CN1386822A - Efficient denitrifying agent for removing nitride from fraction oil of petroleum and its denitrifying process - Google Patents
Efficient denitrifying agent for removing nitride from fraction oil of petroleum and its denitrifying process Download PDFInfo
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- CN1386822A CN1386822A CN 01113973 CN01113973A CN1386822A CN 1386822 A CN1386822 A CN 1386822A CN 01113973 CN01113973 CN 01113973 CN 01113973 A CN01113973 A CN 01113973A CN 1386822 A CN1386822 A CN 1386822A
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Abstract
An efficient denitrifying agent for removing nitride from the fractional oil of petroleum, especially the basic oil of lubricating oil whose boiling point is 350-500 deg.C, contains phosphoric acid (40-85 wt%), sulfuric acid (5-40 %) and organic acid (0-20%). Its advantage is low setting point lower than -20 deg.C. Its application method includes such steps as reaction of said denitrifying agent with said basic oil, settling, oil-residue separation and refining with less clay.
Description
The present invention relates to a kind of denitrfying agent and denitrogenation method of fraction oil of petroleum, especially refer under the normal pressure, the denitrfying agent and the denitrogenation method of the lubricant base of boiling point between 350 ℃～500 ℃.International Classification of Patents belongs to C10G29/10.
Nitrogenous generally higher in the base oil that refines in the oil (distillate), containing because of nitrogen in the crude oil in China that nitrogen in higher (about 0.3%) oil distributes is that rising along with the distillate boiling point raises.The distillate that wherein has 80% nitrogen to concentrate on more than 400 ℃ concentrates in the lubricant base, the oxidation stability of lubricant base and its chemical constitution are closely related, wherein oxidation has certain restraining effect to sulfide to lubricant base, and nitride, especially basic nitrogen compound can quicken oil oxidation to the oxidation stability of lubricant base is very harmful.The method that industry is at present commonly used has the method that adopts post-refining after the furfural treatment again, but the carclazyte consumption is big, and band oil not only influences productive rate, raises the cost, and brings outstanding environmental problem.Hydrofinishing method denitrogenation ability is relatively poor, oil stability is low and its facility investment is big, operational condition is harsh, cost is higher.So the sulfur-preserving and denitrifying agent of seeking a highly selective is the focus that people study always.Now developed the reagent of many excellent propertys, some of them have been widely used in industrial production, but wherein still have some shortcomings.The better performances of CN1103106A denitrfying agent (WSQ-2) for example, but its zero pour height needs tracing system in production, transportation and use, and energy consumption is bigger.
CN1045459A denitrfying agent (TTS) denitrfying agent in denitrification process is adsorbed on the wall, and denitrification effect is poor, removing is difficult.
CN1176289A adopts the method for oxalic acid and carclazyte mixed denitrification, though obtain certain desired result, its oxalic acid and carclazyte consumption are all bigger, are unfavorable for reducing cost, so the environmental problem of bringing is more outstanding.
The required carclazyte amount of CN1177626A denitrfying agent reaction back denitrogenation oil refining is big, furnace temperature is high, power consumption is big, and environmental pollution is bigger.
The EP278694 patent adopts these sorbent materials of solid acid polar adsorption dealkalize nitrogen that silicon-aluminium, silica-based porous catalytic cracking agent, zeolite etc. are arranged, and the renovation process of solid adsorbent is high pressure, high temperature hydrogenation, or uses solvent washing, and power consumption is big, process is complicated.
US 3 223 618 employing zinc chloride are removed impurity and are comprised nitrogen compound, but temperature required (250 ℃--500 ℃) height, selectivity is low, and the deoxidation rate is low, big energy-consuming.
US 4 071 435 reductors need a large amount of inorganic metal materials, and cost of material is more expensive, and treating processes just requires to adopt special liquid liquid separating apparatus owing to contain metal-salt.
US 4 231 858 is not obvious for the removal effect of the nitrogen in the organic fluid, and required temperature and pressure height, and running cost is bigger.
US 4 329 222 adopts metal halide material complexing denitrification percents also higher, but the metal halide material, as nickelous bromide, zinc bromide, Sodium Bromide etc. to produce expense higher, and poisonous, consumption is big, is unfavorable for industrial production and popularization.
In view of this, the purpose of this invention is to provide a kind of efficient denitrification agent and denitrogenation method that from fraction oil of petroleum, removes nitride.According to acid-base theory, find a kind of suitable alkali nitrogen complexing agent.
The object of the present invention is achieved like this: a kind of from fraction oil of petroleum, especially refer under the normal pressure, remove the denitrfying agent and the denitrogenation method of basic nitrogen compound the lubricant base of boiling point between 350 ℃～500 ℃, it is characterized in that denitrfying agent consists of: phosphatase 24 0～85% with mineral acid and the composite denitrfying agent that becomes of organic acid; Sulfuric acid 5～40%; Organic acid 0～20%.Organic acid in the denitrfying agent comprises: oxalic acid, propanedioic acid, citric acid, tartrate, phthalic acid, oxysuccinic acid, toxilic acid, glacial acetic acid, terephthalic acid, phenylformic acid.
The step of denitrogenation method has:
1) as stated above earlier with the composite denitrfying agent that becomes of phosphoric acid, sulfuric acid and organic acid;
2) above-mentioned denitrfying agent was poured into by agent-oil ratio in the container of distillate in 1: 200～1: 700, all
In the time of even the stirring, be heated to 20 ℃～100 ℃ gradually, and kept 10 minutes～60 minutes,
Make the basic nitrogen compound and the denitrfying agent solution layer generation chemical reaction of oil reservoir;
3) then the mixture in the container is left standstill, up to being separated into oil reservoir and denitrfying agent solution layer,
And the two is separated;
4) oil reservoir of separating is carried out clay finishing again, finally obtain denitrogenation oil.
The carclazyte consumption of above-mentioned the 4th step is 0.6wt%～1.0wt%.The temperature of the clay finishing of above-mentioned the 4th step is 120 ℃～160 ℃.
Characteristics of the present invention are that the consumption of denitrfying agent is few, and for the second line of distillation lubricant base, agent-oil ratio is between 1: 500～1: 700; The agent-oil ratio that subtracts three-way lubricant base is between 1: 350～1: 450; The agent-oil ratio that subtracts four line lubricant bases is between 1: 200～1: 300.The alkali nitrogen content of pressing the distillate after above-mentioned agent-oil ratio is made with extra care reduces more than 90%, and sulphur content reduces seldom.Lubricant base oxidation stability after the denitrogenation can be improved significantly, and has significantly reduced the carclazyte consumption.All other indexs all are better than like product, and the zero pour of denitrfying agent low (＜-20 ℃), need not tracing system in production, storage, transportation and use, have reduced energy expenditure.Simultaneously, the denitrfying agent raw material is easy to get, nontoxic, is convenient to industrial promotion and application.
Example of the present invention is described in detail in detail below:
Example one
Phosphoric acid 85%, the vitriol oil 5% and glacial acetic acid 10% are re-dubbed denitrfying agent, getting grand celebration second line of distillation furfural refining oil is raw material, agent-oil ratio is 1: 400, stirred 30 minutes down at 90 ℃, after sedimentation, with 1% carclazyte denitrogenation oil is carried out post-refining down at 120 ℃-130 ℃, the alkali nitrogen content of base oil drops to 4.6ppm by 87.6ppm, dealkalize nitrogen rate 94.7%, total sulfur drops to 596ppm by 620ppm, protects sulphur rate 96.1%
Example two
Phosphoric acid 80%, the vitriol oil 15% and oxalic acid 5% are re-dubbed denitrfying agent, getting grand celebration, to subtract three-way furfural refining oil be raw material, agent-oil ratio is 1: 400, stirred 30 minutes down at 90 ℃, after sedimentation, with 0.8% carclazyte denitrogenation oil is carried out post-refining down at 120 ℃-130 ℃, the alkali nitrogen content of base oil drops to 10.9ppm by 106.44ppm, denitrification percent 89.8%.
Example three
The vitriol oil 15% and phosphoric acid 85% are re-dubbed denitrfying agent.Get grand celebration and subtract that three-way to take off cured oil be raw material, agent-oil ratio is 1: 500, stirs 30 minutes down at 90 ℃, after sedimentation, with 0.8% carclazyte denitrogenation oil is carried out post-refining down at 120 ℃, and the alkali nitrogen content of base oil drops to 1.8ppm by 87.6ppm.
Example four
The vitriol oil 15% and phosphoric acid 85% are re-dubbed denitrfying agent.Get Jinxi petro-chemical corporation second line of distillation and subtract that three-way to take off cured oil be raw material, its performance is carried out The effect.Appreciation condition is: second line of distillation agent-oil ratio 1: 500; Subtract three-way agent-oil ratio 1: 300; Denitrification temperature and time are respectively 80 ℃ and 30 minutes; Settling time is 120 minutes; Carclazyte consumption, clay-filtered temperature and clay-filtered time are respectively 1%, 150 ℃ and 30 minutes.The raw material oil properties sees Table 1, and the quality of treated oil sees Table 2.Table 1 Jinxi subtracts two, subtracts three pressed oil character
Table 2 treated oil quality
| Project | Second line of distillation pressed oil | Subtract three-way pressed oil |
| Total nitrogen/ppm | ?32 | ?74 |
| Alkali nitrogen/ppm | ?30 | ?71 |
| Sulphur/ppm | ?298 | ?534 |
| Acid number/mgKOHg -1 | ?- | ?0.08 |
| Colorimetric/# | ＜1.0 | ?2.0 |
| Project | The second line of distillation treated oil | Subtract three-way treated oil |
| Total nitrogen/ppm | ?2 | ?18 |
| Alkali nitrogen/ppm | ?0 | ?8.4 |
| Sulphur/ppm | ?250 | ?468 |
| Acid number/mgKOHg -1 | ?0.01 | ?0.01 |
| Colorimetric/# | ?＜0.5 | ?＜2.0 |
| Rotary oxygen bomb/min | ?278 | ?237 |
Claims (5)
1, a kind of efficient denitrification agent that removes nitride from fraction oil of petroleum is characterized in that denitrfying agent consists of: phosphatase 24 0～85% with mineral acid and the composite denitrfying agent that becomes of organic acid; Sulfuric acid 5～40%; Organic acid 0～20%.
2, by the described efficient denitrification agent that from fraction oil of petroleum, removes nitride of claim 1, it is characterized in that the organic acid in the denitrfying agent comprises: oxalic acid, propanedioic acid, citric acid, tartrate, phthalic acid, oxysuccinic acid, toxilic acid, glacial acetic acid, terephthalic acid, phenylformic acid.
3, a kind of denitrogenation method that from fraction oil of petroleum, removes nitride, its step has:
1) by the composite denitrfying agent that becomes of claim 1;
2) above-mentioned denitrfying agent was poured into by agent-oil ratio in the container of distillate in 1: 200～1: 700, evenly
When stirring, be heated to 20 ℃～100 ℃ gradually, and kept 10 minutes～60 minutes,
Make the basic nitrogen compound and the denitrfying agent solution layer generation chemical reaction of oil reservoir;
3) then the mixture in the container is left standstill, up to being separated into oil reservoir and denitrfying agent solution layer, and
The two is separated;
4) oil reservoir of separating is carried out clay finishing again, finally obtain denitrogenation oil.
4, by the described method that removes nitride from fraction oil of petroleum of claim 3, it is characterized in that: the carclazyte consumption of above-mentioned the 4th step is 0.6wt%～1.0wt%.
5, by the described method that removes nitride from fraction oil of petroleum of claim 3, it is characterized in that: the temperature of the clay finishing of above-mentioned the 4th step is 120 ℃～160 ℃.
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| CNB011139730A CN1194074C (en) | 2001-05-18 | 2001-05-18 | Efficient denitrifying agent for removing nitride from fraction oil of petroleum and its denitrifying process |
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| CNB011139730A CN1194074C (en) | 2001-05-18 | 2001-05-18 | Efficient denitrifying agent for removing nitride from fraction oil of petroleum and its denitrifying process |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101967392A (en) * | 2010-10-28 | 2011-02-09 | 大庆油田有限责任公司 | Method for denitrification refining of shale oil |
| CN102008938A (en) * | 2010-11-15 | 2011-04-13 | 中国石油化工股份有限公司 | Naphtha denitrification adsorbent and preparation method thereof |
| CN102021014A (en) * | 2009-09-15 | 2011-04-20 | 中国石油天然气股份有限公司 | Method for removing alkali nitrogen from inferior diesel oil |
| CN101574647B (en) * | 2009-04-23 | 2011-06-01 | 中国海洋石油总公司 | Preparation method of ultra-deep absorption desulfurization and denitrogenation agent for hydrocracking tail oil |
| CN103242898A (en) * | 2013-05-10 | 2013-08-14 | 中国石油大学(华东) | Complexing denitrification technique for coker gas oil |
| CN108795483A (en) * | 2017-05-02 | 2018-11-13 | 中国石油天然气股份有限公司 | A method of non-alkaline nitrogenous compound in separation and turpentole fraction |
| CN114907877A (en) * | 2022-04-28 | 2022-08-16 | 武汉工程大学 | Lewis acid-alkoxy complex denitrification reagent and denitrification application thereof in waste lubricating oil regeneration |
-
2001
- 2001-05-18 CN CNB011139730A patent/CN1194074C/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101574647B (en) * | 2009-04-23 | 2011-06-01 | 中国海洋石油总公司 | Preparation method of ultra-deep absorption desulfurization and denitrogenation agent for hydrocracking tail oil |
| CN102021014A (en) * | 2009-09-15 | 2011-04-20 | 中国石油天然气股份有限公司 | Method for removing alkali nitrogen from inferior diesel oil |
| CN101967392A (en) * | 2010-10-28 | 2011-02-09 | 大庆油田有限责任公司 | Method for denitrification refining of shale oil |
| CN101967392B (en) * | 2010-10-28 | 2013-01-23 | 大庆油田有限责任公司 | Method for denitrification refining of shale oil |
| CN102008938A (en) * | 2010-11-15 | 2011-04-13 | 中国石油化工股份有限公司 | Naphtha denitrification adsorbent and preparation method thereof |
| CN103242898A (en) * | 2013-05-10 | 2013-08-14 | 中国石油大学(华东) | Complexing denitrification technique for coker gas oil |
| CN108795483A (en) * | 2017-05-02 | 2018-11-13 | 中国石油天然气股份有限公司 | A method of non-alkaline nitrogenous compound in separation and turpentole fraction |
| CN114907877A (en) * | 2022-04-28 | 2022-08-16 | 武汉工程大学 | Lewis acid-alkoxy complex denitrification reagent and denitrification application thereof in waste lubricating oil regeneration |
| CN114907877B (en) * | 2022-04-28 | 2023-09-05 | 武汉工程大学 | Lewis acid-alkoxy complexation denitrification reagent and denitrification application thereof in regeneration of waste lubricating oil |
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| CN1194074C (en) | 2005-03-23 |
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