CN101050380A - Base oildeemulsifier in high performance - Google Patents
Base oildeemulsifier in high performance Download PDFInfo
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- CN101050380A CN101050380A CN 200710072243 CN200710072243A CN101050380A CN 101050380 A CN101050380 A CN 101050380A CN 200710072243 CN200710072243 CN 200710072243 CN 200710072243 A CN200710072243 A CN 200710072243A CN 101050380 A CN101050380 A CN 101050380A
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Abstract
This invention discloses a method for synthesizing a high-efficiency crude oil demulsifier from cornstarch and conventional polyether demulsifier by graft copolymerization. The method comprises: (1) adding solvent and cornstarch into a reaction kettle with a stirrer, slowly adding proton acid (20-80 wt.% of cornstarch), and stirring for 1-4 h; (2) adding polyether demulsifier and solvent, and refluxing under heating for 2-8 h; (3) adding NaOH solution for neutralization, ending NaOH addition when the pH value is 6.5-8.0, and reacting for 1-3 h until the solution is transparent. The demulsifier has such advantages as simple process, mild operation conditions, wide applications, and good demulsification effect.
Description
Technical field
The present invention relates to a kind of emulsion splitter, particularly relating to a kind of is main raw material and a kind of base oildeemulsifier in high performance of polyether type demulsifying agent graft modification synthetic with the W-Gum.
Background technology
Crude oil because contacting of crude oil and water adds the effect of the naturally occurring emulsifying agent in the crude oil, makes crude oil and water form stable milk sap in recovery process.Especially at present enter in the tertiary oil recovery, a large amount of chemical, the injection of tensio-active agent make emulsification of crude oil serious.In order to reach the requirement of crude oil exporting, just need carry out breakdown of emulsion to crude oil, make crude oil and water sepn.Compare with the emulsion splitter process at Oil extraction initial stage, at present, the breakdown of emulsion process of handling chemical flooding produced liquid is complicated more, difficult more.Along with the chemical flooding application of each elephant at home, chemical flooding output liquid is more and more, because the adding of alkali, tensio-active agent and polymkeric substance in the chemical flooding, changed the state of conventional crude extraction liquid, emulsion is serious, and make the breakdown of emulsion process become complicated, so the processing of chemical flooding output liquid, an important factor that restricts this technical development become.Another unfavorable factor is the energy consumption problem in the breakdown of emulsion process, causes extraction liquid processing cost cumulative year after year, has correspondingly increased the processing cost of crude oil extraction liquid.Reduce oil-collecting, the dehydration energy consumption is the most direct and the most effective measures reduce oil-collecting, dehydration temperaturre exactly, but face one of technical barrier and be exactly the breakdown of emulsion problem in the oily water separation, promptly temperature reduce that back extraction liquid breakdown of emulsion difficulty increases, problem such as water oleaginousness rising behind the breakdown of emulsion.At present, the emulsion splitter of domestic production exists four shortcomings, and the one,, bad adaptability can only be carried out breakdown of emulsion to specific profit, and the 2nd,, bad to the demulsification of chemical flooding produced liquid, dosage is big.The 3rd,, the production cost of emulsion splitter is very high, has reached the meagre profit degree.The 4th,, the low-temperature demulsification poor performance.
Summary of the invention
The present invention is intended to overcome the deficiencies in the prior art, has developed a kind of base oildeemulsifier in high performance.
Base oildeemulsifier in high performance composition principle of the present invention is to be starting raw material with the W-Gum, introduce conventional polyether type demulsifying agent in carrying out after the graft copolymerization and must this agent
It specifically comprises following three steps:
A. the acidifying of W-Gum: under agitation add 5～15 parts of solvents and 5～15 parts of W-Gums by weight in reactor, count 20%～80% protonic acid with W-Gum weight slow the adding, continuation was stirred 1～4 hour;
B. graft copolymerization: in the reactant that a step obtains, add 2～8 parts of octodecyl alcohol polyoxyethylene polyethenoxy ethers, and continue to add 2～10 parts of solvents, heating reflux reaction 2～8 hours;
C. neutralization: under agitation add sodium hydroxide solution in the reactant that the b step obtains, reach 6.5～8.0 to its pH value, sustained reaction 1～3 hour promptly makes base oildeemulsifier in high performance;
Described protonic acid is sulfuric acid, phosphoric acid or hydrochloric acid;
Described solvent is methyl alcohol, ethanol, Virahol, the trimethyl carbinol, propyl carbinol or n-propyl alcohol.
Among the present invention, protonic acid is sulfuric acid preferably, and solvent is preferably methyl alcohol, ethanol.
Base oildeemulsifier in high performance of the present invention is to be raw material with the W-Gum, and acidified processing is carried out graft copolymerization with polyether type demulsifying agent again and obtained higly branched chain and contain netted polyethers product.Acidified product breaking emulsion and dewatering is better than the polyethers of produced in conventional processes, and this is because W-Gum after the acidifying and polyether type demulsifying agent carry out graft copolymerization, have generated higly branched chain and netted polyethers product.Simultaneously, W-Gum is a kind of renewable resources, carry out the W-Gum deep processing and fully utilize the production policy that meets country, for a new way is found out in the W-Gum deep processing, product has good demulsification and adaptability widely, chemical flooding produced liquid and water drive extraction liquid had same demulsification.Simultaneously, owing to adopt the W-Gum raw material, this just makes production cost reduce by 35%, makes this product that good economic benefits be arranged, and has competitive power on market.
Base oildeemulsifier in high performance of the present invention and preparation method have that technology is simple, operational condition is gentle, production cost is low, and suitability is extensive, demulsification good.
Embodiment
Embodiment 1
Base oildeemulsifier in high performance of the present invention is to make by the following method:
A. the acidifying of W-Gum: under agitation add 5～15 parts of solvents and 5～15 parts of W-Gums by weight in reactor, count 20%～80% protonic acid with W-Gum weight slow the adding, continuation was stirred 1～4 hour;
B. graft copolymerization: in the reactant that a step obtains, add 2～8 parts of octodecyl alcohol polyoxyethylene polyethenoxy ethers, and continue to add 2～10 parts of solvents, heating reflux reaction 2～8 hours;
C. neutralization: under agitation add sodium hydroxide solution in the reactant that the b step obtains, reach 6.5～8.0 to its pH value, sustained reaction 1～3 hour promptly makes base oildeemulsifier in high performance;
Above-mentioned protonic acid is sulfuric acid, phosphoric acid or hydrochloric acid;
Above-mentioned solvent is methyl alcohol, ethanol, Virahol, the trimethyl carbinol, propyl carbinol or n-propyl alcohol.
Embodiment 2
Base oildeemulsifier in high performance of the present invention is to make by the following method:
A. the acidifying of W-Gum: under agitation add 8～12 parts of solvents and 8～12 parts of W-Gums by weight in reactor, count 40%～60% protonic acid with W-Gum weight slow the adding, continuation was stirred 2～3 hours;
B. graft copolymerization: in the reactant that a step obtains, add 3～6 parts of octodecyl alcohol polyoxyethylene polyethenoxy ethers, and continue to add 4～8 parts of solvents, heating reflux reaction 3～6 hours;
C. neutralization: under agitation add sodium hydroxide solution in the reactant that the b step obtains, reach 6.5～8.0 to its pH value, sustained reaction 1～3 hour promptly makes base oildeemulsifier in high performance;
Above-mentioned protonic acid is sulfuric acid or phosphoric acid;
Above-mentioned solvent is methyl alcohol, ethanol, Virahol or the trimethyl carbinol.
Embodiment 3
Base oildeemulsifier in high performance of the present invention is to make by the following method:
A. the acidifying of W-Gum: under agitation in reactor, add 9～10 parts of solvents and 9～10 parts of W-Gums by weight, slowly add the protonic acid of counting 45%-55% with W-Gum weight, continue to stir 2～3 hours;
B. graft copolymerization: in the reactant that a step obtains, add 4～5 parts of octodecyl alcohol polyoxyethylene polyethenoxy ethers, and continue to add 5～6 parts of solvents, heating reflux reaction 4～5 hours;
C. neutralization: under agitation add sodium hydroxide solution in the reactant that the b step obtains, reach 6.5～8.0 to its pH value, sustained reaction 1～3 hour promptly makes base oildeemulsifier in high performance;
Above-mentioned protonic acid is a sulfuric acid;
Above-mentioned solvent is methyl alcohol or ethanol.
Embodiment 4
In the reactor of a band stirring arm, add 10 parts of methyl alcohol and 10 parts of W-Gums by weight, slowly add 5 part of 80% sulfuric acid under stirring, continue to stir acidification reaction 2 hours; In reactor, add 5 parts of octodecyl alcohol polyoxyethylene polyethenoxy ethers and replenish and add 5 parts of methyl alcohol, reflux 5 hours; To prepare 40% sodium hydroxide solution, slowly be added dropwise in the reactor, and reach at 6.5～8.0 o'clock until the pH value and stop to drip, stir 2 hours, promptly make base oildeemulsifier in high performance of the present invention.
Embodiment 5
In the reactor of a band stirring arm, add 5 parts of Virahols and 5 parts of W-Gums by weight, slowly add 3 parts of strong phosphoric acid under stirring, add the back and stirred acidification reaction 1 hour; In reactor, add 2 parts of octodecyl alcohol polyoxyethylene polyethenoxy ethers and 2 parts of Virahols, reflux 3 hours; To prepare 40% sodium hydroxide solution, slowly be added dropwise in the reactor, and reach 6.5～8.0 until the pH value and stop to drip, stir 1 hour, promptly get base oildeemulsifier in high performance of the present invention.
Embodiment 6
Add 15 parts of W-Gums of 15 parts of ethanol by weight in the reactor of a band stirring arm, stir down and slowly add 10 part of 80% hydrochloric acid, adding finishes stirred down acidification reaction 4 hours; In reactor, add 7 parts of octodecyl alcohol polyoxyethylene polyethenoxy ethers and replenish and add 8 parts of ethanol, reflux 8 hours; Prepare 40% sodium hydroxide solution, slowly be added dropwise in the reactor, reach 6.5～8.0, stirred 3 hours, promptly make base oildeemulsifier in high performance of the present invention until the pH value.
Claims (3)
1, a kind of base oildeemulsifier in high performance is to make with following operation steps:
A. the acidifying of W-Gum: under agitation add 5～15 parts of solvents and 5～15 parts of W-Gums by weight in reactor, count 20%～80% protonic acid with W-Gum weight slow the adding, continuation was stirred 1～4 hour;
B. graft copolymerization: in the reactant that a step obtains, add 2～8 parts of octodecyl alcohol polyoxyethylene polyethenoxy ethers, and continue to add 2～10 parts of solvents, heating reflux reaction 2～8 hours;
C. neutralization: under agitation add sodium hydroxide solution in the reactant that the b step obtains, reach 6.5～8.0 to its pH value, sustained reaction 1～3 hour promptly makes base oildeemulsifier in high performance;
Above-mentioned protonic acid is sulfuric acid, phosphoric acid or hydrochloric acid;
Above-mentioned solvent is methyl alcohol, ethanol, Virahol, the trimethyl carbinol, propyl carbinol or n-propyl alcohol.
2, a kind of base oildeemulsifier in high performance as claimed in claim 1 is characterized in that making by the following method:
A. the acidifying of W-Gum: under agitation add 8～12 parts of solvents and 8～12 parts of W-Gums by weight in reactor, count 40%～60% protonic acid with W-Gum weight slow the adding, continuation was stirred 2～3 hours;
B. graft copolymerization: in the reactant that a step obtains, add 3～6 parts of octodecyl alcohol polyoxyethylene polyethenoxy ethers, and continue to add 4～8 parts of solvents, heating reflux reaction 3～6 hours;
C. neutralization: under agitation add sodium hydroxide solution in the reactant that the b step obtains, reach 6.5～8.0 to its pH value, sustained reaction 1～3 hour promptly makes base oildeemulsifier in high performance.
3, a kind of base oildeemulsifier in high performance as claimed in claim 1 or 2 is characterized in that protonic acid is a sulfuric acid, and solvent is methyl alcohol or ethanol.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2007100722436A CN100519701C (en) | 2007-05-21 | 2007-05-21 | Crude oil demulsifying agent |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2007100722436A CN100519701C (en) | 2007-05-21 | 2007-05-21 | Crude oil demulsifying agent |
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| Publication Number | Publication Date |
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| CN101050380A true CN101050380A (en) | 2007-10-10 |
| CN100519701C CN100519701C (en) | 2009-07-29 |
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| CNB2007100722436A Active CN100519701C (en) | 2007-05-21 | 2007-05-21 | Crude oil demulsifying agent |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102212384A (en) * | 2011-05-10 | 2011-10-12 | 中国石油天然气股份有限公司 | Emulsion breaker for dehydration of crude oil extracted from acidified oil well |
| CN101671573B (en) * | 2009-10-10 | 2013-06-19 | 山东德仕化工集团有限公司 | Production formula of DSP-1 crude oil demulsifier |
| CN103509592A (en) * | 2013-09-18 | 2014-01-15 | 潍坊华强特种材料科技有限公司 | Preparation method of demulsifying agent |
| CN107746724A (en) * | 2017-11-27 | 2018-03-02 | 辽宁海德新化工有限公司 | A kind of crude oil demulsifying agent being applied under cryogenic conditions and preparation method thereof |
| CN110343544A (en) * | 2018-04-02 | 2019-10-18 | 淮阴师范学院 | A kind of starch base crude oil demulsifier, preparation method and its usage |
| CN111269733A (en) * | 2019-09-17 | 2020-06-12 | 淮阴师范学院 | Modified starch-based crude oil demulsifier and preparation method thereof |
-
2007
- 2007-05-21 CN CNB2007100722436A patent/CN100519701C/en active Active
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101671573B (en) * | 2009-10-10 | 2013-06-19 | 山东德仕化工集团有限公司 | Production formula of DSP-1 crude oil demulsifier |
| CN102212384A (en) * | 2011-05-10 | 2011-10-12 | 中国石油天然气股份有限公司 | Emulsion breaker for dehydration of crude oil extracted from acidified oil well |
| CN102212384B (en) * | 2011-05-10 | 2013-09-04 | 中国石油天然气股份有限公司 | Emulsion breaker for dehydration of crude oil extracted from acidified oil well |
| CN103509592A (en) * | 2013-09-18 | 2014-01-15 | 潍坊华强特种材料科技有限公司 | Preparation method of demulsifying agent |
| CN103509592B (en) * | 2013-09-18 | 2014-07-30 | 潍坊华强特种材料科技有限公司 | Preparation method of demulsifying agent |
| CN107746724A (en) * | 2017-11-27 | 2018-03-02 | 辽宁海德新化工有限公司 | A kind of crude oil demulsifying agent being applied under cryogenic conditions and preparation method thereof |
| CN110343544A (en) * | 2018-04-02 | 2019-10-18 | 淮阴师范学院 | A kind of starch base crude oil demulsifier, preparation method and its usage |
| CN110343544B (en) * | 2018-04-02 | 2021-09-21 | 淮阴师范学院 | Starch-based crude oil demulsifier, preparation method and application thereof |
| CN111269733A (en) * | 2019-09-17 | 2020-06-12 | 淮阴师范学院 | Modified starch-based crude oil demulsifier and preparation method thereof |
| CN111269733B (en) * | 2019-09-17 | 2021-08-06 | 淮阴师范学院 | Modified starch-based crude oil demulsifier and preparation method thereof |
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| Publication number | Publication date |
|---|---|
| CN100519701C (en) | 2009-07-29 |
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Owner name: DAQING HUAYING CHEMICAL INDUSTRY CO., LTD. Free format text: FORMER OWNER: CAI SHENGSHENG Effective date: 20150813 |
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Effective date of registration: 20150813 Address after: 163000 Heilongjiang high tech Zone in Daqing City, Grand Park Patentee after: Daqing Huaying Chemical Industry Co., Ltd. Address before: 163714 Heilongjiang province Daqing city Daqing high tech Zone Xinghua ethylene Park hualongxiang Chemical Co. Ltd. Patentee before: Cai Shengsheng |