填料塔-微乳液增溶吸收法净化甲苯废气

利用甲苯可以和非离子表面活性剂及相应助表面活性剂水溶液形成微乳液,从而增大甲苯表观溶解度的特性,吸收净化甲苯废气。采用微乳液作为吸收剂的填料塔治理甲苯废气,探讨了吸收剂组成、表面活性剂种类及浓度、喷淋量、甲苯浓度负荷和助表面活性剂的加入及其种类对甲苯去除率的影响。结果表明,微乳液吸收处理甲苯废气具有显著的效果,最大去除率达41%;经过体系筛选采用Tween-20作为表面活性剂,此时最适喷淋量为40 L/h(液气比为1∶5),且随着甲苯浓度负荷的升高,甲苯去除率随之增加;添加助表面活性剂可以不同程度地提高甲苯的去除率,Tween-20/正丁胺/甲苯/水微乳体系为吸收甲苯的最佳体系,此时最高去除率可达65%。     

水溶性离子液体对甲苯的吸收效果及影响因素

选择3种水溶性离子液体(十二烷基咪唑氯盐(DDMIM Cl)、十二烷基咪唑硝酸盐(DDMIM NO_3)、十二烷基咪唑双氰胺盐(DDMIM DCA))作为研究对象寸模拟曱苯废气进行吸收实验,研究了吸收液的吸收性能、甲苯浓度、吸收液浓度、进气气速以及盐度等因素对吸收效果的影响以及加热蒸馏法对吸收液的再生与甲苯回收的可行性。结果表明:不同的离子液体对甲苯的吸收率不同J)DMIM DCA的吸收效果最好在质量分数为5%时,初始吸收率达到98%,饱和吸收量为53.39 mg·L~(-1),而DDMIM CKDDMIM NO_3对甲苯的初始吸收率在92%左右,饱和吸收量分别为33.60,37.01 mg·L~(-1);甲苯饱和吸收量与吸收液浓度、甲苯进气浓度呈正相关,与进气气速、含盐度呈负相关;传质系数与甲苯进气浓度、进气气速以及含盐度呈正相关,与吸收液浓度呈负相关;采用加热蒸馏法进行甲苯回收及吸收液再利用时用苯的回收效率达到85%~90%且甲苯的饱和吸收量随着重复利用次数的增加而基本保持不变。因此利用离子液体溶液处理甲苯废气理论上是可行的。     

几种有机废气吸收液对甲苯吸收效果的对比

采用自行设计的吸收装置,对比研究了国内外文献报道的几种有机废气吸收液(二乙基羟胺、聚乙二醇400、硅油、食用油、废机油、0#柴油)对模拟甲苯废气的吸收效果。结果表明,通过改变吸收液种类、废气中甲苯浓度等条件能够对甲苯废气吸收效果产生显著影响。随着吸收时间的延长,吸收液对甲苯的吸收率逐渐降低,直至达到动态饱和。随甲苯废气中甲苯浓度的增大,吸收液的有效吸收量减小,而饱和吸收量则增大。在相同实验条件下,二乙基羟胺对甲苯的有效吸收量与饱和吸收量均最大,其次是食用油、机油、0#柴油,而聚乙二醇与硅油吸收效果最差。本研究结果为合理选择甲苯废气的高效吸收液提供了理论依据。     

介质阻挡放电和水吸收联合降解挥发性有机化合物

依据介质阻挡放电(DBD)和溶液吸收处理气态污染物的原理,设计出一种DBD和水吸收联合降解挥发性有机化合物(VOCs)的实验装置.研究其对甲苯的降解效果.考察了放电电压、甲苯初始浓度、模拟废气流量对甲苯降解效果的影响.分析了DBD和水吸收的相互作用.结果表明.DBD和水吸收联合可以提高甲苯的降解率.在放电电压为15.9 kV时甲苯的降解率为81.5%.比单独放电时提高了13.3百分点;甲苯的降解率随着放电电压增大而升高,随着气体流量和甲苯初始浓度增大而降低.该技术可以作为放电等离子体前处理工艺,为高效处理上业废气提供参考.     

一种新型吸收剂吸收油气效果与影响因素分析

油气回收在倡导节约资源、保护环境的当今社会有着重要的意义。吸收法作为常见的油气回收手段,影响其吸收效果的关键因素之一是吸收剂的选用。分析了传统油气吸收剂的优缺点,在AbsFOV-97油气吸收剂基础上改进开发得到一种新型吸收剂,搭建了小试平台比较新型与传统吸收剂的吸收效果,并针对新型吸收剂,研究了影响吸收效果的因素,包括进塔油气浓度、吸收剂温度、吸收液喷淋量、进塔油气流量等,根据单因素小试实验设计了正交实验。结果表明,新型吸收剂回收率比改进前提高3.06%,进塔油气浓度为影响吸收效果的最大因素。     

鼓泡反应器中Na_2S对低浓度NO_x的吸收

实验研究了在鼓泡反应器中硫化钠溶液吸收低浓度NO_x的吸收特性,分析了NO_x、O_2、Na_2S和Na OH浓度对吸收过程的影响,以及被吸收NO2的形态。结果显示,Na2S浓度在15.8和47.5 mmol·L~(-1)时,气相中NO2浓度变化对吸收率影响不明显,但在0.30~3.25 mmol·L~(-1)时,NO2浓度变化对吸收率有较大影响。气相中的O2会加速吸收反应,但同时也引起吸收剂的额外消耗。当Na2S溶液中加入Na OH,浓度达到0.1%时,可强化NO_2的吸收。NO_x中NO含量增加会导致吸收率下降,即使有Na OH的条件下,也未观察到NOx氧化度为0.5时NO与NO2的协同吸收效应。Na2S溶液将被吸收的NO2一部分还原为N2,一部分还原为NO-2。     

碱性硫酸铝吸收与解吸二氧化硫的机理及性能

采用实验的方法研究了碱性硫酸铝溶液吸收和解吸SO_2机理,同时探讨了碱度20%、铝量20 g·L~(-1)的碱性硫酸铝溶液温度变化对SO_2吸收率的影响效果。结果表明,SO_2进入碱性硫酸铝溶液中首先发生的是与活性Al~(3+)的结合反应,当活性Al~(3+)消耗殆尽后,则进行与H_2O的结合反应;而在解吸过程中,首先是与H_2O结合的SO_2发生解吸反应,其后是与活性Al~(3+)结合的SO_2发生解吸反应。当吸收液温度低于50℃,且每升溶液中SO_2通入量不高于5 L时,其吸收率均能维持在95%以上。     

TEPA调控AMP-DGDE水溶液相变吸收CO2性能及机理

相变吸收剂在降低CO₂捕集能耗方面具有较大优势,但现有吸收剂普遍存在再生性能差的问题。基于2-氨基-2-甲基-1-丙醇(AMP)的吸收剂再生性能优异,但通常难以发生相变。利用四乙烯五胺(TEPA)作为相变调控剂引入AMP-二乙二醇二甲醚(DGDE)水溶液,构建了具有良好再生性能的新型相变吸收剂AMP-DGDE-TEPA。在最佳配比下,AMP-DGDE-TEPA的吸收负荷可达0.88 mol·mol-1,其中97.6%的CO₂富集于溶液下层,下层体积仅占总体积51%。经7次吸收-解吸循环,吸收剂的吸收负荷仍能保持0.63 mol·mol-1,再生效率为71.6%。13C核磁共振结果表明,AMP与CO₂反应生成易于分解的碳酸氢盐,因而吸收剂具有良好的再生性能;而TEPA的引入可使系统中生成稳定的质子化TEPA和氨基甲酸盐。质子化TEPA和氨基甲酸盐具有高极性,可打破吸收剂原有的均相状态,促使吸收剂发生液-液相变。相比于DGDE,H₂O和极性反应产物之间具有更强的相互作用力,这些物质聚集形成CO_...     

中空纤维膜吸收甲苯气体

采用疏水性聚偏氟乙烯(PDVF)中空纤维膜为气液接触膜,n-甲酰吗啉(NFM)水溶液为吸收剂,研究了膜吸收技术分离甲苯/空气混合气的性能。考察了进气气体浓度、气体停留时间、吸收液体积分数和吸收液流量等诸因素对分离性能的影响。研究结果表明,膜吸收技术可以有效地分离甲苯/空气混合气,甲苯去除率可达90%;提高NFM吸收液的浓度和流量可同时增加甲苯的去除效率η和总传质系数K;气体停留时间的减小导致η降低,K反而增大;进气甲苯浓度的增加导致η下降,同时降低总传质系数K。     

吸附联合低温等离子体法去除甲苯废气

对介质阻挡放电条件下产生的低温等离子体联合吸附去除低浓度甲苯废气进行了实验研究。考察了反应器内分别填充分子筛、陶瓷环和混合填料时,甲苯的吸附效果;比较了各种填充条件下,低温等离子体对甲苯的去除效果和副产物臭氧的产生量;并对填充混合填料时不同外加电压、不同操作条件下,吸附联合低温等离子体去除甲苯的过程进行系统的研究。结果表明,外加电压相同,混合填料对甲苯的去除率最高,大于97%,依次是分子筛、陶瓷环、无填充;同时混合填料的臭氧浓度小于其他填料;当电压为18 kV时,混合填料可获得较高的甲苯去除率,同时产生的臭氧副产物最少。     

Cyclodextrins: a new efficient absorbent to treat waste gas streams

Volatile Organic Compounds (VOCs) in the air provoke health and environmental concerns. This paper focuses on the absorption method to treat industrial polluted air loaded with VOCs. The key variable of this treatment being the choice of a suitable liquid absorbent, the aim of this research work is to investigate the effectiveness and the regeneration of a new potential family of absorbent: cyclodextrins (CDs). All CDs derivatives tested are able to decrease the Henry's law constant of toluene: a reduction of volatility up to 95% may be obtained, depending on CD nature and concentration. Moreover, absorption experiments show that beta-CD, which presents the highest absorption ability, is 250 time more efficient than water. The absorption efficiency is not totally correlated with static experiments, suggesting that, in addition to Henry's law constants and inclusion compounds stability, toluene diffusion into such solutions has to be taken into account. It is also to be noted that salt and pH variations seem to have little influence on the absorption capacity of CDs, which may be of great interest for industrial applications. Finally, since production of solid compounds was not observed during these experiments and since temperature decreases the capture ability in a drastic way, regeneration of the washing solution can be achieved by heating the solution in combination with air stripping.     

旋转填料床/柠檬酸盐法吸收-解吸SO2

提出采用旋转填料床结合柠檬酸盐法脱除烟气中SO2的方法,考察了旋转填料床转子转速、液气比、初始柠檬酸根浓度和初始pH值等因素对脱硫效率的影响。结果表明,采用超重力法超重机转子转速为1 000 r/min、液气比为7L/m3、初始柠檬酸根浓度为1.5 mol/L、吸收液的初始pH值为5.0,脱硫效率稳定在99%左右。研究了水蒸气汽提法解吸SO2时初始柠檬酸根浓度、初始pH值、SO2浓度、富液流量和水蒸气流量对解吸效率的影响,得出了影响SO2解吸率的基本规律,并进行了分析。通过实验证明该方法在技术上是可行的,具有良好的应用前景。     

硫酸铅在柠檬酸钠-酸体系中的浸出转化

硫酸铅可以在柠檬酸钠-乙酸体系中脱硫转化生成柠檬酸铅。考察了柠檬酸钠投加量、反应时间、固液比以及反应温度对PbSO4浸出转化的影响。实验结果表明，PbSO4的转化率随着柠檬酸钠投加量和反应时间的增加而增大，固液比和反应温度对浸出过程影响不大。溶液中溶解的铅含量随着柠檬酸钠投加量的增大而增大，其他条件对其影响不明显。最佳浸出工艺条件是：柠檬酸钠与PbSO。的物质的量之比为2：1，固液比为1／5～1／3，反应温度为25℃，反应时间为2h，此时PbSO4的转化率可达到99％左右，溶液中的铅含量为总铅的3．8％左右。PbSO4浸出得到[Pb，（C。H，O，），]·3H2O，它在350℃左右可完全分解，得到PbO／Pb粉末。     

超重力-磷酸钠法脱除低浓度SO2

为开发脱硫率高、成本低、可回收SO2的脱硫技术，以旋转填料床为吸收设备，磷酸钠溶液为吸收剂，系统开展了液气比L／G、转速N、气体中SO2浓度CSO2,in吸收剂磷酸浓度CL和初始pH等工艺参数和溶液再生循环次数对脱硫率叼影响的实验研究。结果表明，叩随L／G、N、CL和初始pH的增加而增大，且它们的值越低时，叩增加越明显；受G和CSO2,in影响较小。在适宜操作条件下，脱硫率达99％以上，出口SO2浓度低于100mg／m^3。磷酸钠溶液可再生循环使用，脱硫率稳定在99％以上。表明超重力-磷酸钠法脱硫技术在小的液气比下即可达到高的脱硫率，吸收剂循环使用，可实现低成本并达标治理SO2废气，且适用范围宽，具有良好的工业应用前景。     

Government Sponsored Air Pollution Research Relating to Agriculture

The absorption of hydrogen sulfide and methyl mercaptan by aqueous solutions of chlorine, sodium hydroxide, and chlorine plus sodium hydroxide was studied using a two-inch diameter absorption column packed with ¼ inch Intalox saddles. Absorption rates were noticeably affected by chemical reactions occurring in the aqueous chlorine and hydroxide media. These solutions were studied as a means of controlling sulfur-containing gas emissions from kraft paper mills. The absorption studies indicated that aqueous chlorine solutions at a pH above 12 were effective absorbents for hydrogen sulfide removal in absorption equipment designed to tolerate sulfur in suspension. The absorption of methyl mercaptan in aqueous chlorine solutions appeared to be impractical since dimethyl disulfide was apparently the only product formed and was stripped from the tower by the gas stream. Sodium hydroxide solution was an effective absorbent for both methyl mercaptan and hydrogen sulfide when hydroxide to sulfide or mercaptan feed ratios were greater than 1 or 1.8, respectively. The mercaptan absorption coefficient was approximately twice that for sulfide absorption.     

胶束强化超滤去除水中双酚A

采用截留分子量(MWCO)为5000 Dalton、1000 Dalton的聚砜超滤膜,MWCO为1 kDa的再生纤维素超滤膜;采用十二烷基苯磺酸钠(SDBS)、曲拉通100(TritonX-100)、吐温80(Tween-80)、烷基多苷(APG)为表面活性剂,用胶团强化超滤工艺去除水中双酚A。研究了不同材质和截留分子量的超滤膜、表面活性剂浓度、膜操作压力、溶液pH和溶液中电解质等因素对该工艺的影响。结果表明,SDBS对双酚A有较好的去除效果,去除率在80%以上。在H+和Na+存在的条件下,双酚A的截留率增加,透过液中SDBS浓度降低。SDBS与非离子表面活性剂的复配可以提高双酚A截留率,降低透过液中SDBS的浓度,复配效果优劣顺序为Tween-80TritonX-100APG。     

Modulation of metabolic activity prevents degradation of sorbed toluene

The factors affecting the ability of a bacterial species to degrade different amounts of toluene (8.5 to 217 mg/g) sorbed to granular activated carbon (GAC), in an aqueous solution of mineral salts, were investigated. After 144 days the amounts of toluene remaining on one type of GAC ranged from 7.5 to 9.5 mg/g, and the aqueous concentrations of toluene ranged from 2 to 7 micrograms/L. Neither bacterial death nor an inhibition by accumulating by-products could explain why the remaining toluene had not been degraded. However, at these low concentrations of toluene, and probably because of cell starvation, bacteria were observed to be more than 100-times less efficient to degrade toluene than at high concentrations. We propose that this low degradation ability is responsible for the presence of residual toluene on the GAC, and that this mechanism may contribute to the persistence of low concentrations of sorbed pollutants in the environment.     

木屑处置漏油事故的室内模拟

用锯木屑作为吸附材料，0#柴油为吸附对象进行室内模拟实验，研究了木屑对纯油、水中浮油的吸附以及吸油后的木屑在水中的漂浮性能；并以木屑粒径、木屑投加量、振荡频率、油膜厚度为研究指标，设计了5因素4水平的正交实验，考察了各因素对0#柴油的吸附量、去除率以及木屑漂浮率的影响并对优化条件进行了讨论。结果表明，在实验研究范围内，木屑对水中柴油的吸附速度极快，1min即可达到饱和，饱和吸附量为8．08g／g；木屑在水中漂浮性能良好，静态时经72h漂浮，漂浮率维持在92％左右；振荡频率为150r／min时，72h内漂浮率维持在68％以上；最佳吸油条件组合为吸附剂粒径10～20目，振荡频率120r／min，木屑投加量0．7g，油膜厚度1．65mm。     

Removal of xylenol orange from its aqueous solution using SDS self-microemulsifying systems: optimization by Box–Behnken statistical design

The aim of present study was to develop and evaluate sodium dodecyl sulfate (SDS) self-microemulsifying systems (SMES) for the removal of an anionic dye xylenol orange (XO) from its bulk aqueous media via liquid–liquid adsorption. The composition of SDS SMES was optimized by Box–Behnken statistical design for the maximum removal of XO from its aqueous solution. Various SDS formulations were prepared by spontaneous emulsification method and characterized for thermodynamic stability, self-microemulsification efficiency, droplet size, and viscosity. Adsorption studies were conducted at 8, 16, and 24 h by mixing small amounts of SDS formulations with relatively large amounts of bulk aqueous solution of XO. Droplet size and viscosity of SDS formulations were significantly influenced by oil phase concentration (triacetin), while surfactant concentration had little impact on droplet size and viscosity. However, the percentage of removal of XO was influenced by triacetin concentration, surfactant concentration, and adsorption time. Based on lowest droplet size (35.97 nm), lowest viscosity (29.62 cp), and highest percentage of removal efficiency (89.77 %), formulation F₁₄, containing 2 % w/w of triacetin and 40 % w/w of surfactant mixture (20 % w/w of SDS and 20 % w/w of polyethylene glycol 400), was selected as an optimized formulation for the removal of XO from its bulk aqueous media after 16 h. These results indicated that SDS SMES could be suitable alternates of solid–liquid adsorption for the removal of toxic dyes such as XO from its aqueous solution through liquid–liquid adsorption.