The role of divertor pumping combined with full drifts in particle exhaust and divertor plasma

Xuele Zhao, C. Sang, Yilin Wang, Chen Zhang, Dezhen Wang
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Abstract

The effect of drifts combined with pumping on particle exhaust is assessed using the SOLPS-ITER code package, considering full drifts. Both drifts and pumping speed S can affect particle exhaust. Drifts change the neutral density by influencing plasma flow and the resulting particle recycling. This leads to the accumulation of neutral particles either far away or close to the pump opening location. While the particle exhaust is enhanced as S raises. When the pump opening is positioned at the common flux region (CFR) of the outer divertor (referred to as Pump CFR/OD), particle exhaust is suppressed by drifts in forward Bt, while it is enhanced by drifts in reversed Bt, with fixed S. On the other hand, when the pump is situated in the private flux region (PFR) of the outer divertor (referred to as Pump PFR/OD), particle exhaust is enhanced by drifts in both reversed and forward Bt compared to the case without drifts. Moreover, the effective pumping in reversed Bt is stronger than in forward Bt. In the same Bt direction, Pump PFR/OD has a higher effective pumping than Pump CFR/OD. Increased S results in higher particle exhaust in all Bt direction and pump location cases. The plasma detachment is affected by drifts, S and pump opening location, respectively. For the specified Bt direction and pump opening location case, higher S suppresses plasma detachment. For an identical particle exhaust rate, stronger pumping capacity can promote plasma detachment. Therefore, Pump PFR/OD can more easily achieve outer divertor detachment than Pump CFR/OD in the same Bt direction. Overall, placing the pump at the PFR side of the outer divertor while running in reversed Bt is the best option from the divertor particle exhaust and plasma detachment point of view.
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分流器泵送与粒子排气和分流器等离子体中的全漂移相结合的作用
使用 SOLPS-ITER 代码包评估了漂移与泵送相结合对颗粒排气的影响,并考虑了全漂移。漂移和泵送速度 S 都会影响粒子排气。漂移通过影响等离子体流和由此产生的粒子循环来改变中性密度。这导致中性粒子在远离或靠近泵开口位置的地方聚集。而粒子排气会随着 S 的升高而增强。当泵开口位于外分流器的公共通量区(CFR)(称为泵 CFR/OD)时,在 S 固定的情况下,正向 Bt 的漂移会抑制粒子排气,而反向 Bt 的漂移则会增强粒子排气;另一方面,当泵位于外分流器的私人通量区(PFR)(称为泵 PFR/OD)时,与没有漂移的情况相比,反向和正向 Bt 的漂移都会增强粒子排气。此外,反向 Bt 的有效泵送比正向 Bt 更强。在相同的 Bt 方向上,泵 PFR/OD 的有效泵送量高于泵 CFR/OD。在所有 Bt 方向和泵位置情况下,增加 S 会导致更高的粒子排气量。等离子体脱离分别受到漂移、S 和泵开口位置的影响。在指定的 Bt 方向和泵开启位置情况下,较高的 S 会抑制等离子体脱离。在粒子排气速率相同的情况下,更强的泵送能力会促进等离子体脱离。因此,在相同的 Bt 方向上,泵 PFR/OD 比泵 CFR/OD 更容易实现外分流器脱离。总之,从分流器粒子排气和等离子体脱离的角度来看,将泵置于外分流器的 PFR 侧并反向 Bt 运行是最佳选择。
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