Patent Application
20200249137
This application claims priority to European Patent Application No. 19275016.4 filed Feb. 1, 2019, the entire contents of which is incorporated herein by reference.
The present disclosure relates to methods for structural testing of pressure vessels and the use of new test fluids in such methods.
During the course of manufacture and during their working life, pressure vessels such as fire extinguishers need to be tested to ensure they will not burst or yield at a pressure higher than their normal service pressure. Such testing methods include pneumatic testing and hydrostatic testing. Pneumatic testing can be conducted at the maximum pressure and maximum operating temperature, e.g. for leak-checking seal welds on a weldment assembly. Pneumatic testing is more hazardous than testing hydraulically, due to the compressibility of the fluids used and the stored energy contained.
Hydrostatic pressure testing (often referred to as proof testing) involves filling the vessel to be tested with a test fluid, applying pressure to the filled vessel and examining the vessel walls, joints and seals for leaks or deformation. The level of over pressurization depends on the National or International pressure regulations that the pressure vessel is being tested to, but is frequently 1.5 or 2 times the normal service pressure.
It is common practice to use water as the test fluid in hydrostatic testing in order to minimise the stored energy hazard during the test. After the pressure vessel has been filled with water and pressure tested, the water is then removed by heat or vacuum or both, which can be expensive and time consuming. Furthermore, this can present problems if any water is not completely removed prior to the tested vessel being returned to its intended purpose. For example, residual water may be present in fire extinguishers after pressure testing. When the fire suppression agent is supplied to the extinguisher, this may react with the residual water. For agents such as Halon 1301 (CF3Br) or Halon 1211 (CF2BrCl), residual water can hydrolyse the CF3Br giving rise to acids such as HF and HBr (and HCl in the case of Halon 1211). These acids can, over time, corrode the fire extinguisher, causing leakage. In extreme cases, such corrosion could lead to catastrophic failure of the pressure vessel.
The problem of residual test fluids can be exacerbated in pressure switches and other components having complex internal geometry, e.g. by water entering crevices etc. In the case of vessels intended to contain dry chemical agents such as sodium bicarbonate, these agents may no longer flow properly due to being wet and/or dissolved by the residual water, which can lead to impaired performance of the pressure vessel.
The present disclosure provides an alternative to pneumatic testing or proof testing with water by using certain halogenated compounds in pressure testing of pressure vessels. The halogenated compounds are selected from the group consisting of tropodegradable halogenated compounds, fluorinated compounds, halogenated ketones, halogenated alkenes and halogenated ethers.
According to a first aspect, the present disclosure provides a method for pressure-testing a pressure vessel, said method comprising using a test fluid which is, or comprises, a halogenated compound selected from the group consisting of tropodegradable halogenated compounds, fluorinated compounds, halogenated ketones, halogenated alkenes and halogenated ethers.
A further aspect provides use of a test fluid in a method of pressure-testing of a pressure vessel, wherein the test fluid is, or comprises, a halogenated compound as herein described.
According to a further aspect, the present disclosure provides use of a halogenated compound as herein described in a method of pressure-testing of a pressure vessel. A further aspect provides a method for pressure-testing a pressure vessel, said method comprising using a halogenated compound as herein described.
In aspects of the disclosure, the method described herein may comprise introducing the test fluid to the pressure vessel.
The method may comprise applying pressure to the vessel containing the test fluid until a desired test pressure is reached.
The test fluid is, or comprises, a halogenated compound. The halogenated compound of the present disclosure is a tropodegradable halogenated compound and/or it is a halogenated compound selected from the group consisting of:
The halogenated compound comprises carbon, one or more halogen atoms and, optionally, hydrogen and/or oxygen. Other elements may also be present. The halogenated compound may be saturated or unsaturated. In certain aspects, the halogenated compound is unsaturated, e.g. it may contain a C═C or C═O bond.
In certain aspects of the disclosure, 50 to 100 vol. %, 70 to 100 vol. %, 85 to 100 vol. %, 95 to 100 vol. %, 98 to 100 vol. %, or 99 to 100 vol. % of the test fluid is a halogenated compound as herein described or a mixture of halogenated compounds as herein described. Additional optional components of the test fluid include coloured dyes (e.g. red or fluorescent) which may be added to the test fluid to make leaks easier to detect. Such materials are typically used in relatively small amounts, e.g. amounting to 0.1 to 5, e.g. 0.5 to 3, e.g. 1 to 3 vol. % of the test fluid.
In some aspects of the present disclosure, the test fluid consists of, or consists essentially of, a halogenated compound as herein described or a mixture of halogenated compounds as herein described.
The halogenated compound as herein described may be a chlorofluoro compound.
According to one aspect of the present disclosure, the halogenated compound is a fluorinated compound, i.e. a compound comprising fluorine, although other halogens, such as chlorine, may also be present. Examples of fluorinated compounds include refrigerants, solvents and foam blowing agents.
The term “fluorinated” should be understood to require the presence of fluorine but does not necessarily exclude the presence of other halogens. For example, unless otherwise specified, fluorinated compounds as described herein may contain both fluorine and chlorine.
The halogenated compound of the present disclosure may be a fluorinated compound selected from the group consisting of fluorinated ketones, fluorinated ethers (i.e. (hydro)fluoroethers/HFEs), fluorinated alkanes, fluorinated alkenes (e.g. (hydro)fluoro olefins/HFOs or (hydro)chlorofluoro olefins/HCFOs), fluorinated aromatic compounds and perfluorinated compounds. The term “(hydro)” is intended to denote that hydrogen atoms are optional.
In the partially fluorinated compounds described herein, provided at least one fluorine is present, the halogens may be independently selected from F, Cl, Br and I, e.g. independently selected from F and Cl. The fluorinated compounds described herein may be (chloro)fluoro compounds, where the term “(chloro)” is intended to denote that chlorine atoms are optional.
Examples of fluorinated ketones include compounds of formula R1C(═O)R2, where:
Each n may be independently selected from 1 to 10, e.g. 1 to 6, or 2 to 4, e.g. 2 or 3.
Each x may be 2n+1, e.g. the fluorinated ketone contains no hydrogen atoms.
Each Hal may be independently selected from F and Cl, e.g. Hal may be F.
Examples of fluorinated ethers include compounds of formula R1—O—R2,
R1 and R2 may both be C(n)H(2n+1−x)Hal(x).
R2 may be —CH3 or —C2H5.
Each n may be independently selected from 1 to 10, e.g. 1 to 7, 2 to 7, 1 to 6, 2 to 6, or 2 to 4, e.g. 2 or 3.
Each x may be 2n+1, e.g. the fluorinated ether contains no hydrogen atoms.
Each Hal may be independently selected from F and Cl, e.g. Hal may be F.
Examples of fluorinated ethers (e.g. (hydro)fluoro ethers/HFEs) include:
Examples of chlorinated fluorinated ethers include CF3CHClCHF2 and CHClFCF2OCHF2.
The fluorinated compound may be a fluorinated alkene. Examples of fluorinated alkenes include perfluorinated alkenes and partially fluorinated alkenes (including chlorofluoro alkenes), e.g. (hydro)fluoro olefins/HFOs or (hydro)chlorofluoro olefins/HCFOs. Those that are partially fluorinated may contain hydrogens and/or other halogens. The halogens may be independently selected from F, Cl, Br and I, e.g. independently selected from F and Cl.
The fluorinated alkene may be a perfluorinated or partially fluorinated propene, butene or pentene, e.g. a perfluorinated or partially fluorinated propene or butene. Provided at least one fluorine is present, the halogens in a fluorinated alkene may be independently selected from F, Cl, Br and I, e.g. independently selected from F and Cl. The fluorinated alkene compound may be a chlorofluoro alkene.
Examples of (hydro)fluoro olefins/HFOs include partially fluorinated alkenes such as CF3CH═CHF, CF3CF═CH2 and CF3CH═CHCF3. Examples of (hydro)chlorofluoro olefins/HCFOs include CF3CH═CHC1, CF3CCl═CH2 and CF3—CF═CHCl.
Examples of fluorinated alkanes include (hydro)fluoroalkanes and (hydro)chlorofluoroalkanes.
Examples of fluorinated aromatic compounds include those containing C═C, C═O or C—O bonds.
Examples of perfluorinated compounds include perfluorinated alkenes and ketones.
In certain aspects of the present disclosure, the halogenated compound is a fluorinated compound selected from the group consisting of fluorinated ketones, fluorinated ethers (e.g. HFEs) and fluorinated alkenes (e.g. (hydro)fluoro olefins/HFCOs) or (hydro)fluorochloro olefins/HFCOs), e.g. selected from the group consisting of (chloro)fluoroketones, (chloro)fluoroethers and (chloro)fluoroalkenes.
In certain aspects, the halogenated compound is a halogenated ketone. Examples of halogenated ketones are aromatic ketones, fluorinated ketones (including (hydro)chlorofluoroketones) and perhaloketones, e.g. perfluoroketones.
The halogenated ketone may be a chlorofluoro ketone.
Examples of halogenated ketones include compounds of formula R1C(═O)R2, where:
R1 and R2 may both be C(n)H(2n+1−x)Hal(x).
Each n may be independently selected from 1 to 10, e.g. 1 to 6, or 2 to 4, e.g. 2 or 3.
Each x may be 2n+1, e.g. the halogenated ketone contains no hydrogen atoms.
Each Hal may be independently selected from F and Cl, e.g. Hal may be F.
Examples of halogenated ketones include the fluorinated ketones discussed herein.
The halogenated compound may be a halogenated alkene. Examples of halogenated alkenes are those containing aromatic groups, partially halogenated alkenes, perhalogenated alkenes and fully- and partially-fluorinated alkenes (including chlorofluoro alkenes). The halogens may be independently selected from F, Cl, Br and I, e.g. independently selected from F and Cl.
The halogenated alkene may be a perhalogenated or partially halogenated propene, butene or pentene, e.g. a perhalogenated or partially halogenated propene or butene. The halogens may be independently selected from F, Cl, Br and I, e.g. independently selected from F and Cl. The halogenated alkene compound may be a chlorofluoro alkene.
The fluorinated alkene may be a perfluorinated or partially fluorinated propene, butene or pentene, e.g. a perfluorinated or partially fluorinated propene or butene. Provided at least one fluorine is present, the halogens in a fluorinated alkene may be independently selected from F, Cl, Br and I, e.g. independently selected from F and Cl. The fluorinated alkene compound may be a chlorofluoro alkene.
Examples of fluorinated alkenes include (hydro)fluoro olefins/HFOs and (hydro)chlorofluoro olefins/HCFOs. Those that are partially fluorinated may contain hydrogens and/or other halogens. Examples of (hydro)fluoro olefins/HFOs include partially fluorinated alkenes such as CF3CH═CHF, CF3CF═CH2 and CF3CH═CHCF3. Examples of (hydro)chlorofluoro olefins/HCFOs include CF3CH═CHCl, CF3CCl═CH2 and CF3—CF═CHCl.
The halogenated compound may be a halogenated ether, e.g. a fluorinated ether (such as a chlorofluoro ether), a perhalogenated ether or an ether containing one or more aromatic groups.
Examples of halogenated ethers include compounds of formula R1—O—R2, where:
R1 and R2 may both be C(n)H(2n+1−x)Hal(x).
R2 may be —CH3 or —C2H5.
Each n may be independently selected from 1 to 10, e.g. 1 to 7, 2 to 7, 1 to 6, 2 to 6, or 2 to 4, e.g. 2 or 3.
Each x may be 2n+1, e.g. the halogenated ether contains no hydrogen atoms.
Each Hal may be independently selected from F and Cl, e.g. Hal may be F.
Examples of halogenated ethers are fluorinated ethers (including (hydro)chlorofluoro ethers) as discussed above.
In some aspects of this disclosure, the halogenated compound may be a halogenated aromatic compound, e.g. one containing a ketone (C═O), alkene (C═C) or ether (C—O) linkage. Examples of such halogenated aromatic compounds are tropodegradable halogenated aromatic compounds, fluorinated aromatics, (hydro)chlorofluoro aromatics and perhalogenated aromatics.
In some aspects of this disclosure, the halogenated compound may be a perhalogenated compound, e.g. a perfluorinated compound, a perhalogenated alkene, a perhalogenated ketone or a perhalogenated aromatic. In certain aspects, the perhalogenated compound is tropodegradable.
The halogenated compound according to the present disclosure is ideally environmentally friendly, e.g. tropodegradable, so it has a very short atmospheric lifetime and does not reach the stratosphere.
In certain aspects, the halogenated compound is tropodegradable, e.g. it degrades in the troposphere such that it does not enter the stratosphere.
The halogenated compound may have an atmospheric lifetime of 10 years or less, e.g. 8 years or less, 6 years or less, 4 years or less or 2 years or less.
The halogenated compound may have an ozone depletion potential of less than 1, e.g. 0 to 0.5, e.g. less than 0.2, e.g. 0.
The halogenated compound may have a low global warming potential (GWP), e.g. 750 or lower, 500 or lower, or 150 or lower (relative to CO2). GWP is expressed in terms of the 100 year integrated time horizon (ITH).
The test fluid (e.g. the halogenated compound as herein described) may be liquid at room temperature, yet volatile enough to evaporate to facilitate removal of the residue once the pressure testing is complete.
The halogenated compound as herein described may have a boiling point in the range of 30 to 200° C., 40 to 150° C. or 40 to 100° C., e.g. 45 to 75 or 60 to 150° C. Boiling points referred to herein are at atmospheric pressure (101.325 kPa) unless otherwise stated.
In certain aspects of the present disclosure, the halogenated compound does not contain bromine. In certain aspects, the halogenated compound does not contain chlorine. In certain aspects, the halogenated compound does not contain iodine.
The halogenated compound may be fluorinated. In certain aspects, the only halogen atoms in the halogenated compound are fluorine atoms and/or chlorine atoms. In certain aspects, the only halogen atoms in the halogenated compound are fluorine atoms.
The halogenated compound may be a perhalogenated compound. In certain aspects, the halogenated compound is only partially halogenated, e.g. less than 100%, e.g. 10 to 90%, 20 to 70% or 30 to 50% of the hydrogen atoms of the parent compound have been replaced with halogen atoms.
The halogenated compound may contain greater than 50 wt. % halogen (in relation to the total weight of halogens as a percentage of the weight of compound as a whole), e.g. 60 to 80 wt. %, 65 to 75 wt. % or greater than 70% wt. % halogen.
In some aspects, halogenated ketones, alkenes, ethers and aromatic compounds may require higher amounts of halogen than saturated halogenated compounds. For example, these may contain greater than 65 wt. % halogen (in relation to the total weight of halogens as a percentage of the weight of compound as a whole), e.g. 70 to 80 wt. %, 65 to 75 wt. % or greater than 70% wt. % halogen.
In certain aspects, the halogenated compound or the test fluid is, or comprises, one or more of the following fluorinated ketones:
In certain aspects, the halogenated compound or the test fluid is, or comprises one or more of the following fluorinated ketones:
In certain aspects, the test fluid is or comprises a halogenated ketone or a mixture of halogenated ketones as herein described. In some aspects, 50 to 100 vol. %, 70 to 100 vol. %, 85 to 100 vol. %, 95 to 100 vol. %, 98 to 100 vol. %, or 99 to 100 vol. % of the test fluid is a halogenated ketone or a mixture of halogenated ketones. In certain aspects, the test fluid consists essentially of a halogenated ketone or a mixture of halogenated ketones.
By halogenated ketone is meant a ketone comprising at least one halogen atom (e.g. F, Cl, Br, I), with hydrogen atoms being optional. In some aspects, the test fluid comprises, or consists essentially of, a perhalogenated ketone or a mixture of perhalogenated ketones. The halogenated ketones described herein may be fluorinated ketones, for example perfluorinated ketones.
Conveniently, the halogenated compound may be miscible with, and/or inert towards, the material which the pressure vessel contains during its standard operation. For example, the halogenated compound may be miscible with, and/or inert towards, fire extinguishing agents such as Halon 1301 (CF3Br). The miscibility/inertness means that any residual compound remaining after pressure testing does not adversely affect the operation of the pressure vessel.
Test fluids of the present disclosure combine the “clean” attributes of pneumatic testing and the relative safety of hydrostatic testing. Compared with hydrostatic testing with water, using these fluids saves time and money by allowing lower temperature ovens to remove residual agent. Depending on the temperature of the ovens used to remove water presently this may also give a benefit in terms of health and safety. Also, the test fluid may be selected to be compatible with the material intended to be used in the pressure vessel, such that if any of the test fluid does remain in the vessel, it does not cause problems such as the corrosion found in fire extinguishers when residual water reacts with Halon. This compatibility means that removal of the test fluid can be less stringent, leading to added convenience.
Examples of suitable compounds are fluorinated ketones, such as those known as FK-5-1-12 (C6F12O) and FK-6-1-14 (C7F14O). These types of materials have low toxicity and low environmental impact (e.g. zero ozone depletion potential (ODP) and a global warming potential (GWP) of <1). In contrast to water, they will not cause hydrolysis of Halon 1301. They are more volatile, have a lower latent heat of vaporization and a lower surface tension than water, making it much easier to remove the test fluid from the pressure vessel after testing.
The method of the present disclosure is one for pressure testing pressure vessels, e.g. for hydrostatically testing the internal pressure strength of a vessel. The test fluids of the present disclosure may be applied to known pressure testing techniques for a variety of pressure vessels.
In aspects of the disclosure, the method described herein comprises:
Pressure vessels include any vessel required to contain material under pressure or to be used under pressure. Examples are fluid containment vessels (e.g. storage tanks, fuel tanks, gas cylinders, boilers, pipelines and heat exchangers), inflation systems (e.g. emergency helium inflation systems for aircraft), fire extinguishers, or other fire suppression devices. Examples of fire extinguishers and fire suppression devices are aviation fire extinguishers, industrial fire suppression devices (e.g. suitable for computer rooms or data storage centres) and military fire suppression devices (e.g. suitable for use in vehicles, e.g. in the engine compartment or the crew compartment).
The test fluids of the present disclosure may be conveniently be applied to pressure testing of any pressure vessels, for example fire extinguishers, e.g. those containing vaporising liquid agents, such as Halon and Halon replacements.
Typically, the pressure testing method is carried out on an empty vessel. If the pressure test is being carried out as part of the manufacturing process, then the pressure vessel is likely to be empty. However, for periodic safety checks, e.g. those required to be carried out on vessels such as fire extinguishers, the material usually contained in the vessel should normally be removed prior to the pressure test taking place. If necessary, the vessel may therefore be emptied of its usual contents prior to the pressure test taking place.
The test fluid according to the present disclosure is introduced into the pressure vessel prior to the pressure vessel being pressurized. Typical means for supplying the pressure vessel with test fluid include pumping, flowing and/or injecting the fluid into the vessel.
In certain aspects, the test fluid is introduced such that it fills 80-100 vol. %, e.g. 85-100, 90-100, 95-100, 98-100, 99.5-100 vol. % of the internal volume of the pressure vessel. The internal volume is the containment volume (i.e. the volume which stores material during the usual operation of the vessel), typically defined by internal walls of the vessel and is dependent on the type of vessel and its intended use. Increased safety benefits are realized when the pressure vessel is completely filled with test fluid. In certain aspects, the pressure vessel is filled, or substantially filled, with test fluid prior to pressurizing the vessel.
Pressure tests involve pressurizing the pressure vessel subsequent to the test fluid being introduced. The level of over pressurization depends on the National or International pressure regulations that the pressure vessel is being tested to, but is frequently 1.5 or 2 times the normal service (operating) pressure.
Examples of pressure vessels and their service pressures are set out in the following table:
The test pressure applied to the pressure vessel during the method of the present disclosure is typically 100-1000%, e.g. 100-500%, e.g. 125-200 or 150-200% of the operating pressure of the pressure vessel. Typical test pressures for fire extinguishers are therefore 3.5-8.5 MPa.
Suitable pressurizing gases include nitrogen, argon and air. Pressurizing the vessel may be carried out by any standard means, e.g. by applying pressure with nitrogen or argon or by applying pressure using air, for example with a hydraulic pump. The vessel pressure may be monitored, e.g. with a pressure gauge or transducer.
The smaller the headspace in the vessel after the test fluid has been added, the lower the amount of pressure needs to be applied to reach the desired test pressure. Supplying as much test fluid as possible to the vessel therefore improves safety by lowering the amount of stored energy present in the vessel (stored energy is the pressure multiplied by the volume of the headspace)
Pressure is applied until the test pressure is reached, e.g. an equilibrium test pressure is reached. In situations where the pressurizing gas is one that is soluble in the test fluid (e.g. nitrogen is soluble in halogenated compounds such as fluorinated ketones) this solubility may need to be taken into account when pressurizing the vessel. For example, pressurizing with a gas that is soluble in the test fluid is likely to take longer than pressurizing with a gas that is not soluble in the test fluid. Having reached a certain pressure, the pressure may then fall if the gas (e.g. nitrogen) is forced into solution. In this case, it may be necessary to “top up” the pressure one or more times to ensure equilibrium (e.g. a constant test pressure) is reached. Monitoring the pressure during the pressurization step can assist in identifying if further pressurization is required.
Pressure tightness can be tested by shutting off the supply valve and observing whether there is a pressure loss. The test pressure is typically held for a time (e.g. 1 to 10 minutes) before or during which any necessary checks are carried out. For example, known weak points such as “weldments”, e.g. as ports for filling, pressure measuring and discharging may be examined for attachment and leaks.
Coloured dyes (e.g. red or fluorescent) may be added to the test fluid (e.g. prior to the test fluid entering the pressure vessel) to make leaks easier to see. Such materials are typically used in relatively small amounts, e.g. amounting to 0.1 to 5, e.g. 0.5 to 3, e.g. 1 to 3 vol. % of the test fluid. Distortion of the vessel may also be measured, e.g. by measuring the volumetric expansion. The degree of volumetric expansion that may be tolerated will typically be set by safety standards.
After the necessary checks have been made, the pressure applied is released. As the volume of pressurizing gas used is very small, venting can typically be accomplished over a period of 2 to 20 s, e.g. 5-10 s. Typical venting rates are 0.5-20, e.g. 1-10 MPa/s.
When the pressurizing gas is one that is soluble in the test fluid, it may be necessary to release the pressure more slowly in order to avoid excess frothing as the pressuring gas comes out of solution. In some cases, agitating the vessel may assist.
The test fluid may be recovered (e.g. to be reused or recycled) from the pressure vessel, e.g. by pumping, applying vacuum to said pressure vessel and/or heating the vessel. Further pumping, vacuum and/or heating may be used to remove residual test fluid.
An embodiment of the disclosure will now be described, by way of example only.
The pressure vessel to be tested may be checked prior to the test, e.g. to ensure that all ports, other than that through which the test fluid is to be introduced, are closed, for example by welding shut.
Test fluid as herein described, e.g. CF3CF2C(═O)CF(CF3)2, is introduced to the vessel through any convenient inlet, such as a pressure switch port. Ensuring that the vessel is as full as conveniently possible (i.e. that the test fluid takes up as much of the internal volume as possible) increases safety by minimizing the amount of stored energy within the vessel.
Pressure is then applied to the vessel, for example by introducing nitrogen. To maximize operator safety, the test, particularly the pressurization stage, can be carried out in a safety enclosure which as a hydro test booth. The pressure in the vessel may be monitored via a pressure gauge or a transducer.
The pressure is held at test pressure, e.g. two times the normal service pressure of the vessel, while the necessary checks are carried out. Volumetric expansion may be measured and vessel walls, joints or seals may be checked for leaks. When the required checks have been finished, the vessel is vented to release the pressure. The test fluid is removed, e.g. by pumping, and may be stored for future use. Additional vacuum may be applied in order to remove the last traces of test fluid.
Test fluids which are more volatile than water require less time and energy to remove, e.g. allowing lower temperature ovens to remove residual fluid. Using test fluids which are compatible with the material intended to be used in the pressure vessel means that removal of the test fluid can be less stringent, leading to added convenience. For example, using a test fluid that is inert towards Halon 1301 to test a Halon 1301 fire extinguisher means that any residual test fluid does not cause any problems for future use of the fire extinguisher.
The above description is of an exemplary embodiment of the disclosure only. It will be readily appreciated by the skilled person that the various optional and exemplary features of the disclosure as described above may be applicable to all the various aspects of the disclosure discussed herein.
The disclosure will now be further described by way of the following non-limiting example.
1. Select the pressure vessel to be tested. Ensure burst discs are installed. Pressure switch/TCPT should be removed. Fill plug and gasket should be removed. All other ports should be welded closed.
2. Seal pressure switch port.
3. Fill container completely with CF3CF2C(═O)CF(CF3)2 through the pressure switch port.
4. Install pressure switch port plug with pressure transducer attached.
5. Install fill port adapter to allow pressurization with nitrogen.
6. Place the vessel in a fixture located inside hydro test booth.
7. Set up the pressure transducer to monitor cylinder pressure.
8. Increase cylinder pressure to 6.2 MPa test pressure (e.g. for a fire extinguisher) by applying nitrogen pressure and hold for 1 minute.
9. Record volumetric expansion.
10. Record the maximum pressure obtained within the cylinder via the pressure transducer.
11. Vent pressure slowly from the test vessel.
12. Recycle/recover liquid CF3CF2C(═O)CF(CF3)2 via Haskell pump.
13. Connect a vacuum pump to the fill valve and pull a vacuum of at least 20″ mercury (˜10 psi, 67728 Pa) on the cylinder. Hold this vacuum for 5 minutes.
14. Remove the vacuum pump and pressure switch plug.
It will be understood that the description above relates to a non-limiting example and that various changes and modifications may be made from the arrangement shown without departing from the scope of this disclosure, which is set forth in the accompanying claims.
It will be understood from the above that the disclosure in its embodiments may provide the advantage of allowing pressure testing of pressure vessels without the safety hazards of pneumatic testing and without contamination issues which can be experienced from existing hydrostatic testing methods.
| Number | Date | Country | Kind |
|---|---|---|---|
| 19275016.4 | Feb 2019 | EP | regional |
