A PROCESS FOR ENCAPSULATING VIABLE ANIMAL CELLS

Abstract: A process for encapsulation of viable animal cells suitable for research and industrial applications, such as production of artificial organs, tissue and cell transplantation and production of cell derived substances, includes the steps of: a) providing sterilized supports made of organic and/or inorganic compounds and with suitable geometry to immobilize the desired loads of cells, b) incubating a cell suspension with the supports in order to ensure adhesion to the support surface, c) encapsulating the cells with a permanent layer formed by investing the supports with a reactive gas current composed of a carrier gas saturated by inorganic alkoxides for time intervals variable in function of cell nature and load, support geometry and porosity, d) treating the encapsulated viable cells with steam under mild conditions to perform total hydrolysis of residual alkoxide groups, e) storing the cells encapsulated on the supports by immersion into appropriate culture media. The encapsulation methods enables self-survival of the cells while avoiding antibody and immune-cell invasive action.

Description: A PROCESS FOR ENCAPSULATING VIABLE ANIMAL CELLS The present invention relates to a process for the encapsulation of viable animal cells, suitable for research and industrial applications, including production of artificial organs, tissue and cell transplantation and production of cell derived substances. It is known that loss or failure of organs and tissues can be treated by the development of functional substitutes made by cells placed on or within matrices which can be implanted or used as extracorporeal devices. Some reviews on this topic are: R. Langer and J.P. Vacanti; Science, 260, 920 (1993); P.E. Lacy, Scientific American, (1995) 40; W.W. Gibbs, Scientific American, (1993) 16. Some literature reports relevant to the problem are T.R. Shockley and M.L. Yarmush, Biotechnol. Bioeng. , 35 (1990) 843; M. Taya, M. Yoshikawa, and T. Kobayashi, J. Ferment. Bioeng. , 67 (1989) 138; Y. Shirai, H. Heshimoto, and H. Kawahara, Appl. Microbiol. Biotechnol., 29 (1988) 113; Y. Ho and T.M.S. Chang, Artif. Organs, 16 (1992) 442; A.A. Demetriou et. al. , Science, 233 (1986) 1190; F. Lim and A. M. Sun, Science, 210 (1980) 908; E.J.A. Pope, J. Sol-Gel Sci. Tech., 4_ (1995) 225; E.J.A. Pope et al . "Sol- Gel Science and Technology", Volume 55 (1955) pages 33-49. In most cases the encapsulation is performed by hydrogels, in particular polysaccaride alginate, acrylonitrile-vinyl chloride copolymers, hollow fibers, carrageenan gel, agar rods and sol-gel derived Siθ 2 from hydrolysis of silicon alkoxides in solution. These approaches are affected by severe shortcomings such as reduction of mass transfer with the medium, insufficient stiffness to avoid cell release, chemical incompatibility with cell viability, production of severe poison byproducts, as for cell encapsulation by sol-gel obtained by hydrolysis and condensation of inorganic alkoxides in solution. These problems can be solved by reacting supported cells and cell aggregates with gas-phase inorganic alkoxides suitable to react with the cell surface, resulting in a thin porous deposit of inorganic oxides in accordance with PCT application No. PCT/IT95/00083 the content of which is incorporated herewith as reference. The aim of the present invention is therefore to avoid the disadvantages of mentioned encapsulation procedures by means of a process which provides a definite encapsulation of viable animal cells by a continuous and permanent layer of inorganic oxide's with a pore size distribution ensuring free exchange of nutrients and metabolic products and avoiding antibody and immune-cell invasive action. Another object of the invention is to provide a general immobilization method for animal cells and cell aggregates without limitations to defined organs, species, and cell functions with preservation of cell viability and metabolic functions. Still another object of the invention is to provide a method involving simple operations under mild conditions of temperature and pressure which can be performed with industrial-scale devices and production equipments under sterile environmental conditions. A further object of the invention is the maintenance of viable animal cell and of their specific functions also for use in extra-corporeal devices and the supply of immobilized cell aggregates for transplantation into the body. These and other objects are achieved, according to the invention by a process for encapsulation of viable animal cells suitable for research and industrial applications, such as production of artificial organs, tissue and cell transplantation and production of cell derived substances, comprising the steps of: a) providing sterilized supports made of organic and/or inorganic compounds and with suitable geometry to immobilize the desired loads of cells; b) incubating a cell suspension with the supports in order to ensure adhesion to the support surface; c) encapsulating the cells with a permanent layer formed by investing the supports with a reactive gas current composed of a carrier gas saturated by inorganic alkoxides for time intervals variable in function of cell nature and load, support geometry and porosity; d) treating the encapsulated viable cells with steam under mild conditions to perform total hydrolysis of residual alkoxide groups; e) storing the cells encapsulated on the supports by immersion into appropriate culture media. Preferably, incubation step b) is accomplished by growing actively replicating cell lines in order to fill most of the available volume of the supports. Furthermore, the reactive gas of step c) may be composed of a gas carrier saturated by Si(OR) 4 and/or SiX χ (OR) 4 _ χ , where x=l,2; X=H, alkyl or halide; R=alkyl. It has been surprisingly and conclusively found that it is possible to encapsulate animal cells, in accordance with the present invention. The supports may be formed from foam of organic polymers, polymeric or glass or ceramic fiber textures, natural products, rock wool, organic or inorganic membranes. The supports may be shaped as sheets, disks, plates, cones, tubes or corrugated solids with void/middle ratios in the interval 0.1-0.9 due to open pores ranging from lμm to 2000μm, in diameter. Supports of inorganic materials, after sterilization, can be dipped into a solution of inorganic-oxide precursors, for example silicon alkoxides, suitable of hydrolysis and condensation. The solution viscosity ranges from 0.1 and 100 Pas, the extraction rate is between 1 and 103 mm/s, the nominal oxide concentration is in the interval 1-100 g/dm 3 , providing a definite increase of stiffness and mechanical strength, for example of textured glass fibers. The cell load may be extended up to the available void volume; supports extracted from culture are mounted in a rack and tranferred into a closed reaction chamber. The items are invested by a sterile air flux saturated by reactive alkoxides, preferably a mixture of HSi (CH 3 ) (OC 2 H 5 ) 2 and s i(°C 2 H 5)4r at room temperature. Saturation is obtained by bubbling the air flux into the alkoxide mixture kept at temperatures in the interval 10- 90°C. The reactive gas flux is variable in fuction of cell load. The treatment is prolonged for some minutes, then steam is introduced at room temperature for appropriate time intervals. The treatment with reactive gas, followed by steam reaction can be repeated several times during which the composition of the reactive gaseous species can be modified, for example changing the alkoxides or their concentrations . These changes can be used to modify the specific surface area and pore size distribution of the deposited layer providing a variable permeability thus affecting the mass transfer as a function of bulkiness and molecular weight. Further characteristics and advantages of the invention will be come apparent from the description of four examples, illustrated hereinafter only by way of non- limitative examples with reference to the accompanying Figures 1 to 11, wherein: Figure 1 shows glucose concentrations in culture medium; Figure 2 shows H activity in proteins secreted into culture medium; Figure 3 is a SEM micrograph of clusters of fibroblosts; Figure 4 is a SEM micrograph of encapsulated cell aggregate; Figure 5 shows J H activity in proteins secreted by H4 cells; Figure 6 is a SEM micrograph showing a group of H4 cells; Figure 7 is a diagram showing incorporation of 3 H leucine into secreted proteins; Figure 8 is a SEM micrograph of control cells; Figure 9 is a SEM micrograph of encapsulated cells; Figure 10A is a diagram showing a microprobe analysis of support membrane without cells; Figure 10B is a diagram showing a microprobe analysis of a small cell duster on the membrane; Figure 11 shows H leucine incorporation into proteins. Example 1 Glass fabric disks, diameter 2.5cm and thickness 1.5 mm, composed of fibers lOμm in diameter and textured by lOOxlOOμm meshes, are hydrolyzed for 30 minutes in a sterilization apparatus operating at 130°C. Disks are coated by a 0.1-0.2μm layer of Si0 2 , modified by Si-CH 3 bonds, upon dipping into a 1 M ethanol solution of CH 3 Si ( OC 2 H 5 ) 3 in the presence of aqueous 10~ 3 M HCl providing a Si-OR/H 2 0=l molar ratio. The solution viscosity ranges in the interval 0.1-5 Pas, the extraction rate is 102 cm/minute. After consolidation for 24 hours at 40°C, the disks are sterilized by steam and placed into 7 cm 3 polistyrene wells, 2.5 cm in diameter. Human fibroblasts are obtained by skin biopsy and cultured in Dulbecco ' s Modified Eagle's Medium (DMEM), supplemented with 10% fetal calf serum (FCS). Two ml of DMEM + 10% FCS, containing a suspension of fibroblasts (1 x 10 6 cells/ml) are added to the wells. Cell cultures are incubated at 37° C for 24 hours. Disks are then transferred in a glass rack and placed into a 5 dm reaction chamber equipped for fluxing- gas treatments and suitable for sample collection. Disks are treated with air saturated by bubbling into Si(OC 2 H 5 ) 4 and CH 3 SiH ( OC 2 H 5 ) 2 at 80°C, relevant concentration corresponding to 1/1 molar ratio. The total reactive gas flux is 100 cm /minute and the treatment lasts for 10 or 20 minutes; then, the same flux of air, satured by bubbling into sterile water at 80°C, is passed into the chamber for 10 minutes. The temperature inside the reactor is between 26 and 28°C. The items are transferred into new culture wells containing 2 ml of DMEM+10% FCS and are incubated at 37°C. The metabolic activity of cultured cells is tested by determination of glucose utilization and of J H-leucine incorporation into secreted proteins. While the former test is an index of energy metabolism, the latter is dependent on the cell ability to take up H-leucine, incorporate it into proteins and secrete such proteins into the culture medium. Analysis are performed on culture media incubated with the following samples: (1) cells on glass support not subjected to immobilization reaction (used as controls); (2) cells on glass support subjected to 10-min reaction; (3) cells on glass support subjected to 20-min reaction. Procedure for metabolic and morphological studies Twenty-four hours after reaction, the culture medium is replaced and incubated with the cells for additional 24 hours. The medium is then aspirated and analysed for glucose concentration by an enzymatic assay. Two ml of medium (DMEM+10% FCS), containing 3 H-leucine (1 mCi/ml; specific activity of 3 H-leucine 40.4 GBq/mg) are placed into each well and incubated for 24 hours. At the end of incubation, 1 ml of medium is aspirated from each well and diluted to a final volume of 4 ml with water. The solution is centrifuged at 3000 rpm for 5 min and the supernatant is filtered through 0.45 mm (pore size) filters (Millipore HV), in order to eliminate any particulate matter. The tubes are placed on melting ice and proteins are precipitated from the solution by addition of an equal amount of ice-cold 20% trichloroacetic acid (TCA) solution. After centrifugation, the supernatant is discarded and the pellet is washed three times with 5 ml of ice-cold 10% TCA, in order to eliminate residual 3 H-leucine. The pellet is finally dissolved in 1 ml 0.5 M NaOH containing 1% sodium duodecylsulphate . One ml of the protein solution is transferred into scintillation vials and added 10 ml of Hionic-Fluor scintillation Fluid (Packard). Four samples (1 ml each) of the original 3 H-leucine/DMEM+10% FCS solution are processed in t'he same way and used as blanks. Final H activity in secreted proteins is calculated by subtracting from each sample the mean of the activities determined in the four blank samples. Fibroblasts are maintained in culture, changing medium every second day. After one week, supports containing the cells are prepared for scanning electron microscopy (SEM). Results of metabolic studies Glucose utilization and 3 H-leucine incorporation into proteins by cultured human fibroblasts under different experimental conditions are reported in figures 1 and 2 respectively. Figure 1 shows glucose concentrations in culture medium after 24 hours of incubation with control (non-encapsulated) fibroblasts (C), and with fibroblasts subjected to 10-min (Tl) or 20-min (T2) encapsulation reaction. Figure 2 shows 3 H activity in proteins secreted into culture medium by the same experimental groups. These results indicate that both glucose utilization and protein synthesis and secretion are well maintained in immobilized encapsulated eufibroblasts. Results of morphological studies Clusters of fibroblasts enveloped by a silicon oxide membrane are shown in SEM micrographs (Figure 3 ) . Figure 4 shows an encapsulated cell aggregate after 10 min of treatment. A transparent silicon oxide layer surrounding a cluster of fibroblasts is clearly evidenced in the micrograph. Example 2 Polyesther rods, diameter 2.5 cm and thickness 0.5 cm, obtained from a continuous sponge-like blanked, are washed until complete release of powdered particles. After drying, rods are placed into polistyrene wells 3 cm in diameter containing 0.6 cm 3 of solution composed a 2 M ethanol solution of CH 3 Si(OC 2 H 5 ) 3 in the presence of 10 -3 M HCl aqueous solution, providing a Si-OR/H 2 0=2 molar ratio. The systems are left in air at room temperature till gelling of the solution into the bottom surface of rods; these are removed and consolidated at 40°C for 24 hours. Samples are sterilized by steam at 130°C for 40 minutes and put into wells, 2.5 cm in diameter and 2.5 cm in depth. Four ml of DMEM + 10% FCS, containing a suspension of 25 x 10 4 /ml H4-II-E-C3 rat hepatoma cells (American Type Culture Collection n° CRL 1600, Rockville, Maryland) are then added to the wells. Cells are incubated for 24 hours at 37° C under 5% C0 2 , in order to allow cell adhesion and reproduction on rod surface. The rods are then transferred into the gas flux reaction chamber, mentioned in example 1, and here reacted as described in the previous example (reaction time: 20 min) . At the end of the reaction, the rods containing the cells are transferred into new wells. Procedure for metabolic and morphological studies Test for incorporation of J H-leucine into secreted proteins is performed 48 hours after the reaction as described in example 1. The rods containing the cells are cultured for 7 additional days and then processed for SEM. Results of metabolic and morphological studies 3 H activity in proteins secretd by H4 cells is reported in figure 5. The following experimental groups are represented: control (non-encapsulated) cells (C) and encapsulated celϊs (T). Figure 6 is a SEM migrograph showing a group of H4 cells growing on polyester fibers. Microprobe analysis reveals a high silicium concentration both on the surface of the cells and on polyester fibers. Example 3 Sterile inorganic membranes, sealed to the bottom of 6 cm 3 polistyrene cups, 2.5 cm in diameter, purchased from Nunc Intermed (Roskilde, Denmark) are added 1.5 ml of a suspension of H4 (rat epatoma ) cells in DMEM + 10% FCS (concentration of 25 x 10 4 /ml). Cells are allowed to grow on the membrane by incubation for 24 hours at 37°C under 5% C0 2 . The liquid medium is poured out and cups are transferred into a 3 dm glass reactor and placed in order over a rack, allowing membrane venting on both sides. Some cups are not sub j ected to re ac t i on and are used as controls . The reactor is equipped with a head , that can be dismantled , and ports for air inl et and outl et and for temperature control . Here , wet samples are invested by an 3 air flux of 100 cm /minute for 10 minutes, then reacted with a 50 cm 3 /minute air flux saturated with Si(0C 2 H 5 ) 4 ~ HSiCH 3 (0C 2 H 5 ) 2 • Air saturation is performed by bubbling into a Si(0C 2 H 5 ) 4 /HSiCH 3 (OC 2 H 5 ) 2 =1/1 molar solution, kept at 70°C by a thermostat. This treatment is prolonged for 10 minutes, then samples are invested by 100 cm 3 /minute air flux saturated by steam, bubbling into sterile water at 70°C, for 10 minutes. The temperature inside the reactor ranges between 24 and 26°C. Samples are divided into two groups (4 samples per group): (1) no treatment, used as controls; (2) one cycle of treatment. After the reaction, samples are then transferred into new wells in the above- mentioned conditions for 48 hours. Results of metabolic and morphological studies Incorporation of H-leucme into proteins synthesized and secreted by the cells is then studied as described in example 1. Figure 7 reports H activity in proteins secreted by control cells (C) and by encapsulated cells (T) . Cells were observed daily by light microscopy. While control cells grew until complete confluence, leaving no free space on the support membrane, encapsulated cells did not grow further, leaving large areas of nude membrane. Such a behaviour is documented by further SEM analysis. Figure 8 is a SEM micrograph of control cells, forming a continuous layer on the membrane. Figure 9 is a SEM micrograph of encapsulated cells, showing large non- colonized areas. Microprobe analysis showed silicium deposition on cell surface (Figure 10A) but not on the inorganic membrane (Figure 10B), where high concentrations of aluminium and phosphorous were found. Example 4 The same support membranes, mentioned in example 4, are treated with a suspension of HepG2 cells. Cell concentration, culture, reaction conditions, metabolic and morphological studies are identical to those described in example 3. Figure 1 1 shows the resu l t s o f 3 H- l e uc ine incorporation into proteins secreted by control Hep G2 cells . Morphological aspect of encapsulated cells at SEM was similar to example 3.

Claims: CLAIMS 1. A process for encapsulation of viable animal cells suitable for research and industrial applications, such as production of artificial organs, tissue and cell transplantation and production of cell derived substances, comprising the steps of: a) providing sterilized supports made of organic and/or inorganic compounds and with suitable geometry to immobilize the desired loads of cells; b) incubating a cell suspension with the supports in order to ensure adhesion to the support surface; c) encapsulating the cells with a permanent layer formed by investing the supports with a reactive gas current composed of a carrier gas saturated by inorganic alkoxides for time intervals variable in function of cell nature and load, support geometry and porosity; d) treating the encapsulated viable cells with steam under mild conditions to perform total hydrolysis of residual alkoxide groups; e) storing the cells encapsulated on the supports by immersion into appropriate culture media. 2. A process as claimed in claim 1 wherein encapsulation step c) is carried out with chemical species, in the gas-phase, suitable of interaction with cell surface creating a permanent layer of inorganic and/or organically modified inorganic species. 3. A process as claimed in claim 2 wherein the reactive gas is composed of a gas carrier saturated by Si(OR) 4 and/or SiX χ (OR) 4 _ χ , where x=l,2; X=H, alkyl or halide; R=alkyl, creating a permanent layer of Siθ 2 and/or organically modified inorganic species. 4. A process as claimed in claim 1 wherein incubation step b) is accomplished by growing of actively replicating cell lines in order to fill most of the available volume of the supports. 5. A process as claimed in claim 2 or 3 wherein said layer is continuous and porous, allowing exchange of substances between the cell and the medium. 6. A process as claimed in any preceding claims wherein the porosity of said layer is sized to exclude direct' contact between encapsulated cells or cell aggregates and antibodies or immune cells. 7. A process as claimed in any preceding claims wherein the encapsulated cells are animal cells, independently of animal species, functions and organs. 8. A process as claimed in any preceding claims, wherein the load of encapsulated cells or cell aggregates is extended up to the available void volume of the support. 9. A process as claimed in any preceding claims, wherein said supports are mounted in extracorporeal devices or directly implantable into animal or human body. 10. A process as claimed in any preceding claims, wherein said supports are dissolved to yield unsupported encapsulated cells or cell aggregates. 11. A process as claimed in any preceding claims, wherein said cell suspension of step (b) is nebulized and reacted in gas-phase of step (c) to provide encapsulation of cell aggregates by ordinary removal procedure of powders from gas or by bubbling the fluxing gas in appropriate solutions. 12. A process as claimed in any preceding claims, wherein the growth of viable cells before encapsulation is stimulated by addition of hormones or other chemicals also favouring cell propagation, aggregation, and occurrence of aggregates and clusters of different cells. 13. A process as claimed in any preceding claims, wherein the growth of viable cells is performed on biocompatible materials used for corporeal implantation irrespective of presence of immunosuppressive drugs.

Inventors: CARTURAN GIOVANNI, DAL MONTE RENZO, MURACA MAURIZIO, CARTURAN, GIOVANNI, DAL MONTE, RENZO, MURACA, MAURIZIO
Applicants: BIOSIL AG, CARTURAN GIOVANNI, DAL MONTE RENZO, MURACA MAURIZIO, CARTURAN, GIOVANNI, DAL MONTE, RENZO, MURACA, MAURIZIO
Application year: 1996
Main classification: C12N11
IPC codes: A61K9, C12N5, C12N11