• 제목/요약/키워드: diffusion dialysis

검색결과 32건 처리시간 0.022초

Testosterone-encapsulated Surfactant-free Nanoparicles of Poly(DL-lactide-co-glycolide): Preparation and Release Behavior

  • Jeong, Young-Il;Shim, Yong-Ho;Song, Ki-Chan;Park, Youeng-Guen;Ryu, Hwa-Won;Nah, Jae-Woon
    • Bulletin of the Korean Chemical Society
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    • 제23권11호
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    • pp.1579-1584
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    • 2002
  • Since surfactant or emulsifiers remained on the nanoparticle surface significantly affect the physicochemical properties, the biodegradation rate, the biodistribution, and the biocompatibility of nanoparticles, surfactant-free nanoparticles should be good candidate. surfactant-free PLGA nanoparticles were successfully prepared by both the dialysis method and the solvent diffusion method. The PLGA nanoparticles prepared using the solvent diffusion method has a smaller particle size than the dialysis method. The solvent diffusion method was better for a higher loading efficiency than the dialysis method but the nanoparticle yield was lower. Testosterone (TST) release from the PLGA nanoparticles was dependent on the particle size rather than the drug contents. Testosterone release from the PLGA nanoparticles prepared by the solvent diffusion method using acetone was faster than those prepared by the dialysis method. TST release from the PLGA nanoparticles prepared by the solvent diffusion method using acetone and the dialysis method using dimethylformamide (DMF) was completed for 4 days while the PLGA nanoparticles prepared by the dialysis method using acetone showed approximately 80% TST release after 4 days. Since the PLGA nanoparticle degradation ratio was below 20% within 5 days at all samples while TST release completed within 4 days, TST release was dependent on the diffusion mechanism rather than degradation.

透析法에 依한 이온量 및 分子量의 決定에 關한 硏究 (第4報). 比表面積 및 透析膜孔이 透析에 미치는 影響 (A Study on the Determination of Ionic and Molecular Weight of Dissolved Substance by Dialysis Method (Ⅳ). Effects of Specific Surface Area and Pore Size of Dialysis Membrane on Dialysis)

  • 신윤경;이전;김태천
    • 대한화학회지
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    • 제21권1호
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    • pp.44-52
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    • 1977
  • 透析係數가 常數로서 나타날 수 있는 條件究明의 一環으로서 透析液 單位體積當의 透析膜面積인 比表面積과 透析膜孔의 크기가 透析에 미치는 영향을 究明하였다. 1回의 透析實驗에서 任意時間區間마다 任意부피의 透析液試料를 잇따라 菜取하는 方法(間歇試料菜取法이라 呼稱하기로 함)은 透析係數를 求하는 方法으로서 採擇할 수 있음과, 또한 透析膜孔이 상당히 크더라도 膜을 通한 擴散係數는 自由擴散係數에 미치지 못함을 밝히었다.

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In vitro release test models for water-insoluble drugs loaded in colloidal carriers

  • Lee, Jung-Min;Choi, Sung-Up;Lee, Byoung-Moo;Lee, Sung-Jae;Choi, Young-Wook
    • 대한약학회:학술대회논문집
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    • 대한약학회 2003년도 Proceedings of the Convention of the Pharmaceutical Society of Korea Vol.1
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    • pp.295.1-295.1
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    • 2003
  • A suitable model for the estimation of the drug release from nanoparticles has been varied and problematic, especially for the release from lipid nanoparticles containing water-insoluble drugs, due to the difficult particle collection from the release medium. Dialysis membrane has been widely used for the release test from colloidal carrier systems. The amount of drug from the carriers in normal dialysis diffusion technique was very low typically. (omitted)

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LCD 제조공정의 혼합폐산으로부터 일인산암모늄 제조 기술 (Manufacture Technology of Monoammonium phosphate from LCD Waste Acid)

  • 이하영;이상길;박성국;김주한;김주엽;김준영
    • 청정기술
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    • 제15권4호
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    • pp.253-257
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    • 2009
  • LCD 제조공정에서 배출되는 질산과 초산, 인산, 그리고 Al과 같은 금속이온을 함유한 폐에칭액으로부터 진공증발과 확산투석을 이용하여 고순도 인산을 회수하여 인산암모늄을 제조하고자 하였다. 진공증발을 이용하여 질산과 초산을 제거하였다. 진공도가 -650 mmHg인 경우에는 온도 413 K 이상에서 완전 분리되었고, 진공도가 -700 mmHg인 경우에는 온도 393 K 이상의 영역에서 완전히 분리되었다. 그리고 진공도 -730 mmHg의 경우는 온도 383 K 이상에서도 완전 분리가 가능하였다. 99%의 질산과 초산을 제거하였으며, 확산투석을 이용하여 약 97.5% 이상의 Al을 제거하였다. 이렇게 얻어진 고순도 인산과 수산화암모늄을 이용하여 일인산암모늄을 제조하는 공정에서 급격한 발열반응을 제어하고 안정된 적정조건을 도출하기 위하여 수산화암모늄의 농도, 적정 몰비, pH, 온도 등의 반응인자를 조절하여 회수율 약 90%의 일인산암모늄을 제조하였다.

폐솔더 박리액으로부터 확산투석법에 의한 질산의 회수 (Recovery of Nitric Acid from Waste Solder Stripper by Diffusion Dialysis)

  • 류승형;김태영;안낙균;강명식;안재우;안종관
    • 자원리싸이클링
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    • 제24권5호
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    • pp.33-39
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    • 2015
  • 음이온 교환막을 이용한 확산투석에 의해 폐솔더 박리액으로부터 질산을 효율적으로 회수하기 위한 기초 연구를 실시하였다. 우선 모의용액 실험의 경우 유속, 유속비, 질산농도, 금속이온 종류 및 농도 등이 질산 회수율에 미치는 영향을 조사하였다. 유속이 증가함에 따라 질산 회수율은 감소하였고 급액에 대한 순수의 유속비(W/F)가 증가할수록 질산 회수율은 증가하여 유속비가 1.5이상에서 약 99%의 질산 회수율을 보였다. 급액중 질산용액의 농도가 증가함에 따라 3.0 M 까지는 산회수율이 증가 하였으나 3.0 M 이후로는 회수율은 점차 낮아 졌다. 확산투석막을 통과하는 금속이온의 투과율은 Pb, Na, Cu순 이었고, Fe과 Sn은 투과되지 않았다. 실제 폐솔더액을 사용하여 유속 $0.9L/hr-m^2$, W/F = 1.3 으로 확산 투석을 실시한 결과 약 94%의 질산 회수율을 얻을 수 있었다.

In Vivo Measurement of Site-Specific Peritoneal Solute Transport Using a Fiber-Optic-based Fluorescence Photobleaching Technique

  • Lee, Donghee;Kim, Jeong Chul;Shin, Eunkyoung;Ju, Kyung Don;Oh, Kook-Hwan;Kim, Hee Chan;Kang, Eungtaek;Kim, Jung Kyung
    • Journal of the Optical Society of Korea
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    • 제19권3호
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    • pp.228-236
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    • 2015
  • Fluorescence recovery after photobleaching (FRAP) is a well-established method commonly used to measure the diffusion of fluorescent solutes and biomolecules in living cells or tissues. Here a fiber-optic-based FRAP (f-FRAP) system was developed, and validated using macromolecules in water and agarose gels of different concentrations. We applied f-FRAP to measure the site-specific diffusion of fluorescein (NaFluo) in peritoneal membranes (PMs) on the liver, cecum, and kidney of a living rat during peritoneal dialysis. Diffusion of fluorescein in PM varied in a time-dependent manner according to the type of organ ($D_{PM\;on\;Liver}/D_{NaFluo}=0.199{\pm}0.085$, $D_{PM\;on\;Cecum}/D_{NaFluo}=0.292{\pm}0.151$, $D_{PM\;on\;Kidney}/D_{NaFluo}=0.218{\pm}0.110$). The proposed method allows direct quantitative measurement of the three-dimensional diffusion in local PM in vivo, which was previously inaccessible by peritoneal function test methods such as peritoneal equilibration test (PET) and standardized PM assessment (SPA). f-FRAP is promising for local and dynamic assessments of peritoneal pathophysiology and the mass transport properties of PMs, presumed to be affected by variation of tissue structures over different organs and functional changes of the PM with years of peritoneal dialysis.

Preparation of diffusion dialysis membrane for acid recovery via a phase-inversion method

  • Khan, Muhammad Imran;Wu, Liang;Hossain, Md. Masem;Pan, Jiefeng;Ran, Jin;Mondal, Abhishek N.;Xu, Tongwen
    • Membrane and Water Treatment
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    • 제6권5호
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    • pp.365-378
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    • 2015
  • Herein, the preparation of anion exchange membrane (AEM) from brominated poly(2,6-dimethyl 1,6-phenylene oxide) BPPO and dimethylaniline (DMA) by phase-inversion process is reported. Anion exchange membranes (AEMs) are prepared by varying the DMA contents. Prepared AEMs show high thermal stability, water uptake (WR) around 202% to 226%, dimensional change ratios of 1.5% to 2.6% and ion exchange capacities (IECs) of 0.34 mmol/g to 0.82 mmol/g with contact angle of $59.18^{\circ}$ to $65.15^{\circ}$. These membranes are porous in nature as confirmed by SEM observation. The porous property of membranes are important as it could reduce the resistance of transportation of ions across the membranes. They have been used in diffusion dialysis (DD) process for recovery of hydrochloric acid (HCl) from the mixture of HCl and ferrous chloride ($FeCl_2$). Presence of $-N+(CH_3)_2C_6H_5Br^-$ as a functional group in membrane matrix facilitates its applications in DD process. The dialysis coefficients of hydrochloric acid ($U_H$) of the membranes are in range of 0.0016 m/h to 0.14 m/h and the separation factors (S) are in range of 2.09 to 7.32 in the $HCl/FeCl_2$ system at room temperature. The porous membrane structure and presence of amine functional group are responsible for the mechanism of diffusion dialysis (DD).

음이온 교환막에서 염산의 이동특성 연구 (A Study on Transport Characteristics of Hydrochloric Acid in an Anion Exchange Membrane)

  • 강문성;오석중;문승현
    • 멤브레인
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    • 제8권3호
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    • pp.148-156
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    • 1998
  • 이온교환막을 이용하는 확산투석은 농도차가 구동력인 막공정으로서 철강 산업, 금속 제련 산업, 전기 도금 산업 등으로부터 발생되어지는 폐산으로부터 염산 및 기타 산들을 회수하는데 사용된다. 이론적으로는 초기산 농도가 증가함에 따라 구동력인 농도차가 커지므로 선형적으로 산의 투과속도가 증가하게 된다. 그러나 염산의 경우 약 3 N 이상의 고농도 범위에서는 투과속도 증가율이 농도차가 커짐에 따라 감소하였다. 본 연구에서는 막흡수 실험과 확산투석조 실험을 통해 염산을 회수하기 위한 확산투석에 산의 농도가 미치는 영향과 농도 범위에 따른 음이온 교환막 내부에서의 산의 이동 기작을 고찰하였다. 실험 결과 저농도(<2 N)산의 경우에는 산의 분자확산, 그리고 고농도 (>2 N)산의 경우에는 수소이온 투과현상 (proton leakage)이 막에서의 지배적인 이동 기작임을 알 수 있었다. 또한 고농도 범위에서는 삼투압에 의한 물분자의 이동과 막의 탈수현상이 수소이온의 이동을 방해하므로 막에서의 산 플럭스 증가율이 감소하였다.

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Seven-year Survival Rate of On-line Hemodiafiltration

  • Yoon, Jung-Hwan;Kim, Nam-Ho
    • 대한의생명과학회지
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    • 제25권1호
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    • pp.32-39
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    • 2019
  • Conventional high-flux hemodialysis (HD) is not as good as normal kidney function. Morbidity and mortality rates of patients receiving HD are still very high. To increase mid-to-large molecule clearance by combining diffusion and convection, on-line hemodiafiltration (HDF) is required. The objective of this study was to compare long-term survival rate of patients treated with on-line HDF to those who received conventional high-flux HD by reviewing data from Chonnam National University Hospital (CNUH). We selected patients who attended the 'CUNH dialysis center' and agreed to participate in the study. Overall, 40 patients with ESRD switched from high flux HD to on-line HDF or started on-line HDF from August 2007 to December 2009. Additionally, a total of 42 patients receiving conventional high-flux HD during the same period were enrolled. We then reviewed long-term survival rate of patients receiving on-line HDF over the next seven years. When we compared survival rates for seven years, the survival rate of the group receiving on-line HDF was 65% (26/40) while that of the group receiving the conventional high-flux HD was 54.8% (23/42). Although the number of patients was small to see survival difference clearly by one specific dialysis modality, there was somewhat difference in survival rate between the two groups. Indicators such as anemia, calcium-phosphate metabolism, nutritional status, treatment adequacy, and hospitalization were also improved in the group receiving HDF. Overall, results of our study showed beneficial effects of on-line HDF on clinical outcomes and survival in chronic HD patients.

Modeling of continuous diffusion dialysis of aqueous solutions of sulphuric acid and nickel sulphate

  • Bendova, Helena;Palaty, Zdenek
    • Membrane and Water Treatment
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    • 제2권4호
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    • pp.267-279
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    • 2011
  • At steady state, the simultaneous transport of sulphuric acid and nickel sulphate through an anion-exchange membrane Neosepta-AFN (Astom Corporation, Tokyo, Japan) was investigated in a two-compartment counter-current dialyzer with single passes. The transport was quantified by the recovery yield of acid, rejection of salt and four phenomenological coefficients, which were correlated with the acid and salt concentrations in the feed. The phenomenological coefficients were determined by the numerical integration of the basic differential equations describing the concentration profiles of the components in the dialyzer. This integration was combined with an optimizing procedure. The experiments proved that the acid recovery yield is in the limits from 63 to 91 %, while salt rejection is in the limits from 79 to 97 % in the dependence on the volumetric liquid flow rate and composition of the feed.