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Experiment And Mechanism Research Of A Novel Process Of Removing SO2 And NO2 From Flue Gas By Sodium Humate

Posted on:2012-06-06Degree:DoctorType:Dissertation
Country:ChinaCandidate:Z G SunFull Text:PDF
GTID:1481303389490824Subject:Engineering Thermal Physics
Abstract/Summary:PDF Full Text Request
With the development of economy and society, the atmospheric pollution caused by SO2 and NO2 from the combustion of fossil fuels has been gradually more serious. Although the wet flue gas desulfurization (FGD) processes based mainly on limestone scrubbing are frequently used, they have many disadvantages such as high capital operating costs, a lager water requirement, poor quality of byproducts, and even producing second pollution, Which is difficult to accept for the developing countries. Therefore, it is important to investigate and develop the cost effective technologies of removing SO2 and NOx for resolving the atmospheric pollution in china.In this thesis, a novel process of simultaneous removing SO2 and NO2 by sodium humate (HA-Na) was proposed. This process is a resourceful type of environmental protection technology for flue gas desulfurization and denitrifcation (FGDD) and has many advantages including: (a) lower costs and energy requirements, (b) almost no waste sludge, (c) the recovery of sulfur and nitrogen as a useful sulfur-containing nitrogen fertilizer, and (d) the simultaneous removal of SO2 and NO2. Therefore, it is hopeful to be used in a large scale. For developing the novel process, investigations were conducted in this thesis as following:(1) Preparation of HA-Na/?-Aluminum (?-Al2O3) and its desulfurization properties.A new composite adsorbent of HA-Na/?-Al2O3 for FGD was prepared using the impregnation method. The desulfurization property of the adsorbent was studied in a fixed-bed. The experimental results show that the HA-Na-coating on the?-Al2O3 fibers improved the property of?-Al2O3 support for FGD. On the other hand, the HA-Na-coating on the adsorbent of HA-Na/?-Al2O3 impregnated with ammonia (NH4OH) played an important role in enhancing the desulfurization property of a-Al2O3. Due to the strong adsorption capability of HA-Na, more NH4OH was adsorbed in the adsorbent of HA-Na/?-Al2O3 the longer a high SO2 conversation rate was maintained. In addition, the desulfurization products can be flushed from?-Al2O3 fibres and make into the compound fertilizer consisting of ammonium sulfate [(NH4)2SO4], ammonium humate (HA-NH4), and HA-Na. the recycling use of?-Al2O3 fibres was also easily achieved. (2) Experiment and mechanism research of FGD by HA-Na solution.Experiments were carried out to examine the effect of various operating parameters, such as the HA-Na concentration, pH, temperature, gas flow rate, O2 concentration, SO2 inlet concentration, and NO2 coexiting with SO2, on the SO2 absorption efficiency and breakthrough time in a lab-scale bubbling reactor. The experimental results indicate that the HA-Na concentration significantly influences the breakthrough time but has little effect on the SO2 absorption efficiency. The breakthrough time increases with the HA-Na concentration reaching 0.06 g/mL, and after this value, it begins to decrease. The SO2 absorption efficiency maintains 99% when pH is above 4.5. The low temperature is favorable to SO2 absorption. The increase of the SO2 inlet concentration improves the mass transfer of SO2 and accelerates the SO2 consumption rate. NO2 coexisting with SO2 can promote SO2 absorption because it may speed up oxidation of sulfite to sulfate. HA-Na solution shows great performance in SO2 absorption, and the SO2 absorption efficiency can be above 98% in the optimal condition. Moreover, the desulfurization products can be made into the humic acid (HA) compound fertilizer, and recycling water can be obtained in this desulfurization process.(3) Experiment and mechanism research of removing NO2 from flue gas by HA-Na solution.The effects of various factors like the HA-Na concentration, NO2 inlet concentration, temperature, O2 concentration, the oxidation extent (the NO2 volume fraction in NOx) and SO2 coexiting with NO2, have been investigated in a bubbling rector The experimental results show that the NO2 absorption efficiency is increased with HA-Na concentration, O2 concentration, and pH. The low absorption temperature is favorable to the absorption of NO2. The inlet NO2 concentration has not significant effect on the NO2 absorption efficiency. It is concluded that SO2 coexisting with NO2 may go against removing NO2 until SO2 concentration is saturation in HA-Na solution. The NOx absorption efficiency is proportional to the oxidation extent when the NO2 concentration is lower than 0.1% in flue gas. HA-Na solution has strong NO2 absorption capability, and the NO2 absorption efficiency can be above 95%. Moreover, the denitrification products can be made into the HA compound fertilizer.(4) Simultaneous removal of SO2 and NO2 from flue gas by HA-Na solution.This study relates to the SO2/NO2 absorption efficiency and products of simultaneous removing SO2 and NO2 in a bubbling reactor, especially the effect of recycled water on the SO2/NO2 absorption. Under alkaline conditions, the sulfate content in S-containing compound decreases with the increase of NO2 concentration, whereas there is a contrary result under acidic conditions. Whether the absorption liquid is alkaline or acidic, the presence of NO2 improves the SO2 absorption into HA-Na solution. The NO2 absorption efficiency in the presence of SO2 is more than that in the absence of SO2.The NO2 absorption efficiency decreases slightly with the increase of NO2 concentration, and NO 3- is the main byproduct of absorption of NO2.The NO2 absorption efficiency can be improved with the cycle number rising due to the increasing amount of sulfite. Although all the ion concentrations of Na+, SO42-, SO32-, and NO 3- have a gradual increase as the cycle number rises, the ion concentrations of SO42- and Na+ are far more than that of the other ions, which results in a slight decrease of the SO2 absorption efficiency. However, the initial pH of HA-Na solution prepared by recycled water decreases from 10 to 8.1 with the cycle number increasing from 1 to 10, whereas the final pH remains almost constant (3.3). The SO2 absorption efficiency is above 98% and the NO2 absorption efficiency may reach above 95% in the optimal condition in this process. The chief byproduct is a compound fertilizer consisting of HA, sulfate, and nitrate. The oxygen content in the byproducts increases with the cycle number rising, which indicates that the O-containing functional groups of HA is increased and the activity of HA is improved by oxygenolysis.(5) Modeling and numerical simulation of mass transferring for FGD by HA-Na in bubbling reactor.According to the double-film theory, the theoretical analysis of gas-liquid mass transfer process for absorption of SO2 by HA-Na solution was carried out, and the mass-transfer model was established. The parameters in this model were determined on the basis of experimental results, such as pseudo-first-order rate constant, average bubble diameter, gas holdup, and specific gas-liquid interfacial area. The nonlinear regression model of SO2 equilibrium pressure was constructed by the losopt-software. According to the SO2 mass-transfer model, the SO2 mass-transfer during the FGD by HA-Na was numerical simulated, and the simulated result is in agreement well with the experimental result.(6) Design and make the spray absorber and process units for the simultaneous removal of SO2 and NO2 process by HA-Na solution.According the working principle, process characteristics and design principle of spray absorber, the spray absorber and process units for removing SO2 and NO2 by HA-Na solution were designed and made. The results show the simultaneous removal of SO2 and NO2 process by HA-Na has a better performance on the whole, and the SO2 absorption efficiency is above 98% and the NO2 absorption efficiency is above 95% in the optimal condition. During this process, not only the high SO2/NO2 absorption efficiency, but also the precipitation separation of by-products, the neutralization and recycling of acidic water solution can be achieved. The economic evaluation of FGD process by HA-Na was also carried out, and this process has good economy.
Keywords/Search Tags:Sodium humate, humic acid, SO2, NO2, NOx, flue gas, desulfurization, denitrification, gas-liquid reaction, chemical absorption, mechanism analysis
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