CN104726082B - A kind of organic base descaling agent applied to ternary composite driving and preparation method thereof - Google Patents
A kind of organic base descaling agent applied to ternary composite driving and preparation method thereof Download PDFInfo
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- CN104726082B CN104726082B CN201510142283.8A CN201510142283A CN104726082B CN 104726082 B CN104726082 B CN 104726082B CN 201510142283 A CN201510142283 A CN 201510142283A CN 104726082 B CN104726082 B CN 104726082B
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/52—Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning
- C09K8/528—Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning inorganic depositions, e.g. sulfates or carbonates
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K8/00—Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
- C09K8/52—Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning
- C09K8/528—Compositions for preventing, limiting or eliminating depositions, e.g. for cleaning inorganic depositions, e.g. sulfates or carbonates
- C09K8/532—Sulfur
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- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
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Abstract
The present invention relates to a kind of organic base descaling agent applied to ternary composite driving and preparation method thereof.Mainly solve the problems, such as that oil well fouling is serious in ternary compound oil drive oil recovery process.It is characterized in that:The mass percent of the organic base descaling agent raw material and raw material is as follows:Sodium gluconate 20~30%, the big ring polyamine 15~35% of methyl, double thioether 15~35%, Malaysia acid disodium 15~25%, ethylenediamine tetra-acetic acid 5~10%, pH adjusting agent 5~6%, softened water 10~15%.The organic base descaling agent for being applied to ternary composite driving can effectively solve the problems, such as oil well fouling in ternary compound oil drive oil recovery process, Extended Pump Detection Period.
Description
Technical field:
The present invention relates to ternary composite oil-displacing descaling agent used in a kind of field of oil field oil extraction, particularly one kind is applied to
Organic base descaling agent of ternary composite driving and preparation method thereof.
Background technology:
Ternary composite driving is one of important technology of tertiary oil recovery, is carried out using physics, chemical, biological new technology
The tertiary oil recovery that tailing recovers the oil, can improve recovery ratio 20% or so, but there are serious scale in systems such as injection, lifting, ground
Problem.To mitigate dirt card inspection pump, ternary composite driving uses screw bolt well more.Generally use acid snaking method scale removal at present, but acid
Chrome plating corrosion to screw pump is strong, has protective effect to coating without effective corrosion inhibiter, and in addition sour scale removal process is to screw pump
Rubber have aging action.Sour snaking is serious to system corrosion.
The content of the invention:
In order to solve the problems, such as present in background technology, it is clear that the present invention provides a kind of organic base applied to ternary composite driving
Dirty agent and preparation method thereof, can should effectively solve ternary compound oil drive applied to the organic base descaling agent of ternary composite driving
Oil well fouling problem in oil recovery process, Extended Pump Detection Period.The present invention also provides one kind to be applied to Ternary composite drive well
The production method of descaling agent.
The present invention solves the problems, such as that it can reach by following technical solution:A kind of organic base applied to ternary composite driving
The mass percent of descaling agent, raw material and raw material is as follows:Sodium gluconate 20~30%, the big ring polyamine 15~35% of methyl are double
Thioether 15~35%, Malaysia acid disodium 15~25%, ethylenediamine tetra-acetic acid 5~10%, pH adjusting agent 5~6%, softened water 10~
15%.
The pH adjusting agent is ammonium chloride or sodium hydroxide;The double thioether is R-S-S-R, alkyl number 2-11.
A kind of preparation method of organic base descaling agent applied to ternary composite driving, comprises the following steps:
(1) softened water is added in reaction kettle, slowly adds sodium gluconate;
(2) stirring system, 80~150r/min of mixing speed are started;
(3) start steam-heating system, be warming up to 90 DEG C;
(4) the big ring polyamine of methyl is added with the speed of 200kg/h;
(5) after adding the big ring polyamine of methyl, double thioether is added with the speed of 100kg/h;
(6) 100 DEG C are warming up to, adds 5%pH conditioning agents and Malaysia acid disodium;
(7) mixing speed is improved to 120-150r/min, adds ethylenediamine tetra-acetic acid;
(8) 120 DEG C are warming up to after adding, stirring reaction 1.5h;
(9) remaining pH adjusting agent is added, control system pH value is more than 12;
(10) start cooling water system, be cooled to 50 DEG C, barrelling.
It is steady mainly as complexing agent, water quality that this is applied to sodium gluconate in the organic base descaling agent raw material of ternary composite driving
Determine agent, calcium carbonate, magnesium can be dissolved, form ionic complex and enter in water, can stablize in water in the form of an ion;The big ring of methyl
There is polyamine surface-active can chelate cation again, can dissolve barium carbonate, barium sulfate, calcium sulfate;Double thioether can dissolve in dirt
Sulfide, such as iron sulfide;Calcium scale can be directly changed into water-soluble substances by Malaysia acid disodium, and increasing has been shared with sodium gluconate
Effect acts on;Ethylenediamine tetra-acetic acid, can play complexing with bivalent cations such as the calcium in snaking system, magnesium, increase system
Solubility for scale;System pH is more than 12, and the hydroxyl of formation is dissociated in system and can be acted on oxygen-octahedron, forms inclined silicon
Acid group, increases system solubility for scale.
It is described of the invention to be had the advantages that compared with above-mentioned background technology:It should be applied to ternary composite driving
Organic base descaling agent, by sodium gluconate, the big ring polyamine of methyl, double thioether (R-S-S-R alkyl number 2-11), ethylenediamine tetrem
Acid, Malaysia acid disodium, pH adjusting agent under agitation during in proportion, process add in reaction kettle at a slow speed, add a small amount of water i.e.
Can.On the coating of screw pump without influence, rubber is produced without aging action, snaking process without gas.Production process without discarded object,
Production process realizes clean manufacturing.Snaking process improves the utilization ratio of descaling agent by the way of well head circulation.During snaking
Between 24 it is small when, snaking rate is up to more than 85%.Preparation method is simple, no waste discharge.Available for stopping well snaking, it can also be used to do not stop
Well snaking.
Below in conjunction with embodiment, the invention will be further described:
Embodiment 1:
At room temperature, 15kg softened waters are added in reaction kettle, slowly add 20kg sodium gluconates, start stirring system,
Mixing speed 80r/min;Start steam-heating system, be warming up to 90 DEG C;The big ring of 18kg methyl is added with the speed of 200kg/h to gather
Amine;After adding the big ring polyamine of methyl, 22kg double thioethers are added with the speed of 100kg/h;100 DEG C are warming up to, adds 0.25kgpH
Conditioning agent ammonium chloride and 15kg Malaysias acid disodium;Mixing speed is improved to 120r/min, adds 5kg ethylenediamine tetra-acetic acids;Add
After be warming up to 120 DEG C, stirring reaction 1.5h;Remaining 4.75kgpH conditioning agents are added, control system pH value is more than 12;Start
Cooling water system, is cooled to 50 DEG C, barrelling.The descaling rate for measuring product is 85%.
6 step of embodiment 2- embodiments repeatedly embodiment 1 the step of, the production of obtained ternary composite driving organic base descaling agent
The formula that example is taken is shown in Table 1.Gained ternary composite driving organic base descaling agent technical target of the product is shown in Table 2.
1 ternary composite driving organic base descaling agent of table production ingredient proportion (%)
Title | Formula 1 | Formula 2 | Formula 3 | Formula 4 | Formula 5 | Formula 6 |
Sodium gluconate | 20 | 23 | 20 | 20 | 23 | 25 |
The big ring polyamine of methyl | 18 | 20 | 15 | 20 | 18 | 15 |
Double thioether | 22 | 15 | 25 | 19 | 18 | 22 |
Malaysia acid disodium | 15 | 16 | 15 | 20 | 18 | 16 |
PH adjusting agent ammonium chloride | 5 | 5 | 5 | 6 | 6 | 6 |
Ethylenediamine tetra-acetic acid | 5 | 6 | 10 | 5 | 8 | 6 |
Softened water | 15 | 15 | 10 | 10 | 10 | 10 |
Descaling rate/% | 82 | 84 | 83 | 80 | 86 | 85 |
It is whether qualified | It is qualified | It is qualified | It is qualified | It is qualified | It is qualified | It is qualified |
2 ternary composite driving organic base descaling agent technical target of the product of table
Project | Formula 1 |
Character | Faint yellow uniform liquid |
Density (20 DEG C, g/cm3) | >1.38 |
Solid content, % | >65% |
PH value (aqueous solution) | >12 |
Descaling rate/% | >80 |
4th, live stain eliminating technology
1. the polished rod of holddown well is above carried first, more than pick up height 50cm;2. closing well, while close and carry out Water gate valve;
3. pipeline pressure testing 15-18MPa, does not spray and does not leak;4. injected clear water, near wellbore zone is pushed into by downhole well fluid;5. inject scale remover
Afterwards, 3-5 side's clear water is reinjected, by scale remover pressure injection to effect well section, closing well reaction 24h;6. driving a well, cleaning mixture is returned into discharge
Come;7. it is transferred to normal production.
Stain eliminating technology needs equipment to have 1, tank car and pump truck 1.After scale removal, pumping unit recovers normal work, and oil pumping is electromechanical
Stream recovers to new pump state more than 70%, reaches scale removal effect.
Feed chemicals used in above-described embodiment are all commercially available.
Claims (3)
- A kind of 1. organic base descaling agent applied to ternary composite driving, it is characterised in that:The mass percent of raw material and raw material is such as Under:Sodium gluconate 20~30%, the big ring polyamine 15~20% of methyl, double thioether 15~25%, Malaysia acid disodium 15~25%, second two Amine tetraacethyl 5~10%, pH adjusting agent 5~6%, softened water 10~15%;The pH adjusting agent is ammonium chloride or sodium hydroxide.
- A kind of 2. organic base descaling agent applied to ternary composite driving according to claim 1, it is characterised in that:It is described double Thioether is R-S-S-R, and wherein R represents alkyl, and the carbon number on the alkyl is 2-11.
- 3. a kind of preparation method of the organic base descaling agent applied to ternary composite driving described in claim 1 or 2, its feature exist In:Comprise the following steps:(1), softened water is added in reaction kettle, add sodium gluconate in softened water;(2), start stirring system, 80~150r/min of mixing speed;(3), start steam-heating system, be warming up to 90 DEG C;(4), the big ring polyamine of methyl is added with the speed of 200kg/h;(5), add the big ring polyamine of methyl after, double thioether is added with the speed of 100kg/h;(6), be warming up to 100 DEG C, add 5%pH conditioning agents and Malaysia acid disodium;(7), improve mixing speed to 120-150r/min, add ethylenediamine tetra-acetic acid;(8), add after be warming up to 120 DEG C, stirring reaction 1.5h;(9), add remaining pH adjusting agent, control system pH value is more than 12;(10), start cooling water system, be cooled to 50 DEG C, barrelling.
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CN106147735A (en) * | 2016-07-01 | 2016-11-23 | 中国石油集团渤海钻探工程有限公司 | A kind of barium strontium calcium scale remover and preparation method thereof |
CN106634914B (en) * | 2016-12-09 | 2017-09-19 | 西南石油大学 | The working solution system removed suitable for water-base drilling fluid filter cake before well cementation |
CN113249104B (en) * | 2020-02-13 | 2022-08-05 | 中国石油天然气股份有限公司 | Scale inhibition and scale removal agent and preparation method thereof |
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US4476930A (en) * | 1982-08-23 | 1984-10-16 | Union Oil Company Of California | Inhibition of scale deposition from steam generation fluids |
CN1486942A (en) * | 2003-06-03 | 2004-04-07 | 中国石油兰州炼油化工总厂 | Scale inhibiting, Corrosion retarding and environment protecting water treating agent |
CN1621362A (en) * | 2003-11-26 | 2005-06-01 | 北京燕化兴业技术开发公司 | Non-phosphorus compound scale and corrosion inhibitor for treatment of circulating cooling water |
CN101671552A (en) * | 2009-09-28 | 2010-03-17 | 大庆油田有限责任公司 | Silicate scale clearing agent for ternary combination flooding extraction well |
CN101768430A (en) * | 2010-03-05 | 2010-07-07 | 陕西延长石油(集团)有限责任公司研究院 | Scale inhibition antiscaling agent for oil-water well salt prevention and scale-inhibition operation and preparation process thereof |
EP2287441A2 (en) * | 1997-01-13 | 2011-02-23 | Ineos Europe Limited | Oil and gas field chemicals |
CN102321464A (en) * | 2011-07-15 | 2012-01-18 | 中国石油天然气股份有限公司 | Corrosion and scale inhibitor for oil well in high water-cut period |
-
2015
- 2015-03-27 CN CN201510142283.8A patent/CN104726082B/en active Active
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
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US4476930A (en) * | 1982-08-23 | 1984-10-16 | Union Oil Company Of California | Inhibition of scale deposition from steam generation fluids |
EP2287441A2 (en) * | 1997-01-13 | 2011-02-23 | Ineos Europe Limited | Oil and gas field chemicals |
CN1486942A (en) * | 2003-06-03 | 2004-04-07 | 中国石油兰州炼油化工总厂 | Scale inhibiting, Corrosion retarding and environment protecting water treating agent |
CN1621362A (en) * | 2003-11-26 | 2005-06-01 | 北京燕化兴业技术开发公司 | Non-phosphorus compound scale and corrosion inhibitor for treatment of circulating cooling water |
CN101671552A (en) * | 2009-09-28 | 2010-03-17 | 大庆油田有限责任公司 | Silicate scale clearing agent for ternary combination flooding extraction well |
CN101768430A (en) * | 2010-03-05 | 2010-07-07 | 陕西延长石油(集团)有限责任公司研究院 | Scale inhibition antiscaling agent for oil-water well salt prevention and scale-inhibition operation and preparation process thereof |
CN102321464A (en) * | 2011-07-15 | 2012-01-18 | 中国石油天然气股份有限公司 | Corrosion and scale inhibitor for oil well in high water-cut period |
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