
For many years the military specification MIL-
As a matter of fact, the American aeronautical manufacturers have always exercised a part, more or less important, of their activities in the Military sector with the DOD (Department of Defence)
Besides, the tied-
Considering the specificity of their manufacturings, the aircraft manufacturers indeed
wrote their own instructions as soon there were liable vis-
So was universally adopted the MIL-
The MIL-
While the aeronautical technology quickly progressed, processing new alloys, in particular
those from titanium and from nickel, it is rather surprising to notice that the MIL-
The following considerations had not been foreseen by the MIL-
The increasing use of titanium-
Indeed, under the effect of some physico-
practically no longer used.
The constant search for improvement of performances required to increase the thermodynamics
yield of gas turbines. According to the second of Carnot’s principles, an increase
of the temperature of the hot section of gas turbines required to resort on one hand
to the technology of hollow air cooled gas turbine blades and on the other hand to
heat resisting alloys, able to resist to higher and higher temperatures, such as
those based, among others, on cobalt, chromium and nickel. At temperatures above
900 °C approximately, nickel may undergo an "oxidation" by sulphur. This chemical
reaction is known as the sulphidation which leads to the formation of black corrosion
products which are nickel sulphide-
The catalystic action of alkaline metals, such as sodium and potassium, was put in evidence in the sulfidation reaction :
Na
Ni + S → NiS
or K
Sulphur is present in organic compounds and as impurities in oil products. Alkaline
metals are present in surfactants, such as those of the anionic type, among which
we can quote one of the most known: the sodium dodecylbenzenesulphonate (CAS N° 27323-
It is necessary to point out that the organic synthesis of some nonionic surfactants may require the use of potassium sulphate as catalyst. So, such surfactants contain unwanted impurities:which are sulphur and potassium. As penetrants and hydrophilic penetrant removers contain surfactants, it is necessary to carry out a rigorous selection of them. To get rid of the alkaline impurities, some manufacturers, at the beginning of the 80s, even made them undergo a long treatment on ion exchange resins.
The drop of the fluorescence brightness of crack indications detected by penetrant testing is a phenomenon known under the name of‚‘‘HEAT FADE‘‘. It mainly appears at the drying stage after water rinsing: because either the drying temperature is too high
or the drying time in the air circulated oven is too long. It is interesting to note that Pierre CHEMIN presented a paper on this subject titled "Thermal effects in Penetrant Testing processes" at the second European Non Destructive Testing Conference held in Vienna, from 14 till 16 September 1981.
Most of red dye and fluorescent penetrants approved according to MIL-
Indeed, higher the flash point higher the hydrocarbons price.
These fluorescent penetrants which had a flash point of 70 °C, had a major drawback when used by immersion. Indeed, in tank, there was a slow but real evaporation of hydrocarbons all the more important as the ambient temperature was high. This also caused the evaporation of the other nevertheless less volatile constituents of the penetrant. The same phenomenon could also occur by dipping parts in the penetrant tank if, the parts were not allowed a sufficient time for cooling down to room temperature after trichloroethylene vapour phase degreasing. This lead to a general imbalance in the penetrant causing on one hand: a viscosity increase and on the other hand an increase of the drag out losses together with a fluorescent background on the part surfaces.
So, to reduce this excessive fluorescent background, operators instinctively went to overwash the parts, while these penetrants exhibited a poor resistance to water overwash. Overwashing consequences were the loss of crack indications, the drop in sensitivity and finally the loss of the reliability of detection.
It is necessary to note that the replenishment of the penetrant baths was usually done by adding, after analysis (distillation of flammable products!), a standard mixture of hydrocarbons and the other relatively volatile materials of the penetrant such as: methylisobutylcarbinol, odourless kerosene, etc. … Nowadays, this replenishment, which was a complex and risky operation, is no longer performed or even necessary.
The first serious works on quantification of the penetrant process sensitivity were undertaken in the seventies. Among these, let us name those of Norman H.HYAM (1972), then later those of Lormerson Junior (Two fold congruency test) of Pratt & Whitney USA and a little later those of Jean VAERMAN (SNECMA).
All these important and remarkable works allowed to determine the influence of the variation of operating parameters of the penetrant processes on the sensitivity of crack
detection.
These works brought Pratt and Whitney, in the absence of the revision of the specification
MIL-
Pratt and Whitney above all took care of flash point figure. Would not one of their factories have been then on fire? However Pratt and Whitney withdrew the qualification and refused all the chemicals, whatever they were, of which the PMCC flash point was lower than 200 °F (93 °C).
As an example, let us quote the compressor washing fluids (designed to restore the thrust of aeroengines and industrial gas turbines) although these fluids are used at the strength of 20% by volume in water.
The Pratt and Whitney specification also required:
– Maximum allowable contents in impurities: chlorine, sulphur, sodium and potassium.
– Resistance to the thermal effects (heat fade).
These new requirements made the penetrants manufacturers design new penetrants because none of those who existed on the market, at that time, meet this specification. So Pratt and Whitney distanced himself by causing certain problems. The penetrant manufacturers worked hastily wanting to be quickly approved.
If new penetrants were approved according to this specification, they gave rise to surprises; in particular, problems of water washability and other problems associated to penetrant removal even by using the hydrophilic penetrant remover at the excessive strength of 20% by volume in the water.
So, the suppliers and the subcontractors working for this aeroengine manufacturer had then to double, at that time, the number of their penetrant process lines, ones to meet Pratt and Whitney’s requirements, the others to meet requirements by the other aeroengines manufacturers which had not concurred with Pratt and Whitney. Same situation in the Repair and Maintenance shops worldwide.
The future praised Pratt and Whitney ideas because its specification became the core
of the MIL-
Let us point out here that the differences between the MIL-
With regard to penetrant materials listed in the QPL of the MIL-
– Guarantee that products were checked about hygiene and safety (in 3.3.1) for operators. Complete absence of asbestos required in developers.
– Higher flash point 200 °F (93 °C) minimum (in 3.3.3), higher safety. Furthermore, there is an empirical rule of thumb establishing a relationship between the flash point and the maximal temperature of penetrant application. The rule is: PMCC flash point less 20 °C is roughly equal to the maximum temperature of penetrant application. For instance, if the flash point is 93 °C, the maximum temperature for penetrant application on the part surface is 73 °C. As consequence it is possible to reduce the cooling time after parts hot degreasing before penetrant application.
– Thermal stability (in 3.4.5.4) which allows to evaluate the penetrant resistance to thermal effects (heat fade).
– Penetrant tank stability (in 3.4.7).
– High temperature titanium stress corrosion (in 4.5.2.2).
– High temperature (1,850 °F ± 50 °F) or (1,010 ± 28 °C) corrosion of cast nickel alloys (in 4.5.2.3).
– Fluorescent brightness test in accordance with ASTM E 1135.
– Ultraviolet stability.-
