mizuki inhibitory effect

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Biological Wastes 33 (1990) 161-168 Inhibitory Effect of Citrus unshu Peel on Anaerobic Digestion E. Mizuki, T. Akao & T. Saruwatari Fukushima Industrial Research Instit ute of Fukuoka Prefecture, Yame-shi, Fuku oka 834 , Japa n (Re ceiv ed 3 Oct ober 19 89 ; revised version received 1 8 Ja nuar y 19 90 ; accepted 24 January 1990) ABSTRACT A significant inhibition of methane fermentation was observed in anaerobic' digestion of Citrus unshu peel at loadings above 2 g/litre per day. This inhibitory effect was mainly due to peel oil, but in part to other substances present in the peel. The limiting load of peel oil to anaerobic digestion was about 65 pl/litre per day. Addition of peel oil below this limit load resulted in a change in the microbial flora and in gas production greater than that of digestion with no peel oil. Citrus unshu peel did not inhibit methane ,fermentation after removal of peel oil by steam distillation or aeration. INTRODUCTION Usually, anaerobic digestion converts solid wastes fro m fruit processing into methane fuel. Previous workers, however, have reported that the citrus wastes are toxic to the anaerobic digestion (McNary et al., 1951; Wolford et al., 1952; Lane, 1980, 1983a, 1983b, 1984). In Japan, Citrus unshu s the commercially most import ant citrus fruit and a number of Japanese plants produce a large amount of canned and juice products of unshu citrus. This creates serious problems in disposing of the waste peel which is produced at more than 70000t/year. The primary objective of this st udy was to assess the level of the toxicity of C. unshu peel to the practical anaerobic digestion of the waste peel. 1 6 1 Biological Wastes 0269- 74 83/ 90/$0 3-5 0 ~ 1990 Else vier Sci ence Publ ishe rs Lt d, England. Printed in Gre at Britain

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Biological Wastes 33 (1990) 161-168

Inhibi tory Effect of Citrus unshu P ee l o n A n a ero b i cD i g e s t i o n

E. Mizuki, T. Akao & T. Saruwatari

Fukushima Industrial Research Institute of Fukuoka Prefecture,Yame-shi, Fukuoka 834, Japan

(Received 3 October 1989; revised version received 18 January 1990;accepted 24 January 1990)

A B S T R A C T

A s ign i fi can t i nh ib i ti on o f methane f erm en ta t i on was observed i n anaerob ic '

d iges t i on o f Citrus unshu pe el a t loadings above 2 g / l i t re per day. This

inh ib i to ry e f f ec t was ma in l y due t o pee l o il , bu t i n par t t o o ther subs tances

presen t i n t he pee l . The l im i t i ng l oad o f pee l o i l t o anaerob ic d iges ti on was

abou t 65 p l / l i t re per day . A dd i t i on o f pee l o i l be low th i s l im i t l oad resu l t ed i n a

change i n t he microb ia l f l o ra and in gas p roduc t ion grea t er t han t ha t o f

d iges t i on w i th no pee l o i l . Citrus unshu pee l d id no t i nh ib i t me thane

, f ermen ta t i on a f t er rem ova l o f pee l o i l by s t ea m d i s t il l a ti on or aera t ion .

INTRODUCTION

Usually, anaerobic digestion converts solid wastes from fruit processing into

methane fuel. Previous workers, however, have reported that the citrus

wastes are toxic to the anaerobic digestion (McNary e t a l . , 1951; Wolford

e t a l . , 1952; Lane, 1980, 1983a, 1983b, 1984).

In Japan, C i t r u s u n s h u is the commercially most important citrus fruit and

a number of Japanese plants produce a large amount of canned and juice

products of u n s h u citrus. This creates serious problems in disposing of the

waste peel which is produced at more than 70000t/year. The primary

objective of this study was to assess the level of the toxicity of C . u n s h u peel tothe practical anaerobic digestion of the waste peel.

161

Biological Wastes 0269-7483/90/$03-50 ~ 1990 Elsevier Science Publishers Ltd, England.Printed in Great B r i t a i n

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162 E. Mizuki, T. Akao, T. Saruwatari

M E T H O D S

M a t e r i a l s

W a s t e p e e ls o f C. unshu w e r e o b t a i n e d f r o m a c a n n i n g p l a n t a n d s t o re d a t

- 4 0 ° C p r i o r t o u s e . P e e l o i l o f C. unshu w a s o b t a i n e d f r o m a c o m m e r c i a l

j u i c i n g p l a n t . 1 9- L im o n e n e a n d c i tr u s p e c t i n w e r e p u r c h a s e d f r o m W a k o

P u r e C h e m i c a l s ( T o k y o ). O t h e r r e a g e n t s a n d s o l v e n t s w e r e c o m m e r c i a l l y

a v a i l a b l e a n a l y t i c a l r e a g e n t s o r l a b o r a t o r y - g r a d e m a t e r i a l s .

F e e d s t o c k s

W a s t e w h o l e p e el s ( fl a v ed o a n d a l b e d o ) w e r e c o m m i n u t e d f o r 1 0 m i n a n d

h o m o g e n i z e d fo r 2 0 m i n . T h e h o m o g e n a t e w a s t h e n s u p p l e m e n te d w i t h

( N H 2 ) 2 C O (1 07 .2 g / k g d r y w t o f p e el ) a n d N a 2 H P O 4 (5 6.0 g / k g d r y w t o f

p e el ), d i l u t e d w i t h d i s t i ll e d w a t e r t o 5 - 4 0 g d r y w t o f p e e l / li t r e a n d s t o r e d a t

4°C.

T h e p e c t i n m e d i u m u s e d a s a p e e l- f re e f e e d s t o c k c o n t a i n e d c i tr u s p e c t i n

( 2 0 g / l it r e ), ( N H z ) 2 C O ( 2 - 1 4 g /l it re ) a n d N a 2 H P O 4 ( 1 -1 2 g / li tr e ), a n d w a s

s t o r e d a t 4 ° C .

D i g e s t i o n s

D i g e s t i o n s w e r e c a r r i e d o u t i n 2 0 0 m l c o n i c a l f la sk s c o n t a i n i n g 2 0 0 m l o f

s e w a g e s l u d g e [ 2 7 . 5 % ( v / v ) s o l i d ] . T h e s l u d g e w a s i n c u b a t e d a t 3 7 ° C w i t h

i n t e r m i t t e n t s h a k i n g . A t 2 4 -h i n te r v a ls , a f te r t h e r e m o v a l o f 2 0 m l d i g e s t er

c o n t e n t s , 2 0 m l o f f e e d s t o c k c o n t a i n i n g 0 . 1 - 0 - 8 g ( d r y w t ) o f s o l i d s ( i . e .

0 - 5 -4 . 0 g d r y s o l i d s / li t r e o f s l u d g e p e r d a y ) w a s a d d e d t o t h e f la s k s to g i v e a

c o n t i n u o u s d i g e s t i o n o f 1 0 d a y s r e t e n t i o n t i m e . P ee l oi l a n d D - l i m o n e n e w e r e

a d d e d u s i n g m i c r o - s y ri n g e s w h e n d i g e s t io n s w e r e f e d w i t h f e ed s t o ck s . G a sy i e ld a n d p H o f d i g e st i n g s lu d g e w e r e d a il y m o n i t o r e d .

E s t i m a t i o n o f o i l c o n t e n t

P e el oi l c o n c e n t r a t i o n w a s d e t e r m i n e d b y t h e m e t h o d o f S c o t t a n d V e l d h u is

(1966).

G a s c h r o m a t o g ra p h y

P e e l o il a n d D - l i m o n e n e w e r e a n a l y s e d b y f l a m e - i o n i z a t i o n g a s c h r o m a -

t o g r a p h y u s i n g a Y a n a c o g a s c h r o m a t o g r a p h G - 8 0 w i t h a s t a i n l e s s s t e e l

c o l u m n ( 20 0 x 0-3 c m ) p a c k e d w i t h 8 0 - t o 1 0 0 -m e s h E G A U n i p o r t B .

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Inhibition of digestion by citrus peel 163

M e t h a n e w a s d e t e r m i n e d b y g as c h r o m a t o g r a p h y ( Y a n a c o G - 80 ) w i t h a

s t a in l e s s s te e l c o l u m n ( 2 0 0 x 0 .3 c m ) p a c k e d w i t h a c t i v e c a r b o n (3 0- t o 6 0-

m e s h ) , u s i n g t h e r m a l c o n d u c t i v i t y d e t e c t i o n .

R e m o v a l o f p e e l o i l f r o m f e e d s t o c k s

P e e l o i l i n f e e d s t o c k s w a s r e m o v e d i n t w o w a y s , a e r a t i o n o r s t e a m

d i s t i l l a t i o n . I n t h e f o r m e r , f e e d s t o c k s o f h o m o g e n i z e d w h o l e p e e l w e r e

i n c u b a t e d i n a n o p e n - t o p p e d f e r m e n t e r a t 3 0 °C w i t h a ir s p a r g in g

(1 5 l i t r e s / l ' 5 l i tr e s f e e d s t o c k p e r r a in ) . I n t h e l a t te r , h o m o g e n i z e d p e e ls w e r e

e x p o s e d i n a s t e a m - j a c k e t e d p a n t o a s t e a m j e t f o r 4 0 m i n .

R E S U L T S

Inhib i tory e f fect of C. unshu p e e l o n m e t h a n e f e r m e n t a t i o n

P e e ls o f C . unshu w ere fed to d ige s te r s a t the load s o f 0 .5 , 1"0 , 2 .0 an d 4 .0 g d r y

w t o f p e e l (d .w . p .) p e r l i tr e o f s l u d g e p e r d a y ( li tr e p e r d a y ) . T h e c h a n g e i n g a s

y i e l d is s h o w n i n F i g . I ( A ) . F i g u r e I (B ) s h o w s t h e t i m e c o u r s e o f p H o f t h e

d i g e s t i n g m i x t u r e . T h e d i g e s t i o n s w i t h 0 . 5 a n d l ' 0 g w a s t e p e e l a n d 2 " 0 g

p e c t i n a l l a t t a i n e d a s t e a d y - s t a t e , w h i l e w i t h 2 " 0 a n d 4 . 0 g w a s t e p e e l g a sp r o d u c t i o n a n d t h e p H d e c r e a s e d w i t h t i m e a n d t h e f a l l i n p H t o b e l o w 6

a f t e r 1 0 - 1 5 d a y s w a s e v i d e n c e o f d i g e s t i o n f a il u r e.

Inhib i tory e f fect of C. unshu p e e l o i l o n m e t h a n e f e r m e n t a t i o n

G a s c h r o m a t o g r a p h y s h o w e d t h a t C. unshu p e e l o i l a n d c o m m e r c i a l l y

a v a i l a b l e D - l i m o n e n e c o n t a i n e d 8 9" 9 a n d 9 8 " 4% o f D - l i m o n e n e , r e s p e c ti v e l y .

T o d i g e s t i o n s f e d w i t h 2 g [ ( d .w . ) /l i tr e p e r d a y ] p e c t i n w e r e a d d e d 0 -9 0/~ 1 o f

p e e l o i l/ l it r e p e r d a y . T o a n o t h e r d i g e s t i o n f e d w i t h p e c t i n [ 2 g ( d .w . ) /l it re p e rd a y ] w a s a d d e d 8 2 -3 # l / li t re p e r d a y o f D - l i m o n e n e as a r e a g e n t t h a t w a s

e q u i v a l e n t t o 9 0 /~ 1 o f p e e l o il i n t e r m s o f D - l i m o n e n e c o n t e n t . D i g e s t i o n s

s u p p l e m e n t e d w i t h p e e l o i l a t 7 0 , 8 0 a n d 9 0/~ 1, a n d 8 2.3 ~1 o f D - l i m o n e n e a s a

reag en t f a i l ed a f te r 46 , 46 , 33 an d 43 d ays r e spec t ive ly (F ig . 2 ). A dd i t io n o f 0

o r 6 0/~ 1 o f p e e l o i l/ l i tr e p e r d a y t o d i g e s t i o n s s h o w e d n o i n h i b i t o r y e ff ec t o n

t h e m e t h a n e p r o d u c t i o n . T h e m a x i m u m a m o u n t o f pe el oi l p e r m is s ib l e fo r a

p r a c t i c a l m e t h a n e f e r m e n t a t i o n w a s a b o u t 6 5 # l / li t re p e r d a y ( F ig . 2).

L i g h t - m i c r o s c o p i c o b s e r v a t i o n s s h o w e d t h a t w h e n 6 0/1 1 o f p e e l o il /l it re

p e r d a y w a s a d d e d t o t h e s l u d g e , G r a m - n e g a t i v e r o d s ( c. 2 x 0 "3 /~ m ) p r e s e n ti n t h e p e e l o i l - fr e e s l u d g e d i s a p p e a r e d a n d G r a m - p o s i t i v e r o d s ( c. 3 x 0 "6 /~ m )

a p p e a r e d . F e w e r m i c r o - o r g a n i s m s w e r e o b s e r v e d i n t h e s l u d g e w i t h 7 0 /A o f

pee l o i l / l i t r e pe r day .

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164 E. M izuk i, T. Ak ao, T. Saruwatari

i I i

20G

Ec_o

, ~ 1 0 CP

r ,0

A' ;o ' 2'o ' '0

Time (dQy)

8.0

p H 7 .0

6 .0

5.0

Bi i i

0 10 20 30

T i m e ( d a y )

Fig. 1. Mesophilic methane fermentation of C. unshu peel. (A) Time course of gas

product ion. (B) Time course o f pH of sludge. Loads are 0"5 g/litre per day (O) , 1"0 g/litre per

day (I-q), 2"0g/iitre per day (A), 4.0g/litre per day (0 ) and 2g (pectin)/litre per day (A).

T A B L E 1

Effect of Peel Oil on Methane Fermentationa

Lo ad o f Colour Volume Gas composition (%)c Residual

pee l o i l o f o f pee l o i l in

(Id/litre per day) sludge sludge (%)b CH 4 CO z sludge (l~l/litre)

0 Normal 45'5 48"4 51'6 0"0

60 Nor mal 37.5 48.5 51.5 47-7

70 Brown 48.0 26-8 73.2 394"2

° Measured 50 days after the start of fermentation.

b The per cent (v/v) of sludge after cent rifugati on for 10 min at 3000 rpm.

CH4 + CO2 = 100%.

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Inhibition o [ digest ion by citrus peel 16 5

"2-

I~ 200

u

1:}o I 0 0

13.

m

A

0 1 ' 0 2 ' 0 3 ' 0 ~ 0 - - 0

T i m e ( d a y )

8 .0

7 .0

pH

6 ,0

5 .0

B

0 10 20 30 ~I0 50

Time (day )

F ig . 2 . I n h i b i t i o n o f m e t ha n e f e r m e n t a t i o n b y p e e l o i l. ( A ) T i m e c o u rs e o f g as p r o d u c t io n .

(B ) T i m e c o u r s e o f p H o f s lu d g e . L o a d s o f p e e l o i l a r e 0 / d / l i t r e p e r d a y ( © ) , 6 0 id / l i t re p er d ay

( O ) , 7 0 / d / l i t r e p e r d a y ( m ) , 8 0 # l / l i tr e p e r d a y ( [ ] ) , 9 0 iLl / l i tre per day (&) . Load of [ ) - l i m o n e n e

i s 82"3/A/l it re p er d ay (A ) . Loa d s o f p ec t in are 2 g / l i t re p er d ay in a l l cases .

T a b l e 1 s u m m a r i z e s t h e re s u lt s o b t a i n e d 5 0 d a y s a f t e r t h e o n s et o f

f e r m e n t a t i o n . I n t h e d i g e s t i o n f e d w i t h 6 0 # 1 o f p e e l o i l / l i t r e p e r d a y , t h e

v o l u m e o f s lu d g e (3 7" 5 % ) w a s l es s t h a n t h a t i n t h e d i g e s t i o n w i t h o u t p e e l o il .

G a s y i e l d w a s a b o u t 1 0% g r ea t er th a n t h a t o f t h e d i g e s t i o n w i t h o u t p e e l oi l.

A m o u n t o f r e s id u a l p e e l o i l w a s 4 7 .7 /~ l /l it re . T h e c o n c e n t r a t i o n o f m e t h a n e

i n t h e d i g e s t e r g a s e s w a s b e l o w 3 0 % , a n d p e e l o i l a c c u m u l a t e d u p t o

3 94 .2 / d / l i tr e , in t h e d ig e s t ion w i t h 70 / d o f p e e l o i l /l i tr e p e r d ay (Tab le 1).

An ae r ob ic d ige s t ion o f C. unshu p e e l a f t e r t h e r e mov a l o f p e e l o i l

F i g u r e 3 sh o w s t h e r e m o v a l o f p e e l o i l f r o m t h e sl u rr y o f C. unshu b y

a e ra t io n . A e r a t i o n f o r 1 2 h r e m o v e d 9 9 % o f th e p e e l o il . M o r e t h a n 9 9 % o f

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166 E. Mizuki , T . Akao , T . Saruwatar i

1 0 0 - -- -- (3 -~

fE

I1)L

5O

I1)

F i g . 3 . R e m o v a l o f p e e l o i l f r o m s lu r ry o f C . ~'

unshu p e el. P ee l w a s c o m m i n u t e d f o r 1 0 m i n a n d

h o m o g e n i z e d f o r 2 0 r a i n . T h e s l u r r y o f p e e l w a s

t h e n i n c u b a t ed in a n o p e n - t o p p e d f e rm e n t er a t 0

30°C with a ir spa rging (15 l i tres /1 .5 l itres feed stock o 6 1'2p e r m i n) . T i m e ( h r )

t h e p e e l o il w a s a l s o r e m o v e d b y s t e a m d i s t il l a t io n f o r 4 0 m i n . N o i n h i b i t i o n

o f f e r m e n t a t i o n w a s o b s e r v e d o v e r 4 4 d a y s i n t h e d i g e s t i o n s f e d w i t h o i l-

r e m o v e d p e e l ( F i g . 4 ) .

D I S C U S S I O N

T h i s r e p o r t d o c u m e n t s t h e f i r s t o b s e r v a t i o n t h a t C . u n s h u p e e l c a u s e s

s i g n i fi c a n t i n h i b i t i o n o f a n a e r o b i c d i g e s ti o n . S e v e r a l i n v e s t i g a t o r s ( M c N a r y

e t a l . , 1 9 51 ; L a n e , 1 9 8 0) h a v e r e p o r t e d t h a t i n h i b i t i o n o f a n a e r o b i c d i g e s t i o n

i

Bv

o

L.,

~ ' 1 0 0+ 11'0 2tO 3ro ~ '0

T i m e ( d a y )

F i g . 4 . A n a e r o b i c d i g e s t i on o f C. unshu pee l a f ter rem ova l o f pee l o i l. Pee l oi l wa s rem ove d

from feeds to cks by aera t ion (O ) a s show n in F ig . 3 or by steam d i s t i ll a t ion ( /X) . T h e loads o f

organic substances were 2 .0 g / l itre p er day .

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Inhibition o f digestion t5)' citrus peel 167

f e d w i t h c i t r u s w a s t e s w a s m a i n l y d u e t o p e e l o i l . I n o u r p r e s e n t s t u d y ,

C. unshu p e e l o il a ls o i n h i b i t e d t h e a n a e r o b i c d i g e s t i o n . T h e l i m i t o f p e e l oi l

loa d in g (c. 65 # l / l i tr e pe r day ) in th i s s tud y w as le s s tha n tha t (88-2/~l /li tr e pe r

d a y ) r e p o r t e d b y L a n e ( 1 9 8 4 ) .

I n a l l e x p e r i m e n t s , d i g e s t io n w a s s a id t o h a v e f a i le d w h e n t h e p H o f t h e

s ludg e fe l l to 6 .4 (Lane , 1980 , 1984). The d ig e s t ion w i th 70/~1 o f pee l o i l / l i t r e

pe r d ay , eq u iv a len t to the pee l o i l co n te n t o f 2 g (d .w .) o f pee l , f a i l ed in 46

d a y s a f t e r t h e s t a r t o f f e r m e n t a t i o n . S i n c e t h e d i g e s t i o n f e d w i t h 2 g o f p e el

( d .w . ) /l it re p e r d a y f a il e d i n 8 d a y s , it i s l i k e ly t h a t o t h e r s u b s t a n c e s p r e s e n t i n

C. unshu p e e l a l s o c a u s e d i n h i b i t i o n o f th e a n a e r o b i c p r o c e s s ( F ig s 1 a n d 2). A

d i g e s t i o n t o w h i c h w a s a d d e d 8 2 - 3 / A o - l i m o n e n e / l i t r e p e r d a y f a i l e d i n

4 3 d a y s . I n t e r e s t i n g l y , h o w e v e r , a d i g e s t i o n f e d w i t h 9 0 ~1 p e e l oi l c o n t a i n i n g

8 2 " 3 pl o f D - l i m o n e n e f a il e d i n 33 d a y s . T h i s s u g g e s t s t h a t t h e o t h e r

c o m p o n e n t s c o n t a i n e d i n p e el o il a ls o h a v e a n i n h i b i t o r y e f fe ct ( F ig . 2). T h e s e

o b s e r v a t i o n s a r e i n a g r e e m e n t w i t h e a r l i e r f i n d i n g s r e p o r t e d b y L a n e (1 98 0).

T h e a d d i t i o n o f 6 0 /A o f p e e l o i l/ l it r e p e r d a y t o t h e d i g e s t e r r e s u l t e d i n a

s u b s t a n t i a l c h a n g e i n t h e m i c r o b i a l f l o r a , f o l l o w e d b y a g a s p r o d u c t i o n

g r e a t e r t h a n t h a t i n t h e c o n t r o l ( w i t h o u t p e e l oi l) ( F ig . 2 (A ) ) . I n t h i s c a se , a

s m a l l a m o u n t o f r es i d u a l p e el o il w a s d e t e c t e d a t t h e e n d o f th e t e st p e r i o d

( T a b l e 1 ) . T h e s e r e s u l t s s u g g e s t t h a t m i c r o - o r g a n i s m s i n t h e s l u d g e

d e g r a d a t e d p e e l o i l t o s o m e e x t e n t , a n d t h e m i c r o b i a l f l o r a c h a n g e d t op r o d u c e g a s e s a t h i g h e r r a t e s a f t e r t h e a d d i t i o n o f p e e l o i l b e l o w t h e l i m i t

l o a d i n g .

T h e r e a r e s o m e r e p o r t s o n t h e r e m o v a l o f p e e l o il f r o m c i t r u s w a s te s b y

a e r a t i o n ( W o l f o rd et al., 1952 ; Lan e , 1980). In the p re sen t w ork , pee l o i l f rom

a s l u r r y o f C. unshu p e e l c o u l d b e s u c c e s s fu l l y r e m o v e d b y s t e a m d i s t i l l a t io n

o r a e r a t i o n ( F i g . 3 ) . D i g e s t i o n s f e d w i t h o i l - f r e e p e e l s l u r r y p r o v e d n o r m a l

( F i g . 4 ) . I t a p p e a r e d t h a t a n a e r o b i c d i g e s t i o n o f C. unshu p e e l w a s a b l e t o

p r o c e e d w h e n p e e l oil w a s r e m o v e d f r o m t h e p e el b y a p p r o p r i a t e m e t h o d s .

A p i l o t - s c a l e a n a e r o b i c d i g e s t i o n e x p e r i m e n t i s n o w i n p r o g r e s s t oe s t a b l i s h a p r a c t i c a l m e t h o d f o r a n a e r o b i c t r e a t m e n t o f C. unshu peel.

A C K N O W L E D G E M E N T

T h e a u t h o r s a c k n o w l e d g e D r S. M u r a o a n d D r M . O h b a f o r t h e ir r e vi ew o f

t h e m a n u s c r i p t a n d f o r u s e f u l d i s c u s s i o n s a n d s u g g e s t i o n s .

R E F E R E N C E S

Lane, A. G. (1980). Pro du ction of arom atic acids du ring an aerob ic digestion ofcitrus peel. J. Chem. Tech. Biotechnol., 30, 345 50.

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168 E. Mizuki, T. Akao, T. Saruwatari

Lane , A . G. (1983a). R em ov al o f pee l o i l f rom c i t rus pee l pres s l iquors b efor ea na e rob i c d i ge s t i on . Environ. Technol . Let t . , 4, 65-72.

Lane , A . G. (1983b). P re t rea tm ent of c it rus pee l pres s l iquor b efore anae rob ic

diges t ion . Environ. TechnoL Let t . , 4, 73-8.La ne , A . G . (1984). A n a e ro b i c d i ge s t ion o f o r a ng e pee l. Food Technol . Aust . , 36 ,

125-7 .M c N a ry , R . R ., W ol fo rd , R . W . & P a t t on , V . D . (1951). Expe r i me n t a l t r e a t me n t o f

c i t rus was te wate r . Food Techno l . , 5, 319-23.Scot t , W. C . & Veldhuis , M. K. (1966) . Ra pid es t im at ion of recovera ble o il in c i t rus

j u i c e s by b rom a t e t it r a ti on . J . A s s o c . O f f . A n a l C h e m . , 49, 623-33.W ol fo rd , R . W . , P a t t on , V . D . & M c N a ry , R . R . ( 1952) . A m e t hod fo r r e mova l o f pe e l

o i l f rom c i t rus ju ices and process l iquids . Food TechnoL, 6, 418-21.