Use of recovered power in a process

Patent metadata

Field	Value
Publication number	US-10753235-B2
Application number	US-201815924034-A
Country	US
Kind code	B2
Filing date	Mar 16, 2018
Priority date	Mar 16, 2018
Publication date	Aug 25, 2020
Grant date	Aug 25, 2020

Abstract

Processes and apparatus for recovering energy from a petroleum, petrochemical, or chemical process are disclosed. The process comprises providing a fluid process stream in a petroleum, petrochemical, or chemical process zone having a direct current power input; controlling a flow rate of the process stream by directing at least a portion of the process stream through a first power-recovery turbine to generate electric power as direct current therefrom; and providing the recovered direct current to the direct current power input of the process zone.

First claim

What is claimed is:

1. A process for recovering energy from a petroleum, petrochemical, or chemical process comprising:
providing a fluid process stream in a petroleum, petrochemical, or chemical process zone in the petroleum, petrochemical, or chemical plant wherein the process zone comprises at least one of an alkylation zone, a separation zone, an isomerization zone, a catalytic reforming zone, a fluid catalyst cracking zone, a hydrocracking zone, a hydrotreating zone, a hydrogenation zone, a dehydrogenation zone, an oligomerization zone, a desulfurization zone, an alcohol to olefins zone, an alcohol to gasoline zone, a petroleum extraction zone, a petrochemical extraction zone, a chemical extraction zone, a distillation zone, a sour water stripping zone, a liquid phase adsorption zone, a hydrogen sulfide reduction zone, a transalkylation zone, a coking zone, or a polymerization zone;
controlling a flow rate of the process stream by directing at least a portion of the process stream through a first variable resistance power-recovery turbine to generate electric power as direct current therefrom;
providing the recovered direct current to at least one of a storage battery, a resistance heater, an electric heater, a pump, a compressor, or a fan in the petroleum, petrochemical, or chemical process zone; and
wherein the fluid process stream is used in the petroleum, petrochemical, or chemical process and is not consumed in the first power-recovery turbine.

2. The process of claim 1 wherein there are at least two power-recovery turbines.

3. The process of claim 2 further comprising combining the recovered direct current from the first and second power-recovery turbines before providing the recovered direct current to the at least one of the storage battery, the resistance heater, the electric heater, the pump, the compressor, or the fan.

4. The process of claim 1 wherein the recovered direct current is provided to the storage battery, and further comprising:
providing direct current from the storage battery to at least one of the fan, the pump, the compressor, the electric heater, or the resistance heater.

5. The process of claim 1 further comprising:
receiving information from a plurality of pressure reducing devices, the plurality of pressure reducing devices comprising: the first power-recovery turbine, a control valve, or both, using a process control system including a computer;
determining a power loss value or a power generated value for each of the pressure reducing devices from the amount of electricity each of the pressure reducing devices produced using the process control system;
determining a total power loss value or a total power generated value based upon the power loss values or the power generated values from each of the pressure reducing devices using the process control system; and,
displaying the total power loss value or the total power generated value on at least one display screen.

6. The process of claim 5 further comprising adjusting at least one process parameter in the process zone based upon the total power loss value or the total power generated value.

7. The process of claim 6 further comprising:
after the at least one process parameter has been adjusted, determining an updated power loss value or an updated power generated value for each of the pressure reducing devices;
determining an updated total power loss value or an updated total power generated value for the process zone based upon the updated power loss values or the updated power generated values from each of the pressure reducing devices; and,
displaying the updated total power loss value or the updated total power generated value on at least one display screen.

8. The process of claim 5 further comprising:
receiving information associated with conditions outside of the process zone, wherein the total power loss value or the total power generated value is determined based in part upon the information associated with conditions outside of the process zone.

9. The process of claim 5 further comprising:
receiving information associated with a throughput of the process zone, wherein the total power loss value or the total power generated value is determined based in part upon the information associated with the throughput of the process zone.

10. The process of claim 9 further comprising:
maintaining the throughput of the process zone while adjusting the at least one process parameter of the portion of a process zone based upon the total power loss value or the total power generated value.

11. The process of claim 1 further comprising:
converting a portion of the recovered direct current to alternating current; and
providing the converted alternating current to a central utility grid.

12. The process of claim 1 further comprising providing electric power to the first power-recovery turbine to increase a pressure on a fluid stream.

13. The process of claim 12 wherein the electric power is provided to the first power-recover turbine from a central utility grid.

14. The process of claim 1 wherein the process zone comprises at least one of the alkylation zone, the separation zone, the isomerization zone, the catalytic reforming zone, the fluid catalyst cracking zone, the hydrocracking zone, the hydrotreating zone, the hydrogenation zone, the dehydrogenation zone, the oligomerization zone, the desulfurization zone, the alcohol to olefins zone, the alcohol to gasoline zone, the distillation zone, the sour water stripping zone, the liquid phase adsorption zone, the hydrogen sulfide reduction zone, the transalkylation zone, the coking zone, or the polymerization zone.

15. A process for recovering energy from a petroleum, petrochemical, or chemical process comprising:
providing a fluid process stream in a petroleum, petrochemical, or chemical process zone in the petroleum, petrochemical, or chemical plant wherein the process zone comprises at least one of an alkylation zone, a separation zone, an isomerization zone, a catalytic reforming zone, a fluid catalyst cracking zone, a hydrocracking zone, a hydrotreating zone, a hydrogenation zone, a dehydrogenation zone, an oligomerization zone, a desulfurization zone, an alcohol to olefins zone, an alcohol to gasoline zone, a petroleum extraction zone, a petrochemical extraction zone, a chemical extraction zone, a distillation zone, a sour water stripping zone, a liquid phase adsorption zone, a hydrogen sulfide reduction zone, a transalkylation zone, a coking zone, or a polymerization zone;
controlling a flow rate of the process stream by directing at least a portion of the process stream through a first variable resistance power-recovery turbine to generate electric power as direct current therefrom;
providing the recovered direct current to at least one of a storage battery, a resistance heater, an electric heater, a pump, a compressor, or a fan in the petroleum, petrochemical, or chemical process zone;
receiving information from a plurality of pressure reducing devices, the plurality of pressure reducing devices comprising: the first power-recovery turbine, a control valve, or both;
determining a power loss value or a power generated value for each of the pressure reducing devices;
determining a total power loss value or a total power generated value based upon the power loss values or the power generated values from each of the pressure reducing devices;
displaying the total power loss value or the total power generated value on at least one display screen; and
wherein the fluid process stream is used in the petroleum, petrochemical, or chemical process an

Assignees

• Uop Llc

Inventors

• Harris James W
• Eizenga Donald A
• Van De Cotte Michael
• Wegerer David A

Classifications

• H02J7/865

  Battery or charger load switching, e.g. concurrent charging and load supply (H02J7/50 takes precedence) · CPC title

• B01D3/007 Primary

  Energy recuperation; Heat pumps · CPC title

• F01K23/064 Primary

  in combination with an industrial process, e.g. chemical, metallurgical · CPC title

• F05D2270/05

  to affect the output of the engine · CPC title

• Y02P20/129

  Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines · CPC title