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CN101041446A - Treatment method of waste potassium carbonate solution in the process of producing hydrogen peroxide by anthraquinone method - Google Patents

Treatment method of waste potassium carbonate solution in the process of producing hydrogen peroxide by anthraquinone method Download PDF

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CN101041446A
CN101041446A CN 200710027101 CN200710027101A CN101041446A CN 101041446 A CN101041446 A CN 101041446A CN 200710027101 CN200710027101 CN 200710027101 CN 200710027101 A CN200710027101 A CN 200710027101A CN 101041446 A CN101041446 A CN 101041446A
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alcohol
potassium carbonate
carbonate solution
hydrogen peroxide
waste
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CN100560497C (en
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钟存仁
庞江洪
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Guangdong Zhongcheng Chemicals Co ltd
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Abstract

The invention relates to a method for treating waste potassium carbonate solution containing a large amount of anthraquinone degradation products generated in the process of preparing hydrogen peroxide by an anthraquinone process. Firstly, adding a waste potassium carbonate solution into a concentration pot, heating and concentrating, and collecting steam while heating to obtain condensed water. Adding methanol into the pot and stirring to obtain alcohol precipitation slurry; putting the alcohol precipitation slurry into a rotary device, and filtering the alcohol washing slurry to obtain alcohol precipitation filter residues and alcohol precipitation filtrate; carrying out alcohol washing and filtering on the alcohol precipitation filter residue by using methanol to obtain an alcohol washing filter cake and an alcohol washing filtrate; and (3) carrying out vacuum drying on the alcohol washing filter cake to obtain solid potassium carbonate with the potassium carbonate content of about 95.3%. Rectifying the alcohol precipitation filtrate to obtain rectification residual liquid and rectification methanol, and burning the rectification residual liquid of the condensed water and the alcohol precipitation filtrate by using a coal gas-making furnace. The recovery rate of the potassium carbonate in the treatment method is 85 percent, and no waste liquid is discharged in the whole treatment process.

Description

蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法Treatment method of waste potassium carbonate solution in the process of producing hydrogen peroxide by anthraquinone method

技术领域technical field

本发明涉及一种在工业废渣治理中回收资源的方法,特别是一种蒽醌法制造双氧水过程中产生的含有大量蒽醌降解物的废碳酸钾溶液的回收处理和利用方法。The invention relates to a method for recovering resources in the treatment of industrial waste residues, in particular to a method for recycling, treating and utilizing waste potassium carbonate solution containing a large amount of anthraquinone degradation products produced in the process of producing hydrogen peroxide by an anthraquinone method.

背景技术Background technique

双氧水在纺织和造纸业用作漂白剂,在绿色化工合成中用作氧化剂和环氧化剂,在食品和医药行业中用作消毒剂、杀菌剂。蒽醌法是双氧水主流生产工艺。蒽醌法双氧水生产中是以2-乙基蒽醌为载体,以重芳烃和磷酸三辛酯为混合溶剂,配制成一定组成的溶液(称为工作液)。碳酸钾在处理双氧水工作液时,工作液中的部分水溶性降解物会溶于碳酸钾溶液中,使得碳酸钾溶液中的有机物不断增多。当碳酸钾溶液中的有机物积累到一定程度,就不适合继续循环使用。因此原工艺采用一部分处理完工作液后的碳酸钾溶液与新配纯碳酸钾溶液混合,重新返回工作液处理系统使用,另一部分则定期排放。不但浪费资源,而且还会造成严重的环境污染。Hydrogen peroxide is used as a bleaching agent in the textile and paper industry, as an oxidizing agent and epoxy oxidizing agent in green chemical synthesis, and as a disinfectant and bactericide in the food and pharmaceutical industries. The anthraquinone method is the mainstream production process of hydrogen peroxide. In the production of hydrogen peroxide by the anthraquinone method, 2-ethylanthraquinone is used as the carrier, and heavy aromatic hydrocarbons and trioctyl phosphate are used as mixed solvents to prepare a solution of a certain composition (called a working solution). When potassium carbonate is processing the hydrogen peroxide working fluid, some of the water-soluble degradation products in the working fluid will be dissolved in the potassium carbonate solution, so that the organic matter in the potassium carbonate solution will continue to increase. When the organic matter in the potassium carbonate solution accumulates to a certain extent, it is not suitable for continuous recycling. Therefore, the original process uses a part of the potassium carbonate solution after the working fluid is processed to be mixed with the newly prepared pure potassium carbonate solution, and then returned to the working fluid treatment system for use, and the other part is discharged regularly. Not only waste resources, but also cause serious environmental pollution.

发明内容Contents of the invention

本发明的目的在于,克服上述现有技术浪费资源、污染环境的问题,提供一种蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,以从废液中回收资源,保护环境,提高社会经济效益。The purpose of the present invention is to overcome the problems of wasting resources and polluting the environment in the prior art, and provide a treatment method for waste potassium carbonate solution in the process of producing hydrogen peroxide by anthraquinone method, so as to reclaim resources from waste liquid, protect the environment, and improve society. economic benefits.

为达上述目的,本发明采用的技术方案是:一种蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,包括如下步骤:For reaching above-mentioned object, the technical scheme that the present invention adopts is: a kind of processing method of waste potassium carbonate solution in the production hydrogen peroxide process of anthraquinone method, comprises the steps:

(1)物料浓缩:将废碳酸钾溶液加热蒸发浓缩,将浓度提高到60-95%;(1) Material concentration: the waste potassium carbonate solution is heated, evaporated and concentrated, and the concentration is increased to 60-95%;

(2)醇析:加入低分子醇,搅拌,得到醇析浆料;(2) Alcohol analysis: add low-molecular alcohol and stir to obtain alcohol analysis slurry;

(3)过滤:把醇析浆料进行过滤,得到醇析滤渣和醇析滤液;(3) Filtration: filter the alcohol analysis slurry to obtain alcohol analysis filter residue and alcohol analysis filtrate;

(4)醇洗过滤:对醇析滤渣进行醇洗和过滤,得到醇洗滤饼和醇洗滤液。(4) Alcohol washing and filtering: Alcohol washing and filtering are carried out on the alcohol analysis filter residue to obtain an alcohol washing filter cake and an alcohol washing filtrate.

上述的蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,包括真空干燥步骤:把醇洗滤饼进行真空干燥,得到固体碳酸钾。The method for treating waste potassium carbonate solution in the process of producing hydrogen peroxide by the above-mentioned anthraquinone method includes a vacuum drying step: vacuum drying the alcohol-washed filter cake to obtain solid potassium carbonate.

上述的蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,所述过滤、醇洗过滤和真空干燥步骤是在一带有过滤、洗涤和真空干燥功能的回转式装置中完成。In the above-mentioned treatment method of waste potassium carbonate solution in the process of producing hydrogen peroxide by anthraquinone method, the steps of filtering, washing with alcohol and vacuum drying are completed in a rotary device with functions of filtering, washing and vacuum drying.

上述的蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,对醇析滤液进行精馏,得到精馏残液和低分子醇。The method for treating waste potassium carbonate solution in the process of producing hydrogen peroxide by the above-mentioned anthraquinone method involves rectifying the alcohol analysis filtrate to obtain rectification raffinate and low-molecular alcohol.

上述的蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,物料浓缩步骤中,将废碳酸钾溶液浓度提高到85-95%。In the above method for treating waste potassium carbonate solution in the process of producing hydrogen peroxide by anthraquinone method, in the material concentration step, the concentration of waste potassium carbonate solution is increased to 85-95%.

蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,包括溶解脱醇步骤:用水溶解所述醇洗滤饼,对溶液进行蒸发分离低分子醇,得到碳酸钾溶液。The method for treating waste potassium carbonate solution in the process of producing hydrogen peroxide by anthraquinone method comprises the step of dissolving and dealcoholizing: washing the filter cake by dissolving the alcohol with water, evaporating the solution to separate low-molecular alcohols, and obtaining potassium carbonate solution.

蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,对溶液进行蒸发分离低分子醇时,收集含醇蒸汽,对含醇蒸汽进行精馏,得到精馏残液和低分子醇。The treatment method of waste potassium carbonate solution in the process of producing hydrogen peroxide by anthraquinone method, when the solution is evaporated to separate low-molecular alcohol, the alcohol-containing vapor is collected, and the alcohol-containing vapor is rectified to obtain rectification raffinate and low-molecular alcohol.

蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,将醇洗滤液在醇析时进行回用。The treatment method of waste potassium carbonate solution in the process of producing hydrogen peroxide by anthraquinone method is to reuse the alcohol wash filtrate during alcohol analysis.

蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,把低分子醇在醇洗时回用。The treatment method of waste potassium carbonate solution in the process of producing hydrogen peroxide by anthraquinone method is to reuse low-molecular alcohol during alcohol washing.

蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,利用煤造气炉焚烧处理冷凝水及精馏残液。这样可使其中难生物降解的有机物在造气炉中在高温下分解为有用的煤气,较彻底地解决了废物排放污染环境的问题。The treatment method of waste potassium carbonate solution in the process of producing hydrogen peroxide by anthraquinone method uses a coal gas furnace to incinerate condensed water and rectification raffinate. In this way, the biodegradable organic matter can be decomposed into useful gas at high temperature in the gas generator, which completely solves the problem of environmental pollution caused by waste discharge.

本发明通过蒸发和醇析等步骤措施,将蒽醌法制造双氧水过程中产生的含有大量蒽醌降解物的废碳酸钾溶液中的不同成分进行适当的分离处理,使得其中的主要成分碳酸钾能够重新进入双氧水的制造流程使用,节约了资源,保护了环境,提高社会经济效益。In the present invention, through steps such as evaporation and alcohol analysis, the different components in the waste potassium carbonate solution containing a large amount of anthraquinone degradation products produced in the process of producing hydrogen peroxide by anthraquinone method are properly separated and treated, so that the main component potassium carbonate can be obtained. Re-entering the hydrogen peroxide manufacturing process, saving resources, protecting the environment, and improving social and economic benefits.

所说的低分子醇主要指甲醇或乙醇。Said low-molecular alcohol mainly refers to methanol or ethanol.

附图说明Description of drawings

以下结合附图对本发明做进一步具体说明。The present invention will be further described in detail below in conjunction with the accompanying drawings.

本说明书所附图1为本发明一种实施例蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法的主要工艺流程图;Accompanying drawing 1 of this specification sheet is the main process flow diagram of the processing method of waste potassium carbonate solution in a kind of embodiment anthraquinone method of the present invention produces hydrogen peroxide process;

图2为第二种实施例的主要工艺流程图。Fig. 2 is the main process flow diagram of the second embodiment.

具体实施方式Detailed ways

实施例1Example 1

在图1所示第一种实施例中,处理蒽醌法生产双氧水过程中废碳酸钾溶液,首先将处理双氧水工作液后、含有大量蒽醌降解物的废碳酸钾溶液,其CODCr为20087.2mg/L,加入浓缩锅内加热浓缩,碳酸钾浓度达到85%时,停止浓缩;加热的同时收集蒸汽得到冷凝水。向浓缩锅内加入甲醇,进行搅拌,使碳酸钾发生醇析,得到醇析浆料;把醇析浆料放入带过滤、洗涤、真空干燥、溶解功能的回转式装置中,在回转式装置中,首先对醇洗浆料进行过滤,得到醇析滤渣和醇析滤液;用甲醇(也可用乙醇)对醇析滤渣进行醇洗和过滤,得到醇洗滤饼和醇洗滤液;醇洗滤液直接在醇析时进行回用。然后将醇洗滤饼进行真空干燥除去甲醇,可得到碳酸钾含量为95.3%左右的固体碳酸钾。然后将得到的固体碳酸钾溶解送到双氧水工艺过程回用。对上述过程中得到的醇析滤液进行精馏,得到精馏残液和精馏甲醇,并将精馏甲醇回用于酸洗。将冷凝水和醇析滤液的精馏残液用煤造气炉焚烧处理,其中的有机物在高温下分解生成有用的煤气。本蒽醌法生产双氧水过程中废碳酸钾溶液处理方法碳酸钾回收率大85%,CODCr去除率大于90%,整个处理过程无废液排放。In the first embodiment shown in Figure 1, the waste potassium carbonate solution in the process of producing hydrogen peroxide by anthraquinone method is first treated with the waste potassium carbonate solution containing a large amount of anthraquinone degradation products after the hydrogen peroxide working solution, and its COD Cr is 20087.2 mg/L, put into the concentration pot and heat to concentrate. When the concentration of potassium carbonate reaches 85%, stop the concentration; while heating, collect steam to obtain condensed water. Add methanol into the concentration pot and stir to make potassium carbonate undergo alcohol analysis to obtain alcohol analysis slurry; put the alcohol analysis slurry into a rotary device with functions of filtering, washing, vacuum drying and dissolving, and in the rotary device In the method, firstly, the alcohol washing slurry is filtered to obtain the alcohol analysis filter residue and the alcohol analysis filtrate; the alcohol analysis filter residue is carried out alcohol washing and filtering with methanol (ethanol can also be used), to obtain the alcohol washing filter cake and the alcohol washing filtrate; the alcohol washing filtrate Reuse directly during alcohol analysis. Then the alcohol-washed filter cake is vacuum-dried to remove methanol to obtain solid potassium carbonate with a potassium carbonate content of about 95.3%. Then the obtained solid potassium carbonate is dissolved and sent to the hydrogen peroxide process for reuse. Carry out rectification to the alcohol analysis filtrate obtained in the above process to obtain rectification raffinate and rectified methanol, and rectify methanol to be used for pickling. The rectification residue of condensed water and alcohol filtrate is incinerated in a coal gas generator, and the organic matter in it is decomposed at high temperature to generate useful gas. In the process of producing hydrogen peroxide by the anthraquinone method, the potassium carbonate recovery rate of the waste potassium carbonate solution treatment method is 85%, the COD Cr removal rate is greater than 90%, and there is no waste liquid discharge in the whole treatment process.

实施例2Example 2

在图2所示第二种实施例中,处理蒽醌法生产双氧水过程中废碳酸钾溶液,首先将处理双氧水工作液后、含有大量蒽醌降解物的废碳酸钾溶液,加入浓缩锅内加热浓缩,碳酸钾浓度达到90%时,停止浓缩;加热的同时收集蒸汽得到冷凝水。向浓缩锅内加入甲醇,进行搅拌,使碳酸钾发生醇析,得到醇析浆料;把上述醇析浆料放入带过滤、洗涤、溶解功能的装置中,在该装置中,首先对醇析浆料进行过滤,得到醇析滤渣和醇析滤液;用甲醇对醇析滤渣进行醇洗和过滤,得到醇洗滤饼和醇洗滤液;醇洗滤液直接在醇析时进行回用。然后加水溶解含甲醇的醇洗滤饼,对溶液进行蒸发分离甲醇并收集含醇蒸汽,得到碳酸钾溶液和含醇蒸汽。然后将得到的碳酸钾溶液送到双氧水工艺过程回用。上述过程中得到的醇析滤液和含醇蒸汽用精馏方法处理,得到精馏残液和精馏甲醇,精馏甲醇回用。将废碳酸钾溶液浓缩产生的冷凝水和精馏残液用煤造气炉焚烧处理。本蒽醌法生产双氧水过程中废碳酸钾溶液处理方法碳酸钾回收率大85%,CODCr去除率大于90%,整个处理过程无废液排放。In the second embodiment shown in Figure 2, the waste potassium carbonate solution in the process of producing hydrogen peroxide by anthraquinone method is firstly treated with the waste potassium carbonate solution containing a large amount of anthraquinone degradation products after the hydrogen peroxide working solution is added to the concentrated pot for heating Concentrate, when the concentration of potassium carbonate reaches 90%, stop concentrating; while heating, collect steam to obtain condensed water. Add methanol into the concentration pot and stir to make potassium carbonate undergo alcohol analysis to obtain alcohol analysis slurry; put the above alcohol analysis slurry into a device with functions of filtering, washing and dissolving. The alcohol analysis slurry is filtered to obtain alcohol analysis filter residue and alcohol analysis filtrate; the alcohol analysis filter residue is alcohol washed and filtered with methanol to obtain alcohol wash filter cake and alcohol wash filtrate; the alcohol wash filtrate is directly reused during alcohol analysis. Then add water to dissolve the methanol-containing alcohol-washed filter cake, evaporate the solution to separate methanol and collect alcohol-containing vapor to obtain potassium carbonate solution and alcohol-containing vapor. Then the obtained potassium carbonate solution is sent to the hydrogen peroxide process for reuse. The alcohol analysis filtrate and alcohol-containing vapor obtained in the above process are treated by rectification to obtain rectification raffinate and rectified methanol, and the rectified methanol is reused. The condensed water and rectification residue produced by concentrating the waste potassium carbonate solution are incinerated in a coal gas generator. In the process of producing hydrogen peroxide by the anthraquinone method, the potassium carbonate recovery rate of the waste potassium carbonate solution treatment method is 85%, the COD Cr removal rate is greater than 90%, and there is no waste liquid discharge in the whole treatment process.

本发明并不局限于上述具体的实施方式,凡依照本发明的特征及原理所做的等效变化,均属于本发明保护范围之内。The present invention is not limited to the specific embodiments described above, and all equivalent changes made according to the features and principles of the present invention fall within the protection scope of the present invention.

Claims (10)

1、一种蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,其特征在于包括如下步骤:1, a kind of processing method of waste potassium carbonate solution in the production hydrogen peroxide process of anthraquinone method is characterized in that comprising the steps: (1)物料浓缩:将废碳酸钾溶液加热蒸发浓缩,将浓度提高到60-95%;(1) Material concentration: the waste potassium carbonate solution is heated, evaporated and concentrated, and the concentration is increased to 60-95%; (2)醇析:加入低分子醇,搅拌,得到醇析浆料;(2) Alcohol analysis: add low-molecular alcohol and stir to obtain alcohol analysis slurry; (3)过滤:把醇析浆料进行过滤,得到醇析滤渣和醇析滤液;(3) Filtration: filter the alcohol analysis slurry to obtain alcohol analysis filter residue and alcohol analysis filtrate; (4)醇洗过滤:对醇析滤渣进行醇洗和过滤,得到醇洗滤饼和醇洗滤液。(4) Alcohol washing and filtering: Alcohol washing and filtering are carried out on the alcohol analysis filter residue to obtain an alcohol washing filter cake and an alcohol washing filtrate. 2.如权利要求1所述的蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,其特征在于包括真空干燥步骤:把醇洗滤饼进行真空干燥,得到固体碳酸钾。2. the processing method of waste potassium carbonate solution in the production hydrogen peroxide process of anthraquinone method as claimed in claim 1, it is characterized in that comprising vacuum drying step: alcohol washing filter cake is carried out vacuum drying, obtains solid potassium carbonate. 3.如权利要求2所述的蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,其特征在于:所述过滤、醇洗过滤和真空干燥步骤是在一带有过滤、洗涤和真空干燥功能的回转式装置中完成。3. the processing method of waste potassium carbonate solution in the production hydrogen peroxide process of anthraquinone method as claimed in claim 2, it is characterized in that: described filtration, alcohol washing filtration and vacuum drying step are to have filtration, washing and vacuum drying function together completed in the rotary device. 4.如权利要求1所述的蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,其特征在于:对醇析滤液进行精馏,得到精馏残液和低分子醇。4. the processing method of waste potassium carbonate solution in the production hydrogen peroxide process of anthraquinone method as claimed in claim 1, it is characterized in that: alcohol analysis filtrate is carried out rectifying, obtains rectifying raffinate and low-molecular alcohol. 5.如权利要求1至4中任意一项所述的蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,其特征在于:物料浓缩步骤中,将废碳酸钾溶液浓度提高到85-95%。5. the processing method of waste potassium carbonate solution in the production hydrogen peroxide process of anthraquinone method as described in any one in claim 1 to 4, it is characterized in that: in the material concentration step, waste potassium carbonate solution concentration is brought up to 85-95 %. 6.如权利要求1所述的蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,其特征在于包括溶解脱醇步骤:用水溶解所述醇洗滤饼,对溶液进行蒸发分离低分子醇,得到碳酸钾溶液。6. the processing method of waste potassium carbonate solution in the production hydrogen peroxide process of anthraquinone method as claimed in claim 1, it is characterized in that comprising the dissolving dealcoholization step: wash filter cake with described alcohol of dissolving with water, carry out evaporation separation low-molecular alcohol to solution , to obtain potassium carbonate solution. 7.如权利要求6所述的蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,其特征在于:对溶液进行蒸发分离低分子醇时,收集含醇蒸汽,对含醇蒸汽进行精馏,得到精馏残液和低分子醇。7. the processing method of spent potassium carbonate solution in the production hydrogen peroxide process of anthraquinone method as claimed in claim 6, it is characterized in that: when solution is evaporated and separated low molecular alcohol, alcohol-containing vapor is collected, and alcohol-containing vapor is rectified , to obtain rectification raffinate and low molecular weight alcohol. 8.如权利要求1至4中任何一项所述的蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,其特征在于:将醇洗滤液在醇析时进行回用。8. the processing method of waste potassium carbonate solution in the production hydrogen peroxide process of anthraquinone method as described in any one in claim 1 to 4, it is characterized in that: alcohol washing filtrate is reused when alcohol analysis. 9.如权利要求4或7所述的蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,其特征在于:把低分子醇在醇洗时回用。9. the processing method of spent potassium carbonate solution in the production hydrogen peroxide process of anthraquinone method as claimed in claim 4 or 7, it is characterized in that: low molecular weight alcohol is reused when washing with alcohol. 10.如权利要求4或7所述的蒽醌法生产双氧水过程中废碳酸钾溶液的处理方法,其特征在于:利用煤造气炉焚烧处理冷凝水及精馏残液。10. The method for processing waste potassium carbonate solution in the process of producing hydrogen peroxide by anthraquinone method as claimed in claim 4 or 7, characterized in that: utilize coal gas generator to incinerate condensed water and rectification raffinate.
CNB2007100271018A 2007-03-09 2007-03-09 Treatment method of waste potassium carbonate solution in the process of producing hydrogen peroxide by anthraquinone method Expired - Fee Related CN100560497C (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104402142A (en) * 2014-11-26 2015-03-11 柳州化工股份有限公司 Pretreatment method of sewage in hydrogen peroxide industry
CN104445735A (en) * 2014-11-26 2015-03-25 柳州化工股份有限公司 Treatment method of wastewater in hydrogen peroxide industry
CN117225604A (en) * 2023-11-10 2023-12-15 山西恒泰佳源生物科技有限公司 Sodium acetate solid-liquid mixture centrifugal separation equipment

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1031501C (en) * 1991-01-22 1996-04-10 山西大学 Process for recovery of aluminium compound from waste water during production of anthraquinone
EP0549013B1 (en) * 1991-11-26 1996-07-17 ENIRICERCHE S.p.A. Process for oxidizing organic compounds with hydrogen peroxide produced in an anthraquinone redox process

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104402142A (en) * 2014-11-26 2015-03-11 柳州化工股份有限公司 Pretreatment method of sewage in hydrogen peroxide industry
CN104445735A (en) * 2014-11-26 2015-03-25 柳州化工股份有限公司 Treatment method of wastewater in hydrogen peroxide industry
CN104445735B (en) * 2014-11-26 2016-04-13 柳州化工股份有限公司 The treatment process of waste water in a kind of hydrogen peroxide industry
CN104402142B (en) * 2014-11-26 2016-06-01 柳州化工股份有限公司 A kind of method of sewage disinfection treatment in hydrogen dioxide solution production by anthraquinone process industry
CN117225604A (en) * 2023-11-10 2023-12-15 山西恒泰佳源生物科技有限公司 Sodium acetate solid-liquid mixture centrifugal separation equipment
CN117225604B (en) * 2023-11-10 2024-01-30 山西恒泰佳源生物科技有限公司 Sodium acetate solid-liquid mixture centrifugal separation equipment

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