CN113789025B - Xerogel for removing organic solvent micro-water and preparation method and application thereof - Google Patents

Xerogel for removing organic solvent micro-water and preparation method and application thereof Download PDF

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CN113789025B
CN113789025B CN202111155974.3A CN202111155974A CN113789025B CN 113789025 B CN113789025 B CN 113789025B CN 202111155974 A CN202111155974 A CN 202111155974A CN 113789025 B CN113789025 B CN 113789025B
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water
xerogel
organic solvent
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polypyrrole
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CN113789025A (en
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王义明
李航
李莉
郭旭虹
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East China University of Science and Technology
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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/28Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof by elimination of a liquid phase from a macromolecular composition or article, e.g. drying of coagulum
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J13/00Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
    • B01J13/0091Preparation of aerogels, e.g. xerogels
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J9/00Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof
    • C08J9/0061Working-up of macromolecular substances to porous or cellular articles or materials; After-treatment thereof characterized by the use of several polymeric components
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G33/00Dewatering or demulsification of hydrocarbon oils
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
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    • C08J2205/00Foams characterised by their properties
    • C08J2205/02Foams characterised by their properties the finished foam itself being a gel or a gel being temporarily formed when processing the foamable composition
    • C08J2205/028Xerogel, i.e. an air dried gel
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
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    • C08J2333/00Characterised by the use of homopolymers or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon-to-carbon double bond, and only one being terminated by only one carboxyl radical, or of salts, anhydrides, esters, amides, imides, or nitriles thereof; Derivatives of such polymers
    • C08J2333/24Homopolymers or copolymers of amides or imides
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    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
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    • C08J2479/00Characterised by the use of macromolecular compounds obtained by reactions forming in the main chain of the macromolecule a linkage containing nitrogen with or without oxygen, or carbon only, not provided for in groups C08J2461/00 - C08J2477/00
    • C08J2479/04Polycondensates having nitrogen-containing heterocyclic rings in the main chain; Polyhydrazides; Polyamide acids or similar polyimide precursors

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Abstract

The invention discloses a dried gel for removing organic solvent micro-water, which is obtained by adding polypyrrole with hygroscopic chloride into common dried gel. The invention also discloses a preparation method of the xerogel for removing the organic solvent micro water and application of the xerogel for removing the organic solvent micro water. The xerogel of the invention has the capability of absorbing and storing trace water in organic solvent more quickly, and solves the problem that the trace water is difficult to remove by common hydrogel. Meanwhile, the xerogel can be recycled, and can still achieve good dehydration effect after more than six times of circulation, thereby realizing the recycling of energy and reducing the energy consumption.

Description

Xerogel for removing organic solvent micro-water and preparation method and application thereof
Technical Field
The invention belongs to the field of chemical engineering and technology, and particularly relates to a xerogel for removing organic solvent micro-water, and a preparation method and application thereof.
Background
In chemical production, a lot of organic solvents are inevitably mixed with trace moisture, which not only affects the properties of the organic solvents, but also corrodes and damages the transportation and storage equipment of the organic solvents, resulting in safety accidents and huge economic losses. In addition, in some specific application occasions, the organic solvent also puts special requirements on the water content of the organic solvent, for example, the water content of oil products such as aviation kerosene, gasoline and the like is always strictly controlled, otherwise, the faults of a conveying pipeline and an engine are caused, and serious results are generated. For another example, in the refining process of petroleum, when water and crude oil are heated together, the water is rapidly vaporized and expanded, the pressure is increased, the normal operation and the product quality of a refinery are affected, and even explosion can occur. In view of this, the removal of the trace water in the organic solvent is an important production process in industrial production, however, the trace water is often present in a form that is miscible with the organic solvent, so that the removal is very difficult. The common micro-water removal method generally adopts an electric dehydration method, which has high efficiency, but has high energy consumption and high economic cost. Therefore, the development of a simple and efficient organic solvent micro-water removal method is urgent.
Hydrogel is a rapidly developing polymer material, is soft in nature, and can maintain a certain shape. The three-dimensional network structure is formed by mutual crosslinking through covalent bonds, hydrogen bonds or van der Waals force and the like, can hold water which is several times or even hundreds times of the weight of the three-dimensional network structure, and can integrate water absorption, water retention and slow release into a whole. As a material having high water absorption and high water retention, hydrogels are widely used for dehydration of petroleum-based organic solvents and the like. Although the use of xerogels for the dehydration of organic solvents has been common, the dehydration is less than ideal due to the limited ability of conventional xerogels to capture free water molecules.
Polypyrrole materials have strong hygroscopicity and the ability of capturing micro water in air, and polypyrrole has been studied to be applied to collection of moisture in the atmosphere and to soil water retention. However, no reports of the use of dry gels containing polypyrrole for removing traces of water in organic solvents have been found in the prior art.
Disclosure of Invention
In order to solve the problem that the common hydrogel can not capture trace water molecules, the invention provides the dry gel containing the polypyrrole, which can more quickly absorb and store trace water in an organic solvent, thereby solving the problem that the common hydrogel is difficult to remove the trace water.
In order to achieve the above objects, in a first aspect of the present invention, there is provided a xerogel for removing organic solvent trace water, which is obtained by adding polypyrrole having a hygroscopic chloride to a conventional xerogel.
In a second aspect of the present invention, there is provided a process for preparing the xerogel for removing organic solvent micro-water, comprising the steps of:
s1: alternately adding 0.5M ammonium persulfate solution and 1M pyrrole solution into 1.5M hydrochloric acid aqueous solution containing 1M lithium chloride, and continuously stirring, wherein the volume ratio of the ammonium persulfate solution to the pyrrole solution to the hydrochloric acid aqueous solution is 1;
s2: polymerizing the mixed solution, washing and filtering the mixed solution by using deionized water, and then uniformly dispersing the mixed solution in the deionized water by using ultrasound to obtain a polypyrrole hydrochloride solution;
s3: mixing a polymerization monomer, deionized water and N, N-methylene-bisacrylamide according to a molar ratio of 50 5555 to form a mixed solution, removing oxygen by using nitrogen for 1 hour, adding an initiator and an accelerator to perform prepolymerization, and then adding a polypyrrole hydrochloride solution, wherein the volume ratio of the mixed solution to the initiator, the accelerator and the polypyrrole hydrochloride solution is 500;
s4: and (3) putting the hydrogel generated by polymerization into an oven for drying to obtain the xerogel.
According to the invention, the polymerized monomer described in S3 is a neutral monomer, a cationic monomer or an anionic monomer, wherein:
the neutral monomer is selected from: n-isopropylacrylamide, acrylamide, hydroxyethyl methacrylate and N-dimethylacrylamide.
The cationic monomer is selected from: dimethylaminopropylacrylamide, [ (2-methacryloxy) ethyl ] trimethylammonium chloride, (2-dimethylamino) ethyl methacrylate, 2-aminoethyl methacrylate hydrochloride, (3-acrylamidopropyl) trimethylammonium chloride, 2- (dimethylamino) ethyl acrylate, N- [3- (dimethylamino) propyl ] methacrylamide, N- [3- (dimethylamino) propyl ] acrylamide, [2- (acryloyloxy) ethyl ] trimethylammonium chloride, [3- (methacrylamido) propyl ] trimethylammonium chloride, and (vinylbenzyl) trimethylammonium chloride.
The anionic monomer is selected from: acrylic acid, acrylamidopropanesulfonic acid esters, 2-acrylamido-2-methylpropanesulfonic acid, vinyl alcohol, and maleic anhydride.
According to the invention, the concentration of the polypyrrole hydrochloride solution in S3 is between 5 and 15 g/l.
In a third aspect of the invention, the application of the xerogel in removing micro water in an organic solvent is provided, wherein the organic solvent is a finished oil product, including crude oil, aviation kerosene and gasoline.
In a fourth aspect of the present invention, there is provided a method for removing trace water from an organic solvent, comprising charging the above-mentioned xerogel into the organic solvent.
Further, the organic solvent is a finished product oil product, including crude oil, aviation kerosene and gasoline.
The invention has the following beneficial effects:
1. the dried gel for removing the organic solvent micro-water greatly enhances the water molecule absorbing capacity of the hydrogel by adding the polypyrrole with hygroscopic chloride in the hydrogel, so that the dried gel can absorb more water more quickly in an environment with lower water content, and the removal of the micro-water in crude oil and various product oils is achieved.
2. The xerogel can quickly capture micro water molecules in the organic solvent and can remove the water content in the organic solvent to be below 10 micrograms/milliliter.
3. The xerogel can be recycled, can still achieve good dehydration effect after more than six cycles, and has wide application prospect.
4. The xerogel has low price and wide source, is more economical and practical compared with the common electric dehydration method, and effectively solves the problem that the hydrogel is difficult to be used for removing organic solvent, especially trace water in the oil product of the product oil.
Drawings
FIG. 1 is a schematic diagram of the removal of trace water from an organic solvent by a xerogel of the present invention.
Figure 2 is a photograph of the hydrogel before oven drying.
Fig. 3 is a photograph of the oven dried xerogel.
FIG. 4 is a schematic representation of the effect of the xerogels of examples 2-5 in removing trace water from aviation kerosene.
FIG. 5 is a graph showing the effect of the xerogels of examples 7-10 in removing trace water from aviation kerosene.
Fig. 6 is a schematic representation of the effect of the xerogel of example 3 for the recycling removal of micro-water from aviation kerosene.
Fig. 7 is a schematic representation of the effect of the xerogel of example 8 on the recycling removal of micro-water from aviation kerosene.
Detailed Description
The technical scheme of the invention is clearly and completely described by specific embodiments in the following combined with the attached drawings. It is to be understood that the described embodiments are only a few embodiments of the present invention, and not all embodiments. All other embodiments, which can be derived by a person skilled in the art from the embodiments of the invention without making creative efforts, fall within the scope of the invention.
The principle of removing the micro water from the organic solvent by the xerogel of the invention is shown in figure 1. The trace amount of water dissolved in the organic solvent is captured by the xerogel by two steps: 1) The trace amount of water dissolved in the organic solvent is enriched in the gel due to the hygroscopicity of polypyrrole hydrochloride; 2) The enriched water molecules in polypyrrole hydrochloride are captured by the hydrophilic polymer network for storage, with the consequent expansion of the gel.
Example 1: preparation of a solution of polypyrrole hydrochloride
S1: alternately adding 0.5M ammonium persulfate solution and 1M pyrrole solution into 1.5M hydrochloric acid aqueous solution containing 1M lithium chloride, and continuously stirring, wherein the volume ratio of the three solutions is 1;
s2: and after polymerizing for 15-30 minutes, washing and filtering by using deionized water, and then uniformly dispersing in the deionized water by using ultrasound to obtain a polypyrrole hydrochloride solution for later use.
Example 2: preparation of dry gel containing polypyrrole hydrochloride
S1: taking the polypyrrole hydrochloride solution obtained in the example 1, and adjusting the concentration to be 5 g/L by using deionized water;
s2: mixing neutral polymerization monomers of N-isopropylacrylamide, deionized water and N, N-methylene-bisacrylamide according to a molar ratio of 50;
s3: the hydrogel resulting from the polymerization was placed in an oven at 70 ℃ for more than 48 hours to obtain a dry gel containing polypyrrole hydrochloride.
Fig. 2 shows a photograph of the hydrogel before oven drying and fig. 3 shows a photograph of the xerogel after oven drying, showing that the hydrogel has a greatly reduced volume after drying, and that the xerogel can store a large amount of water from a comparison of the change in volume of the xerogel.
Example 3: preparation of dry gel containing polypyrrole hydrochloride
S1: taking the polypyrrole hydrochloride solution obtained in the example 1, and adjusting the concentration to be 10 g/L by using deionized water;
s2: mixing neutral polymerization monomers of N-isopropylacrylamide, deionized water and N, N-methylene-bisacrylamide according to a molar ratio of 50;
s3: the hydrogel produced by polymerization is put into an oven at 70 ℃ for drying for more than 48 hours to obtain dry gel containing polypyrrole hydrochloride.
Example 4: preparation of dry gel containing polypyrrole hydrochloride
S1: taking the polypyrrole hydrochloride solution obtained in the example 1, and adjusting the concentration to be 15 g/L by using deionized water;
s2: mixing neutral polymerization monomers of N-isopropylacrylamide, deionized water and N, N-methylene-bisacrylamide according to a molar ratio of 50;
s3: the hydrogel produced by polymerization is put into an oven at 70 ℃ for drying for more than 48 hours to obtain dry gel containing polypyrrole hydrochloride.
Example 5: preparation of a dry gel free of polypyrrole hydrochloride
S1: mixing neutral polymerization monomers, namely N-isopropylacrylamide, deionized water and N, N-methylene-bisacrylamide, according to a molar ratio of 50;
s2: the hydrogel resulting from the polymerization was placed in an oven at 70 ℃ for more than 48 hours to obtain a xerogel free of polypyrrole hydrochloride.
Example 6: test of Water absorption Effect of xerogel in aviation kerosene
10 ml of aviation kerosene was taken, the initial water content thereof was measured, and then 0.1 g of each of the xerogels synthesized in examples 2, 3, 4 and 5 was placed in 10 ml of aviation kerosene for sealed storage, and the water content in aviation kerosene was measured every 2 hours by a micro-moisture meter.
The test results are shown in fig. 4. From the results of FIG. 4, it can be seen that the water absorption rate in aviation kerosene and the effect of the final dehydration of the poly (isopropylacrylamide) xerogels of the present invention containing polypyrrole hydrochloride (examples 2 to 4) are much more enhanced than those of the conventional poly (isopropylacrylamide) xerogels (example 5).
Example 7: preparation of dry gel containing polypyrrole hydrochloride
S1: the polypyrrole hydrochloride solution obtained in example 1 was taken and adjusted to a concentration of 5 g/l with deionized water;
s2: mixing cationic polymerization monomers, namely dimethylamino propyl acrylamide, deionized water and N, N-methylene bisacrylamide, according to a molar ratio of 50;
s3: the hydrogel resulting from the polymerization was placed in an oven at 70 ℃ for more than 48 hours to obtain a dry gel containing polypyrrole hydrochloride.
Example 8: preparation of a Dry gel containing polypyrrole hydrochloride
S1: taking the polypyrrole hydrochloride solution obtained in the example 1, and adjusting the concentration to be 10 g/L by using deionized water;
s2: mixing cationic polymerization monomers, namely dimethylamino propyl acrylamide, deionized water and N, N-methylene bisacrylamide, according to a molar ratio of 50;
s3: the hydrogel produced by polymerization is put into an oven at 70 ℃ for drying for more than 48 hours to obtain dry gel containing polypyrrole hydrochloride.
Example 9: preparation of a Dry gel containing polypyrrole hydrochloride
S1: taking the polypyrrole hydrochloride solution obtained in the example 1, and adjusting the concentration to be 15 g/L by using deionized water;
s2: mixing cationic polymerization monomers, namely dimethylamino propyl acrylamide, deionized water and N, N-methylene bisacrylamide, according to a molar ratio of 50;
s3: the hydrogel produced by polymerization is put into an oven at 70 ℃ for drying for more than 48 hours to obtain dry gel containing polypyrrole hydrochloride.
Example 10: preparation of a dry gel free of polypyrrole hydrochloride
S1: mixing cationic polymerization monomers, namely dimethylamino propyl acrylamide, deionized water and N, N-methylene bisacrylamide, according to a molar ratio of 50;
s2: the hydrogel resulting from the polymerization was placed in an oven at 70 ℃ for more than 48 hours to obtain a xerogel free of polypyrrole hydrochloride.
Example 11: water absorption effect test of xerogel in aviation kerosene
10 ml of aviation kerosene was taken, the initial water content thereof was measured, and then 0.1 g each of the xerogels synthesized in examples 7, 8, 9 and 10 was put into 10 ml of aviation kerosene and stored in a sealed state, and the water content in the aviation kerosene was measured every 2 hours by a micro-moisture meter.
The test results are shown in fig. 5. From the results shown in FIG. 5, it can be seen that the poly (dimethylaminopropyl acrylamide) xerogel containing polypyrrole hydrochloride provided by the present invention (examples 7-9) has a greater gain in water absorption rate in aviation kerosene and the effect of being able to be dehydrated finally compared with the common poly (dimethylaminopropyl acrylamide) xerogel (example 10).
Example 12: effect of dry gel containing polypyrrole hydrochloride on micro-water circulation removal in aviation kerosene
10 ml of aviation kerosene was taken and tested for initial water content, after which 0.1 g of the xerogel synthesized according to example 3 was placed in it and stored sealed for a period of 24 hours, with water content being measured every 2 hours during the first 6 hours. After one cycle, the xerogel was taken out and put into new 10 ml aviation kerosene, and the experiment was repeated.
The test results are shown in fig. 6. The results in fig. 6 show that the poly-isopropyl acrylamide xerogel provided by the invention can still achieve good dehydration effect after more than six cycles in aviation kerosene, and has good recycling property.
Example 13: effect of dry gel containing polypyrrole hydrochloride on micro-water circulation removal in aviation kerosene
10 ml of aviation kerosene was taken and tested for initial water content, after which 0.1 g of the xerogel synthesized according to example 8 was introduced into it and stored in a sealed manner for 24 hours, with the water content being measured every 2 hours during the first 6 hours. After one cycle, the xerogel was taken out and put into new 10 ml aviation kerosene, and the experiment was repeated.
The test results are shown in fig. 7. The result of fig. 7 shows that the polydimethyl propyl acrylamide xerogel provided by the invention can still achieve good dehydration effect after more than six cycles in aviation kerosene, and has good recycling characteristic.

Claims (10)

1. A method for preparing xerogel for removing organic solvent micro-water is characterized by comprising the following steps:
s1: alternately adding 0.5M ammonium persulfate solution and 1M pyrrole solution into 1.5M hydrochloric acid aqueous solution containing 1M lithium chloride, and continuously stirring, wherein the volume ratio of the ammonium persulfate solution to the pyrrole solution to the hydrochloric acid aqueous solution is 1;
s2: polymerizing the mixed solution, washing and filtering the mixed solution by deionized water, and then uniformly dispersing the mixed solution in the deionized water by ultrasonic waves to obtain a polypyrrole hydrochloride solution;
s3: mixing a polymerization monomer, deionized water and N, N-methylene-bisacrylamide according to a molar ratio of 50 5555 to form a mixed solution, removing oxygen by using nitrogen for 1 hour, adding an initiator and an accelerator to perform prepolymerization, and then adding a polypyrrole hydrochloride solution, wherein the volume ratio of the mixed solution to the initiator, the accelerator and the polypyrrole hydrochloride solution is 500;
s4: the hydrogel resulting from the polymerization was placed in an oven at 70 ℃ for 48 hours to obtain the xerogel.
2. The method according to claim 1, wherein the polymerizable monomer in S3 is a neutral monomer, a cationic monomer or an anionic monomer.
3. The method of claim 2, wherein the neutral monomer is selected from the group consisting of: n-isopropylacrylamide, acrylamide, hydroxyethyl methacrylate, and N-dimethylacrylamide.
4. The method of claim 2, wherein the cationic monomer is selected from the group consisting of: dimethylaminopropylacrylamide, [ (2-methacryloxy) ethyl ] trimethylammonium chloride, (2-dimethylamino) ethyl methacrylate, 2-aminoethyl methacrylate hydrochloride, (3-acrylamidopropyl) trimethylammonium chloride, 2- (dimethylamino) ethyl acrylate, N- [3- (dimethylamino) propyl ] methacrylamide, [2- (acryloyloxy) ethyl ] trimethylammonium chloride, [3- (methacrylamido) propyl ] trimethylammonium chloride, and (vinylbenzyl) trimethylammonium chloride.
5. The method of claim 2, wherein the anionic monomer is selected from the group consisting of: acrylic acid, acrylamidopropanesulfonic acid ester, 2-acrylamido-2-methylpropanesulfonic acid, and maleic anhydride.
6. The method according to claim 1, wherein the concentration of the polypyrrole hydrochloride solution in S3 is 5 g/l to 15 g/l.
7. A xerogel for removal of organic solvent water made by the process of any one of claims 1 to 6.
8. Use of the xerogel of claim 7 for the removal of trace water from organic solvents, wherein the organic solvent is a finished oil selected from the group consisting of crude oil, jet fuel, and gasoline.
9. A method for removing trace water from an organic solvent, which comprises charging the xerogel of claim 7 into the organic solvent.
10. The method of claim 9, wherein the organic solvent is a finished petroleum product selected from the group consisting of crude oil, jet fuel, and gasoline.
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