CN115073259B - Preparation method for synthesizing 1, 4-diphenyl-1, 3-diacetylene or derivatives thereof - Google Patents
Preparation method for synthesizing 1, 4-diphenyl-1, 3-diacetylene or derivatives thereof Download PDFInfo
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- 238000002360 preparation method Methods 0.000 title claims abstract description 12
- 230000002194 synthesizing effect Effects 0.000 title claims abstract 8
- 238000006243 chemical reaction Methods 0.000 claims abstract description 73
- 239000003054 catalyst Substances 0.000 claims abstract description 51
- 239000010457 zeolite Substances 0.000 claims abstract description 21
- 229910021536 Zeolite Inorganic materials 0.000 claims abstract description 20
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000002904 solvent Substances 0.000 claims abstract description 19
- -1 aromatic alkyne compound Chemical class 0.000 claims abstract description 14
- 239000010949 copper Substances 0.000 claims description 44
- 239000000243 solution Substances 0.000 claims description 11
- HMQFJYLWNWIYKQ-UHFFFAOYSA-N 1,4-diphenylbutadiyne Chemical compound C1=CC=CC=C1C#CC#CC1=CC=CC=C1 HMQFJYLWNWIYKQ-UHFFFAOYSA-N 0.000 claims description 9
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 9
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 8
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 claims description 5
- 239000007864 aqueous solution Substances 0.000 claims description 5
- 239000007791 liquid phase Substances 0.000 claims description 5
- 238000011068 loading method Methods 0.000 claims description 4
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 claims description 3
- 238000005119 centrifugation Methods 0.000 claims description 3
- 125000000113 cyclohexyl group Chemical group [H]C1([H])C([H])([H])C([H])([H])C([H])(*)C([H])([H])C1([H])[H] 0.000 claims description 3
- WKBOTKDWSSQWDR-UHFFFAOYSA-N Bromine atom Chemical compound [Br] WKBOTKDWSSQWDR-UHFFFAOYSA-N 0.000 claims description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 claims description 2
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 claims description 2
- GDTBXPJZTBHREO-UHFFFAOYSA-N bromine Substances BrBr GDTBXPJZTBHREO-UHFFFAOYSA-N 0.000 claims description 2
- 229910052794 bromium Inorganic materials 0.000 claims description 2
- 239000000460 chlorine Substances 0.000 claims description 2
- 229910052801 chlorine Inorganic materials 0.000 claims description 2
- 239000012153 distilled water Substances 0.000 claims description 2
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 claims description 2
- 229910052731 fluorine Inorganic materials 0.000 claims description 2
- 239000011737 fluorine Substances 0.000 claims description 2
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims description 2
- 125000001997 phenyl group Chemical group [H]C1=C([H])C([H])=C(*)C([H])=C1[H] 0.000 claims description 2
- 230000035484 reaction time Effects 0.000 claims description 2
- 239000007787 solid Substances 0.000 claims description 2
- 150000001879 copper Chemical class 0.000 claims 2
- 239000000203 mixture Substances 0.000 claims 1
- 238000005859 coupling reaction Methods 0.000 abstract description 22
- 239000011521 glass Substances 0.000 abstract description 14
- 238000010168 coupling process Methods 0.000 abstract description 12
- 230000000694 effects Effects 0.000 abstract description 2
- 239000002253 acid Substances 0.000 abstract 1
- 238000001704 evaporation Methods 0.000 abstract 1
- 230000002349 favourable effect Effects 0.000 abstract 1
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 18
- UEXCJVNBTNXOEH-UHFFFAOYSA-N Ethynylbenzene Chemical group C#CC1=CC=CC=C1 UEXCJVNBTNXOEH-UHFFFAOYSA-N 0.000 description 18
- 150000001345 alkine derivatives Chemical class 0.000 description 15
- 238000004817 gas chromatography Methods 0.000 description 13
- XDTMQSROBMDMFD-UHFFFAOYSA-N Cyclohexane Chemical compound C1CCCCC1 XDTMQSROBMDMFD-UHFFFAOYSA-N 0.000 description 11
- 239000000047 product Substances 0.000 description 11
- 238000004440 column chromatography Methods 0.000 description 9
- 239000003480 eluent Substances 0.000 description 9
- 239000003208 petroleum Substances 0.000 description 9
- 238000002390 rotary evaporation Methods 0.000 description 8
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 7
- 239000012295 chemical reaction liquid Substances 0.000 description 6
- 239000012263 liquid product Substances 0.000 description 6
- 150000003839 salts Chemical class 0.000 description 6
- HSFWRNGVRCDJHI-UHFFFAOYSA-N alpha-acetylene Natural products C#C HSFWRNGVRCDJHI-UHFFFAOYSA-N 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 238000001228 spectrum Methods 0.000 description 4
- 238000003786 synthesis reaction Methods 0.000 description 4
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 150000001412 amines Chemical class 0.000 description 3
- 125000003118 aryl group Chemical group 0.000 description 3
- SXTLQDJHRPXDSB-UHFFFAOYSA-N copper;dinitrate;trihydrate Chemical compound O.O.O.[Cu+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O SXTLQDJHRPXDSB-UHFFFAOYSA-N 0.000 description 3
- 230000008878 coupling Effects 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000012071 phase Substances 0.000 description 3
- QXSWHQGIEKUBAS-UHFFFAOYSA-N 1-ethynyl-4-fluorobenzene Chemical group FC1=CC=C(C#C)C=C1 QXSWHQGIEKUBAS-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000001257 hydrogen Substances 0.000 description 2
- 229910052739 hydrogen Inorganic materials 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 229930014626 natural product Natural products 0.000 description 2
- SUSQOBVLVYHIEX-UHFFFAOYSA-N phenylacetonitrile Chemical compound N#CCC1=CC=CC=C1 SUSQOBVLVYHIEX-UHFFFAOYSA-N 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000001308 synthesis method Methods 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- YTPLMLYBLZKORZ-UHFFFAOYSA-N Divinylene sulfide Natural products C=1C=CSC=1 YTPLMLYBLZKORZ-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 125000000304 alkynyl group Chemical group 0.000 description 1
- 229940124350 antibacterial drug Drugs 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 238000006555 catalytic reaction Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 150000001923 cyclic compounds Chemical class 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 125000005594 diketone group Chemical group 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 238000005470 impregnation Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000000178 monomer Substances 0.000 description 1
- 239000006259 organic additive Substances 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 150000003384 small molecules Chemical class 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- JRMUNVKIHCOMHV-UHFFFAOYSA-M tetrabutylammonium bromide Chemical compound [Br-].CCCC[N+](CCCC)(CCCC)CCCC JRMUNVKIHCOMHV-UHFFFAOYSA-M 0.000 description 1
- LPSKDVINWQNWFE-UHFFFAOYSA-M tetrapropylazanium;hydroxide Chemical compound [OH-].CCC[N+](CCC)(CCC)CCC LPSKDVINWQNWFE-UHFFFAOYSA-M 0.000 description 1
- 229930192474 thiophene Natural products 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C2/00—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms
- C07C2/76—Preparation of hydrocarbons from hydrocarbons containing a smaller number of carbon atoms by condensation of hydrocarbons with partial elimination of hydrogen
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/70—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65
- B01J29/72—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65 containing iron group metals, noble metals or copper
- B01J29/7215—Zeolite Beta
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C17/00—Preparation of halogenated hydrocarbons
- C07C17/26—Preparation of halogenated hydrocarbons by reactions involving an increase in the number of carbon atoms in the skeleton
- C07C17/263—Preparation of halogenated hydrocarbons by reactions involving an increase in the number of carbon atoms in the skeleton by condensation reactions
- C07C17/269—Preparation of halogenated hydrocarbons by reactions involving an increase in the number of carbon atoms in the skeleton by condensation reactions of only halogenated hydrocarbons
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2229/00—Aspects of molecular sieve catalysts not covered by B01J29/00
- B01J2229/10—After treatment, characterised by the effect to be obtained
- B01J2229/18—After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself
- B01J2229/186—After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself not in framework positions
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/50—Improvements relating to the production of bulk chemicals
- Y02P20/584—Recycling of catalysts
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Catalysts (AREA)
Abstract
Description
技术领域Technical field
本发明属于有机合成化学技术领域,涉及一种以Beta沸石为载体负载的Cu 的催化剂制备方法及其催化芳烃炔自偶联生成1,4-二苯基-1,3-丁二炔及其衍生物的制备方法。The invention belongs to the technical field of organic synthetic chemistry and relates to a catalyst preparation method using Beta zeolite as a carrier to support Cu and its catalytic self-coupling of aromatic hydrocarbons and alkynes to generate 1,4-diphenyl-1,3-butadiyne and its Methods for Preparing Derivatives.
背景技术Background technique
芳烃炔的自偶联工艺生成的1,3-共轭二炔类化合物具有刚性结构单元和独特的电子特性,是天然产物和抗菌药物的主要成分,同时还是功能分子材料合成中的主要官能团,此外芳烃炔偶联反应也在合成化学领域得到了广泛的应用。例如,合成多种类型炔化物,构建大环系炔化物,天然产物合成和超分子领域的应用。The 1,3-conjugated diynes generated by the self-coupling process of aromatic alkynes have rigid structural units and unique electronic properties. They are the main components of natural products and antibacterial drugs, and are also the main functional groups in the synthesis of functional molecular materials. In addition, aromatic hydrocarbon-alkyne coupling reactions have also been widely used in the field of synthetic chemistry. For example, synthesis of various types of alkynes, construction of macrocyclic alkynes, natural product synthesis and applications in supramolecular fields.
芳烃炔自偶联的反应普遍认为需要Cu2+盐进行催化,1964年Bohlmann和他的同事发现的Cu2+盐可以催化炔的偶联(Chem.Ber.,1964,97,794),然后Keigo Kamata等人利用TBA4[g-H2SiW10O36Cu2(m-1,1-N3)2]催化体系,在苯乙腈做溶剂的条件下,加入TBAB,通入氧气,加入Pd催化剂和CuI,对炔基偶联反应进行催化(Angew.Chem.,2008,47,2407)。同年,Kazuya Yamaguchi等人用一种单体二酮取代物[γ-H2SiW10O36Cu2(μ-1,1-N3)2]4-Cu2+盐作为催化剂,但是需要额外的有机胺等胺类有机小分子,才能够实现芳烃炔的自偶联。因此,芳烃炔的自偶联目前存在如下问题:①需要复杂的金属Cu盐为催化剂,同时需要加入Pd盐或是有机胺,②存在Cu2+盐容易沉积,体系难以分离,③反应体系不环保,对环境不友好。针对目前芳烃炔自偶联存在的问题,本申请专利在不使用额外的金属 Pd或是有机添加剂的条件下,以Cu/NH4 +-Beta为催化剂,直接实现了芳烃炔的自偶联,该方法原子利用率高,绿色环保,而且催化剂可以重复利用。It is generally believed that the self-coupling reaction of aromatic hydrocarbons and alkynes requires Cu 2+ salts for catalysis. In 1964, Bohlmann and his colleagues discovered that Cu 2+ salts can catalyze the coupling of alkynes (Chem. Ber., 1964, 97, 794), and then Keigo Kamata et al. used the TBA 4 [gH 2 SiW 10 O 36 Cu 2 (m-1,1-N 3 ) 2 ] catalytic system. With phenylacetonitrile as the solvent, TBAB was added, oxygen was introduced, and Pd catalyst and CuI were added. , catalyze the alkynyl coupling reaction (Angew. Chem., 2008, 47, 2407). In the same year, Kazuya Yamaguchi et al. used a monomer diketone substitute [γ-H 2 SiW 10 O 36 Cu 2 (μ-1,1-N 3 ) 2 ] 4- Cu 2+ salt as a catalyst, but additional Only with organic amines and other amine organic small molecules can the self-coupling of aromatic hydrocarbons and alkynes be realized. Therefore, the self-coupling of aromatic hydrocarbons and alkynes currently has the following problems: ① It requires complex metal Cu salts as catalysts, and Pd salts or organic amines need to be added at the same time. ② The presence of Cu 2+ salts is easy to precipitate and the system is difficult to separate. ③ The reaction system is not Environmentally friendly, not environmentally friendly. In view of the current problems in the self-coupling of aromatic hydrocarbons and alkynes, this patent application uses Cu/NH 4 + -Beta as a catalyst to directly realize the self-coupling of aromatic hydrocarbons and alkynes without using additional metal Pd or organic additives. This method has high atom utilization rate, is green and environmentally friendly, and the catalyst can be reused.
发明内容Contents of the invention
本发明的目的在于克服现有技术的不足,提供了一种选择性高、产率高、易于分离提纯、对环境友好的合成1,4-二苯基-1,3-丁二炔及其衍生物的制备方法。通过Cu/NH4 +-Beta沸石材料在温和反应条件下可实现芳香炔类化合物的自偶联,合成联炔化合物。The object of the present invention is to overcome the deficiencies of the prior art and provide a synthetic 1,4-diphenyl-1,3-butadiyne with high selectivity, high yield, easy separation and purification, and environmental friendliness and its Methods for Preparing Derivatives. Cu/NH 4 + -Beta zeolite material can realize the self-coupling of aromatic acetylenic compounds under mild reaction conditions, and synthesize bi-alkyne compounds.
具体的合成方法如下:The specific synthesis method is as follows:
(1)催化剂的制备方法:一定量的Beta沸石与硝酸铵水溶液(0.6~1.0mol/L) 在高温下进行铵交换,其中液固质量比为10~20:1,温度为60~100℃,交换2~6 h,铵交换结束后,过滤、干燥,得到铵型的Beta沸石。然后称取一定量的Cu(NO3)2加入蒸馏水中,得到澄清透明溶液后,浸渍到铵型的Beta沸石中,室温静置、干燥得到Cu负载的铵型Beta催化剂,即为Cu/NH4 +-Beta。(1) Preparation method of catalyst: A certain amount of Beta zeolite and ammonium nitrate aqueous solution (0.6~1.0mol/L) are used for ammonium exchange at high temperature, where the liquid-to-solid mass ratio is 10~20:1, and the temperature is 60~100℃ , exchange for 2 to 6 hours. After the ammonium exchange is completed, filter and dry to obtain ammonium-type Beta zeolite. Then weigh a certain amount of Cu(NO 3 ) 2 and add it to distilled water to obtain a clear and transparent solution, which is then immersed in ammonium-type Beta zeolite, left to stand at room temperature, and dried to obtain a Cu-supported ammonium-type Beta catalyst, which is Cu/NH. 4 + -Beta.
进一步,Beta沸石载体采用现有的Beta沸石典型合成方法容易得到,即将二氧化硅、偏铝酸钠、四丙基氢氧化铵和聚二甲基二烯丙基氯化铵溶解于水中,装釜高温晶化、过滤、洗涤、干燥煅烧。Furthermore, the Beta zeolite carrier is easily obtained by using the existing typical synthesis method of Beta zeolite, that is, dissolving silica, sodium metaaluminate, tetrapropylammonium hydroxide and polydimethyldiallylammonium chloride in water, and loading The kettle is used for high-temperature crystallization, filtration, washing, drying and calcining.
进一步,Cu的负载量为1~5wt.%。Furthermore, the loading amount of Cu is 1 to 5 wt.%.
催化剂的制备方法中,高温干燥的温度为80~120℃。In the preparation method of the catalyst, the temperature for high-temperature drying is 80 to 120°C.
(2)Cu/NH4 +-Beta催化芳香炔类化合物的自偶联反应过程如下:将芳香炔、金属沸石催化剂Cu/NH4 +-Beta和溶剂依次加入玻璃反应管中,80~140℃反应一段时间,反应结束后,离心分离催化剂,得到的液相产物经低压旋转蒸发后得到的馏分,便可得到产物。(2) The Cu/NH 4 + -Beta-catalyzed self-coupling reaction process of aromatic acetylenic compounds is as follows: add aromatic acetylene, metal zeolite catalyst Cu/NH 4 + -Beta and solvent into a glass reaction tube in sequence, 80~140℃ The reaction lasts for a period of time. After the reaction is completed, the catalyst is separated by centrifugation, and the product can be obtained from the fraction obtained by low-pressure rotary evaporation of the liquid phase product.
进一步的,芳香炔的结构通式为其中R可以位于邻间对位,R可以是H、甲基、乙基、甲氧基、丁基、氯、氟、溴或苯环。Furthermore, the general structural formula of aromatic alkynes is Wherein R can be located in the ortho-para position, and R can be H, methyl, ethyl, methoxy, butyl, chlorine, fluorine, bromine or benzene ring.
进一步的,芳香炔也可以换成带炔的环状化合物和噻吩炔烃。Furthermore, aromatic alkynes can also be replaced by cyclic compounds with alkynes and thiophene alkynes.
芳烃炔自偶联反应中,所述的溶剂为环己烷、苯、二氯乙烷,优选为环己烷。In the aromatic-alkyne self-coupling reaction, the solvent is cyclohexane, benzene, and dichloroethane, preferably cyclohexane.
芳烃炔自偶联反应中,所述的反应温度为80~140℃,优选为100~120℃,反应时间为3~24h,优选为4~14h。In the aromatic alkyne self-coupling reaction, the reaction temperature is 80-140°C, preferably 100-120°C, and the reaction time is 3-24h, preferably 4-14h.
本发明与现有技术相比取得了如下技术优势:Compared with the existing technology, the present invention has achieved the following technical advantages:
(1)Cu2+直接负载在NH4 +交换Beta上的酸性位点,为反应提供了Cu2+和 NH4 +位点。芳香炔在催化剂上先转变成芳香炔的碳正离子,并进攻与Cu2+结合的芳香炔,从而形成目的产物。Cu/NH4 +-Beta这种催化剂有利于芳烃炔的自偶联,大大提高了反应活性。(1) Cu 2+ is directly loaded on the acidic site on NH 4 + exchange Beta, providing Cu 2+ and NH 4 + sites for the reaction. The aromatic alkyne is first converted into the carbocation of the aromatic alkyne on the catalyst, and attacks the aromatic alkyne combined with Cu 2+ to form the target product. The catalyst Cu/NH 4 + -Beta is beneficial to the self-coupling of aromatic hydrocarbons and alkynes, which greatly improves the reaction activity.
(2)本发明中的的反应体系具有反应条件温和,催化剂易回收,后处理简单,且选择性高、产率高等优势。(2) The reaction system in the present invention has the advantages of mild reaction conditions, easy recovery of the catalyst, simple post-treatment, high selectivity and high yield.
附图说明Description of the drawings
图1为实施例2对氟苯乙炔偶联产物的氢谱谱图;Figure 1 is a hydrogen spectrum spectrum of the p-fluorophenylacetylene coupling product of Example 2;
1H NMR(500MHz,CDCl3),δ:7.53(dd,J=8.7,5.4Hz,4H),7.06(t,J=8.6Hz, 4H). 1 H NMR (500MHz, CDCl 3 ), δ: 7.53 (dd, J=8.7, 5.4Hz, 4H), 7.06 (t, J=8.6Hz, 4H).
图2为实施例3对甲基苯乙炔偶联产物的氢谱谱图。Figure 2 is a hydrogen spectrum spectrum of the p-toluene acetylene coupling product in Example 3.
1H NMR(500MHz,CDCl3),δ:7.45(d,J=8.1Hz,4H),7.17(d,J=7.9Hz,4H), 2.39(s,6H). 1 H NMR (500MHz, CDCl 3 ), δ: 7.45 (d, J = 8.1 Hz, 4H), 7.17 (d, J = 7.9 Hz, 4H), 2.39 (s, 6H).
具体实施方式Detailed ways
合成的沸石载体标记为Beta(参考ACS Catal.,2018,8,9043文献中2.1Materials synthesis典型的介孔Beta沸石方法合成得到),然后采用先铵交换后浸渍的的方法制备催化剂,具体如下:2g Beta沸石与20mL 0.8mol/L的硝酸铵水溶液在80℃交换4小时,过滤、干燥;称取0.2265g三水合硝酸铜溶解于2.0 g水中,然后将溶液倒入1.0g上述沸石载体中,室温静置、干燥,得到目标性催化剂Cu/NH4 +-Beta,其中Cu的负载量3wt.%。将催化剂应用到实施例中。The synthesized zeolite carrier is labeled Beta (synthesized by referring to the typical mesoporous Beta zeolite method in 2.1 Materials synthesis in ACS Catal., 2018, 8, 9043), and then the catalyst is prepared by ammonium exchange first and then impregnation, as follows: 2g Beta zeolite and 20mL 0.8mol/L ammonium nitrate aqueous solution were exchanged at 80°C for 4 hours, filtered, and dried; weigh 0.2265g copper nitrate trihydrate and dissolve it in 2.0g water, and then pour the solution into 1.0g of the above zeolite carrier. Leave to stand and dry at room temperature to obtain the target catalyst Cu/NH 4 + -Beta, in which the Cu loading amount is 3wt.%. Catalysts were used in the examples.
实施例1:Example 1:
先铵交换后负载Cu的Beta催化剂应用到炔的偶联反应:The Beta catalyst loaded with Cu is applied to the coupling reaction of alkynes after first ammonium exchange:
将0.2mmol苯乙炔、30mg Cu/NH4 +-Beta和1mL溶剂环己烷(CYH)依次加入玻璃反应管中,100℃反应4h,反应结束后,离心分离催化剂,得到的液相产物经低压旋转蒸发后得到的馏分,用纯石油醚作为洗脱剂进行柱层析分离纯化,即可得到产物。另外,对反应液相进行气相色谱(GC)分析,计算反应的转化率和选择性。Add 0.2 mmol phenylacetylene, 30 mg Cu/NH 4 + -Beta and 1 mL solvent cyclohexane (CYH) into the glass reaction tube in sequence, and react at 100°C for 4 hours. After the reaction is completed, the catalyst is centrifuged, and the liquid phase product obtained is passed through low pressure The fraction obtained after rotary evaporation is separated and purified by column chromatography using pure petroleum ether as the eluent to obtain the product. In addition, the reaction liquid phase was analyzed by gas chromatography (GC) to calculate the conversion rate and selectivity of the reaction.
反应结构式为:The reaction structural formula is:
实施例2:Example 2:
将0.2mmol对氟苯乙炔、30mg Cu/NH4 +-Beta和1mL溶剂苯依次加入玻璃反应管中,100℃反应4h,反应结束后,离心分离催化剂,得到的液相产物经低压旋转蒸发后得到的馏分,用纯石油醚作为洗脱剂进行柱层析分离纯化,即可得到产物。对反应液相进行GC分析,计算反应的转化率和选择性。Add 0.2 mmol p-fluorophenylacetylene, 30 mg Cu/NH 4 + -Beta and 1 mL solvent benzene into the glass reaction tube in sequence, and react at 100°C for 4 hours. After the reaction is completed, the catalyst is centrifuged and the liquid product obtained is evaporated by low pressure rotary evaporation. The obtained fraction is separated and purified by column chromatography using pure petroleum ether as the eluent to obtain the product. Perform GC analysis on the reaction liquid phase to calculate the conversion rate and selectivity of the reaction.
反应结构式为:The reaction structural formula is:
实施例3:Example 3:
将0.2mmol对甲基苯乙炔、30mg Cu/NH4 +-Beta和1mL溶剂环己烷依次加入玻璃反应管中,100℃反应4h,反应结束后,离心分离催化剂,得到的液相产物经低压旋转蒸发后得到的馏分,用纯石油醚作为洗脱剂进行柱层析分离纯化,即可得到产物。另外,对反应液相进行GC分析,计算反应的转化率和选择性。Add 0.2 mmol p-toluene acetylene, 30 mg Cu/NH 4 + -Beta and 1 mL solvent cyclohexane into the glass reaction tube in sequence, and react at 100°C for 4 hours. After the reaction is completed, the catalyst is centrifuged and the liquid phase product obtained is passed through low pressure The fraction obtained after rotary evaporation is separated and purified by column chromatography using pure petroleum ether as the eluent to obtain the product. In addition, GC analysis was performed on the reaction liquid phase to calculate the conversion rate and selectivity of the reaction.
反应结构式为:The reaction structural formula is:
实施例4:Example 4:
将0.2mmol对甲基苯乙炔、30mg Cu/NH4 +-Beta和1mL溶剂甲苯依次加入玻璃反应管中,100℃反应4h,反应结束后,离心分离催化剂,得到的液相产物经低压旋转蒸发后得到的馏分,用纯石油醚作为洗脱剂进行柱层析分离纯化。另外,对反应液进行GC分析,计算反应的转化率和选择性。Add 0.2 mmol p-toluene acetylene, 30 mg Cu/NH 4 + -Beta and 1 mL solvent toluene into the glass reaction tube in sequence, and react at 100°C for 4 hours. After the reaction is completed, the catalyst is centrifuged and the liquid product obtained is rotary evaporated under low pressure. The fraction obtained was separated and purified by column chromatography using pure petroleum ether as the eluent. In addition, GC analysis was performed on the reaction solution to calculate the conversion rate and selectivity of the reaction.
实施例5:Example 5:
将0.2mmol苯乙炔、30mg Cu/NH4 +-Beta和1mL溶剂二氯乙烷依次加入玻璃反应管中,100℃反应4h,反应结束后,离心分离催化剂,得到的液相产物经低压旋转蒸发后得到的馏分,用纯石油醚作为洗脱剂进行柱层析分离纯化。另外,对反应液进行GC分析,计算反应的转化率和选择性。Add 0.2 mmol phenylacetylene, 30 mg Cu/NH 4 + -Beta and 1 mL solvent dichloroethane into the glass reaction tube in sequence, and react at 100°C for 4 hours. After the reaction is completed, the catalyst is centrifuged and the liquid product obtained is rotary evaporated under low pressure. The fraction obtained was separated and purified by column chromatography using pure petroleum ether as the eluent. In addition, GC analysis was performed on the reaction solution to calculate the conversion rate and selectivity of the reaction.
实施例6:Example 6:
将0.2mmol苯乙炔、30mg Cu/NH4 +-Beta和1mL溶剂环己烷依次加入玻璃反应管中,120℃反应4h,反应结束后,离心分离催化剂,得到的液相产物经低压旋转蒸发后得到的馏分,用纯石油醚作为洗脱剂进行柱层析分离纯化。另外,对反应液进行GC分析,计算反应的转化率和选择性。Add 0.2 mmol phenylacetylene, 30 mg Cu/NH 4 + -Beta and 1 mL solvent cyclohexane into the glass reaction tube in sequence, and react at 120°C for 4 hours. After the reaction is completed, the catalyst is centrifuged and the liquid product obtained is evaporated by low pressure rotary evaporation. The obtained fractions were separated and purified by column chromatography using pure petroleum ether as the eluent. In addition, GC analysis was performed on the reaction solution to calculate the conversion rate and selectivity of the reaction.
实施例7:Example 7:
将0.2mmol苯乙炔、30mg Cu/NH4 +-Beta和1mL溶剂环己烷依次加入玻璃反应管中,80℃反应10h,反应结束后,离心分离催化剂,得到的液相产物经低压旋转蒸发后得到的馏分,用纯石油醚作为洗脱剂进行柱层析分离纯化。另外,对反应液进行GC分析,计算反应的转化率和选择性。Add 0.2 mmol phenylacetylene, 30 mg Cu/NH 4 + -Beta and 1 mL solvent cyclohexane into the glass reaction tube in sequence, and react at 80°C for 10 hours. After the reaction is completed, the catalyst is centrifuged and the liquid product obtained is evaporated by low pressure rotary evaporation. The obtained fractions were separated and purified by column chromatography using pure petroleum ether as the eluent. In addition, GC analysis was performed on the reaction solution to calculate the conversion rate and selectivity of the reaction.
实施例8:Example 8:
将0.2mmol苯乙炔、30mg Cu/NH4 +-Beta和1mL溶剂环己烷依次加入玻璃反应管中,80℃反应4h,反应结束后,离心分离催化剂,得到的液相产物经低压旋转蒸发后得到的馏分,用纯石油醚作为洗脱剂进行柱层析分离纯化。另外,对反应液进行GC分析,计算反应的转化率和选择性。Add 0.2 mmol phenylacetylene, 30 mg Cu/NH 4 + -Beta and 1 mL solvent cyclohexane into the glass reaction tube in sequence, and react at 80°C for 4 hours. After the reaction is completed, the catalyst is centrifuged and the liquid product obtained is evaporated by low pressure rotary evaporation. The obtained fractions were separated and purified by column chromatography using pure petroleum ether as the eluent. In addition, GC analysis was performed on the reaction solution to calculate the conversion rate and selectivity of the reaction.
对比实施例1Comparative Example 1
直接将Beta催化剂应用到炔的偶联反应:Direct application of Beta catalysts to alkynes coupling reactions:
将0.2mmol苯乙炔、30mg Beta和1mL溶剂环己烷依次加入玻璃反应管, 100℃反应4h,反应结束后,离心分离催化剂,得到的液相产物经低压旋转蒸发后得到的馏分,用纯石油醚作为洗脱剂进行柱层析分离纯化。另外,对反应液进行GC分析计算反应的转化率和选择性。Add 0.2 mmol phenylacetylene, 30 mg Beta and 1 mL solvent cyclohexane to the glass reaction tube in sequence, and react at 100°C for 4 hours. After the reaction is completed, the catalyst is separated by centrifugation, and the liquid phase product obtained is subjected to low-pressure rotary evaporation. The fraction obtained is treated with pure petroleum. Ether was used as the eluent for column chromatography separation and purification. In addition, GC analysis was performed on the reaction solution to calculate the conversion rate and selectivity of the reaction.
对比实施例2Comparative Example 2
先负载3wt%Cu后铵交换得到NH4 +/Cu/Beta催化剂,催化剂制备方法如下:称取0.2265g三水合硝酸铜溶解于2.0g水中,然后将溶液倒入2.0g上述Beta 沸石载体中,室温静置、干燥,得到的催化剂标记为Cu/Beta。2.0g Cu/Beta沸石与20mL 0.8mol/L的硝酸铵水溶液在80℃交换4小时,过滤、干燥,得到的催化剂为NH4 +/Cu/Beta。First load 3wt% Cu and then ammonium exchange to obtain the NH 4 + /Cu/Beta catalyst. The catalyst preparation method is as follows: weigh 0.2265g copper nitrate trihydrate and dissolve it in 2.0g water, then pour the solution into 2.0g of the above-mentioned Beta zeolite carrier, Leave to stand and dry at room temperature, and the obtained catalyst is labeled Cu/Beta. 2.0g Cu/Beta zeolite and 20mL 0.8mol/L ammonium nitrate aqueous solution were exchanged at 80°C for 4 hours, filtered and dried, and the obtained catalyst was NH 4 + /Cu/Beta.
将0.2mmol苯乙炔、30mgNH4 +/Cu Beta和1mL溶剂环己烷依次加入玻璃反应管中,100℃反应4h,反应结束后,离心分离催化剂,得到的反应液进行GC分析,计算反应的转化率和选择性。Add 0.2 mmol phenylacetylene, 30 mg NH 4 + /Cu Beta and 1 mL solvent cyclohexane into the glass reaction tube in sequence, and react at 100°C for 4 hours. After the reaction is completed, the catalyst is centrifuged and the obtained reaction liquid is analyzed by GC to calculate the conversion of the reaction. rate and selectivity.
对比实施例3Comparative Example 3
直接Cu负载的Beta催化剂应用到炔的偶联反应,催化剂制备如下:称取 0.2265g三水合硝酸铜溶解于2.0g水中,然后将溶液倒入2.0g上述沸石载体中,室温静置、干燥,得到的催化剂标记为Cu/Beta。The direct Cu-supported Beta catalyst is applied to the coupling reaction of alkynes. The catalyst is prepared as follows: weigh 0.2265g copper nitrate trihydrate and dissolve it in 2.0g water, then pour the solution into 2.0g of the above zeolite carrier, let it stand at room temperature, and dry. The resulting catalyst is labeled Cu/Beta.
将0.2mmol苯乙炔、30mg Cu/Beta和1mL溶剂环己烷依次加入玻璃反应管中,100℃反应4h,反应结束后,离心分离催化剂,得到的反应液进行GC分析,计算反应的转化率和选择性。Add 0.2 mmol phenylacetylene, 30 mg Cu/Beta and 1 mL solvent cyclohexane into the glass reaction tube in sequence, and react at 100°C for 4 hours. After the reaction is completed, the catalyst is centrifuged and the obtained reaction liquid is analyzed by GC to calculate the conversion rate and Selectivity.
对比实施例4Comparative Example 4
将铵交换后Beta催化剂应用到炔的偶联反应,催化剂制备如下:称取2g Beta 沸石与20mL 0.8mol/L的硝酸铵水溶液在80℃交换4小时,过滤、干燥,得到的催化剂为NH4 +-Beta。The ammonium-exchanged Beta catalyst is applied to the coupling reaction of alkynes. The catalyst is prepared as follows: weigh 2g Beta zeolite and 20mL of 0.8mol/L ammonium nitrate aqueous solution, exchange them at 80°C for 4 hours, filter and dry, and the obtained catalyst is NH 4 + -Beta.
将0.2mmol苯乙炔、30mg NH4 +-Beta和1mL溶剂环己烷依次加入玻璃反应管,100℃反应4h,反应结束后,离心分离催化剂,得到的反应液进行GC分析,计算反应的转化率和选择性。Add 0.2 mmol phenylacetylene, 30 mg NH 4 + -Beta and 1 mL solvent cyclohexane to the glass reaction tube in sequence, and react at 100°C for 4 hours. After the reaction is completed, the catalyst is centrifuged and the obtained reaction liquid is analyzed by GC to calculate the conversion rate of the reaction. and selectivity.
上述实施例反应后的转化率和选择性如表1所示。The conversion rate and selectivity after the reaction of the above embodiment are shown in Table 1.
表1:Table 1:
以上描述了本发明的可选实施方案,以教导本领域技术人员如何实施和再现本发明。为了教导本发明方案,已经对一些常规技术方面进行了简化和省去。本领域技术人员应该理解源自这方面的变型,均在本发明的保护范围之内。Alternative embodiments of the invention have been described above to teach those skilled in the art how to practice and reproduce the invention. In order to teach the present invention, some conventional technical aspects have been simplified and omitted. Those skilled in the art should understand that modifications derived from this aspect are within the scope of the present invention.
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