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The Pressure Vessel Test

The UN pressure vessel test was applied to one sheet of sporting paper caps (about 5 g of explosive). The bursting pressure of the rupture disk was 5.9 kg/cm 2, and the average rate of temperature rise was 30 °C /min. [Pg.283]

The test results are shown in Table 5.5. Because the paper caps are well-sealed they decompose violently when heated. [Pg.283]


The pressure vessel test is used to examine the violence of thermal explosions. The test indicates whether a runaway reaction occurs when reactive chemicals in the vessel are heated by a fire or exposure to high temperature, or if the temperature of chemicals in the reactor rises abnormally. This test needs attention because the expulsion of chemicals from inside the vessel may mix with air and cause a mist explosion. [Pg.25]

The pressure vessel test is expected to be adopted as a standard test to check... [Pg.25]

Table 1.8 Hazards of Reactive Chemicals evaluated by the Pressure Vessel Test (PV), Mkm Ballistic Mortar Test (MkHI), BAM 50/60 Steel Tube Test (50/60), Test of Deflagration Violence (DF), and SADT Test (SADT)... Table 1.8 Hazards of Reactive Chemicals evaluated by the Pressure Vessel Test (PV), Mkm Ballistic Mortar Test (MkHI), BAM 50/60 Steel Tube Test (50/60), Test of Deflagration Violence (DF), and SADT Test (SADT)...
Fig. 3. 70 Relationship between PVLD in the pressure vessel test and deflagration rate in the improved time/pressure test on organic peroxides... Fig. 3. 70 Relationship between PVLD in the pressure vessel test and deflagration rate in the improved time/pressure test on organic peroxides...
Further, a relationship between the pressure vessel test (that assesses the pyrolitic hazard using the limited diameter (PVLD) that is considered to correspond to a rate of pressure increase during the heating process) and the improved time/pressure test applied to organic peroxides is shown in Fig.3.70. This suggests 83) a correlation between the results of the tests. [Pg.178]

The thermographic activity on the pressure vessel was carried out considering a part of it because of the axial symmetry. Three different partially overlapping area were inspected since it was optically impossible to scan the curved surface of the pressure vessel by a single sweep. The selected areas are shown in fig.7 and the correspondent positions of the thermographic scan unit are also illustrated. The tests were performed with a load frequency of 2, 5 and 10 Hz. [Pg.411]

The calculation was carried out using the ANSYS F.E.M. code. The pressure vessel was meshed with a 4 nodes shell element. Fig. 18 shows a view of the results of calculation of the sum of principal stresses on the vessel surface represented on the undeformed shape. For the calculation it was assumed an internal pressure equal to 5 bar and the same mechanical characteristics for the test material. [Pg.413]

TDF Drum Filter. This is a fairly conventional dmm filter housed in a vertical pressure vessel. Test data, obtained with the smallest model of only 0.75 m filtration area, is available (18). Larger models have also been announced, ranging up to the filtration area of 46 m and very large vessels. The operating pressures are moderate, up to 25 or 35 kPa, and the dmm speeds fairly conventional from 0.3 to 1.5 rpm. The range of dry cake production quoted is from 250 to 650 kg/m h for fine coal. [Pg.407]

In the case of a pressure vessel subjected to cyclic loading (as here) cracks can grow by fatigue and a vessel initially passed as safe may subsequently become unsafe due to this crack growth. The probable extent of crack growth can be determined by making fatigue tests on pre-cracked pieces of steel of the same type as that used in the pressure vessel, and the safe vessel lifetime can be estimated by the method illustrated in Case Studv 3. [Pg.160]

A series of utuaxial fatigue tests on unnotched plastic sheets show that the fatigue limit for the material is 10 MN/m. If a pressure vessel with a diameter of 120 mm and a wall thickness of 4 mm is to be made from this material, estimate the maximum value of fluctuating internal pressure which would be recommended. The stress intensity factor for the pressure vessel is given by K = 2hoop stress and a is the half length of an internal defect. [Pg.167]

The explosive decomposition of the solid has been studied in detail [6], The effect of moisture upon ignitibility and explosive behaviour under confinement was studied. A moisture content of 3% allowed slow burning only, and at 5% ignition did not occur [7], Thermal instability was studied using a pressure vessel test, ignition delay time, TGA and DSC, and decomposition products were identified [8], The presence of acyl chlorides renders dibenzoyl peroxide impact-sensitive [9], There is a further report of a violent explosion during purification of the peroxide by Soxhlet extraction with hot chloroform [10], Residual traces of the peroxide in a polythene feed pipe exploded when it was cut with a handsaw [11]. The heat of decomposition has been determined as 1.39 kJ/g. The recently calculated value of 69° C for critical ignition temperature coincides with that previously recorded. [Pg.1205]

When large quantities of a substance are handled, sensitivity of the material to heating under confinement may need to be considered to demonstrate the effect on the stored/handled, and probably confined, substance in the event of an external heat load. Tests such as the steel sleeve test or Koenen test [24, 137], the Dutch pressure vessel test (DPVT) [143], and the United States pressure vessel test (US-PVT) [143] may be applicable. These tests are used mostly for transportation considerations. The tests generally subject the sample substances to very high energy inputs under confined conditions, and thus are more severe than the deflagration and autoclave tests previously discussed in Section 2.3.3.2. As an example, the Koenen test, used mainly in Europe, is illustrated in Figure 2.32. [Pg.86]

A 100-mL aliquot of filtered fuel is placed in a borosilicate glass container. The container is placed in a pressure vessel which has been preheated to 194°F (90°C). The pressure vessel is pressurized with oxygen to 800 kPa (absolute) (100 psig)for the duration of the test. The pressure vessel is placed in a forced air oven at 194°F (90°C) for 16 hours. After aging and cooling, the total amount of fuel insoluble products is determined gravimetrically and corrected according to blank determinations. [Pg.180]

The pressure vessel was made by the Los Angeles Boiler Works. It is a 997-p.s.i. A.S.M.E.-approved vessel 18.75 inches in diameter and 20 inches in working depth. The depth was specified because the authors plan to assemble a stack of membranes. So far all tests have been made on a single osmotic gap assembly. [Pg.202]

The disruption and fragmentation of the reactor core as a result of the excursion hurled all the capsules from both locations at least 500 feet away. The Pb styphnate sample which had been mounted on the pressure vessel showed evidenoe of a high-order detonation, which was assumed to be the result of the high rate of energy input from the KIWI—TNT test. This assumption was based upon several premises. Primarily, the possibility of the material detonating as a result of impact rather than by radiation did not seem reasonable, since the other sample... [Pg.50]

Correct SRV sizing, selection, manufacture, assembly, testing, installation and maintenance as described in this book are all critical for the optimal protection of the pressure vessel, system, property and life. This book explains the fundamental terminology, design and codes to allow most engineers to make the correct decisions in applying SRVs in the process industry and to improve the safety to higher levels. [Pg.4]

The SL-1 (Stationary Low Power No. 1) was a 3-MW (thermal) boiling water reactor operated by military personnel at the National Reactor Testing Station, Idaho. As a result of interference with the control rods, there was an explosion on 3 January 1961 in which about 5 tonne of coolant were expelled from the pressure vessel (Horan Gammil, 1963). [Pg.77]

In this section, tests to evaluate the hazards of reactive chemicals more accurately will be introduced. They are assumed to be the best tests available to date, even though they all may not be completely perfected yet. a. Pressure Vessel Test 51 (See Chapter 3)... [Pg.25]

The comparison of the improved time/pressure test method with the test by HSE 0 2 8 4 reveals that the inner volume of the pressure vessel is larger by as much as 27cm 3 (20cm J for HSE) it has a branch nozzle for temperature measurement on the... [Pg.155]

The Keonen test" 3 7i, the Netherlands method 37 4 6 and the American method 3 7 4 7 for pressure vessel testing are known as test methods for evaluating fire dangers. For conventional methods for pressure vessel testing, refer to the previous book 1) where they are described in detail. [Pg.180]

In Japan, the Fire Services Law(FSL) has recently been revised 1011 and a pressure vessel test has been newly stipulated as the test method for determining the pyrolytic severity of Dangerous Goods- Class 5 Self—Reactive Substances—set forth in the FPL 31 . In this section a description will be given of the procedure for pressure... [Pg.180]


See other pages where The Pressure Vessel Test is mentioned: [Pg.133]    [Pg.184]    [Pg.190]    [Pg.190]    [Pg.283]    [Pg.133]    [Pg.184]    [Pg.190]    [Pg.190]    [Pg.283]    [Pg.12]    [Pg.942]    [Pg.248]    [Pg.157]    [Pg.92]    [Pg.100]    [Pg.73]    [Pg.328]    [Pg.7]    [Pg.209]    [Pg.410]    [Pg.412]    [Pg.218]    [Pg.220]    [Pg.419]    [Pg.419]    [Pg.1253]    [Pg.2278]    [Pg.205]    [Pg.942]    [Pg.68]    [Pg.151]   


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