A method to control the production of an extract by means of solid-liquid extraction by means of an extraction container in which a secondary solvent with a first mass and a primary mixture consisting of a solid primary solvent and a transition component with a second mass are brought into contact with each other for a predetermined dwell time to obtain the extract, and in which the obtained extract and a complementary portion of raffinate are separated from each other after the dwell time, the method comprising:
- (i) providing the first mass in the extraction container;
- (ii) supplying the second mass to the first mass without spatial constraints and distributing and mixing the second mass into and with the first mass;
- (iii) discharging a mixture consisting of the extract and the raffinate from the extraction container;
- (iv) separating the mixture discharged according to step (iii) into the raffinate with residual moisture and an extract released from the raffinate with residual moisture;
- (v) further treatment of the raffinate with residual moisture at least such that the residual moisture consisting of the extract is at least partly removed from the raffinate with residual moisture by dehumidification and is supplied to the already separated extract;
- (vi) dehumidifying the raffinate with residual moisture to a tolerable portion of extract in the raffinate with residual moisture by supplying mechanical energy to the raffinate with residual moisture;
- (vii) determining a first mass flow of the mixture discharged according to step (iii), and a second mass flow of the extract freed from raffinate with residual moisture obtained according to steps (iv) and (v), in each case over a span of time;
- (viii) determining the degree of dehumidification by comparing the first mass flow with the second mass flow, wherein the mass difference resulting therefrom in the time span before and after humidification is compared with a mass difference arising with complete dehumidification that corresponds to the mass of the primary solvent before extraction within the relevant time span;
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- (ix) controlling the degree of dehumidification carried out according to steps (v) and (vi) by feedback control intervention to the first mass flow and the supply of mechanical energy.