GB2159510A - Process for the production of calcium hydrogen phosphate dihydrate and/or anhydrous calcium hydrogen phosphate - Google Patents
Process for the production of calcium hydrogen phosphate dihydrate and/or anhydrous calcium hydrogen phosphate Download PDFInfo
- Publication number
- GB2159510A GB2159510A GB08512556A GB8512556A GB2159510A GB 2159510 A GB2159510 A GB 2159510A GB 08512556 A GB08512556 A GB 08512556A GB 8512556 A GB8512556 A GB 8512556A GB 2159510 A GB2159510 A GB 2159510A
- Authority
- GB
- United Kingdom
- Prior art keywords
- calcium
- solution
- ammonia
- hydrogen phosphate
- ammonium
- 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.)
- Granted
Links
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 25
- 235000019700 dicalcium phosphate Nutrition 0.000 title claims abstract description 24
- 238000000034 method Methods 0.000 title claims abstract description 24
- FUFJGUQYACFECW-UHFFFAOYSA-L calcium hydrogenphosphate Chemical compound [Ca+2].OP([O-])([O-])=O FUFJGUQYACFECW-UHFFFAOYSA-L 0.000 title claims abstract description 17
- XAAHAAMILDNBPS-UHFFFAOYSA-L calcium hydrogenphosphate dihydrate Chemical compound O.O.[Ca+2].OP([O-])([O-])=O XAAHAAMILDNBPS-UHFFFAOYSA-L 0.000 title claims abstract description 10
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 claims abstract description 54
- 239000000243 solution Substances 0.000 claims abstract description 29
- 229910021529 ammonia Inorganic materials 0.000 claims abstract description 27
- 159000000007 calcium salts Chemical class 0.000 claims abstract description 23
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000000047 product Substances 0.000 claims abstract description 18
- 239000012266 salt solution Substances 0.000 claims abstract description 16
- CDBYLPFSWZWCQE-UHFFFAOYSA-L Sodium Carbonate Chemical compound [Na+].[Na+].[O-]C([O-])=O CDBYLPFSWZWCQE-UHFFFAOYSA-L 0.000 claims abstract description 10
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims abstract description 10
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000002244 precipitate Substances 0.000 claims abstract description 10
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims abstract description 9
- 239000000920 calcium hydroxide Substances 0.000 claims abstract description 9
- 239000000292 calcium oxide Substances 0.000 claims abstract description 9
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims abstract description 8
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims abstract description 8
- BRPQOXSCLDDYGP-UHFFFAOYSA-N calcium oxide Chemical compound [O-2].[Ca+2] BRPQOXSCLDDYGP-UHFFFAOYSA-N 0.000 claims abstract description 8
- 150000003863 ammonium salts Chemical class 0.000 claims abstract description 6
- 238000006243 chemical reaction Methods 0.000 claims abstract description 5
- 239000000725 suspension Substances 0.000 claims abstract description 5
- 230000018044 dehydration Effects 0.000 claims abstract description 4
- 238000006297 dehydration reaction Methods 0.000 claims abstract description 4
- 230000007062 hydrolysis Effects 0.000 claims abstract description 4
- 238000006460 hydrolysis reaction Methods 0.000 claims abstract description 4
- 238000009621 Solvay process Methods 0.000 claims abstract description 3
- LFVGISIMTYGQHF-UHFFFAOYSA-N ammonium dihydrogen phosphate Chemical compound [NH4+].OP(O)([O-])=O LFVGISIMTYGQHF-UHFFFAOYSA-N 0.000 claims abstract description 3
- 229910000387 ammonium dihydrogen phosphate Inorganic materials 0.000 claims abstract description 3
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 claims abstract description 3
- 235000019837 monoammonium phosphate Nutrition 0.000 claims abstract description 3
- 239000003381 stabilizer Substances 0.000 claims abstract description 3
- 239000000203 mixture Substances 0.000 claims description 15
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 13
- 239000000908 ammonium hydroxide Substances 0.000 claims description 13
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 claims description 8
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 claims description 6
- 238000011084 recovery Methods 0.000 claims description 6
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 4
- 235000019270 ammonium chloride Nutrition 0.000 claims description 4
- 239000001110 calcium chloride Substances 0.000 claims description 4
- 229910001628 calcium chloride Inorganic materials 0.000 claims description 4
- 229910000019 calcium carbonate Inorganic materials 0.000 claims description 3
- 239000001506 calcium phosphate Substances 0.000 claims description 3
- 229910000389 calcium phosphate Inorganic materials 0.000 claims description 3
- 235000011010 calcium phosphates Nutrition 0.000 claims description 3
- 238000010790 dilution Methods 0.000 claims description 3
- 239000012895 dilution Substances 0.000 claims description 3
- 229910052588 hydroxylapatite Inorganic materials 0.000 claims description 3
- XYJRXVWERLGGKC-UHFFFAOYSA-D pentacalcium;hydroxide;triphosphate Chemical compound [OH-].[Ca+2].[Ca+2].[Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O XYJRXVWERLGGKC-UHFFFAOYSA-D 0.000 claims description 3
- 239000007790 solid phase Substances 0.000 claims description 3
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 claims description 3
- 238000005406 washing Methods 0.000 claims description 3
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 claims description 2
- 239000000347 magnesium hydroxide Substances 0.000 claims description 2
- 229910001862 magnesium hydroxide Inorganic materials 0.000 claims description 2
- 239000000395 magnesium oxide Substances 0.000 claims description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 2
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 claims description 2
- 238000000746 purification Methods 0.000 claims description 2
- 239000011780 sodium chloride Substances 0.000 claims description 2
- 239000000126 substance Substances 0.000 claims description 2
- 239000002351 wastewater Substances 0.000 claims description 2
- ABLZXFCXXLZCGV-UHFFFAOYSA-N Phosphorous acid Chemical compound OP(O)=O ABLZXFCXXLZCGV-UHFFFAOYSA-N 0.000 claims 1
- 239000002699 waste material Substances 0.000 abstract description 5
- 235000011116 calcium hydroxide Nutrition 0.000 description 5
- 235000012255 calcium oxide Nutrition 0.000 description 5
- 238000001556 precipitation Methods 0.000 description 4
- 150000003839 salts Chemical class 0.000 description 4
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 3
- 229910052791 calcium Inorganic materials 0.000 description 3
- 239000011575 calcium Substances 0.000 description 3
- 239000002994 raw material Substances 0.000 description 3
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 239000006227 byproduct Substances 0.000 description 2
- 239000000706 filtrate Substances 0.000 description 2
- 238000001914 filtration Methods 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- FQENQNTWSFEDLI-UHFFFAOYSA-J sodium diphosphate Chemical compound [Na+].[Na+].[Na+].[Na+].[O-]P([O-])(=O)OP([O-])([O-])=O FQENQNTWSFEDLI-UHFFFAOYSA-J 0.000 description 2
- 239000003643 water by type Substances 0.000 description 2
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 241001072332 Monia Species 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- -1 alkali metal salt Chemical class 0.000 description 1
- 239000007900 aqueous suspension Substances 0.000 description 1
- 238000005119 centrifugation Methods 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000002537 cosmetic Substances 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 238000000227 grinding Methods 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 229910001629 magnesium chloride Inorganic materials 0.000 description 1
- 239000008267 milk Substances 0.000 description 1
- 210000004080 milk Anatomy 0.000 description 1
- 235000013336 milk Nutrition 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000001376 precipitating effect Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000009290 primary effect Effects 0.000 description 1
- 239000012047 saturated solution Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000007669 thermal treatment Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B25/00—Phosphorus; Compounds thereof
- C01B25/16—Oxyacids of phosphorus; Salts thereof
- C01B25/26—Phosphates
- C01B25/32—Phosphates of magnesium, calcium, strontium, or barium
- C01B25/322—Preparation by neutralisation of orthophosphoric acid
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B25/00—Phosphorus; Compounds thereof
- C01B25/16—Oxyacids of phosphorus; Salts thereof
- C01B25/26—Phosphates
- C01B25/32—Phosphates of magnesium, calcium, strontium, or barium
- C01B25/325—Preparation by double decomposition
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Pharmaceuticals Containing Other Organic And Inorganic Compounds (AREA)
- Fertilizers (AREA)
- Removal Of Specific Substances (AREA)
- Cosmetics (AREA)
Abstract
Phosphoric acid, a water-soluble calcium salt and ammonia are brought into reaction, from the obtained suspension a precipitate is separated, which precipitate is processed into the product. Ammonia and a water-soluble calcium salt solution is recovered from the remaining solution by means of calcium oxide or calcium hydroxide, which ammonia and water-soluble calcium salt solution can be partly or totally returned into the process. A waste calcium chloride solution, which solution issues in the production of soda by the Solvay process, can be employed, either directly or after having been concentrated, as a water-soluble calcium salt, it being economical to interconnect a plant for manufacturing calcium hydrogen phosphate with a plant for manufacturing soda. Instead of starting from a water-soluble calcium salt and ammonia, one can also start from an ammoniacal calcium salt solution formed by the reaction of calcium oxide or calcium hydroxide with an ammonium salt solution. A part or the whole of the phosphoric acid and a part or the whole of the ammonia can be replaced by ammonium hydrogen phosphate and/or ammonium dihydrogen phosphate. In order to slow down the dehydration of the calcium hydrogen phosphate dihydrate and the hydrolysis of the anhydrous calcium hydrogen phosphate, it is useful to add stabilizers during the manufacture.
Description
SPECIFICATION
Process for the production of calcium hydrogen phosphate dihydrate and/or anhydrous calcium hydrogen phosphate
This invention relates to a process for the production of calcium hydrogen phosphate dihydrate and/ or anhydrous calcium hydrogen phosphate and/or a mixture thereof and/or in mixture with hydroxyapatite and/or calcium phosphate and/or calcium carbonate.
Due to their simplicity, the precipitation methods are the most widely employed methods for the preparation of the above mentioned products.
Most commonly one starts when carrying them out, from waste, water-soluble calcium salts which salts are purified, according to need, or these salts are prepared by decomposition of limestone with the respective acid, high demands being mostly made on the purity of the starting calcium raw material. A by-product of the precipitation is the ammonium or the alkali metal salt.
As is thus evident, a drawback of the up to currently employed production processes consist above all in that the quality of the product depends on the purity of the starting calcium raw material and that there results a secondary waste in form of a diluted solution which waste can be utilized with difficulty only.
These disadvantages are avoided by the process for the production of calcium hydrogen phosphate do hydrate and/or anhydrous calcium hydrogen phosphate and/or a mixture thereof and/or in mixture with hydroxyapatite and/or calcium phosphate and/or calcium carbonate which process is characterized in that it starts from trihydrogen phosphoric acid, a water-soluble calcium salt and ammonia and/or ammonium hydroxide which are brought into reaction, from the obtained suspension the precipitate is removed which precipitate is processed into the product, from a part or all of the remaining solution ammonia and/or ammonium hydroxide and a water-soluble calcium salt solution is recovered by means of calcium oxide and/or calcium hydroxide or a mixture thereof or a mixture of these substances with magnesium oxide and/or magnesium hydroxide, a part or all of the water-soluble calcium salt solution and/or the ammonium hydroxide being, if desired, returned into the process.
According to a further feature of the invention, a solution which issues from the recovery of ammonia from lyes arising in the production of soda by the Solvay process, which solution contains mainly calcium chloride, is employed as a water-soluble calcium salt.
According to a further feature of the invention, instead of the solution of calcium chloride issuing from the recovery of ammonia from lyes arising in the production of soda, this solution is employed after concentrating and/or concentrating and reducing the sodium content thereof.
According to a further feature of the invention, in the preceding two processes, ammonia and/or am
monium hydroxide is recovered in soda production
from a part or all of the solution containing mainly
ammonium chloride which remains after removing
the precipitated product.
According to a further feature of the invention,
instead of the water-soluble calcium salt and am
monia and/or ammonium hydroxide, an ammonia
cal calcium salt solution is employed, which
solution is obtained in that calcium oxide and/or
calcium hydroxide or a mixture thereof and an am
monium salt solution are reacted, the remaining
solid phase is removed and the obtained solution
is ammoniacalized, if desired.
According to a further feature of the invention, a
part or all of the trihydrogen phosphoric acid and a
part or all of the ammonia and/or a part or all of the ammonium hydroxide is replaced, directly or after purification thereof, by ammonium dihydro
gen phosphate and/or ammonium hydrogen phos
phate.
According to a further feature of the invention, the dilution of trihydrogen phosphoric acid is car
ried out by waste waters arising from washing the precipitated product and/or by a solution contain
ing ammonium salt.
According to a further feature of the invention, stabilizers slowing down the dehydration of calcium hydrogen phosphate dihydrate and/or the hydrolysis of anhydrous calcium hydrogen phosphate are added.
The primary effect of the production process according to this invention consists in that it is not necessary to start from calcium raw materials of high purity, and that no undesirable salts, as byproducts, are formed. When combining the production of calcium hydrogen phosphate with the production of soda, a part of the machinery for producing both products can be shared what is, from the standpoint of investment, and operating costs, advantageous. In this manner, the production process according to this invention becomes, against other hitherto known processes, economically distinctly more advantageous.
The production can be continuous, discontinuous or a combination of both. One proceeds for instance so that a trihydrogen phosphoric acid solution having a concentration of 1% - 95% by weight, a water-soluble calcium salt solution having a concentration of 1% by weight to a saturated solution thereof, at a given temperature, and ammonia and/ or ammonium hydroxide are mixed together at the same time or successively, in one or more stages, a dilution being made at the same time if desired.
The temperature ranges in dependence of the required composition of the product from 0 C to the boiling point. The formed precipitate is removed for instance by filtration or centrifugation, washed and dried, if necessary partly or wholly dehydrated by thermal treatment to obtain the product of desired composition. Ammonia and the water-soluble calcium salt is recovered from the remaining solution containing the ammonium salt by means of calcium oxide or calcium hydroxide or a mixture thereof in solid state or in water suspension, for instance in form of burnt lime and/or hydrated lime or lime milk. Ammonia and/or ammonium hydroxide and the water-soluble calcium salt solution can be, after elimination of mechanical impurities, if need be, and after optional concentration and cooling, partly or wholly returned into the process.The washing waters can be incorporated into the production cycle. The additives slowing down the dehydration of calcium hydrogen phosphate dihydrate and/or the hydrolysis of anhydrous calcium hydrogen phosphate, for instance sodium diphosphate, are preferably dosed into the solutions led to the precipitation and/or directly into the precipitating apparatus and/or into the damp or dry product and/or in the optional adjustment of the particle size by grinding.
The process according to the invention is illustrated by the following examples.
Example I
A 10% calcium chloride solution was mixed in an agitated batch type reactor with an equimolar quantity of trihydrogen phosphoric acid having a concentration of 85% by weight. The pH was adjusted by gaseous ammonia to 7. The temperature did not exceed 30"C. The resulting precipitate was filtered off, washed and dried at 40 C. The obtained product was calcium hydrogen phosphate dihydrate. The filtrate and the wash waters were introduced together with calcium oxide employed in an amount corresponding to an 0.5% excess over stoichiometry, as related to ammonium chloride, into a recovering apparatus. In said apparatus, a temperature of the boiling point of the solution was maintained.From the suspension leaving the recovering apparatus, mechanical impurities were removed, and clear filtrate, after having been concentrated and cooled, was employed together with recovered ammonia for the precipitation again.
Example 2
The process was operated in the same manner as in Example 1 except that instead of the 10% calcium chloride solution, a waste solution issuing from the recovery of ammonia from lyes arising in the production of soda, by means of lime which solution contains as main components calcium chloride, sodium chloride and magnesium chloride, was employed.
Example 3
The production process was the same as in Example 1 except that the temperature in the reactor was maintained at 80"C and the precipitate was dehydrated by heating at a temperature of 115 C.
The product was anhydrous calcium hydrogen phosphate.
Example 4
To a solution of ammonium chloride having a concentration of 10% by weight calcium hydrate was added in a quantity representing a 10% excess over stoichoimetry. The suspension was agitated in a closed vessel at a temperature of 70"C during 20 minutes whereupon it was cooled to 20"C and separated by filtration into a solution and a solid phase. A ciear ammoniacal calcium salt solution was mixed in an agitated batch type reactor with trihydrogen phosphoric acid having a concentration of 75% by weight in stoichoimetric ratio with regard to the production of calcium hydrogen phosphate. The temperature of the reaction was maintained at 300C. The resulting precipitate was filtered off, washed, mixed with a solution of sodium diphosphate, which contained 1% of said salt as related to the dry product weight, and dried at 40 C.
There was obtained calcium hydrogen phosphate dihydrate as product.
The obtained products are useful for use in cosmetics, foodstuffs and pharmaceuticals producing industries and as enriching additives in feeding mixtures for animals.
Claims (9)
1. A process for the production of calcium hydrogen phosphate dihydrate and/or anhydrous calcium hydrogen phosphate and/or a mixture thereof and/or in mixture with hydroxyapatite and/or with calcium phosphate and/or with calcium carbonate, in which trihydrogen phosphoric acid, a water-soluble calcium salt and ammonia and/or ammonium hydroxide are reacted, from the obtained suspension a precipitate is separated, which precipitate is processed into the products, from a part or from the entire remaining solution ammonia and/or ammonium hydroxide and a water-soluble calcium salt solution is recovered by means of calcium oxide and/or calcium hydroxide or a mixture of said substances with magnesium oxide and/or magnesium hydroxide, a part or all of the water-soluble calcium salt solution and/or a part or all of the ammonia and/or a part or all of the ammonium hydroxide being, if desired, returned into the process.
2. A process according to claim 1, wherein a solution which issues from the recovery of ammonia from lyes arising in the production of soda by the Solvay process, containing mainly calcium chloride, is employed as the water-soluble calcium salt.
3. A process according to claim 2, wherein instead of the calcium chloride solution issuing from the recovery of ammonia from lyes arising in the production of soda, this solution is employed after its concentrating and/or its concentrating and reducing the sodium chloride content thereof.
4. A process according to claim 2 or 3, wherein ammonia and/or ammonium hydroxide is recovered in soda production from a part or all of the solution containing mainly ammonium chloride, which solution remains after removing the precipitated product.
5. A process according to any one of claims 1 to 3, wherein instead of the water-soluble calcium salt and ammonia and/or ammonium hydroxide, an ammoniacal calcium salt solution is employed, which solution is obtained in the recovery of ammonia from an ammonium salt solution in that calcium oxide and/or calcium hydroxide or a mixture thereof and an ammonium salt solution are brought into reaction, the remaining solid phase is removed and the obtained solution is ammoniacalized, if desired.
6. A process according to any one of claims 1 to 5, wherein a part or all of the trihydrogen phosphonic acid and a part or all of the ammonia and/or a part or all of the ammonium hydroxide is replaced, directly or after the purification thereof, by ammonium dihydrogen phosphate and/or ammonium hydrogen phosphate.
7. A process according to any one of claims 1 to 6, wherein the dilution of trihydrogen phosphoric acid is carried out by waste waters arising from washing the precipitated product and/or by a solution containing ammonium salt.
8. A process according to any one of claims 1 to 7, wherein stabilizers slowing down the dehydration of calcium hydrogen phosphate dihydrate and/or the hydrolysis of anhydrous calcium hydrogen phosphate are added.
9. A process according to claim 1 substantially as herein described with reference to Examples 1 to 4.
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CS393584A CS246515B1 (en) | 1984-05-25 | 1984-05-25 | Production method of dihydrate and/or waterless hydrogenphosphate |
| CS393884A CS247512B1 (en) | 1984-05-25 | 1984-05-25 | Method of dihydrate or/and anhydrous hydrogen calcium phosphate production |
| CS46685A CS247432B1 (en) | 1985-01-23 | 1985-01-23 | Method of dihydrate or/and anhydrous calcium hydrogen phosphate production |
Publications (3)
| Publication Number | Publication Date |
|---|---|
| GB8512556D0 GB8512556D0 (en) | 1985-06-19 |
| GB2159510A true GB2159510A (en) | 1985-12-04 |
| GB2159510B GB2159510B (en) | 1988-10-26 |
Family
ID=27179295
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| GB08512556A Expired GB2159510B (en) | 1984-05-25 | 1985-05-17 | Process for the production of anhydrous calcium hydrogen phosphates |
Country Status (7)
| Country | Link |
|---|---|
| DE (1) | DE3517608A1 (en) |
| FR (1) | FR2564817B1 (en) |
| GB (1) | GB2159510B (en) |
| HU (1) | HU201496B (en) |
| IT (1) | IT1183673B (en) |
| NL (1) | NL8501303A (en) |
| YU (1) | YU87585A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115010106B (en) * | 2022-06-07 | 2024-04-05 | 武汉工程大学 | A method for recovering phosphorus from reclaimed water and preparing feed-grade calcium hydrogen phosphate |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB787361A (en) * | 1955-02-22 | 1957-12-04 | Acec | Process for the manufacture of dibasic alkaline-earth metal phosphates and luminescent powders containing such phosphates |
| GB939104A (en) * | 1960-04-07 | 1963-10-09 | Gen Electric Co Ltd | Improvements in or relating to the manufacture of phosphors |
| GB1165578A (en) * | 1965-12-29 | 1969-10-01 | Sylvania Electric Prod | Process for Making Brushite. |
| US3505012A (en) * | 1968-04-11 | 1970-04-07 | Sylvania Electric Prod | Process for making brushite form of calcium hydrogen phosphate |
| GB1389712A (en) * | 1971-11-15 | 1975-04-09 | Prorea | Production of chemical products in high yield |
| GB2053871A (en) * | 1979-07-20 | 1981-02-11 | Bitepazh J A | Method for producing calcium phosphate catalyst |
-
1985
- 1985-05-08 NL NL8501303A patent/NL8501303A/en not_active Application Discontinuation
- 1985-05-15 DE DE19853517608 patent/DE3517608A1/en not_active Withdrawn
- 1985-05-17 GB GB08512556A patent/GB2159510B/en not_active Expired
- 1985-05-20 FR FR8507570A patent/FR2564817B1/en not_active Expired
- 1985-05-24 YU YU00875/85A patent/YU87585A/en unknown
- 1985-05-24 HU HU851997A patent/HU201496B/en not_active IP Right Cessation
- 1985-05-24 IT IT20868/85A patent/IT1183673B/en active
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB787361A (en) * | 1955-02-22 | 1957-12-04 | Acec | Process for the manufacture of dibasic alkaline-earth metal phosphates and luminescent powders containing such phosphates |
| GB939104A (en) * | 1960-04-07 | 1963-10-09 | Gen Electric Co Ltd | Improvements in or relating to the manufacture of phosphors |
| GB1165578A (en) * | 1965-12-29 | 1969-10-01 | Sylvania Electric Prod | Process for Making Brushite. |
| US3505012A (en) * | 1968-04-11 | 1970-04-07 | Sylvania Electric Prod | Process for making brushite form of calcium hydrogen phosphate |
| GB1263570A (en) * | 1968-04-11 | 1972-02-09 | Gte Sylvania Inc | Process for making the brushite form of calcium hydrogen phosphate |
| GB1389712A (en) * | 1971-11-15 | 1975-04-09 | Prorea | Production of chemical products in high yield |
| GB2053871A (en) * | 1979-07-20 | 1981-02-11 | Bitepazh J A | Method for producing calcium phosphate catalyst |
Also Published As
| Publication number | Publication date |
|---|---|
| NL8501303A (en) | 1985-12-16 |
| GB2159510B (en) | 1988-10-26 |
| FR2564817A1 (en) | 1985-11-29 |
| FR2564817B1 (en) | 1988-08-19 |
| IT1183673B (en) | 1987-10-22 |
| HUT39685A (en) | 1986-10-29 |
| IT8520868A0 (en) | 1985-05-24 |
| YU87585A (en) | 1988-02-29 |
| DE3517608A1 (en) | 1985-11-28 |
| GB8512556D0 (en) | 1985-06-19 |
| HU201496B (en) | 1990-11-28 |
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