Document 3QvQ6VaKmpBxBOvwJJQK165GE
fliecesa
Mine -FocUi-fcy
Page PROCESS SURVEY - ENVIRONMENTAL IMPACT ANALYSIS
1
of 2
ASBESTOS
Planf
King City, CA
COMPLETED BY R. 0. Hopper
DATE
March 1973
' II - PROCESS/FACILITY DESCRIPTION
The mining procedure can be divided into three phases:
1. Stripping and Mining 2. Ore screening 3. Ore haulage
*
C Phase 1, Stripping and Mining, is usually done simultaneously. Stripping can be defined as
j the initial removal of approximately thirty (30) feet of surface material that is unsuitable
J"S for ore usage. The overburden material is removed from the pit area by means of heavy duty earth moving scrapers and bulldozers and hauled to a designated dump area so as not to inter/ fere with future mining operations. When necessary, the overburden is used for embankment
material for building future ore stockpile areas.
As soon as the overburden material has been removed, the actual mining of ore can commence. The mining of ore is done in the same manner as the stripping. Ore is removed by means of earth moving scrapers and bulldozers and hauled to a designated ore stockpile area.
Phase 1 is done entirely by contractor. Bid packages are mailed to at least three contractors
for a firm price per cubic yard of material removed, hauled, and dumped. In order to simplif1/
yardage computations, Stripping and Mining costs are integrated. The successful bidder will
then enter into a contract agreement for the project. While Stripping and Mining is being
performed, the Mine Superintendent' and Mine Foreman\will keep close scrutiny on the project so
- as to verify that all rules"and regulations are followed.
>
The present mine design consists of a level pit floor area approximately 1100 feet by 500 feet.
Forty feet wide benches extend from the pit area at an over all wall slope of 20 feet ofvertic
al rise for every 60 feet of horizontal increase. The benches continue until the original
contour of the hillside is reached, and will usually number 10 to 15 in our present mine loca
tion. The bench width is designed to be forty feet so that there is ample room for safe
equipment maneuvering.
_'
Phase 2 will usually begin in early Mayand will last approximately 6 months. This work is
totally performed by UCC personnel, andmay be performed at the same time Stripping and
Mining occurs. The following pieces of equipment are necessary for the completion of the ore
screening process: 2 rubber-tired 4 yard front end loaders; 1 D-8 crawler dozer; 1 3000
gallon capacity water tank truck; 1 portable screening unit; and T portable conveying-stacking
unit.
'
The first part of the ore screening process will be to position the portable screening and conveyor units at the ore stockpile area. The crawler dozer begins by pushing the stockpiled ore closer to the screening unit. The front end loader in turn feeds this ore to the screening unit. The screened material is stockpiled via the conveyor unit for easy loading into the ore haulage trucks. The water tank truck is used to supply water for a dust suppression pro gram that includes water sprays on the screening and conveyor belts, irrigation type sprays on the ore stockpile area, and watering of the entire work area and haul roads.
Once the screened ore has been stockpiled, phase 3 can begin. Ore haulage is done by con tractor and will usually requirej5 to 10 truck4 per hauling season1} The trucks used are tandem bottom-dump units with a 25 ton total capacity. All trucks are equipped with tie-down
A r^4
UCC 003571
Page PROCESS SURVEY - ENVIRONMENTAL IMPACT ANALYSIS
2
2
ASBESTOS
King City, CA
COMPLETED BY R. 0. Hopper
DATE
March 1973
II - PROCESS/FACJL1TY DESCRIPTION
tarps to minimize ore spillage and dusting, and Jacobs electric braking systems. UCC per sonnel will load the trucks during regular shift hours; however the drivers are permitted to load themselves whenever necessary. Once the truck is loaded, it begins a 55 mile trip to the King City Plant. The route includes 10 miles of UCC private access road and L5 miles of paved state and county roads. Due to the irregular alignment and various elevation changes, the round trip will require an average time of 5 hours. Careful maintenance of the UCC private portion of the route is performed periodically in order to maintain peak haulage efficiency. En route to the plant, the trucks are weighed (loaded and empty) across a public scales.
When the ore haulage truck has reached the King City Plant, it is directed to dump its load on a designatedVmi 11 ore stockpile area. A quart jar sample of each load of ore is taken and deposited in the laboratory for moisture analysis. When the ore has been properly dumped, it is considered to be part of the plant procedures for all further operations.
UCC 003572
V
Process Mrne Ea-ilLh
Pago PROCESS SURVEY - ENVIRONMENTAL IMPACT ANALYSIS
1
of 0
ASBESTOS
P^cn!'_________ King; City
COMPLETED BY
F. H. Larrison, Jr.
DATE_______March 1973
II - PROCESS/FACILITY DESCRIPTION
The mill contains 2 separate circuits:
I The main mill circuit in which asbestos ore from the mine is upgraded mechanically to 3 classes of product, i.e., standard grade, superstandard grade, and high purity.
II The RG-244 circuit in which high purity product from the main circuit is further purified and sized, and a fiber coating of Sip2 is obtained by chemical precipitation.
Circuit I Description
' _ .
:
(A) Rock Fiber Department - common to all products. Asbestos ore from the stockpile is moved
from the stockpile to the corn-bin feeder by loader and a conveyor belt. A controlled feed
of ore from the corn-bin reports to the primary vibrating screen where, with water addition to
form a slurry, the material is screened to t 3/^6 inch.
Upgrading-removal of magnetite, serpentine,' and other gangue material - and sizing of fiber content of the primary screen underflow is accomplished by cycloning the slurry through 3 6 inch cyclones, screening of the cyclone product by a 1 mm DSM screen, and cycloning the DSM underflow through 6 4 inch cyclones. The cyclone overflow reports to a 24 ft. thickener to become feed for the Refining Department. The cyclone underflow is processed through a 3 ftand a 6 ft. magnetic separator - in series - and is then routed to the 24 ft. thickener as refiner feed.
The 1 mm DSM screen oversize is tabled to give 3 table products, i.e., asbestos flake, middlings, and tailings. The middlings return to the DSM screen, the tailings report to the tailings classifier, and the asbestos flake reports to a 12 inch flake mill for grinding. Additional feed to the flake mill results from processing of the primary screen overflow which is upgraded by gangue removal in a jig separator and screened over a l/8 inch vibrating screen The screen oversize reportsto the flake mill while the screen undersize reports as feed to the DSM screen. Jig separator heavies are tailings and report to the tailings classifier. Ground fiber slurry from the flake mill is cycloned and the cyclone overflow reports to the 24 ft. thickener as refiner feed. Cyclone underflow material becomes refiner feed following magnetite removal in a 6 ft. magnetic separator.
Total tailings from the mill process are made up of the following streams:
Rock Fiber - Jig 'mill heavy fraction, shaking table tailings, magnetic separator tailings
Refiner Dept. - A cycloned tailings stream from the refiner primary cyclones.
(B) Refiner Department -
1. Standard Grade wet grinding mill surge tank.2
Product- Slurry underflow from the 24 ft. thickener is ground through a a BauerMill - to give 55$ -200 mesh, and is pumped to the filter feed
2. Super Standard C-rade Product - Slurry underflow from the 24 ft. thickener is ground through the Bauer Mill and then additionally ground through an M-30 wet grinding hammer mill. The resulting solids - approximately 75$ -200 mesh, are pumped to the filter feed surge tank.
UCC 003573
Process Mine Enr-LlLiy
Page PROCESS SURVEY - ENVIRONMENTAL IMPACT ANALYSIS
2 of
J
ASBESTOS
Plant
King City
COMPLETED EY
F. H. Larrison, Jr.
DATE
March 1973
I! - PROCESS/FACJLITY DESCRIPTION
3. High Purity Product - Super standard grade pulp is further upgraded and fiber size is
reduced by additional cycloning through a primary cyclone' circuit of 49 4 inch cyclones and
then cycloning this overflow product through 120 3 inch secondary cyclones. The overflow
slurry from the secondary cyclones reports to the filter feed surge tank. Cyclone underflows
become internal circuit circulating streams and tailings result from screening the underflow
of the primary cyclone circuit. Product solids are approximately 0.60$ magnetite and 83$
-200 mesh at this point. The high purity product slurry is used as feed for the RG-244 circui't
and by adding HO2 at 35% by weight to the slurry entering the filter feed surge tank, the
titanated products are made.
'
(C) Filtering & Drying Departments
_
The product slurry from the filter feed surge tank is filtered through Shriver filter presses. The filter cake is approximately 50$ solids and is moved from the filter area to the dryers by drag conveyers. All product is dried as a. pellet by introducing the filter cake to the RotoLouvre dryer by extrusion through a die plate. The normal product pellet is 5/8 inch diameter although-a l/8 inch diameter pellet is available in special products. Drying to less than l.Ot HpO is accomplished in the kiln type dryer using natural gas as fuel, and the dried pellets are then routed to one of two bins for storage by a series of bucket elevators and screw con veyors . Dried pellets can also be routed directly to a rail car for bulk loaded product.
Product Handling Department
.
Product packaging consists of two Raymond Mills, for grinding and opening of pellets prior to packaging, and two pressure baggers for filling bags. Two specialty product mills are avail able for making special grinds, i.e., a Jeffrey Mill and a Disc Mill.
Depending upon the product being packaged - whether pellets or open material - the pellets are fed from the storage bin by screw conveyor to either the grinding mills, for open material, or directly to the baggers in the case of pellet product. Open product from the Raymond Mills is conveyed by the air stream through a cyclone into a live-bottom bin from where it is fed to the baggers by screw conveyors. Filled bags are palletized in normally 40 bag pallets for shipment by truck or rail car. Product for overseas is hand loaded - individual bags - into containers. All product is palletized for removal from the mill building by fork-lift to the mill yard storage area and overseas containers are filled by breaking down of pallets.
Circuit II Description
The RG-244 circuit receives it's feed from two possible sources:
1. RG Feed Preparation circuit - Slurry from the 24 ft. thickener is ground in an 18 inch wet grinding hammer mill - Rietz Mill - and is then cycloned in 3 inch cyclones. The cyclone overflow, containing 8-12$ +200 mesh particles, is routed to the 244 feed surge tank while the cyclone underflow returns to the 24 ft. thickener.
2. High purity product slurry, prior to filtering, can be routed to the 244 feed surge tank
as feed material.
'
UCC 003574
Process Mitie
Fee'eU-ry
Page PROCESS SURVEY - ENVIRONMENTAL IMPACT ANALYSIS
1
ASBESTOS
Plant
King City
COMPLETED BY
F. H. Larrison, Jr.
DATE
March 1973
I! - PROCES5/FAGLITY DESCRIPTION
The slurry from the 211 feed tank is further ground in a Rietz Mill and cycloned in a hank of ll 1 inch cyclones.- The overflow solids from the cyclones, now containing less than 0.30$ magnetite and 0.60-0.70$ +200 mesh particles is routed to one of two treatment tanks. Measure amounts of Na^SiOj and CH3COOH are added and, following the proper mixing times, the treated batch is discharged into the filter feed surge tank.
The treated slurry is filtered in a filter press and the resultant filter cake, approximately
18-20$ solids, is forced through an extruder into the.Roto-Louvre-kiln type-dryer. The dried
pellets are conveyed by a bucket elevator to the storage bin.
;
All RG-211 product is fully opened prior to packaging by routing the pelletized-dried-material
from the storage bin to an 18 inch Raymond Mill. The opened material is- air-swept from the
mill to a dry cyclone and discharged into the bagger supply chamber. The product is packaged
by a pressure packer into paper bags. Each bag is sealed in a polypropylene overwrap bag for
moisture control and the individual bags .are palletized in a 35 "bag pallet enclosed in a waxed
cardboard shroud. As with the other mill products, RG--244 being shipped overseas consists of
individual overwrapped bags hand loaded into containers. -Other shipments are made by rail and
by truck.
. i_
Tailings are removed from the milling circuits at approximately 70-80$ solids by converying to a temporary tailings pile immediately east of the mill building. Periodically the tailings are moved from the temporary pile to the permanent location approximately l/4 mile east of the mill buildings. Haulage of the tailings is accomplished by use of a self propelled scraper.
UCC 003575
pr:OCi'`-'.5i 3t'MVI'Y - rMVIUOMrACTAj^AL^lS
Pcigc 1 of 1
PUOCIiSS COWPUilHD CY
ASBESTOS F. H. Larrison
PLANT DATP.
King City March 1973
XIV.- CTHER EMISSIONS,POL11
PSORIFMS AND EMPLOYEE COMMENTS
MIME
Ore Dust During Ore Screening and Ore Haulage
The mine dust suppression program keeps the ore stockpile, screened ore, and, in
general, the entire pit working area relatively free of.airborne dust particulates.
There are occasions, however, mostly due to area winds and extreme temperature, wh^n
dust conditions will be less favorable.
All UCC personnel are required to wear approved respirators when dust conditions occur.
Ore haulage trucks are covered with tarps and only minor amounts of dust escape along
the haul route.
.
Ore Dust During Stripping and Mining
.
Airborne dust particulates are more noticeable when stripping and mining is being per
formed. The contractor is responsible for keeping the conditions at a minimum. Haul
road blading and watering is necessary not only to improve the dust situation, but
also to attain peak operating efficiency.
Approved respirators are provided for the contracted workmen.
Dust samples are taken on.an average of two times per operating year.
Noise Levels
The maximum noise level of 90 decibels is exceeded when the ore screening equipment is in use, therefore, earplugs or muffs are necessary.
MILL Airborne Asbestos Fiber
tt;6403
Ore stockpiles, as well as the temporary tailings pile, are immediately adjacent to the mill process building, office building, warehouse, laboratory, and maintenance facilities. During the spring-summer-fall months, a 20-30 mph wind from north to south is a daily occurrence in this area and control of blowing dust is a problem. Water sprays are used to keep the stockpile area vet while a sprinkler truck is employed to control dusting on level surfaces. A contract sweeper cleans the parking area and asphalted and concrete areas around the mill buildings. External process transfer points, i.e., in the dryer and dust collector areas - are enclosed and internal negative pressures are maintained.
Airborne fiber levels in the process and service buildings generally range below the TLV. However, in the product grinding and bagging circuit, there are times when the level is well above the TLV. Modifications have been made in the department by en closing the bagging and conveying machines and maintaining a negative pressure in the hoods but levels remain too high when using the palletizer. Use of respirators is required in this area.
Noise levels are right at or slightly above 90 dBA in all production areas and on
loaders. Earplugs are necessary.
UCC 003576
'
".
.
PLANT
King City, CA
CCMPLr.'iCD BY F. H. Larrison
DATE
Page 1 of 1 T ANALYSIS " '
March 1973 Page 1 of 2
A. Ciher Problems (Such as radiation.
MIKE
The UCC private portion of the ore haulage route includes 5-l/2 miles of salt- stahilized red shale roadbase material. During the hot and dry summer months, ore truck traffic produces clouds of dust. Attempts are made to minimize the problem.by periodic re-blading and watering of the roadway.
Since our stripping and mining operations result in a single pit with wide benches at controlled elevations, we do not encounter any land reclamation problems at this time.
The dumping of overburden material at several convenient locations outside the immed
iate pit vicinity might create some future problems since the waste piles are steeply
sloping at the natural angle of repose.
The moisture content of overburden and ore material will range between 15 and 20 per cent, and after material is placed in piles, a semi-crust is formed on the exposed surfaces which effectively eliminates wind-blown dust unless the crusts are disturbed by vehicular traffic.
In general the mine is located in an isolated area with the nearest inhabitant 9 miles distant, and the nearest town (Coalinga, California) some 30 miles to the southeast.
MILL
Product Packaging
Development of leakproof packages to stop leakage of asbestos into shipping containers is necessary. All product is at present packed by a pressure packer and perforation of the multi-layer paper bags is necessary. Another leakage point is the bag fill spout which is not positive 'sealing. Asbestos is leaked from the palleted hags during transit in RB cars, truck vans, overseas containers, and flat-bed trucks. A contam ination problem is thus created for the party unloading the shipping container anri for customers storing our product.
UCC 003577
' Pncje 1__of I
`t n vipon: `,r ni a l protection s ulvey-- cnvironme nta I. impact ana lysis "
PLANT
King City
COMPLETED r.Y
F. H. Larrison
DATE
XV.- SPECIAL PROBLEMS [ B. Ccnm^.'iJ:'/ Cc-Tsplciird cijit! AirlhCc To'.vc.iJs Industry
March 1973
Poyc 2 o.r 2
MINE
Public comments have been limited to two groups: one group being the Bureau of Land Management and the other being the San Benito County Supervisors.
In August 1971 the Bureau of Land Management finalized its designation of the San Benito
Mountain natural area. Prior to this, UCC had agreed to curtail any immediate develop ment of their claims located within this area.
. -1
The San Benito County Board of Supervisors initiated, in June 1972, a proposed quarrying
ordinance which would be directed toward reclamation1 of mined areas. As of this writing,
, UCC has no further word on the status of the ordinance.
Note:The UCC present mining.operations and the majority of its claims are located in San Benito County. Some claims are in adjacent Fresno County.
MILL
There have been no community complaints directed toward the mill. Some complaints have been voiced verbally to people working at the mill - concerning truck traffic on the Bitter Water road during the time ore is being hauled from the mine to the mill.
Community attitude toward the mill operation has been favorable so far as we know.
UCC 003578
bG 1
.. Pcxjc i or i
ENVIRONMENTAL PROTECTION SURVEY - ENVIRONMENTA I. IMPACT ANALYSIS
PLANT
COMPLUlD nv
King City, CA
F. H. Larrison
DATE
XV.- SPECIAL PROBLEMS
March 1973
Pocic 2 of 2
C. Emls3r5,?s/!,ferr.s nor,ln.Corrollerce- 'yit'h Exist! no Rscvjicilens cr Reculolory Aoer.cy Reouesls
_____(L^-stri-.e.r.i
Ihc.w i'ot Lc.'rniinncs; " "
" /- / ,
MILL
Fiber count in the bagging still exceeds TLV at times when operating the palletizer due to the air-magnet mode of operation of the machine. A new palletizer is on order and will be installed by mid 1973*
EPA regulations call for cloth filter type collectors on asbestos ore dryer off-gas' stacks. Baghouse collectors are on order, engineering is completed, and installation of the collectors should be complete by mid 1973*
n~ , V Ou
UCC 003579
Pi'OCCSS SUivYlY - ENV!UONMi'NTAL IMPACT ANALYSIS
PLANT ____________King City, CA .__________ COMniULlKiY___ F. H. Larrison__________
^ATEMarch 1973-
XVL - MiSCf'! LANi-'QUS
rvtj;c i of i .
MINE
'
_
1. Plans for Improvement
A. Resurface portions of the UCC private ore haulage road with asphaltic pavement. This will improve the dust problem and reduce road maintenance costs as well as insuring greater vehicular safety and performance.
B. Insist on more adequate ore truck side boards and better tie downs for the tarps. Past conditions have resulted in minor spillage over the sides of the trucks..
C. Investigate the benefits of cab pressurized air conditioning units on the front end loaders. This would eliminate the wearing of respirators except during severe dust conditions.
D. Continue to collect airborne dust samples during mining operations to determine the need for increased dust suppression methods.
E. Improve and enlarge the water spraying dust control systems installed in 1972.
MILL
'
Improvements
1. It Is possible that government regulations will result in our having to build a change house where each man can have two lockers so separated that his street clothes will not be contaminated by his work clothes. This is in a state of flux and depends upon interpretation of the regulations and our success of failure in achieving TLV levels in the bagging area. It was thought that if necessary a change house would not be required before 197*5-
2. Plant engineering will direct efforts at noise abatement in the mill as time is
available.
'
3- Installation of a pellet cooling circuit will allow bagging of pellets In nonperforated tags by an auger packer rather than a pressure packer, which will help control dust levels somewhat. Other engineering efforts are directed toward bags with positive sealing fill spouts and shrink wrapping of individual bags and pallets to minimize spillage both internally and externally to the mill.
Monitoring - The operation is presently monitored for airborne asbestos fiber by sampling at nine locations each month. Future monitoring will probably require time weighted exposure determinations at six month intervals on operators.
4 ^ Ou 3
UCC 003580
.* ,
'
t acjc
rcocrss r-ur;vrv - rHviroN/^rNTAi. impact analysis
'
rKOCESS/FACfMTY AW^^f'LANT Kwc CIT'/
COMPLETED I'.Y
--DAJE--------- 3/.7^1------- '--
01
Ill- A - INPUT .
.
lUcuv Wc:l'l, Utility, etc.
1 Units
Water, I'Oi 1 cr ;ci,-d
Cecil*?:
ftfirsf? GaJu*
Cycle McL000
- Casa*** WhTixTtueir Stcanv
Utilities, Ciiior
Amount j
Function |
Remarks
2.^00
MO..
___________________ _____ ____
kftP OtsWer fonts 1 ne 3p^A/Mi.aJts SANA* Oft PufS"`5clt&s.tttNi
&tdLt#G PAVU&tft Iff SurtMt*._ SvtfiifsDost 2 IbAQS OffftbAO PS.H.VA'S
2 Uabs on fir ARttftnj;
t
Materials, Rcjv/
-
Diehl FiaZu Gasounl /u&R\Ctm# On.* L__ GntAse !
___ DiCSBu__ Putt. L. ufifttcA TtNC 3 It&fi.EAS
.. __ rhfsiL Put t.
...LuSAvRATt^C O'** GntASJE .
GftSO^i tfS
. Materia!', Auxiliary
\GPD
2S
^ K A At Ti Ttes USED
1 ".. _ 30
fly ucc. &\LtPrrA/vr
1 **
l
tfos PtK VAy
\Ls*fo l i _____
LMkvrHS fttA ^LAR
1 ..
I
! ePO 1 Se>o
atjm*TZ d
UsSoBy CojJ7 ftAc To /?
-j- ft i *" *
7d Maul OfKL
l&%/rs 1 it
i* f
/HmiDay Me>/ YA ^___
1
_____ 1______ ___
i
| CPD 1 3tO 1 / STtmATlo __ US0 3y Ce*tTR8c74ft
**
Las/o i tlfip
ft i *
S n *-
S *
SrAlPP/NiT AND MntttfC Jtfoi/PAY /ffttNTM
1 1 pA 'is.A A. |i 1
1 -.
1
1
1i
'll.
i
Ill-n - USEFUL PRODUCTS
Stream
CciT'.roncnt
r.-ri/ff/dAy
Orf
1 /^OA
I __ QV*8U(ltN____ ____ 1__fdsa _ __
i ... t -- _ ORZ --
1
___________ .1 1
i ! 60
1 j
1
1 .i
L_r
UCC 003581 ^
Hove in! "at-a
VJrttLt A1/ftS/AfO ft ** *
**
_
While J^AuutAf ^Ta/tcSa) BortfM
Du.mp fttsm Minir IB fiAur
.
Mn.es
:
^ c ^ 4
LM k 1',VI s
Jl' it) "I
I[ I
PLANT KttLG-CjT/____ cOMruiun:, a, 0. MAkZTS.ru_____
DATE
3/7 3
XII. - WATER OUA1ITY
DISCHARGE NO. PiSCHbfUtt Jaa PV0 NAME___ vA/*CJL8Tifi - fiNB___g.C0_kA7Z_
P9Cof
Poge I of 2
PARAMETERS Of INTAKE WATER AND DISCHARGE
PARAMETER
untreated
INTAKE V/A1EP.
DAILY f/.eIfaf I-r-l^r:ge
CO. NL N-
TRATiCN
UNITS fnillirionii/lilcr = fipm
ALKALINITY(os C0CO3)
m
lib
B.O.D. 5-DAY
CHEMICAL OXYGEN DEMAND (C.O.D.)
<z
QSH-
TOTAL SOLIDS
TOTAL DISSOLVED SOLIDS
TOTAL SUSPENDED SOLIDS
TOTAL VOLATILE SOLIDS
3SS
3SS
<1 SO
mt nso
}H
3t 7
AMMONIA (os N)
. *<./6
<.10
PARAMETER POTASSIUM - TOTAL
UNTREATED
DAILY AVI ' --r
INTAKE
feOviP
WATER
TRAT 1CN
_ UNITS mi 11 iarcms/ liter L pr*Ti
SODIUM - TOTAL
OIL AND GREASE
kerosene
SURFACTANTS
<.01
6.02
ALGICIDES
CHLORINATED HYDRO CARBONS (EXCEPT PESTICIDES)
KIELDAHL NITROGEN
<>I0
<t 10
PESTICIDES
NITRATE (a: N)
<.oZ <oZ
PHOSPHORUS TOTAL (os Pi
ACIDITY (os C0CO3) TOTAL ORGANIC CARBON (T.O.C.) TOTAL HARDNESS NITRITE (os N)
ORGANIC NITROGEN PHOSPHORUS-ORTHO
fcs Pi SULFATE
SULFIDE
SULFITE
bromide
CHLORIDE
CYANIDE
0.3
--
<.ct
J.IO
4.3 2.4
4*61 <J0
o.z 20
</ <.\ 3H j'.oS'
<1 <J /?2
RADIOACTIVE PARAMETERS
UNITS _ picocorie/litcr
DISSOLVED ALPHA - TOTAL
ALPHA COUNTING
ERROR
.
DISSOLVED BETA - TOTAI
BETA COUNTING FRROR
DISSOLVED
P.A 226
RA 226 COUNTING croon
DISSOLVED T!i 220
Th 230 COUNTING
ERROR
.
9
.27
12? hib
t 2*
99
/.S3
COMMENTS:
/itvTHiy /JccfMOA"7*
/tyflRCW 11V
FLUORIDE CALCIUM - TOTAL
MAGNESIUM - TOTAL j
<\ Si
f9
Zt V*
*7^
A 1 0ov0
UCC 003582
ENVIRONMENTAL PROTECTION SURVEY - I HVIKQNMENTA1. IMPACT ANALYSIS
plant
k>hc c,tv__________________
COMPLETED DY ft. fl , M A ft STtA/__________
DATE
T/_-
ro3e--p:
Of 7 O Page 2 of?.
XHJ - V/ATEP QUALITY
DISCHARGE NO._______ --________
NAME________
__________________ ________
* PARAMETER
ALUMINUM - TOTAL ANTIMONY - TOTAL ARSENIC - TOTAL BARIUM - TOTAL BERYLLIUM - TOTAL BORON - TOTAL CADMIUM - TOTAL
PARAMETERS OF INTAKE WATER AND DISCHARGE
i DAILY
UNTREATED * A V E A G E
INTAKE ! DISCHARGE
WATER
1 1
CONCENTEAT ION -
UNITS
nierograms/liter = ppb ,
PARAMETER
&Soo < looo
COLOR
< So < SO
Zo
to
SPECIFIC '
CONDUCTANCE ( mlios at 25 C.)
ft/O </6
no
mo ZX10
tzo
TURBIDITY (Jackson units)
FECAL STREPTOCOCCI BACTERIA number/100 mi
<t0
<to
COLIFORM BACTERIA
UNTREATED INTAKE WATER
aWrage
DISCHARGE CONCEN TRATION
UNITS
as specified
oo
S*6
tioo
CHROMIUM - TOTAL COBALT - TOTAL COPPER - TOTAL
</o < lOO
!ZO
<to <J00 < 10
number/100 mi
COLIFORM BACTERIA TOTAL number/100 mi
IRON - TOTAL LEAD - TOTAL MANGANESE - TOTAL MERCURY - TOTAL MOLYBDENUM-TOTAL NICKEL - TOTAL SELENIUM - TOTAL
SILVER r TOTAL
<tOC
< too
<10
< /
< 10
<J
<100
<100
< to < to
< to
<J < too tzoo < to
< 10
FLOW
GPD ( )
MGPD( ) GPM ( )
pH B.tS
Temperature ../WinlerJ (F) _______
Temncrature (Summer) (F)
_
ppb - means Parts Per Billion ppm - means Ports Per Million GPD- meorrs Gallons Per Doy MGPD-meons Million GoTlons Per Doy GPM- means Gallons Per Minute
Bjd
THALLIUM - TOTAL TIN - TOTAL
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PROCESS SURVEY - ENVIRONMENTAL IMPACT ANALYSIS
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UCC 003584
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DATE
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IX - NOISE EMISSIONS
A. Abnormal Noise Emissions (above 85 Decibels, dBA)
Location
Sound Pressure
Source
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(dBA)
At Distance (ft)
Exposure (Hrs/Shift)
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Sound Pressure
Location
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Remarks
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Location Measured
A/oas-
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Sound Pressure (dBA)
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Distance from Plant Boundary
Hrs/day
D. Abnormal Noise Abatement Plans or Protective Measures____________________________
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DAT L:
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Stock T*
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DATE
3fl3
VIII. - LOADING AND PACKAGING
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