JPH03225164A - Direct fired generating device - Google Patents
Direct fired generating deviceInfo
- Publication number
- JPH03225164A JPH03225164A JP2238390A JP2238390A JPH03225164A JP H03225164 A JPH03225164 A JP H03225164A JP 2238390 A JP2238390 A JP 2238390A JP 2238390 A JP2238390 A JP 2238390A JP H03225164 A JPH03225164 A JP H03225164A
- Authority
- JP
- Japan
- Prior art keywords
- flue
- furnace
- solution flow
- combustion gas
- flow path
- 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
- 238000010304 firing Methods 0.000 claims description 6
- 239000007788 liquid Substances 0.000 abstract description 46
- 239000000567 combustion gas Substances 0.000 abstract description 29
- 230000000694 effects Effects 0.000 abstract description 10
- 238000005260 corrosion Methods 0.000 abstract description 8
- 230000007797 corrosion Effects 0.000 abstract description 8
- 230000000630 rising effect Effects 0.000 abstract description 8
- 238000013021 overheating Methods 0.000 abstract description 6
- 230000007423 decrease Effects 0.000 abstract description 5
- 238000010438 heat treatment Methods 0.000 abstract description 5
- 230000003247 decreasing effect Effects 0.000 abstract 2
- 238000000034 method Methods 0.000 abstract 1
- 238000005086 pumping Methods 0.000 abstract 1
- 238000010521 absorption reaction Methods 0.000 description 33
- 239000000779 smoke Substances 0.000 description 12
- 238000002485 combustion reaction Methods 0.000 description 4
- 239000002023 wood Substances 0.000 description 4
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- AMXOYNBUYSYVKV-UHFFFAOYSA-M lithium bromide Chemical compound [Li+].[Br-] AMXOYNBUYSYVKV-UHFFFAOYSA-M 0.000 description 2
- 230000002745 absorbent Effects 0.000 description 1
- 239000002250 absorbent Substances 0.000 description 1
- 239000006096 absorbing agent Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Landscapes
- Treating Waste Gases (AREA)
- Chimneys And Flues (AREA)
Abstract
Description
【発明の詳細な説明】
（イ）産業上の利用分野
本発明は吸収冷凍機などに使用される直焚発生器に関す
る。DETAILED DESCRIPTION OF THE INVENTION (a) Field of Industrial Application The present invention relates to a direct firing generator used in absorption refrigerators and the like.
（ロ）従来の技術
例えば特開平１−１１８０８１号公報には、炉（炉筒）
の後方と連通して炉の上方に配置された煙道と、この煙
道及び炉と器胴との間に形成された溶液流路とを備え、
さらに、炉の後部管板と器胴の後部管板との間に溶液流
路が形成された直焚発生器が開示されている。そして、
この直焚発生器の運転時には、炉に臨んだバーナーによ
って炉内に火炎が形成され、炉の後部管板が加熱される
。後部管板の加熱によって溶液から発生した蒸気泡は溶
液流通部を上昇する。(b) Conventional technology For example, in Japanese Patent Application Laid-Open No. 1-118081, a furnace (furnace tube)
a flue disposed above the furnace in communication with the rear of the furnace, and a solution flow path formed between the flue, the furnace and the vessel body,
Additionally, a direct-fired generator is disclosed in which a solution flow path is formed between the rear tubesheet of the furnace and the rear tubesheet of the vessel body. and,
When this direct-fired generator is in operation, a burner facing the furnace forms a flame within the furnace, which heats the rear tubesheet of the furnace. Steam bubbles generated from the solution due to heating of the rear tubesheet rise through the solution flow section.
（ハ）発明が解決しようとする課題
直焚発生器の運転時に発生した蒸気泡の多くは炉の後部
管板と器胴及び器胴の後部管板との間の比較的広い溶液
流路を上昇するため、溶液流路を上昇する溶液は水平方
向成分を持ち、溶液の上昇速度は遅かった。このため、
炉後部の管板と器胴の後部管板との間の溶液流路の下部
の溶液は停滞し、炉、及び炉の後部管板の下部から溶液
への熱伝達量が少なく、炉筒から煙道へ高温の燃焼ガス
の温度が流入する。そして、煙道入口部が高温の燃焼ガ
スによって加熱され、煙道入口部の溶液による腐食が発
生するおそれがあった。(c) Problems to be Solved by the Invention Most of the steam bubbles generated during the operation of a direct-fired generator are caused by the relatively wide solution flow path between the rear tube sheet of the furnace and the container body and the rear tube sheet of the container body. Therefore, the solution rising in the solution flow path had a horizontal component, and the rising speed of the solution was slow. For this reason,
The solution at the bottom of the solution flow path between the rear tube sheet of the furnace and the rear tube sheet of the vessel stagnates, and the amount of heat transferred from the furnace and the lower part of the rear tube sheet of the furnace to the solution is small. The high temperature of combustion gas flows into the flue. Then, the flue inlet was heated by the high-temperature combustion gas, and there was a risk that the flue inlet would be corroded by the solution.
本発明は、溶液流通路の溶液と燃焼ガスとの熱交換量を
増加きせ、煙道へ流入する燃焼ガスの温度を低下させる
ことを目的とする。An object of the present invention is to increase the amount of heat exchange between the solution in the solution flow path and the combustion gas, and to lower the temperature of the combustion gas flowing into the flue.
（ニ）課題を解決するための手段
本発明は上記課題を解決するために、器胴（１）内に炉
筒（４）及び煙道（１１）を配置し、炉筒（４）の後部
管板（６〉の溶液流路（２４）側の面に上下方向に複数
の板（７）・・・を接続した直焚発生器を提供するもの
である。(d) Means for Solving the Problems In order to solve the above problems, the present invention arranges a furnace tube (4) and a flue (11) in the vessel body (1), and A direct firing generator is provided in which a plurality of plates (7) are vertically connected to the surface of the tube plate (6> on the solution flow path (24) side).
又、器胴（１）内に炉筒（４）、及び煙道（１１）を配
置し、器胴（１）の後部管板（３〉の溶液流路（２４）
側の面に上下方向に複数の板（２７）を接続した直焚発
生器を提供するものである。In addition, a furnace tube (4) and a flue (11) are arranged in the container body (1), and a solution flow path (24) in the rear tube plate (3) of the container body (1) is arranged.
A direct firing generator is provided in which a plurality of plates (27) are vertically connected to the side surface.
（ホ）作用
直焚発生器の運転時、炉筒後部管板（６）の溶液流路（
２４）側の面に発生した蒸気泡は複数の板（７）・・・
の間を上昇し、蒸気泡の流れのうち水平方向成分が各板
（７）によって僅かに抑えられるため、蒸気泡の上昇速
度が速くなる。このため、溶液流路（２４）に発生した
気泡ポンプ効果によって溶液流路（２４）下部の吸収液
が吸い上げられ、吸収液の流動が活発になる。そして、
液側の熱伝達量が増大して炉筒（４）から煙道（１１）
へ流れる燃焼ガスの温度が低下するので、煙道（１１）
の入口側の腐食を防止することが可能になる。又、各板
（７）・・・によって炉筒後部管板（６）の液側伝熱面
積が増大し、稀吸収液と燃焼ガスとの熱交換量が増大し
、稀吸収液の加熱効率を向上させることが可能になり、
又、煙道（１１〉に流れる燃焼ガスの温度をさらに下げ
ることが可能になる。(E) Operation During operation of the direct-fired generator, the solution flow path (
24) The steam bubbles generated on the side surface are caused by multiple plates (7)...
Since the horizontal component of the flow of steam bubbles is slightly suppressed by each plate (7), the rate of rise of the steam bubbles becomes faster. Therefore, the absorption liquid at the lower part of the solution flow path (24) is sucked up by the bubble pump effect generated in the solution flow path (24), and the flow of the absorption liquid becomes active. and,
The amount of heat transfer on the liquid side increases and the flow from the furnace tube (4) to the flue (11) increases.
As the temperature of the combustion gases flowing into the flue (11) decreases,
This makes it possible to prevent corrosion on the inlet side. In addition, each plate (7)... increases the heat transfer area on the liquid side of the rear tube plate (6) of the furnace cylinder, increasing the amount of heat exchange between the dilute absorption liquid and the combustion gas, and improving the heating efficiency of the dilute absorption liquid. It becomes possible to improve
Moreover, it becomes possible to further lower the temperature of the combustion gas flowing into the flue (11).
又、直焚発生器の運転時、溶液流路（２４）の蒸気泡は
器胴後部管板（３）に上下方向に接続祢れた複数の板（
２７）・・・に案内されて上昇し、蒸気泡の流れの水平
方向成分は僅かに抑えられ、蒸気泡の上昇速度は速くな
る。そして、溶液流路（２４）に発生した気泡ポンプ効
果によって溶液流路（２４）下部の吸収液が吸い上げら
れ、吸収液の流動が活発になる。このため、液側熱交換
量が増大して炉＃（１１）から煙道（１１）へ流れる燃
焼ガスの温度が低下し、煙道（１１〉の入口側の過熱を
回避して腐食を防止することが可能になる。In addition, during operation of the direct-fired generator, steam bubbles in the solution flow path (24) are removed by a plurality of plates (
27)..., the horizontal component of the flow of steam bubbles is slightly suppressed, and the rising speed of the steam bubbles becomes faster. Then, the absorption liquid at the lower part of the solution flow path (24) is sucked up by the bubble pump effect generated in the solution flow path (24), and the flow of the absorption liquid becomes active. Therefore, the amount of heat exchange on the liquid side increases and the temperature of the combustion gas flowing from the furnace # (11) to the flue (11) decreases, avoiding overheating on the inlet side of the flue (11) and preventing corrosion. It becomes possible to do so.
（へ）実施例
以下、本発明の一実施例を図面に基づいて詳細に説明す
る。(F) Example Hereinafter, an example of the present invention will be described in detail based on the drawings.
第１図は吸収冷凍機などに使用される直焚発生器の断面
図、第２図は同じく発生器の一部切欠き斜視図である。FIG. 1 is a sectional view of a direct firing generator used in an absorption refrigerator, etc., and FIG. 2 is a partially cutaway perspective view of the generator.
第１図、及び第２図において、（１）は器胴（外シェル
）、（２）及び（３）はそれぞれ器胴前部管板及び器胴
後部管板である。（４）は器胴（１）内の下部にほぼ水
平に配置された炉筒、（５）は炉筒前部管板、（６）は
炉筒後部管板である。（７）は炉筒後部管板（６）に上
下方向複数枚接続された整流板である。これらの整流板
（７）・・・は第２図及び第３図に示したように炉筒後
部管板（６）に垂直に溶接接続されている。さらに、整
流板（７）・・・はそれぞれ並行に接続されている。こ
こで、器胴（１）、各管板（２） 、 （３） 、 （
５） 、 （６）、炉筒（４）、整流板（７）・・・は
それぞれ例えば鉄などの金属によって形成されている。In FIGS. 1 and 2, (1) is the vessel body (outer shell), (2) and (3) are the vessel front tube plate and the vessel rear tube plate, respectively. (4) is a furnace cylinder arranged almost horizontally in the lower part of the vessel body (1), (5) is a front tube plate of the furnace cylinder, and (6) is a rear tube plate of the furnace cylinder. (7) is a plurality of rectifying plates connected vertically to the rear tube plate (6) of the furnace cylinder. These rectifier plates (7)... are vertically welded and connected to the furnace tube rear tube plate (6) as shown in FIGS. 2 and 3. Furthermore, the current plates (7)... are connected in parallel. Here, the vessel body (1), each tube plate (2), (3), (
5), (6), the furnace cylinder (4), the rectifier plate (7), etc. are each formed of metal such as iron.
（８）は炉筒（４）及び炉筒後部管板（６）に接続され
た燃焼ガス箱であり、（９〉は後部煙室である。（１０
）は煙管であり、この煙管（１０）は燃焼ガス箱（８）
と器胴前部管板（２）との間に間隔を存してほぼ水平に
複数接続されている。そして、各煙管（１０）内に煙道
（１１）が形成されている。ここで、直焚発生器が例え
ば大型の場合には煙管（１０）が複数段器胴（１）内に
配置きれる。又、（１２）は前部燃焼ガス箱であり、（
１３）は前部煙室、（１４）は煙突である。そして、炉
筒（４）内と、後部煙室（９）と、煙道（１１）と、前
部煙室（１３）とは連通している。さらに（１５）は器
胴（１）の上部に接続された蒸気箱であり、（１６）は
蒸気流出口である。（１７）は補液入口管であり、例え
ば臭化リチウム溶液などの稀吸収液が稀液入口管（１７
）から器胴（１）内に流入する。又、（１８）は中間液
流出箱、（１９）は中間流出管である。（２０）はバー
ナーなどの燃焼装置であり、この燃焼装置（２０）はバ
ーナー取付筒（２１）を介して器胴前部管板（２）及び
炉筒前部管板（５）に取り付けられている。そして、器
胴前部管板（２）と炉筒前部管板（５〉との間、器胴（
１）と炉＊（４＞との間、器胴後部管板“（３）と炉筒
後部管板（６）との間、及び各煙管（１０）・・・の間
に溶液流路（２２） 、 （２３） 、 （２４）、及
び（２５）が形成されている。(8) is a combustion gas box connected to the furnace tube (4) and the rear tube plate (6) of the furnace tube, and (9> is the rear smoke chamber. (10
) is a smoke pipe, and this smoke pipe (10) is a combustion gas box (8)
A plurality of tubes are connected almost horizontally with a space between the tube plate (2) and the front tube plate (2) of the vessel body. A flue (11) is formed within each smoke pipe (10). Here, if the direct firing generator is, for example, large, the smoke pipes (10) can be arranged in a multi-stage vessel body (1). Also, (12) is the front combustion gas box, (
13) is the front smoke chamber, and (14) is the chimney. The inside of the furnace tube (4), the rear smoke chamber (9), the flue (11), and the front smoke chamber (13) communicate with each other. Furthermore, (15) is a steam box connected to the upper part of the vessel body (1), and (16) is a steam outlet. (17) is a replacement fluid inlet pipe, and a dilute absorption liquid such as a lithium bromide solution is supplied to the dilute fluid inlet pipe (17).
) into the vessel body (1). Further, (18) is an intermediate liquid outflow box, and (19) is an intermediate outflow pipe. (20) is a combustion device such as a burner, and this combustion device (20) is attached to the front tube plate of the vessel body (2) and the front tube plate of the furnace tube (5) via the burner mounting tube (21). ing. Then, between the front tube plate of the vessel body (2) and the front tube plate of the furnace tube (5>),
A solution flow path ( 22), (23), (24), and (25) are formed.
上記のように構成された直焚発生器が吸収冷凍機の運転
に伴い運転されているときには、吸収器（図示せず）か
ら稀吸収液が補液入口管（１７）を介して器胴（１）内
へ流入する。又、燃焼装置（２０）が燃焼して火炎が炉
筒（４）内に形成される。火炎は炉筒（４）内で燃焼を
完了し、燃焼ガスが第１図に実線矢印にて示したように
後部煙室（９）を通り、煙道（１１）へ流れる。煙道（
１１）を通った燃焼ガスは前部煙室（１３）及び煙突（
１４）内を通り外部へ排出される。そして、器胴（１〉
内へ流入した稀吸収液は溶液流路（２２） 、 （２３
） 、 （２４）、及び（２５）を流れる間に加熱され
る。加熱されて高温（例えば約１５０℃）になった稀吸
収液から発生した蒸気泡が溶液流路（２３）の後部及び
溶液流路（２４）を上昇する。このとき、炉筒後部管板
（６）の溶液流路（２４）側の面から発生した蒸気泡は
溶液流路（２４）にほぼ垂直に設けられた整流板（７）
・・・に案内され、蒸気泡の流れのうち水平方向の成分
が大幅に減少する。そして、溶液流路（２４）では気泡
ポンプ効果によって稀吸収液の上昇速度が速くなる。こ
のため、溶液流路（２４）の下部の稀吸収液が吸い上げ
られ、溶液流路（２３）の後部下方、及び溶液流路（２
４）の下部の稀吸収液の流動が活発になる。When the direct-fired generator configured as described above is operated in conjunction with the operation of the absorption refrigerator, the diluted absorption liquid is supplied from the absorber (not shown) to the vessel body (1) through the replacement liquid inlet pipe (17). ) flows into the inside. Also, the combustion device (20) burns and a flame is formed in the furnace tube (4). The flame completes combustion within the furnace tube (4), and the combustion gases flow through the rear smoke chamber (9) and into the flue (11) as indicated by solid arrows in FIG. Flue (
The combustion gases passing through 11) are sent to the front smoke chamber (13) and the chimney (
14) It passes through the inside and is discharged to the outside. And the body (1)
The dilute absorption liquid that has flowed into the solution flow path (22), (23
), (24), and (25). Steam bubbles generated from the dilute absorption liquid that has been heated to a high temperature (for example, about 150° C.) rises at the rear of the solution flow path (23) and through the solution flow path (24). At this time, steam bubbles generated from the solution flow path (24) side surface of the rear tube plate (6) of the furnace cylinder are removed by a straightening plate (7) installed almost perpendicularly to the solution flow path (24).
..., and the horizontal component of the flow of vapor bubbles is significantly reduced. In the solution flow path (24), the rising speed of the dilute absorption liquid increases due to the bubble pump effect. For this reason, the dilute absorption liquid at the bottom of the solution flow path (24) is sucked up, and the solution flow path (23) and the rear lower part of the solution flow path (24) are sucked up.
4) The flow of the dilute absorption liquid at the bottom becomes active.
上記のように稀吸収液の流動が活発になると、液側の熱
伝達量が増大し、煙道（１１）へ流れる燃焼ガスの温度
が低下する。又、整流板（７）・・・によって溶液流路
（２４）での液側伝熱面積が増大し、稀吸収液と燃焼ガ
スとの熱交換量がさらに増大して煙道（１１）に流れる
燃焼ガスの温度が一層低下する。When the flow of the dilute absorption liquid becomes active as described above, the amount of heat transferred to the liquid side increases, and the temperature of the combustion gas flowing into the flue (11) decreases. In addition, the heat transfer area on the liquid side in the solution flow path (24) is increased by the current plate (7)..., and the amount of heat exchange between the dilute absorption liquid and the combustion gas is further increased, and the heat transfer area is increased in the flue (11). The temperature of the flowing combustion gas is further reduced.
上記実施例によれば、直焚発生器の運転時、炉筒後部管
板（１６）の溶液流路（２４）側の面から発生した蒸気
泡は整流板（７）・・・に案内されて上昇し、蒸気泡の
流れの水平方向成分が大幅に減少し、溶液流路（２４）
では気泡ポンプ効果によって稀吸収液の上昇速度が速く
なる。このため、溶液流路（２４）の下部、及び溶液流
路（２３）の後部下方の稀吸収液の流れが速くなり、液
側の熱伝達量が増大し、稀吸収液と燃焼ガスとの熱交換
量が増加する。この結果、煙道（１１）へ流れる燃焼ガ
スの温度が低下し、煙管（１０）の入口部の過熱を回避
することができ、煙管（１０）の腐食を防止することが
できる。According to the above embodiment, during operation of the direct-fired generator, steam bubbles generated from the solution flow path (24) side surface of the furnace tube rear tube plate (16) are guided to the rectifier plate (7)... The horizontal component of the vapor bubble flow is significantly reduced, and the solution flow path (24)
In this case, the rising speed of the dilute absorption liquid becomes faster due to the bubble pump effect. Therefore, the flow of the dilute absorption liquid at the lower part of the solution flow path (24) and the rear lower part of the solution flow path (23) becomes faster, the amount of heat transfer on the liquid side increases, and the flow of the dilute absorption liquid and the combustion gas increases. The amount of heat exchange increases. As a result, the temperature of the combustion gas flowing into the flue (11) decreases, making it possible to avoid overheating of the entrance portion of the smoke pipe (10) and preventing corrosion of the smoke pipe (10).
又、整流板（７）・・・によって溶液流路（２４）での
伝熱面積が増大し、稀吸収液と燃焼ガスとの熱交換量を
さらに増大することができ、この結果、稀吸収液の加熱
効率を向上させることができ、又、煙道（１１）へ流れ
る燃焼ガスの温度を一層低くすることができる。In addition, the heat transfer area in the solution flow path (24) is increased by the current plate (7), and the amount of heat exchange between the dilute absorption liquid and the combustion gas can be further increased. The heating efficiency of the liquid can be improved, and the temperature of the combustion gas flowing into the flue (11) can be further lowered.
又、煙道（１１）に上下方向に木管を設け、これらの木
管に吸収液が流れるように構成した発生器においても、
上記実施例のように炉筒後部管板に上下方向に複数の板
を接続することによって煙道入口部の木管の過熱を回避
でき、木管の腐食を防止することができる。Also, in a generator configured such that the flue (11) is provided with wood pipes in the vertical direction, and the absorbent liquid flows through these wood pipes,
By connecting a plurality of plates vertically to the tube plate at the rear of the furnace cylinder as in the above embodiment, overheating of the wood pipe at the flue inlet can be avoided, and corrosion of the wood pipe can be prevented.
第４図は本発明の他の実施例を示した直焚発生器の要部
切欠き断面図であり、第１図及び第２図と同じ構成のも
のには同様の図番を付し、その詳細な説明は省略する。FIG. 4 is a cutaway sectional view of the main parts of a direct-fired generator showing another embodiment of the present invention, and parts having the same configuration as those in FIGS. 1 and 2 are given the same figure numbers. A detailed explanation thereof will be omitted.
第４図において、（２７）・・・は器胴後部管板（３）
の溶液流路（２４）側の面に上下方向に接続された整流
板である。これらの整流板（２７）・・・はそれぞれ器
胴後部管板（３）に並行に例えば溶接接続されている。In Fig. 4, (27)... is the rear tube plate of the vessel (3)
This is a rectifying plate connected vertically to the surface on the solution flow path (24) side. These rectifier plates (27) are each connected in parallel to the vessel rear tube plate (3) by, for example, welding.
このため、上記実施例と同様に、溶液流路（２４）に発
生した蒸気泡は整流板（２７）・・・に案内されて上昇
し、気泡ポンプ効果によって稀吸収液の上昇が速くなり
、稀吸収液と燃焼ガスとの熱交換量が増え、上記実施例
と同様の作用効果を得ることができる。Therefore, similarly to the above embodiment, the vapor bubbles generated in the solution flow path (24) are guided by the rectifying plate (27) and rise, and the dilute absorption liquid rises faster due to the bubble pump effect. The amount of heat exchange between the dilute absorption liquid and the combustion gas increases, and the same effects as in the above embodiment can be obtained.
（ト）発明の効果
本発明は以上のように構成された直焚発生器であり、器
胴後部管板と炉筒後部管板との間に形成された溶液流路
に上下方向に複数の板を設け、これらの板を炉筒後部管
板に接続したので、直焚発生器の運転時、溶液流路に発
生した蒸気泡が各板に案内され、蒸気泡の横方向への流
れを僅かに抑えることができ、気泡ポンプ効果によって
溶液流路の吸収液の上昇速度が速くなる。この結果、溶
液流路の下部の吸収液が吸い上げられて流れが速くなり
、熱の吸収液の伝達量が増大し、煙道に流入する燃焼ガ
スの温度を下げることができ、煙道入口部の過熱を回避
して腐食を防止することができる
さらに、炉筒後部管板に接続された複数の板によって、
溶液流路での燃焼ガスから吸収液への伝熱面積が増大し
、吸収液の加熱効率を向上させることができ、煙道へ流
入する燃焼ガスの温度を一層低くすることができる。(G) Effects of the Invention The present invention is a direct-fired generator configured as described above, in which a plurality of vertically arranged solution channels are formed between the rear tube plate of the vessel body and the rear tube plate of the furnace cylinder. These plates are connected to the tube plate at the rear of the furnace cylinder, so that when the direct-fired generator is operating, steam bubbles generated in the solution flow path are guided by each plate, and the horizontal flow of steam bubbles is prevented. This can be suppressed slightly, and the rising speed of the absorption liquid in the solution flow path becomes faster due to the bubble pump effect. As a result, the absorption liquid at the bottom of the solution flow path is sucked up and the flow becomes faster, the amount of heat transferred by the absorption liquid increases, and the temperature of the combustion gas flowing into the flue can be lowered. In addition, multiple plates connected to the rear tube plate of the furnace cylinder can avoid overheating and prevent corrosion.
The heat transfer area from the combustion gas to the absorption liquid in the solution flow path increases, the heating efficiency of the absorption liquid can be improved, and the temperature of the combustion gas flowing into the flue can be further lowered.
又、器胴後部管板の溶液流路側の面に上下方向に複数の
板を接続することにより、溶液流路に発生した蒸気泡が
各板に案内されて上方へ移動し、気泡ポンプ効果によっ
て吸収液の上昇速度が速くなる。この結果、溶液流路の
下部の吸収液を吸い上げることができ、吸収液の流れが
速くなり吸収液への熱伝達量が増大し、煙道に流入する
燃焼ガスの温度を下げることができ、煙道入口部の過熱
を回避して腐食を防止することができる。In addition, by connecting multiple plates vertically to the solution flow path side surface of the rear tube plate of the vessel, the vapor bubbles generated in the solution flow path are guided by each plate and move upward, resulting in a bubble pump effect. The rising speed of the absorption liquid becomes faster. As a result, the absorption liquid at the bottom of the solution flow path can be sucked up, the flow of the absorption liquid becomes faster, the amount of heat transferred to the absorption liquid increases, and the temperature of the combustion gas flowing into the flue can be lowered. Corrosion can be prevented by avoiding overheating of the flue inlet.
第１図は本発明の一実施例を示す直焚発生器の断面図、
第２図は同じく直焚発生器の一部切欠き斜視図、第３図
は同じく直焚発生器の後部形状を説明するための断面図
、第４図は本発明の他の実施例を示す直焚発生器の後部
形状を説明するための断面図である。
（１）・・・器胴、 （３〉・・・器胴後部管板、 （
４）・・・炉筒、 （６〉・・・炉筒後部管板、 （７
）・・・整流板、 （１１）・・・煙道、 （２４）・
・・溶液流、路、 （２７）・・・整流板。FIG. 1 is a sectional view of a direct-fired generator showing an embodiment of the present invention;
Fig. 2 is a partially cutaway perspective view of the direct-fired generator, Fig. 3 is a sectional view for explaining the rear shape of the direct-fired generator, and Fig. 4 shows another embodiment of the present invention. It is a sectional view for explaining the shape of the rear part of the direct-fired generator. (1)...Vessel body, (3>...Vessel rear tube plate, (
4)...Furnace tube, (6>...Furnace tube rear tube plate, (7)
)... Rectifier plate, (11)... Flue, (24)...
...Solution flow, path, (27)...Brighter plate.
Claims (1)
胴内に配置された炉筒と、この炉筒に接続された炉筒後
部管板と、この炉筒後部管板と器胴後部管板との間に形
成された溶液流路と、上記炉筒の内部と連通した煙道と
を備えた直焚発生器において、炉筒後部管板の溶液流路
側の面に上下方向に複数の板を接続したことを特徴とす
る直焚発生器。 ２、器胴と、この器胴に接続された器胴後部管板と、器
胴内に配置された炉筒と、この炉筒に接続された炉筒後
部管板と、この炉筒後部管板と器胴後部管板との間に形
成された溶液流路と、上記炉筒の内部と連通した煙道と
を備えた直焚発生器において、器胴後部管板の溶液流路
側の面に上下方向に複数の板を接続したことを特徴とす
る直焚発生器。[Claims] 1. A vessel body, a rear tube plate of the vessel body connected to the vessel body, a furnace tube disposed within the vessel body, and a rear tube plate of the furnace tube connected to the furnace tube. In a direct firing generator including a solution flow path formed between the rear tube plate of the furnace cylinder and the rear tube plate of the furnace cylinder, and a flue communicating with the inside of the furnace cylinder, the rear tube plate of the furnace cylinder A direct-fired generator characterized by having a plurality of plates connected vertically to the surface on the solution flow path side. 2. A vessel body, a rear tube plate of the vessel body connected to the vessel body, a furnace tube disposed within the vessel body, a rear tube plate of the furnace tube connected to this furnace tube, and a rear tube of the furnace tube In a direct-fired generator equipped with a solution flow path formed between a plate and a rear tube sheet of the container body, and a flue communicating with the inside of the furnace cylinder, the surface of the rear tube sheet of the container body on the side of the solution flow path. A direct-fired generator characterized by having multiple plates connected vertically.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2022383A JPH0711371B2 (en) | 1990-01-31 | 1990-01-31 | Direct-fired generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2022383A JPH0711371B2 (en) | 1990-01-31 | 1990-01-31 | Direct-fired generator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03225164A true JPH03225164A (en) | 1991-10-04 |
| JPH0711371B2 JPH0711371B2 (en) | 1995-02-08 |
Family
ID=12081132
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2022383A Expired - Lifetime JPH0711371B2 (en) | 1990-01-31 | 1990-01-31 | Direct-fired generator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0711371B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5787727A (en) * | 1995-10-19 | 1998-08-04 | Ebara Corporation | High-temperture generator |
| JP2012237464A (en) * | 2011-05-10 | 2012-12-06 | Kawasaki Thermal Engineering Co Ltd | Absorption refrigerator |
-
1990
- 1990-01-31 JP JP2022383A patent/JPH0711371B2/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5787727A (en) * | 1995-10-19 | 1998-08-04 | Ebara Corporation | High-temperture generator |
| JP2012237464A (en) * | 2011-05-10 | 2012-12-06 | Kawasaki Thermal Engineering Co Ltd | Absorption refrigerator |
Also Published As
| Publication number | Publication date |
|---|---|
| JPH0711371B2 (en) | 1995-02-08 |
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