make 41100 metric loads per calendar year of hydrogen gasoline at 97.4mol% chastity at 20 club absolute stress and 43 C, by steam réforming the naphtha?feed of naphtha at 30 Chemical and 25 pub absolute stress. Componént MoI% Hydrogen 52.01 ![Steam Reforming Massbalance Steam Reforming Massbalance](/uploads/1/2/5/7/125739730/975976595.jpg)
the naphtha includes 15.3% hydrogen by bulk. The average molecular formulation of this naphtha will be G11H24. Queries1.Desulfiration on naptha to L2S material stability? 2.conversion of naptha in principal and supplementary reformer? 3.How very much Vapor to carbon percentage should i use since the procedure needs alot of energy?
Combined Steam Reforming and Partial Oxidation of Methane to Synthesis Gas under Electrical Discharge. Korada Supat† and Sumaeth Chavadej‡. The Petroleum and Petrochemical College, Chulalongkorn University, Bangkok 10330, Thailand. Lobban§ and Richard G. Steam reforming process appears as the most feasible and economical technology to produce hydrogen with high quality. Material and energy balances were calculated for all process equipment’s of SMR process. Also, designing of the process plant equipment is very essential for the process flow diagram.
Carbon
0.84
![Steam Reforming Massbalance Steam Reforming Massbalance](/uploads/1/2/5/7/125739730/975976595.jpg)
Sulphur
22pevening by excess weightBest Regards