CN1088625C - 一步法合成不同比例一、二、三取代烷基酚用催化剂 - Google Patents
一步法合成不同比例一、二、三取代烷基酚用催化剂 Download PDFInfo
- Publication number
- CN1088625C CN1088625C CN95112801A CN95112801A CN1088625C CN 1088625 C CN1088625 C CN 1088625C CN 95112801 A CN95112801 A CN 95112801A CN 95112801 A CN95112801 A CN 95112801A CN 1088625 C CN1088625 C CN 1088625C
- Authority
- CN
- China
- Prior art keywords
- phenol
- acid
- heteropolyacid
- catalyst
- catalyzer
- 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.)
- Expired - Fee Related
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 14
- 238000000034 method Methods 0.000 title claims abstract description 9
- 230000002194 synthesizing effect Effects 0.000 title description 2
- 229910052750 molybdenum Inorganic materials 0.000 claims abstract description 4
- 229910052721 tungsten Inorganic materials 0.000 claims abstract description 4
- 229910052785 arsenic Inorganic materials 0.000 claims abstract description 3
- 229910052796 boron Inorganic materials 0.000 claims abstract description 3
- 229910052732 germanium Inorganic materials 0.000 claims abstract description 3
- 229910052698 phosphorus Inorganic materials 0.000 claims abstract description 3
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 3
- 229910052720 vanadium Inorganic materials 0.000 claims abstract description 3
- 150000003839 salts Chemical class 0.000 claims abstract 3
- 238000006243 chemical reaction Methods 0.000 claims description 9
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 claims description 8
- 239000011964 heteropoly acid Substances 0.000 claims description 7
- -1 substituted alkyl phenol Chemical compound 0.000 claims description 7
- 238000002360 preparation method Methods 0.000 claims description 6
- 230000002378 acidificating effect Effects 0.000 claims description 5
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims description 4
- 150000001336 alkenes Chemical class 0.000 claims description 4
- 239000003456 ion exchange resin Substances 0.000 claims description 4
- 229920003303 ion-exchange polymer Polymers 0.000 claims description 4
- 239000007864 aqueous solution Substances 0.000 claims description 2
- 239000011230 binding agent Substances 0.000 claims description 2
- 230000015572 biosynthetic process Effects 0.000 claims description 2
- 238000007598 dipping method Methods 0.000 claims description 2
- 238000001035 drying Methods 0.000 claims description 2
- 238000001125 extrusion Methods 0.000 claims description 2
- 150000002989 phenols Chemical class 0.000 claims description 2
- 238000003786 synthesis reaction Methods 0.000 claims description 2
- 238000007669 thermal treatment Methods 0.000 claims description 2
- 239000000470 constituent Substances 0.000 claims 2
- 150000003440 styrenes Chemical class 0.000 claims 1
- 239000010457 zeolite Substances 0.000 abstract description 6
- 229910021536 Zeolite Inorganic materials 0.000 abstract description 5
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 abstract description 5
- 239000011973 solid acid Substances 0.000 abstract description 5
- 229910052782 aluminium Inorganic materials 0.000 abstract description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 abstract description 3
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 abstract description 3
- 239000002253 acid Substances 0.000 abstract description 3
- 239000004927 clay Substances 0.000 abstract description 2
- 239000011347 resin Substances 0.000 abstract description 2
- 229920005989 resin Polymers 0.000 abstract description 2
- 239000000741 silica gel Substances 0.000 abstract description 2
- 229910002027 silica gel Inorganic materials 0.000 abstract description 2
- 239000000969 carrier Substances 0.000 abstract 2
- 229910052742 iron Inorganic materials 0.000 abstract 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 abstract 1
- 229910016287 MxOy Inorganic materials 0.000 abstract 1
- 229910003202 NH4 Inorganic materials 0.000 abstract 1
- 229910052788 barium Inorganic materials 0.000 abstract 1
- 229910052792 caesium Inorganic materials 0.000 abstract 1
- 229910052802 copper Inorganic materials 0.000 abstract 1
- 229910044991 metal oxide Inorganic materials 0.000 abstract 1
- 150000004706 metal oxides Chemical class 0.000 abstract 1
- 229910052759 nickel Inorganic materials 0.000 abstract 1
- 229910052709 silver Inorganic materials 0.000 abstract 1
- 238000002791 soaking Methods 0.000 abstract 1
- 239000011949 solid catalyst Substances 0.000 abstract 1
- 239000001117 sulphuric acid Substances 0.000 abstract 1
- 235000011149 sulphuric acid Nutrition 0.000 abstract 1
- 229910052718 tin Inorganic materials 0.000 abstract 1
- 229910052719 titanium Inorganic materials 0.000 abstract 1
- 229910052725 zinc Inorganic materials 0.000 abstract 1
- 229910052726 zirconium Inorganic materials 0.000 abstract 1
- 229910003158 γ-Al2O3 Inorganic materials 0.000 abstract 1
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 10
- 238000004519 manufacturing process Methods 0.000 description 7
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 6
- 239000000243 solution Substances 0.000 description 5
- 230000000694 effects Effects 0.000 description 3
- 239000002815 homogeneous catalyst Substances 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 2
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 description 2
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 description 2
- 239000004480 active ingredient Substances 0.000 description 2
- 239000004411 aluminium Substances 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- WTEOIRVLGSZEPR-UHFFFAOYSA-N boron trifluoride Chemical compound FB(F)F WTEOIRVLGSZEPR-UHFFFAOYSA-N 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 238000006555 catalytic reaction Methods 0.000 description 2
- 238000001816 cooling Methods 0.000 description 2
- 239000013078 crystal Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000003912 environmental pollution Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- BYLSIPUARIZAHZ-UHFFFAOYSA-N 2,4,6-tris(1-phenylethyl)phenol Chemical compound C=1C(C(C)C=2C=CC=CC=2)=C(O)C(C(C)C=2C=CC=CC=2)=CC=1C(C)C1=CC=CC=C1 BYLSIPUARIZAHZ-UHFFFAOYSA-N 0.000 description 1
- 229910015900 BF3 Inorganic materials 0.000 description 1
- IGFHQQFPSIBGKE-UHFFFAOYSA-N Nonylphenol Natural products CCCCCCCCCC1=CC=C(O)C=C1 IGFHQQFPSIBGKE-UHFFFAOYSA-N 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 238000013019 agitation Methods 0.000 description 1
- 230000029936 alkylation Effects 0.000 description 1
- 238000005804 alkylation reaction Methods 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- RYSNDQDGZQEOAL-UHFFFAOYSA-N calcium;phenol Chemical compound [Ca].OC1=CC=CC=C1 RYSNDQDGZQEOAL-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 238000006206 glycosylation reaction Methods 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000002638 heterogeneous catalyst Substances 0.000 description 1
- 239000003112 inhibitor Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- SNQQPOLDUKLAAF-UHFFFAOYSA-N nonylphenol Chemical compound CCCCCCCCCC1=CC=CC=C1O SNQQPOLDUKLAAF-UHFFFAOYSA-N 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 239000005011 phenolic resin Substances 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 239000004848 polyfunctional curative Substances 0.000 description 1
- 150000008442 polyphenolic compounds Polymers 0.000 description 1
- 235000013824 polyphenols Nutrition 0.000 description 1
- 235000019353 potassium silicate Nutrition 0.000 description 1
- 238000010992 reflux Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 229910000029 sodium carbonate Inorganic materials 0.000 description 1
- TVXXNOYZHKPKGW-UHFFFAOYSA-N sodium molybdate (anhydrous) Chemical compound [Na+].[Na+].[O-][Mo]([O-])(=O)=O TVXXNOYZHKPKGW-UHFFFAOYSA-N 0.000 description 1
- 159000000000 sodium salts Chemical class 0.000 description 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 1
- XMVONEAAOPAGAO-UHFFFAOYSA-N sodium tungstate Chemical compound [Na+].[Na+].[O-][W]([O-])(=O)=O XMVONEAAOPAGAO-UHFFFAOYSA-N 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
Landscapes
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
本发明公开一种一步法合成不同比例一、二、三取代烷基酚用催化剂,属固体酸催化剂,其特征是:对于可溶性活性组份杂多酸或其盐,杂多酸[H3A(M1xM2y)O40,A=Si,B,P,As或Ge;M1,M2=Mo,W,V或Co;x+y=12];可将其配成0.1-1克/升的水溶液,采用浸渍方法,按活性组份的含量0.5-70%的比例浸渍于酸性离子交换树脂上,其干燥后,加入适量粘结剂,挤压成型。此固体催化剂用于酚类与C3-C16烯烃的烷基化反应。
Description
本发明属固体酸催化剂,具体说是一种一步法合成不同比例一、二、三取代烷基酚用催化剂。
烷基酚是一种重要的化工产品,被广泛地用作树脂中间体、环氧树脂硬化剂、酚树脂的抗氧剂、紫外吸叫剂、染料及表面活性剂等等。
烷基酚合成用催化剂目前基本上采用无机酸,如盐酸、硫酸、磷酸等,这类均相催化剂主要有以下缺点:(1)腐蚀性强;(2)催化剂在物料中难除去,给后续生产带来麻烦;(3)环境污染严重;(4)某些催化剂对生产原料要求苛刻,不易满足。
由于上述均相催化剂这些问题的存在,目前国内外研究开发的热点已逐步转移到固体酸多相催化剂上来:日本特许公报01-238549提出以八面沸石、CaO-Al2O3、粘土、石膏等固体酸作为烯烃单烷基化催化剂;日本特许公报01-283239提出以二价金属交换的γ沸石催化苯酚的链烯烃单烷基化、转化率达92.3%;US 5276215用β沸石或脱铝Y沸石及经修饰的Y沸石催化、由苯酚制取了单壬基酚;苏联科学院报告1992年326(2),276-8页(化学)报道了用酚铝、酚钙或多聚酚铝等为催化剂,制取单烷基酚;目前日本还有用三氟化硼催化生产苯乙烯化苯酚的工艺。这些催化剂有的会与反应体系中微量的水反应,产生类似均相催化剂存在的问题;有的活性低,用量大。而它们存在的共同问题是其选择性皆不能尽如人意,若要合成多取代烷基酚则需逐步烷基化,而每步皆需换用不同的催化剂。
本发明的目的在于避免上述现有技术中的不足之处而提供一种通过控制催化剂的组成成分、比例及制备方法,从而获得良好的催化活性,并能在广泛的范围内控制催化剂的选择性,可一步合成不同比例的一、二、三取代烷基酚。
本发明的目的可以通过以下措施来达到:一、催化剂的活性组分:
1、杂多酸[H3A(M1xM2y)O40,A=Si,B,P,As,Ge;M1,M2=Mo,W,V,Co;x+y=12]。
其制备方法分别如下:
杂多酸:
将计量比的A,M1,M2的含氧酸的钠盐溶液混合,剧烈搅拌下加热至接近沸腾,随后边搅拌边向其中逐滴加入浓盐酸,并回流一小时,冷却后加入乙醚萃取,将下层的醚合物慢慢蒸发除去乙醚即得相应的杂多酸晶体。二、催化剂的载体
三、催化剂的制备:
比表面积/m2/g | 孔径/nm | |
Y沸石 | 500-700 | 0.4-1 |
酸性白土 | 150-280 | / |
硅胶 | 200-800 | 2-5 |
酸性离子交换树脂 | 50-120 | 8-40 |
γ-Al2O3 | 150-400 | 8 |
对于可溶性活性组分,可将其配成0.1-1克/升的水溶液,采用浸渍方法,按活性组分的含量为0.5-70%的比例浸渍载体。其干燥后,加入适量粘结剂(如胶体二氧化硅,胶体氧化铝),挤压成型后,于50-300℃下热处理数小时,冷却至室温备用。
本发明相比现有技术具有如下优点:
1.无腐蚀,降低了设备损耗;
2.无毒,不造成环境污染;
3.对生产原料要求不高,易满足;
4.不同比例产品的生产皆可一步完成,简化了生产设备及工艺流程;
5.产品与催化剂容易分离,不需进行复杂的后处理,产品可直接进入后续生产。
6.催化剂活性高,反应快,生产效益可提高数倍至数十倍;
7.选择催化剂、控制反应条件,可使反应满足不同的产品要求,使产品系列化。
8.催化剂可直接或经简单处理再生后重复使用,催化剂用量少。
实施例
催化剂制备:将一定量的钨酸钠和钼酸钠分别溶于水中,混合,向混合溶液中加入一定量的水玻璃(比重1.375),使溶液中Si,Mo,W的摩尔比为1∶3∶9。溶液在剧烈搅拌下加热至接近沸腾,向溶液中逐滴加入浓盐酸(比重1.18),回流1小时,冷却后用乙醚萃取,缓慢蒸去乙醚,将所得杂多酸晶体溶于水中,加热搅拌下,缓缓滴加碳酸钠水溶液,使杂多酸与Na2CO3的摩尔比为2∶1。待反应完全,除尽CO2后将酸性离子交换树脂浸入溶液中,缓缓加热,蒸干后即得H3NaSiW9Mo3/酸性离子交换树脂,其中,有效组分为20%。反应过程:在同上的三颈瓶中加入200g苯酚,油浴加热升温至30-160℃,加入催化剂3g,在搅拌下加入苯乙烯480克,反应1小时后,苯酚转化率接近100%,一取代烷基酚12.5%,二取代烷基酚44.3%,三取代烷基酚42.5%。
此固体酸催化剂用于酚类与C3-C16烯烃的烷基化反应,尤其适用于苯酚的苯乙烯基化反应。
Claims (3)
1、一步合成不同比例一、二、三取代烷基酚用催化剂制备方法,其特征在于:对于可溶性活性组份杂多酸或其盐,杂多酸[H3A(M1xM2y)O40,A=Si,B,P,As或Ge;M1,M2=Mo,W,V或Co;x+y=12];可将其配成0.1-1克/升的水溶液,采用浸渍方法,按活性组份的含量0.5-70%的比例浸渍于载体上,
载 体 比表面积/m2/g 孔径/nm酸性离子交换树脂 50-120 8-40其干燥后,加入适量粘结剂,挤压成型,于50~300℃下热处理数小时,冷却至室温备用。
2、根据权利要求1所述方法制备的催化剂用于酚类与C3-C16烯烃的烷基化反应。
3、根据权利要求1所述方法制备的催化剂适用于苯酚与苯乙烯烷基化反应。
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN95112801A CN1088625C (zh) | 1995-12-06 | 1995-12-06 | 一步法合成不同比例一、二、三取代烷基酚用催化剂 |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN95112801A CN1088625C (zh) | 1995-12-06 | 1995-12-06 | 一步法合成不同比例一、二、三取代烷基酚用催化剂 |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1126717A CN1126717A (zh) | 1996-07-17 |
CN1088625C true CN1088625C (zh) | 2002-08-07 |
Family
ID=5079763
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN95112801A Expired - Fee Related CN1088625C (zh) | 1995-12-06 | 1995-12-06 | 一步法合成不同比例一、二、三取代烷基酚用催化剂 |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN1088625C (zh) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1301152C (zh) * | 2004-06-04 | 2007-02-21 | 南京工业大学 | 一种用于乙酸和正丁醇液相酯化反应的脱铝usy沸石负载杂多酸盐催化剂的制备方法 |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1101265C (zh) * | 1999-09-29 | 2003-02-12 | 中国石油化工集团公司 | 一种含有杂多酸的固体酸催化剂及其制备方法 |
CN1106219C (zh) * | 2000-02-17 | 2003-04-23 | 东北师范大学 | 甲醇脱水制二甲醚的负载型杂多酸催化剂及其生产方法 |
CN105251529B (zh) * | 2015-11-25 | 2017-09-12 | 广东工业大学 | 一种负载型催化剂及其制备方法与催化长链烷基酚的合成方法 |
CN110120515A (zh) * | 2019-05-29 | 2019-08-13 | 重庆长安新能源汽车科技有限公司 | 一种表面改性锂离子电池正极材料及其制备方法 |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2120953A (en) * | 1982-06-01 | 1983-12-14 | Ici Plc | Catalyst for the production of alkyl phenols |
US4599465A (en) * | 1984-07-05 | 1986-07-08 | Mitsubishi Chemical Industries, Ltd. | Process for producing orthoalkylphenols |
SU1192306A1 (ru) * | 1984-04-21 | 1987-02-07 | Inst Kataliza So An Sssr | СПОСОБ ПОЛУЧЕНИЯ 2-ТРЕТ-БУТИЛ-4-АЛКИЛФЕН0Л0В, где алкилрадикал, выбранный из группы: метил, этил, метоксикарбонилэтип |
CN87104109A (zh) * | 1986-06-10 | 1988-01-20 | 住友化学工业株式会社 | 含羟基的烷基芳香族化合物的制备方法 |
CN1048990A (zh) * | 1989-07-25 | 1991-02-06 | 烟台市化学工业研究所 | 一种用于酯化的复合固体酸催化剂 |
-
1995
- 1995-12-06 CN CN95112801A patent/CN1088625C/zh not_active Expired - Fee Related
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB2120953A (en) * | 1982-06-01 | 1983-12-14 | Ici Plc | Catalyst for the production of alkyl phenols |
SU1192306A1 (ru) * | 1984-04-21 | 1987-02-07 | Inst Kataliza So An Sssr | СПОСОБ ПОЛУЧЕНИЯ 2-ТРЕТ-БУТИЛ-4-АЛКИЛФЕН0Л0В, где алкилрадикал, выбранный из группы: метил, этил, метоксикарбонилэтип |
US4599465A (en) * | 1984-07-05 | 1986-07-08 | Mitsubishi Chemical Industries, Ltd. | Process for producing orthoalkylphenols |
CN87104109A (zh) * | 1986-06-10 | 1988-01-20 | 住友化学工业株式会社 | 含羟基的烷基芳香族化合物的制备方法 |
CN1048990A (zh) * | 1989-07-25 | 1991-02-06 | 烟台市化学工业研究所 | 一种用于酯化的复合固体酸催化剂 |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1301152C (zh) * | 2004-06-04 | 2007-02-21 | 南京工业大学 | 一种用于乙酸和正丁醇液相酯化反应的脱铝usy沸石负载杂多酸盐催化剂的制备方法 |
Also Published As
Publication number | Publication date |
---|---|
CN1126717A (zh) | 1996-07-17 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101643219B (zh) | 一种纳米zsm-5分子筛的制备方法 | |
MY102324A (en) | Alkoxylation process using calcium based catalysts | |
CN102658174B (zh) | 介孔纤维状SO42-/MxOy型固体酸催化剂及其制备方法 | |
CN114832855B (zh) | 一种改性复合分子筛催化剂及其制备方法 | |
CN1088625C (zh) | 一步法合成不同比例一、二、三取代烷基酚用催化剂 | |
CN1765888A (zh) | 一种尿囊素的合成工艺 | |
CN104671253A (zh) | 一种zsm-22分子筛纳米片的制备方法 | |
CN103570036B (zh) | 一种y型分子筛的合成方法 | |
CN102019181A (zh) | 介孔材料及其制备方法与合成甲醇催化剂及其制备方法 | |
CN101869847B (zh) | 微球型高分子固体酸酯化催化剂及其制备方法 | |
CN111054425A (zh) | 一种水滑石/mcm-41介孔硅复合固体碱催化剂及其原位制备方法和应用 | |
CN102935381A (zh) | 一种两亲型稀土多酸催化材料、制备方法及应用 | |
CN101239889B (zh) | 一种含有烷基苯酚产物的反应液的制备方法 | |
CN102557946A (zh) | 以酸性离子液体催化合成没食子酸丙酯的方法 | |
CN100347211C (zh) | 用大孔强碱性阴离子交换树脂催化制取苯基苯酚甲醛树脂的方法 | |
CN114736175B (zh) | 水相中催化葡萄糖制备5-羟甲基糠醛的方法 | |
CN1935373A (zh) | 含稀土的复合型固体超强酸催化剂及其制备方法 | |
Shyamsundar et al. | Cordierite honeycomb monoliths coated with zirconia and its modified forms for biodiesel synthesis from Pongamia glabra | |
CN100453178C (zh) | 一种合成异丙苯的催化剂 | |
CN100464847C (zh) | 一种制取醇、醚类化合物的组合沸石催化剂及制备方法 | |
CN110433793B (zh) | 一种BiZn水滑石光催化剂及其制备方法与应用 | |
CN114602512A (zh) | 一种酯化反应催化剂的制备方法 | |
CN113856741B (zh) | 一种水滑石固体碱及其制备方法和高效催化环戊酮三聚的应用 | |
CN1367040A (zh) | 一种具有高苯胺收率的新型硝基苯加氢催化剂 | |
CN109824491A (zh) | 一种2,3,4,4’-四羟基二苯甲酮的生产方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C06 | Publication | ||
PB01 | Publication | ||
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 |