WO2009080894A1 - Method for making organic pigment - Google Patents
Method for making organic pigment Download PDFInfo
- Publication number
- WO2009080894A1 WO2009080894A1 PCT/FI2008/050775 FI2008050775W WO2009080894A1 WO 2009080894 A1 WO2009080894 A1 WO 2009080894A1 FI 2008050775 W FI2008050775 W FI 2008050775W WO 2009080894 A1 WO2009080894 A1 WO 2009080894A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- grinding
- starting material
- organic pigment
- treatment
- wood
- Prior art date
Links
- 239000012860 organic pigment Substances 0.000 title claims abstract description 41
- 238000000034 method Methods 0.000 title claims abstract description 37
- 238000000227 grinding Methods 0.000 claims abstract description 98
- 239000007858 starting material Substances 0.000 claims abstract description 50
- 239000002245 particle Substances 0.000 claims abstract description 31
- 239000000463 material Substances 0.000 claims description 26
- 239000000047 product Substances 0.000 claims description 19
- 239000000203 mixture Substances 0.000 claims description 11
- 239000002023 wood Substances 0.000 claims description 11
- 239000000835 fiber Substances 0.000 claims description 10
- 239000000428 dust Substances 0.000 claims description 8
- 238000001816 cooling Methods 0.000 claims description 7
- 229920001131 Pulp (paper) Polymers 0.000 claims description 6
- 238000001035 drying Methods 0.000 claims description 5
- 238000010438 heat treatment Methods 0.000 claims description 5
- 239000002699 waste material Substances 0.000 claims description 5
- 229920002678 cellulose Polymers 0.000 claims description 4
- 239000001913 cellulose Substances 0.000 claims description 4
- 238000007710 freezing Methods 0.000 claims description 4
- 230000008014 freezing Effects 0.000 claims description 4
- 238000009210 therapy by ultrasound Methods 0.000 claims description 4
- 238000005520 cutting process Methods 0.000 claims description 3
- 238000012986 modification Methods 0.000 claims description 3
- 230000004048 modification Effects 0.000 claims description 3
- 239000010802 sludge Substances 0.000 claims description 3
- 235000013339 cereals Nutrition 0.000 claims description 2
- 238000009837 dry grinding Methods 0.000 claims description 2
- 239000012535 impurity Substances 0.000 claims description 2
- 239000002440 industrial waste Substances 0.000 claims description 2
- 238000002203 pretreatment Methods 0.000 claims description 2
- 239000004576 sand Substances 0.000 claims description 2
- 238000012216 screening Methods 0.000 claims description 2
- 239000010865 sewage Substances 0.000 claims description 2
- 238000005406 washing Methods 0.000 claims description 2
- 238000001238 wet grinding Methods 0.000 claims description 2
- 239000000049 pigment Substances 0.000 description 26
- 241000196324 Embryophyta Species 0.000 description 12
- 238000012360 testing method Methods 0.000 description 8
- 238000004519 manufacturing process Methods 0.000 description 7
- 239000011248 coating agent Substances 0.000 description 6
- 239000000945 filler Substances 0.000 description 5
- 239000000126 substance Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- 238000009826 distribution Methods 0.000 description 4
- 235000018185 Betula X alpestris Nutrition 0.000 description 3
- 235000018212 Betula X uliginosa Nutrition 0.000 description 3
- 229920002472 Starch Polymers 0.000 description 3
- 238000000576 coating method Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 description 3
- 239000011707 mineral Substances 0.000 description 3
- 239000008107 starch Substances 0.000 description 3
- 235000019698 starch Nutrition 0.000 description 3
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 238000003490 calendering Methods 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- 239000012141 concentrate Substances 0.000 description 2
- 230000002255 enzymatic effect Effects 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 230000000813 microbial effect Effects 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 238000004381 surface treatment Methods 0.000 description 2
- 239000012756 surface treatment agent Substances 0.000 description 2
- 241000218657 Picea Species 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 239000002551 biofuel Substances 0.000 description 1
- 238000005422 blasting Methods 0.000 description 1
- 238000007664 blowing Methods 0.000 description 1
- 229940000425 combination drug Drugs 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 239000000470 constituent Substances 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000002761 deinking Substances 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000003116 impacting effect Effects 0.000 description 1
- 239000012764 mineral filler Substances 0.000 description 1
- 230000003287 optical effect Effects 0.000 description 1
- 239000012766 organic filler Substances 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 238000010298 pulverizing process Methods 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 210000004872 soft tissue Anatomy 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09B—ORGANIC DYES OR CLOSELY-RELATED COMPOUNDS FOR PRODUCING DYES, e.g. PIGMENTS; MORDANTS; LAKES
- C09B61/00—Dyes of natural origin prepared from natural sources, e.g. vegetable sources
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09B—ORGANIC DYES OR CLOSELY-RELATED COMPOUNDS FOR PRODUCING DYES, e.g. PIGMENTS; MORDANTS; LAKES
- C09B67/00—Influencing the physical, e.g. the dyeing or printing properties of dyestuffs without chemical reactions, e.g. by treating with solvents grinding or grinding assistants, coating of pigments or dyes; Process features in the making of dyestuff preparations; Dyestuff preparations of a special physical nature, e.g. tablets, films
- C09B67/0001—Post-treatment of organic pigments or dyes
- C09B67/0002—Grinding; Milling with solid grinding or milling assistants
-
- D—TEXTILES; PAPER
- D21—PAPER-MAKING; PRODUCTION OF CELLULOSE
- D21H—PULP COMPOSITIONS; PREPARATION THEREOF NOT COVERED BY SUBCLASSES D21C OR D21D; IMPREGNATING OR COATING OF PAPER; TREATMENT OF FINISHED PAPER NOT COVERED BY CLASS B31 OR SUBCLASS D21G; PAPER NOT OTHERWISE PROVIDED FOR
- D21H17/00—Non-fibrous material added to the pulp, characterised by its constitution; Paper-impregnating material characterised by its constitution
- D21H17/02—Material of vegetable origin
Definitions
- the invention relates to a method as defined in the preamble of claim 1 for making organic pigment, wherein the pigment is formed from a starting material of plant origin, and to a paper product as defined in the preamble of claim 18.
- Pigments and fillers of both mineral and organic origin are known.
- a problem with oil-based organic pigments is their price which follows the oil price development, and high production costs. Also the waste treatment of oil-based materials can be considered as one problem of making oil-based pigments.
- a problem of starch-based organic pigments and those formed from cellulose is the complexity of their production due to many production steps and therefore scarcity of their industrial production.
- the objective of the invention is to disclose a new type of method for making organic pigment from new types of organic starting materials.
- a further objective of the invention is to provide an easy and cost-effective production method for the industrial production of organic pigment.
- the method and paper product according to the invention are characterized by what has been presented in the claims.
- the invention is based on a method for making organic pigment in such manner that the organic pigment is formed from a starting material of plant origin.
- the starting material is pulverized to a suitable particle size by mechani- cal grinding in at least two grinding steps to form the organic pigment.
- the invention is specifically based on a method for making organic pigment from the starting material simply by mechanical grinding substantially without any complex chemical treatment.
- the pigment refers to a material or substance or to a mixture thereof that provides an optical property or color or brightness in a carrier, product or the like or their surface.
- the pigment may be translucent or opaque.
- the pigment referred to herein may be used as a filler, coating agent, additive or the like. In this context, the pigment does not refer to a mineral-based pigment.
- grinding refers to any grinding, pulverizing, crushing or decomposition of a mate- rial to a desired particle size.
- the operation of the grinding devices preferably mills, is typically based on applying pressure, on cutting, rubbing, compressing and/or on the effect of an impact provided by blowing, or on an equivalent operational principle. Most mills operate as a combination of many operational principles .
- the starting material is ground by a grinding method selected from the group comprising crushing-based grinding, at- trition-based grinding, cutting-based grinding, blasting-based grinding, wet grinding, dry grinding, grinding under pressure and combinations thereof.
- the applied grinder is selected from the known grinding devices, such as an impact mill, air jet mill, sand grinder, pearl mill, ball mill, vibration mill, screw mill and combinations thereof. Each grinding step may be performed by the same grinding method or alternatively by different grinding methods.
- the starting material is ground by air jet grinding, preferably by an air jet mill. Typically, in the air jet mill, air or steam which is led through the nozzles carries the material that is being pulverized.
- the starting material is ground by Cryo-grinding.
- Cryo- grinding refers to grinding which is performed at low temperatures, i.e. cold grinding.
- a grinding aid e.g. a grinding mediator, which is harder than the starting material is used in the grinding.
- the grinding aid may be e.g. a mineral compound, lime concentrate, grinding ball or the like. Grinding aids allow reducing the mean size of the particles generated during grinding. In one embodiment, grinding aid is used in an amount of 10 to 30% of the total feed material in the grinding.
- grinding is performed in at least two steps by one or more devices. In one embodiment, grinding is performed in at least two steps, so that in each step the material is ground to a predetermined particle size, e.g. to coarse and fine fractions.
- the starting material is preground in the first grinding step to a predetermined particle size before the second mechanical grinding step.
- the starting material is ground in more than two grinding steps. In one embodiment, the starting material is ground in 3 to 10 grinding steps.
- the starting material is pretreated before the first grinding step e.g. by classification, mechanically and/or chemically or in an equivalent manner.
- the pretreatment is selected from the group comprising cooling, freezing, drying, chemicalization, pre- crushing, screening the starting material, washing the starting material, removing the impurities, heat treatment, biotechnical treatment, e.g. enzymatic or micro- bial treatment, ultrasound treatment and combinations thereof.
- the starting material is treated in more than one pretreatment steps.
- the starting material is treated between the grinding steps.
- the treatment between the grinding steps is selected from the group comprising cooling, freezing, drying, chemicalization, heat treatment, biotechnical treatment, e.g. enzymatic or microbial treatment, ultrasound treatment and combina- tions thereof.
- a sorting or classifying device can be used in conjunction with the grinding before any one of the grinding steps, whereby the particles according to a predetermined particle size are conducted to the grinding.
- the starting material is dried before grinding or before a grinding step. In one embodiment, the starting material is cooled before grinding or before a grinding step. In one embodiment, the starting material is cooled to a temperature below 0°C before grinding and/or between grindings, and grinding is preferably performed at a temperature below 0 0 C. In one embodiment, cooling is performed by liquid nitrogen.
- the formed organic pigment is treated after grinding by modifying the surface properties of the pigment and thus improving the properties of the pigment in respect to different uses. In this context, surface modification may re- fer to chemical surface treatment of the pigment, to coating, covering, surface dispersing, dispersing in order to make slurry or to an equivalent modification treatment .
- the material is ground to a particle size of less than lOO ⁇ m, in one embodiment to a particle size of less than 50 ⁇ m, and in one embodi- ment to a particle size of less than 30 ⁇ m to form the organic pigment .
- a classification device is arranged in conjunction with the grinding for classify- ing the particles generated during the grinding to form a desired particle size distribution for the application.
- the moisture level of the starting material is adjusted to affect the particle size of the organic pigment that is being formed.
- the starting material of plant origin is a wood-based material.
- the wood-based material is selected from the group comprising wood bits, dust, sawdust, chips, damp wood, waste wood, fiber pulp, wood pulp, cellulose, mechanical pulp, derivatives thereof or the like or mixtures thereof.
- the starting material of plant origin is a fiber-based material.
- the fiber-based material is selected from the group comprising graminaceous plants, herbaceous plants, cereals or the like or plant bits, various aqueous or sewage sludges, sludge pulps, fiber- based industrial waste flows, starch-based materials, derivatives thereof or the like or mixtures thereof.
- the stalk part of the plants is utilized as the fiber-based material.
- the organic pigment is formed from a mixture of starting materials of plant origin which contains various starting materials of plant origin.
- the method according to the invention may be applied for use in making different kinds of pigments which are applicable in the paper industry in paper products, e.g. fine papers, newsprints, printing papers and soft tissues, in the cosmetics industry, e.g. in dental pastes, in the paint industry, hygienic product industry, plastics industry, coating industry, composite product industry, board industry or in an equivalent application.
- the organic pigment made according to the invention may be used to replace fibrous and/or abrasive constituents in some applications .
- the pigment formed according to the invention may be used either alone or in a mixture with other substances in different kinds or pigment products, mixtures, compounds or the like.
- the invention is based on a paper product which is formed from paper and which contains organic pigment made by any one of the methods pre- sented above.
- the organic pigment formed according to the invention may be used in papermaking and in a paper product as a surface treatment agent for paper, as a coating agent and/or paper filler or their component.
- paper refers to any fiber- based paper or fiber product or the like.
- the paper may have been made from chemical pulp, mechanical pulp, chemimechanical pulp, recycled pulp, fiber pulp and/or mixtures thereof or the like.
- the paper may contain suitable fillers and additives and different kinds of surface treatment and coating agents.
- the paper may be in the form of a web or a sheet, or in other form which is suitable for the purpose.
- the method according to the invention pro- vides considerable advantages compared to the prior art .
- the invention provides an industrially applicable, simple and affordable way of making organic pigment.
- the method according to the invention is easy and simple to carry out as a production process.
- the method according to the invention provides an organic pigment product with a lower grammage than in the previously known pigments.
- the organic pigment according to the invention provides cost sav- ings e.g. in transportation expenses due to the lower grammage, and in the papermaking in the form of a lower calendering pressure and reduced wearing in the equipment parts, thanks to the softer composition of the pigment .
- one advantage of the organic pigment according to the invention is recyclability . Consequently, waste problems resulting from the use of the pigment can be reduced.
- the starting material was ground in two grinding steps, wherein the first step was pregrinding.
- the starting material was preground, and the preground product was subjected to a cooling treatment before the second grinding step.
- heat treatment was applied as the treatment step after pregrind- ing, and then the second grinding step was performed.
- the starting material was preground, followed by a cooling treatment, and grinding mediators were applied in the second actual grinding step to enhance the grinding effect.
- grinding was performed in two steps, and grinding mediators were applied in the second step.
- the starting material was pretreated by drying and ground after pre- treatment in two steps. Based on the grinding tests, one could conclude that grinding in at least two steps provides extremely good quality organic pigment for use in a paper product.
- organic pigment was formed from birch dust with the average particle size of about 230 ⁇ m. Feeding moisture of the wood was arranged to be about 20%. Crushing under a pressure roller was applied as pregrinding, so that the particle size of the starting material could be halved before the second actual grinding step.
- Dust that was utilized as the starting mate- rial was mechanically ground by Cryo-grinding without aids to the particle size class d50 of less than ll ⁇ m in one step.
- the dust was cooled to a temperature of below 0°C by feeding liquid nitrogen, and cold dust was pulverized by grinding. Particles generated in conjunction with grinding were classified with a classifier.
- white-colored and hard lime concentrate with a particle size of about 100 to 200 ⁇ m was used as aid in an amount of about 20% of the fed material in the grinding performed in the above-mentioned manner, the pigment particle size class d50 of less than 8 ⁇ m was obtained.
- the average particle size was 10.14 ⁇ m.
- organic pigment was formed from spruce cutter chips with feeding moisture of about 30%.
- the starting material was first reduced by a hammer mill and then cooled and ground by an air jet mill in one step.
- the rotational speed of the classifier was l ⁇ OOOrpm.
- organic pigment was formed from birch dust.
- the starting material was first reduced by a hammer mill and then cooled at 110 0 C and ground by an air jet mill.
- the rotational speed of the classifier was 20000rpm.
- organic pigments could be formed from starting materials of plant origin by multi-step grinding. An easily industrially applicable way of making organic pigment was discovered.
- the method according to the invention is suitable in different embodiments for use in making the most different kinds of organic pigments.
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Pigments, Carbon Blacks, Or Wood Stains (AREA)
- Crushing And Grinding (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The invention relates to a method for making organic pigment in such manner that the organic pigment is formed from a starting material of plant origin. According to the invention, the starting material is pulverized to a suitable particle size by mechanical grinding in at least two grinding steps to form the organic pigment.
Description
METHOD FOR MAKING ORGANIC PIGMENT
FIELD OF THE INVENTION
The invention relates to a method as defined in the preamble of claim 1 for making organic pigment, wherein the pigment is formed from a starting material of plant origin, and to a paper product as defined in the preamble of claim 18.
BACKGROUND OF THE INVENTION
Known from the prior art are different kinds of pigments and methods for making them. Pigments and fillers of both mineral and organic origin are known.
It is known from the prior art to form or- ganic pigments from starch-based materials and pure cellulose by chemical treatment steps. In these cases, the pigment is usually present in a mixture with some other material or in a dispersion. It is also known from the prior art to make organic pigments from oil- based materials.
When mineral fillers and coating pigments are replaced by materials of organic origin either partially or totally, the environmental load can be reduced. By using fillers or pigments of organic origin e.g. in the papermaking, the recycling of paper is enhanced and the deinking sludge is easier to process further or dispose of. This allows the application of used paper e.g. in the production of biofuels. Additionally, in typical cases, paper strength can be im- proved by organic fillers, and smoothness of the paper surface during calendering can be improved by organic pigments.
A problem with oil-based organic pigments is their price which follows the oil price development, and high production costs. Also the waste treatment of
oil-based materials can be considered as one problem of making oil-based pigments.
A problem of starch-based organic pigments and those formed from cellulose is the complexity of their production due to many production steps and therefore scarcity of their industrial production.
OBJECTIVE OF THE INVENTION
The objective of the invention is to disclose a new type of method for making organic pigment from new types of organic starting materials. A further objective of the invention is to provide an easy and cost-effective production method for the industrial production of organic pigment.
SUMMARY OF THE INVENTION
The method and paper product according to the invention are characterized by what has been presented in the claims. The invention is based on a method for making organic pigment in such manner that the organic pigment is formed from a starting material of plant origin. According to the invention, the starting material is pulverized to a suitable particle size by mechani- cal grinding in at least two grinding steps to form the organic pigment.
The invention is specifically based on a method for making organic pigment from the starting material simply by mechanical grinding substantially without any complex chemical treatment.
In this context, the pigment refers to a material or substance or to a mixture thereof that provides an optical property or color or brightness in a carrier, product or the like or their surface. The pigment may be translucent or opaque. The pigment referred to herein may be used as a filler, coating agent, additive
or the like. In this context, the pigment does not refer to a mineral-based pigment.
In this context, grinding refers to any grinding, pulverizing, crushing or decomposition of a mate- rial to a desired particle size. The operation of the grinding devices, preferably mills, is typically based on applying pressure, on cutting, rubbing, compressing and/or on the effect of an impact provided by blowing, or on an equivalent operational principle. Most mills operate as a combination of many operational principles .
In one embodiment of the invention, the starting material is ground by a grinding method selected from the group comprising crushing-based grinding, at- trition-based grinding, cutting-based grinding, blasting-based grinding, wet grinding, dry grinding, grinding under pressure and combinations thereof. In one embodiment, the applied grinder is selected from the known grinding devices, such as an impact mill, air jet mill, sand grinder, pearl mill, ball mill, vibration mill, screw mill and combinations thereof. Each grinding step may be performed by the same grinding method or alternatively by different grinding methods. In one embodiment, the starting material is ground by air jet grinding, preferably by an air jet mill. Typically, in the air jet mill, air or steam which is led through the nozzles carries the material that is being pulverized. The high speed of the air or steam produces turbulent zones into which the solid particles are fed. The high kinetic energy of the air effects upon the particles impacting each other with sufficiently high force. Strong turbulence reduces the particle size as the particles impact and rub against each other and the mill wall. In one embodiment, the starting material is ground by Cryo-grinding. Cryo-
grinding refers to grinding which is performed at low temperatures, i.e. cold grinding.
In one embodiment of the invention, a grinding aid, e.g. a grinding mediator, which is harder than the starting material is used in the grinding. The grinding aid may be e.g. a mineral compound, lime concentrate, grinding ball or the like. Grinding aids allow reducing the mean size of the particles generated during grinding. In one embodiment, grinding aid is used in an amount of 10 to 30% of the total feed material in the grinding.
In one embodiment of the invention, grinding is performed in at least two steps by one or more devices. In one embodiment, grinding is performed in at least two steps, so that in each step the material is ground to a predetermined particle size, e.g. to coarse and fine fractions.
In one embodiment of the invention, the starting material is preground in the first grinding step to a predetermined particle size before the second mechanical grinding step.
In one embodiment of the invention, the starting material is ground in more than two grinding steps. In one embodiment, the starting material is ground in 3 to 10 grinding steps.
In one embodiment of the invention, the starting material is pretreated before the first grinding step e.g. by classification, mechanically and/or chemically or in an equivalent manner. In one embodiment, the pretreatment is selected from the group comprising cooling, freezing, drying, chemicalization, pre- crushing, screening the starting material, washing the starting material, removing the impurities, heat treatment, biotechnical treatment, e.g. enzymatic or micro- bial treatment, ultrasound treatment and combinations
thereof. In one embodiment, the starting material is treated in more than one pretreatment steps.
In one embodiment of the invention, the starting material is treated between the grinding steps. In one embodiment, the treatment between the grinding steps is selected from the group comprising cooling, freezing, drying, chemicalization, heat treatment, biotechnical treatment, e.g. enzymatic or microbial treatment, ultrasound treatment and combina- tions thereof.
In one embodiment, a sorting or classifying device can be used in conjunction with the grinding before any one of the grinding steps, whereby the particles according to a predetermined particle size are conducted to the grinding.
In one embodiment, the starting material is dried before grinding or before a grinding step. In one embodiment, the starting material is cooled before grinding or before a grinding step. In one embodiment, the starting material is cooled to a temperature below 0°C before grinding and/or between grindings, and grinding is preferably performed at a temperature below 00C. In one embodiment, cooling is performed by liquid nitrogen. In one embodiment of the invention, the formed organic pigment is treated after grinding by modifying the surface properties of the pigment and thus improving the properties of the pigment in respect to different uses. In this context, surface modification may re- fer to chemical surface treatment of the pigment, to coating, covering, surface dispersing, dispersing in order to make slurry or to an equivalent modification treatment .
In one embodiment, the material is ground to a particle size of less than lOOμm, in one embodiment to a particle size of less than 50μm, and in one embodi-
ment to a particle size of less than 30μm to form the organic pigment .
In one embodiment, a classification device is arranged in conjunction with the grinding for classify- ing the particles generated during the grinding to form a desired particle size distribution for the application.
In one embodiment, the moisture level of the starting material is adjusted to affect the particle size of the organic pigment that is being formed.
In one embodiment of the invention, the starting material of plant origin is a wood-based material. In one embodiment, the wood-based material is selected from the group comprising wood bits, dust, sawdust, chips, damp wood, waste wood, fiber pulp, wood pulp, cellulose, mechanical pulp, derivatives thereof or the like or mixtures thereof.
In one embodiment of the invention, the starting material of plant origin is a fiber-based material. In one embodiment, the fiber-based material is selected from the group comprising graminaceous plants, herbaceous plants, cereals or the like or plant bits, various aqueous or sewage sludges, sludge pulps, fiber- based industrial waste flows, starch-based materials, derivatives thereof or the like or mixtures thereof. In one preferred embodiment, the stalk part of the plants is utilized as the fiber-based material.
In one embodiment, the organic pigment is formed from a mixture of starting materials of plant origin which contains various starting materials of plant origin.
The method according to the invention may be applied for use in making different kinds of pigments which are applicable in the paper industry in paper products, e.g. fine papers, newsprints, printing papers and soft tissues, in the cosmetics industry, e.g.
in dental pastes, in the paint industry, hygienic product industry, plastics industry, coating industry, composite product industry, board industry or in an equivalent application. Also, the organic pigment made according to the invention may be used to replace fibrous and/or abrasive constituents in some applications .
The pigment formed according to the invention may be used either alone or in a mixture with other substances in different kinds or pigment products, mixtures, compounds or the like.
Further, the invention is based on a paper product which is formed from paper and which contains organic pigment made by any one of the methods pre- sented above.
The organic pigment formed according to the invention may be used in papermaking and in a paper product as a surface treatment agent for paper, as a coating agent and/or paper filler or their component. In this context, paper refers to any fiber- based paper or fiber product or the like. The paper may have been made from chemical pulp, mechanical pulp, chemimechanical pulp, recycled pulp, fiber pulp and/or mixtures thereof or the like. The paper may contain suitable fillers and additives and different kinds of surface treatment and coating agents. The paper may be in the form of a web or a sheet, or in other form which is suitable for the purpose.
The method according to the invention pro- vides considerable advantages compared to the prior art .
The invention provides an industrially applicable, simple and affordable way of making organic pigment. The method according to the invention is easy and simple to carry out as a production process.
The method according to the invention provides an organic pigment product with a lower grammage than in the previously known pigments. The organic pigment according to the invention provides cost sav- ings e.g. in transportation expenses due to the lower grammage, and in the papermaking in the form of a lower calendering pressure and reduced wearing in the equipment parts, thanks to the softer composition of the pigment . In addition, one advantage of the organic pigment according to the invention is recyclability . Consequently, waste problems resulting from the use of the pigment can be reduced. Various materials of plant origin, forest industry waste, recycling materials and/or materials which were previously considered as reject products can be used as the starting materials for the organic pigment according to the invention. Furthermore, compared to the previously known oil- based pigments, the production costs of the pigment according to the invention are lower.
DETAILED DESCRIPTION OF THE INVENTION
The invention will be described in more de- tail with the aid of the accompanying examples.
Example 1
In this example, different grinding combinations for making organic pigment used in a paper prod- uct were tested. The pigment was formed from birch dust.
In the first grinding test, the starting material was ground in two grinding steps, wherein the first step was pregrinding. In the second grinding test, the starting material was preground, and the preground product was
subjected to a cooling treatment before the second grinding step. In the third grinding test, heat treatment was applied as the treatment step after pregrind- ing, and then the second grinding step was performed. In the third grinding test, the starting material was preground, followed by a cooling treatment, and grinding mediators were applied in the second actual grinding step to enhance the grinding effect. In the fifth grinding test, grinding was performed in two steps, and grinding mediators were applied in the second step.
In the sixth grinding test, the starting material was pretreated by drying and ground after pre- treatment in two steps. Based on the grinding tests, one could conclude that grinding in at least two steps provides extremely good quality organic pigment for use in a paper product.
Example 2
In this example, organic pigment was formed from birch dust with the average particle size of about 230μm. Feeding moisture of the wood was arranged to be about 20%. Crushing under a pressure roller was applied as pregrinding, so that the particle size of the starting material could be halved before the second actual grinding step.
Dust that was utilized as the starting mate- rial was mechanically ground by Cryo-grinding without aids to the particle size class d50 of less than llμm in one step. Before grinding, the dust was cooled to a temperature of below 0°C by feeding liquid nitrogen, and cold dust was pulverized by grinding. Particles generated in conjunction with grinding were classified with a classifier.
When white-colored and hard lime concentrate with a particle size of about 100 to 200μm was used as aid in an amount of about 20% of the fed material in the grinding performed in the above-mentioned manner, the pigment particle size class d50 of less than 8μm was obtained. The average particle size was 10.14μm. The following particle size distribution was obtained for the ground product: dlθ% = 2.87 d30% = 5.34 d50% = 7.86 d70% = 11.51 d90% = 19.43
Example 3
In this example, organic pigment was formed from spruce cutter chips with feeding moisture of about 30%.
The starting material was first reduced by a hammer mill and then cooled and ground by an air jet mill in one step. The rotational speed of the classifier was lβOOOrpm.
The following particle size distribution was obtained for the ground product: dlθ% = 2.26μm d30% = 6.04 d50% = 8.83 d70% = 16.42 d90% = 21.98
Example 4
In this example, organic pigment was formed from birch dust.
The starting material was first reduced by a hammer mill and then cooled at 1100C and ground by an
air jet mill. The rotational speed of the classifier was 20000rpm.
The following particle size distribution was obtained for the ground product: dlθ% = 2.35μm d30% = 3.98 d50% = 5.69 d70% = 8.13 d90% = 13.85
Based on the tests, it was concluded that organic pigments could be formed from starting materials of plant origin by multi-step grinding. An easily industrially applicable way of making organic pigment was discovered.
The method according to the invention is suitable in different embodiments for use in making the most different kinds of organic pigments.
The invention is not limited merely to the example referred to above; instead, many variations are possible within the scope of the inventive idea defined by the claims.
Claims
1. A method for making organic pigment in such manner that the organic pigment is formed from a starting material of plant origin, c h a r a c t e r i z e d in that the starting material is pulverized to a suitable particle size by mechanical grinding in at least two grinding steps to form the organic pigment.
2. The method according to claim 1, c h a r - a c t e r i z e d in that grinding is performed in at least two steps, so that in each step the material is ground to a predetermined particle size.
3. The method according to claim 1 or 2, c h a r a c t e r i z e d in that the starting material is preground in the first grinding step to a predetermined particle size.
4. The method according to any one of claims 1 to 3, c h a r a c t e r i z e d in that the starting material is pulverized by grinding in more than two grinding steps.
5. The method according to any one of claims 1 to 4, c h a r a c t e r i z e d in that the starting material is pretreated before the first grinding step.
6. The method according to any one of claims 1 to 5, c h a r a c t e r i z e d in that the starting material is treated between the grinding steps.
7. The method according to any one of claims 1 to 6, c h a r a c t e r i z e d in that the pretreat- ment is selected from the group comprising cooling, freezing, drying, chemicalization, precrushing, screening the starting material, washing the starting material, removal of impurities, heat treatment, bio- technical treatment, ultrasound treatment and combinations thereof.
8. The method according to any one of claims
1 to 7, c h a r a c t e r i z e d in that the treatment between the grinding steps is selected from the group comprising cooling, freezing, drying, chemicalization, heat treatment, biotechnical treatment, ultrasound treatment and combinations thereof.
9. The method according to any one of claims
1 to 8, c h a r a c t e r i z e d in that the starting material is ground by a grinding method selected from the group comprising crushing-based grinding, attrition-based grinding, cutting-based grinding, blasting- based grinding, wet grinding, dry grinding, grinding under pressure and combinations thereof.
10. The method according to any one of claims 1 to 9, c h a r a c t e r i z e d in that the grinding device used for grinding the starting material is se- lected from the group comprising impact mill, air jet mill, sand grinder, pearl mill, ball mill, vibration mill, screw mill and combinations thereof.
11. The method according to any one of claims 1 to 10, c h a r a c t e r i z e d in that a grinding aid which is harder than the starting material is used in the grinding.
12. The method according to any one of claims 1 to 11, c h a r a c t e r i z e d in that the formed organic pigment is treated after grinding by surface modification.
13. The method according to any one of claims 1 to 12, c h a r a c t e r i z e d in that the starting material of plant origin is a wood-based material.
14. The method according to claim 13, c h a - r a c t e r i z e d in that the wood-based material is selected from the group comprising wood bits, dust, sawdust, chips, damp wood, waste wood, fiber pulp, wood pulp, cellulose, mechanical pulp, derivatives thereof and mixtures thereof.
15. The method according to any one of claims 1 to 14, c h a r a c t e r i z e d in that the starting material of plant origin is a fiber-based material.
16. The method according to claim 15, c h a - r a c t e r i z e d in that the fiber-based material is selected from the group comprising graminaceous plants, herbaceous plants, cereals, plant bits, aqueous or sewage sludges, sludge pulps, fiber-based industrial waste flows, derivatives thereof and mixtures thereof.
17. A paper product formed from paper, c h a r a c t e r i z e d in that the paper contains organic pigment made by the method according to any one of claims 1 to 16.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP08863785A EP2235113A4 (en) | 2007-12-21 | 2008-12-19 | Method for making organic pigment |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI20075954A FI20075954L (en) | 2007-12-21 | 2007-12-21 | Method for preparing an organic pigment |
FI20075954 | 2007-12-21 |
Publications (1)
Publication Number | Publication Date |
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WO2009080894A1 true WO2009080894A1 (en) | 2009-07-02 |
Family
ID=38951649
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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PCT/FI2008/050775 WO2009080894A1 (en) | 2007-12-21 | 2008-12-19 | Method for making organic pigment |
Country Status (3)
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EP (1) | EP2235113A4 (en) |
FI (1) | FI20075954L (en) |
WO (1) | WO2009080894A1 (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2010146244A1 (en) * | 2009-06-18 | 2010-12-23 | Upm-Kymmene Corporation | Paper product and process for making same |
WO2012028788A1 (en) * | 2010-08-31 | 2012-03-08 | Upm-Kymmene Corporation | Method and system for manufacturing organic pigment, as well as organic pigment |
WO2013034811A1 (en) * | 2011-09-07 | 2013-03-14 | Upm-Kymmene Corporation | A method for manufacturing a material component, a material component and its use and a paper product |
WO2013158219A1 (en) * | 2012-04-20 | 2013-10-24 | Empire Technology Development Llc | Cellulose hydrolysis via modified lignosulfonate catalysts |
WO2015052380A1 (en) | 2013-10-11 | 2015-04-16 | Upm-Kymmene Corporation | Method for manufacturing a paper, a paper and its use, a furnish and a wood based composition |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2608922A1 (en) | 1986-12-31 | 1988-07-01 | Germandre Sarl | Improvements to processes for obtaining dehydrated vegetable powders |
US5227024A (en) | 1987-12-14 | 1993-07-13 | Daniel Gomez | Low density material containing a vegetable filler |
EP0433413B1 (en) * | 1989-06-15 | 1993-11-18 | GOMEZ, Daniel | Porous, micronized, low density vegetable filler with a controlled particle size and low specific physical and hydraulic surfaces, and method of preparation and use of same |
EP0624213B1 (en) * | 1992-01-30 | 1995-07-12 | Stora Feldmühle Ag | Paper suitable for rotogravure printing |
JPH08158298A (en) * | 1994-12-06 | 1996-06-18 | Tokushu Paper Mfg Co Ltd | Colored paper and production thereof |
CN1388184A (en) * | 2001-07-22 | 2003-01-01 | 吴和岭 | Natural superfine pigment and its processed paper product |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19636382A1 (en) * | 1996-09-09 | 1998-03-12 | Bayer Ag | Pigment preparations for ink jet printing |
-
2007
- 2007-12-21 FI FI20075954A patent/FI20075954L/en not_active Application Discontinuation
-
2008
- 2008-12-19 EP EP08863785A patent/EP2235113A4/en not_active Withdrawn
- 2008-12-19 WO PCT/FI2008/050775 patent/WO2009080894A1/en active Application Filing
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
FR2608922A1 (en) | 1986-12-31 | 1988-07-01 | Germandre Sarl | Improvements to processes for obtaining dehydrated vegetable powders |
US5227024A (en) | 1987-12-14 | 1993-07-13 | Daniel Gomez | Low density material containing a vegetable filler |
EP0433413B1 (en) * | 1989-06-15 | 1993-11-18 | GOMEZ, Daniel | Porous, micronized, low density vegetable filler with a controlled particle size and low specific physical and hydraulic surfaces, and method of preparation and use of same |
EP0624213B1 (en) * | 1992-01-30 | 1995-07-12 | Stora Feldmühle Ag | Paper suitable for rotogravure printing |
JPH08158298A (en) * | 1994-12-06 | 1996-06-18 | Tokushu Paper Mfg Co Ltd | Colored paper and production thereof |
CN1388184A (en) * | 2001-07-22 | 2003-01-01 | 吴和岭 | Natural superfine pigment and its processed paper product |
Non-Patent Citations (1)
Title |
---|
See also references of EP2235113A4 |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2010146244A1 (en) * | 2009-06-18 | 2010-12-23 | Upm-Kymmene Corporation | Paper product and process for making same |
US9169596B2 (en) | 2009-06-18 | 2015-10-27 | Upm-Kymmene Corporation | Paper product and process for making same |
WO2012028788A1 (en) * | 2010-08-31 | 2012-03-08 | Upm-Kymmene Corporation | Method and system for manufacturing organic pigment, as well as organic pigment |
WO2013034811A1 (en) * | 2011-09-07 | 2013-03-14 | Upm-Kymmene Corporation | A method for manufacturing a material component, a material component and its use and a paper product |
WO2013158219A1 (en) * | 2012-04-20 | 2013-10-24 | Empire Technology Development Llc | Cellulose hydrolysis via modified lignosulfonate catalysts |
US9598452B2 (en) | 2012-04-20 | 2017-03-21 | Empire Technology Development Llc | Cellulose hydrolysis via modified lignosulfonate catalysts |
WO2015052380A1 (en) | 2013-10-11 | 2015-04-16 | Upm-Kymmene Corporation | Method for manufacturing a paper, a paper and its use, a furnish and a wood based composition |
EP3055454A4 (en) * | 2013-10-11 | 2017-07-12 | UPM-Kymmene Corporation | Method for manufacturing a paper, a paper and its use, a furnish and a wood based composition |
Also Published As
Publication number | Publication date |
---|---|
EP2235113A4 (en) | 2011-08-24 |
FI20075954L (en) | 2009-06-22 |
FI20075954A0 (en) | 2007-12-21 |
EP2235113A1 (en) | 2010-10-06 |
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