CN103193740A - Preparation method of alpha-naphtholphthalein - Google Patents
Preparation method of alpha-naphtholphthalein Download PDFInfo
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- 238000002360 preparation method Methods 0.000 title claims abstract description 20
- HQHBAGKIEAOSNM-UHFFFAOYSA-N naphtholphthalein Chemical compound C1=CC=C2C(C3(C4=CC=CC=C4C(=O)O3)C3=CC=C(C4=CC=CC=C43)O)=CC=C(O)C2=C1 HQHBAGKIEAOSNM-UHFFFAOYSA-N 0.000 title claims abstract description 15
- KJCVRFUGPWSIIH-UHFFFAOYSA-N 1-naphthol Chemical compound C1=CC=C2C(O)=CC=CC2=C1 KJCVRFUGPWSIIH-UHFFFAOYSA-N 0.000 claims abstract description 44
- 239000012065 filter cake Substances 0.000 claims abstract description 42
- 239000000706 filtrate Substances 0.000 claims abstract description 37
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 34
- 238000009835 boiling Methods 0.000 claims abstract description 27
- 239000000843 powder Substances 0.000 claims abstract description 27
- 238000006243 chemical reaction Methods 0.000 claims abstract description 25
- 239000008367 deionised water Substances 0.000 claims abstract description 24
- 229910021641 deionized water Inorganic materials 0.000 claims abstract description 24
- 239000007788 liquid Substances 0.000 claims abstract description 24
- 239000000047 product Substances 0.000 claims abstract description 24
- LGRFSURHDFAFJT-UHFFFAOYSA-N Phthalic anhydride Natural products C1=CC=C2C(=O)OC(=O)C2=C1 LGRFSURHDFAFJT-UHFFFAOYSA-N 0.000 claims abstract description 23
- JHIWVOJDXOSYLW-UHFFFAOYSA-N butyl 2,2-difluorocyclopropane-1-carboxylate Chemical compound CCCCOC(=O)C1CC1(F)F JHIWVOJDXOSYLW-UHFFFAOYSA-N 0.000 claims abstract description 22
- 239000002904 solvent Substances 0.000 claims abstract description 17
- 238000000034 method Methods 0.000 claims abstract description 12
- 239000000376 reactant Substances 0.000 claims abstract description 12
- 238000000746 purification Methods 0.000 claims abstract description 10
- 238000000926 separation method Methods 0.000 claims abstract description 10
- 238000004458 analytical method Methods 0.000 claims abstract description 5
- 239000012141 concentrate Substances 0.000 claims abstract description 3
- 238000003756 stirring Methods 0.000 claims description 34
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims description 33
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical group ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 claims description 28
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 24
- AFVFQIVMOAPDHO-UHFFFAOYSA-N Methanesulfonic acid Chemical compound CS(O)(=O)=O AFVFQIVMOAPDHO-UHFFFAOYSA-N 0.000 claims description 20
- ZWEHNKRNPOVVGH-UHFFFAOYSA-N 2-Butanone Chemical group CCC(C)=O ZWEHNKRNPOVVGH-UHFFFAOYSA-N 0.000 claims description 13
- QAOWNCQODCNURD-UHFFFAOYSA-N sulfuric acid Substances OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 13
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical group CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 claims description 10
- 239000003054 catalyst Substances 0.000 claims description 10
- 229940098779 methanesulfonic acid Drugs 0.000 claims description 10
- 238000004811 liquid chromatography Methods 0.000 claims description 9
- 238000010298 pulverizing process Methods 0.000 claims description 9
- 239000003513 alkali Substances 0.000 claims description 7
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 claims description 6
- RTZKZFJDLAIYFH-UHFFFAOYSA-N Diethyl ether Chemical compound CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 claims description 4
- 239000002841 Lewis acid Substances 0.000 claims description 2
- 150000007517 lewis acids Chemical group 0.000 claims description 2
- 238000001914 filtration Methods 0.000 abstract description 8
- 238000001035 drying Methods 0.000 abstract description 7
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 238000005406 washing Methods 0.000 abstract description 2
- 229920000297 Rayon Polymers 0.000 abstract 1
- 239000012670 alkaline solution Substances 0.000 abstract 1
- -1 filter Substances 0.000 abstract 1
- 238000010438 heat treatment Methods 0.000 abstract 1
- 239000002244 precipitate Substances 0.000 description 28
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 24
- 230000007935 neutral effect Effects 0.000 description 13
- 230000002378 acidificating effect Effects 0.000 description 6
- 239000012153 distilled water Substances 0.000 description 6
- 239000007787 solid Substances 0.000 description 6
- 238000005292 vacuum distillation Methods 0.000 description 5
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 4
- 239000006227 byproduct Substances 0.000 description 4
- 238000005070 sampling Methods 0.000 description 4
- 238000010977 unit operation Methods 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- 239000007795 chemical reaction product Substances 0.000 description 2
- 239000012043 crude product Substances 0.000 description 2
- 238000004090 dissolution Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000001291 vacuum drying Methods 0.000 description 2
- 238000005481 NMR spectroscopy Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000052 comparative effect Effects 0.000 description 1
- 208000012839 conversion disease Diseases 0.000 description 1
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Heterocyclic Carbon Compounds Containing A Hetero Ring Having Oxygen Or Sulfur (AREA)
Abstract
一种α-萘酚酞的制备方法,它包括a.粉碎工序:将邻苯二甲酸酐和1-萘酚预先粉碎成粉末;b.反应工序;c.分离提纯工序:用溶剂a溶解上述粘稠的反应物,过滤;用碱溶液中和滤液,过滤,浓缩滤液,得到粘稠液体;向粘稠液体中加入溶剂b,加热至沸腾,降温过滤;将滤饼中加入去离子水,加热至沸腾,过滤,洗涤,将滤饼用溶剂c溶解,加热至沸腾并用去离子水强析,过滤;干燥,得到α-萘酚酞粉体。本发明工艺简单,产品的收率高、纯度高,且易于工业化生产。
A preparation method of α-naphtholphthalein, which comprises a. crushing process: phthalic anhydride and 1-naphthol are pulverized into powder in advance; b. reaction process; c. separation and purification process: dissolve the above viscose with solvent a thick reactant, filter; neutralize the filtrate with alkaline solution, filter, concentrate the filtrate to obtain a viscous liquid; add solvent b to the viscous liquid, heat to boiling, cool down and filter; add deionized water to the filter cake, heat until boiling, filtering, washing, dissolving the filter cake with solvent c, heating to boiling and strong analysis with deionized water, filtering; drying to obtain α-naphtholphthalein powder. The invention has simple process, high product yield and high purity, and is easy for industrialized production.
Description
技术领域 technical field
本发明涉及α-萘酚酞的制备方法。 The invention relates to a preparation method of α-naphtholphthalein.
技术背景 technical background
α-萘酚酞又称1-萘酚酞,甲-萘酚酞,3,3'-双(4-羟基-1-萘基)-1(3H)-异苯并呋喃酮,英文名称:α-Naphtholphthalein,3,3-Bis(4-hydroxy-1-naphthyl)phthalide α-naphtholphthalein is also known as 1-naphtholphthalein, methyl-naphtholphthalein, 3,3'-bis(4-hydroxy-1-naphthyl)-1(3H)-isobenzofuranone, English name: α-Naphtholphthalein , 3,3-Bis(4-hydroxy-1-naphthyl)phthalide
结构式如下: The structural formula is as follows:
其反应原理如下: Its reaction principle is as follows:
公开的制备方法是:3.8克邻苯二甲酸酐和7.0克α-萘酚在60℃使用0.75ml浓硫酸做催化剂反应4小时得到粘稠状粗品,经大量的水稀释硫酸并破碎使产物成粒状,然后用大量0.5%的稀碱(NaOH)加热至70℃溶解产物过滤分离副产物,再经盐酸调pH使产物α-萘酚酞析出,静置沉淀过滤洗涤并重复碱溶酸析一次,经硫酸真空干燥得到2.3克产品。该制备方法存在如下缺点:(1)产品的收率低;(2)产品的纯度低;(3)生产成本高,无法进行大规模工业化生产。 The disclosed preparation method is: 3.8 grams of phthalic anhydride and 7.0 grams of α-naphthol were reacted at 60° C. using 0.75 ml of concentrated sulfuric acid as a catalyst for 4 hours to obtain a viscous crude product. The sulfuric acid was diluted with a large amount of water and crushed to make the product into a Granular, then heated to 70°C with a large amount of 0.5% dilute alkali (NaOH) to dissolve the product, filter and separate the by-products, then adjust the pH with hydrochloric acid to precipitate the product α-naphtholphthalein, set aside to precipitate, filter and wash, and repeat alkali dissolution and acid analysis once. Vacuum drying over sulfuric acid yielded 2.3 g of product. The preparation method has the following disadvantages: (1) the yield of the product is low; (2) the purity of the product is low; (3) the production cost is high, and large-scale industrial production cannot be carried out.
发明内容 Contents of the invention
本发明要解决的技术问题是针对现有技术之不足,提供一种α-萘酚酞的制备方法。 The technical problem to be solved by the present invention is to provide a preparation method of α-naphtholphthalein aiming at the deficiencies of the prior art.
为解决上述技术问题,本发明采用的技术方案是: In order to solve the problems of the technologies described above, the technical solution adopted in the present invention is:
一种α-萘酚酞的制备方法,所述方法包括如下工序: A preparation method of α-naphtholphthalein, said method comprising the following steps:
a.粉碎工序:将邻苯二甲酸酐和1-萘酚预先粉碎成粉末; a. Pulverization process: phthalic anhydride and 1-naphthol are pulverized into powder in advance;
b.反应工序: b. Reaction process:
在反应容器中加入上述粉碎成粉末的邻苯二甲酸酐和1-萘酚,其摩尔比为1:1.5~1:2.5;搅拌下加入催化剂,在0~40℃的温度下反应3h以上,再静置12h以上,然后在35~60℃、搅拌反应3h以上,取样用液相色谱跟踪,待反应主产物含量不再增加时停止反应,得到粘稠的反应物; Add the above-mentioned phthalic anhydride and 1-naphthol crushed into powder in the reaction vessel, the molar ratio is 1:1.5~1:2.5; add the catalyst under stirring, and react at the temperature of 0~40°C for more than 3h, Let it stand still for more than 12 hours, then stir and react at 35-60°C for more than 3 hours, take a sample and track it with liquid chromatography, stop the reaction when the content of the main product of the reaction no longer increases, and obtain a viscous reactant;
c.分离提纯工序: c. Separation and purification process:
用溶剂a溶解上述粘稠的反应物,过滤;用碱溶液中和滤液,过滤,降温析出,过滤;浓缩滤液,得到粘稠液体;向粘稠液体中加入溶剂b,加热至沸腾,降温过滤;将滤饼转移至容器中加入去离子水,加热至沸腾,过滤,洗涤;将滤饼转移至容器中用溶剂c溶解,加热至沸腾并用去离子水强析,过滤;干燥,得到α-萘酚酞粉体。 Dissolve the above viscous reactants with solvent a, filter; neutralize the filtrate with alkali solution, filter, cool down to precipitate, filter; concentrate the filtrate to obtain a viscous liquid; add solvent b to the viscous liquid, heat to boiling, cool down and filter ; transfer the filter cake to a container, add deionized water, heat to boiling, filter, and wash; transfer the filter cake to a container and dissolve it with solvent c, heat to boiling and use deionized water for strong analysis, filter; dry to obtain α- Naphtholphthalein powder.
上述制备方法,所述邻苯二甲酸酐与1-萘酚摩尔比为1:1.8~1:2.2。 In the above preparation method, the molar ratio of phthalic anhydride to 1-naphthol is 1:1.8 to 1:2.2.
上述制备方法,所述催化剂为路易斯酸,优选其中的ZnCl2、AlCl3、TiCl4、浓硫酸或甲磺酸,更优选浓硫酸或甲磺酸。 In the above preparation method, the catalyst is a Lewis acid, preferably ZnCl 2 , AlCl 3 , TiCl 4 , concentrated sulfuric acid or methanesulfonic acid, more preferably concentrated sulfuric acid or methanesulfonic acid.
上述制备方法,所述溶剂a是乙醇、甲醇或醚、苯;所述溶剂b是氯仿、丙酮或丁酮;所述溶剂c是乙醇或甲醇。 In the above preparation method, the solvent a is ethanol, methanol or ether, benzene; the solvent b is chloroform, acetone or butanone; the solvent c is ethanol or methanol.
上述制备方法,在所述b.反应工序中,在加入催化剂后,在10~15℃的温度下反应3h以上,静置12h以上,然后在35~45℃、搅拌反应3h以上。 In the above preparation method, in the b. reaction step, after adding the catalyst, react at a temperature of 10-15°C for more than 3 hours, stand still for more than 12 hours, and then react with stirring at 35-45°C for more than 3 hours.
上述制备方法,在所述b.反应工序中,在加入催化剂后,在10~15℃的温度下反应72h,静置12h以上,然后在35~45℃、搅拌反应10-24h。 In the above preparation method, in the b. reaction step, after adding the catalyst, react at a temperature of 10-15°C for 72h, let stand for more than 12h, and then react with stirring at 35-45°C for 10-24h.
有益效果 Beneficial effect
与现有技术相比,本发明具有如下优点: Compared with prior art, the present invention has following advantage:
1.通过将原料萘酚和邻苯二甲酸酐粉碎,可以大幅度增加反应物接触面积,提高反应速率,并且易于后处理提纯。 1. By pulverizing the raw materials naphthol and phthalic anhydride, the contact area of the reactants can be greatly increased, the reaction rate can be increased, and it is easy to purify after treatment.
2.在反应工序中,采用分步温度和匹配反应时间可以兼顾反应转化率和反应速率,使收率更高,副产物相对较低;采用优选的催化剂可以得到易于后处理的反应产物,尤其是适应工业化单元操作。 2. In the reaction process, the use of step-by-step temperature and matching reaction time can take into account the reaction conversion rate and reaction rate, so that the yield is higher and the by-products are relatively low; the use of a preferred catalyst can obtain a reaction product that is easy to post-process, especially It is suitable for industrialized unit operation.
3.采用本发明的工艺,反应产物不是坚硬的团块状,而是粘稠状,进而可以加入溶剂a溶解并与主要的副产物分离,适合工业化单元操作;本发明的溶剂均可以回收重复利用,减少环境污染和降低成本;可以大幅降低后处理时碱溶液体积(浓度提高40倍),适合工业化单元操作;废水产生量少;分离提纯彻底,可以容易获得含量超过98%的产品;收率高。 3. adopt technology of the present invention, reaction product is not hard agglomerate, but viscous shape, and then can add solvent a to dissolve and separate with main by-product, be suitable for industrialized unit operation; Solvent of the present invention all can reclaim and repeat Utilization can reduce environmental pollution and cost; it can greatly reduce the volume of alkali solution during post-treatment (concentration increased by 40 times), which is suitable for industrial unit operation; the amount of waste water is small; the separation and purification are thorough, and products with a content of more than 98% can be easily obtained; High rate.
附图说明 Description of drawings
附图1是实施例1产物的红外光谱图。
Accompanying
附图2是实施例1产物的核磁共振谱图。
具体实施方式 Detailed ways
比较例: Comparative example:
在1L的三口瓶中装有搅拌(搅拌速度500rpm)。邻苯二甲酸酐190g、α-萘酚350g,投料比(mol比)为1:1.89,搅拌均匀加入浓硫酸37.5ml,外温60℃保温4h,得到极粘稠状粗品,破碎三口瓶,经50L水稀释含硫酸产物并将产物破碎成粒状,用50L水多次浸泡粒状产物及洗涤至水洗水呈中性,然后用0.5%的稀碱(NaOH)100L加热至70℃溶解产物过滤分离副产物,将滤液降温至10℃以下,缓慢滴加1:1(V/V)盐酸调pH使产物α-萘酚酞析出,静置过夜沉淀,过滤并洗涤,并重复碱溶酸析一次,过滤,经硫酸真空干燥得到85.5克产品,液相色谱测定含量为93.45%。 Stirring was installed in a 1L three-necked flask (stirring speed: 500 rpm). Phthalic anhydride 190g, α-naphthol 350g, feed ratio (mol ratio) is 1:1.89, stir evenly, add concentrated sulfuric acid 37.5ml, keep temperature at 60°C for 4h, get very viscous crude product, break the there-necked bottle, Dilute the sulfuric acid product with 50L of water and crush the product into granules. Soak the granulated product with 50L of water for several times and wash until the washing water is neutral, then heat to 70℃ with 100L of 0.5% dilute alkali (NaOH) to dissolve the product, filter and separate For by-products, cool the filtrate to below 10°C, slowly add 1:1 (V/V) hydrochloric acid dropwise to adjust the pH to precipitate the product α-naphtholphthalein, let stand overnight to precipitate, filter and wash, and repeat alkali dissolution and acid analysis once, Filtration, vacuum drying through sulfuric acid to obtain 85.5 grams of product, the content determined by liquid chromatography is 93.45%.
实施例1: Example 1:
a.粉碎工序:邻苯二甲酸酐和α-萘酚预先粉碎成粉末; a. Pulverization process: phthalic anhydride and α-naphthol are pulverized into powder in advance;
b.反应工序: b. Reaction process:
在1L的三口瓶中装有搅拌(搅拌速度225rpm),加入邻苯二甲酸酐粉末190g、α-萘酚粉末350g,投料比(mol比)为1:1.89,搅拌均匀加入甲磺酸150ml,在15℃反应9h,并在10-15℃放置62h,然后升温至40℃,搅拌下恒温9h,取样测液色含量为28.85%; In a 1L three-neck flask equipped with stirring (stirring speed 225rpm), add 190g of phthalic anhydride powder and 350g of α-naphthol powder, the ratio (mol ratio) is 1:1.89, stir evenly and add 150ml of methanesulfonic acid, React at 15°C for 9 hours, and place it at 10-15°C for 62 hours, then raise the temperature to 40°C, keep stirring for 9 hours, and take a sample to measure the color content of the liquid to be 28.85%;
c.分离提纯工序: c. Separation and purification process:
用4.6L的无水乙醇溶解墨绿色粘稠的反应物,有白色不溶物析出,过滤,此时滤液为强酸性,用437ml的20%(w/w)的NaOH(去离子水配置)调节pH值为中性(用试纸测试),有大量的不溶物析出,稍粘稠状,过滤,滤液降温还会有不溶物析出,再次过滤,滤饼用少量无水乙醇冲洗。所有滤液减压蒸馏,蒸馏至无液体滴下,回收乙醇。减压蒸馏后瓶内的粘稠液体加入2L的氯仿,加热至沸腾,再有不溶物析出,过滤,滤饼用1L的氯仿洗涤,滤液减压蒸馏回收氯仿。滤饼用3L的去离子水洗涤,转移至容器中加热至沸腾,煮沸,过滤,滤饼用热去离子水洗至滤液pH为中性。滤饼用2L的无水乙醇溶解,加热至沸腾(完全溶解)用2.25L的蒸馏水强析,有浅粉色的固体析出,过滤,滤饼置于电热干燥箱内35℃干燥,即得浅粉色粉状产物152.1克,收率为30.05%。液相色谱测定含量为99.28%。 Dissolve the dark green viscous reactant with 4.6L of absolute ethanol, white insoluble matter precipitates out, filter, at this time the filtrate is strongly acidic, adjust with 437ml of 20% (w/w) NaOH (deionized water configuration) The pH value is neutral (tested with test paper), and a large amount of insoluble matter precipitates out, which is slightly viscous. After filtering, the filtrate cools down and insoluble matter precipitates out. Filter again, and rinse the filter cake with a small amount of absolute ethanol. All filtrates were distilled under reduced pressure until no liquid dripped down to recover ethanol. After vacuum distillation, add 2L of chloroform to the viscous liquid in the bottle, heat to boiling, then insoluble matter precipitates out, filter, and wash the filter cake with 1L of chloroform, and the filtrate is distilled under reduced pressure to recover chloroform. The filter cake was washed with 3L of deionized water, transferred to a container and heated to boiling, boiled, filtered, and the filter cake was washed with hot deionized water until the pH of the filtrate was neutral. Dissolve the filter cake with 2L of absolute ethanol, heat it to boiling (completely dissolved), analyze it strongly with 2.25L of distilled water, a light pink solid precipitates out, filter it, and dry the filter cake in an electric drying oven at 35°C to obtain a light pink color The powdery product was 152.1 g, and the yield was 30.05%. The content determined by liquid chromatography is 99.28%.
实施例2: Example 2:
a.粉碎工序:邻苯二甲酸酐和α-萘酚预先粉碎成粉末; a. Pulverization process: phthalic anhydride and α-naphthol are pulverized into powder in advance;
b.反应工序: b. Reaction process:
在1L的三口瓶中装有搅拌(搅拌速度225rpm),加入邻苯二甲酸酐粉末190g、α-萘酚粉末370g,投料比(mol比)为1:2.0,搅拌均匀加入甲磺酸150ml,在10℃反应15h,并10-15℃放置60h,然后升温至40℃,搅拌下恒温9h,室温放置14h,室温至40℃。取样测液色含量为29.31%。 In a 1L three-neck flask equipped with stirring (stirring speed 225rpm), add 190g of phthalic anhydride powder and 370g of α-naphthol powder, the ratio of feed (mol ratio) is 1:2.0, stir evenly and add 150ml of methanesulfonic acid, React at 10°C for 15h, and stand at 10-15°C for 60h, then raise the temperature to 40°C, keep stirring for 9h, stand at room temperature for 14h, and room temperature to 40°C. Sampling and measuring liquid color content is 29.31%.
c.分离提纯工序: c. Separation and purification process:
用4.6L的无水乙醇溶解墨绿色粘稠的反应物,有白色不溶物析出,过滤,此时滤液为强酸性,用430ml的20%(w/w)的NaOH(去离子水配置)调节pH值为中性(用试纸测试),有大量的不溶物析出,稍粘稠状,过滤,滤液降温还会有不溶物析出,再次过滤,滤饼用少量无水乙醇冲洗。所有滤液减压蒸馏,蒸馏至无液体滴下,回收乙醇。减压蒸馏后瓶内的粘稠液体加入2L的氯仿,加热至沸腾,再有不溶物析出,过滤,滤饼用1L的氯仿洗涤,滤液减压蒸馏回收氯仿。滤饼用3L的去离子水洗涤,转移至容器中加热至沸腾,煮沸,过滤,滤饼用热去离子水洗至滤液pH为中性。滤饼用2L的无水乙醇溶解,加热至沸腾(完全溶解)用2.25L的蒸馏水强析,有浅粉色的固体析出,过滤,滤饼置于电热干燥箱内35℃干燥,即得浅粉色粉状产物154.3克,收率为30.48%。液相色谱测定含量为99.42%。 Dissolve the dark green viscous reactant with 4.6L of absolute ethanol, and white insoluble matter precipitates out, and filter it. At this time, the filtrate is strongly acidic, adjust it with 430ml of 20% (w/w) NaOH (deionized water configuration) The pH value is neutral (tested with test paper), and a large amount of insoluble matter precipitates out, which is slightly viscous. After filtering, the filtrate cools down and insoluble matter precipitates out. Filter again, and rinse the filter cake with a small amount of absolute ethanol. All filtrates were distilled under reduced pressure until no liquid dripped down to recover ethanol. After vacuum distillation, add 2L of chloroform to the viscous liquid in the bottle, heat to boiling, then insoluble matter precipitates out, filter, and wash the filter cake with 1L of chloroform, and the filtrate is distilled under reduced pressure to recover chloroform. The filter cake was washed with 3L of deionized water, transferred to a container and heated to boiling, boiled, filtered, and the filter cake was washed with hot deionized water until the pH of the filtrate was neutral. Dissolve the filter cake with 2L of absolute ethanol, heat it to boiling (completely dissolved), analyze it strongly with 2.25L of distilled water, a light pink solid precipitates out, filter it, and dry the filter cake in an electric drying oven at 35°C to obtain a light pink color The powdery product was 154.3 g, and the yield was 30.48%. The content determined by liquid chromatography is 99.42%.
实施例3: Example 3:
a.粉碎工序:邻苯二甲酸酐和α-萘酚预先粉碎成粉末; a. Pulverization process: phthalic anhydride and α-naphthol are pulverized into powder in advance;
b.反应工序: b. Reaction process:
在1L的三口瓶中装有搅拌(搅拌速度225rpm)中,加入邻苯二甲酸酐粉末190g、α-萘酚粉末334g,投料比(mol比)为1:1.8,搅拌均匀加入甲磺酸180ml, 在15℃反应9h,并在25℃放置38h,然后升温至40℃,搅拌下反应9h,取样测液色含量为27.63%。 Add 190g of phthalic anhydride powder and 334g of α-naphthol powder into a 1L three-neck flask with stirring (stirring speed 225rpm), and the ratio (mol ratio) is 1:1.8. Stir evenly and add 180ml of methanesulfonic acid , reacted at 15°C for 9h, and stood at 25°C for 38h, then raised the temperature to 40°C, reacted for 9h under stirring, and took a sample to measure the liquid color content to be 27.63%.
c.分离提纯工序: c. Separation and purification process:
用4.6L的无水乙醇溶解墨绿色粘稠的反应物,有白色不溶物析出,过滤,此时滤液为强酸性,用460ml的20%(w/w)的NaOH(去离子水配置)调节pH值为中性(用试纸测试),有大量的不溶物析出,稍粘稠状,过滤,滤液降温还会有不溶物析出,再次过滤,滤饼用少量无水乙醇冲洗。所有滤液减压蒸馏,蒸馏至无液体滴下,回收乙醇。减压蒸馏后瓶内的粘稠液体加入2L的氯仿,加热至沸腾,再有不溶物析出,过滤,滤饼用1L的氯仿洗涤,滤液减压蒸馏回收氯仿。滤饼用3L的去离子水洗涤,转移至容器中加热至沸腾,煮沸,过滤,滤饼用热去离子水洗至滤液pH为中性。滤饼用2L的无水乙醇溶解,加热至沸腾(完全溶解)用2.25L的蒸馏水强析,有浅粉色的固体析出,过滤,滤饼置于电热干燥箱内35℃干燥,即得浅粉色粉状产物146.1克,收率为28.86%。液相色谱测定含量为99.07%。 Use 4.6L of absolute ethanol to dissolve the dark green viscous reactant, white insoluble matter precipitates out, filter, at this time the filtrate is strongly acidic, adjust with 460ml of 20% (w/w) NaOH (deionized water configuration) The pH value is neutral (tested with test paper), and a large amount of insoluble matter precipitates out, which is slightly viscous. After filtering, the filtrate cools down and insoluble matter precipitates out. Filter again, and rinse the filter cake with a small amount of absolute ethanol. All filtrates were distilled under reduced pressure until no liquid dripped down to recover ethanol. After vacuum distillation, add 2L of chloroform to the viscous liquid in the bottle, heat to boiling, then insoluble matter precipitates out, filter, and wash the filter cake with 1L of chloroform, and the filtrate is distilled under reduced pressure to recover chloroform. The filter cake was washed with 3L of deionized water, transferred to a container and heated to boiling, boiled, filtered, and the filter cake was washed with hot deionized water until the pH of the filtrate was neutral. Dissolve the filter cake with 2L of absolute ethanol, heat it to boiling (completely dissolved), analyze it strongly with 2.25L of distilled water, a light pink solid precipitates out, filter it, and dry the filter cake in an electric drying oven at 35°C to obtain a light pink color The powdery product was 146.1 g, and the yield was 28.86%. The content determined by liquid chromatography is 99.07%.
实施例4: Example 4:
a.粉碎工序:将邻苯二甲酸酐和α-萘酚预先粉碎成粉末; a. Pulverization process: phthalic anhydride and α-naphthol are pulverized into powder in advance;
b.反应工序: b. Reaction process:
在1L的三口瓶中装有搅拌(搅拌速度225rpm)中,加入邻苯二甲酸酐粉末190g、α-萘酚粉末389g,投料比(mol比)为1:2.1,搅拌均匀加入甲磺酸150ml,在15℃反应9h,并在10-15℃放置62h,然后升温至40℃,搅拌下反应9h,取样测液色含量为28.18%。 Add 190g of phthalic anhydride powder and 389g of α-naphthol powder into a 1L three-neck flask with stirring (stirring speed 225rpm), and the ratio (mol ratio) is 1:2.1. Stir evenly and add 150ml of methanesulfonic acid , reacted at 15°C for 9h, and placed at 10-15°C for 62h, then raised the temperature to 40°C, reacted for 9h under stirring, and the liquid color content was 28.18% by sampling.
c.分离提纯工序: c. Separation and purification process:
用5.9L的甲醇溶解墨绿色粘稠的反应物,有白色不溶物析出,过滤,此时滤液为强酸性,用437ml的20%(w/w)的NaOH(去离子水配置)调节pH值为中性(用试纸测试),有大量的不溶物析出,稍粘稠状,过滤,滤液降温还会有不溶物析出,再次过滤,滤饼用少量甲醇冲洗。所有滤液减压蒸馏,蒸馏至无液体滴下,回收甲醇。减压蒸馏后瓶内的粘稠液体加入2L的氯仿,加热至沸腾,再有不溶物析出,过滤,滤饼用1L的氯仿洗涤,滤液减压蒸馏回收氯仿。滤饼用3L的去离子水洗涤,转移至容器中加热至沸腾,煮沸,过滤,滤饼用热去离子水洗至滤液pH为中性。滤饼用2.3L的甲醇溶解,加热至沸腾(完全溶解)用2.8L的蒸馏水强析,有浅粉色的固体析出,过滤,滤饼置于电热干燥箱内35℃干燥,即得浅粉色粉状产物142.3克,收率为28.11%。液相色谱测定含量为98.42%。 Use 5.9L of methanol to dissolve the dark green viscous reactant, white insoluble matter precipitates out, filter, the filtrate is strongly acidic at this time, adjust the pH value with 437ml of 20% (w/w) NaOH (deionized water configuration) It is neutral (tested with test paper), a large amount of insoluble matter precipitates, slightly viscous, filter, the filtrate cools down and insoluble matter precipitates out, filter again, and rinse the filter cake with a small amount of methanol. All filtrates were distilled under reduced pressure until no liquid dripped, and methanol was recovered. After vacuum distillation, add 2L of chloroform to the viscous liquid in the bottle, heat to boiling, then insoluble matter precipitates out, filter, and wash the filter cake with 1L of chloroform, and the filtrate is distilled under reduced pressure to recover chloroform. The filter cake was washed with 3L of deionized water, transferred to a container and heated to boiling, boiled, filtered, and the filter cake was washed with hot deionized water until the pH of the filtrate was neutral. Dissolve the filter cake in 2.3L of methanol, heat it to boiling (dissolve completely), analyze it strongly with 2.8L of distilled water, a light pink solid precipitates, filter it, and dry the filter cake in an electric drying oven at 35°C to obtain a light pink powder The product was 142.3 g, and the yield was 28.11%. The content determined by liquid chromatography was 98.42%.
实施例5: Example 5:
a.粉碎工序:将邻苯二甲酸酐和α-萘酚预先粉碎成粉末; a. Pulverization process: phthalic anhydride and α-naphthol are pulverized into powder in advance;
b.反应工序: b. Reaction process:
在1L的三口瓶中装有搅拌(搅拌速度225rpm)中,加入邻苯二甲酸酐粉末190g、α-萘酚粉末350g,投料比(mol比)为1:1.89,搅拌均匀加入甲磺酸150ml,在15℃反应9h,并在10-15℃放置62h,然后升温至40℃,搅拌下反应9h,取样测液色含量为29.32%。 Add 190g of phthalic anhydride powder and 350g of α-naphthol powder into a 1L three-necked flask with stirring (stirring speed 225rpm), and the ratio of feed (mol ratio) is 1:1.89. Stir evenly and add 150ml of methanesulfonic acid , reacted at 15°C for 9h, and placed at 10-15°C for 62h, then raised the temperature to 40°C, reacted for 9h under stirring, and the liquid color content was 29.32% by sampling.
c.分离提纯工序: c. Separation and purification process:
用4.6L的无水乙醇溶解墨绿色粘稠的反应物,有白色不溶物析出,过滤,此时滤液为强酸性,用437ml的20%(w/w)的NaOH(去离子水配置)调节pH值为中性(用试纸测试),有大量的不溶物析出,稍粘稠状,过滤,滤液降温还会有不溶物析出,再次过滤,滤饼用少量无水乙醇冲洗。所有滤液减压蒸馏,蒸馏至无液体滴下,回收乙醇。减压蒸馏后瓶内的粘稠液体加入3.5L的丙酮,加热至沸腾,再有不溶物析出,过滤,滤饼用1.2L的丙酮洗涤,滤液减压蒸馏回收丙酮。滤饼用3L的去离子水洗涤,转移至容器中加热至沸腾,煮沸,过滤,滤饼用热去离子水洗至滤液pH为中性。滤饼用2L的无水乙醇溶解,加热至沸腾(完全溶解)用2.25L的蒸馏水强析,有浅粉色的固体析出,过滤,滤饼置于电热干燥箱内35℃干燥,即得浅粉色粉状产物148.8克,收率为29.40%。液相色谱测定含量为98.87%。 Dissolve the dark green viscous reactant with 4.6L of absolute ethanol, white insoluble matter precipitates out, filter, at this time the filtrate is strongly acidic, adjust with 437ml of 20% (w/w) NaOH (deionized water configuration) The pH value is neutral (tested with test paper), and a large amount of insoluble matter precipitates out, which is slightly viscous. After filtering, the filtrate cools down and insoluble matter precipitates out. Filter again, and rinse the filter cake with a small amount of absolute ethanol. All filtrates were distilled under reduced pressure until no liquid dripped down to recover ethanol. Add 3.5L of acetone to the viscous liquid in the bottle after vacuum distillation, heat to boiling, then insoluble matter is precipitated, filter, the filter cake is washed with 1.2L of acetone, and the filtrate is distilled under reduced pressure to recover acetone. The filter cake was washed with 3L of deionized water, transferred to a container and heated to boiling, boiled, filtered, and the filter cake was washed with hot deionized water until the pH of the filtrate was neutral. Dissolve the filter cake with 2L of absolute ethanol, heat it to boiling (completely dissolved), analyze it strongly with 2.25L of distilled water, a light pink solid precipitates out, filter it, and dry the filter cake in an electric drying oven at 35°C to obtain a light pink color The powdery product was 148.8 g, and the yield was 29.40%. The content determined by liquid chromatography is 98.87%.
实施例6: Embodiment 6:
a.粉碎工序:将邻苯二甲酸酐和α-萘酚预先粉碎成粉末; a. Pulverization process: phthalic anhydride and α-naphthol are pulverized into powder in advance;
b.反应工序: b. Reaction process:
在1L的三口瓶中装有搅拌(搅拌速度225rpm),加入邻苯二甲酸酐粉末190g、α-萘酚粉末350g,搅拌均匀加入甲磺酸150ml,在15℃反应9h,并在10-15℃放置62h,然后升温至40℃,搅拌下反应9h,取样测液色含量为28.50%。 In a 1L three-neck flask equipped with stirring (stirring speed 225rpm), add 190g of phthalic anhydride powder and 350g of α-naphthol powder, stir evenly, add 150ml of methanesulfonic acid, react at 15°C for 9h, and in 10-15 ℃ for 62 hours, then heated to 40 ℃, reacted for 9 hours under stirring, and the liquid color content was 28.50% by sampling.
c.分离提纯工序: c. Separation and purification process:
用4.6L的无水乙醇溶解墨绿色粘稠的反应物,有白色不溶物析出,过滤,此时滤液为强酸性,用437ml的20%(w/w)的NaOH(去离子水配置)调节pH值为中性(用试纸测试),有大量的不溶物析出,稍粘稠状,过滤,滤液降温还会有不溶物析出,再次过滤,滤饼用少量无水乙醇冲洗。所有滤液减压蒸馏,蒸馏至无液体滴下,回收乙醇。减压蒸馏后瓶内的粘稠液体加入2.8L的丁酮,加热至沸腾,再有不溶物析出,过滤,滤饼用1.3L的丁酮洗涤,滤液减压蒸馏回收丁酮。滤饼用3L的去离子水洗涤,转移至容器中加热至沸腾,煮沸,过滤,滤饼用热去离子水洗至滤液pH为中性。滤饼用2L的无水乙醇溶解,加热至沸腾(完全溶解)用2.25L的蒸馏水强析,有浅粉色的固体析出,过滤,滤饼置于电热干燥箱内35℃干燥,即得浅粉色粉状产物145.1克,收率为28.67%。液相色谱测定含量为98.70%。 Dissolve the dark green viscous reactant with 4.6L of absolute ethanol, white insoluble matter precipitates out, filter, at this time the filtrate is strongly acidic, adjust with 437ml of 20% (w/w) NaOH (deionized water configuration) The pH value is neutral (tested with test paper), and a large amount of insoluble matter precipitates out, which is slightly viscous. After filtering, the filtrate cools down and insoluble matter precipitates out. Filter again, and rinse the filter cake with a small amount of absolute ethanol. All filtrates were distilled under reduced pressure until no liquid dripped down to recover ethanol. Add 2.8 L of methyl ethyl ketone to the viscous liquid in the bottle after distillation under reduced pressure, heat to boiling, then insoluble matter is precipitated, filter, the filter cake is washed with 1.3 L of methyl ethyl ketone, and the filtrate is distilled under reduced pressure to recover methyl ethyl ketone. The filter cake was washed with 3L of deionized water, transferred to a container and heated to boiling, boiled, filtered, and the filter cake was washed with hot deionized water until the pH of the filtrate was neutral. Dissolve the filter cake with 2L of absolute ethanol, heat it to boiling (completely dissolved), analyze it strongly with 2.25L of distilled water, a light pink solid precipitates out, filter it, and dry the filter cake in an electric drying oven at 35°C to obtain a light pink color The powdery product was 145.1 g, and the yield was 28.67%. The content determined by liquid chromatography is 98.70%.
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