Mechanically pumped liquid overfeed system arrangement. . tors.1 Table 1 shows the required recirculating liquid flow rate. expressed in gallons per For industrial refrigeration systems using ammonia as the. refrigerant. of a mechanically-pumped liquid overfed refrigerant loop, the refrigerant in the recirculating vessel. Ammonia Refrigeration System Safety. Ammonia refrigeration, the technology. • How is ammonia Survey (). ** Source: ASHRAE Position Document on ammonia (RA ) .. Gravity flooded recirculation system. Compressor(s) Liquid overfeed system components.

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Failure of this liquid flow could result in overheating of the motor and shutdown of the pump.

The pressure of the pumping gas significantly affects syste, rate of liquid delivery, so for low- temperature evaporators in a two-stage system, vapor at the intermediate pressure should be chosen for the pumping gas.

The purpose of this bypass is to always permit a flow of liquid through the pump, even if all the control valves out in the liquid system have closed off.

The pump may operate properly at the low-flow condition but cavitate at high-flow. An important precaution in the design, installation and operation of centrifugal pumps is to prevent cavitation.

Flash gas resulting from refrigerant throttling losses is removed at the low-pressure receiver before entering the evaporators. The following equations can provide a liqui guide for the liquid line size: Both of these influences are embodied in the pump performance curves. This is not to suggest that the positive-displacement pump has no role in industrial refrigefation systems. Computing the system pressure drop.

Liquid Overfeed System | Water Foods Pvt. Ltd.

Assuring this bypass flow is even more critical in the hermetic pump than it is in the open type. Somewhere in the evaporator, perhaps near the outlet, the rising saturation pressure meets the falling actual pressure and vaporization begins. In either concept the mixture of liquid and vapor that floods out of the evaporators flows to a liquid-vapor separator. Because the orifices are always placed at the inlets of the coil circuits they are at the top of top-feed coils.

It is ideally suited for liquid-transfer assignments, such as pumping liquid from a low-pressure vessel to one at high pressure.


The NPSH is defined as the liqjid in elevation between the liquid level of the centerline of the pump reckrculated the liquid level in the vessel supplying the pump.

The balance points or operating points are the intersections of the piping curve with the pump curve and are represented by points A and B.

The critical number of evaporators is a function of the systems, but usually when the system includes more than three to five evaporators, liquid recirculation is chosen. The refrigerant entering the compressor is close to saturated vapor conditions.

In contrast to hermetically sealed compressors where refrigerant vapor is in direct contact with insulated electrical conductors, hermetic pumps prevent refrigerant liquid from contacting the conductors. The advantages and disadvantages of gas pumping with respect to mechanical pumping will finally be explored. The pump is oveerfeed with an impeller diameter of mm 6 inwhich is appealing, but in order to develop the necessary pressure difference it must operate at rpm.

The assignment is to elevate the pressure of a liquid volume VB from that of the low- pressure receiver to that needed to deliver the liquid to the evaporators. ovfrfeed

The target pressure drop for the system that results in a reasonably-sized pump is between to kPa 30 to 50 psi. Selecting the pipe diameters. The mean-temperature difference between the air and refrigerant is represented by the area between the curves of the air and refrigerant temperatures.

After the principles of these two systems are explained, an analysis of the pumping energy of gas pumping and mechanical pumping will be conducted. This requirement is to equip the system with continuous bypass of liquid, as Figure 8.

While circulation ratios from 2 to 4 are standard, the possibility of choosing a circulation ratio much higher between 20 and 40 also has been explored8 on Downloaded from Digital Engineering Library McGraw-Hill www.

This leads to the practice of normally choosing an operating speed of rpm, which necessitates a pump of larger impeller diameter. With horizontal air flow, the lower circuits often draw a greater refrigerant refrgeration rate than the upper circuits, so usually each circuit is equipped with an orifice Sec. Lorentzen2 recommended velocities between 0. Richards3 analyzed the work of several authors including the experimental data of Van Maale and Cosijn4 that is shown in Fig.


The Froude number is a dimensionless term reflecting the ratio of the inertia to the gravity forces and in its simplest form is: The analysis that follows will determine the energy required to pump a liquid volume VB.

Hermetic pumps are usually higher in first cost than open-type pumps, even those with the oil seal. When the only practical source of pumping gas is at a high pressure, some improvement in efficiency can be achieved by passing this recircullated pressure pumping gas through a pressure-regulating valve that reduces the pressure in the pumping vessel.

The value of n affects the performance of the evaporator in several ways.

One manufacturer of coils5 recommends: The oil circulation rate to the evaporators is reduced as a recrigeration of the low compressor discharge superheat and separation at the surge drum- accumulator low-pressure receiver.

The controlled- pressure receiver is the most popular although the two-drum concept is also Downloaded from Digital Engineering Library McGraw-Hill www. This causes a minimum discharge temperature, preventing lubrication breakdown and minimum condenser fouling. When the oil level drops low, the reservoir is refilled by means of refrigeratin manual oil pump.

Liquid can then once again drain from the low- pressure receiver to the pumping vessel.

Liquid Overfeed System

The pumping work is reduced by a factor of 8 by using intermediate-pressure pumping gas compared to that at the condensing pressure. The arrangement in Fig. The discharge line of each of refrigfration pumps should be equipped with a check valve to prevent backflow through the idle pump. Not shown in Fig. The benefit derives from the fact that the pressure in the pumping vessel is lower after expelling the liquid from the pumping vessel. These two reasons are partially compensating, but in general, for a given refrigeration capacity the power required by the liquid pump in an ammonia system is about one-third that in a halocarbon system.