A method for controlling the introduction of a pulverulent material into a liquid consisting of at least one component for a batch mixing method, • in which the introduction and treatment of the pulverulent material takes place under the conditions of a dwell time behavior of a discontinuously working homogenous reaction tank such that ∘ an amount of liquid (m F) is presented and the pulverulent material is discontinuously fed into this liquid, ∘ the liquid and the pulverulent material are constantly stirred and/or mixed to form a mixed product and the mixed product is homogenized, and ∘ the pulverulent material is fed in until a time-dependent progression of a dry material concentration (c(t)) of the pulverulent material in the mixed product has grown to a specified end value (c E), characterized in that • a formulation of the mixed product, at least regarding the time-dependent progression of a dry material concentration (c(t)) associated with the specified end value (c E), and the reaction conditions are each specified in the form of default data, • the discontinuous feeding of the pulverulent material takes place in a pulsed manner by a chronological sequence of metering pulses (i) which are each characterized by a volume flow of the pulverulent material (ṁ P), a duration of the metering pulse (Δt1), and a time interval between neighboring metering pulses (Δt2), • the time-dependent progression of a dry material concentration (c(t)) ending in the specified end value (c E) is defined by the sequence of clearly defined metering impulses (i), • a time-dependent current consumption (I(t)) is ascertained which is proportional to a mixing and/or shearing and homogenizing power required for a temporarily present mixed product (M*), • a time-dependent progression of a reference current consumption (I o (t)) is used from the default data which is characteristic of the stirring and/or shearing and homogenizing power to be delivered to the homogenized mixed product under the conditions of the associated time-dependent progression of a dry material concentration (c(t)), and • at the end of the time interval between neighboring metering pulses (Δt2) and when the time-dependent current consumption (I(t)) deviates from the respectively associated value in the time-dependent progression of a reference current consumption (I o (t)) by more than a specified tolerance, either higher or lower, the duration of the metering pulse (Δt1) for the following metering pulse (i) is shortened in the first case and extended in the second case. • in which the introduction and treatment of the pulverulent material takes place under the conditions of a dwell time behavior of a discontinuously working homogenous reaction tank such that ∘ an amount of liquid (m F) is presented and the pulverulent material is discontinuously fed into this liquid, ∘ the liquid and the pulverulent material are constantly stirred and/or mixed to form a mixed product and the mixed product is homogenized, and ∘ the pulverulent material is fed in until a time-dependent progression of a dry material concentration (c(t)) of the pulverulent material in the mixed product has grown to a specified end value (c E), characterized in that ∘ an amount of liquid (m F) is presented and the pulverulent material is discontinuously fed into this liquid, ∘ the liquid and the pulverulent material are constantly stirred and/or mixed to form a mixed product and the mixed product is homogenized, and ∘ the pulverulent material is fed in until a time-dependent progression of a dry material concentration (c(t)) of the pulverulent material in the mixed product has grown to a specified end value (c E), • a formulation of the mixed product, at least regarding the time-dependent progression of a dry material concentration (c(t)) associated with the specified end value (c E), and the reaction conditions are each specified in the form of default data, • the discontinuous feeding of the pulverulent material takes place in a pulsed manner by a chronological sequence of metering pulses (i) which are each characterized by a volume flow of the pulverulent material (ṁ P), a duration of the metering pulse (Δt1), and a time interval between neighboring metering pulses (Δt2), • the time-dependent progression of a dry material concentration (c(t)) ending in the specified end value (c E) is defined by the sequence of clearly defined metering impulses (i), • a time-dependent current consumption (I(t)) is ascertained which is proportional to a mixing and/or shearing and homogenizing power required for a temporarily present mixed product (M*), • a time-dependent progression of a reference current consumption (I o (t)) is used from the default data which is characteristic of the stirring and/or shearing and homogenizing power to be delivered to the homogenized mixed product under the conditions of the associated time-dependent progression of a dry material concentration (c(t)), and • at the end of the time interval between neighboring metering pulses (Δt2) and when the time-dependent current consumption (I(t)) deviates from the respectively associated value in the time-dependent progression of a reference current consumption (I o (t)) by more than a specified tolerance, either higher or lower, the duration of the metering pulse (Δt1) for the following metering pulse (i) is shortened in the first case and extended in the second case.