WO1985002972A1 - Coating hydrogel capsules - Google Patents
Coating hydrogel capsules Download PDFInfo
- Publication number
- WO1985002972A1 WO1985002972A1 PCT/US1985/000045 US8500045W WO8502972A1 WO 1985002972 A1 WO1985002972 A1 WO 1985002972A1 US 8500045 W US8500045 W US 8500045W WO 8502972 A1 WO8502972 A1 WO 8502972A1
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- WIPO (PCT)
- Prior art keywords
- capsule
- membrane
- recited
- vinyl acetate
- capsules
- Prior art date
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Classifications
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01H—NEW PLANTS OR NON-TRANSGENIC PROCESSES FOR OBTAINING THEM; PLANT REPRODUCTION BY TISSUE CULTURE TECHNIQUES
- A01H4/00—Plant reproduction by tissue culture techniques ; Tissue culture techniques therefor
- A01H4/005—Methods for micropropagation; Vegetative plant propagation using cell or tissue culture techniques
- A01H4/006—Encapsulated embryos for plant reproduction, e.g. artificial seeds
-
- A—HUMAN NECESSITIES
- A01—AGRICULTURE; FORESTRY; ANIMAL HUSBANDRY; HUNTING; TRAPPING; FISHING
- A01C—PLANTING; SOWING; FERTILISING
- A01C1/00—Apparatus, or methods of use thereof, for testing or treating seed, roots, or the like, prior to sowing or planting
- A01C1/06—Coating or dressing seed
Definitions
- This invention relates to the production of membranes for coating hydrogel capsules, and more particularly to membranes which control solute and solvent migration between tfie capsule and its environment.
- the capsule to be coated is a hydrogel capsule intended to contain living material, notably botanic tissue, such as seeds, somatic embryos and other meristematic tissue.
- the membrane must allow respiration by the tissue contained in the capsule, thus an impermeable capsule is undesirable.
- the capsule retains sufficient moisture and solutes for tissue viability.
- the capsule and membrane are often desirably a temporary container for encapsulated tissue, and they will deteriorate or fracture at the desired time for emergence of the tissue, such as e.g. germination.
- an object of this invention is to provide methods and compositions which control the passage of solvents between hydrogel capsules and their environment.
- Another object of the invention is to provide methods and compositions whereby the passage of solutes into and out of hydrogel capsules is controlled.
- Yet another object of the invention is to provide coatings around hydrated capsules which will break down under septic conditions.
- a further object of this invention is to provide hydrogel capsules which can be handled as flowable, non-adherant units.
- An additional object of the invention is to provide a method whereby coated hydrogel capsules can be stored for an extended time period without substantial water loss from the capsule.
- improved methods and membranes are provided for coating hydrogel cap ⁇ sules used for encapsulating material.
- One aspect of the invention provides a method for encapsulating material and ' separating the material from its environ ⁇ ment comprising encapsulating the material in a hydrogel capsule and surrounding the capsule with at least one membrane which controls the migration of solutes or solvents between the capsule and the environment.
- Another aspect of the invention provides a capsule membrane which comprises at least one coating surround ⁇ ing the capsule which reduces the flow of solvents or solutes between the capsule and its environment.
- hydrogel capsules are produced with controlled-reiease membranes .by .coating the...capsules with specific polymers, binders and solvents. . ...-; ; _• -
- the invention provides specific polymers and other compounds which are hydr'ophobic and therefore prevent passage of water when the compounds are formulated as sheets or films. By controlling the passage of water, the present invention also controls the passage of aqueous solutes.
- the hydrophobic membranes provided will individualize the capsules and minimize capsules ' adhesions.
- the coating can break down at an appropriate point in time to release the capsule contents.
- the invention is particularly advantageous in creating a protective, solvent-controlling, ⁇ ontrolled-release membrane around hydrogel capsules.
- Individual capsule particles may be produced from a wide variety of hydrogel polymers.
- Such gels in an uncoated state should allow acceptance, containment and release of specific solvents, solutes and other adjuvants as well as diffusion of gases.
- the gel should provide an environment .strong enough to resist external abrasion and adverse forces, yet pliable enough to allow release of internal components and breakdown of the hydrogel at the appropriate time. It may be desirable to use various gels in combination, either as a mixture, as layers or as discrete regions to achieve the desired results.
- Hydrogel capsules made from sodium alginate complexed with calcium contain approximately 90% water. When stored, the water gradually evaporates because calcium alginate is permeable to water. When stored under refrigeration, this water collects in the container, causing the capsules to adhere to the container and each other.
- Gels which have been found useful for encapsulat ⁇ ing solvents, solutes and other adjuvants include sodium alginate, guar gum, carrageenan with locust bean gum, sodium alginate with gelatin, carboxymethylcellu- lose, gum tragacanth, sodium pectate and vinyl acetate.
- Other suitable gels include, but are not limited to:
- Inorganic Compounds 1. Clay 2. Compounds which adhere by means of a water-soluble plastic such as methyleel: Fly Ash Feldspar Celrite
- a sodium alginate solution for example, will form a gel when ⁇ a—complexing agent is added.
- Calcium chloride (CaCl_) is generally used, however, lanthanum chloride, ferric chloride, cobaltous chloride, calcium nitrate, calcium hydroxide, superphosphate fertilizer, and many pesticides such as benefin, alachlor and chlorpropham are also acceptable, as are other multivalent cation compounds.
- the coated hydrogel capsules of the present invention will find use as delivery systems for, e.g. living material including eukaryotic cells, micro-organisms and botantic tissue such as seeds, somatic embryos and other meristematic tissue capable of developing into an entire plant body.
- living material including eukaryotic cells, micro-organisms and botantic tissue such as seeds, somatic embryos and other meristematic tissue capable of developing into an entire plant body.
- numerous adjuvants may be encapsulated within the capsules of the present invention, either separately or in combination with each other and with encapsulated living material.
- a chosen gel will have a range of concentrations usable in working the invention.
- a concentration should be chosen to optimize ease of handling, gelling time, strength of gel and coating thickness around the encapsulated material. If the gel is too dilute, the encapsulated material can settle during gel formation and produce an uneven encapsulation.
- the sodium alginate may be prepared in a concen ⁇ tration of 1 to 10% w(in grams)/v(in milliliters) in water, more usually 2 to 10% and ideally from 3 to 5%.
- Specific adjuvants to be encapsulated may be mixed with the sodium alginate at concentrations specific for the application rates of the particular adjuvants. The dispersed adjuvants in gel solution may then be added dropwise to the complexing agent.
- the gel solution and complexing agent may be mixed by any of numerous .techniques known to the art. These may include- droplet formation and agent addition as a one step process by a vibrating nozzle which ejects a gel droplet from one source and coats the droplet with complexing agent from another.
- the calcium chloride (or other complexing agent) may be made up in solution at a concentration of 1 to 1,000 millimolar, more usually 20 to 500 millimolar and ideally from 50 to 300 millimolar. Other complexing agents will have different preferred concentration ranges.
- the time for gel formation and temperature of the gelling solutions are interrelated parameters, for selected concentrations of gel and complexing agent.
- the temperature should be chosen in the range of 1 to 50 ⁇ C, more usually 10 to 40 ⁇ C, and preferably at 20 to 40 ⁇ C.
- a particular value may be chosen to give the shortest possible gelling time consistent with complete gel formation. Typically, the gel will form immediately, but the complexation takes much longer.
- a solution of sodium alginate at a concentration of 3.2 grams per 100 milliliters H_0, calcium chloride solution concentration of 50 millimolar, and 25 ⁇ C reaction temperature adequate gelling is obtained in 5 to 120 minutes, more often 10 to 90 minutes and is usually sufficiently complete in 30 to 60 minutes.
- gelation time is decreased to 2-5 minutes. 5
- the gel characteristics described above are modifiable for each gel, but are determined generally by the concentration parameters and chemical properties of the -gel.
- the encapsulated adjuvants can be coated with a membrane resistant to water or solvent
- the membrane should be semipermeable to impede the release of the capsule contents or impermeable to the contents with release being "effected via microbial degradation ⁇ temperature or pH changes, or other physical or biological effects.
- the 20 can also influence the handling properties of the capsules, particularly the flowability of the capsule.
- the coating materials selected to provide membranes for hydrogel capsules will ideally produce membranes with these desirable properties:
- the membrane will be relatively water- impermeable.
- the membrane will adhere to the hydrogel capsule.
- the membrane will optionally be 0 biodegradable.
- hydrophobic substances can be used as water-impermeable membranes when used separately, as mixtures or when combined with polymeric binders, such as e.g. ethylene-vinyl acetate copolymers, and cellulose derivatives.
- a chosen polymer will have a range of concen ⁇ trations usable in working the invention.
- a concentration should be chosen to optimize ease of handling, viscosity, solubility and membrane thickness. If the polymer concentration is too low, the membrane will be readily permeable to water. If too thick, the optionally included meristematic tissue may not germinate.
- the Elvax 4260® may be prepared in a concentration of 1 to 50% w ⁇ in grams)/v(in grams) in cyclohexane, more usually 5 to 20% and preferably 8 to 12%.
- This Elvax solution is then mixed with stearic * acid, cetyl alcohol, and petroleum ether (60-110 ⁇ C boiling point) at concentrations of optionally .01 to 5.0 grams, .01 to 5.0 grams and .1 to 20 grams, respectively, more usually .1 to 1.0, .1 to 1.0 and .5 to 10.0 grams, respectively to produce a polymer solution.
- Capsules containing various material and adjuvants are pretreated with calcium hydroxide at a concentration of .001 to 1.0 grams " per gram water, more usually 0.01 to 0.1 grams per gram.
- the pretreat ent solution is applied to the capsules at a concentration of 0.5 to 20.0 grams pretreatment solution per gram capsules, more usually 1 to 10 grams per gram.
- the capsules are immersed and stirred for 1 to 30 minutes, more usually 3 to 10 minutes in the polymer solution at ambient temperature, 20 to 35°C, more usually 25 to 30°C. Subsequently, the capsules are stirred 1 to 30 minutes, more usually 3 to 10 minutes at 0 to 10 ⁇ C, more usually 3 to 8°C. The capsules are filtered to remove excess polymer solution and. then air dried.
- the polymer solution may be replaced with a solution of 0.05 to- 10.0 grams, more usually 0.5 to 5.0 grams of a 1 to 20%, more usually 5 to 15% Elvax 310 ® (ethylene vinyl acetate copolymer) in high boiling point petroleum ether mixed with .001 to 2.0 grams each of stearic acid and cetyl alcohol, more usually 0.01 to 1.0 grams each.
- Elvax 310 ® ethylene vinyl acetate copolymer
- the polymer solution may be replaced with 0.01 to 10.0 grams, more usually 0.1 to 5.0 grams of .50 to 10%, more usually 1 to 5% aluminum monostearate in toluene mixed with .001 to .10 grams, more usually .01 to .10 grams stearic acid.
- a second coating may be applied consisting of 0.01 to 10.0 grams, more usually 0.1 to 5.0 grams of .5 to 10%, more usually 1 to 5% aluminum tristearate in toluene mixed with .01 to 5.0 grams, more usually .10 to 1.0 grams of .50 to 20%, more usually 5 to 15% Elvax 4260 ® in cyclohexane.
- the polymer solution may be replaced with .10 to 10 grams, more usually .50 to 2.0 grams of methylvinyl ether/maleic anhydride copolymer, high molecular weight, dissolved in 5 to 100 milliliters, more usually 10 to 50 milliliters of anhydrous butanol. One drop of sulfuric acid is added 5 to the mixture. This solution is refluxed for 20 to 30 hours at 100 to 120 ⁇ C.
- Gantrez ES- 435® or ES-425® may be used.
- coating compounds which can be used in the 10 present invention to form membranes include, without limitation: •
- Methylvinyl ether/maleic anhydride 15 Methylvinyl ether/maleic anhydride 15 .
- the capsules were sprayed with the solution of coating compound and the beaker agitated by hand to ensure uniform spraying.
- This procedure consisted of the following steps: 1. The capsules were immersed in the coating compound solution, generally at 30" to 35 ⁇ C. 2. The mixture was stirred 5 min at room temperature and 5 min in an ice-water bath at 10 ⁇ C. 3. The capsules, were filtered, rinsed with low-boiling petroleum ether, and dried with pressurized air or nitrogen.
- the capsules were placed on a basket or bag. (A basket made of polypropylene mesh was used initially, but a bag made of a nylon mesh was found more convenient because of its " flexibility.)
- the bag with the capsules was dipped into the coating compound solution, and agitated to ensure that all the capsules were coated.
- Example A Coating Capsules Containing Alfalfa Seeds
- 500 alfalfa seeds, Saranac AR Lot #27-07-765 (Whitney Dickenson Seed Growers, Homedale, Idaho), were mixed with 200 milliliters of 3.2% sodium alginate. This solution was added drop-wise into 500 milliliters of 100 millimolar calcium chloride to complex the alginate and form spheroid capsules. 40 grams- of the capsules were stirred in 8 grams of lime water .
- the alfalfa seeds imbibed water from the alginate capsule, germinated, and emerged from the capsules undamaged.
- A.l As an alternative polymer solution, 40 grams of 2% aluminum monostearate in toluene plus 2 grams stearic acid can be used. A.2. As another alternative polymer solution, 5.2 grams of spermaceti wax substitute #573, 2 grams cetyl alcohol, 1 gram stearic acid, 10 grams of a 10% solution of Elvax 4260 ® in cyclohexane, and 40 grams of high boiling point petroleum ether can be used. A.3. As a further alternative polymer solution, 4 grams of stearic acid, 4 grams of cetyl alcohol, and 40 grams of a 10% solution of Elvax 310® (ethylene vinyl acetate copolymer) in high boiling point petroleum ether can be used.
- Elvax 310® ethylene vinyl acetate copolymer
- A.4 As another alternative polymer solution, 2 grams of stearic acid plus 40 grams of a 2% solution of aluminum monostearate in toluene can be used as a first coating. A second coating can then be applied consisting of 32 grams of a 2% solution of aluminum tristearate in toluene mixed with 10 grams of a 10% solution of Elvax 4260® in cyclohexane.
- Gantrez ES- 435® or ES-425® was mixed with alginate beads and dropped into water to form coated capsules.
- Example B Coating Capsules Containing Tomato Seeds
- UC-82 VGY9225, Asgrow
- UC-82 VGY9225, Asgrow
- UC-82 VGY9225, Asgrow
- the calcium * hydroxide solution was prepared by stirring 1 gram of calcium hydroxide in 100 milliliters of water for 15 minutes and then filtering the solution.
- the treated capsules were sieved through a nylon screen, patted dry, and dipped 6 times for 1-3 seconds each in the membrane coating solution.
- the capsules were blow- dried between dippings.
- the membrane coating solution consisted of the combination of the following 3 solutions: 2 grams Elvax 4260 ® dissolved in 20 grams cyclohexane, 10 grams of spermacetti wax substitute #573 melted with 4 grams cetyl alcohol and 2 grams stearic acid, and 80 grams each of petroleum ether (50-110°C) and methylene chloride.
- Capsules were planted under both greenhouse and field conditions.
- the membrane coated, encapsulated seeds had a 100% germination frequency in the greenhouse which was equal to the non-coated, encapsulated seeds and non-coated, non-encapsulated seeds.
- membrane-coated, encapsulated seeds had germination frequencies equal to non-coated, encapsulated seeds and better than non- coated, non-encapsulated seeds.
- B.l. As an alternative to encapsulation, non- encapsulated seeds were coated as described. Germination rates of coated seeds in the greenhouse equaled rates for non-coated seeds.
- Example C Coating Capsules Containing Alfalfa Somatic Embryos
- Alfalfa somatic embryos were produced as described by K. A. Walker and S. J. Sato (Plant Cell Tissue and Organ Culture 1:109-121, 1981) using a regeneration medium consisting of Shenk and Hildebrandt (SH) medium (R. V. Shenk and A. C. Hildebrandt, Canadian Journal of Botany 50:199-204, 1972), 100 millimolar proline, and 25 millimolar ammonium.
- SH Hildebrandt
- the somatic embryos were encapsulated as in Example A.
- the encapsulated embryos were then pretreated in a calcium hydroxide solution as in Example B followed by coating as in Example A.
- the coated, encapsulated somatic embryos were placed on one-half strength SH medium and incubated at 27°C under 16 hour light/8 hour dark conditions.
- the percent embryo viability, radicle emergence, and shoot/leaf emergence was statistically equal to that for non-coated, non-encapsulated somatic embryos and for non-coated, encapsulated somatic embryos. l.A. As an alternative, non-encapsulated alfalfa somatic embryos were coated. Percent embryo viability, radicle emergence, and shoot/leaf emergence was statistically equal to that for non-coated somatic embryos.
- the experimental protocol C.l. was duplicated, substituting a dipping process for the immersion coating method.
- the encapsulated alfalfa somatic embryos were placed in a nylon bag and dipped three times in the coating solution.
- the capsules were blow-dried and dipped three more times with a final blow-drying.
- the percent embryo viability, radicle, emergence, and shoot leaf emergence was statistically equal to that for non-coated, encapsulated somatic embryos.
- 2.A As an alternative, non-encapsulated somatic embryos were coated. Percent embryo viability, radicle emergence, and shoot/leaf emergence was statistically equal to that for non-coated somatic embryos.
- Example D Capsule Storage Capsules without seeds were coated as in protocol A and stored either in an open container or in a sealed vial. Initial water loss from the capsules during the coating process was 10% w/w of water per capsule. Subsequent water loss through the membrane for capsules stored in an open container was 0 over a 3-day period. B.l. As an alternative, a different sample retained
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Abstract
Methods and materials for coating hydrogel capsules to control the migration of solutes or solvents between the capsule and the environment. The membranes may be of a single compound or various compounds which provide control over the migration of distinct elements.
Description
Description Coating Hydrogel Capsules
Technical Field
This invention relates to the production of membranes for coating hydrogel capsules, and more particularly to membranes which control solute and solvent migration between tfie capsule and its environment.
Background of the Invention A conventional technique of coating hydrogel capsules is to construct a polylysine membrane around the capsule. See F. Lim, U.S. Patent 4,352,883. Other techniques involve methylcellulose compounds, polyvinyl alcohols, plastics, and other compounds. See L. Lachman, H.A. Lieberman and J.L. Kanig, eds. "The Theory and Practice of Industrial Pharmacy," Lea and Febiger, Philadelphia, PA, 1970, p. 197-225.
However, conventional membranes do. not control the passage of solvents, particularly water. An additional drawback is the failure to control the passage of small molecular weight solutes across the membrane, unless the membrane is rigid and virtually impermeable.
The above limitations are important when the capsule to be coated is a hydrogel capsule intended to contain living material, notably botanic tissue, such as seeds, somatic embryos and other meristematic tissue. In these applications the membrane must allow respiration by the tissue contained in the capsule, thus an impermeable capsule is undesirable. Yet it is important that the capsule retains sufficient moisture and solutes for tissue viability. Furthermore, the capsule and membrane are often desirably a temporary container for encapsulated tissue, and they will
deteriorate or fracture at the desired time for emergence of the tissue, such as e.g. germination.
In addition to the above limitations with available capsule coatings, in some applications it is desirable to provide a coated capsule which is not cohesive or adhesive, as this facilitates handling and bulk storage.
Disclosure of the Invention
Thus, an object of this invention is to provide methods and compositions which control the passage of solvents between hydrogel capsules and their environment.
Another object of the invention is to provide methods and compositions whereby the passage of solutes into and out of hydrogel capsules is controlled.
Yet another object of the invention is to provide coatings around hydrated capsules which will break down under septic conditions.
A further object of this invention is to provide hydrogel capsules which can be handled as flowable, non-adherant units.
An additional object of the invention is to provide a method whereby coated hydrogel capsules can be stored for an extended time period without substantial water loss from the capsule.
In accordance with the invention, improved methods and membranes are provided for coating hydrogel cap¬ sules used for encapsulating material. One aspect of the invention provides a method for encapsulating material and'separating the material from its environ¬ ment comprising encapsulating the material in a hydrogel capsule and surrounding the capsule with at least one membrane which controls the migration of solutes or solvents between the capsule and the environment.
Another aspect of the invention provides a capsule membrane which comprises at least one coating surround¬ ing the capsule which reduces the flow of solvents or solutes between the capsule and its environment.
Best Mode for Carrying Out the Invention
Briefly, in accordance with the invention, hydrogel capsules are produced with controlled-reiease membranes .by .coating the...capsules with specific polymers, binders and solvents. . ...-; ; _• - The invention provides specific polymers and other compounds which are hydr'ophobic and therefore prevent passage of water when the compounds are formulated as sheets or films. By controlling the passage of water, the present invention also controls the passage of aqueous solutes.
The hydrophobic membranes provided will individualize the capsules and minimize capsules ' adhesions.
Desirably, in accordance with the invention, the coating can break down at an appropriate point in time to release the capsule contents. The invention is particularly advantageous in creating a protective, solvent-controlling, σontrolled-release membrane around hydrogel capsules.
Selection of Hydrogels
Individual capsule particles may be produced from a wide variety of hydrogel polymers. Such gels in an uncoated state should allow acceptance, containment and release of specific solvents, solutes and other adjuvants as well as diffusion of gases. The gel should provide an environment .strong enough to resist external abrasion and adverse forces, yet pliable enough to allow release of internal components and breakdown of the hydrogel at the appropriate time. It
may be desirable to use various gels in combination, either as a mixture, as layers or as discrete regions to achieve the desired results.
Hydrogel capsules made from sodium alginate complexed with calcium contain approximately 90% water. When stored, the water gradually evaporates because calcium alginate is permeable to water. When stored under refrigeration, this water collects in the container, causing the capsules to adhere to the container and each other.
Gels which have been found useful for encapsulat¬ ing solvents, solutes and other adjuvants include sodium alginate, guar gum, carrageenan with locust bean gum, sodium alginate with gelatin, carboxymethylcellu- lose, gum tragacanth, sodium pectate and vinyl acetate. Other suitable gels include, but are not limited to:
TABLE 1. GEL AGENTS I. Natural Polymers
A. Ionic bonds (requires complexing agents) Alginate with Gelatin
Sodium Pectate Furcellaran Pectin Hypnean Dextran
Tamarind Guar Gum
B. Hydrophobic Interactions Amylose Agar
Agarose
Agar with Gelatin
Gelatin
Starch Amylopectin
Cornhull Gum
Starch Arabogalactan
Gum Ghatti . Gum Karagan Ti Gum
Gum Tragacanth
Wheat Gum
Chitin
Dextrin II. Chemically Modified Natural Polymers
A. Ionic bonds (requires a complexing agent)
Ethyl Succinylated Cellulose
Succinylated Zein
Carboxymethylceilulose B. Hydrophobic Interactions
Methylcellulose
Hydroxyethyl Cellulose C. Covalent Bonds
Gelatin with Glutaraldehyde III. Synthetic Polymers
A. Covalent Bonds Polyacrylamide
B. Hydrophobic Interactions Polyethylene Glyσol Polyvinylpyrrolidone
Polyoxyethylene
Hydrophilic Urethane
Polyvinylacetate
Vinyl Resins Hydron (hydroxyethylmethacrylate)
2-methyl-5-vinylpyri ine- methylacrylate-methacryliσ acid
C. Ionic Bonds
Sodium poly (styrene sulfonate) with poly(vinyl methyl pyridinium) chloride
Sodium poly (styrene sulfonate) with poly
(vinyl benzyl trimethyl ammonium) chloride Strongly acidic polyanion with strongly basic polycation Bordon Poly Co. 2113® (vinyl acetate homopolymer) (Bordon Co.)
Gelvatol® (polyvinyl alcohol resin) (Monsanto) IV. Stabilizing Compounds
A. Trade Names
Super Slurper® (USDA, SEA-AR, -Nor. Reg. Res. Lab)
-Viterra® (Union Carbide)
Laponite® (Laporte (United States) Inc.)
Gelrite® (Kelco)
SeaKem® (FMC Corporation) SeaPlaque® (FMC Corporation)
SeaPrep® (FMC Corporation)
IsoGel® (FMC Corporation)
B. Organic Compounds
Methylan Clear Wallpaper Paste Lactose
Wax Protein Colloids
C. Inorganic Compounds 1. Clay 2. Compounds which adhere by means of a water-soluble plastic such as methyleel: Fly Ash Feldspar Celrite
Bentonite Vermiculite Diatomaceous Earth Lime Calcium Carbonate
3. Other
Calcium Oxide Magnesium Carbonate . Sodium bicarbonate • Urea
Encapsulation with Selected Gel
Once the gel has been chosen, there are numerous parameters which influence the characteristics previously-.mentioned.
A sodium alginate solution, for example, will form a gel when~a—complexing agent is added. Calcium chloride (CaCl_) is generally used, however, lanthanum chloride, ferric chloride, cobaltous chloride, calcium nitrate, calcium hydroxide, superphosphate fertilizer, and many pesticides such as benefin, alachlor and chlorpropham are also acceptable, as are other multivalent cation compounds.
An important factor which influences the choice of gel agent, and other parameters, is the choice of encapsulated material. In general the coated hydrogel capsules of the present invention will find use as delivery systems for, e.g. living material including eukaryotic cells, micro-organisms and botantic tissue such as seeds, somatic embryos and other meristematic tissue capable of developing into an entire plant body. Alternatively, numerous adjuvants may be encapsulated within the capsules of the present invention, either separately or in combination with each other and with encapsulated living material.
A chosen gel will have a range of concentrations usable in working the invention. A concentration should be chosen to optimize ease of handling, gelling time, strength of gel and coating thickness around the encapsulated material. If the gel is too dilute, the encapsulated material can settle during gel formation and produce an uneven encapsulation.
The sodium alginate may be prepared in a concen¬ tration of 1 to 10% w(in grams)/v(in milliliters) in water, more usually 2 to 10% and ideally from 3 to 5%. Specific adjuvants to be encapsulated may be mixed with the sodium alginate at concentrations specific for the application rates of the particular adjuvants. The dispersed adjuvants in gel solution may then be added dropwise to the complexing agent. Alternatively, the gel solution and complexing agent may be mixed by any of numerous .techniques known to the art. These may include- droplet formation and agent addition as a one step process by a vibrating nozzle which ejects a gel droplet from one source and coats the droplet with complexing agent from another. The calcium chloride (or other complexing agent) may be made up in solution at a concentration of 1 to 1,000 millimolar, more usually 20 to 500 millimolar and ideally from 50 to 300 millimolar. Other complexing agents will have different preferred concentration ranges.
The time for gel formation and temperature of the gelling solutions are interrelated parameters, for selected concentrations of gel and complexing agent. The temperature should be chosen in the range of 1 to 50βC, more usually 10 to 40βC, and preferably at 20 to 40βC.
Within the range of acceptable temperatures, a particular value may be chosen to give the shortest possible gelling time consistent with complete gel formation. Typically, the gel will form immediately, but the complexation takes much longer. For a solution of sodium alginate at a concentration of 3.2 grams per 100 milliliters H_0, calcium chloride solution concentration of 50 millimolar, and 25βC reaction temperature, adequate gelling is obtained in 5 to 120 minutes, more often 10 to 90 minutes and is usually
sufficiently complete in 30 to 60 minutes. Alternatively, if 300 millimolar calcium chloride is substituted for 50 millimolar calcium chloride, gelation time is decreased to 2-5 minutes. 5 The gel characteristics described above are modifiable for each gel, but are determined generally by the concentration parameters and chemical properties of the -gel.
Coating the Capsules with Solvent/Solute J0„ Controlling embrane ~
Subsequent to capsule formation, it may be desirable to control permeability of the outer surface of the gel matrix. The encapsulated adjuvants can be coated with a membrane resistant to water or solvent
15 movement. The membrane should be semipermeable to impede the release of the capsule contents or impermeable to the contents with release being "effected via microbial degradation^ temperature or pH changes, or other physical or biological effects. This membrane
20 can also influence the handling properties of the capsules, particularly the flowability of the capsule.
The coating materials selected to provide membranes for hydrogel capsules will ideally produce membranes with these desirable properties:
25 1. The membrane will be relatively water- impermeable.
2. The membrane will adhere to the hydrogel capsule.
3. The membrane will optionally be 0 biodegradable.
4. The solvent systems (if necessary) and procedures used to apply the membrane will be relatively harmless to the material encapsulated by the hydrogel. 5 In general, hydrophobic substances can be used as water-impermeable membranes when used separately, as
mixtures or when combined with polymeric binders, such as e.g. ethylene-vinyl acetate copolymers, and cellulose derivatives.
For example, various polymers such as Elvax 4260® (ethylene vinyl acetate acrylic acid terpolymer,
DuPont, Wilmington, DE) will form coatings resistant to water penetration when mixed with stearic acid, cetyl alcohol, cyclohexane and petroleum ether. Capsules are pretreated with a calcium oxide solution and immersed in the polymer solution. In a similar manner other polymers can' be-used to coat capsules.
A chosen polymer will have a range of concen¬ trations usable in working the invention. A concentration should be chosen to optimize ease of handling, viscosity, solubility and membrane thickness. If the polymer concentration is too low, the membrane will be readily permeable to water. If too thick, the optionally included meristematic tissue may not germinate. The Elvax 4260® may be prepared in a concentration of 1 to 50% w<in grams)/v(in grams) in cyclohexane, more usually 5 to 20% and preferably 8 to 12%. One gram of this Elvax solution is then mixed with stearic* acid, cetyl alcohol, and petroleum ether (60-110βC boiling point) at concentrations of optionally .01 to 5.0 grams, .01 to 5.0 grams and .1 to 20 grams, respectively, more usually .1 to 1.0, .1 to 1.0 and .5 to 10.0 grams, respectively to produce a polymer solution. Capsules containing various material and adjuvants are pretreated with calcium hydroxide at a concentration of .001 to 1.0 grams" per gram water, more usually 0.01 to 0.1 grams per gram. The pretreat ent solution is applied to the capsules at a concentration of 0.5 to 20.0 grams pretreatment solution per gram capsules, more usually 1 to 10 grams per gram.
Following pretreatment, the capsules are immersed and
stirred for 1 to 30 minutes, more usually 3 to 10 minutes in the polymer solution at ambient temperature, 20 to 35°C, more usually 25 to 30°C. Subsequently, the capsules are stirred 1 to 30 minutes, more usually 3 to 10 minutes at 0 to 10βC, more usually 3 to 8°C. The capsules are filtered to remove excess polymer solution and. then air dried.
As an alternative to the pretreatment protocol, ; .0001 to 1.0 gram each of glucose and-glycerol, more usually .01 to .10 gram each are added to the calcium -hydroxide-sαlutioir before capsules are pretreated.
As an alternative to the polymer solution. Spermaceti Wax Substitute #573 (J. B. Ross Co., Jersey City, N.J.) can be added to the Elvax 4260® solution at a concentration of .001 to 2.0 gram per gram Elvax
4260® solution, more usually .01 to 1.0 gram per gram.
As a further alternative, the polymer solution may be replaced with a solution of 0.05 to- 10.0 grams, more usually 0.5 to 5.0 grams of a 1 to 20%, more usually 5 to 15% Elvax 310® (ethylene vinyl acetate copolymer) in high boiling point petroleum ether mixed with .001 to 2.0 grams each of stearic acid and cetyl alcohol, more usually 0.01 to 1.0 grams each.
As another alternative, the polymer solution may be replaced with 0.01 to 10.0 grams, more usually 0.1 to 5.0 grams of .50 to 10%, more usually 1 to 5% aluminum monostearate in toluene mixed with .001 to .10 grams, more usually .01 to .10 grams stearic acid. After applying this coating, a second coating may be applied consisting of 0.01 to 10.0 grams, more usually 0.1 to 5.0 grams of .5 to 10%, more usually 1 to 5% aluminum tristearate in toluene mixed with .01 to 5.0 grams, more usually .10 to 1.0 grams of .50 to 20%, more usually 5 to 15% Elvax 4260® in cyclohexane. As yet another alternative, the polymer solution may be replaced with .10 to 10 grams, more usually .50
to 2.0 grams of methylvinyl ether/maleic anhydride copolymer, high molecular weight, dissolved in 5 to 100 milliliters, more usually 10 to 50 milliliters of anhydrous butanol. One drop of sulfuric acid is added 5 to the mixture. This solution is refluxed for 20 to 30 hours at 100 to 120βC.
As an additional polymer alternative, Gantrez ES- 435® or ES-425® (GAF Corporation) may be used.
Other coating compounds which can be used in the 10 present invention to form membranes include, without limitation: •
TABLE 2. CAPSULE COATING COMPOUNDS
I. Enteric Coating
Methylvinyl ether/maleic anhydride 15. Styrene maleic acid copolymer
Styrene-maleic anhydride copolymer Ethylene/maleic anhydride copolymer
II. Hydrophobic Polymers Ethylcellulose
20 Isopropyl myristate
Polyvinyl acetate phthalate
Starch acetate phthalate
Amylose acetate phthalate
Cellulose acetate phthalate 25 Saran
Butyl rubber
III. Other Compounds Keratin Shellac
30 Carnuba wax Paraffin Wax Fats Lipids
Triglycerides
Ethylene vinyl acetate copolymer
Benzyl cellulose
Petrolatum
As an alternative »o immersing the capsules in the polymer solution numerous procedures for applying the coating, compound to form a hydrogel capsule membrane were used. ... .^
Spraying For this coating procedure an inlet tube was inserted into the lower side of a stainless steel beaker and the beaker covered with a polypropylene mesh attached to the nozzle of a spray gun. The cover was fastened to the beaker with a rubber band. This apparatus simulates a pan-spray tablet coater. The procedure consisted of the following steps:
1. The capsules were placed in the beaker and the cover- attached.
2. The capsules were sprayed with the solution of coating compound and the beaker agitated by hand to ensure uniform spraying.
3. The capsules were dried with pressurized air through the inlet tube, while agitating the beaker by hand. Steps 2 and 3 were repeated until a suitable coating was applied or the solution was exhausted. Because it was difficult to maintain adequate agitation during this coating process, a nylon mesh bag was substituted for the beaker. The bag was attached to the nozzle, the capsules were alternately sprayed and dried while frequently shaking the bag to uniformly deposit the coating on the capsules.
Immers ion
This procedure consisted of the following steps: 1. The capsules were immersed in the coating compound solution, generally at 30" to 35βC. 2. The mixture was stirred 5 min at room temperature and 5 min in an ice-water bath at 10βC. 3. The capsules, were filtered, rinsed with low-boiling petroleum ether, and dried with pressurized air or nitrogen.
*
Dipping
This procedure consisted of the following steps:
1. The capsules were placed on a basket or bag. (A basket made of polypropylene mesh was used initially, but a bag made of a nylon mesh was found more convenient because of its " flexibility.)
2. The bag with the capsules was dipped into the coating compound solution, and agitated to ensure that all the capsules were coated.
3. The bag was removed from the solution, and allowed to drain on a funnel.
4. The capulses were dried with a gentle flow of pressurized air. 5. Steps 2-4 were repeated three or four times and the capsules dried thoroughly with pressurized air.
Experimental
In order to demonstrate the invention, without implying limitations, the following experiments were carried out with a variety of coatings. All quantities labelled percent (%) are grams per 100 milliliters, unless otherwise indicated.
Example A (Coating Capsules Containing Alfalfa Seeds) 500 alfalfa seeds, Saranac AR Lot #27-07-765 (Whitney Dickenson Seed Growers, Homedale, Idaho), were mixed with 200 milliliters of 3.2% sodium alginate. This solution was added drop-wise into 500 milliliters of 100 millimolar calcium chloride to complex the alginate and form spheroid capsules. 40 grams- of the capsules were stirred in 8 grams of lime water . (containing .20 grams calcium hydroxide plus 1 gram each of glucose and glycerol) for one minute. The solution was "decanted and the capsules were immersed in a 30βC polymer solution containing 2 grams stearic acid, 2 grams cetyl alcohol, 10 grams of a 10% solution of Elvax 4260® (ethylene vinyl acetate acrylic acid terpolymer) in cyclohexane, and 40 grams of petroleum ether. The capsules were stirred for 5 minutes at room temperature followed by 5 minutes more in an icewater bath." The capsules were filtered through a nylon cloth, rinsed with 5 milliliters petroleum ether (30- 60°C), and dried with pressurized air. Subsequent to coating the encapsulated seeds, the alfalfa seeds imbibed water from the alginate capsule, germinated, and emerged from the capsules undamaged. A.l. As an alternative polymer solution, 40 grams of 2% aluminum monostearate in toluene plus 2 grams stearic acid can be used. A.2. As another alternative polymer solution, 5.2 grams of spermaceti wax substitute #573, 2 grams cetyl alcohol, 1 gram stearic acid, 10 grams of a 10% solution of Elvax 4260® in cyclohexane, and 40 grams of high boiling point petroleum ether can be used. A.3. As a further alternative polymer solution, 4 grams of stearic acid, 4 grams of cetyl alcohol, and 40 grams of a 10% solution of Elvax 310®
(ethylene vinyl acetate copolymer) in high boiling point petroleum ether can be used.
A.4. As another alternative polymer solution, 2 grams of stearic acid plus 40 grams of a 2% solution of aluminum monostearate in toluene can be used as a first coating. A second coating can then be applied consisting of 32 grams of a 2% solution of aluminum tristearate in toluene mixed with 10 grams of a 10% solution of Elvax 4260® in cyclohexane.
A.5. As a still further alternative, 10 grams of methylv'inyl ether/ maleic anhydride copolymer was refluxed in 50 milliliters of anhydrous butanol for 21 hours at 110βC. Subsequently, one drop of sulfuric acid was added to the solution. The solution was mixed with alginate-encapsulated alfalfa seeds and dropped into water to produce coated capsules.
A.6. As yet another alternative polymer; Gantrez ES- 435® or ES-425® (GAF Corporation) was mixed with alginate beads and dropped into water to form coated capsules.
Example B (Coating Capsules Containing Tomato Seeds) Six hundred tomato seeds, UC-82 (VGY9225, Asgrow) , were encapsulated in 2% w/v sodium alginate by dropwise complexation in 100 millimolar calcium chloride. Three hundred of these capsules were stirred one minute in 20 grams of a calcium hydroxide solution containing 1 gram of glucose and 2 grams of glycerol. The calcium * hydroxide solution was prepared by stirring 1 gram of calcium hydroxide in 100 milliliters of water for 15 minutes and then filtering the solution. The treated capsules were sieved through a nylon screen, patted dry, and dipped 6 times for 1-3 seconds each in the
membrane coating solution. The capsules were blow- dried between dippings. The membrane coating solution consisted of the combination of the following 3 solutions: 2 grams Elvax 4260® dissolved in 20 grams cyclohexane, 10 grams of spermacetti wax substitute #573 melted with 4 grams cetyl alcohol and 2 grams stearic acid, and 80 grams each of petroleum ether (50-110°C) and methylene chloride. Capsules were planted under both greenhouse and field conditions. The membrane coated, encapsulated seeds had a 100% germination frequency in the greenhouse which was equal to the non-coated, encapsulated seeds and non-coated, non-encapsulated seeds. In the field, membrane-coated, encapsulated seeds had germination frequencies equal to non-coated, encapsulated seeds and better than non- coated, non-encapsulated seeds. B.l. As an alternative to encapsulation, non- encapsulated seeds were coated as described. Germination rates of coated seeds in the greenhouse equaled rates for non-coated seeds.
Example C (Coating Capsules Containing Alfalfa Somatic Embryos) 1. Coating By Immersion
Alfalfa somatic embryos were produced as described by K. A. Walker and S. J. Sato (Plant Cell Tissue and Organ Culture 1:109-121, 1981) using a regeneration medium consisting of Shenk and Hildebrandt (SH) medium (R. V. Shenk and A. C. Hildebrandt, Canadian Journal of Botany 50:199-204, 1972), 100 millimolar proline, and 25 millimolar ammonium. The somatic embryos were encapsulated as in Example A. The encapsulated embryos were then pretreated in a calcium hydroxide solution as in Example B followed by coating as in Example A. The coated, encapsulated somatic embryos were placed on one-half strength SH medium and incubated at 27°C
under 16 hour light/8 hour dark conditions. The percent embryo viability, radicle emergence, and shoot/leaf emergence was statistically equal to that for non-coated, non-encapsulated somatic embryos and for non-coated, encapsulated somatic embryos. l.A. As an alternative, non-encapsulated alfalfa somatic embryos were coated. Percent embryo viability, radicle emergence, and shoot/leaf emergence was statistically equal to that for non-coated somatic embryos.
2. Coating By Dipping
The experimental protocol C.l. was duplicated, substituting a dipping process for the immersion coating method. The encapsulated alfalfa somatic embryos were placed in a nylon bag and dipped three times in the coating solution. The capsules were blow-dried and dipped three more times with a final blow-drying. The percent embryo viability, radicle, emergence, and shoot leaf emergence was statistically equal to that for non-coated, encapsulated somatic embryos. 2.A. As an alternative, non-encapsulated somatic embryos were coated. Percent embryo viability, radicle emergence, and shoot/leaf emergence was statistically equal to that for non-coated somatic embryos.
Example D (Capsule Storage) Capsules without seeds were coated as in protocol A and stored either in an open container or in a sealed vial. Initial water loss from the capsules during the coating process was 10% w/w of water per capsule. Subsequent water loss through the membrane for capsules stored in an open container was 0 over a 3-day period.
B.l. As an alternative, a different sample retained
93% water over a 10-day period. B.2. As an alternative, a further sample retained 75% water over a 30-day period.
Although the foregoing invention has been described in some detail by way of illustration for purposes of clarity of understanding, it will be understood that numerous modifications may be practiced within the spirit and scope of the appended claims.
Claims
1. A capsule membrane for hydrogel capsules encapsulating material and separating said material from its environment, which membrane comprises: at least one coating surrounding the capsule which reduces the flow of solvents or solutes between the capsule and its environment.
2. A capsule membrane as recited in Claim 1 wherein the encapsulated material is living material.
3. A capsule membrane as recited in Claim 2 - wherein the living material is plant meristematic tissue.
4. A capsule membrane as recited in Claim 1 or 3 wherein the capsule further comprises a gel matrix comprising at least one agent selected from the group consisting of sodium alginate, guar gum, carrageenan with locust bean gum, sodium alginate with gelatin, carboxymethylcellulose, gum tragacanth, sodium pectate, vinyl acetate and hydrogel agents identified in Table I.
5. A capsule membrane as recited in Claim 1 or 3 wherein the membrane further comprising at least one compound selected from the group consisting of ethylene vinyl acetate acrylic acid terpolymers, ethylene vinyl acetate copolymers, spermaceti, aluminum stearates, methyl vinyl ether/maleic anhydride copolymers, ethyl cellulose, ethylhydroxyethyl cellulose, stearic acid, glyceryl monooleate, cetyl alcohol, calcium stearate and compounds identified in Table II.
6. A capsule membrane as recited in Claim 4 wherein the membrane further comprising at least one compound selected from the group consisting of ethylene vinyl acetate acrylic acid terpolymers, ethylene vinyl acetate copolymers, spermaceti, aluminum stearates, methyl vinyl ether/maleic anhydride copolymers, ethyl cellulose, ethylhydroxyethyl cellulose, stearic acid, glyceryl monooleate, cetyl alcohol and calcium stearate.
7. A capsule membrane as recited in Claim 1 or 3 wherein the capsule further comprises a gel matrix comprising at least one agent selected from the group consisting of' sodium alginate, guar gum, carrageenan with locust bean gum, sodium alginate with gelatin, carboxymethylcellulose, gum tragacanth, sodium pectate and vinyl acetate.
8. A capsule membrane as recited in Claim 1 or 3 wherein: the capsule further comprises a gel matrix comprising at least one agent selected from the group consisting of sodium alginate, guar gum, carrageenan with locust bean gum, sodium alginate with gelatin, carboxymethylcellulose, gum tragacanth, sodium pectate and vinyl acetate; and the membrane further comprising <at least one compound selected from the group consisting of ethylene vinyl acetate acrylic acid terpolymers, ethylene vinyl acetate copolymers, spermaceti, aluminum stearates, methyl vinyl ether/maleic anhydride copolymers, ethyl cellulose, ethylhydroxyethyl cellulose, stearic acid, glyceryl monooleate, cetyl alcohol and calcium stearate.
9. A method for encapsulating material and separating the material from its environment comprising encapsulating material in a hydrogel capsule, and surrounding the capsule with at least one. membrane which controls the migration of solutes or solvents between the capsule and the environment.
10. A method as recited in Claim 9 wherein the encapsulated material is living material.
11. A method as recited in Claim 10 wherein the living material is plant meristematic tissue.
12. A method as recited in Claim 11 further comprising encapsulating the material in the capsule and membrane of Claim 4.
13. A method as recited in Claim 11 further comprising encapsulating the material in the capsule and membrane of Claim 5.
14. A method as recited in Claim 11 further comprising encapsulating the material in the capsule and membrane of Claim 6.
15. A method as recited in Claim 11 further comprising encapsulating the material in the capsule and membrane of Claim 7.
16. A method as recited in Claim 11 further comprising encapsulating the material in the capsule and membrane of Claim 8.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US57061184A | 1984-01-13 | 1984-01-13 | |
US570,611 | 1984-01-13 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO1985002972A1 true WO1985002972A1 (en) | 1985-07-18 |
Family
ID=24280339
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US1985/000045 WO1985002972A1 (en) | 1984-01-13 | 1985-01-14 | Coating hydrogel capsules |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP0168476A1 (en) |
JP (1) | JPS61501007A (en) |
AU (1) | AU586620B2 (en) |
WO (1) | WO1985002972A1 (en) |
Cited By (20)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0220667A2 (en) * | 1985-10-23 | 1987-05-06 | Plant Genetics, Inc. | Hydrogel encapsulated nematodes |
WO1991002071A2 (en) * | 1989-08-09 | 1991-02-21 | Dekalb Plant Genetics | Methods and compositions for the production of stably transformed, fertile monocot plants and cells thereof |
AU613079B2 (en) * | 1988-06-17 | 1991-07-25 | Imperial Oil Limited | Maintenance of the viability of microorganisms for use in microbial inoculants |
FR2670082A1 (en) * | 1990-12-10 | 1992-06-12 | Rhone Poulenc Agrochimie | ARTIFICIAL SEEDS. |
US5292507A (en) * | 1986-08-01 | 1994-03-08 | Imperial Oil Limited | Method of using polysaccharides to stabilize microorganisms for inoculating plant seeds |
FR2713441A1 (en) * | 1993-12-07 | 1995-06-16 | Buste Jean Claude | Capsule for provision of liquid reserves for plants |
WO1995031889A1 (en) * | 1994-05-19 | 1995-11-30 | Bayer Aktiengesellschaft | Use of gel formulations as dressing agents |
US5484956A (en) * | 1990-01-22 | 1996-01-16 | Dekalb Genetics Corporation | Fertile transgenic Zea mays plant comprising heterologous DNA encoding Bacillus thuringiensis endotoxin |
US5508468A (en) * | 1990-01-22 | 1996-04-16 | Dekalb Genetics Corporation | Fertile transgenic corn plants |
EP0740897A1 (en) * | 1995-05-05 | 1996-11-06 | Ball Horticultural Company | Method for applying hydrogel coatings to embryonic plants |
EP0711813A3 (en) * | 1994-09-29 | 1997-07-16 | Hitachi Chemical Co Ltd | Coating varnish composition and antifouling coating composition |
WO1998005192A1 (en) * | 1996-08-07 | 1998-02-12 | National Research Council Of Canada | Formulation for synthetic seed |
US5780709A (en) * | 1993-08-25 | 1998-07-14 | Dekalb Genetics Corporation | Transgenic maize with increased mannitol content |
EP1290931A1 (en) * | 2001-09-07 | 2003-03-12 | Agritecno Yazaki Co., Ltd. | Gel-coated seed |
AU2005209654B2 (en) * | 2004-09-27 | 2008-07-31 | Weyerhaeuser Company | Manufactured seed having a live end seal |
US8440265B2 (en) | 2010-04-15 | 2013-05-14 | Appleton Papers Inc. | Water- and heat-resistant scratch-and-sniff coating |
US8663671B2 (en) | 2009-11-05 | 2014-03-04 | Philip Morris Usa Inc. | Methods and compositions for producing hydrogel capsules coated for low permeability and physical integrity |
CN116965546A (en) * | 2023-08-03 | 2023-10-31 | 重庆深山生物科技有限公司 | Health food for regulating and lowering blood pressure and preparation method thereof |
GB2597189B (en) * | 2019-04-11 | 2024-06-05 | Meng Lim Kah | Process for producing a genetically modified seed |
DE102023109524A1 (en) | 2023-04-16 | 2024-10-17 | Lite+Fog GmbH | Vertical plant column, associated aeroponic plant cultivation system and method for applying or anchoring hydrogel |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2712919B2 (en) * | 1991-09-02 | 1998-02-16 | 矢崎総業株式会社 | How to preserve and restore gel-coated seeds |
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-
1985
- 1985-01-14 AU AU38885/85A patent/AU586620B2/en not_active Ceased
- 1985-01-14 EP EP19850900867 patent/EP0168476A1/en not_active Withdrawn
- 1985-01-14 JP JP50072585A patent/JPS61501007A/en active Pending
- 1985-01-14 WO PCT/US1985/000045 patent/WO1985002972A1/en unknown
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US3911183A (en) * | 1972-11-10 | 1975-10-07 | Thomas M Hinkes | Seed coating process and product |
US4378367A (en) * | 1978-05-16 | 1983-03-29 | Fbc Limited | Compositions containing 2,2-dimethyl-1,3-benzodioxol-4-yl N-methylcarbamate for treating seeds |
US4344979A (en) * | 1979-04-02 | 1982-08-17 | Interox (Societe Anonyme) | Process for the preparation of coated seeds |
US4434231A (en) * | 1979-04-05 | 1984-02-28 | Rhone-Poulenc Industries | Means for embedding microorganisms in a polymer matrix |
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Cited By (34)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0220667A3 (en) * | 1985-10-23 | 1989-09-13 | Plant Genetics, Inc. | Hydrogel encapsulated nematodes |
EP0220667A2 (en) * | 1985-10-23 | 1987-05-06 | Plant Genetics, Inc. | Hydrogel encapsulated nematodes |
US5292507A (en) * | 1986-08-01 | 1994-03-08 | Imperial Oil Limited | Method of using polysaccharides to stabilize microorganisms for inoculating plant seeds |
AU613079B2 (en) * | 1988-06-17 | 1991-07-25 | Imperial Oil Limited | Maintenance of the viability of microorganisms for use in microbial inoculants |
WO1991002071A2 (en) * | 1989-08-09 | 1991-02-21 | Dekalb Plant Genetics | Methods and compositions for the production of stably transformed, fertile monocot plants and cells thereof |
WO1991002071A3 (en) * | 1989-08-09 | 1992-05-14 | Dekalb Plant Genetics | Methods and compositions for the production of stably transformed, fertile monocot plants and cells thereof |
US5508468A (en) * | 1990-01-22 | 1996-04-16 | Dekalb Genetics Corporation | Fertile transgenic corn plants |
US5780708A (en) * | 1990-01-22 | 1998-07-14 | Dekalb Genetics Corporation | Fertile transgenic corn plants |
US5554798A (en) * | 1990-01-22 | 1996-09-10 | Dekalb Genetics Corporation | Fertile glyphosate-resistant transgenic corn plants |
US5538880A (en) * | 1990-01-22 | 1996-07-23 | Dekalb Genetics Corporation | Method for preparing fertile transgenic corn plants |
US5538877A (en) * | 1990-01-22 | 1996-07-23 | Dekalb Genetics Corporation | Method for preparing fertile transgenic corn plants |
US5484956A (en) * | 1990-01-22 | 1996-01-16 | Dekalb Genetics Corporation | Fertile transgenic Zea mays plant comprising heterologous DNA encoding Bacillus thuringiensis endotoxin |
FR2670082A1 (en) * | 1990-12-10 | 1992-06-12 | Rhone Poulenc Agrochimie | ARTIFICIAL SEEDS. |
US5382269A (en) * | 1990-12-10 | 1995-01-17 | Rhone-Poulenc Agrochimie | Artificial seeds |
WO1992010087A1 (en) * | 1990-12-10 | 1992-06-25 | Rhone Poulenc Agrochimie | Artificial seeds |
US5780709A (en) * | 1993-08-25 | 1998-07-14 | Dekalb Genetics Corporation | Transgenic maize with increased mannitol content |
FR2713441A1 (en) * | 1993-12-07 | 1995-06-16 | Buste Jean Claude | Capsule for provision of liquid reserves for plants |
WO1995031889A1 (en) * | 1994-05-19 | 1995-11-30 | Bayer Aktiengesellschaft | Use of gel formulations as dressing agents |
US5950360A (en) * | 1994-05-19 | 1999-09-14 | Bayer Aktiengesellschaft | Use of gel formulations as dressing agents for plant seed |
AU698941B2 (en) * | 1994-05-19 | 1998-11-12 | Bayer Aktiengesellschaft | Use of gel formulations as dressing compositions |
EP0711813A3 (en) * | 1994-09-29 | 1997-07-16 | Hitachi Chemical Co Ltd | Coating varnish composition and antifouling coating composition |
US5773508A (en) * | 1994-09-29 | 1998-06-30 | Hitachi Chemical Company, Ltd. | Coating varnish composition and antifouling coating composition |
EP0740897A1 (en) * | 1995-05-05 | 1996-11-06 | Ball Horticultural Company | Method for applying hydrogel coatings to embryonic plants |
WO1998005192A1 (en) * | 1996-08-07 | 1998-02-12 | National Research Council Of Canada | Formulation for synthetic seed |
EP1290931A1 (en) * | 2001-09-07 | 2003-03-12 | Agritecno Yazaki Co., Ltd. | Gel-coated seed |
AU2005209654B2 (en) * | 2004-09-27 | 2008-07-31 | Weyerhaeuser Company | Manufactured seed having a live end seal |
AU2005209654B9 (en) * | 2004-09-27 | 2008-09-04 | Weyerhaeuser Company | Manufactured seed having a live end seal |
US8663671B2 (en) | 2009-11-05 | 2014-03-04 | Philip Morris Usa Inc. | Methods and compositions for producing hydrogel capsules coated for low permeability and physical integrity |
US9167848B2 (en) | 2009-11-05 | 2015-10-27 | Philip Morris Usa Inc. | Method and compositions for producing hydrogel capsules coated for low permeability and physical integrity |
US9661875B2 (en) | 2009-11-05 | 2017-05-30 | Philip Morris Usa Inc. | Methods and compositions for producing hydrogel capsules coated for low permeability and physical integrity |
US8440265B2 (en) | 2010-04-15 | 2013-05-14 | Appleton Papers Inc. | Water- and heat-resistant scratch-and-sniff coating |
GB2597189B (en) * | 2019-04-11 | 2024-06-05 | Meng Lim Kah | Process for producing a genetically modified seed |
DE102023109524A1 (en) | 2023-04-16 | 2024-10-17 | Lite+Fog GmbH | Vertical plant column, associated aeroponic plant cultivation system and method for applying or anchoring hydrogel |
CN116965546A (en) * | 2023-08-03 | 2023-10-31 | 重庆深山生物科技有限公司 | Health food for regulating and lowering blood pressure and preparation method thereof |
Also Published As
Publication number | Publication date |
---|---|
EP0168476A1 (en) | 1986-01-22 |
JPS61501007A (en) | 1986-05-22 |
AU586620B2 (en) | 1989-07-20 |
AU3888585A (en) | 1985-07-30 |
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