CN1013578B - Preparation method of corrosion and scale inhibitor of thiophosphate ester and phosphate ester imidazoline derivatives - Google Patents

Preparation method of corrosion and scale inhibitor of thiophosphate ester and phosphate ester imidazoline derivatives

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Publication number
CN1013578B
CN1013578B CN 87104560 CN87104560A CN1013578B CN 1013578 B CN1013578 B CN 1013578B CN 87104560 CN87104560 CN 87104560 CN 87104560 A CN87104560 A CN 87104560A CN 1013578 B CN1013578 B CN 1013578B
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water soluble
preparation
corrosion
soluble mixt
integer
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CN 87104560
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CN1030263A (en
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马金鼎
王建华
任斐
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DESIGN AND PLANNING RESEARCH INST SHENGLI OILFIELD
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DESIGN AND PLANNING RESEARCH INST SHENGLI OILFIELD
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Abstract

The corrosion and scale inhibitor synthesized by the method is a mixture containing fatty acid and resin acid or a compound of fatty acid and polyamine. The thiophosphate or phosphate imidazoline derivative is used in oil field sewage treatment and reinjection water system, and has obvious corrosion and scale inhibiting effect on steel pipeline and equipment without needing other chemical agent. The corrosion inhibition rate reaches about 80%. The scale inhibition rate reaches 80-100%.

Description

Corrosion-inhibitive and anti-sludge agent compond of derivatives of thiophosphate ester and imidazoline phosphate ester
The present invention is the preparation method who is used for the thiophosphatephosphorothioate of disposing polluted water in oil and re-injection water system and imidazoline phosphate ester derivative corrosion inhibiting and descaling agent.
The present invention according to petroleum department's scientific information research correlation technique is not found in external nearly 10 years relevant Searches of Patent Literature as yet.
Adopt the material of synthetic method of the present invention preparation, be used for disposing polluted water in oil and re-injection water system to the corrosion that slows down steel equipment with prevent to have significant effect at the structures surface scale.
The preparation method of thiophosphatephosphorothioate of the present invention and imidazoline phosphate ester derivative utilizes the technology of preparing of existing tetrahydroglyoxaline to synthesize the compound of tetrahydroglyoxaline type, as example 1 and 2.This compounds is used as inhibiter, and is existing at home and abroad historical for many years, generally all is to adopt lipid acid and polyamines reaction to make.From application facet oil soluble and water-soluble two classes are arranged, the oil soluble tetrahydroglyoxaline is owing in aqueous phase dissolving, bad dispersibility, be difficult for using in water system.Mineral acid such as HCL and organic acid such as the CH of adopting when in water system, using more 3COOH etc. neutralize and make water miscible imidazoline salt, these salt compounds generally are used in acidic medium such as the treatment solutions such as pickling and oil well acidation pressure break, do not see the report that is useful on disposing polluted water in oil and re-injection water system, this compounds does not have the scale inhibition effect yet.
The imidazolidine derivatives that this preparation method makes has inhibition and scale effect.The preparation method of tetrahydroglyoxaline is except that taking lipid acid, the mixture such as the Yatall MA of lipid acid and resin acid have also been adopted, for obtaining water-soluble products, adopted the technological line of addition reaction to synthesize water miscible imidazolinium compounds, for the corrosion mitigating effect that improves this compound and make it have scale effect, again with above-mentioned substance and P 2S 5Or P 2O 5Deng the material effect, made water miscible sulfo-phosphide imidazolidine derivatives at last, its corrosion mitigating effect reaches about 80% in the oxygen-containing water system, and scale inhibition effect reaches 80~100%.With the explanation of preparation procedure example, wherein example 1, example 2 are that prior art, example 3~example 8 are invention technology below.
The preparation procedure example:
Example 1: 0,440 kilogram of (1 mole) Yatall MA and 0.1032 kilogram of (1 mole) polyamines adding are equipped with agitator, in the reaction flask of condenser and water trap.Add an amount of band aqua and bathe the temperature backflow at 150~190 ℃, the theoretical water generation reaction of deviating from more than 85% makes brown dope at last.
Figure 87104560_IMG1
R1 is that the remaining base of lipid acid contains the C atomicity less than 17 in the formula, and R2 is that the remaining base of resinous acid contains the C atomicity less than 21.n=2~4 integers.
Example 2: 0.2825 kilogram of (1 mole) oleic acid and 0.1032 kilogram of (1 mole) polyamines adding are equipped with agitator, in the flask of condenser and water trap, add an amount of band aqua again and bathe temperature at 150 °~190 ℃ and reflux, deviate from the theoretical water generation reaction more than 85% and obtain a brown product.
Figure 87104560_IMG2
R is that the remaining base of oleic acid contains C atomicity 16.n=2~4 integers in the formula.
Example 3: take by weighing example 1 product 0.2535 kilogram (0.5 mole) and proper catalyst and add in the pressure reaction still, be warmed up to 100~140 ℃ and add 0.110~0.440 kilogram of (2.5~10 moles) oxyethane again, constant temperature was 0.5 hour after reaction finished, and obtained a water miscible brown viscous mixture A and B.
Figure 87104560_IMG3
P+q+p ' in the formula+q '=m
m=2.5~10
Example 4: take by weighing example 2 products 0.1725 kilogram (0.5 mole) and proper catalyst and add in the reactor, be warmed up to 100~150 ℃ and add 0.110~0.330 kilogram of (2.5~7.5 moles) oxyethane again, reaction finishes, and makes a water-soluble brown thickness product D.
Figure 87104560_IMG4
In the formula: p+q=m m=2.5~7.5
Example 5, take by weighing 0.0652 kilogram of (about 0.08 mole) example 3 product and 0.0178~0.0045 kilogram of (about 0.08~0.02 mole) P 2S 5, add in the reactor have agitator 10~50 ℃ of stirrings, be warmed up to 90~140 ℃ of constant temperature 2~7 hours, make a brown thickness, the homogeneous final product.
Figure 87104560_IMG5
Example 6, take by weighing 0.057 kilogram of (about 0.1 mole) example 4 product and 0.0223~0.0045 kilogram of (0.1~0.02 mole) P 2S 5Adding has in the flask of agitator, then heats up in 90 ℃~150 ℃ reactions 1~6 hour 10~50 ℃ of stirrings, produces a brown thickness, the homogeneous phase final product.
Figure 87104560_IMG6
Example 7, take by weighing 0.0815 kilogram of example 3 product (about 0.1 mole) and 0.0142~0.00284 kilogram of (0.1~0.02 mole) P 2O 5Add and have in the flask of agitator, after low temperature stirs, heat up in 90~140 ℃ of reactions after 1~5 hour, add average molecular weight again and be 217 alcohol mixture 0.0145 kilogram (about 0.067 mole), make brown homogeneous phase final product in 110 ℃~140 ℃ isothermal reactions 2~6 hours.
Figure 87104560_IMG7
R3 is an alkyl in the formula, contains C atomicity 9~12.
Example 8: take by weighing 0.057 kilogram of example 4 product (about 0.1 mole) and 0.0142~0.00284 kilogram of (0.1~0.02 mole) P 2O 5Join in the flask that has agitator, low temperature stirs, and then is warmed up to 85~150 ℃, react 1~6 hour, adds average molecular weight again and be 0.0145 kilogram of 217 alcohol mixture, reacts 2~6 hours in 100~150 ℃, makes brown heavy-gravity homogeneous phase final product.
R in the formula 3Be alkyl
Corrosion mitigating effect: see Table 1
Test conditions: water quality, the Shengli Oil Field station oil-containing on-the-spot water of oxygen that exposes to the sun, test piece, 75 * 12 * 1.5mm plain carbon stool sheet static steel 12 days, 50 ℃ of test temperatures.
Scale inhibition effect: see Table 2
Assessment method: use the quantitative chemical analysis method.
Operation: with dosing water sample and blank not dosing of water water sample, the calcium ion [Ca that then measured in the constant temperature water sample in 5 hours at 70 ℃ of constant temperature with complexometry ++] content, obtain scale inhibition performance.
Figure 87104560_IMG9
Figure 87104560_IMG10
Table 2
Concentration
Medicine sample scale inhibition performance (%)
PPm
Example 5 products 10 62~63
20 79~92
Example 6 products 10 84~96
20 89~96
Example 7 products 10 65.2
20 78.3
Example 8 products 10 90.5~100
20 100

Claims (4)

1, a kind of preparation method of thiophosphatephosphorothioate imidazolidine derivatives corrosion inhibiting and descaling agent, it comprises that at first making Yatall MA and n wherein is the polyamine compounds NH of 2 to 3 integer 2(CH 2CH 2NH) nH,
Make a kind of water soluble mixt with reacting ethylene oxide, this water soluble mixt reacted 2~7 hours at 90~140 ℃ with thiophosphoric anhydride more then.
2, a kind of preparation method of imidazoline phosphate ester derivative corrosion inhibiting and descaling agent, it comprises that at first making Yatall MA and n wherein is the polyamine compounds NH of 2 to 3 integer 2(CH 2CH 2NH) nA kind of water soluble mixt that H and reacting ethylene oxide make, then this water soluble mixt again with Vanadium Pentoxide in FLAKES 90~140 ℃ the reaction 1~5 hour, and then with average molecular weight be 217 alcohol mixtures 110~140,20 ℃ the reaction 2~6 hours.
3, a kind of preparation method of thiophosphatephosphorothioate imidazolidine derivatives corrosion inhibiting and descaling agent, it comprises that at first making oleic acid and n wherein is the polyamine compounds NH of 2 to 3 integer 2(CH 2CH 2NH) nA kind of water soluble mixt that H and reacting ethylene oxide make, this water soluble mixt reacted 1~6 hour at 90~150 ℃ with Vanadium Pentoxide in FLAKES more then.
4, a kind of preparation method of imidazoline phosphate ester derivative corrosion inhibiting and descaling agent, it comprises that at first making oleic acid and n wherein is the polyamine compounds NH of 2 to 3 integer 2(CH 2CH 2NH) nA kind of water soluble mixt that H and reacting ethylene oxide make, then this water soluble mixt again with Vanadium Pentoxide in FLAKES 85~150 ℃ of reactions 1~6 hour, and then with average molecular weight be that 217 alcohol mixture was 100~150 ℃ of reactions 2~6 hours.
CN 87104560 1987-06-27 1987-06-27 Preparation method of corrosion and scale inhibitor of thiophosphate ester and phosphate ester imidazoline derivatives Expired CN1013578B (en)

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CN1038697C (en) * 1995-04-19 1998-06-10 何秋霞 Corrosion inhibitor for corrosion system of HCl-H2S-H2O
CN100400712C (en) * 2003-05-08 2008-07-09 上海久安水质稳定剂厂 Prepn of anticorrosive scale-inhibiting film
CN101230260B (en) * 2007-11-01 2011-04-27 新疆德蓝股份有限公司 Compound inhibitor for exploitation of oil-gas field and preparation method thereof
CN102650061B (en) * 2012-05-07 2014-10-01 中国海洋石油总公司 High-temperature corrosion inhibitor for restraining corrosion of high-acid value crude oil and application of high-temperature corrosion inhibitor
CN102965149B (en) * 2012-12-11 2014-06-25 江苏汉光实业股份有限公司 Preparation method of oil soluble corrosion inhibitor
CN103756660A (en) * 2013-10-11 2014-04-30 中国石油天然气股份有限公司 High-temperature-resistant corrosion inhibitor special for huff and puff of rocket power composite heat carrier
CN108192088B (en) * 2017-12-29 2020-10-30 岳阳凯门水性助剂有限公司 Anti-flash rust agent and preparation method and application thereof
CN108251087B (en) * 2018-01-23 2020-10-13 中国石油天然气股份有限公司 Carbon dioxide flooding injection well annulus protection fluid and preparation method and use method thereof
CN110127871B (en) * 2019-05-21 2022-01-11 四川文理学院 Novel scale inhibitor and application thereof
CN110028170B (en) * 2019-05-21 2022-01-25 四川文理学院 Efficient scale inhibitor and application thereof
CN110468419B (en) * 2019-09-10 2021-03-30 艾茵化学(深圳)有限公司 High-salt-resistance metal antirust agent and preparation method thereof

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