Schafer J A, Troutman S L, Watkins M L, Andreoli T E
Kidney Int. 1981 Nov;20(5):588-97. doi: 10.1038/ki.1981.181.
The present studies tested the hypothesis that osmotic disequilibrium between luminal and peritubular fluids is the driving force for net volume absorption in the isolated proximal straight tubule. Isolated tubule segments from superficial rabbit renal cortex were perfused at varying rates with a high chloride and bicarbonate-free solution as they were bathed with a normal bicarbonate-Krebs-Ringer buffer solution at 38 degrees C. Increasing the perfusion rate from congruent to 4 to congruent to 30 nl/min produced a monotonic increase in net volume absorption (Jv) from 0.18 +/- (sem) 0.03 to 0.62 +/- 0.08 nl . min-1. The chloride concentration in collected fluid samples rose from congruent to 137 to congruent to 147 mEq/liter over the same perfusion rate range. Ouabain (10(-4) m) added to the bathing solution inhibited Jv by a rate which varied from 0.20 to 0.28 nl . min-1 . min-1, depending on the perfusion rate. A mathematical model of the axial flows and transepithelial transport processes was developed. This model, and the experimental data, is consistent with the view that the driving force for isotonic fluid absorption in these tubules depends on the axial maintenance of osmotic disequilibrium between the perfusate and the bathing solution. Increasing the perfusion rate opposes osmotic equilibration by minimizing the extent to which dissipative fluxes of chloride and bicarbonate ions change the transepithelial chloride and bicarbonate concentration gradients, and by minimizing the tendency of the luminal cryoscopic osmolality to increase as volume absorption occurs.
管腔液与肾小管周围液之间的渗透不平衡是离体近端直小管中净体积吸收的驱动力。从兔肾浅表皮质分离出的肾小管节段,在38℃下用正常碳酸氢盐 - 克雷布斯 - 林格缓冲液浴洗的同时,以不同速率灌注一种高氯且无碳酸氢盐的溶液。将灌注速率从约4 nl/min增加到约30 nl/min,净体积吸收(Jv)从0.18±(标准误)0.03增加到0.62±0.08 nl·min⁻¹,呈单调增加。在相同的灌注速率范围内,收集的液体样本中的氯离子浓度从约137 mEq/升升至约147 mEq/升。添加到浴洗液中的哇巴因(10⁻⁴ m)抑制Jv的速率在0.20至0.28 nl·min⁻¹·min⁻¹之间变化,具体取决于灌注速率。建立了轴向流动和跨上皮转运过程的数学模型。该模型与实验数据均表明,这些小管中等渗液体吸收的驱动力取决于灌注液与浴洗液之间渗透不平衡的轴向维持。增加灌注速率可通过最小化氯离子和碳酸氢根离子的耗散通量改变跨上皮氯离子和碳酸氢根浓度梯度的程度,以及最小化随着体积吸收管腔冰点渗透压增加的趋势,来对抗渗透平衡。