Title of Invention

METHOD OF PRODUCING HYDROTALCITE

Abstract The invention discloses a method of producing hydrotalcite of formula: [(Mg)x(Zn) y] 1-z (AlZ(OH)2(An-)z/n•mH20, wherein An- represents an anion having a valence of n; x, y, z and m are values which satisfy the following expressions, 0.5 &#8804; x &#8804; 1, 0 &#8804; y &#8804; 0.5, x+y = 1, 0.1 &#8804; z &#8804; 0.5, and 0 &#8804; m < 1, the method comprising the steps of: providing a slurry of hydrotalcite, wherein the hydrotalcite slurry is obtained using magnesium sulfate as the magnesium source; and washing the slurry with water, whereinsaid hydrotalcite slurry is obtained by combining magnesium sulfate, aluminum sulfate, sodium hydroxide, and sodium carbonate, and optionally zinc sulfate; and subjecting the combination to a hydrothermal synthesis at a temperature of 120° to 250°C; and further wherein the hydrotalcite has a sodium content of 100 ppm or less and a specific surface area of 1 to 40 m2/g.
Full Text DESCRIPTION
TECHNICAL FIELD
The present invention relates to hydrotalcite, a method
of producing the same and a synthetic resin composition.
BACKGROUND ART
Hydrotalcite is an inorganic compound containing
magnesium, zinc and aluminum/ and it is known from WO 99/01509,
Japanese kokoku Publication Sho-46-2280, Japanese kokoku
Publication Sho-47-32198, Japanese kokoku Publication
Sho-48-29477, Japanese kokoku Publication Sho-50-30039,
Japanese kokoku Publication Sho-51-29129 and Japanese Kokai
Publication Sho-55-80445, that by using it as an additive of
synthetic resins for general purpose such as polyolefin,
polyvinyl chloride and the like, properties as a heat stabilizer
of resin or an acid-acceptor of resin can be attained. It is
known that a resin composition containing the hydrotalcite is
particularly superior in a thermal insulating property and
thermal stability and this resin composition can be used in
applications such as a film for agricultural uses and a resin
for covering wires.
But, when the hydrotalcite is mixed into a polyolefin resin
or a copolymer thereof, a problem that die drool or coloring
(yellowing) occurs by being subjected to a step of heating for
processing arises. Therefore, it has been desired to decrease
the occurrence of die drool and coloring resulting from the
hydrotalcite.
Further, as a film for agricultural uses, polyolefinic
resin films such as a polyvinyl chloride film, a polyolefin film
and an ethylene-vinyl acetate copolymer film are mainly used
for houses or tunnels in protected horticulture. The
performance required of such a film for agricultural uses varies
with its use, applications and subjects of crops, and therefore
various properties other than heat resistance may be required.
However, in some cases, specific properties are deteriorated
or other properties are not improved, depending on the additional
amount of hydrotalcite.
For example, the films for agricultural uses are required
to have properties such as weathering resistance (performance
capable of resisting a long-term use in the sunny outdoors),
an anti-f ogging property (performance of preventing a phenomenon
in which an inner surface of a covering film is covered with
fine sweat through condensation due to high humidity in houses
or tunnels and its transparency is deteriorated), a thermal
insulating property (performance of maintaining temperature in
facilities high during the night) and a translucency
(transparency) . With respect to a synthetic resin composition,
containing the hydrotalcite, for polyolefin films for
agricultural uses, it is known that when an amount of the
hydrotalcite is increased, a white discoloration by water due
to rainwater, moisture and sweat in uses further occurs as the
hydrotalcite content in a film increases. Thus, it has been
desired to inhibit a white discoloration by water of a polyolefin
film for agricultural uses.
And, when the hydrotalcite is added to a vinyl chloride
resin film in a relatively large amount, a blooming(effusion
of powder) to the surface of a film arises and therefore
countermeasures for this have been requested.
Further, the hydrotalcite is also used as a stabilizer
of a vinyl chloride resin for covering wires in place of a lead
stabilizer, use of which is not preferred from the view point
of an environmental impact. But, when the conventional
hydrotalcite having a sodium content of more than 100 ppm is
used, there is a problem that the electric resistance (volume
resistivity = VR) of the vinyl chloride resin is reduced compared
with the case of using the lead stabilizer. Thus, there has
been required such hydrotalcite that a vinyl chloride resin
composition having the electric resistance which is equal to
that in using the lead stabilizer can be obtained.
SUMMARY OF THE INVENTION
In view of the above state of the art, it is an object
of the present invention to provide hydrotalcite which can
inhibit a white discoloration by water of a polyolefin film for
agricultural uses, a blooming to the surface of a vinyl chloride
resin film, a reduction in electric resistance in the case of
using the hydrotalcite as a stabilizer of a vinyl chloride resin
for covering wires, the occurrence of die drool in the case of
using the hydrotalcite as a neutralizer of an acid catalyst
residue in a polyolef in resin or a copolymer thereof, and coloring
(yellowing) in extrusion inpreparingpellets and canbe suitably
used as a resin additive, a method of producing the same and
a synthetic resin composition containing the same.
The present invention relates to hydrotalcite expressed
by the following formula (1);
[ (Mg) x (Zn) y] i-z (Al) 2 (OH) 2 (An") z/n-mH20 (1)
in the formula An~ represents an anion having a valence of n,
andx, y, z andmare values whichsatisfy the following expressions,
0.5 the hydrotalcite has a sodium content of 100 ppm or less
and is used as a resin additive.
The above hydrotalcite preferably has a specific surface
area of 1 to 40 m2/g.
The above hydrotalcite is preferably obtained by a
hydrothermal synthesis at a temperature of 120 to 250°C.
The present invention also relates to a method of producing
hydrotalcite, which comprises a step (I) of obtaining
hydrotalcite slurry using magnesium sulfate as a magnesium source
and a step (III) of washing with water.
In the above method of producing hydrotalcite, the above
step (I) is preferably a step of obtaining hydrotalcite slurry
by a hydrothermal synthesis at a temperature of 120 to 250°C.
The above method of producing hydrotalcite preferably
further comprises a step of surface treating.
The present invention also relates to a synthetic resin
composition, which contains the above hydrotalcite and a
synthetic resin.
In the above synthetic resin composition, the content of
the above hydrotalcite is preferably 0.01 to 20 parts by weight
based on 100 parts by weight of the above synthetic resin.
Preferably, in the above synthetic resin composition, the
synthetic resin is a vinyl chloride resin and the content of
the above hydrotalcite is 0.1 to 5 parts by weight based on 100
parts by weight of the vinyl chloride resin.
Preferably, in the synthetic resin composition, the above
synthetic resin is a polyolefin resin or a copolymer thereof,
and the content of the above hydrotalcite is 0.01 to 15 parts
by weight based on 100 parts by weight of the above polyolefin
resin or the above copolymer thereof.
The above synthetic resin composition is preferably used
as a film for agricultural uses.
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the present invention will be described in
detail.
The hydrotalcite of the present invention is expressed
by the above-mentioned formula (1) and has a sodium content of
100 ppm or less. When such hydrotalcite is used as a resin
additive, it improves the stability of resin against heat or
ultraviolet light to give various physical properties required
of resin, such as an excellent thermal insulating property.
As an example of specific applications as the above resin
additive, there can be given, for example, a thermal insulating
material for a polyolefin film for agricultural uses, a
stabilizer for a vinyl chloride resin, a stabilizer of a vinyl
chloride resin for covering wires and a neutralizer of an acid
catalyst residue in a polyolefin resin or a copolymer thereof
obtained by polymerization using an acid catalyst.
The present inventors have found that many of properties,
which were assumed to be defects when using the conventional
hydrotalcite in these uses, were resulted from sodium (Na)
contained in the hydrotalcite. Accordingly, they have found
that many problems in the conventional hydrotalcite can be
resolved by using the hydrotalcite expressed by the
above-mentioned formula (1) and having a sodium content of 100
ppm or less, and have completed the present invention.
For example, Na contained in the surface or in the interior
of the hydrotalcite has a large effect on the occurrence of die
drool to be produced when using the hydrotalcite as a neutralizer
of an acid catalyst residue in a polyolef in resin or a copolymer
thereof obtained by polymerization using an acid catalyst, or
on coloring (yellowing) due to the deterioration of resin in
extrusion in preparing pellets. Therefore, it is possible to
decrease the die drool and the coloring (yellowing) significantly
by reducing the sodium content in the hydrotalcite to a level
of 100 ppm or less. That is, when using the hydrotalcite of
the present invention as a neutral izer of an acid catalyst residue
in a polyolefin resin or a copolymer thereof obtained by
polymerization using an acid catalyst, the occurrence of die
drool can be prevented without reducing an effect of neutralizing
resin, and the coloring (yellowing) in extrusion in preparing
pellets can also be prevented. Thus, it is possible to attain
an advantage that an amount of expensive additives, such as an
antioxidant, to be added can be reduced.
Also when the conventional hydrotalcite is added as a
thermal insula ting material of a polyolefin film for agricultural
uses, the film becomes white due to sweat through condensation
on the surface of film or sweat from rainwater, or prolonged
contact with water causes the film to whiten and the white
discolorationbywater, which inhibits the transmissionof light,
occurs. It has become clear that Na contained in the surface
or in the interior of the hydrotalcite has a large effect on
this white discoloration by water. Accordingly, the white
discoloration by water can be reduced significantly by reducing
the sodium content in the hydrotalcite to a level of 100 ppm
or less . That is, when the hydrotalcite of the present invention
is added to apolyolef in film for agricultural uses for the purpose
of improving a thermal insulating property, the occurrence of
the white discoloration by water can be prevented.
The white discoloration by water arises also when the
conventional hydrotalcite is used as a stabilizer for a vinyl
chloride resin, but these phenomena are improved significantly
in a vinyl chloride resin in which the hydrotalcite of the present
invention is used as a stabilizer. The white discoloration by
water can be acceleratingly tested and evaluated by a hot water
whitening test in which a film is immersed in hot water.
And, the present inventors have found that Na contained
in the surface or in the interior of the hydrotalcite has a large
effect on the blooming to the surface of a film arising when
the conventional hydrotalcite is used as a stabilizer for a vinyl
chloride resin, and the blooming can be improved significantly
by reducing the sodium content in the hydrotalcite to a level
of 100 ppm or less . That is, when the hydrotalcite of the present
invention is used as a stabilizer for a vinyl chloride resin,
the occurrence of the blooming can be prevented and the white
discoloration by water can be prevented.
And, the present inventors have found that Na contained
in the surface or in the interior of the hydrotalcite has a large
effect on the problem of the reduction of electric resistance
(volume resistivity = VR) arising when the conventional
hydrotalcite is used as a Ca/Zn stabilizer of a vinyl chloride
resin for covering wires, and the reduction of electric
resistance can be improved by reducing the sodium content in
the hydrotalcite to a level of 100 ppm or less. That is, when
the hydrotalcite of the present invention is used as a stabilizer
of a vinyl chloride resin for covering wires, the reduction of
electric resistance (volume resistivity = VR) can be prevented.
Further, it has been found that the hydrotalcite having
a sodium content of 100 ppm or less can improve the transparency
of a film when films for agricultural uses is produced using
a synthetic resin composition containing the above hydrotalcite
and a synthetic resin.
The hydrotalcite of the present invention is expressed
by the above-mentioned formula (1) and has a sodium content of
100 ppm or less. When the sodium content is more than 100 ppm,
it is not possible to sufficiently improve the above-mentioned
white discoloration by water, blooming, electric resistance,
die drool and coloring (yellowing). The content of Na is
preferably 95 ppm or less and more preferably 90 ppm or less.
In the above formula (1), anions having a valence of n,
expressedbyAn~, include C104", S042" andC032", etc. Among others,
C032~ is preferred. In the above formula (1), x satisfies 0.5
And, in the above formula (1), z satisfies 0.1 preferably satisfies 0 . 2 (1) , m satisfies 0 The above hydrotalcite particles preferably have an
average secondary particle diameter of 2 urn or less. In this
case, since most of the hydrotalcite particles are primary
particles and not agglomerates of primary particles, thermal
stability and mechanical strength can be improved. The
hydrotalcite particles preferably have an average secondary
particle diameter of 0.4 to 1.0 urn. Incidentally, the above
average secondary particle diameter is a value measured by the
laser diffraction scattering method.
The above hydrotalcite preferably has a specific surface
area of 1 to 40 m2/g. Thereby, thermal stability and mechanical
strength can be improved. This specific surface area is more
preferably 5 to 20 m2/g. Incidentally, a value of the above
specific surface area is measured by the BET method.
The above hydrotalcite may have coating layer formed by
surface treatment. Kinds of the coating layer and methods of
surface treatment are not particularly limited.
The hydrotalcite of the present invention may be one
produced by any method of producing as long as it satisfies the
above properties, and for example, hydrotalcite obtained by a
hydrothermal synthesis at a temperature of 120 to 250°C can be
given. Since hydrotalcite having a relatively large particle
size can be obtained by the above method, hydrotalcite particles
can be dispersed well in the synthetic resin composition
containing the hydrotalcite and the synthetic resin. The good
dispersivity is effective at improving the above-mentioned white
discolorationby water, blooming, electric resistance, die drool
and coloring (yellowing). The conditions other than
temperature in the above hydrothermal synthesis is not
particularly limited and for example, conditions of pressure
0.1 to 4 MPa, a synthesis time 1 to 12 hours can be employed.
Of methods of producing hydrotalcite through the above
hydrothermal synthesis, a method of producing hydrotalcite,
comprising the step (I) of obtaining hydrotalcite slurry using
magnesium sulfate as a magnesium source and the step (III) of
washing with water is preferred. Such a method is particularly
preferred in that the sodium content in the hydrotalcite can
be reduced efficiently.
That is, by using magnesium sulfate as a magnesium source
in the above step (I), it is possible to conduct washing with
water in the step (III) efficiently and to reduce Na efficiently.
When the hydrotalcite slurry is prepared by a hydrothermal
synthesis using magnesium chloride as a magnesium source like
a conventional method and using zinc sulfate, aluminum sulfate,
sodium hydroxide and sodium carbonate as other components, a
large amount of NaCl is produced as a by-product. Since this
NaCl does not have high solubility in water and the temperature
dependency of the solubility is low, the solubility in water
does not become so high even in elevated temperatures in the
hydrothermal synthesis. Thus, an amount of NaCl absorbed in
particles of NaCl produced by a reaction is relatively large
and this absorbedNaCl is hard to be removed through simple washing
with water. Therefore, there may be cases where the sodium
content in the hydrotalcite cannot be adequately reduced or
number of the steps of washing with water becomes necessary.
On the other hand, in the above step (I), when the
hydrotalcite slurry is prepared by a hydro thermal synthesis using
magnesium sulfate as a magnesium source and using zinc sulfate,
aluminum sulfate, sodium hydroxide and sodium carbonate as an
example of other components, Na2S04 is produced as a by-product.
Na2S04 has higher solubility in water than NaCl and the temperature
dependency of its solubility is high. Thus, Na2SC>4 becomes apt
to dissolve in water in elevated temperatures in the hydrothermal
synthesis, and an amount of Na2S04 absorbed in the hydrotalcite
particles is relatively small. Therefore, the removal of Na2S04
adhering to the surfaces of the hydrotalcite particles in the
step of washing with water allows the amount of Na to easily
decrease.
As described above, in the conventional methods of
producing hydrotalcite, since magnesium chloride was used as
a magnesium source, Na ions were apt to be absorbed in the
hydrotalcite particles and were hard to be removed efficiently
through washing with water. And so, the sodium content in the
hydrotalcite commonly commercialized became 120 to 300 ppm.
Therefore, the hydrotalcite of the present invention can
be more efficiently produced by using a method of producing
hydrotalcite, which comprises the above step (I) and the above
step (III). The hydrotalcite obtained by such a method can
sufficiently improve the above-mentioned white discoloration
by water, blooming, electric resistance, die drool and coloring
(yellowing). The method of producing hydrotalcite like this
also constitutes the present invention.
In the method of producing hydrotalcite of the present
invention, the above step (I) can be carried out, for example,
by mixing magnesium sulfate, zinc sulfate, aluminum sulfate,
sodium hydroxide and sodium carbonate and performing the
hydrothermal synthesis . Amethod of reacting magnesium sulfate,
zinc sulfate, aluminum sulfate, sodium hydroxide and sodium
carbonate in the above step (I) can be performed using publicly
known methods, but it is preferred to perform the hydrothermal
synthesis by mixing an aqueous solution (a) of magnesium sulfate,
zinc sulfate and aluminum sulfate, dissolved respectively, and
an aqueous solution (b) of sodium hydroxide and sodium carbonate,
dissolved respectively. By thus carrying out the step (I), the
hydrotalcite particles can be produced.
The above aqueous solution (a) can be obtained by
dissolving magnesium sulfate, zinc sulfate and aluminum sulfate
in water by a common method. In this case, any of a method of
simultaneously dissolving magnesium sulfate, zinc sulfate and
aluminum sulfate in water, and a method of dissolving any one
compound in water in advance, adding the other compounds to this
solution and dissolving the mixture may be employed. And, the
above aqueous solution (a) can also be obtained by mixing an
aqueous solution obtained by dissolving magnesium sulfate in
water and respective aqueous solutions obtained by dissolving
zinc sulfate and aluminum sulfate separately in water. In this
case, in a method of mixing the aqueous solution of magnesium
sulfate, the aqueous solution of zinc sulfate and the aqueous
solution of aluminum sulfate, these aqueous solutions may be
mixed in any order. In the above aqueous solution (a), the
proportions of the above magnesium sulfate, the above zinc
sulfate and the above aluminum sulfate to be mixed can be
appropriately selected so as to satisfy the conditions in the
above formula (1).
The above aqueous solution (b) can be obtained by
dissolving sodium hydroxide and sodium carbonate in water by
a publicly known method. In this case, any of a method of
simultaneously dissolving sodium hydroxide and sodium carbonate
in water, and a method of dissolving any one compound in water
in advance, and further adding the other compound to this solution
and dissolving the mixture may be employed. And, the above
aqueous solution (b) can also be obtained by mixing an aqueous
solution obtained by dissolving sodium hydroxide in water and
an aqueous solution obtained by dissolving sodium carbonate in
water. In this case, there can be employed any of a method of
adding the aqueous solution of sodium hydroxide to the aqueous
solution of sodium carbonate and a method of adding the aqueous
solution of sodium carbonate to the aqueous solution of sodium
hydroxide.
In the above aqueous solution (b) , the amounts of the above
sodium hydroxide and the above sodium carbonate to be mixed may
be appropriately selected so as to be able to obtain the
hydrotalcite expressed by the above formula. And, in the above
aqueous solution (b) , it is possible to appropriately replace
An~ in the above formula (1) with S042" by adjusting the amount
of sodium hydroxide to be mixed, or a part or all of An~ in the
above formula (1) with C104" by changing a part or all of the
above sodium carbonate to sodium hypochlorite.
In the above step (I) , a method of mixing the above aqueous
solution (a) and the above aqueous solution (b) is not
particularly limited as long as it is a method by which an
ingredient in the solution (a) and an ingredient in the solution
(b) can be mixed, and the publicly known method can be used.
Among others, a method of simultaneously charging the above
aqueous solution (a) and the above aqueous solution (b) into
a container for a reaction is preferred. Thereby, the
hydrotalcite slurry can be produced efficiently in the
hydrothermal synthesis. In addition, when charging the above
aqueous solution (b) into a container for a reaction, the aqueous
solution of sodium hydroxide and the aqueous solution of sodium
carbonate may be charged separately.
The above step (I) can be carried out by applying the
publicly known hydrothermal synthesis method after mixing the
above aqueous solution (a) and the above aqueous solution (b) .
As the publicly known hydrothermal synthesis method, there can
be given, for example, a method of pressurizing to synthesize
the hydrotalcite in an autoclave, a method of synthesizing the
hydrotalcite sequentially with an multistage autoclave and a
method of pressurizing to synthesize the hydrotalcite
continuously in a pipe.
Reaction conditions of the above hydrothermal synthesis
is not particularly limited as long as it is the conditions under
which the hydrotalcite expressed by the above formula (1) can
be prepared and it can be appropriately determined, and the
hydrotalcite can be synthesized, for example, under the
conditions of temperature 120 to 250°C, pressure 0.1 to 4 MPa,
a synthesis time 1 to 12 hours.' When the levels of the conditions
are less than lower limits of the above range, there is a
possibility that the hydrotalcite expressedby the above formula
(1) cannot be obtained. When the levels of the conditions are
more than upper limits, the synthesis may become economically
disadvantageous. By carrying out the hydrothermal synthesis
under the conditions like these, hydrotalcite having a relatively
large particle size can be obtained. In the hydrotalcite having
a relatively large particle size, the force agglomeratingprimary
particles is small. Therefore, since hydrotalcite particles
can be dispersed well in a synthetic resin composition, it is
possible to improve the above-mentioned white discoloration by
water, blooming, electric resistance, die drool and coloring
(yellowing).
The above step (III) can be carried out by publicly known
methods by which slurry is washed with water . The publicly known
methods include, for example, a method of filtering and washing
with water, a method of repulping and washing with water
(resuspending and washing with water) and a method of removing
a water content from slurry by decantation or centrifugation
and washing with water but are not limited to these. And, at
the occasion of washing with water, ion-exchanged water or
purified water can be used in order to remove Na2S04 or NaCl
as an impurity efficiently, or hot water of 30°C or higher can
be used in order to enhance the solubility of a salt content
and wash with water efficiently.
The above method of producing hydrotalcite may comprise
a step of surface treating the hydrotalcite. The above surface
treating can be conducted by a method of conducting it in a step
(II) of surface treating, which is carried out between the step
(I) and the step (III), a method of conducting it in a step (IV-1)
of applying wet treatment to filtered cake after the step (III)
or a method of conducting it in a step (IV-2) of applying dry
treatment to a substance obtained by drying the filtered cake
and then milling this as required. The above surface treating
may be conducted in a plurality of steps of these steps. When
surface treating the hydrotalcite is carried out, it is favorable
in that the surface of the hydrotalcite particles is modified
from hydrophilic to lipophilic and the compatibility with a
synthetic resin can be improved.
The above surface treatment agent is not particularly
limited and includes, for example, higher fatty acids, silane-,
titanate- and aluminum-coupling agents, phosphate esters,
anionic surfactants, and esters of polyhydric alcohols and fatty
acids.
As the above higher fatty acids, there can be given, for
example, stearic acid, erucic acid, palmitic acid, lauric acid
and behenic acid, and alkali metal salts of the higher fatty
acids may be used.
As the above silane coupling agents, there can be given,
for example, vinylethoxysilane,
vinyl-tris(2-methoxy-ethoxy)silane, y-methacryloxypropyl
trimethoxysilane, y-aminopropyl trimethoxysilane,
P~(3,4-epoxycyclohexyl)ethyl trimethoxysilane,
y-glycidoxypropyl trimethoxysilane and y-mercaptopropyl
trimethoxysilane.
As the above titanate coupling agents, there can be given,
for example, isopropyltriisostearoyl titanate,
isopropyltris(dioctylpyrophosphate)titanate,
isopropyltri(N-aminoethyl-aminoethyl)titanate and
isopropyltridecylbenzenesulfonyl titanate.
As the above aluminum coupling agents, there can be given,
for example, acetoalkoxyaluminium diisopropylate.
As the above phosphate esters, there can be given, for
example, acid and alkali metal salts and amine salts of mono-
or di-esters of orthophosphoric acid and alcohols such as oleyl
alcohol and stearyl alcohol or mixtures thereof.
As the above anionic surfactants, there can be given, for
example, sulfuric ester salts of higher alcohols such as stearyl
alcohol and oleyl alcohol, sulfuric ester salts of polyethylene
glycol ethers, amide-bonded sulfuric ester salts, ester-bonded
sulfuric ester salts, amide-bonded sulfonates, ether-bonded
sulfonates, ether-bonded alkyl aryl sulfonates, ester-bonded
alkyl aryl sulfonates and amide-bonded alkyl aryl sulfonates.
As the above esters of polyhydric alcohols and fatty acids,
there can be given, for example, glycerin monostearate and
glycerin monooleate. It is preferred to use higher fatty acids
such as stearic acid, erucic acid, palmitic acid, lauric acid
and behenic acid among the above surface treatment agents.
Thereby, the sodium content in the hydrotalcite can be
efficiently reduced in washing with water of the step (III)-.
A method of surface treating in the above step (II) can
be performed by coating the surface of hydrotalcite particle
in the hydrotalcite slurry obtained in the above step (I) using
the above surface treatment agents . Amethod of surface treating
in the above step (IV-1) can be performed using a publicly known
wet or dry process after washing with water of the step (III) .
The surface treatment in the above step (II) can be
conducted by adding a liquid or emulsion of surface treatment
agent to a slurry of hydrotalcite particles and thoroughly mixing
these mechanically at a temperature of 100°C or lower. A wet
process in which surface treatment is performed in the above
step (IV-1) can also be performed by applying the same procedure
as in the above step (II) to slurry or filtered cake.
The dry process in the above step (IV-2) can be performed
by adding a liquid, emulsion or solid surface treatment agent
to hydrotalcite particles while stirring the particles
thoroughly with a mixer such as a Henschel mixer and thoroughly
mixing these with or without application of heat.
In the above surface coating, the amount of the surface
treatment agent added can be appropriately established but is
preferably 10 parts by weight or less based on 100 parts by weight
of the above hydrotalcite particles.
In the above method of producing hydrotalcite, the above
step (III) is a step of washing with water the hydrotalcite slurry
obtained, by performing the above step (I), and the above step
(II) as required. By performing the above step (III), it is
possible to reduce the sodium content in the hydrotalcite
expressed by the above formula (1) to a level of 100 ppm or less.
Since in the step (III) in the above method of producing
hydrotalcite, the hydrotalcite slurry containing Na2S04 instead
of NaCl as an impurity is washed with water, it is possible to
wash with water very efficiently.
The present invention also relates to a synthetic resin
composition containing the above-mentioned hydrotalcite of the
present invention and the synthetic resin. For example, when
a synthetic resin composition formed by adding the above
hydrotalcite to a polyolefin resin is used as a polyolefin film
for agricultural uses, the white discoloration by water in the
film can be prevented. And, when a synthetic resin composition
formed by adding the above hydrotalcite to a vinyl chloride resin
is used, the blooming to the surface of a vinyl chloride resin
film can be inhibited. And, when hydrotalcite is used as a heat
stabilizer (particularly a calcium/zinc stabilizer of resin for
covering wires) of a vinyl chloride resin, Na existing in the
hydrotalcite unfavorably causes the reduction of electric
resistance (volume resistivity = VR) as a covering material of
wires, but the hydrotalcite described above can prevent the
occurrence of the reduction of electric resistance like this
since it has a sodium content of 100 ppm or less. Further, when
the hydrotalcite is added as a neutralizer of an acid catalyst
residue in a polyolefin resin or a copolymer thereof, the
occurrence of die drool can be inhibited and the coloring
(yellowing) in extrusion in preparing pellets can also be
inhibited.
The above synthetic resin may be one which is generally
used for molded articles or film applications and includes, for
example, a thermoplastic synthetic resin.
As the above synthetic resin, there can be given
thermoplastic synthetic resins which are polymers or copolymers
of olefins having 2 to 8 carbon atoms (oc-olefins) such as
polyethylene, polypropylene, ethylene-propylene copolymer,
polybutene and poly(4-methylpentene-l), copolymers of these
olefins with dienes, ethylene-acrylate copolymer, polystyrene,
ABS resin, AAS resin, AS resin, MBS resin, ethylene-vinyl
chloride copolymer, ethylene-vinyl acetate copolymer,
ethylene-vinyl chloride-vinyl acetate graft polymer,
vinylidene chloride, polyvinyl chloride, chlorinated
polyethylene, chlorinated polypropylene, vinyl
chloride-propylene copolymer, vinyl acetate resin, phenoxy
resin, polyacetals, polyamides, polyimides, polycarbonates,
polysulfones, polyphenylene oxide, polyphenylene sulfide,
polyethylene terephthalate, polybutylene terephthalate and
methacrylic resins.
Among others, polyolefin resins, copolymers thereof and
halogen-containing resins thereof are preferred from the
viewpoint of heat deterioration prevention and mechanical
strength retaining characteristics by the hydrotalcite.
Specifically, there can be given polypropylene resins such as
polypropylene homopolymer and ethylene-propylene copolymer;
polyethylene resins such as high-density polyethylene,
low-density polyethylene, straight chain low-density
polyethylene, ultra low-density polyethylene, EVA (ethylene
vinyl acetate resin), EEA (ethylene ethyl acrylate resin), EMA
(ethylene-methyl acrylate copolymer resin), EAA
(ethylene-acrylic acid copolymer resin) and ultra high molecular
weight polyethylene; andpolymers orcopolymers of olefins having
2 to 6 carbon atoms (a-ethylene) such as polybutene and
poly(4-methylpentene-l). Polyethylene, polypropylene/
polybutene, poly(4-methylpentene-l) or copolymers thereof are
more preferred. And, as the above synthetic resin, vinyl
chloride or a copolymer thereof can also be given.
Further, as the above synthetic resin, there can be given
thermosetting resins such as epoxy resins, phenolic resins,
melamine resins, unsaturated polyester resins, alkyd resins and
urea resins, and synthetic rubber such as EPDM, butyl rubber,
isoprene rubber, SBR, NBR and chlorosulfonated polyethylene.
These synthetic resins may be used alone or in combination of
two or more species.
In the above synthetic resin composition, the content of
the above hydrotalcite is preferably 0.01 to 20 parts by weight
based on 100 parts by weight of the synthetic resin in the above
synthetic resin composition. When the content is less than 0 . 01
parts by weight, an effect of adding the hydrotalcite may not
be recognized. When it is more than 20 parts by weight, the
above-mentioned white discoloration by water, blooming,
reduction in electric resistance, die drool and coloring
(yellowing) may arise. It is more preferably 0.03 to 15 parts
by weight.
In the above synthetic resin composition, when the above
synthetic resin is a vinyl chloride resin, the hydrotalcite in
the above synthetic resin composition (a vinyl chloride resin
composition) can function as a stabilizer for a vinyl chloride
resin. In this case, if the sodium content in the hydrotalcite
is 100 ppm or less, the blooming to the surface of a film can
beprevented. And, whenhydrotalcite is usedas aheat stabilizer
(particularly a calcium/zinc stabilizer of resin for covering
wires) of a vinyl chloride resin, Na existing in the hydrotalcite
unfavorably causes the reduction of electric resistance (volume
resistivity = VR) as a covering material of wires, but since
the hydrotalcite described above has a sodium content as low
as 100 ppm or less, it is possible to prevent the occurrence
of the reduction in electric resistance like this.
In the above synthetic resin composition, when the above
synthetic resin is a vinyl chloride resin, the content of the
above hydrotalcite is preferably 0.1 to 5 parts by weight based
on 100 parts by weight of the vinyl chloride resin in the above
synthetic resin composition (a vinyl chloride resin composition)
When the content is less than 0 .1 parts by weight, the hydrotalcite
may not adequately function as a stabilizer for a vinyl chloride
resin. When it is more than 5 parts by weight, the blooming
may arise in a film obtained using the vinyl chloride resin
composition. It is more preferably 0.15 to 3 parts by weight.
In the above synthetic resin composition, when the above
synthetic resin is a polyolefin resin or a copolymer thereof
like the above, the hydrotalcite in the above synthetic resin
composition (a composition of a polyolefin resin or a copolymer
thereof) can function as a neutralizer of an acid catalyst residue
in the polyolefin resin or the copolymer thereof obtained by
polymerization using an acid catalyst. In this case, since the
sodium content in the hydrotalcite is as low as 100 ppm or less,
die drool, or coloring (yellowing) due to the deterioration of
resin in extrusion in preparing pellets can be prevented.
In the above synthetic resin composition, when the above
synthetic resin is a polyolefin resin or a copolymer thereof,
the content of the above hydrotalcite is preferably 0.01 to 15
parts by weight based on 100 parts by weight of the polyolefin
resin or the copolymer thereof in the above synthetic resin
composition (a composition of a polyolefin resin or a copolymer
thereof) . When the content is less than 0.01 parts by weight,
the hydrotalcite may not adequately function as a neutralizer
of an acid catalyst residue. When it is more than 15 parts by
weight, it is economically disadvantageous. It is more
preferably 0.02 to 0.15 parts by weight as a neutralizer of an
acid catalyst residue. And, when the hydrotalcite is used as
a thermal insulating material of a polyolefin film for
agricultural uses, the hydrotalcite content is more preferably
0.5 to 15 parts by weight.
The above synthetic resin composition may contain other
additives in addition to the above components. The above other
additives include, for example, an antioxidant, an ultraviolet
screening agent, an antistatic agent, pigment, a foaming agent,
aplasticizer, filler, a reinforcement, an organic halogen flame
retardant, a crosslinking agent, an optical stabilizer, an
ultraviolet absorber, a lubricant, other inorganic and organic
heat stabilizers and the like.
Amethodof producing the above synthetic resin composition
is not particularly limited and for example, a method of mixing
the above-mentioned hydrotalcite expressed by the above formula
(1) and having a sodium content of 100 ppm or less into a synthetic
resin as uniformly as possible together with or separately from
other additives may be employed. Mixing can be carried out by
publicly known methods of mixing, and a method of mixing, for
example, with a ribbon blender, a high-speed mixer, a kneader,
a pelletizer or an extruder, and a method of adding a suspension
of a resin additive comprising hydrotalcite as an effective
ingredient to a post-polymerization slurry and stirring and
drying the mixture can be given.
Since the above synthetic resin composition is expressed
by the above formula (1) and has a sodium content of 100 ppm
or less, it becomes free of the detrimental effects of die drool
or coloring (yellowing) due to the deterioration of resin in
extrusion in preparing pellets and can be suitably used as a
thermal insula ting material of apolyolef in film for agricultural
uses, a stabilizer for a vinyl chloride resin and a neutralizer
of an acid catalyst residue in a polyolefin resin or a copolymer
thereof obtained by polymerization using an acid catalyst.
Therefore, the above synthetic resin composition can be suitably
used for films for agricultural uses, a stabilizer for a vinyl
chloride resin and a neutralizer of an acid catalyst residue.
The hydrotalcite of the present invention is expressed
by the above formula (1) and has a sodium content of 100 ppm
or less and is used as a resin additive. Therefore, when the
above hydrotalcite is used as a thermal insulating material of
apolyolef in f ilm for agricultural uses, the white discoloration
by water can be prevented. And, when the hydrotalcite of the
present invention is used as a stabilizer for a vinyl chloride
resin, the blooming to the surface of a film can be inhibited.
Also, when it is used as a stabilizer of a vinyl chloride resin
for covering wires, the reduction of electric resistance (volume
resistivity = VR) can be prevented. Further, when the
hydrotalcite is used as a neutralizer of an acid catalyst residue
contained in a polyolef in resin or a copolymer thereof obtained
by polymerization using an acid catalyst, the occurrence of die
drool can be inhibited and the occurrence of coloring (yellowing)
in extrusion in preparing pellets can be inhibited. Accordingly,
the above hydrotalcite can be suitably employed as a resin
additive for various synthetic resins.
EFFECTS OF THE INVENTION
Since the hydrotalcite of the present invention has a
sodium content of 100 ppm or less and provides effects of
preventing the white discoloration by water, inhibiting the
blooming, preventing the reduction in electric resistance
(volume resistivity = VR) , and inhibiting the occurrences of
die drool and coloring (yellowing) in extrusion in preparing
pellets, it can be suitably employed as a resin additive for
various synthetic resins. Thus, the synthetic resin
composition containing the above hydrotalcite and the synthetic
resin can be suitably used in films for agricultural uses, which
are used for houses or tunnels in protected horticulture, such
as a polyolefin film for agricultural uses and a vinyl chloride
resin film.
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, the present invention will be described in
more detail by way of examples, but the present invention is
not limited to these examples. In addition, "part(s)" and "%"
refer to "part(s) by weight" and "weight %", respectively, in
Examples, unless otherwise specified.
Example 1
Preparation of hydrotalcite
Water 400 ml was put in a 3 liter reactor, and to this,
800 ml of a mixed aqueous solution (Mg2+ concentration 33.0 g/1,
Al3+ concentration 17.0 g/1) of magnesium sulfate salt and
aluminum sulfate salt and 800 ml of a mixed aqueous solution
(NaOH concentration 166.2 g/1, Na2C03 concentration 170 g/1)
of sodium hydroxide and sodium carbonate were added
simultaneously while stirring and then the hydrothermal
synthesis was carried out at 200°C for 4 hours. The resulting
hydrotalcite slurry was kept at 95°C and surface treated by adding
5 g of stearic acid. Next, after filtration of the slurry,
filtered cake was washed with 10 1 of water of 35°C, and the
resulting cake washed with water was dried at 100°C for 24 hours
and milled to obtain hydrotalcite. The obtained hydrotalcite
had a Na content of 47 ppm and a Fe content of 24 ppm.
Example 2
Preparation of hydrotalcite
Water 400 ml was put in a 3 liter reactor, and to this,
800 ml of a mixed aqueous solution (Mg2+ concentration 33.0 g/1,
Al3+ concentration 17.0 g/1) of magnesium sulfate salt and
aluminum sulfate salt and 800 ml of a mixed aqueous solution
(NaOH concentration 166.2 g/1, Na2C03 concentration 170 g/1)
of sodium hydroxide and sodium carbonate were added
simultaneously while stirring and the hydrothermal synthesis
was carried out at 200°C for 4 hours . The resulting hydrotalcite
slurry was kept at 95°C and surface treated by adding 100 ml
of a 50 g/1 aqueous solutionof sodiumstearate . Next, filtration
and washing with water were carried out in the same manner as
in Example 1, and the resulting cake washed with water was dried
at 100°C for 24 hours and milled to obtain hydrotalcite. The
obtained hydrotalcite had a Na content of 75 ppm and a Fe content
of 33 ppm.
Comparative Example 1
Preparation of hydrotalcite
Water 400 ml was put in a 3 liter reactor, and to this,
800 ml of a mixed aqueous solution (Mg^+ concentration 33.0 g/1,
Al3+ concentration 17.0 g/1) of magnesium chloride salt and
aluminum sulfate salt and 800 ml of a mixed aqueous solution
(NaOH concentration 166.2 g/1, Na2C03 concentration 170 g/1)
of sodium hydroxide and sodium carbonate were added
simultaneously while stirring and the hydrothermal synthesis
was carried out at 200°C for 4 hours . The resulting hydrotalcite
slurry was kept at 95°C and surface treated by adding 100 ml
of a 50 g/1 aqueous solutionof sodium stearate . Next, filtration
and washing with water were carried out in the same manner as
in Example 1, and the resulting cake washed with water was dried
at 100°C for 24 hours and milled to obtain hydrotalcite. The
obtained hydrotalcite had a Na content of 290 ppm and a Fe content
of 50 ppm.
Example 3
Preparation of hydrotalcite
Water 400 ml was put in a 3 liter reactor, and to this,
800 ml of a mixed aqueous solution {Hqz+ concentration 33.0 g/1,
Al3+ concentration 17.0 g/1) of magnesium chloride salt and
aluminum sulfate salt and 800 ml of a mixed aqueous solution
(NaOH concentration 166.2 g/1, Na2C03 concentration 170 g/1)
of sodium hydroxide and sodium carbonate were added
simultaneously while stirring and the hydrothermal synthesis
was carried out at 200°C for 4 hours . The resulting hydrotalcite
slurry was kept at 95°C and surface treated by adding 100 ml
of a 50 g/1 aqueous solution of sodium stearate. In order to
reduce a Na content, after filtration and washing with water
were carried out in the same manner as in Example 1, the filtered
hydrotalcite was repulped with 2 liter of ion-exchanged water
of 35°C and then filtered. Then, filteredhydrotalcite was dried
at 100°C for 24 hours and milled to obtain hydrotalcite. The
obtained hydrotalcite had a Na content of 87 ppm and a Fe content
of 50 ppm.
Example 4
Preparation of hydrotalcite
Water 400 ml was put in a 3 liter reactor, and to this,
800 ml of a mixed aqueous solution (Mg2+ concentration 28.9 g/1,
Znz+ concentration 11.0 g/1, Al3+ concentration 17.0 g/1) of
magnesium sulfate salt, aluminum sulfate salt and zinc sulfate
and 800 ml of a mixed aqueous solution (NaOH concentration 166.2
g/1, Na2C03 concentration 170 g/1) of sodium hydroxide and sodium
carbonate were added simultaneously while stirring and then the
hydrothermal synthesis was carried out at 200°C for 4 hours.
The resulting hydrotalcite slurry was kept at 95°C and surface
treated by adding 5 g of stearic acid. Next, filtration and
washing with water were carried out in the same manner as in
Example 1, and the resulting cake washed with water was dried
at 100°C for 24 hours and milled to obtain hydrotalcite. The
obtained hydrotalcite had a Na content of 14 ppm and a Fe content
of 12 ppm.
In the method of producing in Example 3, since magnesium
chloride was used as a raw material, repulping and washing with
water is required in order to reduce the sodium content in the
hydrotalcite to a level of 100 ppm or less. From this, it is
shown that the method using magnesium chloride as a raw material
has a lower efficiency of washing with water than the method
(Examples 1 and 2) using magnesium sulfate as a raw material.
Incidentally, the Na and Fe contents in the synthesized
hydrotalcite described above were measured by the following
methods.
(Method of analyzing Na)
About 1 g of the synthesized hydrotalcite was sampled and
to this, 30 ml of ether and 20 ml of nitric acid (1+10) were
added and shaken well to dissolve the sample completely, and
the resulting solution was left standing for 5 minutes and then
a portion of a water layer separated was taken and put in a beaker,
and this portion was gradually heated to purge dissolved ether.
After cooling this solution, the solution was filtered with a
5C filter paper and distilled water was added to make 100 ml
of a test liquid. This test liquid was analyzed with an atomic
absorption spectrophotometer (Z-800 producedby Hitachi, Ltd.) .
(Method of analyzing Fe)
As with the above-mentioned method of analyzing Na, a
prepared sample was analyzed with an atomic absorption
spectrophotometer (described above).
Examples 5 to 7, Comparative Examples 2 to 4
Preparation of polyolefin film for agricultural uses
Each film containing the hydrotalcite synthesized in
Example 1 was prepared as a thermal insulating material of a
polyolefin film for agricultural uses (Examples 5 to 7) . And,
each of films containing the hydrotalcite synthesized in
Comparative Example 1 was prepared (Comparative Examples 2 to
4) . Each film was produced by the following method.
Amaster batch was prepared in a formulation shown in Table
1 and then using the obtained master batch, LDPE (low density
polyethylene, MFR is 5 produced by UBE INDUSTRIES, LTD.,
polyethylene F522N) and the master batch were mixed in such a
way that the amounts of the hydrotalcites shown in Table 2 added
to the resin are 5.0, 7.5 and 10.0 parts by weight, and a film
with thickness of 100 urn was produced with a single screw extruder
(T die) . The transparency (haze value) , the white discoloration
by hot water and the appearance of a film of the obtained films
were evaluated by the following methods and the results of
evaluation are shown in Table 2.
(Transparency)
With respect to the film with thickness of 100 um, a haze
value was measured according to JIS K 7136 with a haze meter
produced by NIPPON DENSHOKU INDUSTRIES CO., LTD.
(White discoloration by hot water)
After the film with thickness of 100 urn was immersed for
24 hours in hot water of 40°C, it was taken out and dried for
10 minutes, and its haze value was measured with a haze meter.
(Appearance of film)
Each film with width of 10 cm and thickness of 100 um was
extruded with an extruder and rolled up with a winder, and when
an outer diameter of the roll of film reached 150 mm, a core
tube of the winder was replaced. The film rolled up on the core
tube was used for the appearance test of film and in this test,
each film was apposed and its appearance was visually observed.
In addition, it was observed that a film which has a large haze
value in the above-mentioned transparency evaluation and
therefore poor transparency was whitish or white in the
appearance, and defective dispersion of the hydro talcite emerges
remarkably in this film.
Table 1
LDPE (low density polyethylene, MFR is 24 produced by TOSOH
CORPORATION, Petrosen 202R: used for a master batch)
Stabiace PH-1010 (produced by Sakai Chemical Industry Co ., Ltd.,
phenolic antioxidant)
Stabiace P-2400 (produced by Sakai Chemical Industry Co ., Ltd.,
phosphorus antioxidant)
From Table 2, it has become clear that when the hydrotalcite,
in which the Na content contained in the surface or in the interior
of the hydrotalcite is 47 ppm, is used, the white discoloration
by hot water does not arise even though the amounts of the
hydrotalcites added are 5.0, 7.5 and 10.0 parts by weight. And,
these films have the excellent transparency and the appearance
of film.
Examples 8 to 11, Comparative Example 5
Stabilizer for vinyl chloride resin
The hydrotalcites synthesized in Examples 1 to 4 and
Comparative Example 1 were used as a stabilizer for a vinyl
chloride resin, and a mixture of a formulation shown in Table
3 was kneaded for five minutes with a 8 inch roll heated to 170°C
and a pressed sheet of 1.0 mm in thickness was produced under
the conditions of temperature 170°C, press time 10 minutes,
pressure 50 kg/cm2 with a press machine using a bared sheet of
0.3 mm in thickness.
The transparency (haze value) , the blooming (effusion of
powder), the thermal stability and the volume resistivity of
the obtained sheets were evaluated by the following methods and
the results of evaluation are shown in Table 3.
(Transparency)
With respect to the obtained sheets, a haze value was
measured according to JIS K 7136 with a haze meter (produced
by NIPPON DENSHOKU INDUSTRIES CO., LTD., NDH 2000).
(Blooming (effusion of powder))
The obtained sheet was immersed in hot water of 40°C, and
it was taken out 4 hours later and a state of effusion of powder
to the surface of the sheet was visually evaluated.
(Thermal stability)
The obtained sheet was put in a gear oven of 180°C, and
it was taken out every 10 minutes and the thermal stability was
investigated based on the quality of blackening of the sheet.
(Volume resistivity: VR)
Using the obtained sheet, a 14 cm square pressed sheet
of 1.0 mm in thickness was produced and stored in a desiccator
of 30°C, 60% RH for a day and the volume resistivity (Q-cm) was
measured according to JIS K 6723.
Table 3
PVC (vinyl chloride resin) produced by Shin Dai-Ichi Vinyl
Corporation, ZEST 1000Z
DOP (plasticizer) produced by Taoka Chemical Co., Ltd.
From Table 3, it has become clear that when the hydrotalcite,
in which the Na contents contained in the surface or in the interior
of the hydrotalcite are 47 ppm, 75 ppm and 14 ppm, are used,
these resins have the excellent transparency and the blooming
(effusion of powder) does not arise at the surface of the film.
And, these resins also have the excellent thermal stability and
the excellent volume resistivity.
Examples 12 to 13, Comparative Example 6
Neutralizer of polyolefin resin
The hydrotalcites synthesized in Examples 1 to 2 and
Comparative Example 1 were used as a neutralizer of an acid
catalyst residue in a polyolefin res in obtained by polymerization
using an acid catalyst, and a film with width of 10 cm and thickness
of 100 jim was obtained by extrusion with a extruder. And, by
conducting repeated extrusion at 200°C with a 30 mm single screw
extruder, a strandof about 4 mm in diameter was extruded, quenched
with water and then cut to obtain pellets.
Using the obtained films and pellets, the yellowness index
YI (heat resistance), the occurrence of die.drool and the
corrosiveness of an iron sheet were evaluated by the following
methods and the results of evaluation are shown in Table 4.
(Heat resistance (yellowness index YI) of resin)
The obtained films were overlaid and this overlaid film
was pressed with a hot press to prepare a pressed sheet of 1.0
mm in thickness. The yellowness index YI of the pressed sheet
was measured by a color difference meter (produced by NIPPON
DENSHOKU INDUSTRIES CO., LTD., SQ-2000).
(Occurrence of die drool)
When producing pellets, the presence or absence of stains
(die drool) adhering to a die in extruding repeatedly was visually
determined.
(Corrosiveness of iron sheet)
After the obtained film was bonded at 150°C to an iron
sheet in a state of being polished at the surface with a sand
paper, the entire iron sheet was put in a thermo-hygrostat of
50°C, 90% RH to accelerate the corrosiveness and the presence
or absence of corrosion was visually determined three days later.
Table 4
Polypropylene (produced by UBE INDUSTRIES, LTD., polyethylene
F522N)
Stabiace PH-1010 (produced by Sakai Chemical Industry Co ., Ltd.,
phenolic antioxidant)
Stabiace P-2400 (produced by Sakai Chemical Industry Co ., Ltd.,
phosphorus antioxidant)
From Table 4, it has become clear that when the hydrotalcite,
in which the Na contents contained in the surface or in the interior
of the hydrotalcite are 47 ppm and 75 ppm, are used, the die
drool is significantly reduced without reducing an effect of
neutralizing resin. And, it has become evident that an increase
in a yellowness index YI due to the degradation of resin can
be prevented. Further, these resins showed the excellent
results in the corrosiveness of an iron sheet. On the other
hand, it has become evident that when the hydrotalcite having
the Na contents of 290 ppm is used, the die drool tends to develop
and the heat resistance of the resin (yellowness index YI) becomes
bad when the resin is extruded repeatedly at 270°C with a single
screw extruder.
INDUSTRIAL APPLICABILITY
The hydrotalcite of the present invention can be suitably
used as a resin additive for various synthetic resins. And,
the synthetic resin composition containing the above
hydrotalcite and the synthetic resin can be suitably used as
a film for agricultural uses, which are used for houses or tunnels
in protected horticulture.
We claim:
1. A method of producing hydrotalcite of formula:
[(Mg)x(Zn) y] 1-z (AlZ(OH)2(An-)z/n•mH20,
wherein An~ represents an anion having a valence of n; x, y, z
and m are values which satisfy the following expressions,
0.5 m providing a slurry of hydrotalcite, wherein the hydrotalcite
slurry is obtained using magnesium sulfate as the
magnesium source; and
washing the slurry with water, wherein
said hydrotalcite slurry is obtained by combining
magnesium sulfate, aluminum sulfate, sodium hydroxide,
and sodium carbonate, and optionally zinc sulfate; and
subjecting the combination to a hydrothermal synthesis at
a temperature of 120° to 250°C;
and further wherein the hydrotalcite has a sodium content of
100 ppm or less and a specific surface area of 1 to 40
m2/g.
2. The method of producing the hydrotalcite as claimed in
claim 1, further comprising a surface treating step.
3. The method of producing the hydrotalcite as claimed in
claim 1, wherein the combining comprises combining (a), an
aqueous solution of magnesium sulfate, aluminum sulfate, and
optionally zinc sulfate, with (b), an aqueous solution of
sodium hydroxide and sodium carbonate.
4. The method of producing the hydrotalcite as claimed in
claim 1 wherein the combining comprises simultaneous changing
of the aqueous solutions to a vessel, with agitation, to
produce the hydtotalcite slurry.
5. The method of producing the hydrotalcite as claimed in
claim 1 wherein the washing step is selected from:
filtering and washing with water,
repulping and washing with water, and
separating water from the slurry by decantation or
centrifugation followed by washing of remaining solids
with water.


The invention discloses a method of producing hydrotalcite of
formula:
[(Mg)x(Zn) y] 1-z (AlZ(OH)2(An-)z/n•mH20,
wherein An- represents an anion having a valence of n; x, y, z
and m are values which satisfy the following expressions, 0.5
≤ x ≤ 1, 0 ≤ y ≤ 0.5, x+y = 1, 0.1 ≤ z ≤ 0.5, and 0 ≤ m the method comprising the steps of: providing a slurry of
hydrotalcite, wherein the hydrotalcite slurry is obtained
using magnesium sulfate as the magnesium source; and washing
the slurry with water, whereinsaid hydrotalcite slurry is
obtained by combining magnesium sulfate, aluminum sulfate,
sodium hydroxide, and sodium carbonate, and optionally zinc
sulfate; and subjecting the combination to a hydrothermal
synthesis at a temperature of 120° to 250°C; and further
wherein the hydrotalcite has a sodium content of 100 ppm or
less and a specific surface area of 1 to 40 m2/g.

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618-kolnp-2007-examination report.pdf

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Patent Number 248246
Indian Patent Application Number 618/KOLNP/2007
PG Journal Number 26/2011
Publication Date 01-Jul-2011
Grant Date 29-Jun-2011
Date of Filing 20-Feb-2007
Name of Patentee SAKAI CHEMICAL INDUSTRY CO. LTD.
Applicant Address 1-1-23, EBISUNOCHONISHI, SAKAI-SHI, OSAKA 5908502
Inventors:
# Inventor's Name Inventor's Address
1 TSUJIMOTO, HIDEO C/O. SAKAI CHEMICAL INDUSTRY CO., LTD. 5-1, EBIS UJIMACHO, SAKAI-SHI, OSAKA 5900985
2 KURATO, MASATO C/O SAKAI CHEMICAL INDUSTRY CO., LTD. 5-1, EBIS UJIMACHO, SAKAI-SHI, OSAKA 5900985
3 SUZUKI, MASAHIRO C/O SAKAI CHEMICAL INDUSTRY CO., LTD. 5-1, EBIS UJIMACHO, SAKAI-SHI, OSAKA 5900985
PCT International Classification Number C01F 7/00
PCT International Application Number PCT/JP2005/010864
PCT International Filing date 2005-06-14
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 2004-305644 2004-10-20 Japan