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Take a good look around In addition to the problem of gas physical property variation, use of the real gas flow solutions offers an important improvement over existing gas flow theory that is particularly important for low permeability for- mations.
That is, the solution in terms of real gas pseudo- pressure includes the second-degree pressure gradient term neglected by methods based on eitiher liquid flow or ideal gas flow solutions. In the case of low-permeability gas well testing, current well test imerpretation methods can lead to formation capacity or deliverability estimates that can be grossly in error. This can be iIIustmted by comparison of flow capacity determinations by various methods for a known capacity system.
J E Schreiner, J R Barbosa Jr, C J Deschamps Federal University of Santa Catarina, Brazil
Excellent data for testing various methods are available from Carter's finite difference solUitions for real gas flow. Carter proposed a method to find flow capacity which was based on a correlation with a dimensionless time wherein viscosity and compressibihty were point time functions.
Thus, it is possible to compare flow capacities developed from his method, the liquid case analogy and from the real gas flow analysis of this paper.
The resulting temperature decrease in the vapour compression affects other regions of the compressor which are, in principle, also directly Figure 3. Vapour temperature behaviour responsible for determining the along a compression cycle.
For instance, the vapour temperature in the suction plenum decreases by as much as 25C, as can be seen in Fig.
To illustrate this point further, the temperatures at several regions of the compressor are shown in Fig. The compressor thermal profile decreases significantly with the Suction Plenum increasing number of Cylinder Wall droplets per family i.
Of particular importance 70 for the compressor under study is the electric 60 motor temperature, 0 whose operational limit Droplets per Family must be kept within Figure 4. Influence of the number of droplets specified boundaries.
For per family on the temperature at specific a total of 1 droplets regions of the compressor. Despite the remarkable temperature reduction produced by the in-cylinder liquid refrigerant atomization, it has been observed that the coefficient of performance, COP, defined by eq. Behaviour of the coefficient of performance of the compressor. Qe W COP 19 The reason for the deterioration of the system performance is due mainly to the mass of vapour generated during the evaporation of the droplets in the cylinder; work is consumed in the compression of the newly formed vapour, which is not utilized for producing the refrigeration capacity in the evaporator.
This is because, in an actual refrigeration cycle, liquid refrigerant at high pressure needs to be extracted from the condenser for injection into the cylinder.
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In other words, it is improbable that high grade energy in the form of liquid refrigerant, capable of producing a cooling effect in the system, can be used for compressor cooling at the expense of added compression work without a performance penalty. Critical regions such as the electrical motor, for example, experienced reductions of the average temperature of as much as 15C for cases where large quantities of liquid are atomized.
Nevertheless, from the performance point of view, despite the increase in volumetric efficiency due to the reduction of the superheating along the suction path, a significant reduction of the COP was observed. The decrease in the COP is directly proportional to the mass of liquid which is evaporated during compression. Summing up, droplet atomization is effective as a means of reducing the compressor thermal profile.Seiketsu Standardize : Standardize work practices Shitsuke Self Discipline : Sustaining, maintaining discipline and reviewing standards.
Seiri Sort : Tidiness, keeping only essential items. Tf R f , t Tf r Tsat t 0 Tf r, t inj, f Tc 18 where t inj,f is the instant at which the fth family is atomized into the cylinder and Tc is system condensing temperature.
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