[go: up one dir, main page]

CN102516817B - Method for preparing indigo white solution - Google Patents

Method for preparing indigo white solution Download PDF

Info

Publication number
CN102516817B
CN102516817B CN2011104462449A CN201110446244A CN102516817B CN 102516817 B CN102516817 B CN 102516817B CN 2011104462449 A CN2011104462449 A CN 2011104462449A CN 201110446244 A CN201110446244 A CN 201110446244A CN 102516817 B CN102516817 B CN 102516817B
Authority
CN
China
Prior art keywords
reactor
indigo
reaction
pressure
hydrogen
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN2011104462449A
Other languages
Chinese (zh)
Other versions
CN102516817A (en
Inventor
高维娟
张小华
张文英
陈洪利
谷俊刚
陈瑞珍
李璟
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Hebei Chemical and Pharmaceutical College
Original Assignee
Hebei Chemical and Pharmaceutical College
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Hebei Chemical and Pharmaceutical College filed Critical Hebei Chemical and Pharmaceutical College
Priority to CN2011104462449A priority Critical patent/CN102516817B/en
Publication of CN102516817A publication Critical patent/CN102516817A/en
Application granted granted Critical
Publication of CN102516817B publication Critical patent/CN102516817B/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Indole Compounds (AREA)

Abstract

本发明公开了一种靛白溶液的环保制备方法,所述制备方法包括以下步骤,步骤1、取未经水洗和酸化处理的氧化后的靛蓝悬浊液,将上述悬浊液和活化后的雷尼镍催化剂、氢氧化钠加入高压反应釜中,先用氮气置换反应釜内的空气,再充入氢气,调节体系的温度和压力,进行催化加氢反应;步骤2、继续通入氢气,升高体系的温度和压力,进行进一步的加氢反应;步骤3、停止反应,加入稳定剂,采用过滤的方法除去催化剂,得到靛白溶液。本发明解决了现有技术中存在的污染环境、反应压力高、温度高、催化剂用量大的缺点,并具有较高的收率。 The invention discloses an environmentally friendly preparation method of indigo white solution. The preparation method comprises the following steps. Step 1. Take the oxidized indigo suspension that has not been washed and acidified, and mix the above suspension with the activated indigo Add the Raney nickel catalyst and sodium hydroxide into the high-pressure reactor, first replace the air in the reactor with nitrogen, then fill in hydrogen, adjust the temperature and pressure of the system, and carry out catalytic hydrogenation reaction; step 2, continue to feed hydrogen, Elevate the temperature and pressure of the system to carry out further hydrogenation reaction; step 3, stop the reaction, add a stabilizer, remove the catalyst by filtering to obtain an indigo white solution. The invention solves the disadvantages of polluted environment, high reaction pressure, high temperature and large amount of catalyst used in the prior art, and has higher yield.

Description

靛白溶液的环保制备方法Environment-friendly preparation method of indigo white solution

技术领域 technical field

本发明属于靛白制备范畴,具体涉及催化加氢制备靛白的方法。 The invention belongs to the category of indigo preparation, and in particular relates to a method for preparing indigo by catalytic hydrogenation.

背景技术 Background technique

靛蓝是一种常见的还原染料,用于染色纤维素纺织品材料,尤其是用于蓝色牛仔布制品的染色。靛蓝本身不溶于水,使用时必须经还原处理使其转化成具有纤维亲和性的水溶性隐色体靛白,附着在待染材料上之后,再经空气氧化成水不溶性的靛蓝从而显色。传统的染色工艺过程中,靛蓝的还原是在染浴上游一容器内的碱性介质中进行,采用无机还原剂,例如保险粉和硫脲氧化物,也可以采用羟基丙酮等有机还原剂。用上述还原剂来还原靛蓝的缺点是,当采用保险粉时,染厂废水中含有高浓度硫酸盐;当采用羟基丙酮时,废水中含有高浓度的耗氧物质。这种还原方式,废水处理成本高昂,对环境存在不良影响。 Indigo is a common vat dye used to dye cellulosic textile materials, especially blue denim. Indigo itself is insoluble in water. It must be converted into a water-soluble leuco indigo with fiber affinity when used. After being attached to the material to be dyed, it is oxidized into water-insoluble indigo by air to develop color. . In the traditional dyeing process, the reduction of indigo is carried out in an alkaline medium in a container upstream of the dye bath, using inorganic reducing agents, such as hydrosulfite and thiourea oxide, or organic reducing agents such as hydroxyacetone. The disadvantage of reducing indigo with the above-mentioned reducing agents is that when sodium hydrosulfite is used, the dyehouse wastewater contains high concentrations of sulfates; when hydroxyacetone is used, the wastewater contains high concentrations of oxygen-consuming substances. In this reduction method, the cost of wastewater treatment is high and has adverse effects on the environment.

WO-A-94/23114公开了一种环保的靛蓝还原方法,采用催化还原的方式,由靛蓝悬浮液制备得到苛性靛白水溶液,相对与常规的染色法方法,可以降低硫酸盐或有机物在废水中的含量。 WO-A-94/23114 discloses an environmentally friendly indigo reduction method, which uses catalytic reduction to prepare caustic indigo white solution from indigo suspension. Compared with conventional dyeing methods, it can reduce sulfate or organic matter in wastewater. content in.

现有的催化还原制备靛蓝隐色体靛白的方式需要预先将靛蓝水洗至中性后再加入质量浓度为10~15%的盐酸进行酸化,再水洗至中性后进行加氢反应,靛蓝的水洗和酸化过程产生大量的废液,对环境存在不良影响,目前缺少一种无需对原料进行水洗和酸化处理、反应温度低、压力低、催化剂用量少的环保型靛白制备方法。 The existing method of catalytic reduction to prepare indigo leuco indigo white needs to wash indigo to neutrality in advance, then add hydrochloric acid with a mass concentration of 10-15% for acidification, and then wash to neutrality before hydrogenation reaction. The washing and acidification process produces a large amount of waste liquid, which has adverse effects on the environment. At present, there is a lack of an environmentally friendly preparation method for indigo white that does not require washing and acidification of raw materials, low reaction temperature, low pressure, and less catalyst consumption.

发明内容 Contents of the invention

本发明要解决的技术问题是提供一种反应收率高、压力低、温度低、催化剂用量少的靛白溶液制备方法,该方法能够避免原料的水洗和酸化工艺,具有节能环保的特点。 The technical problem to be solved by the present invention is to provide a method for preparing indigo white solution with high reaction yield, low pressure, low temperature and less catalyst consumption. The method can avoid the washing and acidification process of raw materials, and has the characteristics of energy saving and environmental protection.

为解决上述技术问题,本发明所采用的技术方案是: In order to solve the problems of the technologies described above, the technical solution adopted in the present invention is:

靛白溶液的环保制备方法,由以下以下步骤组成, The environmental protection preparation method of indigo white solution is made up of following following steps,

步骤1:取未经水洗和酸化处理的氧化后的靛蓝悬浊液,将上述悬浊液和雷尼镍催化剂、氢氧化钠加入高压反应釜中,先用氮气置换反应釜内的空气,再充入0.1~1MPa的氢气,密闭反应釜,升温到80~110℃,继续充入氢气至反应釜内的压力为1.5~3MPa,反应2.5~3.5h,反应过程中,当反应釜内的压力下降值大于0.5 MPa时,补充氢气恢复反应釜内的压力; Step 1: Take the oxidized indigo suspension that has not been washed and acidified, add the above suspension, Raney nickel catalyst, and sodium hydroxide into a high-pressure reactor, first replace the air in the reactor with nitrogen, and then Fill the hydrogen gas of 0.1~1MPa, seal the reaction kettle, raise the temperature to 80~110℃, continue to fill the hydrogen gas until the pressure in the reaction kettle is 1.5~3MPa, and react for 2.5~3.5h. During the reaction, when the pressure in the reaction kettle When the drop value is greater than 0.5 MPa, supplement hydrogen to restore the pressure in the reactor;

反应物料的配比为: The proportioning of reaction materials is:

固体靛蓝∶雷尼镍质量份数比=1∶0.03~0.15; Solid indigo:Raney nickel mass fraction ratio=1:0.03~0.15;

固体靛蓝∶氢氧化钠质量份数比=1∶0.075~0.35; Solid indigo: sodium hydroxide mass fraction ratio = 1: 0.075~0.35;

固体靛蓝∶水=1∶0.5~3; Solid indigo: water = 1: 0.5~3;

步骤2:步骤1中的反应结束后,将反应釜升温至115~145℃,继续充入氢气至反应釜内的压力为3.5~5.5MPa,反应0.5~1h,反应过程中,当反应釜内的压力下降值大于0.5 MPa时,补充氢气恢复反应釜内的压力; Step 2: After the reaction in step 1 is completed, raise the temperature of the reactor to 115~145°C, continue to fill in hydrogen until the pressure in the reactor is 3.5~5.5MPa, and react for 0.5~1h. During the reaction, when the reactor When the pressure drop value is greater than 0.5 MPa, supplement hydrogen to restore the pressure in the reactor;

步骤3:步骤2中的反应结束后,待反应釜冷却,用氮气置换反应釜内的氢气,将稳定剂加入反应釜内,采用过滤的方法除去雷尼镍,得到靛白溶液。 Step 3: After the reaction in step 2 is completed, the reactor is cooled, the hydrogen in the reactor is replaced with nitrogen, the stabilizer is added into the reactor, and the Raney nickel is removed by filtration to obtain an indigo solution.

本发明所述稳定剂为双亚磷酸酯类抗氧剂。 The stabilizer of the present invention is a bisphosphite antioxidant.

本发明的改进在于:步骤1中的反应温度为105℃,反应釜内的压力为2.5MPa,所述步骤2中的反应温度为130℃,反应釜内的压力为4.5 MPa;所述反应物料的配比为: The improvement of the present invention is: the reaction temperature in step 1 is 105 DEG C, the pressure in the reactor is 2.5MPa, the reaction temperature in the step 2 is 130 DEG C, and the pressure in the reactor is 4.5 MPa; The ratio is:

固体靛蓝∶雷尼镍质量份数比=1∶0.1; Solid indigo:Raney nickel mass fraction ratio=1:0.1;

固体靛蓝∶氢氧化钠质量份数比=1∶0.2; Solid indigo: sodium hydroxide mass fraction ratio = 1: 0.2;

固体靛蓝∶水=1∶1。 Solid indigo: water = 1:1.

由于采用了上述技术方案,本发明所取得技术进步为: Owing to having adopted above-mentioned technical scheme, the technological progress that the present invention obtains is:

本发明的靛白制备方法中,首先在较低的反应温度80~110℃和压力1.5~3MPa下,对靛蓝悬浊液进行催化加氢处理,然后再升高体系的反应温度115~145℃和压力3.5~5.5MPa,进行对靛蓝进行进一步的加氢处理。在较低的反应温度和压力进行加氢反应时,在充分发挥催化剂的催化作用的同时,减少副反应的发生,反应进行5~8h后,由于产物靛白的浓度升高,通过在较短的时间内2~3h提高反应体系的温度和压力促进反应进行,提高靛白的产率。由于采用的上述制备法,本发明能够在不对原料靛蓝进行水洗和酸化处理的条件下,反应得到收率高、副产物少的靛白溶液,避免了水洗和酸化工艺产生的废水对环境的不良影响。 In the preparation method of indigo white of the present invention, firstly, the indigo suspension is subjected to catalytic hydrogenation treatment at a lower reaction temperature of 80-110°C and a pressure of 1.5-3 MPa, and then the reaction temperature of the system is raised to 115-145°C And pressure 3.5~5.5MPa, carry out further hydrogenation treatment to indigo. When the hydrogenation reaction is carried out at a lower reaction temperature and pressure, the catalytic effect of the catalyst can be fully exerted, and the occurrence of side reactions can be reduced. Increase the temperature and pressure of the reaction system for 2~3 hours to promote the reaction and increase the yield of indigo white. Due to the above-mentioned preparation method adopted, the present invention can react to obtain an indigo white solution with high yield and few by-products without washing and acidifying the raw material indigo, thereby avoiding the adverse effects of the wastewater produced by washing and acidifying processes on the environment Influence.

1质量份的原料固体靛蓝与1质量份的水混合后得到的悬浊液中,加入0.1质量份的雷尼镍催化剂和0.2质量份的氢氧化钠,在110℃,2.5MPa的条件下反应5~8小时可以使靛白的产率达到85~90%;再将上述反应液在130℃,4.5 MPa的条件下反应2~3h,可以使靛白的产率达到95~98%,采用上述条件参数,能够有效地降低副反应地发生,得到的产物纯度高,溶解性好。 Add 0.1 mass part of Raney nickel catalyst and 0.2 mass part of sodium hydroxide to the suspension obtained by mixing 1 mass part of raw material solid indigo with 1 mass part of water, and react under the conditions of 110 ° C and 2.5 MPa The yield of indigo white can reach 85~90% in 5~8 hours; then react the above reaction solution at 130°C and 4.5 MPa for 2~3 hours, and the yield of indigo white can reach 95~98%. The above condition parameters can effectively reduce the occurrence of side reactions, and the obtained product has high purity and good solubility.

具体实施方式 Detailed ways

下面结合具体实施例对本发明作进一步详细说明。 The present invention will be described in further detail below in conjunction with specific embodiments.

实施例1 Example 1

本实施例的靛蓝原料为氧化法得到的,不经水洗和酸化处理的靛蓝固体。按照以下步骤制备靛白溶液, The indigo raw material of this embodiment is the indigo solid obtained by the oxidation method without washing and acidification treatment. Prepare indigo white solution as follows,

步骤1:进行高压反应釜的检漏,将高压反应釜洗净烘干封闭好,充入0.8MP的氮气,保持30min,压力如没有明显的下降说明反应釜密闭性良好,进行后续操作;称取一定量的原料靛蓝固体,分散在水中,配制成悬浊液。将此悬浊液、雷尼镍催化剂、氢氧化钠加入反应釜内,其中,各组分的质量比为靛蓝固体:雷尼镍:氢氧化钠:水=1∶0.15∶0.35∶3。密闭好反应釜,然后使用氮气置换反应釜中的空气3次,再改用氢气置换3次,使反应釜内的氢气压力为0.5MPa,密闭反应釜,升温到80℃,充入氢气至反应釜内的压力为1.5MPa,反应2.5h,反应过程中,当反应釜内的压力下降值大于0.5 MPa时,补充氢气恢复反应釜内的压力。 Step 1: Carry out leak detection of the autoclave, clean, dry and seal the autoclave, fill it with 0.8MP nitrogen, and keep it for 30 minutes. If the pressure does not drop significantly, it means that the autoclave is well sealed, and proceed to follow-up operations; Take a certain amount of solid indigo raw material, disperse it in water, and prepare it as a suspension. Add the suspension, Raney nickel catalyst, and sodium hydroxide into the reaction kettle, wherein the mass ratio of each component is indigo solid:Raney nickel:sodium hydroxide:water=1:0.15:0.35:3. Seal the reactor well, then use nitrogen to replace the air in the reactor for 3 times, and then replace it with hydrogen for 3 times, so that the hydrogen pressure in the reactor is 0.5MPa, seal the reactor, raise the temperature to 80°C, and fill it with hydrogen until the reaction The pressure in the kettle is 1.5MPa, and the reaction is 2.5h. During the reaction, when the pressure drop in the reactor is greater than 0.5MPa, hydrogen is added to restore the pressure in the reactor.

步骤2:步骤1中的反应结束后,将反应釜升温至115℃,继续充入氢气至反应釜内的压力为3.5MPa,反应0.5h,反应过程中,当反应釜内的压力下降值大于0.5 MPa时,补充氢气恢复反应釜内的压力。 Step 2: After the reaction in step 1 is over, raise the temperature of the reactor to 115°C, continue to fill the reactor with hydrogen until the pressure in the reactor is 3.5MPa, and react for 0.5h. During the reaction, when the pressure drop in the reactor is greater than At 0.5 MPa, add hydrogen to restore the pressure in the reactor.

步骤3:步骤2中的反应结束后,将反应体系内的温度降置室温,泄掉反应釜内的氢气,再用氮气置换3分钟,将双亚磷酸酯类抗氧剂626加入反应釜内,保证反应液在接触空气的情况下不易被氧化变质。然后滤去雷尼镍,得靛白溶液。其中,抗氧剂626化学名称为双(2,4-二叔丁基苯基)季戊四醇二亚磷酸酯,购自宁波金海雅宝化工有限公司。 Step 3: After the reaction in step 2 is completed, lower the temperature in the reaction system to room temperature, vent the hydrogen in the reactor, and then replace it with nitrogen for 3 minutes, and add the bisphosphite antioxidant 626 into the reactor , to ensure that the reaction solution is not easily oxidized and deteriorated when exposed to air. Then filter out Raney nickel to obtain indigo white solution. Among them, the chemical name of antioxidant 626 is bis(2,4-di-tert-butylphenyl)pentaerythritol diphosphite, which was purchased from Ningbo Jinhai Yabao Chemical Co., Ltd.

计算上述方法制备的靛白溶液的收率,结果为95.3%。 Calculate the yield of the indigo white solution prepared by the above method, and the result is 95.3%.

实施例2 Example 2

本实施例的靛白溶液制备方法与实施例1的区别为: The difference between the indigo white solution preparation method of the present embodiment and embodiment 1 is:

步骤1中各组分的质量比为靛蓝固体:雷尼镍:氢氧化钠:水=1∶0.1∶0.2∶1,反应温度为105℃,反应釜压力为2.5MPa,时间为3h; The mass ratio of each component in step 1 is indigo solid:Raney nickel:sodium hydroxide:water=1:0.1:0.2:1, the reaction temperature is 105°C, the reactor pressure is 2.5MPa, and the time is 3h;

步骤2中反应温度为130℃,反应釜压力为4.5 MPa,时间为0.8h。 In step 2, the reaction temperature is 130°C, the reactor pressure is 4.5 MPa, and the time is 0.8h.

所得靛白溶液的收率为98.5%。 The yield of gained indigo solution is 98.5%.

实施例3 Example 3

本实施例的靛白溶液制备方法与实施例1的区别为: The difference between the indigo white solution preparation method of the present embodiment and embodiment 1 is:

步骤1中各组分的质量比为靛蓝固体:雷尼镍:氢氧化钠:水=1∶0.03∶0..075∶0.5,反应温度为110℃,反应釜压力为3 MPa,时间为3.5h; The mass ratio of each component in step 1 is indigo solid: Raney nickel: sodium hydroxide: water=1: 0.03: 0..075: 0.5, the reaction temperature is 110°C, the reactor pressure is 3 MPa, and the time is 3.5 h;

步骤2中反应温度为145℃,反应釜压力为5.5MPa,时间为1h。 In step 2, the reaction temperature is 145° C., the pressure of the reactor is 5.5 MPa, and the time is 1 h.

所得靛白溶液的收率为95.7%。 The yield of gained indigo solution is 95.7%.

实施例4 Example 4

本实施例的靛白溶液制备方法与实施例1的区别为: The difference between the indigo white solution preparation method of the present embodiment and embodiment 1 is:

步骤1中各组分的质量比为靛蓝固体:雷尼镍:氢氧化钠:水=1∶0.12∶0.22∶1.5,反应温度为110℃,反应釜压力为3 MPa,时间为2.8h; The mass ratio of each component in step 1 is indigo solid: Raney nickel: sodium hydroxide: water=1: 0.12: 0.22: 1.5, the reaction temperature is 110°C, the reactor pressure is 3 MPa, and the time is 2.8h;

步骤2中反应温度为135℃,反应釜压力为4MPa,时间为0.6h。 In step 2, the reaction temperature is 135° C., the pressure of the reactor is 4 MPa, and the time is 0.6 h.

所得靛白溶液的收率为96.3%。 The yield of gained indigo solution is 96.3%.

Claims (3)

1. the environment-friendly preparation method of leucoindigo solutions, is characterized in that being comprised of following steps,
Step 1: get without the indigo suspension liquid after the oxidation of washing and acidification, above-mentioned suspension liquid and Raney's nickel catalyst, sodium hydroxide are added in autoclave, first use the air in the nitrogen replacement reactor, use again hydrogen exchange instead 3 times, be filled with again the hydrogen of 0.1~1MPa, closed reactor, be warmed up to 80~110 ℃, continuing to be filled with hydrogen to the pressure in reactor is 1.5~3MPa, reaction 2.5~3.5h, in reaction process, when the pressure drop value in reactor is greater than 0.5MPa, hydrogen make-up is recovered the pressure in reactor;
The proportioning of reaction mass is:
Solid is indigo: Raney's nickel ratio of quality and the number of copies=1: 0.03~0.15;
Solid is indigo: sodium hydroxide ratio of quality and the number of copies=1: 0.075~0.35;
Solid is indigo: water=1: 0.5~3;
Step 2: after the reaction in step 1 finishes, reactor is warming up to 115~145 ℃, continuing to be filled with hydrogen to the pressure in reactor is 3.5~5.5MPa, reaction 0.5~1h, in reaction process, when the pressure drop value in reactor is greater than 0.5MPa, hydrogen make-up is recovered the pressure in reactor;
Step 3: after the reaction in step 2 finishes, the question response still is cooling, and the hydrogen with in the nitrogen replacement reactor, add stablizer in reactor, adopts the method for filtering to remove Raney's nickel, obtains leucoindigo solutions.
2. the environment-friendly preparation method of leucoindigo solutions according to claim 1, it is characterized in that: described stablizer is bisphosphite anti-oxidant.
3. the environment-friendly preparation method of leucoindigo solutions according to claim 2, it is characterized in that: the temperature of reaction in step 1 is 105 ℃, and the pressure in reactor is 2.5MPa, and the temperature of reaction in described step 2 is 130 ℃, and the pressure in reactor is 4.5MPa; The proportioning of described reaction mass is:
Solid is indigo: Raney's nickel ratio of quality and the number of copies=1: 0.1;
Solid is indigo: sodium hydroxide ratio of quality and the number of copies=1: 0.2;
Solid is indigo: water=1: 1.
CN2011104462449A 2011-12-28 2011-12-28 Method for preparing indigo white solution Expired - Fee Related CN102516817B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN2011104462449A CN102516817B (en) 2011-12-28 2011-12-28 Method for preparing indigo white solution

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN2011104462449A CN102516817B (en) 2011-12-28 2011-12-28 Method for preparing indigo white solution

Publications (2)

Publication Number Publication Date
CN102516817A CN102516817A (en) 2012-06-27
CN102516817B true CN102516817B (en) 2013-12-11

Family

ID=46287902

Family Applications (1)

Application Number Title Priority Date Filing Date
CN2011104462449A Expired - Fee Related CN102516817B (en) 2011-12-28 2011-12-28 Method for preparing indigo white solution

Country Status (1)

Country Link
CN (1) CN102516817B (en)

Families Citing this family (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105566949B (en) * 2016-02-04 2017-07-07 浙江长征化工有限公司 A kind of environment-friendly preparation method of sulfur dye solution
CN106975483A (en) * 2017-05-05 2017-07-25 南京工业大学 Catalyst for synthesizing hydrogenated indigo through indigo hydrogenation, and preparation method and application thereof
CN110016816A (en) * 2019-03-13 2019-07-16 广东前进牛仔布有限公司 A kind of indigo dyeing method
CN110423492B (en) * 2019-08-26 2021-04-06 约克夏(浙江)染化有限公司 Process for the preparation of a leucoindigo salt solution and process for the continuous production of a leucoindigo salt solution
JP2023018161A (en) * 2019-12-17 2023-02-08 岩谷産業株式会社 Method for producing dyed fiber article and method of producing dye solution
CN114644585B (en) * 2020-12-18 2023-10-27 沈阳化工研究院有限公司 Method for preparing indigo by fluidized bed catalytic hydrogenation
WO2024083795A1 (en) * 2022-10-17 2024-04-25 Archroma Ip Gmbh Leucoindigo salt mixture from non-synthetic sources for dyeing processes
CN116556088B (en) * 2023-04-07 2025-11-25 广东职业技术学院 A method for dyeing cotton thread with indigo
CN118925746B (en) * 2024-07-22 2025-06-27 重庆市化工研究院有限公司 A Raney nickel catalyst for producing reduced indigo and a method for producing reduced indigo
CN119119770B (en) * 2024-09-05 2025-07-01 重庆市化工研究院有限公司 Vat dye dispersing agent, application thereof and preparation method of liquid pre-vat dye

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1035521A (en) * 1988-02-23 1989-09-13 三井东圧化学株式会社 The preparation method of indigo compound
CN1120357A (en) * 1993-03-30 1996-04-10 Basf公司 Process for dyeing cellulose-containing textile materials with hydrogenated indigo
CN1129008A (en) * 1993-08-13 1996-08-14 Basf公司 Granular indigo white preparation
US6428581B1 (en) * 1998-07-13 2002-08-06 Dystar Textilfarben Gmbh & Co. Deutschland Kg Concentrated leucoindigo solutions
CN101376747A (en) * 2008-10-10 2009-03-04 江苏工业学院 Method for recycling bipseudoindoxyl dye from indigo dyeing waste water

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1035521A (en) * 1988-02-23 1989-09-13 三井东圧化学株式会社 The preparation method of indigo compound
CN1120357A (en) * 1993-03-30 1996-04-10 Basf公司 Process for dyeing cellulose-containing textile materials with hydrogenated indigo
CN1129008A (en) * 1993-08-13 1996-08-14 Basf公司 Granular indigo white preparation
US6428581B1 (en) * 1998-07-13 2002-08-06 Dystar Textilfarben Gmbh & Co. Deutschland Kg Concentrated leucoindigo solutions
CN101376747A (en) * 2008-10-10 2009-03-04 江苏工业学院 Method for recycling bipseudoindoxyl dye from indigo dyeing waste water

Also Published As

Publication number Publication date
CN102516817A (en) 2012-06-27

Similar Documents

Publication Publication Date Title
CN102516817B (en) Method for preparing indigo white solution
Blackburn et al. The development of indigo reduction methods and pre‐reduced indigo products
CN106320015B (en) A kind of digit printing activity red ink and preparation method thereof
CN101024608A (en) Process for preparing fumaric acid by spraying acid water to benzene anhydride oxidized tail gas
EP2248860A1 (en) An orange active dye and the preparation thereof
CN104829028B (en) Nanofiltration membrane method continuous dyeing process
CN106758321B (en) A kind of disperse dye basic printing composite paste color paste and its preparation method and fabric printing method
CN109942434A (en) A kind of production method of large red-based g
CN104264513A (en) Preparation method of printing paste
CN101503853A (en) Method for processing fabric by scouring dyeing one bath
CN103787893A (en) O-phenylenediamine medium-pressure catalytic hydrogenation process
CN101935945A (en) One-bath two-step scouring bleaching and dyeing process of cotton fabric
CN105566949B (en) A kind of environment-friendly preparation method of sulfur dye solution
CN104264515A (en) Printing paste
CN104261419A (en) Production method of liquid sodium silicate
CN109180605A (en) The method of the direct synthetic rubber vulcanization accelerator TBBS of resin in waste water
CN109851127A (en) A kind of processing method of large red-based g spent acid
CN104264512A (en) Printing method
CN106477769A (en) A kind of processing method of nitrobenzene compounds waste water
CN106749304B (en) A kind of method of superacid catalysis hydrolysis 3,4,9,10- tetracarboxylic acid dianhydrides of preparation
CN106590015A (en) Direct orange S dye preparation process
CN105348846B (en) A kind of preparation method of lower salt content acid blue 9 dyestuff
CN111117285A (en) Refining method of vat blue 4
CN101935947B (en) Novel energy-saving environmental-friendly hydrogen peroxide remover for refining and bleaching textile and application thereof
CN102775813A (en) Pollution-free preparation process for acidic dye

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20131211