Document O3NJRnyKavn5zZd89o2mQ1DdQ
| >OLYVINYL chloride--PVC 'hardware' involved'
--is
now
a
household
What .lie the features and piob iuini that arc likely to be associ
sivo material to liquefy and store since it lequiros special and ex
trcmcly costly c o n s l r u e (i o n
(he licensor nnd others dining tt. design stages.
Hie i-i'nrt-iiur opmulUpTM fulH_h
word. A considerable amount ated with this'
materials Vttutevo thorofoi'e-utat c/nriod-ovfl-n"S baiiit o*elgUfrai
of information on its manu IIow will they arise in the pro'- built Jflt'ftnvs.-rald'iitii-ojiai stormzoS
.frumoees rv rjv.qt S frnm-s'rrt
facture, variant forms and applications has already ap
commissioning and commissioning operations?
IIow aie they likely to dtITer m
peared in Double Bond and aspect, in rotation to the three
This Keans.HhaUUu&^tiqijsLtt. ancr the clacking section must be com missioned and run in balance `moving up or down' m through
' in nnolhei .sal t lofnrc moving foi
Ziliimiis which wi separate out the purified VCM pn
elsewhere
mam control sections concerned put together, as conditions dictate. duct and the HCt.
Vinyl chloride monomer--
with the production--the opera tional, technical control and mam
VCM--is the material feed tonance sections'
stock foi the PVC process, In Here arc seme answers , . .
PARALLEL TRAINS
COKING
Ilo\vovci,Jiis-all-*Ui#-otitasoc-
The main problem facing us n
IjjWir-crTvCM complex lholltrK ` tins scrlion will bo in mnintinnini
which by moans of an 'initi hn^^i,?!rt0S,fil!07nall0,Vrnu?,CCfi''''-P-kCt3fi-bi.lio,TMin#,. are-a---g-a-Ii-n' associated with') good fnmarr on strimm limes it
ated' polymerisation reac tion, undei carefully con trolled temperature condi
has ahoady been in- operationiJM^ .corrosion, particularly in the r*/
J!1*1"" ,^ny
- action none In order to ensure
squui'18 ,'lcons,ct* rro.m t"5^Jnawai*hrCtrallnuily -of--BSIincoi
w^vii<iSPh3*fheniiqipAi5,0 l'l.inm opoiation and luss on and ol
JjwerUi1 enking up ol Che^qpilfioh.^uwioeae eisewli ei-c can m*
(rq;o ,3Q to 40 days depending oi tjtg, , inollted oTopprallon, th<
9;
tions, VCM is converted to
PVC. The VCM supplied-as a clear, colourless liquid-- must be nf extremely high chemical purity,
Demand for PVC, and con sequently VCM, is Increasing
and production complexes for these materials arc a notable'part of the Baglan Bay expansion project. So far as
BP Chemicals International
is concerned, all VCM and
Tiie existing plant will become <T poit of the overall VCM complex, especially the crude section. Fur ther EDC will be produced by a
new direct cliloi matron section which will produce, about twenty five per cent mom crude EDC than Hie unit curiently m operation.
Over the last few yc.ns the mam problems associated with the direct
chlorination plant have baer concei nod with corrosion
mem -- in pariiculae, and around the reus
action cooling section.
operation, we have broken the jjrohtp-nf Hie ifj-fiintjg,.hr..tHvd-*un
roaclJon cone up into two equal
each cleaning ou
halves oi 'parallel trains'j_'(liU'IT operation.
Viau will bo capable of producing
Wo leol we have the ability <-
about I he same amount of crude ovi'i cnnie the fli-si aspect b>
EDC as cither of tlui direct chlori establishing good procedures am
nation units
training based on available know
Each half will have its own steam how. We have already started
generation system, the steam be with the close assistance of on,
ing gejuaratotr by (be heat given colleagues in icisemch ami dc
nipt'-by the reaction, T-he., iscpiip-'^ vclopmcut department, Epsom,
hint Will bo of complex design ) closer study of feodstock const >
both nxr-rabTirtrddh' JtflfftlOd mid In/ tuents, By discoveung those which
.materials of constmtettott.
arc more prone to produce coke
ESCTOR FEATURES
deposits we shall improve on the coking-up times in tho longer
PVC production has previ ously been carried out at Barry.
TWO ROUTES
By thermally cracking ethylene (hchlontlc -- EDC -- VCM. is ob- tinned along with hydrogen chloride. Tins ciaelang, or `brent ing up', Is achieved by passing the , EDC through tho coils of furnaces which are held at high tomporature The cracking "stage is fol lowed by a separation 01 purifi cation stage which allows the VCM and HC1 to be dissociated from small quantities of unwanted re sidua! compounds and fiom each otliei--and at the required level of purity.
VCM Is the 'bunding hncli' for PVC, and EDC is used ns the 'building Illicit' for VCM. Thus, heroic we can start any part of the crocking stage we must first produce E11C--and we need twice tbc amount or FIDO la make the required amount of VCM.
Par economic reasons--you'll see why soon--wc mate EDC by two routes . , .
LOCAL EXPERIENCE
, , The reaclois arc about teuelye.
-ieaW in diameter and hove about
ISagbui Bay personnel have .130 long coth in each through
csscufially laid down (be design whioh wafer flows to -keep tho re-
conditions for the new direct aetor temperature under control.
chlorination section based on local
Because the catnlytic ageat
experience. Certain mechanical which assists the reaction Is of a
changes have been designed in, al `fluidised1 character, In so far as
though (lie basic process principles It Is always in motion as compared
and control techniques have been retained.
with other 'firitli*Jj*d-4ypc enta' lysis, spaetateffust cyeloneslare also
It is hoped that tho modifica built Into tfVlWlHWbrreiini reactor
tions incorporated will show for a to pi event the expensive catalyst
satisfactory and quick commission ing in the short-term aptHA
from (lying out ef tho top. Downstream-of* EWK'TdTCCVoT-'ltie
production losses fronfucloSHfi'
Ft ants are `nuenehed* In larger
once sustained opcratioiCiMg-1
toroai-e f)|f- _MMlf,h--p-Mtnam
achieved.
The oxyhydrochlorinatlan pro cess is a new process se far ns B Chemicals International n con cerned. It will bo used under licence from the B. F. Goodrich Chemical Company of America and
e's'S products is such that the towers are lined with synthe
tic rubber, then a further tayer of
Macid resisting ,brickwork, and "packed.wittr'ceramic tiles.' "
, The piping in tMl WtMro seolidn icdlW ptfisttWn
the Hoechst Company of Germany who are co-licensors. Both these
companies havo operated this pro-
e,lu,,llc,,
. iii8 titanium its ibis 'are muelf in
cess Ibr many years, and other "--nit;-control 0f th,
Itceruras are currently operating o^ves-^rtl'tfllWrTSibn and-Wm
512G nan>'- c*nadfCwnw*s analysers as found ne;
AJampaenri,ca
and,
more
recently* in"--BWy"-11)-tli,i iiiust-recmrt-pWHS of this kind, and it Is imperative that
term. Nqyoi thclosa, we must expert
considerable' and frequent malnl.cnanco uround the furnace1 area copuactod witii those (-loaning pro cedures, and also in ard arotind Tnc various tower and lower bollup systems for the same reasons.
The products from the cracking section are finally directed to the separation and fractionation sec
tion, where the vinyl chloride pro duct is separated and purified be fore storage and where the hydrogon chloride is separated and re turned to the oxyhydrochlorina tion suction.
SUMMARY
In summing up H muy be saicl that the mam problems facing us during the preroinmlisionmg and commissioning periods, over and above the normal ones met at any similar stage on any othor complex, will be those which will eali for extreme care m ensuring dial all equipment ts correctly m stalled, physically tight, and care fully anfi efficiently dried- out to rqdupe corrosion potential.
All machinery must bo tested
0 The oxyhydroclilorlnotlon route, BADGER-l*fMOWlWW~-- _ 'these are carefully managed and?,, and run up, and as many perl-
in which etliylopc 11 reacted with
Twj" *'** *' * MW I IV
1 tmwaailHntfaeiinnaeAd kbneilkli oatt ItVhiert oconiinnmmitsa-., p*!hae.r.aIl -sections AaMs ,.poNsHslti.bl l-e acao.r
the by-product HCI resulting from, '""W sS"H >'e th first d sole > sionmg stage and thereafter.
rectly commissioned with the
the cracking stage so that alt oft__ Ilcunsecs .InJilUiiitt* .In preparing
The EDC -purification system materials they will be handling,
this by-product ii reabsorbud
~~llUir-piuL'ess;n engineering and con comprises tlireo autumns of some before the main reactions arc ini
The direct chlorination route, trol design aspects of this plant wc what standard design and moans tiated by introducing the basi-
in which elhylcne is reacted have obviously been largely guided nf control, and apart from nor feedstnek materials
directly with chlorine.
by the licensors' and licensees' mal corrosion aspects should throw
in tho loagcr term our nlm must
Both routes contribute in alllast most rocent plants, oud it has been up problems mainly associated be to nintutalH safe operation and
equal measure the required EDC. of distinct advantage to us that with ensuring good fractionating techniques of maintenance at all
m erode condition, foi VCM are- Badger Limited, selected as our coutrol to the fine limits and speci times whilst achieving an eaily
durtiaa. Refore this EDC ran be mechanical contractors, has built fications demanded.
understanding ef our problems
fed to he cracking stage it must . several of these plants In overseas first` `be puri-fied- to remove un countries, and has had mechanical HELPFROM BARRY
and limitations hrespective of their character.
wanted light nnd heavy materials,' design associations with this par-, ' The cracking section is again
fn this way we woute hope not
The evor-q VCM complex Is tlcular process since the early pilot operated under licence from Cor.d only to achieve eventually a highly
llfli-trateu ii simple block terms plant days.
rich and as such has been used clficuint operation but also, in io
in the diagram on till*. page,
As was indicated earlier tho pro at Barry for several years, albeit doing, collate sufficient data and
cess is concerned with producing on a smaller scdIo.
` knowhow to allow for Uic design
HARDWARE What ol the type of plant, oi
elude EDC from ethylene and re circulated hydrogen chloride.
Hydrogen chloride is an expen-
. Wo are foitunatc In having lmil tho opportunity to (Haw on this experience in addition to that of
and Installation of more efficient,
and large), similar complexes in
She future
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RSV0030198