CN1587086A - Weak alkaline circulation water treating and anti-corrosion method for water cooling generator static wire stick - Google Patents
Weak alkaline circulation water treating and anti-corrosion method for water cooling generator static wire stick Download PDFInfo
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- CN1587086A CN1587086A CN 200410053910 CN200410053910A CN1587086A CN 1587086 A CN1587086 A CN 1587086A CN 200410053910 CN200410053910 CN 200410053910 CN 200410053910 A CN200410053910 A CN 200410053910A CN 1587086 A CN1587086 A CN 1587086A
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Abstract
The present invention discloses weak alkaline circular water treating and anticorrosion method for water cooling generator stator wire stick. The weak alkaline circular treater has the two-layer bed structure, including upper layer comprising Na or K type strong acid cationic exchange resin and H-type strong acid cationic exchange resin connected parallelly, and the lower layer comprising OH-type strong alkaline anionic exchange resin. The Na or K type cationic exchange resin, the H-type cationic exchange resin and the OH-type anionic exchange resin in the treater have the weight ratio of 1 to 4-8 to 10-18. By means of the unique ionic exchange resin layer structure, the cooling water inside the generator contains small amount of sodium or potassium hydroxide to regulate water quality and to reduce corrosion of the copper wire stick effectively.
Description
Technical Field
The invention relates to an anticorrosion method for a water-cooled generator stator bar, in particular to a method for anticorrosion of the water-cooled generator stator bar in a micro-alkaline circulating water treatment mode.
Background
The technique for treating the weakly alkaline circulating water in the generator is developed according to the latest power industry standard DL/T801-2002 requirements on the quality and the system of internal cooling water in the large-scale generator and the requirements on the quality and the system of internal cooling water in the twenty-five key requirements for preventing serious accidents in power production of the national power company by referring to the design and operation experience of the internal cooling water system of the large-scale generator at home and abroad aiming at the problems of low water quality qualification rate, serious corrosion of copper wire rods and large potential safety hazard of the internal cooling water system of the large-scale generator at home in recent years. The technology has the characteristics of good water quality, stable operation, long operation period, simple operation, no need of adding chemicals, no need of changing water and the like, and can fundamentally ensure the quality of the internal cooling water and the safe and economic operation of the generator.
At present, the internal cooling water treatment technical method for preventing the corrosion and scaling of the copper wire rod of the generator at home and abroad mainly comprises the following steps: a bypass small mixed bed exchange treatment method, a copper corrosion inhibitor adding method, a frequent water changing method and the like. Because of the respective technical defects of the methods, the quality of the internal cooling water is difficult to stabilize in the required range, and the method isnot favorable for the safe and economic operation of the generator. In part of power plants, the situation of generator copper wire rod burnout, trip or load reduction operation occurs due to unsatisfactory quality of internal cooling water.
Adding a copper corrosion inhibitor: namely, a copper corrosion inhibitor and an alkalizer are added into the internal cold water periodically to reduce the corrosion of a wire rod. The method has the problems of unstable water quality, high copper content, easy complex deposition of corrosion inhibitor and copper ions and the like. However, most domestic power plants still adopt the technology. Bypass small mixed bed exchange treatment method: the cold water in the part is treated by a small mixing bed to reduce the conductivity and the copper content in the water. When the method is used for treatment, the inner cooling water is weakly acidic, the corrosion of the copper wire rod is serious, and the operation period of the small mixed bed is short. The generator with capacity of more than 200MW in China is basically provided with a small inner cooling water mixing bed, but can run less normally. Frequent water changing mode: when the water quality exceeds the standard, a large amount of desalted water or condensed water is supplemented to the system, and the cooling water is replaced. The mode is not only unfavorable for the safe and stable operation of the system, but also is easy to corrode the copper wire rod because the desalted water contains a large amount of dissolved oxygen and carbon dioxide and free ammonia contained in the condensed water.
Disclosure of Invention
The invention aims to: the defects of the prior art are overcome, the corrosion prevention method of the stator bar of the water-cooled generator adopting the micro-alkaline circulating water treatment mode is provided, no medicament is required to be added, the water quality meets the requirements of high pH value, low conductivity and low copper content, and the aims of slowing down the corrosion of the bar, prolonging the service life of the generator and guaranteeing the safe operation are fulfilled.
The invention is realized by the following scheme: the small mixed bed originally designed and equipped for the internal cooling water system is internally reformed into a micro-alkaline circulating processor, and the bed layer structure of the original mixed bed mixed by H type strong acid cation exchange resin and OH type strong alkaline anion exchange resin is changed into: the composite material consists of an upper layer and a lower layer, wherein the upper layer is formed by connecting Na or K type strong acid cation exchange resin and H type strong acid cation exchange resin in parallel, and the lower layer is directly formed by OH type strong base anion exchange resin.
The proportion of each resin in the alkalescent circulating processor is as follows according to weight: na or K type positive resin, H type positive resin and OH type negative resin are 1: 4-8: 10-18.
The strong-acid Na or K type cation exchange resin is super-gel strong-acid styrene series homogeneous particle resin; the strong-acid H-type cation exchange resin is super-gel strong-acid styrene homogeneous particle resin; the strongly basic OH type anion exchange resin is macroporous strongly basic styrene type homogeneous particle resin.
The Na or K type strongly acidic cation exchange resin of the present invention is Na or K type strongly acidic styrene ion exchange resin (for example, 001X 7FC, 001X 7MB, D001SC, D001MB), the H type strongly acidic cation exchange resin is H type strongly acidic styrene ion exchange resin (for example, 001X 7FC, 001X 7MB, D001SC, D001MB), and the OH type strongly basic anion exchange resin is OH type strongly basic styrene ion exchange resin (for example, 201X 7FC, 201X 7MB, 201X 7SC, D201FC, D201SC, D201 MB).
The invention discloses a micro-alkaline circulating water treatment and corrosion prevention method of a water-cooled generator stator bar, which is characterized by comprising the following steps: the unique ion exchange resin bed layer structure is adopted, so that the water quality of the internal cooling water of the generator is adjusted by containing trace sodium hydroxide or potassium hydroxide after ion exchange, the water quality of the internal cooling water is greatly superior to the latest electric power industry standard DL/T801-2002 'technical requirements for internal cooling water quality and systems of large generators', and the corrosion of a generator stator copper wire rod is effectively slowed down; no medicament is required to be added, so that the phenomenon that copper ions are complexed with the added medicament to generate sediments is avoided, the safe operation of the generator is ensured, a large amount of medicaments are saved, and good social and economic benefits are generated; water is not required to be changed and supplemented, so that a large amount of desalted water is saved, and the operation workload is reduced.
Drawings
FIG. 1 is a schematic diagram of a bed structure of a mixed bed in the prior art;
FIG. 2 is a schematic diagram of the bed structure of the embodiment of the present invention.
Detailed Description
Referring to fig. 2, the method of the present invention comprises: the inner cold water is continuously treated by a alkalescent circulating processor.The bed layer structure of the alkalescent circulating processor is as follows: the composite material consists of an upper layer and a lower layer, wherein the upper layer is formed by connecting Na or K type strong acid cation exchange resin 1 and H type strong acid cation exchange resin 2 in parallel, and the lower layer is directly formed by OH type strong base anion exchange resin 3.
The working principle of the invention is as follows: the ion exchange mode is adopted to continuously treat partial cold water in the generator so as to adjust the quality of the cold water in the generator, so that the water quality meets the requirements of high pH value, low conductivity, low copper content and low impurity content. The difference between the method and the traditional internal cooling water treatment mode is as follows: no chemical is added, the internal cold water contains a trace amount of NaOH (KOH) through ion exchange treatment, and the high pH value of the water enables copper to be in a self-passivation state, so that the corrosion of a copper wire rod is reduced.
The present invention will be described in detail with reference to examples.
Example 1:
the bed layer structure of the alkalescent circulating processor is as follows: the upper layer is composed of 40 kg of H-type strong acid super gel styrene series homogeneous particle resin 001 multiplied by 7MB and 10 kg of Na-type strong acid super gel styrene series homogeneous particle resin 001 multiplied by 7MB which are connected in parallel, and the lower layer is composed of 100 kg of OH-type strong alkaline macroporous styrene series homogeneous particle resin D201.
When cold water in the generator flows through the alkalescent circulation processor, the following ion exchange reaction occurs:
(M is a cation such as copper, iron, or ammonium, and n is the charge number of cation M)
(A is an anion such as chlorine or bicarbonate, and m is the number of charges of the anion A)
According to the ion exchange reaction formula, as long as the cold water in the generator contains trace impurity ions such as copper, iron, bicarbonate radical and the like, after the cold water is treated by the alkalescent circulating processor, the pH value can be increased, the impurity content can be reduced, and the corrosion of the copper wire rod of the generator can be slowed down.
Example 2:
in this example, the Na type strongly acidic cation exchange resin 1, the H type strongly acidic cation exchange resin 2 and the OH type strongly basic anion exchange resin 3 were D001, D001 and D201, respectively, and used in amounts of 15 kg, 75 kg and 180 kg, respectively.
Example 3:
the Na type strongly acidic cation exchange resin 1, H type strongly acidic cation exchange resin 2 and OH type strongly basic anion exchange resin 3 used in this example were D001, D001 and 201X 7MB, respectively, and the amounts used were 10 kg, 50 kg and 120 kg, respectively.
Example 4:
in this example, the Na type strongly acidic cation exchange resin 1, the H type strongly acidic cation exchange resin 2 and the OH type strongly basic anion exchange resin 3 were used in amounts of 001X 7, D001 and 201X 7MB, respectively, and used in amounts of 12 kg, 70 kg and 160 kg, respectively.
Example 5:
in this example, the Na type strongly acidic cation exchange resin 1, the H type strongly acidic cation exchange resin 2 and the OH type strongly basic anion exchange resin 3 were D001, 001X 7 and D201, respectively, and used in amounts of 15 kg, 60 kg and 150 kg, respectively.
Example 6:
in this example, the Na type strongly acidic cation exchange resin 1, the H type strongly acidic cation exchange resin 2 and the OH type strongly basic anion exchange resin 3 were D001MB, D001MB and D201, respectively, and the amounts thereof were 10 kg, 45 kg and 120 kg, respectively.
Example 7:
in this example, the amounts of the Na-type strongly acidic cation exchange resin 1, the H-type strongly acidic cation exchange resin 2 and the OH-type strongly basic anion exchange resin 3 used were D001MB, D001MB and D201MB, respectively, and were 12 kg, 50 kg and 130 kg, respectively.
Example 8:
in this example, the Na type strongly acidic cation exchange resin 1, the H type strongly acidic cation exchange resin 2 and the OH type strongly basic anion exchange resin 3 were D001MB, 001X 7FC and D201FC, respectively, and used in amounts of 12 kg, 80 kg and 180 kg, respectively.
The method is applied to 2 200MW generators in a new power plant, 2 300MW generators in a Jinggang mountain Hua energy power plant, 4 300MW generators in a Fengcheng power plant, 2 200MW generators in a Jiujiang power plant and 1 300MW generator in Hua energy Cool generation Limited company.
After the water-cooled generator alkalescent circulating water treatment is transformed, the condition of an inner cooling water system is greatly improved from the operation condition of 11 units, and various indexes of water quality are greatly superior to the DL/T801-2002 standard requirements. The comparison condition of the inner cooling water system before and after the modification is shown in table 1.
Table 1: running condition comparison table for internal cooling water system before and after reconstruction
| Item | Before transformation | After transformation |
| Main control index of water quality | pH：7.0～9.0 The conductivity is less than 2.0 mu s/cm Copper content less than 40 mug/L | |
| Treatment method | Adding corrosion inhibitor and alkalizer | Slightly alkaline recycle treatment |
| Actual water quality Situation(s) | Low qualified rate of water quality pH：6.0～8.5 Conductivity: 2.8 to 8.0 mu s/cm Copper: 18 to 100μg/L | The water quality is very stable pH：＞7.10 Conductivity: 0.07 to 1.5. mu.s/cm Copper: < 20. mu.g/L |
| Dosing situation | Frequent dosing | Without adding medicine |
| Water change situation | Frequent water change | Without changing water |
| Maintenance situation | Frequent operation of the system | System stability, maintenance free |
Claims (8)
1. The method for treating and preventing corrosion of the micro-alkaline circulating water of the water-cooled generator stator bar adopts an ion exchange mode to treat partial internal cold water, and is characterized in that: the inner cooling water is weak and weak after being continuously treated by the alkalescent circulating processor, and the bed layer structure of the alkalescent circulating processor is as follows: the composite material consists of an upper layer and a lower layer, wherein the upper layer is formed by connecting Na or K type strong acid cation exchange resin (1) and H type strong acid cation exchange resin (2) in parallel, and the lower layer is directly formed by OH type strong base anion exchange resin (3).
2. The method for treating the corrosion resistance of the micro-alkaline circulating water of the water-cooled generator stator bar according to claim 1, is characterized in that: the proportion of each resin in the alkalescent circulating processor by weight is as follows: na or K type positive resin, H type positive resin and OH type negative resin are 1: 4-8: 10-18.
3. The stator bar corrosion prevention method for the water-cooled generator alkalescent circulating water treatment according to claim 1 or 2, characterized in that: the strong-acid Na or K type cation exchange resin is super-gel strong-acid styrene type homogeneous particle resin.
4. The stator bar corrosion prevention method for the water-cooled generator alkalescent circulating water treatment according to claim 1 or 2, characterized in that: the strong-acid H-type cation exchange resin is super-gel strong-acid styrene homogeneous particle resin.
5. The stator bar corrosion prevention method for the water-cooled generator alkalescent circulating water treatment according to claim 1 or 2, characterized in that: the strongly basic OH type anion exchange resin is macroporous strongly basic styrene type homogeneous particle resin.
6. The stator bar corrosion prevention method for the water-cooled generator alkalescent circulating water treatment according to claim 1 or 2, characterized in that: the Na or K type strongly acidic cation exchange resin (1) is Na or K type strongly acidic styrene ion exchange resin 001 × 7 or 001 × 7FC or 001 × 7MB or D001SC or D001 MB.
7. The stator bar corrosion prevention method for the water-cooled generator alkalescent circulating water treatment according to claim 1 or 2, characterized in that: the H-type strongly acidic cation exchange resin (2) is H-type strongly acidic styrene ion exchange resin 001 × 7 or 001 × 7FC or 001 × 7MB or D001SC or D001 MB.
8. The stator bar corrosion prevention method for the water-cooled generator alkalescent circulating water treatment according to claim 1 or 2, characterized in that: the OH type strongly basic anion exchange resin (3) is OH type of strongly basic styrene ion exchange resin 201 × 7 or 201 × 7FC or 201 × 7MB or 201 × 7SC or D201FC or D201SC or D201 MB.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 200410053910 CN1253380C (en) | 2004-08-17 | 2004-08-17 | Weak alkaline circulation water treating and anti-corrosion method for water cooling generator static wire stick |
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|---|---|---|---|
| CN 200410053910 CN1253380C (en) | 2004-08-17 | 2004-08-17 | Weak alkaline circulation water treating and anti-corrosion method for water cooling generator static wire stick |
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| CN1587086A true CN1587086A (en) | 2005-03-02 |
| CN1253380C CN1253380C (en) | 2006-04-26 |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101898159A (en) * | 2010-07-23 | 2010-12-01 | 中国神华能源股份有限公司 | Mixed resin and preparation method thereof |
| CN101920215A (en) * | 2010-07-23 | 2010-12-22 | 中国神华能源股份有限公司 | Mixed resin and preparation method thereof |
| CN104925992A (en) * | 2015-06-11 | 2015-09-23 | 长沙理工大学 | Anti-corrosion method for inner cooling water system of engine |
-
2004
- 2004-08-17 CN CN 200410053910 patent/CN1253380C/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101898159A (en) * | 2010-07-23 | 2010-12-01 | 中国神华能源股份有限公司 | Mixed resin and preparation method thereof |
| CN101920215A (en) * | 2010-07-23 | 2010-12-22 | 中国神华能源股份有限公司 | Mixed resin and preparation method thereof |
| CN104925992A (en) * | 2015-06-11 | 2015-09-23 | 长沙理工大学 | Anti-corrosion method for inner cooling water system of engine |
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| Publication number | Publication date |
|---|---|
| CN1253380C (en) | 2006-04-26 |
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Assignee: Kecheng High-New Technology Development Co., Jiangxi Assignor: Jiangxi Prov. Power Test Inst. Contract fulfillment period: 2008.8.1 to 2015.7.31 contract change Contract record no.: 2008360000032 Denomination of invention: Weak alkaline circulation water treating and anti-corrosion method for water cooling generator static wire stick Granted publication date: 20060426 License type: Exclusive license Record date: 20081023 |
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Free format text: EXCLUSIVE LICENSE; TIME LIMIT OF IMPLEMENTING CONTACT: 2008.8.1 TO 2015.7.31; CHANGE OF CONTRACT Name of requester: JIANGXI KECHEN HIGH AND NEW TECHNOLOGY DEVELOPMENT Effective date: 20081023 |
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Granted publication date: 20060426 Termination date: 20130817 |