共查询到20条相似文献,搜索用时 15 毫秒
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硫化氢具有腐蚀性与毒性,采用吸收剂吸收硫化氢气体是重要的脱硫处理方式。不同的吸收剂在吸收效率上存在较大差别。首先对比了三氯化铁体系、碘酸钾体系和碱性铁氰化钾体系三种不同硫化氢吸收剂的吸收效率。在此基础上重点优化了碘酸钾体系吸收条件参数,讨论了包含浓度、温度、pH、气体流量及时间等因素对硫化氢吸收效率的影响。并建立了四因素三水平正交试验研究较优吸收条件,得到正交试验优化吸收条件为:温度55℃,pH 6.01,硫化氢流量0.3 L·min-1,吸收时间1 min,该条件下8%(质量)碘酸钾体系的三级吸收效率为51.56%。研究结果对硫化氢吸收处理提供了理论参考,也为间接电解法循环处理研究提供了支持。 相似文献
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研究了二氧化锰氧化法吸收硫化氢的新工艺,考查了酸度、时间、温度等条件对吸收硫化氢工艺的影响,确定了适合的工艺参数。较合适的条件为:一段,溶液体积0.3L、硫酸浓度0.4mol/L、温度为室温、二氧化锰用量10g;二段,溶液体积0.5L、硫酸浓度0.4mol/L、温度为室温、二氧化锰用量10g。氧化剂二氧化锰被还原为硫酸锰可用氧化水解的方法再生,循环使用。研究结果表明,采用氧化吸收新工艺可以使硫化氢气体的吸收率大于97%,而且二氧化锰可以通过氧化水解的方式再生,实现了氧化剂的再生和循环利用。 相似文献
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Natural gas industry encounters systems that consist of gases like CO2 and H2S, and aqueous solutions of methanol and mixed electrolytes. A knowledge of the phase behavior of such systems, including hydrate formation, is essential in gas production and the design of facilities for gas transportation and processing. Recently, Dholabhai et al. (1997, 1996) and Bishnoi and Dholabhai (1998) described equilibrium conditions for CO2 and gas mixtures containing CO2 in the presence of methanol, electrolytes and ethylene glycol. In the present work aqueous three phase (aqueous liquid solution, vapor and incipient hydrate) equilibrium conditions of H2S hydrate formation in aqueous solutions of electrolytes and methanol are measured in the temperature range of 272 to 294 K and pressure range of 0.3 to 1.0 MPa. A ‘full view’ sapphire variable volume cell with a movable piston is used to obtain the experimental data. 相似文献
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用氢氧化钠溶液吸收硫化氢制取硫化钠工业技术 总被引:1,自引:0,他引:1
详细阐述了在氯化钡生产过程中,将产生的硫化氢用氢氧化钠溶液吸收并制取硫化钠的生产工艺,分别从技术和经济的角度讨论其可行性:用380~420 g/L氢氧化钠溶液在填料塔中吸收硫化氢,反应终点控制硫化钠质量浓度为330~350 g/L,硫化氢吸收率达95%~98%。该工艺不仅可有效保护环境,而且可为企业创造效益。 相似文献
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Girish M. Deshmukh Aparna Shete Deepali M. Pawar 《Journal of chemical technology and biotechnology (Oxford, Oxfordshire : 1986)》2013,88(3):432-436
BACKGROUND: Oxidative absorption of hydrogen sulfide into a solution of ferric chelates is studied in a stirred cell glass reactor. The experiments were performed to investigate the degradation of chelates sodium salt of nitrilotriacetic acid (NTA) (Merck), ethylenediaminetetraacetic acid diadisodium salt (EDTA) and diethylenetriaminepentaacetic acid (DTPA) at 313 K, pH 6, iron concentration 10 000 g L?1 and Fe:chelate molar ratio 1:2. RESULTS: Oxidative absorption of hydrogen sulfide into a solution of Fe‐NTA was found to be more successful, therefore, further experiments with 10%, 50% and 100% concentrations of hydrogen sulfide were performed. It was shown that this process is applicable for removal of low and high concentrations of hydrogen sulfide. The effect of antioxidants using sodium thiosulfate was also studied in order to minimize degradation of NTA. The kinetics were studied and it was observed that the reaction appeared to be first order in ferric chelate with rate constants for 100, 50 and 10% hydrogen sulfide concentration: 0.035, 0.013 and 0.019 h?1, respectively. CONCLUSIONS: Gas sweetening processes have commercial importance in natural gases, refinery of gases and biogas processing. Desulphurization and cleaning (i.e. removal of H2S and CO2) of petroleum gas and biogas is important to make the gas methane rich and to increase the calorific value of fuel. The same techniques of desulphurization and cleaning can be used for treating natural gas or petroleum gas. The desulphurization and cleaning processes can minimize the atmospheric emission of gases like SOx, NOx and CO. As the iron chelate based process is based on the principle of redox reaction of metal chelate with hydrogen sulfide, this method is very useful for desulphurization of petroleum gas and biogas. This work studied the effective use of Fe‐NTA solution for removal of high to low concentrations of H2S as found in biogas and industrial waste gases. © 2012 Society of Chemical Industry 相似文献
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文昌油田液化石油气(LPG)回收项目是中海油湛江分公司到目前为止唯一一个海上LPG回收项目,项目投产至今,创造了良好的经济效益和社会效益。近年来检测文昌油田LPG产品时而会发生铜腐测试不合格情况。经过现场调研论证发现该铜腐超标和LPG中夹带硫化氢相关。利用液化石油气脱硫剂能够很好地解决该问题。本文讨论了合成液化气脱硫剂的最佳反应条件:合成反应时间8h、PMA质量分数50%、反应温度70℃,DEA/MEA混合液质量分数40%,液化气脱硫剂的脱硫率最高可以达到99.13%。通过以上合成条件,合成了脱硫剂ETTS-1D2。ETTS-1D2在pH低于5,反应温度高于100℃时脱硫效率会受到一定影响。液化气脱硫剂以加注量50mL/min,在现场应用的6个月的时间里,可以有效地将铜腐指标从2a降低到1a。确保LPG产品符合国标标准要求。 相似文献
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以γ-Al2O3为载体,考察了第一过渡金属亲硫元素和Cr系元素及其负载量对Claus尾气加氢生成H2S的催化活性。结果表明,经预硫化后上述负载量为10%质量分数的各元素,其催化活性按大小可以划分为4组:Ni、Co、Fe>Mo、W、Cu>Cr>Zn、Mn。针对第一组的3种元素进行物相分析表明,在反应气体积比为SO2/H2/N2=0.5/3/96.5,重量时间空速(WHSV)=6 000mL/(h.g)的强还原气氛下,Ni的催化活性相为稳定的NiS2,但Co和Fe除主晶相CoS2和FeS2外,还分别具有Co3S4和Co9S8或FeS和Fe7S8的贫硫相。 相似文献
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The kinetics of desulfurization of hydrogen sulfide, using metallic copper as desulfurizer, have been investigated over a range of temperatures and pressures of hydrogen sulfide. Our results indicate that there are two stages of reaction; activation energies for the first and second stages are 63 kJ/mol and 38 kJ/mol, respectively. Possible reaction mechanisms in which the initial rate is controlled by interface reaction and the later stage is controlled by diffusion through or in the Cu2S layer are consistent with the experimental data. 相似文献
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金属氧化物脱硫剂脱硫过程中产生羰基硫的现象缩小了脱硫剂的使用范围。本文从气体中存在一氧化碳、二氧化碳、单质硫和硫化氢出发给出了均相、非均相生成羰基硫的途径,特别综述了生成羰基硫的催化作用。在总结氧化铁基、氧化锌基、氧化锰基及氧化铜基主流金属氧化物脱硫剂脱硫过程中产生羰基硫研究结果的基础上,发现吸附在金属硫化物表面上的一氧化碳与活性硫化物的相互作用是生成羰基硫的主要反应步骤,活性硫化物可能是硫化氢热解成蒸气硫或硫氢根离子及硫化氢与金属氧化物反应生成的金属硫化物。 相似文献