JPS6344070U - - Google Patents
Info
- Publication number
- JPS6344070U JPS6344070U JP12813787U JP12813787U JPS6344070U JP S6344070 U JPS6344070 U JP S6344070U JP 12813787 U JP12813787 U JP 12813787U JP 12813787 U JP12813787 U JP 12813787U JP S6344070 U JPS6344070 U JP S6344070U
- Authority
- JP
- Japan
- Prior art keywords
- gas
- heat exchanger
- flow path
- gas flow
- stand
- 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.)
- Granted
Links
- 238000005192 partition Methods 0.000 claims description 2
- 238000007599 discharging Methods 0.000 claims 1
- 239000010419 fine particle Substances 0.000 claims 1
- 239000007787 solid Substances 0.000 claims 1
- 238000003786 synthesis reaction Methods 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 239000010802 sludge Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/06—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits having a single U-bend
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
- F22B1/18—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
- F22B1/1838—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines the hot gas being under a high pressure, e.g. in chemical installations
- F22B1/1846—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines the hot gas being under a high pressure, e.g. in chemical installations the hot gas being loaded with particles, e.g. waste heat boilers after a coal gasification plant
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Description
第１図は、本考案による一つの熱交換器の垂直
断面図であり、第２図は、第１図の線―にお
ける水平断面図であり、第３図は、第２図のＡの
部分を拡大して示した詳細図である。
１…圧力容器、２…ガス流路、３…隔壁管、４
，４′，１４…フイン、５…漏斗、６，８…管、
７…隔壁管群、９…案内壁、９′…出口開口部、
１０…内室、１１…外室、１２…ガス入口スタン
ド、１２′…ガス案内管、１３…ガス出口スタン
ド、１３′…ガス出口管、１６…溶接線、１７…
給水配管、１８…水、１９…スラツジ排出スタン
ド、２０…主分配ヘツダー、２０′…給水配管、
２１…主集合ヘツダー、２１′…蒸気配管、２２
…ガス流路分配ヘツダー、２３…ガス流路集合ヘ
ツダー、２４…管群分配ヘツダー、２５…管群集
合ヘツダー、２６，２６′，２７，２７′…連絡
配管、３０…吊下げ金具、４０…吊上げ具。
FIG. 1 is a vertical sectional view of one heat exchanger according to the present invention, FIG. 2 is a horizontal sectional view taken along the line - in FIG. 1, and FIG. 3 is a section A in FIG. FIG. 1... Pressure vessel, 2... Gas flow path, 3... Partition pipe, 4
, 4', 14... fin, 5... funnel, 6, 8... tube,
7... Bulkhead tube group, 9... Guide wall, 9'... Outlet opening,
DESCRIPTION OF SYMBOLS 10...Inner chamber, 11...Outer chamber, 12...Gas inlet stand, 12'...Gas guide pipe, 13...Gas outlet stand, 13'...Gas outlet pipe, 16...Welding line, 17...
Water supply piping, 18...Water, 19...Sludge discharge stand, 20...Main distribution header, 20'...Water supply piping,
21...Main collection header, 21'...Steam piping, 22
...Gas flow path distribution header, 23...Gas flow path gathering header, 24...Tube group distribution header, 25...Tube group gathering header, 26, 26', 27, 27'...Connection piping, 30...Hanging fitting, 40... Lifting equipment.
Claims (1)
学合成ガス、に用いられる一つの熱交換器であつ
て、該熱交換器が、一つの圧力容器の中に構成さ
れる一つの垂直方向のガス流路を含んでおり、か
つこのガス流路が、ガスタイトになるように互い
に溶接されていて、かつその内部に受熱側媒体が
流通するようになされている隔壁管によつて構成
されており、かつその際、これらの管の端部がそ
れぞれ一つの分配ヘツダーならびに集合ヘツダー
に接続されており、更に該熱交換器の上端部には
、前記のガス流路を流通するガスのために、一つ
の垂直なガス入口スタンドが設けられており、更
にまた前記のガス流路を流通し終わつたガスのた
めに、少なくとも一つの、ガス流路に直角なガス
出口スタンドが設けられており、かつその際、前
記のガス流路内には、その内部を受熱側媒体が流
通するようになされていて、かつ互いに溶接され
ており、更にそれぞれの端部が一つの分配ヘツダ
ーならびに一つの集合ヘツダーに接続されている
多数の管によつて構成された、幾つかの平らな垂
直の隔壁管パネルが配設されているような、一つ
の熱交換器であつて、 前記のガス流路が、前述の隔壁管ならびにこれ
らと接続されている分配ヘツダーおよび集合ヘツ
ダーを含む、幾つかの構成部分に分割し得るとと
もに、これらの構成部分が、前記のガス入口スタ
ンドを経て外に抜き出され得るような、水平方向
の寸法になされていると同時に、前記の隔壁管パ
ネルの水平方向寸法もまた、それらが前記のガス
入口スタンドを経て外に抜き出され得るようにな
されている ことを特徴とする熱交換器。 (2) 実用新案登録請求の範囲第１項による熱交
換器であつて、 前記の圧力容器が円筒形を、かつ前記のガス流
路が多角柱状をなしているとともに、それらが前
記のガス入口スタンドと同心に配設されているこ
と、ならびに 該多角柱の各辺が、ガス入口スタンドを経て外
に抜き出され得るような一つの構成部分を形成し
ていること、 を特徴とする熱交換器。 (3) 実用新案登録請求の範囲第１項あるいは第
２項による熱交換器であつて、 前記のガス入口スタンドの内部に、断熱性をも
つているとともに、上に向けて抜き出し得るよう
になされた、一つのガス案内管が設けられており
、かつその際、このガス案内管が、前記のガス流
路ならびに／もしくは隔壁管パネルの管の上端に
接続されている分配ヘツダーないしは集合ヘツダ
ーよりも低いレベルまで垂れ下がつて延びている
こと を特徴とする熱交換器。 (4) 実用新案登録請求の範囲第１項から第３項
までのいずれか一つの項による熱交換器であつて
、前記のガス流路が、隔壁管パネルとは無関係に
、圧力容器の頂上部分から吊り下げられているこ
とを特徴とする熱交換器。 (5) 実用新案登録請求の範囲第１項から第４項
までのいずれか一つの項による熱交換器であつて
、前記のガス流路ならびに隔壁管パネルの分配ヘ
ツダーならびに集合ヘツダーが、この熱交換器の
頂上部分に配設されており、かつ各管が、その主
要部が垂直部分からなるＵ字形状をなしているこ
とを特徴とする熱交換器。 (6) 実用新案登録請求の範囲第１項から第５項
までのいずれか一つの項による熱交換器であつて
、前記のガス流路を構成する管が、その下端部分
において、下方に向けて次第に細くなる漏斗を形
成するとともに、更にこれに続いてガス出口開口
部を形成する案内壁となつて終わつており、かつ
その際、前記のガス出口スタンドが、上述の開口
部よりも上の漏斗の部分に配設されていること を特徴とする熱交換器。[Claims for Utility Model Registration] (1) A heat exchanger used for a heat supply gas containing solid fine particles, such as chemical synthesis gas, the heat exchanger being in a pressure vessel. A partition wall that includes one vertical gas flow path, the gas flow paths are welded together to be gas tight, and the heat-receiving medium is configured to flow therein. It consists of tubes, the ends of which are connected in each case to a distribution header and to a collecting header, and at the upper end of the heat exchanger the gas flow channels are connected. one vertical gas inlet stand is provided for the gas flowing through said gas flow path, and also at least one gas outlet perpendicular to said gas flow path for gas that has finished flowing through said gas flow path. A stand is provided, in which the heat-receiving medium flows in the gas flow path, and the stand is welded to each other, and each end is connected to a single stand. A heat exchanger, in which a number of flat vertical bulkhead tube panels are arranged, constituted by a distribution header and a number of tubes connected to a collection header, Said gas flow path can be divided into several components, including said bulkhead tubes and distribution headers and collection headers connected thereto, and these components are connected via said gas inlet stand. The horizontal dimensions of said bulkhead tube panels are also such that they can be withdrawn to the outside via said gas inlet stand. A heat exchanger characterized by: (2) The heat exchanger according to claim 1 of the utility model registration claim, wherein the pressure vessel has a cylindrical shape, the gas flow path has a polygonal column shape, and the gas inlet Heat exchanger characterized in that it is arranged concentrically with the stand, and that each side of the polygonal prism forms a component that can be extracted to the outside via a gas inlet stand. vessel. (3) A heat exchanger according to claim 1 or 2 of the utility model registration claim, which has a heat insulating property inside the gas inlet stand and can be pulled out upward. In addition, a gas guide pipe is provided, in which case this gas guide pipe is connected to the gas channel and/or to the upper end of the pipes of the bulkhead tube panel than the distribution header or the collecting header. A heat exchanger characterized by hanging down to a lower level. (4) A heat exchanger according to any one of claims 1 to 3 of the claims registered as a utility model, wherein the gas flow path is connected to the top of the pressure vessel regardless of the bulkhead pipe panel. A heat exchanger characterized by being suspended from a part. (5) A heat exchanger according to any one of claims 1 to 4 of the claims registered as a utility model, wherein the gas flow path and the distribution header and collection header of the bulkhead tube panel are capable of discharging this heat. A heat exchanger disposed at the top of the exchanger, wherein each tube has a U-shape with a main portion consisting of a vertical portion. (6) A heat exchanger according to any one of claims 1 to 5 of claims registered as a utility model, wherein the pipes constituting the gas flow path are directed downward at their lower end portions. forming a tapered funnel and further terminating in a guide wall forming a gas outlet opening, and in this case said gas outlet stand is located above said opening. A heat exchanger characterized by being disposed in a funnel portion.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CH342086A CH670696A5 (en) | 1986-08-26 | 1986-08-26 | Synthesis gas heat exchanger |
| CH03420/86-7 | 1986-08-26 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6344070U true JPS6344070U (en) | 1988-03-24 |
| JPH064161Y2 JPH064161Y2 (en) | 1994-02-02 |
Family
ID=4255599
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP12813787U Expired - Lifetime JPH064161Y2 (en) | 1986-08-26 | 1987-08-25 | Heat exchanger |
Country Status (6)
| Country | Link |
|---|---|
| JP (1) | JPH064161Y2 (en) |
| CN (1) | CN87212240U (en) |
| AU (1) | AU591328B2 (en) |
| CH (1) | CH670696A5 (en) |
| DE (1) | DE8708850U1 (en) |
| IT (1) | IT210513Z2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007292452A (en) * | 2006-04-21 | 2007-11-08 | Ifp | New internal heat exchanger for fluidized bed reactor for gas, solid and liquid using strong exothermic reaction |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7587995B2 (en) | 2005-11-03 | 2009-09-15 | Babcock & Wilcox Power Generation Group, Inc. | Radiant syngas cooler |
| CN107541884A (en) * | 2016-08-31 | 2018-01-05 | 江门市宪诚环保节能设备有限公司 | Forming machine waste gas residual heat reclaims energy saver |
-
1986
- 1986-08-26 CH CH342086A patent/CH670696A5/en not_active IP Right Cessation
-
1987
- 1987-06-25 IT IT2187587U patent/IT210513Z2/en active
- 1987-06-26 DE DE8708850U patent/DE8708850U1/de not_active Expired
- 1987-08-25 CN CN198787212240U patent/CN87212240U/en active Granted
- 1987-08-25 JP JP12813787U patent/JPH064161Y2/en not_active Expired - Lifetime
- 1987-08-25 AU AU77391/87A patent/AU591328B2/en not_active Ceased
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2007292452A (en) * | 2006-04-21 | 2007-11-08 | Ifp | New internal heat exchanger for fluidized bed reactor for gas, solid and liquid using strong exothermic reaction |
Also Published As
| Publication number | Publication date |
|---|---|
| DE8708850U1 (en) | 1987-08-13 |
| JPH064161Y2 (en) | 1994-02-02 |
| IT210513Z2 (en) | 1988-12-30 |
| CH670696A5 (en) | 1989-06-30 |
| AU591328B2 (en) | 1989-11-30 |
| CN87212240U (en) | 1988-08-10 |
| IT8721875V0 (en) | 1987-06-25 |
| AU7739187A (en) | 1988-03-03 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102059042B (en) | Combination unit for multilevel heat exchange and gas liquid separation | |
| GB1346111A (en) | Liquid metal heat exchanger | |
| NO314290B1 (en) | Horizontal trough and column for contact with gas and liquid | |
| US4493291A (en) | Gas cooler arrangement | |
| CN201129943Y (en) | Fixed tube sheet warm water circulating type gasifier | |
| US3139070A (en) | Vapor generating unit | |
| JPS6344070U (en) | ||
| CN212377950U (en) | Full-film type wall waste heat boiler | |
| CN209790891U (en) | Improved falling film evaporator | |
| CN209085392U (en) | Fixed sheet heat exchanger | |
| GB1264105A (en) | ||
| JPH0374714B2 (en) | ||
| JPH04506561A (en) | Method and apparatus for organizing fluid flow in a vertical steam generator | |
| RS53434B (en) | Heat-exchange reactor for hydrogen production with integrated steam-generation bundle | |
| US2289970A (en) | Steam and water separator | |
| US2535996A (en) | Evaporator | |
| US4474141A (en) | Heat exchanger for cooling a hot gas | |
| US3930537A (en) | Heat exchanger | |
| US4558734A (en) | Heat exchanger having a set of pipes | |
| US2056492A (en) | Heat exchanger | |
| FI59661C (en) | exhaust gas boiler | |
| CN205664353U (en) | Rotary film deaerator | |
| US4743432A (en) | Vertical reactor for the generation of methanol | |
| JPS5840081B2 (en) | Blowdown equipment for steam generators | |
| CN215939097U (en) | Filler support member with intermediate partition plate |