CN1393402A - Process for preparing nano Y zeolite molecular sieve carried by kaolin microspheres - Google Patents
Process for preparing nano Y zeolite molecular sieve carried by kaolin microspheres Download PDFInfo
- Publication number
- CN1393402A CN1393402A CN 01114194 CN01114194A CN1393402A CN 1393402 A CN1393402 A CN 1393402A CN 01114194 CN01114194 CN 01114194 CN 01114194 A CN01114194 A CN 01114194A CN 1393402 A CN1393402 A CN 1393402A
- Authority
- CN
- China
- Prior art keywords
- molecular sieve
- kaolin microspheres
- solution
- zeolite molecular
- weight ratio
- 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
Links
- 239000005995 Aluminium silicate Substances 0.000 title claims abstract description 36
- 235000012211 aluminium silicate Nutrition 0.000 title claims abstract description 36
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 title claims abstract description 36
- 239000002808 molecular sieve Substances 0.000 title claims abstract description 35
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 title claims abstract description 35
- 239000004005 microsphere Substances 0.000 title claims abstract description 32
- 229910021536 Zeolite Inorganic materials 0.000 title claims abstract description 30
- 239000010457 zeolite Substances 0.000 title claims abstract description 30
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title claims abstract description 25
- 238000004519 manufacturing process Methods 0.000 title 1
- 238000003756 stirring Methods 0.000 claims abstract description 21
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 19
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000002360 preparation method Methods 0.000 claims abstract description 10
- 239000001509 sodium citrate Substances 0.000 claims abstract description 9
- NLJMYIDDQXHKNR-UHFFFAOYSA-K sodium citrate Chemical compound O.O.[Na+].[Na+].[Na+].[O-]C(=O)CC(O)(CC([O-])=O)C([O-])=O NLJMYIDDQXHKNR-UHFFFAOYSA-K 0.000 claims abstract description 9
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 30
- 239000013078 crystal Substances 0.000 claims description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 8
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims description 7
- 230000032683 aging Effects 0.000 claims description 5
- 238000000926 separation method Methods 0.000 claims description 4
- 238000001035 drying Methods 0.000 claims description 2
- 238000000967 suction filtration Methods 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- 239000000843 powder Substances 0.000 description 7
- 238000011065 in-situ storage Methods 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 3
- 238000002425 crystallisation Methods 0.000 description 3
- 230000008025 crystallization Effects 0.000 description 3
- 238000010335 hydrothermal treatment Methods 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000004523 catalytic cracking Methods 0.000 description 1
- 239000002283 diesel fuel Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 238000001228 spectrum Methods 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
Images
Landscapes
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
一种高岭土微球担载纳米沸石分子筛Y的制备方法。其步骤:1)制备导向剂;2)取导向剂加入柠檬酸钠,磁力搅拌1.5~3小时;其导向剂与柠檬酸钠重量比为65~75∶2.5~3.5;3)将焙烧后的高岭土微球加入步骤2)溶液中,机械搅拌,加入量与所述溶液的重量比为65~75∶4~15;4)滴入硫酸溶液,滴入量为步骤3)中所述溶液重量的23~32%,浓度为28~32%,得到凝胶,振荡均匀后于90~110℃下晶化;5)取上述产物进行分离得到高岭土微球担载纳米沸石分子筛Y产物。它水热稳定性好。A preparation method of nano zeolite molecular sieve Y loaded on kaolin microspheres. Its steps: 1) preparing the guiding agent; 2) taking the guiding agent and adding sodium citrate, stirring magnetically for 1.5-3 hours; the weight ratio of the guiding agent and sodium citrate is 65-75:2.5-3.5; 3) roasting the Kaolin microspheres are added to the solution in step 2), and mechanically stirred, the weight ratio of the amount added to the solution is 65-75: 4-15; 4) sulfuric acid solution is added dropwise, and the amount added is the weight of the solution described in step 3) 23% to 32% of the concentration, and the concentration is 28% to 32%, to obtain a gel, shake evenly and crystallize at 90°C to 110°C; 5) separate the above product to obtain the nano zeolite molecular sieve Y product supported by kaolin microspheres. It has good hydrothermal stability.
Description
本发明涉及原位合成担载的纳米沸石分子筛Y晶粒催化剂,具体地说是一种高岭土微球担载纳米沸石分子筛Y的制备方法。The invention relates to in-situ synthesis and supported nanometer zeolite molecular sieve Y grain catalyst, in particular to a preparation method of nanometer zeolite molecular sieve Y supported by kaolin microspheres.
沸石分子筛Y与高岭土混合成型的催化剂在催化裂化过程中有重要应用。纳米沸石分子筛Y制成催化剂可以提高柴油产率,但水热稳定性有待改善。在现有技术中,纳米沸石Y分子筛制备过程存在分离困难问题,难以工业应用;纳米沸石Y分子筛水热稳定性差也是制约其应用的一个重要原因。另外在高岭土浆中加入导向剂或晶种后,喷雾干燥成高岭土微球,在合成沸石分子筛Y的体系中,合成得到含沸石分子筛Y40%的产物。例如:美国专利(专利号4493902,申请日1985年1月15日)公开了一种在高岭土微球上原位晶化合成沸石分子筛Y晶粒的方法,其特点是在高岭土微球成型前加入所谓的晶种,然后原位晶化形成沸石分子筛Y。The catalyst mixed with zeolite molecular sieve Y and kaolin has important application in catalytic cracking process. Catalyst made of nano zeolite molecular sieve Y can increase the yield of diesel oil, but the hydrothermal stability needs to be improved. In the prior art, the preparation process of nano-zeolite Y molecular sieve has the problem of difficult separation and industrial application; the poor hydrothermal stability of nano-zeolite Y molecular sieve is also an important reason restricting its application. In addition, after adding a directing agent or seed crystal into the kaolin slurry, it is spray-dried into kaolin microspheres, and in a system for synthesizing zeolite molecular sieve Y, a product containing 40% of zeolite molecular sieve Y is synthesized. For example: U.S. Patent (Patent No. 4493902, date of application on January 15, 1985) discloses a method for in-situ crystallization on kaolin microspheres to synthesize zeolite molecular sieve Y grains, which is characterized in that it is added before kaolin microspheres are formed. The so-called seed crystals are then crystallized in situ to form zeolite molecular sieve Y.
本发明的目的是提供一种分离容易、水热稳定性好的高岭土微球担载纳米沸石分子筛Y的制备方法。The object of the present invention is to provide a preparation method of nano zeolite molecular sieve Y loaded on kaolin microspheres with easy separation and good hydrothermal stability.
本发明的技术方案是:在高岭土微球上生长晶粒,具体步骤为:The technical scheme of the present invention is: crystal grain is grown on the kaolin microsphere, and concrete steps are:
(1)制备导向剂:(1) Preparation of directing agent:
1)称取28~32%浓度的硅溶胶,按55~65∶15~25的重量比加入NaOH,振荡溶解;1) Weigh silica sol with a concentration of 28-32%, add NaOH in a weight ratio of 55-65:15-25, and shake to dissolve;
2)按重量比40~45∶10~15∶8~12另称取水,加入Al2(SO4)3·18H2O和NaOH,搅拌溶解;28~32%浓度的硅溶胶和Al2(SO4)3·18H2O的重量比为55~65∶10~15;2) Separately weigh water according to the weight ratio of 40~45:10~15:8~12, add Al 2 (SO 4 ) 3 ·18H 2 O and NaOH, stir and dissolve; 28-32% concentration of silica sol and Al 2 ( The weight ratio of SO 4 ) 3 ·18H 2 O is 55~65:10~15;
3)将步骤2)中所述溶液加入步骤1)所述溶液中,磁力搅拌1~3小时,室温老化1~15天,制成导向剂;3) adding the solution described in step 2) into the solution described in step 1), stirring magnetically for 1 to 3 hours, and aging at room temperature for 1 to 15 days to make a directing agent;
(2)取上述导向剂加入柠檬酸钠,磁力搅拌1.5~3小时;其中导向剂与柠檬酸钠重量比为65~75∶2.5~3.5;(2) Take the above-mentioned directing agent and add sodium citrate, and magnetically stir for 1.5 to 3 hours; wherein the weight ratio of directing agent to sodium citrate is 65 to 75: 2.5 to 3.5;
(3)将600~650℃焙烧后的高岭土微球加入步骤(2)溶液中,机械搅拌5~8小时,加入量与所述溶液的重量比为4~15∶65~75;(3) Add the kaolin microspheres roasted at 600-650°C to the solution of step (2), and mechanically stir for 5-8 hours, the weight ratio of the amount added to the solution is 4-15: 65-75;
(4)滴入硫酸溶液,滴入量为步骤(3)中所述溶液重量的23~32%,浓度为28~32%,得到凝胶,振荡均匀后于90~110℃下晶化8~12小时;(4) drop into sulfuric acid solution, the drop-in amount is 23~32% of the solution weight described in the step (3), and concentration is 28~32%, obtains gel, crystallizes at 90~110 ℃ after oscillating evenly 8 ~12 hours;
(5)取出上述产物进行分离、抽滤、洗涤、干燥,得到含沸石晶粒的生长产物。(5) The above product is taken out for separation, suction filtration, washing and drying to obtain a growth product containing zeolite crystal grains.
本发明具有如下优点:The present invention has the following advantages:
1.过程简单。本发明使用高碱性导向剂与担载的沸石分子筛Y晶粒作用,在高岭土微球上能生长出80~200纳米的沸石分子筛Y晶粒。1. The process is simple. The invention uses the highly basic directing agent to interact with the loaded zeolite molecular sieve Y crystal grains, and the 80-200 nanometer zeolite molecular sieve Y crystal grains can be grown on the kaolin microspheres.
2.水热稳定性好。采用本发明制备沸石分子筛Y晶粒生长于高岭土微球上,该担载的沸石分子筛Y晶粒的水热稳定性好,明显高于非生长在高岭土微球上的分子筛Y晶粒的水热稳定性(见图1)。非生长在高岭土微球上的分子筛Y经650℃水热处理后分子筛的结晶度几乎全部丧失,说明大部分转化为无定型物质,其水热稳定性差;而担载的沸石分子筛Y在650℃水热处理后结晶度变化不大。2. Good hydrothermal stability. The zeolite molecular sieve Y crystal grains prepared by the present invention are grown on kaolin microspheres, and the hydrothermal stability of the zeolite molecular sieve Y crystal grains carried is good, which is obviously higher than that of molecular sieve Y crystal grains not grown on kaolin microspheres. Stability (see Figure 1). Molecular sieve Y not grown on kaolin microspheres lost almost all of its crystallinity after hydrothermal treatment at 650°C, indicating that most of it was transformed into an amorphous substance, and its hydrothermal stability was poor; while the supported zeolite molecular sieve Y There is little change in crystallinity after heat treatment.
3.分离容易。由于本发明采用直接将纳米Y晶粒生长在高岭土微球上措施,解决了工业上大规模生产纳米分子筛中难以过滤的问题。3. Easy to separate. Since the invention adopts the measure of directly growing the nanometer Y grains on the kaolin microspheres, the problem of difficulty in filtering in the large-scale industrial production of nanometer molecular sieves is solved.
图1为本发明实施例1的Y分子筛结晶度X-射线衍射(XRD)谱图。Fig. 1 is an X-ray diffraction (XRD) spectrum of crystallinity of Y molecular sieve according to Example 1 of the present invention.
下面结合实施例和附图详述本发明。The present invention is described in detail below in conjunction with embodiment and accompanying drawing.
实施例1Example 1
在高岭土微球上生长晶粒,具体步骤为:To grow crystal grains on kaolin microspheres, the specific steps are:
(1)制备导向剂:(1) Preparation of directing agent:
称60.1g 30%的硅溶胶到250ml圆底烧杯中,加入19.5g NaOH,振荡使安全溶解;取小烧杯,称42g水,加入12.5g的Al2(SO4)3·18H2O,9g NaOH,搅拌使完全溶解;然后,加入到前面250ml圆底烧杯中,磁力搅拌1小时,室温老化5天;Weigh 60.1g of 30% silica sol into a 250ml round bottom beaker, add 19.5g of NaOH, shake to dissolve safely; take a small beaker, weigh 42g of water, add 12.5g of Al 2 (SO 4 ) 3 18H 2 O, 9g NaOH, stir to dissolve completely; then, add it to the previous 250ml round bottom beaker, stir it magnetically for 1 hour, and age at room temperature for 5 days;
(2)取71.6g老化后的导向剂,加入2.8g柠檬酸钠,磁力搅拌2小时;(2) Take 71.6g of the aging guiding agent, add 2.8g of sodium citrate, and stir magnetically for 2 hours;
(3)将600℃焙烧后的高岭土微球6.0g加入到步骤(2)烧杯中,机械搅拌6小时;(3) Add 6.0 g of kaolin microspheres roasted at 600° C. to the beaker of step (2), and mechanically stir for 6 hours;
(4)滴入配好的硫酸溶液(已标定的98%浓硫酸15.4g,稀释到35.6g水中)25.5g,将得到的凝胶振荡均匀,于100℃下晶化10小时;(4) 25.5 g of prepared sulfuric acid solution (15.4 g of calibrated 98% concentrated sulfuric acid, diluted into 35.6 g of water) was added dropwise, the obtained gel was shaken evenly, and crystallized at 100° C. for 10 hours;
(5)取出分离、抽滤、洗涤,120℃烘箱内干燥,得到高岭土微球担载纳米沸石分子筛Y的粉体(c)产物约4克,含沸石分子筛Y晶粒约20%,晶粒大小为100~200nm;及没在高岭土微球上生长的纳米沸石分子筛Y的粉体(a)。(5) Take out and separate, suction filter, wash, and dry in an oven at 120°C to obtain about 4 grams of powder (c) product of kaolin microspheres loaded with nano zeolite molecular sieve Y, containing about 20% of zeolite molecular sieve Y crystal grains, and The size is 100-200nm; and the powder (a) of nano zeolite molecular sieve Y not grown on kaolin microspheres.
如图1所示,实施例1中获得的纳米Y粉体(a),在650℃采用100%水气处理2小时后得到纳米Y粉体(b)。实施例1原位晶化制备的高岭土微球担载纳米Y(c),在650℃采用100%水气处理2小时后得到高岭土微球担载纳米Y(d)。图1比较了Y分子筛结晶度的变化。可以看出,非生长在高岭土微球上的分子筛Y经650℃水热处理后分子筛的结晶度几乎全部丧失,说明大部分转化为无定型物质,其水热稳定性差;而担载的沸石分子筛Y在650℃水热处理后结晶度变化不大。因此,原位晶化制备的高岭土微球担载纳米Y比纳米Y粉体的稳定性好。As shown in FIG. 1 , the nano Y powder (a) obtained in Example 1 was treated with 100% water vapor at 650° C. for 2 hours to obtain the nano Y powder (b). The kaolin microsphere-supported nano-Y (c) prepared by in-situ crystallization in Example 1 was treated with 100% water vapor at 650° C. for 2 hours to obtain the kaolin microsphere-supported nano-Y (d). Figure 1 compares the changes in the crystallinity of Y molecular sieves. It can be seen that the crystallinity of molecular sieve Y not grown on kaolin microspheres is almost completely lost after hydrothermal treatment at 650 °C, indicating that most of them are transformed into amorphous substances, and their hydrothermal stability is poor; while the supported zeolite molecular sieve Y The crystallinity did not change much after hydrothermal treatment at 650 °C. Therefore, the kaolin microspheres prepared by in-situ crystallization are more stable than the nano-Y powder loaded with nano-Y.
实施例2Example 2
在高岭土微球上生长晶粒,具体步骤为:To grow grains on kaolin microspheres, the specific steps are:
(1)制备导向剂:(1) Preparation of directing agent:
称57g 32%的硅溶胶到250ml圆底烧杯中,加入25g NaOH,振荡使安全溶解;取小烧杯,称40g水,加入15g的Al2(SO4)3·18H2O,12g NaOH,搅拌使完全溶解;然后,加入到前面250ml圆底烧杯中,磁力搅拌1小时,室温老化15天;Weigh 57g of 32% silica sol into a 250ml round bottom beaker, add 25g of NaOH, shake to dissolve safely; take a small beaker, weigh 40g of water, add 15g of Al 2 (SO 4 ) 3 18H 2 O, 12g of NaOH, stir Make it completely dissolved; then, add it to the previous 250ml round bottom beaker, stir it magnetically for 1 hour, and age it at room temperature for 15 days;
(2)取65g老化后的导向剂,加入3.5g柠檬酸钠,磁力搅拌3小时;(2) Take 65g of the aging guiding agent, add 3.5g of sodium citrate, and stir magnetically for 3 hours;
(3)将650℃焙烧后的高岭土微球10.0g加入到步骤(2)烧杯中,机械搅拌8小时;(3) Add 10.0 g of kaolin microspheres calcined at 650° C. into the beaker of step (2), and mechanically stir for 8 hours;
(4)滴入配好的硫酸溶液(32%浓度)18g,将得到的凝胶振荡均匀,于110℃下晶化8小时;(4) 18 g of prepared sulfuric acid solution (32% concentration) was added dropwise, the obtained gel was shaken evenly, and crystallized at 110° C. for 8 hours;
(5)取出分离、抽滤、洗涤,120℃烘箱内干燥,得到为高岭土微球上生长的纳米沸石分子筛Y的粉体产物约7克,含沸石分子筛Y晶粒约20%,晶粒大小为80~150nm。(5) Take out and separate, suction filter, wash, and dry in an oven at 120° C. to obtain about 7 grams of a powder product of nano-zeolite molecular sieve Y grown on kaolin microspheres, containing about 20% of zeolite molecular sieve Y grains, and the grain size It is 80~150nm.
实施例3Example 3
在高岭土微球上生长晶粒,具体步骤为:To grow crystal grains on kaolin microspheres, the specific steps are:
(1)制备导向剂:(1) Preparation of directing agent:
称65g 28%的硅溶胶到250ml圆底烧杯中,加入15g NaOH,振荡使安全溶解;取小烧杯,称45g水,加入10g的Al2(SO4)3·18H2O,11g NaOH,搅拌使完全溶解;然后,加入到前面250ml圆底烧杯中,磁力搅拌1小时,室温老化8天;Weigh 65g of 28% silica sol into a 250ml round bottom beaker, add 15g of NaOH, shake to dissolve safely; take a small beaker, weigh 45g of water, add 10g of Al 2 (SO 4 ) 3 18H 2 O, 11g of NaOH, stir Make it completely dissolved; then, add it to the previous 250ml round bottom beaker, stir it magnetically for 1 hour, and age it at room temperature for 8 days;
(2)取75g老化后的导向剂,加入2.5g柠檬酸钠,磁力搅拌1.5小时;(2) Take 75g of the aging guiding agent, add 2.5g of sodium citrate, and stir magnetically for 1.5 hours;
(3)将630℃焙烧后的高岭土微球4.0g加入到步骤(2)烧杯中,机械搅拌5小时;(3) Add 4.0 g of kaolin microspheres roasted at 630° C. into the beaker of step (2), and stir mechanically for 5 hours;
(4)滴入配好的硫酸溶液(浓度28%)22.4g,将得到的凝胶振荡均匀,于90℃下晶化12小时;(4) 22.4 g of prepared sulfuric acid solution (concentration 28%) was added dropwise, the obtained gel was shaken evenly, and crystallized at 90° C. for 12 hours;
(5)取出分离、抽滤、洗涤,120℃烘箱内干燥,得到为高岭土微球上生长的纳米沸石分子筛Y的粉体产物约3克,含沸石分子筛Y晶粒约20%,晶粒大小为10~200nm。(5) Take out and separate, suction filter, wash, and dry in an oven at 120° C. to obtain about 3 grams of a powder product of nano-zeolite molecular sieve Y grown on kaolin microspheres, containing about 20% of zeolite molecular sieve Y grains, and the grain size 10-200nm.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01114194 CN1204969C (en) | 2001-07-04 | 2001-07-04 | Preparation method of nano zeolite molecular sieve Y supported by kaolin microspheres |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 01114194 CN1204969C (en) | 2001-07-04 | 2001-07-04 | Preparation method of nano zeolite molecular sieve Y supported by kaolin microspheres |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1393402A true CN1393402A (en) | 2003-01-29 |
| CN1204969C CN1204969C (en) | 2005-06-08 |
Family
ID=4660863
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 01114194 Expired - Fee Related CN1204969C (en) | 2001-07-04 | 2001-07-04 | Preparation method of nano zeolite molecular sieve Y supported by kaolin microspheres |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN1204969C (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7067449B2 (en) | 2003-03-28 | 2006-06-27 | China Petroleum & Chemical Corporation | Y-zeolite-containing composite material and a process for preparing the same |
| CN1313207C (en) * | 2004-02-13 | 2007-05-02 | 中国石油天然气集团公司 | Method for preparing uniform nanometer molecular sieve material with high catalytic activity |
| CN102049278B (en) * | 2009-10-27 | 2012-08-29 | 中国石油化工股份有限公司 | Small-grain Y-type molecular sieve dispersing material |
| CN112642393A (en) * | 2019-10-10 | 2021-04-13 | 中国石油化工股份有限公司 | Y molecular sieve and preparation method thereof |
-
2001
- 2001-07-04 CN CN 01114194 patent/CN1204969C/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7067449B2 (en) | 2003-03-28 | 2006-06-27 | China Petroleum & Chemical Corporation | Y-zeolite-containing composite material and a process for preparing the same |
| CN1313207C (en) * | 2004-02-13 | 2007-05-02 | 中国石油天然气集团公司 | Method for preparing uniform nanometer molecular sieve material with high catalytic activity |
| CN102049278B (en) * | 2009-10-27 | 2012-08-29 | 中国石油化工股份有限公司 | Small-grain Y-type molecular sieve dispersing material |
| CN112642393A (en) * | 2019-10-10 | 2021-04-13 | 中国石油化工股份有限公司 | Y molecular sieve and preparation method thereof |
| CN112642393B (en) * | 2019-10-10 | 2023-08-08 | 中国石油化工股份有限公司 | Y molecular sieve and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1204969C (en) | 2005-06-08 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103482645A (en) | Preparation method for nanometer mordenite molecular sieve with multi-stage holes | |
| CN115924963B (en) | Preparation method for synthesizing tetragonal phase nano barium titanate by hydrothermal method, tetragonal phase nano barium titanate and application thereof | |
| JP3066430B2 (en) | Method for producing zeolite X-shaped compact | |
| CN102060308B (en) | Synthesis method of nano fibrous mordenite | |
| CN1666956A (en) | A kind of synthesis method of nanometer size mordenite | |
| CN113233472B (en) | Synthesis method of nano small-grain ZSM-22 molecular sieve | |
| CN1393402A (en) | Process for preparing nano Y zeolite molecular sieve carried by kaolin microspheres | |
| CN1631773A (en) | Preparation method of hydroxyapatite | |
| CN110240175A (en) | A kind of method of hydrothermal fluorine-free synthetic pure silicon CHA molecular sieve | |
| MX2010010429A (en) | Method for crystallization of 2-amino-2-[2-[4-(3- benzyloxyphenylthio)-2-chlorophenyl]ethyl]-1,3-propanediol hydrochloride. | |
| CN1216801C (en) | Preparation method of titanium silicon moleculor sieve | |
| CN118179480A (en) | Corn stalk-based carbon-doped nano-semiconductor composite material and its preparation method and application | |
| CN1568305A (en) | New anhydrous crystalline forms of gabapentin | |
| CN1281502C (en) | Micrometre grade thin diaspore preparation method | |
| CN102049278B (en) | Small-grain Y-type molecular sieve dispersing material | |
| KR102416759B1 (en) | Method for synthesizing CHA zeolite and CHA zeolite with large particle size therefrom | |
| CN1793101A (en) | Process for hydrothermal synthesizing bismuth citrate | |
| JPH1192137A (en) | Production of aluminum fluoride particles | |
| CN1053635C (en) | Water-heating preparation method for fluoride and composite fluoride material under mild condition | |
| CN113277529A (en) | Zinc-doped AlPO-36 molecular sieve single crystal and preparation method thereof | |
| CN1159218C (en) | The synthetic method of MFI crystal structure chromium silicon molecular sieve | |
| CN1189393C (en) | Method for preparing MCM-48 mesoporous molecular sieve | |
| CN115010594A (en) | Preparation method of charcoal-shaped manganese oxalate crystals | |
| CN1074749C (en) | Super macroporous molecular sieve modifying method | |
| KR101287424B1 (en) | A preparation of crystalline form I of glyceryl phosphoryl choline |
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 | ||
| C19 | Lapse of patent right due to non-payment of the annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |