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    • 4. 发明授权
    • Process for the production of high-purity tetrachloro-1,4-benzoquinone
    • 生产高纯度四氯丙烯-1,4-苯并噻唑酮的方法
    • US5151532A
    • 1992-09-29
    • US724499
    • 1991-06-27
    • Otto ArndtTheodor Papenfuhs
    • Otto ArndtTheodor Papenfuhs
    • C07C50/24C07C37/62C07C45/00C07C46/00C07C46/06C07C67/00
    • C07C46/00C07C37/62C07C46/06
    • A process for the preparation of high-purity tetrachloro-1,4-benzoquinone by the action of hydrogen peroxide and hydrochloric acid on hydroquinone, which comprises causing 3.8 top 4.2 times the molar quantity of 30 to 37% hydrochloric acid and 1.9 to 2.1 times the molar quantity of 50 to 35% hydrogen peroxide, to act at 5 to 50.degree. C. on 1 mole of hydroquinone in at least 12 times the molar quantity of 30 to 37% hydrochloric acid, then heating the resulting suspension, which essentially contains 2,5-dichlorohydroquinone, to 45 to 55.degree. C. and again causing to act on it, at 50 to 95.degree. C., 3.8 to 4.2 times the molar quantity of 30 to 37% hydrochloric acid and 1.9 to 2.1 times the molar quantity of 50 to 35% hydrogen peroxide, in each case based on the hydroquinone used, and finally adding to the suspension, which is now essentially composed of trichloro-1,4-benzoquinone, 1.9 to 2.1 times the molar quantity of hydrochloric acid of the said concentration range, and 0.95 to 1.05 times the molar quantity of hydrogen peroxide of the said concentration range, in each case based on the hydroquinone used, at 95 to 115.degree. C., sufficiently slowly for no chlorine to escape.
    • 一种通过过氧化氢和盐酸对氢醌的作用制备高纯度四氯-1,4-苯醌的方法,其包括使3.8倍上升4.2倍摩尔量的30至37%盐酸和1.9至2.1倍 摩尔量为50至35%的过氧化氢,以5至50℃在1摩尔氢醌中至少12倍摩尔量的30至37%盐酸作用,然后加热得到的悬浮液,其基本上含有 2,5-二氯对苯二酚,至45至55℃,并再次引起其作用,在50至95℃,摩尔量为30至37%盐酸的3.8至4.2倍,摩尔数的1.9至2.1倍 数量为50〜35%的过氧化氢,在各种情况下都是以所使用的氢醌为基准,最后加入到现在基本上由三氯-1,4-苯醌组成的悬浮液中,盐酸的摩尔量为1.9〜2.1倍 该浓度范围为0.95〜1.05倍 所述浓度范围内的摩尔量的过氧化氢,在每种情况下,基于所使用的氢醌,在95至115℃下,足够缓慢地没有氯逸出。
    • 5. 发明授权
    • Process for the production of high-purity tetrachloro-1,4-benzoquinone
    • 生产高纯度四氯丙烯-1,4-苯并噻唑酮的方法
    • US5149850A
    • 1992-09-22
    • US726625
    • 1991-06-28
    • Otto ArndtTheodor Papenfuhs
    • Otto ArndtTheodor Papenfuhs
    • C07C37/62C07C45/00C07C46/00C07C46/06C07C50/24C07C67/00
    • C07C46/00C07C37/62C07C46/06
    • A process for the production of high-purity tetrachloro-1,4-benzoquinone by the action of chlorine and hydrochloric acid on hydroquinone which comprises causing 1.9 to 2.1 times the molar quantity of gaseous chlorine to act at temperatures from 5.degree. to 15.degree. C. on 1 mol of hydroquinone in 6 to 7 times the molar quantity of 30 to 37% hydrochloric acid, then diluting the resulting suspension, essentially containing 2,5-dichlorohydroquinone, with 2 to 3 parts of water, relative to hydroquinone employed, and initially warming to a temperature from 20.degree. to 30.degree. C., subsequently introducing 1.9 to 2.1 times the molar quantity of chlorine gas in an air atmosphere while raising the temperature to 90.degree.-100.degree. C. with simultaneous dilution with 3.5 to 4.5 parts of water, relative to hydroquinone employed, and finally introducing 1 to 2 times the molar quantity of gaseous chlorine, relative to hydroquinone employed, at temperatures from 100.degree. to 115.degree. C.
    • 通过氯和盐酸对氢醌的作用生产高纯度四氯-1,4-苯醌的方法,其包括使气态氯的摩尔量的1.9至2.1倍在5至15℃的温度下起作用 在1摩尔氢醌中的摩尔量为30至37%盐酸的6至7倍,然后相对于所用氢醌将所得悬浮液(基本上含有2,5-二氯对苯二酚)稀释至2至3份水,和 最初升温至20℃至30℃,随后将空气气氛中的氯气的摩尔量引入1.9至2.1倍,同时将温度升至90℃-100℃,同时用3.5至4.5份稀释 的水,相对于所使用的氢醌,并且最终在100-115℃的温度下,相对于所用的氢醌,引入1至2倍的气态氯的摩尔量。
    • 6. 发明授权
    • Process for the preparation of 6-chloro-2,4-dinitroaniline
    • 制备6-氯-2,4-二硝基苯胺的方法
    • US4613698A
    • 1986-09-23
    • US706050
    • 1985-02-27
    • Otto ArndtTheodor Papenfuhs
    • Otto ArndtTheodor Papenfuhs
    • C07C209/74C07C67/00C07C209/00C07C211/52C07C85/24
    • C07C209/74
    • Process for the preparation of 6-chloro-2,4-dinitroaniline by chlorination of 2,4-dinitroaniline with sodium hypochlorite in water using acid, which comprises carrying out the chlorination in the presence of a mineral acid or strong organic acid at a pH value .ltoreq.0 and in the presence of a dispersing agent at temperatures of about 40.degree. to 50.degree. C. and, when the chlorination has ended, either (a) filtering the resulting acid aqueous dispersion hot and washing the filtered reaction product with hot aqueous alkali solution, or (b) initially rendering the resulting acid aqueous dispersion alkaline with aqueous alkali solution and then filtering the mixture hot and subsequently washing the filtered reaction product with hot dilute mineral acid.
    • 通过使用酸在水中使用次氯酸钠氯化2,4-二硝基苯胺来制备6-氯-2,4-二硝基苯胺的方法,其包括在无机酸或强有机酸的存在下在pH下进行氯化 在分散剂存在下,在约40℃至50℃的温度下,并且当氯化结束时,(a)将所得的酸水分散体过滤,并将过滤的反应产物用 热碱水溶液,或(b)最初将所得酸水性分散体用碱性水溶液碱化,然后热过滤混合物,随后用热稀无机酸洗涤过滤的反应产物。
    • 9. 发明授权
    • Process for the preparation of naphthostyril
    • 制备萘普生的方法
    • US4824962A
    • 1989-04-25
    • US170065
    • 1988-03-14
    • Otto ArndtTheodor Papenfuhs
    • Otto ArndtTheodor Papenfuhs
    • C07D209/92
    • C07D209/92
    • Process for the preparation of naphthostyril by dissolving 1,8-naphthalimide in an aqueous solution of lithium hydroxide and potassium hydroxide while heating at 40.degree. C. to 80.degree. C., cooling the solution obtained to 14.degree. C. and seeding it at said temperature with a maximum of 1 mol-% of sodium 1,8-naphthalimide per 1 mol of 1,8-naphthalimide used, then adding chlorine bleaching liquor at 10.degree. C. to 20.degree. C., reductively removing excess active chlorine after the reaction has taken place, adjusting the alkaline aqueous solution produced of the alkali-metal salt of the 1-aminonaphthal-ene-8-carboxylic acid formed to a pH of 2.0 by adding acid and isolating the naphthostyril which precipitates in this process.
    • 通过在40℃至80℃下加热将1,8-萘二甲酰亚胺溶解在氢氧化锂和氢氧化钾的水溶液中而制备萘未斯特林的方法,将所得溶液冷却至14℃,并将其在所述 温度,每1摩尔1,8-萘二甲酰亚胺使用1,8-萘二甲酰亚胺钠最多1摩尔%,然后在10℃至20℃下加入氯漂白液,然后还原除去过量的活性氯 发生反应,通过加入酸调节形成pH为2.0的1-氨基萘-8-羧酸的碱金属盐产生的碱性水溶液,并分离出在该过程中析出的萘并三唑。
    • 10. 发明授权
    • Process for the preparation of 2,6-dichloro-4-nitroaniline
    • 2,6-二氯-4-硝基苯胺的制备方法
    • US4605767A
    • 1986-08-12
    • US734972
    • 1985-05-16
    • Otto ArndtTheodor Papenfuhs
    • Otto ArndtTheodor Papenfuhs
    • C07C209/74C07C67/00C07C209/00C07C211/52C07C85/24C07C87/60
    • C07C209/74
    • Process for the preparation of 2,6-dichloro-4-nitroaniline by chlorination of 4-nitroaniline with chlorine bleaching liquor in water using acids, which comprises chlorinating 1 mole of 4-nitroaniline in 3-6 moles of hydrochloric acid (HCl) or nitric acid (HNO.sub.3) in the form of a dilute, aqueous acid in the presence of a dispersing agent which is stable under the reaction conditions, the chlorination initially being carried out at 5.degree. to 10.degree. C. and then at 15.degree.-20.degree. C. and, finally, after 90-95% of the 2-chloro-4-nitroaniline intermediately formed has been converted into 2,6-dichloro-4-nitroaniline, the temperature of the aqueous suspension being increased from 15.degree.-20.degree. C. to 70.degree. C., without further addition of chlorine bleaching liquor, and then by post-chlorinating, by renewed addition of chlorine bleaching liquor, at temperatures between 20.degree. and 70.degree. C., bringing the pH of the aqueous suspension to 9.0 and filtering off the 2,6-dichloro-4-nitroaniline formed and washing it with dilute mineral acid.
    • 通过使用酸在氯水中用氯漂白液氯化4-硝基苯胺的方法制备2,6-二氯-4-硝基苯胺的方法,该方法包括将1-6摩尔盐酸(HCl)中的1摩尔4-硝基苯胺氯化,或 硝酸(HNO 3)为稀酸水溶液,在分散剂存在下,在反应条件下稳定,氯化最初在5〜10℃进行,然后在15〜-20℃ ℃,最后,90-95%的中间形成的2-氯-4-硝基苯胺已经转化为2,6-二氯-4-硝基苯胺,水悬浮液的温度从15°-20 在不进一步加入氯漂白液的情况下,通过后续氯化,通过在20℃至70℃的温度下再次加入氯漂白液,使水悬浮液的pH值达到70℃ 至9.0,滤出2,6-二氯-4-硝基苯胺 d用稀释的无机酸洗涤。