Key information

Title
Method of testing an integrity of a structure comprising a chamber, and related apparatus
Application number
20180592
Case type
National
Status
07.06.2022 Patent meddelt (B1)
Filed
26.04.2018
Effective date
26.04.2018
Publicly available
28.10.2019
Next annual fee due
30.04.2027
Applicant
SCANWELL TECHNOLOGY AS (NO)
Owner
SCANWELL TECHNOLOGY AS (NO)
Inventor
Morten Kvernvold (NO)
Agent
HÅMSØ PATENTBYRÅ AS (NO)
Granted
07.06.2022
Patent number
346330
Expiry date
26.04.2038

Abstract and drawing

Disclaimer: This text has been machine-scanned and may contain errors – please refer to "Publications" for legally binding content.
There is described a method of testing an integrity of a structure (2) comprising a chamber (22), wherein the method comprises the steps of: a. letting out gas from the chamber (22) in a flow; b. using at least one sensor (11, 12) to obtain at least one parameter associated with the flow or a condition of gas in the flow; and c. determining whether fluid has entered the chamber (22) in performing step a, and/or determining a rate of fluid entering the chamber (22) in performing step a, and/or determining a rate of fluid entering the chamber (22) in performing step a, using the obtained parameter, the determination being based on the amount of gas that has left the chamber (22).

Publications

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 Date Doc. No. Process Case number In/Out Journal description To/from
 08.06.2022 21-01 Saksbehandling 20180592(346330) UT PT Registreringsbrev Nasjonal Patent (15) (PT20180592)
16.03.2022 20-01 Saksbehandling 20180592 UT Intention to grant HÅMSØ PATENTBYRÅ AS
 05.03.2022 19-01 Saksbehandling 20180592 INN 2021.07.12 fig 1-3
12.01.2022 18-01 Saksbehandling 20180592 INN PCT-tegn
02.07.2021 17-07 Saksbehandling 20180592 INN P28332NO00 Translated claims HÅMSØ PATENTBYRÅ AS
 02.07.2021 17-06 Saksbehandling 20180592 INN P28332NO00 Replacement drawings sheet 3_3 HÅMSØ PATENTBYRÅ AS
 02.07.2021 17-05 Saksbehandling 20180592 INN P28332NO00 Letter to IPO HÅMSØ PATENTBYRÅ AS
 02.07.2021 17-04 Saksbehandling 20180592 INN P28332NO00 Amended description HÅMSØ PATENTBYRÅ AS
 02.07.2021 17-03 Saksbehandling 20180592 INN P28332NO00 Amended claims HÅMSØ PATENTBYRÅ AS
 02.07.2021 17-02 Saksbehandling 20180592 INN P28332NO00 Additional sheets description markup HÅMSØ PATENTBYRÅ AS
 02.07.2021 17-01 Saksbehandling 20180592 INN Korrespondanse (Hovedbrev inn) HÅMSØ PATENTBYRÅ AS
 17.04.2021 16-01 Saksbehandling 20180592 UT Substantive examination HÅMSØ PATENTBYRÅ AS
 17.04.2021 15-01 Saksbehandling 20180592 INN D7 2013 Kvernvold Gas-LIft Form -Leak Metering GLV
17.12.2020 14-02 Saksbehandling 20180592 INN P28332NO00_ Response_Official_Action HÅMSØ PATENTBYRÅ AS
 17.12.2020 14-01 Saksbehandling 20180592 INN Korrespondanse (Hovedbrev inn) HÅMSØ PATENTBYRÅ AS
 28.08.2020 13-02 Saksbehandling 20180592 UT D7 2013 Kvernvold Gas-LIft Form -Leak Metering GLV
28.08.2020 13-01 Saksbehandling 20180592 UT Realitet patent HÅMSØ PATENTBYRÅ AS
 28.08.2020 12-01 Saksbehandling 20180592 INN D7 2013 Kvernvold Gas-LIft Form -Leak Metering GLV
15.06.2020 11-04 Saksbehandling 20180592 INN Krav ren HÅMSØ PATENTBYRÅ AS
 15.06.2020 11-03 Saksbehandling 20180592 INN Krav merket HÅMSØ PATENTBYRÅ AS
 15.06.2020 11-02 Saksbehandling 20180592 INN Hovedbrev HÅMSØ PATENTBYRÅ AS
 15.06.2020 11-01 Saksbehandling 20180592 INN Korrespondanse (Hovedbrev inn) HÅMSØ PATENTBYRÅ AS
 18.03.2020 10-01 Saksbehandling 20180592 INN Korrespondanse (Hovedbrev inn) HÅMSØ PATENTBYRÅ AS
 03.03.2020 09-01 Saksbehandling 20180592 UT PT Varsel om betaling av første årsavgift (3317) (PT20180592)
14.01.2020 08-01 Saksbehandling 20180592 UT Realitet patent HÅMSØ PATENTBYRÅ AS
 26.09.2019 07-01 Saksbehandling 20180592 INN Fig1
02.09.2019 06-03 Saksbehandling 20180592 INN Attachment to letter to Patentstyret HÅMSØ PATENTBYRÅ AS
 02.09.2019 06-02 Saksbehandling 20180592 INN Hovedbrev HÅMSØ PATENTBYRÅ AS
 02.09.2019 06-01 Saksbehandling 20180592 INN Korrespondanse (Hovedbrev inn) HÅMSØ PATENTBYRÅ AS
 02.07.2019 05-01 Saksbehandling 20180592 INN Korrespondanse (Hovedbrev inn) HÅMSØ PATENTBYRÅ AS
 02.05.2019 04-02 Saksbehandling 20180592 INN Hovedbrev HÅMSØ PATENTBYRÅ AS
 02.05.2019 04-01 Saksbehandling 20180592 INN Korrespondanse (Hovedbrev inn) HÅMSØ PATENTBYRÅ AS
 02.11.2018 03-02 Saksbehandling 20180592 UT PT_report 12:47:09
02.11.2018 03-01 Saksbehandling 20180592 UT Realitet patent HÅMSØ PATENTBYRÅ AS
 03.05.2018 02-01 Saksbehandling 20180592 UT Infobrev til oppfinner HÅMSØ PATENTBYRÅ AS
 26.04.2018 01-05 Saksbehandling 20180592 INN Erklæring Søkers rett til oppfinnelse HÅMSØ PATENTBYRÅ AS
 26.04.2018 01-04 Saksbehandling 20180592 INN Beskrivelse HÅMSØ PATENTBYRÅ AS
 26.04.2018 01-03 Saksbehandling 20180592 INN Patenttegninger HÅMSØ PATENTBYRÅ AS
 26.04.2018 01-02 Saksbehandling 20180592 INN Fullmakt HÅMSØ PATENTBYRÅ AS
 26.04.2018 01-01 Saksbehandling 20180592 INN Søknadsskjema Patent HÅMSØ PATENTBYRÅ AS

Description, claims and drawings

Disclaimer: This text has been machine-scanned and may contain errors – please refer to "Publications" for legally binding content. Description
METHOD OF TESTING AN INTEGRITY OF A STRUCTURE COMPRISING A CHAMBER, AND RELATED APPARATUSField of inventionThe present invention relates to the field of integrity testing, and in particular, it relates to a method of testing an integrity of a structure which comprises a chamber, and related apparatus. In certain embodiments, such a structure, e.g. components for providing a barrier in a wellbore, is tested as to what extent it may withstand fluid leakages.BackgroundIn a wide range of contexts, it can be important to check that a structure is of the necessary integrity for its intended purpose, e.g. before it is brought into normal operational use or as part of regular operational testing or troubleshooting. One such example may be a structure of a wellbore, such as a portion of a pipe in the wellbore which may be intended to separate an environment on one side of the pipe from a region inside the pipe.In order to verify that the structure is suitable and adequately isolates against the adjacent environment, it may be necessary to perform a test. In the oil and gas exploration and production industry, it is known to perform a so-called “inflow pressure test” on a structure to determine if there is a leak of fluid through a part of a structure, the part typically being referred to as a “barrier element”. Such tests may identify whether the structure “leaks” or not when subjected to a pressure differential, and therefore it may be inferred from the test whether the structure has sufficient integrity.A first type of inflow pressure test known from prior art may have the following features:- The structure to be tested comprises a chamber. This chamber may for instance be an annular space in a wellbore between tubulars.- A bleed valve in fluid communication with the chamber is opened to bleed the pressure of the chamber to zero overpressure.- The volume of fluids in the chamber is determined.- The bleed valve is closed.- At certain intervals the pressure and the fluid volume in the chamber is determined.- It is determined whether there is a leak through the structure, and quantified if there is a leak, based on the determined pressure and fluid volume.A second type of inflow pressure test known from prior art may have the following features:- A pressure-regulating valve is used to lower the pressure in the chamber to create a pressure difference between the chamber and an adjacent environment. - While maintaining the pressure difference constant, a flow meter is used to determine a quantity of fluid flowing through a fluid line in fluid communication with the chamber.- Based on the determined quantity of fluid, it may be determined if there is a leak and to quantify any occurring leak.In the first of the two types of inflow pressure tests, the pressure in the chamber is generally reduced significantly to set up an investigation of the condition of the structure. Any leak is determined, and quantified, after a process of lowering the pressure and keeping the pressure low (while determining the gas volume), pressure is allowed to increase in the chamber. In the second of the two mentioned types of inflow pressure tests, the pressure in the chamber is reduced and then kept constant. Results for determining the condition of the structure may be obtained while the pressure is kept constant. The second type of test typically takes less time to perform, as the pressure is normally not reduced as much in the second test as in the first, and can therefore be advantageous compared to the first type of test.The first type of test is further explained in the publication SPE 117961 titled “Design and Fabrication of a Low Rate Metering Skid to Measure Internal Leak Rates of Pressurized Annuli for Determining Well Integrity Status”, published by Society of Petroleum Engineers in 2008. The second type of test is described in WO 2010151144 A1.Both the above-mentioned tests may suffer from having to lower the pressure of the chamber significantly prior to obtaining results for determining the condition of the structure. Having to reduce the pressure of the chamber can be undesirably time consuming, particularly if the volume of the chamber and the present gas volume is large.The following publications may facilitate an appreciation of how the present invention distinguishes over prior art:● “Well integrity – Christmas tree acceptable leakage rater and sustained casing pressure”, Mrudhul Raj, Atkins Ltd, Aberdeen, UK, 24th Institution of Chemical Engineers Symposium on Hazards, (HAZARDS XXIV), Institution of Chemical Engineers Symposium Series 159, Edinburgh, United Kingdom, 7 – 9 May 2014;● “Leak metering gas lifted wells”, Morten Kvernvold, 36th Gas-Lift Workshop, Stavanger, Norway February 4 – 8, 2013;● US Patent Publication Number US9518461 B2;● US Patent Application Publication Number US2013111985 A1;● PCT Publication Number WO2015012702 A2; and● US Patent Application Publication Number US2016223426 A1.An object of the invention is to remedy or to reduce at least one of the drawbacks of prior art. Summary of the inventionAccording to a first aspect of the invention, there is provided a method of testing an integrity of a structure comprising a barrier and a chamber, wherein the barrier separates an exterior from the chamber, by determining if there is a leak of a fluid through the barrier into the chamber of the structure from the exterior, and wherein the chamber is provided with a valve through which gas can be let out of the chamber, the method comprising the steps of: a. determining an initial amount of gas in the chamber; b. letting out gas from the chamber, through the valve, in a flow; c. while performing step b: determining an amount of gas that has left the chamber in the flow and using at least one sensor to obtain at least one parameter associated with the flow; and d. using the obtained parameter, the determined amount of gas that has left the chamber and the determined initial amount of gas in the chamber to determine whether fluid has entered the chamber in the leak in performing step b.The method may be a method of performing an inflow test.The determination in step d may be performed during step a, or subsequently, e.g. by analysis of acquired data.The valve may control the pressure in the chamber. The valve will typically be closed prior in a preparatory phase, and opened to allow gas to flow from the chamber as the test is started. During the preparatory phase, initial parameters used for later calculations to determine the condition of the structure may be determined. One or more, e.g. all, of the steps of the method may be performed while lowering the pressure in the chamber.The determination in step d may further be based on the amount of gas remaining in the chamber after an amount of the gas has left the chamber in the flow.The parameter may be a pressure of the gas in the flow. The parameter may be obtained by use of a pressure sensor placed in fluid communication with the flow line.The parameter may be a rate of flow through the flow line. The parameter may be obtained by use of a flow rate sensor placed in fluid communication with the flow line.The parameter may be a temperature of the gas. The parameter may be obtained by use of a temperature sensor placed in fluid communication with the flow line.A plurality of parameters may be obtained. The plurality of parameters may comprise any one of or a plurality of a pressure of the gas, a flow rate of the flow, a temperature, gas composition and/or any other parameter that may be used to determine whether a fluid has entered the chamber and/or to determine a rate of fluid entering the chamber.The structure may e.g. be a portion of a pipe of a wellbore. The adjacent environment may be an annulus, a centre pipe, a formation or another environment. The structure may otherwise be e.g. at least a portion of a pipeline or at least a portion of a fluid container such as a tank.An initial mass of gas in the chamber, m, may be calculated using the following formula:where:mi = initial mass of the gas in the chamber;Pi = initial pressure in the chamber;Vi = initial gas volume in the chamber;MW = molecular weight of the gas in the chamber;Zi = initial compressibility of the gas in the chamber;R = rankine constant; andTi = initial temperature of the gas in the chamber.A current mass of gas in the chamber may be calculated using the following formula:where:mc = current mass of the gas in the chamberPc = current pressure in the chamber;Vc = current gas volume in the chamber;MW = molecular weight of gas;Zc = current compressibility of the gas in the chamber;R = rankine constant; andTc = current temperature of the gas in the chamber.A mass of gas having leaked through the barrier may be calculated using the following formula:mi = mc — mi + mpwhere:ml = mass of gas having leaked into the chamber;mc = current mass of the gas in the chamber;mi = initial mass of the gas in the chamber; andmp = mass of gas produced.The step of obtaining the parameter or parameters may be performed a plurality of times. The plurality of times may be spread out over a time interval.The above-mentioned calculations may be repeated for each of the plurality of times the parameter or parameters are determined. By determining the parameters and making the calculations a plurality of times over a time interval, it may be possible to perform a dynamic leak metering, and/or it may be possible to see if a leak rate changes as a pressure differential changes. A pressure response for a theoretical zero-leak situation may be calculated using the following formula:where: = pressure response with zero leak through the barrier.The theoretical pressure response, , may be used to compare to a pressure response determined from the determined parameters. It may be possible to use a value determined from the comparison to deduce and/or calculate if there is a leak into the chamber and, if there is a leak, to quantify the leak.The fluid in the chamber may comprise a gas and a liquid. The amount of liquid in the chamber may be determined. To determine the amount of liquid in the chamber, an acoustic measuring device may be used. The acoustic measuring device may be used to determine a gas-liquid contact in the chamber. The gas-liquid contact in the chamber defines the height of a liquid column in the chamber and may thus be used as a parameter to determine the volume of liquid in the chamber.The information gathered from determining the amount of liquid in the chamber may be used to determine an amount of gas in the chamber, and/or to determine an amount of gas and/or liquid which has entered the chamber in a leak in a barrier of the structure from an exterior of the structure into the chamber. By knowing the total volume of the chamber and the height and volume of a liquid column in the chamber, the remaining volume occupied by a gas can be determined.The step of determining an amount of liquid in the chamber may be performed a plurality of times over a time interval. The plurality of times may include at least once prior to letting out gas from the chamber in a flow, and/or at least once while letting out gas from the chamber in a flow, and/or at least once after having let out gas from the chamber in a flow. Determining the amount of liquid a plurality of times over a time interval may be advantageous to determine if the amount of liquid in the chamber changes over time, e.g. to determine if there has been an influx of liquid into the chamber over the time interval.According to a second aspect of the invention, there is provided apparatus for performing the method according to the first aspect of the invention, for testing an integrity of a structure comprising a chamber, the apparatus comprising: at least one flow line section for containing a flow comprising gas from the chamber; at least one sensor for obtaining at least one parameter associated with the flow or a condition of gas in the flow; and at least one determiner, comprising a computer device for performing calculations to determine whether fluid has entered the chamber, configured to use the obtained parameter for determining whether fluid has entered the chamber, the fluid entering chamber after the gas is let out of the chamber in the flow, the determination being based on the amount of gas that has left the chamber. The apparatus may be an apparatus for performing the method according to the first aspect of the invention. The apparatus is advantageous over known apparatuses as it may be used to test the integrity of a structure comprising a chamber, e.g. a chamber of a wellbore, while lowering the pressure in the chamber, and thus allowing for obtaining results in significantly shorter time than known apparatuses for testing integrity of a structure comprising a chamber, e.g. apparatuses for performing known inflow pressure tests. The apparatus allows for integrity testing in real-time.The apparatus may comprise a pressure sensor and/or a flow meter. The determiner may comprise a computer device for performing calculations to determine whether fluid has entered the chamber and/or determining a rate of fluid entering the chamber.The apparatus may comprise the structure. The pressure sensor and the flow meter may be in fluid communication with the chamber.The apparatus may further comprise a temperature sensor for determining a temperature and an acoustic measuring device for determining a gas-liquid contact.The apparatus may further comprise a computer device.The structure may comprise a portion of a pipe of a wellbore.According to a third aspect of the invention, there is provided a computer program for use in performing the method according to the first aspect of the invention. The computer program may be configured for determining whether fluid has entered the chamber and/or determine a rate of fluid entering the chamber wherein the fluid entering the chamber after gas is let out of the chamber in the flow. The determination may be based on the amount of gas that has left the chamber.The computer program may comprise machine-readable instructions for performing the determination.The computer program may be further configured to utilise at least one obtained parameter associated with the flow or condition of the gas of the flow.According to a fourth aspect of the invention, there is provided a computer device for use in performing the method according to the first aspect of the invention, the computer device comprising at least one processor, the processor being configured to execute the computer program according to the third aspect of the invention, to perform the determination.According to a fifth aspect of the invention, there is provided a computer-accessible storage medium on which at least part of the computer program according to the third aspect of the invention is stored.Description and drawings There will now be described, by way of example only, embodiments of the invention, with reference to the accompanying drawings, in which:Figure 1 shows a schematic representation of an apparatus for testing an integrity of a structure according to an embodiment of the invention;Figure 2 shows a schematic representation of an apparatus for testing an integrity of a structure according to another embodiment; andFigure 3 shows a graph illustrating results from use of the apparatus of Figure 1 or 2, including a calculated theoretical zero-leak pressure response, a determined pressure response from a leak test, a mass leak rate and a volumetric leak rate.Figure 1 shows an apparatus 1 for testing the integrity of the structure 2. More particularly, the apparatus 1 is used to determine if there is a leak through a part of the structure 2, and it is used to determine an amount of fluid leaking through the part of the structure 2 per unit time.The structure 2 forms a chamber 22, which in this embodiment is a first portion 22 of a wellbore 21 of a petroleum well. The structure 2 comprises a barrier 23 for separating the chamber 22 from a second portion 24 of the wellbore 21. The chamber 22 contains a fluid including a gas. The apparatus 1 is employed to determine if there is a leak associated with the barrier 23.A pipe 25 forms a flow path for the gas from the chamber 22 to a receiving end (not shown) for receiving the gas. There is a pressure differential between the chamber 22 and the receiving end. The pressure in the chamber 22 is higher than the pressure in the receiving end, such that a flow of gas through the pipe 25 can be directed from the chamber 22 to the receiving end.The receiving end has for example a closed drain system, a tank, a flaring system, a process plant, or other low-pressure receiver.The apparatus 1 has a valve 13 placed in the pipe 25 for blocking or opening the flow path. Furthermore, the apparatus has a pressure sensor 11 for determining the pressure of the fluid in the chamber 22, and a flow meter 12 for determining a rate of flow of gas from the chamber 22, both placed in the pipe 25.The purpose of the apparatus 1 in this embodiment is mainly to determine if there is a leak of fluid from the second portion 24 into the chamber 22 and to determine a flow rate of fluid from the second portion 24 into the chamber 22 if there is a leak.A method of testing the integrity of the structure 2, using the apparatus 1, is performed as follows.The structure 2 forms the chamber 22, and initially the valve 13 is closed. The chamber 22 is therefore a closed volume containing the gas. The pressure sensor 11 determines an initial pressure of the gas in the chamber 22.The valve 13 is then opened. Gas is let out of the chamber 22 and is conveyed in a flow along the pipe 25 toward the receiving end. The flow rate of the gas in the flow is obtained and pressure obtained from the pressure sensor 11 on a continuous basis while the gas is being let out of the chamber 22 and flows through the pipe 25.By making use of the measured flow rate and pressure, it is then determined as to whether a leak has occurred. The rate of leakage is determined if there is found to be a leak. These “leak” determinations are based upon the amount of gas that has left the chamber 22 at a given “later” point in time, after opening the valve 13 and letting out gas from the chamber 22.The leak determinations are made in this example through determining the mass of gas (i.e. an amount of gas, ml) that has leaked into the chamber 22 by applying the following formula:ml = mc — mi + mpwhere:mi = mass of gas having leaked into the chamber22 ;mc = current mass of the gas in the chamber 22 at the later point in time;mi = initial mass of gas in the chamber 22; andmp = mass of produced gas.Each of the variables on the right hand side of the above equation are determined and combined to obtain the desired quantity (mi), as explained now further.Initial massThis is the mass of the total amount of the gas that is contained in the chamber 22 before the valve 13 is opened. The initial mass of gas mi may be determined by use of the following formula:where:mi = initial mass of a gas in the chamber 22;Pi = initial pressure in the chamber 22;Vi = initial gas volume in the chamber 22;MW = molecular weight of the gas in the chamber 22;Zi = initial compressibility of the gas in the chamber 22;R = rankine constant; andTi = initial temperature in the chamber 22.An operator generally knows the volume of the chamber 22 as this is dictated by the physical design of the structure 2 being investigated. The initial pressure from the pressure sensor 11 is used to determine the initial mass of gas in the chamber 22. The initial pressure P, is obtained from the pressure sensor 11 . The initial gas volume in the chamber 22 the molecular weight of the gas in the chamber 22, the initial compressibility of the gas in the chamber 22 are also generally known to the operator, as is the initial temperature 7) in the chamber 22.The variables discussed above can be determined if not known. The initial temperature 7) can be determined by use of a temperature sensor. The initial gas volume can be determined from determining or knowing the total volume of the chamber 22 and determining a gas-liquid contact in the chamber 22 by use of an acoustic measuring device. The molecular weight MW and the initial compressibility of the gas Zi can be determined by use of a gas chromatograph. A skilled person will understand that other methods of obtaining the variables than those mentioned may be used to obtain the variables.As can be appreciated, any measurements that are dependent upon live conditions, such as for example the temperature measurement, initial pressure, and the amount of the gas that is fed into the chamber 22 to prepare it for the test are made in a preliminary stage, before opening the valve 13 to let out of the chamber 22 through the pipe 25.Produced massWhen the initial mass of the gas and the initial pressure have been determined, the valve 13 is opened and gas flows from the chamber 22. As a result of the flow of gas from the chamber 22, pressure drops over time. The gas that leaves the chamber 22 and flows through a section of the pipe 25 is referred to as “produced gas”.The mass (i.e. amount) of produced gas can be determined by use of the following formula:where:mp = mass of produced gas;Q = average gas flow over a period of time;δp = average density of produced gas over the period of time; andΔt = period of time.Over a period of time, the gas flow is determined and recorded by use of the flow meter 12. Other means for determining the flow are in other embodiments used instead of the flow meter 12.The pressure is determined and recorded by use of the pressure sensor 11 , and the determined pressure is used to determine the density of produced gas. Together with the determined density, the determined gas flow is used to determine a mass of produced gas, i.e. gas that has moved from the chamber 22 through the flow meter 12, at a certain point in time, a period of time after opening the valve 13.Current massThe current mass of gas in the chamber 22 at the later point in time can be determined similarly to how the initial mass, with current, rather than initial, values for the variables in the formula:The current values for the variables can be determined by use of previously mentioned methods, or they can, in some cases, be assumed. E.g. the temperature in the chamber 22, the molecular weight, the compressibility and the volume of gas may be assumed to stay substantially constant during the course of a test.The current mass of gas in the chamber 22 refers to the mass of gas at the later point in time after the method is initiated and gas is flowing or has flowed out of the chamber 22 through the pipe 25.The pressure continuously being measured from the pressure sensor 11 gives the pressure Pc.Leak determinationIn light of the above, by finding the initial mass of gas in the chamber 22, the mass of produced gas, and the current mass of gas in the chamber 22, the mass mi is readily obtainable and it is therefore possible to deduce if there has been a leak of gas into the chamber 22 and to quantify such a leak, e.g. obtain the leak rateThe presence of the leak may be determined as follows. If there is a positive value obtained for the mass ml, then there is a leak. If the leak value is above a predefined threshold, then it could be inferred from the leak value that the structure 2 is not of sufficient integrity, i.e. it fails the test.From the determined mass mi, the leak rate can be found by use of the following formula:where:Ql = average leak rate of gas into the chamber 22 over a period of time;ml = mass of gas having leaked into the chamber 22;δl = average density of gas having leaked into the chamber 22 over the period of time; Δt = period of time.In some variants, the calculations are automated. Recorded data and/or parameters from the flow meter 12 and the pressure sensor 11 are fed as input data to a computer device 17, and the computer device uses the data to perform the necessary determinations and/or analysis to find if there is a leak into the chamber 22 and/or quantify the leak rate if there is a leak.In some variants of the method, a dynamic leak metering may advantageously be achieved. Depending on the case in question, the leak rate may change as a differential pressure between the chamber 22 and the second section 24 changes as gas flows from the chamber 22 and the pressure in the chamber 22 drops. By taking measurements of flow rate and pressure repeatedly and/or continuously, the leak rate development over time can be determined.The determined pressure development can be compared to a modelled pressure development, to determine a characteristic of an inflow into the chamber 22 from the second portion 24. The modelled pressure development can be a calculated pressure development given a determined leak rate in a no-inflow scenario. The comparison of the determined pressure development to the modelled, no-inflow scenario, pressure development could give a clear indication of whether or not there was an inflow of fluid into the chamber 22, and possibly also a rate of leak into the chamber 22.Note that other devices may be used to obtain data than those mentioned as part of the apparatus described above with reference to Figure 1. It is possible to determine the gas flow from the chamber 22 by other means than by use of a flow meter 12. The density of the gas may be determined e.g. by use of a density sensor. The temperature may be determined e.g. by use of a temperature sensor. The compressibility and/or the molecular weight of the gas may be determined e.g. by use of a gas chromatograph. The volume of gas and/or liquid in the chamber 22, the temperature, the compressibility and/or the molecular weight may in many cases be readily available and known to an operator e.g. from earlier knowledge about or earlier operations performed at the site.In Figure 2, another variant of the apparatus 1 has an acoustic measuring device 16 for determining a gas-liquid contact in the chamber 22 in a case where it is expected that the chamber 22 not only contains gas, but also contains liquid, and/or that the inflow fluid can contain liquid. Nevertheless, the technique as described above in relation to Figure 1 can still be used in the scenario of Figure 2.By way of the acoustic measuring device 16, the apparatus 1 can be used to determine an inflow of fluid where the fluid is at least partly in liquid form. The acoustic measuring device 16 is used to determine where in the chamber 22 the gas-liquid contact is, to determine the volume of the liquid to determine the volume of the gas. The volume of gas in the chamber 22 will then be the total volume of the chamber 22 minus the volume of the liquid.The acoustic measuring device 16 may be used a plurality of times over a time interval to determine if and potentially how the gas-liquid contact in the chamber 22 changes over time. The information gathered from the plurality of times the acoustic measuring device 16 may be used to determine a leak rate of liquid into the chamber 22, and/or for more accurately calculating the leak rate of gas into the chamber 22.Furthermore, the apparatus 1 of Figure 2 includes a computer device 17 for making calculations using the data obtained by using the pressure sensor 11, the flow meter 12 and the acoustic measuring device 16. The computer device 17 is connected to the pressure sensor 11, the flow meter 12 and the acoustic measuring device 16 for receiving data therefrom.The computer device 17 has a storage medium (not shown) for storing a computer program for performing the calculation using the data. The program is executed by the processor of the computer and determines whether fluid has entered the chamber 22 in the form of a leak and determines the rate of entry of any such fluid that has enters the chamber 22.Embodiments of the invention can be advantageous in that they may avoid needing to lower pressure in the chamber 22 to the same degree as in the inflow pressure tests of the prior art. In particular, parameters can be obtained from the sensors 11, 12 whilst gas is let out of the chamber 22, such that results may be obtained more quickly. For example, a leak may be revealed and quantified continuously from the moment that the gas is let out of the chamber 22 in the flow.It can be advantageous in various embodiments of the invention to determine the temperature of the gas, as it is a parameter of the above-mentioned formulas for determining mass. The temperature can be determined if it is not known by an operator initially and/or if it may change during an execution of the method. Likewise, it may be advantageous to determine at least one of: a molecular weight of the gas; and a compressibility of the gas. Either one of, or both of the molecular weight of the gas and the compressibility may be determined by use of a gas chromatograph. The molecular weight of the gas and the compressibility of the gas are variables in the formulas mentioned above. The variables may be known by an operator, but may be determined if the variables are not known. The gas composition of the gas in the volume may change during an execution of the method, which may result in a change of the molecular weight and compressibility. Therefore, if there is a risk of the gas composition changing during an execution of the method, the molecular weight and the compressibility of the gas could advantageously be determined as part of the step of obtaining the parameter of the gas of the flow.The method described above may be advantageous compared to prior art, as it may be carried out and even completed while lowering the pressure in the chamber 22, without any preparatory lowering of the pressure prior to obtaining relevant parameters to determine the condition of the structure. The pressure drop in the chamber 22 during the test may typically be lower than in prior art tests, and the pressure build-up needed after completing the test may typically be lower. Thus, an integrity test may be completed in significantly less time than in the prior art.Figure 3 shows a graph illustrating a calculated theoretical zero-leak pressure response 200, a determined pressure response 100 from a leak test, a mass leak rate 400 and a volumetric leak rate 300 from a test case wherein a method as described in relation to Figures 1 or 2 was applied and used to detect the presence of a leak and determine the mass of material leaked. Such a graphical representation of the data may be used as part of the method to present obtained data, to illustrate clearly if there is a leak, the rate of the leak, and how the leak rate changes over time as the pressure of the fluid in the chamber 22 changes. Figure 3 further illustrates that it may be possible to determine early whether there is a leak and whether said leak is of a rate that is not accepted according to industry standards early, while the pressure in the chamber 22 is being reduced.Whether there is a leak may become apparent just by comparing the determined pressure response 100 to the calculated theoretical zero-leak pressure response 200. As shown in Figure 3, there can be a significant, clear difference between the theoretical pressure response 200 and the determined pressure response 100.Although the apparatus 1 described above and shown in Figures 1 and 2 comprises both a pressure sensor 11 and a flow meter 12 for obtaining parameters associated with the flow or a condition of gas in the flow, the method may be performed using only one sensor 11, 12 for obtaining such a parameter.Given that the flow from the chamber 22 through the pipe 25 is restricted to a known flow rate, e.g. by use of a type of flow-restricting device (not shown), it is enough in some variants to obtain information on the pressure of fluid in the chamber and/or gas in the flow by use of a pressure sensor 11 to be able to determine whether fluid has entered the chamber 22.It may also be possible to determine whether fluid has entered the chamber 22 by using a flow meter 12 only, without using a pressure sensor 11. This may be done, e.g. if a pressure downstream of the flow meter 12 is known and substantially constant. It may then be possible to deduce an expected development of flow through the flow meter 12 for a theoretical scenario where there is no inflow into the chamber 22. A comparison of expected development of flow to a flow measured by use of the flow meter 12 may then be used to determine whether fluid has entered the chamber 22.It should be noted that the above-mentioned embodiments illustrate rather than limit the invention, and that those skilled in the art will be able to design many alternative embodiments without departing from the scope of the appended claims.Methods of determining parameters of a fluid, such as pressure, gas volume, molecular weight of a gas, compressibility of a gas, temperature of a gas, mass of a gas, and more, that may be relevant for the method according to the invention, that are not mentioned in this text, that are known to a skilled person, or that will in the future be known to a skilled person, may be performed as part of the method according to the invention. The invention is not restricted to the specific methods of obtaining said parameters mentioned in this text.In the claims, any reference signs placed between parentheses shall not be construed as limiting the claim. Use of the verb "comprise" and its conjugations does not exclude the presence of elements or steps other than those stated in a claim. The article "a" or "an" preceding an element does not exclude the presence of a plurality of such elements.The mere fact that certain measures are recited in mutually different dependent claims does not indicate that a combination of these measures cannot be used to advantage.
Claims
C l a i m s1. A method of testing an integrity of a structure (2) comprising a barrier (23) and a chamber (22), wherein the barrier (23) separates an exterior from the chamber (22), by determining if there is a leak of a fluid through the barrier (23) into the chamber (22) of the structure (2) from the exterior, and wherein the chamber (22) is provided with a valve (13) through which gas can be let out of the chamber (22), the method being c h a r a c t e r i s e d i n that it comprises the steps of:a. determining an initial amount of gas in the chamber (22);b. letting out gas from the chamber (22), through the valve (13), in a flow;c. while performing step b: determining an amount of gas that has left the chamber (22) in the flow and using at least one sensor (11, 12) to obtain at least one parameter associated with the flow; andd. using the obtained parameter, the determined amount of gas that has left the chamber (22) and the determined initial amount of gas in the chamber (22) to determine whether fluid has entered the chamber (22) in the leak in performing step b.2. The method according to claim 1, wherein the method is a method of performing an inflow test.3. The method according to claim 1 or 2, wherein the determination in step d is performed during step a, or subsequently by analysing acquired data.4. The method according to any one of the preceding claims, wherein step a further comprises reducing fluid pressure in the chamber (22) and the determination is performed so as to determine whether fluid has entered the chamber (22) in the leak in performing step b, and/or determine the rate of fluid entering the chamber (22), in a period over which the pressure in the chamber (22) has reduced.5. The method according to any one of the preceding claims, wherein the method further comprises performing at least one calculation to determine an amount of fluid that has entered the chamber (22) in the leak based on any one or more of:i. the amount of gas remaining in the chamber (22) after step b is started;ii. the initial amount of gas in the chamber (22) before step b is started; andiii. the amount of gas that has left the chamber (22) in performing step b.6. The method according to claim 5, wherein the method further comprises calculating any one or more of said amounts i. to iii. using the parameter obtained by use of the sensor (11, 12).7. The method according to any one of the preceding claims, which further comprises using the parameter obtained by way of the sensor to evaluate or calculate the amount of gas that has left the chamber (22).8. The method according to any one of the preceding claims, wherein the determination in step d is further based on the amount of gas remaining in the chamber (22) after said amount of the gas has left the chamber (22) in the flow.9. The method according to any one of the preceding claims, wherein the parameter comprises a pressure of gas in the flow, and is obtained using a pressure sensor (11) in fluid communication with the flow.10. The method according to any one of the preceding claims, wherein the parameter comprises a flow rate of the flow, and is obtained using a flow rate sensor (12) in fluid communication with the flow.11. The method according to any one of the preceding claims, wherein the parameter comprises a temperature of the gas, and wherein the parameter is obtained by use of a temperature sensor in fluid communication with the flow.12. The method according to any one of the preceding claims, wherein the determination in step d comprises determining, calculating, or estimating any one or more of:i. the amount of gas remaining in the chamber (22) after step b is started;ii. the initial amount of gas in the chamber (22) before step b is started; andiii. the amount of gas that has left the chamber (22) in performing step b.13. The method according to claim 12, wherein: the amount of gas comprises a mass of the gas;the initial amount of gas comprises an initial mass of the gas; and the amount of gas that has left the chamber (22) comprises a mass of the gas that has left the chamber (22).14. The method according to claim 13, wherein the initial mass of gas in the chamber (22), m, is determined, calculated, or estimated using the following formula:where:mi = initial mass of the gas in the chamber (22);Pi = initial pressure in the chamber (22);Vi = initial gas volume in the chamber (22);MW = molecular weight of the gas in the chamber (22);Zi = initial compressibility of the gas in the chamber (22);R = rankine constant; andTi = initial temperature of the gas in the chamber (22).15. The method according to claim 12, 13 or 14, wherein the amount of gas remaining in the chamber (22) comprises a current mass of gas in the chamber (22) which is determined, calculated, or estimated using the following formula:where:mc = current mass of the gas in the chamber (22)Pc = current pressure in the chamber (22);Vc = current gas volume in the chamber (22);MW = molecular weight of the gas in the chamber (22);Zc = current compressibility of the gas in the chamber (22);R = rankine constant; andTc = current temperature in the chamber (22).16. The method according to any one of the preceding claims, wherein the method further comprises determining an amount of fluid which has entered the chamber (22) in the leak in the barrier (23) of the structure (2), from an exterior of the structure (2) into the chamber (22).17. The method according to claim 16, wherein the determination of the amount of fluid which has entered the chamber (22) in the leak comprises calculating, determining, or estimating a mass of a gas that has leaked through the barrier (23) portion in the structure (2) using a linear combination of a current mass of gas in the chamber (22), an initial mass of gas in the chamber (22), and a mass of the gas that is produced by the gas leaving the chamber (22) in the flow.18. The method according to claim 17, wherein the mass of the gas that has leaked is calculated, determined, or estimated using the following formula:ml = mc — mi + mpwhere:ml = mass of gas having leaked into the chamber (22);mc = current mass of the gas in the chamber (22);mi = initial mass of the gas in the chamber (22); andmp = mass of gas produced in the flow.19. The method according to any one of the preceding claims, wherein the step of obtaining the parameter or parameters is performed a plurality of times.20. The method according to claim 19, wherein a plurality of calculations are performed using the parameter or parameters obtained from obtaining the parameter or parameters a plurality of times to determine how a leak rate changes over time.21. The method according to any one of the preceding claims, which further comprises:calculating a pressure response for a theoretical zero-leak situation;using the sensor to determine at least one pressure of the gas in the flow from the chamber (22);comparing the calculated response for the theoretical zero-leak situation to the determined pressure response (100) obtained by use of a pressure sensor (11); andusing the comparison to determine a condition of the structure (2).22. The method according to claim 21, wherein the pressure response for the theoretical zeroleak situation is calculated using the following formula:where:= pressure response with zero leak through the barrier (23).23. The method according to any one of the preceding claims, wherein the structure (2) comprises a pipe (25) or a part thereof.24. The method according to any one of the preceding claims, wherein the structure (2) forms a portion of a well.25. The method according to any one of the preceding claims, which further comprises determining an amount of liquid in the chamber (22).26. The method according to claim 25, wherein the step of determining an amount of liquid in the chamber (22) comprises determining a gas-liquid contact in the fluid in the chamber (22).27. The method according to claim 25 or 26, wherein the step of determining an amount of liquid in the chamber (22) comprises using an acoustic measuring device (16).28. The method according to any one of claims 25-27, wherein the step of determining an amount of liquid in the chamber (22) is performed a plurality of times, including prior to, during and after letting out gas from the chamber (22) in a flow.29. The method according to any one of claims 25-28, wherein the determined amount of liquid in the chamber (22) is used as a parameter in determining an amount of liquid which has entered the chamber (22) in a leak in a barrier (23) of the structure (2), from an exterior of the structure (2) into the chamber (22).30. The method according to claim 29, wherein the determined amount of liquid which has entered the chamber (22) in the leak in the barrier (23) of the structure (2) is used as a parameter to determine an amount of gas which has entered the chamber (22) in a leak in the barrier (23) of the structure (2), from an exterior of the structure into the chamber (22).31. Apparatus (1) for performing the method according to any one of claims 1 to 30, for testing an integrity of a structure (2) comprising a chamber (22), the apparatus (1) comprising: at least one flow line section for containing a flow comprising gas from the chamber (22);at least one sensor for obtaining at least one parameter associated with the flow or a condition of gas in the flow; andat least one determiner, comprising a computer device for performing calculations to determine whether fluid has entered the chamber, configured to use the obtained parameter for determining whether fluid has entered the chamber (22), the fluid entering chamber (22) after the gas is let out of the chamber (22) in the flow, the determination being based on the amount of gas that has left the chamber (22).32. Apparatus (1) according to claim 31, wherein the sensor further comprises either or both of:a pressure sensor (11) for obtaining at least one pressure in the flow; and a flow meter (12) for obtaining at least one flow rate of the flow.33. Apparatus (1) according to claim 31 or 32, wherein the determiner comprises a computer device (17).34. Apparatus (1) according to any of claims 31 to 33, wherein the sensor is in fluid communication with the chamber (22) and/or the flow from the chamber (22).35. Apparatus (1) according to any one of the claims 31 to 34, wherein the apparatus (1) further comprises a temperature sensor for determining a temperature and an acoustic measuring device (16) for determining an amount of liquid in the chamber (22).36. Apparatus (1) according to any of claims 31 to 35, further comprising at least one valve (13) operable for opening and closing a flow line for letting gas out of the chamber (22) for performing the test of the integrity of the structure (2).37. A computer program for use in performing the method of any of claims 1 to 30.38. The computer program according to claim 37, wherein the computer program comprises machine readable instructions for determining whether fluid has entered the chamber (22) and/or determine a rate of fluid entering the chamber (22) wherein the fluid entering the chamber (22) after the gas is let out of the chamber (22) in the flow, the determination being based on the amount of gas that has left the chamber (22).39. A computer device (17) for use in performing the method of any of claims 1 to 30, the computer device (17) comprising at least one processor, the processor being configured to execute the computer program of claim 37 or 38, to perform the determination.40. A computer-accessible storage medium on which at least part of the computer program of claims 37 or 38 is stored.PATENTKRAV1. Fremgangsmåte for testing av en integritet til en struktur (2) omfattende en barriere (23) og et kammer (22), hvori barrieren (23) separerer et ytre fra kammeret (22), ved å fastsette om det er en lekkasje av et fluid gjennom barrieren (23) inn i kammeret (22) for strukturen (2) fra det ytre, og hvori kammeret (22) utstyres med en ventil (13) hvorigjennom gass kan slippes ut av kammeret (22), fremgangsmåten karakterisert ved at den omfatter trinnene med:a. fastsetting av en innledende mengde gass i kammeret (22);b. utslipp av gass fra kammeret (22), gjennom ventilen (13), i en strømning; c. under utføring av trinn b: fastsetting av en mengde gass som har forlatt kammeret (22) i strømningen og anvendelse av minst én sensor (11, 12) for å innhente minst én parameter forbundet med strømningen; ogd. anvendelse av den innhentede parameteren, den fastsatte mengden med gass som har forlatt kammeret (22) og den fastsatte innledende mengden med gass i kammeret (22) for å fastsette om fluid har trengt inn i kammeret (22) i lekkasjen i utføring av trinn b.2. Fremgangsmåten ifølge krav 1, hvori fremgangsmåten er en fremgangsmåte for å utføre en innstrømningstest.3. Fremgangsmåten ifølge krav 1 eller 2, hvori fastsettingen i trinn d utføres under trinn a, eller senere ved analyse av innhentede data.4. Fremgangsmåten ifølge et hvilket som helst av de foregående kravene, hvori trinn a videre omfatter reduksjon av fluidtrykk i kammeret (22) og fastsettingen utføres for slik å fastsette om fluid har trengt inn i kammeret (22) i lekkasjen i utføringen av trinn b, og/eller fastsette raten for fluid som trenger inn i kammeret (22), i en periode hvor trykket i kammeret (22) har blitt redusert.5. Fremgangsmåten ifølge et hvilket som helst av de foregående kravene, hvori fremgangsmåten videre omfatter utføring av minst én beregning for å fastsette en mengde fluid som har trengt inn i kammeret (22) i lekkasjen basert på en hvilken som helst én eller flere av:i. mengden gass som er igjen i kammeret (22) etter at trinn b startes; ii. den innledende mengden gass i kammeret (22) før trinn b startes; og iii. mengden gass som har forlatt kammeret (22) i utføring av trinn b.6. Fremgangsmåten ifølge krav 5, hvori fremgangsmåten videre omfatter beregning av en hvilken som helst én eller flere av mengdene i. til iii. ved anvendelse av parameteren innhentet ved anvendelse av sensoren (11, 12).7. Fremgangsmåten ifølge et hvilket som helst av de foregående kravene, som videre omfatter anvendelse av parameteren innhentet ved hjelp av sensoren for å evaluere eller beregne mengden gass som har forlatt kammeret (22).8. Fremgangsmåten ifølge et hvilket som helst av de foregående kravene, hvori fastsettingen i trinn d videre baseres på mengden gass som er igjen i kammeret (22) etter at mengden med gassen har forlatt kammeret (22) i strømningen.9. Fremgangsmåten ifølge et hvilket som helst av de foregående kravene, hvori parameteren omfatter et trykk for gass i strømningen, og innhentes ved anvendelse av en trykksensor (11) i fluidkommunikasjon med strømningen.10. Fremgangsmåten ifølge et hvilket som helst av de foregående kravene, hvori parameteren omfatter en strømningsrate for strømningen, og innhentes ved anvendelse av en strømningsratesensor (12) i fluidkommunikasjon med strømningen.11. Fremgangsmåten ifølge et hvilket som helst av de foregående kravene, hvori parameteren omfatter en temperatur for gassen, og hvori parameteren innhentes ved anvendelse av en temperatursensor i fluidkommunikasjon med strømningen.12. Fremgangsmåten ifølge et hvilket som helst av de foregående kravene, hvori fastsettingen i trinn d omfatter fastsetting, beregning eller estimering av en hvilken som helst én eller flere av:i. mengden med gass som er igjen i kammeret (22) etter at trinn b startes; ii. den innledende mengden med gass i kammeret (22) før trinn b startes; og iii. mengden med gass som har forlatt kammeret (22) i utføringen av trinn b.13. Fremgangsmåten ifølge krav 12, hvori: mengden med gass omfatter en masse for gassen;den innledende mengden med gass omfatter en innledende masse for gassen; og mengden med gass som har forlatt kammeret (22) omfatter en masse for gassen som har forlatt kammeret (22).14. Fremgangsmåten ifølge krav 13, hvori den innledende massen med gass i kammeret (22), mi fastsettes, beregnes eller estimeres ved anvendelse av den følgende formelen:der:mi = innledende masse for gassen i kammeret (22);Pi = innledende trykk i kammeret (22);Vi = innledende gassvolum i kammeret (22);MW= molekylvekten for gassen i kammeret (22);Zi = innledende kompressibilitet for gassen i kammeret (22);R = Rankin-konstant; ogTi = innledende temperatur for gassen i kammeret (22).15. Fremgangsmåten ifølge krav 12, 13 eller 14, hvori mengden med gass som er igjen i kammeret (22) omfatter en nåværende masse med gass i kammeret (22) som fastsettes, beregnes eller estimeres ved anvendelse av den følgende formelen:der:mc = nåværende gass i kammeret (22)Pc = nåværende trykk i kammeret (22);Vc = nåværende gassvolum i kammeret (22);MW= molekylærvekt for gassen i kammeret (22);Zc = nåværende kompressibilitet for gassen i kammeret (22);R = Rankin-konstant; ogTc = nåværende temperatur i kammeret (22).16. Fremgangsmåten ifølge et hvilket som helst av de foregående kravene, hvori fremgangsmåten videre omfatter fastsetting av en mengde fluid som har trengt inn i kammeret (22) i lekkasjen i barrieren (23) for strukturen (2), fra et ytre av strukturen (2) inn i kammeret (22).17. Fremgangsmåten ifølge krav 16, hvori fastsettingen av mengden fluid som har trengt inn i kammeret (22) i lekkasjen omfatter beregning, fastsetting eller estimering av en masse for en gass som har lekket gjennom barrierdelen (23) i strukturen (2) ved anvendelse av en lineær kombinasjon av en nåværende mengde gass i kammeret (22), en innledende masse med gass i kammeret (22) og en masse for gassen som produseres av gassen som forlater kammeret (22) i strømningen.18. Fremgangsmåten ifølge krav 17, hvori massen for gassen som har lekket beregnes, fastsettes eller estimeres ved anvendelse av den følgende formelen:ml = mc - mi + mpder:ml = masse for gass som har lekket inn i kammeret (22);mc = nåværende masse for gassen i kammeret (22);mi = innledende masse for gassen i kammeret (22); ogmp = masse for gass produsert i strømningen.19. Fremgangsmåten ifølge et hvilket som helst av de foregående kravene, hvori trinnet med innhenting av parameteren eller parameterne utføres et flertall ganger.20. Fremgangsmåten ifølge krav 19, hvori et flertall beregninger utføres ved anvendelse av parameteren eller parameterne innhentet fra innhenting av parameteren eller parameterne et flertall ganger for å fastsette hvordan en lekkasjerate endres over tid.21. Fremgangsmåten ifølge et hvilket som helst av de foregående kravene, som videre omfatter:beregning av en trykkrespons for en teoretisk null-lekkasje-situasjon; anvendelse av sensoren for å fastsette minst ett trykk for gassen i strømningen fra kammeret (22);sammenligning av den beregnede responsen for den teoretiske null-lekkasjesituasjonen med den fastsatte trykkresponsen (100) innhentet ved anvendelse av en trykksensor (11); oganvendelse av sammenligningen for å fastsette en tilstand for strukturen (2).22. Fremgangsmåten ifølge krav 21 , hvori trykkresponsen for den teoretiske null-lekkasjesituasjonen beregnes ved anvendelse av den følgende formelen:der:Pzl = trykkrespons med null lekkasje gjennom barrieren (23).23. Fremgangsmåten ifølge et hvilket som helst av de foregående kravene, hvori strukturen (2) omfatter et rør (25) eller en del derav.24. Fremgangsmåten ifølge et hvilket som helst av de foregående kravene, hvori strukturen (2) danner en andel av en brønn.25. Fremgangsmåten ifølge et hvilket som helst av de foregående kravene, som videre omfatter fastsetting av en mengde med væske i kammeret (22).26. Fremgangsmåten ifølge krav 25, hvori trinnet med fastsetting av en mengde væske i kammeret (22) omfatter fastsetting av en gass-væske-kontakt i fluidet i kammeret (22).27. Fremgangsmåten ifølge et krav 25 eller 26, hvori trinnet med fastsetting av en mengde med væske i kammeret (22) omfatter anvendelse av en akustisk måleanordning (16).28. Fremgangsmåten ifølge et hvilket som helst av kravene 25–27, hvori trinnet med fastsetting av en mengde med væske i kammeret (22) utføres et fleretall ganger, inkludert før, under og etter utslipp av gass fra kammeret (22) i en strømning.29. Fremgangsmåten ifølge et hvilket som helst av kravene 25–28, hvori den fastsatte mengden med væske i kammeret (22) anvendes som en parameter i fastsetting av en mengde med væske som har trengt inn i kammeret (22) i en lekkasje i en barriere (23) for strukturen (2), fra et ytre av strukturen (2) inn i kammeret (22).30. Fremgangsmåten ifølge krav 29, hvori den fastsatte mengden med væske som har trengt inn i kammeret (22) i lekkasjen i barrieren (23) for strukturen (2) anvendes som en parameter for å fastsette en mengde med gass som har trengt inn i kammeret (22) i en lekkasje i barrieren (23) for strukturen (2), fra et ytre av strukturen inn i kammeret (22).31. Apparat (1) for utføring av fremgangsmåten ifølge et hvilket som helst av kravene 1 til 30, for testing av integriteten til en struktur (2) omfattende et kammer (22), apparatet (1) omfattende:minst én strømningsledningsseksjon for innehold av en strømning omfattende gass fra kammeret (22);minst én sensor for innhenting av minst én parameter forbundet med strømningen eller en tilstand for gass i strømningen; ogminst én determinator, omfattende en datamaskinenhet for å utføre beregninger for å fastsette om fluid har trengt inn i kammeret, konfigurert for anvendelse av den innhentede parameteren for å fastsette om fluid har trengt inn i kammeret (22), hvor fluidet trenger inn i kammeret (22) etter at gassen er sluppet ut av kammeret (22) i strømningen, hvor fastsettingen baseres på mengden med gass som har forlatt kammeret (22).32. Apparat (1) ifølge krav 31, hvori sensoren videre omfatter enten eller både:en trykksensor (11) for innhenting av minst ett trykk i strømningen; og en strømningsmåler (12) for innhenting av minst én strømningsrate for strømningen.33. Apparat (1) ifølge krav 31 eller 32, hvori determinatoren omfatter en datamaskinenhet (17).34. Apparat (1) ifølge et hvilket som helst av kravene 31 til 33, hvori sensoren er i fluidkommunikasjon med kammeret (22) og/eller strømningen fra kammeret (22).35. Apparat (1) ifølge et hvilket som helst av kravene 31 til 34, hvori apparatet (1) videre omfatter en temperatursensor for fastsetting av en temperatur og en akustisk måleanordning (16) for fastsetting av en mengde med væske i kammeret (22).36. Apparat (1) ifølge et hvilket som helst av kravene 31 til 35, videre omfattende minst én ventil (13) som kan drives for åpning og lukking av en strømningsledning for å slippe gass ut av kammeret (22) for å utføre testen av integriteten til strukturen (2).37. Datamaskinprogram for anvendelse i utføring av fremgangsmåten ifølge et hvilket som helst av kravene 1 til 30.38. Datamaskinprogrammet ifølge krav 37, hvori datamaskinprogrammet omfatter maskinlesbare instruksjoner for fastsetting av om fluid har trengt inn i kammeret (22) og/eller fastsetting av en rate for fluid som trenger inn i kammeret (22) hvori fluidet trenger inn i kammeret (22) etter at gassen er sluppet ut av kammeret (22) i strømningen, fastsettingen baseres på mengden gass som har forlatt kammeret (22).39. Datamaskinenhet (17) for anvendelse i utføring av fremgangsmåten ifølge et hvilket som helst av kravene 1 til 30, datamaskinenheten (17) omfattende minst én prosessor, prosessoren konfigurert for å kjøre datamaskinprogrammet ifølge krav 37 eller 38, for å utføre fastsettingen.40. Datamaskintilgjengelig lagringsmedium som minst deler av datamaskinprogrammet ifølge krav 37 eller 38 lagres på.
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Patent classes

IPC classesE21B 47/117G01M 3/28E21B 47/10CPC classesE21B 47/1025G01M 3/2815

Citations

Mrudhul Raj, Atkins Ltd, Aberdeen, UK, 24th Institution of Chemical Engineers Symposium on Hazards, (HAZARDS XXIV), Institution of Chemical Engineers Symposium Series 159, Edinburgh, United Kingdom, 7 - 9 May 2014. ()US 9518461 B2 (B2)US 2013111985 A1 (A1)WO 2015012702 A1 (A1)US 2016223426 A1 (A1)WO 2017203291 A1 (A1)

Applicants, owners and inventors

Owners
SCANWELL TECHNOLOGY AS
Luramyrveien 51 4313 SANDNES NO (SANDNES Municipality, Rogaland county)Org. number: 998426162Inventors
Morten Kvernvold
Lyngnesvn. 42 4018 STAVANGER NO (STAVANGER Municipality, Rogaland county)

Agent

HÅMSØ PATENTBYRÅ AS
HÅMSØ PATENTBYRÅ AS

Org. number: 918752900

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Open in The Brønnøysund Register Centre
Postboks 9 4068 STAVANGER NO (STAVANGER Municipality, Rogaland county)
Org. number: 918752900
Reference: P28332NO00

Status history

Payment history

Oppositions and appeals

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Administrative limitation

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