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-modified
What 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.

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