ENVIRONMENTAL PROTECTION AGENCY
SURVEY FORM
PULP, PAPER, AND PAPERBOARD INDUSTRY
NON-INTEGRATED MILLS
PART I
I. MILL BACKGROUND DATA
A. Mill & Division Name: Keyes Fibre Co. Western Division
Address: 8^50 Gerber Road, Sacramento, Calif. ZIP: 95828
Telephone: 916 / fr21-?220
Corporate Affiliation (if applicable) Corporate Office Montvale, N.J.
Contacts and Title: (Use an asterisk next to the responsible personnel
completing the survey form).
*Harold J. Desmond
Paul Ball
G. F. Bean
Manager Western Manufacturing
Group Leader, Research
Manager, Process Engineering
B. Age of Mill
1. Year of initial construction 1961
2. Please give the year of initial startup and each year since 1952 in
which any major modifications or permanent shutdowns were made which
significantly affected the composition or amount of effluent from
the mill.
a. Added Paper Machine Saveall(.s)
Year(s) of
Initial Startup
None
Year(s) of. Waste
Significant Modification
or
Permanent Shutdown
b. Added New Paper'Machine(s)
-------
Mill: Keyes Fibre Co.
Location: Sacramento, Calif.
Year(s) of
Initial Startup
CHINET Molding Machine Rebuild MC-5 1975
c. paper Machine Rebuild(s) MC-2 1975
Year(s) of Waste
Significant Modification
or
Permanent Shutdown
MC-1 1976
d. Added Stock Prep. System
e. Added Broke Storage
2 ton storage chest 1977
f. Elimination of Paper Machine(s)
Other (Please List)
CHINET Molding Machines
(2) 1962
(2) 1963
(1) 1965
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(2) 1968
(2) 197^
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1975
1977
1963
1964
021S70
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- 10 -
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Mill: Keyes Fibre Co.
Location: Sacramento
II. PRODUCTION INFORMATION
G.¥.
B.
9.
Average Daily**
Air Dry
A.
3.
4.
5.
6.
7.
8.
pt.1t
Pulp Tons
. Consumed Hardwood
Bleached Kraft 23. 6 1
Unbleached Kraft
Bleached Soda
Sulfite (unbleached)
Wastepaper
Other (please list)
/Day
Softwood
2.377
49.682
8.851
Waste Kraft
Groundwood
4.968
22.383
Maximum Day Maximum Month
Air Dry Air Dry
Tons/Day Tons/Day
Hardwood" Softwood Hardwood Softwood
24.101
698*9
C
3.79
53.^21
9.461
9
27^.3
5.342
23.502
s.i 4 .
"ZMt-
6=1.5 v.
Average Daily** Maximum Day Maximum Month
Air Dry* Air Dry* Air Dry*
Tons/day Tons/day Tons/day
Products
Market Pulp
a. Pulp Bales and/or Rolls
b. Wet Lap Pulp
...... .c. Slushed Pulp
• 9. Hardwood Bleached Kraft Products'
10. Groundwood Molded Pulp Products
11. Newsprint " "
12. Groundwood Printing, Writing and Related
a. Uncoated Groundwood Printing and
Converting
b. Clay (50% or more Kaolin) Coated
Groundwood Printing and Converting
*Measured at the winder or pulp dryer.
f<3, Jl 1 - -
*-*- . -4-J
21.264
Z't.l'Ul
22.381
4s_£S? -tn-trrt-
-69Srf-
021371
Total production forthe year
**Average Daily - Total number of production days for the year
- 11 -
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Mill:
Location:
B- Products (continued)
c. Groundwood Specialties
d. Other
13. Wood Free Printing, Writing
and Related
a. Uncoated Free Sheet Printing
b. Clay (50% or more Kaolin)
Coated Free Printing
c. Uncoated Writing and Related
d. Uncoated Solid Bleached
Bristols
e. Clay (50% or more Kaolin)
Average Daily Maximum Day
Air Dry* Air Dry*
Tons/day Tons/day
Maximum Month
Air Dry*
Tons/day
Coated Solid Bleached Bristols
f. Other
14. Cotton Fiber Papers
a. Writing and Related
b. Technical
c. Other
15. Thin Papers
a. Carbonizing
b. Cigarette
c. Other
16. Packaging and Industrial Converting
a. Unbleached Kraft
Bleached Kraft
Other
b.
2.2.
2V.10!
c.
*Measured at the winder or pulp dryer.
021372
- 12 -
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Mill:
Keyes Fibre Co.
Location:
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I.-378
-------
Mill: Location:
IV. MANUFACTURING PROCESS AND INTERNAL POLLUTION CONTROL PRACTICES j
A. General
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
B. Paper Mill
182. How many paper machines does mill have?
21 Pulp Molding Machines Z/,
183. Give the number of paper machines the mill has which utilize savealls,
or similar devices, for fiber recovery.
184. Give the number of paper machines the mill has which have savealls,
or similar devices, that permit reuse of clarified water.
None
C. .Additional Information
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
021379
- 22 -
-------
Mill:
Location:
V. WATER USAGE AND EFFLUENT TREATMENT PRACTICES
Instructions for Completing Section V
Section V requests information on the mill's wastewater treatment prac-
tices. In Section VIII a general schematic of the effluent treatment
system is requested. You have the option of providing any of the data
requested in Section V on the schematic. If you do this, please in-
dicate on the question(s) involved that the data is presented on the
schematic.
A. Water Usage
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED .IN PART I.
B. Background Data
211. Indicate the method(s) of disposal of the mill wastewater.
(a) Direct
(£b) Indirect
(c) Self-contained
(d) Other (please describe)
212. Please give the year in which the following portions of the mill's
existing wastewater treatment system were started up.
a. Primary Treatment System
b* Secondary Treatment System
Year of Startup
None
None
C. Indirect Discharger (discharge to a POTW-) please provide the
following information;
215. is raw wastewater pretreated externally prior to discharge to the
POTV? (Pretreatment is considered to be any treatment device external
fron the mill production processes which is utilized prior to a pri-
mary and secondary treatment system, or prior to discharge by an
indirect discharger to a POTW.)
(a) Yes
No
021330
- 23 -
-------
Mill: . __ Location:
216. Give the treatment process used by the POTW to which your mill discharges
(Include biological and physical-chemical treatment if applicable)
C<0" Activated sludge
(b) Aerated lagoon
(c) Oxidation ditch
(d) Trickling filter
(e) None
(f) Other (indicate type) _
219. Give the preliminary treatment method used, if any.
(a) Neutralization
(b) Screening (indicate type used)
(c) Other (please describe)
221. Indicate the primary treatment method used, if applicable.
(a) Clarifier
(b) Sedimentation lagoon
(c) Mechanically cleaned sedimentation lagoon
(d) Other (please describe)
(e) Not applicable
225. Give the type of biological treatment used, if applicable.
(a) Storage oxidation basin
(b) Aerated Stabilization basin
(c) Activated sludge (air or oxygen)
(d) Other (please describe)
(e) Not applicable
021381
24
-------
Mill:
Location:
M*
251-254.
Site Conditions and Availability of Land
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
Wastewater Characteristics
Give the (1976) wastewater loads indicated below:
Indirect and Direct
Dichargers
Please Answer
(251)
Paper
Mill
Direct Discharge!
Only
Please Answer
(252)
Total Raw
Wastewater
(253)
Secondary
Treatment
System •
Effluent
(254)
Final
Effluent
c.
IV.
Flow, MGD
(1) Average Day
(2) Maximum Day
(3) Maximum Month
BOD, Ibs/day
(1) Average Day
(2) Maximum Day
(3) Maximum Month
TSS, Ibs/day
(1) Average Day
(2) Maximum Day
(3) Maximum Month
FUEL AND ENERGY .
1.9MM/gaI/day
2.1 " "
.
57.0MM/gals
60/59 Mg/L
. £U00
120/100 " "
26,930?
151/151 Mg/L
226/236
NO QUESTIONS FOR THIS SECTION ARE TO 3E ANSWERED IN PART I.
VII. PRIORITY POLLUTANTS
See Next Page
VIII. PROCESS SCHEMATICS
NO QUESTIONS FOR THIS SECTION ARE TO BE ANSWERED IN PART I.
021382
- 27 -
-------
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021385
- 31 -
-------
PART I
Question
_Number
Question
_Number
Question
_Number
Question
Number
Question
Number
Question
Number
Question
Number
021388
- 32 -
-------
ENVIRONMENTAL PROTECTION AGENCY
SURVEY FORM
PULP, PAPER, AND PAPERBOARD INDUSTRY
NON-INTEGRATED MILLS
PART II
I. MILL BACKGROUND DATA
A. Mill & Division Name: Keyes Fibre Co. Western Div.
Address: 8^50 Gerber Rd., Sacramento, CA _ ZIP: 95821
Telephone: 9l6 / ^21-?
Corporate Affiliation (if applicable) *F Co. Montvale, H.J. _
Contacts and Title: (Use an asterisk next to the responsible personnel
completing the survey form)
*H. J. Desmond __ Her. Western Mfg. _ _
C. F. Bean Hgr., Process Engineering
B. Age of Mill 15 years.
1-2. DELETED - ANSWERED IN PART I
II. PRODUCTION INFORMATION
3-23. DELETED - ANSWERED IN PART I
III. PROCESS RAW MATERIALS
24-164. DELETED - ANSWERED IN PART I
021387
- 33 -
-------
Mill: Keyes Fibre
Location: _Sacramento
IV. MANUFACTURING PROCESS AND PTERNAL POLLUTION CONTROL PRACTICES
A. general
165. Give the typical production days per year
166. High level alarms - do chemical and stock tanks have operable
high level alarms to prevent spills?
@ Yes
(b) No
(c) To the extent possible
Explanation (if needed)
167. pH or conductivity monitor of internal sewers - Do sewers have such
devices to detect or divert spills?
@ Yes
(b) No
(c) To the extent possible
Explanation (if needed)
168-181. Is the cooling water collected and reused, from the following locations:
Indicate answer using one of the following responses: (a) Yes; (b) No;
(c) Seasonal; (d) To Extent Possible; (e) Not Applicable.
168. Air Compressor Cooling Water
169. Dryer Drainage Condensate Cooling
170. Lube Oil Cooling
171. Calendar Cooling Heat Exchangers
172. Rewinder Brake Cooling
x
X
X
X
421288
- 34 -
-------
Mill: Keyes Fibre
Location:
Sacramento
(a) Yes; (b) No; (c) Seasonal; (d) To Extent Possible; (e) Not Applicable
173. Paper Machine Clutch Cooling
174. Cooling in Power Plant
175. Feed Water Pump Bearings
176. Power Plant I.D. Fan Bearings
177. Other Bearing Cooling
178. Refiner Cooling
179. Motor Control Center Cooling
180. Water Chiller
181. Air Conditioning
B. Paper Mill
'182-184. DELETED - ANSWERED IN PART I
X
X
X
x
JL
_x_
7.
X
021389
- 35 -
-------
Sacr3mento
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- 36 -
-------
Mill: Keyes Pit-re
Location: Sacramento
! I
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021391
- 37 -
-------
Mill: ' Key eg Fibre Location; Sacramento
194. Does the mill have a stock spill collection system, prior to external
treatment facilities?
(a) Yes
(b) No
fc^ Partial
195. if the answer to the preceding question is (a), describe the collection
system's function.
(a) Collected and discharged to the sewer at a controlled rate
ib^ Collected and reused in the process
(c) Other (please describe)
196. Give the frequency of waste significant grade changes; also, if
possible, give the stock quantity sewered.
500, Gals.
16^/200, mgl of pulp fines
197. is the mill central storage of white water (a) and slush broke (b) adequate
with regard to effluent discharge?
a. White Water
© Yes
(b) No
(c) To the extent possible
(Explanation, if needed)
fa. Slush Broke
(aj Yes
(b) No
(c) To the extent possible
(Explanation, if needed)
-------
Mill: Keyes Fibre
Location: Sacramento
198. Are special provisions made for spills, screen rejects, and excess
materials from coating or sizing systems?
(a) Yes
(b) No
\c) Limited
199. Does the mill employ organic solvent coating or saturating operations?
(a) Yes
£b) No
200. If yes, please give the type and quantities (Ibs/day) of organic
solvent used.
201. Give the average daily organic solvent coated or saturated paper
produced.
-0-
tons/day
021393
- 39 -
-------
Mill:
Keyes Fibre
Location:
Sacramento
^202. Please indicate effluent from the Combined papermachine facilities
as follows: (i.e., total flow from all machines)
Waste Source
Volume GPM
Suspended Solids
(if applicable)
Ibs/day
g-
h.
Centricleaner and machine
screen rejects
Couch pit, seal box, and
any other unclarified
Whitewater overflows
Thick stock spills, dumps,
washups from stock prepara-
tion area and machine
Excess clarified Whitewater
Cloudy water from vacuum
systems, or pump sealing
applications
Clear water discharges
i.e., cooling services,
condensate, other non-
process services
Other effluent sources
not included above
Total papermill effluent
none
none
None
none
none
1.000,000. c-::'' ~'
1,000,000.
2,000,OOQ, /
gal/day Periodic Wash-ups only
2,500,
2,500,
i. Is (f) discharged via process sewer or separately? (Circle answer)
NO
Additional Information
. Does the mill have a program for disposal of old electrical transformers?
(a) Yes
© No
204. please give the number of people employed at your mill. 2^0 t _
021394
-------
Mill: Keyes Fibre Location: Sacramento
V. WATER USAGE AND EFFLUENT TREATMENT PRACTICES
Instructions for Completing Section V
Section V requests information on the mill's wastewater treatment practices.
In Section VIII a general schematic of the effluent treatment system is
requested. You have the option of providing any of the data requested in
Section V on the schematic. If you do this, please indicate on the
question(s) involved that the data is presented on the schematic.
A. Water Usage
205. Indicate the source and amount of process water.
(a) Surface (i.e., river, lake or reservoir) MGD
(b) Groundwater l._0. MGD
(c) Other (please describe) MGD
206. Does the quality of the raw water limit the reuse of water in this mill?
(a) Yes - explain
|b) No
207. Indicate the source and amount of the mill's cooling water.
(a) Surface MGD
^b) Groundwater 1.0 MGD
(c) Other (please describe) MGD
208. Indicate the source and amount of the mill's boiler feed water.
(a) Surface MGD
(b} Groundwater .°°6 MGD
(c) Other (please describe) MGD
921285
-------
Mill: Keyee fibre • Location: Sacramento
209. Describe treatment used for boiler feed water conditioning.
Nalchelate #8205 liquid chelant - Polymer - antifoam
Nalco #19 catalyzed sodium sulfite type oxygen scavenger
Nalco #35**- filming/volatile amine inhibitor.
210. Give the disposal method now employed for boiler blowdown water.
Saj Sewered to treatment plant
(b) Directly discharged
(c) Directly discharged with pH adjustment
(d) Directly discharged after cooling '
(e) Other (please describe)
B. Background Data
211-212. DELETED - ANSWERED IN PART I
213. How is cooling water disposed?
(a) Separate discharge to receiving stream.
/y Combined with process waters before treatment.
(c) Combined with treated process waters.
(d) Recycled.
C. Indirect Discharger please provide the following information:
214. Nam-:-, and location of POTW which handles your wastewater.
Sacramento Regional County Sanitation District, Si aims R<3. Sacramento 28
215-216. DELETED - ANSWERED IN PART I
217. Are there specific pretreattnent requirements of limits upon pollutant
parameters imposed by the POTW system to which you discharge?
© Yes
(b) No
021386
-------
Mill: Keyes Fibre "Co. Location; Saeramento
218. If the answer to the preceding question was (a), please list the specific
pretreatment requirements or pollutant parameter limits imposed on your
mill by the POTW.
Auto-Lime Feeder to. control effluent to 7.0 pH.
219. DELETED - ANSWERED IN PART I
220. If neutralization is practiced, fill in the following.
Chemical used Lime
221. DELETED - ANSWERED IN PART I .
222. Are any chemicals or other settling aids added to the primary treatment
units?
(a) Yes
@) No
(c) To the extent necessary (intermittent)
223. Please show the wastewater streams which enter the secondary treatment
system (if applicable). NA
Process Source or Sewer No.* Flow, MGD BOD, Ib/D TSS, Ib/D
a. Design Values Average Day
Maximum 'Day
Maximum Month '
b. Primary Treatment Effluent Average Day '
Maximum Day
Maximum Month
c. Other Average Day
Maximum Day • .
Maximum Month :
*Process source or sewer number should be keyed to the mill process and
wastewater treatment schematics requested in Section VIII.
021337
- 43 -
-------
Mill: Keyeg Fibre
(a) 4-6
(b) 6-8
(c) 8-10
Location: Sacramento
225. DELETED - ANSWERED IN PART I
to the secondary
provlde
226.
of
jf current or
228. DELETED - ANSWERED IN PART I
229. If wastewater discharge is seasonal or intermittent non-continuous,
approximately how many days out of the year do you discharge to the
receiving water.
(a) Less than 30
(b) 31-90
(c) 91-120
(d) 121-180
(e) 181-210
E. Preliminary Treatment NA
230. DELETED - ANSWERED IN PART I
NA
211-240
(g) 241-270
(h) 271-300
(i) 301-330
(j) 331-360
231. If neutralization is
Chemical used
fill in the following;
021398
-------
Mill: Keveg Fibre Location: Sacramento
F. Primary Treatment NA
232. DELETED - ANSWERED IN PART I
233. Are any chemicals or other settling aids added to the primary treatment
units?
(a) Yes
(b) No
(c) To the extent necessary (intermittent).
G. Biological Treatment NA
234. Provide the following information for the biological treatment system
(if applicable).
a. Process Source or Sewer No.* Flow, MGD BOD, Ib/D TSS, Ib/D
Design Influent Values Average Day ._
Maximum Day
Maximum Month
b. Primary Treatment Effluent ' Average Day
Maximum Day _
Maximum Month
Other Wastewater Streams Which Enter the Biological Treatment Systems
Without Primary Treatment
c. Average Day ^ t_
Maximum Day
Maximum Month
d. Average "Day ' _•
Maximum Day
Maximum Month'" v •
*Process source or sewer number should be keyed to the mill process and
wastewater treatment schematics requested in Section VIII. ~ "~
021389
- 45 -
-------
Mill: Keyes Fibre
Location: Sacramento
235. Give the normal pH of the wastewater at the influent to the secondary
treatment system.
(a) 4-6
(b) 6-8
(c) 8-10
236. DELETED - ANSWERED IN PART I
H. Secondary Solids Removal JM
237-238. DELETED - ANSWERED IN PART I
I• Spray Irrigation JJA
239. Is treated wastewater used for irrigation?
(a) Yes
(b) No
(c) Partial
J. Sludge Handling and Disposal NA
240. DELETED - ANSWERED IN PART I ••
241. Give the percent solids of the sludge after dewatering and prior to
disposal.
(a) 5-10%
(b) 10-20%
(c) 20-30%
(d) 30-40%
(e) above 40%
242. Describe any leachate management practices performed at the mill for
sludges-which are disposed of on land.
-------
Mill: Keyes Fibre
Location: Sacramento
K. Foam Control - (Wastewater treatment system only) NA
243. Does the mill use foam control measures?
(a) Chemical
(b) Physical Methods
(c) None
(d) Other - explain
021461
-------
Mill: Keyes Fibre Location: Sacramento
L. Cost Information
244. Provide cost data indicated for effluent treatment system in 1976 dollars.
Use the cost multiplier factors, which follow, to convert to 1976 dollars.
Annual Operation
Total Capital Cost and Maintenance Cost*
Internal control devoted to ^87
NA
effluent waste load reduction.
External Treatment: System
Primary Treatment
Secondary Treatment
Construction Cost
Multipliers
to Convert Capital Cost to 1976 Dollars
1956 =
1957 =
1958 =
1959 =
1960 =
1961 -
1962 =
2.535
2.380
2.325
2.254
2.220
2.220
2.207
1963 =
1964 =
1965 =
1966 =
1967 =
1968 •
2.186
2.161
2.124
2.051
1.978
1.884
1969 =
1970 =
1971 -
1972 =
. 1973 -
1974 »
1975 =
1.794
1.689
1.564
1.485
1.317
1.242
1.100
*Factors to be considered in Annual Operation and Maintenance Costs
(0 & M Costs).
1. Manpower - both operators and maintenance personnel
2. Contracted services
3. Energy Cost
4. Trucks for hauling
5. Nutrients
6. Leased equipment
7. Disposal costs
8. Sludge handling
9. Sampling and analysis
10. Equipment replacement (except major capital)
Exclude Depreciation
021402
- 48 -
-------
Mill: Keyes Fibre T . Q ,
— _._ Location: Sacramento
a. Capital Cost Recovery(if available) $22^572 Demand charge
fa. Operation and Maintenance (if available^^o"?! Loading charge
c. Total Annual User Fee 1976 $8?>6^3 Includes monitoring
and contributing agency fee of
$12,600.
246. Please give the-basis used by the POTW to determine the mill's user
fee.
(a) Flow only
(b) BOD only ~" i
(c) TSS only
(fd) Combination of parameters (please indicate) See attached.
(e) Unknown
247. Is there sufficient land for expansion of your wastewater treatment
system for BATEA?
(a) Yes
(b) No
(c) Unknown
248. Can the mill purchase land from adjoining property owners for possible
expansion of the wastewater treatment system?
(a) Yes
© No
(c) Unknown
- 49 -
-------
Mill:
JCeyes. Fibre
Location: Sacramento
User Fee
P. 49 Sec. 246
A. Demand charge (a)
mgd x $862.00
BOD #/D x $0.32
SS #/D x $0.08
B. Loading Charge
mg x $68.80
tp BOD x $34.70
tp SS x $34.50
tp = thousand pounds
C. Monitoring Charge
D. Agency Charge
Dia. inch miles x $17.00
(a) Applied each month of the year, based on the average daily
loading during that month In the preceding 12 months with
the maximum average daily loading.
021*04
-------
Mill:- Keyes Fibre
Location:
Sacramento
-.*»,.-....
•*•*« -'.--•.-.•'.• :- -
249.
Are the soil conditions in the land available for future expansion of
"such a quality as to require special construction methods or special
. facility.equipment (i.e., ledge, water table and liners needed for
. basins)? • - • . • . -
VV(a)>7es; •/•/-. .-•""'. • • '.'•'."-.„ ' " '' •:''' '*
../.i (c) ^Unknown/.;.' ;•/•;.;,•- - . -" : " '.-*•"*.-.
.,,-': . - . >.•.•.„ •--
• -250. -;'; Miscellaneous' Discharges - Indicate- any- was tewater 'discharges -not .
•-.- .-"-described 'in Section V which do not flow -to "the was tewater treat-.
,.., .....
•.-: - ;,. */.--- •
;"*' '- " • -c ^ - * **v - - • • ' ^."" ^, -*!,"• 1 - ^ ' '* ; • " i '
'-••'• '-'.'' N..'.; I. Was tewater -'Character is tics • ,-;. ; - -=. .:T-t\-* Lj - •-.-' V" • . ' . •-.
;• J.,,.. 251-254..-V DELETED -.ANSWERED IN PART I •; '. ' V ,":'' '"''' ' "', ':' .. - " '
^T^';^"^r";255.^J^Was'' the-analysis".procedure used for BOD measurement "in accord with
47;?"v ;^iiS.V ; ^ ;A'-; the .method ^presented in Standard Methods .-for-the Examination of-Water
•;'>'i '-*••'„• •; 7: ••••" •••>-. and-Wastewater? *':» - - . . .. „
-J,-,.":.-';.:",, - ' ./.'f.(a)'.^:13th; Edition.." Analysis by Sewer Dept: ' ': \ .
'•E:';;-;J v v!\.:^:^(b)'^14th/ Edition;;. '"'.-'• • ; '. " •' -' '~^;-'^---; -.;.'•' -.•
.^;.«. XL^ •'-:: ;- .•'-- •%;,-' ,.(c)J- No;, (please describe other method ,usedX; ' "'-'
:|^m5-'^v{>-^^:>%^S-^v------; '- ••'- .".^{v;O..- . --
:''l';"1 ;
ic acid BOD standard;
-------
Mill: Keyes Fibre
- Location: Sacramento
-'*.', v-'-^'-
(a);; Daily .. -
(b). Weekly
(c)*.; Monthly
.*'**"* ' " " .'
(d) Quarterly .
'. <'*•'"--,-... \-.---~, ...'."•
(e) - Semi-annual
"?: 258.;^ Please indicate average percent -
^f;;^/ ;,. :::,-^terminations ,and the Slucose-glutamic acid BOD-standard. .;.'•:/ ,f &£ ;:,^- |
-S.-f '"?"-.'••:'.":"• >"''-/' \- • V»;'cw ' " • ' • ' • ' • ' ' • ' '•••-•- » ' ~ '->•'"'•.., - '"*• '?• ••. • * i '""•.''•;*".*'.•'''.': ,--'•" i
'•i;~ ^..;^:f^- .''V-(a^--.^r5Z,/ .-: -.-._. •- -.. -: ./-• - •-.-._•.• ;•;-.... v/ :•;..- •;••}:•: .tVV;"*.^-;;-^^. ..v;l-l j
.-'• - - "-4,, '• - 'IV ** * 5
-Jft.-*^
analysis"..procedure
subsequent , amendments
Other '(please describe) •'
•
»j^f ' "-3'1-"'" * '*•*,.
•.^KS';?®!'-^?--* r^H-":-"--r>-~^77—:—-t.= '"'•' - "v^'/.-"• -J:-?-'•- ^-^ci •—.'^-r-'v-r.-'*--v"-;!:^.^'^'-^-- '-^^iiJi^feii-ii^TV«C)r
-.'-..I* ^v . . " JJ- ^ ' . "*•., . ' * • •' ,•-''-' •..•*-s", ^.**.*»».^..'--... -
!'.'-"?'••• 5 " -• ' ""."*••> -. '•' ••. .-_'-"',--•-•*'V.-«.-(».«"v"S'f>i>:
- . . " • . '-...' ";i^j;^.>;r-
-------
Mill: * Keyes Fibre Tnn»n««. Sacramento
Location:
>... VI. FUEL AND ENERGY .
A copy of the API "Monthly Fuel and Energy Report" has been included in
::./ this section to assist the mill in calculating (if information is-not
already available) the answer(s) to the questions asked. The API sheets .
should be used as a guide for computation only, do not return the pages .
. . with the questionnaire.
260. Give the total purchased energy (fossil fuel, electricity, steam, etc.)
. " as equivalent millions BTU/ton of product (Items 1 to 9, .less.10 from
•" API forms).' . "• ' • '
.-•"17.83
261. Give^the-energy.used for external treatment operations as equivalent
, KWHr/ton of product.
02H07
- 52 -
-------
Mill: Keyes Fibre
Location:
Sacramento
VIII. PROCESS SCHEMATICS
Attach separate general block diagrams for the three items listed below.
Water Treatment (if applicable) - Provide a general block diagram
showing the water treatment system used, chemical application points,
average flow, and disposal method for backwash water. If the mill has
a raw water analysis available please attach a copy. - • - .
Manufacturing Process Schematic - Provide a general schematic of
the total mill process to include water balance and all process
wastewater streams. (See note at start of Section V.) Wastewater
streams should be cross referenced to the effluent treatment system
schematic. ' '
C. Effluent Treatment System - Provide a general schematic of the
effluent treatment system. Please key the diagram to the manufacturing
process block diagram so that the point of influent to the treatment
system for individual process sewers can be determined. Also show
all chemical application points; chemicals used; flow monitoring and
sampling points; average flow; size or area, -volume, and number of .
each treatment system component; sludge recycle and volume; and
sludge dewatering/thickening system. '- -
Additional information on the mill's wastewater treatment system is
- -• • • also needed to-complete the data request. 'Please provide answers to
the following- questions which pertain to your wastewater treatment
system. -For-questions which do not apply, indicate by writing N/A
(not'applicable) on the space provided for the.answer.
Primary Treatment .'
262. Give the following primary clarifier overflow rates:
a. Design
Spcl/ft at
b. Current
gpd/ft at
MGD
MGD
- 53 -
-------
Mill: Keyes Fibre Location: Sacramento
Biological System NA
263-268. For the biological system employed, please give answers to the appropriate • . . }
~ questions listed below: '. \
System Question Answer :
263- Aerated Stabilization a) Volume of the aeration zone Mil. Gal., -, ; i
<•;-';•• .., Basin" ,' ' • . . . ... ••- .'-•.J% •'•'•"' --•'
b) Connected horsepower for aeration "
. 264. Activated Sludge a) Volume of the aeration zone Mil. Gal.
:•:'•'.•" b) Connected horsepower for aeration - ..
c) MLSS (Mixed Liquor Suspended
Solids) -
265. Trickling Filer a) Volume of media
b) Surface area of filter -ft2
2
KBC a) Surface area of RBC ft -
'-: "267. Post Storage a) Volume of storage . " "" 'Mil. Gal.
,-..._""" . •"' • '" • . 5. ',
/V 268. " "If-nutrient addition is used, please give the average BOD:N:P ratio. .
V.."; .." •• "• BOD:N:P : : .•'.."'
, Secondary Solids Removal
NA
|9. -Give the secondary clarifier overflow rates: - .-
a. Design gp^/f t2 at ^ MGD . . '." '
b. Current gpd/f t2 at MGD . - >;'
021509
- 54 -
-------
PART II
Question
Number .
Question
- Number
Question
Number
- •
Question
Number
Question ...
.. " Number .
Question
Number
Question
Number
•rrr. rrrr/ ;,-.\~—r——. •
"' ' - •*•
- 55 -
-------
AMERICAN PAPER INSTITUTE
RAW MATERIALS AMD ENERGY 'DIVISION
260 Moo'.V-r, Av.ou., N.w York, N>. 10016
CONFIDENTIAL
MONTHLY FUEL AND ENERGY REPORT
Month, Year:_ 10/77
(If this is a "period" mi II,. the
period reported is from 10/1
through 10/31 .) mo./day
mo./day-
company: Keyes Fibre Co. •
Hill Location: Sacramento,
CA
Mi 1 1 Reference NO.:
Region:
FOR API
USE ONLY
03 Monthly Fuel and Energy Consumption Data
For each energy source used in the month, please enter to the nearest tent h information in
• the way you monitor it most accurately. For example, in the case of fuel oil, you would pro- •
babiy enter thousands of barrels. But in the case of bark, you would probably enter Billion
STU's as fired—obtained by applying the bark boiler's rated or estimated efficiency to its
metered steam output. Then apply the BTU conversion factor you believe to be most accurate
for your operation to compute either Billions of BTU's as in the first case, or weight of
fuel at the specified moisture content as in the second case. {See list of average BTU
'vsfues of-nominated fuels, over.) Limit reporting to energy used within the mill fence line,
thereby excluding energy used in wood harvesting, transportation and converting operations.
ACTUAL CONVERSION
FUEL ' UNITS USE FACTOR
Purchased Fossil Fuel t Energy
1. Purchased Electricity 10/77
2. Purchased Steam
3. Coal
4. Residual Fuel Oil (#5,6)
5. Distillate Fuel Oil (#2)
'6. Liquid Propane Gas (L.P.G.)
* 7. Natural Gas
-8. Other (specify)
9. Other (specify)
Millions KWH
Millions Ibs.
Thousands
Short Tons
Thousands 42
Gal. Bbls.
Thousands 42
CaJ. Bbls.
Thousands Gallons
Millions Cu. Ft.
7.014 * 3.1» -
BILLION
BIU's as
FIRED
23.847
x -
X
x . - - '
x . • • . • ' •
X *
28.622 x 1.04 -
29; 767
X -
X
':.: 10. LESS ENERGY SOLO:
• Self Generated 'and Waste Fuels
II. Hogged Fuel: (Wood «• Bark)
*!12. Bark: (Enter separately, if
• • available, bark obtained in
debarking of pulpwood)
klj. .Municipal Waste
14. Spent Liquor (oven dry basis)
15. Self-Generated
Hydroelectric Power
J6. Other (specify)
H7. Other (specify
Thous. Short Tons
(50% moisture
Thous. Short Tons
(50% moisture
content)
Thous. Short Tons
(50% moisture
content)
Thousands Short
Tons of Sol ids
Mill ions KWH
021411
X •
X at
x -
X
X 3.*» -
X •
X a
TOTAL [flj (II to 17):.
. GRAND TOTAL
(A*B) :
Total In Plant Electric Generation:,
(Calculate separately from above
Mill ion KWH
, j '^-'.m
xiti^
•*.•«>
.;?*-
: j/l*. *|
rhf" ;|
-------
[l ( j Mont h I y Produc t i on pa t a
Please enter production for the month in thousands of short tons, to the nearest tenth.
Mills which use both the4r own and-purchased pulp will enter separate c'ata for "integrated
Paper and Paperboard" and "Honintegrated Paper and Paperboard."
I, Pulp (dried and wet lap): Report dried and wet lap pulp (reported on a dried basis).
2. Integrated Paper and Paperfaoard; Report primary product (excluding converted products)
manufactured from on-site pulp production, as normally measured.
3. Honinteqrated Paper and Paperboard: Report primary product (excluding converted products)
manufactured from off-site pulp production and/or waste paper, as normally measured,
(thousand short tons)
I. Pulp (dried and wet lap on dried basis):
2. Integrated Paper t Paoerboard:
3. ' Wonintegrated Paper t Paperboard:
't. TOTAL PRODUCTION fife
-------
PROJECT
i
i
MILL NO. ,
COMR BY
AN6
CHK. BY
JOB NO.
DATE -.
Products:
Average Tons/Day:
•21,-Z.fe- . •
. -*5 -'. ~ ~r ' ' .' '
::,. ; -Check file for
updated data:
Wastewater
;••-!- i : • .
"Flow/ Kgai'T
. ... ._...
j;.= .I . 7...:"..,.!..1.L' i....; .
r; -'-. Check Schematics:
i- - •
;Raw 11-^ "«.-.
Per. Day Per. Ton.; ;. Per.;Day•„...- Per .-Ton -
i .....; i,,:- .i>s;..^'.^.V.-. .; > .-fi
.:.,:. .;;_.^:.-.-i.
: f -:•--.• ••-••:
FORM 00.01 REV. 12/78 .,
-------
FOR THE
NAME:
LOCATION:
AVAILABLE
SUEVEY
-------
ESTABLISHED ]«»»
PLEASE ADDRESS REPLY TO:
WATER VILLE, MAINE 04901
TEL. 207 873-3351
COMPANY
160 SUMMIT AVENUE • MONTVALE. NEW JERSEYO7645
January 10, 19 ?8
U.S. EPA Pulp and Paperboard Survey . . ' • . •
E. C. Jordan Co. . •
P. 0. Box 7050 Downtown Station
Portland, Maine 04112
Attn: Mr. Willard Warren ' • .
Dear Mr." Warren: . -'•••'•
Enclosed is a completed EPA survey form Pulp, Paper and Paperboard • . '„
Industry Non-Integrated Mill Part II for Keyes Fibre plant at ;.-
Sacramento, California. ' . v „ ,_'.\
* '**'""•".-*..*
..-.-• , • Very truly yours, . ' • " "'"*•/'
CFB/mbc ..-•-'•
Enclosures
cci H. J. Desmond
'Clarence P. Bean . • • \
Manager, Process Engineering -.;. .
^.•-•KfrS.j.f*--*.?, -
.--- .1"--•:«••:-.. »»'
021^15
V' - :^&-
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- 12 -
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X
ENVIRONMENTAL PROTECTION AGENCY #/
SURVEY FORM
PULP, PAPER, AND PAPERBOARD INDUSTRY
«, si INTEGRATED MILLS
l<\ PART I
I. MILL BACKGROUND DATA
A. Mill & Division Name: Keyes Fibre Co.
Address: Shawmut, Maine ZIP C&975
Telephone 20? / '873-3351
2,
Corporate Affiliation (if applicable) _
Contacts and Title: (Use an asterisk next to the responsible personnel
completing the survey form)
C, F, Bean Manager, Process Engineering
E. J. Reid man Manager, Eastern Division I-.'fg•_. __
2. L. Clifford Manager, Shaw-taut Plant
*G. D. Ackendorf . Waterville Quality Control Manage:
Director of Research
B. Age of Mill 57 years, est.
1. Year of initial construction 1920 est.
Please give the year of initial startup ancl each year sine* -.1952
in which any major aodifications or permanent shutdowns were made
which significantly affected the composition or amount of effluent
from the mill.
Year(s) of Waste
Significant Modification
Year(s) of or
Initial Startug Permanent Shutdown
a. Woodyard '~ Oct. 10, 197** Wet Debarking
Pulping —
b. Brown Stock ;
Washers
c. Screen Room
021*20
- 13 -
-------
Mill:
d. Bleaching
Chemical Recovery
e. Recausticizing
f. Evaporation
g. Recovery Furnace
h. Paper Machine(s)
i. New or Additional
Refiner(s)
Location:
Year(s) of
Initial Star tup
Year(s) of Waste
Significant; Modification
.>r
Permanent Shutdown
j. Added IMP Process
k. Added CKP Process
1. Blow Heat and Condensate
Recovery
Air Pollution Control
Systems that contribute
to the waste load
m. Wet Scrubber(s)
n. Precipitator (s)
o. Eliminatrion of Process(es)
(please describe)
- 14 -
-------
Mill:
Location:
Year(s) of
Initial Startup
Year(5) of Waste
Significant Modification
or
Permanent Shutdown
p. Products Mix Changes
q. Process Changes
r. Other
021522
- 15 -
-------
Mill:
Keyes Fibre Co,
Location: Shawmut, Maine
II. PRODUCTION INFORMATION
Oct. 1976 thru Sept. 1977
A-
3.
4.
5.
6.
7.
8.
9.
Pulp
Manufactured
Bleached Kraft
Unbleached Kraft
Dissolving Kraft
NSCC
Groundwood-Fine
Groundwood-Coarse
CMP
10. IMP
11- Bleached Sulfite
12. Unbleached Sulfite
13. Dissolving Sulfite
Maximum Month
Air Dry
__ Tons/Day
Hardwood Softwood Hardwood "Softwood Hardwood Softwood
Average Daily*
Air '/Dry
Tons/Day
Maximum Day
Air Dry
Tons/Day
130; 8
21.8.
14. Deinked Groundwood
15. Deinked Kraft
16- Deinked Mixed Waste
17. Wastepaper -
Manufactured Furnish
Other (please list)
*Average Daily - Total Production for year
Total Production days for year
- 16 -
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Mill:
Location:
B,
19.
20.
21.
Fiber
Purchased ;ulp
Baled
Wet Up
Slushed
Average Daily Maximum Day
Air Dry Air D.y
Tor.s/day Tons /day
Hs-rdwood Softwood Hardwood Softwood
Maximum Month
Air Dry
Tons /cay
Hardwood Softwood
22. Broke
23. Other (piaase list)
C. Prjaducts
24. Market Pul?
a. Pulp 3ales and/cr Rolls
b. Wet Lap Pulp
c. Slush Pulp
25. Groundwooc Molded Pulp
26. Newsprint
Ax^erage Day Maximum Day Maximum Month
Air Dry* Air Dry* Air Dry*
Tons/Day Tons/Da1-' Tons/Dav
Il2.\
^Measured s.- the winder or pulp dryer.
- 17 -
021*24
-------
Mill:
r , —
Groundwood Printing, Writing and Related
a- Uncoated Groundwood Printing
and Converting
Month
Ton /
ions/Day.
b- Clay (502 or more kaolin)
Coated Groundwood Printing
and Converting
c. Groundwood Specialties
d. Other
28. Wood Free Printing, Writing
and Related
a. Uncoated Free Sheet Printing
b- Clay (50% or more kaolin)
Coated Free Sheet: Printing
c. Uncoated Writing and Related
d. Uncoated Solid Bleached
Bristols
e- Clay (50% or more kaolin)
Coated Solid Bleached Bristols"
Other
29' Cotton Fiber Papers
a. Writing and Related
b- Technical
c. Other
30- Thin Papers
a. Carbonizing
Measured at the winder or pulp dryer.
b. Cigarette ' ~~ ' ~ " j.
c. Other
- 18 -
-------
Mill:
33.
34.
Location:
Average Daily Maximum Day Maximum Month
Air Dry* Air Dry* Air Dry*
Tons/Day Tons/Day Tons/Dgy
31. Packaging and Industrial Converting
a. Unbleached Kraft
b. Bleached Kraft
c. Other
32. Specialty Packaging and Industrial
Converting .
a. Tape Backing
b. Saturating
c. Gasket
d. Other (list types)
Sanitary Tissue
Unbleached Kraft Paperboard
(80% or more unbleached kraft pulp)
a. Linerboard
b. Folding
c. Other
P35.
Semi-Chemical Paperboarc
(75% or i?.ore semi-chemical pulp)
a. Corrugating
b. Other
*Measured at the winder or pulp dryer.
- 19 -
-------
Mill:
Average Daily Maximum Day Maximuns H-:,-;'
Air DryA All- Dry* Air ))ry*
Tons/Day Tons/Day Tons/Day
36. Bleached Paperboard
(not less than 80% bleached chemical wood pulp)
Clay Coated Bleached Food
Board
b.
c-
d.
e.
Uncoated Bleached Food
Board
Bleached Linerboard
Folding
Other
37. Recycled Paperboard
a. Linerboard
b. Corrugating
c. Chi? & Filler Board
d. Folding
e. Set-up
f. Gypsum Wall Board
g. Other
38. Construction Paper and Board
a. Construction Paper
b. Wet Machine Board
Insulating Board
Hard Pressed Board
Other
c.
d.
e.
*Measured at the winder or pulp dryer.
- 20 -
-------
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Mill; Keyes Fibre Co.
Location: Shawmut, Maine
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Mill: Keyes Fibre Co.
Location: Shawmut, Maine
IV. MANUFACTURING PROCESS AND INTERNAL POLLUTION CONTROL PRACTICES
A. General
189. Are the drum or mechanical barkers operated dry? Steam may be used
for thawing logs.
(a) (Yes)
(b) No
B. Kraft and Soda Mills - Digesters
Give the permanganate number (if applicable) for the following:
Answer either question 220 through 223 or questions 223 through 226.
220. Hardwood
Percent of the
Total Production
(a) 10-11
(b) 11-12
(c) 12-13
(d) 13-14
(e) Above 14
221. Softwood
Percent of the
Total Production
(a) 16-18
(b) 18-20
(c) 20-22
(d) 22-24
(e> Above 24
222. if the mill pulps a mixture of hardwood and softwood, please give the
permanganate number.
Permanganate Number
021£38
-. 31 -
-------
Mill:
Location:
223. Give the normal percent of the following:
a. - Softwood
b. Hardwood
Give the Kappa number (if applicable) at the brown stock washers for
the following:
Percent of the
Total Production
224. Hardwood
(a) 15-17
(b) 17-19
(c) 19-21
(d) 21-23
(e) Above 23
Percent of the
Total Production
225. Softwood
(a) 28-30
(b) 30-32
(c) 32-34
(d) 34-36
(e) Above 36
226. If the mill pulps a mixture of hardwood and softwood, please give
-he Kappa number.
Kappa Number
021*39
- 32 -
-------
Mill:
G.
231-233-
Scr_e.ordn
Krt'f.t. and Soda 'Mills _-_ Browt^ Stock WAshers^
Give the approximate brown stork washer efficiency in terms of pounds
of soda loss as v.-ashable Na-0 for the following:
Percent of the
231.
232.
233.
(a) Less than 15 #Na20/Ton
(b) 15-25
(c) 25-35
(d) 35-45
(e) Greater than 45
(a) Less than 15 #Ka_0
(b) 15-25
(c) 25-35
(d) 35-i5
(e) Creater than 45
Line j?3
(a) Less than 15 i-Na,
(b) 15-?-5
(c) 25-35
(d) 35-45
(e) 'Greater than 45
Percent or -he
Total ?r_c
Percent of the
Total Production.
-------
J-..JC.-.IL.; ca:
240-242,
a.
b.
c.
d.
e.
Kraft end Sod_a Mil_ls - Bleaching
Indicate the normal bleaching sequencers) used, (i.e. OChlorine,
E-Cauitic Extraction, D=Chlorine Dioxide, H=Hypochlorite, P=Peroxide)
ar.c tne G.^. Brightness Range and percent shrinkage for the bleach line(s)
tor the principal grades produced on each line.
Bleach Line #
Normal
Pulp Bleached
Hardwood
SoftWOOG
il 'Fresh
Water Usage •
__ Stage
(240)
Grade $1
Production
ADT/d
1-he.raical
(241)
Grade #2
Production
ADT/d
(242)
Grade #3
Production
ADT/d
Chemical
Chemical
7 :
f. G.E. Srightr.sss
Flange
g. Shrinkage (1)*
*Ecuais tons /day Input - tong^/Jay out
tons/cie:-- input
put
x 100
•21441
-------
Mill:
Location:
D.
Kraft and Soda Mills - Bleaching - Continued
243-245.
a.
c.
d.
e.
Bleach Line #2
Normal
Pulp Bleached
Hardwood
Softwood
Mixed
Normal ?resh
Water Usage
Stage
(243)
Grade #1
Production
ADT/d
Chemical
(244)
Grade $2
Production
ADT/d
Chemical
(254)
Grade #3
Production
ADT/d
Chemical
3
4
5
6
7
f. G.E, Brightness
Range
g. Shrinkage (%)*
*Equals tons/day input - tons/eg y output
tons/day input
12144*
- 35 -
-------
ill:
Locati07.ii
D.
Kraft and Soda Mills-Bleaching - Continued
^46-248.
a.
b.
c.
d.
Bleach Line #3
Normal
Pulp Bleached
Hardwood
Softwood
Mixed
Normal Fresh
Water Usage
(246)
Production
ADT/d
(247)
Grade #2
Production
ADT/d
Cbercica^l
(248)
Grade #5
Production
ADT/d
Chemical
3
4
5
6
7
f. G.E. Brightness
Range
g. Shrinkage (%)'
quals
M
100
tons /day in
- 36 -
-------
Location:
258-260. Give the type of bleach line washing for the principle gradc-s manu-
factured.
258. Bleach Line //I
(a) Jump-stage counter-current washing
(b) Straight counter-current washing
(c) Co-current washing
(d) Other (please describe)
259. Bleach Line i2
(a) Jump-stage counter-current washing
(b) Straight counter-current washing
(c) Co-current washing
(d) Other (please describe)
260. Bleach Line //3
(a) Jump-stage counter-current washing
(b) Straight counter-current washing
(c) Co-current washing
(d) Other (please describe)
E. Kraft and Soda Mills - Recovery System
267. Give the type of evaporator condenser used.
(a) Barometric
(b) Surface
(c) Both (please give the number of-each type)
02H44
- 37 -
-------
Location:
7 . Kraft and Soda Mills - Liquid Was l:e Sources
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PAIlT I
G. Sulflte Mills - Pulping Area
92. What base is used?
(a) Mg
(b) Ca . '
(c) Ka
293. Is the pulping process acid or bisulfite?
(a) Acid
(b) Bisulfite
297-299. Give the overall pulping yield for t':ic following:
297. Line #1
(a) Below 40
(b) 40-45
(c) 45-50
(d) 50-55
(e) Above 55
298. Line. #2
'(a) Below 40
(b) 40-45
(c) 45-50
(d) 50-55
Percent of the
Total Production
Percent of the
Total Production
(e) Above 55 . Q 21 j j $
- 38 -
-------
Mill:
Location:
Percent of the
To"al j T oduct ion
299. Line #
(a) Below 40
(b) 40-45
(c) 45-50
(d) 50-55
(e) Above 55
H. Sulfite Mills - Screen Room and Washers.
305. Line #
(a) 60-75%
(b) 75-90%
(c) 90-95%
(d) 95-100%
306. Line £
(a) 60-75%
(b) 75-90%
(c) 90-95%
(d) 95-100%
Percent of the
Total Production
304-306. Give the approximate red stock washer efficiency.
- is
304. Line ffl
(a) 60-75%
(b) 75-90%
(c) 90-95%
(d) 95-100%
Percent of the
Total Production
Percent cf the
Total Production
- 39 -
-------
Mill:
Location:
I.
312-314
a.
b.
c.
d.
e.
f.
g-
Sul£ite Mills-Bleaching
Indicate the normal bleaching sequence(s) used, (i.e. C=Chlorine,
E=Caustic Extraction, D=Chlorine Dioxide, H=Hypochlorite, P=Peroxide)
and the G.E. Brightness Range and percent shrinkage for the bleach
line(s).
Normal
Pulp Bleached
Hardwood
Softwood
Mixed
Normal Fresh
Water Usage
Stage
1
2
3
4
5
6
7
G.E. Brightness
Range
Shrinkage (%)*
(312)
Bleach Line #1
Production
ADT/d
(313)
Bleach Line #2
Production
ADT/d
(314)
Bleach Line //3
Production
ADT/d
Chemical
Chemical
Chemical
*Equals tons/day input - -tons/day output -__
tons/day input
- 40 -
-------
Mill: Location:
515-317. Give the type of bleach line x^ashir.g for the following:
315. Bleach Line #1
(a) Jump-stage counter-current washing
(b) Straight counter-current washing
(c) Co-current washing
316. Bleach Line $2 -_ •
(a) Jump-stage counter-current washing
(b) Straight counter-current washing
(c) Co-current washing
317 Bleach Line ??3
(a) Jurap-stage counter— curt'ent washing
(b) Straight counter-current washing
(c) Co-current washing
J. SulfiteMill - Recovery System
325. Give the type of condenser used.
(a) Barometric
(b) Surface
(c) Both (please give the number of each type)
K. Sulfite Mills - Liquid Waste Sources
NO QUESTIONS FOR THIS ITEM ARE TO 3E ANSV7ERED IN PART I
021M8
- 41 -
-------
Mill: Keyes Fibre Co. Location: Shawmut, Maine
L. Groundwood Mills - Pulping Area
353. Describe the type of grinding operations; i.e., type of grinder, refiner.
(a) Stone 3 pocket 2 ft, (&)
(b) Refiner
(c) Both
M. Groundwood Mills •- Bleaching
358. Indicate the bleaching chemical(s) used.
(a) Zinc Hydrosulfite
(b) Sodium Hydrosulfite
Peroxide
(d) Other (please note method and/or sequence)
N» Groundwood Mill - Liquid Waste Sources
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I
0. NSSC,CMP andTMP Mills - Pulping Area
377. Give the percent yield:
a. NSSC %
b. CMP %
c. TMP %
P. NSSC, CMP, and TMP Mills - Screens and Washers
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I
- 42 -
-------
Mill:
Location:
Q. NSSC, CMP, and IMP Mills - Bleaching
Indicate the normal bleaching sequence(s) used, (i.e. C=Chlorine,
E=Caustic Extraction, D=Chlorine Dioxide, H=Hypochlorite, P=Peroxide)
and the G.E. Brightness Range and percent shrinkage for the bleach
line(s).
390-392
Normal
Pulp Bleached
Hardwood
Softwood
Mixed
Normal Fresh
Water Usage
Stage
1
- 2
3
4
(390)
Bleach Line //I
Production
ADT/d
(391)
Bleach Line 92
Production
ADT/d
(392)
Bleach Line #3
Production
ADT/d
Chemical
Chemical
Chemical
f.
G.E. Brightness
Range
Shrinkage (%)*
*Equals tons/day input - tons/day output inn
«_ i i * ^C J.UU
tons/day input
-------
Mill:
Location:
R. NSSC and CKP - Recovery System
398. Does the mill have a recovery system?
(a) Yes
- .-, (b) No
S. NSSC, IMP and CMP Mill - Liquid Waste Sources
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I
T. Deink hills - Pulper Area
424-426. Give the overall pulping yield for the following:
424. Line $1
(a) Below 50
(b) 50-60
(c) 60-70
(d) 70-80
(e) Above 80
425. Line $2
(a) Below 50
(b) 50-60
(c) 60-70
(d) 70-80
(e) Above 80
426. Line $
(a) Below 50
(b) 50-60
(c) 60-70
(d) 70-80
(e) Above 80
Percent of the
Total Production
Percent of the
Total Production
Percent of the
Total Production
mist
-------
Mill:
Location:
429. What chemicals are added to the pulper for deinking. (Indicate amounts.)
U. Deink Mills - Stock Washers and Screening
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IK PART I
V. Deink Mills - Bleaching
Indicate the normal bleaching sequence(s) used,'(i-e. C=Chlorine,
E=Caustic Extraction, D=Chlorine Dioxide, H=Hypochlorite, P=Peroxide)
and the G.E. Brightness Range and percent shrinkage for the bleach
line(s) used.
440-441
a- Production
ADT/d
(440)
Bleach Line #1
(441)
Bleach Line #2
b. Normal Fresh
Water Usage
c. Stage
1
2
3
4
Chemical
Chemical
d. G.E. Brightness
Range
e. Shrinkage (%)*
*Equals tons/day input - tons/day output
tons/day
•- 45 -
-------
Mill:
Location:
W. Deink Mills -_ Liquid Waste Sources
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I
X. Paperboard from Wastepaper - Pulper Area
463-465. Give the overall repulped yield for the following:
463. Line ill
(a) Less than 80
(b) £0-85
(c) 85-90
(d) 90-95
(e) Mere than 95
464. Line #2
(a) Less than 80
(b) 80-85
(c) 85-90
(d) 90-95
(e) More than 95
465. Line #3
(a) Less than 80
(b) 80-85
(c) 85-90
(d) 90-95
(e) More than 95
Percent of the
Total Production
Percent of the
Total Production
Percent of the
Total Production
021£
- 46 -
-------
Mill:
Location:
Y. Paperboard from Wastepaper - Washers and Screens
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I
Z. Paperboard from V'astepaper - Liquid Waste Sources
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IH PART I
A-l. Builders Paper — Stock Preparation
476. Is digester used to process wood chips?
(a) Yes
(b) No
B-l. Paper Mill - (All mills except Builders Paper. Builders Paper mills
go to Item C-l)
488. How many paper machines does mill have?
489. Give the number of paper machines the mill has which utilize savealls,
or similar device for fiber recovery.
490. Give the number of paper machines the mill has which have savealls,
or similar device that permit reuse of clarified water.
504. High pressure showers - Are high pressure showers (above 250 psig)
used on the paper machines for wire cleaning?
(a) Yes
(b) No
(c) Limited Application
«21£54
_ 47 _
-------
Mill:
Location:
505. High pressure showers - Are high pressure showers (above 250 psig)
used on the paper machines for felt cleaning?
(a) Yes
(b) No
(c) Limited Application
C-l Builders Paper - Paper Mill
508. Give the number of paper nachines at mill.
D-l Builders Paper - Saturating and Coating (if applicable)
514. Does the mill utilise a saturating and/or coating process?
(a) Yes
(b) No
E-l Builders Paper - Internal Controls
NO QUESTIONS FOR THIS ITEM ARE TO B2 ANSWERED IN PART I
F-l Additional Information (All Mills)
NO QUESTIONS FOR THIS ITEM ARE TO BE 'ANSWERED IN PART I
021£55
- 48 -
-------
Hill: Ke/es Fibre Co. Location: Shawaut, Maine
V. WAIZ?. USAGE AND EFFLUENT TREATMENT PRACTICES
Instructions for Completing SectionV
Section V requests information on the mill's wastewater treatment practices.
In Section VIII a general schematic of the effluent treatment system is
requested. You have the option of providing any of 'the'data requested in
Section V on the schematic. If you do this, please indicate on the
questicn(s) involved that the data is presented on the schematic.
A. Water Usage
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
B. Background Data
532. Indicate the method(s) of disposal of the mill wastewater.
(a) Direct
(£y Indirect
(c) Self-contained
(d) Other (please describe) •
533. Please give the year in which the following portions of the mill's
existing wastewater treatment system were started .up.
Year of Startup
a. Primary Treatment System POTW ^
b. Secondary Treatment System POTW (J
C. jndirect Discharger (discharge to a POTW) please provide the
following information:
536. is raw wastewater pretreated externally prior to discharge to the
POTW? (Pretreatment is considered to be any treatment device external
free: the mill production processes which is utilized prior to a pri-
mary ana secondary treatment system, or prior to discharge by an
indirect discharger to a POTW.)
(a) Yes
(b) No
121556
-------
Mill: _ Keyes^Fibre Co. Location:
537. Give the treatment process used by the POTW to which your mill discharges,
(Include biological and physical-chemical treatment if applicable)
ttaj) Activated sludge
(b) Aerated lagoon
(c) Oxidation ditch
(d) Trickling filter
(e) None
(f) Other (indicate type)
540. Give the preliminary treatment method, used, if any.
/
(a) Neutralization \/"~^
Screening (indicate type used) ^^ ^j ^ ""~ "= "" rAs.Cer
—
(c) Other (please describe)
542. Indicate the primary treatment method used, if applicable.
Clarifier
(b) Sedimentation lagoon
(c) Mechanically cleaned sedimentation lagoon
(d) Other (please describe) ____
(e) Not applicable
546. Give the type of biological treatment used, if applicable.
(a) Storage oxidation basin
(b) Aerated Stabilization basin
Activated sludge le.lr)or wxygen)
(d) Other (please describe)
(e) Not applicable
02U5?
- 50 -
-------
Mill:
Location:
D. Direct Discharger please provide the following information:
549. Is wastewater discharge continuous or non-continuous (effluent stored and
discharged when conditions allow) when production facilites are operating.
(a) Continuous
(b) Non-continuous - daily
(c) Non-continuous - seasonally/intermittent
E. Preliminary Treatment (Direct Discharger)
551. Give the preliminary treatment method used, if any.
(a) Neutralization
(b) Screening (indicate type used)
(c) Other (please describe)
F. Primary Treatment (Direct Discharger)
553. Indicate the method used for primary treatment.
(a) Clarifier
(b) Sedimentation lagoon
(c) Mechanically cleaned sedimentation lagoon
(d) Other (please describe)
G. Biological Treatment (Direct Discharger)
557. Give the type of biological treatment used.
(a) Storage oxidation basin
(b) Aerated stabilization basin
(c) Activated sludge (air or oxygen)
(d) Other (please describe)
-------
Mill: Location: i
i
*** Secondary Solids Removal
558. If secondary clarification is used, what is the method used?
(a) Clarifier " ;
i
i
(b) Reactor clarifier !
(c) Settling basin i
j
(d) Other (please indicate) j
559. Is a holding pond utilized after secondary treatment?
(a) Yes
(b) No
I. Sjaray IrrIgation •
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
J. .. Sludge Handling and Disposaj.
561. Indicate the method used for sludge disposal.
(a) Lagooning
(b) Landfill
(c) Hog fuel boiler
(d) Other (please describe) ___^
K. Foam Control
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
L. Cost Information —
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
02JU59
- 52 -
-------
Mill: Keyes Fibre Co.
Location: Shawmut, Maine
M. Site Conditions and Availability of Land
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
i-.
i
i
N. Wastewater Characteristics
572-577. iQive the (1976) wastewater loads indicated below:
Oct. 1976 - Sept. 1977
Indirect & Direct Dischargers Please'Answer
(572)
Pulp
Mill
(573)
Bleach Plant*
Acid Alkaline
(574)
Paper
Mill
(575)
Total Raw
Wastewater
Direct Discharger
Only•Please Answer
(576)
Secondary
Treatment (577)
System Final
Effluent Effluent
a. Flow, MGD
(1) Average Day
(2) Maximum Day
(3) Maximum Month
b. BOD, Ibs/day
(1) Average Day
(2) Maximum Day
(3) Maximum Month
c. TSS, Ibs/day
(1) Average Day
(2) Maximum Day
(3) Maximum Month
.,82? i
•533 '
;589 »
2329 *
•-970*
364*
3082,
668'
VI. FUEL AND ENERGY •
NO QUESTIONS FOR THIS SECTION ARE.TO BE ANSWERED IN PART I.
*'. ••
VII. PRIORITY POLLUTANTS
SEE NEXT PAGE '' -
VIII. PROCESS SCHEMATICS
NO QUESTIONS FOR THIS SECTION ARE TO BE ANSWERED IN PART I.
92U60
- 53 -
-------
Mill:
Location:
VII. PRIORITY POLLUTANT COMPOUNDS
Please fill in the following information for those priority pollutants
which, to your knowledge, are in your raw water supply, or used, or
generated in any of the processes in the rail! (refer to the following
pages for the priority pollutant list). Use the nucber shown to identify
the compound.
It should be noted that many mills may be using quantities of the listed
chemicals as additives, cleaning solution, or solvents which are purchased
and referred to by a trade name. Please supply trade names of those pro-
prietary type chemicals, which contain one or more of the listed priority
pollutants as constituents, used in the mill. Exclude all laboratory
chemicals',
Compound Number
or Trade
Process Where
Compound is
Used or Generated
Describe Use
•Quantity Frequency
Sampling or Monitoring
Program for Compound
(Yes or No)
~ 54
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- 56 -
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021464
- 57 -
-------
PART I
CONFIDENTIALITY CLAIMED FOR THE FOLLOWING
Question Question
K— -er Number
Question
Nunber
Question
Number
Question
Number "
Question
wuiriber
Question
Number •:
- 58 -
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ENVIRONMENTAL PROTECTION AGENCY
SURVEY FORM
PULP, PAPER, AND PA?ER30ARI? INDUSTRY
INTEGRATED MILLS
PART II
I. KILL BACKGROUND DATA
A. Mill & Division Name: Keyes Fibre
Address: Shawmut, Maine
ZIP:
04975
1e lech en a:
/
873-3351
Corporate Affiliation (if applicable)
Contacts and Title: (Use an asterisk next to the responsible personnel
completing the survey form)
C. F. Bean
E. J. Reidman
*C. R. Clifford
D. L. Palmer
E. H. Waldman
B. Age of Kill
1-2 DELETED - ANSWERED IN PART I
II. PRODUCTION INFORMATION
3-38 DELETED - ANSWERED IN PART I
III, PROCESS RAW MATERIALS
39-185 DELETED - ANSWERED IN PART I
Manager, Process Engineering
Manager, Eastern Division Manufacturing
*i
Plant Manager, Shawmut
Waterville Process Engineer
Director of Research
02H66
- 62 -
-------
Mill: Keyes Fibre Co.
Location:
Shawmut
IV. MANUFACTURING PROCESS AND INTERNAL POLLUTION CONTROL PRACTICES
A. General
186. Give the typical production days per year.
JCennebec Hiver
«•«•' <*« i, the discharge
POTW
188. What ia the discharge rate and frequency from flume?
_ :355,OOP,gallons
189. DELETED - ANSWERED IN PART I
190. If there is a discharge from the barking operation, where does it go?
(a) Effluent treatment
^b) Other (please describe) Dry Djum Barking
191. Use of mill wastewater for woodyard - Is wastewater such as bleach
plant effluent or white water used in the woodroom for flume make-
up, washdown hoses or wood showers?
(a«) Yes
(b) No
192. High level alarms - do chemical and stock tanks have operable
high level alarms to prevent spills?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
02U67
- 63 -
-------
Mill: Keyes Fibre Co.
Location:
Shawmut
193. pH or conductivity monitor of internal sewers - Do most sewers have
such devices to detect or divert spills?
(a) Yes
(b) No
(c) To the extent: possible
Explanation (if needed)
194-214 Is cooling water collected and reused from the following locations:
(a) Yes; (b) No; (c) Seasonal; (d) To Extent Possible; (e) Not Applicable
a b _ c d e
194. Air compressor cooling water x •
195. Dryer drainage condensate cooling
196. Lube oil cooling
197. Calendar cooling heat exchangers
198. Rewinder brake cooling
199. Evaporator surface condenser
200. Digester blow condenser
201. Paper machine clutch cooling
202. Lime kiln turnions (kraft only)
203. Hot Lime conveyors (kraft only)
204. Cooling in power plant x
205. Feed water pump bearings X
206. Power Plant I.D. fan bearings .. . x
207. Other bearing cooling ~ X
208. Refiner Cooling _. X
02H68
- 64 -
-------
Mill; Keyes Fihre Co. Location: Shawmut
209. Motor control center cooling
210. water chiller
211. Smelt spout cooling (kraft only)
212. Condensate sample coolers
213. Air conditioning
214. Concentrator condenser
B. Kraft and Soda Mills - Digesters - NA
215. what type of digester(s) is used at the mill?
(a) Batch
(b) Continuous
216. What is the white liquor sulfidity range?
217-219. Give the overall pulping yield for the following:
Percent of the
Total Production
217. Line 11
(a) Below 40
(b) 40-45
(c) 45-50
(d) 50-55
(e) Above 55
02H69
- 65 -
-------
Mill: Keyes Fibre Co. Location: Shawmul
Percent of the
2IS. Line 112 Total Production
(a) Below 40
(b) 40-45
(c) 45-50
(d) 50-55
(e) Above 55
Percent of the
219' Line #3^ Total Production
(a) Below 40
(b) iO-45
(c) 45-50
(d) 50-55
(e) Above 55
220-226. DELETED - ANSWERED IN PART I
227. Does the mill have a pulp mill spill collection system for floor
. drains?
.(a) Yes
(b) No
(c) Partial
Explanation (if needed)
- 66 -
-------
Keyes Fibre Co, Location: Shawmut
228. If the answer to tbft preceding question is (a), describe the collection
system's function.
(a) Collected and discharged to the sewer at a controlled rate.
(b) Collected and reused in the process
(c) Other (please describe) _ ,
i
229. Prehydrclysate disposal by burning - Only applicable if mill makes J
dissolving kraft. ]
(a) Yes j
]
• (b) No j
(c) To the extent possible S
1
Explanation (if needed) _ 1
C. Kraft and Soda Mills - Brown Stock Washers and Screening - NA
230. If the information is available, indicate the approximate amount of
spills and washdown water from the brown stock washers which goes
to the sewers.
a. Line 1 GPM
b. Line 2 GPM
c. Line 3 GPM
>31-233. DELETED - ANSWERED IN PART I
234. Decker filtrate for vacuum washer showers - Is any decker filtrate
used on the brown stock washer showers?
(a) Yes
(b) No % ' '
(c) To the extent possible
-%
Explanation (if needed) ;
- 67 -
-------
Mill:
Fibre Co.
Location:
Shawmut
235. Give the approximate percent of the total screen room decker filtrate
which is normally sewered.
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-80%
(e) 80-100%
236. Evaporator ccndensates for brown stock washer showers - Is any of
the evaporator condensate reused on the brown stock washer showers?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
237. Close up screen room - Is the decker filtrate used for all of the
dilution on the screens and cleaners? .
(a) Yes
(b) No .„
(c) To the extent possible
Explanation (if needed)
238. Recook screen room rejects - Are screen room rejects normally ex-
cluded from the sewer?
(a) Yes
(b) No
(c) To the extent: possible
Explanation (if needed)
- 68
-------
'•'ill: Keves Kibre Co.
Loc a t ion : Shawmu
Give the norsr.a.1 method of knots disposal,
(a) Sewered
(b) Landfilled
(c) • Reprocessed
(A) Burned
(e) Other (please describe)
Kraft and Soar. Mills - Bleaching - NA
240-248. DELETED - ANSWERED IN PART I
What percent cf the chlorine washer filtrate is reused?
(249)
Bleach Line ?
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-80%
(e) 80-10.0?
(250)
Bleach Line 1(2
(a) 0-20%
(b) 20-40%
(c) 40-60%'
(d) 60-80%
(e) 80-100%
(251)
Bleach Line_
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-80%
(e) 80-100%
52. If any is reused, where is it used and give the approximate amount,
a. Where
b. Usage, G?M
253. What are the typical chlorine residuals in the iiltrates?
Line •/!
Line #2
mg/1
mg/1
Line #3
- 69 -
-------
Mill: Keyes Fibre Co.
Location:
Shawmut
254-256. What percent of the caustic extraction washer filtrate is reused?
(254)
Bleach Line #1
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-80%
(e) 80-100%
(255)
Bleach Line #2
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-80%
(e) 80-100%
(256)
Bleach Line //3
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-80%
(e) 80-100%
257. If it is reused, where is it used and give the approximate amount.
a. Where
b. Usage, GPM
258-260. DELETED - ANSWERED IN PART I
261. Do the materials of construction (washers, pumps, piping and tanks)
in the bleach plant allow for straight counter-current washing?
(a) Yes - .
(b) No
262. White water use on bleach washer showers - Is any excess paper or
pulp machine white water used on the bleach plant washer showers?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
02U74
- 70 -
-------
Mill: Keyes Fibre Co,
Location:
Shawiaut
263. Is the waste acid from C1CL generation normally excluded from the
sewer?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
264. What type of CIO. generation system(s) is used?
(a) Solvay
(b) Mathieson
(c) Hooker or ERCO
(d) Other (please describe)
E. Kraft and Soda Mills - Recovery System - NA
265. Give the percent solids to the evaporators.
a. Set 1 __ % b. Set 2 _ %
7,
c. Set 3
d. Set 4
%
266. Give the percent solids from evaporators.
a. Set 1 % b. Set 2
c. Set 3 %
d. Set 4
267. DELETED - ANSWERED IN PART I
- 71 -
-------
Mill: Keves Fibre Co. Location: Shawmut
268. Is the wsak evaporator boil-out liquor returned to the process? j
l
(a) Yes |
(b) No |
t
(c) To extent possible ,i
• i
Explanation (if needed) j
269. Is strong evaporator boil-out liquor all r-iturned to process?
(a) Yes
(b) No
.(c) To extent possible
\
Explanation (if needed)
270. Does the mill have weak black liquor oxidation?
(a) Yes
(b) No
271. Indicate what is normally done with soap.
(a) Sent to mill's tall oil system
(b) Marketed commercially
(c) Sewered
(d) Burned
(e) Not -applicable
- 72 -
-------
Mill: Keyes Fibre Co.
Location:
Shawmut
272. Black liquor storage tank spill collection:
Total Tankage Volume
a.Weak black liquor
b.Strong black liquor
273. Does the mill steam strip condens^te and reuse?
(a) Yes
(b) No
(c) To extent possible
Explanation (if needed)
274. Does the mill have a turpentine recovery system?
(a) Yes
(b) No
275. Is the causticizing area spill collection system returned to process?
(a) Yes
(b) No
(c) To extent possible
Explanation (if needed)
276. Is blow heat condensate used for causticizing make-up?
(a) Yes
(b) No
021577
- 73 -
-------
Mill: Keyes Fibre Co.
Location:
Shawfcut
277. Does the mill utilize a line mud storage pond?
(a) Yes
(b) No
278. Reuse kiln scrubber water - Is the kiln scrubber water reused so that
the lime dust in it: will be recovered, such as at the mud washer?
(a) Yes
(b) No
279. Are green liquor dregs sewered?
(a) Yes
(b) No
280. How many pounds per day of NSSC liquor solids are reused in the kraft
process?
#/day
281. Is semichemical pulp produced using green liquor?
(a) Yes
(b) No
F. Kraft and Soda Mills - Liquid Waste Sources - NA
For questions 282 through 291 please indicate the usual discharge
point for the liquid waste listed. Indicate the answer utilizing one
.of the ^following: -Ja) Evaporator & Burned; (b) Sewered; (c) Reused
(Totally); (d) Reused (Partially); (e) Landfill or Sold.
282. Digester Relief Condensate
283. Blow Condensate
284. Cleaner Rejects
285. Screen Rejects
121478
-------
Mill: Key eg Fibre Co, Location: Shawinut
286. Pump Seal Water
287. Surface Heat Exchanger Coolant
288. Spills £ Washup
289. Stripped (or clean) Condensate
290. Hot Water fron the Economizers
291. Decker Filtrate (screen room)
G. _Sulfira Hills - Pulping Area - NA
292-293. DELETED - ANSWERED IN PART I
294. .What is the fortified cooking liquor total S0??
295. What is the fortified cooking liquor free SO'
296. Give the permanganate, Kappa or ROE number after the red stock washers.
a. Line £1
b. Line £2 .
c. Line v3
297-299. DELETED - ANSWERED IN PART I
300. Does the mill have a pulp mill spill collection system for floor
drains?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
- 75 -
-------
Mill: Keyes Fibre Co.
Location:
301. if the answer to i:hc ^receding question is (a) describe the collection
sys t CT, 3 f unc t ion.
(a) Collected and discharged "to the sewer at a controlled rate
(b) Collected and reused in the process
(c) Other (please describe)
H. Sulfite Mills - Screen ROPE and Washers - NA
302. Decker f ilt-.v-Te for vacuum washer showers - Is any decker filtrate
used on the brown stock washer showers?
(a) Yes
(b) No
303. Give the approximate percent of the total screen room decker filtrate
which is normally severed.
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-80%
(e) 30-100%
304-306. DELETED - ANSWERED..IN PART I
307. .If the information is available, indicate the approximate amount of
spills and washdown water from the red stock washers which goes
to the sewers.
a. Line #1 GPM
b. Line #2 GPM
c. Line #3 GPM
021430,
- 76 -
-------
Mill:
.-Iere -c.
Location:
Shavnnut
308, Evaporator cor.der.sates for brown stock washer showers - Is any of
the evaporator condensate reused on the broxra stock washer showers?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
309. Close up screen roon - Is the decker filtrate used for all of the
dilution on the screens and cleaners?
(a) Ye"s
(b) No
(c) To the extent possible
Explanation (if needed)
310. Recook screen room rejects - Are screen room rejects either recooked
or refined?
(a) Yes
(b) So
(c) Impractical with quality demands
Explanation (if needed)
311. Give the normal method of knots disposal.
(a) Sewered
(b) Landfilled
(c) Reprocessed
(d) Burned
(e) Other (please describe)
- 77 -
-------
Hill: Keves Fibre Cc. Location: Shavrnmt
I. Sulfite Mills - Bleaching - NA
312-317. DELETED - ANSWERED IN PART I
318. Bo the materials of construction (\
-------
„_.,,. Keves ribre Co. T _ •
hill: '•-- -- -LUJ-c: Location:
J. Sulfite Mill - Recovery System - NA
323. DO you have a recovery system? If answer is (a), please answer
questions 324 through _339 ; if (b), omit questions.
(a) Yes (please describe type) r
(b) So
324. Give the percent solids to the evaporators.
a. Line #1 % b. Line #2 %
c. Line -'-'3 Z d. Line 04 %
325. DELETED - ANSWERED IN PART I
326. Does the mill have an evaporator boil-out tank?
(a) Yes
(b) No
327. What is the pH of the spent liquor to the evaporators?
a. Line «1 b- Line #2
c. Line ?;3 d- Line
328. Does the mill neutralize its spent liquor prior to evaporation?
a. Line *1 (a) Yes (b) No
b. Line #2 (a) Yes (b) No
c. Line #3 (a) Yes (b) No
d. Line £4 (a) Yes (b) No
021583
- 79 -
-------
Mill: Keyes Fibre Co..
Location:
329. Does the strong-boil-out go to the weak liquor tank?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
330. What happens to the weak boil-out liquor?
(a) Recovered
(b) Sewered
331. Acid condensate holding tank for sulfite evaporator boil-out - Is
the acid condensate collected and stored to be used for evaporator
boil-outs?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
332. Waste liquor storage tank spill collection:
Total tankage volume
a. Weak waste liquor
b. Strong waste liquor
333. Does the rail! steam strip condensate and reuse?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
- 80 -
-------
Mill: Keyes Fibre Go. Location: Shawraut
334. Give the following flows to the sewer:
a* Digester Blow Condensate
b. From evaporator system including
the ejector intercondenser and
the surface condenser
335. What percentage of the spent liquor is recovered?
336. is any of the spent liquor sold?
(a) Yes - indicate percentage
(b) No
337. if the answer to the preceding question is "Yes", what is done with
the sold liquor?
(a) Road binder
(b) Cattle feed
(c) Linoleum paste
(d) Other (please describe)
338. Are any by-products manufactured from the spent liquor by the mill?
(a) Yes
(b) No
- 81 -
-------
Mill:
Key BE Fibre Co.
Location:
Shawmui
339. if the snnwer to the preceding question is (a), iru'icate wh.it the
by-products are.
(a) Yeast
. (b) Vanilla
(c) Alcohol
(d) Other (please describe)
K. Sulfite Mills - Liquid Waste Sources - NA
For questions 340 through 352 t please indicate the usual discharge
point for the liquid waste listed. Indicate the answer utilizing one
of the following answers: (a) Evaporated & Burned; (b) Sewered:
(c) Reused (Totally); (d) Reused (Partially); (e) Landfill or Sold.
340. Digester Vent Condensate
341. Blow Vent Condensate
342. Blow Liquor
343. Spent Liquor from Digester Extract
344. Chipwashing or Steaming
345. Cleaner Rejects
346. Screen Rejects
347. Pump Seal Water
348. Surface Heat Exchanger Coolant
349. Spills and Wnshup
350. Stripped (or clean) Condensate
351. Hot Water from the Economizers
352. Decker Filtrate (screen room)
L. Groundwood Mills - Pulping Area
353. DELETED - ANSWERED IN PART I
021'Sfi
- 82 -
-------
Mill:
Fibre C°'
Location:
Shawmut
35, ,oes «. -U
(a) ?es
(b) No
@ To the extent possible
Explanation (if needed)
-11 .PU1 coupon
Uoo,
355.
If the answer to the preceding question is (a), describe the collection
system's function.
(a) Collected and discharged to the sewer at a controlled rate
/b) Collected and reused in the process
(c) Other (please describe) _
356.
357.
Glve the
which is normally sewered
(a) 0-20%
(b) 20-40%
40-60%
60-80%
(e) 80-100%
UP „
dilution on the screens and cleaners.
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed) _
021487
- 83 -
-------
Keves Fibre Co.
Location: Shawnut
M. Grcundwqod Mills - Bleaching
358. DELETED - ANSWERED IN PART I
359. Is neutralization used after bleaching?
(a) Yes
(b) No
360. is washing or thickening used after bleach?
(a) Yes
(b) No
361. Give the quantity of bleach used per ton of pulp.
212.6 ibs. __
362. Give the brightness gain.
•°7 __ points/lb. bleach/ ton 14
points
N. Groundwood Mill •- LiquidWaste Sources
For questions 363 through 371 t please indicate the usual discharge
point for the liquid water listed. Indicate the answer utilizing.one
of the following answers: (a) Evaporator & Burned; (b) Sewered;
(c) Reused (totally); (d) Reused (partially); (e) Landfill or Sold.
363. Grinder and/or Refiner Cooling
364. Chipwashing - NA
365. Pump Seal Water
366. Spills and Washups
367. Hot Water from the Economizers -
368. Decker Filtrate
02U88
- 84 -
-------
.•till:
Location: Shawmut
a
-•">• Cleaner Rejects _
370. Bull Screen Rejects _
371. Final Screen Rejects _
0. NSSC, CMP and IMP Mills - Pulping Area - KA
272. What is the NSSC cooking liquor composition?
__ Ibs/gal
__ Ibs/gal
a. Na2C03
Na SO
373. How raany gallons of cooking liquor per ton of pulp?
gallons
374. What is the pressure, temperature and retention time in the digester^
a. \ psi
°F or °C (indicate one)
hours
b.
c.
375. Indicate the type of digester used.
(a) Batch
(b) M & D
(c) Other Continuous
(d) Other Systems (please describe)
3T5. Are any cooking additives (penetran::.?) used?
(a) Yes
(b) No
377. DELETED - ANSWERED IX PART I
021589
- 85 -
-------
Mill: Keyes Fibre Co.
Location: Shavrmut
378.
Does the mill have a pulp mill spill collection system for floor drains?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
379.
If the' answer to the preceding question is (a), describe the collec-
tion system's function.
(a) Collected and discharged to the sewer at a controlled rate
(b) Collected and reused in the process
(c) Other (please describe)
P.
380.
NSSC, CMP, and TKP Mills - Screens and Washers - NA
Give the type of washer(s) used.
(a) Drum
(b) Screw Press
(c) Other (please describe)
381-383.
381. Line
Indicate the washer(s) efficiency in terms of pounds of Na_0 per ton.
Percent of the
Total Production
(a) Below 25 #Na20/Ton
(b) 25-50
(c) 50-75
(d) 75-100
(e) Above 100
02It 90
- 86 -
-------
Keyeg Fibre Co. Location:
Percent of the
382. u.ne //2 Total Production
(a) Below 25 ??Na,0/Ton
(b) 25-50
(c) 50-75
(d) 75-100
(e) Above 100
Percent of the
383. Line ??3 Total Production
(a) Below 25 ;;Na,C/Ton
(b) 25-50
(c) 50-75
(d) 75-100
(e) Above 100
384. Give the approximate percent of the total screen room decker filtrate
which is normally sewered.
(a) 0-20%
(b) 20-iC%
(c) 40-60%
(d) 60-50%
(e) 80-100%
385. Decker filtrate for vacuum washer showers - Is any decker filtrate
used on the brcvn stock washer showers?
(a) Yes
(b) N'o
(c) To the extent possible
Explanation (if needed)
92U91
- 87 -
-------
Mill: Keyes ribre Co.
Location: Shawmut
385, Evaporator condensates for brown stock washer showers - Is any of
the evaporator condensate reused on the brown stock washer showers?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
387.
Close up screen room - Is the decker filtrate used for all of the
dilution on the screens and cleaners?
(a) Yes
(b) No
(c) To the extent possible
E:rpl.3.r-2tinr. (if needed)
388.
Recook screen roon rejects - Are screen room rejects either recooked
or refined?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
389.
Give the normal nethod of knots disposal.
(a) Sewered
(b) Landfilled
(c) Reprocessed
(d) Burned
(e) Other (please describe)
Q. :;SSC, CMP, and TA? Mills - Bleaching - NA
390-392. DELETED - ANSWERED IN PART I
021432
- 88 -
-------
Mill:
Keyes Fibre Co.
Location:
Shawmut
393-395.
393.
394.
395.
396.
Give the type of bleach plant washing.
Bleach Line #1
(a) Single stage
(b) Multi-stage co-current
(c) None
(d) Other (please describe)
Bleach Line #2
(a) Single Stage
(b) Multi-stage co-current
(c) None
(d) Other (please describe)
Bleach Line#3
(a) Single Stage
(b) Multi-stage co-current
(c) None
(d) Other (please describe)
White water use on bleach washer showers - Is any excess paper or
pulp machine white water used on the bleach plant washer showers?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
021/193
- 89 -
-------
Mill: Keyes Fibre Co. Location: Shawmut
397. Is any of the chlorination washer filtrate reused?
a. Line //I b. Line #2 c. Line #3
(a) Yes (a) Yes (a) Yes
(b) No (b) No (b) No
R. _NS_SC and CMP - Recovery System - NA
398. DELETED - ANSWERED IN PART I
399. Give the percent solids to the evaporators.
a. Line #1 %
b. Line #2 __%
c. Line #3 %
400. Give the percent solids from evaporators.
a. Line #1 %
b. Line $2 %
c. Line //3 %
401. Give the type of condenser used.
(a) Barometric
(b) Surface
(c) Both (please give the number of each type)
402. Does the mill have a recovery area spill collection system?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed) '
021494
- 90 -
-------
Mill: K.eygg_.ffibge Co.
403.
Location: Shawmut
Is evaporator condensate used for liquor make-up?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
404. Is the brown liquor filtered prior to evaporation?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
405. Does the mill have an evaporator boil-out tank?
(a) Yes
(b) No
406. Does the strong boil-out go to the weak liquor tank?
(a) Yes
(b) No
407. What happens to the weak boil-out liquor?
(a) Recovered
(b) Sewered
021*95
- 91 -
-------
Mill: Keyes Fibre Co. Location: Shawmut
408. Brown liquor storage tank spill collection:
Total Tankage Volume
a. Weak Brown Liquor
b. Strong Brown Liquor
409. Does the mill steam strip condensate and reuse?
W (a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
410. Give the following flows to the sewer:
a. Digester blow condensate
b. From evaporator system including
the ejector intercondenser and
the surface condenser
S. NSSC, TMP and CMP Mill - Liquid Waste Sources - NA
For questions 411 through 423^, please indicate the usual discharge
point for the liquid waste listed. Indicate the answer utilizing one
of the following answers: (a) Evaporated & Burned; (b) Sewered;
(c) Reused (totally); (d) Reused (partially); (e) Landfill or Sold.
411. Digester Vent Condensate
412. Blow Vent Condensate
413. Blow Liquor
414. Spent Liquor from the Washers
415. Chipwashing or Steaming
416. Cleaner Rejects
- 92 -
-------
Mill: /Ceyes More Co. Location: Sh_a_w.Eiut_
417. Screen Rejects
418. Pump Seal Water
419. Surface Heat Exchanger Coolant
420. spills and Washup
421. stripped (or clean) Condensate
• Hot Water from the Economizers
23. Decker Filtrate (screen room)
422
I. Deink Mills - Pulper Area - NA
424-425. DELETED - ANSWERED IN PART I
427. Does the mill have a pulp mill spill collection system for floor drains?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
428. If the answer to the preceding question is (a), describe the collection
system's function.
(a) Collected and discharged to the sewer at a controlled rate
(b) Collected and reused in the process
(c) Other (please describe)
429. DELETED - ANSWER IN PART I
430. What is the normal pulper temperature?
02H97
- 93 -
-------
Mill: Keyes Fibre Co, Location: Shawmut
U. Deink Mills- Stock Washers andScreening - NA
431. if the information is available, indicate the approximate amount of
spills and washdown water from the deinked stock washers which goes
to the sewers.
a. Line 1 GPM
b. Line 2 GPM
c. Line 3 GPM
432-434. Indicate the type of washers used.
432. Line fll
(a) Screw washers
(b) Side hill washers
(c) Gravity deckers
(d) Vacuum washers
(e) Other (please describe)
433. Line ??2
(a) Screw washers
(b) Side hill washers
(c) Gravity deckers
(d) Vacuum washers
(e) Other (please describe)
434. Line #3
(a) Screw washers
(b) Side hill washers
(c) Gravity deckers
(d) Vacuum washers
(e) Other (please describe)
02K38
- 94 -
-------
Mill: Keyes Fibre Co.
Location:
Shawmut
435.
436.
Counter-current washing for wasfcpaper and deinking - Is counter-current
washing of the stock practiced?
(a) Yes
(b) No
Close up screen room - Is the decker filtrate used for all of the dilution
on the screens and cleaners?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
Recook screen roon rejects - Are screen room rejects either recooked or
refined?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
Give the approximate percent of the total screen room decker filtrate
which is normally sewered.
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-80%
(e) 80-100%
02U99
- 95 -
-------
Mill: Keyas Fibre Cc.
Location:
Shawraut
439. Decker filtrate for vacuum washer showers
on the brown stock washer showers?
(aj Yes. -
(b) No.
(c) Tp-^the^extent possible
Explanation (if needed.)-
- Is any decker filtrate used
V. Deink Mills - Bleaching ' - NA
440^441. •'
442-443.
442.
r
DELETED - ANSWERED IN PART I
Give the type of bleach line washing for the following:
Bleach Line #1
(a) Jump-stage counter-current washing
'(b) Straight counter-cur rent washing
"~ tc)Co-current washing ~'~~ : • "~"~"
443. Bleach Line #2
(a) Jumpr-stage counter-current; washing
(b) Straight counter-current washing
(c) Co-current washing'""
444.
^ on bleach washer showers - Is any excess paoer or pulp
.macfiine white water used on the bleach plant washer showers?
(a) Yes
(b) No •
(c) To the extenfrpossible -—
Explanation (if needed) ^~~'
021500
-------
Mill: Keyes Fibre Cc.
Location:
Shawrr/a-t
445. Do the materials of construction (washers, pumps, piping and tanks)
in the bleach plant allow for straight counter-current washing?
(a) Yes
(b) No
446-447. What percent of the chlorine washer filtrate is reused?
- (446) (447)
Bleach Line //I Bleach Line #2
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-80%
(e) 80-100%
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-80%
(e) 80-100%
448, If any is reused, Xv'here it is used and give the approximate amount,
a. Where
b. Usage, GPM
449. What is the chlorine residual in the filtrate?
mg/1
W. Deink Mills - Liquid Waste Sources - NA
For questions 450 through 462 please indicate the usual discharge
point for the liquid waste listed. Indicate the answer utilizing one
of the following answers: (a) Evaporated & Burned; (b) Sewered;
(c) Reused (totally); (d) Reused (partially); (e) Landfill or Sold.
450. Digester Vent Condensate
451. Blow Vent Condensate
452. Blow Liquor
453. Spent Liquor from the Washers
454. Chipwashing or Steaming
- 97 -
-------
Mill: Keyes Fibre Co. Location: Shswsiui
455. Cleaner Rejects
456. Screen Rejects
457. pump Seal Water
458. Surface Heat Exchanger Coolant
459. Spills and Washup
460. Stripped (or clean) Condensate
461. Hot Water from the Economizers
462. Decker Filtrate (screen room)
X. Paperboard from Wastepaper__-_ Pulper Area - NA
463-465. DELETED - ANSWERED IN PART I
466. Does the mill have a pulper area spill collection system for floor drains?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
467. if the answer to the preceding question is (a), describe the collection
system's function.
(a) Collected and discharged to the sewer at a controlled rate
(b) Collected and reused in the process
(c) Other (please describe)
021502
- 98 -
-------
Mill:
"•'eyes Fibre Co.
Location:
Shawmut
Y. Paperboard from Vastepaper — Washers and Screens. - NA
468. If the information is available, indicate the approximate amount of
spills .and washdown water from the thickeners which goes to the sewers.
a. Line 1
b. Line 2
c. Line 3
GPM
GPM
GPM
469. Give the approximate percent of the total screen room decker filtrate
which is normally sewered.
(a) 0-20%
(b) 20-40% '
(c) 40-60%
(d) 60-80%
(e) 80-100%
Z. Paperboard from Wastepaper - Liquid Waste Sources - NA
For questions 470 through _47S please indicate the usual discharge
point for the liquid waste listed. Indicate the answer utilizing one
of the following answers: (a) Evaporated & Burned; (b) Sewered;
(c) Reused (totally); (d) Reused (partially); (e) Landfill or Sold.
470. Cleaner Rejects
471. Screen Rejects
472. Pump Seal Water
473. Spills and Washup
474. Hot 'water from the Economizers
475. Decker Filtrate (screen room)
021503
99
-------
Mill: Keyes Fibre Cc. Location:
A-l. Buildv'.rs Paper - Stock Preparation - NA
476 • DELETED - ANSWERED IN PART I
477. if digester is used, indicate whether water or steam is used for cooking.
(a) Water
(b) Steam j
478. if water is used, indicate the source and approximate amount.
a< Fresh Water _ gallons per day.
b- Recycled Water _ gallons per day.
. Are any chemicals used in this digester process?
(a) Yes
(b) No
480. List the approximate tons/day of rejects from the attrition mill (refiner)
_ tons /day
481. HOW and where are rejects handled or disposed of?
482. por other fiber sources used, indicate the preparation process used
prior to the blending chest. (Cutting and shredding, beater tank, etc.)
a. Rags
b. Wastepaper
c. Other
021504
- 100 -
-------
Mill: -"'eves :'ibre Co.
Location: Shgwmut
433.
For each of the preparation processes used, indicate the source and
aizount of water used (i.e., fresh water, white water, etc.)
Source of Water Amount (gal/day)
a.
b.
Rags
wastepaper
Other
484. Please give the source and amount of water used at the refiners.
485. List the approximate tons/day of rejects resulting from the stock pre-
paration process(es) used. (Attrition Mill and/or Pulper)
tons/day
tons/day
tons/day
486. How and where are rejects handled or disposed of?
487.
Please fill in the following information on the rifflers and/or
screening after the blending chest.
Rejects Method of Rejects
(tons/c'ay_) Handling and Disposal
a.
b.
Rifflers
bereens
021505
- 101 -
-------
'Mill: Keyes Fibre Co. Location: Shawmut
No paper mill.
o paper m.
B-l. Paper Mill - (All mills except Builders Paper. Builders Paper mills
go to Item C-l) _ NA
go to Item C-l)
488-490. DELETED - ANSWERED IN PART I
491. Is felt vacuum pump water reused?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
492. Does the mill have a stock spill collection system?
(a) Yes
(b) No
(c) Partial
493. if the ansv/er to the preceding question is (a), describe the collection
system's function.
(a) Collected and discharged to the sewer at a controlled rate
(b) Collected and reused in the process
(c) Other (please describe)
494. Give the frequency of waste significant grade changes; also, if
possible, give the stock quantity sewered.
021506
- 102 -
-------
Mill: Keyes Fibre Co,
Location: Shawmut
495. Is the mill central storage of white water (a) and slush broke (b)
adequate with regard to effluent discharge?
a. White Water
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
b. Slush Broke
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
496. Are special provisions made for spills, screen rejects, and excess
materials from coating or sizing systems?
(a) Yes
(b) No
(c) L invited
497. Does the raill employ organic solvent coating/saturating operations?
(a) Yes
(b) No
498. If yes, please give the type and quantities (Ibs/day) of organic
solvent used.
021507
- 103 -
-------
Location:
Shawmut
Mill: Keyes Fibre Co.
daily organic solvent coated/saturated paper produced.
tons/day
499. Give the average
500. Please indicate effluent from the combined papermaking facilities
as follows: (i.e., total flow from all machines).
Waste Source
a. Centricleaner and machine
screen rejects
b. Couch pit, seal box, and any
other unclarified white water
overflows
c. Thick stock spills, dumps,
washups from stock prep, area
and machine
d. Excess clarified white water
e. Cloudy water from vacuum
systems, or pump sealing
applications
f. Clear water discharges - i.e.
cooling services, condensate,
other non-process services
Other effluent sources - Not
included above.
Total papermill effluent
Volume
GFM
Suspended Solids
(if applicable)
Ibs/dav
gal/day
g-
h.
i.
501.
» •v •— fc 4
Is (f) discharged via process sewer or separately (circle answer)?
(a) Yes
(b) No
White water showers - Are white water showers used on the paper machines
for such purposes as wire cleaning or knock off showers?
(a) *:es
(b) Ko
(c) To the extent possible
Explanation (if needed
- 104 -
-------
Ky/eg Fibre Cc. Location: Shawmut
502. Reuse press effluent - is the press effluent reuses in the taper mill"
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
503. White water for vacuum pump sealing - Is white water used for vacuum
pump sealing?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
504-505. DELETED - ANSWERED IN PART I
506. White water storage for upsets and pulper dilution - Is excess white
water, overflows from the main white water tank or the cloudy side
of the sriveall saved in a white water storage tank of sufficient size
for charging and dilution at the pulpers?
(a) Yes
(b) No
(c.) To the extent possible
Rvplarstion (If needed)
507. Does true mill have either four stages of cleaning or three stages of
cleaning with elutriation in the paper mill?
(a) Yes ' ^
(b) No
021509
- 105 -
-------
Mill: Keyes Fibre Co.
C-l BuildersPaper - Paper Mill - NA
508. DELETED - ANSWERED IN PART I
509. Give the number of savealls used.
Location: Shawmut
510. Provide the following water use information:
Process Water Source Amount of Water
a. Stock Dilution
b. Wet End Showers
(including felt cleaning showers)
511. Are low volume showers used?
(a) Yes
(b) No
512. Average daily discharge of white water from wet end area (forming
section.).
MGD
513.
Fill in the following information on the white water:
White water recycled:
a. Recycled To Amount
MGD
MGD
MGD
White water sewered
MGD
021510
- 106 -
-------
Mill:
Location:
D-l 5ulId-ors Paper - Saturating and Coating (if applicable) - NA
Include the saturating and coating process, specifically the number
of stations, what raw materials are used and where (i.e. asphalt, talc
etc.)> and the amount and location of cooling water used on the
schematic requested in Item 3, Section VIII.
DELETED - ANSWERED IN PART I
515. ^re iow volume cooling water showers in use on the saturating and
coating process?
(a) Yes
(b) No
516. 1= any of this cooling water reused?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
517. Give the amount of cooling water reused and the amount sexfered.
a. Reused MGD
b. Severed MGD
E-l Byilders_ Paper - Internal Controls - -f
-------
Mill: .-.eyes ribre Co. Location:
519. if "Yes" indicate the amount of water recycled.
a- Process pumps packing gland
b- Vacuum pump seal water
520. is a spill control system used?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
521. If "Yes", what process areas are handled by the spill collection system?
522. Which of the following is true of the mill's spill collection system
procedure? j
I
(a) Water recycled 't
I
(b) Water gradually discharged to treatment j
;
(c) Water treated separately
(d) Other (please describe)
523. Describe any other internal controls which are being used to decrease
the water and/or reduce the wastewater pollution load.
- 108 -
-------
Mill: Keyes Fibre Co.
Location: Shawmut
F-l Additional Information (All Mills)
524. Does the mill have a program for disposal of old electrical trans-
formers?
(a) Yes
-------
Mill: Keyes Fibre Cc.
Location:
V. WATER USAGE AND EFFLUENT TREATMENT PRACTICES
Instructionsfor Completing Section V
Section V requests information on the mill's wastewater treatment practices.
In Section VIII a general schematic of the effluent treatment system is
requested. You have the option of providing any of the data requested in
Section V on the schematic. If you do this, please indicate on the
question(s) involved that the data is presented on the schematic.
A. Water Usage
526. Indicate the source and amount of process water.
(a) Surface (i.e., river, lake or reservoir)
(b) Groundvater
(c) Other (please describe)
MGD
MGD
MGD
527. Does the quality of the raw water limit the reuse of water in this mill?
(a) Yes - explain
@ No
528. Indicate the source and amount of the mill's cooling water.
(a) Surface . 850 MGD
(b) Groundwater MGD
(c) Other (please describe) MGD
529. Indicate the source and amount of the mill's boiler feed water.
(a) Surface MGD
(b) Groundwater MGD
(c) Other (please describe) Water District .QQ1 MGD
021514
- 110 -
-------
-Mill: eyer: rlbre C:. Location: Shawmut
530. Describe treatment used for boiler feed water conditioning.
Treat for phosphate, alkalinity, sulphide and pH with Betz solut ion.
Q# Polygperse, 5r adjunct, J? Caustic. 10#
(3. day treatment)
531. Give the disposal method now employed for boiler blowdown water.
^a) Severed to treatment plant
(b) Directly discharged
(c) Directly discharged with pH adjustment
(d) Directly discharged after cooling
(e) Other (please describe) _
B. Background Data
532-533. DELETED - ANSWERED IN PART I
534. How is cooling vater disposed?
^a) Separate discharge to receiving stream.
(b) Combined with process waters before treatment.
(c) Combined with treated process waters.
(d) Recycled.
C. Indirect Discharger please provide the following information:
535. Name and location of POTW which handles your wastewater.
ftz. • J'-
cL.. Waterville _
536-537. DELETED - ANSWERED IN PART I
538. Are there specific pretreatnent requirements or limits upon pollutant
parameters L-apcs-Dd by the POTW system to which you discharge?
Qy Yes
(b) No
021515
- Ill -
-------
Mill: Kg/es Fibre Co. .__ Location: Ehawmut
539. if the answer to the preceding question was (a), please list the specific
pretreatment requirements or pollutant parameter linits- imposed on your
mill by the POTW. Shawmut and Waterville limits combined.
3,000,000 GPD
4,000# BOD Daily
3,000# SS Daily
540. DELETED - ANSWERED IN PART I
541. if neutralization is practiced, fill in the following. _ NA
Chemical used ^
542. DELETED - ANSWERED IN PART I - NA
543. Are any chemicals or other settling aids added to the primary treatment
units? - KA
(a) Yes
(b) No
(c) To the extent necessary (intermittent)
544. Please show the wastewater streams which enter the secondary treatment
system (if applicable). - NA
Process Source or Sever .No.* Flow, MGD BOD, Ib/D TSS, Ib/B
8- Design Values Average Day
Maximum Day
Maximum Month
b. Primary Treatment Effluent Avei'age Day
Maximum Day
Maximum Month
c. Average Day
Maximum Day
Maximum Month
"Process source or sewer number should be keyed to the mill process and
wastewater treatment schematics reflU£%fad^in Section VIII.
- 112 -
-------
Mill: Ke^e£ Fibre Co- Location: Shawnut
545. Give the normal pH of the wastewater at the influent to the secondary
treatment system. - NA
(a) 4-6
(b) 6-8
(c) 8-10
546. DELETED - ANSWERED IN PART I - NA
D. Direct Discharger please provide the following information: - HA
547. Narae of the effluent discharge receiving water
548. Enclose a ccpy of current or proposed NPDES effluent discharge limits.
549. DELETED - ANSWERED IN PART I
550. if wastewater discharge is seasonal or intermittant non-continuous,
approximately how many days out of the year do you discharge to the
receiving water.
(a) Less- than 30 (f) 211-240
(b) 31-90 (g) 241-270
(c) 91-120 (h)' 271-300
(d) 121-180 (i) 301-330
(e) 181-121 (j) 331-360
E. Preliminary Treatment - NA
551. DELETED - ANSWERED IN PART I
552. if neutralization is practiced, fill in the following:
Chemical used
821517
- 113 -
-------
Mill: Keyes FVtre Co.
Location: Shsw-nui
F. Primary Treatment - NA
553. DELETED - ANSWERED IN PART I
554. Are any chemicals or other settling aids added to the primary treatment
units?
(a) Yes
(b) No
(c) To the extent necessary (intermittent).
G. Biological Treatment^ - NA
555. Provide the following information for the biological treatment system
(if applicable).
Process Source or Sever No.* Floj?, MGD BOD, Ib/D TSS, Ib/P
a. Design Influent Values Average Day
Maximum pay
Maximum Month
b. Primary Treatment Effluent Average Day
Maximum Day
Maximum Month
Other Uastewater Streams Which Enter the Biological Treatment Systems
Without Primary Treatment
c. Average Day
Maximum Day
Maximum Month
d. _ Average Day
Maximum Day
Maximum Month
•'•Process source or sewer number should be keyed to the mill process and
wastewater treatment schematics requested in Section VIII.
- 114 -
-------
Mill: Keyes ribre Co,
Location:
Shawmu
556.
Give the normal pH of the wastewater at the influent to the secondary
treatment system.
(a) 4-6
(b) 6-8
(c) 8-10
557. DELETED - ANSWERED IN PART I
H. Secondary Solids Removal - NA
558-559. DELETED - ANSWERED IN PART I
I. Spray Irrigation - NA
560. Is treated wastewater used for irrigation?
(a) Yes
(b) No
(c) Partial
3' Sludge Handling and Disposal _ KA
561. DELETED - ANSWERED IN PART I -
562. Give the percent solids of the sludge after dewatering and prior to
disposal,
(a) 5-10%
(b) 10-20%
(c) 20-30%
(d) 30-40%
(e) above 40%
563. Describe any leachate management practices performed at the mill for
sludges which are disposed of on land.
021D19
- 115 -
-------
Mill: Keyes Fibre Co.
Location: Shaw-nut
K.
564.
Foam Control - (Wastewater treatment system only)
Does the mill use foam control measures?
(a) Chemical
(b) Physical Methods
(c) None
(d) Other - explain
- NA
921520
- 116 -
-------
Mill: Keyes Fibre Co.
Location:
L. Cost Information
565. Provide cost data indicated for effluent treatment system in 1976 dollars,
Use the cost multiplier factors, which follow, to convert to 1976 dollars,
Annual Operation
Total Capital Cost and Maintenance Cost*
Z-SV'f- 1 •'.< JT
a. Internal control devoted to $230,232 $5,000
effluent waste load reduction.
b. External Treatment System
c. Primary Treatment
d. Secondary Treatment
Construction Cost Multipliers
1956
1957
1958
1959
1960
1961
1962
=2
=
=
=
™
—E
=
o
^
2
2
2
2
2
2
to Convert
.535
.380
.325
.254
.220
.220
.207
Capital
1963
1964
1965
1966
1967
1968
Cost
_
=
=
=
=
=
to 1976
2.186
2.161
2.124
2.051
1.978
1.884
Dollars
1969 -
1970 =
1971 =
1972 =
1973 =
1974 = -
1975 -
1
1
1
1
1
1
1
.794
.689
.564
.485
.317
.242
.100
*Factors to be considered in Annual Operation and Maintenance Costs
(0 & M Costs).
1, Manpower - both operators and maintenance personnel
2. Contracted services
3. Energy Cost
4. Trucks for hauling
5. Nutrients
6. Leased equipment
7. Disposal costs
8. Sludge handling
9. Sampling and analysis
10. Equipment replacement (except major capital)
Exclude Depreciation
021S21
- 117 -
-------
Mill:
Keyes Fibre Co.
Location:
Shawnut
566. por mills which discharge to a PCTW, please give the annual user fee
with a breakdown for capital cost recovery and operation and maintenance
costs.
a- Capital Cost Recovery(if available)
b. Operation and Maintenance (if available)__
c. Total Annual User Fee 19?8 Projected
121,58?
12 i.
567. Please give the basis used by the POTW to determine the mill's user
fee.
(a) Flow only
(b) BOD only
(c) TSS only
(d) Combination of parameters (please indicate)
(e) Unknown
Flow $lll.lo/m.g.
BOD 54.06/ton
S3 56.63/ton
60% Flow 20% BOD 20J8 SS
t>0 2-3 2- d
M. Site Conditions and Availability of Land
563. is there sufficient land for expansion of your wastewater treatment
system for BATEA?
(a) Yes
(b) No
(c) Unknown
569. Can the rail! purchase land from adjoining property owners for possible
expansion of the vastewater treatment system?
(a) Yes
(b) No
(c) Unknown
•21522
- 118 -
-------
Mill: Keyes Fibre Co- • Location: Shawmut
570. Are the soil conditions in the land available for future expansion of j
such a quality as to require special construction methods or special j
facility equipment (i.e., ledge, water table and liners needed for K
basins)?
(a) Yes
(b) No
(c) Unknown
571. Miscellaneous Discharges - Indicate any wastewater discharges not
described in Section V which do not flow to the wastewater treat-
ment system.
N. Was t ewa ter Chara c t e r is t i c s
572-577. DELETED - ANSWERED IN PART I
578. Was the analysis procedure used for BOD measurement in accord with
the method presented in Standard Methods for the Examination of Water
and Wastewater?
(£a) 13th Edition
(b) 14th Edition
(c) No (please describe other method used) -
579. Is a glucose-glutamic acid BOD standard analyzed?
(a) Yes
fb) No
•21523
- 119 -
-------
Mill: Keyes ricre Co.
Location:
Shawmut
580. if the answer to the preceding question was (a), please indicate the
normal frequency of the analysis.
(a) Daily
(b) Weekly
(c) Monthly
(d) Quarterly
(e) Semi-annual
581. Please indicate the percent difference found between the BOD determinations
and the glucose-glutaraic acid BOD standard
(a) 0-5%
(b) 5-10%
(c) 10-15%
(d) 15-20%
(e) Over 20
582. Indicate the analysis procedure used for TSS determination at the mill.
(a) Standard Methods for the Examination of Water and Wastewater.
13th and/or 14th Edition.
(b) EPA analysis procedure adopted on October 16, 1973, and any
subsequent amendments.
(c) Other (please describe) Std. Methods Procedure
Exception: Paper substituted for fiberglass filter paper.
021524
- 120 -
-------
Mills Keyes Fibre Co.
Location:
Shawmut
VI. FUEL AND ENERGY
A copy of the API "Monthly Fuel and Energy Report" has been included in
this section to assist the mill in calculating (if information is not
already available) the answer(s) to the questions asked. The API sheets
should be used as a guide for computation only, do not return the pages
with the questionnaire. Por internal treatment energy cost calculations,
include only the following:
1. Equivalent steam (MBTU/Ton product) required to evaporate
reclaimed spilled pulping liquors from the average solids
level at which dumped up to a 10% solids level,
2. Also include steam (MBTU/Ton product) required in condensate
stripping operations necessitated by condensate reuse projects.
^ *^
583. Give the total purchased energy (fossil fuel, electricity, steam,
etc.) as equivalent millions BTU/ton of product (Items 1 to 9, less 10
from API forms).
584. Give the energy used for external treatment operations in KW Hr/Ton
of product.
585. Give the energy used for Internal treatment as equivalent millions
BTU/toh of product.
VII. PRIORITY POLLUTANTS
DELETED - ANSWERED IN PART I
021525
- 121 -
-------
Mill: Keyes Fibre Co.
Location:
Shawn-jut
VIII. PROCESS SCHEMATICS
Attach separate general block diagrams for the three items listed below.
A. Water Treatment (if applicable) - Provide a general block diagram
showing the water treatment system used, chemical application points,
average flow, and disposal method for backwash water. If the mill has
a raw water analysis available please attach a copy.
B. Manufacturing Process Schematic - Provide a general schematic of
the total mill process to include water balance and all process
wastewater streams. (See note at start of Section V.) Wastewater
streams should be cross referenced to the effluent treatment system
schematic.
C. . Effluent Treatment System - Provide a general schematic of the
effluent treatment system. Please key the diagram to the manufacturing
process block diagram so that the point of influent to the treatment
system for individual process sewers can be determined. Also show
all chemical application points; chemicals used; flow monitoring and
sampling points; average flow; size or area, volume, and number of
each treatment system component; sludge recycle and volume; and
sludge dewatering/thickening system.
Additional information on the mill's wastewater treatment system is
also needed to complete the data request. Please provide answers to
the following questions which pertain to your wastewater treatment
system. For questions which do not apply, indicate by writing N/A
(not applicable) on the space provided for the answer.
Primary Treatment
586. Give the following primary clarifier overflow rates: - NA
a. Design gpd/f t2 at MGD
b. Current gpd/f t2 at MGD
02152*
- 122 -
-------
Keyes Fibre Co.
Location: Shawmut
Biological System
For the biological system employed, please give answers to the appropriate
questions listed below:
System
Question
Answer
587. Aerated Stabilization a) Volume of the aeration zone
Basin
HA
Mil. Gal.
588. Activated Sludge
b) Connected horsepower for aeration _
a) Volume of the aeration zone NA
b) Connected horsepower for aeration
c) MLSS (Mixed Liquor Suspended
Solids)
Mil. Gal.
589. Trickling Filer
590. RBC
591 Post Storage
a) Volume of media
b) Surface area of filter
a) Surface area of RBC
a) Volume of storage
NA
NA
NA
ft2
Mil. Gal.
592 If nutrient addition is used, please give the average BOD:N:P ratio. - NA
BOD:N:P . :_:__
Secondary Solids Removal
593.
Give the secondary clarifier overflow rates: ,- NA
a. Design _
b. Current
gpd/ft* at
gpd/ft2 at
MGD
MGD
021527
- 123 -
-------
PART II
>ues=ioa Question
Number
Question
Number^
Question
Number^
Question
Number_
Question
Number^
Questiq
NutnbeJ
021528
- 124 -
-------
*.":*>:•<< PAPER INSTITUTE
t*» . » • HUUS AND ENERGY
Z-". •=!• .«>" *••«»«, N«~ York, M.Y. I-JO'4
CONFIDENTIAL I
MONTHLY FUEL AND ENERGY REPORT!
•to.-nh, Year:
is
-ns.-iod" mi i I . the
repcr:ec -s from
_ . ) mo./Oay
Company:_
Hill Location:
Hill Reference NO.:.
Region:
FOR API
USE ONLY
\ HorthKF.»t • ind Energy Ce~sumpt ion Data
For eacn trij.-jy source used in the month, please enter to the nearest tenth information in
•:.-.e way yo-.- rcr -.sr (t most accurately. For example, in the case of fuel oil, you would pro-
.530ly enter :r.::;:;,inds of barrels. But in the case of bark, you would probably enter Billion
ITu's as fire;—:i:tained by aaalying the bark boiler's rated or estimated efficiency to its
re cere; s'ean :i.-:^ut. Then apaty tne 8TU conversion factor you believe to be most accurate
-or VC-.T as-f. :<•< to compute either Billions of BTU's as in the first case, or weight of
•-•«! a: tn« 53c:'.-'ied moisture content as in the second case. (See list of average BTU
-•siues of -ocir.j:»a fuels, over.) Limit reporting to energy used within the mill fence line,
;:i«reby ext'r-ci": energy used in wood harvesting, transportation and converting operations.
ACTUAL CONVERSION
-.'•::. UNITS OSE FACTOR
-•:.-cne)
Thousands Gal Ions
Hill ions Cu. ft.
BILLION
BTU's as
FIRED
X ).k m
X
X
X -
X .
X .
X .
X
X -
_ *
Sy? TCTi(, i (1 to q le« 10;) •••.••• ••
.si? aenera:»c «:••: Waste Fuels
. Hogge; rut- \<~ood & Bark)
;.. Bar*: \ir-f separately, if
availa; e. :•!-< obtained in
-. ,u,;ci;,« *m.
Thous. Short Tons '
(50% moisture
content)
Thous. Short Tons
(50* moisture
content)
Thous. Short Tons
(50% moisture
content)
i Thousands Short
:-. Ssent U'c-'T- even dry basis) I Tons of Solids
. 3elf-Gs •.€.-*: a:
:-.. Otner •'«;-*: '•!
- Otner ^S,ec •'-.
Mi tl ions KWH
X
X
X
X
X 3.** -
X .
X
•-• luVAL - ' : . .3 17); "-
— ft91:"flQ
-i.ui T-Ti. -• i.oO; VwlaJ'/jtl
Tr:j'. i- : j'i.: Electric Generation: Million HWH
I (Cat :_';*•! ;-?aarg£sLy fron above
totals)
-------
: • ! - "p" t h I y P roc ue_*. -on UUP t a
r lease enter sr-ttfuct ion for tr.e wrjr>th in Uousgnds of short tons, to the negrevt tenth.
"iMs which use 1x3'.- their own and purchased pulp will enter separate data for "Integrated
ssosr ar«d Paperboar -•' ard "Sen integrated Paper arvd Paperboard."
!. Pulp (dried 8«d wet lap): Report dried and wet lap pulp (reported on a dried basis).
2. integrated Paper ang Paperbftard: Report primary product (excluding converted products)
manufactures from on-site pulp production, as normally measured.
3. *oni integrated 3aper arxt Paper board: Report primary product (excluding converted products)
manufactured fron off-site pulp production and/or waste paper, as normally measured.
1.
'z.
3.
H.
iTTi
(thousand short tons)
Pulp (dried »r4 wet lap on dried basis):
Integrated Paper (• Papcrboard:
ton integrated '^per (• Paperboard:_
TOTAL PRODUCT IOW [3:
Please compute atllions of STU's used per ton of output for both "Subtotal BTU's frcxa
fossil r-jtl arvj Energy" and "Grand Total BTU's."
Purchased E^e-'-y Per Ton
Total £3
mi 11 ion BTU's/ton
Total Energy -*.- Ton
S'i-<1 Total
Tcial 13:
mi I 1 ion BTU's/ton
Explanation o* ?wnth to nxsnth chervges in energy use:
!) If the rrJif's energy use per unit of output (either purchased and/or total) for
this :^ «6rtesr.ue
New York, N.>. 10016
Tei. (212) E55-8087
.'•a
Name:
Signature:
Telephone: {_
Date:
021530
-------
COWR BY
/^ V\» v -•
CHK. BY
JOB NO.
DATE
Average Tons/Day:
Check file for updated data:
Wastewater
Flow, Kgal
- BOD, Ib ••--
TS3, Ib
• Check Schematics:
Raw
Per Day Per Ton
Final
Per Day Per Ton
r° *
cnnn OQ.OI REV. 12/79
021531
C. Jordan Co., 1"«-
-------
fi
si
LARGE SIZE PROCESS SCHEMATICS ARE AVAILABLE IN THE
FILE CONTAINING THE ORIGINAL 308 SURVEY RESPONSES
FOR THE FOLLOWING FACILITY:
NAME:
LOCATION:
021532
-------
^1
(K
UK!!U-:DSTA7CG ilf.'ySHOt-JMENTAL PHOTI-CliO,1,1 AGENCY
KLGion i
i,f. Kv;!^:!;3.' FEL::RAL r.uiuwjG, uosici-j, MASGACtu/r-eirs.02203
JUNE 20, 1977
KEYES FIBER COMPANY •
ATTN C F BEAN', NCR PROCESS ENG
COLLEGE AVENUE
WATERVILLE MAINE 0490J
GentlemRn:
'•i,'i-
rtc~
SCEIVED:
5l—P JUW 22 JS77
KEYETFIBRTCO"
f* f. I .'X 1 . . *^*-f.
RE: KPDHS Permit No. ME0000337 & ME0000302
Enclosed is the final (or removed) National Pollution Discharge Elitr.ir.acJ.cn
Systcn Permit for thn nbnvr; rofcror.c.od nar.c and serial nunor (-the "parndttec") .
issued purr.iuint to Secuion -0:^ cr the Federal V?.iter I'ollxition Control Act, as
amended, (tho "Act"). Alro cncloncid is a copy of guidelines specifying test
methods published pursuant to Section 30-'> (o) of the Act. As noted in the pcrnit,
the permictce ir, required to utilize these test methods in monitoring its
effluent.
The P-e.gional Administrator has determined . in accordance with 40 CFR 125.35
that tk permit issued is s^Suiniially uncliansefl froa die tentative (JecerRiir
tions and draft permit prepared pursuant to §125.31 (39'Fed. Reg. 143 (1974)).
Within 10 days of the dace of receipt of this; determination you, or any intcreste:
parties, may request an acljudicatory hearing in accordance with the pro%'isions
of §125.36 (b) and (c). - .
LEGAL RESPONSIBILITIES,
This NPDES permit represents a legal contract between your company and
the U.S. Environmental Protection Agency. Please note that you rujst adhere to
any dates of compliance in the implementation schedule, and you nnjn_t_ resort
monitoring results in a timely fashion. If, for any reason, your company does
not comply with or will not he able to comply vita any.dates or effluent
limitations contained in this pernit, you raust so notify the Regional Admin Istrat:
and the State in writing within _ftve_ (5) days of becoming av?are of such condition.
Notification must follow the procedures set out in Part II, Section 2a and b of
this permit. -.
OIL SPILT. R?-c;'THnMr::yrs ' - -
Please note that thin permit does not relieve the permittee from the
responsibility of complLincf. v:it:h fk-ction 311 of the Act. That section prohibits
the discharge of. harmful quantities of oil into the water of the United States
021533
-------
_ *> -.
and re-:t:ir":3 the perscn in-charge of a facility fron vhich an oil spill into
such -.."-veers emanates to immediately notify the appropriate federal'agency. For-..
oil spills into coastal water:.;, the. appropriate federal .agency is the nearest
.Coast Guard station. For oil spills into inland water, the Environmental
Protection Agency (617-223-7265) is the appropriate federal agency. Violations .
of Section 311 are punishable by various civil and criminal penalties specified"
therein.
MO;:ITORI::G AND UFPORTT.NG . .-
All monitoring data is to be reported on the Maine DEP report forms and , . •
submitted on the- schedule they provide.
Reports concerning any implementation dates are to be submitted to both the
Maine DE? and EPA at the addresses in the permit.
Very truly jc
Edv/ard Jf Conley
Cliief, Pernits Branch
Enclosure
021534
-------
•
ft
^^
I .
j •
i
, Permit No. ME0000302
Applicalion No.
AUTHORIZATION TO DISCHARGE UNDER THE : ' •;• . j
NATIONAL 1'OLLliTANT DISCHARGE ELIMINATION SYSTEM
PERMIT MODIFICATION
Jn compliance with the provisions of the Federal Water Pollution Control Act, as amended,
(33 U.S.C. 1253 et.seq;the"Act"),
.•"""—\
the Keyes Fiber Company
(Shavmut Plant) ' . i
.p
i
is authorized to discharge from a facility located at
. ' Shawmut, Maine
to receiving waters named
Kennebec River
!;
! in accordance with effluent limitations, monitoring requirements and other conditions set forth
j j' in Parts I, II, and III hereof.
;• . This pormit shall become effective30 days from the date of signature, replacing
the permit issued on July 21, 1975.
This permit and the authorization to discharge shall expire at midnight, April 30, 1979.
Signed this [/ day of \/M*S
.
Leslie Carothers, Director
Enfprccncnt Division
Envlroninental Protection Agency
021535
« is . ' £f»A Fo.m 3320-4 ()0-73>
-------
PARTI
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l
. i
PART I
iv.mil N>.!'iEGG00302
C. MONTTOrllNG ANT) REl'OKTING
! . P.rprcs>xiatii-3 Sampling
5.L~;-.i!s and measurements taken as required herein shall be representative of the volume
c,-..c ruu:r^ of the monitored discharge.
'or.;:.:r::v;r Moults obtained during the previous 1 monlhjf shall bo summarized for
L:.;- -''nth ?.rtd reported on a Discharge Monitoring Report Form (EPA No. 3320-1),
•::«:-iir:-:ed ~') later than the 28lh day of lh<- month following the completed reporting
-rio:. The first report is due on (as previously reported) . A signed copy
: t'rtsse, snd all other reports required herein, shall be submitted to
.he izate at the following address:
Division of Industrial Services
Maine Department of Environmental Protection
Hospital Road
Augusta, ME 04333
a... T:-t "daily ax'erapc" discharge moan.s the total discharge hy weipht during a calendar
rr»:i'th ciivided by the number of days in the month that the production or
cnrmercial facility '.va<; operating. Whore less than daily sampling is required by this
:>-::"r.it. thp daily rivpra^v discharge shall be determined by the summation of all the
rr.nsured daily di:charg'?s by weight divided by the number of days during the
CL linear month when the measurements were made.
c . T:«2 "daily maximum" discharge mnans the total discharge by weight during any
Ci.Hr.car day.
7-::5". :•— -Cfdv.ros Tnr {hi- jinulysis of pollutants shaJl conform to rcfiulalions published
pursuit to Section 304(g) of the Act, under which such procedures may be required.
r. -:C^ri:r.§ of Rcsu Its
F :>r -:-;i:r. rr.e-is'jrement or sample- taken pursuant to the requircMents of this permit, the
:>rrrr.: ::..'.* shall record the follo-.ving ir-formaliun:
-. T-.' ---xac: place, date, and time of sampling;
: "i'-'n dates the analyse^: were performed;
.-.. ":'•: -;orsor;i.s) who ^-t-rformed the analyses;
021537
\
-------
PART I
4 or y
i N.». ME0000302
d. The analytical techniques or methods used; and
c. The results of all required analyses.
<}. Additional MonitorinK by Permittee
If the permittee monitors any pollutant at the locations) designated herein more
frequently than required by this permit, using approved analytical methods as specified
above, the. results of sudi monitoring shall be included in the calculation and reporting of
the values required in the Discharge Monitoring Report Form (EPA No. 3320-11. Such
increased frequency shall also be indicated.
7. Records Retention
All records and information resulting from the monitoring activities required-by this
permit including all records of analyses performed and calibration and maintenance of
instrumentation and recordings from continuous monitoring instrumentation shall be
retained for a minimum of three (3) years, or longer if requested by the Regional
Administrator or the State water pollution control agency.
021S38
-------
PART II
F.IM 5 «)' g
Per mil No. HE00003 02
t -V
/A. MAN'ACKMENT REQUIREMENTS
1. Change in Discharge
All discharges authorized herein shall be consistent with the terms and conditions of this
permit. The discharge of any pollutant identified in this permit more frequently than or
at a level in exr<-ss of that aulhori/.ed shall constitute a violation of the permit.'Any
anticipated facility expansions, production increases, or process modifications which will
result in new, different, or increased discharges of pollutants must' be reported by
submission of a new Ni'DKS application or, if such chances will- not violate the effluent
limitations specified in I his permit, by notice to the permit issuing authority of such
changes, l-'ollowing such notice, the permit may bo modified to specify and limit any
pollutants not previously limited.
2. Noiicompliancc Nolifiaitinn . •
if, for any reason, the permittee does not comply with or wi!l be unable to comply with
. any daily maximum effluent limitation specified in this permit, the permittee snail
provide the Regional Administrator and the State wif.h ihn following information, in
writing, within five? (f>) days of becoming aware of such condition:
a. A description of the discharge and cause of noncompliance: and
It. The period of nuncompliante, including exact dales and limes; or, if not corrected,
the anticipated time tin1 noncomplianre is expected to continue, and steps being
taken to reduce, eliminate and prevent recurrence of the noncomplying discharge.
3. Facilities Operation
The permittee shall at all times maintain in ROOD working order and operate as efficiently
as possible all treatment- or control facilities or systems installed or used by the permittee
to achieve compliance with the terms and conditions of this permit.
A. Adverse Impact
The permittee shall laki-
-------
I
I
I. .
PART II
I'jpe g of g
Permit N».ME0000302
6. Removed Substances
Solids, skulks, fil'.'-r backwash, or other pollutants removed in the course.of treatment or
control of wastcwaters shall be disposed of in a manner such as to prevent any pollutant
from such materials from entering navigable waters.
7. Power Failures
In order to main-Lain compliance with the effluent limitations and prohibitions of this
permit, the permittee shaii either:
a. In accordance1 with the Schedule of Compliance contained in Part 1, provide an
alternative power source sufficient to operate the wastewatcr control facilities;
or, if such alternative power source is not in existence, and no date for its implementation
appears in Part I, . " '
b. Halt, reduce or otherwise control production and/or ail discharges upon the
reduction, less, or failure of the primary source of power to the was.tewater control
facilities.
B. RESPONSIBILITIES
1. Right Of Entry •
Thr. permittee, shall allow the head of the State water pollution control agency, the
Regional Administrator, and/or their authorized representatives, upon the presentation of
credentials:
a. To enter upon the permittee's premises where an effluent source is located or in
which any records are required to be kept under the terms and conditions of this
permit: and
b. At reasonable times to have access to and copy any records required to be kept under
the terms and conditions of this permit; to inspect any monitoring equipment or
method required in this permit; and to sample any discharge of pollutant.?.
2. Transfer of Ownership or Control ' •
. In Hut event of any change in control or ownership of facilities from which the authorized
discharges emanate, the permittee shall notify the succeeding owner or controller of the
existence of this permit by letter, a copy of which shall be forwarded to the .tcgionaJ
Administrator and the Stato water pollution control agency.
3. Availability of Reports
Kxcopt for data determined to he confidential under Section 308 of the Act, all reports
prepared in accordance with the terms of this permit shall be available for public
•21548
1
-------
PART II
l';i|-e 7 <)!' 8
I'cnnii No.ME0000302 !'
inspection ft the offices of the Stale water pollution control agency and the Regional
Administrator. As required by the Act, effluent data shall not bo considered confidential.
Knowingly making any false statement on any such report may result in the imposition of
criminal penalties as provided for in Section 300 of the Ac*..
•1. Permit Modification
After notice and opportunity for r. hearing, this permit may be: modified, suspended, or
revoked in whole or in part, during its term for cause including, but not limited to, the
following:
• a. Violation of any torms or conditions of this permit;
n. Obtaining this permit by misrepresentation or failure to disclose fully all relevant
facts; or . .
c. A change in any condition that requires either a temporary or permanent reduction or
elimination of the authorized discharge.
5. Toxic Pollutants
';
Notwithstanding Part II, JM above, if a toxic effluent standard or prohibition (including
any schedule of compliance specified in such effluent standard or prohibition) ,s
established under Section 307(a) of the Act for a toxic pollutant which is present in the
discharge and such standard or prohibition is more stringent, than any limitation for such
pollutant in this permit, this permit shall ho revised or modified in accordance with the
toxic effluent standard or prohibition and the permittee so notified.
,! .. •• 6. Civil and Criminal Liability
'i •', "
'"' • Except as provided in permit conditions on "Bypassing"
' Failures" (Part IJ, A-7), nothing in this permit shall be cons
• . (Part II, A-5) and "Power
construed to relieve the permittee
from civil or criminal penalties for noncompliance.
7. Oil and Hazardous Substance Liability
. Nothing in this permit shall be construed In preclude tin: institution of any legal action or
relieve tho permittee from any responsibilities, liabilities, or' pcrsidiies to which the
permittee is or may be subject under Section 311 of the Ai:t.
: 8. State Laws
'i.
Nothing in (.his permit shall be construed to | '.cclude the institution of any legal action or
relieve the permittee from any responsibilities. liabilities, or penalties established pursuant
to any applicable Sialo law or regulation under authority preserved by Section 510 of the
Act.
021541
-------
PART II
{
•I .
8 of 8
ii NO. ME0000302
9, Property Rights
The issuance of this permit dors not convey any property rights in cither real or personal
property, or any exclusive privileges, nor does it authorize any injury to private property
or any invasion of personal rights, nor any infringement of Federal, State or local laws or
regulations.
10. Seuerability .
The provisions of this permit are sevcrable, and if any provision of this permit, or the
application of any provision of this permit to any circumstance, is held invalid, the
application of such provision to other circumstances, arid the remainder of this permit,
shall not be affected thereby.
'•!
PART 111
OTHER REQUIREMENTS
02154?
v..
-------
•' • MUlKIStmilKSCIWCES:
ZMttlt
STATE ')F MAINE
pen
lilll WU'.ISV SKLll Mflitjl. »WHt» Ct)3)
Kcycs Fibre Company
Watorvillc
Uaine
FIKDIir.S OF FACT AKD ORDER
WASTE DISCHARGE LICENSE AMENK-1EKT
; UilUlS:
• ''.: Hill QUU nUOliniOl
JJU!
X
-'•; ujiui
:.>
••>'.-••
'.-••, J812H1
" uwMicn stmcu
cn'oiiu!io!ico«iifra.
JJ5J53I
. '-. HCIOWOrUCCS:
WUSUOUEJ
' Oil SI
Pursuant to the provisions of Section 451(2) of Title 38, Maine. .-••.:*••
Revised Statutes, Waste Discharges License f;o. A91, icsuccl on '.•''.''.
Hay 8, 197'i by the Board of Environmental Protection to Keyes Fibre ;-':-
Co. (Fair fie Id) for the discharge of process and cooling was tewa tors ;S..';.
to the Kenncbcc River, Class C, after due notice and opportunity for'-1-,1'-?'.
a public hnaring, was amended as hereafter set forth, based upon
' ' ''. ••. *
Kcyes Fibre, has requested that the license requirement to submit .pro-";'
CCRS wastev;ater discharge monitoring rflnnrtf! to this Department be • '•-..-.
deleted, since this discharge han connected to the municipal sewerage/-'
trrsatmciit r;y.r;tcm. The J.icensca fcrtls and t:bc Staff concurs that the .:.--
submission of such monitoring to the Department of Environmental Pro—-/'
tnction is unnecessary. . . '.''\
The 3icc.nr.ee has also requested that thn limitations on their cooling-'.
water dir.charp,e be changed from a monthly average flov; o£ 0.22 HGD at.; :
S^F to 2.0 KfiD at 04°F. Tins change if: neccnsary to reflect the
characteristics of the existing dificharpc. The modification will not •
result in Water quality degradation. ;. '
j
Based upon thf.se findings, and Jn consideration of the characteristics".
of the proposed discharge, the treatment required by the terns of the
proposed amended license, and the vater quality characteristics of thej
receiving v.'at.or, the Hoard concludes that: • ••''..
1. The proposed discharge by itself, or in combination with other dig- '
charges, will not lower the quality of the receiving waters below "thcsV'••*•
minimum requirements of their classification. • .-•••
2. The proposed discharge will receive best practicable treatment.. . :'. •
• '.' '
Therefore, the Board orders War.to. JHschargo License Mo. 491 amended as
follows r.upcrceding the like limitations of the llcenne ns issued on
May 8, 197A. ' ].
A. The requirement to submit: monitoring reports on discharge 001
(effluent to municipal.treatment plant) after October 1, 1976 is deleted.
D. The monthly average flow limitation for the cooling water discharges
is increased from 0.22 MCD to 2.0 IICD. .. .
-------
A.t.l other toms nnci conditions of the license as amended on
August 4, 1975 remain in full force and nffect.
DONE AND DATED AT AUGUSTA, MAINE, THIS 30th DAY OF September
1977.
BOARD OF ENVIRONMENTAL. PROTECTION
-•-^/ c
f
Henry li. VJa.c-rcn, Acting chairman
-------
PLEASE ADDRESS REPLY TO:
WATER V1LLE, MAINE 04901
TEL. 207 873-3351
160 SUMMIT AVENITK • MONTVAUv. NKW JERSEY07645
Deceater 29, 197?
U.S. EPA Pulp & Paperboard Survey
E. C. Jordan Co.
P. 0. Box 7050 Downtown Station
Portland, Maine
Attns Kr. Willard Warren
Dear Mr. Warren:
Enclosed is a completed copy of the Environmental Protection
Agency Survey Form, Pulp, Paper and Paperboard Industry for Integrated
Kills, Part II.
We completed only the questions pertaining to the groundwood
operation at Shawmut.
Very truly yours,
CFB/mbe
Enclosure
C. F. Bean
Manager, Process Engineering
121545
-------
Portlarid^Mainel04111
PRO JECTtDESCRIPlION:
'
SUBJECT:
Of-
DISCUSSION:
Distribution:
021046
-------
\
ENVIRONMENTAL PROTECTION AGENCY
SURVEY FORM
PULP, PAPER, AND PAPERBOARD INDUSTRY
NON-INTEGRATED MILLS
PART I
X
<}"<
MILL BACKGROUND DATA
A. Mill & Division Name: Keyes Fibre Co,, Waterville Plant
Address: Waterville, Maine
ZIP:
04901
Telephone:
20?
873-3351
Corporate Affiliation (if applicable)_
Contacts and Title: (Use an asterisk next to the responsible personnel
completing the survey form).
*Ernest J. Reidman
Paul Pall
Clarence F. Bean
Manager, Eastern Manufacturing
Group Leader, Research Division
Mgr., Process Engineering
B. Age of Mill 7^ years old.
1. Year of initial construction 1903
2.
Please give the year of initial startup and each year since 1952 in
which any major modifications or permanent shutdowns were made which
significantly affected the composition or amount of effluent from
the mill.
a. Added Paper Machine Saveall(s)
b. Added New Paper Machine(s)
Year(s) of
Initial Startup
Year(s) of Waste
Significant Modification
or
Permanent Shutdown
02154"?
-------
Mill: //:'^/.> Location: A',-/ •"//x^-x c :. -<
Year(s) of Waste
Significant Modification
Year(s) of or
Initial Startup Permanent Shutdown
c. Paper Machine Rebuild(s)
Added Stock Prep. System
e. Added Broke Storage
f• Elimination of Paper Machine(s)
g. Other (Please List)
Discharge Waste to KSTD 1976
Discharge Cooling Water
to River 1976
Ma chine Ingta lla tl on H
Stert-Up Start-Uo
B-13 I960 C-22 1964
B-14 1962 C-23, 24, &
B-15 196? 26 1966
C-9, 10, 11, 12 1953 C-25, 2?, 28,
C-13, ifc, 15, ' & 29, 30 196?
& 16 195^ C-31, 32, 33,
C-17 1955 3^. 35, 36 196S
C-iS, 19 1959 c-37. 38, 39,
C-20 1962 & 40 1969
C-21 1963
§21548
- 10 -
-------
Mill:
Location:
//V •'' ~{ A' f\ -j i Lt ~
II.
A.
3.
4.
5.
6.
7.
8.
PRODUCTION INFORMATION
Average Daily**
Air Dry
Pulp Tons /Day
Consumed Hardwood Softwood
Bleached Kraft 66-9
Unbleached Kraft
Bleached Soda
Sulfite
Wastepaper 13.9
Other (please list)
#1 News _T -*
White Ledger 1.3
(2-S) Cup Clippings 2.1
Groundwood 112
Maximum Day
Air Dry
Tons /Day
Maximum Month
Air Dry
Tons /Day
Hardwood Softwood Hardwood Softwood
70.
19.
10,
5
120
Average Daily**
Air Dry*
Tons /day
4£fc * O
7pw ^2
£V-3
c
13 ^
r.i* 65
r
r.
r.H
..<•*
r
3600 C
Maximum Day Maximum Month
Air Dry* Air Dry*
Tons /day Tons /day
B. Products
9. Market Pulp
a. Pulp Bales and/or Rolls
b. Wet Lap Pulp
c. Slushed Pulp
10. Groundwood Molded Pulp Artic?.es
11. Newsprint
12. Groundwood Printing, Writing and Related
a. Uncoated Groundwood Printing and
Converting
b. Clay (50% or more Kaolin) Coated
Groundwood Printing and Converting
*Measured at the winder or pulp dryer.
120,
139,
39T
3,
021549
^, fo
Total production for the year
**Average Daily = Total number of production days for the year
- 11 -
-------
Mill:
Location:
B* Products (continued)
c. Groundwood Specialties
d. Other Bleached Hardwood
Kraft Molded Pulp
13. Wood Free Printing, Writing
and Related
a. Uncoated Free Sheet Printing
b. Clay (50% or more Kaolin)
Coated Free Printing
c. Uncoated Writing and Related
d. Uncoated Solid Bleached
Bristols
e. Clay (50% or more Kaolin)
Average Daily Maximum Day Maximum Month
Air Dry* Air Dry* Air Dry*
Tons/day Tons/day Tons/day
f.
Coated Solid Bleached Bristols
Other
14. Cotton Fiber Papers
a. Writing and Related
b. Technical
c. Other
15. Thin Papers
a. Carbonizing
b. Cigarette
c. Other
16. Packaging and Industrial Converting
a. Unbleached Kraft _
b. Bleached Kraft
c. Other
*Measured at the winder or pulp dryer.
63,
63, 63,1890
021550
- 12 -
-------
Mill:
Location:
B. Products (continued)
17. Specialty Packaging and
Industrial Converting
a. Tape Backing
b. Saturating
c. Gasket
d. Other (please list)
Average Daily Maximum Day
Air Dry* Air Dry*
Tons/day Tons/day
Maximum Month
Air Dry*
Tons/day
18. Sanitary Tissue
19. Unbleached Kraft Paperboard
(80% or more unbleached Kraft pulp)
a. Linerboard
b. Folding
Other
c.
20. Semi-Chemical Paperboard
(75% or more semi-chemical pulp)
a. Corrugating
b. Other
21. Bleached Paperboard
(not less than 30% bleached chemical wood pulp)
a.
b.
Clay Coated Bleached Food
Board
Uncoated Bleached Food Board
c. Bleached Linerboard
d. Folding
e. Other ___
*Measured at winder or pulp dryer.
- 13 -
-------
Mill:
Location:
B. Product^ (continued)
22. Recycled Paperboard
a. Linerboard
b. Corrugating
c. Chip & Filler Board
d. Folding
e. Set-Up
f. Gypsum Wall Board
g. Other
23. Construction Paper and Board
Construction Paper
Wet Machine Board
Insulating Board
Hard Pressed Board
Other
a.
b.
c.
d.
Average Daily Maximum Day
Air Dry* Air Dry*
Tons/day Tons/day
Maximum Month
Air Dry*
Tons/dav
e.
*Measured at the winder or pulp dryer.
02155?-
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e
c
en
- 21 -
-------
TO
CHEMICALS AND RAW MATERIALS (Cent),
-oiler --'sea Water Treatment,
l£~. Neutramlne NA9 (Beta)
165. Permacol 110 (Beta)
© (To) (c) © (e)
166. rolysperse (Beta)
© '(c) © (a) (e)
It?. Adjunct (Beta)
© (b) (c) (d) (e)
Cle3r.ir.gr Solver.ts - Hainter.ar.ee Shop
168. Polar-sol
(a) © © (fi) (e)
lo9. Safety Solvent FO-101
(a) © (c) © (e)
170. Harco Safety Cleaner
(a) (b) (c) (?) (e)
021560
-------
F
Mill: C\fC^ f '~, Location: t-ii & r fT-/?U' <• (—'^-
IV. MANUFACTURING PROCESS AND INTERNAL POLLUTION CONTROL PRACTICES
A. General
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
B. Paper Kill
182. How many paper machines does mill have?
56. Fur? Mel-ing Machines
183. Give the number of paper machines the mill has which utilize savealls,
or similar devices, for fiber recovery.
56.
184. Give the number of paper machines the mill has which have savealls,
or similar devices, that permit reuse of clarified water.
C. Additional Information
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
021561
- 22 -
-------
Mill:
'/T.S
Location:
^^^^^^^
i*^*^^*^^
Section V rea ^~~~~" - -
tice*- in semori rination on
A- -H^SrjJsage
N° QUESTIONS FOR"THIS
B- Backs
T0
presented on the
IN PART I.
of
(a) Direct
Indirect
212'
s.a. Preliminary Treatment
a. Primary Treatment System
b- Secondary Treatment System
Indirect Discharger (discharge to a POTW:) please provide the
following information:
Is raw wastewater pretreated externally prior to discharge to the
POTW? (Pretreatnent is considered to be any treatment device external
from the mill production processes which is utilized prior to a pri-
mary and secondary treatment system, or prior to discharge by an
indirect discharger to a POTW.)
{!aV v*~
021562
- 23 -
-------
Mill: c?f S Location: LA1''J ^ f^'U/L i.-£—
216. Give the treatment process used by the POTW to which your mill discharges
(Include biological and physical-chemical treatment if applicable)
(a) Activated sludge
(b) Aerated lagoon
(c) Oxidation ditch
(d) Trickling filter
(e) None
(f) Other (indicate type)
219. Give the preliminary treatment method used, if any.
(a) Neutralization
(b) Screening (indicate type used) Sweco Screen
(c) Other (please describe)
221. Indicate the primary treatment method used, if applicable.
(a) Clarifier
(b) Sedimentation lagoon
(c) Mechanically cleaned sedimentation lagoon
(d) Other (please describe)
fe) Not applicable
Give the type of biological treatment used, if applicable.
(a) Storage oxidation basin
(b) Aerated Stabilization basin
(c) Activated sludge (air or oxygen)
(d) Other (please describe)
K«y Not applicable
021563
- 24 -
-------
g:
v-;i i. Location:
D. Direct Discharger please provide the following information:
228. Is wastewater discharge continuous or non-continuous (effluent stored and
discharged when receiving water conditions allow) when production
facilities are operating?
(a) Continuous
(b) Non-continuous - daily
(c) Non-continuous - seasonally/intermittent
E. Preliminary Treatment (Direct Discharger)
230. Give the preliminary treatment method used, if any.
(a) Neutralization
(b) Screening (indicate type used)
(c) Other (please describe)
F. Primary Treatment (Direct Discharger)
232. Indicate the method used for primary treatment.
(a) Clarifier
(b) Sedimentation lagoon
(c) Mechanically cleaned sedimentation lagoon
(d) Other (please describe) _
G. Biological Treatment (Direct Discharger)
236. Give the type of biological treatment used.
(a) Storage oxidation basin
(b) Aerated stabilization basin
(c) Activated sludge (air or oxygen)
(d) Other (please describe) fl 2 1JJ 6 4i
25 -
-------
Mill: Location:
H. Secondary Solids Removal . .,- ,-:-..;, r .. .
.:•'": "-.•. '• ::-Su;": • '•"••' ?--?'*
••• . . • v •-• ' . • ; ;il
.. .' •-.•..-. : '••/•; ii
* _, • . • ,'.fciS;--1«
237. If secondary clarification is used, what is the method used? : .'..'. ' '. •--~r-^|!
''..,.-..' =•• •-.",/.. vk^
(a) Clarifier ; ... . . .,;/-W-.- :.;«^§
(b) Reactor clarifier
(c) Settling basin . • , .
(d) Other (please indicate) ;
238. Is a holding pond utilized after secondary treatment?
(a) Yes .
(b) No '"
I. Spray Irrigation
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I. V--~-
J. SludgeHandling and Disposal
240. Indicate the method used for sludge disposal.
(a) Lagooning - ;. ' .
(b) Landfill
(c) Hog fuel boiler - .,
J-.
(d) Other (please describe) • •' •
K. Foam Control
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
L. Cost Information
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
021565
- 26 -
-------
Mill:
Location:
M. Site Conditions and Availability of Land
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
N. Wastewater Characteristics
251-254. Give the (1976) wastewater loads indicated below:
Indirect and Direct
Dichargers
Please Answer
(251)
Paper
Mill
(252)
Total Raw
Wastewater
3.S6:
5.502
.775
Same
$03 /-J
IV. FUEL AND ENERGY U
NO QUESTIONS FOR THIS SECTION ARE TO BE ANSWERED IN PART I.
VII. PRIORITY POLLUTANTS
See Next Page
VIII. PROCESS SCHEMATICS
NO QUESTIONS FOR THIS SECTION ARE TO BE ANSWERED IN PART I.
021566
-------
Mill:
Location:
VII. PRIORITY POLLUTANT COMPOUNDS
Please fill in the following information for those priority pollutants
which, to your knowledge, are in your raw water supply, or used, or
generated in any of the processes in the mill (refer to the following
pages for the priority pollutant list). Use the number shown to identify
the compound.
It should be noted that many mills may be using quantities of the listed
chemicals as additives, cleaning solution, or solvents which are purchased
and referred to by a trade name. Please supply trade names of all pro-
prietary type chemicals used in the mill.
Compound Number
or Trade Name
Process Where
Compound is
Used or Generated
Describe Use
Quantity Frequency
Paraak 4 & Acintol
Oleic Acid Making wax emulsions 13,083 Ibs/month
(130) CX FOR 3/or
Internal sizing 553,839 Ibs/year
Pale rosin N-bOl-7
(?) Solvox 2^0 Pulping aid/dispersant
220 Ibs/year
C87) Slimacide V-10 Slime Control
7,800 Ibs/year
Sampling or Monitoring
Program for Compound
(Yes or No)
No
Yes (in product)
No
No
(Wet EndJ
~ 28
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-------
PART I
CONFIDENTIALITY CLAIMED FOR THE FOLLOWING
Question
Number
Question
Number
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Number
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Number
Question
Number
Question
Number
Question
Number
- 32 -
-------
X /
ENVIRONMENTAL PROTECTION AGENCY
SURVEY FORM
PULP, PAPER, AND PAPERBOARD INDUSTRY
NON-INTEGRATED MILLS
PART II
I. MILL BACKGROUND DATA
A. Mill & Division Name: Waterville Eastern DIv.
Address: College Avenue, Waterville, Maine ZIP: 04901
Telephone: 20? / 573-3351
Corporate Affiliation (if applicable)
Contacts and Title: (Use an asterisk next to the responsible personnel
completing the survey form)
*E. ,". Eeifasn Manager, Eastern Division Manufacturing
C. ~. Bear. Manager, Process Engineering
B. 'Age of Mill 75
1-2. DELETED - ANSWERED IK PART I
II. PRODUCTION INFORMATION
—,—^_^_______^^_^_ ,
i
3-23. DELIIED - ANSWERED IN PART I ' |
III. PROCESS RAW MATERIALS
24-164. DELETED - ANSWERED IN PART I
121572
- 33 -
-------
Mill: Keyes Fibre
Location:
Waterville
IV. MANUFACTURING PROCESS AND INTERNAL POLLUTION CONTROL PRACTICES
A. General
165. Give the typical production days per year
166. High level alarms - do chemical and stock tanks have operable
high level alarms to prevent spills?
MU Yes
(b) No
(c) To the extent possible
Explanation (if needed)
167. pH or conductivity monitor of internal sewers - Do sewers have such
devices to detect or divert spills?
i£a) Yes
(b) No
•fc) To the extent possible
Explanation (if needed) Turbidity Meters
168-181. Is the cooling water collected and reused from the following locations:
Indicate answer using one of the following responses: (a) Yes; (b) No;
(c) Seasonal; (d) To Extent Possible; (e) Not Applicable.
168. Air Compressor Cooling Water
169. Dryer Drainage Condensate Cooling
170. Lube Oil Cooling
171. calendar Cooling Heat Exchangers
172. Rewinder Brake Cooling
02IS73
x
X
-------
Mill:
Keves Fibre
Location; Waterville
(a) Yes; (b) No; (c) Seasonal; (d) To Extent Possible; (e) Not Applicable
a ._ b c d _ e r
173. Paper Machine Clutch Cooling _*
174. Cooling in Power Plant *
175. Feed Water Pump Bearings x
176. Power Plant I.D. Fan Bearings ._.x
177. Other Bearing Cooling x
178. Refiner Cooling *
179. Motor Control Center Cooling y
180. Water Chiller *
181. Air Conditioning *
B. Paper Mill
182-184. DELETED - ANSWERED IN PART I
021574
- 35 -
-------
C .C
O 0) *J
41
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194. Does the mill have a stock spill collection system, prior to external
trear.~ent facilities?
(a) Yes
(b) No
\
c Partial
195. If the answer to the preceding question is (a), describe the collection
system's function.
faj Collected and discharged to the sewer at a controlled race
or
(fb) Collected and reused in the process
(c) Other (please describe)
196. Give the frequency of waste significant grade changes; also, if
possible, give the stock quantity sewered.
.1 ton once a week
197. is the mill central storage of white water (a) and slush broke (b) adequate •
with regard to effluent discharge? j
a. White Water |
(a) Yes |
i
(b) No •
(c) To the extent possible
(Explanation, if needed) j
b. Slush Broke
nO Yes
(b) No
(c) To the extent possible
(Explanation, if needed) 0 21 ft 7 7
- 38 -
-------
Mill: Keyeg Fibre Location: Wat_eryill.e
198. Are special provisions made for spills, screen rejects, and excess
materials from coating or sizing systems?
(a) Yes
(b) No
@ Limited
199. Does the mill employ organic solvent coating or saturating operations?
(a) Yes
fa No
200. If yes, please give the type and quantities (Ibs/day) of organic
solvent used.
201. Give the average daily organic solvent coated or saturated paper
produced.
__—______^_______^_ tons/day
021$78
- 39 -
-------
Mill:
Location:
Waterville
202. Please indicate effluent from the combined papermachine facilities
as follows: (i.e., total flow from all machines)
Waste Source
Volume GPM
Suspended Solids
(if applicable)
Ibs/day
Centricleaner and machine
screen rejects
Couch pit, seal box, and
any other unclarified
Whitewater overflows
Thick stock spills, dumps,
washups from stock prepara-
tion area and machine
Excess clarified Whitewater
Cloudy water from vacuum
systems, or pump sealing
applications
Clear water discharges
i. e., cooling services,
condensate, other non-
process services
Other effluent sources
not included above
Total papermill effluent
l458.gpm
gal/day
3909.
695,
2153>
3909,
? (Circle answer)
i. Is (£) discharged via process sewer or
S~^
YES (NO
Additional Information
203. Does the cill have a program for disposal of old electrical transformers?
(a) Yes
(b) No
204. please cive the number of people employed at your mill. 1000
02157.9
-------
Mill:
Keyes Fibre
Location:
Waterville
V. WATER USAGE AND EFFLUENT TREATMENT PRACTICES
Instructions for Completing Section V
Section V requests information on the mill's vastewater treatment practices.
In Section VIII a general schematic of the effluent treatment system is
requested. You have the option of providing any of the data requested in
Section V on the schematic. If you do this, please indicate on the
question(s) involved that the data is presented on the schematic.
A* Hater Usag_e
205. Indicate the source and amount of process water.
(a) Surface (i.e., river, lake or reservoir)
(b) Groundwater
(c) Other (please describe)
2.1325
MGD 197?
MGD
MGD
206. Does the quality of the raw water limit the reuse of water in this mill?
(a) Yes - explain ...
g>) NO
207. Indicate the source and amount of the mill's cooling water.
@ Surface ,. 1.0000
(b) Groundwauer
(c) Other (pleas-2 describe)
MGD 1977
MGD
MGD
208. Indicate the source and amount of the mill's boiler feed water.
(a) Surface .06?5 MGD
(b) Groundwater - ». MGD
(c) Other (please describe) MGD
1977
02 i:
-------
Mill:
s Flbre
Location:
Watervi_lle_
209. Describe treatment used for boiler feed water conditioning.
Poly Sparse - Caustic Soda .
Adjunct - N.A.-9. - Sulfite .
210. Give the disposal method now employed for boiler blowdown water.
{aj Sewered to treatment plant
(b) Directly discharged
(c) Directly discharged with pH adjustment
(d) Directly discharged after cooling
(e) Other (please describe) .
B. Background Data
211-212. DELETED - ANSWERED IN PART 1
213. How is cooling water disposed?
^y Separate discharge to receiving stream.
(b) Combined with process waters before treatment.
(c) Combined with treated process waters.
(d) Recycled.
C. Indirect Discharger please provide the following information:
214. Name and*location of POTW which handles your wastewater.
Kennebec Sanitary Treatment Diet..,. Wa+.eryn >-,....Maine
215-216. DELETED - ANSWERED IN PART I
217. Areithere specific pretreatment requirements of limits upon pollutant
parameters imposed by the POTW system to which you discharge?
(a) Yes
(b) No
021S81
-------
Mill: Keyes Fibre Location: Waterville
218. If the answer to the preceding question was (a), please list the specific
pretreatraent requirements or pollutant parameter limits imposed on your
mill by the POTW. Total Waterville and Shawmut
Flow 1 mgd
BOD 4000£/D
S3 3000//D
219. DELETED - ANSWERED ~N PART I
220. If. neutralization is practiced, fill in the following.
Chemical us ed ^A
221. DELETED - ANSWERED IN PART I
222. Are any chemicals or other settling aids added to the primary treatment
units? NA
(a) Yes
(b) No"
(c) To the extent necessary (intermittent)
223. Please show the wastevater streams which eater the secondary treatment
system (if applicable). NA
Process Source or Sewer Mo.* Flow, MGD BOD, Ib/D TSS,Ib/D
a. Heisign Values Aviirag^ Day
M.T.iimuiri Month
b. Primary Treatment Effluent Average Day
Maxiiaura Day
Maxlmun Month
c. Other Avc?.v>gfi Day
__ .T ; . _ _ ___ _ _ Max:unum Day
Maximum Month
"Process source or sewer number should be keyed to the mill process and
wastevater treatment schematics requested in Section VIII.
0215S2
-------
Mill:
Location: Waterville
224. c,i-i.-e the ncrnal pH of the wastewater at the influent to the secondary
treatraent system. NA
(a) 4-6
Cb) 6-6
(c) 8-10
225. DELETED - ANSWERED IN PART I
D. Direct Discharger please provide the following information:
226. Name of effluent discharge receiving, water
227. j^iclose a copy of current or proposed NPDES effluent discharge limits.
228. DELETED - ANSWERED IN PART I
229. Zi" vasteiv&cer discharge is seasonal or intermittent non-continuous,
approximate] y how many days out of the year do you discharge to the
receiving water.
(a) Less than 30
(c) 91-120
(d) 121-130
(e) 181-21':
E. ?relir-iInary T r e a tci e n t
230. DELETED - A.^S'-'cRED IN PART I
it: j 211-240
241-270
(h) 271-300
(i) 301-330
(jj 331-360
231. "If neutralizarJ.cn is practiced, fill in the following:
Chemical used NA :.
021583
-------
Mill:
Keyes
Location:
Wsterville
F. Primary Treatment
232. DELETED - ANSWERED IN PART I
233. Are any chemicals or other settling aids added to the primary treatment NA
units?
(a) Yes
(b) No ."
(c) To the extent necessary (intermittent).
^ • Biological Treatment
234. Provide the following information for the biological treatment system NA
(if applicable)'.
c.
d.
a. Process Source : or Sewer >:o. * Flow, KGD BOD, Ib/D TSS, Ib/D
Design Influent Values Average Day _ _ _
'. ' : Kaxinum Day _ _
. . • Maximum Month __ _ _
b. Primary Treatment Effluent Average Day _ _ _
Maximum Month
Other Wastewater Streams Which Ent-?.r the Biological Treatment Systems
Without Primary Treatment
Average Day
Maxiir.um Day
:S£:j:i-j-.un-. i-ionth
Average Day
Maximum Dsy
Maximum Month
*Process source or sewer nunibej should be ksyea to the mill process and
wastewater treatment schsnintics requested in Section VIII.
0215S4
-------
Mill: Keyes Fibre
Location:
Waterville
235. Give the normal pH of the wastewater at the influent to the secondary
treatment system.
(a) 4-6
(b) 6-8
(c) 8-10
236. DELETED - ANSWERED IN PART I
MA
H. Secondary Solids Removal
237-238. DELETED - ANSWERED IN PART I
I. Spray Irrigation
239. Is treated wastewater used for irrigation?
(a) Yes
(b) No
(c) Partial
NA
J. Sludge Handling and Disposal
240. DELETED - ANSWERED LN PART I NA
241. Give the percent solids of the sludge after dex
-------
Mill: Keyes ribre
Location: Waterville
K.
243.
Foam Control - (Wastewater treatment system only)
Does the mill use foam control measures? NA
(a) Chemical
(b) Physical Methods
(c) None
(d) Other - explain
021586
-------
M111: - Key6£ Fibre Location: "aterville
^°st Information
244.
Provide cost data indicated for effluent treatment system in 1976 dollars.
Use the cost multiplier factors, which follow, to convert to 1976 dollars.
Annual Operation
Tnt-'-t f J •- -i "
Internal control de1
effluent waste load
External Treatment J
Primary Treatment
voted to $1,167,99*
reduction. /
>ystem NA
NA
7J7.W
115,300
II-
r.§
Secondary Treatment NA ' •
Construction Cost Multipliers
to Convert Capital Cost to 1976 Dollars
..956 -
:.957 -
.958 -
L959 =
I960 -
'.961 =
1962 »
2.535
2.380
2.325
2.254
2.220
2.220
2.207
1963 =
1964 =
1965 =
1966 =
1967 »
1968 =
2.186
2.161
2.124
2.051
1.978
1.884
1969 =
1970 =
1971 «
1972 -
1973 -
1974 =
1975 =
1.794
1.689
1.564
1.485
1.317
1.242
1.100
*Factors to be considered in Annual Operation and Maintenance Costs
(0 & M Costs).
1. Manpower - both operators and maintenance personnel
2. Contracted services
3. Energy Cost
4. Trucks for hauling
5. Nutrients
6. Leased equipment
7. Disposal costs
8. Sludge handling
9. Sampling and analysis
10. Equipment replacement (except major capital)
Exclude Depreciation A91
- 48 -
-------
Mill:
Keyes Fibre
Location:
Waterville
245. For mills which discharge to a POTW, please give the annual user fee
with a breakdown for capital cost recovery and operation and maintenance
costs.
a. Capital Cost Recovery(if available)
b. Operation and Maintenance (if available)_
c. Total Annual User Fee 1978 Projected
217.523
246.. Please give the basis used by the POTW to determine the mill's user
fee.
(b) BOD only
(c) 'TSS only
SS 56.63/ton
^d) Conbination of parameters (please indicate)
60?£ Flow, 2£f?o BOD,
(e) Unknown
SS
M. Site Conditions and Availability of Land
247. Is there sufficient land for expansion of your wastewater treatment
system for BATEA?
(a) Yes
(b) No
(c) Unknown
248. Can the'mill purchase land from adjoining property owners for possible
expansion of the wastewater treatment system?
(a) Yes
(b) No
(c) Unknown
021588
-------
Mill: Keyes Fibre Location: Wgterville
249. Arc. the soil conditions in the land available for future expansion of
f;ut:h a quality as to require special construction methods or special
1'acilxty equipment (i.e., ledge, water table and liners needed for
basins)?
(a) Yes
«"b) Ho
,c) Vnknown
250. Miscellaneous Discharges - Indicate any wastewater discharges not
described in Section V which do not flow to the wastewater treat- NA
tient system.
N- War.tewauer Characteristics
251-254. IiELETED - ANSWERED IN PART I
255. War. the analysis procedure used for BOD measurement in accord with
"ha iiu.:':hod presented in Standard Methods fpr_ the Examination of Water
.-ind _]fhie tew.-it:er?
•/a) ; 3th Edition
^b) lAth Edition
\c) No (please describe other method used)
256. i.g a glucose-glutaraic acid BOD standard analyzed?
(a) Yes
6^ Ho
021589
- 50 -
-------
Mill:
Keyes Fibre
Location:
Waterville
257. If the answer to Che preceding question was (a), please indicate the
normal frequency of the analysis.
(a) Daily
(b) Weekly
(c) Monthly
(d) Quarterly
(e) Serai-annual
258. Please indicate the average percent difference found between the BOD
deterriinations and -the glucose-glutamic acid BOD standard.
(a) 0-5%
(b) 5-10%
(c) 10-15%
(d) 15-20%
(e) Over 20%
259. Indicate the analysis procedure used for TSS determination at the mill.
(a) Standard Methods for the Examination of Water and Wastewater,
13th and/or 14th Edition.
(^3) UFA analysis procedure adopted on October 16, 1973, and any
subsequent amendments.
(c) Other (please describe)
021SSO
- 51 -
-------
Mill: Keyes Fibre
Location:
Waterville
VI. FUEL AND ENERGY
A copy of the API "Monthly Fuel and Energy Report" has been included in
this section to assist the mill in calculating (if information is not
already available) the answer(s) to the questions asked. The API sheets
should be used as a guide for computation only, do not return the pages
with the questionnaire.
260. Give the total purchased energy (fossil fuel, electricity, steam, etc.)
as equivalent millions BTU/ton of product (Items 1 to 9, less 10 from
API forms).
106,
261. Give the energy used for external treatment operations as equivalent
KWHr/ton of product.
021
- 52 -
-------
r
Mill:
Ksvss .-icr
Location:
Waterville
VIII. PROCESS SCHEMATICS
Attach separate general block diagrams for the three items listed below.
A. Water Treatment (if applicable) - Provide a general block diagram
showing the water treatment system used, chemical application points,
average flow, and disposal method for backwash water. If the mill has
a raw water analysis available please attach a copy.
B. Manufacturing Process Schematic - Provide a general schematic of
the total mill process to include water balance and all process
wastewater streams. (See note at start of Section V.) Wastewater
streams should be cross referenced to the effluent treatment system
schematic.
C. Effluent Treatment System - Provide a general schematic of the
effluent treatment system. Please key the diagram to the manufacturing
process block diagram so that the point of influent to the treatment
system for individual process sewers can be determined. Also show
all chemical application points; chemicals used; flow monitoring and
sampling points; average flow; size or area, volume, .and number of
each treatment system component; sludge recycle and volume; and
sludge dewatering/thickening system.
Additional information on the mill's wastewater treatment system is
also needed to complete the data request. Please provide answers to
'the following questions which pertain to your wastewater treatment
system. For questions which do not apply, indicate by writing N/A
(not applicable) on the space provided for the answer.
Primary Treatment
262. Give the following primary clarifier overflow rates:
a. Design
b. Current
, gpd/ft' at _
2
gpd/ft at
MGD
MGD
021502
- 53 -
-------
Mill:
Fibre
Location:
Waterville
Biological System
NA
For the biological system employed, please give answers to the appropriate
questions listed below:
System
Question
Answer
263. Aerated Stabilization a) Volume of the aeration zone
Basin
*
264. Activated Sludge
265. Trickling Filer
266. RBC
267. Post Storage
b) Connected horsepower for aeration
a) Volume of the aeration zone
b) Connected horsepower for aeration
c) MLSS (Mixed Liquor Suspended
Solids)
a) Volume of media
b) Surface area of filter
a) Surface area of RBC
a) Volume of storage
Mil. Gal.
Mil. Gal.
. 2
tt
Mil. Gal.
268.
If nutrient addition is used, please give the average BOD:N:P ratio,
BOD:N:P : :
Secondary Solids Removal
NA
269. Give the secondary clarifier overflow rates:
a, D'-aigii gpd/ft2 at • MGD
b. Current
gpd/ft at
MGD
0215S3
54
-------
7) A r? T T r
' "--'Vi II
^^IJ^iTUUTLCXAi^JSR™, FOLLO,.ISC
***. SS! Sr sir —
"WI5JI4
-------
Uli
AMERICAN PAPER INSTITUTE
MATERIALS AND ENERGY DIVISION
260 Modiion A»*nu>, N«- Va'li, N.Y, 10016
CONFIDENTIAL
MONTHLY FUEL AND ENERGY REPORT
Month. Year: Wov. 1977
(If this is a "period" mill, the
period reported is from Nov. 1
through Dec. 1 .) mo./day
mo./day
Company:.
Hill Location:
Hill Reference NO.
Region:
FOR API
USE ONLY
QJ Monthly Fuel and Energy Consumption Data
For each energy source used in the month, please enter to the nearest tenth information in
the way you monitor it most accurately. For example, in the case of fuel oil, you would pro-
bably enter thousands of barrels. But in the case of bark, you would probably enter Billion
BTU's as fired—obtained by applying the bark boiler's rated or estimated efficiency to its
metered steam output. Then apply the 8TU conversion factor you believe to be most accurate
for your operation to compute either Billions of BTU's as in the first case, or weight of
fuel at the specified moisture content as in the second case. (See list of average BTU
values of nominated fuels, over.) Limit reporting to energy used within the mill fence line,
thereby excluding energy used in wood harvesting, transportation and converting operations.
BILLION
ACTUAL CONVERSION BTU's as
FIRED
FUEL
UNITS
CONVERSION
FACTOR
Purchased Fossil Fuel & Enerq^
1. Purchased Electricity
2. Purchased Steam
3. Coal
k. Residual Fuel Oil («,&)
5. Distillate Fuel Oil (#2)
6. Liquid Propane Gas (L.P.G.)
7. Natural Gas
8. Other (specify)
9. Other (specify)
Millions KWH
Mi 1 1 ions IbS.
Thousands
Short Tons
Thousands *+2
Gal. Bbls.
Thousands ^2
Gal. Bbls.
Thousands Gallons
Mill ions Cu. Ft.
14.053 x 3.u • . 47.8
X .
X
9.245 x 6.3 . 58.2
X
X
X
X
X
10. LESS ENERGY SOLD:
SUB TOTAL [Aj (I to «i l*« 10:) ' '
Self Generated and Waste Fuels
II. Hoggeo fuel: (Wood & Bark)
12. Bark: (Enter separately, if
available, bark obtained in
debarking of pulpwood)'
13. Municipal Waste
!*», Spent Liquor (oven dry basis)
15. Self -Generated
Hydroelectric Power
16. Other (specify)
17. Other (specify
Thous. Short Tons
(50% moisture
content)
Thous. Short Tons
(50% moisture
content)
Thous. Short Tons
(50% moisture
content)
Thousands Short
Tons of Sol ids
Millions KWH
im r
X
X »
X
X
X 3.*» -
X
(1? "
Sus TOTAL yjj (11 to 17): ••• — ,. ° ~ • " • •*•
i—i . , •. - . - - » . in 6' o
r.RAND TOTAl ra
-------
Please enter production for the month i r> thousands of short tons, to the nearest tenth.
Mills which use both their own and purchased pulp will enter separate data for "Integrated
Paper and Paperboard" and "Monintegrated Paper and Paperboard."
I. Pulp (dried and wet lap): Report dried and wet lap pulp (reported on a dried basis).
2. Integrated Paper and Paperfaoard; Report primary product (excluding converted products)
manufactured from on-site pulp production, as normally measured.
3. Honinteqrated Paper and Paperboard: Report primary product (excluding converted products)
manufactured from off-site pulp production and/or waste paper, as normally Measured.
(thousand short tons)
I. Pulp (dried and wet lap on dried basis):
2. Integrated Paper t, Paperboard:
3. Nonintegrated Paper S. Paperboard:^
4. TOTAL PRODUCTION [2:
^735.0
|ll_lj Please compute millions of BfU's used per ton of output for both "Subtotal BTU's fro*
Purchased Fossil Fuel and Energy" and "Grand Total BTU's."
I.
2.
Purchased Energy Per Ton
Subtotal S3:
106.0
Total Up
Total Energy Per Ton
2.3
mi II ion STU's/ton
46.1
mi 11 ion BTU's/ton
Grand Total {c|: 106.0 —
Total jg: 2.3 ~~
Explanation of month to r?onth changes in eneryy use:
!) If the milt's energy use per unit of output (either purchased and/or total) for
this month varied 25% or more from that in the previous month, please explain:
2) Has this mill put into operation during this month additional equipment for effluent
and emission control?
YES NO x
If yes, what net additional energy will this additional equipment require in a full
month at current operating rates?
Steam: Million Ibs. Electricity: Millions KWH (Calculate
on basis of additional horsepower to be used)
The average temperature of incoming water for the month was J?P degrees fahrenheit.
Suggested Average Conversion Factors To Obtain Billion BTU's (Question I)
Purchased Steam (Ho condensate return) 1.3
Purchased Steam (Condensate return) I.i
Coal 26.2
Residual Fuel Oil 6.3
Distillate Fuel Oil 6.0
L.P.C. 0.092
Natural Gas 1.03
Hogged Fuel 7.7 (50% moisture content).
Earn _JjLP_ (50% moisture content)
Spent Liguor I 3.**
Please return by the 2lst of tne
following month to:
American Paper Institute
Raw Materials and Energy Division
260 Madison Avenue
New York, M.Y. 10016
Tel. (212) 833-8087
Name:
Signature:_
Telephone: (
JHO
Juae.J976
-------
PROJECT
MILL NO.
COMR BY
CHK. BY
JOB NO.
DATE
Products:
6 Ka"NONFOOD (V\o!-C?tD PULP
Average Tons /Day:
3. 0
Check file for updated data;
Wastewater .
- . .
Flow, Kgal
ROT) 1h -,• - - - -- '- ----- -
TSS, lb; .;:...;
Check Schematics: ^
.-.;;•;..
;
, . . s . . . .
. .
- • - ;
. .
, Per D
3^3
- 3-1-0 g
-. ..:-*/.OJ5
... . . , .
• ••••
WtiS?
Raw ....I. Final - - -
ay Per Ton "..;.. Per Day Per Ton
1 20.8 :
- -^7,1-4- ^
" • ' T^
; a i;T---i -----;
•: - :• • •
. ' - j
- -
•'• -; - • - •
?^?££J™;
PDTW'.... -
'.
, . . .
FORM 00.01 REV. 12/78
Edngrd C. Jordan Co., Inc. |M
-------
LARGE SIZE PROCESS SCHEMATICS ARE AVAILABLE IN THE
FILE CONTAINING THE ORIGINAL 308 SURVEY RESPONSES
FOR THE FOLLOWING FACILITY:
-/f=£> r7 ^ /t (? (l
• •••--.
NAME: _ f=-/f=£> r7 ^ /t (? o
' • •••--.
LOCATION:
021SS8
-------
PcrmilNo. ME0000337
Application No.
AUTHORIZATION TO DISCHARGE UNDER THE
NATIONAL POLLUTANT DISCHARGE ELIMINATION SYSTEM
PERMIT MODIFICATION
In compliance wii.h the provisions of the Federal Water Pollution Control Act, as amended,
(33 US.C. 1253 ct. s.>q; the "Act"),
the Keyes Fiber Company;-.
(Waterville Plant):: . '
is authorized to discharge from a facility located at
Upper College Avenue
Waterville, ME 04901
to receiving waters named
Kennebec River
in accordance with effluent limitations, monitoring requirements and other conditions set forth
in Parts I, II, and III hereof.
This permit shall become effective 30 days from the date of signature, replacing
the permit issued on July 21, 1975.
This permit and the authorization to discharge shall expire at midnight, April 30, 1979.
Signed this / / day of W{,-4/ , / / 7 /.
1 • ff f
Leslie Carothers, Director
Enforcement Division
Environmental Protection Agency
021599
!
I fPA Fo,m.3320-4 flO_73l
!
-------
PARTI
B
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021600
-------
PART I
3 «r 8
IVin.it NO. HEQ000337
C. MONITORING AND REPORTING
I. Representative Sampling
Samples and measurements taken as required herein shall be representative of the volume
and nature of the monitored discharge.
2. Reporting . -.
Monitoring results obtained during the previous 1 month^ shall .be summarized for
each mouth and reported on a Discharge Monitoring Report Form (EPA No. 3320-1),
postmarked no later than the 2Sth day of the month following the completed reporting
period. The first report is due on (as previously reported) . A signed copy
of these, and all other reports required herein, shall be submitted to
the State at the follovjing address:
Division of Industrial Services
Maine Department of Environmental Protection
Hospital Road
Augusta, ME 04333
3. Definitions
a. The "daily average" discharge means the total discharge by weight during a calendar
month divided by the number of days in the month that the production or
commercial facility was operating. Where less than daily sampling is required by this
permit, the daily average discharge shall be determined by the summation of all the
measured daily discharges by weight divided by the number of days during the
calendar month when the measurements were made.
b. The "daily maximum" discharge means the total discharge by weight during any
calendar day.
4. Test Procedures
Test procedures for the analysis of pollutants shall conform to regulations published
pursuant to Section 304(g) of the Act, under which such procedures may be required.
5. Recording of Results
For each measurement or sample taken pursuant to the requirements of this permit, tne
permittee shall record the following information:
a. The exact place, date, and tim<; of sampling;
h. The dates the analyses were performed;
r. The pcrson(s> who performed the analyses; v M 16 0 1
\
-------
PARTI
P;i(y 4 01 8
Pciinii NO. ME0000337
d. The analytical techniques or methods used; and
e. The results of all required analyses.
fi. Additional Monitoring by Permittee
If the permittee monitors any pollutant at the location(s) designated herein more
frequently than required by this permit, using approved analytical methods as specified
above, the results of such monitoring shall be included in the calculation and reporting of
the values required in the Discharge Monitoring Report Form (EPA No. 3320-1}. Such
increased frequency shall also be indicated.
7. Records Retention
All records and information resulting from the monitoring activities required by this
permit including all records of analyses performed and calibration and maintenance of
instrumentation and recordings from continuous monitoring instrumentation shall be
retained for a minimum of three (3) years, or lon^or if requested by the lUnjional
- Administrator or the State water pollution control agency.
021602
-------
PART II
1'apc 5 Or 8
IVimiiM... ME0000337
A. MANAGEMENT HEQUIRKMENTS
1. Change in Discharge
All discharges authorised heroin shall ho consistent with tlio terms and conditions of this
permit. The di?eharge of any pollutant identified in this permit more frequently than or
at a level in excess of thai authorized shall constitute a violation of the permit. Any
anticipated facility expansions, production increases, or process modifications which will
result in new, different, or increased discharges of pollutants must be reported by
submission of a new Nl'DKS application or, if such changes will not violate the effluent
limitations specified in this permit, by notice to the permit issuing authority of such
changes. Koilowing such notice, the permit may be modified to specify and limit any
pollutants not previously limited.
2. Noncompliance Notification
If, for any reason, the permittee does not comply with or will be unable to comply with
any daily maximum effluent limitation specified in this permit, the permittee shall
provide the Regional Administrator and the State with the following information, in
writing, within five (5) days of becoming aware of such condition:
a. A description of the discharge and cause of noncompliance; and
b. The period of noncompliance, including exact dates and times; or, il not corrected,
the anticipated time the noncompliance is expected to continue, and steps being
taken to reduce, eliminate and prevent recurrence of the noncomplying discharge.
3. Facilities Operation
The permittee shall at all times maintain in good working order and operate as efficiently
as possible all treatment or control facilities or systems installed or used by the permittee
to achieve compliance with the terms and conditions of this permit.
4. Adverse Impact
The; permittee shall take all reasonable steps to minimize any adverse impact to navigable
waters resulting from noncompliance with any effluent limitations specified in this
permit, including such accelerated or additional monitoring as necessary lo determine the
nature and impact of the noncomplying discharge.
5. bypassing
Any diversion from or .bypass of facilities necessary to maintain compliance with the
terms and conditions of this permit is prohibited, except (i) where unavoidable to prevent
loss of life or severe property damage, or (ii) where excessive storm drainage or runoff
would damage any facilities necessary for compliance with the effluent limitations and
prohibitions of this permit. The permittee shall promptly notify the Regional
Administrator and the State in writing of each such diversion or bypass.
02160?
-------
PART II
6 <>f 8
rcrmiiNo. ME0000337
6. Removed Substances
Solids, .sludges, filter backwash, or other pollutants removed in the course of treatment or
control of was:ewaters shall be disposed of in a manner such as to prevent any pollutant
from such materials from entering navigable waters.
7. Power Failures
In order to maintain compliance with the effluent limitations and prohibitions of this
permit, the permittee shall either:
a. In accordance wilh the Schedule of Compliance contained in Part !, provide an
alternative power source. sufficient to operate the wastcwater control facilities;
or, if such alternative power source is not in existence, and no date for its implementation
appears in Part 1,
b. Halt, reduce or otherwise control production and/or all discharges upon the
rcductior
facilities.
reduction, loss, or failure of the primary source of power to the wastewater control |
B. KKKI'ONSIIilLlTIES
1. Right of Entr,-
The permittee shall allow the head of the State water pollution control agency, the
Regional Administrator, and/or their authorized representatives, upon the presentation of
credentials:
a. To enter upon the permittee's promises where an effluent source is located or in
which any records are required to be kept under the terms and conditions of tins
permit; and
b. At reasonable times to have access to and copy any records required to be kept under
I
the terms find conditions of this permit; to inspect any monitoring equipment or I
monitoring method required in ;his permit; and to sample any discharge of pollutants.
2. Transfer of Ownership or Control
In the event of any change in control or ownership of facilities from which the authorized
discharges .-manate, the pr-rmitlee shaJl notify the succeeding owner or. controller of the
existence of this permit by letter, a copy of which shall be forwarded to the Regional
Administrator and the State water pollution control agency.
4»
3. Availability of Report a
Kxcopt for data di-tcrmincd to be confidential under Section 308 of the Act, a!! reports
prepared in accordance with the terms of this • rmit shall be available for public
021G04
-------
PART II
PapC 7 Of 8
Hermit No. ME0000337
inspection at the offices of the State water pollution control agency and the Regional
Administrator. As required by the Act, effluent data shall not be considered confidential.
Knowingly making any false statement on any sudi report may result in the imposition of
criminal penalties as provided for in Section 309 of the Act.
4. Permit .Modification
After notice and opportunity for a hearing, this permit may be modified, suspended, or
revoked in whole or in part during its term for cause including, but not limited to, the
following:
a. Violation of any terms or conditions of this permit;
b. Obtaining this permit by misrepresentation or failure to disclose fully all relevant
facts; or .
c. A change in airy condition that requires cither a temporary or permanent reduction or
elimination of the authorized discharge,
5. Toxic Pollutants V
Notwithstanding Part II. R-4 above, if a toxic effluent standard or prohibition (including
any schedule of compliance specified in such effluent standard or prohibition i is
established under Section 307(a) of the Act for a toxic pollutant which is present in ths?
discharge and such standard or prohibition is more stringent than any limitation for sm-h
pollutant in this permit, this permit shall be revised or modified in accordance with the
toxic effluent standard or prohibition and the permittee so notified.
G. Ciui7 one? Criminal Liability
Except as provided in permit conditions on "Bypassing" (Tart II, A-5) and "Power
Failures" (Part II, A-7), nothing in this permit shall be construed to relieve the permittee
from civil or criminal penalties for noncotnpliance.
7. Oil u;:d Hazardous Substance Liability
EV
Nothing in this permit shall be construed to preclude the institution of any legal action or
relieve the permittee from any responsibilities, liabilities, or penalties to which the
permittee is or may be subject under Section 311 of the Act.
8. State Laws
Nothing in this permit shall be construed to preclude the institution of any legal action or
relieve the permittee from any responsibilities, liabilities, or penalties established pursuant
to any applicable Rtat«> law or regulation under authority preserved by Section 510 of the
Act.
021605
\
-------
PART u
l'.>i:e 8 of 8 •
Permit NO.ME0000337
9. Property Rights
The issuance of this permit docs not convey any property rights in cither real or personal
property, or any exclusive privileges, nor docs it authorize any-injury to private property
or any invasion of personal rights, nor any infringement of Federal, Slate or local Jaws or
regulations.
10. Severability
The provisions of this permit arc severable, and if sny provision of .this permit, or the
application of ;iny provision of this permit to any circumstance, is held invalid, the
application of such provision to other circumstances, and the remainder of this permit,
shall not be affected thereby.
PART III
OTHER REQUIREMENTS
021606
-------
ESTABLISHED 190}
FORMKD FIBRE PRODUCTS
I •
PLEASE ADDRESS REPLY TO:
WATERVILLE, MAINE 04901
TEL. 207 873-3351
160 SUMMIT AVENUE - MONTVALE. NEW JERSEYO7645
November 7, 1977
U.S. EPA Pulp & Paperboard Survey
E. C. Jordan Co.
P.O. Box 7050 Downtown Station
Portland, Maine
Attn: Mr. Willard Warren
Dear Mr. Warren:
Enclosed is a completed copy of the Environmental Protection Agency
Survey Form, Pulp, Paper and Paperboard Industry for Integrated Mills,
Part I.
We completed only the questions pertaining to the groundwood
operation at Shawmut.
Very truly yours,
CFB/mbc
Enclosure
C. P. Bean
Manager, Process Engineering
021C07
-------
PLEASE ADDRESS REPLY TO:
WATER VILLE, MAINE 04901
TEL. 207 873-3351
IftO SUMMIT AVKNUK • MONTVAI.K. NKW JKKSKVO7645
January li, I9?8
-'U.S. EPA Pulp and Paperboard Survey
E. C, Jordan Co.
P. 0. Box 7050 Downtown Station
Portland, Maine 04112
Attn: Mr. Willard Warren
Dear Mr, Warren:
Enclosed is a completed EPA survey form Pulp, Paper and Paperboarc
Industry Non-Integrated Kill Part II for Keyes Fibre plant at
Waterville, Maine.
Very truly yours,
.-"V
'
CFB/mbc
Enclosures
cc: E. J, Reidman
Clarence F. Bean
Manager, Process Engineering
-------
ENVIRONMENTAL PROTECTION AGENCY
SURVEY FORM
PULP, PAPER, AND PAPERBOARD INDUSTRY
NON-INTEGRATED MILLS
PART I
0
I. MILL BACKGROUND DATA
A, Mill & Division Name: Keyes Fibre Company
Address: P.O. Box ^60, Ifenatchee, Jfash.
: 509 , 663-6537
Corporate Affiliation (if applicable)
ZIP: 98801
Contacts and Title: (Use an asterisk next to the responsible personnel
completing the survey form).
Charles Gurnard
* Pat Van Winkle.
Paul Pall
Clarence Bean
Plant Manager
Plant Controller
Group Leader, Hesearch
Manager, Process Engineering
B. Age of Mill
1. Year of initial construction "-*
2.
Please give the year of initial startup and each year since 1952 in
which any major modifications or permanent shutdowns were made which
significantly affected the composition or amount of effluent from
the mill.
a. Added Paper Machine Saveall(s)
b. Added New Paper Machine(s)
Year(s) of
Initial Startu
Year(s) of Waste
Significant Modification
or
Permanent Shutdown
u
'
(3) StfBCO-SAVEAL! Significant Modification
9/15/77 WT ~ n
(l) SWSCO-SAVEALi Significant Modification f*
021C09
-------
Mill:
t'cyrc cTDnp rn
j\i_ r *„,.) ; 1 .J.\i. M-'*
Paper Machine Rebuild(s)
Locacion:
HEWCMEE
Year(s) of
Initial Startup
Year(s) of Waste
Significant Modification
or
Permanent Shutdown
d« Added Stock Prep. System
e. Added Broke Storage
f• Elimination of Paper Machine(s)
Other (Please List)
INSTALLED STOCK CLEANING
SYSTEM
7/1/75
SIGNIFICKIT : IDDIFICATI ON
021C10
-------
Mill:
KEYES FHRE CO.
Location:
:!
-------
Mill:
KEYES FISRE C1).
Location:
B; Products (continued)
c. Groundwood Specialties
d. Other WASTE MOLDED PULP
13. Wood Free Printing, Writing
and Related
a. Uncoated Free Sheet Printing
b. Clay (50% or more Kaolin)
Coated Free Printing
c. Uncoated Writing and Related
d. Uncoated Solid Bleached
Bristols
e. Clay (50% or more Kaolin)
Average Daily Maximum Day Maximum Month
Air Dry* Air Dry* Air Dry*
Tons/day Tons/day Tons/day
f.
Coated Solid Bleached Bristols
Other
14. Cotton Fiber Papers
a. Writing and Related
b. Technical
Other
c.
15. Thin Papers
a. Carbonizing
b. Cigarette
c. Other
16. Packaging and Industrial Converting
a. Unbleached Kraft
b. Bleached Kraft
c. Other
^Measured at the winder or pulp dryer.
26.5
26.4
26V
792
i
021C12
-------
Mill:
KFYES FIORE CO.
Location:
Vin.ATCHEE, HA
B. Products (continued)
17. Specialty Packaging and
Industrial Converting
a. Tape Backing
b. Saturating
c.
Gasket
d. Other (please list)
Average Daily Maximum Day Maximum Month
Air Dry* Air Dry* Air Dry*
Tons/day Tons/day Tons/day
18.
19.
Sanitary Tissue
Unbleached Kraft Paperboard
(80% or more unbleached Kraft pulp)
a. Linerboard
b. Folding
c. Other
20.
Semi-Chemical Paperboard
(75% or more semi-chemical pulp)
a.
b.
Corrugating
Other
21.
Bleached Paperboard
(not less than 80% bleached chemical wood pulp)
a. Clay Coated Bleached Food
Board
b. Uncoated Bleached Food Board
c. Bleached Linerboard
d. Folding
e.
*Measured at winder or pulp dryer.
-------
Mill:
KEYES FBRE CO.
Location:
HEUATCHEE, HA
B. Products (continued)
22, Recycled Paperboard
a. Linerboard
b. Corrugating
c. Chip & Filler Board
d. Folding
e. Set-Up
f. Gypsum Wall Board
g. Other
a.
23. Construction Paper and Board
Construction Paper
Wet Machine Board
Insulating Board
Hard Pressed Board
Other
b.
c.
d.
e.
Average Daily Maximum Day Maximum Month
Air Dry* Air Dry* Air Dry*
Tons/day Tons/day Tons/day
*Measured at the winder or pulp dryer.
021G14
-------
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Mill: Ks^es i'ibreJ:c: .. . Location: Wenatchee, Wash.
IV._ MANUFACTURING PROCESS AND INTERNAL PQLLUTIQN_CONTROT._PRArTTrES
A. General
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
B. Paper Mill
182. How many paper machines does mill have?
(3) Molding Machines 3«
183. Give the number of paper machines the mill has which utilize savealls,
or similar devices, for fiber recovery.
3i
(3) Molding Machines utilize Sweco Savealls_.
184. Give the number of paper machines the mill has which have savealls,
or similar devices, that permit reuse of clarified water.
3,
(3) Molding Machines reuse clarified water.
. Additional Information
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
021C22
-------
Mill: Location:
V. WATER USAGE AND EFFLUENT TREATMENT PRACTICES
Instructions for Completing Section V
Section V requests information on the mill's wastewater treatment prac-
tices. In Section VIII a general schematic of the effluent treatment
system is requested. You have the option of providing any of the data
requested in Section V on the schematic. If you do this, please in-
dicate on the question(s) involved that the data is presented on the
schematic.
A. Water Usage
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
B. Background Data
211. Indicate the method(s) of disposal of the mill wastewater.
-(a> Direct
(b) Indirect
Self-contained
(d) Other (please describe)
212. Please give the year in which the following portions of the mill's
existing wastewater treatment system were started up.
v
Year of Startup
a. Primary Treatment System I960
b« Secondary Treatment System ,.^-^ft ._.-• -.- / - '~<~ - '
C. Indirect Discharger (discharge to a POTW:) please provide the
following information:
215. is raw wastewater pretreated externally prior to discharge to the
POTW? (Pretreatment is considered to be any treatment device external
from the mill production processes which is utilized prior to a pri-
mary and secondary treatment system, or prior to discharge by an
indirect discharger to a POTW.)
021G23
No
-------
Mill:
Location:
216.
219.
221.
Give the treatment process used by the POTW to which your mill discharges.
(Include biological and physical-chemical treatment if applicable)
(a) Activated sludge
(b) Aerated lagoon
(c) Oxidation ditch
(d) Trickling filter
(e) None
(f) Other (indicate type)
Give the preliminary treatment method used, if any.
(a) Neutralization
(b) Screening (indicate type used)
(c) Other (please describe)
225.
Indicate the primary treatment method used, if applicable.
(a) Clarifier
(b) Sedimentation lagoon
(c) Mechanically cleaned sedimentation lagoon
(d) Other (please describe)
(e) Not applicable
Give the type of biological treatment used, if applicable.
(a) Storage oxidation basin
(b) Aerated Stabilization basin
(c) Activated sludge (air or oxygen)
(d) Other (please describe)
(e) Not applicable
-------
Mill: Location: S
D. Direct Discharger please provide the following information:
228. Is wastewater discharge continuous or non-continuous (effluent stored and
discharged when receiving water conditions allow) when production
facilities are operating?
(a) Continuous
£y Non-continuous - daily
(c) Non-continuous - seasonally/intermittent
E. Preliminary Treatment (Direct Discharger)
230. Give the preliminary treatment method used, if any.
(a) Neutralization
(b) Screening (indicate type used) SWECO
(c) Other (please describe)
F. Primary Treatment (Direct Discharger)
232. Indicate the method used for primary treatment.
(a) Clarifier
/^tb) } Sedimentation lagoon
(c) Mechanically cleaned sedimentation lagoon
(d) Other (please describe)
G. Biological Treatment (Direct Discharger)
236. Give the type of biological treatment used
(a) Storage oxidation basin
(b) Aerated stabilization basin
(c) Activated sludge (air or oxygen)
(d) Other (please describe)
-------
Mill:
Location:
H. Secondary Solids Removal
237. If secondary clarification is used, what is the method used?
(a) Clarifier
(b) Reactor clarifier
(c) Settling basin
(d) Other (please indicate)
238. Is a holding pond utilized after secondary treatment?
(a) Yes
(b) No
I. Spray Irrigation
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
J. Sludge Handling and Disposal
240. Indicate the method used for sludge disposal.
(a) Lagooning
(b) Landfill
(c) Hog fuel boiler
(d) Other (please describe) Municipal Land Fill
K. Foam Control
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
L. Cost Information
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
-------
Mill: Keyes Fibre Co,
Location: Wenatchee, Wash.
M.
N.
251-254.
Site Conditions and Availability of Land
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
Wastewater Characteristics
Give the (1976) wastewater loads indicated below:
Indirect and Direct
- . Dichargers
Please Answer
c.
IV.
•VII.
Direct Discharger
Only
Please Answer
Flow, MGD
(1) Average Day
(2) Maximum Day
(3) Maximum Month
BOD, Ibs/day .
(1) Average Day
(2) Maximum Day
(3) Maximum Month
TSS, Ibs/day
(1) Average Day
(2) Maximum Day
(3) Maximum Month
FUEL AND ENERGY
NO QUESTIONS FOR THIS SECTION ARE TO BE ANSWERED IN PART I.
PRIORITY POLLUTANTS
(251)
Paper
Mill
(252) (253)
Secondary
Treatment
Total Raw System
Wastewater Effluent
o7
&y$z-
(254)
Final
Effluent
»|£?
10
20, 14
• /?, see-'
\*
'••!. 5f
321. 100
I?L 5io
L.
See Next Page
VIII. PROCESS SCHEMATICS
>-./bi
.1 >~^
j \. .M.1,'-..'- '
NO QUESTIONS FOR THIS SECTION ARE TO BE ANSWERED IN PART I.
021G27
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021C30
-------
Mill: Keyes ribre Co.
Location: ^natchee, Vseh.
VII. PRIORITY POLLUTANT COMPOUNDS
Please fill in the following information for those priority pollutants
which, to your knowledge, are in your raw water supply, or used, or
generated in any of the processes in the mill (refer to the following
pages for the priority pollutant list). Use the number shown to identify
the compound.
It should be noted that many mills may be using quantities of the listed
chemicals as additives, cleaning solution, or solvents which are purchased
and referred to by a trade name. Please supply trade names of all pro-
prietary type chemicals used in the mill.
Compound Number
or Trade Name
(130) Rosin Size
Process Where
Compound is
Used or Generated
Internal Sizing
Describe Use
Frequency
Sampling or Monitoring
Program for Compound
(Yes or No)
Quantity
238,050 Ibs/year (June '?6- Yes (in product)
(130) Neuphor 100
189,800 Its/year
May ' (7)
Yes (in product)
4121631
-------
PART I
Question
Number
Question
Number
Question
Number
Question
Number
Question
Number
Question
Number
Question
Number
-------
'" •" / r/y ,
} I /// /v '•'
/.'"'•<
ENVIRONMENTAL PROTECTION AGENCY
SURVEY FORM
PULP, PAPER, AND PAPERBOARD INDUSTRY
NON-INTEGRATED MILLS
PART II
I. MILL BACKGROUND DATA
A. Mill & Division Name: Keyes Fibre Company
Address: P.O. jox 4-60, Wenatchef, Washlr.gton_ ZIP: 98801
Telephone: 509 / 663-853?
Corporate Affiliation (if applicable)
Contacts and Title: (Use an asterisk next to the responsible personnel
completing the survey fprm)
*Charles Gurnard
Pat Van Winkle
Clarence Bean
Plant Manager
Plant Controller
Manager, Process Engineering
B. Age of Mill
1-2. DELETED - ANSWERED IN PART I
II. PRODUCTION INFORMATION
3-23. DELETED - ANSWERED IN PART I
III'. PROCESS RAW MATERIALS
24-164. DELETED - ANSWERED IN PART I
-------
Mill: Keyes Fibre
Location: Wenatchee
IV. MANUFACTURING PROCESS AND INTERNAL POLLUTION CONTROL PRACTICES
A. General
165. Give the typical production days per year
360,
166. High level alarms - do chemical and stock tanks have operable
high level alarms to prevent spills?
(a) Yes
(b) No
^y To the extent possible
Explanation (if needed)
167. pH or conductivity monitor of internal sewers - Do sewers have such
devices to detect or divert spills?
(a) Yes
@ No
(c) To the extent possible
Explanation (if needed) Septic Tank
168-181. Is the cooling water collected and reused from the following locations:
Indicate answer using one of the following responses: (a) Yes; (b) No;
(c) Seasonal; (d) To Extent Possible; (e) Not Applicable.
168. Air Compressor Cooling Water
169. Dryer Drainage Condensate Cooling
170. Lube Oil Cooling
171. calendar Cooling Heat Exchangers
172. Rewinder Brake Cooling
172A. Vacuum seal water reused
021C34
x
X
x
X
X
-------
Mill: Keyes Fibre
Location:
(a) Yes; (b) No; (c) Seasonal; (d) To Extent Possible; (e) Not Applicable
a _ b c d e
173. Paper Machine Clutch Cooling x
174. Cooling in Power Plant x
175. Feed Water Pump Bearings x
176. Power Plant I.D. Fan Bearings x
177. Other Bearing Cooling x
178. Refiner Cooling x
179. Motor Control Center Cooling x
180. Water Chiller x
181. Air Conditioning x
B. Paper Mill
182-184. DELETED - ANSWERED IN PART I
021G35
-------
Mill: Keyes Fibre
Location:
Wenatchee
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021G3R
-------
Mill:
Keves fr'icrs
We r.a tehee
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021C37
- 37 -
-------
Mill: Keyes Fibre
Location: Wenatchee
194. Does the mill have a stock spill collection system, prior to external
treatment facilities?
(a) Yes
@ No
(c) Partial
195. if the answer to the preceding question is (a), describe the collection
system's function.
(a) Collected and discharged to the sewer at a controlled rate
(fa) Collected and reused in the process
(c) Other (please describe)
196. Give the frequency of waste significant grade changes; also, if
possible, give the stock quantity sewered. N
197. is the mill central storage of white water (a) and slush broke (b) adequate
with regard to effluent discharge?
a. White Water
<0 Yes
(b) No
(c) To the extent possible
(Explanation, if needed)
b. Slush Broke
(a) Yes
(b) No
(c) To the extent possible
(Explanation, if needed)
021C38
-------
Mill: Keygs Fibre Location: Wenatchee
198. Are special provisions made for spills, screen rejects, and excess
materials from coating or sizing systems?
.(a) Yes
(b) No
(c) Limited No coating or sizing systems
199. Does the mill eroploy organic solvent coating or saturating operations?
(a) Yes
200. If yes, please give the type and quantities (Ibs/day) of organic
solvent used.
201. Give the average daily organic solvent coated or saturated paper
produced.
N°ne tons/day
021G39
-------
Mill: Keyes Fibre
Location:
Wenatchee
202. Please indicate effluent from the combined_papermachine facilities
as follows: (i.e., total flow from all machines)
Waste Source
Volume GPM
Suspended Solids
(if applicable)
Ibs/day
a. Centricleaner and machine
screen rejects
b. Couch pit, real box, and
any other unclarified
Whitewater overflows
c. Thick stock spills, dumps,
washups from stock prepara-
tion area and machine
Sweco
d. Excess clarified Whitewater
e. Cloudy water from vacuum
systems, or pump sealing
applications
f. Clear water discharges
i.e., cooling services,
condensate, other non-
process services
g. Other effluent sources
not included above
h. Total papermill effluent
None
None
None
100,
None
200,
None
300,
gal/day
i. Is (f) discharged via process sewer or [separately]? (Circle answer)
/f^"
Additional Information
203. Does the mill have a program for disposal of old electrical transformers?
(a) Yes
(b) No
204. Please give the number of people employed at your mill. ^1«
-------
Mill: Keyes Fibre Location: Wenatehee
V. WATER USAGE AND EFFLUENT TREATMENT PRACTICES
Instructions for Completing Section V
Section V requests information on the mill's wastewater treatment practices.
In Section VIII a general schematic of the effluent treatment system is
requested. You have the option of providing any of the data requested in
Section V on the schematic. If you do this, please indicate on the
question(s) involved that the data is presented on the schematic.
A. Water Usage
205. Indicate the source and amount of process water.
((a) Surface (i.e., river, lake or reservoir) . 3.W MGD
(b) Groundwater MGD
(c) Other (please describe) MGD
*
206. Does the quality of the raw water limit the reuse of water in this mill?
(a) Yes - explain
© No
207. Indicate the source and amount of the mill's cooling water.
((a) Surface .288 MGD
(b) Groundwater MGD
(c) Other (please describe) MGD
208. Indicate the source and amount of the mill's boiler feed water. NA
(a) Surface ^_^ MGD
(b) Groundwater _____ MGD
(c) Other (please describe) MGD
021G41
-------
Mill: Keyes Fibre
Location:
w en 2 i
209. Describe treatment used for boiler feed water conditioning.
No boiler used
210. Give the disposal method now employed for boiler blowdown water. NA
(a) Sewered to treatment plant
(b) Directly discharged
(c) Directly discharged with pH adjustment
(d) Directly discharged after cooling
(e) Other (please describe)
B. Background Data
211-212. DELETED - ANSWERED IN PART I
213. How is cooling water disposed?
Qi) Separate discharge to receiving stream. By-pass lagoon
(b) Combined with process waters before treatment.
(c) Combined with treated process waters.
(d) Recycled.
C. Indirect Discharger please provide the following information: NA
214. Name and location of POTW which handles your wastewater.
215-216. DELETED - ANSWERED IN PART I
217. Are there specific pretreattnent requirements of limits upon pollutant
parameters imposed by the POTW system to which you discharge?
NA
(a)
Jes
No
-------
Mill: Keyes Fibre
1- •
Location:
!18. If the answer to the preceding question was (a), please list the specific
pretreatment requirements or pollutant parameter limits imposed on your
mill by the POTW.
219. DELETED - ANSWERED IN PART I
220. If neutralization is practiced, fill in the following. MA
Chemical useci
221. DELETED - ANSWERED IN PART I
222. Are any chemicals or other settling aids added to the primary treatment
units?
(a) Yes
(c) To the extent necessary (intermittent)
223. Please show the wastewater streams which enter the secondary treatment NA
system (if applicable).
Process Source or Sewer No.* Flow.,MGD BOD, Ib/D TSS, Ib/D
a. Design Values Average Day
Maximum Day
Maximum Month
b. Primary Treatment Effluent Average Day
Maximum Day
Maximum Month
c. Other Average Day
Maximum Day
Maximum Month
*Process source or sewer number should be keyed to the mill process and
wastewater treatment schematics requested in Section VIII.
021G43
-------
_., Tnoaon- Wenatches
Mill; Keyes i'lbre.
224. Give the normal pH of the wastewater at the influent to the secondary NA
treatment system.
(a) 4-6
(b) 6-8
(c) 8-10
225. DELETED - ANSWERED IN PART I
D. Direct Discharger please provide the following information:
226. Name of effluent discharge receiving water
Columbia River
227. Enclose a copy of current or proposed NPDES effluent discharge limits. //
228. DELETED - ANSWERED IN PART I
229. If wastewater'discharge is seasonal or intermittant non-continuous,
approximately how many days out of the year do you discharge to the
receiving water.
(a) Less than 30 (f) 211-240
(b) 31-90 (g) 241-270
(c) 91-120 (h) 271-300
(d) 121-180 (i) 301-330
(e) 181-210 (j) 331-360
E. Preliminary Treatment
230. DELETED - ANSWERED IN PART I
231. If neutralization is practiced, fill in the following: NA
Chemical used
021G44
-------
Mill: Keyes Fibre
Location: Wenatehee
F. Primary Treatment
232. DELETED - ANSWERED IN PART I
233.
G.
234.
a.
Are any chemicals or other settling aids added to the primary treatment
units?
(a) Yes
© No
(c) To the extent necessary (intermittent).
Biological Treatment NA
Provide the following information for the biological treatment system
(if applicable).
Process Source or Sewer No.*
Design Influent Values
Flow, MGD BOD, Ib/D TSS, Ib/D
b. Primary Treatment Effluent
Average Day
Maximum Day
Maximum Month
Average Day
Maximum Day
Maximum Month
Other Wastewater Streams Which Enter the Biological Treatment Systems
Without Primary Treatment
c. Average Day
Maximum Day
Maximum Month
d. Average Day -
Maximum Day
Maximum Month
*Process source or sewer number should be keyed to the mill process and
wastewater treatment schematics requested in Section VIII.
021655
-------
Mill: Ke^es -"rore Location: Wens tehee
235. Give the normal pH of the wastewater at the influent to the secondary NA
treatment system.
(a) 4-6
(b) 6-8
(c) 8-10
236. DELETED - ANSWERED IN PART I
H. Secondary Solids Removal NA
237-238. DELETED - ANSWERED IN PART I
I. Spray Irrigation NA
239. Is treated wastewater used for irrigation?
(a) Yes
© No
(c) Partial
J. Sludge Handling and Disposal
240. DELETED - ANSWERED IN PART I
241. Give the percent solids of the sludge after devatering and prior to
disposal.
(a) 5-10%
(b) 10-20%
(c) 20-30%
(d) 30-40%
MU above 40%
242. Describe any leachate management practices performed at the mill for
sludges which are disposed of on land.
121C 4 6
-------
Mill: Keyes Fibre
Location:
Wenatches
K.
243.
Foam Control - (Wastewater treatment system only)
Does the mill use foam control measures?
(a) Chemical
(b) Physical Methods
(c) None
© Other - explain White water sprays
NA
021C47
-------
Mill: ™-K_ Location: __Jfen3tchee.
ouau JL n 1.^1....»»..-. — ..
Provide cost data indicated for effluent treatment system in 1976 dollars.
Use the cost multiplier factors, which follow, to convert to 1976 dollars.
L. Cost Information
244.
Use the cost multiplier tactors, wiu.cu J.UJ..L
Annual Operation
a.
b.
loca
effluent waste load reduction.
External Treatment System
Construction Cost
20,531
Multipliers
12,378
to Convert Capital Cost to 1976 Dollars
1956 - 2.535 1963 =
1957 = 2.380 1964 =
1958 = 2.325 1965 =
1959 = 2.254 1966 =
1960 = 2.220 1967 =
1961 - 2.220 1968 -
1962 * 2.207
2.186
2.161
2.124
2.051
1.978
1.884
1969 =
1970 =
1971 =
1972 =
1973 =
1974 =
1975 =
1.794
1.689
1.564 .
1.485
1.317
1.242
1.100
*Factors to be considered in Annual Operation and Maintenance Costs
(0 & M Costs).
1. Manpower - both operators and maintenance personnel
2. Contracted services
3, Energy Cost
4. Trucks for hauling
5. Nutrients
6. Leased equipment
7. Disposal costs
8. Sludge handling
9. Sampling and analysis
10. Equipment replacement (except major capital)
Exclude Depreciation
021G48
-------
Mill: Keyes Fibre
Location:
Wenatches
245. For mills which discharge to a POTW, please give the annual user fee
with a breakdown for capital cost recovery and operation and maintenance
costs.
a. Capital Cost Recovery(if available)
b. Operation and Maintenance (if available)
c. Total Annual User Fee
246. Please give the basis used by the POTW to determine the raill's user
fee.
(a) Flow only
(b) BOD only
(c) TSS only
(d) Combination of parameters (please indicate)
(e) Unknown
M. Site Conditions and Availability of Land
247. Is there sufficient land for expansion of your wastewater treatment
system for BATEA?
(a) Yes
© No
(c) Unknown
248. Can the mill purchase land from adjoining property owners for possibj
expansion of the wastewater treatment system?
(a) Yes
|b) No
(c) Unknown
021C49
-------
Mill:
Keyes Fibre
Location:
VI ena tehee
249. Are the soil conditions in the land available for future expansion of
such a quality as to require special construction methods or special
facility equipment (i.e., ledge, water table and liners needed for
basins)?
(a) Yes
@ No
(c) Unknown
250. Miscellaneous Discharges - Indicate any wastewater discharges not
described in Section V which do not flow to the wastewater treat-
ment system.
N. Wastewater Characteristics
251-254. DELETED - ANSWERED IN PART I
255. Was the analysis procedure used for BOD measurement in accord with
the method presented in Standard Methods for the Examination of Water
and Wastewater?
((a) 13th Edition
(b) 14th Edition
(c) No (please describe other method used)
256. is a glucose-glutamic acid BOD standard analyzed?
(a) Yes
(b) No
021C50
-------
Mill:
JCeyes Fibre
Location:
Wenatchee
257. If the answer to the preceding question was (a), please indicate the
normal frequency of the analysis. NA
(a) Daily
(b) Weekly
(c) Monthly
(c"> Quarterly
(e) Semi-annual
(a) 0-5%
(b) 5-10%
(c) 10-15%
(d) 15-20%
(e) Over 20%
and
and the
between the BOD
-glutamic acid BOD standard.
259. Indicate the analysis procedure used for TSS determination at the mill.
(a) Standard Methods for the Examination of Water and Wastewater,
13th and/or 14th Edition.
(b) EPA analysis procedure adopted on October 16, 1973, and any
subsequent amendments.
(c) Other (please describe)
(d) None at mill
021C51
-------
Mill; Keyes Fibre
Location:
Wenatehee
VI . FUEL AND ENERGY
A copy of the API "Monthly Fuel and Energy Report" has been included in
this section to assist the mill in calculating (if information is not
already available) the answer(s) to the questions asked. The API sheets
should be used as a guide for computation cnly, do not return the pages
with the questionnaire.
260. Give the total purchased energy (fossil fuel, electricity, steam, etc.)
as equivalent millions BTU/ton of product (Items 1 to 9, less 10 from
API forms).
/
•^7 /
261. Give the energy used for external treatment operations as equivalent
KWHr/ton of product.
None
021C52
-------
Mill: Keyes Fibre Location: Wenatchee
VIII. PROCESS SCHEMATICS
Attach separate general block diagrams for the three items listed below.
'*•
A. Water Treatment (if applicable) - Provide a general block diagram
showing the water treatment system used, chemical application points,
average flow, and disposal method for backwash water. If the mill has
a raw water, analysis available please attach a copy.
B. Manufacturing Process Schematic - Provide a general schematic of *
the total mill process to include water balance and all process r—f
wastewater streams. (See note at start of Section V.) Wastewater / /
streams should be cross referenced to the effluent treatment system
schematic.
Effluent Treatment System - Provide a general schematic of the
effluent treatment system. Please key the diagram to the manufacturing
process block diagram so that the point of influent to the treatment
system for individual process sewers can be determined. Also show
all chemical application points; chemicals used; flow monitoring and
sampling points; average flow; size or area, volume, and number of
each treatment system component; sludge recycle and volume; and
sludge dewatering/thickening system.
Additional information on the mill's wastewater treatment system is
also needed to complete the data request. Please provide answers to
the following questions which pertain to your wastewater treatment
system. For questions which do not apply, indicate by writing N/A
(not applicable) on the space provided for the answer.
Primary Treatment
262. Give the following primary clarifier overflow rates:
2
a. Design gpd/f t at MGD
2
b. Current gpd/ft at MGD
Area of lagoons -
#1 Large Lagoon. 23,000 sq. ft. of area 2,480,000 gals.
#2 Small Lagoon 9,000 sq. ft. of area 1,008,000 gals.
021C53
-------
Mill: Keyes Fibre
263-268,
Biological System
For the biological system employed, please give sr.svers
questions listed below:
System
Question
263-
Aerated Stabilization a) Volume of the aeration zone
Basin
264. Activated Sludge
265. Trickling Filer
266,
RBC
Post: Storage
b) Connected horsepower fcr aera:
a) Volume of the aeration zrne
b) Connected horsepower for aerat
c) MLSS (Mixed Liquor Suspended
Solids)
a) Volume of media
b) Surface area of filter
a) Surface area of RSC
a) Volume of storage
268.
If nutrient addition is used, please give the
BOD:N:P : :
Secondary Solids Removal
269. Gi.ve. the secondary clarifier overflow rates:
a. Design gpd/f t2 at MGD
gpd/f t2 at MGI
b. Current
021C54
-------
PART II
CONFIDENTIALITY CLAIMED FOR THE FOLLOWING
Question
Number
Question
Number
Question
Number
Question
Number
Question
Number
Question
Nurber
Question
Number
021C55"
-------
AMERICAN PAPER INSTITUTE
RAW MATERIALS AND ENERGY DIVISION
:iO Madnon Av.nve. New York. N.Y. 10016
!{ CONF.DsHTIAL
ii MONTHLY FUEL **
Month, Year:
(If this is a "period" mill, the
period reported is from
through .) mo./day
mo./day
Company:_
Mi 11 Location:
Mill Reference SO.
Region:
FOR
'JS£
| 1 .1 Monthly Fuel and Energy Consumption Data
For each energy scjrce ur.ed in the month, please enter to the nearest tenth infr-rvii-on i
the way you monitor it most accurately. For example, in me Cdse of fuet oil. you -:. : pro-
bably enter thousands of barrels. But in the case of bark, you *culd srooably enter : lion
BTU's as fired—obtained by applying the bark boiler's rated or estimate; efficiency :: Us
metered steam output. Then apply the BTU conversion factor you believe :s be nost s—.-ate
for your operation to compute either Billions of BTU's as in the first case, or wei:-: :J
fuet at the specified moisture content as in the second case. (See list of average :*.
values of nominated fuels, over.) Limit reporting to energy used within the mill f»-^t line,
thereby excluding energy used in wood harvesting, transportation and converting operi: :is.
FUEL
UNITS
I'.LIQN
ACTUAL CONVERSION :":'» as
USE FACTOR FIRED
Purchaseo Fossil Fuel & Enerqv.
1. Purchased Electricity
2. Purchased Steam
3. Coal
k. Residual Fuel Oil1 (#5,6)
5. Distillate Fuel Oil (#2)
6. Liquid Propane Gas (L.P.G.)
7. Natural Gas
8. Other (specify)
3. Other (specify)
Mil lions KWH
Millions Ibs.
Thousands
Short Tons
Thousands *>2
Gal. Bbls.
Thousands kz
Gal. Bbls.
Thousands Gal Ions
Hi 1 1 ions Cu. Ft.
13 * 3.* - -.2
X
X .
X
X
X «
'S2 6^ x ' ~" • ' :: • ' •
X >
X .
10. LESS ENERGY SOLD:
Self
1 1.
12.
13.
SUB IOIAL (_AJ (1 to <1 less 10:) -- - -.-.,-
Generated and Waste Fuels
Hoggeo Fuel: (Wood &. Bark)
Bark: (Enter separately, if
available, bark obtained in
debarking of pulpwood)
Municipal Waste
|U. Spent Liquor (oven dry basis)
15.
16.
17.
Self-Generated
Hydroelectric Power
Other (specify)
Other (specify
Thous. Short Tons
(50% moisture ;
content) x •
Thous. Short Tons
(50% moisture
content) * •
Thous. Short Tons
(50% moisture
content) * •
Thousands Short j
Tons of Solids x
Mil 1 ions KWH ! * 3.1*
X
fl2ifi?;fi
SU3 TOTAL [§] (II to 17):
GRAND TOTAL [cl (A+B) : _I
-------
[I I j Mon thIy Producjtjon Oa t a
Please enter production for the month in thousands of short tons, to the nearest tenth.
Mills which use both their own and purchased pulp will enter separate data for "Integrated
Paper and Paperboard" and "Nonintegrated Paper and Paperboard."
I..
i.
2.
3.
H.
Pulp (dried and wet lap): Report dried and wet lap pulp (reported on a dried basis).
Integrated Paper and Paperboard: Report primary product (excluding converted products)
manufactured from on-site pulp production, as nornvatly measured.
Noniftegrated Paper and Paperboard: Report primary produce (excluding converted products)
manufactured from off-site pulp production and/or waste paper, as normally measured.
(thousand short tons)
Pulp (dried and wet lap on dried basis):_
Integrated Paper t Paperboard:
Monintegrated Paper S- Paperboard:
TOTAL PRODUCTION {ft
(H I J Please conpute nil I ions of BTU's used per ton of output for both "Subtotal 8TU*s from
Purchased Fossil Fuel and Energy" and "Grand Total BTU's."
I.
2.
Purchased Energy Per Ton
Subtotal S
million BTU's/ton
mil I ion 8TU's/ton
Total flJJ ~~
Total Energy Per Ton
Grand Total (c}; —
Total ((J:
Explanation of month eo month changes in energy use:
I) If the mill's energy use per unit of output (either purchased and/or total) for
this month varied 25% or more from that in the previous month, please explain:
2) Has this mill put into operation during this month additional equipment for effluent
and emission control?
VES NO
If yes, what net additional energy will this additional equipment require in a -full
month at current operating rates?
Steam; Million Ibs. Electricity: Mi.Hions KWH (Calculate
on basis of additional horsepower co be used)
The average temperature of incoming water for the month was degrees fahrenheit.
Suggested Average Conversion factors To Obtain Billion BTU's (Question l)
(Purchased Steam (No condensate return) J.3 Hogged Fuel
Purchased Steam (Condensate return) I. I Bark
Coal 26.2 Spent Liguor
Residual Fuel Oil 6.3
7.7 (50% moisture content)
g.O (50% moisture content)
iDist i 1 tate Fuel Oi 1
L.P.G.
Natural Gas
Please return by the 21st of the
fol lowing month to:
^ American Paper Institute
i Raw Materials and Energy Division
• 260 Madison Avenue
New York, N.Y. 10016
Tel. (2)2) 883-8087
6.0
0.092
_K03
Name:
Signature:
Telephone:
( )
Date:
-------
PROJECT
MILL NO.
Products:
COM P. av
CHK. BY
JOS NO.
DATE
Average Tons/Day:
Check file for updated data:
Wastewater
Flow, Kgal
BOD, Ib -
TSS, Ib
Check Schematics
ties: ]/
Raw
Per Day Per Ton
700
Final
Per Day Per Ton
021658
-------
LARGE SIZE PROCESS SCHEMATICS ARE AVAILABLE IN THE
FILE CONTAINING THE ORIGINAL 308 SURVEY RESPONSES
FOR THE FOLLOWING FACILITY:
NAME:
LOCATION:
021C59
-------
Permit Ho. WA 00349-2
Issuance Dace: May 13, 1975
Expiration Date: March 1, 1980
NATIONAL POLLUTANT DISCHARGE ELIMINATION SYSTEM
WASTE DISCHARGE PERMIT
*
State of Washington
DEPARTMENT OF ECOLOGY
Olympia, Washington 98504
In compliance with the provisions of .
Chapter 90.48 RCW as amended
and
The Federal Water Pollution Control Act Amendments of 1972,
Public Law 92-500
Keycs Fibre
NW DlvlHlon
P.O. Box 460
Wenatehee, WA 98801
Plant Location: Olds Station Receiving Water: Columbia River
Discharge Location: Sec. 15, T. 23 K.,
R. 20 E.W.M.
ry T.VIHIJ Mnl.luil wnml I'I lira Wnuarwny li
is authorized to discharge in accordance with the special
and general conditions which follow.
-
.-.j.i n v -. I.
Russell K. Taylor,'Regional Manager
' o£ K
..... .. _ 821CGO
Revised: February 22, 1977
-------
Pertnic no. VA 000349-2
SI. FINAL EFFLUENT LIMITATIONS AMU MONITORING RF.OUIRFV.FMT
Beginning Feb 22,. 1977, and lasting, through March 1, 1930, the Pcrnittee
is authorized to discharge treated process waters and non-contact cooling
waters subject to the following limitations and monitoring requirements:
Parameter
Process Waste Water
Flow,
Temperature
pit '.
" Bon5
TSS
Non-contact cooling waters
Flow
EFFLUENT LIMITATIONS
Daily Average
630,000 gallons
within the ranfie 6.0 to 9.0
93 Ibs.
155 Ibs.
300,000 gallons
pll
Parameter
Process Waste Viator
Production
Flow
(til
BOD
1 TSS
Color
Non-contnct Cooling Water
Flow wr.okly
Temperature weekly
ptl weekly
within the ronp.e 6.3 to tl.5
MONITORING REQUIREMENTS
Monitoring Frequency
weekly record
daily record
wonkly
WilMl'.l V
weekly
weekly
weekly
021G61
naily Maximum
630,000 gallons
70° F
Ibs.
310 Ibs.
300,000 gallons
70- F
Sanple Tyne
r.rnb
'.'ft In*. rr»M]ton I f.f*
24 hr. composite
24 hr. composite
24 hr. composite
grab
-------
i ci,;.. ..• i..i a
Permit No. KA 000349-2
FINAL EFFLUENT LIMITATIONS AND MONITORING REQUIREMENTS CON'T
Daily Average - Average of the measured values obtained over a calendar month.
. • ... , Daily Maximum - Greatest allowable value for any calendar day.
S2. MONITORING AND REPORTING - ,
The permittee shall monitor the operation and efficiency of all treatment
and control facilities and the quantity and quality of the waste discharge.
A record of all such data shall be maintained. The permittee shall monitor
the parameters as specified in conditions SI & 52 of this permit. '[
.'• . a. Reporting
t Monitoring results obtained during tlm previous month shall be reported
monthly and summarized and reported on a Discharge Monitoring Report Form
(EPA No. 3320-1) submitted no Inter th.in the 15th day of the month
following the completed reporting pcroid. The report shall be
sent to the Department of EcoloRy, 2802 Main Street, Union Gap,
Washington 98P03. Monitoring shall be started July 1, 1975, and
the first report is due August 15, 1976. . ;
b. Records Retention
Tho pnrrnlttnn nli.il J retain for n minimum of f.lirnn O) yonrn nil
rm'oi'ilH of mini I I or I lie. ni'l: I v t r Irn nn«t r<'urr1lii, I uc. 1 if>l Inr, nil rcpnrt'/i
of ri'cnriliiit'fi from cnntl.nuoun monitoring imitruiifint;tttoii« This
peroid of retention shnll be extended during tho course of any
unresolved litigation regarding the discharge of pollutants by the
permittee or tfhen requested by the Director.
c. Record in t; of Results
The permitce shall record each mensuronont or n.imple taken pursuant
to the requirements of this permit for the following information:
(1) the date, exact place, and tine of sampling; (2) the dates the
analyses were performed; (3) who perfomeH the analyses; (6) the
analytical techniques or methods used; nnd (5) the results of all
rmnl.ynofl,
ili I'MJM <«itiii( ji I Ivii JlMiupt IHJJ
Samples and measurements taken to meet the requirements of this
condition shall be representative of the volume and nature of the
monitored discharge.
e. Test Procedures
All sampling and analytical methods uso'l to mc^t the monotorinp,'
- roqiiirements specified in this permit shnll, unless approver! other- |
_ w.lno in writing, l)y tlio Dnp/irtmnnt, conform to tho f»nij1«»H.nns ns_ta1i1.iflhint» I
' tost: pror.riliirr'.'i for thn nji/ilynl n of pol 1 iir.'injvi, contained in AO CFTl !
part 13<>, ns published in the Federal UcRlstcr on October Ifi, 1973, '
or the latest revision thereof, which references the following :
publications:
021G62
-------
Oft
MONITORING AND REPORTIKG COriT'D
1) American Public He.ilth Association, Stnn'larrl, "ethods for .the
Examination of iTater 'and V.'astewnters (13th ed. 1971)
2) American Society for Testing and Materials, A._S.T.Tt.__jSjtandards,
Part 23, Water, Atmospheric Analysis (1^70)
•
3) Environmental Protection Agency, Water Quality Office Analytical
Control Laboratory, Methods for Chemical Analysisof Water and
Wastes (April, 1971).
S3. SPECIAL CONDITIONS
a. The permittee, shall handle and dispose of all oil, Rreaso., cull
or process materials and/or other solid or semi-solid wastes
associated with the permittee's operation in a manner which will
prevent their entry into stnto. ground or surface waters. Tn
addition the permittee shall not pernit leachate from such waste
materials to degrade state pround waters or surface waters.
b. The permittee shall dispose of all sanitary waste in accordance
with all recommendations,' rules, regulations, and ordinances of
the local Jurisdictional health authority. All such requirements
regarding design, construction, installation, and maintenance of
septic tank and drainfield systems are hereby made a condition of
this permit.
021063
-------
Pane 5 of 6
IV rut if No. WA 000349-2
GENERAL CONDITIONS
*
Gl. All discharges and activities authorized herein shall be consistent with'
• the terms and conditions of this permit. The discharge of any pollutant
more frequently than or at a level in excess of that identifie'd "and autho-
rized by this permit shall constitute a violation of the terms and condi-
tions of this permit.
G2, Whenever a facility expansion, production increase, or process modifica- .
tion is anticipated which will result in a new or increased discharge, or
which will cause any of the conditions of this permit to be exceeded, a
new application must be submitted together with the necessary reports
and engineering plans for the proposed changes. No change shall be made
until plans have been approved and a new permit or permit modification
has been issued.
G3. The diversion or bypass of any discharge from facilities utilized by the
permittee to maintain compliance with the terms and conditions of this
permit is prohibited, except (a) where unavoidable to prevent los* of lixe
or. severe property damage, or (b) Where excessive storm drainage or run-
off would damage any facilities necessary for compliance with the terms
and conditions of this permit. The permittee shall immediately notify
the Department in writing of oach such diversion or bypass in accordance
with the procedure specified in Condition G4.
*
G4. In the event the permittee is unable to comply with any of the conditions
of this permit because of a breakdown of equipment or facilities, an acci-
dent caused by human error or negligence, or any other cause, such as an
act of nature, the permittee shall:
a. Immediately take action to stop, contain, and clean up the unauthori-
zed discharges and correct, the problen.
b. Immediately notify the Department so that an investigation can be
made to evaluate the impact and the corrective actions taken and •
determine additional action that must be taken.
i), Mnlmiil n iliii ,i | I ml million i-ii|incl lu I liu hnji.t rl ninn I ilnsc rl hinjj the
breakilowu, Ltio iiciiial quantity ;md quality of resulting waste dis-
charges, corrective action taken, steps taken to prevent a recurrence,
and any other pertinent information. •
Compliance with these requirements does not relieve the permittee from
responsibility to maintain continuous compliance with the conditions of
this permit or the resulting liability for failure to comply. ••'.
021664
-------
Page 6 of 6
Permit No. WA 000349-2
G5. The permittee shall at all times maintain in good working order .and
efficiently operate all treatment or control facilities or systems
installed or used by the permittee to achieve compliance with the
terms and conditions of this permit. *
G6. 'After notice and opportunity for a hearing, this permit may be modi-
fied, suspended or revoked in whole or in part during its term for
cause including but not limited to the following:
a. Violation of any terms or conditions of this permit;
b. Obtaining this permit by misrepresentation or failure to
disclose fully all relevant facts; j
* 1
c. A change in the condition of the receiving.waters or any j
other condition that requires either a temporary or perma-
nent reduction or elimination of the authorized discharge.
-G7. The permittee shall, at all reasonable times, allow authorized repre-
sentatives of the Department:
a. To enter upon the permittee's premises for the purpose of in-
specting and investigating conditions relating to the pollution
of, or possible pollution of, any of the waters of the state,
or for the purpose of investigating compliance with any of the
terms of this permit;
b. To have access to and copy any records required to.be kept
under the terms and conditions of this permit;
c. To inspect any monitoring equipment or monitoring method re-
quired by this permit; or,
d. To sample s.ny discharge cf pcllutants.
G8. If a toxic effluent standard or prohibition (including any schedule of
compliance specified in such effluent standard or prohibition) is estab-
li-iluxi under Soction 307 (n) of tho Foclernl Act for n toxic pollntimt
wit I ill In |Mi»i"M| In I In1 ill MI IMI rjjn mil linr l/i'il lir«rr!n Miiil ".licit 'it iimturil
or [ifuhl In I nut ib intuit si I'in^uiiL tlinn any llmildl tint ii|>
-------
ESTABLISHED 1903
FORMED FIBRE PRODUCTS
PLEASE ADDRESS REPLY TO:
WATER VILLE, MAINE 04901
TEL. 20T 873-3351
160 SUMMIT AVENUE • MONTVALE. NEW JERSEY07645
December 15, 1977
U.S. SPA Pulp and Paperboard Survey
E, C, Jordan Co.
P.O. Box ?050 Downtown Station
Portland, Maine OM12
Attn: Kr. Willard Warren
Dear Mr. Warren:
Enclosed is s completed EPA survey form Pulp, Paper and Paperboard
Industry Non-Integrated Mill Part I for each of the following Keyes
Fibre pler.ts:
Hammond, Indiana
New Iberia, Louisiana
Sacramento, California
Waterville, Maine
Wenatchee, Washington
Very truly yours,
/
Clarence F. Bean
Manager, Process Engineering
CFB/mbc
Enclosures
021066
-------
E COMPANY
J60 SUMMIT AVKNUE • MONTVALE.;NEWJERSEYO764S
PLEASE ADDRESS REPLY TO:
WATER VILLE, MAINE 04901
TEL. 207 873-3351
January 10, .1978':
U.S. EPA Pulp and Faperboard Survey
E. C. Jordan Co.
P. 0. Box 7050 Downtown Station
Portland, Maine 04H2
Attn: Mr. Willard Warren
Dear Mr. Warren:
Enclosed is a completed EPA survey form Pulp, Paper and Paperboard
Industry Non-Integrated Kill Part II for Keyes Fibre plant at : -
Wenatchee, Washington. . ..,':'"'..;'.:„
Very truly yours,- - ••'.:<•-"'.:/:•• -"•/_< '••-
CFB/rabc
Enclosures
cc: C. V. Gurnard
Clarence F. Bean'- -';'V: ~.^~'"'.'
Manager, Process Engineering
021G67
-------
ENGINEERING
PLANNING
ARCHITECTURE
PROJECT NO.
CLIENT: ;
PROJECT DESCRIPTION:
BETWEEN: Mr,
AND:
Edward C.Jordan Co., inc.
P.O. Box 7050, Downtown Station •
Telephone: 207-775-5401
TELEPHONE MEMORANDUM
Portland, Maine 04112.
TELEX: 94-4329
DATE;
3 '~C/ * ~
-R^K L,,
SUBJECT: _J=
DISCUSSION
: M • / /
/C
C
r-
Distribution:
021C88
/.
-------
DISCLOSURE OF INFORMATION TO NCASI
As-a result of an agreement between the Agency and NCASI information
gathered through this survey form can be made available to the Co.me 11,
if the mill chooses to do so. The following items are ptovided for
you to indicate your mill's course of action in this matter: (It should
be noted that the original of this survey form must be sent to the
Agency's contractor and that a copy must be made if you choose to send
information to the NCASI).
1. A completed copy of this survey, except for the deletions indicated
below (is) (is not) being transmitted directly to the staff of the
National Council of the Paper Industry for Air & Stream Improvement
Inc. (NCASI).
The following items of information or data were deleted f.rom. the
copy of the survey transmitted to NCASI (items delected on the
basis of a claim of confidentiality, even as to NCASI, are in-
dicated by an *):
2. The respondent {dogs) (eo^ r.cc.) consent :,
other information collected by EPA or its contractor ccr^sr-ing
your facility, including any information or reference code needed
to identify the facility (ies) covered by this survey from subsequent
EPA contractor verification surveys or other studies.
The following items or types of information or data subsequently
collected by EPA or its contractor shall not be disclosed to NCASI.
TITLE t
*/• "'
021G69
- 3 -
-------
/
SURVEY FORM
'
ENVIRONMENTAL PROTECTION AGENCY
SURVEY FORM
PULP, PAPER, AND PAPERBOARD INDUSTRY
\S I ' INTEGRATED MILLS
• ;-'. t< PART I
KILL BACKGROUND DATA
Mill & Division Nane:
Address: &t~QCVrf'5loU>tf ZVC///3/V/? ZIP 472^0
/ """
Telephone o/^- /
Corporate Affiliation (if applicable) _____
Contacts and Title: (Use an asterisk next to the responsible p..vr?cane.!
completing the survey form)
B. Age of Mill
1. Year of initial construction / ^ Oh
2. Please give the year of initial startup and each y;;.-r £irK-« .'-';j2
in which any major modifications cr permanent shutdowns ware n^dc
which significantly affected th?. composition or amount of effluent
frora the mill.
Year(s) of Wast-;
Significant Modification
Year(s) of or
Initial Startup Pemanent Si Hit down
a. Woodyard
Pulping
b. Brown Stock
Washers
c. Screen Room
- 13 -
-------
Hill.
d. Bleaching
Cheiafcal Recovery
e. Recausticizing
f. Evaporation
g. Recovery Furnace
h. Paper Machine(s)
i. New or Additional
Refiner(s)
Location:
Year(s) of
Init ial S tar tup
Year(s) of Waste
Significant Modification
or
Permanent Shutdown
( '97?
j. A.... ..id IMP Proc.
k. Added CMP Process
1. Blow Heat and Condensate
Recovery
Air Pollution Control
Systems that contribute
to the waste load
m. Wet Scrubber(s)
n. Precipitator(s)
o. Eliminatrion of Process(es)
(please describe)
021G71
-------
Mill:
p. Products Mix Changes
q. Process Changes
r. Other
Location:
Year(s) of
Initial Startup
Year(f) of Waste
Significant Modification.
or
Permanent Shutdown
- 15 -
-------
Mill:
Location:
II. PRODUCTION INFORMATION
A.
3.
4.
5.
6.
7.
8.
9.
10.
13.
14.
15.
16.
17.
Average Daily* Maximum Day Maximum Month
Air- Dry Air Dry - Air Dry
Pulp • Tons/Dav • Tons/Day Tens/Day
Manufactured Hardwood Softwood Hardwood Softwood Hardwood Softwood
, \.
Bleached Kraft i 1
Unbleached Kraft 1
1 l
Dissolving Kraft \ 1
NSCC 1 I
1 i
i
Groundwood-Fine ~ "" !
Groundwood -Coarse 1 i
CMP . . ! ' :' ^
IMP • ) \\-
i. -r - ~N- r. .
'Jnbleached Sulfic>" . •
Dissolving Sulfite !
1 j
i \
Deinked Groundwood t i
I i
Deinked Kraft 1 '
Deinked Mixed Waste ' i
j i
Wastepaper - * t
,
ft- .
J!
;
Manufactured Furnish
18. other (please list)
*Average Daily = Total Productic
Total Production ^ays"" 3for "year
t b13
-------
KiEFFER PAPER MILLS/INC:
Mill:
s Supplemental
B; Fiber
Purchased pulp
19. Baled
20. , Wet Lap
21. Slushed
22. Broke
23. Other (pleass list)
Average Daily
Air Dry
Tons/day
Hardwood Softwood Hardwood Softxvood Hardwood Softwood
Maximum Day"
Air Dry
Tons /day
Maximum Month
Air ;)ry
Tons/da
C. Products
24.
25.
26.
!
1._
Tons
Maximum Day
Air Dry*
Ton*/Day
Maxim umXMon th
A
Market Pulp
a. Pulp Bales and/or Rolls
b. Wet Lap Pulp
c. Slush Pulp
Groundwood Molded Pulp
Newsprint
*Measured at the winder or pulp dryer.
- 17 -
021674
-------
' r i_ •< -~ M r L. rx iMti.t-o-f utu-
122C. WES" SPSING ST.
BRDWNSTOWN, i>DtANA 4722C
Mill:
Location:
Average Daily Maximum Day Maximum Month
Air Dry* Air Dry* Air Dry*
^cms/Day Tons/Day Tons/Day
27. Groundwood Printing,. Writing and Related
a. Uncoated Groundwood Printing
and Converting • s .' '.;'••
b. Clay (50% or more kaolin)
Coated Groundwood Printing
and Converting
c. Groundwood Specialties
d. Other '" ""' ' ' '- -
28. Wood Free Printing, Writing
and Related .---
a. Uuccated Free Sheet Printing
r ••
.-;r more kaolin)
•• ' ••-. Printing
:; Related
..-.ached
Clay (50% or more kaolin)
Coated Solid Bleached Bristol?
Other
29. Cotton Fiber Papers
a. Writing and Related
b. Technical
c. Other
30. Thin Papers
a. Carbonizing
b. Cigarette
c. Other
^Measured at the winder or pulp dryer
- 18 -
021G75
-------
WE3~ SPRING ST.
Mill:
Location:
31.
32.
33.
34.
35.
Average Daily Maximum Day Maximum Month
Air Dry* Air Dry* Air Ery*
Tons/Pay Tons/Day Tons/Day
Packaging and Industrial Converting
a. Unbleached Kraft
b. Bleached Kraft
c. Other _
Specialty Packaging and Industrial
Converting
a. Tape Backing
b. Saturating
c. Gasket
d. Other (list types)
Sanitary Tissue
Unbleached Kraft Paperboard
(80% or more unbleached kraft pulp)
a. Llnerboard
b. Folding
c. Other
Semi—Chemical Paperboard
(75% or more semi-chemical pulp)
a.
b.
Corrugating
Other
*Measured at the winder or pulp dryer.
- 19 -
021C76
-------
HAPiL'K MILLS, INU.
i22t wes- SPRING ST
Mill:
.
Location:
Average Daily Maximum Day Maximum Month
Air Dry* Air Dry* Air Dry*
Tons/Day Tons/Day Tons/Day
36. Bleached Paperboard
(not less than 80% bleached chemical iro
a. Clay Coated Bleached Food
.«., Board
b.
c-
d.
e.
Uncoated Bleached Food
Board
Bleached Linerboard
Folding
Other
37. Recycled Paperboard
a. Linerboard
b. Corrugating
e. - Filler
d . F o Id ing
e. Set-up
f . Gypsum Wall Board
g. Other
38. Construction Paper and Board
a. Construction Paper
b. Wet Machine Board
Insulating Board
Hard Pressed Board
Other
c.
d.
e.
*Measured at the winder or pulp dryer.
021G77
- 20 -
-------
en
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Mill:
• .
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0) S •
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•H . ' 01 fl
XJ -H
c w jr w
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Mill:
Location:
IV. MANUFACTURING PROCESS AND .INTERNAL ^OLLUTIOJi/CQNTROL .PRACTICES
A. General
189. Are the drum or mechanical barkers operated dry? Steam may be used
for thawing logs.
(a) Yes
(b) No
B. Kraft era! Soda Miljg^- Digesters
Give the permanganate number (if applicable) for the following:
Answer either question 220 through 223 or questions 223 through 226.
220. Hardwood
221. Softwood
(a) 16-18
(b) 18-20
(c) 20-22
(d) 22-24
(e> Above 24
Percenjx'of tne
To talxrroduction
Percent of th
Total Production
222. if the mill pulps ajztucture of hardwood and softwood, please give the
permanganate numbc
Permanganate Number
021G88
-------
HAPcR MILLS, IMC.
I2ZC. WES" SPRI^fi ST.
Mill:
223. Give the normal percent of the followin
a. Softwood
b. Hardwood
Give the Kappa number (if/applicable) at the brown stock washers for
the following:
Percent of the
Total Production
224. Hardwood
(a) 15-17
(b) .;-19
(c) 19-21
(d) 21-23
(e) Above 23
(a) 2S-30
(b) 30-32
(c) 32-34
(d) 34-36
(e) Above 36
Percent of the
Total
226. If the mill pulps a mixture of hardwood and softxrood, please give
the Kappa number.
Kappa Number
021GS-9
-------
Mill:
Location:
C. Kraft and Soda Mills — Brown Stock Washers and Screening
231-233. Give the approximate brown stock washer efficiency in terms of pounds
of soda loss as washable Na»0 for the following:
231.
232.
233.
Line #1
(a) Less than 15
(b) 15-25
(c) 25-35
.(d) 35-45
(e) Greater than/*f5
(e) Greater than 45
Line #3
(a) Less than 15 it-Na-O
(b) 15-25
(c) 25-35
(d)
(e) Greater than 45
Percent of the
Total Production
Percent of the
Total ?r
Percent of the
Total Production
021GSO
-------
Mill:
'KIEFFER PAPER MILLS, INC.
122& WES" SFRSNB ST.
r... .^ BRDWNSTOWV,. N01ANA 4722C
Location:
240-242,
a.
b.
c.
d.
Kraft: and Soda Mills n- Bleaching
Indicate the normal bleaching sequence(s) used, (i.t. C=Chlorine,
E=Caustic Extraction, D=Chlcrine Dioxide, !-l=Hypochlorit;e, P=Peroxida)
and the G.E. Brightness Range and percent shrinkage for the bleach line(s)
for the principal grades produced on each line.
Bleach Line j'l
Normal .
Pulp Bleached
Npjrmal Fresh
water Usage
(240)
Grade #1
(241)
Grade #2
Production
ADT/d
(242)
Grade #3
Production
ADT/d
f. G.E. Brightness
Range
g. Shrinkage (%)*
*Equals tons/day input — tons/day output
tons/day input
021G81
-------
MILLS. INC.
12ZL WES' SPRING ST
BRDWNSTOWK SniANO 47?2C
Location:
Mill:
I). Kraft and Soda Mills - Bleaching - Continued
243-245. Bleach Line #2
(243)
Grade #1
a.
b.
c.
d.
Normal
Pulp Bleached
G.E. Brightness
Range
Shrinkage (%)*
Production
ADT/d
(244)
Grade if2
Production
. ADT/d
"Equals tons /day;__inpu£ - tons/day output
tons/day input
x 100
021C92
- 35 -
-------
'K1EFFER PAPER MILLS, INC.
122C W?.3~ SPaiNG ET.
,:..^ .- 3i!OiVi<37GV/S.. MIA^A 4722C
Mill:
Location:
D.
246-248.
Kraft and Soda Mills - Bleaching - Continued
Bleach Line #3
Normal
Pulp Bleached
a.
b.
c.
d.
Normal Fresh
Water Usage
(246)
Grade //I
C247
Gradex#2
Production
ADT/d
roduction
ADT/d
Production
ADT/d
G.E. Brightness
Range
g. Shrinkage (%)*
*Equals tons/day input - tons/day output ..,._
tons/day input
021C93
-------
Mill:
IKIEFFER PAPER MILLS, INC.
•: 122G WES" SPRING ST.
";. _ SSC'vVJ/STCWN. ..hlJtAil* '4722C •'-
Location:
258-260. Give the type of bleach line washing for the principle grades manu-
factured.
258> Bleach Line //I
(a) Jump-stage counter-current joshing
(b) Straight counter-curpelft washing
(c) Co-current wasjj-itig
(d) Other (jxt^ase describe)
259. Bleach Line #2
(a) Jump-stage counter-curre^e^washing
(b) Straight counter^tfrrent washing
(c) Co-currenJ
(d) Other (please describe)
dashing
260. Bleach Line #3
(a) Jurap-stage counter-curj
(b) Straight counter-current v/ashing
(c) Co-currea^washing
(d) Qfcffer (please describe)
E. Kraft and Soda Mills - Recovery
267. Give the type of evaporatoycondenser used,
(a) Barometric
(b) Surface
(c) Jkmi (please give the number of each type)
•21694
-------
Mill:
KIEFFER PAPER MILLS, INC.
I22t WES' SPRING ST.
'__" Location: '' 47x20' — -'-.
F. Kraft and Soda Mills-Liquid Waste Sources
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I
G. Sulfite Mills - Pulping Area
292. What base is used?
(a) Mg
(b) Ca
acid or bisulfite?
293. Is the pulping
(a) Acid ^>
(b) B^fStTlfite
297-299. Give the overall pulping yield for the foil
cent of the
otal Production
Perceuf'or the
Production
021GD5-
-------
K1EFFER RAPES MILLS, INC.
122C, WES" Sf-'filNG ST.
Mill:
299. Line #
Percent of tfrj.e'
Total Prody
-------
4722C
Mill:
Location :
I.
312-314
a.
b.
c.
d.
e.
f.
Sulfite Mills - Bleaching
Indicate the normal bleaching sequence(s) used, (i.e. C=Chlorine,
E=Caustic Extraction, D=Chlorine Dioxide, H=Hypochlorite, P=Peroxide)
and the G.E. Brightness Range and percent shrinkage for the bleach
line(s).
Normal
Pulp Bleached
(312)
Bleach Line //I
Production
ADT/d
Normal Fresh
Water Usage
Stage
(313)
Bleach Line #2
Production^
ADT/
(314)
Production
ADT/d
Chemical
Chemical
G.E. Brightness
Range
g- Shrinkage (%)*
*Equals tons/day input - tons/day output
tons/day input
x 100
021C97
-------
Mill:
K1EFFER PAPER MlLLb. irti
.;• 122C. WES' SPRING SI.
fc-.v-..^. BROWNSTOWN- iNDlAN*. 4772C
Location:
^*~"—
315-317. Give the type of bleach line washing £efthe following
315. Bleach Line
(a) Jump-stage coun^ef-current washing
(b) Straight^c'ounter-current washing
(c)^6t>-current washing
316. Bleach Line 92
(a) Jurap-stage counter-cu££en"t~ washing "
(b) Straight ^jpartfier-cur rent washing
washing
317 Bleach Line #3
(a) Jurap-stage counter-
(b) Straight couijief-current washing
(c) J>-tSirrent washing
J. Sulfite Mill - Recovery System
325. Give the type of condenser
(a) Barometric
fc
(c) Both (please give the number of each type)
K. Sulfite Mills - Liquid Wastg^StSurces
NO QUESTIONSjerTTHIS ITEM ARE TO BE ANSWERED IN PART I
021GS8
-------
'K1EFFER PAPER MILLS, ING.
122C, WES" SPRING ST.
EROV/NSTOWN.-1 ! NDSAN* 4722C •.. -^
Mill:
Location:
L, Groundwood Mills - Pulping Area
353. Describe the type of grinding operations; i.e., type of grinder, refiner.
M. Groundwood Mills - Bleaching
358. Indicate the bleaching chemicalfi) used.
(a) Zinc Hydrosul|
(b) SodiumJHydrosulfite
IP, arid IMP Mllls^acreens and Washers
FOR THIS ITEM ARE TO BE ANSWERED IN PART I
021G39
-------
KIEFFER PAr::iS
122:.. WES' £Pi"!i:-:S
•'•-' V 'E;iaWNS7QV,'t> , hOlANA
MJLLS. INC.
Mill:
Location:
Q. ;NSSC. CMP, and IMP Mills - Bleaching
Indicate the nonaal bleaching sequence(s) used, (i.e^. C=Chlorine,
E=Caustic Extraction, D=ChIorine Dioxide, H=Hypochi^rite, P=Peroxide)
and the G.E. Brightness Range and percent shrinjtage for the bleach
line(s).
390-392
(390)
Bleach Line #1
e.
Stage
Chemical
1
2
3
4
G.E. Brightness
Range
f.
g- ShrinkageX%)*
ach Line #2
Production
ADT/d
(392)
Bleach Line #3
Production
ADT/d
*Equals tons/day input - tons/day output ^ 1
tons/day input
021700
-------
Mill:
;K!EFFEfi PAPER M1|_LS
'2 WES' CPH,NG ST
R. NSSC and CMP -Recovery System
398. Does the mill have a^recoyery system?
(a) Yes
(b) No
S. NSSC. TMP and CMP MilK- Liquid Waste Sources
NO QUESTIONS FOR THIS ITMsARE TO BE ANSWERED IN PART I
P\
T. Deink Mills - Fu>t>er Area ' \
424-426. Give the overall pulping yield for the following:
42:4. Line //I
(a) Below 50
(b) 50-60
(c) 60-70
(d) 70-80
(e) Above 80
425. Line #2
(a) Below 50
(b) 50-60
(c) 60-70
(d) 70-80
(e) Above 80
426. Line 03
(a) Below 50
(b) 50-60
(c) 60-70
(d) 70-80
(e) Above 80
Percent of-the
Total Production
Percent of the
Total JProductIon
Percent of the
Total Product ion
\
021701.
-------
Mill:
jvik.iTt.rt
Location:
iK MILLS. ING.
- S=K:-:n ST.
.. . bQIA.M*. 4722C .
429. What ^herjiccls are added\to the y.^.pt.r for dai:~ki:;f . (Indicate s.-.
^T • Deink Hills_..r. _Stpck Washers and Screening
NO QUESTIONS FOR THIS IT^M ARE TO BE ^SWERZD IS PA?.-' I
V. Deink Mills - Bleaching
Indicate the normal bleaching
E=Caustic Extraction, D=Chlori
and the G.E. Brightness Range ^
liue(s) used.
440-441
a. Production
ADT/d
(440)
Bleach Line #1
eque
>nce(s) u£i.:d, (i.t. C=Chlorine,
Dioxide, H=tiypochloriue. P=Pero:»ide)
percent shrinkage for the bleach
(441)
Bleach Line 3
\
b. Normal Fresh
Water Usage
c. Stat*a
I
Z
3
4
d. G.E. Brightness
Range
e. Shrinkage (%)*
* Equals tons/day input - tons/Jay gucput .A-,
tons/day input " " \
021702
-------
BROWNSTOWK.
A7Z2C
Mill:
Location:
W. DeinkMills ~ Liquid Was te Sources
. NO QUESTIONS FOR THIS ITHtf ARE TO BE ANSWERED IN PART I
X. Paperboard front Wastepaper -\Pulper Area
' • rt-^-
463-465. Give the overall repulped yifeld^«fbr the following:
463. Line #1
(a) Less than 80
(b) 80-35
(c) 85-90
(d) 90-95
(e) More than 95
464. Line 9
(a) Less than 80
(b) 80-85
(c) 85-90
(d) 90-95
(e) More than 95
465. Line /;3
(a) Less than SO
(b) 80-85
(c) 85-90
(d) 90-95
(e) More than 95
Percent of the
Total. Product ion.
Percent of the
Total Production
Percent of the
ToLal Production
021703
-------
KIEFFER PAPER MILLS. ING.
I2
-------
122C wr5-
BRDVVNGTOWN..
G ST.
47J2C
Mill:
Location:
505. High pressure showers - Are high pressure showers (above 250 psig)
used on the paper machines for felt cleaning?
(a)
(b) No
(c) Limited Application
C-l Builders Paper -Vaper Mill
508. Give the number of paper machines at mill.
D-l Builders Paper - Saturating &>d Coating (if applicable)
514. Does the mill utilize a saturating and/or coating process?
A" \
(a) Yes
(b) No
E-l Builders Paper - Internal
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED\JN PART I
F-l Additional Information (All Mills)
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PARTvI
021705
-------
Mill:
Location:
S HJ.
4722C
V. WATER USAGE AND EFFLUENT TREATMENT PRACTICES
Instructions for Completing Section V
Section V requests information on the mill's wastewater treatment practices.
In Section VIII a general schematic of the effluent treatment system is
requested. You have the option of providing any of the data requested in
Section V on the schematic. If you do this, please indicate on the
question(s) involved that the data is presented ou the schematic.
A. Water Usa.~3
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
B. Background Data *""
532. Indicate the method (s) of disposal of the mill wastewater.
(a) Direct
(c) Self-contained
(d) Other (please describe)
533, Please give the year in which the following portions of the mill's
existing wastewater treatment system were started up.
Year of Startup
a. Primary Treatment System
b. Secondary Treatment System
C. Indirect Discharger (discharge to a POTW) please provide the
following information:
536. Is raw wastewater pretreated externally prior to discharge to the
POTW? (Pretreatment is considered to be any treatment device external
from the mill production processes which is utilized prior to a pri-
mary and secondary treatment system, or prior to discharge by an
indirect discharger to a POTW.)
02170(5
-------
Mill:
Location:
537.
Give the treatment process used by the POTW to whi.:h your mill discharges,
(Include biological and physical-chemical treatment if applicable)
(a) Activated sludge
(b) f Aerated lagoon
(c) Oxidation ditch
(d) Trickling filter
(e) None
(f) Other (indicate type)
540. Give the preliminary treatment method used, if any.
(a) Neutralization
(b) Screening (indicate type used)
(c) Other (please describe)
542. Indicate the primary treatment method used, if applicable.
jS~^ ^^-x.
(a)C Clarifier,
(b) Sedimentation lagoon
(c) Mechanically cleaned sedimentation lagoon
(d) Other (please describe) ._
(e) Not applicable
546. Give the type of biological treatment used, if applicable.
(a) Storage oxidation basin
(b) Aerated Stabilization basin
(c) Activated sludge (air or oxygen)
(d) Other (please describe) .S&ATe
(e) Not applicable
021707
-------
Mill:
KIEFFER PAPLH MiLLii.
^jy.- T2/C, WES" SPRING 31
' 472ZC
D. Direct Discharger please provide the following information:
549. Is wastewater discharge continuous or non-continuous (effluent stored and
discharged when conditions allow) when production facilites are operating
(\a^ Continuous
(b) Non-continuous - daily
(c)'' Non-continuous - seasonally/intermittent
E- Preliminary Treatment (Direct Discharger)
551. Give the preliminary treatment method used, if any.
(a) Neutralization
(b) Screening (indicate type used)
(c) Other (please describe)
F. Primary Treatiaent (Direct Discharger)
553. Indicate the method used for primary treatment.
Clarifier
(b) Sedimentation lagoon
(c) Mechanically cleaned sedimentation lagoon
(d) Other (please describe)
G. Biological Treatment (Direct Discharger)
557. Give the type of biological treatment used.
(a) Storage oxidation basin
f (bj"\ Aerated stabilization basin
(c) Activated sludge (air or oxygen)
(d) Other (please describe)
021708
-------
iKIEFFER PAPER M,LLS< (NC
- 122L *«-
SPRING ST
. * ;DIANA 4722C
*• •*>
-------
Mill:
:..;r K
IZ« WES' SP.9IMO ST
.... UROWNSTOWN.
Location:
M. Site Conditions and Availability ofLand
NO QUESTIONS FOR THIS ITEM ARE TO BE ANSWERED IN PART I.
N. Wastewater Characteristics
572-577. 'Give the (1976) wastewater loads indicated below:
Indirect& Diract Dischargers Please Answer
(572)
Pulp
Mill
a. "Flow, MGD
(1) Average Day
(2) Maximum Day
(3) Maximum Month
b. BOD, Ibs/day
(1) Average Day
(2) Maximum Day
(3) Maximum Month
c. TSS, Ibs/day
(1) Average Day
(2) Maximum Day
(3) Maximum Month
(573) ..(574) (575)
Bleach Plant* Paper Total Raw
Acid Alkaline Mill Wastewater
Direct Discharger ;
Only Please Answer
- (576)
Secondary
Treatment (577)
System Final
Effluent Effluent
VI. FUEL AND ENERGY
NO QUESTIONS FOR THIS SECTION ARE TO BE ANSWERED IN PART I.
VII. PRIORITY POLLUTANTS
fl?1*'1fl
SEE NEXT PAGE V 6 A • •*• "
VIII. PROCESS SCHEMATICS
NO QUESTIONS FOR THIS SECTION ARE TO BE ANSWERED IN PART I.
-------
Mill:
12ZC WES' SPRING SI
OWNSTOWk. LMJIAN* 4722C
Location:
VII. PRIORITY POLLUTANT COMPOUNDS
Please fill in the following information for those priority pollutants
which, to your knowledge, are in your raw water supply, or used, or
generated in any of the processes in the mill (refer to the following
pages for the priority pollutant list). Use the number shown to identify
the compound.
It should be noted that many mills may be using quantities of the listed
chemicals as additives, cleaning solution, or solvents which are purchased
and referred to by a trade name. Please supply trade names of those pro-
prietary type chemicals, which contain one or more of the listed priority
pollutants as constituents, used in the mill. Exclude all laboratory
chemicals.
Compound Number
or Trade Name
Process Where
Compound is
Used or Generated
Describe Use
Quantity Frequency
Sampling or Monitoring
Program for Compound
(Yes or No)
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-------
Question
Number
Question
Number
PART I
CONFIDENTIALITY CLAIMED FOR THE FOLLOWING
Question
Number
Question
Number
Question
__N umber
Question
Number
-------
/{
"'* ^N v ENVIRONMENTAL PROTECTION AGENCY
^..V SURVEY FOFxS
PULP, PAPER, AND PAPER2GAB.D INDUSTRY
vx
INTEGRATED MILLS
PART II
I. MILL BACKGROUND DATA
A. Mill ft Division Name:
Address: rttU /V. ZIP: Z O
Telephone: g/ 2 / 3
Corporate Affiliation (if applicable)
Contacts and Title: (Use an asterisk next to the responsible personnel
completing the survey form) •
£ H. fti^lig.rPre
B. Age of Mill
1-2 DELETED - ANSWERED IN PART I
II. PRODUCTION INFORMATION
3-38 DELETED - ANSWERED IN PART I
III. PROCESS RAH MATERIALS
39-185 DELETED - ANSWERED IN PART I
021716
-------
IV. MANUFACTURING PROCESS _VJO INT.V'.^-j.-'.J. • ';• •.L-';TOr_ COVl^OL PRACTICE
A. General
186. Give the typical product:.;on day? ;>»r y-i.vr. "^ fe*
-------
Mill:
Loca f.ion:
ii^pH or ccnductiv! cy woRitor cf Jnt':i'i-.,r.l <-.
> to detect or divert spills?
(a) Yes
(b) No
(c) To" the axteut possible
Explanation (if needed)
194-214
194.
195.
196.
197.
198.
199.
200.
201.
202.
203.
204.
205.
206.
207.
208.
s
Is cooling water collected and reused from the following locations:
(a) Yes; (b) rio; (c) S^-sona!; (d) To Extent Possible; (e) Not Applicable
a b c d a
Air compressor cooling water _
Dryer drainage condensate cooling
Lube oil cooling
Calendar cooling heat exchangers
Rewinder brake cooling _
Evaporator surface condenser _
Digester blow condenser
Paper inachir.a clutch cooling _
Lime kiln turnions (kraft only)
Hot Lirae conveyors (kraft only)
Cooling in power plant
Feed water pump bearings
Power Plant I.D. fan bearings
Other bearing cooling __
Refiner Cooling
021718
-------
Mill:
Location:
209. Motor control center cooling
210. Water chiller
211. Smelt spout cooling (kraft only)
2.1.2. Condensate sample coolers
213. Air conditioning
214. Concentrator condenser
Kraft and Soda .Mills - Digesters
215. wh^ cype of digester(s) is used at the mill?
(a)
(b)
216. What is the whiteN^quor sulfidity range?
217-219. Give the overall pulping yierSL for the following:
217. Line P
Percent of the
Total Producticn
(a) Belov/ 40
(b) 40-45
(c) 45-50
(d) 50-55
(e) Above 55
021719
-------
Mill:
Location:
2 IS?
219.
Percent of "he
Total Production
Percent of the
Total Production
220-226. DELETED - ANSWERED IN PART I
Jrainsf
(a) Yes
(b) No
(c) Partial
Explanation (if needed)
Spi11
system for floor
021720
-------
Mill: _ __ __ Location:
If c?- a~s:.-e-' •:.-: ::io preceding ^ueuuier. is (•-)., d;==cribe tha collection
V^> Gv-jll2f--::c a."d discharged to the ffzwer at o controlled rate.
{b)\ Co.Liec.cfeG wnd reused in the process
(c) oWr ;please dsscribe)
229.
dissolving ktSjft-
(a) Yes
(b) No
(c) To the. extent pcs\ibls
Explanation (if ne.v;d\a)
.-ninr: - Only applicable if nill makes
C. Kraft and Soda Mill£ - Brown S::c^k Washers and Screening
230. If ths iaforration is available, indi&ate the approximate amount of
spills and vsshdown water frora thie brow^ stock washers which goes
to the severs.
a. Line 1
b. Line 2
c. Line 2
fc?31-233. DELETED - ANSWERED IN PART I
234. Decker filtrate for ira.cuusi washer showers
used on the brown stock washer showers?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
- Is any decker riltrate
021721
-------
Mill:
Location:
236
Give the approximate percent of the total screen room decker filtrate
is normally sewered.
Evaporator condenitetes for brown stock washer showers - Is any of
the evaporator cond\nsate reused on the brown stock washer showers?
(a) Yes
(b) No
(c) To the extent possible^
Explanation (if needed)
237. Close up screen room - Is the decker fi\£rate used for all of the
dilution on the screens and cleaners?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
238. Recook screen room rejects - Are screen room rejects normal\v ex-
cluded from the sewer?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
-------
Mill:
Location:
Give the normal method of knots disposal.
(a) Sewered
Landfilled
Reprocessed
>
(d) Svrned
(e) Oth^r (please describe)
D. Kraft and Sodayiills - Bleaching
240-248. DELETED - ASSWEREDNlN PART I
249-251. What percent of the chlorine washer filtrate is reused?
(249)
Bl_each_ Line #1
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-80%
(e) 80-100%
(250)
ach Line #2
(251)
Bleach Line #3
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-80%
(e) 80-100%
252. If any is reused, where is it used and give tn^ approximate amount.
a. Where
b. Usage, GPM
X
253. What are the typical chlorine residuals in the filtrate
Line #1
mg/1
b.
Line #
mg/1
c.
Line #3
rag/1
021?!>2
-------
Mill;
vocation:
4-255. What percent of the caustic extraction washer filtrate is reuse.-:'?
(25/0.
Bleach Line #1
V-' ->->!
Bleach LIne_"j
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-30%
(e) 80-100%
Bleach Line v3
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 50-50%
(e) 80-100%
257. If it is reused, where is it used and give the approximate amount.
a. Where
~~ ~
b. Usage, GPM
X
258-260. DELETED - ANSWERED IN
261. Do the materials of construecipn (washers, pumps, piping and tanks)
in the bleach plant allow for straight counter-current washing?
(a) Yes
(b) No
262. White v;ater use on bleach washer showers \ Is any excess paper or
pulp machine white water used on the bleacn\plar.t washer showers?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
021724
-------
Mill:
Location:
• Is the waste acid from C102 generation normally excluded fro-n the
sewer?
(a.) Yes
(b\ No
(c) ^ the extent possible
Explanation (if needed)
264. What type of ClO^generation system(s) is used?
(a) Solvay
(b) Mathieson
(c) Hooker or ERGO
(d) Other (please describe^
E* _Rraft and Soda Mills - Recoverv\vstem
"-"v—
265. Gix'e the percent solids to the evap\rators,
a- Set 1 % b. Set 2
% d. Set 4
c. Set 3
266. Give the percent solids from evaporators.
a. Set 1 % b. Set 2 5
c. Set 3 % d. Set 4 ,'
267. DELETED - ANSWERED IN PART I
021725
-------
Mill:
Location:
2681. - Is the weak evaporator boil-out liquor returned to the prcce-ss?
i) Yes
(b)\No
(c) To^extent possible
Expiration (if needed)
269. Is strong evaporao^r boil-out liquor all returned to process;
(a) Yes
(b) No
(c) To extent possible
Explanation (if needed)
270. Does the mill have weak black liquor oxidation?
(a) Yes
(b) No
271. Indicate what is normally done with soap.
(a) Sent to mill's tall oil system
(b) Marketed commercially
(c) Sewered
(d) Burned
(e) Not applicable
021728
-------
Mill:
Location:
?2\ Black liquor storage tank spill collection:
\Total Tankage Volume
a.Week black liquor
b.Strong black liquor
273. Does the rn$.H steam strip condensate and reuse?
(a) Yes
(b) No
(c) To extent
Explanation (if heeded)
274. Does the mill have a turpentine recovery system?
(a) Yes
(b) No
275. Is the causticizing area spill ccllectic
(a) Yes
(b) No
(c) To extent possible
Explanation (if needed)
system returned to process?
276. Is blow heat condensate used for causticizing make-up?
(a) Yes
(b) No
021727
-------
Location:
gtQrage
Mill:
2\ Does the mill utilize a lime mud
(a) Yes
No
278. Reuse ttiln scrubber water - Is the kiln scrubber water reused so thij
the lime\dust in it will be recovered, such as at the mud washar?
279. Are green liquor d\gs sewered?
(a) Yes
(b) No
280. How many pounds per day of
process?
liquor solids are reused in the
///day
281. Is semichemical pulp produced using gr^en liquor?
(a) Yes
(b) No
F.
For questions 282 through 291 please indicate the\isual discharge
point for the liquid waste listed. Indicate the answer utilizing one
of the following: (a) Evaporator & Burned; (b) Sewereoc (c) Reused
(Totally); (d) Reused (Partially); (e) Landfill or Sold?1
a b
282. Digester Relief Condensate
283. Blow Condensate
284. Cleaner Rejects .
285. Screen Rejects
-------
Mill:
Location:
Pump Seal Water
287. \Surface Heat Exchanger Coolant
288. Sp\lls & Washup
289. Striked (or clean) Coadensata
290. Hot Wat£r from the Economizers
291. Decker FiliSrate (screen room)
G.~ Sulfite Mills\ Pulping Area
292-293. DELETED - ANSWEHEDVN PART I
294. What is the fortifiedNpooking liquor total SO?
295. What is the fortified cookin^yliquor free SO,?
Give th.
a. Line #1
D- Line #2
c. Line #3
, fcppl or
297-299. DELETED - ANSWERED IN PART I
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
.......
S"
floor
021729
\
-------
Mill:
Location:
u>
,ollection
Collected and discharged
Collected and reused in the process
OtW (please describe)
- Screen Room and Washers
H. Sulfite MiS _._
302. Decker filtrate,, for vacuum washer showers
used on the browta stock washer showers?
.. (a)! Yes
' (b) No
Is any decker filtrate
the total screen room decker filtrate
\
303. Give the approximate perc«
which is normally sewered.
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-80%
(e) 80-100%
304-306. DELETED - ANSWERED IN PART I
307. if the information is available, indicate the approximate amount of
spills and washdown water from the red stock washers\which goes
to the sewers.
a- Line ffl
b- Line #2
c- Line #3
. GPM
. GPM
GPM
021730
-------
Mill:
Location:
Evaporator condensates for brovn stock washer showers - 15 any cf
the evaporator condensate reused on the brown stock washer showers?
i) Yes
(b)\ No
(c) 1\ the extent possible
Explanation (if needed)
309. Close up screen ^oora - Is the decker filtrate used for all of the
dilution on the screens and cleaners?
(a) Yes
(b) No
(c) To the extent possibl>
Explanation (if needed)
310. Recook screen room rejects - Are sere
or refined?
(a) Yes
(b) No
(c) Impractical with quality demands
Explanation (if needed)
room rejects either recooked
311. Give the normal method of knots disposal.
(a) Sewered
(fa) Landfilled
(c) Reprocessed
(d) Burned • 021731
(e) Other (please describe)
-------
Mill:
312-3^
Location:
318.
(b) Nj
31S. whx-e \- \
,7 ™T - •= =ws==,
(b) No
-------
Mill:
Location:
gulfite Mill - Recovery System
Jo you have a recovery system? If answer is (a), please answer
324 through 339 ; if (b), omit questions.
(a) \yes (please describe type)
(b) NoN
solids to the evaporators.
b- Line //2 _
d. Line #4
325. DELETED - ANSWERED IMPART I
326. Does the mill have an evaporator boil-out tank?
(a) Yes
(b) No
327. What is the pH of the spent liquor tto the evaporators?
a. Line #1 *>• Line #2 __^_
d. Line #4 \
c. Line #3
328. Does the mill neutralize its spent liquor
a. Line #1 (a) Yes (b) No
b. Line #2 (a) Yes (b) No
c. Line #3 (a) Yes (b) No
d. Line #4 (a) Yes (b) No
to evaporation?
021733
_ 79 _
-------
Mill:
Location:
329V Does the strong boil-out go to the weak liquor tank?
Yes
(b)No
(c) Toythe extent possible
Expiration (if needed)
330. What happens to fl^e weak boil-out liquor?
(a) Recovered
(b) Sewered
331. Acid condensate holding tanK for sulfite evaporator boil-out - Is
the acid condensate collected\and stored to be used for evaporator
boil—outs?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
332. Waste liquor storage tank spill collection:
Total tankage volume
a. Weak waste liquor
b. Strong waste liquor
333. Does the mill steam strip condensate and reuse?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
-------
Mill:
Location:
Give the following flows to the sewer:
a-\)igester Blow Condensate
b.
evaporator system including
the'Vjector intercondenser and
the surface condenser
335. What percentage of the spent liquor is recovered?
336. is any of the spent liquor sold?
(a) Yes - indicate percentage
(b) No
337.
If the answer to the
the sold liquor?
preceding question is "Yes", what is done with
(a) Road binder
(b) Cattle feed
(c) Linoleum paste
(d) Other (please describe)
338. Are any by-products manufactured from the spen\liquor by the mill?
(a) Yes
(b) No
021735
- Rl _
-------
Mill:
Location:
K.
340.
341.
342.
343.
344.
345.
346.
347.
348.
349.
350.
351.
352.
If the answer to the preceding question is (a), indicate wh.it the
by-products are.
i) Yeast
(b)\ Vanilla
(c) Alcohol
(d) Othe\ (please describe)
Suifite
- liquid Waste Sources .
L. Groundwood Mills - Pulping Area
353. DELETED - ANSWERED IN PART I
For questions 34S through 352 t please indicate the usual discharge
point for the liquid waste listed. Indicate the answer utilizing one
of the following answers: (a) Evaporated & Burned; (b) Sewered;
(c) Reused (Totally) \(d) Reused (Partially); (e) Landfill or Sold.
Digester Vent Condensate
Blow Vent Condensate
Blow Liquor
Spent Liquor from Digester Extract
Chipwashing or Steaming
Cleaner Rejects
Screen Rejects
Pump Seal Water
Surface Heat Exchanger Coolant
Spills and Washup
Stripped (or clean) Condensate
Hot Water from the Economizers
Decker Filtrate (screen room)
021736
-------
Mill:
Location:
Does the mill have a pulp mill spill collection system for floor drains?
'a) Yes
(b\ No
(c) 1\» the extent possible
Explanation (if needed)
355.
If the answer to\the preceding question is (a), describe the collection
system's function^
(a) Collected and discharged to the sewer at a controlled rate
(b) Collected and reusWj in the process
(c) Other (please describs
356.
357.
Give the approximate percent or^the total screen room decker filtrate
which is normally sewered.
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-80%
(e) 80-100%
Close up screen room - Is the decker filtrate used Xpr all of the
dilution on the screens and cleaners?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
021737
-------
Mill:
Location:
Groundwcod Mills - Bleaching
358.\ DELETED - ANSWERED IN PART I
359. ls\nsutralizaticn used after bleaching?
(a) \es
(b)
360. is washing o\ thickening used after bleach?
(a) Yes
(b) No
361. Give the quantity of bleach used per ton of pulp.
363.
364.
365.
366.
367.
368.
362. Give the brightness gain.
points/lb\ bleach/ton
N. Groundvood Mill - Liquid Waste Source
For questions 363 through 371 t pleas e\indicate the usual discharge
point for the liquid water listed. Indicate the answer utilizing one
of the following answers: (a) Evaporator at Burned; (b) Sewered;
(c) Reused (totally); (d) Reused (paftially\ (e) Landfill or Sold.
Grinder and/or Refiner Cooling
Chipwashing
Pump Seal Water
Spills and Washups
Hot Water from the Economizers
Decker Filtrate
021738
-------
Mill:
Location:
'• Cleaner Rejects
>X^ Bull Screen Rejects
371. Pd.na.1 Screen Rejects
0• NSS*. CMP and TMP Mills - Pulping Area
372. What is\the NSSC cooking liquor composition?
a* Na2C03 \ Ibs/gal
Ibs/gal
373. How many gallons\of cooking liquor per ton of pulp?
gllons
374. What is the pressure, Cemperature and retention time in the digester?
a» psi
b- °F or °C (indicate one)
c* _^__ hours
375.
Indicate the type of digester used.
(a) Batch
(b) M & D
(c) Other Continuous
(d) Other Systems (please describe)
376. Are any cooking additives (penetrants) used?
(a) Yes
(b) No
377. DELETED - ANSWERED IN PART I '
921739
- 85 -
-------
Mill:
Location:
378\ Does the mill have a pulp mill spill collection system for floor drains.?
(a) Yes
(b\ No
(c) to the extent possible
Explanation (if needed)
379.
If the'answer to\the preceding question is (a), describe the collec-
tion system's function.
(a) Collected and discharged to the sewer at a controlled rate
(b) Collected and reusW in the process
(c) Other (please describe
P.
380.
NSSC, CMP,and IMP Mills - Screens and Washers
i^.
Give the type of washer(s) used.
(a) Drum
(b) Screw Press
(c) Other (please describe)
381-383.
381.
Indicate the washer(s) efficiency in terms of pounds of Na20 per ton.
Line #1
Percent of the
Total Productior
(a) Below 25 #Na,0/Ton
(b) 25-50
(c) 50-75
(d) 75-100
(e) Above 100
921756
-------
Mill:
Location:
38\. Line #2
Percent of the
Total Production
(a) Below 25 //Na^O/Ton
25-50
(c) \50-75
(d) 7 5V100
(e) Abovk 100
383. Line #3
Percent of the
Total Production
384.
(a) Below 25 #N\,0/Ton
(b) 25-50
(c) 50-75
(d) 75-100
(e) Above 100
Give the approximate percent of\the total screen room decker filtrate
which is normally sewered.
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-80%
(e) 80-100%
385.
Decker filtrate for vacuum washer showers
used on the brown stock washer showers?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
- Is any\decker filtrate
0217-51.
\
-------
Mill:
Location:
"386. Evaporator condensates for brown stock washer showers - Is any of
the evaporator condensate reused on the brown stock washer showers?
(a) Yes
b) No
To the extent possible
lanation (if needed)
387. Close up sci^een room - Is the decker filtrate used for all o£ the
dilution on o^ie screens and cleaners?
(a) Yes
(b) No
(c) To the extent poVsible
Explanation (if needed)
338.
Recook screen room rejects -
or refined?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
screen room rejects either recooked
339.
Give the normal method of knots disposal.
(a) Sewered
(b) Landfilled
(c) Reprocessed
(d) Burned
(e) Other (please describe)
Q. NSSC, CMP, and TMP Mills - Bleaching
390-392. DELETED - ANSWERED IN PART I
- 88 -
021742
\
\
-------
Mill:
Location:
394
395.
396.
Give the type of bleach plant washing.
Bleach Line ??1
Single stage
(b)\ Multi-stage co-current
(c) N
(d) Othek (please describe)
Bleach Line\2
(a) Single Stage
(b) Multi-stage concurrent
(c) None
(d) Other (please descrvj.be)
Bleach Line #3
(a) Single Stage
(b) Multi-stage co-current
(c) None
(d) Other (please describe)
White water use on bleach washer showers -\Js any excess paper or
pulp machine white vater used on the bleach \lant washer showers?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed) •
- 89
-------
H~
Mill:
Location:
397\ Is any of the chlorination washer filtrate reused?
a. \ine #1 b. Line #2 c. Line #3
(a) Yes (a) Yes
(b) No (b) No
R. NSSC andXMP - Recovery Sy^teia
398. DELETED - ANSWERED IN PART I
399. Give the percent ^solids to the evaporators.
a. Line #1 %
b. Line #2 \_%
\
c. Line #3
400. Give the percent solids from evaporators.
a. Line #1 %
b. Line #2 7,
c. Line #3 %
401. Give the type of condenser used.
(a) Barometric
(b) Surface
(c) Both (please give the number of each type)
402. Does the mill have a recovery area spill collection system?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed) ft*) 1 -*** A
~
-------
Mill: Location:
Is evaporator condensate used for liquor make-up?
(a) Yes
No
(c)\ To the extent possible
planation (if needed)
404. Is the brownMiquor filtered prior to evaporation?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
405. Does the mill have an evaporato\ boil-out tank?
(a) Yes
(b) No
406. Does the strong boil-out go to the weak liquor tank?
(a) Yes
(b) No
407. What happens to the weak boil-out liquor?
(a) Recovered
(b) Sewered
021745
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Mill:
Location:
408 .y Brown liquor storage tank spill collection:
fetal Tankage Volume
a. Weak Brown Liquor
b. StrongVBrown Liquor
409.
411.
412.
413.
414.
415.
416.
Does the m\ll steam strip condensate and reuse?
(a) Yes
(b) No
(c) To the extent ^fcossible
Explanation (if nteeded)
410. Give the following flows to
a. Digester blow condensate
sewer:
From evaporator system including
the ejector intercondenser and
the surface condenser
NSSC,TMP and CMP Mill - Liquid Waste Sources
For questions .411 through 423 , please indicate the usual discharge
point for the liquid waste listed. Indicate tnte answer utilizing one
of the following answers: (a) Evaporated & Burned; (b) Sewered;
(c) Reused (totally); (d) Reused (partially); (e)\andfill or Sold.
Digester Vent Condensate
Blow Vent Condensate
Blow Liquor
Spent Liquor from the Washers
Chipwashing or Steaming
Cleaner Rejects
0217*6
-------
Mill:
Location:
417\^Screen Rejects
418. piimp Seal Water
419. Surface Heat Exchanger Coolant
420. spills "and Washup
421. Stripped Osr clean) Condensate
422. Hot Water froia the Economizers
423. Decker Filtrate \screen room)
T. Deink Mills - PulperNArea
424-426. DELETED - ANSWERED IN PAST I
427. Does the mill have a pulp mill spill collection system for floor drains?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
428. If the answer to the preceding question is (a), ^^.scribe the collection
system's function.
(a) Collected and discharged to the sewer at a controlled rate
(b) Collected and reused in the process
(c) Other (please describe)
429. DELETED - ANSWER IN PART I
430. What is the normal pulper temperature?
0217*7
-------
Mill:
Location:
Deink Mills - Stock Washers and Screening
If the information is available, indicate the approximate amount of
ills and washdown water from the deinked stock washers which goes
td\ the sewers.
a. Line\l
b. Line 2 \
c. Line 3 \
GPM
GPM
GPM
432-434.
432.
Indicate the
Line #1
e of washers used.
(a) Screw washers
(b) Side hill washers
(c) Gravity deckers
(d) Vacuum washers
(e) Other (please describe)
433. Line ??2
(a) Screw washers
(b) Side hill washers
(c) Gravity deckers
(d) Vacuum washers
(e) Other (please describe)
434. Line #3_
(a) Screw washers
(b) Side hill washers
(c) Gravity deckers
(d) Vacuum washers
(e) Other (please describe)
021748
\
-------
Mill:
Location:
436.
Counter-current washing for wastepaper and deinking - Is counter-current
washing of the stock practiced?
0 Yes
No
Close ^m screen room - Is the decker filtrate used for all of the dilution
on the screens and cleaners?
(a) Yes
(b) No
(c) To the extent possible
Explanation (\f needed)
437. Recook screen room reject^- Are screen room rejects either recooked or
refined?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
438. Give the approximate percent of the total screen room decker filtrate
which is normally sewered.
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-80%
(e) 80-100%
021749
-------
Mill:
Location:
43
444.
Decker filtrate for vacuum washer showers
on. the brown stock washer showers?
Yes
(b\ No
(c) XQ the extent possible
Lanation (if needed)
- Is any decker filtrate used
Eid
V. Deink Hills -pleaching
440-441. DELETED - ANSWERED IN PART I
442-443. Give the type of bleach line washing for the following:
442. Bleach Line #1
(a) Jump-stage counter-current washing
(b) Straight counter-curren\ washing
(c) Co-current washing
443. Bleach Line #2
(a) Jump-stage counter-current wash
(b) Straight counter-current washing
(c) Co-current washing
White water use on bleach washer showers - IsVny excess paper or pulp
machine white water used on the bleach plant washer showers?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
021750
\
\
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Mill;
Location:
Do the materials of construction (washers, pumps, piping and tanks)
in the bleach plant allow for straight counter-current washing?
446-447.
What percent of the chlorine washer filtrate is reused?
(446\ (447)
Bleach L\ie i-1 Bleach Line #2
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-80%
(e) 80-100%
(a) 0-20%
(b) 20-40%
(c) 40-60%
(d) 60-80%
(e) 80-100%
448. If any is reused, where ik is used and give the approximate amount.
a. Where
b. Usage, GPM
449. What is the chlorine residual in the filtrate?
mg/1
W.
For questions 450 through 462 please indicate the usual discharge
point for the liquid waste listed. IndicateNthe answer utilizing one
of the following answers: (a) Evaporated & Burned; (b) Sewered;
(c) Reused (totally); (d) Reused (partially); Cfe) Landfill or Sold.
450.
451.
452.
453.
454.
Digester Vent Condensate
Blow Vent Condensate
Blow Liquor
Spent Liquor from the Washers
Chipwashing or Steaming
021751~
\
-------
Mill:
Location: &rClC 4/? "fofr't/ -t
455. ^Meaner Rejects
X.
456. Screen
457. pump seal Water
458. Surface Heat Exchanger
459. Spills and Washup
460. Stripped (or clean) Condensate
461. Hot Water from the Economizers
462. Decker Filtrate (screen room)
X. Paperboard from Wastepaper - Pulper Area
463-465. DELETED - ANSWERED IN PART I
466. Does the mill have a pulper area spill collection system for floor drains?
(a) Yes
(b) No
To the extent possible
Explanation (if needed)
467. if the answer to the preceding question is (a), describe the collection
system's function.
(a) Collected and discharged to the sewer at a controlled rate
(b) Collected and reused in the process
(c) Other (please describe) •
021752
-------
Mill: Location: .t -*-
"" « - T~ «"••'T~ » IIIILILI III I 1 IF _M ... — - I l«fm ._..—
468. if the information is available, indicate the approximate amount of
spills .arid washdown water from the thickeners which goes to the sewers,
a. Line 1 GPM
b. Line 2 . GPM
c. Line 3 GF*
469. Give the approximate percent of the total screen room decker filtrate
which is normally sewered.
(a) 0-20%
w 20-40%
(c) 40-60%
(d) 60-80%
(e) 80-100%
Paperboard from Wastepaper - Liquid Waste Sources
For questions 470 through 475 please indicate the usual discharge
point for the liquid waste listed. Indicate the answer utilizing one
of the following answers: (a) Evaporated & Burned; (b) Sewered;
(c) Reused (totally); (d) Reused (partially); (e) Landfill or Sold,
470. Cleaner Rejects _ _ _ _
471. Screen Rejects _ _ ^ _
472. Pump Seal Water _ \r_ _ _
473. Spills and Washup . _ -V _ _
474. Hot Water from the Economizers _ l/^ _ _
475. Decker Filtrate (screen room) ___ _ *
021753
-------
Mill:
Location:
k-\. Builders Paper - Stock Preparation
476. \ELETED - ANSWERED IN PART I
477. if digester is used, indicate whether water or steam is used for cooking.
(a) Wat
(b) Steam"
l-'8. if water is useoy indicate the source and approximate amount.
a* Fresh Water
Recycled Water
gallons per day.
gallons per day.
479. Are any chemicals used in chis digester process?
(a) Yes
(b) No
480. i±st the approximate tons/day of reje\ts from the attrition mill (refiner),
__________________ tons/day
481. How and where are rejects handled or disposed\of?
482. For other fiber sources used, indicate the preparation process used
prior to the blending chest. (Cutting and shredding, \eater tank, etc.)
a- Rags
b. Wastepaper
c. Other
021754
-------
Mill:
Location;
483,
For each of the preparation processes used, indicate the source and
amount of water used (i.e., fresh water, white water, etc.)
Source of Water Amount (gal/day)
484
Please give the sourceyand amount of water used at the refiners.
485. List the approximate tons/day of r^ects resulting from the stock pre-
paration process(es) used. (Attrition Mill and/or Pulper)
tons/day
tons/day
tons/day
486. How and where are rejects handled or disposed of?
487. Please fill in the following information on the rifflers
screening after the blending chest.
ITEM
a. Rifflers
b. Screens
Rejects . Method of Rejects
(tons/day) Handling and Disposal
021755
-------
Mill: l-} V*V ± Location:
B-l. Paper Mill - (All mills except Builders Paper. Builders Paper mills
go to Item C-l)
488-490. DELETED - ANSWERED IN PART I
491. is felt vacuum pump water reused?
(a) Yes
No
(c) To the extent possible
Explanation (if needed)
492. Does the mill have a stock spill collection system?
(a) Yes
(b) No
A
(c) Partial
493. if the answer to the preceding question is (a), describe the collection
system's function.
(a) Collected and discharged to the sewer at a controlled rate
(b) Collected and reused in the process
(c) Other (please describe)
494. Give the frequency of waste significant grade changes; also, if
possible, give the stock quantity sewered.
021756
-------
Mill:
Location:
495. Is the mill central storage of white water (a) and slush broke (b)
adequate with regard to effluent discharge?
a. White Water
Yes
(b) No
(c) To the extent possible
Explanation (if needed)
b. Slush Broke
Yes
(b) No
(c) To the extent possible
Explanation (if needed)
496. Are special provisions made for spills, screen rejects, and excess
materials from coating or.sizing systems?
**
(b) No
(c) Limited
497. Does the mill employ organic solvent coating/saturating operations?
(a) Yes
V (b) No
498. If yes, please give the type and quantities (Ibs/day) of organic
solvent used.
02175?
-------
Mills
Location:
/' •
499. Give the average daily organic solvent coated/saturated paper produced.
- _ _ tons/day
500. Please indicate effluent from the combined papermaking facilities
as follows: (i.e., total flow from all machines).
Waste Source
a. Centricleaner and machine
screen rejects
b. Couch pit, seal box, and any
other unclarified white water
overflows
c. Thick stock spills, dumps,
washups from stock prep, area
and machine
d. Excess clarified white water
Volume
GEM
Suspended Solids
(if applicable)
Ibs/day
gal/day
•ster fror. v
. or pump s<.
r. Clear water discharges - i.e.,
cooling services, condensate,
other non-process services
g. Other effluent sources - Not
included above.
h. Total paperraill effluent
C
-------
Mill: Location:
502. Reuse press effluent - Is the press effluent reusec in the saper mill''
(a) Yes
(b) No
To the extent possible
Explanation (if needed)
503. White water for vacuum pump sealing - Is white water used for vacuum
pump sealing?
(a) Yes
. No •
(c) To the extent possible
Explanation (if needed)
504-505. DELETED - ANSWERED IN PART I
506. White water storage for upsets and pulper dilution - Is excess white
•water, overflows from the main white water tank or the cloudy side
of the saveall saved in a white water storage tank of sufficient size
for charging and dilution at the pulpers?
(a) Yes
(b) No
S^(c) To the extent possible
.'
Explanation (if needed)
507. Does the mill have either four stages of cleaning or three stages of
cleaning with elutriation in the paper mill?
(a) Yes
(b) No
021759
-------
.-O^'*i il I. Oil
308. \DELETED -- ANSWERED IN PAST '.
509. Civv-S^the ruur.her ni hsaveaj.id; used.
.2
510. Provide the \ollowing \;.-.u^?: ust: jnfoc:r.ir.icn:
Pracees \ v.'a-cer Sourco A«r.junt of Water
Stock Dilution
ii~i iOW VGiUlES £i~-C~-JC'^
(a) Yes
(h) Ka
Average daily ,di::c.^.. .
seccicn.) .
MOD
-.-d ^r?.s (forrair.g
Fill in tru; following iv^onnatlc
'•mite water recycled:
a • Recycled To Aia
•ine -.ants vat&r:
MGD
MC-D
b. Whitfc water sewered
MGD
021760
- 106 -
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Mill:
Location:
D-l Build-virs Paper - Saturating and Coating (if applicable)
Include the saturating and coating process, specifically tht number
of stations, what raw materials are used and where (i.e. asphalt, talc
etc.)» and the amount and location of cooling water used on the
schematic requested in Item B, Section VIII.
514.
ED - ANSWERED IN PART I
515. Are lowSyolume cooling water showers in use on the saturating and
coating process?
(a) Yes
(b) No
516. Is any of this cooing water reused?
(a) Yes
(h) No
lo
517. Give the amount of cooling water reused and the amount sewered.
a. Reused MGD
b. Sewered MGD
E-l Builders Paper - Internal Controls
518. Is recycled water used for the packing glands of process pumps, and/or
the vacuum pump seal water?
(a) Yes
(b) No
(c) To the extent possible
Explanation (if needed)
-------
Mill:
Location:
\519. if "Yes" indicate the amount of water recycled.
Process pumps packing gland -
\
520.
Vacuum pump seal water
Is a sp.ill control system used?
(a) Yes
(b) No
(c) To the exie'ftf possible
Explanation (iXneeded)
521. If "Yes", what process areas\are handled by the spill collection systar.1
522. Which of the following is true of the mill's spill collection system
procedure?
(a) Water recycled
(b) Water gradually discharged to treatment
(c) Water treated separately
(d) Other (please describe)
523. Describe any other internal controls which are being used toxdecrease
the water and/or reduce the wastewater pollution load. -
021762
- 108 -
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/}>L
Location:
F-l Acid It iona 1 Inf orinat ion (All Mills)
524. Does the mill have a program for disposal of old electrical trans
formers?
!/(a) Yes -
(b) No
525. Piaase give the number of people employed at your mill.
021763
- 109 -
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Mill:
Location:
V. . WATER USAGE AND EFFLUENT TREATMENT PRACTICES
Instructions for Completing Section V
Section V requests information on the mill's v?astewater treatment practices.
In Section VIII a general schematic of the effluent treatment system is
requested. You have the option of providing any of the data requested in
Section V on the schematic. If you do this, please indicate on the
question(s) involved that the data is presented on the schematic.
A. Water Usage
526. Indicate the source and amount of process water.
(a) Surface (i.e., river, lake or reservoir)
(b) Groundwater
(c) Other (please, describe)
527. Does the quality of the ;:.••
(a). Yes - :.-..::-• Iain
MGD
MGD
-•r-ter in this mill?
(b) No *""
523. Indicate the source and amount of the mill's cooling water.
6
(a) Surface
(b) Groundwater
(c) Other (please describe)
MGD
MGD
529. Indicate the source and amount of the mill's boiler feed water.
(a) Surface MGD
(b) Groundwater ' ; MGD
(c) Other (please describe) *•_
Y
021764
-------
530. Describe treatment used for boiler feed water conditioning.
531. Give the disposal method now employed for boiler blowdown water.
(/(a) Sexjered to treatment plant
(b) Directly discharged
(c). Directly discharged with pH adjustment
(d) Directly discharged after cooling
(e) Other (please describe)
B. Background Data
532-533. DELETED - ANSWERED IN PART I
534. How is cooling water disposed?
(a) Separate discharge to receiving stream.
(b) Combined with process waters before treatment.
*^(c) Combined with treated process waters. •
(d) Recycled.
C. Indirect Discharger please provide the following information:
535. Name and location of POTW which handles your wastewater.
/i'£~/L,.C''-
536-537. DELETED - ANSWERED IN PART 1
538. Are there specific pretreatment requirements or limits upon pollutant
parameters imposed by the POTW system to which you discharge?
(a) Yes
(b) No
021765
-------
"ill:
Location: /9/ &f(. */*'$• ^CCj 'fa
- . -- . - : - '—
539. if the answer to the preceding question was (a), please list the specific
pretreattaent requirements or pollutant parameter Units' imposed on your
mill by the POTW.
540. DELETED - ANSWERED IN PART I
541. if neutralization is practiced, till in the following.
Chemical used //?fe*><>y
542. DELETED - ANSWERED IS PART I
43. Are any chemicals or other settling aids added to the pi
units?
•(a) Yes •
(b) No
(c) To the extent
• rv treatment
Please show the wastewater strea-ib
system (if applicable).
Process Source or Sewer .No.*
a. Design Values Average Day ""
Maximum Day
Maximum Month
b. Primary Treatment Effluent Average Day
Maximum Day
Maximum Month
c. ._ Average Day
Maximum Day
Maximum Month'
;;r the secondary treatment
Flow, MOD BOD, Ib/D TSS, Ib/D
''Process source or sewer number should be keyed to the mill process and
wastewater treatment scUetnat icued in Section VIII.
-------
Mill: /fu~f£-, '• /£"./>f-t. li/L tl? • Location; &* <^V '/» '' *&& 'A-'^
~
7T
545. Give the normal pH of the wastevater at the influent to the secondary
treatment System.
(a) 4-6
'(c) 8-10
546. DELETED - ANSWERED IN PART I
D. Direct Discharger please provide the following information:
547. Name of the effluent discharge receiving water
/y>^ f
548. Enclose a copy of current or proposed NPDES effluent discharge limits.
Sl/&?-~ S^l'f? /?,!?' Ay*. ___
."•'•?. DELETED - ANSWERED L".
550. If \jastewater discharge !:•; seasonal or intennittant non-continuous,
approximately how many days out of the year do you discharge to the
receiving water.
(a) . Less than 30 (f ) 211-240
(b) 31-90 (g) 241-270
(c) 91-120 (h) 271-300
(d) 121-180 (i) 301-330
(e) 131-121 .fr"X(J) 331-360 ^
E. Preliminary Treatment
551. DELETED - ANSWERED IN PART I
552. if neutralization is practiced, fill in the following:
Chemical used
021767
- 1
-------
Mill:
I -•:.-
I -
/?. .,*.' » f. -,*/**t", ' X". _/ /«/ .
Location:
F. Primary Treatment
553. DELETED - ANSWERED IN PART I
554. Are any chemicals or other settling aids added to the primary treatment
units?
(a) Yes
"(b) No
(c) To the extent necessary (intermittent).
G. Biological Treatment
555. Provide the following information for the biological treatsent system.
(if applicable).
Process Source or Sewer No.* Flow, MGD 50D, Ib/D TSS, Ib/P
a. Design Influent Values Average Day
Maximum Day
Maximum Month
Primary Treatment Effluent Average Day
Maximum Day
Maximum Month
Other Wastewater Streams Which Enter the Biological Tres-sent Systems
Without Primary Treatment
Average Day
Maximum Day
Maximum Month
Average Day
Maximum Day
Maximum Month
^Process source or sewer number should be keyed to the rill process and
wastewater treatment schematics requested in Section VIII.
021768
-------
Mill: /f&'yfcv /6£1 /£// Location: // £Vc ' /«. > /~# Vi
.
556. Give the normal pH of the wastewater at the influent to the secondary
treatment system.
(a) 4-6
/. (b) 6-X9
(c) 8-10
557. DELETED - ANSWERED IN PART I
H. Secondary Solids .Removal
558-559. DELETED - ANSWERED IN PART I
I, Sprav Irr igation
\ 560. T.: ::rc-2';.'.._: w,istewatt?r used for irrigation?
J. Sludge Handling and Disposal
561. DELETED - ANSWERED IN PART I
562. Give the percent solids of the sludge after dewatering and prior tc
disposal.
(a) 5-10%
(b) 10-20%
(c) 20-30%
(d) 30-40%
(e) above 40%
563. Describe any leachate management practices performed at the mill for
sludges which are disposed of on land.
021769
-------
Mill: Afcfl/£ V PafX. -I ' ij/ // Location:
K. Foam Control - (Wastewater treatment system only)
564. Does the mill use foam control measures?
(a) Chemical
(b) Physical Methods
None
(d) Other - explain
021770
- 116 -
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Mill: •lCJfet"' f£
Location:
L. Cost Information
565. Provide cost data indicated for effluent treatment system in 1976 dollars.
Use the cost multiplier factors, which follow, to convert to 1976 dollars.
Annual Operation
Total Capital Cost and Maintenance Cost*
a. Internal control devoted to
effluent waste load reduction.
b. External Treatment System . __ — _ f C^itc e
""•£""" -a.
c. Primary Treatment 2^V^2'3 7. — —"
d. Secondary Treatment ^^ist^t "^ "~" ""
Construction Cost Multipliers
•
to Convert Capital Cost to 1976 Dollars
1956 =
1957 -
1958 =
1959 =
1960 =
1961 -
1962 =
2.535 1963 = 2.186
2.380 1964 = 2.161
2.325 1965 = 2.124
2.25^ 1966 = 2.051
2.22: 1967 = 1.978
2.22Q 1968 - 1.884
2.207
1969 =
1970 =
1971 =
1972 -
1973 -
1974 =
1975 =
1.794
1.689
1.564
1.485
1.317
1.242
1.100
*Factors to be .considered in Annual Operation and Maintenance Costs
(0 & M Costs).
1. Manpower - both operators and maintenance personnel
2. Contracted services
3. Energy Cost
4. Trucks for hauling
5. Nutrients
6. Leased equipment
7. Disposal costs
8. Sludge handling
9. Sampling and analysis
10. Equipment replacement (except major capital)
Exclude Depreciation
021771
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Mill:
1 1
Location:
566. For mills which discharge, to a POTU, please give the annual user fee
with a breakdown for capital cost recovery and operation ami maintenance)
costs.
a. Capital Cost Recovery(if available)
b. Operation and Maintenance (if available)_
c. Total Annual User Fee
567.
Please give the basis used by the POTT.) TSS only
(d) Combination of parameters (please indicate)
(e) Unknown
Sits -editions and Av -.-.I lab ill'. ;•-£ Lanr.
is there sufficient land for expansion of your wastewater treatment
system for BATEA?
) Yes
(b) No
(c) Unknown
559. Can the mill purchase land from adjoining property owners for possible
expansion of the wastewater treatment system?
V (a) Yes
(b) No
(c) Unknown
568.
021772
118 -
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Location:
570. Are the soil conditions in the land available for future expansion of
such a quality as to require special construction methods or special
facility equipment (i.e., ledge, water table and liners needed for
basins)?
V/(a) Yes
(b) No
(c) Unknown
571. Miscellaneous Discharges^ - Indicate any wastewater discharges not
described in Section V which do not flow to the wastewater treat-
ment system.
A
•: r-r-vscer Ch .- racteris- ics
572-577. .. rlLETSD - ANSWERED IN PART I
578. Was the analysis procedure used for BOD measurement in accord with
the method presented in Standard Methods for the Examination ofWater
and Wastewater?
~?
J
(a) 13th Edition
(b) 14th Edition
(c) No (please describe other method used)
579. Is a glucose-glutamic acid BOD standard analyzed?
(a) Yes
021773
- 11Q -
,
-------
Mill: ^'ly/VV &*•{*<• * ty'f> Location: £/&tW * fat.'
5SO. if the ansx^er to the preceding question was (a), please indicate the
normal frequency of the analysis.
(a) Daily
(b) Weekly
/;
(c) Monthly fl
(d) Quarterly
(e) Semi-annual
581. Please indicate the percent difference found between the BOD determinations
and the glucose-glutamic acid BOD standard '
(.") 0-5% ' . .
(b) 5-10% /
(c) 10-15%
(d) 15-20%
(e) Over 20%
582, Indicate the analysis procedure used for TSS determination at the mill.
(a) Standard Methods for the Examination of Water and Wast^water,
13th and/or 14th Edition.
(b) EPA analysis procedure adopted on October 16, 1973, and any
subsequent amendments.
(c) Other (please describe)
021774
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Location:
VI. FUEL AND ENERGY
A copy of the API "Monthly Fuel and Energy Report" has been included in
this section to assist the mill in calculating (if information is not
already available) the answer (s) to the questions asked. The API sheets
should be used as a guide for computation only, do not return the pages
with the questionnaire. For internal treatment energy cost calculations,
include only the following:
1. Equivalent steam (MBTU/Ton product) required to evaporate
reclaimed spilled pulping liquors from the average solids
level at which dumped up to a 10% solids level.
2. Also include steam (MBTU/Ton product) required in condensate
stripping operations necessitated by condensate reuse projects.
583. Give the total purchased energy (fossil fuel, electricity, steam,
etc.) as equivalent millions BTU/ton of product (Items 1 to 9,- less 10
from API forms).
584. Give che energy used for external treatment operations in KW Kr/Ton
of product.
585. Give the energy used for internal treatment as equivalent millions
BTU/ton of product.
VII. PRIORITY POLLUTANTS
DELETED - ANSWERED IN PART I 021775
_
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Mill: It,
Location:
V, -/..
VIII. PROCESS SCHEMATICS
Attach separate general block diagrams for the three items listed below.
Water Treatment (if applicable) - Provide a general block diagram
showing the water treatment system used, chemical application points,
average flow, and disposal method for backwash water. If the mill has
a raw water analysis available please attach a copy.
Manufacturing Process Schematic - Provide a general schematic of
the total mill process to include water balance and all process
wastewater streams. (See note at start of Section V.) Wastewater
streams should be Across referenced to the effluent treatment system
schematic.
B.
H
Effluent Treatment System - Provide a general schematic of the
effluent treatment system. Please key the diagram to the manufacturing
process block diagram so that the point of influent to the treatment
system for individual process sewers can be determined. Also show
all chemical application points; chemicals used; flow monitoring and
sampling points; average flow; size or area, volume, and number of
each treatment sysE-'-Ti component; sludge recycle and volv:ia; and
sludge dewatering/u-Lckening system.
Additional information on the mill's wastewater treatment system is
also needed to complete the data request. Please provide answers to
the following questions which pertain to your wastewater treatment
system. For questions which do not apply, indicate by writing N/A
(not applicable) on the space provided for the answer.
Primary Treatment
586. Give the following primary clarifier overflow rates:
a. Design gpd/f t2 at MGD
b. Current gpd/f t2 at MGD
021776
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Mill:
Location:
Biological System
For the biological system employed, please give answers to the appropriate
questions listed below:
System
Question
Aerated Stabilization a) Volume of the aeration zone
Basin
Answer
O. 22SL Mil. Gal.
Activated Sludge
b) Connected horsepower for aeration /
a) Volume of the aeration zone Mil. Gal,
b) Connected horsepower for aeration
c) MLSS (Mixed Liquor Suspended
Solids)
589. Trickling Filer
.r l-~ '^ •
592
\
a) Volume of media
b) Surface area of filter
a) Sur-" • -•: ->rea of RBC
a) Vol... storage
ft"
~Mil. Gal.
If nutrient addition is used, please give the average BOD:N:P ratio,
BOD:N:P :__:_
Secondary Solids Removal
Give the secondary clarifier overflow rates:
Design
gpd/ft2 at
b. Current
gpd/ft2 at
MGD
MGD
021777
-------
p ,.,.,. J.J.
CONFIDENTIALITY CL....1ED FOR THE FOLLOWING
Question Question Question Question Question Question Question
Number Number Number Number Number Number Number
\
021778
-------
PROJECT
MILL NO.
Products:
Check file for updated data:
COMR BY
CHK. BY
.'OS NO.
DATE
Average Tons/Day:
Wastewater
Flow, Kgal
BOD, Ib - — -
TSS, Ib
Check Schematics:
-Raw
. Per Day Per Ton
Final
. Per Day Per Ton
021??9
-------
i
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021780
133 fOMd
•ONI "CD woaor *o
-------
ENGINEERING
PLANNING
ARCHITECTURE
Edward C. Jordan Co., Inc.
P.O. Box 7050, Downtown Station
Telephone: 207-775-5401
Portland, Maine 04112
TELEX: 94-4329
TELEPHONE MEMORANDUM
PROJECT NO. Z & I &*T ~~& 2- DATE:
CLIENT: • •
PROJECT DESCRIPTION: '_'~~__'_
BETWEEN:
AND:
SUBJECT:
> JET ,
Id
/ I
Kf
y
ic,
DISCUSSION:
r~
II
a i
7P( i/e vr
^ .^- A tfv ;.
M r,
r+-
/ i
/>ic/
-------
\
\ ENGINEERING
.'; PLANNING
• ARCHITECTURE
Edward C. Jordan Co., Inc.
P.O. Box 7050, Downtown Station
Telephone: 207-775-5401
Portland, Maine 04112
TELEX: 34-4329
r
April 4, 1973
Mr. E. Harold Miller
Kieffer Paper Mills, Inc.
1220 W. Spring Street
Brownstown, HI 47220
Dear Mr. Miller;
Pursuant to our telephone conversation on April 3, I would like to
thank you for the information you supplied concerning the EPA 308
survey form. From your description of the mill's effluent treat-
ment system, I have drawn a schematic diagram. Please find en-
closed a copy of this schematic drawing. If there are any errors
in this diagram, please contact me so that I may correct the errors.
Sincerely,
Richard Linscott
021782
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