Enhanced hydroprocessing process with ammonia and carbon dioxide recovery

Patent metadata

Field	Value
Publication number	US-12098331-B2
Application number	US-201916670971-A
Country	US
Kind code	B2
Filing date	Oct 31, 2019
Priority date	Oct 31, 2019
Publication date	Sep 24, 2024
Grant date	Sep 24, 2024

Abstract

A process for capturing carbon dioxide includes the steps of mixing a hydrogen stream and a feedstock stream to produce a mixed stream, wherein the feedstock stream includes hydrocarbons, reacting the hydrocarbons and the hydrogen in the primary reactor of the hydroprocessing unit to produce a hydroprocessing product stream and a carbon dioxide stream, wherein the hydroprocessing product stream includes light products, wherein the hydroprocessing unit is further configured to produce ammonium bisulfide, collecting the ammonium bisulfide in the water to produce a sour water, processing the sour water in the waste water unit to produce an ammonia stream, a hydrogen sulfide stream, and a stripped water stream, introducing the ammonia stream to a carbon dioxide recovery system, and separating carbon dioxide from the carbon dioxide stream using the ammonia in the ammonia stream to produce a carbon dioxide product.

First claim

What is claimed is:

1. A process for capturing carbon dioxide, the process comprising the steps of:
mixing a hydrogen stream and a feedstock stream to produce a mixed stream, wherein the feedstock stream comprises hydrocarbons, wherein the hydrogen stream comprises hydrogen;
introducing the mixed stream to a hydroprocessing unit, the hydroprocessing unit configured to process the hydrocarbons to produce light products in a primary reactor, wherein the pressure of the mixed stream is between 10 bars and 200 bars;
reacting the hydrocarbons and the hydrogen in the primary reactor of the hydroprocessing unit to produce a hydroprocessing product stream and a carbon dioxide stream, wherein the hydroprocessing product stream comprises light products, wherein the carbon dioxide stream comprises carbon dioxide and gas contaminants, wherein the hydroprocessing unit is further configured to produce ammonium bisulfide, wherein the gas contaminants are selected from the group consisting of oxygen, nitrogen, nitrogen oxides, sulfur oxides, and combinations of the same;
introducing a water stream to the hydroprocessing unit, wherein the water stream comprises water;
collecting the ammonium bisulfide produced in the hydroprocessing unit in the water of the water stream to produce a sour water;
introducing the sour water to a waste water unit;
processing the sour water in the waste water unit to produce an ammonia stream, a hydrogen sulfide stream, and a stripped water stream, wherein the ammonia stream comprises ammonia, wherein the waste water unit separates the ammonia bisulfide from sour water stream and then converts the ammonium bisulfide to ammonia;
introducing the ammonia stream to a carbon dioxide recovery system;
introducing the carbon dioxide stream to the carbon dioxide recovery system; and
separating carbon dioxide from the carbon dioxide stream using the ammonia in the ammonia stream to produce a carbon dioxide product.

2. The process of claim 1 , further comprising the steps of:
introducing a hydrocarbon feedstock and an oxygen-containing stream to a hydrogen production unit, wherein the hydrocarbon feedstock comprises hydrocarbons with a carbon number of less than 5, wherein the hydrogen production unit is configured to convert hydrocarbons with a carbon number of less than 5; and
processing the hydrocarbons with a carbon number of less than 5 in the hydrogen production unit to produce the hydrogen stream and a byproduct stream, wherein the byproduct stream comprises carbon dioxide.

3. The process of claim 2 , further comprising the steps of:
mixing the byproduct stream and the carbon dioxide stream to produce a combined stream; and
introducing the combined stream to the carbon dioxide recovery system.

4. The process of claim 1 , wherein the feedstock stream is selected from the group consisting of a whole crude oil, a naphtha stream, a distillate stream, a vacuum gas oil stream, a vacuum residue stream, an intermediate refinery stream, and combinations of the same.

5. The process of claim 1 , wherein the hydroprocessing unit is selected from the group consisting of a hydrotreating unit, a hydrocracking unit, a residue hydrocracking unit, and combinations of the same.

6. The process of claim 2 , wherein the hydrocarbon feedstock comprises natural gas.

7. The process of claim 1 , wherein the carbon dioxide product is operable for use in enhanced oil recovery operations.

Assignees

• Saudi Arabian Oil Co

Inventors

• Koseoglu Omer Refa

Classifications

• C10G2400/04

  Diesel oil · CPC title

• C10G2300/4068

  Moveable devices or units, e.g. on trucks, barges · CPC title

• C10G2300/4056

  Retrofitting operations · CPC title

• C10G2300/301

  Boiling range · CPC title

• C10G2300/202

  Heteroatoms content, i.e. S, N, O, P · CPC title