Device and method for preparing vesica with inner and outer water phase gradient difference
A technology with poor gradient and vesicles is applied in the field of pharmaceutical preparations to achieve the effects of improving the liquid separation process, increasing the filtration speed, and being convenient to operate.
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Embodiment 1
[0128] Example 1 Dialysis method and filtered ion exchange method were used to establish ammonium sulfate gradient for liposomes and load drugs
[0129] Prescription HSPC 4.5g
[0130] CH 1.5g
[0131] PEG-CHS 1.5g
[0132] Hydration medium: 150 mL of 200 mmol ammonium sulfate solution.
[0133] Prepare blank liposomes: Weigh the prescribed amount of HSPC, CH, PEG-CHS (PEG molecular weight is 2000), and dissolve the membrane material with 12 mL of ethanol at 55°C to obtain the lipid phase; hydrate it before heating to 55°C The medium is injected into the lipid phase and incubated for 10 minutes to prepare the primary liposomes. After 20,000 psi high pressure homogenization treatment, the liposomes are reduced to 100 nm in size, and then passed through 0.8, 0.45, and 0.22 μm microporous membranes. , That is, a blank liposome is obtained.
[0134] Dialysis method to establish a gradient: take 1.0 mL blank liposomes, 250 mL 5% ( w / v ) Xylitol solution is the dialysis medium (1:250, v / v)...
Embodiment approach
[0135] Filtration ion exchange method to establish gradient: attached figure 2 An embodiment according to the present invention is given: the membrane separation device (1) in this embodiment is a hollow fiber membrane module (polyethersulfone with a water bath temperature control device, a molecular weight cut-off of 100K Da, and a membrane area of 1.5 m). 2 ); The ion exchange device (2) in this embodiment is a chromatographic column with a constant temperature device; the ion exchanger in the chromatographic column is a mixture of S 100 type cation exchange resin and M 800 type anion exchange resin ( v / v =1 / 1, depending on the wet volume), the exchange capacity of the mixed ion exchange resin used is 12 times the theoretical required exchange capacity; the dialysis medium is 5% ( w / v ) Xylitol solution, the volume ratio of dialysis medium to blank liposome is 10:1; the vesicle suspension pump (5) and dialysis medium pump (6) used are medical peristaltic pumps.
[0136] ste...
Embodiment 2
[0149] take" Example 1 "Blank liposome 50 mL, with a mixture of ZB-1 cation exchange fiber and ZB-2 anion exchange fiber ( v / v =1 / 1, depending on the wet volume) is a mixed ion exchanger, the exchange capacity of the mixed ion exchange fiber used is 3 times the theoretical required exchange capacity; the dialysis medium is isotonic sucrose solution, the volume of the dialysis medium and the blank liposome The ratio is 15:1; the establishment and operation steps of the gradient device are the same as in "Example 1". The obtained gradient liposomes are loaded with epirubicin, doxorubicin and mitoxantrone (the weight ratio of drug to HSPC is 1:10), and the encapsulation efficiency is higher than 95%.
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