CN106565128B - A kind of polyester ethers defoaming agent and its preparation method and application - Google Patents

A kind of polyester ethers defoaming agent and its preparation method and application Download PDF

Info

Publication number
CN106565128B
CN106565128B CN201610918592.4A CN201610918592A CN106565128B CN 106565128 B CN106565128 B CN 106565128B CN 201610918592 A CN201610918592 A CN 201610918592A CN 106565128 B CN106565128 B CN 106565128B
Authority
CN
China
Prior art keywords
defoaming agent
cement slurry
parts
catalyst
polyester ethers
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201610918592.4A
Other languages
Chinese (zh)
Other versions
CN106565128A (en
Inventor
肖丽
吴阳
段红超
白新平
王瑞玲
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
China National Petroleum Corp
CNPC Chuanqing Drilling Engineering Co Ltd
Original Assignee
Shaanxi Solid Petroleum Engineering Co Ltd
Changqing Cementing Branch of CNPC Chuanqing Drilling Engineering Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Shaanxi Solid Petroleum Engineering Co Ltd, Changqing Cementing Branch of CNPC Chuanqing Drilling Engineering Co Ltd filed Critical Shaanxi Solid Petroleum Engineering Co Ltd
Priority to CN201610918592.4A priority Critical patent/CN106565128B/en
Publication of CN106565128A publication Critical patent/CN106565128A/en
Application granted granted Critical
Publication of CN106565128B publication Critical patent/CN106565128B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B24/00Use of organic materials as active ingredients for mortars, concrete or artificial stone, e.g. plasticisers
    • C04B24/24Macromolecular compounds
    • C04B24/28Macromolecular compounds obtained otherwise than by reactions only involving carbon-to-carbon unsaturated bonds
    • C04B24/32Polyethers, e.g. alkylphenol polyglycolether
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08GMACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G65/00Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule
    • C08G65/02Macromolecular compounds obtained by reactions forming an ether link in the main chain of the macromolecule from cyclic ethers by opening of the heterocyclic ring
    • C08G65/32Polymers modified by chemical after-treatment
    • C08G65/329Polymers modified by chemical after-treatment with organic compounds
    • C08G65/331Polymers modified by chemical after-treatment with organic compounds containing oxygen
    • C08G65/332Polymers modified by chemical after-treatment with organic compounds containing oxygen containing carboxyl groups, or halides, or esters thereof
    • C08G65/3322Polymers modified by chemical after-treatment with organic compounds containing oxygen containing carboxyl groups, or halides, or esters thereof acyclic
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2103/00Function or property of ingredients for mortars, concrete or artificial stone
    • C04B2103/50Defoamers, air detrainers

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Polyethers (AREA)

Abstract

The invention belongs to technical field of oilfield chemistry, more particularly to a kind of polyester ethers defoaming agent and its preparation method and application, polyester ethers defoaming agent of the invention is the modified of polyethers defoaming agent, both polyethers defoaming agent high temperature resistant had been saved after the esterification of polyether antifoam agent, had been easily dispersed, the advantages that surface tension is low, stability is good, again because the hydrogen bond of hydrone and polyoxyethylene interchain after esterification is weakened, so that its lipophilicity increases, hydrophily further decreases, advantageously reduce surface tension, get higher its activity, defoaming capacity enhancing.

Description

A kind of polyester ethers defoaming agent and its preparation method and application
Technical field
The invention belongs to technical field of oilfield chemistry, and in particular to a kind of polyester ethers defoaming agent and preparation method thereof and answer With.
Background technique
Oil-well cement defoaming agent is many kinds of at present, and performance is totally different, is divided into mineral oils, organosilicon by the composition of defoaming agent Type, polyether-type, silicon are ether mixed.
Mineral oil defoaming agent is substituted due to bad dispersibility in water;Organic silicon defoaming agent generally comprises poly- diformazan The disadvantages of products such as radical siloxane have the characteristics that antifoaming speed is fast, foam inhibition is preferable, but price is high, not soluble in water causes universal Using limited;And polyether-type defoaming agent is with nontoxic, defoaming effect is excellent, thermal stability is good, scattered in nonirritant and water The features such as, industry, food, in terms of be widely used.
Although polyether-type defoaming agent is widely used, because of the relationship of selectivity, some fields cannot still be used so far.
Summary of the invention
The purpose of the present invention is develop the polyethet surfactant of different structure ester is made by being esterified polyethers Ether type defoaming agent, to widen its application range.
For this purpose, the present invention provides a kind of polyester ethers defoaming agent, the defoaming agent by following mass fraction component Under the action of catalyst obtained by esterification:
8~18 parts of polyethers;
5~15 parts of organic acid.
The polyethers is polyoxypropylene ethylene oxide glycerin ether;The organic acid is lauric acid;The catalyst It is the concentrated sulfuric acid.
The defoaming agent the preparation method is as follows:
Take 5~15 parts of 8~18 parts of polyethers, organic acid addition catalyst by mass fraction, at a temperature of 60~100 DEG C into Row esterification, reaction time 2h~8h, esterification are cooled down after the completion, and adjust pH value 5~8, then with saturation It is required defoaming agent that sodium chloride solution, which removes impurity,.
The catalyst is the concentrated sulfuric acid, and the concentration of catalyst is the 0.2-1.0% for accounting for the amount of reactant total material.
The defoaming agent the preparation method is as follows:
9 parts of polyoxypropylene ethylene oxide glycerin ether, 13 parts of lauric acid are taken by mass fraction, adds total moles quality 0.6% concentrated sulfuric acid is heated to catalyst at 90 DEG C and is dissolved completely in polyoxypropylene ethylene oxide glycerin ether, reaction time 7h, Acid value measuring is carried out per sampling every other hour during the reaction, to determine system esterification yield, when rate to be esterified is constant, is cooled to 60 DEG C, KOH aqueous solution is added and is neutralized, adjusts pH value 7, being extracted with saturated sodium chloride solution remove impurity later is institute The defoaming agent needed.
The polyester ethers defoaming agent is defoamed for cement slurry.
The polyester ethers defoaming agent is used for the concrete mode of cement slurry defoaming are as follows: by polyester ethers defoaming agent to account for water 0.05% deal and cement slurry of quality of mud fluid are mixed to form new cement slurry.
Beneficial effects of the present invention: this polyester ethers defoaming agent provided by the invention and its preparation method and application is The modified of polyethers defoaming agent had both saved polyethers defoaming agent high temperature resistant, had been easily dispersed, surface after the esterification of polyether antifoam agent The advantages that tension is low, stability is good, and because the hydrogen bond of hydrone and polyoxyethylene interchain after esterification is weakened, so that it is lipophilic Increase, hydrophily further decreases, advantageously reduces surface tension, get higher its activity, defoaming capacity enhancing.
Specific embodiment
Embodiment 1:
This city embodiment provides a kind of polyester ethers defoaming agent, and the defoaming agent is being urged by the component of following mass fraction Agent acts on obtained by lower esterification:
8~18 parts of polyethers;
5~15 parts of organic acid.
Wherein, polyethers is polyoxypropylene ethylene oxide glycerin ether;The organic acid is lauric acid;The catalyst is The concentrated sulfuric acid.
Polyester ethers defoaming agent in the present embodiment is obtained after esterification, and polyethers defoaming had both been saved after esterification Agent high temperature resistant is easily dispersed, the advantages that surface tension is low, stability is good, and because of hydrone after esterification and polyoxyethylene interchain Hydrogen bond is weakened, so that its lipophilicity increases, hydrophily further decreases, advantageously reduces surface tension, get higher its activity, Defoaming capacity enhancing.
Embodiment 2:
Defoaming agent in above-described embodiment the preparation method is as follows:
Take 5~15 parts of 8~18 parts of polyethers, organic acid addition catalyst by mass fraction, at a temperature of 60~100 DEG C into Row esterification, reaction time 2h~8h, esterification are cooled down after the completion, and adjust pH value 5~8, then with saturation It is required defoaming agent that sodium chloride solution, which removes impurity,.
Wherein, catalyst is the concentrated sulfuric acid, and the concentration of catalyst is the 0.2-1.0% for accounting for the amount of reactant total material.
More specifically, defoaming agent the preparation method is as follows:
9 parts of polyoxypropylene ethylene oxide glycerin ether, 13 parts of lauric acid are taken by mass fraction, adds total moles quality 0.6% concentrated sulfuric acid is heated to catalyst at 90 DEG C and is dissolved completely in polyoxypropylene ethylene oxide glycerin ether, reaction time 7h, Acid value measuring is carried out per sampling every other hour during the reaction, to determine system esterification yield, when rate to be esterified is constant, is cooled to 60 DEG C, KOH aqueous solution is added and is neutralized, adjusts pH value 7, being extracted with saturated sodium chloride solution remove impurity later is institute The defoaming agent needed.
Embodiment 3:
The polyester ethers defoaming agent referred in above-described embodiment 1 and embodiment 2 can be used for cement slurry defoaming.
Polyester ethers defoaming agent is used for the concrete mode of cement slurry defoaming are as follows: by polyester ethers defoaming agent to account for cement slurry matter 0.05% deal and cement slurry of amount are mixed to form new cement slurry.
The modified polyester ethers defoaming agent of development is defoamed for cement slurry, is added defoaming agent (account for cement amount 0.05%) The density recovery rate of cement slurry is 90% or more afterwards, and temperature resistance is up to 120 DEG C, on the compression strength of cement slurry without influence, no secondary work With.It is good with cement additive compatibility, the performance requirement of cement slurry under different temperatures can be met, can be eliminated in cement slurry Foam, and the performance of other additives is not influenced, there is good application prospect.
It is illustrated below in conjunction with this silicon ethers foam inhibitor of the specific real time data to the present embodiment.
Embodiment 4:
9 parts of polyoxypropylene ethylene oxide glycerin ether, 13 parts of lauric acid are taken by mass fraction, adds total moles quality 0.6% concentrated sulfuric acid is heated to catalyst at 90 DEG C and is dissolved completely in polyoxypropylene ethylene oxide glycerin ether, reaction time 7h, Acid value measuring is carried out per sampling every other hour during the reaction, to determine system esterification yield, when rate to be esterified is constant, is cooled to 60 DEG C, KOH aqueous solution is added and is neutralized, adjusts pH value 7, being extracted with saturated sodium chloride solution remove impurity later is institute The defoaming agent needed, obtained polyester ethers defoaming agent is added in cement slurry, and specific dosage is the 0.05% of cement slurry quality.
Obtained new cement slurry and original cement slurry are divided into point that multiple groups carry out compression strength, temperature, density Analysis experiment, obtains the data in following table 1:
1: the first component cement of table starches compression strength, temperature, density experiment data
Embodiment 5:
18 parts of polyoxypropylene ethylene oxide glycerin ether, 5 parts of lauric acid are taken by mass fraction, adds the 1% of total moles quality The concentrated sulfuric acid, be heated to catalyst at 100 DEG C and be dissolved completely in polyoxypropylene ethylene oxide glycerin ether, reaction time 8h, Acid value measuring is carried out per sampling every other hour in reaction process, to determine system esterification yield, when rate to be esterified is constant, is cooled to 60 DEG C, KOH aqueous solution is added and is neutralized, adjusts pH value 8, is extracted later with saturated sodium chloride solution needed for removing impurity as Defoaming agent, obtained polyester ethers defoaming agent is added in cement slurry, specific dosage be cement slurry quality 0.05%.
Obtained new cement slurry and original cement slurry are divided into point that multiple groups carry out compression strength, temperature, density Analysis experiment, obtains the data in following table 2:
2: the second component cement of table starches compression strength, temperature, density experiment data
Embodiment 6:
8 parts of polyoxypropylene ethylene oxide glycerin ether, 15 parts of lauric acid are taken by mass fraction, adds total moles quality 0.2% concentrated sulfuric acid is heated to catalyst at 90 DEG C and is dissolved completely in polyoxypropylene ethylene oxide glycerin ether, reaction time 3h, Acid value measuring is carried out per sampling every other hour during the reaction, to determine system esterification yield, when rate to be esterified is constant, is cooled to 60 DEG C, KOH aqueous solution is added and is neutralized, adjusts pH value 6, being extracted with saturated sodium chloride solution remove impurity later is institute The defoaming agent needed, obtained polyester ethers defoaming agent is added in cement slurry, and specific dosage is the 0.05% of cement slurry quality.
Obtained new cement slurry and original cement slurry are divided into point that multiple groups carry out compression strength, temperature, density Analysis experiment, obtains the data in following table 3:
Table 3: third component cement slurry compression strength, temperature, density experiment data
By data in the above table 1, table 2 and table 3 it is found that the cement slurry of polyester ethers defoaming agent is added compared to common water Mud, in the case where ordinary cement slurry temperature resistance only has 100 DEG C, be added the present embodiment polyester ethers defoaming agent may make it is new Cement slurry temperature resistance is up to 120 DEG C;And the density recovery rate of cement slurry reaches 90% or more, from the resistance to compression of the above ordinary cement slurry Intensity is compared with the cement slurry of the addition polyester ethers defoaming agent of the present embodiment, and compression strength is without side-effects without influence.
In conclusion this addition polyester ethers defoaming agent of the invention and cement additive compatibility are good, can meet The performance requirement of cement slurry under different temperatures can eliminate the foam in cement slurry and influence the performance of other additives, have Good application prospect.
The foregoing examples are only illustrative of the present invention, does not constitute the limitation to protection scope of the present invention, all It is within being all belonged to the scope of protection of the present invention with the same or similar design of the present invention.

Claims (2)

1. a kind of application of polyester ethers defoaming agent in cement slurry defoaming, it is characterised in that: the defoaming agent is by following matter The component of amount number is under the action of catalyst obtained by esterification:
8~18 parts of polyethers;
5~15 parts of organic acid;
The polyethers is polyoxypropylene ethylene oxide glycerin ether;The organic acid is lauric acid;The catalyst is dense Sulfuric acid;
The defoaming agent the preparation method is as follows:
5~15 parts of 8~18 parts of polyethers, organic acid addition catalyst are taken by mass fraction, carries out ester at a temperature of 60~100 DEG C Change reaction, reaction time 2h~8h, esterification is cooled down after the completion, and adjusts pH value 5~8, then with saturation chlorination It is required defoaming agent that sodium solution extraction, which removes impurity,;
The concentration of the catalyst is the 0.2-1.0% for accounting for the amount of reactant total material;
The polyester ethers defoaming agent is used for the concrete mode of cement slurry defoaming are as follows: by polyester ethers defoaming agent to account for cement slurry 0.05% deal and cement slurry of quality are mixed to form new cement slurry.
2. application as described in claim 1, it is characterised in that: the defoaming agent the preparation method is as follows:
9 parts of polyoxypropylene ethylene oxide glycerin ether, 13 parts of lauric acid are taken by mass fraction, adds the 0.6% of the amount of total material The concentrated sulfuric acid is heated to catalyst at 90 DEG C and is dissolved completely in polyoxypropylene ethylene oxide glycerin ether, and reaction time 7h is reacting Acid value measuring is carried out per sampling every other hour in the process, to determine system esterification yield, when rate to be esterified is constant, is cooled to 60 DEG C, KOH aqueous solution is added to be neutralized, adjusts pH value 7, it is required for being extracted with saturated sodium chloride solution remove impurity later Defoaming agent.
CN201610918592.4A 2016-10-21 2016-10-21 A kind of polyester ethers defoaming agent and its preparation method and application Active CN106565128B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610918592.4A CN106565128B (en) 2016-10-21 2016-10-21 A kind of polyester ethers defoaming agent and its preparation method and application

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610918592.4A CN106565128B (en) 2016-10-21 2016-10-21 A kind of polyester ethers defoaming agent and its preparation method and application

Publications (2)

Publication Number Publication Date
CN106565128A CN106565128A (en) 2017-04-19
CN106565128B true CN106565128B (en) 2019-04-16

Family

ID=58534015

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610918592.4A Active CN106565128B (en) 2016-10-21 2016-10-21 A kind of polyester ethers defoaming agent and its preparation method and application

Country Status (1)

Country Link
CN (1) CN106565128B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108424523B (en) * 2018-05-08 2021-06-01 四会市格鲁森润滑技术有限公司 Microwave catalytic self-defoaming polyether copolymer lubricant and preparation method thereof

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1115261A (en) * 1994-07-16 1996-01-24 朱吉锦 High effective defrother
CN102286146A (en) * 2011-05-04 2011-12-21 湖北富邦科技股份有限公司 Preparation method of defoaming agent for producing phosphoric acid by wet process

Also Published As

Publication number Publication date
CN106565128A (en) 2017-04-19

Similar Documents

Publication Publication Date Title
CN104987858B (en) Barium strontium scale washing agent and preparation method thereof
CN103074050B (en) A kind of high shale content sandstone reservoir scale protective type many hydrogen retarded acid
CN104531121B (en) A kind of methanol tolerance, condensate oil, the foaming water discharge agent of anti-high salinity
CN104342097B (en) A kind of solid foam water discharge agent for gas field
CN108102624B (en) Neutral blockage removal treating agent and preparation method thereof
CN103436247A (en) Retarded-acid acidizing fluid
CN108359437A (en) A kind of oil well lotion paraffin remover and its preparation method and application
CN109135709B (en) Viscosity-reducing oil displacement agent and oil displacement system suitable for heavy oil reservoir
CN106590568A (en) Foam scrubbing agent composition with mineralization resistance for gas recovery by water drainage as well as preparation method and application thereof
CN102295919B (en) Fluoride-free cleanup additive used for acidifying
CN104559983A (en) Corrosion inhibitor composition, corrosion inhibitor, application of corrosion inhibitor and anti-corrosion method of metal component
CN104830298A (en) Water-based emulsion composite blocking remover
CN108048065A (en) A kind of oil/gas well corrosion inhibiter and its preparation method and application
CN103224780A (en) Retardance and low damage acid solution system for high temperature condensate oil gas reservoir acidification
CN104176788A (en) Deoiling agent for oilfield binary composite displacement output sewage and preparation method thereof
CN106565128B (en) A kind of polyester ethers defoaming agent and its preparation method and application
CN111440604B (en) Self-demulsification type salt-resistant heavy oil cold recovery oil-displacing agent and preparation method and application thereof
CN106467732B (en) High-temperature-resistant high-salinity low-permeability reservoir pressure-reducing injection-increasing active system and preparation method thereof
CN106590574A (en) Hypersalinity resistant foam scrubbing agent composition used for drainage gas recovery and preparation method and application thereof
CN105086986A (en) High-temperature-resistant recyclable clean fracturing fluid for gas wells
CN108148566A (en) A kind of ultralow interfacial tension heavy crude thinner and preparation method thereof
CN105001847B (en) Anti-salt type viscous crude dispersing drag reducer and preparation method
CN101735115A (en) Salt resistance and calcium resistant deep extra-heavy oil emulsifier and viscosity dropping agent
CN101955768A (en) Surfactant used for displacement of reservoir oil, preparation method and application thereof in tertiary oil recovery
CN109158050A (en) Cashew nut phenolic anion-nonionic surfactant and the preparation method and application thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20201029

Address after: 100007 Dongcheng District, Dongzhimen, China, North Street, No. 9 Oil Mansion, No.

Patentee after: CHINA NATIONAL PETROLEUM Corp.

Patentee after: CNPC Chuanqing Drilling Engineering Co.,Ltd.

Address before: Company No. 151 Changqing building cementing Weiyang road 710021 Shaanxi city of Xi'an Province

Patentee before: Changqing cementing company of CNPC Chuanqing Drilling Engineering Co.,Ltd.

Patentee before: SHAANXI GUDE PETROLEUM ENGINEERING Co.,Ltd.