1.22
1.70
1
2
0.67
8.50
3.29
1.21
1.72
1
2
0.77
8.51
3.24
1.19
1.74
1
2
0.87
8.51
3.19
1.18
1.76
1
2
0.97
8.51
3.14
1.16
1.78
1
2
1.07
8.51
3.09
1.15
1.80
1
2
1.17
8.51
3.04
1.13
1.82
Seg #
Reach #
Seg Mi (
D.O.
CBOD
NBOD
Flow

SUMMER
aw s cj 7 P r3 o, ��
V006r1V0FuW11
I a P&W
5
---------- MODEL RESULTS _______---
,Dischar-ger : OLDE BEAU GOLF CLUB
Receiving Stream : UT LAUREL BRANCH
_-______________________________________..-_____________-.._____-__w____
The End D.O. is 8.51 mg/ 1 .
T'he End CBOD is 3.06 mg/1.
The End NBOD is 1.07 mg/1.
_-_________-____________________________--____________..__....w_____-____
WLA
WLA
VELA
DO Min CBOD
NBOD
DO
Taste Flow
(mg/1) Milepoint Reach # (mg/1)
(mg/1)
(mg/1)
(mgd)
Segment 1 6.07 0.00 1
Reach 1 45.00
6.75
5.00
0.04000
Reach 2 0.00
0.00
0.00
0.00000

*** MODEL SUMMARY DATA ***
Discharger
: OLDE BEAU GOLF
CLUB
Subbasin
: 050703
Receiving Stream
: UT LAUREL BRANCH
Stream Class:
C TR
Summer
7Q10
: 0.04
Minter 7Q10
: 0.07
Design
Temperature:
23.0
ILENGTHI
SLOPEI VELOCITY I DEPTHI Kd I Kd
I Ka I Ka I
KH I KN I KHR I KHR
I SOD I SOD I
-------------------------------------------------------------------------------------------------------------------
I mile I
ft/mil fps I ft Idesignl @20°
Idesignl @201 Idesignl @201 Idesign) @20°
Idesign) @20' 1
Segment 1
I I
1 0.171
I I I I
70.001 0.131 1 0.25 1 0.59 1 0.51
I I I
117.62 1 16.511
I I I
0.63 1 0.50 1 0.63 1 0.00
I I I
1 0.00 1 0.00 1
Reach i
-------------------------------------------------------------------------------------------------------------------
I I
I I I I
I I I
I I I
I
Segment 1
I I
1 1.001
I I I I
70.001 0.349 1 0.57 1 0.65 1 0.57
I I I
147.00 1 44.031
I I I
0.63 1 0.50 1 0.63 1 0.00
I I I
1 0.00 1 0.00 1
Reach 2
------------------------------------------------------------
1 1
1 1 1 1
1 1 1
-----------------------------------------
1 1 1
1
I Flow I
CBOD 1
1 cf s
I mg/ 1 I
Segment 1
Reach 1
Waste
1 0.062
( 45.000 I
Headwaters) 0.040 1
2.000 1
Tributary
I 0.000
1 2.000 I
* Runoff
i 0.280 1
2.000 i
Segment 1
Reach 2
Waste
1 0.000
I 0.000 1
Tributary
( 1.430
i 2.000
* Runoff
I 0.200
I 2.000 i
* Runoff flow is in cf s/mil e
NBOD 1 D.O. I
mg/l I mg/1 I
6.750 1
5.000
1.000 (
7.720
1.000 1
7.720
1.000 1
7.720
0.000 1 0.000
1.000 i 7.720
1.000 1 7.720

SUMMER
Seg #
Reach #
Seg Mi
D.O.
CBOD
NBOD (
Flow
1
1
0.00
6.07
28.14
4.50
0.10
1
1
0.01
6.22
27.36
4.39
0.10
1
1
0.02
6.36
26.63
4.29
0.11
1
1
0.03
6.49
25.94
4.19
0.11
1
1
0.04
6.60
25.27
4.10
0.11
1
1
0.05
6.71
24.64
4.01
0.12
1
1
0.06
6.80
24.05
3.93
0.12
1
1
0.07
6.89
23.47
3.85
0.12
1
1
0.08
6.97
22.93
3.78
0.12
1
1
0.09
7.04
22.41
3.71
0.13
1
1
0.10
7.11
21.91
3.64
0.13
1
1
0.11
7.17
21.43
3.57
0.13
1
1
0.12
7.23
20.97
3.51
0.14
1
1
0.13
7.28
20..53
3.45
0.14
1
1
0.14
7.33
20.11
3.39
0.14
1
1
0.15
7.37
19.70
3.33
0.14
1
1
0.16
7.41
19.31
3.28
0.15
1
1
0.17
7.45
18.93
3.23
0.15
1
2
0.17
7.69
3.60
1.21
1.58
1
2
0.27
8.15
3.54
1.19
1.60
1
2
0.37
8.35
3.48
1.18
1.62
1
2
0.47
8.44
3.43
1.16
1.64
1
2
0.57
8.48
3.37
1.15
1.66
1
2
0.67
8.50
3.32
1.14
1.68
1
2
0.77
8.51
3.26
1.12
1.70
1
2
0.87
8.51
3.21
1.11
1.72
1
2
0.97
8.51
3.16
1.09
1.74
1
2
1.07
8.51
3.11
1.08
1.76
1
2
1.17
8.51
3.06
1.07
1.78
Seg #
Reach #
Seg Mi
D.O. (
CBOD
NBOD
Flow

CC: Permits and Engineering
Technical Support Branch
County Health Dept.
Central Files
WSRO
To: Permits and Engineering Unit
Water Quality Section
Attention: Susan Robson
Date: October 4, 1995
NPDES STAFF REPORT AND REC! MMENDATION
County: Alleghanv
Permit No. NC00781!8
PART I - GENERAL INFORMATION
1. Facility and Address: Olde Beau Golf Club
P.O. Box 32
Roaring Gap, N.C. 28668
2. Date of Investigation: October 4, 1995
3. Report Prepared by: Allan Smith
Environmental Technician
4. Persons to Contact and Telephone Number:
Dennis Hodge/Clifford Cain - R&A Labs [phone]
Billy Satterfield - owner [phone]
5. Directions to Site: Take Hwy. 421/I-77 or Hwy. 67 to Hwy.
21 and go to Roaring Gap. Olde Beau Golf Club is located on
the right side of Hwy. 21 across from the BP Station and
High Meadows Inn and Restaurant. Go through the entrance
gate to the clubhouse. Take the road to the left before the
clubhouse and go approximately 1/10 mile and the WWTP will
be on the right.
6. Discharge Points(s), List for all discharge points:
Latitude: 360 24' 43" Longitude: 800 58' 51"
U.S.G.S. Quad No. B-15NW U.S.G.S. Quad Name Roaring Gan
7. Site size and expansion area consistent with application ?
X Yes No If No, explain:
8. Topography (relationship to flood plain included):
Mountainous; well above flood plain.
9. Location of nearest dwelling: None within 100 meters.

10. Receiving stream or affected surface waters:
UT to Laurel Branch
a. Classification: C-Trout
b. River Basin and Subbasin No.: 05 07 03
C. Describe receiving stream features and pertinent
downstream uses: Fishing, swimming, agriculture.
Part II - DESCRIPTION OF DISCHARGE AND TREATMENT WORKS
1. a. Volume of Wastewater to be permitted: 0.04 MGD
(Ultimate Design Capacity) Waste is generated from
villas, the clubhouse, and a restaurant.
b. What is the current permitted capacity of the Wasce
Water Treatment facility? 0.04 MGD
C. Actual treatment capacity of the current facility
(current design capacity)? 0.04 MGD
d. Date(s) and construction activities allowed by previous
Authorizations to Construct issued in the previous two
years. N/A
e. Please provide a description of existing or
substantially constructed wastewater treatment
facilities; Extended aeration, dual 20,000 gpd
package plants - flow splitter box, bar screen,
aeration chamber, chlorine basin, dechlorination tank.
f. Please provide a description of proposed wastewater
treatment facilities. N/A
g. Possible toxic impacts to surface waters: Unknown.
2. Residuals handling and utilization/disposal scheme:
a. Septage hauler.
3. Treatment plant classification (attach completed rating
sheet). Class II.
4. SIC Code(s): 7999
Primary 04 Secondary 02
Main Treatment Unit Code: 0 6 0 _ 7
PART III - OTHER PERTINENT INFORMATION
1. Special monitoring or limitations requests: None.
NPDES Permit Staff Report
Version 10/92
Page 2

y 2. Alternative Analysis Evaluation: Has the facility evaluated
all of the non -discharge options available. Please provide
regional perspective for each option evaluated.
Spray Irrigation: There IS adequate land for a spray
irrigation system according to previous reports and
discussions with personnel who initially inspected the
site.
.s
-mot=
Connection to Regional Sewer System: No
Subsurface: Possibility
Other disposal options: Re -use on the golf course
** These should have been thoroughly analyzed **
before a permit was originally issued.
PART IV - EVALUATION AND RECOMMENDATIONS
This Office originally requested that this Permit be denied
due to the non -discharge alternatives available to the land owner
and developer. This development continues to have environmental
impacts to the stream. The ability of the treatment plant to
produce a quality effluent has been, in the past, highly
questionable. However, since Research and Analytical Labs (R&A)
has taken over the wastewater responsibilities, the WWTP is
meeting limits.
WSRO still feels that there are viable alternatives to a
discharge permit. This Office has seen no indication of
legitimate reasons as to why the alternative methods are not
practicable (note Alternative Analysis Evaluation above). It is
strongly suggested that the new permit require an engineering
report evaluating alternatives to discharge if such a report has
not already been performed. If this report has been performed,
WSRO would like to have a copy.
WSRO recommends that the Permit be re -issued only because
the wastewater treatment system is already permitted and in
operation.
�Y ua'ell
Signature of report preparer
i
Water Quality Regional Supervisor
NPDES Permit Staff Report
Version 10/92
Odd-Je.r 4, /111'
Date le
4?5-/0a ix,
Date
Page 3

RATING SCALE FOR CLASSIFICATION OF WATER POLLUTION CONTROL SYSTEMS
• I d Name of FacilityB: Q U l
Owner or Contact Person:
Mailing Address: P-o. 20 X Vz I� oar; no, 6 &D . N. C. 28 kz ( S
County: olt Telephone: 01 0 36 3 � 3 3
Present Classification: New Facility Existing Facility_
NPDES Per. No. NC00 :1 1315 R Nondisc. Per. No.WQ Health Dept.Per No._
Rated by: Telephone:�giO 7`7l - Y600 Date:
Reviewed by: A a q Health Dept. Telephone:
C. , Regional Office Telephone: Lfj7-21- 96 00
Central Office Telephone:
ORC-c-�;,—,m CAGrade: JV- Telephone: *0 95/- 55 i7 W�r
Check Ciassification(s): _ Subsurface Spray Irrigation , Land Application
Wastewater Classification: (Circle One) I II III IV Total Points: �?>Z
SIRSURFACE CLASS FICAMON
(check all units that apply)
1`_septic tanks
2,—,_Pump tanks
3.---&Wm or Pump-dcsing systems
4,__sand filters
5. grease trap/interceptor
6.__,oNwater separators
7- - gmvhy subsurface treatment and disposal:
e. __pressure subsurface treatment and disposal:
SPRAY IRRIGATION CLASSiFirATION
(check all units that apply)
1`_preliminary treatment (definition no. 32 )
2�lag
3,__septic tanks
4`_purmp tanks
6. pumps
6.__sand fiNem
7., _.grease traplrnteroeptor
8,__oil/water separators
5,,,___disinfectlon
10,._chemical addition for nutrientlalgae control
11Lrspray Irrigation d wastewater
In addition to the above classifications, pretreatment of wastewater In excess of these components shall
be rated using the point feting system and will require an operator with an appropriate dual certification.
LAND APPLICATION/RESIDUALS CLASSIFICATION (Applies only to permit holder)
1. —Land application of biosolids. residuals or contaminated soils on a designated site.
---- --•------------------------------------------------------
WASTEWA ITE1 MEATMENT FACILITY CLASSIFICATION
The fotlowin-; ,,stems shall be assigned a Class i dassUkation. un1SSS the flow is of a significant quantity or the technology Is unusually
complex. to lire consideration by the Commission on a case -by -case basis: (Chedc It Appropriate)
1.__W- ater Separator Systems consisting only of physical separation, pumps and disposal;
2 _,_S6iA c Tank/Sand Filter Systems consisting only of septic tanks, dosing apparatus. pumps.sand filters, dssimfedion
and Mired discharge;
3,__L.agcon Systems consisting only of preliminary treatment, lagoons, pumps, disinfection. necessary chemical treatment for
algae or nutrient control, and direct discharge;
4,• Clored-ldop Recycle Systems;
S, _ Groundwaler Remedialion Systems consisting only of oll/Water separators, pumps, air -stripping, carbon adsorption, disinfection
and disposai;
6,. Aquacutture operations with discharge to sudace waters;
7. _W.s1Fr Plant sludge handling and back -wash water treatment;
8. ? 'god processing consisting of screening and disposal.
91 —. )4amiiy discharging systems. with the exception of Aerobic Treatment Units. will be classified if permitted after July 1.
or if upon Inspection by the Division, it Is found that the system Is not being adequately operated or maintained. Such
;-.a:, ns will be notified of the classification or reclassification by the Commission, In writing.

The following scale is used for gating wastewater treatment facilities: (circle appropriate points)
�
POINTS
M
r i_'
1) f�ntdustflat Pretreatmert Urfa are bdust id P.1,nestmerit PmWam (am dellnUm No..7.1)..»w«...ww_wwwwww.»Y.w
- S) DESIGN FLOW OF PLANT IN gpd (rat apptiabb b nonwntamtrnated 0 asters, sty handprnp
ladilties for
' grater purNkaum phnta, totally dosed cycle systsrrns(rree detrnRion No.11� and facilities oansisllrng only of Item
(4)(d) or bans (4)(d) and (11)(d)j
0/.- 20.00�0/� /��/�
��
' . 20.001 • i0.000 w.••....•.
_.+.».w.w..+ii ] '-/�,�
50.001 • 100.000.
w.
IN.001 • 1100.000....».» »•.lulu.
GW,001 • 11000.00y0.....•.•.......•..••w»w•.••w•......
»�.w.w.w»•w.�
w.•»ww.�
1;000.001 • 1 000.000«lulu.www.wY«lulu•...lulu.».....w..••».lulu.w•.rw.•Mw»»..�..w...w.r.•««.w.w«.._7 0
' 2.000.001 (and up) rats 1 patent adOlDr d for each zOf AW gpd ospaeiry up b a malmum of 0
Dalgn Flow (cad)
{0 j PR'E1 MINARY Uhlt S/PR0055sF.S (see definition W32)
(a) Baron eefi
w_wwwww�
W
`b Screens, f aft Somers or Commtnssing IDS" ki
••wYw,•..•»...wwwu.w..•
www.t
W
(d) Mech mical or Aerated GA Remove!
(e) Flow 0 Ic
_.•.www.1
or
f) nsournsntsd Fbw MsaararnettL ..w
g) Preasallonw..,....•••.••••••...••...•••w.w.w.w.•�
•- •--����jj
h) Moen Flow CRusti:atktn.wawa»ww............w»ww...Yw. w.....wwwww...ww«...w
(i) Grass or tail Sepamtom • Gravity ..Z
Mec_h`anical_..»
Dissolved«.........» lulu«.3
solved Air FkMkmw•ww.•»Y•»www»...ww••w».w«.w.» ww.w.w•»wwwwYwwww�c
Fred bnfnstlon.w_.... ww»w.w»rww.••.•••...•.••wwwA
rb))Septic Tank (sae defkftn Na 43)Irrthnohf Tank. •-'"»"»"""""'S
e) Primary CaardMn.w»»»»»w....w..w»...S
d) Settling Ponda or 8ett�ng Tanks for Inorganic Nontoxic Materials (stodge handling facylties for water
purification or » pia Sand. Swat sir». and otter ne�ir�irp operations except recreational activbiss such as g �
{is) lit EW DiAFf 71REATMENT
(a) Carbone aotrs Stage
(I) Aeratlon.High Puffy oxygen 101
Diffused Air System.»»ww_ww».w......»w...
Mechanical Air system (fixed, floating or rotor]
Separate sludge Reasraibn---»»--w-»--�3
{pj Tek#thg Filter T
Migh Rate— -- --- w_a
Standard Rate..
Packed Tower_ wwwwww.«www».www....
-.-.-....»»»»»--»»----»» 0
Bbbgkal Aerated Filter or Aerated dlologkal Filter
Mated Lagoons.-.»•..•.•_.••••w•w..w.ww•.•.
v) Rotating BiologicalContactors«lulu».......» ......»-..«-»....w•10
j Sand Filters •Mtemrittent bblogl
Recirculating biologicalns
Slabtllzation boo
C�.w•....•.•...wwwww•..w...••ww.•.w wwwY..,.».w......Y.•....w«.wwwwww
Ixj Singie stage system for combined carbonaceous removal of BOD and nitrogenous nmoval by
nitrification (see dellnklon No. 12)(Potnts for this itsm have to be In addtbn to Merits
(6)(a)(1) through (S)(a)(W). ..»1
trtlttztng the extended aeration process (sae dsftrntlon No3a) e
utilizing other than the extended asratton
aat) Nutrient additions to enhance 900 removal
xl) Biological Culture (esuper
(b) age
(Ij notra S Aeration • Iflgh Purity Oxygen Syslen0
Otflused Air System.www»».w.»wwwwYwww.«...
Mechanical Air System (hu4 floating or rot
Separate sludge Reaerafion.ww».»».w.»
pj Trf MbV Fitter-Mgh Rate
Standard Rate-... --- """"""'«""""""'»a
Packed Tower..»»«»«»»»»»»»-»-»«--»» 10
Biological Aerated Fitter or Aerated Biological Fitter.
N) Rotating Biological Conttaetors..••.•..••_...• w-»»....»«-~'»"'»"10
nr) Sand Fitter - Urtsnnittent bbbglcaf...Y..»»
Reclrcutating blotogksf
{p�TEATIAF1YORAADMANCWTAEATMWiLNiiS4WCCESSES
{a) Activated carbon Beds •
without carbon nlgenerativn »...... .»w».»»16
with carbon regeneatbnww.
(b) Pa red or Granular Activated Carbon Feed- S
whhout embon regenomtUm— •»�.»--»-- 16
wffh carbon regeneatbn»..............».lulu»»»»«-wwwwww»...w...w»..«.»«.«.-..�-w»»» a
aj Aistiypl..�
rg..wawa»».w.w.•.wawa..www».•»www.w.•w•..w..•wwwww•»www•»..w..».w°'."ww•» :0
d) f�enitrlflcation wwww«w•»wawa.w.»..wwwwwwwww»..»wawa».Yw.w.»•»»•�"""�'�Yw.w.w!
e) Eledrodtalple....•.w».�...«w.w».wr....»»luau..n'o.w»w»»«»»»..w.«w.»»•«w.»ww»w»»w.w»•w��w»w•w.�
f; Foam SeparatktR
Ion Exchange...»....»..»lulu»»«»«.»w.w.».lulu....».lulu.....w»».»ww»w.»..w...»lulu»»w.«»»�-tea
Land Application of Treated Effluent (toe definition No. 22b) (not applicable for sand. gravel. stone
and other stmilar mining operations) by high rate Wftatkft- »lulu
phcsopst�rarnoFierinovsl by �8btopteat Pe aews�(See Z6}»•»w.»»•«»»••.»».,..«...»..»-�w»-_v»-�» �p
t .«wYw.«.»w••.»www»•_»«'M"«wwZ
�. Pofahing Ponds • without ae►at
' with aerst--------»-»»

(1)
Post Aeration -cssude•NN.••N�N•_N•_tNMNN NNMM.MMNMMN«M•.N•N•N..M•NN•N•N.NNNN• NNNN•N•NN•V
• dff used or Mechanical. •N•..NW...MWNN.NNN.......NN...NNN..N.... ....NNNNNNN..NN2
(m)
Reverse Qamosis...NM•NNE.M�..•M.•MNNNNN.•.NN.w..•N...NN.NNNN•NWMw.•.1.►.NN.N ..... N...NNN...N.NN.NNNNN.NNNNNS
(n)
Sand or Mixed-Madia Filters
N•ers - low rate-wNN..N•N.M..N•..MMN••N••N»N•M.N.N..MN.MNN»M•»N.•M....M.N•.••.•N.••2
high rateNW.NWM•N•N.N•«.N.N.•-N.NWN.NN.•.1».N»•...s
(o)
A'/�
Treatment processes fY� removalof notal or cyanide.•NM.M•N.NN•.MN•wNN•N. W.NMN•N..•.NM.W.NNM.N•.NN..N.1 5
(pt)AfsETF
treatme'nt processes for nwwal of toxic maerials other than mow of cyanide»--N:».N».N».N.....wN...........16
())
(a)
Sludge/• Digestion Tank - Heated (anssrobic). w..NN«»N»:NNN.......NWN...N.NN».....N10
•
Aerobic
W./WN.MWWM.w•MWMMWM.WwwN•wM.WNWWNNNN.wwwNw N•M•W«N•M..N•NN.MNN•.N•N•S
/Mw�•w'•
Unheated(a��1•YMV).».»...w«.N».Ww.MwwW»w•.1wN.»..»WWN...W....NwWNN.N.».NWW». N....N......»....3
(b)
Sludge Stabilization (chemical orthenral)
(c)
Sludge Drying Bede-Gravity...-«•Mwwww•MwM.NM.wwWWwMNMMN.M.N•wWWWMN.wwWWM.N•N•MN.•.•2
Vacuum Assisted.www.N«.NwN.WNN»WwNwwww.NwWw«wwwwWwWWNN.wW...WW.NW.N..wN.N.N.S
(d)
Sludge Elutrlatbnwwww«W.MwN.WN.N..»»WwWWWwN.WNN..«N.wN.wW».•MMwWIM•MwWW».MN•WwWS
(e)
Bfudge Conditioner (chemical or thamwl) N..... ... .......6
(f)
Sludge Thickener (gravity)....N.N•NNNNMNI.N...NN.•••.•.•.NNW.•..M.•w.wN•Nw.WNMMMM...M.MMMNWMN...•N1N.....5
h)
Dissolved Air Flotation Unit [not applicable to a tn* pled as(3XI))..Ww..WWWw»wNNNwNwwN.N.».N......d
Sludge Gas Utilization (Including
I)
gas storage).. .»....._.W....N..N»...2
Sludge Folding Tank - Aerated..N.NNN...NNN...Nw.NNNNNN
l�irMr�ad M.M`•w.MWM•M�W1..N�W Www WNwW wWWw.NW WNM.N•N.N•N. ti
(,)
Sludge incinerator (not _.-•oYIng activated carbon n �1�. Ntbn).N.WMN.N•WWMWN.•NW WMWM•N. W.•.N •N•N.1 O
carbon
�0)
k) Vacuum Flker. Centrifuge, or Filter Press or other "far dswatsring devices..N»N»NNN»w»NNNNN»NN.»»»N».10
ESIEN IN ITILRATIOWIQRSPOSAL (Includng incinarawash)
•
(a)
ll•Ngoo�N.WNW-.NWWWN•i.N.Mw••.N.wM.MWWWWN..NMWNN•MNNM.NW wM.ww WN... N.N..N W..W N. N..NN•2
(b)
Land Application (surface and subsurface) (see definition 22a)
by to a land application operator or landfill operator who holds the land application permit
landfill
or lan>dfiA psmnb.NN•.wNN.W....N.N•WNN.WW....-•«.WNWWW»•N•W.NN•N«•WWWWwWWNNN•N..NN•2
(c
dicated Landfill(burial) by the parmittee of the wastiwater treatment facHlty»N•...N-N.w...•....•.NN•w..,N.»S
(g)
(a)
Chllo.`.r•.i•-nattiiofn-.M-.NN.MN..•••NwWNww«wwwWMwwwwNM••N•N.NwwwN•4.WWWWWMN«ww.•....NWN.
(b)
Dechbrfnation NN.M.M•w«.Ww..W.WN.wwW.W..N•M•M..N•W..N•M»WWNNNwW.W..N..N. N..N
(c)
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(d)
Radiation.....______
(10)
CHEMICAL ADDITION SYSTEM(S) (sea definition No. 4) (not applicable to chemical addition rated as Item (3)0).
(5Ha)(xI). (6Xa)• (6Hb). (7)ft (7)(0). (0a). (o)(b) or (0)(c) 6 points each: ,
List
•-..NN.N.-NNiNw.W.wN..•.NMW.«•W.w.N.N.NNN»wN.«.W W NN..N.•N.W...»M•».».-.5R
NNNN-N.N«NNN«NN.NN.•«NN WNN«NNNNWN•.«MNMN•NNNNMNN W N«••NN«N.N NN�RI
N«w.�AN.••.•NNNMM.N....N•.-•.•N«MN w-NNNNWMN--«..MMWM-..N»NN.MNN.•M
N-NN-w««NNM••NMN•-N-.•-N«. M«-NNNN.NN-NN-N•N«N.•N•• W-NM-NNN-M---NN•.•..NN N S
(11)
QI;SCi3J.MIEOUS tNi F10CESSSI~S
(a)
Holding Ponds. Folding Tanks or Settling Ponds for Organic or Toxic Malsdals including wastes from mining
operations containing nitrogen or phosphorus compounds In amounts sigrt2licantly greater than Is common
for domestic wastewater..».WWN..NN.w.w..N...M«.•..w•NNw...w.N.Nwww.N••....NWN.W�
(b)
Effluent Flow Equalization (rot applies bte to storage basins which are krherert In Ord application systsms)•.NN2
(c)
Stage Dladnarge (not applicable to storage basins Inherent In land application systems
(d)
PumPt;.WWN•....r•.•Wr•N.N..N.«.•••wwW.N•N•NN+w.wWN..N...WwwW«.WwN..«•NN.«...N.N.w•w.3+
(e)
Stand -By Power Supply•••...«.w.NNr....NN•NN..«.wN.N.w«caw•—w.w•N..•....—•NN..Nw•.w.w�7
(f)
Thermal Pollution Control 3
Device.W.wNwN�O..�W�»...N.ww..NN».»»»w.W,..w»wW....... w
10.•N.NN.N•N.N..Nw.Nw•N.Nw..w.•Nww•www•,�
TOTALP
CLASSIFICAM I
Chn1Nw..N•NN..•N«.WWN.N••.•.w.-N.W..••N...N..N.Nr..•NwwN. .5-25 Poi nts
Class IL. w..».WN...... N 26-50 Points
C11=11•WPoints
Gans Nw............_......w.-N..NN.-.caw.N.N-N.N...ww..W..»..N:---WUp Points
Facibties having a rating of one through four points. Inclusive, do to require a caffed operator.
Facilities having an acWaled sludge process will be assigned a minimum demon of Class lL
Facilities haft beadment processes for the removal of meta! or cyanide will be asst rod a rrninlmum motion of Clan iL
Fsclifties having treatment processes for the bbbgicai removal d phosphorus will be assigned a ff&dmm classification of Class 51.
AW4DEFWTK)P4
The following deffmions shall apply throughout this Subchapter.
(1) Activated Carbon Beds A physiealkfwmkaf method for reducing soluble organic material from wastewater affluent; The column -type beds used In this
method will have a flow we varying from two to elghl gafiars per minute per square toot and may be either upftow or downtiow carbon beds. Carbon may or
may not be regenerated on the wastewater treatment plant. ske;
(2) Aerated Lagoons. A basin In which all solids are maintained In suspension and by which bbbgial oxidation or organic maker Is reduced through art claly
accelanded transfer of oxygen on a flow -through bads;
(3) Aanklbn. A process of bringing about Intimate contact between air or high purity oxygen In a liquid by spraft. agitation or dffusbnX3a) Extended
Aeration. An activated sludge process utilizing a minimum hydraulic detention time of 10 hours.
(4) Agricubumalty managed alto. Any site on which a crop liproduced. managed. and harvested (Crop
includes grasses• grains. trees. etc);
(5) Air Strfpptng. A process by which the ammonium ion la rivet converted to dissolved ammonia (pH adjustment) with the ammonia then released to the
admo ;Phere by physical means; or other similar processes which remora petroleum products such as benzene. toluene. and xylens;
(6) Carbon Regeneration. The regeneration of exhausted carbon by the use of a furnace to provide extremely high temperatures which volatfbze and oxidize the
absorbed
(7) Carbonaceous age. A "a of wastewater treatment designed to*achleve %oco xW effluent lofts;
(8) CenMfuge. A mechanical device in which antrffugat force Is used to separate scuds from squids or to sepuats squids of d ifentrd donskus;
(9) Chemical Addition Systems- The addition of chemicals) .to wastewater at an application point for purposes d lmproving toil& remav4 pH adjustment.
of nnfty control, etc.; the capabiiity to experiment with different chemicals and different application points to achieve a specific result will be considered one
system; the capability to add chemicals) to dual units will be rated as one system; capability to add a chemical at a cWtennt application points for different
purpcsas will result in the systems being rated as separate systems;
(10) Chemical Sludge Conditioning. The addblon of as ctie:y' U compound such as Wore. tank chloride. or a polymer to wet sludge to coalesce the mass prior to
applicatlon to a dewaterfrg device; t`
(11) Closed Cycle Systems Use of holding ponds w ' tanks for containment of wastewater containing Inorganic, non -toxic rna»rlalt from "r4 t;ravel
cashed stone or other simW operaslons. uch aW.- aarry a maximum of two points regardless of pumping fadtbtas or any other appurtenances;
(12) Combined Removal of Carbonaceous D and 1! t Removal by Nbmlficatbn- A sIngle stage system required to achieve pem* effluent limbs on SW
end ammonia nitrogen within the same b icat cti:
(13) OeehlarInatfon. The peal. or completero►dudion at chrome Ill a squid by arty chemical or physical process;
(14) DwArbkatbn Process. The owmrsbn 61 rArr n to dtrogen gas;

f
f
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USGS Quad No.: B15NW
USGS Quad Name: Roaring Gap i
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Y. 501 FEET 503 57'30"THURmOND 2-3 mi- 50
ELKIN 12 Mi.
apped, edited, and published by the Geological 'z::
intmi hv I 1.1;r,'.; and 1 I.RrPMR