• Journal of Korean Society of Environmental Engineers
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• v.22 no.6
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• pp.1139-1148
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• 2000

To treat and recycle a large quantity of converter slag. the milling properties of -14/ +24 mesh-sized slag has been considered. The optimal conditions in milling process were investigated for producing powder-type slag and the required consumption was derived for the economical grinding. The characteristics of milling processes were studied in the variation of the rotational speed, milling time, filling ratio of ball, and size and amount of feed. The grinding efficiency was also examined. The optimal rotational speed in this experimental condition was observed to be the value of 79% of critical speed. The extent of grinding was increased with increasing the grinding time. but the efficiency of milling was decreased with the time. 50% ball filling was shown to have the optimal grinding effect, and less amount and small-sized feed made the milling efficiency high. As the result, using Bond's equation, power required for efficient milling was considered and the highest value was observed in the condition of high grinding time and optimal rotational speed.

• Journal of Biosystems Engineering
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• v.9 no.2
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• pp.81-88
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• 1984

현재 축산농가에서 쉽게 구할 수 있는 곡류, 조사료 및 부산물을 활용하여 사료의 자급율을 높이는 것은 농가의 소득증대를 위하여 바람직한 일이다. 이러한 사료의 자급자족 체계를 위하여 소형이며 조작이 간편한 사료분쇄기가 요구된다. 따라서 농가에 많이 보급되어 있는 5~10 마력 (3.7-7.5 kw)의 동력경운기에 의하여 작동될 수 있는 소형 햄머타입의 사료분쇄기 시작기를 설계 제작하였다. 그리고 시작기의 성능을 분석하기 위하여 보리, 옥수수, 볏짚, 건초를 사료로 하여 시료의 공급율과 스크린의 구멍크기를 변화시켜가며 실험을 수행하였다. 이상과 같은 햄머 밀 시작기의 설계 및 성능시험을 통하여 얻어진 결과를 요약하면 다음과 같다. 1. 시작기의 평균분쇄능력은 보리의 경우 평균입자직경이 543 마이크론일 때 $82.7kg/kw{\cdot}h$였으며, 옥수수의 경우에는 평균입자직경이 408 마이크론일 때 $132.7kg/kw{\cdot}h$였다. 2. 최대 공급율로 분쇄할 때 소요동력은 보리의 경우 1.9kw, 옥수수의 경우 5.3kw, 볏짚의 경우 1.5kw, 건초의 경우 1.6kw을 필요로 하였으며, 5-10 마력(3.7-7.5kw)의 동력경운기로 개발된 햄머 밀을 작동함에는 별 문제가 없는 것으로 분석되었다. 3. 시작기로 시료를 분쇄할 때 곡류 분쇄는 물론 조사료 분쇄도 가능한 것으로 분석되었다. 4. 시작기에 의해 시료를 분쇄했을 때 분쇄물의 평균온도 상승폭은 $7.2-10.0^{\circ}C$였다. 이러한 온도는 분쇄물의 영양소 파괴및 저장상의 안정성을 고려할 때 안전한 범위의 온도상승으로 판단되었다. 5. 원료공급율과 스크린 구멍크기가 분쇄량과 분쇄정도에 5% 수준에서 유의성 있는 영향을 미쳤다.

• Proceedings of the Korean Society for Agricultural Machinery Conference
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• 2002.02a
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• pp.257-262
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• 2002

본 연구에서는 분쇄방법에 따른 감초 분쇄생성물의 특성을 분석한 결과는 다음과 같다. 1. Hammer mill의 경우 d$_{80}$=750$\mu\textrm{m}$로 중간미분쇄의 입도범위를 가지며 비표면적은 0.269m/g로 분석되었고, Pin mill의 경우 d$_{80}$=600$\mu\textrm{m}$로 Hammer mill보다 입자크기는 조금 작으나 중간미분쇄영역의 입도범위를 가지며 비표면적은 0.324m$^2$/g로 분석되었고, Turbo mill은 d$_{80}$=250$\mu\textrm{m}$와 비표면적은 0.370m$^2$/g로 입자의 크기가 가장 작아 다른 분쇄기보다 분쇄능이 가장 우수한 것으로 분석되었다. 2. Hammer mill의 분쇄메커니즘은 대부분 충격, 일부 전단과 마찰에 의해 분쇄가 행해지고, Pin mill은 핀 사이에서의 전단, 충격, 마찰에 의해 분쇄된다. 즉 충격과 마찰에 의한 분쇄는 전단력에 의한 분쇄메커니즘보다 분쇄 능이나 분쇄효율이 상대적으로 낮은 것을 알 수 있었으며 주로 전단력과 충격, 반발력에 의해 분쇄가 이루어지는 Turbo mill의 분쇄능 및 분쇄 효율이 우수함을 알 수 있었다. 본 연구에 의해서 감초와 같이 섬유질을 많이 함유하고 있는 원료를 분쇄할 경우 분쇄메커니즘이 전단력인 분쇄기가 가장 적합하고, 분쇄중 소요되는 동력 면에서도 기존 분쇄기보다 우수한 Turbo mill의 분쇄조건을 확립해야 한다고 사료된다. 사료된다.

• Korean Journal of Agricultural Science
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• v.10 no.2
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• pp.334-344
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• 1983

This study was conducted to investigate the variables affecting the performance of hammer mills by the theoretical and dimensional analysis, and evaluate the power requirements of hammer mills for farm use in Korea. From the theoretical analysis, 16 variables affecting the performance of hammer mills were defined. In order to develop the mathematical relationships among the variables, the dimensional analysis was made for power requirements and $12{\pi}$ parameters were obtained. For the evaluation of the power requirements of hammer mills, approximate rates of grinding for 1HP, 3HP, 5HP, 6HP, 8HP, and 10HP were analyzed. Then, the fineness of grinding recommendation and average feeding rate of grain for livestock which is native cattle, dairy cattle, beef cattle, swine, broilers, and layers, were estimated. Finally number of livestock feeding shelled corn and barley were estimated from the above for one hour's hammer mill operation having the various power requirements. From this study it is known that 5HP is considered as an enough power for feed grinding of any kinds of livestock of Korean farm, as far as the grinding capacity is concerned.

• Microbiology and Biotechnology Letters
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• v.17 no.4
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• pp.349-357
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• 1989

Uncooked starch can be effectively saccharified in an enzyme reaction system containing attrition-milling media. To develope the high efficiency bioattritor, an agitated bead type bioreactor was constructed, and its effectiveness was evaluated. The optimal operation condition of bioattritor was found to be 300 g glass bead/L, 200 rpm, standard type impeller for 220 g/L of uncooked corn starch. The torque under the various operational conditions were also measured. The interrelation-ship between energy consumption for agitation of attrition-milling media and enhanced extent of saccharification of uncooked starch was evaluated, Power consumption was measured to be around 1.53 watt/L under the optimal operation condition. The attrition coupled enzyme reaction system is identified to tie a very excellent energy saying process for saccharification of uncooked starch, and seems to have a bright prospect of industrial application.

• KSBB Journal
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• v.4 no.3
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• pp.215-220
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• 1989

To develop an attrition coupled enzyme reactor with high efficiency-low energy consumption for saccharification of insoluble biomass, a 5L horizontal paddle type bioreactor was constructed and its performance was evaluated. The optimal condition for saccharification of 50g $\alpha$ -cellulose/L was found to be 200rpm with 500g of 3mm glass bead. Especially, the horizontal paddle type bloreactor was very effective for saccharification of high concentration of insoluble cellulose, in which around 72% of $\alpha$ -cellulose was saccharified for 75g $\alpha$ -cellulose/L, and even up to 70% for 100g of $\alpha$ -cellulose/L after 24hours. Under the optimal condition, the power consumption was measured to be around 1.7watth/g. Horizontal paddle type bioreactor seems to have an appropriated structural feature for industrial scale operation and to be an effective and energy saving attrition coupled enzyme reactor.

• Proceedings of the Korean Society for Agricultural Machinery Conference
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• 2017.04a
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• pp.102-102
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• 2017

제주산 감귤생산량은 51만톤(2016년)으로 수확기에 장마 등과 같은 환경적 요인에 의해 결점과의 비율이 24.9% 정도이다. 결점과로 통칭되는 비상품과는 일부 대기업의 쥬스공장에서 수매하는 량을 제외한 대부분은 자체 농장에서 폐기처분되고 있어 많은 감귤 비상품과 처리에 많은 문제점이 노출되어 오고있다. 성주군에서는 결점과 및 비상품과가 시장에 출하되는 것을 방지하기 위하여 자체 수매하여 액비, 발효퇴비, 사료화 가공 등에 많은 비용을 투자하고 있다. 따라서 본 연구는 당도가 15 Brix에 달하는 고당도 감귤 및 참외의 비상품과를 효과적으로 착즙하여 감귤 착즙액은 생산농자재로 환원하고, 참외 착즙액은 참외조청용 원료로 사용하는 기술을 개발하고자 한다. 착즙장치는 PLATE형 스크류, 테퍼 스크류 하우징, 파쇄된 과즙을 마지막 단계인 압입하는 고깔부 및 동력을 공급하는 구동부로 구성하였다. 개발한 고액분리 착즙장치의 외형은 $W1,000{\times}L2,000{\times}H1,070$이고 사용동력은 0,75kw, 1/30 감속모터를 사용하였다. 일반적인 착즙장치는 1단 분쇄와 동일 원통형의 스크류 압착으로 고액분리를 위한 착즙이 이루어지기 때문에 처리량이 150kg/hr에 불과하지만 개발한 고액분리장치는 2차 분쇄와 원통형과 원추형의 스크류 압착 후 고액분리망을 통과하도록 하여 500kg/hr 이상을 착즙이 가능하도록 개발하였다. 따라서 농산물의 고액분리를 통한 농산물의 가공을 위한 연속 착즙 장치는 2단 분쇄와 원통형 및 원추형 압착 미세망을 이용한 고액분리 착즙기는 기존 착즙기에 비하여 처리량이 3배 이상 증가되었다는 것을 알 수 있었다. 기존 감귤 착즙기의 수율은 60%정도이나 개발 착즙기의 착즙 수율은 66.5%로 나타나 본 연구에서 개발한 착즙기의 수율이 기존 착즙기의 수율보다 약간 높게 나타났다. 기존 착즙기는 원료(농산물의 종류)의 종류나 전처리에 제한이 있어 전용으로 사용하는데 비해 본 연구에서 개발한 고액분리 착즙기는 원료의 종류나 전처리 상태에 관계없이 사용 가능함을 확인하였다.

• Korean Journal of Agricultural Science
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• v.12 no.1
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• pp.101-107
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• 1985

Since most farmers breeding livestocks in Korea is depended on imported feeds, the rate of self-supplying feeds is very important for a stable development of farmers. Therefore, it is considered necessary to increase the rate of self-supplying feeds. In this study, performance tests were carried out with barley and forage to find the design's parameters of hammer for a small size hammer mill which can be driven by 3.7-7.5 kW power tiller being used by most farmers. The revolution speed of hammer mill was 3000 rpm, widths of hammer were 20mm, 30mm, 40mm, and the levels of thickness of hammer were 2mm, 4mm and 6mm. Experimental materials used were barley and forage and screen openings for barley was 4.76mm, and 3.18mm for forage. The study results can be summarized as follows; 1. Results of grinding tests showed that particle sizes were 478-774 microns for barley and 350-434 microns for forage. They were decreased according to the increasing thickness and width of hammer. 2. Fineness modulus of grinded materials were 3.07-3.62 for barley and 2.69-2.93 for forage. They were inversely proportional to thickness and width of hammer. 3. The required power for grinding was 3.8-5.0 kW for barley and 0.9-1.4 kW for forage. The thickness of hammer was more important for less power requirement than width of hammer. 4. Grinding performance of a small size hammer mill was 99-170kg/kWh for barley and 11-21 kg/kWh for forage. The thickness of hammer was an important factor for grinding performance, and inversely proportional to grinding performance. For about 3.2 of fineness modulus, 4 mm thickness was the best, and an optimum width of hammer was 30mm for a small size hammer mill.

• KSBB Journal
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• v.4 no.2
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• pp.78-86
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• 1989

The effective saccharification of cellulosic biomass to glucose is the most critical step for the conversion of renwable biomass to alternative liquid fuel. The enzymatic hydrolysis of biomass can be significantly enhanced provide the attrition milling media is added during hydrolysis. The enhancing mechanism of hydrolysis reaction in an agitated bead system was investigated. An attrition-reactor (bioattritor) which installed specially designed torque measuring apparatus was developed, and the potimal saccharification conditions of bioattritor were determined. The relationship between the power consumption required for agitation of attrition-milling media and enhanced extent of hydrolysis of biomass was compared to evaluatic economic feasibility of the process.

• Korean Journal of Materials Research
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• v.17 no.10
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• pp.532-537
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• 2007

A series of wet grinding experiments have been carried out using a stirred ball mill to systematically investigate consideration of grinding characteristics. The particle size distribution and median diameter of the grinding consumption power for a given grinding time were considered. Also, the effect of grinding aids on particle size and grinding consumption energy defined as the summation of grinding power was investigated. The grinding aids had influence on the smaller products size and decrease grinding consumption energy because the function of grinding aids were to be attribute to the prevention of agglomeration and ball and grinding chamber wall coating of sample powder. The grinding process seemed to be controlled by the force of agglomeration of the ground products. It was demonstrated that the particle size and grinding consumption energy could be more decreased by the addition of grinding aids.