CN108998062A - A kind of method that carbolineum prepares pitch - Google Patents

A kind of method that carbolineum prepares pitch Download PDF

Info

Publication number
CN108998062A
CN108998062A CN201810907227.2A CN201810907227A CN108998062A CN 108998062 A CN108998062 A CN 108998062A CN 201810907227 A CN201810907227 A CN 201810907227A CN 108998062 A CN108998062 A CN 108998062A
Authority
CN
China
Prior art keywords
carbolineum
pitch
prepares
beaker
flask
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201810907227.2A
Other languages
Chinese (zh)
Inventor
李艳红
李根明
訾昌毓
张静
张登峰
赵文波
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.)
Kunming University of Science and Technology
Original Assignee
Kunming University of Science and Technology
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 Kunming University of Science and Technology filed Critical Kunming University of Science and Technology
Priority to CN201810907227.2A priority Critical patent/CN108998062A/en
Publication of CN108998062A publication Critical patent/CN108998062A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10CWORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
    • C10C3/00Working-up pitch, asphalt, bitumen
    • CCHEMISTRY; METALLURGY
    • C10PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10CWORKING-UP PITCH, ASPHALT, BITUMEN, TAR; PYROLIGNEOUS ACID
    • C10C3/00Working-up pitch, asphalt, bitumen
    • C10C3/02Working-up pitch, asphalt, bitumen by chemical means reaction

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Civil Engineering (AREA)
  • Structural Engineering (AREA)
  • Materials Engineering (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Working-Up Tar And Pitch (AREA)

Abstract

The present invention discloses a kind of method that carbolineum prepares pitch, after carbolineum is warming up to 200~300 DEG C, catalyst is added, catalyst accounts for the 10~30% of carbolineum and catalyst gross mass, magnetic agitation, and 4~30h of insulation reaction obtains pitch after cooling;The method of the present invention simple process, reaction condition is mild, and bitumen product yield is high, and economy is stronger, and the method for the present invention increases the carbolineum purposes of high value.

Description

A kind of method that carbolineum prepares pitch
Technical field
The present invention relates to a kind of methods that carbolineum prepares pitch, belong to coal tar pitch technical field of refinement.
Background technique
The product that carbolineum is coal tar after 250~370 DEG C of distillations, China are maximum coke production state and to disappear in the world Fei Guo produces 600~8,000,000 tons of coal tar per year, accounts for about the 1/3 of the world, and about 1,000,000 tons of carbolineum.It is more due to scale and technical reason Using roughing, it is mainly used as carbon black raw oil, fuel oil and pitch ready-mixed oil, added value is lower, and economic benefit is poor, as Low-grade fuel oil environmental pollution is larger.Pitch has huge demand in China, has extensively in road pavement and needle coke etc. General application.Traditional asphalt is mainly derived from petroleum coking, and coal tar asphalt cannot replace petroleum due to its special property Pitch, and China's oil demand relies on import, and therefore, a kind of method for researching and developing carbolineum production novel asphalt is pendulum every Glorious and arduous mission in face of a pitch scientific worker.
The conventionally employed oxidizing process of pitch is produced, chemical polymerization etc., the oxidizing process production time is longer, and step is many and diverse, chemistry Polymerization catalyst is easy inactivation, requires harsh and yield not high reaction condition, limits its popularization and application.
Summary of the invention
In view of the problems of the existing technology and insufficient, the present invention provides a kind of method that carbolineum prepares pitch, more specifically Be a kind of carbolineum catalytic polymerization production novel asphalt method, this method simple process, reaction condition is mild, and bitumen product Have high yield and high softening point, lower needle penetration and stronger economy, increases carbolineum purposes.
The invention is realized by the following technical scheme:
A kind of method that carbolineum prepares pitch, after carbolineum is warming up to 200~300 DEG C, be added catalyst, catalyst account for carbolineum and The 10~30% of catalyst gross mass, magnetic agitation, 4~30h of insulation reaction obtain pitch after cooling.
The carbolineum is product of the coal tar after 250~370 DEG C of distillations.
The heating rate is 4~6 DEG C/min.
The catalyst is sulphur.
The revolving speed of the magnetic agitation is 25~50 revs/min.
The method production pitch can be used for road asphalt or needle coke.
The beneficial effects of the present invention are:
1, the present invention use sulphur as polymerization catalyst production pitch, passes through the initial concentration of control sulphur, reaction temperature, when reaction Between control the performance of pitch, increase the purposes of carbolineum.
2, the yield and production efficiency that the present invention greatly improves, reduce production cost, are conducive to the production of carbolineum catalytic polymerization The industrialized production and application of novel asphalt.
Specific embodiment
With reference to embodiment, the invention will be further described.
Embodiment 1
A kind of method that carbolineum prepares pitch, takes 120g carbolineum to pour into dried beaker, pours into three-necked flask, and three mouthfuls An appropriately sized rotor is placed in flask, then three-necked flask is put into constant temperature blender with magnetic force, is opened recirculated water, is followed For ring water by spherical condensating tube bottom in and top out, the revolving speed of regulating thermostatic magnetic stirring apparatus is 25 turns/min, is warming up to 5 DEG C/min 200 DEG C of reaction temperature, constant temperature to reaction terminates, logical after experimental temperature is stablized in the beaker after taking sulphur 13.33g to be placed in drying It crosses funnel to be added from the side port of three-neck flask, after 200 DEG C of heat preservation 4h, closes magnetic stirring apparatus, stand disassembly reaction dress after 10min It sets, the pitch in three-neck flask is poured into dried beaker and be placed in natural cooling in draught cupboard.
Acquired asphalt softening point is 42.5 DEG C, needle penetration 80.2, ductility 300mm.
Embodiment 2
A kind of method that carbolineum prepares pitch, takes 120g carbolineum to pour into dried beaker, pours into three-necked flask, and three mouthfuls An appropriately sized rotor is placed in flask, then three-necked flask is put into constant temperature blender with magnetic force, is opened recirculated water, is followed For ring water by spherical condensating tube bottom in and top out, the revolving speed of regulating thermostatic magnetic stirring apparatus is 40 turns/min, is warming up to 4 DEG C/min 200 DEG C of reaction temperature, constant temperature to reaction terminates, logical after experimental temperature is stablized in the beaker after taking sulphur 13.33g to be placed in drying It crosses funnel to be added from the side port of three-neck flask, after 200 DEG C of heat preservation 4h, closes magnetic stirring apparatus, stand disassembly reaction dress after 10min It sets, the pitch in three-neck flask is poured into dried beaker and be placed in natural cooling in draught cupboard.
Acquired asphalt softening point is 44 DEG C, needle penetration 79.4, ductility 298mm.
Embodiment 3
A kind of method that carbolineum prepares pitch, takes 120g carbolineum to pour into dried beaker, pours into three-necked flask, and three mouthfuls An appropriately sized rotor is placed in flask, then three-necked flask is put into constant temperature blender with magnetic force, is opened recirculated water, is followed For ring water by spherical condensating tube bottom in and top out, the revolving speed of regulating thermostatic magnetic stirring apparatus is 50 turns/min, is warming up to 5 DEG C/min 200 DEG C of reaction temperature, constant temperature to reaction terminates, logical after experimental temperature is stablized in the beaker after taking sulphur 13.33g to be placed in drying It crosses funnel to be added from the side port of three-neck flask, after 200 DEG C of heat preservation 4h, closes magnetic stirring apparatus, stand disassembly reaction dress after 10min It sets, the pitch in three-neck flask is poured into dried beaker and be placed in natural cooling in draught cupboard.
Acquired asphalt softening point is 45 DEG C, needle penetration 79.4, ductility 298mm.
Embodiment 4
A kind of method that carbolineum prepares pitch, takes 120g carbolineum to pour into dried beaker, pours into three-necked flask, and three mouthfuls An appropriately sized rotor is placed in flask, then three-necked flask is put into constant temperature blender with magnetic force, is opened recirculated water, is followed For ring water by spherical condensating tube bottom in and top out, the revolving speed of regulating thermostatic magnetic stirring apparatus is 40 turns/min, is warming up to 5 DEG C/min 250 DEG C of reaction temperature, constant temperature to reaction terminates, logical after experimental temperature is stablized in the beaker after taking sulphur 13.33g to be placed in drying It crosses funnel to be added from the side port of three-neck flask, after 250 DEG C of heat preservation 4h, closes magnetic stirring apparatus, stand disassembly reaction dress after 10min It sets, the pitch in three-neck flask is poured into dried beaker and be placed in natural cooling in draught cupboard.
Acquired asphalt softening point is 52.5 DEG C, needle penetration 64.2, ductility 282mm.
Embodiment 5
A kind of method that carbolineum prepares pitch, takes 120g carbolineum to pour into dried beaker, pours into three-necked flask, and three mouthfuls An appropriately sized rotor is placed in flask, then three-necked flask is put into constant temperature blender with magnetic force, is opened recirculated water, is followed For ring water by spherical condensating tube bottom in and top out, the revolving speed of regulating thermostatic magnetic stirring apparatus is 25 turns/min, is warming up to 6 DEG C/min 300 DEG C of reaction temperature, constant temperature to reaction terminates, logical after experimental temperature is stablized in the beaker after taking sulphur 13.33g to be placed in drying It crosses funnel to be added from the side port of three-neck flask, after 300 DEG C of heat preservation 4h, closes magnetic stirring apparatus, stand disassembly reaction dress after 10min It sets, the pitch in three-neck flask is poured into dried beaker and be placed in natural cooling in draught cupboard.
Acquired asphalt softening point is 80.2 DEG C, needle penetration 50.1, ductility 242mm.
Embodiment 6
A kind of method that carbolineum prepares pitch, takes 120g carbolineum to pour into dried beaker, pours into three-necked flask, and three mouthfuls An appropriately sized rotor is placed in flask, then three-necked flask is put into constant temperature blender with magnetic force, is opened recirculated water, is followed For ring water by spherical condensating tube bottom in and top out, the revolving speed of regulating thermostatic magnetic stirring apparatus is 40 turns/min, is warming up to 5 DEG C/min 250 DEG C of reaction temperature, constant temperature to reaction terminates, logical after experimental temperature is stablized in the beaker after taking sulphur 13.33g to be placed in drying It crosses funnel to be added from the side port of three-neck flask, after 250 DEG C of heat preservation 5h, closes magnetic stirring apparatus, stand disassembly reaction dress after 10min It sets, the pitch in three-neck flask is poured into dried beaker and be placed in natural cooling in draught cupboard.
Acquired asphalt softening point is 80.2 DEG C, needle penetration 50.1, ductility 242mm.
Embodiment 7
A kind of method that carbolineum prepares pitch, takes 120g carbolineum to pour into dried beaker, pours into three-necked flask, and three mouthfuls An appropriately sized rotor is placed in flask, then three-necked flask is put into constant temperature blender with magnetic force, is opened recirculated water, is followed Ring water is by spherical condensating tube bottom in and top out, and the revolving speed of regulating thermostatic magnetic stirring apparatus is 40 turns/min, and temperature is with 4 DEG C/min liter Temperature arrives 200 DEG C of reaction temperature, and constant temperature to reaction terminates, in the beaker after taking sulphur 21.18g to be placed in drying, when experimental temperature is stablized It is added afterwards by funnel from the side port of three-neck flask, after 200 DEG C of heat preservation 4h, closes magnetic stirring apparatus, disassembly is anti-after standing 10min Device is answered, the pitch in three-neck flask is poured into dried beaker and is placed in natural cooling in draught cupboard.
Acquired asphalt softening point is 50.5 DEG C, needle penetration 75.2, ductility 292mm.
Embodiment 8
A kind of method that carbolineum prepares pitch, takes 120g carbolineum to pour into dried beaker, pours into three-necked flask, and three mouthfuls An appropriately sized rotor is placed in flask, then three-necked flask is put into constant temperature blender with magnetic force, is opened recirculated water, is followed Ring water is by spherical condensating tube bottom in and top out, and the revolving speed of regulating thermostatic magnetic stirring apparatus is 40 turns/min, and temperature is with 5 DEG C/min liter Temperature arrives 200 DEG C of reaction temperature, and constant temperature to reaction terminates, in the beaker after taking sulphur 51.42g to be placed in drying, after experimental temperature is stablized It is added by funnel from the side port of three-neck flask, after 200 DEG C of heat preservation 4h, closes magnetic stirring apparatus, dismantle reaction after standing 10min Pitch in three-neck flask is poured into dried beaker and is placed in natural cooling in draught cupboard by device.
Acquired asphalt softening point is 98.3 DEG C, needle penetration 72.5, ductility 212mm.
Embodiment 9
A kind of method that carbolineum prepares pitch, takes 120g carbolineum to pour into dried beaker, pours into three-necked flask, and three mouthfuls An appropriately sized rotor is placed in flask, then three-necked flask is put into constant temperature blender with magnetic force, is opened recirculated water, is followed Ring water is by spherical condensating tube bottom in and top out, and the revolving speed of regulating thermostatic magnetic stirring apparatus is 40 turns/min, and temperature is with 5 DEG C/min liter Temperature arrives 200 DEG C of reaction temperature, and constant temperature to reaction terminates, in the beaker after taking sulphur 13.33g to be placed in drying, experimental temperature and stabilization It is added afterwards by funnel from the side port of three-neck flask, after 200 DEG C of heat preservation 10h, closes magnetic stirring apparatus, dismantled after standing 10min Pitch in three-neck flask is poured into dried beaker and is placed in natural cooling in draught cupboard by reaction unit.
Acquired asphalt softening point is 50.5 DEG C, needle penetration 70.2, ductility 288mm.
Embodiment 10
A kind of method that carbolineum prepares pitch, takes 120g carbolineum to pour into dried beaker, pours into three-necked flask, and three mouthfuls An appropriately sized rotor is placed in flask, then three-necked flask is put into constant temperature blender with magnetic force, is opened recirculated water, is followed Ring water is by spherical condensating tube bottom in and top out, and the revolving speed of regulating thermostatic magnetic stirring apparatus is 40 turns/min, and temperature is with 5 DEG C/min liter Temperature arrives 200 DEG C of reaction temperature, and constant temperature to reaction terminates, in the beaker after taking sulphur 13.33g to be placed in drying, experimental temperature and stabilization It is added afterwards by funnel from the side port of three-neck flask, after 200 DEG C of heat preservation 20h, closes magnetic stirring apparatus, dismantled after standing 10min Pitch in three-neck flask is poured into dried beaker and is placed in natural cooling in draught cupboard by reaction unit.
Acquired asphalt softening point is 63.5 DEG C, needle penetration 56.2, ductility 248mm.
Embodiment 11
A kind of method that carbolineum prepares pitch, takes 120g carbolineum to pour into dried beaker, pours into three-necked flask, and three mouthfuls An appropriately sized rotor is placed in flask, then three-necked flask is put into constant temperature blender with magnetic force, is opened recirculated water, is followed Ring water is by spherical condensating tube bottom in and top out, and the revolving speed of regulating thermostatic magnetic stirring apparatus is 40 turns/min, and temperature is with 5 DEG C/min liter Temperature arrives 200 DEG C of reaction temperature, and constant temperature to reaction terminates, in the beaker after taking sulphur 13.33g to be placed in drying, experimental temperature and stabilization It is added afterwards by funnel from the side port of three-neck flask, after 200 DEG C of heat preservation 30h, closes magnetic stirring apparatus, dismantled after standing 10min Pitch in three-neck flask is poured into dried beaker and is placed in natural cooling in draught cupboard by reaction unit.
Acquired asphalt softening point is 66.5 DEG C, needle penetration 51.2, ductility 237mm.
Above the embodiment of the present invention is explained in detail, but the present invention is not limited to above-mentioned embodiment party Formula can also be made without departing from the purpose of the present invention within the knowledge of a person skilled in the art Various change out.

Claims (5)

1. a kind of method that carbolineum prepares pitch, which is characterized in that after carbolineum is warming up to 200~300 DEG C, catalyst is added, Catalyst accounts for the 10~30% of carbolineum and catalyst gross mass, magnetic agitation, and 4~30h of insulation reaction obtains pitch after cooling.
2. the method that carbolineum prepares pitch according to claim 1, which is characterized in that the carbolineum is coal tar 250~ Product after 370 DEG C of distillations.
3. the method that carbolineum prepares pitch according to claim 1, which is characterized in that the heating rate be 4~6 DEG C/ min。
4. the method that carbolineum prepares pitch according to claim 1, which is characterized in that the catalyst is sulphur.
5. the method that carbolineum prepares pitch according to claim 1, which is characterized in that the revolving speed of the magnetic agitation be 25~ 50 revs/min.
CN201810907227.2A 2018-08-10 2018-08-10 A kind of method that carbolineum prepares pitch Pending CN108998062A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810907227.2A CN108998062A (en) 2018-08-10 2018-08-10 A kind of method that carbolineum prepares pitch

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810907227.2A CN108998062A (en) 2018-08-10 2018-08-10 A kind of method that carbolineum prepares pitch

Publications (1)

Publication Number Publication Date
CN108998062A true CN108998062A (en) 2018-12-14

Family

ID=64595517

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810907227.2A Pending CN108998062A (en) 2018-08-10 2018-08-10 A kind of method that carbolineum prepares pitch

Country Status (1)

Country Link
CN (1) CN108998062A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109536189A (en) * 2018-12-29 2019-03-29 山东齐创石化工程有限公司 The production technology of needle coke

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6228343B1 (en) * 1996-09-06 2001-05-08 Mitsubishi Gas Chemical Company, Inc. Method for producing isotropic pitch, activated carbon fibers and carbon materials for non-aqueous secondary battery anodes
CN102977906A (en) * 2012-11-15 2013-03-20 四川创越炭材料有限公司 Preparing method of high-purity arene oligomerization asphalt
CN104593033A (en) * 2015-01-12 2015-05-06 中钢集团鞍山热能研究院有限公司 Preparation method of high-performance environment-friendly asphalt

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6228343B1 (en) * 1996-09-06 2001-05-08 Mitsubishi Gas Chemical Company, Inc. Method for producing isotropic pitch, activated carbon fibers and carbon materials for non-aqueous secondary battery anodes
CN102977906A (en) * 2012-11-15 2013-03-20 四川创越炭材料有限公司 Preparing method of high-purity arene oligomerization asphalt
CN104593033A (en) * 2015-01-12 2015-05-06 中钢集团鞍山热能研究院有限公司 Preparation method of high-performance environment-friendly asphalt

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
ADELA L. FERNANDEZ: "Carbon Precursors from Anthracene Oil. Insight into the Reactions of Anthracene Oil with Sulfur", 《ENERGY & FUELS》 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109536189A (en) * 2018-12-29 2019-03-29 山东齐创石化工程有限公司 The production technology of needle coke

Similar Documents

Publication Publication Date Title
CN104650938A (en) Co-production technique of needle coke, mesocarbon microbeads and high-quality asphalt
CN101838542B (en) Manufacturing method of ultra-temperature pitch
CN103436280B (en) Coal directly-liquefied residue is utilized to prepare the method for coke
CN104774635A (en) Treatment method for acid washing and deashing of coal liquefaction residue
CN103740396B (en) The method of modifying of modifying asphalt, DCL/Direct coal liquefaction hard pitch and application thereof
CN105778968A (en) Method for preparing impregnating pitch, impregnating pitch and application thereof
CN103756703B (en) Modifying asphalt, the serialization of coal directly-liquefied residue normal pressure is utilized to prepare method and the application thereof of modifying asphalt
CN109517614A (en) Distillation produces various asphalt Product Process and device in conjunction with extraction phase
CN108998062A (en) A kind of method that carbolineum prepares pitch
CN103555363A (en) High-acid-content raw material oil hydrogen-donating delayed coking method
CN104789248B (en) Method for preparing mesophase pitch by coal-tar pitch
CN103756706B (en) Modified asphalt and preparation method thereof
CN103740400A (en) Method for preparing high-quality needle coke raw material by removing QI (Quinoline Insolubles) in coal tar
CN102304382A (en) Process for coproducing aromatic oil, asphalt and fuel oil
CN109504416B (en) Production process of coal-based needle coke
CN104327879B (en) A kind of combination process producing oil fuel, aromatic hydrocarbon oil, pitch
CN105861014A (en) Method for preparing impregnation pitch using direct coal liquefaction residue, impregnation pitch and application thereof
CN209508153U (en) Distillation produces various asphalt Product Process device in conjunction with extraction phase
CN104479707A (en) Method and device of preparing needle coke
CN101676365A (en) Method for directly producing road asphalt by mild cracking super-heavy crude oil
CN105255510A (en) Method for determining parameters of solvent method based refined asphalt preparing process by utilizing phase diagram
CN112812796B (en) Bio-based needle coke and preparation method thereof
CN203440308U (en) Device for preparing needle coke by using maltha as raw material
CN103756707B (en) Modified asphalt and preparation method thereof
CN102911689A (en) Impregnated pitch with low quinoline insoluble content, low softening point and high residual carbon and preparation process and application of impregnated pitch

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
RJ01 Rejection of invention patent application after publication
RJ01 Rejection of invention patent application after publication

Application publication date: 20181214