CN101992121B - Binderless ZSM-5/Magadiite symbiotic material catalyst and preparation method thereof - Google Patents
Binderless ZSM-5/Magadiite symbiotic material catalyst and preparation method thereof Download PDFInfo
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Abstract
The invention relates to a binderless ZSM-5/Magadiite symbiotic material catalyst and a preparation method thereof, mainly solving the problems that the activity is low if the ZSM-5/Magadiite symbiotic material catalyst prepared by the traditional method contains a binder, the intensity is poor if the ZSM-5/Magadiite symbiotic material catalyst does not contain the binder and the machinery mixture of the ZSM-5/Magadiite symbiotic material catalyst containing the binder has lower activity. In the binderless ZSM-5/Magadiite symbiotic material catalyst, the ZSM-5/Magadiite symbiotic material with SiO2/AI2O3 molar rate of 20-600 is contained, wherein the weight content of the binder is between 0 and 5 percent, the weight ratio of ZSM-5 to Magadiite in the ZSM-5/Magadiite symbiotic material is (0.15-100):1 and the machinery intensity of formed catalyst is 50-200 Newton/particles. By adopting the technical scheme, the problems of the prior art are better solved , and the prepared binderless ZSM-5/Magadiite symbiotic material catalyst can be applied to naphtha catalytic pyrolysis reaction.
Description
Technical field
The present invention relates to a kind of adhesiveless ZSM-5/Magadiite coexisting material Catalysts and its preparation method.
Background technology
Molecular sieve has good shape selective catalysis performance and absorption property owing to have evenly regular pore passage structure, bigger specific area and higher thermally-stabilised row, is applied in field of petrochemical industry widely.Because molecular sieve powder self intensity is lower, be prone to disperse to run off, can't directly be applied in use in the industry; Therefore in use need add the binding agent moulding and gain in strength, in the catalyst after the moulding, because binding agent parcel molecular sieve; Caused the effective rate of utilization of molecular sieve to descend, the duct of the molecular sieve of part is blocked, causes the specific area of catalyst lower; Activity is also lower, and again because binding agent is no regular pore passage structure, reaction raw materials and product are in catalyst diffusion difficulty; Carbon deposit has certain influence to life of catalyst easily.Be converted into the active principle molecular sieve to the binding agent in the catalyst and then can overcome above problem, improve activity of such catalysts and diffusion.
The binder free catalyst is exactly the active principle that changes into the binding agent that is added in the molecular sieve catalyst forming process in molecular sieve, makes not contain the binding agent composition in the whole catalyst, keeps the good intensity of catalyst simultaneously.Transform or almost completely be converted into the molecular sieve composition fully owing to binding agent in the binder free catalyst; So just improved the content of molecular sieve in the per volume of catalyst; Make activity of such catalysts higher, treating capacity is bigger, simultaneously owing to no longer include binding agent in the catalyst; Solved binding agent parcel molecular sieve and reduced the effective rate of utilization of molecular sieve and the problem that binding agent stops up molecular sieve pore passage, the effective rate of utilization of molecular sieve and carbon accumulation resisting ability are improved greatly.
General coexisting molecular sieve is to prepare through the synthetic method of hydro-thermal, is Powdered, and no intensity is prone to run off, and can not directly use, and need add binding agent when industry or laboratory applications and carry out extrusion or spray shaping.In the general molecular sieve catalyst forming process, the weight that add binding agent is no less than 40% of total catalyst weight, though the moulding rear catalyst has had intensity, the effective rate of utilization of catalyst reduces, active and diffusion variation.
General Adhesive-free Molecular Sieve catalyst refers in the catalyst weight of binder content smaller or equal to 5%.
Chinese patent 200510028782 has reported that the present invention of ZSM-5/Magadiite coexisting material prepare zeolite method is a primary raw material through adopting with diatomite or white carbon; Add the crystal seed directed agents; And with Ludox or sodium metasilicate as the binding agent moulding; Handle the technical scheme that is converted into integrated small-grain ZSM-5/Magadiite coexisting material mutually with organic amine and water vapour gas-solid then; Mainly solve the zeolite powder and in practical application, have the difficult weakness that reclaims, is prone to inactivation and gathering, and the adding binding agent can cause that effective surface area reduces the problem that influences with diffusion restriction in the forming process.
Chinese patent 200510029462 has been reported the preparation method of ZSM-type molecular sieve without binding agent.Through adopting content is the mixture that the former powder of 5～50 weight % binding agent silica and ZSM type molecule forms; In the aqueous solution that contains halogenation organic amine and alkyl diamine or steam; Be converted into the technical scheme of integrated ZSM type molecular sieve through hydrothermal treatment consists, mainly solved and add binding agent in the molecular sieve catalyst forming process and can cause that effective surface area reduces the problem with the diffusion restriction influence.
Composite molecular screen, coexisting molecular sieve or the mixed crystal molecular sieve of existing report all need be synthetic synthetic back of molecular sieve or adding crystal seed directed agents hydro-thermal, and building-up process is very complicated comparatively.The synthetic ZSM-5/Magadiite coexisting material of report all is to be prepared from through the synthetic method of hydro-thermal at present.Add crystal seed or template in the building-up process, the complicated and pollution again of preparation method.
The method that directly prepares adhesiveless ZSM-5/Magadiite coexisting material catalyst can be optimized preparation process, avoids preparing the process complicated problems, has tangible economic worth and social value.
At present, adhesiveless ZSM-5/Magadiite coexisting material Preparation of catalysts method is not seen report.
Summary of the invention
One of technical problem to be solved by this invention is the relatively poor and lower problem of mechanical impurity activity that contains the ZSM-5/Magadiite coexisting material of binding agent of activity ZSM-5/Magadiite coexisting material intensity lower, that do not contain binding agent when containing binding agent in the existing ZSM-5/Magadiite coexisting material catalyst, and a kind of new adhesiveless ZSM-5/Magadiite coexisting material catalyst is provided.It is higher that this catalyst has catalytic activity, and the while mechanical strength is advantage of higher also.Two of technical problem to be solved by this invention provides a kind of new a kind of new corresponding preparation method of the catalyst with one of technical solution problem that provides.
For one of solving the problems of the technologies described above, the technical scheme that the present invention adopts is following: a kind of adhesiveless ZSM-5/Magadiite coexisting material catalyst, contain SiO
2/ Al
2O
3Mol ratio is 20～600 ZSM-5/Magadiite coexisting material, and wherein weight of binder content 0～5%; The weight ratio of ZSM-5 and Magadiite is 0.15～100: 1 in the ZSM-5/Magadiite coexisting material, the mechanical strength of preformed catalyst be 50～200 newton/.
In the technique scheme, the SiO of ZSM-5/Magadiite coexisting material
2/ Al
2O
3The mol ratio preferable range is 40～400; Wherein weight of binder content preferable range is 0.1～2%; The weight ratio preferable range of ZSM-5 and Magadiite is 0.5～100: 1 in the ZSM-5/Magadiite coexisting material, the preformed catalyst intensity preferable range that makes be 60～150 newton/.
For solve the problems of the technologies described above two, the technical scheme that the present invention adopts is following: above-mentioned adhesiveless ZSM-5/Magadiite coexisting material Preparation of catalysts method may further comprise the steps:
A) in the catalyst weight behind the shaping and roasting; After the compound of the ZSM-5 20～80%, 0～10% aluminium, 0～10% alkaline matter, 15～80% silica mixing, moulding, the drying; Obtain preformed catalyst precursor mixture I, wherein among the mixture I compound weight content of aluminium less than the weight content of silica;
B) mixture I is put into the steam that contains at least a template that is selected from ammoniacal liquor, hexylamine, ethylenediamine, triethylamine, n-butylamine, hexamethylene diamine, 4-propyl bromide or TPAOH, at 100-200 ℃ of ZSM-5/Magadiite coexisting material catalyst precarsor that carries out not contained after crystallization is handled 10～240 hours binding agent;
C) catalyst precarsor 400～700 ℃ of following roastings 1～10 hour, obtains adhesiveless ZSM-5/Magadiite coexisting material catalyst through super-dry;
Wherein, in the catalyst weight behind the shaping and roasting, template agent is 5～300%, the SiO of ZSM-5
2/ Al
2O
3Mol ratio is 20～200; Alkaline matter is selected from least a in oxide, hydroxide or its salt of weak acid of IA or IIA element; The compound of aluminium is selected from least a in the hydroxide of hydrous oxide or aluminium of oxide, aluminium of aluminium salt, aluminium.
In the technique scheme, in the catalyst weight behind the shaping and roasting, the consumption preferable range of ZSM-5 molecular sieve is 15～70%; The compound amount preferable range of aluminium is 0～10%; The consumption preferable range of silica is 15～70%; Catalyst neutral and alkali material consumption preferable range is 0.5～5%; The crystallization temperature preferable range is 120～180 ℃; The crystallization time preferable range is 20～100 hours; IA element preferred version is to be selected from least a in sodium or the potassium, and IIA element preferred version is to be selected from least a in magnesium or the calcium; The salt of weak acid preferred version is to be selected from least a in carbonate, oxalates or the citrate; In the catalyst weight behind the shaping and roasting, preferred version is also to contain 0.1～2% the expanding agent at least a in sesbania powder, methylcellulose or the soluble starch that is selected among the preformed catalyst precursor mixture I.
It is strip solid cylindrical, that diameter is 0.5～2mm that shape after the catalyst precarsor mixture I extrusion is generally tangent plane, is broken into every grain length degree after the drying and is 5 millimeters short cylindrical shape catalyst bar, is convenient to change brilliant and handles and examination.Catalyst mechanical strength among the present invention is calculated by this shape measure.Catalyst precarsor mixture I also can make cellular as required, clover shape, hollow tubular or shape such as spherical, and its strength criterion is meter in addition.
In the characterization method of binder free catalyst, with the contained thing of XRD test mutually and the content of each thing phase, change the pattern of molecular sieve of situation and the generation of crystalline substance with the scanning electron microscopic observation binding agent.Change brilliant back binder content confirm through the XRD thing mutually quantitatively and in the stereoscan photograph content of binding agent confirm.The catalyst silica alumina ratio is confirmed with chemico-analytic method.The strength test method of catalyst is the crushing strength of the catalyst after test roasting on the pressure testing machine; Every of the catalyst of surveying is of a size of 1.5 millimeters of diameters; 5 millimeters of length; Be disposed across on the testing machine, suffered maximum pressure when measuring catalyst breakage is got its mean value after testing 10 catalyst crushing strengths.
The present invention is through adding single crystal seed ZSM-5 molecular sieve in preformed catalyst; Put into the template steam of specific suitable ZSM-5 molecular sieve and Magadiite growth; Control is suitable for the alkaline environment and the material proportion of ZSM-5 and Magadiite growth simultaneously; Make binding agent under the inducing of crystal seed, can change into molecular sieve active ingredient, simultaneously in the control environment of template steam and alkalescence; Also can induce ZSM-5 molecular sieve and Magadiite crystal seed and can nucleating growth in the binding agent; Therefore binding agent can be transformed into the coexisting molecular sieve active principle through the method for gas phase conversion, obtains binder free type ZSM-5/Magadiite coexisting material catalyst, reaches the purpose of simple environmental protection.The content of binding agent can reach below 0.5% in the binder free type ZSM-5/Magadiite coexisting material catalyst that makes; Even do not contain binding agent; All the ZSM-5/Magadiite coexisting material in the catalyst; Improve the content of coexisting molecular sieve in the per volume of catalyst like this, improved activity of such catalysts.Since change the binder free coexisting molecular sieve thing that obtains behind the crystalline substance mutually between staggered growth, in conjunction with tightr, so the intensity of catalyst is also higher, can reach 180 newton/.The catalyst that makes can be used in the reaction of naphtha catalytic pyrolysis preparing propylene, and the diene weight yield of ethylene, propylene can reach more than 52%, has obtained better technical effect.
Description of drawings
Fig. 1 is the XRD figure spectrum of the adhesiveless ZSM-5/Magadiite coexisting material catalyst of embodiment 1 preparation.
Fig. 2 is the ESEM picture of the adhesiveless ZSM-5/Magadiite coexisting material catalyst of embodiment 1 preparation.
Through embodiment the present invention is done further elaboration below.
The specific embodiment
[embodiment 1]
Get silica alumina ratio (molecular proportion) and be 100 ZSM-5 molecular sieve 60 grams, add weight percentage and be 40% Ludox 40 grams, after the mixing and stirring; 10 milliliters of sodium bicarbonate solutions that add 1 mol again, agent bar moulding after the mixing and stirring, preformed catalyst was 80 ℃ of oven dry 3 hours; Put into the autoclave that the inner bag bottom contains ethylenediamine then, catalyst does not contact with liquid, puts into baking oven after the autoclave sealing; 180 ℃ of crystallization were taken out after 60 hours, washed then 2 times, put into 120 ℃ of oven dry of baking oven 3 hours; Putting into the 400 ℃ of roastings 2 hours that heat up of Muffle furnace internal program, 550 ℃ of roastings 3 hours make the binder free catalyst.The XRD figure spectrum of the catalyst that makes is as shown in Figure 1; It is shown as ZSM-5/Magadiite coexisting material commensal phase; Wherein the weight percentage of ZSM-5 molecular sieve is 78.5%, and Magadiite content is 20.0%, and the withstand voltage broken intensity of detecting catalyst sample is 150 newton.The ESEM picture of the catalyst that makes is as shown in Figure 2, and it is shown as pure ZSM-5/Magadiite coexisting material crystal, and binder content is 1.5%.
[embodiment 2～6]
According to the method for embodiment 1, get SiO respectively
2/ Al
2O
3Mol ratio be 20,60,100,160 and 200 ZSM-5 molecular sieve as crystal seed, other condition is constant, it is as shown in table 1 that raw material is formed proportioning, the adhesiveless ZSM-5 that makes/Magadiite coexisting material catalyst is as shown in table 2.
[embodiment 7～13]
Method according to embodiment 1; Other condition is constant, in forming process, adds soluble starch, sesbania powder or methylcellulose, and it is as shown in table 1 that raw material is formed proportioning; Mixing and stirring; Extruded moulding is processed adhesiveless ZSM-5/Magadiite coexisting material catalyst by the method for embodiment 1 again, and the result is as shown in table 2.
[embodiment 14]
Method according to embodiment 1 makes adhesiveless ZSM-5/Magadiite coexisting material catalyst; Use concentration is 5% ammonium nitrate solution; It in the solid-to-liquid ratio of catalyst and ammonium nitrate solution 1: 10 ratio; 90 ℃ of exchanges three times, 550 ℃ of roastings made the adhesiveless ZSM-5/Magadiite coexisting material catalyst of Hydrogen after 3 hours then.The component that adopts Shanghai Gaoqiao petro-chemical corporation to produce is C
4～C
10Light oil be raw material (the raw material physical index is seen table 3), the examination activity of such catalysts, using diameter is 12 millimeters fixed bed reactors normal pressure examination down, range of reaction temperature is 650 ℃, reaction pressure is 0.02MPa, mass space velocity is 1 hour
-1, water/feedstock oil mass ratio is 1: 1, the reaction half an hour after, products distribution is seen table 4, feed stock conversion is 89%, the ethene mass yield is 27.0%, the propylene mass yield is 25.2%, diene quality total recovery is 52.2%.
[embodiment 15]
Get the binder free type ZSM-5/Magadiite coexisting material that obtains among the embodiment 1, process hydrogen type catalyst, get 100 grams by the method for embodiment 14; Using concentration is that 300 milliliters of the ammonium hydrogen phosphates of 0.5 mol flooded modification 4 hours at 95 ℃; Take out sample 120 ℃ of oven dry 3 hours then,, obtain the binder free type ZSM-5/Magadiite coexisting material catalyst of phosphorus modification again 650 ℃ of roastings 3 hours; Method according to embodiment 14 is checked and rated, and the result sees table 5.
[embodiment 16]
Get binder free type ZSM-5/Magadiite coexisting material catalyst 100 grams of the phosphorus modification that obtains among the embodiment 15; Using concentration is that 300 milliliters of the ammonium hydrogen phosphates of 0.2 mol flooded modification 4 hours at 95 ℃; Take out sample 120 ℃ of oven dry 3 hours then,, obtain the binder free type ZSM-5/Magadiite coexisting material catalyst of lanthanum and phosphorus modification again 650 ℃ of roastings 3 hours; Method according to embodiment 14 is checked and rated, and the result sees table 5.
[comparative example 1]
Preparing silica alumina ratio by the method for Chinese patent CN101279750A is 40 ZSM-5/Magadiite coexisting material; Process the Hydrogen material by the method for embodiment 14; Then mixed crystal molecular sieve direct tablet compressing, break into pieces, sieve, do not contained 20～40 purpose catalyst granules of binding agent, put into fixed bed reactors; Press the method examination of embodiment 14, the result sees table 5.
Table 2
| Embodiment | Gained molecular sieve SiO 2/Al 2O 3 | ZSM-5 content (weight %) | Magadiite content (weight %) | Binder content (weight %) | Catalyst strength (newton) |
| Embodiment 3 | 24 | 65.0 | 34.5 | 0.5 | 185 |
| Embodiment 4 | 72 | 55.4 | 43.6 | 1 | 165 |
| Embodiment 5 | 120 | 68.5 | 29.5 | 2 | 70 |
| Embodiment 6 | 220 | 98.4 | 1.6 | 0 | 180 |
| Embodiment 7 | 280 | 92.2 | 6.4 | 1.4 | 175 |
| Embodiment 8 | 600 | 75.4 | 23.4 | 1.2 | 165 |
| Embodiment 9 | 300 | 10.6 | 84.4 | 5 | 50 |
| Embodiment 10 | 80 | 87.1 | 11.0 | 1.9 | 126 |
| Embodiment 11 | 140 | 81.2 | 18.6 | 0.2 | 160 |
| Embodiment 12 | 60 | 25.5 | 74.1 | 0.4 | 170 |
| Embodiment 13 | 400 | 85.5 | 13.4 | 1.1 | 90 |
[comparative example 2]
Preparing silica alumina ratio by the method for Chinese patent CN101279750A is 40 ZSM-5/Magadiite coexisting material; Method by embodiment 14 is processed hydrogen type molecular sieve; And then, obtain containing the ZSM-5/Magadiite coexisting material catalyst of binding agent according to the method extruded moulding of embodiment 1, put into fixed bed reactors; Press the method examination of embodiment 14, the result sees table 5.
[comparative example 3]
The silica alumina ratio of getting the production of Oil of Shanghai Petrochemical Company research institute is 40 ZSM-5 molecular sieve; Method by embodiment 14 is processed hydrogen type molecular sieve; Then ZSM-5 molecular sieve direct tablet compressing, break into pieces, sieve, do not contained 20～40 purpose catalyst granules of binding agent, put into fixed bed reactors; Press the method examination of embodiment 14, the result sees table 5.
[comparative example 4]
The silica alumina ratio of getting the production of Oil of Shanghai Petrochemical Company research institute is 200 Magadiite; Process the Hydrogen material by the method for embodiment 14; Then the Magadiite direct tablet compressing, break into pieces, sieve, do not contained 20～40 purpose catalyst granules of binding agent, put into fixed bed reactors; Press the method examination of embodiment 14, the result sees table 5.
[comparative example 5]
The silica alumina ratio that Oil of Shanghai Petrochemical Company research institute produces is 40 ZSM-5 molecular sieve; Method by embodiment 14 is processed hydrogen type molecular sieve; And then, obtain containing the ZSM-5 molecular sieve catalyst of binding agent according to the method extruded moulding of embodiment 1, put into fixed bed reactors; Press the method examination of embodiment 14, the result sees table 5.
[comparative example 6]
The silica alumina ratio of getting the production of Oil of Shanghai Petrochemical Company research institute is 200 Magadiite; Process Hydrogen material molecule sieve by the method for embodiment 14; And then, obtain containing the mordenite catalyst of binding agent according to the method extruded moulding of embodiment 1, put into fixed bed reactors; Press the method examination of embodiment 14, the result sees table 5.
[comparative example 7]
The silica alumina ratio of getting the production of Oil of Shanghai Petrochemical Company research institute is 40 ZSM-5 molecular sieve, and silica alumina ratio is 200 Magadiite, is mixed into mechanical impurity at 1: 1 according to weight ratio; Method by embodiment 14 is processed hydrogen type molecular sieve; And then, obtain containing the ZSM-5 molecular sieve of binding agent and the catalyst of Magadiite mechanical impurity according to the method extruded moulding of embodiment 1, put into fixed bed reactors; Press the method examination of embodiment 14, the result sees table 5.
Table 3
| Project | Data |
| Density (20 ℃) kilogram/rice 3 | 704.6 |
| Boiling range is boiling range ℃ just | 40 |
| Whole boiling range ℃ | 160 |
| Saturated vapor pressure (20 ℃) kPa | 50.2 |
| Alkane % (weight %) | 65.2 |
| Cycloalkane % (weight %) | 28.4 |
| Alkene % (weight %) | 0.2 |
| Aromatic hydrocarbons % (weight %) | 6.2 |
Table 4
| Products distribution | Product weight yield (%) |
| Methane | 4.1 |
| Ethane | 7.2 |
| Ethene | 27.0 |
| Propane | 6.8 |
| Propylene | 25.2 |
| Butane | 8.7 |
| Butylene | 8.9 |
| Carbon five above cuts | 8.8 |
| Other | 3.5 |
Table 5
| Embodiment | Catalyst strength (newton /) | Yield of ethene (weight %) | Propene yield (weight %) | Diene yield (weight %) | React 0.5 hour conversion ratio (%) |
| Embodiment 15 | 143 | 26.5 | 25 | 51.5 | 95.5 |
| Embodiment 16 | 138 | 25.0 | 250 | 50 | 92 |
| Comparative example 1 | 30 | 23 | 21 | 43 | 90 |
| Comparative example 2 | 80 | 22 | 20 | 40 | 88 |
| Comparative example 3 | 32 | 23 | 21 | 44 | 85 |
| Comparative example 4 | 31 | 19 | 18 | 37 | 80 |
| Comparative example 5 | 75 | 24 | 21 | 45 | 85 |
| Comparative example 6 | 65 | 22 | 20 | 42 | 80 |
| Comparative example 7 | 68 | 20 | 20 | 40 | 78 |
Claims (6)
1. adhesiveless ZSM-5/Magadiite coexisting material catalyst contains SiO
2/ Al
2O
3Mol ratio is 20～600 ZSM-5/Magadiite coexisting material, and wherein weight of binder content 0～5%; The weight ratio of ZSM-5 and Magadiite is 0.15～100: 1 in the ZSM-5/Magadiite coexisting material, is of a size of 1.5 millimeters of diameters with every of surveyed catalyst, 5 millimeters meters of length, the mechanical strength of preformed catalyst be 50～200 newton/;
Adhesiveless ZSM-5/Magadiite coexisting material Preparation of catalysts method may further comprise the steps:
A) in the catalyst weight behind the shaping and roasting; After the compound of the ZSM-5 20～80%, 0～10% aluminium, 0～10% alkaline matter, 15～80% silica mixing, moulding, the drying; Obtain preformed catalyst precursor mixture I, wherein among the mixture I compound weight content of aluminium less than the weight content of silica;
B) mixture I is put into the steam that contains at least a template that is selected from ammoniacal liquor, hexylamine, ethylenediamine, triethylamine, n-butylamine, hexamethylene diamine, 4-propyl bromide or TPAOH; Carry out the crystallization processing after 10～240 hours at 100-200 ℃, obtain the ZSM-5/Magadiite coexisting material catalyst precarsor of binder free;
C) catalyst precarsor 400～700 ℃ of following roastings 1～10 hour, obtains adhesiveless ZSM-5/Magadiite coexisting material catalyst through super-dry;
Wherein, in the catalyst weight behind the shaping and roasting, template agent is 5～300%, as the SiO of the ZSM-5 of crystal seed
2/ Al
2O
3Mol ratio is 20～200; Alkaline matter is selected from least a in oxide, hydroxide or its salt of weak acid of periodic table of elements IA or IIA element; The compound of aluminium is selected from least a in the hydroxide of hydrous oxide or aluminium of oxide, aluminium of aluminium salt, aluminium; The Adhesive-free Molecular Sieve catalyst refers in the catalyst weight of binder content smaller or equal to 5%.
2. adhesiveless ZSM-5 according to claim 1/Magadiite coexisting material catalyst is characterized in that the SiO of contained ZSM-5/Magadiite coexisting material
2/ Al
2O
3Mol ratio is 40～400; Weight of binder content is 0.1～2%; The weight ratio of ZSM-5 and Magadiite is 0.5～100: 1 in the ZSM-5/Magadiite coexisting material; Every with surveyed catalyst is of a size of 1.5 millimeters of diameters, 5 millimeters meters of length, the preformed catalyst intensity that makes be 60～150 newton/.
3. adhesiveless ZSM-5 according to claim 1/Magadiite coexisting material catalyst is characterized in that in the catalyst weight behind the shaping and roasting consumption of ZSM-5 molecular sieve is 15～70%; The compound amount of aluminium is 0～5%; The consumption of silica is 15～70%; The consumption of alkaline matter is 0.5～5%; Template agent is 5～100% of a shaping and roasting rear catalyst weight.
4. adhesiveless ZSM-5 according to claim 1/Magadiite coexisting material catalyst is characterized in that crystallization temperature is 120-200 ℃; Crystallization time is 20～100 hours.
5. adhesiveless ZSM-5 according to claim 1/Magadiite coexisting material catalyst is characterized in that the IA element is selected from least a in sodium or the potassium, and the IIA element is selected from least a in magnesium or the calcium; Salt of weak acid is selected from least a in carbonate, oxalates or the citrate.
6. adhesiveless ZSM-5 according to claim 1/Magadiite coexisting material catalyst; It is characterized in that in shaping and roasting rear catalyst weight, also contain 0.1～2% the expanding agent at least a in sesbania powder, methylcellulose or the soluble starch that is selected among the preformed catalyst precursor mixture I.
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| CN103030156B (en) * | 2011-09-30 | 2014-10-15 | 中国石油化工股份有限公司 | Preparation method of binderless ZSM-5 molecular sieve |
| CN105268464B (en) * | 2014-07-03 | 2018-02-13 | 中国石油化工股份有限公司 | Pillared Magadiite phyllosilicates and the composite of MFI-type molecular sieve and preparation method thereof |
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| Title |
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| JP特开2007-252989A 2007.10.04 |
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