High purity olefinic naphthas for the production of ethylene and propylene
The present invention relates to an olefinic naphtha and a process for producing lower olefinc from this naphtha. In the process of the present invention for producing lower olefins, preferably ethylene, at least a portion of a hydrocarbon asset is converted to synthesis gas and at least a portion of the synthesis gas is converted to an olefinic naphtha by a Fischer-Tropsch process. At least a portion of the olefinic naphtha is converted in a naphtha cracker to a product stream comprising lower olefins, and at least a portion of the lower olefins from the product stream of the cracker are recovered.
1. An olefinic naphtha comprising:
a. olefins in an amount of 10 to 80 weight %, wherein the olefins comprise greater than 50 weight % linear primary olefins;
b. non-olefins in an amount of 20 to 90 weight %, wherein the non-olefins comprise greater than 50 weight % paraffins;
c. sulfur in an amount of less than 10 ppm by weight;
d. nitrogen in an amount of less than 10 ppm by weight;
e. aromatics in an amount less than 10 weight %;
f. a total acid number of between 0.32 mg KOH/g and 1.5 mg KOH/g; and
g. a boiling range of C 5 to 4000° F.,
wherein the olefinic naphtha is derived from a Fischer-Tropsch process.
2. An olefinic naphtha according to claim 1 , comprising olefins in an amount of 25 to 80 weight %.
3. An olefinic naphtha according to claim 1 , comprising olefins in an amount of 50 to 80 weight %.
4. An olefinic naphtha according to claim 1 , wherein the non-olefins comprise greater than 75 weight % paraffins.
5. An olefinic naphtha according to claim 1 , wherein the non-olefins comprise greater than 90 weight % paraffins.
6. An olefinic naphtha according to claim 1 , wherein the olefins are comprised of greater than 65 weight % linear primary olefins.
7. An olefinic naphtha according to claim 1 , wherein the olefins are comprised of greater than 80 weight % linear primary olefins.
8. An olefinic naphtha according to claim 1 , wherein the paraffins have an i/n ratio of less than 1.
9. An olefinic naphtha according to claim 1 , wherein the paraffins have an i/n ratio of less than 0.5.
10. An olefinic naphtha according to claim 1 , comprising sulfur in an amount of less than 2 ppm by weight and nitrogen in an amount of less than 2 ppm by weight.
11. An olefinic naphtha according to claim 10 , comprising aromatics in an amount of less than 2 weight %.
12. A blended naphtha comprising:
a. an olefinic naphtha comprising olefins in an amount of 10 to 80 weight % and non-olefins in an amount of 20 to 90 weight %, wherein the olefins comprise greater than 50 weight % linear primary olefins and the non-olefins comprise greater than 50 weight % paraffins, wherein the olefinic naphtha is derived from a Fischer-Tropsch process; and
b. a naphtha selected from the group consisting of a hydrotreated Fischer-Tropsch derived naphtha, a hydrocracked Fischer-Tropsch derived naphtha, a hydrotreated petroleum derived naphtha, a hydrocracked petroleum derived naphtha, and mixtures thereof,
wherein the blended naphtha comprises less than 10 ppm sulfur and has an acid number of between 0.32 mg KOH/g and 1.5 mg KOH/g.
13. A blended naphtha according to claim 12 , wherein the blended naphtha comprises less than 5 ppm sulfur.
14. A blended naphtha according to claim 12 , wherein the blended naphtha comprises less than 2 ppm sulfur.
15. A blended naphtha according to claim 12 , wherein the blended naphtha comprises nitrogen in an amount of less than 2 ppm and aromatics in an amount of less than 2 weight %.
16. A blended naphtha according to claim 12 , wherein the olefinic naphtha comprises olefins in an amount of 25 to 80 weight %.
17. A blended naphtha according to claim 12 , wherein the olefins of the olefinic naphtha comprise greater than 65 weight % linear primary olefins.
18. A blended naphtha according to claim 12 , comprising 10 to 90 weight % olefinic naphtha and 90 to 10 weight % naphtha of (b).