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Testing leak test pressure

EN 13184. (2001) Non-Destructive Testing - Leak Test Pressure Change Method, European Standards. [Pg.187]

When constmction is complete, the pipeline must be tested for leaks and strength before being put into service industry code specifies the test procedures. Water is the test fluid of choice for natural gas pipelines, and hydrostatic testing is often carried out beyond the yield strength in order to reHeve secondary stresses added during constmction or to ensure that all defects are found. Industry code limits on the hoop stress control the test pressures, which are also limited by location classification based on population. Hoop stress is calculated from the formula, S = PD/2t, where S is the hoop stress in kPa (psig) P is the internal pressure in kPa (psig), and D and T are the outside pipe diameter and nominal wall thickness, respectively, in mm (in.). [Pg.49]

With all leaks stopped, and the reactor under test pressure with nitrogen, set the nitrogen pressure regulator to the lowest pressure on the controller, but above 0.3 atmosphere or 5 psig. Now open the flow controller and set the N2 flow to 66 mL/s, equivalent to 10.5 mols/hr rate, to start the flow. Also start heating the unit. [Pg.87]

The hydrostatic testing is the first test used on the lube system. The system is tested while assembled or partially assembled, based on the particular system. A test pressure of VA times the maximum allowable working pressure, a minimum of 20 psi for the oil side, is used for the test. For the oil-wetted parts, the test fluid should be light oil, which is normally the recommended lubricant for the compressor train. The test period is the length of time needed to inspect for leaks, or a minimum ol thirty minutes. Acceptance is based on the lack of leaks as visually observed or the lack of a drop in the test pressure. [Pg.415]

STANDARD LEAK TEST PRESSURE setting 3 PERCENT... [Pg.359]

It is possible that the employees concerned did not understand the difference between a pressure test, normally carried out with water, and a leak test, often carried out with compressed air at a pressure well below the test pressure. [Pg.200]

The test pressure should be maintained for at least an hour. In this period a thorough test is made of each joint with soapy water. This method is no more tedious than a refrigerant leak test and saves the time and loss of refrigerant. Targe leaks will be heard. [Pg.137]

A piping system containing expansion joints shall be leak tested without temporary joint or anchor restraint at the lesser of 150% of design pressure for a bellows-type expansion joint or the system test pressure determined in accordance with para. IP-10.6. In no case shall a bellows-type expansion joint be subjected to a test pressure greater than the manufacturer s test pressure. [Pg.131]

If leakage is indicated during the hold period, the pressure may be reduced while locating the leak. After the leak is repaired, a new hold period must be started at full test pressure. [Pg.242]

Method Test gas Smallest detectable leak rate Pressure range Quantitative measurement... [Pg.116]

Another integrity test referred to as the pressure hold test makes use of the fact that below the transition pressure no bulk flow of the test gas takes place. Therefore, in a pressure hold test, once a filter system is in place and the filter medium wetted, pressure is applied to the system and then shut off and sealed. If there are no leaks in the system or holes in the membrane larger than the corresponding test pressure used, the pressure should remain constant. If the pressure drops, there is a leak somewhere in the system that should be corrected. The pressure hold test is popular in testing filter assemblies and systems in... [Pg.167]

Leak test pressure The specified inlet static pressure at which a quantitative seat leakage test is performed in accordance with a standard procedure (e.g. API 527, see Section 4.2). [Pg.40]

As can be seen in Figure 1, the silicon precursor is fed to the reaction cell at the side where the y-alumina layer is situated. The oxygen is fed to the other side of the membrane. The membrane is clamped gas-tight in the cell by polymer O-rings. Before each experiment the apparatus was checked for possible leaks by pressure testing. The cell was heated to the reaction temperature at a rate of 2°C/min. [Pg.107]

The bomb is then placed in the jacket, and the gas inlet tube is fastened securely. The thermocouple is also inserted. From this point on, all operations should be performed on the other side of the wall separating the operator from the equipment. Hydrogen is bled into the bomb from the high-pressure tank, the valve to the tank is closed, and the bomb is allowed to stand for about a half hour in order to test for leaks. If a leak has developed, as indicated by a drop in pressure, one locates it by painting all the joints with a soap solution and looking for bubbles of gas, which indicate a leak. The connector is tightened, and if this does not stop the leak, the pressure in the system should be released, the connection disassembled, and the tapered end of the tube re-formed with a tool supplied for the purpose. These measures usually will stop the leak, but if they do not, it will be necessary to ream out the connector seat with the reamer designed for this purpose. [Pg.233]

Fig. 6. Retain capacity, (a) Leak off pressures and repeat formation test data from the North Sea Central Graben. The curve is the minimum in situ horizontal stress trend, determined from the lower bound of leak off test data, (b) Retain capacity in the North Sea Central Graben. Retain capacity is the difference between the minimum horizontal in situ stress and the fluid pressure at any point. At low retain capacity (1000 psi or lower) the likelihood of trap failure is increased (Gaarenstroom et al., 1993). Fig. 6. Retain capacity, (a) Leak off pressures and repeat formation test data from the North Sea Central Graben. The curve is the minimum in situ horizontal stress trend, determined from the lower bound of leak off test data, (b) Retain capacity in the North Sea Central Graben. Retain capacity is the difference between the minimum horizontal in situ stress and the fluid pressure at any point. At low retain capacity (1000 psi or lower) the likelihood of trap failure is increased (Gaarenstroom et al., 1993).
Fracture pressures are estimated from leak-off tests (LOT), where mud is pumped into the formation until the first evidence of fractures is detected. Leak-off pressure is the pressure at which the formation develops very thin fractures prior to rock failure. A great advantage of this kind of test is that it is an in situ test, thus we do not have to deal with relaxation or unloading problems. Fracture pressures estimated from LOT is in the range of 0.6-0.8 times the litho-static pressure, which is within the fracture pressure domain (0.7-0.9 lithostatic pressure) given by DuRouchet (1981). The overpressures do not reach fracture pressure (LOT) in any of the wells investigated. However, the pore pressure reaches 80% of... [Pg.204]

Confirm suitability of equipment leak test, pressure test. [Pg.308]

You can also put an adjustable relief valve on the feed line, to release the compressed air when the component reaches test pressure. This is handier and safer than just observing the gauge and turning the compressor off when it hits target pressure. With the relief valve, you can focus on observing the leaks without having to turn the pump on and off intermittently. For this testing, the positive pressure should be at least 20% to 25% above your MOP. [Pg.52]


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