Terminology for membranes and membrane processes ( IUPAC Recommendations 1996) 膜および膜プロセス用語1996 IUPAC推奨
Dialysis, Nanofiltration, Ultrafiltration and Microfiltration Separations透析、ナノ濾過、限外濾過、精密濾過分離((61-75)
Electrically Mediated Separations 電気利用分離(76-83)
Gas, Vapor and Pervaporation Separations ガス、蒸気、パーベーパレーション 分離(84-88)
Reverse Osmosis Separations 逆浸透分離(88-92)
Dialysis,
Nanofiltration, Ultrafiltration, and Microfiltration
Separations 透析、ナノ濾過、限外濾過、精密濾過分離 |
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61. | backflush: 逆洗: |
temporary reversal of
the direction of the permeate flow 時々透過流れの方向を逆転すること。 |
62. | bubble point: バブルポイント: |
pressure at which
bubbles first appear on one surface of an immersed porous membrane as gas
pressure is applied to the other surface upstream face of a membrane 浸積した膜のもう一方の側の気体を加圧したとき、膜表面に最初に気泡が生じる圧力。 |
63. | cake layer: ケーク層: |
layer comprised of
rejected particulate materials residing on the upstream face of a membrane
膜の上流側表面に膜を透過しなかった粒子状物がたまった層。 |
64. | concentration
polarization: 濃度分極: |
concentration profile
that has a higher level of solute nearest to the upstream
membrane surface compared with the more-or-less well-
mixed bulk fluid far from
the membrane surface 膜表面からはなれたほぼ完全混合にある液本体の濃度に比較して、膜の上流表面において溶質の濃度が高くなる濃度分布。 |
65. | concentration factor:
濃縮係数: |
ratio of the
concentration of a component i in the retentate to the concentration of the same
component in the feed {Note 1: cF=[(ci)retentate/(ci)feed]
(Note: see Fig.1)}[Note 2:
Compare retention factor (35)] 供給と非透過流れ中の濃度の比。 |
66. | dialysis: 透析: |
membrane process in
which transport is driven primarily by concentration differences, rather
than by pressure or electrical-potential differences,
across the thickness of a membrane 物質移動が圧力や電位差ではなく膜を介する濃度差でおこる膜プロセス。 |
67. | dialysis permeability
coefficient: 透析透過係数: |
permeability
coefficient(28) based on a transmembrane driving force
expressed in terms of the concentration difference of a
given component 推進力を濃度差とする透過係数。 |
68. | gel fouling layer:
ゲルファウリング層: |
highly swollen fouling
layer comprising a three-dimensional, possibly network, structure
residing at the surface of a membrane 膜表面で形成される3次元構造(網目構造)の高含水率度のファウリング層。 |
69. | hemodialysis: 血液透析: |
dialysis process(66) in
which undesired metabolites and toxic by-products, such as urea and
creatine, are removed from blood 尿素・クレアチンのような生体に好ましくない代謝物や有害な副生成物を血液から除去する透析プロセス。 |
70. | hemofiltration: 血液濾過: |
ultrafiltration process
(76) in which undesired metabolites and toxic by-products, such as urea
and creatine, are removed from blood 尿素・クレアチンのような生体に好ましくない代謝物や有害な副生成物を血液から除去する限外濾過プロセス。 |
71. | hindered transport:
相互作用下の移動: |
combined partition,
diffusion and convection process in which the effective partition,
diffusion and viscous drag coefficients in a restricted
environment depend upon the
ratio of the effective radius of the penetrant molecule
to that of pore 分配・拡散・対流が相互に影響しあうプロセス。膜の細孔中で分配係数・拡散係数・粘性係数の有効値が透過分子の有効径と細孔の径の比に依存する。 |
72. | microfiltration: 精密濾過: |
pressure -driven
membrane-based separation process in which particles and dissolved
macromolecules larger than 0.1μm are rejected 0.1μmより大きい粒子や高分子が阻止される圧力駆動の膜分離プロセス。 |
73. | molecular-weight
cutoff: 分子量カットオフ: |
molecular weight of a
solute corresponding to a 9O% rejection coefficient(33) for a
given membrane 膜の阻止率が90%となる溶質の分子量。 |
74. | nanofiltration: ナノ濾過: |
pressure-driven
membrane-based separation proress in which particles and dissolved molecules
smaller than about 2nm are rejected 2nmより小さい程度の粒子や高分子が阻止される圧力駆動の膜分離プロセス。 |
75. | ultrafiltration: 限外濾過: |
pressure-driven
membrane-based separation proccess in which particles and dissolved
macromolecules smaller than 0.1μm and larger than about 2nm are
rejected 0.1μm〜2nmの範囲の粒子や高分子が阻止される圧力駆動の膜分離プロセス。 |
Electrically Mediated Separations電気利用分離 | ||
76. | anion-exchange
membrane: 陰イオン交換膜: |
membrane containing
fixed cationic charges and mobile anions that can be
exchanged with other anions present in an external fluid
in contact with the
membrane 固定陽イオン電荷と可動陰イオンを膜中に持ち、外部流体中のほかの陰イオンと交換可能な膜。 |
77. | bipolar membrane:
両極膜: |
synthetic membrane
containing two oppositely charged ion-exchanging layers in contact
with each other ふたつの反対の荷電をもつイオン交換層を交互に重ねた合成膜。 |
78. | cation-exchange
membrane: 陽イオン交換膜: |
membrane containing
fixed anionic charges and mobile cations which can be
exchanged with the other cations present in an external
fluid in contact with
the membrane 固定陰イオン電荷と可動陽イオンを膜中に持ち、外部流体中のほかの陽イオンと交換可能な膜。 |
79. | charge-mosaic
membranes: モザイク荷電膜: |
synthetic membrane
composed of two-dimensional or three-dimensional alternating
cation- and anion-exchange channels throughout the
membrane 2次元または3次元的に交互に陰イオン交換・陽イオン交換チャネルから形成された合成膜。 |
80. | Donnan exclusion:
ドナン阻止: |
reduction in
concentration of mobile ions within an ion exchange membrane due to the
presence of fixed ions of the same sign as the mobile
ions イオン交換膜の内部で同種の固定イオンの存在により、可動イオンの濃度が減少すること。 |
81. | electro-dialysis: 電気透析: |
membrane-based
separation process in which ions are driven through an ion-selective membrane
under the influence of an electric field イオンを電場によりイオン選択性膜中を透過させる膜分離プロセス。 |
82. | electro-osmosis: 電気浸透: |
process by which water
is transported across the thickness of an anion-exchange(76) or
cation-exchange membrane(78) under an applied
electricfield 電場により陰イオンまたは陽イオン交換膜中を水が移動するプロセス。 |
83. | limiting current
density: 限界電流密度: |
current density at which
dramatic increases in resistance
are observed in an ion exchange membrane system under the
influence of an applied
electric field between the upstream and downstream イオン交換膜を介して電場をかけた場合、抵抗が急に増加する電流密度。 |
Gas, Vapor and Pervaporation Separationsガス、蒸気、パーベーパレーション 分離 | ||
84. | ideal separation
factor: 理想分離係数: |
parameter defined as the
ratio of the permeability coefficient of component A to that
of component B and equal to the "separation
factor" (37)
where a perfect vacuum exists at the downstream membrane
face for gas and vapor
permeation systems A成分とB成分の透過係数の比で定義されるパラメータ。気体・蒸気透過では膜の下流側が真空の場合の分離係数に等しい。 |
85. | pervaporation: パーベーパレーション: |
membrane based process
in which the feed and retentate streams are both liquid phases
while permeant emerges at the downstream face of the
membrane as a vapor 供給と非透過流れが液で、膜の下流側への透過物が蒸気である膜分離プロセス。 |
86. | solution-diffusion(sorption-diffusion):
溶解-拡散(収着-拡散): |
molecular-scale process
in which penetrant is
sorbed into the upstream membrane face from the external
phase, moves by molecular
diffusion in the membrane to the downstream face and
leaves into the external
gas, vapor or liquid phase in contact with the membrane
透過物が外部相から膜の上流表面に溶解し、下流方向に膜内を分子拡散により移動し、膜内から膜に接するガス・蒸気・液相へ移動する分子スケールのプロセス。 |
87. | sweep: スイープ: |
nonpermeating stream
directed past the downstream membrane face to reduce downstream permeant
concentration 下流側の透過物の濃度を下げるために膜下流面を横切る方向に流す非透過流れ。 |
Reverse Osmosis Separations 逆浸透分離 | ||
88. | brackish water: カン水: |
term used to indicate
water having a total dissolved-solids content that is less than that of
sea water but above that of potable water 全溶存固体量が海水以下、飲料水以上の水。 |
89. | feed pretreatment: 前処理: |
process carried out on a
crude feed stream, prior to feeding to a membrane separation system,
to eliminate objectionable components such as biological agents and colloids
that might impede the stable operation of membrane 膜分離装置に供給する前に、原水から膜操作を妨げる生物やコロイドなどの成分を除くための処理。 |
90. | permeate
post-treatment: 透過物の後処理: |
one or more final
conditioning steps to improve permeate quality, e.g., contacting
with anion exchange resins to remove trace ions in the
permeate of a reverse
osmosis product stream 透過物の品質を上げるための最終処理。逆浸透透過物中の微量イオンを除去するためにオン交換樹脂と接触させる操作がその例。 |
91. | potable water: 飲料水: |
term used to indicate
water having a total dissolved solids content of less than 500 ppm with
a sufficiently low level of biological agents, suspended solids, organic odour-
and colour-generating components to be safe and palatable for drinking 飲用として安全でおいしい水のこと。有機物・懸濁固体・臭いや色の成分が十分に低い濃度であり、全溶解固体量が500ppm以下であること。 |
92. | reverse osmosis: 逆浸透: |
liquid-phase
pressure-driven separation process in which applied transmembrane pressure
causes selective movement of solvent against its osmotic pressure difference 膜片側の加圧により浸透圧差と逆方向の溶媒の選択的移動が引き起こされる液相の圧力駆動分離プロセス。 |