CN116715569A - A kind of preparation method of 4,4'-difluorobenzophenone - Google Patents
A kind of preparation method of 4,4'-difluorobenzophenone Download PDFInfo
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- LSQARZALBDFYQZ-UHFFFAOYSA-N 4,4'-difluorobenzophenone Chemical compound C1=CC(F)=CC=C1C(=O)C1=CC=C(F)C=C1 LSQARZALBDFYQZ-UHFFFAOYSA-N 0.000 title claims abstract description 28
- 238000002360 preparation method Methods 0.000 title claims abstract description 10
- 238000006243 chemical reaction Methods 0.000 claims abstract description 51
- 238000000034 method Methods 0.000 claims abstract description 27
- BBYDXOIZLAWGSL-UHFFFAOYSA-N 4-fluorobenzoic acid Chemical compound OC(=O)C1=CC=C(F)C=C1 BBYDXOIZLAWGSL-UHFFFAOYSA-N 0.000 claims abstract description 15
- CTSLXHKWHWQRSH-UHFFFAOYSA-N oxalyl chloride Chemical compound ClC(=O)C(Cl)=O CTSLXHKWHWQRSH-UHFFFAOYSA-N 0.000 claims abstract description 14
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 22
- 239000003054 catalyst Substances 0.000 claims description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 15
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 12
- 239000007787 solid Substances 0.000 claims description 12
- 239000002904 solvent Substances 0.000 claims description 12
- PYLWMHQQBFSUBP-UHFFFAOYSA-N monofluorobenzene Chemical compound FC1=CC=CC=C1 PYLWMHQQBFSUBP-UHFFFAOYSA-N 0.000 claims description 10
- 239000003513 alkali Substances 0.000 claims description 9
- 239000000706 filtrate Substances 0.000 claims description 8
- 238000001035 drying Methods 0.000 claims description 6
- 239000012074 organic phase Substances 0.000 claims description 6
- 239000012071 phase Substances 0.000 claims description 6
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 5
- 238000001914 filtration Methods 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 4
- 239000004927 clay Substances 0.000 claims description 4
- 239000012043 crude product Substances 0.000 claims description 4
- 238000004821 distillation Methods 0.000 claims description 3
- 238000010992 reflux Methods 0.000 claims description 3
- 239000011347 resin Substances 0.000 claims description 3
- 229920005989 resin Polymers 0.000 claims description 3
- 239000011949 solid catalyst Substances 0.000 claims description 3
- ZCYVEMRRCGMTRW-UHFFFAOYSA-N 7553-56-2 Chemical compound [I] ZCYVEMRRCGMTRW-UHFFFAOYSA-N 0.000 claims description 2
- 244000060011 Cocos nucifera Species 0.000 claims description 2
- 235000013162 Cocos nucifera Nutrition 0.000 claims description 2
- 239000012295 chemical reaction liquid Substances 0.000 claims description 2
- IEJIGPNLZYLLBP-UHFFFAOYSA-N dimethyl carbonate Chemical compound COC(=O)OC IEJIGPNLZYLLBP-UHFFFAOYSA-N 0.000 claims description 2
- JBTWLSYIZRCDFO-UHFFFAOYSA-N ethyl methyl carbonate Chemical compound CCOC(=O)OC JBTWLSYIZRCDFO-UHFFFAOYSA-N 0.000 claims description 2
- 229910052740 iodine Inorganic materials 0.000 claims description 2
- 239000011630 iodine Substances 0.000 claims description 2
- 230000035484 reaction time Effects 0.000 claims description 2
- 238000003756 stirring Methods 0.000 claims description 2
- 239000003930 superacid Substances 0.000 claims description 2
- 229910052799 carbon Inorganic materials 0.000 claims 2
- 238000010438 heat treatment Methods 0.000 claims 2
- 238000004321 preservation Methods 0.000 claims 1
- 238000005406 washing Methods 0.000 claims 1
- 238000005727 Friedel-Crafts reaction Methods 0.000 abstract description 4
- CZKLEJHVLCMVQR-UHFFFAOYSA-N 4-fluorobenzoyl chloride Chemical compound FC1=CC=C(C(Cl)=O)C=C1 CZKLEJHVLCMVQR-UHFFFAOYSA-N 0.000 abstract description 3
- 238000003912 environmental pollution Methods 0.000 abstract description 2
- 238000009776 industrial production Methods 0.000 abstract 1
- 239000007858 starting material Substances 0.000 abstract 1
- 239000000243 solution Substances 0.000 description 23
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical group C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 11
- FYSNRJHAOHDILO-UHFFFAOYSA-N thionyl chloride Chemical compound ClS(Cl)=O FYSNRJHAOHDILO-UHFFFAOYSA-N 0.000 description 8
- 239000000047 product Substances 0.000 description 6
- 230000015572 biosynthetic process Effects 0.000 description 5
- 239000007789 gas Substances 0.000 description 5
- 238000004519 manufacturing process Methods 0.000 description 5
- 238000003786 synthesis reaction Methods 0.000 description 5
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 4
- 230000002378 acidificating effect Effects 0.000 description 4
- 238000004128 high performance liquid chromatography Methods 0.000 description 4
- 229910052739 hydrogen Inorganic materials 0.000 description 4
- 239000001257 hydrogen Substances 0.000 description 4
- GEHJYWRUCIMESM-UHFFFAOYSA-L sodium sulfite Chemical compound [Na+].[Na+].[O-]S([O-])=O GEHJYWRUCIMESM-UHFFFAOYSA-L 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 239000004696 Poly ether ether ketone Substances 0.000 description 3
- VSCWAEJMTAWNJL-UHFFFAOYSA-K aluminium trichloride Chemical compound Cl[Al](Cl)Cl VSCWAEJMTAWNJL-UHFFFAOYSA-K 0.000 description 3
- 229940079593 drug Drugs 0.000 description 3
- 239000003814 drug Substances 0.000 description 3
- 229920002530 polyetherether ketone Polymers 0.000 description 3
- BWQOPMJTQPWHOZ-UHFFFAOYSA-N (2,3-difluorophenyl)-phenylmethanone Chemical compound FC1=CC=CC(C(=O)C=2C=CC=CC=2)=C1F BWQOPMJTQPWHOZ-UHFFFAOYSA-N 0.000 description 2
- NGNBDVOYPDDBFK-UHFFFAOYSA-N 2-[2,4-di(pentan-2-yl)phenoxy]acetyl chloride Chemical compound CCCC(C)C1=CC=C(OCC(Cl)=O)C(C(C)CCC)=C1 NGNBDVOYPDDBFK-UHFFFAOYSA-N 0.000 description 2
- -1 4,4'-disubstituted benzophenone Chemical class 0.000 description 2
- 244000025254 Cannabis sativa Species 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 125000002915 carbonyl group Chemical group [*:2]C([*:1])=O 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 229910052731 fluorine Inorganic materials 0.000 description 2
- 239000011737 fluorine Substances 0.000 description 2
- 125000001153 fluoro group Chemical group F* 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 239000002920 hazardous waste Substances 0.000 description 2
- 239000005457 ice water Substances 0.000 description 2
- 150000002576 ketones Chemical class 0.000 description 2
- 238000004811 liquid chromatography Methods 0.000 description 2
- 238000003760 magnetic stirring Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 229920006260 polyaryletherketone Polymers 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- 235000010265 sodium sulphite Nutrition 0.000 description 2
- 239000002910 solid waste Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 208000024827 Alzheimer disease Diseases 0.000 description 1
- 241000486679 Antitype Species 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000002490 cerebral effect Effects 0.000 description 1
- 238000005660 chlorination reaction Methods 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 229920006351 engineering plastic Polymers 0.000 description 1
- IDGUHHHQCWSQLU-UHFFFAOYSA-N ethanol;hydrate Chemical compound O.CCO IDGUHHHQCWSQLU-UHFFFAOYSA-N 0.000 description 1
- 239000012847 fine chemical Substances 0.000 description 1
- SMANXXCATUTDDT-QPJJXVBHSA-N flunarizine Chemical compound C1=CC(F)=CC=C1C(C=1C=CC(F)=CC=1)N1CCN(C\C=C\C=2C=CC=CC=2)CC1 SMANXXCATUTDDT-QPJJXVBHSA-N 0.000 description 1
- 229960000326 flunarizine Drugs 0.000 description 1
- 238000003682 fluorination reaction Methods 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 239000011259 mixed solution Substances 0.000 description 1
- 238000005580 one pot reaction Methods 0.000 description 1
- 238000005832 oxidative carbonylation reaction Methods 0.000 description 1
- 229920001643 poly(ether ketone) Polymers 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 229920001169 thermoplastic Polymers 0.000 description 1
- 239000004416 thermosoftening plastic Substances 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 208000001072 type 2 diabetes mellitus Diseases 0.000 description 1
- 238000001291 vacuum drying Methods 0.000 description 1
- 239000003071 vasodilator agent Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C45/00—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds
- C07C45/45—Preparation of compounds having >C = O groups bound only to carbon or hydrogen atoms; Preparation of chelates of such compounds by condensation
- C07C45/46—Friedel-Crafts reactions
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/58—Preparation of carboxylic acid halides
- C07C51/60—Preparation of carboxylic acid halides by conversion of carboxylic acids or their anhydrides or esters, lactones, salts into halides with the same carboxylic acid part
-
- 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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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Abstract
本发明提供了一种4,4’‑二氟二苯甲酮的制备方法,所述制备方法为以对氟苯甲酸为起始原料,经草酰氯反应后生成对氟苯甲酰氯,再经傅克反应,生成4,4’‑二氟二苯甲酮;本发明反应选择性高,所获产品纯度高,环境污染小,收率高,工艺简单,工业生产前景广阔。
The invention provides a preparation method of 4,4'-difluorobenzophenone. The preparation method uses p-fluorobenzoic acid as a starting material, reacts with oxalyl chloride to generate p-fluorobenzoyl chloride, and then reacts with Friedel-Crafts reaction generates 4,4'-difluorobenzophenone; the reaction of the invention has high selectivity, high purity of the obtained product, little environmental pollution, high yield, simple process and broad industrial production prospects.
Description
技术领域Technical field
本发明属于精细化工技术领域,具体涉及一种4,4’-二氟二苯甲酮的制备方法。The invention belongs to the technical field of fine chemicals, and specifically relates to a preparation method of 4,4'-difluorobenzophenone.
背景技术Background technique
4,4'-二氟二苯甲酮, 英文名称4,4'-difluoro-benzophenon, 简称DFBP,白色晶体,熔点102-105 °C,是一种非常重要的合成芳香族热塑性特种工程塑料(如聚醚酮、聚醚醚酮、聚醚醚酮酮、聚芳醚酮、聚芳醚酮酚等)的重要原料。DFBP也是一种重要的医药原料,如可用于合成新型强效脑血管扩张药物氟苯桂嗪、抗二型糖尿病药物地格列汀,以及合成治疗老年神经性痴呆症药物都可喜等药物。4,4'-Difluoro-benzophenone, English name 4,4'-difluoro-benzophenon, referred to as DFBP, white crystal, melting point 102-105 °C, is a very important synthetic aromatic thermoplastic special engineering plastic ( Such as polyether ketone, polyether ether ketone, polyether ether ketone ketone, polyaryl ether ketone, polyaryl ether ketone phenol, etc.). DFBP is also an important pharmaceutical raw material, for example, it can be used to synthesize the new powerful cerebral vasodilator drug flunarizine, the anti-type 2 diabetes drug digagliptin, and the drug Dukexi for the treatment of Alzheimer's disease.
目前, 随着聚醚醚酮树脂在汽车、电子、机械等领域的广泛应用,以及相关药物的市场需求逐年增加, DFBP具有极其广泛的应用市场。At present, with the wide application of polyetheretherketone resin in automobiles, electronics, machinery and other fields, and the increasing market demand for related drugs year by year, DFBP has an extremely wide application market.
近年来国内外对DFBP的合成技术进行了广泛的研究, 发展出了DFBP众多的合成工艺。根据各种工艺的合成原理,大致可分为傅克反应法、氧化羰基化法、4,4'-二取代基二苯甲酮氟化法等方法。In recent years, extensive research has been conducted on the synthesis technology of DFBP at home and abroad, and numerous synthesis processes for DFBP have been developed. According to the synthesis principles of various processes, they can be roughly divided into Friedel-Crafts reaction method, oxidative carbonylation method, 4,4'-disubstituted benzophenone fluorination method and other methods.
通过研究现有的DFBP的合成方法,都存在一定的不足和缺陷。Through studying the existing synthesis methods of DFBP, there are certain shortcomings and defects.
目前工业化反应第一步为中间体对氟苯甲酰氯的合成,工业化方法均以对氟苯甲酸和氯化亚砜为原料,反应过程如下所示:At present, the first step of the industrial reaction is the synthesis of the intermediate p-fluorobenzoyl chloride. The industrial methods all use p-fluorobenzoic acid and thionyl chloride as raw materials. The reaction process is as follows:
, ,
将对氟苯甲酸投入到过量的氯化亚砜中,反应完成后,减压蒸馏回收过量的氯化亚砜,再精馏得到对氟苯甲酰氯,工艺过程副产大量氯化氢和二氧化硫混合酸性气体,经碱液吸收后,变为氯化钠和亚硫酸钠混合溶液,混合盐的提纯工艺复杂,能耗高,目前多以固废或危废的方式处理,环境污染大。Put p-fluorobenzoic acid into excess thionyl chloride. After the reaction is completed, the excess thionyl chloride is recovered by distillation under reduced pressure, and then distilled to obtain p-fluorobenzoyl chloride. The process produces a large amount of mixed acidic hydrogen chloride and sulfur dioxide. After the gas is absorbed by the alkali liquid, it becomes a mixed solution of sodium chloride and sodium sulfite. The purification process of the mixed salt is complicated and consumes high energy. Currently, it is mostly treated as solid waste or hazardous waste, causing great environmental pollution.
反应第二步为傅克反应,工艺需用大量的三氯化铝作为催化剂, 反应和后处理过程产生大量三氯化铝废水,对生产设备腐蚀严重。其反应方程式如下所示:The second step of the reaction is the Friedel-Crafts reaction. The process requires a large amount of aluminum trichloride as a catalyst. The reaction and post-treatment process produce a large amount of aluminum trichloride wastewater, which seriously corrodes the production equipment. The reaction equation is as follows:
, ,
针对现有技术存在的问题,避免有毒有害化学品对环境的污染,提高4.4'二氟二苯甲酮生产工艺安全性和操作便捷性,亟需提出一种能够提高4.4'二氟二苯甲酮生产工艺安全性和操作便捷性的制备方法。In view of the problems existing in the existing technology, to avoid the pollution of the environment by toxic and harmful chemicals, and to improve the safety and operational convenience of the 4.4' difluorobenzophenone production process, it is urgently needed to propose a method that can improve the production process of 4.4' difluorobenzophenone. The preparation method of ketone production process is safe and easy to operate.
发明内容Contents of the invention
为解决上述问题,本发明公开了一种4,4’-二氟二苯甲酮的制备方法。In order to solve the above problems, the present invention discloses a preparation method of 4,4’-difluorobenzophenone.
为达到上述目的,本发明的技术方案如下:In order to achieve the above objects, the technical solutions of the present invention are as follows:
一种4,4’-二氟二苯甲酮的制备方法,所述制备方法包括以下步骤:A preparation method of 4,4'-difluorobenzophenone, the preparation method includes the following steps:
步骤(1):用氟苯做溶剂,加入对氟苯甲酸和催化剂N,N-二甲基甲酰胺,搅拌升温至35℃,开始滴加草酰氯,反应温度控制在35-40℃,滴加时间4-5h,滴加完毕后,继续保温反应2-3h,第一步反应完成,反应方程式如式(1)所示:Step (1): Use fluorobenzene as solvent, add p-fluorobenzoic acid and catalyst N,N-dimethylformamide, stir and raise the temperature to 35°C, start adding oxalyl chloride dropwise, control the reaction temperature at 35-40°C, and drop The addition time is 4-5h. After the dropwise addition is completed, continue the insulation reaction for 2-3h. The first step of the reaction is completed. The reaction equation is as shown in formula (1):
; ;
步骤(2):向步骤(1)的反应液中直接加入催化剂,继续升温至50-70℃,保温反应3-7h,第二步反应完成,反应方程式如式(2)所示:Step (2): Add the catalyst directly to the reaction solution in step (1), continue to raise the temperature to 50-70°C, and keep the reaction for 3-7 hours. The second step reaction is completed. The reaction equation is as shown in formula (2):
; ;
步骤(3):将步骤(2)的反应液进行过滤,回收固体催化剂,用于二次套用,滤液用等体积的清水进行洗涤,加入清水量2-3%的32%碱液,将水相调至pH值为7-8,以除去残留的草酰氯等酸性物质,静置0.5h,分去水相,得到有机相;Step (3): Filter the reaction solution of step (2) to recover the solid catalyst for secondary use. Wash the filtrate with an equal volume of clean water, add 32% alkali solution with 2-3% of clean water, and mix the water with Adjust the phase to a pH value of 7-8 to remove residual acidic substances such as oxalyl chloride, let it stand for 0.5 hours, separate the water phase, and obtain the organic phase;
步骤(4):有机相经减压蒸馏,所述减压蒸馏的条件为70℃水浴温度,真空度≤-0.095Mpa,回收氟苯,剩余重组分为粗产品,加入3倍粗产品质量的溶剂和溶剂质量的0.5%的活性炭,升温至70-90℃,回流反应2h,热过滤除去活性炭,滤液降温至20-25℃,保温2h后,抽滤,固体经减压干燥6h后,所述减压干燥的条件为温度80℃,真空度≤-0.095Mpa,得到4,4’-二氟二苯甲酮。Step (4): The organic phase is distilled under reduced pressure. The conditions of the reduced pressure distillation are 70°C water bath temperature and vacuum degree ≤ -0.095Mpa. Fluorobenzene is recovered. The remaining recombinants are divided into crude products. Add 3 times the mass of the crude product. Solvent and 0.5% of the solvent mass activated carbon, heat to 70-90°C, reflux for 2 hours, remove the activated carbon by hot filtration, cool the filtrate to 20-25°C, keep it for 2 hours, filter with suction, and dry the solid under reduced pressure for 6 hours. The conditions for drying under reduced pressure are a temperature of 80°C and a vacuum degree of ≤-0.095Mpa to obtain 4,4'-difluorobenzophenone.
作为本发明的一种改进,步骤(1)中所述氟苯的添加量为所述对氟苯甲酸质量的2.5-4倍,反应温度为35-45℃。As an improvement of the present invention, the amount of fluorobenzene added in step (1) is 2.5-4 times the mass of p-fluorobenzoic acid, and the reaction temperature is 35-45°C.
作为本发明的一种改进,步骤(1)中所述草酰氯添加量为对氟苯甲酸摩尔量的1.05-1.1倍。As an improvement of the present invention, the amount of oxalyl chloride added in step (1) is 1.05-1.1 times the molar amount of p-fluorobenzoic acid.
作为本发明的一种改进,步骤(2)中所述催化剂为固体可回收催化剂,所述固体可回收催化剂包括酸性白土、固体超强酸和强酸树脂中的任意一种或多种。As an improvement of the present invention, the catalyst in step (2) is a solid recyclable catalyst, and the solid recyclable catalyst includes any one or more of acid clay, solid super acid and strong acid resin.
作为本发明的一种改进,步骤(2)中所述催化剂添加量为对氟苯甲酸质量的5-10%。As an improvement of the present invention, the amount of catalyst added in step (2) is 5-10% of the mass of p-fluorobenzoic acid.
作为本发明的一种改进,步骤(2)中所述反应温度为50-70℃,反应时间为5-7h。As an improvement of the present invention, the reaction temperature in step (2) is 50-70°C, and the reaction time is 5-7h.
作为本发明的一种改进,步骤(4)中所述溶剂包括乙醇、碳酸二甲酯和碳酸甲乙酯中的任意一种或多种。As an improvement of the present invention, the solvent in step (4) includes any one or more of ethanol, dimethyl carbonate and ethyl methyl carbonate.
作为本发明的一种改进,步骤(4)中所述溶剂添加量为4,4’-二氟二苯甲酮粗品质量比的2-3倍。As an improvement of the present invention, the amount of solvent added in step (4) is 2-3 times the mass ratio of the crude product of 4,4’-difluorobenzophenone.
作为本发明的一种改进,步骤(4)中所述活性炭为椰壳活性炭,碘值≥900mg/g,目数为200目、300目、500目中任意一种或多种。As an improvement of the present invention, the activated carbon in step (4) is coconut shell activated carbon, the iodine value is ≥900 mg/g, and the mesh number is any one or more of 200 mesh, 300 mesh, and 500 mesh.
作为本发明的一种改进,步骤(4)中所述活性炭添加量为溶剂质量的0.3-1%。As an improvement of the present invention, the amount of activated carbon added in step (4) is 0.3-1% of the solvent mass.
本发明的有益效果为:The beneficial effects of the present invention are:
1、第一步氯代反应,采用高效的草酰氯替代传统的氯化亚砜,避免固废或危废(氯化钠和亚硫酸钠的混合物)的产生;1. In the first step of the chlorination reaction, efficient oxalyl chloride is used instead of traditional thionyl chloride to avoid the generation of solid waste or hazardous waste (a mixture of sodium chloride and sodium sulfite);
2、本发明傅克反应采用可回收固体催化剂,反应完成,经简单过滤后,即可实现催化剂与反应液的分离,催化剂可回收套用,避免了传统工艺中三氯化铝废水的产生,极大地提高了工艺的环保性;2. The Friedel-Crafts reaction of the present invention uses a recyclable solid catalyst. After the reaction is completed, the catalyst and the reaction liquid can be separated after simple filtration. The catalyst can be recycled and reused, avoiding the generation of aluminum trichloride wastewater in the traditional process, and extremely Dadi improves the environmental friendliness of the process;
3、本发明将传统的二步两锅合成工艺,合并为一锅法,简化了操作工艺,提高了工艺的安全性和环保性。3. The present invention combines the traditional two-step two-pot synthesis process into a one-pot method, which simplifies the operation process and improves the safety and environmental protection of the process.
附图说明Description of the drawings
图1为4,4’-二氟二苯甲酮标准品超高液相色谱(HPLC)图;Figure 1 shows the ultra-high liquid chromatography (HPLC) chart of 4,4’-difluorobenzophenone standard;
图2为实验合成的4,4’-二氟二苯甲酮超高液相色谱(HPLC)图。Figure 2 shows the ultra-high liquid chromatography (HPLC) chart of experimentally synthesized 4,4’-difluorobenzophenone.
具体实施方式Detailed ways
下面结合附图和具体实施方式,进一步阐明本发明,应理解下述具体实施方式仅用于说明本发明而不用于限制本发明的范围。The present invention will be further clarified below with reference to the accompanying drawings and specific embodiments. It should be understood that the following specific embodiments are only used to illustrate the present invention and are not intended to limit the scope of the present invention.
实施例1Example 1
准确称取氟苯350g于1L四口烧瓶中, 加入对氟苯甲酸140g(1mol)和N,N-二甲基甲酰胺0.5g,开启磁力搅拌,然后缓慢升温至35℃,缓慢滴加草酰氯133.5g(1.05mol),滴加时间4h,滴加期间控制反应液温度为35-40℃,反应产生的尾气用10%碱液吸收,随着滴加的进行,反应液逐渐变为澄清,滴加完毕后,保温反应2h,反应液基本澄清透明,说明对氟苯甲酸反应完全,第一步反应完成;Accurately weigh 350g of fluorobenzene into a 1L four-necked flask, add 140g (1mol) of p-fluorobenzoic acid and 0.5g of N,N-dimethylformamide, turn on magnetic stirring, then slowly raise the temperature to 35°C, and slowly add grass dropwise. Acid chloride 133.5g (1.05mol), the dropping time is 4 hours. During the dropping period, the temperature of the reaction solution is controlled to 35-40°C. The tail gas generated by the reaction is absorbed with 10% alkali solution. As the dropwise addition proceeds, the reaction solution gradually becomes clear. , after the dropwise addition, keep the temperature for 2 hours and the reaction solution is basically clear and transparent, indicating that the p-fluorobenzoic acid reaction is complete and the first step of the reaction is completed;
向上述反应液中投入干燥后的酸性白土14g,所述干燥后的酸性白土活性度≥250mmol/kg,继续升温至50℃,保温反应7h,反应产生的尾气用10%碱液吸收,第二步反应完成;Pour 14g of dried acidic clay into the above reaction solution. The activity of the dried acidic clay is ≥250mmol/kg. Continue to raise the temperature to 50°C and keep the reaction for 7 hours. The tail gas generated by the reaction is absorbed with 10% alkali solution. The second The step reaction is completed;
再将反应液进行抽滤,回收固体为催化剂,不经干燥,直接用于下一批次的反应,滤液转移至2L四口烧瓶中,加入500g水,并用32%碱液调节溶液pH值为7-8,分去水相;有机相用旋转蒸发仪进行减压蒸馏(70℃水浴温度,真空度≤-0.095Mpa),以回收过量的氟苯,剩余重组分呈浅红色,加入450g无水乙醇和2.25g 200目活性炭,加热升温至79℃,保温2h,然后热过滤,滤液转移至夹套玻璃反应釜中,用冰水降温至25℃,保温1h后,抽滤,固体经真空干燥箱干燥(温度80℃,真空度≤-0.095Mpa)6h后,得到4,4’-二氟二苯甲酮成品,产量209.2g,收率96%,产品经高效液相色谱检测,其含量≥99.5%,产品经H1-NMR检测,δ7.28(4H, t, 苯环上氟邻位的氢);δ7.81(4H, m, 苯环上羰基邻位的氢),符合4,4’-二氟二苯甲酮结构。The reaction solution is then suction filtered, and the solid is recovered as a catalyst. It is directly used in the next batch of reactions without drying. The filtrate is transferred to a 2L four-necked flask, 500g of water is added, and the pH value of the solution is adjusted with 32% alkali solution. 7-8, separate the water phase; use a rotary evaporator to distill the organic phase under reduced pressure (70°C water bath temperature, vacuum degree ≤ -0.095Mpa) to recover excess fluorobenzene. The remaining heavy component will be light red, add 450g of free Water ethanol and 2.25g of 200 mesh activated carbon were heated to 79°C, maintained for 2 hours, and then hot filtered. The filtrate was transferred to a jacketed glass reactor, cooled to 25°C with ice water, maintained for 1 hour, filtered, and the solid was vacuum After drying in a drying oven (temperature 80°C, vacuum degree ≤-0.095Mpa) for 6 hours, the finished product of 4,4'-difluorobenzophenone was obtained, with a yield of 209.2g and a yield of 96%. The product was tested by high-performance liquid chromatography. Content ≥99.5%, the product was detected by H1-NMR, δ7.28 (4H, t, hydrogen in the ortho position of the fluorine on the benzene ring); δ7.81 (4H, m, hydrogen in the ortho position of the carbonyl group on the benzene ring), consistent with 4 ,4'-difluorobenzophenone structure.
实施例2Example 2
准确称取氟苯560g于1L四口烧瓶中, 加入对氟苯甲酸140g(1mol)和N,N-二甲基甲酰胺0.5g,开启磁力搅拌,然后缓慢升温至35℃,开始滴加草酰氯140g(1.1mol),滴加时间4h,滴加期间控制反应液温度为35-40℃,反应产生的尾气用10%碱液吸收,随着滴加的进行,反应液逐渐变为澄清,滴加完毕后,保温反应2h,反应液基本澄清透明,说明对氟苯甲酸反应完全,第一步反应完成;Accurately weigh 560g of fluorobenzene into a 1L four-necked flask, add 140g (1mol) of p-fluorobenzoic acid and 0.5g of N,N-dimethylformamide, turn on the magnetic stirring, then slowly raise the temperature to 35°C, and start adding grass dropwise 140g of acid chloride (1.1mol), the dropping time is 4 hours. During the dropping period, the temperature of the reaction solution is controlled to 35-40°C. The tail gas generated by the reaction is absorbed with 10% alkali solution. As the dropwise addition proceeds, the reaction solution gradually becomes clear. After the dropwise addition is completed, the reaction solution is kept warm for 2 hours. The reaction solution is basically clear and transparent, indicating that the p-fluorobenzoic acid reaction is complete and the first step of the reaction is completed;
向上述反应液中投入实例1中回收的催化剂8.5g(湿催化剂总质量约17g),继续升温至70℃,保温反应5h,反应产生的尾气用10%碱液吸收,第二步反应完成;Add 8.5g of the catalyst recovered in Example 1 into the above reaction solution (the total mass of the wet catalyst is about 17g), continue to raise the temperature to 70°C, and keep the reaction for 5 hours. The tail gas generated by the reaction is absorbed with 10% alkali solution, and the second step of the reaction is completed;
再将反应液进行抽滤,回收固体为催化剂,不经干燥,直接用于下一批次的反应,滤液转移至2L四口烧瓶中,加入600g水,并用32%碱液调节溶液pH值为7-8,分去水相。有机相用旋转蒸发仪进行减压蒸馏,以回收过量的氟苯。剩余重组分呈浅红色,加入675g无水乙醇和6.75g 500目的活性炭,加热升温至79℃,回流反应2h,然后热过滤,滤液转移至夹套玻璃反应釜中,用冰水降温至20℃,保温1h后,抽滤,固体经真空干燥箱干燥(温度80℃,真空度≤-0.095Mpa)6h后,得到4,4’-二氟二苯甲酮成品,产量205.4g, 收率94.2%,产品经高效液相色谱检测,其含量≥99.5%,产品经H1-NMR检测,δ7.28(4H, t, 苯环上氟邻位的氢);δ7.81(4H, m, 苯环上羰基邻位的氢),符合4,4’-二氟二苯甲酮结构。The reaction solution is then suction filtered, and the solid is recovered as a catalyst. It is directly used for the next batch of reactions without drying. The filtrate is transferred to a 2L four-necked flask, 600g of water is added, and the pH value of the solution is adjusted with 32% alkali solution. 7-8, separate the water phase. The organic phase was distilled under reduced pressure using a rotary evaporator to recover excess fluorobenzene. The remaining heavy components are light red, add 675g absolute ethanol and 6.75g 500 mesh activated carbon, heat to 79°C, reflux for 2 hours, then hot filter, transfer the filtrate to a jacketed glass reactor, and cool to 20°C with ice water , after being incubated for 1 hour, filtered, and the solid was dried in a vacuum drying oven (temperature 80°C, vacuum degree ≤ -0.095Mpa) for 6 hours, and the finished product 4,4'-difluorobenzophenone was obtained, with an output of 205.4g and a yield of 94.2 %, the product was detected by high performance liquid chromatography, and its content was ≥99.5%. The product was detected by H1-NMR, δ7.28 (4H, t, hydrogen in the ortho position of fluorine on the benzene ring); δ7.81 (4H, m, benzene hydrogen ortho to the carbonyl group on the ring), consistent with the structure of 4,4'-difluorobenzophenone.
需要说明的是,以上内容仅仅说明了本发明的技术思想,不能以此限定本发明的保护范围,对于本技术领域的普通技术人员来说,在不脱离本发明原理的前提下,还可以做出若干改进和润饰,这些改进和润饰均落入本发明权利要求书的保护范围之内。It should be noted that the above content only illustrates the technical idea of the present invention and cannot limit the protection scope of the present invention. For those of ordinary skill in the technical field, without departing from the principle of the present invention, they can also make Several improvements and modifications are made, and these improvements and modifications fall within the protection scope of the claims of the present invention.
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