[go: up one dir, main page]

JPS62277142A - High-pressure chemical reactor - Google Patents

High-pressure chemical reactor

Info

Publication number
JPS62277142A
JPS62277142A JP12081186A JP12081186A JPS62277142A JP S62277142 A JPS62277142 A JP S62277142A JP 12081186 A JP12081186 A JP 12081186A JP 12081186 A JP12081186 A JP 12081186A JP S62277142 A JPS62277142 A JP S62277142A
Authority
JP
Japan
Prior art keywords
reaction
water
reaction product
material supply
pressure
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
JP12081186A
Other languages
Japanese (ja)
Inventor
Masaru Iwaki
勝 岩城
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.)
Mitsui Construction Co Ltd
Original Assignee
Mitsui Construction 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 Mitsui Construction Co Ltd filed Critical Mitsui Construction Co Ltd
Priority to JP12081186A priority Critical patent/JPS62277142A/en
Publication of JPS62277142A publication Critical patent/JPS62277142A/en
Pending 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
    • B01J3/00Processes of utilising sub-atmospheric or super-atmospheric pressure to effect chemical or physical change of matter; Apparatus therefor
    • B01J3/04Pressure vessels, e.g. autoclaves

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

PURPOSE:To obtain the title reactor of high safety by providing a floating base, a submerged reaction vessel, a material supply pipe connecting the base and the vessel, and a reaction product discharge pipe, and filling water, etc., into the vessel and the pipe. CONSTITUTION:The floating base 1 is safely floated on the surface of the ocean, etc., by a buoyancy means. The reaction vessel 2 is arranged in the water at a specified depth, and connected to the floating base 1 through the material supply pipe 3 and the reaction product discharge pipe 4. The inside of the pipes is filled with a specified liq. such as water. When the depth of the reaction vessel 2 from the water surface to the set position is expressed as H, the water pressure P1 corresponding to the depth H is exerted on the reaction vessel 2 internally and externally when the specified liq. is water. In this constitution, the reactants are supplied into the reaction vessel 2 from the floating base 1 through the material supply pipe 3, and reaction is carried out under high pressure in the reaction vessel 2. The reaction product is recovered at the floating base 1 through the reaction product discharge pipe 4.

Description

【発明の詳細な説明】 3、発明の詳細な説明 (産業上の利用分野) 本発明は、高圧下における化学反応により反応生成物を
製造するための装置に関するものである。
Detailed Description of the Invention 3. Detailed Description of the Invention (Field of Industrial Application) The present invention relates to an apparatus for producing a reaction product by a chemical reaction under high pressure.

(従来の技術) 例えばオートクレーブ装置の如く、高圧あるいは超高圧
の条件Fでの化学反応により、反応生成物を製造するた
めの装置か種々利用されている。
(Prior Art) Various apparatuses, such as autoclave apparatuses, are used for producing reaction products by chemical reactions under conditions F of high pressure or ultra-high pressure.

(発明か解決しようとする問題点) しかしながら、かかる従来の高圧化学反応は、いずれも
J′1i!hに設置した反応装置を用いて行われるもの
てあり、内部に発生する高圧に耐え得るためには、装置
の外郭構造体自体、あるいはその接合部、配管m毛等圧
力のかかるすべての個所を高強度のものにする必要かあ
り、さらに爆発“In等の危険を伴なうため、安全性を
確保するためには装置の建設費や運転管理費か非常に高
価なものとなり、生産効率にも影響していた。
(Problem to be solved by the invention) However, in all such conventional high-pressure chemical reactions, J′1i! In order to withstand the high pressure generated inside, the outer structure of the device itself, its joints, pipes, hair, etc. must be protected from all pressure points. It needs to be made of high-strength material, and it also involves the danger of explosions such as In, so in order to ensure safety, the construction and operation management costs of the equipment are extremely expensive, which reduces production efficiency. was also influenced.

(問凹点を解決するための手段) 本発明は、かかる従来の問題点を解決するために提案さ
れたものであり、高圧下における化学反応により反応生
成物を製造するための装置において、少なくとも水上浮
揚台と、所定深度の水中に配設される反応槽と、前記水
上浮揚台と反応槽とを連絡する材料供給管及び反応生成
物抽出管とを備え、前記反応槽、材料供給管及び反応生
成物抽出管内に水等の所定液を充満することにより、反
応槽の内外の圧力差を可及的に均衡させ、しかも該反応
槽内には所定の高圧を確保するよう構成した高圧化学反
応装置を特徴とするものである。
(Means for Solving the Problems) The present invention has been proposed to solve the problems of the conventional art, and provides at least one method for producing a reaction product through a chemical reaction under high pressure. A water floating platform, a reaction tank disposed in water at a predetermined depth, and a material supply pipe and a reaction product extraction pipe connecting the water floating platform and the reaction tank, the reaction tank, the material supply pipe and A high-pressure chemical system that is configured to balance the pressure difference between the inside and outside of the reaction tank as much as possible by filling the reaction product extraction tube with a specified liquid such as water, and to ensure a specified high pressure within the reaction tank. It features a reactor.

・(実施例) 以下、本発明の好適な実施例を図面により説明する。·(Example) Hereinafter, preferred embodiments of the present invention will be described with reference to the drawings.

第1図は本発明の一実施例を示すものであり、本実施例
に係る高圧化学反応装置は、水ト浮揚台lと、反応槽2
と、材料供給管3と、反応生成物抽出管4と、熱交換器
5と、熱移送管6とを備えている。
FIG. 1 shows an embodiment of the present invention, and the high-pressure chemical reaction apparatus according to the present embodiment includes a water floatation table 1 and a reaction tank 2.
, a material supply pipe 3 , a reaction product extraction pipe 4 , a heat exchanger 5 , and a heat transfer pipe 6 .

前記水上浮揚台1は、例えば海洋等の水面上に所定の浮
力手段により安定状態で浮揚しており、一方、前記反応
槽2は、所定深度の水中に配設されており、木り浮揚台
lと反応槽2とは、前記材料供給管3及び反応生成物抽
出管4により連絡されている。
The water floating platform 1 floats in a stable state on the surface of water, such as the ocean, by a predetermined buoyancy means, while the reaction tank 2 is disposed underwater at a predetermined depth, and is a wooden floating platform. 1 and the reaction tank 2 are connected through the material supply pipe 3 and the reaction product extraction pipe 4.

また、本実施例では、前記反応槽2に前記熱交換器5か
付設されており、該熱交換器5と前記水上浮揚台lとが
熱移送管6にて連絡されているものである。
Further, in this embodiment, the heat exchanger 5 is attached to the reaction tank 2, and the heat exchanger 5 and the water floating platform 1 are connected through a heat transfer pipe 6.

しかして、前記反応槽2、材料供給管31反反応生成物
抽出管及び前記熱交換器5、熱移送管6内には水等の所
定液か充満されており、例えば上記氷面から反応槽2の
配設位置までの水深をHとすると、L記所定液が水の場
合には反応槽2には水深Hに応じた水圧PIか内外から
加わっており、試水a!Hを充分深くすれば1反応槽2
内には超高圧が得られる。
Therefore, the reaction tank 2, the material supply pipe 31, the reaction product extraction pipe, the heat exchanger 5, and the heat transfer pipe 6 are filled with a predetermined liquid such as water. Assuming that the water depth up to the installation position of No. 2 is H, when the prescribed liquid in L is water, water pressure PI corresponding to the water depth H is applied to the reaction tank 2 from inside and outside, and the test water a! If H is made deep enough, 1 reaction tank 2
Ultra-high pressure can be obtained inside.

しかして、反応材料は水り浮揚台lから材料供給管3を
経由して反応槽2内に送給され、該反応槽2内て反応を
終えた反応生ashは、反応生成物抽出管4にを経て水
上浮揚台1にて回収されるようになっている。
Thus, the reaction material is fed into the reaction tank 2 from the water flotation platform 1 via the material supply pipe 3, and the reaction product ash that has completed the reaction in the reaction tank 2 is transferred to the reaction product extraction pipe 4. After that, it is collected on floating platform 1.

また、熱交換器5を備えているため、前記反応が発熱を
伴う反応の場合には1反応後の余剰熱を熱交換し1.8
移送管6から水上浮揚台lに回収し、有効利用可濠であ
る。
In addition, since it is equipped with a heat exchanger 5, if the reaction is one that generates heat, the excess heat after one reaction is heat exchanged.
The moat can be collected from the transfer pipe 6 to the floating platform 1 and used effectively.

一方、と記反応か吸熱反応あるいは加熱を必要とする反
応の場合には、水上浮揚台1上で発生させた熱を熱移送
管6を経由して熱交換器5に送給し、反応材料との熱交
換を行わしめるようになっている。
On the other hand, in the case of the reaction, endothermic reaction, or reaction requiring heating, the heat generated on the floating platform 1 is sent to the heat exchanger 5 via the heat transfer pipe 6, and the reaction material is It is designed to allow heat exchange with the

よって、例えば反応槽2でバイオマス等を熱分解させた
り、石炭と所定の化合物から液化石油を製造させたり等
、種々の高圧化学反応に利用しうる。
Therefore, it can be used for various high-pressure chemical reactions, such as thermally decomposing biomass or the like in the reaction tank 2 or producing liquefied petroleum from coal and a predetermined compound.

しかして、反応槽2は上記の如く内外の圧力が肝衡して
いるので、超高圧反応槽としてa丁近しうるにも拘らず
、従来の地上設置の反応槽の様に内部に発生する高圧に
耐え得るために装置の外郭構造体自体、あるいはその接
合部、配管継手等圧力のかかるすべての個所を高強度の
耐圧構造にする必要かなくなる。
As mentioned above, the pressure inside and outside the reaction tank 2 is balanced, so even though it can be used as an ultra-high-pressure reaction tank, the internal pressure of the reaction tank 2 is not as high as that of a conventional ground-mounted reaction tank. In order to withstand high pressure, it is no longer necessary to make the outer structure of the device itself, its joints, piping joints, and all other places where pressure is applied to a high-strength pressure-resistant structure.

さらに、作業者は水上浮揚台1にて種々の操作を行うこ
とがてき、該水上では何等の高圧も発生していないので
爆発二3故等の危険を全く伴わず、安全性を確保するた
めの装を類の建設も不要となるため、建設費や運転管理
費を非常に安価なものとすることがてき、生産効率も向
、Hさせることがi+ff莞となる。
Furthermore, workers can perform various operations on the floating platform 1, and since no high pressure is generated on the water, there is no risk of explosion or other accidents, and to ensure safety. Since there is no need to construct similar equipment, construction costs and operation and management costs can be made very low, and production efficiency can also be improved.

なお、反応槽2等に充満させる液体か木以外のものの場
合には、外側の水との比重差で若干の内外の圧力差が生
じるか、この場合でも上記J1!!L型の反応槽に比較
すれば耐圧構造は極めて軽微なものて済むこととなる。
In addition, if the liquid to be filled in the reaction tank 2 etc. is something other than wood, there will be a slight pressure difference between the inside and outside due to the difference in specific gravity with the water on the outside, or even in this case, the above J1! ! Compared to an L-shaped reaction tank, the pressure-resistant structure is extremely light.

また、L記実施例では海や湖等の自然の水中を利用する
例を示したか、他の実施例として、土中にケ杭を掘削し
、該ケ杭内に水を張り、上記反応装置を配設することに
より、同様の作用効果を得ることがてきる。
In addition, in Example L, an example was shown in which natural water such as the sea or a lake was used, but in another example, a pile was excavated in the soil, water was filled in the pile, and the above-mentioned reaction equipment was used. By arranging this, similar effects can be obtained.

さらに、熱交換器5や熱移送管6は1反応条件によって
は省略することもできる等、L記実施例に限定されるこ
となく本発明の要旨を逸脱しない範囲内て種々の変形例
が可使であることは言うまでもない。
Furthermore, the heat exchanger 5 and the heat transfer tube 6 may be omitted depending on one reaction condition, and various modifications are possible without being limited to the embodiment described in L without departing from the gist of the present invention. Needless to say, he is a messenger.

(発明の効果) 本発明は上述した如く構成されており、自然の水頭差を
利用して高圧を得るように構成されているため、何重の
耐圧構造をも必要とせず、安全性の確保、経済性の点か
らも極めて有用なものである。
(Effects of the Invention) The present invention is configured as described above, and is configured to obtain high pressure by utilizing the natural water head difference, so there is no need for multiple pressure-resistant structures, and safety can be ensured. , which is extremely useful from an economic point of view.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明の一実施例に係る高圧化学反応型この構
成を示す概念図である。 ■・・・水上浮揚台、    2・・・反応槽、3・・
・材料供給管、 4・・・反応生成物抽出管、 5・−・熱交換器、     6・・・熱移送管。
FIG. 1 is a conceptual diagram showing a high-pressure chemical reaction type structure according to an embodiment of the present invention. ■...Floating platform, 2...Reaction tank, 3...
- Material supply pipe, 4... Reaction product extraction pipe, 5... Heat exchanger, 6... Heat transfer pipe.

Claims (2)

【特許請求の範囲】[Claims] (1)高圧下における化学反応により反応生成物を製造
するための装置において、少なくとも水上浮揚台と、所
定深度の水中に配設される反応槽と、前記水上浮揚台と
反応槽とを連絡する材料供給管及び反応生成物抽出管と
を備え、前記反応槽、材料供給管及び反応生成物抽出管
内に水等の所定液を充満してなることを特徴とする高圧
化学反応装置。
(1) In an apparatus for producing a reaction product through a chemical reaction under high pressure, at least a floating platform, a reaction tank disposed in water at a predetermined depth, and communication between the floating platform and the reaction tank. A high-pressure chemical reaction apparatus comprising a material supply pipe and a reaction product extraction pipe, the reaction tank, the material supply pipe and the reaction product extraction pipe being filled with a predetermined liquid such as water.
(2)前記反応槽は、熱交換器が付設されてなり、該熱
交換器と前記水上浮揚台とが熱移送管にて連絡されてい
る特許請求の範囲第1項記載の高圧化学反応装置。
(2) The high-pressure chemical reaction apparatus according to claim 1, wherein the reaction tank is equipped with a heat exchanger, and the heat exchanger and the floating platform are connected through a heat transfer pipe. .
JP12081186A 1986-05-26 1986-05-26 High-pressure chemical reactor Pending JPS62277142A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP12081186A JPS62277142A (en) 1986-05-26 1986-05-26 High-pressure chemical reactor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP12081186A JPS62277142A (en) 1986-05-26 1986-05-26 High-pressure chemical reactor

Publications (1)

Publication Number Publication Date
JPS62277142A true JPS62277142A (en) 1987-12-02

Family

ID=14795561

Family Applications (1)

Application Number Title Priority Date Filing Date
JP12081186A Pending JPS62277142A (en) 1986-05-26 1986-05-26 High-pressure chemical reactor

Country Status (1)

Country Link
JP (1) JPS62277142A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007062273A (en) * 2005-09-01 2007-03-15 Unitec Resin:Kk Autoclave molding apparatus, autoclave molding method, and autoclave molded product

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5921655A (en) * 1982-07-02 1984-02-03 シエ−リング・アクチエンゲゼルシヤフト Novel carbacycline amide, manufacture and hypotensive, bronchodilating and blood platelet coagulation inhibitive medicine
JPS6178597A (en) * 1984-09-22 1986-04-22 Yoshiaki Nagaura High pressure area generating method and its device

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5921655A (en) * 1982-07-02 1984-02-03 シエ−リング・アクチエンゲゼルシヤフト Novel carbacycline amide, manufacture and hypotensive, bronchodilating and blood platelet coagulation inhibitive medicine
JPS6178597A (en) * 1984-09-22 1986-04-22 Yoshiaki Nagaura High pressure area generating method and its device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007062273A (en) * 2005-09-01 2007-03-15 Unitec Resin:Kk Autoclave molding apparatus, autoclave molding method, and autoclave molded product

Similar Documents

Publication Publication Date Title
US3606999A (en) Method of and apparatus for carrying out a chemical or physical process
US4402632A (en) Seabed supported submarine pressure transfer storage facility for liquified gases
JP2001507742A (en) How to recover gas from hydrates
ES467245A1 (en) Marine production riser system
CA2207090A1 (en) Method and system for offshore production of liquefied natural gas
US3831385A (en) Arctic offshore platform
JPS63315796A (en) Module type sea-surface vicinity facility
US3455270A (en) Protective dome for underwater mooring swivel
US3550385A (en) Method of and means for field processing of subsea oil wells
US3608630A (en) Offshore oil production method and apparatus
GB2222961A (en) Crude oil separator
JP6341518B2 (en) Methane gas recovery associated water treatment apparatus and treatment method
JPS62277142A (en) High-pressure chemical reactor
GB1163336A (en) Subsea Fluid Mineral Production Satellite System
CN111483561B (en) Modularization detachable heat supply ship
JP2017141593A (en) Methane hydrate transfer
GB1447413A (en) Oil tankers for storing oil offshore
JPH02501561A (en) Offshore oil well floating production system and drilling vessel
RU2026491C1 (en) Method for mineral mining in development of deposits on sea bottom and complex for its realization
GB2128939A (en) A submersible reservoir for storage and transportation of fluids
GB1308653A (en) Underwater production system
CN113187444A (en) Mining and safe storage and transportation technology of deep-sea combustible ice
RU2016169C1 (en) Platform for exploitation of oil-gas fields
JPH04156241A (en) Marine structure for electric power storage using hydrogen gas
US2091857A (en) Light-buoy and method for feeding same