Abstract: Process for preparing a heat-treated pooled human platelet lysate, said process comprising the steps of: a) Providing a pooled human platelet lysate (p HPL), b) Heat-treating the pooled human platelet lysate at a temperature of 50° C. to 70° C. during 20 to 40 minutes, c) Purifying the heat-treated pooled human platelet lysate of step b).

Abstract: The present invention relates on a process for preparing platelet lysate fraction, said process comprising the steps of: 1) providing a platelet lysate, 2) collecting from said platelet lysate a fraction wherein the components exhibit a maximum molecular weight of 100 kDa, on a specific platelet lysate fraction and its use as a drug.

Abstract: A method for expanding circulating tumor cell in vitro includes preparing a cell culture tool having a multi-particle colloidal crystal layer, preparing a cell solution including circulating tumor cells, and contacting the cell solution with the multi-particle colloidal crystal layer, to attach the circulating tumor cells in the cell solution to the multi-particle colloidal crystal layer and rapidly expand by 20 times or more. The multi-particle colloidal crystal layer at least includes first particles having a particle size of 1000 to 5000 nm and second particles having a particle size of 20 to 400 nm. The culture medium in the cell solution at least includes a platelet lysate.

Abstract: Process for preparing a heat-treated pooled human platelet lysate, said process comprising the steps of: a) Providing a pooled human platelet lysate (p HPL), b) Heat-treating the pooled human platelet lysate at a temperature of 50° C. to 70° C. during 20 to 40 minutes, c) Purifying the heat-treated pooled human platelet lysate of step b).

Abstract: A method for expanding circulating tumor cell in vitro includes preparing a cell culture tool having a multi-particle colloidal crystal layer, preparing a cell solution including circulating tumor cells, and contacting the cell solution with the multi-particle colloidal crystal layer, to attach the circulating tumor cells in the cell solution to the multi-particle colloidal crystal layer and rapidly expand by 20 times or more. The multi-particle colloidal crystal layer at least includes first particles having a particle size of 1000 to 5000 nm and second particles having a particle size of 20 to 400 nm. The culture medium in the cell solution at least includes a platelet lysate.

Abstract: A process for preparing a modified heat-treated platelet pellet lysate, said process comprising the steps of: a) Providing a platelet pellet lysate, b) Heat-treating the platelet pellet lysate at a temperature of 55° C. to 65° C. during 20 to 40 minutes, c) Purifying the heat-treated platelet pellet lysate of step b) so as to obtain a modified heat treated platelet pellet lysate having a total protein content of less than 70% of the total protein content of the platelet pellet lysate of step a).

Abstract: The present disclosure relates to a clottable concentrate of platelet growth factors for therapeutic and/or cosmetic use, preferably comprising the growth factors PDGF, TGT-?, IGF, EGF, CTGF, bFGF and VEGF. In a preferred embodiment, the clottable concentrate of platelet growth factors does not induce blood cell-related transfusion reactions. The present disclosure also relates to a method for preparing a clottable concentrate of platelet growth factors including the steps of contacting a platelet concentrate with a solvent and/or a detergent, incubating the platelet concentrate with the solvent and/or detergent for a period of at least 5 minutes to 6 hours, at a pH maintained in a range from about 6.0 to about 9.0, and at a temperature within the range of from 2° C. to 50° C., preferably within the range of from 25° C. to 45° C., and removing the solvent and/or the detergent by oil extraction and/or chromatographic means.

Abstract: The invention concerns human platelet extracts rich in growth factors (PGF) for wound healing and stem cell expansion. Accordingly the subject invention relates to a virally-inactivated growth factors-containing platelet lysate depleted of PDGF and VEGF, which is preferably enriched in TGF, IGF and EGF-rich. The present invention further concerns a method for obtaining a platelet lysate comprising the steps of contacting a starting platelet concentrate with a solvent and/or a detergent, incubating the starting platelet concentrate with the solvent and/or detergent for a period of at least 5 minutes to 6 hours, at a pH maintained in a range from about 6.0 to about 9.0, and at a temperature within the range of from 2° C. to 50° C., optionally removing the solvent and/or the detergent by oil extraction and obtaining an aqueous protein phase, and incubating the solvent and/or detergent-treated platelet concentrate or the aqueous protein phase with charcoal.

Abstract: The invention concerns human platelet extracts rich in growth factors (PGF) for wound healing and stem cell expansion. Accordingly the subject invention relates to a virally-inactivated growth factors-containing platelet lysate depleted of PDGF and VEGF, which is preferably enriched in TGF, IGF and EGF-rich. The present invention further concerns a method for obtaining a platelet lysate comprising the steps of contacting a starting platelet concentrate with a solvent and/or a detergent, incubating the starting platelet concentrate with the solvent and/or detergent for a period of at least 5 minutes to 6 hours, at a pH maintained in a range from about 6.0 to about 9.0, and at a temperature within the range of from 2° C. to 50° C., optionally removing the solvent and/or the detergent by oil extraction and obtaining an aqueous protein phase, and incubating the solvent and/or detergent-treated platelet concentrate or the aqueous protein phase with charcoal.

Abstract: The invention relates to a novel method of virally inactivating biological fluids by solvent/detergent treatment of the fluid, followed by oil extraction and filtration.

Abstract: The present disclosure relates to a clottable concentrate of platelet growth factors for therapeutic and/or cosmetic use, preferably comprising the growth factors PDGF, TGT-?, IGF, EGF, CTGF, bFGF and VEGF. In a preferred embodiment, the clottable concentrate of platelet growth factors does not induce blood cell-related transfusion reactions. The present disclosure also relates to a method for preparing a clottable concentrate of platelet growth factors including the steps of contacting a platelet concentrate with a solvent and/or a detergent, incubating the platelet concentrate with the solvent and/or detergent for a period of at least 5 minutes to 6 hours, at a pH maintained in a range from about 6.0 to about 9.0, and at a temperature within the range of from 2° C. to 50° C., preferably within the range of from 25° C. to 45° C., and removing the solvent and/or the detergent by oil extraction and/or chromatographic means.

Abstract: The invention relates to the use of polyoxyethylene (4-5) p-t-octyl phenol (t-Oct-C6H4—(OCH2CH2)x0H, x=˜5) or polyoxyethylene (20) sorbitan monooleate in solvent/detergent viral inactivation of biological fluids for the preparation of a virally inactivated biological fluid having a high alpha 2-antiplasmin content.

Abstract: The present invention relates to a plasma product or a serum product with an extremely low risk of viral contamination and a method for producing the same. Before treating plasma or serum to be used as a raw material for producing a plasma product or a serum product using a virus removal membrane, leucocytes contaminating the blood are removed. Thus, a plasma product or a serum product with an extremely low risk of viral contamination can be efficiently produced while preventing clogging. Since clogging scarcely arises, it is possible to carry out efficient filtration without applying an elevated pressure as the filtration proceeds.

Abstract: The invention relates to a set system of disposable bags comprising at least one viral inactivation bag (1), comprising an inner compartment (4), an inlet facility (5) and an outlet facility (6), which are both connected to the inner compartment (4), the bag (1) being characterised in that the inner compartment (4) has an ovoid longitudinal section, and at least one funnel bag (9), and/or a column chromatography bag (15), the different bags being connectable with each other, and to the use of said set system of disposable bags for the viral inactivation of biological fluids with excellent protein recovery.

Abstract: The present invention relates to a plasma product or a serum product with an extremely low risk of viral contamination and a method for producing the same. Before treating plasma or serum to be used as a raw material for producing a plasma product or a serum product using a virus removal membrane, leucocytes contaminating the blood are removed. Thus, a plasma product or a serum product with an extremely low risk of viral contamination can be efficiently produced while preventing clogging. Since clogging scarcely arises, it is possible to carry out efficient filtration without applying an elevated pressure as the filtration proceeds.

Abstract: The invention relates to a plasma derived immunoglobulin G concentrate and to the process for producing said concentrate. The process comprises a series of chromatographic separations but no ethanol precipitation. The process also includes a viral inactivation treatment. The invention relates to the immunoglobulin G concentrate obtained by said process which is of therapeutic quality suitable for any use especially for intraveinous injection.

Abstract: The invention relates to a process for preparing purified albumin from a human or animal physiological solution, such as a plasma or a plasma fraction. The process includes a process of delipidation using an anionic detergent and two chromatographic separation stages using ion-exchange resin. By applying the process according to the invention, it is possible to obtain an albumin solution of great purity, that is stable and suitable for therapeutic use.

Abstract: The invention relates to a process for preparing a concentrate of Factor VIII-von Willebrand factor complex having high specific activity from total (non-cryoprecipitated) plasma.The process comprises pre-purifying by means of a double treatment with barium chloride and with aluminium hydroxide.The process then comprises purification by chromatography on an anion exchange resin, of the DEAE-Fractogel type.The process includes a step of viral inactivation by means of a treatment with solvent-detergent.The process also makes it possible to recover fibrinogen, albumin, immunoglobulins, antithrombin III, fibronectin and prothrombin complex, from the same plasma.The different concentrates obtained using the process according to the invention are intended, in particular, for therapeutic use.

Abstract: The present invention relates to a method for preparing a high purity Factor IX concentrate. The starting material for the process is the supernatant fraction of a cryoprecipitated human plasma. A pre-purification step is performed by DEAE-Sephadex chromatography. The resulting Factor IX fraction has a specific activity of at least 0.5 IU/mg protein. The purification method of the invention comprises two successive chromatography separations. First, ion-exchange chromatography on DEAE-sepharose is conducted so that the Factor IX is eluted when the ionic force of the buffer is increased to 0.34-0.38M sodium chloride. Then, affinity chromatography is conducted on heparin-sepharose. The elution buffer is a citrate buffer at a pH of 7.4 adjusted with 0.45M sodium chloride and supplemented with arginine as a stabilizer for Factor IX activity. Lysine is added as a stabilizer before freeze-drying of the purified Factor IX.

Abstract: The invention relates to a process for purifying human von Willebrand factor from a cryoprecipitated plasma fraction, which comprises a combination of three chromatographic separation steps. The first chromatographic separation step comprises contacting a cryoprecipitated fraction with a large-pore vinyl polymer resin having DEAE group. The effluent from this separation step is again contacted with a large pore vinyl polymer resin having DEAE groups in the second chromatographic step. In the third chromatographic separation step, the effluent from the second step is subjected to affinity chromatography by contacting with gelatin-Sepharose. The concentrate obtained has very high specific activity and a high percentage of high molecular weight multimers. The concentrate is intended, in particular, for therapeutic use.