BE423658A - - Google Patents
Info
- Publication number
- BE423658A BE423658A BE423658DA BE423658A BE 423658 A BE423658 A BE 423658A BE 423658D A BE423658D A BE 423658DA BE 423658 A BE423658 A BE 423658A
- Authority
- BE
- Belgium
- Prior art keywords
- granules
- salt
- water
- size
- produced
- Prior art date
Links
- 150000003839 salts Chemical class 0.000 claims description 11
- 239000008187 granular material Substances 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 7
- 239000000126 substance Substances 0.000 claims description 6
- 238000004519 manufacturing process Methods 0.000 claims description 5
- 150000001450 anions Chemical class 0.000 claims description 2
- 150000001768 cations Chemical class 0.000 claims description 2
- 239000000243 solution Substances 0.000 description 7
- 238000006073 displacement reaction Methods 0.000 description 4
- 239000007788 liquid Substances 0.000 description 3
- 229910002651 NO3 Inorganic materials 0.000 description 2
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 239000012895 dilution Substances 0.000 description 2
- 238000010790 dilution Methods 0.000 description 2
- VWDWKYIASSYTQR-UHFFFAOYSA-N sodium nitrate Chemical compound [Na+].[O-][N+]([O-])=O VWDWKYIASSYTQR-UHFFFAOYSA-N 0.000 description 2
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 1
- 235000011941 Tilia x europaea Nutrition 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000004571 lime Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 239000013535 sea water Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 235000010344 sodium nitrate Nutrition 0.000 description 1
- 239000004317 sodium nitrate Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J39/00—Cation exchange; Use of material as cation exchangers; Treatment of material for improving the cation exchange properties
- B01J39/02—Processes using inorganic exchangers
Landscapes
- Chemical & Material Sciences (AREA)
- Inorganic Chemistry (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
- Treatment Of Water By Ion Exchange (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Description
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Procédé perfectionné pour la fabrication de Sels à l'aide de substances échangeant leurs bases.
Par des brevets qui sont la propriété de la demanderesse, il est connu de produire des sels à l'aide de substances convenables échangeant leurs bases, en faisant passer successivement à travers une couche de la substance d'échange de bases une solution contenant le même anion que le sel à produire, de l'eau, une solution contenant le même cation que le sel à produire, de l'eau etc... ce qui provoque un échange de bases dont le résultat est,' d'une façon alternante, la formation d'une solution du sel désiré sous une concentration qui est suffisamment élevée pour permettre la
<Desc/Clms Page number 2>
production du sel par cristallisation et la régénération de la substance d'échange de bases.
Ce procédé se prête particulièrement à la fabri- cation du nitrate de sodium par l'application du nitrate de chaux ( en solution concentrée) et du chlorure de sodium (par exemple sous forme d'eau de mer ordinaire); - voir le brevet français No 738.253 du 7 juin 1932.
Dans le brevet français No. 773.973 du 29 mai 1934, on a spécifié un certain nombre de détails qui présentent de l'importance en ce qui concerne la réalisation du procédé - mentionné ci-dessus en vue de la production de sels. Il est spécifié dans ce brevet qu'il est d'importance vitale, pour la réalisation du procédé en pratique, d'empêcher autant que possible le mélange des deux solutions de sel ainsi que leur dilution par l'eau adjacente. Pour remplir ces conditions contradictoires, il est important de faire en sorte que les liquides se meuvent à travers la céolite de telle manière qu'ils se déplacent autant que possible en parallélisme ; et la présente invention a pour objet un moyen d'assurer un tel déplacement parallèle.
On a découvert que la grosseur des granules de céolite utilisés est d'importance primordiale en ce qui concerne le déplacement parallèle, et le procédé qui fait l'objet de cette invention réside dans l'application de granules de grosseur comprise entre 0,3 mm et I mm, et de préférence entre 0,45 mm et 0,85 mm.
A condition que la grosseur des granules soit la même en tous les points, la perfection du déplacement parallèle augmente à mesure que cette grosseur diminue.
Toutefois, en mêmetemsp la résistance offerte au mouvenet du liquide augmente a mesure que la grosseur des granules diminue. Or, il a été démontré expérimentalement que, avec
<Desc/Clms Page number 3>
des granules au-dessous de 0, 3 mm la résistance devient si grande que la vitesse du liquide devient beaucoup trop faible pour l'utilisation pratique du procédé. Avec des granules de plus de 1 mm, les vides constitués entre les granules deviennent si grands que les solutions se mélange-nt trop avec l'eau adjacente et que, de ce fait, leur dilution atteint un degré trop élevé. Les conditions les plus défavorables sont celles qui se présentent lorsqu'une solution concentrée de sel, par exemple de nitrate de chaux5 se trouve immédiatement audessus d'eau pure.
Des parties de la solution lourde sont alors très sujettes à descendre en suivant des chemins irré- guliers à travers les granules de céolite et à provoquer ainsi un déplacement parallèle imparfait.
Tout bien considéré, on a trouvé que la grosseur de granule qui donne les meilleurs résultats est comprise entre 0,45 mm. et 0 85 mm.
<Desc / Clms Page number 1>
Improved process for the manufacture of salts using substances exchanging their bases.
By patents which are the property of the applicant, it is known to produce salts using suitable substances exchanging their bases, by successively passing through a layer of the base exchange substance a solution containing the same anion than the salt to be produced, water, a solution containing the same cation as the salt to be produced, water etc ... which causes an exchange of bases, the result of which is, 'in an alternating manner , forming a solution of the desired salt in a concentration which is high enough to allow the
<Desc / Clms Page number 2>
production of salt by crystallization and regeneration of the base exchange substance.
This process is particularly suitable for the manufacture of sodium nitrate by applying nitrate of lime (in concentrated solution) and sodium chloride (for example in the form of ordinary sea water); - see French patent No 738,253 of June 7, 1932.
In French Patent No. 773,973 of May 29, 1934, a number of details have been specified which are of importance as regards the carrying out of the process - mentioned above for the production of salts. It is specified in this patent that it is of vital importance, for carrying out the process in practice, to prevent as much as possible the mixing of the two salt solutions as well as their dilution by adjacent water. To meet these conflicting conditions, it is important to make the liquids move through the ceolite in such a way that they move as much as possible in parallel; and the object of the present invention is a means of ensuring such parallel displacement.
It has been found that the size of the ceolite granules used is of primary importance with regard to parallel displacement, and the method which is the object of this invention is to apply granules of size between 0.3 mm and I mm, and preferably between 0.45 mm and 0.85 mm.
Provided that the size of the granules is the same at all points, the perfection of the parallel displacement increases as this size decreases.
However, at the same time the resistance offered to the movement of the liquid increases as the size of the granules decreases. However, it has been shown experimentally that, with
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granules below 0.3mm the resistance becomes so great that the liquid velocity becomes much too low for the practical use of the process. With granules of more than 1 mm, the voids formed between the granules become so large that the solutions mix too much with the adjacent water and, therefore, their dilution reaches too high a degree. The most unfavorable conditions are those which arise when a concentrated solution of salt, for example nitrate of lime5 is immediately above pure water.
Parts of the heavy solution are then very prone to descend along irregular paths through the ceolite granules and thus cause imperfect parallel displacement.
All things considered, it has been found that the granule size which gives the best results is between 0.45 mm. and 0 85 mm.
Claims (1)
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| NO487292X | 1936-09-22 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| BE423658A true BE423658A (en) |
Family
ID=19905781
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| BE423658D BE423658A (en) | 1936-09-22 |
Country Status (4)
| Country | Link |
|---|---|
| BE (1) | BE423658A (en) |
| DE (1) | DE747098C (en) |
| FR (1) | FR826635A (en) |
| GB (1) | GB487292A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE920545C (en) * | 1943-09-02 | 1954-11-25 | Norsk Hydro Elek Sk Kvaelstofa | Process for the extraction of potash from salt mixtures in aqueous solution, especially salt lake, sea water and brines |
Family Cites Families (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE371796C (en) * | 1916-10-17 | 1923-03-17 | Permutit Akt Ges | Process for the production of base-exchanging substances containing silica |
| US1527199A (en) * | 1920-10-08 | 1925-02-24 | Borromite Company Of America | Base-exchange silicate and process of preparing same |
| US1716663A (en) * | 1928-03-06 | 1929-06-11 | Pike | Process for production of potassium carbonate |
| FR739675A (en) * | 1931-06-02 | 1933-01-16 | Process for the preparation, separation and purification of salts and solutions by base exchangers | |
| GB402770A (en) * | 1931-06-02 | 1933-12-04 | Geza Austerweil | Improvements relating to processes for the separation or purification of salts, saltsolutions and other solutions |
| DE624141C (en) * | 1931-06-03 | 1936-01-14 | Luxemburgeoise Mutosel Sa | Process for the extraction of salts |
| DE612095C (en) * | 1931-12-12 | 1935-04-13 | Luxemburgeoise Mutosel Sa | Process for the production and purification of salts with double conversion with base exchangers |
| GB403077A (en) * | 1932-06-02 | 1933-12-04 | Geza Austerweil | Improvements relating to processes for the preparation, separation or purification of salts or salt solutions |
| FR788692A (en) * | 1934-04-13 | 1935-10-14 | Phillips & Pain Ets | Process for obtaining transformation products of substances containing carbon and their application to the treatment of water and salt solutions |
-
0
- BE BE423658D patent/BE423658A/fr unknown
-
1937
- 1937-09-13 FR FR826635D patent/FR826635A/en not_active Expired
- 1937-09-13 GB GB24873/37A patent/GB487292A/en not_active Expired
- 1937-09-18 DE DEN41172D patent/DE747098C/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| DE747098C (en) | 1944-09-08 |
| GB487292A (en) | 1938-06-17 |
| FR826635A (en) | 1938-04-06 |
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