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CN104262602B - A kind of arylalkyl carboxylic acids's polyoxyethylene polyoxypropylene block copolymer and its preparation method and application - Google Patents

A kind of arylalkyl carboxylic acids's polyoxyethylene polyoxypropylene block copolymer and its preparation method and application Download PDF

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CN104262602B
CN104262602B CN201410466418.1A CN201410466418A CN104262602B CN 104262602 B CN104262602 B CN 104262602B CN 201410466418 A CN201410466418 A CN 201410466418A CN 104262602 B CN104262602 B CN 104262602B
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acid
carboxylic acids
arylalkyl
block copolymer
arylalkyl carboxylic
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CN104262602A (en
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刘春德
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DALIAN DONGFANG INNOVATION SCIENCE & TECHNOLOGY Co Ltd
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DALIAN DONGFANG INNOVATION SCIENCE & TECHNOLOGY Co Ltd
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Abstract

The invention discloses a kind of arylalkyl carboxylic acids's polyoxyethylene polyoxypropylene block copolymer and there is logical structure shown in formula I, preparation method is alkene-carboxylic acid to be alkylated with aromatic hydrocarbon, obtain arylalkyl carboxylic acids, arylalkyl carboxylic acids is carried out ring-opening reaction with expoxy propane, obtain arylalkyl carboxylic acids's polyoxypropylene ester, arylalkyl carboxylic acids's polyoxypropylene ester carries out ethoxylation with oxirane again, obtains arylalkyl carboxylic acids's polyoxyethylene polyoxypropylene block copolymer.Arylalkyl carboxylic acids's polyoxyethylene polyoxypropylene block copolymer, can be used for residual oil emulsification, the field such as prepared by reducing thick oil viscosity, heavy oil pour point depression, nanoemulsions, tertiary oil recovery, daily-use chemical industry.

Description

A kind of arylalkyl carboxylic acids's polyoxyethylene polyoxypropylene block copolymer and its preparation method and application
Technical field
The present invention relates to a kind of arylalkyl carboxylic acids's polyoxyethylene polyoxypropylene block copolymer and preparation method thereof and answer With.
Background technology
Fatty acid polyglycol oxypropylene polyoxyethylene block copolymer is the nonionic surfactant that a class is novel, owing to using Polyoxyethylene polyoxypropylene block copolymeric structure so that it is use as emulsifying agent and have solely in fields such as oil exploitations Special application performance.
The direct-connected alkyl structure of fatty acid polyglycol oxypropylene polyoxyethylene block copolymer with have alkane, aromatic hydrocarbons, colloid with The performance of crude oils difference of asphalitine component is relatively big, and therefore, some performance indications is the most unsatisfactory.
Generally the chemical constituent of crude oil is alkane, aromatic hydrocarbon, resin and asphalt.Daqing crude oil and China are listed below The fractional composition of some crude oil, is shown in Tables 1 and 2.
Table 1 Daqing oil field crude oil forms
Some crude oil fractional compositions of table 2 China
There is the carboxylic acid polyoxyethylene polyoxypropylene block copolymer of aryl alkyl structure, at crude oil, viscous crude, residual oil The aspect performances such as emulsification, viscosity reduction, pour point depression can be more outstanding, simultaneously in fields such as tertiary oil recovery, low permeability oil field exploitations Also it is with a wide range of applications.
Summary of the invention
The purpose of the present invention aims to provide a kind of arylalkyl carboxylic acids's polyoxyethylene polyoxypropylene block copolymer, has logical Structure shown in formula I:
Wherein: m+n is 0,1,2 ... 28,29,30 positive integers;
P is 1,2 ... 4998,4999,5000 positive integers;
Q is 0,1,2 ... 4998,4999,5000 positive integers;
R is phenyl, tolyl, meta-xylene base, paraxylene base, ortho-xylene base, ethylbenzene, n-propylbenzene Base, isopropyl phenyl, n-butylphenyl, isobutyl phenenyl, tert-butyl-phenyl, naphthyl, methyl naphthyl, dimethyl Naphthyl, ethyl naphthyl, propyl group naphthyl, butyl naphthyl, xenyl, the one in phenylol.
Further, in technique scheme, m+n is preferably the positive integer of 8,15,19, and more preferably 15,
Further, in technique scheme, p is preferably 5,6 ... 49,50 positive integers,
Further, in technique scheme, q is preferably 5,6 ... 49,50 positive integers,
Further, in technique scheme, R is preferably meta-xylene.
Another object of the present invention is to provide the preparation of above-mentioned arylalkyl carboxylic acids's polyoxyethylene polyoxypropylene block copolymer Method, technical scheme is:
Under acidic catalyst effect, alkene-carboxylic acid is alkylated with aromatic hydrocarbon, obtains arylalkyl carboxylic acids;
Again arylalkyl carboxylic acids is carried out ring-opening reaction with expoxy propane under acidity or base catalyst effect, obtain virtue Base alkyl carboxylic acid polyoxypropylene ester, arylalkyl carboxylic acids's polyoxypropylene ester again with oxirane at acid or base catalyst Carry out ethoxylation under effect, obtain arylalkyl carboxylic acids's polyoxyethylene polyoxypropylene block copolymer;
Further, in technique scheme, the preparation of present invention acidic catalyst used by arylalkyl carboxylic acids, For sulfuric acid, hydrofluoric acid, pyrovinic acid, TFMS, metal salts of trifluoromethane sulphonic acid or load TFMS root, Any one or a few mixture in heteropoly acid, solid super-strong acid, acid zeolite, perfluorinated resin, ionic liquid, The preferably TFMS root of pyrovinic acid, metal salts of trifluoromethane sulphonic acid or load, more preferably pyrovinic acid.
Further, in technique scheme, acidic catalyst used by ring-opening reaction or ethylation reaction is selected from BF3、 SbCI5、SnCI4, solid acid, heteropoly acid, one in carried molecular sieve catalyst, base catalyst used selects From potassium hydroxide, NaOH, sodium methoxide, caustic alcohol, Mg/AI composite oxides (MAO), the oxide of barium Compound with phosphoric acid with hydroxide, aluminum alkoxide sulfonate, rare metal alcoxyl sulfate, alkaline earth oxide One in thing, preferably potassium hydroxide, sodium methoxide, Mg/AI composite oxides (MAO).
Further, in technique scheme, alkene-carboxylic acid of the present invention, for undecenoic acid: CH2=CH (CH2)8COOH, oleic acid: CH3(CH2)7CH=CH (CH2)7COOH, erucic acid: cis -13-docosenoic acid, preferably oleic acid.
Further, in technique scheme, aromatic hydrocarbon of the present invention, for benzene, toluene, meta-xylene, Paraxylene, ortho-xylene, ethylbenzene, n-propylbenzene, cumene, n-butylbenzene, isobutyl-benzene, tert-butyl benzene, Naphthalene, methyl naphthalene, dimethylnaphthalene, ethylnaphthalene, propyl group naphthalene, dibutyl naphthalene, biphenyl, the one in phenol, preferably between two Toluene.
Further, in technique scheme, pyrovinic acid as catalyst, alkene-carboxylic acid and aromatic hydrocarbon mole Ratio is 1:1.5-3.5, reaction temperature 100-135 DEG C, drips alkene-carboxylic acid, and then reaction 5 hours, are washed to pH value Neutrality, short-path distillation removes unreacted raw material and saturated acid therein, obtains arylalkyl carboxylic acids.Described alkene-carboxylic acid It is 1:1.15-2.0 with the mol ratio of pyrovinic acid.
Further, in technique scheme, arylalkyl carboxylic acids of the present invention and opening that expoxy propane is carried out Ring reacts, and preferred aryl groups alkyl carboxylic acid and expoxy propane mol ratio are the reaction of 1:5~50.
Further, arylalkyl carboxylic acids's polyoxypropylene ester of the present invention is anti-with the ethoxylation that oxirane is carried out Should, preferred aryl groups alkyl carboxylic acid polyoxypropylene ester with molar than the reaction for 1:5~50.
The beneficial outcomes of the present invention is:
1. arylalkyl carboxylic acids's group of the present invention and oxypropylene block are oil-soluble, have the strongest with former The energy that mixes of oil, viscous crude, residual oil etc., by controlling to access the size of ethylene oxide block, can control aryl alkyl carboxylic The hydrophil lyophil balance of acid polyoxyethylene polyoxypropylene block, is widely used in residual oil emulsification, reducing thick oil viscosity, crude oil breast The fields such as change;
2. arylalkyl carboxylic acids's polyoxyethylene polyoxypropylene block copolymer of the present invention, for the nonionic that molecular weight is bigger Type surfactant, has the effect of thickening under finite concentration, can be used for improving oil recovery factor, especially weak Use under alkali and alkali-free system, have thickening, solubilising, emulsify, the effect such as wetting;
3. arylalkyl carboxylic acids's polyoxyethylene polyoxypropylene block copolymer preparation method conversion ratio of the present invention is high, is suitable for Industrialization produces.
Accompanying drawing explanation
Accompanying drawing 3 width of the present invention,
Fig. 1 is the infrared spectrogram of the meta-xylene base octadecane carboxylic acid that embodiment 1 prepares;
Fig. 2 is meta-xylene base octadecane carboxylic acid polyoxypropylene (15) the ester flight time mass spectrum that embodiment 1 prepares Figure;
Fig. 3 is that meta-xylene base octadecane carboxylic acid polyoxypropylene (15) polyoxyethylene (15) that embodiment 1 prepares is embedding Section copolymer flight time mass spectrum figure.
Detailed description of the invention
The present invention is further illustrated below in conjunction with embodiment, but not as a limitation of the invention.
Embodiment 1:
Friedel-Crafts alkylation:
Equipped with agitator, thermometer, constant voltage dropper, condenser 1000ml reaction bulb in, between putting into 248 grams two Toluene (AR), 112 grams of pyrovinic acids (AR), be warming up to 125~130 DEG C, and (oleic acid contains to drip high-purity oleic acid Amount >=75%) 220 grams, time for adding is 5 hours, continues reaction 2 hours.Cooling, is washed to pH value neutral, The meta-xylene of Rotary Evaporators removing excess, molecular clock decolours, obtains meta-xylene base octadecane carboxylic acid.Liquid phase look Analysis of spectrum oleic acid conversion >=90%.
Meta-xylene base octadecane carboxylic acid infrared spectrogram is shown in Fig. 1.
1412cm in FIG-1(carboxylic acid O-H flexural vibrations), 1710cm-1(carboxylic acid C=O stretching vibration);725cm-1 (a disubstituted C-H out-of-plane bending vibration), 1047cm-1(aromatic hydrocarbons C-H in-plane bending vibration), 1459cm-1 (aromatic hydrocarbons C=C stretching vibration);2853cm-1(CH2 alkane symmetrical stretching vibration), 2925cm-1(CH2 alkane Antisymmetric stretching vibration).
Ring-opening reaction:
Weigh 116 grams of meta-xylene base octadecane carboxylic acids and 1.5 grams of Mg/AI composite oxides (MAO) put into 1 liter In synthesis reactor, synthesis reactor is sealed, replace 3 times with nitrogen.Start stirring, be warming up to 140 DEG C, start vavuum pump Vacuumize, stop when being warming up to 170 DEG C vacuumizing.Open inlet valve, with nitrogen by storage tank 261.36 grams of epoxies third Alkane is gradually pressed in reactor, control reaction temperature at 140 DEG C~180 DEG C, pressure≤0.15MPa, react 5 hours. Cooling, discharging, filter, remove catalyst, obtain meta-xylene base octadecane carboxylic acid polyoxypropylene (15) ester.
Meta-xylene base octadecane carboxylic acid polyoxypropylene (15) ester flight time mass spectrum figure is shown in Fig. 2.
It is the normal distribution of polyoxypropylene structure distribution in fig. 2, owing to this experiment used catalyst is that Mg/AI is multiple Close oxide (MAO), embody the feature of narrow ditribution.
Ethylation reaction:
Weigh 252 grams of meta-xylene base octadecane carboxylic acid polyoxypropylene (15) esters and 1.5 grams of sodium methoxides put into 1 liter of conjunction Become in still, synthesis reactor is sealed, replace 3 times with nitrogen.Start stirring, be warming up to 130 DEG C, start vacuum pumping Vacuum, stops when being warming up to 160 DEG C vacuumizing.Open inlet valve, with nitrogen by storage tank 133 grams of oxirane by Gradually press-in reactor in, control reaction temperature at 130 DEG C~170 DEG C, pressure≤0.15MPa, react 6 hours.Fall Temperature, discharging, obtain meta-xylene base octadecane carboxylic acid polyoxypropylene (15) polyoxyethylene (15) block copolymer.
Meta-xylene base octadecane carboxylic acid polyoxypropylene (15) polyoxyethylene (15) block copolymer flight time mass spectrum Figure is shown in Fig. 3.
We have seen that on the basis of meta-xylene base octadecane carboxylic acid polyoxypropylene (15) ester at Fig. 3, add ring Oxidative ethane (15EO), obtains extremely complex flight time mass spectrum figure, this is because in gathering in normal distribution state In oxypropylene structure, each structure all may result in extremely complex structure divide plus the oxirane of normal distribution Cloth form.
Application examples 1
The application in tertiary oil recovery of the arylalkyl carboxylic acids's polyoxyethylene polyoxypropylene block copolymer of the present invention:
Composition components and content:
Erucyl amide propyl group carboxybetaine (from synthesis) 0.20%
Meta-xylene base octadecane carboxylic acid polyoxypropylene (15) polyoxyethylene (15) ester 0.15%
Remaining is water.
Erucyl amide propyl group carboxybetaine therein is with erucyl amide propyl group tertiary amine and sodium chloroacetate proportioning as 1:1.1 (mol ratio), 100 DEG C of methyl alcohol make solvent, carry out quaternary ammonium reaction 8 hours, and separating methanol obtains product.
Using grand celebration to recover the oil ten factory's crude oil and simulate water, the interfacial tension of test system is 5.63x10-3MN/m, system Viscosity is 18.6mPa.s.
Meta-xylene base octadecane carboxylic acid polyoxypropylene (15) polyoxyethylene (15) ester solubilising erucyl amide propyl group carboxyl Glycine betaine, interfacial tension reaches ultralow;Thickening binary system, has certain viscosity in the case of being not added with polymer; And play emulsification.
Natural core oil displacement experiment enters according to People's Republic of China's oil and gas industry standard SY/T6424-2000 OK.Experiment oil is grand celebration ten factory simulated oil, and experimental water is that water is simulated by grand celebration ten factory.When water drive to aqueous 100% Time inject the formula system of above-mentioned composition of 0.7 times of pore volume (PV), then when carrying out water drive to aqueous 100% Terminate.
Natural core parameter is as shown in table 3:
The natural core parameter of table 3. composite formula system
Composite formula system is utilized to carry out natural core oil displacement experiment result as shown in table 4:
The oil displacement experiment result of table 4. composite formula system
Conclusion: erucyl amide propyl group carboxybetaine reaches ultralow with the interfacial tension of profit, but only with surfactant Uncontrollable mobility itself, simultaneously because the beet alkali surface activator dissolubility of big molecule bad, its effect is also difficult To play.Meta-xylene base octadecyl carboxylic acid polyoxyethylene polyoxypropylene block copolymer, can solubilising glycine betaine table Face activating agent, can viscosify again the aqueous phase with glycine betaine activating agent, plays the purpose controlling mobility, has reached raising former The purpose of oil recovery.
Application examples 2
The application in prepared by microemulsion of the arylalkyl carboxylic acids's polyoxyethylene polyoxypropylene block copolymer of the present invention:
Oil-sand is a kind of sand shape mineral reserve containing crude oil, and main component is pitch, water, clay and gravel, its stock number Huge, account for the 30% of world oil reserves.
Being used in by microemulsion in oil-sand washing oil and will have highly important application prospect, microemulsion directly acts on oil-sand, Normal temperature, it is not necessary to more heat energy, it is possible to decrease cost of winning.
Cetyl hydroxypropyl sulfobetaines therein is 1:1.1 (mol ratio), 125 DEG C of methyl alcohol make solvent, carry out quaternary ammonium reaction 8 hours, and separating methanol obtains product.
Form middle microemulsion phase when profit volume ratio is 1, displacement efficiency is up to 89.6%.

Claims (8)

1. arylalkyl carboxylic acids's polyoxyethylene polyoxypropylene block copolymer, it is characterised in that there is formula I knot Structure:
Wherein, m+n is 0-30 positive integer;
P is 1-5000 positive integer;
Q is 0 or 1-5000 positive integer;
R is phenyl, tolyl, meta-xylene base, paraxylene base, ortho-xylene base, ethylbenzene, n-propylbenzene Base, isopropyl phenyl, n-butylphenyl, isobutyl phenenyl, tert-butyl-phenyl, the one in phenylol.
The preparation side of a kind of arylalkyl carboxylic acids's polyoxyethylene polyoxypropylene block copolymer the most as claimed in claim 1 Method, it is characterised in that comprise the following steps:
1.. the alkylated reaction that alkene-carboxylic acid and aromatic hydrocarbon are carried out under acidic catalyst effect, obtain aryl alkyl carboxylic Acid;
2.. arylalkyl carboxylic acids step 1. obtained again is carried out under acidity or base catalyst effect with expoxy propane Ring-opening reaction, then under acidity or base catalyst effect, carry out ethoxylation with oxirane, obtain aryl alkane Yl carboxylic acid polyoxyethylene polyoxypropylene block copolymer.
Preparation method the most according to claim 2, it is characterised in that: described step 1. middle acidic catalyst is sulphur Acid, hydrofluoric acid, pyrovinic acid, TFMS, metal salts of trifluoromethane sulphonic acid or heteropoly acid, solid super-strong acid, acid Any one or a few in property zeolite, perfluorinated resin, ionic liquid.
Preparation method the most according to claim 2, it is characterised in that described step 2. middle ring-opening reaction or ethyl Change the acidic catalyst of reaction selected from BF3、SbCl5、SnCl4, solid acid, heteropoly acid, carried molecular sieve catalysis One in agent;Base catalyst is selected from potassium hydroxide, NaOH, sodium methoxide, caustic alcohol, Mg/Al composite oxygen Compound, oxide and hydroxide, aluminum alkoxide sulfonate, rare metal alcoxyl sulfate, the alkaline-earth metal oxygen of barium Compound and the one in the compound of phosphoric acid.
Preparation method the most according to claim 2, it is characterised in that: described step 1. middle alkene-carboxylic acid is 11 One or more in olefin(e) acid, oleic acid, erucic acid.
Preparation method the most according to claim 2, it is characterised in that: described step 2. in arylalkyl carboxylic acids with The ring-opening reaction that expoxy propane is carried out, arylalkyl carboxylic acids and expoxy propane mol ratio are the reaction of 1:5~50.
Preparation method the most according to claim 2, it is characterised in that: described step 2. middle arylalkyl carboxylic acids gather The ethoxylation that oxypropylene ester is carried out with oxirane, arylalkyl carboxylic acids's polyoxypropylene ester and molar Ratio is 1:5~50.
8. arylalkyl carboxylic acids's polyoxyethylene polyoxypropylene block copolymer as claimed in claim 1 emulsify at residual oil, Prepared by reducing thick oil viscosity, heavy oil pour point depression, nanoemulsions, tertiary oil recovery, application in daily-use chemical industry.
CN201410466418.1A 2014-09-12 2014-09-12 A kind of arylalkyl carboxylic acids's polyoxyethylene polyoxypropylene block copolymer and its preparation method and application Expired - Fee Related CN104262602B (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108117639A (en) * 2016-11-30 2018-06-05 中国石油天然气股份有限公司 Unsaturated fatty alcohol polyoxypropylene polyoxyethylene block copolymer, and preparation method and application thereof

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108084982B (en) * 2016-11-21 2020-08-21 中国科学院化学研究所 Nano-viscosity pour point depressant stabilized emulsion and preparation method and use thereof
CN107235529B (en) * 2017-06-27 2020-07-03 中国石油化工股份有限公司 Oil removal agent for oil-containing sewage treatment of oil field and preparation method thereof

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103320110A (en) * 2013-06-26 2013-09-25 工合聚能(天津)石油精化科技发展有限公司 Nano composite high-temperature-resistant extraction aid for thickened oil and super-thickened oil recovery and preparation method thereof
CN103641750A (en) * 2013-11-28 2014-03-19 中国石油天然气股份有限公司 Surfactant containing aralkyl hydrophobic chain and amido bond connecting group
CN103865053A (en) * 2012-12-10 2014-06-18 辽宁奥克化学股份有限公司 Terminal alkenyl unsaturated acid/ester polyoxyalkyl ether, and preparation method and use thereof

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4041586B2 (en) * 1998-07-23 2008-01-30 三井化学株式会社 Process for producing polyoxyalkylene polyol

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103865053A (en) * 2012-12-10 2014-06-18 辽宁奥克化学股份有限公司 Terminal alkenyl unsaturated acid/ester polyoxyalkyl ether, and preparation method and use thereof
CN103320110A (en) * 2013-06-26 2013-09-25 工合聚能(天津)石油精化科技发展有限公司 Nano composite high-temperature-resistant extraction aid for thickened oil and super-thickened oil recovery and preparation method thereof
CN103641750A (en) * 2013-11-28 2014-03-19 中国石油天然气股份有限公司 Surfactant containing aralkyl hydrophobic chain and amido bond connecting group

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108117639A (en) * 2016-11-30 2018-06-05 中国石油天然气股份有限公司 Unsaturated fatty alcohol polyoxypropylene polyoxyethylene block copolymer, and preparation method and application thereof

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