A method for controlling the introduction of a pulverulent material into a liquid consisting of at least one component for an inline mixing method, • in which the introduction and treatment of the pulverulent material take place under the conditions of a dwell time behavior of a continuously working homogenous reaction tank such that o the liquid is continuously fed to a mixing container, wherein the goal is a specified, temporally unchanging dry material concentration (c) of the pulverulent material in the 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 mixed product is continuously discharged corresponding to the fed amounts of liquid and pulverulent material, • in which a formulation of the mixed product, at least regarding the specified dry material concentration (c), and the reaction conditions are each specified in the form of default data, characterized in that • the pulverulent material is discontinuously fed to the mixing container, • 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 mass flow of the pulverulent material (ṁ P), a duration of the metering pulse (Δt1), and a time interval between neighboring metering pulses (Δt2), • the specified dry material concentration (c) is defined by a fixed duration-to-time interval ratio V between the duration of the metering pulse (Δt1) and the associated time interval between neighboring metering pulses (Δt2) (V = Δt1/Δt2 = constant), • a time-dependent current consumption (I(t)) is ascertained which is proportional to a stirring and/or shearing and homogenizing power required for a temporarily present mixed product (M*), • a reference current consumption (I o) 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, 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 reference current consumption (I o (t)) by more than a specified tolerance, either higher or lower, and in compliance with the fixed duration-to-time interval ratio, 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 take place under the conditions of a dwell time behavior of a continuously working homogenous reaction tank such that o the liquid is continuously fed to a mixing container, wherein the goal is a specified, temporally unchanging dry material concentration (c) of the pulverulent material in the 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 mixed product is continuously discharged corresponding to the fed amounts of liquid and pulverulent material, o the liquid is continuously fed to a mixing container, wherein the goal is a specified, temporally unchanging dry material concentration (c) of the pulverulent material in the 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 mixed product is continuously discharged corresponding to the fed amounts of liquid and pulverulent material, • in which a formulation of the mixed product, at least regarding the specified dry material concentration (c), and the reaction conditions are each specified in the form of default data, characterized in that • the pulverulent material is discontinuously fed to the mixing container, • 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 mass flow of the pulverulent material (ṁ P), a duration of the metering pulse (Δt1), and a time interval between neighboring metering pulses (Δt2), • the specified dry material concentration (c) is defined by a fixed duration-to-time interval ratio V between the duration of the metering pulse (Δt1) and the associated time interval between neighboring metering pulses (Δt2) (V = Δt1/Δt2 = constant), • a time-dependent current consumption (I(t)) is ascertained which is proportional to a stirring and/or shearing and homogenizing power required for a temporarily present mixed product (M*), • a reference current consumption (I o) 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, 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 reference current consumption (I o (t)) by more than a specified tolerance, either higher or lower, and in compliance with the fixed duration-to-time interval ratio, 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.