To optimize industrial Fischer-Tropsch (FT) synthesis with the slurry bubble column reactor (SBCR) and ironbased catalyst

a comprehensive process model for FT synthesis that includes a detailed SBCR model

gas liquid separation model

simplified CO

2

removal model and tail gas cycle model was developed. An effective iteration algorithm was proposed to solve this process model

and the model was validated by industrial demonstration experiments data (SBCR with 5.8 m diameter and 30 m height)

with a maximum relative error 10% for predicting the SBCR performances. Subsequently

the proposed model was adopted to optimize the industrial SBCR performances simultaneously considering process and reactor parameters variations. The results show that C

5+

yield increases as catalyst loading increases within 10-70 ton and syngas H

2

/CO value decreases within 1.3-1.6

but it doesn't increase obviously when the catalyst loading exceeds 45 ton (about 15 wt% concentration). Higher catalyst loading will result in higher difficulty for wax/catalyst separation and higher catalyst cost. Therefore

the catalyst loading (45 ton)

is recommended for the industrial demonstration SBCR operation at syngas H

2

/CO=1.3

and the C

5+

yield is about 402 ton" per day

which has an about 16% increase than the industrial demonstration run result.