A process for integrated production of ammonia and urea comprising the steps of: (a) providing a crude synthesis gas stream comprising H 2, N 2 and CO 2; (b) compressing the crude synthesis gas stream; (c) scrubbing the crude synthesis gas stream with liquid NH 3 in a first scrubbing column to form a CO 2 -enriched first condensate and a CO 2 -depleted prepurified synthesis gas stream; (d) cooling the prepurified synthesis gas stream and separating a first liquid phase; (e) scrubbing the prepurified synthesis gas stream with liquid NH 3 in a second scrubbing column to form a CO 2 -enriched second condensate and a CO 2 -depleted purified synthesis gas stream; (f) cooling the purified synthesis gas stream and separating a second liquid phase; (g) scrubbing the purified synthesis gas stream with liquid NH 3 in a third scrubbing column to form a CO 2 -enriched third condensate and a CO 2 -depleted postprepurified synthesis gas stream; (h) cooling the postpurified synthesis gas stream and separating a third liquid phase; (i) combining the first condensate from step (c), the second condensate from step (e) and the third condensate from step (g) to form a reactant stream comprising NH 3 and CO 2 which may be at least partly in a bound state in the form of ammonium carbamate; and (j) synthesizing urea from the reactant stream to form an aqueous urea composition and a residual gas stream comprising unconverted NH 3 and CO 2; wherein the process further comprises: - dividing the crude synthesis gas stream from step (b) into a first crude synthesis gas substream and a second crude synthesis gas substream; - stripping the aqueous urea composition from step (j) with the first crude synthesis gas substream to form a stripping gas stream; - combining the stripping gas stream with the second crude synthesis gas substream; and - cooling the thus-combined crude synthesis gas stream and separating a fourth liquid phase. (a) providing a crude synthesis gas stream comprising H 2, N 2 and CO 2; (b) compressing the crude synthesis gas stream; (c) scrubbing the crude synthesis gas stream with liquid NH 3 in a first scrubbing column to form a CO 2 -enriched first condensate and a CO 2 -depleted prepurified synthesis gas stream; (d) cooling the prepurified synthesis gas stream and separating a first liquid phase; (e) scrubbing the prepurified synthesis gas stream with liquid NH 3 in a second scrubbing column to form a CO 2 -enriched second condensate and a CO 2 -depleted purified synthesis gas stream; (f) cooling the purified synthesis gas stream and separating a second liquid phase; (g) scrubbing the purified synthesis gas stream with liquid NH 3 in a third scrubbing column to form a CO 2 -enriched third condensate and a CO 2 -depleted postprepurified synthesis gas stream; (h) cooling the postpurified synthesis gas stream and separating a third liquid phase; (i) combining the first condensate from step (c), the second condensate from step (e) and the third condensate from step (g) to form a reactant stream comprising NH 3 and CO 2 which may be at least partly in a bound state in the form of ammonium carbamate; and (j) synthesizing urea from the reactant stream to form an aqueous urea composition and a residual gas stream comprising unconverted NH 3 and CO 2; - dividing the crude synthesis gas stream from step (b) into a first crude synthesis gas substream and a second crude synthesis gas substream; - stripping the aqueous urea composition from step (j) with the first crude synthesis gas substream to form a stripping gas stream; - combining the stripping gas stream with the second crude synthesis gas substream; and - cooling the thus-combined crude synthesis gas stream and separating a fourth liquid phase.