RU2008139206A - METHOD FOR BINDING - Google Patents
METHOD FOR BINDING Download PDFInfo
- Publication number
- RU2008139206A RU2008139206A RU2008139206/04A RU2008139206A RU2008139206A RU 2008139206 A RU2008139206 A RU 2008139206A RU 2008139206/04 A RU2008139206/04 A RU 2008139206/04A RU 2008139206 A RU2008139206 A RU 2008139206A RU 2008139206 A RU2008139206 A RU 2008139206A
- Authority
- RU
- Russia
- Prior art keywords
- thermolysis
- stage
- carried out
- oil
- residues
- Prior art date
Links
- 238000000034 method Methods 0.000 title claims abstract 11
- 238000001149 thermolysis Methods 0.000 claims abstract 10
- 239000000295 fuel oil Substances 0.000 claims abstract 8
- 239000002904 solvent Substances 0.000 claims abstract 6
- 230000003213 activating effect Effects 0.000 claims abstract 4
- 239000000654 additive Substances 0.000 claims abstract 4
- 230000000996 additive effect Effects 0.000 claims abstract 4
- 238000010438 heat treatment Methods 0.000 claims abstract 4
- 239000003921 oil Substances 0.000 claims abstract 4
- 229920002209 Crumb rubber Polymers 0.000 claims abstract 2
- 239000010426 asphalt Substances 0.000 claims abstract 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract 2
- 239000011230 binding agent Substances 0.000 claims abstract 2
- 238000009835 boiling Methods 0.000 claims abstract 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical class O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims abstract 2
- 229920001971 elastomer Polymers 0.000 claims abstract 2
- 238000001704 evaporation Methods 0.000 claims abstract 2
- 230000008020 evaporation Effects 0.000 claims abstract 2
- 239000007789 gas Substances 0.000 claims abstract 2
- 239000004058 oil shale Substances 0.000 claims abstract 2
- 239000001301 oxygen Substances 0.000 claims abstract 2
- 229910052760 oxygen Inorganic materials 0.000 claims abstract 2
- 238000000746 purification Methods 0.000 claims abstract 2
- 238000000197 pyrolysis Methods 0.000 claims abstract 2
- 229920005989 resin Polymers 0.000 claims abstract 2
- 239000011347 resin Substances 0.000 claims abstract 2
- 239000010913 used oil Substances 0.000 claims abstract 2
Landscapes
- Working-Up Tar And Pitch (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
1. Способ получения вяжущего путем нагрева тяжелых нефтяных остатков в присутствии заданного количества резиновой крошки, при заданной температуре и в течение заданного времени, отличающийся тем, что нагрев ведут путем термолиза в два этапа, термолиз на первом этапе осуществляют при 100-250°C в присутствии дистиллятного растворителя, взятого в соотношении с резиновой крошкой 1: 0,1-1, в течение 15-60 мин в присутствии активирующей добавки, затем термолиз осуществляют на 2-ом этапе при 350-450°C в течение 10-60 мин в среде тяжелого нефтяного остатка при постепенном испарении дистиллятного растворителя. ! 2. Способ по п.1, отличающийся тем, что термолиз 2-ой ступени проводят при барботаже кислородом воздуха. ! 3. Способ по п.1, отличающийся тем, что в качестве активирующей добавки используют горючие сланцы и/или природные или синтетические цеолиты. ! 4. Способ по п.1, отличающийся тем, что в качестве дистиллятного растворителя используют фракцию с т.кип.300-400°C от 2-ой ступени термолиза, отработанные масла, вакуумный газойль, экстракт селективной очистки масел. ! 5. Способ по п.1, отличающийся тем, что в качестве тяжелых нефтяных остатков используют мазут, гудрон, смолы пиролиза, асфальт деасфальтизации, крекинг-остатки. 1. A method of producing a binder by heating heavy oil residues in the presence of a given amount of crumb rubber, at a given temperature and for a given time, characterized in that the heating is carried out by thermolysis in two stages, thermolysis in the first stage is carried out at 100-250 ° C the presence of a distillate solvent, taken in the ratio with rubber crumb 1: 0.1-1, for 15-60 minutes in the presence of an activating additive, then thermolysis is carried out at the 2nd stage at 350-450 ° C for 10-60 minutes in medium heavy oil residue at gradual evaporation of a distillate solvent. ! 2. The method according to claim 1, characterized in that the thermolysis of the 2nd stage is carried out by sparging with atmospheric oxygen. ! 3. The method according to claim 1, characterized in that as an activating additive, oil shale and / or natural or synthetic zeolites are used. ! 4. The method according to claim 1, characterized in that as a distillate solvent, a fraction with a boiling point of 300-400 ° C from the 2nd stage of thermolysis, used oils, vacuum gas oil, an extract of selective oil purification is used. ! 5. The method according to claim 1, characterized in that fuel oil, tar, pyrolysis resins, asphalt deasphalting, cracked residues are used as heavy oil residues.
Claims (5)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| RU2008139206/04A RU2415172C2 (en) | 2008-10-02 | 2008-10-02 | Method of producing binder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| RU2008139206/04A RU2415172C2 (en) | 2008-10-02 | 2008-10-02 | Method of producing binder |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| RU2008139206A true RU2008139206A (en) | 2010-04-10 |
| RU2415172C2 RU2415172C2 (en) | 2011-03-27 |
Family
ID=42670908
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| RU2008139206/04A RU2415172C2 (en) | 2008-10-02 | 2008-10-02 | Method of producing binder |
Country Status (1)
| Country | Link |
|---|---|
| RU (1) | RU2415172C2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106701133A (en) * | 2016-12-15 | 2017-05-24 | 榆林学院 | Forming destructive distillation method for crushed low metamorphic coal powder, asphalt and tar residues |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2521988C1 (en) * | 2013-01-09 | 2014-07-10 | Федеральное государственное бюджетное учреждение науки Институт проблем нефти и газа Сибирского отделения Российской академии наук (ИПНГ СО РАН) | Bitumen-concrete mixture on nano-modified binder |
| RU2630529C1 (en) * | 2016-05-26 | 2017-09-11 | Владимир Георгиевич Андриенко | Method for production of modified bituminous binders for road surfaces (versions) |
| RU2656484C1 (en) * | 2016-12-20 | 2018-06-05 | Юрий Моисеевич Штейнберг | Modifier composition for asphalt mixtures |
| RU2707770C1 (en) * | 2018-11-28 | 2019-11-29 | Публичное акционерное общество "Средневолжский научно-исследовательский институт по нефтепереработке" (ПАО "СвНИИНП") | Rubber-bitumen road binder for asphalt-concrete mixture |
Family Cites Families (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB434159A (en) * | 1933-09-27 | 1935-08-27 | Geigy Ag J R | Manufacture of tar products particularly for road construction |
| SU1289872A1 (en) * | 1985-05-30 | 1987-02-15 | Научно-производственное объединение "Дорстройтехника" | Method of preparing rubber-bitumen binder |
| SU1402607A1 (en) * | 1986-08-12 | 1988-06-15 | Предприятие П/Я В-2223 | Binder production process |
| SU1595813A1 (en) * | 1988-07-29 | 1990-09-30 | Научно-производственное объединение "Дорстройтехника" | Method of producing binder for road construction |
| DD289054A5 (en) * | 1989-11-13 | 1991-04-18 | Zeitz Hydrierwerk | METHOD FOR PRODUCING POLYMODIED BITUMENES |
| RU2122555C1 (en) * | 1997-11-06 | 1998-11-27 | Открытое акционерное общество "Московский нефтеперерабатывающий завод" | Binder for asphalt-concrete coatings |
| RU2288940C1 (en) * | 2005-07-20 | 2006-12-10 | Государственное образовательное учреждение высшего профессионального образования "Санкт-Петербургский государственный технологический институт (технический университет)" | Process for thermochemical processing of heavy petroleum residues |
-
2008
- 2008-10-02 RU RU2008139206/04A patent/RU2415172C2/en not_active IP Right Cessation
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106701133A (en) * | 2016-12-15 | 2017-05-24 | 榆林学院 | Forming destructive distillation method for crushed low metamorphic coal powder, asphalt and tar residues |
Also Published As
| Publication number | Publication date |
|---|---|
| RU2415172C2 (en) | 2011-03-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Chaiwong et al. | Study of bio-oil and bio-char production from algae by slow pyrolysis | |
| Kar | Co-pyrolysis of walnut shell and tar sand in a fixed-bed reactor | |
| CN103242881B (en) | The method of separate bitumen class material from coal directly-liquefied residue | |
| Mishra et al. | Bio-oil and biochar production using thermal and catalytic pyrolysis of low-value waste neem seeds over low-cost catalysts: effects of operating conditions on product yields and studies of physicochemical characteristics of bio-oil and biochar | |
| RU2008139206A (en) | METHOD FOR BINDING | |
| WO2013049665A3 (en) | Process for producing a refinery stream compatible bio -oil from a lignocellulosic feedstock | |
| WO2009126508A3 (en) | Fuel and fuel blending components from biomass derived pyrolysis oil | |
| RU2010142300A (en) | KEROSIN BASIC FUEL | |
| JP2017510687A5 (en) | ||
| DE602009000211D1 (en) | Process for removing tar from synthesis gas | |
| Lin et al. | Characterization of rheological properties and aging performance of bitumen modified by bio-oil from bamboo charcoal production | |
| CN103275754B (en) | Method for separating liquefied heavy oil and asphalt substrate from direct coal liquefaction residues | |
| CN102899087B (en) | Deep processing method for medium and low temperature coal tar | |
| Hernando et al. | Thermochemical valorization of camelina straw waste via fast pyrolysis | |
| Anandaram et al. | Co‐pyrolysis characteristics and synergistic interaction of waste polyethylene terephthalate and woody biomass towards bio‐oil production | |
| Zhao et al. | Hydrothermal co-liquefaction of lignite and lignocellulosic biomass with the addition of formic acid: study on product distribution, characteristics, and synergistic effects | |
| EA201691359A1 (en) | METHOD FOR PREPARING RAW MATERIALS FOR INSTALLING HYDRAULIC CLEANING | |
| NZ591736A (en) | Method for extracting a fuel or propellant through thermal cracking of a heavy oil in the presence of moist hydrocarbonaceous biomass | |
| Kashimura et al. | Upgrading the solvent used for the thermal extraction of sub-bituminous coal | |
| WO2010046746A3 (en) | Hydrocarbon composition useful as fuel and combustible obtained from oil components and a biological component | |
| CN103723728A (en) | Activated carbon and method for preparing activated carbon from coal-directly liquefied residue | |
| Liu et al. | Hydrothermal treatment of high ash microalgae: focusing on the physicochemical and combustion properties of hydrochars | |
| WO2011004065A3 (en) | Process for producing hydrocarbons by hydrodesulphurizing a crude turpentine feed | |
| Das | Pyrolytic bio-oil—production and applications | |
| JO3012B1 (en) | Process and Plant for Refining Raw Materials Containing Organic Constituents |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| MM4A | The patent is invalid due to non-payment of fees |
Effective date: 20111003 |
|
| NF4A | Reinstatement of patent |
Effective date: 20120727 |
|
| MM4A | The patent is invalid due to non-payment of fees |
Effective date: 20131003 |