• 한국환경농학회지
• /
• 제28권1호
• /
• pp.15-19
• /
• 2009

대기중으로 휘산되는 대부분의 암모니아는 농경지에서 시용하는 가축분뇨 퇴비와 질소비료에서 유래한다. 본 연구는 밭 토양에서 돈분 퇴비 시용방법에 따른 암모니아 휘산량을 소형원드터널 방법을 이용해서 정량적으로 평가하였다. 돈분 퇴비(20 Mg/ha) 표층살포(SA), 표층살포 후 즉시 경운(IRA), 표층 살포 3일 후 경운(RA-3d) 처리의 13일 동안 암모니아 휘산량은 각각 28.7, 8.7, 24.3 kg N/ha로 IRA 처리구는 SA 처리구에 비해 70% 저감효과를 가져왔다. 그리고 SA 처리구의 퇴비 처리 후 24시간 이내 휘산된 암모니아 양은 총 휘산량의 61%로 대부분의 암모니아는 시용 초기 짧은 시간 내에 휘산됨을 알 수 있었다. 석회와 퇴비 혼용시용 후 교반(L+C mix), 퇴비표층 살포 3일후 석회시용 교반(C+L3D), 석회시용 3일 후 퇴비시용 교반(L+C3D) 처리구의 22일 동안 총 암모니아 휘산량은 각각 40.1, 31.4, 27.7 kg/ha이었다. 따라서 가축분 퇴비 시용시 석회를 혼용하는 것은 피해야 하며, 만일 동일 작기내 시용이 불가피할 경우는 퇴비시용에 앞서 석회를 먼저 충분한 일수를 앞두고 시용하는 것이 암모니아 휘산량을 저감시킬 수 있다는 결론을 얻었다.

• 한국수산과학회지
• /
• 제42권4호
• /
• pp.373-379
• /
• 2009

This study investigated oxygen consumption rate (OCR), $Q_{10}$ coefficient and ammonia excretion rate of the greenling, Hexagrammos otakii Jordan et Starks with the average body weight of 250 g in a semi-recirculated respiratory measuring system. The experiment was done under three different water temperatures (10, 15, $20^{\circ}C$) and five different ambient ammonia concentrations (0, 2.5, 5, 10, 20 mg/L). As the water temperature and ambient ammonia concentration increased the OCR has significantly increased (P<0.05). Given experimental conditions, the OCR of greenling were $50.8{\sim}159.4\;mg\;O_2\;kg^{-1}\;hr^{-1}$ and the relationship of water temperature (T) and ambient ammonia concentration (C) on the OCR were following: OCR = 41.3 - 1.87T - 7.38C + $0.463T^2$ + $0.66lC^2$ + 0.642TC - $0.011T^3$ - $0.010C^2$ - $0.031TC^2$ - $0.001T^2$C ($r^2$= 0.9226). $Q_{10}$ coefficients were $1.88{\sim}3.50$ for $10^{\circ}C$ to $15^{\circ}C$, $1.03{\sim}2.73$ for $15^{\circ}C$ to $20^{\circ}C$ and $1.40{\sim}1.90$ for $10^{\circ}C$ to $20^{\circ}C$, respectively. In general, the ammonia excretion rate tended to increase with increasing of the water temperature within normal ambient ammonia concentration. However, interestingly, it was observed that ammonia was absorbed rather than excreted above the ambient ammonia concentration of $2.5\;mg\;L^{-1}$, regardless of the water temperature. Thus, the largest ammonia absorption rate (AAR) was obserbed at the level of $98.4\;mg\;TAN\;kg^{-1}\;hr^{-1}$. The relationship ambient ammonia concentration (C) on AAR was following: Y = 1.61 + $10.9X^{0.7}$ ($r^2$ = 0.889).

• 미생물학회지
• /
• 제26권3호
• /
• pp.215-222
• /
• 1988

광합성 세균인 Rhodopsedomonas sphaeroides의 질소 고정 효소 활성에 미치는 암모니아와 glutamine의 영향을 조사하였다. 그 결과 RP. sphaeroides의 질소 고정 효소 활성은 암모니아와 glutamine에 의해 저해를 받았으며, 이들의 저해는 암모니아와 glutamine이 다 사용된 후에는 질소 고정 효소의 활성이 되살아나는 가역적인 반응이었다. glutamine synthetase의 활성을 비가역적으로 저해하는 methionine sulfoximine (MSX)를 사용하여 암모니아와 glutamine이 직접 질소 고정 효소의 활성을 저해하는지를 일아보았다. 암모니아에 의한 질소 고정 효소의 switch-off에 미치는 MSX의 영향은 균의 배양 시기에 의존함을 알 수 있었다 . 12시간 배양한 경우, $500{\mu}M$ NH,Cl에 의해 질소 고정 효소는 저해를 받았으며, $500{\mu}M$의 MSX를 주가로 처리하였을 경우, GS는 21% 저해를 받았으며, 이때 유리된 암모니아의 량은 감소하였고, 질소 고정 효소의 활성은 회복되지 않았다. 그러나 20시간 배양한 경우, $500{\mu}M$ NH,CI을 처리한 후 $100{\mu}M$ MSX플 첨가하면, GS의 활성은 완전히 저해되고, 유리된 암모니아의 량은 약간 증가하였으나 질소 고정 효소의 활성의 저해는 MSX에 의해 회복되었다. 따라서 Rp. sphaeroides의 경우, in vivo 상태에서 암모니아에 의한 질소 고정 효소의 활성 저해는 암모니아 자체에 의한 것이 아니라 암모니아 동화산물에 의한 것임을 알 수 있었다.

• Korean Chemical Engineering Research
• /
• 제43권3호
• /
• pp.352-359
• /
• 2005

본 논문에서는 암모니아의 전해 분해를 위한 분리막 반응기의 음극방 및 양극방에서 물의 전해에 따른 암모니아 용액의 pH 변화가 고찰되었으며, 단위 전해 셀이 적층된 다단 전해 반응기에서의 암모니아의 연속식 분해 특성이 평가되었다. 분리막을 가지는 반응기에서 암모니아 용액의 전해 반응 시, 양극에서는 pH가 8 이하에서부터 수소 이온이 생성되는 물 분해 반응이 일어나며, 음극에서는 pH가 11 이상에서부터 수산기 이온이 생성되는 물 분해 반응이 일어나 암모니아 용액의 pH를 변화시켜 암모니아 전해 분해에 영향을 크게 미쳤으며, 음이온 교환막을 사용하는 경우가 양이온 교환막을 사용하는 경우보다 양극방에서 암모니아 분해에 유리한 알카리 분위기를 보다 효과적으로 유지할 수 있었다. 분리막 전해 반응기의 특성을 이용하여 자체 pH 조정 기능을 가지는 연속식 암모니아 전해 반응기가 새롭게 고안하였고, 여기서는 pH-조정조 탱크 용액을 두고 이의 용액 일부를 음극방으로 순환시킴으로써, 양극방으로 주입되는 pH-조정조의 용액의 pH를 높여 암모니아 분해율을 높일 수 있었다. 또한, 그러한 반응기를 이용한 salt-free 연속식 암모니아 전해 분해 공정이 제시되었으며, 이러한 공정에서는 염소 이온을 가지는 암모니아 용액의 80％까지 연속적으로 암모니아를 환경에 무해한 질소로 분해 시킬 수 있었다.

• 한국환경농학회지
• /
• 제40권4호
• /
• pp.366-372
• /
• 2021

BACKGROUND: Ammonia is known as a precursor to fine particulate matter, and according to CAPSS, annual ammonia emissions in the agricultural sector were 249,777 tons as of 2018, accounting for about 79.0% of Korea's total ammonia emissions. In particular, ammonia emissions from agricultural land increased by 19,566 tons (10.2%) compared to the previous year. The Ministry of Environment is setting emission statistics using the ammonia emission coefficient developed in Korea in 2008, but researchers in the agricultural field regard it as a coefficient that does not reflect the reality of Korea's agricultural environment. Accordingly, in order to develop ammonia emission coefficients from the cultivation of apples and pears, Korea's representative fruit type, test agricultural land was set in Iksan, Jeollabuk-do. METHODS AND RESULTS: This study attempted to obtain the ammonia emission coefficient by the treatment of the composite fertilizer (N-P₂O₅-K₂O=12-7-9), and the flux was measured using a dynamic flow-through chamber method. As for the chamber, a total of 12 chambers were installed repeatedly in 4 zones and used to develop emission coefficients. Using compound fertilizers during fruit tree cultivation, the ammonia emission coefficient was evaluated as 10.4 kg NH3/ton for pears and 15.3 kg NH₃/ton for apples. The reason why the ammonia emission coefficient according to the use of composite fertilizers was calculated higher for apple cultivation is believed to be due to the relatively high pH concentration of apple orchard soil. CONCLUSION(S): This study may provide basic data for upgrading the ammonia emission coefficient when using composite fertilizers in agricultural land. In the future, it might be necessary to upgrade the calculation of emissions through the development of ammonia and fine particulate matter emission coefficients considering the agricultural environment of Korea.

• 한국환경농학회지
• /
• 제41권4호
• /
• pp.230-235
• /
• 2022

BACKGROUND: Ammonia gas emitted from nitrogen fertilizers applied in agricultural land is an environmental pollutant that catalyzes the formation of fine particulate matter (PM2.5). A significant portion (12-18%) of nitrogen fertilizer input for crop cultivation is emitted to the atmosphere as ammonia gas, a loss form of nitrogen fertilizer in agricultural land. The widely practiced method for fertilizer use in agricultural fields involves spraying the fertilizers on the surface of farmlands and mixing those with the soils through such means as rotary work. To test the potential reduction of ammonia emission by nitrogen fertilizers from the soil surface, we have added N, P, and K at 2 g each to the glass greenhouse soil, and the ammonia emission was analyzed. METHODS AND RESULTS: The treatment consisted of non-fertilization, surface spray (conventional fertilization), and soil depth spray at 10, 15, 20, 25, and 30 cm. Ammonia was collected using a self-manufactured vertical wind tunnel chamber, and it was quantified by the indophenol-blue method. As a result of analyzing ammonia emission after fertilizer treatments by soil depth, ammonia was emitted by the surface spray treatment immediately after spraying the fertilizer in the paddy soil, with no ammonia emission occurring at a soil depth of 10 cm to 30 cm. In the upland soil, ammonia was emitted by the surface spray treatment after 2 days of treatment, and there was no ammonia emission at a soil depth of 15 cm to 30 cm. Lettuce and Chinese cabbage treated with fertilizer at depths of 20 cm and 30 cm showed increases of fresh weight and nutrient and potassium contents. CONCLUSION(S): In conclusion, rather than the current fertilization method of spraying and mixing the fertilizers on the soil surface, deep placement of the nitrogen fertilizer in the soil at 10 cm or more in paddy fields and 15 cm or more in upland fields was considered as a better fertilization method to reduce ammonia emission.

• 대한수의학회지
• /
• 제30권1호
• /
• pp.103-106
• /
• 1990

Effects of ammonia water on the spornlation of coccidial oocysts collected from bovine feces were studied with particular reference to the various levels of ammonia water (1% to 10%) for 30 minute conservation at room temperature. The sporulation rates showed a negative linear coorelation according to the treatment leavels of ammonia water, 85.3% at 1% level to 8.9% at 10% level. The optimum level of ammonia concentration was regarded as 5% to 10% with more than 80% of sporulation inhibition effect.

• KSBB Journal
• /
• 제16권3호
• /
• pp.314-319
• /
• 2001

A nitrifier consortium immobilized in polyvinyl alcohol was used to remove ammonia nitrogen from synthetic wastewater in an airlift bioreactor. The minimum aeration rates were 0.4, 0.6, 0.8 and 1.0 vvm for 5, 10, 15 and 20% immobilized bead packing volume fraction, respectively. The efficient packing fraction and the aeration rate for ammonia nitrogen removal were 15% and 2.4 vvm, respectively. With a hydraulic retention time of 0.5hr, the removal rate and the efficiency of ammonia nitrogen removal were 1685 g/㎥$.$day and 48% at an influent ammonia nitrogen concentration of 75 g/㎥.

• 한국환경과학회지
• /
• 제8권4호
• /
• pp.479-483
• /
• 1999

Nitrifier consortium immobilized in polyvinyl alcohol was used for the removal of ammonia nitrogen from synthetic aquaculture water in the airlift bioreactor. At the aeration rate fo 0.15 vvm and bead packing volume fraction of 20%, airlift bioreactor was operated effectively for a removal of ammonia nitrogen and for a stability of operation. Ammonia nitrogen removal rate by airlift bioreactor was continuously increased with decreasing hydraulic residence time. At the HRT(hydraulic residence time) of 0.3 hour, ammonia nitrogen removal rate was 84.3 g/$m^3$.d and the highest ammonia nitrogen removal rate was 130.8 g/$m^3$.d when HRT was 0.1 hour.

• 한국생물공학회:학술대회논문집
• /
• 한국생물공학회 2000년도 추계학술발표대회 및 bio-venture fair
• /
• pp.475-478
• /
• 2000

For an integrated nitrification-denitrification process, nitrite formation in the aerobic stage leads to big savings. Dissolved oxygen concentration, temperature, pH and free ammonia concentration have been meet for nitrite accumulation. Also their effects over the ammonia oxidizers and nitrite oxidizers have been studied. Dissolved oxygen limitation and free ammonia inhibition led to slow nitrification and nitrite build up. In this study batch kinetics of ammonium and nitrite oxidations were performed with free ammonia accumulated nitrifiers. From the results it is likely the nitrite oxidizers are inhibited by oxygen limitation rather than free ammonia.