WO2004048652A1

WO2004048652A1 - A full dull polyamide 6 yarn, and a process of preparing for the same

Info

Publication number: WO2004048652A1
Application number: PCT/KR2003/002523
Authority: WO
Inventors: Jae-Young Kim; Young-Tae Park
Original assignee: Kolon Industries Inc
Current assignee: Kolon Industries Inc
Priority date: 2002-11-22
Filing date: 2003-11-21
Publication date: 2004-06-10
Anticipated expiration: 2005-05-22
Also published as: US7736563B2; JP2006507422A; CN1312336C; KR100624153B1; US20060046052A1; US20070060680A1; CN1714179A; AU2003284740A1; US7147914B2; KR20040045342A

Abstract

The present invention relates to a full dull polyamide 6 yarn and a process for preparing the same. The yarn of this invention contains 1.5 to 2.5 % by weight of titanium dioxide relative to the weight of the yarn, has 35 to 95 titanium dioxide particles having a major axial length of greater than 5µm being contained in 50 mg of the yarn, and contains 0.1 to 0.5 % by weight of phosphate salt (wetting agent) relative to the weight of titanium dioxide. In the process of this invention, 0.1 to 0.5 % by weight of phosphate salt relative to the weight of titanium dioxide is added as a wetting agent, carprolactam is applied along with water upon concentration correction, and naphthalene sulfonate based salt is applied along with titanium dioxide slurry during the process of polyamide 6 polymerization. The present invention improves the full dull effect and drape property of the yarn since it contains a great quantity of titanium dioxide having a proper diameter in the yarn without degrading the yarn physical properties and operationability.

Description

A FULL DULL POLYAMIDE 6 YARN, AND A PROCESS OF PREPARING

FOR THE SAME

TECHNICAL FIELD

The present invention relates to a full dull polyamide 6 yarn which

is full dull and has an excellent weightiness (hereinafter refer to as "drape

property") since it contains a great quantity of titanium dioxide within a

yarn, and a process for preparing the same.

Polyamide 6 yarns are being widely used for clothing as a

substitute for natural yarns owing to excellent mechanical properties or

the like. But, there is a problem that they show cold feeling and an

excessively lightweight feeling due to a metallic brilliance and they are too

transparent, thus they cannot satisfy the market demand valuing much

of sensuous properties.

BACKGROUND ART

To solve the above problem, there is being widely used the process

of eliminating brilliance and improving drape property by applying an inorganic material exhibiting a dulling effect during the process of

polymerizing a polyamide 6 yarn. But, this process is problematic in that,

when an input of the inorganic material is set high to 1.5% by weight

relative to the weight of a yarn (polymer), the operationabilit is degraded

and the yarn physical properties are deteriorated due to a nonuniform

dispersion of the inorganic material.

Therefore, in the prior art, there is a limitation that an inorganic

material of greater than 1.5% by weight cannot be contained in a

polyamide 6 yarn, and accordingly, there is a limit to eliminate the

metallic brilliance of the yarn or enhance the drape property.

The process of prior art, applying an inorganic material in a yarn,

will be described in more detail. Slurry of inorganic material is prepared

through a process of wetting an inorganic material with water, a process

of grinding the inorganic material condensed in the above process, a

concentration correction process, and a sedimentation process. Next, the

slurry is applied during the polymerization process of polyamide 6,

thereby to produce a full dull polyamide 6 yarn. As the inorganic material,

mainly used is titanium dioxide having an average diameter of 0.3 to 0.4μm.

In the above process, the degradation of operationability and yarn

physical properties does not occur only due to the original particle size of

titanium dioxide, but it occurs because titanium dioxide is rapidly

condensed during the wetting process.

In the above process of prior art, it is considered that the

condensation of titanium dioxide in the wetting process is unavoidable.

Thus, the problem of titanium dioxide condensation in the wetting

process is overcome by such a process in which large particles of

titanium dioxide are separated before titanium dioxide is applied in the

polymerization process of polyamide 6, and only small particles are

applied.

Due to this, the yield of the titanium dioxide slurry production

process is degraded, the process becomes complicated because the

separation process is added, and the particle size of titanium dioxide

applied in the polymerization process is nonuniform.

Therefore, in the process of prior art, in a case that titanium

dioxide of more than 1.5% by weight relative to the weight of a yarn (polymer) is applied, there occurs a problem that the pressure of a pack

(spinneret) is rapidly increased due to large diameter particles of titanium

dioxide, and the yarn tension becomes nonuniform due to a nonuniform

dispersion of titanium dioxide, to thereby make the bending and cutting

of yarns disposed directly below the spinneret more serious.

In the prior art, the input of titanium dioxide cannot be set to more

than a predetermined level due to the degradation of operationability and

physical properties, and accordingly, it is restricted to improve the full

dull property and drape property of polyamide 6 yarn.

Korean Laid-Open Patent No. 1999-60536 discloses a process for

preparing a polyamide yarn by a high speed spinning, which produces a

polyamide ultrafine yarn having a mono filament fineness of below 1.0

denier by adding titanium dioxide in the step of polyamide polymerization,

wherein the portions directly below the spinneret are maintained at a

heating atmosphere.

Although the detailed description of the above prior patent

describes that titanium dioxide of 1 to 3% by weight is added in the

polyamide polymerization step, every examples of the prior patent describes that titanium dioxide of 1.5% by weight is added in the

polyamide polymerization step.

This is because, as described above, in a case that titanium dioxide

of more than 1.5% by weight is added in the polyamide polymerization

step, there occurs a problem that the operationability is degraded and the

yarn physical properties are deteriorated due to a nonuniform dispersion

of titanium dioxide.

Moreover, the above prior patent does not suggests concrete means,

for example, preparation conditions of slurry of titanium dioxide, for

overcoming the above problems occurred upon applying titanium dioxide

of more than 1.5% by weight in the polyamide polymerization step.

Subsequently, also in the Korean Laid-Open Patent No.

1999-60536, in a case that the amount of titanium dioxide is over 1.5%

by weight, it is inevitable that there occur the degradation of the

operationability and yarn physical properties due to a nonuniform

dispersion of titanium dioxide.

As a prior art for improving the dispersability of titanium dioxide in

polyamide, Korean Laid-Open Patent No. 2003-0012336 discloses a process of applying 0.05 to 0.2 parts by weight of an amine based

material relative to caprolactam monomer while using the existing

viscosity stabilizer, i.e., an acetic acid.

However, the above prior art has a drawback that it is difficult to

prevent recondensation fundamentally since a contact between acetic

acid and titanium dioxide is possible, though the prior art may be

effective to prevent the recondensation of titanium dioxide with an

increase in repulsive force between titanium dioxide particle surfaces by

pH control in the polymerization process. Further, since polymerization is

typically carried out at a high temperature of higher than 250°C, in case

of an amine based compound, there may occur a problem that its effect is

not presented because the polymerization conditions such as a burning

point, viscosity, etc. are not satisfied if a number of carbon atoms is below

10.

Additionally, since acid and amine are used in combination, the

activity of polymerization may differ according to input equivalent ratio.

This may be a factor in generating a difference in molecular weight of final

polymer or a difference in terminal groups. As another prior art, Korean Laid-Open Patent NO. 2003-0034845

discloses a process of applying 0.05 to 0.2 parts by weight of an aromatic

amine relative to caprolactam without using acetic acid.

The above process allows to maintain a good dispersability of

titanium dioxide in the polymerization process, but a reduction of zeta

potential occurs at some portions in a reactor due to the abundance of

the amine, to thereby deteriorate the dispesability of titanium dioxide on

the contrary. In addition, the breadth of change in relative viscosity (RV)

before and after melting increases due to an increase of terminal amine

groups, and it is difficult to manage the strength of a final product. And,

the above process is known to those skilled in the art as the process

generally performed mainly for the purpose of improving deep

color- dyeing or improving color difference. To complement the physical

properties problem, the process of minimizing the breadth of change in

relative viscosity (RV) before and after deep color-dyeing and melting by

using an amine having no reactivity and being utilizable as a dyeing site

is widely used.

Further, the above-described prior art processs all aim only to maintain the dispersability of titanium dioxide in the polymerization

process at a slurry level without mentioning detailed techniques for the

production of titanium dioxide slurry. This shows that it is important to

produce slurry of titanium dioxide with a good dispersability

economically and efficiently.

In addition, in case of generally using a low molecular amine based

compound, there is a possibility that polymerization may be accelerated

by the reactivity of amine, and thus the color of a final polymer becomes

poor.

Accordingly, it is an object of the present invention to provide a

process for allowing much quantity of titanium dioxide to be contained in

a yarn without degrading the operationability and physical properties by

dispersing titanium dioxide uniformly in polymer by preventing the

recondensation of titanium dioxide in a wetting process.

It is another object of the present invention to provide a polyamide

6 yarn which is full dull and has a good drape property since it contains a

much quantity of titanium dioxide. DISCLOSURE OF THE INVENTION

The present invention provides a process for adding much quantity

of titanium dioxide in a yarn (polymer) without degrading the

operationability and the physical properties of yarns by minimizing the

diameter of titanium dioxide to be applied in the step of polyamide 6

polymerization and dispersing the applied titanium dioxide uniformly.

In addition, the present invention provides a polyamide 6 yarn

which is full dull and has an excellent drape property since much

quantity of titanium dioxide having a proper diameter is uniformly

contained in the yarn.

To achieve the above objects, the present invention provides a full

dull polyamide 6 yarn, which contains 1.5 to 2.5% by weight of titanium

dioxide relative to the weight of the yarn, which has 35 to 95 titanium

dioxide particles having a major axial length of greater than 5μm being

contained in 50mg of the yarn, and which contains 0.1 to 0.5% by weight

of phosphate salt (wetting agent) relative to the weight of titanium

dioxide.

Additionally, the present invention provides a process for preparing a full dull polyamide 6 yarn, in which the full dull polyamide 6

yarn is produced by preparing titanium dioxide slurry through wetting,

grinding, concentration correcting, sedimentation and storage processes

and applying the same during the process of polyamide 6 polymerization,

wherein 0.1 to 0.5% by weight of phosphate salt relative to the weight of

titanium dioxide is added as a wetting agent, carprolactam is applied

along with water upon concentration correction, and naphthalene

sulfonate based salt is applied along with titanium dioxide slurry during

the process of polyamide 6 polymerization.

Hereinafter, the present invention will be described in detail.

Firstly, titanium dioxide slurry is prepared through wetting,

grinding, concentration correction, sedimentation and storage processes.

In the wetting process, a titanium dioxide powder is wet with water, a

dispersion medium, in the ratio of 50:50. Then, 0.1 to 0.5% by weight of

phosphate salt, such as sodium biphosphate, is added as a wetting agent

relative to the weight of titanium dioxide, and stirred.

A typical polyamide 6 polymerization is carried out in such a step

that a predetermined amount of water is put into caprolactam, a major material, then ring-opening reaction is performed, and then

polycondensation is performed, thereby making a final polymer. Thus,

the reaction is conducted with a predetermined amount of water being

contained within a reaction system. Hence, in the production process of

titanium dioxide slurry, water is utilized as a dispersion media for wetting

titanium dioxide of a powdery state to turn it into a liquid state under an

economical condition.

The wetting agent is applied in order to reduce the cycle of the

wetting process by increasing the affinity between water and titanium

dioxide and minimize a particle size as much as possible right after the

wetting process.

The wetting agent is such a material in which an ionic bond and a

covalent bond coexist. It firstly increases the affinity between water and

titanium dioxide through an electric charge, and, further, serves to

control an electrical attractive force related to the condensation in a

subsequent process of titanium dioxide slurry production.

In case of applying the wetting agent of below 0.1% by weight

relative to the weight of titanium dioxide, the above-mentioned effect is rarely exhibited. In case of applying the wetting agent of over 0.5% by

weight, the extent of increase of affinity becomes smaller as compared to

when the wetting agent of 0.5% by weight is applied, thus the production

cost is increased. In case of applying an extremely large amount, this may

occur adverse effects from a condensation viewpoint.

But, this does not mean that final titanium dioxide slurry is

completed in the wetting process. The primary objective of the wetting

process is to wet titanium dioxide of a powdery state with water, i.e., a

dispersion medium most efficiently, and, in addition, to provide the

foundation enabling a good dispersion in the subsequent titanium

dioxide slurry production process.

In a case that the average particle diameter of titanium dioxide

powder is 0.3 to 0.4μm, after the wetting process of the present invention,

the average particle diameter of titanium dioxide becomes about 0.6μm.

To solve the problem of physical condensation of titanium dioxide

occurring in the wetting process, it is preferred that stirring is performed

for one hour at a low speed and for one hour at a high speed. The stirring

speed is set to a proper level in conjunction with a geometric structure of a stirring tank. In case of stirring at a high speed from an initial stage,

wetting efficiency may be lowered due to an excessive heat generated in

the stirring. Thus, it is preferred that the stirring is performed at a low

speed at an initial stage, and, after a predetermined time, performed at a

high speed.

After the wetting process, the titanium dioxide slurry made in the

wetting process is made finer and uniformly dispersed through a grinding

process. Preferably, the grinding process is performed repetitively about

two times using a sand grinder filled with about 20% by weight of

zirconium fill. However, the present invention does not specifically limit

the grinding process.

Preferably, upon grinding, the flow rate of titanium dioxide slurry

is maintained at 5 to 20kg/ min, and the temperature of titanium dioxide

grinded is maintained at 35 to 50°C.

After the grinding process, the concentration of titanium dioxide is

corrected so that the grinded titanium dioxide slurry can have such a

concentration capable of allowing the titanium dioxide slurry to have the

most stabilized state. Most preferably, the concentration is corrected with water, i.e., a

dispersion medium. But, in case of correcting the concentration by

increasing in weight of water, the dispersion stability of the titanium

dioxide slurry is reduced because the apparent viscosity of the titanium

dioxide slurry is lowered, whereby titanium dioxide particles may be

recondensed.

In addition, the amount of water is increased in the subsequent

polymerization process to arouse an excessive ring-opening reaction and,

further, cause the problem of decrease in polymerization speed. For this

reason, the present invention is characterized in that, upon

concentration correction, caprolactam, which is a main material, is

mixed with water at a predetermined ratio.

The amount of caprolactam to be applied is preferably 25 to 35%

by weight relative to the total quantity of titanium dioxide slurry. The

reason thereof is that, since final titanium dioxide slurry is made through

sedimentation for four days after the step of concentration correction, the

sorting efficiency of titanium dioxide through sedimentation is more

increased if the amount of caprolactam is more decreased from a sedimentation viewpoint.

And, as the amount of caprolactam is increased, dielectric

constant of the slurry is lowered to thus increase condensation. From

this viewpoint, the less the amount of caprolactam is, the better.

Immediately after the concentration correction, simple sedimentation is

carried out in a concentration correction tank for one day to thus reduce

final sedimentation load.

Next, sedimentation is performed to the titanium dioxide slurry

compensation-corrected and simply sedimented as above. In the

sedimentation process, final titanium dioxide slurry with a minimized

average diameter is made through a long time sedimentation for four

days.

The sedimentation velocity (or settling velocity) in a sedimentation

tank is inverse proportional to the viscosity of a dispersion medium and

the height of the sedimentation tank, and proportional to the

temperature of a dispersion medium, the acceleration of gravity, the

density of titanium dioxide and the like. Of them, the adjustable variables

in the process are the height of the sedimentation tank, the temperature of the dispersion medium and so on, and the proper conditions for these

variables are selected as follows.

It is measured whether the average particle size of final titanium

dioxide slurry sorted through sedimentation in the sedimentation tank

for four days is consistent with a required level, and then the above

variables are adjusted according to the result of the measurement.

In the present invention, according to the result of measurement

by a particle size analyzer, the average particle size of titanium dioxide in

the final titanium dioxide slurry is 0.38μm. The particle concentration of

titanium dioxide in the titanium dioxide slurry is 18.5 to 22.0% by weight

upon measuring by a standard gravimeter at 20°C.

Next, the sorted titanium dioxide slurry is stored. In the above

storage process, it is important to reduce a detention time as much as

possible since the slurry is stored right before being applied into the

process. And, to prevent settlement during detention, it is preferable to

keep the temperature low.

The titanium dioxide slurry made as above has an excellent

dispersability, so it is possible to apply a greater content thereof than that applied in the prior art.

Next, the thusly made titanium dioxide slurry is supplied to a

polyamide 6 polymerization system to thus produce a full dull polyamide

6 yarn. At this time, the present invention is characterized in that a

naphthalene sulfonate based salt is applied together as a dispersion

agent.

In other words, when the titanium dioxide slurry is applied in the

polymerization, condensation may occur again. Thus, in the present

invention, the recondensation of titanium dioxide particles in the

polyamide polymerization process is controlled by adjusting electric

potential with the applied naphthalene sulfonate based salt. The amount

of the dispersion agent applied in this invention is preferably 30 to 60cc

relative to 1kg of titanium dioxide particles.

The thusly produced polyamide 6 yarn (polymer) of this invention

is very excellent in the dispersability of titanium dioxide particles, and is

very excellent in full dull property and drape property since a great

quantity of titanium dioxide, that is, 1.5 to 2.5% by weight, is contained

relative to the weight of the yarn. In addition, the polyamide 6 yarn (polymer) of the present invention has 35 to 95 particles of titanium

dioxide having a major axial length of greater than 5μm in 50mg of the

yarn (polymer).

Additionally, the polyamide 6 yarn (polymer) of this invention

contains 0.1 to 0.5% by weight of phosphate salt (wetting agent) relative

to the weight of titanium dioxide.

The operationability of preparing the yarn of this invention is good,

which is the same level as the operationability of the prior art production

process of a polyamide 6 yarn containing 0.3 to 0.4% by weight of

titanium dioxide.

Various physical properties of the yarn (polymer) in the present

invention are evaluated as follows.

• Number of Coarse Particles

It means the number of condensed titanium dioxide particles

having a major axial length of greater than 5μm contained in 50mg of a

polyamide 6 yarn (polymer). A sheet of slide glass is placed on a hot plate

of 250°C, a sheet of glass film is placed thereon, 50mg of the yarn (polymer) is placed and melted thereon, and then a sheet of cover glass is

covered thereon. Next, the yarn is pressed by 200g of a weight to be thinly

stretched, and then the entire regions of the sample are scanned by a

light microscope of total 200 magnifications, thereby to measure the

number of condensed titanium dioxide particles having a size of greater

than 5μm.

Besides the above-mentioned hot plate process, among the sample

preparation processs for measuring the number of condensed titanium

dioxide particles, there is the process of using a small-sized extruder with

a T-shaped spinneret. In this process, an undrawn film is prepared by a

small-sized extruder, cooled by a casting drum, and then cut to a size

proper to a drawing machine. The cut undrawn film is simultaneously

biaxially oriented, and then heat-treated to prepare a sample for

measurement. At this time, the temperature of the small-sized extruder is

about 260 to 280°C, and the casting drum after the spinneret is

maintained at 10°C, thereby to produce an undrawn film. The undrawn

film is simultaneously biaxially oriented three times transversely and

longitudinally each at about 55°C, and then thermoset for 30 seconds at about 200°C, thereby to produce a final measurement sample.

* Content of Wettin Agent

A polyamide 6 yarn is pre-treated by the wet oxidation process and

the oxidizer application and decomposition process, and then the content

of a wetting agent is measured by an inductively coupled plasma mass

analyzer (a product of VG ELEMENTAL, model name: Plasma Quad3).

• Dispersability of Titanium Dioxide

A specimen made by slicing a polyamide 6 yarn (polymer) by a

cutter of Microtom is immersed on a sheet of slide glass with paraffin, a

sheet of cover glass is covered thereon, and projection photographs of 10

areas are taken by a light microscope of 625 magnifications. Condensed

titanium dioxide particles are found from each of the photographs, and

the size and number thereof are arranged. Among 10 results arranged,

the dispersability of titanium dioxide is judged according to the

remaining 8 results, except for the best result and the worst result. Of the

8 results, if more than 7 results are excellent, it is represented as ©, if 5 to 6 results are excellent, it is represented as O, and if less than 4 results

are excellent, it is represented as Δ .

• Operationability (Full Drum Rate - F/D rate)

The operationability is indicated by the F/D rate showing the ratio

of the number of full drums that are fully wound per the total number of

drums manufactured in a spinning process.

- O--pera -t-i•ona 1b-.i •l-i•.t-,y (_TF- _AD_Γ ra -t.e) -= number of full — drums x - 1, _Λ0_Λ0(_/n%_/ ) total number of drums

• Full Dull Property

Yarns are tube-knitted and then evaluated by an organoleptic test

by panelists. Of five panelists with over seven year's career, if more than

four people agree that the full dull property is excellent, it is indicated as

indicated as O, and less than one people agrees that the full dull

property is excellent, it is indicated as Δ . • Drape Property

A cloth made by tube-knitting yarns is cut to a circular shape

having a 25cm diameter, then placed over a cylinder having a 12.5cm

diameter, and then evaluated in drape property according to how long the

cloth is draped down (drape coefficient: F). If the drape coefficient (F) is

than 0.3, it is indicated as Δ. The drape coefficient is calculated by the

following formula:

Drape

Wherein rD represents the radius of a completely hard twist fabric,

rd represents the radius of a completely soft twist fabric, and r represents

the radius of a specimen.

BEST MODE FOR CARRYING OUT THE INVENTION

The present invention is now understood more concretely by

comparison between examples of the present invention and comparative

examples. However, the present invention is not limited to such

examples.

Example 1

Titanium dioxide with an average diameter of 0.3μm is wet with

water in the ratio of 50:50, then added with 0.3% by weight of sodium

biphosphate (wetting agent) relative to the weight of titanium dioxide and

stirred, and then grinded with a sand grinder.

Next, the concentration of titanium dioxide slurry is corrected by

using water and 30% by weight of caprolactam relative to the weight of

titanium dioxide slurry, and then the titanium dioxide slurry is immersed

for four days, thereby to prepare final titanium dioxide slurry.

Next, the titanium dioxide slurry is applied in a polyamide 6

polymerization process along with sodium naphthalene sulfonate

(dispersion agent) in a 20% aqueous solution state to thus produce a

polyamide 6 polymer. The polyamide 6 polymer is composed of 100% by weight of caprolactam, 5.3 parts by weight of water and 0.1 parts by

weight of acetic acid.

Here, the titanium dioxide slurry is applied in such a composition

in which the quantity of titanium dioxide particles can be 1.8 parts by

weight relative to 100 parts by weight of caprolactam. The dispersion

agent is applied so that it can be 40cc per 1kg of titanium dioxide

particles. The thusly produced polyamide 6 polymer is spun in a typical

spin-direct-draw condition, to thus produce a polyamide 6 yarn having

70 deniers and 36 filaments. The result of evaluating the physical

properties of the produced yarn and operationability is as shown in Table

2.

Examples 2 to 7 and Comparative Examples 1 and 2

Except that the quantity of titanium dioxide particles, the input of

a dispersion agent and the input of a wetting agent are changed as in

Table 1, a polyamide 6 polymer and yarn are produced in the same

process and condition as Example 1. The result of evaluating the physical

properties of the produced yarn and operationability is as shown in Table [Table 1]

Production Condition

Input of titanium

Input of Input of wetting dioxide relative to dispersion agent agent relative to

100 parts by

Classification per 1kg of weight of weight of titanium dioxide titanium dioxide caprolactam particles (cc) (% by weight) (parts by weight)

Example 1 1.8 40 0.3 ^'

Example 2 1.6 40 0.3

Example 3 2.4 40 0.3

Example 4 1.8 35 0.3

Example 5 1.8 60 0.3

Example 6 1.8 40 0.1

Example 7 1.8 40 0.5

Comparative

1.3 0 0 Example 1

Comparative

2.6 0 0 Example 2 [Table 2]

The content of titanium dioxide is % by weight relative to the weight of

yarn. INDUSTRIAL APPLICABILITY

The present invention can prevent the degradation of

operationability and yarn physical properties since a great quantity of

titanium dioxide having a proper diameter are uniformly dispersed in a

polyamide 6 yarn. In addition, the polyamide 6 yarn of this invention

uniformly contains titanium dioxide with a proper diameter, thus it has

no metallic brilliance and has an excellent drape property.

Claims

WHAT IS CLAIMED IS:

1. A full dull polyamide 6 yarn, which contains 1.5 to 2.5% by

weight of titanium dioxide relative to the weight of the yarn, which has 35

to 95 titanium dioxide particles having a major axial length of greater

than 5μm being contained in 50mg of the yarn, and which contains 0.1 to

0.5% by weight of phosphate salt (wetting agent) relative to the weight of

titanium dioxide.

2. A process for preparing a full dull polyamide 6 yarn, in which the

full dull polyamide 6 yarn is produced by preparing titanium dioxide

slurry through wetting, grinding, concentration correcting,

sedimentation and storage processes and applying the same during the

process of polyamide 6 polymerization, wherein 0.1 to 0.5% by weight of

phosphate salt relative to the weight of titanium dioxide is added as a

wetting agent, carprolactam is . applied along with water upon

concentration correction, and naphthalene sulfonate based salt is

applied along with titanium dioxide slurry during the process of

polyamide 6 polymerization.

3. The process of claim 2, wherein the input of caprolactam is 25 to 35% by weight relative to the weight of the titanium dioxide slurry.

4. The process of claim 2, wherein the input of naphthalene

sulfonate based salt is 30 to 60cc per 1kg of titanium dioxide particles.