CN103012904A - Halogen-free flame-retardant master batch - Google Patents
Halogen-free flame-retardant master batch Download PDFInfo
- Publication number
- CN103012904A CN103012904A CN2012105960893A CN201210596089A CN103012904A CN 103012904 A CN103012904 A CN 103012904A CN 2012105960893 A CN2012105960893 A CN 2012105960893A CN 201210596089 A CN201210596089 A CN 201210596089A CN 103012904 A CN103012904 A CN 103012904A
- Authority
- CN
- China
- Prior art keywords
- halogen
- free flame
- master batch
- coupling agent
- retardant master
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
Abstract
The invention discloses a halogen-free flame-retardant master batch. The halogen-free flame-retardant master batch is composed of the following raw materials in parts by mass: 30-80 parts of halogen-free flame retardant, 15-69.7 parts of polyolefin carrier, 0.2-2 parts of silicone oil, and 0.1-3 parts of coupling agent. During preparation, the raw materials aforementioned are weighed according to a ratio at first, and then the polyolefin carrier, the silicone oil and the coupling agent are added in a high-speed stirring machine and stirred for 3 minutes with a medium-low speed, and finally, the halogen-free flame retardant is added and stirred for 5 minutes with a high speed; and the stirred raw materials are transferred into a two-stage vacuum double-screw extruder, and granulated via extrusion, wherein the temperature of the extruder is set to be 100-130 DEG C. The halogen-free flame-retardant master batch disclosed by the invention is excellent in mechanical property, good in water resistance, excellent in physical and mechanical properties, and easy to process and store.
Description
(1) technical field
The present invention relates to a kind of halogen-free flame-retardant master batch.
(2) background technology
In order to improve safety in utilization, make PP carry out a large amount of research and developments to polyacrylic fire-retardantization both at home and abroad in widely field application, the exploitation of fire-retardant PP mainly is to add fire retardant to make PP have flame retardant effect in PP.Conventional flame retardant is halogenated flame retardant, but halogenated flame retardant can send the dense smoke of black when burning, produce toxic substance and go out Dioxins, serious threat physical environment and HUMAN HEALTH, European Union has forbidden containing the product immigration of this type of material at present, so halogenated flame retardant is just progressively replaced by the novel environment friendly fire retardant.
The chemical phosphorus expanding fire retardant is generally take P, N and C as main nucleus, be applicable to the fire-retardant of multiple combustible polymers, in the polymer combustion process, drip without molten drop, also have good resistance to flame in the flame even be exposed to for a long time, and Halogen, without antimony, low cigarette, low toxicity, non-corrosiveness gas.
But expansion type flame retardant has the following disadvantages: 1. the polarity of expansion type flame retardant and polymkeric substance differs greatly and causes its consistency poor, and the electrical property of polymkeric substance and insulating property are descended to some extent, and especially mechanical property such as intensity and toughness significantly descend; 2. the expansion type flame retardant water absorbability is strong.Such as the APP/PER/MA Intumescent Retardant System, the not only easy moisture absorption of poly-hydroxy PER, and alcoholysis easily occurs between each composition, cause the flame-retardant polymer poor water resistance; 3. common, the relative molecular mass of expansion type flame retardant is little, easily migrates to polymer surfaces, thereby causes the poor mechanical property of flame retardant products, and especially aesthetic appearance is poor; 4. processing difficulties, the expanding fire retardant small molecules is more, and poor heat stability is heated and is easily decomposed, and adds to make man-hour NH3 decompose out, causes the tie rod surfaces of tacky, is difficult for processing.
(3) summary of the invention
In order to overcome the above-mentioned deficiency of existing expansion type flame retardant, the invention provides a kind of good mechanical performance, water-tolerant, physical and mechanical properties good, be easy to process the halogen-free flame-retardant master batch of depositing.
The technical scheme that the present invention solves its technical problem is: a kind of halogen-free flame-retardant master batch is characterized in that this halogen-free flame-retardant master batch is comprised of according to mass parts following raw materials according:
Halogen-free flame retardants: 30~80 parts;
Polyolefin carrier: 15~69.7 parts;
Silicone oil: 0.2~2 part;
Coupling agent: 0.1~3 part;
In the preparation, at first proportionally take by weighing above-mentioned raw materials, then polyolefin carrier, silicone oil, coupling agent are added stirring at low speed 3min in the homogenizer, add at last halogen-free flame retardants high-speed stirring 5min; The raw material that stirs is changed in the two-stage vacuum twin screw extruder, and extruding pelletization, extruder temperature are set as 100~130 ℃.
Preferably, described halogen-free flame retardants is phosphor-nitrogen expansion type combustion inhibitor, it is mixed according to arbitrary proportion by acid source, source of the gas, charcoal source and forms, and the ratio between acid source, source of the gas, the charcoal source can effect of the present invention not make a significant impact, and therefore can mix by arbitrary proportion.
Preferably, described acid source is one of ammonium polyphosphate, phosphoric acid, Vanadium Pentoxide in FLAKES, boric acid; Described source of the gas is any one in trimeric cyanamide, Dyhard RU 100, ammonium polyphosphate, amine borate, the Dyhard RU 100 formaldehyde resin; Described charcoal source is any one in tetramethylolmethane, sorbyl alcohol, the Mierocrystalline cellulose.
Preferably, described polyolefin carrier be any one or both in LDPE, the propylene-based elastomeric with any than mixing.
Preferably, described silicone oil is any one in methyl-silicone oil, hydroxy silicon oil, the amido silicon oil.
Preferably, described coupling agent is molecular weight greater than 800 solid-state titanate coupling agent or molecular weight greater than 800 solid-state aluminate coupling agent.
Preferably, when carrying out the stirring of polyolefin carrier, silicone oil, coupling agent, the rotating speed of homogenizer is 500 rev/mins, and the rotating speed of homogenizer is 800 rev/mins behind the adding halogen-free flame retardants.
Beneficial effect of the present invention is: this master batch is processed under 100~130 ℃ of conditions, and processing temperature is far below the decomposition temperature of fire retardant, and the performance that this master batch can intactly be preserved fire retardant is not destroyed, and is easy to processing and preservation.This halogen-free flame-retardant master batch selects polyolefin carrier to do body material, has advantages of that the fire retardant of making is easy to disperse, flame retarding efficiency is higher.This fire-retardant master granule can directly stir injection moulding with resin and also can be used as fire retardant and join in the forcing machine and use as halogen-free flame retardants.
The auxiliary agents (especially adopting toughness LDPE or propylene-based elastomeric higher and that be easy to process is vector resin) such as coupling agent, silicone oil are arranged in the invention, make fire retardant better with resin compatible.After fire-retardant master granule and polypropylene, polyethylene carried out blend, material not only had good flame retardant effect but also has higher toughness and intensity.Owing to utilizing silicone oil and coupling agent that fire retardant is carried out surface treatment, the wetting ability of fire retardant reduces greatly, makes in the material not facile hydrolysis and separating out of fire retardant, so material has excellent water tolerance.
(4) embodiment
Below in conjunction with embodiment the present invention is described in further detail.
Embodiment one
A kind of halogen-free flame-retardant master batch, this halogen-free flame-retardant master batch is comprised of according to mass parts following raw materials according:
Halogen-free flame retardants: 50 parts, in the present embodiment, this halogen-free flame retardants is phosphor-nitrogen expansion type combustion inhibitor, this fire retardant is mixed according to 1: 1: 1 ratio of mass ratio by acid source, source of the gas, charcoal source and forms, acid source described in the present embodiment is ammonium polyphosphate, described source of the gas is trimeric cyanamide, and described charcoal source is tetramethylolmethane.
Polyolefin carrier: 30 parts, in the present embodiment, polyolefin carrier adopts LDPE.
Silicone oil: 1.5 parts, in the present embodiment, silicone oil adopts methyl-silicone oil.
Coupling agent: 1.5 parts, in the present embodiment, coupling agent adopts molecular weight greater than 800 solid-state titanate coupling agent.
In the preparation, at first proportionally take by weighing above-mentioned raw materials, then polyolefin carrier, silicone oil, coupling agent are added stirring at low speed 3min in the homogenizer, stirring velocity is 500 rev/mins, add at last halogen-free flame retardants high-speed stirring 5min, stirring velocity is 800 rev/mins; The raw material that stirs is changed in the two-stage vacuum twin screw extruder, and extruding pelletization, extruder temperature are set as 100~130 ℃.
Embodiment two
A kind of halogen-free flame-retardant master batch, this halogen-free flame-retardant master batch is comprised of according to mass parts following raw materials according:
Halogen-free flame retardants: 30 parts, in the present embodiment, this halogen-free flame retardants is phosphor-nitrogen expansion type combustion inhibitor, this fire retardant is mixed according to 1: 10: 0.5 ratio of mass ratio by acid source, source of the gas, charcoal source and forms, acid source described in the present embodiment is phosphoric acid, described source of the gas is Dyhard RU 100, and described charcoal source is Sorbic Acid.
Polyolefin carrier: 20 parts, in the present embodiment, polyolefin carrier adopts propylene-based elastomeric.
Silicone oil: 0.2 part, in the present embodiment, silicone oil adopts hydroxy silicon oil.
Coupling agent: 0.5 part, in the present embodiment, coupling agent adopts molecular weight greater than 800 solid-state titanate coupling agent.
In the preparation, at first proportionally take by weighing above-mentioned raw materials, then polyolefin carrier, silicone oil, coupling agent are added stirring at low speed 3min in the homogenizer, stirring velocity is 500 rev/mins, add at last halogen-free flame retardants high-speed stirring 5min, stirring velocity is 800 rev/mins; The raw material that stirs is changed in the two-stage vacuum twin screw extruder, and extruding pelletization, extruder temperature are set as 100~130 ℃.
Embodiment three
A kind of halogen-free flame-retardant master batch, this halogen-free flame-retardant master batch is comprised of according to mass parts following raw materials according:
Halogen-free flame retardants: 40 parts, in the present embodiment, this halogen-free flame retardants is phosphor-nitrogen expansion type combustion inhibitor, this fire retardant is mixed according to 1: 2: 3 ratio of mass ratio by acid source, source of the gas, charcoal source and forms, acid source described in the present embodiment is Vanadium Pentoxide in FLAKES, described source of the gas is ammonium polyphosphate, and described charcoal source is Mierocrystalline cellulose.
Polyolefin carrier: 69.7 parts, in the present embodiment, polyolefin carrier adopts the mixture of LDPE and propylene-based elastomeric, and both mass ratioes are 1: 1.
Silicone oil: 0.5 part, in the present embodiment, silicone oil adopts amido silicon oil.
Coupling agent: 1 part, in the present embodiment, coupling agent adopts molecular weight greater than 800 solid-state titanate coupling agent.
In the preparation, at first proportionally take by weighing above-mentioned raw materials, then polyolefin carrier, silicone oil, coupling agent are added stirring at low speed 3min in the homogenizer, stirring velocity is 500 rev/mins, add at last halogen-free flame retardants high-speed stirring 5min, stirring velocity is 800 rev/mins; The raw material that stirs is changed in the two-stage vacuum twin screw extruder, and extruding pelletization, extruder temperature are set as 100~130 ℃.
Embodiment four
A kind of halogen-free flame-retardant master batch, this halogen-free flame-retardant master batch is comprised of according to mass parts following raw materials according:
Halogen-free flame retardants: 80 parts, in the present embodiment, this halogen-free flame retardants is phosphor-nitrogen expansion type combustion inhibitor, this fire retardant is mixed according to 1: 1: 0.2 ratio of mass ratio by acid source, source of the gas, charcoal source and forms, acid source described in the present embodiment is boric acid, described source of the gas is ammonium borate, and described charcoal source is sorbyl alcohol.
Polyolefin carrier: 15 parts, in the present embodiment, polyolefin carrier adopts the mixture of LDPE and propylene-based elastomeric, and mass ratio between the two is 10: 0.1.
Silicone oil: 1 part, in the present embodiment, silicone oil adopts methyl-silicone oil.
Coupling agent: 2.5 parts, in the present embodiment, coupling agent adopts molecular weight greater than 800 solid-state aluminate coupling agent.
In the preparation, at first proportionally take by weighing above-mentioned raw materials, then polyolefin carrier, silicone oil, coupling agent are added stirring at low speed 3min in the homogenizer, stirring velocity is 500 rev/mins, add at last halogen-free flame retardants high-speed stirring 5min, stirring velocity is 800 rev/mins; The raw material that stirs is changed in the two-stage vacuum twin screw extruder, and extruding pelletization, extruder temperature are set as 100~130 ℃.
Embodiment five
A kind of halogen-free flame-retardant master batch, this halogen-free flame-retardant master batch is comprised of according to mass parts following raw materials according:
Halogen-free flame retardants: 70 parts, in the present embodiment, this halogen-free flame retardants is phosphor-nitrogen expansion type combustion inhibitor, this fire retardant is mixed according to 10: 0.1: 10 ratio of mass ratio by acid source, source of the gas, charcoal source and forms, acid source described in the present embodiment is ammonium polyphosphate, described source of the gas is ammonium polyphosphate, and described charcoal source is Mierocrystalline cellulose.
Polyolefin carrier: 40 parts, in the present embodiment, polyolefin carrier adopts the mixture of LDPE and propylene-based elastomeric, and mass ratio between the two is 0.2: 10.
Silicone oil: 2 parts, in the present embodiment, silicone oil adopts hydroxy silicon oil.
Coupling agent: 0.1 part, in the present embodiment, coupling agent adopts molecular weight greater than 800 solid-state aluminate coupling agent.
In the preparation, at first proportionally take by weighing above-mentioned raw materials, then polyolefin carrier, silicone oil, coupling agent are added stirring at low speed 3min in the homogenizer, stirring velocity is 500 rev/mins, add at last halogen-free flame retardants high-speed stirring 5min, stirring velocity is 800 rev/mins; The raw material that stirs is changed in the two-stage vacuum twin screw extruder, and extruding pelletization, extruder temperature are set as 100~130 ℃.
Embodiment six
A kind of halogen-free flame-retardant master batch, this halogen-free flame-retardant master batch is comprised of according to mass parts following raw materials according:
Halogen-free flame retardants: 60 parts, in the present embodiment, this halogen-free flame retardants is phosphor-nitrogen expansion type combustion inhibitor, this fire retardant is mixed according to 0.1: 10: 3 ratio of mass ratio by acid source, source of the gas, charcoal source and forms, acid source described in the present embodiment is ammonium polyphosphate, described source of the gas is Dyhard RU 100, and described charcoal source is tetramethylolmethane.
Polyolefin carrier: 50 parts, in the present embodiment, polyolefin carrier adopts the mixture of LDPE and propylene-based elastomeric, and mass ratio between the two is 2: 7.
Silicone oil: 0.8 part, in the present embodiment, silicone oil adopts methyl-silicone oil.
Coupling agent: 3 parts, in the present embodiment, coupling agent adopts molecular weight greater than 800 solid-state titanate coupling agent.
In the preparation, at first proportionally take by weighing above-mentioned raw materials, then polyolefin carrier, silicone oil, coupling agent are added stirring at low speed 3min in the homogenizer, stirring velocity is 500 rev/mins, add at last halogen-free flame retardants high-speed stirring 5min, stirring velocity is 800 rev/mins; The raw material that stirs is changed in the two-stage vacuum twin screw extruder, and extruding pelletization, extruder temperature are set as 100~130 ℃.
Claims (7)
1. halogen-free flame-retardant master batch is characterized in that this halogen-free flame-retardant master batch is comprised of according to mass parts following raw materials according:
Halogen-free flame retardants: 30~80 parts;
Polyolefin carrier: 15~69.7 parts;
Silicone oil: 0.2~2 part;
Coupling agent: 0.1~3 part;
In the preparation, at first proportionally take by weighing above-mentioned raw materials, then polyolefin carrier, silicone oil, coupling agent are added stirring at low speed 3min in the homogenizer, add at last halogen-free flame retardants high-speed stirring 5min; The raw material that stirs is changed in the two-stage vacuum twin screw extruder, and extruding pelletization, extruder temperature are set as 100~130 ℃.
2. halogen-free flame-retardant master batch as claimed in claim 1, it is characterized in that: described halogen-free flame retardants is phosphor-nitrogen expansion type combustion inhibitor, it is mixed according to arbitrary proportion by acid source, source of the gas, charcoal source and forms.
3. halogen-free flame-retardant master batch as claimed in claim 2, it is characterized in that: described acid source is one of ammonium polyphosphate, phosphoric acid, Vanadium Pentoxide in FLAKES, boric acid; Described source of the gas is any one in trimeric cyanamide, Dyhard RU 100, ammonium polyphosphate, amine borate, the Dyhard RU 100 formaldehyde resin; Described charcoal source is any one in tetramethylolmethane, sorbyl alcohol, the Mierocrystalline cellulose.
4. halogen-free flame-retardant master batch as claimed in claim 1 or 2 is characterized in that: described polyolefin carrier be any one or both in LDPE, the propylene-based elastomeric with any than mixing.
5. halogen-free flame-retardant master batch as claimed in claim 1 or 2, it is characterized in that: described silicone oil is any one in methyl-silicone oil, hydroxy silicon oil, the amido silicon oil.
6. halogen-free flame-retardant master batch as claimed in claim 1 or 2 is characterized in that: described coupling agent is molecular weight greater than 800 solid-state titanate coupling agent or molecular weight greater than 800 solid-state aluminate coupling agent.
7. halogen-free flame-retardant master batch as claimed in claim 1 or 2, it is characterized in that: when carrying out the stirring of polyolefin carrier, silicone oil, coupling agent, the rotating speed of homogenizer is 500 rev/mins, adds that the rotating speed of homogenizer is 800 rev/mins behind the halogen-free flame retardants.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201210596089.3A CN103012904B (en) | 2012-12-19 | 2012-12-19 | Halogen-free flame-retardant master batch |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201210596089.3A CN103012904B (en) | 2012-12-19 | 2012-12-19 | Halogen-free flame-retardant master batch |
Publications (2)
Publication Number | Publication Date |
---|---|
CN103012904A true CN103012904A (en) | 2013-04-03 |
CN103012904B CN103012904B (en) | 2015-07-08 |
Family
ID=47962038
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201210596089.3A Active CN103012904B (en) | 2012-12-19 | 2012-12-19 | Halogen-free flame-retardant master batch |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN103012904B (en) |
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103289373A (en) * | 2013-05-22 | 2013-09-11 | 江苏金发科技新材料有限公司 | Continuous basalt fiber-reinforced halogen-free flame-retardant nylon material and preparation method thereof |
CN104250391A (en) * | 2014-09-26 | 2014-12-31 | 安徽合聚阻燃新材料股份有限公司 | Silane crosslinking halogen-free flame retardant polyolefin composite material and preparation method thereof |
CN104371116A (en) * | 2014-11-04 | 2015-02-25 | 南京林业大学 | Preparation method and application of lignin-based intumescent flame retardant |
CN104830022A (en) * | 2015-04-28 | 2015-08-12 | 中科院广州化学有限公司南雄材料生产基地 | Expansion type flame retardant prepared by electrostatic flocculation, preparation method and applications thereof |
CN105001510A (en) * | 2015-07-02 | 2015-10-28 | 广州科苑新型材料有限公司 | Low temperature resistant halogen-free flame-retardant light scattering polypropylene composition and preparation method thereof |
CN105542305A (en) * | 2016-01-25 | 2016-05-04 | 上海捷棉新材料科技有限公司 | Halogen-free high-temperature-resisting flame-resistant material high in oxygen index and preparation method and application thereof |
CN105802013A (en) * | 2016-04-22 | 2016-07-27 | 东源顺亨塑胶阻燃材料厂 | Flame-retardant masterbatch, flame-retardant masterbatch based phosphorus-nitrogen intumescent flame-retardant material and preparation method thereof |
CN110964259A (en) * | 2019-09-04 | 2020-04-07 | 上海日之升科技有限公司 | Efficient halogen-free flame-retardant master batch with polypropylene carrier and preparation method thereof |
CN112159549A (en) * | 2020-08-31 | 2021-01-01 | 浙江工业大学 | Flame retardant and application thereof |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101643649A (en) * | 2009-08-21 | 2010-02-10 | 练高水 | Expansion-type halogen-free flame retardant and flame retardant master batch using same |
CN102219957A (en) * | 2011-05-13 | 2011-10-19 | 上海化工研究院 | Functional masterbatch of halogen-free intumescent flame retardant, and preparation method thereof |
CN102675737A (en) * | 2012-05-04 | 2012-09-19 | 华东理工大学 | Novel halogen-free flame-retardant master batch material |
-
2012
- 2012-12-19 CN CN201210596089.3A patent/CN103012904B/en active Active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101643649A (en) * | 2009-08-21 | 2010-02-10 | 练高水 | Expansion-type halogen-free flame retardant and flame retardant master batch using same |
CN102219957A (en) * | 2011-05-13 | 2011-10-19 | 上海化工研究院 | Functional masterbatch of halogen-free intumescent flame retardant, and preparation method thereof |
CN102675737A (en) * | 2012-05-04 | 2012-09-19 | 华东理工大学 | Novel halogen-free flame-retardant master batch material |
Cited By (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103289373A (en) * | 2013-05-22 | 2013-09-11 | 江苏金发科技新材料有限公司 | Continuous basalt fiber-reinforced halogen-free flame-retardant nylon material and preparation method thereof |
CN104250391B (en) * | 2014-09-26 | 2016-09-28 | 安徽合聚阻燃新材料股份有限公司 | A kind of silane crosslinked halogen-free flame-retardant composite polyolefine material and preparation method thereof |
CN104250391A (en) * | 2014-09-26 | 2014-12-31 | 安徽合聚阻燃新材料股份有限公司 | Silane crosslinking halogen-free flame retardant polyolefin composite material and preparation method thereof |
CN104371116A (en) * | 2014-11-04 | 2015-02-25 | 南京林业大学 | Preparation method and application of lignin-based intumescent flame retardant |
CN104371116B (en) * | 2014-11-04 | 2017-01-18 | 南京林业大学 | Preparation method and application of lignin-based intumescent flame retardant |
CN104830022A (en) * | 2015-04-28 | 2015-08-12 | 中科院广州化学有限公司南雄材料生产基地 | Expansion type flame retardant prepared by electrostatic flocculation, preparation method and applications thereof |
CN105001510B (en) * | 2015-07-02 | 2018-06-12 | 广州科苑新型材料有限公司 | A kind of low temperature resistant halogen-free flameproof light diffusion polypropene composition and preparation method thereof |
CN105001510A (en) * | 2015-07-02 | 2015-10-28 | 广州科苑新型材料有限公司 | Low temperature resistant halogen-free flame-retardant light scattering polypropylene composition and preparation method thereof |
CN105542305A (en) * | 2016-01-25 | 2016-05-04 | 上海捷棉新材料科技有限公司 | Halogen-free high-temperature-resisting flame-resistant material high in oxygen index and preparation method and application thereof |
CN105802013A (en) * | 2016-04-22 | 2016-07-27 | 东源顺亨塑胶阻燃材料厂 | Flame-retardant masterbatch, flame-retardant masterbatch based phosphorus-nitrogen intumescent flame-retardant material and preparation method thereof |
CN110964259A (en) * | 2019-09-04 | 2020-04-07 | 上海日之升科技有限公司 | Efficient halogen-free flame-retardant master batch with polypropylene carrier and preparation method thereof |
CN110964259B (en) * | 2019-09-04 | 2022-07-29 | 上海日之升科技有限公司 | Efficient halogen-free flame-retardant master batch with polypropylene carrier and preparation method thereof |
CN112159549A (en) * | 2020-08-31 | 2021-01-01 | 浙江工业大学 | Flame retardant and application thereof |
Also Published As
Publication number | Publication date |
---|---|
CN103012904B (en) | 2015-07-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN103012904B (en) | Halogen-free flame-retardant master batch | |
CN102241889A (en) | Halloysite composite flame retardant masterbatch | |
CN101210079B (en) | Mg(OH)2 inorganic anti-flaming material and its preparing method and application | |
CN102875851B (en) | Environment-friendly flame retardant | |
CN102153820A (en) | Preparation method of flame retarding styrene polymer composite material | |
CN102250383B (en) | Halogen-free fire retardant containing benzoxazine and polymer material comprising same | |
CN102964681B (en) | Halogen-free flame-retardant polypropylene material and preparation method thereof | |
CN101982497B (en) | Flame-retardant acrylonitrile-butadiene-styrene (ABS) composite material | |
CN103554598B (en) | The preparation method of halogen-free flameproof high density polyethylene(HDPE)/ethylene-vinyl acetate copolymer | |
CN101134830A (en) | Non-bittern expanding flame-proof material and method for making same | |
CN102093566B (en) | Macromolecular intumescent flame retardant with phosphorus and nitrogen and synthesis method thereof | |
CN102604346A (en) | Biodegradable polylactic acid-starch flame retardant composite material and preparation method thereof | |
CN107304268B (en) | Flame-retardant polyolefin compound and preparation method thereof | |
CN107400286A (en) | The PE materials and its preparation technology of a kind of high barrier | |
CN102964667A (en) | Halogen-free flame-retardant polyethylene composite material and preparation method thereof | |
CN103333423B (en) | Compound flame-retardant polystyrene composition and preparation method thereof | |
CN107353437A (en) | A kind of expansion type flame retardant and preparation method thereof | |
CN102746856A (en) | Composite intumescent fire retardant | |
Huang et al. | Flame retardant polypropylene with a single molecule intumescent flame retardant based on chitosan | |
CN103102593A (en) | Supported metal oxide catalytic synergistic inorganic flame retardant polypropylene composite material and preparation method thereof | |
CN103709666A (en) | Halogen-free and flame retardation modified PET engineering plastic and preparation method thereof | |
CN105602008B (en) | A kind of expanding halide-free fire-retardant and preparation method thereof | |
CN102229719A (en) | Nano mesoporous molecular sieve synergistic intumescent flame retardant flame-retardant polypropylene | |
CN103849041A (en) | Halogen-free flame-retardant masterbatch for polyethylene and preparation method of halogen-free flame-retardant masterbatch | |
CN103333424B (en) | Halogen-free environment-friendly polystyrene flame retardant and preparation method thereof |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CP01 | Change in the name or title of a patent holder | ||
CP01 | Change in the name or title of a patent holder |
Address after: 315335 Cixi City, Zhouxiang Province town, No. two, No. development road, No. 1 Patentee after: Ningbo Yi Bin electronic Polytron Technologies Inc Address before: 315335 Cixi City, Zhouxiang Province town, No. two, No. development road, No. 1 Patentee before: Ningbo ChangHua Auto Decorations Co., Ltd. |