CN1974559A - Skeleton nickel catalyzed 5-nitrobenzimidazole ketone reducing process for preparing 5-aminobenzimidazole ketone - Google Patents
Skeleton nickel catalyzed 5-nitrobenzimidazole ketone reducing process for preparing 5-aminobenzimidazole ketone Download PDFInfo
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- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 title claims abstract description 64
- 229910052759 nickel Inorganic materials 0.000 title claims abstract description 31
- -1 5-nitrobenzimidazole ketone Chemical class 0.000 title claims 5
- 238000004519 manufacturing process Methods 0.000 title 1
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 32
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims abstract description 27
- 238000000034 method Methods 0.000 claims abstract description 21
- 238000006243 chemical reaction Methods 0.000 claims abstract description 14
- 239000000706 filtrate Substances 0.000 claims abstract description 14
- 239000012065 filter cake Substances 0.000 claims abstract description 12
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- 238000002360 preparation method Methods 0.000 claims abstract description 5
- 230000035484 reaction time Effects 0.000 claims abstract description 5
- 238000004821 distillation Methods 0.000 claims abstract description 3
- 230000002829 reductive effect Effects 0.000 claims abstract description 3
- 238000005406 washing Methods 0.000 claims abstract description 3
- 239000008367 deionised water Substances 0.000 claims description 8
- 229910021641 deionized water Inorganic materials 0.000 claims description 8
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 7
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims description 6
- 229910052782 aluminium Inorganic materials 0.000 claims description 6
- 238000009903 catalytic hydrogenation reaction Methods 0.000 claims description 4
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims description 3
- 239000010936 titanium Substances 0.000 claims description 3
- 229910052719 titanium Inorganic materials 0.000 claims description 3
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 claims description 2
- 229910002056 binary alloy Inorganic materials 0.000 claims description 2
- 229910052804 chromium Inorganic materials 0.000 claims description 2
- 239000011651 chromium Substances 0.000 claims description 2
- 239000001257 hydrogen Substances 0.000 claims description 2
- 229910052739 hydrogen Inorganic materials 0.000 claims description 2
- 229910052742 iron Inorganic materials 0.000 claims description 2
- 239000007791 liquid phase Substances 0.000 claims description 2
- 239000002994 raw material Substances 0.000 claims description 2
- 239000002904 solvent Substances 0.000 claims description 2
- 229910002058 ternary alloy Inorganic materials 0.000 claims description 2
- 229910000809 Alumel Inorganic materials 0.000 claims 3
- 239000004411 aluminium Substances 0.000 claims 3
- CRXVBLLLPNWFBS-UHFFFAOYSA-N 4-aminobenzimidazol-2-one Chemical compound NC1=CC=CC2=NC(=O)N=C12 CRXVBLLLPNWFBS-UHFFFAOYSA-N 0.000 claims 2
- 229960000935 dehydrated alcohol Drugs 0.000 claims 2
- 229910045601 alloy Inorganic materials 0.000 claims 1
- 239000000956 alloy Substances 0.000 claims 1
- 239000012141 concentrate Substances 0.000 claims 1
- 230000006837 decompression Effects 0.000 claims 1
- 238000011026 diafiltration Methods 0.000 claims 1
- 229960004756 ethanol Drugs 0.000 claims 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 claims 1
- 238000000967 suction filtration Methods 0.000 claims 1
- 238000001291 vacuum drying Methods 0.000 claims 1
- QOMNJPSRBRDQSU-UHFFFAOYSA-N 5-aminobenzimidazol-2-one Chemical compound C1=C(N)C=CC2=NC(=O)N=C21 QOMNJPSRBRDQSU-UHFFFAOYSA-N 0.000 abstract description 21
- CLHXKSVLPCOPHR-UHFFFAOYSA-N 5-nitrobenzimidazol-2-one Chemical compound C1=C([N+](=O)[O-])C=CC2=NC(=O)N=C21 CLHXKSVLPCOPHR-UHFFFAOYSA-N 0.000 abstract description 17
- 239000003054 catalyst Substances 0.000 abstract description 12
- 229910000838 Al alloy Inorganic materials 0.000 abstract description 10
- NPXOKRUENSOPAO-UHFFFAOYSA-N Raney nickel Chemical compound [Al].[Ni] NPXOKRUENSOPAO-UHFFFAOYSA-N 0.000 abstract description 10
- 238000001914 filtration Methods 0.000 abstract description 6
- 238000003912 environmental pollution Methods 0.000 abstract description 3
- 239000000047 product Substances 0.000 abstract description 3
- 239000002699 waste material Substances 0.000 abstract description 3
- IDGUHHHQCWSQLU-UHFFFAOYSA-N ethanol;hydrate Chemical compound O.CCO IDGUHHHQCWSQLU-UHFFFAOYSA-N 0.000 abstract 1
- 238000002156 mixing Methods 0.000 abstract 1
- 238000006722 reduction reaction Methods 0.000 description 10
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 9
- 238000002844 melting Methods 0.000 description 9
- 230000008018 melting Effects 0.000 description 9
- 239000007788 liquid Substances 0.000 description 6
- 238000003756 stirring Methods 0.000 description 6
- 238000010531 catalytic reduction reaction Methods 0.000 description 3
- NWZSZGALRFJKBT-KNIFDHDWSA-N (2s)-2,6-diaminohexanoic acid;(2s)-2-hydroxybutanedioic acid Chemical compound OC(=O)[C@@H](O)CC(O)=O.NCCCC[C@H](N)C(O)=O NWZSZGALRFJKBT-KNIFDHDWSA-N 0.000 description 2
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 2
- IKDUDTNKRLTJSI-UHFFFAOYSA-N hydrazine monohydrate Substances O.NN IKDUDTNKRLTJSI-UHFFFAOYSA-N 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- CAAMSDWKXXPUJR-UHFFFAOYSA-N 3,5-dihydro-4H-imidazol-4-one Chemical compound O=C1CNC=N1 CAAMSDWKXXPUJR-UHFFFAOYSA-N 0.000 description 1
- 150000004982 aromatic amines Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 150000002431 hydrogen Chemical class 0.000 description 1
- 239000012860 organic pigment Substances 0.000 description 1
- 239000000049 pigment Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 229910001388 sodium aluminate Inorganic materials 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
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- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
本发明公开了一种以骨架镍催化还原5-硝基苯并咪唑酮制备5-氨基苯并咪唑酮的方法,属于5-氨基苯并咪唑酮制备技术。该方法过程包括:将镍铝合金加入到一定温度和浓度NaOH溶液中,反应一定时间,再用水和无水乙醇滤洗数次,得到骨架镍存入无水乙醇中备用;将骨架镍与5-硝基苯并咪唑酮以及无水乙醇按照一定质量比,加入到高压釜中,在温度为80~120℃、压力为1.0~6.0MPa,反应时间为4~15小时,取出滤液,除去催化剂后,滤液减压蒸馏浓缩,抽滤,将滤饼真空干燥得到5-氨基苯并咪唑酮。本发明的优点是工艺简单、反应操作简便,成本低、产品收率为89.0%~94.0%、纯度为97.0%~99.8%,产生的“三废”少,对环境的污染小。The invention discloses a method for preparing 5-aminobenzimidazolone by catalytically reducing 5-nitrobenzimidazolone with skeleton nickel, which belongs to the preparation technology of 5-aminobenzimidazolone. The process of the method comprises: adding nickel-aluminum alloy to a NaOH solution with a certain temperature and concentration, reacting for a certain period of time, and then filtering and washing with water and absolute ethanol several times to obtain the skeleton nickel and storing it in absolute ethanol for later use; mixing the skeleton nickel with 5 - Nitrobenzimidazolone and absolute ethanol are added into the autoclave according to a certain mass ratio, at a temperature of 80-120°C, a pressure of 1.0-6.0MPa, and a reaction time of 4-15 hours, take out the filtrate and remove the catalyst Afterwards, the filtrate was concentrated by distillation under reduced pressure, filtered with suction, and the filter cake was vacuum-dried to obtain 5-aminobenzimidazolone. The invention has the advantages of simple process, convenient reaction operation, low cost, product yield of 89.0%-94.0%, purity of 97.0%-99.8%, less "three wastes" and less environmental pollution.
Description
技术领域Technical field
本发明涉及一种骨架镍催化还原5-硝基苯并咪唑酮制备5-氨基苯并咪唑酮的方法,属于5-氨基苯并咪唑酮制备技术。The invention relates to a method for preparing 5-aminobenzimidazolone through catalytic reduction of 5-nitrobenzimidazolone by skeleton nickel, which belongs to the preparation technology of 5-aminobenzimidazolone.
背景技术 Background technique
5-氨基苯并咪唑酮是一种重要的颜料中间体,用于制备高档有机颜料系。5-氨基苯并咪唑酮通常是经5-硝基苯并咪唑酮还原而制备,主要的还原方法有铁粉还原、水合肼还原和催化加氢还原。目前工业上主要采用铁粉还原法,工艺成熟,设备投资少,铁粉价格低廉,操作简便,但是该过程中产生大量氧化铁泥,后处理比较复杂,对环境造成严重的污染;水合肼还原法,设备投资小,反应条件温和,还原效果好,可进行部分还原,不产生废气废渣,但是只适用与小批量、短线芳胺的合成,而不适用于大规模工业化生产;催化加氢还原法,反应完全,副反应少,产品的质量和收率都很高,对环境的污染少,Okujima等[Koho.JP0259572[9059.572].1990.2],采用Pd/C作为催化剂还原5-硝基苯并咪唑酮来制备5-氨基苯并咪唑酮,收率约为95%,但是该催化剂价格昂贵,循环回收比较困难,难以工业化生产。5-Aminobenzimidazolone is an important pigment intermediate used in the preparation of high-grade organic pigments. 5-aminobenzimidazolone is usually prepared by reducing 5-nitrobenzimidazolone. The main reduction methods include iron powder reduction, hydrazine hydrate reduction and catalytic hydrogenation reduction. At present, the iron powder reduction method is mainly used in industry, the process is mature, the equipment investment is small, the price of iron powder is low, and the operation is simple, but a large amount of iron oxide sludge is produced in the process, and the post-treatment is complicated, causing serious pollution to the environment; hydrazine hydrate reduction method, low equipment investment, mild reaction conditions, good reduction effect, partial reduction can be carried out, and no waste gas and waste residue are produced, but it is only suitable for the synthesis of small batches and short-term aromatic amines, not suitable for large-scale industrial production; catalytic hydrogenation reduction method, complete reaction, few side reactions, high product quality and yield, less environmental pollution, Okujima et al. The yield of 5-aminobenzimidazolone is about 95% by using imidazolone, but the catalyst is expensive, recycling is difficult, and industrial production is difficult.
发明内容Contents of Invention
本发明的目的在于提供一种骨架镍催化还原5-硝基苯并咪唑酮制备5-氨基苯并咪唑酮的方法,采用此方法所制备的5-氨基苯并咪唑酮,收率高,质量好,易于实现工业化。The purpose of the present invention is to provide a method for preparing 5-aminobenzimidazolone by catalytic reduction of 5-nitrobenzimidazolone by skeleton nickel, and the 5-aminobenzimidazolone prepared by this method has high yield and high quality. Well, easy to industrialize.
本发明是通过下述技术方案实现的,一种骨架镍催化还原5-硝基苯并咪唑酮制备5-氨基苯并咪唑酮的方法,其特征在于包括以下过程:The present invention is achieved through the following technical solutions, a method for preparing 5-aminobenzimidazolone by catalytic reduction of 5-nitrobenzimidazolone with framework nickel, characterized in that it comprises the following process:
1、骨架镍催化剂的制备:以镍铝合金为原料,所述的镍铝合金包括:二元合金,其中镍的质量分数为47%,铝的质量分数为53%;三元合金,其中镍的质量分数为46%,钛的质量分数为1~3%,其余为铝;四元合金,镍的质量分数为46%,铬的质量分数为1%,铁的质量分数为1~3%,其余为铝。将镍铝合金加入到温度为20~90℃,质量浓度为10~30%的NaOH溶液中,反应时间为1~15小时,然后用去离子水洗至洗涤液中无NaAlO2为止,再用无水乙醇滤洗数次除去水,后存入无水乙醇溶液中备用。1. Preparation of skeleton nickel catalyst: using nickel-aluminum alloy as raw material, said nickel-aluminum alloy includes: binary alloy, wherein the mass fraction of nickel is 47%, and the mass fraction of aluminum is 53%; ternary alloy, wherein nickel The mass fraction of titanium is 46%, the mass fraction of titanium is 1-3%, and the rest is aluminum; the mass fraction of nickel is 46%, the mass fraction of chromium is 1%, and the mass fraction of iron is 1-3%. , and the rest is aluminum. Add the nickel-aluminum alloy to the NaOH solution with a temperature of 20-90°C and a mass concentration of 10-30%, and the reaction time is 1-15 hours, then wash with deionized water until there is no NaAlO2 in the washing liquid, and then use no Water and ethanol were filtered and washed several times to remove water, and then stored in anhydrous ethanol solution for later use.
2、液相催化加氢还原的过程:以1g的5-硝基苯并咪唑酮为基准,以无水乙醇为溶剂,用量为5~10ml;骨架镍用量为5-硝基苯并咪唑酮的质量的3~10%,加入到高压釜中,通入氢气,反应温度为80~120℃,反应压力为1.0~6.0MPa,反应时间为4~15小时,将反应液取出,除去催化剂后,滤液减压蒸馏浓缩,抽滤,将滤饼真空干燥得到5-氨基苯并咪唑酮。2. The process of liquid-phase catalytic hydrogenation reduction: based on 1g of 5-nitrobenzimidazolone, with absolute ethanol as solvent, the dosage is 5-10ml; the dosage of skeleton nickel is 5-nitrobenzimidazolone Add 3-10% of the mass of the autoclave into the autoclave, feed hydrogen, the reaction temperature is 80-120°C, the reaction pressure is 1.0-6.0MPa, the reaction time is 4-15 hours, the reaction solution is taken out, and after removing the catalyst , the filtrate was concentrated by distillation under reduced pressure, filtered with suction, and the filter cake was vacuum-dried to obtain 5-aminobenzimidazolone.
本发明的优点是工艺简单、反应操作简便,成本低、产品收率为89.0%~94.0%、纯度为97.0%~99.8%,产生的“三废”少,对环境的污染小。The invention has the advantages of simple process, convenient reaction operation, low cost, product yield of 89.0%-94.0%, purity of 97.0%-99.8%, less "three wastes" and less environmental pollution.
具体实施方式 Detailed ways
例1将镍铝合金(二元)30g,加入到质量浓度为19%、体积为200ml的NaOH溶液,搅拌,加料温度为10~15℃,加料时间为2小时,之后升温至20~25℃,反应9小时,然后使用去离子水、无水乙醇滤洗数次,将制得的骨架镍存入无水乙醇中备用,标记为W-1-(二)型。Example 1 Add 30 g of nickel-aluminum alloy (binary) to a NaOH solution with a mass concentration of 19% and a volume of 200 ml, stir, the feeding temperature is 10-15° C., the feeding time is 2 hours, and then the temperature is raised to 20-25° C. , reacted for 9 hours, then used deionized water and absolute ethanol to filter and wash several times, and stored the obtained skeleton nickel in absolute ethanol for subsequent use, and marked it as W-1-(two) type.
取5-硝基苯并咪唑酮18g,无水乙醇80ml,W-1-(二)型骨架镍1.8g加入到高压釜,通入氢气压力至2MPa,升温至85℃,反应6小时,反应液滤除催化剂,滤液浓缩,抽滤,将滤饼于真空中干燥,得到5-氨基苯并咪唑酮14.0g,收率为93.2%,纯度为97.2%,熔点为248~251℃。Take 18g of 5-nitrobenzimidazolone, 80ml of absolute ethanol, and 1.8g of W-1-(two)-type skeleton nickel into the autoclave, feed hydrogen gas to a pressure of 2MPa, heat up to 85°C, and react for 6 hours. The catalyst was removed by liquid filtration, the filtrate was concentrated, filtered with suction, and the filter cake was dried in vacuum to obtain 14.0 g of 5-aminobenzimidazolone with a yield of 93.2%, a purity of 97.2%, and a melting point of 248-251°C.
例2将镍铝台金(二元)40g,加入到浓度为10%、体积为600ml的NaOH溶液,搅拌,加料温度为85~90℃,加料时间为1.5小时,升温至90~95℃,反应1小时,然后使用去离子水、无水乙醇滤洗数次,将制得的骨架镍存入无水乙醇中备用,标记为T-1-(二)型。Example 2 Add 40 g of nickel-aluminum alloy (binary) to a 10% NaOH solution with a volume of 600 ml, stir, the feeding temperature is 85-90° C., the feeding time is 1.5 hours, and the temperature is raised to 90-95° C. React for 1 hour, then use deionized water and absolute ethanol to filter and wash several times, store the prepared skeleton nickel in absolute ethanol for later use, and mark it as T-1-(two) type.
取5-硝基苯并咪唑酮18g,无水乙醇100ml,T-1-(二)型骨架镍1.8g加入到高压釜,通入氢气压力至3MPa,升温至85℃,反应5小时,反应液滤除催化剂,滤液浓缩,抽滤,将滤饼于真空中干燥,得到5-氨基苯并咪唑酮14.0g,收率为93.1%,纯度为98.8%,熔点为248~251℃。Take 18g of 5-nitrobenzimidazolone, 100ml of absolute ethanol, and 1.8g of T-1-(two) skeleton nickel into the autoclave, feed hydrogen gas to a pressure of 3MPa, heat up to 85°C, and react for 5 hours. The catalyst was removed by liquid filtration, the filtrate was concentrated, filtered with suction, and the filter cake was dried in vacuum to obtain 14.0 g of 5-aminobenzimidazolone with a yield of 93.1%, a purity of 98.8%, and a melting point of 248-251°C.
例3将镍铝合金(三元)30g,加入到浓度为19%、体积为200ml的NaOH溶液,搅拌,加料温度为10~15℃,加料时间为2小时,升温至20~25℃,反应9小时,然后使用去离子水、无水乙醇滤洗数次,将制得的骨架镍存入无水乙醇中备用,标记为W-1-(三)型。Example 3 Add 30 g of nickel-aluminum alloy (ternary) to a NaOH solution with a concentration of 19% and a volume of 200 ml, stir, the feeding temperature is 10-15° C., the feeding time is 2 hours, and the temperature is raised to 20-25° C., and the reaction After 9 hours, use deionized water and absolute ethanol to filter and wash several times, and store the obtained skeleton nickel in absolute ethanol for later use, and mark it as W-1-(III) type.
取5-硝基苯并咪唑酮18g,无水乙醇120ml,W-1-(三)型骨架镍1.5g加入到高压釜,通入氢气压力至4MPa,升温至85℃,反应7小时,反应液滤除催化剂,滤液浓缩,抽滤,将滤饼于真空中干燥,得到5-氨基苯并咪唑酮13.9g,收率为92.5%,纯度为98.8%,熔点为249~251℃。Take 18g of 5-nitrobenzimidazolone, 120ml of absolute ethanol, and 1.5g of W-1-(three)-type skeleton nickel into the autoclave, feed hydrogen gas to a pressure of 4MPa, heat up to 85°C, and react for 7 hours. The catalyst was removed by liquid filtration, the filtrate was concentrated, filtered with suction, and the filter cake was dried in vacuum to obtain 13.9 g of 5-aminobenzimidazolone with a yield of 92.5%, a purity of 98.8%, and a melting point of 249-251°C.
例4将镍铝合金(三元)40g,加入到浓度为10%、体积为600ml的NaOH溶液,搅拌,加料温度为85~90℃,加料时间为1.5小时,升温至90~95℃,反应1小时,然后使用去离子水、无水乙醇滤洗数次,将制得的骨架镍存入无水乙醇中备用,标记为T-1-(三)型。Example 4 Add 40 g of nickel-aluminum alloy (ternary) to a NaOH solution with a concentration of 10% and a volume of 600 ml, stir, the feeding temperature is 85 to 90° C., the feeding time is 1.5 hours, and the temperature is raised to 90 to 95° C., and the reaction After 1 hour, filter and wash several times with deionized water and absolute ethanol, and store the obtained skeleton nickel in absolute ethanol for later use, and mark it as T-1-(three) type.
取5-硝基苯并咪唑酮18g,无水乙醇120ml,T-1-(三)型骨架镍0.9g加入到高压釜,通入氢气压力至2MPa,升温至90℃,反应10小时,反应液除去催化剂,滤液浓缩,抽滤,将滤饼于真空中干燥,得到5-氨基苯并咪唑酮13.7g,收率为91.6%,纯度为99.1%,熔点为249~251℃。Take 18g of 5-nitrobenzimidazolone, 120ml of absolute ethanol, and 0.9g of T-1-(three)-type skeleton nickel into the autoclave, feed hydrogen gas to a pressure of 2MPa, heat up to 90°C, and react for 10 hours. The catalyst was removed from the filtrate, the filtrate was concentrated, filtered with suction, and the filter cake was dried in vacuum to obtain 13.7 g of 5-aminobenzimidazolone with a yield of 91.6%, a purity of 99.1%, and a melting point of 249-251°C.
取5-硝基苯并咪唑酮25g,无水乙醇200ml,T-1-(三)型骨架镍1.0g加入到高压釜,通入氢气压力至3MPa,升温至90℃,反应10小时,反应液滤除催化剂,滤液浓缩,抽滤,将滤饼于真空中干燥,得到5-氨基苯并咪唑酮19.4g,收率为93.3%,纯度为99.0%,熔点为250~253℃。Take 25g of 5-nitrobenzimidazolone, 200ml of absolute ethanol, and 1.0g of T-1-(three)-type framework nickel into the autoclave, feed hydrogen gas to a pressure of 3MPa, heat up to 90°C, and react for 10 hours. The catalyst was removed by liquid filtration, the filtrate was concentrated, filtered with suction, and the filter cake was dried in vacuum to obtain 19.4 g of 5-aminobenzimidazolone with a yield of 93.3%, a purity of 99.0%, and a melting point of 250-253°C.
例5将镍铝合金(四元)30g,加入到浓度为19%,体积为200ml的NaOH溶液,搅拌,加料温度为10~15℃,加料时间为2小时,升温至20~25℃,反应9小时,然后使用去离子水、无水乙醇滤洗数次,将制得的骨架镍存入无水乙醇中备用,标记为W-1-(四)型。Example 5 Add 30 g of nickel-aluminum alloy (quaternary) to a concentration of 19%, and a volume of 200 ml of NaOH solution, stir, the feeding temperature is 10-15 ° C, the feeding time is 2 hours, the temperature is raised to 20-25 ° C, and the reaction After 9 hours, use deionized water and absolute ethanol to filter and wash several times, and store the prepared skeleton nickel in absolute ethanol for subsequent use, and mark it as W-1-(four) type.
取5-硝基苯并咪唑酮18g,无水乙醇120ml,W-1-(四)型骨架镍0.9g加入到高压釜,通入氢气压力至2MPa,升温至90℃,反应7小时,反应液滤除催化剂,滤液浓缩,抽滤,将滤饼于真空中干燥,得到5-氨基苯并咪唑酮13.5g,收率为90.1%,纯度为98.7%,熔点为248~251℃。Take 18g of 5-nitrobenzimidazolone, 120ml of absolute ethanol, and 0.9g of W-1-(four)-type skeleton nickel into the autoclave, feed hydrogen gas to a pressure of 2MPa, heat up to 90°C, and react for 7 hours. The catalyst was removed by liquid filtration, the filtrate was concentrated, filtered with suction, and the filter cake was dried in vacuum to obtain 13.5 g of 5-aminobenzimidazolone with a yield of 90.1%, a purity of 98.7%, and a melting point of 248-251°C.
例6将镍铝合金(四元)40g,加入到浓度为10%,体积为600ml的NaOH溶液,搅拌,加料温度为85~90℃,加料时间为1.5小时,升温至90~95℃,反应1小时,然后使用去离子水、无水乙醇滤洗数次,将制得的骨架镍存入无水乙醇中备用,标记为T-1-(四)型。Example 6 Add 40 g of nickel-aluminum alloy (quaternary) to a concentration of 10% and a volume of 600 ml of NaOH solution, stir, the feeding temperature is 85 to 90° C., the feeding time is 1.5 hours, the temperature is raised to 90 to 95° C., and the reaction After 1 hour, use deionized water and absolute ethanol to filter and wash several times, and store the obtained skeleton nickel in absolute ethanol for later use, and mark it as T-1-(four) type.
取5-硝基苯并咪唑酮18g,无水乙醇120ml,T-1-(四)骨架镍0.7g加入到高压釜,通入氢气压力至3MPa,升温至90℃,反应12小时,反应液滤除催化剂,滤液浓缩,抽滤,将滤饼于真空中干燥,得到5-氨基苯并咪唑酮13.7g,收率为91.3%,纯度为99.3%,熔点为250~253℃。Take 18g of 5-nitrobenzimidazolone, 120ml of absolute ethanol, and 0.7g of T-1-(tetra)skeleton nickel into the autoclave, feed hydrogen gas to a pressure of 3MPa, heat up to 90°C, and react for 12 hours. The catalyst was filtered off, the filtrate was concentrated, filtered with suction, and the filter cake was dried in vacuum to obtain 13.7 g of 5-aminobenzimidazolone with a yield of 91.3%, a purity of 99.3%, and a melting point of 250-253°C.
取5-硝基苯并咪唑酮25g,无水乙醇200ml,T-1-(四)骨架镍1.0g加入到高压釜,通入氢气压力至2MPa,升温至90℃,反应14小时,反应液除去催化剂,滤液浓缩,抽滤,将滤饼于真空中干燥,得到5-氨基苯并咪唑酮19.3g,收率为92.8%,纯度为99.0%,熔点为250~253℃。Take 25g of 5-nitrobenzimidazolone, 200ml of absolute ethanol, and 1.0g of T-1-(tetra)skeleton nickel into the autoclave, feed hydrogen gas to a pressure of 2MPa, heat up to 90°C, and react for 14 hours. The catalyst was removed, the filtrate was concentrated, filtered with suction, and the filter cake was dried in vacuum to obtain 19.3 g of 5-aminobenzimidazolone with a yield of 92.8%, a purity of 99.0%, and a melting point of 250-253°C.
取5-硝基苯并咪唑酮30g,无水乙醇250ml,T-1-(四)骨架镍0.9g加入到高压釜,通入氢气压力至2MPa,升温至95℃,反应13小时,反应液滤除催化剂,滤液浓缩,抽滤,将滤饼于真空中干燥,得到5-氨基苯并咪唑酮23.4g,收率为93.5%,纯度为99.4%,熔点为249~252℃。Take 30g of 5-nitrobenzimidazolone, 250ml of absolute ethanol, and 0.9g of T-1-(tetra)skeleton nickel into the autoclave, feed hydrogen gas to a pressure of 2MPa, heat up to 95°C, and react for 13 hours. The catalyst was filtered off, the filtrate was concentrated, filtered with suction, and the filter cake was dried in vacuum to obtain 23.4 g of 5-aminobenzimidazolone with a yield of 93.5%, a purity of 99.4%, and a melting point of 249-252°C.
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CN102527393A (en) * | 2011-12-23 | 2012-07-04 | 中国石油化工股份有限公司 | Modification method for raney nickel catalyst for p-chloronitrobenzene hydrogenation |
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CN102527393A (en) * | 2011-12-23 | 2012-07-04 | 中国石油化工股份有限公司 | Modification method for raney nickel catalyst for p-chloronitrobenzene hydrogenation |
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CN104557727A (en) * | 2013-10-28 | 2015-04-29 | 中国石油化工股份有限公司 | Method for preparing 5-aminobenzimidazole ketone |
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CN104130194A (en) * | 2014-08-12 | 2014-11-05 | 南通醋酸化工股份有限公司 | Synthesis method of 5-amino benzimidazolone |
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CN109225255A (en) * | 2018-09-19 | 2019-01-18 | 东营市天正化工有限公司 | A kind of novel load Raney nickel and its method for preparing 5-Amino-2-benzimidazolinone |
CN113149911A (en) * | 2021-04-13 | 2021-07-23 | 东营市天正化工有限公司 | Preparation method of high-purity 5-aminobenzimidazole ketone |
CN119528815A (en) * | 2025-01-22 | 2025-02-28 | 东营市天正化工有限公司 | A method for preparing 5-nitrobenzimidazolone by continuous nitration |
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