Language selection

Search

Patent 2041584 Summary

Third-party information liability

Some of the information on this Web page has been provided by external sources. The Government of Canada is not responsible for the accuracy, reliability or currency of the information supplied by external sources. Users wishing to rely upon this information should consult directly with the source of the information. Content provided by external sources is not subject to official languages, privacy and accessibility requirements.

Claims and Abstract availability

Any discrepancies in the text and image of the Claims and Abstract are due to differing posting times. Text of the Claims and Abstract are posted:

  • At the time the application is open to public inspection;
  • At the time of issue of the patent (grant).
(12) Patent Application: (11) CA 2041584
(54) English Title: METHOD FOR STEAM FLOODING PROFILE CONTROL
(54) French Title: PROCEDE POUR LA RECUPERATION ASSISTEE DE PETROLE PAR INJECTION DE VAPEUR D'EAU
Status: Deemed Abandoned and Beyond the Period of Reinstatement - Pending Response to Notice of Disregarded Communication
Bibliographic Data
(51) International Patent Classification (IPC):
  • E21B 43/24 (2006.01)
(72) Inventors :
  • SHU, WINSTON R. (United States of America)
  • SHU, PAUL (United States of America)
  • SHU, PAUL (United States of America)
  • SHU, WINSTON R. (United States of America)
(73) Owners :
  • MOBIL OIL CORPORATION
(71) Applicants :
  • MOBIL OIL CORPORATION (United States of America)
(74) Agent: GOWLING WLG (CANADA) LLP
(74) Associate agent:
(45) Issued:
(22) Filed Date: 1991-05-01
(41) Open to Public Inspection: 1991-11-03
Availability of licence: N/A
Dedicated to the Public: N/A
(25) Language of filing: English

Patent Cooperation Treaty (PCT): No

(30) Application Priority Data:
Application No. Country/Territory Date
517,890 (United States of America) 1990-05-02

Abstracts

English Abstract


ABSTRACT
A method for minimizing well recompletions in a multiple
zone hydrocarbonaceous fluid containing formation. A steam
flooding enhanced oil recovery (EOR) is conducted in the upper
zone of said formation via fluidly communicating injector and
producer wells which penetrate the upper and lower zones. The
wells are unperforated and do not communicate with each other in
the lower zone. Thereafter, a temperature activated gellable
composition is injected into the upper zone where it forms a
solid gel. Afterwards, both wells are perforated so as to
fluidly communicate with each other in the lower productive
interval. Subsequently, a steam-flooding EOR operation is
conducted in the lower level and hydrocarbonaceous fluids are
removed therefrom. Polymers utilized in the gellable composition
include polyvinyl alcohol and polyacrylamide cross-linked with
phenol and an aldehyde producing compound sufficient to form a
phenolic resin in situ.


Claims

Note: Claims are shown in the official language in which they were submitted.


WHAT IS CLAIMED IS:
1. A method for minimizing well recompletions in a
formation having multiple intervals of hydrocarbonaceous fluids
comprising:
a) penetrating said formation with at least one injector
well and one spaced apart producer well where fluid communication
exists between said wells at an upper inerval but not at a lower
interval between said wells;
b) heating by steam injection the upper interval via said
injector well to a temperature above about 300°F sufficient to
cause a temperature activated aqueous gellable mixture to form a
solid gel which mixture contains
i) a water dispersible polymer,
ii) a phenolic compound, and
iii) an aldehyde producing compound which upon reaching
a temperature above about 300°F decomposes to yield an aldehyde
and form a phenolic resin in situ in combination with the
phenolic compound sufficient to gel the polymer;
c) terminating steam injection into the upper interval upon
reaching said temperature having removed hydrocarbonaceous fluids
from said upper interval;
d) injecting thereafter into said upper interval the
temperature activated gellable mixture which mixture enters said
upper interval heated to said temperature, where it is heated to
a temperature sufficient to cause a solid gel to form and close
pores in said heated zone regardless of the permeability of said
zone;
e) perforating the injector well and producer wells at a
lower interval so as to provide for fluid communication between
said wells; and
- 17 -

f) injecting steam into said injector well which by-passes
the upper interval and enters the lower interval thereby removing
hydrocarbonaceous fluids therefrom via said producer well.
2. The method as recited in claim 1 where a spacer volume
of cold water is pumped into the formation after step 1) which
keeps any ungelled mixture from forming a solid gel.
3. The method as recited in claim 1 where the gellable
mixture comprises water, polyvinyl alcohol, phenol, and trioxane
which forms a solid gel at a temperature of about 300°F or
greater.
4. The method as recited in claim 1 where the gellable
mixture comprises water, polyvinyl alcohol, phenol, and trioxane
where the polyvinyl alcohol to phenol ratio is about 0.2 to about
2.0, the phenol to trioxane ratio is about 0.5 to about 1.5, and
a gel forms in from about 1 to about 15 days with the addition of
about 0.05 to about 0.5 wt. % of sodium hydroxide.
5. The method as recited in claim 1 where said gellable
mixture comprises a polymer such as polyacrylamide, sulfonated
polyvinyl alcohol, poly(acrylamide-co-acrylamido-2-methylpropane
sulfonate) cross-linked with a phenolic resin which is formed in
situ.
6. The method as recited in claim 1 where steps a) through
f) are repeated until hydrocarbonaceous fluids have been removed
from all desired intervals of the formation.
7. The method as recited in claim 1 where said wells are
cased.
8. A method of minimizing well recompletions in a
formation having multiple intervals or zones of hydrocarbonaceous
fluids comprising:
a) penetrating said formation with at least one injector
well and one spaced apart producer well where fluid communication
- 18 -

exists between said wells at a lower interval but lacks said
communication at a higher interval;
b) heating by steam injection into the injector well, said
lower interval to a temperature above about 300°F sufficient to
cause a temperature activated aqueous gellable mixture to form a
solid gel which mixture contains
i) a water dispersible polymer,
ii) a phenolic compound, and
iii) an aldehyde producing compound which upon reaching
a temperature above about 300°F decomposes to yield an aldehyde
and form a phenolic resin in situ i combination with the
phenolic compound sufficient to gel the polymer;
c) terminating steam injection into said lower interval upon
reaching said temperature having removed hydrocarbonaceous fluids
from said lower interval;
d) injecting thereafter into said lower interval the
temperature activated gellable mixture which mixture enters said
lower interval heated to said temperature, where it is heated to
a temperature sufficient to cause a solid gel to form and close
pores in said heated zone regardless of the permeability of said
zone;
e) perforating said injector and producer wells at a higher
interval so as to allow fluid communication between said wells;
and
f) injecting steam into said injector well which enters said
higher interval thereby removing hydrocarbonaceous fluids
therefrom via said producer well.
9. The method as recited in claim 8 where a spacer volume
of cold water is pumped into the formation after step d) which
keeps any ungelled mixture from forming a solid gel.
- 19 -

10. The method as recited in claim 8 where the gellable
mixture comprises water, polyvinyl alcohol, phenol, and trioxane
which forms a solid gel at a temperature of about 300°F or
greater.
11. The method as recited in claim 8 where the gellable
mixture comprises water, polyvinyl alcohol, phenol, and trioxane
where the polyvinyl alcohol to phenol ratio is about 0.2 to about
2.0, the phenol to trioxane ratio is about 0.5 to about 1.5, and
a gel forms in from about 1 to about 15 days with the addition of
about 0.05 to about 0.5 wt. % of sodium hydroxide.
12. The method as recited in claim 8 where said gellable
mixture comprises a polymer such as polyacrylamide, sulfonated
polyvinyl alcohol, poly(acrylamide-co-acrylamido-2-methylpropane
sulfonate) cross-linked with a phenolic resin which is formed in
situ.
13. The method as recited in claim 8 where said wells are
cased.
14. The method as recited in claim 8 where steps a) through
f) are repeated until hydrocarbonaceous fluids have been removed
from all desired intervals of the formation.
15. The method as recited in claim 8 where said gellable
mixture is injected into said lover interval via both the injector
and producer wells.
-- 16. The method as recited in claim 1 where said
gellable mixture is injected into said upper interval via both
the injector and producer wells. --
-- 17. The method as recited in claim 1 where said
gellable mixture is injected into said upper interval via the
producer wells. --
-- 18. The method as recited in claim 8 where said
gellable mixture is injected into said lower interval via the
producer wells. --

Description

Note: Descriptions are shown in the official language in which they were submitted.


~ ,~,? ~ J !l
57S7.s
~?. F~
~*la~L~ca~
Thi~ applica~ion i~: a continUa~ion-i.n-par~ o~ Se~ial No.
29~, 795 whi~h WAE~ ed on Janu~ry 3, ~9 . I'c i~ so r~lat~d
tD .5erial No. 2~2,8qs whi~h wa~ d on Janua~y 3, 198~.
~h~
Th~s invention rel~e~ to t:lle U~Q ~:E temp~ratur~ ac:tivated
g~l~ that can ~e us~d fc~r prs:~llo ~ont~ol a~r a ~e~m flood ~o
thak increa~;ed amoun~s of hydr~ca~on~oUs ~luLds oan b~
ob~inetl ~o~ a ste~m und~r~wep~ zc~ne in ~ ~orm~tlon.
B~p~ ~ of_th~ I nV~n~
~ n ~ho re~ ry of o~l ~rom oil-aon~alning Xo~mationE;, i~ i~
usually E~ ible to re~over ~nly ~ninor porti~n~; o~ the original
ol~in-pl~ae l~y 6D~c~llod prima~y ~ecovery mQ~hods whiah u~ilixe
only natur~l Por~ D ina~ea~ ~h3 reco~ry oP oil a v~ie~y
~ ~upplementa~y recovery teah~iyu~ are en)~yed. The~e
techniqu~6 lnclu~e wa~cerf loodiny, m~aible floodir~g, and ther~l
recov~ry.
A pr~blem thAt arisQ~ ln v~xiou~ ~looding proaes~e~ i~ th~c
dl~erent ~t~ta or zone~ in the re~ oi~ o~en p~
diP~sren~ perme~abill~s, 'rhu~, di.epl~ain~ f~uid~ enter high
p~ abil~ty or "thief" ~one~ in px~Rfer~ncs to zcms~s o~ lower
~eabill'cy. s~gn~ ant quAn~iti~ o~ oll m~y bQ left in zhne~
o~ w~r pe~meabllity. ~o ~ircum~nt this dlP~lc~lty l:h~
~e~hnique o~ pro~ control 1~ ap~ d to plu~ ~he high
perm~ab~ llty 7.0ne~ with polynle~ia ~el~ and thu~ divert t~e

2 ~J~ 3 h
displac~rlg ~luid into l:h~ ~JIda~wep'c low pe~cm~ ity, oil rich
zones, A~n~ng the pc,lym~x~ ex~mlned ~or imp~P~ins~ w~ter100cl
con~cxm~n~e ar~ ~net~l cro~ link~3d poly~aah~rid~s, m~al
aros~ n~etd poly~o;rylam~e~, and t~r~ania-¢xo~sl1nked
pol~ r~laLni~e~
Pc\lymsrla ~els are: di~3clo~Qd in ~eve~l U. s . pAtan~S. ~mong
~h~Y~ 5. Patent N~, 4 ,157, 32~ whlch i~ue~ ~o Coleqrove on
JunB 5, 1979. rrhi~ gr31 i~ fc)rm~d ~rom w~t:e~, a poly~ h~ride
polymer, ~n a~id ~en~aratlng ~alt arld a mel~minia res~n.
polymeric g~ clo~ed in U.S. I~a~en1: ~o. ~,65B,~s~ which
i~ued ~o P~ul e~ al1 on .~.pril 21, 1~7. This patent dlsclc~e~
an aq~ou~; ~o~U~icn o~ he~R~op~ly~ har~de S-130 ::omb~n~d wi~h
~lDns C1~ ba~$c organ~c: compoundf~ which catiorl~; cont~ined at
l~st two posl~lvely char~ed cen~csrs~. U.S. Paten~ No. 4,71~,9~6,
is~ued to Shu on January 5, 1~8, di~lo~e~ a gel ~oxmed ky amino
re~in~ ~uoh ~ melamln~ ~02~n~ld~3hyde which modi~y biopolym~r~ in
c:omb~n~t:ion with ~ran~itional mQtal ion~. Th~3 pat~nt~ axe
hex~by inc~rpor~ted by ref~enc~ hexein.
Bzlsla ~o th~ pr~ n o~ er~ing di~pla¢ing ~luld wit~
p~lymeria ~el~ is ~he nR~ ity o~ plac~.ng ~h~ polymer whe~e it
i~ na~d~}, i.o. ln the hign permoa}: ility ~n~ . Thi~ i~ po~sible
wh~n Xanthan ~lopolymer~ ~r~ c:ro~s-llnk~d wL~h met~ n~ ~u~h
~3 abcl~rQ ~ro~nd t~ iVQ gelB. The~e ~}e~ ar~ sha2~r ~t~b~e elnd
~ear thlnnir~ hey c:an be ln~ ~c'c6~d into t~ ~orma'clon 6~1her~
~hay the3~ rehQal. I~Ue to th~ gel ~ rh~olo~ical propertles, ~hey
will of nec~ity qo into high p~r~ bil iky æone~ owever, nlany
c~the~ gel ~y~temEa ~r~ form~d in~ . One ~:y~t~m di~lo~ed ln
U.S~ Patent 3,~57,5~2 contain~ a~ryl~mide monom~r,
m~thylen~-bi~-acr~lamlde as àn org~ni~ croE~ ink~r, and a ~re~
radi~al init~at~. T~ y~tem under~aes polymerl.~atio~ ln ~he
~or~tlon tD ylv8 ~ poly~c~ylamide cro~s-link~d ~ith
- 2 w

~ ,'? '~ ? L~
m~thylena-bi~;~a¢rylamide~ ~wever, ~h~ os.lty ~ thç~ G~lu~ion
w~en inj eated ~ ce t~a~ o~ wat~ . Unl~s~ mec~h~ni~ qtion
i~ u~sd, ~he~3e ~olutl~n~ a~3 qU~ pa~ o~ pen~tra~ing lo~
permeabllity, o~l b~a~ing z~ne~ noth~2~ f~nn o~ tn~ u
~atlon involve~ ~hs in~e~ n of p~ cr~lamid~ ~nntaining
ahxomium ; n tlle ~or~n oP chromate . )~ dll~in~ aqen~ such a~
thloUrQ~ or ~c~dium thlo~U~ t~ ~ a al~o inj eGte~ to reduae ~che
¢hroma~e ~n~E~itu ~o C~r~3, ~ ~pecie,s capalble o~ oro~G-llnking
hydr~ly~ad polyaorylamid~. Ev~ thc)ugh ~c~e pol~a~ryl~nide
801U~i 9n ha~ 05ity gre~tex th~n wat~r, it 1~ not c:apabl~ oL
~hc~win~ the ~electlvity tl~t ~ qel can~ ~hus, PO~Q~rY1a~nide8
aroEIs~linke~ w:Lth chronlium in~ u c:an al;o go in'c-:~ low
p~ aabllity ~ont3~ ie not uE~ ul to ~ro~ llnX
polyac~ryl~mid~e above g~:ound and in~ ~a~ khem a3 g01 s, b~¢~u~2
po~ya~rylamide ~el~ unde~gc~ shear degr~dA~lon~ There are ~3r~
~ew g~ h~t are sele~va and th~rmally ~tabla.
:~n addltion tc~ the ~r~Htion o ~Ithie~ z~ne~ durin~ a
wat:elr~l~odln~ ~eCo~rRry toahni~, steam flo~diT)g o~ m
~t:imu~ion proce~ r~3ate ~ unique ~i~uat ~ on in a ~ormatlon
which i~ ~ravity o~rex~ride due to the ~'ce~m ' B low d(3nBi~y~
B~a~u~e o f the s~Ram ~ ~ low den~ y, ~chel ~.wRep path o~ the E;~e~m
1~ ~her~ore bi~E~ed toward~ the ~op o~ th~ p~yzon~. ThU~, ~h~
area im ad~d by tho ov~rricle~ eam may o~ m~y not be o~ low
permeability. Alt~ou~h s~eam pr~f~renkiall~ enter~ ~ hi~h
per~e~bill~ hl~f zone, thæ hlgh ~mp~ ur~ o~ th~ ~t~m
wlll ~1~3o remove hydr~ rbonaaec~u6: ~luida ~rc~m~ por~ion~ o~ lo~
pRrme~bilLt~ zone~ thQ dl~k~nc~ incs~e~q~; ~xom ~eaad entry
lnto the~ ~or~atiPn~ th~ t~mperature will decr~A~o. A8 long as
tl~o temperatur~ i~; hot enou~h hyc~roaarbonac~vu~ flUlds wlll b~
rsmoved from the "thie~1~ zon~ a~ w~ portion~ oP l~w
perm~ablli~ ~ona~.

When ~ rn haF; brok.en ~hrough 'GO a proc~uc~i~n l~ell during a
s~e~mPlo~d, a he~tec~ p~ ion o~ dch~ for~na~.ion will communicate
witl~ an i.n~ct~r we~l. Th~E~ h~ d p~rtiorl may include por~on~
~t' bo~'ch high ~nd l~w p~nee~ y ~eam override zc~nes. Fo~ this
reaE3on, a gel ~yEIt~am w~liah ~an ~el~c~ rel~ ~nter a hlgh
p~rm~ y "~hie~ zone may no~ en'c~r e~ low perme~b$11ty ~one.
Tl~u~, a ~t~e ~leat~e ~el m~y no~ preven~ s~e~m ~rom entaring
lnto ~ hea~6~d low permeabili~y zon~3 whl~h has beell depl~ted of
hydrDc!arbonaceou~ d~.
Th~3xefore, what 1B n0eded 1~; a me~hc~d ~f 2~or~nin~ a ~ol~d gel
in ~rea~3 of ~ m~ iple produck~e zone ~orm~tion which ax~e~s have
b~n hea~ed to 21 t~i3mperel~urf3 above 300DF BO as to minlml~e well
r~~o~plet~ons .
~L~
q~h~ ~ invent.ion is ~Ir~ted tc3 ~ me~hod for minimizing w~ll
recomple~lotl~ in a hydroc:arbonaceou: ~lui~ antainin~ form~ n
having ~nultipl* produc~ive int~ An upp~ pr~ductlvQ
int~rval i~ hRatad to a t~mpe~r~ uro ln exce~ o~ abou'c 300F.
PreP~rably ~ ~aam ~la~d enhanc~3~3 oi~ recovery me~hod 1~ u~ o
h~at tha upper p~oductlve ~one. Th~ upper produc1:ivQ zon~ is
p~n~trated bsr ~lu~dly ~ommunlcat~ng inj6~cltor and produ~3er w~
~he~e w~lls ax~ n~t petfox~at~d ~t ~ lower ln~e~l arld dD no~
fl~dly ~ nuni~ate with each otller.
Wh4~n ~tQ~ r~akthrough occU~ at th~ p~oductlon w~ n~ a
te~npar~ture in ~3xa~ o~ about 3 00 ~ F i~ reach~d in the upp~r
produc~iv~ zone, ~ .m lnjec~ion 1~ ce~ d. A~'cerw~rd~
tomp~atur~ ac~ivated g~lla?~le c~mpo~it1on i5 inj~ct~d into sald
uppe~ prDduatl~6l interv~l 'ch~ough both th~ tn~ectc3r anù producer
w~lls. He~e it ~or~n~ a ~lid gel 'chereby blool~in~ said upper
p~oductlv~ rval to ~luld ~low.

~1 lb:~ FI~UI'I llOBIL FFI!R n~s CC1111~ 10 ~ 1613563g86g P.08
,~ a ~
Th~re,af~r, ~he ln~6~c~or ~nd prc~cluce:~ w~lls ar~ per~ora~d
a~ a lowar produa~ 3 ln~rval ~ A~; ~0 Al10W l!o~ ~luit3,
oo~muni~at~on b~w~nn sai~ w~ n~ id w~ h~ve beon
~eaompl~ed at ~he ~oWer produc~v~ e~ , a ~am-Plooùlng
enhana3~ r~cclvery opelr~tion 1~ ~ommenaed ln~ aid lDw~r
pro~ucti~ in~ral to rsmove hyAruo~bonacs~ouE~ ~luid~ thsrs~rom.
'rh~ llab~e compD~;~ti~n u~iliz~ hor<~in fo~m~ a ~l~id ~olid
~ol upc~n re~hinsJ a temper~ure o~ abou~ 3so~F to aboutc ~sO~F ln
th~ uppex producc~v~ lnt~2tl. The ~e~ble o~npo~lon con~aln~
~ wa~ar disperEl~le polym~3r, ~n ~ld*hyd~ con~aini~g compDund
whi~h daa~mpo~ee ~o yield ~ malduhyde, and a l?h~nolic c~mpound.
Upon r~ahlng ~ activ~inq tempe~a~ure the~ ~yal~c dlmor
d~:OmpO8Q~ tD ~ield an aldehyde which in ~urn rQZ~Clt~ with th~
ph~nolla ~ompound to ~orm phonolic re6:in, ~h~ ge~an~, ~n ~ u.
~he~Q~ r, ~hl3 phenoli~ resin g~ th~ p~lymer thereby fc~rming a
rigid ~el.
~ hl~ rlgld gel r~dua~ 'che~ tr~n m~ ility o~
hydro~bonac:~ou~ ~luld~ ~hrou~h ~che upp~r px~ductiv~ in~rvaL.
In adclit~n tD reducin$~ the 'cran~mi~:ibili~y o~ ~luid~ ~h~ough
the heAt~d upper in~e~l, the ri~ld ~B}. ~au~e~ am ~rom B
~ub~ent ~tea~ ~l~oding ur ~team ~ mulati~n opera~ i~n ~o be
dlv~rted ~o a deep~ Ye1 in th~ produalnq ln~xval, thexeby
pr~ducing addltlonal ~ydr~aar~on~eou~ ~uids to ~he ~;us~ e.
G~lla~l~ aqu~ou~ omp~ ions w~i~h c~a~n ;eorm a ~ol~d g~l
upon ro~ct~lng ~ temper~uro above 300'~ ~re o~mp~i~;od ~
wat~ di~per~ibl~ polymar~, phQn~ compound~, and aldRhyde
produaing aomp~und~, Polyn~er~ wh~ah ~r~ d her~in aa~o
~Qleate~ ~rom a member of ~he ~r~up aonsi~tin~ o~ poly~lnyl
alcoh~l, po~yvin~l Alcohol ~opolymers, pol~acryl~mide, polyvinyl
~mine, ~ul~on~te~ polyvinyl ~laohc~l, and poly~aa~ylamide-
~arylaJn~ 2-me~hylpropann ~ul~on~). Phenoli~ aompound~

w~ioh can be u~:ed ~.nclud2 phenol, c~cho~, r~E~o~inol,
phlo~ogluc~nol, 4, ~ iphenc~ , 3-dihy~r~xy- nap~thalene, and
r~lated ~mllar compound~, Aldehyd~ produc~lng compoun~ which
can bl3 u~ llzEtd herein upo~ reach~.ng ~ np~ratu~e ~bo~ ab~Ut
3 00 F ~noludo trlox~, pa~P~rmaldQhyda, ~nd tetra~xane .
~ t is t~eref~re ~n ~b~ct o~ thls inventlon ~o provid~ ~or a
tQmpsra~.ur~ actlva~ed gella~l~ composi~l~n which c:an be deli~rer~d
inl-~ a ~eated upp~r produa'clve zon~ hav~ ng a kemp~ature
~u~ ient t:o ac~ ate ~ld compo~;itlon and 6~1QCtiV~1Y ~rm
~ol~d gel ~hereln.
nothe~ ob~ec~ o~ ~hi~ inv~ntic1n to pr~rid~ ~or a
~e~nper~turG~ ~ck~va~d gellabl~ co~npDeitlon wh~a~ can be dQlivsr~d
~n~ a ~o~matl~n ' ~ ~'cQam ~ d~d zon~ h~vln~ ~ tempHrature above
~bout 300F and th~reaftex fo~m a ~ d gel ~her#in.
It is ~t ano~he~ ~b~ ~ct D2~ ~hl~ ~nvention t~ pro~ e ~or
~ompo~l~lon which ~idQ ~oxming a solld g~l in a ~o~ler 30ne of
les~e~ permo~bili~y or an unhe~t~d zone o~ a f~natlon,
It is an~the~ Purthe~ ~b~ ~ct o~ lnven~i~n to provid~
~r a compo~itlon ~hat w~11 minimlze gql damag6~ a cool3r znn~
o~ low0r perm~bili~y w~ ing pore~ ln a hi.gher
perm~ahil~ty ~on~ having ~ temper~ku~ ab~ve A~hUt 300~,
It i~ a ~tlll ye~ ~ur~her c~ec~ o~ ~hl~ inven~lon to
pr~vld~ so~npos;L~ion ~hich will inc:r~a~e ~h~ e~cienay o~ A
dri~ ~luid thr~u~h ~ ~or~na~c~on ther~by incr~a~ing th~ yield o~
hydroc~rbonaa~ou3 ~luld~ th~e~rom.
~.~h~
FIG. ~ ~ a diagramn~tlc plall ~lew o~ a ~orm~tien wh~3re
~t~am ha~ p~ed ~21rough a hl~h pe~ne~h~llty zc~ne or upper
productive inter~r~l intcl a p~duc~ion w~
- 6 -

'~ ~, ? ~
J ' 1;, ' 1~,7 '~ ,~
FI~. 2 :i~ a dlag~mn~tic: pla~ vi~w where ~cht3 hig~
p~me~bilit~ ~one ~r upp~r p~c,duc~ive intu~v~l h~ be~3n clo~ed
With ~ he~t ~ tlv~ gel whlle ~eam is p~~1ng through a low
p~r3neabl~ity zon6~ c~r ~ow~ p~uc~iVG~ int~
FIG~ 3 i~ ch~matl~ repr~ n~ation which ~llu~trate~
tempe~Ur~ d1E~t~l~u~ion in~o hlgh and low psrm~abili'c~ ~on~ o~
a ~o~matlon durln~ ~eam ~loo~lng or ste~m ::tlmulationO
D~srlng tho re~ov~r o f hydrocarbonAcG~ou~ f lulc~s ~om a
multipl~ produatlv~ in~erval i~orm~t~on where~n a ~ m ~loodin~
proc0~t is utilized, a~ is ~lown in PIG. 1, ~ m en'c~r~ oonduit
~ o~ in~ection welL 10. A~te~arclE;, ~'ceam exi'Cs in~ectiG~n well
10 vla pe~o~ion~ 12 ~nd en~r~3 high p~rme~bility zGne or ~app~r
p~odu~t~e in~rval 14. St~m ~nd hydrocarbonEI ob~cainad ~rom
h~c~h p~rmeability zone or upper p~oduct~v~ int~rval 12 axit
~h~ough p~oduc:t~on well 16 via per~oration~ 1~. The~e~tQr,
s~e~m and hydroc~rbonaceou~3 ~l uids exi~ produ¢tion w~ll 12 via
c:ondult ~. Du~in~ this E;t~am 1OD~in~ proces~ e high
p~r~e~bill~y Zone or upp6~r produ~ ve in~E3rva~ 14 is heat~:d up by
~che st~am. Whil~ being heelta~ t~mp~rature contaur is
d~v~loped in elth~r a ~ am ~lo~ded o~ a ~t~am stlmul~d
~o~ma~i~n. Thu~, ~he uppe~ produ~L~r~ lntorval or z~n~ ~wept by
~t~am in ~ld p~odua~ivs3 lnt~3rv~1 h~vo the high~t3t temper~ture~
ln th~ ~orm~tion whll~ th~a un~W~pt ar~ or ~Xfl~ not: reCBiVi
~team in the fc~r~na'cl~n h~ he lowe8t. Thl~ conc!epl~ iR
lllu~tr~ted ln ~IB. 3.
Th~ ~onc:ept lllu~ated ~n F~ equ~lly appllcsabl~ t~ a
th~ l t~ct~ni~sue wh~re ~3tea~ ; utillzed wLth ~ sin~) e w~Ll in
multi.ple produa~v~ ~n~ex~al Eormat~on. 0~ course thl~ weli 1
not per~ra~d ~ a lower p~odu~tlve intorval, Thls t~h3~1~ue i~
-- 7

~J (J/ ', 'i" S ~ J~
known aG ~hE~ ~hu~ d puP~ method. Thi~ m~3thod 1~3 de~crib~d Ln
U.6, P~t~nt Nc). 3,~59,1~ff ~hich i~ hur~by lnc~rpor~ted by
refe,~63nae h~reln. Irl t~.B me~chod, E3~ am 1~ in~c~e~ via ~ w~
~n qu~ntit~e~ :uf~ nt to heat an upper ~ub~erranean
hydrooarbon-be~a~"g form~tl.on in ~ vic~ it,y o~ ~.h~ w~ll. The
w411 1~ then shu~-in ~or a E~oa~lng perio~, a~ter whiah it i~
pl~aed on p~o~uction. Arter p~o~ua~ion ha~ d~(:lined in ~he upper
procluctive inte~v~l the "hu~ ~nd puf P~ me~hod may ag~in be
employod ~n the ~ame w~l at ~ low2x produc~ivH ln~arv~l to agalr~
~tin~ulate produoti~n. Fl~id communicatlnn With the lower
procluctiv~ lntar~al i~ ~b~ained ~y recomple~ing or p~or~lng
the~ well at ~h~3 low~ ~nt~al a~e~ ~o~min~ lid ~el in the
upp~r p~oduat~ve inter~10
The applia~ion of ~lngle we~l scheme~ employing ~te~m
lnje~-ion as applied to heavy o~ ur bltum~n i~ desc:rib~d in
U.S. Paten~ No. 2,~ 3~, whlch utllize~ g~avi~y ~r~nag~. Thi~
patent i~ incerpl)ra~d ~y re~erenc~ l~erein. An improvement o~
tht ~ ms~od i~ de~ibe~ ~n a la~ce~ paten~, U. S . Patont No.
3,1~5,1~;0, in whioh ~3teAm i~3 in~ected and app~opr~ately ~imed
whll~ p~es~uring and deprç~6uring ~3p~ ~X'R employed. Whe~
applloable to a ~ield p~te~rn, ~he "hu~ ar~d pu~ hniquo may
be ph~ed ~t~ th~t numerou~ w~ 3 a~e on an in~ation cycl~ whlle
~ther~ aro on ~ productloxl ay~le: ~he cyc:le6 m~y t:hen b~
ra~r~ed~ 'rhl~ pa~en'c is h~reby incorp~r~e~ by r~r~nce
l~ere~n.
U. ~. Pa~n~ No. ~, ~57, 650 d~ ibe~ a method f~r r~ov~in~
h~h ~l~a~sity olls ~om su3~ur~ orm~til~n~ u~n~ ~team and an
in~rt g~ to pre~ r~ze and hea~ the ~orma~ion and the oil whi~
t aon'caltl~ . Th~ ~t~3~m flnd the inert ga~ y be in~eot~d eith~r
~mul'can~ot~sl~,r or s6~u~n~1ally, a.g. ~te~n in~ ion, ~ollow~d by
a ~oak period, ~ollowed ~y ln~e~ion o~ inext ga~ Inert ga~

JL~ r~ lL ~ hlR Of lK5 C0~ i ro 9 161~63g~ P. lZ
' ' ~
raferred ko inc:lude helium, m~thane, aar~on d~c:xid~, ~lue ga~,
s'c~k ~ And oth~r ga~ whic:h ar~ nonconden~;~ble in char~ater
and wh~h do not ira~arala~ ~lther wlth ~he ~orma~ion ma~rlx or ~h~
oil or ~ther ea,~h material~ c:on~,in~sd in ~h~ natrlx. Th~
paten~ 1~ he~reby inc~rporateca ~y re~e~r~nc~e h~rein.
Wh~n it becom~ n~ orlo~nia~.l to aon~ nue~ ln~ ec~.ng s~eam to
rQ~C~r hyàroa~r~on~ceou~ ~luld~ ~rom an upper producs~ro
ln~en~al ViA a "hu~ ~nd pu8`~" me~hod o~ ~rc)m a ~sm ~looding
m~hod wher~ an in~ ection and ~ producer w~ r~ ~3mployed a~
~ho~n ln FIG~ aam in~ea~lon ir~o injec:~ion well lO i~
coQ~ed. ~vc~ntually, ~ a~ ~n~ hydroaa~bonz~ 30s ~luid~ ce~s~ ~o
~low int:o produa~r well 1~ ~rom ~che upp~3r pr~d-~c~lve int~rval.
P~duo~ well 16 i~ t~d to al ~empE~r~ure o~en in exc~ o~
300''~. ~n or~er to obtElln hydroc:arbona~eau~ ~luids fxos~ low~r
produative int~rval 18, skeam ~ant~y ~nto heated upper interval 14
eaq~d. Communia~ion ther~ore ha~ ~co ~ t~bli~hed b~ween
ln~ec~/~r ~4ell 10 and produoer well 16 ~ th~ l~wer produo~ci
level 18.,
~o ~a~mpli~h ~ e, in ~no Qmbodirnent o~ ~hi~ in~r~ntion, a
te~np~ra~ur~ ~tivat~d gellabl~ compe~ition i~ dire¢t~à down
produoo~ well lG. Pr~or to dlrec~lng ~ald compo~ition irlto
prod-~c~ w~ll 16, ~ch~ temp~ra~urla wl~hln ~he well i~: detfl~snined.
Th~ ~emp~ra~ur~ qan b~s m~aa~u~d by A dowa~hc)l~ d~ a~ i~ known
by thO~ ~kiLlled in th~ a~ ch~ w~ll temper~ r~ ~ ho'c
enough to actlvat~ ~he gellab~e co2npo~ition ~o as t~ cau~e
~olid or r~gid ~el to ~o~n ln the well~ ~h~a well iB c~ol~d.
5Qveral m~'chcd~ can be u~e~ to aool the well~ vn~ embo~ nt
a ~o~llnç~ ~luid pr~ferably w~er, ~n be lnj~f3d af3 ~ spac~r
prtor to ir~ectlng th~ gellable aompo~Lti~n into ~ell 1~ and tl
ro~mation~ Xn~eo~ n o~ th~ coolln~ ~luld i~ n~inued until

' ,,i?~ s,? /.~
~ro~uc~r well 1.~ haf3 ~n aoolf~d ~o ~ k~mp~rz~ture o~ ou~ 3~F
~o ~bot~t 4 5 o ~ ~ ~
Xn Anoth~r em~o~ nt, ~ch~ coollny ~luid can be oi~c~l~t~d
lnto produc~ well ~ ~hrouyh ~ n-::entr~c s~ri~ conE~ ing o~
aJl lnn~r and an outer tu~ing . ~hEI cool ing ~lu~d ~1~3WE~ down tha
in~er tub~ng and ou~ o~ t:h~ ~oncQn~rl~ ~crlng by th~ o~'ce~
tul31ng~ ~urin~ the c~r :ul~loh of the cooling ~luid ln~o and out:
o~ produaer wæll 16, t,h~ concen~la Ei~rir~y r~maln~ in oon~eac~
wi~h p~duc~r w~ c~ a~3 ~o cc~ a te~np~ tu~e o~ ~bout
300'F to abo~c 450~F. ~oollng producer w~ll 16 ln 'chi~ manne~
allow~ ~r mo~e p~ec~.~e con~rol o~ ~h~ coo~ proce~. Upo~
obta~n ~ ng a des~ed t~mp~r~ure su~lci~nt ko pr~vent pren~atux~
~llatlon o~ ~h~ g~llablQ c~o~po~i~lon, ciraul~ion o~ co~lin~
~luld in~o p~o~ucsr well 16 i~ ~topped~
~ te~ cir~u?~iDn o~ c:Doling ~luid ln~o ~h~ c:on~en~cric:
~trlng is ~topp~ e ~omp~turq~ ac:t~JA~ed g~llable c~r~p~ lvn
1~ injea~63d d~wn prcduc:~ w6311 1~ vi~ ~ch~ conc:~n~rlc strlng. ~o
accosnplish ~hi~ a ~ur~ r~turn valYe on th~ cont:~n~ri~ ~rlng
1~ cl~o~ ther~by ~oppang ~he c~ul~t~on o~ ~Luld ~rom ~h3
~on~en~rlc ~rirlg. The a~ va~ed g~llable compo~i~ion i~
dl6pl~cad i~to hi~her productive intet:v~l 14 by ~ontlnu~d
c~ion ~ pumplr~g into th~ ~:onc~ntrl~: s~rlng. Dl~pla~em~7~t o~
~he t~nperatur~ aati~JAt~d gell~blQ c~omposi~lon a~n b~ alded by
plaaing a ~railing ~luid e.g, w~a~ in'co p~odu<:ar we~l 16 through
~ prns~ur~ aa~ated valvo or ~uptur~ dl~k.
Alternativ~ly, a --
,-- A pre~ure act~va~ed v~lve or ru~ur~
di~k is ~l~o u~d ~o aau~:~ a ~empera~urt3 ~c'civ~ted g~lla~le
colnpositlon ~o ~low into thQ produc~r w~ r~m th~ concentrio
strinq af~er th~ e;~lrface return v~ ; clo~ed on salcl
cono~ntrl~ ~trln~
Pve~- ~F; '~'ca K6~ep ~n~ gella~le ~ompc~aitlon in ~ ~ool~d

., 7
~or~ltion, thr~ in~3ction e,kr~.n~ c~n be ln~ul~k~d. ~di~l~n~lly,
~he gel~a~le cc,mpo~it~on ca.ll be k~:pt c:o~l by u~ing an ~ lon
strln~ ln ~om~hat~orl ~ith ~.h~ concendcrlc s~riny.
Ona~ the lnje~d g~llab~ e compo~tlc7n ~ ate~ up
p~oduc~r well 1~ ~ heated upper pro~uc~g in~er~al 14, it Porm~R
a ~l~id s~l~d gol, ill produc:ing :In~Br~al 20 upon r~ h1n0 a
temp~ratu~e o rom a~3ou~ 3 oo D ~0 abou~ 450 ~ F . Sin~ ~hf~ lower
pro~Uc~ive inte~val 18 1~ les~ t:~an zlbout 3 00 ~ F, k~ abLe
aompo~it~on ~emain~ ungell~d ln ~:h~ interv~,l, Un~elled material
can ~e ~emo~ rom lower produ~ive int~rv~l 18 by pUmping it
oU~ or in~ectirlg Water to circ1ulat:e lt eu~.
A~ter ~llowillg ~uffl~;ient ~ima for the gQllable cornpoaiti4n
o~n a ~olld gel i~ upp~ lev~al 14, ~ e~m ~l~od ~nha~ od oll
recovery ~ hod i ~ub~qu~ntly comm~ sd ln ln~eation well 10
and ~ommunic~clon is ~t~.bli~ d wi~h prot3ua~ w~ll lG v~ lowsr
p~oduGtive~ level 1~ thro~gh ~ntp~ perPorationE; 12. 13oth
we~ r~ ompl~3t~d ~t lower 1~3vel l~ Por ~luid ~ommunicakion~.
Utlliza~ion o~ thl~ met~od in~r~a~;~a ~weep o~ aien~r in the
PO~Ati On W~ 3 enhanc:lng ~h~ r~acovery ~ additional
h~dxoc~r~on~c~ou~ ~lu~d~3. The ontir~ p~ae~ aan 1~* rG~p~ated
until a ~le~ire~ ~t~3a~n ~r wa~ o oil ra~io ha~; be~n obta~n~d.
Should it ~ecom~ ne~e~ y, ad~ion~l p~3rforati~n~ ~an b~a
di~e~ted ~hrough injoctor W~311 lO and pr~ducq~ wQll lG lrl~o low~r
pxoduQtive ln~s~rval 1~.
~ u~ou~ gsll~ble heA~ ac:~lv~t~d ~omp~ lon~ whlch c~n ~e
utlllzed herein ~re compri~ed oP ~ p~lynl~r, a phenolia compound,
anæ an al~eby~e~ Poly~n~r~: u~cillzed here:Ln ar~ w~t~ perE~lb~a
polyJn~r~. The, t~rm "po~ or~ iG employRd ~enerlca~ly ~o lJ~¢lud~
both homopolymer~ and cop~lymer~. The ~erm ~'w~t~-d~pe~ibl~
polymer~ u~Rd genericEIlly to ~ clu~ tho~ polymorE~ which are
truly w2it~r soluble ~nd tho~e pol~n~ whiah ~re ~i~p~r~ lo lrl

water or in c~h~r El~u~ou~3 medl~ o ~orm G~able colloid~l
~u~p~n~3ionE3 whle:h c~n be gell~ 1$ ~ h~ term l'aqueo~
dl~p~rslon~ t~llz~d g~nerl~ally to in~ud~ b~kh tr~B
so~utic~ns and st~bl~ collo.t.dal E~u~p~ on~: o~ componen~ o~ the
aon~po~ on c~ ~h~ ~nv~n~lon whi~h c~n b~ g~lle~ a~ will b~
de~x~bod l~e~reln. WAter-di~:p~r~:1bl~ pol~nor~ whiah ar¢ u~d
her9i~ ar6~ t~ad ~r~m ~ me~nbor o~ the group c:on~lsting of
polyvinyl alcohol, polya~zryla~i~e, gul~ ated polyvinyl a~cohcl,
and poly(ac~rylamidel-co-acr~lAmido 2-m~hylpropane ~ul~n~t~).
Polyv~nyl al~ohol (PVA) at VAriC)U~3 d~grGl~BE~ O~ hydroly~ls axe
useful~, other polym~r~ cont~ ng OH, Nll2, CONH2, 4nd ~;~
~un~t~oh~l g~oup~ are ~lao us~ul. P~l~v~nyl a~ine, an~
oopc~lymar~ con~ining t~le prev1ou~ly ment~ oned ~un~ L~n~ group~
ar~ use~ul. Any ~i~ thesE~ wa~er-dispe~iblç polym~r~ ~re plac~d
into ~n a~ueous~ mix~uxe in ~noun~ o~ ~rom ~bou~ o . 5 ~o about ~. 0
wt~ rhs aq~2~0u~ m~dium aan ~ompr1~ ~r~h water, b~ack~
~t~r, ~ ~S3fl wa~qr, ~nd m~x~ureE~ ~hereo~. Polya~ryl~mldQ and
poly~-Acrylantid~2-me~hylpropane ~ ona~e) ar~ di~u~ed ~n
U~. P~ n~ No~ 4,44~,22~ whi~h i6~ued c)n Apr~l 3, 19~4 to
~w~n~on. ~hl~ patent 1~ hex~h~r in~orp~r~ed her~in in its
en~1rety.
A~t~ p~clng tha ~o~e~te~ water-dl~p~r~ible polym~r into
the ~queou~ mediu~, a phsnoli~ c~pound 1~ ~dd~d ~o t~ mix~ua~e.
Phenolia co~poun~ w~l~h can ~ u~ed her~ln inal~de ph~nol,
naph~hol, c~te~hol, re~orclnol, phla~ogluainul, 4,~' diph~nol,
1,3-~ihydroxynaph~halene, ahd rel~t~d ~lmilar aompoun~. Tbe
~mount a~ ph~nol~c aompound utllized ~ould ~e in a~aes~ o~ 0.5
~t.~ or higher. ~he amount ~ phenolL~ ~umpound u~ed her~in
~hould bc suf~lcient ~o lmp~rt t~l~ d~ir~d gellation ef~ect
within t~e de~ired ~i~e per~o~.
- 12 --

5, j1~
Ono~ th~ ph~noli~ c~mpound ha~ b~an aclded, a
w~sr-dlspe~sible aldehy~e 1~: tnixed into 'ch~ ~que4us mlxture.
IJnd~ proper ~ondi~ion~ oP u~, ho'ch ~liph~ic ~nd ~romatl¢
monoal~ehydes, And d~aldehydees, oan ~E~ u~Qd. Ths ~lipha~lc
m~no~ld~hyde~ contEIining from ~ ko abou~ lo ~arbon a~oms p~r
mctlecule a~e pre~ntl~ pre~er~ecl. ~p~se~ta~ e exnmp~s of
3uch aldehydeR in~lude ~c~rm;~ldehyde, tri~ane~ t-3tr~0xane,
polyoxy~thylGne, an~ othe~ p~l~meric: ~ldehyd~s. ~p~esentati~
ox~mpl~ oP di ald~hydes incllJde glyoxlll, glutr~ld~hyde ?
ter~aphtt~ dehyde, and mi~tture~ ~her~o~ Th~ m
"t?ato~- d~per~ible~ emplo~d g~ner~oally te in~lude bo~ch tho~e
ald~3hydQs whiah a~e ~rul~ wa~er-~olub~e and kh~se alclehyd~3~ o~
l~mit~d water ~olublli~y ~u1 whtc~ di~per~ible in w~t~r or
other a~u~ou~ m~qia ~o ~0 ~n bs ef~ectl~,re gelling ~gents. ~h~
p~e~erred ald6~hy~ ih trioxane.
An~r ~uitable amoun'c o~ ~riox~ne ~nd ph~no~Lc: comp~und~ can
bQ u~ ed h rein. ~n ~11 in~ noe~, the amount o~ aldehydo ~nd
phenolla compoun~ u~;Qd ~h~uld b~ ~mA~l ~ul: in an amount
~u~flcient to ~ause g~ ion of ~n aqueoU~ di~persion u~ a
polymer, the ~Idehyde, an~ thR pl~enoll~ ~ompound. A~ ~ g~neral
guide, the ~mount oP ald~hyde u~d in preparing thQ s~al
~omposl~ions h~3r~ will be i~l ~h~ ~ange o~ Xr~m abo~t o. O~ to
about ~, pre~ra~ly ~ . O ~o about ~ . O w~. ~; b~d orl th~ a~
weight oP thl3 oc7mpo~ition.
A prePer~ed tempe~aturu aatt ~va~ g~ bl e mixture ~olnp~i~e~
polyvinyl alo~hol, ph~nol, ~nd tri~xan~. Th~ e~ect o~
t~mp~ratu~e on said mlxture i~ ~hown in l~abl~ 1. Wh~n expo:ed to
a ~orrn~iDn having ~ ra~ur~ o~ L~bou~ 300~ t~ ~bout 35~P or
hi~her, ~ m qel will ~orm it~ about 1 day ~o ~bout 1~ day~ when
0. 05 ~o about 0. 5 w~. 96 o~ sodlum hyd~xlde i~ u~ilized a3 i~
~hown ln ~able ~. Poly~inyl al~o~ ol i8 ueed in ~moun~ o~ aboul;
- 13 -

~ 'J
0 . ~ ~o ~bou~c 5 . 0 wt. % . Ph~nDl iQ U~:Qd irl abo-~'c O ~ 5 ~o ~bout 5 . û
w~.~ or hig~er. Thl3 p~le3~ to s;~lox~nl3 r~s.Jcl~ 1~ abou~ 1:5 to
O ~ 5, pr~ r~b~y a~ou~c O . ~. The polyvinyl alcoh~31/pht~nol we~ght
rat I o ~ ~ ~rom abou~ o . 2 ~o ~bou~e z ~ ~f C~UrAa, ~ lowl3r x~tio 1
u~d when ~har highe~ olecul~r w~ h'c po~ r: are utill~d.
Pol~m~ concen~rat~ion 1~ dl~eotly proportlonAl 'co the gel
~trengt~ . A rlgl~ gel 1~ ~or~ned whlch i~ propo~t ional ~o the
~ol;al material~ cor~tent.
~A~I,E
Ten~p~rAture senf~iti~rity op P~tA/~heno~ ioxan~ ~;e~atl~n
~emp, ~ ~oo 300 ~50 ~oO 450
G~l TlSne, days no g~l no gel ~ 1 1
2 . ~6 P~'A. 4% ph~n~l, 3% ~rioxan~
TABLE 2
~e~t o~ NaO~ Conaent~ion ol~ G~ Time
~OH. 3~ $,~F
0 . 05No ~el 15 days ~ days 4 ~ay~
O. 1 ~ lB ~ 5~7 ~ 2
~. 2 " lZ ~' 2 " 1 day
~ 1 d~y 1
~ 1 d~
2 . ~% PVA ~ 4 ~; pheno1, 3 ~ trioxane
PrLc~r ~o in~oc~in0 ~he aqu~ou~ ~omperelture act~v~ed
g~llab~ mixtu~e, ~he f~ tion i~ h~t~d a~ men~Lonad abov~
d~lr~n~ ~ ~te~m ~loodin~ ~r ~am 6~1:imulatic~n ~nhanced oll
r~co~rer~ pr~ceEs~ . A ~orma~ n ~e~mperatura o~ ah~ut 3 50 ' F ~
pre~err~d. Th~ m~tl~od oP tt~ imr~nti~n can el~o be u~ed when
the ar~s in ur ~ub~n~all~t near el~h~r ~h~ in~ection W311 or
tho p~oduat~on w~ll h~ b~n he~d ~0 the d~si~d temp~r~ture,
~ 14 -

S~c~uld lt be de~r~d, t~ gella}~ omp~3itlon c;~n b~ in~e~t~d
into ~uth th~ lnjec~cor ~Jld producer well~ ~o ~ tD e~c~iv~ly
clo~e o~ t;ho~ aa~ed a~eas in al~;e pr~xim~.~y t~ th~ wells.
Thl~ cona~pt lg depia~d in F~gure 2.
Thi~ me~hod i8 alsc~ par~Lcularly ~ne~iclal when i~
d~3~ire~ to ~lo~e the i~e~ d area a~ound a produc'cion well ~hich
hae ~uP~red a p~e~ature ~team brG~1cthrough. ~ hiE~ uation,
s~eam injection i~; c,~ e~ ~nd ~h~ ~empere~k~lr~ tlvated gellable
nix~urG~ i.s in~ ~ctad in~o ~he pr~duc:tion w~çll ror a ~ims
suP~ic:ien~ anter the ~as wh:~ch comp~i~e the prem~ture
bre~3ctllrough zone. ~Ptarw~rds the g~ ble mixture in tnA~c ~on~
llowed to ~or~ a ~olid gel. or~Q the ~lid gel is f4~ d, an
enhancb~d o~l ~ec:ov~3~y m~thod in w~ h a drivQ flui~ i~ u~lized
c~s~ be inJecte~ ei~he~ ~hrough the injeGtion w~ ar tn~
produc~ well to recover hydrocar3~onac:~ou~ fluid~ ~rom ~ le~
pernl~abl~a z one C)I t~e ~orma~lon .
A~ denlun~rat~d ~ tha novel'cy o~ ~h~ lnven'cion 1~3 tllat th~
cro~-linking rl3aa~lon is ~ivated at elev~ted temp~atur~
gr~ r than aba~lt 350D~. The a~o~ linXlng re~otion i~ not
actl~ratsd a~ temper~tures und~:r 300'~ t high temperatu~e~,
trioxane, a cycl ic d~m~3r 4 ~o~mald~hyde d~compose~3 to yiol~
forlnaldehyde whic:h in ~u~n rE~aats wlth ph~nol ~o ~:orm phenPllc
resill, the ~elant, ln ~itU. Ph~nolla re~ln '¢hQn g~ h~
polym~r.
Wh~ t i~ ~esired to obtain lncrea~d ~weep ~f~lci~noy,
gel~ e~ thls lnventlon aan be uf~ed ~o plug a prevlou~ly ~w~pt
portlon c:~ a ~ormation ~rhic:h )2a~ been heat~d ~e a ~ernporatur~
exa~ o~ 300DP~. Sai~ gels aRn ~7e direc:t~d to area~ o~ ln~reased
poro~ity. Ona~ ~ ~olid ~1 ha~ Pormed, hydro~arbon~c~ous fl~lid~
~an b~ r~no~recl ~rom an a~ea o~ er perm~ahllity by utllizatLon
i~ any o~ th~ below me~h~ds,.
- 15 -

ç~ n'. ? ~
Addition~Lly, th~ embo~imt3n~l3 de.~cri~d ~,boY~ cE~ be used
whe~e the p~oduca~ well i~; in-csslng gr~vel pack~d for ~An~3
c~r~t~ol .
S~e~mPlood proceE3~ wh~ch aan be utilize~d af~ clo~in~
pr~ c~ inte~v~l 18 w;L~h ~h~ g deEIcrlbed herein ~r~3
d~ail~ irt U.~. Pat~n~ N~s. 4,~8g,7~3 and 3,91B,521 l~u~d 'co
ShU anc~ ~nav~ly, re3pe~t~vely. ~h~ patent~ are hereby
oc~rp~ra~ed by re~erence h~rein~
~ 1 ~h~ugh the pre~aen~ invention ha~ be~n de~a~ibed wi~h
prererr~3d embs:d~on~ i8 to 1~ under3~0~d ~h~ modi~lca~lon~
and va~iations ~y k~ ~e~30~ o witho~ depax~lng ~rom 'che
8pi~i~ and sc~p~ of thi~ lnv~3n'cion, ~9 ~ho~e ~klll~d in th~ art
wi~l re~dily unde~ nd. Suah n~od~flaa~ion~ ~nd variation~ a~e
con~idered tc~ be ~i~hin the pur~iew ~nd ~ ope c-P 'che app~nded
clai~
-- ~6 --

Representative Drawing
A single figure which represents the drawing illustrating the invention.
Administrative Status

2024-08-01:As part of the Next Generation Patents (NGP) transition, the Canadian Patents Database (CPD) now contains a more detailed Event History, which replicates the Event Log of our new back-office solution.

Please note that "Inactive:" events refers to events no longer in use in our new back-office solution.

For a clearer understanding of the status of the application/patent presented on this page, the site Disclaimer , as well as the definitions for Patent , Event History , Maintenance Fee  and Payment History  should be consulted.

Event History

Description Date
Time Limit for Reversal Expired 1993-11-02
Application Not Reinstated by Deadline 1993-11-02
Deemed Abandoned - Failure to Respond to Maintenance Fee Notice 1993-05-03
Inactive: Adhoc Request Documented 1993-05-03
Application Published (Open to Public Inspection) 1991-11-03

Abandonment History

Abandonment Date Reason Reinstatement Date
1993-05-03
Owners on Record

Note: Records showing the ownership history in alphabetical order.

Current Owners on Record
MOBIL OIL CORPORATION
Past Owners on Record
PAUL SHU
WINSTON R. SHU
Past Owners that do not appear in the "Owners on Record" listing will appear in other documentation within the application.
Documents

To view selected files, please enter reCAPTCHA code :



To view images, click a link in the Document Description column. To download the documents, select one or more checkboxes in the first column and then click the "Download Selected in PDF format (Zip Archive)" or the "Download Selected as Single PDF" button.

List of published and non-published patent-specific documents on the CPD .

If you have any difficulty accessing content, you can call the Client Service Centre at 1-866-997-1936 or send them an e-mail at CIPO Client Service Centre.


Document
Description 
Date
(yyyy-mm-dd) 
Number of pages   Size of Image (KB) 
Abstract 1991-11-02 1 26
Claims 1991-11-02 4 174
Drawings 1991-11-02 2 37
Descriptions 1991-11-02 16 735
Representative drawing 1998-07-27 1 6