The conversion of Fischer-Tropsch derived olefins over solid phosphoric acid (SPA) is practiced commercially. Although it is mostly used for motor-gasoline production, it is also used to produce distillates to increase refinery flexibility. During distillate production, the distillate yield can be increased by recycling some of the naphtha from the process or by cofeeding naphtha-range Fischer-Tropsch olefins. The SPA catalyzed conversion of Fischer-Tropsch olefins and other olefinic naphtha feed materials was investigated at pilot plant scale in the range of 175-260°C and 3.8 MPa. Contrary to expectations based on propene tetramermode operation, it was found that the distillate yield was limited to 70% when processing olefinic feed mixtures containing propene and naphtha. The weak interaction of long chain olefins with phosphoric acid mechanistically limited distillate production, and naphtha-range olefin oligomerization was disrupted by short chain olefins, like propene, which became the main carbocation source. Inhibition of the oligomerization reaction was also found when processing some of the oxygenate containing Fischer-Tropsch material. A processing methodology could be suggested to improve distillate selectivity by separate processing of the short chain and naphtharange olefins, but no productivity advantage was demonstrated.