• 제목/요약/키워드: bleaching process

검색결과 120건 처리시간 0.027초

제지폐수중의 다이옥신 배출 패턴 및 형성 메카니즘(II) - 표백공정이외의 폐수(알칼리폐수)를 중심으로 - (Emission Patterns and Formation Mechanism of PCDDs/PCDFs in Bleaching Wastewater(I) - Alkali Wastewater -)

  • 신선경;장성기
    • 분석과학
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    • 제14권5호
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    • pp.422-431
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    • 2001
  • 염소표백공정을 포함하고 있는 펄프 제지폐수 배출시설의 폐수 중 다이옥신류의 배출특성을 파악하기 위해 표백공정 전 후단을 제외한 회수공정, 마감공정집수조 및 방류수의 알칼리 폐수를 채취 분석하였다. 회수공정과 마감공정에서 2,3,7,8-치환이성체의 배출분포는 2,3,7,8-사염화퓨란(TCDF) > 팔염화다이옥신(OCDD) > 팔염화퓨란(OCDF)의 순으로 배출되고 있으며, 퓨란류(PCDFs)와 다이옥신류(PCDDs)의 배출비는 76:24, 62:38로 조사되어 주로 퓨란류가 배출되고 있음을 알 수 잇었다. 그러나, 집수조에서는 팔염화다이옥신(OCDD) > 1,2,3,7,8-오염화다이옥신(PeCDD) > 1,2,3,4,7,8-육염화다이옥신(HxCDD)의 순으로 2,3,7,8-치환이성체가 배출되고 있으며, 독성등가환산농도로 환산한 결과 1,2,3,7,8-오염화다이옥신(PeCDD)이 81%, 1,2,3,4,7,8-육염화다이옥신(HxCDD)이 12%를 차지하는 것으로 나타났으며, 검출된 다이옥신류의 농도는 0.2266ng-TEQ/L로 조사되었다. 또한, 방류수에서의 2,3,7,8-치환이성체 배출분포는 팔염화다이옥신(OCDD) 및 2,3,7,8-사염화퓨란류(TCDF)의 순으로 배출되고 있으며, 독성등가환산농도의 배출분포는 1,2,3,7,8-오염화다이옥신(PeCDD) 및 2,3,7,8-사염화퓨란(TCDF)의 순으로 배출되었으며, 배출되는 다이옥신류의 농도는 0.377 ng-TEQ/L로 조사되었다.

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복분자를 이용한 식초의 제조 및 그의 항산화 효과 (Production of Vinegar using Rubus coreanus and Its Antioxidant Activities)

  • 홍성민;강민정;이주혜;정지혜;권승혁;서권일
    • 한국식품저장유통학회지
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    • 제19권4호
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    • pp.594-603
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    • 2012
  • 과잉으로 생산되는 복분자의 소비 촉진과 신수요 창출을 위해 복분자 식초를 제조한 후 이화학적 성분분석 및 항산화 효과를 조사하였다. 알코올 발효의 최적 조건은 당도 15 $^{\circ}Brix$, 온도 $30^{\circ}C$, 발효기간 4일이었으며, 초산 발효의 최적 조건은 초기 알코올 함량 6%, 초기 산도 2%, 온도 $30^{\circ}C$, 발효기간은 9일이었다. 최적 조건으로 발효된 복분자 식초의 유리당은 surcose, fructose 및 glucose로 확인되었으며, 주요 유기산은 acetic acid, malic acid, succinic acid 및 malonic acid로 나타났다. 또한 유리아미노산 총 함량은 108.03 ${\mu}g/mL$로 alanine, glutamic acid, ${\gamma}$-amino-N-butyric acid 및 o-phosphoethanolamine가 주된 성분으로 나타났으며, 무기성분은 K, Na, Mg, Ca과 같은 알칼리성 원소를 다량 함유한 것으로 나타났다. 복분자 식초의 총 폴리페놀 및 안토시아닌의 함량은 각각 25.19, 80.71 mg/100 mL이었으며, DPPH, $ABTS^{{\cdot}+}$ 라디칼 소거 활성, 환원력, ${\beta}$-carotene bleaching의 실험에서 복분자 식초는 양성 대조군과 유사한 높은 항산화 활성을 가지는 것으로 나타났다.

리그닌 화학구조 모델의 역사적 고찰 (Historical Consideration of Lignin Models for Native Lignin Structure)

  • 황병호
    • 임산에너지
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    • 제23권1호
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    • pp.45-68
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    • 2004
  • The word of lignin is derived from the Latin word 'ligum' meaning wood. Lignin is complex polymer consisting of coniferyl alcohol, sinapyl alcohol and p-coumaryl alcohol unit and has an amorphous, three dimensional network structure which is hard to be hydrolyzed by acid. Lignin is found in the cell wall of plants lignified. The mode of polymerization of these alcohols in the cell wall lead to a heterogeneous branched and cross-linked polymer in which phenyl propane units are linked by carbon-carbon and carbon-oxygen bonds. This polymerization of precursors, p-coumaryl alcohol, coniferyl alcohol and sinapyl alcohol to lignin is formed by enzymic dehydrolyzation. The reaction is initiated by an electron transfer which results in the formation of resonance-stabilized phenoxy radical. The combination of these radicals produces a variety of dimers, trimers and oligomers and so on. Lignin research has been divided into basic and practical application field. The basic studies contains biosynthesis, chemical structure, distribution in the cell wall and reactivity by reductants, oxidants and organic solvents. The application research will be approached the reaction of lignin in various pulp making involving pulp bleaching and its effect on pulp qualities. Lignin also will be studied for the production of fine chemicals, polymer products and the conservation into an energy source like petroleum oil because the amount of lignin produced in pulp making process is more than 51,000,000 tons per year in the world. Both basic and application research must lay emphasis on the development for the utilization of lignin and the pulping process. But these researches can not be completed without understanding lignin structure containing functional groups. Therefore, this paper was focused on the review of lignin formulation which has been studied since 1948 in chronological order. This review was based on monomers, dimers, trimers and tetramers of phenyl propane unit structures which were isolated and identified by different methods from various wood.ious wood.

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한지 생산공정에서 발생하는 폐수의 탈색 및 슬러지 회수 (Decolorization of Wastewater and Collecting of Sludge from Hanji Production)

  • 최희선;김태진
    • 분석과학
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    • 제13권3호
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    • pp.351-356
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    • 2000
  • 한지 제조공정 중 발생하는 폐수의 탈색과 최종 슬러지 회수조건에 대해 연구하였다. 잿물삶기 공정에서 생긴 50 mL 폐수의 검은 색은 산화제인 $Ca(OCl)_2$를 2.0g 정도 가하면 효과적으로 탈색시킬 수 있었는데 이는 표백공정 중에 사용되는 과량의 표백제를 재활용하면 매우 효과적으로 탈색시킬 수 있을 것으로 생각된다. 그러나 전기분해적 산화에 의한 탈색은 전혀 효과적이지 못하였다. 최종 슬러지를 회수하는데는 현재 사용하는 고분자 응집제로도 효과적으로 슬러지가 제거됨을 알 수 있었지만 고분자 응집제를 사용할 경우 필히 $Al_2(SO_4)_3$을 사용하여야 하고 슬러지를 제거할 때 함께 나오기 때문에 순수한 섬유질 형태의 슬러지를 얻을 수 없었다. 그러나 triethanolamine과 Triton X-100과 같은 계면활성제를 이용하였을 때 슬러지 회수율은 85% 정도로 고분자 응집제를 이용할 때와 거의 같은 효율을 나타내었고, $Al_2(SO_4)_3$을 사용하지 않아도 되며, 슬러지도 섬유질 형태이었기 때문에 재활용하기에도 좋으리라고 예상된다.

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미세결정셀룰로오스의 제조를 위한 억새 바이오매스의 처리 및 특성연구 (Study of Preparation and Characterization of Microcrystalline cellulose from Miscanthus sinensis)

  • 성용주;이영주;이준우;김세빈;박관수;신수정
    • 펄프종이기술
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    • 제42권4호
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    • pp.56-63
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    • 2010
  • Microcrystalline cellulose (MCC) was prepared from Miscanthus in this study. Two pulping methods, soda pulping and alkaline sulfite pulping were applied as a pretreatment process. After pulping, two different bleaching processes such as $ClO_2$ treatment followed by $H_2O_2$ treatment and $O_3$ treatment followed by $H_2O_2$ treatment were carried out. Two concentration of $H_2SO_4$, 47% and 57% were applied to the purified Miscanthus cellulose as a acid hydrolysis process to make MCC. The crystallinity index and morphological properties of the produced MCC were evaluated with X-ray diffractometer and scanning electron microscopy. The MCC originated from the soda pulping sample showed the higher crystallinity index than that originated from the alkaline sulfite pulping sample. The two stages of treatmen twith $O_3$ and $H_2O_2$ resulted in the higher purified cellulose products.

Determining the Proportions of Bone and Cartilage Growth in the Crucian Carp (carassius auratus) Using the Modified Simultaneous Differential Staining Technique

  • Lee, Jin-Heon
    • 한국환경보건학회지
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    • 제36권4호
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    • pp.337-341
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    • 2010
  • The modified simultaneous differential staining technique, which enables double staining of cartilage and bones, needs to be improved to prevent soft tissues from being damaged during the staining process. Key factors influencing the extent to which soft tissues are damaged include the fixative used, macerating time, potassium hydroxide concentration, incubation temperature and the removal of skin from specimens. Here we describe a protocol that enables the hardening of tissues during bleaching and maceration. We also describe a method for objectively measuring rates of cartilage and bone growth. The use of formalin as a fixative rendered soft tissues more rigid due to the resulting chemical bonds formed between proteins. Blotted specimens were immersed in 1% potassium hydroxide (KOH) and incubated at $37^{\circ}C$ for 1 day (smaller specimens) or 2-3 days (larger specimens). The 1% KOH solution was also used as the diluent solution for the subsequent immersion in a graded series of 30%, 50%, 70%, 90%, 100% glycerol solutions, a procedure that made soft tissues even more transparent and hardened. It was not necessary to remove the skin of specimens shorter than 2 cm, since the macerating solution could easily penetrate their thin skin layer and continuously remove those pigments hindering visibility. Since excessive osmosis is another factor that can damage soft tissues in the macerating process by causing the rupture of those cells not able to withstand the osmotic pressure, here it was minimized by balancing the salt concentration between the interior and exterior of cells with the addition of 0.9% sodium chloride (NaCl) in the macerating solution. Finally, to determine the proportions of cartilage and bone growth, photographs of the stained specimens were taken with a dissecting microscope and sections corresponding to the cartilage and bones were cut out from the printed pictures and weighed. Our results show that this method is suitable for the objective evaluation of bone and cartilage growth.

정어리유에 대한 탈색 및 탈취조건의 영향 (Effects of Process Conditions on Sardine Oil During Bleaching and Deodorization)

  • 김철진;안병학;황성연;신현경
    • 한국식품과학회지
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    • 제19권5호
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    • pp.420-425
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    • 1987
  • Rendering에 의하여 추출된 정어리 조유를 이용하여 식품 및 사료의 원료로 직접 사용할 수 있는 정제 정어리유를 제조하기 위하여 탈산, 탈색 및 탈취등의 정제 실험을 실시하였다. 4%의 산성활성백토를 가하여 $105^{\circ}C$에서 20분간 질소가스하에서 탈색하는 것이 conjugated 화합물의 생성없이 가장 효과적이었다. 탈취온도가 높을수록 conjugated 화합물의 생성이 촉진되었으며, 요오드가 및 고도불포화지방산의 함량이 감소되는 경향이 뚜렷하여 정어리유의 경유 $180^{\circ}C$ 이하에서 탈취하는 것이 바람직한 것으로 밝혀졌다.

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4,5-Diphenyl-Imidazolone의 合成 及 螢光效果에 關한 硏究 (Synthesis of 4,5-Diphenyl Imidazolone and Studies on its Fluorescent Effect)

  • 전풍진;김형숙
    • 대한화학회지
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    • 제4권1호
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    • pp.70-77
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    • 1957
  • 4,5-Diphenyl Imidazolone is synthesized from Benzoin, Urea, and Acetic acid catalyser. Nowadays, it is being used as an optical bleaching agent for wool and nylon textiles. Up to now, only one process of synthesis has been known. In order to find out the best conditions governing the yield were examined under various catalysers and conditions. In this experiment, the summary of results were as follows. a. On Acetic acid catalyser. The maximum yield conditions were mol ratio (Benzoin: Urea: Acetic acid) 1 : 2 : 14, Acetic acid concentration 99.9%. Reaction temperature 115$^{\circ}$. Under reaction time of 2 hours, above yield was 96.4%. b. On Mineral acid Catalyser. In using of Sulfonic acid, the color of solution was changed dark purlish black. With other mineral acid catalysers, in spite of increasing of temperature, it was proved that Benzoin floats on the solution, so that this reaction could not be continue. c. On Phosphoric acid catalyser. It was made clear that it can not be used for this reaction. d. On Sodium hydroxide catalyser. As one of Alkali catalyser, Sodium hydroxide was examined but this was unsuitable substance for this reaction. e. On Formic acid catalysers. The maximum yield conditions were mol ratio (Benzoin: Urea: Formic acid) 1: 2: 30. Formic acid concentration 85.%. Reaction temperature 150∼110$^{\circ}$. Under reaction time of 90 minutes, the best yield was 87%. Hereby, it was proved that organic acids such as Acetic acid and Formic acid can be used. When using Acetic acid, the yield was better than Formic acid, but it takes longer reaction time than Formic acid. About the fluorescent effect, the temperature of dye-bath must not be over 904,5-Diphenyl Imidazolone is synthesized from Benzoin, Urea, and Acetic acid catalyser. Nowadays, it is being used as an optical bleaching agent for wool and nylon textiles. Up to now, only one process of synthesis has been known. In order to find out the best conditions governing the yield were examined under various catalysers and conditions. In this experiment, the summary of results were as follows. a. On Acetic acid catalyser. The maximum yield conditions were mol ratio (Benzoin: Urea: Acetic acid) 1 : 2 : 14, Acetic acid concentration 99.9%. Reaction temperature 115$^{\circ}$. Under reaction time of 2 hours, above yield was 96.4%. b. On Mineral acid Catalyser. In using of Sulfonic acid, the color of solution was changed dark purlish black. With other mineral acid catalysers, in spite of increasing of temperature, it was proved that Benzoin floats on the solution, so that this reaction could not be continue. c. On Phosphoric acid catalyser. It was made clear that it can not be used for this reaction. d. On Sodium hydroxide catalyser. As one of Alkali catalyser, Sodium hydroxide was examined but this was unsuitable substance for this reaction. e. On Formic acid catalysers. The maximum yield conditions were mol ratio (Benzoin: Urea: Formic acid) 1: 2: 30. Formic acid concentration 85.%. Reaction temperature 150∼110$^{\circ}$. Under reaction time of 90 minutes, the best yield was 87%. Hereby, it was proved that organic acids such as Acetic acid and Formic acid can be used. When using Acetic acid, the yield was better than Formic acid, but it takes longer reaction time than Formic acid. About the fluorescent effect, the temperature of dye-bath must not be over 90$^{\circ}$. and the ratio of 4,5-Diphenyl Imidazolone and water should be from 1:50000. to 1:10000. It proved that the best effect on textiles, and the best condition were dye-temperature near 704,5-Diphenyl Imidazolone is synthesized from Benzoin, Urea, and Acetic acid catalyser. Nowadays, it is being used as an optical bleaching agent for wool and nylon textiles. Up to now, only one process of synthesis has been known. In order to find out the best conditions governing the yield were examined under various catalysers and conditions. In this experiment, the summary of results were as follows. a. On Acetic acid catalyser. The maximum yield conditions were mol ratio (Benzoin: Urea: Acetic acid) 1 : 2 : 14, Acetic acid concentration 99.9%. Reaction temperature 115$^{\circ}C$. . Under reaction time of 2 hours, above yield was 96.4%. b. On Mineral acid Catalyser. In using of Sulfonic acid, the color of solution was changed dark purlish black. With other mineral acid catalysers, in spite of increasing of temperature, it was proved that Benzoin floats on the solution, so that this reaction could not be continue. c. On Phosphoric acid catalyser. It was made clear that it can not be used for this reaction. d. On Sodium hydroxide catalyser. As one of Alkali catalyser, Sodium hydroxide was examined but this was unsuitable substance for this reaction. e. On Formic acid catalysers. The maximum yield conditions were mol ratio (Benzoin: Urea: Formic acid) 1: 2: 30. Formic acid concentration 85%. Reaction temperature 150∼110$^{\circ}C$. Under reaction time of 90 minutes, the best yield was 87%. Hereby, it was proved that organic acids such as Acetic acid and Formic acid can be used. When using Acetic acid, the yield was better than Formic acid, but it takes longer reaction time than Formic acid. About the fluorescent effect, the temperature of dye-bath must not be over 90$^{\circ}C$. and the ratio of 4,5-Diphenyl Imidazolone and water should be from 1:50000. to 1:10000. It proved that the best effect on textiles, and the best condition were dye-temperature near 70$^{\circ}C$. and dye-time 15 minutes. . and dye-time 15 minutes. . and the ratio of 4,5-Diphenyl Imidazolone and water should be from 1:50000. to 1:10000. It proved that the best effect on textiles, and the best condition were dye-temperature near 70$^{\circ}C$. and dye-time 15 minutes.

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정선-삼척 일대 대기층 상부 고품위 석회석의 생성환경 (Genetic Environments of the High-purity Limestone in the Upper Zone of the Daegi Formation at the Jeongseon-Samcheok Area)

  • 김창성;최선규;김규보;강정극;김경배;김학수;이정상;유인창
    • 자원환경지질
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    • 제50권4호
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    • pp.287-302
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    • 2017
  • 대기층의 고품위 석회석 생성기작은 고품위로 퇴적되었다는 견해와 퇴적 이후 열수의 작용에 의해 상부 영역에 국한되어 백색화와 함께 고품위화 하였다는 두 가지 견해로 나뉘어 있으며, 광물-암석화학적 연구를 통해 이들 견해를 검토하였다. 대기층의 암색은 크게 백색, 담갈색, 담회색, 회색, 암회색의 다섯 단계로 구분할 수 있다. 이 중 백색~담회색 암석은 53.15 ~ 55.64 wt. % CaO의 고품위 석회석이며, 담갈색은 20.71 ~ 21.67 wt. % MgO로 거의 순수한 백운석이다. 대기층은 상부와 하부의 석회암대와 그 사이에 중부 백운암대로 구성되어 있으며, 상부가 하부에 비해 전반적으로 높은 CaO 함량을 보인다. 다만, 대기층 상부와 하부에서 전반적으로 백색화 현상이 관찰되며, 하부에서 백색에 비해 담회색 암석의 CaO 함량이 높은 경향이 나타나고 있어, 백색화와 CaO 함량은 상관관계가 없는 것으로 확인된다. 또한, 고품위 석회석과 중-저품위 석회석의 구분은 CaO 성분과 함께 $Al_2O_3$, $K_2O$ 등 이질성분의 함유정도에 따라 구분되는데, 백색도가 높은 영역에서 이질성분의 함량이 증가하는 양상을 보이기도 한다. 특히, $Al_2O_3$는 열수에 의해 쉽게 제거될 수 없는 성분이므로, 열수 작용에 의해 백색화와 함께 이질 성분이 제거되었다는 이론은 증거가 미약한 것으로 판단된다. 산소-탄소 안정동위원소 분포는 대기층 상부와 하부의 석회암대 모두에서 탄소 안정동위원소의 변화 폭은 2 ‰ 이내인 반면, 산소 안정동위원소는 16 ‰ 이상의 큰 폭의 변화가 인지되어, 대기층 전반적으로 열수의 영향을 받은 것으로 확인된다. 열수작용의 시기는 $85.1{\pm}1.7Ma$로 주변 동원광산의 광화시기와 일치한다. 회색-담회색-백색으로 백색화가 진행될수록 산소 안정동위원소 비는 낮아지는 경향이 확인되며, 이는 이 지역 탄산염암의 백색화는 열수에 의한 현상임을 지시한다. 따라서, 대기층은 전반적으로 열수의 영향을 받았으며, 열수에 의해 백색화가 진행되었으나, 고품위 석회석화는 백색화와 관련이 없으며, 열수에 의한 현상이 아닌 것으로 판단된다. 대기층 상부에서의 고품위화는 이질물 특히, $Al_2O_3$ 성분이 효과적으로 제거될 수 있는 퇴적환경을 고려하여야 하며, 중부 백운암대를 중심으로 상-하부 주변에서 CaO 함량이 증가하는 양상으로부터 순차층서적으로 퇴적 당시 이질물의 퇴적작용이 배제된 탄산염 천해환경이 조성된 결과로 보는 것이 타당할 것이다.

과산화수소 표백조건에 따른 면셀룰로오스의 특성 변화 (Changes in the Properties of Cotton Cellulose by Hydrogen Peroxide Bleaching)

  • 허용대;성용주;정양진;김덕기;김태영
    • 펄프종이기술
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    • 제45권3호
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    • pp.59-68
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    • 2013
  • The cotton contains various impurities such as protein, wax, pectins, coloring matter, even though cotton has been a major source of pure cellulose. The purification processes have been commonly applied to obtain the pure cellulose. However the excessive purification treatments could lead to the damage in the cellulose structure which could result in the degradation of cellulose and the limited application of cotton cellulose. In this study, the changes in cellulose structural properties such as crystallinity and DP(degree of polymerization) by the various conditions of the purification processes were investigated. The less toxic agents such as hydrogen peroxide and sodium silicate were applied for the purification treatment in this study. The increase in the process times, the temperature and the applied amount of chemical agents resulted in the more purified cellulose. The DP of cotton cellulose was increased at the first weak conditions by the reduction of small molecules such as pectin, wax, and so on. Especially the 2 % addition amount of $H_2O_2$ with $Na_2SiO_3$ resulted in the higher value in the DP and the brightness compared to the 1.5 % addition amount of $H_2O_2$. However, the 4 % addition amount of $H_2O_2$ with $Na_2SiO_3$ showed the decreased value because of excessive treatment. In case of the changes in the crystallinity (Gjk), the highest value of the crystallinity was obtained by the 2% addition amount of $H_2O_2$ on the cotton cellulose, which showed similar with the change in the DP.