CN102925202A - FCC gasoline electrochemical desulfurization method based on ionic liquid - Google Patents

FCC gasoline electrochemical desulfurization method based on ionic liquid Download PDF

Info

Publication number
CN102925202A
CN102925202A CN2012105005159A CN201210500515A CN102925202A CN 102925202 A CN102925202 A CN 102925202A CN 2012105005159 A CN2012105005159 A CN 2012105005159A CN 201210500515 A CN201210500515 A CN 201210500515A CN 102925202 A CN102925202 A CN 102925202A
Authority
CN
China
Prior art keywords
ionic liquid
electrode
fcc gasoline
electrochemical
gasoline
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.)
Granted
Application number
CN2012105005159A
Other languages
Chinese (zh)
Other versions
CN102925202B (en
Inventor
臧树良
房大维
宋笑雨
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.)
Eric Dalian Safety Technology Group Co ltd
Original Assignee
Liaoning University
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 Liaoning University filed Critical Liaoning University
Priority to CN201210500515.9A priority Critical patent/CN102925202B/en
Publication of CN102925202A publication Critical patent/CN102925202A/en
Application granted granted Critical
Publication of CN102925202B publication Critical patent/CN102925202B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
  • Liquid Carbonaceous Fuels (AREA)

Abstract

The invention relates to an FCC gasoline electrochemical desulfurization method based on ionic liquid. The method comprises the following steps of: putting a fixed amount of ionic liquid and gasoline into an electrolytic tank, wherein the addition amount of the ionic liquid is 1/25-1/50 of that of the FCC gasoline by volume; connecting a working electrode, a counter electrode and a reference electrode with an electrolysis line with a chuck corresponding to an electrochemical workstation respectively; adjusting the electrode height so that the electrode is totally soaked in the liquid; controlling the reaction temperature to 20-80 DEG C; starting the power; and controlling the voltage to 1.0-2.5V, wherein the power-on time is 0.5-2 hours. Through the method provided by the invention, the desulfurization rate exceeds 95%, the sulfur content in the FCC gasoline can be reduced to below 10ppm, other quality indexes are not influenced, and the gasoline quality is upgraded to the European V standard. According to the invention, the technology is simple and can be performed at normal temperature under normal pressure; and moreover, the conditions are mild, byproducts are avoided, and the sulfides in fuel can be removed without changing the fuel composition.

Description

A kind of FCC gasoline electrochemical desulphurization method based on ionic liquid
Technical field
The invention belongs to chemical industry catalysis and petrol and diesel oil desulfuration field, relate in particular to a kind of electrochemical desulphurization method based on ionic liquid.
Background technology
Because electrochemical reaction is normally carried out at normal temperatures and pressures, toxicity and the hazardness all method than traditional organic synthesis are little.Electrochemical process also is the important component part of cleaning technique, and in Global Environmental Problems increasingly serious today, electrochemical techniques have demonstrated its importance more.Ionic liquid has high ionic conductivity, negligible vapour pressure and wide electrochemical window, and these character all are very important to electrochemical reaction exactly.
Countries in the world have proposed stricter requirement to the sulphur content in the oil product, and the clean oil manufacture of low sulfur content becomes the task of top priority.Because the harm that the existence of sulphur is used petroleum refining process and products thereof in the oil product is many-sided, such as corroding metal equipment, cause in poisoning of catalyst, the use procedure contaminate environment etc.Sulphur also makes the destabilization component oxidation in the oil product, and polymerization forms gelatinoid, thereby directly affects the stability of oil product, and affects oil product to additive, such as the susceptibility of octane promoter, antioxidant etc., oil quality is produced material impact.At present, be used for the multiple desulfurization technology of vehicle fuel oil, mainly comprise hydrogenating desulfurization, catalytic cracking and desulfurizing, adsorption desulfurize, abstraction desulfurization, biological desulphurization etc.For new standard of fuel, each oil company is just in the production technology of active research with the exploitation clean fuel oil both at home and abroad.
At present more existing ionic liquids are used for patent and the paper of catalysis desulfurizing oil, but used method mostly is oxidation style, or extraction-oxidation style, and the ionic liquid usage quantity is large, and are comparatively harsh for equipment and processing requirement, do not meet the requirement of green chemical industry.
Summary of the invention
The purpose of this invention is to provide a kind of method simple, pollution-free, easy handling carries out the green desulfurization method of Electrochemistry Desulfurization as ionogen with all kinds of ionic liquids.
The technical solution used in the present invention is: quantitative ionic liquid and gasoline are put into electrolyzer, the ionic liquid add-on is 1/25 to 1/50(volume ratio of FCC gasoline), with working electrode, to electrode, reference electrode respectively the chuck corresponding with electrochemical workstation connect the electrolysis circuit, adjust electrode height, electrode is immersed in the liquid entirely, the control temperature of reaction is at 20~80 ℃, power-on, control voltage 1.0~2.5V, under the normal pressure, 0.5 hour~2 hours conduction time.Take out reacted oil product and measure sulphur content with Microcoulomb comprehensive analysis instrument.Desulfurization degree reaches more than 95%, and sulphur content is reduced to below the 10ppm, reaches Europe V emission standard.
The positively charged ion of above-mentioned ionic liquid is: dialkylimidazolium, alkyl pyridine, alkylammonium, alkylphosphines, quinoline or morpholine positively charged ion.
Above-mentioned ionic liquid negatively charged ion is rehenic acid root, trifluoroacetic acid root, acetate, nitrate radical, sulfur hydrogen anion, hypochlorite, perchlorate, aluminum tetrachloride, tri-chlorination copper, titanium tetrachloride, tetrafluoroborate, hexafluoro-phosphate radical, thiocyanate ion, trifluoromethane sulfimide, trifluoromethanesulfonic acid root, two cyanamides, lactate, oxalate or each amino acid root.
The invention has the beneficial effects as follows: take out reacted oil product and measure sulphur content with Microcoulomb comprehensive analysis instrument.Desulfurization degree reaches more than 95%, and sulphur content is reduced to below the 10ppm, reaches Europe V emission standard.Adopt method of the present invention, the sulphur content in the FCC gasoline can be down to below the 10ppm, do not affect other quality index, make quality of gasoline be upgraded to Europe
Figure 983212DEST_PATH_IMAGE001
Standard.Compare with other desulfurization technologies, this technological process is simple, and normal temperature and pressure carries out, and mild condition without byproduct, can remove wherein sulfide in the situation that do not change the fuel oil component.
Embodiment
Embodiment 1:1-butyl-3-methyl-imidazoles perrhenate ionic liquid is used for electrochemical desulphurization method
1-butyl-3-methyl-imidazoles perrhenate ionic liquid and FCC gasoline are put into electrolyzer, the ionic liquid add-on is 1/50 (volume ratio) of FCC gasoline, with working electrode, to electrode, reference electrode respectively the chuck corresponding with electrochemical workstation connect the electrolysis circuit, adjust electrode height, electrode is immersed in the liquid entirely, the control temperature of reaction is at 20 ℃, power-on, control voltage 1.6V, under the normal pressure, 2 hours conduction time.Take out reacted oil product and measure sulphur content with Microcoulomb comprehensive analysis instrument.Desulfurization degree reaches more than 98%, and sulphur content is reduced to below the 10ppm by initial 500ppm, reaches Europe V emission standard.
Embodiment 2: ethylpyridine trifluoroacetate ionic liquid is used for electrochemical desulphurization method
With ethylpyridine trifluoroacetate ionic liquid, FCC gasoline is put into electrolyzer, the ionic liquid add-on is the 1/50(volume ratio of FCC gasoline), with working electrode, to electrode, reference electrode respectively the chuck corresponding with electrochemical workstation connect the electrolysis circuit, adjust electrode height, make electrode entirely immerse in the liquid, the control temperature of reaction is at 20 ℃, and power-on is controlled voltage 1.0V, under the normal pressure, 0.5 hour conduction time.Take out reacted oil product and measure sulphur content with Microcoulomb comprehensive analysis instrument.Desulfurization degree reaches more than 95%, and sulphur content is reduced to below the 10ppm by initial 500ppm, reaches Europe V emission standard.
Embodiment 3 acetic acid four octyl ammonium ion liquid are used for electrochemical desulphurization method
With acetic acid four octyl ammonium ion liquid, FCC gasoline is put into electrolyzer, and the ionic liquid add-on is the 1/25(volume ratio of FCC gasoline), with working electrode, to electrode, reference electrode respectively the chuck corresponding with electrochemical workstation connect the electrolysis circuit, adjust electrode height, electrode is immersed in the liquid entirely, control temperature of reaction at 50 ℃, power-on, control voltage 1.6 V, under the normal pressure, 1.5 hours conduction time, take out reacted oil product and measure sulphur content with Microcoulomb comprehensive analysis instrument.Sulphur content is reduced to below the 10ppm by initial 100ppm, reaches Europe V emission standard.
Embodiment 4: oxalic acid three heptyl-ethyl phosphine ionic liquid is used for electrochemical desulphurization method
With oxalic acid three heptyl-ethyl phosphine ionic liquid, FCC gasoline is put into electrolyzer, and the ionic liquid add-on is the 1/30(volume ratio of FCC gasoline), with working electrode, to electrode, reference electrode respectively the chuck corresponding with electrochemical workstation connect the electrolysis circuit, adjust electrode height, electrode is immersed in the liquid entirely, control temperature of reaction at 50 ℃, power-on, control voltage 1.5V, under the normal pressure, 1 hour conduction time, take out reacted oil product and measure sulphur content with Microcoulomb comprehensive analysis instrument.Sulphur content is reduced to below the 10ppm by initial 300ppm, reaches Europe V emission standard.
Embodiment 5: trifluoromethane sulfimide quinoline ionic liquid is used for electrochemical desulphurization method
With trifluoromethane sulfimide quinoline ionic liquid, FCC gasoline is put into electrolyzer, the ionic liquid add-on is the 1/35(volume ratio of FCC gasoline), with working electrode, to electrode, reference electrode respectively the chuck corresponding with electrochemical workstation connect the electrolysis circuit, adjust electrode height, make electrode entirely immerse in the liquid, the control temperature of reaction is at 70 ℃, power-on, control voltage 2.0V, under the normal pressure, 0.8 hour conduction time, take out reacted oil product and measure sulphur content with Microcoulomb comprehensive analysis instrument.Sulphur content is reduced to below the 10ppm by initial 200ppm, reaches Europe V emission standard.
Embodiment 6:1-ethyl-3-methylimidazole glycinate ionic liquid is used for electrochemical desulphurization method
With 1-ethyl-3-methylimidazole glycinate ionic liquid, FCC gasoline is put into electrolyzer, the ionic liquid add-on is the 1/40(volume ratio of FCC gasoline), with working electrode, to electrode, reference electrode respectively the chuck corresponding with electrochemical workstation connect the electrolysis circuit, adjust electrode height, make electrode entirely immerse in the liquid, the control temperature of reaction is at 50 ℃, power-on, control voltage 2.5V, under the normal pressure, 2 hours conduction time, take out reacted oil product and measure sulphur content with Microcoulomb comprehensive analysis instrument.Sulphur content is reduced to below the 10ppm by initial 200pm, reaches Europe V emission standard.
Embodiment 7: hypochlorous acid morpholine ionic liquid is used for electrochemical desulphurization method
With hypochlorous acid morpholine ionic liquid, FCC gasoline is put into electrolyzer, and the ionic liquid add-on is the 1/25(volume ratio of FCC gasoline), with working electrode, to electrode, reference electrode respectively the chuck corresponding with electrochemical workstation connect the electrolysis circuit, adjust electrode height, electrode is immersed in the liquid entirely, control temperature of reaction at 30 ℃, power-on, control voltage 1.2 V, under the normal pressure, 2 hours conduction time, take out reacted oil product and measure sulphur content with Microcoulomb comprehensive analysis instrument.Sulphur content is reduced to below the 10ppm by initial 125ppm, reaches Europe V emission standard.
Embodiment 8: aluminum tetrachloride propyl group pyridine ion liquid is used for electrochemical desulphurization method
With aluminum tetrachloride propyl group pyridine ion liquid, FCC gasoline is put into electrolyzer, and the ionic liquid add-on is the 1/25(volume ratio of FCC gasoline), with working electrode, to electrode, reference electrode respectively the chuck corresponding with electrochemical workstation connect the electrolysis circuit, adjust electrode height, electrode is immersed in the liquid entirely, control temperature of reaction at 80 ℃, power-on, control voltage 1.6 V, under the normal pressure, 1 hour conduction time, take out reacted oil product and measure sulphur content with Microcoulomb comprehensive analysis instrument.Sulphur content is reduced to below the 10ppm by initial 400ppm, reaches Europe V emission standard.
Embodiment 9: trifluoromethanesulfonic acid trioctylamine ionic liquid is used for electrochemical desulphurization method
With trifluoromethanesulfonic acid trioctylamine ionic liquid, FCC gasoline is put into electrolyzer, and the ionic liquid add-on is the 1/30(volume ratio of FCC gasoline), with working electrode, to electrode, reference electrode respectively the chuck corresponding with electrochemical workstation connect the electrolysis circuit, adjust electrode height, electrode is immersed in the liquid entirely, control temperature of reaction at 30 ℃, power-on, control voltage 1. 5V, under the normal pressure, 1.5 hours conduction time, take out reacted oil product and measure sulphur content with Microcoulomb comprehensive analysis instrument.Sulphur content is by initial 50ppm, and sulphur content is reduced to below the 10ppm, reaches Europe V emission standard.
Embodiment 10:1-hexyl-3-Methylimidazole lactate ions liquid is used for electrochemical desulphurization method
With 1-hexyl-3-Methylimidazole lactate ions liquid, FCC gasoline is put into electrolyzer, the ionic liquid add-on is the 1/25(volume ratio of FCC gasoline), with working electrode, to electrode, reference electrode respectively the chuck corresponding with electrochemical workstation connect the electrolysis circuit, adjust electrode height, make electrode entirely immerse in the liquid, the control temperature of reaction is at 60 ℃, power-on, control voltage 1.2 V, under the normal pressure, 2 hours conduction time, take out reacted oil product and measure sulphur content with Microcoulomb comprehensive analysis instrument.Sulphur content is reduced to below the 10ppm by initial 70ppm, reaches Europe V emission standard.

Claims (4)

1. FCC gasoline electrochemical desulphurization method based on ionic liquid, it is characterized in that step is as follows: quantitative ionic liquid and FCC gasoline are put into electrolyzer, connect working electrode, to electrode and reference electrode, adjust electrode height, make electrode entirely immerse in the liquid, plugged carries out electrolysis.
2. according to a kind of FCC gasoline electrochemical desulphurization method based on ionic liquid claimed in claim 1, it is characterized in that: in electrolysis system, consumption by volume, the consumption of FCC gasoline is 25 times to 50 times of ionic liquid consumption, in the electrolytic process, voltage is 1.0~2.5V, and temperature is 20~80 ℃, under the normal pressure, 0.5 hour~2 hours conduction time.
3. according to claim 1 or 2 described a kind of FCC gasoline electrochemical desulphurization methods based on ionic liquid, it is characterized in that: positively charged ion is dialkylimidazolium, alkyl pyridine, alkylammonium, alkylphosphines, quinoline or morpholine in the described ionic liquid.
4. according to claim 1 or 2 described a kind of FCC gasoline electrochemical desulphurization methods based on ionic liquid, it is characterized in that: negatively charged ion is rehenic acid root, trifluoroacetic acid root, acetate, nitrate radical, sulfur hydrogen anion, hypochlorite, perchlorate, aluminum tetrachloride, tri-chlorination copper, titanium tetrachloride, tetrafluoroborate, hexafluoro-phosphate radical, thiocyanate ion, trifluoromethane sulfimide, trifluoromethanesulfonic acid root, two cyanamides, lactate, oxalate or amino acid group in the described ionic liquid.
CN201210500515.9A 2012-11-30 2012-11-30 FCC gasoline electrochemical desulfurization method based on ionic liquid Active CN102925202B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201210500515.9A CN102925202B (en) 2012-11-30 2012-11-30 FCC gasoline electrochemical desulfurization method based on ionic liquid

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201210500515.9A CN102925202B (en) 2012-11-30 2012-11-30 FCC gasoline electrochemical desulfurization method based on ionic liquid

Publications (2)

Publication Number Publication Date
CN102925202A true CN102925202A (en) 2013-02-13
CN102925202B CN102925202B (en) 2015-03-11

Family

ID=47640135

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201210500515.9A Active CN102925202B (en) 2012-11-30 2012-11-30 FCC gasoline electrochemical desulfurization method based on ionic liquid

Country Status (1)

Country Link
CN (1) CN102925202B (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103242897A (en) * 2013-04-23 2013-08-14 上海交通大学 Method for removing sulfur from fuel oil through electrolytic reduction
CN103450088A (en) * 2013-09-22 2013-12-18 辽宁石油化工大学 Novel sulfonic acid functionalized rhenium ionic liquid and preparation method and application thereof
CN103467384A (en) * 2013-09-22 2013-12-25 辽宁石油化工大学 Novel carboxylic acid functional rhenium iron liquid and preparation method and application thereof
CN106881151A (en) * 2017-04-07 2017-06-23 辽宁大学 A kind of heterocycle rhenium ionic liquid and preparation method thereof and the application in EPOXIDATION OF ALKENES CATALYZED BY
CN106984358A (en) * 2017-04-07 2017-07-28 辽宁大学 A kind of heterocycle rhenium ion liquid as catalyst BV reactions
CN107916129A (en) * 2017-12-14 2018-04-17 三峡大学 A kind of method of oxidative desulfurization of fuel oils
CN110157461A (en) * 2019-05-15 2019-08-23 上饶师范学院 One kind being based on NaBH4Fuel oil extraction-deoxidized desulfurization method of electrochemical regeneration
CN114577868A (en) * 2022-02-18 2022-06-03 山东大学 Electrochemical sensor for measuring sulfur content in diesel oil

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6274026B1 (en) * 1999-06-11 2001-08-14 Exxonmobil Research And Engineering Company Electrochemical oxidation of sulfur compounds in naphtha using ionic liquids
US6338788B1 (en) * 1999-06-11 2002-01-15 Exxonmobil Research And Engineering Company Electrochemical oxidation of sulfur compounds in naphtha
CN1699518A (en) * 2004-05-20 2005-11-23 石油大学(北京) Process for desulfurization of oil products by electrochemical catalytic oxidation
CN1699519A (en) * 2004-05-20 2005-11-23 石油大学(北京) Process for desulfurization of oil products by electrochemical catalytic reduction

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6274026B1 (en) * 1999-06-11 2001-08-14 Exxonmobil Research And Engineering Company Electrochemical oxidation of sulfur compounds in naphtha using ionic liquids
US6338788B1 (en) * 1999-06-11 2002-01-15 Exxonmobil Research And Engineering Company Electrochemical oxidation of sulfur compounds in naphtha
CN1699518A (en) * 2004-05-20 2005-11-23 石油大学(北京) Process for desulfurization of oil products by electrochemical catalytic oxidation
CN1699519A (en) * 2004-05-20 2005-11-23 石油大学(北京) Process for desulfurization of oil products by electrochemical catalytic reduction

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
亓西敏,张爱健,张贵荣,薛腾,罗仪文,陆嘉星: "噻吩在离子液体中的电化学聚合及其在模拟汽油脱硫中的应用", 《环境化学》, vol. 25, no. 2, 31 March 2006 (2006-03-31), pages 183 - 186 *
朱洪法: "《石油化工辞典》", 30 June 2012, article "石油化工辞典", pages: 128 - 286 *

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103242897A (en) * 2013-04-23 2013-08-14 上海交通大学 Method for removing sulfur from fuel oil through electrolytic reduction
CN103242897B (en) * 2013-04-23 2015-04-22 上海交通大学 Method for removing sulfur from fuel oil through electrolytic reduction
CN103450088A (en) * 2013-09-22 2013-12-18 辽宁石油化工大学 Novel sulfonic acid functionalized rhenium ionic liquid and preparation method and application thereof
CN103467384A (en) * 2013-09-22 2013-12-25 辽宁石油化工大学 Novel carboxylic acid functional rhenium iron liquid and preparation method and application thereof
CN103467384B (en) * 2013-09-22 2015-05-13 辽宁石油化工大学 Novel carboxylic acid functional rhenium iron liquid and preparation method and application thereof
CN106881151A (en) * 2017-04-07 2017-06-23 辽宁大学 A kind of heterocycle rhenium ionic liquid and preparation method thereof and the application in EPOXIDATION OF ALKENES CATALYZED BY
CN106984358A (en) * 2017-04-07 2017-07-28 辽宁大学 A kind of heterocycle rhenium ion liquid as catalyst BV reactions
CN107916129A (en) * 2017-12-14 2018-04-17 三峡大学 A kind of method of oxidative desulfurization of fuel oils
CN107916129B (en) * 2017-12-14 2020-09-01 三峡大学 Method for oxidative desulfurization of fuel oil
CN110157461A (en) * 2019-05-15 2019-08-23 上饶师范学院 One kind being based on NaBH4Fuel oil extraction-deoxidized desulfurization method of electrochemical regeneration
CN110157461B (en) * 2019-05-15 2021-07-02 上饶师范学院 Based on NaBH4Electrochemical regeneration fuel oil extraction-reduction desulfurization method
CN114577868A (en) * 2022-02-18 2022-06-03 山东大学 Electrochemical sensor for measuring sulfur content in diesel oil

Also Published As

Publication number Publication date
CN102925202B (en) 2015-03-11

Similar Documents

Publication Publication Date Title
CN102925202B (en) FCC gasoline electrochemical desulfurization method based on ionic liquid
US7198712B2 (en) Processing for eliminating sulfur-containing compounds and nitrogen-containing compounds from hydrocarbon
WO2007063879A1 (en) Hydrorefining process and hydrorefined oil
CN102757809A (en) Mercaptan removal and lye regeneration device and method for gasoline light fractions
CN104941639A (en) Selective hydrogenation catalyst and preparation method and application thereof
CN102527367B (en) Catalyst for selective hydrogenation of cracked gasoline and preparation and application thereof
CN102690676A (en) FCC (fluid catalytic cracking) gasoline oxidation desulfurization method by utilizing ionic liquids
Shu et al. Mild process for reductive desulfurization of diesel fuel using sodium borohydride in situ generated via sodium metaborate electroreduction
CN103467384B (en) Novel carboxylic acid functional rhenium iron liquid and preparation method and application thereof
CN103289728A (en) Straight-run diesel oil desulfurating method
CN103450088B (en) A kind of novel sulfonic acid funtionalized rhenium ionic liquid and its preparation method and application
CN202808717U (en) Gasoline light fraction mercaptan removal and alkali liquid regeneration device
CN102925199A (en) Gasoline desulfurization method
CN201154953Y (en) System for preparing high quality gasoline by catalytic hydrocarbon recombination
CN102921457A (en) Preparation method of deodorizing activator for gasoline
CN103242897B (en) Method for removing sulfur from fuel oil through electrolytic reduction
CN102746874A (en) Method for FCC (Fluid Catalytic Cracking) gasoline oxidation sweetening with ionic liquid
CN103285940B (en) There is the Catalysts and its preparation method of hydrogenation catalyst effect and application and hydrofinishing process
CN101173184B (en) Selective hydrogenation desulfurization method for bastard gasoline
CN103881749B (en) The removal methods of thiophene-type sulfide in a kind of fuel oil
CN103805240A (en) Low-cost combined hydrofinishing method
CN103740398B (en) Method for desulfurizing fuel oil through catalytic oxidation by adopting piperidine ionic liquid
CN102453532B (en) Method for producing low-sulfur gasoline
CN102618322A (en) Method for desulfurizing fuel oil extracted by catalytic oxidation of carboxyl functionalized benzimidazole ionic liquid
CN105368492A (en) High-efficiency and environmental-friendly gasoline desulphurization method

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C14 Grant of patent or utility model
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20190920

Address after: 116000 No. 7, 8-1, Taishan Street, Shahekou District, Dalian City, Liaoning Province

Patentee after: Gao Linyu

Address before: 110136, Liaoning, Shenyang, Shenbei New Area moral South Avenue No. 58

Patentee before: Liaoning University

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20230516

Address after: No. 1, Xiaopingdao Square, Ganjingzi District, Dalian City, Liaoning Province, 116000

Patentee after: Eric (Dalian) Safety Technology Group Co.,Ltd.

Address before: 8-1, No. 7, Mount Taishan East Street, Shahekou District, Dalian City, Liaoning Province, 116000

Patentee before: Gao Linyu