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Sommaire du brevet 1281393 

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Disponibilité de l'Abrégé et des Revendications

L'apparition de différences dans le texte et l'image des Revendications et de l'Abrégé dépend du moment auquel le document est publié. Les textes des Revendications et de l'Abrégé sont affichés :

  • lorsque la demande peut être examinée par le public;
  • lorsque le brevet est émis (délivrance).
(12) Brevet: (11) CA 1281393
(21) Numéro de la demande: 528239
(54) Titre français: DISPOSITIF THERMOSTATIQUE AUTOMATIQUE A POINT DE CONSIGNE, POUR DISPOSITIF DEBITEUR D'EAU GLACEE, REAGISSANT A LA TEMPERATURE DE L'EAU GLACEE REFOULEE
(54) Titre anglais: AUTOMATIC CHILLED WATER SETPOINT TEMPERATURE CONTROL USING RETURN CHILLED WATER TEMPERATURE
Statut: Périmé
Données bibliographiques
(52) Classification canadienne des brevets (CCB):
  • 341/27
(51) Classification internationale des brevets (CIB):
  • G05D 23/19 (2006.01)
  • F25B 49/00 (2006.01)
  • F25B 49/02 (2006.01)
  • G05D 23/24 (2006.01)
(72) Inventeurs :
  • ZINSMEYER, THOMAS M. (Etats-Unis d'Amérique)
(73) Titulaires :
  • CARRIER CORPORATION (Etats-Unis d'Amérique)
(71) Demandeurs :
(74) Agent: GOWLING LAFLEUR HENDERSON LLP
(74) Co-agent:
(45) Délivré: 1991-03-12
(22) Date de dépôt: 1987-01-27
Licence disponible: S.O.
(25) Langue des documents déposés: Anglais

Traité de coopération en matière de brevets (PCT): Non

(30) Données de priorité de la demande:
Numéro de la demande Pays / territoire Date
825,404 Etats-Unis d'Amérique 1986-02-03

Abrégés

Abrégé anglais






AUTOMATIC CHILLED WATER SETPOINT TEMPERATURE
CONTROL USING RETURN CHILLED WATER TEMPERATURE
ABSTRACT OF THE DISCLOSURE
A control system for controlling the entering chilled water
temperature of a refrigeration system at a selected setpoint.
A microcomputer system receives electrical input signals
indicating of an operator selected entering chilled water
temperature setpoint and refrigeration system operating
parameters indicative of an operator selected entering chilled water
The microcomputer processes these input signals to generate a
leaving chilled water temperature control point which is a
function of the entering chilled water temperature setpoint
and the temperature drop across the chiller.

Revendications

Note : Les revendications sont présentées dans la langue officielle dans laquelle elles ont été soumises.





12

CLAIMS

What is claimed is:
1. A capacity control system for a refrigeration
system of the type which includes an evaporator wherein a
refrigerant absorbs heat from a heat transfer medium passing
therethrough, comprising:
means for generating a setpoint signal correspond-
ing to a selected fixed setpoint temperature for the heat
transfer medium entering the evaporator;
means for generating a first control signal which
is a function of the temperature of the heat transfer medium
entering the evaporator;
means for generating a second control signal which
is a function of the temperature of the heat transfer medium
leaving the evaporator; and
processor means for receiving said setpoint signal,
and said first and second control signals for processing the
received signals according to preprogrammed procedures to
determine a control point temperature for the heat transfer
medium leaving the evaporator, and for generating a control
point temperature signal for controlling the load on the
evaporator.
2. A capacity control system as set forth in
claim 1 wherein said processor means determines said control
point temperature in proportion to the difference between
said selected fixed setpoint temperature and a difference in
temperature of the heat transfer medium across the
evaporator.
3. A method of generating a leaving chilled fluid
temperature control point for a refrigeration system having
an evaporator wherein a refrigerant absorbs heat from the
chilled fluid passing therethrough, which comprises:



13
generating a temperature setpoint signal corre-
sponding to a desired entering chilled fluid temperature;
generating a first temperature signal corresponding
to actual entering chilled fluid temperature;
generating a second temperature signal correspond-
ing to actual leaving chilled fluid temperature; and
generating a leaving chilled fluid temperature
control point as a function of said setpoint, said first
temperature, and said second temperature signals.
4. A method as set forth in claim 3 wherein said
generated leaving chilled fluid temperature control point is
in proportion to the difference of said temperature setpoint
signal and, the difference between said first and said second
temperature signals.
5. In a refrigeration system having a centrifugal
compressor, an evaporator, a liquid heat exchanger in the
evaporator, and a condenser, a method of controlling the
liquid entering the heat exchanger at a predetermined
setpoint temperature comprising the steps of:
sensing the temperature of the liquid entering the
heat exchanger;
sensing the temperature of the liquid leaving the
heat exchanger;
producing a control point temperature signal for
the liquid leaving the heat exchanger that is a function of
the predetermined setpoint temperature and said temperatures
of the liquid entering and leaving the heat exchanger; and
varying the capacity of the liquid heat exchanger
in response to the deviation between the temperature of the
liquid leaving the heat exchanger and the produced control
point temperature.
6. A method controlling the liquid entering
the heat exchanger at a predetermined setpoint temperature as


14
set forth in claim 5 wherein the step of producing a control
point temperature signal includes the step of producing said
control point temperature signal in proportion to the differ-
ence between (a) the predetermined setpoint temperature of
the liquid entering the heat exchanger, and (b) the differ-
ence between the sensed temperature of the entering the heat
exchanger and the sensed temperature of the liquid leaving
the heat exchanger.

Description

Note : Les descriptions sont présentées dans la langue officielle dans laquelle elles ont été soumises.


J

~ ERATIJRE
CO~TROL USING 3~ETURN CHILLED WATEP~ TEMPERATU:RE
.
Baok~uund o~ the Invention
The ~res~nt inven~i~n r~lates to ~ethod~ of.~perating and
conkrDl rystEm~.for refrigeratiDn ~yst~ms and, more particu-
larly, to ~ethod~ of op~rati~g and con*rol systems for
pacity :control devices, such as com~ressor ~nlet ~uide
vanes,:in centrifugal vapoI.cDmpr~ssion ~efr.igeration ~ystem~
where~y a predeteImin~d e~tP~ingise~poi~ ~0mperature is
-~i~tained at ~he.chiller.

-~enerally9 r~rigeratIGn-systems include an evaporat~r Dr
.~ooler/chiller, a compr~ssor, and a condenser.. Usually, a
heat transfer fl~id is circulated through tubing in the
evaporator thereby ~orming a heat transfer coil in the
evapDrator to ~ransfer h~at fr~ the h~at transfer fluid
flowing~.throu~jh :~he ~u~ing to:re~ri~rant.in ~he ~vaporator.
The heat ~ransfer~ fluid -chilled in-~the tubirlg in the evapora-
~r is-~ormally ~at~r ~r glycol ~hich is.circulated ~o a
r~mote location t~ satisfy a ref~igeration load. The re.rig-
er~n~ in thc ev~porato~v~porates as it absorbs he~t.fxom
the heat traTIsfer.:fluid flowing ~roug~i-the ~ing in the
evapo~ator, and. *h comp:ressor o~erates to extrac~ ~his
25 refrig~2nt vap~r from~.~e evapor~tor, ~to comp:~es~ .this
r~fri~seTan~ va~r9. and to discha~ge the. ~ompl~ssed- vapor *o
: ~he c~ndenser. .In th~- con~enser, the ~l~friger~Lnt va~or is
; conden~ed ~nd deliYered ~c~c to ~he evaporator where the
-1 ref~ig~la~ion cycl~ ~Pgi~s agai~.
T ~ maximiz~ o~ r~ting e:Eficiency1 it .i~ d~sir~3~1~ tc~ ~atc~
am~mt ~ w~sk-~dDne ~ e.~resa~I *o ~hE~ wo~k.-ne~d
-- *o sati~:~y.-the r~ atiDn 1l~2rd- placæd ~m t~e: Terig~tion
syst~m. .C~nly, thl~ s .~one ~y capa~i:ty c~n~rol ~ans
3~ which~ adjust the :~mount t3:~ refri~erant vapor fl~wing thrnugh
- t~e compre~sQr. ~Ehe capacity cQ~trol ~nea~ may be a ~evice

1.3~3

- such as guide var.es which are positioned between the compres- !
.60r and the evaporator which m~.between ~ fully.open and a
:Eully closed posi~ion in riesponse to the t~mperature of the
. chilled heat trans~er fluid leaving t~e coil-in the eva~ora-
:tor Wh~n the-.-evapDrator chilled heat trans~er.fl~id temper-
atuTe~falls, indicating a-reduction in ~efri~eraticn load on
the.refrigeration syste~, the guide vanes move *oward their
losed position, decreasing t~le amount of refrigerant vapor
fl~wi~g thro~gh the compT~ssor. This decreases the amount of
wor~ that ~t be done by.the c~mpresso~ there~y decreasing
the ~mount.o~.~nergy ne~:ded to operateithe refrige~ation
system.: At ~e samei tim~i, thi~s hai~ t.~e ieffect o~:.increasing
the tempera*ure of the chilled heat.transfer ~luid leaving
the.evaporator. I7~ contrast, when the tempe~atur~ of the
1~ leavin~ chilled he~t transfer ~l~id.ri-ses, i~dicating an
increase in load on the refrigeration system, ~he guide vanes
move toward ~iir:ully open pos~ion.~.~his-increases the
amount of vapor fl~ing-through the c~mpreS~oT and.~he
compressor does more work theTeby decreasing the-t~mperature
2~ Df.the ehilled hez~ transfer ~luid leavin~ the ~vaporator ~nd
- allowin~ th~ refrigeration system to respond to the increased
:re~igeration load. In-~his manner~.the c~mpressor operates
to maintain the temperature of ~he chilled heat transfer
fluid leaving the-evapo~ r at,~r.wit~in a certain. range
.2~ of, a se~ p~in~ tempera~ure.

~ny di~feTent.c~pacity rDntrol.systems~are known ~Dr run-
...trolling a.refrigeratiDn syst~m in the manner described
`ahove. For e~ample,.one ~uch control system,. a mod~l
~P-8142-024`Electronic Chiller ContTol ~vaila~le from ~he
~r~er-Colma~ C~mpany ~v~n~ a plac~ ~f;~usin~ss in Ro~kford,
IIlinois, ad~sts a-capac~ d~vi~e in~a refriger~L-
n syst~ Ps.a functi-on ~ d vi ~iDn .~ l~avin~ eY~po-
sa*or chille~l- water .tem~erat~ ~rom a` ~desi~e~ set point
3~ t~mperature. ~hen the evapo~ator chi~led wate~ tempe~ature~
de~i~tes fT~m~thP~selected set point ~emperature ~y a

3~33

~redetermined ~mount the capacity control device is cuntinu-
ously adiu~ted by an actuator whi~h is cuntinuously energized
by a stream of electrical p~l6es s~pplied to the actuator.

5 Cercain energy ~nanag~men~ sy~tems ~ake it desirable to
maintain a constant enteTi~ chilled water tempeTature and
-.let the leavin~ ~hilled water t~mperature "float" Qr seek its
,own eq~ili~rium tempera~ure a~ the load varies. ~his is the
~ ~ reveT~e Df conv~tional ~rior art chilled wat~r temperature
'.eont~ y~t~ms. ~oweves,. co~trolling chiller caparity based
solely on a deviation of e~ter.i~g.chilled wa ~r t~m~erature
.from.a fi~ed e~t~ring chilled1w~ter ~e~peTatu~e setpoint, in
.a manner analo~ous to ~ha~ used in .priox.l~aving chilled
'.water te~.perature control systems causes exagge~ated vane
movements:~ith little:s~bility in the!~ys~2m, ~eca~6e a
substantial time delay e~ists ~etween capacity ~hanges made
al.~he ~chiller.and the res~lting.temperat~re chan~es sensed
.in the wat~r ~nt~ring the chiller. ~.hi~ .ti~e lag.in.the
WateT 1ODP cause-s the-c~ntrol-~o ~v~rcvmpensa~e and the
~Q ~esult is cantrol instability and exces~ive te~pera~ur~
oscill~tion.

Thus, th~e ~xist~ a ne~d to develop cap-acity.~ontrol tech-
.niques f~r chillers whi~h maint~in a cDn~tan~ ~ntering
:~hilled ~a~..te~pera~ur~ and-w~l~h minInize ~he ~isadvan~ag-
~s.of controlling'~hill~ cap~city in-r~spons~ to.leaving
chilled.water.temp~rature-o~ devia~ion~f entering chille~
- water tFmp~a~ure.from^~ fiæe~ setpoint..
-
30 Summary of the Invention
- T~r~fore, i~ n o~i~ct..... ~f ~he pre~ent inv~nti~m~to
^ ~ovid~-a..~im~ .f~i~i~n~-2nd ~ffe~ti~e.~ic~c~m~te~
- sys.~m-fDr :cv~trQlling ~he:cap~ity ~f ~ refrig~ra~ion ~ystem
;in ~on~ ~D.~en~er~ng wat~r.~pQin~:tem~ ux~.


393

It i~ ~nother object of the present invention ~o p~ovide an
easily programmable microcom~u~er system for controlling the
capacity of a ~efrigera~i~n sys~em by gene~ating a leaving
::chilled water control point so ~s to ~rovide a desired
. entering chilled wat~ 3etpoint ~mpera~uT~.

It is still an~t~er o~j~ct of the present-inven~i~n to
proYide a control sche~e for controlling the capacity of a
-refrige~ation system ~at is ~er~ious to changes in chiller
10 i. water flow rate~

~hese and o~her ~jects.of the present invEn~i~n are A~tained
by a capacity control ~ystem for a refrigeration system
co~prising means::for generating a setpoint signal corre~pond-
ing to a selected setpoint temperature~for the hat transfermedium entering the evaporator ~the setpo-int tFmperatU~e is a
~alue selected by an -~perator ~D~ inpu~d lnto the mirr~p~o
~SB or);^~earls ~r generating~a first co~t~ ignal..~hich is
a functior~ of the temreraturP-o~ the hea~ transfe~ ~nedium
en~eTing th~ evaporato~,- means for generating a.~econd
control si~nal which is a func~ion of the ~emperature of the
~e2t t~anæfer me~tium l~a~ving ~the ev~poTator, and processor
- means for' Teceiving said setpoint ~ignal, and said firl;t and
æecond c~m~rol signals :for p~:~cessing th~- received si~nals
25 according --to ~prog~ammed ~locedllr~s ~D det2~1ine ! a .control
- :point t~perature fDr the hea~ tr~ilsfe~medium .1~ vi~g the
e~7~porator (the ~:ont~ol poi~t temperatu~e is -a; value generat-
ed ~y the mi~op~oc~ssor al~d i~ used to cont~ol the lo~d,
- e.g. -~y~ positioning.~he gllide vanes), and for gene~ating an
30 o~ control -si~;nal I'or cont~ollin~ the capacity ~f.~he
rhille~ i~ ~esponse to ~ ollt~ C ontrDI signal.

Ih~:p~o~so~means, a micro~mputer,~ t~Imine~st~ leavi~g
~hilled-w~r~t~mp~satllre ~on~o~ i~t using A`~he e~t~in~
3~ c~illed wat~r se~point and the t~mperature drop acT~ss.~he

3~3


.~vaporator. This c~ntrol feature is stated mathematieally as
follows:

LWCP = ~P - ~T )
Wh~re;
. ~ Ti ~o

. and wher~;

I,WCP ifi the.leavrng.e~illed wa~eT ~mp~rature eontrol
poi~t,
`. EWSP i~:the ente~ng c~illed ~ater t~mperature setpoin~,
Ti is the water..t~mperature enteri.ng the:e~p~rat~T, and
To is t~e water t~mperatUre l~aviDg ~he ~vaporator.
. :
By selecting a desired BetpOint or the enteri~s chilled
water, .o~erA~:io~ of tl~e capacity co~:rol dev~ce may be
easily, efficiently, and ~Eec~lv~ily .tailored l:~.mee~ i
sp~`~ific job requirements~ af a par~icular jo~ -appli~ati~n far
20 ~he.ref~igeration syst~m ~y ~stah~i~hi~ .~he leaving chillec J
~a~er te~perature control point.

;Brief Descri~ion of t~;ie Drawin~s
i St:ill oi~her ob3ect~: an~iadvar~tages o- ~hæ pr~?sent inven~tion
25 will be c.pp~:r~t ~from t~e ~ foll~ing .de~ailed des~riptir~n of
-the pre~ t ~reIltion i~ cDnjLm~ i~n ~i~h the. accompanying
dsawings, in whieh th~ ~eferenc~eTals designate li~ce or
. correspondin~-part~ thT~ Lou~ :the ~ame, In ~ish:
.
3 u . Figure ~: is a` schema~ismillustra~i~ .of a ce~ rifugal -va~or
- - - .. c~mpre~;sion :r~frigera~ y~t~m ~i~:h. a .~on1:rol sys~m. for
~ . v~r~ng ~ apacity~ ~ r~fri~ ~Lt3~n 3~st~m acrl~di~s t:o
h~ prin~ip1~ of . ~:h~ .. ;~s4nt i~x5~II~ icm7';' ~nd - I


, ~ ,", . . : i




. .; .

~8~ 3

~igure ~ is a graph of entering and lea~ing chilled water
tempera~re as a function of load for a typical chiller
system.

Referring to Figure 1, a~,~apor.compressi~n re~ig~ration
0.` 6~'StEm 1 iS shown having a cen~i~gal ccmpress~r 2 with a
corltrol systFm 3 for varying the c~pacity of the refrigera~
. tio~-~ystem 1 accoTding^~o the principles of the present
10 ,.invention. ~s shown i~ ~igur~ 1, the ref~igera~ion system 1
.includes a c~nden~er 4, an evaporator 5 and ~ poppet valve 6.
.In operatiDn, c~mpress~d~gaseous -refrigeT~nt,,is.discharged
from t~e cDnrp~essor 2 ,~through c~ressor~ discharge lin~ 7 to
the condenser 4 wherein the gas~us reriger~nt.is condGnsed
15 : by r~la~ivPly cool cDndensing wa~er flowlng through tubing 8
in the condenser 4. .'The condensed liquid refrigerant rom
the condenser 4 pad~es ~hrough ~he poppet valve 6, which
forms,~,liquid,s~al.-..t~,keep cQ~de~r vapo~ from ~nte~ing.~he
--- evaporator and ~o ~intain ~he pre~sur-P.difference between
~0 the condens, r,and the evaporator, in rEfrig2~ant line 9 *o
evapora~or:5. Th~ uid refrigerant in the evaporator 5 is
~f -`evaporated to cool ~ hea~.tran~fer.~luid, such,as water or
~. glycoI-, flowing through tubing 10 in the evapora~or 5. This
~.chilled h~a~ transfer ~fluid is: use~ ~o cool a bui:L~ling or is
25 used fo- :o~:~er .sLlch purposes. ~e gas~ous refri~e~ant fro
^ the evapo~tor ~ flaw6 ~rough :com~essr~ suc~ion: :lins~
- back i~ com~Te~sor ~ under the control Df compr~ssDr .inlet
- . guide^ sranes 12. ~ gaseous refrig ra~ enterin~- the com-
pressor . 2 through the .guid~ .vanes 12- is compressed ~y ~he
3D. compressor 2 .and dis~har~;ed fram:*h~-c~mpT~ssor 2 ~rough ~he
co~ps~ssor ~isch~r~se line 7 .~:o com~lete the - re:~rigeration
'~; CyC~ i8 ~.~frig~ativn~ ycle i~:ro~im~ y r~ted
.; dlIrin~; nDrmal Dper~ion of the rPfrig~ra:tion ~;y~;tem 1.

: 3~i The compresso~- inl~e~ guide :~anes 1~ are~ op~ened and clos{~d ~y ~ I
a gilide vane ac~u~tor 14 c~ntroll d :~ the capa~:i~y c~m~Tol



system 3 which comprises a syste~ inter~ace board 16l a
- -proc~s~or board 17, a set point and dis~lay b~a~d 18, and an
analog/digi~al c~nverter 19.. Also, te~eratur~ sensor l3 ~or
s~nsing the tem~era~ure of ~h~ ~eat transfer fluid leaving
the ~v~poTatQ~ -~ thr~ugh the.t~L~g 10 an~ t~mperature ~ens~r
15 for ~ensing~he ~emperature of the heat transfer fluid
enteTi2ng the evaporatar 5 ~hrough the ~ubi~g lO, are con-
: nected by electrical lines 20 and 2~ directly to the A/D
:~ conve~ter 19.
10Pre~erablv9 the ~æmperature ~,e~lsors 13 and l~are t~mperature
respon~ive r~sistane~ devices ~uch as a ~hermlstor6 having
their sensing portions located in` the heat transfer fl~id in
the ~u~ing lO in the evaporator ~ with their.resistances
1~ monito~ed by the.AlD,conver*er, ~s shown in.~i~ure 1. Of
cours4 ~ as will be r~adily apparent to one o~ oTdinary skill
- in t~e art to ~hich the~present in~ntion peItainsl--the
tempesat~re sen~ors. 13 and 1~ ~ay be any of a vari~ty of
temperature sensors sui~able.for ~ererating a~signal-indic2-
20~ ~ive o~ the temperature o~ t~e heat transfe~ ~luid in the
tubing 10 in th~ e~apora~or ~ and for supplying these gener- i
ated- signals tc~th~ AID con~erter.l9.

,: Th~rocessoT 'Doald 17 may ~e any slevic~ or. combin tion of
,5 . de~ es,. c~pa~le o-E rec~iving ~ ~lurality o~.: input signal~,
~roc~ssing t~ :rg~ceiv~d :inpllt -s ignalB aoc o~ding to
prep~Dgrammed prDcedllres, ~d prod~cing. d~ired o~l~Ut
. contTol signals- ill:. r~pons~` to ~he- Tec~eived and p~ocessed
input signals, i~^a ~anner ~accord~ng~ to the principles of- the
30 pTes~nt iIl~entioIl. Ft)r e:Eample, ~-processor b~ld l7 m~
co~pri~e ~ microcsm~ut~r, su~ a~ ~L ~odel .8D31 micIoeomputer
svail~bl~-- f~Dm Inl~ ion ~ch ha~ la~ Qf bu~
. nes~ at S~nt2~ Cla~

` 3 ~ Also, pref~ra~ly, the AID -ronv~ter 19 i~3 -~ duaI :s~ope A/D
co~v~rter~whi~h ~;~all ~roces~ n~ g-illputs and ~sich is

L3~

suitable fo~ u~e with the processor board 17. Also, it
should be no~ed tha~, although the A/D ~onverter 19 i~ shown
as a sepaT~te module in Figure l, thi~ A/D converter 19 may
~e physically pa~ of ~he ~rocessor board 17~in an actu~l
5 - cap~ity c~ol sys~2m 3.

F~rtheT, ~r~ferably, the set point and di~play ~ard 1~
-cDrprises a ~isual display, includingt ~or example, light
emit~ing diodes (LED'~) or :liqui.d ~ys~al disp~ay (LCD'~)
1~ :devices forming a ~Llt~-digit display which is under the
cun~rol of the processor board.l7.. Al~o, th~ ~et p~int -and
. display board 18 .includes a device, such as- a key pad which
se~es a~s a da~a entry ~ort as well as a programming tool~
- for en~ering the te~pe~a~ure setpoint of the,rhllled water
1~ entering-~he Evapor tor ~ through the ~aporator chilled -~
wa~er tu~ing.lG.

~till-furth~r, p~efera~ly, the sy~tem in~r~ace ~oar.d 16
includes at least Dr.e s~itching device~ ~uch--as a ~del
S~-140 ~riac availa~le from G~neTal El~ctric, ~rp. which has
.. a plac~ of business at Auburn, New York~ which is used as a
-~witching element ~or~.c~ntrolli~g:~a su~ply o~ elect~ical
pow2r (not shown) thrcugh electrical lines ~-1 $~ the guide
. ~ne ~ctua~or-14.:.~The t~iac switches on the sys~em interf~ce
boa~d 16 a~ contr~lled in~resp~nse to ~Gntrol ~i~nals
:- rer~i~ed ~y~the-.t~iac s~itche~-~ro~^~he-pr~ces~r ~ard 17.
In *his manner, elec~rical power iS ~u~lied th~ough the
eleetrical lines 21.~o the ~uide vane.~ctuator 14 under
c~n~rol of t~e processor:~ard 17 to ~perat~ t~e-g~de vane
30 actllator ~ e ma~rnGr.-aco~rding.t o ~h~prin~ipl~s of t~e
pT~B~nt i~vention ~hich i~ descri~ed i~ tail below. Of
- c~n~.~e7 - aB~ eadily.-~p~ar~D~-to-~ne- D ~rdinaTy skill
in ~he art to whi~h ~he~res~nt-inven~ion ~e~ains,~witchi~g
- devi~s other ~h~n tri~ s~itc~e~ ~ay ~e-~ d in-.. r~ntro~lin~ I
3~ poweT~flow ~rom ~he pOW~T ~uppl~.(not sh~wn) thr~ugh ~h~
!

3~33

electrical lines 21 to the guide vane actuator 14 in response.
to output con~Tol signals from the proc~ssor board 17.

Ihe ~uide vane actuator 14 may ~e any device sui*able for
~riving the guid~ v~nes 12 ~ow~rd either their open or closed
position in response to el~trical power signals rec~ived via
- electrical lines ? 1 . For example, ~he guide vane actuator 14
- ~ay be an electric motor, such as a model~.MC-351 mDtor
-~vailzble.f~m the-~ar~ Colm2m C~mpany ha~ing a pla~ç of
~usin~ss in ~ockfard, Illinois" for driv~ng. the ~uide vanes
12. t~ward ~ithe~ their open Dr ~l~sed posi~ion de~Fnding on
whic-h one.of two-~riac switches ~n the fiyfitem int~Tf~ce board
l& is actua~ed.in TespOnse to. CDntrOl signals received ~y the
triac switches fr~m the proce~s~r~board.17. .The guide:vane
~15 actuatQr 14 drives.the.:gui~e van~ 12 t~ward ~ither their
fully open or fully closed position at a con~tant~ fixed rate
only.during that portion of a ~el~cted ~ase.time i~terv~l
during which:the ~ppropriate.traic s~-itch o~..~he.system
int~rface board 1~ is ac~uated.
2D
Re$erring now to ~igure 2, a sDlid straight-line hori~on~al
- -curve~A is sh~wn whic~ represents the entering.chilled w~ex
- temperature se~p~int that i~ de~iTed tG ~e ~aint~ined by ~he
~ ~efrig~x~ion syatem of the pres~nt inv~ntion. .This setpoint
25 -iis arbi~rary a~d~. is-.en~red .in~o -the setp~int and displaY.
oa~d by the operatQre~y-way D~ the ~y pad. d~y ~aintainir.
a:fixe~ enterIng chllled wa~e~ tempeTature the ~p~rat~r may
redu~e-~nergy.c~nsumptiGn d~rlng cer.~in load condi~ions,
. partic~larly ~ low loads.; ~hæ leaving chill~d-water con~rol
30~. point ~f the ~esent:inven~iDn, 2S shown by .~he sDli~ sloped
- :. li~e curv~ B7-~pres~nt~ the.. contrDl pDin~ a~ ~hich the
le~vi~g ~hiIl~d w~t~r;is ~e~at~d~ur~ng.~ny.l~ d~nditiDn
:. w~ e setp~t of;c~rve A. '~2 v~r~ic l axi~.~f Figur~ 2
-~s the~ temper~ture o~ ~he Ghilled ~a~er.-;-enterin~ or leaving
3~ the e~pora~r~ The horizontal a~is of Figure 2.is.~he.loa~ !
. .

3~3


on the refrigeration sys~em. An arbitrary val~e of 10F was
chosen as evapor~tor
~T at full load and coIles~nding~Yalu~s of ~T at various
loads a~e shown.
In Figure 2, the curve labeled ~ ~llustrates an arbitrary
fi~d setpDi~t for the ~ntering chill~d.~ater temperature.
! Thus, in this example, ~he opel-a*or desiTes the refTigeratiol-
~yst~m to~control the te~p~ratllre of the ent ring chilled
water at ~F.

The dashed s ~ ight-line ho~izontal ~ur~ C reprYsents ~he
: fi~ed leaving chilled wat~r ten~er~ture setpoint Df the pTior
art, while the dashed sloped line Curve.D represents the
`1~ floatin~ en*~ring chilled water te~per~ure of the prior art.

Once ~ predetermined enteri~ chilled ~a~er.set~o~nt is
selected, the l~aving ~hill~d water temp~x~t~re .control p~int
i5 calculated by the ~icroprocessor, and is-perio~ically
.,0 updated e.~. once ev~xy ~ive- ~econds, to e~sure that:the
leaving chilled water.temper~ture is t~ correct value for
- ~he ~resen~.load. If hDweuer, t~ a* changest. for example
a load would, over a period of time, decrease ~r~m 50% to
10~, *~e l~aving chill-ed wat~r ~mpera~ure con*rDl point
2~ would incr~àse fr~ 50~-.to:54~ hi6-incr~ase ~ill b~ d~ne
- at a`gradual Ia~e s~ch a~ ~.12~-d~gre~.e-~er minute. ~Thus,
: the~ac~ual leaving.chill~d ~ater temperatur~ sensed~ he
- sEn-sor 13 w~uld, instantaneousIy, still indicate '~D~ while
- the leaving chilled wat~r temperature ~Dnt~ol-~oin~.w~uld be
calling for A leaving chill d water slightlY abDv~Q~.
Th~,.~ d~ia~ion would-2xifit.~ h~ ac~al leaving
;chi~ d wa~er ~mperatur~nd-th~ Ying `~ ~at~r
tgm~ature. c~ntrol ~ and :th~ devi~tiD~ is i~pu~ted .to
~he sy~em intf~rf ce-~ad:which ~ he ~aid~-vane
~35 - actuatDr 14 ~ ~o~-e~the gu}de ~ane~ 12:toward th~ir.closed
po~ition untit-~he actuàl temper~ur~ ~ the leaving chilled

~8~.3~3::~
11

water is equal to the l~aving chilled wa~er temperature
cont~ol point.

In this manner th~ chill~eT will make a ~mooth t~ansition ~rom
a ~iven load lev~l to a~D~r ~e~au~e ~he. leaving chilled
water temperature sensursImmed-iately det~cts the water
t~mperature change caused by the altera~ion in guide vane
p~sition. Thus throu~h the use of the g~nerated control
~oint, ~he desired enterlng chiilled wate~ t~pe~ature is
~ain~ain~d during~he tran~ition.

~rther, it shDuld be n~te~ that the ~hilled w~t~ flow rate
~ay vary without changir.~ *he control scheme, sin~e the
leaving.chilled water tempe~ture contTol point is only a
function of t~ entering chilled.water ~mperat~re setpoin~
and the water ~emperature enterin~ and leaving the
evaporator.

While this invention has been des~ ed ~nth ~efe~ence to a
particular em~odiment discl~sed h~reinl it-is not confined to
the d~tails s~t.forth h~rein.and this.application is i~tended
to cov~r anv mDdifica~ions or c~ es ~s may come wit~in the
scope of the i~ention.

Dessin représentatif
Une figure unique qui représente un dessin illustrant l'invention.
États administratifs

Pour une meilleure compréhension de l'état de la demande ou brevet qui figure sur cette page, la rubrique Mise en garde , et les descriptions de Brevet , États administratifs , Taxes périodiques et Historique des paiements devraient être consultées.

États administratifs

Titre Date
Date de délivrance prévu 1991-03-12
(22) Dépôt 1987-01-27
(45) Délivré 1991-03-12
Expiré 2008-03-12

Historique d'abandonnement

Il n'y a pas d'historique d'abandonnement

Historique des paiements

Type de taxes Anniversaire Échéance Montant payé Date payée
Le dépôt d'une demande de brevet 0,00 $ 1987-01-27
Enregistrement de documents 0,00 $ 1987-03-25
Taxe de maintien en état - brevet - ancienne loi 2 1993-03-12 100,00 $ 1993-02-08
Taxe de maintien en état - brevet - ancienne loi 3 1994-03-14 100,00 $ 1994-02-22
Taxe de maintien en état - brevet - ancienne loi 4 1995-03-13 100,00 $ 1995-02-17
Taxe de maintien en état - brevet - ancienne loi 5 1996-03-12 150,00 $ 1996-02-20
Taxe de maintien en état - brevet - ancienne loi 6 1997-03-12 150,00 $ 1997-02-17
Taxe de maintien en état - brevet - ancienne loi 7 1998-03-12 150,00 $ 1998-02-19
Taxe de maintien en état - brevet - ancienne loi 8 1999-03-12 150,00 $ 1999-02-17
Taxe de maintien en état - brevet - ancienne loi 9 2000-03-13 150,00 $ 2000-02-17
Taxe de maintien en état - brevet - ancienne loi 10 2001-03-12 400,00 $ 2001-05-22
Taxe de maintien en état - brevet - ancienne loi 11 2002-03-12 200,00 $ 2002-03-01
Taxe de maintien en état - brevet - ancienne loi 12 2003-03-12 200,00 $ 2003-02-26
Taxe de maintien en état - brevet - ancienne loi 13 2004-03-12 250,00 $ 2004-05-25
Expiré 2019 - Taxe de paiement en souffrance, selon le par. 3.1(1) 2004-07-20 50,00 $ 2004-05-25
Taxe de maintien en état - brevet - ancienne loi 14 2005-03-14 250,00 $ 2005-01-31
Taxe de maintien en état - brevet - ancienne loi 15 2006-03-13 450,00 $ 2006-02-06
Taxe de maintien en état - brevet - ancienne loi 16 2007-03-12 450,00 $ 2007-02-05
Titulaires au dossier

Les titulaires actuels et antérieures au dossier sont affichés en ordre alphabétique.

Titulaires actuels au dossier
CARRIER CORPORATION
Titulaires antérieures au dossier
ZINSMEYER, THOMAS M.
Les propriétaires antérieurs qui ne figurent pas dans la liste des « Propriétaires au dossier » apparaîtront dans d'autres documents au dossier.
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Description du
Document 
Date
(yyyy-mm-dd) 
Nombre de pages   Taille de l'image (Ko) 
Dessins représentatifs 2002-03-18 1 11
Dessins 1993-10-19 2 40
Revendications 1993-10-19 3 120
Abrégé 1993-10-19 1 27
Page couverture 1993-10-19 1 16
Description 1993-10-19 11 615
Correspondance 2004-05-17 1 11
Taxes 1997-02-17 1 71
Taxes 1996-02-20 1 66
Taxes 1995-02-17 1 71
Taxes 1994-02-22 1 76
Taxes 1993-02-08 1 55