JPS602889A - Heat exchanging device - Google Patents
Heat exchanging deviceInfo
- Publication number
- JPS602889A JPS602889A JP58110233A JP11023383A JPS602889A JP S602889 A JPS602889 A JP S602889A JP 58110233 A JP58110233 A JP 58110233A JP 11023383 A JP11023383 A JP 11023383A JP S602889 A JPS602889 A JP S602889A
- Authority
- JP
- Japan
- Prior art keywords
- pipe
- tube group
- condensing tube
- condensing
- heat
- 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
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23D—BURNERS
- F23D14/00—Burners for combustion of a gas, e.g. of a gas stored under pressure as a liquid
- F23D14/46—Details, e.g. noise reduction means
- F23D14/66—Preheating the combustion air or gas
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23L—SUPPLYING AIR OR NON-COMBUSTIBLE LIQUIDS OR GASES TO COMBUSTION APPARATUS IN GENERAL ; VALVES OR DAMPERS SPECIALLY ADAPTED FOR CONTROLLING AIR SUPPLY OR DRAUGHT IN COMBUSTION APPARATUS; INDUCING DRAUGHT IN COMBUSTION APPARATUS; TOPS FOR CHIMNEYS OR VENTILATING SHAFTS; TERMINALS FOR FLUES
- F23L15/00—Heating of air supplied for combustion
- F23L15/04—Arrangements of recuperators
- F23L15/045—Arrangements of recuperators using intermediate heat-transfer fluids
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Central Heating Systems (AREA)
Abstract
Description
【発明の詳細な説明】
この発明は分離型のヒートバイブ熱交換装置の構造に関
する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to the structure of a separate heat vibrator heat exchange device.
熱交換装置のうち、一つの加熱流体（高温流体）によっ
て２以上の被加熱流体（低温流体）を加熱する場合、熱
交換器の形式に応じて各々工夫が施されている。このう
ち再生式、多管式、またはプレート式熱交換器の場合に
は被加熱流体の数に応じて加熱流体もこれに対応する数
に分流させて各々熱交換を行うが５、または加熱流体中
に各被加熱流体を加熱する熱交換器を各々設置する必要
があった。In a heat exchange device, when two or more fluids to be heated (low-temperature fluids) are heated by one heating fluid (high-temperature fluid), various measures are taken depending on the type of heat exchanger. Among these, in the case of a regeneration type, multi-tube type, or plate type heat exchanger, the heating fluid is divided into a corresponding number of fluids depending on the number of fluids to be heated, and heat exchange is performed respectively. It was necessary to install a heat exchanger to heat each fluid to be heated inside.
この点に関し、発明者等は先に蒸発管部と凝縮管部とを
分離して構成し各々加熱流体および被加熱流体中に配置
した熱交換装置である分離型ヒートパイプを提案してい
る。In this regard, the inventors have previously proposed a separate type heat pipe, which is a heat exchange device in which an evaporating tube section and a condensing tube section are separated and placed in a heating fluid and a heated fluid, respectively.
第１図はその分離型ヒートパイプの構造を示すもので、
符号５は加熱流体（ガス等）の流れるダクトｌ内に配置
された蒸発管群で、伝達された熱は媒体の蒸気によりそ
の上部でラダ６から管路７により受熱する流体（ガス等
）の流れるダクトｚ内に位置する凝縮管群９の上部ヘッ
ダ８に運ばれる。この蒸気は凝縮して下部ヘッダ１０よ
り管路１１により蒸発管群の下部へラダ４に流入する。Figure 1 shows the structure of the separate heat pipe.
Reference numeral 5 denotes a group of evaporation tubes arranged in the duct l through which the heating fluid (gas, etc.) flows, and the transferred heat is transferred to the fluid (gas, etc.) which receives heat from the ladder 6 through the pipe line 7 at the top of the duct 1 through the vapor of the medium. It is conveyed to the upper header 8 of the condensing tube bank 9 located in the flowing duct z. This vapor condenses and flows from the lower header 10 into the ladder 4 through the pipe line 11 to the lower part of the evaporator tube group.
下部へラダ１０は下部へラダ４よりレベル位置が高い処
に位置するので蒸発と凝縮は媒体の自然循環により行な
われることとなる。Since the lower ladder 10 is located at a higher level than the lower ladder 4, evaporation and condensation occur through natural circulation of the medium.
管路７には女゛全弁１７及び不凝縮ガスを抜く弁１６が
設けられる。The pipe line 7 is provided with a female valve 17 and a valve 16 for removing non-condensable gas.
第２図はこの構造を模式に示す図面である。FIG. 2 is a drawing schematically showing this structure.
第３Ａ図はこのような分離型ヒートパイプによりダクト
］、内を流れる高温ガス（例えば炉の燃焼ガス）Ｇ１の
熱を２つの流体Ｇ２（例えば燃焼用空気）Ｇ３（例えば
燃料ガス）に伝達する場合の従来の手段を示す図面であ
る。このようにすることは安全弁の数は図示例では６個
、ガス抜き用の弁も６個必要なこととなる。Figure 3A shows a duct using such a separate heat pipe], which transfers the heat of the high-temperature gas (e.g., combustion gas from a furnace) G1 flowing therethrough to two fluids G2 (e.g., combustion air) and G3 (e.g., fuel gas). FIG. In this case, six safety valves are required in the illustrated example, and six gas vent valves are also required.
またこれに加えて、直列配置では高漂流体と各低湿流体
の出口温度差が第３Ｂ図に示す如く極端に小さくなると
いう不利もあり、上流側熱交換の交換熱量を犬にする必
要がある。In addition to this, the serial arrangement has the disadvantage that the difference in outlet temperature between the high-drifting fluid and each low-humidity fluid becomes extremely small as shown in Figure 3B, so it is necessary to reduce the amount of heat exchanged in the upstream heat exchange. .
第４図はこの発明の一実施例を示すもので、第１図にお
ける管路７より分岐する管路７１及び管路１１より分岐
する管路１１１を設はダクト３内を流れる第３の流体Ｇ
３を加熱するようにしたものである。FIG. 4 shows an embodiment of the present invention, in which a pipe line 71 branching from pipe line 7 and a pipe line 111 branching from pipe line 11 in FIG. G
3 is heated.
図示例では蒸発管群を３組を設けたものに対し凝縮管群
を６組接続しかつ２種の流体Ｇ２． Ｇ。In the illustrated example, six condensing tube groups are connected to three evaporation tube groups, and two types of fluid G2. G.
を加熱することができる。この構造では安全弁３個、ガ
ス抜き用の弁は３個で済み、第３図の場合の王の数でよ
いことになる。can be heated. With this structure, only three safety valves and three gas vent valves are required, which means that the number of valves required in the case of Fig. 3 is sufficient.
第５Ａ図は本発明の第２の実施例を示すもので、凝縮液
を蒸発管群の下部ヘッダ４に戻し入れする管路］−１を
分岐させた管路１２を第３の流体Ｇの流れるダクト３内
に位置する凝縮管群１４の下部ヘッダ１３に接続するも
のである。管路１工内の蒸気及び不凝縮ガスは凝縮管群
１４に流れ媒体（作動液）のみ凝縮し、不凝縮ガスは必
要に応じ弁１６（第５図）より抜き出し伝熱効果の低下
を防ぐことができる。FIG. 5A shows a second embodiment of the present invention, in which a pipe line 12 branching off from a pipe line 1-1 for returning the condensate to the lower header 4 of the evaporator tube group is connected to a third fluid G. It is connected to the lower header 13 of the condensing tube group 14 located in the flowing duct 3. The steam and non-condensable gas in the pipe line 1 condenses only the flow medium (working fluid) in the condensing pipe group 14, and the non-condensable gas is extracted from the valve 16 (Fig. 5) as necessary to prevent a decrease in the heat transfer effect. be able to.
またこの第５Ａ図のような構成とするときは即ち複合型
とするときは第５Ｃ図の温度勾配と積は小さくとること
ができるという効果を奏する。Further, when the configuration as shown in FIG. 5A is used, that is, when a composite type is used, the temperature gradient and the product shown in FIG. 5C can be made small.
第６図は本発明の第３の実施例を示す図面である。この
場合は凝縮液を蒸発管群の下部ヘッダに戻し入れする管
路から分岐する管路（第一、５４図の符号１２）を設け
ることでは第５Ａ図と変りがないが、不凝縮ガスを除く
凝縮管群１４を凝縮管群９と共に同一ダクト２内に位置
させることである。同様にして凝縮管群１０９と不凝縮
ガスを除く凝縮管群１工４を第３流体の流れるダクト３
内に位置させたものである。FIG. 6 is a diagram showing a third embodiment of the present invention. In this case, it is the same as in Fig. 5A in that a pipe (number 1, number 12 in Fig. 54) is provided that branches off from the pipe that returns the condensate to the lower header of the evaporator tube group, but the non-condensable gas is The condensing tube group 14 except for the condensing tube group 9 is located in the same duct 2 together with the condensing tube group 9. Similarly, the condensing tube group 109 and the condensing tube group 1 work 4 excluding non-condensable gas are connected to the duct 3 through which the third fluid flows.
It is located inside.
以上分離型ヒートパイプにおいて第３の流体を加熱する
場合を例にとり説明したが、第４−２第５等複数の流体
を加熱する場合においても前記第４図、第５図、第６図
の手段を分岐管路を設けて実施することができる。The explanation above has been given by taking as an example the case where the third fluid is heated in the separate type heat pipe, but when heating a plurality of fluids such as the 4-2, 5-5, etc., the above-mentioned FIGS. The means can be implemented by providing branch lines.
この発明を実施することにより接散の流体を−の加熱源
の流体の保有する熱を利用して同時に加熱することがで
きる。また使用する弁の数も加熱する流体の数に応じて
増大することなく少い数で済むなど種々の効果を奏する
ものである。By carrying out this invention, it is possible to simultaneously heat the diffused fluid using the heat possessed by the fluid of the heating source. Moreover, the number of valves used does not increase in proportion to the number of fluids to be heated, and can be reduced in number, resulting in various effects.
第１図は分離型ヒートパイプの構造を示す図面、第２図
は第１図を模式に示す図面、第３Ａ図は従来の２流体Ｇ
２．Ｇ３を同時に加熱する場合の分離型ヒートパイプの
配置を示す図面、第３Ｂ図はその場合における温度勾配
線図、第４図は本願発明の第１実施例の配置と配管を示
す図面、第５Ａ図は第２の実施例の図面、第５Ｂ図は第
５Ａ図の面鋏の図面、第５Ｃ図は温度勾配線図、第６図
は第３実施例を示す図面である。
５・・・・・蒸発管群
７・・・・・・蒸発管群と凝縮管群の上部ヘッダ相互を
接続する管路
９・・・・凝縮管群
１１・・・・・蒸発管群と凝縮管群の下部ヘッダ相互を
接続する管路
Ｇ１ ・・・・・・加熱流体
Ｇ２．Ｇ３・・・・・被加熱流体
第１図
Ｉら
第４図
第５Ｂ図Fig. 1 is a drawing showing the structure of a separate type heat pipe, Fig. 2 is a drawing schematically showing Fig. 1, and Fig. 3A is a drawing showing the structure of a separate type heat pipe.
2. A drawing showing the arrangement of separate heat pipes in the case of heating G3 at the same time, Fig. 3B is a temperature gradient diagram in that case, Fig. 4 is a drawing showing the arrangement and piping of the first embodiment of the present invention, Fig. 5A 5B is a drawing of the surface scissors shown in FIG. 5A, FIG. 5C is a temperature gradient diagram, and FIG. 6 is a drawing showing the third embodiment. 5...Evaporation tube group 7...Pipe line 9 connecting the upper headers of the evaporation tube group and the condensation tube group...Condensation tube group 11...Evaporation tube group Pipe line G1 connecting the lower headers of the condensing pipe group . . . Heating fluid G2. G3...Fluid to be heated Fig. 1 I et al. Fig. 4 Fig. 5B
Claims (1)
おいて、蒸発管群と凝縮管群とを接続する管路より分岐
する管路を設け、２以上の流体を同時に加熱するように
分岐管路に対応する一以上の凝縮管群を設けたことを特
徴とする熱交換装置。 ２６ 蒸発管群の上部ヘッダと凝縮管群の上部ヘッダと
を結ぶ管路と、蒸発管群の下部ヘッダと凝縮管群の下部
ヘッダとを結ぶ管路とに、夫々分岐する管路を設け、こ
の分岐管路に対応する一以上の他の凝縮管群の上部ヘッ
ダと下部ヘッダとに夫々接続することを特徴とする特許
請求の範囲第１項記載の熱交換装置。 ３、−の蒸発管群と−の凝縮管群の下部ヘッダを相互に
接続する管路より分岐する管路に不−縮ガス分離手段を
有する一以上の凝縮管群を接続することを特徴とする特
許請求の範囲第１項記載の熱交換装置。 ４、−の凝縮管群の下部ヘッダと蒸発管群の下部ヘッダ
を結ぶ管路より分岐する管路に不凝縮ガス分離手段をも
つ他の凝縮管群を接続しこれら２つの凝縮管群を−の加
熱流体の流れるダクト内に収容した凝縮管群組を一以上
設けることを特徴とする特許請求の範囲第１項記載の熱
交換装置。[Claims] 1. In a heat exchanger using a separate type heat vibrator, a pipe line branching from a pipe line connecting an evaporating tube group and a condensing tube group is provided to simultaneously heat two or more fluids. 1. A heat exchange device characterized in that one or more condensing tube groups are provided corresponding to branch pipes. 26 A pipe line connecting the upper header of the evaporating tube group and the upper header of the condensing tube group and a pipe line connecting the lower header of the evaporating tube group and the lower header of the condensing tube group are provided with branching pipe lines, respectively. 2. The heat exchange device according to claim 1, wherein the heat exchange device is connected to an upper header and a lower header of one or more other condensing tube groups corresponding to the branch pipe line. 3. One or more condensing tube groups having non-condensable gas separation means are connected to a conduit branching from the conduit connecting the lower headers of the evaporation tube group - and the condensing tube group - A heat exchange device according to claim 1. 4. Connect another condensing tube group having non-condensable gas separation means to a conduit branching from the conduit connecting the lower header of the condensing tube group and the lower header of the evaporating tube group, and connect these two condensing tube groups to the condensing tube group - 2. The heat exchange device according to claim 1, further comprising one or more condensing tube groups housed in a duct through which heated fluid flows.
Priority Applications (13)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58110233A JPH0665955B2 (en) | 1983-06-21 | 1983-06-21 | Heat exchanger |
| US06/622,725 US4616697A (en) | 1983-06-21 | 1984-06-20 | Heat exchanger |
| DK300584A DK300584A (en) | 1983-06-21 | 1984-06-20 | HEAT EXCHANGE |
| DE8787115697T DE3485375D1 (en) | 1983-06-21 | 1984-06-20 | HEAT EXCHANGER. |
| EP84107107A EP0129257B1 (en) | 1983-06-21 | 1984-06-20 | Heat exchanger |
| KR8403471A KR890001769B1 (en) | 1983-06-21 | 1984-06-20 | Heat exchanger |
| EP87115696A EP0270800B1 (en) | 1983-06-21 | 1984-06-20 | Heat exchanger |
| DE3486308T DE3486308T2 (en) | 1983-06-21 | 1984-06-20 | Heat exchanger. |
| DE3486440T DE3486440T2 (en) | 1983-06-21 | 1984-06-20 | Heat exchanger |
| EP87115697A EP0270801B1 (en) | 1983-06-21 | 1984-06-20 | Heat exchanger |
| US06/728,867 US4573524A (en) | 1983-06-21 | 1985-04-30 | Heat exchanger |
| KR1019870000369A KR880000052B1 (en) | 1983-06-21 | 1987-01-19 | Heat exchanger |
| US07/355,109 US4928753A (en) | 1983-06-21 | 1989-05-19 | Heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58110233A JPH0665955B2 (en) | 1983-06-21 | 1983-06-21 | Heat exchanger |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS602889A true JPS602889A (en) | 1985-01-09 |
| JPH0665955B2 JPH0665955B2 (en) | 1994-08-24 |
Family
ID=14530466
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58110233A Expired - Lifetime JPH0665955B2 (en) | 1983-06-21 | 1983-06-21 | Heat exchanger |
Country Status (2)
| Country | Link |
|---|---|
| JP (1) | JPH0665955B2 (en) |
| KR (1) | KR890001769B1 (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61235686A (en) * | 1985-04-10 | 1986-10-20 | Kawasaki Steel Corp | Waste heat retrieving device for boiler |
| JPS62793A (en) * | 1985-06-26 | 1987-01-06 | Mitsubishi Heavy Ind Ltd | Combination heater |
| JPS62166472U (en) * | 1986-04-07 | 1987-10-22 | ||
| US5607011A (en) * | 1991-01-25 | 1997-03-04 | Abdelmalek; Fawzy T. | Reverse heat exchanging system for boiler flue gas condensing and combustion air preheating |
| JP2009216262A (en) * | 2008-03-07 | 2009-09-24 | Toyota Industries Corp | Ebullient cooling device and cooling method |
| JP2013257086A (en) * | 2012-06-13 | 2013-12-26 | Hitachi Appliances Inc | Air conditioner, and control method thereof |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS55140093A (en) * | 1979-04-17 | 1980-11-01 | Babcock Hitachi Kk | Method and apparatus for removing noncondensable gas from heat exchanger |
| JPS56119491A (en) * | 1980-01-31 | 1981-09-19 | Sumitomo Metal Ind Ltd | Exhaust heat collecting device of hot blast furnace |
-
1983
- 1983-06-21 JP JP58110233A patent/JPH0665955B2/en not_active Expired - Lifetime
-
1984
- 1984-06-20 KR KR8403471A patent/KR890001769B1/en not_active IP Right Cessation
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS55140093A (en) * | 1979-04-17 | 1980-11-01 | Babcock Hitachi Kk | Method and apparatus for removing noncondensable gas from heat exchanger |
| JPS56119491A (en) * | 1980-01-31 | 1981-09-19 | Sumitomo Metal Ind Ltd | Exhaust heat collecting device of hot blast furnace |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61235686A (en) * | 1985-04-10 | 1986-10-20 | Kawasaki Steel Corp | Waste heat retrieving device for boiler |
| JPS62793A (en) * | 1985-06-26 | 1987-01-06 | Mitsubishi Heavy Ind Ltd | Combination heater |
| JPS62166472U (en) * | 1986-04-07 | 1987-10-22 | ||
| US5607011A (en) * | 1991-01-25 | 1997-03-04 | Abdelmalek; Fawzy T. | Reverse heat exchanging system for boiler flue gas condensing and combustion air preheating |
| JP2009216262A (en) * | 2008-03-07 | 2009-09-24 | Toyota Industries Corp | Ebullient cooling device and cooling method |
| JP2013257086A (en) * | 2012-06-13 | 2013-12-26 | Hitachi Appliances Inc | Air conditioner, and control method thereof |
Also Published As
| Publication number | Publication date |
|---|---|
| KR890001769B1 (en) | 1989-05-19 |
| JPH0665955B2 (en) | 1994-08-24 |
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