EXAMINATION PROCESS FOR THE IN SITU DETERMINATION OF RATE OF FEEDING AN INHIBITOR INTO A GAS PIPELINE FOR PREVENTING HYDRATE FORMATION

• US 20170114941A1
• Filed: 03/22/2016
• Published: 04/27/2017
• Est. Priority Date: 10/21/2015
• Status: Active Grant

• Current Assignee: Pal Farkas
• Original Assignee: Pal Farkas
• Inventors: Farkas, Pal
• Granted Patent: US 9,772,061 B2
• Time in Patent Office: Days
• CPC Class Codes: F16L 58/00 Protection of pipes or pipe fittings against corrosion or incrustation compound tubes F16L9/14
• CPC Class Codes: G01N 33/225 Gaseous fuels, e.g. natural gas
• CPC Class Codes: G05D 11/135 by sensing at least one property of the mixture G05D11/139 takes precedence

Abstract

The invention relates to an examination process for replicating hydrate forming conditions in a gas pipeline and monitoring the effect of a low dosage hydrate inhibitor (LDHI) in suppressing hydrate formation at temperatures encountered in gas pipelines for dynamically determining LDHI feed rate for inhibition of hydrate formation comprising the steps of:

• • diverting from a gas well a sample gas stream at a preselected rate;
  • introducing the diverted gas stream into a gas conduit through an inlet of the gas conduit;
  • feeding LDHI into the diverted gas stream at one or more predetermined rates to produce a LDHI-containing gas stream;
  • introducing the LDHI-containing gas stream into a coolable portion of the gas conduit, which coolable portion is provided with pressure sensors along the coolable portion;
  • cooling the LDHI-containing gas stream passing through the coolable portion of the gas conduit to a predetermined temperature; and
  • monitoring pressure of the LDHI-containing gas stream passing through the coolable portion of the gas conduit for a predetermined time range being at least as long as the gas residence time within the gas pipeline;

whereby a substantially uniform pressure drop along the coolable portion of the gas conduit during the predetermined time range indicates a LDHI feed rate sufficient to suppress hydrate formation at the predetermined temperature.

Claims

1. Examination process for replicating hydrate forming conditions in a gas pipeline and monitoring the effect of a low dosage hydrate inhibitor (LDHI) in suppressing hydrate formation at temperatures and pressures encountered in gas pipelines for dynamically determining LDHI feed rate for inhibition of hydrate formation comprising the steps of:

diverting from a gas well a sample gas stream at a preselected rate;

introducing the diverted gas stream into a gas conduit through an inlet of the gas conduit;

feeding LDHI into the diverted gas stream at one or more predetermined rates to produce a LDHI-containing gas stream;

introducing the LDHI-containing gas stream into a coolable portion of the gas conduit at a predetermined pressure, which coolable portion is provided with pressure sensors along the coolable portion;

cooling the LDHI-containing gas stream passing through the coolable portion of the gas conduit by cooling the coolable portion to a predetermined temperature; and

monitoring pressure of the LDHI-containing gas stream passing through the coolable portion of the gas conduit for a predetermined time period;

whereby a substantially uniform pressure drop along the coolable portion of the gas conduit during the predetermined time period indicates a LDHI feed rate sufficient to suppress hydrate formation at the predetermined temperature.

2. The process according to claim 1, characterized by performing the examination of the hydrate formation for a LDHI delivered at least at two different feeding rates and/or for at least two types of LDHIs and/or at least at two given temperatures.

3. The process according to claim 1, characterized by that the predetermined observation time is at least twice the gas residence time within the gas pipeline.

4. The process according to claim 1, characterized by providing a coil pipe as the coolable portion of the gas conduit, the coil pipe having an inner diameter of at least 7 mm, more preferably of at least 10 mm and having a length of at least 100 m, preferably not more than 200 m.

5. The process according to claim 1, characterized by washing the coolable portion of the gas conduit with hot water and blowing air or nitrogen there through between consecutive measurements.

6. The process according to claim 1, characterized by providing temperature sensors along the coolable portion of the gas conduit and measuring the temperature of the coolable portion in at least two locations, whereby a substantially uniform temperature along the coolable portion of the gas conduit during the predetermined time range indicates a LDHI feed rate sufficient to suppress hydrate formation.

7. The process according to claim 1, characterized by separating the liquid phase and solid contaminants from the gas with a separator prior to feeding the LDHI into the gas conduit.

8. The process according to claim 1, characterized by determining the quantity of stratum water and natural gas condensate carried in the gas pipeline, and after having separated the liquid phase feeding stratum water and natural gas condensate to the gas inside the gas conduit in accordance with the determined quantities prior to introducing the gas into the coolable portion.

9. The process according to claim 1, characterized by cooling the coolable portion by introducing a cooling medium into a heat exchange space of a heat exchanger and in case of hydrate formation discharging the cooling medium into a tank, and heating the coolable portion by an air heater connected to the heat exchange space until the hydrate plug is eliminated.

10. The process according to claim 1, characterized by setting a desired mass flow of the gas inside the gas conduit by a choke valve connected to the gas conduit.

11. The process according to claim 1, characterized by performing a pre-measurement in a laboratory scale measuring system for pre-screening the LDHIs that are to be examined, by:

taking gas sample from a gas well,

introducing the gas sample into a gas conduit of the laboratory scale measuring system,

feeding LDHI that is to be pre-screened into the gas conduit of the laboratory scale measuring system to produce a LDHI-containing gas sample,

introducing the LDHI-containing gas sample into a maximum 20 m long coolable portion of the gas conduit of the laboratory scale measuring system, which coolable portion is provided with pressure sensors along the coolable portion;

cooling the LDHI-containing gas sample passing through the coolable portion of the gas conduit of the laboratory scale measuring system by cooling said coolable portion to a predetermined temperature; and

monitoring pressure of the LDHI-containing gas sample passing through the coolable portion of the gas conduit of the laboratory scale measuring system;

whereby a substantially uniform pressure drop along the coolable portion of the gas conduit during of the laboratory scale measuring system indicates a LDHI feed rate sufficient to suppress hydrate formation in the gas sample.

12. The process according to claim 11, characterized by providing a measuring cell as the coolable portion of the gas conduit of the laboratory scale measuring system, the measuring cell having an inner diameter of 3 to 5 mm, preferably of about 4 mm.

13. The process according to claim 11, characterized by performing the examination of the hydrate formation in the laboratory scale measuring system for an LDHI added in various different quantities and/or at least two types of LDHIs and/or at least at two given temperatures.

14. The process according to claim 13, characterized by washing the coolable portion of the gas conduit of the laboratory scale measuring system with hot water and blowing air there through between consecutive measurements.

15. The process according to claim 11, characterized by separating the liquid phase and eventually solid contaminants from the gas taken from the gas well with a separator.

16. The process according to claim 11, characterized by determining the amount of stratum water and natural gas condensate carried in the gas pipeline, and after having separated the liquid phase, feeding stratum water and natural gas condensate into the gas in accordance with the determined amounts prior to introducing the gas into the coolable portion of the laboratory scale measuring system.

17. The process according to claim 11, characterized by taking the gas from a gas inlet of the gas conduit of the laboratory scale measuring system, which gas conduit is connectable to a well-head of the gas well for the purpose of pre-measurement.

18. The process according to claim 11, characterized by introducing the gas from the gas well into a gas bottle and feeding the gas into the gas of the laboratory scale measuring system conduit therefrom for the purpose of pre-measurement.

19. The process according to claim 1, characterized by providing an LDHI feeder comprising a telemetric data transmission system for the remote control and monitoring of the LDHI feeder, and connecting the LDHI feeder to a feeding point of the gas pipeline, determining a temperature of the gas pipeline, and feeding the LDHI into the gas pipeline through the feeding point by the LDHI feeder at a LDHI feed rate sufficient to suppress hydrate formation at a temperature not exceeding the gas pipeline temperature.

20. The process according to claim 19, characterized by that the LDHI feeder comprises a tank for storing the LDHI, a pump for delivering the LDHI from the tank into the gas pipeline and during the remote monitoring of the LDHI feeder by the telemetric data transmission system measuring, via measuring devices, the quantity of the LDHI within the tank and/or the temperature of the LDHI within the tank and/or the pressure at a well head of the gas well and/or the pressure at the feeding point and/or the pressure of the gas actuating the pump and/or the flow rate of the LDHI flowing through the feeding point, and transmitting the measured data to a remote center.

21. The process according to claim 19, characterized by that the telemetric data transmission system comprises a control unit, and by collecting and storing the data measured by the measuring devices of the telemetric data transmission system, and controlling the pump by the control unit.

22. The process according to claim 19, characterized by determining the temperature of the gas pipeline by measuring the temperature of the gas pipeline at least at one location and transmitting the measured data to a remote center by the telemetric data transmission system.

23. The process according to claim 22, characterized by adjusting the feed rate of the LDHI with regard to the measured temperatures.

24. The process according to claim 20, characterized by that the pump comprises a piston and a remotely controllable stroke rate regulator for regulating the stroke rate of the piston, and by controlling the stroke rate of the piston from the remote center in the course of the remote control of the LDHI feeder.

25. The process according to claim 20, characterized by that the pump comprises a piston and a remotely controllable stroke length regulator for regulating the stroke length of the piston, and by controlling the stroke length of the piston from the remote center in the course of the remote control of the LDHI feeder.

26. The process according to claim 20, characterized by that the LDHI feeder comprises as the pump a pneumatic pump actuated by gas obtained from the gas well, and by separating liquid phase and in a given case solid contaminants by a separator from the gas actuating the pneumatic pump that is obtained from the gas well before introducing the gas into the pneumatic pump.

27. The process according to claim 19, characterized by providing the telemetric data transmission system with an energy supply system for current supply necessary for its operation, which preferably comprises an accumulator and/or fuel cell and/or solar cell.

28. The process according to claim 19, characterized by arranging the LDHI feeder in a container having solid walls.