Point-of-sale octane/cetane-on-demand systems for automotive engines

Patent metadata

Field	Value
Publication number	US-2020002154-A1
Application number	US-201916570456-A
Country	US
Kind code	A1
Filing date	Sep 13, 2019
Priority date	Oct 13, 2017
Publication date	Jan 2, 2020
Grant date	—

Abstract

A point-of-sale fuel dispensing system, a pump assembly and a method of dispensing fuel at a point-of-sale. The system includes a market fuel storage tank, pump assembly, fuel conduit, separation unit, numerous enriched fuel product tanks and a controller. The separation unit may selectively receive at least a portion of market fuel and convert it into an octane-rich fuel component and a cetane-rich fuel component that may be subsequently dispensed to a vehicle being fueled, where a fuel grade selection and retail payment of a fuel containing the octane-rich or cetane-rich fuel components is provided to the vehicle based on user input at the customer interface.

First claim

What is claimed is:

1 . A method of dispensing fuel at a point-of-sale, the method comprising:
using a pump assembly to convert at least a portion of a market fuel that is stored in an storage tank that is situated at the point-of-sale into an octane-rich fuel component and a cetane-rich fuel component; and conveying at least one of the market fuel, the octane-rich fuel component and the cetane-rich fuel component to a vehicle through the pump assembly, wherein the pump assembly comprises:
a customer interface for both retail payment and fuel grade selection for the vehicle;
a separation unit that receives at least a portion of the market fuel and converts it into the octane-rich fuel component and the cetane-rich fuel component;
a first enriched fuel product tank that receives the octane-rich fuel component;
a second enriched fuel product tank that receives the cetane-rich fuel component; and
a controller to direct the flow of at least one of the market fuel, the octane-rich fuel component and the cetane-rich fuel component through the pump assembly based on user input at the customer interface.

2 . The method of claim 1 , wherein the separation unit is selected from the group consisting of a membrane-based separation unit, an extractive-based separation unit, a volatility-based separation unit and combinations thereof.

3 . The method of claim 2 , wherein the separation unit comprises a plurality of sub-units comprising a membrane-based sub-unit and an extractive-based sub-unit.

4 . The method of claim 3 , wherein the membrane-based sub-unit is configured to provide at least a majority of the cetane-rich fuel component and the extractive-based sub-unit is configured to provide at least a majority of the octane-rich fuel component.

5 . The method of claim 1 , further comprising pressurizing at least one of the market fuel, the octane-rich fuel component and the cetane-rich fuel component.

6 . The method of claim 5 , wherein the pressurizing is performed by a pump that is adapted to receive electric power from a source selected from the group consisting of at least one photovoltaic cell, wind power, geothermal power, hydroelectric power and biomass power.

7 . The method of claim 5 , wherein the pressurizing is performed by a pump that is adapted to receive power from the operation of an internal combustion engine.

8 . The method of claim 5 , wherein the pressurizing is done by a pump that is adapted to receive power from the operation of an electric power generating station.

9 . The method of claim 5 , wherein the pressurizing is done by a pump that is adapted to receive power from the operation of a battery.

10 . The method of claim 1 , further comprising using the controller to introduce at least one of an octane booster and a cetane booster to at least one of the first and second enriched fuel product tanks through fuel conduit that places the pump assembly and the storage tank that contains the market fuel in selective fluid communication with one another.

11 . The method of claim 10 , further comprising using a mixer that is fluidly disposed between (a) a respective one of a source of the octane booster and a source of the cetane booster and (b) the first and second enriched fuel product tanks through the fuel conduit.

12 . The method of claim 10 , wherein the octane booster is selected from the group consisting of an oxygenate and an aromatic.

13 . The method of claim 1 , further comprising using an additional market fuel storage tank such that a second market fuel contained within the additional market fuel storage tank may be selectively blended with at least one of the octane-rich fuel component and the cetane-rich fuel component prior to the blended fuel being conveyed through the pump assembly.

14 . The method of claim 14 , further comprising using at least one separator unit such that upon passing of the fuel contained within at least one of the market fuel storage tanks prior to delivery of such fuel to the pump assembly, the at least one separator unit performs at least one of oxygenate separation and aromatics separation of the respective market fuel.

15 . The method of claim 1 , wherein the storage tank that contains the market fuel is situated underground.

Assignees

• Saudi Arabian Oil Co

Inventors

• Al Khowaiter Ahmad O
• Hamad Esam Z
• Baaqel Husain A
• Amer Amer A

Classifications

• B67D2007/746

  by mixing different fuel grades or fuel and oil · CPC title

• C10L1/04

  essentially based on blends of hydrocarbons · CPC title

• C10G2300/305

  Octane number, e.g. motor octane number [MON], research octane number [RON] · CPC title

• C10G2300/307

  Cetane number, cetane index · CPC title

• B67D7/743

  electrically or electro-mechanically operated · CPC title