CN1288000A - Method for preparing liquid alkyl diphenylamine - Google Patents
Method for preparing liquid alkyl diphenylamine Download PDFInfo
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- CN1288000A CN1288000A CN 99119033 CN99119033A CN1288000A CN 1288000 A CN1288000 A CN 1288000A CN 99119033 CN99119033 CN 99119033 CN 99119033 A CN99119033 A CN 99119033A CN 1288000 A CN1288000 A CN 1288000A
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Abstract
The preparation method of liquid alkyldiphenylamine is as follows. Under the exitence of activated clay catalyst and 170-230 deg.C and 0.2-0.5 MPa pressure, diisobutylene and diphenylamine are made to react, and when the content of 4,4'-ditert octyldiphenylamine is less than 20%, reaction is stopped and product is collected. Compared with the method disclosed. in EP149,422, the present invention can reduce reaction time by 4-5 hrs, and the liquid aklyldiphenylamine produced me method of present invention is light yellow, rather than dark brown as the product produced using method is EP 149422.
Description
The present invention relates to the preparation method of alkylated diphenylamine, exactly, is the preparation method as the liquid alkyl diphenylamine of oxidation inhibitor.
Alkylated diphenylamine oxidation inhibitor not only has good antioxidant effect in oil product, and has higher thermostability, good oil soluble and characteristics such as ashless, thereby in oil product, obtained using widely.
Alkylated diphenylamine oxidation inhibitor is generally formed by alkene and diphenylamine reaction.Because the difference of aspects such as alkene structures, catalyzer and preparation technology, the alkylated diphenylamine structure that obtains is not quite similar, and makes product that the branch of liquid and solid be arranged.Because liquid alkyl diphenylamine oxidation inhibitor oil soluble is good and easily allotment, its consumption has substantially exceeded solid alkylation pentanoic oxidation inhibitor.
US 3,714, and 257 have described the method for preparing alkylated diphenylamine oxidation inhibitor.In autoclave equipment, diisobutylene and pentanoic are at AlCl
3Catalyzer reacts under existing, and reaction is removed catalyzer after finishing, and unreacted diisobutylene is removed in distillation, obtains 4, and 4 '-dioctyl diphenylamine, this product at room temperature are solid-state, 75～85 ℃ of fusing points.With nonene and diphenylamine reaction, obtain the dinonyldiphenylamine product with method, product at room temperature is liquid.
US 4,704, and 219 to disclose the preparation contraposition be butyl and octyl group, and the ortho position is the method for the pentanoic oxidation inhibitor that replaces of ethyl, in autoclave, adds pentanoic and aluminum chloride, forms intermediate, adds ethene and HCl gas reaction, adds the diisobutylene reaction again.Obtaining a kind of ortho position is that ethyl replaces, and contraposition is the pentanoic product that butyl and octyl group replace, and product at room temperature is liquid.
It is catalyzer that JP2-188555 discloses with the atlapulgite, is the preparation method of the alkylated diphenylamine of raw material with Propylene trimers and pentanoic, obtain a kind of faint yellow liquid 4,4 '-dinonyldiphenylamine product, product nitrogen content 3.2%.
EP 149,422 discloses pentanoic and diisobutylene (refering in particular to 2,2,4-2,4,4-Trimethyl-1-pentene-1) reacts in the presence of activated bauxite catalyst, the method that preparation butyl, octyl group are mixed the pentanoic oxidation inhibitor that replaces, and product at room temperature is liquid.This method is at normal pressure and is not less than under 160 ℃ the temperature, and the mode by continuous dropping diisobutylene is constantly carried out reaction, and 4,4 '-two uncle's octyl diphenylamine content are less than 25% in product.Because the diisobutylene boiling point is 102 ℃, be liquid under temperature of reaction, and pentanoic is solid-state, the reaction system that enters diisobutylene one gasifies immediately, refluxes, reaction is actually to be carried out in the surface molecular of the backflow drop of diisobutylene and pentanoic, and the reactant contact is insufficient, cause long reaction time, the product color is darker, is dark-brown.On the other hand, the speed of response of this reaction is along with reaction reduces gradually, when the rate of addition of diisobutylene during greater than speed of response quantity of reflux increase, make temperature of reaction be lower than the reference mark; And when rate of addition during less than speed of response, temperature sharply rises again, causes temperature fluctuation excessive, and it is steady that operating process is difficult to reach.
The objective of the invention is to overcome the above-mentioned defective of prior art, a kind of smooth operation is provided, the reaction times is the preparation method of short liquid alkyl diphenylamine relatively.
The preparation method of liquid alkyl diphenylamine provided by the invention, be in the presence of activated bauxite catalyst, at 170～230 ℃ with make under the pressure that diisobutylene is in a liquid state, make diisobutylene and pentanoic contact reacts, in product 4,4 '-two uncle's octyl diphenylamine content were less than 20% o'clock, and stopped reaction is also collected product.
Specifically, the preparation method of liquid alkyl diphenylamine provided by the invention is at 170～230 ℃, under preferred 170～200 ℃, makes pentanoic and the diisobutylene reaction that is in a liquid state in the presence of activated bauxite catalyst and the stopper and under the nitrogen protection.Reaction steams unreacted diisobutylene after finishing, and filtered while hot is removed catalyst waste slag.The diisobutylene performance that steams is unaffected, recyclable utilization.
Reaction pressure should make diisobutylene be in a liquid state under service temperature, and general operation pressure is 0.2～0.5MPa.For guaranteeing this working pressure, can adopt airtight reactor or autoclave, and conversion unit preferably has two kinds of functions of reaction and distillation concurrently.
In the reaction raw materials, diisobutylene should be suitably excessive, can be 1: 1.3～1: 2.0 as pentanoic and diisobutylene mol ratio.Diisobutylene can once add also can divide and adds reaction system several times, and preferably gradation adds, and can make the pressure of initial reaction stage be unlikely to too high.
The atlapulgite consumption can change in a big way and be unlikely to reaction is produced detrimentally affect, and general consumption is 5～30% of a pentanoic weight, and preferred 10～20%.Best thermal dehydration was 2 hours before said carclazyte used, to prevent that bumping takes place in the reaction process.
In the inventive method, also can prevent highly active diisobutylene autohemagglutination in reaction process, thereby improve utilization ratio of raw materials by using stopper.Said stopper can be this areas such as Resorcinol or MEHQ stoppers commonly used, and consumption is 5～200ppm usually, preferred 5～100ppm.In the inventive method, initial reaction stage 4,4 '-two uncle's octyl diphenylamine content are higher, after reaction is carried out 20～25 hours, 4,4 '-dioctyl diphenylamine content is reduced to below 20%, gets final product stopped reaction.On the contrary, if 4,4 '-two uncle's octyl diphenylamine content surpass 20% in the product, easily separate out solid under the normal temperature in the product.In the pentanoic product that the light yellow liquid mixed alkyl that adopts the inventive method to obtain replaces, tertiary butyl substituted diphenylamine accounts for 15～25%, uncle's octyl group substituted diphenylamine accounts for 25～30%, the tertiary butyl and uncle's octyl group substituted diphenylamine account for 25～30%, two uncle's octyl group substituted diphenylamines account for 10～20%, and the free pentanoic accounts for 2～4%.
Adopt the liquid amine type oxidation inhibitor of the inventive method preparation, with the composite use of the oxidation inhibitor of different structure, as dialkyl dithio amino formate.(zinc), zinc dialkyl dithiophosphate, 4,4 '-methylene-bis (2, the 6-di-tert-butylphenol) has better effect.With mono butonediimide ashless dispersant agent, high alkaline calcium sulfonate (magnesium) purification agent, metal passivator etc. have good compatibleness.
The preparation method of liquid alkyl diphenylamine provided by the invention, by the control reaction pressure, diisobutylene is reacted with pentanoic under liquid state, increased the contact probability of diisobutylene and pentanoic molecule, with EP 149,422 disclosed methods are compared, and the reaction times shortens 4～5 hours, have solved the unsteady shortcoming of temperature fluctuation in the reaction process that causes owing to the diisobutylene backflow simultaneously.And the light yellow liquid alkylated diphenylamine oxidation inhibitor outward appearance of the inventive method preparation is better than adopting EP149, the similar product of dark-brown of 422 methods preparation.
The invention will be further described below by example.4,4 '-two uncle's octyl diphenylamine content gas chromatography determinations in the example.
Example 1
The pentanoic that in the autoclave of 250ml, adds 64.4 grams, and 85.0 gram diisobutylene (the Shijiazhuang Oil Refinery product, 2,2,4-2,4,4-Trimethyl-1-pentene-1 content 80%, 2,2,4-2,4,4-Trimethyl-1-pentene-2 content 15%, surplus is the hydrocarbon mixture component.), 13 gram atlapulgites (Yi County, Jinzhou oil carclazyte company limited product), 20ppm Resorcinol stopper with nitrogen replacement third-order reaction system, begins in the time of 100 ℃ to stir, heat temperature raising to 175 ℃, reaction pressure 0.52MPa.Along with reaction is carried out, pressure is reduced to 0.3MPa gradually.After reaction was carried out 24 hours, sampling analysis recorded that 4,4 '-two uncle's octyl diphenylamine content are 17.8% in the product.The cooling material also is transferred in the there-necked flask of 250ml, and unreacted diisobutylene and less water are removed in underpressure distillation, temperature of charge is reduced to below 140 ℃ then, remove by filter catalyst waste slag, obtain the light yellow liquid product of 110 grams, this product nitrogen content 4.36%.
Example 2
The pentanoic that in the stainless autoclave of 250ml, adds 64.4 grams, 34 gram diisobutylene, 13 gram activated bauxite catalysts, 20ppm MEHQ stopper is with nitrogen replacement third-order reaction system.Begin in the time of 100 ℃ to stir, heat temperature raising to 180 ℃, reaction pressure 0.3MPa, along with reaction is carried out, pressure is reduced to 0.18MPa gradually.After reaction is carried out 4 hours, the diisobutylene that adds 12.8 grams by volume pump, keep temperature to continue reaction, after reaction proceeds to 16 hours, add 21.2 gram diisobutylene, keep temperature to continue reaction, after the reaction to 20 hour, add 17 gram diisobutylene again, continue reaction to 24 hours, sampling analysis records that 4,4 '-two uncle's octyl diphenylamine content are 15.6% in the product.After reaction finishes, collect product, obtain the light yellow liquid product of 108 grams, this product nitrogen content 4.45% according to the method for example 1.
Example 3
In the 250ml stainless steel autoclave, add 64.4 gram pentanoic, 46.8 gram diisobutylene, 9.6 grams are active in native catalyzer, and 50ppm Resorcinol stopper is with nitrogen replacement third-order reaction system.Be warming up to 175 ℃ and begin reaction, reacting kettle inner pressure 0.21MPa.React after 10 hours, add 17.0 diisobutylene that restrain, keep temperature by volume pump, continue reaction after 18 hours, add 8.5 gram diisobutylene for the second time, reaction finished to 22 hours, sampling analysis records that 4,4 '-two uncle's octyl diphenylamine content are 17.2% in the product.Method according to example 1 is collected product, obtains light yellow liquid product 107 grams, nitrogen content 4.62%.
Example 4
In the 250ml stainless steel autoclave, add 64.4 gram pentanoic, 34 gram diisobutylene, 12.5 gram activated bauxite catalysts, 50ppm Resorcinol stopper is with nitrogen replacement third-order reaction system.Start stirring in the time of 100 ℃, be warming up to 180 ℃ and begin reaction, still internal pressure 0.22MPa.After reaction is carried out 2 hours, the diisobutylene that adds 12.8 grams by volume pump, keep temperature to continue reaction, after 16 hours, add 17.8 gram diisobutylene again, after reaction proceeds to 20 hours, add 13.2 gram diisobutylene again, reaction to 22 hour finishes, and sampling analysis records that 4,4 '-two uncle's octyl diphenylamine content are 13.8% in the product.Method according to example 1 is collected product, obtains light yellow liquid product 108 grams, nitrogen content 4.53%.
Example 5
In the 250ml stainless steel autoclave, add 64.4 gram pentanoic, 46.8 gram diisobutylene, 9.6 gram atlapulgites, 60ppm Resorcinol stopper is with nitrogen replacement third-order reaction system.Start stirring in the time of 100 ℃, be warming up to 180 ℃ and begin reaction.React after 10 hours, add 17.4 diisobutylene that restrain, keep temperature of reaction to continue reaction by volume pump, after reaction proceeds to 18 hours, add 13.5 gram diisobutylene again, reaction finished to 22 hours, sampling analysis records that 4,4 '-two uncle's octyl diphenylamine content are 1 8.0% in the product.Method according to example 1 is collected product, obtains light yellow liquid product 109 grams, nitrogen content 4.68%.
Example 6
Adopt ASTMD-2272 rotary oxygen bomb method, the example product is carried out oxidation test, measure oil oxidation inductive phase, inductive phase is long more, and antioxygen property is good more.Base oil is selected the 150SN of Dalian Petrochemical Industry Company neutral oil, adds 0.5% example, 3 products, and compares with external several like products, and test-results sees Table 1.
Table 1
| Additive | Dosage, % | Oxidation induction period, minute |
| Example 3 | 0.5 | 104 |
| L-57 | 0.5 | 100 |
| V-81 | 0.5 | 77 |
| LZ5150A | 0.5 | 64 |
| Base oil 150SN | - | 34 |
Claims (8)
1. the preparation method of liquid alkyl diphenylamine, it is characterized in that, in the presence of activated bauxite catalyst, at 170～230 ℃ with make under the pressure that diisobutylene is in a liquid state, make diisobutylene and pentanoic contact reacts, 4,4 '-two uncle's octyl diphenylamine content were less than 20% o'clock in product, and stopped reaction is also collected product.
2. according to the said preparation method of claim 1, it is characterized in that temperature of reaction is 170～200 ℃.
3. according to the said preparation method of claim 1, it is characterized in that reaction pressure is 0.2～0.5MPa.
4. according to the said preparation method of claim 1, it is characterized in that the mol ratio of pentanoic and diisobutylene is 1: 1.3～2.0.
5. according to the said preparation method of claim 1, it is characterized in that diisobutylene can once add or divide and adds reaction system several times.
6. according to the said preparation method of claim 1, it is characterized in that the atlapulgite consumption is 5～30% of a pentanoic weight.
7. according to the said preparation method of claim 1, it is characterized in that, also can add stopper in the reactant, consumption is 5～200ppm.
8. according to the said preparation method of claim 7, it is characterized in that said stopper is selected from Resorcinol or MEHQ.
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| CN99119033A CN1112348C (en) | 1999-09-10 | 1999-09-10 | Method for preparing liquid alkyl diphenylamine |
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| CN99119033A CN1112348C (en) | 1999-09-10 | 1999-09-10 | Method for preparing liquid alkyl diphenylamine |
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Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1305605C (en) * | 2002-02-27 | 2007-03-21 | 奥地利钢铁联合企业阿尔卑斯工业设备制造有限公司 | Device for continuously casting molten metals |
| CN102320983A (en) * | 2011-06-14 | 2012-01-18 | 江苏飞亚化学工业有限责任公司 | A kind of preparation method of liquid octylated diphenylamine oxidation inhibitor |
| CN101348720B (en) * | 2007-07-18 | 2012-07-18 | 中国石油化工股份有限公司 | Composite amine antioxidant, preparation and use thereof |
| CN101745423B (en) * | 2008-11-28 | 2012-11-14 | 中国石油化工股份有限公司 | Catalyst and diphenylamine alkylation method |
| CN103709046A (en) * | 2013-12-23 | 2014-04-09 | 山东省临沂市三丰化工有限公司 | Preparation method of liquid-state octyl diphenylamine antioxidant |
| CN104628580A (en) * | 2013-11-08 | 2015-05-20 | 中国石油天然气股份有限公司 | Mixed-alkene-participating preparation method of nonyl diphenylamine |
| CN104628579A (en) * | 2013-11-08 | 2015-05-20 | 中国石油天然气股份有限公司 | Method for preparing liquidized butyl diphenylamine/octyl diphenylamine |
| CN109130400A (en) * | 2018-08-06 | 2019-01-04 | 合肥中通防水工程有限公司 | A kind of HDPE Macromolecular self-adhesive membrane waterproof roll and its manufacturing process |
| CN109369418A (en) * | 2018-10-10 | 2019-02-22 | 河南师范大学 | A kind of continuous synthesis technology and synthesizer of energy saving and environment friendly alkyl benzene amine class I liquid I antioxidant |
| CN113045429A (en) * | 2019-12-27 | 2021-06-29 | 中国石油天然气股份有限公司 | Method for simultaneously preparing antioxidant of butyl octyl diphenylamine and dioctyl diphenylamine and obtained product |
| CN114989777A (en) * | 2022-06-22 | 2022-09-02 | 湖北绿新环保包装科技有限公司 | Environment-friendly water-based transfer glue capable of improving firmness of paper |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB8332797D0 (en) * | 1983-12-08 | 1984-01-18 | Ciba Geigy Ag | Antioxidant production |
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1999
- 1999-09-10 CN CN99119033A patent/CN1112348C/en not_active Expired - Lifetime
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1305605C (en) * | 2002-02-27 | 2007-03-21 | 奥地利钢铁联合企业阿尔卑斯工业设备制造有限公司 | Device for continuously casting molten metals |
| CN101348720B (en) * | 2007-07-18 | 2012-07-18 | 中国石油化工股份有限公司 | Composite amine antioxidant, preparation and use thereof |
| CN101745423B (en) * | 2008-11-28 | 2012-11-14 | 中国石油化工股份有限公司 | Catalyst and diphenylamine alkylation method |
| CN102320983A (en) * | 2011-06-14 | 2012-01-18 | 江苏飞亚化学工业有限责任公司 | A kind of preparation method of liquid octylated diphenylamine oxidation inhibitor |
| CN104628580A (en) * | 2013-11-08 | 2015-05-20 | 中国石油天然气股份有限公司 | Mixed-alkene-participating preparation method of nonyl diphenylamine |
| CN104628579A (en) * | 2013-11-08 | 2015-05-20 | 中国石油天然气股份有限公司 | Method for preparing liquidized butyl diphenylamine/octyl diphenylamine |
| CN104628580B (en) * | 2013-11-08 | 2016-08-17 | 中国石油天然气股份有限公司 | The preparation method of the nonyl diphenylamine that a kind of mixed olefins participates in |
| CN104628579B (en) * | 2013-11-08 | 2016-08-17 | 中国石油天然气股份有限公司 | A kind of method preparing fluidization fourth, octyl diphenylamine |
| CN103709046B (en) * | 2013-12-23 | 2015-05-13 | 山东省临沂市三丰化工有限公司 | Preparation method of liquid-state octyl diphenylamine antioxidant |
| CN103709046A (en) * | 2013-12-23 | 2014-04-09 | 山东省临沂市三丰化工有限公司 | Preparation method of liquid-state octyl diphenylamine antioxidant |
| CN109130400A (en) * | 2018-08-06 | 2019-01-04 | 合肥中通防水工程有限公司 | A kind of HDPE Macromolecular self-adhesive membrane waterproof roll and its manufacturing process |
| CN109369418A (en) * | 2018-10-10 | 2019-02-22 | 河南师范大学 | A kind of continuous synthesis technology and synthesizer of energy saving and environment friendly alkyl benzene amine class I liquid I antioxidant |
| CN113045429A (en) * | 2019-12-27 | 2021-06-29 | 中国石油天然气股份有限公司 | Method for simultaneously preparing antioxidant of butyl octyl diphenylamine and dioctyl diphenylamine and obtained product |
| CN114989777A (en) * | 2022-06-22 | 2022-09-02 | 湖北绿新环保包装科技有限公司 | Environment-friendly water-based transfer glue capable of improving firmness of paper |
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| CN1112348C (en) | 2003-06-25 |
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Address after: 100029, No. 6, Xin Xin Street East, Beijing, Chaoyang District Applicant after: China Petrochemical Group Corp. Co-applicant after: Sinopec Research Institute of Petroleum Processing Address before: 100029, No. 6, Xin Xin Street East, Beijing, Chaoyang District Applicant before: China Petrochemical Group Corp. Co-applicant before: Chinese petrochemical industry Research Institute of Petro-Chemical Engineering of group company |
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Granted publication date: 20030625 |