JPS6320031A - Chemical reaction device - Google Patents
Chemical reaction deviceInfo
- Publication number
- JPS6320031A JPS6320031A JP16247186A JP16247186A JPS6320031A JP S6320031 A JPS6320031 A JP S6320031A JP 16247186 A JP16247186 A JP 16247186A JP 16247186 A JP16247186 A JP 16247186A JP S6320031 A JPS6320031 A JP S6320031A
- Authority
- JP
- Japan
- Prior art keywords
- floating body
- chemical reaction
- protein
- injected
- gas
- 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
- 238000006243 chemical reaction Methods 0.000 title claims abstract description 24
- 239000007788 liquid Substances 0.000 claims abstract description 18
- 239000000126 substance Substances 0.000 claims description 9
- 239000006199 nebulizer Substances 0.000 claims description 3
- 238000007599 discharging Methods 0.000 claims 1
- 239000007789 gas Substances 0.000 abstract description 15
- 108090000623 proteins and genes Proteins 0.000 abstract description 9
- 102000004169 proteins and genes Human genes 0.000 abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 6
- 239000000463 material Substances 0.000 abstract description 5
- DTQVDTLACAAQTR-UHFFFAOYSA-N Trifluoroacetic acid Chemical compound OC(=O)C(F)(F)F DTQVDTLACAAQTR-UHFFFAOYSA-N 0.000 abstract description 4
- 229920006362 Teflon® Polymers 0.000 abstract description 3
- 239000011521 glass Substances 0.000 abstract description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 abstract description 2
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 abstract description 2
- 229910000041 hydrogen chloride Inorganic materials 0.000 abstract description 2
- 239000007858 starting material Substances 0.000 abstract 2
- 230000007062 hydrolysis Effects 0.000 abstract 1
- 238000006460 hydrolysis reaction Methods 0.000 abstract 1
- 238000002347 injection Methods 0.000 description 5
- 239000007924 injection Substances 0.000 description 5
- 239000000376 reactant Substances 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 239000004809 Teflon Substances 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000007791 liquid phase Substances 0.000 description 2
- 239000003595 mist Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000012459 cleaning agent Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 239000012071 phase Substances 0.000 description 1
- 108090000765 processed proteins & peptides Proteins 0.000 description 1
- 239000003531 protein hydrolysate Substances 0.000 description 1
- 230000007065 protein hydrolysis Effects 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 230000000717 retained effect Effects 0.000 description 1
- 238000007086 side reaction Methods 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J4/00—Feed or outlet devices; Feed or outlet control devices
- B01J4/001—Feed or outlet devices as such, e.g. feeding tubes
- B01J4/002—Nozzle-type elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J10/00—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor
- B01J10/02—Chemical processes in general for reacting liquid with gaseous media other than in the presence of solid particles, or apparatus specially adapted therefor of the thin-film type
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J19/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J19/24—Stationary reactors without moving elements inside
- B01J19/2415—Tubular reactors
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/18—Details relating to the spatial orientation of the reactor
- B01J2219/185—Details relating to the spatial orientation of the reactor vertical
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
- B01J2219/19—Details relating to the geometry of the reactor
- B01J2219/194—Details relating to the geometry of the reactor round
- B01J2219/1941—Details relating to the geometry of the reactor round circular or disk-shaped
- B01J2219/1946—Details relating to the geometry of the reactor round circular or disk-shaped conical
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は、微量の化学合成若しくは化学分析等の化学反
応に用いる、化学反応装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a chemical reaction apparatus used for chemical reactions such as trace amounts of chemical synthesis or chemical analysis.
従来、微量の化学合成若しくは、化学分析等の化学反応
に用いる化学反応装置に於て、化学反応物質を固着、保
持する部分は、微粒子を充填したカラムを用いたり、回
転式カップを用いていた。Conventionally, in chemical reaction devices used for chemical reactions such as small amounts of chemical synthesis or chemical analysis, the parts that fix and hold chemical reactants have used columns filled with fine particles or rotating cups. .
例えば、市販のDNA合成装置は前者の例であり又、市
販のペプチド分析装置は後者の例である。For example, a commercially available DNA synthesizer is an example of the former, and a commercially available peptide analyzer is an example of the latter.
従来のカラム式化学反応装置は、少量の化学反応を、液
相で行う場合には優れていたが、微粒子間に入った液体
が、毛細現象によって、浸透してしまうので、液体を排
除しに<<、逆に一度乾燥させたカラムに液体を注入し
た場合は、気泡が生じ、気泡の存在する部分では、反応
が進行しなかったり、副反応によって不純物が生成した
りした。Conventional column-type chemical reaction devices are excellent for performing small amounts of chemical reactions in the liquid phase, but the liquid that gets between the particles permeates through the capillary phenomenon, so it is difficult to remove the liquid. << Conversely, when a liquid was injected into a column that had been dried once, bubbles were generated, and in the areas where the bubbles existed, the reaction did not proceed or impurities were generated due to side reactions.
一方回転式力7ブを用いた方法では、カップの上方には
少量の化学反応物質が、下方には、重力によって多量の
化学反応物質が集中するため、特に高分子物質が反応物
質である場合には、カップの上方と下方で、反応速度が
異なってしまい、反応時間の設定が困難で、収率が低下
する欠点があった。On the other hand, in the method using a rotary force 7, a small amount of the chemically reacting material is concentrated above the cup, and a large amount of the chemically reacting material is concentrated below the cup due to gravity, especially when the reactant is a polymeric substance. This had the disadvantage that the reaction rate was different between the upper and lower parts of the cup, making it difficult to set the reaction time and reducing the yield.
本発明は、前記問題点を解決するために、テーパー管の
、太い端を上に、細い端を下にして設置し、前記テーパ
ー管の中に、テーパー管の下端の内径より大きく、上端
の内径より小さい外径を持つ浮遊体の表面に化学反応物
質を固着、保持させることによって、均質な膜を形成さ
せ、テーパー管内を通過させた反応薬と化学反応を行わ
させ、気相、液相のいずれの反応をもよういに制御でき
る化学反応装置を供給するものである。In order to solve the above-mentioned problems, the present invention installs a tapered pipe with the thick end on top and the thin end on the bottom, and inside the tapered pipe, the inside diameter is larger than the lower end of the tapered pipe, and the upper end of the tapered pipe has a larger inner diameter than the lower end of the tapered pipe. By fixing and retaining the chemical reactant on the surface of the floating body, which has an outer diameter smaller than the inner diameter, a homogeneous film is formed, and a chemical reaction occurs with the reactant passed through the tapered tube, resulting in a gas phase and a liquid phase. The purpose is to provide a chemical reaction device that can control any of the following reactions.
第1図は、本発明による化学反応装置の作用を示す断面
図であり、テーパー管1内に挿入された浮遊体2に、供
給口3から供給した出発試料を固着、保持させるが、そ
のときの出発試料の供給のし方は、液体に出発試料を溶
解又は懸濁した液体を、供給する場合と、出発試料を、
液解又は懸濁した気体を、ガス又は霧として供給する場
合があり、出発試料中の、化学反応物質を、吸着又は、
化学結合によって、浮遊体表面に固着、保持させた後、
洗浄用のガス又は液体を供給口から供給し、浮遊体表面
に固着、保持された出発試料以外の余剰出発試料をテー
パー管中へ、排出し、順次、反応薬や洗浄剤をガス、霧
、又は液体として供給することによって、所定の化学反
応を進行させる事ができる。FIG. 1 is a sectional view showing the operation of the chemical reaction apparatus according to the present invention, in which a starting sample supplied from a supply port 3 is fixed and retained on a floating body 2 inserted into a tapered tube 1. There are two ways to supply the starting sample: one is to supply a liquid in which the starting sample is dissolved or suspended in a liquid, and the other is to supply the starting sample to a liquid in which the starting sample is dissolved or suspended.
The dissolved or suspended gas may be supplied as a gas or a mist to absorb or adsorb chemically reactive substances in the starting sample.
After being fixed and held on the surface of the floating body through chemical bonding,
A cleaning gas or liquid is supplied from the supply port, excess starting samples other than the starting samples fixed and held on the surface of the floating body are discharged into the tapered tube, and reactants and cleaning agents are sequentially added to the gas, mist, or Alternatively, by supplying it as a liquid, a predetermined chemical reaction can proceed.
第2図は、本発明による化学反応装置の実施例を示す断
面図であり、テフロン製のテーパー管中にガラス製のら
せん形浮遊体を入れて、排出口を有すキャップをかぶせ
、・管材によって、排出物を廃液タンクに誘導している
。一方テーパー管の下端には液体注入ロアと、ガス注入
口6と、排液口8を備えたネブライザ9が接続され、排
液口8は、排液時のみ開放する様に、栓を備えている。FIG. 2 is a sectional view showing an embodiment of the chemical reaction apparatus according to the present invention, in which a glass spiral floating body is placed in a Teflon tapered tube, and a cap with a discharge port is covered. This directs the waste to the waste tank. On the other hand, a nebulizer 9 equipped with a liquid injection lower, a gas injection port 6, and a liquid drain port 8 is connected to the lower end of the tapered tube, and the liquid drain port 8 is equipped with a stopper so as to be opened only when draining the liquid. There is.
上記化学反応装置を使用して、例えば、蛋白質の加水分
解を行うときは、第一に液体注入口から、出発試料であ
る蛋白質の水溶液を注入すると同時にガス注入口から窒
素ガスを注入すると、出発試料は霧状となり、テーパー
管内を上昇し、テーパー管内壁及び浮遊体表面に付着さ
せると共に、浮遊体は、ガス圧により、押し上げられる
と同時に、回・ 転するが、ガラス製の浮遊体表面には
出発試料中の蛋白質が吸着するが、テフロン製のテーパ
ー管内壁に付着した出発試料は、その内部に含有する蛋
白質と共に水滴として落下し、ネブライザ下部にたまり
、回収して再度液体注入口から注入することができ、第
二にガス注入口から、三弗化酢酸と塩化水素と、水蒸気
の高温混合ガスを注入すると、浮遊体表面に付着した蛋
白質は加水分解され、次に、ガス注入口から注入された
窒素ガスによって残存する混合ガスが排除され、最後に
、液体注入口から注水した水に、浮遊体表面の蛋白質加
水分解物が溶解し、排液口から取り出すことができ〔発
明の効果〕
本発明によれば、均一な反応を行うことができるので、
反応条件の設定が容易で、しかも高い収率を得ることが
できるという著しい効果を達成できるものである。For example, when performing protein hydrolysis using the chemical reaction apparatus described above, first inject an aqueous solution of protein, which is a starting sample, from the liquid injection port, and at the same time inject nitrogen gas from the gas injection port. The sample becomes atomized and rises inside the tapered tube, adhering to the inner wall of the tapered tube and the surface of the floating body.The floating body is pushed up by the gas pressure and rotates at the same time, but it does not touch the surface of the glass floating body. The protein in the starting sample is adsorbed, but the starting sample adhering to the inner wall of the tapered Teflon tube falls as water droplets along with the proteins contained inside, collects at the bottom of the nebulizer, and is collected and injected again from the liquid inlet. Second, when a high-temperature mixed gas of trifluoroacetic acid, hydrogen chloride, and water vapor is injected from the gas inlet, the proteins attached to the surface of the floating body are hydrolyzed, and then the proteins attached to the surface of the floating body are hydrolyzed. The remaining mixed gas is removed by the injected nitrogen gas, and finally, the protein hydrolyzate on the surface of the floating body is dissolved in the water injected from the liquid injection port, and can be taken out from the drain port. ] According to the present invention, since a uniform reaction can be carried out,
It is possible to easily set reaction conditions and to obtain a high yield, which is a remarkable effect.
第1図は本発明による化学反応装置の作用を示す断面図
、第2図は、本発明の実施例を示す断面図である。
1・・・テーパー管
2・・・浮遊体
3・・・供給口
以上
第1図
第2図FIG. 1 is a sectional view showing the operation of a chemical reaction apparatus according to the present invention, and FIG. 2 is a sectional view showing an embodiment of the present invention. 1... Tapered tube 2... Floating body 3... Above the supply port Figure 1 Figure 2
Claims (1)
の内径が前記浮遊体の外径よりも細く、上端の内径は前
浮遊体よりも太いテーパー管より成る化学反応装置。 2)前記テーパー管の下端にネブライザを接続した事を
特徴とした前記特許請求の範囲第1項記載の化学反応装
置。 3)前記テーパー管の上端若しくは下端に液体若しくは
気体を給排する手段を具備する事を特徴とした前記特許
請求の範囲第1項及び第2項記載の化学反応装置。 4)前記浮遊体をらせん形にしたことを特徴とした前記
特許請求の範囲第1項、第2項及び第3項記載の化学反
応装置。[Claims] 1) A floating body for fixing and holding a chemically reactive substance, and a tapered tube whose inner diameter at the lower end is thinner than the outer diameter of the floating body and whose inner diameter at the upper end is thicker than the front floating body. Chemical reactor. 2) The chemical reaction device according to claim 1, characterized in that a nebulizer is connected to the lower end of the tapered tube. 3) The chemical reaction apparatus according to claims 1 and 2, further comprising means for supplying and discharging liquid or gas to the upper end or lower end of the tapered tube. 4) The chemical reaction device according to Claims 1, 2, and 3, wherein the floating body has a spiral shape.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16247186A JPS6320031A (en) | 1986-07-10 | 1986-07-10 | Chemical reaction device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP16247186A JPS6320031A (en) | 1986-07-10 | 1986-07-10 | Chemical reaction device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPS6320031A true JPS6320031A (en) | 1988-01-27 |
Family
ID=15755254
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP16247186A Pending JPS6320031A (en) | 1986-07-10 | 1986-07-10 | Chemical reaction device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6320031A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5585574A (en) * | 1993-02-02 | 1996-12-17 | Mitsubishi Materials Corporation | Shaft having a magnetostrictive torque sensor and a method for making same |
| US8124697B2 (en) | 2008-02-27 | 2012-02-28 | Westlake Longview Corporation | Method of preventing or reducing agglomeration on grid in fluidized-bed vessel |
| US8129482B2 (en) | 2008-02-27 | 2012-03-06 | Westlake Longview Corporation | Method of preventing or reducing polymer agglomeration on grid in fluidized-bed reactors |
-
1986
- 1986-07-10 JP JP16247186A patent/JPS6320031A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5585574A (en) * | 1993-02-02 | 1996-12-17 | Mitsubishi Materials Corporation | Shaft having a magnetostrictive torque sensor and a method for making same |
| US8124697B2 (en) | 2008-02-27 | 2012-02-28 | Westlake Longview Corporation | Method of preventing or reducing agglomeration on grid in fluidized-bed vessel |
| US8129482B2 (en) | 2008-02-27 | 2012-03-06 | Westlake Longview Corporation | Method of preventing or reducing polymer agglomeration on grid in fluidized-bed reactors |
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