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Specifications - Lord and Son Construction, Inc.

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systems served by this system are not enabled, this system shall<br />

not be enabled.<br />

(2) When this system is enabled (SYS-ENA) the Pressure Control loop<br />

shall be enabled.<br />

b. HAND-OFF-AUTO Switch: The hot water pump variable frequency drive (VFD)<br />

unit shall have an integral H-O-A switch:<br />

(1) HAND: With the H-O-A switch in HAND position, the pump shall<br />

start <strong>and</strong> run continuously. Pump speed shall be under manualoperator<br />

control.<br />

(2) OFF: With the H-O-A switch in OFF position, the pump shall stop.<br />

(3) AUTO: With the H-O-A switch in AUTO position, the pump shall run<br />

subject to the Hot Water Pump Start/Stop (HW-PMP-SS) comm<strong>and</strong> <strong>and</strong><br />

pump speed shall be under control of the DDC system.<br />

c. roofs <strong>and</strong> Safeties<br />

(1) DDC Hardware shall monitor all proofs <strong>and</strong> safeties.<br />

(2) Proofs: None<br />

(3) Safeties: None<br />

(4) DDC Hardware reset of all proofs <strong>and</strong> safeties shall be via a<br />

local binary push-button (RST-BUT) input to the DDC Hardware, via a<br />

remote comm<strong>and</strong> to the DDC Hardware via SNVT or both (where the<br />

Contractor provides both reset functions <strong>and</strong> the operator can use<br />

either one to perform the reset), as shown on the Points Schedule<br />

drawing.<br />

d. Pressure Control: When this loop is enabled the DDC Hardware shall<br />

modulate the pump variable frequency drive unit to maintain the pipe<br />

system pressure at setpoint as shown, as measured by the differential<br />

pressure tap <strong>and</strong> sensor as shown. When this loop is disabled, the DDC<br />

Hardware capacity modulation output to the VFD shall be zero percent.<br />

3.5 CONTROLLER TUNING<br />

The Contractor shall tune each controller in a manner consistent with that<br />

described in the ASHRAE FUN IP. Tuning shall consist of adjustment of the<br />

proportional, integral, <strong>and</strong> where applicable, the derivative (PID) settings<br />

to provide stable closed-loop control. Each loop shall be tuned while the<br />

system or plant is operating at a high gain (worst case) condition, where<br />

high gain can generally be defined as a low-flow or low-load condition.<br />

Upon final adjustment of the PID settings, in response to a change in<br />

controller setpoint, the controlled variable shall settle out at the new<br />

setpoint with no more than two (2) oscillations above <strong>and</strong> below setpoint.<br />

Upon settling out at the new setpoint the controller output shall be steady.<br />

With the exception of naturally slow processes such as zone temperature<br />

control, the controller shall settle out at the new setpoint within five (5)<br />

minutes. The Contractor shall return the controller to its original<br />

Section 23 09 23 Page 43

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