• Title/Summary/Keyword: Adsorber

Search Result 48, Processing Time 0.028 seconds

A Study of HC Reduction with Hydrocarbon Adsorber Systems

  • Son, Geon-Seog;Yun, Seung-Won;Kim, Dae-Jung;Lee, Kwi-Young;Choi, Bung-Chul
    • Journal of Mechanical Science and Technology
    • /
    • v.14 no.10
    • /
    • pp.1168-1177
    • /
    • 2000
  • Hydrocarbon adsorber is considered as a promising technology to reduce cold start HCs in automotive exhaust gas. In this study, three in-line adsorber systems were tried to reduce the cold start emission. To check the basic characteristics of adsorber converters, surface areas, TPD and TP A were examined after a hydrothermal aging. Also idle engine bench was used to find the adsorption and desorption capabilities of the adsorber systems at cold start. Finally a practicability of the adsorber systems for the LEV achievement was checked with FTP test on a 2.0 D MIT vehicle. The results of this study indicate that hydrocarbon adsorber system is one of the promising passive technologies to meet the ULEV regulation.

  • PDF

Economical Evaluation Based on Method of Coagulation with GAC Adsorber Operation (활성탄 흡착지의 운영시 응집 방법에 따른 경제성 평가)

  • Hong, Seongho;Sung, Dae-Hyun
    • Journal of Korean Society of Water and Wastewater
    • /
    • v.19 no.4
    • /
    • pp.473-479
    • /
    • 2005
  • Applying enhanced coagulation is not uncommon not only to improve water quality but also to obtain economical advantages in water treatment. In this study, the economical evaluation was investigated with considering dosage of coagulant, produced sludges and usage of activated carbon with two different water sources. To simulate the granular activated carbon(GAC) adsorber mini-column test was adapted. Even if there were some variation according to the source waters, the life time of GAC was extended 60 to 110days with adding 2.5 to 3 times of coagulant in enhanced coagulation. With assumption of changing GAC adsorber at 50% of breakthrough the total treatment cost can be reduced to range from 25% to 44% with adapting the enhanced coagulation. The obtained value can not be generalized because the value can be varied by water quality and cost of the GAC or coagulant. However, the evaluation can be basis starting point to find optimum operation methods for the drinking water treatment which has plan to adapt GAC adsorber.

A Study on the Reduction of Cold Start Hydrocarbon from Gasoline Engines Using Hydrocarbon Adsorbers

  • Choi, Byung-Chul;Lee, Nam-Seog;Son, Geon-Seog
    • Journal of Mechanical Science and Technology
    • /
    • v.14 no.6
    • /
    • pp.699-703
    • /
    • 2000
  • Experiments were carried out to investigate the characteristics of the hydrocarbon (HC) emissions and to reduce cold start hydrocarbons in gasoline engines. An HC adsorber was, used and it coated was by Pd/Rh catalyst with zeolite on a honeycomb monolith. The HCs were efficiently trapped at temperatures below $100^{\circ}C by physical adsorption. After adsorption, they were reduced gradually by the catalytic oxidation of Pd/Rh catalysts as the adsorber temperature increased above $100^{\circ}C. Increasing amounts of methane, ethylene and n-butane were emitted as the fuel-air mixture became richer and the engine speed decreased. As the temperature of adsorber increased, high-number carbons into low-number carbons. Thus, the C4 concentration decreased significantly during the first 30 seconds, and the C2 concentration increased continuously.

  • PDF

A simple and rapid approach to modeling chromium breakthrough in fixed bed adsorber

  • Chu, Khim Hoong
    • Advances in environmental research
    • /
    • v.7 no.1
    • /
    • pp.29-37
    • /
    • 2018
  • A simple mathematical model for predicting fixed bed adsorption dynamics is described. The model is characterized by a linear adsorption isotherm and a linear driving force expression for mass transfer. Its analytic solution can be approximated with an algebraic equation in closed form which is easily evaluated by spreadsheet computation. To demonstrate one application of the fixed bed model, a previously published adsorption system is used as a case study in this work. The adsorption system examined here describes chromium breakthrough in a fixed bed adsorber packed with imidazole functionalized adsorbent particles and is characterized by a nonlinear adsorption isotherm. However, the equilibrium behavior of the fixed bed adsorber is in essence governed by a linear adsorption isotherm due to the use of a low influent chromium concentration. It is shown that chromium breakthrough is predicted reasonably well by the fixed bed model. The model's parameters can be easily extracted from independent batch experiments. The proposed modeling approach is very simple and rapid, and only Excel is used for computation.

Evaluation of Filter-Adsorber(F/A) Process for Removal of Disinfection By-products(DBPs) (소독부산물 제어를 위한 실공정 F/A 운영에 관한 고찰)

  • Kim, Seong-Su;Lee, Kyung-Hyuk;Lim, Jae-Lim;Chae, Seon-Ha;Kang, Byeong-Soo;Moon, Pil-Joong;Ahn, Hyo-Won
    • Journal of Korean Society of Environmental Engineers
    • /
    • v.27 no.10
    • /
    • pp.1035-1042
    • /
    • 2005
  • Granular Activated Carbon(GAC) is widely used in drinking water treatment. At S and B Water Treatment Plant, GAC is used in place of granular media in conventional rapid filters(GAC Filter-Adsorber) for removal of Disinfection By-products(DBPs). The primary focus of this study is on the performance of existing filter-adsorber, and their operation. It was found that F/A process removed turbidity as effective as sand system. The ratio of Hydrophobic DOM (HPO) and hydrophilic DOM (HPI) fraction in the raw water at S and B WTP was similar. Filter Adsorber presented earlier DOC breakthrough and steady state condition which was contributed by biodegradation during operation period. The removal efficiency of DBPs were used to evaluate the filter performance. The DBPs concentration of F/A treated water was below treatment goal level (THM < $80\;{\mu}g/L$, HAA < $60{\mu}g/L$). The removal efficiency of THM decreased rapidly during operation period. However, HAA were removed steadily regardless of the influent concentration of HAA. These results indicate that the removal of THM depend upon the adsorption mechanism while the removal of HAA depend upon biodegradation as well as adsorption. The decrease of adsorption capacity and characteristic value of GAC may be attributed to the effect of high organic loading, residual free chlorine, coagulants, manganese oxidants and frequently backwashing. This study has confirmed that Filter adsorber process can be considered as effective alternatives for the removal of DBPs, especially HAA.

Evaluation on Filter/Adsorber Granular Activated Carbon using in Advanced Drinking Water Treatment: Abrasion number, Floater, Water-soluble ash, and Adsorption characteristics (고도정수처리용 Filter/Adsorber Granular Activated Carbon 특성 평가: 마모지수, floater, water-soluble ash 및 흡착특성 평가)

  • Park, Byeong-Joo;Do, Si-Hyun;Kim, Tae-Yang;Hong, Seong-Ho
    • Journal of Korean Society of Water and Wastewater
    • /
    • v.30 no.1
    • /
    • pp.77-85
    • /
    • 2016
  • The characteristics of filter/adsorber granular activated carbon (F/A GAC) were investigated by measuring various parameters, which include surface area, pore volume, abrasion number, floater, and water-soluble ash. The correlation between parameters was also evaluated. Moreover, rapid small-scale column test (RSSCT) was conducted for adsorption characteristics. Thirteen F/A GAC were tested, and the average values of abrasion number and water-soluble ash were 88.9 and 0.15%, respectively. F/A GAC with the larger external surface area and greater mesopore volume had the lower abrasion number, which indicated that it was worn out relatively easily. Water-soluble ash of coconut-based GAC (about 2.6%) was greater than that of coal-based GAC (less than 1%), and the pH of solution was increased with GAC, which had the higher water-soluble ash. On the other hand, floater of thirteen F/A GAC was divided as two groups, which one group had relatively higher floater (2.7~3.5%) and the other group had lower floater (approximately 0.5%). The results of RSSCT indicated that coconut-based GAC (i.e. relatively higher water-soluble ash) had less adsorption capacity. Moreover, adsorption capacity of coal-based GAC with larger surface area and greater mesopore volume was superior to others.

Adsorption Characteristics of Reverse Stratified Tapered Adsorber (역층상 점증형 흡착탑에서의 흡착특성)

  • Lee, Seung-Mok;Kim, Dae-Hyun;Lee, II-Young
    • Journal of Korean Society of Environmental Engineers
    • /
    • v.22 no.10
    • /
    • pp.1861-1867
    • /
    • 2000
  • Granular activated carbon(GAC) adsorption is one of the best available technology to remove synthetic organic chemicals(SOCs) from water supplies and wastewater. In order to satisfy enviromental criteria and reduce GAC treatment cost, optimal study of reverse stratified tapered adsorber(RSTA) has been conducted. The RSTA was found to provide on increase in breakthrough time when compared to a conventional cylindrical adsorber(CA). Through the RSTA optimal experiment, optimal mean bed velocity was decided 19.10cm/min and optimal angle was decided RSTA($3.0^{\circ}$). Adsorption efficiency was increased with increasing activated carbon doses and the number of activated carbon layers.

  • PDF

Experimental Investigation on Small-scale Sorption Refrigerator (소형 흡착식 냉동기에 대한 실험적 연구)

  • 고준석;정상권
    • Korean Journal of Air-Conditioning and Refrigeration Engineering
    • /
    • v.15 no.4
    • /
    • pp.312-317
    • /
    • 2003
  • This paper describes an experimental study on small-scale sorption refrigerator. Silica gel (type A) as an adsorbent, HFC-l34a as a refrigerant were selected for a sorption refrigerator The focus of the design was to reduce the cycle time of the sorption refrigerator. Through the experiment, pressure and temperature variations in the adsorber were measured and the performance of refrigerator was predicted. In this paper, the small-scale sorption refrigerator operates with the cycle time of 4805. Its predicted cooling capacity is 25 W at -15$^{\circ}C$ and COP is 0.23.

Exhaust Emissions Reduction using Unburned Exhaust Gas Ignition Technology and Hydrocarbon Adsorber (미연 배기가스 점화 기술과 탄화수소 흡착기를 이용한 배기저감)

  • Kim, C.S.;Chun, J.Y.;Choi, J.W.;Kim, D.S.;Lee, Y.S.;Kim, I.T.;Ohm, I.Y.;Cho, Y.S.
    • Proceedings of the KSME Conference
    • /
    • 2000.11b
    • /
    • pp.150-155
    • /
    • 2000
  • Exhaust emissions from vehicles are the main source of air pollution. Many researchers are trying to find the way of reducing vehicle emissions, especially in the cold transient period of the FTP-75 test. In this study, UEGI (Unburned Exhaust Gas Ignition) technology, warming up the close-coupled catalytic converter (CCC) by igniting the unburned exhaust mixture using two glow plugs installed in the upstream of the catalyst, was developed. It was applied to an exhaust system with a hydrocarbon adsorber to ensure an effective reduction of HC emission during the cold start period. Results showed that the CCC reaches the light-off temperature (LOT) in a shorter time compared with the baseline exhaust system, and HC and CO emissions are reduced significantly during the cold start.

  • PDF