本文選題：微生物脫鹽燃料電池　切入點(diǎn)：生物陰極　出處：《哈爾濱工業(yè)大學(xué)》2015年博士論文　論文類型：學(xué)位論文

【摘要】：自從1980年之后,全球范圍內(nèi)的海水淡化裝機(jī)容量大幅度上升,海水淡化規(guī)模以每年最高30%的速度在增長(zhǎng)。在使用海水淡化增加飲用水的同時(shí),能源的消耗巨大,在最近建設(shè)的反滲透海水淡化廠中,能量的消耗大約為3到4 k Wh/m3,能源的短缺及過(guò)高的運(yùn)行成本,限制了其廣泛應(yīng)用。特別是對(duì)于遠(yuǎn)離陸地的海島及長(zhǎng)期海上作業(yè)的輪船等特殊環(huán)境,由于沒有足夠的電能而無(wú)法從海水中獲得淡水。2009年,微生物脫鹽燃料電池(Microbial desalination cell,MDC)的提出使得在不消耗電能的情況下實(shí)現(xiàn)海水淡化成為可能。經(jīng)過(guò)5年多的研究,MDC技術(shù)雖然在脫鹽效率上有所提高,但是由于MDC陰極中仍使用難以循環(huán)利用的鐵氰化鉀溶液或昂貴的鉑(Pt)做催化劑的空氣陰極,限制了MDC的擴(kuò)大化、降低了實(shí)際應(yīng)用的可能性。在MDC脫鹽過(guò)程中,隨著脫鹽室鹽濃度的降低,其系統(tǒng)的內(nèi)阻導(dǎo)致脫鹽效率的顯著下降,這方面的特性也使得MDC不適用于低濃度含鹽水,難以將海水脫鹽到可飲用的標(biāo)準(zhǔn)。針對(duì)以上問(wèn)題,本研究在開發(fā)廉價(jià)可持續(xù)性催化劑、MDC與其他技術(shù)耦合深度脫鹽等方面做了系統(tǒng)性研究。提出了以同步脫鹽、產(chǎn)電為目的的生物陰極MDC;并將生物陰極MDC產(chǎn)生的電能用于驅(qū)動(dòng)膜電容脫鹽技術(shù)(Membrane capacitive deionization,MCDI)進(jìn)行深度脫鹽。為MDC低成本應(yīng)用于海水除鹽獲得淡水方面提供新思路。開發(fā)了以微生物作為陰極催化劑的空氣陰極MDC。與不添加微生物作為催化劑的曝氣陰極相比,MDC陰極電極表面生長(zhǎng)的生物膜能夠降低陰極的內(nèi)阻、提高M(jìn)DC的輸出電壓和輸出功率,從而提高了MDC的脫鹽速率。運(yùn)行穩(wěn)定后在1000Ω外電阻條件下的最高電壓可達(dá)570 m V,對(duì)于初始濃度為35 g/L的模擬海水,經(jīng)過(guò)480 h的運(yùn)行后,鹽濃度最低可以降到1 g/L以下,去除率可達(dá)90%以上。但隨著鹽水濃度的降低,脫鹽速率大幅度下降,對(duì)于1 g/L以下的鹽溶液,脫鹽速率只有35 g/L時(shí)的16%。MDC脫鹽室內(nèi)鹽溶液濃度的降低會(huì)導(dǎo)致電池內(nèi)阻的急劇上升,其脫鹽速率也大幅度降低。當(dāng)鹽水濃度為1 g/L時(shí),運(yùn)行48 h后,內(nèi)阻由217Ω上升為793Ω。為了實(shí)現(xiàn)能量自給的深度脫鹽,提出用MDC驅(qū)動(dòng)MCDI深度脫鹽的連用技術(shù)。當(dāng)處理1 g/L的低濃度含鹽水時(shí),MCDI的處理效果要遠(yuǎn)高于傳統(tǒng)的電容脫鹽技術(shù)(CDI)的處理效果。與0.8 V的直流穩(wěn)壓電源相比,以MDC作為MCDI供電可使MCDI具有更高的電吸附容量,當(dāng)兩個(gè)MDC并聯(lián)為MCDI供電時(shí),MCDI的吸附容量為直流穩(wěn)壓電源供電的1.6倍。MDC與MCDI系統(tǒng)耦合后不僅實(shí)現(xiàn)對(duì)MCDI脫鹽的連續(xù)運(yùn)行,并且MDC自身在供電的同時(shí),相比于固定外阻200Ω的條件下,脫鹽室的電導(dǎo)率下降速度提高了36.2%。經(jīng)過(guò)MDC與MCDI聯(lián)用處理18個(gè)周期后,處理水可以達(dá)到飲用標(biāo)準(zhǔn)。經(jīng)過(guò)5500h的運(yùn)行,生物陰極MDC的功率密度、庫(kù)倫效率及脫鹽速率分別下降71%,44%和27%,主要是由于陰離子交換膜和陽(yáng)離子交換膜上的生物沉積造成的。膜污染不僅會(huì)引起膜通透性的下降,還會(huì)升高電池的內(nèi)阻。對(duì)系統(tǒng)內(nèi)微生物相的分析表明,MDC陽(yáng)極微生物多樣性要低于報(bào)道的MFC陽(yáng)極微生物組成。在MDC中Proteobacteria的含量要高于MFC陽(yáng)極中大約30%。在MDC系統(tǒng)中,陰極生物膜中的Planctomycetes含量要遠(yuǎn)高于陽(yáng)離子交換膜(CEM),表明生物陰極的好氧反應(yīng)有助于Planctomycetes累積。經(jīng)過(guò)長(zhǎng)期運(yùn)行后,發(fā)現(xiàn)脫鹽室內(nèi)會(huì)出現(xiàn)微生物污染。脫鹽室內(nèi)微生物污染的主要原因是陽(yáng)極內(nèi)的有機(jī)物成分通過(guò)AEM進(jìn)入到脫鹽室內(nèi)污染了脫鹽水。為解決該問(wèn)題,設(shè)計(jì)了帶緩沖室的四室MDC,分別增加了質(zhì)子交換膜(PMDC)和增設(shè)陽(yáng)離子交換膜(CMDC)。與三室MDC相比,PMDC和CMDC在外電阻1000Ω情況下兩端電壓分別下降33.8%和37.4%。對(duì)于初始濃度為35 g/L的鹽溶液,在前240 h內(nèi),PMDC的脫鹽性能優(yōu)于三室MDC。并且PMDC能夠有效地防止乙酸根和磷酸根進(jìn)入到鹽水中,PMDC中乙酸根和總磷的轉(zhuǎn)移量分別為105.7±26.3 mg/L和28.8±9.8 mg/L,只是MDC中的15.8%和35.6%。采用生物陰極MDC和膜電容脫鹽法技術(shù),能夠?qū)⒛M海水(Na Cl濃度35 g/L)的含鹽量降到飲用水標(biāo)準(zhǔn)(氯化物250 mg/L)。但由于其中有機(jī)物的滲透問(wèn)題,仍需要對(duì)脫鹽后的水進(jìn)行后續(xù)處理。雖然有諸多問(wèn)題,但MDC-MCDI技術(shù)使得遠(yuǎn)離陸地的海島及遠(yuǎn)航船只在不消耗電能的情況下獲得淡水成為可能。
[Abstract]:Since 1980, global desalination capacity increased substantially, desalination scale to the highest annual growth at a rate of 30%. In the use of desalination increased drinking water at the same time, the energy consumption is huge, in the recent construction of reverse osmosis desalination plant, energy consumption is about 3 to 4 K Wh/m3, the energy shortage and high operating cost, limits its wide application. Especially for away from the land of the island and maritime operations ships and other special circumstances, because there is not enough power to get fresh water from seawater desalination.2009, microbial fuel cell (Microbial desalination, cell, MDC) makes in the consumption of electrical energy to achieve desalination possible. After 5 years of study, although the MDC technology improves the efficiency of desalination, but because MDC is still difficult to follow the use of cathode Using potassium ferricyanide solution or expensive platinum ring (Pt) air cathode catalyst, limiting the MDC expansion, to reduce the possibility of practical application. In the MDC desalination process, with the decrease of desalination chamber salt concentration, resistance of the system resulting in a significant decrease in the efficiency of desalination, this characteristic also makes MDC is not suitable for the low concentration of salt water, to the desalination of seawater to drinking standards. To solve the above problems, the research on sustainable development of cheap catalyst, made a systematic study of MDC and other technical aspects. The coupling depth desalting is proposed to synchronize the desalination, producing electricity for biocathode MDC purposes; and biocathode MDC generated electricity is used to drive the membrane capacitance (Membrane capacitive deionization, desalination technology MCDI) depth desalting. MDC low cost used in seawater desalination provides a new way to obtain fresh water. Developed with The air microorganism as cathode MDC. cathode catalyst with no microbial aeration as compared to cathode catalyst, MDC biofilm growth on the surface of the cathode electrode can decrease the cathode resistance, improve MDC output voltage and output power, thereby improving the MDC desalination rate. After the stable operation of the highest voltage up to 1000 ohm resistance in external conditions 570 m V, the initial concentration of simulated seawater 35 g/L, 480 h after the operation, the lowest salt concentration can be reduced to below 1 g/L, the removal rate can reach more than 90%. But with lower salt concentration, the desalting rate decreased to below 1 g/L, salt solution, reduce the concentration of indoor 16%.MDC desalination of salt the solution is only 35 g/L when the desalination rate will lead to a sharp rise in the internal resistance of the battery, the desalting rate is also greatly reduced. When the salt concentration was 1 g/L, 48 h after operation, the internal resistance increased to 79 from 217. 3. In order to achieve energy self-sufficiency in desalting, put forward to drive the MCDI MDC for desalting technology. When treated with 1 g/L of low concentration of saline water, the treatment efficiency of MCDI is much higher than the traditional capacitive desalination technology (CDI) treatment effect. Compared with the DC power supply of 0.8 V, with MDC as the MCDI power supply can make the MCDI has a higher adsorption capacity, when the two MDC parallel MCDI power supply, the adsorption capacity of MCDI for the DC power supply 1.6 times.MDC and MCDI coupling system not only realize continuous operation of MCDI desalination, and MDC itself in the power supply at the same time, compared to the fixed external resistance 200 Omega conditions, conductivity decreased desalination chamber rate increased 36.2%. after MDC combined with MCDI treatment after 18 cycles of treatment can reach the standard of drinking water. After the operation of 5500h, power density of biocathode MDC, and the desalting rate efficiency of Kulun Don't drop 71%, 44% and 27%, mainly due to biological deposition of anion and cation membrane. The membrane pollution can not only cause the decline of membrane permeability, the internal resistance of battery is also increased. According to the analysis of the system of microorganisms, microbial diversity is lower than that of MDC anode anode microbial composition. MFC reports the content of Proteobacteria in MDC was higher than that of MFC anode is about 30%. in the MDC system, the content of Planctomycetes cathode in the biofilm is much higher than the cation exchange membrane (CEM), showed that the aerobic reaction biocathode contributes to the accumulation of Planctomycetes. After a long run, found that indoor microbial contamination. Desalination will appear the main reason of microorganisms indoor pollution is desalination of organic compounds in the anode through the AEM into the desalted water desalination indoor pollution. In order to solve this problem, designed with a buffer chamber and four MDC, Increase of the proton exchange membrane (PMDC) and a cation exchange membrane (CMDC). Compared with three MDC, PMDC and CMDC in the voltage across the 1000 resistor under salt solution were decreased 33.8% and 37.4%. for the initial concentration of 35 g/L, within the first 240 h, PMDC 3 and MDC. is better than the desalination performance PMDC can effectively prevent the acetic acid and phosphate into salt water, transfer amount of acetate and total phosphorus in PMDC is 105.7 + 26.3 + 9.8 mg/L and 28.8 mg/L respectively, only 15.8% in MDC and 35.6%. using the technology of bio cathode MDC and membrane capacitance desalination, can be simulated seawater (Na concentration of 35 Cl g/L) the salt content is reduced to the standard of drinking water (250 mg/L chloride). But because the permeability of organic matter, still need follow-up treatment of desalinated water. Although there are many problems, but the MDC-MCDI technology makes the island far away from land and ships in It is possible to get fresh water without consumption of electricity.

【學(xué)位授予單位】：哈爾濱工業(yè)大學(xué)
【學(xué)位級(jí)別】：博士
【學(xué)位授予年份】：2015
【分類號(hào)】：P747

【參考文獻(xiàn)】

相關(guān)期刊論文 前4條

1 吳麗;陳曉;張秀云;于芳;;同步廢水處理及產(chǎn)電的微生物燃料電池研究進(jìn)展[J];廣州化工;2012年23期

2 姚森;何雅玲;謝濤;席奐;;微生物碳捕獲電池陰極室CO_2捕獲速率的計(jì)算[J];工程熱物理學(xué)報(bào);2012年12期

3 馮玉杰;王鑫;李賀;楊俏;曲有鵬;史昕欣;劉佳;何偉華;解明利;;基于微生物燃料電池技術(shù)的多元生物質(zhì)生物產(chǎn)電研究進(jìn)展[J];環(huán)境科學(xué);2010年10期

4 李琦;;海水淡化—沿海城市水資源可持續(xù)發(fā)展的重要策略[J];科學(xué)管理研究;2010年01期

相關(guān)博士學(xué)位論文 前1條

1 程浩毅;生物電化學(xué)系統(tǒng)定向還原硝基苯及能量循環(huán)補(bǔ)償模式研究[D];哈爾濱工業(yè)大學(xué);2013年

，

本文編號(hào)：1644280