User Guide for Desiccant Dehumidification Technology

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    FACILITIES ENGINEERING

    APPLICATIONS PROGRAM

    User Guide for DesiccantDehumidification Technology

    byThomas E. Durbin and Michael A. Caponegro

    U.S. Army Construction Engineering Research LaboratoriesChampaign, IL 61826-9005

    Approved for Public Release; Distribution Is Unlimited.

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    The contents of this report are not to be used for advertising, publication,

    or promotional purposes. Citation of trade names does not constitute an

    official endorsement or approval of the use of such commercial products.

    The findings of this report are not to be construed as an official

    Department of the Army position, unless so designated by other authorized

    documents.

    DESTROY THI S REPORT WHEN IT I S NO LONGER NEEDED

    DO NOT RETURN IT TO THE ORIG INATOR

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    USACERL FEAP UG-97/107

    Foreword

    This study w a s done for t he U .S. Army Cent er for public Works (U SACP W) under

    the Facilities Engineering Application Program (FEAP); Work Unit F56, FEAP

    Desiccant Demonstrat ion at APG. The technical monitor was Dennis Vevang,

    CECPW-EM.

    The work was performed by the Troop Installation Operation Division (UL-T) of the

    Util i t ies and Industrial Operations Laboratory (UL), U.S. Army Construction

    Engineering Research Laboratories (USACERL). The USACERL princ ipa l

    investigator was Thomas E. Durbin. Chang W. Sohn is Acting Chief, CECER-UL-U;

    Mart in J . Sa voie is Act ing Operat ions Chief, CE CE R-U L; a nd G ary W. Schanche is

    the associated Technical Director, CECER-UL. The USACERL technical editor was

    William J . Wolfe, Technical R esources.

    COL J am es T. Scott is Comman der an d Dr . Micha el J . OConnor is D irector of

    USACERL.

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    2 USACERL FEAP UG-97/107

    Contents

    Foreword . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 1

    1 Executive Summary . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 3

    2 Pre-Acquisition: . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 5

    Technology Description and Application . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .5

    Possible Solutions Offered by Desiccant Dehumidification . . . . . . . . . . . . . . . . . . . . . ...8

    Costs and Benefits . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .12

    Sample Cost Summary . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 12

    Life Cycle Cost/Benefit Prediction . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .13

    Utility and Space Requirements . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .14

    3 Acquisition/Procurement . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 16

    Acquisition/Procurement Strategy.. . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .16

    Potential Funding Sources . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .17

    Procurement Documents . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .17

    Procurement Scheduling . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .17

    Design Considerations . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .18

    Construction Considerations . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .19

    4 Post Acquisition . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 20Acquisition Scheduling . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .20

    Commissioning . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .20

    Operation and Maintenance issues . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .20

    Performance Evaluation . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . .21

    Appendix A: Vendors . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 23

    Appendix B: Example Scope of Work for Two-Wheel Desiccant Dehumidification

    Systems . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 24

    Appendix C: Sample Specifications for Two-Wheel Desiccant

    Dehumidification/Cooiing System . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . . 29

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    USACERL FEAP UG-97/107 3

    1 Executive Summary

    Manufacturing industries have used desiccants in various applications for over 50

    years, but have only recently begun to apply desiccant dehumidification systems

    (DDSs) to Heating, Ventilation, and Air-Conditioning (HVAC) applications.

    Depending on climat e an d fa cility loading, a high percent a ge of a buildings cooling

    load can be la tent (moisture) load. C onventional cooling equipment operat es at low

    temperat ures to cool the a ir to i ts dew point t empera ture, w here dehumidif ica t ion

    via condensat ion on the coils begins. I t ma y t hen be necessary t o reheat the a ir to

    a comfortable tempera ture before i t enters t he occupied space. DD Ss, by contr ast ,

    remove water from the air by using a desiccant , or chemical drying agent. DDSs

    offer several benefits when used in conjunction with air-conditioning systems.

    Removing moisture from the air by desiccation decreases the amount of vapor-

    compression energy needed to dehumidify the air being supplied to the user, and

    increases the comfort level in the conditioned space. Desiccant systems also decrease

    moisture accumulation in ducts and around coils, inhibiting the growth of mold and

    mildew.

    While research in desiccant dehumidification technology development has been

    conducted for severa l yea rs, commercial a pplica tions of desiccant dehumidifica tiontechnology have been l imited in th e past by ma terial a nd ma nufacturing consider-

    ations. Current desiccant dehumidification systems range in capacity to 30,000 cubic

    feet per minute (cfm) and are near the commercialization stage. Since these systems

    are heat driven (not electrically driven), conversion to a desiccant system can reduce

    site peak electrical demand and levelize utility loads, allowing for more efficient

    power plant operation. Energy cost savings result from reduced chiller loads,

    reduced electrici ty peak demand, and el imination of air reheating requirements .

    Desiccant dehumidification systems can also reduce or eliminate the use of harmful

    CFC s in the HVAC system by using na tura l gas or l iquid propane gas (LPG ) as t he

    prima ry fuel for dehumidifica tion.

    AS yet , very few desiccant systems have been instal led at mil i tary instal la t ions, and

    only then in specialized applications. Desiccant dehumidification systems may offer

    advantages for military applications over other energy supply options by increasing

    force readiness, providing greater system reliability, controlling humidity in areas

    with sensit ive mat erial and equipment, a nd by reducing environmental impact a nd

    energy costs.

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    4 USACERL FEAP UG-97/107

    Points of Contact :

    Dennis Vevang

    U .S. Army C enter for P ublic Works (U SACP W)

    ATTN: CE CP W-E M

    2701 Telegra ph R oadAlexandria, VA 22312-3862

    Comm: (703) 806-6071

    FAX: (703) 806-5220

    Thomas E. Durbin

    U .S. Army C onstruction En gineering Resear ch L aborat ories (U SACERL)

    ATTN: CECER-ULU

    P O B ox 9005

    Champaign, IL 61826-9005tel : 217/352-6511, X5543

    F AX: 217/373-7222

    U RL : ht t p://w w w .cecer.a rm y.m il

    Micha el A Ca ponegro

    USACERL

    ATTN: CECER-ULU

    P O B ox 9005

    Champaign, IL 61826-9005tel: 217/352-6511, X5552

    F AX: 217/373-7222

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    USACERL FEAP UG-97/107 5

    2 Pre-Acquisition:

    Technology Description and Application

    Conventional Air-Conditioning/Ventilation Process

    Conventional air-conditioning systems are typically controlled by a thermostat (or

    simila r ty pe receiver/cont roller combina tion). They opera te in a ma nn er th a t keeps

    the space dry bulb temperature from exceeding the thermostat setpoint. To

    maintain that setpoint , condit ioned air is typical ly introduced into the space

    approximately 20 F* lower than the setpoint, so that the conditioned air can absorb

    the so-called sensible heat entering the space. Having absorbed this heat, air from

    the space is drawn back to the air-handling unit , where i ts temperature is again

    decreased before being returned to the space. The temperature decrease is

    accomplished by the returned air being drawn (or blown) through a cooling coil

    within the air handling unit. The coil is typically a specially designed finned-tube

    heat exchanger, containing a relatively cold circulating fluid (usually chilled water

    or a ref i igerant) into which heat from the air is transferred. Invariably, the

    described situation is somewhat more complicated since some amount of outside air

    is mixed with the returned air from the space, and then the mixture is cooled by thecoil. The most common reason for introducing outside (fresh) air is to provide

    ventila tion for th e occupant s of the spa ce. As the cooling coil reduces t he dry bulb

    temperature of the air so that the air, in turn, will provide sensible cooling for the

    space, the dry bulb temperature of the air is reduced almost to i ts dew point

    temperat ure. In fact , a considera ble portion of the a ir a ctua l ly reaches sat ura tion

    due to its contact with, or proximity to, the cooling coil, which has a temperature

    considerably lower than the air s dew point temperature. As a result , water

    condenses from th e a ir ont o the coil, w here proper selection of a irflow velocities (