CN102965152A - Coking-delaying anti-coking yield increasing additive - Google Patents
Coking-delaying anti-coking yield increasing additive Download PDFInfo
- Publication number
- CN102965152A CN102965152A CN 201210532159 CN201210532159A CN102965152A CN 102965152 A CN102965152 A CN 102965152A CN 201210532159 CN201210532159 CN 201210532159 CN 201210532159 A CN201210532159 A CN 201210532159A CN 102965152 A CN102965152 A CN 102965152A
- Authority
- CN
- China
- Prior art keywords
- coking
- delaying
- yield increasing
- oil
- increasing additive
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
Abstract
The invention discloses a coking-delaying anti-coking yield increasing additive which comprises the following components in percentage by weight: 25.2-27.5% of T154, 1.5.5-17% of alkyl benzene sulfonic acid, 6.3-9.5% of organic amine, 3-7.2% of alkylamide and 43-48% of solvent. According to the invention, all used raw materials are resistant to high temperature, oxidation, scaling and corrosion, and good in dispersing performance; when injected into raw oil, the coking-delaying anti-coking yield increasing additive can be used to prevent coking in a high-temperature high-pressure pipeline with alternating-current speed, also play a certain role in dissolving coke after entering the bottom of a coke tower, has an anticorrosion effect for steel materials of inner walls of the pipeline and the tower, and has the advantages of delaying coking time and increasing the recovery rate of light oil. The raw materials of the coking-delaying anti-coking yield increasing additive are free from toxic and harmful components, have no adverse influence on downstream products, and cannot cause secondary pollution to the environment.
Description
Technical field
The invention belongs to oil refining and increase income the agent field, specifically anti-Jiao of a kind of delayed coking increases income agent.
Background technology
The refinery with crude oil through atmospheric and vacuum distillation, after the part lightweight oil distillated, the remaining dregs of fat are the 60-75% that residual oil accounts for the crude oil total amount, delayed coking then is a kind of method of residual oil deep processing, and it is by high temperature residual oil to be generated coking gas, gasoline as the raw material cracking, diesel oil, the product that wax oil and coke etc. can directly utilize, this technique belong to low-cost, the residual oil treatment process of high yield.In whole technique, delayed coking is the key of flow process, adds the anti-scorch generation that agent can reduce coke and dry gas that increases income in raw material residual oil, increases liquid product yield, and equipment is played certain anti-corrosion function, receives larger economic benefit and social benefit.
Usually there is certain problem in the agent that increases income of prior art, cause coking and fouling because of high temperature oxidation easily, the residual oil green coke is serious in the coking tower, device is subject to corrosion to a certain degree, has increased the cleaning frequency of device, has not only brought trouble to production, frequent washing unit, caused the damaged probability of device, the life-span of device will reduce, and then affects normally carrying out of producing.If things go on like this, the rate of recovery of lightweight oil must descend.
Summary of the invention
The object of the present invention is to provide anti-Jiao of a kind of delayed coking to increase income agent.
Purpose of the present invention can be achieved through the following technical solutions:
Anti-Jiao of a kind of delayed coking increases income agent, it is characterized in that comprising the moiety of following weight percent: T154 25.2-27.5%, alkyl benzene sulphonate (ABS) 15.5-17%, organic amine 6.3-9.5%, alkylamide 3-7.2%, solvent 43-48%.
The present invention includes the moiety of following proportioning: T154 26%, alkyl benzene sulphonate (ABS) 16%, organic amine 8%, alkylamide 5%, solvent 45%.
Described solvent is diesel oil or kerosene.
Preparation method of the present invention is:
(1) solvent, T154, alkyl benzene sulphonate (ABS), alkylamide are added reactor successively, stirring is warming up to 240-250 ℃, collect simultaneously the phlegma of steam, then oil-soluble material in the phlegma is passed back into still, the water of collecting is injected test tank, continue 2h, be cooled to 50 ℃ and obtain intermediates;
(2) add organic amine and stirring in the intermediates that step (1) obtains, reaction 1-3h obtains increasing income agent.
Beneficial effect of the present invention: raw material used in the present invention is for having high temperature resistant antioxygen, ant-scaling, anticorrosive, the various compositions that dispersing property is good, after injecting stock oil with it, in High Temperature High Pressure, exchange and prevent in the fast pipeline that coking from generating, enter at the bottom of the coke drum, also played certain molten burnt effect, also play simultaneously the preservative activity to pipe, inner wall of tower steel, postponed scorch time, increased the rate of recovery of lightweight oil.Advantages of nontoxic raw materials evil composition of the present invention has no adverse effects to derived product, can not cause secondary pollution to environment.After using the present invention to increase income agent, the rate of recovery of lightweight oil significantly improves, and coking gas and coke yield descend, and equipment is played certain anti-corrosion function.Receive larger economic benefit and social benefit.
Embodiment
The invention will be further described below in conjunction with specific embodiment.
Embodiment 1
Anti-Jiao of a kind of delayed coking increases income agent, may further comprise the steps: (1) adds reactor with 45kg diesel oil, 26kgT154,16kg alkyl benzene sulphonate (ABS), 5kg alkylamide, stir and be warming up to gradually 240-250 ℃, collect simultaneously the phlegma of steam, then oil-soluble material in the phlegma is passed back into still, the water of collecting is injected test tank, continue 2 hours, be cooled to 50 ℃ and obtain intermediates;
(2) in the intermediates that step (1) obtains, add 8kg organic amine and stirring, make it fully react 1-3h and obtain increasing income agent.
Embodiment 2
Anti-Jiao of a kind of delayed coking increases income agent, may further comprise the steps: (1) adds reactor with 44.1kg kerosene, 25.5kgT154,16.5kg alkyl benzene sulphonate (ABS), 4.6kg alkylamide, stir and be warming up to gradually 240-250 ℃, collect simultaneously the phlegma of steam, then oil-soluble material in the phlegma is passed back into still, the water of collecting is injected test tank, continue 2 hours, be cooled to 50 ℃ and obtain intermediates;
(2) in the intermediates that step (1) obtains, add 9.3kg organic amine and stirring, make it fully react 1-3h and obtain increasing income agent.
Embodiment 3
Anti-Jiao of a kind of delayed coking increases income agent, may further comprise the steps: (1) adds reactor with 45.4kg kerosene, 26.4kgT154,15.8kg alkyl benzene sulphonate (ABS), 5.5kg alkylamide, stir and be warming up to gradually 240-250 ℃, collect simultaneously the phlegma of steam, then oil-soluble material in the phlegma is passed back into still, the water of collecting is injected test tank, continue 2 hours, be cooled to 50 ℃ and obtain intermediates;
(2) in the intermediates that step (1) obtains, add 6.9kg organic amine and stirring, make it fully react 1-3h and obtain increasing income agent.
Embodiment 4
Anti-Jiao of a kind of delayed coking increases income agent, may further comprise the steps: (1) adds reactor with 46.6kg diesel oil, 25.2kgT154,16.1kg alkyl benzene sulphonate (ABS), 4.7kg alkylamide, stir and be warming up to gradually 240-250 ℃, collect simultaneously the phlegma of steam, then oil-soluble material in the phlegma is passed back into still, the water of collecting is injected test tank, continue 2 hours, be cooled to 50 ℃ and obtain intermediates;
(2) in the intermediates that step (1) obtains, add 7.4kg organic amine and stirring, make it fully react 1-3h and obtain increasing income agent.
Table 1 increases income every character of agent for anti-Jiao of delayed coking of the present invention's preparation.
Anti-Jiao of delayed coking of the present invention increases income the coking and fouling that agent can prevent that the boiler tube Raw from causing because of high temperature oxidation, and anti-burnt scale inhibition performance reaches more than 92%, postpones simultaneously the residual oil coking period in coking tower, improves recovering of vaporized hydrocarbons rate 4-5%.
The present invention adopts without the agent of silicon anti-coking, and adding of the present invention increasing income does not affect device after the agent and normally produce, and does not change product and distributes and quality product, and subsequent handling is had no side effect.
The present invention adopts the high temperature technology that dewaters, and effectively avoids moisture to cause emulsification, and the moisture gasification causes the erratic fluctuations of device, and the extension fixture cycle of operation is more than one times.
Claims (3)
1. anti-Jiao of delayed coking increases income agent, it is characterized in that comprising the moiety of following weight percent: T154 25.2-27.5%, alkyl benzene sulphonate (ABS) 15.5-17%, organic amine 6.3-9.5%, alkylamide 3-7.2%, solvent 43-48%.
2. anti-Jiao of delayed coking according to claim 1 increases income agent, it is characterized in that comprising the moiety of following proportioning: T154 26%, alkyl benzene sulphonate (ABS) 16%, organic amine 8%, alkylamide 5%, solvent 45%.
3. anti-Jiao of delayed coking according to claim 1 and 2 increases income agent, it is characterized in that described solvent is diesel oil or kerosene.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201210532159 CN102965152A (en) | 2012-12-11 | 2012-12-11 | Coking-delaying anti-coking yield increasing additive |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 201210532159 CN102965152A (en) | 2012-12-11 | 2012-12-11 | Coking-delaying anti-coking yield increasing additive |
Publications (1)
Publication Number | Publication Date |
---|---|
CN102965152A true CN102965152A (en) | 2013-03-13 |
Family
ID=47795588
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 201210532159 Pending CN102965152A (en) | 2012-12-11 | 2012-12-11 | Coking-delaying anti-coking yield increasing additive |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN102965152A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103351888A (en) * | 2013-06-25 | 2013-10-16 | 黄河三角洲京博化工研究院有限公司 | Oil slurry scale inhibitor |
CN106381170A (en) * | 2016-10-21 | 2017-02-08 | 鞍钢贝克吉利尼水处理有限公司 | Cleaning dispersing agent for separating and removing scale of oil extraction and conveying equipment |
CN107987887A (en) * | 2017-11-24 | 2018-05-04 | 浙江杭化科技股份有限公司 | A kind of oil refining apparatus increases income agent with high temperature inhibition |
-
2012
- 2012-12-11 CN CN 201210532159 patent/CN102965152A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103351888A (en) * | 2013-06-25 | 2013-10-16 | 黄河三角洲京博化工研究院有限公司 | Oil slurry scale inhibitor |
CN103351888B (en) * | 2013-06-25 | 2015-04-08 | 黄河三角洲京博化工研究院有限公司 | Oil slurry scale inhibitor |
CN106381170A (en) * | 2016-10-21 | 2017-02-08 | 鞍钢贝克吉利尼水处理有限公司 | Cleaning dispersing agent for separating and removing scale of oil extraction and conveying equipment |
CN106381170B (en) * | 2016-10-21 | 2018-01-09 | 鞍钢贝克吉利尼水处理有限公司 | A kind of cleaning dispersant that dirty scale removal is analysed for the oil transporting appliance that recovers the oil |
CN107987887A (en) * | 2017-11-24 | 2018-05-04 | 浙江杭化科技股份有限公司 | A kind of oil refining apparatus increases income agent with high temperature inhibition |
CN107987887B (en) * | 2017-11-24 | 2020-05-12 | 浙江杭化科技股份有限公司 | High-temperature corrosion inhibition yield increasing agent for oil refining device |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101831316A (en) | Polyelement composite heavy oil emulsion splitter and preparation method thereof | |
CN105086976A (en) | Efficient wax inhibitor for oilfields | |
CN102965152A (en) | Coking-delaying anti-coking yield increasing additive | |
CN107574011B (en) | Regeneration treatment method for complexing, membrane separation, hydrogenation and fractionation of waste lubricating oil | |
CN104479773B (en) | A kind of heavy-oil emulsifying agent and preparation method thereof | |
CN102977921B (en) | Method for preparing delayed coking coke-resistant yield-increasing agent | |
CN102071047A (en) | Residual oil modifier for coking delaying device and use thereof | |
CN103101988A (en) | Method for stripping gas washing water | |
CN106479555A (en) | A kind of delayed coking anti-coking agent and preparation method thereof | |
CN101724436B (en) | Thermal cracking method for reducing viscosity and condensation point of extra-heavy crude oil | |
CN104178767B (en) | A kind of coking chemical waste water pyrolysis coal gas corrosion inhibiter and preparation method thereof | |
CN104451699B (en) | A kind of H2s-HCl-H2o system high-temperature corrosion inhibitor and preparation method thereof | |
CN110607193B (en) | Resource recycling method of Fischer-Tropsch wax residues | |
CN201903794U (en) | Ethylene unit process water pH value control system | |
CN205907221U (en) | Vacuum residue's refining device | |
CN101255349A (en) | Highly effective production technique of waste oil regenerative fuel oil | |
CN105861054B (en) | Method for preventing or delaying salt deposition of delayed coking fractionating tower | |
CN103952182B (en) | A kind ofly process the process unit that fractionation tower top follows system salt crust | |
CN104059700A (en) | Efficient liquid fuel additive and liquid fuel with additive | |
CN104560408B (en) | A kind of production method of biodiesel | |
CN109628169A (en) | A kind of preparation method that can inhibit gas barrier methanol gasoline | |
CN203741276U (en) | Waste oil disposal system capable of improving use ratio | |
CN108410495B (en) | Biofuel prepared from waste oil and fat and preparation method thereof | |
CN110152347A (en) | A kind of method that coal liquefaction residue progress detoxification is modified | |
CN211626161U (en) | Device for generating superheated steam by recovering waste heat of crude gas riser of coke oven |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20130313 |