CN106590729A - Treatment technology for softening oil - Google Patents
Treatment technology for softening oil Download PDFInfo
- Publication number
- CN106590729A CN106590729A CN201710087675.8A CN201710087675A CN106590729A CN 106590729 A CN106590729 A CN 106590729A CN 201710087675 A CN201710087675 A CN 201710087675A CN 106590729 A CN106590729 A CN 106590729A
- Authority
- CN
- China
- Prior art keywords
- oil
- product
- heated
- modified
- softening
- 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.)
- Granted
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G29/00—Refining of hydrocarbon oils, in the absence of hydrogen, with other chemicals
- C10G29/20—Organic compounds not containing metal atoms
- C10G29/22—Organic compounds not containing metal atoms containing oxygen as the only hetero atom
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L7/00—Compositions of natural rubber
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1003—Waste materials
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/10—Feedstock materials
- C10G2300/1037—Hydrocarbon fractions
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
- C10G2300/00—Aspects relating to hydrocarbon processing covered by groups C10G1/00 - C10G99/00
- C10G2300/40—Characteristics of the process deviating from typical ways of processing
- C10G2300/4006—Temperature
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Organic Chemistry (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Engineering & Computer Science (AREA)
- General Chemical & Material Sciences (AREA)
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
Abstract
The invention relates to a treatment technology for softening oil. A preparing method of the softening oil comprises the following steps that a coupling agent accounting for a certain percent of mass of raw oil and a catalyst accounting for a certain percent of mass of raw oil are added in byproduct residual oil or heavy oil generated after refining of petroleum, and heating and uniform stirring are conducted under the nitrogen protection condition; and after grinding treatment, the mixture is beaten into a microchannel reactor through a mass flow pump to be subjected to the modification reaction, and a modified oil product is obtained. The requirement for related methods and devices is simple, the oil product treatment technology is rapid and efficient, and the obtained oil product is a softening agent with good performance. The content of polycyclic aromatic hydrocarbons in the modified oil product is low, the product is environment-friendly and free of pollution, the sizing material bonding performance can be effectively improved by applying the product to rubber, and good economic benefits are achieved.
Description
Technical field
The present invention relates to a kind of handling process of softening oil, belongs to chemical products field, product is mainly used in rubber system
In the industries such as product such as tire.
Background technology
Residual oil or heavy oil are the remaining mink cell focuses after crude oil extracts gasoline, diesel oil, and its elementary cell is low molecular monocyclic
Aromatic hydrocarbons, polycyclic aromatic hydrocarbon (polycyclic aromatic hydrocarbons, abbreviation PAHs) and polycyclic aromatic hydrocarbon.And 4-6
The polycyclic aromatic hydrocarbon of ring has strong carcinogenecity, and most representational is 3,4- benzopyrene (BaP).Its mechanism of carcinogenesis is multi-ring
Aromatic hydrocarbon enters internal, generates various intermediate products and end-product with function oxidase metabolism, and some of them metabolite can be with
DNA covalent bond forms PAH-DNA adducts, causes DNA damage, induced gene mutation, or even induced tumor to be formed.For this purpose,
The western countries such as Germany and Poland have had been switched off most of softening oil processing factories, while specifying to soften polycyclic aromatic hydrocarbon in oil product
Content is less than 50mg/kg, which limits application of the oil product in many fields, and China is also in developing country, rubber
It is also quite big to the dependence of rubber softening oil and demand in field, polycyclic aromatic hydrocarbon content in oil product how is effectively reduced, is subtracted
Few environmental pollution becomes the important topic of current research.
The method for reducing polycyclic aromatic hydrocarbon in the softening oil product such as residual oil or heavy oil at present mainly has Ozonation, vacuum distilling
Method, ultraviolet irradiation, low boiling point solvent extract method and chemic modified method etc., most economical most convenient is most expected in these methods
Realize that industrialized is exactly chemical modification, according to similar compatibility principle, the cross-linking agent of selection should be dissolved each other with polycyclic aromatic hydrocarbon in oil product,
Contain active group simultaneously (such as electron-donating group).
Chemic modified method generally using the cross-linking agent such as Polyethylene Glycol, polystyrene, furan resin, paraformaldehyde and heavy oil or
Polycyclic aromatic hydrocarbon reaction (PAHs) in residual oil, generates condensation polycyclic aromatic hydrocarbon resin.But, heavy oil or residual oil composition are more multiple
It is miscellaneous, along with polycyclic aromatic hydrocarbon reactivity differs, and cross-linking agent factor such as dissolubility in oil product so that the extent of reaction
It is low, the detoxification treatment effect on driving birds is not good of polycyclic aromatic hydrocarbon (PAHs).
Based on previous karyotype studies, present invention seek to address that chemic modified method polycyclic aromatic hydrocarbon (PAHs) detoxification treatment is low,
The extent of reaction is low, and gained softening oil is because the problems such as in mixed process, heterogeneity causes poor-performing.The present invention is proposed using micro-
Channel reactor as reaction vessel, to solving the above problems.Micro passage reaction is size between 10 to 300 microns
A kind of duct type microreactor of continuous flowing, microreactor have great specific surface area, up to stirred tank specific surface area
Even thousands of times of hundred times, the basic advantage thus brought is great heat exchange efficiency and mixing efficiency, can be anti-with precise control
Answer temperature and reaction mass instantaneously to mix by accurate proportioning, greatly improve reaction efficiency.Exactly these features so that in microchannel
Reactor serves good effect in terms of polycyclic aromatic hydrocarbon (PAHs) detoxification is processed, and greatly improves the extent of reaction, so as to have
Effect solves the problems such as detoxification efficiency is low, and the extent of reaction is low, oil product mixes heterogeneity.
The content of the invention
The present invention relates to a kind of handling process of softening oil, its preparation method is comprised the following steps：After taking Petroleum refining
Byproduct residual oil or heavy oil, add the catalyst of the 5-50% cross-linking agent and raw material oil quality 1-10% of raw material oil quality, in nitrogen
Under the conditions of gas shielded, 70-200 DEG C is heated to, is stirred, after milled processed, Jing mass flow pumps squeeze into micro passage reaction
In, 70-200 DEG C is heated to, 0.5-6h is processed, modified oil product is obtained.Method equipment requirements involved in the present invention are simple, oil product
Rapidly and efficiently, gained oil product is a kind of softening agent of function admirable to handling process, and in oil product, polycyclic aromatic content is low, product ring
Border close friend is pollution-free, applies in rubber, can effectively improve glue bond, with preferable economic benefit.
Byproduct residual oil or heavy oil that described raw oil is selected after taking Petroleum refining.Can be subdivided into according to viscosity and density
The mixing of high viscosity, low-viscosity, big density, little density oil product or above-mentioned four kinds of oil products.
Described cross-linking agent, it is characterised in that：Cross-linking agent selects Polyethylene Glycol, polystyrene, furane resins, polyethylene tree
The derivant of fat, 5 resin of carbon, aldehydes, aromatic alcohol, aromatic aldehydes and above compound, or the mixing of above-mentioned cross-linking agent.
Described catalyst, it is characterised in that：Catalyst selects sulphuric acid, p-methyl benzenesulfonic acid, P-TOLUENE SULFO ACID 99, nitric acid, salt
The Bronsted acids such as acid；Or it is sour from Lewis such as boron chloride, aluminum chlorides, or the mixing of above-mentioned catalyst.
Described micro passage reaction, it is characterised in that：Micro passage reaction is -100～400 DEG C using temperature range,
Pipe diameter is 10～1000 microns.
Containing the polycyclic aromatic hydrocarbon that concentration is higher in oil product selected by the present invention, usual content in 35-55%, in order to process
Fall the polycyclic aromatic hydrocarbon in oil product, obtain a kind of environmentally friendly, of good performance rubber softening oil, add Polyethylene Glycol, paraformaldehyde
Deng polymer as chemical modification cross-linking agent, it is heated to be condensed to yield condensation polycyclic aromatic hydrocarbon resin, change many in oil product
Aromatic hydrocarbon ring structure, reduces which to environmental hazard toxicity, while during using as rubber softening oil, Ji Nengti
For bating effect, can play a part of again to improve sizing material autohension.
The reactor that the present invention is adopted is different from traditional heated and stirred kettle, but selects more several than stirred tank specific surface area
The micro passage reaction that even thousands of times of Radix Achyranthis Bidentatae, its great heat exchange efficiency and mixing efficiency, can be with precise control reaction temperature
Instantaneously mix by accurate proportioning with reaction mass, greatly improve reaction efficiency and speed, obtain the high modified softening of the extent of reaction
Oil, it is to avoid in course of reaction because steric effect, material composition is complicated, react insufficient the problems such as occur, reduce reaction used time
So as to reduce production cost.
The technique that the application is proposed has following some beneficial effect：
Beneficial effect
A kind of handling process of softening oil involved in the present invention, has an advantage in that：
(1) equipment requirements are simple, and process characteristic is adapted to heavy industrialization, consecutive production.
(2) needed raw material is simple and easy to get, and process is simple is easy to operate, and reaction time consumption is short, and be modified with low cost, modification efficiency
It is high.
(3) production technology involved by is safe, and product detoxification efficiency is good, environmental friendliness, three-waste free discharge.
(4) product yield is high, and gained softening oil mass uniformity is good.
(5) this product is good using bating effect in rubber, can be uniformly distributed, be effectively improved sizing material in sizing material
Processing characteristics.
(6) product combination property is projected, and improves the autohension of sizing material, the cohesive of steel wire and rubber when improving manufacture tire
Can, give rubber good combination property.
(7) the modified low cost of this product, product quality stability are high, and the market competitiveness is strong, with good economic benefit,
Social benefit.
Specific embodiment
Embodiment 1
Take the by-product heavy oil after 100kg Petroleum refinings and pour reacting by heating kettle into, add 5kg Polyethylene Glycol, 1kg sulphuric acid,
Nitrogen is passed through, 70 DEG C is heated to, is stirred, milled processed, after crossing 100nm sieves, Jing mass flow pumps squeeze into size
In 1000nm micro passage reactions, 70 DEG C are heated to, modified-reaction 0.5h obtains modified oil product.Modified oil product is carried out multi-ring
18 detections of aromatic hydrocarbon (PAHs), bond propertiess detection formula：Smoke sheet rubber 100pr, Zinc Oxide 8pr, accelerator DZ 1.25pr,
White carbon black N330 55pr, insoluble sulfuy 4.4pr, antioxidant 4020 2pr, carry out the physical property detection of rubber according to national standard.
Embodiment 2
Take the byproduct residual oil after 100kg Petroleum refinings and pour reacting by heating kettle into, add 50k metaformaldehydes, 10kg sulphuric acid,
Nitrogen is passed through, 200 DEG C is heated to, is stirred, milled processed, after crossing 100nm sieves, Jing mass flow pumps squeeze into size 50nm
Micro passage reaction in, be heated to 200 DEG C, modified-reaction 6h obtains modified oil product.Polycyclic aromatic hydrocarbon is carried out to modified oil product
(PAHs) 18 detections, bond propertiess detection formula：Smoke sheet rubber 100pr, Zinc Oxide 8pr, accelerator DZ 1.25pr, white carbon black
N330 55pr, insoluble sulfuy 4.4pr, antioxidant 4020 2pr, carry out the physical property detection of rubber according to national standard.
Embodiment 3
Take the byproduct residual oil after 100kg Petroleum refinings and pour reacting by heating kettle into, add 20kg polystyrene, 2kg is to first
Base benzenesulfonic acid, is passed through nitrogen, is heated to 100 DEG C, stirs, milled processed, and after crossing 100nm sieves, Jing mass flow pumps are beaten
Enter in the micro passage reaction of size 100nm, be heated to 150 DEG C, modified-reaction 2h obtains modified oil product.Modified oil product is entered
18 detections of row polycyclic aromatic hydrocarbon (PAHs), bond propertiess detection formula：Smoke sheet rubber 100pr, Zinc Oxide 8pr, accelerator DZ
1.25pr, white carbon black N330 55pr, insoluble sulfuy 4.4pr, antioxidant 4020 2pr, carries out the thing of rubber according to national standard
Property detection.
Embodiment 4
Take the byproduct residual oil after 100kg Petroleum refinings and pour reacting by heating kettle into, add 30kg formaldehyde, 3kg is to methylbenzene
Sulfonic acid, is passed through nitrogen, is heated to 90 DEG C, stirs, milled processed, and after crossing 100nm sieves, Jing mass flow pumps squeeze into size
In the micro passage reaction of 10nm, 100 DEG C are heated to, modified-reaction 1h obtains modified oil product.Many cyclophanes are carried out to modified oil product
18 detections of fragrant hydrocarbon (PAHs), carry out the physical property detection of rubber according to national standard.
Embodiment 5
Take the by-product heavy oil after 100kg Petroleum refinings and pour reacting by heating kettle into, add 40kg terephthalyl alcohols, 3kg tri-
Aluminum chloride, is passed through nitrogen, is heated to 140 DEG C, stirs, milled processed, and after crossing 100nm sieves, Jing mass flow pumps are squeezed into
In the micro passage reaction of size 80nm, 180 DEG C are heated to, modified-reaction 6h obtains modified oil product.Modified oil product is carried out many
18 detections of aromatic hydrocarbon ring (PAHs), bond propertiess detection formula：Smoke sheet rubber 100pr, Zinc Oxide 8pr, accelerator DZ
1.25pr, white carbon black N330 55pr, insoluble sulfuy 4.4pr, antioxidant 4020 2pr, carries out the thing of rubber according to national standard
Property detection.
Embodiment 6
Take the byproduct residual oil after 100kg Petroleum refinings and pour reacting by heating kettle into, add 25kg paraformaldehydes, 2kg sulphuric acid,
Nitrogen is passed through, 110 DEG C is heated to, is stirred, milled processed, after crossing 100nm sieves, Jing mass flow pumps squeeze into size
In the micro passage reaction of 300nm, 180 DEG C are heated to, modified-reaction 4h obtains modified oil product.Modified oil product is carried out multi-ring
18 detections of aromatic hydrocarbon (PAHs), bond propertiess detection formula：Smoke sheet rubber 100pr, Zinc Oxide 8pr, accelerator DZ 1.25pr,
White carbon black N330 55pr, insoluble sulfuy 4.4pr, antioxidant 4020 2pr, carry out the physical property detection of rubber according to national standard.
Embodiment 7
Take the byproduct residual oil after 100kg Petroleum refinings and pour reacting by heating kettle into, add 20kg terephthalyl alcohols and 10kg
Polyethylene Glycol, 2kg sulphuric acid and 2kg aluminum chlorides, are passed through nitrogen, are heated to 120 DEG C, stir, milled processed, cross 100nm
After sieve, Jing mass flow pumps are squeezed in the micro passage reaction of size 500nm, are heated to 160 DEG C, and modified-reaction 5h is obtained
Modified oil product.18 detections of polycyclic aromatic hydrocarbon (PAHs), bond propertiess detection formula are carried out to modified oil product：Smoke sheet rubber 100pr,
Zinc Oxide 8pr, accelerator DZ 1.25pr, white carbon black N330 55pr, insoluble sulfuy 4.4pr, antioxidant 4020 2pr, according to state
Family's standard carries out the physical property detection of rubber.
Embodiment 8
Take the by-product heavy oil after 100kg Petroleum refinings and pour reacting by heating kettle into, add 10kg metaformaldehydes and 10kg pair
Benzene dimethanol, 1kg p-methyl benzenesulfonic acids and 1kg nitric acid, are passed through nitrogen, are heated to 105 DEG C, stir, milled processed, mistake
After 100nm sieves, Jing mass flow pumps are squeezed in the micro passage reaction of size 800nm, are heated to 150 DEG C, modified-reaction 3h,
Obtain modified oil product.18 detections of polycyclic aromatic hydrocarbon (PAHs), bond propertiess detection formula are carried out to modified oil product：Smoke sheet rubber
100pr, Zinc Oxide 8pr, accelerator DZ 1.25pr, white carbon black N330 55pr, insoluble sulfuy 4.4pr, antioxidant 4020 2pr,
The physical property detection of rubber is carried out according to national standard.
Embodiment 9
Take the by-product heavy oil after 100kg Petroleum refinings and pour reacting by heating kettle into, add 28kg polyvinyl resins, 3kg sulfur
Acid, is passed through nitrogen, is heated to 150 DEG C, stirs, milled processed, and after crossing 100nm sieves, Jing mass flow pumps squeeze into size
In the micro passage reaction of 250nm, 190 DEG C are heated to, modified-reaction 4h obtains modified oil product.Modified oil product is carried out multi-ring
18 detections of aromatic hydrocarbon (PAHs), bond propertiess detection formula：Smoke sheet rubber 100pr, Zinc Oxide 8pr, accelerator DZ 1.25pr,
White carbon black N330 55pr, insoluble sulfuy 4.4pr, antioxidant 4020 2pr, carry out the physical property detection of rubber according to national standard.
Embodiment 10
Take the byproduct residual oil after 100kg Petroleum refinings and pour reacting by heating kettle into, add 15kg furane resins, 2kg is to first
Base benzenesulfonic acid, is passed through nitrogen, is heated to 200 DEG C, stirs, milled processed, and after crossing 100nm sieves, Jing mass flow pumps are beaten
Enter in the micro passage reaction of size 100nm, be heated to 200 DEG C, modified-reaction 1h obtains modified oil product.Modified oil product is entered
18 detections of row polycyclic aromatic hydrocarbon (PAHs), carry out the physical property detection of rubber according to national standard.
Comparative example 1：
The byproduct residual oil after Petroleum refining or heavy oil are taken, 18 detections of polycyclic aromatic hydrocarbon (PAHs) is carried out to oil product, is glued
Close performance detection formula：Smoke sheet rubber 100pr, Zinc Oxide 8pr, accelerator DZ 1.25pr, white carbon black N330 55pr, insoluble sulfuy
4.4pr, antioxidant 4020 2pr, carry out the physical property detection of rubber according to national standard.
In table 1, embodiment, softening oil applies the physical property testing result in rubber
Claims (4)
1. a kind of handling process of softening oil, it is characterised in that：Take the byproduct residual oil after Petroleum refining or heavy oil pours heating into
Stirred tank, adds the catalyst of 5～50% cross-linking agent and raw material oil quality 1～10% of raw material oil quality, in nitrogen ceiling
Under part, heated and stirred kettle is heated to into 70～200 DEG C, is stirred, milled processed, after crossing 100nm sieves, Jing mass flow pumps
Micro passage reaction is squeezed into, 70～200 DEG C are heated to, 0.5～6h is processed, modified oil product is obtained.
2. cross-linking agent according to claim 1, it is characterised in that：Cross-linking agent selects polyvinyl resin, 5 resin of carbon, poly- second
The derivant of glycol, polystyrene, furane resins, aldehydes, aromatic alcohol, aromatic aldehydes or more compound, or above-mentioned friendship
The mixing of connection agent.
3. catalyst according to claim 1, it is characterised in that：Catalyst selects sulphuric acid, p-methyl benzenesulfonic acid, toluene sulphur
Acid, nitric acid, hydrochloric acid；Or select boron chloride, aluminum chloride, or the mixing of above-mentioned catalyst.
4. micro passage reaction according to claim 1, it is characterised in that：Micro passage reaction using temperature range for-
100～400 DEG C, pipe diameter is 10～1000 microns.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710087675.8A CN106590729B (en) | 2017-02-18 | 2017-02-18 | A kind for the treatment of process of softening oil |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710087675.8A CN106590729B (en) | 2017-02-18 | 2017-02-18 | A kind for the treatment of process of softening oil |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN106590729A true CN106590729A (en) | 2017-04-26 |
| CN106590729B CN106590729B (en) | 2018-08-28 |
Family
ID=58587598
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710087675.8A Active CN106590729B (en) | 2017-02-18 | 2017-02-18 | A kind for the treatment of process of softening oil |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN106590729B (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111635778A (en) * | 2020-06-22 | 2020-09-08 | 中海沥青股份有限公司 | Rubber plasticizer for petroleum-based environment-friendly reclaimed rubber and preparation method thereof |
| CN112063186A (en) * | 2020-09-14 | 2020-12-11 | 江苏麒祥高新材料有限公司 | Preparation method of environment-friendly rubber oil and prepared environment-friendly rubber oil |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1626559A (en) * | 2003-12-09 | 2005-06-15 | 中国石油化工股份有限公司九江分公司 | New method for separating reaction of catalyzing oil slurry |
| CN103756708A (en) * | 2014-01-16 | 2014-04-30 | 神华集团有限责任公司 | Modified asphalt and preparation method thereof |
| US20160194580A1 (en) * | 2012-08-13 | 2016-07-07 | Research Institute Of High Way, Ministry Of Transportation | Bio-asphalt, bio-asphalt composition and method for preparing them |
-
2017
- 2017-02-18 CN CN201710087675.8A patent/CN106590729B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1626559A (en) * | 2003-12-09 | 2005-06-15 | 中国石油化工股份有限公司九江分公司 | New method for separating reaction of catalyzing oil slurry |
| US20160194580A1 (en) * | 2012-08-13 | 2016-07-07 | Research Institute Of High Way, Ministry Of Transportation | Bio-asphalt, bio-asphalt composition and method for preparing them |
| CN103756708A (en) * | 2014-01-16 | 2014-04-30 | 神华集团有限责任公司 | Modified asphalt and preparation method thereof |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111635778A (en) * | 2020-06-22 | 2020-09-08 | 中海沥青股份有限公司 | Rubber plasticizer for petroleum-based environment-friendly reclaimed rubber and preparation method thereof |
| CN112063186A (en) * | 2020-09-14 | 2020-12-11 | 江苏麒祥高新材料有限公司 | Preparation method of environment-friendly rubber oil and prepared environment-friendly rubber oil |
| WO2022052436A1 (en) * | 2020-09-14 | 2022-03-17 | 江苏麒祥高新材料有限公司 | Environmentally friendly rubber oil preparation method, and prepared environmentally friendly rubber oil |
Also Published As
| Publication number | Publication date |
|---|---|
| CN106590729B (en) | 2018-08-28 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN104474966B (en) | Modified lignin-based dispersing agent and preparation method thereof | |
| CN101899196A (en) | Water-borne phenolic epoxy resin emulsion and preparation method thereof | |
| CN101003664B (en) | Latex of epoxy resin of aqueous phenolic aldehyde, and preparation method | |
| CN102153717A (en) | Fluorine-containing novolac resin and preparation method and application of fluorine-containing novolac resin | |
| CN106590729A (en) | Treatment technology for softening oil | |
| CN101700990A (en) | Method for preparing C9 petroleum resin with light color and high softening-point | |
| CN106397673A (en) | Method and apparatus for continuous kettle type hydrogenation of petroleum resin | |
| CN103665273A (en) | Demulsifying agent as well as preparation method and application thereof | |
| CN102993386B (en) | Method for preparing modified C5 petroleum resin based on irradiation grafting | |
| CN110003443A (en) | A kind of recoverable version epoxy resin and its preparation and recovery method | |
| CN101497677B (en) | Method for preparing C5 hydrocarbon resin from methyl tetrahydro benzoic anhydride production waste liquor | |
| CN106188400B (en) | A kind of preparation process of polystyrene multi-component copolymer high molecular material | |
| CN102276957A (en) | Phenolic resin for refractory bricks and preparation method thereof | |
| CN101712625A (en) | Method for synthesizing amphoteric slow-breaking quick-setting asphalt emulsifier | |
| CN101381505B (en) | Synthetic resin produced by renewable resource and preparation method thereof | |
| CN105754451A (en) | Konjac fly powder based epoxy resin, preparation method thereof and coating prepared from konjac fly powder based epoxy resin | |
| CN104262557B (en) | A kind of preparation method of green high-purity thermoplastic phenolic resin | |
| CN102161740A (en) | Preparation method phenolic resin | |
| CN101818026A (en) | Method for preparing oligomeric rosin by taking slash pine rosin as raw material | |
| CN104164051A (en) | Toughening-type environmental protection phenolic resin and preparation method of its composite material | |
| CN112898516B (en) | Phenolic aldehyde modified amine and preparation method thereof | |
| CN107286726A (en) | The response type epoxy emulsifying agent prepared using carboxylic acid APEO hydrophilic monomer | |
| CN103102449A (en) | Manufacturing method of piperylene petroleum resin | |
| CN112409573A (en) | Byproduct polyphenol epoxy resin and preparation method and application thereof | |
| CN104164050A (en) | Heatproof environmental protection phenolic resin and preparation method of its composite material |
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 | ||
| CP02 | Change in the address of a patent holder | ||
| CP02 | Change in the address of a patent holder |
Address after: 236000 Yingzhou District, Fuyang City, Anhui Province Patentee after: New Anhui Mstar Technology Ltd Address before: 236000 Xin'an Avenue 518, Fuyang Economic and Technological Development Zone, Fuyang City, Anhui Province Patentee before: New Anhui Mstar Technology Ltd |