CN108277052B - A kind of heavy oil, diesel oil in alcohol group compound emulsifying agent preparation method - Google Patents
A kind of heavy oil, diesel oil in alcohol group compound emulsifying agent preparation method Download PDFInfo
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- CN108277052B CN108277052B CN201810337464.XA CN201810337464A CN108277052B CN 108277052 B CN108277052 B CN 108277052B CN 201810337464 A CN201810337464 A CN 201810337464A CN 108277052 B CN108277052 B CN 108277052B
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- Prior art keywords
- parts
- component
- oil
- added
- organic solvent
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- 239000000295 fuel oil Substances 0.000 title claims abstract description 35
- 239000003995 emulsifying agent Substances 0.000 title claims abstract description 34
- 239000002283 diesel fuel Substances 0.000 title claims abstract description 27
- 238000002360 preparation method Methods 0.000 title claims abstract description 15
- -1 alcohol group compound Chemical class 0.000 title claims description 10
- 239000000178 monomer Substances 0.000 claims abstract description 31
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000011737 fluorine Substances 0.000 claims abstract description 20
- 229910052731 fluorine Inorganic materials 0.000 claims abstract description 20
- 235000021355 Stearic acid Nutrition 0.000 claims abstract description 17
- QIQXTHQIDYTFRH-UHFFFAOYSA-N octadecanoic acid Chemical compound CCCCCCCCCCCCCCCCCC(O)=O QIQXTHQIDYTFRH-UHFFFAOYSA-N 0.000 claims abstract description 17
- OQCDKBAXFALNLD-UHFFFAOYSA-N octadecanoic acid Natural products CCCCCCCC(C)CCCCCCCCC(O)=O OQCDKBAXFALNLD-UHFFFAOYSA-N 0.000 claims abstract description 17
- 239000008117 stearic acid Substances 0.000 claims abstract description 17
- LGRFSURHDFAFJT-UHFFFAOYSA-N Phthalic anhydride Natural products C1=CC=C2C(=O)OC(=O)C2=C1 LGRFSURHDFAFJT-UHFFFAOYSA-N 0.000 claims abstract description 16
- JHIWVOJDXOSYLW-UHFFFAOYSA-N butyl 2,2-difluorocyclopropane-1-carboxylate Chemical compound CCCCOC(=O)C1CC1(F)F JHIWVOJDXOSYLW-UHFFFAOYSA-N 0.000 claims abstract description 16
- 150000002191 fatty alcohols Chemical class 0.000 claims abstract description 16
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 claims abstract description 16
- 229940051841 polyoxyethylene ether Drugs 0.000 claims abstract description 16
- 229920000056 polyoxyethylene ether Polymers 0.000 claims abstract description 16
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 claims abstract description 15
- GEMHFKXPOCTAIP-UHFFFAOYSA-N n,n-dimethyl-n'-phenylcarbamimidoyl chloride Chemical compound CN(C)C(Cl)=NC1=CC=CC=C1 GEMHFKXPOCTAIP-UHFFFAOYSA-N 0.000 claims abstract description 14
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims abstract description 11
- 229910052708 sodium Inorganic materials 0.000 claims abstract description 11
- 239000011734 sodium Substances 0.000 claims abstract description 11
- 125000003158 alcohol group Chemical group 0.000 claims abstract description 10
- 150000001875 compounds Chemical class 0.000 claims abstract description 10
- QJZYHAIUNVAGQP-UHFFFAOYSA-N 3-nitrobicyclo[2.2.1]hept-5-ene-2,3-dicarboxylic acid Chemical class C1C2C=CC1C(C(=O)O)C2(C(O)=O)[N+]([O-])=O QJZYHAIUNVAGQP-UHFFFAOYSA-N 0.000 claims abstract description 9
- 238000006243 chemical reaction Methods 0.000 claims description 29
- 239000003960 organic solvent Substances 0.000 claims description 28
- 238000003756 stirring Methods 0.000 claims description 24
- 239000000243 solution Substances 0.000 claims description 17
- 239000011347 resin Substances 0.000 claims description 16
- 229920005989 resin Polymers 0.000 claims description 16
- PPBRXRYQALVLMV-UHFFFAOYSA-N Styrene Chemical compound C=CC1=CC=CC=C1 PPBRXRYQALVLMV-UHFFFAOYSA-N 0.000 claims description 14
- 239000012456 homogeneous solution Substances 0.000 claims description 13
- 239000011259 mixed solution Substances 0.000 claims description 12
- 238000009413 insulation Methods 0.000 claims description 7
- 239000000203 mixture Substances 0.000 claims description 7
- 238000010792 warming Methods 0.000 claims description 7
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 6
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 claims description 6
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 4
- NWGKJDSIEKMTRX-MDZDMXLPSA-N Sorbitan oleate Chemical compound CCCCCCCC\C=C\CCCCCCCC(=O)OCC(O)C1OCC(O)C1O NWGKJDSIEKMTRX-MDZDMXLPSA-N 0.000 claims description 3
- 229920000642 polymer Polymers 0.000 claims description 3
- 239000012948 isocyanate Substances 0.000 claims description 2
- 239000003921 oil Substances 0.000 abstract description 17
- NIXOWILDQLNWCW-UHFFFAOYSA-N acrylic acid group Chemical group C(C=C)(=O)O NIXOWILDQLNWCW-UHFFFAOYSA-N 0.000 abstract description 4
- 238000005516 engineering process Methods 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 9
- NIXOWILDQLNWCW-UHFFFAOYSA-M Acrylate Chemical compound [O-]C(=O)C=C NIXOWILDQLNWCW-UHFFFAOYSA-M 0.000 description 8
- 238000004945 emulsification Methods 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- CAQWNKXTMBFBGI-UHFFFAOYSA-N C.[Na] Chemical compound C.[Na] CAQWNKXTMBFBGI-UHFFFAOYSA-N 0.000 description 5
- VVQNEPGJFQJSBK-UHFFFAOYSA-N Methyl methacrylate Chemical compound COC(=O)C(C)=C VVQNEPGJFQJSBK-UHFFFAOYSA-N 0.000 description 5
- 239000003795 chemical substances by application Substances 0.000 description 5
- 150000002148 esters Chemical class 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 4
- 230000001804 emulsifying effect Effects 0.000 description 4
- 239000000839 emulsion Substances 0.000 description 4
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- 239000005864 Sulphur Substances 0.000 description 3
- 239000002253 acid Substances 0.000 description 3
- 239000002131 composite material Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 239000003208 petroleum Substances 0.000 description 3
- 239000002904 solvent Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- XMWRBQBLMFGWIX-UHFFFAOYSA-N C60 fullerene Chemical compound C12=C3C(C4=C56)=C7C8=C5C5=C9C%10=C6C6=C4C1=C1C4=C6C6=C%10C%10=C9C9=C%11C5=C8C5=C8C7=C3C3=C7C2=C1C1=C2C4=C6C4=C%10C6=C9C9=C%11C5=C5C8=C3C3=C7C1=C1C2=C4C6=C2C9=C5C3=C12 XMWRBQBLMFGWIX-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000010941 cobalt Substances 0.000 description 2
- 229910017052 cobalt Inorganic materials 0.000 description 2
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 229910003472 fullerene Inorganic materials 0.000 description 2
- 235000013336 milk Nutrition 0.000 description 2
- 239000008267 milk Substances 0.000 description 2
- 210000004080 milk Anatomy 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- CERQOIWHTDAKMF-UHFFFAOYSA-N Methacrylic acid Chemical compound CC(=C)C(O)=O CERQOIWHTDAKMF-UHFFFAOYSA-N 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- MOFINMJRLYEONQ-UHFFFAOYSA-N [N].C=1C=CNC=1 Chemical class [N].C=1C=CNC=1 MOFINMJRLYEONQ-UHFFFAOYSA-N 0.000 description 1
- 150000008065 acid anhydrides Chemical class 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 150000001336 alkenes Chemical class 0.000 description 1
- 150000001412 amines Chemical class 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 235000010290 biphenyl Nutrition 0.000 description 1
- 239000004305 biphenyl Substances 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000004939 coking Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 150000001924 cycloalkanes Chemical class 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 229910021389 graphene Inorganic materials 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- XLYOFNOQVPJJNP-ZSJDYOACSA-N heavy water Substances [2H]O[2H] XLYOFNOQVPJJNP-ZSJDYOACSA-N 0.000 description 1
- 208000021760 high fever Diseases 0.000 description 1
- XJRAOMZCVTUHFI-UHFFFAOYSA-N isocyanic acid;methane Chemical compound C.N=C=O.N=C=O XJRAOMZCVTUHFI-UHFFFAOYSA-N 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- ZUOUZKKEUPVFJK-UHFFFAOYSA-N phenylbenzene Natural products C1=CC=CC=C1C1=CC=CC=C1 ZUOUZKKEUPVFJK-UHFFFAOYSA-N 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- DCKVNWZUADLDEH-UHFFFAOYSA-N sec-butyl acetate Chemical compound CCC(C)OC(C)=O DCKVNWZUADLDEH-UHFFFAOYSA-N 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
- 239000010729 system oil Substances 0.000 description 1
- 125000003944 tolyl group Chemical group 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 210000002268 wool Anatomy 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L1/00—Liquid carbonaceous fuels
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- C10L1/14—Organic compounds
- C10L1/143—Organic compounds mixtures of organic macromolecular compounds with organic non-macromolecular compounds
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- C10L1/00—Liquid carbonaceous fuels
- C10L1/32—Liquid carbonaceous fuels consisting of coal-oil suspensions or aqueous emulsions or oil emulsions
- C10L1/328—Oil emulsions containing water or any other hydrophilic phase
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- C10L1/16—Hydrocarbons
- C10L1/1608—Well defined compounds, e.g. hexane, benzene
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- C10L1/18—Organic compounds containing oxygen
- C10L1/182—Organic compounds containing oxygen containing hydroxy groups; Salts thereof
- C10L1/1822—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms
- C10L1/1826—Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms poly-hydroxy
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- C10L1/1881—Carboxylic acids; metal salts thereof carboxylic group attached to an aliphatic carbon atom
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- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
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- C10L1/1886—Carboxylic acids; metal salts thereof naphthenic acid
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- C10L1/14—Organic compounds
- C10L1/18—Organic compounds containing oxygen
- C10L1/19—Esters ester radical containing compounds; ester ethers; carbonic acid esters
- C10L1/1905—Esters ester radical containing compounds; ester ethers; carbonic acid esters of di- or polycarboxylic acids
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- C10L1/192—Macromolecular compounds
- C10L1/198—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid
- C10L1/1985—Macromolecular compounds obtained otherwise than by reactions involving only carbon-to-carbon unsaturated bonds homo- or copolymers of compounds having one or more unsaturated aliphatic radicals, each having only one carbon to carbon double bond, and at least one being terminated by an acyloxy radical of a saturated carboxylic acid, of carbonic acid polyethers, e.g. di- polygylcols and derivatives; ethers - esters
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- C10L1/22—Organic compounds containing nitrogen
- C10L1/222—Organic compounds containing nitrogen containing at least one carbon-to-nitrogen single bond
- C10L1/2222—(cyclo)aliphatic amines; polyamines (no macromolecular substituent 30C); quaternair ammonium compounds; carbamates
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- C10L1/228—Organic compounds containing nitrogen containing at least one carbon-to-nitrogen double bond, e.g. guanidines, hydrazones, semicarbazones, imines; containing at least one carbon-to-nitrogen triple bond, e.g. nitriles
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- C10L1/2431—Organic compounds containing sulfur, selenium and/or tellurium sulfur bond to oxygen, e.g. sulfones, sulfoxides
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Abstract
The present invention discloses a kind of preparation method for heavy oil, the compound emulsifying agent of diesel oil in alcohol group, mass ratio including component A and B component is 3-5:1, wherein, wherein component A includes 30-60 parts of acrylic monomers, 1-10 parts of fluorine component, 1-3 parts of polyisocynate monomer, 0.1-2 parts of fatty alcohol polyoxyethylene ether, 5-10 parts of methyl benzotriazazole;B component includes 0.5-10 parts of sulfomethylated humic acid sodium, 5-20 parts of sorbester p17,1-30 parts of cobalt naphthenate, 5-10 parts of ethylenediamine, 15-25 parts of phthalic anhydride, 4-8 parts of stearic acid.The compound emulsifying agent of this technology production can be used for oil products system, be widely used, and production is simple, and cost is relatively low, and stability is good.
Description
Technical field
The present invention relates to a kind of systems of the high-efficiency environment friendly energy-conservation emulsifier in emulsifier more particularly to heavy oil, diesel oil in alcohol group
Preparation Method.
Background technique
The energy is the lifeline of national security, wherein non-renewable petroleum resources are that most important the energy safety of supply is asked
One of topic.In order to effectively construct energy security, each state all attaches great importance to oil consumption and deposit, and various methods is taken actively to grind
Study carefully reduction or substitutes the consumption of petroleum resources.With science and technology and economic rapid development, the practical owning amount of the automobile in China and by
This caused oil demand is always in rapid growth.Auto industry is one of the mainstay of the national economy industry in China, since
Since 2010, auto industry accounts for 5.5% or more of the specific gravity of GDP, and China's auto output has leapt to third place in the world, accounted for about
The 6%~8% of world car total output.According to statistics, China is in motor benzines in 2018 and diesel consumption total amount than 2014
It nearly doubles, reaches 300,000,000 tons or so, therefore petrol and diesel oil problem in short supply will be more serious.
Heavy oil and diesel oil in alcohol group are all a kind of important fuel, many in oil plant, chemical plant, steel mill and power plant etc.
Place generally all uses heavy oil as fuel, still, since heavy oil is petroleum deep processing surplus materials, no matter which kind of high fever is used
The combustion apparatus of effect, direct combusting heavy oil inevitably cause combustion reaction incomplete, form black smoke, coking and carbon deposit,
The problem of causing fuel largely to waste, while also bringing environmental pollution.It is abundant generally for burning is guaranteed, excessive sky need to be injected
Gas, and heat has been taken away in the discharge of these excess airs, causes thermal loss.
To generally burn after heavy oil emulsive to solve the above problems at present, but do not have also it is a kind of effectively can make emulsification after
Heavy oil active combustion, while can also environmental emission reduction emulsifier.
Summary of the invention
For overcome the deficiencies in the prior art, the present invention provides that a kind of performance is stable, can efficiently synthesize heavy oil, also has section
It can the heavy oil of environment protecting, the high-efficiency environment friendly energy-conservation emulsifier in diesel oil and preparation method thereof.In addition, the composite milk of the application
Agent can be also used for emulsification alcohol radical-diesel oil system, so that diesel oil in alcohol group is steadily in the state of alcohol oil-in always, effective
It is not layered in time limit.
The technical solution of the present invention is as follows: the preparation method of a kind of heavy oil, diesel oil in alcohol group environment-friendly type compound emulsifying agent, including with
Lower step:
A, organic solvent is added in reaction kettle, is warming up to 50-70 DEG C, then mix acrylate monomer, fluorochemical monomer
It closes uniformly, then is slowly dropped into organic solvent, control feed time, charging, which finishes, continues insulation reaction 2-4h, stops reaction simultaneously
It is cooled to room temperature to obtain fluorine-containing oligomer resin solution;
B, it by fatty alcohol polyoxyethylene ether, polyisocynate monomer investment fluorine-containing oligomer resin solution, fills
After dividing 1~2h of stirring, methyl benzotriazazole, stirring is added, reaction 1h obtains component A mixed solution;
C, by sulfomethylated humic acid sodium, sapn, cobalt naphthenate, ethylenediamine stirs evenly at 40-70 DEG C according to the proportion, then
Phthalic anhydride and stearic acid is added, continues to stir 1h, forms B component homogeneous solution;
D, the B component homogeneous solution of step c is added in the component A mixed solution that step b is obtained, is kept for 40-60 DEG C
1-3h is reacted, excessive organic solvent is removed, obtains mixed emulsifier, preferably 50 DEG C of reaction condition, 2h;
Wherein,
Component A includes the component of following mass fraction:
About 30-60 parts of acrylic monomers,
1-10 parts of fluorine component,
1-3 parts of polyisocynate monomer,
0.1-2 parts of fatty alcohol polyoxyethylene ether,
5-10 parts of methyl benzotriazazole;
B component includes the component of following mass fraction:
0.5-10 parts of sulfomethylated humic acid sodium,
5-20 parts of sorbester p17,
1-30 parts of cobalt naphthenate,
5-10 parts of ethylenediamine,
15-25 parts of phthalic anhydride,
4-8 parts of stearic acid.
Preferably, the mass ratio of compound emulsifying agent of the present invention, component A and B component is 3-5:1, wherein A group agent
Component and its weight fraction ratio are as follows: 40-50 parts of acrylic monomers, 5-10 parts of fluorine component, 1-2 parts of polyisocynate monomer,
0.1-1 parts of fatty alcohol polyoxyethylene ether, 5-8 parts of methyl benzotriazazole;
The component and its weight fraction ratio of B group agent are as follows: 0.5-3 parts of sulfomethylated humic acid sodium, 8-10 parts of sorbester p17, cycloalkanes
Sour cobalt 10-20 parts, 8-10 parts of ethylenediamine, 15-20 parts of phthalic anhydride, 4-6 parts of stearic acid.
Wherein, it according to mass ratio is 1:(2- that the acrylate monomer, which is styrene, methyl methacrylate or the two,
20) it forms;The fluorine component is Hexafluorobutyl mathacrylate.
The polyisocynate monomer is toluene di-isocyanate(TDI) and its polymer, 4,4- diphenylmethane diisocyanate
One of ester or its multiple combinations.
The organic solvent is propylene glycol or ethylene glycol.
In the present invention, because generating fluorine-containing propene acid oligomer using acrylate monomer in component A and fluorochemical monomer polymerization,
So that polymer shows certain physico-chemical properties of fluorochemical to a certain extent.Therefore, to have excellent hydrophobicity same
When, it is also equipped with certain oil repellency, can steadily emulsify alcohol-containing-oil interface or heavy oil, diesel oil system, increases alcohols and bavin
The intersolubility of oil, application system is extensive, and effect stability;Because feeding intake using the naphthenic compound in group agent B and suitably
Proportion, has the function of catalytic combustion-supporting, to make emulsifier of the invention by after heavy oil emulsive, the discharge of heavy oil combustion subtracts significantly
It is few, SO2Discharge can reduce 90% or more, the work that methyl benzotriazazole also prevents gasoline engine or diesel-engine equipment from corroding
With;The emulsifiers such as component B stearic acid, phthalic anhydride, make emulsifier of the invention have very strong emulsifying capacity, heavy oil emulsification when,
The ratio of heavy oil and water can reach 1:1, and the heavy oil after emulsification is the molecular structure of water-in-oil type, and the heavy oil storage one after emulsification
Year or more be for a long time not in water-oil separating, performance is highly stable.
Emulsifier of the invention can be applied not only to emulsification heavy oil, while can also be applied to diesel oil emulsification or contain alcohol
Base-diesel oil system combines compound system, and application is good, and the compound emulsifying agent of formation has stability good, is easy recycling,
The advantages of recycling.
Emulsifier of the invention can effectively emulsify heavy oil, diesel oil or fuel oil, make emulsification after heavy oil, diesel oil or
It can more effectively burn, it, can fuel-economizing 35%-45%, reduction SO after heavy oil uses emulsifier of the invention290% or more discharge, storage
Depositing 1 year or more is not in water-oil separating, and performance is highly stable.The present invention is by a part of conventional heavy oils emulsifier component and newly
Type resin emulsifier forms composite emulsifying system, heavy wool system can be emulsified, small for different oil product usage amounts,
Preparation method is simple, at low cost, can be recycled, and the stability of oil emulsion is good, not stratified, is taking into account the same of many body system oil product raw material
When, good emulsifying effectiveness may be implemented.
Specific embodiment
The present invention will be further described in detail with reference to the specific embodiments.
Embodiment 1
The preparation method of heavy oil, alcohol radical-diesel oil high efficiency composition emulsifier, by component A and B component according to mass ratio 3:1
It is prepared in organic solvents, wherein component A includes styrene and methyl methacrylate 30-60 parts, methacrylic acid six
1-10 parts of fluorine butyl ester, 4,4- 1-3 parts of methyl diphenylene diisocyanates, 0.1-2 parts of fatty alcohol polyoxyethylene ether, methyl benzo three
5-10 parts of nitrogen azoles;B component includes 0.5-10 parts of sulfomethylated humic acid sodium, and 5-20 parts of sorbester p17,1-30 parts of cobalt naphthenate, second two
5-10 parts of amine, 15-25 parts of phthalic anhydride, 4-8 parts of stearic acid.It prepares: organic solvent being added in reaction kettle in accordance with the following methods a,
It is warming up to 50-70 DEG C, is then uniformly mixed acrylate monomer, fluorochemical monomer, then be slowly dropped into organic solvent, control adds
Expect the time, charging, which finishes, continues insulation reaction 2-4h, stops reacting and is cooled to room temperature to obtain fluorine-containing oligomer resin
Solution;B, it by fatty alcohol polyoxyethylene ether, polyisocynate monomer investment fluorine-containing oligomer resin solution, sufficiently stirs
After mixing 1~2h, methyl benzotriazazole, stirring is added, reaction 1h obtains mixed solution;C, by methyl sodium humate, sapn, ring
Alkanoic acid cobalt, ethylenediamine are stirred evenly at 40-70 DEG C according to the proportion, and phthalic anhydride and stearic acid is then added, and continue to stir 1h, are formed equal
Even solution;D, the homogeneous solution of step c is added in the mixed solution that step b is obtained, keeps 40-60 DEG C of reaction 1-3h, root
According to needs, excessive organic solvent is removed, mixed emulsifier is obtained.
Embodiment 2
The preparation method of heavy oil, alcohol radical-diesel oil high efficiency composition emulsifier, by component A and B component according to mass ratio 3:1
It is prepared in organic solvents, wherein component A includes 30 parts of styrene, and 1 part of Hexafluorobutyl mathacrylate, 4,4- diphenyl
1 part of methane diisocyanate, 0.1 part of fatty alcohol polyoxyethylene ether, 5 parts of methyl benzotriazazole;B component includes sulphur methyl humic
0.5 part of sour sodium, 5 parts of sorbester p17,1 part of cobalt naphthenate, 5 parts of ethylenediamine, 15 parts of phthalic anhydride, 4 parts of stearic acid.It makes in accordance with the following methods
It is standby: a, organic solvent is added in reaction kettle, is warming up to 50 DEG C, is then uniformly mixed acrylate monomer, fluorochemical monomer, then
It is slowly dropped into organic solvent, controls feed time, charging, which finishes, continues insulation reaction 2h, stops reacting and being cooled to room temperature
To fluorine-containing oligomer resin solution;B, fatty alcohol polyoxyethylene ether, polyisocynate monomer are put into fluorine-containing
In oligomer resin solution, after 1h is sufficiently stirred, methyl benzotriazazole, stirring is added, reaction 1h obtains mixed solution;C, will
Methyl sodium humate, sapn, cobalt naphthenate, ethylenediamine are stirred evenly at 40 DEG C according to the proportion, and phthalic anhydride and stearic acid is then added,
Continue to stir 1h, forms homogeneous solution;D, the homogeneous solution of step c is added in the mixed solution that step b is obtained, keeps 40
DEG C reaction 1h, as needed, remove excessive organic solvent, obtain mixed emulsifier.
Embodiment 3
The preparation method of heavy oil, alcohol radical-diesel oil high efficiency composition emulsifier, by component A and B component according to mass ratio 3:1
It is prepared in organic solvents, wherein component A includes 40 parts of methyl methacrylate, and 5 parts of Hexafluorobutyl mathacrylate, 4,
2 parts of 4- methyl diphenylene diisocyanate, 1 part of fatty alcohol polyoxyethylene ether, 8 parts of methyl benzotriazazole;B component includes sulphur first
5 parts of base sodium humate, 10 parts of sorbester p17,10 parts of cobalt naphthenate, 6 parts of ethylenediamine, 20 parts of phthalic anhydride, 6 parts of stearic acid.According to following
Organic solvent: a, being added in reaction kettle, be warming up to 60 DEG C by method preparation, then mixes acrylate monomer, fluorochemical monomer
Uniformly, it then is slowly dropped into organic solvent, controls feed time, charging, which finishes, continues insulation reaction 3h, and stopping reaction is simultaneously cooling
Fluorine-containing oligomer resin solution is obtained to room temperature;B, fatty alcohol polyoxyethylene ether, polyisocynate monomer investment are contained
In perfluoroalkyl acrylate oligomer resin solution, after 1~2h is sufficiently stirred, methyl benzotriazazole, stirring is added, reaction 1h is mixed
Close solution;C, by methyl sodium humate, sapn, cobalt naphthenate, ethylenediamine stirs evenly at 50 DEG C according to the proportion, and benzene is then added
Acid anhydride and stearic acid continue to stir 1h, form homogeneous solution;D, that the homogeneous solution of step c is added to the mixing that step b is obtained is molten
In liquid, 50 DEG C of reaction 2h are kept, as needed, excessive organic solvent is removed, obtains mixed emulsifier.
Embodiment 4
The preparation method of heavy oil, alcohol radical-diesel oil high efficiency composition emulsifier, by component A and B component according to mass ratio 3:1
It is prepared in organic solvents, wherein component A includes styrene and 60 parts of methyl methacrylate, methacrylic acid hexafluoro fourth
10 parts of ester, 4,4- 3 parts of methyl diphenylene diisocyanates, 2 parts of fatty alcohol polyoxyethylene ether, 10 parts of methyl benzotriazazole;B group
Point include 10 parts of sulfomethylated humic acid sodium, 20 parts of sorbester p17,30 parts of cobalt naphthenate, 10 parts of ethylenediamine, 25 parts of phthalic anhydride, stearic acid
8 parts.Prepare: organic solvent being added in reaction kettle in accordance with the following methods a, be warming up to 70 DEG C, then by acrylate monomer,
Fluorochemical monomer is uniformly mixed, then is slowly dropped into organic solvent, and feed time is controlled, and charging, which finishes, continues insulation reaction 4h, is stopped
It only reacts and is cooled to room temperature to obtain fluorine-containing oligomer resin solution;B, by fatty alcohol polyoxyethylene ether, polyisocyanic acid
Ester monomer is put into fluorine-containing oligomer resin solution, and after 2h is sufficiently stirred, methyl benzotriazazole is added, stirs, instead
1h is answered to obtain mixed solution;C, by methyl sodium humate, sapn, cobalt naphthenate, ethylenediamine stirs evenly at 70 DEG C according to the proportion,
Then phthalic anhydride and stearic acid is added, continues to stir 1h, forms homogeneous solution;D, the homogeneous solution of step c step b is added to obtain
To mixed solution in, keep 60 DEG C of reaction 3h, as needed, remove excessive organic solvent, obtain mixed emulsifier.
Embodiment 5
The preparation method of heavy oil, alcohol radical-diesel oil high efficiency composition emulsifier, by component A and B component according to mass ratio 2:1
It is prepared in organic solvents, wherein component A includes styrene and 50 parts of methyl methacrylate, methacrylic acid hexafluoro fourth
8 parts of ester, 4,4- 2 parts of methyl diphenylene diisocyanates, 1 part of fatty alcohol polyoxyethylene ether, 6 parts of methyl benzotriazazole;B component
Including 8 parts of sulfomethylated humic acid sodium, 10 parts of sorbester p17,20 parts of cobalt naphthenate, 7 parts of ethylenediamine, 16 parts of phthalic anhydride, 6 parts of stearic acid.
Prepare: organic solvent being added in reaction kettle in accordance with the following methods a, be warming up to 50-60 DEG C, then by acrylate monomer, contain
Fluorine monomer is uniformly mixed, then is slowly dropped into organic solvent, and feed time is controlled, and charging, which finishes, continues insulation reaction 2-3h, is stopped
It only reacts and is cooled to room temperature to obtain fluorine-containing oligomer resin solution;B, by fatty alcohol polyoxyethylene ether, polyisocyanic acid
Ester monomer is put into fluorine-containing oligomer resin solution, and after 2h is sufficiently stirred, methyl benzotriazazole is added, stirs, instead
1h is answered to obtain mixed solution;C, by methyl sodium humate, sapn, cobalt naphthenate, ethylenediamine stirs at 40-50 DEG C equal according to the proportion
It is even, phthalic anhydride and stearic acid is then added, continues to stir 1h, forms homogeneous solution;D, the homogeneous solution of step c is added to step
In the mixed solution that b is obtained, 40-50 DEG C of reaction 1-3h is kept, as needed, excessive organic solvent is removed, obtains composite milk
Agent.
By oil product: compound emulsifying agent: solvent: graphene or fullerene are according to 100-120:10-20:5-10:0.1-1 weight
Than obtaining oil emulsion after mixing, our experiments show that, it can stablize after oil emulsion is static not stratified;For heavy oil emulsive, by one
Year or more still there is not water-oil separating, and sulphur-containing substance discharge can be reduced with fuel-economizing 30%, for diesel oil in alcohol group, due to tool
There is the effect of part resin, diesel oil in alcohol group can dissolve each other very well, less carbon emission, and component A can be played with component B and be cooperateed with work
With the consumption of diesel oil or heavy oil can be substantially reduced, and can reduce petrochemical industry cost, while being applicable in multiple systems, to simultaneously
System with diesel oil and/or diesel oil in alcohol group has good emulsifying effectiveness.
Application examples 1
100kg heavy oil is taken, 60 DEG C is heated to and stirs evenly, adds 10 kg emulsifiers, 5g solvent, 0.1g fullerene, warp
Appropriate 60 DEG C of water is added in high-speed stirred 5-15min as needed, uses after standing 24 hours.
Application examples 2
120kg diesel oil in alcohol group is taken, 60 DEG C is heated to and stirs evenly, adds 10 kg emulsifiers, 10g solvent, 0.5g fowler
Alkene, through high-speed stirred 5-15min, the water of 70 DEG C of addition, which is mixed evenly, as needed becomes high-efficiency environment friendly oil emulsion, quiet
It is used after setting 24 hours.
The above description is merely a specific embodiment, but scope of protection of the present invention is not limited thereto, any
Those skilled in the art within the technical scope disclosed by the invention, can without the variation that creative work is expected or
Replacement, should be covered by the protection scope of the present invention.Therefore, protection scope of the present invention should be limited with claims
Subject to fixed protection scope.
Claims (2)
1. a kind of preparation method for heavy oil, the compound emulsifying agent of diesel oil in alcohol group, which comprises the following steps:
A, organic solvent is added in reaction kettle, is warming up to 50-70 DEG C, then mix styrene, Hexafluorobutyl mathacrylate
It closes uniformly, then is slowly dropped into organic solvent, control feed time, charging, which finishes, continues insulation reaction 2-4h, stops reaction simultaneously
It is cooled to room temperature to obtain fluorine-containing oligomer resin solution;
B, it by fatty alcohol polyoxyethylene ether, polyisocynate monomer investment fluorine-containing oligomer resin solution, sufficiently stirs
After mixing 1~2h, methyl benzotriazazole, stirring is added, reaction 1h obtains component A mixed solution;
C, by sulfomethylated humic acid sodium, sapn, cobalt naphthenate, ethylenediamine stirs evenly at 40-70 DEG C according to the proportion, is then added
Phthalic anhydride and stearic acid continue to stir 1h, form B component homogeneous solution;
D, the B component homogeneous solution of step c is added in the component A mixed solution that step b is obtained, keeps 50 DEG C of reaction 2h,
Excessive organic solvent is removed, compound emulsifying agent is obtained;
Wherein,
Wherein component A is grouped as by the group of following mass fraction:
30 parts of styrene,
1 part of Hexafluorobutyl mathacrylate,
1 part of polyisocynate monomer,
0.1 part of fatty alcohol polyoxyethylene ether,
5 parts of methyl benzotriazazole;
B component is grouped as by the group of following mass fraction:
0.5 part of sulfomethylated humic acid sodium,
5 parts of sorbester p17,
1 part of cobalt naphthenate,
5 parts of ethylenediamine,
15 parts of phthalic anhydride,
4 parts of stearic acid;
The polyisocynate monomer is in toluene di-isocyanate(TDI) and its polymer, 4,4- methyl diphenylene diisocyanate
One kind or its multiple combinations, organic solvent be propylene glycol or ethylene glycol.
2. preparation method according to claim 1, which is characterized in that the mass ratio of component A and B component is 3-5:1.
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CN1153203A (en) * | 1995-12-08 | 1997-07-02 | 刘志强 | Fuel oil emulsifying agent |
CN102226117A (en) * | 2011-05-12 | 2011-10-26 | 周鼎力 | Preparation method of diesel emulsifier and emulsified diesel for vehicles and ships |
CN102676249A (en) * | 2012-06-05 | 2012-09-19 | 广州埃尔辟能源科技有限公司 | High-efficiency environment-friendly energy-saving emulsifier for heavy oil, diesel oil or fuel oil and preparation method of emulsifier |
CN104818057A (en) * | 2015-04-10 | 2015-08-05 | 中山职业技术学院 | Automobile alcohol-based diesel oil composite resin type emulsifier, preparation method and auxiliary agent with application of emulsifier |
-
2016
- 2016-03-24 CN CN201810337464.XA patent/CN108277052B/en not_active Expired - Fee Related
- 2016-03-24 CN CN201610170704.2A patent/CN105802682B/en not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1153203A (en) * | 1995-12-08 | 1997-07-02 | 刘志强 | Fuel oil emulsifying agent |
CN102226117A (en) * | 2011-05-12 | 2011-10-26 | 周鼎力 | Preparation method of diesel emulsifier and emulsified diesel for vehicles and ships |
CN102676249A (en) * | 2012-06-05 | 2012-09-19 | 广州埃尔辟能源科技有限公司 | High-efficiency environment-friendly energy-saving emulsifier for heavy oil, diesel oil or fuel oil and preparation method of emulsifier |
CN104818057A (en) * | 2015-04-10 | 2015-08-05 | 中山职业技术学院 | Automobile alcohol-based diesel oil composite resin type emulsifier, preparation method and auxiliary agent with application of emulsifier |
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CN105802682B (en) | 2018-07-06 |
CN108277052A (en) | 2018-07-13 |
CN105802682A (en) | 2016-07-27 |
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