Pressure-control temperature-control hypergravity experimental device for simulating deep-sea seabed responses
US-11187691-B2 · Nov 30, 2021 · US
US11834620B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11834620-B2 |
| Application number | US-202117527608-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 16, 2021 |
| Priority date | Nov 16, 2020 |
| Publication date | Dec 5, 2023 |
| Grant date | Dec 5, 2023 |
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Systems and methods related to centrifuge energy harvesting chambers (CEHCs) for gas production simulation are provided. Certain CEHCs may include a high-pressure chamber, high-pressure syringe pumps, cooling systems, an actuator and surcharge, backpressure control inside the wellbore, a heating element on the wellbore, water gas separation systems, and flow measurement systems. Certain CEHCs may also provide software operably connected to sensors and instrumentation, comprising a module to continuously, in real-time, periodically, or asynchronously, measure and monitor simulation variables.
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What is claimed is: 1. A centrifuge energy harvesting chamber (CEHC) comprising: a high-pressure chamber configured to sustain sufficient pressure and temperature for hydrate formation within a sediment bed in an operating centrifuge, one or more high-pressure pumps configured to sustain sufficient pore pressure and boundary pressure for hydrate formation around the sediment bed, a cooling system comprising a cooling coil inside the high-pressure chamber configured to cool the sediment bed inside the high-pressure chamber, an actuator configured to provide an activation force acting within the high-pressure chamber, and a surcharge plate to configured to load the sediment bed when acted upon by the activation force. 2. The CEHC of claim 1 , wherein the one or more high-pressure pumps comprise a pair of syringe pumps. 3. The CEHC of claim 2 , wherein the pair of syringe pumps are configured for repeated sequential operation to provide a continuous high-pressure fluid flow at an elevated gravity of the centrifuge. 4. The CEHC of claim 1 , further comprising a backpressure control system comprising an inert gas source configured to control a pressure inside a wellbore. 5. The CEHC of claim 1 , further comprising a water gas separation system configured to produce a flow of gas and a flow of water, a gas flow measurement system configured to measure the flow of gas, and a water flow measurement system configured to measure the flow of water. 6. The CEHC of claim 1 , the cooling system further comprising a circulating heat exchanger outside the high-pressure chamber and configured to selectively sustain the required temperatures for hydrate formation or hydrate stability, respectively. 7. The CEHC of claim 1 , further comprising a high-pressure linear variable displacement transducer (LVDT) configured to measure settlement within the sediment bed. 8. The CEHC of claim 1 , wherein the CEHC is securely fastened to the centrifuge and sufficiently sealed and insulated to operate as an adiabatic system. 9. The CEHC of claim 1 , wherein the CEHC further comprises an instrumentation module, sensors, and software configured to continuously measure one or more of temperature, pressure, pumping rate, and wellbore pressure while the centrifuge is in-flight. 10. The CEHC of claim 4 , wherein the inert gas source comprises a N 2 gas cylinder. 11. The CEHC of claim 7 , wherein the high-pressure LVDT is configured to measure settlement of a simulated seabed and one of more offshore structures within the sediment bed. 12. A method of gas production simulation, the method comprising the following steps: providing, within an operating centrifuge, a centrifuge energy harvesting chamber (CEHC) comprising: a high-pressure chamber, a sediment bed within the high-pressure chamber, a high-pressure pump operably connected to the high-pressure chamber, a cooling system operably connected to the high-pressure chamber, an actuator configured to provide an activation force, and a surcharge plate to configured to load the sediment bed when acted upon by the activation force; creating a centrifugal loading by operation of the centrifuge; pressurizing, by the high-pressure pump, the sediment bed within the high-pressure chamber to a first pressure sufficient for gas hydrate formation or maintenance; cooling, by the cooling system, the sediment bed within the high-pressure chamber to a first temperature sufficient for gas hydrate formation or maintenance at the first pressure; forming or maintaining gas hydrates within the sediment bed under centrifugal loading; performing, within the sediment bed and under the centrifugal loading, a simulation of hydrate dissociation, wellbore casing deformation, or seabed subsidence during gas production from hydrate-bearing soils. 13. The method of claim 12 , wherein the high-pressure pump comprises a pair of syringe pumps and the step of pressurizing, by the high-pressure pump, the sediment bed within the high-pressure chamber comprises repeated sequential operation of the pair of syringe pumps to provide a continuous high-pressure fluid flow at an elevated gravity of the centrifuge. 14. The method of claim 12 , the provided CEHC further comprising a backpressure control system comprising an inert gas source and configured to control a pressure inside a wellbore. 15. The method of claim 12 , the provided CEHC further comprising: a water gas separation system configured to produce a flow of gas and a flow of water; a set of sensors comprising at least one sensor selected from the group containing: a temperature sensor, a pressure sensor, a gas flow measurement system configured to measure the flow of gas, a water flow measurement system configured to measure the flow of water, and a high-pressure linear variable displacement transducer (LVDT) configured to measure settlement within the sediment bed; and an instrumentation module configured to monitor at least one sensor from the set of sensors while the centrifuge is in-flight. 16. The method of claim 15 , the instrumentation module further comprising: a processor in operable communication with at least one sensor from the set of sensors, and a machine-readable medium in operable communication with the processor and having instructions stored thereon that, when executed by the processor, report or record at least one value correlated to temperature, pressure, pumping rate, or wellbore pressure. 17. The method of claim 16 , wherein the provided CEHC is securely fastened to the centrifuge and sufficiently sealed and insulated to operate as an adiabatic system. 18. A centrifuge energy harvesting chamber (CEHC) system comprising: a centrifuge, a high-pressure chamber mounted to the centrifuge, a sediment bed within the high-pressure chamber, a high-pressure pump comprising a multiplicity of syringe pumps, the high pressure pump operably connected to the high-pressure chamber and configured for repeated sequential operation of the multiplicity of syringe pumps to provide a continuous high-pressure fluid flow at an elevated gravity of the centrifuge, a cooling system operably connected to the high-pressure chamber, an actuator configured to provide an activation force, and a surcharge plate to configured to load the sediment bed when acted upon by the activation force. 19. The CEHC system of claim 18 , further comprising a backpressure control system comprising an inert gas source and configured to control a pressure inside a wellbore. 20. The CEHC system of claim 19 , further comprising at least one seal and at least one insulating member configured to allow operation of the CEHC as an adiabatic system while the centrifuge is in-flight.
Production of gas hydrates · CPC title
Pressure vessels, e.g. autoclaves · CPC title
resulting in a turbulent flow of the reactants, such as in centrifugal-type reactors, or having a high Reynolds-number · CPC title
Flow rate measurement · CPC title
Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00 · CPC title
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