CN114653213A - Preparation method and application of cleaning agent for removing ultrafiltration membrane grease and organic matters - Google Patents

Preparation method and application of cleaning agent for removing ultrafiltration membrane grease and organic matters Download PDF

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Publication number
CN114653213A
CN114653213A CN202111605711.8A CN202111605711A CN114653213A CN 114653213 A CN114653213 A CN 114653213A CN 202111605711 A CN202111605711 A CN 202111605711A CN 114653213 A CN114653213 A CN 114653213A
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CN
China
Prior art keywords
ultrafiltration membrane
cleaning agent
preparation
grease
organic matters
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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.)
Pending
Application number
CN202111605711.8A
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Chinese (zh)
Inventor
马海龙
郭焱
马正佳
张得涛
郭宏栋
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GD Power Jiuquan Power Generation Co Ltd
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GD Power Jiuquan Power Generation Co Ltd
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Priority to CN202111605711.8A priority Critical patent/CN114653213A/en
Publication of CN114653213A publication Critical patent/CN114653213A/en
Pending legal-status Critical Current

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D65/00Accessories or auxiliary operations, in general, for separation processes or apparatus using semi-permeable membranes
    • B01D65/02Membrane cleaning or sterilisation ; Membrane regeneration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D61/00Processes of separation using semi-permeable membranes, e.g. dialysis, osmosis or ultrafiltration; Apparatus, accessories or auxiliary operations specially adapted therefor
    • B01D61/14Ultrafiltration; Microfiltration
    • B01D61/145Ultrafiltration
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2321/00Details relating to membrane cleaning, regeneration, sterilization or to the prevention of fouling
    • B01D2321/16Use of chemical agents
    • B01D2321/168Use of other chemical agents

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Water Supply & Treatment (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

The invention discloses a preparation method and application of a cleaning agent for removing ultrafiltration membrane grease and organic matters, wherein the preparation method comprises the following steps: mixing anionic surfactant and pH regulator, adding microorganism inhibitor, and adding water. The synergistic effect of various functional groups contained in each component of the cleaning agent prepared by the invention can effectively improve the removal rate of grease and organic matters, and simultaneously can keep the membrane flux and prolong the service life of the membrane. The addition of sodium hypochlorite can realize the effective removal and growth inhibition of microorganisms. The cleaning agent has the advantages of simple preparation process, no three-waste discharge, good medicament stability and water solubility, biodegradable main components, no toxicity, no pollution, no corrosiveness, environmental protection and environmental friendliness.

Description

Preparation method and application of cleaning agent for removing ultrafiltration membrane grease and organic matters
Technical Field
The invention relates to the technical field of new materials, in particular to an isopolymolybdic acid coordination polymer catalyst and a preparation method and application thereof.
Background
Polycaprolactone (PCL) is a semi-crystalline aliphatic polyester high molecular polymer, with a crystallinity of about 45%, a melting point of 59-64 deg.C, and a glass transition temperature of-60 deg.C. PCL has good biocompatibility and biodegradability, and is a polyester-based high-molecular polymer approved by the Food and Drug Administration (FDA) for clinical use. Because the chain segment structure of the PCL contains nonpolar methylene and polar ester group, the PCL has degradability and also has flexibility, processability and mechanical properties similar to those of polyolefin. In the medical field, PCLs may be used as, for example, bandages, orthotics, surgical sutures, and the like.
PCL is typically obtained by ring opening polymerization of caprolactone over a catalyst. At present, the most researched catalysts comprise an aluminum alkoxide catalyst, a stannous octoate catalyst, a rare earth alkoxide catalyst, a lipase catalyst and the like (Labet M, Thielemans W.chem.Soc.Rev.2009,38, 3484-3504). The above catalysts are highly active but are sensitive to water and air, so that the polymerization must be carried out under strictly anhydrous and anaerobic conditions. The preparation of PCL is mostly carried out in organic solvents such as tetrahydrofuran, dichloromethane, toluene and the like, the continuous production requirement of the polymerization industry is difficult to adapt, and the use of low-boiling organic solvents causes great harm to the environment.
As a novel inorganic-organic hybrid material, the metal-organic coordination polymer has the characteristics of containing unsaturated metal active sites, functionalized organic ligands, large specific surface area and the like, and shows excellent catalytic activity in organic conversion such as oxidation reaction, condensation reaction, ester exchange reaction, alkylation reaction, polymerization reaction and the like. In recent years, it has been found that heteropoly acid salt coordination polymers (Shenn., Tian F., Chang J., Huang K. -L., Zhang Z. -H., Feng X., Gu J., Chen S. -C., He M. -Y., Chen Q. CrystEngComm 2020,22, 3656-. However, no document is reported on the preparation of high molecular weight PCL by using the isopolyacid coordination polymer to catalyze the ring-opening polymerization of caprolactone. The research and development of the novel isopolyoxometalate coordination polymer catalyst for synthesizing the PCL with high molecular weight and narrow molecular weight distribution has wide space, and also has strong vitality for the research and injection of biomedical degradable high molecular materials.
Disclosure of Invention
This section is for the purpose of summarizing some aspects of embodiments of the invention and to briefly introduce some preferred embodiments. In this section, as well as in the abstract and the title of the invention of this application, simplifications or omissions may be made to avoid obscuring the purpose of the section, the abstract and the title, and such simplifications or omissions are not intended to limit the scope of the invention.
The present invention has been made in view of the above and/or other problems occurring in the prior art isopolymolybdic acid coordination polymer catalysts.
Therefore, one of the purposes of the invention is to overcome the defects of the existing cleaning agent and provide a preparation method of the cleaning agent for removing the grease and organic matters of the ultrafiltration membrane.
To solve the above technical problem, according to an aspect of the present invention, the present invention provides the following technical solutions: a preparation method of a cleaning agent for removing grease and organic matters of an ultrafiltration membrane is characterized by comprising the following steps: the method comprises the following steps:
mixing anionic surfactant and pH adjuster: mixing an anionic surfactant and a pH regulator;
adding a microbial inhibitor: adding a microbial inhibitor, and uniformly mixing;
adding water: and adding deionized water to prepare the ultrafiltration membrane cleaning agent.
As a preferred scheme of the preparation method of the cleaning agent for removing the grease and the organic matters of the ultrafiltration membrane, the preparation method comprises the following steps: mixing an anionic surfactant and a pH regulator, wherein the anionic surfactant comprises one or two of sodium dodecyl benzene sulfonate and sodium fatty alcohol-polyoxyethylene ether sulfate.
As a preferred scheme of the preparation method of the cleaning agent for removing the grease and the organic matters of the ultrafiltration membrane, the preparation method comprises the following steps: mixing an anionic surfactant and a pH regulator, wherein the pH regulator is hydroxide, and the hydroxide is sodium hydroxide.
As a preferred scheme of the preparation method of the cleaning agent for removing the grease and the organic matters of the ultrafiltration membrane, the preparation method comprises the following steps: adding the microbial inhibitor into the mixture, wherein the microbial inhibitor is sodium hypochlorite.
As a preferred scheme of the preparation method of the cleaning agent for removing the grease and the organic matters of the ultrafiltration membrane, the preparation method comprises the following steps: the anionic surfactant is sodium dodecyl benzene sulfonate and sodium fatty alcohol-polyoxyethylene ether sulfate, the pH regulator is sodium hydroxide, and the microbial inhibitor is sodium hypochlorite and comprises the following components in percentage by weight: 25-35% of sodium dodecyl benzene sulfonate; 8.0-15.0% of fatty alcohol-polyoxyethylene ether sodium sulfate; 0.1 percent of sodium hydroxide; 0.2-0.5% of sodium hypochlorite; the balance being deionized water.
As a preferred scheme of the preparation method of the cleaning agent for removing the grease and the organic matters of the ultrafiltration membrane, the preparation method comprises the following steps: mixing the anionic surfactant and the pH regulator, and stirring for 15-25 min at a rotating speed of 500-600 rpm.
As a preferred scheme of the preparation method of the cleaning agent for removing the grease and the organic matters of the ultrafiltration membrane, the preparation method comprises the following steps: and adding the microbial inhibitor into the microbial inhibitor, and stirring for 10-15 min at a rotating speed of 500-600 rpm.
The invention also aims to provide application of the cleaning agent for removing the ultrafiltration membrane to optimize organic matters.
To solve the above technical problem, according to an aspect of the present invention, the present invention provides the following technical solutions: the application of the cleaning agent for removing the optimized organic matters of the ultrafiltration membrane is characterized in that the prepared ultrafiltration membrane cleaning agent and pure water are diluted according to the mass fraction ratio of 1: 8.
As a preferable scheme of the application of the cleaning agent for removing the ultrafiltration membrane optimized organic matter, the cleaning agent comprises the following components: when the ultrafiltration membrane cleaning agent is used, the pH value is controlled to be 10.0-11.5.
As a preferable scheme of the application of the cleaning agent for removing the ultrafiltration membrane optimized organic matter, the cleaning agent comprises the following components: in the heating process, the temperature of the reaction kettle in the oven is 160-200 ℃, and the heating time is 48-96 hours. Compared with the prior art, the invention has the following beneficial effects:
1. the synergistic effect of various functional groups contained in each component of the cleaning agent can effectively improve the removal rate of grease and organic matters, and simultaneously can keep the membrane flux and prolong the service life of the membrane. The addition of sodium hypochlorite can realize the effective removal and growth inhibition of microorganisms.
2. The cleaning agent has the advantages of simple preparation process, no three-waste discharge, good medicament stability and water solubility, biodegradable main components, no toxicity, no pollution, no corrosiveness, environmental protection and environmental friendliness.
Detailed Description
In order to make the aforementioned objects, features and advantages of the present invention more comprehensible, specific embodiments thereof are described in detail below with reference to examples of the specification.
In the following description, numerous specific details are set forth in order to provide a thorough understanding of the present invention, but the present invention may be practiced in other ways than those specifically described and will be readily apparent to those of ordinary skill in the art without departing from the spirit of the present invention, and therefore the present invention is not limited to the specific embodiments disclosed below.
Furthermore, reference herein to "one embodiment" or "an embodiment" means that a particular feature, structure, or characteristic described in connection with the embodiment is included in at least one implementation of the invention. The appearances of the phrase "in one embodiment" in various places in the specification are not necessarily all referring to the same embodiment, nor are separate or alternative embodiments mutually exclusive of other embodiments. The following examples are set forth to enable those skilled in the art to practice the invention.
Example 1
The embodiment comprises the following raw materials in percentage by mass: 27.0% of sodium dodecyl benzene sulfonate, 9.0% of sodium fatty alcohol-polyoxyethylene ether sulfate, 0.1% of sodium hydroxide and 0.3% of sodium hypochlorite; 63.6% deionized water.
The preparation method of the ultrafiltration cleaning agent comprises the following steps: mixing sodium dodecyl benzene sulfonate, sodium fatty alcohol-polyoxyethylene ether sulfate and sodium hydroxide in proportion, stirring at the stirring speed of 550rpm for 20min, then adding sodium hypochlorite, stirring at the stirring speed of 550rpm for 12min, and adding deionized water in proportion to prepare the ultrafiltration membrane cleaning agent.
The cleaning agent prepared in the embodiment is diluted by pure water according to the mass fraction ratio of 1:8 according to the cleaning agent, the pH value is controlled at 10.7, an ultrafiltration membrane seriously polluted by grease and organic matters is cleaned, and experimental data of membrane pressure difference and water permeation flux before and after cleaning are measured. The test results are shown in Table 1.
Table 1 cleaning agent test results
State of state Membrane differential pressure Mpa Water flux m3/h
Before cleaning 1.27 0.31
After cleaning, cleaning 0.92 0.44
As can be seen from the test results in table 1: the cleaning agent disclosed by the invention is used for cleaning an ultrafiltration membrane, so that the membrane pressure difference can be effectively reduced, and the water permeation flux is recovered, thereby showing that the cleaning agent disclosed by the invention has an excellent cleaning effect on grease and organic matters, and cannot damage the membrane.
Example 2
34.0 percent of sodium dodecyl benzene sulfonate, 13.5 percent of fatty alcohol-polyoxyethylene ether sodium sulfate, 0.1 percent of sodium hydroxide and 0.5 percent of sodium hypochlorite by mass percent; 51.9% deionized water.
The preparation method of the ultrafiltration cleaning agent comprises the following steps: mixing sodium dodecyl benzene sulfonate, sodium fatty alcohol-polyoxyethylene ether sulfate and sodium hydroxide in proportion, stirring at the stirring speed of 550rpm for 20min, then adding sodium hypochlorite, stirring at the stirring speed of 550rpm for 12min, and adding deionized water in proportion to obtain the ultrafiltration membrane cleaning agent.
The cleaning agent prepared in the embodiment is diluted by pure water according to the mass fraction ratio of 1:8 according to the cleaning agent, the pH value is controlled at 10.7, an ultrafiltration membrane seriously polluted by grease and organic matters is cleaned, and experimental data of membrane pressure difference and water permeation flux before and after cleaning are measured. The test results are shown in Table 2.
Table 2 cleaning agent test results
State of state Membrane differential pressure Mpa Water flux m3/h
Before cleaning 1.45 0.26
After cleaning, cleaning 0.95 0.42
As can be seen from the test results in table 2: the cleaning agent disclosed by the invention is used for cleaning an ultrafiltration membrane, so that the membrane pressure difference can be effectively reduced, and the water permeation flux is recovered, thereby showing that the cleaning agent disclosed by the invention has an excellent cleaning effect on grease and organic matters, and cannot damage the membrane.
Example 3
31.5 percent of sodium dodecyl benzene sulfonate, 12.0 percent of sodium fatty alcohol-polyoxyethylene ether sulfate, 0.1 percent of sodium hydroxide and 0.4 percent of sodium hypochlorite by mass percent; 56.0% deionized water.
The preparation method of the ultrafiltration cleaning agent comprises the following steps: mixing sodium dodecyl benzene sulfonate, sodium fatty alcohol-polyoxyethylene ether sulfate and sodium hydroxide in proportion, stirring at the stirring speed of 550rpm for 20min, then adding sodium hypochlorite, stirring at the stirring speed of 550rpm for 12min, and adding deionized water in proportion to obtain the ultrafiltration membrane cleaning agent.
The cleaning agent prepared in the embodiment is diluted by pure water according to the mass fraction ratio of 1:8 according to the cleaning agent, the pH value is controlled at 10.7, an ultrafiltration membrane seriously polluted by grease and organic matters is cleaned, and the weight of the membrane before and after cleaning, the membrane pressure difference and the water yield are measured. The test results are shown in Table 3.
Table 3 cleaning agent test results
Status of state Membrane differential pressure Mpa Water yield m3/h
Before cleaning 1.36 0.32
After cleaning, cleaning 0.96 0.40
As can be seen from the test results in table 3: the cleaning agent disclosed by the invention is used for cleaning an ultrafiltration membrane, so that the membrane pressure difference can be effectively reduced, and the water permeation flux is recovered, thereby showing that the cleaning agent disclosed by the invention has an excellent cleaning effect on grease and organic matters, and cannot damage the membrane.
It should be noted that the above-mentioned embodiments are only for illustrating the technical solutions of the present invention and not for limiting, and although the present invention has been described in detail with reference to the preferred embodiments, it should be understood by those skilled in the art that modifications or equivalent substitutions may be made on the technical solutions of the present invention without departing from the spirit and scope of the technical solutions of the present invention, which should be covered by the claims of the present invention.

Claims (9)

1. A preparation method of a cleaning agent for removing grease and organic matters of an ultrafiltration membrane is characterized by comprising the following steps: the method comprises the following steps:
mixing anionic surfactant and pH adjuster: mixing an anionic surfactant and a pH regulator;
adding a microbial inhibitor: adding a microbial inhibitor, and uniformly mixing;
adding water: and adding deionized water to prepare the ultrafiltration membrane cleaning agent.
2. The preparation method of the detergent for removing the grease and the organic matters from the ultrafiltration membrane according to claim 1, which is characterized by comprising the following steps: in the mixed anionic surfactant and the pH regulator, the anionic surfactant comprises one or two of sodium dodecyl benzene sulfonate and sodium fatty alcohol-polyoxyethylene ether sulfate.
3. The preparation method of the detergent for removing the grease and the organic matters from the ultrafiltration membrane according to claim 1, which is characterized by comprising the following steps: in the mixed anionic surfactant and the pH regulator, the pH regulator is hydroxide, and the hydroxide is sodium hydroxide.
4. The preparation method of the detergent for removing the grease and the organic matters from the ultrafiltration membrane according to claim 1, which is characterized by comprising the following steps: the microbial inhibitor is added, and the microbial inhibitor is sodium hypochlorite.
5. The preparation method of the detergent for removing the grease and the organic matters from the ultrafiltration membrane according to the claims 1 to 4, which is characterized by comprising the following steps: the anionic surfactant is sodium dodecyl benzene sulfonate and sodium fatty alcohol-polyoxyethylene ether sulfate, the pH regulator is sodium hydroxide, and the microbial inhibitor is sodium hypochlorite, and comprises the following components in percentage by weight: 25-35% of sodium dodecyl benzene sulfonate; 8.0-15.0% of fatty alcohol-polyoxyethylene ether sodium sulfate; 0.1 percent of sodium hydroxide; 0.2-0.5% of sodium hypochlorite; the balance being deionized water.
6. The preparation method of the detergent for removing the grease and the organic matters from the ultrafiltration membrane according to claim 1, which is characterized by comprising the following steps: and stirring the mixed anionic surfactant and the pH regulator for 15-25 min at a rotating speed of 500-600 rpm.
7. The preparation method of the detergent for removing the grease and the organic matters on the ultrafiltration membrane according to claim 1 is characterized in that: adding the mixture into a microbial inhibitor, and stirring for 10-15 min at a rotating speed of 500-600 rpm after adding the microbial inhibitor.
8. The application of the cleaning agent for removing the ultrafiltration membrane to optimize the organic matters is characterized in that: diluting the prepared ultrafiltration membrane cleaning agent and pure water according to the mass fraction ratio of 1: 8.
9. The use of a cleaning agent for removing ultrafiltration membrane optimized organic matter according to claim 8, wherein: when the ultrafiltration membrane cleaning agent is used, the pH value is controlled to be 10.0-11.5.
CN202111605711.8A 2021-12-25 2021-12-25 Preparation method and application of cleaning agent for removing ultrafiltration membrane grease and organic matters Pending CN114653213A (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102343217A (en) * 2011-09-21 2012-02-08 石家庄开发区德赛化工有限公司 Ultrafiltration membrane alkaline cleaner
US20150105313A1 (en) * 2012-06-27 2015-04-16 Henkel Ag & Co. Kgaa Highly concentrated liquid washing or cleaning composition
CN105709605A (en) * 2015-08-13 2016-06-29 常州联江环保科技有限公司 Alkaline cleaning agent and bactericide applicable to ultra-filtration membranes or reverse osmosis membranes
CN107398185A (en) * 2017-07-19 2017-11-28 湖南军信环保股份有限公司 A kind of chemical cleaning method of milipore filter
CN112029592A (en) * 2020-07-25 2020-12-04 上海宝聚表面技术有限公司 Alkaline cleaning agent for hollow fiber ultrafiltration membrane and preparation method and application thereof

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102343217A (en) * 2011-09-21 2012-02-08 石家庄开发区德赛化工有限公司 Ultrafiltration membrane alkaline cleaner
US20150105313A1 (en) * 2012-06-27 2015-04-16 Henkel Ag & Co. Kgaa Highly concentrated liquid washing or cleaning composition
CN105709605A (en) * 2015-08-13 2016-06-29 常州联江环保科技有限公司 Alkaline cleaning agent and bactericide applicable to ultra-filtration membranes or reverse osmosis membranes
CN107398185A (en) * 2017-07-19 2017-11-28 湖南军信环保股份有限公司 A kind of chemical cleaning method of milipore filter
CN112029592A (en) * 2020-07-25 2020-12-04 上海宝聚表面技术有限公司 Alkaline cleaning agent for hollow fiber ultrafiltration membrane and preparation method and application thereof

Non-Patent Citations (1)

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Title
苏锡南等: "《环境微生物学》", 31 March 2015, 北京:中国环境科学出版社, pages: 153 - 155 *

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