ITUB20153877A1 - Method of purification of glycerides of fatty acids, compositions derived from them, and their use - Google Patents
Method of purification of glycerides of fatty acids, compositions derived from them, and their use Download PDFInfo
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- ITUB20153877A1 ITUB20153877A1 ITUB2015A003877A ITUB20153877A ITUB20153877A1 IT UB20153877 A1 ITUB20153877 A1 IT UB20153877A1 IT UB2015A003877 A ITUB2015A003877 A IT UB2015A003877A IT UB20153877 A ITUB20153877 A IT UB20153877A IT UB20153877 A1 ITUB20153877 A1 IT UB20153877A1
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- composition
- glycerides
- equal
- acids
- omega
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- 239000000203 mixture Substances 0.000 title claims description 117
- 238000000034 method Methods 0.000 title claims description 72
- 125000005456 glyceride group Chemical group 0.000 title claims description 57
- 238000000746 purification Methods 0.000 title claims description 26
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- 229930195729 fatty acid Natural products 0.000 title claims description 21
- 239000000194 fatty acid Substances 0.000 title claims description 21
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- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims description 65
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 54
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- MBMBGCFOFBJSGT-KUBAVDMBSA-N all-cis-docosa-4,7,10,13,16,19-hexaenoic acid Chemical compound CC\C=C/C\C=C/C\C=C/C\C=C/C\C=C/C\C=C/CCC(O)=O MBMBGCFOFBJSGT-KUBAVDMBSA-N 0.000 claims description 44
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- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 17
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- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 6
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 6
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- WTJKGGKOPKCXLL-RRHRGVEJSA-N phosphatidylcholine Chemical compound CCCCCCCCCCCCCCCC(=O)OC[C@H](COP([O-])(=O)OCC[N+](C)(C)C)OC(=O)CCCCCCCC=CCCCCCCCC WTJKGGKOPKCXLL-RRHRGVEJSA-N 0.000 claims description 3
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- JZNWSCPGTDBMEW-UHFFFAOYSA-N Glycerophosphorylethanolamin Natural products NCCOP(O)(=O)OCC(O)CO JZNWSCPGTDBMEW-UHFFFAOYSA-N 0.000 claims description 2
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Description
DESCRIZIONE DESCRIPTION
La presente invenzione riguarda un nuovo metodo di purificazione di gliceridi di acidi grassi (mono- e/o di- e/o trigliceridi), di qualsiasi origine, inclusi gli oli naturali, e in particolare quelli caratterizzati da una almeno parziale esterificazione con acidi grassi poiinsaturi (PUFAs) a lunga catena, in particolare C 18 - C22, preferibilmente C20 - C22, e comprendenti 2-6 doppi legami, preferibilmente 5-6 doppi legami. The present invention relates to a new purification method of glycerides of fatty acids (mono- and / or di- and / or triglycerides), of any origin, including natural oils, and in particular those characterized by at least partial esterification with fatty acids long-chain polyunsaturates (PUFAs), in particular C 18 - C22, preferably C20 - C22, and comprising 2-6 double bonds, preferably 5-6 double bonds.
Il metodo di purificazione secondo l'invenzione consente di rimuovere da tali gliceridi prodotti strutturalmente estranei ad essi. Questi prodotti estranei, specie nel caso dei gliceridi naturali, sono costituiti essenzialmente, non certo dal punto di vista ponderale ma per la loro estrema tossicità, dai cosiddetti inquinanti organici “persistenti" (Persistent Organic Pollutants, POPs) ormai ubiquitariamente presenti neirambiente (terreni, terreni agricoli, acque marine e fluviali, eco). The purification method according to the invention allows to remove from said glycerides products structurally unrelated to them. These foreign products, especially in the case of natural glycerides, are essentially made up, certainly not from the weight point of view but due to their extreme toxicity, of the so-called "persistent" organic pollutants (POPs) now ubiquitously present in the environment (soils, agricultural land, marine and river waters, eco).
Tra i numerosi POPs noti dalla letteratura e presenti nelle composizioni di gliceridi si possono menzionare, ad esempio, le policloro-dibenzo-diossine e i policloro-dibenzo-furani, i policlorobifenili, i polibromo- difenile Ieri, gli idrocarburi aromatici poli eie li ci, e altri, anche essi usualmente presenti ed estremamente tossici. Among the numerous POPs known from the literature and present in glyceride compositions, it is possible to mention, for example, the polychlorinated dibenzo-dioxins and the polychlorinated dibenzo-furans, the polychlorinated biphenyls, the polybromo-diphenyl Yeri, the polyethylene aromatic hydrocarbons, and others, also usually present and extremely toxic.
BACKGROUND DELL' INVENZIONE BACKGROUND OF THE INVENTION
1 gliceridi degli acidi grassi (esteri con il glicerolo) oggetto del metodo di purificazione deirinvenzione, possono essere mono-, e/o di-, e/o tri-gliceridi e sono così denominati in funzione del loro grado di sostituzione. Sono anche riportati in letteratura come acil-gliceroli, distinguendo in base alla loro posizione e struttura sterica i monoacilgliceroli in posizione sn. 1 o sn-2, oppure i diaci 1-glicero li in posizione 671-1,2 o sn-1,3, oppure ancora i triadi- gliceroli. The glycerides of the fatty acids (esters with glycerol) object of the purification method of the invention can be mono-, and / or di-, and / or tri-glycerides and are so named according to their degree of substitution. They are also reported in the literature as acyl-glycerols, distinguishing monoacylglycerols in the sn position on the basis of their position and steric structure. 1 or sn-2, or the 1-glycerol diaci in position 671-1,2 or sn-1,3, or again the triadi-glycerols.
Se i sostituenti in posizione 1 e 3 sono differenti, il carbonio in posizione 2 diventa asimmetrico e può essere in forma otticamente attiva o racemica. If the substituents in position 1 and 3 are different, the carbon in position 2 becomes asymmetric and can be in optically active or racemic form.
Le proprietà chimico -fisiche e biologiche dei gliceridi dipendono essenzialmente dal numero, dalla posizione e dal tipo di radicale acido presente come estere glicerico. The chemical-physical and biological properties of glycerides essentially depend on the number, position and type of acid radical present as glycerine ester.
E’ noto che gli acidi grassi contenuti nei gliceridi possono essere a catena corta o più spesso a catena media oppure lunga, intendendo in questa sede designare come tali gli acidi con 18 o più acidi di carbonio. E’ anche noto che detti acidi possono essere saturi (come l’acido stearico C18:0), oppure monoinsaturi (come l 'acido oleico C18: l n-9), oppure polinsaturi, contenenti spesso da 2 a 6 doppi legami, e generalmente appartenenti alla classe degli acidi omega-6 (o n-6) come faci do arachidonico (ARA, C20:4 n-6) o a quella degli acidi omega-3 (o n-3) come p.e. l’acido eicosapentaenoico (EPA, 020:5 n-3, tutto cis ) e l’acido docosaesaenoico (DHA, C22:6 n-3, tutto cis ), o anche 1’ acido docosapentaenoico (DPA, C22:5 n-3). It is known that the fatty acids contained in the glycerides can be short-chain or more often medium-chain or long-chain, meaning herein as such the acids with 18 or more carbon acids. It is also known that said acids can be saturated (such as C18: 0 stearic acid), or monounsaturated (such as C18: 1 n-9 oleic acid), or polyunsaturated, often containing from 2 to 6 double bonds, and generally belonging to the class of omega-6 (or n-6) acids such as arachidonic acid (ARA, C20: 4 n-6) or to that of omega-3 (or n-3) acids such as e.g. eicosapentaenoic acid (EPA, 020: 5 n-3, all cis) and docosahexaenoic acid (DHA, C22: 6 n-3, all cis), or also docosapentaenoic acid (DPA, C22: 5 n- 3).
In particolare questi acidi omega-3 e i loro esteri etilici hanno assunto negli ultimi decenni una importanza sempre crescente per le loro proprietà biologiche e per il loro uso come nutraceutici, supplementi alimentari e dietetici, alimenti per uso medico speciale, e come farmaci. Lo stesso sta succedendo attualmente per i loro gliceridi, ritenuti più “naturali* e meglio assorbiti neirorganismo umano, che hanno l’ulteriore pregio di essere la loro prevalente fonte di produzione. ;Infatti, in relazione alla loro origine, tutti questi acidi si trovano in natura in rapporti ampiamente variabili tra di loro e sotto forma di svariate strutture chimiche, come p.e. nei fosfolipidi, eoe., ma più frequentemente si presentano sotto forma di trigliceridi naturali, costituenti degli oli e grassi vegetali e animali. Gli acidi omega-6 sono particolarmente abbondanti negli oli e nei semi vegetali, mentre gli acidi oinega-3 e in particolare EPA e DHA hanno prevalentemente provenienza marina e derivano essenzialmente dagli oli di pesce, anche da acquacolture, o dai “krill oils” oppure ancora da alghe e altri microrganismi oleaginosi, o da “single celi fermentation” a partire da selezionati ceppi di alghe o altri microrganismi. ;I mono-gliceridi (e anche i di-gliceridi) sono invece prevalentemente prodotti industriali, utilizzati per le loro eccellenti proprietà emulsionanti, e rappresentano il 70-80% degli emulsionanti usati al mondo nei prodotti alimentari, cosmetici e farmaceutici. Si ottengono usualmente, sebbene con rese non elevate e con scarsa purezza, per glicerolisi chimica dei trigliceridi (gli oli e grassi naturali) ad alte temperature e per catalisi alcalina. ;In tempi recenti, i gliceridi sostituiti con acili poiinsaturi vengono preferibilmente sottoposti a idrolisi o alcoolisi per via enzimatica, mediante lipasi - anche immobilizzate - selettive per la struttura deiracile e per la sua posizione sul glicerolo: è così possibile agire in condizioni di reazione molto blande e inoltre - in virtù della maggiore resistenza degli acili polinsaluri alla scissione enzimatica, rispetto agli acili saturi e monoin saturi - è possibile isolare composizioni di gliceroli ancora parzialmente acilati e in particolare arricchiti in acidi poiinsaturi. ;E' poi noto che detta idrolisi o alcoolisi per via enzimatica, così come le più tradizionali scissioni per via chimica, possono essere portate a completezza con separazione totale degli acidi poiinsaturi PUPA (o loro esteri) dal glicerolo, acidi poiinsaturi che possono essere arricchiti in composizioni concentrate mediante varie tecnologie, anche abbinate, ma queste fasi riguardano la tecnologia produttiva degli acidi poiinsaturi e dei loro esteri etilici (vedi monografia 07/2012: 1250 della E.P, 8.0 e monografia pag. 4059-61 della USP 37), e non il presente procedimento di purificazione dei gliceridi. Troveranno comunque applicazione, come vedremo, anche sui gliceridi già purificati con il metodo in oggetto. ;Sui vari procedimenti ed effetti biologici che coinvolgono gli oli polinsaturi e ì vari “concentrati” di PUPA ed esteri ottenibili, sono attualmente disponibili molte migliaia di pubblicazioni scientifiche. Quando possibile, faremo tuttavia riferimento alfe codiente volume di Breivik H, “Long-Chain Ortiega-3 Special ty Oils” (H Breivik, ed.), The Oily Press, Bridgwater, (2007), nel seguito citato come “Breivik 2007". ;Fatte queste premesse, in conclusione il metodo di purificazione della presente invenzione si riferisce preferibilmente, oltre che ai gliceridi saturi e monoinsaturi, alla purificazione di mono-, di-, tri-gliceridi di qualsiasi origine e comunque ottenuti, o loro miscele, inclusi gli oli naturali, sostituiti almeno parzialmente con radicali di acidi grassi a lunga catena, comprendenti 18-22 atomi di carbonio, preferibilmente 20-22 atomi di carbonio, e di tipo poiinsaturo, cioè comprendenti 2-6 doppi legami, preferibilmente 5-6 doppi legami. Ci si riferisce in particolare agli acidi appartenenti alla classe degli acidi omega-6 e/o omega-3, più preferibilmente alla classe degli acidi omega-3, in particolare a EPA e/o DHA. ;Il contenuto di àcido grasso poiinsaturo come sopra definito, p.e. EPA o DHA, oppure della loro somma, è compreso tra 15-45%, più spesso 15-30%, e 90%, oppure tra 30-60%, più spesso 45-60%, e 90%, del peso della composizione, essendo 15-30% il contenuto medio in EPA o DHA o della loro somma in un olio naturale (di pesce o similari) usato per la produzione dei PUFA, essendo 45% e 60% i contenuti minimi della somma di EPA e DHA e rispettivamente della somma degli acidi omega-3 - tutti espressi come trigliceridi - previsti dalla monografia 01/2009: 1352 della E.P.7.0 relativa ai gliceridi degli acidi omega-3, ricostituiti per via chimica o enzimatica e arricchiti in PUFA, ed essendo 90% attorno ai contenuto massimo possibile per un gliceride avente come sostituenti solo acidi poiinsaturi come sopra descritti, preferibilmente EPA e/o DHA. ;In termini più generali, riassumeremo il contenuto in acidi poiinsaturi come sopra descritti, come compreso tra 15 e 90% del peso della composizione, più frequentemente tra 15 e 60%. ;Questa provenienza dei gliceridi, direttamente o indirettamente, da fonti “naturali” ed apparentemente rassicuranti, comporta invece gravi pericoli per la salute in tutti gli usi sopra accennati, dovuti alla nota presenza di numerosi inquinanti ambientali (“diossine’', policloro-bifenili,ecc.). Molti di questi sono particolarmente lipo- solubili e tendenzialmente portati a concentrarsi assieme ai vari componenti grassi (da cui la definizione di Persistent Organic Pollutants, POPs). Le caratteristiche principali di queste sostanze sono la persistenza nel tempo, il bioaccumulo attraverso la catena alimentare, il potenziale per la loro diffusione e trasporto ambientale a lunga distanza, e la loro tossicità. Molte di queste sostanze sono chiaramente teratogene, mutagene e carcinogene. ;11 pericolo rappresentato da queste sostanze per l'uomo e gli animali ha indotto una crescente preoccupazione per il contenuto di sostanze tossiche negli alimenti e nella catena alimentare. Prodotti alimentari che non contengono, o hanno contenuto limitato di inquinanti, stanno guadagnando una maggiore popolarità e capacità di mercato. Pertanto reliminazione o la riduzione di inquinanti nei prodotti alimentari ha un grande potenziale per aumentare sostanzialmente la loro possibilità di vendita e il loro valore aggiunto, ma ha anche un elevato valore etico con particolare riferimento al loro uso nel settore dei “baby foods” e delle “infant formulas” ed al rischio di trasmissione al lattante con il latte materno. ;Il primo atto ufficiale contro queste sostanze derivò dalla “Stockholm Convention on POPs” tenutasi nel Maggio 2001 in Svezia, che individuò 12 distinte classi chimiche come più aggressive e pericolose per la salute dell’uomo e per l’ambiente, inclusa l’agricoltura e l’allevamento del bestiame. Molte di queste sostanze erano nel passato usate come pesticidi (erbicidi, insetticidi, fungicidi, rodenticidi, eco), per altre la produzione era inconsapevole e non intenzionale, essendo sottoprodotti indesiderati di una serie di processi chimici e/o di combustione. La conclusione della Convention fu quella di bandire la produzione e l’uso di numerose di queste sostanze, e Lobbie ttivo di controllare tutti gli inquinanti ambientali è stato poi perseguito negli anni successivi dai vari POPs Review Committecs, cóme pure dalle varie Agenzie Regionali per la Protezione Ambientale. ;Nel dettaglio, le “diossine” sono in realtà costituita dalle due famiglie chimiche delle policloro dibenzo-para-diossine (PCDDs) e dei policloro-dibenzo-furani (PCDFs): di questi soltanto 7 PCDDs e 10 PCDFs destano particolare preoccupazione dal punto di vista tossicologico. ;Generalmente i PCDD/PCDF vengono rilevati come miscele di questi ultimi congeneri tossici, avendo attribuito a ciascuno di essi un opportuno “fattore di tossicità equivalente” (TEF), più precisamente il WHO-TEF (European Commission Regulation(EC) 1881 /2006, Off.J.EU, L364/5; 20 December 2006, p.20). Il massimo livello di WHO PCDD/ PCDF TEQ (Tossicità EQuivalente) per oli di origine marina destinati al consumo nell’uomo secondo la suddetta Regulation (EC) 1881/2006, p. 18, è pari a 2 pg/g olio. Secondo USP 37, il criterio di accettabilità corrisponde a “non più di” (NMT) 1 pg/g di equivalenti tossici WHO. ;Un altro gruppo di contaminanti chimici è costituito da agenti industriali come i policloro-bifenili (PCBs), costituiti da molecole di bifenile variamente clorurate: solo 12 hanno caratteristiche tossicologiche simili alle "diossine” e ai “furani”, e sono pertanto definiti dio ssino- simili (DL-PCBs). Anche per i DL-PCB sono stati determinati i fattori di tossicità equivalente TEF e la loro tossicità equivalente TEQ è usualmente data cumulativamente con quella delle diossine. Il loro massimo livello è pari a 10,0 pg/g olio. ;La somma di altri 6 congeneri definiti “indicatori” o “markers” è ritenuto dalla EFSA (European Food Security Agency) un adeguato indicatore della presenza di PCB non diossino simili (N DL-PCBs) e dell'esposizione umana agli stessi. Secondo USP 37, l’accettabilità dei PCB markers - incluso anche il PCB 118 (denominaz. IUPAC)- è limitata a NMT 0,5 ppm (0,5 microgrammi/g). ;I PBDEs sono polibromo-difenileteri, costituiti pertanto da molecole di difeniletere variamente bromurate, e alcuni di essi sono altamente neuro tossici e anche can cerogen i .Son o utilizzati come ritardanti di fiamma, e sono considerati come inquinanti chimici persistenti di tipo “emergente”. Di alcuni termini la produzione industriale è già stata bandita, ma la loro presenza è stata comunque dimostrata in acque inquinate e nelle discariche, e in molti campioni di oli di pesce (Zennegg M et al, Organohalogen Compounds, 68, 1967,2006; US 7,732,488). ;Gli idrocarburi policiclici aromatici (IPA o PAHs) sono composti formati da due o più anelli aromatici condensati e sono di interesse tossicologico in quanto considerati possibili cancerogeni. Gli IPA sono espressi usualmente come sostanza marker benzo[a]pirene, con un limite massimo tollerato di 2 ng/g negli oli e nei grassi ( Regolati on (EC) 1881/2006, Section 6, p.18). ;Tra gli altri POPs qui non discussi in dettaglio, citiamo ancora a titolo di esempio non esaustivo il 2,2 bis- (p-clorofenil) -etano (DDE), il 2,2 bis-(p-clorofentl)-l, 1 -dicloroetano (DDD), e il 2,2 bis-(p-clorofenil)-1,1, 1-tricloroetano (DDT), quest’ultimo rintracciato ovunque nell 'ambi ente globale, i polibromo-bifenili (PBB), Tesacloro benzene, gli isomeri deiresacloro-cicloesano, e altri. ;Le attuali metodiche per attenuare il contenuto di questi inquinanti ambientali nei gliceridi, p.e. nei trigliceridi degli oli di pesce, relativamente molto elevato se il pescato proviene da mari molto inquinati, rientra nei procedimenti base di routine sui materiali grezzi, come lo “sbiancamento” (trattamento con carboni attivi) e la deodorizzazione (stripping in corrente di vapore). Queste procedure standard sono comunque di modesta efficacia (Breivik 2007, pagina 133), e in una fase più avanzata del trattamento si ricorre pertanto alla distillazione o distillazione molecolare o short path, che rappresenta attualmente la metodica più usuale appunto per la purificazione dagli inquinanti ambientali. ;In tempi più recenti, la domanda di brevetto W004/007654 (EP1523541 e US 7,732,488) ha descritto un procedimento per diminuire la quantità di inquinanti ambientali in una miscela di oli o grassi, per cui si aggiunge alla miscela un “working” fluido volatile, e quindi si sottopone la miscela ad almeno una fase di “stripping” durante il quale si distilla una parte degli inquinanti ambientali assieme al “working “ fluido volatile. ;Questo metodo sembra essere migliorativo, ma non è decisivo rispetto all’arte precedente, in quanto comporta temperature elevate per una efficiente fase di stripping, lunghi tempi di riscaldamento, formazione di sottoprodotti, impianti complessi come il distillatore molecolare, e quindi in complesso alti costi. Inoltre, la presenza di numerose classi e al loro interno di differenti specie molecolari dì POPs, ciascuna con proprie caratteristiche chimico -fisiche e un ampio range di punti di ebollizioni in . dipendenza dal loro grado di sostituzione (clorurazione, bromurazione.ecc), rendono questo lavoro molto difficoltoso, e generalmente in grado di diminuire la presenza di un inquinante senza praticamente eliminarlo mai nella sua totalità, e nel caso favorevole per un singolo prodotto senza poter estendere la purificazione alla totalità dei POPs. ;Noi abbiamo quindi concluso che nessuna delle tecniche attuali è in grado di depurare le composizioni in discussione da tutte le impurezze sopra descritte, e solo se usate in combinazione, ripetutamente e con gravi perdite di resa possono avvicinarsi ai limiti imposte dalle varie legislazioni, senza mai giungere ad una sostanziale assenza di ogni inquinante, come sarebbe eticamente auspicabile, o addirittura imperativo almeno nell’uso delle composizioni nella prima infanzia o durante 1’allattamento materno. ;L’eliminazione sistematica di ciascuno e di tutti i POPs appare invece agevolmente ottenibile con il metodo dell Invenzione. ;SOMMARIO DELL’ INVENZIONE ;In un primo aspetto, la presente invenzione riguarda un metodo per la purificazione di una composizione comprendente monogliceridi, e/o di-gliceridi e/o tri-gliceridi di qualsiasi origine, in cui il glicerolo è almeno parzialmente esterificato con acidi grassi saturi o insaturi a lunga catena aventi 16-22 atomi di carbonio, tale composizione contenendo inquinanti ambientali organici persistenti (POPs), in cui il metodo comprende le Tasi di: ;a) trattare una parte in peso della suddetta composizione con almeno 3 parti in peso di urea in un solvente polare, preferibilmente un solvente protico come un alcool inferiore, quale metanolo o etanolo, eventualmente contenente fino al 20% dì acqua, a temperatura prossima allebollizione, per formare un complesso ureico di inclusione essenzialmente totale della composizione; ;b) raffreddare fino a precipitazione del suddetto complesso ureico, e isolarlo, mediante filtrazione o centrifugazione, dalle acque madri contenenti i suddetti inquinanti ambientali organici persistenti (POPs); ;c) ottenere una composizione purificata e con ridotto contenuto di POPs mediante dissoluzione in acqua del complesso ureico di inclusione e separazione della fase oleosa separatasi a seguito della dissoluzione o mediante estrazione della fase oleosa con un solvente organico immiscibile con acqua, tipicamente esano o simili, e successiva evaporazione del solvente l<'>ino a secchezza, o per estrazione diretta dal complesso ureico di inclusione mediante fluidi allo stato supercritico, in particolare anidride carbonica. ;Preferibilmente, nella fase b) di raffreddamento la temperatura viene portata a circa 4~5<C>C e il complesso ureico isolato viene lavato con il suddetto solvente polare, previamente saturato di urea e preferibilmente raffreddato a una temperatura di circa 4-5°C, prima di essere disciolto in acqua o estratto mediante fluidi allo stato supercritico. ;Inoltre, le acque madri e le acque di lavaggio del suddetto complesso ureico isolato possono essere riunite e trattate, come secondo step di purificazione, con ulteriori 2-3 parti in peso di urea (rispetto alla composizione di partenza), ripetendo le fasi da a) a c) di formazione del complesso ureico di inclusione, raffreddamento, isolamento e ottenimento della composizione purificata. ;Eventualmente si possono raccogliere e riunire anche le acque madri ottenute dalla seconda fase di precipitazione e isolamento, così come le acque di lavaggio del secondo complesso ureico di inclusione isolato e ripetere nuovamente le fasi da a) a c) (terzo step di purificazione) . ;In un aspetto del metodo secondo la presente invenzione, i suddetti acidi grassi a lunga catena hanno 18-22 atomi di carbonio, preferibilmente 20-22 atomi di carbonio, e sono di tipo poiinsaturo (PUFA), cioè contenenti 2-6 doppi legami, preferibilmente 5-6 doppi legami, appartenenti alla classe degli acidi omega-6 e/o omega-3, preferibilmente alla classe degli acidi omega-3, più preferibilmente rappresentati da acido eicosapentaenoico (EPA, C20:5 n-3, tutto cis ) e/o acido docosaesaenoico (DHA, C22:6 n-3, tutto cis ). ;In un ulteriore aspetto, i trigliceridi della suddetta composizione hanno origine naturale e provengono da oli di semi vegetali comprendenti prevalentemente acidi omega- 6, oppure da oli di pesce, anche da acquacoltura, o da “krill oils” oppure ancora da alghe e altri microrganismi oleaginosi, o da “single celi fermentation” a partire da selezionati ceppi di alghe o altri microrganismi e comprendono prevalentemente acidi omega-3, in particolare EPA e/o DHA, e in cui il contenuto di acidi grassi polinsaturi come sopra definiti, in particolare EPA e/o DHA, è maggiore o uguale al 15%, oppure è compreso tra 15 e 90%, oppure in particolare è compreso tra 15 e 65%. ;in un ulteriore aspetto del metodo secondo la presente invenzione, la composizione comprendente i suddetti mono-, e/o di-, e/o tri-gliceridi è ottenuta per via chimica e/o enzimatica, mediante lipasi selettive per lacido grasso e la sua posizione sul glìcerolo, a partire da trigliceridi naturali, oppure da gliceridi o glicerolo e acidi grassi poiinsaturi, attraverso procedure note, e in cui la suddetta composizione ha un contenuto di acidi grassi poiinsaturi come sopra definiti maggiore o uguale al 30%, oppure compreso tra 30 e 90%, oppure in particolare il contenuto - espresso come trigliceridi - della somma di EPA e DHA è maggiore o uguale al 45% e la somma degli acidi omega-3 totali è maggiore o uguale al 60%, in accordo con la monografia 01/2009:1352 della E.P.7.0. ;In un altro aspetto del metodo secondo la presente invenzione, la suddetta composizione comprende digliceridi, in cui il glicerolo è esterificato con acido fosforico condensato con amminoalcoli a formare il corrispondente fosfolipide, in particolare la fosfatidilcolina e/o fosfatidiletanolamina. ;Preferibilmente, la fase a) del metodo secondo la presente invenzione, ovvero il trattamento della suddetta composizione con urea, viene eseguita utilizzando quale solvente polare metanolo in quantità pari a 4.5-7 parti in peso, oppure etanolo in quantità pari a 45-65 parti in peso. ;Gli inquinanti ambientali organici persistenti (POPs) più sopra menzionati comprendono principalmente policloro-dibenzo-paradiossine (PCDDs) e policloro-dibenzo-furani (PCDFs), e/o policlorobifenili (PCBs) diossino-simili (DL-PCBs) e marker, e/o polibromodifenileteri (PBDEs), e/o idrocarburi aromatici policiclici (PAHs), e la loro presenza nella composizione purificata ottenuta nella fase c) ri sulta almeno 2 volte ridotta, preferibilmente almeno 5 volte ridotta, convenientemente almeno 10 volte ridotta, e in ogni caso inferiore - per ciascun componente - al rispettivo limite di quantificazione (LOQ) con metodica standard GC-MS. ;In altri suoi aspetti, la presente invenzione riguarda una composizione comprendente mono-gliceridi, e/o di-gliceridi e/o trigliceridi, come definita nelle rivendicazioni 10, I l e 23, così come fuso di tale composizione, per la preparazione, dai mono-gliceridi, e/o digliceridi e/o tri-gliceridi, dei corrispondenti acidi grassi poiinsaturi, o loro sali, mediante idrolisi chimica o enzimatica, oppure per la preparazione dei relativi esteri alchilici C1-C3, come specificato nelle rivendicazioni 12 e 13. ;Inoltre, la presente invenzione si riferisce a una composizione comprendente tali acidi grassi poiinsaturi o loro sali o esteri alchilici C1-C3 ottenuti mediante idrolisi chimica o enzimatica, come specificata nelle rivendicazioni 14- 16. ;In un altro suo aspetto, la presente invenzione riguarda l’uso di una composizione comprendente i summenzionati mono-, di- e trigliceridi o i corrispondenti acidi grassi poiinsaturi o loro sali o esteri alchilici C1-C3 per la preparazione di formulazioni utili come ingredienti alimentari, integratori alimentari e dietetici, alimenti per scopi medici speciali (alimenti funzionali), alimenti per uso animale e per acquacoltura, formulazioni alimentari per l’infanzia, preparazioni cosmetiche e farmaceutiche, come specificato nella rivendicazione 17. ;Infine, la presente invenzione riguarda una composizione comprendente i summenzionati mono-, di- e trigliceridi o i corrispondenti acidi grassi polinsaturi o loro sali o esteri alchilici C1-C3 per gli usi terapeutici definiti nelle rivendicazioni 18-21, nonché una formulazione farmaceutica che li comprende secondo la rivendicazione 22. ;DESCRIZIONE DETTAGLIATA ;Precisiamo che l’impiego dell’urea nella chimica dei lipidi è assolutamente noto. ;Una procedura standard prevede che un olio o grasso viene idrolizzato per dare i componenti acidi, oppure transesterificato in mezzo alcoolico per dare i corrispondenti esteri, per via chimica o enzimatica, e quindi si procede alla concent razione dei componenti polinsaturi: questo avviene generalmente mediante distillazione molecolare, estrazione con fluidi allo stato supercritico, o altre metodiche, ma ancora più spesso per compicssazione appunto con urea (“inclusione” in urea}. L’uso dell’urea tuttavia è presentato solo come mezzo idoneo all’isolamento ed all’allontanamento degli acidi grassi saturi e monoinsaturi, e pertanto alla concentrazione degli acidi poiinsaturi nel solvente della reazione: questo si accompagna pertanto -tra l’altro - ad una incrementata concentrazione delle impurezze estranee assieme ai componenti poi insaturi. L’inclusione dei componenti poiinsaturi nell’urea appare dalla letteratura di difficoltà crescente al crescere della loro concentrazione e del loro grado relativo di in saturazione: nel trattamento di una miscela di acidi grassi, il PUFA appare essere così il componente “passivo" della complessazione. ;Ne risulta pertanto la profonda differenza con il metodo della presente invenzione, per cui p.e.: ;—la “complessazione” viene effettuata direttamente su gliceridi (inclusi oli e grassi naturali, o altri gliceridi particolarmente selezionati), invece che su acidi grassi o loro esteri); ;— i gliceridi sono la parte “attiva” della complessazione, mentre i PUFA della letteratura nella loro essenza non sono idonei alla complessazione, se non marginalmente, e rimangono inalterati nel solvente; ;—la procedura di letteratura è indirizzata ad aumentare la concentrazione dei PUFA, arricchendoli nelle acque madri della complessazione, mentre rimane essenzialmente costante durante il nostro processo di purificazione; ;—la finalità della compie ssazione secondo il nuovo procedimento è quella di diminuire fortemente, essenzialmente di annullare, la presenza degli inquinanti ambientali tutti ufficialmente dichiarati teratogeni, mutageni e cancerogeni o genericamente tossici, invece di portare semplicemente alla concentrazione dei PUFA e loro esteri, secondo le finalità standard attuali. ;Sull’uso dell’urea come agente complessante e sui procedimenti connessi, esistono moltissime pubblicazioni, tra le quali si citano le ampie rassegne di Schlenk H, “Urea inclusion compounds of fatty acids”, in: Progress in thè Chernistry of Fats and Other Lipids Voi Il (RT Holmar, ed.), Pergamo n Press, New York, pp. 243-267 (1954), e di Swem D, “Techniques of separation. Urea complexes”, in: Fatty Acids, Pari 3 (KS Markley, ed.), Interscience, New’ York, pp. 2309-2358 (1963). In particolare si segnala il già citato “Breivik 2007”, nel capitolo “Concentrates”, pagine 111-130. ;In relazione ai gliceridi, oggetto della presente Domanda, Aylward F e Wood PDS, Chem&fnd. (London), 53 ((1956); Nature, 177, 146 (1956) (rif. 127 e rif.129 di Swern, succitato, pagina 2337-8), e altri, riportano il complesso ureico del mono-gliceride in posizione 1 clell’acido stearico (CI 8:0), come pure di una serie di omologhi inferiori, dall’acido caprilico C8:0 all’acido palmitico C16:0. Apparentemente i rnonogliceridi in posizione 2 non formano complessi. ;Si tratta comunque in tutti i casi di gliceridi di acidi saturi e di tentativi di frazionamento e arricchimento di vari componenti, e non di purificazione da inquinanti ambientali. ;Gli stessi autori e altri (Martinez Moreno JM et al, Grasas y aceites (Siviglia, Spagna), 7, 285 (1956), rif. 131 di Swern, succitato) riferiscono che i di-gliceridi in posizione 1,3 sono in grado di dare complessi con urea, mentre i tri-gliceridi non formano complessi. L'assenza di complessazione dei tri-gliceridi, già anticipata da Schlenk, succitato, pagina 251 , viene poi confermata anche nella rassegna di “Breivik 2007”, pagina 1 18, come esperto nelharte. ;Altri autori citati da Swern, pagina 2338 (rif. 128, 132, 133), hanno studiato la formazione di monogliceridi per glicerolisi di oli vegetali, usualmente contenenti arili di lunghezza fino a C18 e fino a 3 doppi legami, e hanno tentato con scarsi risultati la loro separazione dagli altri gliceridi mediante complessazione con urea in determinate condizioni. In particolare Heckles J.S. e Dunlap L.H., J Am Oil Chernists<7>Soc, 32, 224, 1955 (rif. 133) riportano che i monogliceridi di acidi saturi e monoinsaturi (acido oleico) formano complessi urcici, mentre quelli con 2 o 3 punti di insaturazione (risp. acido linoleico e linolenìco) non complessano. In miscela con digliceridi saturi e insaturi, una separazione per complessazione è ottenibile per i gliceridi di acidi saturi, mentre solo un lieve arricchimento è ottenibile con i gliceridi di acidi insaturi. Questa conclusione non è comunque condivisa da Mehta T.N. e Shah S.N., J Am Oil Chernists’ Soc, 34, 587, 1957 (rif. 128). ;Anche in questi casi, e nei limiti dei prodotti specificati, la discussione verte solo sulla possibilità di frazionamento e arricchimento mediante complessazione. ;In tempi recenti, Hayes D.G. et al., JAOCS, 77,207, 2000 riportano che i mono-, di-, e tri-acilgliceroli sono modelli scadenti (poor templates) per La formazione di complessi ureìci (UC) rispetto agli acidi grassi liberi (FFA) e che la loro inclusione, in miscele di acilgliceroli contenenti FFA, riduce addirittura La formazione di UC (vedi Abstract), una conclusione poi ripresa anche dagli esperti nell'arte, come esemplificato da “Breivik 2007”, pagina 118. ;Dall’esame della letteratura, i dati riportati sugli acilgliceroli ci appaiono assolutamente scarsi, spesso in conflitto tra di loro, limitati (in quanto solo occasionalmente, se pure avviene, comprendono i PUFA di maggior interesse, a catena più lunga e più insaturi), e quasi sempre vincolati ai casi specifici e quindi non generalizzabili. La capacità di complessazione viene spesso attribuita a un singolo o a pochi fattori, mentre a nostro parere dipende da tutti i parametri di reazione nel loro complesso, come p.e. il grado di sostituzione del gliceride, la lunghezza e il grado di insaturazione dell’acile, il rapporto con l’urea. il tipo e il volume di solvente, la temperatura di precipitazione del solvente, e cosi via, ciascun fattore interferendo con tutti gli altri. ;Il problema può essere così risolto solo sperimentalmente, avendo ben in mente l’obiettivo da raggiungere e i prodotti da indagare. ;Noi abbiamo così trovato, attraverso una serie di esperimenti, che tutti i gliceridi nel senso più ampio e in modo essenzialmente totale e in determinate condizioni in modo poco correlato alla loro struttura, possono essere complessati con urea. Questo permette poi la precipitazione del complesso e l’allontanamento totale, disciolti nel solvente in forma non complessata, di tutti gli inquinanti organici persistenti (come le temute diossine e sostanze correlate, i pesticidi usati in agricoltura, ecc ) che oggi sempre più si trovano diffusamente neirambiente animale e vegetale e in molti alimenti, in particolare negli oli e nei grassi naturali e nelle sostanze che ne derivano, rappresentando una fonte continua di pericolo per la salute dell'uomo seppure presenti entro i limiti imposti dalle presenti legislazioni e dalle varie Farmacopee . ;Un primo aspetto delFinvenzione prevede un metodo di purificazione che consiste nel trattare il gliceride di un acido grasso ~ in idoneo solvente - con una quantità in eccesso di urea, sufficiente ad una complessazione essenzialmente totale del gliceride, di regola superiore o uguale a 3 parti in peso e fino a 6 parti in peso o più, suddividendo eventualmente il trattamento in 2-3 steps consecutivi, se necessari, preferibilmente in 2 steps consecutivi, e comunque fino a raggiungere una complessazione essenzialmente totale. La suddivisione in più steps non è particolarmente nociva alfeconornia del procedimento poiché comporta solo una filtrazione aggiuntiva, in quanto è possibile aggiungere fulteriore aliquota di urea direttamente alla soluzione filtrata e alle acque di lavaggio del complesso ureico di inclusione senza ulteriore manipolazione. ;Al trattamento consegue una precipitazione del complesso, eventualmente suddiviso nelle rispettive 1-3 frazioni, quindi il complesso viene raccolto per filtrazione o per centrifugazione, e lavato accuratamente con lo stesso solvente saturato di urea e preraffreddato attorno a 4-5°C, o meno, mentre il solvente contenente la totalità degli inquinanti ambientali (POPs) come sopra descritti e altri riportati nella letteratura specialistica, ed eventuali altre impurezze non legate covalentemente al gliceride e non complessabili, viene eliminato. Dal complesso ureico, o dalle frazioni riunite, si recupera quindi agevolmente il gliceride purificato ed essenzialmente privo dei POPs succitati. ;Nelhambito del presente metodo, il gliceride può essere un mono-, e/o di- e/o preferibilmente un tri-gliceride (anche detti monoacil-, diacil-, e triacil-gliceroli), e questi saranno almeno parzialmente esterificati - nel caso di gran lunga più preferito - con acidi grassi a lunga catena, comprendenti 18-22 atomi di carbonio, preferibilmente 20-22 atomi di carbonio, e di tipo poiinsaturo, cioè comprendenti 2-6 doppi legami, preferibilmente 5-6 doppi legami. Ci si riferisce in particolare agli acidi appartenenti alla classe degli acidi omega-6 e/o omega-3, più preferibilmente alla classe degli acidi omega-3, in particolare a EPA e/o DIIA. ;Questi gliceridi possono avere qualsiasi origine e nel caso dei trigliceridi rappresentano usualmente gli oli (o grassi) naturali, in particolare gli oli vegetali, preferibilmente gli oli di pesce e similari. ;Gli acidi omega-6 sono particolarmente abbondanti negli oli e nei semi vegetali, mentre gli acidi omega-3 e in particolare EPA e ΌΗΑ hanno prevalentemente provenienza marina e derivano essenzialmente dagli oli di pesce, anche da acquacolture, o dai “krill oils” oppure ancora da alghe e altri microrganismi oleaginosi, o da “single cell fermentation” a partire da selezionati ceppi di alghe o altri microrganismi. ;Il contenuto di acidi grassi poiinsaturi come sopra definiti, in particolare EPA e/o DHA è maggiore o uguale al 15%, oppure è compreso tra 15 e 90%, oppure in particolare è compreso tra 15 e 65%. ;A titolo esemplificativo ricordiamo che un tipico contenuto di un olio naturale di pesce usato per la produzione dei PUFA è rappresentato da EPA 18% e DHA 12%. mentre 90% è attorno al contenuto massimo possibile per un gliceride avente come sostituenti solo acidi poiinsaturi come descritti, p.e. EPA e/o DHA. ;I mono-gliceridi e i di -gliceridi sono invece prevalentemente prodotti industriali, e così pure vengono ottenuti con procedimenti chimici e/o enzimatici tutti i glìceridi arricchiti in acidi polinsaturi. A questo scopo si utilizzano spesso lipasi selettive per l’acido grasso e la sua posizione sul glicerolo, partendo dai trigliceridi naturali per idrolizzare gli acidi saturi e monoinsaturi, oppure da vari glìceridi o dal glicerolo per azione di acidi poiinsaturi concentrati e usando procedure note. ;In questi casi il contenuto di acidi poiinsaturi sarà usualmente maggiore o uguale al 30%, oppure compreso tra 30 e 90%, oppure ancora in particolare i contenuti minimi della somma di EPA e DHA e della somma degli acidi omega-3 totali -- tutti espressi come trigliceridi - saranno rispettivamente del 45% e del 60%, in accordo con la monografia 01/2009:1352 della E.P.7.0 relativa ai glìceridi degli acidi omega-3 ricostituiti per via chimica o enzimatica e arricchiti in PUFA. ;Questi contenuti della materia prima non si incrementano di solito in modo sostanziale nel corso delia purificazione in oggetto, tranne che in casi particolari. ;Da un punto di vista operativo, il presente procedimento di purificazione mostra alcune analogie con il procedimento di arricchimento dei PUFA e loro esteri mediante complessazione con urea, potendosi distinguere: ;—a) una fase di reazione per cui una parte in peso di gliceride viene trattata con 3 -6 parti o più in peso di urea (suddivisa in 1-3 steps) in un solvente polare, preferibilmente un solvente pratico come un alcool inferiore, quale metanolo o etanolo, eventualmente contenente fino al 20% di acqua (o altri, come indicato da Swern D, già citato), a temperatura prossima allebollizione , per formare un complesso ureico di inclusione del gliceride; ;— b) una fase di raffreddamento a circa 4<5>-5C fino a precipitazione di tale complesso (o complessi) ureico, isolamento mediante filtrazione o centrifugazione (con eliminazione delle acque madri filtrate) e lavaggio a fondo del complesso o dei complessi riuniti con lo stesso solvente saturo di urea e preraffreddato a circa 4-5°C; ;— c) una fase di ottenimento di una composizione purificata mediante dissoluzione in acqua di tale complesso ureico di inclusione e isolamento diretto della fase oleosa separatasi a seguito di detta dissoluzione o mediante estrazione di detta fase oleosa con un solvente organico immiscibile con acqua, tipicamente esano o simili e successiva evaporazione di detto solvente fino a secchezza, oppure ancora per estrazione diretta da tale complesso ureico di inclusione mediante fluidi allo stato supercritico, in particolare anidride carbonica, operazioni seguite da opzionale distillazione molecolare. ;Risulterà peraltro evidente airesperto che la finalità dell’intero processo è totalmente differente, come pure evidenzierà nella, fase a) l’impiego di urea in forte eccesso ed eventualmente in più steps, nella fase b) l’accurato lavaggio del complesso per eliminare gii inquinanti contenuti nelle acque madri inglobate, nella fase c) il recupero del prodotto purificato dal complesso solido, invece del recupero della composizione arricchita in PUFA effettuato sulle acque madri come insegnato dalla “prior art”. ;La composizione purificata secondo l’invenzione avrà essenzialmente la stessa composizione in gliceridi e quindi in acidi grassi come nella materia prima, ma sarà sostanzialmente esente dalla totalità degli inquinanti ambientali tossici sopra descritti, come le diossine e i furani, i policlorobifenili, i polibromodifenileteri, gli idrocarburi ciclici e policiclici, semplici e condensati, e altri POPs noti nella letteratura specializzata. ;In particolare rimane inteso che ciascuna delle sostanze suddette e la loro somma risulterà almeno 2 volte, oppure almeno 5 volte ridotta, o preferibilmente almeno 10 volte ridotta (riduzione di almeno 90%) rispetto alle composizioni da cui provengono, se inizialmente presenti in concentrazioni corrispondentemente più elevate del loro limite di quantificazione (LOQ), oppure ancora ciascuna sostanza sarà inferiore al suo limite di quantificazione (LOQ) con metodica standard GC-MS per cui, assimilando il suo valore a “zero” (lower bound), definiremo la Loro somma “essenzialmente zero”. Un valore “zero" corrisponde invece a una somma di dati inferiori al limite di rilevamento (LOD). ;Come indicato dalle prove sperimentali, le composizioni purificate di gliceridi possono essere caratterizzate dai contenuti di POPs che seguono, anche se nella generalità dei casi ogni congenere risulterà inferiore al suo limite di quantificazione LOQ {essenzialmente zero) . ;~ policloro-dibenzo-pàra-diossine (PCDDs, n=7) e policloro<1>dibenzo-furani (PCDFs, η<~>10) in concentrazione complessiva inferiore o uguale 1,0 pg/g, valore determinato in accordo con i fattori di tossicità equivalente (TEFs) della WHO ed espressi come equivalenti tossici (TEQs}; ;- PCDDs, PCDFs e polle lo ro-bifenili (PCBs) dios sino- simili (DL-PCBs, n=12) in concentrazione complessiva inferiore o uguale a 5,0 pg/g, valore determinato come sopra definito (TEQs); ;- PCBs marker (n=6) in concentrazione complessiva inferiore o uguale a 5,0 ng/g; ;- polibromo- difenileteri (PBDEs, testati n=9) in concentrazione complessiva inferiore a uguale a 5,0 ng/ g; ;- una somma di idrocarburi aromatici policiclici (PAHs, testati n-4), espressa come sostanza marker benzolajpirene, inferiore o uguale a 1,0 ng/g; ;- altri inquinanti ambientali (pollutants) organici persistenti (POPs) comprendenti 2,2 bis-(p-diclorofenil)-etano (DDE), e/o 2,2 bis~{p~ diclorolenil) -1,1 -dicloroeta.no (DDD), e/o 2,2 bis-(p-diclorofenil)- 1,1,1-tricloroetano (DDT) in concentrazione complessiva inferiore o uguale a 2,0 ng/g, polibromo-bifenili (PBB) in concentrazione complessiva inferiore o uguale a 5,0 ng/g; esaclorobenzene in concentrazione inferiore o uguale a 0,1 ng/g, e isomeri di e sacloro- ciclo esano in concentrazione complessiva inferiore o uguale a 0, 1 ng/g. ;Anche tutti gli altri POPs elencati dalla Convenzione di Stoccolma del 2001 e dai successivi Comitati di Revisione, potrebbero essere qui citati in quanto si tratta in tutti i casi di molecole sfericamente “ingombranti”, non idonee alia complessazione con urea, e agevolmente eliminabili quantitativamente nel corso del presente processo di purificazione. ;Risulterà poi evidente che anche altre impurezze potranno essere eliminate nel procedimento, se non legate covalentemente al gliceride, e se non complessabili con urea, come alcuni idrocarburi alifatici a lunga catena e struttura ramificata (tipico lo squalene) , alcuni oligomeri e polimeri degli acidi grassi, alcune sostanze sterolichc, e simili. ;Un secondo aspetto delhinvenzione riguarda le composizioni stesse di gliceridi ottenute secondo il metodo di purificazione più sopra descritto. ;Tra queste composizioni citiamo esplicitamente una composizione purificata di mono-, di-, e tri-esteri di acidi omega-3 con glicerolo, contenente principalmente tri- esteri e una somma di EPA e DHA espressi come rrigliceridi del 45% minimo, e di acidi omega-3 totali espressi come trigliceridi del 60% minimo, in accordo con la monografia 01 /2009: 1352 della E.P. 7.0, e avente un contenuto di inquinanti POPs fortemente ridotti, ben oltre i limiti sopra descritti (essenzialmente assenti). ;Un terzo aspetto dell’invenzione è quello stesso facilmente deducibile dalla disponibilità stessa di gliceridi, preferibilmente trigliceridi, in particolare trigliceridi naturali ricchi in acidi poiinsaturi PUPA e più in particolare in acidi omega-3 come gli oli di pesce e gli altri sopra descritti, tutti esenti da inquinanti ambientali e altamente purificati: questo aspetto riguarda dunque Fuso di detti gliceridi per la produzione, per via chimica o enzimatica, di altre composizioni a base di PUPA e di acidi omega-3 e derivati in forma più o meno concentrata, secondo procedure standard della letteratura descritte nell’ambito della chimica di queste sostanze. ;Già l’attuale tecnologia prevede infatti che, a partire dagli oli naturali di varia origine e quindi da miscele complesse, si proceda all’isolamento dei componenti acidi più interessanti per l’uso farmaceutico o come supplementi alimentari o dietetici, come appunto p.e. EPA e/o DHA, e quindi alla loro concentrazione. ;A questo scopo, in una prima fase gli oli naturali (trigliceridi) più idonei allo scopo prestabilito vengono sottoposti a un blando procedimento idrolitico, p.e. mediante potassa alcolica, ottenendo così i corrispondenti sali potassici e quindi gli acidi liberi e - se desiderato -gli esteri alchilici; oppure più spesso si ricorre a reazione di transesterificazione p.e. in presenza di alcoli alitatici in eccesso, preferibilmente C1-C3, e di catalizzatore alcalino o acido, ottenendo così direttamente i corrispondenti esteri alchilici degli acidi grassi, e da questi -- se desiderato *- i relativi acidi o sali. In particular, these omega-3 acids and their ethyl esters have assumed increasing importance in recent decades for their biological properties and for their use as nutraceuticals, food and dietary supplements, foods for special medical use, and as drugs. The same is currently happening for their glycerides, considered more "natural * and better absorbed in the human body, which have the additional advantage of being their main source of production. In fact, in relation to their origin, all these acids are found in nature in widely varying ratios with each other and in the form of various chemical structures, such as e.g. in the phospholipids, eoe., but more frequently they occur in the form of natural triglycerides, constituents of vegetable and animal oils and fats. Omega-6 acids are particularly abundant in vegetable oils and seeds, while oinega-3 acids and in particular EPA and DHA are mainly of marine origin and derive essentially from fish oils, also from aquacultures, or from "krill oils" or again from algae and other oil-bearing microorganisms, or from "single celi fermentation" starting from selected strains of algae or other microorganisms. Mono-glycerides (and also di-glycerides) are mainly industrial products, used for their excellent emulsifying properties, and represent 70-80% of the emulsifiers used in the world in food, cosmetic and pharmaceutical products. They are usually obtained, although with low yields and low purity, by chemical glycerolysis of triglycerides (natural oils and fats) at high temperatures and by alkaline catalysis. ; In recent times, the glycerides substituted with polyunsaturated acyls are preferably subjected to hydrolysis or alcoholysis by enzymatic way, by means of lipases - even immobilized - selective for the structure of the acyl and for its position on the glycerol: it is thus possible to act in very reaction conditions. and furthermore - by virtue of the greater resistance of polyunsalide acyls to enzymatic cleavage, compared to saturated and monoin saturated acyls - it is possible to isolate compositions of glycerols still partially acylated and in particular enriched in polyunsaturated acids. It is also known that said enzymatic hydrolysis or alcoholysis, as well as the more traditional chemical splits, can be brought to completion with total separation of PUPA polyunsaturated acids (or their esters) from glycerol, polyunsaturated acids that can be enriched in concentrated compositions through various technologies, also combined, but these phases concern the production technology of polyunsaturated acids and their ethyl esters (see monograph 07/2012: 1250 of the E.P, 8.0 and monograph pages 4059-61 of USP 37), and not the present glyceride purification process. However, as we shall see, they will also find application on glycerides already purified with the method in question. Many thousands of scientific publications are currently available on the various biological processes and effects involving polyunsaturated oils and the various "concentrates" of PUPA and esters that can be obtained. Whenever possible, however, we will refer to the next volume of Breivik H, "Long-Chain Ortiega-3 Special ty Oils" (H Breivik, ed.), The Oily Press, Bridgwater, (2007), hereinafter referred to as "Breivik 2007" . including natural oils, substituted at least partially with long-chain fatty acid radicals, comprising 18-22 carbon atoms, preferably 20-22 carbon atoms, and of the polyunsaturated type, i.e. comprising 2-6 double bonds, preferably 5-6 double bonds. This refers in particular to acids belonging to the class of omega-6 and / or omega-3 acids, more preferably to the class of omega-3 acids, in particular to EPA and / or DHA.; The fatty acid content polyunsaturated as above de finished, e.g. EPA or DHA, or their sum, is between 15-45%, more often 15-30%, and 90%, or between 30-60%, more often 45-60%, and 90%, of the weight of the composition , being 15-30% the average content in EPA or DHA or their sum in a natural oil (fish or similar) used for the production of PUFA, being 45% and 60% the minimum contents of the sum of EPA and DHA and respectively of the sum of the omega-3 acids - all expressed as triglycerides - provided for by monograph 01/2009: 1352 of the E.P.7.0 relating to the glycerides of omega-3 acids, chemically or enzymatically reconstituted and enriched in PUFA, and being around 90% at the maximum possible content for a glyceride having as substituents only polyunsaturated acids as described above, preferably EPA and / or DHA. In more general terms, we will summarize the polyunsaturated acid content as described above, as between 15 and 90% of the weight of the composition, more frequently between 15 and 60%. ; This origin of the glycerides, directly or indirectly, from "natural" and apparently reassuring sources, instead entails serious health hazards in all the uses mentioned above, due to the known presence of numerous environmental pollutants ("dioxins", polychlorinated biphenyls ,etc.). Many of these are particularly fat-soluble and tend to concentrate together with the various fat components (hence the definition of Persistent Organic Pollutants, POPs). The main characteristics of these substances are persistence over time, bioaccumulation through the food chain, the potential for their long-distance diffusion and environmental transport, and their toxicity. Many of these substances are clearly teratogenic, mutagenic and carcinogenic. The danger posed by these substances to humans and animals has led to growing concern about the content of toxic substances in food and the food chain. Food products that do not contain, or have limited content of pollutants, are gaining greater popularity and market capacity. Therefore, the elimination or reduction of pollutants in food products has a great potential to substantially increase their sales potential and their added value, but it also has a high ethical value with particular reference to their use in the "baby foods" and "Infant formulas" and the risk of transmission to the infant through breast milk. ; The first official act against these substances resulted from the "Stockholm Convention on POPs" held in May 2001 in Sweden, which identified 12 distinct chemical classes as the most aggressive and dangerous for human health and the environment, including agriculture and cattle breeding. Many of these substances were in the past used as pesticides (herbicides, insecticides, fungicides, rodenticides, etc.), for others the production was unconscious and unintentional, being unwanted by-products of a series of chemical and / or combustion processes. The conclusion of the Convention was to ban the production and use of numerous of these substances, and the attempt to control all environmental pollutants was then pursued in the following years by the various POPs Review Committecs, as well as by the various Regional Agencies for the Environmental Protection. ; In detail, the "dioxins" are actually made up of the two chemical families of polychlorinated dibenzo-para-dioxins (PCDDs) and polychlorinated dibenzo-furans (PCDFs): of these only 7 PCDDs and 10 PCDFs cause particular concern from the point from a toxicological point of view. ; Generally PCDD / PCDF are detected as mixtures of the latter toxic congeners, having attributed to each of them an appropriate "toxic equivalent factor" (TEF), more precisely the WHO-TEF (European Commission Regulation (EC) 1881/2006 , Off.J.EU, L364 / 5; 20 December 2006, p.20). The maximum level of WHO PCDD / PCDF TEQ (Equivalent Toxicity) for oils of marine origin intended for human consumption according to the aforementioned Regulation (EC) 1881/2006, p. 18, is equal to 2 pg / g oil. According to USP 37, the acceptability criterion corresponds to “no more than” (NMT) 1 pg / g of WHO toxic equivalents. ; Another group of chemical contaminants consists of industrial agents such as polychlorinated biphenyls (PCBs), made up of variously chlorinated biphenyl molecules: only 12 have toxicological characteristics similar to "dioxins" and "furans", and are therefore defined as dio ssino-like (DL-PCBs). The TEF equivalent toxicity factors have also been determined for DL-PCBs and their TEQ equivalent toxicity is usually given cumulatively with that of dioxins. Their maximum level is equal to 10.0 pg / g oil.; The sum of 6 other congeners defined as "indicators" or "markers" is considered by the EFSA (European Food Security Agency) to be an adequate indicator of the presence of non-dioxin-like PCBs (N DL-PCBs) and human exposure According to USP 37, the acceptability of PCB markers - including PCB 118 (IUPAC denomination) - is limited to NMT 0.5 ppm (0.5 micrograms / g).; PBDEs are polybromo-diphenyl ethers, therefore consisting of diphenylether molecules variamen te brominated, and some of them are highly neuro toxic and also can cerogen i. They are used as flame retardants, and are considered as persistent chemical pollutants of the "emerging" type. Of some terms, industrial production has already been banned, but their presence has nevertheless been demonstrated in polluted waters and landfills, and in many fish oil samples (Zennegg M et al, Organohalogen Compounds, 68, 1967,2006; US 7,732,488). ; Polycyclic aromatic hydrocarbons (PAHs or PAHs) are compounds formed by two or more condensed aromatic rings and are of toxicological interest as they are considered possible carcinogens. PAHs are usually expressed as a marker substance benzo [a] pyrene, with a maximum tolerated limit of 2 ng / g in oils and fats (Regolati on (EC) 1881/2006, Section 6, p.18). ; Among the other POPs not discussed in detail here, we still mention by way of non-exhaustive example the 2,2 bis- (p-chlorophenyl) -ethane (DDE), the 2,2 bis- (p-chlorofentl) -l, 1-dichloroethane (DDD), and 2,2 bis- (p-chlorophenyl) -1,1, 1-trichloroethane (DDT), the latter found everywhere in the global environment, the polybromo-biphenyls (PBB), Tesachlor-benzene, the isomers of hydrochlor-cyclohexane, and others. ; Current methods to mitigate the content of these environmental pollutants in glycerides, e.g. in the triglycerides of fish oils, relatively very high if the catch comes from very polluted seas, it is part of the basic routine procedures on raw materials, such as "bleaching" (treatment with activated carbon) and deodorization (stripping in a current of steam) . These standard procedures are however of modest effectiveness (Breivik 2007, page 133), and in a more advanced phase of the treatment, therefore, molecular distillation or distillation or short path is used, which currently represents the most usual method for the purification of environmental pollutants. . ; In more recent times, the patent application W004 / 007654 (EP1523541 and US 7,732,488) described a process for decreasing the quantity of environmental pollutants in a mixture of oils or fats, whereby a "working" volatile fluid is added to the mixture , and then the mixture is subjected to at least one "stripping" phase during which part of the environmental pollutants are distilled together with the "working" volatile fluid. ; This method seems to be an improvement, but it is not decisive with respect to the previous art, as it involves high temperatures for an efficient stripping phase, long heating times, formation of by-products, complex systems such as the molecular still, and therefore overall high costs. Furthermore, the presence of numerous classes and within them of different molecular species of POPs, each with its own chemical-physical characteristics and a wide range of boiling points in. dependence on their degree of substitution (chlorination, bromination, etc.), make this work very difficult, and generally able to reduce the presence of a pollutant without practically ever eliminating it in its entirety, and in the favorable case for a single product without being able to extend the purification of all POPs. ; We have therefore concluded that none of the current techniques is able to purify the compositions under discussion from all the impurities described above, and only if used in combination, repeatedly and with serious losses in yield can they approach the limits imposed by the various legislations, without never reach a substantial absence of any pollutant, as it would be ethically desirable, or even imperative at least in the use of the compositions in early infancy or during breastfeeding. ; The systematic elimination of each and all POPs, on the other hand, appears to be easily achievable with the method of the Invention. ; SUMMARY OF THE INVENTION; In a first aspect, the present invention relates to a method for the purification of a composition comprising monoglycerides, and / or di-glycerides and / or tri-glycerides of any origin, in which the glycerol is at least partially esterified with long-chain saturated or unsaturated fatty acids having 16-22 carbon atoms, this composition containing persistent organic environmental pollutants (POPs), in which the method comprises the steps of:; a) treating a part by weight of the above composition with at least 3 parts by weight of urea in a polar solvent, preferably a protic solvent such as a lower alcohol, such as methanol or ethanol, optionally containing up to 20% water, at a temperature close to boiling, to form an ureic complex of essentially total inclusion of the composition ; b) cooling until precipitation of the aforesaid urea complex, and isolating it, by filtration or centrifugation, from the mother liquors containing the aforesaid persistent organic environmental pollutants (POPs); ; c) obtaining a purified composition with a reduced POPs content by dissolving in water the ureic complex of inclusion and separation of the oily phase separated following dissolution or by extraction of the oil phase with an organic solvent immiscible with water, typically hexane or the like , and subsequent evaporation of the solvent until dryness, or by direct extraction from the inclusion urea complex by means of supercritical fluids, in particular carbon dioxide. Preferably, in the cooling step b) the temperature is brought to about 4 ~ 5 <C> C and the isolated urea complex is washed with the aforementioned polar solvent, previously saturated with urea and preferably cooled to a temperature of about 4-5 ° C, before being dissolved in water or extracted with supercritical fluids. Furthermore, the mother liquors and the washing waters of the aforementioned isolated urea complex can be combined and treated, as a second purification step, with an additional 2-3 parts by weight of urea (with respect to the starting composition), repeating the steps from a) a c) formation of the ureic complex of inclusion, cooling, isolation and obtaining the purified composition. ; If necessary, the mother liquors obtained from the second phase of precipitation and isolation can also be collected and combined, as well as the washing waters of the second isolated inclusion urea complex and repeat steps a) to c) again (third purification step). In one aspect of the method according to the present invention, the aforementioned long-chain fatty acids have 18-22 carbon atoms, preferably 20-22 carbon atoms, and are of the polyunsaturated type (PUFA), i.e. containing 2-6 double bonds , preferably 5-6 double bonds, belonging to the class of omega-6 and / or omega-3 acids, preferably to the class of omega-3 acids, more preferably represented by eicosapentaenoic acid (EPA, C20: 5 n-3, all cis ) and / or docosahexaenoic acid (DHA, C22: 6 n-3, all cis). ; In a further aspect, the triglycerides of the above composition have natural origin and come from vegetable seed oils mainly comprising omega-6 acids, or from fish oils, also from aquaculture, or from "krill oils" or from algae and other oil-bearing microorganisms, or from "single celi fermentation" starting from selected strains of algae or other microorganisms and mainly include omega-3 acids, in particular EPA and / or DHA, and in which the content of polyunsaturated fatty acids as defined above, in particular EPA and / or DHA, is greater than or equal to 15%, or is between 15 and 90%, or in particular it is between 15 and 65%. ; in a further aspect of the method according to the present invention, the composition comprising the aforesaid mono-, and / or di-, and / or tri-glycerides is obtained chemically and / or enzymatically, by means of selective lipases for fatty acid and its position on glycerol, starting from natural triglycerides, or from glycerides or glycerol and polyunsaturated fatty acids, through known procedures, and in which the above composition has a content of polyunsaturated fatty acids as defined above greater than or equal to 30%, or including between 30 and 90%, or in particular the content - expressed as triglycerides - of the sum of EPA and DHA is greater than or equal to 45% and the sum of the total omega-3 acids is greater than or equal to 60%, in accordance with monograph 01/2009: 1352 of the E.P.7.0. In another aspect of the method according to the present invention, the above composition comprises diglycerides, wherein the glycerol is esterified with phosphoric acid condensed with amino alcohols to form the corresponding phospholipid, in particular phosphatidylcholine and / or phosphatidylethanolamine. Preferably, step a) of the method according to the present invention, that is the treatment of the above composition with urea, is carried out using methanol as the polar solvent in a quantity equal to 4.5-7 parts by weight, or ethanol in a quantity equal to 45-65 parts by weight. ; The persistent organic environmental pollutants (POPs) mentioned above mainly include polychlorinated dibenzo-paradixins (PCDDs) and polychlorinated dibenzo-furans (PCDFs), and / or dioxin-like polychlorinated biphenyls (PCBs) (DL-PCBs) and markers, and / or polybromodiphenyl ethers (PBDEs), and / or polycyclic aromatic hydrocarbons (PAHs), and their presence in the purified composition obtained in step c) is at least twice reduced, preferably at least 5 times reduced, conveniently at least 10 times reduced, and in any case lower - for each component - to the respective limit of quantification (LOQ) with the standard GC-MS method. In other aspects, the present invention relates to a composition comprising mono-glycerides, and / or di-glycerides and / or triglycerides, as defined in claims 10, 11 and 23, as well as the melt of this composition, for the preparation, from mono-glycerides, and / or diglycerides and / or tri-glycerides, of the corresponding polyunsaturated fatty acids, or their salts, by chemical or enzymatic hydrolysis, or for the preparation of the relative C1-C3 alkyl esters, as specified in claims 12 and 13 Furthermore, the present invention relates to a composition comprising such polyunsaturated fatty acids or their C1-C3 alkyl salts or esters obtained by chemical or enzymatic hydrolysis, as specified in claims 14-16. invention relates to the use of a composition comprising the aforementioned mono-, di- and triglycerides or the corresponding polyunsaturated fatty acids or their salts or C1-C3 alkyl esters for the preparation of formulations useful as food ingredients, food and dietary supplements, foods for special medical purposes (functional foods), foods for animal use and for aquaculture, food formulations for children, cosmetic and pharmaceutical preparations, as specified in claim 17.; Finally, the present invention relates to a composition comprising the aforementioned mono-, di- and triglycerides or the corresponding polyunsaturated fatty acids or their C1-C3 alkyl salts or esters for the therapeutic uses defined in claims 18-21, as well as a pharmaceutical formulation which comprises them according to claim 22.; DETAILED DESCRIPTION; We specify that the use of urea in lipid chemistry is absolutely known. ; A standard procedure provides that an oil or fat is hydrolyzed to give the acid components, or transesterified in an alcoholic medium to give the corresponding esters, by chemical or enzymatic way, and then the polyunsaturated components are concentrated: this generally takes place by molecular distillation, extraction with supercritical fluids, or other methods, but even more often by complication with urea ("inclusion" in urea}. The use of urea, however, is presented only as a suitable means for isolation and removal of saturated and monounsaturated fatty acids, and therefore to the concentration of the polyunsaturated acids in the reaction solvent: this is therefore accompanied - among other things - by an increased concentration of foreign impurities together with the then unsaturated components. urea appears from the literature of increasing difficulty as their concentration and theirs increase relative degree of saturation: in the treatment of a mixture of fatty acids, the PUFA thus appears to be the “passive” component of the complexation. ; The profound difference with the method of the present invention therefore results, for which, for example:; —the "complexation" is carried out directly on glycerides (including natural oils and fats, or other particularly selected glycerides), instead of on fatty acids or their foreigners); - the glycerides are the “active” part of the complexation, while the PUFAs of the literature in their essence are not suitable for complexation, if not marginally, and remain unchanged in the solvent; ; —The literature procedure is aimed at increasing the concentration of PUFAs, enriching them in the mother liquors of the complexation, while it remains essentially constant during our purification process; ; - the purpose of the completion according to the new procedure is to strongly decrease, essentially cancel, the presence of environmental pollutants all officially declared teratogenic, mutagenic and carcinogenic or generally toxic, instead of simply leading to the concentration of PUFAs and their esters, according to the current standard purposes. ; On the use of urea as a complexing agent and related processes, there are many publications, among which we cite the extensive reviews of Schlenk H, "Urea inclusion compounds of fatty acids", in: Progress in the Chernistry of Fats and Other Lipids Voi Il (RT Holmar, ed.), Pergamum n Press, New York, pp. 243-267 (1954), and by Swem D, “Techniques of separation. Urea complexes ", in: Fatty Acids, Pari 3 (KS Markley, ed.), Interscience, New York, pp. 2309-2358 (1963). In particular, mention should be made of the aforementioned “Breivik 2007”, in the chapter “Concentrates”, pages 111-130. ; In relation to the glycerides, subject of this Application, Aylward F and Wood PDS, Chem & fnd. (London), 53 ((1956); Nature, 177, 146 (1956) (ref. 127 and ref. 129 by Swern, cited above, page 2337-8), and others, report the ureic complex of the mono-glyceride in position 1 of stearic acid (CI 8: 0), as well as a series of lower homologs, from caprylic acid C8: 0 to palmitic acid C16: 0. Apparently the rnonoglycerides in position 2 do not form complexes. in all cases of glycerides of saturated acids and attempts at fractionation and enrichment of various components, and not purification from environmental pollutants.; The same authors and others (Martinez Moreno JM et al, Grasas y aceites (Seville, Spain), 7, 285 (1956), ref. 131 by Swern, cited above) report that the di-glycerides in position 1,3 are capable of giving complexes with urea, while the tri-glycerides do not form complexes. tri-glycerides, already anticipated by Schlenk, cited above, page 251, is then also confirmed in the review of "Breivik 2007", page 1 18 , as an expert in the harte. ; Other authors cited by Swern, page 2338 (ref. 128, 132, 133), have studied the formation of monoglycerides by glycerolysis of vegetable oils, usually containing aryls up to C18 in length and up to 3 double bonds, and have attempted with their separation from the other glycerides by complexation with urea under certain conditions is poor. In particular Heckles J.S. and Dunlap L.H., J Am Oil Chernists <7> Soc, 32, 224, 1955 (ref. 133) report that monoglycerides of saturated and monounsaturated acids (oleic acid) form urci complexes, while those with 2 or 3 unsaturation points ( resp. linoleic and linolenic acid) do not complex. When mixed with saturated and unsaturated diglycerides, a separation by complexation is obtainable for the glycerides of saturated acids, while only a slight enrichment is obtainable with the glycerides of unsaturated acids. However, this conclusion is not shared by Mehta T.N. and Shah S.N., J Am Oil Chernists' Soc, 34, 587, 1957 (ref. 128). Also in these cases, and within the limits of the specified products, the discussion focuses only on the possibility of fractionation and enrichment through complexation. ; In recent times, Hayes D.G. et al., JAOCS, 77,207, 2000 report that mono-, di-, and tri-acylglycerols are poor templates for the formation of urea complexes (UC) compared to free fatty acids (FFA) and that their inclusion, in mixtures of acylglycerols containing FFA, even reduces the formation of UC (see Abstract), a conclusion then taken up also by experts in the art, as exemplified by "Breivik 2007", page 118. data reported on acylglycerols appear to us to be absolutely scarce, often in conflict with each other, limited (as only occasionally, if indeed it happens, do they include the PUFAs of greatest interest, with a longer chain and more unsaturated), and almost always linked to specific cases and therefore not generalizable. The ability to complex is often attributed to a single or a few factors, while in our opinion it depends on all the reaction parameters as a whole, such as e.g. the degree of glyceride substitution, the length and degree of unsaturation of the acyl, the relationship with urea. the type and volume of solvent, the precipitation temperature of the solvent, and so on, each factor interfering with all the others. ; The problem can thus be solved only experimentally, having in mind the goal to be achieved and the products to be investigated. We have thus found, through a series of experiments, that all glycerides in the broadest sense and in an essentially total way and under certain conditions in a way that is little correlated to their structure, can be complexed with urea. This then allows the precipitation of the complex and the total removal, dissolved in the solvent in an uncomplexed form, of all persistent organic pollutants (such as the dreaded dioxins and related substances, pesticides used in agriculture, etc.) that are increasingly found today widely in the animal and vegetable environment and in many foods, in particular in natural oils and fats and in the substances deriving from them, representing a continuous source of danger for human health even if present within the limits imposed by these laws and by the various Pharmacopoeias . A first aspect of the invention provides a purification method which consists in treating the glyceride of a fatty acid in a suitable solvent with an excess quantity of urea, sufficient for an essentially total complexation of the glyceride, usually greater than or equal to 3 parts. by weight and up to 6 parts by weight or more, possibly dividing the treatment into 2-3 consecutive steps, if necessary, preferably into 2 consecutive steps, and in any case until essentially total complexation is reached. The subdivision into several steps is not particularly harmful to the process because it involves only an additional filtration, as it is possible to add a further aliquot of urea directly to the filtered solution and to the washing waters of the inclusion urea complex without further manipulation. ; The treatment results in a precipitation of the complex, possibly divided into the respective 1-3 fractions, then the complex is collected by filtration or centrifugation, and carefully washed with the same solvent saturated with urea and pre-cooled around 4-5 ° C, or less, while the solvent containing all the environmental pollutants (POPs) as described above and others reported in the specialist literature, and any other impurities not covalently linked to the glyceride and not complexable, is eliminated. From the urea complex, or from the combined fractions, the purified glyceride is therefore easily recovered and essentially devoid of the aforementioned POPs. In the context of the present method, the glyceride may be a mono-, and / or di- and / or preferably a tri-glyceride (also called monoacyl-, diacyl-, and triacyl-glycerols), and these will be at least partially esterified - in the far more preferred case - with long-chain fatty acids, comprising 18-22 carbon atoms, preferably 20-22 carbon atoms, and of the polyunsaturated type, i.e. comprising 2-6 double bonds, preferably 5-6 double bonds. It refers in particular to acids belonging to the class of omega-6 and / or omega-3 acids, more preferably to the class of omega-3 acids, in particular to EPA and / or DIIA. These glycerides can have any origin and in the case of triglycerides usually represent natural oils (or fats), in particular vegetable oils, preferably fish oils and the like. ; Omega-6 acids are particularly abundant in vegetable oils and seeds, while omega-3 acids and in particular EPA and ΌΗΑ have mainly marine origin and derive essentially from fish oils, also from aquacultures, or from "krill oils" or even from algae and other oil-bearing microorganisms, or from "single cell fermentation" starting from selected strains of algae or other microorganisms. ; The content of polyunsaturated fatty acids as defined above, in particular EPA and / or DHA, is greater than or equal to 15%, or is between 15 and 90%, or in particular is between 15 and 65%. ; By way of example, we remind you that a typical content of a natural fish oil used for the production of PUFAs is represented by EPA 18% and DHA 12%. while 90% is around the maximum possible content for a glyceride having as substituents only polyunsaturated acids as described, e.g. EPA and / or DHA. Mono-glycerides and di-glycerides, on the other hand, are mainly industrial products, and all the glycerides enriched in polyunsaturated acids are also obtained by chemical and / or enzymatic processes. For this purpose, selective lipases are often used for fatty acid and its position on glycerol, starting from natural triglycerides to hydrolyze saturated and monounsaturated acids, or from various glycerides or glycerol for the action of concentrated polyunsaturated acids and using known procedures. ; In these cases the content of polyunsaturated acids will usually be greater than or equal to 30%, or between 30 and 90%, or in particular the minimum contents of the sum of EPA and DHA and of the sum of the total omega-3 acids - all expressed as triglycerides - will be respectively 45% and 60%, in accordance with monograph 01/2009: 1352 of the E.P.7.0 relating to the glycerides of omega-3 acids chemically or enzymatically reconstituted and enriched in PUFA. These raw material contents do not usually increase substantially in the course of the purification in question, except in special cases. ; From an operational point of view, the present purification process shows some similarities with the enrichment process of PUFAs and their esters by complexation with urea, being able to distinguish:; -a) a reaction phase for which a part by weight of glyceride is treated with 3-6 parts or more by weight of urea (divided into 1-3 steps) in a polar solvent, preferably a practical solvent such as a lower alcohol, such as methanol or ethanol, possibly containing up to 20% water (or others, as indicated by Swern D, already mentioned), at a temperature close to boiling, to form a ureic complex of inclusion of the glyceride; ; - b) a cooling phase at about 4 <5> -5C until precipitation of this ureic complex (or complexes), isolation by filtration or centrifugation (with elimination of the filtered mother liquors) and thorough washing of the complex or complexes combined with the same solvent saturated with urea and pre-cooled to about 4-5 ° C; ; - c) a step of obtaining a purified composition by dissolving in water of said ureic complex of inclusion and direct isolation of the oily phase separated as a result of said dissolution or by extraction of said oily phase with an organic solvent immiscible with water, typically hexane or the like and subsequent evaporation of said solvent to dryness, or again by direct extraction from said inclusion urea complex by means of supercritical fluids, in particular carbon dioxide, operations followed by optional molecular distillation. ; It will also be evident to the expert that the purpose of the entire process is totally different, as well as in phase a) the use of urea in strong excess and possibly in several steps, in phase b) the careful washing of the complex to eliminate the pollutants contained in the mother liquors incorporated, in phase c) the recovery of the purified product from the solid complex, instead of the recovery of the composition enriched in PUFA carried out on the mother liquors as taught by the "prior art". ; The purified composition according to the invention will have essentially the same composition in glycerides and therefore in fatty acids as in the raw material, but will be substantially free from all the toxic environmental pollutants described above, such as dioxins and furans, polychlorinated biphenyls, polybromodiphenyl ethers, cyclic and polycyclic hydrocarbons, simple and condensed, and other POPs known in the specialized literature. ; In particular, it is understood that each of the aforementioned substances and their sum will be at least twice, or at least 5 times reduced, or preferably at least 10 times reduced (reduction of at least 90%) with respect to the compositions from which they come, if initially present in concentrations correspondingly higher than their limit of quantification (LOQ), or still each substance will be lower than its limit of quantification (LOQ) with the standard GC-MS method for which, equating its value to "zero" (lower bound), we will define the They add "essentially zero". A value "zero" corresponds instead to a sum of data below the limit of detection (LOD). congener will be lower than its LOQ limit of quantification (essentially zero).; ~ polychlorinated dibenzo-pàra-dioxins (PCDDs, n = 7) and polychlorinated <1> dibenzo-furans (PCDFs, η <~> 10) in overall concentration less than or equal to 1.0 pg / g, value determined in accordance with the WHO toxic equivalent factors (TEFs) and expressed as toxic equivalents (TEQs}; - similar (DL-PCBs, n = 12) in total concentration lower than or equal to 5.0 pg / g, value determined as defined above (TEQs);; - PCBs marker (n = 6) in total concentration lower than or equal to 5.0 ng / g;; - polybromo-diphenyl ethers (PBDEs, tested n = 9) in complete concentration ssiva less than equal to 5.0 ng / g; ; - a sum of polycyclic aromatic hydrocarbons (PAHs, tested n-4), expressed as benzolapyrene marker substance, less than or equal to 1.0 ng / g; ; - other persistent organic pollutants (POPs) including 2,2 bis- (p-dichlorophenyl) -ethane (DDE), and / or 2,2 bis ~ {p ~ dichlorolenyl) -1,1 -dichloroeta. no (DDD), and / or 2,2 bis- (p-dichlorophenyl) - 1,1,1-trichloroethane (DDT) in a total concentration lower than or equal to 2.0 ng / g, polybromo-biphenyls (PBB) in total concentration less than or equal to 5.0 ng / g; hexachlorobenzene in a concentration less than or equal to 0.1 ng / g, and isomers of and sacloro-hexane in a total concentration less than or equal to 0.1 ng / g. ; Also all the other POPs listed by the Stockholm Convention of 2001 and by the subsequent Review Committees, could be cited here as they are in all cases of spherically "bulky" molecules, not suitable for complexation with urea, and easily eliminated quantitatively during the present purification process. ; It will then be evident that other impurities can also be eliminated in the process, if not covalently linked to the glyceride, and if not complexable with urea, such as some aliphatic hydrocarbons with a long chain and branched structure (typical squalene), some oligomers and polymers of acids fats, some sterol substances, and the like. A second aspect of the invention relates to the glyceride compositions themselves obtained according to the purification method described above. ; Among these compositions we explicitly mention a purified composition of mono-, di-, and tri-esters of omega-3 acids with glycerol, containing mainly tri-esters and a sum of EPA and DHA expressed as rriglycerides of at least 45%, and of Total omega-3 acids expressed as triglycerides of at least 60%, in accordance with the monograph 01/2009: 1352 of the E.P. 7.0, and having a highly reduced content of POPs pollutants, well beyond the limits described above (essentially absent). A third aspect of the invention is the same easily deducible from the availability of glycerides itself, preferably triglycerides, in particular natural triglycerides rich in polyunsaturated PUPA acids and more particularly in omega-3 acids such as fish oils and the others described above, all free from environmental pollutants and highly purified: this aspect therefore concerns the use of said glycerides for the chemical or enzymatic production of other compositions based on PUPA and omega-3 acids and derivatives in more or less concentrated form, according to standard literature procedures described in the chemistry of these substances. ; In fact, the current technology already provides that, starting from natural oils of various origins and therefore from complex mixtures, the most interesting acid components for pharmaceutical use or as food or dietary supplements, such as eg e.g. EPA and / or DHA, and therefore their concentration. by means of alcoholic potash, thus obtaining the corresponding potassium salts and therefore the free acids and - if desired - the alkyl esters; or more often a transesterification reaction is used, e.g. in the presence of excess alitatic alcohols, preferably C1-C3, and of an alkaline or acid catalyst, thus directly obtaining the corresponding alkyl esters of the fatty acids, and from these - if desired * - the relative acids or salts.
La successiva fase di concentrazione dei componenti più pregiati, e/o di aggiustamento del loro rapporto secondo richiesta, e/o di isolamento di un singolo componente, viene effettuata con diverse metodiche, anche abbinate, tra le quali principalmente: The subsequent phase of concentration of the most valuable components, and / or adjustment of their ratio according to request, and / or isolation of a single component, is carried out with different methods, also combined, among which mainly:
-la distillazione sotto alto vuoto, usualmente la distillazione molecolare o short path più idonea a limitare i processi termici degradativi, provvedendo ovviamente agli opportuni frazionamenti; -the distillation under high vacuum, usually the molecular distillation or short path more suitable for limiting the thermal degradative processes, obviously providing for the appropriate fractionations;
-al ermi procedimenti cromatografici, anche sotto alta pressione (HPLC), più idonei tuttavia alla scala di laboratorio o a scopo analitico; - for chromatographic processes, even under high pressure (HPLC), which are however more suitable for the laboratory scale or for analytical purposes;
-la estrazione con fluidi supercritici (SFE), usualmente con C02, anche in abbinamento con processi cromatografici (SFC) su scala preparativa e con idonea fase stazionaria, più specifici per La separazione di componenti singoli; - extraction with supercritical fluids (SFE), usually with C02, also in combination with chromatographic processes (SFC) on a preparative scale and with suitable stationary phase, more specific for the separation of single components;
-nel caso più generale ed industrialmente accettato, si ricorre tuttavia ad una reazione di complessazione con urea in vari solventi, come gli alcoli. E’ noto che l<a>urea in particolari condizioni può cristallizzare in cristalli esagonali, con formazione di canali in grado di includere le catene lineari degli acidi grassi, essenzialmente quelle degli acidi ed esteri saturi e / o monoinsaturi o a più basso grado di insaturazione. Il complesso di inclusione formatosi precipita per raffreddamento dalla soluzione alcolica e viene isolato ed eliminato, permettendo quindi di recuperare dalla soluzione una composizione arricchita in componenti poiinsaturi, come p.e. EPA e DHA (complessazione “passiva”), -in the most general and industrially accepted case, a complexation reaction is however used with urea in various solvents, such as alcohols. It is known that urea under particular conditions can crystallize in hexagonal crystals, with the formation of channels capable of including the linear chains of fatty acids, essentially those of saturated and / or monounsaturated acids and esters or with a lower degree of unsaturation. . The formed inclusion complex precipitates by cooling from the alcoholic solution and is isolated and eliminated, thus allowing to recover from the solution a composition enriched in polyunsaturated components, such as e.g. EPA and DHA ("passive" complexation),
A questa fase di concentrazione segue usualmente una distillazione molecolare finale per allontanare piccole frazioni basso- e alto -bollenti. This concentration phase is usually followed by a final molecular distillation to remove small low- and high-boiling fractions.
Tutti questi procedimenti, agevolmente adottabili anche con i gliceridi purificati dell’invenzione, sono estesamente descritti p.e. da “Breivik 2007”, Capitolo “Concentrate s”, pag. 111-130 e Riferimenti citati, e non richiedono ulteriore descrizione. All these procedures, which can be easily adopted also with the purified glycerides of the invention, are extensively described e.g. from “Breivik 2007”, Chapter “Concentrate s”, pag. 111-130 and References cited, and require no further description.
A partire da anni recenti, detti procedimenti di idrolisi o alcoolisi, oltre che per via chimica vengono anche condotti per via enzimatica, mediante lipasi selettive, anche immobilizzate: questo permette di operare in condizioni di reazione ancora più blande, inoltre - in virtù della maggiore resistenza dei PUFAs alla scissione enzimatica, rispetto agli aci ii saturi e monoinsaturi<.>è possibile isolare composizioni intermedie di gliceroli ancora parzialmente aci lati e arricchiti in PUFAs da sottoporre a reazioni di idrolisi ad acidi o di alcoolisi ad esteri in fasi separate, come pure a successivi opzionali processi di frazionamento dei componenti e/o di arricchimento per dare composizioni di acidi o loro sali, di esteri e persino di gliceridi “strutturati”, tutti arricchiti e concentrati in determinati componenti poiinsaturi. Starting from recent years, said hydrolysis or alcoholysis processes, as well as chemically are also carried out by enzymatic way, by means of selective lipases, even immobilized: this allows to operate in even milder reaction conditions, moreover - by virtue of the greater resistance of PUFAs to enzymatic cleavage, with respect to saturated and monounsaturated acids as well as subsequent optional processes of fractionation of the components and / or enrichment to give compositions of acids or their salts, of esters and even of “structured” glycerides, all enriched and concentrated in certain polyunsaturated components.
Anche questi procedimenti per catalisi enzimatica sono ben descritti da “Breivik 2007”, Capitolo “Enzvmatic processing of omega- 3 specialty oils”, pag. 141- 164, e sono chiaramente adottabili anche con le composizioni purificate delFinvcnzione. These processes for enzymatic catalysis are also well described in “Breivik 2007”, Chapter “Enzvmatic processing of omega-3 specialty oils”, p. 141-164, and are clearly adoptable also with the purified compositions of the invention.
Ne consegue pertanto che, a partire dai gliceridi purificati secondo procedimento, sarà possibile ottenére le tutte le composizioni comprendenti i corrispondenti acidi in forma libera, oppure i relativi sali, oppure ancora i relativi esteri. In aggiunta sarà ancora possibile ottenere tutte le rispettive composizioni arricchite nei componenti poiinsaturi, esattamente come fattìbile p.e. a partire dai “fish oils” naturali o altri oli, con la sola differenza che si ottengono in questo caso composizioni essenzialmente esenti dai vari inquinanti definiti POPs e dai conseguenti rischi per la salute dell’u tenie. It therefore follows that, starting from the glycerides purified according to the process, it will be possible to obtain all the compositions comprising the corresponding acids in free form, or the relative salts, or the relative esters. In addition, it will still be possible to obtain all the respective compositions enriched in the polyunsaturated components, exactly as feasible e.g. starting from natural "fish oils" or other oils, with the only difference that in this case compositions are obtained that are essentially free from the various pollutants defined as POPs and from the consequent health risks of the humankind.
Mentre gli acidi sono ottenuti per idrolisi dei gliceridi per via chimica o enzimatica, come sopra riportato, i sali degli acidi poiinsaturi sono ottenibili da questi p.e. per salificazione diretta e sono rappresentati dai sali con metalli alcalini, p.e. sodio e potassio, metalli alcalino- terrosi, p.e. calcio, con aminoacidi basici come lisina e arginili a, con meglumina, con colina e mono-, di-, e tri-etanolamina, e simili, se farmacologicamente accettabili. While the acids are obtained by chemical or enzymatic hydrolysis of the glycerides, as reported above, the salts of the polyunsaturated acids are obtainable from these e.g. by direct salification and are represented by salts with alkali metals, e.g. sodium and potassium, alkaline earth metals, e.g. calcium, with basic amino acids such as lysine and arginyl a, with meglumine, with choline and mono-, di-, and tri-ethanolamine, and the like, if pharmacologically acceptable.
Gli esteri alchilici sono ottenibili p.e. per alcoolisi chimica o enzimatica e sono rappresentati da esteri con alcoli alifatici, anche a catena molto lunga come reperibili nelle “cere" naturali, ma sono preferibilmente rappresentati da esteri con alcoli inferiori C1-C3, in particolare Pesiere etilico. Alkyl esters are obtainable e.g. by chemical or enzymatic alcoholysis and are represented by esters with aliphatic alcohols, even with a very long chain as found in natural "waxes", but they are preferably represented by esters with lower C1-C3 alcohols, in particular ethyl weight.
I gliceridi ricostituiti e concentrati in PUFA possono essere preparati per esterificazione p.e. degli acidi omega-3 concentrati e purificati con glicerolo, oppure per transesterificazione degli esteri con glicerolo. The reconstituted and concentrated PUFA glycerides can be prepared by esterification e.g. omega-3 acids concentrated and purified with glycerol, or by transesterification of esters with glycerol.
Passando a un maggiore dettaglio, si può ottenere così, a titolo di esempio, una generica composizione di lipidi e alcune composizioni degli acidi o esteri che ne possono derivare come sotto descritte. Moving on to greater detail, it is thus possible to obtain, by way of example, a generic composition of lipids and some compositions of the acids or esters that can derive from them as described below.
—Una composizione comprendente mono-gliceridi, e/o digliceridi e/o tri-gliceridi di qualsiasi origine, in cui il glicerolo è almeno parzialmente esterificato con acidi grassi a lunga catena aventi 18-22 atomi di carbonio, preferibilmente 20-22 atomi di carbonio, e dì tipo poiinsaturo (PUFA), cioè contenenti 2-6 doppi legami, preferibilmente 5-6 doppi legami, appartenenti alla classe degli acidi omega-6 e/ o omega-3, preferibilmente alla classe degli acidi omega-3, più preferibilmente rappresentati da acido eicosapentaenoico (EPA, C20:5 n-3, tutto cis ) e/o acido docosaesaenoico (DHA, C22:6 n-3, tutto cis ), in cui la composizione contiene ulteriormente i seguenti inquinanti ambientali organici persistenti (POPs): - A composition comprising mono-glycerides, and / or diglycerides and / or tri-glycerides of any origin, in which the glycerol is at least partially esterified with long chain fatty acids having 18-22 carbon atoms, preferably 20-22 carbon atoms carbon, and polyunsaturated type (PUFA), i.e. containing 2-6 double bonds, preferably 5-6 double bonds, belonging to the class of omega-6 and / or omega-3 acids, preferably to the class of omega-3 acids, plus preferably represented by eicosapentaenoic acid (EPA, C20: 5 n-3, all cis) and / or docosahexaenoic acid (DHA, C22: 6 n-3, all cis), in which the composition further contains the following persistent organic environmental pollutants ( POPs):
policloro -dibenzo-para-diossine (PCDDs) e policlorodibenzo-furani (PGDFs) in concentrazione complessiva inferiore o uguale a 1,0 pg/g, valore determinato in accordo con i fattori di tossicità equivalente (TEFs) della WHO ed espressi come equivalenti tossici (TEQs); polychlorinated dibenzo-para-dioxins (PCDDs) and polychlorinated dibenzo-furans (PGDFs) in a total concentration lower than or equal to 1.0 pg / g, value determined in accordance with the WHO toxicity equivalent factors (TEFs) and expressed as equivalents toxic (TEQs);
PCDDs, PCDFs e policloro-bifenili (PCBs) di ossi no· simili (DL PCBs) in concentrazione complessiva inferiore o uguale a 5,0 pg/g, valore determinato in accordo con i valori di TEF della WHO ed espressi come TEQs; PCDDs, PCDFs and polychlorinated biphenyls (PCBs) of non-similar oxydes (DL PCBs) in a total concentration lower than or equal to 5.0 pg / g, a value determined in accordance with the TEF values of the WHO and expressed as TEQs;
- PCBs marker in concentrazione complessiva inferiore o uguale a 5,0 ng/g; - PCBs marker in overall concentration less than or equal to 5.0 ng / g;
- poli bromo-difenile ieri (PBDEs) in concentrazione complessiva inferiore o uguale a 5,0 ng/ g; e - poly bromo-diphenyl yesterday (PBDEs) in a total concentration lower than or equal to 5.0 ng / g; And
- una somma di idrocarburi aromatici policicici (PAIfs), espressa come sostanza marker benzo[a]pirene, inferiore o uguale a 1 ,0 ng/g; - a sum of polycyclic aromatic hydrocarbons (PAIfs), expressed as a marker substance benzo [a] pyrene, less than or equal to 1.0 ng / g;
ciascuno di detti POPs essendo preferibilmente contenuto in detta composizione in concentrazione inferiore al suo limite di quantificazione LOQ con metodica standard GC-MS. each of said POPs being preferably contained in said composition in a concentration lower than its quantification limit LOQ with the standard GC-MS method.
— Una composizione che comprende EPA e/o DHA in forma di acidi liberi oppure in forma di esteri etilici, in cui la concentrazione totale è compresa tra 15 e 100%, preferibilmente tra 50 e 100% , del peso della composizione, e un contenuto di inquinanti come sopra descritti e in accordo con le composizioni purificate di gliceridi dalle quali provengono. - A composition comprising EPA and / or DHA in the form of free acids or in the form of ethyl esters, in which the total concentration is between 15 and 100%, preferably between 50 and 100%, of the weight of the composition, and a content of pollutants as described above and in accordance with the purified compositions of glycerides from which they come.
— Una composizione in cui la concentrazione in peso di EPA estere etilico, oppure di DI-IA estere etilico, è superiore o uguale a 80%, preferibilmente superiore o uguale a 90%, oppure la loro somma è superiore o uguale a 80%, preferibilmente superiore o uguale a 84%, essendo la concentrazione di EPA estere etilico superiore o uguale a 40%, la concentrazione di DHA estere etilico superiore o uguale a 34% e la somma delle concentrazioni di tutti gli esteri etilici omega-3 superiore o uguale a 90% in accordo con le specifiche della farmacopea europea (EP), e un contenuto di inquinanti come sopra descritti. - A composition in which the concentration by weight of EPA ethyl ester, or DI-IA ethyl ester, is greater than or equal to 80%, preferably greater than or equal to 90%, or their sum is greater than or equal to 80%, preferably greater than or equal to 84%, being the concentration of EPA ethyl ester greater than or equal to 40%, the concentration of DHA ethyl ester greater than or equal to 34% and the sum of the concentrations of all the omega-3 ethyl esters greater than or equal 90% in accordance with the specifications of the European Pharmacopoeia (EP), and a pollutant content as described above.
— Una composizione in cui la somma delle concentrazioni in peso di EPA estere etilico e di DHA estere etilico è compresa tra 80,0 e 88,0%, essendo la concentrazione di EPA estere etilico compresa tra 43,0 e 49,5%, ia concentrazione di DHA estere etilico compresa tra 34,7 e 40,3%, e la somma delle concentrazioni .di tutti gli esteri etilici omega-3 superiore o uguale a 90% in accordo con le specifiche della farmacopea degli Stati Uniti (USP), e un contenuto di inquinanti come sopra descritti. - A composition in which the sum of the concentrations by weight of ethyl ester EPA and ethyl ester DHA is between 80.0 and 88.0%, the concentration of ethyl ester EPA being between 43.0 and 49.5%, ia concentration of DHA ethyl ester between 34.7 and 40.3%, and the sum of the concentrations of all omega-3 ethyl esters greater than or equal to 90% in accordance with the specifications of the United States Pharmacopoeia (USP) , and a pollutant content as described above.
Definite alcune delle composizioni ottenibili per via chimica o enzimatica a partire dai gliceridi purificati, un quarto aspetto deirinvenzione comprende fi aggiunta ai gliceridi purificati e suoi derivati di idonei diluenti, eccipienti, sospendenti, eoe e/o conservanti, antiossidanti, ecc, secondo tutte le tecnologie note nelFarte per dare tutte le formulazioni note nelFarte per permettere il loro utilizzo in tutti gli usi proposti. Dette formulazioni comprendono, oltre alla loro inclusione diretta p. e. nei vari alimenti, oppure sotto forma di micro incapsulati o nano incapsulati o incocleati ottenuti secondo Farte nota, anche le formulazioni per Fuso orale - come gocce, capsule di gelatina molle, capsule auto sigillanti di gelatina dura, compresse, se necessario previo adsorbimento su sopporto solido o come complesso di inclusione, se necessario anche in formulazione gastroresistente, ecc - come noto nelFarte, oppure per Fuso topico<.>come creme, pomate, ecc ~ come pure noto nelFarte, oppure ancora per Fuso iniettivo -- come fiale per Fuso intramuscolare, flebo per infusione endovenosa lenta, ecc, previa sterilizzazione e/o se necessario previa modificazione per via chimica e/o fisica, p.e. come i gliceridi in emulsione, come pure noto nell’arte. Con riferimento al loro uso, dette composizioni purificate e le loro formulazioni saranno indirizzate alla preparazione e all’uso come alimento o ingrediente alimentare, di ogni tipo e per ogni scopo, come supplemento alimentare e dietetico, alimento per scopi medici speciali (alimento funzionale), sia nuovi che deducibili dall’uso farmaceutico, alimento per uso animale e per acquacoltura, formula alimentare per l’infanzia, cosmetico e preparato farmaceutico, tutti contenenti o arricchiti in acidi grassi a lunga catena o loro derivati, a carattere poiinsaturo o specificamente della serie omega-3. Having defined some of the compositions obtainable chemically or enzymatically starting from the purified glycerides, a fourth aspect of the invention comprises the addition to the purified glycerides and their derivatives of suitable diluents, excipients, suspensions, eoe and / or preservatives, antioxidants, etc., according to all the technologies known in the part to give all the formulations known in the part to allow their use in all the proposed uses. These formulations include, in addition to their direct inclusion, p. And. in the various foods, or in the form of micro-encapsulated or nano-encapsulated or cochleate obtained according to the known art, also the formulations for oral fusion - such as drops, soft gelatin capsules, hard gelatin self-sealing capsules, tablets, if necessary after adsorption on support solid or as an inclusion complex, if necessary also in a gastro-resistant formulation, etc. - as known in the part, or for topical fuso <.> such as creams, ointments, etc. ~ as also known in the part, or again for injection fuso - as vials for fuso intramuscular, slow intravenous infusion drip, etc., after sterilization and / or if necessary after chemical and / or physical modification, e.g. such as glycerides in emulsion, as well known in the art. With reference to their use, said purified compositions and their formulations will be addressed to the preparation and use as food or food ingredient, of every type and for every purpose, as a food and dietary supplement, food for special medical purposes (functional food) , both new and deductible from pharmaceutical use, food for animal use and aquaculture, baby food formula, cosmetic and pharmaceutical preparation, all containing or enriched in long-chain fatty acids or their derivatives, with a polyunsaturated character or specifically of omega-3 series.
Per tutti gli usi, ma in particolare il preparato per l’uso farmaceutico, sarà preferibilmente arricchito e concentrato nei componenti poiinsaturi, in particolare in EPA e/o in DHA, o loro sale, o loro estere etilico, o loro gliceride. For all uses, but in particular the preparation for pharmaceutical use, it will preferably be enriched and concentrated in the polyunsaturated components, in particular in EPA and / or DHA, or their salt, or their ethyl ester, or their glyceride.
Di grande e crescente importanza risultano gli alimenti per scopi medici speciali, o alimenti funzionali - comprendenti anche bevande e supplementi - che comprendono specifici ingredienti, come in particolare gli acidi omega-3 in ogni loro forma, in grado di impartire certi specifici benefici per la salute (fortified foods). Questi alimenti funzionali sono attualmente noti con il termine inglese FOSHU (Foods for Specified Health Use) o con il termine giapponese Tokuho. Of great and growing importance are foods for special medical purposes, or functional foods - including drinks and supplements - which include specific ingredients, such as omega-3 acids in all their forms, capable of imparting certain specific benefits for the health (fortified foods). These functional foods are currently known under the English term FOSHU (Foods for Specified Health Use) or the Japanese term Tokuho.
Scendendo al particolare, Fuso delie composizioni sarà indirizzato alla prevenzione e al trattamento di fattori di rischio per malattie cardiache, cardiovascolari e cardiocircolatorie, come Piperten sione, lipertrigliceridemia severa e moderata (risp. >500mg/dl e >200mg/dl) e 1 ipercolesterolemia , in particolare le forme famigliari e genetiche, anche in associazione con altri farmaci e in particolare con le statine, e come i difetti della coagulazione e dell’aggregazione piastrinica. Going into detail, the composition of the compositions will be aimed at the prevention and treatment of risk factors for heart, cardiovascular and cardiovascular diseases, such as piperten sione, severe and moderate hypertriglyceridemia (resp.> 500mg / dl and> 200mg / dl) and 1 hypercholesterolemia , in particular the familial and genetic forms, also in association with other drugs and in particular with statins, and as the defects of coagulation and platelet aggregation.
Un uso di grande rilievo è quello per la prevenzione e il trattamento di malattie cardiache, cardiovascolari e cardiocircolatorie, come quelle coronariche-aterosclerotiche e gli stati ischemici cardiaci e cerebrali, includendo linfarto miocardico e cerebrale e la riduzione del rischio di mortalità cardiaca improvvisa conseguente ad infarto del miocardio; quelle di origine elettrica e coinvolgenti l’insorgenza e la propagazione del ritmo cardiaco, includenti l’aritmia e la fibrillazione atriale e/o ventricolare; e quelle dovute ai difetti meccanici della pompa cardiaca, come l’insufficienza e lo scompenso cardiaco e/o la “heart failure” congestizia. A very important use is that for the prevention and treatment of heart, cardiovascular and cardiovascular diseases, such as coronary-atherosclerotic and ischemic cardiac and cerebral states, including myocardial and cerebral linfarction and the reduction of the risk of sudden cardiac mortality resulting from myocardial infarction; those of electrical origin and involving the onset and propagation of the heart rhythm, including arrhythmia and atrial and / or ventricular fibrillation; and those due to mechanical defects of the heart pump, such as heart failure and heart failure and / or congestive "heart failure".
In altri usi farmaceutici le composizioni sono utilizzate per la prevenzione e il trattamento di disordini del sistema nervoso centrale (CNS), includenti l’epilessia, le varie forme depressive, i disordini bipolari, le patologie pediatriche da difetto dell’attenzione e disordini da iperattività (ADHD), i difetti dell’apprendimento e della memoria, le varie forme di schizofrenia, la malattia di Alzheimer e le diverse forme di demenza. I miglioramenti della memoria, particolarmente in età pediatrica, risultano di estremo interesse. In other pharmaceutical uses the compositions are used for the prevention and treatment of disorders of the central nervous system (CNS), including epilepsy, various forms of depression, bipolar disorders, pediatric attention deficit disorders and hyperactivity disorders. (ADHD), learning and memory defects, various forms of schizophrenia, Alzheimer's disease and various forms of dementia. Memory improvements, particularly in children, are of great interest.
Ancora altri usi farmaceutici includono la prevenzione e ii trattamento della retinopatia e dei sintomi di secchezza, oculare, della sindrome metabolica, di difetti del metabolismo e correlati all’obesità, del diabete di tipo 2, delle disfunzioni epatiche, di malattie del tessuto connettivo e delle articolazioni, degli stati infiammatori, di malattie autoimmuni, della colite ulcerosa, della psoriasi e della malattia tumorale. Still other pharmaceutical uses include the prevention and treatment of retinopathy and symptoms of dryness, ocular, metabolic syndrome, metabolic and obesity-related defects, type 2 diabetes, liver dysfunction, connective tissue disease and joints, inflammatory states, autoimmune diseases, ulcerative colitis, psoriasis and cancer.
Un ulteriore aspetto deirinvenzione riguarda ancora il metodo di purificazione come sopra descritto, ma applicato ad una composizione che comprende digliceridi, in cui il glicerolo è esterificato con acido fosforico condensato con animino alcoli a formare il corrispondente fosfolipide, in particolare la fosfatidilcolina e/o fosfatid lieta n oi am i na. A further aspect of the invention still relates to the purification method as described above, but applied to a composition comprising diglycerides, in which the glycerol is esterified with phosphoric acid condensed with amino alcohols to form the corresponding phospholipid, in particular phosphatidylcholine and / or phosphatid. happy n oi am i na.
Questo aspetto deirinvenzione riguarda anche, ovviamente, la composizione fosfolipidica purificata che ne deriva. This aspect of the invention obviously also relates to the purified phospholipid composition resulting therefrom.
L'aspetto finale del l’invenzione riguarda infine la purificazione di una composizione comprendente un mono-gliceride, e/o di-gliceride e/o trì-glìceride di qualsiasi origine, esterificato con acidi grassi a lunga catena costituiti da 16-20, preferibilmente 18-20 atomi di carbonio, di tipo saturo e/o monoinsaturo, e la composizione purificata che si ottiene. The final aspect of the invention finally concerns the purification of a composition comprising a mono-glyceride, and / or di-glyceride and / or tri-glyceride of any origin, esterified with long-chain fatty acids consisting of 16-20, preferably 18-20 carbon atoms, of the saturated and / or monounsaturated type, and the purified composition obtained.
ESEMPI SPERIMENTALI EXPERIMENTAL EXAMPLES
L’invenzione sarà ora illustrata per mezzo di alcuni Esempi che non avranno comunque nessun carattere limitativo. The invention will now be illustrated by means of some examples that will not have any limiting character.
ESEMPIO 1 EXAMPLE 1
E<?>stato utilizzato un campione commerciale di "olio di pesce” (trigliceridi di acidi grassi) presentato in forma di capsule di gelatina molle da 0,5 g e indicato come integratore alimentare. A commercial sample of "fish oil" (fatty acid triglycerides) presented in the form of 0.5 g soft gelatin capsules and indicated as a food supplement was used.
Il contenuto dichiarato per una dose giornaliera di 4 “perle”, è qui riportato per grammo di prodotto (2 capsule) e corrisponde ad omega-3 totali pari a 350 mg, di cui EPA 180 mg e DHA 120 mg, composizione da noi confermata mediante transesterificazione in condizioni standard a medi esteri di acidi grassi (FAME) e analisi GC/MS. Gli altri componenti sono risultati essere prevalentemente acidi grassi saturi C16-C18 e acidi grassi mono insaturi. The declared content for a daily dose of 4 "pearls" is reported here per gram of product (2 capsules) and corresponds to total omega-3 equal to 350 mg, of which EPA 180 mg and DHA 120 mg, a composition we have confirmed. by transesterification under standard conditions to medium fatty acid esters (FAME) and GC / MS analysis. The other components were found to be predominantly C16-C18 saturated fatty acids and mono unsaturated fatty acids.
In assenza di altri eccipienti, l’olio è stato prelevato direttamente dalle capsule mediante siringa o per puntura e spremitura diretta e dal controllo dei principali parametri di qualità (valore di perossidi, ànisidina, colore, ecc) è stato giudicato come olio di pesce di buona qualità e debitamente raffinato per Fuso nutraceutico. In the absence of other excipients, the oil was taken directly from the capsules by syringe or by puncture and direct squeezing and from the control of the main quality parameters (value of peroxides, anisidine, color, etc.) it was judged as fish oil of good quality and duly refined for nutraceutical use.
Alcuni dati informativi sul contenuto di POPs saranno dati in confronto al prodotto purificato ottenuto al termine dello Step 1 del Procedimento. Some informative data on the content of POPs will be given in comparison with the purified product obtained at the end of Step 1 of the Procedure.
Procedimento - Step 1 Procedure - Step 1
Si caricano in un pallone 200 mL di metanolo e 100 g di urea, quindi si riscalda a riflusso sotto agitazione ottenendo una soluzione sostanzialmente limpida. 200 mL of methanol and 100 g of urea are loaded into a flask, then heated under reflux under stirring to obtain a substantially clear solution.
Si aggiungono quindi 25 g dei trigliceridi delFolio di pesce (rapporto in peso olio : urea 1 : 4), e si lascia quindi sotto agitazione e airebollizionc ancora per 5 min, ottenendo una miscela debolmente giallastra con molto olio ancora in sospensione. Then 25 g of the triglycerides of fish oil are added (ratio by weight of oil: urea 1: 4), and it is then left under stirring and boiling for a further 5 min, obtaining a slightly yellowish mixture with a lot of oil still in suspension.
Si lascia quindi raffreddare sotto agitazione ed a circa 45 °C inizia rapidamente la precipitazione del complesso desiderato, che viene raffreddato per pochi minuti con acqua corrente e quindi a riposo per 1 ora in frigorifero a circa 5<n>C per completare la precipitazione. It is then left to cool under stirring and at about 45 ° C the precipitation of the desired complex rapidly begins, which is cooled for a few minutes with running water and then at rest for 1 hour in a refrigerator at about 5 <n> C to complete the precipitation.
Alla fine il precipitato è raccolto per filtrazione su buckner e spremuto bene per separare al massimo le acque madri ni etano lic he, che vengono tenute a parte per un secondo trattamento. Non si nota nel metanolo alcuna separazione di sostanze oleose. At the end the precipitate is collected by filtration on buckner and squeezed well to separate as much as possible the mother liquors, which are kept apart for a second treatment. No separation of oily substances is noted in methanol.
Il precipitato raccolto viene lavato a fondo su buckner con 2 porzioni da 50 mL di una soluzione di urea in metanolo, ottenuta sciogliendo 16 g di urea in 100 mL di etanolo a caldo e raffreddando poi a 5 "C, ottenendo così alla fine acque di lavaggio incolori. The collected precipitate is washed thoroughly on a buckner with 2 portions of 50 mL of a solution of urea in methanol, obtained by dissolving 16 g of urea in 100 mL of hot ethanol and then cooling to 5 "C, thus obtaining at the end water of colorless washing.
Si ottengono quindi 98 g ancora umidi di precipitato, dal quale si procede direttamente al recupero dei gliceridi purificati per dissoluzione in 200 mL di soluzione al 5% di NaCl in acqua e successiva estrazione con 2 porzioni ciascuna da 50 mL di iv esano. 98 g still wet of the precipitate are obtained, from which the purified glycerides are recovered directly by dissolution in 200 mL of 5% solution of NaCl in water and subsequent extraction with 2 portions each of 50 mL of iv hexane.
Le 2 fasi organiche vengono separate dalla fase acquosa e riunite, quindi il n-esano viene evaporato a secchezza a circa 35 °C ed a pressione ridotta fino a peso costante, ottenendo 21.2 g di residuo costituito da olio di pesce purificato che viene conservato attorno a 5 °C in atmosfera di azoto. The 2 organic phases are separated from the aqueous phase and reunited, then the n-hexane is evaporated to dryness at about 35 ° C and at reduced pressure to constant weight, obtaining 21.2 g of residue consisting of purified fish oil which is stored around at 5 ° C in a nitrogen atmosphere.
II prodotto è usualmente utilizzato tal quale, eventuali tracce di solventi possono essere eliminate, se desiderato, con metodi noti e con rese quantitative. The product is usually used as it is, any traces of solvents can be eliminated, if desired, with known methods and with quantitative yields.
L’analisi GCMS dei corrispondenti esteri metilici FAME dimostra che la composizione è simile a quella del prodotto di partenza. The GCMS analysis of the corresponding FAME methyl esters shows that the composition is similar to that of the starting product.
L’analisi dei POPs viene qui riportata solo come numero di congeneri non dosabili, in quanto il loro contenuto è inferiore al loro LOQ, rispetto al numero di controlli effettuati. Per confronto vengono riportati i corrispondenti valori della materia prima nelle capsule originali, in forma cautelativa senza riportare i valori assoluti trattandosi di prodotto regolarmente autorizzato alla commercializzazione. The analysis of POPs is reported here only as the number of undetectable congeners, as their content is lower than their LOQ, compared to the number of checks performed. For comparison, the corresponding values of the raw material in the original capsules are reported, as a precaution without reporting the absolute values since it is a product duly authorized for marketing.
Prodotto Materia purificato prima Product Purified raw material
Diossine 7 / 7 7 / 7 Dioxins 7/7 7/7
Furani 10 / 10 8 / 10 Furani 10/10 8/10
PCB diossino-simili 12 / 12 1 / 12 Dioxin-like PCBs 12/12 1/12
PCB markers 6 / 6 3 / 6 PCB markers 6/6 3/6
PBDE 9 / 9 2 / 9 PBDE 9/9 2/9
PAH 4 / 4 0 / 4 PAH 4/4 0/4
Nel prodotto purificato, tutti i congeneri di inquinanti ambientali tossici e cancerogeni (POPs: persisi ent organic pollutants) sono risultati inferiori al limite dosabile ed essenzialmente assenti, in 48 casi su 48. Questo porta a ritenere che la complessazione con urea agisca come una sorta di cromatografia “size exclusion” e che questa purificazione può essere estesa a tutte le classi di inquinanti ambientali di analoga struttura e ingombro sierico, senza rischio di eccezioni. In the purified product, all the congeners of toxic and carcinogenic environmental pollutants (POPs: persisi ent organic pollutants) were found to be below the measurable limit and essentially absent, in 48 out of 48 cases. This leads us to believe that the complexation with urea acts as a sort size exclusion chromatography and that this purification can be extended to all classes of environmental pollutants of similar structure and serum size, without risk of exceptions.
In relazione al prodotto di riferimento, si può notare che il contenuto di diossine e furani è accettabile, essendo la normativa di controllo più rigorosa e vigente da più tempo. Per altri inquinanti, altrettanto tossici, la situazione è decisamente peggiore e presenta alcuni picchi di concentrazione ad elevato rischio per latente e scarsa aderenza alle norme etiche e legislative. In relation to the reference product, it can be noted that the dioxin and furan content is acceptable, as the control legislation has been more rigorous and has been in force for the longest time. For other pollutants, equally toxic, the situation is decidedly worse and presents some concentration peaks with high risk due to latent and poor adherence to ethical and legislative standards.
Sten 2 Sten 2
Le acque madri metanoliche isolate per filtrazione del complesso di inclusione dello step 1 in urea, riunite con il metanolo di lavaggio come sopra descritto, vengono addizionate con altri 5Q g di urea (rapporto totale in peso trigliceridi : urea di 1 : 6) e portate airebollizione per 5 minuti sotto lenta agitazione ottenendo soluzione con poco materiale oleoso in sospensione. The methanolic mother liquors isolated by filtration of the inclusion complex of step 1 in urea, combined with the washing methanol as described above, are added with another 5Q g of urea (total ratio by weight of triglycerides: urea of 1: 6) and flow re-boil for 5 minutes under slow stirring obtaining a solution with a little oily material in suspension.
Si lascia raffreddare sempre sotto agitazione, ottenendo a circa 45 °C una rapida precipitazione, e quindi a riposo per 1 ora in frigorifero a circa 5 "C. It is allowed to cool, always under stirring, obtaining rapid precipitation at about 45 ° C, and then at rest for 1 hour in the refrigerator at about 5 "C.
Alla fine si filtra il precipitato su buckner, si allontanano a fondo le acque madri, e si lava bene con 2 porzioni da 50 mL di una soluzione di urea in metanolo ottenuta come sopra descritto e preraffreddata a 5 “C. At the end the precipitate is filtered on buckner, the mother liquors are removed thoroughly, and washed well with 2 portions of 50 mL of a solution of urea in methanol obtained as described above and pre-cooled to 5 “C.
Si ottiene così un abbondante precipitato, dal quale ancora umido si recupera ulteriore prodotto purificato come descritto nello Step 1 , mediante dissoluzione in 200 mL di soluzione acquosa al 5% di NaCl ed estrazione con 2 porzioni da 50 mL di n-esano. An abundant precipitate is thus obtained, from which further purified product is recovered as described in Step 1, by dissolving in 200 mL of a 5% aqueous solution of NaCl and extraction with 2 portions of 50 mL of n-hexane.
L’evaporazione a secchezza degli estratti in n-esano come sopra descritto porta a un ulteriore residuo oleoso di 3,3 g, costituito anche esso da olio di pesce purificato, che viene conservato a 5 °C sotto azoto. The dry evaporation of the n-hexane extracts as described above leads to a further oily residue of 3.3 g, also consisting of purified fish oil, which is stored at 5 ° C under nitrogen.
L’analisi GCMS conferma la purezza del prodotto e dimostra che la sua composizione è essenzialmente uguale a quella ottenuta nello Step 1, per cui i prodotti vengono riuniti, portando così a una resa totale di 24,5 g. The GCMS analysis confirms the purity of the product and shows that its composition is essentially the same as that obtained in Step 1, so the products are combined, thus leading to a total yield of 24.5 g.
L'analisi dei POPs dimostra che il loro contenuto è ancora non dosabile ed “essenzialmente zero<5>’, in 48 casi su 48. The analysis of POPs shows that their content is still undetectable and "essentially zero <5>", in 48 cases out of 48.
ESEMPIO 2 EXAMPLE 2
E' stato utilizzato un campione commerciale di “olio di pesce” (trigliceridi di acidi grassi) fornito in bulk e definito come se mi- raffinato, batch 200907. Contenuto in EPA (valutato come area GC, FAME) 17%, contenuto in DHA 11,5%, normale quadro GC. Non è noto a quali trattamenti fisici e chimici fosse già stato sottoposto, tra quelli usuali in questa tecnologia (deodorizzazione in corrente di vapore, distillazione, winterizzazione, sbiancamento e trattamento con carbone, trattamento con silice, lavaggio alcalino, degommazione}. A commercial sample of "fish oil" (fatty acid triglycerides) was used, supplied in bulk and defined as if mi-refined, batch 200907. EPA content (evaluated as GC area, FAME) 17%, DHA content 11.5%, normal GC framework. It is not known which physical and chemical treatments it had already undergone, among those usual in this technology (deodorization in a current of steam, distillation, winterization, bleaching and treatment with coal, treatment with silica, alkaline washing, degumming}.
Al controllo analitico molti valori risultavano superiori o molto superiori ai valori normali (perossidi, anisidina, Totox, ecc.), il colore era arancio intenso. L’analisi dei POPs dimostrava che 42 congeneri tra quelli controllati (n=48) erano presenti e superiori al LOQ, in alcuni casi con valori individuali così elevati da portare i valori complessivi TEQs decine di volte sopra i limiti comunemente tollerati, e altri ancora. At the analytical control many values were higher or much higher than normal values (peroxides, anisidine, Totox, etc.), the color was intense orange. The analysis of POPs showed that 42 congeners among those controlled (n = 48) were present and above the LOQ, in some cases with individual values so high as to bring the overall TEQs values tens of times above the commonly tolerated limits, and others again .
La purificazione di questo prodotto è stata effettuata seguendo il procedimento dell 'Esempio 1, in 2 steps. La resa complessiva è risultata del 95%, il colore giallo chiaro e le prime analisi di qualità indicavano che le proprietà chimiche e organolettiche della composizione a seguito del procedimento di purificazione erano fortemente migliorate (deodorizzazione, sbiancameli to, assenza di prodotti di ossidazione e materiale polimerico e oligomerico, ecc), rendendo così superflua una parte dei procedimenti tecnologici standard sopra citati. The purification of this product was carried out following the procedure of Example 1, in 2 steps. The overall yield was 95%, the light yellow color and the first quality analyzes indicated that the chemical and organoleptic properties of the composition following the purification process were greatly improved (deodorization, bleaching, absence of oxidation products and material polymeric and oligomeric, etc.), thus making a part of the standard technological procedures cited above superfluous.
Soprattutto, in conseguenza dello specifico scopo della purificazione, le analisi delle 6 classi di POPs routinariamente controllate, confermavano che i 48 congeneri delle varie famiglie erano tutti inferiori ai loro limite di quantificazione LOQ e quindi essenzialmente assenti. Above all, as a consequence of the specific purpose of the purification, the analyzes of the 6 classes of POPs routinely checked confirmed that the 48 congeners of the various families were all below their LOQ quantification limit and therefore essentially absent.
Pure assenti si rivelavano alcuni pesticidi della famiglia del 2,2 bis -(p-diclorofcnil)- etano variamente clorurati, come il DDT, e così pure i bifenili polibromurati e gli esacloro derivati del benzene e del cicloesano, presenti invece in concentrazione attorno a l-2ng/g nel prodotto di partenza. Also absent were some pesticides of the family of 2,2 bis - (p-dichlorofcnil) - ethane variously chlorinated, such as DDT, as well as polybrominated biphenyls and hexachlor derivatives of benzene and cyclohexane, present instead in concentrations around l-2ng / g in the starting product.
ESEMPIO 3 EXAMPLE 3
E<7>stato utilizzato un campione commerciale di "olio di pesce azzurro” (a base di acidi grassi polinsaturi della serie omega-3) presentato in forma di capsule di gelatina molle da 1,0 g (peso totale 1313 mg) e indicato come integratore alimentare che contribuisce alla normale funzionalità cardiaca, cerebrale e visiva. Composizione (espressa come etil esteri): EPA 360mg, DHA 180mg, omega-3 totali 630mg, vitamina E 5,5mg. A commercial sample of "blue fish oil" (based on polyunsaturated fatty acids of the omega-3 series) presented in the form of soft gelatin capsules of 1.0 g (total weight 1313 mg) was used and indicated as a food supplement that contributes to normal heart, brain and visual function Composition (expressed as ethyl esters): EPA 360mg, DHA 180mg, total omega-3 630mg, vitamin E 5.5mg.
Si tratta quindi di un normale olio di pesce raffinato e arricchito in omega-3 presumibilmente mediante catalisi indotta da specifiche lipasi e in presenza di una composizione di EPA e DHA, o con altro metodo della letteratura. It is therefore a normal fish oil refined and enriched in omega-3 presumably by catalysis induced by specific lipases and in the presence of a composition of EPA and DHA, or by another method of the literature.
Dopo purificazione per complessazione totale in urea e recupero dei gliceridi dal complesso, secondo procedimento dell’Esempio 1, si confermava ancora una volta la sostanziale assenza di tutti i POPs controllati, come sopra riportato. After purification by total complexation in urea and recovery of glycerides from the complex, according to the procedure of Example 1, the substantial absence of all controlled POPs was once again confirmed, as reported above.
ESEMPIO 4 EXAMPLE 4
Mediante esterificazione diretta con gliceroìo di una composizione concentrata a circa 80% dì acidi poiinsaturi omega-3 (PUFA n-3: EPA 40% circa, DHA 30%, DPA 5%, C18:4 8%, e altri), più altri componenti saturi e monoinsaturi, è stata ottenuta una preparazione circa di pari contenuto di monogliceridi, digliceridi e trigliceridi ricchi in acidi omega-3 di buona qualità, ma confermata per la presenza di inquinanti ambientali POPs (28/48). La sintesi è stata condotta in presenza di una preparazione immobilizzata di lipasi da Candida antartica (NV-435), e i rapporti dei componenti, le temperature e i tempi di reazione adottati sono stati quelli riportati per Esperimento 14 di Noriega-Rodriguez J.A. et al, J. Food Res. 2(6), 97, 2013. By direct esterification with glycerol of a composition concentrated at about 80% of omega-3 polyunsaturated acids (PUFA n-3: EPA 40% about, DHA 30%, DPA 5%, C18: 4 8%, and others), plus others saturated and monounsaturated components, a preparation of approximately equal content of monoglycerides, diglycerides and triglycerides rich in good quality omega-3 acids was obtained, but confirmed for the presence of environmental pollutants POPs (28/48). The synthesis was carried out in the presence of an immobilized preparation of antarctic Candida lipase (NV-435), and the component ratios, temperatures and reaction times adopted were those reported for Experiment 14 by Noriega-Rodriguez J.A. et al, J. Food Res. 2 (6), 97, 2013.
Il prodotto ottenuto ed analizzato mediante HPLC, come indicato dallo stesso Autore, è stato utilizzato tal quale, senza ulteriore manipolazione, ed è stato sottoposto a purificazione come descritto in Esempio 1. The product obtained and analyzed by HPLC, as indicated by the same Author, was used as it is, without further manipulation, and was subjected to purification as described in Example 1.
Ancora una volta si confermava che i 48 congeneri delle 6 classi di POPs controllate erano tutti senza alcuna eccezione al di sotto del loro limite di quantificazione. Once again it was confirmed that the 48 congeners of the 6 classes of POPs checked were all without exception below their limit of quantification.
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