T* A' .'•'-.' r - United States Environmental Protection Agency · Concentration(ppni) Pounds/Day...

17
- -. Form SCC 2 <? ——— "T* / ^^ : : A' " v .' •' ^ STATE OF LOUISIANA ' ,-' : /<: DEPARTMENT OF NATURAL RESOURCES " ' . j - N i' Office of Environmental Affairs i Post Office Box 44066, Capitol Station J . - ' . - Baton Rouge, Louisiana 70804 r"*^ _AJ i" • - -r; c^ r^ . £^; : - _.'•'-.' __r ==== ^ <:; « 000^4 c 3 ' ••:, PERMIT APPLICATION TO DISCHARGE WASTE WATER ?| This application to the Environmental Control Commission mffjjrbe submitted on either of the following forms: . flSti. '~ J 1. National Pollutant Discharge Elimination System (NPDES) Standard/ iidtiuiidi ruiiuccmL u ibuiidrye c i imiridL lun oybceiii \.nruiL3) ocdnadro /? Form C [EPA Form 7550-23 (7/73) Sections I, II, and IIIJ plus ^ Sections III and IV of Form SCC 2 or Q ' 2. Environmental Control Commission Form SCC 2 - /J^DESt±6 f ','] SECTION I Check One: Initial Permit_^-§f_ Permit Revision /.#>/ Legal Name of Applicant Combustion, Inc. (Firm, Partnership, Corporation, etc.) Mailing Address p.p. Drawer B Enterprise. MS. 39330 Faci 1 i ty Name Combustion - Denham Plant__________Tel ephone 504-665-5503 Facility Location Intersection Arnold & Milton Rd.____________ Parish Livinsston___________________________________ Responsible Representative of Application: Name: H.A. Gammons, Sr.___________ Title: President ____________________________________ Mailing Address: P.O. Drawer B____________________________________ Enterprise, MS. 39330___________________________ Tel ephone: 601 -693-2608______________________________ Type Facility Waste Oil Reclaiming Plant________________________ (Cannery, Oil Refinery, Dairy, etc.) Products No. 4 Fuel 143872

Transcript of T* A' .'•'-.' r - United States Environmental Protection Agency · Concentration(ppni) Pounds/Day...

- -. F o r m SCC 2<? ——— "T* / ^^ : • : A'" v .' •' ^ STATE OF LOUISIANA ^

' , - ' : / < : D E P A R T M E N T O F N A T U R A L R E S O U R C E S" ' . j - N i ' O f f i c e o f E n v i r o n m e n t a l A f f a i r si Post O f f i c e B o x 44066, C a p i t o l S t a t i o nJ . - ' . - Baton Rouge , L o u i s i a n a 70804r"*_AJ i" • --r; cr — .£ ;:-

_.'•'-.' __ r====^<:;

« 000^4c 3 ' ••:,P E R M I T A P P L I C A T I O N T O D I S C H A R G E W A S T E W A T E R ? |

T h i s a p p l i c a t i o n t o t h e Environmenta l Contro l C o m m i s s i o n m f f j j r b e submittedon e i t h e r o f the f o l l o w i n g f o r m s : . f lSti . '~ J

1 . N a t i o n a l P o l l u t a n t D i s c h a r g e E l i m i n a t i o n S y s t e m ( N P D E S ) S t a n d a r d /i i d t i u i i d i r u i i u c c m L u i b u i i d r y e c i i m i r i d L lun oybc e i i i \.nruiL3) o c d n a d r o /?F o r m C [ E P A Form 7550-23 ( 7 / 7 3 ) S e c t i o n s I , I I , a n d I I I J p l u s ^S e c t i o n s I I I a n d I V o f F o r m S C C 2 o r Q '2. Env ironmen ta l Contro l C o m m i s s i o n F o r m SCC 2 - /J^DESt±6f',']S E C T I O N I

Check One: I n i t i a l Permit_^-§f_ Permit Rev i s i on /.#>/L e g a l N a m e o f A p p l i c a n t Combustion, Inc.( F i r m , P a r t n e r s h i p , C o r p o r a t i o n , e t c . )

M a i l i n g A d d r e s s p . p . Drawer BEnterprise. MS. 39330

F a c i 1 i ty N a m e Combustion - Denham Plant__________Tel ephone 504-665-5503F a c i l i t y L o c a t i o n Inter s e c t i on Arnold & M i l t o n Rd.____________

P a r i s h Livinsston___________________________________R e s p o n s i b l e R e p r e s e n t a t i v e o f A p p l i c a t i o n :

N a m e : H . A . Gammons, Sr.___________T i t l e : President____________________________________

M a i l i n g A d d r e s s : P.O. Drawer B____________________________________Enterprise , M S . 39330___________________________

Tel ephone: 601 -693-2608______________________________T y p e F a c i l i t y W a s t e O i l Reclaiming Plant________________________( C a n n e r y , O i l R e f i n e r y , D a i r y , e t c . )Produc t s No. 4 Fuel

143872

• F o r m bCU 2

S E C T I O N I / •- \\ **Raw M a t e r i a l s W a s t e lubr i ca t ing oils. No. 2. 4 & 6 ~ F i i e l oi l

dirt & water _________________________ . _______________________Process used which produc e s i n d u s t r i a l waste s d i s c h a r g e d i n t o waters o f t h e S t a t e .( I f a p p r o p r i a t e , make proce s s e s c o i n c i d e w i t h sources i d e n t i f i e d i n S e c t i o n V I . )

S E E A T T A C H M E N T A

Source o f W a t e r S u p p l y in G a l l o n s Per Day ( L i s t each source g i v i n g q u a l i t y such asf r e s h , b r a c k i s h , s a l t , h a r d , or s o f t ; and g ive breakdown as to how each source isu s e d . )Public water system s u p p l i e s a p p T - m H m a f . P l y ^p,OOQ g a l , o f wat.pr PPT M o n t hto the plant Primary use is for B o i l e r , hut: a l s o n s p d fn-rSanitary F a c i l i t i e s .

A n t i c i p a t e d d a t e o f s t a r t u p or change in e f f l u e n t :

sr.cnon n

C o m p l e t e t h i s s e c t i o n F o r e f j c l i d i o c l K i r g e p o i n t . U s e s e p a r a t e shc s t f o r cschd i s c h a r g e . A t t a c h a wat er f l o w d i a g r a m ( b l o c k t y p e ) f o r c o m p l e t e f a c i l i t y i n -c l u d i n g t r e a t m e n t o f each d i s c h a r g e .D i s c h a r g e I d e n t i f i c a t i o n 001

A. C h a r a c t e r i s t i c s :

Oil and GreaseT o t a l S o l i d sT o t a l S u s p e n d e dS o l i d sT o t a l D i s s o l v e dS o l i d sV o l a t i l e S u s p e n d e dS o l i d s .F i x e d S u s p e n d e dS o l i d sV o l a t i l e Dis so lvedS o l i d sF i x e d D i s s o l v e dS o l i d s . .T o t a l A l k a l i n i t y(as C a C 0 3 )orT o t a l A c i d i t y(as C a C o 3 )T o t a l H a r d n e s s( a s C a C C h )C h l o r i d e s (asCD ' . .Sul f a t e s (asso4=)CODTOCBOD5

F l o w ( G P M )pHT e m p e r a t u r e ( ° C )T u r b i d i t y ( J C U )C o l o r ( T r u e /A p p a r e n t )

C o n c e n t r a t i o n ( p p n i ) P o u n d s / D a yD a i l y A v e r a g e D a i l y M a x i m u m D a i l y A v e r a q a D a i l y M a x ." " ' .-«•140 19. S .68 1.0

640 1110 2860 410144 • 60 1.54 3.0

600 1050 ' 2820 ' 3980NA

NAN A • • - - - - .NA ' -

' N A

NANA

"s4n 1.1.00 1920 3960. . ' 100 200 340 680

250 300 • 8.75 1075.4 80 2.64 390 100 3.15 5

_ _ * - •

Average Maximum M i n i m u minnn 1500 05.6 5.6 5.627 40 5

Clear Aniber Clear

l - U n i l -iU, LW S E C T I O N I I

' D i s c h a r g e I d e n t i f i c a t i o n _ _ _ _ _ _ _ _ _ _ _ _ _B . L i s t p e r t i n e n t p h y s i c a l a n d ch emica l p r o p e r t i e s ( e . g . , t o x i c c o m p o n e n t s ,t a s t e and odor c o m p o u n d s , heavy m e t a l s , e t c . )

Phenols l e s s 1 PPMS u r f a c t a n t s le s s 1 PPM

,.., ' : . .^C. , ^Toxic i ty d a t a . L : ( S h o w : p q n c i s e l y th e nature and r e s u l t s o f any t e s t s and• . " . . ' . ;.;. ;0:=^ ."( subsequent .^evaluat ions cqnqerning . the . tox i . c . i ty o f t h e waste o f f i s h o r: - . . ' ; r . h i - , - - . o f h e r . / a n J m a - T s ^ ) ^ J V i b i o a s s a y test ( 9 6 h r . T L m ) i s required i f t o x i c compoundsare p r e s en t . 'N O N E

D. How waste reaches s t a t e waters ( C h e c k a p p r o p r i a t e w o r d s ) : d i r e c t l y xby d i t c h x______; by p r i v a t e sewer_________ ; by p u b l i cw e l l •__________. W a s t e f l o w s into: (1) p i t ch ____ __( 2 ) thence in to Canal_________________'• ( 3 ) thence in t oBeaver Branch____________.; (4) thence i n t o W e s t C o l y e l l Crpek________v • (Name of s tream, l a k e , marsh,

or u n d e r g r o u n d hor izon r e c e i v i n g the w a s t e )N o r m a l d u r a t i o n o f d i s c h a r g e (hours p er d a y )Method used to measure rate of f l o w M a x , pump di s charge rate

FORM SCC 2 •^

S E C T I O N I I I

C o m p l e t e t h i s s e c t i on f o r each d i s c h a r g e p o i n t u s i n g s e p a r a t e sheet f o reach d i s c h a r g e p o i n t .D i s c h a r g e I d e n t i f i c a t i o n : 001_____D i s p o s a l methods a n d f a c i l i t i e s :

S E E A T T A C H M E N T C

B. - T r e a t m e n t m e t h o d s in o p e r a t i o n : ( P l e a s e be s p e c i f i c )Three s tage oil removal by phase separation for water f rom process area.T h i s water combines with storage area run o f f , and passe s through af inal oil skimming di tch. Fina l treatment for removal of BOD, and______suspended s o l i d s is in a two cell oxidation pond._________________

F O R M S C C 2S E C T I O N I V

C o m p l e t e t h i s s ec t ion for each s i g n i f i c a n t source even i f the varioussources combine to a common d i s c h a r g e p o i n t . Use s e p a r a t e sheet for eachsource o f d i s c h a r g e .S o u r c e I d e n t i f i c a t i o n : 001

A . C h a r a c t e r i s t i c sD a i l y A v e r a g e C o n c e n t r a t i o nB e f o r e - T r e a t m e n t

25280Q... .

600 :-,..2 6 9 Q , : ; ' . . .

NANANANANANANA

600100

11,500NA

35005-9.150

Amber27

100Q

;r d a y ) 8

A f t e r T r e a t m e n t5

103030

1000

600T O O160

306-9

20C l e a r

Ambient1000

.Oil and Greas eT o t a l S o l i d sT o t a l S u s p e n d e d S o l i d s ; , , ; . _T o t a l D i s s o l v e d S o l i d s ; . . : = .V o l a t i l e S u s p e n d e d S o l i d sF i x e d S u s p e n d e d S o l i d s ;V o l a t i l e D i s s o l v e d S o l i d sF i x e d D i s s o l v e d S o l i d sT o t a l A l k a l i n i t y ( a s C a C O g )orT o t a l A c i d i t y ( a s CaCO.JT o t a l H a r d n e s s ( a s C a C O ~ )C h l o r i d e ( a s C 1 - )S u l f a t e s ( a s S 0 4 = )CODTOCBOD5pH ,T u r b i d i t y ( J C U )C o l o rT e m p e r a t u r e ( C )F l o w ( G P M )N o r m a l d u r a t i o n o f d i s c h a r g e ( h o u r s p er d a y ) 8B. P e r t i n e n t p h y s i c a l and chemical p r o p e r t i e s ( e . g . , t o x i c c o m p o u n d s , ta s t eand odor c o m p o u n d s , heavy m e t a l s , e t c . )

Before A f t e rPhenols 210 L e s s 1 PPMS u r f a c t a n t s T . P S S 1 P P M

F O R M S C C 2S E C T I O N I V

C . D i s p o s a l m e t h o d s a n d f a c i l i t i e s :S E E A T T A C H M E N T C

D. T r e a t m e n t me thod s in o p e r a t i o n : ( P l e a s e b e s p e c i f i c . )T h r e e s tage oil removal by phase s^pai-ai-ion for- Mat-or- fr^m process areaT h i s water n o m h i n p s wil:b Rt.rrragp ar-pa m-nnffj q p r ] pa s s e s through a f i n a loil skimmin di

F i n a l trea1-.THp.nl: for rpmnval nf BOHj anrl q u c ; p p n f l g r l s o l i d s i s in a twocell ox idat ion pond. ___________________________________________

A T T A C H M E N T A

1 • Des cr ip t i on of Process

Raw material cons i s t ing of contaminated crude oi l , N o s . 2, 4, 6 F u e l Oilsand small amounts of lubricat ion oil is unloaded into s torage tanks and lagoons.ThE raw material normal ly contains small amounts of su sp ended and entrained water.Oil stored in the lagoons will also be contaminated by rain f a l l and recycledprocess water.

Raw material oi l s are t ran s f e r ed to the p lant where it is heated by directcontact with steam in a phase separation process. The top layer of oil is removedfor sale as a fue l oil and the m i d d l e layer of oi ly s l u d g e is pumped to storagelagoon. The bot tom or water layer that results^ is from steam condensate, waterremoved from solut ion and entrained water. The bottoms, along with any proce s s ing.area storm drainage, are returned to the raw material oil lagoons by a sump pump.

: .-..; ^ As. the concentration of.:water builds up. in the, lagoons, .A f r e e water layer willf orm in the .bottom.of the lagoon. A bottom drain, i s ,used., to remove thi s water layer .and thus maintain the p lant water balance. Sec t i on III contains a d e s c r ip t i on off a c i l i t i e s to be ins tal l ed for water treatment prior to di scharge from the f a c i l i t y .

' P L A N TP L A N T " N ^ O U T P U T S :I N P U T S :P U B L I C W A T E RS U P P L YP R O C E S S A R ED R A I N A G E

O I L R A WM A T E R I A LR A I N F A L LO N P O N D S

S T O R A G E A R E AO R A i N A G E

S L U D G EO I LS T O R A G ER A WM A T E R i A LS T O R A G E

P R I M A R YO I LR E M O V A L

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• - - • i ! ' . - { . i = r v : • • ! • A T T A C H M E N T C

" D I S P O S A L M E T H O D S A N D F A C i L i t i r s

W A T E R i s R E M O V E D F R O M S T O R A G E L A G O O N S A S AS E P A R A T E L A Y E R B Y U S E O F A N U N D E R F L O W P I P E . T H I S W A T E R "C O N S I S T S O F :

.... A . W A T E R o i S S O L V E D . . A N D . , E N T R A i N E D I N T H E R A W. M A T E R I A L A S D E L I V E R E D .

. : / B . R A I N F A L L A N D A T M O S P H E R I C M O I S T U R E A C C U M U ---~.-r- ^ , _ ; - L A T E D B Y T H E O I L I N S T O R A G E .

. , ; ; ; _ : " • • . ..-C. W A T E R R E M O V E D I N T H E . P R O C E S S A N D R E C Y C L E DT O T H E P O N D .

; — - - D . P R O C E S S A R E A D R A I N A G E .E . S T E A M C O N D E N S A T E F R O M T H E P R O C E S S .

T H E S T R E A M T H E N F L O W S T H R O U G H P R I M A R Y , S E C O N D A R YA N D T E R T I A R Y S E T T L I N G P O N D S T O R E M O V E E N T R A I N E D O I L . E A C HP O N D H A S A N U N D E R F L O W P I P E A N D T H E O I L L A Y E R W I L L B E P E R I O D -I C A L L Y R E T U R N E D T O T H E S T O R A G E L A G O O N S . O U T F L O W F R O M T H ET E R T I A R Y S E T T L E R W I L L B E D O N E M A N U A L L Y A F T E R A V I S U A LC H E C K F O R A N O I L L A Y E R .

W A T E R R E M O V E D . F R O M T H E T E R T I A R Y S E T T L E R W I L L E N T E RA P E R I M E T E R D R A I N A G E D I T C H A L O N G W I T H R U N O F F F R O M T H E S T O R A G EA R E A . T H E P E R I M E T E R D I T C H W I L L T E R M I N A T E W I T H A N U N D E R F L O WP I P E T O A C T A S A F I N A L O I L S K I M M E R . T H E U N D E R F L O W F R O M T H ED I T C H W I L L E N T E R T H E F I R S T O F T W O O X I D A T I O N P O N D S F O R F I N A LB O D R E D U C T I O N . T H E " P R I M A R Y A N D S E C O N D A R Y O X I D A T I O N P O N D SW I L L B E C O N N E C T E D B Y A N U N D E R F L O W P I P E T O P R O V I D E A D D I T I O N A L

P R O T E C T I O N I N T H E E V E N T A M A J O R S P I L L O C C U R S .

E F F L U E N T D I S C H A R G E D F R O M T H E F A C I L I T Y W I L L B ER E M O V E D F R O M T H E . S E C O N D A R Y O X I D A T I O N P O N D B Y A M A N U A L L Y

O P E R A T E D P U H - P F O L L O W I N G A V I S U A L C H E C K O F W A T E R Q U A L I T Y ,

i ••-;-: • • • : • ". ATTACHMENT G

• : . ' . H O L D U P T I M E S

H O L D I N G T I M E O F O X I D A T I O N P O N D S A S S U M I N G 3 F T . L E V E L C H A N G E :C A P A C I T Y O F O X I D A T I O N P O N D ' S ( F . & F ) = 10,700 G A L / I N

OR ( 3 F T ) ( 1 2 i N / F T ) ( 1 0 , 7 0 0 G A L / I N ) =385,200 G A L .i

F O R . A U G . A N N U A L R A I N F A L L :r^ ".• ,- i • - ?- -. - . - - r . - -. 385..200 GAL X 365 D A Y S / Y R _ _ _ _ _ _ _ _ _ _ _ _ _ _: . • (2.81 ,800. F T . ^ ) < 5 6 . 5 4 ' i N / Y K ) " ( ( 5 ; 6233L G A L / . I N ) I - 384,000 G A L F E E D

= - 1 4 D A Y S H O L D U P

F O R M A X I M U M M O N T H L Y R A I N F A L L :' _ _ _ _ _ _ 385.200 G A L X 3 0 D A Y S / M O _ _ _ _ _ _ _ _ _ _ _ _ _ _ _( 2 8 1 , 8 0 0 F T . 2 ) ( 1 4 . 6 3 i N / M O ) ( 0 . 6 2 3 3 G A L / I N ) +32,000 G A L . F E E D

- 4 . 4 D A Y S H O L D U P

FORM SCC 2

A FT I D A V I T

S t a t e o f /Y)P a r i s h OP C o u n t y of

B e f o r e me , the u n d e r s i g n e d a u t h o r i t y , on t h i s day p e r s o n a l l y a p p e a r e d7 / r\ • & l°t t"w t~n Q /w^S* ______________ known to me to be the p er s on

whose name is sub s cr ib ed to t h i s i n s t r u m e n t , who a f t e r b e i n g by me d u l y swornon oath or a f f i r m a t i o n s ta t e s that he has had t h i s report p r e p a r e d , a n d , thatt h i s report is a true and correct r e f l e c t i o n of the record of the o p e r a t i o n srepor t ed herein, that no p e r t i n e n t matter inqu i r ed i n t o t h i s r e p o r t , andknown by h i m , has been o m i t t e d t h e r e f r o m .

to and sub s cr ibed b e f o r e me, t h i s ^/ *-& day of

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