Direct FiredLiBr Absorption Chiller/Heater

Steam Operated LiBr Absorption Chiller

Flue Gas OperatedLiBr Absorption Chiller/Heater

Hot Water OperatedLiBr Absorption Chiller

China Well-known Trade MarkChina Famous Brand

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Flu

e G

as T

ype L

ithiu

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rom

ide A

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tion C

hiller/

heate

r ········································································ 1

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as typ

e a

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5

At

least

till to

day

we s

till only

have

one e

arth for

livin

g,

but

ob

vious

clim

ate

change in

recent ye

ars

linke

d to g

reenhouse g

as e

mis

sio

n

rem

ind

s h

um

an b

ein

g that im

med

iate

measure

s s

hould

be take

n to

pro

tect

our

pla

net

well.

Fro

m K

yoto

Pro

tocol,

Cop

enhagen A

gre

e-

ment

to C

ancun C

limate

Confe

rence t

he w

orld

has b

een w

ork

ing

hard

to p

rom

ote

ap

plic

atio

ns o

f energ

y savi

ng s

olu

tions a

nd

gre

en

energ

y so that re

duce e

mis

sio

n o

f gre

enhouse g

as.

Actin

g a

s o

ne o

f effectiv

e s

olu

tions f

or

this

purp

ose,

Lith

ium

Bro

-

mid

e

Ab

sorp

tion

Coolin

g

technolo

gy

ad

op

ts

non-v

ola

tiliz

atio

n,

non-d

ete

riora

tion a

nd

pollu

tion-f

ree s

olu

tion o

f Lith

ium

Bro

mid

e a

s

work

ing m

ed

ium

, re

cove

r w

aste

heat

exi

ste

d w

idely

in i

nd

ustria

l

and

com

merc

ial a

rea a

s m

ajo

r d

rivin

g s

ourc

e for

chilled

wate

r p

ro-

ductio

n,

not only

help

ing to r

ais

e e

fficie

ncy

of energ

y consum

ptio

n

but als

o r

ed

ucin

g e

mis

sio

n s

ignifi

cantly

.

Sin

ce f

ound

atio

n i

n 1

98

2,

in 2

8 y

ears

Shuanglia

ng E

co-E

nerg

y

Sys

tem

s C

o.,

Ltd

have

been d

evo

ting in s

up

ply

ing s

olu

tions a

nd

pro

ducts

of

energ

y savi

ng and

envi

ronm

enta

l p

rote

ctio

n b

ased

on L

ithiu

m B

rom

ide A

bsorp

tion C

hiller/

Heat

Pum

p o

n b

elo

w m

ile-

sto

nes,

� )�*+,-

pro

duced

the fi

rst LiB

r ab

sorp

tion c

hiller

� )�*++!

dra

fted

the C

hin

ese n

atio

nal sta

nd

ard

for

LiB

r ab

sorp

-

tion c

hiller

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set

up

the o

nly

one s

tate

-leve

l ente

rpris

e t

echnolo

gy

cente

r fo

r ab

sorp

tion c

oolin

g technolo

gy

in C

hin

a

� )�!//*

the o

nly

one P

ostd

octo

ral

Scie

ntifi

c R

esearc

h W

ork

Sta

tion w

as s

et up

� )�!//0

becam

e t

he o

nly

one p

ub

lic l

iste

d c

om

pany

in L

iBr

ab

sorp

tion c

hiller

ind

ustry

of C

hin

a in

sto

ck

exc

hange m

ark

et.

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Insta

lled

the la

rgest LiB

r A

bsorp

tion H

eat P

um

p p

roje

ct

of th

e w

orld

in C

hin

a

� )�!/*/

deve

loped t

he fi

rst

unit

of

trip

le e

ffect

dire

ct

fired L

iBr

ab

sorp

tion c

hiller

in C

hin

a

Gre

en h

eart,

Gre

en f

utu

re is s

logan t

o r

ep

resent

targ

et

of

Shuan-

glia

ng,

als

o ind

icate

s r

esp

onsib

ility

we s

hall

take

, so w

e n

ot

only

deve

lop

Lib

r ab

sorp

tion te

chnolo

gy

for

coolin

g b

ut

als

o sp

read

its a

pplic

atio

n t

o h

eatin

g b

y heat

pum

p,

not

only

adopt

com

mon

hot

wate

r and

ste

am

to d

rive c

hiller

but

als

o e

xpand

driv

ing h

eat

sourc

e t

o w

aste

heat

and

gre

en e

nerg

y sola

r and

geoth

erm

al

, not

only

pla

y ro

le a

s lead

ing a

bsorp

tion c

hiller

manufa

ctu

rer, b

ut

als

o u

pgra

de to c

om

pre

hensiv

e s

olu

tion p

rovi

der of energ

y savi

ng,

fresh w

ate

r savi

ng a

nd

pro

ducin

g b

y ab

sorp

tion c

hiller/

heat

pum

p

and

new

deve

lop

ed

air

coole

d c

ond

enser, s

eaw

ate

r d

esalin

atio

n

sys

tem

s, pro

vide e

conom

ically

feasib

le s

olu

tions to h

elp

more

and

more

com

panie

s t

o r

ealiz

e t

heir

resp

onsib

ilitie

s o

n e

nerg

y savi

ng

and

em

issio

n r

ed

uctio

n.

In p

ast

25

years

, S

huanglia

ng p

rovi

ded

the c

om

munity

with

ove

r

20

,00

0 u

nits

of

energ

y savi

ng e

quip

ments

, b

rought

not

only

sig

-

nifi

cant savi

ngs in

ele

ctric

ity s

up

ply, th

e e

quiv

ale

nt of savi

ng in

vest-

ment

on r

are

15×

60

0M

W t

herm

al p

ow

er

pla

nts

, b

ut

als

o a

nnual

savi

ngs o

f 2

2.5

millio

n t

ons o

f sta

nd

ard

coal,

em

issio

n r

ed

ucin

g

of 5

7.6

millio

n t

ons o

f C

O2 a

nd

85

,00

0 t

ons o

f S

O2,

eq

uiv

ale

nt

to

rep

lant 1

60

,00

0 h

ecta

res o

f fo

rest eve

ry y

ear.

There

’ s o

nly

one e

arth, so there

’ s a

responsib

ility

, fo

r a c

leaner and

gre

ener

earth w

e n

eed

to w

ork

togeth

er,

exp

ect our

solu

tions c

an

win

your

trust to

o..

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Shuanglia

ng c

onstructe

d t

he fi

rst

in C

hin

a a

bsorp

tion c

hiller

with

tw

o p

um

ps a

nd w

ithout

spra

y nozz

les,

whic

h e

limin

ate

s t

he r

apid

deg-

radatio

n o

f coolin

g c

apacity

. In

ord

er

to a

ttain

the a

im,

a c

hiller

with

tw

o p

um

ps a

nd w

ithout

nozz

les is m

anufa

ctu

red w

ith t

he k

now

how

,

such a

s L

eft-M

iddle

-Rig

ht

arrangem

ent

of

absorb

er-

eva

pora

tor-

absorb

er, a

bsorb

er

with

drip

pin

g p

late

s inste

ad o

f spra

y nozz

les,

whic

h

don’ t

need s

olu

tion s

pra

y pum

p. W

ith this

technolo

gy,

the c

hiller can b

e o

pera

ted for m

uch lo

nger tim

e.

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Heat

exc

hangers

are

desig

ned

with

new

tub

es a

nd

their

sup

ports,

furtherm

ore

with

new

flow

pattern

, th

at

lead

s t

o im

pro

ve h

eat

transfe

r

and

red

uce fl

ow

pre

ssure

dro

p.

These m

easure

s im

pro

ved

chiller

energ

y effi

cie

ncy

and

red

uced

fuel c

onsum

ptio

n.

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The s

pecia

l fo

rm o

f d

istrib

utio

n o

f re

frig

era

nt

by

drip

pin

g p

late

s im

pro

ves t

he w

ettin

g o

f tu

bes b

y re

frig

era

nt, f

ully

uses t

he h

eat

transfe

r

are

a,

red

uces the r

efrig

era

nt fil

m thic

kness,

incre

ases the h

eat transfe

r effects

, and

results

in im

pro

vem

ent of chiller

energ

y effi

cie

ncy

and

red

uctio

n o

f fu

el c

onsum

ptio

n.

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Ap

plic

atio

n o

f new

tub

es a

nd

their

arr

angem

ent

in e

vap

ora

tor

make

s m

ore

eve

n d

istrib

utio

n o

f heat

transfe

r effect, a

nd

thus t

o im

pro

ve

chiller

energ

y effi

cie

ncy

and

red

uce fuel c

onsum

ptio

n.

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Hig

h p

ressure

genera

tor

with

solu

tion insid

e t

ub

es a

nd

wet

back

of com

bustio

n c

ham

ber

imp

rove

s c

hiller

op

era

tion s

afe

ty,

and

red

uces

fuel c

onsum

ptio

n.

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eatin

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fficie

ncy

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nd

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rove

the o

pera

tion li

fe.

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Eva

pota

tor

tub

es a

re p

rote

cte

d f

rom

fre

ezi

ng w

ith s

uch m

easure

, as c

hiller

can s

top

coolin

g v

ery

quic

kly.

It

is r

ealiz

ed

by

inte

rrup

ttin

g

the o

pera

tion o

f re

frig

era

nt

pum

p,

if fa

ilure

of p

ow

er

or

chilled

wate

r occurs

, b

ecause r

efrig

era

nt

wate

r from

cond

enser

is c

olle

cte

d in

the

sum

p o

f eva

pora

tor, a

nd

pum

ped

to the d

ripp

ing p

late

for

dis

trib

utin

g o

ver

tub

es.

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l flow

of solu

tion in

chiller

make

s s

olu

tion far

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cry

sta

lliza

tion li

ne to im

pro

ve c

hillle

r re

liab

ility

and

sim

plif

y th

e c

ontrol o

f chiller.

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The d

irect

fired

ab

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hiller

can b

e p

urg

ed

durin

g h

eatin

g m

od

e b

y p

ioneerin

g t

echnolo

gy

to im

pro

ve t

he c

hiller

relia

bility

and im

-

pro

ves c

hiller

op

era

tion li

fe.

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DFM

technolo

gy

is o

ne o

f th

e a

dva

nced

technolo

gy

to c

ove

r th

e n

eed

s o

f

custo

mer. S

huanglia

ng m

eets

the req

uire

ments

of custo

mer b

y ze

ro d

efe

ct

and

shortest

deliv

ery

perio

d b

y D

FM

technolo

gy

and

qualit

y m

anagem

ent

sys

tem

.

Qualit

y of S

huanglia

ng p

rod

ucts

are

guara

nte

ed

by

seve

ral h

und

red

s o

f im

-

ported

eq

uip

ments

, such a

s p

lasm

a c

uttin

g m

achin

es, horiz

onta

l and

verti-

cal m

achin

e c

ente

rs,

num

eric

al c

ontrolle

d d

rillin

g a

nd m

ill c

ente

rs,

weld

ing

rob

ots

and

heliu

m le

ak

dete

cto

rs,

and

all

perform

ance test sta

nd

s.

67

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Lithiu

m b

rom

ide a

bso

rptio

n c

hiller

is o

pera

ting u

nd

er

hig

h v

acuum

, w

hic

h w

ould

be i

mp

aired

by

leakin

g o

f air i

nto

the c

hiller

and

non-c

ond

ensab

le g

ases g

enera

ted

insid

e o

f th

e c

hiller

due t

o c

orr

osio

n.

Poor

vacuum

will r

ed

uce c

hiller

coolin

g c

ap

acity

and

eve

n

incre

ase t

he c

orr

osio

n o

f m

eta

l p

art

s in c

hiller. S

o h

igh a

ir-tig

htn

ess is t

he d

ecis

ive f

acto

r to

guara

nte

e t

he q

ualit

y of

lithiu

m b

rom

ide

ab

sorp

tion c

hiller, a

nd

the k

ey

para

mete

r fo

r eva

luatio

n o

f chiller

chara

cte

ristic

s.

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��3���������&�������#����&����&����������������@

1

The c

hiller

and

its

part

s h

ave

been insp

ecte

d b

y heliu

m m

ass s

pectro leak

teste

r w

ith leakage r

ate

of 1 ×

10

-10P

a·m

3/s

, w

hic

h is 4

ord

er

low

er

than 2

.03×

10

-6P

a·m

3/s

sp

ecifi

ed

by

Jap

anese Ind

ustr

ial S

tand

ard

JIS

B8

662-1

99

4.

The r

igid

leak

teste

r ap

plie

d b

y

Shuanglia

ng is t

he o

nly

eq

uip

ment

used

in a

bsorp

tion c

hiller

ind

ustr

y in

the w

orld.

During v

isiti

ng S

huanglia

ng,

a f

am

ous a

tom

ic

exp

ert

said

, "S

huanglia

ng h

as the s

am

e le

ak

testin

g facility

as u

sed

in a

tom

ic in

dustr

y".

2 A

pate

nte

d a

uto

matic

purg

ing u

nit

is insta

lled

on t

he c

hiller

to p

urg

e o

ut

non-c

ond

ensab

le g

ases d

uring o

pera

tion e

nsuring t

he

vacuum

in the c

hiller.

'��� �&������&����������&�A���� ������:

1

The d

egra

dato

n o

f coolin

g c

ap

acity

is s

olv

ed

in the p

ossib

le w

ay;

2 H

igh r

elia

ble

op

era

tion w

ith le

ss m

ain

tenance a

nd

rep

air

cost is

guara

nte

ed;

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Data

, such a

s c

hilled

hot

wate

r outle

t te

mp

era

ture

, can b

e s

et

in a

c-

cord

ance w

ith t

he r

eq

uire

ments

to e

nsure

the o

pera

tion o

f unit

in t

he

pre

dete

rmin

ed

or

op

timiz

ed

op

era

tion c

ond

itions.

������

���������

Auto

/ M

anual c

ontrol m

ode c

an b

e s

ele

cte

d b

y pre

ssin

g the touch s

cre

en

with

the a

id o

f in

structio

n in

dic

ate

d o

n the s

cre

en.

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Op

era

tor

with

out

passw

ord

is r

efu

sed

to r

e-s

et

the o

pera

tion d

ata

, and

unit

is p

rote

cte

d fro

m m

is-o

pera

tion o

r ill in

tentio

n.

������������ ��������&

The m

em

ory

of control sys

tem

sto

res t

he o

pera

tion d

ata

for

last

five fail-

ure

s o

f unit

and

norm

al o

pera

tion for

one w

eek,

whic

h c

an b

e a

ccessed

at eve

ry m

om

ent.

��� �������������� �����������

Dis

pla

y o

f sp

ecia

l w

ork

ing

princip

les a

nd

guid

ance t

o o

pera

tio

n a

nd

main

tenance e

nab

les o

pera

tors

to m

ore

rap

idly

and

dire

ctly

und

ers

tand

the o

pera

tion m

eth

od

and

main

tenance info

rmatio

n,

facilita

ting t

he u

nit

managem

ent b

y users

and

pro

longin

g the s

erv

ice li

fe o

f th

e u

nit.

%���&'��('

��������� ����)�������

���#����

More

consid

era

te w

ay

of control:

Runnin

g c

ontrol—

limit

control—

safe

ty p

rote

ctio

n c

ontrol.

When c

hiller's n

orm

al ru

nnin

g e

nd

angere

d,

the s

elf-

dia

gnosis

and

self-

ad

justm

ent fu

nctio

n w

ill c

arr

y out to

ensure

sta

ble

and

safe

op

era

tion.

Chille

d

hot

and c

oolin

g w

ate

r pum

ps a

nd f

ans f

or

coolin

g t

ow

er

can b

e

opera

ted a

uto

matic

ally

only

by

connectio

n o

f control w

ires w

ith t

he c

ontrol

panel o

f unit.

In s

uch c

onditions,

full auto

matic

sta

rt a

nd s

top o

f chille

d

hot

and c

oolin

g w

ate

r pum

ps a

nd fans for coolin

g tow

er

will

be s

et.

����

���)��� ��&��#��������

���*���� +

���

By

pre

-settin

g,

with

out

limita

tion,

the s

witc

h-o

n/o

ff t

imer

on t

he t

ouch

scre

en o

r centraliz

ed

monito

ring c

om

pute

r, t

he u

nit

can b

e a

uto

matic

ally

sta

rted

or

sto

pp

ed

at th

e p

reset tim

e.

,�����������

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.���

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89

The c

oolin

g w

ate

r flo

w c

an b

e a

dju

ste

d in a

ccord

ance w

ith t

he o

pera

-

tion m

od

e o

f unit

by

means o

f th

e In

vert

er, w

hic

h c

ontrol t

he o

pera

tion o

f

wate

r p

um

p. In

such a

way

the c

onsum

ptio

n o

f energ

y by

the p

um

p c

an

be s

ave

d,

and

unit

can b

e o

pera

ted

und

er

low

er

tem

pera

ture

of coolin

g

wate

r. T

hen t

he u

nit

can b

e o

pera

ted

und

er

full

load

eve

n a

t lo

wer

tem

-

pera

ture

of coolin

g w

ate

r. T

he c

ontrol f

unctio

ns a

re o

ptio

nal f

or

ord

er.

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The s

tart

and

shutd

ow

n o

f unit

can b

e r

ealiz

ed

by

pre

ssin

g t

he S

tart

/

Sto

p b

utt

ons i

n t

he c

ontr

ol

roo

m r

em

ote

ly a

nd

the o

pera

tio

n s

tatu

s

can b

e d

isp

laye

d t

hro

ugh ind

icato

r lig

hts

to o

pera

te a

nd

know

the u

nit

data

with

out th

e n

eed

to b

e o

n t

he s

ite.

Und

er

sp

ecia

l req

uire

ment, t

he

touch s

cre

en c

an b

e in

sta

lled

in the c

ontrol r

oom

to k

now

the o

pera

tion

sta

tus o

f th

e u

nit

and

op

era

tion d

ata

and

info

rmatio

n o

f each p

art

of th

e

unit

anytim

e,

thus t

o m

onito

r th

e u

nit

on a

real tim

e b

asis

as w

ell

as t

o

sto

re a

nd

print th

e o

pera

tion d

ata

.

The c

om

pany'

s m

onito

ring a

nd c

ontrol cente

r is

able

to c

arr

y out

patrol

insp

ectio

n o

n t

he u

nits

locate

d in t

he u

sers

' m

achin

e r

oom

to k

now

and

analy

ze t

he o

pera

tion s

tatu

s o

f th

e u

nits

anyt

ime.

Should

there

be a

ny

ab-

norm

ity d

urin

g t

he o

pera

tion,

the c

ontrol sys

tem

will

auto

matic

ally

dia

l and

connect

to t

he c

om

pany'

s m

onito

ring a

nd c

ontrol cente

r and t

he s

erv

ice

engin

eer re

sponsi

ble

for

this

unit

by

sendin

g o

ut fa

ilure

info

rmatio

n.

The c

ontrol f

unctio

ns a

re o

ptio

nal f

or

ord

er.

���

��'������������������� ,���

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The c

entr

al

co

ntr

ol

of

a b

uild

ing i

s s

up

po

rted

by

the c

ontr

ol

sys

tem

.

The u

nit c

ontr

ol

panel

is p

rovid

ed

with i

nte

rfaces R

S2

32,

RS

42

2 o

r

RS

48

5 a

nd

data

com

munic

atio

n p

roto

col f

or

acq

uis

ition a

nd

dis

pla

ying

of th

e o

pera

tion d

ata

and

control of th

e u

nit

realiz

ed

by

the c

ontrol sys

-

tem

of a b

uild

ing.

The c

ontrol f

unctio

ns a

re o

ptio

nal f

or

ord

er.

0 �*�� �#��������-��#���� ����

#���� ��1

�� �����

Centr

al c

ontrol o

f units

, such a

s a

uto

matic

change-o

ver, c

entr

al c

ontrol,

sto

rage a

nd

print-

out

of

op

era

tion d

ata

of

para

llel op

era

ted

units

, and

etc

. can b

e r

ealiz

ed

by

means o

f a c

om

pute

r w

ith t

he s

oft

ware

MM

I2

for

centr

aliz

ed

control d

eve

lop

ed

by

the c

om

pany.

In s

uch a

way,

the

co

mp

ute

r au

tom

atically

dis

pla

ys t

he o

pera

tio

n d

ata

and

co

nd

itio

ns,

troub

les a

nd

ala

rm s

ignal and

sta

rts o

r sto

ps t

he u

nits

, w

hen t

he load

incre

ases o

r d

ecre

ases,

and

the e

nerg

y co

nsum

ptio

n c

an b

e s

ave

d.

The c

ontrol f

unctio

ns a

re o

ptio

nal f

or

ord

er.

�� ��� ��������#���� ����

#���� �����

%������!����������������&

Th

e s

olu

tio

n c

oncentr

atio

n c

ontr

ol, s

pecific

to

the c

om

pany,

allo

ws t

he u

nit

to o

pera

te u

nd

er

hig

h c

oncentr

atio

n s

afe

ly a

nd

sta

bly

by

monito

ring t

he s

pra

y concentr

atio

n o

f th

e s

trong s

olu

-

tion a

nd

controlling t

he h

eatin

g c

ap

acity,

thus n

ot only

to p

reve

nt

cry

sta

lliza

tion b

ut

als

o t

o im

pro

ve t

he o

pera

tion e

fficie

ncy

of

the

unit.

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When failu

re o

f th

e u

nit

occurs

, th

e lo

catio

n, re

ason a

nd

rem

ed

y of fa

ilure

shall

be d

isp

laye

d b

y m

eans o

f in

terf

ace, th

us m

ake

s o

pera

tor

to t

reat

the failu

re c

ond

itions e

asily

and

quic

kly

, and

im

pro

ve t

he o

pera

tion e

fficie

ncy

of th

e u

nit.

The c

ontrol sys

tem

als

o a

uto

matic

ally

keep

s in

the m

em

ory

op

era

tional d

ata

in a

week

and

conte

nts

of la

st 5

failu

res a

s w

ell

as v

arious p

ara

mete

rs for

check

at anytim

e.

0�� ���'������

���

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The c

ontrol s

yste

m m

onito

rs the c

oncentr

atio

n o

f sp

raye

d s

trong

solu

tion to c

alc

ula

te t

he o

ptim

ized

dilu

tion c

ycle

to far

aw

ay

from

pre

ferr

ed

solu

tion c

oncentr

atio

n d

uring s

hutd

ow

n,

thus n

ot

only

to p

reve

nt cry

sta

lliza

tion b

ut als

o to d

ecre

ase the re-s

tart

tim

e.

0������ ��� ����#�� �

The c

ontrol s

yste

m p

rovi

des w

ith c

oolin

g w

ate

r in

let te

mp

era

ture

limit

control m

ake

s t

he u

nit

safe

op

era

tion in t

he lim

its o

f coolin

g

wate

r te

mp

era

ture

in the r

ange o

f 18℃

~3

4℃

.

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�� ���/���,��

�������

The I

nve

rter

co

ntr

ol of

so

lutio

n p

um

p i

s a

dop

ted

in t

he c

ontr

ol

syste

m,

make

s t

he u

nit o

pe

rate

un

de

r b

est

so

lutio

n f

low

to

imp

rove

the o

pera

tion e

fficie

ncy

and

red

uce t

he s

tart

tim

e a

nd

energ

y consum

ptio

n.

�� �������

���#���� ��

��'������)������

Chilled

hot

wate

r outle

t te

mp

era

ture

, controlle

d b

y analo

g s

ys-

tem

, w

hic

h is

sp

ecifi

c for

the c

om

pany,

can s

tab

ilize

at hig

h p

re-

cis

ion,

imp

rovi

ng t

he o

pera

tion e

fficie

ncy

of

the u

nit

and m

ore

suita

ble

for

pla

ces that are

hig

hly

tem

pera

ture

-sensiti

ve.

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10

11

The c

ontr

ol

sys

tem

ad

op

ts t

he a

dva

nced

PID

co

ntr

ol

tech-

nolo

gy

and

touch s

cre

en L

CD

to d

isp

lay

the o

pera

tion c

on-

diti

ons a

nd

data

of

the u

nit

in a

real-

time m

anner

with

both

text

s a

nd

pic

ture

s,

featu

ring d

irect

exp

ressio

n o

f conte

nts

and

easin

ess f

or

und

ers

tand

ing,

enab

ling t

he o

pera

tor

to k

now

the

op

era

tion c

ond

itions a

nyt

ime a

nd

to t

ake t

imely

measure

s i

n

em

erg

ency.

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This

functio

n e

nsure

s that th

e o

pera

tor can u

nders

tand the u

nit

easily

and rapid

ly thus to w

ell

manage the u

nit

and g

reatly

impro

ve the li

fe o

f

the u

nit

and

guara

nte

e the in

cre

ase o

f effi

cie

ncy

for

users

as w

ell.

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Data Display

Chill

ed

(hot)

wate

r in

let te

mp

era

ture

Evap

ora

ting

tem

pera

ture

Chill

ed

(hot)

wate

r outlet te

mp

era

ture

Flu

e g

as tem

pera

ture

Coolin

g w

ate

r in

let te

mp

era

ture

HP

G p

ressure

Inte

rme

dia

te s

olu

tio

n t

em

pe

ratu

re

from

HP

GP

ressure

of auto

purg

ing

unit

Concentr

ate

d s

olu

tion

tem

pera

ture

fro

m L

PG

Chill

er

op

era

tion tim

e

Str

ong

solu

tion s

pra

y tem

pera

ture

Vacuum

pum

p s

tart

/sto

p n

um

ber

Cond

ensation tem

pera

ture

Str

ong

solu

tion d

ynam

ic

De-c

rysta

llizin

g p

ipe tem

pera

ture

Work

ing

princip

le

Coolin

g flo

w c

hart

Heating

flo

w c

hart

Work

ing

princip

le o

f chill

er

Work

ing

princip

le o

f heate

r

Operation instructions

Op

era

tion o

f chill

er

Refr

igera

nt b

y-p

ass

Op

era

tion o

f heate

rLeak test of unit

Op

era

tion o

f chill

ed

(hot)

and

coolin

g w

ate

r p

um

ps

Solu

tion c

harg

e

Burn

er

op

era

tion

Rem

oval of solu

tion fro

m u

nit

Op

era

tion o

f vacuum

pum

p

Rota

tion d

irection test

for

canned

moto

r-p

um

ps

Sam

plin

g o

f re

frig

era

nt

Chang

e o

f valv

e s

ealin

g r

ing

s

Maintenanceinstructions

Routing

main

tenance

Coolin

gU

nit

Syste

m

Heating

Unit

Syste

m

Long

term

shutd

ow

n

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12

13

With

ab

out 10

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tance w

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g s

old

in m

ore

than 1

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countr

ies a

nd

regio

ns,

ove

r 2

0,0

00

ab

sorp

tion c

hillers

are

serv

ing g

lob

al c

usto

mers

well.

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CC

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HP

, w

hic

h a

pp

lies t

he o

il or

gas a

s t

he

prim

e e

nerg

y re

sourc

e t

o m

eet

the r

eq

uire

ments

of

com

munity

or

build

ings for

the p

ow

er, h

eatin

g a

nd

/or

coolin

g,

can r

ealiz

e t

he

cascad

e r

esourc

es a

pp

licatio

ns,

such a

s t

he h

igh g

rad

e e

nerg

y

is u

sed

for

pow

er

genera

tion,

and

less p

ote

ntia

l energ

y fo

r heat-

ing a

nd

/or

coolin

g t

o r

ais

e t

he u

tiliz

atio

n p

erc

enta

ge o

f p

ow

er

to

85

%,

imp

rove

the s

afe

ty o

f p

ow

er

sup

ply

by

ele

ctric

pow

er

net-

work

, save

energ

y consid

era

bly,

pro

tect

envi

ronm

ent

and

con-

tinuous d

eve

lop

natio

nal

econom

y. A

pp

licatio

n o

f tr

igenera

tion,

whic

h g

ives a

dd

itional p

ow

er

sup

ply

to t

he s

ocie

ty a

nd

red

uces

the e

nerg

y consum

ptio

n b

y air

cond

itionin

g insta

llatio

ns,

has t

he

activ

e r

ole

to s

olv

e t

he p

ow

er

sup

ply

shortage.

So,

the t

rigenera

-

tion s

yste

m is

the o

nly

choic

e o

f d

eve

lop

ment of p

ow

er

sup

ply.

In t

he t

rigenera

tion s

yste

m,

the li

thiu

m b

rom

ide a

bsorp

tion c

hiller/

heate

rs,

op

era

ted

by

hig

h t

em

pera

ture

flue g

as

or

flue g

as a

nd

waste

hot

wate

r,

can f

ully

util

ize t

he low

pote

ntia

l heat

energ

y, e

fficie

ntly

im

pro

ve t

he inte

gra

ted

energ

y ap

plic

atio

n p

erc

enta

ge.

Sum

-

min

g u

p,

lithiu

m b

rom

ide a

bsorp

tion c

hiller

is the b

est heat re

cove

ry u

nits

in the trig

enera

tion s

yste

ms.

The w

aste

heat,

whic

h u

sually

is d

ischarg

ed

into

atm

osp

here

, no

w i

s u

tiliz

ed

to

drive t

he l

ithiu

m b

rom

ide a

bso

rptio

n c

hill

er/

heate

rLB

AC

/H,

realiz

ed

the c

ascad

e a

pp

licatio

n o

f p

rime e

nerg

y re

sourc

e.

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yste

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an b

e w

idely

used

in p

laces w

here

ele

ctric

pow

er

and

air

cond

itionin

g r

eq

uire

ments

exi

st

sim

ulta

neously,

such a

s

facto

ries,

hosp

itals

, la

rge d

ep

artm

ent sto

res,

com

muniti

es a

nd

ind

ustria

l park

s.

Flue

Gas

Typ

e Li

thiu

m B

rom

ide

Abso

rptio

n Ch

iller

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ter

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go

ries:

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yp

e a

nd

flue g

as/h

ot

wate

r ty

pe.

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h t

em

pe

ratu

re f

lue g

as t

yp

e a

bso

rptio

n c

hill

er/

he

ate

rs a

re

main

ly a

pp

licab

le to t

he t

rigenera

tion insta

llatio

ns w

ith t

urb

o g

en-

era

tors

in

clu

din

g m

icro

turb

ine

and

oth

er

pla

ces w

here

hig

h

tem

pera

ture

flue g

as i

s a

vaila

ble

and

air c

ond

itio

nin

g i

s n

eces-

sary

such a

s ind

ustr

ial kiln

s.

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flue g

as-h

ot

wate

r fir

ed

typ

es,

main

heat

so

urc

es c

an fi

nd

the fl

ue g

as a

nd

jacket

wate

r fro

m

inte

rnal

co

mb

ustio

n e

ng

ine.

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yp

es c

an a

lso b

e u

sed

in

oth

er

pla

ces w

here

hig

h t

em

pera

ture

flue g

as is a

vaila

ble

and a

ir

cond

itionin

g is

necessary

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In o

rder

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eet

the r

eq

uire

ments

to c

om

fort

and

technolo

gic

al

need

s o

f air c

ond

itio

nin

g s

yste

m,

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m b

rom

ide a

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rptio

n

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rs w

ith a

fter-

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eans c

an b

e i

nsta

lled,

where

heat

fro

m g

enera

tor

flue g

as

or

flue g

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nd

hot

wate

r i

s n

ot

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rive

them

.

Fo

r tr

igenera

tor

insta

llatio

n w

ith i

nte

rnal

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mb

ustio

n e

ng

ine a

s

drive

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eq

uire

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air

con-

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g,

and

hot

wate

r w

ill b

e u

sed

for

oth

er

ap

plic

atio

ns,

then

flue g

as t

ype o

r such t

ype w

ith a

fter-

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ing w

ill b

e a

vaila

ble

.

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ce

hig

h p

ressu

re a

nd

tem

pera

ture

gas t

o d

rive

gas

turb

ine g

enera

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lue g

as o

f

wh

ich

is d

ire

cte

d t

o l

ith

ium

bro

mid

e a

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hille

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t

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eet th

e c

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ap

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uire

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m is

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diti

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f fu

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pro

ve r

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aste

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e g

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m g

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ine is

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ue g

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ype li

thiu

m b

rom

ide a

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lify

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l-

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rove

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y in

tegra

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n in

sys

tem

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n o

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e li

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m b

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ide a

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tion c

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ing a

llow

s r

atio

nal c

onfig

ura

tion o

f genera

tor

and c

hiller/

heate

r cap

acity

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on t

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g s

yste

m c

oolin

g a

nd

heatin

g load

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eq

uip

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inve

stm

ent, a

nd

im

pro

ve t

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n-

erg

y in

tegra

ted

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izatio

n in

sys

tem

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e is

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plic

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le to the trig

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yste

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al c

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conte

nt of

sulp

hur

and

fore

ign m

atter

is

ava

ilab

le a

nd

air

cond

itionin

g

is n

ecessary

.

Pla

ces,

where

hig

h tem

p.

flue g

as

with

low

conte

nt of

sulp

hur

and

fore

ign m

atter

is

ava

ilab

le a

nd

air

cond

itionin

g

is n

ecessary

.

Pla

ces,

where

hig

h tem

p.

flue g

as

with

low

conte

nt of

sulp

hur

and

fore

ign m

atter

and

hot w

ate

r is

ava

ilab

le a

nd

air

cond

itionin

g is

necessary

.

Pla

ces,

where

hig

h tem

p.

flue g

as

with

low

conte

nt of

sulp

hur

and

fore

ign m

atter

is

ava

ilab

le.

Ap

plic

atio

nFeatu

res

Ap

plie

d m

ain

ly for

trig

enera

-tio

n s

yste

m w

ith g

as turb

ine

inclu

din

g m

icro

turb

ine

, in

tern

aI c

om

bustio

n e

ngin

e,

fuel c

ell

as g

enera

tor

driv

e,

als

o c

an b

e u

sed

for

coolin

g

heatin

g b

y hig

h tem

pera

ture

flu

e g

as

such a

s fl

ue g

as o

f in

dustria

l kiln

s

Ap

plie

d m

ain

ly for

trig

enera

-tio

n s

yste

m w

ith g

as turb

ine

inclu

din

g m

icro

turb

ine

, in

tern

al c

om

bustio

n e

ngin

e,

fuel c

ell

as g

enera

tor

driv

e,

als

o c

an b

e u

sed

for

coolin

g

heatin

g b

y hig

h tem

pera

ture

flu

e g

as

such a

s fl

ue g

as o

f in

dustria

l kiln

s

Applie

d m

ain

ly for trig

enera

tion

sys

tem

with

inte

rnal c

om

bus-

tion e

ngin

e a

s g

enera

tor

driv

e,

als

o c

an b

e u

sed

for

coolin

g

heatin

g b

y hig

h tem

pera

ture

flu

e g

as

such a

s fl

ue g

as o

f in

dustria

l kiln

s a

nd

waste

hot

wate

r

Ap

plie

d for

gas turb

ine

genera

tor

pla

nt, m

icro

-turb

o

genera

tors

, and

inte

rnala

n

ext

ern

al c

om

bustio

n e

ngin

e

genera

tors

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Flu

e g

as t

ype lith

ium

bro

mid

e a

bsorp

tion c

hiller/

heate

r is

a e

quip

ment, w

hic

h u

ses h

igh t

em

pera

ture

flue g

as d

ischarg

ed

by

gas t

urb

ine

insta

llatio

n,

as f

uel,

wate

r as r

efrig

era

nt, lith

ium

bro

mid

e a

s a

bsorb

ent

solu

tion,

pro

duces c

hilled

and

/or

hot

wate

r fo

r th

e p

urp

ose o

f air-

cond

itionin

g a

nd

technolo

gy

pro

cess.

It consis

ts o

f flu

e g

as h

igh p

ressure

genera

tor

HP

genera

tor

, lo

w p

ressure

genera

tor

LP

gen-

era

tor

, cond

enser, e

vap

ora

tor, a

bsorb

er, h

igh t

em

pera

ture

heat

exc

hanger

HT h

eat

exc

hanger

, lo

w t

em

pera

ture

heat

exc

hanger

LT

heat

exc

hanger

; and

such a

uxi

liary

parts,

as h

erm

etic

ally

-seale

d p

um

ps a

nd

vacuum

pum

p,

and

keep

s its

elf

und

er

vacuum

cond

itions

by

vacuum

pum

p a

nd

auto

matic

purg

e u

nit

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g w

ate

rin

let

Chill

ed

wate

rin

let

Chill

ed

wate

routle

t

Coolin

g w

ate

routle

t

Refr

igera

nt p

um

p

HT h

eat

exchang

er

Cond

enser

Ab

sorb

er

Evap

ora

tor

Flue gas exhaust

HP

Genera

tor

3C

heck v

alv

e

Sam

plin

gvalv

e

Exhaust

Vacuum

pum

pOil trap

Auto purging unit

Auto de-crysta-llization pipe

LP

Genera

tor

Flu

e g

as in

let

Coole

r

Coole

r in

let valv

e

Byp

ass

valv

e

Ab

sorb

er

Solu

tion p

um

p

LT h

eat

exchang

er

① C

hill

ed

wate

r in

let te

mp

. (

I)

② C

hill

ed

wate

r outle

t te

mp

. (C

,I,A

)

③ C

oolin

g w

ate

r in

let te

mp

. (C

,I,A

)

④ A

uto

purg

ing

unit p

ressure

(I)

⑤ L

P g

enera

tor

str

ong

solu

tion tem

p. (C

,I)

⑥ C

ond

ensatio

n tem

p. (C

,I,A

)

⑦ H

P g

enera

tor

inte

rmed

iate

solu

tion tem

p. (I,A

)

⑧ E

vap

ora

tion tem

p. (I,A

)

⑨ C

hill

ed

wate

r flo

w (

A)

⑩ D

e-c

rysta

llizatio

n p

ipe tem

p. (I,A

)

⑪ H

P g

enera

tor

pre

ssure

(C

,I,A

)

⑫ S

trong

solu

tion s

pra

yin

g tem

p. (C

,I)

⑬ H

P s

olu

tion le

vel(C

,I))

⑭ F

lue g

as in

let te

mp

. (I)

⑮ F

lue g

as e

xhauste

d tem

p. (I)

Chill

ed

wate

r

Coolin

g w

ate

r

Refr

igera

nt w

ate

r

HP

refr

igera

nt vap

or

Weak s

olu

tion

Inte

rmed

iate

solu

tion

Str

ong

solu

tion

Refr

igera

nt vap

or

(A)－

Ala

rm

(I)－

Ind

icatio

n

(C)－

Contr

ol

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Chilled

w

ate

r from

custo

mer

ab

out

12℃

ente

rs

heat

transfe

r tu

bes,

and

eva

pora

tes re

frig

era

nt

wate

r, w

hic

h is

drip

ped

ove

r th

e tub

es. Thus p

rod

uced

chilled

wate

r ru

ns fro

m the

eva

pora

tor

at te

mp

era

ture

ab

out 7℃

into

the e

xtern

al s

yste

m.

Re-

frig

era

nt w

ate

r ab

sorb

s h

eat from

ext

ern

al s

yste

m, b

ecom

es w

ate

r

vap

or, a

nd

flow

s in

to a

bsorb

er.

�������S

trong li

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m b

rom

ide s

olu

tion p

ossesses tre

mend

ous

wate

r va

por

ab

sorb

ing c

ap

acity

drip

s o

ver

tub

es,

ab

sorb

s r

efrig

er-

ant

vap

or, p

rod

uced

in t

he e

vap

ora

tor, a

nd

becom

es w

eak

so-

lutio

n.

Coolin

g w

ate

r from

coolin

g t

ow

er

ente

rs t

he h

eat

transfe

r

tub

es t

o c

ool

the s

trong s

olu

tion d

istrib

ute

d o

uts

ide t

ub

es,

and

carr

ies a

way

heat

i.e. heat from

ext

ern

al s

yste

m. A

fter ab

sorb

ing

wate

r va

por, s

olu

tion is d

ilute

d a

nd

sent

to H

P g

enera

tor

thro

ugh

heat exc

hangers

.

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boil

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ide w

eak

solu

tion in

the

HP

genera

tor. T

he w

eak

solu

tion is c

oncentrate

d into

inte

rmed

iate

solu

tion,

whic

h fl

ow

s into

the low

pre

ssure

genera

tor

thro

ugh H

T

heat

exc

hanger, a

nd

pro

duces h

igh t

em

pera

ture

refrig

era

nt

vap

or,

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h e

nte

rs L

P g

enera

tor

als

o.

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tor

Lith

ium

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r-

med

iate

solu

tion,

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ow

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rom

the H

P g

enera

tor

via L

T h

eat

exc

hanger

and

tem

pera

ture

is r

ed

uced

, is

heate

d b

y re

frig

era

nt

vap

or, p

rod

uced

in t

he H

P g

enera

tor, a

nd

concentrate

d t

o s

trong

solu

tion,

whic

h fl

ow

s in

to the a

bsorb

er

thro

ugh L

T h

eat exc

hanger,

pro

duced

va

por

flow

s in

to cond

enser. R

efrig

era

nt

vap

or, w

hic

h

flow

s f

rom

HP

genera

tor, i

s c

ond

ensed

by

heatin

g t

he s

olu

tion,

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ente

rs c

ond

enser

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o.

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ond

enser

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ap

or

outs

ide t

he t

ub

es into

refrig

era

nt

wate

r.

The p

rod

uced

refrig

era

nt

wate

r ente

rs t

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vap

ora

tor

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ugh U

pip

e a

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era

nt ele

ment fo

r re

frig

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solu

tion fro

m L

P g

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hanges h

eat w

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eak

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tion fro

m

ab

sorb

er

for

rais

ing the tem

pera

ture

of w

eak

solu

tion a

nd

recove

r-

ing h

eat from

strong s

olu

tion.

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eat

Exc

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In-

term

ed

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solu

tion f

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HP

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exc

hanges h

eat

with

weak

solu

tion fro

m L

T h

eat exc

hanger fo

r ra

isin

g the tem

pera

ture

of w

eak

solu

tion further. H

eat exc

hangers

red

uced

the h

eat re

quire

ments

of

HP

genera

tor, in

the m

ean tim

e, re

duced

the c

oolin

g w

ate

r re

quire

-

ments

. P

erform

ance o

f heat

exc

hangers

dete

rmin

es t

he o

pera

tion

cond

itions o

f chiller/

heate

rs.

Hot w

ate

rin

let

Hot w

ate

routle

t

HP

Genera

tor

Cond

enser

LP

Genera

tor

Flue gas exhaust

Flu

e g

as in

let

Check v

alv

e

Exhaust

Vacuum

pum

pC

oole

r in

let valv

e

Ab

sorb

er

Evap

ora

tor

Sam

plin

gvalv

e

Byp

ass

valv

e

Ab

sorb

er

Refr

igera

nt p

um

pS

olu

tion p

um

p

HT h

eat

exchang

er

Oil trap

Auto purging unit

Auto de-crysta-llization pipe

LT h

eat

exchang

er

Chill

ed

wate

r

Refr

igera

nt w

ate

r

HP

refr

igera

nt vap

or

Weak s

olu

tion

Inte

rmed

iate

solu

tion

Refr

igera

nt vap

or

(A)－

Ala

rm

(I)－

Ind

ica

tio

n

(C)－

Co

ntr

ol

① H

ot

wa

ter

inle

t te

m.

(I)

② H

ot

wa

ter

ou

tle

t te

mp

. (C

,I,A

)

④ A

uto

pu

rgin

g u

nit p

ressu

re (

I)

⑦ H

P g

en

era

tor

inte

rme

dia

te s

olu

tio

n t

em

p.

(I,A

)

⑨ H

ot

wa

ter

flo

w (

A)

⑪ H

P g

en

era

tor

pre

ssu

re (

C,I

,A)

⑬ H

P s

olu

tio

n le

ve

l (C

,I))

⑭ F

lue

ga

s in

let

tem

p.

(I)

⑮ F

lue

ga

s e

xh

au

ste

d t

em

p.

(I)

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Typ

eY

X4

80

-3

5H

24

7H

25

8H

27

0H

28

1H

29

3H

210

5H

21

16

H2

14

5H

21

74

H2

Coolin

g C

ap

acity

kW350

470

580

700

810

930

1050

1160

1450

1740

10

4kc

al/h

30

40

50

60

70

80

90

100

125

150

US

Rt

99

132

165

198

231

265

298

331

413

496

Heatin

g C

ap

acity

10

4kc

al/h

24

32

40

48

56

64

72

80

100

120

Chilled

/Hot

Wate

r

Chilled

Wate

r In

/Out Te

mp

℃1

2→

7

Hot W

ate

r In

/Out Te

mp

℃5

6→

60

Flo

wm

3/h

60

80

100

120

140

160

180

200

250

300

Pre

ssure

Loss

mH

2O

4.5

4.5

56

5.5

6.5

99

44

Connectio

n D

iam

ete

r D

Nm

m1

00

10

01

25

125

150

150

150

150

200

200

Coolin

g W

ate

r

In/O

ut Te

mp

℃3

2→

38

Flo

wm

3/h

86

114

143

172

200

229

257

286

357

429

Pre

ssure

Loss

mH

2O

76

.56

.57

89

5.5

5.5

7.0

7.0

Connectio

n D

iam

ete

r D

Nm

m100

125

150

150

150

150

200

200

200

250

Flu

e G

as

Flo

wkg

/h2

74

53

65

54

57

05

48

56

40

07

31

08

22

59

14

01

14

25

13

71

0

Pre

ssure

Loss

mm

H2O

70

110

90

120

130

140

160

160

150

160

Inle

t D

iam

ete

r Φ

mm

250

300

350

350

400

400

450

450

500

600

Outle

t D

iam

ete

r Φ

mm

250

300

350

350

400

400

450

450

500

600

Ele

ctric

Pow

er

Pow

er

Sup

ply

3Φ

- 3

80

V -

50

Hz

Tota

l Curr

ent

A1

2.6

13

.71

3.7

16

.81

6.8

16

.81

7.4

19

.21

9.8

19

.8

Ele

ctric

Pow

er

kW3.8

4.2

4.2

55

55.2

5.5

5.9

5.9

Ove

rall

Dim

en-

sio

ns

Length

mm

38

00

38

20

38

08

38

20

38

40

38

40

43

40

43

40

48

10

48

85

Wid

th2

29

62

40

62

60

62

71

62

86

12

87

12

91

13

02

13

33

836

15

Heig

ht

23

32

23

51

23

49

24

11

24

96

25

44

25

64

28

07

28

97

30

34

Ship

pin

g W

eig

ht

t7

.28

.39

.81

0.5

11

.41

2.5

13

.81

4.2

17

.119

.6

Op

era

tion W

eig

ht

8.2

9.6

11

.61

2.7

14

.21

5.6

17

.51

8.4

23

26

.4

6��

1 V

alu

es for chilled w

ate

r,hot w

ate

r,coolin

g w

ate

r in

the a

bove

tab

le a

re for nom

inal o

pera

tion c

ond

itions,

and c

an b

e p

rop

erly

ad

juste

d in

actu

al o

pera

tion.

2 T

he lo

west outle

t te

mp.fo

r chilled

wate

r is

5℃

. In

let te

mp

of co

olin

g w

ate

r can b

e a

dju

ste

d in

the r

ang

e o

f 18

~3

4℃

3 F

low

of chilled

/hot w

ate

r can b

e a

dju

ste

d in

the r

ang

e o

f 6

0~12

0%

.

4 F

oulin

g facto

r o

n c

hilled

/hot/

co

olin

g w

ate

r sid

e is

0.0

86

m2K

/kw

0.0

001m

2·h·℃

/kcal.

5 C

oolin

g c

ap

acity

can b

e a

dju

ste

d in

the r

ang

e o

f 2

0~10

0%

.

6 F

lue g

as tem

pera

ture

fo

r m

od

els

mentio

ned

in the s

heet is

48

0℃

.

20

21

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Vacuum

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LP

G

Ab

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LT H

eat

Exchang

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eat

Exchang

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Auto-purge Unit

Oil Trap

Auto-decrysta-llization Pipe

Chang

e-o

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Valv

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e-o

ver

Valv

e

flue gas out

gas flue in

flue gas out

Ab

sorb

er

Evap

ora

torC

ond

ensor

hot w

ate

rin

hot w

ate

rout

Burn

er

HP

G

Flu

e G

as H

PG

Burn

er

flam

e

Flu

e g

as

Hot w

ate

r

HP

G r

efr

igera

nt vap

or

Weak s

olu

tion

Refr

igera

nt vap

or

Refr

igera

nt

Burn

er

HP

G in

term

ed

iate

solu

tion

Flu

e g

as H

PG

inte

rmed

iate

solu

tion

①

Hot w

ate

r in

let te

mp

. (I)

②

Hot w

ate

r outle

t te

mp

. (C

,I,A

)

④

Auto

-purg

e u

nit p

ressure

(I)

⑦

HP

G in

term

ed

iate

solu

tion tem

p. (I,A

)

⑨

Hot w

ate

r flo

w r

ate

(A

)

⑩

Burn

er

flue g

as tem

p. (I,A

)

⑫

HP

G p

ressure

(C

,I,A

)

⑭

Burn

er

HP

G s

olu

tion le

vel (C

,I)

⑮

Flu

e g

as b

urn

er

HP

G s

olu

tion le

vel (C

,I)

⑯

Flu

e g

as in

let te

mp

. (I)

⑰

Gas flu

e o

utle

t te

mp

. (I)

(I)−

Dis

pla

y

(C)−

Contr

ol

(A)−

Ala

rm

Non-r

etu

rn V

alv

e

Vacuum

Pum

pg

as o

ut

Coole

r

Solu

tion P

um

pR

efr

igera

nt P

um

p

coolin

g w

ate

rin

HT H

eat

Exchang

er

LT H

eat

Exchang

er

Auto-purge Unit

Oil Trap

Auto-decrysta-llization Pipe

Flu

e G

as H

PG

Chang

e-o

ver

Valv

e

Chang

e-o

ver

Valv

e

flue gas in

flue gas out

flue gas out

Evap

ora

tor

Ab

sorb

er

By-p

ass

Valv

e

Sam

plin

gValv

e

Ab

sorb

er

Cond

ensor

chill

ed

wate

rin

coolin

g w

ate

rout

chill

ed

wate

rout

LP

G

Burn

er

HP

G

①

Chill

ed

wate

r in

let te

mp

. (I)

②

Chill

ed

wate

r outle

t te

mp

. (C

,I,A

)

③

Coolin

g w

ate

r in

let te

mp

. (C

,I,A

)

④

Auto

-purg

e u

nit p

ressure

(I)

Burn

er

flam

e

Flu

e g

as

Coolin

g w

ate

r

Chill

ed

wate

r

Str

ong

solu

tion

HP

G r

efr

igera

nt vap

or

Weak s

olu

tion

Refr

igera

nt vap

or

Refr

igera

nt w

ate

r

Burn

er

HP

G in

term

ed

iate

solu

tion

Flu

e g

as H

PG

inte

rmed

iate

solu

tion

⑤

LP

G s

trong

solu

tion tem

p. (C

,I)

⑥

Cond

ensatio

n tem

p. (C

,I,A

)

⑦

HP

G in

term

ed

iate

solu

tion tem

p. (I,A

)

⑧

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ora

tion tem

p.e

ratu

re (

I,A

)

⑨

Chill

ed

wate

r flo

w (

A)

⑩

Burn

er

flue tem

p. (I,A

)

⑪

Auto

-decry

sta

llizatio

n p

ipe tem

p. (I,A

)

⑫

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G p

ressure

(C

,I,A

)

⑬

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ong

solu

tion s

pra

y tem

p. (C

,I)

⑭

Burn

er

HP

G s

olu

tion le

vel (C

,I)

⑮

Flu

e g

as s

olu

tion level (C

,I)

⑯

Flu

e g

as in

let te

mp

. (I)

⑰

Gas flu

e o

ut te

mp

. (I)

(I)−

Dis

pla

y

(C)−

Contr

ol

(A)−

Ala

rm

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Typ

eY

X4

80

-2

04

H2

23

3H

22

62

H2

29

1H

23

49

H2

40

7H

24

65

H2

52

3H

25

82

H2

Coolin

g C

ap

acity

kW2

04

02

33

02

62

02

91

03

49

04

07

04

65

05

23

05

82

0

10

4kc

al/h

17

52

00

22

52

50

30

03

50

40

04

50

50

0

US

Rt

57

96

61

74

48

27

99

21

15

71

32

31

48

81

65

3

Heatin

g C

ap

acity

10

4kc

al/h

14

01

60

18

02

00

24

02

80

32

03

60

40

0

Chilled

/Hot

Wate

r

Chilled

Wate

r In

/Out Te

mp

℃1

2→

7

Hot W

ate

r In

/Out Te

mp

℃5

6→

60

Flo

wm

3/h

35

04

00

45

05

00

60

07

00

80

09

00

10

00

Pre

ssure

Loss

mH

2O

45

6.5

6.5

8.5

89

12

.51

2

Connectio

n D

iam

ete

r D

Nm

m2

00

25

02

50

25

03

00

30

03

50

35

03

50

Coolin

g W

ate

r

In/O

ut Te

mp

℃3

2→

38

Flo

wm

3/h

50

05

72

64

37

15

85

71

00

01

14

31

28

61

42

9

Pre

ssure

Loss

mH

2O

79

10

9.0

11

.51

15

.56

.57

Connectio

n D

iam

ete

r D

Nm

m2

50

25

02

50

30

03

50

35

04

00

40

04

00

Flu

e G

as

Flo

wkg

/h1

59

90

18

28

02

05

60

22

85

02

74

10

31

98

03

65

50

41

12

04

56

90

Pre

ssure

Loss

mm

H2O

16

01

60

18

01

60

17

01

70

16

01

55

16

0

Inle

t D

iam

ete

r Φ

mm

60

07

00

70

07

00

80

09

00

90

01

00

01

00

0

Outle

t D

iam

ete

r Φ

mm

60

07

00

70

07

00

80

09

00

90

01

00

01

00

0

Ele

ctric

Pow

er

Pow

er

Sup

ply

3Φ

- 3

80

V -

50

Hz

Tota

l Curr

ent

A1

9.8

21

.72

62

6.9

31

.83

3.5

36

.53

6.5

42

.3

Ele

ctric

Pow

er

kW5

.96

.97

.97

.99

.61

0.1

11

.11

1.1

12

.6

Ove

rall

Dim

en-

sio

ns

Length

mm

48

85

53

08

57

33

59

58

72

30

72

30

72

30

79

30

79

60

Wid

th3

82

53

78

53

92

54

01

04

43

74

71

25

02

25

13

25

55

9

Heig

ht

31

50

32

80

33

20

34

70

37

60

40

60

42

40

44

20

45

70

Ship

pin

g W

eig

ht

t2

2.1

24

.72

5.9

31

.13

8.1

44

.34

8.7

52

.76

0.5

Op

era

tion W

eig

ht

29

.43

3.7

36

42

52

.36

0.1

66

.37

28

2.4

6��

1 V

alu

es fo

r chilled

wate

r,hot w

ate

r,co

olin

g w

ate

r in

the a

bove

tab

le a

re fo

r no

min

al o

pera

tion c

ond

itio

ns,a

nd

can b

e p

rop

erly

ad

juste

d in

actu

al o

pera

tion.

2 T

he lo

west outle

t te

mp.fo

r chilled

wate

r is

5℃

. In

let te

mp

of co

olin

g w

ate

r can b

e a

dju

ste

d in

the r

ang

e o

f 18

~3

4℃

3 F

low

of chilled

/hot w

ate

r can b

e a

dju

ste

d in

the r

ang

e o

f 6

0~12

0%

.

4 F

oulin

g facto

r o

n c

hilled

/hot/

co

olin

g w

ate

r sid

e is

0.0

86

m2K

/kw

0.0

001m

2·h·℃

/kcal.

5 C

oolin

g c

ap

acity

can b

e a

dju

ste

d in

the r

ang

e o

f 2

0~10

0%

.

22

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e

Oil trap

Auto purging unit

Decrystalliza-tion pipe

Solu

tion P

um

pR

efr

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nt

Pum

pByp

ass

Valv

e

Sam

plin

gValv

e

Coolin

g w

ate

rin

let

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outle

t

Ste

am

inle

t

Clie

nt scop

e

H.T

Heat

Exchang

er

Ste

am

HP

G

Flu

e g

as

HP

G

Flue gas out

Ab

sorb

er

Ab

sorb

er

Evap

ora

tor

Chill

ed

wate

routle

t

Chill

ed

wate

rin

let

Coolin

g w

ate

routle

t

Flue gas in

Ste

am

Reg

ula

ting

Valv

e

Chill

ed

wate

r

Weak s

olu

tion

Coolin

g w

ate

r

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rmed

iate

solu

tion in

flu

e g

as H

PG

.

Refr

igera

nt w

ate

r

Str

ong

solu

tion

HP

G. re

frig

era

nt vap

or

Ste

am

cond

ensate

Inte

rmed

iate

solu

tion in

ste

am

HP

G

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am

①

Chill

ed

wate

r in

let te

mp

. (I)

②

Chill

ed

wate

r outle

t te

mp

. (C

,I,A

)

③

Coolin

g w

ate

r in

let te

mp

. (C

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)

④

Purg

ing

unit p

ressure

(I)

⑤

Str

ong

solu

tion tem

p.in

LP

G (

C,I)

⑥

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ensatio

n T

em

p. (I,A

)

⑦

Inte

rmed

iate

solu

tion tem

p.(I,A

)

⑧

Solu

tion le

vel in

ste

am

HP

G (

C,I)

⑨

Evap

ora

tion tem

p. (I,A

)

⑩

Chill

ed

wate

r flo

w (

A)

⑪

Flu

e g

as o

utle

t te

mp

. (I)

⑫

Decry

sta

llizatio

n p

ipe tem

p. (I,A

)

⑬

Pre

ssure

in H

PG

(C

,I,A

)

⑭

Str

ong

solu

tion s

pra

yin

g tem

p (

C,I)

⑮

Solu

tion le

vel in

flu

e g

as H

PG

(C

,I)

⑯

Flu

e g

as in

let te

mp

. (I)

⑰

Ste

am

pre

ssure

(C

,I,A

)

⑱

Ste

am

cond

ensate

tem

p. (I)

(C)—

Contr

ol

(A)—

Ala

rm

(I)—

Ind

icatio

n

Coole

r

Sam

plin

gvalv

e

Byp

ass

valv

e

Solu

tion p

um

p

LP

G

Ab

sorb

er

Evap

ora

tor

Ab

sorb

er

Flu

e-g

as H

PG

3-w

ays r

eg

ula

ting

valv

e

Heat sourc

eH

ot-

wate

r

Heat sourc

eH

ot-

wate

r

flue-g

as

out

flue-g

as

in

Cond

enser

Coolin

g w

ate

rout

Coolin

g w

ate

rin

Refr

igera

nt p

um

p

Decrysta-lization piping

Auto purging unit

Non-r

etu

rn v

alv

e

Vacuum

pum

pD

ischarg

e

Oil trap

L.T

. heat

exchang

er

H.T

. heat

exchang

er

Chill

ed

wate

r

Weak s

olu

tion

Coolin

g w

ate

r

Inte

rmed

iate

solu

tion

Refr

igera

nt w

ate

r

Str

ong

solu

tion

HP

G r

efr

igera

nt vap

or

Hot w

ate

r

Refr

igera

nt vap

or

①

Chill

ed

wate

r in

let te

mp

. (I)

②

Chill

ed

wate

r out te

mp

. (C

,I,A

)

③

Coolin

g w

ate

r in

let te

mp

.(C

,I,A

)

④

Puring

unit p

ressure

(I)

⑤

Str

ong

solu

tion tem

p. in

LP

G (

C,I)

⑥

Cond

ensatio

n tem

p. (C

,I,A

)

⑦

Inte

rmed

iate

solu

tion tem

p.in

HP

G (

I,A

)

⑧

Evap

ora

tion tem

p. (I,A

)

⑨

Chill

ed

wate

r flo

w (

A)

⑩

Decry

sta

lizato

n p

ipin

g tem

p. (I,A

)

⑪

Pre

ssure

in H

PG

(C

,I,A

)

⑫

Str

ong

solu

tion s

pra

yin

g tem

p. (C

,I)

⑬

Solu

tion le

vel in

HP

G (

C,I)

⑭

Flu

e-g

as in

let te

mp

. (I)

⑮

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e-g

as o

utle

t te

mp

. (I)

⑯

Heat sourc

e h

ot-

wate

r outle

t te

mp

. (C

,I)

(A)–

Ala

rm

(I)–

Dis

pla

y

(C)–

Contr

ol

Sam

plin

gvalv

e

Byp

ass

valv

e

Hot w

ate

rout

Hot w

ate

rin

3-w

ays r

eg

ula

ting

valv

e

Flu

e-g

as H

PG

L.T

. heat

exchang

er

H.T

. heat

exchang

er

Flu

e-g

as

inFlu

e-g

as

out

Cond

enser

LP

G

Ab

sorb

er

Ab

sorb

er

Evap

ora

tor

Oil trap

Auto purging unit

De-crysta-lization piping

Dis

charg

eVacuum

pum

p

Non-r

etu

rn v

alv

eR

efr

igera

nt p

um

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olu

tion p

um

p

Coole

r

①

Hot w

ate

r in

let te

mp

. (I)

②

Hot w

ate

r out te

mp

. (C

,I,A

)

Hot-

wate

r

Weak s

olu

tion

Refr

igera

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ate

r

Str

ong

solu

tion in

HP

G

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pg

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④

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ressure

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HP

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)

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ate

r flo

w r

ate

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)

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ssure

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PG

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)

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Solu

tion le

vel in

HP

G (

C,I)

⑭

Flu

e-g

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let te

mp

. (I)

⑮

Flu

e-g

as o

utle

t te

mp

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rm

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pla

y

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Sam

plin

gvale

Non-r

etu

rn v

alv

e

Coole

r

Gas o

ut

Vacuum

pum

p

Solu

tion p

um

pR

efr

igera

nt p

um

p

Coolin

g w

ate

rin

Burn

er

HP

G

Flue out

HT h

eat

exchang

er

Oil trap

Auto purge unit

Auto decrysta-llization pipe

chang

e-o

ver

valv

e

Gas flu

eH

PG

Ab

sorb

er

Evap

ora

tor

By p

ass

valv

e

Ab

sorb

er

Chill

ed

wate

rin

Chill

ed

wate

rout

Coolin

g w

ate

rout

Gas flue in

Sourc

ehot w

ate

r in

Sourc

ehot w

ate

r out

3 w

ay m

od

ula

ting

valv

e

Flue out

Cond

ensor

LP

G

LT h

eat

exchang

er

Burn

er

flam

e

Flu

e

Coolin

g w

ate

r

Chill

ed

wate

r

Str

ong

solu

tion

HP

G r

efr

igera

nt vap

or

Weak s

olu

tion

Refr

igera

nt vap

or

Refr

igera

nt

Burn

er

HP

G inte

rmed

iate

solu

tion

Gas flu

e H

PG

inte

rmed

iate

solu

tion

Hot w

ate

r

① C

hill

ed

wate

r in

let te

mp

. (I

)

② C

hill

ed

wate

r outlet te

mp

. (C

,I,A

)

③ C

oolin

g w

ate

r in

let te

mp

. (C

,I,A

)

④ P

urg

e u

nit p

ressure

(I)

⑤ L

PG

str

ong

solu

tion tem

p. (C

,I)

⑥ C

ond

ensation tem

p. (C

,I,A

)

⑦ H

PG

inte

rmed

iate

solu

tion tem

p. (I

,A)

⑧ E

vap

ora

tion (

I,A

)

⑨ C

hill

ed

wate

r flow

rate

(A

)

⑩ B

urn

er

flue o

ut te

mp

. (I

,A)

⑪ D

ecry

sta

llization p

ipe tem

p. (I

,A)

⑫ H

PG

pre

ssure

(C

,I,A

)

⑬ S

trong

solu

tion s

pra

y tem

p. (C

,I)

⑭ B

urn

er

HP

G s

olu

tion level (C

,I)

⑮ G

as flu

e b

urn

er

solu

tion level (C

,I)

⑯ G

as flu

e inle

t te

mp

. (I

)

⑰ G

as flu

e o

ut te

mp

. (I

)

⑱ S

ourc

e h

ot w

ate

r out te

mp

. (C

,I)

(I)−

Dis

pla

y

(C)−

Contr

ol

(A)−

Ala

rm

Auto purge unit

Auto decrysta-llization pipe

Burn

er

HP

G

Gas flu

eH

PG

Solu

tion p

um

pR

efr

igera

nt p

um

p

Ab

sorb

er

Evap

ora

tor

By p

ass

valv

e

Ab

sorb

er

Hot w

ate

rin

Hot w

ate

rout

7

Oil trap

Chang

e-o

ver

valv

e

Flue out

Gas flue in

3 w

ay m

od

ula

ting

valv

e

Flue out

Cond

ensor

LP

G

Non-r

etu

rn v

alv

e

Coole

r

Gas o

ut

Vacuum

pum

p

HT h

eat

exchang

er

LT h

eat

exchang

er

Bu

rne

r fla

me

Flu

e g

as

Ho

t w

ate

r

HP

G r

efr

ige

ran

t va

po

r

We

ak s

olu

tio

n

Re

frig

era

nt

va

po

r

Re

frig

era

nt

Bu

rne

r H

PG

str

on

g s

olu

tio

n

Ga

s f

lue

HP

G s

tro

ng

so

lutio

n

① H

ot

wa

ter

inle

t te

mp

. (I

)

② H

ot

wa

ter

ou

tle

t te

mp

. (C

,I,A

)

④ P

urg

e u

nit p

ressu

re (

I)

⑦ H

PG

in

term

ed

iate

so

lutio

n t

em

p.

(I,A

)

⑨ H

ot

wa

ter

flo

w (

A)

⑩ B

urn

er

flu

e o

ut

tem

p.

(I,A

)

⑫ H

PG

pre

ssu

re (

C,I

,A)

⑭ B

urn

er

HP

G s

olu

tio

n le

ve

l (C

,I)

⑮ G

as f

lue

HP

G s

olu

tio

n le

ve

l (C

,I)

⑯ G

as f

lue

in

let

tem

p.

(I)

⑰ G

as f

lue

ou

t te

mp

. (I

)

(I)−

Dis

pla

y

(C)−

Co

ntr

ol

(A)−

Ala

rm

#�� ���#�� �

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H2 T

ype

Dire

ct F

ired

Lith

ium

Bro

mid

e Ab

sorp

tion

Chill

er/H

eate

r� H

2-t

ype d

irect

fired

lit

hiu

m b

rom

ide ab

-

sorp

tion chiller/

heate

r is

a kin

d of

larg

e-

siz

e in

dustr

ial f

acility

to s

up

ply

cool o

r heat

with

gas

natu

ral g

as,

city

gas,

or LP

G o

r

oil

die

sel

oil

as t

he d

rivi

ng e

nerg

y and

lithiu

m b

rom

ide s

olu

tion a

s t

he a

bsorb

ent

and

wate

r as r

efr

igera

nt.

H2-t

ype

dire

ct

fired

chiller/

heate

r,

usin

g

fuel

as t

he e

nerg

y sourc

e

with

only

lim

-

ited

ele

ctr

icity

as a

uxi

liary

pow

er

, not only

red

uces g

reatly

the c

ost fo

r ele

ctr

icity

and

op

era

tes in

regio

ns w

here

there

are

cheap

natu

ral gas r

esourc

es,

but

als

o c

om

pen-

sate

s

the

peak-

valle

y lo

ad

d

iffere

nce.

When the h

ot sum

mer ro

lls in

, short

age o

f

ele

ctr

ic p

ow

er

will p

oses a

gre

at

worr

y fo

r

various c

ities.

Concentr

ate

d c

onsum

ptio

n

of

pow

er

by

air-

cond

itioners

is t

he s

tick-

ing p

oin

t fo

r such a

seasonal p

rob

lem

, fo

r

whic

h,

H2-t

ype d

irect

fired

chiller/

heate

r

offer

an a

ttra

ctiv

e s

olu

tion.

The m

ost att

ractiv

e featu

re o

f S

huanglia

ng

H2-t

ype

dire

ct

fired

chiller/

heate

r is

its

stu

nnin

g p

erf

orm

ance in

energ

y savi

ng.

Hig

h C

OP

of

1.3

25

and

pro

venly

hig

h e

f-

ficie

ncy

rank

Shuanglia

ng H

2-t

ype d

irect

fired

chiller/

heate

r in

the l

ead

ing p

ositi

on

world

wid

e.

Shuanglia

ng

H2-t

ype

dire

ct

fired

chiller/

heate

r are

w

idely

ap

plie

d

in

ind

ustr

ies,

such

as

pre

cis

ion

machin

ery

m

anufa

c-

turing,

instr

um

ents

&

m

ete

rs,

avi

atio

n &

aero

sp

ace,

textil

es,

ele

ctronic

s,

ele

ctr

ic

pow

er, m

eta

llurg

y, p

harm

aceutic

als

, cig

a-

rettes,

chem

icals

, hosp

itals

, fo

od,

etc

. B

y

util

izin

g d

oze

ns o

f p

ate

nte

d t

echnolo

gie

s

with

featu

res o

f extrem

ely

hig

h e

nerg

y ef-

ficie

ncy

and o

uts

tand

ing e

nvi

ronm

enta

l ef-

fects

, in

ad

diti

on t

o h

er

custo

mer

serv

ice

exp

erience o

f ove

r 25

years

, S

huanglia

ng

guara

nte

es t

o r

ew

ard

her

users

with

op

ti-

mal r

etu

rns.

26

27

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ate

r to

be c

hill

ed

of

12℃

is s

up

plie

d i

nto

the

tub

es o

f eva

pora

tor, a

nd

coole

d t

o 7℃

by

the s

pra

yed

refrig

er-

ant, a

nd

retu

rns t

o t

he e

xtern

al sys

tem

. R

efrig

era

nt

gain

s t

he h

eat

from

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xtern

al sys

tem

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es v

ap

or, w

hic

h e

nte

rs t

he

ab

sorb

er.

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r so

lutio

n,

as a

n a

bso

rbent,

po

ssesses s

tro

ng

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sorb

ing c

ap

acity

to w

ate

r va

por

and

is s

pra

yed

on t

he h

eat-

ex-

changin

g t

ub

es o

f th

e

ab

sorb

er

to a

bsorb

the v

ap

or

genera

ted

in

the e

vap

ora

tor

and

is t

hen d

ilute

d.

Heat

of solu

tion

i.e.

heat

from

the e

xtern

al s

yste

m is

carr

ied

aw

ay

by

the c

oolin

g w

ate

r from

the

coolin

g t

ow

er

thro

ugh h

eat

exc

hange t

ub

es in t

he a

bsorb

er, a

nd

dilu

ted

solu

tion c

olle

cts

und

er

the b

ottom

of

the a

bsorb

er, a

fter

bein

g p

urg

ed

by

solu

tion p

um

p a

nd

heate

d in

the h

eat exc

hanger,

it ente

rs the H

PG

.

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arg

e q

uantit

y of

vap

or

is g

enera

ted

by

heatin

g t

he s

olu

tion w

ith h

igh-t

em

pera

ture

flam

e a

nd

meanw

hile

the s

olu

tion is c

oncentrate

d into

inte

rmed

i-

ate

solu

tion,

whic

h e

nte

rs w

ith v

ap

or

the low

pre

ssure

genera

tor

after bein

g c

oole

d d

ow

n though h

igh-t

em

pera

ture

heat exc

hanger.

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he i

nte

rmed

i-

ate

solu

tion,

whic

h is c

oole

d d

ow

n a

nd

ente

rs t

he L

PG

, is

once

again

heate

d b

y va

por

from

HP

G a

nd

vap

or

genera

ted

. The s

olu

-

tion is f

urther

concentrate

d.

The s

trong s

olu

tion fl

ow

s b

ack

to t

he

ab

sorb

er

after

bein

g c

oole

d d

ow

n t

hro

ugh h

eat-

exc

hangin

g in t

he

low

-tem

pera

ture

heat exc

hanger. T

he v

apor th

us g

enera

ted e

nte

rs

the c

ond

enser. T

he v

ap

or

from

HP

G is c

ond

ensed

to w

ate

r after

heatin

g t

he s

olu

tion a

nd

ente

rs t

he c

ond

enser

after

bein

g r

egu-

late

d.

In H

P g

enera

tor

solu

tion is h

eate

d t

o p

rod

uce v

ap

or, w

hic

h is led

to t

he e

vap

ora

tor

to h

eat

the h

ot

wate

r in

the t

ub

es.

Strong s

olu

tion

mix

es w

ith refrig

era

nt w

ate

r to

form

weak

solu

tion. Then s

olu

tion is

pum

ped

to H

P g

enera

tor to

rep

eat th

e c

ircula

tion a

nd

heatin

g.

Durin

g c

hangin

g c

hiller/

heate

r from

coolin

g m

od

e t

o h

eatin

g m

od

e,

two c

hangeove

r va

lves

see fl

ow

chart

should

be o

pened s

imulta

-

neously,

and

coolin

g w

ate

r p

um

p a

nd

refrig

era

nt p

um

p s

hould

be s

hut d

ow

n.

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g w

ate

r flo

ws t

hro

ugh t

ub

es in t

he c

ond

enser

and

cond

enses t

he v

ap

or

outs

ide t

he t

ub

es into

refrig

era

nt

wate

r.

The p

rod

uced

refrig

era

nt

wate

r ente

rs t

he e

vap

ora

tor

thro

ugh U

pip

e a

s r

efrig

era

nt ele

ment fo

r re

frig

era

tion.

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tem

pera

ture

heat

exc

hanger

is u

sed

to e

xchange h

eat

betw

een t

he s

olu

tion f

rom

LP

G a

nd

weak

solu

-

tion f

rom

ab

sorb

er

to incre

ase t

he t

em

pera

ture

of

weak

solu

tion

and

thus to r

ecove

r th

e h

eat of strong s

olu

tion.

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igh t

em

pera

ture

heat

exc

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sed

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xchange h

eat

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een t

he i

nte

rmed

iate

solu

tion f

rom

HP

G

and

the w

eak

solu

tion a

fter

bein

g h

eate

d in t

he low

tem

per a

ture

heat

exc

hanger, t

o f

urther

incre

ase t

he t

em

pera

ture

of

weak

solu

-

tion.

Heat

exc

hangers

are

used

to d

ecre

ase t

he h

eat

consum

ptio

n in

the H

PG

and

red

uce t

he c

oolin

g w

ate

r lo

ad

req

uire

d f

or

low

erin

g

the t

em

pera

ture

of

str

ong s

olu

tion,

whic

h i

s v

ital

to t

he e

nerg

y-

savi

ng e

fficie

ncy

of th

e u

nit.

Ch

ille

d w

ate

ro

ut

Co

olin

g w

ate

ro

ut

Re

frig

era

nt

pu

mp

HT

he

at

exc

ha

ng

er

Co

nd

en

se

r

Ab

so

rbe

rE

va

po

rato

r

Flue gas out

HP

ge

ne

rato

rC

ha

ng

e-o

ve

r

By-p

ass

va

lve

32 19

8

13

7

14

12

56

Ch

ec

k v

alv

e

10

Exh

au

st

Va

cu

um

pu

mpOil trap

4

Auto purging unit

Auto decrystallization pipe

11

LP

ge

ne

rato

r

Co

ole

r

Co

ole

r in

let

va

lve

va

lve

Ch

ille

d w

ate

rin

Co

olin

g w

ate

rin

Ab

so

rbe

r

Sa

mp

ling

va

lve

So

lutio

np

um

p

Ch

an

ge

-ove

rva

lve

LT h

ea

te

xc

ha

ng

er

Fla

me

Flu

e g

as

Coolin

g w

ate

r

Chill

ed

wate

r

Str

ong

Solu

tion

Inte

rmed

iate

Solu

tion

Weak S

olu

tion

HP

G r

efr

igera

nt vap

or

Refr

igera

nt w

ate

r

Refr

igera

nt vap

or

① C

hill

ed

wate

r in

let te

mp

. (I)

② C

hill

ed

wate

r outle

t te

mp

. (C

,I,A

)

③ C

oolin

g w

ate

r in

let te

mp

. (C

,I,A

)

④ A

uto

-purg

ing

unit p

ressure

(I)

⑤ L

PG

str

ong

solu

tion tem

p. (C

,I)

⑥ C

ond

ensatio

n tem

p. (C

,I,A

)

⑦ H

PG

inte

rmed

iate

solu

tion tem

p. (I,A

)

⑧ E

vap

ora

tion tem

p. (I,A

)

⑨ C

hill

ed

wate

r flo

w (

A)

⑩ F

lue g

as e

xit tem

p. (I,A

)

⑪ D

e-c

rysta

llizatio

n p

ipe tem

p. (I,A

)

⑫ H

PG

pre

ssure

(C

,I,A

)

⑬ H

PG

pre

ssure

(C

,I,A

)

⑭ H

PG

solu

tion le

vel (C

,I)

(I)-

-Ind

icatio

n

(C)-

-Contr

ol

(A)-

-Ala

rm

13

7

41

1

8

3

19

14

12

56

2

10

Ho

t w

ate

ro

ut

Ho

t w

ate

rin

HT

he

at

exc

ha

ng

er

LT h

ea

te

xc

ha

ng

er

Flue gas out

HP

ge

ne

rato

r

LP

ge

ne

rato

r

Co

nd

en

se

r

Auto purging unit

Oil trap

Ch

ec

k v

alv

e

Va

cu

um

pu

mp

Exh

au

st

Co

ole

r

Auto decrystallization pipe

Eva

po

rato

rA

bso

rbe

rA

bso

rbe

r

So

lutio

n p

um

pR

efr

ige

ran

t p

um

p

Co

ole

r in

let

va

lve

va

lve

va

lve

By-p

ass

Sa

mp

ling

Ch

an

ge

-ove

rva

lve

Ch

an

ge

-ove

rva

lve

Fla

me

Hot w

ate

r

Weak s

olu

tion

HP

G c

oncentr

ate

d s

olu

tion

Refr

igera

nt w

ate

r

HP

G r

efr

igera

nt vap

or

Flu

e g

as

Refr

igera

nt vap

or

① H

ot w

ate

r in

let te

mp

. (I)

② H

ot w

ate

r outle

t te

mp

. (C

,I,A

)

③ C

oolin

g w

ate

r in

let te

mp

. (C

,I,A

)

④ A

uto

-purg

ing

unit p

ressure

(I)

⑤ L

PG

str

ong

solu

tion tem

p. (C

,I)

⑥ C

ond

ensatio

n tem

p. (C

,I,A

)

⑦ H

PG

inte

rmed

iate

solu

tion

tem

p. (I,A

)

⑧ E

vap

ora

tion tem

p. (I,A

)

⑨ H

ot w

ate

r flo

w (

A)

⑩ F

lue g

as e

xit tem

p. (I,A

)

⑪ D

e-c

rysta

llizatio

n p

ipe tem

p. (I,A

)

⑫ H

PG

pre

ssure

(C

,I,A

)

⑬ S

trong

soltu

ion s

pra

y tem

p. (C

,I)

⑭ H

PG

solu

tion le

vel (C

,I)

(I)-

-Ind

icatio

n

(C)-

-Contr

ol

(A)-

-Ala

rm

28

29

,�� ���,������� �����

����5�)6

Mo

del

DF-

99

H2

132H

216

5H

219

8H

2231H

2265H

229

8H

2331H

241

3H

2

Coolin

g C

ap

acity

kW

350

470

58

070

0810

93

010

50

116

014

50

10

4kc

al/h

30

40

50

60

70

80

90

100

125

US

Rt

99

132

165

198

231

265

29

8331

413

Heatin

g C

ap

acity

10

4kc

al/h

24

32

40

48

56

64

72

80

100

Chilled

/H

ot

Wate

r

Inle

t/O

utle

t Te

mp.

Chilled

Wate

r℃

12 →

7

Inle

t/O

utle

t Te

mp.

Heate

d W

ate

r℃

56 →

60

50 →

60

Flo

w R

ate

m3/h

60

24

80

32

100

40

120

48

140

56

160

64

180

72

20

08

0250

100

Pre

ssure

Loss

mH

3O

4.4

0.7

4.5

0.7

24.7

0.7

65.7

0.9

25.6

0.9

6.2

1.0

8.8

1.41

8.8

1.41

3.8

0.6

1

Co

nnectio

n D

iam

ete

rD

Nm

m10

010

012

512

515

015

015

015

020

0

Coolin

g

Wate

r

Inle

t/O

utle

t Te

mp.

℃32 →

38

Flo

w R

ate

m3/h

85

113

141

170

198

226

255

283

353

Pre

ssure

Loss

mH

3O

6.5

6.2

6.4

6.9

7.5

7.7

5.3

5.3

7.1

Co

nnectio

n D

iam

ete

rD

Nm

m10

012

515

015

015

015

020

020

020

0

Fuel

Lig

ht O

il10

40

0kc

al/

kg

Co

nsum

ptio

nC

oolin

gkg

/h21.

328.5

35.6

42.7

49.8

56.9

64

71.1

88.9

Heatin

g24.6

32.8

4149.2

57.

465.6

73.8

82

102.5

Co

nnectio

n D

iam

ete

rG

in3/8

"

Heavy

Oil

10

00

0kc

al/

kg

Co

nsum

ptio

nC

oolin

gkg

/h22.2

29.6

37

44.4

51.8

59.2

66.6

7492.5

Heatin

g25.6

34.1

42.7

51.2

59.7

68.2

76.8

85.3

106.6

Co

nnectio

n D

iam

ete

rG

in2"

City

Gas

35

00

kcal/

Nm

3

Den-

sity=

0.6

2

Co

nsum

ptio

nC

oolin

gN

m3/h

63.4

84.5

105.6

126.8

147.

916

9.0

190.2

211

.326

4.1

Heatin

g73.1

97.

512

1.8

146.2

170.6

194.9

219

.324

3.7

30

4.6

Inle

t P

ressure

mm

H3O

20

0~

30

00

40

0~

30

00

50

0~

30

00

Co

nnectio

n D

iam

ete

rG

mm

in2"

65

80

Natu

ral G

as

110

00

kcal/

Nm

3

Den-

sity=

0.6

4

Co

nsum

ptio

nC

oolin

gN

m3/h

20.2

26.9

33.6

40.3

47.1

53.8

60.5

67.

28

4

Heatin

g23.3

31

38.8

46.5

54.3

62

69.8

77.

59

6.9

Inle

t P

ressure

mm

H3O

150~250

0250~250

0350~250

04

00~

30

00

Co

nnectio

n D

iam

ete

rG

mm

in1 1

/2"

2"

65

Air

Flo

w fo

r C

om

bustio

n3

0℃

Coolin

gm

3/h

324

432

54

06

48

755

865

970

108

013

50

Heatin

g372

49

6620

744

86

89

92

1120

124

015

50

Exhaust C

onnectio

n D

imensio

nm

m17

0 ×250

170 ×

250

20

0 ×3

00

20

0 ×3

00

250 ×

36

0250 ×

36

0250 ×

36

0250 ×

450

250 ×

50

0

Ele

ctr

i-cal D

ata

Pow

er S

up

ply

3Φ

- 3

80

VA

C -

50

Hz

Tota

l Curr

ent

Lig

ht O

il

A

14.7

15.4

15.4

19.6

19.6

20.2

20.8

22.6

24.9

Heavy

Oil

16.9

18.9

18.9

27.

627.

627.

628.6

46.5

46.5

Gas

14.7

15.4

15.4

19.6

19.6

20.2

20.8

22.6

24.9

Ele

ctr

ic

Pow

er

Lig

ht O

il

kW

4.4

54.9

56.4

6.4

6.8

77.

38.5

Heavy

Oil

8.5

89.1

9.1

10.7

610

.76

10.7

611

20.6

721.14

Gas

4.4

54.9

56.4

6.4

6.8

77.

38.5

Ove

rall

Dim

en-

sio

ns

Leng

th

mm

38

00

3820

3810

3820

38

40

38

40

434

04

34

04810

Wid

th19

66

212

5223

023

44

2561

2561

2554

2707

28

34

Heig

ht

2332

2351

2349

241

1249

6254

4256

428

07

2897

Op

era

ting W

eig

ht

t6.7

7.8

8.9

9.5

10.3

1111

.812.2

14.3

Ship

pin

g W

eig

ht

8.2

9.6

11.1

12.2

13.6

14.5

15.6

16.5

20.3

49

6H

2579

H2

66

1H

27

44

H2

82

7H

29

92

H2

11

57

H2

13

23

H2

14

88

H2

16

53

H2

19

84

H2

26

46

H2

33

07

H2

174

02

04

02

33

02

62

02

91

03

49

04

07

04

65

05

23

05

82

06

98

09

30

01

16

30

15

0175

20

02

25

25

03

00

35

04

00

45

05

00

60

080

01

00

0

49

6579

66

17

44

82

79

92

11

57

13

23

14

88

16

53

19

84

26

46

33

07

12

014

01

60

18

02

00

24

02

80

32

03

60

40

04

80

64

08

00

12

→

7

56

→

60

5

0 →

60

30

012

03

50

14

04

00

16

04

50

18

05

00

20

06

00

24

07

00

28

08

00

32

09

00

36

01

00

0400

12

00

480

1600

640

20

00

800

3.8

0.6

14.1

0.6

64

.90

.79

6.6

1.0

66

.41

.03

8.4

1.3

58

.11

.30

8.8

1.4

11

2.4

1.9

91

1.8

1.8

92

.60.4

25

.00

.67

.51

.1

20

02

00

25

02

50

25

03

00

30

03

50

35

03

50

40

04

00

45

0

32

→

38

424

49

55

65

63

67

07

84

89

89

11

30

12

72

14

13

16

96

22

64

28

30

6.6

6.8

8.7

9.6

9.1

11.1

11

5.2

6.2

6.6

8.6

12

16

25

025

0250

250

300

350

350

400

400

400

450

500

600

10

6.7

124.4

142.2

160

177.8

213.3

248.9

284.4

320

355.5

426.6

568.8

711

123

14

3.5

164

184.5

205

246

287

328

369

410

492

656

820

1"

2-1

"

111

129.5

14

81

66

.51

85

22

2259

296

333

370

444

592

740

128

14

9.3

17

0.6

19

1.9

21

3.3

25

5.9

29

8.6

34

1.2

38

3.9

42

6.5

51

1.8

68

2.4

85

3

2"

2-2

"

316.9

36

9.7

422.5

475.4

528.2

633.8

739.4

845.1

950.7

1056.3

1267.6

1690.4

2113

36

5.5

426.4

487.3

548.2

609.1

731

852.8

974.6

1096.5

1218.3

1462

1949.6

2437

80

0-3

00

01

10

0~

30

00

13

00

~3

00

015

00

~3

00

0

80

10

01

25

15

02

-12

52

-15

0

10

0.8

117.

61

34

.41

51

.31

68

.12

01

.72

35

.32

68

.93

02

.53

36

.14

03

.35

37

.66

72

116.3

13

5.7

155.1

174.4

193.8

232.6

271.3

310.1

348.9

387.6

465.2

620

775

40

0~

30

00

55

0~

30

00

80

0~

30

00

10

00

~3

00

01

20

0~

30

00

65

80

100

125

2-8

02-1

00

162

018

90

21

60

24

30

27

00

32

40

37

80

43

20

48

60

54

00

64

80

88

50

11

00

0

18

60

2170

24

80

27

90

31

00

37

20

43

40

49

60

55

80

62

00

74

40

99

50

12

50

0

30

0×

50

03

00×

50

03

60×

55

03

60×

55

04

00×

60

04

20×

70

04

20×

70

05

50×

75

05

50×

75

05

50×

75

06

50×

800

2-5

50×

75

0

3Φ

- 3

80

VA

C -

50

Hz

28.9

28.9

30

.84

3.5

43

.55

8.6

59

.56

2.5

62

.56

8.3

90

.512

3.1

13

4.7

48.8

50.8

50.8

61.1

62.1

71

89.6

91.3

91.6

111.4

124.4

180.7

220.9

28.9

28.9

30

.84

14

15

5.8

57

.560.5

76.5

82.3

83.4

119.1

162.7

11.8

11.8

12.8

17.9

17.9

24.6

25.1

26.1

24.6

24.6

41.4

550.8

50.8

22.4

82

2.9

52

4.1

28

.19

28

.13

3.7

14

44

6.2

44

6.4

34

8.5

75

6.2

99

1.7

39

6.3

9

11.4

11.4

12

.41

6.9

16

.92

3.6

24

.12

5.1

32

.13

3.6

33

.14

8.8

65

.8

48

85

48

85

53

08

57

25

59

60

72

30

72

30

72

30

79

30

79

60

91

50

98

50

11

58

0

312

03170

32

20

34

00

33

74

39

00

40

50

43

57

43

62

46

29

46

52

49

60

52

20

30

34

315

03218

3221

3320

3441

3720

3864

3864

4214

4224

5160

5160

16.7

18.2

20

.82

22

63

1.8

36

.24

1.2

43

.95

1.1

59

.38

9.6

11

5.2

23.4

25.1

28

.93

1.1

36

.34

5.1

51

.55

8.4

62

71

.68

4.3

11

31

45

.2

6��

*

Valu

es fo

r chilled

/heate

d/c

oolin

g w

ate

r in

ab

ove

tab

le a

re fo

r no

min

al c

ond

itio

ns a

nd c

an b

e p

rop

erly

ad

juste

d in

actu

al o

pera

tion.

!

The lo

west outle

t te

mp

era

ture

of chilled

wate

r is

5℃

0

Chilled

/Heate

d w

ate

r can b

e a

dju

ste

d in

rang

e o

f 6

0~120

%.

.

On the c

hilled

/heate

d/c

oolin

g w

ate

r sid

e, scale

facto

r is

0.0

86

m2K

/kW

0.0

001m

2·h

· ℃/k

cal.

-

Co

olin

g/H

eatin

g c

ap

acity

can b

e a

dju

ste

d in

rang

e o

f 3

0~10

5%

fo

r O

il-fir

ed

typ

e, 25

~10

5%

fo

r G

as-fi

red

typ

e.

8

No

min

al d

ischarg

e tem

pera

ture

of flu

e g

as:

170℃

fo

r co

olin

g m

od

e, 15

5℃

fo

r heatin

g m

od

e.

9

The m

axi

mum

chilled

/heate

d/c

oolin

g w

ate

r b

ox

pre

ssure

bearing c

ap

acity

of n

orm

al p

ressure

chiller

is 0

.8 M

Pa

G.

,

Heat va

lues in

dic

ate

d in

the tab

le a

re lo

w h

eat va

lues.

+

Consum

ptio

n o

f fu

el n

ot in

dic

ate

d in

the tab

le c

an b

e c

alc

ula

ted

=Low

heat va

lue in

dic

ate

d in

the tab

le/L

ow

heat va

lue o

f ad

op

ted fuel ×

consum

ptio

n

ind

icate

d in

the tab

le.

*/G

as in

let p

ressure

ind

icate

d in

the tab

le is

the p

ressure

at th

e o

utle

t of b

all

valv

e then the c

hiller

is u

nd

er op

era

tion..

**G

as R

ela

tive D

ensity

= G

as d

ensity/

Air

density

*!O

vera

ll d

imensio

ns in

dic

ate

d in

the tab

le in

clu

de r

ack

dim

ensio

ns.

*0T

he s

hip

pin

g w

eig

ht in

clu

des the r

ack

weig

ht, e

xlud

ing s

olu

tion w

eig

ht.

*.W

hen r

efe

rrin

g t

o C

hilled

/Heate

d W

ate

r sub

-regio

n,

data

ind

icate

d in t

he r

ound b

racke

ts a

re p

ara

mete

rs in h

eatin

g m

od

e w

ith inle

t/outle

t te

mp

era

-

ture

diffe

rence a

s 1

0℃

.

30

31

�St

eam

-Ope

rate

d Do

uble

Eff

ect

Lith

ium

Bro

mid

e Ab

sorp

tion

Chill

er

H2

-typ

e s

team

op

era

ted

doub

le e

ffect

lithiu

m b

rom

ide a

bsorp

tion c

hiller

is a

kin

d o

f la

rge-s

ize ind

ustria

l fa

cility

with

ste

am

as t

he d

rivin

g

energ

y and

lith

ium

bro

mid

e s

olu

tion a

s the a

bsorb

ent and

wate

r as r

efrig

era

nt.

H2

-typ

e s

team

op

era

ted

doub

le e

ffect

units

, usin

g s

team

as t

he e

nerg

y sourc

e,

not

only

red

uces g

reatly

the c

ost

for

ele

ctric

ity a

nd

op

-

era

tion fees in r

egio

ns w

here

there

are

ric

h s

team

resourc

es,

but

als

o c

om

pensate

s t

he p

eak-

valle

y lo

ad

diff

ere

nce.

When t

he h

ot

sum

-

mer

rolls

in,

shortage o

f ele

ctric

pow

er

will p

oses a

gre

at w

orr

y fo

r va

rious c

ities.

Concentrate

d c

onsum

ptio

n o

f p

ow

er

by

air-

cond

itioners

is the s

ticki

ng p

oin

t fo

r such a

seasonal p

rob

lem

, fo

r w

hic

h,

H2

-typ

e s

team

op

era

ted

doub

le e

ffect chillers

offer

an a

ttra

ctiv

e s

olu

tion.

The m

ost

attra

ctiv

e f

eatu

re o

f S

huanglia

ng H

2-t

ype s

team

op

era

ted

doub

le e

ffect

chiller

is its

stu

nnin

g p

erform

ance in e

nerg

y savi

ng.

Hig

h C

OP

of 1

.33

and

pro

venly

hig

h e

fficie

ncy

rank

Shuanglia

ng H

2-t

ype s

team

op

era

ted

chiller

in the le

ad

ing p

ositi

on w

orld

wid

e.

Shuanglia

ng H

2-t

ype s

team

op

era

ted

doub

le e

ffect

chillers

are

wid

ely

ap

plie

d in ind

ustrie

s,

such a

s p

recis

ion m

achin

ery

manufa

ctu

ring,

instrum

ents

& m

ete

rs,

avi

atio

n &

aero

sp

ace,

text

iles,

ele

ctronic

s,

ele

ctric

pow

er, m

eta

llurg

y, p

harm

aceutic

als

, cig

are

ttes,

chem

icals

, hos-

pita

ls,

food

, etc

. B

y util

izin

g d

oze

ns o

f p

ate

nte

d t

echnolo

gie

s w

ith f

eatu

res o

f ext

rem

ely

hig

h e

nerg

y effi

cie

ncy

and

outs

tand

ing e

nvi

ron-

menta

l effects

, in

ad

diti

on to h

er

custo

mer

serv

ice e

xperie

nce o

f ove

r 2

5 y

ears

, S

huanglia

ng g

uara

nte

es to r

ew

ard

her

users

with

op

timal

retu

rns.

�������������� �����������������������������������������������&�7��������������������7��

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%3������

Wate

r to

be c

hill

ed

of

12℃

is s

up

plie

d i

nto

the t

ub

es o

f

eva

pora

tor, a

nd

coole

d to 7℃

by

the s

pra

yed

refrig

era

nt, a

nd

retu

rns to the

ext

ern

al s

yste

m.

Refrig

era

nt gain

s the h

eat from

the c

hilled

wate

r of ext

ern

al

sys

tem

, and

becom

es v

ap

or, w

hic

h e

nte

rs the a

bsorb

er.

�������

LiB

r solu

tion,

as a

n a

bsorb

ent,

possesses s

trong a

bsorb

ing

cap

acity

to w

ate

r va

por

and

is s

pra

yed

on t

he h

eat-

exc

hangin

g t

ub

es o

f

the a

bsorb

er

to a

bsorb

the v

ap

or

genera

ted

in t

he e

vap

ora

tor

and

is t

hen

dilu

ted

. H

eat of solu

tion

i.e.

heat from

the c

hilled

wate

r of ext

ern

al s

yste

m

is c

arr

ied

aw

ay

by

the c

oolin

g w

ate

r from

the c

oolin

g t

ow

er

thro

ugh h

eat

exc

hange t

ub

es in t

he a

bsorb

er, a

nd

weak

solu

tion c

olle

cts

und

er

the b

ot-

tom

of th

e a

bsorb

er. A

fter

bein

g p

urg

ed

by

solu

tion p

um

p a

nd

heate

d in

the

heat exc

han

ger, it

ente

rs the H

PG

.

�&�����������������

here

inafter

HP

G

Larg

e q

uantit

y of

vap

or

is

genera

ted

by

heatin

g t

he s

olu

tion w

ith h

igh-t

em

pera

ture

ste

am

and

mean-

while

the s

olu

tion is c

oncentrate

d into

inte

rmed

iate

solu

tion,

whic

h e

nte

rs

the low

pre

ssure

genera

tor

after

bein

g c

oole

d d

ow

n t

hro

ugh h

igh-t

em

pera

-

ture

heat

exc

hanger. T

he r

efrig

era

nt

vap

or

is a

lso f

ed

into

the low

pre

ssure

genera

tor.

�(����������������

here

inafter

LP

G

The inte

rmed

iate

solu

tion,

whic

h is c

oole

d d

ow

n a

nd

ente

rs t

he L

PG

, is

once a

gain

heate

d b

y va

por

from

HP

G.

The s

olu

tion is f

urther

concentrate

d.

The s

trong s

olu

tion fl

ow

s

back

to t

he a

bsorb

er

after

bein

g c

oole

d d

ow

n t

hro

ugh h

eat-

exc

hangin

g in

the low

-tem

pera

ture

heat

exc

hanger. T

he v

ap

or

thus g

enera

ted

ente

rs t

he

cond

enser. T

he v

ap

or

from

HP

G is c

ond

ensed

to w

ate

r after

heatin

g t

he

solu

tion a

nd

ente

rs the c

ond

enser

thro

ugh thro

ttle

.

�� �����@

Co

olin

g w

ate

r flo

ws t

hro

ug

h t

ub

es i

n t

he c

ond

enser

and

cond

enses the v

ap

or

outs

ide the tub

es in

to r

efrig

era

nt w

ate

r. T

he p

rod

uced

refrig

era

nt w

ate

r ente

rs the e

vapora

tor th

rough U

pip

e a

s refrig

era

nt ele

ment

for

refrig

era

tion.

�� ���%4����&��

Low

tem

pera

ture

heat

exc

hanger

is u

sed

to e

x-

change h

eat

betw

een

the s

olu

tion f

rom

LP

G a

nd

weak

solu

tion f

rom

ab

-

sorb

er

to incre

ase t

he t

em

pera

ture

of

dilu

ted

solu

tion a

nd

thus t

o r

ecove

r

the h

eat of strong s

olu

tion.

�� �����������4����&��

H

eat

exc

hangin

g b

etw

een w

ork

ing s

team

cond

ensate

and

weak

solu

tion a

fter

bein

g h

eate

d in

LT h

eat exc

hanger

fur-

ther

incre

ase the tem

pera

ture

of th

e w

eak

solu

tion.

� ���%4����&��

Hig

h t

em

pera

ture

heat

exc

hanger

is u

sed

to e

x-

change h

eat

betw

een t

he i

nte

rmed

iate

solu

tion f

rom

HP

G a

nd

the w

eak

solu

tion a

fter

bein

g h

eate

d in

the lo

w tem

pera

ture

heat exc

hanger, to further

incre

ase the tem

pera

ture

of w

eak

solu

tion.

Heat

exc

hangers

are

used t

o d

ecre

ase t

he h

eat

consum

ptio

n in t

he H

PG

and r

educe t

he c

oolin

g w

ate

r lo

ad r

equire

d f

or

low

erin

g t

he t

em

pera

ture

of

strong s

olu

tion, w

hic

h is

vita

l to the e

nerg

y-savi

ng e

fficie

ncy

of th

e u

nit.

������ 0��������#�� ���#�� �

-�.��!���������

#�� ���#�� �

������������ ������

�����

�����������������

���������������

���������� ���

��������������

���������� ���

�� �� ����

���������� ���

�� �� ����

��

����������

���������

�������

������� �� ��

������������!���� �����

"���

���

������

�#��� �����

�#��� ������

�� �� ���

�����

���

$�%������ �

������

�� �

����

&�'����

����

�������

�������

(���������

���� �������

�

���� ������

�

���� ������

��

���� �������

��

⑩S

team

Condensate

Strong s

olu

tion

Inte

rmedia

te s

olu

tion

Weak

solu

tion

HP

G refrig

era

nt va

por

Coolin

g w

ate

r

Chilled w

ate

r

Refrig

era

nt w

ate

r

Refrig

era

nt va

por

① C

hilled w

ate

r in

let te

mp. (I)

② C

hilled w

ate

r outle

t te

mp. (C

,I,A

)

③ C

oolin

g w

ate

r in

let te

mp. (C

,I,A

)

④ A

uto

-purg

ing u

nit

pre

ssure

(I)

(C

)—C

ontr

ol

(A

)—A

larm

(I)

—In

dic

atio

n

⑤ L

ow

pre

ssure

genera

tor S

trong s

olu

tion tem

p. (C

,I)

⑥ C

ondensatio

n tem

p. (C

,I,A

)

⑦ H

igh p

ressure

genera

tor in

term

edia

te s

olu

tion tem

p. (I,

A)

⑧ E

vapora

tion tem

p. (I,

A)

⑨ C

hilled w

ate

r flo

w (A

)

⑩ S

team

condensate

tem

p. (I)

⑪ D

e-c

rysta

lliza

tion p

ipe tem

p. (I,

A)

⑫ H

igh p

ressure

genera

tor pre

ssure

(C,I,

A)

⑬ S

trong s

olu

tion s

pra

y te

mp. (C

,I)

⑭ H

igh p

ressure

genera

tor

solu

tion le

vel(C

,I)

⑮ S

team

pre

ssure

(C

,I,A

)

32

33

,�� ���,������� �����

����5@!A'

��65�

)6

���������������'�������

Mod

el

ST-

99

H2

H1

32

H2

H1

65

H2

H1

98

H2

H2

31

H2

H2

65

H2

H2

98

H2

H3

31

H2

H4

13

H2

H4

96

H2

H

Coolin

g C

ap

acity

kW3

50

47

05

80

70

08

10

93

01

05

01

16

01

45

01

74

0

10

4kc

al/h

30

40

50

60

70

80

90

10

01

25

15

0

US

Rt

99

13

21

65

19

82

31

26

52

98

33

14

13

49

6

Chilled Water

Inle

t/outle

t Te

mp

.℃

12

→

7

Flo

w R

ate

m3/h

60

80

10

01

20

14

01

60

18

02

00

25

03

00

Pre

ssure

Loss

mH

2H

O5

.55

.55

.75

.87

.87

.37

.91

0.9

11

5.5

Connectio

n D

iam

ete

rD

Nm

m1

00

10

01

25

12

51

50

15

01

50

15

02

00

20

0

Cooling Water

Inle

t/outle

t Te

mp

.℃

32

→

38

Flo

w R

ate

m3/h

85

11

31

42

17

01

98

22

72

55

28

33

54

42

5

Pre

ssure

Loss

mH

2H

O7

.26

.97

7.4

98

.98

.56

6.6

8.4

Connectio

n D

iam

ete

rD

Nm

m1

00

12

51

50

15

01

50

15

02

00

20

02

00

25

0

Steam

Consum

ptio

nkg

/h3

72

49

66

20

74

48

68

99

21

11

61

24

01

55

01

86

0

Ste

am

Cond

ensate

Tem

p.

℃≤

95

Ste

am

Cond

ensate

Back

Pre

ssure

GM

Pa

≤0

.05

Ste

am

Pip

e D

iam

ete

rD

Nm

m4

05

05

05

06

56

56

56

58

08

0

Ele

ctric

Mod

ula

ting V

alv

e

Dia

.D

Nm

m4

04

04

04

04

05

05

05

06

56

5

Ste

am

Cond

ensate

Pip

e

Dia

mete

rD

Nm

m2

52

52

52

52

53

23

23

23

24

0

Electrical Data

Pow

er

Sup

ply

3Φ

- 3

80

VA

C -

50

Hz

Tota

l Curr

ent

A8

10

10

10

17

.31

7.3

20

.32

0.8

20

.82

1.8

Ele

ctric

Pow

er

kW3

.84

.14

.14

.15

.95

.96

.87

77

.2

Overall Dimensions

Length

mm

38

10

38

10

37

90

37

90

38

20

38

40

38

90

43

57

43

57

48

95

Wid

th1

94

22

02

72

06

02

06

02

18

32

30

82

35

52

33

22

45

02

55

8

Heig

ht

21

52

21

70

21

69

22

17

22

31

23

16

23

64

23

84

27

02

27

17

Op

era

ting W

eig

ht

t6

.46

.97

.37

.98

.39

9.6

10

.11

11

3.1

Ship

pin

g W

eig

ht

7.7

8.5

9.1

9.8

10

.31

1.4

12

.11

3.4

14

.61

7.4

Mod

el

ST-

57

9H

2H

66

1H

2H

74

4H

2H

82

7H

2H

99

2H

2H

11

57

H2

H1

32

3H

2H

14

88

H2

H1

65

3H

2H

19

84

H2

H

Coolin

g C

ap

acity

kW2

04

02

33

02

62

02

91

03

49

04

07

04

65

05

23

05

82

06

98

0

10

4kc

al/h

17

52

00

22

52

50

30

03

50

40

04

50

50

06

00

US

Rt

57

96

61

74

48

27

99

21

15

71

32

31

48

81

65

31

98

4

Chilled Water

Inle

t/outle

t Te

mp

.℃

12

→

7

Flo

w R

ate

m3/h

350

400

450

500

600

700

800

900

1000

1200

Pre

ssure

Loss

mH

2H

O5

.25

.36

.18

.28

.11

1.5

10

.51

1.1

15

.31

4.1

Connectio

n D

iam

ete

rD

Nm

m2

00

25

02

50

25

03

00

30

03

50

35

03

50

400

Cooling Water

Inle

t/outle

t Te

mp

.℃

32

→

38

Flo

w R

ate

m3/h

49

65

67

63

87

09

85

09

92

11

34

12

75

14

17

17

00

Pre

ssure

Loss

mH

2H

O8

.18

.71

0.2

10

.81

1.2

14

.31

4.1

5.9

7.6

6.9

Connectio

n D

iam

ete

rD

Nm

m2

50

25

02

50

30

03

00

35

03

50

40

04

00

45

0

Steam

Consum

ptio

nkg

/h2

17

02

48

02

79

03

10

03

72

04

34

04

96

05

58

06

20

07

44

0

Ste

am

Cond

ensate

Tem

p.

℃≤

95

Ste

am

Cond

ensate

Back

Pre

ssure

GM

Pa

≤0

.05

Ste

am

Pip

e D

iam

ete

rD

Nm

m80

80

100

100

100

125

125

150

150

150

Ele

ctric

Mod

ula

ting V

alv

e

Dia

.D

Nm

m65

80

80

80

80

100

100

100

125

65

Ste

am

Cond

ensate

Pip

e

Dia

mete

rD

Nm

m40

40

40

40

50

50

50

65

65

65

Electrical Data

Pow

er

Sup

ply

3Φ

- 3

80

VA

C -

50

Hz

Tota

l Curr

ent

A2

2.8

22

.82

2.8

28

.63

33

33

6.6

37

.64

9.4

49

.4

Ele

ctric

Pow

er

kW7

.57

.57

.59

9.5

9.5

12

12

.513

.915

Overall Dimensions

Length

mm

49

18

49

18

53

08

58

05

57

95

65

25

65

25

68

13

75

13

75

70

Wid

th2

74

02

76

02

81

52

80

02

93

03

20

93

33

43

35

43

35

43

75

6

Heig

ht

28

54

29

70

30

38

30

41

33

35

33

81

36

69

38

04

38

04

42

54

Op

era

ting W

eig

ht

t1

4.5

16

.21

6.8

20

.22

4.2

26

.63

1.5

33

39

46

Ship

pin

g W

eig

ht

20

21

.92

2.8

28

.43

3.4

37

.24

4.2

48

54

.76

4.2

6���

*

Valu

es fo

r ste

am

,chilled

wate

r and c

oolin

g w

ate

r in

ab

ove

tab

le a

re fo

r no

min

al c

ond

itio

ns a

nd c

an b

e p

rop

erly

ad

juste

d in

actu

al o

pera

tion.

W

ith the in

let/

outle

t te

mp

era

ture

of co

olin

g w

ate

r as 3

0℃

/36℃

, th

e s

team

co

nsum

ptio

n is

only

12.2

kg/

10

4kc

al/h

, and

the C

OP

valu

e is

1.4

3.

!

Ste

am

pre

ssure

0. 8

Mp

aG

refe

rs to the in

let p

ressure

with

out any

valv

e p

ressure

loss. The lo

west outle

t te

mp

era

ture

of chilled

wate

r is

5℃

0

Co

olin

g c

ap

acity

can b

e a

dju

ste

d in

rang

e o

f 2

0~10

0%

, a

nd

chilled

wate

r can b

e a

dju

ste

d in

rang

e o

f 6

0~12

0%

.

.

On the c

hilled

wate

r/co

olin

g w

ate

r sid

e, scale

facto

r is

0.0

86

m2K

/kW

0.0

001m

2·h

· ℃/k

cal.

-

The m

axi

mum

chilled

/co

olin

g w

ate

r b

ox

pre

ssure

bearing c

ap

acity

of n

orm

al p

ressure

chiller

is 0

.8 M

Pa

G.

8

The u

nit

is t

ransp

ort

ed w

ith r

ack

of

18

0m

m in h

eig

ht, a

nd f

or

the u

nits

ST-

992H

2H

and a

bove

, sub

merg

ed t

ype r

ack

will b

e a

dop

ted,

extr

a 6

0m

m

shall

be in

clu

ded.

9

The s

hip

pin

g w

eig

ht in

clu

des the r

ack

weig

ht, e

xlud

ing s

olu

tion w

eig

ht.

34

35

,�� ���,������� �����

����5@!B'��65�

)6

Mod

el

ST-

99

H2

13

2H

21

65

H2

19

8H

22

31

H2

26

5H

22

98

H2

33

1H

24

13

H2

49

6H

25

79

H2

Coolin

g C

ap

acity

kW3

50

47

05

80

70

08

10

93

01

05

01

16

01

45

01

74

02

04

0

10

4kc

al/h

30

40

50

60

70

80

90

10

01

25

15

01

75

US

Rt

99

13

21

65

19

82

31

26

52

98

33

14

13

49

65

79

Chilled Water

Inle

t/outle

t Te

mp

.℃

12

→

7

Flo

w R

ate

m3/h

60

80

10

01

20

14

01

60

18

02

00

25

03

00

35

0

Pre

ssure

Loss

mH

2O

4.4

4.5

4.7

5.7

5.6

6.2

8.8

8.8

3.8

3.8

4.1

Connectio

n D

iam

ete

rD

Nm

m1

00

10

01

25

12

51

50

15

01

50

15

02

00

20

02

00

Cooling Water

Inle

t/outle

t Te

mp

.℃

32

→

38

Flo

w R

ate

m3/h

86

11

41

43

17

22

00

22

92

57

28

63

57

42

95

00

Pre

ssure

Loss

mH

2O

6.6

6.3

6.5

77

.67

.85

.45

.47

.26

.66

.9

Connectio

n D

iam

ete

rD

Nm

m1

00

12

51

50

15

01

50

15

02

00

20

02

00

25

02

50

Steam

Consum

ptio

nkg

/h3

76

50

16

27

75

28

77

10

03

11

28

12

53

15

66

18

80

21

93

Ste

am

Cond

ensate

Tem

p.

℃≤

90

Ste

am

Cond

ensate

Back

Pre

ssure

GM

Pa

≤0

.05

Ste

am

Pip

e D

iam

ete

rD

Nm

m4

05

05

06

56

56

56

58

08

08

08

0

Ele

ctric

Mod

ula

ting V

alv

e

Dia

.D

Nm

m4

04

04

05

05

05

05

06

56

56

58

0

Ste

am

Cond

ensate

Pip

e

Dia

mete

rD

Nm

m2

52

52

52

53

23

23

23

24

04

04

0

Electrical Data

Pow

er

Sup

ply

3Φ

- 3

80

VA

C -

50

Hz

Tota

l Curr

ent

A8

10

10

17

.31

7.3

20

.32

0.8

20

.82

1.8

22

.82

2.8

Ele

ctric

Pow

er

kW3

.84

.14

.15

.95

.96

.87

77

.27

.57

.5

Overall Dimensions

Length

mm

38

10

38

10

37

90

38

20

38

40

38

40

43

57

43

57

48

55

49

18

49

18

Wid

th1

94

22

02

72

06

02

18

32

30

82

35

52

33

22

45

02

55

82

74

02

76

0

Heig

ht

21

52

21

70

21

69

22

31

23

16

23

64

23

84

26

27

27

17

28

54

29

70

Op

era

ting W

eig

ht

t6

.57

.17

.58

.19

9.4

10

.11

0.5

12

.81

4.5

15

.6

Ship

pin

g W

eig

ht

7.8

8.7

9.3

10

.11

1.4

11

.91

3.4

14

17

.12

02

1.3

Model

ST-

661H

2744H

2827H

2992H

21157H

21323H

21488H

21653H

21984H

22646H

23307H

2

Coolin

g C

ap

acity

kW2

33

02

62

02

91

03

49

04

07

04

65

05

23

05

82

06

98

09

30

01

16

30

10

4kc

al/h

200

225

250

300

350

400

450

500

600

800

1000

US

Rt

66

17

44

82

79

92

11

57

13

23

14

88

16

53

19

84

26

46

33

07

Chilled Water

Inle

t/outle

t Te

mp

.℃

12

→

7

Flo

w R

ate

m3/h

400

450

500

600

700

800

900

1000

1200

1600

2000

Pre

ssure

Loss

mH

2O

4.9

6.6

6.4

8.4

8.1

8.8

12.4

11.8

2.6

57

.5

Connectio

n D

iam

ete

rD

Nm

m2

50

25

02

50

30

03

00

350

350

350

400

400

450

Cooling Water

Inle

t/outle

t Te

mp

.℃

32

→

38

Flo

w R

ate

m3/h

57

26

43

71

58

58

10

01

11

44

12

87

14

30

17

16

22

88

28

60

Pre

ssure

Loss

mH

2O

8.8

9.8

9.2

11

.31

1.2

5.2

6.3

6.7

8.7

12

16

Connectio

n D

iam

ete

rD

Nm

m2

50

25

03

00

35

03

50

40

04

00

40

04

50

50

06

00

Steam

Consum

ptio

nkg

/h2

50

62

81

931

33

37

59

43

86

50

12

56

39

62

65

75

18

10

02

41

25

30

Ste

am

Cond

ensate

Tem

p.

℃≤

90

Ste

am

Cond

ensate

Back

Pre

ssure

GM

Pa

≤0

.05

Ste

am

Pip

e D

iam

ete

rD

Nm

m1

00

10

01

00

12

51

25

15

01

50

15

0150

200

200

Ele

ctric

Mod

ula

ting V

alv

e

Dia

.D

Nm

m80

80

100

100

100

125

125

125

150

150

200

Ste

am

Cond

ensate

Pip

e

Dia

mete

rD

Nm

m40

40

50

50

50

65

65

65

6 5

80

100

Electrical Data

Pow

er

Sup

ply

3Φ

- 3

80

VA

C -

50

Hz

Tota

l Curr

ent

A2

2.8

28

.62

8.6

33

36

.63

7.6

37

.64

9.4

49

.47

1.8

95

.4

Ele

ctric

Pow

er

kW7

.59

99

.51

21

2.5

12

.51

3.9

15

23

.626

.4

Overall Dimensions

Length

mm

53

08

57

33

57

95

65

25

65

25

68

13

75

13

75

13

91

18

95

00

11

58

0

Wid

th2

81

52

80

02

93

03

20

93

33

43

35

43

35

43

75

63

76

644

00

4400

Heig

ht

30

38

30

41

32

60

33

81

36

69

38

04

38

04

41

54

41

64

51

00

51

00

Op

era

ting W

eig

ht

t1

6.8

18

.62

22

6.6

30

33

36

.54

3.6

51

76

10

3

Ship

pin

g W

eig

ht

22

.82

6.8

31

.13

7.2

42

.74

85

2.2

61

.872

.79

41

25

6���

*

Valu

es fo

r ste

am

,chilled

wate

r and c

oolin

g w

ate

r in

ab

ove

tab

le a

re fo

r no

min

al c

ond

itio

ns a

nd c

an b

e p

rop

erly

ad

juste

d in

actu

al o

pera

tion.

W

ith the in

let/

outle

t te

mp

era

ture

of co

olin

g w

ate

r as 3

0℃

/36℃

, th

e s

team

co

nsum

ptio

n is

onl y

12.3

5kg

/10

4kc

al/h

, and

the C

OP

valu

e is

1.4

1.

!

Ste

am

pre

ssure

0.6

Mp

aG

refe

rs to the in

let p

ressure

with

out any

valv

e p

ressure

loss. The lo

west outle

t te

mp

era

ture

of chilled

wate

r is

5℃

0

Co

olin

g c

ap

acity

can b

e a

dju

ste

d in

rang

e o

f 2

0~10

0%

, a

nd

chilled

wate

r can b

e a

dju

ste

d in

rang

e o

f 6

0~12

0%

.

.

On the c

hilled

wate

r/co

olin

g w

ate

r sid

e, scale

facto

r is

0.0

86

m2K

/kW

0.0

001m

2·h

· ℃/k

cal.

-

The m

axi

mum

chilled

/co

olin

g w

ate

r b

ox

pre

ssure

bearing c

ap

acity

of n

orm

al p

ressure

chiller

is 0

.8 M

Pa

G.

8

The u

nit

is t

ransp

ort

ed w

ith r

ack

of

18

0m

m in h

eig

ht, a

nd f

or

the u

nits

ST-

827H

2 a

nd a

bove

, sub

merg

ed t

ype r

ack

will b

e a

dop

ted,

extr

a 6

0m

m

shall

be in

clu

ded.

9

The s

hip

pin

g w

eig

ht in

clu

des the r

ack

weig

ht, e

xlud

ing s

olu

tion w

eig

ht.

36

37

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eam

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rate

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ngle

Eff

ect

Lith

ium

Bro

mid

e Ab

sorp

tion

Chill

er

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Mod

el

SX

Z4

-

83H2L

99H2L

132H2L

165H2L

198H2L

231DH2L

265H2L

331H2L

413H2L

496H2L

579H2L

661H2L

827H2L

992H2L

1157H2L

1323H2L

Coolin

g C

ap

acity

kW2

90

35

04

70

58

07

00

81

09

30

11

60

14

50

17

40

20

40

23

30

29

10

34

90

40

70

46

50

10

4kc

al/h

25

30

40

50

60

70

80

10

01

25

15

01

75

20

02

50

30

03

50

40

0

US

Rt

83

99

13

21

65

19

82

31

26

53

31

41

34

96

57

96

61

82

79

92

11

57

13

23

Chilled Water

Inle

t/O

utle

t Te

mp

.℃

12

→

7

Flo

w R

ate

m3/h

50

60

80

10

01

20

14

01

60

20

02

50

30

03

50

40

05

00

60

07

00

80

0

Cooling Water

Inle

t/O

utle

t Te

mp

.℃

32

→

38

Flo

w R

ate

m3/h

72

86

11

51

44

17

32

02

23

02

88

36

04

32

50

45

76

72

08

64

10

08

11

52

Steam

Consum

ptio

nkg

/h3

19

38

35

10

63

87

65

89

31

02

01

27

51

59

41

91

32

23

12

55

03

18

83

82

54

46

35

10

0

Ste

am

cond

ensate

Tem

p.

℃≤

85

Ste

am

Cond

ensare

Back

Pre

ssure

GM

Pa

≤0

.05

Electrical Data

Pow

er

Sup

ply

3Φ

- 3

80

VA

C -

50

Hz

6���

*

Valu

es for

ste

am

,chilled w

ate

r and c

oolin

g w

ate

r in

ab

ove

tab

le a

re for nom

inal c

ond

itions a

nd c

an b

e a

dju

ste

d in

pro

per actu

al o

pera

tion.

W

ith the in

let/

outle

t te

mp

era

ture

of coolin

g w

ate

r as 3

0℃

/36℃

, th

e s

team

consum

ptio

n is

only

12.6

kg/

10

4kc

al/h

, and the C

OP

valu

e is

1.3

8.

!

Ste

am

pre

ssure

0.4

Mp

aG

refe

rs to the in

let p

ressure

with

out any

valv

e p

ressure

loss.

The lo

west outle

t te

mp

era

ture

of chilled w

ate

r is

5℃

0

Coolin

g c

ap

acity

can b

e a

dju

ste

d in

range o

f 20

~10

0%

, a

nd c

hilled w

ate

r can b

e a

dju

ste

d in

range o

f 6

0~12

0%

.

.

On the c

hilled w

ate

r/coolin

g w

ate

r sid

e, scale

facto

r is

0.0

86

m2K

/kW

0.0

001m

2·h

· ℃/k

cal.

-

The m

axi

mum

chilled

/coolin

g w

ate

r b

ox

pre

ssure

bearing c

ap

acity

of n

orm

al p

ressure

chiller is

0.8

MP

aG

.

38

39

-�.��!���������

Ste

am

Cond

ensate

Coolin

g w

ate

r

Chilled

wate

r

Strong

solu

tion

Weak s

olu

tion

Refrig

era

nt w

ate

r

Refrig

era

nt vap

or

Vacuum

pum

p

Moto

r re

gula

ting

valv

e

Ste

am

in

Sup

plie

d b

y c

usto

mer

Cond

ensate

out

Cond

ensate

heat exchang

er

Heat exchang

er

Check v

alv

e

Dis

charg

e

Oil trap

Auto purging unit

Auto decrysta-llization pipe

Ab

sorb

er

By-p

ass

valv

e

Ab

sorb

er

Cond

enser

Genera

tor

Sam

plin

gvalv

e

Coolin

g w

ate

rout

Chilled

wate

rout

Chilled

wate

rin

Coolin

g w

ate

rin

Evap

ora

tor

Refrig

era

nt

pum

p

Solu

tion p

um

p

Coole

r

#�� ���#�� �

Lith

ium

bro

mid

e s

olu

tion is a

bsorb

ent

and

wate

r is

refrig

era

nt. A

s

we k

now

Wate

r is

vap

oriz

ed

at

low

boiling p

oin

t in

deep

vacuum

.

It is

the featu

re t

hat

is u

sed

in o

ur

chiller

to a

bsorb

heat

and

to r

e-

aliz

e c

oolin

g e

ffect.

Chiller

is p

um

ped

into

deep

vacuum

by

vacuum

pum

p,

whic

h c

re-

ate

s t

he n

ecessary

cond

ition f

or

boiling o

f w

ate

r at

low

tem

pera

-

ture

. The r

esulti

ng r

efrig

era

nt

vap

or

is a

ttra

cte

d t

o t

he a

bsorb

er

by

the p

ressure

diff

ere

nce b

etw

een a

bsorb

ers

and

eva

pora

tor

and

then a

bsorb

ed

by

str

ong l

ithiu

m b

rom

ide s

olu

tion a

nd

there

fore

perform

s c

ontin

uous b

oiling o

f re

frig

era

nt w

ate

r.

In s

team

op

era

ted

sin

gle

effect chiller, w

eak

solu

tion in

ab

sorb

er

is

pum

ped

into

genera

tor

via h

eat exc

hangers

by

solu

tion p

um

p a

nd

then c

oncentr

ate

d i

nto

str

ong s

olu

tion w

hen h

eate

d b

y ste

am

.

Refrig

era

nt

vap

or

genera

ted

at

the s

am

e t

ime is c

ond

ensed

into

wate

r in

cond

enser. R

esulti

ng la

tent heat is

carr

ied

out of chiller

by

coolin

g w

ate

r.

Refrig

era

nt

wate

r ente

rs e

vap

ora

tor

and

then is p

um

ped

to s

pra

y

thro

ugh s

pra

ying d

evi

ce b

y re

frig

era

nt p

um

p.

The tra

nsfe

r of heat from

the s

yste

m w

ate

r to

the refrig

era

nt causes

the r

efrig

era

nt

wate

r to

vap

orize

again

, p

rod

ucin

g c

hilled

wate

r

coolin

g s

ourc

e p

rovi

ded

by

the c

hiller

. S

trong s

olu

tion d

irectly

ente

rs a

bsorb

er

via h

eat

exc

hangers

and

sp

ray

on h

eat

exc

hang-

ing tubes o

f absorb

er th

rough d

ispers

ion tra

ys. A

s refrig

era

nt va

por

is a

bsorb

ed

by

the s

olu

tion,

strong s

olu

tion is d

ilute

d a

nd

heat

is

genera

ted a

nd reje

cte

d to the c

oolin

g w

ate

r flo

win

g in

the a

bsorb

er

tub

es.

In c

oolin

g c

ycle

, Lith

ium

bro

mid

e s

olu

tion i

s c

ircula

ted

betw

een

str

ong a

nd

weak c

on

centr

atio

n a

nd

refrig

era

nt

is c

hanged

be-

tween li

quid

sta

te a

nd

gaseity

. These tw

o c

ycle

s c

arr

y out sim

ulta

-

neously

and

go r

ound

and

round

.

Heat

exc

hanger

is a

sort o

f heat-

exc

hangin

g e

quip

ment

betw

een

hig

h a

nd

low

tem

pera

ture

solu

tion.

In s

team

sin

gle

effect

chiller,

there

is s

till

a c

ond

ensate

heat

exc

hanger, i

n w

hic

h h

eat

is e

x-

changed

betw

een s

trong a

nd

weak

solu

tion,

there

fore

, in

cre

asin

g

the h

eat effi

cie

ncy

of chiller.

������ 0�������#

�� ���#�� �

①

Chilled w

ate

r in

let te

mpera

ture

(I)

②

Chilled w

ate

r outle

t te

mpera

ture

(I,C

,A)

③

Coolin

g w

ate

r in

let te

mpera

ture

(I,C

,A)

④

Condensate

tem

pera

ture

(I)

⑤

Solu

tion s

pra

y te

mpera

ture

(I,C

)

⑥

Strong s

olu

tion o

utle

t te

mpera

ture

(I,C

,A)

⑦

Condensatio

n tem

pera

ture

(I,C

,A)

⑧

Eva

pora

tion tem

pera

ture

(I,A

)

⑨

De-c

rysta

lliza

tion tem

pera

ture

(I,A

)

(I

)—In

dic

atio

n

(C

)—C

ontrol

(A

)—A

larm

⑩

Chilled w

ate

r flo

w (A

)

⑪

Vacuum

pre

ssure

(I)

⑫

Ste

am

pre

ssure

(I,C

,A)

���������������'�������

Mod

el

SS

-9

9H

21

65

H2

26

5H

23

31

H2

41

3H

24

96

H2

57

9H

26

61

H2

74

4H

28

27

H2

99

2H

21

15

7H

213

23

H2

Coolin

g C

ap

acity

kW3

50

58

09

30

11

60

14

50

17

40

20

40

23

30

26

20

29

10

34

90

40

70

46

50

10

4kc

al/h

30

50

80

10

01

25

15

01

75

20

02

25

25

03

00

35

04

00

US

Rt

99

16

52

65

33

14

13

49

65

79

66

17

44

82

79

92

11

57

13

23

Chilled Water

Inle

t/outle

t Te

mp

.℃

12

→ 7

Flo

w R

ate

m3/h

60

10

01

60

20

02

50

30

03

50

40

04

50

50

06

00

70

08

00

Pre

ssure

Loss

mH

2O

5.5

5.4

5.4

8.2

3.5

3.5

3.5

4.6

5.8

5.8

7.9

8.1

8.1

Connectio

n D

iam

ete

rD

Nm

m1

00

12

51

50

15

02

00

20

02

00

25

02

50

25

03

00

30

03

50

Cooling Water

Inle

t/outle

t Te

mp

.℃

32

→

40

Flo

w R

ate

m3/h

85

14

12

27

28

33

54

42

54

95

56

66

37

70

88

63

99

111

32

Pre

ssure

Loss

mH

2O

8.5

88

10

.78

.98

.48

.41

0.6

6.5

6.5

7.9

88

Connectio

n D

iam

ete

rD

Nm

m1

00

15

02

00

20

02

00

25

02

50

25

03

00

30

03

50

35

04

00

Steam

Pre

ssure

GM

Pa

0.1

Consum

ptio

nkg

/h6

90

11

14

18

40

23

00

28

75

34

50

40

25

46

00

51

75

57

50

69

00

80

50

92

00

Ste

am

Cond

ensate

Tem

p.

℃≤

90

Ste

am

Cond

ensate

Back

Pre

ssure

GM

Pa

≤0

.02

Ste

am

Pip

e D

iam

ete

rD

Nm

m1

00

12

51

50

15

02

00

20

02

00

25

02

50

30

03

00

30

03

00

Ste

am

Cond

ensate

Pip

e

Dia

mete

rD

Nm

m25

25

40

40

40

50

50

50

65

65

65

80

80

Electrical Data

Pow

er

Sup

ply

3Φ

- 3

80

VA

C -

50

Hz

Tota

l Curr

ent

A8

10

20

.32

0.8

21

.82

2.8

22

.82

2.8

28

.62

8.6

33

36

.637

.6

Ele

ctric

Pow

er

kW3

.84

.16

.87

7.2

7.5

7.5

7.5

99

9.5

12

12

.5

Overall Dimensions

Length

mm

3950

3900

4020

4475

5180

5218

5200

5650

5960

6083

6695

6715

6855

Wid

th1

59

21

80

22

04

82

13

52

41

02

41

82

62

62

51

92

52

12

576

2895

3203

3215

Heig

ht

23

46

24

38

27

53

28

04

29

80

32

26

33

64

33

81

34

25

36

83

37

59

41

00

44

95

Op

era

ting W

eig

ht

t7

.38

.81

11

3.1

15

.71

8.1

20

.52

3.4

24

.92

7.4

32

.437

.14

1.3

Ship

pin

g W

eig

ht

66

.88

.39

.91

1.8

13

.41

4.9

17

.21

81

9.9

23

.22

6.5

29

.1

6���

*

Valu

es fo

r ste

am

,chilled

wate

r and c

oolin

g w

ate

r in

ab

ove

tab

le a

re fo

r no

min

al c

ond

itio

ns a

nd c

an b

e p

rop

erly

ad

juste

d in

actu

al o

pera

tion.

!

The lo

west outle

t te

mp

ratu

re o

f chilled w

ate

r is

5℃

.

0

Co

olin

g c

ap

acity

can b

e a

dju

ste

d in

rang

e o

f 2

0~10

0%

, a

nd

chilled

wate

r can b

e a

dju

ste

d in

rang

e o

f 6

0~12

0%

.

.

On the c

hilled

wate

r/co

olin

g w

ate

r sid

e, scale

facto

r is

0.0

86

m2K

/kW

0.0

001m

2·h

· ℃/k

cal.

-

The m

axi

mum

chilled

/co

olin

g w

ate

r b

ox

pre

ssure

bearing c

ap

acity

of n

orm

al p

ressure

chiller

is 0

.8 M

Pa

G.

8

The u

nit

is t

ransp

ort

ed w

ith r

ack

of

18

0m

m in h

eig

ht, a

nd f

or

the u

nits

SS

-661H

2 a

nd

ab

ove

, sub

merg

ed

typ

e r

ack

will b

e a

dop

ted,

extr

a 6

0m

m

shall

be in

clu

ded.

9

The s

hip

pin

g w

eig

ht in

clu

des the r

ack

weig

ht, e

xlud

ing s

olu

tion w

eig

ht.

40

41

Hot w

ate

r op

era

ted

tw

o s

tage li

thiu

m b

rom

ide a

bsorp

tion c

hiller is

a k

ind

of la

rge-s

ize in

dustria

l facility

with

hot w

ate

r as the d

rivin

g e

nerg

y

and

lith

ium

bro

mid

e s

olu

tion a

s the a

bsorb

ent and

wate

r as r

efrig

era

nt.

Hot

wate

r tw

o s

tage u

nits

, usin

g h

ot

wate

r as t

he e

nerg

y sourc

e,

not

only

red

uces g

reatly

the c

ost

for

ele

ctric

ity a

nd

op

era

tion f

ees in

regio

ns w

here

there

are

ric

h h

ot

wate

r re

sourc

es,

but

als

o c

om

pensate

s t

he p

eak-

valle

y lo

ad

diff

ere

nce.

When t

he h

ot

sum

mer

rolls

in,

shortage o

f ele

ctric

pow

er w

ill p

oses a

gre

at w

orr

y fo

r va

rious c

ities. C

oncentrate

d c

onsum

ptio

n o

f p

ow

er b

y air-

cond

itioners

is the s

ticki

ng

poin

t fo

r such a

seasonal p

rob

lem

, fo

r w

hic

h,

hot w

ate

r op

era

ted

tw

o s

tage c

hillers

offer

an a

ttra

ctiv

e s

olu

tion.

Shuanglia

ng h

ot w

ate

r op

era

ted

tw

o s

tage c

hillers

are

wid

ely

ap

plie

d in

ind

ustrie

s, such a

s p

recis

ion m

achin

ery

manufa

ctu

ring, in

strum

ents

& m

ete

rs,

avi

atio

n &

aero

sp

ace,

text

iles,

ele

ctronic

s,

ele

ctric

pow

er, m

eta

llurg

y, p

harm

aceutic

als

, cig

are

ttes,

chem

icals

, hosp

itals

, fo

od

,

etc

. B

y util

izin

g d

oze

ns o

f p

ate

nte

d technolo

gie

s w

ith featu

res o

f ext

rem

ely

hig

h e

nerg

y effi

cie

ncy

and

outs

tand

ing e

nvi

ronm

enta

l effects

, in

ad

diti

on to h

er

custo

mers

erv

ice e

xperie

nce o

f ove

r 2

5 y

ears

, S

huanglia

ng g

uara

nte

es to r

ew

ard

her

users

with

op

timal r

etu

rns.

�Ho

t Wat

er O

pera

ted

Two

Stag

eLi

thiu

m B

rom

ide

Abso

rptio

n Ch

iller

-�.��!���������

The a

bsorp

tion c

hiller

uses a

queous lith

ium

bro

mid

e s

olu

tion a

s

ab

sorb

ent,

and

wate

r as r

efrig

era

nt,

whic

h i

s e

vap

ora

ted

und

er

hig

h v

acuum

to a

bsorb

heat and

pro

duce c

oolin

g e

ffect.

Firs

t, t

he c

hiller

is e

vacuate

d t

o h

igh v

acuum

by

vacuum

pum

p

to c

reate

the n

ecessary

cond

itions f

or

wate

r eva

pora

tion u

nd

er

low

tem

pera

ture

. The r

esulti

ng r

efrig

era

nt

vap

or

was a

ttra

cte

d t

o

the a

bsorb

er

by

the p

ressure

diff

ere

nce b

etw

een a

bsorb

er

and

eva

pora

tor, t

hen a

bsorb

ed

by

concentrate

d lith

ium

bro

mid

e s

olu

-

tion.

Thus p

rovi

des t

he p

ossib

ility

of

contin

uous e

vap

ora

tion o

f

refrig

era

nt w

ate

r.

Hot

wate

r op

era

ted

tw

o s

tage lith

ium

bro

mid

e a

bsorp

tion c

hiller

can p

rod

uce c

hilled

wate

r w

ith o

utle

t te

mp

era

ture

of

7℃

in

let

tem

pera

ture

of

12℃

und

er

cond

itions o

f hot

wate

r in

let

tem

pera

-

ture

of

13

0℃

, m

axi

mum

tem

pera

ture

diff

ere

nce o

f hot

wate

r of

62℃

, hot

wate

r outle

t te

mp

era

ture

of

68℃

, coolin

g w

ate

r in

let

and

outle

t te

mp

era

ture

of 3

2℃

and

38℃

resp

ectiv

ely.

The c

hiller

consis

ts o

f genera

tors

, cond

enser, a

bsorb

er, h

eat

ex-

changer, a

nd

herm

etic

ally

seale

d p

um

ps a

nd

vacuum

pum

p.

One

of

the h

erm

etic

ally

seale

d p

um

ps u

sed

as s

olu

tion p

um

p,

whic

h

transfe

rs the w

eak

solu

tion fro

m the a

bsorb

er to

genera

tor th

rough

heat

exc

hanger, a

nd

concentrate

d t

o s

trong s

olu

tion in g

enera

tor,

and

refrig

era

nt va

por

is p

rod

uced

. R

efrig

era

nt va

por

is c

ond

ensed

to form

cond

ensate

, and

late

nt heat is

reje

cte

d b

y coolin

g w

ate

r.

Refrig

era

nt

wate

r is

sp

raye

d i

n t

he e

vap

ora

tor

thro

ugh d

rip

pin

g

pla

te.

Refrig

era

nt

wate

r is

eva

pora

ted

to f

orm

refrig

era

nt

vap

or

in

the e

vap

ora

tor

und

er

hig

h v

acuum

by

the h

eat

sup

plie

d b

y chilled

wate

r, a

nd

low

tem

pera

ture

chilled

wate

r is

pro

duced

th

e c

old

energ

y sup

plie

d b

y th

e c

hiller

. C

oncentr

ate

d s

trong s

olu

tion i

s

fed

thro

ugh h

eat

exc

hanger

into

the a

bsorb

er, a

nd

sp

raye

d o

ver

the h

eat

exc

hange t

ub

es b

und

les in t

he a

bsorb

er

to a

bsorb

the

refrig

era

nt

vap

or

to f

orm

weak

solu

tion.

Meanw

hile

the a

bsorp

tion

heat is

tra

nsfe

rred

to the c

oolin

g w

ate

r.

Refrig

era

tion c

ycle

is r

ealiz

ed

by

two c

ycle

s s

imulta

neously

and

rep

eate

dly

: th

e s

olu

tion c

ycle

, in

whic

h t

he s

olu

tion c

hanges f

rom

strong t

o w

eak s

tate

and

vic

e v

ers

a;

and

refrig

era

nt

solu

tion,

in

whic

h t

he r

efrig

era

nt

is c

hanged

fro

m l

iquid

to v

ap

or

sta

te a

nd

vice v

ers

a.

Heat

exc

hangers

are

used

to im

pro

ve t

he e

fficie

ncy

of

chiller

by

heat exc

hange b

etw

een the h

igh a

nd

low

heat sourc

es.

For

hot

wate

r op

era

ted

tw

o s

tage a

bsorp

tion c

hiller, t

here

is a

pair

of

genera

tors

, co

nd

ensers

, eva

po

rato

rs a

nd

ab

so

rbers

, w

hic

h

form

tw

o ind

ep

end

ently

coup

led

sub

sys

tem

s w

ith r

efrig

era

nt

and

solu

tion c

ycle

s. In

the s

am

e tim

e h

ot w

ate

r, c

hilled w

ate

r and c

ool-

ing w

ate

r is

connecte

d s

eria

lly b

etw

een t

hese s

yste

ms,

and

hot

wate

r flo

ws a

gain

st

the c

hilled

and

coolin

g w

ate

r to

form

counte

r-

curr

ent heat exc

hange.

In o

rder

to o

ptim

ize t

he g

enera

tion,

co

nd

ensatio

n,

eva

po

ratio

n

and a

bsorp

tion p

rocesses a

nd u

se the h

ot w

ate

r energ

y m

axi

mally

,

the r

atio

nal ra

tio o

f d

istrib

utio

n o

f coolin

g c

ap

acity

and

tem

pera

-

ture

diff

ere

nce b

etw

een tw

o s

ub

sys

tem

s a

nd

data

ol t

em

pera

ture

,

pre

ssure

and

concentratio

n o

f solu

tion s

hould

be s

ele

cte

d,

������ 0�������#

�� ���#�� �

① C

hille

d w

ate

r in

let te

mpera

ture

(I)

② C

hille

d w

ate

r outle

t te

mpera

ture

(C

,I,A

)

③ C

oolin

g w

ate

r in

let te

mp. (C

,I,A

)

④ H

ot w

ate

r in

let te

mp. (C

.I,A

)

⑤ H

ot w

ate

r outle

t te

mp. (I)

⑥ S

trong s

olu

tion s

pra

y te

mp. (C

.I)

⑦ S

trong s

olu

tion o

utle

t te

mp. (C

.I)

⑧ C

ondensa

tion te

mp. (C

.I.A

)

⑨ E

vapora

tion tem

p. (I.

A)

⑩ D

e-c

rysta

llizatio

n p

ipe tem

p. (I.

A)

⑪ C

hille

d w

ate

r flo

w s

witc

h (A

)

⑫ V

acuum

pre

ssure

(I)

(C)-C

ontrol

(A)-A

larm

(I)-Indic

atio

n

#�� ���#�� �

13

Heat Exchanger (2)

12

9

7

8

10

6

112

4

5

M

Co

olin

g W

ate

r in

Chilled

Wate

r in

Condenser (2)

Condenser (1)

Genera

tor

(2)

Genera

tor

(1)

Ho

t W

ate

r o

ut

Reg

ula

ting

Valv

e

Sup

plie

d b

y C

usto

mer

Ho

t W

ate

r in

Heat Exchanger (1)

Co

olin

g W

ate

r o

ut

Chilled

Wate

r o

ut

Reg

ula

ting

Valv

e

Oil Trap

Automatic Decry-stallization Pipe

Automatic Decry-stallization Pipe

Vacuum

Pum

pC

oo

ler

Refr

igera

nt

Pum

p

So

lutio

nP

um

p (2

)S

olu

tio

nP

um

p (1

)

Sam

plin

gValv

e

By-

pass V

alv

e

Absorber (2)

Absorber (1)

Evaporator (2)

Evaporator (1)

Reg

ula

ting

Valv

e

Pip

elin

e

Valv

e

Hot w

ate

r (H

igh tem

pera

ture

)

Hot w

ate

r (L

ow

tem

pera

ture

)

Strong s

olu

tion

Weak

solu

tian

Coolin

g w

ate

f

Chilled w

ate

r

Liq

uid

refrig

era

nt

Refrig

era

nt va

por

42

43

���������������'�������

,�� ���,������� �����

����5�)6

,������� ��3����������� �����

��������� ����

Lith

ium

bro

mid

e s

olu

tion is

sup

plie

d b

y th

e C

om

pany,

and

its q

ualit

y w

ill b

e h

igher

than that of p

rovi

sio

n o

f N

atio

nal s

tand

ard

.

�Ho

t Wat

er O

pera

ted

Sing

le S

tage

Lith

ium

Bro

mid

e Ab

sorp

tion

Chill

er

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Mod

el

HS

C1

30

/68

-H

SB

12

0/6

8-

99H2

165H2

265H2

331H2

413H2

496H2

579H2

661H2

744H2

827H2

992H2

1157H2

1323H2

1488H2

Coolin

g C

ap

acity

kW3

50

58

09

30

11

60

14

50

17

40

20

40

23

30

26

20

29

10

34

90

40

70

46

50

52

30

10

4kc

al/h

30

50

80

10

01

25

15

01

75

20

02

25

25

03

00

35

04

00

45

0

US

Rt

99

16

52

65

33

14

13

49

65

79

66

17

44

82

79

92

11

57

13

23

14

88

Chilled Water

Inle

t/O

utle

t Te

mp

.℃

12

→

7

Flo

w R

ate

m3/h

60

10

01

60

20

02

50

30

03

50

40

04

50

50

06

00

70

08

00

90

0

Pre

ssure

Loss

mH

2O

13

12

.71

0.8

7.1

6.1

8.7

8.9

10

.41

0.5

14

.31

41

6.1

11

.71

3.6

Connectio

n D

iam

ete

rD

Nm

m1

00

12

51

50

15

02

00

20

02

00

25

02

50

25

03

00

30

03

50

35

0

Cooling Water

Inle

t/O

utle

t Te

mp

.℃

32

→

38

Flo

w R

ate

m3/h

11

41

89

30

33

78

47

35

67

66

27

56

85

19

45

11

34

13

23

15

12

17

01

Pre

ssure

Loss

mH

2O

8.5

8.7

79

.68

.81

2.1

10

.61

3.3

12

.81

0.4

10

.31

0.3

13

16

.3

Connectio

n D

iam

ete

rD

Nm

m1

25

15

02

00

25

02

50

30

03

00

30

03

50

35

04

00

45

04

50

45

0

Hot Water

Inle

t/O

utle

t Te

mp

.℃

68

Consum

ptio

n1

30

/68

t/h

6.1

10

.21

6.3

20

.42

5.5

30

.63

5.7

40

.84

5.9

51

61

.27

1.4

81

.69

1.8

Consum

ptio

n1

20

/68

7.3

12

.21

9.4

24

.33

0.4

36

.54

2.5

48

.65

4.7

60

.87

6.9

85

.19

7.2

10

9.4

Pre

ssure

Loss

mH

2O

9.3

9.8

9.3

9.1

91

1.9

11

.99

.61

01

3.3

13

.31

1.4

15

.61

1.1

Pip

ing D

iam

ete

rD

Nm

m4

05

06

58

08

08

08

01

00

10

01

00

12

51

25

15

01

50

Electrical Data

Pow

er

Sup

ply

3Φ

- 3

80

VA

C -

50

Hz

Tota

l Curr

ent

A2

0.4

23

.32

5.5

25

.52

8.1

28

.73

0.9

30

.93

3.4

37

.74

1.6

44

45

45

.9

Ele

ctric

Pow

er

kW6

.55

7.2

57

.65

7.6

58

.65

9.0

59

.45

9.4

51

0.2

51

1.2

51

2.3

51

3.3

51

3.9

51

4.4

5

Overall Di-mensions

Length

mm

41

00

41

44

46

10

50

95

51

90

55

93

57

60

61

47

62

70

71

10

71

60

78

60

87

42

95

42

Wid

th1

80

32

02

32

17

02

27

52

49

22

50

82

63

22

70

02

85

62

91

23

22

63

26

83

14

63

17

6

Heig

ht

24

89

26

98

29

00

28

57

31

51

32

34

34

80

36

54

38

52

38

16

40

90

42

25

43

50

43

50

Op

era

ting W

eig

ht

t8

.21

0.2

13

.41

5.9

17

.82

0.4

23

.42

5.7

27

.52

9.9

34

41

.14

7.4

53

.3

Ship

pin

g W

eig

ht

10

12

.91

7.1

20

.42

3.5

27

.33

1.6

34

.73

8.5

41

.34

7.5

56

.76

4.8

73

.3

6���@

*

The lo

west outle

t te

mp

ratu

re o

f chilled

wate

r is

5℃

.

!

Co

olin

g c

ap

acity

can b

e a

dju

ste

d in

rang

e o

f 2

0~10

0%

, a

nd

chilled

wate

r can b

e a

dju

ste

d in

rang

e o

f 6

0~12

0%

.

0

On the c

hilled

wate

r/co

olin

g w

ate

r/hot w

ate

r sid

e, scale

facto

r is

0.0

86

m2K

/kW

0.0

001m

2·h

· ℃/k

cal.

.

Chilled

/co

olin

g/h

ot

wate

r b

oxe

s h

ave

the m

axi

mum

pre

ssure

bearing c

ap

acity

of

0.8

Mp

aG

fo

r sta

nd

ard

typ

e a

nd 1

.6 M

pa

G fo

r H

igh p

ressure

typ

e.

-

The c

hiller

is t

ransp

ort

ed

with

rack

of 18

0m

m in h

eig

ht fo

r chiller

less t

han u

nit

HS

B-4

13

H2,

and

ad

diti

onal h

eig

ht of ra

ck

of 6

0m

m fo

r th

e u

nit

HS

B-

49

6H

2 a

nd

move

.

8

The s

hip

pin

g w

eig

ht in

clu

des the r

ack

weig

ht, e

xlud

ing s

olu

tion w

eig

ht.b

ala

nced

during h

and

ling.

44

45

-�.��!���������

So

lutio

nP

um

p

Co

ole

r

Refr

igera

nt

Pum

p

Sam

plin

gValv

e

By-

pass

Valv

e

Heat

Exchang

er

Sup

plie

d B

y C

usto

mer

Mo

tor

Reg

ula

ting

Valv

e

Ho

t W

ate

rO

ut

Ho

t W

ate

rIn

Check V

alv

e

Dis

charg

e

Oil Trap Vacuum

Pum

p

Ab

so

rber

Ab

so

rber

Eva

po

rato

r

Genera

tor

Co

nd

enser

Co

olin

g W

ate

rO

ut

Co

olin

g W

ate

rIn

Chilled

Wate

rO

ut

Chilled

Wate

rIn

Auto Purging Unit

Automatic Decrystallization Pipe

Hot w

ate

r (H

igh tem

pera

ture

)

Hot w

ate

r (L

ow

tem

pera

ture

)

Coolin

g w

ate

r

Chilled

wate

r

Strong s

olu

tion

Weak

solu

tion

Refrig

era

nt w

ate

r

Refrig

era

nt va

por

Lith

ium

bro

mid

e s

olu

tion is a

bsorb

ent

and

wate

r is

refrig

era

nt. A

s

we k

now

Wate

r is

vap

oriz

ed

at

low

boiling p

oin

t in

deep

vacuum

.

It is

the featu

re t

hat

is u

sed

in o

ur

chiller

to a

bsorb

heat

and

to r

e-

aliz

e c

oolin

g e

ffect.

Chiller

is p

um

ped

into

deep

vacuum

by

vacuum

pum

p,

whic

h c

re-

ate

s t

he n

ecessary

cond

ition f

or

eva

pora

tion o

f w

ate

r at

low

tem

-

pera

ture

. The resulti

ng refrig

era

nt va

por is

attra

cte

d to the a

bsorb

er

by t

he p

ressure

diff

ere

nce b

etw

een a

bso

rber

and

evap

ora

tor

and

then a

bsorb

ed

by

concentrate

d lith

ium

bro

mid

e s

olu

tion a

nd

there

fore

perform

s c

ontin

uous e

vap

ora

tion o

f re

frig

era

nt w

ate

r.

In h

ot w

ate

r opera

ted s

ingle

effect chiller, w

eak

solu

tion in

absorb

er

is p

um

ped

into

genera

tor

via h

eat

exc

hangers

by

solu

tion p

um

p

and

then c

oncentrate

d into

strong s

olu

tion w

hen h

eatin

g b

y hot

wate

r.

Refrig

era

nt

vap

or

genera

ted

at

the s

am

e t

ime is c

ond

ensed

into

wate

r in

cond

enser. R

esulti

ng la

tent heat is

carr

ied

out of chiller

by

coolin

g w

ate

r.

Refrig

era

nt

wate

r ente

rs e

vap

ora

tor

and

then is p

um

ped

to s

pra

y

thro

ugh s

pra

ying d

evi

ce b

y re

frig

era

nt p

um

p.

The tra

nsfe

r of heat from

the s

yste

m w

ate

r to

the refrig

era

nt causes

the r

efrig

era

nt

wate

r to

vap

orize

again

, p

rod

ucin

g c

hilled

wate

r

co

olin

g s

ourc

e p

rovi

ded

by

the c

hill

er

. co

ncentr

ate

d s

tro

ng

solu

tion d

irectly

ente

rs a

bsorb

er

via h

eat

exc

hangers

and

sp

ray

on h

eat

exc

hangin

g t

ub

es o

f ab

sorb

er

thro

ugh d

isp

ers

ion t

rays

.

As r

efrig

era

nt

vap

or

is a

bsorb

ed

by

the s

olu

tion,

strong s

olu

tion

is d

ilute

d a

nd

heat

is g

enera

ted

and

reje

cte

d t

o t

he c

oolin

g w

ate

r

flow

ing in

the a

bsorb

er

tub

es.

Heat

exc

hanger

is a

sort o

f heat-

exc

hangin

g e

quip

ment

betw

een

hig

h a

nd

low

tem

pera

ture

solu

tion.

In h

ot w

ate

r sin

gle

effect chiller,

there

is s

till

a h

eat

exc

hanger, i

n w

hic

h h

eat

is e

xchanged

be-

tween h

igh tem

pera

ture

strong s

olu

tion a

nd

low

tem

pera

ture

weak

solu

tion,

there

fore

, in

cre

asin

g the h

eat effi

cie

ncy

of chiller.

������ 0�������#

�� ���#�� �

#�� ���#�� �

①

Chilled w

ate

r in

let te

mp. (I)

②

Chilled w

ate

r outle

t te

mp. (I,

C,A

)

③

Coolin

g w

ate

r in

let te

mp. (I,

C,A

)

④

Hot w

ate

r in

let te

mp. (I,

C,A

)

⑤

Hot w

ate

r outle

t te

mp. (I)

⑥

Solu

tion s

pra

y te

mp. (I,

C)

⑦

Strong s

olu

tion o

utle

t te

mp. (I,

C,A

)

⑧

Condensatio

n tem

p. (I,

C,A

)

⑨

Eva

pora

tion tem

p. (I,

A)

(C)—

Control

(A)—

Ala

rm

(I)—

Indic

atio

n

⑩

De-c

rysta

lliza

tion tem

p. (I,

A)

⑪

Chilled w

ate

r flo

w (A

)

⑫

Vacuum

pre

ssure

(I)

���������������'�������

Mod

el

HS

A9

5/8

5-

99H

2165H

2265H

2331H

2413H

2496H

2579H

2661H

2744H

2827H

2992H

21157H

21

323H

2

Coolin

g C

ap

acity

kW3

50

58

09

30

11

60

14

50

17

40

20

40

23

30

26

20

29

10

34

90

40

70

46

50

10

4kc

al/h

30

50

80

100

125

150

175

200

225

250

300

350

400

US

Rt

99

165

265

331

413

496

579

661

744

827

992

1157

1323

Chilled Water

Inle

t/O

utle

t Te

mp

.℃

15

→

1

0

Flo

w R

ate

m3/h

60

10

01

60

20

02

50

30

03

50

40

04

50

50

06

00

70

08

00

Pre

ssure

Loss

mH

2O

5.4

5.4

8.2

8.2

11

.81

1.8

4.6

5.8

5.8

8.1

8.1

8.1

11

.4

Connectio

n D

iam

ete

rD

Nm

m1

00

12

51

50

15

02

00

20

02

00

25

02

50

25

03

00

30

03

50

Cooling Water

Inle

t/O

utle

t Te

mp

.℃

32

→

38

Flo

w R

ate

m3/h

11

21

86

29

83

72

46

55

58

65

17

44

83

793

01

11

61

30

21

48

8

Pre

ssure

Loss

mH

2O

6.7

6.7

5.1

5.1

6.2

6.7

7.3

8.5

910

.710

.71

0.7

14

.4

Connectio

n D

iam

ete

rD

Nm

m1

25

15

02

00

25

02

50

25

03

00

30

03

00

35

04

00

40

04

00

Hot Water

Inle

t/O

utle

t Te

mp

.℃

95

→

85

Consum

ptio

nt/

h3

6.9

61

.59

8.4

12

31

53

.81

84

.52

15

.32

46

27

6.8

30

7.5

36

94

30

.54

92

Pre

ssure

Loss

mH

2O

4.3

4.3

3.2

3.2

4.6

4.6

2.5

3.1

3.1

4.2

4.2

4.2

5.9

Pip

ing D

iam

ete

rD

Nm

m8

01

00

12

51

50

15

02

00

20

02

00

20

02

00

25

02

50

25

0

Ele

ctric

Mod

ula

ting V

alv

e

Dia

.D

Nm

m6

58

01

25

12

51

50

15

01

50

20

02

00

20

02

50

25

025

0

Electrical Data

Pow

er

Sup

ply

3Φ

- 3

80

VA

C -

50

Hz

Tota

l Curr

ent

A9.5

10

.71

3.1

14

.61

5.8

15

.81

5.8

18

.82

1.8

21

.82

6.9

28

.43

1.4

Ele

ctric

Pow

er

kW3

.15

3.5

54

.35

4.8

55

.25

5.2

55

.25

6.2

57

.25

7.2

58

.95

9.4

51

0.4

5

Overall Dimensions

Length

mm

38

70

38

60

44

20

45

35

50

38

50

80

55

35

59

35

59

35

66

35

67

35

67

45

74

45

Wid

th1

50

61

66

81

78

41

98

32

12

62

20

62

30

02

56

72

53

82

52

52

78

03

06

03

09

7

Heig

ht

2239

2541

2711

2860

2860

3080

3195

3315

3460

3460

3770

4170

4170

Op

era

ting W

eig

ht

t7

.39

.31

31

5.2

17

.92

1.3

24

.82

7.8

30

33

.33

9.6

45

.550

.9

Ship

pin

g W

eig

ht

5.8

7.1

9.5

10

.81

2.7

15

17

.71

9.9

21

.32

32

7.4

31

.33

4.7

6���

*

The lo

west outle

t te

mp

ratu

re o

f chilled w

ate

r is

5℃

.

!

Coolin

g c

ap

acity

can b

e a

dju

ste

d in

range o

f 20~1

00

% , a

nd c

hilled w

ate

r can b

e a

dju

ste

d in

range o

f 6

0~1

20%

.

0

On the c

hilled w

ate

r/coolin

g w

ate

r/hot w

ate

r sid

e, scale

facto

r is

0.0

86

m2K

/kW

0.0

001m

2·h

· ℃/k

cal.

.

Chille

d/c

oolin

g/h

ot w

ate

r boxe

s h

ave

the m

axi

mum

pre

ssure

bearin

g c

apacity

of 0.8

MP

aG

for sta

ndard

typ

e a

nd 1

.6 M

Pa

G for H

igh p

ressure

typ

e.

-

The c

hiller

is t

ransp

ort

ed w

ith r

ack

of

180

mm

in h

eig

ht

for

chiller

less t

han u

nit

HS

A-4

96

H2,

and a

dditi

onal heig

ht

of

rack

of

60

mm

for

the u

nit

HS

A-

579

H2 a

nd m

ove

.

8

The s

hip

pin

g w

eig

ht in

clu

des the rack

weig

ht, e

xludin

g s

olu

tion w

eig

ht.

SHUANGLIANG ECO-ENERGY SYSTEMS CO., LTD

Cat. No.: SL-IT-C1101(E) New Release

2011 Copyright Reserved. Information subject to change without prior notice.

Printed in China Printed on recyclable paper.

Add: Shuangliang Industry Park in Ligang, Jiangyin City, Jiangsu Provine, China

Tel: +86-510-86638824 86632095

Fax: +86-510-86634678

Post Code: 214444

Email: ktsales@shuangliang.com

www.shuangliang.com