CN107841355B - Boiler fuel oil containing industrial fusel and preparation method thereof - Google Patents

Boiler fuel oil containing industrial fusel and preparation method thereof Download PDF

Info

Publication number
CN107841355B
CN107841355B CN201711373500.XA CN201711373500A CN107841355B CN 107841355 B CN107841355 B CN 107841355B CN 201711373500 A CN201711373500 A CN 201711373500A CN 107841355 B CN107841355 B CN 107841355B
Authority
CN
China
Prior art keywords
parts
fusel
industrial
fuel oil
industrial fusel
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201711373500.XA
Other languages
Chinese (zh)
Other versions
CN107841355A (en
Inventor
李法香
孔永平
陈荣霞
刘建付
王素勤
郑冀鲁
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.)
Henan Longzheng Bioenergy Co ltd
Henan Yulong Science And Technology Research Institute Co ltd
Original Assignee
Zhengzhou Star Creation Energy Technology Co Ltd
HENAN LONGZHENG BIOLOGICAL ENERGY Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Zhengzhou Star Creation Energy Technology Co Ltd, HENAN LONGZHENG BIOLOGICAL ENERGY Co Ltd filed Critical Zhengzhou Star Creation Energy Technology Co Ltd
Priority to CN201711373500.XA priority Critical patent/CN107841355B/en
Publication of CN107841355A publication Critical patent/CN107841355A/en
Application granted granted Critical
Publication of CN107841355B publication Critical patent/CN107841355B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/02Liquid carbonaceous fuels essentially based on components consisting of carbon, hydrogen, and oxygen only
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/12Inorganic compounds
    • C10L1/1233Inorganic compounds oxygen containing compounds, e.g. oxides, hydroxides, acids and salts thereof
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/16Hydrocarbons
    • C10L1/1608Well defined compounds, e.g. hexane, benzene
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/182Organic compounds containing oxygen containing hydroxy groups; Salts thereof
    • C10L1/1822Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms
    • C10L1/1824Organic compounds containing oxygen containing hydroxy groups; Salts thereof hydroxy group directly attached to (cyclo)aliphatic carbon atoms mono-hydroxy
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/185Ethers; Acetals; Ketals; Aldehydes; Ketones
    • C10L1/1857Aldehydes; Ketones
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/192Macromolecular compounds
    • C10L1/198Macromolecular 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
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/18Organic compounds containing oxygen
    • C10L1/192Macromolecular compounds
    • C10L1/198Macromolecular 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
    • C10L1/1985Macromolecular 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
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10LFUELS 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
    • C10L1/00Liquid carbonaceous fuels
    • C10L1/10Liquid carbonaceous fuels containing additives
    • C10L1/14Organic compounds
    • C10L1/28Organic compounds containing silicon

Landscapes

  • Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Processing Of Solid Wastes (AREA)
  • Detergent Compositions (AREA)
  • Solid Fuels And Fuel-Associated Substances (AREA)

Abstract

The invention discloses boiler fuel oil containing industrial fusel, which is prepared from the following raw materials in percentage by mass: 70-80 parts of industrial fusel, 20-30 parts of durene, 2-5 parts of butanone, 2-4 parts of castor oil and ethylene oxide condensate, 3-6 parts of tween, 2-4 parts of nonylphenol polyoxyethylene ether, 3-8 parts of silane coupling agent and Na2O25-10 parts. The main raw material of the boiler fuel oil prepared by the invention is industrial fusel, the source of the raw material is guaranteed, and the cost is low; the calorific value of the boiler fuel oil is up to 9600Kcal/kg, and the calorific value of the existing boiler fuel oil prepared by using methanol is about 6000-8000 Kcal/kg.

Description

Boiler fuel oil containing industrial fusel and preparation method thereof
Technical Field
The invention belongs to the technical field of fuel oil, and particularly relates to boiler fuel oil containing industrial fusel and a preparation method thereof.
Background
Methanol is an important chemical raw material and is also a clean fuel. The development of coal-based methanol and the processing of the coal-based methanol into alcohol-containing fuel to replace petrochemical energy is a demand for the development of the chemical industry. However, in the process of preparing methanol from coal, a large amount of pungent industrial fusel is generated, the main component of the fusel is methanol, and the impurities mainly comprise water, polyhydric alcohols and amines. The calorific value of the methanol is only 5000Kcal/kg, the calorific value of the fusel is lower, and how to improve the calorific value of the fusel is a problem which needs to be solved urgently when the fusel is applied to the fields of industrial boilers and kilns.
Disclosure of Invention
The invention aims to overcome the defects of the existing fusel recycling technology and provide boiler fuel oil containing industrial fusel and a preparation method thereof.
The object of the invention is achieved in the following way:
the boiler fuel oil containing industrial fusel is prepared from the following raw materials in percentage by mass: 70-80 parts of industrial fusel, 20-30 parts of durene, 2-5 parts of butanone, 2-4 parts of castor oil and ethylene oxide condensate, 3-6 parts of tween, 2-4 parts of nonylphenol polyoxyethylene ether, 3-8 parts of silane coupling agent and Na2O25-10 parts.
The industrial fusel consists of the following raw materials in percentage by mass: 43.10-52.40 parts of methanol, 10.27-14.33 parts of ethanol, 0.35-0.49 part of propanol, 0.17-0.26 part of butanol, 31.54-36.91 parts of water and 0.001-0.002 part of trimethylamine.
The preparation method of the boiler fuel oil containing the industrial fusel comprises the following steps:
(1) filtering industrial fusel to remove upper-layer floating substances;
(2) standing and settling the fusel obtained in the step (1) to discharge the water at the lower part;
(3) adding aluminum borate into the industrial fusel obtained in the step (2) according to the alcohol-acid ratio of 1:0.0005-1:0.005, stirring for 30-50min, precipitating, and discharging acid residues; then adding Na2CO3Neutralizing, precipitating and removing residues;
(4) putting the industrial fusel obtained in the step (3) into a funnel filled with quartz sand for filtering, and further removing impurities;
(5) weighing the industrial fusel obtained in the step (4), durene and butanone according to the mass ratio, and fully mixing the industrial fusel, the durene and the butanone under the stirring condition;
(6) sequentially mixing castor oil, an ethylene oxide condensate, tween, nonylphenol polyoxyethylene ether, a silane coupling agent and Na according to the mass ratio2O2And (5) adding the mixture obtained in the step (5), and stirring for 30-50min to obtain the boiler fuel oil.
Compared with the prior art, the method uses aluminum borate to pickle the industrial fusel firstly, and then uses Na2CO3Neutralization is carried out, so that the odor of fusel can be effectively removed; the butanone is dissolved in the durene and then dissolved in the fusel, so that the heat value of the boiler fuel oil can be improved; na (Na)2O2The fuel oil is an oxygen increasing agent, so that the oxygen content of the fuel oil is increased, and the fuel oil is fully combusted; the condensation compound of castor oil and ethylene oxide is used as a dispersant to promote the uniform mixing of different substances, so that the solution becomes a uniform single phase; tween and polyoxyethylene nonyl phenyl ether are used as emulsifiers, so that the surface tension among substances is reduced, and the compatibility is improved; the silane coupling agent is an adhesive, and improves the binding performance between different functional groups to ensure that the functional groups are tightly bound. The method for producing the boiler fuel oil at normal temperature and normal pressure has the advantages of no three-waste discharge in the production process, cleanness and environmental protection. The main raw material of the boiler fuel oil prepared by the invention is industrial fusel, the source of the raw material is guaranteed, and the cost is low; the calorific value of the boiler fuel oil is up to 9600Kcal/kg, and the calorific value of the existing boiler fuel oil prepared by using methanol is about 6000-8000 Kcal/kg.
Detailed Description
The condensation compound of castor oil and ethylene oxide is sold in the market and purchased from national mechanical chemical industry Co., Ltd, Haian county; commercial fusel is commercially available from the Geranium coal industry group.
Example 1:
the boiler fuel oil containing industrial fusel is prepared from the following raw materials in percentage by mass: 70-80 parts of industrial fusel, 20-30 parts of durene, 2-5 parts of butanone, 2-4 parts of castor oil and ethylene oxide condensate, 3-6 parts of tween, 2-4 parts of nonylphenol polyoxyethylene ether, 3-8 parts of silane coupling agent and Na2O25-10 parts.
The industrial fusel consists of the following raw materials in percentage by mass: 43.10-52.40 parts of methanol, 10.27-14.33 parts of ethanol, 0.35-0.49 part of propanol, 0.17-0.26 part of butanol, 31.54-36.91 parts of water and 0.001-0.002 part of trimethylamine.
The preparation method of the boiler fuel oil containing the industrial fusel comprises the following steps:
(1) filtering industrial fusel to remove upper-layer floating substances;
(2) standing and settling the fusel obtained in the step (1) to discharge the water at the lower part;
(3) adding aluminum borate into the industrial fusel obtained in the step (2) according to the alcohol-acid ratio of 1:0.0005-1:0.005, stirring for 30-50min, precipitating, and discharging acid residues; then adding Na2CO3Neutralizing, precipitating and removing residues;
(4) putting the industrial fusel obtained in the step (3) into a funnel filled with quartz sand for filtering, and further removing impurities;
(5) weighing the industrial fusel obtained in the step (4), durene and butanone according to the mass ratio, and fully mixing the industrial fusel, the durene and the butanone under the stirring condition;
(6) sequentially mixing castor oil, an ethylene oxide condensate, tween, nonylphenol polyoxyethylene ether, a silane coupling agent and Na according to the mass ratio2O2And (5) adding the mixture obtained in the step (5), and stirring for 30-50min to obtain the boiler fuel oil.
Example 2:
the boiler fuel oil containing industrial fusel is prepared from the following raw materials in percentage by mass: 70kg of industrial fusel, 20kg of durene, 2kg of butanone, 2kg of condensation product of castor oil and ethylene oxide, 3kg of tween, 2kg of nonylphenol polyoxyethylene ether, 3kg of silane coupling agent and Na2O25kg。
The industrial fusel consists of the following raw materials in percentage by mass: 43.10kg of methanol, 10.27kg of ethanol, 0.35kg of propanol, 0.17kg of butanol, 31.54kg of water and 0.001kg of trimethylamine.
The preparation method of the boiler fuel oil containing the industrial fusel comprises the following steps:
(1) filtering industrial fusel to remove upper-layer floating substances;
(2) standing and settling the fusel obtained in the step (1) to discharge the water at the lower part;
(3) adding aluminum borate according to the alcohol-acid ratio of 1:0.0005 to the step(2) Stirring the obtained industrial fusel for 30min, and precipitating to remove acid residue; then adding Na2CO3Neutralizing, precipitating and removing residues;
(4) putting the industrial fusel obtained in the step (3) into a funnel filled with quartz sand for filtering, and further removing impurities;
(5) weighing the industrial fusel obtained in the step (4), durene and butanone according to the mass ratio, and fully mixing the industrial fusel, the durene and the butanone under the stirring condition;
(6) sequentially mixing castor oil, an ethylene oxide condensate, tween, nonylphenol polyoxyethylene ether, a silane coupling agent and Na according to the mass ratio2O2And (5) adding the mixture obtained in the step (5), and stirring for 30min to obtain the boiler fuel oil.
Example 3:
the boiler fuel oil containing industrial fusel is prepared from the following raw materials in percentage by mass: 72kg of industrial fusel, 22kg of durene, 2.5kg of butanone, 2.4kg of condensation product of castor oil and ethylene oxide, 3.5kg of Tween, 2.4kg of nonylphenol polyoxyethylene ether, 4kg of silane coupling agent and Na2O26kg。
The industrial fusel consists of the following raw materials in percentage by mass: 45.62kg of methanol, 11.05kg of ethanol, 0.38kg of propanol, 0.19kg of butanol, 32.28kg of water and 0.0012kg of trimethylamine.
The preparation method of the boiler fuel oil containing the industrial fusel comprises the following steps:
(1) filtering industrial fusel to remove upper-layer floating substances;
(2) standing and settling the fusel obtained in the step (1) to discharge the water at the lower part;
(3) adding aluminum borate into the industrial fusel obtained in the step (2) according to the alcohol-acid ratio of 1:0.001, stirring for 34min, precipitating, and discharging acid residues; then adding Na2CO3Neutralizing, precipitating and removing residues;
(4) putting the industrial fusel obtained in the step (3) into a funnel filled with quartz sand for filtering, and further removing impurities;
(5) weighing the industrial fusel obtained in the step (4), durene and butanone according to the mass ratio, and fully mixing the industrial fusel, the durene and the butanone under the stirring condition;
(6) sequentially mixing castor oil, an ethylene oxide condensate, tween, nonylphenol polyoxyethylene ether, a silane coupling agent and Na according to the mass ratio2O2And (5) adding the mixture obtained in the step (5), and stirring for 34min to obtain the boiler fuel oil.
Example 4:
the boiler fuel oil containing industrial fusel is prepared from the following raw materials in percentage by mass: 74kg of industrial fusel, 24kg of durene, 3kg of butanone, 2.8kg of condensation product of castor oil and ethylene oxide, 4kg of tween, 2.8kg of nonylphenol polyoxyethylene ether, 5kg of silane coupling agent, and Na2O27kg。
The industrial fusel consists of the following raw materials in percentage by mass: 47.25kg of methanol, 12.23kg of ethanol, 0.40kg of propanol, 0.20kg of butanol, 33.71kg of water and 0.0014kg of trimethylamine.
The preparation method of the boiler fuel oil containing the industrial fusel comprises the following steps:
(1) filtering industrial fusel to remove upper-layer floating substances;
(2) standing and settling the fusel obtained in the step (1) to discharge the water at the lower part;
(3) adding aluminum borate into the industrial fusel obtained in the step (2) according to the alcohol-acid ratio of 1:0.002, stirring for 38min, precipitating and discharging acid sludge; then adding Na2CO3Neutralizing, precipitating and removing residues;
(4) putting the industrial fusel obtained in the step (3) into a funnel filled with quartz sand for filtering, and further removing impurities;
(5) weighing the industrial fusel obtained in the step (4), durene and butanone according to the mass ratio, and fully mixing the industrial fusel, the durene and the butanone under the stirring condition;
(6) sequentially mixing castor oil, an ethylene oxide condensate, tween, nonylphenol polyoxyethylene ether, a silane coupling agent and Na according to the mass ratio2O2Adding the mixture obtained in the step (5),stirring for 38min to obtain the boiler fuel oil.
Example 5:
the boiler fuel oil containing industrial fusel is prepared from the following raw materials in percentage by mass: 76kg of industrial fusel, 26kg of durene, 3.5kg of butanone, 3.2kg of condensation product of castor oil and ethylene oxide, 4.5kg of Tween, 3.2kg of nonylphenol polyoxyethylene ether, 6kg of silane coupling agent and Na2O28kg。
The industrial fusel consists of the following raw materials in percentage by mass: 49.03kg of methanol, 13.41kg of ethanol, 0.42kg of propanol, 0.22kg of butanol, 34.62kg of water and 0.0016kg of trimethylamine.
The preparation method of the boiler fuel oil containing the industrial fusel comprises the following steps:
(1) filtering industrial fusel to remove upper-layer floating substances;
(2) standing and settling the fusel obtained in the step (1) to discharge the water at the lower part;
(3) adding aluminum borate into the industrial fusel obtained in the step (2) according to the alcohol-acid ratio of 1:0.003, stirring for 42min, precipitating and discharging acid residues; then adding Na2CO3Neutralizing, precipitating and removing residues;
(4) putting the industrial fusel obtained in the step (3) into a funnel filled with quartz sand for filtering, and further removing impurities;
(5) weighing the industrial fusel obtained in the step (4), durene and butanone according to the mass ratio, and fully mixing the industrial fusel, the durene and the butanone under the stirring condition;
(6) sequentially mixing castor oil, an ethylene oxide condensate, tween, nonylphenol polyoxyethylene ether, a silane coupling agent and Na according to the mass ratio2O2And (5) adding the mixture obtained in the step (5), and stirring for 42min to obtain the boiler fuel oil.
Example 6:
the boiler fuel oil containing industrial fusel is prepared from the following raw materials in percentage by mass: 78kg of industrial fusel, 28kg of durene, 4kg of butanone, 3.6kg of castor oil and ethylene oxide condensate, 5kg of tween, and nonylphenol polyoxyethylene3.6kg of ether, 7kg of silane coupling agent and Na2O29kg。
The industrial fusel consists of the following raw materials in percentage by mass: 50.59kg of methanol, 14.08kg of ethanol, 0.45kg of propanol, 0.24kg of butanol, 35.86kg of water and 0.0018kg of trimethylamine.
The preparation method of the boiler fuel oil containing the industrial fusel comprises the following steps:
(1) filtering industrial fusel to remove upper-layer floating substances;
(2) standing and settling the fusel obtained in the step (1) to discharge the water at the lower part;
(3) adding aluminum borate into the industrial fusel obtained in the step (2) according to the alcohol-acid ratio of 1:0.004, stirring for 46min, precipitating, and discharging acid residues; then adding Na2CO3Neutralizing, precipitating and removing residues;
(4) putting the industrial fusel obtained in the step (3) into a funnel filled with quartz sand for filtering, and further removing impurities;
(5) weighing the industrial fusel obtained in the step (4), durene and butanone according to the mass ratio, and fully mixing the industrial fusel, the durene and the butanone under the stirring condition;
(6) sequentially mixing castor oil, an ethylene oxide condensate, tween, nonylphenol polyoxyethylene ether, a silane coupling agent and Na according to the mass ratio2O2And (5) adding the mixture into the mixture obtained in the step (5), and stirring for 46min to obtain the boiler fuel oil.
Example 7:
the boiler fuel oil containing industrial fusel is prepared from the following raw materials in percentage by mass: 80kg of industrial fusel, 30kg of durene, 5kg of butanone, 4kg of condensation product of castor oil and ethylene oxide, 6kg of tween, 4kg of polyoxyethylene nonylphenol ether, 8kg of silane coupling agent and Na2O210kg。
The industrial fusel consists of the following raw materials in percentage by mass: 52.40kg of methanol, 14.33kg of ethanol, 0.49kg of propanol, 0.26kg of butanol, 36.91kg of water and 0.002kg of trimethylamine.
The preparation method of the boiler fuel oil containing the industrial fusel comprises the following steps:
(1) filtering industrial fusel to remove upper-layer floating substances;
(2) standing and settling the fusel obtained in the step (1) to discharge the water at the lower part;
(3) adding aluminum borate into the industrial fusel obtained in the step (2) according to the alcohol-acid ratio of 1:0.005, stirring for 50min, precipitating, and discharging acid residues; then adding Na2CO3Neutralizing, precipitating and removing residues;
(4) putting the industrial fusel obtained in the step (3) into a funnel filled with quartz sand for filtering, and further removing impurities;
(5) weighing the industrial fusel obtained in the step (4), durene and butanone according to the mass ratio, and fully mixing the industrial fusel, the durene and the butanone under the stirring condition;
(6) sequentially mixing castor oil, an ethylene oxide condensate, tween, nonylphenol polyoxyethylene ether, a silane coupling agent and Na according to the mass ratio2O2And (5) adding the mixture obtained in the step (5), and stirring for 50min to obtain the boiler fuel oil.
The properties of the boiler fuel oil prepared by the invention are as follows: the flash point is more than or equal to 73 ℃, the acid value (calculated by KOH) is less than or equal to 0.3mg/g, and the density is 0.842-0.883g/cm3Ash content is less than or equal to 0.002%, sulfur content is less than or equal to 0.01%, copper sheet corrosion (50 ℃, 3 h) is less than 1 grade, and kinematic viscosity is less than or equal to 6.1mm2The condensation point is less than or equal to minus 10 ℃, the cold filter plugging point is less than or equal to minus 6 ℃, and the heat value is more than or equal to 9600Kcal/kg, which reaches the national standard of GB25989-2010 furnace fuel oil.
The foregoing is only a preferred embodiment of the present invention, and it should be noted that, for those skilled in the art, various changes and modifications can be made without departing from the overall concept of the present invention, and these should also be considered as the protection scope of the present invention.

Claims (2)

1. The boiler fuel oil containing industrial fusel is characterized in that: the material is prepared from the following raw materials in percentage by mass: 70-80 parts of industrial fusel, 20-30 parts of durene, 2-5 parts of butanone, 2-4 parts of castor oil and ethylene oxide condensation compound,3-6 parts of tween, 2-4 parts of nonylphenol polyoxyethylene ether, 3-8 parts of silane coupling agent and Na2O25-10 parts;
the preparation method of the boiler fuel oil containing the industrial fusel comprises the following steps:
(1) filtering industrial fusel to remove upper-layer floating substances;
(2) standing and settling the fusel obtained in the step (1) to discharge the water at the lower part;
(3) adding aluminum borate into the industrial fusel obtained in the step (2) according to the alcohol-acid ratio of 1:0.0005-1:0.005, stirring for 30-50min, precipitating, and discharging acid residues; then adding Na2CO3Neutralizing, precipitating and removing residues;
(4) putting the industrial fusel obtained in the step (3) into a funnel filled with quartz sand for filtering, and further removing impurities;
(5) weighing the industrial fusel obtained in the step (4), durene and butanone according to the mass ratio, and fully mixing the industrial fusel, the durene and the butanone under the stirring condition;
(6) sequentially mixing castor oil, an ethylene oxide condensate, tween, nonylphenol polyoxyethylene ether, a silane coupling agent and Na according to the mass ratio2O2And (5) adding the mixture obtained in the step (5), and stirring for 30-50min to obtain the boiler fuel oil.
2. The boiler fuel oil containing industrial fusel as claimed in claim 1, characterized in that: the industrial fusel consists of the following raw materials in percentage by mass: 43.10-52.40 parts of methanol, 10.27-14.33 parts of ethanol, 0.35-0.49 part of propanol, 0.17-0.26 part of butanol, 31.54-36.91 parts of water and 0.001-0.002 part of trimethylamine.
CN201711373500.XA 2017-12-19 2017-12-19 Boiler fuel oil containing industrial fusel and preparation method thereof Active CN107841355B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711373500.XA CN107841355B (en) 2017-12-19 2017-12-19 Boiler fuel oil containing industrial fusel and preparation method thereof

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711373500.XA CN107841355B (en) 2017-12-19 2017-12-19 Boiler fuel oil containing industrial fusel and preparation method thereof

Publications (2)

Publication Number Publication Date
CN107841355A CN107841355A (en) 2018-03-27
CN107841355B true CN107841355B (en) 2019-12-24

Family

ID=61665089

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711373500.XA Active CN107841355B (en) 2017-12-19 2017-12-19 Boiler fuel oil containing industrial fusel and preparation method thereof

Country Status (1)

Country Link
CN (1) CN107841355B (en)

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101724474A (en) * 2008-10-14 2010-06-09 陈若歆 Mode for preparing M15-M100 complexing methanol petrol and gas normal-temperature liquefaction mixed combustion technology

Also Published As

Publication number Publication date
CN107841355A (en) 2018-03-27

Similar Documents

Publication Publication Date Title
CN104946288B (en) Modified coal tar pitch and preparation method thereof
CN105073943A (en) Low viscosity metal-based hydrogen sulfide scavengers
CN102733230A (en) Process for producing high-purity ammonium lignin by taking papermaking black liquid as material
CN107841355B (en) Boiler fuel oil containing industrial fusel and preparation method thereof
CN101619249B (en) Alcohol-based fuel modifier, enhancer, alcohol-based liquid fuel after modification and enhancement and production process thereof
CN210656170U (en) Recycling system of tar residue waste
CN114920489B (en) Cement raw material additive and application thereof and cement production process
CN115637168A (en) High-efficiency composite desulfurizer for oil extraction in oil and gas field
CN101165145A (en) Anti-corrosive methanol or ethanol composite fuel oil and preparation method thereof
CN104178767B (en) A kind of coking chemical waste water pyrolysis coal gas corrosion inhibiter and preparation method thereof
WO2017127988A1 (en) Scale inhibitor for oil refining technology process and preparation method therefor
CN103643043B (en) Nickel slag for comprehensive Application way
CN101781590B (en) Accelerating agent for heavy fuel oil
CN109097112B (en) Industrial alcohol-based fuel and preparation method and application thereof
CN101255349A (en) Highly effective production technique of waste oil regenerative fuel oil
CN106479585B (en) A kind of method that high concentration PVA waste water prepares water-coal-slurry
CN110724568A (en) Methanol matrix mixed clean liquid fuel and preparation method thereof
CN108949255B (en) Preparation method of biological fuel oil
CN104130808A (en) Clean liquid fuel and preparation method thereof
CN104531238B (en) A kind of high clean industrial fuel
CN102585956B (en) Briquette and preparation method thereof
CN110923025B (en) Fuel oil produced by using distillation residues of waste stripping liquid and production method thereof
CN102701986B (en) Method for preparing antioxidant for plastic or rubber processing
CN106753610A (en) The automobile-used coal derived fuel of high heating value
CN106635207A (en) Semi-coke liquor and production process thereof

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant
CP01 Change in the name or title of a patent holder
CP01 Change in the name or title of a patent holder

Address after: 459014 Liugou Village, Shaoyuan Town, Jiyuan City, Jiaozuo City, Henan Province

Patentee after: HENAN LONGZHENG BIOENERGY CO.,LTD.

Patentee after: Henan Yulong science and Technology Research Institute Co.,Ltd.

Address before: 459014 Liugou Village, Shaoyuan Town, Jiyuan City, Jiaozuo City, Henan Province

Patentee before: HENAN LONGZHENG BIOENERGY CO.,LTD.

Patentee before: ZHENGZHOU XINGCHUANG ENERGY TECHNOLOGY CO.,LTD.

TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20220114

Address after: 459014 Liugou Village, Shaoyuan Town, Jiyuan City, Jiaozuo City, Henan Province

Patentee after: HENAN LONGZHENG BIOENERGY CO.,LTD.

Address before: 459014 Liugou Village, Shaoyuan Town, Jiyuan City, Jiaozuo City, Henan Province

Patentee before: HENAN LONGZHENG BIOENERGY CO.,LTD.

Patentee before: Henan Yulong science and Technology Research Institute Co.,Ltd.

CI03 Correction of invention patent
CI03 Correction of invention patent

Correction item: Patentee|Address

Correct: Henan Yulong science and Technology Research Institute Co., Ltd.|450000 No. 45, floor 5, unit 1, building 4, No. 26, Dongqing street, high tech Industrial Development Zone, Zhengzhou, Henan Province

False: Henan Longzheng bioenergy CO., Ltd.|459014 Liugou Village, Shaoyuan Town, Jiyuan City, Jiaozuo City, Henan Province

Number: 04-02

Volume: 38