Flexible fuel converter for producing liquefied petroleum gas from transportation fuels

Patent metadata

Field	Value
Publication number	US-9855540-B2
Application number	US-201414495182-A
Country	US
Kind code	B2
Filing date	Sep 24, 2014
Priority date	Sep 24, 2013
Publication date	Jan 2, 2018
Grant date	Jan 2, 2018

Abstract

Fuel converters configured to convert a transportation fuel to a low-C hydrocarbon fuel, along with methods of their use, are provided. The fuel converter can comprise: an evaporator configured to receive a transportation fuel from a fuel tank in a liquid state, wherein the evaporator converts the transportation fuel from a liquid to a gas; a fuel burner configured to heat the evaporator; a catalyst cartridge in fluid communication with the evaporator so as to receive the gas from the evaporator; and a condenser in fluid communication with the catalyst cartridge so as to receive the reaction product mixture from the catalyst cartridge. The catalyst cartridge comprises a catalyst configured to convert the transportation fuel into a reaction product mixture comprising a low-C hydrocarbon fuel. The condenser is configured to separate the low-C hydrocarbon fuel from a condensed fuel in the reaction product mixture.

First claim

What is claimed:

1. A fuel converter comprising:
an evaporator configured to receive a transportation fuel from a fuel tank in a liquid state, wherein the evaporator converts the transportation fuel from a liquid to a gas;
a fuel burner configured to heat the evaporator;
a plurality of catalyst cartridges in fluid communication with the evaporator so as to receive the gas from the evaporator, wherein each catalyst cartridge comprises a catalyst configured to convert the transportation fuel into a reaction product mixture comprising a low-C hydrocarbon fuel, wherein the evaporator, the fuel burner, and the plurality of catalyst cartridges are contained within a section of walls, wherein one or more of the walls are insulated;
a condenser in fluid communication with each of the catalyst cartridges so as to receive the reaction product mixture from the catalyst cartridges, wherein the condenser is configured to separate the low-C hydrocarbon fuel from a condensed fuel in the reaction product mixture, wherein the condenser is operated at a condensing temperature of about −10° C. to about 35° C.;
a return system configured to return the condensed fuel from the condenser to the fuel tank or to the evaporator; and
a collection system configured to collect the low-C hydrocarbon fuel from the condenser.

2. The fuel converter of claim 1 , wherein the return system is configured to return the condensed fuel to the fuel tank.

3. The fuel converter of claim 1 , wherein the return system is configured to return the condensed fuel to the evaporator.

4. The fuel converter of claim 1 , further comprising:
a pump in fluid communication with the fuel tank and the evaporator such that the high-C hydrocarbon fuel is pumped to the evaporator from a fuel tank.

5. The fuel converter of claim 4 , wherein the pump is a peristaltic pump.

6. The fuel converter of claim 1 , wherein the high-C hydrocarbon fuel is converted from a liquid state to a gaseous state in the evaporator heated by the fuel burner.

7. The fuel converter of claim 1 , wherein each catalyst cartridge is individually piped to the evaporator.

8. The fuel converter of claim 7 , wherein a valve is present between the evaporator and each catalyst cartridge such that the flow from the evaporator to each catalyst cartridge is individually controlled.

9. The fuel converter of claim 8 , wherein each catalyst cartridge is configured to operate for a specified time, and then be regenerated thermally.

10. The fuel converter of claim 9 , wherein each catalyst cartridge is configured to operate for a specified time of about 6 hours to about 20 hours.

11. The fuel converter of claim 10 , wherein each catalyst cartridge is configured to be regenerated thermally via heating for about 30 minutes to about 5 hours.

12. The fuel converter of claim 8 , wherein each catalyst cartridge is individually piped to the condenser.

13. The fuel converter of claim 1 , wherein the condenser is configured to cool the reaction product mixture to a temperature that liquefies the condensed fuel while keeping the low-C hydrocarbon fuel in a gaseous state.

14. The fuel converter of claim 13 , wherein the gaseous product is collected from the top of the condenser and piped to the collection system as a reaction product.

15. The fuel converter of claim 14 , wherein the liquid product is collected from the bottom reservoir of condenser and piped via the return system to the fuel tank or to the evaporator.

16. The fuel converter of claim 15 , wherein the gaseous product is piped from the condenser to a compressor where it is pressurized into a liquid fuel within the collection system.

17. The fuel converter of claim 1 , wherein the fuel converter is a portable device.

18. The fuel converter of claim 1 , wherein the fuel converter has a compact design.

19. The fuel converter of claim 1 , wherein the fuel converter has dimensions of approximately 20 inches by 20 inches by 24 inches.

Assignees

• Lauterbach Jochen
• Sasmaz Erdem
• Kim Sungtak
• Mayeda Michael Kai
• Univ South Carolina

Inventors

• Lauterbach Jochen
• Sasmaz Erdem
• Kim Sungtak
• Mayeda Michael Kai

Classifications

• B01J2219/00108

  involving reactant vapours · CPC title

• B01J2219/00099

  the reactor being immersed in the heat exchange medium · CPC title

• B01J2208/00504

  by means of a burner · CPC title

• B01J2208/0053

  Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling · CPC title

• B01J2219/00157

  by means of a burner · CPC title