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2
Chairp
1 DAP Mr.
2 PhosMr. R
3 NoveProdMr. R
4 GuaSysteMr. A
5 UtilMr.:
24th AFA I
person:
Sami
P & PhosphJohn Wing
sphate PlanRichard D.
el Large Scduction Rinat Ander
ranteed (Riems throughArmaghan Y
lization of SZaid Halas
Int’l. Te
i AMARN
horic Acid Pg - Phosphat
nt Yield ComHarrison –
cale Energy
rzhanov, De
isk Free) Engh AvanceonYusuf – Bus
Satellite Imasah - Senior
echnical F
EH
QES Man
Plant Improe Consultan
mparisons Process Sup
Efficient T
eputy Techn
nergy Savinn's Proprietsiness Mana
age To Imprr Chemist
Fertilizers
S
nager – T
vement nt
pervisor / Fe
Technology f
nical Directo
ngs in Watetary "iwaterager
rove Solar P
s Confere
Sessio
The Arab
ertilizer Con
for Urea
or of Innovi
er and Steamr" & “iboile
Ponds Prod
ence
on I
Potash C
J
nsultant P
iations
RU
m er”
A
duction
Company
John Wing
PegasusTSI
R&D InstitUrea
Avanceon
APC
y
, P.E. U
I Inc. U
tute of R
P
C J
USA
USA
Russia
Pakistan
Jordan
Session II
24
Abstrac A selectDAP inn
D B th s P A a D P C T
Phosph
C N C U R R A A P
Project
4th AFA In
D
ct:
tion of attranovations iDual Mole RBFL Vaporihe reactor-scrubbing –Product ScAutomated adjusts proDual diamePipe ReactCooler Air CTran-Tech
oric Acid pConversionNo need foConversionUtilize gypsRecover urRecover fluA variety ofAdvances iPurify phosmanageme
nt’l. Tec
DAP & PHMr
active modnclude: Reactor-Grizer/Scrubb-granulator– potentiallreen DiverRecycle Ccess to kee
eter reactoror Chiller Product Co
plant projecn from Dihyr most eva
n to Hemi-Dsum – mananium – m
uosilicic acif profitable n dry gyps
sphoric acident and sta
chnical Fe
HOSPHORIr. John Win
John
difications a
ranulator Aber - Vapor acid scruby eliminatinrter SystemControl - coep size in mr (pre-neut
ooler
cts to consydrate to Haporation. UDi – similarny ways to
major investid – high-puses for p
sum stackind to technicart-up issue
ertilizers
IC ACID PLng - Phosp Wing, P.E
are describ
Acid Scrubbrizes all ambber. This ng need fo
ms – easy continuouslymid-range.ralizer)
ider includeemi: Make
Usually no r benefits pmake gypstment with urity grade
phosphogypng cal or foodes are disc
Confere
LANT IMPphate ConsE. - USA
bed, based
bing mmonia witunit provid
or any tail-gcapacity incy monitors r.
e: es acid at 4
rock grindplus 98.5% sum an asshigh profit
e for AlF3 fepsum
grade cussed
nce
PROVEMENsultant
on succes
th free heades a 3rd stgas scrubbecrease recycle par
42% concening is needrecovery &
set rather tpotential eed
NTS
ssful projec
at from air letage of er.
rticle size a
ntration vsded. & clean gypthan liability
cts.
eaving
and
. ~27%
psum y
Session II
2
Abstrac IntroducEstimatProcess◦ Elimin◦ Reduc◦ Identif◦ RedireProcess1. Site s2. Open3. Close4. Proce5. High 6. Impro7. Non-C8. Calci
24th AFA I
Rich
ct:
ction - Peged Range s Changes ate off-site
ce phosphafy opportunect fresh was Alternativselection an Circuit Pred Circuit Pess Water Strength F
oved WashContact Evnation
nt’l. Te
Phard D. Ha
asusTSI Cof P2O5 Lto Reduce
e dischargeate flow to nities to recater make-
ves nd climate rocesses – Processes Recycling
Fluoride Rehing and/orvaporator C
chnical F
Phosphatearrison – Pr
Peg
Core Busineosses to Ge Phosphates gypsum st
cycle proce-up to gyps
conditionsno recove– some re
ecycle r Double FiCondenser
Fertilizers
e Plant Yielrocess SupasusTSI In
ess ActivitieGypsum State Losses:
tack ess water sum stack
s - typical pery of pore covery of p
iltration r Cooling
s Confere
ld Comparpervisor / Fnc. - USA
es acks
plants, Flormoisture P
pore moistu
ence
risons Fertilizer Co
rida and N.P2O5 ure P2O5
onsultant
Africa
Session II
Abstrac R&D Inadvancestock coproprietoffer staBy the (URECOTo be aindustryplants (ceffectiveThe key- Synthincludin - Urea mlosses a- Strippand pro� Submthe proc- Doubtechnolo - Simplifdifferentinvestm Innovatiunit as wfor it to increaseR&D Insfor urea
2
Novel LMr. R
ct:
stitute of Ued productosts, improtary licenseate of the a
present mON 2006®able to proy we’ve devcapacity oveness requy features oesis reactog Vortex M
melt separand increasing distillatlonging the
merged carcess internble-stage ogies.
fied equipmt pressure.
ment and co
ive R&D Inwell as forbe the moes up to 60stitute of U
a production
24th AFA
Large ScalRinat Ande
Urea is a tion technoove safetyes and “knart solutionsmoment w) and avera
ovide compveloped anver 2000 tpuirements. of our advaor operate
Mixer, Long
ation at sese the effiction in CO2e operatingrbamate coal heat to gmelt distil
ment lay-ou. Thus, theonstruction
nstitute of Ur the rehabost rational 0% and eneUrea univern providing
Int’l. Te
le Energy Eerzhanov, D
R&D Ins
leading enologies tha
y and ecolonow-hows” s to increae have deage-scale plete servin energy-efpd) that co
anced teches at 200 bgitudinal Se
everal stagciency of di2 flow at 9g period of ondenser ogenerate 3lation red
ut as a rese HP equip
and assem
Urea technbilitation of
investmenergy costs rsal technog perfect op
echnical F
Efficient TDeputy Tecstitute of U
ngineering at help ouogy efficie for the mse plant preveloped t(URECONce and to fficient tecrresponds
nology arebars and iectioning E
es during tistillation p90 bars allothe strippe
operating a3 Bar steamduces the
ult of the sment can bmbly costs
nology can an existing
nt there shdeplete su
ology for laperational
Fertilizer
Technologchnical DireUrea – Rus
company r customency. R&D
majority of uroductivity.technologie
N 2007®) ube on the
hnology foto the pres
e: s equippe
Element and
the syntherocess. ows achiever due to leat 90 bars m.
equipmen
synthesis abe positionfor the ere
be used fog plant witould be at
ufficiently (arge capacand econo
rs Confere
gy for Ureaector of Innssia
focused oers to cut t
Institute ourea techn es for conrea plants.
e edge of or constructsent enviro
d with a sd Trays.
esis reactio
ving higheess wearingprovides e
nt costs
and HP distned at a lowection of a
or the consh total liquleast 2 un
reaching 5city units isomical perfo
ence
a Productinoviations
on the devtheir energof Urea is nologies al
nstruction . modern tretion of largonment and
set of inter
on helps to
r process g service cefficient rec
compared
tillation uniwer height urea unit.
struction ouid recycle nits at a pla50% for stes a competormance
ion
velopment gy and feean owner lowing us
of low-sca
ends in urge-scale urd operation
rnal device
reduce he
performanconditions. cuperation
with oth
ts working that reduc
f a new urprocess, b
ant. Capacam). titive soluti
of ed-
of to
ale
rea rea nal
es,
eat
ce of
her
at ces
ea but city
on
Session II
Gu
Abstrac Water anecessacorpora HoweveWho guWill my Project I need asure if I
Avanceunique absolute
The paguarantPakistan
Abstrac The use the usagesolar ponpotash). Satellite and depththe final Infrared the areasThe main1. Improv
2. Plan thlocatin
3. Locatidikes.
4. Locatipheno
2
uaranteed
ct:
and steam ary measute objectiv
er certain quarantees t
manufactuInvolves ha specific can mana
on, a US partnersh
ely no finan
per brieflyteed (no risn respectiv
Utiliza
ct:
of satellite ie of satellitends system
images wereh profiles wimages werelayer of the of any suspn benefits ofve the proce
he salt dredgng any close
ing any susp
ing the reveromenon.
24th AFA
(Risk FreeAvan
Mr
systems aures to mies of impro
questions dhe savingsuring proceigh capital ROI or IRRge it to ach
based syip to reduncial risk to
y describessk) savingsvely.
ation of Sa
images is wie imagery to at the Arab
e processed which used to
e saved in spimage was
pect sink holef processing ess control of
ging works ined area aroun
ected sinkho
rse flow of th
Int’l. Te
e) Energy nceon's Pr. Armagha
Ava
re big enernimize theoved qualit
do arise whs and what ess be distu
investmenR to investhieve my fi
ystem inteuce energo customer
s Avanceos, and det
atellite ImaMr. Zaid
idely used inimprove the
b Potash Co
using specio improve thpecial softwaused to checes. the satellite f the solar po
n the solar pnd high dens
ole (coordina
he brine in th
echnical F
Savings inroprietary n Yusuf – anceon – P
rgy cost cee energy ty, profitab
hile initiatin if savings urbed? nt!!! t; Energy onancial go
grator andgy consumrs.
on’s “iwatetails of proj
age to ImpHalaseh/ SAPC – Jo
n many appe efficiency
ompany that
al software he process coare as an arcck for seepa
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pond system sity brine an
ates) and the
he solar pon
Fertilizer
n Water an"iwater" &Business MPakistan
enters in a consumptiility and en
g energy sare not ac
optimizatiooals.
d energy mmption in w
er” and “ibjects at En
prove SolaSenior Cheordan
lications all of the contrused to pro
like Infograontrol and p
chiving and cage of the br
the Arab Potm.
by calculatinnd evaluate th
e risk of thes
nds system an
rs Confer
nd Steam & “iboiler”Manager
fertilizer plon in orde
nvironment
savings prochieved?
n is not my
managemewater and
boiler” pacngro Fertili
ar Ponds Pemist
around the rol and increoduce Carna
agh and Irdaspredict for fucomparison rine from the
tash compan
ng the salt ghe dredged a
se sinkholes
nd set the rig
ence
Systems t”
ant. Everyer to bettet sustainab
ojects, som
y business
ent compad steam s
ckages, thezer Limited
Production
world. Thisease the prodallite ( the
ss to have duture actionssystem (Arce solar pond
ny are:
growth in eacareas.
on the syste
ght solution
through
y facility taker align wility.
me are;
s and am n
any, offerssystems w
e concept d and Nes
n
s paper revieductivity of raw martial
density, therms. The data acMap GIS) ds and to loc
ch subarea,
em and the
for this
kes with
not
s a with
of stle
ews the of
mal and
cate
Session II
Chairp
1 ThFeMr
2 FSMr
3 CaMrDeMrSyn
4 IJCPhMr
5 RepUrMrSup
person:
Mr. J
e major resrtilizers (JS
r. Yuri Cher
SA Neutralizr. Salah Albu
atalysts for Srs. Ayten Yevision r. Henrik Lanthesis
C Experiencosphoric Ac
r. AWINASH
placement orea Plant r. Bellary Mperintenden
ohn Win
search activSC “NIUIFrnenko – Ge
zation with ustami - Pr
Sulphuric AY. Wagner –
arsen - Gene
ce on Revamcid Plants
H PESHWE,
of High Pr
Muhammad Unt
g
Phospha
vities of the ”)
eneral Direc
Calcium Crocess Engin
Acid and Am– Arae Man
eral Manage
mping of Su
, PLANT HE
ressure Scru
Usman – Ma
S
ate Consu
Research In
ctor
Compoundsneer
mmonia Planager – Caty
er, Marketin
ulfuric Acid
EAD
ubber in SA
aintenance
Sessio
ultant– J
Institutes for
ants ylest
ng & Sales
d and
AFCO-II
on II
John Win
r JSC “N
JACOB
HaldorTopsoe
IJC
SAFCO
g P.E. - U
NIUIF” R
BS U
r e
D
Jo
O S.
USA
Russia
USA
Denmark
Jordan
S. Arabia
2
The m
Abstrac
The pap“NIUIF”Russian m
Abstrac As enviplant opphosphacooling precipitatreat fluneutralizscrubbecondenswith phused beseveral
24th AFA I
major resea
ct:
er describes”) and showsmineral ferti
ct
ronmental perators wate plantspond wate
ate as the uoride conzation prioers to remosers. If a mosphate roecause it icalcium co
nt’l. Te
arch activiM
s the main s technologiilizers plants
FSA NMr
regulationwill eventu currently er that is srecirculati
ntaminated or to dischove fluoridemarket canock to pros not profiompounds
chnical F
ities of theMr. Yuri Che
JSC
research acical processes and plants
Neutralizatr. Salah Alb
J
s continueally be reuse direc
saturated wng water cwater, ph
harging effes as fluosnnot be fouduce a weitable. Thissuch as ph
Fertilizers
e Researcernenko –C “NIUIF”
ctivities of es developedlocated in th
tion with Cbustami - JACOBS –
to restrict equired to ct contact with fluoridcools in lahosphate pfluent. A bilicic acid pund for theeak phosps paper dihosphate r
s Confere
h InstituteGeneral D- Russia
Russian Rd by this Inhe former So
Calcium CoProcess E
– USA
chemical pneutralizebarometri
de salts. Mrge coolingproducers better envprior to cone fluosilicic
phoric acidscusses Frock, lime a
ence
es for FertDirector
Research Inststitute that h
oviet Union s
ompoundsngineer
processinge fluoride wic condens
Most of thisg pond systypically u
vironmentandensing thc acid, it ca. This tech
Fluosilicic Aand limesto
tilizers (JS
titute for Fehave been imstates
s
g emissionswaste matsers with s fluoride istems. Whuse lime ol alternativhe vapors ian then behnique is Acid neutraone.
SC “NIUIF”
ertilizers (JSmplemented
s, phosphaterials. Morecirculati
is allowed hen forced or limestove is to uin baromete neutraliznot currenalization w
S
”)
SC d at
ate ost ng to to ne se tric ed
ntly with
Session III
24th AF
M
Abstrac The firsexperienFor maplant shbuild-upAn imprdust proprotectiothis uniqbetweenconsumsame ti1oday, 4are in oThe secof our 2AdvancHaldor change many teThis paoffered primary for amm
Variouconve
reformeachieve The HTunit hasresulted
FA Int’l.
CMr. Henrik
Mrs.
ct:
st Part of tnce we havny sulphur
hutdowns isp caused byroved proteotection caon catalystque VK38 n screening
ming and exme signific4 years latperating arcond part o5-mm dais
ced ReformTopsoe Afreforming
echnologiesper descrito the ammreformer a
monia produus options ective gas
er (HTER) ted, while th
ER teleolos been revad in a 33%
. Technic
Catalysts fk Larsen –
Ayten Y.
this paper ve gained ric acid plas the screey plugging ection agaiatalyst in tt in the shadust prote
gs comparxpensive shcant savingter, close toround the wof this papesy dust proming TechfS (Topsoe technologs such as sbes how thmonia induand due touction. are availabheated refo
technologye methane
gy has nowamped withincrease in
al Fertiliz
for Sulphu– General MWagner –
Haldor T
describeson VK69 aants the boening requi
by dust prnst pressuhe top of ape of a 2ection catared to the 1hutdowns fgs in blowo 80 installworld. er disclosetection inst
hnology foe) suppliesgy. The Hasyngas, hyhe HTER tustry. For ao high refor
ble for a caorming sta
effective y is a provee leakage is
w been in sh an HTERn reforming
zers Conf
uric Acid aManager , Area Man
Topsoe – D
s case storand VK-701ottleneck firement of resent in thure drop buBed 1. In 5-mm Dais
alyst result12 mm Daifor catalyst
wer energy lations with
s actual optallations.
or Ammons a full ranaldor Topsydrogen. mtechnologya new ammrming temp
apacity incrands out asperspectiven revamp s retained
successful R installed dg capacity.
ference
and AmmoMarketing
nager – CaDenmark
ries disclos1 LEAP5TMfor prolongBed 1 due
he feed gasuild-up can
2007 Topsy. Installats in a dousy. Conseqt screeningresult from
h 25 mm D
perating ex ia Plantsnge of refosoe Exchan
methanol, any .is adoptemonia planperature st
rease in thes an attractve. The Hal
option what a low le
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onia Plantsg & Sales Satylest Dev
sing someM. ged operate to increass. be obtaine
psee introdation of a 1ubling of thquently, thg is reducem the lowe
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xperience o
orming tecnge Reformnd ammoned in an at, implemetill retains a
e front-endive option ldor Topsiehere a capvel.
al operatiom of an Au
s Synthesisvision
e of the op
ting time bsed pressu
ed by the uduced a ne15 cm top he operatine number d and at ther pressurprotection c
obtained fro
chnologies mer (HTERnia. mmonia pl
enting the Ha low meth
d of an ammfrom both a
e exchangeacity incre
on since: eauto thermal
Session
s
perating
between ure drop
use of a ew dust layer of ng time of time-
he re drop. catalyst
om one
which alsoR) technolo
lant and wHTER reduhane slippa
monia coma technicae ase of 20 -
arly 2003. Al Reformer
n II
Mr. Henr
Mrs.Ayten
o includesogy is app
what benefiuces the siage, which
mplex. Out ol as well as
-25 % can
A full size (ATR), thi
rik Larsen
n Y. Wagner
s heat ex-plicable to
ts can be ize Of the is crucial
of these s a cost
easily be
industrial s has
2
IJC E
AbstracFrequecontinuAfter sto operIn orderthe equiManufactime to 1. OBJEC2. PROJE3. CHAL
of any pro Our IJC’sproposal
Abstrac The Indoperatiophospho IJC is hDouble Agri’s scapacity NormallWe seeoptimizaonly it re Debottleof any p Our IJCrestrictioimprove
24th AFA I
EXPERIEN
ct: ent failureuous prodeveral shrate the pr to overcompment with
cturing of nput the plaCTIVE ECT SCOPE
LLENGE IN H
ocess is limit
s experiencesof capacity e
ReplaMr.
ct
do Jordan onal and oric acid pl
having 200Absorption
single stagy since its c
ly the proce lots of ation. Debequires cor
enecking isprocess is l
C’s experieons, inadeed efficienc
Int’l. Te
CES ON R
Mr
e of High Pduction losut downs
plant at deme the chalh upgraded ew Scrubbent back in o
E HAND
ted by the low
s on debottleenhancemen
cement of. Bellary M
Chemicalssafety fiellants.
00 MTPD n process ge hemihydcommissio
cess plantsplants areottleneckinrrect evalu
s like remolimited by t
ences on equacy in cy are discu
echnical F
REVAMPIN
r. AWINAS
Pressure ss. and repaesigned pllenge on pmaterial in
er, Air liftinoperation.P
west capacity
enecking like t with improv
f High Preuhammad
SA
s Companyld at its
sulfuric aand 700 Mdrate proc
oning.
s will have e expandeng for increation studi
oving the wthe lowest
debottlenecooling s
ussed.
Fertilizers
NG OF SULPLANT
SH PESHWIJC – Jor
Scrubber
airs equipparameterlant reliabiln May 2011g of 65 T n
Paper Conte
y steps in the
waste heat bved efficiency
essure ScrUsman – M
AFCO - S.
y is commiEshidiya c
acid plant MTPD of P2cess. Both
10-15% eed to highemental caes.
weakest lincapacity st
ecking likesystems &
s Confere
LFURIC ACTS WE, PLANTrdan
in SAFCO
pment relirs.ity, SAFCO. ew Scrubbe
ent ( not lim4. 5. 6. 7.
e process.
boiler limitatioy are discuss
rubber in MaintenanArabia
itted for itscomplex c
based on 2O5 phosp
h the proce
xtra margiher capacitapacity co
k in a chateps in the
e waste h& proposal
ence
CID AND P
T HEAD
O-II Urea
ability co
Manageme
er and replamited to thePRE-SD PREXECUTIONSUCCESS VSUCCESS S
on, sulfur flowsed.
SAFCO-II ce Superin
s continualcomprising
Monsantophoric acidesses are
n than theties througsts less th
in, maximu process.
heat boiler of capac
PHOSPHO
Plant cau
uld not be
ent decided
acement wae below, fewEPARTIONSN (SD PHASVALUE STORY
w restrictions
Urea Planntendent
improvem of sulfur
o’s Doubled plant bas in operat
e nameplatgh modernhan the ne
um produc
limitationcity enhan
ORIC ACID
used
e achieve
d to take the
as done sucw more poinS SE)
s, inadequacy
nt
ments in boric acid a
e Conversised on Hydtion with f
e capacitienization aew plant a
ction capac
, sulfur flocement w
Se
D
ed
e challenge
ccessfully innts may be
y in cooling s
oth nd
on dro full
es. nd nd
city
ow with
ession II
e to replace
n short added)
systems &
e
Chairp
1 MeeFluMr.
2 RevMr.
3 BesConMr.(De
4 HeaStorof LMr.
2
person:
Mr. S
eting envirouid –bed Gra. Harald Fra
vamping of . Narayansa
st-practice oncept to Imp. salah Abduesignated).
alth, Safety ry behind A
LTI-s . Sami Amar
24th AFA I
Saed BOK
P
U
onmental isanulation wanzrahe – P
f a Conventiamy Selvaraj
on RBI drivplementatioulaziz Zaina
and EnviroAPC Succes
rneh/ QES M
nt’l. Te
KISHA
Plant Ma
UAE
ssues facingwith Plants Process Man
ional Total Raj – Head of
ven Integrityon aldin - Senio
onment in Fss in achievi
Manager
chnical F
Se
anager -
g new and e
nager
Recycle Uref Urea -1 Pl
y Assurance
or Inspectio
Fertilizer Ining 4000000
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essio
Ruwais F
existing urea
ea Plant lant
e from
n Engineer
ndustry 0 MHW Fr
s Confere
n III
Fertilizer
a Uhde FTechno
QAFC
GPIC
ree
ence
Industrie
Fertilizer ology B. V.
CO
APC
es (Fertil)
Netherlan
Qatar
Bahrain
Jordan
)
nds
S
ession IIII
Meetin
Abstrac In recebodies. ammonwith theWhile thefficiencammonindustryIn NPK without and the from theevaporaThe blevarious In accorfor achieWith UFintegratIn this pespeciaTechno
ng environ
ct:
nt years mThis has leia and ure
e demands he reductiocy, reducinia reductio
y. or AN planany difficuproduct. F
e acidic scation plant eed from thways. rdance witeving ammFT's Ammoed into the
paper varioally UFT´s plogy, which
nmental is
MrUhde F
many envied to a signa dust for from their
on of dust ng ammoniaons can b
nts the resulty, as in thFor a urea crubber conand which he ammon
h our commonia emisonia Convee granulatioous availabproprietaryh combines
ssues faci
. Harald FrFertilizer T
ronmental nificant rednew urea environmeemissions
a emissionbe achieve
sulting bleehese plantfluid-bed gntains comuntil now a
nia scrubbe
mitment tosion reducert Technoon processble and indy Ammonia s minimize
ing new anwith Pla
ranzrahe –Technolog
regulationduction in tfluid-bed g
ental authos can be ans in a ureaed by insta
ed stream fts the bleedgranulation mponents ware usuallyer must be
o improve octions from ology the a. ustrially prConvert
ed ammonia
nd existingnts Process My B. V. – N
ns have behe permissgranulationorities to redachieved ba granulatioalling acid
from the acd contains plant the s
which canny not part oe processe
our fluid-beurea fluidb
acidic bleed
roven optio
a emission
g urea Flu
Manager Netherland
een amensible emissn plants. Buduce their
by using scon plant is ic scrubbi
cidic scrubcomponen
situation isnot be procof the produed in som
ed granulabed granulad from the
ons for gran
ns with redu
uid –bed G
ds
nded by thsion levels ut existing emissions crubbing smore com
ng system
bber can bents which as more comcessed in uct specifice way. Th
ation proceation plantsammonia
nulation pla
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he regulatofor plant operto the env
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24th AFA
Health, Saehind APC
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ve safety ums out of mployees d they are . The rum.
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1 10 Mr
2 CapMr
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person:
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Years of Sar. Joost Roe
apacity Increr. Thomas K
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arbon Dioxidr. Jamal Ali
test improvrtilizer s. Marietta M
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afurex Expees – Acqisiti
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24
10 Ye
ct : bat the seveStamicarbonade named St properties,tended for
rbon urea pstalled in exiction materiaonstruction h vol % (whic
he past 10 yfrom high pr
er, including
inspectionsand comparL UG and Xoverview wiyears in non® vessels wi concentrat
ct :
pical naturalverted to ureoduction caso modificatfor urea pla
s examplesentation.
4th AFA In
ears of SafMr. Jo
ere carbaman started to dSafurex®. S, even at ve
plants. The misting urea pal and sincehaving a coch is advise
years over 1ressure vesHP piping a
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ammonia / limited avaes togetherammonia p
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chnical Fe
eriences in– Acqisitiontamicarbo
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rea Reactorories such a
by Stamicabehavior of t
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ncrease of KrawczykUhde Gm
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ertilizers
n Stamican Manageron – Nethe
s prevailing her with Sanlex materialvation air. T
d in the marciated equiprbon grass ron in Safurents) to as lo
® equipment , Pool Condas (control)
arbon on Sathe tradition
on forms whhe corrosionrosion resists section.
f Urea Plak – Senior
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making refe
Confere
arbon Urear Mechanicerlands
in the synthndvik Swedel having supThe materia
rket in 1996ment. In 20root urea plex® materialow as 0.1 %
have been denser, Poovalves, HP
afurex® equinal stainless
hich occur inn behavior otance of Sa
nts Process Emany
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s of ammonfor an increall ammon
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98 the first S® became thbeen commiws to reduce
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nia which is ease of the nia to urea. ses several O2 side. It ects under
Se
Safurex® equhe standardissioned or
e the passiv
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experienceynthesis sec
observed o40 inspecte
nstrated, ev
ession IV
uipment d are ation air
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es will be ctions
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AbstracFERTILwith relPressurThe boi Boiler d
T T E D O S F F N C
In the pduring Manufa
During ABoiler (Bhydro-tethe totathe coils
Due to removekept at 5 Based oboth boMitsubis This papheater cotechniqu
24
M.P. BO
ct: L operates ated utilitie
re steam bler was in s
etails: Type of BoileTag numberEvaporation Design PresOperating prSteam TempFeed water TFuel Fired: NNumber of BCommissionpast 28 yeathe year cturer, and
April 2008,B-5501A) west of the bl 28 coils. Ts at this lea
non-availad and plug50% load.
on the failuoilers and ashi, Japan
per describeoil replacem
ues to inspe
4th AFA In
OILER SUPMr. A
a 1300 MTes in Ruw
boilers (B-5service for
er : Mitsubhr: B-5501 A
(MCR) Capssure : 48 Kgressure: 40 perature: 42TemperaturNatural GasBurners- 2 ( ning Year : 1ars during a2005 boile
d concluded
, while utilizwas carrieboiler reveThe leak wak location
ability of spgged at theAdditional
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hishi 36VP-1& B
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front side) 1983 all turnarouer integrityd that boile
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FAILURE AWahedi - MTIL – UAE
t and 2300AE. The Ud and suppy problem.
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plied by M/
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ondition.
rtunity, routn from its eater coils in the coill NDT meth
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ALCMENTl Engineer
ranulated Unt has two/s Mitsubis
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tine inspecsuper hea. The leak assemblyhods due t
he down timd the boilere the safe o
ded to replaOriginal E
n plan for prd out, usage
T
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shi, Japan.
party insppan the O
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ection ageOriginal Eq
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m three coiy, the inspessibility.
aky coils wn in to servof the boile
uper heaterManufactu
of the coils,ed inspectio
ession IV
ency and quipment
Pressure bsequent ls out of ection of
were cut, vice and
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r coils in urer, M/s
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AmmoncommisAmmonCO2, 10Howeveplant waas no fuPurely flevel anadditionenvironmDi-oxideoption to
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AbstraSince moindustry During timprove Middle E operatin
Solex wafriendly
24
ations. My and ana
Carbon
ct: ulf Petrocemical pro
nia and Messioned in 1nia plant w015 MTPDer, after theas utilized urther CO2for environnd also to tnal CO2 frment; GPICe Recoveryo enhance
test impro
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East, India ang condition
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4th AFA In
Material oalysis ind
n Dioxide Mr. jam
chemical Inocessing co
ethanol pl1998.In theas utilized from Amme commissfor urea p was availamental contest maximrom CDR C installed y (CDR) pla methanol
ovements Ms. Mari
years, Solexn it’s reliabil
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e this experias well as p
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mal Ali Al S
ndustries omplex com
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in Indirectietta Mansv
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ience and prproviding the
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missioneddesign philce 120 MTt was ventehe Urea plThis led to
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resent their e most cost
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in 1985 osophy of PD of meted to the aant in Januo the reducgn capacityorder to bria plant thatame time
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n made base“ no caking
proof of Sole
latest techneffective so
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r 1 Mo stdue to ink
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and 17001985, 275
thanol (totaatmosphereuary 1998,ction in mey of 1200 Ming the met can be accut down
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found it’s plfor all types
ed on intens– no cleani
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s seen as al natural ga
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ed in the Ay about 120
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ble and sus
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ea plant, O2) from balance
Ammonia 0 MTPD
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stainable
Chairp
1 PoIss
2 AnMr
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person:
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ort worker dsa Awad HA
nalysis of Sar. Manish G
ommissioninbjective Orier. Gian Pietevelopment
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24
Ana
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s been conthe status
r plants impwas carriedyears 2005parametersents and fto minimize
OMMISSIO
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ND REVAMBJECTIVE
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24
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Example: N000 t of oreRecycling St takes lessRecycling HUsing recycproduction essened. Recycling RBy recyclinghe most ouawareness Recycling HRecycling psystem.
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