Fractionation of charged polysaccharide

09790288 · 2017-10-17

Assignee

Inventors

Cpc classification

International classification

Abstract

Polydisperse and charged polysaccharides are fractionated into low polydispersity fractions (preferably having pd<1.1), each containing species within a narrow range of molecular weights. An aqueous solution of the polydisperse polysaccharides is contacted with an ion exchange resin in a column and the polysaccharides are subjected to selective elution by aqueous elution buffer. The selective elution consists of at least 3 sequential elution buffers having different and constant ionic strength and/or pH and in which the subsequent buffers have ionic strength and/or pH than those of the preceding step. The new preparations are particularly suitable for the production of PSA-derivatised therapeutic agents intended for use in humans and animals.

Claims

1. A process for separating a population of polydisperse polysialic acid compounds into fractions of different molecular weight and narrow polydispersity, the process comprising the steps of: sequentially applying at least three elution buffers to an ion-exchange column previously contacted with a solution comprising the population of polydisperse polysialic acid compounds, the application of each of the at least three elution buffers resulting in a selective elution of a fraction of polysialic acid compounds, thereby separating the population of polydisperse polysialic acid compounds into fractions of different molecular weight and narrow polydispersity, wherein each of the fractions comprise polysialic acid compounds having at least 10 sialic acid units and a polydispersity of less than 1.2, wherein the at least three elution buffers include a first elution buffer, a second elution buffer and a third elution buffer, and wherein the second elution buffer has a higher pH than the first elution buffer and the third elution buffer has a higher pH than the second elution buffer.

2. The process of claim 1, wherein each of the at least three elution buffers is non-reactive and volatile.

3. The process of claim 1, wherein each of the at least three elution buffers comprises an amine.

4. The process of claim 3, wherein the amine comprises triethanolamine.

5. The process of claim 1, wherein the ionic strength of each of the at least three elution buffers is less than 25 mM.

6. The process of claim 1, wherein the pH of each of the at least three elution buffers is in the range of 7.4 to 13.

7. The process of claim 1, wherein the pH value of the first elution buffer is 7.4.

8. The process of claim 1, wherein the higher pH difference between the first elution buffer and the second elution buffer is 0.2 units.

9. The process of claim 1, wherein the higher pH difference between the second elution buffer and the third elution buffer is 0.2 units.

10. The process of claim 1, wherein the higher pH difference between the first elution buffer and the second elution buffer is substantially the same as the higher pH difference between the second elution buffer and the third elution buffer.

11. The process of claim 10, wherein the higher pH difference between the first elution buffer and the second elution buffer is 0.2 units and wherein the higher pH difference between the second elution buffer and the third elution buffer is 0.2 units.

12. The process of claim 1, wherein a volume used for each of the at least three elution buffers is no more than 3 column volumes.

13. The process of claim 12, wherein a volume used for each of the at least three elution buffers is at least 1 column volume.

14. The process of claim 13, wherein a volume used for each of the at least three elution buffers is at least 1.25 column volumes.

15. The process of claim 14, wherein a volume used for each of the at least three elution buffers is at least 1.5 column volumes.

16. The process of claim 1, wherein the process comprises the application of at least five elution buffers, wherein the at least five elution buffers include a first elution buffer, a second elution buffer, a third elution buffer, a fourth elution buffer and a fifth elution buffer, wherein the second elution buffer has a higher ionic strength than the first elution buffer, the third elution buffer has a higher ionic strength than the second elution buffer, the fourth elution buffer has a higher ionic strength than the third elution buffer and the fifth elution buffer has a higher ionic strength than the fourth elution buffer.

17. The process of claim 15, wherein the process further comprises the application of from 6 to 12 elution buffers, wherein the 6 to 12 elution buffers include a sixth elution buffer, a seventh elution buffer, an eighth elution buffer, a ninth elution buffer, a tenth elution buffer, a eleventh elution buffer and a twelfth elution buffer, wherein the seventh elution buffer has a higher ionic strength than the sixth elution buffer, the third eighth buffer has a higher ionic strength than the seventh elution buffer, the ninth elution buffer has a higher ionic strength than the eighth elution buffer, the tenth elution buffer has a higher ionic strength than the ninth elution buffer, the eleventh elution buffer has a higher ionic strength than the tenth elution buffer and the twelfth elution buffer has a higher ionic strength than the eleventh elution buffer.

18. The process of claim 1, wherein the fraction of polysialic acid compounds comprise native polysialic acid compounds or activated polysialic acid compounds.

19. The process of claim 1, wherein the fraction of polysialic acid compounds comprise (i) a polysialic acid polymer, (ii) a polysialic acid copolymer, (iii) a hydrolyzed product of (i) or (ii), or (iv) a functionalized derivative of (i), (ii), or (iii).

20. The process of claim 19, wherein the polysialic acid polymer comprises a poly(2,8-linked sialic acid) polymer, a poly(2,9-linked sialic acid) polymer, or both.

21. The process of claim 19, wherein the polysialic acid co-polymer comprises alternating 2,8-linked sialic acid and 2,9-linked sialic acid co-polymers.

22. The process of claim 19, wherein the functionalized derivative comprises an oxidized derivative, a reduced derivative, an aminated derivative, and/or a hydrazide derivative.

23. The process of claim 1, wherein the fraction of polysialic acid compounds comprise (i) colominic acid, (ii) a hydrolyzed product of (i), or (ii) a functionalized derivative of (i) or (ii).

24. The process of claim 1, wherein the fraction of polysialic acid compounds have 10-500 sialic acid units.

25. The process of claim 1, wherein the fraction of polysialic acid compounds comprise polysialic acid having an average molecular weight of above 5 kDa.

26. The process of claim 1, wherein the fraction of polysialic acid compounds comprise a polysialylated macromolecule.

27. The process of claim 1, wherein the fraction of polysialic acid compounds comprise a polysialylated macromolecule.

28. The process of claim 27, wherein the polysialylated macromolecule is a protein or peptide therapeutically active agent conjugated to a polysialic acid.

29. The process of claim 27, wherein the protein or peptide therapeutically active agent is a cytokine, a growth hormone, an enzyme, a hormone, an antibody or an antibody fragment.

30. The process of claim 1, wherein each of the fractions comprise polysialic acid compounds having at least 10 sialic acid units and a polydispersity of less than 1.1.

Description

(1) FIG. 1a is a reaction scheme showing preparation of monofunctional CA;

(2) FIG. 1b is a reaction scheme showing preparation of products using original conjugation methods;

(3) FIG. 2 is a reaction scheme showing preparation of protein-CA conjugates;

(4) FIG. 3 shows the results of the Gel Permeation Chromatography of CA;

(5) FIG. 4 shows % population of different CA fractions;

(6) FIG. 5 shows a typical native page of CA with molecular weights;

(7) FIG. 6 shows the native PAGE of CA (22.7 KDa; pd 1.34);

(8) FIG. 7 shows a typical chromatogram for CA fractions;

(9) FIG. 8 shows the CA samples from different steps of fractionation;

(10) FIG. 9 shows the loading of different amounts of CA samples;

(11) FIG. 10 shows the fractionation of CA (150 mg of CA; 5 ml matrix);

(12) FIG. 11 shows the fractionation of CA (200 mg; 5 ml);

(13) FIG. 12 shows the fractionation of CA-N H.sub.2,

(14) FIG. 13 shows the anion exchange chromatography of oxidised CA (22.7 KDa);

(15) FIG. 14 shows the anion exchange chromatography of monofunctional CA;

(16) FIG. 15 shows SDS PAGE for preparation of protein-polymer conjugates with broad and narrow dispersed polymer;

(17) FIG. 16 shows native PAGE results for fractionation of CA by anion exchange chromatography vs filteration;

(18) FIG. 17 shows the fractionation of CA by ethanol precipitation;

(19) FIG. 18 shows the fractionation of CA by ultrafilteration;

(20) FIG. 19 shows the anion exchange chromatography of GH-CA conjugates;

(21) FIG. 20 shows the characterization of CA (35 KDa) by NMR;

(22) FIG. 21 shows % population of large scale IEC fractionation of CA (39 kDa; pd 1:4);

(23) FIG. 22 shows the native PAGE of CA (39 kDa; 12.5 g) IEC fractions;

(24) FIG. 23 shows % population of small scale IEC fractionation of CA (39 kDa; pd 1.4);

(25) FIG. 24 shows the native PAGE of CA (39 kDa; 200 mg) IEC fractions;

(26) FIG. 25 shows a typical GPC chromatogram for a narrow dispersed CA;

(27) FIG. 26 shows optimisation of native-PAGE analysis of CA;

(28) FIG. 27 shows native PAGE of CA fractions from IEC;

(29) FIG. 28 shows native PAGEs of CA (22.7 kDa) IEC fractions using increasing ionic strength of triethanolamine;

(30) FIG. 29 shows the native PAGE of Q FF fractionation of CA (22.7 kDa) using increasing ionic strength of triethanolamine acetate; and

(31) FIG. 30 shows the native PAGE of DEAE fractionation of CA (22.7 kDa) using a gradient pH system.

(32) The invention is illustrated further in the accompanying examples.

EXAMPLES

(33) Materials

(34) Ammonium carbonate, ethylene glycol, PEG (8 KDa), sodium cyanoborohydride (>98% pure), sodium meta-periodate, triethanolamine, sodium chloride, sodium nitrate, sodium azide, PBS tablets and molecular weight markers were obtained from Sigma Chemical Laboratory, UK. The CA used, linear alpha-(2.fwdarw.8)-linked E. coli K1 PSAs (22.7 kDa average, high polydispersity 1.34; 39 kDa, p.d. 1.4; 11 kDa, p.d. 1.27) was from Camida, Ireland, Other materials included 2,4 dinitrophenyl hydrazine (2,4 DNPH) (Aldrich Chemical Company, UK), dialysis tubing (3.5 kDa and 10 kDa cut off limits; Medicell International Limited, UK), Sepharose SP HiTrap, PD-10 columns (Pharmacia, UK), Tris-glycine polyacrylamide gels (4-20%), Tris-glycine sodium dodecylsulphate running buffer and loading buffer (Novex, UK), Sepharose Q FF and DEAE (Amersham Biosciences, UK), Tris-Borate-EDTA (TBE) polyacrylamide gels (4-20% and 20%), TBE buffer and loading buffer (Invitrogen, UK). Deionised water was obtained from an Elgastat Option 4 water purification unit (Elga Limited, UK). All reagents used were of analytical grade. A plate reader (Dynex Technologies, UK) was used for spectrophotometric determinations in protein or CA assays.

(35) Methods

(36) Protein and Colominic Acid Determination

(37) Quantitative estimation of PSAs (as sialic acid) was carried out by the resorcinol method [Svennerholm 1957] as described elsewhere [Gregoriadis et. al., 1993; Fernandes and Gregoriadis, 1996, 1997]. Protein was measured by the bicinchoninic acid (BCA) colorimetric method.

Example 1

Preparation of Monofunctional PSA

(38) 1a Activation of CA

(39) Freshly prepared 0.02 M sodium metaperiodate (NaIO.sub.4; 6 fold molar excess over CA) solution was mixed with CA at 20° C. and the reaction mixture was stirred magnetically for 15 min in the dark. The oxidised CA was precipitated with 70% (final concentration) ethanol and by centrifuging the mixture at 3000 g for 20 minutes. The supernatant was removed and the pellet was dissolved in a minimum quantity of deionised water. The CA was again precipitated with 70% ethanol and then centrifuged at 12,000 g. The pellet was dissolved in a minimum quantity of water, lyophilized and stored at −20° C. until further use (FIG. 1; step 1).

(40) 1b. Reduction of CA

(41) Oxidised CA (CAO; 22.7 kDa) was reduced in presence of sodium borohydride. Freshly prepared 15 mM sodium borohydride (NaBH.sub.4; in 0.1M NaOH diluted to pH 8-8.5 by diluting with dilute H.sub.2SO.sub.4 solution) was mixed with CAO (100 mg CA/ml) at 20° C. and the reaction mixture was stirred for up to 2 h in the dark. The pH was brought down to 7 by the completion of the reaction. The oxidised/reduced CA (CAOR) was dialysed (3.5 kDa molecular weight cut-off for dialysis tubing) against 0.01% ammonium carbonate buffer pH 7 at 4° C. Ultracentrifugation was used to concentrate the CAOR solution, from the dialysis tubing. The filtrate was lyophilized and stored at 4° C. until further required. The determination of any aldehyde content was determined as described under ‘determination of CA oxidation’ (FIG. 1; step 2).

(42) 1c Reoxidation of CA

(43) After confirmation of no aldehyde content the CAOR was again oxidised as reported under activation of CA except CAOR was incubated with periodate solution for a longer time (up to 1 h). The degree of oxidation in the CAORO product was measured on lyophilized powder obtained from this stage as well (FIG. 1; step 3).

(44) 1d Determination of the Oxidation State of CA and Derivatives

(45) Qualitative estimation of the degree of colominic acid oxidation was carried out with 2,4 DNPH, which yields sparingly soluble 2,4 dinitrophenyl-hydrazones on interaction with carbonyl compounds. Non-oxidised (CA), oxidised (CAO), reduced (CAOR) and re-oxidised (CAORO) (5 mg each), were added to the 2,4-DNPH reagent (1.0 ml), the solutions were shaken and then allowed to stand at 37° C. until a crystalline precipitate was observed [Shriner et. al., 1980]. The degree (quantitative) of CA oxidation was measured with a method [Park and Johnson, 1949] based on the reduction of ferricyanide ions in alkaline solution to ferric ferrocyanide (Persian blue), which is then measured at 630 nm. In this instance, glucose was used as a standard.

(46) 1e Preparation of CA-NH.sub.2

(47) CAO at (10-100 mg/ml) was dissolved in 2 ml of deionised water with a 300-fold molar excess of NH.sub.4Cl, in a 50 ml tube and then NaCNBH.sub.4 (5 M stock in 1 N NaOH(aq), was added at a final concentration of 5 mg/ml. The mixture was incubated at room temperature for 3 days. A control reaction was also set up with colominic acid instead of CAO. Product colominic acid amine derivative was precipitated by the addition of 5 ml ice-cold ethanol. The precipitate was recovered by centrifugation at 4000 rpm, 30 minutes, room temperature in a benchtop centrifuge. The pellet was retained and resuspended in 2 ml of deionised water, then precipitated again with 5 ml of ice-cold ethanol in a 10 ml ultracentrifuge tube. The precipitate was collected by centrifugation at 30,000 rpm for 30 minutes at room temperature. The pellet was again resuspended in 2 ml of deionised water and freeze-dried.

(48) 1f Assay for Amine Content

(49) The TNBS (picrylsulphonic acid i.e. 2,4,6-tri-nitro-benzene sulphonic acid) assay was used to determine the amount of amino groups present in the product [Satake et. al., 1960]. In the well of a microtitre plate TNBS (0.5 μl of 15 mM TNBS) was added to 90 μl of 0.1 M borate buffer pH 9.5. To this was added 10 μl of a 50 mg/ml solution of CA-amide. The plate was allowed to stand for 20 minutes at room temperature before reading the absorbance at 405 nm. Glycine was used as a standard, at a concentration range of 0.1 to 1 mM. TNBS trinitrophenylates primary amine groups. The TNP adduct of the amine is detected. Testing the product purified with a double cold-ethanol precipitation using the TNBS assay showed close to 90% conversion.

(50) 1g Preparation of Maleimide Polymer (CA-M)

(51) The CAORO synthesised in Example 1c above was reacted with 5 molar equivalents of N-[β-maleimidopropionic acid] hydrazide in 0.1 M sodium acetate for 2 h at 20° C. The product hydrazone was precipitated in ethanol, resuspended in sodium acetate and precipitated again in ethanol, redissolved in water and freeze-dried. The product is useful for site-specific conjugation to the thiol groups of cysteine moieties in proteins and peptides.

(52) 1h Gel Permeation Chromatography

(53) CA samples (CA, CAO, CAOR and CAORO) were dissolved in NaNO.sub.3 (0.2M), CH.sub.3CN (10%; 5 mg/ml) and were chromatographed on over 2× GMPW.sub.XL columns with detection by refractive index (GPC system: VE1121 GPC solvent pump, VE3580 RI detector and collation with Trisec 3 software (Viscotek Europe Ltd). Samples (5 mg/ml) were filtered over 0.45 .mu.m nylon membrane and run at 0.7 cm/min with 0.2M NaNO.sub.3 and CH.sub.3CN (10%) as the mobile phase (FIG. 3).

(54) Results of Example 1

(55) Preparation of Monofunctional PSA

(56) The integrity of the internal alpha-2,8 linked Neu5Ac residues post periodate and borohydride treatment was analysed by GPC and the chromatographs obtained for the oxidised (CAO), oxidised reduced (CAOR), double oxidised (CAORO), amino CA (CA-NH2) materials were compared with that of native CA. It was found (FIG. 3) that oxidized (15 minutes) (CAO), reduced (CAOR), double oxidised (1 hr) (CAORO) and native CA exhibit almost identical elution profiles, with no evidence that the successive oxidation and reduction steps give rise to significant fragmentation of the polymer chain. The small peaks are indicative of buffer salts.

(57) The results of quantitative assay of CA intermediates in the double oxidation process using ferricyanide were consistent with the results of qualitative tests performed with 2,4 DNPH which gave a faint yellow precipitate with the native CA, and intense yellow colour with the aldehyde containing forms of the polymer, resulting in an intense yellow precipitate after ten minutes of reaction at room temperature.

(58) The amination content of the polymer was found to be 85% by the 2,4,6-tri-nitro-benzene sulphonic acid (TN BS) assay. The PSA aldehyde derivative could also be reacted with a linking compound having a hydrazide moiety and a N-maleimide moiety to form a stable hydrazone having an active maleimide functionally useful for reacting with a thiol group. The maleimide content of the polymer was found to be 95% by the maleimide assay.

Example 2

Fractionation of Colominic Acid by IEC (CA, 22.7 KDa, pd 1.34)

(59) 2.1 Fractionation at Large Scale

(60) An XK50 column (Amersham Biosciences, UK) was packed with 900 ml Sepharose Q FF (Amersham Biosciences) and equilibrated with 3 column volumes of wash buffer (20 mM triethanolamine; pH 7.4) at a flow rate of 50 ml/min. CA (25 grams in 200 ml wash buffer) was loaded on column at 50 ml per minute via a syringe port. This was followed by washing the column with 1.5 column volumes (1350 ml) of washing buffer.

(61) The bound CA was eluted with 1.5 column volumes of different elution buffers (Triethanolamine buffer, 20 mM, pH 7.4, with 0 mM to 475 mM NaCl in 25 mM NaCl steps) and finally with 1000 mM NaCl in the same buffer to remove all residual CA and other residues (if any). The flow rate was 7 ml/minute.

(62) The samples were concentrated to 20 ml by high pressure ultra filtration over a 3-10 kDa membrane (Vivascience, UK). These samples were buffer exchanged into deionised water by repeated ultra filtration at 4° C. The samples were analysed for average molecular weight and other parameters by GPC (as reported in example 1 h) and native PAGE (stained with alcian blue) [Table 1 and 2; FIG. 4, 5,6].

Example 2.2

Fractionation at Medium and Smaller Scale

(63) The following samples were fractionated using an identical wash and gradient system on a smaller scale (1-75 ml matrix; 0.2-3 gram of colominic 10 acid): CA (CA, 22.7 kDa, pd 1.34; CA, 39 KDa, pd 1.4), CAO (CAO, 22.7 kDa, pd 1.34), monofunctional CAO (RO, 22.7 kDa; pd 1.34), CA-NH.sub.2 (22.7 kDa, pd 1.34), CAM (as per example 1 g) produced were monitored throughout.

(64) Narrow fractions of CA produced using above procedure were oxidised is with 20 mM periodate and analysed by gel permeation chromatography (GPC) and native PAGE for gross alteration to the polymer (FIGS. 7, 8).

(65) Results of Example 2: Fractionation at Large, Medium and Small Scale

(66) CA and its derivatives (22.7 kDa) were successfully fractionated into 20 various narrow species with a polydispersity less than 1.1 with m.w. averages of up to 46 kDa with different % of populations (Tables 1-2 and FIGS. 4-8). Table 1 shows the results of fractionating the 22.7 kDa material at a scale of 75 ml. FIG. 7 is the GPC results and FIGS. 4-6 are native PAGEs of CA fractions.

(67) TABLE-US-00001 TABLE 1 IEC (22.7 KDa; 75 ml matrix; 3 g of CA) Elution buffers (in 20 mM Triethanolamine buffer + mM NaCl, pH 7.4) M.W. Pd % Population 325 mM 12586 1.091 77.4% 350 mM 20884 1.037 3.2% 375 mM 25542 1.014 5.0% 400 mM 28408 1.024 4.4% 425 mM * * 7.4% 450 mM 43760 1.032 2.3% 475 mM 42921 1.096 0.2% * Not done

(68) TABLE-US-00002 TABLE 2 Anion exchange chromatography of CA(22.7 KDa; pd 1.34): Large Scale (900 matrix) Sample (in 20 mM Triethanolamine buffer + mM NaCl, pH 7.4) M.W. Pd 350 mM 15490 (1.008) 10.470 (1.173) 375 mM 19960 (1.010) 24659 (1.019) 400 mM 25829 (1.019) 29573 (1.018) 425 mM 33763 (1.023) 34160 (1.011) 450 mM 46880 (1.058) 44400 (1.013) 475 mM — 28500 (1.376) 400 + 425 mM (mixed) 26418 (1.082) —

(69) This process was scalable from 1 ml to 900 ml of matrix with the fractionation profile almost identical at each scale (not all results shown).

(70) The fractionation of larger polymer (CA, 39 kDa, pd 1.4) produced species up to 90 kDa. This process can successfully be used for the fractionation of even large batches of the polymer. FIG. 8 shows the native PAGE results for the 3 CA samples as supplied and for fractions separated by ion exchange analysed as in Table 3. The PAGE results show that the ion exchange fractions are narrowly dispersed. This is consistent with the GPC data shown in FIG. 7, which shows the results for 3 of the fractions separated from the 22.7 kDa CA (Table 3).

(71) TABLE-US-00003 TABLE 3 Sample M.W. Mn PD 1 18727 15016 1.25 (original CA) 2 27677 25095 1.10 (fractionated CA) 3 40950 40279 1.02 (fractionated CA)

(72) The 22.7 kDa material is separated on a larger scale. Using GPC the fractions from ion exchange are analysed.

(73) All narrow fractions were successfully oxidised with 20 mM periodate and samples taken from different stages of the production process and analysed by GPC and native PAGE showed no change in the molecular weight and polydispersity. The data for some of the samples are shown in FIG. 8.

Example 3

Factors Affecting the Fractionation of CA

(74) The various factors affecting the fractionation of CA (e.g. washing volume etc.) were studied [FIG. 7-14].

(75) Results of Example 3: Factors Affecting the Fractionation of CA

(76) The various factors affecting the fractionation of CA were studied. The binding studies were done by loading 50, 100, 150 and 200 mg of CA on to the column (5 ml matrix). Using 200 mg of CA, more than 99% of CA was bound to the column (FIG. 9). When the column was washed with one column volume of eluting buffer, by step gradient, the polydispersity of polymer was found to be more than 1.1 (FIG. 11). The washing of the column with 1.5 column volume generated CA fractions with polydispersities less than 1.1 (FIG. 10).

(77) The amino CA (CA-NH.sub.2; FIG. 12), oxidised CA (FIG. 13) and monofunctional CA could successfully be fractionated in the fractions with polydispersity 1.1.

Example 4

Synthesis of Growth Hormone (GH) CA Conjugates (Broad and Narrow Dispersed)

(78) CAO (22.7 KDa) and narrow dispersed-CAO (27.7 kDa pd=1.09; 40.9 kDa. pd=1.02) prepared in Reference example 2 were used for the preparation of GH conjugates.

(79) Preparation of Growth Hormone—Ca Conjugates

(80) Growth hormone was dissolved in 0.15 M PBS (pH 7.4) and covalently linked to different CAs (CAO and NCAO). Different CAs (22 kDa, CAO; 27.7 kDa & 40.9 kDa, NCA) were individually added to GH (2 mg) in a CA:GH molar ratios (12.5:1), sodium cyanoborohydride was added to a final concentration of 4 mg/ml. The reaction mixtures were sealed and stirred magnetically for 24 h at 35±2° C. The mixtures were then subjected to ammonium sulphate ((NH.sub.4).sub.2SO.sub.4) precipitation by adding the salt slowly whilst continuously stirring, to achieve 70% w/v saturation, stirred for 1 h at 4° C., then spun (5000×g) for 15 min and the pellets resuspended in a saturated solution of (NH.sub.4).sub.2SO.sub.4 and spun again for 15 min (5000×g). The precipitates recovered were redissolved in 1 ml PBS pH 7.4 and dialysed extensively (24 h) at 4° C. against the same buffer. Controls included subjecting the native protein to the conjugation procedure in the presence of non-oxidised CA or in the absence of CA. Shaking was kept to a minimum to avoid concomitant denaturation of the protein. Polysialylated GH was characterised by SDS-PAGE. The polysialylated GH was passed through anion exchange chromatography and the product fractions subjected to SDS PAGE (FIG. 15).

(81) Results of Example 4: Synthesis of GH-CA Conjugates (Broad and Narrow Dispersed)

(82) The GH-CA conjugates were successfully synthesised. The results of SDS-PAGE (FIG. 15) show that in the control (with GH) migration of the sample is similar to that for fresh GH. In the conjugate lanes there are shifts in the bands which typically indicates an increase in mass indicative of a polysialylated-GH. The band width was significantly narrowed down in case of conjugates with narrow dispersed polymer in comparison to conjugates with broad dispersed polymers. Further, GH conjugates (with broad dispersed polymer) were successfully separated into different species by anion exchange chromatography (FIG. 19).

Example 5

Precipitation of CA

(83) Differential ethanol precipitation was used to precipitate different chain lengths of colominic acid [FIGS. 16, 17].

(84) Results of Example 5: Precipitation of CA

(85) The CA (22.7; pd 1.34) could not be precipitated into narrow dispersed fractions using different strengths of ethanol (FIG. 17). However, differential ethanol precipitation showed that smaller narrow CAs required more ethanol (EtOH). Broad 22.7 kDa polymer was precipitated with 70% EtOH giving a yield>80% of product polymer. A concentration of 80% EtOH was required to precipitate>80% of a lower MW 6.5 KDa (pd<1.1). This process also removes part of the salt contaminating the product.

Example 6

Fractionation of CA by Ultrafiltration

(86) Samples of 22.7 kDa were purified by ultrafiltration over different molecular weight cut off membranes (5, 10, 30, 50, and 100 kDa). In all cases retentate was examined by GPC and native PAGE [FIG. 18].

(87) Results of Example 6: Fractionation of CA by Ultrafiltration

(88) Samples of 22.7 kDa purified by ultrafiltration over different molecular weight cut off membranes showed that there was a decrease in polydispersity of the polymer and a shift towards higher molecular weight with increase in membrane cut off (FIG. 18). FIG. 16 shows fractionation of CA by anion exchange chromatography (left) and filtration (right). IEC of CA generated fractions with much narrow dispersed CAs as compared to fractionation by filtration.

Example 7

Characterization by NMR Spectroscopy

(89) The fractionated CA polymers were characterized by .sup.1H (400 MHz) and .sup.13C (100 MHz) NMR spectroscopy for impurities (if any) using D.sub.2O(FIG. 20).

(90) Results of Example 7: Characterization by NMR Spectroscopy

(91) The .sup.1H and .sup.13C NMR of narrow dispersed polymer fractionated material is free from impurities. In addition, the chemical shifts of the H-3 protons in the .sup.1H NMR and the C-2 carbon in the .sup.13C NMR spectra confirm that the polymer is indeed the expected alpha-2,8 linked sialic acid material.

Example 8

Fractionation of CA (39 kDa, pd 1.4) by IEC 8.1 Fractionation at Large Scale

(92) An XK50 column (Amersham Biosciences, UK) was packed with 900 ml Sepharose Q FF and equilibrated with 3 column volumes of wash buffer (20 mM triethanolamine; pH 7.4) at a flow rate of 50 ml/min. CA (12.5 g in 200 ml wash buffer) was loaded on column at 50 ml per minute via a syringe port. This was followed by washing the column with 1.5 column volumes (1350 ml) of washing buffer.

(93) The bound CA was eluted with 1.5 column volumes of elution buffer (triethanolamine, 20 mM, pH 7.4) containing different salt concentrations (0, 200, 250, 300, 350, 375, 400, 425, 450, 475, 500 and 525 mM NaCl) and finally with 1000 mM NaCl in the same buffer to remove all residual CA and other residues (if any).

(94) The samples were concentrated to approximately 20 ml by either high-pressure ultrafiltration over a 3 or 10 kDa membrane (Vivascience, UK) or by Vivaflow 50 diafiltration (filtration by constantly passing the sample through a membrane) having a 3 kDa mwco membrane (Vivascience, UK). These samples were buffer exchanged into deionised water by either repeated ultrafiltration or Vivaflow at 4° C. The samples were analysed for average molecular weight and other parameters by GPC (as reported in Example 2) and native PAGE (4-20% Tris-glycine gel stained with alcian blue) (FIGS. 21 and 22).

(95) 8.2 Fractionation at Small Scale

(96) CA was also fractionated on a smaller scale (200 mg of CA) using Sepharose Q FF (5 ml matrix, prepacked; Amersham Biosciences, UK) employing an identical buffer system (20 mM triethanolamine; pH 7.4) containing different salt concentrations (0, 200, 250, 300, 350, 375, 400, 425, 450, 475, 500, 525, 550 and 575 mM NaCl). The bound CA was eluted by washing the column with 1.5 column volumes (7.5 ml) at a flow rate of 1 ml/min with a final wash of the column using 1000 mM NaCl in the usual triethanolamine buffer.

(97) The samples were concentrated to approximately 0.75 ml by Vivaspin membrane filtration (mwco 3 kDa) (Vivascience, UK), buffer exchanged into deionised water by repeated membrane filtration at 8° C. and then lyophilised.

(98) The samples were analysed by native PAGE (4-20% tris-glycine gel stained with alcian blue) (FIGS. 23 and 24).

(99) Results of Example 8: Polydispersed CA (39 kDa; pd 1.4) was successfully fractionated into various narrow dispersed species with molecular weight averages ranging from 7 to 97 kDa and with different % of populations (FIGS. 21-24 and Table 4).

(100) TABLE-US-00004 TABLE 4 GPC analysis of various fractionated CA CA fraction Mw (kDa) pd 475 97.2 1.285 450 52.3 1.109 425 37.9 1.062 400 28.0 1.048 375 19.0 1.080 350* 14.5 — 300* 10.0 — 250* 7.0 — *Estimated approximate values by native PAGE

(101) In the analysis the solvent used was 0.2M NaNO.sub.3 in MECN and PEO and dextron were used as standards. The temperature was 22° C., 3 injection volume 100 μL and flow rate was 0.7 mL/mn.

(102) FIGS. 21 and 23 show the % population of CA in various fractions as a result of fractionating 39 kDa CA polymer on a large scale (12.5 g CA; 900 ml matrix) and a small scale (200 mg CA; 5 ml matrix), respectively. FIGS. 22 and 24 are the native PAGEs obtained as a result of the fractionation of CA on a large and small scale. Table 4 is the GPC results of the fractions obtained by IEC at various salt concentrations. The GPC data shows that species up to 97 kDa are generated by the fractionation process (see Example 9 for further details). These larger molecular weight polymers have been shown to have a greater percentage phosphate moiety present on the reducing end of CA compared to their lower molecular weight counterparts by a phosphate assay, which tests for the presence of inorganic phosphate (Rouser et. al. 1970).

Example 9

Characterisation of Fractionated CA by GPC

(103) Freshly prepared CA samples, by dissolving for example either CA, CAO, CAOR or CAORO (4-5 mg/ml) in 0.2 M NaNO.sub.3/0.1% NaN.sub.3/10% acetonitrile (1 ml) (or alternatively 10 mM PBS, pH 7.4) and then filtering the resulting solution over 0.2 μm nylon membrane (Whattman, UK), were analysed by GPC.

(104) Samples were chromatographed with 2× GMPWxI (250×4.6 mm) columns employing a triple detection GPC (SEC.sup.3) system (Viscotek Europe Ltd, UK). Detectors consisted of a Viscotek Laser Refractometer (refractive index) and a Viscotek 270 Dual Detector (right-angle light scattering detector configured with a 4-capillary viscometer detector) collated with an OmniSEC 3.1 workstation (Viscotek Europe Ltd).

(105) The analysis conditions used were; eluent: buffer employed to dissolve the CA sample; flow rate: 0.7 ml/min; sample loading: 100 μl; temperature: 22° C. The system was calibrated with narrow molecular weight polyethylene glycol and broad molecular weight Dextran reference materials.

(106) The time it takes for a polymer to be eluted from the GPC column is converted to its molecular weight using various detectors. The light scattering detector provides a direct measurement of absolute molecular weight and eliminates the need for column calibration (detector gives a proportional response to molecular weight and concentration). The radius of gyration is not calculated when measurements are performed using a single angle. The viscometer provides a direct measurement of intrinsic viscosity and allows for the determination of molecular size, conformation and structure (detector gives an inversely proportional response to molecular density). The response from the refractive index detector is proportional to the concentration of polymer: the constant of proportionality is dn/dc (the same specific refractive index increment needed in light scattering).

(107) The GPC system described above enables a number of parameters of CA to be determined. For instance, the number average molecular weight (Mn) and the weight average molecular weight (Mw) can be obtained and from these numbers the polydispersity of CA can be calculated. Other information acquired from the GPC data include the percentage recovery of CA and the degree of branching (if any) on the polymer. The exact concentration of the sample can also be determined from the dn/dc value (or alternatively the dn/dc value can be calculated from the exact known concentration of the polymer).

(108) Results of Example 9: Table 5 shows typical data for a range of parameters that was obtained from the analysis of a CA fraction (400 mM NaCl in 20 mM triethanolamine, pH 7.4) from IEC fractionation of CA (39 kDa, pd 1.4). In this table, the following definitions apply: Mn=number average molecular weight Mw=weight average molecular weight Mz=Z-average molecular weight Mp=peak average molecular weight Mv=viscosity average molecular weight Mw/Mn=molecular weight distribution (polydispersity) Rh=hydrodynamic radius IV=intrinsic viscosity dn/dc=change in refractive index with concentration for the sample

(109) TABLE-US-00005 TABLE 5 Typical GPC data of the CA fraction (400 mM NaCl in 20 mM triethanolamine, pH 7.4) from IEC Parameters Values Mn (Da) 26,666 Mw (Da) 27,956 Mz (Da) 31,129 Mp (Da) 22,969 Mw/Mn 1.048 IV (dl/g) 0.2395 Rh (nm) 4.683 Branches 0.00 Sample Conc (mg/ml) 5.600 Sample Recovery (%) 90.71 dn/dc (ml/g) 0.156 dA/dc (ml/g) 0.000 Mark-Houwink a −0.048 Mark-Houwink logK −0.425

(110) For example, 27,956 and 26,666 Da were the values for Mw and Mn, respectively, which gave a polydispersity of 1.048. Table 4 shows the range of narrow dispersed molecular weights obtained by GPC analysis on the fractionation of polydispersed CA (39 kDa; pd 1.4) with IEC, while FIG. 25 shows a typical GPC chromatogram for the combined viscometer, refratometer and light scattering curves obtained for a narrow dispersed CA sample.

Example 10

Optimisation Studies

(111) 10.1 Optimisation of the Analysis of CA by Native PAGE

(112) Fractionated and the non-fractionated CA have been analysed further by TBE and Tris-glycine gels on native PAGE in order to optimise the resolution of these polymers on the gel. In general, 40 ig of either narrow or broad dispersed CA was loaded, as a 20 il solution containing 10 il of loading buffer, per well on the gel. The gel was run at three different speeds (150, 25 or 15 mV/cm) and then stained with alican blue, followed by destaining with 2% acetic acid.

(113) Results of Example 10.1: FIG. 26 demonstrates the various resolutions that can be obtained for different molecular weights of CA with 4-20% Tris-glycine, 4-20% and 20% TBE gels. From the gels it can be observed that good separation of high and low molecular weight CAs can be observed with 4-20 and 20% TBE gels, with particularly good resolution with the 20% TBE gel. Narrow bands are best observed when the gel is run at 25 or 15 mV/cm compared to when the gel speed is 150 mV/cm.

(114) 10.2 Concentration of CA

(115) The filtrates of high-pressure ultrafiltration obtained from IEC fractionation of CA (22.7 kDa, pd 1.34) were concentrated by Vivaflow (mwco 3 kDa). These CA samples were analysed with the corresponding filters of the high-pressure ultrafiltration by native-PAGE using a 4-20% TBE gel (FIG. 27) for any degradation of the polymer.

(116) Results of Example 10.2: Results from the native PAGE (FIG. 27) of the CA samples obtained by Vivaflow purification of the filtrates show that both materials had the same molecular weight. This observation of the presence of CA in the filtrates of high-pressure ultrafiltration maybe accounted for by a process known as reptation, whereby due to the flexibility, deformability and its rod-like conformation of the CA polymer, the polymer can pass through the membrane resulting in the presence of CA in the filtrates. The gel also demonstrates that both Vivaflow and ultrafiltration can be successfully employed to process the fractions obtained by IEC fractionation of CA.

Example 11

Fractionation of CA (22.7 kDa, pd1.34) by IEC Using Increasing Ionic Strength of Triethanolamine/HCl

(117) Polydispersed CA was also fractionated by Sepharose Q FF (1 ml matrix, prepacked) using a range of triethanolamine concentrations at pH 7.4 in the absence of any salt such as NaCl. Thus, CA (40 mg; 1 ml) (22.7 kDa; pd 1.34) was loaded on to a Q FF column (1 ml matrix; prepacked; Amersham Biosciences). The bound CA was eluted by passing 1 ml of each triethanolamine buffer (50, 100, 200, 300, 400, 500, 600, 700, 800, 900, 1000, 1100 and 1200 mM triethanolamine) through the column at a flow rate of 1 ml/min with a final wash of the column using 200 mM triethanolamine. The samples were directly lyophilised and then analysed by native PAGE (TBE gel stained with alcian blue).

(118) Results of Example 11: FIG. 8 demonstrates that fractionation of CA can be achieved in the presence of a varying concentration of triethanolamine at pH 7.4.

Example 12

Fractionation of CA (22.7 kDa, pd 1.34) by IEC Using Increasing Ionic Strength of Triethanolamine Acetate

(119) Polydispersed CA was also fractionated by Sepharose Q FF (1 ml matrix, prepacked) using a range of triethanolamine acetate concentrations at pH 7.4 in the absence of any salt such as NaCl. The triethanolamine acetate buffer was prepared using triethanolamine and adjusting the pH to 7.4 using acetic acid. Polydispersed CA (40 mg; 1 ml) (22.7 kDa; pd 1.34) was loaded on to a Q FF column (1 ml matrix; prepacked). The bound CA was eluted by passing 1 ml of each triethanolamine acetate buffer (300, 400, 500, 600, 700, 800, 900, 1000, 1100, 1200, 1300, 1400 and 1500 mM triethanolamine acetate) through the column at a flow rate of 1 ml/min with a final wash of the column using 200 mM triethanolamine acetate. A small sample of each fraction (20 .mu.l) was then buffer exchanged with water using a micro membrane dialysis system, lyophilised and then analysed by native PAGE (20% TBE gel stained with alcian blue).

(120) Results of Example 12: FIG. 29 demonstrates that fractionation of CA can be successfully achieved in the presence of a varying concentration of triethanolamine at pH 7.4.

Example 13

Fractionation of CA (22.7 kDa, pd 1.34) Using a pH Gradient

(121) HEPES and ethanolamine buffer system was used to create a pH step gradient. Buffers at pH 7.6, 7.8 and 8.0 were set up using increasing concentrations of HEPES from 10 to 50 mM and setting the pH to the appropriate value with NaOH. The concentration of sodium ions did not exceed 36 mM. Buffers at pH 8.2, 8.3, 8.5, 8.7, 8.9, 9.1, 9.3, 9.5 and 9.7 were created by mixing appropriate amounts of 1M ethanolamine (20 to 70 mM final concentration) with HEPES 50 mM (10 to 50 mM final concentration) and setting the pH with NaOH, making sure that the sodium ion concentration did not exceed 30 mM. The final buffer was a 70 mM ethanolamine pH 11.

(122) 30 mg of polydispersed CA (22.7 kDa; pd 1.34) was dissolved in pH 7.6 buffer (1 mL) and loaded onto a DEAE sepharose column (1 ml matrix, prepacked) also with the pH 7.6 buffer. The column was washed with 5 ml of the pH 7.6 buffer (flow rate 1 ml/min) followed by passing 2 ml of each buffer through the column, collecting 1 ml fractions. 500 il of each eluted fraction was lyophilised and then re-dissolved in 50 il of deionized water for analysis by native PAGE (20% TBE gel stained with alcian blue).

(123) Results of Example 12: FIG. 30 demonstrates that fractionation of CA can be successfully achieved in the presence of an increasing pH strength. DEAE sepharose is an anion exchange matrix with a tertiary amino group, N-diethyl-amino-ethyl, which looses its charge at high pH. Thus, high pH is used to deprotonate the matrix, change its charge and elute any species bound by ionic interactions on the column. A mixed gradient can also be used where a pH gradient is first used to fractionate the low molecular weight species followed by an ionic strength gradient to elute the higher m.w. species.

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