HomeMy WebLinkAboutWQ0005479_Final Permit_19911024State of North Carolina
Department of Environment, Health and Natural Resources
Division of Environmental Management
512 North Salisbury Street • Raleigh, North Carolina 27626-0535
James G. Martin, Governor
William W. Cobey, Jr., Secretary
George T. Everett,Ph.D.
Director
October 24, 1991
Mr. Irvin M. Allen
Cleveland County Health Department
315 Grover Street
Shelby, North Carolina 28150
Subject: Permit No, WQ0005479
County of Cleveland
Solid WasWRecycling Site # 5
Subsurface Disposal System
Cleveland County
Dear Mr. Allen:
In accordance with your application received August 9, 1991, we are forwarding herewith
Permit No. WQ0005479, dated October 24, 1991, to County of Cleveland for the construction
and operation of a 100 GPD septic tank nitrification subsurface wastewater disposal system.
This permit shall be effective from the date of issuance until rescinded and shall be subject
to the conditions and limitations as specified therein. Please pay particular attention to the
monitoring requirements in this permit. Failure to establish an adequate system for collecting and
maintaining the required operational information will result in future compliance problems.
If any parts, requirements, or limitations contained in this permit are unacceptable to you,
you have the right to request an adjudicatory hearing upon written request within 30 days
following receipt of this permit. This request must be in the form of a written petition,
conforming to Chapter 150B of North Carolina General Statutes, and filed with the Office of
Administrative Hearings, P.O. Drawer 27447, Raleigh, NC 27611-7447. Unless such demands
are made this permit shall be final and binding.
One set of approved plans and specifications is being forwarded to you. If you need
additional information concerning this matter, please contact Mr. John Seymour at 919/ 733-5083.
cc
Cleveland County Health Dep
Mooresville Regional Office
Groundwater Section
Training and Certification Unit
Mr. Mark Thompson, P.E.
Pollution Prevention Pays
P.O. Box 29535, Raleigh, North Carolina 27626-0535 Telephone 919-733-7015
An Equal Opportunity Affirmative mative Action Employer
NORTH CAROLINA
ENVIRONMENTAL MANAGEMENT COMMISSION
DEPARTMENT OF ENVIRONMENT, HEALTH AND NATURAL RESOURCES
RALEIGH
SUBSURFACE DISPOSAL SYSTEM PERMIT
In accordance with the provisions of Article 21 of Chapter 143, General Statutes of North
Carolina as amended, and other applicable Laws, Rules, and Regulations
PERMISSION IS HEREBY GRANTED TO
County of Cleveland
Cleveland County
FOR THE
construction and operation of a 100 GPD subsurface wastewater disposal system consisting of a
1,000 gallon septic tank, a distribution box, two 50 foot by 3 foot nitrification trenches, and
associated piping, valves and appurtenances to serve Cleveland County manned solid
waste/recycle site # 5 (Lawndale) with no discharge of wastes to the surface waters, pursuant to
the application received August 9, 1991 and in conformity with the project plan, specifications,
and other supporting data subsequently filed and approved by the Department of Environment,
Health and Natural Resources and considered a part of this permit.
This permit shall be effective from the date of issuance until rescinded and shall be subject
to the following specified conditions and limitations:
�14AMM 121.11411161
Upon completion of construction and prior to operation of this permitted facility, a
certification must be received from a professional engineer certifying that the
permitted facility has been installed in accordance with this permit, the approved
plans and specifications. Mail the Certification to the Permits and Engineering
Unit, P.O. Box 29535, Raleigh, NC 27626-0535.
2. The Mooresville Regional Office, phone no. 704/ 663-1699, shall be notified at
least forty-eight (48) hours in advance of backfilling of the installed facilities so
that an in-place inspection can be made. Such notification to the regional supervisor
shall be made during the normal office hours from 8:00 a.m. until 5:00 p.m, on
Monday through Friday, excluding State Holidays.
3. In the event that the facilities fail to perform satisfactorily, including the creation of
nuisance conditions, the Permittee shall take immediate corrective action, including
those as may be required by this Division, such as construction of additional or
replacement wastewater treatment or disposal facilities.
4. The issuance of this permit shall not relieve the Permittee of the responsibility for
damages to surface or groundwaters resulting from the operation of this facility.
5. This permit shall become voidable if the soils fail to adequately absorb the wastes
and may be rescinded unless the facilities are installed, maintained, and operated in
a manner which will protect the assigned water quality standards of the surface
waters and ground waters.
b. Adequate measures shall be taken to divert stormwater from the disposal area and
prevent wastewater runoff from the subsurface disposal field.
7. The sludge generated from these treatment facilities must be disposed of in
accordance with General Statute 143-215.1 and in a manner approved by the North
Carolina Division of Environmental Management.
A usable reserve area shall be maintained for wastewater disposal. The reserve area
shall have the capability of accommodating the average daily flow of the facility
being served without exceeding the loading rates of the reserve area while meeting
all required buffer requirements.
9. Diversion or bypassing of the untreated wastewater from the treatment facilities is
prohibited.
10. The following buffers shall be maintained:
a) 100 feet between disposal area and any public or private water supply including
wells
b) 100 feet between disposal area and "SA and SB" classified surface waters
c) 50 feet between disposal area and any stream, lake, river or natural drainageway
d) 50 feet between disposal area and property lines
e) 10 feet between disposal area and surface water interceptor drains or diversions
(upslope)
f) 25 feet between disposal area and surface water interceptor drains or diversions
(downslope) and groundwater drainage systems.
11. A leakage test shall be performed on the septic tank and dosing tank to insure that
any exfiltration occurs at a rate which does not exceed twenty (20) gallons per
twenty-four (24) hour per 1,000 gallons of tank capacity. The engineer's
certification will serve as proof of compliance with this condition.
II. OPERATION AND MAINTENANCE REQUIREMENTS
1. The facilities shall be properly maintained and operated at all times.
2. Upon classification of the facility by the Certification Commission, the Permittee
shall employ a certified waster treatment plant operator to be in responsible charge
of the wastewater treatment facilities. The operator must hold a certificate of the
type and grade at least equivalent to the classification assigned to the wastewater
treatment facilities by the Certification Commission. Once the facility is classified,
the Permittee must submit a letter to the Certification Commission which designates
the operator in responsible charge within thirty days after the wastewater treatment
facilities are 50% complete.
3. The application rates to the disposal field shall not exceed 0.4 Gallons/ day/ square
foot.
4. The facilities shall be effectively maintained and operated as a non -discharge system
to prevent the discharge of any wastewater resulting from the operation of this
facility.
F
5. No traffic or equipment shall be allowed on the disposal area except while
installation occurs or while normal maintenance is being performed.
III. MONITORING AND REPORTING REQUIREMENTS
Any monitoring deemed necessary by the Division of Environmental Management
to insure surface and ground water protection will be established and an acceptable
sampling reporting schedule shall be followed.
If Groundwater sampling indicates or predicts problems with the compliance with
Groundwater Standards, this permit will be modified to include additional and/or
more restrictive limitations.
2. A record shall be maintained of all residuals removed from this facility. This record
shall include the name of the hauler, permit authorizing the disposal or a letter from
a municipality agreeing to accept the residuals, date the residuals were hauled, and
volume of residuals removed.
3. Noncompliance Notification:
The Permittee shall report by telephone to the Mooresville Regional Office,
telephone no. 704/ 663-1699, as soon as possible, but in no case more than 24
hours or on the next working day following the occurrence or first knowledge of
the occurrence of any of the following:
a. Any occurrence at the wastewater treatment facility which results in the
treatment of significant amounts of wastes which are abnormal in quantity
or characteristic, such as the dumping of the contents of a basin or tank; the
known passage of a slug of hazardous substance through the facility; or any
other unusual circumstances.
b. Any process unit failure, due to known or unknown reasons, that render the
facility incapable of adequate wastewater treatment such as mechanical or
electrical failures of pumps, aerators, compressors, etc.
C. Any failure of a pumping station, sewer line, or treatment facility resulting
in a by-pass of all or any portion of the influent to such station or facility.
d. Any time that self-monitoring information indicates that the facility has gone
out of compliance with its permit limitations.
Persons reporting such occurrences by telephone shall also file a written report in
letter form within 15 days following first knowledge of the occurrence. This report
must outline the actions taken or proposed to be taken to ensure that the problem
does not recur.
IV. (iROUNDWATER REQUIREMENTS
Any groundwater quality monitoring as deemed necessary by the Division of
Environmental Management shall be provided.
3
V. INSPECTIONS
1. Adequate inspection, maintenance, and cleaning shall be provided by the Permittee
to insure proper operation of the subject facilities.
2. The Permittee or his designee shall inspect the wastewater treatment and disposal
facilities to prevent malfunctions and deterioration, operator errors and discharges
which may cause or lead to the release of wastes to the environment, a threat to
human health, or a nuisance. The Permittee shall keep an inspection log or
summary including at least the date and time of inspection, observations made, and
any maintenance, repairs, or corrective actions taken by the Permittee. This log of
inspections shall be maintained by the Permittee for a period of three years from the
date of the inspection and shall be made available upon request to the Division of
Environmental Management or other permitting authority.
3. Any duly authorized officer, employee, or representative of the Division of
Environmental Management may, upon presentation of credentials, enter and
inspect any property, premises or place on or related to the disposal site and facility
at any reasonable time for the purpose of determining compliance with this permit;
may inspect or copy any records that must be kept under the terms and conditions
of this permit; or may obtain samples of groundwater, surface water, or leachate.
V1. GENERAL CONDITIONS
1. This permit shall become voidable unless the facilities are constructed in accordance
with the conditions of this permit, the approved plans, specifications and other
supporting data.
2. This permit is effective only with respect to the nature and volume of wastes
described in the application and other supporting data.
3. This permit is not transferable. In the event there is desire for the facilities to
change ownership, or there is a name change of the Permittee, a formal permit
request must be submitted to the Division of Environmental Management
accompanied by an application fee, documentation from the parties involved, and
other supporting materials as may be appropriate. The approval of this request will
be considered on its merits and may or may not be approved.
4. Prior to any transfer of this land, a notice shall be given to the new owner that gives
full details of the materials applied or incorporated at this site.
5. A set of approved plans and specifications for the subject project must be retained
by the applicant for the life of the project.
6. The annual administering and compliance fee must be paid by the Permittee within
thirty (30) days after being billed by the Division. Failure to pay the fee
accordingly may cause the Division to initiate. action to revoke this permit as
specified by 15 NCAC 2H.0205 (c)(4).
7. Failure to abide by the conditions and limitations contained in this permit may
subject the Permittee to an enforcement action by the Division of Environmental
Management in accordance with North Carolina General Statute 143-215.6.
8. The subject wastewater treatment and disposal facilities shall be connected to an
operational publicly owned wastewater collection system within 180 days of its
availability to the subject facilities, if the subject wastewater treatment or disposal
facilities are in noncompliance with the terms and conditions of this non -discharge
permit or the governing statutes or regulations.
Prior to the initiation of these connection activities, appropriate approval must be
received from this Division.
9. The issuance of this permit does not preclude the Permittee from complying with
any and all statutes, rules, regulations, or ordinances which may be imposed by
other government agencies (local, state, and federal) which have jurisdiction.
10. The Permittee, at least six (6) months prior to the expiration of this permit, shall
request its extension. Upon receipt of the request, the Commission will review the
adequacy of the facilities described therein, and if warranted, will extend the permit
for such period of time and under such conditions and limitations as it may deem
appropriate.
Permit issued this the 24th day of October, 1991
CAROLINA ENVIRONMENTAL MANAGEMENT COMMISSION
George T. Everett, e4o�Me
Division of Environ ntal ag ent
By Authority of the En t Management Commission
5
Permit No. WQ0005479
October 24, 1991
Engineer's Certification
I, , as a duly registered Professional Engineer in the State of North
Carolina, having been authorized to observe (periodically, weekly, full time) the construction of
the
project, for the
Project Name Location
Permittee hereby state that, to the best of my abilities, due care and diligence was used in the
observation of the construction such that the construction was observed to be built within
substantial compliance and intent of the approved plans and specifications.
Signature Registration No.
Date
9
r
-S
N
RATING SCALE FOR CLASSIFICATION OF FACILITIES
Name of Plan#: C So/ro/ k/ s Lgwladolt)
Owner or Contact Berson:.
Mailing Address: , IrV d _ �YGI�I � 3!S Gree. S
-- ShsLky_rW C.-- ----------------- ----------------
County:
-------------------------------
County: c 4,W Telephone:
NPDES Permit No. NC00 Nondisc. Per. No. �%aoo SrrTy
IssueDate:_y , zy, /99/ Expiration Date: -aG.,. Iq&
Existing Facility New Facility r/
Rated By: 3-,--Sgzh,.sHr- Date: Sr" 71 as?,
Reviewed (Train. & Cert.) Reg. Office_
Reviewed (Train. & Cert.) Central Office
LI
Grade
ITEM ` POINTS ITEM
(1) Industrial Pretreatment Units and/or
Septic Tank (see definition no. 43) ..............
industrial Pretreatment Program
(b)
(see definition No. 33)
4
(2) D5_�I� NN FLOW OF PLANT IN GPD
Primary Clarifiers ............................
(nal applicable to non -contaminated cooling
(d)
waters, sludge handling facilities for water
purification plants, totally closed cycle
Non-toxic Materials (sludge handling facilities
systems (def. No. 11), and facilities
consisting only of Item (4) (d) or Items (4) (d)
mid (11) (d))
stone, and other mining operations except
0 - 20,000..........................
Q
20,001 50,000 ..........................
2
50,001 -- 100,000 ..........................
3
100,001 -- 250.000 ..........................
4
. 250,001 - 500,000 ..........................
5
500,001 --1,000.000..........................
8
1,000,001 -- 2,000,000 ..................... . ..
10
2,000,001 (and up) - rale 1 point additional for each
20
200,000 gpd capacity up to a
Diffused Air System ...........
maximum of 30
Design Flow (gpd) :
(3) PRELIMINARY UMTS (see definition no. 32)
(a) Bar Screens ................................ 1
or
(b) Mechanical Screens, Static Screens or
Comminuting Devices ......... . ... 2
(c) Grit Removal ............................... 1
or
(d) Mechanical or Aerated Grit Removal ........... 2
(e) Flow Measuring Device ....................... 1
or
(1) Instrumented Flow Measurement .............. 2
(g) Preaeralion ............................. . .. 2
Influent Flow Equalization ................... 2
�t) Grease or Oil Separalors - Gravity .......... 2
Mechanical.......... 3
Dissolved Air f=lotation. 8
(I) Prechlorination .............................. 5
(4) PRIMARY `fREATMENT UNITS
POINTS
(a)
Septic Tank (see definition no. 43) ..............
(b)
Imhoff Tank ..................................
5
(c)
Primary Clarifiers ............................
5
(d)
Settling Ponds or Settling Tanks for Inorganic
Non-toxic Materials (sludge handling facilities
for water purification plants, sand, gravel,
stone, and other mining operations except
recreational activities such as gem or gold
mining) ......................................
2
(5) SECONDARY
TREATMENT UNITS
(a)
Carbonaceous Stage
(i)Aeration - High Purity Oxygen System .... }
20
Diffused Air System ...........
10
Mechanical Air System (fixed,
floating or rotor) ..............
8
Separate Sludge Reaeration .....
3
(ii) Trickling Filter
}high Rale ...................
7
Standard Rale ...............
5
Packed Tower ...............
5
(iii) Biological Aerated Filter or Aerated
Biological Filler ......................
10
(iv) Aerated Lagoons ..................... .
10
(v) Rotating Biological Contactors ..........
10
(vi) Sand Filters -
intermittent biological .. ..
2
recirculating biological .. . . .
3
(vii) Stabilization Lagoons .............. . ....
5
(viii)Clarifier .................. . ...........
5
(ix) Single stage system for combined
carbonaceous removal of BOD and
nitrogenous removal by nitrification
(see del. No. 12) (Points for this item
have to be in addition to ilems (5) (a)
(i) through (5) (a) (viii) .................
B
(x) Nutrient additions to enhance BOD
removal ...............................
S
(xi) Biological Culture (-Super Bugs') addition
to enhance organic compound removal . - ...
5
Nitrogenous Stage
5
(i)
Aeration - Nigh Purity Oxygen System ...
20
3
Diffused Air System .. - - . - - ....
10
with carbon regeneration _ _ _ _ _ _ .... _ .... _ ...
Mechanical Air System (fixed,
Air Stripping .............................
5
floating, or rotor) - - - - -- - -- - --
8
)Electrodialysis ........ .. .... . ...............
Separate Sludge Reaeration .....
3
,ii)
-trickling Filter -
5
Land Application of Treated E=ffluent
HighRate..............
7
2
Standard Rate . ......... . . .
5
operations)
Packed Tower ............
5
(iii)
Biological Aerated Filter or Aerated
10
(ii) by high rate infiltration on non -agriculturally
Biological Filter .... . . . ... . . . . . . . .. - . - ...
10
(iv)
Rotating Biological Conlaclors . - ...... - ...
10
(v)
Sand Filter -
plants consisting of septic lank and nitrifica-
intermittent biological ........
2
4
recirculating biological .. - .....
3
(vi)
Clarifier ................................
5
IARY OR ADVANCED TREATMENT UNIT
Activated Carbons Beds -
without carbon regeneration _ .. _ _ ........ - ....
5
with carbon regeneration ...... . .............
15
?owdered or Granular Activated Carbon Feed -
3
without carbon regeneration _ ..... • • • .... _ ...
5
with carbon regeneration _ _ _ _ _ _ .... _ .... _ ...
15
Air Stripping .............................
5
Denitrification Process (separate process) . . _ . .
10
)Electrodialysis ........ .. .... . ...............
5
Foam Separation ..... . .... . ........ . . . . _ - _ _
5
Eon Exchange ............................ ....
5
Land Application of Treated E=ffluent
J3
(see definition no. 22b) (not applicable for
2
sande gravel, stone and other similar mining
(b) Dechlorination ....... . . . . .............
operations)
(c) Ozone ..........................
,(i) on agriculturally managed sites (See dei.
(d) Radiation .... . . ......... . ..........
No.4)...................................
10
(ii) by high rate infiltration on non -agriculturally
(not applicable to chemical additions rated as item
managed sites (includes rotary distributors
(3) 6). (5) (a) (A). (6) (a), (6) (b). (7) (b), (7) (e),
and similar fixed nozzle systems) ...........
4
(iii) by subsurface disposal (includes low pressure
pipe systems and gravity systems except at
plants consisting of septic lank and nitrifica-
tion lines only) .............................
4
Microscreens..................................
5
Phosphorus Removal by Biological Processes
(See def. No. 26) .............................
20
Polishing Ponds - without aeration .......
2
With aeration ........ _ .
5
Post Aeration - cascade ... _ .. _ . - _ . - ..
0
diffused or mechanical . - .
5
Reverse Osmosis ...............................
5
Sand or Mixed -Media Fillers - low rate ...........
2
high rate ..........
5
Treatment processes for removal of metal or
cyanide ....................................
15
Treatment processes for removal of toxic
materials other than metal or cyanide .........
15
DGE TREATMENT
Sludge Digestion Tank - Heated ...............
10
Aerobic _ ..... - ........
5
Unheated ...... .......
3
Sludge Stabilization (chemical or thermal) . .. . - . .
5
Sludge Drying Beds - Gravity .. - . - ... " ........
2
Vacuum Assisted .......
5
Sludge Elutriation ....... . . . . .. . .... . .. . .......
s
Sludge Conditioner (chemical or thermal) - ...... -
5
Sludge Thickener (gravity) - . _ - . " . . ...... . ..... . .
5
Dissolved Air Flotation Unit
(c) Landfilled (burial) .............................
,not applicable to a unit rales as (3) (i) . " . , _ .. _ _
J3
Sludge Gas Utilization (including gas storage) . - . .
2
(ij Sludge Holding Tank - Aerated ................ 5
Non-aerated . - ....... - .. 2
(j) Sludge Incinerator - (not including activated
carbon regeneration) - . - .. 1
(k) Vacuum Filter, Centrifuge or Filter Press or other
similar dewatering devices . . . . ............ . . . . 10
(8) SLUDGE DISPOSAL (including incinerated ash)
5
(a)Lagoons........................
5
(b) Land Application (surface and subsurface)
(see definition 22a)
5
-where the facility holds the fand app. permit - .
1 0
-by contracting to a land application operator who
Holding Ponds, Holding Tanks or Settling Ponds
holds the land application permit ...... . .........
2
-land application of sludge by a contractor who does
not hold the permit for the wastewater treatment
facility where the sludge is generated -
10
(c) Landfilled (burial) .............................
5
(9) DISINFECTION
(a) Chlorination ............ _ • . . . ..... . .. . ....
5
(b) Dechlorination ....... . . . . .............
5
(c) Ozone ..........................
5
(d) Radiation .... . . ......... . ..........
5
(10) CHEMICAL ADDITION SYSTEM (S) (See definition No. 9)
(f)
(not applicable to chemical additions rated as item
(3) 6). (5) (a) (A). (6) (a), (6) (b). (7) (b), (7) (e),
(9) (a), (9) (b), or (9) (c) 5 points each: List:
TOTAL POINTS 3
��ff ..[[ii CLASSIFICATION
rL' C�t{SSr(�l CG�'fvel
Class I ------• .................................................... 5 - 25 Points
Class 11 ............... ............................. ............ 26- 50 Points
Class III ..............................................•---..- - 51- 65 Points
Class IV ........................................................ 66- Up Points
Facilities having a facing of one through four points, inclusive,
do not require a certified operator. Classification of all other
facilities requires a comparable grade operator in responsible
charge.
Facilites having an activated sludge process will be assigned
a minimum classification of Class 11.
Facilifies having treatment processes for the removal of metal
or cyanide will be assigned a minimum classifica[ion of Class tl
Facilities having treatment processes for the biological removal
of phosphorus will be assigned a minimum classification of Class`
Ill.
Rf FI ITI k
(I)Act;.aled Gafbon Bids. A Physk Auchemica] melhed for reducing aeluble organic mltehaf Iron
wa[lswale� .env. nt: 1h'.' --)---type beds vs.d in Ih;z method will have a Itow rel, varying ream Iwo
to "Phi Vast— par minus• per aqua • loot And MAY tae silher vpnew or dewnitow c.rbon bads, Carbon
msy or r be 1e9en-rated on she wast.wal•r trutm.nl plant it..
(21Aer= A basin In which oro fa6ds are m inls;n•d in aysp.ns and br which b;arog;c.l
eR;Ja li n,c malls, is ruduc.d Ilsrouph arlific;Ally ACs -Leased Iran. (.r of -TV— on a It.-.
Ihferrgh
11)A.r2lien, n precsu of bfie ging about ;nrvmal. conlacl belw. air er high purilr osyoon ;n a Gq,Bd
by spraying, agnztion diHvuon••
(a)Agr;cuhu AIy manaood ska. Any silo on which A crop h produced, m-nxgad, and hvvuvod (Crop
inesud•x presses, gesso-, Noes, •Ic):
(51A;r Stripping. A peee.ss by which the ammonium ion is rust eonvrl+d to dissolved ammonia (pill
adivstmanl) with ahs ammonia shin frlus.d to the alracphv■ by physical means- or oft— similar
Processes which rim— palrofoum products such as bonen. lolu.n•, and yyfone.
(6)CAtboet Re9ensfl6on" The regenanlion or aahlusloe carbon by the use of a Ivinlca to provide
esuamely high temperalur•s which volaldite and oxidize the absorbed impurities:
f1)Carbonac.ou. 51.14, A .1.94 of xastewaset 11-11M-nt designed la ach;a v. yoc onda rye all] ... I
;;M41.
)a?Conuivgs, A awcfonical dovico in which c eu,4-p-1 lefco is Used ta'.epaialo solids iron liquids
andtor to sapAral• Ygvids of different den,Wo,.,
(9)Chenticil Add;6on Systems • Th• addition of chemic:] (s) to w311ewalar at an apptical;on point for
purposes of ;mpfevirsg solids removal, par adjustment, alkalinity control, ete,: the capability to
espeliunent with dirfe,.nt ehanucals and ddl•lanl apPGcaliun points le achieve a specific rosWl win be
canard "ed one sys.om: she capability to add chemical (a) to dual units watt be salad as ono systum;
capsWity to add A-h—teal At dirr.rencs Application points lot diil•renl pufpoaas ,All result in the
sym.ms being 111. a. separate system,
(10)Ch.mie.l Sludge Gonditionirsp_ The addidon of a eher..;ezl eampaund such as 11n•, ferric chloride. or
- pelyms( to wet sludge to eealasc. the mass prior to its apptca[ion to a dowalerang device:
[I%jClos.d Cycle Systems_ Ut• of holding ponds or hold'utq [asks fa eonliinmenl of wastewater
conlaising iraorgar,ie. Pon•loxie materials from sand, gravel, crushed alone ec other s;miar operations,
from which than is nor discharge to the sufracs waters; such systems shall calif, a maximum of two
points s.9aedless of pumping lac;F({.a u any other Sppun.nanees-
(12)Gomb;nad RIfwvat of Carbonaceous SOD and lrtrogancus Removal by Ndcificaaon • A &!note snga
system'deugnad• to achieve-advanead- permit slauset limits on BOo and ammonia nitrogen %;thin
the same Wacipical -actor.
[t3)01•chbrinal;on,
The panus or complet. ,duction o[ fisidual chlorine in a fquid by any chomical
or physical pr«ass;
(lt)Der1;11:tclfen Process, The cenverslon of ltivzt. •nitrogen 10 r;l(og.n gas;
(15)Eteelroda.lysts, Procoss It
r remoA" Ionized alts Ilam water tiveugh the use of ion•saloctivc
!on-each-nqe membrane:• _
{]6)Fi1.r ri.sx- A process operated mechatic.tly lot pzrtisly d.waler-u,g sludge;
(s7)Foam Saparadon: The plamad bathing of w-xlawtiet w wast4w2tar effluent as a maans of
remarrirsq .xnss;vr amounts of dol.io.rsl MA14421S through the Introduction of air In the term of rine
laubble -, rya ca Rod foam rfaetion.tion:
06JGrk R.mevAL The pfoeess of remoarGnq 914 and elhat heavy min.far mailer from waslowalat•
(19)tmhogf Tank, A deep Iwo story wlslew-ler link consisting of an upper a.d mentztion chamber and
I bwof sir' - dgest;oo chamber:
(20)Eat, Fsew Measurement, A device which �c-l.s andlor rseo(ds este of flow;
(21)Ion A chslnical pfoc•ss in which tens Isom two ddf•tant molecules orf. rxchang. d-
(221[•an ,aw (1) Sludge Olsposak A Fetal sludge disposal m.lhod by which sludge may be
1pprwd to rand upset by spraying on tit. surface or by subsurface fnist0on (Ls, ehis.l plow): [not
apPGtabta ler typos at sludge described in (11) of INS Ru(el: (b)Treated Efpvenl, Th• process of
1 ng Nested waslewalor onto a 'fix methods
find ax olhar of apptcation of waslewa[ar oma a
is nd area as A means of rrnaf dspasal And,/., Nesun.n[;
(23JLktosCs--fL A law xp..d, eonlmuovsly back -washed, totaling drum filler apafalinq under
gfavky condi"As as a Pe5shln9 method lemoving suspended solids from eNhsent-
WINitr;I"C-Aan Pleeas/. The biochemical 40ft-fuel of unoxidiz.d Ishaogen (ammonia and olganic
nev994n) la oludaed (atrogen (lrsualy rdU lij.
r25)rrilrog-mut, Stasi, A Separate stage of wall .wahr uwlmenl designed for the spedrK purpose of
tonvetdng amr"& duegen to rutrata nruogen;
(26)Plwsphlle Removal Wologic2t The removal of phosphorus Gam wastewater by An ox;Uanoxic
process dasyned to tnhante luxury uptake of phosphorus by the. rsalcreafganlsms;
(27)Porish)np Pond, A holding pond folow,ng sacondary, treatment with stdric;•nl detention to allow for :
the 96TIQ q el rvwiy susponded aoters: t
(28)Post Aetadon. Aeration following eonvenfionat secondary tr.alm.nl unit to Inc,easa altluen[ P.O.
er lot any ogler pwpe. o;
1291pos1 Aeragm (CA reldaJ A po6shtng method by which di[tah.d oxygen is added to the elft o 1 by
a nocunoch"eal' pcavky means of !towing down a series of slops u we;n; The $ow occurring across
U'
steps ar we" encu'- In a fairly thin lay.f and Use epor-llon a1 the ea[ead• iagv;r.s no operator
adi"u—ca, Vous- 2-10 points are assigned oven though Wis Is an ass.ntiat slop to me. ring the @mils of
the dischsege permit;
(30)Powdered or Gfanl,laf AtUvA%d Carbon F..e, A bicap iyslcal carbon process %hit utilizes b;oto9tcal
ac livill' and 0193nic absorption by using pawdn.d or granufir aclivated carbon- Virgin and/or
11glener11*4 nfban is laid denNoflad Into the ryn.m;
(10Pn Itflam A lank eonsuue.ed to provide Aualion price to primary ua At,nanl:
(32)prarrm'-1r1 units, Unit operations ;n the lrallmenl process, such As acrs.runq and comrrvnudon.
Ih11 pcepan sit1 rgvor lot subsequent major op.ra@ons;
l37)Indurula[ Pct u.avn. nt: Writ--Ifeatmenl unit, Industrial. The wnditioring of a waits al its
source balw• discharge. to 1-1110y- or It rnulfalil, substances Injurious 10 sewers and Iramm•nl
Peet@a or $0 affect A penial redueuan in load on A treatment process which Is operated by the sem,
pov, ening body at tti. waste wafer treat_.^, pian being ;11.d• (b)Pr•-lie 11m•nl Plogram, Indus Uial -
n"'s[ be a Stale or EPA required peogram to r.c." po]nl, on lh••taeing sheet:
{]J}Primary C]a fit;.,. The rHtl &•ItUrig links through which waslawater Is passed in - Uaalm.nl
i olidx: orks for IM purpaa. el removing a.ltluble and sysp,nd.d solids and Boo which is 1111 sled with the
115)Pvmps" AC inllaenl" •Itlwnl, and in -punt pumps-
P'fF4dnti-n_ Disinl,cl;an and/or sleriitll;on piocest li,Qlinq dsvicat emitting uhnviatot o, gamma
r
13719e,erse Osmosis. A leeatm•nl process in xNch A h.avy contaminated l;quid l(pr.ssvris.d
through a m4_-4 lol"rig neatly Pur• liquid tragi from ayspsnded sol;dr
P SIRalalin si conuciofs• A rued Din?a Ic AI
Ihrovgh tA. C growth grocers in which wits—tor It—p9}5 and 1 °ries of pan;&Uy avDmeag oil c'vcvlar 1.c...cea
a.r lie rola t. e"
munant Biological- F"ll"ion at eft]uent fohow;ng septic ranks ]age.— or
tom. all., „v„r... nl prasest m whish funher biod.eomposil;on is .ap.et.d to predue. d.sind
.illy. nla; Nyd,a c foaling rales en these l;[lalt ar. compv,.d tri 9Pdrac and hav, a a.&uflinq tow
gpM.l (las, than an.): (b}Re[ircvlAl;n9 b;etag;_al .lh,, t of 'And filler as doll
the added ram yp. nod in (a) with
upaD;Gty so ngcle 4:111-1 back through Ih. send fill.,;
(eo)Sand or "d—media $7;1%1(1. A poC.hing pro:,ra by which effluent 11m;ls if, aeh;_d Ihr gh A
farther fedvc[ion el aysp.nd.e aotld-;(allow Est.cavil h d,auli-P S
oleo :n eh. on � 4 Y. Y r oAdsd tiller with lording
n lea in 3M live+ la shr.a gpmesf aan9.;gb)h;gh lay. - a pre&, hyd-ulicany load,d lilt— w;ah loadinq
gpavrf rang.; At any sal., the loading las. wilt .ore. oil the.. 9pnv&I:
(rl)Secondiry Ctari Cart_ A link which loftow, the biolog;c Af unit or a vestment latent and which has
.he P -p... or r.,noj"'Fudge astccia lid A,h the 41olag;csl Vratm-m units;
(42)5•p2nl• Slvdg• Res.radon. A pan of the cannel slab;Grlsion proe•st whore the aerivatod I.dg.
is If 0-11ed to a tank and -•ral,tl Woe, f—„.Ing it la the basin;
(cl)SepSc Tank. A .in9:e.nary . iISI-2 lank In which -ental ship- Is in ce nla c[ will, the wast.wv.r
hawing through In. tAnk: .halt no, b• appil ably lar .optic tank syuemc sowing .;.pro lamily
I..ide,c.[ hav[nq a eapadty or 2C<4 grub.+ ar let. which di.chugo to s nilair.At;— ri.td:
(44)51,49• Op•alion. 71,. pro,.., by whkh oro Attic or ralalP, -0-f and tivdge 4 q-slhed, Igv.6od_
minaratiz.d or con $1.d into m,ae t[abl. ofpank matter through [he %c[ivity of living organisms,
Which includes --riled 4,AeG q sant,•
1451Sludga Dry;ng Dada. An oral C.e;A;irg natural w artiriclil layers of parous material, upon which
dipesl.d sewage sludge is dried by eninagr and waposal;oA;
(46)Slud9• Ehaltialion. A Pf«arc of uvdge conditioning in which certain cons,ituems are !.moved by
s ucc.ssivs washings with fresh wale, or plaru .)Hoon[:
071Slud0e GAL Utikaaeicr- The lancets el wing sew.pe pis lot the purpose of hailing buildings,
driving engines, arc.;
(4015sudge Holdlnq lank (Aaralod zeal Hona•aated). A urd4Ui� t,#, -for small wa&l.wAler Voatmonl
planta not coots kung a d eraaf 1. wr�ch dvtlge -y tau keel he:h. and 4 rp , Mint wilt,Jr:,wn pi;o, to
a :(T.V method (i..- shrC,s drying Ind): Ins may be done by adding a emelt amount of air simply to
keep the sludge fresh, bs: not nocauadi, An amount that would be requvod la achiw. atabir_alian of
organic miller. A nonasra:ad tank wuvd simply be used to docanl sludge lariat to dowel -1119 and wou;d
simply be used to docanl 11.119e prior la if—Wing and would not Allow long ia-id. (several days o1
detention) without rosull;ry odor proYwmt•
(z9)Sludge Incinafatoet.' A !Waco eol;gned to bwn sludge and to tamava -e moisture and combustibles
MAW411 and reduce the IW,). Ie a mole ash:
(50)Slvd9e Slabi;zation (Chemical or Tharmaq. A protest W make treated sludge less odorous and
puuescrible, and to educe the P1Vogene organism content; This may be done by pli adivttmenl
chlorine dosing, or by heal tree:men[;
(51)Sludoe Thickener. A type of ..eLmenszlien lards In which the sludge Is permitted to settle and
tldck.n through agiution and prl rdy:
02)Slabi6z19en t -9--M A-lyp. of e.idation lagoon In which biological oxld-[;an el organic matter is
tltacled by naturaf lrantlar al oxygen W lite water lrom iU (nal 1poSth;nq pond);
(51)S1and•By Power Supply, on sill of portable elocL(kal generating equipment:
(SiJ Static Screens, A s(ationaq IOlen designed to umovs solids Including non•b;odagradab[a
parliculat. (Iloatable solids, svapended solids and BOD reduction) from munic;pat and industrial
waslswilaftreatment systems;
[$5)Tetllasy Treslmafk4 A stage of troalmant following socendary which is primarily lot the pulpose
of orliveni poilhy'ag; A LeC`erag 11900, of sand or coal (ale( m,;ghl be emptayid (of (his purpos.-
(S6)Theimal Pclulio, Con.-ol Devks. A devics providng for the transfer of heat from a quid Ilow;ng
in tube, to another fluid wlside the lubes, u vita versa; ”, other means of regWal;ng
liquid lamp.ralufas:
(57)Thumal Sludge Condis;ener. A ccneilioting p(ocoxr by which haat It added for a protracted poriod
of time to Insptw. the dowalsfablay of sludge by the s01u1IIEW sp and hyd.auGzing of the smaller and
more hlghfy hydrated study. parlicler
(5a)Tosic Materials, Those wssl.a ar combinAl;enl el -MUS lncludtng thous..Causing agents which
after discharge and upon eapasuf., ingestion, inhalation er assimilation into any organism a;1hor
dveclfy from the emriecamerd or lndvictly by ingestion through good chains, will cause death, disoaso
behavioral abnerm2ltiex, cancer, gon[tic mutations, physiological malfunctions (inctwing m-Ifuncl;o ,
)n ispioduc[ion) or physical detWrs%4on5, in such organisms or their ofispf;ng; Toxic mzlerials
inalvde, by way ihustfalion and not fiositalion; (sad, cadmium, chromium, mercury, vanadium, ,
atsank, lint, 991210 rbrwaJorebonzaei. (OHCS polychkrinalad Wph.nyls (PCBs) and dkhlorod;pha^yl
lrichfwaa[hsna (DOT): and any other Materials that have or may Mr.14.1 be determined to have logic
proper[hs..
4591Ts;ek6ng Wlar, A biological tre.;Mem ten;[ consisting of material such as broken stony or sock
over which wastawaler is dilWbu[ed: A high fate lfkkr'uV fillet is one which Is opef-tea"•at be:.votn
10 and 30 mgd par acts. A law tate ukkrmq lillar is one which it designed to opofole al ono otc four
mgd pat act&;
(60)71itktinp Filer (Packed Tower). A plug flow type of operation in which wastewaterflaws down
h
through succ•ise (ayets at mall or 6ltrste matallai; Ofgank material is removed continua::y by
active t>tolopkal used growth is each sxcosslvt laye(. This m•lhod mly preduco "sacondaifl, c�atity
.trlverll, or may be adapl.d to product A ruined Hllueni;
flil)Yleuvm Fifties Caraldruges- or F214r Aossas, Devices which are designed to rameve eatoas
water from .fisher dgealad or und;gesI#d sludge prior to disposal or further treatment.
5
5
5
(11) MISCELLANEOUS
UNiTS
(a)
Holding Ponds, Holding Tanks or Settling Ponds
for Organic or Toxic Materials including wastes
from mining operations containing nitrogen and/or
Phosphorous compounds in amounts significantly
greater than is common for domestic wastewater .......... 4
(b)
Effluent Flow Equalization (not applicable to storage .
basins which are inherent in land application systems). 2
(c)
Stage Discharge (not applicable to storage basins
inherent in land application systems ....................................... 5
(d)
Pumps ..... ................................................................... ....---....-.- 3
(e)
Stand -By Power Supply ..................... ............................................ 3
(f)
Thermal Pollution Control Device ............................................. 3
TOTAL POINTS 3
��ff ..[[ii CLASSIFICATION
rL' C�t{SSr(�l CG�'fvel
Class I ------• .................................................... 5 - 25 Points
Class 11 ............... ............................. ............ 26- 50 Points
Class III ..............................................•---..- - 51- 65 Points
Class IV ........................................................ 66- Up Points
Facilities having a facing of one through four points, inclusive,
do not require a certified operator. Classification of all other
facilities requires a comparable grade operator in responsible
charge.
Facilites having an activated sludge process will be assigned
a minimum classification of Class 11.
Facilifies having treatment processes for the removal of metal
or cyanide will be assigned a minimum classifica[ion of Class tl
Facilities having treatment processes for the biological removal
of phosphorus will be assigned a minimum classification of Class`
Ill.
Rf FI ITI k
(I)Act;.aled Gafbon Bids. A Physk Auchemica] melhed for reducing aeluble organic mltehaf Iron
wa[lswale� .env. nt: 1h'.' --)---type beds vs.d in Ih;z method will have a Itow rel, varying ream Iwo
to "Phi Vast— par minus• per aqua • loot And MAY tae silher vpnew or dewnitow c.rbon bads, Carbon
msy or r be 1e9en-rated on she wast.wal•r trutm.nl plant it..
(21Aer= A basin In which oro fa6ds are m inls;n•d in aysp.ns and br which b;arog;c.l
eR;Ja li n,c malls, is ruduc.d Ilsrouph arlific;Ally ACs -Leased Iran. (.r of -TV— on a It.-.
Ihferrgh
11)A.r2lien, n precsu of bfie ging about ;nrvmal. conlacl belw. air er high purilr osyoon ;n a Gq,Bd
by spraying, agnztion diHvuon••
(a)Agr;cuhu AIy manaood ska. Any silo on which A crop h produced, m-nxgad, and hvvuvod (Crop
inesud•x presses, gesso-, Noes, •Ic):
(51A;r Stripping. A peee.ss by which the ammonium ion is rust eonvrl+d to dissolved ammonia (pill
adivstmanl) with ahs ammonia shin frlus.d to the alracphv■ by physical means- or oft— similar
Processes which rim— palrofoum products such as bonen. lolu.n•, and yyfone.
(6)CAtboet Re9ensfl6on" The regenanlion or aahlusloe carbon by the use of a Ivinlca to provide
esuamely high temperalur•s which volaldite and oxidize the absorbed impurities:
f1)Carbonac.ou. 51.14, A .1.94 of xastewaset 11-11M-nt designed la ach;a v. yoc onda rye all] ... I
;;M41.
)a?Conuivgs, A awcfonical dovico in which c eu,4-p-1 lefco is Used ta'.epaialo solids iron liquids
andtor to sapAral• Ygvids of different den,Wo,.,
(9)Chenticil Add;6on Systems • Th• addition of chemic:] (s) to w311ewalar at an apptical;on point for
purposes of ;mpfevirsg solids removal, par adjustment, alkalinity control, ete,: the capability to
espeliunent with dirfe,.nt ehanucals and ddl•lanl apPGcaliun points le achieve a specific rosWl win be
canard "ed one sys.om: she capability to add chemical (a) to dual units watt be salad as ono systum;
capsWity to add A-h—teal At dirr.rencs Application points lot diil•renl pufpoaas ,All result in the
sym.ms being 111. a. separate system,
(10)Ch.mie.l Sludge Gonditionirsp_ The addidon of a eher..;ezl eampaund such as 11n•, ferric chloride. or
- pelyms( to wet sludge to eealasc. the mass prior to its apptca[ion to a dowalerang device:
[I%jClos.d Cycle Systems_ Ut• of holding ponds or hold'utq [asks fa eonliinmenl of wastewater
conlaising iraorgar,ie. Pon•loxie materials from sand, gravel, crushed alone ec other s;miar operations,
from which than is nor discharge to the sufracs waters; such systems shall calif, a maximum of two
points s.9aedless of pumping lac;F({.a u any other Sppun.nanees-
(12)Gomb;nad RIfwvat of Carbonaceous SOD and lrtrogancus Removal by Ndcificaaon • A &!note snga
system'deugnad• to achieve-advanead- permit slauset limits on BOo and ammonia nitrogen %;thin
the same Wacipical -actor.
[t3)01•chbrinal;on,
The panus or complet. ,duction o[ fisidual chlorine in a fquid by any chomical
or physical pr«ass;
(lt)Der1;11:tclfen Process, The cenverslon of ltivzt. •nitrogen 10 r;l(og.n gas;
(15)Eteelroda.lysts, Procoss It
r remoA" Ionized alts Ilam water tiveugh the use of ion•saloctivc
!on-each-nqe membrane:• _
{]6)Fi1.r ri.sx- A process operated mechatic.tly lot pzrtisly d.waler-u,g sludge;
(s7)Foam Saparadon: The plamad bathing of w-xlawtiet w wast4w2tar effluent as a maans of
remarrirsq .xnss;vr amounts of dol.io.rsl MA14421S through the Introduction of air In the term of rine
laubble -, rya ca Rod foam rfaetion.tion:
06JGrk R.mevAL The pfoeess of remoarGnq 914 and elhat heavy min.far mailer from waslowalat•
(19)tmhogf Tank, A deep Iwo story wlslew-ler link consisting of an upper a.d mentztion chamber and
I bwof sir' - dgest;oo chamber:
(20)Eat, Fsew Measurement, A device which �c-l.s andlor rseo(ds este of flow;
(21)Ion A chslnical pfoc•ss in which tens Isom two ddf•tant molecules orf. rxchang. d-
(221[•an ,aw (1) Sludge Olsposak A Fetal sludge disposal m.lhod by which sludge may be
1pprwd to rand upset by spraying on tit. surface or by subsurface fnist0on (Ls, ehis.l plow): [not
apPGtabta ler typos at sludge described in (11) of INS Ru(el: (b)Treated Efpvenl, Th• process of
1 ng Nested waslewalor onto a 'fix methods
find ax olhar of apptcation of waslewa[ar oma a
is nd area as A means of rrnaf dspasal And,/., Nesun.n[;
(23JLktosCs--fL A law xp..d, eonlmuovsly back -washed, totaling drum filler apafalinq under
gfavky condi"As as a Pe5shln9 method lemoving suspended solids from eNhsent-
WINitr;I"C-Aan Pleeas/. The biochemical 40ft-fuel of unoxidiz.d Ishaogen (ammonia and olganic
nev994n) la oludaed (atrogen (lrsualy rdU lij.
r25)rrilrog-mut, Stasi, A Separate stage of wall .wahr uwlmenl designed for the spedrK purpose of
tonvetdng amr"& duegen to rutrata nruogen;
(26)Plwsphlle Removal Wologic2t The removal of phosphorus Gam wastewater by An ox;Uanoxic
process dasyned to tnhante luxury uptake of phosphorus by the. rsalcreafganlsms;
(27)Porish)np Pond, A holding pond folow,ng sacondary, treatment with stdric;•nl detention to allow for :
the 96TIQ q el rvwiy susponded aoters: t
(28)Post Aetadon. Aeration following eonvenfionat secondary tr.alm.nl unit to Inc,easa altluen[ P.O.
er lot any ogler pwpe. o;
1291pos1 Aeragm (CA reldaJ A po6shtng method by which di[tah.d oxygen is added to the elft o 1 by
a nocunoch"eal' pcavky means of !towing down a series of slops u we;n; The $ow occurring across
U'
steps ar we" encu'- In a fairly thin lay.f and Use epor-llon a1 the ea[ead• iagv;r.s no operator
adi"u—ca, Vous- 2-10 points are assigned oven though Wis Is an ass.ntiat slop to me. ring the @mils of
the dischsege permit;
(30)Powdered or Gfanl,laf AtUvA%d Carbon F..e, A bicap iyslcal carbon process %hit utilizes b;oto9tcal
ac livill' and 0193nic absorption by using pawdn.d or granufir aclivated carbon- Virgin and/or
11glener11*4 nfban is laid denNoflad Into the ryn.m;
(10Pn Itflam A lank eonsuue.ed to provide Aualion price to primary ua At,nanl:
(32)prarrm'-1r1 units, Unit operations ;n the lrallmenl process, such As acrs.runq and comrrvnudon.
Ih11 pcepan sit1 rgvor lot subsequent major op.ra@ons;
l37)Indurula[ Pct u.avn. nt: Writ--Ifeatmenl unit, Industrial. The wnditioring of a waits al its
source balw• discharge. to 1-1110y- or It rnulfalil, substances Injurious 10 sewers and Iramm•nl
Peet@a or $0 affect A penial redueuan in load on A treatment process which Is operated by the sem,
pov, ening body at tti. waste wafer treat_.^, pian being ;11.d• (b)Pr•-lie 11m•nl Plogram, Indus Uial -
n"'s[ be a Stale or EPA required peogram to r.c." po]nl, on lh••taeing sheet:
{]J}Primary C]a fit;.,. The rHtl &•ItUrig links through which waslawater Is passed in - Uaalm.nl
i olidx: orks for IM purpaa. el removing a.ltluble and sysp,nd.d solids and Boo which is 1111 sled with the
115)Pvmps" AC inllaenl" •Itlwnl, and in -punt pumps-
P'fF4dnti-n_ Disinl,cl;an and/or sleriitll;on piocest li,Qlinq dsvicat emitting uhnviatot o, gamma
r
13719e,erse Osmosis. A leeatm•nl process in xNch A h.avy contaminated l;quid l(pr.ssvris.d
through a m4_-4 lol"rig neatly Pur• liquid tragi from ayspsnded sol;dr
P SIRalalin si conuciofs• A rued Din?a Ic AI
Ihrovgh tA. C growth grocers in which wits—tor It—p9}5 and 1 °ries of pan;&Uy avDmeag oil c'vcvlar 1.c...cea
a.r lie rola t. e"
munant Biological- F"ll"ion at eft]uent fohow;ng septic ranks ]age.— or
tom. all., „v„r... nl prasest m whish funher biod.eomposil;on is .ap.et.d to predue. d.sind
.illy. nla; Nyd,a c foaling rales en these l;[lalt ar. compv,.d tri 9Pdrac and hav, a a.&uflinq tow
gpM.l (las, than an.): (b}Re[ircvlAl;n9 b;etag;_al .lh,, t of 'And filler as doll
the added ram yp. nod in (a) with
upaD;Gty so ngcle 4:111-1 back through Ih. send fill.,;
(eo)Sand or "d—media $7;1%1(1. A poC.hing pro:,ra by which effluent 11m;ls if, aeh;_d Ihr gh A
farther fedvc[ion el aysp.nd.e aotld-;(allow Est.cavil h d,auli-P S
oleo :n eh. on � 4 Y. Y r oAdsd tiller with lording
n lea in 3M live+ la shr.a gpmesf aan9.;gb)h;gh lay. - a pre&, hyd-ulicany load,d lilt— w;ah loadinq
gpavrf rang.; At any sal., the loading las. wilt .ore. oil the.. 9pnv&I:
(rl)Secondiry Ctari Cart_ A link which loftow, the biolog;c Af unit or a vestment latent and which has
.he P -p... or r.,noj"'Fudge astccia lid A,h the 41olag;csl Vratm-m units;
(42)5•p2nl• Slvdg• Res.radon. A pan of the cannel slab;Grlsion proe•st whore the aerivatod I.dg.
is If 0-11ed to a tank and -•ral,tl Woe, f—„.Ing it la the basin;
(cl)SepSc Tank. A .in9:e.nary . iISI-2 lank In which -ental ship- Is in ce nla c[ will, the wast.wv.r
hawing through In. tAnk: .halt no, b• appil ably lar .optic tank syuemc sowing .;.pro lamily
I..ide,c.[ hav[nq a eapadty or 2C<4 grub.+ ar let. which di.chugo to s nilair.At;— ri.td:
(44)51,49• Op•alion. 71,. pro,.., by whkh oro Attic or ralalP, -0-f and tivdge 4 q-slhed, Igv.6od_
minaratiz.d or con $1.d into m,ae t[abl. ofpank matter through [he %c[ivity of living organisms,
Which includes --riled 4,AeG q sant,•
1451Sludga Dry;ng Dada. An oral C.e;A;irg natural w artiriclil layers of parous material, upon which
dipesl.d sewage sludge is dried by eninagr and waposal;oA;
(46)Slud9• Ehaltialion. A Pf«arc of uvdge conditioning in which certain cons,ituems are !.moved by
s ucc.ssivs washings with fresh wale, or plaru .)Hoon[:
071Slud0e GAL Utikaaeicr- The lancets el wing sew.pe pis lot the purpose of hailing buildings,
driving engines, arc.;
(4015sudge Holdlnq lank (Aaralod zeal Hona•aated). A urd4Ui� t,#, -for small wa&l.wAler Voatmonl
planta not coots kung a d eraaf 1. wr�ch dvtlge -y tau keel he:h. and 4 rp , Mint wilt,Jr:,wn pi;o, to
a :(T.V method (i..- shrC,s drying Ind): Ins may be done by adding a emelt amount of air simply to
keep the sludge fresh, bs: not nocauadi, An amount that would be requvod la achiw. atabir_alian of
organic miller. A nonasra:ad tank wuvd simply be used to docanl sludge lariat to dowel -1119 and wou;d
simply be used to docanl 11.119e prior la if—Wing and would not Allow long ia-id. (several days o1
detention) without rosull;ry odor proYwmt•
(z9)Sludge Incinafatoet.' A !Waco eol;gned to bwn sludge and to tamava -e moisture and combustibles
MAW411 and reduce the IW,). Ie a mole ash:
(50)Slvd9e Slabi;zation (Chemical or Tharmaq. A protest W make treated sludge less odorous and
puuescrible, and to educe the P1Vogene organism content; This may be done by pli adivttmenl
chlorine dosing, or by heal tree:men[;
(51)Sludoe Thickener. A type of ..eLmenszlien lards In which the sludge Is permitted to settle and
tldck.n through agiution and prl rdy:
02)Slabi6z19en t -9--M A-lyp. of e.idation lagoon In which biological oxld-[;an el organic matter is
tltacled by naturaf lrantlar al oxygen W lite water lrom iU (nal 1poSth;nq pond);
(51)S1and•By Power Supply, on sill of portable elocL(kal generating equipment:
(SiJ Static Screens, A s(ationaq IOlen designed to umovs solids Including non•b;odagradab[a
parliculat. (Iloatable solids, svapended solids and BOD reduction) from munic;pat and industrial
waslswilaftreatment systems;
[$5)Tetllasy Treslmafk4 A stage of troalmant following socendary which is primarily lot the pulpose
of orliveni poilhy'ag; A LeC`erag 11900, of sand or coal (ale( m,;ghl be emptayid (of (his purpos.-
(S6)Theimal Pclulio, Con.-ol Devks. A devics providng for the transfer of heat from a quid Ilow;ng
in tube, to another fluid wlside the lubes, u vita versa; ”, other means of regWal;ng
liquid lamp.ralufas:
(57)Thumal Sludge Condis;ener. A ccneilioting p(ocoxr by which haat It added for a protracted poriod
of time to Insptw. the dowalsfablay of sludge by the s01u1IIEW sp and hyd.auGzing of the smaller and
more hlghfy hydrated study. parlicler
(5a)Tosic Materials, Those wssl.a ar combinAl;enl el -MUS lncludtng thous..Causing agents which
after discharge and upon eapasuf., ingestion, inhalation er assimilation into any organism a;1hor
dveclfy from the emriecamerd or lndvictly by ingestion through good chains, will cause death, disoaso
behavioral abnerm2ltiex, cancer, gon[tic mutations, physiological malfunctions (inctwing m-Ifuncl;o ,
)n ispioduc[ion) or physical detWrs%4on5, in such organisms or their ofispf;ng; Toxic mzlerials
inalvde, by way ihustfalion and not fiositalion; (sad, cadmium, chromium, mercury, vanadium, ,
atsank, lint, 991210 rbrwaJorebonzaei. (OHCS polychkrinalad Wph.nyls (PCBs) and dkhlorod;pha^yl
lrichfwaa[hsna (DOT): and any other Materials that have or may Mr.14.1 be determined to have logic
proper[hs..
4591Ts;ek6ng Wlar, A biological tre.;Mem ten;[ consisting of material such as broken stony or sock
over which wastawaler is dilWbu[ed: A high fate lfkkr'uV fillet is one which Is opef-tea"•at be:.votn
10 and 30 mgd par acts. A law tate ukkrmq lillar is one which it designed to opofole al ono otc four
mgd pat act&;
(60)71itktinp Filer (Packed Tower). A plug flow type of operation in which wastewaterflaws down
h
through succ•ise (ayets at mall or 6ltrste matallai; Ofgank material is removed continua::y by
active t>tolopkal used growth is each sxcosslvt laye(. This m•lhod mly preduco "sacondaifl, c�atity
.trlverll, or may be adapl.d to product A ruined Hllueni;
flil)Yleuvm Fifties Caraldruges- or F214r Aossas, Devices which are designed to rameve eatoas
water from .fisher dgealad or und;gesI#d sludge prior to disposal or further treatment.