[go: up one dir, main page]

CN108949703A - A kind of thick method of purification of hemicellulose corpusculum analog - Google Patents

A kind of thick method of purification of hemicellulose corpusculum analog Download PDF

Info

Publication number
CN108949703A
CN108949703A CN201810684749.0A CN201810684749A CN108949703A CN 108949703 A CN108949703 A CN 108949703A CN 201810684749 A CN201810684749 A CN 201810684749A CN 108949703 A CN108949703 A CN 108949703A
Authority
CN
China
Prior art keywords
ultrafiltration
centrifugation
centrifuged
alcl
corpusculum
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Withdrawn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
CN201810684749.0A
Other languages
Chinese (zh)
Inventor
窦同意
陈静
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.)
Dalian University of Technology
Original Assignee
Dalian University of Technology
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 Dalian University of Technology filed Critical Dalian University of Technology
Priority to CN201810684749.0A priority Critical patent/CN108949703A/en
Publication of CN108949703A publication Critical patent/CN108949703A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C12BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12NMICROORGANISMS OR ENZYMES; COMPOSITIONS THEREOF; PROPAGATING, PRESERVING, OR MAINTAINING MICROORGANISMS; MUTATION OR GENETIC ENGINEERING; CULTURE MEDIA
    • C12N9/00Enzymes; Proenzymes; Compositions thereof; Processes for preparing, activating, inhibiting, separating or purifying enzymes

Landscapes

  • Life Sciences & Earth Sciences (AREA)
  • Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Genetics & Genomics (AREA)
  • Organic Chemistry (AREA)
  • Zoology (AREA)
  • Engineering & Computer Science (AREA)
  • Bioinformatics & Cheminformatics (AREA)
  • Wood Science & Technology (AREA)
  • Microbiology (AREA)
  • Biotechnology (AREA)
  • Biomedical Technology (AREA)
  • Molecular Biology (AREA)
  • Biochemistry (AREA)
  • General Engineering & Computer Science (AREA)
  • General Health & Medical Sciences (AREA)
  • Medicinal Chemistry (AREA)
  • Preparation Of Compounds By Using Micro-Organisms (AREA)
  • Polysaccharides And Polysaccharide Derivatives (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

本发明提供了一种半纤维小体类似物粗提纯方法,属工业生物技术领域。将发酵液采用二级串联离心法进行离心处理,离心条件大于20000g离心20min,转子常数K大于900;离心后取上清发酵液超滤处理进行浓缩;超滤采用无机陶瓷中空超滤膜,孔径10nm<d<50nm;超滤过程中,反复加pH 7.5、50mM Tris‑HCl缓冲液,超滤;采用AlCl3溶液滴加的方式对得到的超滤液进行絮凝处理,所加入AlCl3应控制在3~7g/L的终浓度,充分颠倒混匀后静置3‑5min,即观察到显著絮凝,此时6000g离心10min,即获得目的产物。本发明的方法用于工业生物转化、生物能源、医药中间体制备等领域。

The invention provides a crude purification method for hemicellulosome analogues, which belongs to the field of industrial biotechnology. The fermentation broth is centrifuged by two-stage tandem centrifugation, the centrifugation condition is greater than 20000g and centrifuged for 20min, and the rotor constant K is greater than 900; 10nm<d<50nm; during the ultrafiltration process, repeatedly add pH 7.5, 50mM Tris-HCl buffer solution for ultrafiltration; use AlCl 3 solution dropwise to carry out flocculation treatment on the obtained ultrafiltrate, the added AlCl 3 should be controlled At a final concentration of 3-7g/L, after fully inverting and mixing for 3‑5 minutes, significant flocculation was observed. At this time, the target product was obtained by centrifuging at 6000g for 10 minutes. The method of the invention is used in the fields of industrial biotransformation, bioenergy, preparation of pharmaceutical intermediates and the like.

Description

一种半纤维小体类似物粗提纯方法A kind of crude purification method of hemicellulosome analog

技术领域technical field

本发明涉及一种针对由纤维微细菌产生的半纤维小体类似物的粗提纯方法,属工业生物技术领域。The invention relates to a crude purification method for hemicellulosome analogs produced by cellulobacteria, belonging to the technical field of industrial biology.

背景技术Background technique

半纤维小体类似物可由一种纤维微细菌发酵产生。发酵液成分复杂,除半纤维小体类似物外,还含有菌体、蛋白质、色素、残糖及发酵副产物等杂质,将严重影响半纤维小体类似物的分离提纯和产品的品质。目前常用于发酵液预处理的方法有:传统过滤、高速离心分离以及膜分离。过滤是在推动力或者其他外力作用下悬浮液(或含固体颗粒发热气体)中的液体(或气体)透过介质,固体颗粒及其他物质被过滤介质截留,从而使固体及其他物质与液体(或气体)分离的操作。但是,该分离方法分离效率低,且耗时较高。离心分离是根据各物质的比重不同而进行分离的方法,但是不能保证在高效去除大分子杂质的同时又保留目的产物在发酵液上清中。而膜分离法也存在同样的问题,并且由于放线菌发酵液成分复杂,在膜分离操作时极易造成膜污染和膜孔堵塞,从而使膜通量锐减。絮凝是指使水或液体中悬浮微粒集聚变大,或形成絮团,从而加快粒子的聚沉,达到固-液分离的目的。通常絮凝的实施靠添加适当的絮凝剂,其作用是吸附微粒,在微粒间“架桥”,从而促进集聚。絮凝技术不仅能有效除去发酵液中的固体微粒以及蛋白质,而且溶解状态的蛋白质等组分也可能在絮凝过程中得到部分去除。目前,投资少、效果好的絮凝预处理方法正在菌体分离中得到应用。絮凝技术在透明质酸发酵液、西梭霉素发酵液、万古霉素发酵液和2,3丁二醇发酵液等预处理上均有成功报道,但是,还没有针对纤维小体类似物发酵液絮凝技术的相关报道。Hemicellulosome analogues can be produced by fermentation of a cellulobacterium. The composition of the fermentation broth is complex. In addition to the hemicellulosome analogs, it also contains impurities such as bacteria, protein, pigment, residual sugar and fermentation by-products, which will seriously affect the separation and purification of the hemicellulosome analogues and the quality of the product. At present, the commonly used methods for pretreatment of fermentation broth are: traditional filtration, high-speed centrifugation and membrane separation. Filtration is when the liquid (or gas) in the suspension (or the heating gas containing solid particles) penetrates the medium under the action of driving force or other external force, and the solid particles and other substances are trapped by the filter medium, so that the solid and other substances and the liquid ( or gas) separation operation. However, this separation method has low separation efficiency and high time consumption. Centrifugation is a method of separating substances according to their specific gravity, but it cannot guarantee that the target product will be kept in the supernatant of the fermentation broth while efficiently removing macromolecular impurities. The membrane separation method also has the same problem, and due to the complex composition of the actinomycete fermentation broth, it is easy to cause membrane fouling and membrane pore blockage during membrane separation operation, thereby reducing the membrane flux sharply. Flocculation refers to the aggregation of suspended particles in water or liquid, or the formation of flocs, so as to accelerate the coagulation and sedimentation of particles and achieve the purpose of solid-liquid separation. Usually, flocculation is implemented by adding an appropriate flocculant, whose function is to adsorb particles and "bridge" between particles, thereby promoting agglomeration. Flocculation technology can not only effectively remove solid particles and proteins in fermentation broth, but also components such as dissolved proteins may be partially removed during the flocculation process. At present, the flocculation pretreatment method with low investment and good effect is being applied in the separation of bacteria. Flocculation technology has been successfully reported in the pretreatment of hyaluronic acid fermentation broth, sisomycin fermentation broth, vancomycin fermentation broth, and 2,3-butanediol fermentation broth. Related reports on liquid flocculation technology.

为使纤维微细菌所产生的半纤维小体类似物得到粗提纯,同时达到固体微粒、色素、残糖及发酵副产物等杂质去除的目的,需要更高效的粗提纯技术方法。In order to roughly purify the hemicellulosome analogues produced by cellulobacteria, and at the same time achieve the purpose of removing impurities such as solid particles, pigments, residual sugars, and fermentation by-products, more efficient crude purification techniques are needed.

发明内容Contents of the invention

为了解决上述问题,本发明的目的在于,为半纤维小体类似物的粗提纯提供更高效的技术手段。In order to solve the above problems, the purpose of the present invention is to provide more efficient technical means for crude purification of hemicellulosome analogs.

本发明的技术方案:Technical scheme of the present invention:

一种半纤维小体类似物的粗提纯方法,步骤如下:A crude purification method for hemicellulosome analogues, the steps are as follows:

(1)离心(1) centrifugal

将发酵液采用二级串联离心法进行离心处理,离心条件要求必须大于20000g离心20min,转子常数K必须大于900;离心就是利用各物质不同的沉降系数进行分离的一种方法,经过离心处理后的发酵液,绝大部分比目的产物大的细胞等水不溶性物质都可以沉降下来。The fermentation broth is centrifuged by two-stage series centrifugation. The centrifugation conditions must be greater than 20000g and centrifuged for 20 minutes, and the rotor constant K must be greater than 900. Centrifugation is a method of separation using different sedimentation coefficients of various substances. In the fermentation broth, most water-insoluble substances such as cells larger than the target product can settle down.

(2)超滤(2) ultrafiltration

离心后取上清发酵液超滤处理进行浓缩。超滤采用无机陶瓷中空超滤膜,孔径要求10nm<d<50nm,主要目的是截留>50nm的半纤维小体类似物。超滤过程中,要反复加Tris-HCl缓冲液(pH 7.5 50mM)超滤6-10次,每次超滤发酵液将浓缩为原液体积的十分之一。该部分主要目的去除发酵液中比目的产物小的杂质,进一步获得较为纯净的发酵液。After centrifugation, the supernatant fermentation broth was treated by ultrafiltration for concentration. Ultrafiltration adopts inorganic ceramic hollow ultrafiltration membrane, the pore size requirement is 10nm<d<50nm, the main purpose is to intercept the hemifibrillary body analogs >50nm. During the ultrafiltration process, Tris-HCl buffer solution (pH 7.5 50mM) should be added repeatedly for ultrafiltration 6-10 times, and the ultrafiltration fermentation broth will be concentrated to one-tenth of the volume of the stock solution each time. The main purpose of this part is to remove impurities smaller than the target product in the fermentation broth, and to further obtain a relatively pure fermentation broth.

(3)絮凝(3) Flocculation

超滤所制备的浓缩液一般蛋白浓度为20-30mg/mL,但是,此时的超滤浓缩液(即截留液)中仍有大量杂质呈胶体状悬浮,可以采用AlCl3溶液滴加的方式进行絮凝处理,所加入AlCl3应控制在3~7g/L的终浓度,充分颠倒混匀后静置3-5min即可观察到显著絮凝,此时6000g离心10min即可获得目的产物。The concentrated solution prepared by ultrafiltration generally has a protein concentration of 20-30 mg/mL. However, there are still a large amount of impurities suspended in colloidal form in the ultrafiltration concentrated solution (ie, the retentate) at this time, and the AlCl 3 solution can be added dropwise. For flocculation treatment, the added AlCl 3 should be controlled at a final concentration of 3-7g/L. After fully inverting and mixing, stand for 3-5 minutes to observe significant flocculation. At this time, the target product can be obtained by centrifuging at 6000g for 10 minutes.

本发明的有益效果:本发明提供的一种半纤维小体类似物的粗提纯方法,可以去除纤维微细菌发酵液中的菌体、色素、残糖及发酵副产物等杂质,同时保留溶解状态的半纤维小体类似物。本粗提纯方法在去除掉原液中90%的可见杂质的同时,酶活力保留90%以上,为半纤维小体类似物纯品的获得提供有效的技术手段,继而可用于工业生物转化、生物能源、医药中间体制备等领域。Beneficial effects of the present invention: the present invention provides a crude purification method for hemicellulosome analogues, which can remove impurities such as cells, pigments, residual sugar and fermentation by-products in cellulobacteria fermentation broth, while retaining the dissolved state hemifibrillary body analogs. This crude purification method removes 90% of the visible impurities in the stock solution while retaining more than 90% of the enzyme activity, providing an effective technical means for obtaining pure hemicellulosome analogs, which can then be used in industrial biotransformation and bioenergy , Preparation of pharmaceutical intermediates and other fields.

附图说明Description of drawings

图1为10个样品的相对酶活图。Figure 1 is a graph of the relative enzyme activity of 10 samples.

具体实施方式Detailed ways

以下结合附图和技术方案,进一步说明本发明的具体实施方式。The specific implementation manners of the present invention will be further described below in conjunction with the accompanying drawings and technical solutions.

1.离心1. Centrifuge

将纤维微细菌发酵液进行离心处理。离心条件为20000g×10min。离心结束后,弃去沉淀取上清进行下一步操作。The cellulosic microbacteria fermentation broth is subjected to centrifugation. The centrifugation condition is 20000g×10min. After centrifugation, discard the precipitate and take the supernatant for the next step.

2.超滤2. Ultrafiltration

超滤采用的是30L的工业小试级别的超滤设备,设备使用的是气动泵,滤膜是无机陶瓷中空超滤膜,滤膜孔径为50nm,采用pH为7.5的50mM的Tris-HCl缓冲液超滤10次,实验结果总结如表1。超滤结束后,接出截流液备用。The ultrafiltration adopts 30L industrial laboratory level ultrafiltration equipment, the equipment uses a pneumatic pump, and the filter membrane is an inorganic ceramic hollow ultrafiltration membrane with a pore size of 50nm, buffered by 50mM Tris-HCl with a pH of 7.5 The liquid was ultrafiltered 10 times, and the experimental results are summarized in Table 1. After the ultrafiltration is completed, the intercepted liquid is taken out for use.

表1超滤结果总结Table 1 Summary of ultrafiltration results

3.絮凝3. Flocculation

(1)将上述超滤制备的浓缩液分装1mL至10个2mL的EP管中;(1) Dispense 1 mL of the concentrated solution prepared by the above ultrafiltration into ten EP tubes of 2 mL;

(2)按实验顺序分别滴加不同体积的1%(1g/100mL)AlCl3进行絮凝实验;(2) According to the experimental sequence, different volumes of 1% (1g/100mL) AlCl3 were added dropwise to carry out the flocculation experiment;

表2 AlCl3加入量Table 2 AlCl 3 addition amount

(3)絮凝结束后,6000g离心10min;(3) After flocculation, centrifuge at 6000g for 10min;

(4)离心结束后,取上清进行pNPX酶活检测,检测结果如表3,图1。(4) After centrifugation, the supernatant was taken for pNPX enzyme activity detection, and the detection results are shown in Table 3, Figure 1.

表3 pNPX酶活检测结果Table 3 pNPX enzyme activity detection results

4.结果分析4. Result analysis

实验结果说明,当AlCl3加入量为60μL,也即AlCl3终浓度为6g/L时,酶液的胶体状态被破坏,大量黑褐色杂质被絮凝沉淀下来,而上清液中酶活仍能保持为90%左右。The experimental results show that when the amount of AlCl 3 added is 60 μL, that is, when the final concentration of AlCl 3 is 6g/L, the colloidal state of the enzyme solution is destroyed, and a large amount of dark brown impurities are flocculated and precipitated, while the enzyme activity in the supernatant can still Keep it around 90%.

Claims (1)

1. a kind of thick method of purification of hemicellulose corpusculum analog, which is characterized in that steps are as follows:
(1) it is centrifuged
Fermentation liquid is subjected to centrifugal treating using two-stage tandem centrifugal process, centrifugal condition requires to have to be larger than 20000g centrifugation 20min, rotor constant K have to be larger than 900;
(2) ultrafiltration
Supernatant fermentation liquid hyperfiltration treatment is taken to be concentrated after centrifugation;Ultrafiltration uses inorganic ceramic hollow fiber ultrafiltration film, and aperture requires The hemicellulose corpusculum analog of 10nm<d<50nm, retention>50nm;In ultra-filtration process, to add pH 7.5,50mM Tris- repeatedly HCl buffer, ultrafiltration 6-10 times, it is 1/10th of stoste volume that each ultrafiltration fermentation liquid, which will be concentrated,;
(3) it flocculates
Using AlCl3The mode that solution is added dropwise carries out flocculation treatment, AlCl be added to the ultrafiltrate that step (2) obtains3It should control In the final concentration of 3~7g/L, 3-5min is stood after being sufficiently mixed by inversion, that is, observes significant flocculation, and 6000g is centrifuged at this time 10min, i.e. acquisition purpose product.
CN201810684749.0A 2018-06-28 2018-06-28 A kind of thick method of purification of hemicellulose corpusculum analog Withdrawn CN108949703A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201810684749.0A CN108949703A (en) 2018-06-28 2018-06-28 A kind of thick method of purification of hemicellulose corpusculum analog

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201810684749.0A CN108949703A (en) 2018-06-28 2018-06-28 A kind of thick method of purification of hemicellulose corpusculum analog

Publications (1)

Publication Number Publication Date
CN108949703A true CN108949703A (en) 2018-12-07

Family

ID=64487331

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201810684749.0A Withdrawn CN108949703A (en) 2018-06-28 2018-06-28 A kind of thick method of purification of hemicellulose corpusculum analog

Country Status (1)

Country Link
CN (1) CN108949703A (en)

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1186498A (en) * 1995-06-02 1998-07-01 诺沃挪第克公司 Al/Iron Treatment and Membrane Concentration of Protein Solutions
CN1216780A (en) * 1997-11-05 1999-05-19 中国科学院微生物研究所 Tech. and process for extracting pullulan from fermentation liquor
CN103789286A (en) * 2014-02-28 2014-05-14 多多药业有限公司 Preparation method of amylase
CN106701719A (en) * 2017-01-16 2017-05-24 中国科学院合肥物质科学研究院 Method for co-producing vitamin K2 and nattokinase by fermenting bacillus natto
CN106978408A (en) * 2017-03-29 2017-07-25 四川新华扬山野生物有限公司 A kind of production method of the middle temperature alpha amylase of food-grade

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1186498A (en) * 1995-06-02 1998-07-01 诺沃挪第克公司 Al/Iron Treatment and Membrane Concentration of Protein Solutions
CN1216780A (en) * 1997-11-05 1999-05-19 中国科学院微生物研究所 Tech. and process for extracting pullulan from fermentation liquor
CN103789286A (en) * 2014-02-28 2014-05-14 多多药业有限公司 Preparation method of amylase
CN106701719A (en) * 2017-01-16 2017-05-24 中国科学院合肥物质科学研究院 Method for co-producing vitamin K2 and nattokinase by fermenting bacillus natto
CN106978408A (en) * 2017-03-29 2017-07-25 四川新华扬山野生物有限公司 A kind of production method of the middle temperature alpha amylase of food-grade

Non-Patent Citations (3)

* Cited by examiner, † Cited by third party
Title
TONG-YI DOU等: "Functional and structural properties of a novel cellulosome-like multienzyme complex: efficient glycoside hydrolysis of water-insoluble 7-xylosyl-10-deacetylpaclitaxel", 《SCIENTIFIC REPORTS》 *
TONG-YI DOU等: "Isolation and subunit compositions of the xylanosome complexes produced by Cellulosimicrobium species", 《ENZYME AND MICROBIAL TECHNOLOGY》 *
侯爱华等: "细菌纤维小体的结构和功能", 《纤维素科学与技术》 *

Similar Documents

Publication Publication Date Title
RU2541635C2 (en) Method of producing polymer agarose from seaweed extract
CN109337862B (en) Sperm washing solution and preparation method and application thereof
Milburn et al. Selective flocculation of nucleic acids, lipids, and colloidal particles from a yeast cell homogenate by polyethyleneimine, and its scale-up
EP2039777A1 (en) Method for purification of hyaluronic acid salt
SK10632001A3 (en) Process for purifying high molecular weight hyaluronic acid
CN115287275B (en) Method for purifying hyaluronidase
CN103992363B (en) Utilize the method that beer waste yeast prepares trehalose and yeast extract
CN103789373B (en) A kind of method utilizing immobilization enzyme heparin sodium extracting
CN113195730A (en) Method for separating biomass from a solution comprising biomass and at least one oligosaccharide
CN103724456B (en) The Technology for normal-temperature salt-free extraction of heparin sodium
CN102603926B (en) New preparing process of high-titer heparin sodium
CN108949703A (en) A kind of thick method of purification of hemicellulose corpusculum analog
WO2013132506A1 (en) Process for the purification of hyaluronic acid salts (ha) from fermentation broth
CN117925507A (en) Milk exosome and extraction and purification method thereof
CN110804078B (en) Deep decolorization and purification method of glycerol glucoside
CN108456262A (en) A kind of preparation process of high purity heparin sodium
CN111996183A (en) Preparation method of bromelain
CN101215422A (en) The Refining Method of Lac Red Pigment
CN1821276A (en) Device and process for extracting hyaluronic acid by electro-membrane separation technology
CN113373134B (en) A kind of extraction method of N-acetylglucosamine deacetylase
CN113454204B (en) Method for extracting phycocyanin
JP3899462B2 (en) Cancer cell apoptosis inducer
CN102372624A (en) Method for extracting sodium gulonate from sodium gulonate fermented liquid
CN111166873B (en) Crude and pure process for recombinant hansenula polymorpha expressed hand-foot-and-mouth disease vaccine antigen, vaccine stock solution and preparation method thereof
CN113896811B (en) Process for extracting chondroitin sodium sulfate and peptide from bovine trachea by air-floatation method

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: 20181207

WW01 Invention patent application withdrawn after publication