IP Library › Granted Patent US 11,161,796
Granted Patent B2
US 11,161,796 · App. 17/264,430 · Granted Nov 2, 2021

Systems and processes for efficient production of one or more fuel additives

Inventors: Guillermo Leal (Riyadh, SA); Mohammed Bismillah Ansari (Riyadh, SA); Vijay Dinkar Bodas (Riyadh, SA); Sultan Eid Al-Otaibi (Riyadh, SA); Mohammed A. Al-Ghamdi (Riyadh, SA); Naif Mohammed Al-Naddah Al-Otaibi (Riyadh, SA)
Assignee: SABIC GLOBAL TECHNOLOGIES B.V.
C07C5/05C07C7/04C07C29/04
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Quick Facts
Patent No.
US 11,161,796
App. No.
17/264,430
Granted
Nov 2, 2021
Kind
B2
Abstract

A method for the production of a fuel additive includes passing a hydrocarbon stream comprising crude mixed C4 hydrocarbons through a first hydrogenation unit to produce a first product stream; passing the first product stream from the first hydrogenation unit to a methyl tert-butyl ether synthesis unit forming methyl tert-butyl ether and a byproduct stream; passing the byproduct stream through a first distillation unit to separate the byproduct stream into a first 1-butene stream, an isobutane stream, and a 2-butene and n-butane stream; forming a second product stream by passing the 2-butene and n-butane stream to a selective conversion unit; passing the second product stream into a second distillation unit to form an n-butane stream and a second 1-butene stream; passing the second 1-butene stream to a fuel additive production unit; and passing the first 1-butene stream to the fuel additive production unit to form the fuel additive.

Claims (22)

1. A method for the production of a fuel additive, comprising:

passing a hydrocarbon stream comprising crude mixed C4 hydrocarbons from one or more cracker units through a first hydrogenation unit to convert butadiene components to 1-butene and 2-butene to produce a first product stream;

passing the first product stream from the first hydrogenation unit to a methyl tert-butyl ether synthesis unit forming methyl tert-butyl ether and a byproduct stream;

passing the byproduct stream through a first distillation unit to separate the byproduct stream into at least three streams including a first 1-butene stream, an isobutane stream, and a 2-butene and n-butane stream;

forming a second product stream by passing the 2-butene and n-butane stream to a selective conversion unit to transform the 2-butene to 1-butene;

passing the second product stream into a second distillation unit to separate the n-butane from the 1-butene to form an n-butane stream and a second 1-butene stream;

passing the second 1-butene stream to a fuel additive production unit to form the fuel additive; and

passing the first 1-butene stream to the fuel additive production unit to form the fuel additive.

2. The method of claim 1 , wherein the hydrocarbon stream comprises ethyl acetylene, vinyl acetylene, 1,3-butadiene, 1,2-butadiene, isobutene, cis-2-butene, trans-2-butene, 1-butene, isobutane, n-butane, or a combination comprising at least one of the foregoing.

3. The method of claim 1 , wherein the hydrocarbon stream is a portion of an effluent from an olefins production plant.

4. The method of claim 1 , wherein the hydrocarbon stream is a stream from a cracker unit.

5. The method of claim 1 , wherein greater than or equal to 90 wt % of butadiene present in the hydrocarbon stream is converted to 1-butene and/or 2-butene within the first hydrogenation unit.

6. The method of claim 1 , wherein the isobutane stream comprises at least 0.1 wt % butenes.

7. The method of claim 1 , further comprising passing the isobutane stream to a methyl tert-butyl ether production unit.

8. The method of claim 7 , further comprising passing additional isobutane to the methyl tert-butyl ether production unit.

9. The method of claim 7 , wherein the methyl tert-butyl ether production unit comprises dehydrogenation and methyl tert-butyl ether synthesis units.

10. The method of claim 7 , further comprising passing the n-butane stream to the methyl tert-butyl ether production unit.

11. The method of claim 7 , wherein the methyl tert-butyl ether production unit comprises deisobutanizer, isomerization, dehydrogenation and methyl tert-butyl ether synthesis units.

12. The method of claim 1 , further comprising recycling the isobutane to a cracker unit to produce ethylene and propylene.

13. The method of claim 1 , further comprising recycling the n-butane stream to a cracker unit to produce ethylene and propylene.

14. The method of claim 1 , wherein the selective conversion unit is a selective hydrogenation unit.

15. The method of claim 1 , wherein the fuel additive comprises 1-butanol, 2-butanol, tert-butyl alcohol, C4-dimer, trimethyl-pentane, di-isobutene, 2,2,4 trimethyl-pentane, 2,3,3 trimethyl-pentane, or a combination comprising at least one of the foregoing.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 29, 2021
From: LEAL, GUILLERMO; ANSARI, MOHAMMED BISMILLAH; BODAS, VIJAY DINKAR; AL-OTAIBI, SULTAN EID; AL-GHAMDI, MOHAMMED A; AL-OTAIBI, NAIF MOHAMMED AL-NADDAH
To: SABIC GLOBAL TECHNOLOGIES B.V.
Reel/Frame 055077/0082 →
Continuity (2)
Provisional Application 62732751 · Sep 18, 2018
Related Publication 20210246088A1 · Aug 12, 2021