Patent Application
20220349809
The present invention relates to an installation for carrying out degradation and corrosion tests on samples exposed to a fluid such as a melted medium in a circulation loop line, and in particular dynamic corrosion tests on samples exposed to molten salt in the loop.
The present invention also relates to the method for achieving corrosion tests in the installation.
The present invention is applicable in technical fields where corrosion of molten salt corrosion or any other fluid at a given temperature has to be monitored within an installation, and in the particular in the field of concentrated solar power (CSP) technology.
In the molten salt solar tower power plants, and in other fields where molten salt is used, there is a need to know the degradation of the equipment which is in contact with the hot salt.
As molten salt behaviour in these technologies is still at an early stage of knowledge, most of the market actors currently base their design on literature-available data. Static corrosion tests have been performed to go deeper into salt expertise. In these static tests, the temperature of the metal used in the solar receivers is equal to the salt temperature and there is no salt circulation and further no dynamic effect (erosion and dilution).
Improving and completing corrosion understanding however will require performing dynamic corrosion tests, especially with use of alloys typically of interest in solar receiver tubes (nickel-based superalloys 230, Inconel 625, etc.).
To this end, static and dynamic corrosion tests have been developed, in which samples made of different materials such as steel, carbon, stainless steel, etc. are put into contact with salt, and in conditions as close as possible of normal operation conditions. Many studies are aiming at understanding the actual corrosion mechanism and to classify the different alloys for their suitability to be used in molten salt heat exchangers and in thermal storage applications.
Document EP 3 239 690 discloses an installation for carrying out degradation tests on specimens exposed to materials in a melted state (such as metals, alloys, salts or glass, etc.). The method disclosed therein ensures continuous stable test conditions throughout the duration of the test. The dynamic test is limited to a closed circuit established between a storage tank and a testing chamber. In order to control the degradation process developed during the test, the samples are introduced beforehand into the testing chamber. This system ensures continuous circulation of the melted medium from the testing chamber to the tank and vice versa. In the tank, the optimal temperature of the test is maintained by a temperature control system, acting on a system of electrical resistors arranged in the walls of the tank. The assembly of conduits through which the melted fluid circulates is duly heated and thermally insulated in order to minimize the loss of temperature in the fluid, in addition to preventing any phase change that could lead to mechanical problems in auxiliary systems.
In the document “A forced-circulation loop for corrosion studies: Hastelloy N compatibility with NaBF4-NaF (92-8 mole %)”, of J. W KOGER, Oak Ridge National Laboratory, ORNL-TM-4221, Dec. 1972, a molten salt forced-circulation loop is described. Standardized test facilities were developed and operated for investigating the compatibility of structural materials with flowing molten fluoride salts. In this document, a sophisticated pumped loop system is designed and operated to study the compatibility of Hastelloy N to flowing NaBF4-NaF (92-8 mole %) at a maximum temperature of 620° C. and a minimum temperature of 454° C. The design of this loop allows to remove or add corrosion test specimens without draining the fluid from the loop. Principal test variables include temperature, velocity, time, and impurities in the fluid. To simulate MSBR (molten salt breeder reactor) coolant circuit conditions, the salt is circulated in a loop piping at a velocity of about 3.05 m/s at bulk fluid temperatures from 454° C. to 620° C. Corrosion test specimens are installed at three locations in the loop circuit for exposure to the salt at three different temperatures (620° C., 537° C. and 454° C.) and at bulk flow velocities of 3.05 m/s and 6.09 m/s.
Document WO 2008/115050 A1 relates to a laboratory degradation test system for testing degradation of a test specimen in a test fluid flow, the test system comprising a reactor assembly, which reactor assembly comprises:
a reactor vessel, the reactor vessel having a reaction space, an inlet and an outlet and a specimen holder for retaining a test specimen inside the reactor vessel,
a heater for heating the reactor vessel,
a fluid circulation system generating a test fluid flow over the test specimen, which fluid circulation system comprises a circulation line which extends between the outlet of the reactor vessel and the inlet of the reactor vessel, which circulation line is arranged outside the reactor vessel, and a pump for providing fluid circulation through the circulation line and the reactor vessel, which pump is arranged in the circulation line. The laboratory test system is characterised in that the volume available to the test fluid inside the reaction space after insertion of the degradation test specimen is less than or equal to 10 ml.
Document DE 10 2012 221673 A1 discloses a sample holder for a test device intended to test environmental effects on a sample. The sample holder has at least one fluid test section which is connected to the at least one sample area bringing at least one sample into fluid contact and designed to expose the at least one sample at the least one sample area to a fluid.
Molten salt technology has been used for many years in thermal storage, industrial process heat transfer, nuclear reactors, etc. Currently, it is very challenging to improve the accuracy and performances of a molten salt test loop to know its material compatibility. It is important to obtain results which are closer to the real conditions, by performing a test when taking into account material behavior in molten salt.
In an embodiment, the present invention provides a dynamic corrosion and degradation testing installation comprising: a tank for heating and storing, in use, a fluid at a given temperature; a looped circuit comprising a pipe containing the fluid during one or more tests, having a first end and a second end both connected to the tank; a pump for circulating the fluid in the pipe; and a plurality of test stands located at different locations along the pipe, each test stand of the plurality of test stands comprising a sample holder or testing chamber holding, in use, a solid sample in contact with the fluid and a heater, configured to heat the sample holder, wherein each test stand of the plurality of test stands comprises the sample holder to hold, in use, the solid sample in a specific portion of the pipe, the specific portions of the pipe having the functionality of a test chamber in addition to that of containing the fluid, a heating unit comprising an inductor coil wrapped around the portion of the pipe and configured to provide, in use, a steady energy flow and to ensure a gradient of temperature between the fluid and the solid sample to be tested.
Subject matter of the present disclosure will be described in even greater detail below based on the exemplary figures. All features described and/or illustrated herein can be used alone or combined in different combinations. The features and advantages of various embodiments will become apparent by reading the following detailed description with reference to the attached drawings, which illustrate the following:
The present invention provides a high performance test installation that enables carrying out corrosion dynamic tests on sample parts in contact with a fluid.
In some embodiments, the present invention obtains representative corrosion and degradation tests to accurately determine the behaviour of actual solar receivers.
The present invention further provides a dynamic corrosion test loop exposing samples to conditions as close as possible to real use conditions, for example in terms of temperature differences, flow rate, flow type, etc.
In some embodiments, the present invention obtains a dynamic corrosion test loop presenting high flexibility in terms of thermal gradient between the circulating the molten salt and the test tube specimens, as well as improved accuracy thanks to fast and precise reaching of desired temperature.
A first aspect of the present invention relates to a dynamic corrosion and degradation testing installation, comprising:
a tank for heating and storing, in use, a fluid at a given temperature;
a looped circuit comprising a pipe containing the fluid during the tests, having a first end and a second end both connected to the tank;
a pump for circulating the fluid in the pipe;
a plurality of test stands located at different locations along the pipe, each test stand comprising a sample holder or testing chamber holding, in use, at least one solid sample in contact with the fluid and a heater intended to heat said sample holder;
characterized in that each test stand comprises a portion of the pipe made of the solid sample to be tested, preferably a metal sample, having the function of a testing chamber, said solid sample being in tubular form with fluid flowing therein, the heater being under the form of an inductor wrapped around said portion of pipe and intended to provide, in use, a steady energy flow and ensure a gradient of temperature between the fluid and the sample to be tested.
The present invention also provides a shipping container comprising the aforementioned installation.
According to preferred embodiments of the invention, the installation further includes one of the following features or by a suitable combination thereof:
the portion of the pipe made of the solid sample to be tested is inserted in the looped circuit pipe thanks to welded connections at both ends or to connections using flanges;
the welded connections are full penetration butt welds out of chamfered tube ends; the flanges are non-conducting flanges;
the installation comprises an electrical resistor provided around or within the tank to heat the fluid;
the pipe is tilted from the horizontal, preferably at about 4° from the horizontal;
the heated sample holders and the corresponding inductors are in the number of one or more;
the tank comprises an external insulation and draining means;
the installation also comprises a cooling device to avoid the overheating of the fluid;
the cooling device comprises a heat exchanger.
Another aspect of the present invention relates to a method for carrying out dynamic corrosion and degradation tests on samples being in contact with a fluid, by means of the aforementioned installation, comprising at least the following steps of:
putting metal samples on each of the test stands within the pipe;
heating the fluid contained in the tank;
circulating the fluid in the pipe according to the looped circuit by activating the pump;
cooling the pipe in the cooler by circulating therein a cooling fluid;
heating the samples in the test stands using the corresponding inductors to provide at each heated test stand a steady heat flow and to create a temperature gradient between the fluid and the sample;
after having stopped the heating of the fluid and having drained the fluid out of the installation, opening the test stands, removing the samples therefrom, and performing degradation tests on the samples.
According to preferred embodiments of the invention, the method further comprises one of the following features or by a suitable combination thereof:
the samples are heated in the test stands by the corresponding inductors so that the steady heat flow is comprised between 1 and 3 MW/m2 and the temperature gradient between the fluid and the respective samples is up to 150° C.;
the degradation tests are weight loss measurement after descaling and micrographic cross-section examination;
the fluid is circulated at a velocity comprised between 2 and 8 m/s and preferably at a velocity of about 4 m/s;
the minimal temperature of the sample holders is comprised between 100° C. and 290° C. and the maximal temperature of the sample holders is comprised between 380° C. and 800° C.;
the heating is operated in order to have, with sample holders at least in number of five, an unheated sample holder and four sample holders respectively heated at 600° C., 625° C., 650° C. and 700° C.;
the fluid is heated in the tank from 100° C. to 700° C.;
the pump is run from 7 to 15 m3/s;
the fluid is a molten salt or thermal oil.
The present invention relates to an installation 1 to carry out dynamic corrosion and/or degradation tests on samples, preferably metal samples 4 being in contact with a fluid circulating in a pipe 3.
To this end, and as illustrated by
According to the invention, the installation comprises several test points that will be called hereinafter “test stands”, located at different locations along the pipe 3. As illustrated by
According to a preferred embodiment, the metal samples 4 are made of tubular portions of the metal to be tested that are inserted with butt welding connections in the pipe 3. Still preferably the welding connections are full penetration butt welds out of chamfered tube ends. For example, in the test pipe area, sections of specific stainless steel to be tested (e.g. SB 626 NO6230) may alternate with sections made of ordinary stainless steel (such as AISI 304 for example).
According to another embodiment, the sections to be tested can be connected with other pipe sections using flanges, preferably non-conducting flanges. This solution has the advantage that the heat created locally does not propagate toward the whole pipe and further to the fluid. Alternately, the sample holder can comprise a series of pipe sections to be tested separated by non-conducting flanges. This solution could however suffer from sealing problems at high temperature.
The fluid, for example a molten medium, circulating in the pipe 3 of the loop has a temperature that is essentially constant, and is heated by heating means such as an electrical resistor provided around or within heating tank 2. Typically 50-100 L molten salt circulate in the installation.
In this way, the installation of the present invention allows to provide a gradient of temperature between the circulating fluid and each sample holder, in order to simulate real conditions. This coupling between inductor 6 and sample holder 5B allows a high flexibility in terms of thermal gradient between the molten salt and the test tube samples 4, as well as improved accuracy thanks to fast and precise reaching of desired temperature specifically obtained by induction heating. As a result, this test configuration allows a better understanding of the behaviour of a fluid that is in contact with a metal of higher temperature.
A temperature difference up to 150° C. between the fluid (molten salt) circulating in the pipe 3 and metal samples 4 can be obtained using an external induction heating. The critical element of the installation is to maintain this temperature difference between metal sample and fluid. Circulating fluid will permanently absorb a certain energy quantity from the hotter metal, with the consequence that the metal temperature will decrease, unless the latter is subject to a steady energy flow. This energy flow should be of the same order of magnitude as in real conditions, e.g. from 1 to 3 MW/m2 in the solar energy domain.
For example, in the CSP molten salt solar tower technology, the heat transfer fluid is a molten salt typically entering at 290° C. in the solar receiver and coming out thereof at about 565° C. The surface temperature of the solar receiver panels is comprised between 500° C. and more than 600° C. or even 700° C., according to their position relative to the sun direction. The elements of the solar receiver brought into contact with the molten salt are at different temperatures depending on their location. It is therefore important to consider these temperature differences during corrosion tests. To simulate molten salt solar circuit conditions, samples 4 are installed at different locations in the loop circuit, in test stands, in which the pipe 3 acts as a test tube and is at a different temperature from the other test stands. The dynamic test loop of the present invention allows to modulate different temperature gradients between the molten medium and the test tubes (stands) so that to be close to real conditions.
According to a preferred embodiment of the present invention, the minimal temperature of the sample holder 5 will be in the range between 100 and 290° C. and the maximal temperature will be in the range between 380 and 800° C., according to the specific fluid used (water, thermal oil or molten salt). These temperatures are obtained very quickly thanks to each inductor 6 heating each portion of the pipe 3 comprising a sample-holder 5.
A pump 8 is provided in order to circulate the fluid in the pipe 3, as illustrated by
The fluid used in the invention can be a molten salt such as a binary or ternary alkali nitrate molten salt (e.g. KNO3/NaNO3; KNO3/NaNO2/NaNO3), or a carbonate salt, or thermal oil.
In a preferred embodiment of the present invention, the installation comprises an unheated test stand with an unheated sample holder 5A and four heated test stands, where the four heated sample holders 5B are heated respectively for example at 600° C., 625° C., 650° C. and 675° C. These temperatures suitably simulate the level of temperature of the solar receiver panel surface according to its respective positions relative to the sun.
The tank 2 comprises an external insulation 21 at its external surface to keep the molten salt at the desired temperature (
Advantageously, the present installation 1 can be provided in the form of a shipping container. In this way, the installation is easily transportable and can be located close to the installation to be analyzed, such as at the base of a solar tower for example.
In use, samples 4 are place on different sample holders 5. Each sample holder 5 is quickly, separately and independently heated at the desired temperature, by its assigned inductor 6, while the fluid located in the tank 2 is heated by an electric resistor. Once the fluid has reached the desired temperature in tank 2, pump 8 circulates the fluid in the different test stands located on the pipe 3. The samples 4, which are hold at an accurate temperature, are then in contact with the fluid which is at another temperature. The turbulent flow of the fluid circulating in the pipe 3, in contact with the samples 4, allows to obtain test conditions as close as possible to the real conditions.
After having been in contact with the fluid and removed from the pipe 3, the samples 4 are analyzed, for example by mass loss analysis, to determine the degradation and corrosion rate of the samples in contact with the fluid. Advantageously the present installation 1 permits to cycle the tests.
While subject matter of the present disclosure has been illustrated and described in detail in the drawings and foregoing description, such illustration and description are to be considered illustrative or exemplary and not restrictive. Any statement made herein characterizing the invention is also to be considered illustrative or exemplary and not restrictive as the invention is defined by the claims. It will be understood that changes and modifications may be made, by those of ordinary skill in the art, within the scope of the following claims, which may include any combination of features from different embodiments described above.
The terms used in the claims should be construed to have the broadest reasonable interpretation consistent with the foregoing description. For example, the use of the article “a” or “the” in introducing an element should not be interpreted as being exclusive of a plurality of elements. Likewise, the recitation of “or” should be interpreted as being inclusive, such that the recitation of “A or B” is not exclusive of “A and B,” unless it is clear from the context or the foregoing description that only one of A and B is intended. Further, the recitation of “at least one of A, B and C” should be interpreted as one or more of a group of elements consisting of A, B and C, and should not be interpreted as requiring at least one of each of the listed elements A, B and C, regardless of whether A, B and C are related as categories or otherwise. Moreover, the recitation of “A, B and/or C” or “at least one of A, B or C” should be interpreted as including any singular entity from the listed elements, e.g., A, any subset from the listed elements, e.g., A and B, or the entire list of elements A, B and C.
1 Installation for carrying out dynamic corrosion and degradation tests
2 Hot pot of fluid
3 Pipe (similar to test tube)
4 Sample
5A Unheated sample holder
5B Heated sample holder
6 Inductor for heating a heated sample holder
7 Power system/supply
8 Pump for circulating the fluid
9 Heat exchanger (cooling device)
10 DCS (digital control system)
11 Air supply
12 Drain tank
13 Fluid
14 Heating unit
15 Pressure sensor
16 Flow sensor
17 Temperature sensor
18 Pyrometer
19 Air blower
21 Tank insulation
22 Chamfer
| Number | Date | Country | Kind |
|---|---|---|---|
| 19184129.5 | Jul 2019 | EP | regional |
This application is a U.S. National Phase application under 35 U.S.C. § 371 of International Application No. PCT/EP2020/067786, filed on Jun. 25, 2020, and claims benefit to European Patent Application No. EP 19184129.5, filed on Jul. 3, 2019. The International Application was published in English on Jan. 7, 2021 as WO 2021/001249 A1 under PCT Article 21(2).
| Filing Document | Filing Date | Country | Kind |
|---|---|---|---|
| PCT/EP2020/067786 | 6/25/2020 | WO |
