Adsorbent circulation for onboard octane on-demand and cetane on-demand

Patent metadata

Field	Value
Publication number	US-10801422-B2
Application number	US-201916551047-A
Country	US
Kind code	B2
Filing date	Aug 26, 2019
Priority date	Mar 29, 2018
Publication date	Oct 13, 2020
Grant date	Oct 13, 2020

Abstract

A vehicular propulsion system, a vehicular fuel system and a method of operating an internal combustion engine. A separation unit that makes up a part of the fuel system may selectively receive and separate at least a portion of onboard fuel and a flowable adsorbent in order to separate the fuel into octane-enhanced and cetane-enhanced fuel components. A controller may be used to determine a particular operating condition of the internal combustion engine such that the onboard fuel can be sent to one or more combustion chambers within the internal combustion engine without first passing through the separation unit during one operating condition, or instead to the separation unit in situations where the internal combustion engine may require an octane-rich or cetane-rich mixture in another operating condition.

First claim

What is claimed is:

1. A vehicular propulsion system comprising:
an internal combustion engine; and
a fuel system cooperative with the internal combustion engine to deliver fuel to a combustion chamber that makes up a portion of the internal combustion engine, the fuel system comprising:
an onboard fuel supply tank configured to contain a market fuel;
a first tank configured to contain at least a portion of a flowable adsorbent;
a separation unit configured such that upon receipt of a quantity of the market fuel from the onboard fuel supply tank and a quantity of the adsorbent from the first tank, the separation unit generates an adsorbate and a remainder, the remainder defining a first enriched fuel;
a heat exchanger configured to deliver residual thermal energy to the adsorbate in order to regenerate at least a portion of the adsorbent through the creation of a desorbate that defines a second enriched fuel;
a second tank configured to contain at least a portion of the second enriched fuel;
conduit configured to fluidly couple at least the onboard fuel supply tank, first tank, second tank, separation unit and combustion chamber; and
a controller cooperative with the conduit to convey at least one of the market fuel, the first enriched fuel and the second enriched fuel to the combustion chamber depending on an operating condition of the internal combustion engine.

2. The system of claim 1 , wherein the adsorbate comprises an octane-rich fuel component, while the remainder comprises a cetane-rich fuel component.

3. The system of claim 1 , wherein the adsorbate comprises a cetane-rich fuel component, while the remainder comprises an octane-rich fuel component.

4. The system of claim 1 , wherein the operating condition of the internal combustion engine comprises a bypass condition and an adsorption condition such that when the controller determines that the internal combustion engine is in the bypass condition, the controller is configured to direct the market fuel to the combustion chamber without first passing through the separation unit, and when the controller determines that the internal combustion engine is in the adsorption condition, the controller is configured to direct at least a portion of the market fuel to the separation unit.

5. The system of claim 1 , wherein the adsorbent comprises adsorbent particles that define at least one functional group that comprises at least one of activated carbon, zeolite, silica and alumina.

6. The system of claim 5 , wherein the adsorbent comprises adsorbent particles that define a molecular sieve comprising at least one of zeolite, metal organic framework and structured porous material.

7. The system of claim 1 , further comprising a plurality of sensors cooperative with the controller to determine whether the adsorbent that is present within the first tank is in a saturated state or an unsaturated state such that upon determination that a signal received from at least one of the plurality of sensors indicates that the adsorbent that is present within the first tank is in a saturated state, the controller instructs the conduit to convey at least a portion of the saturated state adsorbent from the first tank to the heat exchanger in order to produce the desorbate and regenerated adsorbent.

8. The system of claim 7 , wherein the adsorbent that is present within the first tank is considered to be in a saturated state when the controller determines that the adsorbent that is present within the first tank is no longer substantially capable of capturing a measurable quantity of octane-rich fuel components.

9. The system of claim 8 , wherein the controller determines that the adsorbent that is present within the first tank is in a saturated state through determination of at least one of a liquid level height of the adsorbent in the first tank or a concentration difference of the adsorbent in the first tank.

10. The system of claim 9 , wherein the controller is further configured to selectively recycle both the market fuel and the adsorbent that are conveyed from the first tank to the adsorption chamber of the separation unit until such time as the adsorbent that is present within the first tank is in a saturated state.

11. A fuel system for converting a fuel into octane-rich and cetane-rich components, the fuel system comprising:
an onboard fuel supply tank configured to contain a market fuel;
a first tank configured to contain at least a portion of a flowable adsorbent;
a separation unit configured such that upon receipt of a quantity of the market fuel from the onboard fuel supply tank and a quantity of the adsorbent from the first tank, the separation unit generates an adsorbate and a remainder at least a portion of both of which are conveyed from the separation unit to the first tank, wherein the remainder defines a first enriched fuel;
a heat exchanger configured to selectively deliver residual thermal energy to the adsorbate in order to regenerate at least a portion of the adsorbent through the creation of a desorbate that defines a second enriched fuel;
a second tank configured to contain at least a portion of the second enriched fuel; and
a controller cooperative with at least one of the onboard fuel supply tank, first tank and second tank to selectively convey at least one of the market fuel, the first enriched fuel and the second enriched fuel to a combustion chamber of an internal combustion engine.

12. A method of delivering at least one of an onboard-generated octane-rich fuel and an onboard-generated cetane-rich fuel to an internal combustion engine through a fuel system, the method comprising:
configuring the fuel system to comprise an onboard fuel supply tank, a first tank, a second tank, a separation unit, a plurality of sensors, a controller and conduit configured to selectively fluidly couple at least the onboard fuel supply tank, first tank, second tank and separation unit, the method comprising:
determining by the controller whether the internal combustion engine is in a bypass condition or an adsorption condition such that when the internal combustion engine is in the adsorption condition, the controller instructs the fuel system to:
generate within the separation unit an adsorbate and a remainder the latter of which defines a first enriched fuel;
convey at least a portion of the adsorbate and the first enriched fuel from the separation unit to the first tank;
regenerate at least some of the adsorbent contained within the portion of the adsorbate and the first enriched fuel that was conveyed from the separation unit to the first tank by creating a desorbate that defines a second enriched fuel;
convey the second enriched fuel to the second tank; and
convey the regenerated adsorbent to the separation unit; and

conveying at least one of the market fuel, the first enriched fuel and the second enriched fuel to the internal combustion engine.

13. The method of claim 12 , wherein the controller further instructs at least one of the separation unit and the first tank to receive heat sufficient to generate the desorbate.

14. The method of claim 13 , wherein a heat exchanger is used to receive heat by at least one of the separation unit and the first tank.

15. The method of claim 14 , wherein the heat sufficient to generate the desorbate is provided by operation of the internal combustion engine.

16. The method of claim 15 , wherein a substantial entirety of fuel being conveyed to the internal combustion engine comprises conveying a cetane-rich fuel component to the combustion chamber.

17. The method of claim

Assignees

• Saudi Arabian Oil Co

Inventors

• Hamad Esam Zaki
• Tora Eman Abdelhakim A M
• Amer Amer A
• Chang Junseok

Classifications

• Y02T10/30

  Use of alternative fuels, e.g. biofuels · CPC title

• F02D2200/0611

  Fuel type, fuel composition or fuel quality · CPC title

• F02D2200/0606

  Fuel temperature · CPC title

• F02D41/0025

  Controlling engines characterised by use of non-liquid fuels, pluralities of fuels, or non-fuel substances added to the combustible mixtures · CPC title

• F02D33/003

  Controlling the feeding of liquid fuel from storage containers to carburettors or fuel-injection apparatus (control of electrical fuel pumps F02D41/3082, controlling fuel flow to a common rail F02D41/3845); Failure or leakage prevention; Diagnosis or detection of failure; Arrangement of sensors in the fuel system; Electric wiring; Electrostatic discharge · CPC title