CH128483A - Process for the regeneration of base-exchanging filter media in water softeners. - Google Patents
Process for the regeneration of base-exchanging filter media in water softeners.Info
- Publication number
- CH128483A CH128483A CH128483TA CH128483A CH 128483 A CH128483 A CH 128483A CH 128483T A CH128483T A CH 128483TA CH 128483 A CH128483 A CH 128483A
- Authority
- CH
- Switzerland
- Prior art keywords
- regeneration
- base
- filter media
- water softeners
- salt solution
- Prior art date
Links
- 230000008929 regeneration Effects 0.000 title claims description 10
- 238000011069 regeneration method Methods 0.000 title claims description 10
- 238000000034 method Methods 0.000 title claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims description 9
- 239000000463 material Substances 0.000 claims description 7
- 239000007788 liquid Substances 0.000 claims description 3
- 230000001172 regenerating effect Effects 0.000 claims 1
- 239000012266 salt solution Substances 0.000 description 11
- 235000002639 sodium chloride Nutrition 0.000 description 5
- 150000003839 salts Chemical class 0.000 description 4
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 3
- 238000011001 backwashing Methods 0.000 description 2
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229910052602 gypsum Inorganic materials 0.000 description 1
- 239000010440 gypsum Substances 0.000 description 1
- 239000008233 hard water Substances 0.000 description 1
- 229940072033 potash Drugs 0.000 description 1
- 235000015320 potassium carbonate Nutrition 0.000 description 1
- BWHMMNNQKKPAPP-UHFFFAOYSA-L potassium carbonate Substances [K+].[K+].[O-]C([O-])=O BWHMMNNQKKPAPP-UHFFFAOYSA-L 0.000 description 1
- 235000015598 salt intake Nutrition 0.000 description 1
- 239000011780 sodium chloride 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
- B01J49/00—Regeneration or reactivation of ion-exchangers; Apparatus therefor
- B01J49/75—Regeneration or reactivation of ion-exchangers; Apparatus therefor of water softeners
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Treatment Of Water By Ion Exchange (AREA)
Description
Verfahren zum Regenerieren von basenaustausehender Filtermasse iu
WasserenthÏrtungsapparaten.
Das Schweizer Patent Nr. 57551 be schreibt ein Verfahren, nach welchem Was ser von beliebiger Härte durch einfache kalte
Filtration durch eine basenaustauschende
Filtermasse auf () Grad enthärtet wird. Die vollständige Enthärtung findet in der Weise statt., dass das harte Wasser von oben nach unten durch die basenaustauschende Filter masse fliesst, wobei die Härtebildner, wie Kali, Gips usw. in die Filtermasse über gehen, bis diese erschöpft ist. Um die Filter masse wieder austauschfÏhig zu machen, muss dieselbe mit einer 6 bis 8% igen Kochsalz- lösung regeneriert werden, welches in der
Weise geschieht, dass in einem Salzlösegefäss die Salzlösung angesetzt wird.
Nachdem die
Filtermasse durch R cksp len aufgelockert ist, wird das im Apparat befindliche Wasser ? bis zur Oberfläche der Permutit bezw. Filter schicht abgelassen. Hierauf lässt man die Salzlösung in den Enthärtungsapparat laufen und öffnet einen kleinen Auslaufhahn so weit, da. ¯ die Salzl¯sung in zirka 6 bis 8 Stunden die Filtermasse durchfliesst. Diese Art der Regeneration der Filtermasse er fordert ausser der Zeit einen erheblichen Überschuss an Salz, da die Salzlösung nicht einmal zur Hälfte ausgenutzt werden kann.
Nach dem den Gegenstand der vorlie genden Erfindung bildenden Regenerierver- fahren ist es möglich :
1. Den Salzverbrauch auf die Hälfte zu reduzieren, 2. Die Zeit für die Regeneration auf zirka 1 bis 2 Stunden abzukürzen und 3. Eine vollkommene Auflockerung der
Filtermasse während der ganzen Dauer des
Regene. rationsprozesses zu bewirken.
Das Verfahren ist dadurch gekennzeich- net, dass die Salzlösung mit Hilfe einer Um- wälzvorrichtung die Filtermasse von unten nach oben durchfliesst, wobei die Salzlösung gleichzeitig in einem Lösegefäss filtriert wird.
Während der Enthärtungsprozess in gleicher Weise, wie oben beschrieben, vor sich geht, das heisst, da¯ die Flüssigkeit den Apparat von oben nach unten durchfliesst, erfolgt die Regeneration wie folgt :
Ausf hrungsbeispiel: Nach erfolgter Rückspülung wird der Enthärtungsapparat durch Schieber a vollständig entleert. Im Salzlösegefäss L wird vorher eine 25% ige Salzlösung S angesetzt. Nachdem Schieber a geschlossen ist, werden die Schieber b und c geöffnet und die Pumpe d in Betrieb gesetzt, welche die Salzlösung S von unten nach oben durch die Filtermasse F drückt.
Gleichzeitig lässt man durch Offnen des Schiebers R so lange Wasser zuflieBen, bis aus c Flüssigkeit ausfliesst, worauf Schieber R geschlossen wird. Nun läBt man die Pumpe d zirka 1 bis 2 Stunden laufen, wobei die Salzlösung S die Filtermasse F im Kreislauf von unten nach oben durchfliesst. Nachdem keine Abnahme der Konzentration der Salzlösung S festgestellt wird, ist der RegenerationsprozeB beendigt. Schieber c wird geschlossen, und der noch im SalzlösegefäB L befindliche Rest Salzlösung in den Apparat A gepumpt. Hierauf wird Pumpe d auBer Betrieb gesetzt und Schieber b geschlossen.
Vor der Wiederinbetriebnahme des Apparates A wird die Salzlösung, wie bisher, durch Schieber a verdrängt und so lange ausgewaschen, bis das aus a ausflieBende Wasser kein Kochsalz mehr enthält. Die Regeneration ist be endigt, und der Apparat kann wieder in Betrieb genommen werden.
Process for the regeneration of base-exchanging filter mass iu
Water softeners.
The Swiss patent no. 57551 be describes a process according to which water of any hardness by simple cold
Filtration through a base exchange
Filter mass is softened to () degrees. Complete softening takes place in such a way that the hard water flows from top to bottom through the base-exchanging filter mass, with the hardness components such as potash, gypsum, etc. passing into the filter mass until it is exhausted. In order to make the filter material exchangeable again, it must be regenerated with a 6 to 8% saline solution, which is in the
It happens that the salt solution is prepared in a salt dissolving vessel.
after the
Filter material is loosened by backwashing, is the water in the device? up to the surface of the permutite respectively. Filter layer drained. Then you let the salt solution run into the water softener and open a small tap as far as possible. ¯ the saline solution flows through the filter material in about 6 to 8 hours. This type of regeneration of the filter mass requires, apart from the time, a considerable excess of salt, since the salt solution cannot even be used halfway.
According to the regeneration process forming the subject of the present invention, it is possible:
1. To reduce the salt consumption by half, 2. To shorten the regeneration time to around 1 to 2 hours and 3. To completely loosen up the
Filter mass for the entire duration of the
Rain. the ration process.
The method is characterized in that the salt solution flows through the filter material from bottom to top with the aid of a circulation device, the salt solution being filtered at the same time in a dissolving vessel.
While the softening process proceeds in the same way as described above, i.e. the liquid flows through the device from top to bottom, regeneration takes place as follows:
Exemplary embodiment: After backwashing, the water softener is completely emptied using slide a. A 25% salt solution S is prepared in the salt dissolving vessel L beforehand. After slide a is closed, slide b and c are opened and pump d is put into operation, which pushes the salt solution S through the filter material F from bottom to top.
At the same time, by opening slide R, water is allowed to flow in until liquid flows out of c, whereupon slide R is closed. Now the pump d is allowed to run for about 1 to 2 hours, the salt solution S flowing through the filter mass F in a circuit from bottom to top. After no decrease in the concentration of the salt solution S is found, the regeneration process is ended. Slide c is closed and the residual salt solution still in the salt dissolving vessel L is pumped into apparatus A. Pump d is then switched off and valve b is closed.
Before the apparatus A is started up again, the salt solution is, as before, displaced by slide a and washed out until the water flowing out of a no longer contains any common salt. The regeneration is finished and the device can be started up again.
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CH128483T CH128483A (en) | 1927-01-25 | 1927-01-25 | Process for the regeneration of base-exchanging filter media in water softeners. |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CH128483T CH128483A (en) | 1927-01-25 | 1927-01-25 | Process for the regeneration of base-exchanging filter media in water softeners. |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CH128483A true CH128483A (en) | 1928-11-01 |
Family
ID=4386952
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CH128483T CH128483A (en) | 1927-01-25 | 1927-01-25 | Process for the regeneration of base-exchanging filter media in water softeners. |
Country Status (1)
| Country | Link |
|---|---|
| CH (1) | CH128483A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE759179C (en) * | 1939-09-01 | 1951-08-02 | Permutit A G | Process for the desilification of water |
| DE767790C (en) * | 1937-02-04 | 1953-05-18 | Permutit Ag | Method for reviving replacement filters connected in series |
| EP0031535A3 (en) * | 1979-12-17 | 1981-09-23 | Gebr. Heyl Kg Gesellschaft Fur Analysentechnik | Process for the cyclic regeneration of water softening apparatus and programme-controlled apparatus therefor |
-
1927
- 1927-01-25 CH CH128483T patent/CH128483A/en unknown
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE767790C (en) * | 1937-02-04 | 1953-05-18 | Permutit Ag | Method for reviving replacement filters connected in series |
| DE759179C (en) * | 1939-09-01 | 1951-08-02 | Permutit A G | Process for the desilification of water |
| EP0031535A3 (en) * | 1979-12-17 | 1981-09-23 | Gebr. Heyl Kg Gesellschaft Fur Analysentechnik | Process for the cyclic regeneration of water softening apparatus and programme-controlled apparatus therefor |
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