Process for the manufacture of diesel range hydrocarbons
The invention relates to a process for the manufacture of diesel range hydrocarbons wherein a feed is hydrotreated in a hydrotreating step and isomerized in an isomerization step, and a feed comprising fresh feed containing more than 5 wt % of free fatty acids and at least one diluting agent is hydrotreated at a reaction temperature of 200-400° C., in a hydrotreating reactor in the presence of catalyst, and the ratio of the diluting agent/fresh feed is 5-30:1.
1. A process for the manufacture of diesel range hydrocarbons comprising the following steps:
introducing a feed comprising at least one organic or inorganic sulphur compound hydrogen, and a feedstock comprising bio oil and/or fat from renewable sources to a hydrotreatment step in which hydrocarbons are formed,
isomerizing the formed hydrocarbons in an isomerization step,
wherein
gas phase impurities formed in the hydrotreatment step are removed from the stream comprising hydrocarbons prior to contacting the hydrocarbons with the isomerization catalyst.
2. The process according to claim 1 , further comprising a step of purifying the feedstock prior to the hydrotreatment step so as to remove impurities.
3. The process according to claim 1 , wherein the gas phase impurities formed in the hydrotreatment step comprise propane, water, carbon oxides, H 2 S, NH 3 or mixtures thereof.
4. The process according to claim 1 , wherein the removal of the gas phase impurities formed in the hydrotreatment step is performed in a stripping step upstream of the isomerization catalyst.
5. The process according to claim 4 , wherein the stripping step is performed by stripping with water vapor or a suitable gas comprising light hydrocarbon, nitrogen or hydrogen.
6. The process according to claim 4 , wherein the stripping step is carried out in a counter-current manner.
7. The process according to claim 1 , wherein the feedstock comprises more than 10 wt % of free fatty acids.
8. The process according to claim 1 , wherein the feedstock contains less than 10 w-ppm alkaline and alkaline earth metals, calculated as elemental alkaline and alkaline earth metals, less than 10 w-ppm other metals, calculated as elemental metals, and less than 30 w-ppm phosphorus, calculated as elemental phosphorus.
9. The process according to claim 2 , wherein the purified feedstock contains less than 10 w-ppm alkaline and alkaline earth metals, calculated as elemental alkaline and alkaline earth metals, less than 10 w-ppm other metals, calculated as elemental metals, and less than 30 w-ppm phosphorus, calculated as elemental phosphorus.
10. The process according to claim 1 , wherein the feed contains 50-20000 w-ppm of sulphur, calculated as elemental sulphur.
11. The process according to claim 1 , wherein the feedstock is selected from plant oils/fats, animal fats/oils, fish fats/oils, fats contained in plants bred by means of gene manipulation, recycled fats of the food industry and mixtures thereof.
12. The process according to claim 1 , wherein the feedstock is selected from rapeseed oil, colza oil, canola oil, tall oil, sunflower oil, soybean oil, hempseed oil, olive oil, linseed oil, mustard oil, palm oil, peanut oil, castor oil, coconut oil, lard, tallow, train oil or fats contained in milk.
13. The process according to claim 1 , wherein an isomerization catalyst containing molecular sieve is used in the isomerization step.
14. The process according to claim 2 , wherein the gas phase impurities formed in the hydrotreatment step comprise propane, water, carbon oxides, H 2 S, NH 3 or mixtures thereof.
15. The process according to claim 2 , wherein the removal of the gas phase impurities formed in the hydrotreatment step is performed in a stripping step upstream of the isomerization catalyst.
16. The process according to claim 2 , wherein the stripping step is performed by stripping with water vapor or a suitable gas comprising light hydrocarbon, nitrogen or hydrogen.
17. The process according to claim 2 , wherein the stripping step is carried out in a counter-current manner.
18. The process according to claim 2 , wherein the purified feedstock comprises more than 10 wt % of free fatty acids.
19. The process according to claim 2 , wherein the feed comprising the purified feedstock contains 50-20000 w-ppm of sulphur, calculated as elemental sulphur.
20. The process according to claim 2 , wherein an isomerization catalyst containing molecular sieve is used in the isomerization step.