Compressed air power is an effective and versatile servant in all field of industry. Next to Electricity & steam, Compressed air has become an important utility. There is no industry which does not use compressed air as a mode of power. It operate cylinder, runs motor, conveys material, clamps and apply pressure, atomise materials and so on and on. There is no limit to the use of compressed air power. Compressed air has a lot of advantages which cannot be achieved by other method. This has made the use of compressed air power more sophisticated, not limiting the same cleaning and inflating driers as it used to be. Compressed air power, like any other power costs money, and although air exists all around us, it cannot be put to use until it has been compressed to a pressure considerably higher than atmospheric. More over the air from the compressor is of little use to us unless the contamination from the air like Dust, rust, Moisture, scales. Oil are removed and made suitable for our application.
Air-cooled heat exchangers cool water by rejecting heat directly to the atmosphere,but the first cost and fan energy consumption of these devices are high and the plan area required is relatively large. They can economically cool water to within approximately 20°F of the ambient dry-bulb temperature—too high for the cooling water requirements of most refrigeration systems and many industrial processes.
This process of compression costs money - First Capital outlay for the Compressor and other equipment and secondly the running cost for the same. Thus the right selection of equipment is of Primer importance. 10 select the right equipment we need to know the right quality and quantity of air required for our application. We have come to a stage where invariably all areas of Textile Industry uses compressed air power in some machinery or other, either it is your Blow room, spinning frame, comber loom splicers to name a few. With the use of more sophisticated, high production machine the need for more and more complicated Pneumatic controls is required. To have minimum breakdown, and reliable performance with min. failure and to have good quality products the compressed air supplied to the machine should be of the highest order, Both in QUALITY and QUANTITY.
Compressed air contaminated with solid contaminant, like dirt, scales, rust etc. Moisture in the form of water vapour & condensed water and oil.
Any average atmosphere contains as much as 8000 ppm of water particles at 45°C and at 7kg/cm² pressure. In other words, at 75% humidity a 100cfm compressor takes in 18 Gallon of water vapour when it runs for a full day. Even a very efficient after cooler will be able to only remove 60% of moisture. The remaining moisture is carried along the line to causes scales, rust and all kinds of problem in the pneumatic equipments and also contaminates with anything to which this air gets in contact.
As an example, if we assume air is compressed from 10 ft³ to 1 ft³ the pressure is increased to 132 psig (9.10bars) (P₁V₁ = P₂V₂). Here, P₁V₁, equals original pressure and volume, and P₁ and P₂ must be stated as absolute pressure for calculation purposes. At 132 psig (9.10 bars) and 80°f (27°C), the 1 ft³ volume of air can hold only 0.00002 gal (0.00008 litre). Since there were 0.0061 litre in the air, but it can now hold only 0.00002 gal (0.00008 litre, the excess moisture will condense. If the excess water is not removed and the pressure is reduced to atmospheric, the excess water will gradually evaporate back into the air until an equilibrium is established. This will happen because the air under this condition can again hold 0.0016 gal (0.0061 litre) of water vapor. If the condensed water is removed as shown in Fig.A and the pressure again reduced as shown in Fig.A. The excess water will not be available for evaporation back into the air. The water vapor content of the 10 ft³ will than be 0.00002 gal (0.00008 litre), which was the maximum vapor content that 1 ft³ of air can hold at 80°F (27°C) and 132 psig (9.10 bars). The 0.00002 gal (0.00008 litre) per 10 ft³ thus determined is 0.002 gal per 1000 ft³. The 0.002 gal per 1000 ft³ is less than any quantity listed for 80°F (27°C). Therefore, the relative humidity is less than 5%.
A more useful term than relative humidity for indicating the condition of water vapor in a compressed air system is dew point. The dew point is the temperature at which condensate will begin to form if the air is cooled at constant pressure. At this point, the relative humidity is 100 per cent. In Fig. It will be noted that the dew point is equal to the saturated air temperature and follows the air temperature until it reaches its lowest point of 40°F (4.4° C). At this point, the air temperature was increased but the dew point remained at 40°F since the excess moisture had been removed. No further condensation would occur unless the temperature dropped below 40°F. This is further illustrated in Fig.C. If a refrigerant air dryer set at +35°F (+1.7°C) were installed at point A, Fig.B, it would cool the air to 35°C, and the moisture in the air would condense and be removed at this point. No further condensation would occur unless the temperature somewhere in the system were dropped below 35°F.
It should be noted that as air leaves a compressor it is under both an elevated pressure and elevated temperature. A delicate balance exists under this condition since air under pressure has less capacity for water vapor, where as air at elevated temperatures has a greater capacity for water vapor. The air leaving the compressor, however, is generally saturated, and any reduction in air temperature will cause water to begin to condense inside the downstream piping.
Refrigerant driers are rated at pressure dew points whereas desiccant driers have been traditionally rated at atmospheric dew points. However, there is a trend toward rating desiccant driers at the pressure dew point as well. A pressure dew point temperature is the more meaningful, since it indicates the temperature at which water vapor will begin to condense inside a pipeline at a given pressure. For reference purposes, pressure dew points can be converted to atmospheric dew points by use of the graph shown in Fig.C. To convert a 100 psig (6.9 bars), 35°F (1.7°C) pressure dew point to atmospheric dew point, one draws a vertical line midway between 30 and 40°F (-1 and +4°C) on the bottom scale until it intersects with the 100 psig line: then move to the left to the vertical coordinate. The atmospheric dew point will be -12°F (-24°C). For a 100 psig (6.9 bar), 50°F (10°C) dew point, the atmospheric dew point will be approximately 80°F (-18°C).
An oil lubricated compressor of 50 dm³/s capacity may introduce into the compressed air system as much as 0.16 litres of oil a week and since this oil has been subjected to high temperatures during compression of the air, it becomes oxidised and can no longer be considered as a lubricant and should be removed.
Normal air line filters will remove sufficient quantities of the oil to leave the air in a suitable condition to supply pneumatic tools and cylinders but certain processes demand completely oil-free air.
Whilst oil free compressors are available these still produce compressed air contaminated with dirt and water and it is generally more economical to use lubricated compressors, in conjunction with after coolers and standard air line filters, and to fit special High Performance Efficiency Filters to remove oil only from those parts of the compressed air system where oil free air is essential.
Oil can exist in three forms, oil/water emulsions, minute droplets suspended in the air as an aerosol and oil vapours.
As already mentioned the oil/water emulsions can be removed by standard air line filters but special techniques are needed to remove the aerosol form and oil vapours.
Theses droplets exist in the air stream in the particular size range from 0.01 micrometre up to 1.0 micrometer and ever larger but the most troublesome lie in the range quoted and over 90% of the oil particles present fall within this size range.
Because of their small particular size they are unaffected by the centrifugal action of most standard airline filters and can be only be removed by specially designed Ultra High Efficiency coalescing filters.
In addition to removing oil droplets, such filters have an equally high efficiency in removing minute water droplets but they should be protected against gross dirt or water contamination by means of standard air line filters mounted upstream.
It is advisable to ensure that these pre-filters, fitted in the line ahead of the Ultra High Efficiency Filter, are capable of removing dirt particles down to 5 micrometers or less as otherwise the coalescing filter may quickly become choked with dirt.
Coalescing filters must High Performance Efficiency Filters to accomplish their purpose and although standard filter tests exist, there is no accepted standard laid down to establish the efficiency of a coalescing filter in removing oil.
One can however predict the comparative efficiency of a coalescing filter in removing oil by assessing its performance under the test conditions laid down in the D.O.P. Test.
A coalescing filter showing a penetration of less than 0.001% when tested by any of these methods should provide compressed air in which the remaining oil contamination will be much less than 1mg/m³ (1 part in 1 million by weight).
For most processes the removal of oil vapors is unnecessary since, unlike water vapor, oil vapor exists only in minute quantities and is not objectionable except in those circumstances where its odor is unacceptable!
For certain processes in the food, pharmaceutical and beverage industries or where air is being used to supply breathing masks it is necessary to remove oil vapors.
This is most commonly done by passing the air through an adsorbing bed, usually of activated carbon, although other materials can be used.
Combination filters incorporating both coalescing elements and adsorbent beds are available to supply Ultra Clean Air which will satisfy the requirements of BS 4275 for breathing quality air as far as freedom from oil is concerned but special filter units are required to remove carbon monoxide or carbon dioxide.
Gem Equipments entered the engineering and fabrication industry in 1984. We specialise in design, engineering and fabrication of Cooling Towers, Compressed Air Dryers, Industrial Chillers and Compressed Air Treatment Accessories.
Gem Equipments Private Limited
S.F. No.103, Avinashi Road, Arasur,
Coimbatore - 641 407,
Tamil Nadu , India
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