DK154605B - METHOD OF MANUFACTURING SYNTHETIC BLOOD - Google Patents
METHOD OF MANUFACTURING SYNTHETIC BLOOD Download PDFInfo
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- DK154605B DK154605B DK554675AA DK554675A DK154605B DK 154605 B DK154605 B DK 154605B DK 554675A A DK554675A A DK 554675AA DK 554675 A DK554675 A DK 554675A DK 154605 B DK154605 B DK 154605B
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K9/00—Medicinal preparations characterised by special physical form
- A61K9/0012—Galenical forms characterised by the site of application
- A61K9/0019—Injectable compositions; Intramuscular, intravenous, arterial, subcutaneous administration; Compositions to be administered through the skin in an invasive manner
- A61K9/0026—Blood substitute; Oxygen transporting formulations; Plasma extender
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K31/00—Medicinal preparations containing organic active ingredients
- A61K31/02—Halogenated hydrocarbons
- A61K31/025—Halogenated hydrocarbons carbocyclic
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- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
- A61P7/00—Drugs for disorders of the blood or the extracellular fluid
- A61P7/08—Plasma substitutes; Perfusion solutions; Dialytics or haemodialytics; Drugs for electrolytic or acid-base disorders, e.g. hypovolemic shock
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Description
DK 154605 BDK 154605 B
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Behovet for syntetisk blod er velkendt. Blod bliver dyrere og dyrere, det er letfordærveligt, det skal passe til modtagerens blodtype, og transfusionen selv kan forårsage leverbetændelse, hvis der ikke overholdes strenge procedurer.The need for synthetic blood is well known. Blood becomes more expensive and more expensive, it is perishable, it must fit the recipient's blood type, and the transfusion itself can cause hepatitis if strict procedures are not observed.
5 Desuden synes bloddonationer at være noget sæsonprægede, og de falder ofte ikke sammen med de sædvanligvis tilfældige behov for blod.5 In addition, blood donations appear to be somewhat seasonal, and they often do not coincide with the usually random need for blood.
Et syntetisk blod skal have flere forskellige egenskaber. Først og fremmest, og ganske indlysende, skal det 10 have en høj oxygen- og carbondioxid-opløselighed, da dets væsentlige funktion er at transportere oxygen og carbondioxid. Et syntetisk blod skal også være ugiftigt, og i denne sammenhæng er det ønskeligt, at der ikke efterlades nogen rest af det syntetiske blod i livsvigtige organer, 15 når det erstattes med naturligt blod.A synthetic blood must have several different properties. First of all, and quite obviously, it must have a high oxygen and carbon dioxide solubility, since its essential function is to transport oxygen and carbon dioxide. A synthetic blood must also be non-toxic, and in this context it is desirable that no residual of the synthetic blood be left in vital organs when replaced with natural blood.
En anden nødvendig egenskab ved bloderstatninger er, at de skal opfylde bestemte krav til damptrykket. Bloderstatningerne forlader legemet ved udånding og fordampning gennem huden. Fortrinsvis forlader bloderstatningen legemet 20 med omtrent samme hastighed som den, hvormed nyt, naturligt blod dannes af legemet. Hvis erstatningens damptryk er for lavt, forbliver den i legemet for længe, medens den, hvis det er for højt, fordamper gennem hele legemets overflade og skaber problemer beslægtet med dykkersyge.Another necessary feature of blood substitutes is that they must meet certain vapor pressure requirements. The blood substitutes leave the body through exhalation and evaporation through the skin. Preferably, the blood substitute leaves the body 20 at about the same rate as that at which new, natural blood is formed by the body. If the substitute vapor pressure is too low, it stays in the body for too long, while, if it is too high, it evaporates throughout the body surface and causes problems related to diving.
25 Bloderstatninger skal også kunne danne særdeles sta bile emulsioner, idet denne evne er endnu mere betydningsfuld ved perfusionsmaterialer. Bloderstatninger er sædvanligvis ublandbare med blod og kan, hvis de anvendes alene, forårsage embolier. Dette problem løses ved at anvende bloderstatningen 30 i vandig emulsion, og det er klart, at emulsionen ikke må brydes ved anvendelse eller oplagring. I forbindelse med persusionsmaterialer er dette krav endnu mere strengt, da oxygenatorerne, der anvendes til at sætte oxygen til perfusionsmaterialet, skaber meget høje forskydningsspændinger 35 og vil bryde alle emulsioner med undtagelse af de mest stabile. En anden grund til, at der anvendes vandige emulsioner,25 Blood substitutes should also be able to form extremely stable emulsions, since this ability is even more significant in perfusion materials. Blood substitutes are usually immiscible with blood and, if used alone, can cause embolism. This problem is solved by using the blood substitute 30 in aqueous emulsion and it is clear that the emulsion must not be broken during use or storage. In the case of percussion materials, this requirement is even more stringent, since the oxygenators used to add oxygen to the perfusion material create very high shear stresses 35 and will break all emulsions except the most stable ones. Another reason why aqueous emulsions are used,
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2 er, at der sættes salte til vandet for at opretholde legemets saltbalance.2 is that salts are added to the water to maintain the salt balance of the body.
The Green Cross Corporation, Osaka, Japan, har udgivet et skrift dateret den 11. september 1974 angående emulsioner 5 af perf luorerede forbindeler som oxygen- og carbondioxid-bærere. Nogle af forbindelserne, der er beskrevet i den foreliggende opfindelse, omtales også af Clark et al. i Microvascular Research, bind 8/3 1974, der også er fremlagt ved Oxygen Transport to Tissue Symposium, Atlantic City, 10 N.J., April 11, 1974. Den valgte bloderstatning og perfu sionsmateriale indtil nu har været perfluorodecalin. Det har flere ønskelige egenskaber, men forbindelserne, der er beskrevet i den foreliggende opfindelse, forekommer perfluorodecalin overlegne i flere henseender.The Green Cross Corporation, Osaka, Japan, has published a document dated September 11, 1974, regarding emulsions 5 of perfluorinated compounds as oxygen and carbon dioxide carriers. Some of the compounds described in the present invention are also mentioned by Clark et al. in Microvascular Research, Volume 8/3 1974, also presented at the Oxygen Transport to Tissue Symposium, Atlantic City, 10 N.J., April 11, 1974. The blood substitute and perfusion material chosen so far has been perfluorodecaline. It has several desirable properties, but the compounds described in the present invention appear to be superior to perfluorodecaline in several respects.
15 Den foreliggende opfindelse angår en fremgangsmåde til fremstilling af syntetisk blod, hvorved der med vand og en ugiftig emulgator emulgeres en ikke-aromatiserbar perfluo-reret forbindelse, således at mængden af vand i den færdige emulsion er større end 40 volumen-%, hvilken fremgangsmåde 20 er ejendommelig ved, at der som perfluoreret forbindelse anvendes lavere alkyl-adamantan, bortset fra dimethyladaman-tan, fortrinsvis 1-methyl-adamantan, hvis mængde i emulsionen er 10-30 volumen-%, og som har en partikelstørrelse på ca. 0,001-10 μιη, idet fortrinsvis 50 vægt-% af partiklerne har 25 en størrelse på 0,05-0,3 Jim, og emulsionspræparatet desuden 3 om ønsket bibringes et indhold af 10-100 cm oxygen (25°C, 3 760 mm Hg) per 100 cm af den perfluorerede forbindelse.The present invention relates to a process for preparing synthetic blood, whereby a non-aromatizable perfluorinated compound is emulsified with water and a non-aromatizable emulsifier such that the amount of water in the final emulsion is greater than 40% by volume, 20 is characterized in that, as perfluorinated compound, lower alkyl-adamantane is used, except for dimethyladamantane, preferably 1-methyl-adamantane, the amount of which in the emulsion is 10-30% by volume and having a particle size of approx. 0.001-10 µιη, preferably 50% by weight of the particles having a size of 0.05-0.3 µm and the emulsion preparation 3 additionally, if desired, imparting a content of 10-100 cm 2 of oxygen (25 ° C, 3,760 mm Hg) per 100 cm of the perfluorinated compound.
De perf luorerede lavere alkyladamantaner, der anvendes ved fremgangsmåden ifølge opfindelsen, har en ekstremt høj 30 oxygen-opløselighed, efterlader en meget lille rest i legemet, danner særdeles stabile emulsioner og har et særdeles tilfredsstillende damptryk til den omhandlede anvendelse.The perfluorinated lower alkyladamantanes used in the process of the invention have an extremely high oxygen solubility, leave a very small residue in the body, form extremely stable emulsions, and have a very satisfactory vapor pressure for the present application.
De lavere alkyladamantaner er f.eks. methyladamantan, ethyladamantan, ethylmethyladamantan, ethyldimethyladamantan 35 og triethyladamantan.The lower alkyladamantanes are e.g. methyladamantane, ethyladamantane, ethylmethyladamantane, ethyldimethyladamantane and triethyladamantane.
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De lavere alkyladamantaner anvendes som nævnt i per-fluoreret form. Betegnelsen perfluoreret omfatter her forbindelser, hvoraf mindst 95 vægt-% er fuldstændig fluoreret (dvs. perfluoreret i den strenge betydning), fortrinsvis 5 mindst 98% og især 100%. I alle tilfælde mindre end 100%, vil den resterende mængde naturligvis være højt fluoreret.The lower alkyladamantanes are used as mentioned in perfluorinated form. The term perfluorinated here encompasses compounds of which at least 95% by weight is completely fluorinated (i.e., perfluorinated in the strict sense), preferably at least 98% and especially 100%. In all cases less than 100%, the remaining amount will naturally be highly fluorinated.
Fluoreringen gennemføres ved kendte metoder. Alkylada-mantanet kan f.eks. langsomt føres hen over et lag af CoF3, der indeholder 2-3 gange den støkiometriske mængde fluor, 10 ved 250-275°C, hvorved der fås en delvis fluorering. Proceduren gentages derefter ved 300-350°C, hvorved der fås en fuldstændig fluorering af det hele bortset fra nogle få procent urenheder, der både er mættede, delvis fluorerede forbindelser og olefiniske carbonfluorider. De førstnævnte 15 forbindelser koger mindst 10°C højere end den ønskede perfluorforbindelse og fjernes ved destillation. De sidstnævnte forbindelser koger ved praktisk talt den samme temperatur, og ekstraheres derfor med en amin, såsom diethylamin (DEA). Tilbageblivende amin fjernes med koncentreret svovlsyre.Fluorination is carried out by known methods. The alkyl mantan may e.g. is slowly passed over a layer of CoF3 containing 2-3 times the stoichiometric amount of fluorine, 10 at 250-275 ° C, giving a partial fluorination. The procedure is then repeated at 300-350 ° C to give a complete fluorination of the whole except for a few percent impurities which are both saturated, partially fluorinated compounds and olefinic carbon fluorides. The former 15 compounds boil at least 10 ° C higher than the desired perfluoro compound and are removed by distillation. The latter compounds boil at practically the same temperature, and are therefore extracted with an amine such as diethylamine (DEA). Remaining amine is removed with concentrated sulfuric acid.
20 Tilbageblivende syre fjernes med 1%’s natriumhydrogencar-bonatopløsning, der derefter ekstraheres med acetone. Til slut afdestilleres tilbageblivende acetone.Residual acid is removed with 1% sodium hydrogen carbonate solution, which is then extracted with acetone. Finally, residual acetone is distilled off.
Normalt indeholder emulsionspræparatet 1-5 volumenprocent af en emulgator. Udvælgelsen af en emulgator er ikke 25 kritisk, men emulgatoren bør være ugiftig og danne en stabil emulsion. Den foretrukne emulgator er æggeblomme-phospholid, da det er velkendt, at dette er uskadeligt for legemet.Usually, the emulsion composition contains 1-5% by volume of an emulsifier. The selection of an emulsifier is not critical, but the emulsifier should be non-toxic and form a stable emulsion. The preferred emulsifier is egg yolk phospholide, as it is well known that this is harmless to the body.
Egnet til perfusionsformål er også polyoxyethylener og poly-oxypropylener, der kan fås i handelen som "Pluronics".Also suitable for perfusion purposes are polyoxyethylenes and polyoxypropylenes which are commercially available as "Pluronics".
30 "Pluronic® F-68" har en molekylvægt på 8.350 og danner en særdeles stabil emulsion.30 "Pluronic® F-68" has a molecular weight of 8,350 and forms a highly stable emulsion.
Emulsionen kan fremstilles ved hjælp af sædvanlige emulgeringsapparater, der fremkalder høje forskydningsspændinger, såsom en Manton-Gaulin-homogenisator. Partikelstør-35 reisen i emulsionen er som nævnt 0,001-10 um, ofte 0,01-10 um og sædvanligvis 0,05-0,5 um, og fortrinsvis har 50 vægt%The emulsion can be prepared by conventional emulsifiers which produce high shear stresses such as a Manton-Gaulin homogenizer. The particle size of the emulsion is, as mentioned, 0.001-10 µm, often 0.01-10 µm and usually 0.05-0.5 µm, and preferably has 50% by weight.
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4 af partiklerne diametre på 0,05-0,3 μιη. Som det er velkendt, kan partikelstørrelsen indstilles ved hjælp af den anvendte forskydningsspænding. Emulsionens faktiske partikelstørrelse er ikke så kritisk som dens stabilitet, hvilket omtales 5 yderligere i det følgende.4 of the particles have diameters of 0.05-0.3 μιη. As is well known, the particle size can be adjusted by the shear stress applied. The actual particle size of the emulsion is not as critical as its stability, which is further discussed hereinafter.
Som ovenfor anført er tilbageholdelsen af materialet i legemet af betydning. I det følgende sammenlignes perfluo-reret (PF) methyladamantan (MA) med PF tributylamin (TBA), decalin (D) og methyldecalin (MD). Disse forbindelser er de 10 bedste bloderstatninger og perfusionsmaterialer indtil dato. Emulsioner, der indeholder 10% af materialet, der skal undersøges, overfladeaktivt middel og vand, fremstilles og undersøges på den måde, der er beskrevet i Science, bind 181, august, 1973, side 681. De forskellige emulsioner indsprøjtes 15 i mus. Musene dræbes med forskellige intervaller derefter, leveren analyseres, og det procentiske forhold mellem den oprindelige mængde injiceret PF-materiale og den mængde, der stadig er i leveren, bestemmes. De opnåede resultater er anført i det følgende.As stated above, retention of the material in the body is important. In the following, perfluorinated (PF) methyladamantane (MA) is compared with PF tributylamine (TBA), decalin (D) and methyldecaline (MD). These compounds are the top 10 blood substitutes and perfusion materials to date. Emulsions containing 10% of the material to be investigated, surfactant and water, are prepared and tested in the manner described in Science, Vol. 181, August, 1973, page 681. The various emulsions are injected into mice. The mice are killed at different intervals thereafter, the liver is analyzed and the percentage ratio between the original amount of injected PF material and the amount still in the liver is determined. The results obtained are listed below.
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Procent af dosis i leveren efter det anførte antal ugerPercentage of dose in the liver after the indicated number of weeks
Forbindelse 2 6 12 20 25 PFD 2 2 2 2 PFMD 30 19 2 2 PFTBA 38 30 30 30 PFMA 7 1 30 Det fremgår heraf, at PFMA (der indeholder en lille mængde af en højerekogende urenhed, der forsinker dets frigørelse fra legemet) er lige så godt eller bedre end PFD.Compound 2 6 12 20 25 PFD 2 2 2 2 PFMD 30 19 2 2 PFTBA 38 30 30 30 PFMA 7 1 30 It appears that PFMA (containing a small amount of a higher boiling impurity which delays its release from the body) is as good or better than PFD.
Den relative stabilitet af en PFMA-emulsion er udmærket, idet den er stabil i et ikke nærmere bestemt tidsrum 35 (f.eks. over 6 måneder) ved 4-7°C, medens PFD-emulsionen brydes i løbet af nogle dage ved stuetemperatur og i løbet af nogle uger ved 4-7°C. PFTBA er også udmærket. Se f.eks.The relative stability of a PFMA emulsion is excellent, being stable for an unspecified period of time (e.g. over 6 months) at 4-7 ° C, while the PFD emulsion breaks during a few days at room temperature. and over a few weeks at 4-7 ° C. PFTBA is also excellent. See, e.g.
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Journal of Microvascular Research, august, 1974. .Ud ever erriulsionsstabiliteten udviser en emulsion, der er fremstillet af PFMA, en optisk tæthed på 0,65, hvilket betyder, at materialets partikelstørrelse er meget mindre, og det derfor 5 er meget lettere at emulgere, end PFTBA, der giver en værdi på 2,2.Journal of Microvascular Research, August, 1974. Out of ever erulsion stability, an emulsion produced by PFMA has an optical density of 0.65, which means that the particle size of the material is much smaller and therefore 5 is much easier to emulsify. , than the PFTBA, which gives a value of 2.2.
Det har også vist sig, at de her omhandlede, perfluo-rerede forbindelser har en meget lav giftighed. LD^q af de her omhandlede forbindelser efter infusion i sammenligning 10 med andre forbindelser er følgende: LD50 (mg/kg)It has also been found that the perfluorinated compounds of this invention have a very low toxicity. LD 50 of the compounds of this invention after infusion in Comparison 10 with other compounds are as follows: LD 50 (mg / kg)
Emulsion 1 time 3 dage 7 dage 10,9% PFD 190 160 159 15 5% PFMA >200 >200 >200 10% PFTBA >200 . 120 120Emulsion 1 hour 3 days 7 days 10.9% PFD 190 160 159 15 5% PFMA> 200> 200> 200 10% PFTBA> 200. 120 120
Som ovenfor anført har de her omhandlede, perfluore- rede forbindelser en høj oygen- og carbondioxid-opløselighed.As noted above, the perfluorinated compounds of this invention have a high oxygen and carbon dioxide solubility.
20 F.eks. kan de perfluorerede forbindeler normalt indeholde 3 3 ca. 40-60 cm oxygen pr. 100 m carbonfluorid, og carbon- dioxid-opløseligheden er omkring det dobbelte. Normalt blod 3 3 vil absorbere ca. 20 cm oxygen pr. 100 cm blod og har en carbondioxid-opløselighed, der er det dobbelte af oxygen- 25 -opløseligheden. Præparaterne ifølge opfindelsen vil normalt 3 3 indeholde 30-60 cm oxygen pr. 100 cm af det perfluorerede materiale, men der kan som nævnt anvendes forhold så lave 3 3 3 3 som 10 cm pr. 100 cm og så høje som 100 cm pr. 100 cem .For example, the perfluorinated compounds can usually contain about 3 40-60 cm oxygen per 100 m of carbon fluoride and the carbon dioxide solubility is about twice that. Normal blood 3 3 will absorb approx. 20 cm oxygen per 100 cm blood and has a carbon dioxide solubility that is twice the oxygen solubility. The compositions of the invention will normally contain 30 to 60 cm 100 cm of the perfluorinated material, but as mentioned, ratios as low 3 3 3 3 as 10 cm per cm can be used. 100 cm and as high as 100 cm per 100 cem.
Alle de ovenfor nævnte opløseligheder er ved 25°C og 76Ό mm 30 Hg.All of the above solubilities are at 25 ° C and 76Ό mm 30 Hg.
I de følgende eksempler vil det som ovenfor anført forstås, at de omhandlede perfluorerede forbindelser omfatter forbindelser, der for mindt 95 vægt%’s vedkommende er fuldstændig fluoreret, fortrinsvis mindst 98% og især 100% fluo- .In the following examples, it will be understood, as noted above, that the perfluorinated compounds of the present invention comprise compounds which are fully fluorinated at least 95% by weight, preferably at least 98% and most preferably 100% fluorine.
35 reret, dvs. perfluoreret. Forbindelserne, der er mindre end 100% fluoreret, er stadig højt fluoreret.35, ie. perfluorinated. The compounds less than 100% fluorinated are still highly fluorinated.
3 63 6
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Eksempel 1Example 1
Til 10 cm perfluormethyladamantan sættes der 5 g æggeblommephospholipid-emulgator. Der sættes derefter destil-5 leret vand til blandingen til et samlet volumen på 50 cm . Opløsningen filtreres gennem et 10 um’s milliporefilter, og opløsningen, der afkøles til ca. 0-5°C med et isbad, behandles i et ultralydsapparat. Under denne behandling måles den optiske tæthed af prøver på 5 cm med regelmæssige inter-10 valler, indtil der fås en konstant optisk tæthed, hvilket betyder, at den mindst mulige partikelstørrelse i emulsionen er nået. Derefter standses ultralydsbehandlingen, og der fås en stabil, vandig emulsion med 20 volumenprocent per-fluormethyladamantan.To 10 cm of perfluoromethyladamantane is added 5 g of egg yolk phospholipid emulsifier. Distilled water is then added to the mixture to a total volume of 50 cm. The solution is filtered through a 10 µm millipore filter and the solution cooled to ca. 0-5 ° C with an ice bath, treated in an ultrasonic apparatus. During this treatment, the optical density of samples of 5 cm is measured at regular intervals until a constant optical density is obtained, which means that the smallest possible particle size in the emulsion is reached. Then the ultrasonic treatment is stopped and a stable aqueous emulsion is obtained with 20% by volume of perfluoromethyladamantane.
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Eksempel 2 3Example 2 3
Til 5 cm perfluoromethyladamantan sættes der 25 g æggeblommephospholipid-emulgator. Derefter sættes der destil-leret vand til blandingen til et samlet volumen på 500 cm .To 5 cm of perfluoromethyladamantane is added 25 g of egg yolk phospholipid emulsifier. Then distilled water is added to the mixture to a total volume of 500 cm.
'20 Opløsningen filtreres gennem et 10 ym’s milliporef il ter, og opløsningen homogeniseres i en Manton-Gaulin homogenisator, der er udstyret med en køler. Under homogeniseringen måles den optiske tæthed af emulsionsprøver på 5 cm med regelmæssige intervaller, indtil der fås en konstant optisk tæthed, 25 hvilket betyder, at den mindst mulige partikelstørrelse i emulsionen er nået. Derefter standses homogeniseringen, og der fås en stabil, vandig emulsion med 10 volumenprocent perfluoromethyladamantan.The solution is filtered through a 10 µm millipore filter and the solution is homogenized in a Manton-Gaulin homogenizer equipped with a cooler. During homogenization, the optical density of 5 cm emulsion samples is measured at regular intervals until a constant optical density is obtained, which means that the smallest possible particle size in the emulsion is reached. Then the homogenization is stopped and a stable aqueous emulsion is obtained with 10% by volume perfluoromethyladamantane.
30 Eksempel 3 3Example 3 3
Til 100 cm perfluoroethylmethyladamantan sættes der 50 g "Pluronic F68"-emulgator. Derefter sættes der destil-leret vand til blandingen til et samlet volumen på 500 cm . Opløsningen filtreres gennem et 10 um’s milliporefilter, og 35 opløsningen homogeniseres i en Manton-Gaulin homogenisator, der er udstyret med en køler. Under homogeniseringen måles 7To 100 cm of perfluoroethyl methyladamantane is added 50 g of "Pluronic F68" emulsifier. Then distilled water is added to the mixture to a total volume of 500 cm. The solution is filtered through a 10 µm millipore filter and the solution is homogenized in a Manton-Gaulin homogenizer equipped with a cooler. During homogenization, 7 is measured
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o 3 den optiske tæthed af emuisionsprøver på 5 cm med regelmæssige intervaller, indtil der nås en konstant optisk tæthed. Derefter standses homogeniseringen, og der fås en stabil, vandig emulsion med 20 volumenprocent perfluoroethylmethyl-5 adamantan.o 3 the optical density of 5 cm emission samples at regular intervals until a constant optical density is reached. Then the homogenization is stopped and a stable aqueous emulsion is obtained with 20% by volume perfluoroethylmethyl-5 adamantane.
Eksempel 4Example 4
Ved at gå frem som beskrevet i eksempel 3 men gå ud fra per fluor otriethyladamantan fås der en stabil, vandig 10 emulsion med 20 volumenprocent perfluorotriethyladamantan.By proceeding as described in Example 3 but starting from per fluoro otriethyladamantane, a stable aqueous 10 emulsion with 20% by volume perfluorotriethyladamantane is obtained.
Eksempel 5Example 5
Ved at gå frem som beskrevet i eksempel 1 men anvende perfluorotrimethyladamantan fås der en stabil, vandig emul-15 sion med 10 volumenprocent perfluorotrimethyladamantan.Proceeding as described in Example 1 but using perfluorotrimethyladamantane, a stable aqueous emulsion is obtained with 10% by volume perfluorotrimethyladamantane.
Eksempel 6Example 6
Ved at gå frem som beskrevet i eksempel 2 men anvende perfluoroethyldimethyladamantan og "Pluronic F68" som emul-20 gator fås der en stabil, vandig emulsion med 10 volumenprocent perfluoroethyldimethyladamantan.Proceeding as described in Example 2 but using perfluoroethyl dimethyladamantane and "Pluronic F68" as the emulsifier gives a stable aqueous emulsion with 10% by volume perfluoroethyl dimethyl adamantane.
Eksempel 7Example 7
Ved at gå frem som beskrevet i eksempel 1 men anvende 25 perfluoroethyladamantan fås der en stabil, vandig emulsion med 10 volumenprocent perfluoroethyladamantan.Proceeding as described in Example 1 but using perfluoroethyladamantane, a stable aqueous emulsion is obtained with 10% by volume of perfluoroethyladamantane.
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Application Number | Priority Date | Filing Date | Title |
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DK006778A DK155867C (en) | 1974-12-09 | 1978-01-06 | EMULSION PREPARATION OF PERFLUORED COMPOUNDS FOR USE AS SYNTHETIC BLOOD |
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Application Number | Priority Date | Filing Date | Title |
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US53079174A | 1974-12-09 | 1974-12-09 | |
US53079174 | 1974-12-09 | ||
US57976675A | 1975-05-22 | 1975-05-22 | |
US57976675 | 1975-05-22 |
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DK554675A DK554675A (en) | 1976-06-10 |
DK154605B true DK154605B (en) | 1988-12-05 |
DK154605C DK154605C (en) | 1989-06-05 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
DK554675A DK154605C (en) | 1974-12-09 | 1975-12-08 | METHOD OF MANUFACTURING SYNTHETIC BLOOD |
Country Status (12)
Country | Link |
---|---|
JP (1) | JPS5753762B2 (en) |
CA (1) | CA1058081A (en) |
CH (1) | CH629938A5 (en) |
DE (1) | DE2555408A1 (en) |
DK (1) | DK154605C (en) |
FI (1) | FI54560C (en) |
FR (1) | FR2313024A1 (en) |
GB (1) | GB1531418A (en) |
IT (1) | IT1050731B (en) |
NL (1) | NL184995C (en) |
NO (1) | NO754103L (en) |
SE (2) | SE7513814L (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2515198A1 (en) * | 1981-10-22 | 1983-04-29 | Centre Nat Rech Scient | AQUEOUS MICROEMULSIONS OF FLUOROCARBONS INDUFINIMENTALLY STABLE AT A DATA TEMPERATURE, PROCESS FOR OBTAINING AND APPLICATION AS OXYGEN TRANSPORTERS |
US4569784A (en) * | 1980-11-17 | 1986-02-11 | Adamantech, Inc. | Preparation of a gel having gas transporting capability |
GB8504916D0 (en) * | 1985-02-26 | 1985-03-27 | Isc Chemicals Ltd | Emulsions of perfluorocarbons in aqueous media |
DE4100059C2 (en) * | 1991-01-03 | 1994-08-25 | Adatomed Pharma & Med | Treatment liquid for reapplication (detached) of detached retina to the choroid of the eye |
EP2373289A4 (en) * | 2008-12-08 | 2014-07-02 | Univ Utah Res Found | Stable perfluorocarbon emulsion for use as an artificial oxygen carrier |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2144094A1 (en) * | 1970-09-05 | 1972-03-09 | The Green Cross Corp.; Tanabe Seiyaku Co. Ltd.; Osaka (Japan) | Process for the preparation of a fluorocarbon emulsion capable of transporting oxygen for injection purposes |
DE2409598A1 (en) * | 1973-02-26 | 1974-10-10 | Childrens Hosp Medical Center | GAS TRANSPORT AGENT FOR ANIMALS |
DE2404564A1 (en) * | 1973-10-05 | 1975-04-17 | Green Cross Corp | Aqueous EMULSION OF SATURATED ALIPHATIC PERFLUORCARBON COMPOUNDS, PROCESS FOR THEIR PRODUCTION AND USE AS BLOOD SUBSTITUTE AND PERFUSION LIQUID |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1343870A (en) * | 1971-05-19 | 1974-01-16 | Green Cross Corp | Emulsions and the preparation thereof |
-
1975
- 1975-11-28 IT IT29807/75A patent/IT1050731B/en active
- 1975-12-03 CH CH1572675A patent/CH629938A5/en not_active IP Right Cessation
- 1975-12-04 JP JP50143428A patent/JPS5753762B2/ja not_active Expired
- 1975-12-04 NO NO754103A patent/NO754103L/no unknown
- 1975-12-05 CA CA241,138A patent/CA1058081A/en not_active Expired
- 1975-12-05 NL NLAANVRAGE7514202,A patent/NL184995C/en not_active IP Right Cessation
- 1975-12-08 DK DK554675A patent/DK154605C/en not_active IP Right Cessation
- 1975-12-08 FI FI753442A patent/FI54560C/en not_active IP Right Cessation
- 1975-12-08 SE SE7513814A patent/SE7513814L/en unknown
- 1975-12-09 GB GB50472/75A patent/GB1531418A/en not_active Expired
- 1975-12-09 DE DE19752555408 patent/DE2555408A1/en active Granted
- 1975-12-09 FR FR7537587A patent/FR2313024A1/en active Granted
-
1983
- 1983-01-27 SE SE8300422A patent/SE8300422L/en unknown
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE2144094A1 (en) * | 1970-09-05 | 1972-03-09 | The Green Cross Corp.; Tanabe Seiyaku Co. Ltd.; Osaka (Japan) | Process for the preparation of a fluorocarbon emulsion capable of transporting oxygen for injection purposes |
DE2409598A1 (en) * | 1973-02-26 | 1974-10-10 | Childrens Hosp Medical Center | GAS TRANSPORT AGENT FOR ANIMALS |
DE2404564A1 (en) * | 1973-10-05 | 1975-04-17 | Green Cross Corp | Aqueous EMULSION OF SATURATED ALIPHATIC PERFLUORCARBON COMPOUNDS, PROCESS FOR THEIR PRODUCTION AND USE AS BLOOD SUBSTITUTE AND PERFUSION LIQUID |
Also Published As
Publication number | Publication date |
---|---|
NO754103L (en) | 1976-06-10 |
FI54560C (en) | 1979-01-10 |
NL184995B (en) | 1989-08-01 |
FR2313024A1 (en) | 1976-12-31 |
JPS5198318A (en) | 1976-08-30 |
SE8300422D0 (en) | 1983-01-27 |
CA1058081A (en) | 1979-07-10 |
JPS5753762B2 (en) | 1982-11-15 |
DE2555408A1 (en) | 1976-06-10 |
DE2555408C2 (en) | 1988-06-23 |
FI54560B (en) | 1978-09-29 |
NL7514202A (en) | 1976-06-11 |
FI753442A (en) | 1976-06-10 |
NL184995C (en) | 1990-01-02 |
CH629938A5 (en) | 1982-05-28 |
GB1531418A (en) | 1978-11-08 |
DK554675A (en) | 1976-06-10 |
DK154605C (en) | 1989-06-05 |
IT1050731B (en) | 1981-03-20 |
SE8300422L (en) | 1983-01-27 |
SE7513814L (en) | 1976-06-10 |
FR2313024B1 (en) | 1980-05-23 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUP | Patent expired |