PROCESS FOR THE PREPARATION OF PROTEIN MASS

Abstract

The invention relates to a process for the production of a protein mass from insect larvae, comprising the steps of, cleaning insect larvae, applying pulsed electric fields to the cleaned insect larvae and comminuting the insect larvae to produce an insect mass; and subsequently fractionating the insect mass into a solid and at least one liquid phase with subsequent drying of the solid.

Claims

1. A process of producing protein mass from insect larvae comprising cleaning insect larvae, applying pulsed electric fields to the insect larvae and comminuting the insect larvae to produce an insect mass, and subsequently fractionating the insect mass into a solid and at least one liquid phase, with subsequent drying of the solid to produce the protein mass.

2. The process according to claim 1, wherein the insect larvae are suspended in water and subjected to pulsed electric fields while suspended in water.

3. The process according to claim 1, wherein the insect larvae are comminuted and a mass of comminuted insect larvae is subjected to pulsed electric fields.

4. The process according to claim 1, wherein the cleaning and the application of pulsed electric fields is carried out by suspending the insect larvae in water and applying pulsed electric fields to the insect larvae suspended in water and subsequently separating the insect larvae from the water, and the insect larvae are subsequently comminuted.

5. The process according to claim 1, wherein the insect larvae are dried at least superficially before comminution and in that no water is added to the mass of comminuted insect larvae.

6. The process according to claim 1, wherein an aqueous liquid phase and a lipid-rich liquid phase are produced during fractionation.

7. The process according to claim 1, wherein the fractionation is carried out by a press with at least 4 MPa or at least 5 MPa pressure or by a decanter.

8. The process according to claim 1, wherein the fractionation is carried out by a screw press or filter press.

9. The process according to claim 1, wherein the comminution is carried out by a cutter, a mill, an extruder or a press.

10. The process according claim 1, wherein the insect laves are heated to a temperature of 50° C. to 90° C. for a period of 10 s to 10 min by contact with hot air, steam or hot water before applying pulsed electric fields or before comminution.

11. The process according to claim 1, wherein before or after cleaning the insect larvae are frozen at −18° C. to −60° C. and thawed.

12. The process according to claim 1, wherein the drying of the solid is carried out at at least 70° C.

13. The process according claim 6, wherein protein is separated from the aqueous liquid phase and is added to the protein mass.

14. The process according to claim 1, wherein the insect larvae are raw.

15. A protein mass, in particular obtainable by a process according to claim 1, wherein the protein mass is dried and produced from cleaned insect larvae which have been subjected to pulsed electric fields and been comminuted to an insect mass and subsequently fractionated to a solid and an aqueous liquid phase, with separation of protein from the aqueous liquid phase and subsequent drying of the solid and the protein separated from the aqueous liquid phase.

16. The protein mass according to claim 15, wherein the solid is combined with the protein separated from the aqueous liquid phase and subsequently dried.

17. The protein mass according to claim 15, comprising separate oil separated from the insect mass as a lipid-rich liquid phase.

Description

[0028] The invention is now described in more detail by means of examples with reference to the figures, which show in

[0029] FIG. 1 schematically the process in the first embodiment,

[0030] FIG. 2 schematically the process in the second embodiment,

[0031] FIG. 3 the drying behavior of an exemplary protein mass.

[0032] FIG. 1 schematically shows the first embodiment of the process, in which insect larvae 1 are subjected to cleaning 2, optionally with freezing 10, and are treated in suspension in water with pulsed electric fields (PEF) 3. Therein, after freezing 10, thawing can be done during suspending in water and treating with pulsed electric fields 3. The insect larvae treated with PEF 3 and suspended in water are separated from the water 4 and subjected to comminution 5 to form an insect mass M, subsequently subjected to fractionation 6 into a solid phase 7 and a liquid phase 9, preferably in one fractionation step directly, or in a subsequent further fractionation into an aqueous liquid phase 9a and a lipid phase 9b. By drying 8 the solid phase 7 becomes the protein mass 10.

[0033] FIG. 2 schematically shows the second embodiment of the process, in which insect larvae 1 are subjected to comminution 5 after cleaning 2 and optional freezing 10, and the insect mass M thus produced is then subjected to treatment with pulsed electric fields 3. Preferably, after cleaning 2 and before or after optional freezing 10, the insect larvae are separated from water 4 with which they were brought into contact during cleaning 2. After treatment with PEF 3, the insect mass is subjected to fractionation 6 into a liquid phase 9, preferably directly into a lipid phase 9b and an aqueous liquid phase 9a, and a solid phase 7, from which the protein mass 10 is subsequently produced by drying 8.

[0034] In both embodiments, the separation 4 of water from the insect larvae can be performed by sieving, preferably followed by hot air drying, e.g. with air of a temperature of 50 to 90° C., in particular at 50, 60, 70, 80 or 90° C., e.g. in an air stream of a speed of 1 to 3 m/s on average, in particular 2 m/s.

EXAMPLE 1: PRODUCTION OF DRIED PROTEIN MASS FROM LARVAE OF HERMETIA ILLUCENS

[0035] As an example of insect larvae, approximately 1 kg of fresh, live larvae of Hermetia illucens were suspended in cold tap water and separated from the water by means of a coarse sieve plate after a standing time of approximately 5 to 30 min with gentle stirring. The larvae were subsequently re-suspended in cold tap water and between two electrodes exposed to pulsed electric fields from at least 1 kV/cm, pulse duration from at least 5 μs, pulse frequency from 1 to 500 Hz, pulse energy 5 to 20 kJ/kg larvae.

[0036] Subsequently, the larvae were separated from the water using the coarse sieve plate and dried in an air stream of 80° C., 2 m/s. In the process, 0.65 kg of water was separated from the larvae. Subsequently, these larvae in one step were comminuted into an insect mass using a screw press at a pressure of 4 to 5 MPa and fractionated into a solid phase and a liquid phase. The solid phase had a high content of protein, chitin, carbohydrates, and traces of oil and water. The liquid phase had water with protein dissolved in it as well as lipids, which could be separated from the aqueous phase by means of a decanter. The solid phase was dried by hot air drying with an air flow starting at 2 m/s from 50° C. to 90° C.

[0037] The composition of the solid and liquid phase (with PEF) produced by the process according to the invention (with PEF) and of a solid or liquid phase produced by the otherwise identical process steps for comparison without treatment with pulsed electric fields (comparison, without PEF) are shown in the Table.

TABLE-US-00001 Liquid Solid Liquid Solid phase comparison, phase with with without comparison, PEF PEF PEF without PEF mass 0.22 kg 0.13 kg 0.23 kg 0.12 kg protein 65.3% 1-2% 59.3% 1-2% other solids   17%   17% oil 16.7% 96.4% 18.5% 96.9% water 2-3% 2-3%

[0038] This result shows that the process according to the invention by PEF treatment can produce a solid having a higher protein content and a larger liquid phase.

EXAMPLE 2: PRODUCTION OF DRIED PROTEIN MASS FROM LARVAE OF HERMETIA ILLUCENS

[0039] As an example of insect larvae, about 1 kg of fresh, live larvae of Hermetia illucens were frozen at −18° C. and after 10 d suspended in 15° C. tap water and thawed therein and immediately subjected to pulsed electric fields from at least 1 kV/cm, pulse duration from at least 5 μs, pulse frequency from 1 to 500 Hz, pulse energy 5 to 20 kJ/kg larvae. The larvae were separated from the water with a perforated plate and by means of screw press at 5 MPa pressing pressure were comminuted and fractionated in one step at a temperature of about 20° C. The fractions obtained had a temperature of about 110 to 120° C. For comparison, the same process was carried out but without applying electrical voltage to the electrodes (comparison, without PEF). The compositions of the respective solids and of the liquid phases are shown in the table.

TABLE-US-00002 liquid solid, liquid Solid, phase, comparison, phase, with with without comparison, PEF PEF PEF without PEF mass 0.22 kg 0.22 kg 0.79 kg 0.176 kg protein   16% low   15% low content, content, not not determined determined other   19%   15% solids oil    7%   12%   7%   17% water 54.57% 86.7% 59.9% 75.7%

[0040] This result shows that pulsed electric field treatment leads to higher yield of protein in the solid.

EXAMPLE 3: PRODUCTION OF DRIED PROTEIN MASS FROM LARVAE OF HERMETIA ILLUCENS

[0041] As an example of insect larvae, approximately 1 kg of fresh, live larvae of Hermetia illucens was suspended in cold tap water for washing and separated from it using a perforated plate, re-suspended in cold tap water and subjected to pulsed electric fields from 1 kV/cm, pulse duration from 5 μs, pulse frequency from 1 to 500 Hz larvae.

[0042] The larvae were then separated from the water using a perforated plate. The larvae were comminuted with the adhering water by means of a cutter, meat grinder or hammer mill, and the obtained insect mass was directly fractionated into three phases by means of a spindle press, alternatively by means of a 3-phase separating decanter, at a pressure of 5 MPa to obtain with this one step a lipid-rich liquid phase (oil phase), an aqueous liquid phase and a solid.

[0043] The compositions of the respective solid and liquid phases are shown in the Table.

TABLE-US-00003 Oil solid, oil phase, solid, phase, aqueous comparison, comparison, liquid phase, with with liquid phase, without without comparison, PEF PEF with PEF PEF PEF without PEF mass 0.21 kg 0.14 kg 0.65 kg 0.25 kg 0.12 kg 0.63 kg protein 40%  2%  7% 46% 3%  2% other 49%  2% low content, 38% 2% low content, solids not not determined determined oil  3% 93% low content, 10% 93%  low content, not not determined determined water  8%  3% 93%  6% 2% 98%

[0044] This result shows that treatment with pulsed electric fields leads to a high yield of protein and lower oil content in the solid, a high yield of protein in the aqueous liquid phase, and a high yield of oil in the separated liquid oil phase. Accordingly, it is generally preferred to isolate the protein from the aqueous liquid phase.

[0045] FIG. 3 shows the relative drying behavior of the solid phases produced by the process upon application of pulsed electric fields (PEF) of 5 kJ/kg larvae, 10 kJ/kg larvae and 20 kJ/kg larvae to the larvae, respectively, in relation to a solid phase used at the beginning of drying (0 s), which was produced by the same process steps but without exposure to pulsed electric fields (untreated).

[0046] This result shows that application of pulsed electric fields significantly shortens the drying time. It was also found that, compared to the process without PEF, application of pulsed electric fields leads to a 10 vol.-% higher separation of lipids contained in the liquid phase from the insect mass.