NO162913B - APPLICATION OF ORGANOSILICIUM-MODIFIED POLYDIANS AS DEMULGATORS FOR OIL OIL / WATER EMULSIONS. - Google Patents
APPLICATION OF ORGANOSILICIUM-MODIFIED POLYDIANS AS DEMULGATORS FOR OIL OIL / WATER EMULSIONS. Download PDFInfo
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- NO162913B NO162913B NO831471A NO831471A NO162913B NO 162913 B NO162913 B NO 162913B NO 831471 A NO831471 A NO 831471A NO 831471 A NO831471 A NO 831471A NO 162913 B NO162913 B NO 162913B
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- 239000000839 emulsion Substances 0.000 title claims abstract description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 18
- 125000004432 carbon atom Chemical group C* 0.000 claims abstract description 14
- 125000000217 alkyl group Chemical group 0.000 claims abstract description 10
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims abstract description 6
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 5
- 239000001257 hydrogen Substances 0.000 claims abstract description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical group [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 4
- 125000002947 alkylene group Chemical group 0.000 claims description 5
- 239000002689 soil Substances 0.000 claims description 2
- 239000003208 petroleum Substances 0.000 abstract description 16
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 21
- 150000001875 compounds Chemical class 0.000 description 18
- 239000003921 oil Substances 0.000 description 11
- 239000000047 product Substances 0.000 description 10
- -1 amine salts Chemical class 0.000 description 9
- 239000000203 mixture Substances 0.000 description 8
- 229920000570 polyether Polymers 0.000 description 8
- 239000010779 crude oil Substances 0.000 description 7
- 229920000642 polymer Polymers 0.000 description 6
- 239000002253 acid Substances 0.000 description 5
- 238000007792 addition Methods 0.000 description 5
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 4
- 239000004721 Polyphenylene oxide Substances 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 4
- 239000007795 chemical reaction product Substances 0.000 description 4
- 150000002367 halogens Chemical class 0.000 description 4
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 4
- 238000000926 separation method Methods 0.000 description 4
- 150000004756 silanes Chemical class 0.000 description 4
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 3
- 125000005037 alkyl phenyl group Chemical group 0.000 description 3
- 150000001735 carboxylic acids Chemical class 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000004821 distillation Methods 0.000 description 3
- 229910052736 halogen Inorganic materials 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 229920001296 polysiloxane Polymers 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- IAYPIBMASNFSPL-UHFFFAOYSA-N Ethylene oxide Chemical compound C1CO1 IAYPIBMASNFSPL-UHFFFAOYSA-N 0.000 description 2
- 229920003171 Poly (ethylene oxide) Polymers 0.000 description 2
- BLRPTPMANUNPDV-UHFFFAOYSA-N Silane Chemical group [SiH4] BLRPTPMANUNPDV-UHFFFAOYSA-N 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical group [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 2
- GSMXFJOGPOXVHH-UHFFFAOYSA-L [Cl-].[Cl-].[Pt+2].C=C.C1=CC=NC=C1 Chemical compound [Cl-].[Cl-].[Pt+2].C=C.C1=CC=NC=C1 GSMXFJOGPOXVHH-UHFFFAOYSA-L 0.000 description 2
- 125000004423 acyloxy group Chemical group 0.000 description 2
- 150000001298 alcohols Chemical class 0.000 description 2
- 125000003545 alkoxy group Chemical group 0.000 description 2
- 229910021529 ammonia Inorganic materials 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 125000000484 butyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 description 2
- 238000005119 centrifugation Methods 0.000 description 2
- 230000008021 deposition Effects 0.000 description 2
- 238000000151 deposition Methods 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 238000005187 foaming Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 125000005702 oxyalkylene group Chemical group 0.000 description 2
- 125000006353 oxyethylene group Chemical group 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 229920001451 polypropylene glycol Polymers 0.000 description 2
- 229920005989 resin Polymers 0.000 description 2
- 239000011347 resin Substances 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 229910000077 silane Inorganic materials 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 229920005830 Polyurethane Foam Polymers 0.000 description 1
- GOOHAUXETOMSMM-UHFFFAOYSA-N Propylene oxide Chemical compound CC1CO1 GOOHAUXETOMSMM-UHFFFAOYSA-N 0.000 description 1
- 229910007161 Si(CH3)3 Inorganic materials 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 150000008055 alkyl aryl sulfonates Chemical class 0.000 description 1
- 150000008051 alkyl sulfates Chemical class 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229920001400 block copolymer Polymers 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 239000004359 castor oil Substances 0.000 description 1
- 235000019438 castor oil Nutrition 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 150000004292 cyclic ethers Chemical class 0.000 description 1
- 150000001991 dicarboxylic acids Chemical class 0.000 description 1
- 230000037213 diet Effects 0.000 description 1
- 235000005911 diet Nutrition 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 1
- 125000005442 diisocyanate group Chemical group 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 125000001301 ethoxy group Chemical group [H]C([H])([H])C([H])([H])O* 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 150000002191 fatty alcohols Chemical class 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 125000002485 formyl group Chemical class [H]C(*)=O 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- ZEMPKEQAKRGZGQ-XOQCFJPHSA-N glycerol triricinoleate Natural products CCCCCC[C@@H](O)CC=CCCCCCCCC(=O)OC[C@@H](COC(=O)CCCCCCCC=CC[C@@H](O)CCCCCC)OC(=O)CCCCCCCC=CC[C@H](O)CCCCCC ZEMPKEQAKRGZGQ-XOQCFJPHSA-N 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
- 239000012442 inert solvent Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 125000000956 methoxy group Chemical group [H]C([H])([H])O* 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 239000011496 polyurethane foam Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 150000003138 primary alcohols Chemical class 0.000 description 1
- 239000003380 propellant Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 239000011541 reaction mixture Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 150000003871 sulfonates Chemical class 0.000 description 1
- 239000004753 textile Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G33/00—Dewatering or demulsification of hydrocarbon oils
- C10G33/04—Dewatering or demulsification of hydrocarbon oils with chemical means
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D17/00—Separation of liquids, not provided for elsewhere, e.g. by thermal diffusion
- B01D17/02—Separation of non-miscible liquids
- B01D17/04—Breaking emulsions
- B01D17/047—Breaking emulsions with separation aids
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Emulsifying, Dispersing, Foam-Producing Or Wetting Agents (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Colloid Chemistry (AREA)
Abstract
Anvendelse av organosiliciummodifiserte polydiener med den generelle formel. hvori Z betyr kjedebegrensende grupper,. R1 i molekylet er lik eller forskjellig og betyr hydrogen eller metylrest,. R 2 i molekylet er lik eller forskjellig og betyr en eventuelt fluorert alkyl-, eller alkylarylrest med 6 til 24 karbonatomer,. R^ i molekylet er lik eller forskjellig og betyr resten (R 4 0-)mY, idet R 4 betyr alkylenrester med 2 til 4 karbonatomer, m = 2 og Y betyr en alkylrest med 1 til karbonatomer, og. idet gjennomsnittlig. w 0,. x = 0,. y i,. a = 0 til 2,. b = 0 eller 1. 0 < c < 3, idet 0 < a + c < 3,. som dismulgatorer for jordolje/vannæemulsjoner.Use of organosilicon modified polydienes of the general formula. wherein Z represents chain limiting groups,. R1 in the molecule is the same or different and means hydrogen or methyl residue ,. R 2 in the molecule is the same or different and represents an optionally fluorinated alkyl or alkylaryl radical having 6 to 24 carbon atoms. R 2 in the molecule is the same or different and represents the residue (R 40 -) m Y, where R 4 represents alkylene radicals having 2 to 4 carbon atoms, m = 2 and Y represents an alkyl radical having 1 to carbon atoms, and. as average. w 0 ,. x = 0 ,. y i ,. a = 0 to 2,. b = 0 or 1. 0 <c <3, where 0 <a + c <3 ,. as dismulgators for petroleum / water emulsions.
Description
Foreliggende oppfinnelse vedrører anvendelse av organosilisiummodifiserte polydiener som demulgatorer for jordolje/- vannemuls j oner. The present invention relates to the use of organosilicon-modified polydienes as demulsifiers for petroleum/water emulsions.
En stor del av råjordoljen inneholder ved transport mindre eller større mengder saltvann i emulgert form. Slike emulsjoner som overveiende opptrer som vann/oljeemulsjoner må oppdeles i sine faser, da det i emulsjonen inneholdte saltvann ville virke forstyrrende ved en videre forarbeidelse av jordoljen, spesielt ved transport og ved destillering. During transport, a large part of the crude oil contains smaller or larger amounts of salt water in emulsified form. Such emulsions which predominantly act as water/oil emulsions must be divided into their phases, as the salt water contained in the emulsion would interfere with further processing of the crude oil, especially during transport and during distillation.
Adskillelsen av slike jordoljeemulsjoner lykkes enten ved avsetning, varmebehandling, sentrifugering, ved påtrykking av elektriske felt eller ved tilsetning av demulgatorer, respektiv kombinasjonen av flere metoder. The separation of such petroleum emulsions is successful either by deposition, heat treatment, centrifugation, by the application of electric fields or by the addition of demulsifiers, respectively the combination of several methods.
De transporterte råjordoljeemulsjoner er for det meste for stabile til at de kan brytes alene eller ved sedimentering, filtrering, sentrifugering eller oppvarming. Derimot bevirker demulgatorer allerede i små konsentrasjoner en adskillelse av emulsjonen. The transported crude oil emulsions are mostly too stable to be broken alone or by sedimentation, filtration, centrifugation or heating. In contrast, demulsifiers already cause a separation of the emulsion in small concentrations.
Demulgatorer er allerede foreslått i stort antall. Dette skyldes hovedsaklig at de forskjellige jordoljer har forskjellige sammensetninger, og demulgatorer som er egnet til å bryte emulsjoner og jordoljer fra et opprinnelsessted er uegnet ved jordoljeemulsjoner fra andre forekomster. De kjente dispergatorer virker derfor mer eller mindre utpreget spesifikt på de enkelte jordoljer. Demulsifiers have already been proposed in large numbers. This is mainly because the different petroleum oils have different compositions, and demulsifiers that are suitable for breaking emulsions and petroleum oils from one place of origin are unsuitable for petroleum emulsions from other deposits. The known dispersants therefore act more or less distinctly specifically on the individual petroleum oils.
Som demulgatorer har man allerede foreslått alkylsulfater og alkylarylsulfonater samt petroleumsulfonater i form av aminsalter. Videre er det nevnt tilleiringsprodukter av etylenoksyd til egnede forbindelser med aktivt hydrogenatom som f.eks. alkylfenoler, ricinusolje, fettsyre, fettalkohol, alkylfenol og aldehydharpikser. Tilsvarende angivelser finnes f.eks. i boken "Oberflachenaktive Anlagerungsprodukte des Ethylenoxids" av N. Schonfeld, Wissenschaftiiche Verlagsgesellschaft mbH. , Stuttgart, 1959, side 295. Alkyl sulfates and alkyl aryl sulfonates as well as petroleum sulfonates in the form of amine salts have already been proposed as demulsifiers. Furthermore, addition products of ethylene oxide to suitable compounds with an active hydrogen atom such as e.g. alkylphenols, castor oil, fatty acid, fatty alcohol, alkylphenol and aldehyde resins. Corresponding information can be found, e.g. in the book "Oberflachenaktive Anlagerungsprodukte des Ethylenoxids" by N. Schonfeld, Wissenschaftiiche Verlagsgesellschaft mbH. , Stuttgart, 1959, page 295.
I DE-PS 10 37 130 omtales at bestemte kjente polyoksyalkylen-polyslloksan-blokkblandingspolymerisater har fremragende egenskaper som demulgatorer for jordoljeemulsjoner av typen vann/olje av forskjellig opprinnelse<1> og dessuten virker demulgerende i meget små mengder, dvs. mindre mengder enn produktene i henhold til teknikkens stand. Polyoksyalkylen-polysiloksan-blokkblandingspolymerisatene har polyoksy-alkylen-blokker av en molvekt på 500 til 4000, som består av polyoksyetylen-, polyoksypropylenblokker i vektforhold på 40:60 til 100:0. Polysiloksanblokkene har 5 til 50 sllisium-atomer pr. blokk. In DE-PS 10 37 130 it is mentioned that certain known polyoxyalkylene-polysloxane block mixture polymers have outstanding properties as demulsifiers for petroleum emulsions of the water/oil type of different origins<1> and also act as demulsifiers in very small quantities, i.e. smaller quantities than the products in according to the state of the art. The polyoxyalkylene-polysiloxane block blend polymers have polyoxyalkylene blocks of a molecular weight of 500 to 4000, consisting of polyoxyethylene, polyoxypropylene blocks in weight ratios of 40:60 to 100:0. The polysiloxane blocks have 5 to 50 silicon atoms per block.
i in
i in
Gjenstand for DE-PS 22 50 920 er blandinger av 0,2 til 30 vekt-# av ovennevnte polyoksyalkylen-polysiloksan-blokk-blandingspolymerisater med 70 til 99^8 vekt-$ silisiumfrie demulgatorer, som består av alkylenoksyd-tilleiringsprodukter til organiske forbindelser inneholdende reaksjonsdyktige Subject matter of DE-PS 22 50 920 are mixtures of 0.2 to 30% by weight of the above-mentioned polyoxyalkylene-polysiloxane block blend polymers with 70 to 99^8% by weight of silicon-free demulsifiers, which consist of alkylene oxide addition products to organic compounds containing reactive
-Ia - -Ia-
omsetningsproduktei- av alkylenoksyder med alkylfenolaldehyd-harpikser, blokk- og blandingspolymerisater av propylenoksyd og etylenoksyd, deres omsetningsprodukter med dikarboksyl-syrer eller diisocyanater samt blandinger av disse produkter. Derved ble det fastslått at blandingene ifølge tysk patent reaction products of alkylene oxides with alkylphenolaldehyde resins, block and mixed polymers of propylene oxide and ethylene oxide, their reaction products with dicarboxylic acids or diisocyanates as well as mixtures of these products. Thereby it was determined that the mixtures according to German patent
22 50 920 har spesielt gunstige egenskaper med hensyn til demulgering og samtidig skumhindring. i 22 50 920 has particularly favorable properties with regard to demulsification and at the same time preventing foaming. in
Fra DE-PS 23 21 557 er det kjent .silisiumholdige blokk-kopolymerisater på basis av organosilisiummodifiserte polydiener. Disse forbindelser fåes; ved at man til polydiener adderer hydrogenrestholdige silaner, idet silanene i tillegg har halogen-, alkoksy- eller akryloksyrester som deretter omsettes med polyetrene. <:> Disse forbindelser er mangesidig anvendbare. De er tilsetningsmiddel ved fremstilling av polyuretanskum, de egner seg, som drivmiddel, de kan anvendes som prepareringsmiddel i tekstilindustrien eller anvendes i kosmetikk. Som ytterligere anvendelsesformål er det nevnt anvendelsen av forbindelsene som demulgatorer til adskillelse av jordolje/vannemulsjoner. From DE-PS 23 21 557 silicon-containing block copolymers based on organosilicon-modified polydienes are known. These compounds are obtained; by adding silanes containing hydrogen residues to polydienes, as the silanes also have halogen, alkoxy or acryloxy acid residues which are then reacted with the polyethers. <:> These compounds are versatile. They are additives in the production of polyurethane foam, they are suitable as a propellant, they can be used as a preparation agent in the textile industry or used in cosmetics. As a further purpose of use, the use of the compounds as demulsifiers for the separation of petroleum/water emulsions has been mentioned.
Til grunn for foreliggende oppfinnelse ligger den oppgave å tilveiebringe forbindelser som er spesielt egnet som demulgatorer, spesielt til adskillelse av jordolje/- vannemulsjoner, idet de hurtigst mulig og fullstendig utskiller det i jordoljen inneholdte vann. Dessuten skal det tilstrebes at forbindelsene bibeholder deres demulgerings-egenskaper overfor de forskjellige typer råjordoljer og derfor er mest mulig universelt anvendbare. Demulgatorene skal også være forenlige og blandbare med slike fra teknikkens stand for også på denne måte om mulig å utvide deres anvendelsesområde. The present invention is based on the task of providing compounds which are particularly suitable as demulsifiers, especially for separating petroleum/water emulsions, as they separate the water contained in the petroleum as quickly and completely as possible. In addition, efforts must be made to ensure that the compounds retain their demulsifying properties against the various types of crude oils and are therefore as universally applicable as possible. The demulsifiers must also be compatible and miscible with those from the state of the art in order also in this way, if possible, to expand their area of application.
Det er funnet at bestemte organosilisiummodifiserte polydiener oppfyller disse krav. Spesielle karakteristika ved disse forbindelser er Si-O-C tilknyttede langkjedede alkyl-eller alkylfenylgrupper, som åpenbaret bidrar til en øket vekselvirkning med oljefasen i jordoljeemulsjonene. Certain organosilicon modified polydienes have been found to meet these requirements. Special characteristics of these compounds are Si-O-C attached long-chain alkyl or alkylphenyl groups, which obviously contribute to an increased interaction with the oil phase in the petroleum emulsions.
Oppfinnelsen vedrører følgelig anvendelse av organosilisiummodifiserte polydiener med den generelle formel The invention therefore relates to the use of organosilicon-modified polydienes with the general formula
hvori X betyr kjedebegrensende grupper, where X means chain-limiting groups,
R<1> i molekylet er like eller forskjellige og betyr et hydrogenatom eller en metylrest, R<1> in the molecule are the same or different and mean a hydrogen atom or a methyl residue,
R<2> i molekylet er like eller forskjellige og betyr en eventuelt fluorert alkyl- eller alkylfenylrest med 6 til 24 karbonatomer, R<2> in the molecule are the same or different and mean an optionally fluorinated alkyl or alkylphenyl residue with 6 to 24 carbon atoms,
r<3> i molekylet er like eller forskjellige og betyr resten (R<4>0-)mY, idet R<4> omfatter alkylenrester med 2 til 4 karbonatomer, m 2 2 og Y er en alkylrest med 1 til 4 karbonatomer , og r<3> in the molecule are the same or different and mean the residue (R<4>0-)mY, with R<4> comprising alkylene residues with 2 to 4 carbon atoms, m 2 2 and Y is an alkyl residue with 1 to 4 carbon atoms, and
idet gjennomsnittlig being average
w 2 0 w 2 0
x 2 0 x 2 0
y 3 y 3
a = 0 til 2 a = 0 to 2
b = 0 eller 1 b = 0 or 1
0 < c < 3, idet 0 < a + c < 3, 0 < c < 3, since 0 < a + c < 3,
som demulgatorer for jordolje/vannemulsjoner. as demulsifiers for soil oil/water emulsions.
1 formelen betyr Z kjedebegrensende grupper som er på forhånd gitt ved den valgte fremstillingsfremgangsmåte for poly-i 1 the formula means Z chain-limiting groups which are provided in advance by the chosen production process for poly-i
dienet. Eksempler på slike grupper er -H, CH2=CH-CH2-CH2-, -CH2-CH2-OH, -COOH, -CH3, -C4H9, -C6H5,-CH2-C6H5, -Si(CH3)3. the diet. Examples of such groups are -H, CH2=CH-CH2-CH2-, -CH2-CH2-OH, -COOH, -CH3, -C4H9, -C6H5, -CH2-C6H5, -Si(CH3)3.
R<1> kan i det polymere molekyl være like eller forskjellige og bety hydrogen eller metylresten. R<1> in the polymeric molecule can be the same or different and mean hydrogen or the methyl residue.
1 1
R<2> kan likeledes i det polymere molekyl være like eller forskjellig. Derved er R<2> en alkyl- eller alkylfenylrest med 6 til 24 karbonatomer, fortrinnsvis 18 til 24 karbonatomer, spesielt 12 til 24 karbonatomer, idet alkylgruppen skal være forgrenet. Forgrenede alkylgrupper med et høyere karbon-innhold har den fordel at modifiseringsmidlets viskositet nedsettes. Alkylrestene kan også være fluorerte, spesielt delvis fluorerte. Eksempler på slike, fluorerte rester er R<2> can likewise be the same or different in the polymeric molecule. Thereby, R<2> is an alkyl or alkylphenyl residue with 6 to 24 carbon atoms, preferably 18 to 24 carbon atoms, especially 12 to 24 carbon atoms, the alkyl group having to be branched. Branched alkyl groups with a higher carbon content have the advantage that the viscosity of the modifier is reduced. The alkyl radicals can also be fluorinated, especially partially fluorinated. Examples of such fluorinated residues are
CF3-(CF2-)6CH2-, CF3(CF2-)5CH2-CH2-, jCF3-(CF2-)7-CH2-CH2-. CF3-(CF2-)6CH2-, CF3(CF2-)5CH2-CH2-, jCF3-(CF2-)7-CH2-CH2-.
1 1
R^ kan i det polymere molekyl være like eller forskjellige og bety polyeterresten med formel (R<4>0-)mY. R<4> er en alkylenrst med 2, 3 eller 4 karbonatomer. Også R<4> kan i det midlere molekyl være like eller forskjellige. Foretrukket er polyetere med polyetylenoksyd og/eller polypropylenoksyd-enheter, idet ved blandingspolymerisater kan disse enheter opptre statistisk blandet eller opptre adskilt i blokker. Foretrukket er produkter med en sekundær OH-gruppe. Oksyalkylenblokken kan således være sammensatt av oksyetylen-og propylen- og/eller oksybutylenenheter. Fortrinnsvis består oksyalkylenresten i det minste i et omfang på 40 vekt-# av oksyetylenenheter. m > 2. Fortrinnsvis har m en slik verdi at molekylvekten av resten R<3> utgjør 300 til 600. Y er en alkylrest med 1 til 4 karbonatomer. Spesielt foretrukket er metyl- og butylresten. R^ in the polymeric molecule can be the same or different and mean the polyether residue with the formula (R<4>0-)mY. R<4> is an alkylene group with 2, 3 or 4 carbon atoms. Also R<4> in the middle molecule can be the same or different. Polyethers with polyethylene oxide and/or polypropylene oxide units are preferred, since in the case of mixed polymers these units can appear statistically mixed or appear separately in blocks. Products with a secondary OH group are preferred. The oxyalkylene block can thus be composed of oxyethylene and propylene and/or oxybutylene units. Preferably, the oxyalkylene residue consists of at least 40% by weight of oxyethylene units. m > 2. Preferably, m has such a value that the molecular weight of the residue R<3> amounts to 300 to 600. Y is an alkyl residue with 1 to 4 carbon atoms. Particularly preferred are the methyl and butyl residues.
Tal langi vel sene for indeksene w, x, y, a, b og c refererer til det midlere molekyl. Det betyr at de innenfor polymer-blokkdanningen kan anta forskjellige verdier. De må imidlertid gjennomsnittlig 'oppfylle de angitte betingelser. Long numbers for the indices w, x, y, a, b and c refer to the average molecule. This means that within the polymer block formation they can assume different values. They must, however, on average meet the specified conditions.
Fortrinnsvis anvendes forbindelser hvori de usubstituerte dobbeltbindingholdige og med indeksene w og x betegnede enheter foreligger i en mengde fra25til 80 mol-% av summen av enhetene w + x + 7. Compounds are preferably used in which the units containing unsubstituted double bonds and denoted by the indices w and x are present in an amount of from 25 to 80 mol% of the sum of the units w + x + 7.
Spesielt foretrukket anvendes forbindelser hvori indeksen b gjennomsnittlig er 1 og idet R<2> er utledet fra en primær alkohol eller fenol. Compounds in which the index b is on average 1 and where R<2> is derived from a primary alcohol or phenol are particularly preferred.
Forbindelser som eksempelvis anvendes ifølge oppfinnelsen er: Compounds which, for example, are used according to the invention are:
C:0 forholdet av resten R<4> = 2,2:1. ! l C:0 ratio of the residue R<4> = 2.2:1. ! l
C:0 forholdet av resten R<4> = 2,5:1. C:0 ratio of the residue R<4> = 2.5:1.
t t
C:0 forholdet av resten R<4> = 2,2:1. C:0 ratio of the residue R<4> = 2.2:1.
I IN
l i i
C:0 forholdet av resten R<4*> - 2,2:1 C:0 ratio of the residue R<4*> - 2.2:1
C:0 forholdet av resten R<4**> - 2,5:1 C:0 ratio of the residue R<4**> - 2.5:1
De ifølge oppfinnelsen anvendbare forbindelser med formel I kan fremstilles på i og for seg kjent måte, som ikke omfattes av oppfinnelsen, ved at minst y mol silaner med den generelle formel The compounds of formula I that can be used according to the invention can be prepared in a manner known per se, which is not covered by the invention, by at least y mol of silanes of the general formula
idet X betyr en halogen-, alkoksy- eller acyloksyrest, på i og for seg kjent måte tilleires til polydiener med den generelle formel som har en molvekt fra 300 til 200 000 i nærvær av edel-metall-katalysatorer, og de dannede tilleiringsprodukter omfattes med minst y(3-a-c) mol forbindelser med den generelle formel where X means a halogen, alkoxy or acyloxy acid residue, is added in a manner known per se to polydienes of the general formula having a molecular weight of from 300 to 200,000 in the presence of noble metal catalysts, and the formed addition products include at least y(3-a-c) moles of compounds with the general formula
I IN
I IN
°g y-c m°l forbindelser med den generelle formel °g y-c m°l compounds with the general formula
i in
Restene R<1>, R<2>, R<3> og Z som indeksene a, b, c, w, x og y har den allerede angitte betydning. The residues R<1>, R<2>, R<3> and Z as the indices a, b, c, w, x and y have the meaning already indicated.
Gjennomføringen av en slik fremgangsmåte er analog den som er omtalt i tysk patent 23 21 557.' Som katalysatorer for tilleiring av silanene med formel VI til polydienene med formel VII anvendes spesielt platinakatalysatorer som f.eks. heksaklorplatinasyre eller platinaetylenpyridindiklorid. Reaksjonen gjennomføres hensiktsmessig i nærvær av et oppløsningsmiddel, spesielt toluen. Tilleiringen av silanet til polydienet foregår fortrinnsvis ved forhøyede tempera-turer, f.eks. ved toluenets kokepunkt. The implementation of such a method is analogous to that described in German patent 23 21 557.' As catalysts for adding the silanes of formula VI to the polydienes of formula VII, platinum catalysts are used in particular, such as e.g. hexachloroplatinic acid or platinum ethylene pyridine dichloride. The reaction is conveniently carried out in the presence of a solvent, especially toluene. The deposition of the silane to the polydiene preferably takes place at elevated temperatures, e.g. at the boiling point of toluene.
Omsetningene av de dannede mellomprodukter med forbindelsene med formel The conversions of the intermediates formed with the compounds of formula
og med forbindelser med formel 1 i and with compounds of formula 1 i
foregår hensiktsmessig likeledes i nærvær av et oppløsnings-middel, idet igjen toluen er foretrukket. Det kan imidlertid også anvendes andre Inerte oppløsningsmidler som f.eks. metylenklorid, glykoleter eller ' cykliske etere. Har X suitably also takes place in the presence of a solvent, with toluene again being preferred. However, other inert solvents such as e.g. methylene chloride, glycol ether or cyclic ethers. Have X
betydningen av en halogenrest, blir det frigjorte halogen-hydrogen hensiktsmessig oppfanget med ammoniakk. I stedet for ammoniakk kan det også anvendes amin. På tilsvarende måte når X har betydningen av en acyloksyrest kan den frigjorte karboksylsyre nøytraliseres. Har X betydningen av en alkoksyrest så lønner det seg å fjerne det frigjorte lavmolekylære alkanol fra reaksjonsblandingen ved destilla-sjon. Av denne grunn er det også foretrukket som alkoksyrest å anvende metoksy- eller etoksyresten. the importance of a halogen residue, the liberated halogen hydrogen is suitably captured with ammonia. Instead of ammonia, amine can also be used. Similarly, when X has the meaning of an acyloxy acid residue, the liberated carboxylic acid can be neutralized. If X is the meaning of an carboxylic acid residue, then it pays to remove the liberated low molecular weight alkanol from the reaction mixture by distillation. For this reason, it is also preferred to use the methoxy or ethoxy residue as the carboxylic acid residue.
Demulgeringsmidlene ifølge oppfinnelsen tilsettes til jordolje/vannemulsjonene, fortrinnsvis i mengder på 1-300 ppm. Det er også mulig å oppløse demulgatorene i et oppløsningsmiddel som f.eks. toluen og å sette oppløsningen til jordoljen. Forbindelsene fører til en hurtig og meget fullstendig adskillelse av vann fra råoljen. Forbindelsene virker ikke forstyrrende ved den videre opparbeidelse av oljen og føre spesielt ikke til skumproblemer ved destillering og opparbeidelse av oljen. The demulsifiers according to the invention are added to the petroleum/water emulsions, preferably in quantities of 1-300 ppm. It is also possible to dissolve the demulsifiers in a solvent such as e.g. toluene and adding the solution to the petroleum. The compounds lead to a rapid and very complete separation of water from the crude oil. The compounds do not interfere with the further processing of the oil and in particular do not lead to foaming problems during distillation and processing of the oil.
I de følgende eksempler vises fremstilling av de ifølge oppfinnelsen anvendbare demulgatorer og deres tekniske anvendelsesegenskaper. In the following examples, the production of the demulsifiers that can be used according to the invention and their technical application properties are shown.
Generel1 fremst i11ingsfremgangsmåte General first in11ing procedure
En ca. 50^-ig toluenisk oppløsning av polydien fremstilles med 15 mg platinaetylenpyridindiklorid pr. mol SiH som katalysator ved toluenets kokepunkt, og oppløsningen tildryppes den ønskede mengde hydrogensilan. Etter avslut-ning av reaksjonen bestemmes produktets syreverdi og tilsettes den tilsvarende mengde av alkoholpolyeterblanding med molar mengde av trietylamin. Etter filtrering og avdestillering av toluen får man det ønskede sluttprodukt som dessuten eventuelt kan stabiliseres ved tilsetninger. An approx. A 50% toluene solution of the polydiene is prepared with 15 mg of platinum ethylene pyridine dichloride per mol SiH as a catalyst at the boiling point of toluene, and the desired amount of hydrogen silane is added dropwise to the solution. After completion of the reaction, the acid value of the product is determined and the corresponding amount of alcohol polyether mixture with a molar amount of triethylamine is added. After filtering and distilling off the toluene, you get the desired end product, which can also possibly be stabilized by additions.
Demulgeringsforsøk Demulsification test
i in
Det ble anvendt to forskjellige nordtyske råoljer, olje A med 48# vann og olje B med 28% vann. Til hver 50 ml råolje i et kalibrert iakttagelsesglass ble det tilsatt 20 ppm av de forskjellige stoffer og de utskilte vannmengder i ml ble bestemt etter bestemte tider. ; Temperaturen ble holdt konstant ved 50* C under forsøke^. Det ble undersøkt polyetere med forskjellig E0/P0-f6rhold samt deres omsetningsprodukter med polydien-vann-hydrogen-silan-addukter samt produkter ifølge oppfinnelsen som i tillegg inneholdt langkjedede alkoholderivater. Two different North German crude oils were used, oil A with 48% water and oil B with 28% water. To each 50 ml of crude oil in a calibrated observation glass, 20 ppm of the various substances were added and the secreted amounts of water in ml were determined after specific times. ; The temperature was kept constant at 50* C during the experiment. Polyethers with different E0/P0 ratios and their reaction products with polydiene-water-hydrogen-silane adducts and products according to the invention which additionally contained long-chain alcohol derivatives were investigated.
i in
Til .sammenligning med teknikkens stand ble eksempel 1 i det tyske patent 16 42 825 og 23 21557 etterarbeidet. For comparison with the state of the art, example 1 in the German patent 16 42 825 and 23 21557 was revised.
I den etterfølgende tabellen, som gjengir forsøksresultatene, er de følgende stoffer betegnet med tallene fra 1 til 13. In the following table, which reproduces the test results, the following substances are designated by numbers from 1 to 13.
i in
1) Polyeter C4Hg0(CnH2n0)36>gH 1) Polyether C4Hg0(CnH2n0)36>gH
n=2og3, C:0=2,2:ln=2and3, C:0=2,2:1
i in
i in
2) Polyeter C4HgO(CnH2n0)33f8<H>2) Polyether C4HgO(CnH2n0)33f8<H>
n = 2, 3 og 4, C:0 = 2,5:1 n = 2, 3 and 4, C:O = 2.5:1
3) 3)
4) 4)
6) Formel I med w = 5,x = 25,y = 30, R<1> = H, 6) Formula I with w = 5,x = 25,y = 30, R<1> = H,
R<2> = isooktadecyl-, a-l,b-l, C-o R<2> = iso-octadecyl-, a-l, b-l, C-o
7) som 6, med a=l,c = 2, R<3> = C4Hg(0Cn<H>2n)36,9» n ■= 2 og 3, C:0 = 2,2:1 8) som 7, med R<3> - C4H9(0CnH2ri )33 ,g > 7) as 6, with a=l,c = 2, R<3> = C4Hg(0Cn<H>2n)36.9» n ■= 2 and 3, C:0 = 2.2:1 8) as 7, with R<3> - C4H9(0CnH2ri )33 ,g >
n = 2, 3 og4, C:= = 2,5:1 n = 2, 3 and 4, C:= = 2.5:1
9) som 6, med R<2> = isotridecyl-, 9) as 6, with R<2> = isotridecyl-,
R<3> = C4Hg( (0CnH2n)33^R<3> = C4Hg( (0CnH2n)33^).
a = l,b = l, c = l, a = l,b = l, c = l,
n = 2 og 3, C:0 2,5:1 10) som 9, med R<2> = Isooktadecyl-, = C4H9(0CnH2n)36>q, n = 2 and 3, C:0 2.5:1 10) as 9, with R<2> = Isoctadecyl-, = C4H9(0CnH2n)36>q,
n = 2 og 3, C:= = 2,2:1 n = 2 and 3, C:= = 2.2:1
11) som 10, med R<2> nonylfenyl- 11) as 10, with R<2> nonylphenyl-
12) Produkt fra DE-PS 16 42 825, eksempel 1 12) Product from DE-PS 16 42 825, example 1
13) Produkt fra DE-PS 23 21 557, eksempel 1 13) Product from DE-PS 23 21 557, example 1
Ved sammenligning av eksemplene 9 til 12 Ifølge oppfinnelsen med eksemplene som ikke faller inn under oppfinnelsen fremgår at bare ved nærvær av polyeter og langkjedede alkoholer i molekylene med formel I kan det oppnås en meget god effekt ved demulgeringen av jordolje/vannemulsjoner. When comparing examples 9 to 12 according to the invention with the examples which do not fall within the scope of the invention, it appears that only in the presence of polyethers and long-chain alcohols in the molecules of formula I can a very good effect be achieved in the demulsification of petroleum/water emulsions.
Sammenligningen med demulgatorer ifølge teknikkens stand (eksempel 12 og 13) demonstrerer overlegenheten av forbindelsene ifølge oppfinnelsen. The comparison with prior art demulsifiers (Examples 12 and 13) demonstrates the superiority of the compounds of the invention.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE3228133 | 1982-07-28 |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| NO831471L NO831471L (en) | 1984-01-30 |
| NO162913B true NO162913B (en) | 1989-11-27 |
| NO162913C NO162913C (en) | 1990-03-07 |
Family
ID=6169500
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| NO831471A NO162913C (en) | 1982-07-28 | 1983-04-26 | APPLICATION OF ORGANOSILICIUM-MODIFIED POLYDIANS AS DEMULGATORS FOR OIL OIL / WATER EMULSIONS. |
Country Status (2)
| Country | Link |
|---|---|
| GB (1) | GB2125414B (en) |
| NO (1) | NO162913C (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1090328A (en) * | 1965-10-23 | |||
| GB1353743A (en) * | 1970-09-07 | 1974-05-22 | Ici Ltd | Organosilicon-modified polymers |
-
1983
- 1983-04-26 NO NO831471A patent/NO162913C/en unknown
- 1983-05-19 GB GB08313896A patent/GB2125414B/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| GB2125414B (en) | 1985-10-23 |
| GB2125414A (en) | 1984-03-07 |
| NO831471L (en) | 1984-01-30 |
| NO162913C (en) | 1990-03-07 |
| GB8313896D0 (en) | 1983-06-22 |
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