CN1493652A - Road asphalt agglutinate and its preparation method - Google Patents
Road asphalt agglutinate and its preparation method Download PDFInfo
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- CN1493652A CN1493652A CNA021445397A CN02144539A CN1493652A CN 1493652 A CN1493652 A CN 1493652A CN A021445397 A CNA021445397 A CN A021445397A CN 02144539 A CN02144539 A CN 02144539A CN 1493652 A CN1493652 A CN 1493652A
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Abstract
An asphalt cementing material for spreading pavement in tropical region is prepared from proper heavy oil through ordinary-pressure or vacuum distilling to obtain vacuum residual oil, removing asphalt by solvent to obtain the target asphat, and optionally further treating such as oxidizing or mixing it with residual oil. Its advantages are high content of asphalt colloid, low content of asphalt, and high softening point (60 deg.C) and viscosity.
Description
1, technical field
The present invention relates to a kind of road bitumen agglutinate and preparation method thereof, bituminous cements of using especially for the torrid areas laying of roadway and preparation method thereof.
2, background technology
Pitch is owing to have good thermoplasticity and visco-elasticity, is widely used in aspects such as laying of roadway, waterproof and dampproof, anticorrosion and insulation.Wherein topmost purposes is to be used for road construction.According to statistics, the output of whole world road bitumen accounts for about 85% of pitch ultimate production.Usually, pitch can satisfy the laying of roadway requirement well, but along with the increase day by day of the volume of traffic and the continuous increase of vehicle capacity, many bituminous pavements are seriously damaged.Especially in the weather hot area, under the summer high temperature condition, the effect repeatedly that the road surface is rolled by wheel, when load stress surpasses the stability limit of asphalt, just accumulation forms rut easily, destroy pavement structure, the tension set of bituminous pavement or rut are the major causes that causes pavement destruction.
Prevent that rut from damaging effective measures is to improve the use properties of bituminous cements under the summer high temperature condition.The index of representing the anti-rut performance of asphalt high-temperature mainly is 60 ℃ of viscosity and softening temperature.Thereby under the road oil material penetration degree scope fixed situation of selecting for use, we wish that it has the softening temperature of bigger 60 ℃ of viscosity and Geng Gao.Wish that particularly bituminous material penetration degree has the softening temperature of bigger 60 ℃ of viscosity and Geng Gao in the time of bigger.
A kind of bituminous composition that U.S. Pat 5302638 discloses with good high-temperature viscosity and low temperature flexibility.Said composition is under the oxygen existence condition, with the method interpolation polyethylene of shearing basic asphalt is carried out modification and makes, and paves the way with it and can improve the anti-rut performance on road surface.Though polymer modification can significantly improve anti-rut of bituminous high temperature and low temperature anti-cracking performance, the costing an arm and a leg of polymkeric substance, and need additionally purchase modified device, thereby will increase final production cost greatly.
What day disclosure special permission communique spy opened flat 6-116499 proposition is raw material with a kind of de-oiled asphalt that obtains with solvent deasphalting technology, extracts the method that the high viscosity road bitumen is produced in components blendings such as oil, vacuum residuum, visbreaking residue out with lubricant base, the solvent treatment of 10～70m%.Wherein the asphalt content of de-oiled asphalt is 20～60m%, and saturated minute content of blending component is 15～35m%, and finally concocting the bituminous gum level is 5～30m%, and bituminous matter is 5～20m%.The disclosed a kind of vacuum residuum with Oman's crude oil of Chinese patent CN1064987 is raw material, behind propane deasphalting, through the half oxidizing process high viscosity method for producing road asphalt that to produce 60 ℃ of viscosity be 600～1000Pas, this bituminous group composition is that saturated branch 18～21m%, fragrance divide 50～53m%, colloid 26～28m%, bituminous matter 1～3m% again.Though 60 ℃ of viscosity of above-mentioned two kinds of bituminous are higher, satisfied the service requirements under the hot conditions, but because their gum level is low, the penetration degree of asphaltic products. is less than normal, generally about 50 1/10mm, and in the road construction work of reality, mostly use the asphaltic products. of penetration degree about 70 or 90 1/10mm because the too little pitch of penetration degree often low-temperature performance is relatively poor, low temperature damage takes place easily with its back of paving the way.
3, summary of the invention
At existing road oil ubiquitous under the bigger situation of penetration degree 60 ℃ of viscosity and the lower problem of softening temperature, the present invention proposes a kind of gum level height, bituminous cements that asphalt content is low and preparation method thereof, this bituminous cements has good anti-rut performance under higher road surface use temperature.
Bituminous cements of the present invention consists of: saturated branch 2～10m%, and fragrance divides 25～35m%, colloid 60～70m%, bituminous matter 0.1～2m%, under the identical condition of penetration degree, higher 3～6 ℃ than ordinary road bituminous softening temperature, than 60 ℃ of high 40～200Pas of viscosity of ordinary road bituminous.
The production process of bituminous cements of the present invention is: select 20 ℃ of density greater than 0.93g/cm
3Heavy crude be raw material, after distillation (normal, underpressure distillation), obtain vacuum residue fraction, the highest normal pressure temperature of underpressure distillation correspondence is between 460～540 ℃, directly produce pitch of the present invention by solvent deasphalting technology then, perhaps the de-oiled asphalt that solvent deasphalting technology is obtained carries out oxidation or produces pitch of the present invention with vacuum residuum, visbreaking residue blending.
Find after deliberation, the saturated branch in pitch and asphalt content is less, gum level more for a long time, can obtain under the identical condition of penetration degree, have the bituminous cements that has higher softening temperature and bigger 60 ℃ of viscosity than the road bitumen that generally uses.Thereby under higher road surface use temperature, has better anti-rut performance.The present invention is a basic material by selecting specific heavy crude for use, after certain complete processing is handled, obtain a kind of saturated branch, asphalt content is low, the bituminous cements that gum level is high, softening temperature and 60 ℃ of performance index such as viscosity of product are increased substantially, have the anti-rut performance of excellent high-temperature.The difficult processing of the heavy crude that the present invention selects for use is unsuitable for producing products such as light Fuel.The heavy crude price is lower, and does not need to add properties-correcting agent such as polymkeric substance in the course of processing, and is therefore low with the asphaltic products. cost of its production, good economy performance.
4, embodiment
The production method of bituminous cements of the present invention is that the heavy crude of selecting to suit is raw material, after distillation (normal, underpressure distillation), obtain vacuum residue fraction, the highest normal pressure temperature of underpressure distillation correspondence is between 460～540 ℃, then under suitable operational condition, directly produce pitch of the present invention by solvent deasphalting technology, perhaps the de-oiled asphalt that solvent deasphalting technology is obtained carries out oxidation or produces pitch of the present invention with vacuum residuum, visbreaking residue blending.No matter use above-mentioned which kind of technology and combination thereof, should guarantee that all the asphaltic products. that finally makes has following composition: saturated branch 2～10m%, fragrance divides 25～35m%, colloid 60～70m%, bituminous matter 0.1～2m%.
Suitable heavy crude of the present invention is meant that 20 ℃ of density are greater than 0.93g/cm
3Crude oil.The cycloalkyl that the light constituent yield is low, intermediate base or cycloalkanes-intermediate base heavy crude preferably.These crude oil are used for producing the complex manufacturing of high value added products such as gasoline, kerosene, diesel oil, lubricating oil, and cost is higher, is used for producing road bitumen and will produces better economic benefit.Optimum heavy crude is as belonging to the Sudan Fula crude oil of cycloalkanes-intermediate base.
The normal pressure temperature of the highest distillation temperature correspondence of distillation of the present invention (normal, underpressure distillation) technology should be preferably between 480 ℃～520 ℃ between 460～540 ℃.If the highest distillation temperature is lower than 460 ℃, then will there be the part light constituent to remain in the vacuum residuum, can the stability of asphaltic products. be had a negative impact; If the highest distillation temperature is higher than 540 ℃, then the vacuum residuum of gained will be too hard, is not suitable as the raw material of solvent deasphalting technology.
Solvent deasphalting technology of the present invention solvent commonly used is a kind of in propane, butane, the pentane or the mixture of two or three solvent wherein.Solvent deasphalting process can carry out under undercritical conditions, and promptly service temperature and pressure are lower than the critical temperature and the emergent pressure of solvent respectively; Also can carry out under super critical condition, promptly service temperature and pressure are higher than the critical temperature and the emergent pressure of solvent respectively.Generally under undercritical conditions, the service temperature of using propane to do the solvent deasphalting technology of solvent is 60～80 ℃, 90～140 ℃ of butane solvents, and 140～190 ℃ of pentane solvent, extraction tower top and bottom should keep 10～20 ℃ of temperature difference.Working pressure is 2.8～4.2MPa, and the volume ratio of solvent and raw material is 3～10: 1, preferably 6～8: 1.Generally under super critical condition, the service temperature of using propane to do the solvent deasphalting technology of solvent is 105～170 ℃, 155～240 ℃ of butane solvents, and 200～290 ℃ of pentane solvent, extraction tower top and bottom should keep 10～20 ℃ of temperature difference.Working pressure is 4.2～12MPa, and the volume ratio of solvent and raw material is 3～10: 1, preferably 6～8: 1.The deasphalted oil yield that solvent deasphalting technology obtains should be preferably between 40～60m% between 30～70m%.
Oxidizing process of the present invention is meant under hot conditions, by the method for blowing air bituminous composition and character is changed, thereby reaches the specification of quality of product.Oxidation can be carried out in the intermittent type oxidation unit, also can carry out in the oxidation unit continuously.General oxidizing temperature is 170 ℃～300 ℃, preferably 200 ℃～250 ℃.Oxidization time is 1.0h～7.0h, preferably 3.0h～5.0h.
Mixing process of the present invention is meant at tempering tank or dynamically, in the static mixer, select de-oiled asphalt and the inventive method the vacuum residuum of crude oil for use or concoct with visbreaking residue.25 ℃ of penetration degrees of de-oiled asphalt are 0～50 1/10mm, preferably 10～30 1/10mm; 60 ℃ of viscosity of vacuum residuum or visbreaking residue should be 2～50Pas, preferably 5～20Pas.Blending ratio is de-oiled asphalt 50～90m%, preferably 50～70m%; Vacuum residuum or visbreaking residue are 10～50m%, preferably 30～50m%.
The following examples will the present invention will be further described.
Embodiment 1
With a kind of 20 ℃ of density is 0.94g/cm
3, the Sudan Fula crude oil that belongs to cycloalkanes-intermediate base is raw material, and distillation obtains vacuum residue fraction on laboratory true boiling point distillation device, and the normal pressure temperature of the highest distillation temperature correspondence is 520 ℃.It is as follows to subtract slag character: 25 ℃ of penetration degrees are greater than 300 1/10mm, 60 ℃ of viscosity 6.6Pas, and saturated minute 20.5m%, fragrance divides 32.9m%, colloid 46.1m%, bituminous matter 0.5m%.
With the butane is that solvent carries out the solvent deasphalting test to vacuum residuum on the supercritical solvent deasphalting unit.174 ℃ of tower top temperatures, in the tower 167 ℃, at the bottom of the tower 160 ℃, solvent ratio is 6: 1, working pressure is 9.2MPa.When the deasphalted oil yield is respectively 39m% and 45m%, can make pitch of the present invention, character is as shown in table 1.
Table 1
Analysis project product 1 product 2
Penetration degree (25 ℃), 1/10mm 100 69
Softening temperature, ℃ 49.0 53.2
Viscosity (60 ℃), Pa.s 164 355
Compositional analysis, %
Saturated branch 2.8 2.0
Fragrance divides 32.0 30.4
Colloid 64.7 67.4
Bituminous matter 0.5 0.2
Embodiment 2
With propane is that solvent carries out the solvent deasphalting test to the vacuum residuum among the embodiment 1 on the supercritical solvent deasphalting unit.118 ℃ of tower top temperatures, in the tower 112 ℃, at the bottom of the tower 105 ℃, solvent ratio is 6: 1, working pressure 12.0MPa.When the deasphalted oil yield is 31m%, can obtain penetration degree 240 1/10mm, the de-oiled asphalt that softening temperature is 41.5 ℃.Get the 500g de-oiled asphalt and on the small-sized batch still formula oxidation unit of laboratory, carry out oxidation test, 250 ℃ of temperature of reaction, air-blowing quantity 0.3m
3/ kg.h when oxidization time is respectively 2.5h and 3.0h, can make pitch of the present invention, and character is as shown in table 2.
Table 2
Analysis project product 3 products 4
Penetration degree (25 ℃), 1/10mm 97 70
Softening temperature, ℃ 49.8 52.2
Viscosity (60 ℃), Pa.s 173 355
Compositional analysis, %
Saturated branch 5.3 5.2
Fragrance divides 30.1 28.8
Colloid 63.5 64.8
Bituminous matter 1.1 1.2
Embodiment 3
With the butane is that solvent carries out the solvent deasphalting test to the vacuum residuum among the embodiment 1 on the supercritical solvent deasphalting unit.174 ℃ of tower top temperatures, in the tower 167 ℃, at the bottom of the tower 160 ℃, solvent ratio is 6: 1, working pressure is 10.5MPa.When the yield of deasphalted oil is 58m%, can obtain penetration degree 24 1/10mm, the de-oiled asphalt that softening temperature is 68.3 ℃.Vacuum residuum among this pitch and the embodiment 1 is concocted, can be made pitch of the present invention.Test-results is as shown in table 3.
Table 3
Analysis project product 5 products 6
Blending ratio
De-oiled asphalt, % 58 60
Vacuum residuum, m% 42 40
Penetration degree (25 ℃), 1/10mm 106 94
Softening temperature, ℃ 48.7 49.5
Viscosity (60 ℃), Pa.s 209 242
Compositional analysis, %
Saturated branch 6.4 6.9
Fragrance divides 30.2 30.1
Colloid 63.1 62.7
Bituminous matter 0.3 0.3
Embodiment 4
With the butane is that solvent carries out subcritical solvent deasphalting test to the vacuum residuum among the embodiment 1.112 ℃ of tower top temperatures, in the tower 106 ℃, at the bottom of the tower 100 ℃, solvent ratio is 6: 1, working pressure is 4.0MPa.When the yield of deasphalted oil is 69%, can obtain penetration degree 11 1/10mm, the de-oiled asphalt that softening temperature is 83.1 ℃.The visbreaking residue that 60 ℃ of viscosity that this de-oiled asphalt and vacuum residuum are obtained through viscosity breaking technology are 9.2Pas is concocted, and can make pitch of the present invention.Test-results is as shown in table 4.
Table 4
Analysis project product 7 products 8
Blending ratio
De-oiled asphalt, m% 55 58
Visbreaking residue, m% 45 42
Penetration degree (25 ℃), 1/10mm 71 74
Softening temperature, ℃ 51.0 52.9
Viscosity (60 ℃), Pa.s 339 440
Compositional analysis, %
Saturated branch 8.5 8.3
Fragrance divides 29.8 30.2
Colloid 60.2 60.2
Bituminous matter 1.5 1.3
Embodiment 5
With the Sudan Fula crude oil is raw material, and distillation obtains vacuum residue fraction on laboratory true boiling point distillation device, and the normal pressure temperature of the highest distillation temperature correspondence is 490 ℃.It is as follows to subtract slag character: 25 ℃ of penetration degrees are greater than 300 1/10mm, 60 ℃ of viscosity 5.8Pas, and saturated minute 23.7m%, fragrance divides 31.7m%, colloid 44.2m%, bituminous matter 0.4m%.
With the butane is that solvent carries out the solvent deasphalting test to this vacuum residuum on the supercritical solvent deasphalting unit.169 ℃ of tower top temperatures, in the tower 162 ℃, at the bottom of the tower 155 ℃, solvent ratio is 6: 1, working pressure is 9.5MPa.When the deasphalted oil yield is 47m%, can make pitch of the present invention, character is as shown in table 5.
Table 5
Analysis project product 9
Penetration degree (25 ℃), 1/10mm 74
Softening temperature, ℃ 52.6
Viscosity (60 ℃), Pa.s 296
Compositional analysis, %
Saturated branch 2.3
Fragrance divides 31.2
Colloid 66.2
Bituminous matter 0.3
Compare by pitch that the present invention is obtained and the road bitumen character of generally using, will help further to understand bituminous cements of the present invention.Comparative test result is shown in table 6, table 7, and bituminous Maoming pitch, Panjin pitch and middle extra large pitch all are bituminous cements relatively more commonly used in the domestic high-grade highway making engineering as a comparison.By data in the table as can be seen: compare with general road bitumen, the outstanding feature of pitch of the present invention is that gum level is obviously higher, about 2 times of the general bituminous of average out to; Asphalt content then is significantly less than general road bitumen product; Under the suitable situation of penetration degree, pitch of the present invention obviously has higher softening temperature and 60 ℃ of bigger viscosity, and under the close situation of viscosity or softening temperature, then tool is in bigger penetration degree for pitch of the present invention, thereby pitch of the present invention has better high temperature resistance rut performance.
Table 6
No. 90, Maoming
Analysis project product 1 product 3 products 5 products 6 Panjin pitches
Pitch
Penetration degree (25 ℃), 1/10mm 100 97 106 94 86 95
Softening temperature, ℃ 49.0 49.8 48.7 49.5 46.3 44.6
Viscosity (60 ℃), Pa.s 164 173 209 242 152 132
Compositional analysis, %
Saturated branch 2.8 5.3 6.4 6.9 10.2 23.4
Fragrance divides 32.0 30.1 30.2 30.1 50.3 35.5
Colloid 64.7 63.5 63.1 62.7 30.7 35.7
Bituminous matter 0.5 1.1 0.3 0.3 8.8 5.4
Table 7
No. 70, Maoming
Extra large pitch in analysis project product 2 products 4 products 7 products 8
Pitch
Penetration degree (25 ℃), 1/10mm 69 70 71 74 73 73
Softening temperature, ℃ 53.2 52.2 51.0 52.9 48.0 47.1
Viscosity (60 ℃), Pa.s 355 355 339 440 274 234
Compositional analysis, %
Saturated branch 2.0 5.2 8.5 8.3 7.5 16.2
Fragrance divides 30.4 28.8 29.8 30.2 52.9 44.2
Colloid 67.4 64.8 60.2 60.2 36.3 31.4
Bituminous matter 0.2 1.2 1.5 1.3 3.3 8.2
Claims (10)
1, a kind of bituminous cements is characterized in that consisting of in mass: saturated branch 2～10m%, fragrance divides 25～35m%, colloid 60～70m%, bituminous matter 0.1～2m%.
2, according to the described bituminous cements of claim 1, it is characterized in that described bituminous cements under the identical condition of penetration degree, higher 3～6 ℃ than ordinary road bituminous softening temperature, than 60 ℃ of high 40～200Pas of viscosity of ordinary road bituminous.
3, the production method of the described bituminous cements of a kind of claim 1 is characterized in that selecting 20 ℃ of density greater than 0.93g/cm
3Heavy crude be raw material, often, obtain vacuum residue fraction after the underpressure distillation, the highest normal pressure temperature of underpressure distillation correspondence is between 460～540 ℃, directly produce pitch of the present invention by solvent deasphalting technology then, perhaps the de-oiled asphalt that solvent deasphalting technology is obtained carries out oxidation or produces pitch of the present invention with vacuum residuum, visbreaking residue blending.
4,, it is characterized in that described heavy crude is cycloalkyl, intermediate base or cycloalkanes-intermediate base heavy crude according to the described production method of claim 3.
5,, it is characterized in that described heavy crude is the Sudan Fula crude oil of cycloalkanes-intermediate base according to claim 3 or 4 described production methods.
6, according to the described production method of claim 3, it is characterized in that solvent that described solvent deasphalting technology uses is a kind of in propane, butane, the pentane or the mixture of two or three solvent wherein, the temperature difference of solvent extraction top of tower and bottom is 10～20 ℃, working pressure is 2.8～12MPa, and the volume ratio of solvent and raw material is 3～10: 1.
7, according to the described production method of claim 3, it is characterized in that described oxidizing process at intermittent type or carry out in the oxidation unit continuously, oxidizing temperature is 170 ℃～300 ℃, oxidization time is 1.0h～7.0h.
8, according to the described production method of claim 6, it is characterized in that described oxidizing temperature is 200 ℃～250 ℃, oxidization time is 2.0h～5.0h.
9, according to the described production method of claim 3,25 ℃ of penetration degrees that it is characterized in that the de-oiled asphalt of described blending usefulness are 0～50 1/10mm, the vacuum residuum of blending usefulness or 60 ℃ of viscosity of visbreaking residue are 2～50Pas, blending ratio is de-oiled asphalt 50m%～90m%, and vacuum residuum or visbreaking residue are 10m%～50m%.
10, according to the described production method of claim 9,25 ℃ of penetration degrees that it is characterized in that the de-oiled asphalt of described blending usefulness are 10～30 1/10mm, the vacuum residuum of blending usefulness or 60 ℃ of viscosity of visbreaking residue are 5～20Pas, blending ratio is de-oiled asphalt 50m%～70m%, and vacuum residuum or visbreaking residue are 30m%～50m%.
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| CN 02144539 CN1230495C (en) | 2002-11-02 | 2002-11-02 | Road asphalt agglutinate and its preparation method |
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| CN 02144539 CN1230495C (en) | 2002-11-02 | 2002-11-02 | Road asphalt agglutinate and its preparation method |
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| CN1230495C CN1230495C (en) | 2005-12-07 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102300957B (en) * | 2009-02-03 | 2014-04-02 | 吉坤日矿日石能源株式会社 | Process for producing binder for coke production and process for producing coke |
| CN109207182A (en) * | 2018-10-09 | 2019-01-15 | 中国石油化工股份有限公司 | A kind of method of deasphalted oil production road asphalt |
| CN114163826A (en) * | 2020-09-11 | 2022-03-11 | 中国石油化工股份有限公司 | Color-paved cementing material and preparation method and application thereof |
-
2002
- 2002-11-02 CN CN 02144539 patent/CN1230495C/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102300957B (en) * | 2009-02-03 | 2014-04-02 | 吉坤日矿日石能源株式会社 | Process for producing binder for coke production and process for producing coke |
| US9493708B2 (en) | 2009-02-03 | 2016-11-15 | Jx Nippon Oil & Energy Corporation | Process for producing caking additive for coke production and process for producing coke |
| CN109207182A (en) * | 2018-10-09 | 2019-01-15 | 中国石油化工股份有限公司 | A kind of method of deasphalted oil production road asphalt |
| CN109207182B (en) * | 2018-10-09 | 2021-07-20 | 中国石油化工股份有限公司 | Method for producing road asphalt by deasphalted oil |
| CN114163826A (en) * | 2020-09-11 | 2022-03-11 | 中国石油化工股份有限公司 | Color-paved cementing material and preparation method and application thereof |
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| CN1230495C (en) | 2005-12-07 |
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