CN109110778A - Hierarchical pore MTT structure molecular sieve prepared by controlling dealkalized lignin, preparation method and application - Google Patents
Hierarchical pore MTT structure molecular sieve prepared by controlling dealkalized lignin, preparation method and application Download PDFInfo
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- CN109110778A CN109110778A CN201811254095.4A CN201811254095A CN109110778A CN 109110778 A CN109110778 A CN 109110778A CN 201811254095 A CN201811254095 A CN 201811254095A CN 109110778 A CN109110778 A CN 109110778A
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- 229920005610 lignin Polymers 0.000 title claims abstract description 28
- 238000002360 preparation method Methods 0.000 title claims abstract description 18
- 239000002808 molecular sieve Substances 0.000 title abstract description 37
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 title abstract description 37
- 239000002149 hierarchical pore Substances 0.000 title abstract 3
- 238000006243 chemical reaction Methods 0.000 claims abstract description 24
- 239000003054 catalyst Substances 0.000 claims abstract description 17
- 239000011148 porous material Substances 0.000 claims abstract description 13
- 150000001335 aliphatic alkanes Chemical class 0.000 claims abstract description 8
- 239000000047 product Substances 0.000 claims description 53
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical group O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 28
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Inorganic materials [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 18
- 239000000377 silicon dioxide Substances 0.000 claims description 14
- 238000006317 isomerization reaction Methods 0.000 claims description 12
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 11
- 229910052710 silicon Inorganic materials 0.000 claims description 11
- 239000010703 silicon Substances 0.000 claims description 11
- 229910052681 coesite Inorganic materials 0.000 claims description 9
- 229910052906 cristobalite Inorganic materials 0.000 claims description 9
- 229910052682 stishovite Inorganic materials 0.000 claims description 9
- 229910052905 tridymite Inorganic materials 0.000 claims description 9
- 238000001354 calcination Methods 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 229910052782 aluminium Inorganic materials 0.000 claims description 5
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 5
- KWYUFKZDYYNOTN-UHFFFAOYSA-M potassium hydroxide Substances [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 5
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 4
- 150000002460 imidazoles Chemical class 0.000 claims description 3
- 239000000243 solution Substances 0.000 claims description 3
- CSDREXVUYHZDNP-UHFFFAOYSA-N alumanylidynesilicon Chemical compound [Al].[Si] CSDREXVUYHZDNP-UHFFFAOYSA-N 0.000 claims description 2
- 239000004411 aluminium Substances 0.000 claims description 2
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 claims description 2
- 239000007864 aqueous solution Substances 0.000 claims description 2
- 229910052593 corundum Inorganic materials 0.000 claims description 2
- PWSKHLMYTZNYKO-UHFFFAOYSA-N heptane-1,7-diamine Chemical compound NCCCCCCCN PWSKHLMYTZNYKO-UHFFFAOYSA-N 0.000 claims description 2
- 230000035484 reaction time Effects 0.000 claims description 2
- 239000012265 solid product Substances 0.000 claims description 2
- 229910001845 yogo sapphire Inorganic materials 0.000 claims description 2
- HQABUPZFAYXKJW-UHFFFAOYSA-N butan-1-amine Chemical compound CCCCN HQABUPZFAYXKJW-UHFFFAOYSA-N 0.000 claims 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims 1
- 229910052739 hydrogen Inorganic materials 0.000 claims 1
- 239000001257 hydrogen Substances 0.000 claims 1
- 230000001105 regulatory effect Effects 0.000 abstract description 2
- 230000000052 comparative effect Effects 0.000 description 9
- DCAYPVUWAIABOU-UHFFFAOYSA-N hexadecane Chemical compound CCCCCCCCCCCCCCCC DCAYPVUWAIABOU-UHFFFAOYSA-N 0.000 description 8
- 238000000034 method Methods 0.000 description 8
- 239000002199 base oil Substances 0.000 description 7
- 230000015572 biosynthetic process Effects 0.000 description 7
- 239000013078 crystal Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 7
- 238000003786 synthesis reaction Methods 0.000 description 7
- 238000007670 refining Methods 0.000 description 6
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 5
- KDSNLYIMUZNERS-UHFFFAOYSA-N 2-methylpropanamine Chemical compound CC(C)CN KDSNLYIMUZNERS-UHFFFAOYSA-N 0.000 description 4
- 229910052799 carbon Inorganic materials 0.000 description 4
- 238000002425 crystallisation Methods 0.000 description 4
- 230000008025 crystallization Effects 0.000 description 4
- 238000011065 in-situ storage Methods 0.000 description 4
- 239000010687 lubricating oil Substances 0.000 description 4
- 239000003921 oil Substances 0.000 description 4
- 239000012188 paraffin wax Substances 0.000 description 4
- 230000032683 aging Effects 0.000 description 3
- 238000003556 assay Methods 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 229910000510 noble metal Inorganic materials 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 238000002336 sorption--desorption measurement Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- 229920002472 Starch Polymers 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 150000001721 carbon Chemical group 0.000 description 2
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000009826 distribution Methods 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 125000000524 functional group Chemical group 0.000 description 2
- DCAYPVUWAIABOU-NJFSPNSNSA-N hexadecane Chemical class CCCCCCCCCCCCCCC[14CH3] DCAYPVUWAIABOU-NJFSPNSNSA-N 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 229910052763 palladium Inorganic materials 0.000 description 2
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N phenol group Chemical group C1(=CC=CC=C1)O ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 2
- 229910052697 platinum Inorganic materials 0.000 description 2
- 239000010970 precious metal Substances 0.000 description 2
- 238000000197 pyrolysis Methods 0.000 description 2
- 238000001228 spectrum Methods 0.000 description 2
- 239000008107 starch Substances 0.000 description 2
- 235000019698 starch Nutrition 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 239000001993 wax Substances 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- KMWBBMXGHHLDKL-UHFFFAOYSA-N [AlH3].[Si] Chemical group [AlH3].[Si] KMWBBMXGHHLDKL-UHFFFAOYSA-N 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 239000012675 alcoholic extract Substances 0.000 description 1
- 239000012670 alkaline solution Substances 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 1
- 210000003850 cellular structure Anatomy 0.000 description 1
- 239000001913 cellulose Substances 0.000 description 1
- 229920002678 cellulose Polymers 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000008367 deionised water Substances 0.000 description 1
- 229910021641 deionized water Inorganic materials 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000009415 formwork Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 1
- 239000010931 gold Substances 0.000 description 1
- 229910052737 gold Inorganic materials 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 229920002521 macromolecule Polymers 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 238000001144 powder X-ray diffraction data Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 239000012498 ultrapure water Substances 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
- C01B39/02—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
- C01B39/04—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof using at least one organic template directing agent, e.g. an ionic quaternary ammonium compound or an aminated compound
-
- 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
- B01J29/7046—MTT-type, e.g. ZSM-23, KZ-1, ISI-4 or EU-13
-
- 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
- B01J29/72—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65 containing iron group metals, noble metals or copper
- B01J29/74—Noble metals
- B01J29/7492—MTT-type, e.g. ZSM-23, KZ-1, ISI-4 or EU-13
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
- C01B39/02—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
- C01B39/46—Other types characterised by their X-ray diffraction pattern and their defined composition
- C01B39/48—Other types characterised by their X-ray diffraction pattern and their defined composition using at least one organic template directing agent
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
- C07C5/22—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by isomerisation
- C07C5/27—Rearrangement of carbon atoms in the hydrocarbon skeleton
- C07C5/2767—Changing the number of side-chains
- C07C5/277—Catalytic processes
- C07C5/2775—Catalytic processes with crystalline alumino-silicates, e.g. molecular sieves
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- 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
- C10M105/00—Lubricating compositions characterised by the base-material being a non-macromolecular organic compound
- C10M105/02—Well-defined hydrocarbons
- C10M105/04—Well-defined hydrocarbons aliphatic
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2002/00—Crystal-structural characteristics
- C01P2002/70—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data
- C01P2002/72—Crystal-structural characteristics defined by measured X-ray, neutron or electron diffraction data by d-values or two theta-values, e.g. as X-ray diagram
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- C01P2006/16—Pore diameter
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- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2529/00—Catalysts comprising molecular sieves
- C07C2529/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites, pillared clays
- C07C2529/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- C07C2529/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups C07C2529/08 - C07C2529/65
- C07C2529/72—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups C07C2529/08 - C07C2529/65 containing iron group metals, noble metals or copper
- C07C2529/74—Noble metals
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- 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
- C10M2203/00—Organic non-macromolecular hydrocarbon compounds and hydrocarbon fractions as ingredients in lubricant compositions
- C10M2203/02—Well-defined aliphatic compounds
- C10M2203/0206—Well-defined aliphatic compounds used as base material
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- Chemical & Material Sciences (AREA)
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- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Crystallography & Structural Chemistry (AREA)
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Abstract
The invention discloses a molecular sieve with a hierarchical pore MTT structure, which contains mesopores and micropores, and the specific surface area of the molecular sieve is 400m2The pore diameter of the mesopores is 2-20nm, and the pore size of the micropores is 0.52nm multiplied by 0.45 nm. The invention also discloses a preparation method of the molecular sieve with the hierarchical pore MTT structure, which is regulated and controlled by dealkalized lignin, and application of the molecular sieve to a catalyst carrier in improving the yield of a single-branched chain isomerized product in a normal alkane hydroisomerization reaction.
Description
Technical field
The invention belongs to catalyst technical fields, and in particular to a kind of multi-stage porous MTT by the regulation preparation of dealkalize lignin
Structure molecular screen, Preparation method and use.
Background technique
In oil product, lubricating oil, jet fuel etc. are all the various properties focused under low temperature, especially condensation point, freezing point
Deng.In recent years, the hydrocarbon product that coal is obtained by Fischer-Tropsch Synthesis is cleaner, has the characteristics that no sulphur, nitrogen-free, low aromatic hydrocarbons,
It is attracted attention as the feedstock oil for manufacturing fuel, lube base oil etc..It is reduced for pour point from lubricating oil, it is undesirable that raw
At the isomers for having many branches, the isomerization of wax is wished to generate few branched isomer, especially when there is a branch in center
Pour point is lower.
Micropore MTT structure molecular screen carried metal active group is generally used for the isomerization dewaxing reaction of lube base oil
Divide the catalyst of the VIIIth race's elements such as Pt, Pd preparation.The pore size of MTT structure molecular screen is generally the left side 0.52nm × 0.45nm
The right side, structure limit the generation and diffusion of highly-branched chain isomerous product, cause isomerized products that secondary response occurs, that is, crack
Reaction, pyrolysis product promote the generation of carbon distribution, easy blocking catalyst duct；And only it is located at the active sites near molecular sieve aperture
Just work to the generation of double branched isomers.The isomerization reaction of long-chain normal paraffin (carbon atom number > 15) occurs mainly in
At the aperture of catalyst, being only located at the active sites near molecular sieve aperture can just work.Therefore, long chain alkane isomerization
High activated catalyst requires molecular sieve used to have more aperture number.The method for improving molecular sieve orifice number generally has
Two kinds: 1, preparing the molecular sieve of little crystal grain, 2, synthesis hierarchical porous structure molecular sieve.
Patent US7390763 B2 discloses a kind of preparation method of small crystallite MTT structure molecular screen and its in C10+Positive structure
Application in the isomerization-visbreaking of alkane can make target product yield improve 7.14% using small crystallite MTT structure molecular screen.Specially
Sharp 103153860 A of CN is proposed and is prepared small crystal grain molecular sieve in the case that amine component is not present in one kind, but MTT structure point
The cellular structure of son sieve causes isomerized products that secondary response occurs the generation and diffusion limitation of highly-branched chain isomerous product, that is, cracks
Reaction；Pyrolysis product promotes the generation of carbon distribution, easy blocking catalyst duct.
105645428 A of patent CN describes a kind of system of SSZ-32 molecular sieve with mesoporous-micropore graded structure
Preparation Method, this method by by raw material homogenize mixing after starch is added, be prepared into using aging, crystallization, calcining and other processes
To the SSZ-32 molecular sieve of graded structure, which can be improved isomerization in linear paraffin in hydroisomerization reaction
The content of highly-branched chain isomerous body in product, but single branched chain isomer product assay is still lower.105640607 A of patent CN is introduced
A kind of preparation method of the SSZ-23 molecular sieve with mesoporous-micropore graded structure, this method is also by the way that raw material is equal
Starch is added after matterization mixing, the SSZ-32 molecule of graded structure is prepared using aging, crystallization, calcining and other processes
Sieve, the molecular sieve are also that highly-branched chain isomerous body in isomerization product can be improved in hydroisomerization reaction in linear paraffin
Content, but single branched chain isomer product assay is still lower.
Above-mentioned molecular sieve catalyst carrier, activity, selectivity and stability in hydroisomerizing reaction are also not
Enough ideals, the specific surface area of especially molecular sieve are still less；For normal alkane hydro-refining isomery reaction, single branch in product is different
Structure product assay is still lower.
Lignin is a kind of how solid netted macromolecule organic rich in negative electricity group, and there are phenolic hydroxyl groups, alcohol on molecule
The functional groups such as hydroxyl, carboxyl are conducive to the modification of macromolecular structure.In nature, the reserves of lignin are only second to cellulose,
It is inexpensively, is easy to get, reproducible resource.Dealkalize lignin is the product that alkaline lignin obtains after sour neutralization precipitation.
The present invention is added dealkalize lignin in situ on the basis of microcellular structure molecular sieve for the first time and prepares in crystal and crystal
Between it is mesoporous, obtain multi-stage porous MTT structure molecular screen.The specific surface area of multi-stage porous MTT structure molecular screen is larger, in 400m2/g
More than, it is used for normal alkane hydro-refining isomery reaction, excellent activity, selectivity and stability is shown, product can be significantly improved
Middle list branched chain isomer product yield.
Summary of the invention
First aspect present invention discloses a kind of multi-stage porous MTT structure molecular screen, contains mesoporous and micropore, specific surface
Product is 400m2/ g or more, the mesoporous pore size are 2-20nm, and the pore size of the micropore is 0.52nm × 0.45nm.
Second aspect of the present invention discloses the preparation method of the multi-stage porous MTT structure molecular screen, includes the following steps:
(1) template, lye, silicon source, silicon source are added to the water uniformly mixed；
(2) dealkalize lignin is added in the mixed liquor obtained to step (1), is reacted at a certain temperature；
(3) solid product that step (2) obtains is washed to neutrality, is being calcined after dry, is cooled to room temperature to get to institute
The multi-stage porous MTT structure molecular screen stated.
Preferably, template described in step (1) is one or more of imidazole salts, isobutyl amine, 1,7- heptamethylene diamine；
Source of aluminium is one or more of 18 water and aluminum sulfate, Aluminum sol, silicon-aluminum sol；The silicon source is silica solution；It is described
Lye is NaOH or KOH aqueous solution.
Preferably, the molar ratio of the template, lye, silicon source, silicon source, lignin and water are as follows: SiO2/Al2O3, 15-
100；Template/SiO2, 0.01-0.3；H2O/SiO2, 10-80；OH-/SiO2, 0.05-0.7；Lignin/SiO2, 0.05-1.5.
Preferably, step (2) reaction condition are as follows: temperature is 150~180 DEG C, and the reaction time is 3~10 days.
Preferably, it is 600 DEG C or more that step (3) described calcination condition, which is temperature, and calcination time is 3~5 hours.
Third aspect present invention discloses purposes of the multi-stage porous MTT structure molecular screen for catalyst carrier.
Preferably, the multi-stage porous MTT structure molecular screen improves single branch in product in normal alkane hydro-refining isomery reaction
The yield of isomerized products.
Beneficial effects of the present invention:
1, multi-stage porous MTT structure molecular screen of the invention is graduation pore structure molecular sieve, and existing micropore has mesoporous, tool again
There are more orifice number, higher specific surface area and Kong Rong, biggish active sites accessibility, is loaded as catalyst carrier
The group VIIIs element such as metal active constituent Pt, Pd, can optimize the porous of porous catalyst and the reasonable disposition of active sites,
It has broad application prospects in the reaction that hydroisomerizing etc. needs acidic site.Especially it is used for the long-chain normal paraffin of the content of wax
Isomerization-visbreaking reaction needed for catalyst, show it is higher activity and stereoselectivity, can significantly improve in product
Single branched chain isomer product yield.
2, the present invention obtains specific surface area in 400m for the first time2The molecular sieve of/g or more is used for normal alkane hydro-refining isomery reaction,
Excellent activity and selectivity is shown, single branched product and more connect product object molar ratios significantly improve profit 12 or more
The quality of lubricating oil.
3, the preparation method of multi-stage porous MTT structure molecular screen of the invention in order to the aperture for making up micro porous molecular sieve it is small, anti-
The deficiencies of answering object and product diffusion limited and poor catalytic activity, the dealkalize lignin in situ for the first time that introduces is as template altogether, dealkalize
There are the modifications that the functional groups such as phenolic hydroxyl group, alcoholic extract hydroxyl group, carboxyl are conducive to macromolecular structure on lignin molecule.Under aging temperature
Spongelike structure itself is formed, while hydroxyl and silicon-aluminum structure interact, realizes the graduation of one-step synthesis method micropore-mesopore
The MTT molecular sieve of structure is prepared in situ out in crystal on the basis of microcellular structure, is abundant mesoporous between crystal, has higher
Specific surface area and Kong Rong.On the one hand can be used as mesoporous directed agents generates Jie on microporous base for the introducing of dealkalize lignin
Hole optimizes the porous of porous catalyst and the reasonable disposition of active sites, increases the orifice number and specific surface of molecular sieve
Product；Second is that the use of organic formwork agent can be reduced, reduce environmental pollution, reduce the preparation cost of catalyst, is conducive to more
The large-scale application of grade hole MTT molecular sieve.And the ratio being added by adjusting dealkalize lignin, it can regulate and control in grade porous molecular sieve
Jie's micropore ratio.And effect of the invention is not achieved using common lignin.
Detailed description of the invention
Fig. 1 is the powder xrd pattern of multi-stage porous MTT structure molecular screen made from comparative example and embodiment 1.
Fig. 2 is the N of multi-stage porous MTT structure molecular screen made from comparative example and embodiment 12Adsorption-desorption isothermal curve.
Fig. 3 is multi-stage porous MTT structure molecular screen made from micropore MTT structure molecular screen made from comparative example and embodiment 1
To the comparison diagram of hexadecane hydro-isomerization selectivity.
Fig. 4 is multi-stage porous MTT structure molecular screen made from micropore MTT structure molecular screen made from comparative example and embodiment 1
To the comparison diagram of branched chain isomer product and highly-branched chain isomerous product molar ratio single in hexadecane hydro-isomerization product.
Specific embodiment
In order to which technical characteristic of the invention, purpose and beneficial effect are more clearly understood, now to technology of the invention
Scheme carries out following detailed description, and the following examples embody the process that the present invention describes, but the invention is not limited to this
A little examples.
Embodiment 1:
1.53g imidazole salts, 22.5g high purity water, 12.0g potassium hydroxide solution (1mol/L) is weighed to be added in polytetrafluoro
In lining, stir evenly.It is molten for 50 7.62g silica solution and 2.5g sial that silica alumina ratio is added into above-mentioned alkaline solution again
Glue, 0.9g isobutyl amine, stir evenly.Dealkalize lignin is finally added, the mole of dealkalize lignin is lignin/SiO2=
0.5, after mixing evenly, reactant gel is fitted into band polytetrafluoroethyllining lining hydrothermal synthesis kettle, sealing, at autogenous pressures
175 DEG C, crystallization 8 days.
Crystallization product is taken out, cooling, centrifuge separation, and be washed with deionized water to neutrality, it is dry in 120 DEG C of baking ovens；So
After place it in Muffle furnace, 650 DEG C of calcining 6h to get arrive the multi-stage porous MTT structure molecular screen.
The XRD diffracting spectrum of obtained multi-stage porous MTT structure molecular screen as shown by the curve in figure 1, N2Adsorption-desorption etc.
Warm curve is as shown by the curves in figure 2.As shown in Figure 1, the molecular sieve product crystal form in situ that obtain after dealkalize lignin that is added does not have
It changes, is still MTT structure molecular screen；As shown in Figure 2, there is mesoporous presence in the molecular sieve that embodiment 1 obtains.
Obtained multi-stage porous MTT molecular sieve specific surface area is 410m2/ g, mesoporous pore size range are 2-20nm.
Embodiment 2:
Specific synthesis condition is similar to embodiment 1, but the mole that dealkalize lignin is added is dealkalize lignin/SiO2=
0.05.Obtained multi-stage porous MTT molecular sieve specific surface area is 420m2/ g, mesoporous pore size range are 2-20nm.
Embodiment 3:
Specific synthesis condition is similar to embodiment 1, but the mole that dealkalize lignin is added is dealkalize lignin/SiO2=
1.5.Obtained multi-stage porous MTT molecular sieve specific surface area is 430m2/ g, mesoporous pore size range are 2-20nm.
Embodiment 4
Specific synthesis condition is similar to embodiment 1, but silicon source is Aluminum sol, silica alumina ratio 65.Obtained multi-stage porous MTT points
Sub- sieve ratio surface area is 420m2/ g, mesoporous pore size range are 2-20nm.
Embodiment 5:
Specific synthesis condition is similar to embodiment 1, and calcination temperature is 700 DEG C.Obtained multi-stage porous MTT molecular sieve specific surface
Product is 156m2/ g, mesoporous pore size range are 2-20nm.
Comparative example:
Other than being added without dealkalize lignin, raw material is same as Example 1 with synthesis condition.Obtain micropore MTT structure
The XRD diffracting spectrum of molecular sieve as shown by the curve in figure 1, N2Adsorption-desorption isothermal curve is as shown by the curves in figure 2.
Embodiment 6: hexadecane hydro-refining isomery reaction
By the multi-stage porous MTT molecular sieve that above-described embodiment 1 obtains and the micropore MTT structure molecular screen that comparative example obtains difference
As carrier, carried noble metal Pt, load capacity 0.5wt% are applied in the hydro-refining isomery reaction of hexadecane, reaction pressure
5MPa, the results are shown in Table 1 for product analysis.As can be seen from Table 1, at the same reaction temperature, Pt/
The conversion ratio of multi-stage porous MTT structural molecule sieve catalyst and the conversion ratio and isomery of isomery amount ratio Pt/ micropore MTT structure molecular screen
Amount is substantially improved, and single branched chain isomer product significantly improves in product, and single branched product and highly branched chain product molar ratio are 270
At DEG C, by being increased to 15 or more less than 4 or less；Illustrate that multi-stage porous MTT structure molecular screen produced by the present invention is applied to N-alkanes
Hydrocarbon isomerization-visbreaking reaction in, can with high activity, with high selectivity be made isoparaffin mixture, significantly improve in product and singly prop up
The ratio between chain isomerism product and highly-branched chain isomerous product molar.
Stereoselectivity is as shown in figure 3, the ratio of single branched chain isomer product and highly-branched chain isomerous product is such as in isomerized products
Shown in Fig. 4.
1 catalytic performance test result of table
"≤C in [remarks] table 115/ wt% " indicates the gross mass point of substance of the carbon atom number less than or equal to 15 in product
Number；" isomery C16/ wt% " indicates the total mass fraction of hexadecane isomers in product；" stereoselectivity/% " indicates reaction
Object selectively produces the percentage of hexadecane isomers；Single branched product/more connect product objects indicate single branched product in product
With highly branched chain product molar ratio.
Embodiment 7: the isomerization dewaxing of n-alkane
By the multi-stage porous MTT molecular sieve that above-described embodiment 1 obtains and the micropore MTT structure molecular screen that comparative example obtains difference
As carrier, carried noble metal Pt, load capacity 0.5wt% are applied to n-C20~n-C60Mix the isomerization dewaxing of n-alkane
It prepares in lube base oil.
As a result are as follows: embodiment 1 obtains Group III+lubrication oil base that the molecular sieve carried precious metals pt of multi-stage porous MTT is catalyzed
The yield of plinth oil is 50% or more；And under the same conditions, comparative example obtains micropore MTT structure molecular screen as carrier loaded expensive
Group III+lube base oil yield that Pt metal obtains is 30% or so.And embodiment 1 obtains multi-stage porous MTT molecular sieve and bears
Group III+lube base oil viscosity index (VI) that supported noble metal Pt is catalyzed can achieve 140 or more, keep higher receipts
Under rate, pour point obtains Group III+lubricating oil that micropore MTT structure molecular screen is obtained as carrier-supported precious metal Pt than comparative example
The reduction amplitude of base oil is up to 15% or more.Your illustrate produced by the present invention with multi-stage porous MTT structure molecular screen load gold
Belong to Pt catalyst n-alkane isomerization dewaxing reaction, can with high activity, with high selectivity be made lube base oil.
Claims (8)
1. a kind of multi-stage porous MTT structure molecular screen, which is characterized in that it contains mesoporous and micropore, specific surface area 400m2/g
More than, the mesoporous pore size is 2-20nm, and the pore size of the micropore is 0.52nm × 0.45nm.
2. a kind of preparation method of multi-stage porous MTT structure molecular screen according to claim 1, which is characterized in that including such as
Lower step:
(1) template, lye, silicon source, silicon source are added to the water uniformly mixed；
(2) dealkalize lignin is added in the mixed liquor obtained to step (1), is reacted at a certain temperature；
(3) solid product that step (2) obtains is washed to neutrality, is being calcined after dry, is cooled to room temperature described to get arriving
Multi-stage porous MTT structure molecular screen.
3. preparation method according to claim 2, which is characterized in that template described in step (1) is imidazole salts, different
One or more of butylamine, 1,7- heptamethylene diamine；Source of aluminium is 18 water and aluminum sulfate, Aluminum sol, one in silicon-aluminum sol
Kind is several；The silicon source is silica solution；The lye is NaOH or KOH aqueous solution.
4. preparation method according to claim 2, which is characterized in that the template, lye, silicon source, silicon source, lignin
With the molar ratio of water are as follows: SiO2/Al2O3, 15-100；Template/SiO2, 0.01-0.3；H2O/SiO2, 10-80；OH-/SiO2,
0.05-0.7；Lignin/SiO2, 0.05-1.5.
5. preparation method according to claim 2, which is characterized in that step (2) described reaction condition are as follows: temperature 150
~180 DEG C, the reaction time is 3~10 days.
6. preparation method according to claim 2, which is characterized in that it is 600 DEG C that step (3) described calcination condition, which is temperature,
More than, calcination time is 3~5 hours.
7. multi-stage porous MTT structure molecular screen is used for the purposes of catalyst carrier according to claim 1.
8. purposes according to claim 7, which is characterized in that the multi-stage porous MTT structure molecular screen faces hydrogen in normal alkane
The yield of single branched chain isomer product in product is improved in isomerization reaction.
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Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5332566A (en) * | 1993-07-16 | 1994-07-26 | Mobil Oil Corp. | Synthesis of crystalline ZSM-23 |
| CN108069435A (en) * | 2016-11-17 | 2018-05-25 | 中国石油化工股份有限公司 | A kind of Beta molecular sieves and its synthetic method with multistage pore canal |
| CN109336130A (en) * | 2018-10-26 | 2019-02-15 | 天津大学 | Hierarchical pore MTT structure molecular sieve prepared by glucan regulation and control, preparation method and application |
-
2018
- 2018-10-26 CN CN201811254095.4A patent/CN109110778B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5332566A (en) * | 1993-07-16 | 1994-07-26 | Mobil Oil Corp. | Synthesis of crystalline ZSM-23 |
| CN108069435A (en) * | 2016-11-17 | 2018-05-25 | 中国石油化工股份有限公司 | A kind of Beta molecular sieves and its synthetic method with multistage pore canal |
| CN109336130A (en) * | 2018-10-26 | 2019-02-15 | 天津大学 | Hierarchical pore MTT structure molecular sieve prepared by glucan regulation and control, preparation method and application |
Non-Patent Citations (3)
| Title |
|---|
| HIDESHI HATTORI等: "《固体酸催化剂》", 31 May 2016, 复旦大学出版社 * |
| XIAOYUN CHEN等: ""Synthesis and photocatalytic activity of mesoporous TiO2 nanoparticle using biological renewable resource of un-modified lignin as a template"", 《MICROPOROUS AND MESOPOROUS MATERIALS》 * |
| 张瑀健等: ""短轴纳米ZSM-23的合成及异构化功能"", 《高等化学学报》 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109336130A (en) * | 2018-10-26 | 2019-02-15 | 天津大学 | Hierarchical pore MTT structure molecular sieve prepared by glucan regulation and control, preparation method and application |
| CN109336130B (en) * | 2018-10-26 | 2021-07-13 | 天津大学 | Hierarchical pore MTT structure molecular sieve prepared by glucan regulation and control, preparation method and application |
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