CN1079444A - The preparation method of small crystal grain NaY molecular sieve - Google Patents

The preparation method of small crystal grain NaY molecular sieve Download PDF

Info

Publication number
CN1079444A
CN1079444A CN 92103885 CN92103885A CN1079444A CN 1079444 A CN1079444 A CN 1079444A CN 92103885 CN92103885 CN 92103885 CN 92103885 A CN92103885 A CN 92103885A CN 1079444 A CN1079444 A CN 1079444A
Authority
CN
China
Prior art keywords
directed agents
preparation
solution
molecular sieve
crystal grain
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.)
Granted
Application number
CN 92103885
Other languages
Chinese (zh)
Other versions
CN1033503C (en
Inventor
马跃龙
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Sinopec Research Institute of Petroleum Processing
Original Assignee
Sinopec Research Institute of Petroleum Processing
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Sinopec Research Institute of Petroleum Processing filed Critical Sinopec Research Institute of Petroleum Processing
Priority to CN 92103885 priority Critical patent/CN1033503C/en
Publication of CN1079444A publication Critical patent/CN1079444A/en
Application granted granted Critical
Publication of CN1033503C publication Critical patent/CN1033503C/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B39/00Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
    • C01B39/02Crystalline 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
    • C01B39/20Faujasite type, e.g. type X or Y
    • C01B39/24Type Y

Landscapes

  • Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Materials Engineering (AREA)
  • Inorganic Chemistry (AREA)
  • Silicates, Zeolites, And Molecular Sieves (AREA)
  • Catalysts (AREA)

Abstract

A kind of method that the directed agents technology prepares small crystal grain NaY molecular sieve of improving that adopts.Its preparation process is: at first sodium silicate solution is joined in the conventional directed agents of transmittance<30%, make a kind of mole and consist of (12-180) Na 2O:Al 2O 3: (17-210) SiO 2: (160-3100) H 2The improvement directed agents solution of O, transmittance>75%, will improving directed agents then, to be used for the NaY hydro-thermal of different ingredients synthetic, makes the NaY zeolite product of little crystal grain according to the preparation method of conventional NaY molecular sieve.

Description

The preparation method of small crystal grain NaY molecular sieve
The invention belongs to the molecular sieve synthetic technology, specifically about the preparation method of small crystal grain NaY molecular sieve.
Along with the understanding that the NaY molecular sieve is acted on is goed deep into, it is found that small crystal grain NaY molecular sieve has catalytic performance preferably in catalytic cracking process.EPO, 204,236(1986) reported the cracking catalyst that makes by small crystal grain NaY molecular sieve and big crystal NaY molecular sieve relatively, heavy oil fluid catalytic cracking there are higher activity and selectivity preferably.
Corma thinks to have high SiO 2/ Al 2O 3NaY molecular sieve than, little crystal grain can improve gasoline octane rating, have preferably water, thermostability (ACS Symp ser, 375, Chap, 2,1988, P.17).
Synthetic method report about small crystal grain NaY molecular sieve is more, concludes to get up to mainly contain:
1, improve the basicity of NaY when synthetic, add directed agents (US3,755,538).As the synthetic total proportioning of NaY is 6.5Na 2O: Al 2O 3: 16SiO 2: 280H 2O, mole consist of 16Na 2O: Al 2O 3: 15SiO 2: 320H 2The directed agents add-on of O is that 20%(is with total Al in the system 2O 3The mole number meter).Crystal grain diameter with this method synthetic NaY molecular sieve is 0.06 micron, and lattice constant is 24.66 nanometers.
2, by control directed agents digestion time, factors such as temperature are improved crystal seed, preparation small crystal grain NaY molecular sieve (KR8601-488B).
3, add dispersion medium.As add methyl alcohol, ethanol, dimethyl sulfoxide (DMSO), and the left and right sugar etc. that revolves can make the X.Y-type small crystal grain molecular sieve that crystal grain diameter is the 0.01-0.1 micron (US3,516,786 as dispersion medium; EP0.041,338).
4, by improving processing condition, become glue as low temperature, stir for a long time at a high speed, modes such as micro-wave energy heating make small-grain Y-type, X-type, and ZSM-5 equimolecular sieve (GB1,223,592; US4,587,115; US4,778,666).
Adopting the common feature of the little brilliant NaY molecular sieve of above several method synthetic is the SiO of product 2/ Al 2O 3Than low, only be suitable for synthetic X-type molecular sieve and SiO 2/ Al 2O 3Y-shaped molecular sieve than≤5.
Prepare high SiO 2/ Al 2O 3The report of the NaY molecular sieve of ratio is more, as adopting the crystallization guiding technique, replaces the work of more expensive silicon sol synthesizing high-silicon Y-shaped molecular sieve more and more to cause people's attention with the water glass of cheapness.Industrialized at present high SiO 2/ Al 2O 3Ratio-NaY molecular sieve mainly is that employing water glass, sodium metaaluminate, sodium hydroxide and Tai-Ace S 150 are (US4,166,099 that raw material makes; CN85102733A; " refining of petroleum " 11-12 phase, P22-25,1978), but also be only limited to the NaY molecular sieve of crystal grain diameter>0.30 micron.
EP0.204,455 have reported a kind of directed agents technology of preparing that can improve molecular sieve catalyst intensity, promptly join by the sodium silicate solution with significant quantity and generate a kind of as clear as crystal improvement directed agents solution in the conventional directed agents.The long service life of this improvement directed agents is used this directed agents to carry out the carclazyte microspherical catalyst that in-situ crystallization makes and is had advantages of high strength, but in this patent and the grain size of the not mentioned synthetic NaY of institute molecular sieve.
The purpose of this invention is to provide a kind of by adopting the method that the directed agents technology prepares small crystal grain NaY molecular sieve of improving.This method both can synthesize SiO 2/ Al 2O 3Small crystal grain NaY molecular sieve than≤5 can synthesize SiO again 2/ Al 2O 3Small crystal grain NaY molecular sieve than>5.
The preparation process of the said small crystal grain NaY molecular sieve of the present invention is as follows:
1, prepare conventional directed agents: with modulus be 0.5-3.5, preferably 1.0-3.3 concentration is the heavy % of 20-65, the sodium silicate solution of the heavy % of 25-60 preferably, causticity than for the high alkali deflection aluminium acid sodium solution of 10-12 and deionized water 0-45 ℃, preferably 5-40 ℃ mix stirring 0.5-2 hour, then 15-60 ℃, preferably left standstill aging 6-30 hour at 20-40 ℃, make transmittance<30%, mole consists of (13-36) Na 2O: Al 2O 3: (12-21) SiO 2: (250-800) H 2O, preferably (15-19) Na 2O: Al 2O 3: (14-19) SiO 2: (300-380) H 2The conventional directed agents of O;
2, preparation improves directed agents: the sodium silicate solution that specification is identical with step 1 is pressed 5-80 volume %, preferably the amount of 10-70 volume % joins in the conventional directed agents that step 1 makes, at room temperature placed 0.5-2 hour, and made transmittance>75%, mole consists of (12-180) Na 2O: Al 2O 3: (17-210) SiO 2: (160-3100) H 2O, (16-150) Na preferably 2O: Al 2O 3: (20-180) SiO 2: (250-2500) H 2The improvement directed agents solution of O;
3, sodium silicate solution that specification is identical with step 1, improvement directed agents solution, Al that step 2 makes 2O 3Content is the alum liquor of 0.085-0.095 grams per milliliter and causticity than synthetic according to the NaY hydro-thermal that the preparation method of conventional NaY molecular sieve carries out different ingredients for the low alkali aluminium acid sodium solution of 1.0-3.0, and the add-on of wherein improving directed agents is 0.5-25%, preferably 1.0-20%(is with total Al in the system 2O 3The mole number meter), stirred 0.5-2 hour, be warming up to 95-100 ℃, crystallization 5-35 hour, filter, dry, the NaY zeolite product that makes little crystal grain.
The said employing of the present invention improves directed agents technology synthetic NaY molecular sieve and relatively has the short characteristics of the little crystallization time of crystal grain with adopting conventional directed agents synthetic NaY molecular sieve.
The said sodium silicate solution that joins in the conventional directed agents among the present invention if modulus reduces, just makes the life-span of improving directed agents prolong, and crystallization time shortens, and the crystal grain of NaY zeolite product diminishes.
Said improvement directed agents of the present invention and conventional directed agents relatively have active high, long service life, anti-95 ℃ of characteristics such as left and right sides high temperature.
To improve directed agents and conventional directed agents mix be used in the NaY hydro-thermal synthetic in, the grain size of gained NaY molecular sieve is between using two kinds of directed agents respectively between the grain size of synthetic NaY molecular sieves.
Adopt its SiO of synthetic small crystal grain NaY molecular sieve of the present invention 2/ Al 2O 3Than both can≤5.0, also can>5.0.And the latter also is characteristics of the present invention.
Fig. 1 is the stereoscan photograph (* 9400) of example 4 of the present invention, and its crystal grain diameter is 0.22 micron, SiO 2/ Al 2O 3Than being 5.4;
Fig. 2 is the stereoscan photograph (* 9400) of Comparative Examples 2, and its crystal grain diameter is 0.63 micron, SiO 2/ Al 2O 3Than being 5.4.
The following examples are described further the present invention.
Example one
The preparation of sodium aluminate solution: with sodium hydroxide (medication purchasing supply station, Wenzhou, Zhejiang, chemical pure) is dissolved in the deionized water, evenly add aluminium hydrate powder (Shandong Aluminum Plant then, technical pure), 120 ℃ of reactions 5 hours, treat below the as clear as crystal postcooling to 60 of solution ℃, can be mixed with different causticities than (Na according to the test needs 2O/Al 2O 3Mol ratio) sodium aluminate solution.
With 158 milliliters of sodium silicate solution (moduluses 3.28, proportion 1.261, concentration 27.3 heavy %, the water glass plant, Tianjin) (causticity is than=11.76 with 109 milliliters of high alkali deflection aluminium acid sodium solution, proportion 1.343) and 12 ml deionized water mix to stir 1 hour at 35 ℃, leave standstill at 35 ℃ then and made mole in aging 6 hours and consist of 16Na 2O: Al 2O 3: 15SiO 2: 320H 2O, the conventional directed agents of transmittance<30%.
158 milliliters of specification sodium silicate solutions same as described above are joined in the conventional directed agents by 36.2 volume % amount, and after 1.5 hours, making transmittance is 90% 30 ℃ of placements, and mole consists of 20.6Na 2O: Al 2O 3: 30SiO 2: 495H 2The improvement directed agents solution that O is as clear as crystal uses after room temperature is placed 24 hours.
According to mol ratio is 3.84Na 2O: Al 2O 3: 12SiO 2: 220H 2The NaY hydro-thermal synthesizing formula of O, with 316 milliliters of sodium silicate solutions that specification is same as described above, (add-on of improving directed agents is with total Al in the system for 437 milliliters of above-mentioned improvement directed agents solution that make 2O 3Mole number counts 20%), 204 milliliters of Al 2O 3Content is that (causticity is than 2.45 for the alum liquor (Xian Xingta chemical plant, Kingsoft, Shanghai, chemical pure) of 0.0856 grams per milliliter (proportion=1.262) and 12 milliliters of low alkali aluminium acid sodium solutions, proportion=1.239) mix stirring 1 hour, be warming up to 97 ℃ then, crystallization 26 hours, filtration, drying obtain SiO 2/ Al 2O 3Than being 5.8, the small crystal grain NaY molecular sieve product, analytical results sees Table 1.
In the table 1:
1, x-ray diffraction method is measured the lattice constant of NaY molecular sieve.
Product SiO 2/ Al 2O 3Ratio and crystalline substance bag constant a 0The pass be:
SiO 2/ Al 2O 3Mol ratio=((25.858-a 0) * 2)/((a 0-24.191))
2, the mensuration of outer specific surface data adopts the t-pLot method, and t value scope is the 60-80 nanometer, crystal grain diameter D(micron) with the pass of outer specific surface Sex be:
D Micron=6/ (ρ Sex)
Wherein p is a NaY molecular sieve ideal granule degree, is 1.92 gram per centimeters 3, Sex is an outer specific surface (rice 2/ gram)
3, crystallization time: finish till back 2 hours since 97 ℃ of crystallization to crystallization.
Example 2
Except the add-on of improving directed agents is (with total Al in the system 5.0% 2O 3The mole number meter), other experimental procedure is with example 1, crystallization 34 hours, and the analytical results of products obtained therefrom sees Table 1.
Example 3
Except conventional directed agents digestion time changed into 20 hours by 6 hours, improve the add-on of directed agents, and other experimental procedure is with example 2, product analysis the results are shown in Table 1.
Comparative Examples 1
Except replace improving directed agents with conventional directed agents, other preparation process is with example 2, and the add-on of conventional directed agents is that 5.0%(is with total Al in the system 2O 3The mole number meter), the analytical results of products obtained therefrom sees Table 1.
From the analytical results of example 1-3 and Comparative Examples 1 as can be seen: the NaY molecular sieve that the present invention makes and the NaY molecular sieve that adopts conventional directed agents to make relatively, it is little to have crystal grain, the short characteristics of crystallization time, the SiO of products obtained therefrom 2/ Al 2O 3Ratio can be up to 5.8.As example 2 and Comparative Examples 1SiO 2/ Al 2O 3Than identical (5.8), the directed agents add-on all is that 5.0%(is with Al in the system 2O 3The mole number meter), but the former crystal grain has only 0.16 micron, and the latter but is 0.78 micron; The former is 34 hours for a crystallization time, and the latter is 55 hours (latter's crystallization 34 hours, crystallization are trace).
Example 4
The proportioning of directed agents, raw material and preparation method are with example 1, and the add-on of improving directed agents is that 5%(is with total Al in the system 2O 3The mole number meter), the proportioning of synthetic NaY molecular sieve is 3.0Na 2O: Al 2O 3: 9.4SiO 2: 180H 2O, crystallization 24 hours, other experimental procedure are with example 1, and the analytical results of product sees Table 2, and stereoscan photograph is seen Fig. 1.
Comparative Examples 2
Except replace improving directed agents with conventional directed agents, other preparation process is with example 4, and the add-on of conventional directed agents is that 5.0%(is with total Al in the system 2O 3The mole number meter), the analytical results of product sees Table 2, and stereoscan photograph is seen Fig. 2.
By table 2 and Fig. 1, Fig. 2 as can be seen: the NaY molecular sieve that the present invention makes is with to adopt conventional directed agents synthetic NaY molecular sieve relatively to have crystal grain little, the characteristics that crystallization time is short.As example 4 and Comparative Examples 2, SiO 2/ Al 2O 3Than all is 5.4, example 4 is the NaY molecular sieves that make by the present invention, its crystal grain diameter is 0.22 micron, crystallization time is 24 hours, and Comparative Examples 2 is NaY molecular sieves of making of directed agents routinely, its crystal grain diameter is 0.63 micron, and crystallization time reaches 32 hours (latter's crystallization 24 hours, crystallization are trace).
Figure 921038852_IMG2
Example 5
Conventional directed agents and improvement directed agents preparation method are with example 2, and just improving the directed agents add-on is that 1.0%(is with total Al in the system 2O 3The mole number meter), the proportioning of synthetic NaY molecular sieve is 3.6Na 2O: Al 2O 3: 9.8SiO 2: 202H 2O, crystallization 14 hours, the products obtained therefrom analytical results is: SiO 2/ Al 2O 3Than 4.9; 0.15 micron of crystal grain diameter.
Example 6-9
The proportioning of directed agents, raw material and preparation method are with example 1, and the add-on of improving directed agents is that 20%(is with total Al in the system 2O 3The mole number meter), improve directed agents and be followed successively by 1 hour by example number storage period, 4 hours, 15 hours, 52 hours.
The proportioning of synthetic NaY molecular sieve is 3.6Na 2O: Al 2O 3: 9.8SiO 2: 200H 2O, crystallization 16 hours, other step are with example 1, and the analytical results of product sees Table 3.
Comparative Examples 3
Except replace improving directed agents with conventional directed agents, the proportioning of directed agents, raw material and preparation method are with example 1, and the add-on of conventional directed agents is that 20%(is with total Al in the system 2O 3The mole number meter), the proportioning of synthetic NaY molecular sieve, raw material and preparation method are with example 6, and the analytical results of product sees Table 3.
From the analytical results of example 6-9 and Comparative Examples 3 as can be seen: the improvement directed agents according to example 1 preparation was placed about 50 hours, and the crystal grain of gained NaY molecular sieve is still little than the crystal grain according to the NaY molecular sieve of conventional directed agents preparation.
Figure 921038852_IMG3
Example 10
Conventional directed agents proportioning, raw material and preparation method are with example 1, the specification that joins the sodium silicate solution in the conventional directed agents is with example 1, just add-on is 12.5 volume %, adds the back and places 20 hours, obtains as clear as crystal improvement directed agents solution, its transmittance is 85%, the proportioning of synthetic NaY molecular sieve, raw material and preparation method are with example 2, and 34 hours products obtained therefrom analytical resultss of crystallization see Table 4.
Comparative Examples 4
Except replace improving directed agents with conventional directed agents, other preparation process is with example 2, and the add-on of conventional directed agents is that 5.0%(is with total Al in the system 2O 3The mole number meter), crystallization 34 hours, the analytical results of products obtained therefrom sees Table 4.
As can be seen from Table 4: when crystallization time is 34 hours, the SiO of example 2 and example 10 products 2/ Al 2O 3Than and the grain size basically identical, and Comparative Examples 4 is in the same time, the crystallization of product is a trace, has only the crystallization could crystallization after 55 hours, its crystal grain diameter is 0.78 micron, shown in Comparative Examples 1.
Figure 921038852_IMG4
Annotate ※: Comparative Examples 4 is in 34 hours, and the crystallization of product is a trace.
Example 11
50 milliliters of the sodium silicate solutions that raw material specification and example 1 is identical, 27 milliliters of high alkali deflection aluminium acid sodium solution, 3 milliliters of mixing of deionized water, stirring at normal temperature 1 hour left standstill in 45 ℃ of water-baths aging 12 hours then, and making transmittance is 28%, and mole consists of 17.6Na 2O: Al 2O 3: 19SiO 2: 369H 2The conventional directed agents of O.
With modulus is that 2.0 concentration are 40.1 heavy %, proportion is that 80 milliliters of 1.473 sodium silicate solutions (account for add back cumulative volume 50%) join in the above-mentioned conventional directed agents, obtain transmittance after 1 hour and be 86% as clear as crystal improvement directed agents solution, place after 10 days and use, this moment, transmittance was 91%, and mole consists of 40.4Na 2O: Al 2O 3: 64.7SiO 2: 710H 2O.
The proportioning raw materials preparation method of synthetic NaY molecular sieve is with example 6, and the add-on of improving directed agents is that 5.0%(is with total Al in the system 2O 3The mole number meter), crystallization time is 12 hours, and the analytical results of products obtained therefrom sees Table 5.
Example 12
The modulus of sodium silicate solution is 1.0, and concentration is 40.6 heavy %, and proportion is 1.549, and add-on is 120 milliliters (account for add back cumulative volume 60%), places 15 days, and obtaining transmittance is 92%, mole consists of 72.3Na 2O: Al 2O 3: 73.7SiO 2: 903H 2The as clear as crystal improvement directed agents solution of O.In addition, other preparation process is with example 11, crystallization 10 hours, and the analytical results of products obtained therefrom sees Table 5.
From the analytical results of the NaY zeolite product of example 9,11,12 gained as can be seen: the modulus that joins the sodium silicate solution the conventional directed agents reduces, and improves directed agents and prolongs work-ing life, and crystallization time shortens, and the crystal grain of product diminishes.
Figure 921038852_IMG5
Annotate: the modulus=SiO of ※ sodium silicate solution 2/ Na 2The O mol ratio
Example 13
The improvement directed agents that example 2 is made be heated to 95 ℃ 30 minutes, reduce to normal temperature then and use, other technical recipe and preparation method are with example 4, the analytical results of products obtained therefrom sees Table 6.From the product analysis result of example 13 as can be seen: improve directed agents through 95 ℃ handle 30 minutes after, still can keep the directed agents activity, the performance of product is suitable with example 4.
Example 14
NaY synthesizing formula and preparation method will add respectively according to conventional directed agents and the improvement directed agents that example 4 makes with example 4, and the add-on of mixing directed agents is that 5.0%(is with total Al in the system 2O 3The mole number meter), wherein two kinds of directed agents respectively account for 2.0% and 3.0%, the analytical results of product sees Table 6, from the analytical results of example 14 products as can be seen: with conventional directed agents and improve directed agents mixed its grain size of NaY molecular sieve between distinguishing with two kinds of directed agents between the synthetic NaY zeolite crystal sizes.
Figure 921038852_IMG6
Annotate: mix directed agents and mean conventional directed agents and improve the directed agents that the directed agents mixing is used.
Example 15
The preparation method of conventional directed agents and improvement directed agents is with example 1, and the synthesizing formula of NaY molecular sieve is 4.4Na 2O: Al 2O 3: 10SiO 2: 182H 2O, the add-on of improving directed agents is that 5.0%(is with total Al in the system 2O 3The mole number meter), crystallization 6 hours, the analytical results of products obtained therefrom sees Table 7.
Example 16
The preparation method of conventional directed agents and improvement directed agents is with example 1, and the synthesizing formula of NaY molecular sieve is 3.0Na 2O: Al 2O 3: 6.5SiO 2: 170H 2O, the add-on of improving directed agents is that 5.0%(is with total Al in the system 2O 3The mole number meter), crystallization 10 hours, the analytical results of products obtained therefrom sees Table 7.
As can be seen from Table 7, the present invention can synthesize SiO 2/ Al 2O 3Than≤5, small crystal grain NaY molecular sieve.

Claims (10)

1, a kind of preparation method of small crystal grain NaY molecular sieve is characterized in that:
(1) be that 0.5-3.5, concentration are that the sodium silicate solution, causticity of the heavy % of 20-65 is than mixing stirring 0.5-2 hour for the high alkali deflection aluminium acid sodium solution of 10-12 and deionized water at 0-45 ℃ with modulus, left standstill aging 6-30 hour at 15-60 ℃ then, make transmittance<30%, mole consists of (13-36) Na 2O: Al 2O 3: (12-21) SiO 2: (250-800) H 2The conventional directed agents of O;
(2) sodium silicate solution that specification is identical with (1) joins in the conventional directed agents that (1) make by 5-80 volume % amount, places 0.5-2 hour in room temperature, makes transmittance>75%, mole consists of (12-180) Na 2O: Al 2O 3: (17-210) SiO 2: (160-3100) H 2The improvement directed agents solution of O;
(3) sodium silicate solution that specification is identical with (1) improves directed agents solution, Al 2O 3Content is the alum liquor of 0.085-0.095 grams per milliliter and causticity than synthetic according to the NaY hydro-thermal that the preparation method of conventional NaY molecular sieve carries out different ingredients for the low alkali aluminium acid sodium solution of 1.0-3.0, and the add-on of wherein improving directed agents is that 0.5-25% is (with total Al in the system 2O 3The mole number meter), stirred 0.5-2 hour, be warming up to 95-100 ℃, crystallization 5-35 hour, filter, drying, make the NaY zeolite product of little crystal grain.
2, according to the said preparation method of claim 1, the modulus that it is characterized in that said sodium silicate solution in (1) is 1.0-3.3.
3, according to the said preparation method of claim 1, the concentration that it is characterized in that said sodium silicate solution in (1) is the heavy % of 25-60.
4,, it is characterized in that the mole of the conventional directed agents that makes in (1) consists of (15-19) Na according to the said preparation method of claim 1 2O: Al 2O 3: (14-19) SiO 2: (300-380) H 2O.
5,, it is characterized in that said mixing temperature is 5-40 ℃ in (1) according to the said preparation method of claim 1.
6,, it is characterized in that said aging temperature is 20-40 ℃ in (1) according to the said preparation method of claim 1.
7, according to the said preparation method of claim 1, the add-on that it is characterized in that said sodium silicate solution in (2) is 10-70 volume %.
8,, it is characterized in that the mole of said improvement directed agents solution consists of (16-150) Na in (2) according to the said preparation method of claim 1 2O: Al 2O 3: (20-180) SiO 2: (250-2500) H 2O.
9,, it is characterized in that said improvement directed agents solution can at room temperature be deposited 15 days in (2) according to the said preparation method of claim 1.
10, according to the said preparation method of claim 1, the add-on that it is characterized in that said improvement directed agents solution in (3) is that 1.0-20%(is with total Al in the system 2O 3The mole number meter).
CN 92103885 1992-06-02 1992-06-02 Process for preparation of small crystal grain Na Y molecular sieve Expired - Lifetime CN1033503C (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN 92103885 CN1033503C (en) 1992-06-02 1992-06-02 Process for preparation of small crystal grain Na Y molecular sieve

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN 92103885 CN1033503C (en) 1992-06-02 1992-06-02 Process for preparation of small crystal grain Na Y molecular sieve

Publications (2)

Publication Number Publication Date
CN1079444A true CN1079444A (en) 1993-12-15
CN1033503C CN1033503C (en) 1996-12-11

Family

ID=4940529

Family Applications (1)

Application Number Title Priority Date Filing Date
CN 92103885 Expired - Lifetime CN1033503C (en) 1992-06-02 1992-06-02 Process for preparation of small crystal grain Na Y molecular sieve

Country Status (1)

Country Link
CN (1) CN1033503C (en)

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1050585C (en) * 1996-10-11 2000-03-22 中国石油化工总公司 Method for preparation of Na Y zeolite
CN1058682C (en) * 1996-12-25 2000-11-22 中国石油化工总公司 High efficiency manufacture of NaY zeolite
CN1113814C (en) * 1999-06-05 2003-07-09 中国石化集团齐鲁石油化工公司 Method for preparation of small crystal grain NaY molecular sieve
CN103449469A (en) * 2012-06-01 2013-12-18 中国石油天然气股份有限公司 Preparation method of NaY molecular sieve for improving stability
CN105032472A (en) * 2015-08-05 2015-11-11 湖北赛因化工有限公司 FCC catalyst preparation method reducing ex situ crystallization reaction products
CN106673031A (en) * 2015-11-09 2017-05-17 中国石油化工股份有限公司 NaY molecular sieve and alumina compound and preparation method thereof
CN107519924A (en) * 2016-06-21 2017-12-29 中国石油天然气股份有限公司 Y/EU-1/ZSM-23/ZSM-5/ASA composite material and preparation method thereof
CN107519921A (en) * 2016-06-21 2017-12-29 中国石油天然气股份有限公司 Y/Sm2O3ZSM-22/ZSM-5/ASA composite material and preparation method thereof
CN107519933A (en) * 2016-06-21 2017-12-29 中国石油天然气股份有限公司 Y/EU-1/SBA-15/ASA/MOF composite material and preparation method thereof
CN107519938A (en) * 2016-06-21 2017-12-29 中国石油天然气股份有限公司 Y/CeO2SBA-15/ASA/MOF composite material and preparation method thereof
CN107519927A (en) * 2016-06-21 2017-12-29 中国石油天然气股份有限公司 Y/ZSM-22/SAPO-34/ASA/MOF composite material and preparation method thereof
CN107519922A (en) * 2016-06-21 2017-12-29 中国石油天然气股份有限公司 Y/Gd2O3ZSM-23/ZSM-5/ASA composite material and preparation method thereof

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP4257551A1 (en) 2021-01-07 2023-10-11 China Petroleum & Chemical Corporation Y-type molecular sieve and synthesis method therefor

Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1050585C (en) * 1996-10-11 2000-03-22 中国石油化工总公司 Method for preparation of Na Y zeolite
CN1058682C (en) * 1996-12-25 2000-11-22 中国石油化工总公司 High efficiency manufacture of NaY zeolite
CN1113814C (en) * 1999-06-05 2003-07-09 中国石化集团齐鲁石油化工公司 Method for preparation of small crystal grain NaY molecular sieve
CN103449469A (en) * 2012-06-01 2013-12-18 中国石油天然气股份有限公司 Preparation method of NaY molecular sieve for improving stability
CN103449469B (en) * 2012-06-01 2016-05-11 中国石油天然气股份有限公司 Preparation method of NaY molecular sieve for improving stability
CN105032472A (en) * 2015-08-05 2015-11-11 湖北赛因化工有限公司 FCC catalyst preparation method reducing ex situ crystallization reaction products
CN106673031A (en) * 2015-11-09 2017-05-17 中国石油化工股份有限公司 NaY molecular sieve and alumina compound and preparation method thereof
CN106673031B (en) * 2015-11-09 2018-06-19 中国石油化工股份有限公司 A kind of NaY molecular sieve and alumina compound and preparation method thereof
CN107519938A (en) * 2016-06-21 2017-12-29 中国石油天然气股份有限公司 Y/CeO2SBA-15/ASA/MOF composite material and preparation method thereof
CN107519933A (en) * 2016-06-21 2017-12-29 中国石油天然气股份有限公司 Y/EU-1/SBA-15/ASA/MOF composite material and preparation method thereof
CN107519921A (en) * 2016-06-21 2017-12-29 中国石油天然气股份有限公司 Y/Sm2O3ZSM-22/ZSM-5/ASA composite material and preparation method thereof
CN107519927A (en) * 2016-06-21 2017-12-29 中国石油天然气股份有限公司 Y/ZSM-22/SAPO-34/ASA/MOF composite material and preparation method thereof
CN107519922A (en) * 2016-06-21 2017-12-29 中国石油天然气股份有限公司 Y/Gd2O3ZSM-23/ZSM-5/ASA composite material and preparation method thereof
CN107519924A (en) * 2016-06-21 2017-12-29 中国石油天然气股份有限公司 Y/EU-1/ZSM-23/ZSM-5/ASA composite material and preparation method thereof
CN107519938B (en) * 2016-06-21 2019-10-11 中国石油天然气股份有限公司 Y/CeO2SBA-15/ASA/MOF composite material and preparation method thereof
CN107519933B (en) * 2016-06-21 2019-10-11 中国石油天然气股份有限公司 Y/EU-1/SBA-15/ASA/MOF composite material and preparation method thereof
CN107519922B (en) * 2016-06-21 2019-10-11 中国石油天然气股份有限公司 Y/Gd2O3ZSM-23/ZSM-5/ASA composite material and preparation method thereof
CN107519924B (en) * 2016-06-21 2019-10-11 中国石油天然气股份有限公司 Y/EU-1/ZSM-23/ZSM-5/ASA composite material and preparation method thereof
CN107519921B (en) * 2016-06-21 2019-10-11 中国石油天然气股份有限公司 Y/Sm2O3ZSM-22/ZSM-5/ASA composite material and preparation method thereof
CN107519927B (en) * 2016-06-21 2019-10-11 中国石油天然气股份有限公司 Y/ZSM-22/SAPO-34/ASA/MOF composite material and preparation method thereof

Also Published As

Publication number Publication date
CN1033503C (en) 1996-12-11

Similar Documents

Publication Publication Date Title
CN1034718C (en) Cracking catalyst and preparing process thereof
CN1033503C (en) Process for preparation of small crystal grain Na Y molecular sieve
CN1059133C (en) Phosphorus containing molecular sieve with MFI structure
CN1915819A (en) Method for preparing ZSM-5 zeolite in small crystal grain
CN103204515A (en) Preparation method for high-dispersion zeolite molecular sieves
CN1435374A (en) Combined molecular sieve and preparation method thereof
CN1789125A (en) Small crystal grain molecular sieve preparation method
CN1785807A (en) High-silica-alumina-ratio small-crystal-grain NaY molecular sieve
CN1267345C (en) Preparation method of NaY molecular sieve
CN1072031C (en) Preparation method for penta-basic cyclic molecular sieve composite
CN1552801A (en) Catalytic cracking catalyst and preparing method thereof
CN1162327C (en) Rare-earth Y-type zeolite
CN102198950A (en) Preparation method of NaY molecular sieve with high silicon-aluminum ratio
CN1669925A (en) Preparation method of L zeolite with high silicon aluminum ratio
CN1660496A (en) REY molecular sieve containing phosphor and amorphous silica, preparation method and application
CN1699171A (en) Manufacturing process of 4A type molecular sieve primary powder with low bulk density
CN1007879B (en) Cracking catalyst of clay molecular sieve with layer structure
CN1062750A (en) The cracking catalyst of phosphorous and hyperastable Y-type RE zeolite
CN86107531A (en) Contain the molecular sieve and the preparation thereof of rare earth oxide
CN1034680A (en) The rich silicon molecular sieve by crystal Cracking catalyst that contains rare earth
CN1132898C (en) Petroleum catalytic cracking catalyst
CN1242917C (en) Small moleoule rare-earth atom containing composite molecular sieve and preparing method thereof
CN1063680C (en) Catalytic cracking catalyst and its preparation
CN1023639C (en) Formula for L-zeolite molecular sieve guiding agent and compounding method thereof
CN1055062C (en) Method for synthesis of small granular NaY molecular sieve

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
C15 Extension of patent right duration from 15 to 20 years for appl. with date before 31.12.1992 and still valid on 11.12.2001 (patent law change 1993)
OR01 Other related matters
C17 Cessation of patent right
CX01 Expiry of patent term

Expiration termination date: 20120602

Granted publication date: 19961211