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1.
    
In the present study, a simple model was used to predict the removal efficiency of a venturi scrubber for H2S absorption into a ferric chelate solution. From momentum and mass balances in the scrubber, a set of first‐order, nonlinear ordinary differential equations relating predominantly the liquid velocity with the H2S concentration in the liquid along the axial direction in the scrubber were formulated. These relationships were numerically solved to give performance profiles. The validity of the model was examined by comparing the results of the model with experimental data from the working laboratory scale. The results predicted from the model are in good agreement with the experimental data obtained in different sizes of the venturi scrubber and operating variables.  相似文献   

2.
本文就木质素磺酸钠溶液脱除烟道气中SO_2进行了实验研究。实验采用双搅拌气-液反应器,探讨了木质素磺酸钠的浓度、温度等因素对SO_2吸收的影响,并求取了化学吸收增强因子。结果表明,木质素磺酸钠能有效地脱除烟道气中的SO_2。  相似文献   

3.
A rate-based model of a counter-current reactive absorption/desorption process has been developed for the absorption of SO2 into NaHCO3/Na2CO3 in a packed column. The model adopts the film theory, includes diffusion and reaction processes, and assumes that thermodynamic equilibrium among the reacting species exists in the bulk liquid. Model predictions were compared to experimental data from literature. For the calculation of the absorption rate of SO2 into NaHCO3/Na2CO3 solutions and concomitant CO2-desorption, it is important to take into account all reversible reactions simultaneously. It is clear that the approximate analytical based model cannot be expected to predict the absorption rates under practical conditions because of the complicated nature of the reactive absorption processes. The rigorous numerical approach described here only requires definition of the individual reactions in the system, and subsequent solution is independent of specific assumptions made, or operational variables like pH or compound concentrations. As an example of the flexibility of this approach, additional calculations were conducted for SO2 absorption in a phosphate-based buffer system.  相似文献   

4.
A mathematical model has been developed to predict So2 absorption and removal during the constant rate drying period of a spray dryer. The model, based on film theory, treats the atomized slurry droplets as spheres containing discrete sorbent particles of slaked lime with the fluid uniformly distributed around the individual particles. The model includes gas and liquid phase mass transfer coefficients as well as resistance to Ca(OH)2 dissolution. A sensitivity analysis has been conducted and a comparison was made between pilot-scale experimental data and model-predicted values of S02 removal efficiency.  相似文献   

5.
火电厂二氧化硫排放量的测算方法研究   总被引:1,自引:0,他引:1  
SO2排放量的准确测算是企业内部科学管理和有效控制其排放量的基础,针对传统的SO2排放量的测算方法存在的问题与局限,本文提出了一种基于硫平衡的更简单、科学地测算SO2排放量的方法。通过该方法,可以准确地测算火电厂生产过程中二氧化硫的排放量,从而有利于对火电厂生产的工艺与组织实施更有效的监控,既节省了时间,又节约了成本,并提高了工作效率。  相似文献   

6.
The interaction of sulfur dioxide with a commercial NOx storage-reduction catalyst (NSR) has been investigated using in situ IR and X-ray absorption spectroscopy. Two pathways of catalyst deactivation by SO2 were identified. Under lean conditions (exposure to SO2 and O2) at 350 °C the storage component forms barium sulfates, which transform from surface to hardly reducible bulk sulfate species. The irreversible blocking of the Ba sites led to a decrease in NOx storage capacity. Under fuel rich conditions (SO2/C3H6) at 350–500 °C evidence for the formation of sulfides on the oxidation/reduction component (Pt) of the catalyst was found, which blocks the metal surface and thus hinders the further reduction of the sulfides.  相似文献   

7.
8.
新型HS—2钒催化剂上SO2氧化的本征动力学研究   总被引:1,自引:0,他引:1  
HS-2钒催化剂是在钾-钒系催化剂内添加了适量的低温活性物质而成。作者用无梯度反应器和积分反应器,在较宽的温度范围(653~843K)和转化率范围(3.9%~89%)内对其动力学特性进行了测试,并采用 Powell 非线性最小二乘法回归出动力学方程。  相似文献   

9.
Chemical absorption of CO2 and SO22 as single gases and as a mixture into slurries of Ca(OH) 2 was studied in a stirred vessel with a flat gas-liquid interface. In the case of CO2, the reaction product interrupted the subsequent gas absorption in the absence of a surface active agent. With single gases, the enhancement factor for SO2 was much larger than that for CO2, though both were larger than that into saturated solution. With the mixed gases, the enhancement factor for S02 was almost equal to that for the single gas absorption, but for CO2 it was only slightly larger than that into the saturated solution  相似文献   

10.
Adsorption experiments of SO2 on activated carbon has been carried out for low concentrations (about 100 ppm) at room temperature (15 to 33 °C) with varying humidity in the air. The breakthrough curves show that at high relative humidity or relative higher SO2 concentration, the load capacity increases with respect to temperature. The humidity of the air is also of benefit to the load capacity of SO2. When an adsorption process is interrupted and the activated carbon is kept closed for a while, the SO2 concentration at the exit of a fixed‐bed adsorber is similar to that of the fresh activated carbon and begins at a very low value. It appears that the sorption potential has been refreshed after the storage period. Analysis of desorption experiments by simultaneous thermal analysis combined with mass spectrometry (MS) after loading, shows that the physisorbed SO2 and H2O are desorbed at low temperatures. At higher temperatures, the MS peak of SO2 and H2O occur at the same time. Compared with desorption immediately after loading, after one day, the desorption peak due to the physisorbed SO2 disappears. From this, it can be concluded that the refreshment of the loading capacity of the activated carbon after storage is mainly due to a change in the nature of the SO2 from a physisorbed state to a chemisorbed form. The same mechanism leads to a continuous refreshment of the sorption potential by means of a chemical reaction during the adsorption process.  相似文献   

11.
曹建新  张远  杨静 《贵州化工》2006,31(5):54-56
煤炭是贵州省的重要资源,针对遵义碱厂的废弃物电石渣,利用其组分中含有Ca(OH)2,用于吸收煤燃烧过程中的SO2,从而达到以废治废,变废为宝。  相似文献   

12.
    
Among numerous techniques existing for reducing CO2 emissions, CO2 capture by absorption in aqueous alkanolamine solutions was specifically studied in this work. For the choice of the adequate amine solution, two major criteria must be taken into account: absorption performances (higher with primary and secondary amines) and energy costs for solvent regeneration (more interesting with tertiary and sterically hindered amines). The different types of amines can also be mixed in order to combine the specific advantages of each type of amines, an activation phenomenon being observed. Aqueous solutions of (piperazinyl‐1)‐2‐ethylamine (PZEA, a polyamine known as absorption activator) and 1‐amino‐2‐propanol (AMP, a sterically hindered amine), pure or mixed with other amines, are experimentally compared with respect to CO2 removal performances by means of absorption test runs achieved in a special gas‐liquid contactor at 25 °C. The positive impact of addition of PZEA to monoethanolamine (MEA), N‐methyldiethanolamine (MDEA), and AMP solutions was clearly highlighted. The absorption performances have also been satisfactorily simulated with coherent physicochemical data.  相似文献   

13.
    
A reactor using d.c. corona discharge of negative polarity was applied to remove sulfur dioxide from an oxygen‐nitrogen mixture in the presence or absence of water vapor for temperatures ranging from room temperature to 350 °C. It was observed that increasing the reactor temperature caused a decrease in the removal efficiency. Mixing water vapor with the process gas resulted in an increase of the removal efficiency. The effect of the presence of water vapor on improving the removal efficiency was significant under low temperature conditions, while it was relatively moderate under high temperature conditions. In addition, the solid deposit formed inside the reactor at two temperatures, room temperature and 200 °C, was analyzed with both a differential scattering calorimeter and an X ray diffractometer. The analysis indicated that SO2 was ultimately converted to solid sulfur in both the presence and absence of water vapor in the gas flow.  相似文献   

14.
Literature regarding the mechanism of the electrochemical oxidation of aqueous sulfur dioxide to sulfuric acid has been critically evaluated to provide a detailed understanding of the reaction under various applied conditions. This reaction is of high relevance to the hybrid sulfur cycle for large scale hydrogen production, as well as other industrial applications such as flue gas desulfurisation. Widespread disagreement in the literature and non-reproducible behaviour of the electrochemical oxidation reaction has been found in this review to often be a result of poorly defined electrode preconditioning procedures. It has also been found that the mechanistic pathway of the oxidation reaction is heavily influenced by the electrode material, solution pH and the applied anodic potential. These factors are thought to influence adsorption and the reductive formation of sulfur species at low potentials.  相似文献   

15.
    
A new process for converting sulfur dioxide to elemental sulfur by a cyclic process involving calcium sulfide and calcium sulfate without generating secondary pollutants, developed at the University of Utah, was described in Part I of this series. In this process, sulfur dioxide is reacted with calcium sulfide to produce elemental sulfur and calcium sulfate; the latter is reduced by hydrogen to regenerate calcium sulfide. Here, in Part II, the effects of different pelletization conditions for the initial reactant calcium sulfate on the reactivity of CaS pellets produced from calcium sulfate pellets toward sulfur dioxide were studied. Experiments were performed to investigate the effects of temperature in the range 1023–1173 K, pellet size, cycle repetition, and water vapor or carbon dioxide content in the sulfur dioxide stream. The binder amount and the presence of nickel catalyst did not significantly affect the reaction rate.  相似文献   

16.
概述了国内外烟气脱硫技术的应用现状、脱硫原理及其特点,并提出了我国烟气脱硫技术的研究开发方向。  相似文献   

17.
翟翼  张磊  徐迪  康艳红 《辽宁化工》2009,38(3):195-197
阐述了燃煤烟气中二氧化碳脱除的各种方法。研究了各种CO2的吸收方法,包括物理吸收法中的膜吸收法、吸附剂等,物化吸附法,还有化学吸收剂中的氨水、有机氨等吸收方法,并分析各种方法的特点及优缺点。  相似文献   

18.
《分离科学与技术》2012,47(11-12):3003-3019
Abstract

Carbon dioxide was absorbed into aqueous solution of sodium glycinate (SG) at different SG concentrations, CO2 partial pressures, and temperatures in the range of 0.5–3.0 kmol/m3, 25–101.3 kPa, and 298–318 K, respectively, using a stirred semi-batch vessel with a planar gas-liquid interface. Both the reaction order and rate constant are determined from gas absorption rates under the fast reaction regime. The reaction was found to be first order with respect to both CO2 and SG. The activation energy for the CO2-SG reaction has been found to be 59.8 kJ/mol. The second-order reaction rate constants were used to obtain the theoretical values of absorption rate based on the film theory.  相似文献   

19.
    
A DC corona discharge reactor was applied to remove sulfur dioxide (SO2) and benzene (C6H6) from N2‐O2‐H2O mixed gas in the temperature range from room temperature to 400 °C. When SO2 was removed, the temperature elevation caused the decrease of the removal efficiency of SO2. On the other hand, the removal efficiency of C6H6 was not significantly influenced by the temperature elevation. In the simultaneous removal of SO2 and C6H6 in the relatively low temperature range below 200 °C, the removal efficiency of SO2 is significantly inhibited by coexisting C6H6. When the simultaneous removal was conducted in the high temperature range, the removal efficiency of SO2 was not sensitive against the coexisting C6H6. On the other hand, the removal efficiency of C6H6 was almost independent of coexisting SO2 at all temperatures. A hypothesis of reaction mechanism was discussed based on radical reactions with SO2 and C6H6 to explain the trend observed in the experiment.  相似文献   

20.
Absorption rates of carbonyl sulfide and carbon dioxide into aqueous methyldiethanolamine solutions with and without heterocyclic amine additives were measured in a stirred cell apparatus. All of the heterocyclic amine additives catalyzed COS absorption more strongly than that for CO2. In instances in which absorption rates were improved by the additives, those with the lowest pKb's were the most effective, although steric factors also apparently influence reaction kinetics.  相似文献   

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