EP1292385A1

EP1292385A1 - Method and facility for producing micromembrane capsules

Info

Publication number: EP1292385A1
Application number: EP01947241A
Authority: EP
Inventors: Rainer Pommersheim
Original assignee: Pommersheim Rainer
Current assignee: CAVIS MICROCAPS GmbH
Priority date: 2000-04-28
Filing date: 2001-04-25
Publication date: 2003-03-19
Also published as: WO2001083099A1; AU6898001A; US20040017018A1; CA2408025A1

Abstract

The invention relates to a method and a facility for industrial scale production of MICROMEMBRANE capsules for immobilizing active ingredients, proteins, live cells and/or microorganisms. According to the invention, the material dissolved in a base material or in suspended form that is to be encapsulated is fed from a reservoir into a reactor, wherein drops are produced from said material and balls are formed by precipitating said drops. The balls enclose the material and are then in turn coated by repeated rinsing in the same and/or different vessel.

Description

Process and plant for the production of micro-membrane capsules

The invention relates to a method and to a plant for the production of micro-membrane capsules on an industrial scale, for use in food technology, biotechnology, the chemical and / or pharmaceutical industry and medicine. Such capsules consist of a preferably spherical core which contains the immobilized substance or living cells or microorganisms and which can be surrounded by a shell which completely surrounds this core.

In technological practice, but also in medicine, it is often necessary to immobilize substances as well as living cells. In this way, their manageability can be improved, which leads to a significant reduction in costs. Sometimes it is the only way to use certain active ingredients or living cells. A known method for this is microencapsulation.

In order to be able to encapsulate cells, enzymes or other substances, they are mixed with a liquid, mostly water-soluble base substance, which is then dripped by suitable devices. The drops formed are hardened and include the substance or cells dissolved or suspended in them. This can be done either by crosslinking in a precipitation bath or by changing physical parameters such as temperature. The spheres thus formed, the diameter of which is in the range from a few micrometers to a few millimeters, can then be coated. Methods have been described in the specialist literature which use microorganisms such as yeasts immobilized in beads. For example, G.Troost et.al. (G.Troost et. Al. Sekt, Schaumwein, Perlwein, Stuttgart 1995) yeast immobilized in alginate spheres for bottle fermentation in the production of sparkling wine. This means that the time-consuming, manual shaking of the yeast deposit can be replaced by the rapid sinking of the beads in the champagne bottle. A disadvantage of these immobilizates, however, is the fact that yeast growth from the beads cannot always be prevented.

1

The German laid-open specification DE 3836894 AI describes a method and an apparatus which can be used to produce such alginate beads. A suspension is formed from the microorganisms to be immobilized and the alginate base material, which is then dripped into a precipitation bath. This is done via capillaries, which are set in vibration. Although the process described here can also be used to produce larger amounts of capsules, the immobilisates obtained are not suitable for including chemical substances due to the lack of an additional capsule membrane. The cells cannot grow out of the capsules either.

The PCT application PCT / CH96 / 00097 describes a similar process for the production of microcapsules which, in contrast to the above-mentioned production process, enables the beads to be prepared under sterile conditions, that is to say mainly provides capsules for the medical field. However, the immobilisates obtained with the device described here have the same shortcomings as those in the above method. Here too one can Cell growth cannot be guaranteed and chemical compounds such as proteins (enzymes) cannot be kept in the capsules.

F. Lim and A. Sun describe in “Science; Volume 210, pages 908-910; Born in 1980, a capsule with a semipermeable membrane for immobilizing living cells in which the capsule core is surrounded by a single layer of a ply-1-lysine / alginate complex. With these capsules, the cells are prevented from escaping from the capsule core. Because of its relatively low mechanical stability, this membrane capsule is not suitable for use in technical processes. Also, no molecules the size of an enzyme or smaller can be included because the membrane is permeable to it.

Patent specification P 43 12 970.6 describes a membrane capsule which is suitable for immobilizing enzymes and proteins, but also living cells. Here is the core, which contains the immobilizate, surrounded by a multilayer shell, each of these layers imparting a certain property to the entire shell. Through the advantageous choice of the shell polymers, the permeability of the membrane can be reduced so that enzymes also remain in the capsule, while the much smaller substrates and products can pass through the membrane. So far, however, these capsules can only be produced on a laboratory scale, i.e. in small quantities.

Starting from the known prior art, the invention has for its object to provide a method and an associated system that or that makes it possible for the first time to manufacture micro-membrane capsules in large quantities, that is, on an industrial scale. The solution of the disclosure of the invention is carried out with a method according to claim 1 and a system according to claim 26.

The manufacturing process according to the invention is therefore divided into two sections, namely the shaping and the coating.

During shaping, the material to be encapsulated is suspended or dissolved in a basic solution, preferably sodium alginate. This basic material suspension or solution is then conveyed into a coating reactor via a suitable device. This can either be done with compressed air, but pumps, screw conveyors etc. can also be used. This suspension or solution is then added dropwise to a precipitation bath

Ball shaped. This can be done either by complexing with a polyvalent salt solution as in the case of the alginate, or by changing physical parameters such as e.g. Temperature. When immersed in the precipitation bath, the

Liquid drops thus form the gel and enclose the material to be encapsulated.

Depending on the desired size, productivity and size distribution, several methods can be used to drop the liquid. For example, capillaries can be used in which the drop is torn off by an air stream, as in F. Lim and A. Sun in Science; Volume 210, pages 908-910, year 1980. This gives capsule sizes between approx. 200 μm and approx. 2 mm with a very narrow size distribution. To ensure sufficient productivity, several nozzles are arranged on a nozzle plate incorporated in the reactor. Another usable method for droplet generation is that described in patent application DE 3836894. Several capillaries are vibrated here, which leads to the liquid jets being broken down into individual drops. Such nozzle plates can be introduced into the reactor. The capsules obtained here also have a diameter between approximately 200 μm and approximately 2 mm, the productivity being significantly higher than in the case of the above-mentioned nozzles, but with a much broader size distribution.

Very small particles, in the range from approx. 20 μm to approx. 200 μm, are obtained by spinning on a turntable. Here, however, the flight cone of the drops must be taken into account when designing the reactor, so that they get into the precipitation bath and do not get caught on the walls.

The resulting gel particles are coated by immersing them in the respective coating solutions. These are dilute aqueous solutions of polymers with anionic or cationic groups such as chitosan, polyvinylpyrrolydone, polyethyleneimine, carbocymethyl cellulose, alginate, polyacrylic acid, etc., which form so-called polyelectrolyte complex layers on the capsule surface. By repeatedly immersing the particles in these solutions, several layers of the capsule shell are formed. In order to prevent the beads from sticking during the coating and thus to ensure optimal membrane formation, they must be kept in suspension. This can be done according to the invention by stirring with special agitators, so-called Visco-Jet stirrers, but it is also possible to introduce the coating reagents into the reactor tangentially and at high speed, so that a movement of the liquid which swirls the capsules is achieved, similar to a hydrocyclone. In addition can be washed in between with a suitable detergent. The required coating or washing solutions are in storage tanks and can either be ready for use or as a concentrate.

The manufacturing process takes place at approx. 25 ° C and atmospheric pressure. Nevertheless, a temperature control option can be provided for the reactors to heat the liquids up to approx. 65 ° C or to cool them down to approx. 5 ° C if necessary.

Fig. La; 1b; 2a: 2b; 3a; and 3c show several exemplary embodiments of the method and the associated plants for the large-scale production of membrane capsules.

In the systems shown in FIGS. 1 a and 1 b, all of the solutions in the storage containers are ready for use, ie in a diluted form. It works in two separate reactors, one for shaping and one for coating.

2a and 2b., Which also have two reactors, only the precipitation reagent is stored in dilute form, while the coating reagents are present as concentrates which are subsequently diluted.

3a and 3b show variants of a plant which only works with one reactor and in which, as shown in FIG. 3b, all the reagents used in the process can initially be present as concentrates.

Of course, other variants are also conceivable, which consist of combinations of the system diagrams shown in the figures. The designs with two reactors are characterized by higher productivity, since the beads can be coated while the dropletization of the liquid, i.e. the shaping, continues.

The variants with one reactor therefore have lower productivity, but are simpler and less expensive to implement.

In all of the versions described, a suspension of the material to be encapsulated and the basic material solution is first prepared and poured into the pressure vessel GS. By opening the valve RV, the vessel is pressurized (approx. 8-10 bar), whereby the suspension is pressed into the corresponding reactor via the open valve V. This can be FR or R depending on the system. The vessel GS can be additionally ventilated by means of an additional valve BV, which is shown in some embodiments according to the invention. The liquid must be transported using compressed air so that the material to be encapsulated is not damaged. However, other gentle systems such as suitable pumps or screw conveyors can also be used.

In the appropriate reactor (FR or R), the suspension is broken down into individual drops using a suitable device. Due to the precipitation reagent into which the drops fall, they gel into gel particles. The size of the resulting particles depends on the dropletisation process used. The volume flow of the basic material suspension is regulated via RV. Depending on the variant, the precipitation reagent can get from the storage vessel FB into the reactor FR or R in different ways. Since the liquid is introduced tangentially in all cases, the gel particles are swirled, so that additional stirring is not necessary. The suction tube must be provided with a filter so that no capsules are sucked in. The solutions can be tempered by means of the heat exchanger WT1 or WT.

In the embodiment shown in FIG. 1 a, the precipitation reagent is conveyed into the shaping reactor FR by opening the valve V17, V19, and V22 and by pumping via the pump P1. After reaching a corresponding level in FR, V17 and VI9 are closed and V20 is opened, whereby the solution circulates in a circle. After the gel particles formed have spent a few minutes in the precipitation bath, the solution is pumped back to FB by closing V22 and opening V21 and V18. The beads are then washed with DI water by closing V18 and V21 and by opening V15, V19 and V22, which, like the precipitation reagent, is first circulated by means of an analog valve position and then by closing V22 and opening V21 and V16 Part is pumped out again. The gel particles formed are then conveyed as an aqueous suspension into the coating reactor BR by gravity by opening the ball valve KHL.

In the embodiment according to the invention shown in FIG. 2a, this method step takes place analogously to that in FIG. 1 a, but here the 2-way valves VI9 and V20 or V21 and V22 from FIG. 1 a have been replaced by correspondingly arranged 3-way valves V15 and V12 , V17 and V18 or V15 and V16 from la correspond to valves V13 and V14 or V8 and Vll. Likewise analogous to the system shown in variant 1a, this first method step proceeds according to the invention in the embodiment shown in FIG. 3a. V15 and VI6; V17 and V18; V19 and V20; V21 and V22 from the system shown in FIG. 1 a correspond to valve pairs VI and V2; V15 and V16; V17 and V18; V19 and V20. Since the variant in FIG. 3a works with a single reaction vessel R, there is no need to rinse out the capsules in the coating reactor. The wash water is completely pumped out here after the hardening of the gel balls formed, since the coating is carried out in the same vessel.

In the case of FIGS. 1b and 2b. represented variants can thanks to the presence of two pumps (Pl and P2) the precipitation reagent with the appropriate position of the valves V13 and V14 in Fig. lb or V10 and Vll in Fig. 2b, ^■ during the entire first step of the process from the reservoir FB to Reactor FR can be pumped back and forth to FB. Since the precipitation bath in FR is constantly renewed in this way, the active substance concentration in the precipitation bath remains almost constant during this entire first process step. After a few minutes of curing time, the beads are also washed with di-water in the variants shown here by switching the valves V13 and V14 (Fig. Lb) or V10 and Vll (Fig. 2b). Thanks to the two pumps Pl and P2, the reaction vessel can always be supplied with new water and does not have to be circulated as in the variants shown in FIGS. 1a, 2a and 3a.

The embodiment shown in Fig. 3b does not work with ready-to-use solutions but with concentrates that have to be diluted first. For this purpose, before the beginning of the dropping in via the valve V8, the filter F and the valve V10 by means of the pump P via the Mixing chamber MK and the heat exchanger WT di-water passed into the reaction vessel R. With the appropriate level, V8 is closed and V9 is opened so that the water circulates in a circle. The quantity of concentrate corresponding to the desired final concentration is then metered in from V4. The suspension in reaction vessel R is then dripped from GS. As already described for the embodiment shown in FIG. 3a, the beads remain in the reactor R after they have hardened.

After the beads have hardened, the second process step, coating, takes place. In all embodiments according to the invention, this is done by rinsing the capsules alternately with a cationic and an anionic, dilute polymer solution. Wash steps are provided in between. The ^'particles are each exposed to the solutions for a few minutes, which can be pumped back into the Vorratsbehäter. It is important that the capsules are kept in a kind of fluidized bed during the entire process, so that the membrane can form all around. This can be done by means of special agitators, or, as shown in the present explanations, by tangentially introducing the solutions at a relatively high speed, which should be several meters per second at the pipe outlet opening. The liquids can be tempered via the appropriate heat exchangers WT2 or WT. When the coating is complete, the finished membrane capsules are washed and rinsed out of the reaction vessel. A drying step can then be carried out, whereby the water is removed from the capsules. The selected drying process is largely determined by the material enclosed in the capsules. In the embodiment shown in FIG. 1 a, the first coating reagent, the polycation 1, is conveyed from the storage vessel PK1 into the coating reactor BR by opening the valve V3, V23, and V26 and by pumping via the pump P2. After reaching a corresponding level in BR, V3 and V23 are closed and V24 is opened, whereby the solution circulates in a circle. After the gel particles formed have spent a few minutes in the coating bath, the solution is pumped back to PKI by closing V26 and opening V25 and V4. The beads are then washed with di-water by closing V4, V24 and V25 and by opening VI, V23 and V26, which, like the precipitation reagent, is first circulated through an analog valve position and then by closing VI, V23 and V26 and opening V2, V24 and V26 is pumped out again. By switching the corresponding valves, the reactor BR is then rinsed in an analog circuit with the detergent solution from the storage tank E, and then with the first polyanion from the container PA1, which is followed by 2-3 washing steps. The reactor is then supplied from the PK2 vessel with the second polycationic solution, which is then pumped back there. This process is carried out in the same way with the appropriate reagents. Repeat from the storage containers PA2 (second polyanion) or PA3 (third polyanion) until the desired membrane is built up. The membrane capsules are then rinsed out of the reactor by opening the ball valve KH2.

In the embodiment according to the invention shown in FIG. 3a, this method step takes place analogously to that in FIG. 1a, but here the coating is carried out in the same vessel R as the shaping. 3a corresponds to V17 and V18, V23 and V24 from la, or V19 and V20, V25 and v26 from FIG. When the coating is complete, the finished capsules are rinsed out of the reactor by opening the KH ball valve.

In the Fig. Lb. represented variant, thanks to the presence of two pumps (P3 and P4), the coating reagents can always be pumped back and forth from the storage containers to the reactor BR during the entire process step if the valves are in the appropriate position. Since the coating baths in BR are constantly renewed in this way, the active substance concentrations in the reactor remain almost constant during this entire process step. In order to supply the reactor BR with the cationic reagent PK1, for example, the valves VI and V2 are opened and V15, 17 and V16 are switched accordingly. The pump P4 pushes the liquid into the reactor P3 and returns it to the storage tank. The liquid level in BR is set via the corresponding control of the two pumps. By opening and closing the respective valves in the appropriate order, the

Coating reactor with the coating reagents from E

(Detergent), PA1 (polyanion 1), PK2 (polycation 2) etc. By opening KH2 you will be finished

Coating rinsed out the capsules.

The embodiment variants shown in FIGS. 2a and 2b do not work with ready-to-use solutions but with concentrates which first have to be diluted. For this purpose, before the start of the first coating process via valve VI, filter F and valve V10 (FIG. 2a) or V9 (FIG. 2b) by means of pump P2 (FIG. 2a) or P3 (FIG. 2b) passed through the mixing chamber MK and the heat exchanger WT2 di-water into the reaction vessel R. With the appropriate level, V7 is closed and V9 (Fig. 2a) or V8 (Fig. 2b) opened so that the water circulates in a circle. The amount of polycation 1 concentrate corresponding to the desired final concentration is then metered in via VI from PKl and the solution is circulated. After the dwell time in the first coating solution has expired, V9 (FIG. 2a) or V8 (FIG. 2b) is opened and V10 (FIG. 2a) or V9 (FIG. 2b) is changed over and the solution is discarded. Then the reactor BR is again filled with water via V7 and the detergent is removed from the vessel E and then discarded. In the same way, the beads are washed around with the other coating solutions, the concentrates of PA1 (polyanion 1), PK2 (polycation 2) etc. being metered in. The capsules are rinsed out by opening KH2 after the coating has been completed.

In the variant according to the invention shown in FIG. 3b, the coating process takes place analogously to the explanations given in FIGS. 2a and 2b. The difference is that coating is carried out in the same vessel R in which the dropletization (shaping) of the suspension has previously taken place. V4, V5, V6, V7 from Fig. 2a. correspond to the valves V5, V6, V7, V8.

Claims

claims

1. A process for the preparation of micro-membrane capsules for immobilizing chemical agents, proteins, living cells and / or microorganisms on an industrial scale, characterized in that the material to be encapsulated in one

Raw material dissolved or suspended form is conveyed from a storage container into a reactor, from which drops are generated and balls are formed by their precipitation, which enclose the material and which in turn are subsequently coated in the same and / or another vessel by repeated rinsing.

2. The method as claimed in claim 1, several or all of the following steps, which can also be repeated several times:

Dissolving or suspending the material to be encapsulated in a base material - dropletization of this base material suspension or

solution

Cases of drops

Rinse and suspend the precipitates in a washing liquid

Flushing the beads with a polycationic polymer solution and forming a cationic charge on the surface of the ball Wash the beads with a washing liquid - Wash the beads with a detergent solution - Rinse the beads with a polyanionic polymer solution and form an anionic charge on the surface of the beads

Rinse and suspend the precipitates * in one

Washing liquid drying the beads

3. The method of claim 1 and 2, d a d u r c h g e k e n n z e i c h n e t that the base material is a soluble natural material or plastic.

4. The method according to claim 3, d a d u r c h g e k e n n z e i c h n e t that the base material is a ceramic or a wax.

5. The method according to any one of claims 1 to 4, that the base material is conveyed into a device for droplet generation by a mechanical aid, preferably a screw conveyor or a pump.

6. The method according to any one of claims 1 to 5, characterized in that the base material is conveyed pneumatically into a device for generating drops.

7. The method according to any one of claims 1 to 6, so that the device for droplet formation is part of a reaction vessel

8. The method according to any one of claims 1 to 7, so that drops are formed from the base material by vibration, by an air stream, by a rotational movement (centrifugal forces) and / or by emulsification.

9. The method according to any one of claims 1 to 8, d a d u r c h g e k e n n z e i c h n e t that the drops formed chemically, e.g. be precipitated by the influence of salts.

10. The method according to any one of claims 1 to 8, d a d u r c h g e k e n n z e i c h n e t that the drops formed physically, e.g. be precipitated by temperature change.

11. The method according to any one of claims 1 to 10, such that the precipitated drops contain the material to be immobilized.

12. The method according to any one of claims 1 to 11, so that the precipitated drops are kept in suspension in the precipitation bath.

13. The method according to any one of claims 1 to 11, characterized in that the precipitated drops in the precipitation bath are kept in suspension by stirring.

14. The method according to any one of claims 1 to 11, so that the precipitated drops are kept in suspension in the precipitation bath by the flow rate of the surrounding medium.

15. The method according to any one of claims 1 to 14, so that the precipitated drops are coated by rinsing with suitable polymer solutions.

16. The method according to any one of claims 1 to 15, d a d u r c h g e k e n e z e i c h n e t that the precipitated drops are kept in suspension during coating

17. The method according to claim 16, so that the precipitated drops are kept in suspension during the coating by stirring.

18. The method according to claim 16, so that the precipitated drops are kept in suspension by the flow rate of the surrounding medium during the coating.

19. The method according to any one of claims 1 to 18, characterized in that the coated beads have a shell, which completely encloses the core and thus the encapsulated material.

20. The method of claim 19, so that the envelope of the coated spheres consists of one or more radially arranged layers.

21. The method according to claim 20, so that layers of the shell can be regions of different densities. "

22. The method according to any one of claims 1 to 21, that the coated beads are stored and used undried, that is to say moist, in a moist manner.

23. The method according to any one of claims 1 to 21, d a d u r c h g e k e n n z e i c h n e t that the coated beads are freeze-dried.

24. The method according to claim 1 to 21, d a d u r c h g e k e n n z e i c h n e t that the coated beads are air dried.

25. The method according to any one of claims 1 to 24, d a d u r c h g e k e n n z e i c h n e t that used for felling and / or coating

Solutions either as concentrates or ready to use, in diluted form.

26. Installation for carrying out the method according to one of the preceding claims, that a d u r c h g e k e n n z e i c h n e t that it has at least the following main components:

- Storage container for the basic material and the material to be immobilized (GS)

- Reservoir for the precipitation bath (FB)

- Storage container for a washing solution, preferably detergent (E)

- Storage containers for the coating polymers (PKl, PK2, PA1, PA2, PA3)

- Reaction vessel for dropletization and precipitation of the basic solution or suspension (FR, R)

- reaction vessel for coating the precipitated beads (BR, R)

- Device for drying the coated beads

- Heat exchanger for tempering the reaction vessels (WT1, WT2, WT)

- Pumps (Pl, P2, P) and valves (VI, V2, ...) for filling and emptying the

Reaction vessels, as well as ball valves (KHl, KH2, KH) and a mixing chamber (MK).

27. System according to claim 26, so that its components are arranged and / or connected to one another as shown in FIG.

28 Installation according to claim 26, characterized in that its components are arranged according to FIG. 1b and / or are connected to one another.

29. System according to claim 26, so that its components are arranged and / or connected to one another according to FIG. 2a.

30. System according to claim 26, so that its components are arranged and / or connected to one another according to FIG. 2b.

31. The system as claimed in claim 26, so that its components are arranged and / or connected to one another according to FIG. 3a.

32. System according to claim 26, so that its components are arranged and / or connected to one another according to FIG. 3b.