CA1075848A - New-phosphorus-containing compounds - Google Patents

Abstract

ABSTRACT

Compounds of formula

Description

75841~3 r ilC ~rescn L invcl)tion rclates to ne~ phosphorus-corltainil~cJ
compounds. Mo~e yarticul~lrly, the invention is concerned with n~`J p~losp~lor-ls-co~lt~lini~lcJ cornpound5 W~liC~l S~10W arl exc~ rlt compatibility and heclt stability when aclded to high molecular weight compounds such as polyesters or polyam:ides to produce shaped products, and which are capable of providing a high flame retardancy.
In recent years, emphasis is laid on the necessity for rendering flame-retardant various shaped products including fibers from the s-tandpoint of human impor-tance, and much effort is directed to this purpose. To impart flame retardancy to shaped produc-ts produced from linear polyesters, various pro-posals have been made: for example a process wherein, upon the production of the polymer, a flame retardant substance is added for the purpose of copolymerization or blending; a process wherein, upon the manufacture of shaped products, a flame re-tardant substance is kneaded into the linear polyester; or a process wherein flame retardancy is imparted by after-treating shaped products from -the linear polyester. Among these processes, when industrial value is taken into consideration, the process in which a flame retardant substance is added upon the production of the polyester for the purpose of copolymerization is the most advantageous from the viewpoint that it is easiest and various properties of shaped products obtained are not impaired. For this purpose, various phosphorus compounds have been heretofore used. When phosphorus compounds are added upon the produc-tion of polyesters, it has been common practice to use phosphoric acid esters such as triphenyl phosphate, or phosphonic acids such as benzenephosphonic acid derivatives. ~owever, when using such compounds, there have been various problems: the phonomenon of a catalyst activity loss may occur upon the production of polyesters; ether linkages may be formed to lower the melting point of the resulting polymer or to become a cause of the gellation of the polymer; in addition, because of large dissipating of phosphorus compounds from the polymerization system, it is diffcult to obtain a polymer having excellent flame retardancy; and moreover the environment is polluted by the dissipation phosphorus compounds.
To solve such problems, we made a research for suitable ~0 phosphorus compounds. As a result, we have found that, by using the later-mentioned phosphonic acid derivatives having a particular structure, linear polyesters can be produced without any substantial problem in the same way as in the polymerization of the usual polyesters, and that the polyesters thus obtained . - . . .

~(~758~8 have a v~ry sn~ mount o~ ether ]inkacle and have an e~cellent flame r~tar(lancy (Japarlese Patent 95~,~90). The above-mentioned phosphorlic acid derivatives have a structure shown by the EolLowing ger~eral Eormula (II):
O
(RiO)2-P - C~ - C~ICOOR2 (II) ~ I D ~
'`3 '`~
wherein R~ and R2 are each a monovalent hydrocarbon group having 1-18 carbon atoms; and R3 and R4 are each a hydrogen atom or a hydrocarbon group having 1-4 carbon atoms.
However, when the phosphonic acid derivatives represented by the general ~ormula (I~) are added upon the production of flame retardant polyesters, there is a possibility of causing a cross-linking reaction because the phosphonic acid derivatives are trifunctional compounds, and there~ore it is inevitable that cross-linked portions may be mixed in the resulting product. Therefore, when such flame retardant polyesters are melt-shaped into products such as fibers or films, there is a tendency that the physical properties of the shaped products may be lowered or the operation efficiency may be lowered.
To improve such a situation, we further made a research for phosphorus compounds which will provide excellent flame ~- retardant p~lyesters~ a~d which hav~ no cross-linking.actio~.
As a result, we have found very suitable compounds. This finding led to the accomplishment of the present invention.
The above-mentioned compounds are new phosphorus-containing compounds represented by the following general formula tI):

(R )n2 ~ P-A-(R )nl ~I~
(R )n3 ~
wherein R is an ester-forming functional group selected from the class consisting of -COOR , -oR5 and -OCOR6 wherein R4 is a hydrogen atom, a carbonyl group or a hydrocarbon group having 1-10 carbon àtoms which may contain a hydroxyl group or a carboxyl group and R5 is a hydrogen atom or a hydrocarbon group having 1-10 carbon atoms which may contain a hydroxyl group or a carboxyl group and R6 is a hydrocarhon group having 1-10 carbon atoms which may contain a hydroxyl group or a carboxyl group; R2 and R3 are the same or different groups and are selected from halogen atoms, hydrocarbon groups having 1-10 carbon atoms and Rl, respectively; A is a divalent or trivalent '. ~ ' : ' .

3L~75~
h~clrocarl~or- cJro~lp ~ virlcJ l-~ carbon a~oms; nl is an integer o~ 1 or 2, n2 a~d ~13 are eclcll an interger of 0-4.
Concret~ examples of producin~ the phosphorus-con-taining compounds of the present inven-tion will be described herein-after, but said compounds can be produced, Eor ex~mple, by the processes shown in the following: they can be produced by reacting 9,10-dihydro-9-oxa-10-phosphaphenanthrene-10-oxide (hereinafter referred to as DOP) or its benzene nucleus substituted compound thereof with an unsaturated compound having an ester-forming functional group, or by esterifying with a diol or a dicarboxylic acid at the same time with or after the above-mentioned reaction. As regards the above-mentioned unsaturated compound, it is preferable to select it from dicarboxylic acids such as maleic acid, fumaric acid, itaconic acid, acrylica acid, methacrylica acid, mesaconic acid, citraconic acid, glutàconic acid, etc. or their anhydrides and esters, but oxy-carboxylic acids such as brantenolic acid or unsaturated glycols such as 2-butene-1,4-diol and 3-butene-1,2-diol may be used. As the particularly preferred unsaturated compounds in the present invention, itaconic acid or lower alkyl esters or the anhydride of itaconic acid may be mentioned.
The above-mentioned DOP or its benzene nucleus substituted com~ounds can be svnthesized from 2-hydroxybiphen~vl or its nucleus substituted compounds and phosphorus trichloride, as shown in Japanese Patent No. 784,757 issued to Sanko Kagaku K.K. ~b produce the phosphorus-containing compounds of the present invention, it is particularly preferable to use the compound having no substituent group at the benzene nuclei, namely the compound of the formula (I) wherein n2 and n3 are both O
(i.e. DOP). In the reaction of DOP o~ its benzene nucleus substituted compound thereof with the above-mentioned un-saturated compound, it is preferable to react them so that the molar ratio of the former to the latter is nearly 1 : 1, but it is also possible to use any one of them in some excess.
As an example of the processes for producing the phosphorus-containing compounds of the present invention, a concrete explanation is given for the case of using DOP and dimethyl itaconat`e as the starting compounds: after the starting compounds are mixed at room temperature, the mixture is heated ~0 under stirring at a temperature above 100C., preferably between 120 and 200C. under an iner~ gas atmosphere, whereby the object substance can be produced. Cases are most frequently met with where the use of a metal alkoxide such as sodium methoxide, sodium ethoxide, potassium ethoxide, etc. as the . . .
-, .

catalys~, is ~dv~nt~cJeous ~or :increasing the reaction speed.
In order to suppress any side-reaction, a lower alcohol such as me-thanol, ethanol, isopropallol, n-butanol, etc. may be present in the reaction system.
In concrete examples of the new phosphorus-con-taining compounds of the presen-t inven-tion, R in the general formula (I) is a carboxyl group, an alkyl ester of a carboxyl group having 1-7 carbon atoms, cycloal~yl ester, aryl ester, hydroxyl group, hydroxyalkoxycarbonyl group having 1-7 carbon atoms or a group represented by -C-O-C-; and nl is preEerably 2. When nl ,. .
O O
is 2, R may be the same or different groups. As regards R
and R3, a halogen atom such as chlorine atom, bromine a-toms, an alkyl group having 1-6 carbon atoms, a cycloalkyl group, an aryl group and the above-mentioned monovalent groups of Rl may be mentioned as preferred ones. As the preferred examples of A, there may be mentioned lower alkylene groups such as methylene, ethylene, 1,2-propylene, 1,3-propylene, etc.; arylene groups such as 1,3-phenylene, 1,4-phenylene, etc.; divalent groups having arylene such as 1,3-xylylene, 1,4-xylylene, -CH2- ~ -, etc.; a trivalent group represented by -CH2-C ( CH2 ~~n4 (wherein R8 stands for a hydrogen atom, or a lower alkyl group such as methyl, ethyl, etc., and n4 stands for O or 1) and --CH2- ~ . The above-mentioned hydrocarbon groups may be substituted by a halogen atom such as chlorine atom, bromine atom, etc. As for A, a trivalent group is preferable.
Among the concrete examples of the phosphorus compounds represented by the above-mentioned general formula (I), the following compounds may be mentioned:

~, ~ " 2 2 OOH (a) l l O
- ~

~ 7 ~ P-cH2cH2-coocH3 (b) . , ~
_4--. .

.: . . ' .

.'. . , . ' ' .

~075848 ~
~P-C112C~12COOC2EI5 (c) ~,0 ~3~P-CH2CH2COOCH3 (d) ~r ~

[~ P-CH2CH2COOC2H5 (e) ' - ', : ~.

Cl~Cl ~-CH2CH--COOH (f ) ~ O CH2COOH

Br ~Br :

P - cH2cH-coocH3 ~g) ~: ;

;
~3~ P-CH-CEI2COOH (h) ' ' 1075B4~

[~0, C113 ' [~P-CII-C112COOC113 (i) ~0 ~, p-cH2cH2coocH2cH2o}l ( j Br~ Br , 2 ,C~I CoocH2cH2cH2oH (k) Br P-CH--CH2coocH2cH2oH (1) \0 ~P-CH2cH 20H (m) ~0 CI13 ~P-CH-CH20H . ~n) .

..... . . . . .
.' 1~:)758~8 ~o ~,P Cll-COOC~13 (o) ~¦ O C H 2COoC11 3 (~,0 P-CH-COOC2H5 (P) ~0 ~.
O CH2 C~o O
1~ ~P-CH-COOCH3 (r) ~ O CH2--COOII
;

~ '.
. ~0 G ~ ~P-CH2CHCOOH (s) g3~ ' O
- ~P-CH 2CHCOOCH 3 ( t ) ~ O CH2COOC1~13 `!

" . ,, " ' --.7--;.. - . . . .
, . . , , , , ~ .
,. . . .

;, :: . , ..:

89~13 r cOOc2ll5 ~ P C112CII (u) P-CII 2CH- C ~o ( v ) ~0 ~ P CH2--~-CH20H (w) ~ - ' . .
H2cH2oH (x) .
~ . .
~ 0 ~ ~ OCH2CCH2--~}CH2H
,~
.
~ P-CH-CH20H ( z ~

' ;. : ' : . ' , ' ' .:

S~3~8 sy polyconde~sin(J ~ phospllorus-collt~:ining compound of the present invention wi-th a dihy~lric alcohol, a dihydric phenol or a divalent amine, or by copolycondensinc3 a phosphorus-containing compound of the present invention with a dihydric alcohol, a dihydric phenol, a divalent amine or/and ano-ther dicarboxylic acid or a derivative thereof, it is possible to easily produce a phosphorus-containing high molecular weight compound such as polyester, polyamide, polyure-thane, polyether, etc.
Furthermore, it is possible to utilize the phosphorus-containing compounds as flame re-tardants for various high molecular weight compounds. Namely, the above-mentioned phos-phorus-containing flame retardants are obtained by reacting at least one kind of unsaturated compound containing at least one ester-forming functional group, DOP or its benzene nucleus substituted compound thereof, and at least one kind of the ester-forming compounds selected from dicarboxylic acids or their ester-forming derivatives, diols or their ester-forming deriva-tives, and oxycarboxylic acids or their ester-forming derivatives. Upon producing the above-mentioned phosphorus-containing flame retardants, it is particularly preferable inthe present inven-tion to employ the process wherein a phosphorus-containing compound is first produced by reacting the above- ;
mentioned unsaturated compound with DOP or a benzene nucleus substituted derivative thereof and then the phosphorus-containing compound is reacted with at least one kind of the above-mentioned ester-forming compounds to obtain the intended flame retardant.
Especially when the flame retardant is applied to polyesters, after the unsaturated compound containing ester-forming groups and DOP are dissolved in a diol, it is convenient to add the resulting solution directly to the polyester polymerization process.
The above-mentioned ester-forming compound is suitably selected from the dicarboxylic acid component, diol component and oxycarboxylic acid component used upon the production of the polyester. Namely as the dicarboxylic acids or their ester-forming derivatives used for the produc-tion of the flame retardants, there may be used any of the ester-forming deriva-tives such as aromatic dicarboxylic acids, aliphatic dicarboxylic acids, alicyclic dicarboxylic acids or their alkyl ~0 esters.
Upon producing the flame retardants of the present invention by reacting an ester-forming compound as mentioned above, it is desirable to adjust the amount of use of each starting material so that the phosphorus content in the resulting ~: . , . , ~ . :

~o~s~
flam~ r~tardant should ~e above 2,000 ppm, pre~erably wi.thin the range of 5,000 to 90,000 ppm. This is because, if the phosphorus content is lower than 2,000 ppm, the fl~me retard-anc~ impartinc~ power of the resul-ting flame retardant is undesirably lowered. Vice versa, if the phosphorus content in the flame retardant is too high, it is impossible to ob-tain a satisEactor~ produc-t even by the process which will be described hereinafter.
The processes for producing the flame re-tardants of the present invention are not particularly limited except that the pllosphorus-containing compound and the ester-forming compound are used so that the phosphorus content in -the resulting flame retardant should be within the above-mentioned range. However, the flame re-tardants can be produced as described hereinafter, for example.
Namely, in the presen-t invention, it is desirable to select such a phosphorus-containing compound that R in said compound is a carboxyl group, carboxylate group, or in the form of acid anhydride. When usin~ a phosphorus compound whose Rl is a carboxylate group, it is necessary to produce the object flame retardant by using a diol as the ester-forming compound, namely by the so-called transesterification reaction. As the conditions for this transesterification reaction, it is possible to employ conditions nearly in accordance with the conditions under which aromatic polyesters are produced. Namely, the object flame retardant can be produced by heating the reaction mixture under reflux within the temperature range of from about 50 to 280C. under atmospheric pressure in the presence of a compound of metals selected from zinc, manganese, titanium, cobaltJ magnesium, etc. as the catalyst for the transesterification reaction.
Where the phosphorus-containing compound is in the form of free acid or anhydride, it is possible to produce the flame retardants of the present invention by using a diol as the ester-forming compound and in ac~ordance with the so-called : direct es-terification used upon producing aromatic polyesters.
Namely, -the object substance can be produced by heating the reaction mixture within the temperature range of from about 100C. to about 280C. under atmospheric pressure or under an increased pressure up to 5 kg/cm2 in the presence of a same ~etal compound as in the case of the above-mentioned trans-esterification reaction or a tin compound, as the esterifica-: tion catalyst. Either in the case of this method or in the case of the above-mentioned-transesterification reaction, when .

'.

1~7S8~

thc reaction system is brought to a somewhat higher tempera~
tur~ and a reduced pressure at the last stage of the reaction, the resulting fl~me retardant can have a higher sof-tening point, so that -the compa-tibility of this flame retardant with high molecular weight compounds is improved and thus this procedure is very useEul. ~ven flame retardan-ts having a softening point of 30~C. can have a suf-Eicient utility, but ~those having a softening poin-t higher than 70~C. are easier in handling.
The flame retardants of the present invention may be produced by other processes, but said flame retardants can be produced more easily by the above-mentioned processes, and the physical properties of the flame retardants so produced are very satisfactory.
The flame retardants of the present invention thus produced not only can provide excellent flame retardancy to high molecular weight polymers such as polyamides~ poly-olefins, polystyrenes, polyacrylonitriles and polyesters, but - in addition, when mixed particularly with polyesters to produce shaped products, they have no action of lowering the degree of polymerization of the polyesters, so that it is extremely rare that they exert adverse effects on the physical properties and color of the resulting polyester shaped products.
The flame retardants of the present invention have very good compatibility with polyesters, presumably because they have an analogous chemical structure to the fundamental skeleton of polyesters. Therefore-, they can be used for producing various excellent flame retardan-t shaped products by mixing with polyesters by a simple operation.
As mentioned earlier, the phosphorus-containing compounds and phosphorus-containing flame retardants of the present invention are very useful for producing flame retardant poly-esters having excellent properties by mixing them with polyesters. Especially, even at high temperatures of the production system of polyesters, the phosphorus-containing compounds of the present invention cause no substantial heat decomposition or gellation, so that the resulting flame retardant polyesters have an excellent color tone. Also, the mechanical properties thereof are so good that there is no perceivable difference from the properties of those produced without using the phosphorus-containing compounds of the present invention. When flame retardant polyesters are produced using the phosphorus-containing compounds of the ;:
' ;~

~()7~84~3 present invention, :it is desirable that the content of phos-phorus atoms in -the resul-tincJ polyes-ter should be 500 to 50000 ppm, ancl particularly in the case o~ polyesters for producing fibers, it is preferable -to use the phosphorus-con-taining compouncl in such a manner that the phosphorus atom content should be 1,000 to 10,000 ppm.
Where the amount of use of the above-mentioned phosphorus compounds is smaller than the above-mentioned range, it becomes difficult to obtain polyesters having the desired flame retardancy. Vice versa, where the amount of use is larger than tha-t range, not only the physical properties of the resulting polyes-ter are impaired, but also the production efficiency upon producing the polyester is lowered. There-fore such amounts of use are not desirable.
Upon producing flame retardant polyesters in the present invention, the method of adding the above-mentioned phospho-rus-containing compounds to the polyester production system is no-t particularly limited. Namely, for example, when polyesters are produced by the so-called transesterification process of dicarboxylic acid diester and diol, the above-mentioned phosphorus-containing compounds or phosphorus~
containing flame retardants may be added upon the transester-ification reaction, or they may be added before the polycon-densation reaction after the transes-teriication reaction, or at a relatively early stage of the polycondensation reaction.
Also, upon producing polyesters by the so-called esterification process of dicarboxylic acid and diol, they may be added at any stage of esterification. In the present invention, it is desirable to add the above-men-tioned phosphorus-containing compounds to the reaction system as a solution or a dispersion in a monohydric alcohol such as methanol, ethanol, etc. or in a dihydric alcohol such as ethylene glycol, propylene glycol, butan diol, etc.
Also, it is possible -to prepare polyester master pellets c~ntaining more than about 2,000 ppm of the phosphorus-containing flame retardant and mix them with the ordinary pellets to supply the mixture to the shaping step.
Among -the clicarboxylic acids used for the production of flame retardants or flame retardant polyes-ters, the aromatic dicarboxylic acids include for example terephthalic acid, isophthalic acid, 1,4-naph-thalenedicarboxylic acid, 2,6-naph-thalenedicarboxylic acid, 1,2-bis(4-carboxyphenoxy) ethane, which are particularly preferred ones, and in addition, tetra-bromoterephthalic acid, 2,2- bis (4-carboxyphenyl) propane, -- 1(1175848 ~is(~-cclr~o,:yp~ny~ orlc, bls~-cclrboxypherlyl)ethe~r,

2,2-bis(3,5-dibrolno-~-carboxyphcnyl)propane, 4,4'~dicarboxy-phenylbiphe~lyl, and sod:ium 3,5-dicarboxyben~enesulfonate.
Amon~ other dicarboxylic acids, there may be mentioned aliph~tic or alicyclic dicarboxylic acids such as adipic acid, suberic acid, azelaic acid, sebacic acid, hexahydro-terephthalic acid, etc. or their mix-tures.
On the other hand, among the cliol compounds, there may be mentioned ethylene glycol, 1,2-propylene glycol, trimethylene glycol, bu-tan diol, neopentylene glycol, 1,4-cyclohexane diol, 1,4-cyclohexane dimethanol, diethylene glycol and polyethylene glycol. When the diols representecl by the following general formulae are used as copolymerization components, the flame retardancy of the resulting polyester becomes more excellent.

HOCH2CH20 ~ Y ~ OCH2CH20H
(X)m (X)m HCH2CH2 ~ 2 2 (X)m wherein X represents a halo~en atom, Y represents an alkylidene group, cycloalkylidene group, arylalkylidene group, -S-, -SO-, -SO2- or -O-, and _ represents an integer of 1-4.
Also, the carbonate of the above-mentioned glycols or ethylene oxide, propylene oxide, etc. may be used.
Among the oxycarboxylic acid or its ester-forming derivative components, there may be mentioned for example 4-oxybenzoic acid, 4-hydroxyethoxybenzoic acid, oxypivalic acid and -their alkyl esters.
In the present invention, the flame retardant polyesters are produced from the above-mentioned dicarboxylic acid components, diol components and the phosphorus compounds represented by the general formula ~I), or from oxycarboxylic acid components and the phosphorus compounds represented by the general formula (I), but the conditions for the production of polyesters, for example the conditions of transesterification or esterification and polycondensation can be in accordance with the conventional known process. For example, in the case-of producing the flame retardan-t polyesters of the present invention using tereph-thalic acid as the dicarboxylic acid component and ethylene glycol as the diol component, the transesterificatio reaction is carried ou-t a-t 150-240C. using, as the catalyst, a conven-tional alkali metal, alkali-earth metal, or a compound -~3-:,, , .~ :, .
, .. . . .

` 1~7SI~

o~ metals suc~ s 7.inc~ man{Jallese, co~aLt, t;tar~ium, etc., and on the other hancl, tlle esterification reaction is carried out, usincJ as the~ catalyst nearLy the same rne-ta~ cornpounds as used in the transesteriEication reaction, at a pressure from a-t-mospheric pressure to 5 kg/cm2-G and a-t a temperature between 200 and 280~C., to obtain the object reac-tion product, which is then polycondensed under a high vacuum below 1 mm ~Ig a-t a temperature between 250 and 320C. in the presence of a compound of metals such as an-timony, german:ium, titanium, e-tc. -to obtain the object polyes-ter. ThereEore, one of the greatest features of the presen-t invention is that polyesters havinc3 excellent flame retardancy can be produced by followiny the conventional known process nearly in every respect.
When the flame re-tardant polyes-ters are produced in the present invention~ the phosphorus compounds represented by the above-mentioned general formula (I) are ex-tremely s-table against heat in comparison with the usually used phosphorus compounds, presumably because, in the phosphorus compounds represen-ted by the formula (I), the phosphorus atom constitutes a ring member.
Therefore, since no substantial side-reaction occurs such as gellation reac-tion resulting from -the heat decomposition of the phosphorus compound upon the polycondensation reaction, the polyesters obtained by the process of the present invention are excellent in color tone, and have better physical proper-ties ; than conventional flame retardant polyesters. Accordingly, it is possible to produce shaped flame retardant produc-ts having excellent properties from -the polyesters in question.
When the phosphorus compound represented by the above-mentioned general formula (I) has only one ester-forming functional group, this phosphorus compound can act as a terminal stopper, so that cases may occur where the use in combination with a known polyfunctional compound for example pentaerythritol or a trifunctional carboxylic acid is preferable.
It does not depart from the spirit of the present invention to use the usual additives, for example the so-called ether linkage inhibitor such as organic amines and organic carbonic acid amides; pigments such as titanium oxide and carboxylic black; stabilizers, plasticizers, antistatic agents, etc. upon producing the flame retardan-t polyesters according to the ~0 present invention.
~ s mentioned above, the flame retardant polyesters obtained according to the present invention have various excellent properties in addition to flame retardancy, so that they are used not only for fibers but also for ~ilms, boards and other - 107S8~8 s~lap~cl ~2-~luc ts.
The ~rcsent invention wil:L be rnore concrctely exp]ained with refer~llce to examples of the preparation of the phosphorus-containing compounds and phosphorus-containing flame retardants, and to examples of the production of flame re-tardant polyes-ters.
In these examples, -th~ parts and percentages are by weight. The in-trinsic viscosity was obtained from the values measured in a mixed solvent of phenol and 1,1,2,2--tetrachloroethane (weigh-t ra-tio 3 : 2) at 30C. The phosphorus conten-t was measured colorimetrically after the sample was heat-decomposed with sulfuric acid, nitric acid and perchloric acid and color-developed with ammonium molybda-te and hydrazinium sulfate. The content of trivalent phosphorus was measured by iodometry after the sample was dissolved in isopropyl alcahol. The refractive index was measured by means of an Abbe's refractometer at 30C.
The viscosity was measured with a Brookfield viscosimeter at 30C. The acid value was measured by titrating an ethyl alcohol solution of the sample with an aqueous 1/10 N sodium hydroxide solution in the presence of a phenolphthalein solution as the indicator. As for the measurement of the saponification value, the sample was saponified with a 1/2 N potassium hydroxide/95~
ethyl alcohol solution at 75C. for 60 minutes and the saponified solution was titrated with a 1/2 N hydrochloric acid solution in the presence of a phenolphthale in solution as the indicator.
The infrared absorption spec-trum was measured from a potassium bromide plate on which the sample was spreaded. The nucleus magnetic resonance absorption spectrum (hereinafter abbreviated as NMR) was measured from a solution of the sample in 10 weight %
heavy-hydrogenated chloroform by means of a Varian A-60 apparatus (60 M Hz; produced by Varian Co.) under the conditions of a filter width of 1 cycle/sec., a sweep time of 250 seconds and a sweep wid-th of 500 cycles/sec., at 70C. with TMS as the inner standard. As for the high-speed liquid chromatograph, a Waters*High-Speed Chromatographic Apparatus (Waters Co.) was used with Microbondapack C-18 as the packing agent and methyl - alcohol as the liquid phase (at the rate of 1 ml/min.), and an ultraviolet absorption detector was used for the detection. The flame retardancy was measured as follows: Yarns obtained by spinning and drawing a polyes-ter in the usual way were knitted 40- into a tricot cloth. One gram of the tricot was rounded in a length oE 10 cm and was inserted into a wire coil having a diameter of 10 mm. While the tricot in the wire coil was held at the angle of 45, it was ignited at the lower end. When the ~ ~r~e rq~ks -15-. , 58~

firc clicd out ~y ~erlloving th~ f:ire sourc~, the ignition was repeated. Thc number o~ -the ignition r~qulred for burning down the whole sampl~ completely was obtained Eor five samples. The flame retardarlcy was expressed by the average number of the ignition.
Preparation 1 Into a four-necked flask equipped with a stirrer, a reflux condenser, a thermome-ter and a dropping funnel, 503 g. 9,10 dihydro-9-oxa-10-phosphaphenanthrene-10-oxide (DOP), 200 g. me-thyl acrylate and 440 g. methyl alcohol were charged. With the flask held on a water bath maintained at 35C., a 1 N methyl alcohol solution of sodium methoxide was added dropwise from the dropping funnel. While taking care so thatthe temperature of the reaction system did not exceed 65C., 35 g. of the above-mentioned me-thyl alcohol solution was added dropwise in 10 minutes. The thus-obtained solu-tion was slightly brown. It was confirmed from iodometric analysis that the reaction rate of DOP was 99.3%, and from gas chromatographic analysis that the reaction rate of methyl acrylate was 98.9~.
The solution was heated to 100C. at a reduced pressure below 1 mm Hg for 2 hours to remove volatile matter including methanol. The residue at room temperature was a slightly brown viscous li~uid (A), and the remaining ratio of the residue was ; 59.8%. Its refractive index ~nD) was 1.6071. By distilling a part of the liquid (A) at 220C. under 0.2 mm Hg, the main fraction was obtained, which had a reEractive index of 1.6068.
From the analysis by infrared absorption spectrum and NMR, it was found that this main fraction had the following structure.
The values obtained by the elemental analysis of this main ` 30 fraction were: P=10.20%, C=63.62% and H=5.01% which coincided well with the theoretical values: P=10~25%, C=63.57% and H=5.00%.
; ~ : ' ~P-cH2cH2cOOCH3 I 1~ o ~ .
Preparation_2 508 g. of DOP, 372 g. of dimethyl itaconate and 390 g. of methyl alcohol were charged into the four-necked flask as used in Preparation 1. In the same way as in Preparation 1, 33 g.
of a lN methyl alcohol solution of sodium methoxide was added dropwise in 10 minutes, whereby the reaction was made to proceed.
The solution thus ob-tained was slightly brown. From the . .

iLO'7~8'~
-analysiL; by io(lollletry, it was conEirmed that the reaction rate of dimethyl itaconate was 98.8'~.
This solution was removed Erom volatile ma-tter by heating at 100~C. uncler a recl~lcecl pressure below 1 mm ~Ig for 2 hours.
The residue was a glassy semi-solid (s) at room temperature and the remaining ratio was 66.7~. The acid value of the semi-solid (~) was 0 meq/kg and the phosphorus content by elemental analysis was 8.24%. By recrystallizing the semi-solid (B) from ethylene qlycol, a white solid (B) having a melting point of 88.1C. was obtained.
The infrared spectrum of this white solid (B) had maximum absorption values at 3060, 3000, 2945, 1740, 1600, 1480, 1~40, 1375, 1280, 1260, 1240, 1210, 1200, 1170, 1120, 914, 760, 720, 620, 600, and 530 cm 1, respectively. The~ values by NMR
measured in CDC13 at 60C. were 2.0-3.0, 6.4-6.5, and 7.0-8Ø
The values of elemental analysis were: P=8.28~, C=61.03~ and H=5.14~, which coincided well with the theoretical values P=8.27~, C=60.98~ and H=5.12% of the following structure.
.~ . ' .
, ~ -CH2CHCOOCH3 ~ CH2COOCH3 The acid value of the solid (B) was 0.00 meq/kg and the saponification value was 7.99 eq/kg (theoretical value:
8.01 eq/kg).
Preparation 3 - 497 g. DOP, and 400 g. dimethyl itaconate were charged into a four-necked flask equipped with a stirrer, a reflux condenser, a thermometer and a nitrogen inlet tube. While the flask was held on an oil bath maintained at 150C.j the ;~
reaction mixture was allowed to react under stirring for 4 hours under a ni~rogen atmosphere. Therea~-ter, unreacted dimethyl itaconate was distilled at 150C., and under a reduced pressure below 1 mm Hg spending 2 hours. The thus-obtained substance at room lemperature was a colorless transparent semi-solid (C) having a boiling point of 235 - 237C./0.08 mm Hg. It was found that the remaining ratio of unreacted DOP was 0.5~, from iodometric analys:is, and the phosphorus content by elemental analysis was 8.26-~ and the acid value was 4 meq/kg. After the recrystallization of the semi-solid (C) from ethylene glycol, a white solid (C) having a melting poin-t of 88.2C. was obtained.

~0~58~
It was con~irmed that this solid (~) WclS a compound having the following s~ructure rom l-he analysis by infrarcd absorption spectrum and NMR spectrum. The phosphorus content by elementa]
analysis was 8.29~ which coincided well with the theoretical value of 8.27~.

o ~ " 2, 3 .. ~ O CH2COOCH3 Preparation 4 540 g. DOP and 316 g. itaconic acid were charged into the four-necked flask as used in Preparation 3, and the reaction mixture was reacted in the same way as in Preparation 3, and then the volatile matter was distilled off. The thus-obtained substance was a colorless transparent solid (D) having a melting poin-t of 86C. It was confirmed from the analysis by iodometry tha-t the remaining ratio of unreacted DOP was 0.7%, and from elemental analysis, that the phosphorus content was 8.93-Q. sy recrystallizing the solid (D) from dioxane, a white solid having a melting point of 189.4C. was obtained. The infrared spectrum of this solid had a maximum absorption at 1712 cm 1 which was due to ~ c=0 of carboxylic acids. NMR
showed absorption at a ~value of 7.0-7.3 due to H of -P-CH2-. -The values of the elemental analysis were: P=8.95%, C=58.88 and H=4.39%, which coincided well with the values P=8.94%, C=58.96~ and H=4.37~ of the following structure:

[~0 ~P-CH2CHCOOH
I ~ J CH2COOH

Preparation 5 346 g. of the solid (D) produced in Preparation 4 and 346 g. ethylene glycol were charged into a four-necked flask equipped with a stirrer, a thermometer, a nitrogen inlet tube and a distillation apparatus. With the flask held on an oil bath maintained at 200C., the reaction mixture was reacted under a nitrogen atomsphere for 4 hours while the water formed was distilled off with ethylene glycol. A total of a 65 g.
solution containing 36 g. water and 29 g. ethylene glycol was .. , . .. .. . . .. - -'' ~

1~5~
fil~ally di~.Lil lecl out. 'I`~le ~ s-o~tairled solution was a colorless transpclrellt visco-ls liquid (1:) at room temperat-lre which had the str~lctul-e cle~scr:ibed hereinaEter. The phosphorus content by elemental analysls oE the liquid (E) was 5.11~.
The content of trivalent phosphorl-ls by iodometry was 0.01~, the refractive index ].5362, the viscosi-ty 2~.0 poises, the acid value 0.09 eq/kg, and the saponifica-tion value 4.77 e~/kg.
The ethylene glycol esterifica-tion ra-tio of the carboxylic acid calculated from these values were 98~. The infrared absorption spectrum had a maximum absorp-tion at 1740 cm 1 due to Vc=0 of carboxylic acid esters. NMR showed an absorption at the~ value of 7.0-7.3 due to H of -P-CH2-.
30 par-ts of the liquid (E) thus-obtained was dissolved in 2 liter cold water. The solution was fil-tered to remove un-dissolved viscous liquid. The thus-obtained aqueous solution was charged into a separating funnel and extracted wi-th 50 ml chloroform three times. The chloroform solution was washed with 50 ml water 3 -times. The thus-obtained chloroform solution was put into a round bottom flask and the volatile matter was distilled off with an evaporator at 60C. under a reduced pressure of 0.1 mm Hg finally. The content thus obtained was a colorless, transparent, highly viscous liquid at room temperature. This liquid is named liquid (e).
` The phosphorus content of this liquid (e) was 7.12%; the trivalent phosphorus content 0.00~; the elemental analysis values C=58.02r H=5.33~; the acid value 0.00 eq/kg; the saponification value 6.88 eq/kg; and the esterification value was 100%. The infrared spectrum had a maximum absorption at 1740 cm 1 due to ~c=0 of carboxylic acid esters. NMR had 30 absorption at the~ values of 1.8-2.8; 5.6-6.0; 6.0-6.2;
6.2-6.5; 6.5-7.0; 7.0-7.3 and 7.3-7.8 due to H of nucleus, -COOCH2-, OH, -CH2O-, ~CH-, P-CH2- and -CH2-, ; respectively, and the absorption ratio of these was 8:4:2:4:
1:2:2. As regards the high-speed liquid chromatograph, only a single peak was observed after 180 seconds. From these analytical values, it was found that the liquid (e) is 10-~2,3-di(2-hydroxyethoxy)carbonylpropyl) -9~10-dihydro-9-oxa-- 10-phosphapenanthrene-10-oxide having the following structure:
~

¦ , 2 2 2 ~p-cH2cHcoocH2cH2oH
.' ~ ' .

.

. ,.~ .

iO7S~
Pre@aration 6 216 g,DOP, ].30 g. itaconic acid ancl 3~6 g. ethy].erle glycol were char~ed into a four-neckcd flask as used in Preparation 5.
With the flask hcld on an oil bath maintained at 160C., the reac-tion mixture was allowed to react for 2 hours under a nitrogen atmosphere while the water formed was distilled out with ethylene glycol, and Einally a 33 g. solution in total containing 30 g. water and 3 g. ethylene glycol was dis-tilled out. The thus-obtained solution was a colorless, transparent, viscous liquid (F) at room temperature. The phosphorus content of this liquid (F) was 4.506, the trivalent phosphorus content : 0.04%, the refractive index 1.5227, the viscosity 9.7 poises, the acid value 0.17 eq/kg and the saponification value was 4.42 eq/kg. The ethylene glycol es-terification ratio of the carboxylic acid calculated from these values was 95%. The infrared absorption spectrum had a maximum absorption at 1740 cm 1, and NMR had an absorp-tion at the ~C value of 7.0-7.3.
30 par-ts of the liquid (F) thus-obtained was extracted with chloroform, washed with water and dried in the same way as in Preparation 5, whereby a liquid was obtained which was colorless, transparent and highly viscous at room temperature. This liquid is named (f). The phosphorus content of this liquid (f) was 7.15%, the trivalent phosphorus content 0.00~, the elemental analysis values C=58.09~ and H=5.27~, the acid value 0.00 eq/kg, the saponification value 692 eq/kg and the esterification ratio 100%. The infrared spectrum had a maximum absorption at 1740 cm 1. The NMR had absorption at the~C values of 1.8-2.9, 5.6-6.0, 6.0-6.2, 6.2-6.5, 6.5-7.0, 7.0-7.3 and 7.3-7.8, and their absorption ratio was 8:4:2:4:1:2:2. As regards the high speed liquid chromatograph, only a single peak was observed after 180 seconds. From these analytical values, it was found that the liquid (f) was a compound having the same structure as that of the liquid (e) obtained in Preparation 5.
Preparation 7 54 parts of DOP and 28 parts of commercial itaconic acid :
al~hydride were put into a reaction vessel. After nitrogen replacement under reduced pressure, the reaction vessel was immersed into an oil bath of 150C., and the reaction mixture was allowed to react by heating for 240 minutes under stirring.
The reaction product was a viscous liquid, which when removed and cooled became a colorless, transparent, glassy solid having a softening point of 84-88C. Upon recrystallizing this substance from tetrahydrofuran/hexane ~1 : 1), 72 parts of the object compound having the following structure:

:: .

~S8~8 ~, O C112-CO~
-C~I2C~-CO
~ o The purified product thus-ob-tained was white needle-like crystals having a meltin~ point of 187.4C. The inErared spectrum of the crystals had a maximum absorption value at 2940, 1788, 1600, 1480, 1438, 1235, 1120, 1068, 914, 760, 720!
620 and 530 cm , respectively. The elemental analysis values were P=9.42~, C=62.29% and H=4.14~, which showed a good coincide~ce with the theoretical values: P-9.44%, C=62.20~ and H=3.99~.
Preparation 8 32.8 parts of the previously mentioned phosphorus compound (q) represented by the formula below, 31.0 parts of ethylene ~ , glycol and 0.04 part of potassium titanyl oxalate were supplied to an autoclave equipped with pressure and temperature regulating means. The reaction mixture was allowed to react under a nitrogen atomsphere in a temperature range of ~rom 200 to 220C for 120 minutes under stirring. The pressure of the reaction system was then gradually reduced to 1 mm Hg in 60 minutes. Subsequently, the reaction mixture was reacted for 120 minutes at a temperature of 220C. under a pressure ~elow 1 mm Hg. The resulting product was a yellow solid having a softening point of 75C. Its phosphorus content was 8.30%.
~ .
..
~f'~
CH 2 ICH C o ( q Preparation 9 35.8 parts o~ 9,10-dihydro-10-(1,2-dicarboxy)ethyl-9-ox-a-10-phosphaphenanthrene-10-oxide, 31 parts of ethylene glycol and 0.04 part of potassium titanyl oxalate were supplied to the same autoclave as used in Preparation 8. ~he reaction mixture was allowed to react under a nitrogen atmosphere in a tempera-ture range o~ from 160 to 240C. for 120 minutes under stirrin~. The pressure of the reaction system was then gradually reduced to 1 mm Hg in 60 minutes. Subsequently, the reaction mixture was reacted at 240C. under a pressure o~

, .~.. . -:; , - 1~7S1~

1 mm ~IC3 for 60 ~inutes. The resultiny product was a yellow solid having a softenincJ point of about 30C. Its phosphorus content was 8.90~o.
Preparation 10 ~ mixture of 18.7 g. of 9,10-dihydro-10-(2,3-dimethoxy-carbonyl)propyl-9-oxa-10-phosphaphenanthrene-10-oxide, 14.~
parts of l,~-cyclohexane dimethanol and 0.02 part of ammonium titanyl oxalate was charged into the same autoclave as used in Preparation 8 and was reacted under a nitrogen atmosphere in a temperature range of from 200 to 250C. for 90 minutes. The pressure of the reaction system was then gradually reduced to 5 mm Hg in 60 minutes Subsequently, the mixture was reacted at 250C. under a pressure of 5 mm Hg. The resulting product was a yellow solid having a softening point of 78C. and its phosphorus content was 6.48~.
Preparation 11 18.7 parts of 9,10-dihydro-10-(1,2-dicarboxyl)ethyl-9-oxa-10-phosphaphenanthrene-10-oxide, 8.7 parts of dimethyl phthalate, 24.8 parts of ethylene glycol, 0.01 part of zinc acetate and 0.02 part of potassium titanyl oxalate were supplied to the same reaction vessel as used in Preparation 8. The reaction mixture was reacted under a nitrogen atmosphere in a temperature range of from 150 to 240C. for 200 minutes under stirring. The pressure of the reaction system was then gradually reduced to 1 mm Hg in 60 minutes. ~ubsequently, the reaction mixture was reacted at 250C. under a pressure below 1 mm Hg for 100 minutes. The resulting product was a yellow solid having a softening point of 79C. and its phosphorus content was 5.
Preparation 12 32.8 par-ts of the phosphorus compound (q), 12.4 parts of ethylene glycol, 19.0 parts of 2,2-bis(3,5-dibromo-4-hydroxy-phenyl) propane and 0.04 part of potassium titanyl oxalate were supplied to the same autoclave as used in Preparation 8. The reaction mixture was reacted under a nitrogen atmosphere in the temperature range of from 150 to 200C. for 60 minutes, and then the pressure of the reaction system was reduced to lmm Hg in 80 minutes. Subsequently, the reaction mixture was reacted at 210C. under 1 mm Hg for 120 minutes. The resulting product was a yellow solid having a softening point of 7~C. ~nd its ~0 phosphorus content was 5.70% and the bromine content was 17.63%.
Preparation 13 570 g. of 6,8-dicllloro-9,10-dihydro-9-oxa-10-phosphaphen-~ .

8~8 anthre~ lO-<)~iclc was c~larcJ~d into a five-rlecked flask, 1000 ml in capac:ity, ecluipped w:ith a thermometer, a cJas introduciny inlet, a c~as vent, a charg:incJ inlet and a stirrer. While nitrogen gas was blown into the flask, the temperature of the content was raisecl. ~hen the temperature reached 160C., stirring was started. 260 cJ. itaconic acid was gradually added at this temperature. After the comple-tion of the addition, the reaction was con-tinued for a further period of 7 hours, whereby a pale yellow resinous reaction product was obtained. It was found by the analysis of infrared absorption spectrum that this reaction product is a compound having the following structure:

Cl~[~Cl ' ,~ P-cH2c~lcooH

Preparation 14 576 g. of 2,6,8-tri-tert-butyl-9,10-dihydro-9-oxa-10-phosphaphenanthrene-10-oxide was charged into the same five-necked flask as used in Preparation 13. While nitrogen gas was blown into the flask, the temperature of the content was raised. At 150C., 237 g. dimethyl itaconate was gradually added dropw:ise under stirring. After the completion of the addition, the reaction mixture was maintained at this temperature for a further period of 10 hours to complete the reaction. It was found by the analysis of infrared absorption spectrum that the reaction product was a compound having the following structure:

H3C - C ~ C - CH3 H3C ~ ~ 3 ~ O
~ ,, 2, 3 H3c-,c CH3 _ample 1 A mixture consisting of 388 parts of dimethyl terephthalate, ~758~
2~8 p~lrts o~ ethy~ e cJlycoL, ~ artC; of the phosphorus-containinc~ coml~our.cl (b), 0 . 0~" zinc acetate and 0.03~ antimony trio~ide based on the dirnethyl terephthalate, was heated at 150 - 230C. for 120 minutes to perEorm transesterification reaction. Then the -temperature of the reac-tion system was raised to 275C. in 30 minute~s and the pressure of -the system was gradually reduced so that it reached 0.2 mm ~g after 45 minutes. The reaction was continued under this condition for a further period of 80 minutes. The intrinsic viscosity oE the resulting polymer was 0.56, the meL-ting point was 256C. and the ratio of phosphorus remaining in the polymer was 97~. The flame retardancy was 5.1 times.
Example 2 A polymer was obtained in the same way as in Example 1, except that 9.8 par-ts of phosphorus compound (m) was used in place of the phosphorus compound used in Example 1. The resulting polymer had an intrinsic viscosity of 0.5~, a melting point of 255C., and a remaining phosphorus ratio of 91%. The flame - retardancy was 5.1 times.
Comparative Example 1 Upon performing the transesterifica-tion reaction in the same way as in Example 1 except for using 10.2 parts of triphenyl phosphate instead of the phosphorus compound used in Example 1, ethylene glycol began to dis-till out during the reaction to inhibit the completion of the reaction, so that it was impossible to produce the object polymer.
Comparative Example 2 A mixture consisting of 388 parts oE dimethyl terephthalate, - 248 parts of ethylene glycol, 0.03% zinc acetate and 0.03%
antimony trioxide based on the dimethyl terephthalate was heated at 150 - 230C. for 120 minutes to perform transesterification reaction. 10.2 parts of triphenyl phosphate was added to this reaction system and the temperature of the system was raised to 270C. in 30 minutes and the pressure of the system was gradually reduced. At this time, the viscosity arose sharply and the reaction mixture gelled. Therefore, the object poly- ~
ester fiber could not be obtained.
Comparative Example 3 A polymer was obtained in the same way as in Example 1 excep-t that 8.1 parts of diethyl benzenephosphonate was used instead of the phosphorus compound used in Example 1. The intrinsic viscosity of the obtained polymer was 0.59, the meltin~ point was 256C. and the remaining phosphorus ratio was 45%. The flame retardancy was 3.2 times.

- .: , , - ~75~ 8 rn~ 3 ~ mixture conc;istincJ o~ 3~ parts of dimethyl terc~phthalate, 2~8 parts of ethylene g]ycol, 1~6 parts o~ the phosphorus compound (p), 0.07% zinc acetat~, 0.02~, potassium titanyl oxalate and 0.01~ antimony trioxide based on the dimethyl tere-phthalate, was heated to 150 - 230C. to perform transester-ifica-tion reaction. The -temperature of this reaction system was raised to 275C. in 30 minutes, and the pressure of the sys-tem was gradually recluced so that it reached 0.2 mm Hg aEter 45 minutes. Under this condition, the reac-tion was further continued for 60 minutes. The intrinsic viscosity of the result-ing polymer was 0.61, the melting point was 254C., and the remaining phosphorus ratio was 93%. The flame retardancy was 5.2 times.
Example ~
A mixture consisting of 388 parts of dimethyl terephthalate, 248 parts of ethylene glycol, 5.7 parts of the phosphorus compound used in Example 1, 23 parts of 2,2-bis(3,5-dibromo-4-hydroxyethoxyphenyl)propane, 0.05~ zinc acetate and 0.05~
antimony trioxide based on the dimethyl terephthala-te, was - heated at 150 - 230C. for 120 minutes to perform transester-ification reaction. The temperature of the system was raised to 275C. in 30 minutes and the pressure of the system was gradually reduced so that it reached 0.2 mm Hg after ~5 minutes. Under this condition, the reaction was further continued for 100 minutes. The intrinsic viscosity of the resulting polymer was 0.59, the melting point was 250C. and the remaining phosphorus ratio was 96%. The flame retardancy was 5r 6 times.
- Example 5 A mixture consisting of 335 parts of terephthalic acid, 2~3 parts of ethylene glycol, 0.2 part of antimony trioxide and 1.0 part of triethylamine, was heated at 230C. under 2.5 kg/cm2 for 60 minutes. At this poin-t of time, 10.3 parts of the phosphorus compound (s) was added, and the reaction was further continued under the condition of 230C. and 2.5 kg/cm . The resulting reaction product was transferred to a reac-tion vessel for polycondensation. The temperature of the system was raised from 230C. to 275C. in 40 minutes, and the pressure was gradually reducecl to 0.3 mm Hg finally. The reaction was 40 further continuecl fox 60 minutes under -the condition of 275C.
and 0.3 mm Ilg. The intrinsic viscosity of the resulting polymer was 0.59, the melting point was 254C., and the remaining phosphorus ratio was 94%. The flame retardancy was 5.0 times.

~ 0'751 3~
Example 6 The l~olymer obtained in Example 1 was spun in the usual way a-t a tcmperature o~ 290C. and at a spinning speed of 300 m/min to ob-tain an undrawn ~arn. The undrawn yarn was then drawn in the usual way at a hot pin -temperature of 80 - 85C.
to find the maximum drawing ratio until the yarn was broken.
The maximum drawiny ratio was fowld to be 6.1 times.
Comp rative ExaTnple ~
A mixture consis-ting of 388 parts of dimethyl terephthalate, 2~8 par-ts of ethylene glycol, 7.4 parts of die-thyl 2-ethoxy-carbonylethylphosphonate, 0.09% z:inc acetate, 0.02% potassium titanyl oxalate and 0.01~ antimony trioxide basecl on the dimethyl terephthalate, was hea-ted at 150 - 230C. for 120 minutes to perform tranesterification reaction. Then the -temperature of this system was raised to 275C. in 30 minutes, and the pressure of the system was gradually reduced so as to reach 0.2 mm Hg after 45 minutes. Under this condition, the reaction was continued for an additional time of 35 minutes. The intrinsic viscosity of the resulting polymer was 0.56, the melting point was 256C. and the remaining phosphorus ratio was 97~. The flame retardancy was 5.1 times. Upon drawing this polymer in the same way as in Example 6, the maximum drawing ra-tio was 5.7 times.
Example 7 A mixture consisting of 500 parts of dimethyl terephthalate, 360 parts of ethylene glycol, 20.2 parts of the phosphorus-containing compound-containing liquid (E) obtained in Preparation ~5), 0.045% zinc acetate and 0.05% antimony trioxide based on the dimethyl terephthalate, was charged into an aut~-clave and was heated at 150 - 230C. for 120 minutes to perform transesterification reaction. The temperature of the reaction system was raised to 275C. in 30 minutes, and the pressure of the sys-tem was gradually reduced so as to be 0.2 mm Hg after 45 minutes. Under this condition, the reaction was further continued for 60 minutes. The intrinsic viscosity of the resulting polymer was 0.636, the melting point was 257C. and the remaining phosphorus ratio in the polymer was 99% ~content 3025 ppm as phosphorus atom). This polymer was spun at 290C.
by means of an extruder-type spinning machine in the usual way.
The fiber thus obtained was drawn 3.8 times the length on a ho-t plate at 87C. in the usual way to obtain the final fiber, of which the strength was 5.6 g/d and the elonga-tion was 36%.
This fiber was knitted into a tricot and its flame re-tardancy was measured according to the flame retardancy standard .: .

lO~S~
(coil mctho~) estal~lisllecl by the Firc Services Act Enforcelnent ordinance Section ~, Subsection 3, Paragraph ~1 o~ ~apan. The ignition -time was fi~e times. In comparison with the fact -that the icJnition time o~ the polyester fiber c:ontaininy no phosphorus compound was below ~ times, this fiber had an excellen-t flame retardant effect.
Example 8 A polymer was obtained in the same way as in Example 7 except that 21.9 par-ts of -the liquid (F) obtained in Example 6 was used in place of the phosphorus-con-tainincJ compound used in xample 7. The intrinsic viscosity of -the resulting polymer was 0~629~ the melting point was 258C. and the remaining phosphorus ratio was 98% ~ The flame re-tardancy was 5.5 times.
Example 9 A mixture consisting of 500 parts of dime-thyl terephthalate, - 360 par-ts of ethylene glycol 20~ 0 par-ts of the phosphorus compount (z), 0.0~5~ manganese acetate and 0.02~ amorphous germanium dioxide based on the dime-thyl tereph-thalate, was charged into a reaction vessel and was heated at 150 - 230C~
for 140 minutes to perform transesterification reaction. After 0.34 part of trimethyl phosphate was added to this reaction mixture, the temperature of this reac-tion system was raised to 275C. in 40 minutes and the pressure of the system was gradually reduced so as to be 0.1 mm Hg after 40 minutes. Under this condition, the reaction was further continued for 95 minutes.
The intrinsic viscosity of the resulting polymer was 0.601, the melting point was 257C~ I and the ratio of phosphorus remaining in the polymer was 90~. The flame retardancy was 5.5 times.
Example 10 A mixture consisting of 2500 parts of dimethyl tere-phthalate, 1600 parts of ethylene glycol, 0.04 weight ~ zinc acetate and a. 05 weight % antimony trioxide was subjected to transesterification reaction at 150 - 230Co for 120 minutes.
The temperature of this reaction system was gradually raised and at the same time the pressure was gradually reduced so as to be 275C~ and 0.09 mm Hg, respectively, after 100 minutes at the end. The polymerization was continued for an additional time of 30 minutes. The intrlnsic viscosity of the resulting polymer was 0. 62 r and the b value of the polymer measured by means of a Color Difference Meter 101-D produced by Nippon Densho]~u Kogyo Co. was 3 ~ 0~ The flame retardant obtained in Preparation 9 crushed into granules was mixed with pellets of this polymer by means of a blender so tha-t the flame retardant granules form 6 ~ 2~ by weight. The mixture was spun ' :~0~7~8~
.into fi:Laments in the ~Is~lclL way by means oE a melt-spinning apparatus at th~ ~p:innincJ tempe:ratllre of 285C. at a sp.inning speecl of 600 m/min. The intrinsic viscosity of the thus-obtained filaments was 0.55, and the phosphorus content was 0.4%.
The filaments were drawn 4.6 times the length on a heated plate a-t 90C. The thus-obtained Arawn yarn was knit-ted into a tricot and the b value of the -trico-t measured in the same way was found to be 4.5. The flame retardancy was 5.0 times.
Example 11 A mixture consistin~ of 2500 parts of dimethyl tere-phthalate, 1600 parts of ethylene glycol, 122 parts of 9,10-dihydro-10-(2,3-dimethoxycarbonyl)propyl-9-oxa-10-phospha-phenanthrene-10-oxide, 0.04 weight % zinc ace-tate and 0.05 weight % antimony trioxide, was subjected to transesterification reaction at 150 - 230~C. for 140 minutes. Then the -temperature of the reaction system was gradually raised and a-t the same time the pressure was gradually reduced so that the temperature and the pressure reached 275C. and 0.09 mm Hg respectively after 100 minutes at the end. The polymerization was further continued -20 for 67 minutes. The intrinsic viscosity of the resulting polymer was 0.60 and the b value was 6.1. In the same way as in - Example 10, pellets of this polymer were spun into filaments and the filaments were drawn. The intrinsic viscosity of the filaments was 0.56 and the phosphorus conten-t was 0.4%. The b value of a tricot from the filaments was 6.7. The flame retardancy of the tricot was 5.1 times.
Examples 12-17 Mixtures each consisting of 500 parts of dimethyl tere-phthalate, 360 parts of ethylene glycol and the prescribed amoun-t of each catalyst, based on the dimethyl terephthalate, shown in ~able 1, were put into reaction vessels, respectively, and were subjected to transesterification reaction at 150 - 230C. ~or 120 minutes~ To each of the reaction vessels, 46.5 parts of the phosphorus composition tthe liquid (F)) obtained in Preparation 6 and the prescribed amount of each phosphorus : compound as a stabilizer, shown in Table 1 were added. Then the temp.erature of the reaction system was raised to 275C. in 40 minutes and the pressure was gradually reduced so that it reached 0.1 mm Hg after 40 minutes. Under this condition, the reaction was further con-tinued. The polymerizatioh time and the characteristic values of each of the polymers thus obtained are shown in Table 1. The color tone (b value) of the polymer shown in Table 1 was measured from polymer pellets ~0.8 mm x 4 nun) packed into a cel.l having a diameter of 40 mm and a heigh-t of ~n . -28-.

~0758~8 mm, by means oE a Co:Lor Di~Ecrellce Meter lOI-D produced by Nippon Del-lslloku Co. The l:ransparellcy o:E the polymer upon beiny meltecl is also observed and the result is shown toycther in Table 1.
It is apparent from TabLe 1 that -the addition of the phosphorus compounds as stabilizers, even in -the presence of the phosphorus compound oE the presen-t invent:ion, improves polymer color and transparency, and the flame retardancy of ea`ch polymer was 5.6 - 5.8 times, so that any loweriny of flame retardancy by ~he addition of the s-tabilize:rs was not observed.

5~3~8 ____ ._ __ _ _ ~_ ~o ~
h ~ ~ ~ co O :> m ~r ~r ~r ~r 0 ~1 ~__ . . ---- 1--h O h ~ ~
D ~ D ~ h h O h U~
_ . . _ _ O ~
u~ ~1 ~ ~ o o o~ ~
'~ O ~D ~D ~O , ~ U~ ~
H ~ O O O O O O

' 1 ~0 ~
N ~
S~ ~ In O n o Ll~ o ' ~Q) ~ ) ,ol ,o~ ~ I~
~1' P~
~ . --.
~ ~ . ~
O O
~ ~ ~ ~ a I ~n ~ ~ ~ r~
_ X~ ~ ~ ~: ~ ::
O ~ ~D O P~ 1-- ~ ~`1 U~ O U~
~; ~1 ~r .~:: ~1 In O t`l O u~ O ~
1~~ ~ . -~ ~ ~ ~C ~ .t~ ~ . ,:
u~ Q~ a) .~: o a) .~ o ~ o ~ o ~ o ~ . ~ t~ a) ~1 a) ~_1 ~-1 ~-1 ~ ~ ~ -O ~ ~1 ~: ~ ~ ~ a o ~ o ~ o a) ~ a ~o ~,~ Q ~ Q ~ Q-g ~ a) ~ o s~ ,, ,~ ,, O ~1 ~ ~1 U ~ O ~ C) E~ E~ E~
~' ' _ :', . U~ Ul U~ In In n I~ ~ 1-r-l O N . ~ 1 ~ ~1 ~1 . o . . O O. . . . ~ O

a) ~ ~ a3 ~ ~ ~ ~ a) ~ ~
~-~1 ~ ~ ~1 ~ ~1 1~ ~ ~ ~ ~ ~1 X ~ ~ X ~ X' ~-~1 ~ ~ ~
~n_ ~ o ~ ~ o ~ o-1~ x ~ ~ ~ o u, ~-~1 ~ a) ,, ~ ~a~ o a) o ~-,, O ~ ~) o h 0 5~ 0-,1 ~-,1 C) h ~ ~ ~ ~ ~ ~~ ra (d ~ ~ ~
~ ~:4 ~:i Q ~ O Q ~: Q ~; ~ ~ a) ~ Q
C~ ~ u~ ~ ~ u~ ~ ~ ~ ~7 r~ ~q _ __ __ ~ ~ s~ ~r In ~ ~
X ~1 ~ ~ ~1 ~1 ~
FL1 __ _ _ .
~.~.. .
.~ . ,

Claims (5)

THE EMBODIMENTS OF THE INVENTION IN WHICH AN EXCLUSIVE PROPERTY
OR PRIVILEGE IS CLAIMED ARE DEFINED AS FOLLOWS:

1. Flame retardant polyesters whose phosphorus atom content is 500-5-,000 ppm which contain a phosphorus-containing compound represented by the general formula (I) (I) wherein R1 is an ester-forming functional group selected from the class consisting of -COOR4, -OR5 and -OCOR6 wherein R4 is a hydrogen atom, a carbonyl group or a hydrocarbon group having 1-10 carbon atoms which may contain a hydroxyl group or a carboxyl group and R5 is a hydrogen atom or a hydrocarbon group having 1-10 carbon atoms which may contain a hydroxyl,group or a carboxyl group and R6 is a hydrocarbon group having 1-10 carbon atoms which may contain a hydroxyl group or a carboxyl groups;
R2 and R3 are the same or different groups which are selected from halogen atoms, hydrocarbon groups having 1-10 carbon atoms;
A is a divalent or trivalent hydrocarbon group having 1-8 carbon atoms; and n1 is an integer of 1 or 2 and n2 and n3 are each an integer of 0-4; and/or the residue of the formula (I) as a part of the repeating units of said polyester.

2. Flame retardant polyesters claimed in Claim I obtained from at least one kind of dicarboxylic acid or an ester-forming derivative thereof, or at least one kind of oxycarboxylic acid or an ester-forming derivative thereof, and a phosphorus-containing compound represented by the general formula (I).

3. Flame retardant polyesters as claimed in Claim 1 which are obtained by using a compound represented by the general formula (I) wherein A is a trivalent hydro carbon group having 1-4 carbon atoms, R1 is -COOR7 wherein R7 is a group selected from a hydrogen atom, a methyl group, ethyl group and 2-hydroxyethyl group.

4. Flame retardant polyesters as claimed in Claim 1 by using terephthalic acid or an ester-forming derivative thereof as the diearboxylic acid or the ester-forming derivative thereof, and at least one kind of glycol selected from the class consisting of alkylene glycols whose carbon atom number is less than 5 and 1, 4-cyclohexane dimethanol as diol or an ester-forming derivative thereof.

5. Flame retardant polyesters as claimed in Claim 1 obtained by using a glycol represented by the following general formula as a part of the diol or the ester-forming derivative thereof:

wherein X represents a halogen atom, Y represents an alkylidene group, cycloalkylidene group, arylalkylidene group, -S-, -SO-, -S02- or -0-, and m represents an integer of 1 4.