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Diffusion of carbon dioxide through lipid bilayer membranes. Effects of carbonic anhydrase, bicarbonate, and unstirred layers

机译:二氧化碳通过脂质双层膜扩散。碳酸酐酶,碳酸氢盐和未搅拌层的影响

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Diffusion of (14)C-labeled CO(2) was measured through lipid bilayer membranes composed of egg lecithin and cholesterol (1:1 mol ratio) dissolved in n-decane. The results indicate that CO(2), but not HCO(3-), crosses the membrane and that different steps in the transport process are rate limiting under different conditions. In one series of experiments we studied one-way fluxes between identical solutions at constant pCO(2) but differing [HCO(3-)] and pH. In the absence of carbonic anhydrase (CA) the diffusion of CO(2) through the aqueous unstirred layers is rate limiting because the uncatalyzed hydration-dehydration of CO(2) is too slow to permit the high [HCO(3-)] to facilitate tracer diffusion through the unstirred layers. Addition of CA (ca. 1 mg/ml) to both bathing solutions causes a 10-100-fold stimulation of the CO(2) flux, which is proportional to [HCO(3-)] over the pH range 7-8. In the presence of CA the hydration- dehydration reaction is so fast that CO(2) transport across the entire system is rate limited by diffusion of HCO(3-) through unstirred layers. However, in the presence of CA when the ratio [HCO(3-) + CO(3=)]:[CO(2)] more than 1,000 (pH 9-10) the CO(2) flux reaches a maximum value. Under these conditions the diffusion of CO(2) through the membrane becomes rate limiting, which allows us to estimate a permeability coefficient of the membrane to CO(2) of 0.35 cm s(-1). In a second series of experiments we studied the effects of CA and buffer concentration on the net flux of CO(2). CA stimulates the net CO(2) flux in well buffered, but no in unbuffered, solutions. The buffer provides a proton source on the upstream side of the membrane and proton sink on the downstream side, thus allowing HCO(3-) to facilitate the net transport of CO(2) through the unstirred layers.
机译:(14)C标记的CO(2)的扩散是通过由卵卵磷脂和胆固醇(1:1摩尔比)溶解在正癸烷中组成的双层脂质膜测量的。结果表明,CO(2)而不是HCO(3-)穿过膜,并且运输过程中的不同步骤在不同条件下限制了速率。在一系列实验中,我们研究了恒定pCO(2)但[HCO(3-)]和pH不同的相同溶液之间的单向通量。在没有碳酸酐酶(CA)的情况下,CO(2)通过未搅拌的水层的扩散是速率限制的,因为CO(2)的未催化水合脱水太慢而无法使高[HCO(3-)]促进示踪剂通过未搅拌的层扩散。在两种沐浴液中添加CA(约1 mg / ml)会引起10%到100倍的CO(2)通量刺激,这与[HCO(3-)]在7-8的pH范围内成比例。在CA的存在下,水合脱水反应是如此之快,以至于CO(2)在整个系统中的传输速度受到HCO(3-)通过未搅拌层的扩散的限制。但是,在存在CA的情况下,当[HCO(3-)+ CO(3 =)]:[CO(2)]的比率大于1,000(pH 9-10)时,CO(2)通量达到最大值。在这些条件下,CO(2)通过膜的扩散成为速率限制,这使我们能够估计膜对CO(2)的渗透系数为0.35 cm s(-1)。在第二系列实验中,我们研究了CA和缓冲液浓度对CO(2)净通量的影响。 CA会在缓冲良好的溶液中刺激净CO(2)通量,但在无缓冲溶液中则不会。缓冲液在膜的上游提供质子源,在下游提供质子沉,因此允许HCO(3-)促进CO(2)通过未搅拌层的净传输。

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