預處理方案:
PiperION® 膜以非氫氧化物形式(更具體地說以碳酸氫鹽形式)運輸,需要遵循適當的預處理方案才能將其轉化為所需的陰離子形式。
對於標準鹼性燃料電池/電解應用:
使用前,讓膜在環境條件下放置 1 小時(不加蓋板)。
對於氫氧根交換膜燃料電池或氫氧根交換電解應用或任何其他需要氫氧根離子跨膜轉移的應用,膜應從碳酸氫鹽形式轉化為OH-形式以獲得最佳電導率。
若要將膜轉化為 OH- 形式,請將膜在室溫下置於 0.5 M NaOH 或 KOH 水溶液中 1 小時。 1 小時後,用新鮮的 0.5 M NaOH 或 KOH 取代溶液,並讓膜再次在室溫下浸泡 1 小時。兩次浸泡後,用去離子水(pH ~ 7)沖洗膜。盡量減少與環境空氣的接觸,因為二氧化碳可以交換回膜中,導致膜轉化回碳酸氫鹽形式。 CO2 和氫氧根離子之間的反應是純粹的化學反應,如果膜的 OH- 形式暴露於含有 CO2 的環境(例如環境空氣等),則很容易發生這種反應。只需在無二氧化碳的乾燥箱環境中進行轉換和測試,就可以完全消除這種轉換。
對於 CO2 或 CO 的電化學還原或 CO2 電解應用:
使用前,讓膜在環境條件下放置 1 小時(不加蓋板)。
PiperION® 膜以碳酸氫鹽形式運輸。如果您在設定中使用碳酸氫鹽電解質,則無需對薄膜進行預處理,並且可以按原樣使用。
如果您使用碳酸鹽電解質,則需要將 PiperION® 膜轉換為碳酸鹽形式。為了實現這一點,只需在室溫下將膜浸入 0.1 – 0.5 M 碳酸鈉或碳酸鉀的水溶液中 12 小時。然後,用新鮮的 0.1 – 0.5 M 碳酸鈉或碳酸鉀更換溶液,並讓膜再次在室溫下浸泡 12 小時。浸泡兩到三次後,用去離子水(pH ~ 7)沖洗膜。
如果您在CO2 還原實驗中使用KOH 或NaOH 型純鹼性電解質,而不是碳酸氫鹽或碳酸鹽電解質,那麼您可以簡單地遵循“對於標準鹼性燃料電池/電解應用”協議將膜轉換為OH – 形式。
對於其他電化學(電滲析、海水淡化、電電滲析、反電滲析、酸回收、鹽分解等)及非電化學應用:
使用前,讓膜在環境條件下放置 1 小時(不加蓋板)。
在將膜組裝到電化學裝置或裝置中之前,應將膜轉化成與預期應用相關的陰離子形式。例如,如果應用要求 Cl- 陰離子透過膜轉移,則該陰離子交換膜需要轉化為 Cl- 形式。為了將此膜轉化為Cl-形式,需要將其浸入0.1至0.5M的NaCl或KCl鹽溶液(溶解在去離子水中)12-24小時,然後用去離子水沖洗以除去去除膜表面多餘的鹽。或者,如果預期應用需要跨膜轉移硫酸根陰離子,則 PiperION® AEM 需要在組裝到電池中之前轉化為硫酸根形式。在室溫下將膜完全浸入鹽溶液中12-24小時後,0.1至0.5M Na 2 SO 4 或K 2 SO 4的中性鹽溶液 通常足以實現膜完全轉化為硫酸鹽形式。始終建議重複浸泡過程 2-3 次,以實現接近 100% 的轉化,然後用大量去離子水沖洗。
Scientific Literature for Various Use of Versogen Membranes and Dispersion Products:
The article by Wang et al. entitled “Poly(aryl piperidinium) membranes and ionomers for hydroxide exchange membrane fuel cells” is considered to be an excellent source that describes the polymer chemistry and fuel cell operation of PiperION® membranes with hydrogen and CO2-free air reactants at a temperature of 95 °C. This article also investigates the ionic conductivity, chemical stability, mechanical robustness, gas separation, and selective solubility aspects of poly(aryl piperidinium) based AEMs.
The article by Wang et al. entitled “High-Performance Hydroxide Exchange Membrane Fuel Cells THrough Optimization of Relative Humidity, Backpressure, and Catalyst Selection” is considered to be an excellent source that describes the polymer chemistry and fuel cell operation of PiperION® membranes under different operational parameters in order to eliminate the anode flooding and cathode drying out issues in order to achieve a blanced water management. With further optimization on the catalyst, a peak power density of 1.89 W/cm2 in H2/O2 and 1.31 W/cm2 in H2/Air have been achieved.
The article by Luo et al. entitled “Structure-Transport Relationships of Poly(aryl piperidinium) Anion-Exchange Membranes: Effect of Anions and Hydration” is considered to be an excellent source that describes the transfer of different anions across AEMs that are manufactured from poly(aryl piperidinium) resin. Nanostructure, hydration or water uptake as a function of the counter anion, phase-separation in regars of its polymer morphology, anion conductivity as a function of water content (vapor or liquid) and anion radius are some of the other aspects that have been discussed in this publication.
The article by Zhao et al. entitled “An Efficient Direct Ammonia Fuel Cell for Affordable Carbon-Neutral Transportation” is considered to be an excellent source that describes economics of hydrogen, methanol, and ammonia as fuel for transportation applications, performance of poly(aryl piperidinium) based AEMs for direct ammonia fuel cell at 80 °C.
The article by Archrai et al. entitled “A Direct Ammonia Fuel Cell with a KOH-Free Anode Feed Generating 180 mW cm-2 at 120 °C” investigates the electrochemical performance of poly(aryl piperidinium) based AEMs for direct ammonia fuel cell at 120 °C.
The article by Endrodi et al. entitled “High carbonate ion conductance of a robust PiperION membrane allows industrial current density and conversion in a zero-gap carbon dioxide electrolyzer cell” investigates the electrochemical performance of poly(aryl piperidinium) based AEMs for electrochemical reduction of CO2 or carbon dioxide electrolyzer applications. This study demonstrated that partial current densities of greater than 1 A/cm2 can be achieved while maintaining high conversion (25-40%), selectivity (up to 90%), and low cell voltage (2.6-3.4 V).
Electrochemical performance of anion exchange membranes would usually depend on the design of the electrochemical testing hardware, operational parameters, membrane thickness, catalyst loading and type, gas diffusion layer thickness and type, the way the MEA/CCM manufactured and assembled, etc. Fuel Cell Store does not provide any warranties or guarantees for the performances obtained by other researchers.