CN1667043A - Polyurethane rubber roller - Google Patents
Polyurethane rubber roller Download PDFInfo
- Publication number
- CN1667043A CN1667043A CN 200510010660 CN200510010660A CN1667043A CN 1667043 A CN1667043 A CN 1667043A CN 200510010660 CN200510010660 CN 200510010660 CN 200510010660 A CN200510010660 A CN 200510010660A CN 1667043 A CN1667043 A CN 1667043A
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- Prior art keywords
- portions
- polyurethane
- temperature
- coverred
- roll
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Abstract
This invention provides a polyurethane coverred roll. The features are that it is made by following weight proportion materials. polytetramethylene terephthalate diol 100 portions, diethyl hydrine 10~30 portions, toluene diisocynate 10~40 portions, triethanolamine 20~40 portions, ethanol 10~25 portions, butanediol 5~15 portions, taipai powder 0.5~1 portion, 3, 3-dichloro-4, 4-diamido diphenyl methane 10~30 portions. It makes the polyurethane product has great abrasion resistance, high pressure resistance, corrosion proof and aging resistance and other capability, and the price is only 1~2 times of common rubber. Common polyurethane coverred roll is unable to use for foaming or serious friction within one month, comparing to common polyurethane coverred roll, the polyurethane coverred roll made by this method can be used for three month and there is nothing change. Its all round properties is also better than foreign homogeneous product, and it is a fully product to replace import product.
Description
Technical field
The present invention relates to a kind of high rigidity and elastomeric rubber roll, especially a kind of polyurethane rubber roller between rubber and plastics.
Background technology
The durometer level broad of urethanes, be low to moderate the following low modulus rubber of Shao Er A10, high high impact-resistant resilient material to Shao Er D85, its Young's modulus can be up to hundreds of MPas, well beyond the Young's modulus scope (about 0.2~10MPa) of other rubber, so the performance range of urethanes is very wide, be between the family macromolecule material from rubber to plastics.Also just because of characteristics such as outstanding wear-resisting, the oil resistant of urethane, ageing-resistant, low temperature resistant, high rigidity, snappiness, the consumption of urethane increases sharply in recent years, range of application constantly enlarges, be widely used in industries such as petrochemical complex, mining machinery, light industry and machinery, hydro project, traffic and shoemaking, papermaking, electromechanics, replace and saved a large amount of timber, steel and various rare metal.But the result of use in some particular surroundings such as existing polyurethane rubber roller is not ideal.When especially using under long-time, high speed conditions, it is high temperature resistant, rub resistance, performance such as corrosion-resistant can obviously descend.The urethane part that uses on the overseas high speed cigarette machine as China's import, because of will be under high speed conditions long-play, the wearing and tearing of component are comparatively serious, only be 20~35 days duration of service, not only influences production efficiency, and this type component is entirely by import, therefore, running cost is higher.Therefore, be necessary prior art is improved.
Summary of the invention
The object of the present invention is to provide a kind of polyurethane rubber roller that has high-performance at aspect such as wear-resisting, corrosion-resistant, high temperature resistant.
The present invention realizes by following technical proposal: a kind of polyurethane rubber roller is characterized in that it makes with the raw material of following mass parts:
100 parts of polytetramethylene glycol
Glycerine 10-30 part
Tolylene diisocyanate 10-40 part
Trolamine 20-40 part
Ethanol 10-25 part
Butyleneglycol 5-15 part
Cornstarch 0.5-1 part
3,3 '-two chloro-4,4 '-diaminodiphenyl-methane 10-30 part.
Above-mentioned raw materials is the commercially available prod.
Compound method:
At first glycerine is joined in the polytetramethylene glycol, be heated to 150-170 ℃, dehydration is 1-2 hour under the vacuum, and reheat is to 150-170 ℃, dewater under the vacuum, three times so repeatedly, when treating that temperature is reduced to 40-60 ℃, add toluene di-iso-cyanide ester, trolamine, ethanol, butyleneglycol, Cornstarch, stirred 2-3 hour, and maintain the temperature at 80 ℃, and carry out vacuum defoamation, add 3 afterwards, 3-two chloro-4, the 4-diaminodiphenyl-methane, be poured into die needed in, under 80-150 ℃ of temperature, dry 30-60 minute, behind the shaping and demoulding, sulfuration is 10-15 hour under 50-70 ℃ of temperature, promptly gets product.
The present invention compared with prior art has following advantage and effect: adopt such scheme, the polyurethane products that preparation is come out have extraordinary wear-resisting, high temperature resistant, corrosion-resistant, performance such as ageing-resistant, its wear resistance is 9 times of natural rubber, the over-all properties of its goods is 10 times of rubber item, and price only is 1-2 times of ordinary rubber, especially use the polyurethane rubber roller of above-mentioned formulated, in the Working environment of high rotating speed and spraying industry glycerol, use three monthly any variation not take place, and existing conventional polyurethanes rubber roll, use less than one month can't use because of foaming or heavy wear, its over-all properties is also than external like product excellence, and cost is low, expense is few, is the ideal product that can substitute import fully.
Provide performance of the present invention below:
Relative density: 1.10~1.25 pull apart unit elongation: 500~1000
Shao Er hardness: 10~100 working temperatures :-20~80 ℃
Tensile strength: 0.6~70mpa thermotolerance: excellent
Winter hardiness: winning time epistasis: can
Tear strength: excellent wear resistance: splendid
Ageing resistance: excellent anti-ozone/corona: splendid
Oil-proofness: excellent water tolerance: in
Embodiment
Below in conjunction with embodiment the present invention is described further.
Embodiment 1
Take off the row marketable material:
Polytetramethylene glycol 100 grams
Glycerine 10 grams
Tolylene diisocyanate 10 grams
Trolamine 20 grams
Ethanol 10 grams
Butyleneglycol 5 grams
Cornstarch 0.5 gram
3,3 '-two chloro-4,4 '-diaminodiphenyl-methane, 10 grams
Through following method: earlier glycerine is joined in the polytetramethylene glycol, be heated to 150 ℃, dehydration is 1 hour under the vacuum, reheat to 150 ℃, dewater under the vacuum, three times so repeatedly, when treating that temperature is reduced to 40 ℃, add toluene di-iso-cyanide ester, triethanolamine, ethanol, butyleneglycol, Cornstarch, stirred 2 hours, and maintaining the temperature at 80 ℃, deaeration is 1 hour under the vacuum, adds 3 afterwards, 3 '-two chloro-4,4 '-diaminodiphenyl-methane, be poured into die needed in, under 80 ℃ of temperature, dry 60 minutes, behind the shaping and demoulding, sulfuration is 10 hours under 50 ℃ of temperature, promptly gets product.
Embodiment 2
Take off the row marketable material:
100 kilograms of polytetramethylene glycol
30 kilograms of glycerine
40 kilograms of toluene di-iso-cyanide esters
40 kilograms of triethanolamines
25 kilograms of ethanol
15 kilograms of butyleneglycols
1 kilogram of Cornstarch
3,3 '-two chloro-4,30 kilograms of 4 '-diaminodiphenyl-methanes
Through following method: earlier glycerine is joined in the polytetramethylene glycol, be heated to 170 ℃, dehydration is 2 hours under the vacuum, reheat to 170 ℃, dewater under the vacuum, three times so repeatedly, when treating that temperature is reduced to 60 ℃, add toluene di-iso-cyanide ester, triethanolamine, ethanol, butyleneglycol, Cornstarch, stirred 3 hours, and maintain the temperature at 80 ℃, and carry out vacuum defoamation, add 3 afterwards, 3-two chloro-4,4 '-diaminodiphenyl-methane, be poured into die needed in, under 150 ℃ of temperature, dry 30 minutes, behind the shaping and demoulding, sulfuration is 15 hours under 70 ℃ of temperature, promptly gets product.
Embodiment 3
Take off the row marketable material:
100 kilograms of polytetramethylene glycol
20 kilograms of glycerine
30 kilograms of toluene di-iso-cyanide esters
30 kilograms of triethanolamines
20 kilograms of ethanol
10 kilograms of butyleneglycols
0.8 kilogram of Cornstarch
3,3-two chloro-4,20 kilograms of 4 '-diaminodiphenyl-methanes
Through following method: at first glycerine is joined in the polytetramethylene glycol, be heated to 160 ℃, dehydration is 1.5 hours under the vacuum, reheat to 160 ℃, dewater under the vacuum, three times so repeatedly, when treating that temperature is reduced to 50 ℃, add toluene di-iso-cyanide ester, triethanolamine, ethanol, butyleneglycol, Cornstarch, stirred 2 hours, and maintain the temperature at 80 ℃, and carry out vacuum defoamation, add 3 afterwards, 3 '-two chloro-4,4 '-diaminodiphenyl-methane, be poured into die needed in, under 100 ℃ of temperature, dry 45 minutes, behind the shaping and demoulding, sulfuration is 12 hours under 60 ℃ of temperature, promptly gets product.
Embodiment 4
Take off the row marketable material:
Polytetramethylene glycol 100 grams
Glycerine 12.5 grams
Tolylene diisocyanate 12.6 grams
Trolamine 15.8 grams
Ethanol 12.9 grams
Butyleneglycol 13.7 grams
Cornstarch 0.5 gram
3,3 '-two chloro-4,4 '-diaminodiphenyl-methane, 15.6 grams
Method through identical with embodiment 3 can make desired product.
Claims (2)
1, a kind of polyurethane rubber roller is characterized in that it makes with the raw material of following mass parts:
100 parts of polytetramethylene glycol
Glycerine 10-30 part
Tolylene diisocyanate 10-40 part
Trolamine 20-40 part
Ethanol 10-25 part
Butyleneglycol 5-15 part
Cornstarch 0.5-1 part
3,3 '-two chloro-4,4-diaminodiphenyl-methane 10-30 part.
2, polyurethane rubber roller according to claim 1, it is characterized in that it makes by following method: at first glycerine is joined in the polytetramethylene glycol, be heated to 150-170 ℃, dehydration is 1-2 hour under the vacuum, reheat dewaters under the vacuum to 150-170 ℃, three times so repeatedly, when treating that temperature is reduced to 40-60 ℃, add toluene di-iso-cyanide ester, trolamine, ethanol, butyleneglycol, Cornstarch stirred 2-3 hour, and maintains the temperature at 80 ℃, carry out vacuum defoamation, add 3,3 '-two chloro-4 afterwards, 4 '-diaminodiphenyl-methane, be poured into die needed in, under 80-150 ℃ of temperature, dry 30-60 minute, behind the shaping and demoulding, sulfuration is 10-15 hour under 50-70 ℃ of temperature, promptly gets product.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB2005100106609A CN1294205C (en) | 2005-02-21 | 2005-02-21 | Polyurethane rubber roller |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CNB2005100106609A CN1294205C (en) | 2005-02-21 | 2005-02-21 | Polyurethane rubber roller |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1667043A true CN1667043A (en) | 2005-09-14 |
CN1294205C CN1294205C (en) | 2007-01-10 |
Family
ID=35038333
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CNB2005100106609A Expired - Fee Related CN1294205C (en) | 2005-02-21 | 2005-02-21 | Polyurethane rubber roller |
Country Status (1)
Country | Link |
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CN (1) | CN1294205C (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102166799A (en) * | 2010-12-21 | 2011-08-31 | 攀枝花钢城集团铁路设备修造有限公司 | Horizontal production process of polyurethane rubber roller |
CN102807665A (en) * | 2012-08-27 | 2012-12-05 | 马鞍山市天鑫辊业有限责任公司 | Low-hardness pouring polyurethane rubber roller and production method thereof |
CN103817965A (en) * | 2014-03-03 | 2014-05-28 | 上海汇聚自动化科技有限公司 | Machining method for Mecanum roller |
CN106750133A (en) * | 2016-12-30 | 2017-05-31 | 山东诺威聚氨酯股份有限公司 | Low hardness polyurethane rubber roll material and preparation method thereof |
CN107629442A (en) * | 2017-10-20 | 2018-01-26 | 安徽亚源印染有限公司 | A kind of special heat-resistant antifriction compound polyurethane material of printer's roll |
CN107746567A (en) * | 2017-10-20 | 2018-03-02 | 安徽亚源印染有限公司 | A kind of printer's roll composite material special |
CN110591049A (en) * | 2019-09-26 | 2019-12-20 | 昆山博益鑫成高分子材料有限公司 | Permanent antistatic natural color polyurethane rubber roller |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1100828C (en) * | 1999-04-05 | 2003-02-05 | 长岛县聚氨酯制品厂 | Polyurethane and its use |
CN1273979A (en) * | 1999-05-17 | 2000-11-22 | 珠海市江奇家具有限公司 | Furniture core material made of polyurethane and its production method |
-
2005
- 2005-02-21 CN CNB2005100106609A patent/CN1294205C/en not_active Expired - Fee Related
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102166799A (en) * | 2010-12-21 | 2011-08-31 | 攀枝花钢城集团铁路设备修造有限公司 | Horizontal production process of polyurethane rubber roller |
CN102166799B (en) * | 2010-12-21 | 2013-11-20 | 攀枝花钢城集团铁路设备修造有限公司 | Horizontal production process of polyurethane rubber roller |
CN102807665A (en) * | 2012-08-27 | 2012-12-05 | 马鞍山市天鑫辊业有限责任公司 | Low-hardness pouring polyurethane rubber roller and production method thereof |
CN103817965A (en) * | 2014-03-03 | 2014-05-28 | 上海汇聚自动化科技有限公司 | Machining method for Mecanum roller |
CN106750133A (en) * | 2016-12-30 | 2017-05-31 | 山东诺威聚氨酯股份有限公司 | Low hardness polyurethane rubber roll material and preparation method thereof |
CN107629442A (en) * | 2017-10-20 | 2018-01-26 | 安徽亚源印染有限公司 | A kind of special heat-resistant antifriction compound polyurethane material of printer's roll |
CN107746567A (en) * | 2017-10-20 | 2018-03-02 | 安徽亚源印染有限公司 | A kind of printer's roll composite material special |
CN110591049A (en) * | 2019-09-26 | 2019-12-20 | 昆山博益鑫成高分子材料有限公司 | Permanent antistatic natural color polyurethane rubber roller |
Also Published As
Publication number | Publication date |
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CN1294205C (en) | 2007-01-10 |
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Granted publication date: 20070110 Termination date: 20110221 |