WO2008017899A3 - Process for ph-control and stoichiometric ph-stat mean - Google Patents
Process for ph-control and stoichiometric ph-stat mean Download PDFInfo
- Publication number
- WO2008017899A3 WO2008017899A3 PCT/HU2007/000070 HU2007000070W WO2008017899A3 WO 2008017899 A3 WO2008017899 A3 WO 2008017899A3 HU 2007000070 W HU2007000070 W HU 2007000070W WO 2008017899 A3 WO2008017899 A3 WO 2008017899A3
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- value
- titrant
- fixed
- measured
- stoichiometric
- 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
-
- G—PHYSICS
- G05—CONTROLLING; REGULATING
- G05D—SYSTEMS FOR CONTROLLING OR REGULATING NON-ELECTRIC VARIABLES
- G05D21/00—Control of chemical or physico-chemical variables, e.g. pH value
- G05D21/02—Control of chemical or physico-chemical variables, e.g. pH value characterised by the use of electric means
Landscapes
- Physics & Mathematics (AREA)
- General Physics & Mathematics (AREA)
- Engineering & Computer Science (AREA)
- Automation & Control Theory (AREA)
- Control Of Non-Electrical Variables (AREA)
- Physical Or Chemical Processes And Apparatus (AREA)
Abstract
The present invention relates to a process for adjusting pH to a fixed value and a stoichiometric pH-stat means (10) for completing the process. The process comprises the steps of (a) measuring a pH-value in a system of known reactants with reactions of known courses; (b) establishing at least one equilibrium material balance equation and at least one electroneutrality equation, wherein the reactants are taken as components; (c) solving the equations and determining thereby an amount of titrant required to decrease the difference between the measured pH-value of the system and the fixed pH-value to be reached; (d) adding a single type of titrant to the system along with applying the calculated amount of titrant as control parameter, whereby converging the measured pH- value of the system towards the fixed pH- value, wherein the added titrant is of the action of the compensation for the change in pH occurring in the system without intervention, and, if desired, in cases where the difference between the measured pH-value and the fixed pH- value exceeds a threshold value, repeating steps (a) to (d) with the same type of titrant until the reactions of the system take place or are interrupted, whereby maintaining the pH-value of the system at the fixed value (within a given tolerance level).
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| HU0600636A HU227659B1 (en) | 2006-08-08 | 2006-08-08 | Process for ph-control and stochiometric ph-stat apparatus |
| HUP0600636 | 2006-08-08 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| WO2008017899A2 WO2008017899A2 (en) | 2008-02-14 |
| WO2008017899A3 true WO2008017899A3 (en) | 2008-11-13 |
Family
ID=89986956
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/HU2007/000070 Ceased WO2008017899A2 (en) | 2006-08-08 | 2007-08-08 | Process for ph-control and stoichiometric ph-stat mean |
Country Status (2)
| Country | Link |
|---|---|
| HU (1) | HU227659B1 (en) |
| WO (1) | WO2008017899A2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP3212300B1 (en) * | 2014-10-30 | 2019-06-05 | GE Healthcare Bio-Sciences AB | Method for predicting the dynamic ph range of a buffer |
| CN116969574B (en) * | 2023-08-03 | 2025-09-26 | 华能南京金陵发电有限公司 | Automatic dosing system and method of use thereof |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1532071A (en) * | 1976-02-06 | 1978-11-15 | Niemi A | Method for controlling concentration variables of process materials |
| US4273146A (en) * | 1979-01-05 | 1981-06-16 | Phillips Petroleum Company | Cooling tower operation with automated pH control and blowdown |
| JPS58161013A (en) * | 1982-03-19 | 1983-09-24 | Toshiba Corp | Controller of ph value of water |
| US5352350A (en) * | 1992-02-14 | 1994-10-04 | International Business Machines Corporation | Method for controlling chemical species concentration |
-
2006
- 2006-08-08 HU HU0600636A patent/HU227659B1/en not_active IP Right Cessation
-
2007
- 2007-08-08 WO PCT/HU2007/000070 patent/WO2008017899A2/en not_active Ceased
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1532071A (en) * | 1976-02-06 | 1978-11-15 | Niemi A | Method for controlling concentration variables of process materials |
| US4273146A (en) * | 1979-01-05 | 1981-06-16 | Phillips Petroleum Company | Cooling tower operation with automated pH control and blowdown |
| JPS58161013A (en) * | 1982-03-19 | 1983-09-24 | Toshiba Corp | Controller of ph value of water |
| US5352350A (en) * | 1992-02-14 | 1994-10-04 | International Business Machines Corporation | Method for controlling chemical species concentration |
Also Published As
| Publication number | Publication date |
|---|---|
| HUP0600636A2 (en) | 2008-03-28 |
| HU227659B1 (en) | 2011-10-28 |
| HU0600636D0 (en) | 2006-09-28 |
| WO2008017899A2 (en) | 2008-02-14 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| NENP | Non-entry into the national phase |
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| NENP | Non-entry into the national phase |
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| 122 | Ep: pct application non-entry in european phase |
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