CN108949221A - A kind of magnetism dewaxing agent and magnetic process for dewaxing - Google Patents
A kind of magnetism dewaxing agent and magnetic process for dewaxing Download PDFInfo
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- 230000005389 magnetism Effects 0.000 title description 4
- 230000005285 magnetism related processes and functions Effects 0.000 title 1
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 141
- 229920000642 polymer Polymers 0.000 claims abstract description 68
- 239000002122 magnetic nanoparticle Substances 0.000 claims abstract description 55
- 238000000034 method Methods 0.000 claims abstract description 36
- 125000000217 alkyl group Chemical group 0.000 claims abstract description 8
- 229920001577 copolymer Polymers 0.000 claims abstract description 8
- 125000004185 ester group Chemical group 0.000 claims abstract description 8
- 125000000468 ketone group Chemical group 0.000 claims abstract description 8
- 125000003368 amide group Chemical group 0.000 claims abstract description 7
- 229910001566 austenite Inorganic materials 0.000 claims abstract description 7
- 229920001519 homopolymer Polymers 0.000 claims abstract description 7
- 125000003277 amino group Chemical group 0.000 claims abstract description 6
- 125000004354 sulfur functional group Chemical group 0.000 claims abstract description 4
- 239000000203 mixture Substances 0.000 claims description 32
- 238000002156 mixing Methods 0.000 claims description 17
- -1 carbon alcohol ester Chemical class 0.000 claims description 8
- 239000002245 particle Substances 0.000 claims description 8
- 229910052799 carbon Inorganic materials 0.000 claims description 7
- 238000001816 cooling Methods 0.000 claims description 6
- 238000010907 mechanical stirring Methods 0.000 claims description 5
- 238000004018 waxing Methods 0.000 claims description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 claims description 3
- 229910052717 sulfur Inorganic materials 0.000 claims description 3
- 239000011593 sulfur Substances 0.000 claims description 3
- 125000002924 primary amino group Chemical group [H]N([H])* 0.000 claims description 2
- 239000001993 wax Substances 0.000 description 29
- 239000003921 oil Substances 0.000 description 24
- 239000010779 crude oil Substances 0.000 description 23
- 230000000694 effects Effects 0.000 description 17
- 230000009286 beneficial effect Effects 0.000 description 11
- 238000000926 separation method Methods 0.000 description 6
- 238000005119 centrifugation Methods 0.000 description 4
- 230000007423 decrease Effects 0.000 description 3
- 238000001556 precipitation Methods 0.000 description 3
- 238000003756 stirring Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000006116 polymerization reaction Methods 0.000 description 2
- 239000009671 shengli Substances 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- 238000000844 transformation Methods 0.000 description 2
- 229920002125 Sokalan® Polymers 0.000 description 1
- 230000004308 accommodation Effects 0.000 description 1
- 150000001408 amides Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000003760 magnetic stirring Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000004584 polyacrylic acid Substances 0.000 description 1
- 125000004149 thio group Chemical group *S* 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING 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
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
- C10G29/20—Organic compounds not containing metal atoms
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING 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
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/20—Characteristics of the feedstock or the products
- C10G2300/201—Impurities
- C10G2300/202—Heteroatoms content, i.e. S, N, O, P
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- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
- Soft Magnetic Materials (AREA)
Abstract
本发明公开了一种磁性脱蜡剂及磁性脱蜡方法,所述磁性脱蜡剂包括,磁性纳米颗粒和包覆在所述磁性纳米颗粒外周的聚合物脱蜡剂;所述磁性纳米颗粒包括Fe3O4、γ‑Fe2O3、Co2O3、NiO中的一种或两种及以上的组合;所述聚合物脱蜡剂包括分子中带有非极性基团和极性基团的高分子聚合物,包括均聚物和共聚物;所述聚合物脱蜡剂分子量在4000~100000之间;所述非极性基团包括长链烷基,所述极性基团包括酯基、酮基、氨基、酰胺基、硫基。通过上述方式,本发明能够简化脱蜡过程并降低脱蜡成本。
The invention discloses a magnetic dewaxing agent and a magnetic dewaxing method. The magnetic dewaxing agent includes magnetic nanoparticles and a polymer dewaxing agent coated on the outer periphery of the magnetic nanoparticles; the magnetic nanoparticles include Fe 3 O 4 , γ-Fe 2 O 3 , Co 2 O 3 , NiO or a combination of two or more; the polymer dewaxing agent includes non-polar groups and polar The macromolecular polymer of the group includes homopolymer and copolymer; the molecular weight of the polymer dewaxing agent is between 4,000 and 100,000; the non-polar group includes a long-chain alkyl group, and the polar group Including ester group, ketone group, amino group, amido group, sulfur group. Through the above method, the present invention can simplify the dewaxing process and reduce the cost of dewaxing.
Description
技术领域technical field
本发明涉及脱蜡技术领域,尤其涉及一种磁性脱蜡剂及磁性脱蜡方法。The invention relates to the technical field of dewaxing, in particular to a magnetic dewaxing agent and a magnetic dewaxing method.
背景技术Background technique
原油、成品油中含有一定量的蜡。这些蜡由C16以上的正构烷烃组成。随着温度的降低,这些蜡结晶析出并在原油中无规则搭接、缠绕,形成连续的三维结晶网络,使原油由溶胶体系向凝胶体系转变,形成具有一定强度的胶凝结构,这就给原油的开采、输送和使用带来了巨大的挑战。Crude oil and refined oil contain a certain amount of wax. These waxes are composed of normal paraffins above C16. As the temperature decreases, these waxes crystallize out and randomly overlap and entangle in the crude oil to form a continuous three-dimensional crystalline network, which makes the crude oil transform from a sol system to a gel system, forming a gel structure with a certain strength, which is It has brought great challenges to the extraction, transportation and use of crude oil.
现有技术中,原油中蜡的分离通常采用向原油中加入脱蜡剂并混合均匀,在降温过程中使蜡析出,并通过离心等方法使脱蜡后的原油与析出的蜡及剩余的脱蜡剂分离。这就使得脱蜡过程较为复杂,且脱蜡成本较高。In the prior art, the separation of wax in crude oil is usually done by adding a dewaxing agent to the crude oil and mixing it evenly, and the wax is precipitated during the cooling process, and the dewaxed crude oil is separated from the precipitated wax and the remaining wax by centrifugation and other methods. Wax separation. This makes the dewaxing process more complicated, and the cost of dewaxing is higher.
因此,现有技术还有待于改进和发展。Therefore, the prior art still needs to be improved and developed.
发明内容Contents of the invention
鉴于上述现有技术的不足,本发明的目的在于提供一种磁性脱蜡剂及磁性脱蜡方法,旨在解决现有脱蜡过程复杂,脱蜡成本高的问题。In view of the above deficiencies in the prior art, the object of the present invention is to provide a magnetic dewaxing agent and a magnetic dewaxing method, aiming at solving the problems of complicated dewaxing process and high dewaxing cost in the prior art.
本发明的技术方案如下:Technical scheme of the present invention is as follows:
一种磁性脱蜡剂,其中,所述磁性脱蜡剂包括:A magnetic dewaxing agent, wherein the magnetic dewaxing agent comprises:
磁性纳米颗粒和包覆在所述磁性纳米颗粒外周的聚合物脱蜡剂;Magnetic nanoparticles and a polymer dewaxing agent coated on the periphery of the magnetic nanoparticles;
所述磁性纳米颗粒包括Fe3O4、γ-Fe2O3、Co2O3、NiO中的一种或两种及以上的组合;The magnetic nanoparticles include one or a combination of two or more of Fe 3 O 4 , γ-Fe 2 O 3 , Co 2 O 3 , and NiO;
所述聚合物脱蜡剂包括分子中带有非极性基团和极性基团的高分子聚合物,包括均聚物和共聚物;所述聚合物脱蜡剂分子量在4000~100000之间;所述非极性基团包括长链烷基,所述极性基团包括酯基、酮基、氨基、酰胺基、硫基。The polymer dewaxing agent includes polymers with non-polar groups and polar groups in the molecule, including homopolymers and copolymers; the molecular weight of the polymer dewaxing agent is between 4000 and 100000 ; The non-polar group includes a long-chain alkyl group, and the polar group includes an ester group, a ketone group, an amino group, an amido group, and a sulfur group.
其中,所述磁性纳米颗粒的粒径为5-50nm。Wherein, the particle size of the magnetic nanoparticles is 5-50nm.
其中,所述磁性纳米颗粒与所述聚合物脱蜡剂通过溶液共混或熔融共混的方式复合在一起。Wherein, the magnetic nanoparticles and the polymer dewaxing agent are compounded together by solution blending or melt blending.
其中,所述聚合物脱蜡剂包括聚丙烯酸高碳醇酯和/或聚乙烯-醋酸乙烯酯。Wherein, the polymer dewaxing agent includes polyacrylic high carbon alcohol ester and/or polyethylene-vinyl acetate.
一种磁性脱蜡方法,其中,所述方法包括:A magnetic dewaxing method, wherein said method comprises:
提供预设质量的磁性脱蜡剂,所述磁性脱蜡剂包括磁性纳米颗粒和包覆在所述磁性纳米颗粒外周的聚合物脱蜡剂;所述磁性纳米颗粒包括Fe3O4、γ-Fe2O3、Co2O3、NiO中的一种或两种及以上的组合;所述聚合物脱蜡剂包括分子中带有非极性基团和极性基团的高分子聚合物,包括均聚物和共聚物;所述聚合物脱蜡剂分子量在4000~100000之间;所述非极性基团包括长链烷基,所述极性基团包括酯基、酮基、氨基、酰胺基、硫基;Provide a preset quality magnetic dewaxing agent, the magnetic dewaxing agent includes magnetic nanoparticles and a polymer dewaxing agent coated on the outer periphery of the magnetic nanoparticles; the magnetic nanoparticles include Fe 3 O 4 , γ- One or a combination of two or more of Fe 2 O 3 , Co 2 O 3 , and NiO; the polymer dewaxing agent includes high molecular polymers with non-polar groups and polar groups in the molecule , including homopolymers and copolymers; the molecular weight of the polymer dewaxing agent is between 4,000 and 100,000; the non-polar groups include long-chain alkyl groups, and the polar groups include ester groups, ketone groups, Amino, amido, sulfur;
将所述预设质量的磁性脱蜡剂与预设质量的待处理油品混合,得到混合物;Mixing the preset quality magnetic dewaxing agent with the preset quality oil product to be treated to obtain a mixture;
对所述混合物进行降温至预设温度及以下,使所述待处理油品中的蜡分子在所述磁性脱蜡剂表面结晶,得到含有析出蜡的磁性脱蜡剂;cooling the mixture to a preset temperature or below, so that the wax molecules in the oil to be treated crystallize on the surface of the magnetic dewaxing agent to obtain a magnetic dewaxing agent containing precipitated wax;
对所述混合物施加磁场,使所述磁性脱蜡剂析出。A magnetic field is applied to the mixture to precipitate the magnetic dewaxing agent.
其中,当所述预设质量的待处理油品为100g时,所述预设质量的磁性脱蜡剂为5-20mg。Wherein, when the preset mass of oil to be treated is 100g, the preset mass of magnetic dewaxing agent is 5-20mg.
其中,所述预设温度为所述待处理油品的析蜡点。Wherein, the preset temperature is the waxing point of the oil to be treated.
其中,所述对所述混合物进行降温至预设温度之前还包括:Wherein, before the said mixture is cooled to the preset temperature, it also includes:
将所述混合加热至50-80℃,并采用机械搅拌的方式搅拌0.2-1h。The mixture was heated to 50-80° C. and stirred by mechanical stirring for 0.2-1 h.
其中,对所述混合物施加磁场,使所述磁性脱蜡剂析出之后还包括:Wherein, applying a magnetic field to the mixture, after the magnetic dewaxing agent is separated out, also includes:
对所述混合物进行过滤,将包括析出蜡的磁性脱蜡剂从所述混合物中分离出来。The mixture is filtered to separate the magnetic dewaxing agent including precipitated wax from the mixture.
其中,所述磁场来自永磁体或电磁铁。Wherein, the magnetic field comes from a permanent magnet or an electromagnet.
有益效果:本发明的磁性脱蜡剂包括磁性纳米颗粒和包覆在所述磁性纳米颗粒外周的聚合物脱蜡剂;所述磁性纳米颗粒包括Fe3O4、γ-Fe2O3、Co2O3、NiO中的一种或两种及以上的组合。这种纳米磁性内核外周包裹聚合物脱蜡剂的结构能够使聚合物脱蜡剂与原油更好的接触,提高脱蜡效果。而具有磁性的所述磁性脱蜡剂可通过外加磁场进行分离,且不必采用离心等分离操作就能将脱蜡后的原油与析出的蜡及剩余的脱蜡剂分离,不仅简化脱蜡流程且有利于降低脱蜡成本。Beneficial effects: the magnetic dewaxing agent of the present invention includes magnetic nanoparticles and a polymer dewaxing agent coated on the periphery of the magnetic nanoparticles; the magnetic nanoparticles include Fe 3 O 4 , γ-Fe 2 O 3 , Co One or a combination of two or more of 2 O 3 and NiO. The structure of the polymer dewaxing agent wrapped around the nano-magnetic inner core can make the polymer dewaxing agent better contact with crude oil and improve the dewaxing effect. The magnetic dewaxing agent with magnetism can be separated by an external magnetic field, and the dewaxed crude oil can be separated from the precipitated wax and the remaining dewaxing agent without using separation operations such as centrifugation, which not only simplifies the dewaxing process and It is beneficial to reduce the cost of dewaxing.
附图说明Description of drawings
图1为本发明一种磁性脱蜡剂较佳实施例的结构示意图;Fig. 1 is the structural representation of a preferred embodiment of a magnetic dewaxing agent of the present invention;
图2为本发明一种磁性脱蜡方法较佳实施例的流程示意图。Fig. 2 is a schematic flow diagram of a preferred embodiment of a magnetic dewaxing method of the present invention.
具体实施方式Detailed ways
本发明提一种磁性脱蜡剂及磁性脱蜡方法,为使本发明的目的、技术方案及效果更加清楚、明确,以下对本发明进一步详细说明。应当理解,此处所描述的具体实施例仅仅用以解释本发明,并不用于限定本发明。The present invention provides a magnetic dewaxing agent and a magnetic dewaxing method. In order to make the purpose, technical solution and effect of the present invention clearer and clearer, the present invention will be further described in detail below. It should be understood that the specific embodiments described here are only used to explain the present invention, not to limit the present invention.
请参考图1,图1是本发明一种磁性脱蜡剂较佳实施例的结构示意图,所述磁性脱蜡剂包括,磁性纳米颗粒100和包覆在所述磁性纳米颗粒外周的聚合物脱蜡剂200;所述磁性纳米颗粒100包括Fe3O4、γ-Fe2O3、Co2O3、NiO中的一种或两种及以上的组合;所述聚合物脱蜡剂200包括分子中带有非极性基团和极性基团的高分子聚合物,包括均聚物和共聚物;所述聚合物脱蜡剂200分子量在4000~100000之间;所述非极性基团包括长链烷基,所述极性基团包括酯基、酮基、氨基、酰胺基、硫基。Please refer to FIG. 1. FIG. 1 is a schematic structural view of a preferred embodiment of a magnetic dewaxing agent of the present invention, which includes magnetic nanoparticles 100 and polymer dewaxing coatings on the outer periphery of the magnetic nanoparticles. Wax agent 200; the magnetic nanoparticles 100 include one or a combination of two or more of Fe 3 O 4 , γ-Fe 2 O 3 , Co 2 O 3 , and NiO; the polymer dewaxing agent 200 includes High molecular polymers with non-polar groups and polar groups in the molecule, including homopolymers and copolymers; the molecular weight of the polymer dewaxing agent 200 is between 4,000 and 100,000; the non-polar group The groups include long-chain alkyl groups, and the polar groups include ester groups, ketone groups, amino groups, amido groups, and sulfur groups.
在本实施方式中,采用纳米磁性内核外周包裹聚合物脱蜡剂的结构能够使聚合物脱蜡剂与原油更好的接触,提高脱蜡效果。而具有磁性的所述磁性脱蜡剂可通过外加磁场进行分离,且不必采用离心等分离操作就能将脱蜡后的原油与析出的蜡及剩余的脱蜡剂分离,不仅简化脱蜡流程且有利于降低脱蜡成本。In this embodiment, the polymer dewaxing agent is wrapped around the outer periphery of the nano-magnetic core, so that the polymer dewaxing agent can better contact with the crude oil and improve the dewaxing effect. The magnetic dewaxing agent with magnetism can be separated by an external magnetic field, and the dewaxed crude oil can be separated from the precipitated wax and the remaining dewaxing agent without using separation operations such as centrifugation, which not only simplifies the dewaxing process and It is beneficial to reduce the cost of dewaxing.
在一个实施方式中,所述磁性纳米颗粒100为球形磁性纳米颗粒。所述磁性纳米颗粒100的粒径为5-50nm,如,5nm、10nm、20nm、30nm、40nm或50nm,且随着所述磁性纳米颗粒100的粒径减小,所述磁性纳米颗粒100的比表面积越大。为给所述聚合物脱蜡剂200提供更大的容置空间,且保证所述聚合物脱蜡剂200能够充分伸展而发挥脱蜡作用,所述磁性纳米颗粒100的粒径为30nm。In one embodiment, the magnetic nanoparticles 100 are spherical magnetic nanoparticles. The particle size of the magnetic nanoparticles 100 is 5-50nm, such as 5nm, 10nm, 20nm, 30nm, 40nm or 50nm, and as the particle size of the magnetic nanoparticles 100 decreases, the magnetic nanoparticles 100 The larger the specific surface area. In order to provide a larger accommodation space for the polymer dewaxing agent 200 and ensure that the polymer dewaxing agent 200 can fully stretch to perform the dewaxing effect, the particle diameter of the magnetic nanoparticles 100 is 30 nm.
在一个实施方式中,所述磁性纳米颗粒100与所述聚合物脱蜡剂200通过溶液共混或熔融共混的方式复合在一起。采用溶液共混或熔融共混的方式都能使所述聚合物脱蜡剂200包覆在所述磁性纳米颗粒100外周,从而得到所述磁性脱蜡剂。为减少溶剂的使用以及所述磁性纳米颗粒100与所述聚合物脱蜡剂200之间更强的相互作用,所述磁性纳米颗粒100与所述聚合物脱蜡剂200通过熔融共混的方式复合在一起。In one embodiment, the magnetic nanoparticles 100 and the polymer dewaxing agent 200 are composited together by solution blending or melt blending. The polymer dewaxing agent 200 can be coated on the outer periphery of the magnetic nanoparticles 100 by solution blending or melt blending, so as to obtain the magnetic dewaxing agent. In order to reduce the use of solvents and achieve a stronger interaction between the magnetic nanoparticles 100 and the polymer dewaxing agent 200, the magnetic nanoparticles 100 and the polymer dewaxing agent 200 are melt-blended Composite together.
在一个实施方式中,所述聚合物脱蜡剂包括聚丙烯酸高碳醇酯和/或聚乙烯-醋酸乙烯酯。采用聚丙烯酸高碳醇酯和/或聚乙烯-醋酸乙烯酯作为聚合物脱蜡剂能够与所述磁性纳米颗粒密切配合,避免在使用的过程中,所述磁性脱蜡剂中的所述聚合物脱蜡剂与所述磁性纳米颗粒分离。为获得较好的脱蜡效果,所述聚合物脱蜡剂为聚丙烯酸高碳醇酯和聚乙烯-醋酸乙烯酯的混合物。当然,根据待脱蜡原油的特点,可以选择不同的聚合物脱蜡剂或聚合物脱蜡剂的组合。In one embodiment, the polymeric dewaxing agent comprises polyacrylic acid higher alcohol ester and/or polyethylene-vinyl acetate. Using polyacrylic high carbon alcohol ester and/or polyethylene-vinyl acetate as the polymer dewaxing agent can closely cooperate with the magnetic nanoparticles, avoiding the polymerization in the magnetic dewaxing agent during use The dewaxing agent is separated from the magnetic nanoparticles. In order to obtain a better dewaxing effect, the polymer dewaxing agent is a mixture of polyacrylic high carbon alcohol ester and polyethylene-vinyl acetate. Of course, according to the characteristics of the crude oil to be dewaxed, different polymer dewaxing agents or combinations of polymer dewaxing agents can be selected.
为解决上述技术问题,本发明还提供了一种磁性脱蜡方法。In order to solve the above technical problems, the present invention also provides a magnetic dewaxing method.
请参考图2,图2是本发明一种磁性脱蜡方法较佳实施例的流程示意图,所述方法包括步骤:Please refer to Fig. 2, Fig. 2 is a schematic flow diagram of a preferred embodiment of a magnetic dewaxing method of the present invention, the method includes steps:
S100、提供预设质量的磁性脱蜡剂。S100, provide preset quality magnetic dewaxing agent.
在所述步骤S100中,所述磁性脱蜡剂包括磁性纳米颗粒和包覆在所述磁性纳米颗粒外周的聚合物脱蜡剂;所述磁性纳米颗粒包括Fe3O4、γ-Fe2O3、Co2O3、NiO中的一种或两种及以上的组合;所述聚合物脱蜡剂包括分子中带有非极性基团和极性基团的高分子聚合物,包括均聚物和共聚物;所述聚合物脱蜡剂分子量在4000~100000之间;所述非极性基团包括长链烷基,所述极性基团包括酯基、酮基、氨基、酰胺基、硫基。In the step S100, the magnetic dewaxing agent includes magnetic nanoparticles and a polymer dewaxing agent coated on the outer periphery of the magnetic nanoparticles; the magnetic nanoparticles include Fe 3 O 4 , γ-Fe 2 O 3. One or a combination of two or more of Co 2 O 3 and NiO; the polymer dewaxing agent includes high molecular polymers with non-polar groups and polar groups in the molecule, including homogeneous Polymers and copolymers; the molecular weight of the polymer dewaxing agent is between 4,000 and 100,000; the non-polar groups include long-chain alkyl groups, and the polar groups include ester groups, ketone groups, amino groups, and amides base, sulfur base.
由于纳米磁性内核外周包裹聚合物脱蜡剂的结构能够使聚合物脱蜡剂与原油更好的接触,提高脱蜡效果。而具有磁性的所述磁性脱蜡剂可通过外加磁场进行分离,且不必采用离心等分离操作就能将脱蜡后的原油与析出的蜡及剩余的脱蜡剂分离,不仅简化脱蜡流程且有利于降低脱蜡成本。Due to the structure of the polymer dewaxing agent wrapped around the nano-magnetic inner core, the polymer dewaxing agent can better contact the crude oil and improve the dewaxing effect. The magnetic dewaxing agent with magnetism can be separated by an external magnetic field, and the dewaxed crude oil can be separated from the precipitated wax and the remaining dewaxing agent without using separation operations such as centrifugation, which not only simplifies the dewaxing process and It is beneficial to reduce the cost of dewaxing.
进一步的,所述磁性纳米颗粒为球形磁性纳米颗粒。所述磁性纳米颗粒100的粒径为5-50nm,如,5nm、10nm、20nm、30nm、40nm或50nm,且随着所述磁性纳米颗粒的粒径减小,单位质量的所述磁性纳米颗粒的比表面积越大。为给所述聚合物脱蜡剂提供更大的容置空间,且保证所述聚合物脱蜡剂能够充分伸展而发挥脱蜡作用,所述磁性纳米颗粒的粒径为30nm。Further, the magnetic nanoparticles are spherical magnetic nanoparticles. The particle diameter of the magnetic nanoparticles 100 is 5-50nm, such as 5nm, 10nm, 20nm, 30nm, 40nm or 50nm, and as the particle diameter of the magnetic nanoparticles decreases, the magnetic nanoparticles per unit mass The larger the specific surface area. In order to provide the polymer dewaxing agent with a larger accommodating space and ensure that the polymer dewaxing agent can be fully stretched to perform the dewaxing effect, the particle diameter of the magnetic nanoparticles is 30 nm.
进一步的,所述磁性纳米颗粒与所述聚合物脱蜡剂通过溶液共混或熔融共混的方式复合在一起。采用溶液共混或熔融共混的方式都能使所述聚合物脱蜡剂包覆在所述磁性纳米颗粒外周,从而得到所述磁性脱蜡剂。为减少溶剂的使用,所述磁性纳米颗粒与所述聚合物脱蜡剂通过熔融共混的方式复合在一起。Further, the magnetic nanoparticles and the polymer dewaxing agent are compounded together by solution blending or melt blending. The polymer dewaxing agent can be coated on the outer periphery of the magnetic nanoparticles by solution blending or melt blending, thereby obtaining the magnetic dewaxing agent. In order to reduce the use of solvent, the magnetic nanoparticles and the polymer dewaxing agent are compounded together by melt blending.
更进一步的,所述聚合物脱蜡剂包括聚丙烯酸高碳醇酯和/或聚乙烯-醋酸乙烯酯。采用聚丙烯酸高碳醇酯和/或聚乙烯-醋酸乙烯酯作为聚合物脱蜡剂能够与所述磁性纳米颗粒密切配合,避免在使用的过程中,所述磁性脱蜡剂中的所述聚合物脱蜡剂与所述磁性纳米颗粒分离。为获得较好的脱蜡效果,所述聚合物脱蜡剂为聚丙烯酸高碳醇酯和聚乙烯-醋酸乙烯酯的混合物。当然,根据待脱蜡原油的特点,可以选择不同的聚合物脱蜡剂或聚合物脱蜡剂的组合。Furthermore, the polymer dewaxing agent includes polyacrylic high carbon alcohol ester and/or polyethylene-vinyl acetate. Using polyacrylic high carbon alcohol ester and/or polyethylene-vinyl acetate as the polymer dewaxing agent can closely cooperate with the magnetic nanoparticles, avoiding the polymerization in the magnetic dewaxing agent during use The dewaxing agent is separated from the magnetic nanoparticles. In order to obtain a better dewaxing effect, the polymer dewaxing agent is a mixture of polyacrylic high carbon alcohol ester and polyethylene-vinyl acetate. Of course, according to the characteristics of the crude oil to be dewaxed, different polymer dewaxing agents or combinations of polymer dewaxing agents can be selected.
S200、将所述预设质量的磁性脱蜡剂与预设质量的待处理油品混合,得到混合物。S200. Mix the preset mass of magnetic dewaxing agent with the preset mass of oil to be treated to obtain a mixture.
在所述步骤S200中,采用机械搅拌或磁力搅拌的方式将所述预设质量的磁性脱蜡剂与预设质量的待处理油品混合,得到混合物。进一步地的,当所述预设质量的待处理油品为100g时,所述预设质量的磁性脱蜡剂为5-20mg,也即所述磁性脱蜡剂与所述待处理油品的质量比为50-200mg/Kg,如,50mg/Kg、100mg/Kg、150mg/Kg或200mg/Kg等。由于所述聚合物脱蜡剂包覆在所述磁性纳米颗粒外周,所述磁性脱蜡剂能够更好的与所述待处理油品混合并发挥脱蜡作用,处理相同质量的所述待处理油品,所述磁性脱蜡剂中含有的聚合物脱蜡剂的量小于单独使用聚合物脱蜡剂时的用量,有利于降低脱蜡成本。In the step S200, the predetermined mass of magnetic dewaxing agent is mixed with the predetermined mass of oil to be treated by means of mechanical stirring or magnetic stirring to obtain a mixture. Further, when the preset quality of the oil to be treated is 100g, the preset quality of the magnetic dewaxing agent is 5-20mg, that is, the ratio of the magnetic dewaxing agent to the oil to be treated is The mass ratio is 50-200 mg/Kg, such as 50 mg/Kg, 100 mg/Kg, 150 mg/Kg or 200 mg/Kg. Since the polymer dewaxing agent is coated on the outer periphery of the magnetic nanoparticles, the magnetic dewaxing agent can better mix with the oil to be treated and exert a dewaxing effect, and treat the same quality of the untreated oil For oil products, the amount of the polymer dewaxing agent contained in the magnetic dewaxing agent is less than the amount when the polymer dewaxing agent is used alone, which is beneficial to reduce the cost of dewaxing.
S300、对所述混合物进行降温至预设温度及以下,使所述待处理油品中的蜡在所述磁性脱蜡剂表面生成,得到包括析出蜡的磁性脱蜡剂。S300, cooling the mixture to a preset temperature or below, so that the wax in the oil to be treated is generated on the surface of the magnetic dewaxing agent to obtain a magnetic dewaxing agent including precipitated wax.
在所述步骤S300中,在持续搅拌的条件下,将混合物降温至预设温度以下,使得待处理油品中的蜡在所述磁性脱蜡剂表面生成。在一个实施方式中,所述预设温度可以是0-18℃,如,0℃、5℃、10℃、15℃或18℃等,降低温度有利于蜡的析出。而对于不同种类的待处理油品,如,形成环境不同的待处理油品或含水量等组成不同的待处理油品,其在相同的温度下蜡的析出情况不同,因此,为获得更好的脱蜡效果,所述预设温度为所述待处理油品的析蜡点。将所述混合物温度将至对应的所述待处理油品的析蜡点或以下,能够快速高效的脱除待处理油品中的蜡。In the step S300, under the condition of continuous stirring, the temperature of the mixture is lowered to below the preset temperature, so that the wax in the oil to be treated is generated on the surface of the magnetic dewaxing agent. In one embodiment, the preset temperature may be 0-18°C, such as 0°C, 5°C, 10°C, 15°C or 18°C, etc. Lowering the temperature is beneficial to the precipitation of wax. And for different types of oil products to be treated, such as oil products to be treated with different formation environments or oil products to be treated with different compositions such as water content, the precipitation of wax is different under the same temperature. Therefore, in order to obtain better The dewaxing effect, the preset temperature is the waxing point of the oil to be treated. Lowering the temperature of the mixture to or below the waxing point of the corresponding oil to be treated can quickly and efficiently remove the wax in the oil to be treated.
S400、对所述混合物施加磁场,使所述磁性脱蜡剂析出。S400, applying a magnetic field to the mixture to precipitate the magnetic dewaxing agent.
在所述步骤S400中,由于所述磁性脱蜡剂具有磁性内核,可以通过施加磁场的方式将所述磁性脱蜡剂与所述待处理油品进行分离。当然,分离出的所述磁性脱蜡剂中至少部分为包括析出蜡的磁性脱蜡剂。进一步的,所述磁场来自永磁体或电磁铁。为降低生产成本及简化工艺,所述磁场来自永磁体。In the step S400, since the magnetic dewaxing agent has a magnetic inner core, the magnetic dewaxing agent can be separated from the oil to be treated by applying a magnetic field. Of course, at least part of the separated magnetic dewaxing agent is the magnetic dewaxing agent including the precipitated wax. Further, the magnetic field comes from a permanent magnet or an electromagnet. In order to reduce the production cost and simplify the process, the magnetic field comes from a permanent magnet.
进一步的,由于磁场的作用,所述磁性脱蜡剂不能随液体的流动而流出,可通过简单的倾倒,将脱蜡后的所述待处理油品与所述磁性脱蜡剂进行分离。为获得较高分离效率,对所述混合物施加磁场,使所述磁性脱蜡剂析出之后还包括:对所述混合物进行过滤,将包括析出蜡的磁性脱蜡剂从所述混合物中分离出来。Further, due to the effect of the magnetic field, the magnetic dewaxing agent cannot flow out with the flow of the liquid, and the dewaxed oil to be treated can be separated from the magnetic dewaxing agent by simple pouring. In order to obtain higher separation efficiency, after applying a magnetic field to the mixture to precipitate the magnetic dewaxing agent, the method further includes: filtering the mixture, and separating the magnetic dewaxing agent including the precipitated wax from the mixture.
在另一个实施方式中,所述对所述混合物进行降温至预设温度之前还包括:将所述混合加热至50-80℃,并采用机械搅拌的方式搅拌0.2-1h。采用搅拌和升温的方式有利于所述磁性脱蜡剂与所述待处理油品进行充分混合,有利于将所述待处理油品中蜡的充分脱除。In another embodiment, before cooling the mixture to a preset temperature, it further includes: heating the mixture to 50-80° C., and stirring for 0.2-1 h by means of mechanical stirring. The method of stirring and heating is beneficial to the thorough mixing of the magnetic dewaxing agent and the oil to be treated, and the full removal of wax in the oil to be treated.
下面结合实施例对本发明的技术方案进行进一步阐述,在下述实施中,处理方式为机械搅拌,降温至析蜡点后,待析出的蜡质量不再增加后,将析出的蜡按照上述方法分离,计算脱蜡率,所述脱蜡率为析出的蜡的质量与测得的该种原油的蜡含量的比值。The technical solution of the present invention is further described below in conjunction with the examples. In the following implementation, the treatment method is mechanical stirring. After cooling down to the wax precipitation point, after the quality of the precipitated wax no longer increases, the precipitated wax is separated according to the above method. Calculate the dewaxing rate, which is the ratio of the mass of the precipitated wax to the measured wax content of the crude oil.
表1采用200mg脱蜡剂对1Kg胜利原油进行脱蜡的效果对比表Table 1 uses 200mg dewaxing agent to carry out the comparison table of the effect of dewaxing 1Kg Shengli crude oil
从表1中可以看出,在脱蜡剂种类和用量相同的条件下,采用磁性脱蜡的方式能够提高脱蜡率。也即达到相同的脱蜡率,采用磁性脱蜡可以减少脱蜡剂的用量,有利于降低点成本。It can be seen from Table 1 that under the same type and amount of dewaxing agent, the magnetic dewaxing method can improve the dewaxing rate. That is to say, to achieve the same dewaxing rate, the use of magnetic dewaxing can reduce the amount of dewaxing agent, which is beneficial to reduce the point cost.
表2采用200mg脱蜡剂对1Kg塔里木原油进行脱蜡的效果对比表Table 2 adopts 200mg dewaxing agent to carry out the comparison table of the effect of dewaxing 1Kg Tarim crude oil
对比表1和表2可知,当聚合物脱蜡剂用量相同时,采用不同脱蜡剂的组合能够进一步提高脱蜡效果。也即,针对同一种待处理原油,选择相应的脱蜡剂能够进一步提高脱蜡效果。Comparing Table 1 and Table 2, it can be seen that when the amount of polymer dewaxing agent is the same, the combination of different dewaxing agents can further improve the dewaxing effect. That is, for the same crude oil to be treated, selecting the corresponding dewaxing agent can further improve the dewaxing effect.
表3采用100mg脱蜡剂对1Kg胜利原油进行脱蜡的效果对比表Table 3 uses 100mg dewaxing agent to carry out the comparison table of the effect of dewaxing 1Kg Shengli crude oil
对比表1和表3可知,处理相同质量的待处理原油,增加脱蜡剂的用量有利于脱蜡率的提高。Comparing Table 1 and Table 3, it can be seen that increasing the amount of dewaxing agent is beneficial to improve the dewaxing rate when treating the same quality crude oil to be treated.
表4采用100mg脱蜡剂对1Kg塔里木原油进行脱蜡的效果对比表Table 4 adopts 100mg dewaxing agent to carry out the comparison table of the effect of dewaxing 1Kg Tarim crude oil
同理,比较表2和表4可知,处理相同质量的待处理原油,增加脱蜡剂的用量有利于脱蜡率的提高。Similarly, comparing Table 2 and Table 4, it can be seen that increasing the amount of dewaxing agent is beneficial to the improvement of dewaxing rate when treating the crude oil to be treated with the same quality.
通过上述实施例对比可知,与单独使用脱蜡剂相比,本发明的磁性脱蜡剂能够有效提高脱蜡率,有利于进一步降低脱蜡成本。Through the comparison of the above examples, it can be seen that compared with using the dewaxing agent alone, the magnetic dewaxing agent of the present invention can effectively increase the dewaxing rate, which is beneficial to further reduce the dewaxing cost.
综上所述,本发明公开了一种磁性脱蜡剂及磁性脱蜡方法,所述磁性脱蜡剂包括,磁性纳米颗粒和包覆在所述磁性纳米颗粒外周的聚合物脱蜡剂;所述磁性纳米颗粒包括Fe3O4、γ-Fe2O3、Co2O3、NiO中的一种或两种及以上的组合;所述聚合物脱蜡剂包括分子中带有非极性基团和极性基团的高分子聚合物,包括均聚物和共聚物;所述聚合物脱蜡剂分子量在4000~100000之间;所述非极性基团包括长链烷基,所述极性基团包括酯基、酮基、氨基、酰胺基、硫基。通过上述方式,本发明能够简化脱蜡过程并降低脱蜡成本。In summary, the present invention discloses a magnetic dewaxing agent and a magnetic dewaxing method. The magnetic dewaxing agent includes magnetic nanoparticles and a polymer dewaxing agent coated on the outer periphery of the magnetic nanoparticles; The magnetic nanoparticles include one or a combination of two or more of Fe 3 O 4 , γ-Fe 2 O 3 , Co 2 O 3 , and NiO; the polymer dewaxing agent includes a non-polar The macromolecular polymers of groups and polar groups, including homopolymers and copolymers; the molecular weight of the polymer dewaxing agent is between 4,000 and 100,000; the non-polar groups include long-chain alkyl groups, so The polar groups include ester groups, ketone groups, amino groups, amido groups, and thio groups. Through the above method, the present invention can simplify the dewaxing process and reduce the cost of dewaxing.
应当理解的是,本发明的应用不限于上述的举例,对本领域普通技术人员来说,可以根据上述说明加以改进或变换,所有这些改进和变换都应属于本发明所附权利要求的保护范围。It should be understood that the application of the present invention is not limited to the above examples, and those skilled in the art can make improvements or transformations according to the above descriptions, and all these improvements and transformations should belong to the protection scope of the appended claims of the present invention.
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CN103339234A (en) * | 2011-02-09 | 2013-10-02 | 赢创油品添加剂有限公司 | Method for dewaxing mineral oil compositions |
CN105112090A (en) * | 2015-09-06 | 2015-12-02 | 中国石油天然气股份有限公司 | Oil wax separating agent, preparation method thereof and oil wax separating method |
CN105152841A (en) * | 2015-09-25 | 2015-12-16 | 中北大学 | Low-temperature-freezing magnetic separation method and device for long-chain alkene and long-chain alkane mixture |
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CN111394394A (en) * | 2020-03-16 | 2020-07-10 | 江苏省环科院环境科技有限责任公司 | Process for producing hydrogen and ethanol by degrading lignocellulose |
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