CN1290717A - Process for preparing hindered plenol polyolefine antioxidant - Google Patents
Process for preparing hindered plenol polyolefine antioxidant Download PDFInfo
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- CN1290717A CN1290717A CN 99109935 CN99109935A CN1290717A CN 1290717 A CN1290717 A CN 1290717A CN 99109935 CN99109935 CN 99109935 CN 99109935 A CN99109935 A CN 99109935A CN 1290717 A CN1290717 A CN 1290717A
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- antioxidant
- crystal
- crystal formation
- water
- polyolefine
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- 239000003963 antioxidant agent Substances 0.000 title abstract description 6
- 230000003078 antioxidant effect Effects 0.000 title abstract description 5
- 229920000098 polyolefin Polymers 0.000 title description 5
- 238000004519 manufacturing process Methods 0.000 title description 2
- 239000013078 crystal Substances 0.000 claims abstract description 33
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 23
- 238000001035 drying Methods 0.000 claims abstract description 13
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 11
- BGYHLZZASRKEJE-UHFFFAOYSA-N [3-[3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoyloxy]-2,2-bis[3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoyloxymethyl]propyl] 3-(3,5-ditert-butyl-4-hydroxyphenyl)propanoate Chemical compound CC(C)(C)C1=C(O)C(C(C)(C)C)=CC(CCC(=O)OCC(COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)(COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)COC(=O)CCC=2C=C(C(O)=C(C=2)C(C)(C)C)C(C)(C)C)=C1 BGYHLZZASRKEJE-UHFFFAOYSA-N 0.000 claims description 37
- 230000015572 biosynthetic process Effects 0.000 claims description 17
- 238000002425 crystallisation Methods 0.000 claims description 11
- 230000008025 crystallization Effects 0.000 claims description 10
- 239000012043 crude product Substances 0.000 claims description 8
- 238000005516 engineering process Methods 0.000 claims description 8
- 238000002360 preparation method Methods 0.000 claims description 8
- 238000001816 cooling Methods 0.000 claims description 7
- 238000005406 washing Methods 0.000 claims description 7
- 239000012046 mixed solvent Substances 0.000 claims description 4
- 239000002244 precipitate Substances 0.000 claims description 3
- 239000003795 chemical substances by application Substances 0.000 claims description 2
- 239000002904 solvent Substances 0.000 abstract description 7
- 238000003723 Smelting Methods 0.000 abstract 1
- 238000005755 formation reaction Methods 0.000 description 14
- 239000000047 product Substances 0.000 description 10
- KFZMGEQAYNKOFK-UHFFFAOYSA-N Isopropanol Chemical compound CC(C)O KFZMGEQAYNKOFK-UHFFFAOYSA-N 0.000 description 9
- 238000000034 method Methods 0.000 description 7
- 239000000470 constituent Substances 0.000 description 6
- 239000012452 mother liquor Substances 0.000 description 6
- 206010013786 Dry skin Diseases 0.000 description 5
- 150000001875 compounds Chemical class 0.000 description 4
- -1 pentaerythritol ester Chemical class 0.000 description 4
- 238000010792 warming Methods 0.000 description 4
- 230000008030 elimination Effects 0.000 description 3
- 238000003379 elimination reaction Methods 0.000 description 3
- 239000003112 inhibitor Substances 0.000 description 3
- 238000002844 melting Methods 0.000 description 3
- 230000008018 melting Effects 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 238000007254 oxidation reaction Methods 0.000 description 3
- 229940059574 pentaerithrityl Drugs 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000005809 transesterification reaction Methods 0.000 description 3
- BAPJBEWLBFYGME-UHFFFAOYSA-N Methyl acrylate Chemical compound COC(=O)C=C BAPJBEWLBFYGME-UHFFFAOYSA-N 0.000 description 2
- BTANRVKWQNVYAZ-UHFFFAOYSA-N butan-2-ol Chemical compound CCC(C)O BTANRVKWQNVYAZ-UHFFFAOYSA-N 0.000 description 2
- XBDQKXXYIPTUBI-UHFFFAOYSA-N dimethylselenoniopropionate Natural products CCC(O)=O XBDQKXXYIPTUBI-UHFFFAOYSA-N 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- ZXEKIIBDNHEJCQ-UHFFFAOYSA-N isobutanol Chemical compound CC(C)CO ZXEKIIBDNHEJCQ-UHFFFAOYSA-N 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- WXZMFSXDPGVJKK-UHFFFAOYSA-N pentaerythritol Chemical compound OCC(CO)(CO)CO WXZMFSXDPGVJKK-UHFFFAOYSA-N 0.000 description 2
- 230000001376 precipitating effect Effects 0.000 description 2
- 238000002834 transmittance Methods 0.000 description 2
- DKCPKDPYUFEZCP-UHFFFAOYSA-N 2,6-di-tert-butylphenol Chemical class CC(C)(C)C1=CC=CC(C(C)(C)C)=C1O DKCPKDPYUFEZCP-UHFFFAOYSA-N 0.000 description 1
- 239000005956 Metaldehyde Substances 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- RJUFJBKOKNCXHH-UHFFFAOYSA-N Methyl propionate Chemical compound CCC(=O)OC RJUFJBKOKNCXHH-UHFFFAOYSA-N 0.000 description 1
- ISWSIDIOOBJBQZ-UHFFFAOYSA-N Phenol Chemical compound OC1=CC=CC=C1 ISWSIDIOOBJBQZ-UHFFFAOYSA-N 0.000 description 1
- 239000004698 Polyethylene Substances 0.000 description 1
- 239000004743 Polypropylene Substances 0.000 description 1
- 239000004793 Polystyrene Substances 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 1
- 239000004676 acrylonitrile butadiene styrene Substances 0.000 description 1
- 238000007259 addition reaction Methods 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 231100000053 low toxicity Toxicity 0.000 description 1
- GKKDCARASOJPNG-UHFFFAOYSA-N metaldehyde Chemical compound CC1OC(C)OC(C)OC(C)O1 GKKDCARASOJPNG-UHFFFAOYSA-N 0.000 description 1
- 229940017219 methyl propionate Drugs 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000009965 odorless effect Effects 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 229920000728 polyester Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 229920001155 polypropylene Polymers 0.000 description 1
- 229920002223 polystyrene Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 235000019260 propionic acid Nutrition 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- IUVKMZGDUIUOCP-BTNSXGMBSA-N quinbolone Chemical compound O([C@H]1CC[C@H]2[C@H]3[C@@H]([C@]4(C=CC(=O)C=C4CC3)C)CC[C@@]21C)C1=CCCC1 IUVKMZGDUIUOCP-BTNSXGMBSA-N 0.000 description 1
- 238000001953 recrystallisation Methods 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 238000003809 water extraction Methods 0.000 description 1
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- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
By using mixed ternary system comprising ethanol, C3 or C4 lower alcohol and water as crystallizing solvent, mixed coarse No.1010 antioxidant is refined into dalta-crystal form No.1010 antioxidant with high purity, short smelting period, great bulk density, good flowability, less volatile component and easy drying.
Description
The present invention relates to a kind of preparation technology of polyolefine oxidation inhibitor, particularly the preparation technology of δ-crystal formation antioxidant 1010.
Antioxidant 1010 is the higher Hinered phenols antioxidant of a kind of molecular weight, by 2,6-DI-tert-butylphenol compounds and methyl acrylate carry out addition reaction earlier, generate β-(3, the 5-di-tert-butyl-hydroxy phenyl) methyl propionate, and then carry out transesterification reaction with tetramethylolmethane and make, its chemical name is four [β-(3, the 5-di-tert-butyl-hydroxy phenyl) propionic acid] pentaerythritol ester, chemical structural formula is as follows:
This material is as the oxidation inhibitor of polypropylene, linear low density of polyethylene, polyester, polyvinyl chloride, polystyrene, ABS, poly-urethane, metaldehyde and vegetable and animals oils, hydro carbons, fatty acid ester, lubricated wet goods, has efficient, low toxicity, odorless, nondiscoloration, do not pollute, many-sided excellent properties such as not volatile and heat-resisting water extraction.When adapteds such as it and other auxiliary antioxidants, stablizer, UV light absorber, present tangible synergy.At present at home and abroad, antioxidant 1010 all is regarded as optimal polyolefine oxidation inhibitor.
Say that from crystal antioxidant 1010 has the polycrystalline characteristic.Although its chemical structure is identical, there is multiple different crystalline structure, bibliographical information has multiple crystal formations such as α, β, δ, λ and γ, and there are different differences in various crystalline structure products on performance, particularly aspects such as fusing point, flowability, bulk density.
General industrial product, the outward appearance powder that is white in color, bulk density is little, and is mobile poor, causes in transit, and easily dispersing floats in the air operating environment of pollution; When in forcing machine, during melting mixing, being difficult to problems such as accurate measurement with polyolefine.It is big how to make particle, and the product of good fluidity is the purpose that the various countries researchist pursues always.U.S. U.S.Pat4,405,807 by the analysis to the previous patent method, has proposed a kind of δ-type antioxidant 1010 method that makes better performances.
Patent is pointed out, at compd A
Existence under, with 3, the reaction of 5-methyl esters and tetramethylolmethane generates antioxidant 1010.With product of transesterification reaction, do recrystallisation solvent then, make between antioxidant 1010 molecule and the Virahol molecule to form the molecular addition compound sedimentation and separate out with Virahol.Filtration washing precipitating thing in vacuum and 45 ℃ of baking dryings down, is deviate from the solvent Virahol in the precipitating thing.Dried antioxidant 1010 is dissolved in again a certain amount of ethanolic soln that contains 4% water, after the rising temperature for dissolving, decrease temperature crystalline makes that purity is good, bulk density is big, good fluidity, the easy δ-crystal formation antioxidant 1010 product of transportation and accurate measurement again.Patent is pointed out, adding compd A and Virahol crystallization formation molecular addition compound operation is the key that makes δ-crystal formation antioxidant 1010, and the existence of compd A, in the finished product, influence the purity and the yield of antioxidant 1010, make its yield low, purity difference, it synthesizes and separates and be the big technical problem of one in the industrial production.After transesterification reaction finishes, need make solvent with Virahol, make it and the antioxidant 1010 molecule between form molecular addition compound, isolate antioxidant 1010, drying is deviate from the solvent Virahol under vacuum then.Because the solubility with temperature of antioxidant 1010 in the solvent Virahol changes, and alters a great deal, its technology is difficult to control.Virahol is difficult for deviating from drying, and molecular addition compound facilitation material needs vacuum, low temperature, and time of drying is very long, causes the cost height, and is of poor benefits, and operational difficulty is in industrial difficult employing; In addition, δ-crystal formation antioxidant 1010 product that this method is produced, melting range is 111-118 ℃, a wider range.
The objective of the invention is provides a kind of suitability for industrialized production that is easy in order to overcome the deficiency of aforesaid method, and aftertreatment is simple, and the goods crystal formation is single, the preparation method of the δ that purity is good-crystal formation antioxidant 1010.
For realizing the object of the invention, adopt following method:, fully be dissolved in by ethanol, C with antioxidant 1010 mixed crystal crude product
3-C
4In the ternary mixed solvent that rudimentary alcohol and water is formed, δ-N-type waferN is done crystal seed, and crystallization range is at 75-10 ℃, and crystallization precipitate promptly gets goods through washing after drying, the cooling.
For example can take following method, best results:, be dissolved in by ethanol, C with antioxidant 1010 mixed crystal crude product
3-C
4In the ternary mixed solvent that rudimentary alcohol and water is formed, stir, be warming up to 70-73 ℃ and make its dissolving, form a homogeneous phase transparent solution, decrease temperature crystalline adds 0.5-5wt% δ-N-type waferN and does crystal seed about 57 ℃, crystallisation by cooling, when being cooled to 20 ℃, constant temperature is kept 30min.Cross the elimination mother liquor, precipitate after washing with alcohol, drying, cooling can make well behaved δ-crystal formation antioxidant 1010.
Best matter agent is 1 than scope: 3-1: 4, and best solvent consists of: water is 2-5wt%, C
3-C
4Lower alcohol is 6-10wt%, and all the other are ethanol.
In order to have guaranteed the higher crystalline yield, the whole temperature of crystallization must be controlled at below 20 ℃, and constant temperature is kept 30min.
The preparation technology of δ of the present invention-crystal formation antioxidant 1010, maximum characteristics are that product drying speed is fast, and fugitive constituent is low.Under ventilation condition, 70 ℃ of dryings two hours, 80 ℃ of dryings one hour, the fugitive constituent of product remains on below 0.1%.With transmittance at the 425nm place less than 90%, the 500nm place is less than 95%, fusing point 112-116 ℃ antioxidant 1010 mixed crystal crude product, after process for purification of the present invention is handled, can make the purity height (transmittance at the 425nm place greater than 95%, at the 500nm place greater than 97%), melting range short (112-114 ℃), the big (0.50g/cm of bulk density
3), good fluidity (8.3s/100ml), fugitive constituent low (less than 0.1%), the single δ of the easy exsiccant of product-crystal formation antioxidant 1010.
Embodiment 1:
Experimental installation is made up of with the there-necked flask of whipping appts, temperature measuring equipment, condensing works 500ml, and temperature control is carried out with water bath with thermostatic control in the outside.80g antioxidant 1010 mixed crystal crude product and 400ml are contained 4% water, the ethanolic soln of 10% Virahol mixes mutually, be warming up to 73 ℃, antioxidant 1010 crude product and impurity are dissolved fully, adding 1wt% δ-N-type waferN about 57 ℃ does crystal seed and induces, continue to be cooled to 20 ℃, antioxidant 1010 is separated out in crystallization.Cross the elimination mother liquor, crystallisate after washing with alcohol, directly 70 ℃ of down oven dry 2 hours, 80 ℃ following 1 hour, promptly get 73g δ-type antioxidant 1010 after the cooling.Fusing point 112-114 ℃, bulk density 0.48g/cm
3, mobile 8.3s/100ml is used to measure mobile funnel as shown in Figure 2, and fugitive constituent is less than 0.08%, and X-is diffracted to δ-crystal formation, as shown in Figure 1.
Fig. 1 uses funnel for measuring flowability, 1-cylinder among the figure, 2-cone, 3-outlet.
Fig. 2 is the X-diffractogram of embodiment 1 resulting product.
Embodiment 2:
80g antioxidant 1010 mixed crystal crude product and 400ml are contained 4% water, and the ethanolic solution of 8% isobutanol is mutually mixed Close, be warming up to 75 ℃, antioxidant 1010 and impurity are dissolved fully, about 58 ℃, add 1.5wt% δ-type crystal is done crystal seed, and induced crystallization, mother liquor continue to be cooled to 20 ℃, separate out antioxidant 1010. Filter Remove mother liquor, crystal was directly dried 2 hours under 70 ℃ after the ethanol washing, 80 ℃ of lower oven dry 1 hour, Cooling namely gets 70g δ-type antioxidant 1010. Fusing point 111-113 ℃, bulk density 0.50g/cm3, flowability 8.3s/100ml fugitive constituent is diffracted to δ-crystal formation less than 0.06%, X-.
Embodiment 3:
100g antioxidant 1010 mixed crystal crude product and 400ml are contained 4% water, and the ethanolic soln of 10% sec-butyl alcohol mixes mutually, is warming up to 72 ℃, make it abundant dissolving, cooling adds 3wt% δ-N-type waferN and does crystal seed, induced crystallization about 58 ℃, mother liquor continues to be cooled to 20 ℃, and antioxidant 1010 is separated out in crystallization.Cross the elimination mother liquor, crystallisate is after washing with alcohol, and 70 ℃ of dryings two hours, 80 ℃ of dryings one hour promptly got 88g δ-type antioxidant 1010.Fusing point 112-114 ℃, bulk density 0.54g/cm
3, mobile 8.3s/100ml, fugitive constituent are less than 0.09%, and X-is diffracted to δ-crystal formation.
Claims (3)
1. the preparation technology of δ-crystal formation antioxidant 1010, its characteristics are antioxidant 1010 mixed crystal crude product fully is dissolved in by ethanol, C
3-C
4In the ternary mixed solvent that rudimentary alcohol and water is formed, add 0.5-5wt% δ-N-type waferN and do crystal seed in the time of 56-60 ℃, crystallization range is at 75-10 ℃, and crystallization precipitate promptly gets goods through washing after drying, the cooling.
2. the preparation technology of δ according to claim 1-crystal formation antioxidant 1010, its characteristics are that the matter agent is 1 than scope: 3-1: 4.
3. the preparation technology of δ according to claim 1 and 2-crystal formation antioxidant 1010, its characteristics are consisting of of mixed solvent: water is 2-5wt%, C
3-C
4Lower alcohol is 6-10wt%, and all the other are ethanol.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB991099354A CN1149257C (en) | 1999-06-25 | 1999-06-25 | Process for preparing hindered plenol polyolefine antioxidant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB991099354A CN1149257C (en) | 1999-06-25 | 1999-06-25 | Process for preparing hindered plenol polyolefine antioxidant |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1290717A true CN1290717A (en) | 2001-04-11 |
| CN1149257C CN1149257C (en) | 2004-05-12 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB991099354A Expired - Fee Related CN1149257C (en) | 1999-06-25 | 1999-06-25 | Process for preparing hindered plenol polyolefine antioxidant |
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| Country | Link |
|---|---|
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114773194A (en) * | 2022-06-06 | 2022-07-22 | 宁波市鼎瑞翔新材料科技有限公司 | Method for preparing antioxidant 1010 |
-
1999
- 1999-06-25 CN CNB991099354A patent/CN1149257C/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114773194A (en) * | 2022-06-06 | 2022-07-22 | 宁波市鼎瑞翔新材料科技有限公司 | Method for preparing antioxidant 1010 |
| CN114773194B (en) * | 2022-06-06 | 2024-01-02 | 宁波市鼎瑞翔新材料科技有限公司 | Method for preparing antioxidant 1010 |
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| Publication number | Publication date |
|---|---|
| CN1149257C (en) | 2004-05-12 |
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