JPH02147857A - Spherical carrier for chromatography separation and production thereof - Google Patents
Spherical carrier for chromatography separation and production thereofInfo
- Publication number
- JPH02147857A JPH02147857A JP63302794A JP30279488A JPH02147857A JP H02147857 A JPH02147857 A JP H02147857A JP 63302794 A JP63302794 A JP 63302794A JP 30279488 A JP30279488 A JP 30279488A JP H02147857 A JPH02147857 A JP H02147857A
- Authority
- JP
- Japan
- Prior art keywords
- carrier
- spherical
- solidified
- substance
- calcium phosphate
- 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
- 238000004519 manufacturing process Methods 0.000 title claims 3
- 238000004587 chromatography analysis Methods 0.000 title abstract 2
- 238000000926 separation method Methods 0.000 title abstract 2
- 239000000463 material Substances 0.000 claims abstract 7
- 230000002378 acidificating effect Effects 0.000 claims abstract 3
- 229910052586 apatite Inorganic materials 0.000 claims abstract 3
- 229910000389 calcium phosphate Inorganic materials 0.000 claims abstract 3
- 239000001506 calcium phosphate Substances 0.000 claims abstract 3
- 235000011010 calcium phosphates Nutrition 0.000 claims abstract 3
- 150000002500 ions Chemical class 0.000 claims abstract 3
- VSIIXMUUUJUKCM-UHFFFAOYSA-D pentacalcium;fluoride;triphosphate Chemical compound [F-].[Ca+2].[Ca+2].[Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O VSIIXMUUUJUKCM-UHFFFAOYSA-D 0.000 claims abstract 3
- 239000007788 liquid Substances 0.000 claims abstract 2
- 239000000126 substance Substances 0.000 claims 5
- 238000013375 chromatographic separation Methods 0.000 claims 3
- 239000007864 aqueous solution Substances 0.000 claims 2
- -1 calcium phosphate compound Chemical class 0.000 claims 1
- 229910010272 inorganic material Inorganic materials 0.000 claims 1
- 239000011147 inorganic material Substances 0.000 claims 1
- 239000007787 solid Substances 0.000 abstract 4
- QORWJWZARLRLPR-UHFFFAOYSA-H tricalcium bis(phosphate) Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]P([O-])([O-])=O.[O-]P([O-])([O-])=O QORWJWZARLRLPR-UHFFFAOYSA-H 0.000 abstract 2
- 238000001816 cooling Methods 0.000 abstract 1
- 238000000034 method Methods 0.000 abstract 1
- 239000002245 particle Substances 0.000 abstract 1
Landscapes
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、カラムクロマトグラフィー用充填材として最
適な分離用担体およびその製造方法に関し、特に該担体
の球状化を図った技術に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a separation carrier optimal as a packing material for column chromatography and a method for producing the same, and particularly relates to a technique for making the carrier spherical. .
[従来の技術]
カラム法による液体クロマトグラフィー(以下単にクロ
マトグラフィーと呼ぶことがある)は物質の分離や精製
等に利用されており、いろいろな物質の二相間(固定相
と移動相)の分配係数の違いに基づいて分離・精製を行
なうものである。[Prior art] Liquid chromatography using a column method (hereinafter sometimes simply referred to as chromatography) is used for separation and purification of substances, and is used to partition various substances between two phases (stationary phase and mobile phase). Separation and purification are performed based on differences in coefficients.
前記固定相に用いられる固体物質は担体と呼ばれるが、
移動相の高速化技術の発展に伴ないこの担体には高い強
度が要求される様になってきた。The solid substance used in the stationary phase is called a carrier,
With the development of high-speed mobile phase technology, this carrier is required to have high strength.
即ち高速液体クロマトグラフィーの如く、移動相を10
〜30 arm/secの高速で流して分離の高速化を
図るのが近年の傾向であるが、この様な高速化に対処す
るには高圧力に耐え得るだけの強度が要求される。That is, as in high performance liquid chromatography, the mobile phase is
In recent years, there has been a trend to speed up separation by flowing at a high speed of ~30 arm/sec, but in order to handle such high speeds, strength sufficient to withstand high pressure is required.
またクロマトグラフィーによる分離能力を高く維持する
には、担体の充填をでとるだけクロマトグラフィーの近
似的分布平衡状態に維持することが必要である。また担
体の粒子径が!OO〜150μm程度の大きさであると
、移動相の高速状態下においては前記平衡状態を維持す
ることは困難である。従って前記平衡状態を高速状態下
で達成するには、担体の粒子径を充分細かくすると共に
その粒子径を揃えることが必要である。Furthermore, in order to maintain a high separation ability by chromatography, it is necessary to maintain the approximate distribution equilibrium state of chromatography as much as possible by loading the carrier. Also, the particle size of the carrier! If the size is about OO to 150 μm, it is difficult to maintain the equilibrium state under the high speed state of the mobile phase. Therefore, in order to achieve the above-mentioned equilibrium state under high-speed conditions, it is necessary to make the particle size of the carrier sufficiently fine and to make the particle size uniform.
これまで使用されてきた担体用素材としては、シリカ、
ガラス、アルミナ、高架橋度の樹脂等が挙げられ、特に
シリカやアルミナ等は比較的良好な特性を有すると言わ
れている。しかしながらこれらはシリカやアルミナでさ
えも、微細なビード状物質として得ることは困難であり
、従来担体として用いる際には破砕によって細かく且つ
粒度を揃える様にしている。しかし粒子形状が様々とム
リしかも依然として粒度分布が広いことから圧損が大き
い等の欠点がある。The carrier materials that have been used so far include silica,
Examples include glass, alumina, and highly cross-linked resins, and silica and alumina are said to have relatively good properties. However, even silica and alumina are difficult to obtain as fine bead-like substances, and conventionally, when used as a carrier, they are crushed to make them fine and of uniform particle size. However, since the particle shapes vary, and the particle size distribution is still wide, there are drawbacks such as large pressure loss.
ところでクロマトグラフィーはタンパク質等の生体関連
物質の分離・精製にも利用されているが、こうした物質
分離を対象とする場合の担体には生体との親和性が良好
であることが要求される。これまで広く用いられてきた
シリカ系担体では、担体表面に化学修飾を施すと共に溶
出液への薬品添加等によって担体からの物質の溶出が行
なわれるのが一般的である。しかしながらこうした条件
は生体関連物質にとって過酷な条件となってしまい、該
物質の活性を失なう等の変性を招くことになる。またタ
ンパク質や菌などの洗浄においては酸性液による洗浄だ
けでは不充分であり、アルカリ性液による洗浄をも行な
う必要があるが、シリカ系担体を用いた場合にはアルカ
リ洗浄の際に担体自体若しくは担体表面の修飾基が溶脱
してしまうという欠点がある。By the way, chromatography is also used for the separation and purification of biologically related substances such as proteins, and when the purpose is to separate such substances, the carrier is required to have good affinity with the living body. With silica-based carriers that have been widely used so far, substances are generally eluted from the carrier by chemically modifying the carrier surface and adding chemicals to the eluate. However, these conditions are harsh for biological substances, leading to degeneration such as loss of activity of the substances. Furthermore, when cleaning proteins, bacteria, etc., cleaning with an acidic solution alone is insufficient, and it is necessary to also perform cleaning with an alkaline solution. However, when a silica-based carrier is used, the carrier itself or the carrier is washed with an alkaline solution. There is a drawback that the surface modification group is leached out.
こうしたことからヒドロキシアパタイト(以下HAPと
記すことがある)がクロマトグラフィー分離用担体とし
て用いられる様になってきた。即ちHAPは生体関連物
質との親和性が良好であるばかりでなく、それ自体がイ
オン交換能を有し、特に104〜109の分子量を持つ
荷電性生体関連高分子物質のカルボキシル基、燐酸基、
ε−アミノ基、グアニジノ基等を吸着する性質があり、
しかもアルカリ性に対して安定である。For these reasons, hydroxyapatite (hereinafter sometimes referred to as HAP) has come to be used as a carrier for chromatographic separation. That is, HAP not only has good affinity with biological substances, but also has ion exchange ability itself, and is particularly suitable for carboxyl groups, phosphoric acid groups, and
It has the property of adsorbing ε-amino groups, guanidino groups, etc.
Furthermore, it is stable against alkalinity.
[発明が解決しようとする課題]
クロマトグラフィー分離用担体として用いられるHAP
は、湿式法で合成されたものをそのまま或は造粒物とし
て使用するのが一般的である。[Problem to be solved by the invention] HAP used as a carrier for chromatography separation
is generally synthesized by a wet method and used as it is or in the form of granules.
しかしながら粒径10μm以下の微粒子とするには歩留
りが悪く、しかも形状や粒度分布等の面では前述した問
題が未解決のまま残されている。However, the yield is low when producing fine particles with a particle size of 10 μm or less, and the aforementioned problems in terms of shape, particle size distribution, etc. remain unsolved.
本発明はこうした技術的課題を解決する為になされたも
のであって、その第1の目的は、粒子形状を球状にする
と共に粒度を均一にし、良好な平衡状態を維持でき且つ
圧損を極力抑えることができしかも理論段数を多くする
ことのできるHAP系クロりトグラフィー分離用担体、
およびその様な担体を製造する為の方法を提供すること
にある。また本発明の第2の目的は、HAP系担体自体
のイオン交換能力を高めることによって、特に生体関連
物質のより良好な分離を達成しようとするものである。The present invention was made to solve these technical problems, and its first purpose is to make the particle shape spherical and uniform in particle size, maintain a good equilibrium state, and minimize pressure loss. HAP-based chromatography separation carrier that can increase the number of theoretical plates,
and to provide a method for producing such a carrier. A second object of the present invention is to achieve better separation of biologically related substances, in particular, by increasing the ion exchange capacity of the HAP carrier itself.
[課題を解決する為の手段]
上記目的を達成し得た本発明の担体とは、粉粒状の無機
物質を核とし、その表面にCa−P系アパタイト相を含
むりん酸カルシウム系化合物を形成した二層構造を有す
る点に要旨を有するものである。[Means for Solving the Problems] The carrier of the present invention that achieves the above object has a core of a powdery inorganic substance, and a calcium phosphate compound containing a Ca-P apatite phase is formed on the surface of the carrier. The main point is that it has a two-layer structure.
上記担体は、溶融状態にある無機物質を飛散急冷して球
状の固化物とし、この固化物を酸性若しくはアルカリ性
水溶液に浸漬して固化物表面の可溶部を溶脱せしめた後
、PO4イオンを含む液に浸漬させることによって得ら
れる。The above-mentioned carrier is produced by scattering and rapidly cooling the molten inorganic substance to form a spherical solidified substance, and immersing this solidified substance in an acidic or alkaline aqueous solution to leach out the soluble portion on the surface of the solidified substance, which contains PO4 ions. Obtained by immersion in liquid.
また上記担体は、粉粒状無機物質を半溶融状態で転動さ
せることによって球状の固化物とし、この固化物を酸性
若しくはアルカリ性水溶液に浸漬して固化物表面の可溶
部を溶脱せしめた後、PO4イオンを含む液に浸漬させ
ることによっても得られる。Further, the above-mentioned carrier is made by rolling a particulate inorganic substance in a semi-molten state to form a spherical solidified substance, and after immersing this solidified substance in an acidic or alkaline aqueous solution to leach out the soluble portion on the surface of the solidified substance, It can also be obtained by immersion in a solution containing PO4 ions.
[作用]
本発明は上述の如く構成されるが、要するに無機物質を
球状の固化物とし、この固化物を酸性若しくはアルカリ
性水溶液に浸漬して表面の可溶部を溶脱して粉粒状とし
た後PO4イオン含有溶液に浸漬させることによって、
表面にCa−P、%アパタイト相を含むりん酸カルシウ
ム系化合物を形成することを基本要旨とするものである
。この様にして得られる担体は、その表面が少なくとも
アパタイト相を含んだりん酸カルシウム系化合物で被覆
されているので、生体親和性といつたアパタイト相の本
来特性を損なうことはない、また全体形状がほぼ球状の
ものが得られるので、圧損が生じにくく且つ近似的分布
平衡状態を維持でき、より高い流速で物質の分離を行な
うことが可能になる。しかも粒度の分布を狭くすること
ができるので、理論段数を大きくとることができ、送液
の圧力や流量等の調整も容易になる。更に可溶性成分を
溶脱して微細な孔を形成することによって表面積を増大
して担体自体のイオン交換能を高めることができ、クロ
マトグラフィーでの分離能を高めることができる0本発
明で核として用いる物質は、PO4イオンを含む液に浸
漬させることによってCa−P系アパタイト相を含むり
ん酸カルシウム系化合物を析出する化合物であればよい
が、少なくとも無機物質であることが必要である。この
様な物質としては種々考えられるが、溶融軟化させ易さ
からすれば、無機ガラスが挙げられる。[Function] The present invention is constructed as described above, but in short, the inorganic substance is solidified into a spherical shape, the solidified material is immersed in an acidic or alkaline aqueous solution, the soluble portion on the surface is leached, and then the solidified material is made into powder and granules. By immersing it in a solution containing PO4 ions,
The basic gist is to form a calcium phosphate compound containing Ca-P and % apatite phase on the surface. Since the surface of the carrier obtained in this way is coated with a calcium phosphate compound containing at least an apatite phase, the original properties of the apatite phase such as biocompatibility are not impaired, and the overall shape Since a substantially spherical shape can be obtained, pressure loss is less likely to occur and an approximate distribution equilibrium state can be maintained, making it possible to separate substances at a higher flow rate. Moreover, since the particle size distribution can be narrowed, the number of theoretical plates can be increased, and the pressure and flow rate of liquid feeding can be easily adjusted. Furthermore, by leaching soluble components and forming fine pores, the surface area can be increased and the ion exchange ability of the carrier itself can be increased, and the separation ability in chromatography can be improved.0 Used as a core in the present invention The substance may be any compound that precipitates a calcium phosphate compound containing a Ca-P apatite phase when immersed in a solution containing PO4 ions, but it is required to be at least an inorganic substance. Various materials can be considered as such materials, but inorganic glass is an example of ease of melting and softening.
無機物質を球状の固化物とする方法としては、粉末を転
動造粒する方法が挙げられるが、100μm以下の粒径
(実質的には40μm以下)を得ようとすれば、原料を
まず1μ−以下の微粉末に粉砕してから造粒する必要が
あり、粉砕コストが高くなることや粉末の取扱い面で難
があり実用的でない、そこで本発明では、溶融温度直前
の高温下で(これを溶融状態と呼ぶ)、粉末を相互に焼
結しない様に、且つ夫々の粒子に回転力を与える為に転
動を行なって球状化する方法を採用した[請求項(3)
]、但し、これ以外の方法として、例えば溶融状態にあ
る無機物質に水や油類等の液体または空気、N2.Ar
等のガスを吹付けて飛散急冷するアトマイズ法、或は回
転ディスク上に滴下して遠心力で飛散させて急冷する方
法等も球状化に有効である[請求項(2)]。A method for turning an inorganic substance into a spherical solidified substance is a method of rolling granulation of powder, but if you want to obtain a particle size of 100 μm or less (substantially 40 μm or less), the raw material must first be sized to 1 μm. - It is necessary to grind the powder into the following fine powder and then granulate it, which increases the grinding cost and makes it difficult to handle the powder, making it impractical. (referred to as a molten state), a method is adopted in which the powder is rolled into a spheroid in order to prevent the powder from sintering with each other and to apply rotational force to each particle [Claim (3)
], However, as a method other than this, for example, a liquid such as water or oil or air, N2. Ar
An atomization method in which a gas such as the above is sprayed to rapidly cool the material by scattering, or a method in which the material is dropped onto a rotating disk and dispersed by centrifugal force to rapidly cool the material are also effective for spheroidization [Claim (2)].
球状の固化物表面にりん酸系化合物を形成する方法とし
ては、例えばスパッタリング法、スプレードライ法1回
転々動造粒法等が公知である(例えば特開昭63−16
044号公報)、シかしスパッタリング法では専用の装
置が必要であり、しかも100μ■以下の各粒子表面に
完全にコーティングすることは非常に難しい、同様にス
プレードライ法においては100μ11以下の各粒子表
面にコーティングするのは難しい、また転動造粒法にお
いても、粒子の細かさに難がある。As a method for forming a phosphoric acid compound on the surface of a spherical solidified product, for example, a sputtering method, a spray drying method, a one-rotation granulation method, etc. are known (for example, JP-A-63-16
044 Publication), the Shikashi sputtering method requires a special equipment, and it is very difficult to completely coat the surface of each particle of 100μ or less. It is difficult to coat the surface, and even in the rolling granulation method, there is a problem with the fineness of the particles.
こうしたことから本発明では、溶液中に粒子を浸漬させ
て表面にりん酸カルシウム系化合物を析出させる方法に
着目し、この方法を採用すべく検討した。ところが本発
明者らの研究によると、アパタイト等のりん酸カルシウ
ム系化合物は水溶性でないものが多く、そのほとんどが
粒子として析出してしまい、該化合物を固化物表面にコ
ーティングするにはスラリー物質を用いても容易でない
ことが判明した。そこで本発明では球状の固化物を酸性
若しくはアルカリ性水溶液に浸漬して固化物表面の可溶
部を溶脱させ、P Oaイオンと反応したときにアパタ
イト相を含むりん酸カルシウム系化合物を析出する化合
物を固化物表面に多、く露出しておく様な手段を採用し
た。このことによって固化物表面に上述りん酸カルシウ
ム系化合物を比較的容易に析出させることができる。こ
の様な思想からすれば、溶融状態にある無機物質を飛散
急冷して得られる球状の固化物を、PO4イオンを含む
液に浸漬する前に(即ち可溶部を溶脱する工程の前また
は後)、溶融直前の温度で加熱して固化物表面を結晶化
する工程を付加することは推奨される。即ちこの様な工
程を加えて固化物表面にりん酸カルシウム系化合物やC
a5iOs(ウオラストナイトまたは凝ウオラストナイ
ト)等をできるだけ多く、PO4イオンと反応させる前
に予め結晶化させておけば4、これを起点として固化物
表面にはアパタイト相を含むりん酸カルシウム系化合物
が析出し易い状態となる。またこうした観点からすれば
、球状固化物となる無機物質は結晶化することによって
アパタイト相を含むりん酸カルシウム系化合物およびC
a5te、の2相が同時に析出し易い組成のものである
ことが好ましい、AIやT1を含むとりん酸カルシウム
の析出を阻害するので好ましくない、尚粉粒状無機物質
を半溶融状態で転動して球状の固化物を得る工程を採用
する場合には、固化物の球状化と同時に表面の結晶化も
進行することになる。For this reason, in the present invention, we focused on a method in which particles are immersed in a solution to precipitate a calcium phosphate compound on the surface, and we investigated the possibility of adopting this method. However, according to the research conducted by the present inventors, many calcium phosphate compounds such as apatite are not water-soluble, and most of them precipitate as particles.In order to coat the surface of a solidified product with this compound, a slurry substance must be used. It turns out that it is not easy to use. Therefore, in the present invention, a spherical solidified material is immersed in an acidic or alkaline aqueous solution to leach out the soluble portion on the surface of the solidified material, and a compound that precipitates a calcium phosphate compound containing an apatite phase when reacted with POa ions is used. A method was adopted to expose a large amount of the material to the surface of the solidified material. This allows the above-mentioned calcium phosphate compound to be deposited on the surface of the solidified product relatively easily. From this point of view, the spherical solidified material obtained by scattering and rapidly cooling the molten inorganic material should be immersed in a solution containing PO4 ions (i.e., before or after the process of leaching the soluble part). ), it is recommended to add a step of crystallizing the surface of the solidified material by heating it at a temperature just before melting. In other words, by adding such a process, calcium phosphate compounds and C are added to the surface of the solidified product.
If as much as possible of a5iOs (wollastonite or precipitated wollastonite) etc. is crystallized in advance before reacting with PO4 ions,4, using this as a starting point, a calcium phosphate compound containing an apatite phase will form on the surface of the solidified product. is likely to precipitate. Also, from this point of view, the inorganic substance that becomes the spherical solidified substance is crystallized to form a calcium phosphate compound containing an apatite phase and carbon dioxide.
It is preferable that the two phases of a5te and a5te are easily precipitated at the same time, but it is not preferable because it inhibits the precipitation of calcium phosphate containing AI and T1. When a step of obtaining a spherical solidified product is adopted, crystallization of the surface will proceed at the same time as the solidified product becomes spherical.
本発明の担体表面に形成されるりん酸カルシウム系化合
物は、少なくともCa−Pアパタイト相を含む必要があ
るが、その他Ca2 F207.Ca (PO3)2
、 Cat(P 04)s。The calcium phosphate compound formed on the surface of the carrier of the present invention must contain at least a Ca-P apatite phase, but may also contain Ca2F207. Ca (PO3)2
, Cat(P 04)s.
Ca+o(PO4)6 F2.Ca+o(PO4)I!
C1等を含んだものであってもよく、Caの一部をS
r。Ca+o(PO4)6 F2. Ca+o(PO4)I!
It may contain C1, etc., and a part of Ca may be replaced with S.
r.
Ba等の金属で置換したものやPo4の一部をCO2で
置換したものを含んでいてもよい。これらの化合物は核
となる無機物質の組成に応じて主に結晶化の際に生成す
るものである。またこれらの化合物を基本としてPo4
イオンとの反応によってエピタキシアル成長する非晶質
りん酸カルシウム、 OP C[Caa H2(P 0
4)a・5 H201゜Ca HP Oa、Ca HP
04”2 H20゜Ca (H2PO4)2.ca
()12PO4)2・2H20若しくはこれらの加熱に
よって生成するCa3(HF20?)2等の一連のりん
酸カルシウム等を含み得る。It may also include one in which a metal such as Ba is substituted or a part of Po4 is substituted with CO2. These compounds are mainly produced during crystallization depending on the composition of the core inorganic substance. Also, based on these compounds, Po4
Amorphous calcium phosphate, OP C[Caa H2 (P 0
4)a・5 H201゜Ca HP Oa, Ca HP
04”2 H20°Ca (H2PO4)2.ca
It may contain a series of calcium phosphates such as ()12PO4)2.2H20 or Ca3(HF20?)2 produced by heating these.
一部PO4イオンを含む液については、りん酸がイオン
化している状態のものであればよく何ら限定されるもの
ではないが、りん酸、メタりん酸、りん酸ナトリウム、
りん酸カリウム、りん酸アンモニウム等の可溶性りん酸
塩を溶解させた液の他、リン酸トリメチルやリン酸トリ
エチル等のエステル類、リン酸トリメトキシド等のアル
コキシド類を溶解した液等が挙げられる。Regarding the liquid partially containing PO4 ions, there are no limitations as long as the phosphoric acid is in an ionized state, but phosphoric acid, metaphosphoric acid, sodium phosphate,
Examples include liquids in which soluble phosphates such as potassium phosphate and ammonium phosphate are dissolved, as well as liquids in which esters such as trimethyl phosphate and triethyl phosphate, and alkoxides such as phosphoric acid trimethoxide are dissolved.
以下本発明を実施例によって更に詳細に説明するが、下
記実施例は本発明を限定する性質のものではなく、前・
後記の趣旨に徴して設計変更することはいずれも本発明
の技術的範囲に含まれるものである。Hereinafter, the present invention will be explained in more detail with reference to examples, but the following examples are not intended to limit the present invention.
Any design changes for the purposes described below are included within the technical scope of the present invention.
[実施例]
CaO: 44%、S i 02 : 34.6%、
F20゜: 15.5%、残部ホウ酸ナトリウムの割合
で試薬を混合し、1550℃で溶解した。これを水中投
下して急冷し、振動ミルにて44μ■以下に粉砕して粉
末試料とした。これを回転型るつぼに投入し、1100
℃の加熱によって半溶融状態として転動しつつ1時間保
持し、その後200℃/時間の速度で冷却した。こうし
て得られた固化物は、角がとれて球状となっていた。[Example] CaO: 44%, S i 02: 34.6%,
F20°: Reagents were mixed at a ratio of 15.5% and the remainder was sodium borate, and dissolved at 1550°C. This was dropped into water, rapidly cooled, and ground to a size of 44 μm or less using a vibration mill to obtain a powder sample. Pour this into a rotating crucible and
The mixture was kept in a semi-molten state for 1 hour while being rolled at a temperature of 0.degree. C., and then cooled at a rate of 200.degree. C./hour. The solidified product thus obtained had rounded corners and a spherical shape.
次に上記固化物の100gを0.IN酢酸100ccに
添加し、表面の可溶性成分を溶脱した。続いて該固化物
を、りん酸アンモニウムを溶解した液中で50℃に加温
しながら24時間転動した。得られた粒子(担体)をE
SCAによって分析したところ、表面にリン酸カルシウ
ムめ相が生成しているのが確認できた。上記担体をカラ
ムに充填して高速液体クロマトグラフィーを行なったと
ころ、何らの不都合を生じることなく被検液中に含まれ
る各穏タンパク質(およびアミノ酸)の分離が行なえた
。このときのクロマトグラムを第1図に示す。Next, 100 g of the above solidified material was added to 0.0 g. It was added to 100 cc of IN acetic acid to leach out the soluble components on the surface. Subsequently, the solidified product was rolled for 24 hours while being heated to 50° C. in a solution containing ammonium phosphate. The obtained particles (carrier) are
When analyzed by SCA, it was confirmed that a calcium phosphate phase was formed on the surface. When high performance liquid chromatography was performed by filling a column with the above carrier, it was possible to separate each moderate protein (and amino acid) contained in the test liquid without causing any problems. The chromatogram at this time is shown in FIG.
[発明の効果]
以上述べた如く本発明によれば、球状且つ粒度が均一な
担体が得られ、クロマトグラフィーにおける分離能を高
めることができた。またHAP系担体自体のイオン交換
能力をも高めることができ、特に生体関連物質の分離に
おいて好都合な結果得られた。[Effects of the Invention] As described above, according to the present invention, a carrier having a spherical shape and uniform particle size could be obtained, and the separation ability in chromatography could be improved. Furthermore, the ion exchange ability of the HAP-based carrier itself can be increased, which is particularly advantageous in the separation of biologically related substances.
第1図は本発明の担体を用いて液体クロマトグラフィー
を行なったときに得られたクロマトグラムである。FIG. 1 is a chromatogram obtained when liquid chromatography was performed using the carrier of the present invention.
Claims (3)
系アパタイト相を含むりん酸カルシウム系化合物を形成
した二層構造を有することを特徴とするクロマトグラフ
ィー分離用球状担体。(1) The core is a powdery inorganic substance, and the surface is Ca-P.
A spherical carrier for chromatographic separation characterized by having a two-layer structure formed of a calcium phosphate compound containing an apatite phase.
化物とし、この固化物を酸性若しくはアルカリ性水溶液
に浸漬して固化物表面の可溶部を溶脱せしめた後、PO
_4イオンを含む液に浸漬して請求項(1)の担体を製
造することを特徴とするクロマトグラフィー分離用担体
の製造方法。(2) The inorganic substance in the molten state is rapidly cooled by scattering to form a spherical solidified substance, and this solidified substance is immersed in an acidic or alkaline aqueous solution to leach out the soluble portion on the surface of the solidified substance, and then PO
A method for producing a carrier for chromatographic separation, which comprises producing the carrier according to claim (1) by immersing the carrier in a liquid containing _4 ions.
よって球状の固化物とし、この固化物を酸性若しくはア
ルカリ性水溶液に浸漬して固化物表面の可溶部を溶脱せ
しめた後、PO_4イオンを含む液に浸漬して請求項(
1)の担体を製造することを特徴とするクロマトグラフ
ィー分離用担体の製造方法。(3) The powdered inorganic material is rolled in a semi-molten state to form a spherical solidified material, and this solidified material is immersed in an acidic or alkaline aqueous solution to leach out the soluble portion on the surface of the solidified material, and then PO_4 ions are formed. Claims (
A method for producing a carrier for chromatographic separation, which comprises producing the carrier according to 1).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63302794A JPH02147857A (en) | 1988-11-29 | 1988-11-29 | Spherical carrier for chromatography separation and production thereof |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63302794A JPH02147857A (en) | 1988-11-29 | 1988-11-29 | Spherical carrier for chromatography separation and production thereof |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02147857A true JPH02147857A (en) | 1990-06-06 |
Family
ID=17913199
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63302794A Pending JPH02147857A (en) | 1988-11-29 | 1988-11-29 | Spherical carrier for chromatography separation and production thereof |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02147857A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04303766A (en) * | 1991-03-30 | 1992-10-27 | Kobe Steel Ltd | Method of forming pores in surface of separation material for liquid chromatography |
JPH0627098A (en) * | 1992-05-15 | 1994-02-04 | Fuji Shirishia Kagaku Kk | Filler for chromatographic separation |
JP2008522073A (en) * | 2004-11-26 | 2008-06-26 | ルノー・エス・アー・エス | Automotive internal combustion engine including continuous diesel fuel recovery surface |
US7574991B2 (en) | 2006-01-19 | 2009-08-18 | Toyota Jidosha Kabushiki Kaisha | Camshaft support structure for an internal combustion engine |
US7757646B2 (en) | 2006-01-19 | 2010-07-20 | Toyota Jidosha Kabushiki Kaisha | Camshaft support structure of an internal combustion engine |
US8042508B2 (en) | 2006-01-19 | 2011-10-25 | Toyota Jidosha Kabushiki Kaisha | Camshaft support structure for internal combustion engine |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6316044A (en) * | 1986-07-05 | 1988-01-23 | Asahi Optical Co Ltd | Packing agent for column |
JPS63126548A (en) * | 1986-11-14 | 1988-05-30 | Koken Co Ltd | Adsorbent |
JPS63157973A (en) * | 1986-12-22 | 1988-06-30 | Koken Co Ltd | Liquid chromatography |
-
1988
- 1988-11-29 JP JP63302794A patent/JPH02147857A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6316044A (en) * | 1986-07-05 | 1988-01-23 | Asahi Optical Co Ltd | Packing agent for column |
JPS63126548A (en) * | 1986-11-14 | 1988-05-30 | Koken Co Ltd | Adsorbent |
JPS63157973A (en) * | 1986-12-22 | 1988-06-30 | Koken Co Ltd | Liquid chromatography |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04303766A (en) * | 1991-03-30 | 1992-10-27 | Kobe Steel Ltd | Method of forming pores in surface of separation material for liquid chromatography |
JPH0627098A (en) * | 1992-05-15 | 1994-02-04 | Fuji Shirishia Kagaku Kk | Filler for chromatographic separation |
JP2008522073A (en) * | 2004-11-26 | 2008-06-26 | ルノー・エス・アー・エス | Automotive internal combustion engine including continuous diesel fuel recovery surface |
US7574991B2 (en) | 2006-01-19 | 2009-08-18 | Toyota Jidosha Kabushiki Kaisha | Camshaft support structure for an internal combustion engine |
US7757646B2 (en) | 2006-01-19 | 2010-07-20 | Toyota Jidosha Kabushiki Kaisha | Camshaft support structure of an internal combustion engine |
US8042508B2 (en) | 2006-01-19 | 2011-10-25 | Toyota Jidosha Kabushiki Kaisha | Camshaft support structure for internal combustion engine |
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