KR100976753B1 - 1-도데센 및 1-데센의 공동올리고머화 방법 - Google Patents
1-도데센 및 1-데센의 공동올리고머화 방법 Download PDFInfo
- Publication number
- KR100976753B1 KR100976753B1 KR1020030012993A KR20030012993A KR100976753B1 KR 100976753 B1 KR100976753 B1 KR 100976753B1 KR 1020030012993 A KR1020030012993 A KR 1020030012993A KR 20030012993 A KR20030012993 A KR 20030012993A KR 100976753 B1 KR100976753 B1 KR 100976753B1
- Authority
- KR
- South Korea
- Prior art keywords
- decene
- weight
- dodecene
- oligomerization
- cst
- Prior art date
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- AFFLGGQVNFXPEV-UHFFFAOYSA-N 1-decene Chemical compound CCCCCCCCC=C AFFLGGQVNFXPEV-UHFFFAOYSA-N 0.000 title claims abstract description 88
- CRSBERNSMYQZNG-UHFFFAOYSA-N 1-dodecene Chemical compound CCCCCCCCCCC=C CRSBERNSMYQZNG-UHFFFAOYSA-N 0.000 title claims abstract description 62
- 229940069096 dodecene Drugs 0.000 title claims abstract description 32
- 238000006384 oligomerization reaction Methods 0.000 title claims abstract description 25
- 238000000034 method Methods 0.000 claims abstract description 22
- 230000004580 weight loss Effects 0.000 claims abstract description 12
- 229920013639 polyalphaolefin Polymers 0.000 claims abstract description 7
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 44
- 238000006243 chemical reaction Methods 0.000 claims description 22
- LRHPLDYGYMQRHN-UHFFFAOYSA-N N-Butanol Chemical compound CCCCO LRHPLDYGYMQRHN-UHFFFAOYSA-N 0.000 claims description 21
- 239000000203 mixture Substances 0.000 claims description 20
- 239000003054 catalyst Substances 0.000 claims description 4
- 238000004519 manufacturing process Methods 0.000 claims description 2
- 150000001336 alkenes Chemical class 0.000 claims 1
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims 1
- 150000003138 primary alcohols Chemical group 0.000 claims 1
- SNRUBQQJIBEYMU-UHFFFAOYSA-N Dodecane Natural products CCCCCCCCCCCC SNRUBQQJIBEYMU-UHFFFAOYSA-N 0.000 abstract description 2
- 239000000047 product Substances 0.000 description 40
- 239000013638 trimer Substances 0.000 description 22
- 239000003921 oil Substances 0.000 description 11
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 10
- 238000004821 distillation Methods 0.000 description 9
- 239000002994 raw material Substances 0.000 description 9
- 239000012043 crude product Substances 0.000 description 7
- 238000005984 hydrogenation reaction Methods 0.000 description 5
- 239000000314 lubricant Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 5
- 229910052757 nitrogen Inorganic materials 0.000 description 5
- 239000011541 reaction mixture Substances 0.000 description 5
- KWKAKUADMBZCLK-UHFFFAOYSA-N 1-octene Chemical compound CCCCCCC=C KWKAKUADMBZCLK-UHFFFAOYSA-N 0.000 description 4
- 238000007792 addition Methods 0.000 description 4
- WTEOIRVLGSZEPR-UHFFFAOYSA-N boron trifluoride Chemical compound FB(F)F WTEOIRVLGSZEPR-UHFFFAOYSA-N 0.000 description 4
- 230000035484 reaction time Effects 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 125000004432 carbon atom Chemical group C* 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- BDERNNFJNOPAEC-UHFFFAOYSA-N propan-1-ol Chemical compound CCCO BDERNNFJNOPAEC-UHFFFAOYSA-N 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- KBPLFHHGFOOTCA-UHFFFAOYSA-N 1-Octanol Chemical compound CCCCCCCCO KBPLFHHGFOOTCA-UHFFFAOYSA-N 0.000 description 2
- 229910015900 BF3 Inorganic materials 0.000 description 2
- AMQJEAYHLZJPGS-UHFFFAOYSA-N N-Pentanol Chemical compound CCCCCO AMQJEAYHLZJPGS-UHFFFAOYSA-N 0.000 description 2
- MWKFXSUHUHTGQN-UHFFFAOYSA-N decan-1-ol Chemical compound CCCCCCCCCCO MWKFXSUHUHTGQN-UHFFFAOYSA-N 0.000 description 2
- ZSIAUFGUXNUGDI-UHFFFAOYSA-N hexan-1-ol Chemical compound CCCCCCO ZSIAUFGUXNUGDI-UHFFFAOYSA-N 0.000 description 2
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 description 2
- TVMXDCGIABBOFY-UHFFFAOYSA-N n-Octanol Natural products CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 2
- 229920002554 vinyl polymer Polymers 0.000 description 2
- 239000011345 viscous material Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 239000004711 α-olefin Substances 0.000 description 2
- NMRPBPVERJPACX-UHFFFAOYSA-N (3S)-octan-3-ol Natural products CCCCCC(O)CC NMRPBPVERJPACX-UHFFFAOYSA-N 0.000 description 1
- GGQQNYXPYWCUHG-RMTFUQJTSA-N (3e,6e)-deca-3,6-diene Chemical compound CCC\C=C\C\C=C\CC GGQQNYXPYWCUHG-RMTFUQJTSA-N 0.000 description 1
- 239000005968 1-Decanol Substances 0.000 description 1
- WOFPPJOZXUTRAU-UHFFFAOYSA-N 2-Ethyl-1-hexanol Natural products CCCCC(O)CCC WOFPPJOZXUTRAU-UHFFFAOYSA-N 0.000 description 1
- YIWUKEYIRIRTPP-UHFFFAOYSA-N 2-ethylhexan-1-ol Chemical compound CCCCC(CC)CO YIWUKEYIRIRTPP-UHFFFAOYSA-N 0.000 description 1
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 150000002009 diols Chemical class 0.000 description 1
- AZHSSKPUVBVXLK-UHFFFAOYSA-N ethane-1,1-diol Chemical compound CC(O)O AZHSSKPUVBVXLK-UHFFFAOYSA-N 0.000 description 1
- 125000002573 ethenylidene group Chemical group [*]=C=C([H])[H] 0.000 description 1
- 239000003517 fume Substances 0.000 description 1
- 238000004817 gas chromatography Methods 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- SFMJNHNUOVADRW-UHFFFAOYSA-N n-[5-[9-[4-(methanesulfonamido)phenyl]-2-oxobenzo[h][1,6]naphthyridin-1-yl]-2-methylphenyl]prop-2-enamide Chemical compound C1=C(NC(=O)C=C)C(C)=CC=C1N1C(=O)C=CC2=C1C1=CC(C=3C=CC(NS(C)(=O)=O)=CC=3)=CC=C1N=C2 SFMJNHNUOVADRW-UHFFFAOYSA-N 0.000 description 1
- 238000005192 partition Methods 0.000 description 1
- 229920005862 polyol Polymers 0.000 description 1
- 150000003077 polyols Chemical class 0.000 description 1
- 238000005070 sampling Methods 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000010409 thin film Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10M—LUBRICATING COMPOSITIONS; USE OF CHEMICAL SUBSTANCES EITHER ALONE OR AS LUBRICATING INGREDIENTS IN A LUBRICATING COMPOSITION
- C10M107/00—Lubricating compositions characterised by the base-material being a macromolecular compound
- C10M107/02—Hydrocarbon polymers; Hydrocarbon polymers modified by oxidation
- C10M107/10—Hydrocarbon polymers; Hydrocarbon polymers modified by oxidation containing aliphatic monomer having more than 4 carbon atoms
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F10/00—Homopolymers and copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/02—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons
- C07C2/04—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation
- C07C2/06—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition between unsaturated hydrocarbons by oligomerisation of well-defined unsaturated hydrocarbons without ring formation of alkenes, i.e. acyclic hydrocarbons having only one carbon-to-carbon double bond
- C07C2/08—Catalytic processes
- C07C2/14—Catalytic processes with inorganic acids; with salts or anhydrides of acids
- C07C2/20—Acids of halogen; Salts thereof ; Complexes thereof with organic compounds
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2527/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
- C07C2527/06—Halogens; Compounds thereof
- C07C2527/08—Halides
- C07C2527/12—Fluorides
- C07C2527/1213—Boron fluoride
Abstract
Description
특 징 | 실시예 7 의 생성물 |
KV 100 ℃ (cSt) | 6.1 |
KV 40 ℃ (cSt) | 31.94 |
KV -40 ℃ (cSt) | 9574 |
VI | 141 |
유동점 (℃) | -4.4 |
노아크 (%) | 4.7 |
%〈 삼량체 | 1.6 |
% 삼량체 | 70.1 |
% 사량체 | 21.1 |
% 오량체 | 7.2 |
특 징 | 실시예 9 의 생성물 |
KV 100 ℃ (cSt) | 6.25 |
KV 40 ℃ (cSt) | 33.16 |
KV -40 ℃ (cSt) | 8610 |
VI | 141 |
유동점 (℃) | -44 |
노아크 (%) | 4.4 |
%〈 삼량체 | 0 |
% 삼량체 | 58.8 |
% 사량체 | 30.9 |
% 오량체 | 10.3 |
특 징 | 실시예 10 의 생성물 |
KV 100 ℃ (cSt) | 5.81 |
KV 40 ℃ (cSt) | 29.8 |
KV -40 ℃ (cSt) | 5110 |
VI | 142 |
유동점 (℃) | -49 |
노아크 (%) | 4.8 |
%〈 삼량체 | 1.1 |
% 삼량체 | 55.7 |
% 사량체 | 31.8 |
% 오량체 | 11.4 |
특 징 | 생성물 A 삼량체 (증류 오버헤드) |
생성물 B 삼량체 + (증류 바닥) |
KV 100 ℃ (cSt) | 4.36 | 7.02 |
KV 40 ℃ (cSt) | 19.82 | 38.06 |
KV -40 ℃ (cSt) | 3068 | 11330 |
VI | 132 | 144 |
유동점 (℃) | -58 | -49 |
노아크 (%) | 9.1 | 3.0 |
%〈 삼량체 | 1.3 | 0 |
% 삼량체 | 98.7 | 37.9 |
% 사량체 | 0 | 48.5 |
% 오량체 | 0 | 13.6 |
특 징 | 생성물 C |
KV 100 ℃ (cSt) | 5.21 |
KV 40 ℃ (cSt) | 25.27 |
KV -40 ℃ (cSt) | 4920 |
VI | 142 |
유동점 (℃) | -52 |
노아크 (%) | 7.1 |
%〈 삼량체 | 0.9 |
% 삼량체 | 75.1 |
% 사량체 | 18.7 |
% 오량체 | 5.3 |
특 징 | 생성물 D | 생성물 E |
KV 100 ℃ (cSt) | 4.54 | 8.62 |
KV 40 ℃ (cSt) | 20.76 | 52.83 |
KV -40 ℃ (cSt) | 3636 | 23270 |
VI | 136 | 140 |
유동점 (℃) | -50 | -48 |
노아크 (%) | 8.4 | 2.9 |
%〈 삼량체 | 0.8 | - |
% 삼량체 | 99.2 | 6.0 |
% 사량체 | 0 | 81.6 |
% 오량체 | 0 | 12.4 |
특 징 | 생성물 D | DS164/DS166 | DS164/5cSt (100% C12) |
KV 100 ℃ (cSt) | 4.54 | 4.54 | 4.56 |
KV 40 ℃ (cSt) | 20.76 | 21.25 | 21.07 |
KV -40 ℃ (cSt) | 3636 | 3860 | 3596 |
VI | 136 | 130 | 135 |
유동점 (℃) | -50 | -60 | -54 |
노아크 (%) | 8.4 | 11.9 | 9.8 |
인화점(PMCC) | 208 | 220 | 218 |
CCS-30 (cP) | 1170 | 1190 | 1100 |
CCS-35(cP) | 1880 | 2010 | 1990 |
특 징 | 생성물 E | SHF-83 | DS168 |
KV 100 ℃ (cSt) | 7.93 | 7.94 | 7.93 |
KV 40 ℃ (cSt) | 46.80 | 47.32 | 47.51 |
KV -40 ℃ (cSt) | 17979 | 18650 | 18170 |
VI | 140 | 139 | 137 |
유동점 (℃) | -48 | -50 | -55 |
노아크 (%) | 3.3 | 3.8 | 3.6 |
Claims (11)
- BF3 촉매 및 알콜 촉진제의 존재 하에서 60 내지 90 중량% 의 1-도데센 및 10 내지 40 중량% 의 1-데센을 포함하는 혼합물을 20 ℃ 내지 60 ℃ 범위의 온도에서 공동올리고머화시켜 이에 의해 100 ℃ 에서의 동적 점도 4 내지 6 cSt 범위, 노아크 중량 손실 4 내지 9 % 범위, 점도 지수 130 내지 145 범위 및 유동점 -60 ℃ 내지 -50 ℃ 범위의 폴리알파올레핀을 형성하는 것을 포함하는, 폴리알파올레핀 생성물의 제조 방법.
- 제 1 항에 있어서, 1-도데센 대 1-데센의 중량비가 2:1 이상인 방법.
- 제 1 항에 있어서, 1-데센이 반응 기간 동안 연속적으로 또는 간헐적으로 도입되는 방법.
- 제 3 항에 있어서, 올리고머화가 진행함에 따라 올리고머화에 사용되는 1-데센 총량의 50 중량% 이상이 도입되는 방법.
- 제 4 항에 있어서, 1-데센 공급률이 1 시간 당 1-도데센 및 1-데센 1000 중량부 당 1-데센 400 내지 800 부인 방법.
- 제 1 항에 있어서, 알콜 촉진제가 일차 알콜인 방법.
- 제 6 항에 있어서, 알콜 촉진제가 1-부탄올과 에탄올 중 하나 이상인 방법.
- 제 1 항에 있어서, 알콜 촉진제가 1-도데센 및 1-데센 총량의 0.3 내지 0.7 중량% 수준으로 사용되는 방법.
- 제 1 항에 있어서, 올리고머화가 진행함에 따라 알콜 촉진제가 연속적으로 또는 간헐적으로 도입되는 방법.
- 제 1 항에 있어서, 올리고머화가 진행함에 따라 올리고머화에 사용되는 알콜 촉진제 총량의 50 중량% 이상이 도입되는 방법.
- 제 10 항에 있어서, 알콜 촉진제 공급률이 1 시간 당 1-도데센 및 1-데센 1000 중량부 당 알콜 촉진제 0.8 내지 4 부인 방법.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/090,194 | 2002-03-04 | ||
US10/090,194 US6646174B2 (en) | 2002-03-04 | 2002-03-04 | Co-oligomerization of 1-dodecene and 1-decene |
Publications (2)
Publication Number | Publication Date |
---|---|
KR20030072233A KR20030072233A (ko) | 2003-09-13 |
KR100976753B1 true KR100976753B1 (ko) | 2010-08-18 |
Family
ID=27753979
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
KR1020030012993A KR100976753B1 (ko) | 2002-03-04 | 2003-03-03 | 1-도데센 및 1-데센의 공동올리고머화 방법 |
Country Status (8)
Country | Link |
---|---|
US (1) | US6646174B2 (ko) |
EP (1) | EP1342707B1 (ko) |
JP (1) | JP4392177B2 (ko) |
KR (1) | KR100976753B1 (ko) |
CN (1) | CN1274725C (ko) |
CA (1) | CA2418801C (ko) |
ES (1) | ES2554761T3 (ko) |
RU (1) | RU2309930C2 (ko) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR102323813B1 (ko) * | 2020-05-22 | 2021-11-09 | 아주대학교산학협력단 | 알파-올레핀의 삼량화 혼합물, 이의 제조 방법 및 이를 포함하는 윤활유 |
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- 2003-02-14 CA CA002418801A patent/CA2418801C/en not_active Expired - Fee Related
- 2003-02-24 ES ES03251087.7T patent/ES2554761T3/es not_active Expired - Lifetime
- 2003-02-24 EP EP03251087.7A patent/EP1342707B1/en not_active Expired - Lifetime
- 2003-02-28 RU RU2003105734/04A patent/RU2309930C2/ru not_active IP Right Cessation
- 2003-03-03 KR KR1020030012993A patent/KR100976753B1/ko active IP Right Grant
- 2003-03-04 JP JP2003056627A patent/JP4392177B2/ja not_active Expired - Fee Related
- 2003-03-04 CN CNB031051146A patent/CN1274725C/zh not_active Expired - Fee Related
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US4045508A (en) | 1975-11-20 | 1977-08-30 | Gulf Research & Development Company | Method of making alpha-olefin oligomers |
US4950822A (en) | 1988-06-27 | 1990-08-21 | Ethyl Corporation | Olefin oligomer synlube process |
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Publication number | Priority date | Publication date | Assignee | Title |
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KR102323813B1 (ko) * | 2020-05-22 | 2021-11-09 | 아주대학교산학협력단 | 알파-올레핀의 삼량화 혼합물, 이의 제조 방법 및 이를 포함하는 윤활유 |
WO2021235681A1 (ko) * | 2020-05-22 | 2021-11-25 | 아주대학교 산학협력단 | 알파-올레핀의 삼량화 혼합물, 이의 제조 방법 및 이를 포함하는 윤활유 |
Also Published As
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RU2309930C2 (ru) | 2007-11-10 |
KR20030072233A (ko) | 2003-09-13 |
CA2418801A1 (en) | 2003-09-04 |
CN1274725C (zh) | 2006-09-13 |
ES2554761T3 (es) | 2015-12-23 |
US20030166986A1 (en) | 2003-09-04 |
CA2418801C (en) | 2009-04-14 |
EP1342707A2 (en) | 2003-09-10 |
EP1342707A3 (en) | 2004-03-10 |
US6646174B2 (en) | 2003-11-11 |
JP2003286203A (ja) | 2003-10-10 |
JP4392177B2 (ja) | 2009-12-24 |
EP1342707B1 (en) | 2015-11-11 |
CN1442434A (zh) | 2003-09-17 |
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