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Substrates emulsification process to improve lipase-catalyzed sardine oil glycerolysis in different systems. Evaluation of lipid oxidation of the reaction products

García Solaesa, Ángela,Sanz Díez, Mª Teresa,Melgosa Gómez, Rodrigo,Beltrán Calvo, Sagrario

Abstract

European Regional Development Fund (ERDF) and Junta de Castilla y León [grant number BU055U16] for financial support. AGS acknowledges University of Burgos and RM MINECO [grant number BES-2013-063937] for their pre-doctoral contracts.

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Accep ed Manusc ip Subs a es emulsi ica ion p ocess o imp o e lipase-ca alyzed sa dine oil glyce olysis in di e en sys ems. E alua ion o lipid oxida ion o he eac ion p oduc s Ángela Ga cía Solaesa, Ma ía Te esa Sanz, Rod igo Melgosa, Sag a io Bel án PII: S0963-9969(17)30370-8 DOI: doi: 10.1016/j. ood es.2017.07.048 Re e ence: FRIN 6845 To appea in: Food Resea ch In e na ional Recei ed da e: 18 May 2017 Re ised da e: 18 July 2017 Accep ed da e: 19 July 2017 Please ci e his a icle as: Ángela Ga cía Solaesa, Ma ía Te esa Sanz, Rod igo Melgosa, Sag a io Bel án , Subs a es emulsi ica ion p ocess o imp o e lipase-ca alyzed sa dine oil glyce olysis in di e en sys ems. E alua ion o lipid oxida ion o he eac ion p oduc s, Food Resea ch In e na ional (2017), doi: 10.1016/j. ood es.2017.07.048 This is a PDF ile o an unedi ed manusc ip ha has been accep ed o publica ion. As a se ice o ou cus ome s we a e p o iding his ea ly e sion o he manusc ip . The manusc ip will unde go copyedi ing, ypese ing, and e iew o he esul ing p oo be o e i is published in i s inal o m. Please no e ha du ing he p oduc ion p ocess e o s may be disco e ed which could a ec he con en , and all legal disclaime s ha apply o he jou nal pe ain. ACCEPTED MANUSCRIPT 1 Subs a es emulsi ica ion p ocess o imp o e lipase-ca alyzed sa dine oil glyce olysis in di e en sys ems. E alua ion o lipid oxida ion o he eac ion p oduc s Ángela Ga cía Solaesa, Ma ía Te esa Sanz  , Rod igo Melgosa, Sag a io Bel án Depa men o Bio echnology and Food Science (Chemical Enginee ing Sec ion), Uni e si y o Bu gos, 09001 Bu gos. Spain Abs ac Mono- and diacylglyce ols ich in omega-3 ha e a g ea in e es due o hei good bioa ailabili y and oxida ion s abili y compa ed wi h o he kind o omega-3 concen a es. The main d awback in mono- and diacylglyce ols p oduc ion by glyce olysis is he immiscibili y o he subs a es, oil and glyce ol. To imp o e mass ans e a es, a oiding he use o o ganic sol en s, emulsi ica ion o bo h eac an s as e e se micelles (glyce ol-in-oil) was ca ied ou p e ious o lipase-ca alyzed sa dine oil glyce olysis. Subs a e emulsi ica ion yielded highe eac ion a es compa ed o kine ics wi h no p e ious emulsi ica ion, bu s ill lowe han in o ganic sol en s. To a oid he use o o ganic sol en , SC-CO2 was used as eac ion medium bu no kine ic ad an ages we e demons a ed in he p essu e ange om 15 o 25 MPa. By inc easing empe a u e, om 40 o 90 ºC, eac ion a es inc eased bo h in a sol en - ee sys em and in SC-CO2 medium. I was also ound ha an inc ease in empe a u e does no lead o an inc ease in he inal oxida ion s a us o he eac ion p oduc s. This beha io was due o he so p ion capaci y o he Lipozyme 435 suppo , gi ing lowe oxida ion s a us a he highes empe a u e, 80-90 ºC. Keywo ds: ish oil, glyce olysis, mic oemulsion, SC-CO2, pe oxides adso p ion. Chemical compounds s udied in his a icle: Glyce ol (PubChem CID: 753); Eicosapen aenoic acid (PubChem CID: 446284); Docosahexaenoic acid (PubChem CID: 445580); Ae osol OT (PubChem CID: 23673837); Tween 80 (PubChem CID: 5281955).  Co esponding au ho . Tel.: +34 947 258810. Fax: ++34947258831. E-mail add ess e [email protected] ACCEPTED MANUSCRIPT ACCEPTED MANUSCRIPT 2 1. In oduc ion The impo ance o omega-3 polyunsa u a ed a y acids (n-3 PUFA), especially eicosapen aenoic acid (EPA) and docosahexaenoic acid (DHA), in human nu i ion and disease p e en ion is ully ecognized scien i ically (K is-E he on, Ha is, & Appel, 2002; Riedige , O hman, Suh, & Moghadasian, 2009). n-3 PUFA supplemen s a e a ailable in di e en chemical o ms. Among he di e en ypes o lipid de i a i es con aining n-3 PUFA concen a es, monoacylglyce ols (MAG) and diacylglyce ols (DAG) ha e good bioa ailabili y and oxida ion s abili y (He nandez, 2014; Lawson & Hughes, 1988). Addi ionally, i mus be also conside ed ha die a y TAG a e hyd olyzed in he small in es ine o sn-2-MAG being he mos a o able s uc u e o n- 3 PUFA o be adso bed by in es inal mucosa (Banda a e al. 2012). In addi ion, MAG o i s mix u es wi h DAG accoun o 75% o he wo ldwide emulsi ie p oduc ion (Zhong e al., 2009). The well-known d awbacks o he con en ional chemical glyce olysis echnique (ene gy in ensi e, low yields (30–40%), oxidized p oduc s) ha e p omp ed a g owing in e es in he de elopmen o al e na i e p ocesses o he p oduc ion o MAG and DAG ich in n-3 PUFA. Enzyme-ca alyzed eac ion is an a ac i e al e na i e since he eac ion can be ca ied ou unde mild condi ions (Bo nscheue , 1995; Fel es, de Oli ei a, Block, & Ninow, 2013). To o e come he p oblem o he immiscibili y o glyce ol and oil, di e en app oaches ha e been used in he li e a u e o imp o e he con ac be ween he eac an s and hence educe mass ans e limi a ion. Lipase-ca alyzed glyce olysis has been ca ied ou in di e en eac ion media such as o ganic sol en s (Dams up e al., 2006), comp essed luids (Moquin, Temelli, King, & Palcic, 2005) and ionic liquids (Guo & Xu, 2006), in o de o imp o e he mass ans e . The cos , oxici y and ene gy equi ed o sol en emo al om he p oduc mix u e, a e impo an aspec s o be conside ed when dealing wi h con en ional sol en sys ems (P a , Hayle , & Wells, 2014). Recen ly, he uses o di e en su ac an s o inc ease he in e acial a ea, and ul asound i adia ion ha e been also p oposed o educe mass ans e limi a ion (Fiame i e al., 2012; Valé io, Ro ani, T eichel, De Oli ei a, & Oli ei a, 2010). Bioca aly ic p ocessing in mic oemulsion sys em has ecei ed a en ion in o de o inc ease con ac be ween subs a es. The o ma ion o a mic oemulsion o he eac an s (glyce ol-in-oil) as e e se micelles can help o imp o e mass ans e a es. Fu he mo e, lipases demons a e high in e acial ac i i y in micelle sys ems because he o ma ion o he ac i e si e du ing he eac ion ACCEPTED MANUSCRIPT ACCEPTED MANUSCRIPT 3 occu s a he in e ace be ween he subs a es and he enzyme. Se e al ood g ade su ac an s a e able o s abilize he micella sys em imp o ing sys em homogenei y (Ca alho & Cab al, 2000; S ama is, Xenakis, & Kolisis, 1999). Ne e heless, i mus be aken in o accoun ha some ood g ade su ac an s ha e chemical unc ions ha could be modi ied by lipases. Fo ins ance, he lipase No ozym 435 p esen ed ac i i y a pa icula condi ions owa ds some su ac an s as soy leci hin and Tween in glyce olysis eac ions (Camino Fel es, Villeneu e, Ba éa, de Oli ei a, & Ninow, 2012). To a oid his p oblem, o he syn he ic su ac an s, such as sodium (bis-2-e hyl-hexyl) sul osuccina e (ae osol-OT o AOT), ha e been used. AOT has been epo ed o o m micelles in a g ea numbe o nonpola subs ances and se e al o he pola sol en s such as glyce ol (Fiame i e al., 2009). In his case, good esul s ha e been ob ained in glyce olysis sys ems when adding mo e ha 7.5% o AOT (Fiame i e al., 2009). Howe e , he high amoun o his su ac an may gene a e p oblems du ing emo al p ocesses (S ama is, Xenakis, & Kolisis, 1994). Ano he al e na i e o o ganic sol en s is he use o he supe c i ical luids (SCFs) as eac ion medium. Supe c i ical ca bon dioxide (SC-CO2) is p obably he mos used SCF due o i s addi ional bene i s (non- oxic, non- lammable, eadily a ailable a high pu i ies and low cos s, and ela i ely mild c i ical condi ions) ha a e appealing when choosing en i onmen al eplacemen o o ganic sol en s (Ma suda, 2013; Rezaei, Temelli, & Jenab, 2007). SC-CO2 has liquid-like densi y bu gas-like iscosi y esul ing in high mass ans e being a clean al e na i e o eplace o ganic sol en s. Enzyma ic concen a ion o n-3 PUFA in supe c i ical luids (SCFs) is an in e es ing op ion o he p e en ion o oxida ion du ing p ocessing o ish oil (Lin, Chen, & Chang, 2006; Roh, Kim, & Choi, 2015). Besides, SC-CO2 can be easily sepa a ed om he eac ion p oduc s by simple dep essu iza ion and allows ac iona ion o he eac ion p oduc s. Some p e ious s udies o enzyma ic eac ions o di e en lipid sou ces in SC-CO2 ha e been epo ed in he li e a u e. Howe e , in case o enzyma ic glyce olysis, o he comp essed luids such as p opane, n-bu ane, and ace one, ha e been used (Esmelind o e al., 2008; Tai & B unne , 2011; Valé io e al., 2010). Some s udies o glyce olysis o ege able oils in SC-CO2 a high empe a u es can be ound bu wi h no enzyma ic ca alys (Moquin e al., 2005; Temelli, King, & Lis , 1996). In a p e ious wo k, a de ail kine ic s udy o glyce olysis o sa dine oil using Lipozyme 435 o m Candida an a c ica B as bioca alys in an op imized amoun o e -bu anol was pe o med (Solaesa, Sanz, Bel án, e al., 2016). Te .bu anol helped o c ea e a ACCEPTED MANUSCRIPT ACCEPTED MANUSCRIPT 4 homogeneous phase and o educe mass ans e limi a ions. Howe e , o ganic sol en s p esen di e en en i onmen al conce ns. In his wo k, o imp o e con ac be ween subs a es, a oiding he use o o ganic sol en s, emulsi ica ion o glyce ol and oil be o e glyce olysis eac ion was conside ed. Glyce olysis eac ion has been pe o med in a sol en ee sys em a a mosphe ic p essu e and in SC-CO2 as eac ion medium wi h p e ious susbs a es emulsi ica ion. The e ec o adding a su ac an , AOT o Tween 80, o s abilize he emulsion, on glyce olysis pe o mance has been also s udied. Glyce olysis has been de e mined a di e en ope a ing empe a u esa a mosphe e p essu e, 0.1 MPa, and in SC-CO2 medium in he p essu e ange om 15 o 25 MPa. Since n-3 PUFA a e highly suscep ible o oxida ion; he oxida i e s a us o he inal eac ion p oduc s was e alua ed h ough he pe oxide and anisidine alues. Reac ion yields and he oxida ion alues o he eac ion p oduc s we e compa ed o bo h sys ems. 2. Ma e ials and me hods 2.1 Ma e ials Re ined sa dine oil was p o ided by Indus ias A ines S.L. (Spain) wi h 18.3% o EPA and 7% o DHA and a wa e con en o 0.2% (Solaesa, Bucio, Sanz, Bel án, & Rebolleda, 2014). Glyce ol was pu chased om Sigma Ald ich wi h a pu i y o ≥ 99.5% and a wa e con en o 0.18%. The ood g ade lipase Lipozyme 435 om Candida an a c ica B (immobilized on a mac opo ous hyd ophobic ac ylic esin), was dona ed by No ozymes A/S (Bags ae d, Denma k). Ca bon dioxide (99.9%) was supplied by Ai Liquide S.A. (Spain). Polyoxye hylene so bi an monoolea e (Tween 80) and sodium bis (2-e hylhexyl) sul osuccina e (Ae osol AOT o AOT), used as ood g ade su ac an s, we e pu chased by Sigma Ald ich. All o he chemicals used in di e en analyses we e o analy ical o HPLC g ade. 2.2 Emulsi ica ion p ocess Mic oemulsions o he glyce olysis sys em o sa dine oil we e p epa ed a a ixed mole a io o 3:1 (glyce ol:oil) since his mole a io was ound as he op imum in a p e ious kine ic s udy (Solaesa, Sanz, Bel án, e al., 2016). A high-speed blende (Micc a D9 equipped wi h a DS-20/PF EMR o o –s a o ) a di e en speeds, om 16000 o 35000 pm, was used by pulses du ing 3 minu es. To p epa e he su ac an - ee emulsion as e e se micelles, he app op ia e amoun o glyce ol (10 g) was added d op by d op o ACCEPTED MANUSCRIPT ACCEPTED MANUSCRIPT 5 he sui able amoun o oil (30 g) while being comple ely mixed a high speed. Dispe sed (glyce ol) and con inuous (sa dine oil) phases we e iden i ied by he dilu ion es (Mize e al., 2013). Fu he mo e, di e en concen a ions (0.5, 1 and 1.5% in glyce ol o oil as indica ed in Table 2) o wo ood g ade su ac an s, AOT and Tween 80, we e es ed in o de o imp o e he s abili y o he emulsion. A de ined quan i y o each su ac an was dissol ed in oil o in glyce ol, depending on i s solubili y. The cha ac e iza ion o he emulsions was pe o med 10 min a e emulsi ica ion o a oid any c eaming o coalescence e ec . Pa icle size dis ibu ion (PSD), mean d ople diame e and polydispe si y index (PDI) o samples we e measu ed by dynamic ligh sca e ing (DLS), using a Ze asize Nano ZS appa a us (Mal e n Ins umen s L d., UK) o e alua e he bes condi ions o p oduce a s able emulsion wi h small (o he smalles ) d ople size. 2.3 Lipase-ca alyzed glyce olysis o sa dine oil in di e en sys ems A compa a i e s udy o lipase-ca alyzed glyce olysis in di e en sys ems was ca ied ou . All he expe imen s we e conduc ed in a ba ch mode keeping cons an he enzyme concen a ion a 5 w % (by weigh o subs a es) and he subs a e mole a io (3:1, glyce ol o oil) acco ding o p e ious wo k (Solaesa, Sanz, Bel án, e al., 2016). Table 1 summa izes all glyce olysis eac ions ha ha e been done in his wo k. Expe imen s 1 - 6 ha e been ca ied ou a a mosphe ic p essu e in a sol en ee sys em in a 100 mL jacke ed ba ch eac o . Fi s o all, expe imen s 1 and 2 we e ca ied ou o e alua e he e ec o p e ious subs a es emulsi ica ion on eac ion a e. Expe imen s 3 and 4 we e pe o med wi h emulsi ied subs a es s abilized by adding a ood g ade su ac an , AOT and Tween 80 espec i ely, a he op imum concen a ion p e iously de e mine in sec ion 2.2. Expe imen s 2, 5 and 6 we e pe o med o e alua e he e ec o eac ion empe a u e, 50, 80 and 90ºC espec i ely. Glyce olysis eac ion was ca ied ou as ollows. Once emulsion was p epa ed, i was cha ged in o he eac o . La e , he lipase was added and a ni ogen s eam was applied. The eac o was hen closed and he s i ing sys em by impelle s was connec ed. A he mos a ic wa e ba h allows wo king a he desi ed empe a u e. The eac o was co e ed wi h oil pape o a oid he ligh exposu e. On he o he hand, expe imen s 7-13 ha e been ca ied ou in SC-CO2 as eac ion medium. They we e pe o med in a high p essu e ba ch s i ed ank eac o made o s ainless s eel, ha ing an in e nal olume o 100 mL (Melgosa e al., 2017). A eshly ACCEPTED MANUSCRIPT ACCEPTED MANUSCRIPT 6 p epa ed emulsion and he lipase we e cha ged in o he eac o p o ided wi h magne ic agi a ion and hen i was closed, placed in a he mos a ic wa e ba h and connec ed o he p essu e ci cui . Subsequen ly, SC-CO2 was ed in o he eac o by means o a high p essu e pump (ISCO 260 D) up o he desi ed p essu e, which was main ained by a digi al p essu e con olle . Ope a ing p essu e and empe a u e ha e been a ied in he ange be ween 15-25 MPa (Exp.7-9) and 40-90ºC (Exp. 7 and 10-13). In bo h sys ems, samples we e aken pe iodically du ing 8 h, il e ed and s o ed a -18ºC up o analysis. 2.4 Analysis o he eac ion p oduc s The neu al lipid p o ile (TAG, DAG, MAG and FFA) was analyzed by a no mal phase high pe o mance liquid ch oma og aphy (NP-HPLC). The ch oma og aphic appa a us consis ed o a HPLC sys em (Agilen 1200) o med by a qua e na y pump and an au o- injec o . The ch oma og aphic sepa a ion o he compounds was ca ied ou a oom empe a u e wi h a Lich osphe Diol column (5 μm, 4 mm × 250 mm) and de ec ion was pe o med by an e apo a i e ligh sca e ing de ec o (Agilen 1200 se ies) a 35ºC and 0.35 MPa. G adien elu ion was achie ed by mobile phases A (isooc ane) and B (me hyl e -bu yl e he :ace ic acid = 99.9:0.1, / ). The me hod and calib a ion p ocedu e ha e been p e iously epo ed (Solaesa, Sanz, Falkebo g, e al., 2016). The egioisome s o DAG and MAG could no be dis inguished by he applied analy ical p ocedu e, so he o al amoun o MAG and DAG was epo ed o he kine ic expe imen s. The lipid p o ile esul s we e exp essed in glyce ol ee basis. 2.5 Lipid oxida ion analysis The oxida ion s a us has been de e mined using wo assays: pe oxide alue (PV) and anisidine alue (AV). The PV measu es he concen a ion o hyd ope oxides o med in he ini ial s ages o lipid oxida ion (p ima y oxida ion). PV was de e mined ollowing he AOAC O icial Me hod 965.33 by an au oma ic i a o Me h om 905 Ti ando (AOAC O icial Me hod 965.33, 2000). The AV is an es ima ion o he concen a ion o non- ola ile seconda y oxida ion p oduc s (mainly 2-alkenals and 2,4-dienals). The AV was measu ed acco ding o AOCS o icial me hod (Cd 18–90), using a UV-Visible spec opho ome e (AOCS O icial Me hod Cd 18-90, 2017). PV and AV allow calcula ing o al oxida ion (TOTOX) by he o mula: TOTOX = 2PV + AV [1] ACCEPTED MANUSCRIPT ACCEPTED MANUSCRIPT 7 PV and AV ha e been de e mined o he supplied e ined sa dine oil and he inal eac ion mix u es ob ained a e 8 h a he di e en empe a u es The lipid phase was sepa a ed o analysis om he lipase and he emained glyce ol by cen i uga ion a 5000 pm and 35ºC du ing 10 minu es. The uppe phase, ee o glyce ol, o med by he lipid ac ion (TAG, DAG, MAG and FFA) was collec ed unde N2 a mosphe e and s o ed a -18ºC up o analysis. 2.6 S a is ical analysis All analyses we e conduc ed using so wa e S a g aphics X64. The esul s a e p esen ed as a mean  s anda d de ia ion o a leas h ee eplica es. The signi icance o he di e ences was de e mined based on an analysis o he a iance wi h he Tukey’s hones ly signi ican di e ence (HSF) me hod a p- alue ≤ 0.05. 3. Resul s and discussion 3.1 Op imiza ion o he emulsi ica ion p ocess and cha ac e iza ion o he emulsion 3.1.1 Su ac an - ee emulsions The e ec o emulsi ica ion speed on emulsion s abili y wi hou he addi ion o su ac an s has been e alua ed by measu ing he polydispe si y index (PDI) and he d ople diame e o he emulsion ob ained in he ange om 16000 o 35000 pm. A any o he emulsi ica ion speeds essayed, d ople diame e was lowe han 2 µm bu 29000 pm we e needed o ob ain a PDI below 1. The lowes polydispe si y index was ob ained a he highes speed assayed in his wo k, 35000 pm; howe e , oaming was obse ed. The e o e 29000 pm was selec ed o u he subs a e emulsi ica ions. A his speed he mean d ople diame e o he emulsion was 301 ± 34 nm and he PDI a ound 0.4. The su ac an - ee emulsion p esen ed a PDI lowe han 1 only up o 20 minu es, al hough a longe imes, s ill a anslucen and homogeneous sys em was isually obse ed. In any case, he emulsion was p epa ed and immedia ely used as eac ion media. 3.1.2 Su ac an s abilized emulsions The use o a su ac an was also es ed in his wo k o imp o e he emulsion s abili y and eac ion a es. Two ood g ade su ac an s, AOT and Tween 80, wi h hyd ophilic ACCEPTED MANUSCRIPT ACCEPTED MANUSCRIPT 8 lipophilic balance (HLB) alues o 10 and 15 espec i ely, we e used a di e en amoun s (0.5, 1 and 1.5%). PDI o he emulsions p epa ed adding hese su ac an s we e measu ed a speci ic imes o e alua e hei s abili y (Table 2). Al hough a su ac an was added o s abilize he emulsions, PDI in he di e en emulsions inc eased wi h ime in all cases (Table 2). The highe s abili y was obse ed when 0.5% o Tween 80 and 1.5% o AOT we e p e iously dissol ed in glyce ol. In hese cases he emulsion was ound o be s able o a leas 1 h. PSD was e alua ed o emulsions wi h he highes s abili y o med by adding 0.5 % o Tween 80 and 1.5 % o AOT in glyce ol and compa ed wi h hose ob ained in su ac an - eeemulsion. Smalle micelles we e ob ained when a su ac an was added o he sys em wi h medium pa icle sizes alues o 67 ± 5 nm, 94 ± 4 nm and 301 ± 34 nm o AOT 1.5 % and 0.5 % o Tween 80 dissol ed in glyce ol and su ac an - ee emulsion, espec i ely. 3.2 Glyce olysis eac ion o sa dine oil by Lipozyme 435 3.2.1 E ec o subs a es emulsi ica ion on he eac ion a e Fig. 1 compa es he kine ics o he glyce olysis eac ion in a sol en ee medium a a mosphe ic p essu e wi h and wi hou p e ious emulsi ica ion o he subs a es (Exp 1 and 2 espec i ely). As i can be obse ed, when no p e ious emulsi ica ion o he eac an s was ca ied ou , mass ans e limi a ions lead o lowe ini ial eac ion a e. These limi a ions a e e lec ed in he alues o he ini ial slope o TAG composi ion as unc ion o ime being 0.15  0.01 (mol TAG %·min-1) wi hou subs a es emulsi ica ion and 0.279  0.008 (mol TAG %·min-1) o subs a e emulsi ica ion. Fo a e e se micelle sys em, highe in e acial a ea is p o ided, which a o s lipase- ca alyzed eac ions. A longe eac ion imes, eac ion a es become simila due o he MAG and DAG o ma ion as emulsi ie s. The low HLB alues o MAG and DAG mean ha hey end o s abilize e e se micelles sys ems (O’B ien, 2004). Simila esul s we e obse ed by Awadallak e al. (Awadallak, Voll, Ribas, Ca dozo, & Edson, 2013) in he enzyma ic palm oil hyd olysis unde ul asound i adia ion o p oduce DAG. They also pe o med a con ol eac ion (wi hou ul asound in luence) o compa e he deg ee o hyd olysis in bo h sys ems, being a ound 20% a e 12 h in he con ol eac ion and almos 40% when ul asound was used be o e he eac ion. Bu a longe eac ion imes (24 h) he deg ee o hyd olysis becomes simila . The e o e, hey also ACCEPTED MANUSCRIPT ACCEPTED MANUSCRIPT 15 Oil Chemis s’ Socie y. h p://doi.o g/10.1007/s11746-006-1171-5 Esmelind o, Â. F. A., Fiame i, K. G., Ceni, G., Co azza, M. L., T eichel, H., de Oli ei a, D., & Oli ei a, J. V. (2008). Lipase-ca alyzed p oduc ion o monoglyce ides in comp essed p opane and AOT su ac an . Jou nal o Supe c i ical Fluids. h p://doi.o g/10.1016/j.sup lu.2008.05.004 Eu opean Pha macopoeia 5.0 (2005). Omega-3-acid T iglyce ides. Fel es, M. M. C., de Oli ei a, D., Block, J. M., & Ninow, J. L. (2013). The P oduc ion, Bene i s, and Applica ions o Monoacylglyce ols and Diacylglyce ols o Nu i ional In e es . Food and Biop ocess Technology. h p://doi.o g/10.1007/s11947-012-0836-3 Fiame i, K. G., Us a, M. K., De Oli ei a, D., Co azza, M. L., Fu igo, A., & Vladimi Oli ei a, J. (2012). Kine ics o ul asound-assis ed lipase-ca alyzed glyce olysis o oli e oil in sol en - ee sys em. 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JAOCS, Jou nal o he Ame ican Oil Chemis s’ Socie y, 86, 783–789. h p://doi.o g/10.1007/s11746-009-1402-7 ACCEPTED MANUSCRIPT ACCEPTED MANUSCRIPT 18 Fig. 1 .TAG composi ion as a unc ion o ime in he glyce olysis o sa dine oil in sol en ee sys em wi h () and wi hou (◊) subs a es emulsi ica ion a a mosphe ic p essu e (0.1 MPa). Reac ions we e pe o med a MR = 3:1 (glyce ol:oil), T = 50ºC, enzyme loading 5 % w . o subs a es. 0 20 40 60 80 100 0 100 200 300 400 500 TAG (mol %) Time (min) ACCEPTED MANUSCRIPT ACCEPTED MANUSCRIPT 19 Fig. 2. TAG composi ion as a unc ion o ime in he glyce olysis o sa dine oil p e ious subs a es emulsi ica ion wi h 1.5% o AOT in glyce ol (□), 0.5% o Tween 80 in glyce ol (○) and su ac an ee () a a mosphe ic p essu e (0.1 MPa).. Reac ions we e pe o med a MR = 3:1 (glyce ol:oil), T = 50ºC, enzyme loading 5 % w . o subs a es. 0 20 40 60 80 100 0 100 200 300 400 500 TAG (mol %) Time (min) ACCEPTED MANUSCRIPT ACCEPTED MANUSCRIPT 20 Fig. 3. Time cou se o lipase-ca alyzed glyce olysis eac ion o sa dine oil in e -bu anol medium (hollow symbols) and in sol en ee (solid symbols) wi h p e ious emulsi ica ion o he subs a es a a mosphe ic p essu e (0.1 MPa). Legend: TAG (, ▲), DAG (□, ■), MAG (◇, ◆) and FFA (○, ●). Reac ions we e pe o med a MR = 3:1 (glyce ol:oil), T = 50ºC, enzyme loading 5 % w . o subs a es. 0 20 40 60 80 100 0 100 200 300 400 500 Lipid composi ion (mol %) Time (min) ACCEPTED MANUSCRIPT ACCEPTED MANUSCRIPT 21 Fig. 4. E ec o p essu e in SC-CO2 as eac ion medium on glyce olysis con e sion o sa dine oil and p oduc s yield wi h p e ious subs a es emulsi ica ion . (∆) con e sion o TAG, (□, ◊, and ○) yields o DAG, MAG and FFA, espec i ely a e 7 h o eac ion ime. Reac ions we e pe o med a MR = 3:1 (glyce ol:oil), T = 50ºC, enzyme loading 5 % w . o subs a es. 0 20 40 60 80 100 0 5 10 15 20 25 Con e sion o Yield (mol %) P essu e (MPa) ACCEPTED MANUSCRIPT ACCEPTED MANUSCRIPT 22 Fig. 5. E ec o empe a u e on MAG + DAG composi ion as unc ion o ime in he glyce olysis o sa dine oil wi h p e ious subs a es emulsi ica ion in SC-CO2 a 15 MPa: 40ºC (◊), 50ºC (□), 65ºC (∆), 80ºC (○) and 90ºC (x). Reac ions we e pe o med a MR = 3:1 (glyce ol:oil) and enzyme loading 5 % w . o subs a es. 0 20 40 60 80 100 0 100 200 300 400 500 600 MAG + DAG (mol %) Time (min) ACCEPTED MANUSCRIPT ACCEPTED MANUSCRIPT 23 Fig. 6. In luence o eac ion empe a u e on PV (whi e ba s) and AV (g ey ba s) in he inal eac ion mix u e a e 7 h a 15 MPa in SC-CO2 as eac ion medium wi h p e ious subs a es emuls icia ion. Measu emen s gi en a e mean alues based on ou de e mina ions. Limi allowed is he maximum o each axis. Values wi h di e en le e s in each ype o analysis (PV o AV) a e signi ican ly di e en when applying he Tukey's hones ly signi ican di e ence (HSD) me hod a p- alue ≤ 0.05. ab c b b a ab ab a ab b b b 10 15 20 25 30 0 2 4 6 8 10 Ini ial 40 50 65 80 90 AV PV (mEq pe oxide kg-1 oil) Reac ion empe a u e (ºC) ACCEPTED MANUSCRIPT ACCEPTED MANUSCRIPT 24 Table 1. Summa y o he eac ion condi ions o lipase-ca alyzed sa dine oil glyce olysis eac ions ca ied ou in his wo k. Exp. Reac ion medium P essu e (MPa) Tempe a u e (ºC) Emulsi ica ion Su ac an 1 Sol en ee 0.1 50 No - 2 Yes - 3 Yes AOT 4 Yes Tween 80 5 80 Yes - 6 90 Yes - 7 SC-CO2 as sol en 15 50 Yes - 8 20 Yes - 9 25 Yes - 10 15 40 Yes - 11 65 Yes - 12 80 Yes - 13 90 Yes - ACCEPTED MANUSCRIPT