초록 ▼

A process has been developed for producing a hydrocarbon component useful as diesel fuel from biorenewable feedstocks such as plant oils and greases. The process involves hydrogenating and deoxygenating, i.e. decarboxylating and/or hydrodeoxygenating the feedstock to provide a hydrocarbon fraction u

A process has been developed for producing a hydrocarbon component useful as diesel fuel from biorenewable feedstocks such as plant oils and greases. The process involves hydrogenating and deoxygenating, i.e. decarboxylating and/or hydrodeoxygenating the feedstock to provide a hydrocarbon fraction useful as a diesel fuel. An optional pretreatment step to remove contaminants such as alkali metals from the feedstock can also be carried out. If desired, the hydrocarbon fraction can be isomerized to improve cold flow properties.

대표청구항 ▼

The invention claimed is: 1. A process for producing a hydrocarbon fraction from a biorenewable feedstock comprising pre-treating the feedstock in a pretreatment zone at pretreatment conditions to remove at least a portion of contaminants in the feedstock and produce a first effluent stream; reacti

The invention claimed is: 1. A process for producing a hydrocarbon fraction from a biorenewable feedstock comprising pre-treating the feedstock in a pretreatment zone at pretreatment conditions to remove at least a portion of contaminants in the feedstock and produce a first effluent stream; reacting the first effluent stream in a reaction zone by contacting the first effluent stream with a catalyst at reaction conditions comprising a temperature of about 200�� C. to about 300�� C., a hydrogen partial pressure of about 1034 kPa (150 psi) to less than 2000 kPa (290 psi) and a liquid hourly space velocity of about 0.5 hr-1 to about 2 hr-1 thereby hydrogenating and deoxygenating the first effluent stream to provide a reaction product comprising a hydrocarbon fraction comprising n-paraffins. 2. The process of claim 1 further comprising isomerizing the reaction product by contacting it with an isomerization catalyst at isomerization conditions to isomerize at least a portion of the n-paraffins to iso-paraffins. 3. The process of claim 1 where the pretreatment step comprises contacting the feedstock with an acidic ion exchange resin, contacting the feedstock with an acid solution, or contacting the feedstock with a guard bed. 4. The process of claim 1 where deoxygenation comprises at least one of decarboxylation and hydro-deoxygenation. 5. The process of claim 1 further comprising mixing the first effluent stream with a petroleum fraction. 6. A process for producing a hydrocarbon fraction from a biorenewable feedstock comprising passing the feedstock to a reaction zone; contacting the feedstock with a catalyst at reaction conditions comprising a temperature of about 200�� C. to about 300�� C., a hydrogen partial pressure of about 1034 kPa (150 psi) to less than 2000 kPa (290 psi) and a liquid hourly space velocity of about 0.5 hr-1 to about 2 hr-1 thereby deoxygenating the first effluent stream and providing a reaction product comprising a hydrocarbon fraction comprising n-paraffins. 7. The process of claim 5 further comprising isomerizing the reaction product by contacting it with an isomerization catalyst at isomerization conditions to isomerize at least a portion of the n-paraffins to iso-paraffins. 8. The process of claim 5 where deoxygenation comprises at least one of decarboxylation and hydro-deoxygenation. 9. The process of claim 5 where prior to passing the feedstock to the reaction zone, the feedstock is contacted with an acidic ion exchange resin or an acid solution at pretreatment conditions thereby removing at least a portion of contaminants in the feedstock. 10. The process of claim 5 further comprising mixing the feedstock with a petroleum fraction.