US2001003580A1PendingUtilityA1
Preparation of a lipid blend and a phospholipid suspension containing the lipid blend
Priority: Jan 14, 1998Filed: Jan 13, 1999Published: Jun 14, 2001
Est. expiryJan 14, 2018(expired)· nominal 20-yr term from priority
A61K 49/00A61K 9/1277A61K 9/10A61K 47/44A61K 49/226A61K 49/227A61B 8/00A61K 47/24A61K 47/10
30
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Claims
Abstract
The present invention describes processes for the preparation of a lipid blend and a uniform filterable phospholipid suspension containing the lipid blend, such suspension being useful as an ultrasound contrast agent.
Claims
exact text as granted — not AI-modifiedWhat is claimed as new and desired to be secured by Letter Patent of United States is:
1 . A process for preparing a phospholipid suspension, comprising:
(1) contacting a lipid blend with a non-aqueous solvent, whereby the lipid blend substantially dissolves in the non-aqueous solvent; and, (2) contacting the solution from step (1) with an aqueous solution to form a lipid suspension.
2 . A process according to claim 1 , wherein the non-aqueous solvent is selected from propylene glycol, ethylene glycol, and polyethylene glycol 300.
3 . A process according to claim 2 , wherein the non-aqueous solvent is propylene glycol.
4 . A process according to claim 2 , wherein the lipid blend, comprises:
(a) 1,2-dipalmitoyl-sn-glycero-3-phosphatidylcholine; (b) 1,2-dipalmitoyl-sn-glycero-3-phosphotidic, mono sodium salt; and, (c) N-(methoxypolyethylene glycol 5000 carbamoyl)-1,2-dipalmitoyl-sn-glycero-3-phosphatidylethanolamine, mono sodium salt.
5 . A process according to claim 2 , wherein the non-aqueous solvent is heated to a temperature of about 30 to 70° C. prior to contacting with the lipid blend.
6 . A process according to claim 5 , wherein the non-aqueous solvent is heated to a temperature of about 50 to 55° C. prior to contacting with the lipid blend.
7 . A process according to claim 2 , wherein the ratio of lipid blend to non-aqueous solvent is from about 5 mg of lipid blend per mL of non-aqueous solvent to about 15 mg/mL.
8 . A process according to claim 7 , wherein the ratio of lipid blend to non-aqueous solvent is about 10 mg/mL.
9 . A process according to claim 2 , wherein in step (2), the aqueous solution is selected from water, saline, a saline/glycerin mixture, and a saline/glycerin/non-aqueous solvent mixture.
10 . A process according to claim 9 , wherein the aqueous solution is a saline and glycerin mixture.
11 . A process according to claim 9 , wherein the aqueous solution is a saline, glycerin, and propylene glycol mixture.
12 . A process according to claim 11 , wherein 6.8 mg/mL of sodium chloride are present, 0.1 mL/mL of glycerin are present, 0.1 mL/mL of propylene glycol are present, and about 0.75 to 1.0 mg/mL of the lipid blend are present.
13 . A process according to claim 12 , wherein 0.75 mg/mL of lipid blend are present.
14 . A process according to claim 12 , wherein 1.0 mg/mL of lipid blend are present.
15 . A process according to claim 2 , wherein in step (2), the aqueous solution is heated to a temperature of about 45 to 60° C. prior to contacting with the solution from step (1).
16 . A process according to claim 15 , wherein the aqueous solution is heated to a temperature of about 50 to 55° C. prior to contacting with the solution from step (1).
17 . A process according to claim 1 , wherein the process further comprises:
(3) heating the lipid suspension from step (2) to a temperature about equal to or above the highest gel to liquid crystalline phase transition temperature of the lipids present in the suspension.
18 . A process according to claim 17 , wherein in step (3), the lipid suspension is heated to a temperature of at least about 67° C.
19 . A process according to claim 17 , wherein the process further comprises:
(4) filtering the lipid suspension through a sterilizing filter.
20 . A process according to claim 19 , wherein in step (4), the filtration is performed using two sterilizing filter cartridges.
21 . A process according to claim 20 , wherein in step (4), the sterilizing filter cartridges are at a temperature of from about 70 to 80° C.
22 . A process according to claim 21 , wherein in step (4), 0.2 μm hydrophilic filters are used.
23 . A process according to claim 19 , wherein the process further comprises:
(5) dispensing the filtered solution from step (4) into a vial.
24 . A process according to claim 23 , wherein the process further comprises:
(6) exchanging the headspace gas of the vial from step (5) with a perfluorocarbon gas.
25 . A process according to claim 24 , wherein the perfluorocarbon gas is perfluoropropane.
26 . A process according to claim 25 , wherein exchange of headspace gas is performed using a lyophilizing chamber.
27 . A process according to claim 24 , wherein the process further comprises:
(7) sterilizing the vial from step (6).
28 . A process according to claim 27 , wherein in step (7), the vial is sterilized at about 126-130° C. for 1 to 10 minutes.
29 . A process for preparing a lipid blend, comprising:
(a) contacting at least two lipids with a first non-aqueous solvent; (b) concentrating the solution to a thick gel; (c) contacting the thick gel with a second non-aqueous solvent; and, (d) collecting the resulting solids.
30 . A process according to claim 29 , wherein in step (a), the lipids are:
(i) 1,2-dipalmitoyl-sn-glycero-3-phosphatidylcholine; (ii) 1,2-dipalmitoyl-sn-glycero-3-phosphotidic, mono sodium salt; and, (iii) N-(methoxypolyethylene glycol 5000 carbamoyl)-1,2-dipalmitoyl-sn-glycero-3-phosphatidylethanolamine, mono sodium salt.
31 . A process according to claim 30 , wherein in step (a), the first non-aqueous solvent is a mixture of methanol and toluene.
32 . A process according to claim 30 , wherein in step (c), the second non-aqueous solvent is a methyl t-butyl ether.
33 . A process according to claim 30 , wherein in step (a), the solution is warmed to a temperature sufficient to complete dissolution of the lipids into the solvent.
34 . A process according to claim 33 , wherein in step (a), the solution is warmed to about 25 to 75° C.
35 . A process according to claim 30 , wherein in step (d), the solids collected are washed with methyl t-butyl ether and dried in vacuo.
36 . A phospholipid suspension, comprising:
(a) a lipid blend in an amount of about 0.75-1.0 mg/mL of suspension; (b) sodium chloride in an amount of about 6.8 mg/mL of suspension; (c) glycerin in an amount of about 0.1 mL/mL of suspension; (d) propylene glycol in an amount of about 0.1 mL/mL of suspension; and (e) water; wherein the suspension is prepared by the process, comprising: (1) contacting a lipid blend with a non-aqueous solvent, whereby the lipid blend substantially dissolves in the non-aqueous solvent; (2) contacting the solution from step (1) with an aqueous solution to form a lipid suspension; (3) heating the lipid suspension from step (2) to a temperature about equal to or above the highest gel to liquid crystalline phase transition temperature of the lipids present in the suspension; and, (4) filtering the lipid suspension through a sterilizing filter.
37 . A phospholipid suspension according to claim 36 , wherein the lipid blend, comprises:
(a) 1,2-dipalmitoyl-sn-glycero-3-phosphatidylcholine; (b) 1,2-dipalmitoyl-sn-glycero-3-phosphotidic, mono sodium salt; and, (c) N-(methoxypolyethylene glycol 5000 carbamoyl)-1,2-dipalmitoyl-sn-glycero-3-phosphatidylethanolamine, mono sodium salt.
38 . A phospholipid suspension according to claim 37 , wherein the non-aqueous solvent is heated to a temperature of about 50 to 55° C. prior to contacting with the lipid blend.
39 . A phospholipid suspension according to claim 37 , wherein the ratio of lipid blend to non-aqueous solvent is about 10 mg/mL.
40 . A phospholipid suspension according to claim 37 , wherein the aqueous solution is a saline, glycerin, and propylene glycol mixture.
41 . A phospholipid suspension according to claim 40 , wherein 0.75 mg/mL of lipid blend are present.
42 . A phospholipid suspension according to claim 37 , wherein the aqueous solution is heated to a temperature of about 50 to 55° C. prior to contacting with the solution from step (1).
43 . A phospholipid suspension according to claim 37 , wherein in step (3), the lipid suspension is heated to a temperature of at least about 67° C.
44 . A phospholipid suspension according to claim 43 , wherein in step (4), two 0.2 μm hydrophilic filters are used.Join the waitlist — get patent alerts
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