• 펄프종이기술
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• 제43권2호
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• pp.1-8
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• 2011

The presence of high silica in bamboo hinders the use of this material for production of rayon grade pulp. Research has been carried out to overcome this deficiency and improve quality of rayon grade pulp with the modification in pulping and bleaching process. Effect of acid boosted water prehydrolysis, sulphuric acid pre-treatment of unbleached pulp, chlorination stage at lower pH and treatment of bleached pulp with $SO_2$ water were evaluated. Acid boosted water prehydrolysis of chips reduces prehydrolysis time by 50 minutes as compared to water prehydrolysis. Treatment of unbleached pulp with sulphuric acid reduces ash, acid insoluble, silica, calcium and iron contents of the pulp by 56, 31, 82, 84 and 60% respectively. The addition of acid, increase in kappa factor in $C_D$ stage and combination of both were effective in removing silica in the pulp. Treatment of final bleached pulp with $SO_2$ water removes silica to a great extent and improves optical properties of the pulp as compared to $H_2SO_4$ or PAA. Pretreatment of the pulp with acid and modification in the bleaching process can reduce silica substantially and improve the quality of rayon grade bamboo pulp.

• 한국산림과학회지
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• 제98권3호
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• pp.305-310
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• 2009

백합나무를 원료로 바이오 에탄올을 생산하기 위하여 알칼리 가수분해 처리 후 잔재물을 상업용 혼합 셀룰라아제(Celluclast 1.5L과 Novozym 342)를 사용하여 효소당화 후, 발효하여 바이오 에탄올을 생산하였다. 알칼리 가수분해 후 51.1%의 목재 성분이 회수 되었으며, 이중 셀룰로오스가 82.2%, xylan이 17.6%와 리그닌 2.0%의 조성을 보였다. 백합나무의 알칼리 가수분해과정에서 셀룰로오스 96.9%, xylan 38.0%, 리그닌 5.7%가 잔류하였다. 알칼리 가수분해 잔류물을 상업용 혼합 셀룰라아제에 의한 효소 당화결과, 셀룰로오스의 glucose 전환율은 87.0%였으며 xylan의 xylose로의 전환율은 87.2%였다. 분해된 단당류를 발효효모를 사용하여 바이오 에탄올을 생산하였는데 Saccharomycess cerevisiae 균주는 대부분의 glucose를 발효에 사용하였고, 0.4-1.4%의 소량의 glucose만을 잔류 시킨데 대하여, xylose의 경우는 92.1-99.5%가 잔류하여 이 균주는 발효과정에서 xylose를 거의 사용하지 않았다. 24시간 발효에서 에탄올의 농도는 57.2 g/L수준이었지만 발효 균주에 의한 에탄올 소비로 인하여 48시간 및 72시간 발효에서 에탄올 농도가 각각 56.2 g/L와 54.3 g/L로 점차 감소하였다.

• 한국세라믹학회지
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• 제30권12호
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• pp.987-992
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• 1993

In order to synthesize the heat resistance ceramics of LAS system, we studied on preparing the fine powder with homogeneity by sol-gel method using metal alkoxide. Various results were obtained depending on the composition and process. When the amount of H2O added at initial stage is higher than 10mol/$\ell$, and when the amount of catalyst is 0.1mol/$\ell$, the particle size of synthesized hydrate becomes finer. On condition that partial prehydrolysis time of TEOS is more than 50 hours, the monosized fine powder is obtained(below 1${\mu}{\textrm}{m}$).

• 공업화학
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• 제10권7호
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• pp.963-968
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• 1999

CFCs(chlorofluorocarbons)에 의한 여러 지구 환경문제들이 발생되고 있는 가운데, 사용후 회수된 CFCs에 대하여 보다 안전한 파괴방법이 요구되고 있다. 이런 관점에서 CFC-113의 분해를 위한 보다 좋은 조건을 개발하고자 접촉 산화분해반응하에서 솔-젤법으로 만들어진 에어로젤 $TiO_2-SiO_2(ATS)$ 촉매에 대하여 본 연구를 행하였다. 솔-젤법으로 만들어진 ATS 촉매가 초기 활성에서 우수하였지만 반응시간이 경과함에 따라 침전법에 의해 제조된 촉매보다 급격한 활성저하를 나타내었다. 이런 비활성화의 원인은 SEM-EDX와 XRD의 분석으로부터 생성가스 $F_2$에 의한 촉매표면의 Si 원자에 대한 결합, 유출에 기인된 것으로 판단되었다. 그리고 ATS 촉매제조과정에서 prehydrolysis 방법으로 처리된 촉매가 촉매 표면의 산성도가 증가됨에 따라 촉매활성이 지속적으로 유지되고 촉매 피독에 의한 비활성화가 느리게 진행되는 것이 관찰되었다. 또한 ATS 촉매 반응에 있어서 Ti의 mol 비가 80%까지 증가함에 따라서도 산성도가 증가되어 본 반응에서 활성 유지와 비활성화 진행속도가 느리게 됨을 발견할 수 있었다. 한편, ATS 촉매에 대해 황산이온처리된 $ATS/SO_4{^{2-}}$ 촉매가 촉매의 활성유지와 비활성화 방지에 있어서 우수한 성질을 나타내었다. 그러므로 본 반응에 있어서 촉매 표면에 대한 황산이온의 처리가 촉매의 비활성화 방지에 기여할 수 있음을 알 수 있었다.

• KSBB Journal
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• 제14권6호
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• pp.707-712
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• 1999

Dextransucrse와 ${\alpha}$-amylase의 혼합효소반응 통하여 새로운 구조의 올리고당을 생산하였고, 그 특성을 조사하였다. 기질인 설탕과 녹말의 농도를 10%(w/v), 5%(w/v)로 하였을 때 dextransucrase와 ${\alpha}$-amylase의 활성비가 100U대 1000U일 경우 올리고당의 종류와 생산수율이 66.4%로 가장 높았다. 녹말의 분해산물이 dextransucrase의 수용체 반응을 활성화시켜 dextransucrase 활성을 증가시켰다. 혼합효소의 활성이 증가할수록 올리고당보다는 다당을 생산하였다. 5%(w/v)의 녹말을 1시간동안 반응시켜 수용체로 이용될 수 있는 산물의 양을 증가시킨 후 설탕의 농도가 10%(w/v)가 되도록 반응시킨 방법이 녹말과 설탕을 반응초기부터 모두 반응시킨 방법보다 올리고당 생산수율이 12% 더 증가하였다. 새로운 구조의 올리고당은 pH 3에서는 10.6, pH 4에서는 7.8%의 분해를 보였다. 새로운 구조의 올리고당은 pH 6과 140$^{\circ}C$ 고온에서 89.3%까지 안정하였다.

• 환경위생공학
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• 제13권1호
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• pp.16-25
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• 1998

Laboratory-scale experiment using anaerobic fluidized bed reactor was carried out to investigate the prehydrolysis step with caustic soda on the treatment efficiency of anaerobic sludge treatment, since the overall rate-limiting step for the complete anaerobic digestion of sludge was the hydrolysis step by extracellular bacterial enzymes of insoluble polymeric molecules. Reactors received a sludge which had not been pretreated, a 50-50 mixture of pretreated and untreated sludge, and the fully pretreated sludge. Hydraulic retention time of 10, 5, 2.5 days and 1 day were applied with an respective equivalent organic loading rate of 1.17, 2.23, 4.17, 11.24 gCOD/L/d. Reactor with the untreated sludge did not archieve adequate digestion even at the HRT of 5 days, and reactor, which received the 50-50 mixture, operated well at the HRT of 5 days, but began to show signs of unstable digestion at the HRT of 2.5 days. While, reactor, which was fed the hydrolyzed sludge, operated reasonably well at the 2.5 days, but was showing somewhat decrease in removal efficiencies. Results, therefore, have substantiated that the limiting reaction in the anaerobic treatment process is hydrolysis. The soluble COD did not significantly accumulate in the reactor as organic acid form, even when they were highly stressed. It was believed that this resistance to a build-up of organic acids and soluble COD behavior was mainly due to the maintenance of the methane bacteria in the fixed-film system which prevents washout as the organic loading increased. The anaerobic fluidized bed reactor was therefore effective for the digestion of waste activated sludge at short HRT.

• Asian-Australasian Journal of Animal Sciences
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• 제25권1호
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• pp.66-74
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• 2012

The effects of exogenous fibrolytic enzymes (EFE; a mixture of two preparations from Trichoderma spp., with predominant xylanase and ${\beta}$-glucanase activities, respectively) on colonization and digestion of ground barley straw and alfalfa hay by Fibrobacter succinogenes S85 and Ruminococcus flavefaciens FD1 were studied in vitro. The two levels (28 and 280 ${\mu}g$/ml) of EFE tested and both bacteria were effective at digesting NDF of hay and straw. With both substrates, more NDF hydrolysis (p<0.01) was achieved with EFE alone at 280 than at 28 ${\mu}g$/ml. A synergistic effect (p<0.01) of F. succinogenes S85 and EFE on straw digestion was observed at 28 but not 280 ${\mu}g$/ml of EFE. Strain R. flavefaciens FD1 digested more (p<0.01) hay and straw with higher EFE than with lower or no EFE, but the effect was additive rather than synergistic. Included in the incubation medium, EFE showed potential to improve fibre digestion by cellulolytic ruminal bacteria. In a second batch culture experiment using mixed rumen microbes, DM disappearance (DMD), gas production and incorporation of $^{15}N$ into particle-associated microbial N ($^{15}N$-PAMN) were higher (p<0.001) with ammoniated (5% w/w; AS) than with native (S) ground barley straw. Application of EFE to the straws increased (p<0.001) DMD and gas production at 4 and 12 h, but not at 48 h of the incubation. EFE applied onto S increased (p<0.01) $^{15}N$-PAMN at 4 h only, but EFE on AS increased (p<0.001) $^{15}N$-PAMN at all time points. Prehydrolysis increased (p<0.01) DMD from both S and AS at 4 and 12 h, but reduced (p<0.01) $^{15}N$-PAMN in the early stage (4 h) of the incubation, as compared to non-prehydrolyzed samples. Application of EFE to barley straw increased rumen bacterial colonization of the substrate, but excessive hydrolytic action of EFE prior to incubation decreased it.