• Title/Summary/Keyword: Airflow rate

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Fire Suppression Effect of PPV with Water Mist System (미세물분무를 이용한 PPV의 화재진압효과)

  • Kim, Sung-Won;Shin, Chang-Sub
    • Journal of the Korean Society of Safety
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    • v.18 no.4
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    • pp.71-77
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    • 2003
  • To inject fresh air into a fire room, Positive Pressure Ventilation (PPV) can be used and the blower of PPV increases inside pressure of the room. It makes high flow rate of products of combustion, smoke and heat from the structure, and it is very helpful to fireman on the fire extinguishing work. The flame moves to the direction of airflow and the temperature of flame can be decreased rapidly. In this experiment, a water mist system is applied to PPV to increase the effectiveness, and various effective factors are studied. n-Heptane and pine wood stick were used as fuel. Temperatures at the above and behind the combustion pan were strongly reduced by the water mist system and by the convective cooling with airflow. The smoke density was also decreased by PPV with water mist system and it can be explained by the absorption of smoke particles on the water mist droplet and by the strong exhausting effects of mobile fan.

Gasification Characteristics of Rice Husks in Batch Operation (배치공정에서 왕겨가스화 특성)

  • Kim, Y.J.;Kang, Y.K.;Ryou, Y.S.;Kang, G.C.;Paek, Y.
    • Journal of Biosystems Engineering
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    • v.33 no.4
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    • pp.248-252
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    • 2008
  • An experiment was conducted in order to investigate gasification characteristics of rice husks in a fixed bed, which was a pre-step to design a continuous gasification system. Two air supply levels for gasification were chosen and their effects on the producer gas amount and producer gas composition were discussed. The main components of the producer gas were CO, $CO_2$, $O_2$, $H_2$ and THC (Total HydroCarbon). As airflow rate decreased, more producer gas was produced. The peak amount of CO, $H_2$ and THC were 28%, 7.5% and 0.68% in volume when constant airflow rate of $3.36\;m^3/s$ was used in the batch operation. About 4.5 kg of ash (9%) and condensed water including tars of 6 kg (11%) were produced from 50 kg rice husks in the gasification. Excluding the byproducts, all rice husks seemed to be transformed into producer gas. This gasification study was conducted prior to developing a continuous gasification system for biomass including agricultural byproducts.

Acoustic Analysis of Reinke Edema (라인케부종환자의 음성분석)

  • 김상균;최홍식;공석철;홍원표
    • Journal of the Korean Society of Laryngology, Phoniatrics and Logopedics
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    • v.7 no.1
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    • pp.11-19
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    • 1996
  • Reinke's edema is used for describing varying degrees of chronic swelling of the vocal folds. The acoustic analysis of Reinke's edema has not been reported so far in this country. The purpose of this study is to clarify acoustic and aerodynamic characteristics of the Reinke's edema. Several acoustic evaluations & aerodynamic studies were done in 20 Reinke's edema patients and the data was compared with those of 20 normal controls. Videolaryngoscopy also was done to classify the severity in grading. We used C-Speech, Doctor speech science, and Phonatory function analyser. In C-Speech, we compared jitter, shimmer, and SNR(signal to noise ratio) of normal and Rrinke's edema patient. In Doctor speech science, we compared NNE(Glottal noise energy), speech fundamental frequency, voice quality between two groups. And in phonatory function analyser for aerodynamic function test, we compared speech intensity, airflow rate, and expiratory pressure between two groups. In conclusion, Reinke's edema patients showed lower voice pitches than normal, additionally jitter, shimmer, SNR(signal to noise ratio), NNE(Glottal noise energy), airflow rate, and expiratory pressure may be meaningful parameters for diagnosis and prognosis for treatment.

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Optimization of photo-catalytic degradation of oil refinery wastewater using Box-Behnken design

  • Tetteh, Emmanuel Kweinor;Naidoo, Dushen Bisetty;Rathilal, Sudesh
    • Environmental Engineering Research
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    • v.24 no.4
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    • pp.711-717
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    • 2019
  • The application of advanced oxidation for the treatment of oil refinery wastewater under UV radiation by using nanoparticles of titanium dioxide was investigated. Synthetic wastewater prepared from phenol crystals; Power Glide SAE40 motor vehicle oil and water was used. Response surface methodology (RSM) based on the Box-Behnken design was employed to design the experimental runs, optimize and study the interaction effects of the operating parameters including catalyst concentration, run time and airflow rate to maximize the degradation of oil (SOG) and phenol. The analysis of variance and the response models developed were used to evaluate the data obtained at a 95% confidence level. The use of the RSM demonstrated the graphical relationship that exists between individual factors and their interactive effects on the response, as compared to the one factor at time approach. The obtained optimum conditions of photocatalytic degradation are the catalyst concentration of 2 g/L, the run time of 30 min and the airflow rate of 1.04 L/min. Under the optimum conditions, a 68% desirability performance was obtained, representing 81% and 66% of SOG and phenol degradability, respectively. Thus, the hydrocarbon oils were readily degradable, while the phenols were more resistant to photocatalytic degradation.

An Experiment on Verification of Multi-Gas Tracer Technique for Air Exchange Rate Between Rooms (실간환기량 측정을 위한 멀티추적가스법의 검증실험)

  • Han, Hwa-Taik;Cho, Seok-Hyo
    • Proceedings of the SAREK Conference
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    • 2007.11a
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    • pp.99-104
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    • 2007
  • Tracer gas technique is widely used to measure the ventilation rates and/or ventilation effectiveness of building spaces. However, the conventional method using a single tracer gas can measure only outdoor air change rates in a single zone. This paper deals with the multi-gas tracer technique to measure air exchange rates between rooms. Interzonal air movements are important to characterize overall ventilation performance of complicated multi-zone buildings. Experiments are conducted in a simple two-room model with known airflow rates using tracer gases of SF6 and R134a. The concentration decays of two tracer gases are measured after simultaneous injections in each room. The governing equations are derived from the continuity and the mass balance of each room. The data reduction procedure are developed to obtain the inter-room airflow rates using the governing matrix inversion, and various data manipulation methods are tested, such as data shift, interpolation, smoothing, and etc, to improve the estimate and interpretation of the results.

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The Aerodynamic Evaluation of Velopharyngeal Function after Uvulopalatopharyngoplasty (구개인두성형술 후 공기역학적 구개기능 평가)

  • Hong, Ki-Hwan;Lim, Hyun-Sil;Choi, Seung-Chul;Kim, Byum-Kyu;Lee, Sang-Heon;Kim, Hyun-Gi
    • Speech Sciences
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    • v.9 no.2
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    • pp.167-177
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    • 2002
  • Uvulopalatopharyngoplasty (UPPP) is one of the popular surgical procedure for snoring and sleep apnea syndrome. The main principle of this procedure is to reduce abundant velopharyngeal soft tissues resulting in a shortened soft palate, which may cause some alterations in speech sound. The purpose of this study is to evaluate the change of velopharyngeal function after UPPP in the view of aerodynamics. Thirty three patients who received uvulopalatopharyngoplasty for correcting snoring and sleep apnea were included in this study. The airflow, airflow rate and air pressure during the production of oral and nasal consonants were measured before surgery and 4 week and 8 week after surgery. The oral air flows and pressures for oral and nasal consonants were not changed after surgery. However, oral air pressure for nasal consonants were increased significantly after surgery. The nasal air flows for oral consonants were not changed after surgery, but for nasal consonants were decreased at 8 weeks after surgery. The nasal flow rate for oral and nasal consonants were increased at 8 weeks after surgery. The uvulopalatopharyngoplasty may result in affecting the aerodynamic air streams during speech production.

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Heat Exchanging Performance as Affected by Arrangement of Heat Exchanging Pipe (열회수장치의 열교환 파이프배치 형식별 열교환 성능)

  • 윤용철;강종국;서원명
    • Journal of Bio-Environment Control
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    • v.11 no.3
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    • pp.101-107
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    • 2002
  • This study was carried out to improve the performance of heat recovery device attached to exhaust gas flue connected to combustion chamber of greenhouse heating system. Three different units were prepared far the comparison of heat recovery performance; A-type is exactly the same with the typical one fabricated for previous study of analyzing heat recovery performance in greenhouse heating system, other two types (B-type and C-type) modified from the control unit are different in the aspects of airflow direction (U-turn airflow) and pipe arrangement. The results are summarized as follows ; 1. In the case of Type-A, when considering the initial cost and current electricity fee required for system operation, it was expected that one or two years at most would be enough to return the whole cost invested. 2. Type-B and Type-C, basically different with Type-A in the aspect of airflow pattern, are not sensitive to the change of blower capacity with higher than 25m$^3$.min$^{-1}$ . Therefore, heat recovery performance was not improved so significantly with the increment of blower capacity. This was assumed to be that air flow resistance in high air capacity reduced the heat exchange rate as well. Never the less, compared with control unit, resultant heat recovery rate of Type-B and Type-C was improved by about 5% and 13%, respectively 3. Desirable blower capacity of these heat recovery units experimented were expected to be about 25m$^3$.min$^{-1}$ , and at the proper blower capacity, U-turn airflow units showed better heat recovery performance than control unit. But, without regard to the type of heat recovery unit, it was recommended that comprehensive consideration of system's physical factors such as pipe arrangement density, unit pipe length and pipe thickness, etc., was required for the optimization of heat recovery system in the aspects of not only energy conservation but economic system design.

Effect of Step-aeration on Inorganic Particle Mixtures Filtration in a Submerged Hollow Fiber Microfiltration Membrane (침지식 중공사 정밀여과 분리막에서 무기혼합입자 여과에 대한 단계별 공기세정의 영향)

  • Choi, Youngkeun;Kim, Hyun-Chul;Noh, Soohong
    • Membrane Journal
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    • v.25 no.3
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    • pp.256-267
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    • 2015
  • The goal is to compare two different aeration strategies for a pilot scale operation of submerged microfiltration with respect to the minimization of membrane fouling. A constant aeration (65 L/min) was examined parallel with a step-wise increase in airflow rate (40 to 65 L/min). The airflow rate was stepped to a higher rate every 5 min and the step-aeration cycles were repeated at regular intervals of 15 min. The comparative filtration runs were conducted with synthetic water containing powdered activated carbon (~10 g/L) and/or kaolin (~20 g/L) at a constant flux of 80 LMH. The extent and mechanisms of fouling in the microfiltration were identified by determining hydraulic resistance to filtration and the fouling reversibility after cleaning. Results showed that the step-aeration effectively alleviated fouling in the microfiltration of synthetic water compared to when using constant aeration. A substantial decrease in fouling was achieved by combining with coagulation using aluminum salts regardless of the aeration strategies. The constant aeration resulted in increased pore blocking likely due to increased accumulation of particles on the surface of membrane.

Characteristics of particle mixing and detection of poor fluidization in a fluidized bed ash cooler (유동층 저회냉각기에서의 입자 혼합특성과 비유동 진단)

  • Kim, D.W.;Lee, J.M.;Kim, J.S.;Kim, J.J.
    • 한국연소학회:학술대회논문집
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    • 2005.10a
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    • pp.231-237
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    • 2005
  • Interruption of good fluidization in a fluidized bed ash cooler(FBAC) for discharging bed materials such as sand or coal ash particles from the CFB combustor is frequently happened because of agglomeration of the particles in the bed. This unstable operation may, in the worst case, result in an unscheduled boiler shut down. In this study, we examined the operation problems of the FBAC of Tonghae CFB boiler and studied and introduced the simple detection and solution techniques with analyzing the mixing property and the occurrence of defluidization in a simulated fluidized bed ash cooler system (0.5m-H x 0.5m-W x 1.0m-L). The bridge of the large particles at the bed surface could be observed, and this caused to form the defluidization area at the entrance of the FBAC. The defluidization was affected not only by airflow rates but also by the particles discharging rates as well as particle size distribution in the FBAC. The local defluidization could be detected by analysis of the accumulated standard deviation error at a given period of time. Also, the regulation of the overall or local airflow rate made clearing up the local defluidization possible.

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Cellulolytic Enzymes Production Cultivation Using Air Circulation Bioreactor

  • Seo, Jin-Ho;Song, Hyo-Jung;Kim, Seong-Jun
    • 한국생물공학회:학술대회논문집
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    • 2005.10a
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    • pp.232-237
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    • 2005
  • The cellulloytic enzymes, such as FPase and amylase, production by Trichoderma inhamatum KSJ1 using 10L air circulation bioreactor were tried. Physical properties of the employed bioreactor, mixing time, $k_{L}$ a were examined in airflow conditions of enzyme production cultures. Mixing time of distilled water at 0.6, 1.2, 1.8 vvm were 25, 21, 9 sec, respectively, and mandel's medium using rice straw and pulp as carbon sources were 31, 25, 15 sec. Mixing time decreased when airflow rate increased. $k_L$ a of distilled water at 0.6, 1.2, 1.8 vvm were measured -22.52, -29.31, -39.62, respectively, and the mandel's medium were -47.8, -18.5, -21.4. The $k_L$ a values was increased linearly as the air-flow rates increased. However the values in mandel's medium showed different results, especially at 0.6 vvm. Amylase and FPase activity at the 1.2 vvm was 3.39U/mL, 0.72U/mL in 5 days cultivation. and the activities at 0.6 vvm were 2.01U/mL, 0.39U/mL, respectively. The enzyme productivity at 1.2 vvm was higher than at 0.6 vvm, indicating that high oxygen tension is requested for the efficient enzyme production culture of T. inhamatum KSJ1.

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