SE433038B - PROCEDURE FOR CLEANING LIPOSOM SUSPENSIONS FROM NON-CONTAINED MEDICINAL PRODUCTS - Google Patents

PROCEDURE FOR CLEANING LIPOSOM SUSPENSIONS FROM NON-CONTAINED MEDICINAL PRODUCTS

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Publication number
SE433038B
SE433038B SE7810109A SE7810109A SE433038B SE 433038 B SE433038 B SE 433038B SE 7810109 A SE7810109 A SE 7810109A SE 7810109 A SE7810109 A SE 7810109A SE 433038 B SE433038 B SE 433038B
Authority
SE
Sweden
Prior art keywords
suspensions
liposom
cleaning
procedure
activated
Prior art date
Application number
SE7810109A
Other languages
Swedish (sv)
Other versions
SE7810109L (en
Inventor
L Moro
G Neri
A Rigamonti
Original Assignee
Farmaceutici Italia
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Farmaceutici Italia filed Critical Farmaceutici Italia
Publication of SE7810109L publication Critical patent/SE7810109L/en
Publication of SE433038B publication Critical patent/SE433038B/en

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Classifications

    • AHUMAN NECESSITIES
    • A61MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61KPREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K9/00Medicinal preparations characterised by special physical form
    • A61K9/10Dispersions; Emulsions
    • A61K9/127Liposomes
    • A61K9/1277Processes for preparing; Proliposomes

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  • Health & Medical Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Medicinal Chemistry (AREA)
  • Pharmacology & Pharmacy (AREA)
  • Epidemiology (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Animal Behavior & Ethology (AREA)
  • General Health & Medical Sciences (AREA)
  • Public Health (AREA)
  • Veterinary Medicine (AREA)
  • Medicinal Preparation (AREA)

Description

7810109-4 molekylarfilter Sepharose GB. 7810109-4 molecular filter Sepharose GB.

Liposomerna elueras först medan det fria läkemedlet hålles tillbaka genom sepharosen.The liposomes are first eluted while the free drug is retained by the sepharose.

Ett annat lämpligt förfarande är ultracentrifugering vid 100.000 g och efterföljande tvättning, alltid med ultra- centrifugering, med buffrad lösning. Det har visat sig att liposomerna vid djur kan transportera antitumöralt verksamt läkemedel selektivt till neoplastiska celler.Another suitable method is ultracentrifugation at 100,000 g and subsequent washing, always with ultracentrifugation, with buffered solution. It has been shown that the liposomes in animals can transport antitumor active drug selectively to neoplastic cells.

Föreliggande uppfinning avser ett nytt förfarande för separation av liposomer från icke-inneslutet läkemedel.The present invention relates to a novel process for the separation of liposomes from non-entrapped drug.

Därvid användes jonbytarhartser och adsorberande hartser utan att användning av kromatografi är nödvändig. Jonbytarv hartset tillsättes liposomsuspensionen av läkemedlet som måste renas och det hela skakas l till 120 minuter.Ion exchange resins and adsorbent resins were used without the need for chromatography. The ion exchange resin is added to the liposome suspension of the drug which must be purified and the whole is shaken for 1 to 120 minutes.

Den fria liposomsuspensionen erhålles efter filtrering genom ett poröst skikt, som håller tillbaka hartset på vilket det fria läkemedlet är absorberat. Detta nya renings- förfarande vid vilket jonbytarhartser användes uppvisar den stora fördelen att mycket koncentrerade liposomsuspensioner (upp till 4 mg/ml adriamycinhydroklorid) kan erhållas vilka icke kan uppnås genom kromatografi med ett molekylarfilter (maximalt 200Y7ml. Den sålunda erhållna liposomsuspensionen är mycket stabil och har i motsats till de suspensioner som erhålles genom centrifugering med högt varvtal icke någon benägenhet för sedimentation. Den definitiva kemiska stabiliseringen uppnås genom frystorkning av liposomsuspen- sionen.The free liposome suspension is obtained after filtration through a porous layer, which holds back the resin on which the free drug is absorbed. This new purification process in which ion exchange resins are used has the great advantage that highly concentrated liposome suspensions (up to 4 mg / ml adriamycin hydrochloride) can be obtained which cannot be obtained by chromatography with a molecular filter (maximum 200 .mu.m ml. The highly stable liposome suspension thus obtained In contrast to the suspensions obtained by high speed centrifugation, there is no tendency for sedimentation.The definitive chemical stabilization is achieved by freeze-drying the liposome suspension.

Uppfinningcn åskådliggöres närmare medelst följande exempel.The invention is further illustrated by the following examples.

Exempel l: I en förtvålningskolv löstes 1,5 g ägglecitin, 0,4 g koleste- rin och 0,2 g dicetylfosfat i kloroform och lösningsmedlet «--».. .....--.-_.___......____a_..._.__.._ . ___ ,,_ 781.01 09-13 avdunstades till torrhet. En adriamycinhydrokloridlösning (koncentration 20 mg/ml) i 0,007 N buffertfosfat tillsattes därpå och lösningen skakades under 1 minut med ultraljud.Example 1: In a saponification flask, 1.5 g of egg lecithin, 0.4 g of cholesterol and 0.2 g of dicetyl phosphate in chloroform and the solvent were dissolved. ....____ a _..._.__.._. ___ ,, _ 781.01 09-13 was evaporated to dryness. An adriamycin hydrochloride solution (concentration 20 mg / ml) in 0.007 N buffer phosphate was then added and the solution was shaken for 1 minute with ultrasound.

Därefter fick suspensionen stå under 30 minuter vid rums- temperatur och under kväveatmosfär varpå 2 g BDH IR-50-harts, som i förväg aktiverats i natriumformen, tillsattes (vikten hänför sig till torrvikten och motsvarar 5 ml expan- derat harts). Innehållet i kolven skakades under 30 minuter.The suspension was then allowed to stand for 30 minutes at room temperature and under a nitrogen atmosphere, after which 2 g of BDH IR-50 resin, previously activated in the sodium form, were added (the weight refers to the dry weight and corresponds to 5 ml of expanded resin). The contents of the flask were shaken for 30 minutes.

Därefter filtrerades suspensionen genom ett poröst skikt (G 1). Liposomer med en varierande storlek av från 0,5 till 2 mikron Ofllmed en halt av 60 % av utgångsmängden adriamycin erhölls. De gjordes stabila medelst frystorkning.Then the suspension was filtered through a porous layer (G 1). Liposomes with a varying size of from 0.5 to 2 microns of oil with a content of 60% of the starting amount of adriamycin were obtained. They were made stable by freeze-drying.

Exempel 2.Example 2.

Samma förfaringssätt som i exempel l användes och samma mängder adriamycin och lipider användes varvid skakningen med ultraljud förlängdes till 10 minuter för erhållande av liposomer med en storlek mindre än l mikron. Ett icke- -granulärt harts valdes, som likaledes uppvisar funktionen av ett filter, eftersom den totala kroppen av liposomerna uppvisar en storlek som inte är helt homogen. I överens- stämmelse med detta infördes i kolven lO ml Dowex 5OW-4 (100-200 mesh) harts som i förväg aktiverats i natrium- formen. Efter filtreringen erhölls en suspension som inne- höll liposomer med en storlek av 0,2-0,8 mikron samt 75 % av utgångsadriamycinen. Därefter gjordes liposomerna stabila medelst frystorkning.The same procedure as in Example 1 was used and the same amounts of adriamycin and lipids were used, the ultrasound shaking being extended to 10 minutes to obtain liposomes with a size smaller than 1 micron. A non-granular resin was chosen which also exhibits the function of a filter, since the total body of the liposomes exhibits a size which is not completely homogeneous. Accordingly, 10 ml of Dowex 5OW-4 (100-200 mesh) resin previously activated in the sodium form was introduced into the flask. After filtration, a suspension was obtained which contained liposomes with a size of 0.2-0.8 microns and 75% of the starting adriamycin. Thereafter, the liposomes were made stable by lyophilization.

Exempel 3.Example 3.

En lösning av 5-fluoruracil med en koncentration av 10 mg/ml i 0,007 N buffertfosfat och med pH-värde av 8 hälldes i förtvålningskolven som innehöll lipidfasen, vilken var fram- ställd såsom beskrevs ovan. Suspensionen behandlades såsom- i exempel l varvid man som filterharts använde lO ml Amberlite RA-400 (Cl) som i förväg aktiverats som klor- hydrat. De sålunda erhållna liposomerna gjordes stabila 7810109-4 medelst frystorkning.A solution of 5-fluorouracil having a concentration of 10 mg / ml in 0.007 N buffer phosphate and having a pH of 8 was poured into the saponification flask containing the lipid phase, which was prepared as described above. The suspension was treated as in Example 1 using 10 ml of Amberlite RA-400 (Cl) previously activated as chlorohydrate as the filter resin. The liposomes thus obtained were made stable by lyophilization.

Exemgel 4.Exemgel 4.

Liposomer_av 5-fluoruracil framställdes, såsom beskrevs ovan, under användning av 1,5 g ägglecitin, 0,4 g kolesterin och 0,2 g stearylamin. Som reningssystem användes 10 ml Dowexšà-harts (50-100 mesh) som var aktiverat i förväg. De sålunda erhållna liposomerna stabiliserades medelst frys- torkning.Liposomes of 5-fluorouracil were prepared as described above using 1.5 g of egg lecithin, 0.4 g of cholesterol and 0.2 g of stearylamine. 10 ml of pre-activated Dowexšà resin (50-100 mesh) were used as the purification system. The liposomes thus obtained were stabilized by freeze-drying.

Exemgel 5.Example 5.

En adriamycin-liposomsuspension framställdes under samma betingelser och under användning av samma mängder som beskrevs i exempel 2 och renades under användning av l5 g adsorberande XAD -harts från Rohm & Haas, som infördes direkt i framställningskolven.An adriamycin liposome suspension was prepared under the same conditions and using the same amounts as described in Example 2 and purified using 15 g of Rohm & Haas adsorbent XAD resin, which was introduced directly into the preparation flask.

Efter skakning under 40 minuter och filtrering genom sinterfilterglas(3 l erhölls en liposomsuspension som inne- höll ungefär 50 % av utgångsmängden adriamycin; denna suspension stabiliserades medelst frystorkning.After shaking for 40 minutes and filtering through sintered filter glass (3 l, a liposome suspension was obtained which contained about 50% of the initial amount of adriamycin; this suspension was stabilized by freeze-drying.

Claims (4)

7810109-4 PATENTKRAV7810109-4 PATENT REQUIREMENTS 1. l. Förfarande för rening av liposomsuspensioner från icke- -inneslutet läkemedel k ä n n e t e c k n a t därav, att jonbytarhartser användes både i aktiverad cch även i icke-akti- verad form i saltform och, om så önskas , frystorkas liposomsuspensionerna för stabilisering.1. A process for purifying liposome suspensions from non-entrapped drug is characterized in that ion exchange resins are used both in activated and non-activated form in salt form and, if desired, the liposome suspensions are lyophilized for stabilization. 2. Förfarande enligt patentkravet 1, k ä n n e t e c k n a t därav, att man använder absorberande polymersubstan§er.2. A method according to claim 1, characterized in that absorbent polymeric substances are used. 3. Förfarande enligt patentkravet l, k ä n n e t e c k n a t därav, att starka eller svaga hartser av anjontyp användes.3. A method according to claim 1, characterized in that strong or weak anion-type resins are used. 4. Förfarande enligt patentkravet l, k ä n n e t e c k n a t därav, att starka eller svaga hartser av katjontyp användes. . .__ _..,.__..._..._..__.__.... 7810109-4 SAMMANDRAG. Föreliggande uppfinning avser ett nytt förfarande för fram- ställning av injicerbara liposomer varvid liposomsuspensioner renas från icke-inneslutet läkemedel varvid jonbytarhartser användes såväl i aktiverad som även i iclše-aktiverad form i saltform.4. A method according to claim 1, characterized in that strong or weak cation-type resins are used. . .__ _ .., .__..._..._..__.__.... 7810109-4 SUMMARY. The present invention relates to a novel process for the preparation of injectable liposomes in which liposome suspensions are purified from non-entrapped drug using ion exchange resins in both activated and iclet-activated form in salt form.
SE7810109A 1977-09-30 1978-09-26 PROCEDURE FOR CLEANING LIPOSOM SUSPENSIONS FROM NON-CONTAINED MEDICINAL PRODUCTS SE433038B (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
IT2814777 1977-09-30

Publications (2)

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SE7810109L SE7810109L (en) 1979-03-31
SE433038B true SE433038B (en) 1984-05-07

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Application Number Title Priority Date Filing Date
SE7810109A SE433038B (en) 1977-09-30 1978-09-26 PROCEDURE FOR CLEANING LIPOSOM SUSPENSIONS FROM NON-CONTAINED MEDICINAL PRODUCTS

Country Status (13)

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JP (1) JPS5459314A (en)
AT (1) AT368879B (en)
AU (1) AU528260B2 (en)
BE (1) BE870882A (en)
CA (1) CA1116518A (en)
CH (1) CH642540A5 (en)
DE (1) DE2842608C2 (en)
DK (1) DK154048C (en)
FR (1) FR2404454A1 (en)
GB (1) GB2004745B (en)
NL (1) NL7809709A (en)
SE (1) SE433038B (en)
ZA (1) ZA785510B (en)

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT1110989B (en) * 1979-01-19 1986-01-13 Erba Farmitalia PHARMACEUTICAL FORMS CONSTITUTED BY LIPOSOMES AND RELATED PROCEDURES
JPS5775916A (en) * 1980-10-29 1982-05-12 Nippon Chemiphar Co Ltd Coenzyme q pharmaceutical and its preparation
JPS5782310A (en) * 1980-11-11 1982-05-22 Tanabe Seiyaku Co Ltd Production of liposome preparation
CA1270198C (en) * 1984-08-08 1990-06-12 Marcel B Bally Encapsulation of antineoplastic agents in liposomes
US4619795A (en) * 1984-12-24 1986-10-28 Technicon Instruments Corp. Method for preparing lipid vesicles
DE4038075C1 (en) * 1990-11-29 1992-03-19 B. Braun Melsungen Ag, 3508 Melsungen, De Encapsulating solid or liq. lipophilic agents - comprises mixing hydration medium with phospholipid increasing temp. to above soln. phase change temp. and adding remaining medium
DE10137515A1 (en) * 2001-07-26 2003-02-13 Diagnostikforschung Inst Production of pharmaceutical preparations in charged particle dispersion form, e.g. contrast agent dispersion, including separation of particles using ion exchangers or by electrophoresis

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2249552A1 (en) * 1971-10-12 1973-05-30 Inchema S A PROCESS FOR THE INCAPSULATION OF IN PARTICULAR WATER-SOLUBLE COMPOUNDS
GB1523965A (en) * 1976-03-19 1978-09-06 Ici Ltd Pharmaceutical compositions containing steroids

Also Published As

Publication number Publication date
DK154048B (en) 1988-10-10
DE2842608A1 (en) 1979-04-12
AT368879B (en) 1982-11-25
BE870882A (en) 1979-03-29
FR2404454A1 (en) 1979-04-27
JPS5459314A (en) 1979-05-12
ZA785510B (en) 1979-09-26
DE2842608C2 (en) 1986-02-06
SE7810109L (en) 1979-03-31
CH642540A5 (en) 1984-04-30
JPS6134402B2 (en) 1986-08-07
FR2404454B1 (en) 1980-06-20
GB2004745B (en) 1982-04-07
GB2004745A (en) 1979-04-11
AU4017478A (en) 1980-04-03
NL7809709A (en) 1979-04-03
DK425478A (en) 1979-03-31
CA1116518A (en) 1982-01-19
DK154048C (en) 1989-03-13
AU528260B2 (en) 1983-04-21
ATA693178A (en) 1982-04-15

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