CN106118720A - A kind of heavy high-acid crude oil rapid demulsifier and preparation method thereof - Google Patents

A kind of heavy high-acid crude oil rapid demulsifier and preparation method thereof Download PDF

Info

Publication number
CN106118720A
CN106118720A CN201610640939.3A CN201610640939A CN106118720A CN 106118720 A CN106118720 A CN 106118720A CN 201610640939 A CN201610640939 A CN 201610640939A CN 106118720 A CN106118720 A CN 106118720A
Authority
CN
China
Prior art keywords
ether
polyoxyethylene polyoxypropylene
crude oil
acid crude
demulsifier
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.)
Withdrawn
Application number
CN201610640939.3A
Other languages
Chinese (zh)
Inventor
王从伟
程伟
李化真
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.)
Hefei Yongjia New Mstar Technology Ltd
Original Assignee
Hefei Yongjia New Mstar Technology 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 Hefei Yongjia New Mstar Technology Ltd filed Critical Hefei Yongjia New Mstar Technology Ltd
Priority to CN201610640939.3A priority Critical patent/CN106118720A/en
Publication of CN106118720A publication Critical patent/CN106118720A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G33/00Dewatering or demulsification of hydrocarbon oils
    • C10G33/04Dewatering or demulsification of hydrocarbon oils with chemical means
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/10Feedstock materials
    • C10G2300/1033Oil well production fluids
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10GCRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G2300/00Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
    • C10G2300/20Characteristics of the feedstock or the products
    • C10G2300/201Impurities

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

The invention discloses a kind of heavy high-acid crude oil rapid demulsifier and preparation method thereof, it is made up of the raw material of following weight portion: rosin amine polyoxyethylene polyoxypropylene ether 13 17, alkylphenol-formaldehyde resin polyoxyethylene polyoxypropylene ether 11 16, polyoxyethylene polyoxypropylene tetramethylolmethane ether 10 15, methyl glucoside polyethenoxy ether 8 13, different cetearyl alcohol polyoxyethylenated alcohol stearate 6 11, glycerin polyoxyethylene ether laurate 5 10, cocamido propyl betaine 48, epoxychloropropane diethanolamine copolymer 7 12.The demulsifier that the present invention uses the raw materials such as rosin amine polyoxyethylene polyoxypropylene ether, polyoxyethylene polyoxypropylene tetramethylolmethane ether, different cetearyl alcohol polyoxyethylenated alcohol stearate, epoxychloropropane diethanolamine copolymer to prepare has the features such as de-emulsification speed is fast, dewatering efficiency is high, consumption is few, it is adaptable to heavy high-acid crude oil fast emulsion breaking.

Description

A kind of heavy high-acid crude oil rapid demulsifier and preparation method thereof
Technical field
The present invention relates to a kind of demulsifier and preparation method thereof, be specifically related to a kind of heavy high-acid crude oil rapid demulsifier and Its preparation method.
Background technology
Along with oil field large area is taked to increase water filling, the measure of steam injection raising oilwell produced fluid amount, oil well produced liquid is aqueous Rate rises rapidly;Meanwhile, the extensive application of various oil recovery auxiliary agents also makes the Produced Liquid group of crude oil, particularly viscous crude and super-viscous oil Become become more complicated, cause the efficient breakdown of emulsion of viscous crude and super-viscous oil have become as affect cost for oil production, crude quality, yield and Control the key technology that oilfield environment pollutes.
Demulsifier is a kind of surfactant, and it can make the liquid structure of emulsifying shape destroy, to reach each in emulsion Be separated the purpose come.Crude oil demulsification refers to that the chemical action utilizing demulsifier is by oil and water in the oil-water mixture of emulsifying shape Separate, make up to the purpose of crude oil dehydration, make water content reach requirement, to ensure that crude oil exporting contains water quality standard energy.Existing With the presence of on market for the shortcoming that the demulsifier de-emulsification speed of heavy high-acid crude oil is slow, greatly limit its range of application.
Summary of the invention
For the deficiencies in the prior art, the problem to be solved in the present invention is to provide a kind of heavy high-acid crude oil fast emulsion breaking Agent and preparation method thereof.
For solving prior art problem, the present invention provides following technical scheme:
A kind of heavy high-acid crude oil rapid demulsifier, is made up of the raw material of following weight portion: rosin amine polyoxyethylene polyoxypropylene Ether 13-17, alkylphenol-formaldehyde resin polyoxyethylene polyoxypropylene ether 11-16, polyoxyethylene polyoxypropylene tetramethylolmethane ether 10- 15, methyl glucoside polyethenoxy ether 8-13, different cetearyl alcohol polyoxyethylenated alcohol stearate 6-11, glycerin polyoxyethylene ether Laurate 5-10, cocamido propyl betaine 4-8, epoxychloropropane-diethanolamine copolymer 7-12.
The preparation method of a kind of heavy high-acid crude oil rapid demulsifier, comprises the following steps:
(1) by rosin amine polyoxyethylene polyoxypropylene ether, methyl glucoside polyethenoxy ether, different cetearyl alcohol polyoxyethylenated alcohol Stearate, cocamido propyl betaine, epoxychloropropane-diethanolamine copolymer mix homogeneously, then at power be 700-800W, rotating speed is magnetic agitation 5-6min under conditions of 600-700r/min, obtains compound A;
(2) by remaining raw material mix homogeneously, being then 600-700W at microwave power, rotating speed is the condition of 500-600r/min Lower microwave stirring 6-7min, obtains compound B;
(3) being mixed homogeneously with compound B by the compound A obtained, be then 400-500W at ultrasonic power, supersonic frequency is Ultrasonic vibration 20-30min under conditions of 30-40KHz, gets product.
The method have the benefit that
The present invention uses rosin amine polyoxyethylene polyoxypropylene ether, alkylphenol-formaldehyde resin polyoxyethylene polyoxypropylene ether, polyoxy Ethylene polyoxypropylene tetramethylolmethane ether, different cetearyl alcohol polyoxyethylenated alcohol stearate, epoxychloropropane-diethanolamine copolymerization The demulsifier that the raw materials such as thing prepare has the features such as de-emulsification speed is fast, dewatering efficiency is high, consumption is few, it is adaptable to heavy peracid Crude oil fast emulsion breaking.
Detailed description of the invention
Embodiment
A kind of heavy high-acid crude oil rapid demulsifier, is made up of the raw material of following weight (kg): rosin amine polyoxypropylene gathers Oxygen vinyl Ether 15, alkylphenol-formaldehyde resin polyoxyethylene polyoxypropylene ether 13, polyoxyethylene polyoxypropylene tetramethylolmethane ether 12, first Base glucose polyethenoxy ether 10, different cetearyl alcohol polyoxyethylenated alcohol stearate 9, glycerin polyoxyethylene ether laurate 8, Cocamido propyl betaine 6, epoxychloropropane-diethanolamine copolymer 10.
The preparation method of a kind of heavy high-acid crude oil rapid demulsifier, comprises the following steps:
(1) by rosin amine polyoxyethylene polyoxypropylene ether, methyl glucoside polyethenoxy ether, different cetearyl alcohol polyoxyethylenated alcohol Stearate, cocamido propyl betaine, epoxychloropropane-diethanolamine copolymer mix homogeneously, then at power be 750W, rotating speed is magnetic agitation 5min under conditions of 650r/min, obtains compound A;
(2) by remaining raw material mix homogeneously, being then 650W at microwave power, rotating speed is that microwave stirs under conditions of 550r/min Mix 6min, obtain compound B;
(3) being mixed homogeneously with compound B by the compound A obtained, be then 450W at ultrasonic power, supersonic frequency is 35KHz Under conditions of ultrasonic vibration 25min, get product.
The above-mentioned heavy high-acid crude oil rapid demulsifier prepared is joined heavy peracid according to chemical feeding quantity 8mg/L former In oil, in 60-70 DEG C of temperature, the interior water abjection more than 90% moisture content in the viscous crude of 70-80% of 15min.

Claims (2)

1. a heavy high-acid crude oil rapid demulsifier, it is characterised in that be made up of the raw material of following weight portion: rosin amine polyoxy Propylene polyoxyethylene ether 13-17, alkylphenol-formaldehyde resin polyoxyethylene polyoxypropylene ether 11-16, polyoxyethylene polyoxypropylene season Penta 4 alcohol ether 10-15, methyl glucoside polyethenoxy ether 8-13, different cetearyl alcohol polyoxyethylenated alcohol stearate 6-11, sweet Oil polyoxyethylene ether laurate 5-10, cocamido propyl betaine 4-8, epoxychloropropane-diethanolamine copolymer 7-12.
The preparation method of a kind of heavy high-acid crude oil rapid demulsifier the most according to claim 1, it is characterised in that include Following steps:
(1) by rosin amine polyoxyethylene polyoxypropylene ether, methyl glucoside polyethenoxy ether, different cetearyl alcohol polyoxyethylenated alcohol Stearate, cocamido propyl betaine, epoxychloropropane-diethanolamine copolymer mix homogeneously, then at power be 700-800W, rotating speed is magnetic agitation 5-6min under conditions of 600-700r/min, obtains compound A;
(2) by remaining raw material mix homogeneously, being then 600-700W at microwave power, rotating speed is the condition of 500-600r/min Lower microwave stirring 6-7min, obtains compound B;
(3) being mixed homogeneously with compound B by the compound A obtained, be then 400-500W at ultrasonic power, supersonic frequency is Ultrasonic vibration 20-30min under conditions of 30-40KHz, gets product.
CN201610640939.3A 2016-08-08 2016-08-08 A kind of heavy high-acid crude oil rapid demulsifier and preparation method thereof Withdrawn CN106118720A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610640939.3A CN106118720A (en) 2016-08-08 2016-08-08 A kind of heavy high-acid crude oil rapid demulsifier and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610640939.3A CN106118720A (en) 2016-08-08 2016-08-08 A kind of heavy high-acid crude oil rapid demulsifier and preparation method thereof

Publications (1)

Publication Number Publication Date
CN106118720A true CN106118720A (en) 2016-11-16

Family

ID=57255855

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201610640939.3A Withdrawn CN106118720A (en) 2016-08-08 2016-08-08 A kind of heavy high-acid crude oil rapid demulsifier and preparation method thereof

Country Status (1)

Country Link
CN (1) CN106118720A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1772844A (en) * 2005-11-15 2006-05-17 中国石化胜利油田有限公司孤东采油厂 Binary re-compound oil soluble demulsifier
CN101121898A (en) * 2007-07-30 2008-02-13 辽宁大学 Fast emulsion breaking method
CN101328429A (en) * 2008-07-24 2008-12-24 中国石油天然气股份有限公司 Demulsifying agent for dehydration of high-sulphur heavy crude

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1772844A (en) * 2005-11-15 2006-05-17 中国石化胜利油田有限公司孤东采油厂 Binary re-compound oil soluble demulsifier
CN101121898A (en) * 2007-07-30 2008-02-13 辽宁大学 Fast emulsion breaking method
CN101328429A (en) * 2008-07-24 2008-12-24 中国石油天然气股份有限公司 Demulsifying agent for dehydration of high-sulphur heavy crude

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
李柏林等: "环氧氯丙烷-二乙醇胺共聚物合成研究", 《化学与生物工程》 *

Similar Documents

Publication Publication Date Title
CN101121898B (en) Fast emulsion breaking method
CN203874710U (en) Stirring kettle for glue making machine
CA2674246C (en) Oil sands treatment system and process
CN107823914B (en) Large-scale built-in ultrasonic alginic acid extractor
CN205289109U (en) Glass bead ultrasonic cleaning device
US8685211B2 (en) Oil sands treatment system and process
CN104004032A (en) Method for preparing sucralose by continuously deacetylating sucralose-6-acetate
CN102849908B (en) Ultrasonic treatment method and device of oil field sand-containing oil sludge
CN204522966U (en) A kind of automatic froth breaking drift look device preparing high viscosity glucosides class material
CN106190229A (en) A kind of super-viscous oil high-efficient demulsifier and preparation method thereof
CN106118720A (en) A kind of heavy high-acid crude oil rapid demulsifier and preparation method thereof
CN106065335A (en) A kind of heavy oil low-temperature demulsifier and preparation method thereof
CN202465637U (en) Reaction device for heterogeneous ultra-refined continuous production of biodiesel
CN202263591U (en) High-speed emulsification reaction device
CN106267916B (en) A kind of method that defoamer is prepared using gutter oil
CN206837547U (en) A kind of extraction separation device for catalytic cracking clarified oil
CN107937020A (en) A kind of efficient breaking method of the two-step method of lipopeptid
CN105694953B (en) A kind of preparation method of crude oil demulsifier
CN204503095U (en) Multifunctional rotating device in a kind of sewage disposal device
CN103981292B (en) A kind of method that content of wax waste paper resourcesization utilizes
CN209049331U (en) A kind of pilot scale vacuum emulsification agitating device
CN205635497U (en) Quick equipment that glues thick crude oil acid number that reduces of improved generation
CN206587642U (en) Liquid detergent mixing equipment
CN204865652U (en) Mix cauldron
CN204745725U (en) Ultrafiltration formula sound wave traditional chinese medicine extractor

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
WW01 Invention patent application withdrawn after publication
WW01 Invention patent application withdrawn after publication

Application publication date: 20161116