JP7292426B2 - 水添石油樹脂の製造方法 - Google Patents
水添石油樹脂の製造方法 Download PDFInfo
- Publication number
- JP7292426B2 JP7292426B2 JP2021568790A JP2021568790A JP7292426B2 JP 7292426 B2 JP7292426 B2 JP 7292426B2 JP 2021568790 A JP2021568790 A JP 2021568790A JP 2021568790 A JP2021568790 A JP 2021568790A JP 7292426 B2 JP7292426 B2 JP 7292426B2
- Authority
- JP
- Japan
- Prior art keywords
- catalyst
- weight
- hydrogenation catalyst
- reaction
- nickel
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
- 239000011347 resin Substances 0.000 title claims description 60
- 229920005989 resin Polymers 0.000 title claims description 60
- 239000003208 petroleum Substances 0.000 title claims description 59
- 238000004519 manufacturing process Methods 0.000 title claims description 23
- 238000005984 hydrogenation reaction Methods 0.000 claims description 120
- 239000003054 catalyst Substances 0.000 claims description 117
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 claims description 99
- 229910052759 nickel Inorganic materials 0.000 claims description 44
- 238000006243 chemical reaction Methods 0.000 claims description 24
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 23
- 229910052717 sulfur Inorganic materials 0.000 claims description 23
- 239000011593 sulfur Substances 0.000 claims description 23
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims description 21
- 238000005899 aromatization reaction Methods 0.000 claims description 20
- 239000002904 solvent Substances 0.000 claims description 20
- 241001550224 Apha Species 0.000 claims description 17
- 238000000034 method Methods 0.000 claims description 16
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 12
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 12
- 239000002002 slurry Substances 0.000 claims description 10
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 7
- 229910052751 metal Inorganic materials 0.000 claims description 6
- 239000002184 metal Substances 0.000 claims description 6
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims description 6
- 229910000510 noble metal Inorganic materials 0.000 claims description 6
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 4
- IMNFDUFMRHMDMM-UHFFFAOYSA-N N-Heptane Chemical compound CCCCCCC IMNFDUFMRHMDMM-UHFFFAOYSA-N 0.000 claims description 4
- CTQNGGLPUBDAKN-UHFFFAOYSA-N O-Xylene Chemical compound CC1=CC=CC=C1C CTQNGGLPUBDAKN-UHFFFAOYSA-N 0.000 claims description 4
- OFBQJSOFQDEBGM-UHFFFAOYSA-N Pentane Chemical compound CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 4
- DIOQZVSQGTUSAI-UHFFFAOYSA-N decane Chemical compound CCCCCCCCCC DIOQZVSQGTUSAI-UHFFFAOYSA-N 0.000 claims description 4
- UAEPNZWRGJTJPN-UHFFFAOYSA-N methylcyclohexane Chemical compound CC1CCCCC1 UAEPNZWRGJTJPN-UHFFFAOYSA-N 0.000 claims description 4
- BKIMMITUMNQMOS-UHFFFAOYSA-N nonane Chemical compound CCCCCCCCC BKIMMITUMNQMOS-UHFFFAOYSA-N 0.000 claims description 4
- 230000008569 process Effects 0.000 claims description 4
- 239000008096 xylene Substances 0.000 claims description 4
- 239000004215 Carbon black (E152) Substances 0.000 claims description 3
- 239000010949 copper Substances 0.000 claims description 3
- 229930195733 hydrocarbon Natural products 0.000 claims description 3
- 150000002430 hydrocarbons Chemical group 0.000 claims description 3
- 239000000377 silicon dioxide Substances 0.000 claims description 3
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 2
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 claims description 2
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 2
- 229910052802 copper Inorganic materials 0.000 claims description 2
- 239000012530 fluid Substances 0.000 claims description 2
- 239000000395 magnesium oxide Substances 0.000 claims description 2
- GYNNXHKOJHMOHS-UHFFFAOYSA-N methyl-cycloheptane Natural products CC1CCCCCC1 GYNNXHKOJHMOHS-UHFFFAOYSA-N 0.000 claims description 2
- 230000007423 decrease Effects 0.000 description 18
- 230000003197 catalytic effect Effects 0.000 description 14
- 239000001257 hydrogen Substances 0.000 description 13
- 229910052739 hydrogen Inorganic materials 0.000 description 13
- 238000002360 preparation method Methods 0.000 description 9
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 8
- 230000000052 comparative effect Effects 0.000 description 8
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 7
- 125000003118 aryl group Chemical group 0.000 description 7
- 230000000694 effects Effects 0.000 description 7
- 239000002243 precursor Substances 0.000 description 7
- 239000007789 gas Substances 0.000 description 6
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 6
- 150000001875 compounds Chemical class 0.000 description 5
- 238000002156 mixing Methods 0.000 description 5
- JRZJOMJEPLMPRA-UHFFFAOYSA-N olefin Natural products CCCCCCCC=C JRZJOMJEPLMPRA-UHFFFAOYSA-N 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- 239000000843 powder Substances 0.000 description 5
- 239000002994 raw material Substances 0.000 description 5
- KAKZBPTYRLMSJV-UHFFFAOYSA-N Butadiene Chemical compound C=CC=C KAKZBPTYRLMSJV-UHFFFAOYSA-N 0.000 description 4
- 150000001336 alkenes Chemical class 0.000 description 4
- 239000003426 co-catalyst Substances 0.000 description 4
- 230000001747 exhibiting effect Effects 0.000 description 4
- 229910052757 nitrogen Inorganic materials 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 238000010926 purge Methods 0.000 description 4
- 239000000376 reactant Substances 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000005481 NMR spectroscopy Methods 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 239000013078 crystal Substances 0.000 description 3
- 239000012153 distilled water Substances 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- -1 olefin compounds Chemical class 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 229910052763 palladium Inorganic materials 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 2
- 229910021586 Nickel(II) chloride Inorganic materials 0.000 description 2
- 239000004820 Pressure-sensitive adhesive Substances 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- 230000032683 aging Effects 0.000 description 2
- 125000001931 aliphatic group Chemical group 0.000 description 2
- 239000012298 atmosphere Substances 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 239000012467 final product Substances 0.000 description 2
- 125000000524 functional group Chemical group 0.000 description 2
- 230000014509 gene expression Effects 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 239000003350 kerosene Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- QMMRZOWCJAIUJA-UHFFFAOYSA-L nickel dichloride Chemical compound Cl[Ni]Cl QMMRZOWCJAIUJA-UHFFFAOYSA-L 0.000 description 2
- 239000003921 oil Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- 230000009257 reactivity Effects 0.000 description 2
- 239000010948 rhodium Substances 0.000 description 2
- 229920006395 saturated elastomer Polymers 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000012360 testing method Methods 0.000 description 2
- 238000005160 1H NMR spectroscopy Methods 0.000 description 1
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 1
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- HECLRDQVFMWTQS-UHFFFAOYSA-N Dicyclopentadiene Chemical compound C1C2C3CC=CC3C1C=C2 HECLRDQVFMWTQS-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- KJTLSVCANCCWHF-UHFFFAOYSA-N Ruthenium Chemical compound [Ru] KJTLSVCANCCWHF-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 150000001242 acetic acid derivatives Chemical class 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001299 aldehydes Chemical class 0.000 description 1
- 150000001338 aliphatic hydrocarbons Chemical group 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 229910052786 argon Inorganic materials 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical group 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000002925 chemical effect Effects 0.000 description 1
- 239000007809 chemical reaction catalyst Substances 0.000 description 1
- 239000012295 chemical reaction liquid Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- XTVVROIMIGLXTD-UHFFFAOYSA-N copper(II) nitrate Chemical class [Cu+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O XTVVROIMIGLXTD-UHFFFAOYSA-N 0.000 description 1
- 238000005336 cracking Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- 238000009775 high-speed stirring Methods 0.000 description 1
- 125000004435 hydrogen atom Chemical group [H]* 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 150000002466 imines Chemical class 0.000 description 1
- 239000003622 immobilized catalyst Substances 0.000 description 1
- 230000003100 immobilizing effect Effects 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 239000000543 intermediate Substances 0.000 description 1
- 150000002576 ketones Chemical class 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 150000002816 nickel compounds Chemical class 0.000 description 1
- KBJMLQFLOWQJNF-UHFFFAOYSA-N nickel(ii) nitrate Chemical compound [Ni+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O KBJMLQFLOWQJNF-UHFFFAOYSA-N 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 239000010970 precious metal Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 229910052703 rhodium Inorganic materials 0.000 description 1
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 1
- 229910052707 ruthenium Inorganic materials 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000005245 sintering Methods 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- 229910052979 sodium sulfide Inorganic materials 0.000 description 1
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 description 1
- 238000002352 steam pyrolysis Methods 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 150000003467 sulfuric acid derivatives Chemical class 0.000 description 1
- 238000004227 thermal cracking Methods 0.000 description 1
- 238000011282 treatment Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J125/00—Adhesives based on homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and at least one being terminated by an aromatic carbocyclic ring; Adhesives based on derivatives of such polymers
- C09J125/02—Homopolymers or copolymers of hydrocarbons
-
- 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
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/06—Silicon, titanium, zirconium or hafnium; Oxides or hydroxides thereof
- B01J21/08—Silica
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/74—Iron group metals
- B01J23/755—Nickel
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/30—Catalysts, in general, characterised by their form or physical properties characterised by their physical properties
- B01J35/391—Physical properties of the active metal ingredient
- B01J35/393—Metal or metal oxide crystallite size
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/40—Catalysts, in general, characterised by their form or physical properties characterised by dimensions, e.g. grain size
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/61—Surface area
- B01J35/615—100-500 m2/g
-
- 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
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/60—Catalysts, in general, characterised by their form or physical properties characterised by their surface properties or porosity
- B01J35/64—Pore diameter
- B01J35/647—2-50 nm
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0201—Impregnation
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/03—Precipitation; Co-precipitation
- B01J37/031—Precipitation
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/06—Washing
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/08—Heat treatment
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/16—Reducing
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/16—Reducing
- B01J37/18—Reducing with gases containing free hydrogen
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/20—Sulfiding
-
- 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
- C08F2/00—Processes of polymerisation
- C08F2/01—Processes of polymerisation characterised by special features of the polymerisation apparatus used
-
- 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
- C08F240/00—Copolymers of hydrocarbons and mineral oils, e.g. petroleum resins
-
- 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
- C08F8/00—Chemical modification by after-treatment
- C08F8/04—Reduction, e.g. hydrogenation
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J145/00—Adhesives based on homopolymers or copolymers of compounds having no unsaturated aliphatic radicals in a side chain, and having one or more carbon-to-carbon double bonds in a carbocyclic or in a heterocyclic system; Adhesives based on derivatives of such polymers
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
- C09J157/00—Adhesives based on unspecified polymers obtained by reactions only involving carbon-to-carbon unsaturated bonds
- C09J157/02—Copolymers of mineral oil hydrocarbons
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Health & Medical Sciences (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Catalysts (AREA)
- Adhesives Or Adhesive Processes (AREA)
- Crystallography & Structural Chemistry (AREA)
Description
本出願は2019年6月3日付韓国特許出願第10-2019-0065352号および2020年6月1日付韓国特許出願第10-2020-0065848号に基づく優先権の利益を主張し、当該韓国特許出願の文献に開示されたすべての内容は本明細書の一部として含まれる。
本発明の一実施形態による、芳香族化度(Aromaticity)が10%以上であり、ASTM D1209に準じて測定したAPHA値が20以下である水添石油樹脂の製造方法は、石油樹脂と溶媒を混合した混合物に選択的水素化触媒および水素気体を投入して水素化反応を行う段階を含み、このとき前記選択的水素化触媒はニッケル(Ni)および硫黄(S)が担体に担持された担持触媒として、選択的水素化触媒の総重量に対して前記ニッケルを40~80重量%で含む。
前記選択的水素化触媒は活性金属としてニッケル(Ni)および助触媒として硫黄(S)を含み、前記ニッケルと硫黄は担体に担持された担持触媒である。
その後、前記乾燥された触媒を水素雰囲気で200~500℃、好ましくは300~450℃の温度で還元して活性化する段階をさらに含み得、活性化した担持触媒は0.1~20%の酸素が含まれた窒素混合ガスで不動化して粉末触媒を製造することができる。
前記ニッケル系選択的水素化触媒は粉末、粒子、顆粒の形態であり得、好ましくは粉末形態であり得る。
具体的には、ニッケルと助触媒として銅(Cu)を含む選択的水素化触媒;貴金属を含む選択的水素化触媒;およびニッケル金属の非選択的水素化触媒のうち1種以上をさらに含み得、前記貴金属はパラジウム(Pd)、白金(Pt)、ルテニウム(Ru)、およびロジウム(Rh)からなる群より選ばれる1種以上である。
また、前記水素化触媒は前記水素化反応対象物である石油樹脂100重量部に対して0.2~10重量部で投入する。前記水素化触媒の投入量が過度に少ないと触媒活性がろくに発現されず、投入量が過度に多いと投入量に対して生産性が落ちるため、このような観点から前記重量部の範囲で投入することが好ましい。好ましくは、前記水素化触媒は石油樹脂100重量部に対して0.2重量部以上、あるいは1重量部以上、あるいは3重量部以上、あるいは5重量部以上であり、10重量部以下、あるいは8重量部以下の含有量で投入することができる。
前記水素化反応時の温度は150~250℃であり得、好ましくは150℃以上、あるいは200℃以上であり、250℃以下であり得る。また、圧力は20~100barであり得、好ましくは20bar以上、あるいは50bar以上であり、100bar以下であり得る。水素化反応時の温度が150℃未満であるか、圧力が20bar未満の場合、十分な反応が起きない恐れがあり、また、反応温度が250℃を超えたり、圧力が100barを超える場合は過反応および副反応物生成の恐れがある。
準備例1:水素化触媒(A)
200m2/gの表面積と28nmの孔径を有する多孔性シリカ粉末1gと塩化ニッケル(243g/lニッケル)を蒸溜水に溶解した溶液50mlを沈殿容器に入れて攪拌しながら80℃に昇温した。80℃に到達した後、炭酸ナトリウム(175g/l)および硫化ナトリウム(15g/l)が含まれた溶液40mlをsyringe pumpを用いて1時間以内にすべて注入した。沈殿完了後のスラリーのpHは7.7であり、これを約1.5Lの蒸溜水で洗浄および濾過した後乾燥オーブンを用いて120℃で12時間以上乾燥した。これを小分した後水素雰囲気で400℃の温度で還元して活性化した。活性化した触媒は1%酸素が含まれた窒素混合ガスを用いて不動化してニッケル系の選択的水素化触媒を製造した。
触媒の総重量を基準として、不動化された触媒におけるニッケルの含有量は、62.5重量%、硫黄の含有量は4.5重量%、そしてシリカ担体の含有量は33重量%であり、硫黄/ニッケルモル比が0.13であり、前記ニッケルの平均結晶の大きさは5.1nm、触媒の平均粒子の大きさは5μmで測定された。
5% Pd/Carbon powder触媒(5R452,Johnson Matthey社製)を準備した。
Ni powder触媒を準備した。
前記準備例1~3で製造した触媒を用いて下記のように水素化反応を実施した。
実施例1
1Lの1,600RPMの高速攪拌Batchタイプの反応器に、原料として非水添石油樹脂(DCPD重合石油樹脂)と溶媒ExxsolTM D40(EXXONMOBIL CHEMICAL社製)を60:40の重量比で投入した後、前記準備例1で準備した触媒(A)を反応器に入れ、反応器を締結した後5kg/cm2のN2で3回パージし、H2で3回パージし、反応器圧力を10barとした。この時、前記触媒(A)は非水添石油樹脂100重量部に対して8重量部の量で投入した。
下記表1に記載されたように、反応器内の温度を250℃まで昇温させた後、反応圧力90barで加圧して水素化反応を行った。また、水素化反応の間反応圧力を90barに維持するために、水素を継続的に供給した。
実施例1で、準備例1の水素化触媒(A)と準備例3の水素化触媒(C)を10:90の重量比で混合して使用することを除いては、実施例1と同様の方法で水素化反応を行った。
触媒として0.5% Pd Pelletタイプの触媒を使用し、また、スラリー反応器の代わりに固定層反応器を用いて反応器内の反応温度250℃、圧力90bar、そして反応器内の滞留時間を2時間にして行うことを除いては前記実施例1と同様の方法で水素化反応を行った。
下記表1に記載されたように、触媒として準備例1での触媒(A)の代わりに前記準備例2で準備した触媒(B)を使用することを除いては、前記実施例1と同様の方法で水素化反応を行った。
下記表1に記載されたように、触媒として準備例1での触媒(A)の代わりに前記準備例3で準備した触媒(C)を使用することを除いては、前記実施例1と同様の方法で水素化反応を行った。
前記実施例および比較例の水素化反応に対してオレフィン結合に対する選択度テストを下記方法により行い、その結果を下記表1に示した。
前記実施例および比較例の水素化反応の反応物を溶媒CDCl3に2.5重量%の濃度に溶解させた後、1H-NMR分析(600MHz)を行い、下記数式1のように、重合体全体水素(proton)個数に対する芳香族(Aromatic)領域でのproton個数の比率から芳香族化度(Aromaticity,%)を求めた。
前記実施例および比較例の水素化反応の反応物に対してASTM D1209に準じてAPHA値を測定した。
APHA値は石油樹脂内のオレフィン含有量に比例してオレフィン結合が多いほど大きくなり、水素化反応前の石油樹脂のAPHA値は1,500であった。
ASTMD1544に従って評価した。
具体的には、試験管にサンプル10gを計量した後180℃オーブンで72時間の間Agingを行って、その後ガードナー比色計(Gardner color scale)で評価した。Gardner colorは合計18段階の色相があり、Gardner ColorでAgingされた樹脂の色相と最も類似の色相を肉眼で見つけて、該当色相の段階を記録した。
Claims (12)
- 石油樹脂と溶媒を混合した混合物に、選択的水素化触媒および水素気体を投入して水素化反応を行う段階を含み、
前記選択的水素化触媒はニッケルおよび硫黄が担体に担持された担持触媒であり、前記ニッケルを選択的水素化触媒の総重量に対して40~80重量%の含有量で含み、前記ニッケル1モルに対する硫黄のモル比が0.03~0.5であり、
芳香族化度が10%以上であり、ASTM D1209に準じて測定したAPHA値が20以下である、水添石油樹脂の製造方法。 - 前記担体はシリカ、アルミナ、マグネシアまたはこれらの混合物を含む、請求項1に記載の製造方法。
- 前記担体の含有量が前記選択的水素化触媒の総重量に対して10~50重量%である、請求項1に記載の製造方法。
- 前記選択的水素化触媒は前記石油樹脂100重量部に対して0.2~10重量部の量で使用される、請求項1に記載の製造方法。
- 前記水素化反応時、ニッケルと銅を含む選択的水素化触媒;貴金属を含む選択的水素化触媒;およびニッケル金属の非選択的水素化触媒からなる群より選ばれる1種以上の水素化触媒がさらに添加される、請求項1に記載の製造方法。
- 前記水素化触媒は前記選択的水素化触媒1重量部に対して0.1~10重量部で含まれる、請求項5に記載の製造方法。
- 前記溶媒はペンタン、ヘキサン、ヘプタン、ノナン、デカン、シクロヘキサン、メチルシクロヘキサン、ベンゼン、トルエン、キシレン、およびこれらの混合物からなる群より選ばれる炭化水素系溶媒である、請求項1に記載の製造方法。
- 前記溶媒は前記石油樹脂100重量部に対して40~80重量部で使用される、請求項1に記載の製造方法。
- 前記水素化反応がスラリー反応器で行われる、請求項1に記載の製造方法。
- 前記スラリー反応器は攪拌機が取り付けられたオートクレーブ反応器あるいは反応流体を循環させながら混合するループ方式の反応器である、請求項9に記載の製造方法。
- 前記水素化反応は150~250℃の温度、および20~100barの圧力で行われる、請求項1に記載の製造方法。
- 前記水素化反応は反応の間反応圧力が維持されるように水素気体を連続して投入して行われる、請求項1に記載の製造方法。
Applications Claiming Priority (5)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR20190065352 | 2019-06-03 | ||
KR10-2019-0065352 | 2019-06-03 | ||
KR10-2020-0065848 | 2020-06-01 | ||
KR1020200065848A KR102424826B1 (ko) | 2019-06-03 | 2020-06-01 | 수첨 석유수지의 제조 방법 |
PCT/KR2020/007110 WO2020246765A1 (ko) | 2019-06-03 | 2020-06-02 | 수첨 석유수지의 제조 방법 |
Publications (2)
Publication Number | Publication Date |
---|---|
JP2022532682A JP2022532682A (ja) | 2022-07-15 |
JP7292426B2 true JP7292426B2 (ja) | 2023-06-16 |
Family
ID=73652997
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2021568790A Active JP7292426B2 (ja) | 2019-06-03 | 2020-06-02 | 水添石油樹脂の製造方法 |
Country Status (6)
Country | Link |
---|---|
US (1) | US20220325011A1 (ja) |
EP (1) | EP3978539A4 (ja) |
JP (1) | JP7292426B2 (ja) |
CN (1) | CN113939548B (ja) |
TW (1) | TWI751574B (ja) |
WO (1) | WO2020246765A1 (ja) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113880969A (zh) * | 2021-11-08 | 2022-01-04 | 大连理工大学 | 一种冷聚石油树脂加氢制氢化石油树脂的方法 |
CN116273015A (zh) * | 2023-03-06 | 2023-06-23 | 上海迅凯新材料科技有限公司 | 石油树脂加氢催化剂及其制备方法和应用 |
CN116328770A (zh) * | 2023-03-23 | 2023-06-27 | 福州大学 | 负载型镍基催化剂及在dcpd石油树脂加氢中的应用 |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010504188A (ja) | 2006-09-20 | 2010-02-12 | 中国石油化工股▲分▼有限公司 | 選択的水素化のためのニッケル触媒 |
JP2018526482A (ja) | 2015-06-30 | 2018-09-13 | コーロン インダストリーズ インク | 石油樹脂、石油樹脂の製造方法及び接着剤組成物 |
Family Cites Families (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4695560A (en) * | 1985-10-01 | 1987-09-22 | Uop Inc. | Catalyst for the selective hydrogenation of diolefinic hydrocarbons |
GB8620395D0 (en) * | 1986-08-21 | 1986-10-01 | Exxon Research Patents Inc | Hydrogenated petroleum resins |
US4897175A (en) * | 1988-08-29 | 1990-01-30 | Uop | Process for improving the color and color stability of a hydrocarbon fraction |
NL9001536A (nl) * | 1990-07-05 | 1992-02-03 | Meern Bv Engelhard De | Zwavel-gepromoteerde nikkelkatalysator en bereiding daarvan. |
JP3289310B2 (ja) * | 1992-04-06 | 2002-06-04 | 東ソー株式会社 | 水添石油樹脂の製造方法 |
US6162350A (en) * | 1997-07-15 | 2000-12-19 | Exxon Research And Engineering Company | Hydroprocessing using bulk Group VIII/Group VIB catalysts (HEN-9901) |
US6755963B2 (en) * | 1997-07-15 | 2004-06-29 | Exxonmobil Chemical Patents Inc. | Hydrogenation process for hydrocarbon resins |
JP3379448B2 (ja) * | 1998-09-30 | 2003-02-24 | 荒川化学工業株式会社 | 水素化c9系石油樹脂の製造方法および当該製造方法により得られた水素化c9系石油樹脂 |
EP1101530A1 (en) * | 1999-11-19 | 2001-05-23 | Engelhard Corporation | Nickel-iron containing hydrogenation catalyst |
JP2002088116A (ja) * | 2000-09-14 | 2002-03-27 | Idemitsu Petrochem Co Ltd | 水素添加石油樹脂の製造法 |
US6657078B2 (en) * | 2001-02-07 | 2003-12-02 | Celanese International Corporation | Low energy carbonylation process |
JP4930741B2 (ja) * | 2001-03-21 | 2012-05-16 | 荒川化学工業株式会社 | 水素化石油樹脂の製造方法および当該製造方法に用いる水素化触媒 |
JP4481554B2 (ja) * | 2002-06-18 | 2010-06-16 | 出光興産株式会社 | 石油樹脂の水素化触媒及び水素化石油樹脂の製造方法 |
CN102002130B (zh) * | 2010-09-20 | 2012-07-25 | 中国海洋石油总公司 | 一种氢化碳九石油树脂的制备方法 |
CA2943027C (en) * | 2014-03-26 | 2022-03-22 | Maruzen Petrochemical Co., Ltd. | Method for producing hydrogenated petroleum resin |
KR101805892B1 (ko) * | 2015-06-30 | 2017-12-07 | 코오롱인더스트리 주식회사 | 수소첨가 석유수지, 이의 제조방법 및 용도 |
KR102327050B1 (ko) * | 2017-12-29 | 2021-11-15 | 한화솔루션 주식회사 | 선택적 수소화 방법 |
KR102311346B1 (ko) * | 2018-12-31 | 2021-10-08 | 한화솔루션 주식회사 | 수소화반응용 촉매 및 이의 제조방법 |
-
2020
- 2020-06-02 JP JP2021568790A patent/JP7292426B2/ja active Active
- 2020-06-02 WO PCT/KR2020/007110 patent/WO2020246765A1/ko unknown
- 2020-06-02 EP EP20818502.5A patent/EP3978539A4/en active Pending
- 2020-06-02 US US17/615,885 patent/US20220325011A1/en active Pending
- 2020-06-02 CN CN202080038204.8A patent/CN113939548B/zh active Active
- 2020-06-03 TW TW109118655A patent/TWI751574B/zh active
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010504188A (ja) | 2006-09-20 | 2010-02-12 | 中国石油化工股▲分▼有限公司 | 選択的水素化のためのニッケル触媒 |
JP2018526482A (ja) | 2015-06-30 | 2018-09-13 | コーロン インダストリーズ インク | 石油樹脂、石油樹脂の製造方法及び接着剤組成物 |
Also Published As
Publication number | Publication date |
---|---|
EP3978539A4 (en) | 2023-07-05 |
TW202106719A (zh) | 2021-02-16 |
EP3978539A1 (en) | 2022-04-06 |
US20220325011A1 (en) | 2022-10-13 |
TWI751574B (zh) | 2022-01-01 |
CN113939548B (zh) | 2024-04-26 |
WO2020246765A1 (ko) | 2020-12-10 |
CN113939548A (zh) | 2022-01-14 |
JP2022532682A (ja) | 2022-07-15 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP7053850B2 (ja) | 選択的水素化方法 | |
JP7292426B2 (ja) | 水添石油樹脂の製造方法 | |
JP7352631B2 (ja) | 水素化反応用触媒及びこれの製造方法 | |
US11987659B2 (en) | Hydrogenation reaction catalyst and preparation method therefor | |
JP7304976B2 (ja) | 水素化反応用触媒及びその製造方法 | |
EP3991843A1 (en) | Catalyst for hydrogenation reaction and preparation method for same | |
JP2024502831A (ja) | 耐硫黄性が向上した水素化反応用触媒及びその製造方法 | |
KR102424826B1 (ko) | 수첨 석유수지의 제조 방법 | |
KR102687289B1 (ko) | 수첨 석유수지의 연속적 제조 방법 | |
KR20220082575A (ko) | 수첨 석유수지의 연속적 제조 방법 | |
KR20220082574A (ko) | 수첨 석유수지의 연속적 제조 방법 | |
TW202231675A (zh) | 氫化石油樹脂的連續製備方法 | |
TW202330653A (zh) | 氫化石油樹脂的連續製備方法 | |
KR20220082576A (ko) | 수첨 석유수지의 연속적 제조 방법 | |
TW202330652A (zh) | 連續製備氫化石油樹脂的方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
A621 | Written request for application examination |
Free format text: JAPANESE INTERMEDIATE CODE: A621 Effective date: 20211117 |
|
A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20221109 |
|
A131 | Notification of reasons for refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A131 Effective date: 20221205 |
|
A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A523 Effective date: 20230213 |
|
TRDD | Decision of grant or rejection written | ||
A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20230508 |
|
A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20230606 |
|
R150 | Certificate of patent or registration of utility model |
Ref document number: 7292426 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |