CN107667135A - 多糖珠粒的制备方法 - Google Patents
多糖珠粒的制备方法 Download PDFInfo
- Publication number
- CN107667135A CN107667135A CN201680032270.8A CN201680032270A CN107667135A CN 107667135 A CN107667135 A CN 107667135A CN 201680032270 A CN201680032270 A CN 201680032270A CN 107667135 A CN107667135 A CN 107667135A
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- CN
- China
- Prior art keywords
- methyl
- polysaccharide
- ketone
- organic solvent
- bead
- Prior art date
- Legal status (The legal status 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 status listed.)
- Granted
Links
- 239000011324 bead Substances 0.000 title claims abstract description 56
- 150000004676 glycans Chemical class 0.000 title claims abstract description 54
- 229920001282 polysaccharide Polymers 0.000 title claims abstract description 53
- 239000005017 polysaccharide Substances 0.000 title claims abstract description 53
- 238000002360 preparation method Methods 0.000 title description 5
- 238000000034 method Methods 0.000 claims abstract description 44
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims abstract description 32
- 239000012071 phase Substances 0.000 claims abstract description 29
- 239000003960 organic solvent Substances 0.000 claims abstract description 28
- -1 alicyclic ketone Chemical class 0.000 claims abstract description 22
- 239000008346 aqueous phase Substances 0.000 claims abstract description 21
- 239000003995 emulsifying agent Substances 0.000 claims abstract description 21
- 239000007762 w/o emulsion Substances 0.000 claims abstract description 13
- 125000001931 aliphatic group Chemical group 0.000 claims abstract description 4
- 238000007711 solidification Methods 0.000 claims abstract description 4
- 230000008023 solidification Effects 0.000 claims abstract description 4
- 238000004132 cross linking Methods 0.000 claims description 17
- 229920006217 cellulose acetate butyrate Polymers 0.000 claims description 15
- JHIVVAPYMSGYDF-UHFFFAOYSA-N cyclohexanone Chemical compound O=C1CCCCC1 JHIVVAPYMSGYDF-UHFFFAOYSA-N 0.000 claims description 13
- 239000000203 mixture Substances 0.000 claims description 12
- 229920002307 Dextran Polymers 0.000 claims description 11
- FFWSICBKRCICMR-UHFFFAOYSA-N 5-methyl-2-hexanone Chemical compound CC(C)CCC(C)=O FFWSICBKRCICMR-UHFFFAOYSA-N 0.000 claims description 10
- NTIZESTWPVYFNL-UHFFFAOYSA-N Methyl isobutyl ketone Chemical compound CC(C)CC(C)=O NTIZESTWPVYFNL-UHFFFAOYSA-N 0.000 claims description 10
- UIHCLUNTQKBZGK-UHFFFAOYSA-N Methyl isobutyl ketone Natural products CCC(C)C(C)=O UIHCLUNTQKBZGK-UHFFFAOYSA-N 0.000 claims description 10
- CATSNJVOTSVZJV-UHFFFAOYSA-N heptan-2-one Chemical compound CCCCCC(C)=O CATSNJVOTSVZJV-UHFFFAOYSA-N 0.000 claims description 10
- 229940043265 methyl isobutyl ketone Drugs 0.000 claims description 10
- LFSAPCRASZRSKS-UHFFFAOYSA-N 2-methylcyclohexan-1-one Chemical group CC1CCCCC1=O LFSAPCRASZRSKS-UHFFFAOYSA-N 0.000 claims description 9
- VGVHNLRUAMRIEW-UHFFFAOYSA-N 4-methylcyclohexan-1-one Chemical class CC1CCC(=O)CC1 VGVHNLRUAMRIEW-UHFFFAOYSA-N 0.000 claims description 9
- 229920002678 cellulose Polymers 0.000 claims description 7
- 239000003431 cross linking reagent Substances 0.000 claims description 7
- SKTCDJAMAYNROS-UHFFFAOYSA-N methoxycyclopentane Chemical compound COC1CCCC1 SKTCDJAMAYNROS-UHFFFAOYSA-N 0.000 claims description 7
- PTTPXKJBFFKCEK-UHFFFAOYSA-N 2-Methyl-4-heptanone Chemical compound CC(C)CC(=O)CC(C)C PTTPXKJBFFKCEK-UHFFFAOYSA-N 0.000 claims description 6
- UJBOOUHRTQVGRU-UHFFFAOYSA-N 3-methylcyclohexan-1-one Chemical class CC1CCCC(=O)C1 UJBOOUHRTQVGRU-UHFFFAOYSA-N 0.000 claims description 6
- 239000001913 cellulose Substances 0.000 claims description 4
- 150000002148 esters Chemical class 0.000 claims description 4
- 229910052739 hydrogen Inorganic materials 0.000 claims description 4
- 239000001257 hydrogen Substances 0.000 claims description 4
- BRLQWZUYTZBJKN-UHFFFAOYSA-N Epichlorohydrin Chemical compound ClCC1CO1 BRLQWZUYTZBJKN-UHFFFAOYSA-N 0.000 claims description 3
- 238000004113 cell culture Methods 0.000 claims description 3
- 125000000753 cycloalkyl group Chemical group 0.000 claims description 3
- 229910052736 halogen Inorganic materials 0.000 claims description 3
- 150000002367 halogens Chemical class 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 239000000356 contaminant Substances 0.000 claims description 2
- 239000012535 impurity Substances 0.000 claims description 2
- UXJMXERXJQAWSP-UHFFFAOYSA-N 2-pentylcyclohexan-1-one Chemical compound CCCCCC1CCCCC1=O UXJMXERXJQAWSP-UHFFFAOYSA-N 0.000 claims 2
- 125000004435 hydrogen atom Chemical group [H]* 0.000 claims 2
- 150000002576 ketones Chemical class 0.000 claims 2
- MQWCXKGKQLNYQG-UHFFFAOYSA-N methyl cyclohexan-4-ol Natural products CC1CCC(O)CC1 MQWCXKGKQLNYQG-UHFFFAOYSA-N 0.000 claims 2
- 125000000218 acetic acid group Chemical group C(C)(=O)* 0.000 claims 1
- UGZICOVULPINFH-UHFFFAOYSA-N acetic acid;butanoic acid Chemical compound CC(O)=O.CCCC(O)=O UGZICOVULPINFH-UHFFFAOYSA-N 0.000 claims 1
- 125000002723 alicyclic group Chemical group 0.000 claims 1
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 15
- 230000006698 induction Effects 0.000 abstract description 4
- 239000002904 solvent Substances 0.000 description 18
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 12
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- 239000000523 sample Substances 0.000 description 11
- 239000002245 particle Substances 0.000 description 10
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 8
- WSLDOOZREJYCGB-UHFFFAOYSA-N 1,2-Dichloroethane Chemical class ClCCCl WSLDOOZREJYCGB-UHFFFAOYSA-N 0.000 description 7
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 6
- 125000002777 acetyl group Chemical group [H]C([H])([H])C(*)=O 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 5
- 238000004945 emulsification Methods 0.000 description 5
- 238000002474 experimental method Methods 0.000 description 4
- 238000001000 micrograph Methods 0.000 description 4
- 238000003756 stirring Methods 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
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- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical compound CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 description 2
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- 229920002472 Starch Polymers 0.000 description 2
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- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 2
- NOESYZHRGYRDHS-UHFFFAOYSA-N insulin Chemical compound N1C(=O)C(NC(=O)C(CCC(N)=O)NC(=O)C(CCC(O)=O)NC(=O)C(C(C)C)NC(=O)C(NC(=O)CN)C(C)CC)CSSCC(C(NC(CO)C(=O)NC(CC(C)C)C(=O)NC(CC=2C=CC(O)=CC=2)C(=O)NC(CCC(N)=O)C(=O)NC(CC(C)C)C(=O)NC(CCC(O)=O)C(=O)NC(CC(N)=O)C(=O)NC(CC=2C=CC(O)=CC=2)C(=O)NC(CSSCC(NC(=O)C(C(C)C)NC(=O)C(CC(C)C)NC(=O)C(CC=2C=CC(O)=CC=2)NC(=O)C(CC(C)C)NC(=O)C(C)NC(=O)C(CCC(O)=O)NC(=O)C(C(C)C)NC(=O)C(CC(C)C)NC(=O)C(CC=2NC=NC=2)NC(=O)C(CO)NC(=O)CNC2=O)C(=O)NCC(=O)NC(CCC(O)=O)C(=O)NC(CCCNC(N)=N)C(=O)NCC(=O)NC(CC=3C=CC=CC=3)C(=O)NC(CC=3C=CC=CC=3)C(=O)NC(CC=3C=CC(O)=CC=3)C(=O)NC(C(C)O)C(=O)N3C(CCC3)C(=O)NC(CCCCN)C(=O)NC(C)C(O)=O)C(=O)NC(CC(N)=O)C(O)=O)=O)NC(=O)C(C(C)CC)NC(=O)C(CO)NC(=O)C(C(C)O)NC(=O)C1CSSCC2NC(=O)C(CC(C)C)NC(=O)C(NC(=O)C(CCC(N)=O)NC(=O)C(CC(N)=O)NC(=O)C(NC(=O)C(N)CC=1C=CC=CC=1)C(C)C)CC1=CN=CN1 NOESYZHRGYRDHS-UHFFFAOYSA-N 0.000 description 2
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- WMOVHXAZOJBABW-UHFFFAOYSA-N tert-butyl acetate Chemical compound CC(=O)OC(C)(C)C WMOVHXAZOJBABW-UHFFFAOYSA-N 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- BFSVOASYOCHEOV-UHFFFAOYSA-N 2-diethylaminoethanol Chemical compound CCN(CC)CCO BFSVOASYOCHEOV-UHFFFAOYSA-N 0.000 description 1
- 229920000945 Amylopectin Polymers 0.000 description 1
- 238000007445 Chromatographic isolation Methods 0.000 description 1
- 102000010911 Enzyme Precursors Human genes 0.000 description 1
- 108010062466 Enzyme Precursors Proteins 0.000 description 1
- 239000001856 Ethyl cellulose Substances 0.000 description 1
- ZZSNKZQZMQGXPY-UHFFFAOYSA-N Ethyl cellulose Chemical group CCOCC1OC(OC)C(OCC)C(OCC)C1OC1C(O)C(O)C(OC)C(CO)O1 ZZSNKZQZMQGXPY-UHFFFAOYSA-N 0.000 description 1
- 241000287828 Gallus gallus Species 0.000 description 1
- 229920002907 Guar gum Polymers 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 102000004877 Insulin Human genes 0.000 description 1
- 108090001061 Insulin Proteins 0.000 description 1
- 229920002752 Konjac Polymers 0.000 description 1
- 229920000161 Locust bean gum Polymers 0.000 description 1
- 102000016943 Muramidase Human genes 0.000 description 1
- 108010014251 Muramidase Proteins 0.000 description 1
- 108010062010 N-Acetylmuramoyl-L-alanine Amidase Proteins 0.000 description 1
- 108020002230 Pancreatic Ribonuclease Proteins 0.000 description 1
- 102000005891 Pancreatic ribonuclease Human genes 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 102000007056 Recombinant Fusion Proteins Human genes 0.000 description 1
- 108010008281 Recombinant Fusion Proteins Proteins 0.000 description 1
- MZVQCMJNVPIDEA-UHFFFAOYSA-N [CH2]CN(CC)CC Chemical group [CH2]CN(CC)CC MZVQCMJNVPIDEA-UHFFFAOYSA-N 0.000 description 1
- 125000002252 acyl group Chemical group 0.000 description 1
- 230000001464 adherent effect Effects 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
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- 235000010443 alginic acid Nutrition 0.000 description 1
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- CGZZMOTZOONQIA-UHFFFAOYSA-N cycloheptanone Chemical compound O=C1CCCCCC1 CGZZMOTZOONQIA-UHFFFAOYSA-N 0.000 description 1
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- AFOSIXZFDONLBT-UHFFFAOYSA-N divinyl sulfone Chemical compound C=CS(=O)(=O)C=C AFOSIXZFDONLBT-UHFFFAOYSA-N 0.000 description 1
- 230000001804 emulsifying effect Effects 0.000 description 1
- IDGUHHHQCWSQLU-UHFFFAOYSA-N ethanol;hydrate Chemical compound O.CCO IDGUHHHQCWSQLU-UHFFFAOYSA-N 0.000 description 1
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- JBTWLSYIZRCDFO-UHFFFAOYSA-N ethyl methyl carbonate Chemical compound CCOC(=O)OC JBTWLSYIZRCDFO-UHFFFAOYSA-N 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 238000002523 gelfiltration Methods 0.000 description 1
- 239000000665 guar gum Substances 0.000 description 1
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- 229960002154 guar gum Drugs 0.000 description 1
- 125000005843 halogen group Chemical group 0.000 description 1
- 125000004836 hexamethylene group Chemical group [H]C([H])([*:2])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[*:1] 0.000 description 1
- 230000007062 hydrolysis Effects 0.000 description 1
- 238000006460 hydrolysis reaction Methods 0.000 description 1
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- 229940125396 insulin Drugs 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 235000010420 locust bean gum Nutrition 0.000 description 1
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- 239000004325 lysozyme Substances 0.000 description 1
- 229960000274 lysozyme Drugs 0.000 description 1
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- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
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- BDERNNFJNOPAEC-UHFFFAOYSA-N n-propyl alcohol Natural products CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 1
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- 108090000623 proteins and genes Proteins 0.000 description 1
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- 150000003839 salts Chemical class 0.000 description 1
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- 229910052708 sodium Inorganic materials 0.000 description 1
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- 239000012279 sodium borohydride Substances 0.000 description 1
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- RYFMWSXOAZQYPI-UHFFFAOYSA-K trisodium phosphate Chemical class [Na+].[Na+].[Na+].[O-]P([O-])([O-])=O RYFMWSXOAZQYPI-UHFFFAOYSA-K 0.000 description 1
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- UHVMMEOXYDMDKI-JKYCWFKZSA-L zinc;1-(5-cyanopyridin-2-yl)-3-[(1s,2s)-2-(6-fluoro-2-hydroxy-3-propanoylphenyl)cyclopropyl]urea;diacetate Chemical compound [Zn+2].CC([O-])=O.CC([O-])=O.CCC(=O)C1=CC=C(F)C([C@H]2[C@H](C2)NC(=O)NC=2N=CC(=CC=2)C#N)=C1O UHVMMEOXYDMDKI-JKYCWFKZSA-L 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L5/00—Compositions of polysaccharides or of their derivatives not provided for in groups C08L1/00 or C08L3/00
- C08L5/02—Dextran; Derivatives thereof
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/12—Powdering or granulating
- C08J3/16—Powdering or granulating by coagulating dispersions
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/02—Making microcapsules or microballoons
- B01J13/06—Making microcapsules or microballoons by phase separation
- B01J13/14—Polymerisation; cross-linking
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
- C07K1/14—Extraction; Separation; Purification
- C07K1/16—Extraction; Separation; Purification by chromatography
- C07K1/18—Ion-exchange chromatography
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07K—PEPTIDES
- C07K1/00—General methods for the preparation of peptides, i.e. processes for the organic chemical preparation of peptides or proteins of any length
- C07K1/14—Extraction; Separation; Purification
- C07K1/16—Extraction; Separation; Purification by chromatography
- C07K1/22—Affinity chromatography or related techniques based upon selective absorption processes
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
- C08B37/00—Preparation of polysaccharides not provided for in groups C08B1/00 - C08B35/00; Derivatives thereof
- C08B37/0006—Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid
- C08B37/0009—Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid alpha-D-Glucans, e.g. polydextrose, alternan, glycogen; (alpha-1,4)(alpha-1,6)-D-Glucans; (alpha-1,3)(alpha-1,4)-D-Glucans, e.g. isolichenan or nigeran; (alpha-1,4)-D-Glucans; (alpha-1,3)-D-Glucans, e.g. pseudonigeran; Derivatives thereof
- C08B37/0021—Dextran, i.e. (alpha-1,4)-D-glucan; Derivatives thereof, e.g. Sephadex, i.e. crosslinked dextran
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/24—Crosslinking, e.g. vulcanising, of macromolecules
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- C—CHEMISTRY; METALLURGY
- C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
- C12N—MICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
- C12N5/00—Undifferentiated human, animal or plant cells, e.g. cell lines; Tissues; Cultivation or maintenance thereof; Culture media therefor
- C12N5/0068—General culture methods using substrates
- C12N5/0075—General culture methods using substrates using microcarriers
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- C—CHEMISTRY; METALLURGY
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Abstract
本发明公开一种制备多糖珠粒的方法,其包括以下步骤:i)提供包含多糖水溶液的水相;ii)提供包含至少一种水‑不混溶的有机溶剂和至少一种油溶性乳化剂的油相;iii)使水相在油相中乳化以形成油包水(w/o)乳液;和iv)诱导水相在w/o乳液中的凝固,其中有机溶剂是脂族或脂环族酮或醚。
Description
本发明的技术领域
本发明涉及多糖珠粒,且更特别地涉及通过反相悬浮技术制备多糖珠粒。本发明也涉及交联的多糖珠粒和涉及珠粒用于分离目的的用途。
发明背景
交联的多糖珠粒通常用作蛋白和其它生物分子的色谱分离的静止相。这样的珠粒在二十世纪六十年代早期引入(见例如US3208994,其通过引用以其整体结合到本文中),主要用于实验室分离目的。由于此后它们的应用有极大的提高,并且交联的多糖珠粒现在常规用于分离许多生物药物例如单克隆抗体、血浆成分、胰岛素和各种重组蛋白的大规模制备方法。
制备多糖珠粒的最常见的方法是通过反相悬浮方法,其中多糖的水溶液被乳化为在连续的油相中的油包水(w/o)乳液,并且乳液液滴通过交联或者通过热凝胶化凝固。这样的方法描述于例如US3208994、US4794177和US6602990中(通过引用以其整体结合到本文中),其使用卤代烃或芳族烃作为油相。本文的问题是当前卤代烃和芳族烃的大规模使用因环境原因而被淘汰。
因此对制备多糖珠粒而不使用卤化或芳族溶剂的方法存在着需求。
发明概述
本发明的一个方面是提供制备多糖珠粒的环境可接受的方法。这用如在权利要求中定义的方法实现。
一个优点是所述方法不使用卤化或芳族溶剂。进一步的优点是可获得具有良好的孔隙结构和机械特性的球形珠粒。
本发明的第二个方面是提供适合于分离目的的多糖珠粒。这用如在权利要求书中定义的珠粒实现。
本发明的第三个方面是提供用于分离交联珠粒的目的的用途。这采用如在权利要求中定义的用途实现。
本发明的进一步的合适实施方案描述于从属权利要求中。
附图
图1显示本发明的方法的概要。a) 将水相加入到油相中,b) 油包水乳液,c) 分散于油相中的凝固珠粒。
图2显示依据本发明的实施方案的右旋糖苷与表氯醇的交联。
图3显示来自a) 样品9090 (2-MCH)和b) 样品5595 (3-MCH)的溶胀颗粒的显微镜照片。
图4显示来自样品5624 (环己烷 + 3-MCH)的溶胀颗粒的显微镜照片。
图5显示来自a) 样品6462 (CPME)和b) 样品5182 (CPME + 3-MCH)的溶胀颗粒的显微镜照片。
图6显示来自a) 样品6671 (DIBK)和b) 样品5382 (DIBK + 3-MCH)的溶胀颗粒的显微镜照片。
图7显示来自样品9355 (MAK)的溶胀颗粒的显微镜照片。
实施方案的详述
在一个方面,由图1-2所说明的,本发明公开一种制备多糖珠粒的方法,其包括以下步骤:
i) 提供包含多糖水溶液的水相1。这可通过使多糖溶于水或溶于包含一种或多种另外的成分例如盐、缓冲剂、碱、还原剂等的水中而完成。多糖可例如是天然多糖例如右旋糖苷、支链淀粉、淀粉、藻酸盐、瓜尔胶、刺槐豆胶、魔芋、琼脂、琼脂糖、角叉菜胶等。作为实例,多糖可以是右旋糖苷,例如具有20-4000 kDa、40-2000 kDa或100-500 kDa的重均分子量(Mw)的右旋糖苷。或者,多糖可以是天然多糖的衍生物,例如纤维素醚、琼脂糖醚、淀粉醚、DEAE右旋糖苷等。有利地,多糖在室温或在升高的温度下是水溶性的。
ii) 提供包含至少一种水-不混溶的有机溶剂和至少一种油溶性乳化剂的油相2。水-不混溶的有机溶剂可合适地具有在25℃的小于5 vol. %,例如小于3 vol. %或小于2vol. %的水溶性,并且水在25℃的水-不混溶的有机溶剂中的溶解度可合适地小于5 vol.%,例如小于3 vol. %或小于2 vol. %。油溶性乳化剂可合适地溶于有机溶剂中,并且油相可通过使一种或多种油溶性乳化剂溶于水-不混溶的有机溶剂或水-不混溶的有机溶剂的混合物中来制备。乳化剂在油相中的浓度可例如是0.01-0.5 g/ml,例如0.05-0.3 g/ml。在使用混合的乳化剂的情况下,这些值也可指乳化剂在油相中的总浓度。如果使用聚合物乳化剂,油相的粘度可随着乳化剂的分子量和浓度而变化。
iii) 使水相在油相中乳化以形成油包水(w/o)乳液。如在图1中所说明的,这可例如在通过搅拌器4提供的搅拌下,将水相1加入到在乳化容器3中的油相2中进行,以使水相作为离散的液体小滴5分散于连续油相2中,经乳化剂稳定。本领域已知的其它技术也可使用,例如使用静态混合器、膜乳化等连续乳化。取决于油相的粘性,可能需要某些优化的搅拌强度以获得所产生的珠粒的特定粒径。作为选择(或另外地),乳化剂的浓度和/或类型可以变化以得到一定的粒径。
iv) 诱导水相在w/o乳液中凝固。这意味着液体小滴5通过多糖的凝胶化转化为(固体)凝胶珠粒6。凝胶化可例如通过加入交联剂诱导以化学(共价)交联多糖(如下文进一步讨论的),或通过降低温度以引起多糖的热凝胶化(也如下文讨论的)。一旦水相液滴已凝固成凝胶珠粒,所述珠粒可通过沉降和/或过滤回收,并且它们可被进一步洗涤和加工,以提供适合于分离或细胞培养目的的珠粒。进一步的加工可例如包括进一步的交联步骤和/或用试剂衍生化以引入官能团。
至少一种有机溶剂是脂族或脂环族酮或醚。作为选择,或另外地,至少一种有机溶剂不含卤素(即溶剂的分子不含有卤原子)且具有在δD = 15.0-18.5 MPa1/2,δP = 3.5-8.5MPa1/2和δH = 4.0-5.5 MPa1/2的范围内的汉森溶解度参数值。油相也可包含无卤素的水-不混溶有机溶剂的混合物,其中所述混合物具有在δD = 15.0-18.5 MPa1/2,δP = 3.5- 8.5MPa1/2和δH = 4.0-5.5 MPa1/2的范围内的汉森溶解度参数值。 合适地,卤化溶剂在油相中的含量可小于1 mol %,例如小于0.1%或小于0.01 %。汉森溶解度参数详细讨论于C MHansen:三维溶解度参数和溶剂扩散系数 - 它们在表面涂布制剂中的重要性(The threedimensional solubility parameter and solvent diffusion coefficient – Theirimportance in surface coating formulation), Copenhagen 1967。δD是对溶剂的溶解度参数(内聚能密度)的分散力贡献(dispersion force contribution),而δP是极性力贡献和δH是氢键力贡献。对于不同溶剂的汉森溶解度参数表可例如在J Brandrup, E HImmergut Eds. 聚合物手册(Polymer Handbook),第3版, John Wiley & Sons 1989, pp.VII/540-VII/544中发现。
在某些实施方案中,由图2说明,步骤iv)包括交联多糖。这可例如通过加入交联剂至w/o乳液中实现。交联剂可例如是具有两个亲电子官能团的化合物,其可例如与多糖上的两个羟基反应并通过在多糖链之间形成共价键的链接引起交联。羟基在高pH条件下是特别亲核的,并且在方法中使用高pH水相,例如通过加入NaOH或其它合适的碱(例如KOH)至水相中可能是有利的。在水相中的碱(NaOH或KOH)浓度可例如是至少0.1 M,例如0.1-2 M或0.5-1 M。亲电子交联剂的实例包括表氯醇、二环氧化物和多功能环氧化物,以及二乙烯砜和卤代醇像1,3-二溴-丙醇-2。交联剂可合适地被加入到w/o乳液中,以使它溶于油相并分散到水相液滴中。
在某些实施方案中,步骤iv)包括多糖的热凝胶化。在这种情况下,多糖可以是热水可溶性多糖,其在冷却时形成凝胶。这样的多糖的实例是例如琼脂和琼脂糖,其在约60℃和更高的温度下是可溶性的,但在冷却至例如约40℃或更低温度时形成固体凝胶。在这种情况下,步骤i)-iii)可在多糖为可溶性的温度下进行,而在步骤iv)中,温度被降至低于所用特殊多糖的凝胶点的温度。
在某些实施方案中,至少一种乳化剂是纤维素衍生物,例如纤维素酯或纤维素醚。在纤维素酯中,纤维素混合的酯,例如乙酸丁酸纤维素可能是特别有用的。不同级别的乙酸丁酸纤维素(CAB)是可市售获得的,例如得自Eastman Chemical Company (USA)。CAB的分子量可合适地是10-100 kDa,例如15-75 kDa或16-70 kDa,通过凝胶渗透层析作为聚苯乙烯等同物数均分子量(Mn)测定。乙酰基和丁酰基含量可例如是2-20 wt. %乙酰基含量和20-60 wt. %丁酰基含量,例如a) 10-15wt.%乙酰基含量和30-40 wt.%丁酰基含量或b) 2-5 wt.%乙酰基含量和50-60 wt.%丁酰基含量或c) 2-15 wt.%乙酰基含量和30-60 wt.%丁酰基含量。可用作乳化剂的纤维素醚的实例是乙基纤维素。
在一些实施方案中,至少一种有机溶剂是C6-C10脂族或脂环族酮或醚,例如C6-C10脂环族酮或醚。这样的溶剂的实例是由式I、II或III定义的那些,
其中:
R1和R2各自独立地为C1-C5烷基;
R3是C1-C5亚烷基;
R4是连接于环结构中的非-羰基碳原子的任何一个上的氢或C1-C5烷基;和
R5和R6各自独立地为C1-C6烷基或环烷基。
在一些实施方案中,至少一种有机溶剂由式II定义,其中R3和R4如上定义。R3可以例如是C2亚烷基和R4可以是甲基。
在某些实施方案中,有机溶剂可选自2-甲基环己酮、3-甲基环己酮、4-甲基环己酮、环己酮、二异丁基酮、甲基正戊基酮、甲基异戊基酮、甲基异丁基酮、环戊基甲基醚及其混合物。至少一种有机溶剂可例如选自2-甲基环己酮、3-甲基环己酮、4-甲基环己酮、环己酮、甲基正戊基酮、甲基异戊基酮、甲基异丁基酮和环戊基甲基醚,例如选自2-甲基环己酮、3-甲基环己酮、4-甲基环己酮和环己酮。在特殊的情况下,至少一种有机溶剂可以是2-甲基环己酮。
在第二个方面,本发明公开一种通过以上公开的任何实施方案的方法制备的多糖珠粒,或多种多糖珠粒。本发明也公开一种交联的多糖珠粒,或多种交联的多糖珠粒,包含至少0.1 ppm,例如0.1-100 ppm的C6-C10脂族或脂环族酮或醚。这可例如构成来自如上讨论的制备方法的溶剂残留物。所述量可例如通过顶部空间GC或提取物的GC分析,使用例如质谱或火焰电离作为检测方法来测量。C6-C10脂族或脂环族酮或醚可通过如上讨论的式I、II或III定义,并且它可例如选自2-甲基环己酮、3-甲基环己酮、4-甲基环己酮、环己酮、二异丁酮、甲基正戊基酮、甲基异戊基酮、甲基异丁基酮、环戊基甲基醚及其混合物。
在一些实施方案中,所述珠粒或多个珠粒在干燥的形式具有40-125 μm的直径。在多个珠粒的情况下,直径可作为体积-权重中位数直径d50v,例如通过激光衍射或通过电区(electrozone)传感计数技术测定。
在某些实施方案中,所述珠粒或多个珠粒包含至少0.1 mmol/g,或1-6 mmol/g,共价键合的荷电基团,例如羧甲基-、磺丙基-、二乙基氨基乙基-,和/或二乙基-(2-羟基-丙基)氨基乙基-基团。这样的基团对于离子交换分离是有用的,并且当所述珠粒被用作细胞培养中的微载体时,基团像二乙基氨基乙基也可促进粘附细胞的生长。使用荷电基团的衍生化可通过本领域熟知的方法完成。
在第三个方面,本发明公开一种或多种如上所述的多糖珠粒用于将目标生物分子例如目标蛋白与杂质或污染物分离的用途。
在第四个方面,本发明公开一种或多种如上所述的多糖珠粒作为细胞培养的微载体的用途。
实施例
乳化方法(参考实施例使用1,2-二氯乙烷)
使165 g右旋糖苷(Mw 150-250 kD)溶于390 ml蒸馏水,同时在搅拌下加入22 ml 50%氢氧化钠(NaOH)。将0.8 g硼氢化钠(NaBH4)加入到溶液中。
将21g乙酸丁酸纤维素(CAB)加入到一个附有顶部搅拌器的1000 ml玻璃反应器中。启动搅拌器并加入350 ml 1,2-二氯乙烷(EDC) (因此CAB浓度是0.060 g/ml EDC)。搅拌溶液直至CAB溶解。然后于50℃搅拌下,将水相加入到油相中,并继续搅拌直至达到合适的液滴大小,如从抽出的小样本的显微镜检所判断的。当获得合适的大小时,通过加入22.4ml表氯醇(ECH)以交联右旋糖苷并因此固化液滴来立即稳定乳液。加入ECH后20分钟,加入50 ml EDC使反应混合物较少粘性并容易搅拌。
在加入500 ml丙酮20±4h后终止交联反应。然后将反应混合物转移至一个含有1250 ml丙酮的3000 ml玻璃反应器中。搅拌溶液30 min,然后允许凝胶沉降。倾出上清液,并且洗涤程序用丙酮重复5次,然后用60%乙醇水溶液洗涤7次并用95%乙醇洗涤4次。然后于60℃真空下干燥凝胶48 h,并且生成的粉末经40和100 μm之间的筛过筛。
来自该实验的5次重复的结果示于表2,如样品3077、3088、3092、3081和1175。
SEC分析
将大约3-4克粉末称重至一塑料瓶中,该瓶中已加入大约100 ml的或者9 mg/ml NaCl溶液或者运行缓冲液(0.15M NaCl+ 0.05 M磷酸盐缓冲液,pH 7.0)。凝胶经放置溶胀并沉降至少16小时。然后将其洗涤数次并以运行缓冲液稀释以生成一种50-60%的凝胶浆液。10mm直径和30 cm高度的柱(GE Healthcare HR10/30)用1.0或者1.2 ml/min的初始流速填充,并且最终流速是1.2或者1.7 ml/min。然后在有效性试验中测试填充柱并通过选择性试验,用右旋糖苷标准品和蛋白评价,如描述于L Hagel: pp. 51-87,J C Janson (Ed):蛋白纯化:原理,高分辨率的方法,和应用(Protein Purification: Principles, HighResolution Methods, and Applications),第3版,Wiley 2011。试验蛋白是α胰凝乳蛋白酶原II型,牛(Mw 26 kDa),核糖核酸酶A,牛(Mw 13.7 kDa)和溶菌酶,鸡(Mw 14.3 kDa),伴有0.15 M NaCl、0.05M磷酸钠(pH 7.0)作为运行缓冲液。这些蛋白关于原型的KD数据(即可接近特定尺寸的探针分子的珠粒体积的分数)示于表3。
吸水量(Water regain)
吸水量(Wr)是1 g干燥珠粒在所述珠粒内吸收的水的量。高Wr值指示溶胀的凝胶是密度较低的并可分离高Mw目标分子。用500 ml水平衡15 g干燥珠粒24 h。带有10 μm底部过滤器的3.3 x 11.5 cm称重离心管填充有凝胶浆液并以1800 rpm离心10 min。在测定管的湿重后,于105℃干燥过夜,并测定干重。吸水量被计算为每g干燥凝胶的干燥重量损失(作为ml水)。
粒径分布
粒径分布以库尔特粒度分析仪(Coulter Multisizer) (Beckman Coulter),使用电区感应技术测定。
显微镜检查
交联后,所述珠粒以具有相差光学器件的光学显微镜检查,并且注意到表面凹痕、夹杂物、聚集体等的存在。
使用不同溶剂的乳化
溶剂缩略语
CPME - 环戊基甲基醚
DIBK - 二异丁酮(2,6-二甲基-4-庚酮)
EDC - 1,2-二氯乙烷
MAK - 甲基正戊基酮
2-MCH - 2-甲基环己酮
3-MCH - 3-甲基环己酮
4-MCH - 4-甲基环己酮
依据以上参考实施例,用其它溶剂代替EDC,并在某些情况下用不同类型和/或浓度的CAB进行乳化。所用的CAB类型在表1中指定。所述珠粒如上所述进行表征,并且结果整理于表2和3中并在下文讨论。
表1. 所用的CAB类型(全部来自Eastman Chemical Company并伴有依据供应商的数据表的数据)
CAB类型 | 分子量*, kDa | 粘度**,泊 | 丁酰基含量, wt % | 乙酰基含量, wt % |
381-0.5 | 30 | 1.9 | 37 | 13 |
381-20 | 70 | 76 | 37 | 13.5 |
500-5 | 57 | 19 | 51 | 4 |
551-0.01 | 16 | 0.038 | 53 | 2 |
* 聚苯乙烯等同物数均分子量(Mn),如通过凝胶渗透层析测定的
** 通过ASTM方法D 1343测定的粘度。使用如对于ASTM方法D 817 (20%纤维素酯、72%丙酮、8%乙醇)中所述的式A的溶液密度,将结果转化为泊(ASTM方法D 1343)。
表2. 得自用不同溶剂和溶剂组合乳化的结果
表3. 在用填充在柱中的原型进行的凝胶过滤实验中3种试验蛋白的KD数据
所用的溶剂也在右旋糖苷和乳化剂的不存在下执行的乳化模型实验前后,通过NMR光谱学分析。之前和之后的光谱是基本上相同的,显示在所用的反应条件期间没有降解发生。这与酯溶剂乙酸叔丁酯形成对比,虽然乙酸叔丁酯是一种空间位阻酯,但在所用的强碱性条件下完全水解。
讨论
经评价的溶剂产生可用于层析的珠粒,例如通过它们在SEC分析中的性能所证实的。测量的特性是在关于参考原型的相同范围内,其显示新溶剂表现优异。由于溶剂和CAB乳化剂之间的不同相互作用,CAB类型和浓度必须变化以得到合适的油相粘度。珠粒通常是球形的(图7-11),但使用溶剂3-MCH和4-MCH (特别是当单独使用时),一些夹杂物和表面凹痕出现在珠粒上。
本书面描述使用实施例来公开本发明,包括最佳模式,并且还能使本领域任何技术人员实践本发明,包括制作和使用任何装置或系统并执行任何合并的方法。本发明的可专利范围受权利要求书的限定,并可包括本领域技术人员想到的其它实施例。意欲使这样的其它实施例落入权利要求书的范围内,如果它们具有不同于权利要求书的文字语言的结构元素,或如果它们包括与权利要求书的文字语言无实质不同的等同结构元素的话。本文提供的任何专利或专利申请通过引用以其整体结合到本文中,如同它们各自被结合到本文中一样。
Claims (29)
1.一种制备多糖珠粒的方法,其包括以下步骤:
i) 提供包含多糖水溶液的水相;
ii) 提供包含至少一种水-不混溶的有机溶剂和至少一种油溶性乳化剂的油相;
iii) 使所述水相在所述油相中乳化以形成油包水(w/o)乳液;和
iv) 诱导所述水相在所述w/o乳液中的凝固,
其中所述至少一种有机溶剂是脂族或脂环族酮或醚。
2.一种制备多糖珠粒的方法,其包括以下步骤:
i) 提供包含多糖水溶液的水相;
ii) 提供包含至少一种水-不混溶的有机溶剂和至少一种油溶性乳化剂的油相;
iii) 使所述水相在所述油相中乳化以形成油包水(w/o)乳液;和
iv) 诱导所述水相在所述w/o乳液中的凝固,
其中所述至少一种有机溶剂不含卤素且具有在δD = 15.0-18.5 MPa1/2,δP = 3.5-8.5MPa1/2和δH = 4.0-5.5 MPa1/2的范围内的汉森溶解度参数值,或其中所述油相包含无卤素的水-不混溶有机溶剂的混合物,所述混合物具有在δD = 15.0-18.5 MPa1/2,δP = 3.5-8.5MPa1/2和δH = 4.0-5.5 MPa1/2的范围内的汉森溶解度参数值。
3.权利要求2的方法,其中所述至少一种有机溶剂是脂族或脂环族酮或醚,例如脂环族酮或醚。
4.任一项前述权利要求的方法,其中步骤iv)包括交联所述多糖。
5.权利要求4的方法,其中在步骤iv)中,交联剂被加入到所述w/o乳液中。
6.权利要求的方法,其中所述交联剂包含表氯醇或二环氧化物。
7.权利要求4-6的任一项的方法,其中所述交联在碱性条件下进行。
8.任一项前述权利要求的方法,其中所述多糖包含右旋糖苷。
9. 权利要求8的方法,其中所述右旋糖苷具有20-4000 kDa的重均分子量,Mw。
10. 任一项前述权利要求的方法,其中所述乳化剂在所述油相中的浓度是0.01-0.5g/ml。
11.任一项前述权利要求的方法,其中所述至少一种乳化剂是纤维素衍生物,例如纤维素酯。
12.权利要求11的方法,其中所述至少一种乳化剂是纤维素混合的酯,例如乙酸丁酸纤维素。
13. 权利要求12的方法,其中所述至少一种乳化剂是具有10-100 kDa,例如15-75 kDa的平均分子量Mn的乙酸丁酸纤维素。
14. 权利要求12或13的方法,其中所述至少一种乳化剂是具有2-20 wt. %乙酰基含量和20-60 wt. %丁酰基含量的乙酸丁酸纤维素。
15.任一项前述权利要求的方法,其中所述至少一种有机溶剂是C6-C10脂族或脂环族酮或醚,例如C6-C10脂环族酮或醚。
16.任一项前述权利要求的方法,其中所述至少一种有机溶剂由式I、II或III定义,
其中:
R1和R2各自独立地为C1-C5烷基;
R3是C1-C5亚烷基;
R4是氢或C1-C5烷基;和
R5和R6各自独立地为C1-C6烷基或环烷基。
17.权利要求16的方法,其中所述至少一种有机溶剂由式II定义。
18.任一项前述权利要求的方法,其中所述至少一种有机溶剂选自2-甲基环己酮、3-甲基环己酮、4-甲基环己酮、环己酮、二异丁酮、甲基正戊基酮、甲基异戊基酮、甲基异丁基酮、环戊基甲基醚及其混合物。
19.权利要求18的方法,其中所述至少一种有机溶剂选自2-甲基环己酮、3-甲基环己酮、4-甲基环己酮和环己酮。
20.权利要求19的方法,其中所述至少一种有机溶剂是2-甲基环己酮。
21.一种多糖珠粒,其由任一项前述权利要求的方法制备。
22. 一种交联的多糖珠粒,其包含至少0.1 ppm,例如0.1-100 ppm的C6-C10脂族或脂环族酮或醚。
23.权利要求19的交联的多糖珠粒,其中所述C6-C10脂族或脂环族酮或醚由式I、II或III,例如由式II定义,
其中:
R1和R2各自独立地为C1-C5烷基;
R3是C1-C5亚烷基;
R4是氢或C1-C5烷基;和
R5和R6各自独立地为C1-C6烷基或环烷基。
24.权利要求19或20的交联的多糖珠粒,其中所述C6-C10脂族或脂环族酮或醚选自2-甲基环己酮、3-甲基环己酮、4-甲基环己酮、环己酮、二异丁酮、甲基正戊基酮、甲基异戊基酮、甲基异丁基酮、环戊基甲基醚及其混合物。
25.权利要求23的珠粒,其中所述有机溶剂选自2-甲基环己酮、3-甲基环己酮、4-甲基环己酮和环己酮。
26. 权利要求20-24的任一项的交联的多糖珠粒,其在干燥形式具有40-125 μm的直径。
27. 权利要求20-25的任一项的交联的多糖珠粒,其包含至少0.1 mmol/g,或1-6mmol/g,共价键合的荷电基团,例如羧甲基-、磺丙基-、二乙基氨基乙基-,和/或二乙基-(2-羟基-丙基)氨基乙基-基团。
28.依据权利要求20-26的任一项的一种或多种多糖珠粒在将目标生物分子例如目标蛋白与杂质或污染物分离中的用途。
29.依据权利要求20-26的任一项的一种或多种多糖珠粒作为细胞培养的微载体的用途。
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