CA2060545C - Process for coloring building materials - Google Patents
Process for coloring building materials Download PDFInfo
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- CA2060545C CA2060545C CA002060545A CA2060545A CA2060545C CA 2060545 C CA2060545 C CA 2060545C CA 002060545 A CA002060545 A CA 002060545A CA 2060545 A CA2060545 A CA 2060545A CA 2060545 C CA2060545 C CA 2060545C
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- pigments
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- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09C—TREATMENT OF INORGANIC MATERIALS, OTHER THAN FIBROUS FILLERS, TO ENHANCE THEIR PIGMENTING OR FILLING PROPERTIES ; PREPARATION OF CARBON BLACK ; PREPARATION OF INORGANIC MATERIALS WHICH ARE NO SINGLE CHEMICAL COMPOUNDS AND WHICH ARE MAINLY USED AS PIGMENTS OR FILLERS
- C09C3/00—Treatment in general of inorganic materials, other than fibrous fillers, to enhance their pigmenting or filling properties
- C09C3/04—Physical treatment, e.g. grinding, treatment with ultrasonic vibrations
- C09C3/045—Agglomeration, granulation, pelleting
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B18/00—Use of agglomerated or waste materials or refuse as fillers for mortars, concrete or artificial stone; Treatment of agglomerated or waste materials or refuse, specially adapted to enhance their filling properties in mortars, concrete or artificial stone
- C04B18/02—Agglomerated materials, e.g. artificial aggregates
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2004/00—Particle morphology
- C01P2004/60—Particles characterised by their size
- C01P2004/61—Micrometer sized, i.e. from 1-100 micrometer
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01P—INDEXING SCHEME RELATING TO STRUCTURAL AND PHYSICAL ASPECTS OF SOLID INORGANIC COMPOUNDS
- C01P2006/00—Physical properties of inorganic compounds
- C01P2006/10—Solid density
Abstract
Colored building materials are produced by incorporating into the building materials inorganic pigments in the form of granulates which are free-flowing and not dust forming wherein the pigments are produced from spray dried granulates by after-granulating.
Description
2~~~~~.~
Process for coloring building materials The present invention relates to a process for coloring building materials with inorganic pigments in the form of granulates which are free flowing and not dust forming.
_BACKGROUND OF THE INVENTION
l0 den cement- and lime-bonded building materials such as plaster, lime brick, fibre cement parts or concrete blocks, in particular roof tiles, paving stones or promenade tiles, are to be colored, the coloring materials used are generally inorganic pigments. The pigments conventionally used in the building materials industry are iron oxides or iron hydroxides for red, black, brown or yellow, manganese oxides for black-brown, chromium oxides for green and titanium dioxides far white.
In addition, carbon blacks may be used as black pigments, nickel or chromium rutiles as yellow pigments, spinels containing cobalt as blue and green pigments, spinels containing copper as black pigments and mixed crystals of barium sulphate and barium manganate as blue pigments.
For coloring concrete materials, the pigments are generally used in powder form. When ground up as powders they have the advantage of being readily dispersible:
such pigment powders can be distributed completely homogeneously in concrete mixtures within a short time of up to a few minutes. The disadvantage of these fine Le A 28 094-Foreign Countries powders, however, is that they do not flow freely and in many cases cake together and form lumps when kept in storage. This renders accurate dosing difficult and another disadvantage of some powders is that they tend to form dust.
It is known that these disadvantages can be avoided in the pigmentation of concrete parts by using aqueous pigment suspensions instead of dry pigment powders. The use of such pastes or slurries containing 30 to 70% by weight of pigment, however, has only slowly become established as the additional water content may considerably increase the transport costs, depending on the distance between the place of manufacture and the building site. Moreover, not all concrete preparations are capable of absorbing the large quantity of water carried with the pigment.
The building materials industry has therefore far the most part continued to use dry pigment powders. The use of pigments in the form of microgranulates such as are commonly used in the plastics and lacquer industry has hitherto been prevented by the commonly held belief that granulates are not easily dispersible in concrete preparations. Pigment agglomerates which are not easily dispersible require substantially longer mixing times. In the short mixing times conventionally used in the manufacture of building materials, patches, streaks and nests of color occur on the surface of tl~e concrete due to imperfect pigment distribution. The intensity of color contained in the pigment cannot fully develop, with the result that larger quantities of pigment are required for obtaining a'given intensity of color in the concrete.
Pigment granulates consisting substantially of pigment and one or more binders which promote dispersion of the Le p. 28 094 2 ~~~~~~~.~9 pigment in the concrete are described in DE-C 3 619 363 for coloring concrete. The following are mentioned there as binders which function as dispersing auxiliaries in concrete: Alkyl benzene sulphonates, alkyl naphthalene sulphonates, lignin sulphonate, sulphated polyglycol ethers, melamine formaldehyde condensates, naphthalene formaldehyde condensates, gluconic acid, salts of low molecular weight, partially esterified styrene/maleic acid anhydride copolymers and copolymers of vinyl acetate and crotonic acid. The proportion of these in the pigment should preferably be from 2 to 6% by weight.
The above-mentioned dispersing auxiliaries act as liqueFiers in concrete mixtures. They influence the water-cement ratio and ha s an effect on the consistency of the concrete.
In the inorganic pigment itself, the added binders act as foreign organic substances. According to DE-A 2 950 156, the inorganic starting pigment has a resin content of at least 20%. Distribution of the granulates, in concrete is rendered very difficult by the resin contents of hydro-phobic agglomerates.
Pigments which are free-flowing and produce little dust can be produced according to DE-C 3 918 694 but the free flowing character and the amount of dust formation are not entirely satisfactory due to the high proportion of particles smaller than 100 ~.m.
It is an object of the present invention to provide free flowing, non-dust forming inorganic pigment granulates which are free from the above-described disadvantages of the state of the art for coloring building materials.
GRIEF DESCRIPTION OF THE INVENTION
Colored building materials are produced by incorporating into the building materials inorganic pigments in the form of granulates which are free-flowing and not dust forming Le A 28 Og~l 3 wherein the pigments are produced from :pray dried pigment granulates by after-granulating the spray dried pigment.
According to one aspect of the. present invention, there is provided a process for coloring building materials with inorganic pigments which comprises incorporating into said materials pigments in the form of granulates which are free-flowing and not dust forming wherein the pigment granulates are produced from spray dried granules by after-granulating.
According to another aspect o:E the present invention, there is provided a colored building material comprising inorganic pigments in the foam of granulates which are free-flowing and not dust forming, wherein the pigment granulates are produced from spray dried granules by after-granulating.
DETAILED DESCRIPTION
The problem encountered by the prior art was solved by a process for coloring building materials with inorganic pigments in the form of free-:Flowing, non-dust forming granulates, in which the pigment granulates were obtained from spray dried granules by after-granulating these for some time.
This process is the subject o.f the present invention. The granulates produced according to DE-C3 918 694 are suitable for the process according to the invention.
Particularly good results are obtained when the after-granulation is carried out for a period of from 5 minutes to 10 hours, preferably from 15 minutes to 2 hours.
It is surprisingly found that the granules do not break up under these conditions and the proportion of fine particles smaller than 100 ~cm is decreased and of particles larger than 100 ,um is increased.
The process according to the invention may advantageously be carried out at a temperature from the ambient temperature to 300°C. The after.-granulation is preferably carried out in drums, screws, rotary plates or similar apparatus. The after-granulated granules obtained are very free-flowing and produce substantially less dust than the granules put into the process.
In one embodiment of the prose ss according to the invention, the after-granulation is carried out without any additive. Under certain conditions, the effect obtained by the process according to the invention may be assisted by spraying a few percent of water over the granules during the after-granulation.
In another embodiment of the process according to the 4a invention, the granules are therefore sprayed with 0.5 to 5% by weight, preferably 1 to 3% by weight of water, based on the quantity of pigments, during the process of after-granulation.
It may be equally advantageous to spray the granules during the after-granulation with 0.5 to 5% by weight, preferably 1 to 3% by weight, based on the quantity of pigments, of aqueous solutions of salts of boron, aluminium, silicon, titanium, zinc and/or tin. This enables a further reduction in the content of fine particles smaller than 100 ,um to be obtained.
It is particularly suitable to use inorganic pigments selected from one or more of the group comprising titanium dioxide, iron oxide, chromium oxide, manganese oxide and zinc oxide. Iron oxide pigments are particularly pre ferred.
In another embodiment of the process according to the invention, the inorganic pigments are mixed phase pigments containing at least two rations selected from the rations of chromium, manganese, iron, cobalt, nickel, zinc, titanium, copper, aluminium, arsenic and antimony, and oxygen as counter-ion.
It has bean shown that the particle size of the granulates according to the invention should not exceed a particular value which depends on the pigment. This size depends primarily on the bulk density of the granulate, which in turn is a measure of the porosity of the particles. In the case of spray granulation; the porosity depends on the solids content of the pumpable starting suspension before drying, a value which may vary considerably in dependence upon the particle size and particle form of the pigment.
Le A 28 094 5 ~fl~~~~
The compacted bulk density defined in DIN 53 194 of August 1957 serves as measure of the bulk density. The pigment granulates according to the invention are distinguished by the fact that they do not disintegrate during deter-s urination of the compacted bulk density. The granulates according to the invention preferably have a compacted bulk density of from 0.5 to 2.5 g/cur3, most preferably from 0.8 to 1.5 g/cm3.
The average particle size of granulates particularly suitable for the process according to the invention is from 100 to 500 ~.m.
Pigment granulates having this particle size are powders which are stable in handling and freely pourable, do not form dust and are very suitable for coloring building materials. Contrary to the previously held opinion (DE-C
Process for coloring building materials The present invention relates to a process for coloring building materials with inorganic pigments in the form of granulates which are free flowing and not dust forming.
_BACKGROUND OF THE INVENTION
l0 den cement- and lime-bonded building materials such as plaster, lime brick, fibre cement parts or concrete blocks, in particular roof tiles, paving stones or promenade tiles, are to be colored, the coloring materials used are generally inorganic pigments. The pigments conventionally used in the building materials industry are iron oxides or iron hydroxides for red, black, brown or yellow, manganese oxides for black-brown, chromium oxides for green and titanium dioxides far white.
In addition, carbon blacks may be used as black pigments, nickel or chromium rutiles as yellow pigments, spinels containing cobalt as blue and green pigments, spinels containing copper as black pigments and mixed crystals of barium sulphate and barium manganate as blue pigments.
For coloring concrete materials, the pigments are generally used in powder form. When ground up as powders they have the advantage of being readily dispersible:
such pigment powders can be distributed completely homogeneously in concrete mixtures within a short time of up to a few minutes. The disadvantage of these fine Le A 28 094-Foreign Countries powders, however, is that they do not flow freely and in many cases cake together and form lumps when kept in storage. This renders accurate dosing difficult and another disadvantage of some powders is that they tend to form dust.
It is known that these disadvantages can be avoided in the pigmentation of concrete parts by using aqueous pigment suspensions instead of dry pigment powders. The use of such pastes or slurries containing 30 to 70% by weight of pigment, however, has only slowly become established as the additional water content may considerably increase the transport costs, depending on the distance between the place of manufacture and the building site. Moreover, not all concrete preparations are capable of absorbing the large quantity of water carried with the pigment.
The building materials industry has therefore far the most part continued to use dry pigment powders. The use of pigments in the form of microgranulates such as are commonly used in the plastics and lacquer industry has hitherto been prevented by the commonly held belief that granulates are not easily dispersible in concrete preparations. Pigment agglomerates which are not easily dispersible require substantially longer mixing times. In the short mixing times conventionally used in the manufacture of building materials, patches, streaks and nests of color occur on the surface of tl~e concrete due to imperfect pigment distribution. The intensity of color contained in the pigment cannot fully develop, with the result that larger quantities of pigment are required for obtaining a'given intensity of color in the concrete.
Pigment granulates consisting substantially of pigment and one or more binders which promote dispersion of the Le p. 28 094 2 ~~~~~~~.~9 pigment in the concrete are described in DE-C 3 619 363 for coloring concrete. The following are mentioned there as binders which function as dispersing auxiliaries in concrete: Alkyl benzene sulphonates, alkyl naphthalene sulphonates, lignin sulphonate, sulphated polyglycol ethers, melamine formaldehyde condensates, naphthalene formaldehyde condensates, gluconic acid, salts of low molecular weight, partially esterified styrene/maleic acid anhydride copolymers and copolymers of vinyl acetate and crotonic acid. The proportion of these in the pigment should preferably be from 2 to 6% by weight.
The above-mentioned dispersing auxiliaries act as liqueFiers in concrete mixtures. They influence the water-cement ratio and ha s an effect on the consistency of the concrete.
In the inorganic pigment itself, the added binders act as foreign organic substances. According to DE-A 2 950 156, the inorganic starting pigment has a resin content of at least 20%. Distribution of the granulates, in concrete is rendered very difficult by the resin contents of hydro-phobic agglomerates.
Pigments which are free-flowing and produce little dust can be produced according to DE-C 3 918 694 but the free flowing character and the amount of dust formation are not entirely satisfactory due to the high proportion of particles smaller than 100 ~.m.
It is an object of the present invention to provide free flowing, non-dust forming inorganic pigment granulates which are free from the above-described disadvantages of the state of the art for coloring building materials.
GRIEF DESCRIPTION OF THE INVENTION
Colored building materials are produced by incorporating into the building materials inorganic pigments in the form of granulates which are free-flowing and not dust forming Le A 28 Og~l 3 wherein the pigments are produced from :pray dried pigment granulates by after-granulating the spray dried pigment.
According to one aspect of the. present invention, there is provided a process for coloring building materials with inorganic pigments which comprises incorporating into said materials pigments in the form of granulates which are free-flowing and not dust forming wherein the pigment granulates are produced from spray dried granules by after-granulating.
According to another aspect o:E the present invention, there is provided a colored building material comprising inorganic pigments in the foam of granulates which are free-flowing and not dust forming, wherein the pigment granulates are produced from spray dried granules by after-granulating.
DETAILED DESCRIPTION
The problem encountered by the prior art was solved by a process for coloring building materials with inorganic pigments in the form of free-:Flowing, non-dust forming granulates, in which the pigment granulates were obtained from spray dried granules by after-granulating these for some time.
This process is the subject o.f the present invention. The granulates produced according to DE-C3 918 694 are suitable for the process according to the invention.
Particularly good results are obtained when the after-granulation is carried out for a period of from 5 minutes to 10 hours, preferably from 15 minutes to 2 hours.
It is surprisingly found that the granules do not break up under these conditions and the proportion of fine particles smaller than 100 ~cm is decreased and of particles larger than 100 ,um is increased.
The process according to the invention may advantageously be carried out at a temperature from the ambient temperature to 300°C. The after.-granulation is preferably carried out in drums, screws, rotary plates or similar apparatus. The after-granulated granules obtained are very free-flowing and produce substantially less dust than the granules put into the process.
In one embodiment of the prose ss according to the invention, the after-granulation is carried out without any additive. Under certain conditions, the effect obtained by the process according to the invention may be assisted by spraying a few percent of water over the granules during the after-granulation.
In another embodiment of the process according to the 4a invention, the granules are therefore sprayed with 0.5 to 5% by weight, preferably 1 to 3% by weight of water, based on the quantity of pigments, during the process of after-granulation.
It may be equally advantageous to spray the granules during the after-granulation with 0.5 to 5% by weight, preferably 1 to 3% by weight, based on the quantity of pigments, of aqueous solutions of salts of boron, aluminium, silicon, titanium, zinc and/or tin. This enables a further reduction in the content of fine particles smaller than 100 ,um to be obtained.
It is particularly suitable to use inorganic pigments selected from one or more of the group comprising titanium dioxide, iron oxide, chromium oxide, manganese oxide and zinc oxide. Iron oxide pigments are particularly pre ferred.
In another embodiment of the process according to the invention, the inorganic pigments are mixed phase pigments containing at least two rations selected from the rations of chromium, manganese, iron, cobalt, nickel, zinc, titanium, copper, aluminium, arsenic and antimony, and oxygen as counter-ion.
It has bean shown that the particle size of the granulates according to the invention should not exceed a particular value which depends on the pigment. This size depends primarily on the bulk density of the granulate, which in turn is a measure of the porosity of the particles. In the case of spray granulation; the porosity depends on the solids content of the pumpable starting suspension before drying, a value which may vary considerably in dependence upon the particle size and particle form of the pigment.
Le A 28 094 5 ~fl~~~~
The compacted bulk density defined in DIN 53 194 of August 1957 serves as measure of the bulk density. The pigment granulates according to the invention are distinguished by the fact that they do not disintegrate during deter-s urination of the compacted bulk density. The granulates according to the invention preferably have a compacted bulk density of from 0.5 to 2.5 g/cur3, most preferably from 0.8 to 1.5 g/cm3.
The average particle size of granulates particularly suitable for the process according to the invention is from 100 to 500 ~.m.
Pigment granulates having this particle size are powders which are stable in handling and freely pourable, do not form dust and are very suitable for coloring building materials. Contrary to the previously held opinion (DE-C
3 619 3639), the shear forces acting on the granulates in concrete preparations axe sufficient for complete dispersion of the pigment during the mixing cycle.
Particularly good results are obtained with iron oxide pigments.
The compacted bulk density of the granulates may vary according to the pigment, the type and quantity of additive and the water content of the suspension. If the compacted bulk density is too low, the granulates will be insufficiently stable, whereas granulates with high compacted bulk densities are difficult to disperse. The iron oxide black granulates according to the invention preferably have compacted bulk densities of from 0.8 to 1.4 g/cur3.
The process accarding to the invention will now be Le A 28 094 6 explained more fully with the aid of the following Examples but must not be regarded as limited by the Examples.
The dispersibility in concrete was tested by measuring the color intensity of prisms produced with white cement conforming to the following data: Cement . sharp sand ratio 1 : 4, water-cement value 0.35, level of pigmenta-tion 1.2%, based on the cement, mixer used: RK Toni Technik, Berlin, 5 1 mixing dish, Model 1551, speed of rotation 140 revs/min (Batch : 500 g of cement). Four samples of mixture (300 g) were removed after 30, 40, 50, 60 , 70 and 80 seconds arid used to produce sample bodies (5 x 10 x 2.5 cm) under pressure (32.5 N/mm2) . Hardening of the samples: 24 hours at 30°G and 95% relative humidity followed by drying at 50°C for 24 hours. Colour data measured with Hunterlab apparatus: 3 measuring points on the upper and 3 on the under side, 24 measuring points per pigment mixture. The average values obtained are based on a sample obtained with a mixing time of 80 seconds (final color intensity = 100%).
Le A 28 094 7 Examples Example 1 An aqueous suspension containing about 50% by weight of Fe304 (Bayferrox(R) 318, Trade Product of Bayer AG) and 1%
by weight of soda waterglass solution containing 360 g/1 of Si42, based on the solids content, arrived at the distribution disc of a disc spray drier under a pressure of 0.5 bar. The circumferential velocity of the disc was 88 m/s. The combustion gases from the natural gas surface burner entered the spray drier at a temperature of 380°C.
The discharge temperature of the gases was 75°G. 90 kg per hour of iron oxide black granules having a residual moisture content of 3.5% by weight were obtained. The com-pacted bulk density of the granules was 1.14 g/cm3. Screen analysis of the granules showed that 23.7% of the granules were smaller than 100 ~Cm and only 76.3% were greater than 100 ~.m.
Rolling of the resulting granules was continued, in the present Example in a tablet coating drum having a diameter of 80 cm and an angle of inclination of 45°C and rotating at 25 revs/min. The granules obtained after 60 minutes were free-flowing and according to sieve analysis contained only 14% of particles smaller than 100 ~,m. The compacted bulk density was 1.18 g/cm3. In the dispers-ibility test in concrete prisms, the final color intensity was obtained after 50 seconds.
Exam 1e 2 The granules from Example 1 containing 23.7% of particles smaller than-100 ~Cm were after-rolled in the coating drum for one hour as in Example 1. In addition, they were Le A 28 094 8 sprayed during this time with 2% by weight of water, based on the solids content.
The granules then contained only 4.5% of particles smaller than 100 Vim. The compacted bulk density raas 1.22 g/cm3.
The flow was excellent and the amount of dust produced very slight. In the dispersibility test in concrete prisms, the final color intensity was obtained after 40 seconds.
Example 3 An aqueous suspension having a solids content of 55% by weight of iron oxide red (Bayferrox(R) 130, Trade product of Bayer AG) reached the distribution disc of a disc spray drier under an initial pressure of 0.3 bar. The circum-ferential velocity of the disc was 75 m/s. The combustion gases from the natural gas surface burner entered the spray drier at a temperature of 400°C. The discharge temperature was 160°C. 125 kg per hour of iron oxide red granules having a residual maisture content of 0.3% by weight were obtained. The compacted bulk density was 1.48 g/cm3. Screen analysis, however, showed that 24.8% of the granules were smaller than 100 ~m°
These granules were then after-rolled for 30 minutes as described in Example 1. This reduced the proportion of particles smaller than 100 ~Sm to 13%. The flow was excellent and the amount of dust produced very slight.
In the test for dispersibility in concrete prisms, the final color intensity was obtained after 70 seconds:
The compacted bulk density was 1.40 g/cm3.
Le A 28 094 9 ' ~~fl~~~
Example 4 The granules from Example 3 were sprayed with 1% by weight of water during the after-rolling. Granules containing less than 10% of particles below 100 ~m were obtained after one hour. The flow and dust content were excellent.
In the dispersibility test in concrete prisms, the final colour intensity was obtained after 60 seconds. The com-pacted bulk density was 1.41 g/cm3.
Example 5 Granules of iron oxide yellow were produced as described in Examples 1 and 3 (Bayferrox(R) 420, Trade Product of Bayer AG) . The compacted bulk density was 0.92 g/cm3 and the residual moisture content was 0.3% by weight. Screen analysis showed that 87.5% by weight of the particles were greater than 100 ~Cm. These granules were kept at 190°C in a rotary tube furnace for 30 minutes at a circumferential velocity of 4 revs/min. 98. 8 % by weight of the resulting granules were larger than 100 Vim. The compacted bulk density was 0.96 g/cm3.
The final color intensity in the dispersibility test in concrete prisms was obtained after 50 seconds.
Le A 28 094 10
Particularly good results are obtained with iron oxide pigments.
The compacted bulk density of the granulates may vary according to the pigment, the type and quantity of additive and the water content of the suspension. If the compacted bulk density is too low, the granulates will be insufficiently stable, whereas granulates with high compacted bulk densities are difficult to disperse. The iron oxide black granulates according to the invention preferably have compacted bulk densities of from 0.8 to 1.4 g/cur3.
The process accarding to the invention will now be Le A 28 094 6 explained more fully with the aid of the following Examples but must not be regarded as limited by the Examples.
The dispersibility in concrete was tested by measuring the color intensity of prisms produced with white cement conforming to the following data: Cement . sharp sand ratio 1 : 4, water-cement value 0.35, level of pigmenta-tion 1.2%, based on the cement, mixer used: RK Toni Technik, Berlin, 5 1 mixing dish, Model 1551, speed of rotation 140 revs/min (Batch : 500 g of cement). Four samples of mixture (300 g) were removed after 30, 40, 50, 60 , 70 and 80 seconds arid used to produce sample bodies (5 x 10 x 2.5 cm) under pressure (32.5 N/mm2) . Hardening of the samples: 24 hours at 30°G and 95% relative humidity followed by drying at 50°C for 24 hours. Colour data measured with Hunterlab apparatus: 3 measuring points on the upper and 3 on the under side, 24 measuring points per pigment mixture. The average values obtained are based on a sample obtained with a mixing time of 80 seconds (final color intensity = 100%).
Le A 28 094 7 Examples Example 1 An aqueous suspension containing about 50% by weight of Fe304 (Bayferrox(R) 318, Trade Product of Bayer AG) and 1%
by weight of soda waterglass solution containing 360 g/1 of Si42, based on the solids content, arrived at the distribution disc of a disc spray drier under a pressure of 0.5 bar. The circumferential velocity of the disc was 88 m/s. The combustion gases from the natural gas surface burner entered the spray drier at a temperature of 380°C.
The discharge temperature of the gases was 75°G. 90 kg per hour of iron oxide black granules having a residual moisture content of 3.5% by weight were obtained. The com-pacted bulk density of the granules was 1.14 g/cm3. Screen analysis of the granules showed that 23.7% of the granules were smaller than 100 ~Cm and only 76.3% were greater than 100 ~.m.
Rolling of the resulting granules was continued, in the present Example in a tablet coating drum having a diameter of 80 cm and an angle of inclination of 45°C and rotating at 25 revs/min. The granules obtained after 60 minutes were free-flowing and according to sieve analysis contained only 14% of particles smaller than 100 ~,m. The compacted bulk density was 1.18 g/cm3. In the dispers-ibility test in concrete prisms, the final color intensity was obtained after 50 seconds.
Exam 1e 2 The granules from Example 1 containing 23.7% of particles smaller than-100 ~Cm were after-rolled in the coating drum for one hour as in Example 1. In addition, they were Le A 28 094 8 sprayed during this time with 2% by weight of water, based on the solids content.
The granules then contained only 4.5% of particles smaller than 100 Vim. The compacted bulk density raas 1.22 g/cm3.
The flow was excellent and the amount of dust produced very slight. In the dispersibility test in concrete prisms, the final color intensity was obtained after 40 seconds.
Example 3 An aqueous suspension having a solids content of 55% by weight of iron oxide red (Bayferrox(R) 130, Trade product of Bayer AG) reached the distribution disc of a disc spray drier under an initial pressure of 0.3 bar. The circum-ferential velocity of the disc was 75 m/s. The combustion gases from the natural gas surface burner entered the spray drier at a temperature of 400°C. The discharge temperature was 160°C. 125 kg per hour of iron oxide red granules having a residual maisture content of 0.3% by weight were obtained. The compacted bulk density was 1.48 g/cm3. Screen analysis, however, showed that 24.8% of the granules were smaller than 100 ~m°
These granules were then after-rolled for 30 minutes as described in Example 1. This reduced the proportion of particles smaller than 100 ~Sm to 13%. The flow was excellent and the amount of dust produced very slight.
In the test for dispersibility in concrete prisms, the final color intensity was obtained after 70 seconds:
The compacted bulk density was 1.40 g/cm3.
Le A 28 094 9 ' ~~fl~~~
Example 4 The granules from Example 3 were sprayed with 1% by weight of water during the after-rolling. Granules containing less than 10% of particles below 100 ~m were obtained after one hour. The flow and dust content were excellent.
In the dispersibility test in concrete prisms, the final colour intensity was obtained after 60 seconds. The com-pacted bulk density was 1.41 g/cm3.
Example 5 Granules of iron oxide yellow were produced as described in Examples 1 and 3 (Bayferrox(R) 420, Trade Product of Bayer AG) . The compacted bulk density was 0.92 g/cm3 and the residual moisture content was 0.3% by weight. Screen analysis showed that 87.5% by weight of the particles were greater than 100 ~Cm. These granules were kept at 190°C in a rotary tube furnace for 30 minutes at a circumferential velocity of 4 revs/min. 98. 8 % by weight of the resulting granules were larger than 100 Vim. The compacted bulk density was 0.96 g/cm3.
The final color intensity in the dispersibility test in concrete prisms was obtained after 50 seconds.
Le A 28 094 10
Claims (10)
1. A process for coloring building materials with inorganic pigments which comprises incorporating into said materials pigments in the form of granulates which are free-flowing and not dust forming wherein the pigment granulates are produced from spray dried granules by after-granulating.
2. A process according to claim 1, wherein the after-granulation is carried out for a period of from 5 minutes to hours.
3. A process according to claim 1 or 2, wherein the after-granulation is carried out at a temperature from ambient temperature to 300°C.
4. A process according to any one of claims 1 to 3, wherein the after-granulation is carried out in drums, screws or rotary plates.
5. A process according to any one of claims 1 to 4, wherein the after-granulation is carried out without any additive.
6. A process according to any one of claims 1 to 4, wherein during after-granulation the granules are sprayed with 0.5 to 5% by weight of water, based on the quantity of pigments.
7. A process according to any one of claims 1 to 4, wherein during after-granulation the granules are sprayed with 0.5 to 5o by weight of aqueous solutions of a salt of a metal selected from boron, aluminum, silicon, titanium, zinc, tin and a mixture thereof, based on the quantity of pigments.
8, A process according to any one of claims 1 to 7, wherein the inorganic pigments are selected from a group consisting of titanium dioxide, iron oxide, chromium oxide, manganese oxide and zinc oxide.
9. A process according to claim 8, wherein the inorganic pigments are iron oxide pigments.
10. A process according to any one of claims 1 to 7, wherein the inorganic pigments are mixed phase pigments containing at least two metal cations selected from a metal group consisting of chromium, manganese, iron, cobalt, nickel, zinc, titanium, copper, aluminum, arsenic and antimony, together with the oxygen as anion.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DEP4103531.3 | 1991-02-06 | ||
| DE4103531A DE4103531A1 (en) | 1991-02-06 | 1991-02-06 | METHOD FOR COLORING BUILDING MATERIALS |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CA2060545A1 CA2060545A1 (en) | 1992-08-07 |
| CA2060545C true CA2060545C (en) | 2003-08-19 |
Family
ID=6424467
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CA002060545A Expired - Fee Related CA2060545C (en) | 1991-02-06 | 1992-02-03 | Process for coloring building materials |
Country Status (6)
| Country | Link |
|---|---|
| US (1) | US5199986A (en) |
| EP (1) | EP0507046B1 (en) |
| JP (1) | JP3224260B2 (en) |
| AU (1) | AU649516B2 (en) |
| CA (1) | CA2060545C (en) |
| DE (2) | DE4103531A1 (en) |
Families Citing this family (32)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5489333A (en) * | 1993-10-25 | 1996-02-06 | Board Of Trustees Operating Michigan State University | Shrinkage compensating concrete with expansive additive |
| DE4336613C1 (en) * | 1993-10-27 | 1995-02-09 | Bayer Ag | Process for colouring building materials |
| DE4342331A1 (en) * | 1993-12-11 | 1995-06-14 | Krueger Gmbh & Co Kg | Pigment granules for coloring building materials |
| IT1269247B (en) * | 1994-08-05 | 1997-03-26 | Manfredini E Schianchi Srl | METHOD FOR THE GRANULES AGGROMERATION OF MIXTURES ATOMIZED FOR CERAMIC USE, IN PARTICULAR FOR PORCELAIN STONEWARE, AND RELATED PRODUCT |
| DE4429147A1 (en) | 1994-08-17 | 1996-02-22 | Glatt Ingtech Gmbh | Process for the production of granulated additives for building materials |
| US5562765A (en) * | 1994-10-21 | 1996-10-08 | E. I. Du Pont De Nemours And Company | Iron-manganese colorant |
| MY132071A (en) * | 1995-05-11 | 2007-09-28 | Cure Corp C | A composition and method for dispersing pigment in cement based compositions |
| US5558708A (en) * | 1995-05-11 | 1996-09-24 | C-Cure Corporation | System and method for dispersing pigment in cement based compositions |
| DE19649756B4 (en) | 1996-04-18 | 2005-05-25 | Bayer Chemicals Ag | Process for the preparation of briquetting and pressed granules from carbon black pigments and their use |
| US5993536A (en) * | 1997-02-05 | 1999-11-30 | Toda Kogyo Corporation | Method of decoloring colored concrete |
| DE19706899C1 (en) * | 1997-02-21 | 1998-11-05 | Bayer Ag | Inorganic, compacted pigment granules, process for their preparation and their use |
| US5853476A (en) * | 1997-08-11 | 1998-12-29 | Elementis Pigments, Inc. | Process for coloring concrete using compacted inorganic granules |
| WO2000037386A1 (en) * | 1998-12-18 | 2000-06-29 | Oy Custone Ltd | Method for the colouration/intensification of the colour of concrete |
| JP3182648B2 (en) * | 1999-05-12 | 2001-07-03 | ティーディーケイ株式会社 | Ceramic granules for molding a ceramic molded body, method for producing or treating the same, ceramic molded body and method for producing the same |
| DE19950712A1 (en) * | 1999-10-21 | 2001-04-26 | Vti Thueringer Verfahrenstechn | Colored pigment granules for coloring concrete comprises individual granules surrounded by a soluble enveloping material without a binder |
| CA2353207A1 (en) | 2000-11-20 | 2002-05-20 | C-Cure Corporation | Colored cement |
| US6908675B1 (en) * | 2002-04-22 | 2005-06-21 | William Louis Bohach | Process to reduce dusting and improve flow properties of pigments and powders |
| US7566497B2 (en) * | 2002-04-22 | 2009-07-28 | Manufacturing and Process Technologies, L.L.C. | Method for forming pigment pseudoparticles |
| CA2610864C (en) * | 2005-06-06 | 2014-05-27 | William L. Bohach | Methods for forming pigment pseudoparticles |
| DE102006017109A1 (en) * | 2006-04-10 | 2007-10-11 | Lanxess Deutschland Gmbh | Pigment granule, useful e.g. to dye building materials, comprises a compressed or briquetted core and a granulated outer layer, where the core contains an organic or inorganic pigment and an auxiliary agent |
| US7976963B2 (en) * | 2007-05-01 | 2011-07-12 | Boral Stone Products, LLC | Concrete product with enhanced ornamental surface layer |
| DE102007023913A1 (en) | 2007-05-23 | 2008-11-27 | Lanxess Deutschland Gmbh | Pigment preparations of pasty or gelatinous consistency |
| DE102007023912A1 (en) * | 2007-05-23 | 2008-11-27 | Lanxess Deutschland Gmbh | Pigment preparations of pasty or gelatinous consistency |
| DE102008020573A1 (en) * | 2008-04-24 | 2009-10-29 | Klaus Hudelmaier | Process for producing pigmented products |
| US7815728B2 (en) * | 2008-05-02 | 2010-10-19 | L. M. Scofield Company | High SRI cementitious systems for colored concrete |
| DE102008045121A1 (en) | 2008-09-01 | 2010-03-04 | Lanxess Deutschland Gmbh | Pigment granules containing inorganic filter aids |
| US10717674B2 (en) | 2010-04-27 | 2020-07-21 | Biomason, Inc. | Methods for the manufacture of colorfast masonry |
| JP5678950B2 (en) * | 2012-01-06 | 2015-03-04 | Tdk株式会社 | Glass ceramic sintered body and wiring board |
| JP2014196493A (en) * | 2014-04-11 | 2014-10-16 | マニユフアクチヤリング・アンド・プロセス・テクノロジーズ・エルエルシー（デイー／ビー／エイ エムピー テクノロジーズ） | Method of forming pigment pseudo-particle |
| WO2015178784A1 (en) * | 2014-05-23 | 2015-11-26 | Lacy Rachel D Arcy | Concrete colourants |
| CN109923090A (en) | 2016-10-31 | 2019-06-21 | 拜奥梅森股份有限公司 | Microorganism load gather materials and manufacturing method |
| FI3692009T3 (en) | 2017-10-05 | 2023-07-27 | Biomason Inc | Biocementation method and system |
Family Cites Families (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CH604880A5 (en) * | 1976-05-25 | 1978-09-15 | Ciba Geigy Ag | |
| DE2723221B2 (en) * | 1976-05-25 | 1980-09-04 | Ciba-Geigy Ag, Basel (Schweiz) | Dyestuff granules and device for their production |
| AU525215B2 (en) * | 1976-12-16 | 1982-10-28 | Solar Pump Corp. | Vapour operated motor |
| FR2438073A1 (en) * | 1978-10-06 | 1980-04-30 | Ciba Geigy Ag | Granulating pigment powder in fluidised bed |
| US4277288A (en) * | 1978-10-06 | 1981-07-07 | Ciba-Geigy Corporation | Fluidized granulation of pigments using organic granulating assistant |
| DE3619363A1 (en) * | 1986-06-09 | 1987-12-10 | Brockhues Chem Werke Ag | METHOD FOR COLORING CONCRETE |
| DE3918694C1 (en) * | 1989-05-10 | 1990-10-25 | Bayer Ag, 5090 Leverkusen, De | |
| ES2079014T3 (en) * | 1990-10-24 | 1996-01-01 | Bayer Ag | PROCEDURE FOR DYING CONSTRUCTION MATERIALS. |
-
1991
- 1991-02-06 DE DE4103531A patent/DE4103531A1/en not_active Withdrawn
-
1992
- 1992-01-24 DE DE59201211T patent/DE59201211D1/en not_active Expired - Fee Related
- 1992-01-24 EP EP92101126A patent/EP0507046B1/en not_active Expired - Lifetime
- 1992-01-27 US US07/826,432 patent/US5199986A/en not_active Expired - Lifetime
- 1992-02-03 JP JP04639492A patent/JP3224260B2/en not_active Expired - Fee Related
- 1992-02-03 CA CA002060545A patent/CA2060545C/en not_active Expired - Fee Related
- 1992-02-05 AU AU10850/92A patent/AU649516B2/en not_active Ceased
Also Published As
| Publication number | Publication date |
|---|---|
| DE4103531A1 (en) | 1992-08-13 |
| JP3224260B2 (en) | 2001-10-29 |
| DE59201211D1 (en) | 1995-03-02 |
| AU649516B2 (en) | 1994-05-26 |
| EP0507046B1 (en) | 1995-01-18 |
| CA2060545A1 (en) | 1992-08-07 |
| JPH04367547A (en) | 1992-12-18 |
| EP0507046A1 (en) | 1992-10-07 |
| AU1085092A (en) | 1992-08-13 |
| US5199986A (en) | 1993-04-06 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EEER | Examination request | ||
| MKLA | Lapsed |