아민(암모니아 또는 MPA)은 가압경수로 원전 2차측 부식을 방지하는 최적 pH를 유지하기 위해 사용되고, 온도가 동일하게 유지되지 않는 물-증기 순환 영역에서 모든 아민은 평형상수에 따라 2차측에서 서로 다른 pH를 나타낸다. 부식제어에서 pH는 유일한 인자가 아니므로 두 번째 변수, 즉 불순물의 유입 또는 부식 반응으로 인해 $H^+$가 추가되거나 제거되었을 때 안정된 pH를 지속하는 능력인 완충세기의 고려가 필요하다. 온도를 고려한 완충세기는 2차측 최적 pH 제어제 선정과 유체가속부식의 특징을 기본적으로 이해할 수 있도록 한다. PWRs의 전체 운전범위에서 암모니아와 MPA의 완충세기를 조사하였다. 낮은 온도$(25{\sim}100^{\circ}C)$에서는 암모니아 그리고 높은 온도$(150{\sim}250^{\circ}C)$에서는 MPA가 부식 억제를 위한 충분한 완충세기를 나타내었다. 완충세기 측면에서, i) 최적 pH 제어제 pH 범위는 pH(T)- $1{\leq}pK_a(T){\leq}pH(T)$+0.5, ii) 아민 용액은 부식 억제를 위해 충분한 완충세기$({\beta})$를 가져야하고, iii) 최대 유체가속부식은 ${\beta}_B/{\beta}$ 비율이 최저인 온도에서 최대를 나타낸다.
아민(암모니아 또는 MPA)은 가압경수로 원전 2차측 부식을 방지하는 최적 pH를 유지하기 위해 사용되고, 온도가 동일하게 유지되지 않는 물-증기 순환 영역에서 모든 아민은 평형상수에 따라 2차측에서 서로 다른 pH를 나타낸다. 부식제어에서 pH는 유일한 인자가 아니므로 두 번째 변수, 즉 불순물의 유입 또는 부식 반응으로 인해 $H^+$가 추가되거나 제거되었을 때 안정된 pH를 지속하는 능력인 완충세기의 고려가 필요하다. 온도를 고려한 완충세기는 2차측 최적 pH 제어제 선정과 유체가속부식의 특징을 기본적으로 이해할 수 있도록 한다. PWRs의 전체 운전범위에서 암모니아와 MPA의 완충세기를 조사하였다. 낮은 온도$(25{\sim}100^{\circ}C)$에서는 암모니아 그리고 높은 온도$(150{\sim}250^{\circ}C)$에서는 MPA가 부식 억제를 위한 충분한 완충세기를 나타내었다. 완충세기 측면에서, i) 최적 pH 제어제 pH 범위는 pH(T)- $1{\leq}pK_a(T){\leq}pH(T)$+0.5, ii) 아민 용액은 부식 억제를 위해 충분한 완충세기$({\beta})$를 가져야하고, iii) 최대 유체가속부식은 ${\beta}_B/{\beta}$ 비율이 최저인 온도에서 최대를 나타낸다.
Amines, ammonia or 3-methoxypropylamine (MPA), are used to maintain the optimized pH for the prevention of corrosion in the secondary side of Pressurized Water Reactors (PWRs). They are differently dissociated as a function of temperature which is not same in each location of the water-steam cycle. ...
Amines, ammonia or 3-methoxypropylamine (MPA), are used to maintain the optimized pH for the prevention of corrosion in the secondary side of Pressurized Water Reactors (PWRs). They are differently dissociated as a function of temperature which is not same in each location of the water-steam cycle. pH at the operation temperature depends on temperature of fluid and equilibrium constants of water and amines. Thus, every amine provides the different pH in the entire secondary side so that pH is not only the sufficient parameter in corrosion control. The secondary parameter, i.e., buffer intensity, is the ability to maintain a stable pH when $H^+$ are added or removed due to the ingress of impurities or the reaction of corrosion. The buffer intensity is necessary to provide the selection criteria for the best pH control agent for secondary side and the basic understanding of the reason why the flow-accelerated corrosion(FAC) rate may demonstrate the bell-shape curve over temperature. The buffer intensities of ammonia and MPA were reviewed over the entire operation temperature of PWRs. The sufficient buffer intensity is provided for the inhibition of corrosion by ammonia in low temperature $(25{\sim}100^{\circ}C)$ and by DMA in high temperature $(150{\sim}250^{\circ}C)$. In terms of buffer intensity, i) the best pH control agent is an amine with $pK_a(T)$ range of pH(T)- $1{\leq}pK_a(T){\leq}pH(T)$ + 0.5 and ii) the amine solution should have sufficient buffer intensity, ${\beta}$ to inhibit corrosion, and iii) FAC rate may be maximum at the temperature, where ${\beta}_B/{\beta}$ ratio is lowest.
Amines, ammonia or 3-methoxypropylamine (MPA), are used to maintain the optimized pH for the prevention of corrosion in the secondary side of Pressurized Water Reactors (PWRs). They are differently dissociated as a function of temperature which is not same in each location of the water-steam cycle. pH at the operation temperature depends on temperature of fluid and equilibrium constants of water and amines. Thus, every amine provides the different pH in the entire secondary side so that pH is not only the sufficient parameter in corrosion control. The secondary parameter, i.e., buffer intensity, is the ability to maintain a stable pH when $H^+$ are added or removed due to the ingress of impurities or the reaction of corrosion. The buffer intensity is necessary to provide the selection criteria for the best pH control agent for secondary side and the basic understanding of the reason why the flow-accelerated corrosion(FAC) rate may demonstrate the bell-shape curve over temperature. The buffer intensities of ammonia and MPA were reviewed over the entire operation temperature of PWRs. The sufficient buffer intensity is provided for the inhibition of corrosion by ammonia in low temperature $(25{\sim}100^{\circ}C)$ and by DMA in high temperature $(150{\sim}250^{\circ}C)$. In terms of buffer intensity, i) the best pH control agent is an amine with $pK_a(T)$ range of pH(T)- $1{\leq}pK_a(T){\leq}pH(T)$ + 0.5 and ii) the amine solution should have sufficient buffer intensity, ${\beta}$ to inhibit corrosion, and iii) FAC rate may be maximum at the temperature, where ${\beta}_B/{\beta}$ ratio is lowest.
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가설 설정
. The FAC rate decreases as at-temperature pH increases.
. The FAC rate varies with temperature. The effect of temperature on the FAC rate is demonstrated by the bell-shaped curve.
ii) the amine solution should have sufficient buffer intensity, P, to inhibit corrosion, and ⅲ) FAC rate may be maximum at the temperature, where Ph2o/P ratio is highest. The critical temperature in the bell-shape curve, calculated using dissociation constants of water and amines, is usually between 150C and 250C depending upon the solution pH and the type of amine.
제안 방법
The objectives of the study were to review the buffer intensity of ammonia and MPA solutions at each location in the water-steam cycle and to provide the selection criteria for the best pH control agent, and the reason why the FAC rate may demonstrate the bell-shape curve over temperature.
성능/효과
The resistance of amine solution to change pH may be reduced at ~ 180C where corrosion occurs. In conclusion, amine solution should have the minimum buffer intensity to achieve the corrosion inhibition, while the resisting power to pH change in the metal-water interface may be lowest at the highest ratio of Pb to p (minimum Ph2o/P ratio) over the temperature of 100 ~ 250C .
5 above 200C. In conclusion, there is no amine with pKa(T)=pH(T) to provide the maximum contribution to the solution buffer in the temperature range of 25 ~ 300 C (no ideal pH control agent for PWR secondary side). Thus, the best pH control agent should
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