project on treatment of dye by hydro-dynamic cavitation process
TRANSCRIPT
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Waste Water Treatment Of Dyes By Hydrodynamic Cavitation Process
Chapter 1
Introduction
1.1 Water a precious resource
Water covers about 71% of the Earths surface! and is vita" for a"" #no$nforms of "ife On Earth!
&7 % of the '"anets $ater is found in oceans! 17% in(round$ater! 17% in ("aciers and the ice
ca's of )ntarctica and *reen"and! a sma""fraction in other "ar(e $ater bodies On"y +,% of the
Earths $ater is fresh $ater! and&--% of that $ater is in ice and (round$ater .ess than /0% of
a"" fresh$ater is inrivers! "a#es! and the atmos'hereafe drin#in( $ater is essentia" to humans
and other "ivin( "ife Water is the#ey to "ife2 a crucia" resource for humanity and the rest of the
"ivin( $or"d Everyoneneeds it and not 3ust for drin#in( ociety uses $ater to (enerate and
sustainedeconomic (ro$th and 'ros'erity! throu(h activities such as farmin(! commercia"fishin(!
ener(y 'roduction! manufacturin(! trans'ort and tourism The mostcha""en(in( 'rob"em in
todays $or"d is mana(in( the su''"y and avai"abi"ity of safedrin#in( $ater for a"" human and
"ivin( creatures on this earth Water scarcity hasemer(ed as a 'rominent issue for communities
across the country 4ear"y everyre(ion of the country has e5'erienced $ater shorta(es in the "ast
five years Watersu''"ies have decreased due to the dryin( u' of streams! the dec"ine of
(round$ater"eve"s because of over 'um'in(! contamination of $ater resources! and an increase
in drou(ht conditions caused by c"imate chan(e The increase in human 'o'u"ation!6rbaniation
and ever8increasin( industria"iation causes de'"etion and contamination of our 'recious $ater
resources The society is "ess concerned about the conservationand 'rotection of our $ater body
from bein( 'o""uted Each year more than fivemi""ion 'eo'"e die from $ater8re"ated disease and
around one bi""ion 'eo'"e do nothave accesses to safe drin#in( $ater and sti"" $e are
deterioratin( this 'recious natura"resource On"y 1% of the tota" fresh $ater on the earth is
avai"ab"e for drin#in( 'ur'ose throu(h the different $ater bodies such as river! "a#es! 'ond etc
Des'ite thisfact that the $or"ds 'o'u"ation is (ro$in( by rou(h"y -/ mi""ion 'eo'"e each
yearand demand for fresh$ater is increasin( by 9: bi""ion cubic meters a year $e are 'o""utin(
this on"y avai"ab"e ;1%< form of $ater by contaminatin( this $ith $aste
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1.2 Water availability and use in India
=ndia accounts for +:,% of "and area and :% of $ater resources of the $or"d but re'resents 19%
of the $or"d 'o'u"ation Tota" uti"iab"e $ater resource in thecountry has been estimated to be
about 11+0 bi""ion cubic meter ;BC>< ;9&/ BC>from surface and :00 BC> from (round
$hich is 3ust +-% of the $ater derivedfrom 'reci'itation )bout -,% ;9-- BC>< of $ater usa(e
is bein( diverted forirri(ation! $hich may increase to 1/7+ BC> by +/,/ >a3or source for
irri(ation is(round$ater )nnua" (round$ater rechar(e is about :00 BC> of $hich +1+,
BC>is used for irri(ation and 1-1 BC> for domestic and industria" use ;C*WB! +/11
further reduce to 10:1 m0 in+/+, and11:/ m0 in +/,/ Hence! there is an ur(ent need for
efficient $ater resourcemana(ement throu(h enhanced $ater use efficiency and $aste $ater
recyc"in(
1.3 Water pollution
When to5ic substances enter "a#es! streams! rivers! oceans! and other $aterBodies! they (et
disso"ved or remain sus'ended in $ater or (et de'osited on the bed This resu"ts in the 'o""ution
of $ater $hereby the ?ua"ity of the $ater deteriorates!affectin( a?uatic ecosystems Po""utants
can a"so see' do$n and affect the(round$ater de'osits
Water 'o""ution has many sources The most 'o""utin( of them are the citye$a(e and industria"
$aste dischar(ed into the rivers The effects of $ater 'o""utionare not on"y devastatin( to 'eo'"e
but a"so to anima"s! fish! and birds Po""uted $ateris unsuitab"e for drin#in(! recreation!
a(ricu"ture! and industry =t diminishes theaesthetic ?ua"ity of "a#es and rivers >ore serious"y!
contaminated $ater destroys a?uatic "ife and reduces its re'roductive abi"ity Eventua""y! it is a
haard to humanhea"th 4obody can esca'e the effects of $ater 'o""ution
1.4 Wastewater Treatment Technologies
Waste$ater Treatment P"ant is a faci"ity desi(ned to receive the $aste fromdomestic!
commercia"! and industria" sources and to remove materia"s that dama(e$ater ?ua"ity and
com'romise 'ub"ic hea"th and safety $hen dischar(ed into $aterreceivin( systems The 'rinci'a"
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ob3ective of $aste$ater treatment is (enera""y toa""o$ domestic and industria" eff"uents to be
dis'osed off $ithout dan(er to humanhea"th or unacce'tab"e dama(e to the natura"
environment>ethods of treatment in $hich the a''"ication of 'hysica" forces 'redominateare
#no$n as unit o'erations. >ethod of treatment in $hich the remova" ofcontaminants is brou(ht
about by chemica" or bio"o(ica" reactions are #no$n as a unit'rocesses. )t the 'resent time! unit
o'erations and 'rocesses are (rou'ed to(ether to'rovide various "eve"s of treatment #no$n as
're"iminary! 'rimary! advanced 'rimary!secondary ;$ithout or $ith nutrient remova"< and
advanced ;or tertiary< treatment ;seeTab"e 1+etca"f A Eddy!:thed
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1.5 Cavitation
Cavitation is defined as the 'henomena of the formation! (ro$th andubse?uent co""a'se of
micro bubb"es or cavities occurrin( in e5treme"y sma"" interva" of time ;mi""iseconds< and at
mu"ti'"e "actations in the reactor! re"easin( "ar(e >a(nitudes of ener(y The effects of cavity
co""a'se are! creation of hot s'ots!re"easin( hi(h"y reactive free radica"s! c"eanin( of so"id
surfaces! and enhancement = mass transfer rates The co""a'se of bubb"es (enerates "oca"ied
hot s'ots $ithtransient tem'erature of about 1/!/// ! 'ressures of about +/// atm ;Diden#o
et a"1&&&
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*o(ate! +/1+any researchers have re'orted that u"trasonic irradiation 'rocess $as ca'ab"e
of de(radin( Farious reca"citrant or(anic com'ounds such as 'heno" com'ounds! ch"oroaromatic
Com'ounds! a?ueous carbon tetrach"oride! 'esticides! herbicides! benene com'ounds!
'o"ycyc"ic aromatic hydrocarbons and or(anic dyes The fre?uency of u"trasound! irradiatin(
surface! intensity of sound $ave! ca"orimetric efficiency of u"trasonic E?ui'ment ;'o$er
dissi'ated into the system 'er unit 'o$er su''"ied
medium and the 'resence of air and so"id Partic"es are the im'ortant 'arameters $hich affects the
cavitationa" efficiency o )coustic cavitationa" reactor
1.5.2 !ydrodynamic cavitation
One of the a"ternative techni?ues for the (eneration of cavitation is the use of hydrau"ic devices
$here cavitation is (enerated by the 'assa(e of the "i?uid throu(h Constriction such as va"ve!
orifice '"ate! venturi etc ;*o(ate and Pandit! +///I enthi"umar and Pandit! 1&&&I >oho"#ar et
a"! 1&&&I *o(ate and Pandit! +//,I >oho"#ar and Pandit! +//1
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Chapter 2
"iterature #urvey
2.1 Introduction
Waste$ater treatment ;WWTP< has deve"o'ed a "ot over the "ast fe$ decades
@rom a sma"" system! it has become a hu(e industry no$ The most common method to treat the
$aste$ater is the activated s"ud(e 'rocess! $here treatment is done by uti"iin( different
microor(anisms under different o'eratin( conditions )"thou(h a si(nificant im'rovement has
been achieved in $aste$ater treatment! sti"" the (eneration of s"ud(e or bioso"ids has remained
'rob"ematic Primary and secondary c"arification is the t$o unit o'erations $hich (enerate
s"ud(e in a $aste$ater treatment '"ant "ud(e recovered from the 'rimary c"arifier is ty'ica""y
readi"y de(radab"e com'ared to the secondary s"ud(e (enerated from biomass $hich is more
resistant to de(radation ) si(nificant 'ortion of money is s'ent to treat and dis'ose of this
s"ud(e =n WWTPs
To reduce the amount of s"ud(e as $e"" as to im'rove the s"ud(e ?ua"ity! different disinte(ration
techno"o(ies have been a''"ied in the s"ud(e treatment 'rocess Disinte(ration techno"o(ies he"'
to fra(ment the ce"" $a"" and re"ease the intrace""u"ar com'ounds by the a''"ication of different
'hysica" or chemica" methods Disinte(rated s"ud(e can be used in both aerobic and anaerobic
bio"o(ica" 'rocesses as a substrate Disinte(rated s"ud(e can be further treated in one of the
fo""o$in( $ays
)naerobic di(estion can be im'roved as $e"" as acce"erated by first a''"yin( disinte(ration to
$aste s"ud(e Disinte(ration he"'s to acce"erate the hydro"ysis 'rocess by disru'tin( the ce""
$a""s and re"easin( the or(anic matter inside the ce""! $hich is the "imitin( ste' in the di(estion
'rocess Disinte(rated s"ud(e im'roves biomass 'roduction in an anaerobic di(estion 'rocess
and it im'roves 'hos'horus recovery and the nutrient remova" 'rocesses by transferrin( the
activated s"ud(e so"ids into the "i?uid 'hase=n a $aste$ater nitro(en remova" treatment 'rocess!
disinte(rated s"ud(e can be used as a source of carbon for (entrification
Disinte(rated s"ud(e can be a''"ied to reduce s"ud(e bu"#in( and foamin( in an activated s"ud(e
Treatment 'rocess by brea#in( u' the fi"amentous structure and "ar(er f"oc#s ome of the
common disinte(ration 'rocesses are (iven in Tab"e 1 )"" the methods have been deve"o'ed $ith
a common (oa" to achieve 'artia" or com'"ete "ysis of the ce""! $hich means the destruction and
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re"ease of the or(anic matter inside in the bacteria" ce"" E5trace""u"ar 'o"ymeric substances may
a"so be de(raded by these disinte(ration techni?ues
Tab"e 1 Different methods of disinte(ration ;,ore $or# needs to be done to find out the behavior of this instrument under
hi(h fre?uency and hi(h dissi'ation conditions Hi(her fre?uencies of o'eration are suitab"e for
the destruction of 'o""utants u' to an o'timum va"ue $hich de'ends on the characteristics of the
'o""utant Fery fe$ investi(ations have been made on the destruction of 'o""utants usin( hi(her
fre?uencies as its difficu"t to o'erate at fre?uencies (reater than +// #H unnin( a sono
chemica" reactor at hi(her fre?uencies in continuous o'eration at a "ar(er sca"e is difficu"t as it
causes erosion of the transducer surface Po$er re?uirement increases $ith fre?uency and this
can ma#e the 'rocess uneconomica" due to the fact that a "ar(e amount of su''"ied ener(y $i"" be
used on"y for the (eneration of the cavities >u"ti'"e fre?uencies 'roduce more intense cavitation
than sin("e fre?uency o'eration and resu"ts in hi(her yie"d of transformation but $ith minima"
'rob"ems of o'eration With an increase in cavitationa" activity! "ar(er vo"umes of eff"uent can be
treated effective"y 6"trasonic 'robes $ith hi(her irradiatin( surface areas are more ener(y
efficient as they ensure the uniform dissi'ation of ener(y;-achnic#a et a" combined hydrodynamic cavitation $ith anaerobic
di(estion and sho$ed that bio(as 'roduction increased u' to 101% $ith the addition of 0/% of
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vo"ume disinte(rated s"ud(e in the fermentation 'rocess They used a 1+ mm no"e for the
(eneration of cavitation =t $as a"so re'orted that so"ub"e COD increased by +-: m(G. after
a''"ication of cavitation for &/ minutes! sho$in( evidence that the or(anic matter and 'o"ymer
in the activated s"ud(e $as transferred from the so"id 'hase to the "i?uid 'hase Hydrodynamic
cavitation $as sho$n to im'rove 'hos'horus remova" and recovery in the form of struvite by
so"ubi"iin( 'hos'horus and ammonium nitro(en! as $e"" as 'otassium! ma(nesium and ca"cium
cations from the so"id 'hase to the "i?uid imi"ar resu"ts $ere obtained $hen this techno"o(y
$as a''"ied to the foam co""ected from a fu"" sca"e enhanced bio"o(ica" nutrient treatment
remova" '"ant Huan( et a" demonstrated that de$ater abi"ity of s"ud(e can be im'roved by
a''"yin( hydrodynamic cavitation;1-artin and *a"ey used static
mi5ers in their study and observed an increasin( mass transfer coefficient $ith decreasin( $ater
f"o$ rate and increasin( (as f"o$ rate =t has a"so been that oone transfer efficiency in static
mi5ers increases $ith an increase in the 'ressure dro' or a decrease in (asG"i?uid ratio and that
transfer is inde'endent of oone "oadin( )s static mi5ers are not used fre?uent"y $ith
$aste$ater! more studies are re?uired to ca"cu"ate the ener(y re?uirement! as the 'ressure dro'
$ou"d be hi(her due to the sus'ended so"ids and other eff"uent 'ro'erties com'ared to $ater
containin( microor(anisms
Tab"e : o"ubi"ity of oone and o5y(en in $ater
2.4.2 -one in water treatment
Oone is used for the treatment of $aste$ater as $e"" as for the disinfection of $ater )s a
'o$erfu" o5idant! oone is used to o5idie a variety of contaminants 'resent in $ater and
$aste$ater ome of the a''"ications of oone in $ater treatment are "isted in Tab"e , Oone is
a"so used to increase the biode(radabi"ity of or(anic com'ounds =n $aste$ater treatment '"ants
oone can be used as a 're8treatment before the bio8di(estion and a"so can be used in the recyc"e
"oo' to reduce the overa"" s"ud(e 'roduction in the '"ant;++ost of the studies $ere focused on thede(radation of different 'o""utants
usin( sin("e or mu"ti'"e ho"e orifice '"ates andsyner(etic effect of hydrodynamic cavitation and
other additives 4o studies havebeen found on the com'arison of venturies of different sha'es
and orifice '"ate andthe subse?uent effect of the cavitatin( device on the de(radation #inetics
)sdiscussed ear"ier the (eometry of a cavitatin( device has a stron( inf"uence on theentire
cavitation ;ince'tion! (ro$th and co""a'se< behaviours The C@D ana"ysis byBashir et a" ;+/11oyno 00+! \ h'! +/- F)C
contro""ed The sam'"es $ere co""ected from the tan# and du'"icate measurements $ere made for
a"" the sam'"es;+:ethods ,01/ B ;)PH) et a"! +//,< by usin( a =.
,,/ TOC8T4 ana"yer ;C)
=n case of the sam'"es ta#en after &/ minutes! 0 m. and , m. of fi"tered sam'"e $ere used to
measure the BOD,
4.4.4 /iodegradable C*
) sim'"e batch reactor $as used to determine the readi"y biode(radab"e COD as i""ustrated in
@i(ure & )n Er"enmeyer f"as# of 1 . vo"ume $as used as a reactor )ir $as su''"ied
continuous"y by usin( a sma"" tube at the bottom of the f"as# and a ma(netic stir '"ate and stir bar
$ere used to #ee' the contents of the reactor in sus'ension The $ater "oss due to eva'oration
$as accounted for and re'"aced by disti""ed $ater The e5'eriment $as o'erated at room
tem'erature The sides of the reactor and aeration tubin( $ere c"eaned re(u"ar"y by usin( a bott"e
brush to ensure the sus'ension of biomass in the reactor am'"es co""ected initia""y and after &/
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minutes of a''"ication of oone8hydrodynamic cavitation $ere assessed for so"ub"e
biode(radab"e COD =n both cases! +// m. of fi"tered sam'"e $ere ta#en from the reactor and
then + m. of activated s"ud(e from the 'i"ot '"ant $as added Phos'hate buffer $as added to
both reactors to maintain the 'H around 7/ =nitia" so"ub"e COD $as measured am'"es $ere
ta#en from the reactor and so"ub"e COD $as measured unti" the so"ub"e COD stabi"ied in the
reactor ;1,8+/
a"so have a critica" inf"uence on a?uatic biota! and every #ind of or(anism has a ty'ica" sa"inity
ran(e that it can to"erate >oreover! the ionic com'osition of the $ater can be critica" @or
e5am'"e! c"adocerans ;$ater f"eas< are far more sensitive to 'otassium ch"oride than sodium
ch"oride at the same concentration Conductivity $i"" vary $ith $ater source2 (round $ater!
$ater drained from a(ricu"tura" fie"ds! munici'a" $aste $ater! rainfa"" Therefore! conductivity
can indicate (round$ater see'a(e or a se$a(e "ea# Conductivity is measured by a 'robe! $hich
a''"ies vo"ta(e bet$een t$o e"ectrodes The dro' in vo"ta(e is used to measure the resistance of
the $ater! $hich is then converted to conductivity Conductivity is reci'roca" to resistance and is
measured in the amount of conductance over a certain distance The conductivity unit has been
ca""ed ^mho_ because it is the inverse of ^ohm_! the resistance unitThe basic unit is mhoGcm!
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other$ise #no$n as 1 iemenWe have ta#en the resu"ts for above terms and discussed the
re"ation of resu"ts to our 'ro3ect to'ic These discussion is made in fo""o$in( cha'ter
Chapter 5
esults and *iscussion
5.1 Introduction
=n this cha'ter e5'erimenta" resu"ts are 'resented! com'ared and discussed for 're8treatment ie!
cavitation )''"icabi"ity of the disinte(rated s"ud(e is a"so discussed
+ercentage o% %ree area %or the %low
To ?uantify the effect of free area on the cavitation intensity a 'arameter ca""ed
is introduced $hich is the ratio of the tota" 'erimeter of the ho"e to the tota" area of the o'enin(
Q Tota" 'erimeter of the ho"es G Tota" area of o'enin(
Q n R +S ;dhG+< G ;dhG+
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simi"ar trend for iodine "iberation! e5ce't $ith a different order of ma(nitude This $as due to
the fact that a hi(her va"ue of co""a'se 'ressure is re?uired forrhodamine B de(radation
com'ared to the decom'osition of = =t $as a"so observed that a '"ate $ith a "ar(er number of
ho"es 'roduced a hi(her rate of de(radation $ith the same va"ue!$hich $as a"so confirmed by
umar in a bubb"e dynamics mode" On the other hand cavity co""a'se 'ressure decreased $ith
an increase of free f"o$ area Thus for a certain f"o$ area! an orifice '"ate $ith a "ar(er number
of ho"es $ith a sma"" diameter $i"" (ive a better cavitation effect! as a "ar(er number of cavities
e5'eriences hi(her turbu"ence due to the increase of shear "ayer;19oreover the cavitation number ;CF< $as
ca"cu"ated from the e?uation +1 Cavitation (enera""y occurs at CvN1 The cavitation numbers
ca"cu"ated for the in"et 'ressures of 0, 'si $as /,:indicatin( the stron( "i#e"ihood that cavitation
$as occurrin( @or both ca"cu"ations! atmos'heric 'ressure $as ta#en as recovered 'ressure
5.3 Chemical Aygen *emand (C*)&
o"ubi"isation of s"ud(e $as assessed in terms of the (eneration of so"ub"e COD ;COD
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indicated that the tota" COD of the s"ud(e $as a''ro5imate"y 17// m(G. $hich means that after
about + hours of treatment! ,/% of the s"ud(e $as so"ubi"ised
TIMEplate1mm
plate2mm
plate 1mm 5!le
plate 2mm5 !le
0 1500 1500 1500 150030 1445 1458 1456 146660 1220 1330 1340 1345
90 1032 1038 1046 1058
120 867 873 888 909
Tab"e 72 COD F Time
0 20 40 60 80 100 120 140
850
950
1050
1150
1250
1350
1450
1550
plate 1mm plate 2mm plate 1mm 5 !le plate 2mm 5 !le "#E$%
"#E$% "#E$% "#E$%
time
COD
@i(ure -2 Concentration of COD $ith in"et 'ressures in hydrodynamic cavitation treatment
Based on the concentration of COD obtained in the e5'eriments it can be conc"uded that (reater
so"ubi"isation of s"ud(e $as obtained in the combined a''"ication of oone and cavitation at
hi(her in"et 'ressure and a"so the rate of so"ubi"isation decreases $ith time
5.4 #oluble total organic carbon (TC)
The amount of or(anic matter re"eased by s"ud(e so"ubi"isation $as estimated by measurin(
so"ub"e TOC @i(ure 1& i""ustrates the amount of TOC re"eased for the combined! as $e"" as
individua" a''"ication of oone and cavitation in the short term e5'eriments On"y cavitation did
not 'roduce any si(nificant re"ease of so"ub"e TOC com'ared to the other treatments @i(ure +/
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i""ustrates the effect of in"et 'ressure on or(anic matter re"ease =t $as observed that after /
minutes of treatment! the TOC concentration $as about -&1- ''m usim( an in"et 'ressure of 0,
'a!for a"" '"ates! $hereas at after 1+/ min TOC concentration for /&, mm orifice '"ate $as
01:9''m $hich $as minimum as com'ared to other '"ates
)mon( a"" the '"ates a''"ied! the /&,mm orifice '"ate demonstrated the hi(hest re"ease of
or(anic carbon at the hi(her in"et 'ressure due to a hi(her rate of so"ubi"isation of the s"ud(e The
concentration of TOC continued to increase $ith time! indicatin( the re"ease of or(anic matter
due to the ce"" disru'tion
Tab"e -2 TOC vs time
0 5 10 15 20 25 30 35 40 450
10
20
30
40
50
60
70
80
90
100
plate 1mm plate 2mm plate 1mm &5 !le' plate 2mm &5 !le'
t(me
TOC
@i(ure &2 e"ease of so"ub"e tota" or(anic carbon usin( different disinte(ration conditions
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TIMEplate1mm
plate2mm
plate 1mm &5!le' plate 2mm &5 !le'
0 92.18 92.18 92.18 92.18
10 60.65 62.25 63.26 69.645
20 46.533 58.63 50.56 62.36
30 41.235 51.36 42.35 49.54
40 34.26 45.36 36.64 46.26
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5.5Total dissolved solids (T*#)&
The amount of disso"ved so"ids re"eased by s"ud(e so"ubi"isation $as estimated by measurin(
TD @i(ure 1& i""ustrates the amount of TD re"eased for the hydrodynamic cavitation in the
short term e5'eriments On"y cavitation did not 'roduce any si(nificant re"ease of so"ub"e TD
com'ared to the other treatments =t $as observed that after / minutes of treatment! the TD
concentration $as about 10&1- ''m usin( an in"et 'ressure of 0, 'si!for a"" '"ates! $hereas at
after 1+/ min TD concentration for /&, mm orifice '"ate $as &1:9''m $hich $as minimum
as com'ared to other '"ates
)mon( a"" the '"ates a''"ied! the /&,mm orifice '"ate demonstrated the hi(hest re"ease of
disso"ved so"ids at the hi(her in"et 'ressure due to a hi(her rate of so"ubi"isation of the s"ud(e
The concentration of TD continued to increase $ith time! indicatin( the re"ease of or(anic
matter due to the ce"" disru'tion
Tab"e &
TD F
T=>E
Dept. Of CHEMICAL Page 37
TIME plate 1mmplate2mm
plate 1mm &5!le')
plate 2mm &5!le'
0 138.43 138.43 138.43 138.43
10 96.43 97.15 98.23 98.6620 97.65 99.6 100.25 98.32
30 95.45 97.64 98.235 97.24
40 94.52 96.32 98.21 97.56
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0 10 20 30 40 50
plate 1mm plate 2mm plate 1mm &5 !le') plate 2mm &5 !le'
TIME
TDS
@i(ure 1/2 e"ease of tota" disso"ve so"ids usin( different disinte(ration conditions
5.B Conductivity&
Conductivity is measured by a 'robe! $hich a''"ies vo"ta(e bet$een t$o e"ectrodes The dro' in
vo"ta(e is used to measure the resistance of the $ater! $hich is then converted to conductivity
Conductivity is reci'roca" to resistance and is measured in the amount of conductance over a
certain distance =t $as observed that after / minutes of treatment! the conductivity $as about
++, sGsusim( an in"et 'ressure of 0, 'si! for a"" '"ates! $hereas at after 1+/ min conductivity
for /&, mm orifice '"ate $as 19,-, sGs $hich $as minimum as com'ared to other '"ates
)mon( a"" the '"ates a''"ied! the /&,mm orifice '"ate demonstrated the hi(hest re"ease ofdisso"ved so"ids at the hi(her in"et 'ressure due to a hi(her rate of so"ubi"isation of the s"ud(e
The concentration of conductivity continued to decrease $ith time! indicatin( the re"ease of
or(anic matter due to the ce"" disru'tion
5. Temperature and p!
The chan(es in tem'erature are i""ustrated in @i(ures 09 for different disinte(ration conditions
@rom @i(ure 09! a simi"ar tem'erature ;9,C in &/ minutes< increase $as observed for both the
combined a''"ication of oone and cavitation! and cavitation a"one This mi(ht be due to the
co""a'se of cavities $hich causes the increase of tem'erature ;Benito et a"! +//,
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TIMEplate1mm
plate2mm
plate 1mm &5!le'
plate 2mm &5!le'
0 31.5 31.5 31.5 31.5
20 41.3 40.4 39.2 39.6
40 49 47.23 47.54 48
60 53.5 50.4 53.65 54.32
Tab"e 11 tem'erature vs time
0 10 20 30 40 50 60 70
20
30
40
50
60
70
80
plate 1mm plate 2mm plate 1mm &5 !le' plate 2mm &5 !le'
t(me
Temp*at+*e
@i(ure 112 Chan(es in tem'erature for different diameters of orifice '"ate
5.D *iscussion
)"" the e5'eriments indicate that combined a''"ication of hydrodynamic cavitation and oone
resu"ted in better s"ud(e disinte(ration than did the individua" treatments This may be due to the
fo""o$in( reasons
Cavitation causes the dese(re(ation of f"ocs of microor(anisms >icroor(anisms 'resentin the
form of f"ocs may 'rotect the inner microor(anisms from contact $ith oone The cavitation
brea#s these f"ocs and e5'oses the inner microor(anisms to oone
Cavitation increases the 'enetration of oone mo"ecu"es to the microor(anisms by acce"eratin(
mass transfer
Cavitation can a"so increase the 'ermeabi"ity of the substances by brea#in( the chemica"
bonds bet$een the mo"ecu"ar substances
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The oone decom'osition and the activity of free radica"s may be increased due to the
cavitation 'rocess =n activated s"ud(e! bacteria" ce""s form macrof"ocs $ith sies ran(in( from
1// to 1,/ ]m as 'resented in @i(ure :+ These macrof"ocs are com'osed of microf"ocs! of sie
ran(in( from 1/81, ]m! $hich are main"y active ce""s entra''ed in a matri5 of e5o'o"ymer
Cavitation he"'s to brea# these f"ocs and to e5'ose the inner 'artic"es to oone! and this may
increase the oone activity a(ainst the s"ud(e Cavitation has been sho$n to increase the aeration
;.a< efficiency $hich resu"ts in intensified inter'hase mass transfer imi"ar"y! $ith oonation
more effective uti"iation of oone (as $ou"d be obtained ;Dah" et a"! 1&79
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5.E pplication o% disintegrated sludge
) ty'ica" set8u' of the activated s"ud(e bio"o(ica" nutrient remova" 'rocess is 'resented in @i(ure
+: The 'rocess is com'osed of anaerobic! ano5icGdenitrification! aerobic reactors to treat the
$aste$ater by usin( biomass @i(ure :0 i""ustrates the 'otentia" '"aces for the a''"ication of
s"ud(e disinte(ration $ith re(ards to the $aste$ater treatment and s"ud(e mana(ement
Disinte(rated s"ud(e can be returned to both interna" ;D< and e5terna" ;E< recircu"ation "ines in
the 'rocess to(ether $ith s"ud(e from the secondary sett"in( tan# to any of the anaerobic ;)
ano5ic ;B< aerobic ;C< reactors
@i(ure 102 Potentia" '"aces for addin( s"ud(e disinte(ration techno"o(y
=n the anaerobic one F@)s (enerated by fermentative bacteria! are ta#en u' by 'hos'horus
accumu"atin( bacteria ;P)O
nitrate remova" throu(h denitrification if there is a shorta(e of or(anic matter in the $aste$ater
f"o$in( into the recator =n the aerobic one it $i"" a"so he"' the 'hos'horus8accumu"atin(
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bacteria to re'roduce and easier co""ection of 'hos'horus and $i"" (uarantee their surviva"
sho$ed that the addition of disinte(rated s"ud(e to the ano5ic reactor cou"d 'rovide an effective
carbon source and it im'roved the nitro(en remova" efficiency by 1/% $ithout reducin( the
eff"uent ?ua"ity
=n the aerobic one! non8sett"in(! so"ub"e and co""oida" carbon com'ounds in $aste$ater are
metabo"ied by heterotro'hic microor(anisms The introduction of disinte(rated s"ud(e $i""
'rovide additiona" or(anic substrate that may contribute to faster bacteria" (ro$th $hich $i""
favor the deve"o'ment of feedin( fauna =t has been re'orted that the addition of disinte(rated
s"ud(e in the activated s"ud(e chamber did not "ead to the rea''earance of fi"amentous bacteria
Disinte(rated s"ud(e can a"so be cou'"ed to nutrient recovery! asstruvite due to the re"ease of
'hos'hate and ammonia The introduction of disinte(rated s"ud(e direct"y ;*< or $ith thic#ened
activated s"ud(e ;@< to a fermenter $i"" im'rove the fermentation 'rocess The direct addition of
disinte(rated s"ud(e into the di(estion chamber $i"" he"' to increase the enymatic activity of the
fermentation 'rocess! $hich $i"" increase the bio(as 'roduction The disinte(ration 'rocess he"'s
to re"ease the intra and e5trace""u"ar enymes by ce"" "ysis and su''"ies the or(anic substrate to
bacteria" 'o'u"ation in more di(estib"e form
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Chapter B
Conclusions and ecommendations
=t has been conc"uded that hydrodynamic cavitation can be effective"y uti"iedfor the de(radation
of bio refractory 'o""utants This study sho$s that hydrodynamiccavitation has a 'otentia" of
a''"ication on an industria" sca"e! $hi"e its successfu" im'"ementation on an industria" sca"e
de'ends on severa" 'arameters such as (eometrica"! o'eratin( ;o'eratin( 'ressure and cavitation
number< and 'hysicochemica" 'ro'erties ;density! viscosity and 'H of the so"ution< of
$aste$ater to be treated The fo""o$in( conc"usion can be dra$n from this study
=t has been found that hydrodynamic cavitation is ca'ab"e of o5idiin( or(anic'o""utants and
further the efficiency can be enhanced by re(u"atin( o'eratin('arameters ;o'eratin( 'ressure and
cavitation number< and 'hysico8chemica"'ro'erties of the f"uid to be treated The studied carried
out in cha'ter + and 0indicates that in"et 'ressure and cavitation number are the t$o im'ortant
'arameters $hich affects the de(radation rate of dyes =t $as conc"uded that a moderate in"et'ressure ;, bar< is sufficient for o5idiin( or(anic com'ounds and the hydrodynamic cavitation
shou"d a"$ays be o'erated above the cho#ed cavitation condition;Cv Q /10< to (et the ma5imum
cavitationa" yie"d for the cavitatin( device studied in these $or#
=t has a"so been found that the efficiency of hydrodynamic cavitation isstron("y de'endent on the
o'eratin( 'H! state of mo"ecu"e ;$hether mo"ecu"ar or ionic< and nature ;hydro'hobic and
hydro'hi"ic< of the 'o""utant mo"ecu"e The syner(istic coefficient (reater than one indicates that
the combination ofhydrodynamic cavitation and H+O+ ;o5idiin( a(ent< (ives hi(her ener(y
efficiency and therefore combination is recommended instead of individua" 'rocesses to (et the
enhanced de(radation rate The com'arison of hydrodynamic cavitation and acoustic cavitation
sho$ed that hydrodynamic cavitation is more ener(y efficient than the acoustic cavitation and
a"most 10 times hi(her cavitationa" yie"d $as obtained in the case of hydrodynamic cavitation as
com'ared to acoustic cavitation The hi(her ener(y efficiency of hydrodynamic cavitation ma#es
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it a cost effective techno"o(y $hich has 'otentia" of sca"e u' on an industria" sca"eThe studied
carried out in cha'ter : indicates that the cavitation yie"d in the case of hydrodynamic cavitation
de'ends on the (eometrica" 'arameters of hydrodynamica""y cavitatin( device
The throat sie ;area and 'erimeter of throat
because considerin( on"y one 'arameter in the desi(n of a cavitatin( device $ou"d not resu"t in
the 'ossib"e o'timiation of a"" cavitationa" condition for the desired effects The treatment of
industria" eff"uent havin( bio refractory 'o""utants usin( hydrodynamic cavitation sho$ed that
hydrodynamic cavitation is ca'ab"e of reducin( 'o""utant concentration of such eff"uent u' to a
reusab"e "eve"
@urther the 'otentia" of hydrodynamic cavitation for an industria" a''"icationis e5'"ored throu(h
the successfu" treatment of disti""ery $aste$ater =t $as conc"uded that the hydrodynamic
cavitation is ca'ab"e of enhancin( the efficiency of conventiona" bio"o(ica" 'rocesses in terms of
reduction of to5icity as $e"" as increase in bio(as (eneration! a"on( $ith a si(nificant"y net
hi(her reduction in COD and co"or for the treatment of com'"e5 disti""ery $aste$ater Hence! it
can be conc"uded that the hydrodynamic cavitation can be effective"y uti"ied for the treatment of
com'"e5 bio refractory 'o""utants and can serve as a cost effective advance treatment
techni?ue$hich can be used as an individua" or in combination $ith other conventiona"treatment
'rocesses! such that the efficiency of conventiona" bio"o(ica" treatment
'rocesses in hand"in( the com'"e5 $aste$ater can be im'roved
B.1 Conclusions
The fo""o$in( conc"usions $ere made based on the resu"ts obtained from the 'resent study of
hydrodynamic cavitation for 'aint industry $aste $ater s"ud(e disinte(ration
@rom this 'ro3ect $e conc"ude that the $hen the diameter of orifice '"ate is as sma"" as
then better resu"t can be obtained
Hydrodynamic cavitation has hi(her ca'acity for s"ud(e disinte(ration than any oher
$aste$ater treatment techno"o(ies a''"ied a"one
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Within the o'eratin( conditions a''"ied! cavitation itse"f is not sufficient for the
disinte(ration of s"ud(e
) ma5imum of ,/% of the s"ud(e $as so"ubi"ised after + hours treatment=t $as a"so
observed that most of the s"ud(e $as so"ubi"ised $ithin the first + hours of treatment
B.2 ecommendations
=n our 'resent study $e have used an in"et 'ressure of 0, 'si at a f"o$ of , .'m for cavitation
$hich $as "o$ com'ared to the f"o$ and 'ressure a''"ied in other studies esearch shou"d be
conducted at hi(her in"et 'ressure to find out the fu"" 'otentia" of cavitation on s"ud(e
disinte(ration
=n our 'resent research $e used a different sies of orifice '"ates to (enerate the cavities Other
researchers have sho$n that mu"ti'"e ho"e orifices (ive better cavitationa" yie"d to de(rade =
and rhodamine B )"thou(h cavitation can be induced $ith sin("e or mu"ti'"e ho"e orifices! there
may be advanta(es in usin( a venturi for this 'ur'ose @urther research mi(ht be usefu" to assess
the effect of cavitation on s"ud(e disinte(ration by usin( different sets of orifices or a venturi
=n our 'resent research $e measured on"y the a''"ied oone concentration 4o measurements
$ere made of off8(as oone concentration To find out the actua" oone transfer efficiency it is
necessary to find out the amount of oone consumed by the s"ud(e in a certain 'eriod of time o
in the ne5t ste' of the research! off8(as oone concentration shou"d be considered to ?uantify the
increase in the oone transfer efficiency due to cavitation
=t $as assumed in severa" 'revious studies that cavitation re"eases hi(h"y reactive free radica"s!
but none of the studies actua""y ?uantified the radica" effects se'arate"y @urther research is
re?uired to find out the radica" effects of cavitation
@ina""y! a''"ication of hydrodynamic cavitation shou"d be a''"ied in a 'i"ot sca"e $aste$ater
treatment 'rocess and research is necessary to find out the behaviour of the 'rocess due to this
a''"ication
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C!+TF
eferences
1 )de$uyi! * ;+//1
;+//+
6"trasonics onochemistry! 1,;0
Enhanced anaerobic de(radation of mechanica""y disinte(rated s"ud(e Water cience and
Techno"o(y! 09;11
1/+1
11 Benito! ! )rro3o! ! Hau#e! *! Fida"! P! de Conceicao Cunha! > and Brebbia! C
;+//,
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1+ Hydrodynamic cavitation as a "o$8cost )OP for $aste$ater treatment2 Pre"iminary
resu"ts and a ne$ desi(n a''roach Water esources >ana(ement ===! ! :&,8,/:10 Berna"8>artine! )! Carrere! H! Patureau! D and De"(enes! V ;+//,
Techno"o(y!+-;-
1, Boeh"er! >! ie(rist! H! O"es#ie$ic! V! van .oosdrecht! >! E#ama! *! "a Vansen! V!
et a" ;+//9ana(ement in
Waste$ater Treatment Processes and ecyc"e treams e"ected Pa'ers from the =W)
=nternationa"Conference! He"d in ra#o$! Po"and! 1&8+1 e'tember +//, ! ,0 ;1+< ''
+/78+19 Bou(rier! C! )"basi! C! De"(enes! V and Carrere! H ;+//9
and economic as'ects The Canadian Vourna" of Chemica" En(ineerin(! ,1;0! Wu! L and Ondrusch#a! B ;+/1/
+/ Cata""o! W V and Vun#! T ;1&&,ana(ement! 1,;:
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++ Chu! . B! in(! H! u! ) @! Lhou! 4! un! . and Vurci#! B ;+//7