Klaren International

7/24/2019 Klaren International

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KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology 1

2013 KLAREN INTERNATINAL !" "inc# van $oghsingel %0& NL-21'2 L( )illego*& The Netherlan+s& T,31 10% 2 ... /#larenv#co* Einfolarenv#co*

MultiStageFlash/FluidisedBedEvaporatorRevisited:

A Ver !ro"isi#g Ther"al $esali#atio# !ro%ess

&ith !o&er'ul Spi#(O''s

$i%) *+ KLAREN a#dEri% F+ de BoerKLAREN INTERNATINAL !"& )illego*& the Netherlan+s

Presented by:

$r+Ir+I#g+ $i%) *+ Klare# M+S%+

at

2n+ Ann4al (oer an+ 5esalination 64**it - 2013&

7ENA $ran+ Khal+ia )otel& Riya+h& King+o* of 6a4+i Araia

7arch 18-1'& 2013


2/46


,o#te#ts

Intro+4ction# The +evelo9*ent of the 76:;:!E +4ring the 9erio+ 180 - 1'0#

(oerf4l s9in-offs of the self-cleaning fl4i+ise+ e+ heat exchange

technology as a99lie+ in the 76:;:!E& for a99lications other than

+esalination +4ring the 9erio+ 1'0 - 2010#

Res4rrection of the 76:;:!E in 2010 an+ its conse


3/46


I#trodu%tio#

>76:;:!E Revisite+?*eans@Re-exa*ination of the 76:;:!E after a ti*e interval&

ith a vie to *aing a fresh a99raisal#

As a consethe technology?& forin+4strial a99lications other than seaater

+esalination#

2010 BBBB @ The res4rrection of the 76:;:!E an+ its

conse


4/46

KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology %

The develop"e#t o' the MSF/FBE -.01 2 .314

Principle:76:;:!E characterise+ as follos@

"erticalconfig4ration ith a short stage-height an+ stace+ co*9act

flash cha*ers#

Large n4*er of 9arallel vertical con+enser t4es#

)eat transfer in t4es enhance+ y a fl4i+ise+ e+ in each t4e at

very lo lince-thro4gh? +esign#


5/46

KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology C


Rectangular cross section.

S t e a "

, o # d e # s a t e

$ i s % h a r g e

- B r i # e 4

F e e d

- N a t u r a l s e a & a t e r 4

$ i s t i l la t e

: l a s hc h a * e r s

i n s e r i e s

I n l e t c h a n n e l

R e c o v e r y s e c t io nD f l4 i + i e + e +D : ! F c o n + e n s e r si n s e r i e s F

5 i s t i l la t eD i n t e r s t a g e F

: i n a l f l4 i + i e + e + D : ! F h e a t e r

4 t l e t c h a n n e l

6 h a l lo l a y e r o ff l4 i + i s e + 9 a r t i c le s

5 i s t ri 4 t i o n s y s t e *

T o 9 v i e

Cylindrical cross section.

S t e a "

, o # d e # s a t e

$ i s % h a r g e - B r i # e 4

F e e d - s e a & a t e r 4

$ i s t i l l a t e

I n le t c h a n n e l

4 t l e tc h a n n e l

T 4 e 9 l a t e

= o n + e n s e r & i th 9 a r a l le lf l4 i + i s e + e + s

T 4 e 9 l a t e

! r i n e h e a t e r

: l a s h c h a * e r

: l a s hc h a * e r s

i n s e r i e s

R e c o v e r y s e c t io nD f l4 i + i e + e +D : ! F c o n + e n s e r si n s e r i e s F

6 h a l lo l a y e r o ff l4 i + i s e + 9 a r t i c le s

5 i s t r i 4 t io n s y s t e *

T o 9 v i e

Two differentsimplified designs:


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KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology .


Some theory, process design features and design consequences:

/here@

Lt G=on+enser t4e length 9er stage H*5o G4ter +ia*eter of the con+enser t4e H*5i G Inner +ia*eter of the con+enser t4e H*Jl G 7ean +ensity of the li


7/46KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology 8


Typical design features and consequences for the MSF/FB: =on+enser t4e +ia*eter G 1 **

5ia*eter glass ea+s G 2 **

:l4i+ise+ e+ 9orosity in t4es G 8C

Li


8/46KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology '


More consequences:5Lo#g(tu6e7 MSF/FBE ith 30 stages incl4+ing final heater an+ a gain-

ratio of 10 o4l+ fit in one D1F vessel ith total length or height of 12 to

1% * an+ re


9/46KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology


"nd e!en more consequences::or the 76:;:!E ith a gain-ratio of 10& *echanical energy D94*9ing

9oerF re




Summary of the advantages andoperating characteristics of the

MSF/FBE:

nce-thro4gh single-vessel +esign#

Non-fo4ling fl4i+ise+ e+

con+ensers an+ final heater#

nly to ater oxes#

5e-aeration in first stage#

Lo corrosion in flash cha*ers&

9) U '#%

Thin-alle+ titani4* t4es#

=onstant seaater fee+ flo#

.

. A8 e a t r e % o v e r s e % t i o #

. BF i # a lh e a t e r

S t e a "

, o # d e # s a t e

8 o t s e a & a t e r

O u t le t & a t e r 6 o 9

F l u i d i s e d g l a s s 6 e a d s

$ i s t i l la t e

S e a & a t e r

B l o & d o & #

I # l e t & a t e r 6 o 9

F l o & d i s t r i 6 u t io # s s t e "

F l u i d i s e d g l a s s 6 e a d s

$ i s t i ll a t e' la s h % o l u " #

, o # d e # s e r s

7

$ r o p l e t s e p a r a t o r

F i 9 e d o r i 'i % e ' o r6 r i # e t r a # s p o r t

E v a p o r a t o r% h a " 6 e r s

I # t e r s t a g ev a l v e s




Interstage valves# "ariation +istillate 9ro+4ction&

0 V 100 V 0#

No ire *esh +e*isters#

=o*9lete flash-off#

No anti scaling che*icals re




Example of evenly distributed fluidised beds in outlet water box.




500 m/d Demonstration of te !"#/#$E tecnology% &sle of 'exel% 'e (eterlands.

>once thro4gh? +esign&

2. stages& average stage height 0#% *&

*axi*4* o9erating te*9erat4re11CQ= at gain-ratio W10&

no +osing of anti-scale che*icals&

no ire *esh +e*isters&

co*9lete flash-off of the rine&

+istillate 9ro+4ction co4l+e varie+ eteen0 an+ 100 in a

X ho4r *aintainingexcellent +istillate


14/46


15/46KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology 1C


Failure of the market introduction of the MSF/FBE: E67IL International hich one+ the technology ran into financial

9role*s an+ lace+ f4n+s to contin4e the +evelo9*ent of the

76:;:!E for 9ro+4ctions of 20000 to 30000 *;+# re


16/46KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology 1.

!o&er'ul spi#(o''s o' 5the te%h#olog7 -.3121.14

Poerful spin!offs of the self!cleaning fluidised "ed heate#change technology as applied for the MSF/FBE, for applications

other than desalination:

After o4r fareell fro* seaater +esalination ith the 76:;:!E& e

realise+ the 9otential for the self-cleaning 9erfor*ance of o4r heat

exchange technology 4se+ in the 76:;:!E in other in+4stries& here*any 9rocesses s4ffer fro* very severe fo4ling heat exchangers#

A99lications other than seaater +esalination often re




=o**ercial o9erating ex9eriences@ The self-cleaning fl4i+ise+ e+heat exchanger& hich can re*ain clean in+efinitely& is a cost-effective

alternative to the conventional heat exchanger hich s4ffers fro*

severe fo4ling in a co49le of ho4rs& +ays or ees an+ even *onths#

Any ty9e of fo4ling +e9osit@

hether har+ or softY iological or che*icalY

firo4s& 9rotein& or other organic ty9esY

or a co*ination of the aove

can e han+le+ y the self-cleaning fl4i+ise+ e+ heat exchanger#


18/46KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology 1'


#oechst$%elanese& #ouston& T'& (S")A force+ circ4lation reoiler for the 9ro+4ction of a

9ro9rietary che*ical re9lace+ a conventional heat

exchangerthat re




Borden %hemicals * Plastics +B%P,& -eismar& ."& (S")A large che*ical 9lant in the 6 ase+ 4s to solve their very severe

fo4ling 9role*s in one of their 9lants#

Comparison conventional vs. self-cleaning fluidised bed eat excangers in +

and 005.

Unit

Conventional

heatexchanger

Self-cleaning

heat

exchanger

(1998)

Self-cleaning

heat

exchanger

(2005)

Heat transfer surface m 24000 4600 3300

Pumping power kW 2100 840 450um!er of cleaningsper "ear

# 12 0 0




Borden %hemicals * Plastics +B%P,& -eismar& ."& (S")

1 200 m3 self-cleaning fluidised bed eat excangers replacing 1 000 m3 conven-

tional eat excangers.




"ll maor oil companies and amongst them %onoco Phillips)

A99reciation for o4r innovative a99roach to 9ro+4ce high 9ress4re

stea* fro* che*ically 4ntreate+ 9ro+4ce+ ater for 6tea* Assiste+

$ravity 5ischarge D6A$5F an+ Enhance+ il Recovery DERF?#

Comparison conventional tecnology *!4C/##E, vs. new innovative tecnology

*R#",.

Conventional technology New technology

RS!"#tion 1 "#tion 2

$team pro%uction &100 !ar' kg() *0000

Pro%uce% water fee% kg() *2164

+low %own kg() 2164

+low %own to atmosp)ere kg()2 1$%

(& 'of fee)

21

(*1 'of fee)

Heat transfer surface

&reco,er" an% pre)eater not inclu%e%'m 95 1 950 2&%

-ec)anical energ" for separation kW 2333.10 116*.10 25

-ec)anical energ" for pressurisation

an% circulation t)roug) / an% /$

kW 350

/otal mec)anical energ" reuirements kW 2 $9& 1 52 &5

C)emical treatment pro%uce% water

fee%# es il




%aspi Meruerty Operating %ompany +%MO%& 0a1a2hstan,& Shell& BP&

etc)

All *aZor oil co*9anies an+ ; or *aZor 9layers in this 4siness have

ex9resse+ their interest in o4r +irect seaater cooling technology

4sing self-cleaning fl4i+ise+ e+ exchangers for offshore 9latfor*s#

Comparison gas cooling systems on offsore platforms

+ir cooler,nirect ,eawater

cooler,

.irect,eawater cooler,

(,elf-cleaning/e)

Heat %ut" -W 46

as temperature &n# utlet' 7C 120 43

as pressure !ar 150

$eawater temperature 7C 26 50

Plot area m 5&0 90 %0

Weig)t tonne &50 &00 1901)

Power kW 850 2 000 80

1 W)en cooler is su!merge% !ut supporte% !" t)e structure of t)e platform t)e weig)t re%uces to appro89

*5 tonne




%aspi Meruerty Operating %ompany +%MO%& 0a1a2hstan,& Shell& BP&

etc)

O''shore plat'or" &ith heav; volu"i#ous a#d e#erg %o#su"i#g air(%oolers o#

top de%) i#di%ated 6 arro&+


24/46KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology 2%

Specifications:

1.1 Resurre%tio# o' the MSF/FBE < ,o#se=ue#%es

"pecification of te 10

000 m/d !"#/#$E considered.

Pro%uction : 40000 m;(%

ain#ratio : 10 #

$eawater temperature : 35 7C

-a8imum seawater temperature in final )eater : 115 7C

um!er of e,aporator stages : 30 #

iameter glass !ea%s : 290 mm

/otal weig)t glass !ea%s : ?350 t

-aterial in contact wit) seawater : >uple8 #

-aterial in contact wit) %istillate : $tainless steel #

-aterial outsi%e reinforcements : Car!on steel #


25/46KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology 2C


6rinciple !"#/#$E.

.

. A8 e a t r e % o v e r s e % t i o #

. BF i # a lh e a t e r

S t e a "

, o # d e # s a t e

8 o t s e a & a t e r

O u t le t & a t e r 6 o 9

F l u i d is e d g l a s s 6 e a d s

$ i s t i l la t e

S e a & a t e r

B l o & d o & #

I # le t & a t e r 6 o 9

F l o & d i s t r i 6 u t io # s s t e "

F l u i d is e d g l a s s 6 e a d s

$ i s t i l la t e' la s h % o l u " #

, o # d e # s e r s

7

$ r o p l e t s e p a r a t o r

F i 9 e d o r i 'i % e ' o r6 r i # e t r a # s p o r t

E v a p o r a t o r% h a " 6 e r s

I # t e r s t a g ev a l v e s

3esign:


26/46

KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology 2.


Cross section of our preferred rectangular vessel-type of 10

000 m/d evaporator.

E v a p o r a t o r% h a " 6 e r

1 # 2 C * 1 # 2 C *

%

0

*

C *

, o # d e # s e r

B u # d l e

, o l d s e % t io #

$ i s t i l la t e ' l a s h% o l u " # s

N o # (% o # d e # s a 6 l e s

V a p o u r

V a p o u r

V a p o u r

V a p o u r

V a p o u r

V a p o u r

V a p o u r

2 # C *

E v a p o r a t o r% h a " 6 e r

, o # d e # s e r

B u # d l e

, o l d s e % t i o #

$ i s t il la t e ' l a s h% o l u " # s

F l a s h % h a " 6 e r' l o o r

$ r i l l e d % o # d e # s e rp a r t i t io # & a l l s

L o # g 6 e a " s

, r o s s 6 e a " s

3esign:


27/46



#las cambers% condensers 7 pat of te vapour flow units way to te condensers.

2

#0

*

2

#0

*

1 # 2 C * 2 # C * 1 # 2 C *

= o n + e n s e r

E v a 9 o r r a t o r

c h a * e r

" e r t ic a l + e f le c t o r

T h r o t t l i n g g a 9 : l a s h i n g c h 4 t e s

/ i r e * e s h+ e * i s t e r

5 e f l e c t o r ! a f f l e 9 l a t e

AA

, r o s s s e % t io # A ( A

= o n + e n s e r

" e r t ic a l + r a i n

" a 9 o 4 r l a n e s

E v a 9 o r a t o r

c h a * e r

3esign:


28/46

KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology 2'


Explanation construction and erection of te evaporator at plant site.

2 # 0 * 2 # 0 *2 # 0 * 2 # 0 *

S

ta

g

e

1

2

9

S

ta

g

e

3

0

,

in

cl.

su

m

p

1

*

1

2

*

2

*

2

#C

*

2 # 0 * 2 # 0 *

% 0 *

0

#.

*

0

#%

*

A % % e s sd o o r s - : > 4

B l o & d o & #? F e e d - : > 4

$ i s t il la t e ' la s h% o l u " # s -: > @ 4

V i e & A ( A

,

,

S t a g e .

S t a g e : /

S t a g e @ 1

S u " p

1 # 2 C * 2 # C * 1 # 2 C *

$ i s t i l la t e ' l a s h% o l u " # s -: > @ 4

, r o s s s e % t i o # , ( ,A

A

F o u # d a t i o #

S u p p o r t

O u t l e t & a t e r (6 o 9 - : > 4

F i # a lh e a t e r - : > 4

, r o s s6 e a " s

, o # d e # s e r s

I # l e t & a t e r (6 o 9 - : > 4

F e e d - : > 4

B l o & d o & #

A % % e s sd o o r s - : > 4

$ i s t r i 6 u t i o #s s t e "

T u 6 e p l a te

T u 6 e p l a te

V e r t i % a ls u p p o r t ss t a g e .

V e r t i % a ls u p p o r t ss t a g e : /

M u l t ip l e p a r r a l e l# o l e s

8 e a v % r o s s 6 e a " s 8 a t % h ' o r

d i s t r i 6 u t io # s s t e "

V e r t i % a ls u p p o r t s

s t a g e @ 1

%onstruction * erection:


29/46



Explanation of te arguments8 standardisation 7 mass production of components.

1

%

*

6 t a g e 3 0

6 t a g e 1

6 t a g e 2 C %0

*

2

#0

*

= r o s s - s e c t i o n A - AD 6 t a g e 2 C i n r e + F

"

a

ria

tio

n

o

fc

a

9

a

c

ity

"

a

ria

tio

n

o

f

g

a

in

-ra

tio

A A

C # 0 *

B l o & d o & #

S e a & a t e r ' e e d $ i s t i l l a t e

S t e a "

, o # d e # s a t e

Standardisation

* mass fabrication

of components:


30/46



Data for !"#% !ED and "9R: obtained from article by lobal 9ater &ntelligence

*9&,% :ctober 0+% titled8 ;'ecnology coice still open at .

Co,t in$(2) 3S 34. SR" 3S641)3S641(wa,te heat

riven)


31/46



%omparison operating cost MSF& M3& S45O and MSF/FB :

7aZor reasons for *4ch loer a*ortise+ ca9ital cost of the 76:;:!E

D[ 0#21 * +istillateF vs# 76: D[ 0#%2* +istillateF vs# 7E5 D[ 0#2*

+istillateF@

5esign ase+ on stan+ar+ *o+4les hich re+4ces engineering costs#

>nce-thro4gh? 9rocess ith +eaeration an+ re*oval non-con+ensales in the first stage#

=o*9act single vessel +esign& only to ater oxes& no connecting

9i9ing eteen stages an+ final heater#

6o9histicate+ +esign internals res4lts in +ra*atic re+4ction in eight#=o*9are n4*ers for 76:& 7E5 an+ 76:;:!E@ 38vs# 28vs# 1'g

steel ;D*3 +istillate;+F#

##


32/46



7ass 9ro+4ction of internals loers farication cost 9er g *aterial#

Elegant con+enser +esign& 4sing thin-alle+ titani4* t4es& incl4+es

ne 9roce+4res for t4ing an+ sealing con+enser t4es in t4e 9lates

an+ 9reventing interstage leaage thro4gh con+enser 9artitions alls#

Erection at 9lant site an+ installation of all internal co*9onents s4ch

as s499orts& flash cha*er floors& con+enser 9artition alls in acli*ate controlle+ shell of the eva9orator vessel#


33/46


Other appli%atio#s 'or the MSF/FBE

Expansion of existing !"# wit ig-temperature front-end !"#/#$E.

S e a & a t e r

' e e d

B l o & d o & #

$ i s t i l l a t e

L I =

( - 0 1

= o n v e n t i o n a l 7 6 :

) i g h - t e * 9 # f r o n t - e n +7 6 : ; : ! E

S t e a "

, o # d e # s a t e

: ) E \ - 0 2

: ) E \ - 0 1

5 i s t i l l a t e

( - 0 2

: I =

7

#igh$temperature

front$end

MSF/FB:


34/46

KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology 3%


9ind and/or solar powered !"#/#$E.

6 t e e l s 4 9 9 o r tc o n s t r 4 c t i o n

S t e a ", o # d e # s a t e

= o n + e n s e r s

: i n a l h e a t e r

4 t le t a t e r o x

: l a s hs t a g e s

5 i s t i ll a t e s 4 * 9

! r i n e s 4 * 9

B r i # e d i s % h a r g e

! r a n c h e + o f f c o l +s e a a t e r fe e +

e t 9 4 * 9

S e a & a t e r 'e e d

7

: I

$ i s % h a r g e d i s t i l l a t e

I n l e t a t e r o x

E l e c t r ic o i l e r ]/ a t e r ; s t e a *s e 9 a r a t o r ,h o l + - 4 9 v e s s e l

/ i n +t 4 r i n e

7

I n t e r s t a g ev a l v e s

W

W

( a r a o l i c* i r r o r

, o l d- & a t e r 4

8 o t- & a t e r ?

s t e a " 4

= i rc #9 4 * 9

MSF/FB in combination

with renewable energy:


35/46

KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology 3C

Package

Variatio# heat i#put / &i#d velo%it i# %o"6i#atio# &ith i#tera%tio# o' i#terstage

valves 'or 6ri#e level %o#trol6o9+



36/46

KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology 3.


MSF/FB in combination with renewable energy:

64**ary of the a+vantages of the in+ an+;or solar 9oere+

76:;:!E@

=o*9act single vessel +esign#

)igh gain-ratio#

9eration on varying external heat in94t con+itions res4lting in

varying +istillate 9ro+4ction D0 to 100F of excellent


37/46


!o&er'ul spi#(o''s o' 5the te%h#olog7 i# desali#atio#

Comparison operation ori?ontal -pass conventional brine eater wit vertical

single-pass self-cleaning fluidised bed brine eater.

S t e a "

, o # d e # s a t e

1 2 8 Q = 1 1 8 Q =

1 2 C Q =

6 t a g e 1

R e * o v a ls 9 o n g e

a l l s

6 9 o n g e a l l re c y c l e

5 e * i s t e r

4 t le t c h a n n e l 6 e 9 a r a t o r

" e r t i c a l! r i n e ) e a t e r D 1 - 9 a s s F

5 o n -c o * * e r

( a r t i c l e s

= o n t r o lc h a n n e l

I n l e t c h a n n e l i t h+ i s t r i 4 t i o n s y s t e *

S t e a "

, o # d e # s a t e

) o r i o n t a l ! r i n e ) e a t e r D 2 - 9 a s s F

1 2 8 Q =

1 0 8 Q =

1 1 C Q =

6 t a g e 1

R e * o v a ls 9 o n g e a l l s

6 9 o n g e a l l r e c y c l e

5 e * i s t e r

1 1 Q =

1 1 Q =

Self$cleaning fluidised bed brine heaters in e6isting MSF plants:

6tea*-heate+ rine heaters#


38/46

KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology 3'


Self$cleaning fluidised bed brine heaters in e6isting MSF plants:

6elf-cleaning fl4i+ise+ e+ rine heater o9erating on the exha4st

gases of o9en-cycle gas t4rines@

In the 9erio+ 1.0 to 1'0 *4ch attention has een 9ai+ to o9erate

76: 9lants on the exha4st gases of o9en-cycle gas t4rines#

All atte*9ts faile+ +4e to heavy scaling of the t4es in s4ch rineheaters ca4se+ y 4n9re+ictale >hot s9ots? ca4se+ y 4neven flo

+istri4tion of flos an+ local fil* coefficients#

)oever& in 18 it has alrea+y een +e*onstrate+ that a self-

cleaning fl4i+ise+ e+ rine heater co4l+ in+ee+ o9erate on the hot

gases of a 4rner ith a te*9erat4re of .00Q=# The sco4ring action

of the fl4i+ise+ glass ea+s +i+ in+ee+ re*ove the scale for*e+ on

s4ch >hot s9ots?#


39/46



Self$cleaning fluidised bed brine heater operating on the e6haust

gases of open$cycle gas turbines and installed in e6isting MSF plant:

Intereste+ =lient in the $4lf Region ants to increase its generate+

9oer an+ has availale@

%^.C 7/ an+ .^%C 7/ o9en-cycle gas t4rines#

% 76: 9lants each having a 9ro+4ction of 1% 7I$5 an+ 4sing2C0 t;h extraction stea* of a99rox# 2 ar an+ 23CQ= in their rine

heaters#

Atte*9ts to increase the 9oer o4t94t y reva*9ing a n4*er of the

existing o9en-cycle gas t4rines in +4al-cycle co-generation 4nits is

i*9ossile#


40/46

KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology %0


Re*ains the very interesting o9tion@

se the exha4st gases of the o9en-cycle gas t4rines for the heating

of the self-cleaning fl4i+ise+ e+ rine heaters& an+ 4se the extraction

stea* s499lie+ to the rine heaters for the generation of %^30 G

120 7/ extra 9oer in the stea* t4rines#


41/46



"implified flow diagram for many potential applications in te ulf Region.

1 % 7 $ 5 7 6 :

1 1 0 Q =

1 ' 0 Q =

6 9 o n g e a l l r e c y c l e

2 2 0 0 * K ; h Y1 0 3 # C Q =

, o # d e # s a t e

S t e a "

6 t e a * h e a t e +

r i n e h e a t e r

R e * o v a ls 9 o n g e a l ls

= h i * n e y

F u e l

A i r

= o * 9 r e s s o r T 4 r i n e

A i r

. C 7 /

E x h a 4 s t g a s h e a t e +s e l f - c l e a n i n g f l 4 i + i s e + e + r i n e h e a t e r

= o * i n e + e x h a 4 s to f g a s t 4 r i n e

F u e l = o * 4 s t i o nc h a * e r

$ e n e r a t o r . C 7 /

$

$

E x h a 4 s t g a s s e s W C . 0 Q =

Self$cleaning fluidised bed brine heater operating on the e6haust gases

of open$cycle gas turbines and installed in e6isting MSF plant:


42/46



Data for !"#% !ED and "9R: obtained from article by lobal 9ater &ntelligence

*9&,% :ctober 0+% titled8 ;'ecnology coice still open at .

Co,t in$(2) 3S 34. SR" 3S641)

3S641

(wa,te heat

riven)


43/46


,o#%lusio#s

6o*eti*es a ne roa+ rings yo4 to exiting 9laces ith great vies&

here existing roa+s cannot ring yo4& an+ very often& it is a *atter of

l4c to +iscover s4ch a ne roa+#

r in or+s of the sa*e tenor ith res9ect to the contents of this

9resentation@

76: an+ 7E5 Dthe >existing roa+s?F +o not ring the ther*al+esalination co**4nity the i*9rove*ents in technology an+

o9erating cost they nee+#

7ore attention sho4l+ e 9ai+ to the self-cleaning fl4i+ise+ e+ heat

exchange technology D>the technology?F in co*ination ith the *any

i+eas intro+4ce+ in this 9resentation Dthe >ne roa+s?F&

an+& ho9ef4lly& in the near f4t4re& the ther*al +esalination co**4nity

ill enZoy the enefits of the 76:;:!E an+ the great variety of

fascinating s9in-offs Dthe >exiting 9laces ith great vies?F#


44/46


45/46

KLAREN INTERNATIONAL BV Inventors self-cleaning heat exchange technology %C

A%)#o&ledge"e#ts

5r# Alesan+ar "lasi DArca+isF& ho *a+e *e +eci+e to ret4rn to *y

roots an+ 9ay attention again to the 76:;:!E for reason that this >ol+

forgotten? ther*al +esalination technology still shoe+ the 9otential of

>eing the very est?#

5r# Roerto !orsani D:isia Itali*9iantiF& 5r# A+il !4shna D7oya

!4shnaF& oost "er*ey DTeo+inF& =le*ens /olters an+ 7ohsen

7o4ssao4i D5e4tsche !acoc 7i++le EastF for their enco4rage*ent

an+ ee9ing 4s *otivate+#


46/46

Thank You For Your Attention

KLAREN INTERNATIONAL BV

A++ress @ "incent van $oghsingel %0NL-21'2 L( )illego*

the Netherlan+s

Tel# @ ,31 2C2C 30.0.

:ax @ ,31 2C2C 30.0CE-*ail @ infolarenv#co*

/// @ #larenv#co*

Thank You For Your AttentionFor more information you can always contact us)
mailto:[email protected]?subject=Request%20info,%2011%202006%20PPThttp://www.klarenbv.com/http://www.klarenbv.com/mailto:[email protected]?subject=Request%20info,%2011%202006%20PPT

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