阅读说明：本技术 一种难溶有机化合物的溶解方法和乳化方法 (Dissolving method and emulsifying method of insoluble organic compound ) 是由 平原 李寅 王义永 马敏 任鹏 于 2021-10-22 设计创作，主要内容包括：本发明提供一种难溶有机化合物的溶解方法和乳化方法。为了解决现有技术中用于难溶有机化合物类的溶解体系中多使用石化系列溶剂油,溶剂油使用量大、成本高且不环保,以及在使用时溶液与水乳化分散效果不好、稳定性不好、贮存时间短等问题,本发明提供一种难溶有机化合物的溶解方法,其步骤包括：(1)将烷基酚和主乳化剂搅拌混合得到初步混合物；(2)将初步混合物与助乳化剂搅拌混合得到二次混合物；(3)将二次混合物和脂肪酸酯混合并剪切匀化得到溶解体系；(4)将难溶有机化合物加入溶解体系内溶解得到混合溶液。通过本发明的溶解方法制备的混合溶液长期储存稳定性好、乳化性能好且低毒、环保、成本低。(The invention provides a method for dissolving and emulsifying a hardly soluble organic compound. In order to solve the problems that in the prior art, petrochemical solvent oil is mostly used in a dissolving system for insoluble organic compounds, the solvent oil is large in using amount, high in cost and not environment-friendly, and the solution and water are poor in emulsifying and dispersing effects, poor in stability, short in storage time and the like during use, the invention provides a dissolving method for insoluble organic compounds, which comprises the following steps: (1) stirring and mixing alkylphenol and a main emulsifier to obtain a primary mixture; (2) stirring and mixing the primary mixture and the auxiliary emulsifier to obtain a secondary mixture; (3) mixing the secondary mixture with fatty acid ester, shearing and homogenizing to obtain a dissolving system; (4) and adding the indissolvable organic compound into a dissolving system to dissolve to obtain a mixed solution. The mixed solution prepared by the dissolving method has the advantages of good long-term storage stability, good emulsifying property, low toxicity, environmental protection and low cost.)

1. A method for dissolving a sparingly soluble organic compound, characterized in that: the method comprises the following steps:

(1) stirring and mixing alkylphenol and a main emulsifier at a stirring speed of 300-500 rpm to obtain a primary mixture;

(2) stirring and mixing the primary mixture and an auxiliary emulsifier to obtain a secondary mixture;

(3) mixing the secondary mixture with fatty acid ester, shearing and homogenizing to obtain a dissolving system;

(4) stirring and mixing the insoluble organic compound and the dissolving system to obtain a mixed solution, controlling the stirring speed to be 300-500 rpm, controlling the temperature to be 50-70 ℃,

wherein, the main emulsifier comprises one or more of polyoxyethylene ether surfactants and/or one or more of polyoxyethylene phosphate surfactants;

the co-emulsifier comprises one or more of alcohol amine surfactants and/or one or more of pyrrolidone surfactants.

2. The dissolution process according to claim 1, characterized in that: the main emulsifier is one or more of fatty alcohol polyoxyethylene ether, phenethyl phenol polyoxyethylene ether phosphate and castor oil polyoxyethylene ether.

3. The dissolution process according to claim 1, characterized in that: the coemulsifier is one or more of ethanolamine, diethanolamine, triethanolamine and N-methyl pyrrolidone.

4. The dissolution process according to claim 1, characterized in that: the alkylphenol is selected from one or more of alkylphenol with alkyl chain length of 9-18 carbons.

5. The dissolution process according to claim 4, characterized in that: the alkylphenol is one or more of p-dodecylphenol, p-tetradecylphenol, p-hexadecylphenol and m-pentadecylphenol.

6. The dissolution process according to claim 1, characterized in that: the fatty acid ester is one or more of fatty acid methyl ester, fatty acid ethyl ester, fatty acid isooctyl ester and epoxy fatty acid methyl ester.

7. The dissolution process according to claim 1, characterized in that: the mass ratio of the main emulsifier to the auxiliary emulsifier is 1.5-8: 1.

8. The dissolution process according to claim 1, characterized in that: the mass ratio of the fatty acid ester to the alkylphenol is 1-10: 1.

9. The dissolution process according to claim 1, characterized in that: the sum of the mass of the alkylphenol and the fatty acid ester is 3-5 times of the sum of the mass of the main emulsifier and the mass of the auxiliary emulsifier.

10. The dissolution process according to claim 1, characterized in that: the mass ratio of the alkylphenol, the main emulsifier, the fatty acid ester and the auxiliary emulsifier is (2-15): (1.5-8): (5-20): 1.

11. the dissolution process according to claim 1, characterized in that: the indissolvable organic compound is an organic compound with the solubility of less than or equal to 250mg/L in water at 20 ℃ and 1 atm.

12. A method for emulsifying a sparingly soluble organic compound, characterized in that: the emulsification method includes the step of emulsifying and dispersing the mixed solution prepared by the dissolution method of any one of claims 1 to 11 with water to form an emulsion.

Technical Field

The invention relates to a dissolving method and an emulsifying method of an insoluble organic compound.

Background

In the existing production and operation, some organic compounds need to be diluted by a large amount of water for use, and the organic compounds are very inconvenient to transport and store due to the small solubility in water and the preparation of the organic compounds into aqueous solutions. The most common method in the prior art is to dissolve the insoluble organic compound in a system formed by petrochemical solvent oil, emulsifier and the like, and then mix the insoluble organic compound with water to form an oil-in-water emulsion so as to disperse the insoluble organic compound in the water. In addition, for the convenience of storage and transportation, the sparingly soluble organic compound is usually stored in a mixed solution prepared from a petrochemical solvent oil and an emulsifier, and the mixed solution is mixed with water when it is required to be used. However, because of the low flash point and high volatility of petrochemical solvent oil, great care is needed in storage and application; the petrochemical solvent oil belongs to non-renewable resources, and along with the industrial development, the total amount of the petrochemical solvent oil is lower and lower, and the use cost is higher and higher; and with the increasing importance of environmental protection and the control of VOCs, the use of solvent oil is limited. In addition, the solubility of the insoluble organic compound in the mixed solution is still low, the storage stability of the mixed solution is poor, and the insoluble organic compound is easy to precipitate for a long time and under the temperature change. Therefore, the conventional mixed solution has the problems of large using amount of solvent oil, emulsifier and surfactant and high cost. It is desired to further improve the solubility of the sparingly soluble organic compound in the mixed solution and to improve the stability and emulsification performance of the mixed solution to reduce the costs for raw materials, storage, transportation, etc. while reducing costs and reducing toxicity and protecting the environment, and therefore, there is an urgent need to develop a dissolving method and an emulsifying method which are environmentally friendly, have low toxicity, can improve the solubility of the sparingly soluble organic compound, and have good emulsification dispersibility and stability of the dissolved solution, for some sparingly soluble organic compounds.

Disclosure of Invention

The invention aims to provide a dissolving method and an emulsifying method which are safe and environment-friendly, can improve the solubility of insoluble organic compounds and have good emulsifying dispersibility and emulsifying stability.

In order to achieve the purpose, the invention adopts the technical scheme that:

in a first aspect, the present invention provides a method for dissolving a sparingly soluble organic compound, comprising the steps of:

(1) stirring and mixing alkylphenol and a main emulsifier at a stirring speed of 300-500 rpm to obtain a primary mixture;

(2) stirring and mixing the primary mixture and an auxiliary emulsifier to obtain a secondary mixture;

(3) mixing the secondary mixture with fatty acid ester, shearing and homogenizing to obtain a dissolving system;

(4) stirring and mixing the insoluble organic compound and the dissolving system to obtain a mixed solution, controlling the stirring speed to be 300-500 rpm, and controlling the temperature to be 50-70 ℃.

According to the invention, the main emulsifier comprises one or more polyoxyethylene ether surfactants and/or one or more polyoxyethylene phosphate surfactants.

According to the invention, the co-emulsifier comprises one or more of alcohol amine surfactants and/or one or more of pyrrolidone surfactants.

According to some embodiments, the primary emulsifier is one or more of fatty alcohol polyoxyethylene ether, phenethyl phenol polyoxyethylene ether phosphate, and castor oil polyoxyethylene ether.

Preferably, the fatty alcohol-polyoxyethylene ether comprises straight-chain fatty alcohol-polyoxyethylene ether and isomeric alcohol-polyoxyethylene ether.

According to some embodiments, the co-emulsifier is one or more of ethanolamine, diethanolamine, triethanolamine, N-methylpyrrolidone.

According to some embodiments, the primary emulsifier is a polyoxyethylene ether surfactant and the co-emulsifier is an alkanolamine surfactant.

According to some embodiments, the primary emulsifier is a combination of a polyoxyethylene ether surfactant and a polyoxyethylene phosphate surfactant, and the co-emulsifier is a pyrrolidone surfactant.

According to the invention, the alkylphenol is selected from one or more of alkylphenols with alkyl chain length of 9-18 carbons.

Specifically, the alkylphenol is selected from one or more of alkylphenols with alkyl chain length of 10-16 carbons.

According to some embodiments, the alkylphenol is one or more of p-dodecylphenol, p-tetradecylphenol, p-hexadecylphenol, and m-pentadecylphenol.

The fatty acid ester is one or more of fatty acid methyl ester, fatty acid ethyl ester, fatty acid isooctyl ester and epoxy fatty acid methyl ester.

Preferably, the fatty acid ester is selected from two or more of fatty acid methyl ester, fatty acid ethyl ester or epoxy fatty acid methyl ester.

In the present invention, the fatty acid ester is an ester of a fatty acid having a chain length of 12 to 22 carbon atoms and a fatty alcohol having a chain length of 1 to 10 carbon atoms.

According to some embodiments, the fatty acid ester comprises a fatty acid methyl ester and an epoxidized fatty acid methyl ester, and the mass ratio of the fatty acid methyl ester to the epoxidized fatty acid methyl ester is 1-3: 1.

According to other embodiments, the fatty acid ester comprises a fatty acid methyl ester and a fatty acid ethyl ester, and the mass ratio of the fatty acid methyl ester to the fatty acid ethyl ester is 1.2-2: 1.

According to other embodiments, the fatty acid ester comprises fatty acid ethyl ester and epoxidized fatty acid methyl ester, and the mass ratio of the fatty acid ethyl ester to the epoxidized fatty acid methyl ester is 1-1.5: 1.

According to the invention, the mass ratio of the main emulsifier to the auxiliary emulsifier is 1.5-8: 1.

Still more preferably, the mass ratio of the main emulsifier to the auxiliary emulsifier is 1.5-5: 1.

More preferably, the mass ratio of the main emulsifier to the auxiliary emulsifier is 1.5-3: 1.

According to the invention, the mass ratio of the fatty acid ester to the alkylphenol is 1-10: 1.

More preferably, the mass ratio of the fatty acid ester to the alkylphenol is 1-5: 1.

Still more preferably, the mass ratio of the fatty acid ester to the alkylphenol is 1-4: 1.

More preferably, the mass ratio of the fatty acid ester to the alkylphenol is 1-3.5: 1.

According to the invention, the sum of the mass of the alkylphenol and the fatty acid ester is 3-5 times of the sum of the mass of the main emulsifier and the mass of the auxiliary emulsifier.

According to the invention, the mass ratio of the alkylphenol, the main emulsifier, the fatty acid ester and the auxiliary emulsifier is (2-15): (1.5-8): (5-20): 1.

more preferably, the mass ratio of the alkylphenol, the main emulsifier, the fatty acid ester and the auxiliary emulsifier is (2-15): (1.5-5): (5-15): 1.

still more preferably, the mass ratio of the alkylphenol, the main emulsifier, the fatty acid ester and the auxiliary emulsifier is (3-10): (1.5-5): (5-13): 1.

in the present invention, the sparingly soluble organic compound is an organic compound having a solubility in water of 250mg/L or less at 20 ℃ and 1 atm.

Further, the hardly soluble organic compound is an organic compound having a solubility in water of 200mg/L or less at 20 ℃ under 1 atm.

Further, the insoluble organic compound contains one or more of phenyl, oxazoline group, phenoxy, ether bond, ester group or carboxyl.

Specifically, the insoluble organic compound is one or more of 8- (2, 6-diethyl-p-tolyl) -1,2,4, 5-tetrahydro-7-oxo-7H-pyrazolo [1,2-d ] [1,4,5] diazepin-9-yl-2, 2-dimethylpropionate, 3-chloro-4- [ 4-methyl-2-1H-1, 2, 4-triazol-1-ylmethyl) -1, 3-dithiacropin-2-yl) phenyl 4-chlorophenyl ether and 2- [4- (6-chloro-2-benzoxazoloxy) phenoxy ] propionic acid.

According to some embodiments, steps (1), (2) and (3) are all performed at room temperature.

The invention also provides an emulsification method of the indissolvable organic compound, which is characterized by comprising the following steps: the emulsification method comprises the step of emulsifying and dispersing the mixed solution prepared by the dissolution method and water to form an emulsion.

The invention also provides a dissolving system for dissolving the insoluble organic compound, and the components of the dissolving system comprise the following components by taking the total mass of the dissolving system as 100 percent:

40% -70% of fatty acid ester;

15% -45% of alkylphenol;

10% -16% of a main emulsifier;

4-9% of auxiliary emulsifier.

Further preferably, the components of the dissolution system comprise, based on 100% of the total mass of the dissolution system:

40% -60% of fatty acid ester;

20% -40% of alkylphenol;

10% -15% of a main emulsifier;

5% -8% of auxiliary emulsifier.

In a third aspect, the invention provides a product of 8- (2, 6-diethyl-p-tolyl) -1,2,4, 5-tetrahydro-7-oxo-7H-pyrazolo [1,2-d ] [1,4,5] diazepin-9-yl-2, 2-dimethylpropionate, which comprises 8- (2, 6-diethyl-p-tolyl) -1,2,4, 5-tetrahydro-7-oxo-7H-pyrazolo [1,2-d ] [1,4,5] diazepin-9-yl-2, 2-dimethylpropionate and the dissolution system.

Preferably, the mass ratio of the 8- (2, 6-diethyl-p-tolyl) -1,2,4, 5-tetrahydro-7-oxo-7H-pyrazolo [1,2-d ] [1,4,5] diazepin-9-yl-2, 2-dimethylpropionate to the dissolving system is 1-4: 1, more preferably 2-4: 1, even more preferably 2.5-3.5: 1, and the product is oily.

The 8- (2, 6-diethyl-p-tolyl) -1,2,4, 5-tetrahydro-7-oxo-7H-pyrazolo [1,2-d ] [1,4,5] diazepin-9-yl-2, 2-dimethylpropionate product can be used for inhibiting the growth of certain plants.

Due to the application of the technical scheme, compared with the prior art, the invention has the following advantages:

the method comprises the steps of firstly dissolving the insoluble organic compound in a dissolving system formed by fatty acid ester, alkylphenol and emulsifier, then emulsifying and dispersing the mixture with water to form emulsion, and adjusting the components of the dissolving system through the dissolving step, so that the insoluble organic compound can be dissolved by a smaller amount of the dissolving system while the petrochemical solvent oil is replaced by the fatty acid ester with wide sources, and the dissolved solution has good long-term storage stability, good emulsifying and dispersing performance with water and good stability of the formed emulsion, thereby improving the emulsifying performance and stability of the mixed solution while reducing the storage and transportation cost of the insoluble organic compound and improving the storage and transportation safety, and the method is environment-friendly, low-toxicity, simple and is worthy of popularization and utilization.

Detailed Description

All of the features disclosed in the specification of the invention, or all of the steps of any method or process so disclosed, may be combined in any combination, except combinations where mutually exclusive features or steps are claimed. The invention will now be further described with reference to specific examples, but the invention should not be limited to these examples, but may be substituted by other equivalent or similarly purposed alternative features unless specifically stated. Unless expressly stated otherwise, each feature is only an example of a generic series of equivalent or similar features. Terms used in the present invention generally have meanings commonly understood by those of ordinary skill in the art, unless otherwise specified.

In the prior art, in order to facilitate storage and transportation, a mixture solution of a slightly soluble organic compound, petrochemical solvent oil, an emulsifier and the like is generally prepared, and the mixture solution is mixed with water when the mixture solution is required to be used. The problems that the petrochemical solvent oil has low flash point, strong volatility, non-regeneration, limited use and the like, and the problems that the indissoluble organic compound is easy to separate out when being stored for a long time or the temperature is changed, the emulsifying performance of the mixed solution and water is poor and the like because the solubility of the indissoluble organic compound in the mixed solution is low, so that the storage and transportation cost of the indissoluble organic compound is high, the utilization rate is low and the use effect is poor are caused. Therefore, there is a need for developing a dissolving method and an emulsifying method which can improve the solubility of a hardly soluble organic compound without using a petrochemical solvent oil and have excellent emulsion dispersibility and emulsion stability.

In view of the deficiencies in the prior art, the inventors of the present invention have made extensive studies and extensive practices to provide technical solutions of the present invention. The technical solution, its implementation and principles, etc. will be further explained as follows.

The invention provides a method for dissolving an insoluble organic compound, which comprises the steps of adjusting and optimizing a dissolving step and a dissolving system, replacing petrochemical solvent oil with the compound of fatty acid ester and alkylphenol, selecting a proper main emulsifier and auxiliary emulsifier for compounding, improving the solubility and the dissolving stability of the insoluble organic compound in an oily dissolving system through the optimization of the dissolving step, forming emulsion with water, wherein the emulsion has good emulsifying dispersibility and high emulsion stability, can be used for the stable storage and the safe transportation of the organic compound with the solubility of less than or equal to 250mg/L in water at 20 ℃ and 1atm, and can be mixed with water according to a required proportion when in use.

The method for dissolving a sparingly soluble organic compound in the examples specifically comprises the steps of:

(1) stirring and mixing alkylphenol and a main emulsifier at a stirring speed of 300-500 rpm to obtain a primary mixture;

(2) stirring and mixing the primary mixture obtained in the step (1) and an auxiliary emulsifier to obtain a secondary mixture;

(3) mixing the secondary mixture obtained in the step (2) with fatty acid ester, shearing and homogenizing to obtain a dissolving system;

(4) and (2) mixing 8- (2, 6-diethyl p-tolyl) -1,2,4, 5-tetrahydro-7-oxo-7H-pyrazolo [1,2-d ] [1,4,5] diazepin-9-yl-2, 2-dimethylpropionate with the dissolved system obtained in the step (3) at a mixing temperature of 50-70 ℃ at a stirring speed of 300-500 rpm to obtain a mixed solution.

The method for emulsifying a sparingly soluble organic compound in the examples specifically includes: and (4) emulsifying and dispersing the mixed solution obtained in the step (4) and water according to a required mass ratio to form an emulsion.

The invention further improves the stability and the emulsifying property of the dissolving system by adjusting the dissolving step.

In the embodiment, the alkylphenol in the step (1) is alkylphenol with the alkyl chain length of 9-18 carbons; the main emulsifier in the step (1) comprises polyoxyethylene ether surfactant and/or polyoxyethylene phosphate surfactant.

The step (1) is carried out at normal temperature, the stirring time is 30-50 min at the stirring speed of 300-500 rpm, and the stirring time can be flexibly adjusted according to the state of the mixture.

The coemulsifier in the step (2) comprises an alcohol amine surfactant and/or a pyrrolidone surfactant.

And (2) carrying out the step (2) at normal temperature, and stirring and mixing uniformly at the stirring speed of 300-500 rpm.

The fatty acid ester in the step (3) is one or more of fatty acid methyl ester, fatty acid ethyl ester, fatty acid isooctyl ester and epoxy fatty acid methyl ester.

The feeding mass ratio of the main emulsifier in the step (1) to the auxiliary emulsifier in the step (2) is controlled to be 1.5-8: 1.

The mass ratio of the fatty acid ester in the step (3) to the alkylphenol in the step (1) is 1-10: 1

In some preferred embodiments, the ratio of the charged mass of the alkylphenol, the main emulsifier, the fatty acid ester and the auxiliary emulsifier is (2-15): (1.5-8): (5-20): 1.

and (3) carrying out the step (3) at normal temperature, and stirring and mixing uniformly at the stirring speed of 300-500 rpm.

The step (4) is carried out at the mixing temperature of 50-70 ℃, so that the dissolution of the insoluble organic compound is facilitated, and the properties of the product and the properties of a dissolution system are not influenced.

The emulsification step is carried out at normal temperature.

The fatty acid ester is used for replacing petrochemical solvent oil, so that the toxicity is reduced, and the method is safer and more environment-friendly.

Through compounding alkylphenol and fatty acid ester, proper main emulsifier and auxiliary emulsifier are selected for compounding, and through adjustment of a dissolving step, less dissolving systems are used for dissolving insoluble organic compounds, so that the insoluble organic compounds are good in long-term storage stability, good in emulsifying and dispersing effect and high in emulsion stability, and a large amount of solid is not separated out or emulsion breaking and layering phenomena occur in the emulsion under long-term or temperature fluctuation.

The solution dissolved with the organic compound by the dissolving method provided by the invention does not need any operation before use, has good emulsifying and dispersing performance with water and good emulsion stability, so that the solution containing the organic compound can be directly packaged into a product for sale to downstream use manufacturers. Of course, it is also possible to dispense the components of the dissolving system, dissolve the organic compound to be dissolved by the dissolving method according to the invention at the user's discretion, and then carry out the emulsification.

The present invention will be further described with reference to the following examples. However, the present invention is not limited to the following examples. The implementation conditions adopted in the embodiments can be further adjusted according to different requirements of specific use, and the implementation conditions not mentioned are conventional conditions in the industry. The technical features of the embodiments of the present invention may be combined with each other as long as they do not conflict with each other.

The starting materials used in the following examples and comparative examples are all commercially available.

The fatty acid methyl ester is manufactured by Viger Biotech limited of gold Tanskia, under the brand name of 1507/1192;

the fatty acid ethyl ester is produced by Viger Biotech limited of gold Tan district, Changzhou, under the mark of 2175;

epoxy fatty acid methyl ester is produced by Viger Biotechnology Inc. of gold Tan district, Changzhou, under the trademark ME 018;

the straight chain fatty alcohol polyoxyethylene ether is produced by Haian petrochemical plants in Jiangsu province under the brand MOA-5;

phenethylphenol polyoxyethylene ether is produced by Haian petrochemical plants in Jiangsu province, and has the brand number of 600 #;

the cardanol polyoxyethylene ether is produced by Haian petrochemical plants in Jiangsu province, and is of a mark GF-9;

the isomeric alcohol polyoxyethylene ether is produced by Haian petrochemical plants of Jiangsu province, and is of a brand number E-1310;

the phenethyl phenol polyoxyethylene ether phosphate ester is produced by Haian petrochemical plants in Jiangsu province, and is of a brand number of 600P;

the solvent oil No. 150 is produced by Jiangsu Hualun chemical industry limited company and is of a brand number S-150;

the castor oil polyoxyethylene ether is produced by a Haian petrochemical plant of Jiangsu province, and is of a brand EL-10;

calcium dodecylbenzenesulfonate is produced by Nantong de Yi chemical Co., Ltd., and is available under the brand name 505.

Example 1

A method for dissolving a sparingly soluble organic compound 8- (2, 6-diethyl-p-tolyl) -1,2,4, 5-tetrahydro-7-oxo-7H-pyrazolo [1,2-d ] [1,4,5] diazepin-9-yl-2, 2-dimethylpropionate:

(1) 20g of p-dodecylphenol and 12g of main emulsifier (10 g of straight-chain fatty alcohol polyoxyethylene ether and 2g of phenethyl phenol polyoxyethylene ether) are put into a high-shear stirring kettle, stirring is started, the rotating speed is 400rpm, stirring is carried out for 40min, and uniform mixing is carried out;

(2) adding 5g of co-emulsifier (ethanolamine) into a high-shear stirring kettle, rotating at the speed of 300rpm, and continuously stirring until the mixture is uniformly mixed;

(3) putting 43g of fatty methyl ester and 20g of epoxy fatty acid methyl ester into a high-shear stirring kettle, and shearing at the rotating speed of 300rpm until the appearance of the flowing liquid is homogeneous and transparent;

(4) 35g of 8- (2, 6-diethyl-p-tolyl) -1,2,4, 5-tetrahydro-7-oxo-7H-pyrazolo [1,2-d ] [1,4,5] oxadiazol-9-yl-2, 2-dimethylpropionate was put into a high shear stirred tank, and the stirring and heating device was turned on, the temperature was controlled at 60 ℃, the stirring speed was controlled at 400rpm, and the stirring time was 80min, so that sample 1 was obtained, which had a clear and oily appearance.

Example 2

(1) Putting 25g of m-pentadecyl phenol, 9g of cardanol polyoxyethylene ether, 3g of phenethyl phenol polyoxyethylene ether phosphate and 3g of isomeric alcohol polyoxyethylene ether into a high-shear stirring kettle, starting stirring at the rotating speed of 500rpm, stirring for 30min, and uniformly mixing;

(2) substantially the same as in step (2) of example 1, except that the coemulsifier was 6g of diethanolamine;

(3) substantially the same as in step (3) of example 1, except that the fatty acid ester was 29g of a fatty acid ethyl ester and 25g of an epoxidized fatty acid methyl ester;

(4) substantially the same procedure as in step (4) of example 1, except that the temperature was controlled to 50 ℃, the stirring speed was controlled to 400rpm, and the stirring time was 90min, gave sample 2 as a clear oil in appearance.

Example 3

(1) Putting 30g of p-hexadecylphenol, 11g of cardanol polyoxyethylene ether and 3g of isomeric alcohol polyoxyethylene ether into a high-shear stirring kettle, starting stirring at the rotating speed of 300rpm for 45min, and uniformly mixing;

(2) substantially as in step (2) of example 1, except that the co-emulsifier is 6g triethanolamine;

(3) substantially the same as in step (3) of example 1, except that the fatty acid ester was 30g of a fatty acid methyl ester and 20g of a fatty acid ethyl ester;

(4) substantially the same procedure as in step (4) of example 1, except that the temperature was controlled to 70 ℃, the stirring speed was controlled to 300rpm, and the stirring time was 70min, gave sample 3 as a clear oil in appearance.

Example 4

(1) Substantially the same as in step (1) of example 1, except that the alkylphenol was 40g of m-pentadecylphenol, and the main emulsifier was 10g of phenethylphenol polyoxyethylene ether phosphate and 3g of phenethylphenol polyoxyethylene ether;

(2) essentially the same as in step (2) of example 1, except that the co-emulsifier was 5g of N-methylpyrrolidone;

(3) substantially the same as in step (3) of example 1, except that the fatty acid ester was 22g of a fatty acid methyl ester and 20g of an epoxidized fatty acid methyl ester;

(4) sample 4 was obtained in the same manner as in step (4) of example 1, and was clear and oily in appearance.

Example 5

(1) Substantially the same as in step (1) of example 1 except that the alkylphenol was 30g of p-hexadecylphenol, the main emulsifier was 10g of phenethylphenol polyoxyethylene ether phosphate and 8g of phenethylphenol polyoxyethylene ether;

(2) essentially the same as in step (2) of example 1, except that the co-emulsifier was 2g of N-methylpyrrolidone;

(3) substantially the same as in step (3) of example 1, except that the fatty acid ester was 30g of a fatty acid methyl ester and 20g of a fatty acid ethyl ester;

sample 5, which was clear and oily in appearance, was obtained in the same manner as in step (4) of example 1.

Comparative example 1

(1) Putting 91g of solvent oil 150#, 5.5g of castor oil polyoxyethylene ether and 3.5g of calcium dodecylbenzene sulfonate into a high-shear stirring kettle, starting stirring, rotating at 400rpm for 40min, and obtaining flowing liquid with homogeneous and transparent appearance;

(2) 35g of 8- (2, 6-diethyl-p-tolyl) -1,2,4, 5-tetrahydro-7-oxo-7H-pyrazolo [1,2-d ] [1,4,5] diazepin-9-yl-2, 2-dimethylpropionate was put into a high shear stirred tank, and the stirring and heating device was turned on, the temperature was controlled at 70 ℃, the stirring speed was controlled at 500rpm, and the stirring time was 80min, so that sample 6 was obtained, which had a clear and oily appearance.

Comparative example 2

(1) Putting 27.5g of solvent oil 150#, 5.5g of castor oil polyoxyethylene ether and 3.5g of calcium dodecylbenzenesulfonate into a high-shear stirring kettle, starting stirring, rotating speed of 400rpm for 40 min;

(2) adding 23.5g of n-amyl alcohol and 40g of sec-butyl acetate into a high-shear stirring kettle, and continuously stirring at the rotating speed of 400rpm for 30min to obtain flowing liquid with homogeneous and transparent appearance;

(3) 35g of 8- (2, 6-diethyl-p-tolyl) -1,2,4, 5-tetrahydro-7-oxo-7H-pyrazolo [1,2-d ] [1,4,5] oxadiazol-9-yl-2, 2-dimethylpropionate was charged into a high shear stirred tank, and the stirring and heating apparatus was turned on, the temperature was controlled at 70 ℃, the stirring speed was controlled at 500rpm, and the stirring time was 80min, to give sample 7 as a clear oil in appearance.

Comparative example 3

(1) Putting 62g of fatty acid methyl ester, 25g of epoxy fatty acid methyl ester, 10g of phenethylphenol polyoxyethylene ether and 3g of calcium dodecylbenzene sulfonate into a high-shear stirring kettle, starting stirring, rotating at 400rpm for 40min, and obtaining flowing liquid with homogeneous and transparent appearance;

(2) 35g of 8- (2, 6-diethyl-p-tolyl) -1,2,4, 5-tetrahydro-7-oxo-7H-pyrazolo [1,2-d ] [1,4,5] oxadiazol-9-yl-2, 2-dimethylpropionate was placed in a high shear stirred tank, and the stirring and heating apparatus was turned on, the temperature was controlled at 70 ℃, the stirring speed was controlled at 500rpm, and the stirring time was 80min, to give sample 8 as a clear oil.

Comparative example 4

(1) Putting 40g of m-pentadecylphenol, 10g of phenethylphenol polyoxyethylene ether phosphate, 5g of phenethylphenol polyoxyethylene ether and 3g of calcium dodecylbenzene sulfonate into a high-shear stirring kettle, starting stirring, rotating at 450rpm, and stirring for 40 min;

(2) adding 17g of fatty acid methyl ester and 25g of epoxy fatty acid methyl ester into a high-shear stirring kettle, and continuously stirring at the rotating speed of 300rpm for 30min to obtain flowing liquid with homogeneous and transparent appearance;

(3) 35g of 8- (2, 6-diethyl-p-tolyl) -1,2,4, 5-tetrahydro-7-oxo-7H-pyrazolo [1,2-d ] [1,4,5] oxadiazol-9-yl-2, 2-dimethylpropionate was charged into a high shear stirred tank, and the stirring and heating apparatus was turned on, the temperature was controlled at 70 ℃, the stirring speed was controlled at 500rpm, and the stirring time was 80min, to give sample 9 as a clear oil in appearance.

Comparative example 5

(1) The procedure is substantially the same as in step (1) of example 4, except that the charged amount of m-pentadecylphenol is 5 g;

(2) the process is substantially the same as the step (2) in example 4, except that the charge amount of N-methylpyrrolidone is 3 g;

(3) substantially the same as in step (3) of example 4 except that the charged amount of fatty acid methyl ester was 54g and the charged amount of epoxidized fatty acid methyl ester was 25g, a fluid having a homogeneous and transparent appearance was obtained;

(4) in the same manner as in step (4) of example 4, sample 10 was obtained as a clear oil in appearance.

Comparative example 6

(1) The procedure is substantially the same as in step (1) of example 4, except that the charged amount of m-pentadecylphenol is 50 g;

(2) the process is substantially the same as the step (2) in example 4, except that the charge amount of N-methylpyrrolidone is 7 g;

(3) substantially the same as in step (3) of example 4, except that the fatty acid ester was 30g of a fatty acid methyl ester, to give a flowing liquid which was homogeneous and transparent in appearance;

(4) sample 11, which was clear and oily in appearance, was obtained in the same manner as in step (4) of example 4.

Stability test 1: and respectively taking 20mL of samples 1-11 as test samples, sealing and storing the samples in sample bottles, standing the samples at natural temperature for 365 days, and visually observing whether solids are separated out.

Stability test 2: adding 100ml of 25-30 ℃ standard hard water (342 ppm hard water) into a 250ml beaker, respectively sucking 1-115 ml of a sample by using a pipette, dropwise adding the sample into the standard hard water under the condition of continuous stirring to prepare 1-11 emulsion, stirring for 30s, respectively transferring the 1-11 emulsion into a clean 100ml measuring cylinder with a plug, placing the measuring cylinder with the plug into 35 ℃ constant-temperature water bath, standing for 2h, taking out, and observing the condition of the emulsion.

The results of stability test 1 and stability test 2 are shown in table 1.

The present invention has been described in detail in order to enable those skilled in the art to understand the invention and to practice it, and it is not intended to limit the scope of the invention, and all equivalent changes and modifications made according to the spirit of the present invention should be covered by the present invention.