Renewable diesel fuel production in retrofitted fossil petroleum refinery to produce biofuel and bio-feedstock for steam crackers

Patent metadata

Field	Value
Publication number	US-11549062-B2
Application number	US-201917059581-A
Country	US
Kind code	B2
Filing date	May 28, 2019
Priority date	May 30, 2018
Publication date	Jan 10, 2023
Grant date	Jan 10, 2023

Abstract

The present invention relates to a process for the conversion of a feedstock comprising at least 50 wt % related to the total weight of the feedstock of triglycerides, fatty acid esters and/or fatty acids having at least 10 carbon atoms into hydrogen, olefins, dienes, aromatics, gasoline, diesel fuel, jet fuel, naphtha and liquefied petroleum gas comprising:
a) introducing of said feedstock in a first reactor to produce linear paraffins in presence of a hydrodesulfurization catalyst and hydrogen, b) separating the effluent of said first reactor in at least three parts to produce at least a first stream comprising part of said linear paraffins and at least a second stream comprising part of said linear paraffins, and at least a third stream comprising part of said linear paraffins c) sending said first stream to a steam cracker to produce hydrogen, olefins, dienes, aromatics and gasoline, diesel fuel being further fractionated; d) introducing said second stream into a second reactor in presence of a hydrocracking or hydroisomerization catalyst to produce a mixture comprising diesel fuel, jet fuel, naphtha and liquefied petroleum gas being further fractionated e) blending said third stream with the diesel fuel obtained at said step d)

wherein said feedstock of said first reactor is diluted in order to limit the temperature increase within said first reactor; and wherein before entering the first reactor said dilution is performed with a weight ratio diluent:feedstock being 1:1, and wherein said diluent comprises at least part of said paraffins obtained at step b).

First claim

The invention claimed is:

1. A process for the conversion of a feedstock comprising at least 50 wt % related to the total weight of the feedstock of triglycerides, fatty acid esters and/or fatty acids having at least 10 carbon atoms into hydrogen, olefins, dienes, aromatics, gasoline, diesel fuel, jet fuel, naphtha and liquefied petroleum gas comprising:
a) introducing the feedstock in a first reactor to produce linear paraffins in presence of a hydrodesulfurization catalyst and hydrogen;
b) separating the linear paraffins produced by the first reactor in at least three parts to produce at least a first stream comprising part of the linear paraffins, a second stream comprising part of the linear paraffins, and third stream comprising part of the linear paraffins;
c) sending the first stream to a steam cracker to produce hydrogen, olefins, dienes, aromatics and gasoline;
d) introducing the second stream into a second reactor in presence of a hydrocracking or hydro-isomerization catalyst to produce a mixture comprising diesel fuel, jet fuel, naphtha and liquefied petroleum gas; and
e) blending the third stream with the diesel fuel obtained at the step d),

wherein the feedstock of the first reactor is diluted in order to limit the temperature increase within the first reactor; and wherein before entering the first reactor the dilution is performed with a weight ratio diluent : feedstock being 1:1 to 4:1, and wherein the diluent comprises at least part of the paraffins obtained at step b).

2. The process according to claim 1 wherein the first and second reactors are existing units and wherein the process is obtained from the retrofit of an existing plant.

3. The process according to claim 1 wherein the feedstock comprises at least 75 wt % of triglycerides, fatty acid esters and/or fatty acids related to the total weight of the feedstock.

4. The process according to claim 1 wherein hydrogen used in step a) is supplied from a naphtha reformer, the steam cracker of step c), or a steam methane reformer.

5. The process according to claim 1 wherein in step c) a sum of hydrogen, ethylene, propylene, butadiene and benzene produced from the steam cracker is at least 60 wt % of the first stream converted in the steam cracker.

6. The process according to claim 1 wherein the naphtha or liquefied petroleum gas or any mixture thereof produced in step d) are mixed with the first stream of step c) before being sent to the steam cracker of step c).

7. The process according to claim 1 wherein the triglycerides, fatty acids esters and/or fatty acids contained in the feedstock are obtained by at least one of the following purification steps:
chemical refining or physical refining, of fats and oils, or
hydrolysis of triglycerides of fats and oils, to obtain glycerol and a mixture of free fatty acids.

8. The process according to claim 1 wherein the hydrodesulfurization catalyst comprises Ni, Mo, W, or Co, or mixtures, metal oxides, or metal sulphides thereof.

9. The process according to claim 1 wherein the dilution of feedstock to limit the temperature increase within the first reactor is performed with a weight ratio diluent : feedstock being 2:1.

10. The process according to claim 1 wherein the first reactor contains a plurality of catalytic beds comprising the hydrodesulfurization catalyst and wherein between the catalytic beds part of the feedstock of the first reactor and/or hydrogen containing gas or any mixture thereof are injected in order to control temperature across the plurality of catalytic beds.

11. The process according to claim 1 wherein the first reactor contains a plurality of catalytic beds comprising the hydrodesulfurization catalyst and wherein between the catalytic beds part of the paraffins obtained at step b) are injected in order to control temperature across the plurality of catalytic beds.

12. The process according to claim 1 wherein the feedstock is heated upstream of the first reactor and the linear paraffins of the second stream are heated upstream of the second reactor.

13. The process according to claim 7 , wherein the chemical refining or physical refining of fats and oils comprises degumming, bleaching, steam distillation, or vacuum distillation.

14. The process according to claim 8 , wherein the mixtures of Ni, Mo, W, or Co comprise NiW, NiMo, CoMo, NiCoW, NiCoMo, NiMoW, or CoMoW.

Assignees

• Total Res & Technology Feluy

Inventors

• Vermeiren Walter

Classifications

• C10G9/36 Primary

  with heated gases or vapours · CPC title

• C10G2400/02

  Gasoline · CPC title

• C10G2400/30

  Aromatics · CPC title

• C10G47/00

  Cracking of hydrocarbon oils, in the presence of hydrogen or hydrogen- generating compounds, to obtain lower boiling fractions (C10G15/00 takes precedence; destructive hydrogenation of non-melting solid carbonaceous or similar materials C10G1/06) · CPC title

• C10G3/52

  Hydrogen in a special composition or from a special source · CPC title