CN100371420C - Modified coal tar, and producing method - Google Patents
Modified coal tar, and producing method Download PDFInfo
- Publication number
- CN100371420C CN100371420C CNB2005100475887A CN200510047588A CN100371420C CN 100371420 C CN100371420 C CN 100371420C CN B2005100475887 A CNB2005100475887 A CN B2005100475887A CN 200510047588 A CN200510047588 A CN 200510047588A CN 100371420 C CN100371420 C CN 100371420C
- Authority
- CN
- China
- Prior art keywords
- coal
- pitch
- temperature
- tar
- modified coal
- 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.)
- Expired - Fee Related
Links
Landscapes
- Working-Up Tar And Pitch (AREA)
Abstract
The present invention belongs to the technical field of chemical engineering, and relates to resinified modified coal asphalt with adjustable softening point in a certain range and a production method thereof. The present invention is characterized in that the modified coal asphalt is prepared from one of coal tar, or coal tar extract, anthracene oil, carbolic oil, naphthalene oil, or coal pitch with the softening point less than 130 DEG, or the mixture of more than one raw material. The pH value is adjusted by acid, and the modified coal asphalt carries out polymerization reaction with formaldehyde, trioxymethylene or paraformaldehyde. Through controlling the temperature, the pressure and the time of the polymerization reaction, modified coal asphalt with adjustable softening point in a certain range, wide softening temperature range, large plasticity and a linear resin molecular structure is produced. The raw material sources are wide, and thus, the price is suitable. The present invention has the advantages of simple technological process, little equipment investment, easy operation, little land occupation, low cost, high output and obvious effect. The method can artificially control the product performance, and satisfy the requirements of different levels, the product quality is good, and the performance is stable.
Description
Technical field
The invention belongs to chemical technology field, relate to a kind of resinification, adjustable within the specific limits modified coal pitch of softening temperature and production method thereof.
Background technology
Coal-tar pitch is the residue after coal tar distillation extracts cut, mainly elementary composition by C, H, C/H is generally 18/1, the chemical constitution of coal-tar pitch is very complicated, kind surplus the eutectic mixture of the multiple composition that it has been established that has 70, therefore utilize solvent-extracted method that coal-tar pitch is divided into different material groups, i.e. appellation α component, β component, γ component, its characterizes the general characteristic of coal-tar pitch.The α component: softening fusion when heating separately, be present in the coal-tar pitch with solid-state form, belong to difficult greying component, but the residual carbon amount of α component can improve the coal-tar pitch coking time.The β component: be the main composition that plays cohesive action in the coal-tar pitch, the β components contents is high more, and the cohesiveness of coal-tar pitch is good, and coking value is big more, and the structure that is generated is fibrous, has preferably easily graphitization characteristic.γ component: in coal-tar pitch, play solvent action, coal-tar pitch is had good dispersiveness, perviousness, application property, usability.For existing common medium temperature coal pitch, because the γ component concentration is than higher, corresponding softening temperature is lower, and generally between 65-95 ℃, coal-tar pitch viscosity reduces constructing strong, has made things convenient for use.But follow the β component concentration lower simultaneously, can reduce coal-tar pitch coking value and cohesive strength, the coal-tar pitch exhaust gas volumn that adds thermogenesis is bigger, causes environmental pollution.For addressing the above problem, developed at present the modification technology of various coal-tar pitch, mean that coal-tar pitch handles through thermopolymerization, make a part of β component be converted into the α component, part γ component is converted into the β component, thereby to obtain softening temperature be 100-120 ℃, the massfraction of β component greater than 18%, α constituent mass mark is at the fat coal pitch of 6%-15%.Wish to improve the massfraction of β component in the coal-tar pitch as ideal coal-tar pitch modification technology, but do not wish that a part of β component is converted into the α component in the coal-tar pitch.With manufacturing enterprise's investigation, do not find the modified coal pitch product of directly producing with the raw material of coal-tar pitch or production coal-tar pitch by literature search by the aldehydes polymerization.Retrieval Chinese patent ZL991026748 disclosed a kind of efficient asphalt soaker and preparation method thereof is to be raw material with coal-tar pitch or petroleum pitch, adds the durol of 5-15%, the bitumen-impregnated method that adopts the pressurization chemical copolymerization to obtain.It is raw material that Chinese patent ZL011352817 discloses with quadrol, formaldehyde, enanthic acid, phenyl aldehyde, through the method for amine aldehyde, amino acid condensation synthetic asphalts properties-correcting agent.Chinese patent ZL961223944 discloses aromatic hydroxy compound durol, poly methylbenzene and linking agent formaldehyde, trioxymethylene and Paraformaldehyde 96, catalyzer toluene sulfonic acide, phosphoric acid, chloric acid or sulfonic acid, the method for the synthetic aromatic hydrocarbons oligopolymer of meticulous crosslinking reaction under 60-150 ℃.Above-mentioned patent is not strong to the component selectivity of wanting modification in the coal-tar pitch, does not embody the coal-tar pitch resinifying.Also there are its production method more complicated, cost problem of higher.
Summary of the invention
The present invention has overcome the defective of above-mentioned existence, purpose is the resinifying technology to coal-tar pitch, selectively with the volatilizable composition of γ component, convert resin to as far as possible, require not increase α component concentration in the coal-tar pitch, make coal-tar pitch have the linear resin characteristic, adjustable within the specific limits modified coal pitch of a kind of softening temperature and production method thereof are provided.
Modified coal pitch of the present invention and production method content Description thereof:
Modified coal pitch of the present invention and production method thereof, it is characterized in that: the material choice of preparation modified coal pitch: adopt coal tar, or coal tar extract carbolineum, carbolic oil, naphtalene oil, or＜a kind of in 130 ℃ of softening temperature coal-tar pitch, or above-mentioned more than one mixture is raw material, with formaldehyde, trioxymethylene or Paraformaldehyde 96 generation chemical reaction;
The production method of modified coal pitch is finished through the following steps:
(1), raw material is added reactor, control temperature in the kettle＜100 ℃;
(2), 100 parts coal tar by weight, or 100 parts coal tar extract carbolineum, carbolic oil, naphtalene oil, or 100 parts＜a kind of in 130 ℃ of softening temperature coal-tar pitch, or 100 parts above-mentioned more than one mixture is a raw material, the formaldehyde, trioxymethylene or the Paraformaldehyde 96 that add 0.1-60 part
(3), adjust pH value, in still, add acid, preferably HCl is adjusted at pH between the 0.001-6.5;
(4), polyreaction: close atmospheric dump valve after interior boiling of still and backflow situation are normal, make by heat temperature raising and polyreaction to form pressure in the still, the peak pressure＜1.0Mpa in the control still, dwell time was at 0.1-24 hour, polyreaction is finished, and puts pressure gas, makes the still internal pressure return zero;
(5), neutralization reaction: start stirrer, add alkaloids in still, preferred NaOH is adjusted at pH between the 6-8;
(6), vacuum exhaust, release discharge: the control temperature in the kettle is greater than the coal-tar pitch softening temperature, start vacuum pump, starting stirrer, slowly regulate vacuum tightness in the still, is the boundary not produce fierce bubble, volatilization along with moisture content, temperature raises gradually, during moisture content in detecting still＜2%, stops heating, eliminate vacuum, blowing.
When the coal-tar pitch pH value to modification does not require, can omit step (5).
When the coal-tar pitch of modification is not controlled moisture content, can omit step (6).
When coal-tar pitch softening temperature＞98 after the modification ℃, also can omit step (6), adopt 100 ℃ of-150 ℃ of modes of direct heating temperature to get rid of moisture content in the modified coal pitch.
Compare with existing coal-tar pitch product with the modified coal pitch that the present invention produces, have:
1, as the perfect adhesion agent of greying carbon element electrode, α change of component amount can be controlled in＜below 1.0%, directly replace the dipping coal-tar pitch, reach the result of use of dipping coal-tar pitch with the production technology of common coal-tar pitch, simultaneously can increase carbon pole content more than 1%, improve pole strength nearly 5%.
2, be used for prebaked anode, cathode carbon pieces wedding agent, compare with international coal-tar pitch, kneading temperature reduces by 20 ℃, and the coal-tar pitch of 85 ℃ of softening temperatures improves intensity 2% than 106 ℃ of softening temperature GB modified coal asphalts; Be used for negative electrode and stick with paste, adopt bituminization agent accelerated solidification, not only improve, and it is nearly 80% to save baking cathode can time and energy consumption, reduces negative electrode simultaneously and sticks with paste volumetric shrinkage in cathode can intensity.
3, replace carbon containing refractory and comprise magnesium, the typing of aluminium matter or indefinite form product wedding agent resin, can reduce by 5 times of wedding agent production costs, improve use properties simultaneously more than 10%, with the converter thermal-state repair material is example, can reduce the coal-tar pitch smoke discharge amount more than 50%, improve repair material work-ing life 30% simultaneously.
The production method of modified coal pitch has: all raw materials that common law is produced coal-tar pitch comprise that coal-tar pitch all can be used as the raw materials for production of modified coal pitch, so raw material sources are extensive, and price is suitable; Technical process is simple, facility investment is few, easy to operate, floor space is little, cost is low, output is high, instant effect; This method can make coal-tar pitch realize the resinifying characteristic; This method is easy to control the structure and the composition of product.Adjust molecular resin amount content and size by extent of polymerization, the realization softening point temperature can be adjusted, and makes the coal-tar pitch inerting, reduces the coal-tar pitch smoke discharge amount; Can artificially control and produce the crystallinity energy, satisfy the needs of different levels, good quality of product, stable performance, the coal-tar pitch that this method can the production various uses.
Embodiment
Embodiment one
Take by weighing coal tar 500g and put into reactor, under agitation condition, be warming up to 85 ℃ with 5 ℃/min heat-up rate; The formalin 75g that adds content 35%, add 25% the HCl aqueous solution, adjusting pH value of water solution is 0.1, control temperature of reaction kettle＜130 ℃, reaction mass is at 0.2Mpa pressure, constant 90min, polyreaction finishes, after the still internal pressure is zero, being evacuated down to moisture＜2% detects, softening temperature is 10 ℃, and the α component concentration is brought up to reaction back 1.01% by reaction preceding 1.00%, and the β component concentration is 8.7%.
Embodiment two
Take by weighing naphtalene oil 500g and put into reactor, be warming up to 65 ℃ with 3 ℃/min heat-up rate; The Paraformaldehyde 96 aqueous solution that adds 100g content 30%, the H of adding 30%
3PO
4The aqueous solution, adjusting pH value of water solution is 1.0, control temperature of reaction kettle＜125 ℃, reaction mass is at 0.2Mpa pressure, constant 60min, polyreaction finishes, after the still internal pressure is zero, be evacuated down to moisture＜2% and detect, softening temperature is 18 ℃, and the β component concentration is 9.5%.
Embodiment three
Taking by weighing softening temperature is that 78 ℃ of coal-tar pitch 1000g put into reactor, is warming up to 90 ℃ with 3 ℃/min heat-up rate; The trioxymethylene aqueous solution that adds 150g content 30%, the H of adding 30%
2SO
4The aqueous solution, adjusting pH value of water solution is 0.2, control reaction temperature＜130 ℃, reaction mass is at 0.25Mpa pressure, constant 120min, polyreaction finishes, after the still internal pressure is zero, add the 30%NaOH aqueous solution, adjusting the pH value is 7.0, is evacuated down to moisture＜2% and detects, and softening temperature is brought up to 134 ℃ by 78 ℃, the α component concentration is brought up to reaction back 7.26% by reaction preceding 7.25%, and the β component concentration is 30.6%.
Embodiment four
Taking by weighing softening temperature is that 10 ℃ of carbolineum 500g put into reactor, is warming up to 45 ℃ with 3 ℃/min heat-up rate; The formalin 80g that adds content 37%, the HNO of adding 20%
3The aqueous solution, adjusting pH value of water solution is 1, control reaction temperature＜120 ℃, reaction mass are at 0.15Mpa pressure, constant 60min, polyreaction finishes, the still internal pressure is evacuated down to moisture＜2% and detects after being zero, and softening temperature is brought up to 46 ℃ by 10 ℃, not changing before and after the reaction of α component concentration all is 1.56%, and the β component concentration is 17.8%.
Embodiment five
Take by weighing carbolic oil 500g and put into reactor, be warming up to 55 ℃ with 3 ℃/min heat-up rate; The Paraformaldehyde 96 aqueous solution 60g that adds content 36%, the aqueous acetic acid of adding 10%, adjusting pH value of water solution is 0.8, control reaction temperature＜124 ℃, and reaction mass is at 0.18Mpa pressure, constant 60min, polyreaction finishes, and the still internal pressure is evacuated down to moisture＜2% and detects after being zero, softening temperature is 24 ℃, and the β component concentration is 15.6%.
Claims (9)
1. the production method of a modified coal pitch, it is characterized in that: the material choice of preparation modified coal pitch: adopt coal tar, or coal tar extract carbolineum, carbolic oil, naphtalene oil, or＜a kind of in 130 ℃ of softening temperature coal-tar pitch, or above-mentioned more than one mixture is a raw material, with formaldehyde, trioxymethylene or Paraformaldehyde 96 generation chemical reaction, the production method of modified coal pitch is finished through the following steps:
(1), raw material is added reactor, control temperature in the kettle＜100 ℃;
(2), 100 parts coal tar by weight, or 100 parts coal tar extract carbolineum, carbolic oil, naphtalene oil, or 100 parts＜a kind of in 130 ℃ of softening temperature coal-tar pitch, or 100 parts above-mentioned more than one mixture is raw material, adds formaldehyde, trioxymethylene or the Paraformaldehyde 96 of 0.1-60 part;
(3), adjust the pH value, in still, add acid, pH is adjusted between the 0.001-6.5;
(4), polyreaction: close atmospheric dump valve after interior boiling of still and backflow situation are normal, make by heat temperature raising and polyreaction to form pressure in the still, the peak pressure＜1.0Mpa in the control still, dwell time was at 0.1-24 hour, polyreaction is finished, and puts pressure gas, makes the still internal pressure return zero;
(5), neutralization reaction: start stirrer, in still, add alkaloids, pH is adjusted between the 6-8;
(6), vacuum exhaust, release discharge: the control temperature in the kettle is greater than the coal-tar pitch softening temperature, start vacuum pump, starting stirrer, slowly regulate vacuum tightness in the still, is the boundary not produce fierce bubble, volatilization along with moisture content, temperature raises gradually, during moisture content in detecting still＜2%, stops heating, eliminate vacuum, blowing.
2. the production method of modified coal pitch according to claim 1 is characterized in that: when the coal-tar pitch pH value to modification does not require, can omit step (5).
3. the production method of modified coal pitch according to claim 1 is characterized in that: when the coal-tar pitch of modification is not controlled moisture content, can omit step (6).
4. the production method of modified coal pitch according to claim 1 is characterized in that: when coal-tar pitch softening temperature＞98 after the modification ℃, also can omit step (6), adopt 100 ℃ of-150 ℃ of modes of direct heating temperature to get rid of moisture content in the modified coal pitch.
5. the production method of modified coal pitch according to claim 1 is characterized in that: take by weighing coal tar 500g and put into reactor, under agitation condition, be warming up to 85 ℃ with 5 ℃/min heat-up rate; The formalin 75g that adds content 35% adds 25% the HCl aqueous solution, and adjusting pH value of water solution is 0.1, control temperature of reaction kettle＜130 ℃, and reaction mass is at 0.2Mpa pressure, constant 90min, polyreaction finishes.
6. the production method of modified coal pitch according to claim 1 is characterized in that: take by weighing naphtalene oil 500g and put into reactor, be warming up to 65 ℃ with 3 ℃/min heat-up rate; The Paraformaldehyde 96 aqueous solution that adds 100g content 30%, the H of adding 30%
3PO
4The aqueous solution, adjusting pH value of water solution is 1.0, control temperature of reaction kettle＜125 ℃, reaction mass is at 0.2Mpa pressure, constant 60min, polyreaction finishes.
7. the production method of modified coal pitch according to claim 1, it is characterized in that: taking by weighing softening temperature is that 78 ℃ of coal-tar pitch 1000g put into reactor, is warming up to 90 ℃ with 3 ℃/min heat-up rate; The trioxymethylene aqueous solution that adds 150g content 30%, the H of adding 30%
2SO
4The aqueous solution, adjusting pH value of water solution is 0.2, control reaction temperature＜130 ℃, reaction mass is at 0.25Mpa pressure, constant 120min, polyreaction finishes.
8. the production method of modified coal pitch according to claim 1, it is characterized in that: taking by weighing softening temperature is that 10 ℃ of carbolineum 500g put into reactor, is warming up to 45 ℃ with 3 ℃/min heat-up rate; The formalin 80g that adds content 37%, the HNO of adding 20%
3The aqueous solution, adjusting pH value of water solution is 1, control reaction temperature＜120 ℃, reaction mass is at 0.15Mpa pressure, constant 60min, polyreaction finishes.
9. the production method of modified coal pitch according to claim 1 is characterized in that: take by weighing carbolic oil 500g and put into reactor, be warming up to 55 ℃ with 3 ℃/min heat-up rate; The Paraformaldehyde 96 aqueous solution 60g that adds content 36% adds 10% aqueous acetic acid, and adjusting pH value of water solution is 0.8, control reaction temperature＜124 ℃, and reaction mass is at 0.18Mpa pressure, constant 60min, polyreaction finishes.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100475887A CN100371420C (en) | 2005-10-27 | 2005-10-27 | Modified coal tar, and producing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2005100475887A CN100371420C (en) | 2005-10-27 | 2005-10-27 | Modified coal tar, and producing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1760331A CN1760331A (en) | 2006-04-19 |
| CN100371420C true CN100371420C (en) | 2008-02-27 |
Family
ID=36706554
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2005100475887A Expired - Fee Related CN100371420C (en) | 2005-10-27 | 2005-10-27 | Modified coal tar, and producing method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100371420C (en) |
Families Citing this family (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102504206A (en) * | 2011-10-26 | 2012-06-20 | 中国石油大学(华东) | Method for preparing high-viscosity heat-resistant resin with ethylene tar as raw material |
| CN102976773B (en) * | 2012-11-23 | 2014-07-30 | 上海柯瑞冶金炉料有限公司 | Coal tar pitch binding agent and preparation method thereof |
| CN103756707B (en) * | 2014-01-16 | 2015-06-03 | 神华集团有限责任公司 | Modified asphalt and preparation method thereof |
| CN103756703B (en) * | 2014-01-16 | 2015-12-02 | 神华集团有限责任公司 | Modifying asphalt, the serialization of coal directly-liquefied residue normal pressure is utilized to prepare method and the application thereof of modifying asphalt |
| CN103756705B (en) * | 2014-01-16 | 2015-06-03 | 神华集团有限责任公司 | Modified asphalt and preparation method thereof |
| CN103755926B (en) * | 2014-01-16 | 2016-03-23 | 神华集团有限责任公司 | Condensation multinuclear polyaromatic hydrocarbon resin and preparation method thereof |
| CN103740396B (en) * | 2014-01-16 | 2015-11-11 | 神华集团有限责任公司 | The method of modifying of modifying asphalt, DCL/Direct coal liquefaction hard pitch and application thereof |
| CN103740395B (en) * | 2014-01-16 | 2015-05-20 | 神华集团有限责任公司 | Modified asphalt and preparation method thereof |
| CN111138670B (en) * | 2020-01-19 | 2022-05-31 | 济宁辰星碳素有限公司 | Preparation method of binder asphalt for low-cost high-performance prebaked anode |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1058985A (en) * | 1991-04-19 | 1992-02-26 | 煤炭科学研究总院合肥研究所 | Bitumen and preparation method thereof |
-
2005
- 2005-10-27 CN CNB2005100475887A patent/CN100371420C/en not_active Expired - Fee Related
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1058985A (en) * | 1991-04-19 | 1992-02-26 | 煤炭科学研究总院合肥研究所 | Bitumen and preparation method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1760331A (en) | 2006-04-19 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN100371420C (en) | Modified coal tar, and producing method | |
| Iroegbu et al. | Furfuryl alcohol a versatile, eco-sustainable compound in perspective | |
| CN109609111B (en) | Wood tar resin sand consolidation agent and preparation method and application thereof | |
| CN102351564B (en) | Method for preparing wood ceramics by sintering coal tar pitch and biomass materials | |
| CN102976773B (en) | Coal tar pitch binding agent and preparation method thereof | |
| CN109160512A (en) | A kind of gasification of biomass residue pressed active carbon and preparation method thereof | |
| CN104946288B (en) | Modified coal tar pitch and preparation method thereof | |
| CN102304224B (en) | Phthalaznone-containing poly(aryl ether nitrile) end-capped with maleimide and preparation method thereof | |
| CN1570026A (en) | Modified asphalt and its production method | |
| CN107128914A (en) | The preparation method of petroleum coke pilum shaped activated carbon | |
| CN102225922A (en) | Preparation method of urethane modified tung oil vinylite | |
| CN102585532A (en) | Fiber-filled tung-oil-based resin composite material and preparation method thereof | |
| CN104212142B (en) | The plant oil based unsaturated polyester composite of a kind of bamboo fiber enhancing modified | |
| CN102190898B (en) | Preparation method of paving asphalt modified at normal temperature | |
| CN101659736A (en) | Modification method of petroleum resin | |
| CN109021599A (en) | A kind of regenerative agent and preparation method thereof suitable for aged asphalt | |
| Wang et al. | A novel condensation–addition-type phenolic resin (MPN): synthesis, characterization and evaluation as matrix of composites | |
| CN102108115B (en) | Phenolic resin for environment-friendly thermoplastic refractory material and preparation method thereof | |
| CN103756707B (en) | Modified asphalt and preparation method thereof | |
| CN110194825A (en) | A kind of modified low nitrogen furan resin and production technology | |
| CN103773032A (en) | Epoxy asphalt corrosion-resistant coating | |
| CN103756705B (en) | Modified asphalt and preparation method thereof | |
| CN108855162A (en) | A kind of method preparing catalyst, by this method preparation catalyst and use the method for the catalyst preparation glycerol monomethyl ether | |
| CN107163227B (en) | Using bark as epoxy hardener of raw material and preparation method thereof | |
| CN107880921B (en) | Petroleum-series multifunctional asphalt resin and preparation method thereof |
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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080227 Termination date: 20181027 |