Process to prepare base oil from a Fisher-Tropsch synthesis product
View Patent ↗A process to prepare base oils from a Fischer-Tropsch synthesis product by (a) separating the Fischer-Tropsch synthesis product into a fraction (i) boiling in the middle distillate range and below, a heavy ends fraction (iii) and an intermediate base oil precursor fraction (ii) boiling between fraction (i) and fraction (iii), (b) subjecting the base oil precursor fraction (ii) to a catalytic hydroisomerisation and catalytic dewaxing process to yield one or more base oil grades, (c) subjecting the heavy ends fraction (iii) to a conversion step to yield a fraction (iv) boiling below the heavy ends fraction (iii) and (d) subjecting the high boiling fraction (v) of fraction (iv) to a catalytic hydroisomerisation and catalytic dewaxing process to yield one or more base oil grades.
1. A process to prepare base oils from a Fischer-Tropsch synthesis product, the processing comprising
(a) separating the Fischer-Tropsch synthesis product into a fraction (i) boiling in the middle distillate range and below, a heavy ends fraction (iii) and an intermediate base oil precursor fraction (ii) boiling between fraction (i) and fraction (iii);
(b) subjecting the base oil precursor fraction (ii) to a first catalytic hydroisomerization and catalytic dewaxing process to yield one or more base oil grades;
(c) subjecting the heavy ends fraction (iii) to a thermal cracking process to yield a fraction (iv) boiling below the heavy ends fraction (iii); and,
(d) subjecting a high boiling fraction (v) of fraction (iv) to the first catalytic hydroisomerization and catalytic dewaxing process or a second catalytic hydroisomerization and catalytic dewaxing process to yield one or more base oil grades.
2. The process of according to claim 1 , wherein the heavy ends fraction (iii) has an initial boiling point of between 500° C. and 600° C.
3. The process of claim 1 , wherein step (b) is performed in the presence of a catalyst comprising a noble metal hydrogenation component and a molecular sieve selected from the group consisting of zeolite beta, ZSM-23, ZSM-22, ZSM-35 or ZSM-12.
4. The process of claim 1 , wherein step (d) is performed in the presence of a catalyst comprising a noble metal hydrogenation component and a molecular sieve selected from the group of zeolite beta, ZSM-23, ZSM-22, ZSM-35 or ZSM-12.
5. The process of claim 1 , wherein the feed to step (a), step (b) and/or step (c) is first hydrogenated.
6. The process of claim 1 , wherein the fraction boiling below 370° C. as obtained in step (c) is subjected to an oligomerization step (f).
7. The process of claim 6 , wherein a base oil fraction is prepared in step (f) and which base oil fraction is mixed with the base oil products obtained in step (b) and/or (d).
8. The process of claim 6 , wherein a base oil fraction is prepared in step (f) and which base oil fraction is dewaxed in step (b).
9. The process of claim 1 , wherein the effluent of step (c) is provided to step (a), such that in effect steps (b) and (d) take place simultaneously.
10. The process of claim 2 , wherein step (b) is performed in the presence of a catalyst comprising a noble metal hydrogenation component and a molecular sieve selected from the group consisting of zeolite beta, ZSM-23, ZSM-22, ZSM-35 or ZSM-12.
11. The process of claim 2 , wherein step (d) is performed in the presence of a catalyst comprising a noble metal hydrogenation component and a molecular sieve selected from the group of zeolite beta, ZSM-23, ZSM-22, ZSM-35 or ZSM-12.
12. The process of claim 2 , wherein the feed to step (a), step (b) and/or step (c) is first hydrogenated.