Control system and method for pressure-let-downs stations

Patent metadata

Field	Value
Publication number	US-10677392-B2
Application number	US-201615780731-A
Country	US
Kind code	B2
Filing date	Dec 1, 2016
Priority date	Dec 2, 2015
Publication date	Jun 9, 2020
Grant date	Jun 9, 2020

Abstract

A system for depressurizing a gas in a pipeline is described. The system com-prises an expander configured and arranged for generating mechanical power by expanding gas from a first pressure to a second pressure. The system further comprises a heat pump and a heat transfer circuit containing a heat transfer fluid circu-lating therein, for receiving heat from the heat pump and delivering heat to the gas through a heat exchanger. A controller is further provided, configured and arranged for modulating a flow rate of the heat transfer fluid circulating in the heat transfer circuit as a function of a heat rate to be transferred from the heat transfer fluid to the gas, particularly as a function of temperature differentials between the gas and the heat transfer fluid at a gas inlet side and a gas outlet side of the heat exchang-er.

First claim

What we claim is:

1. A system for depressurizing a gas in a pipeline, comprising:
an expander configured and arranged to generate mechanical power by expanding gas from a first pressure to a second pressure, the first pressure being higher than the second pressure;
a heat pump;
a heat transfer circuit having a heat transfer fluid circulating therein to receive heat from the heat pump and deliver the heat to the gas through a heat exchanger;
a controller configured to modulate a flow rate of the heat transfer fluid circulating in the heat transfer circuit as a function of a heat rate to be transferred from the heat transfer fluid to the gas, specifically as a function of temperature differentials between the gas and the heat transfer fluid at a gas inlet side and a gas outlet side of the heat exchanger;
a gas delivery duct arranged in parallel to the expander and the heat exchanger;
a pressure control valve arrangement comprising a plurality of pressure control valves arranged in parallel; and
a heater,
wherein the pressure control valve arrangement and the heater are arranged along the gas delivery duct and the heater is located upstream of the pressure control valve arrangement with respect to the gas flow direction in the gas delivery duct.

2. The system of claim 1 , wherein the heat exchanger is arranged upstream of the expander with respect to a direction of flow of the gas in the pipeline.

3. The system of claim 1 , wherein the heat pump is a transcritical heat pump.

4. The system of claim 1 , wherein the controller is functionally connected to temperature sensors configured to measure gas and heat temperature fluid temperatures at an inlet and an outlet of the heat exchanger.

5. The system of claim 1 , wherein the controller comprises a flowrate control loop to modulate the flow rate of the heat transfer fluid to minimize a difference between a first temperature differential between the gas and the heat transfer fluid at the a gas inlet side of the heat exchanger and a second temperature differential between the gas and the heat transfer fluid at the a gas outlet side of the heat exchanger.

6. The system of claim 5 , wherein the flowrate control loop is configured to change the flow rate of the heat transfer fluid in the heat transfer circuit so to maximize the coefficient of performance (COP) of the heat pump.

7. The system of claim 1 , wherein the controller features a temperature control loop arranged and configured for minimizing a difference between a gas temperature downstream of the expander and a gas temperature set point, by acting upon the heat rate from the heat transfer fluid to the gas.

8. The system of claim 1 , wherein the controller features a pressure control loop arranged and configured for minimizing a difference be-tween a gas pressure downstream of the expander and a gas pressure set point, by acting upon the gas flow rate through the expander.

9. The system of claim 1 , wherein the expander has variable inlet guide vanes, and wherein the controller is configured and arranged for adjusting a gas flow rate through the expander by acting upon the variable inlet guide vanes.

10. A method for depressurizing a gas in a pipeline, comprising the following steps:
delivering a gas through a heat exchanger and an expander;
heating the gas in the heat exchanger by delivering thereto heat from a heat pump through a heat transfer fluid circulating in a heat transfer circuit and in heat ex-change relationship with the gas and with a working fluid processed by the heat pump;
expanding the gas from a first pressure to a second pressure in the expander and generating mechanical power therewith; and
modulating a flow rate of the heat transfer fluid in the heat transfer circuit to minimize a difference between a first temperature differential between the gas and the heat transfer fluid at a gas inlet side of the heat exchanger and a second temperature differential between the gas and the heat transfer fluid at a gas outlet side of the heat exchanger.

11. The method of claim 10 , wherein the heat pump is a transcritical heat pump.

12. The method of claim 10 , wherein the step of heating the gas in the heat exchanger is performed prior to the step of expanding the gas in the expander, and the heat exchanger is arranged upstream of the expander with respect to a gas flow direction.

13. The method of claim 10 , comprising the step of modulating the flow rate of the heat transfer fluid as a function of temperature differentials between the gas and the heat transfer fluid at the gas inlet side and the gas outlet side of the heat exchanger.

14. The method of claim 10 , comprising the step minimizing a difference between a gas temperature downstream of the expander and a gas temperature set point by acting upon the heat rate from the heat transfer fluid to the gas.

15. The method of claim 10 , comprising the step of minimizing a difference between a gas pressure downstream of the expander and a gas pressure set point by acting upon the gas flow rate in the pipeline.

16. A system for depressurizing a gas in a pipeline, comprising:
an expander configured and arranged for generating mechanical power by expanding gas from a first pressure to a second pressure, the first pressure being higher than the second pressure;
a heat pump;
a heat transfer circuit having a heat transfer fluid circulating therein to receive heat from the heat pump and deliver the heat to the gas through a heat exchanger; and
a controller configured to modulate a flow rate of the heat transfer fluid circulating in the heat transfer circuit when a first temperature differential between the gas and the heat transfer fluid at a gas inlet side of the heat exchanger varies from a second temperature differential between the gas and the heat transfer fluid at a gas outlet side of the heat exchanger to minimize the difference between the first temperature differential and the second temperature differential.

Assignees

• Nuovo Pignone Tecnologie Srl
• Nuovo Pignone Srl

Inventors

• Monti Francesca
• Amidei Simone

Classifications

• F17C2225/0123

  gaseous, e.g. CNG, GNC · CPC title

• F17C2221/033

  Methane, e.g. natural gas, CNG, LNG, GNL, GNC, PLNG · CPC title

• F17C2250/0636

  Flow or movement of content · CPC title

• F17C2265/07

  Generating electrical power as side effect · CPC title

• F17C2227/0316

  Water heating · CPC title