A process for producing an aqueous polymer dispersion by free-radically initiated aqueous emulsion polymerization, characterized in that, in an aqueous medium,
- (a) 40 to 75 parts by weight of styrene,
- (b) 24.9 to 59.9 parts by weight of butadiene,
- (c) 0.1 to 10 parts by weight of at least one ethylenically unsaturated carboxylic acid and
- (d) 0 to 15 parts by weight of one or more other monomers, where the parts by weight of monomers (a) to (d) add up to 100 parts by weight, are polymerized by a monomer feed process comprising the following steps:
- a) initially charging a seed latex and 1 to 10 parts by weight of monomers based on the total amount of monomers,
- b) initiating the polymerization at a temperature ≥80° C. in this initial charge,
- c) and then constantly metering monomers and emulsifier into this reaction mixture,
- c1) characterized in that, at a time when 40% to 55% of the total monomer metering time has elapsed and 40 to 55 parts by weight of the amount of monomers to be metered in have been metered in, the metering rate of the emulsifier is increased for a period P2 of not longer than 30 minutes to 10 to 150 times the average metering rate of the emulsifier during the period P1, where the period P1 is the preceding period of time commencing with the start of emulsifier metering,
- c2) and, at a time when 60% to 85% of the total monomer metering time has elapsed and 60 to 85 parts by weight of the amount of monomers to be metered in have been metered in, the metering rate of the emulsifier is increased for a period P4 of not longer than 30 minutes to 10 to 150 times the average metering rate of the emulsifier in period P1,
- with the proviso that the aqueous polymer dispersion has a solids content of ≥58% by weight.