石油与天然气化工
石油與天然氣化工
석유여천연기화공
CHEMICAL ENGINEERING OF OIL AND GAS
2014年
1期
33-38
,共6页
邢艳青%祁影霞%喻志广%王乐
邢豔青%祁影霞%喻誌廣%王樂
형염청%기영하%유지엄%왕악
CH4%水合物%置换率%CO2
CH4%水閤物%置換率%CO2
CH4%수합물%치환솔%CO2
methane%hydrate%replacement ratio%carbon dioxide
CO2置换CH4水合物是一种开发CH4的新方法,该方法既可以开发CH4,又可以永久储存CO2。通过自行优化设计的实验装置,研究了石英砂介质体系中温度和压力对置换效率的影响。实验结果表明,在置换压力为2.5 M Pa ,温度为273.15 K 、274.15 K 、275.15 K、276.15 K、277.15 K、278.15 K时,置换率分别为1.75%、6.99%、13.43%、5.53%、22.64%、44.90%;在温度为275.15K,置换压力为2.0MPa、2.5MPa、3.0MPa、3.5MPa时,置换效率分别为37.11%、13.43%、3.44%、4.58%。可见,温度和压力都是推动CO2置换CH4水合物反应的影响因素。
CO2置換CH4水閤物是一種開髮CH4的新方法,該方法既可以開髮CH4,又可以永久儲存CO2。通過自行優化設計的實驗裝置,研究瞭石英砂介質體繫中溫度和壓力對置換效率的影響。實驗結果錶明,在置換壓力為2.5 M Pa ,溫度為273.15 K 、274.15 K 、275.15 K、276.15 K、277.15 K、278.15 K時,置換率分彆為1.75%、6.99%、13.43%、5.53%、22.64%、44.90%;在溫度為275.15K,置換壓力為2.0MPa、2.5MPa、3.0MPa、3.5MPa時,置換效率分彆為37.11%、13.43%、3.44%、4.58%。可見,溫度和壓力都是推動CO2置換CH4水閤物反應的影響因素。
CO2치환CH4수합물시일충개발CH4적신방법,해방법기가이개발CH4,우가이영구저존CO2。통과자행우화설계적실험장치,연구료석영사개질체계중온도화압력대치환효솔적영향。실험결과표명,재치환압력위2.5 M Pa ,온도위273.15 K 、274.15 K 、275.15 K、276.15 K、277.15 K、278.15 K시,치환솔분별위1.75%、6.99%、13.43%、5.53%、22.64%、44.90%;재온도위275.15K,치환압력위2.0MPa、2.5MPa、3.0MPa、3.5MPa시,치환효솔분별위37.11%、13.43%、3.44%、4.58%。가견,온도화압력도시추동CO2치환CH4수합물반응적영향인소。
Replacement of methane hydrate by CO2 is a new approach for the development of CH4 ,and the method can develop CH4 and store CO2 permanently .By optimizing design of ex-periment device ,the influences on displacement efficiency of temperature and pressure in the sys-tem of quartz sand media are studied .The experiment results show that the replacement rates are 1 .75% ,6 .99% ,13 .43% ,5 .53% ,22 .64% ,44 .90% respectively ,the corresponding replace-ment temperature are 273 .15 K ,274 .15 K ,275 .15 K ,276 .15 K ,277 .15 K ,278 .15 K ,and the CO2 charge pressure is constant at 2 .5 M Pa .On the other hand ,the replacement efficiency are 37 .11% ,13 .43% ,3 .44% ,4 .58% respectively ,corresponding to the CO2 charge pressure at 2 .0 M Pa ,2 .5 M Pa ,3 .0 M Pa ,3 .5 M Pa and the replacement temperature being constant at 275 .15 K .Therefore ,temperature and pressure are driving force factors of CO 2 replacement of CH4 hydrate reaction .