JPH04256437A - Pyrogen adsorbent - Google Patents
Pyrogen adsorbentInfo
- Publication number
- JPH04256437A JPH04256437A JP3103226A JP10322691A JPH04256437A JP H04256437 A JPH04256437 A JP H04256437A JP 3103226 A JP3103226 A JP 3103226A JP 10322691 A JP10322691 A JP 10322691A JP H04256437 A JPH04256437 A JP H04256437A
- Authority
- JP
- Japan
- Prior art keywords
- adsorbent
- acid
- pyrogen
- aliphatic hydrocarbon
- hydrocarbon group
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
- 239000003463 adsorbent Substances 0.000 title claims abstract description 26
- 239000002510 pyrogen Substances 0.000 title claims abstract description 20
- 125000001931 aliphatic group Chemical group 0.000 claims abstract description 15
- 239000002253 acid Substances 0.000 claims abstract description 13
- 229920002307 Dextran Polymers 0.000 claims abstract description 8
- 239000011148 porous material Substances 0.000 claims abstract description 7
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 claims description 8
- 229920000805 Polyaspartic acid Polymers 0.000 claims description 2
- 108010020346 Polyglutamic Acid Proteins 0.000 claims description 2
- 108010064470 polyaspartate Proteins 0.000 claims description 2
- 229920002643 polyglutamic acid Polymers 0.000 claims description 2
- 239000000126 substance Substances 0.000 abstract description 14
- CKLJMWTZIZZHCS-REOHCLBHSA-N L-aspartic acid Chemical compound OC(=O)[C@@H](N)CC(O)=O CKLJMWTZIZZHCS-REOHCLBHSA-N 0.000 abstract description 6
- WHUUTDBJXJRKMK-VKHMYHEASA-N L-glutamic acid Chemical compound OC(=O)[C@@H](N)CCC(O)=O WHUUTDBJXJRKMK-VKHMYHEASA-N 0.000 abstract description 6
- 235000003704 aspartic acid Nutrition 0.000 abstract description 6
- OQFSQFPPLPISGP-UHFFFAOYSA-N beta-carboxyaspartic acid Natural products OC(=O)C(N)C(C(O)=O)C(O)=O OQFSQFPPLPISGP-UHFFFAOYSA-N 0.000 abstract description 6
- WHUUTDBJXJRKMK-UHFFFAOYSA-N Glutamic acid Natural products OC(=O)C(N)CCC(O)=O WHUUTDBJXJRKMK-UHFFFAOYSA-N 0.000 abstract description 5
- 235000013922 glutamic acid Nutrition 0.000 abstract description 5
- 239000004220 glutamic acid Substances 0.000 abstract description 5
- 239000007924 injection Substances 0.000 abstract description 5
- 238000002347 injection Methods 0.000 abstract description 5
- 238000000034 method Methods 0.000 abstract description 5
- 238000000502 dialysis Methods 0.000 abstract description 3
- 206010037660 Pyrexia Diseases 0.000 abstract 1
- 230000027950 fever generation Effects 0.000 abstract 1
- 238000001179 sorption measurement Methods 0.000 description 14
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 12
- 239000002158 endotoxin Substances 0.000 description 8
- 238000006116 polymerization reaction Methods 0.000 description 7
- 239000000243 solution Substances 0.000 description 7
- 238000005227 gel permeation chromatography Methods 0.000 description 5
- 229920006008 lipopolysaccharide Polymers 0.000 description 5
- 239000002245 particle Substances 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 5
- 125000000217 alkyl group Chemical group 0.000 description 4
- 239000012153 distilled water Substances 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- ZSIAUFGUXNUGDI-UHFFFAOYSA-N hexan-1-ol Chemical compound CCCCCCO ZSIAUFGUXNUGDI-UHFFFAOYSA-N 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000005259 measurement Methods 0.000 description 4
- 150000004702 methyl esters Chemical class 0.000 description 4
- 229910001220 stainless steel Inorganic materials 0.000 description 4
- 239000010935 stainless steel Substances 0.000 description 4
- 102000009027 Albumins Human genes 0.000 description 3
- 108010088751 Albumins Proteins 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 3
- ZMANZCXQSJIPKH-UHFFFAOYSA-N Triethylamine Chemical compound CCN(CC)CC ZMANZCXQSJIPKH-UHFFFAOYSA-N 0.000 description 3
- 235000001014 amino acid Nutrition 0.000 description 3
- 229940024606 amino acid Drugs 0.000 description 3
- 150000001413 amino acids Chemical class 0.000 description 3
- 239000011324 bead Substances 0.000 description 3
- 125000001165 hydrophobic group Chemical group 0.000 description 3
- 235000018102 proteins Nutrition 0.000 description 3
- 102000004169 proteins and genes Human genes 0.000 description 3
- 108090000623 proteins and genes Proteins 0.000 description 3
- 150000003839 salts Chemical class 0.000 description 3
- 239000012798 spherical particle Substances 0.000 description 3
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 description 2
- 241000588724 Escherichia coli Species 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 2
- ZGEYCCHDTIDZAE-BYPYZUCNSA-N L-glutamic acid 5-methyl ester Chemical compound COC(=O)CC[C@H](N)C(O)=O ZGEYCCHDTIDZAE-BYPYZUCNSA-N 0.000 description 2
- 239000004372 Polyvinyl alcohol Substances 0.000 description 2
- 239000000969 carrier Substances 0.000 description 2
- 239000000385 dialysis solution Substances 0.000 description 2
- JRBPAEWTRLWTQC-UHFFFAOYSA-N dodecylamine Chemical compound CCCCCCCCCCCCN JRBPAEWTRLWTQC-UHFFFAOYSA-N 0.000 description 2
- 238000000921 elemental analysis Methods 0.000 description 2
- 238000010828 elution Methods 0.000 description 2
- 230000007717 exclusion Effects 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 230000020169 heat generation Effects 0.000 description 2
- 230000002209 hydrophobic effect Effects 0.000 description 2
- 238000001802 infusion Methods 0.000 description 2
- -1 infusions Substances 0.000 description 2
- 238000004811 liquid chromatography Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229920002451 polyvinyl alcohol Polymers 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- JOXIMZWYDAKGHI-UHFFFAOYSA-N toluene-4-sulfonic acid Chemical compound CC1=CC=C(S(O)(=O)=O)C=C1 JOXIMZWYDAKGHI-UHFFFAOYSA-N 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- BMVXCPBXGZKUPN-UHFFFAOYSA-N 1-hexanamine Chemical compound CCCCCCN BMVXCPBXGZKUPN-UHFFFAOYSA-N 0.000 description 1
- 125000003903 2-propenyl group Chemical group [H]C([*])([H])C([H])=C([H])[H] 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- ROHFNLRQFUQHCH-YFKPBYRVSA-N L-leucine Chemical compound CC(C)C[C@H](N)C(O)=O ROHFNLRQFUQHCH-YFKPBYRVSA-N 0.000 description 1
- COLNVLDHVKWLRT-QMMMGPOBSA-N L-phenylalanine Chemical compound OC(=O)[C@@H](N)CC1=CC=CC=C1 COLNVLDHVKWLRT-QMMMGPOBSA-N 0.000 description 1
- ROHFNLRQFUQHCH-UHFFFAOYSA-N Leucine Natural products CC(C)CC(N)C(O)=O ROHFNLRQFUQHCH-UHFFFAOYSA-N 0.000 description 1
- 241000239218 Limulus Species 0.000 description 1
- YGYAWVDWMABLBF-UHFFFAOYSA-N Phosgene Chemical compound ClC(Cl)=O YGYAWVDWMABLBF-UHFFFAOYSA-N 0.000 description 1
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical group OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 1
- 239000002202 Polyethylene glycol Substances 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 239000003377 acid catalyst Substances 0.000 description 1
- 125000003342 alkenyl group Chemical group 0.000 description 1
- 125000000304 alkynyl group Chemical group 0.000 description 1
- 150000003862 amino acid derivatives Chemical class 0.000 description 1
- 125000000539 amino acid group Chemical group 0.000 description 1
- 125000003277 amino group Chemical group 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 125000004432 carbon atom Chemical group C* 0.000 description 1
- 210000002421 cell wall Anatomy 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 238000011981 development test Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- LQZZUXJYWNFBMV-UHFFFAOYSA-N dodecan-1-ol Chemical compound CCCCCCCCCCCCO LQZZUXJYWNFBMV-UHFFFAOYSA-N 0.000 description 1
- ILRSCQWREDREME-UHFFFAOYSA-N dodecanamide Chemical group CCCCCCCCCCCC(N)=O ILRSCQWREDREME-UHFFFAOYSA-N 0.000 description 1
- 125000003438 dodecyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 239000003480 eluent Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000032050 esterification Effects 0.000 description 1
- 238000005886 esterification reaction Methods 0.000 description 1
- 125000001495 ethyl group Chemical group [H]C([H])([H])C([H])([H])* 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 102000034238 globular proteins Human genes 0.000 description 1
- 108091005896 globular proteins Proteins 0.000 description 1
- 125000004051 hexyl group Chemical group [H]C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])* 0.000 description 1
- 239000012510 hollow fiber Substances 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000003456 ion exchange resin Substances 0.000 description 1
- 229920003303 ion-exchange polymer Polymers 0.000 description 1
- 150000002500 ions Chemical class 0.000 description 1
- 125000000959 isobutyl group Chemical group [H]C([H])([H])C([H])(C([H])([H])[H])C([H])([H])* 0.000 description 1
- 125000004491 isohexyl group Chemical group C(CCC(C)C)* 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 125000002496 methyl group Chemical group [H]C([H])([H])* 0.000 description 1
- IOQPZZOEVPZRBK-UHFFFAOYSA-N octan-1-amine Chemical compound CCCCCCCCN IOQPZZOEVPZRBK-UHFFFAOYSA-N 0.000 description 1
- COLNVLDHVKWLRT-UHFFFAOYSA-N phenylalanine Natural products OC(=O)C(N)CC1=CC=CC=C1 COLNVLDHVKWLRT-UHFFFAOYSA-N 0.000 description 1
- 229920001308 poly(aminoacid) Polymers 0.000 description 1
- 229920001223 polyethylene glycol Polymers 0.000 description 1
- 229920000642 polymer Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 150000003141 primary amines Chemical class 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 235000000346 sugar Nutrition 0.000 description 1
- 150000008163 sugars Chemical class 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 238000005809 transesterification reaction Methods 0.000 description 1
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は、注射、人口透析等によ
り生体内に投与または溶出混入された場合に発熱を誘発
する物質、即ち発熱物質(パイロジェン)の除去に有効
な吸着剤に関する。さらに詳しくは、注射液、輸液、透
析液等に混入している発熱物質の吸着除去剤に関するも
のである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an adsorbent effective for removing a pyrogen, a substance that induces heat generation when administered or eluted into a living body by injection, artificial dialysis, etc. More specifically, the present invention relates to an adsorption/removal agent for pyrogens contained in injection solutions, infusions, dialysates, and the like.
【0002】0002
【従来の技術】現在発熱物質として問題になっているの
は、大腸菌等のグラム陰性細菌の細胞壁由来のリポポリ
サッカライド(LPS)であることがわかっている。発
熱物質の除去に関しては種々の研究がなされており、活
性炭、イオン交換樹脂、各種分離膜による除去が試みら
れているが未だ実用の域には達していない。即ちこれら
の吸着剤ではパイロジェンの選択性が低く、また吸着除
去量も満足のいく値は得られていない。さらに吸着剤の
合成過程の不純物溶出の問題もあって実際に用いること
はできないのが現状である。BACKGROUND OF THE INVENTION It has been found that lipopolysaccharide (LPS), which is derived from the cell walls of Gram-negative bacteria such as Escherichia coli, is currently a problematic pyrogen. Various studies have been conducted regarding the removal of pyrogens, and attempts have been made to remove them using activated carbon, ion exchange resins, and various separation membranes, but they have not yet reached the level of practical use. That is, these adsorbents have low selectivity for pyrogen, and a satisfactory amount of adsorption and removal cannot be obtained. Furthermore, there is also the problem of impurity elution during the adsorbent synthesis process, so it is currently impossible to use it in practice.
【0003】0003
【発明の解決しようとする課題】注射、人工透析等によ
り生体内に投与または溶出混入された場合に発熱を誘発
する物質(パイロジエン)が効率的に除去することを目
的とする。OBJECTS OF THE INVENTION It is an object of the present invention to efficiently remove a substance (pyrogiene) that induces heat generation when administered or eluted into a living body by injection, artificial dialysis, etc.
【0004】0004
【課題を解決するための手段】本発明者らは、ポリアミ
ノ酸骨格が生体親和性に優れ、吸着系に存在する生理活
性蛋白質、糖類を変性させにくいことを見いだし鋭意研
究した結果、LPSが糖鎖の他に燐酸基と疎水基を有し
ておりイオン的な吸着、疎水的な吸着の双方が可能であ
ること、イオン的な吸着は吸着系の共存イオン、pHに
大きく影響され吸着できる条件範囲が狭いこと、疎水性
吸着の場合はこれらの影響が小さく、むしろ高イオン強
度下でもよく吸着できること、疎水性基の中でも長鎖ア
ルキル基がLPS吸着性能に優れ他の共存物質の非特異
的な吸着が少ないことまた共存物質の回収率を高めるた
めには共存物質が拡散できるような細孔をなくする方が
よいことを見いだし本発明を完成するに至った。[Means for Solving the Problems] The present inventors discovered that the polyamino acid skeleton has excellent biocompatibility and is difficult to denature physiologically active proteins and sugars present in the adsorption system.As a result of intensive research, we found that LPS In addition to the chain, it has a phosphoric acid group and a hydrophobic group, so both ionic adsorption and hydrophobic adsorption are possible.Ionic adsorption is greatly influenced by the coexisting ions and pH of the adsorption system, and the conditions for adsorption. In the case of hydrophobic adsorption, these effects are small, and in fact, it can be adsorbed well even under high ionic strength. Among hydrophobic groups, long-chain alkyl groups have excellent LPS adsorption performance and are non-specific for other coexisting substances. The present inventors have completed the present invention by discovering that there is less adsorption and that in order to increase the recovery rate of coexisting substances, it is better to eliminate pores through which coexisting substances can diffuse.
【0005】即ち本発明は側鎖に長鎖脂肪族炭化水素基
が結合していることを特徴とするポリグルタミン酸また
はポリアスパラギン酸のうち少なくとも1種を含むポリ
アミノ酸で構成される吸着剤の細孔径がデキストランの
分子量にして1000以下で実質的に無孔質である発熱
物質吸着剤を提供するものである。この長鎖脂族炭化水
素基は、例えば、アミド結合、又はエステル結合で該ポ
リアミノ酸の−(CH2 )m −COOH(m=1
又は2)側鎖のカルボキシル部位に結合することができ
る。That is, the present invention provides an adsorbent material comprising a polyamino acid containing at least one of polyglutamic acid and polyaspartic acid, which is characterized in that a long-chain aliphatic hydrocarbon group is bonded to the side chain. The object of the present invention is to provide a pyrogen adsorbent that is substantially non-porous and has a pore size of 1000 or less based on the molecular weight of dextran. This long-chain aliphatic hydrocarbon group is, for example, an amide bond or an ester bond of the polyamino acid -(CH2)m-COOH (m=1
or 2) can be attached to the carboxyl site of the side chain.
【0006】本発明におけるポリアミノ酸とは、グルタ
ミン酸、アスパラギン酸の側鎖に長鎖脂肪族炭化水素基
が結合した誘導体の1種または2種を重合したものであ
り、これらのアミノ酸誘導体を含むものであれば他のア
ミノ酸との共重合体でもよい。[0006] The polyamino acid in the present invention is a polymerized product of one or two derivatives of glutamic acid or aspartic acid in which a long-chain aliphatic hydrocarbon group is bonded to the side chain, and a polyamino acid containing these amino acid derivatives. If so, it may be a copolymer with other amino acids.
【0007】また長鎖脂肪族炭化水素基の導入は重合し
た後に行ってもよい。本発明における長鎖脂肪族炭化水
素基とは飽和又は不飽和長鎖脂肪族炭化水素基であって
、例示すると、アルキル基、例えば、エチル基、ヘキシ
ル基、ラウリル基等の直鎖アルキル基、イソブチル基、
イソヘキシル基等の分岐を有するアルキル基、アルケニ
ル基、例えば、アリル基等の不飽和基のうち炭素数が2
以上、好ましくは4以上、更に好ましくは6以上有する
基、更にはアルキニル基などである。[0007] Furthermore, the long-chain aliphatic hydrocarbon group may be introduced after polymerization. The long-chain aliphatic hydrocarbon group in the present invention refers to a saturated or unsaturated long-chain aliphatic hydrocarbon group, and examples thereof include alkyl groups such as straight-chain alkyl groups such as ethyl group, hexyl group, and lauryl group; isobutyl group,
A branched alkyl group such as an isohexyl group, an alkenyl group, an unsaturated group such as an allyl group having 2 carbon atoms
The above-mentioned groups preferably have 4 or more, more preferably 6 or more, and further include alkynyl groups.
【0008】これら長鎖脂肪族炭化水素基の含有量は該
ポリアミノ酸を構成するアミノ酸残基のうち1%以上好
ましくは5%以上、更に好ましくは10%以上である。The content of these long-chain aliphatic hydrocarbon groups is 1% or more, preferably 5% or more, and more preferably 10% or more of the amino acid residues constituting the polyamino acid.
【0009】これらの長鎖脂肪族炭化水素基を前述のポ
リアミノ酸に導入する方法はグルタミン酸またはアスパ
ラギン酸と長鎖脂肪族炭化水素基を有するアルコール例
えばヘキサノール、ラウリルアルコールとを酸触媒の存
在下でエステル結合させた後重合を行う方法、あるいは
グルタミン酸またはアスパラギン酸をメタノールによっ
てメチルエステル化した後重合を行い、更にパラトルエ
ンスルホン酸を用いて長鎖脂肪族炭化水素基を有するア
ルコールとエステル交換によって導入することができる
。また、長鎖脂肪族炭化水素基を有する一級アミン例え
ばモノヘキシルアミン、オクチルアミン、ラウリルアミ
ン等をグルタミン酸またはアスパラギン酸のメチルエス
テルと加熱反応させることによりアミド結合で導入でき
る。A method for introducing these long-chain aliphatic hydrocarbon groups into the above-mentioned polyamino acids is to combine glutamic acid or aspartic acid with an alcohol having a long-chain aliphatic hydrocarbon group, such as hexanol or lauryl alcohol, in the presence of an acid catalyst. A method of ester bonding followed by polymerization, or methyl esterification of glutamic acid or aspartic acid with methanol followed by polymerization, followed by transesterification with an alcohol having a long chain aliphatic hydrocarbon group using para-toluenesulfonic acid. can do. Furthermore, an amide bond can be introduced by reacting a primary amine having a long-chain aliphatic hydrocarbon group, such as monohexylamine, octylamine, laurylamine, etc., with methyl ester of glutamic acid or aspartic acid.
【0010】グルタミン酸及びアスパラギン酸の重合は
γ位あるいはβ位のカルボキシル基をメチルエステル等
の誘導体にして保護し、ホスゲンを反応させてNCA(
N−カルボキシ−α−アミノ酸無水物)を生成させた後
トリエチルアミン等によって重合することができる。
またこの時他のアミノ酸例えばロイシン、フェニルアラ
ニン等のNCAと共重合することもできる。In the polymerization of glutamic acid and aspartic acid, the carboxyl group at the γ or β position is protected with a derivative such as methyl ester, and phosgene is reacted to form NCA (
After producing N-carboxy-α-amino acid anhydride), it can be polymerized using triethylamine or the like. At this time, it can also be copolymerized with other amino acids such as NCA such as leucine and phenylalanine.
【0011】本発明でいう吸着剤の形状は、前述のアミ
ノ基とカルボキシル基を含有するポリアミノ酸自身を膜
化しても良いし、繊維化したものでも良いし、ビーズ化
したものでもよい。また、各種担体上にコーティングさ
せても良い。これらに用いられる担体は、ガラス、金属
塩類、炭素等の無機物質でも良いし、ポリマー等の有機
物質であってもよい。また、これらの担体の形状も、粉
状、ビーズ状、膜状、繊維状、中空糸状、等いろいろな
形状のものが利用できるが、吸着カラム、吸着カートリ
ッジ等のモジュールに合わせて選ぶことが出来る。[0011] The shape of the adsorbent according to the present invention may be such that the polyamino acid containing an amino group and a carboxyl group described above may be formed into a film, a fiber, or a bead. Moreover, it may be coated on various carriers. The carrier used for these may be an inorganic substance such as glass, metal salts, or carbon, or an organic substance such as a polymer. In addition, various shapes of these carriers can be used, such as powder, beads, membranes, fibers, and hollow fibers, and they can be selected according to the module such as the adsorption column or adsorption cartridge. .
【0012】本発明における吸着剤の細孔径はデキスト
ランの分子量換算で1000以下で実質的に無孔質であ
ることが必要である。吸着剤の細孔径はデキストラン標
準分子量物質によるゲルパーミエーションクロマトグラ
フィー(GPC)によって評価できる。すなわち、吸着
剤を適当な方法でふるい分け、液体クロマトグラフィー
用のステンレスカラムに充填する。孔径評価用のビーズ
は100μm以下のもので、できるだけ均一サイズが好
ましい。ステンレスカラムのサイズは、通常市販されて
いる(例えば日本精密(株)社製4.6mmφ*150
mm)カラムで充分である。GPC測定を行を標準分子
量物質は、できるだけ該吸着剤との相互作用が無いもの
が好ましく、デキストラン標準分子量物質(シグマケミ
カル社製)が適当と考えられる。その他の標準分子量物
質、例えば球状タンパク質、ポリエチレングリコール等
は、必ずしも分子量の順番に溶出しなかったり、吸着さ
れてしまうことがあり適当でない。測定方法は、標準分
子量デキストランを用いた通常の水系GPC測定でよい
。即ち、蒸留水を溶離液として、液体クロマトグラフィ
ー装置により種々の分子量のデキストランの溶出容量を
測定するものである。[0012] The pore diameter of the adsorbent used in the present invention is required to be 1000 or less in terms of the molecular weight of dextran, and it is required to be substantially non-porous. The pore size of the adsorbent can be evaluated by gel permeation chromatography (GPC) using dextran standard molecular weight substances. That is, the adsorbent is sieved by an appropriate method and packed into a stainless steel column for liquid chromatography. The beads for pore size evaluation are preferably 100 μm or less, and are preferably as uniform in size as possible. The size of the stainless steel column is usually commercially available (for example, 4.6 mmφ*150 manufactured by Nippon Seimitsu Co., Ltd.
mm) column is sufficient. The standard molecular weight substance used for GPC measurement is preferably one that has as little interaction as possible with the adsorbent, and dextran standard molecular weight substance (manufactured by Sigma Chemical Co.) is considered suitable. Other standard molecular weight substances, such as globular proteins and polyethylene glycol, are not suitable because they do not necessarily elute in the order of molecular weight or are adsorbed. The measurement method may be normal aqueous GPC measurement using standard molecular weight dextran. That is, the elution capacity of dextran of various molecular weights is measured using a liquid chromatography device using distilled water as an eluent.
【0013】[0013]
【作用】本発明により、注射液、透析液、輸液、培養薬
品等に含まれる発熱物質の吸着技術が確立された。その
メカニズムは明かではないが、吸着剤の有する疎水基に
よってpHやイオン強度の影響によらず発熱物質が効率
的に吸着され、さらに吸着剤を実質的に無孔質にするこ
とにより他の共存タンパク質等の吸着剤内部への拡散を
制御できるものと考えられる。[Operation] According to the present invention, a technology for adsorbing pyrogens contained in injection solutions, dialysates, infusions, culture chemicals, etc. has been established. Although the mechanism is not clear, pyrogens are efficiently adsorbed by the hydrophobic group of the adsorbent regardless of the effects of pH or ionic strength, and by making the adsorbent substantially non-porous, other coexistence substances can be absorbed. It is thought that the diffusion of proteins etc. into the interior of the adsorbent can be controlled.
【0014】[0014]
【発明の効果】本発明の発熱物質吸着剤は、(1)発熱
物質以外の塩類、アミノ酸、有用タンパク質を吸着する
ことなく選択性が高い(2)広いpH、イオン強度範囲
で発熱物質の吸着量及び吸着速度が大きい(3)吸着剤
は生体適合性を有するなどの優れた効果を奏する。Effects of the Invention The pyrogen adsorbent of the present invention (1) has high selectivity without adsorbing salts other than pyrogens, amino acids, and useful proteins; (2) adsorbs pyrogens over a wide pH and ionic strength range; The adsorbent (3) with a large amount and adsorption rate exhibits excellent effects such as biocompatibility.
【0015】[0015]
【実施例】以下実施例にしたがって、本発明をさらに詳
しく説明するが、本発明は、これら実施例に限られるも
のではない。なお発熱物質の定量測定は生化学工業社(
株式会社)製エンドトキシン定量試薬キットによるリム
ルス発色テストを行った。
製造例1
平均重合度500のポリ−γ−メチル−L−グルタメー
ト(以下PMLG)の2.5%ジクロルエタン溶液25
0g中を、部分鹸化ポリビニルアルコール2.5%水溶
液500ml中に撹拌分散しながら50℃でジクロルエ
タンを蒸発除去する。得られたポリアミノ酸球状粒子を
濾過し、温水で充分洗浄して、完全にポリビニルアルコ
ールを除去する。この球状粒子を分級して、37〜74
μmのものを取り出し、ステンレスカラムに充填して、
GPC測定を行った。その結果、排除限界分子量は約5
00であった。更にこのポリアミノ酸球状粒子3gをメ
タノール中に分散し12gヘキサノール及び1.5gの
パラトルエンスルホン酸を加えて60℃で5時間反応さ
せた後蒸留水で十分洗浄した。得られた粒子の一部を乾
燥して元素分析を行ったところ下表の通りであった。こ
の結果よりメチルエステル部分のうち約35%がヘキシ
ルエステルに置換されていることが解った。EXAMPLES The present invention will be explained in more detail with reference to Examples below, but the present invention is not limited to these Examples. The quantitative measurement of pyrogens was conducted by Seikagaku Kogyo Co., Ltd. (
A limulus color development test was conducted using an endotoxin quantitative reagent kit manufactured by Co., Ltd.). Production Example 1 2.5% dichloroethane solution of poly-γ-methyl-L-glutamate (hereinafter referred to as PMLG) with an average degree of polymerization of 500 25
Dichloroethane was removed by evaporation at 50° C. while stirring and dispersing 0 g of the solution in 500 ml of a 2.5% aqueous solution of partially saponified polyvinyl alcohol. The obtained polyamino acid spherical particles are filtered and thoroughly washed with warm water to completely remove polyvinyl alcohol. This spherical particle was classified and 37 to 74
Take out the μm one and fill it into a stainless steel column.
GPC measurement was performed. As a result, the exclusion limit molecular weight was approximately 5
It was 00. Further, 3 g of the polyamino acid spherical particles were dispersed in methanol, 12 g of hexanol and 1.5 g of para-toluenesulfonic acid were added, and the mixture was reacted at 60° C. for 5 hours, followed by thorough washing with distilled water. A part of the obtained particles was dried and subjected to elemental analysis, and the results were as shown in the table below. From this result, it was found that about 35% of the methyl ester moiety was substituted with hexyl ester.
【0016】製造例2
製造例1において、平均重合度500のポリ−γ−メチ
ル−L−グルタメートの代わりに平均重合度450のポ
リ−βーメチル−L−アスパルテートを用いた他は製造
例1と全く同様な方法で粒子を製造した。得られた粒子
の排除限界分子量は1000であった。この粒子3gを
メタノール中に分散してラウリルアミン15gを添加し
て撹拌しながら60℃7時間反応させた後メタノール及
び蒸留水で十分洗浄した。得られた粒子の一部を乾燥し
て元素分析を行ったところ下表の通りであった。この結
果よりメチルエステル部分のうち約40%がラウリルア
ミドに置換されていることが解った。Production Example 2 Production Example 1 was repeated except that poly-β-methyl-L-aspartate with an average degree of polymerization of 450 was used instead of poly-γ-methyl-L-glutamate with an average degree of polymerization of 500. Particles were produced in exactly the same manner. The exclusion limit molecular weight of the obtained particles was 1000. 3 g of these particles were dispersed in methanol, 15 g of laurylamine was added, and the mixture was reacted with stirring at 60° C. for 7 hours, followed by thorough washing with methanol and distilled water. A part of the obtained particles was dried and subjected to elemental analysis, and the results were as shown in the table below. From this result, it was found that about 40% of the methyl ester moiety was substituted with laurylamide.
【0017】実施例
製造例1及び2で得られた吸着剤それぞれ1gを、ステ
ンレスカラム(内径4.5mm、長さ150mm)に充
填し1mol食塩水150mlを0.5ml/minで
通液したのち発熱物質の含まれない蒸留水で完全に食塩
を洗浄する、その後大腸菌由来のエンドトキシン(生化
学工業社(株)製LPSコントロールE、coli
055−B5)1510ng/mlに調整したアルブミ
ン溶液(アルブミン濃度25mg/ml pH=5.
6)250mlを、流速0.5ml/minで通液しカ
ラム出口より捕集した溶液中に含まれるエンドトキシン
濃度およびアルブミン回収率を定量した。Example 1 g of each of the adsorbents obtained in Production Examples 1 and 2 was packed into a stainless steel column (inner diameter 4.5 mm, length 150 mm), and 150 ml of 1 mol saline solution was passed through the column at a rate of 0.5 ml/min. Thoroughly wash off the salt with pyrogen-free distilled water, then remove endotoxin derived from Escherichia coli (LPS Control E, manufactured by Seikagaku Corporation).
055-B5) Albumin solution adjusted to 1510 ng/ml (albumin concentration 25 mg/ml pH = 5.
6) 250 ml of the solution was passed through the column at a flow rate of 0.5 ml/min, and the endotoxin concentration and albumin recovery rate contained in the solution collected from the column outlet were quantified.
Claims (3)
ていることを特徴とするポリグルタミン酸またはポリア
スパラギン酸のうち少なくとも1種を含むポリアミノ酸
で構成される吸着剤の細孔径がデキストランの分子量に
して1000以下で実質的に無孔質である発熱物質吸着
剤。Claim 1: An adsorbent comprising a polyamino acid containing at least one of polyglutamic acid and polyaspartic acid, characterized in that a long-chain aliphatic hydrocarbon group is bonded to the side chain, has a pore diameter of A pyrogen adsorbent having a molecular weight of dextran of 1000 or less and being substantially non-porous.
該ポリアミノ酸の−(CH2 ) m −COOH(m
=1又は2)側鎖のカルボキシル部位に結合しているこ
とを特徴とする請求項1記載の発熱物質吸着剤。2. The long-chain aliphatic hydrocarbon group is an amide bond, and the polyamino acid has -(CH2) m -COOH(m
=1 or 2) The pyrogen adsorbent according to claim 1, wherein the pyrogen adsorbent is bonded to a carboxyl site of a side chain.
でポリアミノ酸の−(CH2 ) m −COOH(m
=1又は2)側鎖のカルボキシル部位に結合しているこ
とを特徴とする請求項1記載の発熱物質吸着剤。3. The long-chain aliphatic hydrocarbon group is an ester bond of the polyamino acid -(CH2) m -COOH(m
=1 or 2) The pyrogen adsorbent according to claim 1, wherein the pyrogen adsorbent is bonded to a carboxyl site of a side chain.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3103226A JPH04256437A (en) | 1991-02-06 | 1991-02-06 | Pyrogen adsorbent |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3103226A JPH04256437A (en) | 1991-02-06 | 1991-02-06 | Pyrogen adsorbent |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04256437A true JPH04256437A (en) | 1992-09-11 |
Family
ID=14348568
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3103226A Pending JPH04256437A (en) | 1991-02-06 | 1991-02-06 | Pyrogen adsorbent |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04256437A (en) |
-
1991
- 1991-02-06 JP JP3103226A patent/JPH04256437A/en active Pending
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US4747956A (en) | Method of adsorbing subtances | |
Garipcan et al. | A novel affinity support material for the separation of immunoglobulin G from human plasma | |
EP1220868B1 (en) | Extracorporeal endotoxin removal method | |
US20020130082A1 (en) | Endotoxin adsorbent, and a method of removing endotoxin by using the same | |
CA1223859A (en) | Surface-grafted particulate support, process for its preparation and adsorbants for affinity chromatography incorporating such support, and their use, particularly in biology | |
JPH0144725B2 (en) | ||
WO2001074420A1 (en) | Adsorbents for high mobility group proteins and column for purifying body fluid | |
JPH0427504B2 (en) | ||
Wu et al. | Adsorption of bilirubin by amine-containing polyacrylamide resins | |
US9505850B2 (en) | Endotoxin adsorbent | |
JP3748927B2 (en) | Glycolipid antibody adsorbent | |
JPH04256437A (en) | Pyrogen adsorbent | |
JP4606524B2 (en) | Polylysine, polylysine production method, polylysine composition, and pharmaceutical production method for removing endotoxin | |
RU2641924C1 (en) | Sorption material, method of its production and method of its application | |
JPH04256438A (en) | Pyrogen adsorbent | |
Jin et al. | Novel method for human serum albumin adsorption/separation from aqueous solutions and human plasma with Cibacron Blue F3GA-Zn (II) attached microporous affinity membranous capillaries | |
JPH02209155A (en) | Porous adsorbent for beta2-microglobulin | |
JPWO2015056680A1 (en) | Method for producing porous cellulose beads | |
JPH04256441A (en) | Adsorbent for beta2-microglobulin | |
EP0611592A2 (en) | Membranes for use in affinity separation and methods for activating membranes | |
JPH04156943A (en) | Pyrogen adsorbent | |
SU1186243A1 (en) | Method of obtaining adsorbent for affine chromatography | |
Narinesingh et al. | Activation of supports containing hydroxyl groups using bis (4-nitrophenyl) carbonate | |
RU2040274C1 (en) | METHOD FOR PRODUCTION OF IMMUNOSORBENT FOR BINDING α- GROUP SPECIFIC AND β-AGGLUTININES | |
JPH04256434A (en) | Pyrogen adsorbent |