NO830032L - COMPOSITION AND PROCEDURE FOR CLEANING HYDROCARBON OIL FROM HARD SURFACES - Google Patents
COMPOSITION AND PROCEDURE FOR CLEANING HYDROCARBON OIL FROM HARD SURFACESInfo
- Publication number
- NO830032L NO830032L NO830032A NO830032A NO830032L NO 830032 L NO830032 L NO 830032L NO 830032 A NO830032 A NO 830032A NO 830032 A NO830032 A NO 830032A NO 830032 L NO830032 L NO 830032L
- Authority
- NO
- Norway
- Prior art keywords
- oil
- weight
- water
- carbon atoms
- concentrate
- Prior art date
Links
- 239000000203 mixture Substances 0.000 title claims description 17
- 238000000034 method Methods 0.000 title claims description 16
- 238000004140 cleaning Methods 0.000 title description 14
- 229930195733 hydrocarbon Natural products 0.000 title description 6
- 150000002430 hydrocarbons Chemical class 0.000 title description 6
- 239000004215 Carbon black (E152) Substances 0.000 title description 5
- 238000005520 cutting process Methods 0.000 claims description 36
- 238000005553 drilling Methods 0.000 claims description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 239000012141 concentrate Substances 0.000 claims description 16
- -1 phosphate ester Chemical class 0.000 claims description 11
- 125000004432 carbon atom Chemical group C* 0.000 claims description 9
- 239000004094 surface-active agent Substances 0.000 claims description 9
- 239000013535 sea water Substances 0.000 claims description 8
- 239000000243 solution Substances 0.000 claims description 7
- 239000002904 solvent Substances 0.000 claims description 7
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 5
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 4
- 150000001298 alcohols Chemical class 0.000 claims description 4
- 125000000217 alkyl group Chemical group 0.000 claims description 4
- 239000007864 aqueous solution Substances 0.000 claims description 4
- 229910019142 PO4 Inorganic materials 0.000 claims description 3
- 239000010452 phosphate Substances 0.000 claims description 3
- 150000001732 carboxylic acid derivatives Chemical class 0.000 claims description 2
- 239000003960 organic solvent Substances 0.000 claims description 2
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical group C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 claims 2
- 125000003342 alkenyl group Chemical group 0.000 claims 1
- 238000007865 diluting Methods 0.000 claims 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 claims 1
- 239000003921 oil Substances 0.000 description 49
- 239000000839 emulsion Substances 0.000 description 11
- 239000000463 material Substances 0.000 description 9
- 239000012530 fluid Substances 0.000 description 8
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 6
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 5
- 239000011435 rock Substances 0.000 description 5
- 239000008346 aqueous phase Substances 0.000 description 4
- 239000007788 liquid Substances 0.000 description 4
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 238000010998 test method Methods 0.000 description 3
- 239000012085 test solution Substances 0.000 description 3
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 2
- 235000013162 Cocos nucifera Nutrition 0.000 description 2
- 244000060011 Cocos nucifera Species 0.000 description 2
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 2
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 2
- 229910001209 Low-carbon steel Inorganic materials 0.000 description 2
- 239000013543 active substance Substances 0.000 description 2
- 239000010779 crude oil Substances 0.000 description 2
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 125000001301 ethoxy group Chemical group [H]C([H])([H])C([H])([H])O* 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000002736 nonionic surfactant Substances 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- 239000007762 w/o emulsion Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- 150000001342 alkaline earth metals Chemical class 0.000 description 1
- 125000003545 alkoxy group Chemical group 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000015556 catabolic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 239000012459 cleaning agent Substances 0.000 description 1
- 239000013527 degreasing agent Substances 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 239000003599 detergent Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 239000000975 dye Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003995 emulsifying agent Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 230000003165 hydrotropic effect Effects 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 239000002480 mineral oil Substances 0.000 description 1
- 239000002304 perfume Substances 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 description 1
- 150000003014 phosphoric acid esters Chemical class 0.000 description 1
- 238000000053 physical method Methods 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 239000003755 preservative agent Substances 0.000 description 1
- 150000003138 primary alcohols Chemical class 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 230000002787 reinforcement Effects 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 239000012747 synergistic agent Substances 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 125000004417 unsaturated alkyl group Chemical group 0.000 description 1
- GDJZZWYLFXAGFH-UHFFFAOYSA-M xylenesulfonate group Chemical group C1(C(C=CC=C1)C)(C)S(=O)(=O)[O-] GDJZZWYLFXAGFH-UHFFFAOYSA-M 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D1/00—Detergent compositions based essentially on surface-active compounds; Use of these compounds as a detergent
- C11D1/38—Cationic compounds
- C11D1/52—Carboxylic amides, alkylolamides or imides or their condensation products with alkylene oxides
- C11D1/526—Carboxylic amides (R1-CO-NR2R3), where R1, R2 or R3 are polyalkoxylated
-
- C—CHEMISTRY; METALLURGY
- C11—ANIMAL OR VEGETABLE OILS, FATS, FATTY SUBSTANCES OR WAXES; FATTY ACIDS THEREFROM; DETERGENTS; CANDLES
- C11D—DETERGENT COMPOSITIONS; USE OF SINGLE SUBSTANCES AS DETERGENTS; SOAP OR SOAP-MAKING; RESIN SOAPS; RECOVERY OF GLYCEROL
- C11D1/00—Detergent compositions based essentially on surface-active compounds; Use of these compounds as a detergent
- C11D1/38—Cationic compounds
- C11D1/52—Carboxylic amides, alkylolamides or imides or their condensation products with alkylene oxides
- C11D1/523—Carboxylic alkylolamides, or dialkylolamides, or hydroxycarboxylic amides (R1-CO-NR2R3), where R1, R2 or R3 contain one hydroxy group per alkyl group
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B21/00—Methods or apparatus for flushing boreholes, e.g. by use of exhaust air from motor
- E21B21/06—Arrangements for treating drilling fluids outside the borehole
- E21B21/068—Arrangements for treating drilling fluids outside the borehole using chemical treatment
-
- E—FIXED CONSTRUCTIONS
- E21—EARTH OR ROCK DRILLING; MINING
- E21B—EARTH OR ROCK DRILLING; OBTAINING OIL, GAS, WATER, SOLUBLE OR MELTABLE MATERIALS OR A SLURRY OF MINERALS FROM WELLS
- E21B41/00—Equipment or details not covered by groups E21B15/00 - E21B40/00
- E21B41/005—Waste disposal systems
Landscapes
- Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Geology (AREA)
- Mining & Mineral Resources (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Geochemistry & Mineralogy (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Fluid Mechanics (AREA)
- Physics & Mathematics (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Wood Science & Technology (AREA)
- Organic Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Mechanical Engineering (AREA)
- Detergent Compositions (AREA)
- Earth Drilling (AREA)
Description
Foreliggende oppfinnelse vedrører fremgangsmåter for rensing av olje/bergart-blandinger i oljeboreoperasjoner og spesielt rensing av boreolje fra borekutt på offshore-boreplattformer, fjerning av olje fra flaten i nyborede hull før forsterkning med foringsrør, og rensing av oljeslåm fra boreplattfomrer. The present invention relates to methods for cleaning oil/rock mixtures in oil drilling operations and in particular cleaning drilling oil from drill cuttings on offshore drilling platforms, removing oil from the surface in newly drilled holes before reinforcement with casing, and cleaning oil sludge from drilling plate casings.
Ved boring etter olje og gass er det av en rekke grunner nød-vendig å benytte en borefluid eller boreslam. Typene av borefluid eller -slam som vanligvis benyttes er: When drilling for oil and gas, it is necessary for a number of reasons to use a drilling fluid or drilling mud. The types of drilling fluid or mud that are usually used are:
a) vannbasert,a) water-based,
b) ' oljebasert,b) ' oil-based,
c ). vann-i-olje-emulsjonbasert (invert).c). water-in-oil emulsion-based (invert).
Oljebaserte boremedia (b) kan også inneholde vann i formOil-based drilling media (b) can also contain water in form
av vann-i-olje-emulsjon. Det er vanlig innen teknikken å referere til et'boremedium inneholdende opptil ca. 15% vandig fase, beregnet på volum, som oljebasert. De boremedia som betegnes som invefte fluider eller slam, (c) inneholder generelt mellom 15% og 55% vann. Foreliggende oppfinnelse angår spesielt typer (b og c) hvorav begge omfattes av beteg-nelsen "olje" slik den benyttes heri, sammen med råoljer og raffinerte mineraloljer. of water-in-oil emulsion. It is common in the art to refer to a drilling medium containing up to approx. 15% aqueous phase, calculated by volume, as oil-based. The drilling media referred to as interwoven fluids or mud, (c) generally contain between 15% and 55% water. The present invention relates in particular to types (b and c), both of which are covered by the term "oil" as used herein, together with crude oils and refined mineral oils.
En av funksjonene til borefluid er å . føre borekutt fra bor-kronen til overflaten, hvoretter kuttene fjernes ved hjelp av fysikalske teknikker, f.eks. ved bruk av sold, sikter, sykloner o sentrifuger. Etter fjerning av borekuttmaterialer blir borefluidet brukt på nytt og borekuttmater.ialene kasseres.. Dersom boringen foretas offshore så vil borekuttmaterialet uttømt i sjøen, hvor i tilfellet for vandige bore-fluider borekuttmaterialet dispergeres og sedimenteres uten 'å bevirke betydelige problemer. I tilfelle for oljebore-fluider er imidlertid borekuttmaterialet oljefuktet og sedimenterer hurtig til sjøbunnen under boreriggen og danner en oljeaktige, klebrig masse som kan forstyrre boreopera-sjonér, f.eks. ved å hindre bevegelse for dykkere som er involvert i arbeid med undervannskonstruksjoner og vedlike-hold.. Det antas at svellingen av leirematerialer i bore kutt er ansvarlig for dannelsen av denne massen. I tillegg forårsaker borekuttmaterialet oljeforurensning ved .gradvis frigjøring åv oljen. One of the functions of drilling fluid is to . bring drill cuttings from the drill bit to the surface, after which the cuttings are removed using physical techniques, e.g. using sieves, sieves, cyclones or centrifuges. After removal of the cuttings, the drilling fluid is reused and the cuttings are discarded. If the drilling is carried out offshore, the cuttings will be discharged into the sea, where in the case of aqueous drilling fluids the cuttings are dispersed and sedimented without causing significant problems. In the case of oil drilling fluids, however, the cuttings are oil-moistened and quickly settle to the seabed below the drilling rig, forming an oily, sticky mass that can interfere with drilling operations, e.g. by preventing the movement of divers involved in work with underwater structures and maintenance. It is believed that the swelling of clay materials in drill cuts is responsible for the formation of this mass. In addition, the drill cuttings cause oil pollution by gradually releasing the oil.
En teknikk for å fjerne olje fra borekutt er å vaske,borekuttmaterialet med et oppløsningsmiddel slik som diesel, dette har den virkning at det•fjerner mesteparten av oljen, men etterlater fremdeles overflaten forurenset med hydrokar-boner som gradvis kan frigjøres til omgivelsene. En annen måte er å benytte et vannblandbart oppløsningsmiddel slik som en glykoleter, men disse er kostbare. Nok en annen måte er å vaske borekuttmaterialet i sjøvann under anvendelse av god omrøring for å løsne oljen fra borekuttoverflaten. One technique for removing oil from drill cuttings is to wash the drill cuttings with a solvent such as diesel, this has the effect of removing most of the oil, but still leaves the surface contaminated with hydrocarbons which can gradually be released into the environment. Another way is to use a water-miscible solvent such as a glycol ether, but these are expensive. Yet another way is to wash the drill cutting material in seawater using good agitation to loosen the oil from the drill cutting surface.
Denne prosess kan benyttes enten som den eneste metode for fjerning av boreolje fra borekuttmaterialet, eller som et annet trinn for å fjerne et oljeoppløsningsmiddel fra borekutt som på forhånd er vasket med et hydrokarbon. Denne prosess kan forbedres ved tilsetning av et overflateaktivt middel til sjøvannet for a nedsette olje/vann-grenseflate-. spenningen. Borekuttmaterialet kan deretter tømmes i sjøen hvor det. dispegerer og sedimenterer over et stort sjøbunn-areal i stedet for å akkumuleres direkte i området for bore--operasjonene. 01je-i-vann-emulsjonene som dannes som et resultat av vasking av borekuttmaterialet kan tømmes i sjøen der fin dispergering av oljen vil lette dens nedbrytelse av mikroorganismer. This process can be used either as the only method for removing drilling oil from the cuttings, or as another step to remove an oil solvent from cuttings that have been previously washed with a hydrocarbon. This process can be improved by adding a surfactant to the seawater to reduce the oil/water interface. the tension. The drill cuttings can then be emptied into the sea where it disperses and sediments over a large seabed area instead of accumulating directly in the area of the drilling operations. The water-in-water emulsions formed as a result of washing the cuttings can be discharged into the sea where fine dispersion of the oil will facilitate its breakdown by microorganisms.
Et vanlig benyttet overflateaktivt middel for de ovenstående formål er Cg_-^-alkoholer med seks mol etoksygrupper. Et formål med foreliggende oppfinnelse er å tilveiebringe mer effektive metoder for rensing av olje fra borekutt av bergarter . A commonly used surface-active agent for the above purposes are C8--alcohols with six moles of ethoxy groups. One purpose of the present invention is to provide more efficient methods for cleaning oil from drill cuttings of rocks.
Et ytterligere formål med oppfinnelsen er å tilveiebringe■ A further object of the invention is to provide■
en fremgangsmåte hvorved olje kan separeres fra emulsjonen som resulterer fra rensing av borekuttmateriale. Man har oppdaget at en spesiell blanding av et etoksylert ikke-ionisk overflateaktivt middel med et alkanolamid utviser a process by which oil can be separated from the emulsion resulting from the cleaning of drill cuttings. It has been discovered that a particular mixture of an ethoxylated nonionic surfactant with an alkanolamide exhibits
en synergistisk effekt som tillater en mer effektiv rensing av olje fra borekutt. Ifølge en foretrukket utførelse, av oppfinnelsen har man ytterligere oppdaget at når emulsjonene av olje-i-vann dannet ved rensing ifølge oppfinnelsen opp-varmes, brytes emulsjonen lett og oljen kan deretter ut-vinnes. a synergistic effect that allows a more efficient cleaning of oil from drill cuttings. According to a preferred embodiment of the invention, it has further been discovered that when the emulsions of oil-in-water formed by purification according to the invention are heated, the emulsion is easily broken and the oil can then be extracted.
Foreliggende oppfinnelse tilveiebringer følgelig en fremgangsmåte for rensing som omfatter at en oljebelagt bergart brin-ges i kontakt med en vandig oppløsning inneholdende en effektiv mengde av en blanding av (A) 5-95 vekt-% av minst en alkoksylert alkohol, karboksylsyre, alkylfenol eller ikke-ionisk fosfatester, som i hvert tilfelle har minst en alkyl- . gruppe med 6-22 karbonatomer og 1-20 etylenoksygruppe, med The present invention accordingly provides a method for cleaning which comprises bringing an oil-coated rock into contact with an aqueous solution containing an effective amount of a mixture of (A) 5-95% by weight of at least one alkylated alcohol, carboxylic acid, alkylphenol or nonionic phosphate ester, which in each case has at least one alkyl- . group with 6-22 carbon atoms and 1-20 ethyleneoxy group, med
(B) 95-5 vekt-% av. minst et alkanolamid med formelen:(B) 95-5% by weight of. at least one alkanolamide of the formula:
hvor R er en mettet eller umettet alkylgruppe med 5-17 karbonatomer, og x og y er hver valgt fra 0 og hele tall fra, where R is a saturated or unsaturated alkyl group of 5-17 carbon atoms, and x and y are each selected from 0 and whole numbers from,
1 til 12, slik at x + y er fra 1 til 12.1 to 12, so x + y is from 1 to 12.
(A) er fortrinnsvis en primær'rettkjedet eller forgrenet alkohol med 6-18 karbonatomer og alkoksylert med 1-10 (A) is preferably a primary straight-chain or branched alcohol with 6-18 carbon atoms and alkylated with 1-10
etylenoksygrupper.ethyleneoxy groups.
(A) kan alternativt være normal eller forgrenet alkan- eller '• alkensyre med 7-23. karbonatomer, alkoksylert med 1-10 etylenoksygruppe; rettkjedet eller forgrenet alkylfenol med 6-12 alifatis.ke karbonatomer, alkoksylert med i-12 etylenoksy- (A) can alternatively be normal or branched alkano- or '• alkenoic acid with 7-23. carbon atoms, alkoxylated with 1-10 ethyleneoxy groups; straight-chain or branched alkylphenol with 6-12 aliphatic carbon atoms, alkoxylated with i-12 ethyleneoxy-
> >
grupper; ikke-ionisk fosforsyreester med minst en rettkjedet eller forgrenet alkylgruppe med 6-22 karbonatomer, minst en alkoksy- eller polyalkoksygruppe med 1-20 etylenoksy-enheter (B) har typisk 1-4 etylenoksygrupper. Mens man har oppdaget groups; non-ionic phosphoric acid ester with at least one straight-chain or branched alkyl group with 6-22 carbon atoms, at least one alkyloxy or polyalkyloxy group with 1-20 ethyleneoxy units (B) typically has 1-4 ethyleneoxy groups. While one has discovered
at monoetanolamider er særlig effektive synergistiske midler og. kan foretrekkes benyttet på steder med varmt klima, h.ar Konsentrert blanding av monoetanolamid med komponent (A) tendens til å være utilstrekkelig fluid ved lave temperaturer for hensiktsmessig håndtering under de betingelser man kan møte i f.eks. operasjoner i Nordsjøen. For slike lave temperaturer er det foretrukket å benytte dietanol^amider. that monoethanolamides are particularly effective synergistic agents and. can be preferably used in places with a warm climate, h.ar Concentrated mixture of monoethanolamide with component (A) tends to be insufficiently fluid at low temperatures for appropriate handling under the conditions that can be encountered in e.g. operations in the North Sea. For such low temperatures, it is preferred to use diethanolamides.
En blanding.av (A) og (B) tilføres typisk som et konsentrat som er oppløst, eller fortynnet med vann for tilveiebringelse av renseoppløsningen på stedet for boreplattformen. Slike konsentrater inneholder eventuelt et oppløsningsmiddel slik som vann eller en vannblandbar.alkohol, glykol eller, glykoleter, f.eks. isopropanol, etylenglykol, propylenglykol, polyetylenglykol, etter behov for tilveiebringelse av en flytende, hellbar sammensetning under de betingelser som man sannsynligvis vil møte. Konsentratet kan i tillegg inneholde mindre mengder hydrotropiske midler, slik som jord-alkalimetall-, natrium-, kalium-, mono-, di- eller tri-alkylbenzensulfonatsalter med.mindre enn .6 alifatiske karbonatomer, f.eks. toluen- eller xylensulfonater, fosfatester-salter, preservativer slik som formalin, fargestoffer og./ eller parfymer.- Vann kan være tilstede i en hvilken som helst hensiktsmessig mengde mellom null og rensemidlets sluttlige arbeidskonsentråsjon. Generelt, jo lavere andelen av vann er, jo større er hensiktsmessigheten for transport og lagring av konsentratet. Disse betraktninger må imidlertid balanseres mot preferansen for en stabil, hellbar sammensetning. Organiske oppløsn.ingsmidler kan merkbart forøke prisen på sammensetningen og benyttes derfor fortrinnsvis med måte, f.eks. mindre enn 50 vekt-% og fortrinnsvis mindre enn 20 vekt-% av konsentratet. A mixture of (A) and (B) is typically supplied as a concentrate which is dissolved or diluted with water to provide the cleaning solution at the site of the drilling platform. Such concentrates optionally contain a solvent such as water or a water-miscible alcohol, glycol or glycol ether, e.g. isopropanol, ethylene glycol, propylene glycol, polyethylene glycol, as needed to provide a liquid, pourable composition under the conditions likely to be encountered. The concentrate may also contain smaller amounts of hydrotropic agents, such as alkaline earth metal, sodium, potassium, mono-, di- or tri-alkylbenzene sulphonate salts with less than 6 aliphatic carbon atoms, e.g. toluene or xylene sulfonates, phosphate ester salts, preservatives such as formalin, dyes and/or perfumes.- Water may be present in any suitable amount between zero and the final working concentration of the cleaning agent. In general, the lower the proportion of water, the greater the suitability for transport and storage of the concentrate. However, these considerations must be balanced against the preference for a stable, pourable composition. Organic solvents can noticeably increase the price of the composition and are therefore preferably used sparingly, e.g. less than 50% by weight and preferably less than 20% by weight of the concentrate.
Konsentratet kan typisk inneholde 5-95 vekt-% av (A) ogThe concentrate can typically contain 5-95% by weight of (A) and
95-5 vekt-% av (B). (A) er imidlertid fortrinnsvis tilstede- i konsentrasjoner over 10 vekt-%, helst over 20% og 95-5% by weight of (B). (A) is, however, preferably present - in concentrations above 10% by weight, preferably above 20% and
vanligvis over 30%. (B) er fortrinnsvis også tilstede i konsentrasjoner over 10 vekt-%, helst over 20% og vanligvj s over 30%. En egnet blanding inneholder 40-60% av (A), usually over 30%. (B) is preferably also present in concentrations above 10% by weight, preferably above 20% and usually above 30%. A suitable mixture contains 40-60% of (A),
60-40% av-(B) og 0-20% oppløsningsmiddel.60-40% of-(B) and 0-20% solvent.
Konsentratet oppløses eller dispergeres i vann ved anvendelses-stedet. For offshore-anvendelser kan konsentratet hensiktsmessig oppløses -eller dispergeres i sjøvann. Konsentratet blir typisk fortynnet til fra 0,5 til 10% aktivt stoff, beregnet på vekt, fortrinnsvis fra 1-6. Høyere konsentrasjoner utelukkes ikke>men det er usannsynlig at de viser seg å være priseffektive. Konsentrasjoner under 0,5% utelukkes ikke, men er bare marginalt effektive. The concentrate is dissolved or dispersed in water at the point of use. For offshore applications, the concentrate can be suitably dissolved - or dispersed - in seawater. The concentrate is typically diluted to from 0.5 to 10% active substance, calculated by weight, preferably from 1-6. Higher concentrations are not ruled out>but are unlikely to prove cost effective. Concentrations below 0.5% are not excluded, but are only marginally effective.
Benyttet for rensing av borekutt av bergarter, blir disse borekutt fortrinnsvis omrørt med oppløsningen av konsentratet i vann eller saltoppløsning i et tilstrekkelig tidsrom til å emulgere en vesentlig andel av oljen. Emulsjonen kan der-, etter separeres fra borekuttmaterialet som, nar det er tilstrekkelig rent, dumpes. Emulsjonen kan kasseres. Ifølge en foretrukken utførelse av foreliggende oppfinnelse blir imidlertid oljen-, utvunnet fra emulsjonen ved moderat oppvarming. Typiske temperaturer i overkant av 40°C, f.eks. 50-70°C er tilstrekkelig til å bryte emulsjonen og tillate utvinning av den separerte oljefasen. Used for cleaning drill cuttings from rocks, these drill cuttings are preferably stirred with the solution of the concentrate in water or salt solution for a sufficient period of time to emulsify a significant proportion of the oil. The emulsion can then be separated from the drill cutting material which, when it is sufficiently clean, is dumped. The emulsion can be discarded. According to a preferred embodiment of the present invention, however, the oil is extracted from the emulsion by moderate heating. Typical temperatures in excess of 40°C, e.g. 50-70°C is sufficient to break the emulsion and allow recovery of the separated oil phase.
Renseoppløsningen ifølge foreliggende oppfinnelse kan også injiseres i borehull for å rense olje fra sidene til berg-artmaterialet. Dette er nødvendig når et foringsrør skal bindes med sement til borehullets sider. Oppløsningen kan også anvendes ifølge oppfinnelsen for å rense oljeslam fra selve boreplattformene og generelt for å. fjerne viskøse 'hydrokarbonol j er fra harde overflater. The cleaning solution according to the present invention can also be injected into boreholes to clean oil from the sides of the rock material. This is necessary when a casing is to be cemented to the sides of the borehole. The solution can also be used according to the invention to clean oil sludge from the drilling platforms themselves and generally to remove viscous hydrocarbon oils from hard surfaces.
Oppløsningen skal illustreres ved følgende eksempler: The resolution shall be illustrated by the following examples:
Produktene ble testet som. følger:The products were tested as following:
Testmetode for vasking av borekuttTest method for washing drill cuttings
a) 43 g oljeslam-borekutt oppnådd fra en boreoperasjon i Nordsjøen ble tilsatt til 150 g overf lateakt.iv oppløs-ning med X% aktivt stoff i syntetisk sjøvann. b) Dette ble omrørt i 5 minutter under anvendelse av et Janke4Kunkel-røreverk ved innstilling 2 ved 800 omdr./min. c) Blandingen ble hensatt i 5 minutter hvoretter væsken bre dekaritert. Denne væske inneholdt den emulgerte oljen a) 43 g of oil mud drill cuttings obtained from a drilling operation in the North Sea were added to 150 g of surfactant solution with X% active substance in synthetic seawater. b) This was stirred for 5 minutes using a Janke4Kunkel stirrer at setting 2 at 800 rpm. c) The mixture was left for 5 minutes after which the liquid was decaritated. This liquid contained the emulsified oil
som kunne separeres ved oppvarming til over 40°C.which could be separated by heating above 40°C.
d) Blandingen ble deretter supplert til 150 ml med standard sjøvann og omrørt i ytterligere 1 minutt som ib). e) Blandingen ble deretter filtrert gjennom to lag musselin. f) 20 g vaskede borekutt ble veiet nøyaktig (Wl) i en' 250 ml rundbunnet kolbe og vanninnholdet ble bestemt ifølge Dean-og Stark-metoden under anvendelse av 100-120 petroleum-eter. Vekten av fjernet vann-ble bestemt som-W2. g) Ytterligere 10 g av.det vaskede borekuttmaterialet ble veiet nøyaktig (W3) i en fordampningsskål og tørket til■ d) The mixture was then made up to 150 ml with standard seawater and stirred for a further 1 minute as ib). e) The mixture was then filtered through two layers of muslin. f) 20 g of washed drill cuttings were weighed accurately (Wl) into a 250 ml round bottom flask and the water content was determined according to the Dean and Stark method using 100-120 petroleum ether. The weight of water removed was determined as W2. g) A further 10 g of the washed drill cutting material was accurately weighed (W3) into an evaporating dish and dried to
konstant vekt (W4) ved 110°C.constant weight (W4) at 110°C.
Vekten av olje på borekuttmaterialet, ,\ The weight of oil on the cutting material, ,\
Vekten av olje som.var tilbake på borekuttmaterialer uttrykt som en vékt-%-andel av tørre borekutt + vekt av olje The weight of oil that remained on cuttings materials expressed as a weight % share of dry cuttings + weight of oil
Testen ble foretatt to ganger. Det skal påpekes at man har funnet at mengden av olje fjernet fra overflaten av bore-kuttematerialet ved hejlp av et hvilket som helst gitt overflateaktivt middel eller blanding av overflateaktive midler ér avhengig av alderen på borekuttmaterialet,. idet mer olje. The test was carried out twice. It should be pointed out that it has been found that the amount of oil removed from the surface of the drill cutting material by any given surfactant or mixture of surfactants is dependent on the age of the drill cutting material. taking more oil.
blir fjernet fra friske borekutt enn fra gamle, borekutt. is removed from fresh drill cuts than from old drill cuts.
Eksempel 1Example 1
Under anvendelse av den ovenfor angitte testmetoden ble følgende resultater oppnådd ved å benytte oljeslam-borekutt fra Nordsjøen. Using the test method stated above, the following results were obtained by using oil mud drill cuttings from the North Sea.
Eksempel 4 Example 4
I tillegg ble emulsjonen som ble dekantert i trinn c) og oppnådd under''anvendelse av A (1,5%) = B (3,75%) oppvarmet til 40°G og separert til atskilte olje- og vandige faser. In addition, the emulsion decanted in step c) and obtained using A (1.5%) = B (3.75%) was heated to 40°C and separated into separate oil and aqueous phases.
Eksempel 5Example 5
Eksempel 6 Example 6
Emulsjonen dekantert i trinn c) og oppnådd under anvendelse av A (3,75%) + B (1,25%) ble oppvarmet til 40°C og separert i atskilte olje- og vandige faser. The emulsion decanted in step c) and obtained using A (3.75%) + B (1.25%) was heated to 40°C and separated into separate oil and aqueous phases.
Eksempel 7Example 7
Et konsentrat ble fremstilt for bruk ifølge oppfinnelsen bestående av 4 5 vekt-% CIO C12 fettalkohol 5 mol etoksylat, A concentrate was prepared for use according to the invention consisting of 45% by weight CIO C12 fatty alcohol 5 mol ethoxylate,
45 vekt-% kokosdietanolamid, 5 vekt-% propylenglykol, 5 vekt-% vann. Produktet var flytende og stabilt ved temperaturer mellom -5°C og 35°C og dispergerte lett i sjøvann. Ved bedømmelse i den ovenfor angitte rensetest for borekutt ble følgende resultater oppnådd: 45% by weight coconut diethanolamide, 5% by weight propylene glycol, 5% by weight water. The product was liquid and stable at temperatures between -5°C and 35°C and dispersed easily in seawater. When judged in the cleaning test for drill cuts stated above, the following results were obtained:
A = C9/C1<1>''primær alkohol med nominelt 6 mol etoksygrupper. Dette er det overflateaktive middel som er mest vanlig benyttet for rensing av oljeslam-borekutt. A = C9/C1<1>''primary alcohol with nominally 6 mol ethoxy groups. This is the surfactant that is most commonly used for cleaning oil mud drill cuttings.
Emulsjonen dekantert i trinn c) i fremgangsmåten og oppnådd under anvendelse av formuleringen i eksempel 7, ble oppvarmet til 50°C og separert i atskilte olje- og vandige faser. The emulsion decanted in step c) of the process and obtained using the formulation in Example 7 was heated to 50°C and separated into separate oil and aqueous phases.
Eksempel 8Example 8
Følgende' test ble benyttet for å vise effektiviteten til blandingen av ikke-ioniske overflateaktive midler av'typer A og B som definert ovenfor, for fjerning av olje fra metalloverflater. a) En plate av .bløtt stål ble vasket grundig med en hushold-ningsvaskemiddeloppløsning fulgt av skylling med lednings-vann og deretter med aceton. b) En overflate av platen ble belagt jevnt med 0,4 g hydro-karbonolje, f.eks. råolje. c) 0,6 g testoppløsning ble deretter blandet intimt med over-flateoljen og platen ble hensatt horisontalt med den be-lagte flate øverst i 15 minutter.. d) Overflaten ble deretter vasket méd 200 ml syntetisk sjø-vann fra en laboratorie-vaskeflaske. e) Mengden av olje som var tilbake på platen ble bestemt visuelt. The following test was used to demonstrate the effectiveness of the mixture of non-ionic surfactants of types A and B as defined above, for the removal of oil from metal surfaces. a) A mild steel plate was washed thoroughly with a household detergent solution followed by rinsing with tap water and then with acetone. b) One surface of the plate was coated evenly with 0.4 g of hydrocarbon oil, e.g. crude oil. c) 0.6 g of test solution was then mixed intimately with the surface oil and the plate was placed horizontally with the coated surface at the top for 15 minutes.. d) The surface was then washed with 200 ml of synthetic seawater from a laboratory wash bottle . e) The amount of oil remaining on the plate was determined visually.
I denne test inneholdt den benyttede testoppløsning 7,5% av et CIO C12 fettalkohol 5 mol etoksylat, 7,5% kokosdietanolamid og 85% vann. Oljen ble vesentlig fjernet fra overflaten av det bløte stål og etterlot en ren ikke-oljeholdig over- In this test, the test solution used contained 7.5% of a CIO C12 fatty alcohol 5 mol ethoxylate, 7.5% coconut diethanolamide and 85% water. The oil was substantially removed from the surface of the mild steel, leaving a clean non-oily surface
.flate..fleet.
I en annen test var testoppløsningen et kommersielt hydro-karbonoppløsningsmiddelbasert avféttingsmiddel som var an-tatt å inneholde emulgeringsmidler. Det bløte stål ble mindre, grundig renset og overflaten var oljeholdig. In another test, the test solution was a commercial hydrocarbon solvent-based degreaser that was assumed to contain emulsifiers. The soft steel was smaller, thoroughly cleaned and the surface was oily.
Eksempel 9Example 9
Testmetoden beskrevet ovenfor (eksempler 1-7) ble benyttet, men konsentrasjonen for det overflateaktive middel (X%) ble endret.. The test method described above (Examples 1-7) was used, but the concentration of the surfactant (X%) was changed.
Dette er det overflateaktive middel som ér.mest vanlig benyttet for rensing av oljeslam-borekutt og var klart mindre effektivt over det studerte brede konsentrasjonsområdet. Alkylfordeling for alkoholer. benyttet i eksemplene De følgende er typiske fordelinger. This is the surfactant most commonly used for cleaning oil mud drill cuttings and was clearly less effective over the wide concentration range studied. Alkyl distribution for alcohols. used in the examples The following are typical distributions.
Claims (9)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| GB8200376 | 1982-01-07 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| NO830032L true NO830032L (en) | 1983-07-08 |
Family
ID=10527518
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| NO830032A NO830032L (en) | 1982-01-07 | 1983-01-06 | COMPOSITION AND PROCEDURE FOR CLEANING HYDROCARBON OIL FROM HARD SURFACES |
Country Status (11)
| Country | Link |
|---|---|
| EP (1) | EP0084411B1 (en) |
| CA (1) | CA1203450A (en) |
| DE (1) | DE3360678D1 (en) |
| DK (1) | DK3483A (en) |
| ES (1) | ES518812A0 (en) |
| GB (1) | GB2116579B (en) |
| GR (1) | GR77136B (en) |
| IE (1) | IE53660B1 (en) |
| IN (1) | IN158886B (en) |
| NO (1) | NO830032L (en) |
| PH (1) | PH19657A (en) |
Families Citing this family (13)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2480613A (en) * | 1944-11-09 | 1949-08-30 | Vernon O Sipe | Building wall of angular tile |
| EP0103779A3 (en) * | 1982-09-20 | 1985-01-09 | John E. Oliver | Removing contaminates from a well fluid and well system |
| DE4023334A1 (en) * | 1990-07-23 | 1992-01-30 | Henkel Kgaa | LIQUID, POURABLE AND PUMPABLE SURFACTANT CONCENTRATE |
| SE468855B (en) * | 1990-08-09 | 1993-03-29 | Eriksson Tord Utveckling | PROCEDURES FOR CLEANING AND DEATH, COMPOSITION INTENDED AS PRIOR MIXTURE AND WATER AND ELECTROLYTHEATIC MICROEMULSION |
| SE500534C2 (en) * | 1990-11-12 | 1994-07-11 | Eriksson Tord Utveckling | Procedure for cleaning and degreasing |
| FR2689138B1 (en) * | 1992-03-26 | 1994-05-20 | Institut Francais Petrole | METHOD FOR WASHING SOLID PARTICLES COMPRISING A SOPHOROSIDE SOLUTION. |
| US5501816A (en) * | 1994-07-12 | 1996-03-26 | Basf Corporation | Aqueous based solvent free degreaser composition |
| GB9623823D0 (en) * | 1996-11-16 | 1997-01-08 | Reckitt & Colmann Prod Ltd | Improvements in or relating to organic compositions |
| US7951755B2 (en) | 2002-12-02 | 2011-05-31 | An-Ming Wu | Emulsified polymer drilling fluid and methods of preparation |
| US20040116304A1 (en) * | 2002-12-02 | 2004-06-17 | An-Ming Wu | Emulsified polymer drilling fluid and methods of preparation and use thereof |
| US6846420B2 (en) | 2002-12-19 | 2005-01-25 | Halliburton Energy Services, Inc. | Process for removing oil from solid materials recovered from a well bore |
| WO2006010375A1 (en) * | 2004-07-27 | 2006-02-02 | Rhodia Chimie | Formulation for degreasing metal comprising a demulsifyiing agent, use of the agent, and process for degreasing metal. |
| US7192527B2 (en) | 2004-08-10 | 2007-03-20 | Halliburton Energy Services, Inc. | Processes for removing oil from solid wellbore materials and produced water |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AT179693B (en) * | 1951-04-02 | 1954-09-25 | Metallgesellschaft Ag | Acid emulsion cleaners for pickling and degreasing metals |
| NL168553C (en) * | 1951-04-02 | Takeda Chemical Industries Ltd | PROCESS FOR THE MICROBIOLOGICAL PREPARATION OF CITRIC ACID. | |
| US2831814A (en) * | 1951-12-19 | 1958-04-22 | Poor & Co | Acid pickling of metals and compositions therefor |
| GB1213792A (en) * | 1966-11-30 | 1970-11-25 | Diversey Ltd | Inhibition of corrosion of metallic surfaces |
| SE400575B (en) * | 1974-12-13 | 1978-04-03 | Nordnero Ab | BATH FOR CELLING OF COPPER AND ITS ALLOYS |
| US4280915A (en) * | 1977-06-23 | 1981-07-28 | Nl Industries, Inc. | Salt stable lubricant for water base drilling fluids |
| DE2918364A1 (en) * | 1979-05-07 | 1980-11-20 | Henkel Kgaa | DETERGENT FOR TEXTILES |
| US4268406A (en) * | 1980-02-19 | 1981-05-19 | The Procter & Gamble Company | Liquid detergent composition |
-
1982
- 1982-12-23 GB GB08236665A patent/GB2116579B/en not_active Expired
- 1982-12-31 IN IN948/DEL/82A patent/IN158886B/en unknown
-
1983
- 1983-01-04 GR GR70199A patent/GR77136B/el unknown
- 1983-01-05 PH PH28349A patent/PH19657A/en unknown
- 1983-01-05 ES ES518812A patent/ES518812A0/en active Granted
- 1983-01-06 DK DK3483A patent/DK3483A/en not_active Application Discontinuation
- 1983-01-06 NO NO830032A patent/NO830032L/en unknown
- 1983-01-06 IE IE26/83A patent/IE53660B1/en unknown
- 1983-01-06 DE DE8383300048T patent/DE3360678D1/en not_active Expired
- 1983-01-06 EP EP83300048A patent/EP0084411B1/en not_active Expired
- 1983-01-07 CA CA000419049A patent/CA1203450A/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| PH19657A (en) | 1986-06-09 |
| GB2116579B (en) | 1985-08-29 |
| IE53660B1 (en) | 1989-01-04 |
| DK3483D0 (en) | 1983-01-06 |
| EP0084411A1 (en) | 1983-07-27 |
| GR77136B (en) | 1984-09-07 |
| GB2116579A (en) | 1983-09-28 |
| IE830026L (en) | 1983-07-07 |
| IN158886B (en) | 1987-02-07 |
| ES8405878A1 (en) | 1984-06-16 |
| DK3483A (en) | 1983-07-08 |
| ES518812A0 (en) | 1984-06-16 |
| DE3360678D1 (en) | 1985-10-10 |
| CA1203450A (en) | 1986-04-22 |
| EP0084411B1 (en) | 1985-09-04 |
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