CN106833587A - A kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease - Google Patents

A kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease Download PDF

Info

Publication number
CN106833587A
CN106833587A CN201611233558.XA CN201611233558A CN106833587A CN 106833587 A CN106833587 A CN 106833587A CN 201611233558 A CN201611233558 A CN 201611233558A CN 106833587 A CN106833587 A CN 106833587A
Authority
CN
China
Prior art keywords
kitchen waste
waste grease
bio oil
oil
production process
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.)
Pending
Application number
CN201611233558.XA
Other languages
Chinese (zh)
Inventor
龙运前
刘静
黄小荷
高良军
陈立桥
许林
宋付权
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.)
Zhejiang Ocean University ZJOU
Original Assignee
Zhejiang Ocean University ZJOU
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 Zhejiang Ocean University ZJOU filed Critical Zhejiang Ocean University ZJOU
Priority to CN201611233558.XA priority Critical patent/CN106833587A/en
Publication of CN106833587A publication Critical patent/CN106833587A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C09DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09KMATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
    • C09K8/00Compositions for drilling of boreholes or wells; Compositions for treating boreholes or wells, e.g. for completion or for remedial operations
    • C09K8/58Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids
    • C09K8/584Compositions for enhanced recovery methods for obtaining hydrocarbons, i.e. for improving the mobility of the oil, e.g. displacing fluids characterised by the use of specific surfactants

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Lubricants (AREA)
  • General Preparation And Processing Of Foods (AREA)

Abstract

The present invention relates to a kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease, it is raw material using kitchen waste grease, bio oil hydroxy sulfonate is obtained by processing the series reaction such as purification, sulfonating reaction, hydrolysis neutralization, point liquid and vacuum distillation, the kitchen waste grease that the present invention is used, it is the mixture of various triglycerides after processing purification, the oil resource enriches, low production cost;Described bio oil hydroxy sulfonate is a kind of surfactant, is applied to field of petroleum exploitation.The bio oil hydroxyl sulfoacid salt surfactant of present invention synthesis has preferable surface-active, interfacial activity, and biological degradability is good, environmental toxicity is small, alternative traditional petroleum sulfonate surfactant.

Description

A kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease
Technical field
The invention belongs to organic compound synthesis field, in particular it relates to a kind of there is preferable surface-active, interface to live Property, the bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease that biological degradability is good, environmental toxicity is small, and apply In oil exploitation.
Background technology
Kitchen waste grease refers to that the mankind produce in edible natural vegetable oil and animal tallow, and grease deep-processing process A series of raw fatty wastes for losing edibility, are commonly called as waste oil, hogwash fat, swill oil etc..It was found that waste grease Amount account for the 20~30% of edible oil total quantity consumed.A large amount of accumulations of kitchen waste grease are gone back except triggering food security accident Huge risk of environmental pollution can be brought.It is in particular in several aspects:1) food-safety problem is caused.Due to kitchen abandoned oil The easy oxidative rancidity of fat goes bad, and produces aflatoxins with strong carcinogenesis etc., once dealing with improperly, reenters food Chain, it will have a strong impact on human health, in some instances it may even be possible to cause great food security accident.2) polluted-water.Kitchen waste grease It is one of important trophism water pollutant, water quality deterioration and eutrophication can be caused into water body, and make sewage treatment plant Biological processing unit treatment effeciency is significantly reduced.3) emitting offensive odor.Exposure time is long in atmosphere for kitchen waste grease, and oxygen occurs Change is become sour, and distributes volatile fat acids foul gas, has a strong impact on environment, be trigger public's kickback main cause it One.
With the fast development of China's economy, China is in rising trend always to the demand of oil and oil product, stone The demand of oil and exploitation contradiction.How to effectively improve oil recovery factor, find Development of Novel oil recovery technique into It is the key subjects of China Petroleum, wherein surfactant flooding has become one of key means of this kind of new technology. The main large-medium-sized oilfield of China is already in the latter stage in waterflooding development stage, enters the new technology that tertiary oil recovery is representative Phase of development, surfactant flooding agent is widely used in each elephant.At present, domestic surface used for tertiary oil recovery is lived Property agent mainly has petroleum carboxylate, petroleum sulfonate, heavy alkylbenzene sulfonate etc..The raw material for synthesizing these surfactants is available for The scope of selection is not extensive enough, mainly refining oil byproduct petroleum distillate (mainly heavy aromatics, aromatic hydrocarbons), heavy alkyl benzene and SO3 Based on produce, produced using autoclave or falling film sulfonation units, the technique such as auxiliary neutralization, compounding obtains can be used for the displacement of reservoir oil Alkylaryl sulfonates.Due to oil product as raw material, these sulfosalt surfactants are substantially all containing aromatic ring, especially It is that aromatic ring structure is also contained in part, biological decomposition ability, environmental improvement difficulty are big, have pollution to environment.And pass through in recent years Often there is the nervous situation of raw material supply, cause cost of material to go up year by year, need the available sources for expanding raw material badly.
Using the active ingredient in kitchen waste grease as the raw material of tertiary oil recovery surfactant, meal can be effectively solved Kitchen waste grease is directly discharged into sewer or is filled or burned by Domestic Waste Collection processing system and causes resource Waste and problem of environmental pollution.Kitchen waste grease recycling is promoted, is turned waste into wealth, turned harm into good, be not only development and follow The important content of ring economy, is also the fundamental measure for solving the food-safety problem that kitchen waste grease triggers.Or stone Bulk petroleum resource is saved in the production of oil exploitation surfactant.
The content of the invention
It is an object of the invention to provide a kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease, profit The bio oil hydroxyl sulfoacid salt surfactant prepared with the method has preferable surface-active, interfacial activity, biodegradable The good, environmental toxicity of property is small, alternative traditional petroleum sulfonate surfactant.
To achieve these goals, the present invention uses following technical scheme:
A kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease, comprises the following steps:
A, the processed purification of kitchen waste grease, obtain treatment grease, and the treatment grease is the mixing of several triglycerides Thing;
B, kitchen waste grease and the solvent that will process purification are mixed in and are burnt equipped with magnetic rotor, condenser pipe, three mouthfuls of thermometer In bottle, there-necked flask is placed in heat collecting type constant-temperature heating magnetic stirring apparatus, quickly stirs 10-20min, makes kitchen waste grease complete CL, obtains the mixed solution of light brown;
C, at room temperature toward oleum is slowly dropped into the mixed solution of there-necked flask, while quickly being stirred, timing is opened After beginning to instill oleum 10-15min, heat up and be incubated;
D, reach the reaction time after, toward reaction solution instilling ammoniacal liquor is hydrolyzed neutralization reaction, until reaction solution is in acidity When, stop that ammoniacal liquor is added dropwise, after reaction solution stirring 2-5min is sufficiently mixed, product is poured into separatory funnel, use distilled water diluting Solution, vibrates and stirs, and stands 10-15min, the crude product of isolated bio oil hydroxy sulfonate, by the crude product In the thermostat water bath using after simulating vacuum distillation apparatus vacuum distillation 1.5-2h, obtain bio oil hydroxy sulfonate into Product.
Preferably, the kitchen waste grease is selected from any one in frying oil, swill oil, waste oil.
Preferably, the solvent is selected from any one in carbon tetrachloride, 1,2- dichloroethanes, hexamethylene.
Preferably, the volume ratio of described kitchen waste grease and solvent is 1:1-1:4.
Preferably, described kitchen waste grease is 9 with the volume ratio of oleum:1-3:1.
Preferably, described reaction temperature is 40-80 DEG C
Preferably, the described reaction time is 2-6h.
Preferably, the application of described bio oil hydroxyl sulfoacid salt surfactant, is applied to field of petroleum exploitation.
Beneficial effects of the present invention:
1st, it is of the invention with kitchen waste grease as raw material, for kitchen waste grease resource higher value application provides new thinking, Also for the synthesis of Surfactants Used for Oil field class provides raw material new way.
2nd, production low cost, process is simple, the environment-protecting asepsis of present invention synthesis, can rely on the existing surface-active in oil field Agent production equipment device, is capable of achieving industrialized production.
3rd, the bio oil hydroxy sulfonate of present invention synthesis has preferable surface-active, and mass fraction is at 45 DEG C The surface tension of 0.5% solution is 29.44mN/m.
4th, the bio oil hydroxy sulfonate of present invention synthesis has preferable interfacial activity, in 45 DEG C, 5000mg/L mineralisings Under the conditions of degree, mass fraction is 0.5% solution and the interfacial tension of Daqing crude oil is 1.97 × 10-3mN/m。
5th, the bio oil hydroxy sulfonate with present invention synthesis is oil displacement agent, because without aromatic rings, phase in the raw material of synthesis Sulfonate surfactant more very widely used today than oil field, with biological degradability it is good, environmental toxicity is small the characteristics of, to open Hair is efficient, environment-friendly type oil displacement agent provides new method.
6th, bio oil hydroxyl sulfoacid salt surfactant of the invention is used for the oil displacement system of chemical flooding, energy and Daqing crude oil Form 10-3The ultralow interfacial tension of mN/m number of levelss, realizes the purpose of optimal oil displacement efficiency.In 45 DEG C, 5000mg/L mineralisings 10 can be formed under the reservoir condition of degree with Daqing crude oil-3The ultralow interfacial tension of the mN/m orders of magnitude, improves oil recovery factor 12.52%, achieve and preferably improve oil recovery factor effect.
Specific embodiment
Below by specific embodiment, technical scheme is described in further detail.
In the present invention, if not refering in particular to, raw material and equipment for being used etc. is commercially available or commonly used in the art. Method in following embodiments, unless otherwise instructed, is the conventional method of this area.
Embodiment 1
A kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease, comprises the following steps:A, frying oil are through adding Work is purified, and obtains treatment grease, and the treatment grease is the mixture of various triglycerides;B, will process purification frying oil with 1,2- dichloroethanes is by volume 1:2 are mixed in equipped with magnetic rotor, condenser pipe, the there-necked flask of thermometer, and three mouthfuls are burnt Bottle is placed in heat collecting type constant-temperature heating magnetic stirring apparatus, quickly stirs 10min, is completely dissolved kitchen waste grease, obtains shallow The mixed solution of brown;C, it is 3 according to kitchen waste grease and oleum volume ratio:1, at room temperature toward the mixing of there-necked flask Oleum is slowly dropped into solution, while quickly being stirred, after timing starts to instill oleum 10min, is warming up to anti- 40 DEG C of temperature is answered, and keeps reacting 6h;D, reach 6h after, toward reaction solution instilling ammoniacal liquor is hydrolyzed neutralization reaction, until When reaction solution is not in acidity, stop that ammoniacal liquor is added dropwise, after reaction solution stirring 2min is sufficiently mixed, product poured into separatory funnel, Use distilled water diluting solution, vibrate and stir, by 10min standing after, isolated bio oil hydroxy sulfonate it is thick Product, the crude product is utilized in thermostat water bath after simulating vacuum distillation apparatus vacuum distillation 1.5h, obtains bio oil hydroxyl The finished product of base sulfonate.Yield is 60.15%.
The bio oil hydroxy sulfonate that the present embodiment is obtained mass fraction at 45 DEG C is the surface tension of 0.5% solution It is 30.12mN/m, under the conditions of 45 DEG C, 5000mg/L salinities, mass fraction is 0.5% solution and the interface of Daqing crude oil Tension force is 2.16 × 10-3mN/m。
It is 5.26cm in length, a diameter of 2.54cm, permeability is 0.136 μm2Grand celebration natural core on be simulated Oil displacement experiment.Step is:Water drive to aqueous 98% first is injected with Daqing oil field, metaideophone 0.4PV (rock pore volume) concentration is Bio oil hydroxy sulfonate surfactant solution prepared by 0.5% the present embodiment, then sequent water flooding to the port of export loses Oil, can improve oil recovery factor 12.52% on the basis of water drive.
Embodiment 2
A kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease, comprises the following steps:A, frying oil are through adding Work is purified, and obtains treatment grease, and the treatment grease is the mixture of various triglycerides;B, will process purification frying oil with 1,2- dichloroethanes is by volume 1:1 is mixed in equipped with magnetic rotor, condenser pipe, the there-necked flask of thermometer, and three mouthfuls are burnt Bottle is placed in heat collecting type constant-temperature heating magnetic stirring apparatus, quickly stirs 16min, is completely dissolved kitchen waste grease, obtains shallow The mixed solution of brown;C, it is 8 according to kitchen waste grease and oleum volume ratio:1, at room temperature toward the mixing of there-necked flask Oleum is slowly dropped into solution, while quickly being stirred, after timing starts to instill oleum 13min, is warming up to anti- Temperature 50 C is answered, and keeps reacting 4h;D, reach 4h after, toward reaction solution instilling ammoniacal liquor is hydrolyzed neutralization reaction, until When reaction solution is not in acidity, stop that ammoniacal liquor is added dropwise, after reaction solution stirring 3min is sufficiently mixed, product poured into separatory funnel, Use distilled water diluting solution, vibrate and stir, by 12min standing after, isolated bio oil hydroxy sulfonate it is thick Product, the crude product is utilized in thermostat water bath after simulating vacuum distillation apparatus vacuum distillation 1.8h, obtains bio oil hydroxyl The finished product of base sulfonate.Yield is 54.82%.
The bio oil hydroxy sulfonate that the present embodiment is obtained mass fraction at 45 DEG C is the surface tension of 0.5% solution It is 32.68mN/m, under the conditions of 45 DEG C, 5000mg/L salinities, mass fraction is 0.5% solution and the interface of Daqing crude oil Tension force is 2.39 × 10-3mN/m。
It is 5.52cm in length, a diameter of 2.56cm, permeability is 0.147 μm2Grand celebration natural core on be simulated Oil displacement experiment.Step is:Water drive to aqueous 98% first is injected with Daqing oil field, metaideophone 0.4PV (rock pore volume) concentration is Bio oil hydroxy sulfonate surfactant solution prepared by 0.5% the present embodiment, then sequent water flooding to the port of export loses Oil, can improve oil recovery factor 10.92% on the basis of water drive.
Embodiment 3
A kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease, comprises the following steps:A, frying oil are through adding Work is purified, and obtains treatment grease, and the treatment grease is the mixture of various triglycerides;B, will process purification frying oil with Hexamethylene is by volume 1:During 2 are mixed in equipped with magnetic rotor, condenser pipe, the there-necked flask of thermometer, there-necked flask is placed in In heat collecting type constant-temperature heating magnetic stirring apparatus, 20min is quickly stirred, be completely dissolved kitchen waste grease, obtain light brown Mixed solution;C, it is 7 according to kitchen waste grease and oleum volume ratio:1, at room temperature toward in the mixed solution of there-necked flask Oleum is slowly dropped into, while quickly being stirred, after timing starts to instill oleum 15min, reaction temperature is warming up to 80 DEG C, and keep reacting 2h;D, reach 2h after, toward reaction solution instilling ammoniacal liquor is hydrolyzed neutralization reaction, until reaction solution When not in acidity, stop that ammoniacal liquor is added dropwise, after reaction solution stirring 5min is sufficiently mixed, product is poured into separatory funnel, with distillation Water dilute solution, vibrates and stirs, by after 15min standings, the crude product of isolated bio oil hydroxy sulfonate will The crude product, using after simulating vacuum distillation apparatus vacuum distillation 2h, obtains bio oil hydroxy sulfonate in thermostat water bath Finished product.Yield is 65.78%.
The bio oil hydroxy sulfonate that the present embodiment is obtained mass fraction at 45 DEG C is the surface tension of 0.5% solution It is 29.64mN/m, under the conditions of 45 DEG C, 5000mg/L salinities, mass fraction is 0.5% solution and the interface of Daqing crude oil Tension force is 1.85 × 10-3mN/m。
It is 5.47cm in length, a diameter of 2.51cm, permeability is 0.143 μm2Grand celebration natural core on be simulated Oil displacement experiment.Step is:Water drive to aqueous 98% first is injected with Daqing oil field, metaideophone 0.4PV (rock pore volume) concentration is Bio oil hydroxy sulfonate surfactant solution prepared by 0.5% the present embodiment, then sequent water flooding to the port of export loses Oil, can improve oil recovery factor 13.04% on the basis of water drive.
Embodiment 4
A kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease, comprises the following steps:A, frying oil are through adding Work is purified, and obtains treatment grease, and the treatment grease is the mixture of various triglycerides;B, will process purification frying oil with Carbon tetrachloride is by volume 1:During 2 are mixed in equipped with magnetic rotor, condenser pipe, the there-necked flask of thermometer, there-necked flask is put In heat collecting type constant-temperature heating magnetic stirring apparatus, 20min is quickly stirred, be completely dissolved kitchen waste grease, obtain light brown Mixed solution;C, it is 7 according to kitchen waste grease and oleum volume ratio:1, at room temperature toward the mixed solution of there-necked flask In be slowly dropped into oleum, while quickly stirred, after timing starts to instill oleum 10min, be warming up to reaction temperature 60 DEG C of degree, and keep reacting 4h;D, reach 4h after, toward reaction solution instilling ammoniacal liquor is hydrolyzed neutralization reaction, until reaction When liquid is not in acidity, stop that ammoniacal liquor is added dropwise, after reaction solution stirring 2min is sufficiently mixed, product is poured into separatory funnel, with steaming Distilled water dilute solution, vibrates and stirs, after 10min stands, the crude product of isolated bio oil hydroxy sulfonate, The crude product is utilized in thermostat water bath after simulating vacuum distillation apparatus vacuum distillation 2h, obtain bio oil hydroxy sulfonate Finished product.Yield is 71.69%.
The bio oil hydroxy sulfonate that the present embodiment is obtained mass fraction at 45 DEG C is the surface tension of 0.5% solution It is 31.27mN/m, under the conditions of 45 DEG C, 5000mg/L salinities, mass fraction is 0.5% solution and the interface of Daqing crude oil Tension force is 2.01 × 10-3mN/m。
It is 5.73cm in length, a diameter of 2.58cm, permeability is 0.151 μm2Grand celebration natural core on be simulated Oil displacement experiment.Step is:Water drive to aqueous 98% first is injected with Daqing oil field, metaideophone 0.4PV (rock pore volume) concentration is Bio oil hydroxy sulfonate surfactant solution prepared by 0.5% the present embodiment, then sequent water flooding to the port of export loses Oil, can improve oil recovery factor 12.15% on the basis of water drive.
Embodiment 5
A kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease, comprises the following steps:A, frying oil are through adding Work is purified, and obtains treatment grease, and the treatment grease is the mixture of various triglycerides;B, will process purification frying oil with 1,2- dichloroethanes is by volume 1:4 are mixed in equipped with magnetic rotor, condenser pipe, the there-necked flask of thermometer, and three mouthfuls are burnt Bottle is placed in heat collecting type constant-temperature heating magnetic stirring apparatus, quickly stirs 10min, is completely dissolved kitchen waste grease, obtains shallow The mixed solution of brown;C, it is 9 according to kitchen waste grease and oleum volume ratio:1, at room temperature toward the mixing of there-necked flask Oleum is slowly dropped into solution, while quickly being stirred, after timing starts to instill oleum 15min, is warming up to anti- Temperature 50 C is answered, and keeps reacting 3h;D, reach 3h after, toward reaction solution instilling ammoniacal liquor is hydrolyzed neutralization reaction, until When reaction solution is not in acidity, stop that ammoniacal liquor is added dropwise, after reaction solution stirring 5min is sufficiently mixed, product poured into separatory funnel, Use distilled water diluting solution, vibrate and stir, by 15min standing after, isolated bio oil hydroxy sulfonate it is thick Product, the crude product is utilized in thermostat water bath after simulating vacuum distillation apparatus vacuum distillation 1.5h, obtains bio oil hydroxyl The finished product of base sulfonate.Yield is 49.57%.
The bio oil hydroxy sulfonate that the present embodiment is obtained mass fraction at 45 DEG C is the surface tension of 0.5% solution It is 32.83mN/m, under the conditions of 45 DEG C, 5000mg/L salinities, mass fraction is 0.5% solution and the interface of Daqing crude oil Tension force is 2.48 × 10-3mN/m。
It is 5.19cm in length, a diameter of 2.52cm, permeability is 0.129 μm2Grand celebration natural core on be simulated Oil displacement experiment.Step is:Water drive to aqueous 98% first is injected with Daqing oil field, metaideophone 0.4PV (rock pore volume) concentration is Bio oil hydroxy sulfonate surfactant solution prepared by 0.5% the present embodiment, then sequent water flooding to the port of export loses Oil, can improve oil recovery factor 11.68% on the basis of water drive.
Embodiment described above is a kind of preferably scheme of the invention, not makees any formal to the present invention Limitation, also has other variants and remodeling on the premise of without departing from the technical scheme described in claim.

Claims (8)

1. a kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease, it is characterised in that comprise the following steps:
A, the processed purification of kitchen waste grease, obtain treatment grease, and the treatment grease is the mixing of several triglycerides Thing;
B, kitchen waste grease and the solvent that will process purification are mixed in and are burnt equipped with magnetic rotor, condenser pipe, three mouthfuls of thermometer In bottle, there-necked flask is placed in heat collecting type constant-temperature heating magnetic stirring apparatus, quickly stirs 10-20min, makes kitchen waste grease complete CL, obtains the mixed solution of light brown;
C, at room temperature toward oleum is slowly dropped into the mixed solution of there-necked flask, while quickly being stirred, timing is opened After beginning to instill oleum 10-15min, heat up and be incubated;
D, reach the reaction time after, toward reaction solution instilling ammoniacal liquor is hydrolyzed neutralization reaction, until reaction solution is in acidity When, stop that ammoniacal liquor is added dropwise, after reaction solution stirring 2-5min is sufficiently mixed, product is poured into separatory funnel, use distilled water diluting Solution, vibrates and stirs, and stands 10-15min, the crude product of isolated bio oil hydroxy sulfonate, by the crude product In the thermostat water bath using after simulating vacuum distillation apparatus vacuum distillation 1.5-2h, obtain bio oil hydroxy sulfonate into Product.
2. a kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease according to claim 1, it is special Levy and be, kitchen waste grease described in step a is selected from any one in frying oil, swill oil, waste oil.
3. a kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease according to claim 1, it is special Levy and be, solvent described in step b is selected from any one in carbon tetrachloride, 1,2- dichloroethanes, hexamethylene.
4. a kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease according to claim 1, it is special Levy and be, the volume ratio of kitchen waste grease and solvent described in step b is 1:1-1:4.
5. a kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease according to claim 1, it is special Levy and be, the kitchen waste grease described in step c is 9 with the volume ratio of oleum:1-3:1.
6. a kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease according to claim 1, it is special Levy and be, the reaction temperature described in step c is 40-80 DEG C.
7. a kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease according to claim 1, it is special Levy and be, the reaction time described in step c is 2-6h.
8. a kind of bio oil hydroxyl sulfoacid salt surfactant based on kitchen waste grease according to claim 1 should With, it is characterised in that it is applied to field of petroleum exploitation.
CN201611233558.XA 2016-12-28 2016-12-28 A kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease Pending CN106833587A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201611233558.XA CN106833587A (en) 2016-12-28 2016-12-28 A kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201611233558.XA CN106833587A (en) 2016-12-28 2016-12-28 A kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease

Publications (1)

Publication Number Publication Date
CN106833587A true CN106833587A (en) 2017-06-13

Family

ID=59112958

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201611233558.XA Pending CN106833587A (en) 2016-12-28 2016-12-28 A kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease

Country Status (1)

Country Link
CN (1) CN106833587A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107185508A (en) * 2017-06-26 2017-09-22 焦作市新科资源综合利用研发有限公司 A kind of method that utilization dichloroethanes reclaims oily waste water atlapulgite
CN109762613A (en) * 2019-02-26 2019-05-17 太原理工大学 A kind of method that novel water-coal slurry dispersing agent is prepared by bio oil
CN113880510A (en) * 2021-10-19 2022-01-04 山西省交通科技研发有限公司 Stabilizer for road base mixture and construction method thereof

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009156241A1 (en) * 2008-06-27 2009-12-30 Evonik Goldschmidt Gmbh Hair treatment product and hair after-treatment product containing ether guanidines as active substances, for protecting from damage caused by chemical treatment and for repairing already damaged hair
CN101955451A (en) * 2010-09-03 2011-01-26 中国石油大学(华东) Method for preparing petroleum sulfonate surfactant by falling film sulfonation
AU2011204791A1 (en) * 2004-01-20 2011-08-04 Huntsman Petrochemical Llc Novel acylalkylisethionate esters and applications in consumer products
CN104496864A (en) * 2014-12-16 2015-04-08 中国石油天然气股份有限公司 Swill-cooked dirty oil sulfonate as well as preparation method and application thereof
CN105523968A (en) * 2015-04-17 2016-04-27 陇东学院 Synthesis method of heavy crude oil sulfonate surfactant

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU2011204791A1 (en) * 2004-01-20 2011-08-04 Huntsman Petrochemical Llc Novel acylalkylisethionate esters and applications in consumer products
WO2009156241A1 (en) * 2008-06-27 2009-12-30 Evonik Goldschmidt Gmbh Hair treatment product and hair after-treatment product containing ether guanidines as active substances, for protecting from damage caused by chemical treatment and for repairing already damaged hair
CN101955451A (en) * 2010-09-03 2011-01-26 中国石油大学(华东) Method for preparing petroleum sulfonate surfactant by falling film sulfonation
CN104496864A (en) * 2014-12-16 2015-04-08 中国石油天然气股份有限公司 Swill-cooked dirty oil sulfonate as well as preparation method and application thereof
CN105523968A (en) * 2015-04-17 2016-04-27 陇东学院 Synthesis method of heavy crude oil sulfonate surfactant

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
李江石: "地沟油磺酸盐驱油剂的设计合成及使用前景研究", 《中国优秀硕士学位论文全文数据库 工程科技 I辑》 *

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107185508A (en) * 2017-06-26 2017-09-22 焦作市新科资源综合利用研发有限公司 A kind of method that utilization dichloroethanes reclaims oily waste water atlapulgite
CN109762613A (en) * 2019-02-26 2019-05-17 太原理工大学 A kind of method that novel water-coal slurry dispersing agent is prepared by bio oil
CN113880510A (en) * 2021-10-19 2022-01-04 山西省交通科技研发有限公司 Stabilizer for road base mixture and construction method thereof

Similar Documents

Publication Publication Date Title
CN103265981B (en) Alcohol-based fuel combustion improver and alcohol-based fuel
CN106833587A (en) A kind of bio oil hydroxyl sulfoacid salt production process based on kitchen waste grease
CN106630545B (en) Drying treatment method for oil-containing sludge
He et al. Enhanced biodiesel production from diseased swine fat by ultrasound-assisted two-step catalyzed process
CN101327908A (en) Method for using sludge in supercritical water for preparing hydrogen-rich gas by continuous catalysis gasification
CN104941993B (en) A kind of method for comprehensive repairing in serious pollution soil
CN105384292B (en) A kind of H acid production process for treating industrial waste water
DE602007002794D1 (en) TREATMENT OF AQUEOUS LIQUIDS AND PREPARATION OF ANTHRANILIC ACID
CN102286273B (en) Oil-in-water emulsifier as well as preparation and use methods thereof
CN106753753A (en) The extraction process of fatty acid mixed in a kind of vegetable oil residue
Shao et al. Direct humification of biowaste with hydrothermal technology: a review
RU2009133479A (en) THE PROCESS OF CHANGING THE VISCOSITY OF RAW OIL
CN104293473B (en) A kind of method that oils and fatss are extracted from oleaginous microorganism
CN109759424A (en) A kind of method for organic waste disposal
CN103333720B (en) Bio-based methanol gasoline emulsification melt water agent and preparation method thereof
CN109209268A (en) The method that drain is returned in acidification is handled using reproducibility iron powder
CN105084634A (en) Pretreatment method of rubber ingredient production wastewater
CN104356176A (en) Preparation method of tannins ether stearate
CN105670803A (en) Method for preparing biodiesel by enhancing microorganisms in excess sludge to enrich and produce grease
Ambreen et al. Anaerobic biotechnology for industrial wastewater treatment
JP2006246878A (en) Seaweed reef material given by circulating and reclaiming biomass and device thereof
CN102504917B (en) Method for producing industrial emulsion cutting fluid by using waste oil
CN104845683A (en) High-efficiency environment-friendly emulsifier
CN103865641B (en) A kind of preparation method of drilling fluid base oil
CN102807305A (en) Biological agent for treating oily sludge and using method 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
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20170613