CN110436599A - A kind of regulator for marine small-sized heap - Google Patents
A kind of regulator for marine small-sized heap Download PDFInfo
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- CN110436599A CN110436599A CN201910615403.XA CN201910615403A CN110436599A CN 110436599 A CN110436599 A CN 110436599A CN 201910615403 A CN201910615403 A CN 201910615403A CN 110436599 A CN110436599 A CN 110436599A
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- China
- Prior art keywords
- amino
- regulator
- methyl
- sized heap
- amylalcohol
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- 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.)
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Classifications
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- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F1/00—Treatment of water, waste water, or sewage
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/02—Non-contaminated water, e.g. for industrial water supply
- C02F2103/023—Water in cooling circuits
Abstract
The invention discloses a kind of regulators for marine small-sized heap, are related to reactor secondary circuit water quality adjustment technical field, its composition includes: 5~20% organic amine and 0.01~0.05% dispersing agent as mass fraction;Surplus is demineralized water, and the present invention by the organic amine of setting can complete that small-sized heap pH value of secondary circuit is adjusted, so can reduce liquid in pipe pH value is lower or containing corrosion product etc. due to corrosion to therrmodynamic system.
Description
Technical field
The present invention relates to reactor secondary circuit water quality adjustment technical fields, and in particular to a kind of tune for marine small-sized heap
Save agent.
Background technique
Since to have mobility good for floating nuclear power plant, transportable power supply, heat supply and the advantages that desalinize seawater, therefore, for sea
Foreign development of resources energy safeguard provides optimal settling mode.Wherein, steam generator be floating nuclear power plant one, secondary circuit it
Between the most weak link of important heat exchange equipment and primary Ioops pressure boundary, the failure cause of steam generator it is most of with
Conducting heat, tracheal rupture is related, and therefore, the reliability of steam generator heat-transfer pipe is most important to nuclear plant safety and economy.
Steam generator tube rupture mainly liquid in pipe pH value is lower or containing corrosion product etc. due to make
At, and use basifier appropriate can reduce condensate system and the corrosion product of water supply system enters steam generator, maximum limit
The corrosion of the reduction steam generator heat-transfer pipe of degree.With the development of naval vessel science and technology, control secondary circuit is adjusted frequently with phosphate
Water quality indicator, with certain particularity and limitation, as being only capable of reducing steam generator heat-transfer pipe using phosphate method
Corrosion rate not can be reduced the corrosion product into steam generator, can not protect entire therrmodynamic system, in addition to this, contain
The remote superstate standard requirements of phosphate concentration (0.045mg/L in terms of P) in phosphorus sewage, if discharge will lead to water body after not handling
Eutrophication, and cause large area " red tide ", the safety for influencing floating nuclear power plant operates normally, and causes the deterioration of the ecological environment.
Ammonia, ethanol amine and the morpholine that domestic nuclear power is used to control water quality and use belong to hazardous chemical, in transport, store and use
There are many restrictions in journey.In addition to this, the CO that the demineralized water and condenser of secondary coolant circuit system supplement are leak into2, may make
At condensate, the corrosion of supply line.
Summary of the invention
In view of the deficiencies in the prior art, the purpose of the present invention is to provide a kind of adjustings for marine small-sized heap
Agent can control small-sized heap pH value of secondary circuit, and reduce the corrosion to therrmodynamic system.
To achieve the above objectives, the technical solution adopted by the present invention is that:
A kind of regulator for marine small-sized heap is provided, its composition includes: 5~20% organic amine as mass fraction
With 0.01~0.05% dispersing agent;Surplus is demineralized water.
Based on the above technical solution, the density of the regulator is 0.9~1.0g/cm3, pH value is 9~11.
Based on the above technical solution, the organic amine is 5- amino 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol.
Based on the above technical solution, the purity of the 5- amino 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol is extremely
It is less that the analysis that mass fraction is 97% is pure.
Based on the above technical solution, the mass ratio of the 5- amino 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol is
1:1~1:4.
Based on the above technical solution, the mass ratio of the 5- amino 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol is
1:1。
Based on the above technical solution, the dispersing agent is sodium polymethacrylate.
Based on the above technical solution, the dispersing agent is that poly is total to acrylic acid.
Compared with the prior art, the advantages of the present invention are as follows:
A kind of regulator for marine small-sized heap of the invention can be completed by the organic amine of setting to small-sized heap
PH value of secondary circuit is adjusted, so can drop low liquid in pipe pH value is lower or containing corrosion product etc. due to heating power
The corrosion of system.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of marine small-sized heap in the embodiment of the present invention;
Fig. 2 is the operation schematic diagram of steam generator in the embodiment of the present invention.
In figure: 1- chemicals dosing plant, 2- dosing pipe, the first pipeline of 21-, the second pipeline of 22-, 23- third pipeline, 3- water quality
Sensor, the first pH sensor of 31-, the 2nd pH sensor of 32-, the 3rd pH sensor of 33-, 4- condenser, 5- oxygen-eliminating device, 6- steam
Vapour generator.
Specific embodiment
Invention is further described in detail with reference to the accompanying drawings and embodiments.
Shown in Figure 1, the embodiment of the present invention provides a kind of regulator for marine small-sized heap, as mass fraction its
Composition includes: 5~20% organic amine and 0.01~0.05% dispersing agent;Surplus is demineralized water, it is preferable that organic amine 5-
Amino 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol, dispersing agent is that sodium polymethacrylate or poly are total to acrylic acid, into one
Step, at least mass fraction is pure for 97% analysis for the purity of 5- amino 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol,
In, the mass ratio of 5- amino 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol is 1:1~4:1, it is preferable that 5- amino 1- amylalcohol and 2-
The mass ratio of amino 2- methyl 1- propyl alcohol is 1:1, meanwhile, the density of the regulator is 0.9~1.0g/cm3, pH value is 9~11.
After the regulator is added in small-sized heap secondary circuit, by the organic amine of setting, that is, the 5- amino 1- that is arranged
Amylalcohol and 2- amino 2- methyl 1- propyl alcohol, can complete that small-sized heap pH value of secondary circuit is adjusted, and 2- amino 2- methyl 1-
Propyl alcohol can also absorb the carbon dioxide leak by condenser 4, then the regulator can reduce due to liquid in pipe pH value compared with
Corrosion low or containing reasons such as corrosion products to therrmodynamic system;Meanwhile chemicals used in the regulator is routine
Chemicals, toxic is small, and easy resolution process uses easy-to-operate;The regulator is in 3.7MPa, 250 DEG C or less, property
Matter is stablized, and resolution ratio is low, and has gas-liquid partition coefficient appropriate, it is ensured that there is higher pH value in gas-liquid two-phase region, slows down stream
Dynamic accelerated corrosion;Not phosphorus element-containing in the regulator, not will cause water eutrophication, overcomes tradition and is brought using phosphate
Negative effect, reduce discharge, and state modulator is stablized.
Wherein, the dispersing agent of addition can make 4~6ug/L of concentration of secondary circuit water loading amount.Dispersing agent is poly- methyl-prop
Olefin(e) acid sodium or poly are total to acrylic acid, pollution-free to steam, good with the compatibility of conventional material, and the dispersing agent is for dispersing corruption
Product and scale are lost, is present in it in steam generator with doughy state, heat exchange pipe surface will not be deposited on, and influences heat transfer
With cause underdeposit corrosion.The corrosion product dirt in steam generator can be made to arrange more easily by drainage by dispersing agent
Out, the iron concentration for further decreasing steam generator secondary side slows down the corrosion of heat-transfer pipe.
Shown in Figure 1, the embodiment of the present invention also provides a kind of medicine system with above-mentioned regulator, comprising:
Chemicals dosing plant 1 is stored with regulator in chemicals dosing plant 1;
Dosing pipe 2, dosing pipe 2 include the first pipeline 21, the second pipeline 22 and third pipeline 23, the first pipeline 21,
The first metering pump, the second metering pump and third metering pump, and the first pipeline are respectively equipped on second pipeline 22 and third pipeline 23
21 both ends are separately connected the condensation water out of chemicals dosing plant 1 and condenser 4, and 22 both ends of the second pipeline are separately connected chemicals dosing plant 1
With the downcomer of oxygen-eliminating device 5,23 both ends of third pipeline are separately connected the water supply pipeline section of chemicals dosing plant 1 and steam generator 6;
Water quality sensor 3, water quality sensor 3 include the first pH sensor 31, the 2nd pH sensor 32 and the 3rd pH sensing
Device 33, the first pH sensor 31 are set to the condensed water exit of condenser 4, and the 2nd pH sensor 32 is set to being lauched for oxygen-eliminating device 5
Guan Shang, the 3rd pH sensor 33 are set on the sewage pipe of steam generator 6;
Controller, controller include the first controller, second controller and third controller, and the first controller is respectively with the
One metering pump and the connection of 31 signal of the first pH sensor, second controller are believed with the second metering pump and the 2nd pH sensor 32 respectively
Number connection, third controller connect with third metering pump and 33 signal of the 3rd pH sensor respectively.
Wherein, the first pH sensor 31, the 2nd pH sensor 32 and the 3rd pH sensor 33 are respectively used to detection condenser 4
Condensation water out, oxygen-eliminating device 5 downcomer and steam generator 6 sewage pipe pH value, when water quality sensor 3 detect pH
When being worth lower than the predetermined pH value of its corresponding position, dosing signal will be generated and be sent to corresponding controller, controller is according to connecing
The dosing signal received is to control the dosing that corresponding first metering pump, the second metering pump or third metering pump carry out corresponding position
Operation reaches scheduled pH value requirement, so as to detect that the pH value of the pH value position lower than predetermined pH value increases to reduce in pipe
The lower corrosion to therrmodynamic system of liquid pH value, simultaneously as the selection of regulator, additionally it is possible to which the corrosion product contained is carried out
It absorbs, avoids corrosion of the corrosion product to therrmodynamic system.
Chemicals dosing plant 1 includes medical fluid blending tank, mixes tank connected centrifugal pump and two and medical fluid blending tank company with medical fluid
The medicine storing pot connect, medical fluid blending tank are used for stored adjustment agent, and centrifugal pump is for injecting demineralized water, two drug storages into medical fluid blending tank
Being stored with 5- amino 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol in tank respectively can be completed by the setting of the chemicals dosing plant 1
Allotment to the regulator different proportion, so that the case where medicine system can complete different dosing requirements.
Wherein, blender is equipped in medical fluid blending tank, it can be in centrifugal pump and two medicine storing pots respectively to medical fluid blending tank
After interior addition demineralized water, 5- amino 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol, mixed liquor in medical fluid blending tank is stirred in completion
It mixes, can be uniformly mixed, to help to improve the adjustment effect to small-sized heap pH value of secondary circuit;It is set in medical fluid blending tank
There is conductivity meter, is used to detect the additional amount of 5- amino 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol, passes through conductivity meter
The mass fraction being able to detect in medical fluid blending tank is acted on, to reflect wherein 5- amino 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol
Additional amount, and then can complete that the regulation for the amount that 5- amino 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol is added can be made
The regulator finally matched out can satisfy scheduled requirement.
Preferably, water quality sensor 3 is online pH meter, can complete condensation water out, oxygen-eliminating device 5 to condenser 4
PH value real-time detection at the sewage pipe of downcomer and steam generator 6, to reduce the reaction time of the medicine system, energy
Enough instantaneous adjustings completed to pH value in small-sized heap secondary circuit;First metering pump, the second metering pump and third metering pump are liquid
Pressure-type diaphragm metering pump, can be in the water supply of the downcomer and steam generator 6 of condensation water out, oxygen-eliminating device 5 to condenser 4
When carrying out dosing at pipe, different dosages is controlled, so that the condensation water out of the condenser 4 after dosing, oxygen-eliminating device 5 are lauched
PH value is met the requirements at the sewage pipe of pipe and steam generator 6, and is not in waste problem caused by adding regulator.
Shown in Figure 1, the embodiment of the present invention also provides a kind of small-sized heap in sea equipped with above-mentioned medicine system, comprising:
The condensation water out of condenser 4, condenser 4 is equipped with the first pH sensor 31, and connect with 21 one end of the first pipeline;
The downcomer of oxygen-eliminating device 5, oxygen-eliminating device 5 is equipped with the 2nd pH sensor 32, and connect with 22 one end of the second pipeline;
Steam generator 6, the sewage pipe of steam generator 6 be equipped with the 3rd pH sensor 33, and steam generator 6 is given
Water pipe section is connect with 23 one end of third pipeline.
Respectively by the condensation of the first pH sensor 31, the 2nd pH sensor 32 and the 3rd pH sensor 33 detection condenser 4
The pH value of the sewage pipe of water out, the downcomer of oxygen-eliminating device 5 and steam generator 6, to be completed by dosing pipe 2 to condenser
The feeding operations of the feed pipe of 4 condensation water out, the downcomer of oxygen-eliminating device 5 and steam generator 6, to complete to small-sized heap
The pH value of secondary circuit is adjusted, reduce small-sized heap secondary circuit liquid in pipe pH value it is lower or containing reasons such as corrosion products to heating power
The corrosion of system.
When the regulator is added to secondary circuit, 5-A P (5-amino-1- can be calculated according to dissociation situation
Pentanol, 5- amino 1- amylalcohol) and AMP (2-amino-2-methyl-1-propanol, 2- amino 2- methyl 1- propyl alcohol)
The relationship of initial concentration and pH value
Wherein, if the dissociation constant of 5-AP, AMP are respectively Kb1And Kb2, concentration is respectively Cb1And Cb2, mixed at 25 DEG C
Dissociation equation after conjunction is as follows:
Wherein, KwThe ion-product constant of water will can obtain after above-mentioned formula abbreviation
According in solution the principle that product and the amount of the proton gain and loss of product after mistake proton should be equal after proton, can arrange
Proton condition out, such as following formula:
[OH-]=[C5H14NO+]+[C4H12NO+]+[H+] (4)
The influence of water decomposition is not considered and the case where single weak base
And formula (1), (2), (3) are substituted into known to formula (4):
The concentration of 5-AP and AMP and the concentration relationship of OH- can be obtained after abbreviation:
The initial concentration of 5-AP and AMP and the relationship of pH value can be obtained according to formula (5).
According to the gas-liquid partition coefficient that 5-AP and AMP in secondary circuit is added, point of 5-AP and AMP concentration in secondary circuit is carried out
It is calculated with situation
The distribution coefficient of 5-AP and AMP at different temperatures is as follows:
The gas-liquid partition coefficient data of two kinds of alkali
Shown in Figure 2, to after secondary circuit dosing, 5-AP and AMP enter steam generator with water supply, a portion with
Enter secondary coolant circuit system with steam, another part enters furnace water, and loses with steam generator blowdown.According to 5-AP, AMP and give
Water conservation of matter, steam generator blowdown rate define Gp=λ GwAnd the distribution coefficient of 5-AP and AMP is respectively Cw1=KdCp1
And Cw2=KdCp2, wherein GpFor the blowdown flow of steam generator, GwFor the evaporation capacity of steam generator, Cw1For steam generation
5-AP concentration in device evaporation capacity, Cp1For the 5-AP concentration in steam generator blowdown flow, Cw2For steam generator evaporation capacity
In AMP concentration, Cw2For the AMP concentration in steam generator evaporation capacity, KdFor dissociation constant, formula can be obtained.
Gf=Gw+Gp
Gf×Cf1=Gw×Cw1+(Gp+V)×Cp1
Gf×Cf2=Gw×Cw2+(Gp+V)×Cp2
Wherein, GfFor the feedwater flow of steam generator, Cf1For the 5-AP concentration in steam generator feedwater flow, Cf2For
The AMP concentration of steam generator feedwater flow.
The regulator of the embodiment of the present invention is with mass fraction for 5% 5- amino 1- amylalcohol and 5% 2- amino 2- methyl
It is illustrated for 1- propyl alcohol;
It is known that the dissociation equation of 5- amino 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol at 25 DEG C is as follows:
The initial concentration of 5- amino 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol and the pass of pH value can be solved to obtain according to above formula
System.
According in NB/T 20436-2017 " control of PWR nuclear power plant water chemistry " to steam generator secondary side water quality
It is required that the pH value of water supply should control between 9~10, it is computed, the concentration of the 5- amino 1- amylalcohol of steam generator secondary side
1.2~14.4mg/kg need to be reached, the concentration of 2- amino 2- methyl 1- propyl alcohol need to reach 1.1~26.7mg/kg.It is kept according to quality
Constant rule and gas-liquid Distribution dynamics, can calculate each node of secondary coolant circuit system needs 5- amino in pH value to be achieved and each node
Concentration needed for 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol, specific calculated result are as follows:
By above-mentioned regulator as desired the condensate of stable injection condenser, in the feedwater piping of steam generator, with
For the evaporation capacity of steam generator is 160 ton/hours;5- amino 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol when initial launch
Dosage need to be respectively as follows: 0.4~0.8Kg/h and 0.45~0.9Kg/h, the magnitude of recruitment in later period need to be respectively as follows: 6.5~13g/h
With 10~20g/h, wherein dosage when initial launch is the initial stage for adding regulator, is needed within the unit time to two times
The quality of 5- amino 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol is added in the system of road so that in secondary coolant circuit system each node pH
Value reaches pre-provisioning request, during the magnitude of recruitment in later period is secondary coolant circuit system stable operation, needs within the unit time to two times
The quality of 5- amino 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol is added in the system of road, the magnitude of recruitment in later period is mainly due to existing
The amount of 5- amino 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol drop in secondary coolant circuit system caused by steam generator blowdown etc. consumes
Low problem.
When regulator is by taking mass fraction is 5% 5- amino 1- amylalcohol and 5% 2- amino 2- methyl 1- propyl alcohol as an example,
Its specific dosing process are as follows: when the first pH sensor 31 shows that pH value is lower than 8.5, medicine system fills chain promoter dosing
1 is set, the regulator prepared and completed is added to the condensed water exit of condenser 4;When the 2nd pH sensor 32 shows that pH value is lower than
When 9.3, system by chain promoter chemicals dosing plant 1, to the downcomer of oxygen-eliminating device 5 at be added prepare complete regulator;Work as third
PH sensor 33 show pH value be lower than 9.6 when, system by chain promoter chemicals dosing plant 1, to the feed pipe of steam generator 6 at add
Enter to prepare the regulator completed;The feed pipe of colleague, steam generator 6 can also be 6 wet preservation of steam generator during shutdown
Dosing mouth.
Assuming that the water loading amount of secondary circuit is 40m3, the pH value of demineralized water is 7, and pH value need to be controlled 9.3, then under initial situation
Need to be added the alkali of 0.792mol to secondary circuit.I.e. condensate, the hydroxyl concentration in water supply should be 2*10-5mol/L。
Weight proportion when regulator of the present invention reaches said effect can be obtained
5-AP:5%, AMP:5%, PAMA:0.01%, surplus are water;
5-AP:10%, AMP:15%, PAMA:0.015%, surplus are water;
5-AP:15%, AMP:20%, PAMA:0.02%, surplus are water;
5-AP:20%, AMP:20%, PAMA:0.02%, surplus are water.
After the regulator is added, the average iron-content of solidifying water supply is down to 8~10ug/L by 75 original~10ug/L, hence it is evident that
Ground slows down the corrosion rate of secondary circuit steam-water pipe equipment.
The present invention is not limited to the above-described embodiments, for those skilled in the art, is not departing from
Under the premise of the principle of the invention, several improvements and modifications can also be made, these improvements and modifications are also considered as protection of the invention
Within the scope of.The content being not described in detail in this specification belongs to the prior art well known to professional and technical personnel in the field.
Claims (8)
1. a kind of regulator for marine small-sized heap, which is characterized in that its composition includes: 5~20% as mass fraction
Organic amine and 0.01~0.05% dispersing agent;Surplus is demineralized water.
2. a kind of regulator for marine small-sized heap as described in claim 1, it is characterised in that: the density of the regulator
For 0.9~1.0g/cm3, pH value is 9~11.
3. a kind of regulator for marine small-sized heap as described in claim 1, it is characterised in that: the organic amine is 5- ammonia
Base 1- amylalcohol and 2- amino 2- methyl 1- propyl alcohol.
4. a kind of regulator for marine small-sized heap as claimed in claim 3, it is characterised in that: the 5- amino 1- amylalcohol
It is pure to be at least the analysis that mass fraction is 97% with the purity of 2- amino 2- methyl 1- propyl alcohol.
5. a kind of regulator for marine small-sized heap as claimed in claim 3, it is characterised in that: the 5- amino 1- amylalcohol
Mass ratio with 2- amino 2- methyl 1- propyl alcohol is 1:1~1:4.
6. a kind of regulator for marine small-sized heap as claimed in claim 3, it is characterised in that: the 5- amino 1- amylalcohol
Mass ratio with 2- amino 2- methyl 1- propyl alcohol is 1:1.
7. a kind of regulator for marine small-sized heap as described in claim 1, it is characterised in that: the dispersing agent is poly- first
Base sodium acrylate.
8. a kind of regulator for marine small-sized heap as described in claim 1, it is characterised in that: the dispersing agent is poly- horse
Carry out sour acrylic acid altogether.
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2019
- 2019-07-09 CN CN201910615403.XA patent/CN110436599A/en active Pending
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CN1522296A (en) * | 2001-06-20 | 2004-08-18 | 西屋电气有限责任公司 | Improved scale conditioning agents |
WO2012068590A1 (en) * | 2010-11-19 | 2012-05-24 | Chemtreat, Inc. | Methods for reducing scale formation on and removing deposits from heat transfer surfaces |
CN102557225A (en) * | 2010-12-28 | 2012-07-11 | 秦山核电有限公司 | Method for adjusting pH value of secondary circuit of nuclear power plant |
CN105417668A (en) * | 2015-12-25 | 2016-03-23 | 中国核动力研究设计院 | Novel composite alkalizer and application thereof |
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Application publication date: 20191112 |