WO1984002900A1 - A method of reducing eczema-inducing chromium in cement by adding ferrous sulfate, an additive comprising ferrous sulfate and the use of the additive - Google Patents
A method of reducing eczema-inducing chromium in cement by adding ferrous sulfate, an additive comprising ferrous sulfate and the use of the additive Download PDFInfo
- Publication number
- WO1984002900A1 WO1984002900A1 PCT/SE1984/000011 SE8400011W WO8402900A1 WO 1984002900 A1 WO1984002900 A1 WO 1984002900A1 SE 8400011 W SE8400011 W SE 8400011W WO 8402900 A1 WO8402900 A1 WO 8402900A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- cement
- gypsum
- ferrogypsum
- ferrous sulfate
- green salt
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
Links
Classifications
-
- 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
- C04B11/00—Calcium sulfate cements
-
- 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
- C04B22/00—Use of inorganic materials as active ingredients for mortars, concrete or artificial stone, e.g. accelerators or shrinkage compensating agents
- C04B22/0006—Waste inorganic materials
-
- 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
- C04B22/00—Use of inorganic materials as active ingredients for mortars, concrete or artificial stone, e.g. accelerators or shrinkage compensating agents
- C04B22/08—Acids or salts thereof
- C04B22/14—Acids or salts thereof containing sulfur in the anion, e.g. sulfides
- C04B22/142—Sulfates
- C04B22/149—Iron-sulfates
-
- 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
- C04B7/00—Hydraulic cements
- C04B7/22—Iron ore cements ; Iron rich cements, e.g. Ferrari cements, Kühl cements
-
- 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
- C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
- C04B2111/10—Compositions or ingredients thereof characterised by the absence or the very low content of a specific material
- C04B2111/1075—Chromium-free or very low chromium-content materials
- C04B2111/1081—Chromium VI, e.g. for avoiding chromium eczema
Definitions
- Portland cement always contains a certain amount of readily soluble hexavalent chromium in the form of chromates, usu- ally 10-20 ppm Cr , stemming from” the raw material and in smaller amounts from the fuel, the kiln lining and the various machines.
- This chromium produces eczema in brick ⁇ layers and concrete workers among others.
- a known and tested additive for reducing the content of easily soluble hexavalent chromium in the concrete, and thus reducing the risk of chromium contact eczema, is divalent iron in the form of ferrous sulfate.
- Ferrous sulfate is present in large amounts in the form of so-called green salt, a waste product from certain chemical and hydrometallurgical process industries.
- green salt a waste product from certain chemical and hydrometallurgical process industries.
- 3-4 tons of green salt are obtained for example for each ton of titanium dioxide.
- a small amount of this can be used for water purification, but the major portion is deposited as waste or is pumped into the sea.
- Green salt is such ferrous sulfate which leaves a precipita ⁇ tion process after a varying degree of mechanical dehydra- ti ⁇ n by filtering and possibly centrifuging.
- the major component of the green salt is ferrous sulfate with 7 hygro ⁇ scopic water, FeS0 4 «7H 2 0, with varying amounts of impurities and a moisture content of 2-25 % by weight depending on the dehydration method. Centrifuged green salt has the consis- tency of wet snow.
- Green salt has been approved as a concrete additive and is sold in 25 kg plastic bags for manual addition in conjunc ⁇ tion with the mixing of concrete.
- green salt can have a negative effect on the grinding pro ⁇ cess itself by hardened deposits in the mill with tendencies for blockage especially at the mill inlet.
- an excessively high water content of the ferrous sulfate can cause the chromate-reducing effect to be lossed when the green salt with an excess of water is subjected in the cement mill to an alkaline environment and high temper ⁇ ature.
- the handling problem can be avoided by dumping the salt directly into a tank for dissolving and then add the ferrous sulfate solution to the process.
- a corresponding technique has also been tried in the cement industry by spraying a saturated aqueous solution of the green salt into the cement mill, but this produced insufficient chromate reduction in the concrete.
- Another method which has been tested is to pump into the mill a slurry consisting of undissolved ferrous sulfate and saturated ferrous sulfate solution, but this process did not produce sufficient chromate reduction either.
- the present invention intends to produce cement with an additive of green salt in a mechanized and automated process with already existing equipment, by a method which does not produce the negative effects on the cement mill operation and which produces sufficient chro ate reduction to eliminate the risk of eczema.
- Cement refers here to all hydraulic binders and mortar products containing Portland cement clinker as the major component, 1-10 % by weight gypsum, CaS0 4 «2H-0 as a regulator of setting time and varying amounts of additives such as limestone, ash, slag and silicon powder, e.g. an amorphous, finely dispersed kieselguhr from the manufacture of silicon, ferrosilicon and ferrochromium.
- Green salt refers to a wet to moist salt containing 15-20 % iron in the form of FeS0 4 «7H 0 and 2-25 % by weight of non- chemically bonded water.
- the invention is based on replacing the ordinary gypsum • component in the cement milling with a mixture of gypsum and green salt, called ferrogypsum in the following, which is responsible in the process both for controlling the setting time and chromate reduction.
- the gypsum can be natural gypsum or so-called chemical gypsum, a by-product of certain chemical processes. especially the production of phosphoric acid.
- the granules of chemical gypsum are normally fine and can be easily mixed with green salt into a homogeneous mixture which will not separate during handling up to the cement mill.
- natural gypsum one should select a quality witha low proportion of heavy particles over about 20 mm, so that the separation of gypsum and green salt will be minimized.
- the composition of the ferrogypsum must be such that the amount of sulfate which regulates the setting time and the amount of divalent iron for reducing chromates have a certain relative proportion in view of the desired sulfate content in the finished cement, the original content of easily soluble chromate and the desired chromate reduction.
- the sulfate content and the chromate content in the cement vary from case to case, but have been shown to be virtually constant over time for a particular production unit. It is therefore possible to maintain the composition of the ferro ⁇ gypsum once it has been determined.
- a suitable addition of ferrous sulfate is 3-12 kg FeSO. «7H 2 0 per ton of finished cement, depending on the original con ⁇ tent of Cr in the cement clinker and the desired chromate reduction.
- the addi ⁇ tion of gypsum is reduced by 0.6 parts gypsum for each part ferrous sulfate heptahydrate added.
- the proportion of green salt in the ferrogypsum can also be reduced if the original content of Cr in the cement is lower than 10 ppm or if the chromate reduction is not to be carried as far.
- the mixing in of green salt in the ferrogypsum can be calculated from the size of the gypsum addition if it is initially greater or less than 50 kg per ton of cement.
- the proportion of green salt in the ferrogypsum can then vary from case to case between 2 and 90 % by weight, preferably between 5 and 25 % by weight.
- the ferrogypsum has good storage stability and the cement grinding process is rela- tively insensitive to fluctuations in the composition of the ferrogypsum, due to inhomogeneity. This allows the ferrogypsum to be prepared with simple equipment and at the.most advantageous location for transport, for example at the factory or delivery location for gypsum or green salt, at the reloading terminal or at the cement factory.
- the preparation of the ferrogypsum can be done by laying out a specific quantity of gypsum on a flat supporting surface in a layer about one meter thick. On top of this there is then laid a layer of a certain amount of green salt corresponding to the desired mixing proportions.
- the materials can be laid out with a bucket loader and the mixture can be homogenized by redigging with the loader, whereafter the mixture is loaded into a bin for transport to the next station, which can be a ship or a transport vehicle, intermediate storage plant or dosing bin for feeding into a cement mill.
- the ferrogypsum thus produced can then be used as a re ⁇ placement for gypsum in the making of cement after recal ⁇ culating the dosing as specified above.
- the chromium contents refer to analyses done after two minutes of shaking of equal amounts of cement and water.
- the ferrogypsum had better handling pro ⁇ perties than both green salt and gypsum individually due to less dust and easy passage through loading bins and shuts.
- the invention provides a method for using green salt as a chromate reducing raw material because - the ferrogypsum has significantly better handling charac ⁇ teristics than green salt, and at least equally good handling characteristics as gypsum;
- the ferrogypsum does not negatively affect the operation of the cement mill with baked-on deposits and the like, as is the case when using green salt and gypsum individu ⁇ ally;
- the divalent iron in the ferrogypsum is only oxidated to an insignificant degree to trivalent iron during the milling process, which can be done by direct addition of wet green salt and gypsum individually.
- the invention permits the replacement of two additives by a single additive which provides appreciable advantages as regards transport and economy. No extra investments are required for the addition of ferrous sulfate in each produc ⁇ tion line, as is the case with separate addition of ferrous sulfate and gypsum. Rather, existing equipment is used.
- OMPI done in fewer and larger boats, and the existing receiving and storage system for gypsum at the cement plant can be used.
- the present invention thus provides a simple method for producing a cement with significantly reduced risk of chromium eczema, without changing existing production lines, by using an inexpensive waste product, and the finished cement has equally good properties as cement without the addition, and at the same time without risk of causing chromium eczema.
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- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Abstract
In order to reduce the risk of chromium eczema when working with cement, the hexavalent chromium in the cement is reduced with ferrous sulfate in the form of ferrogypsum. Ferrogypsum is prepared by mixing green salt, a waste product from i.a. the manufacture of titanium dioxide, in moist state without any preceding drying or granulating, with gypsum in predetermined proportions. The ferrogypsum is used in making cement as a replacement for the ordinary gypsum and is added to the cement milling process with the existing dosing system for the gypsum. In order to reduce the content of easily soluble, hexavalent chromium from ca 10 ppm to ca 0.5 ppm, an addition of green salt is required of ca 5-10 kg per ton of cement. With a normal gypsum addition of 50 kg per ton of cement, the ferrogypsum should consist of 10% by weight green salt and 90% by weight gypsum and be added in an amount of 52 kg per ton of cement.
Description
A method of reducing eczema-inducing chromium in cement by adding ferrous sulfat^ an additive com¬ prising ferrous sulfat€and the use of the additive.
Portland cement always contains a certain amount of readily soluble hexavalent chromium in the form of chromates, usu- ally 10-20 ppm Cr , stemming from" the raw material and in smaller amounts from the fuel, the kiln lining and the various machines. This chromium produces eczema in brick¬ layers and concrete workers among others. A known and tested additive for reducing the content of easily soluble hexavalent chromium in the concrete, and thus reducing the risk of chromium contact eczema, is divalent iron in the form of ferrous sulfate.
Ferrous sulfate is present in large amounts in the form of so-called green salt, a waste product from certain chemical and hydrometallurgical process industries. When extracting titanium dioxide from il enite with sulphuric acid leaching, 3-4 tons of green salt are obtained for example for each ton of titanium dioxide. A small amount of this can be used for water purification, but the major portion is deposited as waste or is pumped into the sea.
Green salt is such ferrous sulfate which leaves a precipita¬ tion process after a varying degree of mechanical dehydra- tiόn by filtering and possibly centrifuging. The major component of the green salt is ferrous sulfate with 7 hygro¬ scopic water, FeS04«7H20, with varying amounts of impurities and a moisture content of 2-25 % by weight depending on the dehydration method. Centrifuged green salt has the consis- tency of wet snow.
Green salt has been approved as a concrete additive and is sold in 25 kg plastic bags for manual addition in conjunc¬ tion with the mixing of concrete.
Up to now, for additing ferrous sulfate to cement during mix¬ ing, there has been necessary to use dry ferrous sulfate in
the form of granulates or powder, produced from the green salt in special drying or granulating plants. Such purified ferrous .sulfate can be easily stored, transported and dosed by means of known technology and can also be easily mixed with the dry cement powder. In addition to being substanti¬ ally more expensive than the corresponding amount of green salt, it is also dusty and moisture sensitive and therefore requires sealed handling with special equipment for freight, storage and internal transport in bulk form, or alternative- ly the use of the product in sacks, which makes the product - even more expensive. Such dry ferrous..Isjulfate is at present being used in a Danish cement plant.
It is primarily three factors which prevent the ready addi- tion of green salt to the cement mixer. In the first place, it is not possible to store, transport and dose green salt with sufficient reliability in a mechanized, remote control¬ led and automated continuous process in the same manner as can be done with dry ferrous sulfate. In the second place, green salt can have a negative effect on the grinding pro¬ cess itself by hardened deposits in the mill with tendencies for blockage especially at the mill inlet. In the third place, an excessively high water content of the ferrous sulfate can cause the chromate-reducing effect to be lossed when the green salt with an excess of water is subjected in the cement mill to an alkaline environment and high temper¬ ature.
When using green salt for water purification for example, the handling problem can be avoided by dumping the salt directly into a tank for dissolving and then add the ferrous sulfate solution to the process. A corresponding technique has also been tried in the cement industry by spraying a saturated aqueous solution of the green salt into the cement mill, but this produced insufficient chromate reduction in the concrete. Another method which has been tested is to pump into the mill a slurry consisting
of undissolved ferrous sulfate and saturated ferrous sulfate solution, but this process did not produce sufficient chromate reduction either.
The present invention intends to produce cement with an additive of green salt in a mechanized and automated process with already existing equipment, by a method which does not produce the negative effects on the cement mill operation and which produces sufficient chro ate reduction to eliminate the risk of eczema.
Cement refers here to all hydraulic binders and mortar products containing Portland cement clinker as the major component, 1-10 % by weight gypsum, CaS04«2H-0 as a regulator of setting time and varying amounts of additives such as limestone, ash, slag and silicon powder, e.g. an amorphous, finely dispersed kieselguhr from the manufacture of silicon, ferrosilicon and ferrochromium.
Green salt refers to a wet to moist salt containing 15-20 % iron in the form of FeS04«7H 0 and 2-25 % by weight of non- chemically bonded water.
The invention is based on replacing the ordinary gypsum • component in the cement milling with a mixture of gypsum and green salt, called ferrogypsum in the following, which is responsible in the process both for controlling the setting time and chromate reduction.
This premixture of gypsum and green salt is possible by virtue of the fact that these substances are chemically closely related and tests have shown that the mixture has good resistance when stored against oxidation of the divalent iron.
The gypsum can be natural gypsum or so-called chemical gypsum, a by-product of certain chemical processes.
especially the production of phosphoric acid. The granules of chemical gypsum are normally fine and can be easily mixed with green salt into a homogeneous mixture which will not separate during handling up to the cement mill. When using natural gypsum, one should select a quality witha low proportion of heavy particles over about 20 mm, so that the separation of gypsum and green salt will be minimized.
The composition of the ferrogypsum must be such that the amount of sulfate which regulates the setting time and the amount of divalent iron for reducing chromates have a certain relative proportion in view of the desired sulfate content in the finished cement, the original content of easily soluble chromate and the desired chromate reduction. The sulfate content and the chromate content in the cement vary from case to case, but have been shown to be virtually constant over time for a particular production unit. It is therefore possible to maintain the composition of the ferro¬ gypsum once it has been determined.
A suitable addition of ferrous sulfate is 3-12 kg FeSO.«7H20 per ton of finished cement, depending on the original con¬ tent of Cr in the cement clinker and the desired chromate reduction. In order to keep the sulfate content in the • cement for regulating the setting time unchanged, the addi¬ tion of gypsum is reduced by 0.6 parts gypsum for each part ferrous sulfate heptahydrate added.
In order to reduce the content of Cr + from 10 ppm to 0.5 ppm, ca 5 kg FeSO. * 7 0 are required per ton of cement. If 50 kg*of gypsum were originally added per ton of cement, this must then be reduced by 0.6x5 kg to 47 kg. The ferro¬ gypsum can in this case consist of about 10 % by weight green salt and 90 % by weight gypsum and be added to the cement grinding process in an amount corresponding to 47+5= 52 kg per ton cement. The mixing proportions of green salt and gypsum can be adjusted somewhat in view of the prevail¬ ing moisture and impurity contents in the raw materials. .^^ OMTl
If the original content of easily soluble hexavalent chromium in the cement is higher than 10 ppm or if it is desired to make an even greater chromate reduction, the proportion of green salt in the ferrogypsum is raised to at most about 20 kg per ton of cement.
The proportion of green salt in the ferrogypsum can also be reduced if the original content of Cr in the cement is lower than 10 ppm or if the chromate reduction is not to be carried as far. In the same manner, the mixing in of green salt in the ferrogypsum can be calculated from the size of the gypsum addition if it is initially greater or less than 50 kg per ton of cement. The proportion of green salt in the ferrogypsum can then vary from case to case between 2 and 90 % by weight, preferably between 5 and 25 % by weight.
As is previously mentioned, the ferrogypsum has good storage stability and the cement grinding process is rela- tively insensitive to fluctuations in the composition of the ferrogypsum, due to inhomogeneity. This allows the ferrogypsum to be prepared with simple equipment and at the.most advantageous location for transport, for example at the factory or delivery location for gypsum or green salt, at the reloading terminal or at the cement factory.
The preparation of the ferrogypsum can be done by laying out a specific quantity of gypsum on a flat supporting surface in a layer about one meter thick. On top of this there is then laid a layer of a certain amount of green salt corresponding to the desired mixing proportions. The materials can be laid out with a bucket loader and the mixture can be homogenized by redigging with the loader, whereafter the mixture is loaded into a bin for transport to the next station, which can be a ship or a transport vehicle, intermediate storage plant or dosing bin for feeding into a cement mill.
The ferrogypsum thus produced can then be used as a re¬ placement for gypsum in the making of cement after recal¬ culating the dosing as specified above.
In full scale tests at the cement plant in Degerhamn, 100 tons of ferrogypsum were prepared by mixing 10 tons of green salt containing 10 % moisture with 90 tons of chemical gypsum, whereafter the mixture was stored for one month prior to addition to the cement mill. The dosing corre¬ sponded to 6 kg FeS04«7H20 per ton of cement and the con¬ tent of easily soluble, hexavalent chromium in the cement was reduced from the original 12 ppm to an average of 0.6 ppm. The storage stability of the ferrogypsum is thus very good and completely sufficient to continue a cement produc- tion where the storage time is at most a few weeks. Addi¬ tional full scale tests were done at the cement plant in Skovde with three different mixtures containing 9 %, 12.5 % and 16.7 %, respectively, of green salt with ca 5 % moisture i.i the gypsum, which corresponded to 4.5 kg, 6.5 kg and
8,5 kg, respectively, of FeSO.-^H-O per ton of cement. The amount of easily soluble Cr 6+ was reduced from the original
11 ppm to 1.2 ppm, 1.0 ppm and 0.55 ppm, respectively. The chromium contents refer to analyses done after two minutes of shaking of equal amounts of cement and water.
Storage tests have been made with finished cement which immediately after the manufacture had 0.25 ppm easily soluble chromium. The chromium content remained unchanged for two months and after three months it had risen to 0.5 ppm and after seven months to 0.7 ppm.
During the tests, the ferrogypsum had better handling pro¬ perties than both green salt and gypsum individually due to less dust and easy passage through loading bins and shuts.
The special features of this invention compared with already known products and processes for addition-of ferrous sulfate
and gypsum are the following:
The invention provides a method for using green salt as a chromate reducing raw material because - the ferrogypsum has significantly better handling charac¬ teristics than green salt, and at least equally good handling characteristics as gypsum;
- the ferrogypsum does not negatively affect the operation of the cement mill with baked-on deposits and the like, as is the case when using green salt and gypsum individu¬ ally;
- the divalent iron in the ferrogypsum is only oxidated to an insignificant degree to trivalent iron during the milling process, which can be done by direct addition of wet green salt and gypsum individually.
The invention permits the replacement of two additives by a single additive which provides appreciable advantages as regards transport and economy. No extra investments are required for the addition of ferrous sulfate in each produc¬ tion line, as is the case with separate addition of ferrous sulfate and gypsum. Rather, existing equipment is used.
By virtue of the fact that the common dosing will assure that the total weight of gypsum and green salt is constant, the fluctuations in sulfate content in the cement which would otherwise arise due to uneven dosing of ferrous sul¬ fate are largely eliminated. The dosing of the ferrous sulfate thus does not need to be as exact as when the ferrous sulfate and gypsum are added separately to the cement mill.
It is also possible to centralize the mixing of ferrogypsum to a location from which it can be distributed to a number of cement plants, thus profiting from the economies of scale over separate handling of ferrous sulfate and gypsum. The mixing can be done on a larger scale, water transport can be
OMPI
done in fewer and larger boats, and the existing receiving and storage system for gypsum at the cement plant can be used.
The present invention thus provides a simple method for producing a cement with significantly reduced risk of chromium eczema, without changing existing production lines, by using an inexpensive waste product, and the finished cement has equally good properties as cement without the addition, and at the same time without risk of causing chromium eczema.
OMPI
Claims
1. Method of reducing eczema-inducing chromium in cement by adding ferrous sulfate, characterized in that ferrous 5 sulfate in the form of green salt without previous drying is mixed with calcium sulfate in the form of natural gypsum or chemical gypsum into a ferrogypsum with a content of ferrous sulfate heptahydrate of 2-90 % by weight and a content of calcium sulfate dihydrate of 10-98 % by weight 10 and is added to the starting materials included in the finished cement in amounts corresponding to 10-100 kg per ton of cement.
2. Method according to Claim 1, characterized in that the „5 ferrogypsum is added in the milling process.
3. Ferrogypsum for making cement with a low content of eczema-inducing chromium in water and concrete, character¬ ized in that it consists of a physical mixture of ferrous 0 sulfate in the form of raw green salt which has not been pre-dried and calcium sulfate in the form of natural gypsum or chemical gypsum, the proportion of ferrous sulfate heptahydrate being 2-90 % by weight and the proportion of calcium sulfate dihydrate 10-98 % by weight. 5
4. Ferrogypsum according to Claim 5, characterized in that the content of ferrous sulfate heptahydrate is 5-25 % by weight and the content of calcium sulfate dihydrate 75-95 % by weight. 0
5. The use of ferrogypsum according to any one of Claim 3 or 4 as an additive in the manufacture of cement with a low content of eczema-inducing, easily soluble chromium in mortar and concrete. 5
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| AU24342/84A AU2434284A (en) | 1983-01-20 | 1984-01-17 | Ferrogypsum in the manufacture of cement |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| SE8300283 | 1983-01-20 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1984002900A1 true WO1984002900A1 (en) | 1984-08-02 |
Family
ID=20349686
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/SE1984/000011 Ceased WO1984002900A1 (en) | 1983-01-20 | 1984-01-17 | A method of reducing eczema-inducing chromium in cement by adding ferrous sulfate, an additive comprising ferrous sulfate and the use of the additive |
Country Status (10)
| Country | Link |
|---|---|
| EP (1) | EP0133434A1 (en) |
| KR (1) | KR840007392A (en) |
| AU (1) | AU2434284A (en) |
| DD (1) | DD217503A5 (en) |
| GR (1) | GR79711B (en) |
| IT (1) | IT1173095B (en) |
| PL (1) | PL245835A1 (en) |
| RO (1) | RO90804B (en) |
| WO (1) | WO1984002900A1 (en) |
| YU (1) | YU9684A (en) |
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| RU2129868C1 (en) * | 1993-06-24 | 1999-05-10 | Дикерхофф Актиенгесельшафт | Method of prophylaxis of allergic responses caused by effect of water-soluble hexavalent chrome containing in cement and/or cement-containing compositions |
| EP1092690A1 (en) | 1999-10-12 | 2001-04-18 | Povazská cementáren, a.s. | Method of producing a cement with reduced content of chromium |
| EP1440954A1 (en) * | 2003-01-25 | 2004-07-28 | Ferro Duo GmbH | Chromate reduced hydraulic binder |
| EP1533287A1 (en) * | 2003-11-21 | 2005-05-25 | W.R. Grace & Co.-Conn. | Dispersion comprising tin sulfate or ferrous sulfate for reducing chromate in cement |
| EP1544182A1 (en) * | 2003-12-12 | 2005-06-22 | Kehrmann Alexander | Hydraulic binder |
| CN100441533C (en) * | 2004-02-04 | 2008-12-10 | 格雷斯公司 | A method for reducing hexavalent chromium in cement composition |
| CZ300050B6 (en) * | 2005-09-30 | 2009-01-21 | Peringer@František | Treatment process of handling properties of heptahydrated iron sulfate, particularly reduction of hygroscopic properties thereof |
| ES2316283A1 (en) * | 2007-05-31 | 2009-04-01 | Fertisac, S.L. | Procedure for the manufacture of granulated ferrous sulphate as an additive for cementers (Machine-translation by Google Translate, not legally binding) |
| US7717999B1 (en) | 2008-12-24 | 2010-05-18 | The National Titanium Dioxide, Co., Ltd. (Cristal) | Titanium production waste byproduct as partial cement replacement |
| EP1648840B2 (en) † | 2003-07-17 | 2019-01-09 | crenox GmbH | Reducing agent for the soluble chromate content of cement and methods for the production thereof |
| CN113060948A (en) * | 2021-04-01 | 2021-07-02 | 重庆康尼睿能商贸有限公司 | Cement raw meal and preparation method of cement |
| CN113072318A (en) * | 2021-04-25 | 2021-07-06 | 湖北新洋丰新型建材科技有限公司 | Spherical phosphogypsum and preparation method and application thereof |
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| US8076175B2 (en) | 2008-02-25 | 2011-12-13 | Suniva, Inc. | Method for making solar cell having crystalline silicon P-N homojunction and amorphous silicon heterojunctions for surface passivation |
| CN111099849A (en) * | 2019-12-26 | 2020-05-05 | 安徽迪诺环保新材料科技有限公司 | Titanium gypsum building cement mortar and preparation method thereof |
| CN111807749B (en) * | 2020-06-11 | 2022-04-12 | 内蒙古同佳技术发展有限公司 | Hexavalent chromium reducing agent and preparation method thereof |
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|---|---|---|---|---|
| US2307270A (en) * | 1940-08-04 | 1943-01-05 | Mellon Inst Of Ind Res | Building material |
| US3425892A (en) * | 1965-10-22 | 1969-02-04 | Grace W R & Co | Cement set retarder |
| EP0054314A1 (en) * | 1980-12-17 | 1982-06-23 | Aktieselskabet Aalborg Portland-Cement-Fabrik | A method and a plant for producing a dry cement composition |
| WO1984001942A1 (en) * | 1982-11-17 | 1984-05-24 | Aalborg Portland Cement | Methods of producing a dry cement mixture and a free flowing ferrous sulphate hydrate product and products prepared by the methods |
-
1984
- 1984-01-17 AU AU24342/84A patent/AU2434284A/en not_active Abandoned
- 1984-01-17 GR GR73541A patent/GR79711B/el unknown
- 1984-01-17 WO PCT/SE1984/000011 patent/WO1984002900A1/en not_active Ceased
- 1984-01-17 EP EP84900553A patent/EP0133434A1/en not_active Withdrawn
- 1984-01-20 IT IT19258/84A patent/IT1173095B/en active
- 1984-01-20 YU YU00096/84A patent/YU9684A/en unknown
- 1984-01-20 DD DD84259515A patent/DD217503A5/en unknown
- 1984-01-20 KR KR1019840000257A patent/KR840007392A/en not_active Withdrawn
- 1984-01-20 PL PL24583584A patent/PL245835A1/en unknown
- 1984-09-20 RO RO115758A patent/RO90804B/en unknown
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US2307270A (en) * | 1940-08-04 | 1943-01-05 | Mellon Inst Of Ind Res | Building material |
| US3425892A (en) * | 1965-10-22 | 1969-02-04 | Grace W R & Co | Cement set retarder |
| EP0054314A1 (en) * | 1980-12-17 | 1982-06-23 | Aktieselskabet Aalborg Portland-Cement-Fabrik | A method and a plant for producing a dry cement composition |
| WO1984001942A1 (en) * | 1982-11-17 | 1984-05-24 | Aalborg Portland Cement | Methods of producing a dry cement mixture and a free flowing ferrous sulphate hydrate product and products prepared by the methods |
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| Title |
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| Chemical Abstracts, Vol 88 (1978) abstract No. 140777a, Nordisk Betong, 1977, 6, 28-30. * |
| Chemical Abstracts, Vol.79 (1973), abstract No. 96214c, Acta Derum - Venereol, 1973, 53 (4), 267-270. * |
Cited By (18)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| RU2129868C1 (en) * | 1993-06-24 | 1999-05-10 | Дикерхофф Актиенгесельшафт | Method of prophylaxis of allergic responses caused by effect of water-soluble hexavalent chrome containing in cement and/or cement-containing compositions |
| EP1092690A1 (en) | 1999-10-12 | 2001-04-18 | Povazská cementáren, a.s. | Method of producing a cement with reduced content of chromium |
| EP1440954A1 (en) * | 2003-01-25 | 2004-07-28 | Ferro Duo GmbH | Chromate reduced hydraulic binder |
| EP1648840B2 (en) † | 2003-07-17 | 2019-01-09 | crenox GmbH | Reducing agent for the soluble chromate content of cement and methods for the production thereof |
| EP2143698A1 (en) * | 2003-11-21 | 2010-01-13 | W.R. Grace & Co.-Conn. | Dispersion comprising tin sulfate or ferrous sulfate for reducing chromate in cement |
| EP1533287A1 (en) * | 2003-11-21 | 2005-05-25 | W.R. Grace & Co.-Conn. | Dispersion comprising tin sulfate or ferrous sulfate for reducing chromate in cement |
| US7128782B2 (en) | 2003-11-21 | 2006-10-31 | W.R. Grace & Co.-Conn. | Sulfate dispersion chromate reducer |
| JP2007522061A (en) * | 2003-11-21 | 2007-08-09 | ダブリュー・アール・グレイス・アンド・カンパニー−コネチカット | Sulfate-dispersed chromate reducing agent |
| EP1544182A1 (en) * | 2003-12-12 | 2005-06-22 | Kehrmann Alexander | Hydraulic binder |
| WO2005056491A1 (en) * | 2003-12-12 | 2005-06-23 | Kerr-Mcgee Pigments International Gmbh | Hydraulic binder and a chromate reducer and use thereof |
| CN100441533C (en) * | 2004-02-04 | 2008-12-10 | 格雷斯公司 | A method for reducing hexavalent chromium in cement composition |
| CZ300050B6 (en) * | 2005-09-30 | 2009-01-21 | Peringer@František | Treatment process of handling properties of heptahydrated iron sulfate, particularly reduction of hygroscopic properties thereof |
| ES2316283A1 (en) * | 2007-05-31 | 2009-04-01 | Fertisac, S.L. | Procedure for the manufacture of granulated ferrous sulphate as an additive for cementers (Machine-translation by Google Translate, not legally binding) |
| ES2316283B1 (en) * | 2007-05-31 | 2010-02-05 | Fertisac, S.L. | MANUFACTURING PROCEDURE OF GRANULATED FERROUS SULPHATE AS ADDITIVE FOR CEMETERIES. |
| US7717999B1 (en) | 2008-12-24 | 2010-05-18 | The National Titanium Dioxide, Co., Ltd. (Cristal) | Titanium production waste byproduct as partial cement replacement |
| US7824322B2 (en) | 2008-12-24 | 2010-11-02 | The National Titanium Dioxide, Co. Ltd. (Cristal) | Titanium production waste byproduct as partial cement replacement |
| CN113060948A (en) * | 2021-04-01 | 2021-07-02 | 重庆康尼睿能商贸有限公司 | Cement raw meal and preparation method of cement |
| CN113072318A (en) * | 2021-04-25 | 2021-07-06 | 湖北新洋丰新型建材科技有限公司 | Spherical phosphogypsum and preparation method and application thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| KR840007392A (en) | 1984-12-07 |
| YU9684A (en) | 1986-08-31 |
| IT1173095B (en) | 1987-06-18 |
| GR79711B (en) | 1984-10-31 |
| PL245835A1 (en) | 1985-01-30 |
| EP0133434A1 (en) | 1985-02-27 |
| RO90804A (en) | 1987-01-30 |
| RO90804B (en) | 1987-01-31 |
| IT8419258A0 (en) | 1984-01-20 |
| AU2434284A (en) | 1984-08-15 |
| DD217503A5 (en) | 1985-01-16 |
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