CN1188120A - Method for preparing polyurethane elastic body for multiplying wheel - Google Patents
Method for preparing polyurethane elastic body for multiplying wheel Download PDFInfo
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- CN1188120A CN1188120A CN97101616A CN97101616A CN1188120A CN 1188120 A CN1188120 A CN 1188120A CN 97101616 A CN97101616 A CN 97101616A CN 97101616 A CN97101616 A CN 97101616A CN 1188120 A CN1188120 A CN 1188120A
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- elastic body
- polyurethane elastic
- preparing polyurethane
- multiplying wheel
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Abstract
The present invention relates to a preparation method of polyurethane elastomer which can be used as material for making speed-increasing gear. Said preparation method is characterized by that it uses common polyurethane raw material MDI as base material, changes molecular weight distribution of chain segment, rigid chain segment content and crosslinking density to make the structures of configuration and conformation of molecular chain and state of aggregation of polyurethane produce microphase separation so as to raise its heat resisting property and mechanical property, and make its product possess high heat stability and high chemical resistance. Said invented preparation method is simple and easy to implement.
Description
The invention belongs to a kind of method for preparing polyurethane elastic body, relate in particular to a kind of method for preparing polyurethane elastic body that is used for multiplying wheel.
One of working method of chemical fibre industry recoverable deformation silk---in the rotor-type false-twisting device, multiplying wheel is with ten thousand rev/mins of 30,000 rev/mins speed friction bowl and speedups to 33, to satisfy processing requirement.This just requires multiplying wheel to have excellent elasticity, wear resisting property and enough frictional coefficient.Simultaneously, because high speed rotary grinding certainly will produce Nei Shengre, thermostability and ageing-resistant performance proposition higher requirement to multiplying wheel make common polyurethane elastomer can't be used as the multiplying wheel material.Offshore company mostly adopts with 1,5-naphthalene diisocyanate (NDI) be the base polyurethane elastomer as the multiplying wheel material, because the characteristic of the molecular structure of NDI raw material own has determined that its elastomerics has higher thermostability and mechanical property, and be the method for preparing polyurethane elastic body that high thermal stability and ageing-resistant performance can be used for the multiplying wheel material that has of base with conventional polyurethanes raw material MDI, find as yet by retrieval.
It is base with conventional polyurethanes raw material MDI that goal of the invention of the present invention provides a kind of, can be used for the method for preparing polyurethane elastic body of multiplying wheel material.
The object of the present invention is achieved like this: divided amount distribution, the content of rigid chain segment, cross-linking density by changing segmental, make the structure generation microphase-separated such as state of aggregation of configuration, conformation and the urethane of molecular chain, thereby improve resistance toheat and mechanical property.
Its preparation method is as follows:
(1) consist of (equivalence ratio) MDI by material: the proportioning of dehydration dibasic alcohol=4: 1～8: 1 adds in the reactor, is warming up to 80-90 ℃ under whipped state, reacts 2-4 hour, makes poly-aggressiveness;
(2) consist of (weight ratio) performed polymer by material: after heat-resisting mineral filler=100: 5～adding mineral filler in 100: 20, mix and obtain raw material;
(3) with in second raw material that obtain of step-NCO and mixed chain extender in-OH consists of (equivalence ratio) by material to be mixed in 1: 0.85～1: 1, chain extending reaction 3-8 minute, pour into a mould;
(4) pour mass after 6 hours, through anneal, promptly gets product 100 ℃ of sulfurations.
Aforesaid dibasic alcohol comprises all polyester diol of poly-epsilon-caprolactone, polyethylene glycol adipate, poly-hexanodioic acid second/propylene glycol ester, and molecular weight is 800～2000.
Aforesaid chainextender is the mixture of dibasic alcohol and trivalent alcohol, and its equivalence ratio is
Dibasic alcohol: trivalent alcohol=1.5: 1～8: 1
Aforesaid dibasic alcohol chainextender comprises ethylene glycol, propylene glycol, 1.4-butyleneglycol (BDO), hexylene glycol, hydroquinone two hydroxy ethyl ether etc.
The trivalent alcohol chainextender comprises: TriMethylolPropane(TMP) (TMP), glycerine, 1.2.6-hexanetriol etc.
Aforesaid heat-resisting mineral filler comprises: carbon black, white carbon black, superfine silicon dioxide etc.Can single adding also can mix adding.Granularity is the 200-300 order.
The present invention has following advantage,
1. replace the higher NDI raw material of price with common MDI raw material.
2. the cost of product reduces.
3. preparation process is simple, easy goes.
4. have high thermal stability and ageing resistance, can be used for the multiplying wheel material.
Embodiments of the invention are as follows:
Embodiment one
(1) 50gMDI and 44.4g polyethylene glycol adipate dibasic alcohol (M=1000) are added in the reactor, after under whipped state, freely heating up 10 minutes, be heated to 85 ℃, keep reaction 3.5 hours, make performed polymer.The equivalence ratio of reactant is MDI: polyethylene glycol adipate=4.5: 1.(NCO) content is-NCO%=13.3% performed polymer through deaeration post analysis free isocyanate groups.
(2) press performed polymer: carbon black=100: 10 (weight ratio), in performed polymer, add the 9.4g carbon black, mix and obtain raw material.
(3) by in second raw material that obtain of step-NCO: in the chainextender-OH=1: 0.9 (equivalence ratio), get raw material that 808 second steps obtained and 5.5gBDO+3.7gTMP mixed chain extender and in the time of 85 ℃, mix, stirred rapidly 3.5 minutes, pour into a mould.
The mixed chain extender equivalence ratio is BDO: TMP=1.5: 1.
(4) pour mass after 6 hours, through anneal, promptly obtains product 100 ℃ of sulfurations.
Embodiment two
(1) the poly-hexanodioic acid second/propylene glycol ester (M=2000) of 60gMDI and 64.0g is kept reaction 3.0 hours at 83 ℃, make performed polymer, the equivalence ratio of reactant is MDI: poly-hexanodioic acid second/propylene glycol ester=7.5: 1, performed polymer is through deaeration post analysis-NCO%=13.4%
(2) press performed polymer: carbon black=100: 5 (weight ratio), in performed polymer, add the 6.2g carbon black, mix and obtain raw material.
(3) by in second raw material that obtain of step-NCO: in the chainextender-OH=1: 0.95 (equivalence ratio), get raw material that second step of 80g obtains and 8.3gBDO+1.4g glycerine mixed chain extender and in the time of 83 ℃, mix, stirring reaction was poured into a mould after 4 minutes.
Mixed chain extender equivalence ratio BDO: glycerine=4: 1
(4) pour mass after 6 hours, through anneal, promptly obtains product 100 ℃ of sulfurations.
Embodiment three
(1) the poly-hexanodioic acid second/propylene glycol ester (M=2000) of 60gMDI and 68.6g is kept reaction 3.5 hours at 85 ℃, makes performed polymer.
The equivalence ratio of reactant is MDI: poly-hexanodioic acid second/propylene glycol ester=7: 1
Performed polymer is through deaeration post analysis NCO%=13.0%
(2) press performed polymer: superfine silicon dioxide=100: 8 (weight ratio) adds the 10.3g superfine silicon dioxide in performed polymer, obtain raw material after mixing.
(3) by in second raw material that obtain of step-NCO: in the chainextender-OH=1: 0.98 (equivalence ratio), get the raw material that 808 second steps obtained and mix at 85 ℃ with 5.2g ethylene glycol+2.5gTMP mixed chain extender, stirred 3.5 minutes, pour into a mould.
The mixed chain extender equivalence ratio is ethylene glycol: TMP=3: 1
(4) be cast in 100 ℃ of sulfurations after 6 hours,, promptly obtain product through anneal.
Embodiment four
(1) 608MDI and 56.9g poly-epsilon-caprolactone (M=996) are kept reaction 3 hours at 80 ℃, make performed polymer.The equivalence ratio of reactant is MDI: poly-epsilon-caprolactone=4.2: 1
Performed polymer is through deaeration post analysis-NCO%=12.8%.
(2) press performed polymer: white carbon black=100: 15 (weight ratio), in performed polymer, add 17.5% white carbon black, obtain raw material after mixing.
(3) by in second raw material that obtain of step-NCO: in the chainextender-OH=1: 0.96 (equivalence ratio), get the raw material that 808 second steps obtained and mix at 80 ℃ with 9.8g hexylene glycol+1.5gTMP mixed chain extender, stirring reaction 5 minutes is poured into a mould.
The mixed chain extender equivalence ratio is hexylene glycol: TMP=5: 1.
(4) pour mass after 6 hours, through anneal, promptly obtains product 100 ℃ of sulfurations.
Embodiment five
(1) 60gMDI and 73.3g poly-epsilon-caprolactone (M=1680) are kept reaction 3.5 hours at 82 ℃, make performed polymer.Reactant equivalence ratio MDI: poly-epsilon-caprolactone=5.5: 1
Performed polymer is through taking off vapour post analysis NCO%=12.1%.
(2) press performed polymer: superfine silicon dioxide=100: 10 (weight ratio) adds the 13.3g superfine silicon dioxide in performed polymer, obtain raw material after mixing.
(3) by in second raw material that obtain of step-NC: in the chainextender-OH=1: 0.95 (equivalence ratio), get the raw material that second step of 80g obtains and mix at 82 ℃ with 7.6gBDO+0.9g glycerine mixed chain extender, stirring reaction 4 minutes is poured into a mould.
The mixed chain extender equivalence ratio is BDO: glycerine=6: 1.
(4) pour mass after 6 hours, through anneal, promptly gets product 100 ℃ of sulfurations.
Claims (6)
1. method for preparing polyurethane elastic body that is used for multiplying wheel, its system is levied and is:
(1) consist of (equivalence ratio) MDI by material: the proportioning of dehydration dibasic alcohol=4: 1～8: 1 adds in the reactor, is warming up to 80-90 ℃ under whipped state, reacts 2-4 hour, makes poly-aggressiveness;
(2) consist of (weight ratio) performed polymer by material: after heat-resisting mineral filler=100: 5～adding mineral filler in 100: 20, mix and obtain raw material;
(3) with in second raw material that obtain of step-NCO and mixed chain extender in-OH consists of (equivalence ratio) by material to be mixed in 1: 0.85～1: 1, chain extending reaction 3-8 minute, pour into a mould;
(4) pour mass after 6 hours, through anneal, promptly gets product 100 ℃ of sulfurations.
2. a kind of method for preparing polyurethane elastic body that is used for multiplying wheel according to claim 1, it is characterized in that described dibasic alcohol comprises all polyester diol of poly-epsilon-caprolactone, polyethylene glycol adipate, poly-hexanodioic acid second/propylene glycol ester, molecular weight is 800～2000.
3. a kind of method for preparing polyurethane elastic body that is used for multiplying wheel according to claim 1 is characterized in that described chainextender is the mixture of dibasic alcohol and trivalent alcohol, and its equivalence ratio is a dibasic alcohol: trivalent alcohol=1.5: 1～8: 1
4. a kind of method for preparing polyurethane elastic body that is used for multiplying wheel according to claim 1 is characterized in that described dibasic alcohol chainextender comprises ethylene glycol, propylene glycol, 1.4-butyleneglycol (BDO), hexylene glycol, hydroquinone two hydroxy ethyl ether.
5. a kind of method for preparing polyurethane elastic body that is used for multiplying wheel according to claim 1 is characterized in that described trivalent alcohol chainextender comprises: TriMethylolPropane(TMP) (TMP), glycerine, 1.2.6-hexanetriol.
6. a kind of method for preparing polyurethane elastic body that is used for multiplying wheel according to claim 1 is characterized in that described heat-resisting mineral filler comprises: carbon black, white carbon black, superfine silicon dioxide.Can single adding also can mix adding.Granularity is the 200-300 order.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN97101616A CN1057313C (en) | 1997-01-17 | 1997-01-17 | Method for preparing polyurethane elastic body for multiplying wheel |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN97101616A CN1057313C (en) | 1997-01-17 | 1997-01-17 | Method for preparing polyurethane elastic body for multiplying wheel |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1188120A true CN1188120A (en) | 1998-07-22 |
| CN1057313C CN1057313C (en) | 2000-10-11 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN97101616A Expired - Fee Related CN1057313C (en) | 1997-01-17 | 1997-01-17 | Method for preparing polyurethane elastic body for multiplying wheel |
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| Country | Link |
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| CN (1) | CN1057313C (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107602796A (en) * | 2017-09-26 | 2018-01-19 | 苏州米颜生物科技有限公司 | A kind of preparation method of compounded rubber for solid tyre |
| CN109810485A (en) * | 2019-01-29 | 2019-05-28 | 天津百恩威新材料科技有限公司 | Graphite/elastic resin composite grain, its preparation method and the application in production polishing wheel |
| CN110951034A (en) * | 2019-12-19 | 2020-04-03 | 万果新材料科技(上海)有限公司 | High-load-bearing low-endogenous heat polyurethane elastomer and preparation method thereof |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3457234A (en) * | 1966-11-18 | 1969-07-22 | Uniroyal Inc | Polyurethane elastoplastic resistant to high speed flexural impact and gear made therefrom |
| US4164251A (en) * | 1975-04-21 | 1979-08-14 | The Goodyear Tire & Rubber Company | Polyurethane tire and wheel assembly |
| US4071279A (en) * | 1975-04-21 | 1978-01-31 | The Goodyear Tire & Rubber Company | Solid polyurethane tire and wheel assembly |
| US5290903A (en) * | 1992-11-09 | 1994-03-01 | Norton Company | Composite abrasive wheels |
-
1997
- 1997-01-17 CN CN97101616A patent/CN1057313C/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107602796A (en) * | 2017-09-26 | 2018-01-19 | 苏州米颜生物科技有限公司 | A kind of preparation method of compounded rubber for solid tyre |
| CN109810485A (en) * | 2019-01-29 | 2019-05-28 | 天津百恩威新材料科技有限公司 | Graphite/elastic resin composite grain, its preparation method and the application in production polishing wheel |
| CN110951034A (en) * | 2019-12-19 | 2020-04-03 | 万果新材料科技(上海)有限公司 | High-load-bearing low-endogenous heat polyurethane elastomer and preparation method thereof |
| CN110951034B (en) * | 2019-12-19 | 2022-03-01 | 万果新材料科技(上海)有限公司 | High-load-bearing low-endogenous heat polyurethane elastomer and preparation method thereof |
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| Publication number | Publication date |
|---|---|
| CN1057313C (en) | 2000-10-11 |
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