Treatment of amine wastes generated in industrial processes.
←
→
Page content transcription
If your browser does not render page correctly, please read the page content below
IOP Conference Series: Materials Science and Engineering PAPER • OPEN ACCESS Treatment of amine wastes generated in industrial processes. To cite this article: S. R. S. Salim 2021 IOP Conf. Ser.: Mater. Sci. Eng. 1092 012051 View the article online for updates and enhancements. This content was downloaded from IP address 46.4.80.155 on 16/09/2021 at 22:43
iCITES 2020 IOP Publishing IOP Conf. Series: Materials Science and Engineering 1092 (2021) 012051 doi:10.1088/1757-899X/1092/1/012051 Treatment of amine wastes generated in industrial processes. S. R. S. Salim Abstract. Amines such as monoethanolamines (MEA), ethanolamines (EA), diethanolamines (DEA), and N-methyldiethanolamine (MDEA) are widely used in post combustion CO 2 capture process (CCP) at natural gas conditioning plants to remove acid gas impurities. These amines have significant impact to the environment and human health. Therefore, amine wastes generated from CCP must be treated before they are exposed to the environment. This paper reviews some of the available methods to treat amines such as using physical treatments (filters, increase in temperature, polymerization), chemical treatments (SOX and NOX in the flue gas, fly ash, acid solvents), and biological treatments (aerobic degradation and anaerobic degradation by microbacteria, nitrate respiration). 1. Introduction The release of green house gases has affected earth climate change as the temperature rises. One of the most common green house gases is carbon dioxide (CO2). In this modern world, the release of CO2 from industrial factories is high as there are raising demands in productions sector. Thus, there is a need to develop cost effective and energy saving CO2 absorption schemes [1]. Amine has been used commercially in many industrial processes mainly for the removal of acid gas impurities such as hydrogen sulfide (H2S), carbonyl sulfide (COS), carbon disulfide (CS2), and also carbon dioxide (CO2) in post combustion CO2 capture at natural gas conditioning plants [2]. It has been established for over 60 years in chemical, oil, and gas industries to remove hydrogen sulphide and CO2 from gas stream. This process is called natural gas sweetening operations [3]. This is an absorption process where flue gas stream is exposed to an aqueous amine solution to remove CO2 and recycle CO2 in the flue gas stream. This chemical absorption by amines has been used to reduce CO2 release to the environment. There are several reasons to why amines have been used in the natural gas conditioning operations. This is because it is easy to use as aqueous amines have high CO2 absorption capability in the chemical reactions and can obtain high yield of CO2 [4]. For example, Figure 1 showed the reaction of ethanolamine (EA) with CO2 to form (2-hydroxyethyl) carbamate ion and a protonated amine. In today’s world, the need of clean and environmentally friendly energy resources has increased the demand for natural gases. This is why amines have to be used in natural gas conditioning plants in order to reduce the CO2 release to the environment. . Figure 1: Reaction of two MEA molecules with CO2 to form the carbamate anion and a protonated amine [4]. There are a few types of amines used in the process, which can be classified into two categories: chemical and physical solvents [5]. Amines used in treating low and medium pressured gas streams are Content from this work may be used under the terms of the Creative Commons Attribution 3.0 licence. Any further distribution of this work must maintain attribution to the author(s) and the title of the work, journal citation and DOI. Published under licence by IOP Publishing Ltd 1
iCITES 2020 IOP Publishing IOP Conf. Series: Materials Science and Engineering 1092 (2021) 012051 doi:10.1088/1757-899X/1092/1/012051 called chemical solvents such as monoethanolamine (MEA), diethanolamine (DEA), N- methyldiethanolamine (MDEA), and several other alkanolamines mixtures. The examples of chemical formulae of different types of amine used in CCP are listed in Table 1. High-pressurised gas streams are treated with physical solvents such as propylene carbonate. Amines are organic compounds that can be used in rapid reaction with CO2 selectively and reversibly as they have active N atoms. Monoethanolamines (MEA) have been used commercially in many post combustion CO2 capture plant as they have suitable characteristics such as high reactivity, water solubility, and also cost effective [6]. Table 1: Examples of common amines used in CO2 capture process [4]. 2. The problems of using amines The wide usage of amines in post combustion CO2 capture has it significant effect to the environment. The high reaction rate and its capability of removing traces of CO2 made it the most suitable and cost effective solvents in CO2 capture processes but at a hefty price. There are non-volatile degradation products from the process that must be removed from amines solvents before the recycling of solvents and to be treated as hazardous chemical wastes [7]. This removal process will add extra works and cost to the CO2 capture process. The increase of industrial wastewater production and its release to the environment leads to the rise of xenobiotic compound in the aquatic environment. Most of the amines solvents used in the process are recycled to the top of the absorber [8]. A certain amount of the recycled amines are periodically distilled to remove the impurities and insoluble materials. During these processes, there are a few problems occured. Accidental spill to the environment is one of the major problems. The amines used in natural gas capture plants are highly soluble in water [9]. The reclaimer waste will contain water, amine, ammonia, other degradation products, heat-stable salts, flue gas impurities, and also corrosion products. The amines solvents loss due to degradation also occurs during the process in natural gas sweetening [10]. This will add to the cost of operation, as amines solvents must be top up frequently. Amine gases that are released to the air could be dissolved in the rain droplets and ended up in water supplies such as rivers and lakes. High concentration of amines disposed to the environment could leads to disruption of aquatic life and bioconcentration potential [3]. The reaction of amines with CO2 in flue gas treatment may also leads to emission of compounds such as ammonia as the main degradation products of amines [11]. High concentrations of ammonia released to the environment are fairly toxic and could cause skin burns and irritations to human. Corrosion of metals especially in the natural gas plants is one of the problems occured when using alkanolamines [12]. Foaming also occured during the interaction between natural gas and amines that leads to accumulation of organic acids. The leachate from this process will accidentally released to the 2
iCITES 2020 IOP Publishing IOP Conf. Series: Materials Science and Engineering 1092 (2021) 012051 doi:10.1088/1757-899X/1092/1/012051 environment through water table and air thus affect the aquatic life as well as increase in the maintenance costs. Amines also have high vapour pressure. This characteristic results in significant vapourization and solvent loss in the condition with high temperature [7]. This will increase the cost of post combustion CO2 capture as the need to continuously adding alkanolamines solvent to the process. 3. Treatment options There are a few criteria in determining good amines treatment methods. The decomposition of amines into ammonia (NH3) is one of the ways to reduce nitrogen oxides (NOx) emission in the reclaimer plants to the environment [6]. Amine decomposition is important to reduce their effect to the environment. The end product to be released to the environment must have the least effect on human health, as well as the environment. This process can be achieved by physical treatment, chemical treatment and biological treatment. Summary of these treatments are illustrated in Table 2. 3.1. Physical treatments of amines There are a few methods to treat amine using physical treatment. Methods such as gravitational breaking (floatation), ultra-filtration membrane separation, and micro-filtration have been used in the reduction of ethanolamine in oily wastewater. Thermal methods such as heating and evaporation were also used in the physical treatments of amines including air stripping [13]. These processes were done to separate amines waste from oily wastewater. The increase of temperature up to 160°C reduces the concentration of MEA by 95% in a high pressured vessel during CO2 removal process [14]. The reduction of MEA concentration was determined and their capacity to remove CO2 is measured after the concentration reduced. According to Davis and Rochelle [7], the increase of temperature and loading also increases the degradation of MEA in the presence of CO2. Thus, the higher the concentration of CO2, the more amines degraded during thermal degradation [15]. As amines and other degradation product may be emitted through gas phase emission and mist (aerosol production) during gas conditioning processes, these mist particles must also be contained before accidentally being released to the open air. Conventionally, water wash sections and demisters were built together in the plant. Research has been done to control amine mist emission is by using filter consists of wetted rotating brush and candle filter [16]. Physical treatments of amines have a few disadvantages. The removal of amines wastes by high temperature is regarded as non-economical [8]. This is because of the high water content that requires high-energy usage for its evaporation. The trend of degradation reduced after a few weeks of exposure to the high temperature [17]. This is because of the reduction of other byproducts that are crucial for amines wastes degradation during the high temperature treatment. As filters are being used for the treatment process, it must be maintained regularly for the amines to be treated properly. Some filters must be built in the CCP to ensure the effectiveness of amine treatment process. 3.2. Chemical treatments of amines The chemical treatment usually involves in the changing of pH of the solvents [13]. Further amine biodegradation is related greatly to the pH values. There are acid-base reactions where acids and acid gases reacts irreversibly with amines to form anions that are heat-resistant [4]. This includes SOX and NOX in the flue gas, mineral acids in feed coal, and also carboxylic acids generated by oxidative degradation [18]. Amines reactions with NOX can produce nitrates and nitrites. Nitrogen-fixing bacteria can easily fix these two compounds. Some nitrosamine formation must be expected from any amine degradation reaction with NOX [19]. Carbamate polymerization of amines can occur under low oxygen level, high CO2 loading, and in high temperature conditions in the boiler of stripper column [4]. Carbamate polymerization can be 3
iCITES 2020 IOP Publishing IOP Conf. Series: Materials Science and Engineering 1092 (2021) 012051 doi:10.1088/1757-899X/1092/1/012051 observed in stripping column where there are possibilities of thermal degradation can happen at temperature above 205°C. Thermal degradation of alkanolamines can also takes place in reaction with CO2 through a cyclization reaction of carbamate to 2-oxazolidone shown in Figure 2 [20]. Figure 2: The degradation of MEA carbamate to 2-oxazolidone mechanism and transition state [20]. The usage of fly ash can improve amines degradation. Fly ash contains varying amount of transition metal ions known to catalyze solvent degradations [21]. Oxidative degradation using fly ash can be done with two mechanisms; electron abstraction and hydrogen abstraction. During both mechanisms, the presence of redox reactive metal ions in fly ash such as Fe2O3 and CaO could generate high numbers of free radicals. Thus accelerating the rate of amine degradation. Oxidative degradation of amines falls under chemical treatments of amines. Amines degradation occurs in the presence of O2. Reaction between MEA and carboxylic acids play roles in solvent degradation. This is proven when N-(2-hydroxyethyl)formamide (HEF) and N-(2- hydroxyethyl)acetamide (HEA) formation were observed during MEA oxidative degradation using carboxylic acids [22]. This type of amines degradation can also be done in closed-batch system with a wet gas blend of CO2 and O2 air [23]. The examples of oxidative degradation of ethanolamines are shown in Figure 3. Oxidative degradation of amines are more complex than thermal degradation [17]. This is because both ionic reactions and radical reactions can take place at the same time. However, by using batch reactors, degradation of amines can be accelerated [24]. This can be done by alternately exposing amines to oxidative and thermal degradation in a single system. 4
iCITES 2020 IOP Publishing IOP Conf. Series: Materials Science and Engineering 1092 (2021) 012051 doi:10.1088/1757-899X/1092/1/012051 Figure 3: Oxidative degradation pathways for MEA [20]. Chemical treatments of amines also have a few disadvantages. Degradation products such as methylated amines are more volatile compared to the parent amine [25]. During chemical treatments of amines, byproducts such as organic acids, aldehyde, and various cyclic compounds were produced [21]. These byproducts need to be collected and treated accordingly. 3.3. Biological treatments of amines Amines are organic subtances that consist of high amount of carbon and nitrogen. Biological treatment could be the most suitable method to reduce the amount of amines released to the environment. Biological treatments of amines consist of two types: Aerobic degradation and anaerobic degradation. Biological treatment could transform amines wastes into recoverable products without harming the environment. Aerobic degradation is much more preferable as compared to anaerobic. This is because it is easier to control aerobic conditions such as to provide sufficient O2 to the reactor. Ethanolamine in soil is biodegraded and converted to ammonium and acetaldehyde through hydrolisis process [26]. This biodegradation process occured in aerobic conditions where ammonium is oxidized to nitrite and nitrate as shown in Figure 4. Ethanol and acetic acid are degraded from acetaldehyde that is produced from the ethanolamine hydrolisis reaction. Acetic acid and ethanol produced from this reaction are then used in denitrification process and both compounds can be easily degraded and used by bacteria. 5
iCITES 2020 IOP Publishing IOP Conf. Series: Materials Science and Engineering 1092 (2021) 012051 doi:10.1088/1757-899X/1092/1/012051 Figure 4 Biodegradation of monoethanolamine into ammonium and acetaldehyde [26]. Aerobic degradation using microorganisms require constant supply of oxygen to degrade amines wastes. Escherichia coli (E.coli) K12 strains culture have been used effectively to transform amines wastes into biomass, acetyldehyde, and acetic acid [27]. The increase of E.coli K12 growth in amines wastes solution indicated that the presence of additional nitrogen sources helps in the bioremediation of amines wastes [27]. The biological removal of nitrogen from amines wastes through nitrification process increases the rate of amines wastes biodegradation [11]. The main degradation product of amines is ammonia. Aerobic nitrification process includes the oxidization of ammonia to NO2- and NO3- by nitrite-oxidizing bacteria and ammonia-oxidizing bacteria. MEA biodegradation process started in anoxic environment of the denitrification reactor after the nitrification process [11]. This is where nitrous oxides produced during nitrification process are reduced to nitrogen by electron donated by organic carbon sources. This process reduces the amount of nitrous oxides released to the environment. According to Lai & Shieh [28], monoethanolamines can be degraded via nitrate respiration under anoxic condition. This can be done using bacterial biofilms obtained from a reactor which treats a mixture of MEA. Anaerobic degradation of amines produces CO2 and methane [10]. Anaerobic reactor must be built for zero O2 presence at all times which can be hard to controlled. Amines can also be treated in slurry system using suspension of microbacteria in a bioreactor [29]. Slurry bioreactor system is used for soil polluted by amines under controlled environment. Reactions in slurry bioreactors increase the mass transfer rates and also increase the contact between microorganisms and amines. There were also researches that had been done on anaerobic-aerobic combined system for amines degradation [30]. Anaerobic degradation process causes amines discoloration by reductive degradation. Aerobic degradation that occured after introduction of O2 breaks down amines waste into environmentally friendly elements such as nitrogen and hydrogen. This showed by using both anaerobic and aerobic degradation systems, the treatment of amines wastes could be achieved. There are a few disadvantages using biological treatment to treat amines wastes. First, it is hard to find bacteria that can reduce amines wastes at optimal rates. A group of microbacteria must be used to achieve this. Second, it is important to consider the end product that does not have any significant effect when released to the environment. This includes the removal of contaminated media to a specific treatment area such as designated land treatment area or by composting [31]. Third, it is costly to keep a reactor O2 free during anaerobic degradation [10]. 6
iCITES 2020 IOP Publishing IOP Conf. Series: Materials Science and Engineering 1092 (2021) 012051 doi:10.1088/1757-899X/1092/1/012051 Table 2: Summary of amines treatment options. Treatment Options Methods References Physical treatment Heating and evaporation including air [13] stripping. Carbamate polymerization of amine. [4] Thermal degradation of alkanolamines with [20] CO2 through a cyclization reaction of carbamate to 2-oxazolidone. Increased temperature reduces the [14] concentration of MEA in a high-pressured [32] vessel. [15] Filter consists of wetted rotating brush and [16] candle filter to control amines mist emission. Chemical treatment The changing of pH of the solvents. [13] Acid-base reactions. [4] SOX and NOX in the flue gas, mineral acids in [18] feed coal, and also carboxylic acids generated by oxidative degradation. The usage of fly ash as metal ions source. [21] MEA oxidative degradation using carboxylic [22] acids. Closed-batch system with a wet gas blend of [23] CO2 and O2 air. Ionic reactions and radical reactions can take [17] place at the same time Alternately exposing amines to oxidative and [24] thermal degradation in a single system. Biological treatment EA is biodegraded and converted to [26] ammonium and acetaldehyde through hydrolisis (aerobic conditions). Aerobic degradation using microorganisms [27] (E.coli). Nitrification process. [11] Anoxic environment of the denitrification [11] reactor. Nitrate respiration under anoxic condition [28] using bacterial biofilm. Anaerobic degradation of amines produces [10] CO2 and methane. Treatment in slurry system using suspension of [29] microbacteria in a bioreactor. Anaerobic-aerobic combined system in [30] breaking down amines wastes. 7
iCITES 2020 IOP Publishing IOP Conf. Series: Materials Science and Engineering 1092 (2021) 012051 doi:10.1088/1757-899X/1092/1/012051 4. Conclusions and recommendations The goal of amines treatment is to reduce their impact to the environment. While physical and chemical degradation of amines are simpler to be applied such as increasing the temperature, building filters into the treatment plants, and adding more chemicals to degrade amines wastes, these methods can be cost ineffective. From the review presented, the best amines treatment is by using biological methods. This is because by using biological methods (aerobic and anaerobic degradation), amines waste can be reduced to their simplest forms and also the most economically feasible technology to degrade industrial organic compound. Since amines have carbon and nitrogen, many types of bacteria use these elements as source of living. This shows that more research needs to be done in this field to obtain more information on the removal of amines waste from the environment. Research such as using different types of bacteria, upgrading on-site removal systems, and using blends of amines and other chemicals can be done to add more information on this field. The research on what type of bacteria that is less harmful to the environment during the removal of amines can also be done. The usage of other materials and techniques in CO2 capture plants such as solid sorbents can also reduce the usage of amines. Such an understanding is essential as amines bioremediation processes are further optimized. 5. References [1] Chakravarti S, Gupta A, & Hunek B 2001 Advance technology for the capture of CO2 from flue gases 1st National Conference on Carbon Sequestration Washington DC [2] Islam MS, Ali BS, & Yusoff R 2010 Degradation studies of amines and alkanolamines during CO2 absorption and stripping system Engineering e-Transaction 5 97-109 [3] Eide-Haugmo I, Brakstad OG, Hoff KA, Sørheim KR, daSilva EF, & Svendsen HF 2009 Environmental impact of amines Energy Procedia 1 1297-1304 [4] Dumeé L, Scholes C, Stevens G, & Kentish S 2012 Purification of aqueous amine solvents used in post combustion CO2 capture: A Review International Journal of Greenhouse Gas Control 10 443-455 [5] Thitakamol B, Veawab A, & Aroonwilas A 2007 Environmental impacts of absorption-based CO2 capture unit for post-combustion treatment of flue gas from coal-fired power plant International Journal of Greenhouse Gas Control 1 318–342 [6] Botheju D, Li Y, Hovland J, Haugen HA, & Bakke R 2011 Biological treatment of amine wastes generated in post combustion CO2 capture Energy Procedia 4 496-503 [7] Veltman K, Singh B, & Hertwich EG 2010 Human and environmental impact assessment of post combustion CO2 capture focusing on emissions from amine-based scrubbing solvents to air Environmental, Science, & Technology 44 1496-1502 [8] Ohtaguchi K & Yokoyama T 1997 The synthesis of alternatives for the bioconversion of waste- monoethanolamine from large-scale CO2 removal processes Energy Conversion and Management 38 539–44 [9] Gjernes E, Iren L, & Maree Y 2013 Health and environmental impact of amine based post combustion CO 2 capture Energy Procedia 00 1–8 8
iCITES 2020 IOP Publishing IOP Conf. Series: Materials Science and Engineering 1092 (2021) 012051 doi:10.1088/1757-899X/1092/1/012051 [10] Henry IA, Kowarz V, & Østgaard K 2017 Aerobic and anoxic biodegradability of amines applied in CO2 capture International Journal of Greenhouse Gas Control 58 266-275 [11] Hauser I, Colaço AB, & Skjæran JA 2013 Biological N Removal from Wastes Generated from Amine-Based CO 2 Capture : Case Monoethanolamine Journal of Biochemical Bi 1449–1458 [12] Reynolds AJ, Verheyen TV, Adeloju SB, Meuleman E, & Feron P 2012 Towards commercial scale postcombustion capture of CO2 with monoethanolamine solvent: key considerations for solvent management and environmental impacts Environmental Science & Technology 46 3643–54 [13] Libralato G, Ghirardini AV, & Avezzù F 2008 Evaporation and air-stripping to assess and reduce ethanolamines toxicity in oily wastewater Journal of Hazardous Materials 153 928– 936 [14] Zoannou KS, Sapsford DJ, & Griffiths AJ 2013 Thermal degradation of monoethanoalmine and its effect on CO2 capture capacity International Journal of Greenhouse Gas Control 17 423- 430 [15] Mahmud N, Benamor A, Soliman A, & Nasser MS 2018 Thermal degradation of aqueous amine/amino acid solutions in the presence and absence of CO2 IOP Conference Series: Materials Science & Engineering 423 [16] Bade OM, Knudsen JN, Gorset O, & Askestad I 2014 Controlling amine mist formation in CO2 capture from residual catalytic cracker (RCC) flue gas Energy Procedia 63 884-892 [17] Lepaumier H, da Silva EF, Einbu A, Grimstvedt A, Knudsen JN, Zahlsen K, & Svendsen HF 2011 Comparison of MEA degradation in pilot-scale with lab-scale experiments Energy Procedia 4 1652–1659 [18] Strazisar BR, Anderson RR, & White CM 2003 Degradation pathways for monoethanolamine in a CO2 capture facility Energy and Fuels 17 1034-1039 [19] Fosts B, Gangstad A, Nenseter B, Pedersen S, Sjøvoll M, & Sørensen A L 2011 Effects of NOX in the flue gas degradation of MEA Energy Procedia 4 1566-1573 [20] Vevelstad SJ, Eide-Haugmo I, daSilva EF, & Svendsen HF 2011 Degradation of MEA; A theoretical study Energy Procedia 4 1608–1615 [21] Chandan P, Richburg L, Bhatnagar S, Remias JE, & Liu K 2014 Impact of fly ash on methylethanolamine degradation during CO2 capture International Journal of Greenhouse Gas Control 25 102-108 [22] Jens K J, & Wang T 2013 Oxidative degradation of AMP/MEA blend for post-combustion CO2 capture Energy Procedia 37 306-313 [23] Vevelstad SJ, Grimstvedt A, Einbu A, Knuutila H, daSilva EF, & Svensen HF 2013 Oxidative degradation of amines using a closed batch system International Journal of Greenhouse Gas Control 18 1-14 [24] Closmann F & Rochelle G 2011 Degradation of aqueous methyldiethanolamine by temperature and ovygen cycling Energy Procedia 4 23-28 9
iCITES 2020 IOP Publishing IOP Conf. Series: Materials Science and Engineering 1092 (2021) 012051 doi:10.1088/1757-899X/1092/1/012051 [25] Rochelle GT 2012 Thermal degradation of amines for CO2 capture Current Opinion in Chemical Engineering 1 183-190 [26] Ndegwa AW, Wong RCK, Chu A, Bentley LR, & Lunn SRD 2004 Degradation of monoethanolamine in soil Journal of Environmental Engineering Sciences 145 137–145 [27] Ohtaguchi K, Koide K, & Yokoyama T 1995 An ecotechnology-integrated MEA process for CO2-removal Energy Conversion and Management 36 401–404 [28] Lai B & Shieh WK 1996 Batch monoethylamine degradation via nitrate respiration Water Research 30 2530–34 [29] Robles-González IV, Faba F, & Poggi-Vavaldo HM 2008 A review on slurry bioreactors for bioremediation of soils and sediments Microbial Cell Factories 7 [30] Baêta BEL, Lima DRS, Silva SQ, & Aquino SF 2015 Evaluation of soluble microbial products and aromatic amines accumulation during a combined anaerobic/aerobic treatment of a model azo dye Chemical Engineering Journal 259 936-944 [31] EPA 2006 In Situ and Ex Situ Biodegradation Technologies for Remediation of Contaminated Sites Engineering Issue US of Research Office Transfer Support Division Technology Grosse Douglas [32] Davis J & Rochelle G 2009 Thermal degradation of monoethanolamine at stripper conditions Energy Procedia 1 327-333 10
You can also read