JPH09291A - Method for synthesizing active protein in cell-free protein synthesis system - Google Patents

Method for synthesizing active protein in cell-free protein synthesis system

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Publication number
JPH09291A
JPH09291A JP14854495A JP14854495A JPH09291A JP H09291 A JPH09291 A JP H09291A JP 14854495 A JP14854495 A JP 14854495A JP 14854495 A JP14854495 A JP 14854495A JP H09291 A JPH09291 A JP H09291A
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JP
Japan
Prior art keywords
cell
protein
treatment
protein synthesis
synthesis system
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
Application number
JP14854495A
Other languages
Japanese (ja)
Inventor
Tomoko Takeshita
智子 竹下
Norio Shimizu
範夫 清水
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Hitachi Ltd
Original Assignee
Hitachi Ltd
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Filing date
Publication date
Application filed by Hitachi Ltd filed Critical Hitachi Ltd
Priority to JP14854495A priority Critical patent/JPH09291A/en
Publication of JPH09291A publication Critical patent/JPH09291A/en
Pending legal-status Critical Current

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  • Preparation Of Compounds By Using Micro-Organisms (AREA)

Abstract

(57)【要約】 【目的】 無細胞系において活性型の蛋白質を合成する
方法を提供する。 【構成】 合成反応液から透析処理あるいは塩析処理ま
たはそれらの組合せによって還元剤を除去し、酸化条件
とすることにより、目的蛋白質に正しい構造を保持さ
せ、比活性を上昇させる。
(57) [Summary] [Objective] To provide a method for synthesizing an active protein in a cell-free system. [Structure] The reducing agent is removed from the synthetic reaction solution by dialysis treatment, salting-out treatment, or a combination thereof, and an oxidizing condition is applied so that the target protein retains a correct structure and the specific activity is increased.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は無細胞蛋白質合成系にお
いて、特に、蛋白質分子内にジスルフィド結合を有する
蛋白質を合成する際に、正しいジスルフィド結合を有す
る活性型蛋白質を合成する方法に関する。
TECHNICAL FIELD The present invention relates to a cell-free protein synthesis system, and more particularly to a method for synthesizing an active protein having a correct disulfide bond when synthesizing a protein having a disulfide bond in a protein molecule.

【0002】[0002]

【従来の技術】従来、無細胞系による蛋白質合成方法
は、主として連続系を用いた大量生産手段、あるいはバ
ッチ法を用いた遺伝子解析の手段として提案されている
(特表平5−505095号、特表平6−503477
号)。これらの方法によって、目的の蛋白質を効率的に
得ることが可能になった。
2. Description of the Related Art Conventionally, a cell-free protein synthesis method has been proposed mainly as a means for mass production using a continuous system or a means for gene analysis using a batch method (Japanese Patent Publication No. 5-505095). Special table flat 6-503477
issue). By these methods, it became possible to efficiently obtain the target protein.

【0003】しかし、無細胞系において、合成された蛋
白質の種類によっては、活性がないかまたは低いものが
多いという問題点があった。
However, in the cell-free system, there was a problem that many of them were inactive or low in activity depending on the kind of the synthesized protein.

【0004】[0004]

【発明が解決しようとする課題】上記の問題点を解決す
るために、無細胞系により合成された蛋白質の形態がど
のようになっているかを3個のジスルフィド結合を有す
るヒト神経成長因子(hNGF)を用いて検討した。合
成されたhNGFをSDS−PAGEにて分析した結
果、hNGF蛋白質分子内に6個あるシステインはジス
ルフィド結合を形成しておらず、フリーの状態になって
いることが判明した。
In order to solve the above-mentioned problems, the form of the protein synthesized by the cell-free system is determined, and the human nerve growth factor (hNGF) having three disulfide bonds. ) Was used. As a result of analyzing the synthesized hNGF by SDS-PAGE, it was found that six cysteines in the hNGF protein molecule did not form a disulfide bond and were in a free state.

【0005】このことは、無細胞蛋白質合成系では、反
応試薬としてDTT(ジチオトレイトール)等の還元剤
を添加しており、これらによって反応系が還元状態にな
っているため、ジスルフィド結合を形成できないのでは
ないかと考えられた。
This is because in the cell-free protein synthesis system, a reducing agent such as DTT (dithiothreitol) is added as a reaction reagent, and the reaction system is in a reduced state by these, so that a disulfide bond is formed. I thought it was impossible.

【0006】このような状態の蛋白質は凝集して不溶性
顆粒を形成し易いし、間違ったジスルフィド結合が形成
されることによって比活性が低下する原因となる。つま
り、細胞の蛋白質合成装置であるリボゾームで合成され
た紐状の蛋白質が活性の有る高次構造を形成できるよう
にすることが必要になる。このためには、無細胞蛋白質
合成系に人為的に添加された還元剤を蛋白質合成後、除
去し、正しいジスルフィド結合を形成させるために蛋白
質溶液を酸化条件下に保持する必要がある。
[0006] Proteins in such a state tend to aggregate to form insoluble granules, and the formation of an incorrect disulfide bond causes a decrease in specific activity. In other words, it is necessary to enable a string-like protein synthesized by ribosome, which is a protein synthesizer of cells, to form an active higher-order structure. For this purpose, it is necessary to remove the reducing agent artificially added to the cell-free protein synthesis system after the protein synthesis and remove it, and keep the protein solution under oxidizing conditions in order to form a correct disulfide bond.

【0007】本発明は、合成反応後の目的蛋白質を含ん
だ反応液から還元剤を除去し、酸化条件下におくことに
より、比活性を上昇させる方法を提供するものである。
The present invention provides a method for increasing the specific activity by removing the reducing agent from the reaction solution containing the target protein after the synthesis reaction and subjecting it to oxidizing conditions.

【0008】[0008]

【課題を解決するための手段】蛋白質合成反応液に含ま
れている還元剤の分子量は、例えばDTTが154であ
り、低分子物質であるため、透析処理や塩析処理により
除去することが可能である。
[Means for Solving the Problems] The molecular weight of the reducing agent contained in the protein synthesis reaction solution is, for example, DTT of 154, which is a low-molecular substance and can be removed by dialysis treatment or salting-out treatment. Is.

【0009】透析処理は、半透膜を用いて低分子物質を
蛋白質のような高分子物質溶液から除去する操作であ
り、セロファンチューブやコロジオン膜等が使用でき
る。また、限外濾過によって低分子物質を除去すること
も可能である。
The dialysis treatment is an operation of removing a low molecular weight substance from a high molecular weight substance solution such as a protein using a semipermeable membrane, and a cellophane tube, collodion membrane or the like can be used. It is also possible to remove low molecular weight substances by ultrafiltration.

【0010】本発明の実施例でも、透析処理はセロファ
ンチューブを用い、セロファンチューブ内に無細胞蛋白
質合成反応液を入れ、透析外液としてpH1−10の範
囲の緩衝液を用いて、透析処理を行う。緩衝液は通常2
0mMリン酸緩衝液(pH8.0)が用いられるが、特
に、これに限定されるものではない。透析処理時の温度
は、4−60℃でよいが、望ましくは25℃が良く、透
析時間は、目的蛋白質の種類や無細胞蛋白質合成反応液
の種類によって異なるが、2−120時間、望ましくは
72時間が良い。この透析中に還元剤が除かれていくに
従って、蛋白質溶液は徐々に酸化状態になり、ジスルフ
ィド結合が形成される。
Also in the examples of the present invention, the dialysis treatment uses a cellophane tube, the cell-free protein synthesis reaction solution is put in the cellophane tube, and the dialysis treatment is carried out using a buffer solution in the range of pH 1-10 as the external dialysis solution. To do. Buffer is usually 2
A 0 mM phosphate buffer solution (pH 8.0) is used, but it is not particularly limited thereto. The temperature during the dialysis treatment may be 4 to 60 ° C., preferably 25 ° C., and the dialysis time varies depending on the type of the target protein and the type of cell-free protein synthesis reaction solution, but it is preferably 2 to 120 hours, preferably 72 hours is good. As the reducing agent is removed during this dialysis, the protein solution gradually becomes in an oxidized state and a disulfide bond is formed.

【0011】塩析処理は、蛋白質等の高分子電解質溶液
に大量の塩類を加えて溶解度を低下させることにより、
目的の蛋白質を沈殿させる操作であり、これによって、
蛋白質の分別ができると共に、還元剤を除去可能であ
る。塩類としては、リン酸塩、硫酸塩が利用できるが、
望ましくは硫酸アンモニウムが良い。硫酸アンモニウム
の最終濃度は、20−80%の範囲が用いられるが、目
的の蛋白質の性質によって適切な最終濃度を選択する必
要がある。
The salting-out treatment is carried out by adding a large amount of salts to a polymer electrolyte solution such as protein to reduce the solubility.
This is an operation to precipitate the target protein.
The protein can be separated and the reducing agent can be removed. As salts, phosphates and sulfates can be used,
Ammonium sulfate is preferable. The final concentration of ammonium sulfate used is in the range of 20-80%, but it is necessary to select an appropriate final concentration depending on the properties of the protein of interest.

【0012】なお、塩析による蛋白質の沈殿分離後、沈
殿した蛋白質を緩衝液に溶解した後、透析処理によって
塩析に使用した塩類を除去することが必要である。この
際の透析処理は、上記の透析処理と同様に実施できる
が、透析時間の短縮が可能である。ジスルフィド結合の
形成は、塩析による蛋白質沈殿中や塩類除去のための透
析処理中に徐々に行われる。
After precipitation and separation of the protein by salting out, it is necessary to dissolve the precipitated protein in a buffer solution and then to remove salts used for salting out by dialysis. The dialysis treatment at this time can be performed in the same manner as the above dialysis treatment, but the dialysis time can be shortened. The formation of disulfide bonds is gradually performed during protein precipitation by salting out and during dialysis treatment for salt removal.

【0013】無細胞蛋白質合成反応後に、還元剤を透析
処理または塩析処理によって除去することにより、蛋白
質溶液は酸化状態になり、ジスルフィド結合が形成され
るのであるが、これらの処理を組み合わせることによっ
て、より効率的な還元剤除去と酸化反応が可能である。
また、塩析処理は目的の蛋白質を特異的に沈殿分離する
ことができるため、蛋白質を精製することになり、有利
である。
After the cell-free protein synthesis reaction, the reducing agent is removed by dialysis treatment or salting-out treatment, so that the protein solution becomes in an oxidized state and a disulfide bond is formed. , More efficient reducing agent removal and oxidation reaction are possible.
Further, the salting-out treatment is advantageous in that the target protein can be specifically precipitated and separated, so that the protein is purified.

【0014】塩析処理後に透析処理をする組合せの場
合、透析による蛋白質の酸化が主体となるが、後述する
ように、処理に要する時間を短縮する上でのメリットが
大きい。
In the case of a combination in which dialysis treatment is carried out after salting-out treatment, protein oxidation by dialysis is the main component, but as will be described later, there is a great advantage in reducing the time required for treatment.

【0015】本発明は、無細胞蛋白質合成系において、
回分式または連続式いずれの場合においても適用可能で
ある。連続式では連続式の限外濾過を用いることによ
り、効率的な蛋白質合成が可能になる。
The present invention relates to a cell-free protein synthesis system,
It is applicable to both batch type and continuous type. In the continuous method, efficient protein synthesis becomes possible by using continuous ultrafiltration.

【0016】[0016]

【作用】本発明では、無細胞系による蛋白質合成反応後
の反応液から透析処理あるいは塩析処理後に透析処理を
する組合せによって還元剤を除去し、かつ酸化条件とす
ることができるので、目的蛋白質に正しい構造を保持さ
せることができ、その比活性の上昇が可能になる。
In the present invention, the reducing agent can be removed from the reaction solution after the protein synthesis reaction in the cell-free system by a combination of dialysis treatment or salting-out treatment followed by dialysis treatment, and the oxidizing condition can be obtained. Can retain the correct structure and increase its specific activity.

【0017】[0017]

【実施例】無細胞蛋白質合成系としてはZubayらが
開発した大腸菌のS−30抽出液を用いる転写翻訳共役
系を使用し、hNGFを合成した。合成後の反応液、透
析処理、硫安塩析処理後の反応液に含まれるhNGFの
量は抗ヒト抗体を用いたウエスタンブロッティングの発
色量から換算した。また、比活性はニワトリ胚後根神経
節から単離した培養細胞系の神経突起の伸展によって測
定した。なお、標品として市販のヒト神経成長因子(コ
スモバイオ社)を用いた。
EXAMPLE As a cell-free protein synthesis system, a transcription-translation coupling system using S-30 extract of Escherichia coli developed by Zubay et al. Was used to synthesize hNGF. The amount of hNGF contained in the reaction solution after synthesis, the dialysis treatment, and the reaction solution after ammonium sulfate salting-out treatment was converted from the amount of color developed by Western blotting using an anti-human antibody. Specific activity was also measured by neurite outgrowth in a cultured cell line isolated from chicken embryo dorsal root ganglia. A commercially available human nerve growth factor (Cosmo Bio) was used as a standard.

【0018】(1)大腸菌S−30抽出液の調製 Zubayらの方法によって、T7ポリメラーゼ遺伝子
を挿入した大腸菌JM109(DE3)より、S−30
抽出液を調製した。
(1) Preparation of Escherichia coli S-30 Extract S-30 was obtained from Escherichia coli JM109 (DE3) into which the T7 polymerase gene had been inserted by the method of Zubay et al.
An extract was prepared.

【0019】(2)プラスミドDNA 高効率で転写を行うT7プロモータの下流にhNGF遺
伝子を組み込んだプラスミドDNA、pT7MNGFを
鋳型として用いた。
(2) Plasmid DNA pT7MNGF, which is a plasmid DNA in which the hNGF gene is incorporated downstream of the T7 promoter for highly efficient transcription, was used as a template.

【0020】(3)合成反応 無細胞蛋白質合成反応は、容量100μl、37℃,2
時間で行った。反応溶液として、16.8μlのS−3
0抽出液、24μgのプラスミドDNA、17μgのt
RNA、56.4mMのTris−酢酸緩衝液(pH
8.4)、2.75mMのDTT、1.22mMのAT
P、0.75mMのCTP・GTP・UTP、27.0
mMのホスホエノールピルビン酸、0.64mMのcA
MP、34.6μgのフォリン酸、1.9%のポリエチ
レングリコール6000、11.7mMの酢酸マグネシ
ウム、36mMの酢酸アンモニウム、72mMの酢酸カ
リウム、および0.2mMの蛋白質を構成する20種類
のアミノ酸から成る混合物を用いた。
(3) Synthetic reaction The cell-free protein synthetic reaction was carried out at a volume of 100 μl, 37 ° C., and 2
Went in time. As a reaction solution, 16.8 μl of S-3
0 extract, 24 μg plasmid DNA, 17 μg t
RNA, 56.4 mM Tris-acetate buffer (pH
8.4) 2.75 mM DTT, 1.22 mM AT
P, 0.75 mM CTP / GTP / UTP, 27.0
mM Phosphoenolpyruvate, 0.64 mM cA
Comprised of MP, 34.6 μg folinic acid, 1.9% polyethylene glycol 6000, 11.7 mM magnesium acetate, 36 mM ammonium acetate, 72 mM potassium acetate, and 20 amino acids that make up 0.2 mM protein. The mixture was used.

【0021】(4)透析 合成反応後、ただちに反応液を氷冷し、続いて透析用セ
ロファンチューブに移した。その後、1000倍の液量
の20mM燐酸緩衝液(pH8.0)に対して透析処理
を25℃、72時間行い、hNGF蛋白質を得た。。な
お、透析外液は12時間ごとに全量交換した。
(4) Dialysis After the synthesis reaction, the reaction solution was immediately cooled with ice and then transferred to a dialysis cellophane tube. Then, a dialysis treatment was carried out at 25 ° C. for 72 hours against a 1000-fold volume of 20 mM phosphate buffer (pH 8.0) to obtain hNGF protein. . The total amount of the external dialysate was replaced every 12 hours.

【0022】(5)硫安塩析 合成反応後、ただちに反応液を氷冷し、最終濃度40%
となるように硫酸アンモニウムを加え、12時間、4℃
にて静置した。塩析した反応液を15000rpm、4
℃、10分間遠心し、沈殿物を回収し、20mM燐酸緩
衝液(pH8.0)に再懸濁した。
(5) Salting Out with Ammonium Sulfate Immediately after the synthesis reaction, the reaction solution was cooled with ice to give a final concentration of 40%.
Ammonium sulphate for 12 hours at 4 ° C
At rest. The reaction solution salted out was 15,000 rpm, 4
The precipitate was collected by centrifugation at 10 ° C for 10 minutes and resuspended in 20 mM phosphate buffer (pH 8.0).

【0023】(6)硫安塩析後に透析 合成反応後、ただちに反応液を氷冷し、最終濃度40%
となるように硫酸アンモニウムを加え、12時間、4℃
にて静置した。塩析した反応液を15000rpm、4
℃、10分間遠心し、沈殿物を回収し、20mM燐酸緩
衝液(pH8.0)に再懸濁した。さらに15000r
pm、4℃、10分間遠心し、上清液を回収した。回収
した上清液を1000倍の液量の20mM燐酸緩衝液
(pH8.0)に対して25℃、12時間、透析処理し
てhNGF蛋白質を得た。
(6) Dialysis after salting out with ammonium sulfate Immediately after the synthesis reaction, the reaction solution was cooled with ice to give a final concentration of 40%.
Ammonium sulphate for 12 hours at 4 ° C
At rest. The reaction solution salted out was 15,000 rpm, 4
The precipitate was collected by centrifugation at 10 ° C for 10 minutes and resuspended in 20 mM phosphate buffer (pH 8.0). 15,000r
It was centrifuged at pm, 4 ° C. for 10 minutes, and the supernatant was collected. The recovered supernatant was dialyzed against 1000 mM volume of 20 mM phosphate buffer (pH 8.0) at 25 ° C. for 12 hours to obtain hNGF protein.

【0024】(7)生物活性 ニワトリ8日胚の後根神経節由来の神経細胞の初代培養
系を用いて、無細胞系によって合成されたhNGFの生
物活性を測定した。神経細胞に対し、標品、一定液量の
反応液、透析処理後の反応液、硫安塩析処理後の反応液
を投与し、投与から72時間後の神経線維の突起を有す
る細胞数を計数し、該当する標品濃度から各反応液中の
活性を有するhNGF量を算出した。この際、投与した
反応液中に含まれるhNGFの全量は抗hNGF抗体を
用いたウエスタンブロッテイングの発色量から算出し
た。反応液中のhNGFの全量と活性を有するhNGF
量の比から、未処理、硫安塩析処理、透析処理および硫
安塩析処理後に透析処理を施す処理のそれぞれによる還
元剤の除去および酸化反応の進行の効果を図1に比較し
て示す。この結果、未処理のものあるいは硫安塩析処理
と比較して、透析処理または硫安塩析処理後に透析処理
を施したものは、比活性は格段に向上していることが分
かった。これらのデータからも分かるように、硫安塩析
処理後に透析処理を施す場合は、比活性において透析処
理を施したものに遜色が無く、処理時間が1/3で済む
というメリットがある。
(7) Biological activity The biological activity of hNGF synthesized by the cell-free system was measured using a primary culture system of neurons derived from dorsal root ganglia of the 8-day-old chicken. A standard preparation, a fixed amount of reaction solution, a reaction solution after dialysis treatment, and a reaction solution after ammonium sulfate salting-out treatment were administered to nerve cells, and the number of cells having nerve fiber protrusions was counted 72 hours after administration. Then, the amount of active hNGF in each reaction solution was calculated from the corresponding standard concentration. At this time, the total amount of hNGF contained in the administered reaction solution was calculated from the amount of color developed by Western blotting using an anti-hNGF antibody. HNGF having activity and total amount of hNGF in reaction solution
From the ratio of the amounts, the effects of removing the reducing agent and advancing the oxidation reaction by each of the untreated, ammonium sulfate salting-out treatment, dialysis treatment, and treatment after performing dialysis treatment after ammonium sulfate salting-out treatment are shown in comparison with FIG. As a result, it was found that the specific activity of the untreated one or the one subjected to the dialysis treatment after the dialysis treatment or the ammonium sulfate salting-out treatment was markedly improved as compared with the untreated one. As can be seen from these data, when the dialysis treatment is performed after the ammonium sulfate salting-out treatment, there is an advantage that the dialysis treatment is comparable in specific activity and the treatment time is 1/3.

【0025】[0025]

【発明の効果】本発明では、蛋白質合成反応後に、目的
蛋白質を含んだ反応液に対し、透析処理あるいは塩析処
理、またはそれらの組み合わせによって、反応液から還
元剤を除去し、酸化反応を進行させることにより、目的
蛋白質に正しい構造を保持させ、比活性を上昇させるこ
とができる。
INDUSTRIAL APPLICABILITY According to the present invention, after the protein synthesis reaction, the reaction solution containing the target protein is subjected to dialysis treatment, salting-out treatment, or a combination thereof to remove the reducing agent from the reaction solution and proceed with the oxidation reaction. By doing so, the target protein can retain the correct structure and the specific activity can be increased.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の無細胞蛋白質合成系により合成された
hNGFの比活性を示す図。
FIG. 1 shows the specific activity of hNGF synthesized by the cell-free protein synthesis system of the present invention.

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】無細胞蛋白質合成系の合成反応液から還元
剤を除去し、かつ酸化条件にすることを特徴とする無細
胞蛋白質合成系における活性型蛋白質の合成方法。
1. A method for synthesizing an active protein in a cell-free protein synthesis system, which comprises removing a reducing agent from a synthesis reaction solution of the cell-free protein synthesis system and applying oxidizing conditions.
【請求項2】還元剤を除去する方法が透析処理である請
求項1記載の無細胞蛋白質合成系における活性型蛋白質
の合成方法。
2. The method for synthesizing an active protein in a cell-free protein synthesis system according to claim 1, wherein the method for removing the reducing agent is dialysis.
【請求項3】還元剤を除去する方法が塩析処理後に透析
処理をするものである請求項1記載の無細胞蛋白質合成
系における活性型蛋白質の合成方法。
3. The method for synthesizing an active protein in a cell-free protein synthesis system according to claim 1, wherein the method for removing the reducing agent is a dialysis treatment after a salting-out treatment.
【請求項4】無細胞蛋白質合成系の蛋白質合成反応後の
反応液から還元剤を除去し、かつ酸化条件にすることを
特徴とする無細胞蛋白質合成系における活性型蛋白質の
合成方法。
4. A method for synthesizing an active protein in a cell-free protein synthesis system, which comprises removing a reducing agent from a reaction solution after a protein synthesis reaction in a cell-free protein synthesis system and applying oxidizing conditions.
【請求項5】還元剤を除去する方法が透析処理である請
求項4記載の無細胞蛋白質合成系における活性型蛋白質
の合成方法。
5. The method for synthesizing an active protein in a cell-free protein synthesis system according to claim 4, wherein the method for removing the reducing agent is dialysis treatment.
【請求項6】還元剤を除去する方法が塩析処理後に透析
処理をするものである請求項4記載の無細胞蛋白質合成
系における活性型蛋白質の合成方法。
6. The method for synthesizing an active protein in a cell-free protein synthesis system according to claim 4, wherein the method of removing the reducing agent is a dialysis treatment after a salting-out treatment.
JP14854495A 1995-06-15 1995-06-15 Method for synthesizing active protein in cell-free protein synthesis system Pending JPH09291A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14854495A JPH09291A (en) 1995-06-15 1995-06-15 Method for synthesizing active protein in cell-free protein synthesis system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14854495A JPH09291A (en) 1995-06-15 1995-06-15 Method for synthesizing active protein in cell-free protein synthesis system

Publications (1)

Publication Number Publication Date
JPH09291A true JPH09291A (en) 1997-01-07

Family

ID=15455149

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14854495A Pending JPH09291A (en) 1995-06-15 1995-06-15 Method for synthesizing active protein in cell-free protein synthesis system

Country Status (1)

Country Link
JP (1) JPH09291A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1143009A4 (en) * 1998-12-14 2002-03-27 Riken PROCESS FOR PRODUCING POLYPEPTIDE IN A CELLULAR PROTEIN SYNTHESIS SYSTEM
US6702487B2 (en) 2001-03-30 2004-03-09 Konica Corporation Photographic processor for silver halide photographic material and remote control system for the processor
US6987174B2 (en) 2003-04-01 2006-01-17 Fuji Photo Film Co., Ltd. Azo compound, colorant-containing curable composition, color filter and color filter production method
US8734856B2 (en) * 2002-01-31 2014-05-27 Cellfree Sciences Co., Ltd. Cell extract for cell-free protein synthesis and process for producing the same

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1143009A4 (en) * 1998-12-14 2002-03-27 Riken PROCESS FOR PRODUCING POLYPEPTIDE IN A CELLULAR PROTEIN SYNTHESIS SYSTEM
US6702487B2 (en) 2001-03-30 2004-03-09 Konica Corporation Photographic processor for silver halide photographic material and remote control system for the processor
US8734856B2 (en) * 2002-01-31 2014-05-27 Cellfree Sciences Co., Ltd. Cell extract for cell-free protein synthesis and process for producing the same
US6987174B2 (en) 2003-04-01 2006-01-17 Fuji Photo Film Co., Ltd. Azo compound, colorant-containing curable composition, color filter and color filter production method

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