CN101376692B - Preparation of flame-retardant polyester for preparing industrial yarn - Google Patents
Preparation of flame-retardant polyester for preparing industrial yarn Download PDFInfo
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- CN101376692B CN101376692B CN2007100453783A CN200710045378A CN101376692B CN 101376692 B CN101376692 B CN 101376692B CN 2007100453783 A CN2007100453783 A CN 2007100453783A CN 200710045378 A CN200710045378 A CN 200710045378A CN 101376692 B CN101376692 B CN 101376692B
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Abstract
A method for preparing flame-retardant polyester for manufacturing industrial yarn comprises the following steps: 1) carrying out the esterification of monomer terephthalic acid, ethylene glycol and pentaerythritol ester; and 2) adding a reactive flame retardant having a structural formula I, and sequentially carrying out the pre-polymerization reaction and the polycondensation reaction in the presence of a polycondensation catalyst to obtain the flame-retardant polyester. In the structural formula I, R1 is alkylidene of C1 to C4, and R2 and R3 are respectively H or hydroxyalkyl of C2 to C4. Nano kaolin particles which serve as a flame-retardant polyester crystallization nucleating agent are added to the reaction system, wherein the nano kaolin particles are added before the esterification or before the pre-polymerization reaction, and the adding amount by the content of the nano kaolin particles existing in the polycondensation products at the end is 0.06 wt% to 1.0 wt%. The deviation of the thermal transformation performance existing between the conventional polyester and the prepared flame-retardant polyester is obviously reduced, so that the conventional polyester fiber manufacturing equipment and the manufacturing process thereof can be adopted to reliably manufacture the flame-retardant industrial yarn.
Description
Technical field
The present invention relates to a kind of preparation method of flame retardant polyester, particularly be used for the process industry silk, contain the preparation method that phosphorus is the flame retardant polyester of organic reaction type fire retardant.
Background technology
Polyester development in recent years with flame retardant properties is rapid, the Application Areas of product relates to civilian and industrial, wherein the application of fire-retardant polyester fibre is then extensive, especially just at the indusrial polyester fiber (or claiming polyester industrial fiber) of sustainable growth, possess excellent flame-retardant performance becomes its basic performance requriements to consumption gradually.The fire retardant that flame retardant polyester adopts mainly comprises three types: addition type, copolyreaction type and back arrangement type, comparatively speaking, copolyreaction type flame retardant polyester is linked on the macromolecular chain of polyester because of fire retardant, so flame retardant properties is more stable and long-acting.Phosphorus is the flame retardant properties excellence of reactive flame retardant, and environmental friendliness, is acknowledged as one of optimal polyester flame-retardant agent, uses the flame retardant polyester product of this based flame retardant also to become the main flow of research and development.
Employing phosphorus is that the flame retardant polyester of reactive flame retardant also can be described as phosphorous copolyester, the introducing of fire retardant has destroyed the regularity of macromolecular structure, thereby cause its heat deflection performance that tangible change has taken place, the change of this heat deflection performance is particularly outstanding to the manufacturing processing adverse effect of polyester industrial fiber.In order to obtain higher modulus, the common needs of polyester that are used for the process industry silk are again by its limiting viscosity of the incompatible increase of solid polycondensation, just because the change of heat deflection performance, in carrying out drying crystalline and solid state polymerization processes, serious adhesion caking phenomenon can take place in phosphorous copolyester, makes that drying crystalline and solid state polymerization processes are difficult to carry out smoothly.In the prior art, people have to by taking to reduce pre-Tc, drying temperature, slow down temperature rise rate, prolong time of drying, using the intermittent type vacuum drum drying plant that falls behind, reduce measures such as solid phase polymerization temperature and prolongation polymerization time and overcome, this has just increased production cost greatly and has reduced production efficiency.The change of this heat deflection performance disadvantageous effect that manufacturing brings to fiber also is present in the spinning drafting process, and it is stable that it will make that the drawing-off operating procedure is difficult for.
In the prior art, the technical scheme release that much is intended to improve the phosphorous copolyester thermal characteristics is arranged.Introduce by in flame retardant polyester, adding inorganic additive as Chinese patent 02133602.4, Chinese patent application 200510021959.4 and can improve its thermal characteristics, can obviously reduce the generation of melt drippage after the flame retardant polyester fusion.But it is bigger that existing these methods add the amount of inorganic additivess, and additive level reaches 5wt% and just brings about tangible results when above in the polyester, the highest even reach 10wt% or 30wt%.This has been similar in fact, and the adding inorganic filler improves its thermal characteristics in phosphorous copolyester, it is little for making the influence of film or other moulded product to mix the higher inorganic particulate matter of content in the polymer melt, but to spinning processing obviously is disadvantageous, causes broken end, filament spinning component life cycle to shorten during as spinning easily; Yielding stress reduces and influences macromolecular orientation degree etc. during drawing-off, and the latter will directly influence the mechanical property of fiber product.
Existing technical scheme all proposes to attempt to dwindle departing from that phosphorous copolyester and normal polyester exist clearly on the heat deflection performance, and for the manufacturing firm of trevira, dwindling phosphorous copolyester and normal polyester departing from the heat deflection performance should expect the most, because the manufacturing difficulty of processing that this will reduce fiber greatly reduces production costs effectively.
Summary of the invention
The invention provides a kind of preparation method who makes the flame retardant polyester of industry silk usefulness, its technical problem to be solved is that the flame retardant polyester that makes is dwindled and departing from that normal polyester produces on the heat deflection performance, thereby overcome the defective that prior art exists, simultaneously, require the technical measures itself solve the problems of the technologies described above can the performance of the manufacturing of flame retardant polyester industry silk or the product that makes not to be had a negative impact.
Below be the technical scheme that the present invention solves the problems of the technologies described above:
A kind of preparation method who makes the flame retardant polyester of industry silk usefulness, this method may further comprise the steps:
1) monomers terephthalic acid, ethylene glycol and tetramethylolmethane carry out esterification, and the feed ratio of raw material is respectively: with molar ratio computing, and terephthalic acid: ethylene glycol=100: 110～200; In weight ratio, terephthalic acid: tetramethylolmethane=100: 0.01～0.12, temperature of reaction are 260～280 ℃, and reaction pressure is 100～300kPa, and reactant residence time is 1.5～4 hours;
2) add reactive flame retardant in the esterification products, carry out prepolymerization reaction and polycondensation successively and obtain the polycondensation product flame retardant polyester in the presence of polycondensation catalyst, reactive flame retardant is the compound with following structural formula:
R in the structural formula
1Be the alkylidene group of C1～C4, R
2And R
3Respectively the do for oneself hydroxyalkyl of H or C2～C4, the add-on of reactive flame retardant is a benchmark with the charging capacity of monomers terephthalic acid, the weight ratio of terephthalic acid and reactive flame retardant is 100: 2.90～14.60, reactive flame retardant spent glycol making beating mixes, and adds in the esterification products after being mixed with the slurry that concentration is 20～45wt%.
Prepolymerization reaction and polycondensation are all carried out under negative pressure, temperature of reaction is 270～285 ℃, reactant residence time respectively is 1～3 hour, the vacuum tightness of prepolymerization reaction is 1.0～2.0kPa, the vacuum tightness of polycondensation is 0.1～0.2kPa, and the limiting viscosity of polycondensation product is controlled to be 0.60～0.75dl/g.
In above-mentioned preparation process, in reactive system, add nano kaoline particle as the flame retardant polyester crystallization nucleating agent, nano kaoline particulate median size is 200～600nm, its adding mode is for adding before esterification or adding before prepolymerization reaction, and nano kaoline particulate add-on is counted 0.06～1.0wt% with the content that it finally is present in the polycondensation product.
Above-mentioned nano kaoline particulate median size is preferably 200～500nm; Nano kaoline particulate add-on is preferably 0.2～0.9wt% in the content that it finally is present in the polycondensation product.
The limiting viscosity of above-mentioned polycondensation product preferably is controlled to be 0.60～0.70dl/g.
When nano kaoline particulate adding mode is fashionable for adding before esterification, the nano kaoline particle can be pulled an oar with the raw material of esterification and mix back adding reactive system; Before nano kaoline particulate adding mode is prepolymerization reaction, add fashionable, generally should be with nano kaoline particle, reactive flame retardant with the mixing of pulling an oar as the ethylene glycol of solvent, add reactive system after being mixed with the slurry that total concn is 20～45wt%.
Above-mentioned polycondensation catalyst can be taken from any in antimony glycol, antimony acetate or the antimonous oxide; The consumption of polycondensation catalyst is a benchmark with monomers terephthalic acid weight, in antimony ion, is 120～300mg/kg.
Existing studies show that, Chang Gui polyester relatively, the second-order transition temperature T of phosphorous copolyester
g, fusing point T
mReduce, and cold crystallization peak temperature T
HcRaising, fusion-crystallization peak temperature T
CcReduce, this crystallizing power that is indicating phosphorous copolyester descends, be that crystallization rate descends, and the change of this crystal property should be to cause phosphorous copolyester to be difficult for stable main and direct reason at drying crystalline, solid state polymerization processes generation adhesion caking, drawing-off operating procedure.The contriver has given one's full attention to this point, and has finished the present invention in view of the above.
Key of the present invention is that the process in esterification or polycondensation has added an amount of nano kaoline in system, makes and introduces a kind of suitable crystallization nucleating agent in the phosphorous copolyester that makes, and then adjust its heat deflection performance.Can promote the crystalline generation and accelerate crystallization rate to be well-known though in superpolymer, introduce nucleator in right amount, yet, will find a kind of suitable and ideal nucleator pointedly is not apparent also, and this relates to the negative impact that the dispersibility of nucleator in polyester, nucleator may bring spinning and post-treatment performance the introducing of the ability that promotes crystal to generate, nucleator as nucleus, the problems such as possibility that cause the form and aspect variation.
The contriver screens the multiple material that may possess nucleogenesis by a large amount of experiments, finds that finally above-mentioned nano kaoline is ideal as the nucleator of above-mentioned phosphorous copolyester.Characteristics such as this nucleator has easy dispersion, and is easy to operate generate, accelerate crystallization rate to the crystal that promotes above-mentioned phosphorous copolyester and have very ideal effect.Required add-on is very little, thereby can make the various negative impacts that introducing produced by nucleator can be controlled at minimum degree.Know that by experimental result the nucleator in being present in phosphorous copolyester is 0.2wt% when above, the second-order transition temperature T of phosphorous copolyester
g, fusing point T
m, that crystallization rate etc. characterizes the critical index and the normal polyester of heat deflection performance is very approaching.Production application by reality is also found, even the drying crystalline that the flame retardant polyester that makes thus adopts general continuous drying equipment and adopts conventional section drying process condition to cut into slices, and adopt conventional processing condition to carry out solid state polymerization, the adhesion caking phenomenon obviously reduces even disappears, and post-treatment processes such as spinning process and drawing-off are also highly stable.
The adding of nucleator can add system with other raw material before esterification is carried out, also can be before esterification finishes aftercondensated reaction and carries out the adding system.Nucleator adopts mixing of reaction process with polyester, is uniformly distributed in the polyester with can guaranteeing the nucleator high dispersing.
Should say that except adding an amount of nano kaoline particle as the crystallizing polyester nucleator in esterification or polycondensation process, other parts and prior art in the technical solution of the present invention are basic identical in system.And as the raw material of spinning, the various additives that also can add other in the above-mentioned flame retardant polyester as required, as matting agent, be used to prevent that polyester from producing the pyrolysated stablizer, adjusting the toning agent of form and aspect etc., everything is those of ordinary skill in the art and knows.
Compared with prior art, departing from obviously that flame retardant polyester that the present invention makes and normal polyester exist on the heat deflection performance dwindled, and can satisfy fiber manufacturing firm fully and adopt conventional trevira producing apparatus and technology stably to produce the requirement of flame retardant polyester industry silk.Simultaneously, just because dwindling of departing from of heat deflection performance, make the decline of mechanical property of fiber also be improved.On the other hand, because the add-on of nucleator is very low, itself is little of the degree that can ignore fully in the negative impact that the spinning processing process produces to polyester.
Below will the invention will be further described by specific embodiment, because essence of the present invention is to have added in system in esterification or polycondensation process a kind of crystallization nucleating agent of polyester, and other parts and prior art are basic identical, and those skilled in the art can predict, and other parts change back the present invention can obtain identical effect equally.One of monomer in polyester tetramethylolmethane is the chainextender of solid state polymerization, helps the increase of limiting viscosity, and this also is known in prior art.So embodiment will pay attention to relating in the technical solution of the present invention description of nucleator partial content.
Embodiment
[embodiment 1～4]
One, esterification process:
Monomers terephthalic acid, ethylene glycol and tetramethylolmethane carry out esterification, and the feed ratio of raw material is controlled to be respectively: with molar ratio computing, and terephthalic acid: ethylene glycol=100: 110～200; In weight ratio, terephthalic acid: tetramethylolmethane=100: 0.01～0.12, tetramethylolmethane content sees Table 1 in concrete data and the flame retardant polyester product.
The adding mode of nano kaoline adds before being chosen in esterification.When raw material pulping mixed before esterification was carried out, the nano kaoline particle of aequum is joined in the esterification feed, nano kaoline particulate median size is 200～500nm.The concrete nano kaoline batch sizes of particles of each embodiment is pressed in the flame retardant polyester product nano kaoline content and is determined that nano kaoline content sees Table 1 in the flame retardant polyester product of each embodiment.
Temperature of reaction is controlled to be 260～280 ℃, and reaction pressure is controlled to be 100～300kPa, and reactant residence time is controlled to be 1.5～4 hours.
Two, precondensation and polycondensation process:
Add reactive flame retardant in the esterification products, in the presence of polycondensation catalyst, carry out prepolymerization reaction and polycondensation successively.Reactive flame retardant is the compound with following structural formula:
Wherein, R
1Be methylene radical, R
2, R
3Be hydroxyethyl.
The add-on of reactive flame retardant is a benchmark with the charging capacity of monomers terephthalic acid, and the weight ratio of terephthalic acid and reactive flame retardant is 100: 2.90～14.60, and flame retardant agent content sees Table 1 in concrete data and the flame retardant polyester product.Reactive flame retardant spent glycol making beating mixes, and adds in the esterification products after being mixed with the slurry that concentration is 20～45wt%.
Prepolymerization reaction and polycondensation are all carried out under negative pressure, and temperature of reaction all is controlled to be 270～285 ℃, and reactant residence time respectively is controlled to be 1～3 hour.The vacuum degree control of prepolymerization reaction is 1.0～2.0kPa, and the vacuum degree control of polycondensation is 0.1～0.2kPa.
Polycondensation catalyst adopts antimony glycol, and consumption is a benchmark with monomers terephthalic acid weight, in antimony ion, is controlled to be 120～300mg/kg.Polycondensation promptly gets the polycondensation product flame retardant polyester product after finishing, and its limiting viscosity is controlled to be 0.60～0.70dl/g.
[embodiment 5～8]
The adding mode of nano kaoline changes into before polycondensation and adding, earlier with nano kaoline particle, reactive flame retardant with the mixing of pulling an oar as the ethylene glycol of solvent, be mixed with the slurry that total concn is 20～45wt%, add reactive system by the oligopolymer pipeline then.All the other are with embodiment 1～4.
[comparative example 1]
Do not add nano kaoline in the reactive system, other is with embodiment 1～4.
[comparative example 2]
Terephthalic acid and ethylene glycol are made normal polyester through esterification, precondensation and polycondensation, and limiting viscosity is controlled to be 0.60～0.70dl/g.
Get flame retardant polyester or normal polyester that embodiment and comparative example make, measure physical index and other main quality index that its reflect heat changes performance, data see Table 2.
Table 1.
Table 2.
T in the table 2
gBe second-order transition temperature; T
mBe fusing point; t
1/2Be the hypocrystalline time.By the data of table 2 as seen, the flame retardant polyester composition of the foregoing description obviously dwindles with the conventional deviation of polyester (comparative example 2) on the heat deflection performance, particularly directly reflects the t of crystallization rate
1/2Very approaching with the data of normal polyester.The flame retardant polyester composition of the foregoing description adopts conventional trevira producing apparatus and technology to make flame retardant polyester industry silk, the adhesion caking phenomenon does not all appear when chip drying crystallization, solid state polymerization, post-treatment such as spinning process and drawing-off process is also highly stable, makes the industrial filament that fiber number is 933dtex/192f.The fabric of making is tested according to GB GB/T 5454-1997, GB/T 5455-1997, and limiting oxygen index(LOI) (LOI) reaches more than 32%, and combustionproperty reaches " difficult combustion " B1 grade standard.
Claims (8)
1. preparation method who makes the flame retardant polyester of industry silk usefulness, this method may further comprise the steps:
1) monomers terephthalic acid, ethylene glycol and tetramethylolmethane carry out esterification, and the feed ratio of raw material is respectively: with molar ratio computing, and terephthalic acid: ethylene glycol=100: 110～200; In weight ratio, terephthalic acid: tetramethylolmethane=100: 0.01～0.12, temperature of reaction are 260～280 ℃, and reaction pressure is 100～300kPa, and reactant residence time is 1.5～4 hours;
2) add reactive flame retardant in the esterification products, carry out prepolymerization reaction and polycondensation successively and obtain the polycondensation product flame retardant polyester in the presence of polycondensation catalyst, reactive flame retardant is the compound with following structural formula:
R in the structural formula
1Be the alkylidene group of C1～C4, R
2And R
3Respectively the do for oneself hydroxyalkyl of H or C2～C4, the add-on of reactive flame retardant is a benchmark with the charging capacity of monomers terephthalic acid, the weight ratio of terephthalic acid and reactive flame retardant is 100: 2.90～14.60, the making beating of reactive flame retardant spent glycol mixes, add in the esterification products after being mixed with the slurry that concentration is 20～45wt%
Prepolymerization reaction and polycondensation are all carried out under negative pressure, temperature of reaction is 270～285 ℃, reactant residence time respectively is 1～3 hour, the vacuum tightness of prepolymerization reaction is 1.0～2.0kPa, the vacuum tightness of polycondensation is 0.1～0.2kPa, the limiting viscosity of polycondensation product is controlled to be 0.60～0.75dl/g
It is characterized in that in reactive system, adding nano kaoline particle as the flame retardant polyester crystallization nucleating agent, nano kaoline particulate median size is 200～600nm, its adding mode is for adding before esterification or adding before prepolymerization reaction, and nano kaoline particulate add-on is counted 0.06～1.0wt% with the content that it finally is present in the polycondensation product.
2. the preparation method of flame retardant polyester according to claim 1 is characterized in that in described nano kaoline particulate median size be 200～500nm.
3. the preparation method of flame retardant polyester according to claim 1 is characterized in that counting 0.2～0.9wt% in described nano kaoline particulate add-on with the content that it finally is present in the polycondensation product.
4. the preparation method of flame retardant polyester according to claim 1 is characterized in that the limiting viscosity of described polycondensation product is controlled to be 0.60～0.70dl/g.
5. according to the preparation method of claim 1,2,3 or 4 described flame retardant polyesters, it is characterized in that described nano kaoline particulate adding mode for to add before esterification, the nano kaoline particle is pulled an oar with the raw material of esterification and is mixed back adding reactive system.
6. according to the preparation method of claim 1,2,3 or 4 described flame retardant polyesters, it is characterized in that before described nano kaoline particulate adding mode is prepolymerization reaction, adding, nano kaoline particle, reactive flame retardant be with the mixing of pulling an oar as the ethylene glycol of solvent, adds reactive system after being mixed with the slurry that total concn is 20～45wt%.
7. the preparation method of flame retardant polyester according to claim 1 is characterized in that described polycondensation catalyst takes from any in antimony glycol, antimony acetate or the antimonous oxide.
8. the preparation method of flame retardant polyester according to claim 7 is characterized in that the consumption of described polycondensation catalyst is a benchmark with monomers terephthalic acid weight, in antimony ion, is 120～300mg/kg.
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| CN101376692B true CN101376692B (en) | 2011-04-06 |
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| CN104119538A (en) * | 2013-04-24 | 2014-10-29 | 东丽纤维研究所（中国）有限公司 | Flame retardant and preparation method thereof, and flame-retardant polyester and application thereof |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1127764A (en) * | 1995-11-21 | 1996-07-31 | 南亚塑胶工业股份有限公司 | Method for modification of colour of flame retardant polyester |
| CN1131164A (en) * | 1995-03-15 | 1996-09-18 | 天津石油化工公司研究所 | Method for preparation of far-infrared ceramic polyester |
| US5955565A (en) * | 1996-12-28 | 1999-09-21 | Eastman Chemical Company | Polyesters from terephthalic acid, 2,2,4,4-tetramethyl-1,3-cyclobutanediol and ethylene glycol |
| JP2006169359A (en) * | 2004-12-15 | 2006-06-29 | Nippon Ester Co Ltd | Flame-retardant polyester for molding and method for producing the same |
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2007
- 2007-08-30 CN CN2007100453783A patent/CN101376692B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1131164A (en) * | 1995-03-15 | 1996-09-18 | 天津石油化工公司研究所 | Method for preparation of far-infrared ceramic polyester |
| CN1127764A (en) * | 1995-11-21 | 1996-07-31 | 南亚塑胶工业股份有限公司 | Method for modification of colour of flame retardant polyester |
| US5955565A (en) * | 1996-12-28 | 1999-09-21 | Eastman Chemical Company | Polyesters from terephthalic acid, 2,2,4,4-tetramethyl-1,3-cyclobutanediol and ethylene glycol |
| JP2006169359A (en) * | 2004-12-15 | 2006-06-29 | Nippon Ester Co Ltd | Flame-retardant polyester for molding and method for producing the same |
Non-Patent Citations (1)
| Title |
|---|
| JP特开2006169359A 2006.06.29 |
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