Shell-based sterilizing deodorant and preparation method thereof

文档序号:1250074 发布日期:2020-08-21 浏览:35次 中文

阅读说明:本技术 一种贝壳基杀菌消臭剂及其制备方法 (Shell-based sterilizing deodorant and preparation method thereof ) 是由 宋文东 蔡璐 纪丽丽 郭健 于 2020-04-23 设计创作,主要内容包括:本发明公开了一种杀菌除臭剂的制备方法,包括如下步骤:(a)使用第一表面活性剂对贝壳进行渗透处理,得到经渗透处理的贝壳;(b)对经渗透处理的贝壳进行微波膨化处理,得到经膨化处理的贝壳;(c)对经膨化处理的贝壳进行粉碎处理,得到粉碎的贝壳;(d)制备第二表面活性剂、粉碎的贝壳与水的混合物,得到所述杀菌除臭剂。本发明还公开了根据前述方法所制备的杀菌除臭剂。该杀菌除臭剂能够良好地杀灭细菌和消除臭味。(The invention discloses a preparation method of a sterilization deodorant, which comprises the following steps: (a) performing permeation treatment on the shell by using a first surfactant to obtain a permeation-treated shell; (b) performing microwave puffing treatment on the permeated shell to obtain a puffed shell; (c) crushing the expanded shell to obtain crushed shell; (d) preparing a mixture of a second surfactant, crushed shells and water to obtain the sterilizing deodorant. The invention also discloses the sterilization deodorant prepared by the method. The sterilizing deodorant can well kill bacteria and eliminate odor.)

1. A preparation method of a sterilizing deodorant comprises the following steps:

(a) performing permeation treatment on the shell by using a first surfactant to obtain a permeation-treated shell;

(b) performing microwave puffing treatment on the permeated shell to obtain a puffed shell;

(c) crushing the expanded shell to obtain a crushed shell;

(d) preparing a mixture of a second surfactant, the crushed shell and water to obtain the sterilizing deodorant solution.

2. The method of claim 1, further comprising the steps of:

(e) and drying the sterilization deodorant solution to obtain a dried sterilization deodorant.

3. The method according to claim 1, wherein the reaction mixture,

the shell is selected from bivalves;

preferably, the raw material of the bivalves shell is selected from one or the combination of more of mussel, scallop, oyster, pearl shell, clam and clam;

preferably, the first surfactant is a nonionic surfactant;

more preferably, the first nonionic surfactant is selected from one or a combination of more of PEG-9, TX100, PVP, AEO3, Span20 and APG;

more preferably, the first surfactant is an aqueous solution with a concentration of 0.5 w/v% to 8 w/v%, more preferably 1 w/v% to 5 w/v%;

preferably, the second surfactant is a nonionic surfactant;

more preferably, the second nonionic surfactant is selected from coconut diethanolamide and/or fatty alcohol polyoxyethylene ether.

4. The production method according to any one of claims 1 to 3,

before step (a), pretreating the shell, wherein the pretreatment comprises the following steps: treating the shell with weak acid, washing with water to neutrality, and performing primary drying;

preferably, the weak acid is selected from hydrochloric acid and/or phosphoric acid;

preferably, the weak acid is present in a concentration of 0.2-2M, more preferably 0.5-1M;

preferably, the shells are treated with a weak acid for 2-10 hours;

preferably, the first drying is natural drying at room temperature;

preferably, in the step (a), the mass g of the shell and the first surfactant is: the volume ml ratio is 1 (3-15), preferably 1 (5-10);

preferably, in step (a), the infiltration treatment time is 1 to 10h, preferably 2 to 6 h;

preferably, in the step (b), the second drying and then the microwave puffing treatment are carried out on the permeation-treated shells;

preferably, the second drying is drying treatment for 1-10h at 50-70 ℃;

preferably, the microwave power of the microwave puffing treatment is 300w-1500w, preferably 600w-1000 w;

preferably, the puffing time of the microwave puffing treatment is 10-500s, preferably 60-200 s;

preferably, the microwave puffing treatment is carried out under the protection of inert gas;

preferably, the inert gas is selected from one or a combination of several of nitrogen, helium, neon and argon;

preferably, the flow rate of the inert gas is 50-300ml/min, preferably 80-150 ml/min;

preferably, in the step (c), a micro-nano pulverizer is used for pulverizing;

preferably, in step (c), the average particle size of the crushed shell is 1 to 20 μm, preferably 2 to 10 μm.

5. The production method according to any one of claims 1 to 3,

in step (d), the mixture is prepared by the steps of: mixing the second surfactant, the crushed shells and water to obtain the sterilizing deodorant;

preferably, the mass g of the second surfactant, the crushed shell and water is: mass g: the volume ml ratio is: 1: (2-10): (10-50), more preferably, 1: (3-6): (15-30).

6. The production method according to any one of claims 1 to 3,

in step (d), the mixture is prepared by the steps of: mixing the crushed shell with water to obtain a micro-nano shell solution;

mixing a second surfactant with the micro-nano shell solution to obtain the sterilization deodorant;

preferably, the mass g of the crushed shell and the water is: the volume ml ratio is: 1: (2-15), more preferably, 1: (3-10);

preferably, the mass ratio of the second surfactant to the crushed shell is 1: (2-10), more preferably, 1: (3-6).

7. The method according to claim 2,

in step (e), the drying is spray drying.

8. A bactericidal deodorant prepared by the preparation method according to any one of claims 1 to 7.

9. Use of the method of production according to any one of claims 1 to 7 or the germicidal deodorant according to claim 8 for the preparation of a preparation for killing bacteria and eliminating odor.

10. The use according to claim 9,

the bacteria are selected from escherichia coli, staphylococcus aureus, salmonella, pseudomonas aeruginosa and staphylococcus albus;

preferably, the odor eliminated is odor caused by any one or combination of hydrogen sulfide, ammonia, methyl mercaptan and methyl sulfide.

Technical Field

The invention belongs to the technical field of processing of daily chemical articles, relates to a sterilization deodorant and a preparation method thereof, and particularly relates to a shell-based sterilization deodorant and a preparation method thereof.

Background

In the living environment of human beings, various microorganisms such as bacteria, viruses, and molds exist. When these microorganisms multiply on the clothes in large quantities, it is easy to cause various diseases. In addition, in the rainy season in the south and in a humid clothes drying room, the clothes are not easy to dry due to high air humidity, bacteria and mold are bred, and peculiar smell is generated in the clothes. Along with the improvement of living standard, people pay more attention to the cleanness and the comfort of clothes in life, so that how to effectively sterilize and deodorize the clothes of people becomes a research hotspot and a focus in the field of daily chemical industry at present.

The special disinfectant for clothes sold in the market at present is usually prepared by mixing a surfactant and a disinfectant, wherein the disinfectant is mainly polychlorinated compounds and hydrogen peroxide compounds, the disinfectant has the characteristics of pungent smell, fabric damage, inapplicability to colored clothes and the like, and if the disinfectant is not rinsed cleanly, the disinfectant has strong irritation to skin and mucous membranes and is harmful to body health. In addition, the sewage generated by washing the clothes by the clothes bactericide causes certain pollution to the environment after being discharged.

High temperature sterilization often causes damage to the laundry.

Therefore, a green and safe clothes sterilizing and deodorizing agent with good sterilizing performance is needed.

Disclosure of Invention

The invention aims to provide a safe, cheap and environment-friendly sterilization deodorant prepared by taking shells as raw materials, which has excellent sterilization and deodorization effects and overcomes the damage of the existing clothing sterilization agent to clothing, human bodies and the environment.

The invention provides a preparation method of a sterilizing deodorant, which comprises the following steps:

(a) performing permeation treatment on the shell by using a first surfactant to obtain a permeation-treated shell;

(b) performing microwave puffing treatment on the permeated shell to obtain a puffed shell;

(c) crushing the expanded shell to obtain a crushed shell;

(d) preparing a mixture of a second surfactant, the crushed shell and water to obtain the sterilizing deodorant solution.

The first surfactant functions to: improve the size of shell particles and the structure of holes, so that the shell particles are more uniform.

The microwave puffing treatment has the following effects: organic matters in the shells escape to form the biomass material with a special hole structure, and the puffing is a key step for preparing the material.

The second surfactant functions as: the micro-nano shell solution is mixed with a surfactant to enhance the washing effect.

The first surfactant is mainly used for regulating and controlling the surface structure in the shell modification process; the second surfactant is mainly a surfactant commonly used in the current detergent and is used for enhancing the washing performance.

In some embodiments, the method of making further comprises the steps of:

(e) and drying the sterilization deodorant solution to obtain a dried sterilization deodorant.

In some embodiments, the shell is selected from bivalves.

In some embodiments, the raw material of bivalve shell is selected from one or more of mussel, scallop, oyster, pearl shell, clam and clam.

In some embodiments, the first surfactant is a nonionic surfactant.

In some embodiments, the first nonionic surfactant is selected from the group consisting of PEG-9, TX100, PVP, AEO3, Span20, APG, in combination with one or more thereof.

In some embodiments, the first surfactant is an aqueous solution having a concentration of 0.5 w/v% to 8 w/v% (e.g., 1 w/v%, 2 w/v%, 3 w/v%, 4 w/v%, 5 w/v%, 6 w/v%, 7 w/v%), preferably 1 w/v% to 5 w/v%.

In some embodiments, the second surfactant is a nonionic surfactant.

In some embodiments, the second nonionic surfactant is selected from coconut diethanolamide and/or fatty alcohol polyoxyethylene ether.

In some embodiments, prior to step (a), the shell is pretreated by: treating the shell with weak acid, washing with water to neutrality, and performing primary drying.

In some embodiments, the weak acid is selected from hydrochloric acid and/or phosphoric acid.

In some embodiments, the weak acid is present in a concentration of 0.2 to 2M, preferably 0.5 to 1M.

In some embodiments, the shell is treated with the weak acid for 2-10 hours, such as 3 hours, 5 hours, 7 hours, 9 hours).

In some embodiments, the first drying is natural drying at room temperature.

In some embodiments, in step (a), the mass g: the volume ml ratio is 1 (3-15) (e.g., 1:5, 1:7, 1:9, 1:11, 1:13), preferably 1 (5-10).

The meaning of the mass-to-volume ratio is: the ratio between the mass of the shell and the volume of the first surfactant in step (a). For example: when the mass-volume ratio is 1:3, the dosage of the shell is 100g, the volume of the first surfactant is 300ml, or: the amount of shell is 1kg, and the volume of the first surfactant is 3L.

In some embodiments, in step (a), the time for the infiltration treatment is 1 to 10h (e.g., 3h, 5h, 7h, 9h), preferably 2 to 6 h.

In some embodiments, in step (b), the osmotically treated shell is subjected to a second drying step followed by a microwave expansion step.

In some embodiments, the second drying is a drying treatment at 50-70 ℃ (e.g., 55 ℃, 60 ℃, 65 ℃) for 1-10h (e.g., 3h, 5h, 7h, 9 h).

In some embodiments, the microwave power of the microwave puffing process is 300w-1500w (e.g., 500w, 700w, 900w, 1100w), preferably 600w-1000 w.

The microwave power is too low to reach the instantaneous temperature, so that the volatilization in the shells is incomplete, and the excessive power can cause the excessive decomposition of calcium carbonate and the collapse of holes.

In some embodiments, the microwave bulking process has a bulking time of 10 to 500s (e.g., 50s, 100s, 150s, 200s, 250s, 300s, 350s, 400s, 450s), preferably 60 to 200 s.

In some embodiments, the microwave puffing process is performed under an inert gas blanket.

In some embodiments, the inert gas is selected from one or a combination of nitrogen, helium, neon and argon.

In some embodiments, the inert gas flow rate is 50-300ml/min (e.g., 80ml/min, 100ml/min, 150ml/min, 200ml/min, 250ml/min, 280ml/min), preferably 80-150 ml/min.

In some embodiments, in step (c), the pulverization is performed using a micro-nano pulverizer.

In some embodiments, in step (c), the average particle size of the comminuted shell is 1 to 20 μm (e.g., 3 μm, 6 μm, 9 μm, 12 μm, 15 μm, 18 μm), preferably 2 to 10 μm, for use.

In some embodiments, in step (d), the step of preparing the mixture is: and mixing the second surfactant, the crushed shells and water to obtain the sterilizing deodorant.

In some embodiments, the mass g of the second surfactant, the crushed shell, and water: mass g: the volume ml ratio is: 1: (2-10): (10-50) (e.g., 1 (3, 4, 5, 6, 7, 8, 9): 12, 15, 20, 25, 30, 35, 40, 45, 48)), more preferably, 1: (3-6): (15-30).

In some embodiments, in step (d), the step of preparing the mixture is: mixing the crushed shell with water to obtain a micro-nano shell solution;

and mixing a second surfactant with the micro-nano shell solution to obtain the sterilizing deodorant.

In some embodiments, the mass g of the crushed shell and the water: the volume ml ratio is: 1: (2-15) (e.g., 1:3, 1:5, 1:7, 1:9, 1:11, 1:13), preferably, 1: (3-10).

In some embodiments, the amount by mass ratio of the second surfactant to the crushed shell is 1: (2-10) (e.g., 1:3, 1:4, 1:5, 1:6, 1:7, 1:8, 1:9), preferably, 1: (3-6).

In some embodiments, in step (e), the drying is spray drying.

In a second aspect, the present invention provides a bactericidal deodorant prepared by the preparation method according to the first aspect of the present invention.

The third aspect of the present invention provides the use of the method of manufacture according to the first aspect or the germicidal deodorant according to the second aspect of the present invention in the manufacture of a preparation for killing bacteria and eliminating off-flavors.

In some embodiments, the bacterium is selected from the group consisting of escherichia coli, staphylococcus aureus, salmonella, pseudomonas aeruginosa, staphylococcus albus.

In some embodiments, the odor eliminated is an odor caused by any one or a combination of hydrogen sulfide, ammonia, methyl mercaptan, methyl sulfide.

Compared with the prior art, the invention has the beneficial effects that:

the clothing sterilization deodorant is prepared by taking the shell-based modified material as a main body for the first time, and is excellent in sterilization and deodorization effects and environment-friendly; the material can realize instantaneous temperature rise and instantaneous temperature drop by utilizing the microwave puffing heating characteristic, can enable organic matters in the shells to escape instantaneously, has better puffing effect, forms uniform and rich calcium-based framework materials with holes, and can effectively adsorb and kill microorganisms such as bacteria, viruses, molds and the like by utilizing the adsorption characteristic and alkalescence formed by the structure of the material; after the calcium-based framework material and the surfactant are mixed and dried, the surfactant is embedded on the surface of the calcium-based framework material, so that the elution of microorganisms on the surface of clothes is facilitated in the process of washing the clothes, and a certain synergistic effect is achieved. The raw materials, the steps and the parameters of the preparation method of the product of the invention are synergistic, and the excellent effects of disinfection, sterilization and deodorization are achieved together.

Detailed Description

In order to make the objects, technical solutions and advantages of the present invention more apparent, embodiments of the present invention will be described in further detail below.

The instruments, materials and reagents used in the invention:

PVP (polyvinylpyrrolidone): homopolymers having a molecular weight of 3000-7000.

PEG-9: the molecular weight is 597.

Micro-nano rubbing crusher: manufactured by japan zenith corporation, model MKZA 10.

Instruments and reagents which are not particularly described are all conventional in the field, and have no special requirements; the particular illustrated instruments and reagents may be substituted without departing from the spirit of the invention, and no obvious difference is deemed by those skilled in the art.

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