[go: up one dir, main page]

CN107999036A - The high pressure resistant affinity chromatography medium of chromatographic column - Google Patents

The high pressure resistant affinity chromatography medium of chromatographic column Download PDF

Info

Publication number
CN107999036A
CN107999036A CN201711277799.9A CN201711277799A CN107999036A CN 107999036 A CN107999036 A CN 107999036A CN 201711277799 A CN201711277799 A CN 201711277799A CN 107999036 A CN107999036 A CN 107999036A
Authority
CN
China
Prior art keywords
medium
affinity chromatography
high pressure
pressure resistant
chromatographic column
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.)
Withdrawn
Application number
CN201711277799.9A
Other languages
Chinese (zh)
Inventor
瞿欢欢
朱至放
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
SUZHOU BOJIN BIOLOGICAL TECHNOLOGY Co Ltd
Original Assignee
SUZHOU BOJIN BIOLOGICAL TECHNOLOGY Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by SUZHOU BOJIN BIOLOGICAL TECHNOLOGY Co Ltd filed Critical SUZHOU BOJIN BIOLOGICAL TECHNOLOGY Co Ltd
Priority to CN201711277799.9A priority Critical patent/CN107999036A/en
Publication of CN107999036A publication Critical patent/CN107999036A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/26Synthetic macromolecular compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D15/00Separating processes involving the treatment of liquids with solid sorbents; Apparatus therefor
    • B01D15/08Selective adsorption, e.g. chromatography
    • B01D15/26Selective adsorption, e.g. chromatography characterised by the separation mechanism
    • B01D15/38Selective adsorption, e.g. chromatography characterised by the separation mechanism involving specific interaction not covered by one or more of groups B01D15/265 and B01D15/30 - B01D15/36, e.g. affinity, ligand exchange or chiral chromatography
    • B01D15/3804Affinity chromatography
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/02Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
    • B01J20/06Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising oxides or hydroxides of metals not provided for in group B01J20/04
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J20/00Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
    • B01J20/22Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising organic material
    • B01J20/24Naturally occurring macromolecular compounds, e.g. humic acids or their derivatives

Landscapes

  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Organic Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

This case is related to a kind of high pressure resistant affinity chromatography medium of chromatographic column, including medium one and medium two;Wherein, the medium one is bonded with chitosan molecule using makrolon microballoon as kernel in the makrolon microsphere surface;Hydroxyl terminal connection aglucon in the chitosan molecule;The medium two includes titanium dioxide and zinc oxide.This case introduces high pressure resistant particle by being designed improvement to the formula of affinity chromatography medium in conventional single medium, to improve the mechanical strength of affinity chromatography medium, so as to improve the separative efficiency of chromatography media at elevated pressures and recycle number;Meanwhile this improved method is simple, production cost is low.

Description

The high pressure resistant affinity chromatography medium of chromatographic column
Technical field
The present invention relates to a kind of chromatography media, more particularly to a kind of high pressure resistant affinity chromatography medium of chromatographic column.
Background technology
At present, in pharmaceutical field, the purity and biological safety of medicine how is improved, is the biologies such as recombinant protein, antibody Medicine is researched and developed and the final steps in production process.Acquisition of medicine enterprise in China for the separating medium of chromatographic column rely primarily on into Mouthful, therefore, state's domestic demand breaks away from the dependence to import separating medium, reduces the production cost of medicine.To protein drug purifies and separates Affinity chromatography medium is mainly agar sugar product, but this kind of product mechanical strength is relatively low, so as to cause it to be chromatographed in filling After column, proof pressure reduces, and limits the room for promotion of its separative efficiency, while also inhibits the reuse time of agarose Number.
The content of the invention
For technical problem existing in the prior art, this case provides a kind of high pressure resistant affinity chromatography medium of chromatographic column.
To achieve the above object, this case is achieved through the following technical solutions:
A kind of high pressure resistant affinity chromatography medium of chromatographic column, wherein, including medium one and medium two;
Wherein, the medium one is bonded with shell in the makrolon microsphere surface and gathers using makrolon microballoon as kernel Glycan molecule;Hydroxyl terminal connection aglucon in the chitosan molecule;
The medium two includes titanium dioxide and zinc oxide.
Preferably, the high pressure resistant affinity chromatography medium of the chromatographic column, wherein, the matter of the medium one and medium two Amount is than being 100:12-18.
Preferably, the high pressure resistant affinity chromatography medium of the chromatographic column, wherein, the matter of the medium one and medium two Amount is than being 100:14-16.
Preferably, the high pressure resistant affinity chromatography medium of the chromatographic column, wherein, the titanium dioxide and zinc oxide Mass ratio is 10:6-8.
Preferably, the high pressure resistant affinity chromatography medium of the chromatographic column, wherein, the titanium dioxide and zinc oxide Mass ratio is 10:7.
Preferably, the high pressure resistant affinity chromatography medium of the chromatographic column, wherein, the particle diameter of the titanium dioxide is 10-20nm。
The beneficial effects of the invention are as follows:
This case introduces resistance to height by being designed improvement to the formula of affinity chromatography medium in conventional single medium Grain son, to improve the mechanical strength of affinity chromatography medium, thus improve the separative efficiency of chromatography media at elevated pressures and Recycle number;Meanwhile this improved method is simple, production cost is low.
Embodiment
With reference to embodiment, the present invention is described in further detail, to make those skilled in the art with reference to specification Word can be implemented according to this.
A kind of high pressure resistant affinity chromatography medium of chromatographic column, wherein, including medium one and medium two;
Wherein, the medium one is bonded with shell in the makrolon microsphere surface and gathers using makrolon microballoon as kernel Glycan molecule;Hydroxyl terminal connection aglucon in the chitosan molecule;
The medium two includes titanium dioxide and zinc oxide.
Wherein, the mass ratio of the medium one and medium two is 100:12-18.
Wherein, the mass ratio of the medium one and medium two is 100:14-16.
Wherein, the mass ratio of the titanium dioxide and zinc oxide is 10:6-8.
Wherein, the mass ratio of the titanium dioxide and zinc oxide is 10:7.
Wherein, the particle diameter of the titanium dioxide is 10-20nm.
Embodiment 1
Preparation process is as follows:
1) 5-8mol dimethyl sulfoxide (DMSO)s, 1.2-1.5mol bromoacetyl bromides and 0.5-1mol hydroxides are added into 1mol carriers Sodium, stirs 3h at 25 DEG C, and after reaction, filtering, washs drying;Carrier has the poly- carbonic acid of chitosan molecule for surface bond Ester microsphere;
2) aglucon, the acetone of 8mol and the sodium hydroxide of 4mol of 1.5mol is added, stirring reaction 8h, reaction at 45 DEG C After be filtered to remove solvent, washing is three times;
3) it is 10 by the mass ratio of medium one and medium two:13rd, the mass ratio of titanium dioxide and zinc oxide is 10:6 ratio Example adds titanium dioxide and zinc oxide, and mixing is sufficiently stirred under organic solvent, filters off solvent, is drying to obtain affinity chromatography Jie Matter.
Embodiment 2
Preparation process is as follows:
1) 5-8mol dimethyl sulfoxide (DMSO)s, 1.2-1.5mol bromoacetyl bromides and 0.5-1mol hydroxides are added into 1mol carriers Sodium, stirs 3h at 25 DEG C, and after reaction, filtering, washs drying;Carrier has the poly- carbonic acid of chitosan molecule for surface bond Ester microsphere;
2) aglucon, the acetone of 8mol and the sodium hydroxide of 4mol of 1.5mol is added, stirring reaction 8h, reaction at 45 DEG C After be filtered to remove solvent, washing is three times;
3) it is 10 by the mass ratio of medium one and medium two:15th, the mass ratio of titanium dioxide and zinc oxide is 10:7 ratio Example adds titanium dioxide and zinc oxide, and mixing is sufficiently stirred under organic solvent, filters off solvent, is drying to obtain affinity chromatography Jie Matter.
Embodiment 3
Preparation process is as follows:
1) 5-8mol dimethyl sulfoxide (DMSO)s, 1.2-1.5mol bromoacetyl bromides and 0.5-1mol hydroxides are added into 1mol carriers Sodium, stirs 3h at 25 DEG C, and after reaction, filtering, washs drying;Carrier has the poly- carbonic acid of chitosan molecule for surface bond Ester microsphere;
2) aglucon, the acetone of 8mol and the sodium hydroxide of 4mol of 1.5mol is added, stirring reaction 8h, reaction at 45 DEG C After be filtered to remove solvent, washing is three times;
3) it is 10 by the mass ratio of medium one and medium two:16th, the mass ratio of titanium dioxide and zinc oxide is 10:8 ratio Example adds titanium dioxide and zinc oxide, and mixing is sufficiently stirred under organic solvent, filters off solvent, is drying to obtain affinity chromatography Jie Matter.
Embodiment 4
Preparation process is as follows:
1) 5-8mol dimethyl sulfoxide (DMSO)s, 1.2-1.5mol bromoacetyl bromides and 0.5-1mol hydroxides are added into 1mol carriers Sodium, stirs 3h at 25 DEG C, and after reaction, filtering, washs drying;Carrier has the poly- carbonic acid of chitosan molecule for surface bond Ester microsphere;
2) aglucon, the acetone of 8mol and the sodium hydroxide of 4mol of 1.5mol is added, stirring reaction 8h, reaction at 45 DEG C After be filtered to remove solvent, washing is three times;
3) it is 10 by the mass ratio of medium one and medium two:18th, the mass ratio of titanium dioxide and zinc oxide is 10:6 ratio Example adds titanium dioxide and zinc oxide, and mixing is sufficiently stirred under organic solvent, filters off solvent, is drying to obtain affinity chromatography Jie Matter.
Following table lists the test result of embodiment 1-4:
Although embodiment of the present invention is disclosed as above, it is not restricted in specification and embodiment listed With it can be applied to various suitable the field of the invention completely, can be easily for those skilled in the art Realize other modification, therefore under the universal limited without departing substantially from claim and equivalency range, it is of the invention and unlimited In specific details.

Claims (6)

1. the high pressure resistant affinity chromatography medium of a kind of chromatographic column, it is characterised in that including medium one and medium two;
Wherein, the medium one is bonded with chitosan point using makrolon microballoon as kernel in the makrolon microsphere surface Son;Hydroxyl terminal connection aglucon in the chitosan molecule;
The medium two includes titanium dioxide and zinc oxide.
2. the high pressure resistant affinity chromatography medium of chromatographic column as claimed in claim 1, it is characterised in that the medium one and medium Two mass ratio is 100:12-18.
3. the high pressure resistant affinity chromatography medium of chromatographic column as claimed in claim 1, it is characterised in that the medium one and medium Two mass ratio is 100:14-16.
4. the high pressure resistant affinity chromatography medium of chromatographic column as claimed in claim 1, it is characterised in that the titanium dioxide and oxygen The mass ratio for changing zinc is 10:6-8.
5. the high pressure resistant affinity chromatography medium of chromatographic column as claimed in claim 1, it is characterised in that the titanium dioxide and oxygen The mass ratio for changing zinc is 10:7.
6. the high pressure resistant affinity chromatography medium of chromatographic column as claimed in claim 1, it is characterised in that the grain of the titanium dioxide Footpath is 10-20nm.
CN201711277799.9A 2017-12-06 2017-12-06 The high pressure resistant affinity chromatography medium of chromatographic column Withdrawn CN107999036A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711277799.9A CN107999036A (en) 2017-12-06 2017-12-06 The high pressure resistant affinity chromatography medium of chromatographic column

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711277799.9A CN107999036A (en) 2017-12-06 2017-12-06 The high pressure resistant affinity chromatography medium of chromatographic column

Publications (1)

Publication Number Publication Date
CN107999036A true CN107999036A (en) 2018-05-08

Family

ID=62057041

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711277799.9A Withdrawn CN107999036A (en) 2017-12-06 2017-12-06 The high pressure resistant affinity chromatography medium of chromatographic column

Country Status (1)

Country Link
CN (1) CN107999036A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114054006A (en) * 2021-11-17 2022-02-18 苏州纳微科技股份有限公司 Oligo-dT affinity chromatography filler

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20110217539A1 (en) * 2009-02-19 2011-09-08 Alex Garfield Bonner Porous interpenetrating polymer network
WO2012030512A1 (en) * 2010-09-03 2012-03-08 Percivia Llc. Flow-through protein purification process
CN106475074A (en) * 2016-12-22 2017-03-08 苏州楚博生物技术有限公司 High mechanical properties affinity chromatography medium
CN106582580A (en) * 2016-12-22 2017-04-26 苏州楚博生物技术有限公司 High-pressure-resistant affinity chromatography media for chromatographic column

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20110217539A1 (en) * 2009-02-19 2011-09-08 Alex Garfield Bonner Porous interpenetrating polymer network
WO2012030512A1 (en) * 2010-09-03 2012-03-08 Percivia Llc. Flow-through protein purification process
CN106475074A (en) * 2016-12-22 2017-03-08 苏州楚博生物技术有限公司 High mechanical properties affinity chromatography medium
CN106582580A (en) * 2016-12-22 2017-04-26 苏州楚博生物技术有限公司 High-pressure-resistant affinity chromatography media for chromatographic column

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114054006A (en) * 2021-11-17 2022-02-18 苏州纳微科技股份有限公司 Oligo-dT affinity chromatography filler

Similar Documents

Publication Publication Date Title
CN106475074A (en) High mechanical properties affinity chromatography medium
CN104372045B (en) A kind of preparation method of high-purity sulforaphane
CN101245121A (en) Preparation method of sulfamethoxazole molecularly imprinted polymer
CN102596987B (en) Method for purification of colistin and purified colistin components
CN102863519A (en) Refining method for vancomycin hydrochloride
CN106582580A (en) High-pressure-resistant affinity chromatography media for chromatographic column
CN108218681B (en) A kind of purification method of coenzyme Q10
CN108047016B (en) Method for extracting bisdemethoxycurcumin from turmeric
CN107814732B (en) Choline deep eutectic solvent, preparation method and application in extracting nasturtine from nasturtium
CN104289210B (en) Preparation method of phenylalanine chiral chromatographic column stationary phase
EP3239165B1 (en) Composition containing nitrogen heterocyclic hexapeptide precursor and preparation method and application thereof
CN102020724B (en) Method for extracting sodium hyaluronate from fermentation liquor containing hyaluronic acid
CN107999036A (en) The high pressure resistant affinity chromatography medium of chromatographic column
CN101033229A (en) Separation of monosomic tetrandrine from tetrandrine total alkaloid by adsorption resin method
CN103819572A (en) Extraction technology for production of polysaccharide from mulberry leaf
CN106622159A (en) Affinity chromatography medium for purifying protein drug
CN110882357A (en) High-purity bamboo leaf flavonoid powder and preparation method thereof
CN107674116A (en) A kind of purification process of Pneumocandin B0
WO2012116520A1 (en) Method for preparing orlistat
CN106622184B (en) Chromatography media for antibody drug purifying
CN106582578B (en) High Pressure Affinity Chromatography Media
CN104277177B (en) The false template molecule imprinted polymer of a kind of gingerol and extract the method for gingerol with it from ginger
CN104480091A (en) Method for highly purifying kallikein and drug composition containing kallikein
CN112521259B (en) Preparation method of natural curcumin without vanillin
CN106727765B (en) A kind of preparation method of total flavonoids in sea asparagus

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
WW01 Invention patent application withdrawn after publication

Application publication date: 20180508

WW01 Invention patent application withdrawn after publication