CN108525703A - A kind of ionic-liquid catalyst and preparation method thereof preparing high carbon chain alkylbenzene - Google Patents
A kind of ionic-liquid catalyst and preparation method thereof preparing high carbon chain alkylbenzene Download PDFInfo
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- CN108525703A CN108525703A CN201810489339.0A CN201810489339A CN108525703A CN 108525703 A CN108525703 A CN 108525703A CN 201810489339 A CN201810489339 A CN 201810489339A CN 108525703 A CN108525703 A CN 108525703A
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- ionic liquid
- catalyst
- room temperature
- preparing high
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- 239000002608 ionic liquid Substances 0.000 title claims abstract description 144
- 239000003054 catalyst Substances 0.000 title claims abstract description 61
- -1 carbon chain alkylbenzene Chemical class 0.000 title claims abstract description 40
- 238000002360 preparation method Methods 0.000 title claims abstract description 31
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims abstract description 48
- LSNNMFCWUKXFEE-UHFFFAOYSA-M Bisulfite Chemical compound OS([O-])=O LSNNMFCWUKXFEE-UHFFFAOYSA-M 0.000 claims abstract description 30
- 239000002253 acid Substances 0.000 claims abstract description 30
- 150000001336 alkenes Chemical class 0.000 claims abstract description 28
- 238000005804 alkylation reaction Methods 0.000 claims abstract description 24
- 230000029936 alkylation Effects 0.000 claims abstract description 18
- 239000002841 Lewis acid Substances 0.000 claims abstract description 17
- RAXXELZNTBOGNW-UHFFFAOYSA-N imidazole Natural products C1=CNC=N1 RAXXELZNTBOGNW-UHFFFAOYSA-N 0.000 claims abstract description 17
- 150000007517 lewis acids Chemical class 0.000 claims abstract description 17
- 229910001510 metal chloride Inorganic materials 0.000 claims abstract description 16
- 229910052751 metal Inorganic materials 0.000 claims abstract description 12
- 239000002184 metal Substances 0.000 claims abstract description 12
- 238000005349 anion exchange Methods 0.000 claims abstract description 7
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 claims abstract description 5
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 3
- 229910052802 copper Inorganic materials 0.000 claims abstract description 3
- 229910052742 iron Inorganic materials 0.000 claims abstract description 3
- 229910052718 tin Inorganic materials 0.000 claims abstract description 3
- 229910052725 zinc Inorganic materials 0.000 claims abstract description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 75
- 238000006243 chemical reaction Methods 0.000 claims description 44
- 239000002243 precursor Substances 0.000 claims description 33
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 claims description 12
- 150000004996 alkyl benzenes Chemical class 0.000 claims description 12
- 239000003960 organic solvent Substances 0.000 claims description 12
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 10
- 238000001816 cooling Methods 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 10
- 229910021591 Copper(I) chloride Inorganic materials 0.000 claims description 8
- OXBLHERUFWYNTN-UHFFFAOYSA-M copper(I) chloride Chemical compound [Cu]Cl OXBLHERUFWYNTN-UHFFFAOYSA-M 0.000 claims description 8
- MHYFEEDKONKGEB-UHFFFAOYSA-N oxathiane 2,2-dioxide Chemical compound O=S1(=O)CCCCO1 MHYFEEDKONKGEB-UHFFFAOYSA-N 0.000 claims description 6
- MCMFEZDRQOJKMN-UHFFFAOYSA-N 1-butylimidazole Chemical compound CCCCN1C=CN=C1 MCMFEZDRQOJKMN-UHFFFAOYSA-N 0.000 claims description 5
- KGWVFQAPOGAVRF-UHFFFAOYSA-N 1-hexylimidazole Chemical compound CCCCCCN1C=CN=C1 KGWVFQAPOGAVRF-UHFFFAOYSA-N 0.000 claims description 5
- FSSPGSAQUIYDCN-UHFFFAOYSA-N 1,3-Propane sultone Chemical compound O=S1(=O)CCCO1 FSSPGSAQUIYDCN-UHFFFAOYSA-N 0.000 claims description 4
- 150000002739 metals Chemical class 0.000 claims description 4
- 238000005406 washing Methods 0.000 claims description 4
- UPYVYJSWGZMBOU-UHFFFAOYSA-N 1-pentylimidazole Chemical compound CCCCCN1C=CN=C1 UPYVYJSWGZMBOU-UHFFFAOYSA-N 0.000 claims description 3
- 229910021578 Iron(III) chloride Inorganic materials 0.000 claims description 3
- 229910021586 Nickel(II) chloride Inorganic materials 0.000 claims description 2
- 229910052759 nickel Inorganic materials 0.000 claims description 2
- QMMRZOWCJAIUJA-UHFFFAOYSA-L nickel dichloride Chemical group Cl[Ni]Cl QMMRZOWCJAIUJA-UHFFFAOYSA-L 0.000 claims description 2
- 239000011592 zinc chloride Substances 0.000 claims description 2
- JIAARYAFYJHUJI-UHFFFAOYSA-L zinc dichloride Chemical compound [Cl-].[Cl-].[Zn+2] JIAARYAFYJHUJI-UHFFFAOYSA-L 0.000 claims description 2
- 238000010438 heat treatment Methods 0.000 claims 2
- 229910021592 Copper(II) chloride Inorganic materials 0.000 claims 1
- 229910021626 Tin(II) chloride Inorganic materials 0.000 claims 1
- 229910021627 Tin(IV) chloride Inorganic materials 0.000 claims 1
- ORTQZVOHEJQUHG-UHFFFAOYSA-L copper(II) chloride Chemical compound Cl[Cu]Cl ORTQZVOHEJQUHG-UHFFFAOYSA-L 0.000 claims 1
- 238000001035 drying Methods 0.000 claims 1
- 238000002156 mixing Methods 0.000 claims 1
- AXZWODMDQAVCJE-UHFFFAOYSA-L tin(II) chloride (anhydrous) Chemical compound [Cl-].[Cl-].[Sn+2] AXZWODMDQAVCJE-UHFFFAOYSA-L 0.000 claims 1
- 150000002500 ions Chemical class 0.000 abstract description 4
- 239000007788 liquid Substances 0.000 abstract description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 24
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N Ethylbenzene Chemical compound CCC1=CC=CC=C1 YNQLUTRBYVCPMQ-UHFFFAOYSA-N 0.000 description 10
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 10
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 description 8
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 description 8
- 229910052794 bromium Inorganic materials 0.000 description 8
- 239000005416 organic matter Substances 0.000 description 8
- 239000007864 aqueous solution Substances 0.000 description 7
- 239000000203 mixture Substances 0.000 description 7
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 description 6
- 238000004821 distillation Methods 0.000 description 6
- 239000002994 raw material Substances 0.000 description 6
- 239000008096 xylene Substances 0.000 description 6
- GQEZCXVZFLOKMC-UHFFFAOYSA-N 1-hexadecene Chemical compound CCCCCCCCCCCCCCC=C GQEZCXVZFLOKMC-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 4
- 238000013517 stratification Methods 0.000 description 4
- 239000011831 acidic ionic liquid Substances 0.000 description 3
- 230000003197 catalytic effect Effects 0.000 description 3
- CCCMONHAUSKTEQ-UHFFFAOYSA-N octadecene Natural products CCCCCCCCCCCCCCCCC=C CCCMONHAUSKTEQ-UHFFFAOYSA-N 0.000 description 3
- AKHNMLFCWUSKQB-UHFFFAOYSA-L sodium thiosulfate Chemical compound [Na+].[Na+].[O-]S([O-])(=O)=S AKHNMLFCWUSKQB-UHFFFAOYSA-L 0.000 description 3
- 235000019345 sodium thiosulphate Nutrition 0.000 description 3
- 239000012086 standard solution Substances 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- HIXDQWDOVZUNNA-UHFFFAOYSA-N 2-(3,4-dimethoxyphenyl)-5-hydroxy-7-methoxychromen-4-one Chemical compound C=1C(OC)=CC(O)=C(C(C=2)=O)C=1OC=2C1=CC=C(OC)C(OC)=C1 HIXDQWDOVZUNNA-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- 208000012839 conversion disease Diseases 0.000 description 2
- 238000011161 development Methods 0.000 description 2
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 2
- 239000001282 iso-butane Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 description 1
- IQQRAVYLUAZUGX-UHFFFAOYSA-N 1-butyl-3-methylimidazolium Chemical compound CCCCN1C=C[N+](C)=C1 IQQRAVYLUAZUGX-UHFFFAOYSA-N 0.000 description 1
- LXJNAOKLRCANID-UHFFFAOYSA-N C(N)(O)=O.C(N)(O)=O.CC(C1=CC=CC=C1)C1=CC=CC=C1 Chemical compound C(N)(O)=O.C(N)(O)=O.CC(C1=CC=CC=C1)C1=CC=CC=C1 LXJNAOKLRCANID-UHFFFAOYSA-N 0.000 description 1
- 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
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 150000001335 aliphatic alkanes Chemical class 0.000 description 1
- 125000005210 alkyl ammonium group Chemical group 0.000 description 1
- 125000000217 alkyl group Chemical group 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 150000001450 anions Chemical group 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- IAQRGUVFOMOMEM-UHFFFAOYSA-N butene Natural products CC=CC IAQRGUVFOMOMEM-UHFFFAOYSA-N 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- 235000019441 ethanol Nutrition 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 150000004693 imidazolium salts Chemical class 0.000 description 1
- 150000008040 ionic compounds Chemical class 0.000 description 1
- 150000007522 mineralic acids Chemical class 0.000 description 1
- 238000006053 organic reaction Methods 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000011973 solid acid Substances 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- BDHFUVZGWQCTTF-UHFFFAOYSA-M sulfonate Chemical compound [O-]S(=O)=O BDHFUVZGWQCTTF-UHFFFAOYSA-M 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 239000000271 synthetic detergent Substances 0.000 description 1
- 238000004448 titration Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 235000005074 zinc chloride Nutrition 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J31/00—Catalysts comprising hydrides, coordination complexes or organic compounds
- B01J31/16—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes
- B01J31/18—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms
- B01J31/1805—Catalysts comprising hydrides, coordination complexes or organic compounds containing coordination complexes containing nitrogen, phosphorus, arsenic or antimony as complexing atoms, e.g. in pyridine ligands, or in resonance therewith, e.g. in isocyanide ligands C=N-R or as complexed central atoms the ligands containing nitrogen
- B01J31/181—Cyclic ligands, including e.g. non-condensed polycyclic ligands, comprising at least one complexing nitrogen atom as ring member, e.g. pyridine
- B01J31/1815—Cyclic ligands, including e.g. non-condensed polycyclic ligands, comprising at least one complexing nitrogen atom as ring member, e.g. pyridine with more than one complexing nitrogen atom, e.g. bipyridyl, 2-aminopyridine
-
- 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
- C07C2/54—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by addition of unsaturated hydrocarbons to saturated hydrocarbons or to hydrocarbons containing a six-membered aromatic ring with no unsaturation outside the aromatic ring
- C07C2/64—Addition to a carbon atom of a six-membered aromatic ring
- C07C2/66—Catalytic processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/02—Compositional aspects of complexes used, e.g. polynuclearity
- B01J2531/0202—Polynuclearity
- B01J2531/0205—Bi- or polynuclear complexes, i.e. comprising two or more metal coordination centres, without metal-metal bonds, e.g. Cp(Lx)Zr-imidazole-Zr(Lx)Cp
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/02—Compositional aspects of complexes used, e.g. polynuclearity
- B01J2531/0213—Complexes without C-metal linkages
- B01J2531/0216—Bi- or polynuclear complexes, i.e. comprising two or more metal coordination centres, without metal-metal bonds, e.g. Cp(Lx)Zr-imidazole-Zr(Lx)Cp
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/02—Compositional aspects of complexes used, e.g. polynuclearity
- B01J2531/0238—Complexes comprising multidentate ligands, i.e. more than 2 ionic or coordinative bonds from the central metal to the ligand, the latter having at least two donor atoms, e.g. N, O, S, P
- B01J2531/0241—Rigid ligands, e.g. extended sp2-carbon frameworks or geminal di- or trisubstitution
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/10—Complexes comprising metals of Group I (IA or IB) as the central metal
- B01J2531/16—Copper
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/20—Complexes comprising metals of Group II (IIA or IIB) as the central metal
- B01J2531/26—Zinc
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/30—Complexes comprising metals of Group III (IIIA or IIIB) as the central metal
- B01J2531/31—Aluminium
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/40—Complexes comprising metals of Group IV (IVA or IVB) as the central metal
- B01J2531/42—Tin
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/80—Complexes comprising metals of Group VIII as the central metal
- B01J2531/84—Metals of the iron group
- B01J2531/842—Iron
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2531/00—Additional information regarding catalytic systems classified in B01J31/00
- B01J2531/80—Complexes comprising metals of Group VIII as the central metal
- B01J2531/84—Metals of the iron group
- B01J2531/847—Nickel
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- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种用于长链烯烃烷基化制备高碳链烷基苯的离子液体催化剂及其制备方法,属于有机合成领域的催化剂制备技术。The invention relates to an ionic liquid catalyst used for the alkylation of long-chain olefins to prepare high-carbon chain alkylbenzenes and a preparation method thereof, belonging to the catalyst preparation technology in the field of organic synthesis.
背景技术Background technique
高碳链烷基苯是合成洗涤剂烷基苯磺酸钠的主要原料,是由甲苯(二甲苯、乙苯、苯等)与C16、C18、C20~24的长链烯烃,在强酸性催化剂作用下发生烷基化反应生产得到,强酸性催化剂常用的主要有AlCl3、HF、BF3、浓硫酸等,但这些催化剂大多具有较大的腐蚀性和毒性,尤其对设备腐蚀严重,投资较大、设备要求高,且存在产物后处理难、“三废”多等问题。因此,开发环境友好、腐蚀性低、可循环使用的酸性催化剂是大势所趋。High-carbon chain alkylbenzene is the main raw material of synthetic detergent sodium alkylbenzene sulfonate, which is composed of toluene (xylene, ethylbenzene, benzene, etc.) It is produced by alkylation reaction under the influence of AlCl 3 , HF, BF 3 , concentrated sulfuric acid, etc., but most of these catalysts are highly corrosive and toxic, especially for equipment, and the investment is relatively high. Large, high equipment requirements, and there are problems such as difficult product post-processing and many "three wastes". Therefore, the development of environmentally friendly, low-corrosion, and recyclable acidic catalysts is the general trend.
离子液体作为一种特殊形态的离子化合物,在有机合成反应上应用广泛,它作为溶剂、催化剂和模板剂等方面起了很重要的作用,在化学合成和化学工业应用方面有重大的意义。酸性离子液体,兼具固体酸和液体酸的许多优点,在酯化反应、烷基化反应等许多有机反应的应用中,提供并改进了适宜的反应条件,提高了反应转化率,降低了成本且环境友好。因此,离子液体在催化剂方面的应用受到了极大的关注,酸性离子液体可有效替代无机酸进行相应的催化反应。As a special form of ionic compound, ionic liquid is widely used in organic synthesis reactions. It plays a very important role as solvent, catalyst and template agent, and has great significance in chemical synthesis and chemical industry application. Acidic ionic liquid has many advantages of both solid acid and liquid acid. In the application of many organic reactions such as esterification reaction and alkylation reaction, it provides and improves the suitable reaction conditions, improves the reaction conversion rate and reduces the cost. And the environment is friendly. Therefore, the application of ionic liquids in catalysts has received great attention, and acidic ionic liquids can effectively replace inorganic acids for corresponding catalytic reactions.
近年来,三氯化铝与咪唑鎓盐或者烷基铵盐的结合制备氯铝酸型离子液体的制备方法的报道越来越多,中国专利CN1225617A报道了采用三氯化铝与含烷基的胺类有机盐结合制备了氯铝酸型离子液体催化剂,用于催化平均碳原子数C10以上的烯烃与平均碳原子数C6以上的氯代烷烃的烷基化反应;中国专利CN102703112A介绍了一种用添加剂改性的氯镓酸离子液体催化剂的制备方法,该催化剂用于催化丁烯与异丁烷的烷基化反应;中国专利CN106939173A介绍了一种硫酸和离子液体[BMIM][PF6]复合催化剂的制备方法,该催化剂用于催化异丁烷和C4烯烃烷基化;中国专利CN102516128A公开了采用Bronsted-Lewis酸性离子液体催化的二苯甲烷二氨基甲酸甲酯合成工艺,该离子液体催化剂具有较好的催化性能,但该催化剂在使用过程中存在结构不够稳定、循环使用性能差等问题。上述研究报道的催化剂大多是应用于低碳烯烃的烷基化反应,应用于长链烯烃烷基化反应的研究报道较少。因此,开发出一种用于长链烯烃烷基化制备高碳链烷基苯的离子液体催化剂具有较好的理论意义和应用前景。In recent years, there have been more and more reports on the preparation of chloroaluminate-type ionic liquids by combining aluminum trichloride with imidazolium salts or alkylammonium salts. Chinese patent CN1225617A reports the use of aluminum trichloride and alkyl-containing Chloroaluminate-type ionic liquid catalysts were prepared in combination with amine organic salts, which are used to catalyze the alkylation reaction of olefins with an average carbon number of C10 or more and chlorinated alkanes with an average carbon number of C6 or more; Chinese patent CN102703112A introduces a Preparation method of chlorogallate ionic liquid catalyst modified with additives, the catalyst is used to catalyze the alkylation reaction of butene and isobutane; Chinese patent CN106939173A introduces a sulfuric acid and ionic liquid [BMIM][PF 6 ] A method for preparing a composite catalyst, which is used to catalyze the alkylation of isobutane and C4 olefins; Chinese patent CN102516128A discloses a process for synthesizing methyl diphenylmethane dicarbamate catalyzed by Bronsted-Lewis acidic ionic liquid, the ionic liquid catalyst It has good catalytic performance, but the catalyst has problems such as unstable structure and poor recycling performance during use. Most of the catalysts reported in the above studies are applied to the alkylation reaction of light olefins, and there are few research reports on the alkylation reaction of long-chain olefins. Therefore, the development of an ionic liquid catalyst for the alkylation of long-chain olefins to prepare high-carbon-chain alkylbenzenes has good theoretical significance and application prospects.
发明内容Contents of the invention
技术问题:本发明的目的是提供一种用于长链烯烃烷基化制备高碳链烷基苯的离子液体催化剂及其制备方法,该催化剂是由双酸型离子液体与金属氯化物配合而得,双酸型离子液体是由磺酸型离子液体与路易斯酸进行阴离子交换制备而成,磺酸型离子液体是由离子液体前驱体与盐酸反应而得,离子液体前驱体是由烷基咪唑与烷烃磺内酯反应制得。Technical problem: The purpose of this invention is to provide a kind of ionic liquid catalyst and preparation method thereof for the alkylation of long-chain olefins to prepare high-carbon chain alkylbenzene. Obtained, bis-acid ionic liquid is prepared by anion exchange between sulfonic acid ionic liquid and Lewis acid, sulfonic acid ionic liquid is obtained by reacting ionic liquid precursor with hydrochloric acid, and ionic liquid precursor is made of alkylimidazole It can be obtained by reacting with alkanes sultones.
技术方案:本发明的一种制备高碳链烷基苯的离子液体催化剂是由双酸型离子液体与金属氯化物配合而得,双酸型离子液体是由磺酸型离子液体与路易斯酸进行阴离子交换制备而成,磺酸型离子液体是由离子液体前驱体与盐酸反应而得,离子液体前驱体是由烷基咪唑与烷烃磺内酯反应制得,该催化剂的结构通式为:Technical solution: An ionic liquid catalyst for the preparation of high-carbon chain alkylbenzene of the present invention is obtained by combining a bis-acid ionic liquid with a metal chloride, and the bis-acid ionic liquid is prepared by a sulfonic acid ionic liquid and a Lewis acid. It is prepared by anion exchange. The sulfonic acid type ionic liquid is obtained by the reaction of the ionic liquid precursor and hydrochloric acid. The ionic liquid precursor is prepared by the reaction of alkylimidazole and alkane sultone. The general structural formula of the catalyst is:
其中,R1为中的一种;where R1 is one of
R2为 R2 is
M1为金属Al或Fe;M2M3为金属Ni、Cu、Zn、Sn中的任意二种金属的组合;n为7~10。M 1 is metal Al or Fe; M 2 M 3 is a combination of any two metals in Ni, Cu, Zn and Sn; n is 7-10.
用于长链烯烃烷基化制备高碳链烷基苯的离子液体催化剂Ionic Liquid Catalysts for Alkylation of Long-Chain Olefins to High-carbon Alkanes
本发明的制备高碳链烷基苯的离子液体催化剂的制备方法为:The preparation method of the ionic liquid catalyst preparing high carbon chain alkylbenzene of the present invention is:
步骤a)室温下,将烷烃磺内酯与烷基咪唑加入反应釜,50℃~80℃下反应6~12h,降至室温后,静置分层,去除上层有机物得下层产物,每次按有机溶剂:下层产物的质量比为0.5:1~3:1,用有机溶剂洗涤下层产物1~3次,静置分层,去除有机溶剂洗涤层,洗涤后的下层产物在60℃~70℃下真空干燥2~6h,得离子液体前驱体;Step a) At room temperature, add alkane sultone and alkylimidazole to the reaction kettle, react at 50°C-80°C for 6-12 hours, after cooling down to room temperature, stand and separate layers, remove the upper layer of organic matter to obtain the lower layer product, press each time Organic solvent: the mass ratio of the lower layer product is 0.5:1~3:1, wash the lower layer product with organic solvent for 1~3 times, let it stand for stratification, remove the organic solvent washing layer, and wash the lower layer product at 60℃~70℃ Dry under vacuum for 2-6 hours to obtain the ionic liquid precursor;
步骤b)室温下,将步骤a)制得的离子液体前驱体溶于水,滴加盐酸,0.1~0.5h滴完后再反应0.1~1h,升温至80℃~90℃继续反应2~6h,70℃~80℃下真空除水2~3h,冷至室温,得磺酸型离子液体;Step b) At room temperature, dissolve the ionic liquid precursor prepared in step a) in water, add hydrochloric acid dropwise, react for 0.1~1h after dripping for 0.1~0.5h, raise the temperature to 80°C~90°C and continue the reaction for 2~6h , 70 ℃ ~ 80 ℃ vacuum dewatering 2 ~ 3h, cooled to room temperature, to obtain sulfonic acid type ionic liquid;
步骤c)室温下,将甲苯和步骤b)制得的磺酸型离子液体加入反应釜中,将路易斯酸分批加入反应釜中,1~3h内加完,反应0.5~1.5h,升温至80℃~100℃继续反应2~6h,冷却至室温,得双酸型离子液体;Step c) At room temperature, add toluene and the sulfonic acid-type ionic liquid prepared in step b) into the reactor, add the Lewis acid in batches to the reactor, complete the addition within 1 to 3 hours, react for 0.5 to 1.5 hours, and heat up to Continue to react at 80°C to 100°C for 2 to 6 hours, and cool to room temperature to obtain a bis-acid ionic liquid;
步骤d)在室温、N2保护下,将金属氯化物和步骤c)制得的双酸型离子液体加入反应釜中混匀,80℃~100℃下反应1~3h,冷却至室温,得用于长链烯烃烷基化制备高碳链烷基苯的离子液体催化剂。Step d) Add the metal chloride and the bis-acid ionic liquid prepared in step c) into the reaction kettle and mix them evenly at room temperature under the protection of N2 , react at 80°C-100°C for 1-3h, and cool to room temperature to obtain An ionic liquid catalyst for the alkylation of long-chain olefins to produce high-chain alkylbenzenes.
其中,in,
该制备方法步骤a)中所述的烷烃磺内酯为1,3-丙烷磺内酯或1,4-丁烷磺内酯,所述的烷基咪唑为1-丁基咪唑、1-戊基咪唑或1-己基咪唑中的一种,所述的有机溶剂为乙酸乙酯、乙醚或甲苯中的一种或者两者的组合。The alkane sultone described in step a) of the preparation method is 1,3-propane sultone or 1,4-butane sultone, and the described alkyl imidazole is 1-butylimidazole, 1-pentane sultone One of imidazole or 1-hexylimidazole, and the organic solvent is one of ethyl acetate, ether or toluene or a combination of both.
该制备方法步骤b)中所述的盐酸为20wt.%~30wt.%的盐酸水溶液。The hydrochloric acid described in step b) of the preparation method is a 20wt.%-30wt.% hydrochloric acid aqueous solution.
该制备方法步骤c)中所述路易斯酸为AlCl3或FeCl3,所述的金属氯化物为NiCl2、ZnCl2、CuCl2、CuCl、SnCl2、SnCl4中的任意两种的组合。The Lewis acid in step c) of the preparation method is AlCl 3 or FeCl 3 , and the metal chloride is a combination of any two of NiCl 2 , ZnCl 2 , CuCl 2 , CuCl, SnCl 2 , and SnCl 4 .
该制备方法步骤a)中,所述烷烃磺内酯:烷基咪唑的摩尔比为1:1~2:1。In step a) of the preparation method, the molar ratio of the alkane sultone:alkylimidazole is 1:1˜2:1.
该制备方法所述步骤b)中,所述水:离子液体前驱体的质量比为2:1~5:1;所述盐酸:离子液体前躯体的质量比为0.1:1~0.4:1。In step b) of the preparation method, the mass ratio of water:ionic liquid precursor is 2:1-5:1; the mass ratio of hydrochloric acid:ionic liquid precursor is 0.1:1-0.4:1.
该制备方法所述步骤c)中甲苯:磺酸型离子液体的体积比为1:1~3:1,路易斯酸:磺酸型离子液体的摩尔比为1:1~4:1。In the step c) of the preparation method, the volume ratio of toluene:sulfonic acid type ionic liquid is 1:1-3:1, and the molar ratio of Lewis acid:sulfonic acid type ionic liquid is 1:1-4:1.
该制备方法所述步骤d)中,金属氯化物:双酸型离子液体的质量比为0.001:1~0.01:1。In step d) of the preparation method, the mass ratio of metal chloride:bisacid-type ionic liquid is 0.001:1˜0.01:1.
有益效果:本发明的目的是提供一种用于长链烯烃烷基化制备高碳链烷基苯的离子液体催化剂及其制备方法,该催化剂是由双酸型离子液体与金属氯化物配合而得,双酸型离子液体是由磺酸型离子液体与路易斯酸进行阴离子交换制备而成,磺酸型离子液体是由离子液体前驱体与盐酸反应而得,离子液体前驱体是由烷基咪唑与烷烃磺内酯反应制得。本发明的特点是:Beneficial effect: the object of the present invention is to provide a kind of ionic liquid catalyst and preparation method thereof for the alkylation of long-chain olefins to prepare high-carbon chain alkylbenzene, the catalyst is formed by the coordination of bis-acid ionic liquid and metal chloride Obtained, bis-acid ionic liquid is prepared by anion exchange between sulfonic acid ionic liquid and Lewis acid, sulfonic acid ionic liquid is obtained by reacting ionic liquid precursor with hydrochloric acid, and ionic liquid precursor is made of alkylimidazole It can be obtained by reacting with alkanes sultones. The features of the present invention are:
(1)该离子液体催化剂由烷基咪唑、烷烃磺内酯、路易斯酸和金属氯化物合成,具有布朗斯特酸性、路易斯酸性的双酸型特性,两种不同类型的酸性功能位之间的协同作用,可以更好地提高反应活性,反应转化率也大大提高。(1) The ionic liquid catalyst is synthesized from alkylimidazole, alkane sultone, Lewis acid and metal chloride, and has the double-acid characteristics of Bronsted acidity and Lewis acidity. The synergistic effect can better improve the reaction activity, and the reaction conversion rate is also greatly improved.
(2)该离子催化剂的阴离子部分含有三种金属,可以通过调变金属种类、金属价态及金属组合方式,实现对离子催化剂催化性能的调控,如:Al3+、Zn2+、Cu+三种价态金属组合在一起可以形成带有空配位点的“倒圆锥”结构,这个结构具有较高的结构稳定性,从而离子催化剂的结构稳定性明显提高,因此较大提高催化剂的使用寿命,除此之外,该结构中的空配位点会优先与烯烃发生配位,起到了稳定烯烃的作用,降低副反应的发生,提高了催化选择性和产品收率。(2) The anion part of the ionic catalyst contains three kinds of metals, and the catalytic performance of the ionic catalyst can be adjusted by adjusting the metal type, metal valence state and metal combination, such as: Al 3+ , Zn 2+ , Cu + The combination of three valence metals can form an "inverted cone" structure with empty coordination sites. This structure has high structural stability, so the structural stability of the ion catalyst is significantly improved, so the use of the catalyst is greatly improved. In addition, the vacant coordination sites in the structure will preferentially coordinate with olefins, which plays a role in stabilizing olefins, reducing the occurrence of side reactions, and improving catalytic selectivity and product yield.
具体实施方式Detailed ways
本发明是提供一种用于长链烯烃烷基化制备高碳链烷基苯的离子液体催化剂及其制备方法,该催化剂是由双酸型离子液体与金属氯化物配合而得,双酸型离子液体是由磺酸型离子液体与路易斯酸进行阴离子交换制备而成,磺酸型离子液体是由离子液体前驱体与盐酸反应而得,离子液体前驱体是由烷基咪唑与烷烃磺内酯反应制得。The present invention provides an ionic liquid catalyst for the alkylation of long-chain olefins to prepare high-carbon-chain alkylbenzenes and a preparation method thereof. Ionic liquids are prepared by anion exchange between sulfonic acid-type ionic liquids and Lewis acids. Sulfonic acid-type ionic liquids are obtained by reacting ionic liquid precursors with hydrochloric acid. The reaction is made.
用于长链烯烃烷基化制备高碳链烷基苯的离子液体催化剂的制备方法为:The preparation method of the ionic liquid catalyst used for the alkylation of long-chain olefins to prepare high-carbon chain alkylbenzenes is as follows:
步骤a)室温下,按烷烃磺内酯:烷基咪唑的摩尔比为1:1~2:1,将烷基咪唑和烷烃磺内酯加入反应釜,50℃~80℃下反应6~12h,降至室温后,静置分层,去除上层有机物得下层产物,每次按有机溶剂:下层产物的质量比为0.5:1~3:1,用有机溶剂洗涤下层产物1~3次,静置分层,去除有机溶剂洗涤层,洗涤后的下层产物在60℃~70℃下真空干燥2~6h,得离子液体前驱体;Step a) At room temperature, according to the molar ratio of alkane sultone: alkylimidazole is 1:1~2:1, add alkylimidazole and alkane sultone into the reaction kettle, and react at 50°C~80°C for 6~12h , after cooling down to room temperature, let stand for stratification, remove the organic matter in the upper layer to obtain the lower layer product, each time according to the mass ratio of organic solvent: lower layer product is 0.5:1 to 3:1, wash the lower layer product with organic solvent 1 to 3 times, statically Put layers into layers, remove the organic solvent washing layer, and vacuum dry the washed lower layer product at 60°C-70°C for 2-6 hours to obtain the ionic liquid precursor;
步骤b)室温下,按水:离子液体前驱体的质量比为2:1~5:1,将步骤a)制得的离子液体前驱体溶于水,按盐酸:离子液体前躯体的质量比为0.1:1~0.4:1,滴加盐酸,0.1~0.5h滴完后再反应0.1~1h,升温至80℃~90℃继续反应2~6h,70℃~80℃下真空除水2~3h,得磺酸型离子液体;step b) at room temperature, according to the mass ratio of water: ionic liquid precursor is 2:1 ~ 5:1, the ionic liquid precursor prepared in step a) is dissolved in water, according to the mass ratio of hydrochloric acid: ionic liquid precursor 0.1:1~0.4:1, add hydrochloric acid dropwise, react for 0.1~1h after dripping for 0.1~0.5h, raise the temperature to 80℃~90℃ and continue the reaction for 2~6h, remove water under vacuum at 70℃~80℃ for 2~ 3h, get sulfonic acid type ionic liquid;
步骤c)室温下,按甲苯:磺酸型离子液体的体积比为1:1~3:1,将甲苯和步骤b)制得的磺酸型离子液体加入反应釜中,按路易斯酸:磺酸型离子液体的摩尔比为1:1~4:1,将路易斯酸分批加入反应釜,1~3h内加完,反应0.5~1.5h,升温至80℃~100℃继续反应2~6h,冷却至室温,得双酸型离子液体;Step c) At room temperature, according to the volume ratio of toluene: sulfonic acid type ionic liquid is 1:1 ~ 3:1, add toluene and the sulfonic acid type ionic liquid prepared in step b) into the reaction kettle, according to Lewis acid: sulfonic acid type ionic liquid The molar ratio of the acid-type ionic liquid is 1:1-4:1. Add the Lewis acid to the reactor in batches, and finish adding within 1-3 hours. React for 0.5-1.5 hours, then raise the temperature to 80°C-100°C and continue the reaction for 2-6 hours. , cooled to room temperature to obtain a bis-acid ionic liquid;
步骤d)在室温、N2保护下,按金属氯化物:双酸型离子液体质量比为0.001:1~0.01:1,将金属氯化物和步骤c)制得的双酸型离子液体加入反应釜中混匀,80℃~100℃下反应1~3h,冷却至室温,得用于长链烯烃烷基化制备高碳链烷基苯的离子液体催化剂。Step d) At room temperature and under the protection of N2 , according to the mass ratio of metal chloride: bis-acid type ionic liquid of 0.001:1 to 0.01:1, adding the metal chloride and the bis-acid type ionic liquid prepared in step c) to react Mix in the still, react at 80°C-100°C for 1-3h, and cool to room temperature to obtain an ionic liquid catalyst for the alkylation of long-chain olefins to prepare high-chain alkylbenzenes.
上述用于长链烯烃烷基化制备高碳链烷基苯的离子液体催化剂制备方法步骤a)中所述的烷烃磺内酯为1,3-丙烷磺内酯或1,4-丁烷磺内酯,所述的烷基咪唑为1-丁基咪唑、1-戊基咪唑、1-己基咪唑中的一种,所述的有机溶剂为乙酸乙酯、乙醚、甲苯中的一种或者两种的组合;制备方法步骤b)中所述的盐酸为20wt.~30wt.%的盐酸水溶液;制备方法步骤c)中所述路易斯酸为AlCl3或FeCl3,所述的金属氯化物为NiCl2、ZnCl2、CuCl2、CuCl、SnCl2、SnCl4中的两种的组合。The alkane sultone described in step a) of the above-mentioned preparation method of an ionic liquid catalyst for the alkylation of long-chain olefins to prepare high-carbon chain alkylbenzenes is 1,3-propane sultone or 1,4-butane sultone lactone, the alkyl imidazole is one of 1-butyl imidazole, 1-pentylimidazole, and 1-hexylimidazole, and the organic solvent is one or both of ethyl acetate, ether, and toluene. The combination of species; the hydrochloric acid described in the preparation method step b) is 20wt.~30wt.% hydrochloric acid aqueous solution; the Lewis acid described in the preparation method step c) is AlCl3 or FeCl3 , and the described metal chloride is NiCl 2. A combination of two of ZnCl 2 , CuCl 2 , CuCl, SnCl 2 , and SnCl 4 .
催化剂烷基化性能评价:Catalyst Alkylation Performance Evaluation:
按离子液体催化剂:长链烯烃的质量比为0.1:1,甲苯(或二甲苯或乙苯或苯):长链烯烃的摩尔比为10:1,将甲苯(或二甲苯或乙苯或苯)、长链烯烃和离子液体催化剂加入反应釜中,50℃下反应0.5h,冷却至室温,静置分层后,取上层有机物进行蒸馏以除去原料中未反应的甲苯(或二甲苯或乙苯或苯),得到高碳链烷基苯。考察高碳链烷基苯的溴值。Press ionic liquid catalyst: the mass ratio of long-chain olefin is 0.1:1, toluene (or xylene or ethylbenzene or benzene): the molar ratio of long-chain olefin is 10:1, will toluene (or xylene or ethylbenzene or benzene ), long-chain olefins and ionic liquid catalysts were added to the reactor, reacted at 50°C for 0.5h, cooled to room temperature, and after standing for stratification, the organic matter in the upper layer was taken for distillation to remove unreacted toluene (or xylene or ethyl alcohol) in the raw material. Benzene or benzene), to obtain high-carbon chain alkylbenzene. Investigate the bromine value of high carbon chain alkylbenzene.
按GB/T1815测定苯类产品的溴价X,计算公式为:Determine the bromine value X of benzene products according to GB/T1815, and the calculation formula is:
X(g/100mL)=(V1-V2)×0.008÷5×100X(g/100mL)=(V 1 -V 2 )×0.008÷5×100
V1:空白试验时所消耗的硫代硫酸钠标准溶液量,mL;V 1 : the amount of sodium thiosulfate standard solution consumed during the blank test, mL;
V2:滴定试验时所消耗的硫代硫酸钠标准溶液量,mL;V 2 : the amount of sodium thiosulfate standard solution consumed during the titration test, mL;
0.008:1mL硫代硫酸钠标准溶液量相当于溴的量,g。0.008: The amount of 1mL sodium thiosulfate standard solution is equivalent to the amount of bromine, g.
本发明的用于长链烯烃烷基化制备高碳链烷基苯的离子液体催化剂是由双酸型离子液体与金属氯化物配合而得,双酸型离子液体是由磺酸型离子液体与路易斯酸进行阴离子交换制备而成,磺酸型离子液体是由离子液体前驱体与盐酸反应而得,离子液体前驱体是由烷基咪唑与烷烃磺内酯反应制得。The ionic liquid catalyst used for the alkylation of long-chain olefins to prepare high-carbon chain alkylbenzenes of the present invention is obtained by coordinating a bis-acid type ionic liquid with a metal chloride, and the bis-acid type ionic liquid is obtained by combining a sulfonic acid type ionic liquid with a metal chloride The Lewis acid is prepared by anion exchange, and the sulfonic acid-type ionic liquid is prepared by reacting an ionic liquid precursor with hydrochloric acid, and the ionic liquid precursor is prepared by reacting an alkylimidazole with an alkane sultone.
实施例1:Example 1:
25℃下,将12.214g的1,3-丙烷磺内酯和12.418g的1-丁基咪唑加入反应釜中,50℃下反应6h,降至室温后,静置分层,下层产物用12.316g乙酸乙酯洗涤,洗涤后的下层产物在60℃真空干燥2h,得离子液体前驱体;在25℃下,将上述的离子液体前驱体全部溶于49.265g水中,滴加2.463g的20wt.%的盐酸水溶液,6分钟内滴完后再反应6分钟,升温至80℃继续反应2h,70℃下真空除水2h,得磺酸型离子液体;25℃下,将上述磺酸型离子液体全部加入反应釜中,加入30mL甲苯,再将13.333g的AlCl3分批加入反应釜中,1h内加完后,反应0.5h,升温至80℃继续反应2h,冷却至室温,得双酸型离子液体;在25℃、N2保护下,将0.0380g的NiCl2和0.0380g的ZnCl2加入上述的双酸型离子液体中,混匀,80℃下反应1h,冷却至室温,得用于长链烯烃烷基化制备高碳链烷基苯的离子液体催化剂。At 25°C, add 12.214g of 1,3-propane sultone and 12.418g of 1-butylimidazole into the reaction kettle, react at 50°C for 6h, after cooling down to room temperature, let stand to separate layers, and the lower layer product is mixed with 12.316 g of ethyl acetate was washed, and the washed lower layer product was vacuum-dried at 60°C for 2h to obtain an ionic liquid precursor; at 25°C, all the above-mentioned ionic liquid precursors were dissolved in 49.265g of water, and 2.463g of 20wt. % hydrochloric acid aqueous solution, after dripping within 6 minutes, react for 6 minutes, raise the temperature to 80°C and continue the reaction for 2h, remove water under vacuum for 2h at 70°C, and obtain a sulfonic acid ionic liquid; at 25°C, the above sulfonic acid ionic liquid Put everything into the reaction kettle, add 30mL of toluene, then add 13.333g of AlCl 3 into the reaction kettle in batches, after adding within 1h, react for 0.5h, raise the temperature to 80°C and continue the reaction for 2h, cool to room temperature, and obtain the bis-acid type Ionic liquid; under the protection of N2 at 25°C, add 0.0380g of NiCl2 and 0.0380g of ZnCl2 into the above-mentioned bis-acid type ionic liquid, mix well, react at 80°C for 1h, cool to room temperature, and obtain Ionic liquid catalysts for the alkylation of long-chain olefins to high-chain alkylbenzenes.
将92.138g甲苯、25.200g十八烯和2.520g的离子液体催化剂加入反应釜中,50℃下反应0.5h,冷却至室温,静置分层后,取上层有机物进行蒸馏以除去原料中未反应的甲苯,得到长链烷基苯。该长链烷基苯的溴值为0.071g/100mL。Add 92.138g of toluene, 25.200g of octadecene and 2.520g of ionic liquid catalyst into the reaction kettle, react at 50°C for 0.5h, cool to room temperature, and after standing to separate layers, take the upper organic matter and carry out distillation to remove unreacted raw materials. of toluene to obtain long-chain alkylbenzenes. The bromine value of this long-chain alkylbenzene was 0.071 g/100 mL.
实施例2:Example 2:
25℃下,将27.234g的1,4-丁烷磺内酯和13.821g的1-戊基咪唑加入反应釜中,80℃下反应12h,降至室温后,静置分层,下层产物用82.314g乙醚洗涤3次,洗涤后的下层产物在70℃真空干燥6h,得离子液体前驱体;25℃下,将上述的离子液体前驱体全部溶于137.190g水中,滴加10.976g的30wt.%的盐酸水溶液,0.5h滴完后再反应1h,升温至90℃继续反应6h,80℃下真空除水3h,得磺酸型离子液体;25℃下,将上述的磺酸型离子液体全部加入反应釜中,加入90mL甲苯,将48.661g的FeCl3分批加入反应釜中,3h加完后,反应1.5h,升温至100℃继续反应6h,冷却至室温,得双酸型离子液体;在25℃、N2保护下,将0.924g的CuCl2和0.924g的CuCl加入上述的双酸型离子液体中,混匀,100℃下反应3h,冷却至室温,得用于长链烯烃烷基化制备高碳链烷基苯的离子液体催化剂。At 25°C, add 27.234g of 1,4-butane sultone and 13.821g of 1-pentylimidazole into the reaction kettle, and react at 80°C for 12h. 82.314g of diethyl ether was washed three times, and the washed lower layer product was vacuum-dried at 70°C for 6h to obtain an ionic liquid precursor; at 25°C, all the above-mentioned ionic liquid precursors were dissolved in 137.190g of water, and 10.976g of 30wt. % hydrochloric acid aqueous solution, after 0.5h of dripping, react for 1h, heat up to 90°C and continue to react for 6h, and vacuum remove water for 3h at 80°C to obtain sulfonic acid ionic liquid; at 25°C, all the above sulfonic acid ionic liquid Put it into the reaction kettle, add 90mL of toluene, add 48.661g of FeCl3 into the reaction kettle in batches, after 3h of addition, react for 1.5h, raise the temperature to 100°C and continue the reaction for 6h, cool to room temperature, and obtain the bis-acid ionic liquid; Add 0.924g of CuCl 2 and 0.924g of CuCl to the above-mentioned bis-acid ionic liquid at 25°C under the protection of N2 , mix well, react at 100°C for 3 hours, and cool to room temperature to obtain long-chain alkenes Ionic liquid catalysts for the preparation of high-carbon chain alkylbenzenes.
将106.2g二甲苯、22.400g十六烯和2.240g的离子液体催化剂加入反应釜中,50℃下反应0.5h,冷却至室温,静置分层后,取上层有机物进行蒸馏以除去原料中未反应的二甲苯,得到高碳链烷基苯。该高碳链烷基苯的溴值为0.016g/100mL。Add 106.2g of xylene, 22.400g of hexadecene and 2.240g of ionic liquid catalyst into the reaction kettle, react at 50°C for 0.5h, cool to room temperature, and after standing for stratification, take the upper organic matter and carry out distillation to remove untreated Reaction of xylene, high carbon chain alkyl benzene. The bromine value of this higher carbon chain alkylbenzene is 0.016g/100mL.
实施例3:Example 3:
25℃下,将20.426g的1,4-丁烷磺内酯和15.224g的1-己基咪唑加入反应釜中,70℃下反应8h,降至室温后,静置分层,下层产物用43.261g甲苯洗涤2次,洗涤后的下层产物在65℃真空干燥4h,得离子液体前驱体;25℃下,将上述的离子液体前驱体全部溶于86.520g水中,滴加5.768g的25wt.%的盐酸水溶液,18分钟滴完后再反应0.5h,升温至85℃继续反应3h,75℃下真空除水2.5h,得磺酸型离子液体;25℃下,将上述的磺酸型离子液体全部加入反应釜中,加入60mL甲苯,将26.667g的AlCl3分批加入反应釜中,2h加完后,反应1h,升温至90℃继续反应4h,冷却至室温,得双酸型离子液体;在25℃、N2保护下,将0.278g的SnCl2和0.278g的SnCl4加入上述的双酸型离子液体中,混匀,90℃下反应2h,冷却至室温,得用于长链烯烃烷基化制备高碳链烷基苯的离子液体催化剂。At 25°C, add 20.426g of 1,4-butane sultone and 15.224g of 1-hexylimidazole into the reaction kettle, react at 70°C for 8h, after cooling down to room temperature, let stand and separate the layers, and the lower layer product is mixed with 43.261 g of toluene was washed twice, and the washed lower layer product was vacuum-dried at 65°C for 4 hours to obtain an ionic liquid precursor; at 25°C, all the above-mentioned ionic liquid precursors were dissolved in 86.520g of water, and 5.768g of 25wt.% Hydrochloric acid aqueous solution, after 18 minutes of dripping, react for 0.5h, heat up to 85°C and continue to react for 3h, remove water in vacuum at 75°C for 2.5h, and obtain sulfonic acid ionic liquid; Put everything into the reaction kettle, add 60mL of toluene, add 26.667g of AlCl3 into the reaction kettle in batches, after 2h of addition, react for 1h, raise the temperature to 90°C and continue the reaction for 4h, cool to room temperature, and obtain the bis-acid ionic liquid; Add 0.278g of SnCl 2 and 0.278g of SnCl 4 into the above-mentioned bis-acid ionic liquid at 25°C under the protection of N2 , mix well, react at 90°C for 2 hours, and cool to room temperature to obtain long-chain olefins An ionic liquid catalyst for the preparation of high-carbon chain alkylbenzenes by alkylation.
将106.2g乙苯、25.200g十八烯和2.520g的离子液体催化剂加入反应釜中,50℃下反应0.5h,冷却至室温,静置分层后,取上层有机物进行蒸馏以除去原料中未反应的乙苯,得到高碳链烷基苯。该高碳链烷基苯的溴值为0.002g/100mL。Add 106.2g of ethylbenzene, 25.200g of octadecene and 2.520g of ionic liquid catalyst into the reaction kettle, react at 50°C for 0.5h, cool to room temperature, and after standing to separate layers, take the upper layer of organic matter and carry out distillation to remove unsaturated ions in the raw materials. Reaction of ethylbenzene, high carbon chain alkylbenzene. The bromine value of this higher carbon chain alkylbenzene is 0.002g/100mL.
实施例4:Example 4:
25℃下,将20.426g的1,4-丁烷磺内酯和15.224g的1-己基咪唑加入反应釜中,80℃下反应10h,降至室温后,静置分层,下层产物用43.261g甲苯洗涤3次,洗涤后的下层产物在65℃真空干燥3h,得离子液体前驱体;25℃下,将上述的离子液体前驱体全部溶于57.680g水中,滴加5.768g的20wt.%的盐酸水溶液,12分钟滴完后再反应48分钟,升温至85℃继续反应4h,75℃下真空除水2h,得磺酸型离子液体;25℃下,将上述的磺酸型离子液体全部加入反应釜中,加入45mL甲苯,将26.667g的AlCl3分批加入反应釜中,2h加完后,反应1h,升温至80℃继续反应5h,冷却至室温,得双酸型离子液体;在25℃、N2保护下,将0.167g的SnCl2和0.111g的SnCl4加入上述的双酸型离子液体中,混匀,90℃下反应2h,冷却至室温,得用于长链烯烃烷基化制备高碳链烷基苯的离子液体催化剂。At 25°C, add 20.426g of 1,4-butane sultone and 15.224g of 1-hexylimidazole into the reaction kettle, react at 80°C for 10h, after cooling down to room temperature, let stand to separate layers, and the lower layer product is mixed with 43.261 g of toluene was washed 3 times, and the washed lower layer product was vacuum-dried at 65°C for 3 hours to obtain an ionic liquid precursor; at 25°C, all the above-mentioned ionic liquid precursors were dissolved in 57.680g of water, and 5.768g of 20wt.% Hydrochloric acid aqueous solution, after 12 minutes of dripping, react for 48 minutes, heat up to 85°C and continue to react for 4h, and vacuum remove water for 2h at 75°C to obtain sulfonic acid ionic liquid; at 25°C, all the above sulfonic acid ionic liquid Put it into the reaction kettle, add 45mL of toluene, add 26.667g of AlCl3 into the reaction kettle in batches, after 2h of addition, react for 1h, raise the temperature to 80°C and continue the reaction for 5h, cool to room temperature, and obtain the bis-acid ionic liquid; Add 0.167g of SnCl 2 and 0.111g of SnCl 4 into the above-mentioned bis-acid ionic liquid at 25°C under the protection of N 2 , mix well, react at 90°C for 2 hours, and cool to room temperature to obtain long-chain alkenes Ionic liquid catalysts for the preparation of high-carbon chain alkylbenzenes.
将78.114g苯、22.400g十六烯和2.240g的离子液体催化剂加入反应釜中,50℃下反应0.5h,冷却至室温,静置分层后,取上层有机物进行蒸馏以除去原料中未反应的苯,得到高碳链烷基苯。该高碳链烷基苯的溴值为0.014g/100mL。Add 78.114g of benzene, 22.400g of hexadecene and 2.240g of ionic liquid catalyst into the reaction kettle, react at 50°C for 0.5h, cool to room temperature, and after standing to separate layers, take the upper organic matter and carry out distillation to remove unreacted raw materials. Benzene to obtain high-carbon chain alkylbenzene. The bromine value of this higher carbon alkylbenzene was 0.014g/100mL.
实施例5:Example 5:
25℃下,将20.426g的1,4-丁烷磺内酯和12.418g的1-丁基咪唑加入反应釜中,80℃下反应7h,降至室温后,静置分层,下层产物用26.035g甲苯洗涤3次,洗涤后的下层产物在70℃真空干燥2h,得离子液体前驱体;25℃下,将上述的离子液体前驱体全部溶于52.071g水中,滴加4.927g的30wt.%的盐酸水溶液,18分钟滴完后再反应1h,升温至85℃继续反应6h,75℃下真空除水2.5h,得磺酸型离子液体;25℃下,将上述的磺酸型离子液体全部加入反应釜中,加入60mL甲苯,将26.667g的AlCl3分批加入反应釜中,2h加完后,反应1h,升温至80℃继续反应3h,冷却至室温,得双酸型离子液体;在25℃、N2保护下,将0.103g的SnCl2和0.103g的CuCl加入上述的双酸型离子液体中,混匀,90℃下反应3h,冷却至室温,得用于长链烯烃烷基化制备高碳链烷基苯的离子液体催化剂。At 25°C, add 20.426g of 1,4-butane sultone and 12.418g of 1-butylimidazole into the reaction kettle, react at 80°C for 7h, after cooling down to room temperature, let stand and separate, and use the lower layer product 26.035g of toluene was washed three times, and the washed lower layer product was vacuum-dried at 70°C for 2 hours to obtain an ionic liquid precursor; at 25°C, all the above-mentioned ionic liquid precursors were dissolved in 52.071g of water, and 4.927g of 30wt. % hydrochloric acid aqueous solution, after 18 minutes of dripping, react for 1 hour, heat up to 85°C and continue to react for 6h, remove water under vacuum for 2.5h at 75°C, and obtain sulfonic acid ionic liquid; Put everything into the reaction kettle, add 60mL of toluene, add 26.667g of AlCl3 into the reaction kettle in batches, after 2h of addition, react for 1h, raise the temperature to 80°C and continue the reaction for 3h, cool to room temperature, and obtain the bis-acid ionic liquid; Add 0.103g of SnCl 2 and 0.103g of CuCl to the above-mentioned bis-acid ionic liquid at 25°C under the protection of N 2 , mix well, react at 90°C for 3 hours, and cool to room temperature to obtain long-chain alkenes Ionic liquid catalysts for the preparation of high-carbon chain alkylbenzenes.
将92.138g甲苯、25.200g十八烯和2.520g的离子液体催化剂加入反应釜中,50℃下反应0.5h,冷却至室温,静置分层后,取上层有机物进行蒸馏以除去原料中未反应的甲苯,得到高碳链烷基苯。该高碳链烷基苯的溴值为0.004g/100mL。Add 92.138g of toluene, 25.200g of octadecene and 2.520g of ionic liquid catalyst into the reaction kettle, react at 50°C for 0.5h, cool to room temperature, and after standing to separate layers, take the upper organic matter and carry out distillation to remove unreacted raw materials. of toluene to obtain high-carbon chain alkylbenzene. The bromine value of the higher chain alkylbenzene was 0.004g/100mL.
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CN110157473A (en) * | 2019-04-08 | 2019-08-23 | 南京工业大学 | Method for synthesizing alkylate oil by catalyzing isopentane-propylene with double-acid ionic liquid |
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CN113769780A (en) * | 2021-10-08 | 2021-12-10 | 浙江吉泰新材料股份有限公司 | Magnetic microsphere-loaded bi-acidic ionic liquid catalyst and preparation and application thereof |
CN113769780B (en) * | 2021-10-08 | 2022-05-03 | 浙江吉泰新材料股份有限公司 | Magnetic microsphere-loaded bi-acidic ionic liquid catalyst and preparation and application thereof |
CN114011459A (en) * | 2021-11-16 | 2022-02-08 | 沈阳工业大学 | Titanium series double-acid type ionic liquid catalyst, preparation method and application |
CN114011459B (en) * | 2021-11-16 | 2023-12-26 | 沈阳工业大学 | Titanium double-acid ionic liquid catalyst and preparation method and application thereof |
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