The concept of supported ionic liquid phase (SILP) catalysis has been established in recent years by our group and others. Its application in continuous catalytic gas‐phase processes provides a very attractive way to bridge the gap between homogeneous and heterogeneous catalysis. In this contribution, we extend SILP hydroformylation catalysis to reactions with a highly diluted, technical C4 feed containing 1.5 % 1‐butene, 28.5 % 2‐butenes, and 70 % of inert n‐butane. To obtain the desired product, n‐pentanal, the Rh‐biphephos catalyst system was immobilized in the SILP system to allow for consecutive isomerization/hydroformylation activity. The resulting SILP catalyst material converted up to 81 % of the reactive butenes, with a residence time of 155 s in the reactor. An n‐pentanal selectivity greater than 92 % was realized for more than 500 h time‐on‐stream in the continuous gas‐phase reaction. Post‐reaction NMR studies revealed no significant loss of the phosphite ligand through ligand oxidation during the reaction.