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    • 专利摘要:
    The present invention relates to a method comprising heat treating a composition comprising chitin and water-soluble vitamins and / or their derivatives. The invention also relates to a granule obtainable by the process according to the invention, a granule comprising chitin and water-soluble vitamins and / or their derivatives, and the use of these granules in human or animal nutrition , especially in fish feed. Finally, the invention relates to the use of chitin for the protection of water-soluble vitamins during a heat treatment.
    公开号:FR3042387A1
    申请号:FR1560014
    申请日:2015-10-20
    公开日:2017-04-21
    发明作者:Antoine Hubert；Nathalie Berezina；Benjamin Armenjon
    申请人:Ynsect SAS；
    IPC主号:
    专利说明:

    The present invention relates to a method comprising a heat treatment of a composition comprising water-soluble vitamins. The invention also relates to the granules obtained by the process according to the invention, and the use of these granules in the human or animal diet, in particular in fish feed. Aquaculture is today one of the most dynamic sectors of the food industry. The high demand for fish has led researchers to develop aquaculture feeds that would allow efficient and fast fish culture. Typically, aquaculture foods include fishmeal. Indeed, fishmeal is one of the main sources of protein in these foods. It is a flour that is very rich in animal protein (and in particular rich in lysine and methionine amino acids) easy to digest.
    Aquaculture foods may also include vitamins. It is well known that vitamins, especially water-soluble vitamins, have an important role in the development and growth of fish. Thus, it is common to add vitamins during the preparation of aquaculture foods.
    Processes for preparing aquaculture feeds, such as extrusion, generally include a heat treatment step at temperatures of 90 ° C or higher. Unfortunately, this type of heat treatment leads to a degradation of vitamins, especially water-soluble vitamins, so that the granules obtained have a reduced amount of vitamins.
    There is therefore a need for methods for preparing aquaculture feeds, including a heat treatment, which would make it possible to avoid or limit the degradation of the water-soluble vitamins during the heat treatment.
    The work of the inventors made it possible to demonstrate that it was possible to preserve the water-soluble vitamins during a heat treatment when this was carried out under specific conditions.
    The present invention therefore relates to a process comprising a heat treatment of a composition at a temperature greater than or equal to 90 ° C, wherein the composition comprises at least 0.8% by weight of chitin and at least 0.005% by weight of vitamins water-soluble and / or their derivatives, relative to the total weight of the composition.
    It should be noted that in the context of the present application, and unless otherwise stated, the ranges of values indicated are inclusive.
    According to the invention, "chitin" is understood to mean any type of chitinic derivative, that is to say of a polysaccharide derivative comprising N-acetylglucosamine units and D-glucosamine units, in particular the chitin-type copolymers. polypeptides (sometimes referred to as "chitin-polypeptide composite"). These copolymers may also be associated with pigments, often of the melanin type.
    Chitin is the second most synthesized polymer in the world after cellulose. Indeed, chitin is synthesized by many species of the living world: it is partly the exoskeleton of crustaceans and insects and the side wall that surrounds and protects mushrooms. More particularly, in insects, chitin thus constitutes 3 to 60% of their exoskeleton. The determination of the chitin level can be carried out by assay according to the ADAC 991.43 method. Such a method is used in Example 1, and is a preferred method for this determination.
    The chitin present in the composition can result from the introduction into the composition of chitin or advantageously from the introduction into the composition of a meal of arthropods, cephalopods (such as squid), gastropods, annelids, and / or mushrooms. More preferably, the presence of chitin results from the introduction of a meal of insects, crustaceans, squid and / or fungi, even more preferably from an insect meal and / or crustaceans.
    Even more preferably, the chitin present in the composition results from the introduction of an insect meal and optionally a crustacean meal.
    By insect meal, it is more particularly a powder prepared from insects. Such flour may be prepared by a process comprising the following steps: 1. slaughtering insects, 2. hot or cold pressing of insects to obtain a press cake, 3. drying of the press cake, and 4. crushing of the cake. dried press cake.
    This method of preparing the insect meal is more fully detailed below.
    Step 1: killing the insects
    This slaughtering stage 1 can advantageously be carried out by boiling or bleaching. This step 1 makes it possible to kill the insects while lowering the microbial load (reduction of the risk of deterioration and health) and by inactivating the internal enzymes of the insects that can trigger an autolysis, and thus a rapid browning of these.
    For scalding, insects, preferably larvae, are thus scalded with water for 2 to 20 minutes, preferably 5 to 15 minutes. Preferably, the water is at a temperature of between 95.degree. And 105.degree. C., preferably 100.degree.
    The quantity of water introduced during scalding is determined as follows: the ratio of the volume of water in ml to the weight in g of insect is advantageously between 0.3 and 10, preferably between 0, 5 and 5, more preferably between 0.7 and 3, even more preferably of the order of 1.
    For bleaching, insects, preferably larvae, are bleached with steam (nozzles or steam bed) at a temperature between 95 and 105 ° C, preferably 98 ° C or with water at a temperature between 95 and 105 ° C, preferably 100 ° C (by spray nozzles) or in mixed mode (water + steam). The residence time in the bleaching chamber is between 1 to 15 minutes, preferably between 3 and 7 min.
    Step 2: pressing
    The insects from the slaughter stage 1 are then placed in a press according to a procedure which makes it possible to press and separate a juice comprising both an oily fraction and a protein fraction.
    Preferably, the pressing step makes it possible to obtain a press cake having an oil content less than or equal to 20%, preferably less than or equal to 17%, more preferably less than or equal to 15%, the percentages by weight being given on the dry weight of cake press.
    Likewise, the pressing step makes it possible to obtain a press cake having a solids content of between 30% and 60%, preferably between 40% and 55%, and more preferably between 45% and 55%. the percentages by weight being given on the press cake weight.
    Any press system can be used to carry out the pressing step, such as, for example, a single-screw or twin-screw press (Angel twin-screw press), a filter press (Choquenet-type filter press). ), a plate press, etc. These systems are well known to those skilled in the art who is able to determine the pressing conditions in order to obtain the oil and / or water contents mentioned above.
    In particular, it is possible to perform hot or cold pressing. Advantageously, the pressing will be carried out hot, which increases the deoiling of the press cake. In particular, hot pressing makes it possible to obtain a press cake having an oil content of less than or equal to 17%, preferably less than or equal to 15%, the percentages by weight being given on the dry weight of the cake. hurry.
    Step 3: Drying
    The press cake is then dried by conventional technologies known to those skilled in the art. The drying can be direct or indirect (thin-bed dryer, paddle dryer, tubular dryer, disc-dryer, etc.) at a temperature between 60 ° C and 200 ° C, for a period of 15 minutes. min to 24 hours. By way of example, the press cake may be arranged and dried in ventilated / stirred air at a temperature of between 80 and 100 ° C., preferably at 90 ° C. for a period of between 3 and 7 hours, preferably 5 to 7 hours. hours. The purpose of this drying step is to obtain a press cake having a moisture content of between 2 and 15%, preferably between 5 and 10%, more preferably between 4 and 8%.
    Step 4: final grinding
    The dried press cake is then placed in a mill, such as a hammer mill, to reduce the particulate press cake.
    Preferably, at the end of this final grinding, the size of the insect particles is less than 0.5 cm (larger particle size observable by means of a microscope), preferably of the order of 1 mm.
    The preferred insects for the preparation of such flour are, for example, Coleoptera, Diptera, Lepidoptera, Isoptera, Orthoptera, Hymenoptera, Blattoptera, Hemyptères, Heteroptera, Ephemeroptera and Mecoptera, preferably Coleoptera, Diptera, Orthoptera and Lepidoptera.
    The insects are preferably selected from the group consisting of Tenebrio molitor, Hermetia illucens, Galleria mellonella, Alphitobius diaperinus, Zophobas morio, Blattera fusca, Tribolium castaneum, Rhynchophorus ferrugineus, Musca domestica, Chrysomya megacephala, Locusta migratoria, Schistocerca gregaria, Acheta domestica and Samia ricini, and even more preferentially, T. molitor.
    By "water-soluble vitamins" is meant one or more water-soluble vitamins, whether of natural or synthetic origin. Water-soluble vitamins are known to those skilled in the art. The water-soluble vitamins targeted by the invention are, in particular, the vitamins of group B, such as vitamin B1 (thiamine), vitamin B2 (riboflavin), vitamin B3 (niacin or nicotinic acid), vitamin B5 (acid pantothenic), vitamin B6 (pyridoxine), vitamin B8 (biotin or vitamin H), vitamin B9 (folic acid), vitamin B12 (cobalamin), and vitamin C (ascorbic acid). Derivatives of these water-soluble vitamins are also encompassed by the present invention and may be their salts. Preferably, the water-soluble vitamin derivatives are provitamines. By "provitamins" is meant a substance that can be converted into a vitamin after ingestion by an animal. By way of example, mention may be made of the calcium salt of vitamin B5, namely calcium pantothenate, or cyanocobalamin, which is a provitamin of vitamin B12.
    The amounts of vitamins can be determined by methods well known to those skilled in the art. For example, the amount of vitamin B6 can be determined according to standard NF EN 14164. The amount of vitamin B9 can, for its part, be determined by HPLC (High Pressure (Performance) Liquid Chromatoraphy) type liquid chromatography analysis. UPLC ("Ultra Pressure (Performance) Liquid Chromatography") with UV, RI (refractive index) or MS / MS (Tandem Mass Spectrometry) detection. These determination methods, used in Example 2, are preferred according to the invention.
    Throughout the application, where no date is specified for a regulation, standard or directive, it is the regulation, standard or directive in effect on the filing date.
    The method according to the invention makes it possible to protect the water-soluble vitamins present in the composition during the heat treatment. By "protect" is meant that the method according to the invention makes it possible to avoid or limit the degradation of the water-soluble vitamins present in the composition during its granulation. The presence of chitin in the composition makes it possible to protect the water-soluble vitamins during this heat treatment.
    Chitin is generally considered a compound difficult to digest by animals, especially fish. Chitin is often cited as a reason for the mixed results in terms of growth of fish fed with insect meal. However, as demonstrated in Example 4, the presence of chitin in aquaculture feeds has no negative impact on fish growth.
    Advantageously, the composition has a residual moisture content of between 2 and 15%, preferably between 5 and 10%, more preferably between 6 and 8%. This humidity level can for example be determined according to the method resulting from the EC Regulation 152/2009 of 27-01-2009 (103 ° C / 4 h).
    According to a first embodiment of the process according to the invention, the composition comprises at least 0.05% by weight of vitamins of group B, group C and / or their derivatives, relative to the total weight of the composition, preferably at least 0.1% by weight.
    According to a second embodiment of the process according to the invention, the composition comprises at least 0.005% by weight of vitamins B6 and / or B9 and / or their derivatives relative to the total weight of the composition, preferably at least 0.006% by weight. weight.
    Whatever the embodiment of the process according to the invention, the composition comprises at least 0.8% by weight of chitin, relative to the total weight of the composition. Indeed, the protective effect of water-soluble vitamins is observable as soon as the composition comprises at least 0.8% by weight of chitin, relative to the total weight of the composition.
    Advantageously, the composition comprises at least 1.5% by weight of chitin relative to the total weight of the composition, preferably at least 2% by weight of chitin relative to the total weight of the composition, more preferably at least 2.4% by weight. % by weight of chitin relative to the total weight of the composition.
    When the composition comprises at least 1.5% of chitin, there is an increase in the protective effect on water-soluble vitamins, in particular vitamins B6 and / or B9. This effect is even greater when the composition comprises at least 2% of chitin, preferably 2.4% of chitin. These effects are more fully described in Example 2 below.
    In the process according to the invention, the heat treatment is carried out at a temperature greater than or equal to 90 ° C.
    Preferably, the heat treatment is carried out at a temperature greater than or equal to 100 ° C, more preferably between 115 and 145 ° C.
    The heat treatment can also be carried out under pressure, said pressure being between 5 and 50 bars.
    Preferably, the process according to the invention is an extrusion.
    According to a preferred embodiment of the invention, the extrusion process comprises the following steps: grinding a composition comprising at least 0.8% by weight of chitin and at least 0.005% by weight of water-soluble vitamins, by relative to the total weight of the composition, to obtain a powder; the addition of the powder obtained in an extruder; the treatment of the powder by the extruder at a temperature between 90 and 250 ° C, and at a specific mechanical energy (MSE) of between 25 and 100
    Wh / kg; and drying said granules.
    By "grinding" is meant any step to obtain a powder.
    Preferably, the particles forming the powder obtained after grinding have a size of between 10 and 850 μm, more preferentially between 100 and 500 μm, and even more preferentially between 150 and 350 μm.
    By extruder, we target any type of extruder. Preferably, the extruder is a single-screw or twin-screw extruder.
    Following the addition of the powder in the extruder and before the heat treatment, the powder may, optionally, be subjected to a heat pretreatment at a temperature of 25 and 50 ° C. This pretreatment heat step can be done in a particular compartment of the extruder, generally called preconditioner.
    Preferably, the specific mechanical energy is between 35 and 85 Wh / kg, preferably between 50 and 70 Wh / kg.
    The extrusion process according to the invention may also comprise a coating step. The term "coating" is intended to mean any step of applying compounds, and in particular liquid-type compounds, to the granule. Generally, the coating step is by spraying, for example using a wrapper, these compounds on the surface of the granule, for example before the drying step.
    Advantageously, the compounds incorporated are oils, such as vegetable oils such as oleaginous (rapeseed) or animal (fish) oils.
    All the preferred features of the heat treatment method according to the invention, as described above, can also be applied to this preferred embodiment of the invention. The invention also relates to a second process for extruding a composition (containing no or little chitin) comprising the following steps: adding at least 0.8% of chitin to the composition, the percentage by weight being given on the total weight of the composition, and extrusion of the composition.
    Indeed, it has been observed that the addition of chitin to a composition makes it possible to reduce the EMS necessary to perform the extrusion. The invention therefore also relates to the use of chitin to reduce the EMS required for extrusion. The invention also relates to a granule obtainable by the process according to the invention. The invention further relates to a granule comprising at least 0.6% chitin and at least 0.004% by weight of water-soluble vitamins, relative to the total weight of the granule.
    Preferably, the granule comprises at least 1% by weight of chitin relative to the total weight of granules, more preferably at least 1.2% by weight of chitin relative to the total weight of granules, more preferably at least 2% by weight. weight of chitin relative to the total weight of granules.
    According to a first aspect, the granule comprises at least 0.04% by weight of vitamins of group B, of group C and / or their derivatives, relative to the total weight of granules, preferably at least 0.08% by weight of vitamins of group B, group C and / or their derivatives, based on the total weight of granules.
    According to a second aspect, the granule comprises at least 0.004% by weight of vitamins B6 and / or B9, relative to the total weight of granules, preferably at least 0.005% by weight of vitamins B6 and / or B9, relative to the weight total pellet.
    Preferably, the granule will have a size of between 1 and 10 mm, preferably between 1.5 and 5 mm, even more preferably between 2 and 4 mm.
    Advantageously, the chitin present in the granule results from the introduction of a meal of arthropods, cephalopods (such as squid), gastropods, annelids, and / or fungi. More preferably, chitin results from the introduction of a meal of insects, crustaceans, squid and / or fungi, more preferably an insect meal and / or crustaceans.
    Even more preferably, the chitin present in the granule results from the introduction of an insect meal and optionally a crustacean meal.
    Preferably, the insect meal is as described above.
    The granule may furthermore comprise one or more ingredients selected from the group consisting of: fishmeal, - gluten, such as wheat or corn gluten, vegetable flour, such as oleaginous plant meal (s) (s) or protein crop (s), such as soybean or pea flour, or such as cereal flour, such as wheat flour. oils, such as vegetable oils, such as oleaginous (rapeseed) or animal (fish) oils, minerals, amino acids such as methionine, vitamins other than water-soluble vitamins.
    Advantageously, the granule is obtained by extrusion and has the characteristics of a granule obtained by extrusion. In particular, the granulate according to the invention has an apparent density after drying of between 400 and 650 g / l, preferably between 450 and 600 g / l.
    Preferably, a granulate comprising all the above ingredients (fish meal being optional) is particularly suitable for feeding fish. The invention also relates to the use of a granule according to the invention, in human or animal nutrition.
    Advantageously, the granulate according to the invention is used in the feeding of pets such as dogs, cats, birds, fish.
    Preferably, the granulate according to the invention is used for the feeding of poultry (chicken, turkey, any type of game (for example, quail, pheasant, bustard), feeding of pigs, ruminants (cattle, sheep, goats) , equine) or mink, more preferably in aquaculture (fish, crustaceans, molluscs, shells).
    The granule according to the invention can also be used as a dietary supplement. The invention finally relates to the use of chitin for the protection of water-soluble vitamins during a heat treatment at a temperature greater than or equal to 90 ° C.
    In particular, chitin is used for the protection, during said heat treatment, of vitamins of group B, of group C and / or their derivatives, and more particularly vitamins B6 and / or B9. The invention will be better understood from the following examples, given by way of illustration, with reference to:
    Figure 1, which comprises three diagrams representing the amounts of vitamins A (Figure 1A), B6 (Figure 1B) and B9 (Figure 1C) in granules obtained according to the process according to the invention, and in granules obtained according to a comparative method;
    Figure 2, which is a diagram showing the percent loss of vitamin A, B6 and B9 with the method according to the invention and with the comparative method;
    Figure 3, which is a diagram showing the mass density of granules obtained according to the process according to the invention and granules obtained according to a comparative method.
    Example 1 Method According to the Invention and Comparative Method 1. Materials and Methods 1.1. Equipment
    Ingredients for the preparation of granulating compositions - Insect meal
    Mechanically defatted insect meal is obtained by treating larvae of Tenebrio molitor. The composition of this flour is shown in Table 1 below.
    *% Are expressed in dry weight relative to the total weight of flour.
    Table 1: Composition of the insect meal used in Example 1 - Other ingredients o Fish meal LT70 (Peruvian fish meal LT70: 71% crude protein (PB), 11% raw lipid (LB), EXALMAR , Peru) o Krill meal (2 to 4% chitin) (krill meal: 61% BW, 19% LB, Aker BioMarine Antarctic AS, Norway) o Squid meal (Super Prime without viscera: 82% PB, 3.5 % LB, Sopropêche, France) o Soy protein concentrate (Soycomil P: 62% PB, 0.7% LB, ADM, The Netherlands) o Wheat gluten (VITEN: 84.7% PB, 1.3% LB , ROQUETTE, France) o Corn gluten (Corn gluten meal: 61% PB, 6% LB, COPAM, Portugal) o Soy flour 48 o Whole peas o Fish oil o Rape oil o Premix of vitamins and minerals (PREMIX Lda, Portugal) o Soy lecithin o Guar gum o Antioxidant o Sodium propionate o Mono Calcium phosphate o DL-methionine
    Machine for heat treatment
    The heat treatment is carried out by a twin-screw extruder (CLEXTRAL BC45, France) with a screw diameter of 55.5 mm and a maximum flow rate of around 90-
    100 kg / h. The extruder was equipped with a 1 mm round die and a high speed cutter to cut the products into the defined pellet size.
    Other materials
    The mixing is carried out in a double helix mixer (model 500L, TGC Extrusion, France).
    The grinding is carried out in a micro-pulverising hammer mill (model SH1, Hosokawa-Alpine, Germany).
    The drying is carried out using a vibrating fluidized bed dryer (model DR 100, TGC Extrusion, France). The coating is carried out in a wrapper (model PG-10VCLAB, Dinnisen, the Netherlands). 1.2. Methods
    Preparation of compositions
    Three compositions Y7.5, Y15 and Y25 were formulated, respectively comprising 7.5%, 15% and 25% by dry weight of insect meal on the total dry weight of the composition. These three compositions were used in processes according to the invention. Two other compositions, CTRL and Y5, have also been formulated for implementation in comparative methods.
    Some adjustments on the formulation of the compositions were made to maintain the iso-nitrogenous conditions (crude protein, 48.5% by dry weight on the total weight of the dry matter (DM)), isolipidic (22.7% by dry weight on the total weight of the MS) and isoenergetic (gross energy, 23.2 MJ / kg DM).
    All ingredients (except fish and rapeseed oils) were weighed and mixed according to the different formulations in the double helix mixer.
    The various mixtures obtained were milled in the micropulverizer hammer mill to obtain compositions CTRL, Y5, Y7,5, Y15 and Y20, in powder form whose particles have a size of less than 250 microns. 60 kg of each composition were prepared.
    The formulations of the compositions are summarized in Table 2 below.
    *% of dry matter relative to the total weight of the composition **% by dry weight relative to the total weight of the dry matter
    Table 2: Summary of the compositions prepared. Determination of the amount of chitin
    The dietary fiber of the insect meal is mainly composed of chitin, the latter was therefore determined according to the ADAC 991.43 method. The values thus obtained are therefore slightly overestimated.
    Heat treatment of compositions
    Compositions CTRL, Y5, Y7.5, Y15 and Y25 were then extruded to a 3.0 mm pellet size.
    Heat treatment
    The temperature of the heat treatment performed during the extrusion is indicated in Table 3 below, for each composition.
    Throughout the extrusion of the various compositions, the operating parameters were recorded and allowed the calculation of the specific mechanical energy (EMS), in Watt hour / kg (Wh / kg).
    Table 3: Extrusion Conditions and EMS in Example 1.
    By "Fût 1", a preconditioner is aimed at, where the mixture resulting from the double helix mixer is brought to temperature.
    By "Fût 2", it is intended a conditioner: it is the heat treatment step and rise in pressure that takes place in the extruder.
    The water level is an indication of the water added during steam heating and therefore the amount added may vary depending on the ingredients. It is adjusted by drying at the end of the process. The EMS was calculated as follows: TT T _ ESSSS U x 1 x cos Φ-
    EMS (W h / kg) = -MaxSS
    Qs Where: U: motor operating voltage (U = 460 V) I: current supplying the motor (A)
    cos Φ: theoretical output of the extruder motor (cos φ = 0.95) ESS SS: test speed (rpm) of the rotating screws.
    Max SS: maximum speed (267 rpm) of the rotating screws.
    Qs: input rate of the composition (kg / h). Drying
    Following extrusion, extrusion, CTRL, Y5, Y7.5, Y15 and Y25 extrudates were dried in the vibrating fluid bed dryer.
    Coating
    After cooling the Y7.5, Y15 and Y25 granules, the fish and rapeseed oils described in Table 2 were added by vacuum coating with the enrober. 2. Conclusion
    During the extrusion process, increasing doses of insect meal require a reduction of added water and an increase in melee feed rates and screw speed, resulting in a reduction in specific mechanical energy (EMS).
    EXAMPLE 2 Evaluation of Vitamins Water-soluble in Granules Obtained by the Process According to the Invention and Comparative Methods
    In order to determine the effect on the conservation of the water-soluble vitamins, samples of the compositions CTRL, Y5, Y7,5, Y15 and Y25 before extrusion, the extrudates CTRL, Y5, Y7,5, Y15 and Y25 (before drying), and Dried granules CTRL, Y5, Y7.5, Y15 and Y25 (without coating / coating) were removed for analysis of vitamin A, B6 and B9 content. 1. Material and methods
    The amount of vitamin B6 was determined according to standard NF EN 14164.
    The amount of vitamin B9 was determined by HPLC or UPLC analysis with UV, RI or MS / MS detection.
    The results of these analyzes are shown in Table 4 below.
    * Weight in mg / kg of composition
    Table 4: Quantities of vitamin A, B6 and B9 at various stages of the granulation process
    The results in Table 4 are shown in Figure 1.
    Figure 2 shows the percent loss of vitamin A, B6 and B9 in the granulation process for each composition CTRL, Y5, Y7.5, Y15 and Y25.
    The results show that:
    Losses of vitamin A (fat soluble) during granulation were low (2-3%) and vitamin A was little affected by the presence of chitin.
    In a CTRL diet, losses of vitamins B6 and B9 (water-soluble) during extrusion ranged from 11 to 12%. However, the inclusion of 15% and 25% chitin-containing flour tended to significantly reduce treatment losses for these two vitamins. This preservation effect of the water-soluble vitamins is therefore observable as soon as a chitin content greater than or equal to 0.8% is reached in the composition undergoing heat treatment, preferably greater than or equal to 1.5%.
    Example 3: Evaluation of the quality criteria of the granules
    1. Material and methods
    The quality of the CTRL, Y5, Y7.5, Y15 and Y25 granules as prepared in Example 1 was evaluated. 1.1. Moisture content
    The moisture level of the extrudate (at the exit of the extruder and before drying) and granules (when dried) was measured, determining the weight loss after drying 10 grams of sample (made in triplicate) at 105 ° C for 24 h. 1.2. Water Activity Water activity (aw) represents the vapor pressure of a product divided by the vapor pressure of pure water at the same temperature. The activity of water is commonly used as a criterion to characterize the shelf life of products, because below certain levels, it inhibits the growth of bacteria and molds. Water activity was measured in triplicate samples (2.5 g) of food using AquaLab LITE (DECAGON, USA). 1.3. Apparent density
    The apparent density of the extruded foods was determined, in triplicate, by filling a pre-weighed plastic volumetric beaker (known volume of 1 L) with pellets. Excess granules at the top of the plastic beaker were gently scraped off the edge. Care has been taken to avoid slitting ( ) Of the sample. The plastic beaker was weighed and the apparent density expressed as mass of the sample (g) per unit volume (L). 1.4. Statistical treatment of data
    The data was analyzed by unidirectional ANOVA. Where appropriate, averages were compared by the Newman-Keuls test. Statistical significance was tested at P <0.05. All statistical tests were performed using SPSS software (v21, IBM, USA). 2. Results
    The results relating to the quality of the different granules are presented in Table 5 below and in Figure 3.
    The values are mean ± standard deviation (n = 3). Different letters exhibiting in a column indicate a significant difference (P <0.05).
    Table 5: Apparent Density, Moisture, and Water Activity of Experimental Foods 3. Conclusion
    The bulk density of the extruded granules varied considerably from 622 to 485 g / L. A significant reduction in bulk density (P <0.05) was closely associated with increasing increasing doses of insect meal.
    Regardless of the level of inclusion, insect meal did not affect the moisture content (measured both before and after drying) and the water activity of the extruded foods.
    It is interesting to note that in order to maintain iso-nitrogenated and isolipidic conditions between diets, in addition to the direct replacement of fishmeal with insect meal, diets rich in insect meal have a slight increase in gluten. wheat (from 9.05% in CTRL to 10.10% in Y25) and a reduction of whole peas (from 6.15% in CTRL to 3.70% in Y25). Both wheat gluten and starch from whole peas are known to affect the expansion and physical structure of the pellets.
    Example 4: Impact of chitin on fish growth
    The CTRL regime described in Example 1 was formulated with practical ingredients to meet the known nutritional requirements of juvenile rainbow trout. This CTRL diet consists of 25% fishmeal, 8% other marine protein sources (squid meal and krill meal), while the remaining protein sources were soy protein concentrate, wheat gluten and corn gluten. On the basis of this formulation, the four regimes Y5, Y7,5, Y15 and Y25, also
    described in Example 1, were formulated, in which the fish meal was replaced by the insect meal at respective levels of 20, 30, 60 and 100%. 1. Material and methods 1.1. Equipment
    Diets
    The diets consist of granules having the compositions CTRL, Y5, Y7.5, Y15 and Y25 respectively, as prepared in Example 1.
    The levels of squid meal and krill were kept constant across all diets to ensure high palatability. Minor adjustments to the formulation of the tested diets were made to maintain iso-nitrogen (crude protein, 48.5% DM), isolipidic (22.7% DM) and isoenergetic (gross energy, 23.2 MJ / kg DM) conditions ).
    Levels of methionine and monocalcium phosphate supplementation in diets tested were adjusted to match those found in the CTRL diet.
    Throughout the trial, the experiment foods were stored at room temperature, but in a cool, ventilated location.
    The fish
    Triplicate groups of 35 rainbow trout (Oncorhynchus mykiss) with an initial body weight (ICP) of 5.01 ± 0.1 g were fed one of five experimental diets for 90 days. The fish grew in circular fiberglass tanks (volume: 250 L) fed with continuous flow fresh water, at temperatures between 14.1 ± 0.3 ° C and dissolved oxygen levels above 7.4 mg / L (Figure 1). The fish were subjected by summer conditions to natural photoperiod changes (May-July). The fish were fed ostentatiously, by hand, three times a day (9am, 2pm and 6pm) on weekdays and twice a day on weekends (10am and 4pm), with the utmost care to avoid wastage food. The distributed food was quantified throughout the study. Anesthetized fish were weighed individually at the beginning and at the end of the study and the group was weighed at day 28 and day 60. At the beginning, 15 fish from the same initial stock were sampled and stored at -20 ° C. for subsequent analysis of the integral body composition. After 90 days of experimental feeding, 6 fish from each tank were sampled for the same purpose. 1.2. Methods
    Criterion for PCI growth and nutrient utilization assessment (g): Initial body weight. PCF (g): Final body weight.
    Specific growth rate, TCS (% / day): (Ln PCF - Ln PCI) x 100 / days. Consumption index, IC: gross food intake / weight gain.
    Voluntary dietary intake, AAV (% CP / day): (gross food intake / (PCI + PCF) 121 days) x 100.
    Protein efficiency coefficient, CEP: wet weight gain / raw protein intake.
    Statistical analysis
    The data is presented by the average of three repetitions ± standard deviation. The data were subjected to one-way analysis of variance. Before ANOVA, the values expressed in% were subjected to a transformation of the square root arc sinus. Statistical significance was tested at a level of a probability of 0.05. All statistical tests were performed using IBM SPSS V21 software. 2. Results
    Growth performance
    Data on growth performance, feed conversion, and protein efficacy of rainbow trout fed for 90 days with experimental diets are reported in Table 6. No mortality occurred during the survey. trial.
    Values are means ± standard deviation (n = 3).
    Values within a row with different exponents differ significantly (P <0.05).
    Table 6: Growth Performance at Day 90 Incorporation of increasing doses of insect meal (and thus increasing doses of chitin) with a concomitant reduction in fish meal was progressively linked to a significant increase in body weight of the fish meal. fish. In addition, compared with CTRL treatment, all insect meal diets led to a significant reduction in dietary intake and a significant increase in CEP values (P <0.05). The introduction of chitin into the granules according to the invention therefore does not have any disadvantages as regards the nutritional contribution delivered to the animal.
    权利要求:
    Claims (12)
    [1" id="c-fr-0001]
    A process comprising heat treating a composition at a temperature greater than or equal to 90 ° C, wherein the composition comprises at least 0.8% by weight of chitin and at least 0.005% by weight of water-soluble vitamins and / or their derivatives, relative to the total weight of the composition.
    [2" id="c-fr-0002]
    2. The method of claim 1, wherein the composition comprises at least 0.05% by weight of vitamins of group B, group C and / or their derivatives, relative to the total weight of the composition.
    [3" id="c-fr-0003]
    The method of claim 1, wherein the composition comprises at least 0.005% by weight of vitamins B6 and / or B9 and / or their derivatives.
    [4" id="c-fr-0004]
    4. Method according to any one of claims 1 to 3, wherein the composition comprises at least 1.5% by weight of chitin relative to the total weight of the composition.
    [5" id="c-fr-0005]
    5. Process according to any one of claims 1 to 4, wherein the temperature is greater than or equal to 100 ° C.
    [6" id="c-fr-0006]
    6. Process according to any one of claims 1 to 5, wherein the heat treatment is carried out under pressure.
    [7" id="c-fr-0007]
    The method of any one of claims 1 to 6, wherein the process is extrusion.
    [8" id="c-fr-0008]
    8. Granule obtainable by the method according to one of claims 1 to 7.
    [9" id="c-fr-0009]
    9. Granule comprising at least 0.6% of chitin and at least 0.004% by weight of water-soluble vitamins, relative to the total weight of the granule.
    [10" id="c-fr-0010]
    10. Use of chitin for the protection of water-soluble vitamins during a heat treatment at a temperature greater than or equal to 90 ° C.
    [11" id="c-fr-0011]
    11. Granule according to claim 9, wherein the chitin results from the introduction of a meal of insects, crustaceans, squid and / or fungi.
    [12" id="c-fr-0012]
    12. Use of a granulate according to one of claims 8, 9 or 11, in food or feed.
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    CL2018001017A1|2018-06-29|
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    JP2019500010A|2019-01-10|
    EP3364777A1|2018-08-29|
    FR3042387B1|2019-05-24|
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    MX2018004796A|2018-08-01|
    WO2017068278A1|2017-04-27|
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    PE20180964A1|2018-06-12|
    DK3364777T3|2021-05-25|
    CA3001830A1|2017-04-27|
    JP2021126120A|2021-09-02|
    AU2016342515A1|2018-05-31|
    RU2018118184A|2019-11-21|
    HUE054592T2|2021-09-28|
    PL3364777T3|2021-07-26|
    EP3364777B1|2021-02-24|
    RU2018118184A3|2020-03-19|
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    法律状态:
    2016-10-21| PLFP| Fee payment|Year of fee payment: 2 |
    2017-04-21| PLSC| Publication of the preliminary search report|Effective date: 20170421 |
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    2018-10-30| PLFP| Fee payment|Year of fee payment: 4 |
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    2020-10-21| PLFP| Fee payment|Year of fee payment: 6 |
    2021-10-29| PLFP| Fee payment|Year of fee payment: 7 |
    优先权:
    申请号 | 申请日 | 专利标题
    FR1560014|2015-10-20|
    FR1560014A|FR3042387B1|2015-10-20|2015-10-20|PRESERVATION OF WATER-SOLUBLE VITAMINS|FR1560014A| FR3042387B1|2015-10-20|2015-10-20|PRESERVATION OF WATER-SOLUBLE VITAMINS|
    AU2016342515A| AU2016342515A1|2015-10-20|2016-10-18|Preservation of water-soluble vitamins|
    KR1020187013757A| KR20180066228A|2015-10-20|2016-10-18|Preservation of water-soluble vitamins|
    MX2018004796A| MX2018004796A|2015-10-20|2016-10-18|Preservation of water-soluble vitamins.|
    RU2018118184A| RU2730028C2|2015-10-20|2016-10-18|Preservation of water-soluble vitamins|
    DK16809457.1T| DK3364777T3|2015-10-20|2016-10-18|PRESERVATION OF WATER-SOLUBLE VITAMINS|
    BR112018008108-6A| BR112018008108A2|2015-10-20|2016-10-18|preservation of water soluble vitamins|
    PE2018000506A| PE20180964A1|2015-10-20|2016-10-18|CONSERVATION OF WATER-SOLUBLE VITAMINS|
    EP16809457.1A| EP3364777B1|2015-10-20|2016-10-18|Preservation of water-soluble vitamins|
    ES16809457T| ES2870009T3|2015-10-20|2016-10-18|Preservation of water-soluble vitamins|
    CA3001830A| CA3001830A1|2015-10-20|2016-10-18|Preservation of water-soluble vitamins|
    JP2018520160A| JP6998300B2|2015-10-20|2016-10-18|Retention of water-soluble vitamins|
    PCT/FR2016/052694| WO2017068278A1|2015-10-20|2016-10-18|Preservation of water-soluble vitamins|
    PL16809457T| PL3364777T3|2015-10-20|2016-10-18|Preservation of water-soluble vitamins|
    CN201680061290.8A| CN108135226A|2015-10-20|2016-10-18|The preservation of water soluble vitamin|
    HUE16809457A| HUE054592T2|2015-10-20|2016-10-18|Preservation of water-soluble vitamins|
    US15/769,536| US20180303126A1|2015-10-20|2016-10-18|Preservation of water-soluble vitamins|
    CL2018001017A| CL2018001017A1|2015-10-20|2018-04-19|Conservation of water-soluble vitamins.|
    JP2021080554A| JP2021126120A|2015-10-20|2021-05-11|Retention of water-soluble vitamin|
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