CN102039168B - Method for preparing adhesive-free ZSM-5/mordenite symbiotic molecular sieve catalyst - Google Patents
Method for preparing adhesive-free ZSM-5/mordenite symbiotic molecular sieve catalyst Download PDFInfo
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Abstract
The invention discloses a method for preparing an adhesive-free ZSM-5/mordenite symbiotic molecular sieve catalyst. The method mainly solves the problems that the ZSM-5/mordenite symbiotic molecular sieve has low activity in the presence of adhesive and poor strength in the absence of adhesive and the mechanical mixture of adhesive-containing mordenite and ZSM-5 molecular sieve has low activity in the prior art. The problems are well solved by adopting the technical scheme that the method comprises the following steps of: mixing, shaping and drying 10 to 80 percent of ZSM-5/mordenite symbiotic molecular sieve, 0.1 to 10 percent of alkali substance, 0 to 20 percent of aluminum compound and 10 to 80 percent of silicon oxide to obtain a shaped catalyst precursor mixture I, putting the mixture I in template agent steam, and performing crystallization for 10 to 300 hours at the temperature of between 120 and 200 DEG C to obtain a catalyst precursor; and drying the precursor, and roasting the dried precursor for 1 to 10 hours at the temperature of between 400 and 700 DEG C to obtain the adhesive-free ZSM-5/mordenite symbiotic molecular sieve catalyst. The prepared adhesive-free ZSM-5/mordenite symbiotic molecular sieve catalyst can be used in the reaction of preparing propylene by catalytic cracking of naphtha.
Description
Technical field
The present invention relates to a kind of adhesiveless ZSM-5/mercerization zeolite symbiosis molecular screen Preparation of catalysts 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.General Adhesive-free Molecular Sieve catalyst refers in the catalyst weight of binder content smaller or equal to 5%.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.
In the document, the general title of two kinds of molecular sieves of using of the literary style of coexisting molecular sieve is write together at present, and the centre adds one "/" expression, for example, and the coexisting molecular sieve that modenite and ZSM-5 form, writing " ZSM-5/ mercerization zeolite symbiosis molecular screen ".
At present the binder free catalyst of report has the adhesiveless ZSM-5 molecular sieve, is to make through gas phase conversion at the presoma that preformed catalyst adds ZSM-5.
Chinese patent 200510028782 has reported that the present invention of small crystal grain without bonding agent ZSM-5 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 with organic amine mutually with the 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/ mercerization zeolite symbiosis molecular screen 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/mercerization zeolite symbiosis molecular screen catalyst can be optimized preparation process, avoids preparing the process complicated problems, has tangible economic worth and social value.
Summary of the invention
Technical problem to be solved by this invention is the relatively poor and lower problem of mechanical impurity activity that contains the modenite and the ZSM-5 molecular sieve of binding agent of activity ZSM-5/ mercerization zeolite symbiosis molecular screen intensity lower, that do not contain binding agent when containing binding agent in the existing ZSM-5/ mercerization zeolite symbiosis molecular screen catalyst; A kind of new adhesiveless ZSM-5/mercerization zeolite symbiosis molecular screen Preparation of catalysts method is provided; This method prepares the simple advantage of process; It is higher to use this method catalyst to have catalytic activity, and the while mechanical strength is advantage of higher also.
In order to solve the problems of the technologies described above, the technical scheme that the present invention adopts is following: a kind of adhesiveless ZSM-5/mercerization zeolite symbiosis molecular screen 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/ mercerization zeolite symbiosis molecular screen 10～80%, 0.1～10% alkaline matter, 0～20% aluminium and 10～80% the silica mixed-forming 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 placed to put into to contain be selected from least a template steam of ammoniacal liquor, ethylenediamine, triethylamine, n-butylamine, hexamethylene diamine, 4-propyl bromide or TPAOH; Carry out crystallization after 10～300 hours at 120～200 ℃, obtain adhesiveless ZSM-5/mercerization zeolite symbiosis molecular screen catalyst precarsor;
C) catalyst precarsor 400～700 ℃ of following roastings 1～10 hour, obtains adhesiveless ZSM-5/mercerization zeolite symbiosis molecular screen 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/ mercerization zeolite symbiosis molecular screen of crystal seed
2/ Al
2O
3Mol ratio is 20～60; Alkaline matter is selected from least a in oxide, hydroxide or its salt of weak acid of period of element Table I A or II A 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, I A element preferred version is selected from least a in sodium or the potassium, and II A element preferred version is selected from least a in magnesium or the calcium; The salt of weak acid preferred version is selected from least a in carbonate, oxalates or the citrate; In the catalyst weight behind the shaping and roasting, the consumption preferable range of ZSM-5/ mercerization zeolite symbiosis molecular screen is 20～70%; The consumption preferable range of alkaline matter is 0.5～10%; The compound amount preferable range of aluminium is 2～15%; The consumption preferable range of silica is 15～70%; The crystallization temperature preferable range is 140～190 ℃; The crystallization time preferable range is 20～100 hours; 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.The SiO of ZSM-5/ mercerization zeolite symbiosis molecular screen in the binder free catalyst of preparation
2/ Al
2O
3The mol ratio preferable range is 20～120, and wherein weight of binder content preferable range is 0～5%, and more preferably scope is 0.1～2%; The weight ratio preferable range of ZSM-5 and modenite is 0.2～5: 1 in the ZSM-5/ mercerization zeolite symbiosis molecular screen, the preformed catalyst intensity preferable range that makes be 70～150 newton/.
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 ZSM-5/ mercerization zeolite symbiosis molecular screen crystal seed in preformed catalyst; Put into the template steam of specific suitable ZSM-5 molecular sieve and modenite growth; Control is suitable for the alkaline environment and the material proportion of ZSM-5 and modenite growth simultaneously; Make binding agent under the inducing of crystal seed; Molecular sieve active ingredient be can change into, simultaneously in the control environment of template steam and alkalescence, ZSM-5 molecular sieve or modenite crystal seed and can nucleating growth also can be induced 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/ mercerization zeolite symbiosis molecular screen catalyst.The content of binding agent can reach below 0.5% in the binder free type ZSM-5/ mercerization zeolite symbiosis molecular screen catalyst that makes; Even do not contain binding agent; All the ZSM-5/ mercerization zeolite symbiosis molecular screen 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 54%, has obtained better technical effect.
Description of drawings
Fig. 1 is the XRD figure spectrum of the adhesiveless ZSM-5/mercerization zeolite symbiosis molecular screen catalyst of embodiment 1 preparation.
Fig. 2 is the ESEM picture of the adhesiveless ZSM-5/mercerization zeolite symbiosis molecular screen catalyst of embodiment 1 preparation.
Through embodiment the present invention is done further elaboration below.
The specific embodiment
[embodiment 1]
Get SiO
2/ Al
2O
3Mol ratio is 20 ZSM-5/ mercerization zeolite symbiosis molecular screen 60 grams, and the adding weight percentage is 40% Ludox 40 grams and aluminum sulfate 16 grams, after the mixing and stirring; 10 milliliters of sodium hydroxide solutions that add 1 mol again, mixing and stirring, the moulding of agent bar then; Preformed catalyst is 80 ℃ of oven dry 3 hours, put into then the inner bag bottom moisture with the 4-propyl bromide weight ratio be 200 milliliters autoclave of 1: 1 mixed solution 40 gram, catalyst does not contact with liquid water; Put into baking oven after the autoclave sealing, 180 ℃ of crystallization were taken out after 60 hours, washed then 2 times; Put into 120 ℃ in baking oven oven dry 3 hours, putting into the 400 ℃ of roastings 2 hours that heat up of Muffle furnace internal program, 550 ℃ of roastings 3 hours; Make adhesiveless ZSM-5/mercerization zeolite symbiosis molecular screen catalyst; Wherein the weight percentage of ZSM-5 molecular sieve is 68.5%, and modenite content is 30.0%, and the withstand voltage broken intensity of detecting catalyst sample is 150 newton.The XRD figure spectrum of the catalyst that makes is as shown in Figure 1, and it is shown as the thing phase of ZSM-5/ mercerization zeolite symbiosis molecular screen.The ESEM picture of the catalyst that makes is as shown in Figure 2, and it is shown as the mixture of ball-type ZSM-5 crystal grain and cubic modenite crystal grain, and binder content is 1.5%.
[embodiment 2]
Get SiO
2/ Al
2O
3Mol ratio is 40 ZSM-5/ mercerization zeolite symbiosis molecular screen 60 grams, and the adding weight percentage is 40% Ludox 40 grams, after the mixing and stirring; 10 milliliters of sodium carbonate liquors that add 0.5 mol again, mixing and stirring, extruded moulding then; 80 ℃ the oven dry 3 hours, put into then the inner bag bottom moisture with the TPAOH weight ratio be the autoclave of 1: 1 mixed solution, catalyst does not contact with liquid water; Put into baking oven after the autoclave sealing, 180 ℃ of crystallization were taken out after 60 hours, washed then 2 times; Put into 120 ℃ in baking oven oven dry 3 hours, putting into the 400 ℃ of roastings 2 hours that heat up of Muffle furnace internal program, 550 ℃ of roastings 3 hours; Make adhesiveless ZSM-5/mercerization zeolite symbiosis molecular screen catalyst, wherein the weight percentage of ZSM-5 molecular sieve is 38.0%, and modenite content is 60.0%; The withstand voltage broken intensity of detecting catalyst sample be 150 newton/, binder content is 2%.
[embodiment 3～7]
According to the method for embodiment 1, get SiO respectively
2/ Al
2O
3Mol ratio be 20,30,40,50 and 60 ZSM-5/ mercerization zeolite symbiosis molecular screen 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/mercerization zeolite symbiosis molecular screen catalyst is as shown in table 2.
[embodiment 8～13]
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/mercerization zeolite symbiosis molecular screen 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 the binder free 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/mercerization zeolite symbiosis molecular screen 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, weight space velocity is 1 hour
-1, water/feedstock oil weight ratio is 1: 1, the reaction half an hour after, products distribution is seen table 4, feed stock conversion is 96%, the weight ethylene yield is 29.0%, the propylene weight yield is 26.0%, diene weight total recovery is 55.0%.
Table 2
| Embodiment | The SiO of gained ZSM-5/ mercerization zeolite symbiosis molecular screen 2/Al 2O 3 | The content (weight %) of ZSM-5 in the gained ZSM-5/ mercerization zeolite symbiosis molecular screen | The content (weight %) of modenite in the gained ZSM-5/ mercerization zeolite symbiosis molecular screen | The content of binding agent (weight %) in the gained catalyst | The gained catalyst strength (newton /) |
| Embodiment 3 | 22 | 65.5 | 34.0 | 0.5 | 180 |
| Embodiment 4 | 44 | 45.4 | 53.6 | 1 | 160 |
| Embodiment 5 | 58 | 58.5 | 39.5 | 2 | 90 |
| Embodiment 6 | 76 | 98.0 | 1.7 | 0.3 | 185 |
| Embodiment 7 | 120 | 91.2 | 7.4 | 1.4 | 170 |
| Embodiment 8 | 100 | 25.4 | 73.4 | 1.2 | 175 |
| Embodiment 9 | 53 | 11.6 | 83.4 | 5 | 60 |
| Embodiment 10 | 85 | 88.1 | 10.0 | 1.9 | 156 |
| Embodiment 11 | 31 | 82.4 | 17.6 | 0 | 180 |
| Embodiment 12 | 80 | 35.5 | 64.1 | 0.4 | 175 |
| Embodiment 13 | 112 | 84.5 | 14.4 | 1.1 | 125 |
[embodiment 15]
Get the binder free type ZSM-5/ mercerization zeolite symbiosis molecular screen 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/ mercerization zeolite symbiosis molecular screen 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/ mercerization zeolite symbiosis molecular screen 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/ mercerization zeolite symbiosis molecular screen 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 CN101428233A is 40 ZSM-5/ mercerization zeolite symbiosis molecular screen mixed crystal molecular sieve; Method by embodiment 14 is processed hydrogen type molecular sieve; 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.
[comparative example 2]
Preparing silica alumina ratio by the method for Chinese patent CN101428233A is 40 ZSM-5/ mercerization zeolite symbiosis molecular screen mixed crystal molecular sieve; Method by embodiment 14 is processed hydrogen type molecular sieve; And then, obtain containing the ZSM-5/ mercerization zeolite symbiosis molecular screen mixed crystal 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 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 40 modenite; Method by embodiment 14 is processed hydrogen type molecular sieve; Then the modenite 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 40 modenite; Method by embodiment 14 is processed hydrogen type molecular sieve; 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 20 modenite, and silica alumina ratio is 40 ZSM-5 molecular sieve, 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 modenite of binding agent and the catalyst of ZSM-5 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 | 4.6 |
| Ethane | 5.2 |
| Ethene | 29.0 |
| Propane | 6.5 |
| Propylene | 26.0 |
| Butane | 8.7 |
| Butylene | 7.9 |
| Carbon five above cuts | 8.5 |
| Other | 3.8 |
Table 5
| Embodiment | Yield of ethene (weight %) | Propene yield (weight %) | Diene yield (weight %) | React 0.5 hour conversion ratio (%) | Catalyst strength (newton /) |
| Embodiment 15 | 28.5 | 26 | 54.5 | 97.5 | 143 |
| Embodiment 16 | 27.0 | 25.5 | 52.5 | 96 | 138 |
| Comparative example 1 | 23 | 21 | 43 | 90 | 30 |
| Comparative example 2 | 22 | 20 | 40 | 88 | 80 |
| Comparative example 3 | 21 | 20 | 41 | 85 | 32 |
| Comparative example 4 | 22 | 19 | 40 | 84 | 31 |
| Comparative example 5 | 25 | 21 | 46 | 86 | 75 |
| Comparative example 6 | 24 | 21 | 45 | 84 | 65 |
| Comparative example 7 | 22 | 22 | 44 | 81 | 68 |
Claims (6)
1. adhesiveless ZSM-5/mercerization zeolite symbiosis molecular screen 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/ mercerization zeolite symbiosis molecular screen 10～80%, 0.1～10% alkaline matter, 0～20% aluminium and 10～80% the silica mixed-forming 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 placed to put into to contain be selected from least a template steam of ammoniacal liquor, ethylenediamine, triethylamine, n-butylamine, hexamethylene diamine, 4-propyl bromide or TPAOH; Carry out crystallization after 10～300 hours at 120～200 ℃, obtain adhesiveless ZSM-5/mercerization zeolite symbiosis molecular screen catalyst precarsor;
C) catalyst precarsor 400～700 ℃ of following roastings 1～10 hour, obtains adhesiveless ZSM-5/mercerization zeolite symbiosis molecular screen 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/ mercerization zeolite symbiosis molecular screen of crystal seed
2/ Al
2O
3Mol ratio is 20～60; Alkaline matter is selected from least a in oxide, hydroxide or its salt of weak acid of period of element Table I A or II A 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.
2. adhesiveless ZSM-5 according to claim 1/mercerization zeolite symbiosis molecular screen Preparation of catalysts method is characterized in that I A element is selected from least a in sodium or the potassium, and II A 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.
3. adhesiveless ZSM-5 according to claim 1/mercerization zeolite symbiosis molecular screen Preparation of catalysts method; It is characterized in that in the catalyst weight behind the shaping and roasting; The consumption of ZSM-5/ mercerization zeolite symbiosis molecular screen is 20～70%, the consumption of alkaline matter is 0.5～5%; The compound amount of aluminium is 2～15%, and the consumption of silica is 15～70%, and template agent is 10～100%.
4. adhesiveless ZSM-5 according to claim 1/mercerization zeolite symbiosis molecular screen Preparation of catalysts method is characterized in that crystallization temperature is 140-190 ℃, and crystallization time is 20～100 hours.
5. adhesiveless ZSM-5 according to claim 1/mercerization zeolite symbiosis molecular screen Preparation of catalysts method; It is characterized in that in the catalyst weight behind the shaping and roasting, 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.
6. adhesiveless ZSM-5 according to claim 1/mercerization zeolite symbiosis molecular screen Preparation of catalysts method is characterized in that contained ZSM-5/ mercerization zeolite symbiosis molecular screen SiO
2/ Al
2O
3Mol ratio is 20～120; Wherein weight of binder content 0.1～2%; The weight ratio of ZSM-5 and modenite is 0.2～5: 1 in the ZSM-5/ mercerization zeolite symbiosis molecular screen; Every with catalyst is of a size of 1.5 millimeters of diameters, 5 millimeters meters of length, the preformed catalyst intensity that makes be 70～150 newton/.
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| CN102671692A (en) * | 2012-05-04 | 2012-09-19 | 江苏扬农化工集团有限公司 | H-ZSM-5 zeolite molecular sieve, and preparation and application thereof |
| US9180441B2 (en) | 2012-09-20 | 2015-11-10 | Saudi Basic Industries Corporation | Method of forming zeolite shaped body with silica binder |
| US9782758B2 (en) | 2013-04-23 | 2017-10-10 | Saudi Basic Industries Corporation | Method of preparing hydrocarbon aromatization catalyst, the catalyst, and the use of the catalyst |
| CN115501907B (en) * | 2021-06-23 | 2024-01-12 | 中国石油化工股份有限公司 | ZSM-5/mordenite composite phase full-crystallization molecular sieve catalyst, preparation and application thereof |
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| CN101259424A (en) * | 2008-03-18 | 2008-09-10 | 南京工业大学 | Preparation of toluene shape-selective disproportionation without adhesive |
| CN101348261A (en) * | 2007-07-18 | 2009-01-21 | 中国石油化工股份有限公司 | Preparation of binderless ZSM-11 zeolite |
| CN101491772A (en) * | 2008-01-23 | 2009-07-29 | 中国石油化工股份有限公司 | Catalyst for naphtha catalytic cracking |
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Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101348261A (en) * | 2007-07-18 | 2009-01-21 | 中国石油化工股份有限公司 | Preparation of binderless ZSM-11 zeolite |
| CN101491772A (en) * | 2008-01-23 | 2009-07-29 | 中国石油化工股份有限公司 | Catalyst for naphtha catalytic cracking |
| CN101259424A (en) * | 2008-03-18 | 2008-09-10 | 南京工业大学 | Preparation of toluene shape-selective disproportionation without adhesive |
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| JP特开2007-252989A 2007.10.04 |
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