CN108689416A - A kind of preparation method of rare earth metal Ce doping H-ZSM-34 molecular sieves - Google Patents
A kind of preparation method of rare earth metal Ce doping H-ZSM-34 molecular sieves Download PDFInfo
- Publication number
- CN108689416A CN108689416A CN201810507380.6A CN201810507380A CN108689416A CN 108689416 A CN108689416 A CN 108689416A CN 201810507380 A CN201810507380 A CN 201810507380A CN 108689416 A CN108689416 A CN 108689416A
- Authority
- CN
- China
- Prior art keywords
- zsm
- doping
- rare earth
- earth metal
- molecular sieves
- 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.)
- Pending
Links
Classifications
-
- 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
-
- 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
- B01J29/50—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the erionite or offretite type, e.g. zeolite T, as exemplified by patent document US2950952
- B01J29/505—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of the erionite or offretite type, e.g. zeolite T, as exemplified by patent document US2950952 containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead
-
- 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
- B01J29/7049—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65 containing rare earth elements, titanium, zirconium, hafnium, zinc, cadmium, mercury, gallium, indium, thallium, tin or lead
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C1/00—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon
- C07C1/26—Preparation of hydrocarbons from one or more compounds, none of them being a hydrocarbon starting from organic compounds containing only halogen atoms as hetero-atoms
-
- 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
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/18—After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/52—Improvements relating to the production of bulk chemicals using catalysts, e.g. selective catalysts
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Crystallography & Structural Chemistry (AREA)
- Life Sciences & Earth Sciences (AREA)
- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Inorganic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
Abstract
The invention discloses the preparation method that a kind of rare earth metal Ce adulterates H-ZSM-34 molecular sieves, the preparation method of rare earth metal Ce doping H-ZSM-34 molecular sieves is:Silicon source is added in water, continuously adds alkali source, silicon source, is aged after stirring and obtains clear seed-solution.Aluminum sulfate crystal is sequentially added after sequentially adding sodium hydroxide, the stirring of water-soluble silica gel in the aqueous solution of certain volume and the seed-solution of certain volume obtains precursor liquid.Ce (the NO into precursor liquid3)3·6H2O solids.It stirs at room temperature, enters kettle, crystallization goes out kettle, and filtering and washing is dry, and air roasting obtains the Na-ZSM-34 of Ce doping.The Ce Na-ZSM-34 adulterated are added in ammonium nitrate solution, are stirred, filtering and washing, it is dry.It is repeated four times after ammonium exchanges and obtains NH4-ZSM-34.Through air roasting, rare earth metal Ce doping H-ZSM-34 molecular sieves are obtained.Ce adulterates H-ZSM-34 molecular sieves, and conversion ratio is up to 78.9% in chloromethane, and Propylene Selectivity is up to 40.6%, and propene yield is up to 32%, and without deactivation phenomenom in 7h.Have the advantages that simple process, production efficiency are high.
Description
Technical field
The present invention relates to energy catalytic fields, and in particular to a kind of preparation of rare earth metal Ce doping H-ZSM-34 molecular sieves
Method.
Background technology
Propylene can be used for producing polypropylene, propylene oxide, acetone, isopropanol, phenol, and the important chemical products such as glycerine are
The indispensable Chemical Manufacture raw material of development of modern society economy, however the less efficient of propylene is prepared at present, cause for not answering
It asks, it is therefore desirable to the method for the efficient production propylene of exploitation.
The production path of halide propylene is ripe at present, and halide propylene needs molecular sieve catalyst,
Although this method improves the yield of propylene, but due to the pore passage structure of molecular sieve catalyst, acidity etc., it is made to be easy
Inactivation, therefore it is particularly important to prepare long catalytic life, stability is good, catalytic performance is high molecular sieve catalyst.
Invention content
The present invention adulterates H-ZSM-34 to overcome the shortcomings of that existing molecular sieve catalyst provides a kind of rare earth metal Ce
The preparation method of molecular sieve.
Realize that technical solution of the invention is:Include the following steps:
1. the preparation of precursor liquid:Silicon source, alkali source, silicon source and water are uniformly mixed, ageing obtains mixture A;By water, sodium hydroxide
Mixture B is obtained after being stirred with water-soluble silica gel, aluminum sulfate crystal and mixture A are added into mixture B, obtains precursor liquid;
2. after precursor liquid is stirred 0.5 h, Ce (NO are added into precursor liquid3)3·6H2O stirs 13 h, enters at room temperature
Kettle, 120 DEG C of 7 d of crystallization go out kettle, filtering and washing, 100 DEG C of dryings, and 550 DEG C of 6 h of air roasting obtain the Na- of Ce doping
ZSM-34;
3. the Ce Na-ZSM-34 adulterated are added in ammonium nitrate solution, 80 DEG C of 3 h of stirring, filtering and washing, by what is obtained
Solid is in 100 DEG C of dryings;
4. repetitive operation step 3. four times(It is repeated four times ammonium exchange)The NH of Ce doping is obtained afterwards4-ZSM-34;
5. the NH of Ce doping4- ZSM-34 obtains rare earth metal Ce doping H-ZSM-34 molecular sieves through 6 h of air roasting.
Preferably, 1. middle silicon source is sodium metaaluminate to the step, and silicon source is water-soluble silica gel, and alkali source is sodium hydroxide and hydrogen-oxygen
Change potassium.
Preferably, the step 2. in press Ce/Al(Molar ratio)=0.06~0.08:Ce is added into precursor liquid for 1 ratio
(NO3)3·6H2O solids.
Preferably, the step 3. in be added ammonium nitrate solution a concentration of 1mol/L.
Preferably, 5. air roasting temperature is 550 DEG C to the step.
Preferably, mole group of mixture A becomes n (Al2O): n(Na2O): n(K2O):n(SiO2):n(H2O) =1:
5.1:9.13:10.54: 129.98。
The advantageous effect that the present invention generates compared with the existing technology is:Rare earth metal Ce doping H-ZSM-34 molecular sieves have
Unique pore passage structure, suitable acidity, good stability and larger specific surface area are the reactions of chloromethane propylene
In potential excellent catalysts.In addition to this catalysis that can be also used for hydro carbons, has wide range of applications.In addition rare earth metal
On the basis of so that the molecular sieve stability improves, and catalytic performance improves, and the service life is elongated.H-ZSM-34 points of rare earth metal Ce doping
Conversion ratio is up to 78.9% in chloromethane for son sieve, and Propylene Selectivity is up to 40.6%, and propene yield is up to 32%, and in 7h
There is no deactivation phenomenom.And this method has the advantages that simple process, production efficiency are high.
Specific implementation mode
The specific implementation mode of form by the following examples is described in further details the above of the present invention,
But the range that this should not be interpreted as to the above-mentioned theme of the present invention is only limitted to embodiment below, all to be based on the above of the present invention
The technology of realization all belongs to the scope of the present invention.Water-soluble silica gel used in following embodiment is purchased from the limited public affairs of Qingdao Haiyang chemical industry
Department, trade name:JN-40, alkaline 40% purity Ludox.
Embodiment 1
A kind of preparation method of rare earth metal Ce doping H-ZSM-34 molecular sieves, includes the following steps:
1. by 3.5 g NaAlO2, 7 g NaOH, the 22 water-soluble silica gel of g KOH, 67.5 g are added sequentially to 100 m L water
In, 0.5 h is stirred, mixture is aged 3 days, clear seed-solution is obtained(Mixture A);By 5.54 g NaOH,
The water-soluble silica gel of 28.85 g is added sequentially in 83 m L water, is stirred 5 h, is sequentially added 2.71 g Al2(SO4)3·
18H2O and 10m L mixtures A obtains precursor liquid;
2. after precursor liquid is stirred 0.5 h, in the ratio of Ce/Al=0.06, Ce (NO are added into precursor liquid3)3·6H2O is solid
Body stirs 13 h at room temperature, enters kettle, and 120 DEG C of 7 d of crystallization go out kettle, filtering and washing, 100 DEG C of dryings, 550 DEG C of air roastings
6 h obtain the Na-ZSM-34 of Ce doping;
3. the 2g Ce Na-ZSM-34 adulterated are added in 40 mL 1mol/L ammonium nitrate solutions, 80 DEG C of 3 h of stirring take out
Filter washing, obtained solid is 5 hours dry at 100 DEG C;
4. 3. repetitive operation step obtains the NH of Ce doping after four times4-ZSM-34;
5. through 6 h of air roasting, rare earth metal Ce doping H-ZSM-34 molecular sieves are obtained.
Rare earth metal Ce doped molecular sieve H-ZSM-34 catalyst prepared by embodiment 1 is for chloromethane propylene
It reacts, conversion ratio is up to 64.4% in chloromethane, and up to 35.7%, propene yield does not have up to 23% in 6h Propylene Selectivity
There is deactivation phenomenom.
Embodiment 2
A kind of preparation method of rare earth metal Ce doping H-ZSM-34 molecular sieves, includes the following steps:
1. by 3.5 g Na Al O2, 7 g NaOH, the 22 water-soluble silica gel of g KOH, 67.5 g are added sequentially to 100 m L water
In, stir 0.5 h.Mixture is aged 3 days, clear seed-solution is obtained(Mixture A);By 5.54 g NaOH,
The water-soluble silica gel of 28.85 g is added sequentially in 83 m L water, is stirred 5 h, is sequentially added 2.71 g Al2(SO4)3·
18H2O and 10m L mixtures A obtains precursor liquid;
2. after precursor liquid is stirred 0.5 h, in the ratio of Ce/Al=0.07, Ce (NO are added into precursor liquid3)3·6H2O is solid
Body stirs 13 h at room temperature, enters kettle, and 120 DEG C of 7 d of crystallization go out kettle, filtering and washing, 100 DEG C of dryings, 550 DEG C of air roastings
6 h obtain the Na-ZSM-34 of Ce doping;
3. the 2g Ce Na-ZSM-34 adulterated are added in 40 mL 1mol/L ammonium nitrate solutions, 80 DEG C of 3 h of stirring take out
Filter washing, obtained solid is 5 hours dry at 100 DEG C;
4. 3. repetitive operation step obtains the NH of Ce doping after four times4-ZSM-34;
5. through 6 h of air roasting, rare earth metal Ce doping H-ZSM-34 molecular sieves are obtained.
Rare earth metal Ce doped molecular sieve H-ZSM-34 catalyst prepared by embodiment 2 is for chloromethane propylene
Reaction, conversion ratio is up to 66.4% in chloromethane, and Propylene Selectivity is up to 35.9%, and propene yield is up to 23.8%, and in 7h
There is no deactivation phenomenom.
Embodiment 3
A kind of preparation method of rare earth metal Ce doped molecular sieves H-ZSM-35, includes the following steps:
1. by 3.5 g Na Al O2, 7 g NaOH, the 22 water-soluble silica gel of g KOH, 67.5 g are added sequentially to 100 m L water
In, 0.5 h is stirred, mixture is aged 3 days, clear seed-solution is obtained(Mixture A);By 5.54 g NaOH,
The water-soluble silica gel of 28.85 g is added sequentially in 83 m L water, is stirred 5 h, is sequentially added 2.71 g Al2(SO4)3·
18H2O and 10m L mixtures A obtains precursor liquid;
2. after precursor liquid is stirred 0.5 h, in the ratio of Ce/Al=0.08, Ce (NO are added into precursor liquid3)3·6H2O is solid
Body stirs 13 h at room temperature, enters kettle, and 120 DEG C of 7 d of crystallization go out kettle, filtering and washing, 100 DEG C of dryings, 550 DEG C of air roastings
6 h obtain the Na-ZSM-34 of Ce doping;
3. the 2g Ce Na-ZSM-34 adulterated are added in 40 mL 1mol/L ammonium nitrate solutions, 80 DEG C of 3 h of stirring take out
Filter washing, obtained solid is 5 hours dry at 100 DEG C;
4. 3. repetitive operation step obtains the NH of Ce doping after four times4-ZSM-34;
5. through 6 h of air roasting, rare earth metal Ce doping H-ZSM-34 molecular sieves are obtained.
Rare earth metal Ce doped molecular sieve H-ZSM-34 catalyst prepared by embodiment 3 is for chloromethane propylene
Reaction, chloromethane conversion ratio is up to 78.9%, and up to 40.6%, propene yield does not have up to 32% in 7h Propylene Selectivity
Deactivation phenomenom.
Above example is explained and is described to the synthetic ratio and method of modifying of the present invention, and of the present invention one
The preparation method of kind rare earth metal Ce doped molecular sieves H-ZSM-34 provides the rare earth gold that catalytic performance is preferable, lasts a long time
Belong to Ce doped molecular sieves, when Ce/Al=0.08 constantly, prepared rare earth metal Ce doped molecular sieve H-ZSM-34 performances are best,
Longest-lived, in the reaction of chloromethane propylene, for chloromethane conversion ratio up to 78.9%, Propylene Selectivity is reachable
40.6%, propene yield is up to 32%, and without deactivation phenomenom in 7h.This method is simple for process, method is convenient, has good
Application prospect.
Claims (7)
1. a kind of preparation method of rare earth metal Ce doping H-ZSM-34 molecular sieves, which is characterized in that include the following steps:
1. the preparation of precursor liquid:Silicon source, alkali source, silicon source and water are uniformly mixed, ageing obtains mixture A;By water, sodium hydroxide
Mixture B is obtained after being stirred with water-soluble silica gel, aluminum sulfate crystal and mixture A are added into mixture B, obtains precursor liquid;
2. after precursor liquid is stirred 0.5 h, Ce (NO are added into precursor liquid3)3·6H2O stirs 13 h, enters at room temperature
Kettle, 120 DEG C of 7 d of crystallization go out kettle, filtering and washing, 100 DEG C of dryings, and 550 DEG C of 6 h of air roasting obtain the Na- of Ce doping
ZSM-34;
3. the Ce Na-ZSM-34 adulterated are added in ammonium nitrate solution, 80 DEG C of 3 h of stirring, filtering and washing, by what is obtained
Solid is in 100 DEG C of dryings;
4. 3. repetitive operation step obtains the NH of Ce doping after four times4-ZSM-34;
5. through 6 h of air roasting, rare earth metal Ce doping H-ZSM-34 molecular sieves are obtained.
2. the preparation method of rare earth metal Ce doping H-ZSM-34 molecular sieves as described in claim 1, it is characterised in that:The step
Suddenly 1. middle silicon source is sodium metaaluminate, and silicon source is water-soluble silica gel, and alkali source is sodium hydroxide and potassium hydroxide.
3. the preparation method of rare earth metal Ce doping H-ZSM-34 molecular sieves as described in claim 1, it is characterised in that:The step
Suddenly 2. in the ratio of Ce/Al=0.06 ~ 0.08 Ce (NO are added into precursor liquid3)3·6H2O solids.
4. the preparation method of rare earth metal Ce doping H-ZSM-34 molecular sieves as described in claim 1, it is characterised in that:The step
The rapid 3. middle a concentration of 1mol/L that ammonium nitrate solution is added.
5. the preparation method of rare earth metal Ce doping H-ZSM-34 molecular sieves as described in claim 1, it is characterised in that:The step
Suddenly 5. air roasting temperature is 550 DEG C.
6. the preparation method of rare earth metal Ce doping H-ZSM-34 molecular sieves as described in claim 1, it is characterised in that:Mixture
Mole group of A becomes n (Al2O): n(Na2O): n(K2O):n(SiO2):n(H2O) =1:5.1:9.13:10.54:
129.98。
7. adulterating H-ZSM-34 molecular sieves using rare earth metal Ce prepared by claim 1-6 either method.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810507380.6A CN108689416A (en) | 2018-05-24 | 2018-05-24 | A kind of preparation method of rare earth metal Ce doping H-ZSM-34 molecular sieves |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201810507380.6A CN108689416A (en) | 2018-05-24 | 2018-05-24 | A kind of preparation method of rare earth metal Ce doping H-ZSM-34 molecular sieves |
Publications (1)
Publication Number | Publication Date |
---|---|
CN108689416A true CN108689416A (en) | 2018-10-23 |
Family
ID=63846963
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201810507380.6A Pending CN108689416A (en) | 2018-05-24 | 2018-05-24 | A kind of preparation method of rare earth metal Ce doping H-ZSM-34 molecular sieves |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN108689416A (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0198437A2 (en) * | 1985-04-16 | 1986-10-22 | BASF Aktiengesellschaft | Crystalline zeolite borosilicate catalysts, process for their preparation and their use |
CN106673000A (en) * | 2015-11-09 | 2017-05-17 | 中国石油化工股份有限公司 | Synthesis method of ZSM-11 molecular sieve comprising rare earth metals and synthesized molecular sieve |
CN107500312A (en) * | 2017-08-10 | 2017-12-22 | 河南师范大学 | A kind of fluorine richness molecular sieve H ZSM 35 and preparation method thereof |
-
2018
- 2018-05-24 CN CN201810507380.6A patent/CN108689416A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0198437A2 (en) * | 1985-04-16 | 1986-10-22 | BASF Aktiengesellschaft | Crystalline zeolite borosilicate catalysts, process for their preparation and their use |
CN106673000A (en) * | 2015-11-09 | 2017-05-17 | 中国石油化工股份有限公司 | Synthesis method of ZSM-11 molecular sieve comprising rare earth metals and synthesized molecular sieve |
CN107500312A (en) * | 2017-08-10 | 2017-12-22 | 河南师范大学 | A kind of fluorine richness molecular sieve H ZSM 35 and preparation method thereof |
Non-Patent Citations (1)
Title |
---|
徐霆: ""改性分子筛催化剂上卤代甲烷制备丙烯和乙烯的研究"", 《万方数据知识服务平台》 * |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105197956B (en) | The preparation method of the HTSs of TS 1 | |
CN110372483B (en) | Process method for preparing glutaraldehyde by catalytic oxidation of cyclopentene | |
CN104291352A (en) | Method for preparing and modifying titanium silicalite molecular sieve catalyst and application of titanium silicalite molecular sieve catalyst in ketone oximation | |
CN114210363B (en) | Preparation method of SSZ-16 copper-containing catalyst | |
CN108559101B (en) | Method for preparing two-dimensional sheet Cu-MOF material | |
CN101148260A (en) | Titanium-silicon molecular screen with MWW structure and its synthesis and application | |
CN111704145A (en) | Method for in-situ synthesis of nano hydrogen type Cu-SSZ-13 molecular sieve | |
CN107500312A (en) | A kind of fluorine richness molecular sieve H ZSM 35 and preparation method thereof | |
CN107572585B (en) | A kind of bismuth oxybromide visible light catalyst and preparation method thereof | |
CN104418357A (en) | ZSM-35 molecular sieve preparation method | |
CN108452805B (en) | NiTiO for photolyzing water to produce hydrogen3/TiO2Catalyst, preparation method and application thereof | |
CN103708496A (en) | HZSM-5@silicalite-1 core-shell structure molecular sieve, and preparation method and application thereof | |
CN106219569B (en) | A method of no one step of secondary template prepares porous zeotile | |
CN103787360B (en) | A kind of preparation method of whole process TS-1 mesoporous titanium-silicon molecular screen | |
CN102730712A (en) | Preparation method of nano GaZSM-5 molecular sieve | |
CN108516564A (en) | A kind of H-ZSM-34 molecular sieves and preparation method thereof | |
CN114804136B (en) | Preparation method and application of nano SSZ-13 molecular sieve | |
CN108689415A (en) | A kind of dealuminzation H-ZSM-34 molecular sieves and preparation method thereof | |
CN110038629A (en) | A kind of preparation method of rare earth metal Nd doping H-ZSM-34 molecular sieve | |
CN108689416A (en) | A kind of preparation method of rare earth metal Ce doping H-ZSM-34 molecular sieves | |
CN110013875A (en) | A kind of preparation method of fluorine richness molecular sieve FER | |
CN102294251B (en) | Nano-oxide catalyst for preparing propylene by oxidative dehydrogenation of propane and preparation method thereof | |
CN110436479A (en) | A kind of Titanium Sieve Molecular Sieve and its preparation method and application | |
CN115475654A (en) | Microcapsule-like modified Zn @ ZSM-5 catalyst and preparation method and application thereof | |
WO2018218736A1 (en) | Aluminosilicate zeolite molecular sieve having bog structure and preparation method therefor |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20181023 |
|
WD01 | Invention patent application deemed withdrawn after publication |