Patent Application
20230357097
The invention relates to the biological sector of methods for the transformation of a culture of microorganisms in liquid state into a solid state.
More specifically, the invention relates to a method for the transformation of a liquid substrate comprising microorganisms, such as bacteria or fungi, into a substance in solid state, while preserving the viability of the strains for a long time, particularly for use in agriculture.
The invention also relates to the substance in solid state directly obtained by this transformation method.
The most commonly used current techniques for transforming a substrate from liquid to solid are:
Freeze-drying: this is a drying technique that, starting from a solution, makes it possible to obtain a porous, friable, hygroscopic solid having a large specific surface area and being rapidly soluble (freeze-dried). The product is obtained by freezing the solution followed by vacuum sublimation of the solvent. The steps that characterise freeze-drying are:
This technique involves the use of complex machinery dedicated exclusively to freeze-drying.
The freeze-drying technique makes it possible to obtain:
The advantages of this technique are:
However, this technique also has certain drawbacks, such as the high cost of machinery, high energy costs and very long processing times (on average 24 hours/cycle).
There also exist certain specific problems linked to freeze-drying for use in the agricultural sector: the method is very costly and therefore not easy to use in all contexts, requiring process optimisation, specific skills and numerous experiments. Furthermore, when dealing with microorganisms, final viability may be considerably reduced by the presence of extreme conditions such as cold and high vacuum conditions.
Spray-drying: this is a technique involving the drying of a fluid current which is reduced to solid particulate by sub-dividing it into fine drops and striking it with a current of hot air (or another gas). Based on the type of fluid dried (solution, suspension, paste, etc.), the solid product may be a fine powder, granules or agglomerates. The drying process involves four steps:
Actuation of this method involves the use of very complex, and once again dedicated machinery.
Spray drying has several advantages:
On the other hand, disadvantages associated with this method include: a high initial cost of investment, low thermal efficiency, little flexibility during “work in progress” and low product density without further processing.
Both techniques described, and currently most widely used, also have several disadvantages in common, especially when used for the manufacture of products for the agricultural industry.
First of all, the high costs involved, since both techniques require very costly machinery both in terms of start-up (purchase) and in terms of running and use (maintenance, utility costs, high energy consumption). Furthermore, the machinery is very bulky, requiring dedicated company spaces to be set aside.
Another aspect to consider is the exclusiveness of the machinery currently available. When buying a freeze-drier or a spray-drier, the instrument can only be used for that specific purpose.
Both freeze-drying, which requires a highly complex initial design stage to optimise the finished product, and spray-drying, which does not allow the product to be modulated during production, are complex, rigid techniques.
CN 105 272 459 A discloses a procedure for obtaining a composite fertilizer, comprising at least two microorganism-based products that are mixed and then re-suspended in a soil for growth. The procedure creates a composite fertilising product, containing a plurality of microorganisms, in a liquid formulation.
US 2013/236522 A1 discloses a procedure that comprises the growth of microorganisms in a liquid substrate and a subsequent drying phase using known freeze-drying or spray-drying processes.
E. Malusà et Al. “Technologies for Beneficial Microorganism Inocula Used as Biofertilizer” THE SCIENTIFIC WORLD JOURNAL, vol. 133, no. 3, 1 Jan. 2012 (2012 Jan. 2001), pages 3473-12, XP055325563, DOI: 10.1100/2012/491206 discloses various examples of procedures for the production of both solid and liquid microorganism-based inoculants, using known laboratory techniques, that enable the microorganisms to survive for a short time when stored at low temperatures, making them unsuitable for commercial use, which requires considerably longer life times.
U.S. Pat. No. 4,956,295 A discloses a procedure for obtaining a stable solid product, but the microorganisms are subjected to a traditional high-temperature drying stage, with consequent high process costs.
US 2008/107689 A1 discloses a procedure for growing and developing a microorganism on a solid substrate until complete colonisation. The resultant product is a humid paste that can be stored at low temperatures and used as a fertiliser only after being dissolved in water.
U.S. Pat. No. 9,090,884 B2 discloses a procedure for obtaining a product containing a formulation comprising a plurality of vital organisms and micro-encapsulating agents. The process is complex for the number of phases and components involved, and the product is consequently very costly.
US 2019/194600 A1 discloses a procedure for producing a porous substance on which to multiply, or grow, microorganisms. Growth of the microorganisms is difficult to control, however, and the duration and methods of conservation of the product are not defined.
WO 00/29544 A1 discloses a method for extracting active compounds deriving from a fermentation process conducted in a specific bioreactor. It therefore does not involve the direct use of the microorganisms developed in the reactor.
The invention proposes to overcome these limits and defects.
The main object of the invention is to define a method for the transformation of a liquid substrate comprising microorganisms, into a substance in solid state, of a powdery type, while preserving the viability of the strains of microorganisms, such as bacteria or fungi.
A further object of the invention is to define a process that is efficient, flexible, modulable, and can be implemented over time, involving machinery and instrumentation that require a minimum investment cost, occupy little space, can also be used for other activities and enable the process to be modulated.
Another object is to use the transformation method to obtain a substance in solid state that is economical, can be stored for a long time at ambient temperature, with the viability of the microorganisms stable over time, that does not aggregate, is extremely versatile and suitable for use in agriculture in various agronomic applications, from fertigation to more traditional methods, mixed with other solid or liquid products, or on its own in formulations with a high content of active microorganisms.
These objects are achieved with a method for the transformation of a liquid substrate into a substance in solid state as disclosed and claimed.
In particular, the objects are achieved with a method that makes a liquid culture become solid by mixing it with an inert compound, such as synthetic amorphous silica for example, so as to obtain a constant humidity (even very low) while preserving the viability of the microorganisms for a long time.
A further object of the invention is a substance in solid state, particularly a powder, directly obtained through this process.
The method makes it possible to obtain the following main advantages:
The advantages of the invention will become more apparent from the following preferred mode of implementation of the invention, given by way of non-limiting illustration, and with the help of the figures, where:
With reference to
More specifically, the first step involves the production of a liquid culture through a process of fermentation. This step can be carried out using a bioreactor 1 or in laboratory conditions.
Excellent results have been obtained using 50 and/or 500-litre bioreactors.
Once fermentation has taken place, the liquid product is drained from the bioreactor 1 and if necessary passed through the centrifuge 2 (max. speed 9600 rpm), so as to remove excess liquid and thereby concentrate the product. This step can be avoided if considered unnecessary, for example in the case of high titre concentrations or particular production needs. This step is also modulable, meaning that it is possible to obtain a more or less liquid product.
The liquid product—as is or centrifuged—is used for micronisation, a step in which a pump pushes the liquid through a turbine, which micronises any solid components present in the product (frustules, fungal myceleum), producing a homogeneous product.
The processed product is then sent to the final phase, mixing. Through a pump 5, the liquid L is aspirated and pushed through nozzles 6 (with variable dimensions depending on needs) that nebulise the product on the adsorbent solid S, advantageously amorphous silica in powder form.
In this phase, it is possible to modulate the dimensions of the drops of liquid L and the quantity of solid S, so that it will be possible to obtain a highly-flexible product based on needs.
Once this phase is completed, the product is drained from the mixer and can be stored in bulk or bagged directly, based on needs.
With reference to
The solid substrate used (amorphous silica) is in powder form, using the mixer jet one obtains a solid substrate also in powder form, to which the microorganisms can adhere.
The substance in solid state obtained with this process is a fine powder, with variable granule size, 40% of which can pass through a 60 mesh (250 micron) sieve without the need for further processing. The humidity of the substance is on average between 20% and 60%, but processing can also be conducted with variable humidity, based on the characteristics of the final product one wishes to obtain.
The powder containing microorganisms can be added as an additive to other formulations used in the agricultural sector, whether liquid or solid, and is therefore highly versatile. Otherwise the product can be used as the sole component of formulations with a high technological value, i.e. without chemical additives, substantially containing only pure microorganisms, capable of performing an active function on the soil without compromising the viability of the other microorganisms already present.
40 L of soil suitable for the development of the bacterial microorganism under study were inserted in a bioreactor 1. Inoculation was carried out and the growing conditions needed for multiplication of the bacterium were applied.
At the end of the fermentation process the product was drained from the bioreactor and stored until the mixing phase.
The liquid product was fed to the mixer 4 and nebulized, using small-dimension nozzles 6, directly into the device containing only the adsorbent solid product S (amorphous silica).
Mixing of the two components was performed for several hours, in order to obtain a uniform product. The product was then drained and stored in suitable containers until required for use.
The result of this process was a fine powder, with a residual humidity between 20% and 60%.
The viability of the product thus obtained was at least one year, with storage at ambient temperature.
30 L of soil suitable for the development of the fungal microorganism under study were inserted in a bioreactor 1. Inoculation was carried out and the growing conditions needed for multiplication of the fungus were applied.
At the end of the fermentation process the product was drained from the bioreactor 1 and stored until the micronisation phase.
The liquid fungal product contained a significant solid proportion, mycelium, requiring passage through a microniser 3.
Following a series of cycles in the microniser 3 the product had suitable dimensions, and it was thus possible to move on to the next phase.
The micronised product was fed to the mixer 4 and nebulized, using medium-dimension nozzles 6, directly into the device containing only the adsorbent solid product S (amorphous silica).
Mixing of the two components was performed for several hours, in order to obtain a uniform product. The product was then drained and stored in suitable containers until required for use.
The result of this process was a fine powder, with a residual humidity between 20% and 60%.
The viability of the product thus obtained was at least one year, with storage at ambient temperature.
| Number | Date | Country | Kind |
|---|---|---|---|
| 102019000022365 | Nov 2019 | IT | national |
This application is the U.S. national phase of International Application No. PCT/IT2020/050285 filed Nov. 18, 2020 which 10 designated the U.S. and claims priority to IT Patent Application No. 102019000022365 filed Nov. 28, 2019, the entire contents of each of which are hereby incorporated by reference.
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/IT2020/050285 | 11/18/2020 | WO |
