Method for in-vitro preparation of double-layered virus-like particles of rotavirus
09862933 ยท 2018-01-09
Assignee
Inventors
- Shengxiang Ge (Xiamen, CN)
- Tingdong LI (Xiamen, CN)
- Qingshun Guo (Xiamen, CN)
- Feihai Xu (Xiamen, CN)
- Jun Zhang (Xiamen, CN)
- Ningshao Xia (Xiamen, CN)
Cpc classification
C12N7/00
CHEMISTRY; METALLURGY
C12N2720/12322
CHEMISTRY; METALLURGY
C12N2720/12334
CHEMISTRY; METALLURGY
A61K39/00
HUMAN NECESSITIES
C12N2720/12333
CHEMISTRY; METALLURGY
C12N7/04
CHEMISTRY; METALLURGY
International classification
C12N7/04
CHEMISTRY; METALLURGY
A61K38/16
HUMAN NECESSITIES
Abstract
The invention relates to a method for preparing double-layered virus-like particles of rotavirus in vitro. The method comprises the following steps: purifying rotavirus VP6 proteins from a lysis supernatant, and in vitro assembling double-layered virus-like particles consisting of VP2 proteins and VP6 proteins, wherein the proteins and the virus-like particles can be used for preventing or reducing the clinical symptoms caused by rotavirus infection.
Claims
1. A method for preparing a double-layered virus-like particle of rotavirus comprising rotavirus VP2 protein and VP6 protein, the method comprising the following steps of: a) expressing VP6 in a soluble form in a prokaryotic expression system, and purifying the VP6, wherein the purified VP6 protein retains its native conformation and is present in a form of trimer; and b) co-assembling the purified VP6 with VP2 extracellularly, and with VP2 in a non-particulate state, to form a double-layered particle 2/6-VLP.
2. The method according to claim 1, wherein the VP6 protein is prepared by the following steps of: 1) expressing a rotavirus VP6 protein in E. coli; 2) to lysis supernatant comprising the VP6 protein, adding polyethylene imine (PEI) or an analog thereof, or a divalent or trivalent metal ion, to precipitate nucleic acids and some undesired proteins, wherein the concentration of PEI is between 0.05% and 0.2%, the metal ion includes Mn.sup.2+, Mg.sup.2+, Ca.sup.2+, Zn.sup.2+ and Al.sup.3+, when used, the concentration of Ca.sup.2+ is between 10 and 80 mM; 3) performing centrifugation, and subjecting the lysis supernatant to salting-out and chromatographic purification.
3. The method according to claim 2, wherein the salting-out is performed using saturated ammonium sulfate.
4. The method according to claim 3, wherein the assembly of the double-layered virus-like particle 2/6-VLP comprises, mixing VP6 and VP2 proteins, then replacing the buffer with an assembly buffer to form a double-layered virus-like particle, wherein: a) VP2 and VP6 are purified proteins which are not assembled into particles and have a purity of above 95%; b) the assembly buffer is a phosphate buffer, a MES buffer or a citrate buffer, with a pH of between 3.0 and 7.0; c) the assembly buffer contains 0-2M NaCl; and d) the ratio of VP2 and VP6 by mass is between 1:1 and 1:10.
5. The method according to claim 4, wherein the assembly of the double-layered virus-like particle 2/6-VLP comprises, mixing VP6 and VP2 proteins, then replacing the buffer with an assembly buffer to form a double-layered virus-like particle, wherein: a) VP2 and VP6 are purified proteins which are not assembled into particles and have a purity of above 95%; b) the assembly buffer is a phosphate buffer, a MES buffer or a citrate buffer, with a pH of between pH 4.0 and pH 6.4; c) the assembly buffer contains 150 mM-2 M NaCl; and d) the ratio of VP2 and VP6 by mass is between 1:2 and 1:3.
6. The method according to claim 1, wherein the VP2 protein is VP2 protein in a non-particulate state prepared by the following steps: 1) expressing rotavirus VP2 protein in E. coli; 2) adding polyethyleneimine (PEI) to lysis supernatant containing the VP2 protein, wherein the concentration of PEI is between 0.05% and 1%; 3) performing centrifugation, and purifying the lysis supernatant by salting-out and chromatography.
7. The method according to claim 6, wherein the salting-out is performed using ammonium sulfate.
8. The method according to claim 7, wherein the assembly of the double-layered virus-like particle 2/6-VLP comprises, mixing VP6 and VP2 proteins, then replacing the buffer with an assembly buffer to form a double-layered virus-like particle, wherein: a) VP2 and VP6 are purified proteins which are not assembled into particles and have a purity of above 95%; b) the assembly buffer is a phosphate buffer, a MES buffer or a citrate buffer, with a pH of between 3.0 and 7.0; c) the assembly buffer contains 0-2M NaCl; and d) the ratio of VP2 and VP6 by mass is between 1:1 and 1:10.
9. The method according to claim 8, wherein the assembly of the double-layered virus-like particle 2/6-VLP comprises, mixing VP6 and VP2 proteins, then replacing the buffer with an assembly buffer to form a double-layered virus-like particle, wherein: a) VP2 and VP6 are purified proteins which are not assembled into particles and have a purity of above 95%; b) the assembly buffer is a phosphate buffer, a MES buffer or a citrate buffer, with a pH of between pH 4.0 and pH 6.4; c) the assembly buffer contains 150 mM-2 M NaCl; and d) the ratio of VP2 and VP6 by mass is between 1:2 and 1:3.
10. The method according to claim 1, wherein the assembly of the double-layered virus-like particle 2/6-VLP comprises, mixing VP6 and VP2 proteins, then replacing the buffer with an assembly buffer to form a double-layered virus-like particle, wherein: a) VP2 and VP6 are purified proteins which are not assembled into particles and have a purity of above 95%; b) the assembly buffer is a phosphate buffer, a MES buffer or a citrate buffer, with a pH of between 3.0 and 7.0; c) the assembly buffer contains 0-2M NaCl; and d) the ratio of VP2 and VP6 by mass is between 1:1 and 1:10.
11. The method according to claim 10, wherein the assembly of the double-layered virus-like particle 2/6-VLP comprises, mixing VP6 and VP2 proteins, then replacing the buffer with an assembly buffer to form a double-layered virus-like particle, wherein: a) VP2 and VP6 are purified proteins which are not assembled into particles and have a purity of above 95%; b) the assembly buffer is a phosphate buffer, a MES buffer or a citrate buffer, with a pH of between pH 4.0 and pH 6.4; c) the assembly buffer contains 150 mM-2 M NaCl; and d) the ratio of VP2 and VP6 by mass is between 1:2 and 1:3.
12. The method according to claim 2, wherein the chromatography includes hydrophobic interaction chromatography and ion exchange chromatography.
13. The method according to claim 12, wherein the assembly of the double-layered virus-like particle 2/6-VLP comprises, mixing VP6 and VP2 proteins, then replacing the buffer with an assembly buffer to form a double-layered virus-like particle, wherein: a) VP2 and VP6 are purified proteins which are not assembled into particles and have a purity of above 95%; b) the assembly buffer is a phosphate buffer, a MES buffer or a citrate buffer, with a pH of between 3.0 and 7.0; c) the assembly buffer contains 0-2M NaCl; and d) the ratio of VP2 and VP6 by mass is between 1:1 and 1:10.
14. The method according to claim 13, wherein the assembly of the double-layered virus-like particle 2/6-VLP comprises, mixing VP6 and VP2 proteins, then replacing the buffer with an assembly buffer to form a double-layered virus-like particle, wherein: a) VP2 and VP6 are purified proteins which are not assembled into particles and have a purity of above 95%; b) the assembly buffer is a phosphate buffer, a MES buffer or a citrate buffer, with a pH of between pH 4.0 and pH 6.4; c) the assembly buffer contains 150 mM-2 M NaCl; and d) the ratio of VP2 and VP6 by mass is between 1:2 and 1:3.
15. The method according to claim 12, wherein the chromatography is chromatography by Phenyl HP (GE) under the condition of 3M NaCl, wherein nucleic acids pass through the column, VP6 protein is eluted under the condition of 2M NaCl, and the undesired protein is eluted under the condition of no salts.
16. The method according to claim 2, wherein the assembly of the double-layered virus-like particle 2/6-VLP comprises, mixing VP6 and VP2 proteins, then replacing the buffer with an assembly buffer to form a double-layered virus-like particle, wherein: a) VP2 and VP6 are purified proteins which are not assembled into particles and have a purity of above 95%; b) the assembly buffer is a phosphate buffer, a MES buffer or a citrate buffer, with a pH of between 3.0 and 7.0; c) the assembly buffer contains 0-2M NaCl; and d) the ratio of VP2 and VP6 by mass is between 1:1 and 1:10.
17. The method according to claim 16, wherein the assembly of the double-layered virus-like particle 2/6-VLP comprises, mixing VP6 and VP2 proteins, then replacing the buffer with an assembly buffer to form a double-layered virus-like particle, wherein: a) VP2 and VP6 are purified proteins which are not assembled into particles and have a purity of above 95%; b) the assembly buffer is a phosphate buffer, a MES buffer or a citrate buffer, with a pH of between pH 4.0 and pH 6.4; c) the assembly buffer contains 150 mM-2 M NaCl; and d) the ratio of VP2 and VP6 by mass is between 1:2 and 1:3.
18. The method according to claim 2, wherein the concentration of PEI is 0.1% and the metal ion is Ca.sup.2+ with a concentration of 20 mM.
19. The method according to claim 6, wherein the chromatography includes ion exchange chromatography and hydrophobic interaction chromatography.
20. The method according to claim 19, wherein the assembly of the double-layered virus-like particle 2/6-VLP comprises, mixing VP6 and VP2 proteins, then replacing the buffer with an assembly buffer to form a double-layered virus-like particle, wherein: a) VP2 and VP6 are purified proteins which are not assembled into particles and have a purity of above 95%; b) the assembly buffer is a phosphate buffer, a MES buffer or a citrate buffer, with a pH of between 3.0 and 7.0; c) the assembly buffer contains 0-2M NaCl; and d) the ratio of VP2 and VP6 by mass is between 1:1 and 1:10.
21. The method according to claim 20, wherein the assembly of the double-layered virus-like particle 2/6-VLP comprises, mixing VP6 and VP2 proteins, then replacing the buffer with an assembly buffer to form a double-layered virus-like particle, wherein: a) VP2 and VP6 are purified proteins which are not assembled into particles and have a purity of above 95%; b) the assembly buffer is a phosphate buffer, a MES buffer or a citrate buffer, with a pH of between pH4.0 and pH6.4; c) the assembly buffer contains 150 mM-2 M NaCl; and d) the ratio of VP2 and VP6 by mass is between 1:2 and 1:3.
22. The method according to claim 19, wherein the chromatography is chromatography by SP FF (GE) under the condition of Tris-HCl (pH 8.0), wherein nucleic acids and some undesired proteins pass through the column or are eluted under the condition of 150 mM NaCl, and VP2 protein is eluted under the condition of 500 mM NaCl.
23. The method according to claim 6, wherein the assembly of the double-layered virus-like particle 2/6-VLP comprises, mixing VP6 and VP2 proteins, then replacing the buffer with an assembly buffer to form a double-layered virus-like particle, wherein: a) VP2 and VP6 are purified proteins which are not assembled into particles and have a purity of above 95%; b) the assembly buffer is a phosphate buffer, a MES buffer or a citrate buffer, with a pH of between 3.0 and 7.0; c) the assembly buffer contains 0-2M NaCl; and d) the ratio of VP2 and VP6 by mass is between 1:1 and 1:10.
24. The method according to claim 23, wherein the assembly of the double-layered virus-like particle 2/6-VLP comprises, mixing VP6 and VP2 proteins, then replacing the buffer with an assembly buffer to form a double-layered virus-like particle, wherein: a) VP2 and VP6 are purified proteins which are not assembled into particles and have a purity of above 95%; b) the assembly buffer is a phosphate buffer, a MES buffer or a citrate buffer, with a pH of between pH 4.0 and pH 6.4; c) the assembly buffer contains 150 mM-2 M NaCl; and d) the ratio of VP2 and VP6 by mass is between 1:2 and 1:3.
Description
DESCRIPTION OF THE DRAWINGS
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SEQUENCE INFORMATION
(14) The information of sequences as involved in the invention is provided in the following Table 1.
(15) TABLE-US-00001 TABLE 1 Primer list Primer name Primer sequence VP6-DF GCTTTWAAACGAAGTCTTC VP6-DR GGTCACATCCTCTCACTA VP6-1F GGATCCCAT ATGGATGTCCTTTATTCTT VP6-397R AAGCTT TCATTTAATAAGCATGCT
(16) The invention is further illustrated by combining the following Examples. These Examples should not be construed as limiting the invention.
SPECIFIC MODES FOR CARRYING OUT THE INVENTION
(17) The present invention is further illustrated in detail by reference to the examples as follows. It is understood by those skilled in the art that the examples are used only for the purpose of illustrating the present invention, rather than limiting the protection scope of the present invention. When the conditions are not indicated in the Examples, the Examples are carried out under the conventional conditions or the conditions recommended by the manufacturers. The reagents and instruments used in the present invention, the manufacturers of which are not indicated, are the conventional products that are commercially available.
Example 1: Expression and Purification of VP6 in E. coli
(18) Preparation of VP6 Gene as a Template
(19) Rotavirus strain (BEIJING WANTAI BIO-PHARMACEUTICAL CO., LTD.) was extracted with Trizol agent to get its genomic RNA. VP6-DR was used as a primer, and MMLV reverse transcriptase was used for reverse transcription. The reverse transcription was carried out at 55? C. in the following system for 30 min to get VP6 cDNA.
(20) TABLE-US-00002 RNA template dNTP VP6-DR ddH2O 5 ? buffer MML RNAsin 5 ul 1 ul 0.6 ul 8.2 ul 4 ul 1 ul 0.2 ul
(21) The cDNA obtained in the previous step was used as a template, VP6-DF was used as a forward primer, and VP6-DR was used as a reverse primer. The PCR reaction was performed to amplify VP6 gene in a PCR thermocycler (Biometra T3) under the following conditions.
(22) TABLE-US-00003 94? C. denaturation for 5 min 1 cycle 94? C. denaturation for 30 s 56? C. annealing for 30 s 35 cycles.sup. 72? C. elongation for 90 s 72? C. elongation for 10 min 1 cycle
(23) The PCR products of about 1.3 kb in length were obtained after amplification. Upon extraction with a gel extraction kit, the PCR products were ligated into the commercially available pMD 18-T vector (Takara), and were transformed into E. coli DH5?. The plasmids were extracted. After digestion with PstI/EcoR I, it was identified that positive clones containing VP6 genes, designated as PMD18-T-VP6F, were obtained.
(24) M13F and M13R primers (Shanghai Boya Bio Co.) were used for sequencing. The results showed that the gene had an identity of above 90% to the corresponding gene of Rotavirus A.
(25) Construction of a Non-Fusion Expression Vector Expressing VP6 Protein
(26) The PMD18-T-VP6F obtained in the previous step was used as the template, VP6-1F was used as a forward primer, at the 5 terminal of which BamH I/Nde I enzyme cleavage site was introduced, and VP6-397R was used as a reverse primer, at the 5 terminal of which Hind III enzyme cleavage site was introduced. The PCR reaction was performed in a PCR thermocycler (Biometra T3) under the following conditions.
(27) TABLE-US-00004 94? C. denaturation for 5 min 1 cycle 94? C. denaturation for 30 s 56? C. annealing for 30 s 15 cycles.sup. 72? C. elongation for 90 s 72? C. elongation for 10 min 1 cycle
(28) The DNA fragments of about 1.2 kb in length were obtained after amplification. The fragments were ligated into the commercially available pMD 18-T vector, and were transformed into E. coli DH5?. The plasmids were extracted. After digestion with NdeI/Hind III enzyme, it was identified that positive clones containing VP6 genes, designated as PMD18-T-VP6, were obtained.
(29) M13F and M13R primers (Shanghai Boya Bio Co.) were used for sequencing. The results show that the nucleotide sequence of the fragment of interest, which was inserted into PMD18-T-VP6, is 100% homologous to the sequence inserted into PMD18-T-VP6F.
(30) The VP6 gene fragment was obtained by Nde I/Hind III enzymatic digestion of said PMD18-T-VP6 plasmid. The fragment was ligated into the prokaryotic expression vector Pet30a (Novagen) digested with Nde I/Hind III enzyme, and was transformed into E. coli DH5?. The plasmids were extracted. After digestion with NdeI/Hind III enzyme, it was identified that the plasmid P-VP6 having VP6 gene inserted was obtained.
(31) Expression of VP6 Protein in E. coli
(32) 1 ?L of the plasmid P-VP6 was used to transform E. coli BL21 (DE3). Single colonies were transferred to 4 ml liquid LB media containing kanamycin and were cultured at 37? C. with shaking until OD600 reached about 0.6. 0.5 ml bacterial solution was added to glycerol (a final concentration of 10%) and stored at ?20? C. or ?80? C. The remaining bacteria were added with IPTG to a concentration of 0.8 mM, and were further cultured at 37? C. for 2-4 h. Then, 1.5 mL bacteria were collected and were added with 100 uL ddH.sub.2O to re-suspend the bacteria. 20 uL 6?Loading Buffer was added, mixed thoroughly, and was placed in a water-bath at 100? C. for 10 min. As identified by 10% SDS-PAGE, a protein band of about 45 KDa in size was clearly observed.
(33) The bacteria carrying the recombinant plasmid P-VP6 obtained in the previous step were taken out from ?80? C. refrigerator, were thawed, and then 5 ?L were seeded in 50 mL LB medium containing kanamycin and incubated at 200 rpm and 37? C. overnight. The resultant solution was used as a seed solution. The seed solution was transferred to 15 flasks at a ratio of 1:1000, each of the flasks contained 500 mL Auto-Induction Medium (containing 10 g peptone, 5 g yeast powder, 10 g NaCl, 0.5 g glucose, 5 mL glycerol and 5 g ?-lactose per liter, the pH of which was adjusted to neutral with NaOH solution), and was incubated in a shaking incubator at 180 rpm and 37? C. until the OD600 reached about 0.6. The temperature was then adjusted to 20? C., the bacteria were collected by centrifugation 20 h later, to get about 30 g bacteria expressing VP6 protein.
(34) Preparation of VP6 Protein with a Purity of about 85%
(35) Bacteria were re-suspended at a proportion of 1 g bacteria corresponding to 15 ml lysis solution. Bacteria were disrupted by ultrasonication in an ice-water bath, for 4 min per 1 g bacteria, with a 4 s-interval every 2 s. The resultant solution was centrifuged at 13,000 rpm using JA-14 rotor for 15 min, and the supernatant was retained. The supernatant was subjected to 10% SDS-PAGE. At this stage, the VP6 protein in the supernatant had a purity of about 10% (as shown in
(36) The lysis supernatant was subpackaged into 1 ml per tube. To each tube, 0.05%-0.5% polyethyleneimine (PEI) or 10-100 mM MnCl.sub.2, MgCl.sub.2 or CaCl.sub.2 was added, and the mixture was homogeneously mixed. Centrifugation was performed 30 min later, the supernatant was taken, and saturated ammonia sulfate was added to a concentration of 40%. After homogeneous mixing, standing for 0.5-2 h, and centrifugation, the supernatant was discarded. The precipitate was re-dissolved in 1/5 volume of buffer, and it was found by 10% SDS-PAGE that PEI or metal ion precipitation could remove a lot of nucleic acids and undesired proteins; after further purification and concentration posterior to ammonia sulfate precipitation, the purity of VP6 protein was greatly improved, wherein the purity was best improved at 20 mM CaCl.sub.2 (as shown in
(37) In an ice-water bath, to the solution of disrupted bacteria, 2M CaCl.sub.2 solution was added under stirring to a final concentration of 20 mM. 30 min later, the resultant solution was centrifuged at 13,000 rpm using JA-14 rotor for 15 min, and the supernatant was retained. In an ice-water bath, solid ammonia sulfate was added under stirring to a saturation of 25%. The resultant mixture was placed in an ice-water bath for 1-2 h, and then was centrifuged at 13,000 rpm using JA-14 rotor for 15 min. The precipitate was kept and was re-suspended in 1/10 volume of 50 mM Tris-HCl buffer pH7.0+3M NaCl. The resultant mixture was centrifuged at 13,000 rpm using JA-14 rotor for 15 min, and the supernatant was kept. It was found by 10% SDS-PAGE that CaCl.sub.2 precipitation could remove a lot of nucleic acids and undesired proteins, after further purification and concentration posterior to ammonia sulfate precipitation, the purity of VP6 protein was increased from 10% to about 85% (as shown in
(38) Chromatographic Purification of VP6 Protein
(39) Hydrophobic Interaction Chromatography
(40) Equipment: AKTA Purifier UPC-100 preparative liquid chromatography system produced by GE Healthcare (i.e. the original Amershan Pharmacia Co.)
(41) Chromatographic media: Phenyl Sepharose 6B High Performance (GE Healthcare Co.)
(42) Column Volume: 5.5 cm?20 cm
(43) Buffer: 50 mM Tris-HCl, pH7.0,
(44) 50 mM Tris-HCl, pH7.0+4M NaCl
(45) Flow Rate: 8 mL/min
(46) Detector Wavelength: 280 nm
(47) Sample: VP6 protein solution in Example 1, which had a purity of about 85% and was filtered through a filter membrane with an aperture of 0.22 ?m.
(48) Elution protocol: eluting the protein of interest with 2M NaCl, eluting the undesired proteins with 50 mM Tris-HCl, pH7.0, collecting the eluate eluted with 2M NaCl, with a purity of about 98% as identified by 10% SDS-PAGE and Coomassie brilliant blue staining (as shown in
Example 2: Expression and Purification of VP2 Protein in E. coli
(49) P-VP2 plasmid was constructed by the applicant (Xiamen University, Li Tingdong, Prokaryotic expression of rotavirus structure protein and in vitro assembly of virus-like particles, 2009), and the expression strain was B121 (DE3). B121(DE3) was transformed with the P-VP2 plasmid, single colonies were picked and transferred to LB medium comprising kanamycin, and were cultured at 37? C. until OD600 reached about 0.6. 0.5 mL bacterial solution was added with glycerol to a final concentration of 10%, and was stored at ?80? C. The bacteria carrying the plasmid P-VP2 in glycerol were taken out from ?80? C. refrigerator, were thawed, and then were seeded in 50 mL LB medium comprising kanamycin and incubated under shaking at 37? C. overnight. The resultant solution was seeded and cultured in 500 mL LB medium comprising kanamycin until OD600 reached about 0.6. The temperature of the shaking table was adjusted to 25? C. Then the cultures were induced by adding 0.8 mM IPTG, and were further cultured for 6 h. The bacteria were collected.
(50) The bacteria were re-suspended at a proportion of 1 g bacteria corresponding to 15 ml TB8.0+150 mM NaCl+0.5 mM EDTA. Bacteria were lysed by ultrasonication, and were centrifuged. The supernatant was collected. PEI was added to a final concentration of 0.25% under stirring. 30 min later, centrifugation was performed and the supernatant was collected. In an ice-water bath, saturated ammonia sulfate was added to a final concentration of 30%; stirring was performed for 1-2 h. After centrifugation, the precipitate was taken and was re-suspended in 1/10 volume of 50 mM Tris-HCl, pH8.0, and then was centrifuged. After centrifugation, the supernatant was taken. At this stage the VP2 had a purity of above 80% (as shown in
(51) Cation Exchange Chromatography
(52) Equipment: AKTA Purifier UPC-100 preparative liquid chromatography system produced by GE Healthcare (i.e. the original Amershan Pharmacia Co.)
(53) Chromatographic Media: SP Sepharose Fast Flow (GE Healthcare Co.)
(54) Column Volume: 5.5 cm?20 cm
(55) Buffer: 50 mM Tris-HCl, pH8.0,
(56) 50 mM Tris-HCl, pH8.0+2M NaCl
(57) Flow Rate: 10 mL/min
(58) Detector Wavelength: 280 nm
(59) Sample: VP2 protein solution in the last step, which had a purity of about 80%, and was filtered through a filter membrane with an aperture of 0.22 ?m.
(60) Elution protocol: eluting the undesired proteins with 150 mM NaCl, eluting the VP2 protein with 500 mM NaCl, collecting the eluate eluted with 500 mM NaCl, with a purity of about 95% as identified by 10% SDS-PAGE and Coomassie brilliant blue staining (as shown in
Example 3: Identification of Rotavirus VP6 and VP2 Protein
(61) The samples were the VP6 protein with a purity of above 98% obtained in Example 1 and VP2 protein with a purity of above 95% obtained in Example 2.
(62) SDS-PAGE
(63) The samples were treated in the following four manners, respectively: 1) the loading buffer comprising mercaptoethanol was used, and the samples were treated in a water bath at 100? C. for 10 min; 2) the loading buffer comprising mercaptoethanol was used; 3) the loading buffer free of mercaptoethanol was used, and the samples were treated in a water bath at 100? C. for 10 min; 4) the loading buffer free of mercaptoethanol was used. After separation by 10% SDS-PAGE, the protein was identified by coomassie brilliant blue staining. The SDS-PAGE results showed that the purified VP2 protein was present in a form of monomer or in a form of hydrophobic polymer, but the conformation was affected by disulfide bond, and VP6 was present in a form of polymer.
(64) Size Exclusion Chromatographic Analysis
(65) Equipment: AKTA Purifier UPC-100 preparative liquid chromatography system produced by GE Healthcare
(66) Chromatographic column: Superdex200, 10 mm?300 mm (GE Healthcare), with a column volume of 24 mL
(67) Buffer: Tris-HCl, pH8.0+500 mM NaCl for VP2; Tris-HCl, pH7.0+2M NaCl for VP6
(68) Flow Rate: 0.5 mL/min
(69) Detector Wavelength: UV.sub.280 nm
(70) The results showed that the purified VP2 protein and VP6 protein each were a single component, and had a retention time of 27.34 and 33.91 min, respectively, and were homogenous.
(71) Analytic Ultracentrifugation
(72) The equipment was Beckman XL-A analytical ultracentrifuger, and the methods were sedimentation velocity method and sedimentation equilibrium method. Firstly, the sedimentation coefficients of VP2 protein and VP6 protein were analyzed by sedimentation velocity method, SEDIFIT software was used to carry out C(S) analysis, and the molecular weights of VP2 protein and VP6 protein were calculated primarily. The results showed that VP2 protein and VP6 protein might be present in a form of dimer and trimer, respectively. On the basis of this, the precise molecular weights of VP2 protein and VP6 protein were further analyzed by sedimentation equilibrium method. Origin Nonlin software and SEDPHAT software were used to analyze SE. The results showed that VP2 protein and VP6 protein had a molecular weight of 204?5.6 KDa and 114.9?1.6 KDa, respectively (
(73) VP2 protein of native state is present in a form of dimer, and VP6 protein is present in a form of trimer, and their theoretic molecular weights are 205 KDa and 135 KDa, respectively. It was identified by analytic ultracentrifugation that the purified VP2 protein had a molecular weight of 204?5.6 KDa, which was consistent with the theoretic molecular weight. However, since SDS can interrupt hydrogen bond and hydrophobic interaction, VP2 in SDS-PAGE is mainly in a form of monomer. It was identified by analytic ultracentrifugation that the purified VP6 protein had a molecular weight of 114.9?1.6 KDa, and was present in a form of polymer in SDS-PAGE, which was between 119 and 211 KDa in size. According to the SDS-PAGE results in combination with the analytic ultracentrifugation results, the purified VP6 protein was present in a form of trimer. It was consistent with the result of size exclusion chromatography, i.e. the retention time of VP2 protein was shorter than that of VP6 protein. Accordingly, VP2 and VP6 protein obtained by prokaryotic expression retained their native confirmations. Moreover, the whole process was simple and was convenient for operation, and thus had incomparable advantages relative to eukaryotic expression.
Example 4: Assembly of VP2 Virus-Like Particle 2-VLP
(74) The sample was the VP2 protein with a purity of above 95% obtained in Example 2.
(75) Method: VP2 protein was dialyzed at 4? C. to an assembly buffer 50 mM TB8.0+0.2M (NH.sub.4).sub.2SO.sub.4, the buffer was changed every 12 h, and the dialysis was carried out for more than 24 h. After dialysis, the solution was centrifuged at 10000 rpm for 15 min, the precipitate was collected, and was dissolved in 50 mM TB8.0. The resultant solution was centrifuged at 10000 rpm for 15 min, and the supernatant was collected, i.e. monolayer virus-like particle 2-VLP consisting of VP2.
Example 5: Assembly of 6-VLP and 2/6-VLP
(76) The samples were the VP6 protein with a purity of above 98% as obtained in Example 1, the VP2 protein with a purity of above 95% as obtained in Example 2, and 2-VLP as obtained in Example 4.
(77) Assembly of 6-VLP
(78) VP6 protein was dialyzed to the assembly buffer as shown in Table 2, and the buffer was changed every 12 h, and the dialysis was carried out for more than 24 h. Then centrifugation was carried out, and the supernatant was collected, i.e. 6-VLP.
(79) TABLE-US-00005 TABLE 2 Assembly of 6-VLP in different buffer systems pH NaCl concentration Results 1 3.0 0 trimer 2 3.0 0.5M aggregation 3 3.0 1M aggregation 4 4.0 0 spherical particle 5 4.0 0.2M spherical particle 6 4.35 0 spherical particle 7 4.35 0.5M spherical particle 8 4.35 1M precipitant 9 5.0 0 spherical particle 10 6.0 0 spherical particle 11 6.0 0.5M spherical particle 12 6.0 1M spherical particle 13 6.4 0.3M spherical particle 14 7.0 0 trimer 15 7.0 0.5M trimer 16 7.0 1M trimer
(80) Assembly of 2/6-VLP
(81) Process 1: 2-VLP and VP6 protein were mixed in a ratio of 1:3 by mass, and were dialyzed to CN4.0, CN5.0 or MES6.0, the buffer was changed every 12 h, and the dialysis was carried out for more than 24 h. After dialysis, the solution was centrifuged for 15 min at 10000 rpm, the supernatant was collected, i.e. 2/6-VLP.
(82) Process 2: VP2 protein which was not assembled into VLP and VP6 protein were mixed in a given ratio, and were dialyzed to an assembly buffer (Table 3). The ratio of VP2 and VP6 was shown in table 4. The buffer was changed every 12 h, and the dialysis was carried out for more than 24 h. After dialysis, the solution was centrifuged at 10000 rpm for 15 min, and the supernatant was collected, i.e. 2/6-VLP.
(83) TABLE-US-00006 TABLE 3 Assembly of 2/6-VLP in different buffer systems pH NaCl concentration Results 1 3.0 0 polymer 2 4.35 0 2/6-VLP 3 4.35 0.5M 2/6-VLP 4 6.0 0 6-VLP 5 6.0 0.15M 6-VLP and 2/6-VLP 6 6.0 0.3M 2/6-VLP 7 6.0 0.5M 2/6-VLP 8 6.4 0.3M 2/6-VLP 9 6.4 0.5M 2/6-VLP 10 6.4 1M 2/6-VLP 11 7.0 0.3M polymer 12 8.0 0 polymer 13 8.0 0.5M polymer
(84) TABLE-US-00007 TABLE 4 Ratio of VP2 and VP6 for assembly of 2/6-VLP VP2:VP6 Results 1 1:2 2/6-VLP 2 .sup.1:2.2 2/6-VLP 3 .sup.1:2.4 2/6-VLP 4 .sup.1:2.6 2/6-VLP 5 .sup.1:2.8 2/6-VLP 6 1:3 2/6-VLP 7 1:4 6-VLP and 2/6-VLP 8 1:5 6-VLP and 2/6-VLP 9 1:6 6-VLP and 2/6-VLP 10 1:8 6-VLP and 2/6-VLP 11 1:10 6-VLP and 2/6-VLP 12 0:1 6-VLP
Example 6: Morphologic Measurement of Rotavirus VLPs and Evaluation of Assembly Efficiency
(85) TEM Observation of Rotavirus VLPs
(86) The equipment was a JEOL 100 kV Transmission Electron Microscope (100,000? magnification). 2-VLPs obtained in Example 4 were fixed on a copper grid and negatively stained with 2% phosphotungstic acid at pH 7.4 for 30 min, and then was observed. A large number of hollow VLPs with a radius of 50-60 nm were observed (
(87) Dynamic Light-Scattering Observation of RV VLPs
(88) DynaPro MS/X dynamic light-scattering instrument (including a temperature controller) produced by US Protein Solutions Co. was used for light-scattering measurements. The Regulation algorithm was used in the measurements. The samples were 6-VLP and 2/6-VLP obtained in Example 5. The samples were centrifuged at 12000 rpm for 10 min prior to the measurement. The results showed that 6-VLP and 2/6-VLP had a hydrodynamic radius of 40.36 nm (
(89) Analysis of RV VLPs by Size Exclusion Chromatography
(90) Equipment: Agilent 1200 high performance liquid chromatograph (HPLC)
(91) Chromatographic column: G5000PWXL 7.8 mm?30 cm (Japan TOSOH Co.), with a column volume of 13.4 ml
(92) Buffer: 20 mM phosphate buffer pH6.4+300 mM NaCl
(93) Flow rate: 0.5 ml/min
(94) Detection wavelength: 280 nm
(95) Sample: 6-VLP and 2/6-VLP obtained in Example 4
(96) The results showed that 6-VLP had a retention time of 10.551 min and an assembly efficiency of 94.6% (
(97) Analytical Ultracentrifugation of RV VLPs
(98) The equipment was Beckman XL-A analytical ultracentrifuger, the sample was 6-VLP and 2/6-VLP obtained in Example 5, the method was sedimentation velocity method, SEDIFIT software was used to analyze C(S). The results showed that at pH4.0-6.0, sedimentation velocities were different in different buffer systems to some extent, the sedimentation velocity of 6-VLP was between 237S and 240S, the sedimentation velocity of 2/6-VLP was between 278S and 290S, and both of them could be assembled at pH4.0-6.0 (
(99) To sum up, 6-VLP and 2/6-VLP assembled in vitro had good homogeneity and an assembly efficiency of above 90%; their preparation processes were simple and convenient for operation; and they were obviously superior to virus-like particles of multiple different components produced by eukaryotic expression.
Example 7: Evaluation of Immunogenicity of VP6 Protein
(100) The immunogenicity of VP6 protein was evaluated in a mouse model. The animals to be immunized were SPF grade female Balb/C mice of 5-8 weeks old (purchased from Shanghai Slac Laboratory Animal Co. Ltd), 3 mice per group, and the samples were VP6 protein obtained in Example 1, 6-VLP and 2/6-VLP obtained in Example 5 and rotavirus A obtained by MA104 cell culture. Said samples were mixed with an equal volume of Freund's adjuvant (complete Freund's adjuvant was used for primary immunization, and incomplete Freund's adjuvant was used for booster), the immunization dose was 100 ?g, and the immunization route was subcutaneous immunization; or said samples were mixed with aluminum adjuvant, and the immunization dose was 1-100 ?g, and the immunization route was muscular injection. The immunization procedure was as followed: the primary immunization at Day 0, and the boosters at Day 7 and Day 14.
(101) Peripheral venous blood was taken from mice every week, serum was isolated, the titer of VP6 antibody in serum was determined by an EIA method. The procedure was as followed: 1) coating: the sample was VP6 protein obtained in Example 1, the buffer was 50 mM carbonate buffer pH9.6, the coating concentration was 500 ng/mL, the coating amount was 100 ?L per well, and the coating condition was 37? C., 2 h; 2) washing: PBST (20 mM PBS+0.05% Tween20), once, drying by bottom up; 3) blocking: the blocking solution was PBS+0.5% casein, the blocking condition was 2004 per well, 37? C., 2 h; after blocking, drying by bottom up; 4) loading: sample: mouse serum; the diluent was PBS+10% calf serum; 10-fold serial dilution; 100 ?L per well, 37? C., 30 min; 5) washing: PBST, 5 times, drying by bottom up: 6) adding an enzyme-labeled second antibody: the enzyme-labeled second antibody was GAM-HRP, the diluent was PBS+0.5% casein, the dilution fold was 1:5000, 100 ?L per well, 37? C., 30 min; 7) washing: PBST, 5 times, drying by bottom up; 8) developing: TMB developing solution, 100 ?L per well, 37? C., 15 min; 9) stopping: stop buffer, 50 ?L per well; 10) readout: Antos enzyme-labeling equipment, OD450/600.
(102) The greatest dilution fold, at which OD450/600 was of greater than 0.2, was determined as antibody titer in mouse serum. The results showed that as compared to an equal amount of inactivated virus, VP6 antigen had a higher immunogenicity; and Freund's adjuvant could better improve the immunogenicity of VP6 protein as compared to aluminum adjuvant (
Example 8: Evaluation of Immune Protection of VP6 Protein and VLP Thereof
(103) Since VP6 antibodies do not have in vitro neutralizing activity and adult mice have poor sensitivity to rotavirus, a pregnant mice-neonatal mice model is used to evaluate immune protection of VP6 protein. 4-5 week old SPF-grade female Balb/c mice were divided into five groups, VP6 obtained in Example 1, 6-VLP and 2/6-VLP obtained in Example 5, rotavirus A obtained by MA104 cell culture, or PBS was mixed with an equal volume of Freund's adjuvant (complete Freund's adjuvant was used for primary immunization, and incomplete Freund's adjuvant was used for booster), the immunization route was subcutaneous immunization, and the immunization dose was 10 ?g VP6 per mouse. The immunization procedure was as followed: the primary immunization at Day 0, and the boosters at Day 10 and Day 20, and a final booster at Day 30 (using antigens in the same dose mixed with aluminum adjuvant by muscular injection). Peripheral venous blood was taken two weeks after the last immunization, and serum was isolated and stored for further detection. Female mice and male mice were kept in the same cage, and male mice were taken out after mating. Neonatal mice were challenged with a virus 4-6 days after birth, at a dose of 5*10.sup.6 TCID50 per neonatal mouse, wherein the virus was human rotavirus obtained by MA104 cell culture. After challenging with the virus, health condition of the neonatal mice was observed and recorded, such as diarrhea condition, and change in weight. A mouse was killed at each of 0, 24, 48 and 72 hpc, pathological changes in tissues of the mice were observed after anatomy, small intestine tissues were taken, and the virus was detected by methods such as immunohistochemistry and EIA. In addition, serum was isolated and titer of serum antibody was determined by EIA.
(104) VP6 Immunogenicity and Passage of Maternal Antibody
(105) Titers of VP6 antibody were determined by EIA in sera of mother mice and neonatal mice from different immunization groups. The coated antigen was VP6 protein recombinantly expressed in E. coli, the coated amount was 50 ng/well, and the method was as described in Example 7.
(106) Protective Effect of VP6 Antibody from Mother Mice on Diarrhea of Neonatal Mice
(107) After challenging with virus, diarrhea condition was monitored in neonatal mice. Mice were scored depending on the color and shape of feces, and it was found that diarrhea was most serious in neonatal mice 24 h after challenging with virus. The results were shown in Table 5. Within 24 h after challenging with virus, obvious diarrhea symptoms developed in the control group, while no diarrhea or only mild diarrhea symptoms developed in the experimental groups. Antibodies from mother mice immunized with VP6, 6-VLP, 2/6-VLP and inactivated virus alleviated the symptoms of diarrhea in neonatal mice, there was no significant difference among antibodies from mother mice immunized with VP6, 2/6-VLP and inactivated virus with respect to immune protection (P value was 0.070 and 0.946, respectively), while immune protection of 6-VLP was significantly lower than that of RV (P=0.001) and 2/6-VLP (P<0.001).
(108) TABLE-US-00008 TABLE 5 Diarrhea condition in neonatal mice 24 h after rotavirus infection Score VP6 6-VLP 2/6-VLP RV PBS 1 2 6 12 7 3 5 11 2 1 5 4 2 3 4 5 1 4 1. Normal feces; 2. Brown shaped feces; 3. Brown-yellow soft feces; 4. Yellow, loose feces; 5. Watery feces
(109) Score?3 was diagnosed as diarrhea, score>3 was diagnosed as serious diarrhea.
(110) TABLE-US-00009 TABLE 6 Protection efficiency of VP6 antibodies from mother mice on diarrhea caused by rotavirus infectious Diarrhea Serious diarrhea VP6 42.86%* 65.18%*.sup., & (?37.86%, 76.31%) (?31.24%, 90.76%) 6-VLP / 65.18%*.sup., & (?31.24%, 90.76%) 2/6-VLP 85.71%*.sup., & 100%*.sup., & (36.7%, 96.78%) (?, 100%) RV 87.5%* 100%* (4.46%, 98.36%) (?, 100%) *significant difference relative to PBS control; .sup.&significant difference relative to inactivated RV
(111) Inhibition of VP6 Antibodies from Mother Mice on Replication of Rotavirus
(112) After challenging with virus, 1-2 neonatal mice were killed every 24 h, pathological change in tissues was observed, and it was found that intestinal tissues were aerated seriously in the control group. Intestinal tissues were taken and were grinded and disrupted by high pressure homogenization, and then centrifuged. The supernatant was taken, and VP6 antigen therein was determined by a sandwich method. The method was as followed: 1) coating: VP6 monoclonal antibody 9F10; the buffer was 20 mM PB7.4, the coating concentration was 4 ?g/mL, the coating amount was 100 ?L per well, and the coating condition was 37? C., 2 h; 2) washing: PBST (20 mM PBS+0.05% Tween20), 400 ?L per well, once, drying by bottom up; 3) blocking: the blocking solution was 20 mM PBS+0.5% casein; the blocking condition was 200 ?L per well, 37? C., 2 h; after blocking, drying by bottom up; 4) loading: diluting homogenate of small intestinal tissues with PBS+10% calf serum to 2-fold serial dilution, 100 ?L per well, 37? C., 30 min; 5) washing: PBST, 5 times, 4004 per well, drying by bottom up: 6) adding an enzyme-labeled antibody: diluting HRP-labeled VP6 monoclonal antibody 15H10-HRP with diluent 20 mM PBS+0.5% casein by 5000 fold, 100 ?L per well, 37? C., 30 min; 7) washing: PBST, 5 times, 400 ?L per well, drying by bottom up; 8) developing: TMB developing solution, 100 ?L per well, 37? C., 15 min; 9) stopping: stop buffer, 50 ?L per well; 10) readout: Antos enzyme-labeling equipment, determining OD450/600, wherein the greatest dilution fold at which the OD450/600 value was greater than 0.2 was taken as a virus titer.
(113) The results showed that VP6 antibodies could effectively inhibit the infection and replication of rotavirus.
(114) To sum up, the VP6, 6-VLP and 2/6-VLP antibodies from the mother mice had protective effect on rotavirus infection and diarrhea caused by rotavirus infection, wherein 2/6-VLP exhibited the best protective effect, and was not significantly different from inactivated virus in the same dose with respect to prevention of serious diarrhea and diarrhea.
(115) Although the specific embodiments of the present invention have been described in details, those skilled in the art would understand that, according to the teachings disclosed in the specification, various modifications and changes can be made without departing from the spirit or scope of the present invention as generally described, and that such modifications and changes are within the scope of the present invention. The scope of the present invention is given by the appended claims and any equivalents thereof.