共查询到17条相似文献,搜索用时 93 毫秒
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醇胺溶液吸收CO2是沼气提纯领域重要的研究课题。在实验填料吸收塔中,以乙醇胺(MEA)、二乙醇胺(DEA)为吸收剂,研究了吸收剂浓度、进气流量、CO2浓度、进液温度对吸收过程转化率η、吸收速率N以及气相总体积传质系数KGae的影响。结果表明,吸收剂浓度增加可有效提高η、N及KGae;进气流率增加,η逐渐降低,N先增加后降低,KGae先增加后降低最终趋于稳定;随着CO2浓度增加,η和KGae不断降低,N逐渐增加;随着进液温度升高,η和KGae均先升高后降低;MEA、DEA的最佳进液温度在40~60℃之间,并随CO2负载量增大而逐渐降低。研究结果对于醇胺溶液吸收法沼气提纯技术的研究开发和实际应用有参考作用。 相似文献
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为满足有机胺法脱硫设计开发的需要,采用动态吸收法测定了填料塔中哌嗪二胺(PA-A)水溶液吸收低浓度SO2的体积总传质系数KGa,考察了吸收工艺参数如吸收液中的PA-A浓度和初始pH值、液相流率、吸收温度、进气SO2浓度及流速等对KGa的影响。结果表明:KGa随着吸收液中的PA-A浓度和初始pH值、液相喷淋密度的增加而增大;随着吸收温度、气相流率及进气SO2浓度的增加而减小。通过实验结果分析得到体积总传质系数KGa与气液相流率比(qG/qL)之间符合指数关系式,该经验关系可用于工程设计计算。 相似文献
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为了探究有机胺溶液吸收二氧化碳的发展潜力和应用前景,本文综述了有机胺溶液对于CO2的吸收效果,其中单组分有机胺法存在一定的局限性,使用混合胺体系可以弥补存在的问题,着重讨论了乙醇胺(MEA)/2-氨基-2-甲基-1-丙醇(AMP)、三乙烯四胺(TETA)/氨乙基哌嗪(AEP)和三乙醇胺(TEA)/N-氨乙基哌嗪(AEP)的混合胺复配吸收剂对CO2的吸收效果,同时讨论了金属离子对复合胺溶液捕集CO2过程的强化作用。 相似文献
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《化学工程》2016,(4):6-10
空间位阻胺2-氨基-2-甲基-1-丙醇(AMP)捕集CO_2技术具有吸收容量大、低能耗、腐蚀性小等优势,但因其吸收速度慢,制约了该项技术的大规模应用。将AMP分别与乙醇胺(MEA)和N-氨乙基哌嗪(AEP)混合,探讨不同配比以AMP为主体的混合胺溶液捕获CO_2性能。结果表明:常温常压下,AMP和MEA的体积比为5∶5时,该混合胺捕集CO_2效果最佳,相对纯AMP溶液,吸收容量提高了12.34%,吸收速率提高了29.21%,解析速率提高了20.00%;AMP和AEP的体积比为7∶3时,捕集效果最佳,相对纯AMP溶液,吸收容量提高了9.680%,吸收速率提高了28.10%,解析速率提高了32.50%;在最佳配比时,AMP和MEA的混合胺溶液,与AMP和AEP的混合胺溶液相比较,前者吸收容量比后者大2.558%,吸收速率比后者快1.587%,解析速率比后者慢18.52%。 相似文献
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醇胺溶液吸收CO2是沼气提纯领域重要的研究课题。在实验填料吸收塔中,以NaOH水溶液吸收低浓度CO2的实验结果估算了填料的有效相界面积,建立了乙醇胺(MEA)溶液吸收高浓度CO2增强因子的数学模型,并从数学模型和实验的角度研究了MEA浓度、进气流率、CO2浓度等工艺参数对MEA吸收CO2增强因子的影响。结果表明,增强因子数学模型计算值与实验值能够良好吻合,MEA吸收CO2化学反应增强因子随进气CO2浓度增加而降低,随MEA浓度增加而增加,随进气流率增加而减小。 相似文献
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利用热力学模型和通用流程模拟软件,分三段模拟CO2吸收塔,并结合水力学计算软件确定各段采用的塔板型式. 相似文献
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在鼓泡式CO2吸收和再生装置中,研究了N-甲基二乙醇胺(MDEA)/乙醇胺(MEA)、MDEA/乙醇胺基甘氨酸(MEAGLY)和MDEA/乙醇胺基肌氨酸(MEASAR)混合吸收剂的沼气CO2吸收及再生特性。结果表明:混合吸收剂的沼气CO2吸收速率随MEA、MEAGLY和MEASAR等添加剂添加量的增加而提高,但再生速率却呈现下降趋势。再生过程中,吸收剂在升温阶段均发生了CO2再生,且混合吸收剂再生效果要优于单一吸收剂。综合考虑CO2吸收速率、再生速率和CO2循环携带量,MDEA与活化剂质量配比为3∶2时所组成的混合吸收剂的沼气CO2吸收-再生综合性能最优。沼气CO2分离成本对比分析显示,与质量分数为30%的MEA相比,总质量分数为30%的MDEA/MEAGLY(3∶2)和MDEA/MEA(3∶2)的CO2分离成本可分别下降约12%和30%,在未来具有替代MEA进行工程应用的潜能。 相似文献
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Spatial Scale Effects on Rayleigh Convection and Interfacial Mass Transfer Characteristics in CO2 Absorption 下载免费PDF全文
Concentration gradient‐induced Rayleigh convections in the CO2 absorption process were investigated by the hybrid Lattice‐Boltzmann/finite‐difference method (LBM‐FDM). The spatial scale effects on Rayleigh convection were studied by simulating Rayleigh convections with different liquid layers. The scale of convection increased with the liquid layer height but the average mass transfer coefficient showed the adverse tendency. The Rayleigh convection had a pronounced effect on the surface renewal. For better assessment of the renewal intensity, two statistical quantities were proposed. The transient variations of these quantities provided a good following feature with the mass transfer coefficient which confirms their accuracy and precision in characterizing the mass transfer process. 相似文献
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The key challenge in amine‐based CO2 capture from flue gases is to reduce the energy consumption required for solvent regeneration. Lipophilic amines exhibit a thermomorphic phase transition upon heating, giving rise to autoextractive behavior, which intensifies desorption at temperatures well below the boiling point of aqueous solutions. The low regeneration temperature of less than 80 °C together with the high cyclic CO2 loading capacity of ~0.9 mol molabsorbent–1 of such thermomorphic biphasic solvent (TBS) systems permit the use of low‐value and even waste heat at temperatures below 100 °C for desorption. In order to reduce the exergy demands still further, techniques for enhancing CO2 release using extractive regeneration with inert solvent addition were investigated at temperatures of 40–50 °C to permit the use of waste heat at temperatures of ~70 °C or less. The regeneration of 3 M absorbed lipophilic amine solutions with 0.93 mol mol–1 CO2 loading by using various additional solvents and the evaluation of the extractive performance in multiple‐stage crosscurrent and countercurrent configurations indicated the promise of adding certain hydrophobic solvents to enhance the low‐temperature regeneration of TBS absorbents. 相似文献
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Comparison of Overall Gas‐Phase Mass Transfer Coefficient for CO2 Absorption between Tertiary Amines in a Randomly Packed Column 下载免费PDF全文
Le Wen Helei Liu Wichitpan Rongwong Zhiwu Liang Kaiyun Fu Raphael Idem Paitoon Tontiwachwuthikul 《化学工程与技术》2015,38(8):1435-1443
The mass transfer performance of CO2 absorption into an innovative tertiary amine solvent, 1‐dimethylamino‐2‐propanol (1DMA2P), was investigated and compared with that of methyldiethanolamine (MDEA) in a packed column with random Dixon‐ring packing. All experiments were conducted under atmospheric pressure. The effects of inert gas flow rate, amine concentration, liquid flow rate, CO2 loading, and liquid temperature on mass transfer performance were analyzed and the results presented in terms of the volumetric overall mass transfer coefficient (KGav). The experimental findings clearly indicate that 1DMA2P provided better mass transfer performance than MDEA. For both 1DMA2P and MDEA solutions, the KGav increased with rising amine concentration and liquid flow rate, but decreased with higher CO2 loading. The inert gas flow rate only slightly affected the KGav. A satisfactory correlation of KGav was developed for the 1DMA2P‐CO2 system. 相似文献