• 유기물자원화
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• 제16권3호
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• pp.29-37
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• 2008

본 연구는 연속적 연풍건조와 열분해 장치를 이용한 Full Scale 최적조건 하에서 하수슬러지 케익를 처분하는 방안을 제시하는데 목적이 있다. 본 연구는 P시 N하수처리장의 탈수슬러지 케익를 사용하였으며, 열풍건조와 열분해로의 연계 공정에서 운전조건은 건조온도가 $130{\sim}180^{\circ}C$와 열분해 장치의 온도는 $650{\sim}750^{\circ}C$의 조건에서 장치를 실행하였다. 열풍식 컨베이어식 열풍건조 온도는 $130{\sim}180^{\circ}C$. 부하량 600~750kg/h(W =79.5%)와 체류시간은 110~120분대에서 최적조건을 연구하였다. 연속적 로타리식 열분해공정의 온조조건은 $650{\sim}750^{\circ}C$, 유입부하량 100~158kg/h와 체류시간은 20~40분대에서 최적운전 조건을 평가하기 위해서 실험을 실행하였다. 하수슬러지 케익의 함수율은 78~80%의 조건에서 운전을 실행한 결과 내부수 세포벽 파괴로 인하여 최종적으로 1~3%범위 내까지 수분이 감소하는 것으로 나타났다. 본 연구에서 증발건조와 열분해의 연속공정에 발생되는 동역학적인 변화에 영향을 미치는 주요 매개 변수는 체류운전시간, 슬러지내 수분함량, 슬러지 고형물량, 컨베이어속도, 회전속도 등의 결과에 따라서 최적조건을 산출하였다.

• 대한설비공학회:학술대회논문집
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• 대한설비공학회 2007년도 하계학술발표대회 논문집
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• pp.74-74
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• 2007

• 한국정밀공학회:학술대회논문집
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• 한국정밀공학회 2010년도 추계학술대회 논문집
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• pp.261-262
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• 2010

• 한국기계가공학회지
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• 제21권9호
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• pp.35-41
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• 2022

The moisture content of many inorganic sludges is less than 70% during dewatering. Hence, a mono or piston pump cannot feed the sludge dryer. Thus, most inorganic sludge should be moved to a landfill or recycled directly without any reduction method. This development was invented to apply cyclone dryers using air and specially designed for the continuous injection of sludge sources by negative pressure and high air velocity for low moisture inorganic matter. Therefore, wastewater sludge and raw water treatment sludge discharged from various industrial fields might be settled by this development. The cyclone dryer was commercialized useful as moisture reduction equipment. This development was applied using a sludge injection system for sludge feeding and under the cooperation of ejector design computational fluid dynamics. Furthermore, this paper presented good ejector model results, blowing an airflow of 264 m³/min at an actual performance test.

• Journal of Advanced Marine Engineering and Technology
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• 제23권5호
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• pp.687-694
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• 1999

This study was conducted to develop new drying process for automatic control and marine engi-neering system. Air-water tests were carried out to investigate dryer performance. The dispersed flow in he dryer test apparatuses was also simulated by using a numerical code which solves the Dittus-Boelter equation for continuous liquid phase and the Reynolds equation of droplet motion for continuous liquid phase and the Reynolds equation of droplet motion for dispersed phase to predict droplet removal efficiency. Proper conditions for dehumidification were optimized by response ambient conditions. When the selected indexes were constrained in the range of 85-98% moisture content above $15^{\circ}$ and more than mass flow rates of moist air 750kg/h. The numerical results were compared with the experimental data pertaining to the removal effi-ciency at chamber stage and overall pressure drop along concentric tubes Good agreement was obtained as for the efficiency while relatively poor agreement was obtained for the relative humidity. The results also showed that the efficiency depended strongly on the relative humidity at the inlet condition which indicated the importance of estimating the heat exchanger length. Effects of some design parameters in both removal efficiency and breakthrough onset condition are discussed.

• 한국농업기계학회:학술대회논문집
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• 한국농업기계학회 1994년도 SIEMSTA94 농업과학 기계기술 심포지엄
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• pp.139-160
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• 1994

The-state-of-the-art of rice drying in the U.S.A. is presented. The U.S.A. is a minor producer but major exporter of rice. Head yield is its major criterion in evaluating rice quality . A decrease of 1 to 3 points in head yield can be expected to occur in a well-designed rice-drying system. Rice is dried on the farm in bins in the U.S. A., and n high-temperature continuous -flow dryers at the elevator level. Two relatively new rice-drying systems are discussed in some detail. : The top-bin/in -bin-counterflow bin-type on-farm dryer, and the concurrent-flow high-temperature elevator dryer.

• 생명과학회지
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• 제27권7호
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• pp.754-759
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• 2017

100 l scale 미세조류 배양 시스템은 LED 광을 기반으로 자체 제작하였으며 Nannochloropsis oculata를 f/2 medium에서 광도($100{\mu}mol/m^2/s$), 배양온도($20^{\circ}C{\pm}1^{\circ}C$), LD cycle (12 hr)으로 배양하였다. 그 결과 LED blue (475 nm)에서 $100{\mu}mol/m^2/s$의 광도, 24 mg/l의 nitrate 농도에서 100 l 대량배양 결과 최대 biomass인 1.07 g/l를 배양하였다. 이렇게 배양된 미세조류에서 유용물질을 추출의 위한 추출방법을 확보하고 나아가 산물의 추출, 농축 및 건조공정 기술을 최적화하고자 하였다. 추출은 물리적인 방법인 sonicator, homogenizer를 이용한 파쇄법과 화학적인 방법인 0.5M HCl 파쇄법을 이용한 결과 chlorophyll a, chlorophyll b, carotenoid 함량은 물리적인 파쇄법인 sonicator를 이용 시 1.6, 0.5, 0.3 mg/g cell, homogenizer 이용 시 1.0, 0.6, 0.2 mg/g cell로 측정되었다. 0.5M HCl의 화학적 파쇄법 이용 시 chlorophyll a, chlorophyll b 함량은 0.9, 0.8 mg/g cell으로 측정되었다. 파쇄시간당 추출되는 영양물질이 가장 높은 시간은 15 min 파쇄 시 3.6 mg/g cell로 측정되었으며 acetone, methanol, ethanol의 3가지 용매 중 acetone이 3.6 mg/g cell로 효과적이 용매로 측정되었다. 농축은 2종류의 연속원심분리장비(tubular type, disk type), 마이크로필터, 필터프레스 4종 장비를 이용하여 시험한 결과 마이크로필터, disk type 연속원심분리기, Tubular type 연속원심분리기의 경우 16.0, 1.1, 0.5 g/l의 순으로 시간당 수율을 확인하였다. 건조공정 최적화를 위하여 열풍건조기, 진공건조기, 분무건조기, 동결건조기 등의 4종 시생산설비를 이용해 미세조류의 시간당 회수율 분무건조기는 Dextrin 0.5 kg이 첨가되면 회수율이 80%이지만 순도가 떨어졌고 동결건조기 회수율은 60%로 측정되었다.

• 한국농업기계학회:학술대회논문집
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• 한국농업기계학회 1999년도 하계 학술대회 논문집
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• pp.301-306
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• 1999

현재까지 인삼건조에 관한 연구는 단편적이며 또한 열풍건조의 온도 조건에 따른 물리 화학적 품질 변화 등에 국한되고 있으며 최 등(1992)이 백삼과 태극삼의 평형함수율과 열풍 건조 방정식을 체계적으로 개발한 연구가 있었으나 건조 에너지와 품질의 관점에서 새로운 건조기의 개발 등에 관한 연구는 거의 없는 실정이다. (중략)

• 한국해양공학회:학술대회논문집
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• 한국해양공학회 2003년도 추계학술대회 논문집
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• pp.24-29
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• 2003

Deep sea water has cold temperature, abundant nutrients and minerals, and good water quality that is pathogen-free and stable. Compared with surface water, deep sea water contains more nutrition salt, such as nitrogen and phosphor. Moreover, if has the good balance of minerals. Because of the ability of the spray drying process to produce a free-flowing power considering of spherical particles with a well-defined size distribution and the rapid drying times for heat-sensitive material, spray drying is attractive for a wide range of applications spray drying is a unique unit operation in which powders are produced from a liquid feed in a single processing step. Key component of the process are atomizer, spray chamber. Design of spray chamber should be based on the atomizer type, the production rate, and the particle size required. Because of the complex processes taking place during spray drying, traditional design method are based on pilot-plant tests and empirical scale-up rules. Modern technique such as CFD have a role to play in design and troubleshooting.

• 한국농업기계학회:학술대회논문집
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• 한국농업기계학회 2000년도 THE THIRD INTERNATIONAL CONFERENCE ON AGRICULTURAL MACHINERY ENGINEERING. V.II
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• pp.413-422
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• 2000

Samples of banana were dried in a two-stage heat pump dryer capable of producing stepwise control of the inlet drying air temperature while keeping absolute humidity constant. Two stepwise air temperature profiles were tested. The incremental temperature step change in temperature of the drying air about the mean air temperature of 30 $^{\circ}C$ was 5 $^{\circ}C$. The total drying time for each temperature-time profile was about 300 minutes. The drying kinetics and color change of the products dried under these stepwise variation of the inlet air temperature were measured and compared with constant air temperature drying. The stepwise air temperature variation was found to yield better quality product in terms of color of the dried product. Further, it was found that by employing a step-down temperature profile, it was possible to reduce the drying time to reach the desired moisture content.