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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The above-mentioned general trends must be verified by laboratory measurements and field experience.

This calculation of energy does not include an allowance for liquid bypass, as was discussed in Sec. The oil circulation rate to the evaporators is reduced as a result of the low compressor discharge superheat and separation at the surge drum- accumulator low-pressure receiver. This arrangement is often used for ice thermal storage units or in some cases for cooling air.

Liquid Overfeed System

The pump is small with an impeller diameter of mm 6 inwhich is appealing, but in order to develop the necessary pressure difference it must operate at rpm. Cavitation is the conversion of liquid into bubbles of vapor because of an abrupt drop in pressure as the liquid flows into the pump housing or impeller.

Failure of this liquid flow could result in overheating of the motor and shutdown of the pump. The fact that the pressure drops as the flow increases will result in reduced bypass flow, but that is no problem because the flow through the system is adequate to assure that the pump work does not vaporize the liquid. In both cases sysgem drain is from a region of ammomia motion where oil, being heavier reciculated liquid ammonia, will separate.

Some basic objectives in designing and installing the pump and its inlet piping are: Also shown are the head-flow curves for two systems.

Assuring this bypass flow is even more critical in the hermetic pump than it is in the open type. This arrangement shares most features of the layout of the pverfeed pump including the provisions for adequate NPSH and a bypass line back to the vessel to assure that there is always some liquid flow through the pump even if valves in the discharge pipe network are closed.


For multiple cold rooms and freezers it is supposed to be the best choice to save electric energy as well getting the highest efficiency of the refrigeration systems.

Liquid from the condenser flows through a float valve which allows only liquid to pass and also drops the pressure from the condensing pressure to that of the CPR. Knowledge of the pressure drop to be experienced in the liquid distribution system is required for selection of the pump.

The difference in elevation between the liquid level in the low- pressure receiver and the pump should generously exceed the minimum NPSH. So at the exit of the coil a mixture of liquid and vapor flow out of the evaporator, as shown in Fig. For example, the maximum power that the pump with the mm 9-in impeller diameter can draw is approximately 2. The piping interfaces to the other segments of the system are: This gas is drawn directly to the compressors and eliminated as a factor in the design of the system low side.

The individual factors12 that would be included in a calculation are the following: Properly applied flooded evaporator coils operate with the same effectiveness of coils served by liquid recirculation. Geltz6 recommends a higher n when the coil is circuited for top feed of refrigerant to achieve good wetting of the evaporating surfaces.

The liquid level is not controlled in the intercooler, so the option is not available to bubble discharge vapor from the low-stage compressor through liquid for desuperheating.

The arrangement in Figure 8. As valves in the system progressively open, the flow rate increases and eventually the pressure differential that the pump can develop drops. This regulator prevents the pressure and temperature in the evaporator from falling so low that products would be damaged or that frost would form on the coil requiring defrost provisions.


There is, however, another loss associated with gas pumping that must be charged, and this loss is occasioned by the warm vapor heating the cold liquid and the walls of the pumping vessel.

To enhance the desuperheating of the discharge gas, the bypass liquid can be atomized with a spray nozzle The flow rate vaporized, recurculated, is dictated by the total refrigeration rate, qtotal, 8.

Liquid Overfeed System | Water Foods Pvt. Ltd.

Furthermore, the low-pressure receiver can be smaller and contain less charge. Furthermore, the liquid recirculation is forced by either mechanical pumps or by gas-pressure pumping. The conversion of head to pressure is dependent upon the liquid density as expressed by the equations: In either concept the mixture of liquid and vapor that floods out of the evaporators flows to a liquid-vapor separator.

None of the energy of the high-pressure rffrigeration is recovered, and the pumping energy for the cycle is that required to elevate the low-pressure vapor back to that of the high-pressure pumping gas. In addition to low-temperature applications where liquid liqquid now predominates, the concept may have advantages in higher-temperature systems used for air conditioning Furthermore, achieving more than about 1. Usually designers try to select the maximum-flow operating point rather high on the performance curve, preferring Point A over Point B.

Flash gas is removed in the machine room rather than having it appear after the expansion valve at each evaporator. When the oil level drops low, recirculater reservoir is refilled by means of a manual oil pump. The density of vapor is less than liquid, so the mass will be less.

The maximum-flow orifice limits the flow rate so that the NPSH provided by the installation is not exceeded. In comparison to ammonia, the latent heat ammpnia the halocarbon refrigerants is lower, but the liquid ammoniw is higher.