• 제목/요약/키워드: Ammonia gas removal

검색결과 121건 처리시간 0.052초

암모니아 가스 제거용 개질 활성탄의 표면특성 (Surface Properties of Modified Activated Carbon for Ammonia Gas Removal)

  • 이성우;오길용;김리나;김대근
    • 한국대기환경학회지
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    • 제29권3호
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    • pp.317-324
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    • 2013
  • This research assessed the surface properties of modified activated carbons with three different acids and five different metals for ammonia gas removal. Raw bituminous coal-based activated carbon ($4{\times}8$ mesh) had low adsorption capacity of 0.72 mg $NH_3/g$ based on the analysis in the column adsorption experiment. Adsorption capacities of carbons modified with $CH_3COOH$, $H_3PO_4$, and $H_2SO_4$ increased up to 3.34, 21.00, and 35.21 mg $NH_3/g$, respectively. Those of carbons with Cu, Zn, Zr, Fe, and Sn were 9.63, 9.13, 7.09, 25.12 and 15.03 mg $NH_3/g$. Ammonia adsorption was enhanced by the presence of surface oxygen groups on carbon materials, which influenced pH of carbon surface. BET surface area of raw carbon was analyzed to be $1087m^2/g$, but it decreased by carbon surface modification. Fe-impregnated carbon showed $503.02m^2/g$ of surface area. These observations were mostly caused by chemical adsorption.

지렁이 분변토와 주정슬러지 혼합 배양액을 이용한 Biofilter에서의 고농도 악취제거 (Removal of High Odor Concentration with Biofilter using Mixture of Earthworm Cast and Distillery Sludge)

  • 박종웅;장석조
    • 한국환경보건학회지
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    • 제40권2호
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    • pp.127-136
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    • 2014
  • Objectives: This study was conducted to investigate the removal of high odor concentration from swine wastewater treatment facility by full scale biofilter using liquid with deodorant mixed with earthworm cast and distillery sludge. Methods: The supply of the culture liquid to the microorganism on the media in the biofilter increases the activity and growth of biomass. The experimental equipment was biofilter tower with treatment capacity of 90 m 3/min. The experimental conditions included gas flow of $60m^3/min$, retention time of 20 sec, and gas/liquid ratio of 67. Results: With changing season from winter to summer, the inlet odor concentration of ammonia increased from 2.5 ppm to 29 ppm, and of hydrogen sulfide from 21 ppm to 91 ppm, respectively. The odor treatment system with biofilter using the culture liquid was stable when the high loading rate increased and showed excellent removal grade with an average of 96.7% for ammonia, and an average of 93.7% for hydrogen sulfide. The pH and SCOD in the recirculating culture liquid near the bottom of the biofilter tower decreased with operation time, but its influence on the odor removal rate was negligible, because the organic matter (SCOD) was replaced by some culture liquid supplied 2-4 times per day. Conclusions: The biofilter using culture liquid could successfully remove high odor concentration which was generated from swine wastewater treatment facility.

돈분뇨로부터 발생하는 암모니아의 배출 특성 (Emission Characterization of Ammonia Produced from Swine Nightsoil)

  • 이은영;이소진
    • 한국미생물·생명공학회지
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    • 제38권3호
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    • pp.308-314
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    • 2010
  • 축산 악취물질인 암모니아가스를 대상으로 하여 환경개선제 사용시 자돈의 돈분뇨에서 발생되는 암모니아가스의 발생특성에 대한 연구를 수행하였다. 이 실험을 위하여 96 L의 부피를 가지는 아크릴 악취발생기를 제작하였다. 돈분으로부터 악취를 발생한지 한시간이 경과되면, 대략 평균 24.3ppmv의 암모니아가 발생되고, 범위는 16~40 ppmv였다. 실험결과 분무용 제제의 경우 분무 직후에 50~90%의 저감효과를 보였고, 1차 분무 시 지속성은 약 2일 정도로 나타났다. 천연탈취제의 지속성이 타 제품과 비교할 때 가장 우수하였다. 본 연구에서는 6구획의 실험구를 설정하였고, 5종류의 사료용 제제 첨가구와 일반 사료구에서 모두 항생제를 제외한 사료를 자돈에 급이하였다. 실험구엔 자돈($6.3{\pm}0.2\;kg$) 60마리를 대상으로 하여 각 구획당 10마리였으며, 총 35일간 실험이 진행되어 각 제제가 암모니아 방출에 미치는 영향을 일주일에 한번씩 살펴보았다. 사료용 제제를 급여한 자돈의 돈분에서의 암모니아 발생량은 일반사료만을 먹은 자돈의 돈분에서의 암모니아 발생량보다 낮았다. 사료용 제품중 효율이 우수한 제품은 7주 전 기간에 걸쳐 71~99%의 지속적 암모니아 저감효율을 보여주었으며, 일부 제품의 경우 초기 저감효율이 일시적이고 전기간에 걸쳐 전혀 암모니아 저감효율을 보여주지 않은 제품도 있었다.

갈대(Phragmites australls)수초를 적용한 바이오필터에서의 하수처리시설 악취저감기술 (Odor Reduction Technology in Sewage Treatment Facility Using Biofilter with Reed Grass(Phragmites australls))

  • 정진도;김규열
    • 상하수도학회지
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    • 제27권3호
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    • pp.373-382
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    • 2013
  • In this study, a biological odor treatment system was proposed to remove odor(foul smell) materials causing several problems in the closed sewage treatment plant. This odor treatment system was composed of a two-step biofilter system in one reactor. The two-step biofilter reactor was constructed with natural purification layer in upper part and artificial purification layer in lower part. The reed grasses of water purification plants were planted in the surface area and mixed porous ceramic media were filled with the lower part of biofilter reactor. By using the above experimental apparatus, the ammonia gas removal efficiency was attained to 98.3 % and the hydrogen sulfide gas removal efficiency was appeared more than 97.7 % which shows more effective than the conventional odor removal process.

종속영양세균과 독립영양세균을 고정화한 Polyurethane Biofilter의 돈분뇨 악취제거 (Removal of Malodorous Gases from Swine Manure by a Polyurethane Biofilter Inoculated with Heterotrophic and Autotrophic Bacteria.)

  • 이연옥;조춘구;류희욱;조경숙
    • 한국미생물·생명공학회지
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    • 제30권1호
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    • pp.91-97
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    • 2002
  • Removal of malodorous gases from swine manure by a polyurethane biofilter inoculated with heterotrophic and autotrophic bacteria was investigated. Ammonia, hydrogen sulfide and other gases could be efficiently treated at 3~3.6 second of empty bed retention time by the polyurethane biofilter. In the range of SV $200~l,200h^{-1}$ , the average removal efficiency of odor was about 89% when the odor unit of inlet gas was below 4100. Odor elimination capacity of the polyurethane biofilter was$ 1.8$\times$10^{5}$ $~5.0$\times$10^{7}$OUㆍm$^{-3}$$h^{-1}$ that were 84~90% of the inlet load. The critical loads of $NH_3$ and $H_2$S, which mean 97% removal with respect to the inlet loads, were 31 and $27 g.m^{-3}$$h^{-1}$ , respectively. The maximum elimination capacities of $NH_3$ and $H_2$S were 56 and $157 gㆍm^{-3}$ ㆍh$^{-1}$ , respectively. Although the removability for$ NH_3$ and $H_2$S was not influenced by $H_2$S$NH_3$ ratio (ppmv/ppmv), the $H_2$S removability was inhibited by high $H_2$S concentration more than 80 ppmv.

Recovery of ammonia from wastewater by liquid-liquid membrane contactor: A review

  • Jang, Yoonmi;Lee, Wooram;Park, Jaebeom;Choi, Yongju
    • Membrane and Water Treatment
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    • 제13권3호
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    • pp.147-166
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    • 2022
  • Liquid-liquid membrane contactor (LLMC), a device that exchanges dissolved gas molecules between the two sides of a hydrophobic membrane through membrane pores, can be employed to extract ammoniacal nitrogen from a feed solution, which is transported across the membrane and accumulated in a stripping solution. This LLMC process offers the promise of improving the sustainability of the global nitrogen cycle by cost-effectively recovering ammonia from wastewater. Despite recent technological advances in LLMC processes, a comprehensive review of their feasibility for ammonia recovery is rarely found in the literature. Our paper aims to close this knowledge gap, and in addition to analyze the challenges and provide potential solutions for improvement. We begin with discussions on the operational principles of the LLMC process for ammonia recovery and membrane types and membrane configurations commonly used in the process. We then assess the performance of the process by reviewing publications that demonstrate its practical application. Challenges involved in the implementation of the LLMC process, such as membrane fouling, membrane wetting, and chemical requirements, are presented, along with discussions on potential strategies to address each. These strategies, including membrane modification, hybrid process design, and process optimization based on cost-benefit analysis, guide the reader to identify key areas of future research and development.

금속 이온이 교환된 석탄 비산재 유래 합성 제올라이트 물질의 암모니아 흡착성능 평가 (Evaluation of Ammonia Adsorption Capacity Using Various Metal Ion-Exchanged Zeolitic Materials Synthesized from Coal Fly Ash )

  • 박종원;곽주영;이창한
    • 한국환경과학회지
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    • 제32권5호
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    • pp.343-353
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    • 2023
  • A zeolite material (ZCH) was synthesized from coal fly ash in an HD thermal power plant using a fusion/hydrothermal method. ZCH with high crystallinity could be synthesized at the NaOH/CFA ratio of 0.9. Ion-exchanged ZCH adsorbents for ammonia removal were prepared by ion-exchanging various cation (Cu2+, Co2+, Fe3+, and Mn2+) on the ZCH. They were used to evaluate the ammonia adsorption breakthrough curves and adsorption capacities. The ammonia adsorption capacities of the ZCH and ion-exchanged ZCHs were high in the order of Mn-ZCH > Cu-ZCH ≅ Co-ZCH > Fe-ZCH > ZCH according to NH3-TPD measurements. Mn-ZCH ion-exchanged with Mn has more Brønsted acid sites than other adsorbents. The ion-exchanged Cu2+, Co2+, Fe3+, or Mn2+ ions uniformly distributed on the surface or in the pores of the ZCH, and the number of acidic sites increased on the alumina sites to form the crystal structure of zeolite material. Therefore, when the ion-exchanged ZCH was used, the adsorption capacity for ammonia gas increased.

무창 비육돈사에서 습식공기정화기의 여름철 공기정화효율 분석 (An Air Cleaning Efficiencies of Wet Air Cleaner in the Windowless Swine Fattening Stall in Summer)

  • 오인환;이종현;이경훈;이정훈;이동섭;어성만;이미림
    • 한국축산시설환경학회지
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    • 제12권3호
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    • pp.133-140
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    • 2006
  • The climate of stall significantly influences on animal production ability. High concentration of ammonia gas, $CO_2$ and lots of dust are found in modern densely raising stall system, as results, they provide a negative influence on animal and farmer health, and production ability. Therefore, it is necessary to keep clean the inside air of stall to increase the productivity. An air cleaner of wet type, consisting of a fan, a motor, rotating discs, a dust collector, a water bowl, an ozone generator etc, has been developed to clean the stall air. The work principle is that the inside air is sucked through the fan, and the rotating discs make water into fineness spray and blow into the stall. The rest water flows down to the dust collector. In the present study, we measured the dust, ammonia gas, odor, temperature and humidity in a swine stall that were installed two wet air cleaners with 700 fattening swine with On-mode and Off-mode of wet air cleaners. The dust measure was divided into 3 categories, TSP, $PM_{10}$, and $PM_{2.5}$. In summer, the TSP in on-mode were maximum $0.259mg/m^3$ and minimum $0.128mg/m^3$, and the average was $0.195mg/m^3$. These are comparable to the data from Off-mode stall that maximum $0.308mg/m^3$, minimum $0.139mg/m^3$, and average $0.277mg/m^3$. However, $PM_{10}$ and $PM_{2.5}$ showed any significant differences between the tests. The concentrations of ammonia gas in Off-mode stall were maximum 13.8 ppm and minimum 5.9 ppm, and the average was 8.47 ppm. However in On-mode stall the ammonia gas concentrations were maximum 10.5 ppm and minimum 5.5 ppm, and the average was 7.63 ppm. The concentration of ammonia gas in On-mode was 10% in average lower than off-mode stall. Odor was measured by olfactometer. In the Off-mode stall, the odor unit were maximum 420 $Ou/m^3$ and minimum $300\;OU/m^3$, and the average was $367\;OU/m^3$, but in the On-mode stall the odor unit were maximum $330\;OU/m^3$ and minimum $210\;OU/m^3$, and the average was $253\;OU/m^3$. Odor removal efficiency was about 31% in On-mode stall.

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