HIGH EFFICIENCY DEHUMIDIFICATION SYSTEM AND METHOD
This document describes a high efficiency dehumidification system (HEDS) and method of operating the same. The HEDS systems and physical implementations can include a variety of equipment, such as fans, filtration systems, fluid-conveying coils, piping or tubing, heat transfer coils, vents, louvers, dampers, valves, fluid chillers, fluid heaters, or the like. Any of the implementations described herein can also include controls and logic, responsive to one or more sensors or other input devices, for controlling the equipment for each implementation described herein.
1 . A high efficiency dehumidification system for an air handling unit (AHU), the system comprising:
a cooling coil including an inlet to receive chilled liquid at a first temperature from a cooling plant to cool and dehumidify air that passes over the cooling coil, and including an outlet to output spent chilled liquid at a second temperature, the second temperature being greater than the first temperature due to heat exchange from the air to the chilled liquid;
a first fluid conduit including an input connected with the outlet of the cooling coil, the first fluid conduit further including an output junction comprising first and second outputs;
a cooling recovery coil including an inlet connected with the first output of the output junction of the first fluid conduit to receive at least a portion of the spent chilled liquid at about the second temperature, and including an outlet to return the spent chilled liquid from the cooling recovery coil to the cooling plant, a remaining portion of the spent chilled liquid bypassing the cooling recovery coil via the second output of the output junction of the first fluid conduit and returning to the cooling plant;
a second fluid conduit including at least one input connected with each of the first and second outputs of the output junction, the second fluid conduit further including an outlet to return the spent chilled liquid to the cooling plant; and
a control mechanism on the second fluid conduit to control a flow rate of the spent chilled liquid from the cooling recovery coil to the cooling plant, based on at least a dewpoint temperature of the air.
2 . The system of claim 1 , wherein the control mechanism includes a control valve.
3 . The system of claim 1 , wherein the control mechanism includes a variable flow pump.
4 . The system of claim 1 , further comprising a manual bypass line valve between the second output of the first fluid conduit and the input of the second fluid conduit, to control an amount of the portion and the remaining portion of the spent chilled liquid entering the at least one input of the second fluid conduit.
5 . The system of claim 1 , further comprising a differential pressure control valve between the second output of the first fluid conduit and the at least one input of the second fluid conduit, to control an amount of the portion and the remaining portion of the spent chilled liquid entering the input of the second fluid conduit.
6 . The system of claim 1 , further comprising an automatic flow control valve between the second output of the first fluid conduit and the at least one input of the second fluid conduit, to control an amount of the portion and the remaining portion of the spent chilled liquid entering the input of the second fluid conduit.
7 . The system of claim 1 , further comprising a control system to evaluate input data representing one or more variables, and to determine one or more outputs to control the system to control the one or more variables.
8 . The system of claim 1 , further comprising a second cooling recovery coil comprising:
an inlet configured to receive at least a portion of the spent chilled liquid from the first cooling recovery coil; and
an outlet configured to return the spent chilled liquid from the second cooling recovery coil to the cooling plant.
9 . The system of claim 8 , further comprising a modulating control valve connected with the first and second outputs of the output junction, the modulating control valve configured to modulate an amount of the spent chilled liquid passing from the cooling recovery coil to control a temperature of air that passes over the second cooling recovery coil.
10 . The system of claim 1 , further comprising a preheat coil for preheating air passing over the preheat coil to the cooling coil.
11 . The system of claim 1 , further comprising a reheat coil for controlling a temperature of the air passing from the cooling recovery coil.
12 . The system of claim 1 , further comprising a control system configured to modulate the control mechanism to control an amount of the portion of the spent chilled liquid entering the cooling recovery coil and an amount of the remaining portion of the spent chilled liquid bypassing the cooling recovery coil and returning to the cooling plant.
13 . A method of operating a high efficiency dehumidification system for an air handling unit (AHU), the method comprising:
receiving, via an inlet of a cooling coil, chilled liquid at a first temperature from a cooling plant to cool and dehumidify air that passes over the cooling coil,
transmitting, via an outlet of the cooling coil through a first fluid conduit, spent chilled liquid at a second temperature, the second temperature being greater than the first temperature due to heat exchange from the air to the chilled liquid, wherein the first fluid conduit includes an input connected with the outlet of the cooling coil, and wherein the first fluid conduit further includes an output junction comprising first and second outputs;
receiving, via an inlet of a cooling recovery coil that is connected with the first output of the output junction of the first fluid conduit, at least a portion of the spent chilled liquid at about the second temperature,
returning, via an outlet of the cooling recovery coil, the spent chilled liquid from the cooling recovery coil to the cooling plant, a remaining portion of the spent chilled liquid bypassing the cooling recovery coil via the second output of the output junction of the first fluid conduit and returning to the cooling plant; and
controlling, via a control mechanism connected with a second fluid conduit, a flow rate of the spent chilled liquid from the cooling recovery coil to the cooling plant, based at least in part on a dewpoint temperature of the air, wherein the second fluid conduit comprises at least one input connected with each of the first and second outputs of the output junction, the second fluid conduit including an outlet to return the spent chilled liquid to the cooling plant.
14 . The method of claim 13 , further comprising controlling, via a manual bypass line valve, an amount of the portion and the remaining portion of the spent chilled liquid entering the at least one input of the second fluid conduit.
15 . The method of claim 13 , further comprising controlling, via a differential pressure control valve, an amount of the portion and the remaining portion of the spent chilled liquid entering the at least one input of the second fluid conduit
16 . The method of claim 13 , further comprising controlling, via an automatic flow control valve, an amount of the portion and the remaining portion of the spent chilled liquid entering the at least one input of the second fluid conduit.
17 . The method of claim 13 , further comprising evaluating, via a control system, input data representing one or more variables, and to determine one or more outputs to control the system to control the one or more variables.
18 . The method of claim 13 , wherein the flow control valve is an automatic flow control valve.
19 . The method of claim 13 , further comprising:
receiving, via an inlet of a second cooling recovery coil, at least a portion of the spent chilled liquid from the first cooling recovery coil; and
returning, via an outlet of the second cooling recovery coil, the spent chilled liquid from the second cooling recovery coil to the cooling plant.
20 . The method of claim 19 , further comprising modulating, via a variable flow pumping system connected with the first and second outputs of the output junction, an amount of the spent chilled liquid from the cooling recovery coil to control a temperature of air that passes over the second cooling recovery coil.