A method to control 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 using at least one supply connection, wherein:
- the extraction container has an inner region that, in a top region, possesses at least one supply connection for supplying the primary mixture and for supplying the transition component as a secondary solvent, and, in a bottom region, a drainage connection for drainage of a mixture consisting of an extract and a raffinate,
- the drainage connection discharges into a drain line,
- the drain line has, viewed in a direction of flow and at a vertical distance from the drainage connection by a supply height relative to the direction of gravity, a control valve, a first mass flow meter for determining a first mass flow for the mixture, a separating device for separating the mixture into the extract and a raffinate with residual moisture, a dehumidification apparatus for dehumidifying the raffinate with residual moisture, and a second mass flow meter for determining a second mass flow for an extract free from raffinate with residual moisture, and
- the separating device and the dehumidification apparatus each comprise a vibration or shaking sieve;
- (ii) supplying the second mass to the first mass and distributing and mixing the second mass into and with the first mass;
- (iii) discharging, into the drain line, a mixture consisting of the extract and the raffinate from the extraction container using the drainage connection;
- (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 treating 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 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, using the first mass flow meter, the first mass flow of the mixture discharged according to step (iii), and determining, using the second mass flow meter, the 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 a degree of dehumidification by comparing the first mass flow with the second mass flow, wherein a 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 time span;
- and
- (ix) controlling, using a control apparatus, the degree of dehumidification carried out according to steps (v) and (vi) by feedback control intervention to the first mass flow and a supply of the mechanical energy based on the tolerable portion, wherein the control apparatus, in terms of signaling, is connected to the control valve, the first mass flow meter, the second mass flow meter, and the vibration or shaking sieve.