JP2783864B2 - Direct-fired high-temperature regenerator - Google Patents
Direct-fired high-temperature regeneratorInfo
- Publication number
- JP2783864B2 JP2783864B2 JP1259333A JP25933389A JP2783864B2 JP 2783864 B2 JP2783864 B2 JP 2783864B2 JP 1259333 A JP1259333 A JP 1259333A JP 25933389 A JP25933389 A JP 25933389A JP 2783864 B2 JP2783864 B2 JP 2783864B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- water pipe
- temperature regenerator
- refrigerant vapor
- burner
- 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.)
- Expired - Fee Related
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 107
- 239000007788 liquid Substances 0.000 claims description 29
- 239000003507 refrigerant Substances 0.000 claims description 28
- 238000010438 heat treatment Methods 0.000 claims description 4
- 238000004140 cleaning Methods 0.000 description 23
- 238000011144 upstream manufacturing Methods 0.000 description 13
- 238000010521 absorption reaction Methods 0.000 description 9
- 230000002745 absorbent Effects 0.000 description 6
- 239000002250 absorbent Substances 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 238000013021 overheating Methods 0.000 description 5
- 239000000567 combustion gas Substances 0.000 description 4
- 239000012459 cleaning agent Substances 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000004071 soot Substances 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 239000006096 absorbing agent Substances 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000002542 deteriorative effect Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
Landscapes
- Sorption Type Refrigeration Machines (AREA)
Description
【発明の詳細な説明】 (イ)産業上の利用分野 本発明は炉筒に水管群を配設した直焚高温再生器に関
する。The present invention relates to a direct-fired high-temperature regenerator in which a water tube group is provided in a furnace tube.
(ロ)従来の技術 例えば特開昭58−173360号公報には、炉筒内に溶液管
群を略垂直に配設し、バーナの燃焼ガスにより溶液管内
の吸収液を加熱して冷媒蒸気を発生させる直焚高温再生
器が開示されている。上記直焚高温再生器では、水管を
千鳥に配列することによって燃焼ガスの乱流促進効果が
得られるので炉内圧力を一般に低く抑えることができ
る。(B) Conventional technology For example, in Japanese Patent Application Laid-Open No. 58-173360, a group of solution tubes is disposed substantially vertically in a furnace tube, and the absorption liquid in the solution tube is heated by combustion gas of a burner to generate refrigerant vapor. A direct-fired high temperature regenerator to be generated is disclosed. In the above-mentioned direct-fired high-temperature regenerator, by arranging the water pipes in a staggered manner, the effect of promoting the turbulence of the combustion gas can be obtained, so that the pressure in the furnace can generally be kept low.
(ハ)発明が解決しようとする課題 上記従来の技術において、長期間バーナを燃焼させた
場合には、水管の表面にススや、イオウ分などの未燃物
が付着して、伝熱性能が低下する。そして、例えばバー
ナを外して水管群に薬剤をジェット噴霧して未燃物の除
去作業を行っていたが、水管配列が千鳥状になっている
ため、薬剤が水管群の中央部までとどきにくいばかりで
なく、水管群から剥離した未燃物の堆積物を完全に除去
できないという問題が発生していた。又、バーナの奥に
水管群が配置されているため、高温再生器の奥行きが長
くなり、吸収冷凍機に占める高温再生器の設置スペース
の割合が大きくなり、この結果、機械全体が大型化する
という問題が発生していた。(C) Problems to be solved by the invention In the above-mentioned conventional technology, when the burner is burned for a long time, unburned substances such as soot and sulfur adhere to the surface of the water pipe, and the heat transfer performance is reduced. descend. And, for example, removing the burner and spraying chemicals to the water tube group to remove unburned substances, but since the water tube arrangement is staggered, it is difficult for the chemical to reach the center of the water tube group In addition, there has been a problem that the deposits of unburned matter separated from the water tube group cannot be completely removed. In addition, since the water tube group is arranged at the back of the burner, the depth of the high-temperature regenerator becomes longer, and the proportion of the installation space of the high-temperature regenerator in the absorption refrigerator becomes larger, and as a result, the entire machine becomes larger. The problem had occurred.
本発明は、高温再生器の洗浄作業の簡略化を図るとと
もに、高温再生器の伝熱性能を損うことなくコンパクト
化を図ることを目的とする。An object of the present invention is to simplify the cleaning operation of the high-temperature regenerator and to make the high-temperature regenerator compact without impairing the heat transfer performance.
(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、吸収液の供給さ
れる水管群(11A)を炉筒(2)に設け、水管(11)…
内の吸収液をバーナ(13)により加熱して冷媒蒸気を発
生する直焚高温再生器において、炉筒(2)の周囲に水
壁(4)を形成し、水管群(11A)を上流側が低く下流
側が高くなるように傾斜して炉筒に設け、かつ、バーナ
(13)を水管群(11A)の上流側の炉筒(2)下部に設
けた直焚高温再生器(1)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 provides a water pipe group (11A) to which an absorbent is supplied in a furnace tube (2), and a water pipe (11) ...
A water wall (4) is formed around a furnace tube (2) in a direct-fired high-temperature regenerator that generates refrigerant vapor by heating an absorbing solution in a furnace by a burner (13), and an upstream side of a water tube group (11A) is formed. Provided is a direct-fired high-temperature regenerator (1) provided in a furnace tube at an angle so as to be low and high on the downstream side, and a burner (13) provided below the furnace tube (2) on the upstream side of the water tube group (11A). Is what you do.
(ホ)作 用 吸収冷凍機の運転に伴い直焚高温再生器(1)が運転
されているときには、バーナ(13)からの燃焼ガスによ
り水管群(11A)が加熱され、水管群(11A)で冷媒蒸気
が発生し、この冷媒蒸気は水管群(11A)の傾斜のため
に水管(11)…内を上流側から下流側へ流れ、それに伴
い水管(11)…内の吸収液も下流側から上流側に流れ、
水管群(11A)に冷媒蒸気、及び吸収液が滞溜して水管
群(11A)の局部過熱、吸収液の過濃縮を回避すること
が可能になる。又、水管群(11A)とバーナ(13)との
上下配置により直焚高温再生器(1)のコンパクト化を
図ることが可能になる。さらに、水管群(11A)の清掃
時、水管群(11A)に上方から噴霧された洗浄剤は下方
の水管まで流下し、水管群(11A)のほぼ全体にゆきわ
たり、水管群(11A)全体の未燃物を除去することが可
能になる。(E) Operation When the direct-fired high-temperature regenerator (1) is operated in conjunction with the operation of the absorption refrigerator, the water pipe group (11A) is heated by the combustion gas from the burner (13), and the water pipe group (11A) is heated. The refrigerant vapor is generated at this time, and the refrigerant vapor flows from the upstream side to the downstream side in the water pipe (11) due to the inclination of the water pipe group (11A), and accordingly, the absorbing liquid in the water pipe (11) also flows downstream. Flows upstream from
Refrigerant vapor and absorption liquid stay in the water pipe group (11A), and local overheating of the water pipe group (11A) and excessive concentration of the absorption liquid can be avoided. Further, the vertical arrangement of the water pipe group (11A) and the burner (13) makes it possible to reduce the size of the direct-fired high-temperature regenerator (1). Furthermore, when cleaning the water pipe group (11A), the cleaning agent sprayed from above onto the water pipe group (11A) flows down to the lower water pipe, and spreads over almost the entire water pipe group (11A), and the entire water pipe group (11A). It becomes possible to remove the unburned matter.
又、炉筒(2)の上部に傾斜して設けられた水管群
(11A)で発生した冷媒蒸気は水管群(11A)の各水管内
を上方へ移動し、それに伴い吸収液も移動し、冷媒蒸気
の局部過熱、吸収液の過濃縮を回避することが可能にな
り、又、水管群の清掃時上方から噴霧された洗浄剤は水
管群の下部まで移動し、ほぼ全体にゆきわたり、未燃物
の除去作業を完全にかつ容易に行うことが可能になる。Refrigerant vapor generated in the water tube group (11A) provided at the upper part of the furnace tube (2) is moved upward in each water tube of the water tube group (11A), and the absorbing liquid is moved accordingly, It is possible to avoid local overheating of the refrigerant vapor and overconcentration of the absorbing liquid, and the cleaning agent sprayed from above during cleaning of the water pipe group moves to the lower part of the water pipe group, and spreads over almost the entirety, and does not spread. It is possible to completely and easily perform the work of removing the combustibles.
さらに、水管群(11A)の上流側の炉筒(2)下部に
設けられたバーナ(13)により、直焚高温再生器(1)
の運転時、バーナ(13)に相対した水壁(4)の吸収液
が温度上昇し、大量に発生した冷媒蒸気は水壁(4)を
上方へ移動して水管群(11A)から流出した冷媒蒸気と
ともに高温再生器(1)から流出し、冷媒蒸気の高温再
生器(1)内での滞溜を回避することが可能になる。Further, a direct-fired high-temperature regenerator (1) is provided by a burner (13) provided below the furnace tube (2) on the upstream side of the water tube group (11A).
During the operation, the temperature of the absorbent on the water wall (4) facing the burner (13) rises, and a large amount of refrigerant vapor moves upward along the water wall (4) and flows out of the water pipe group (11A). The refrigerant vapor flows out of the high-temperature regenerator (1) together with the refrigerant vapor, and the refrigerant vapor can be prevented from remaining in the high-temperature regenerator (1).
(ヘ)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 with reference to the drawings.
(1)は吸収冷凍機の直焚高温再生器であり、(2)
は炉筒、(3A),(3B)は端板である。そし、炉筒
(2)と端板(3A),(3B)との間には水壁(4)が設
けられている。又、炉筒(2)と外壁(5)との間には
水壁(4)が設けられ、この水壁(4)に吸収液か溜っ
ている。さらに、端板(3A)には吸収液入口ヘッダ
(6)が取付けられ、この入口ヘッダ(6)には吸収液
管(7)が接続されている。又、端板(3B)には吸収
液、及び冷媒の出口ヘッダ(8)が取付けられ、この出
口ヘッダ(8)には吸収液、及び冷媒の送り管(10)が
接続されている。(11A)は炉筒(2)内の燃焼室(2
A)の上方に渡された水管群であり、各水管(11)…の
一端は入口ヘッダ(6)内に開口し、他端は出口ヘッダ
(8)内に開口している。さらに、各水管(11)…は入
口ヘッダ(6)側、即ち上流側を低く、出口ヘッダ
(8)側、即ち下流側を高くして角度(θ)傾斜してい
る。又、下部の水管(11)…は上部2段の水管(11)…
より密に設けられている。(1) is a direct-fired high-temperature regenerator of an absorption refrigerator, and (2)
Is a furnace tube, and (3A) and (3B) are end plates. A water wall (4) is provided between the furnace tube (2) and the end plates (3A) and (3B). Further, a water wall (4) is provided between the furnace tube (2) and the outer wall (5), and the absorbing liquid is stored on the water wall (4). Further, an absorbing liquid inlet header (6) is attached to the end plate (3A), and an absorbing liquid pipe (7) is connected to the inlet header (6). An outlet header (8) for absorbing liquid and refrigerant is attached to the end plate (3B), and a feed pipe (10) for absorbing liquid and refrigerant is connected to the outlet header (8). (11A) is the combustion chamber (2
A group of water pipes passed above A). One end of each water pipe (11) is open in the inlet header (6), and the other end is open in the outlet header (8). Further, each water pipe (11) is inclined at an angle (θ) with the inlet header (6) side, that is, the upstream side being low, and the outlet header (8) side, that is, the downstream side being high. The lower water pipe (11) is the upper two-stage water pipe (11).
It is provided more densely.
(12)は入口ヘッダ(6)下方の炉筒(2)、及び端
板(3A)を貫通して設けられたバーナ取付け用の開口
で、この開口(12)に例えば石油バーナ(13)が取付け
られている。又、(14)は炉筒(2)の上端に接続され
た蓋であり、この蓋には燃焼ガス排気筒(15)が接続さ
れている。そして排気筒(15)に排気管(図示せず)が
接続される。(12) is an opening for mounting a burner provided through the furnace tube (2) below the inlet header (6) and the end plate (3A). For example, an oil burner (13) is inserted into the opening (12). Installed. Reference numeral (14) denotes a lid connected to the upper end of the furnace tube (2), and a combustion gas exhaust tube (15) is connected to this lid. Then, an exhaust pipe (not shown) is connected to the exhaust pipe (15).
上記のように構成された高温再生器(1)では、吸収
冷凍機の運転時、吸収器(図示せず)から稀吸収液が入
口ヘッダ(6)へ流れる。また、石油バーナ(13)は燃
焼し各水管(11)…内の稀吸収液が加熱される。そし
て、水管(11)…内にて発生した冷媒蒸気は傾斜した水
管(11)…内を蒸気と吸収液との密度差により出口ヘッ
ダ(8)側へ移動する。また、冷媒蒸気が水管(11)…
内を出口ヘッダ(8)側へ移動するのに伴い、各管内の
濃縮された吸収液を出口ヘッダ(8)へ押し出すととも
に、水管(11)…の入口ヘッダ(7)側開口から稀吸収
液が各水管(11)…内に流入する。また、出口ヘッダ
(8)より下の水壁(4)はバーナ(13)と対している
ため、水管(11)…の出口側の水壁(4)の稀吸収液は
バーナ(13)からの炎により加熱される。そして、稀吸
収液から多量の冷媒蒸気が分離し、この冷媒蒸気は上方
へ移動し、出口ヘッダ(8)に入り、出口ヘッダ(8)
から各水管(11)…を移動して来た冷媒蒸気、吸収液と
一緒に出口ヘッダ(8)上方の分離器(図示せず)へ移
動する。In the high-temperature regenerator (1) configured as described above, the diluted absorption liquid flows from the absorber (not shown) to the inlet header (6) during the operation of the absorption refrigerator. Further, the oil burner (13) burns, and the rare absorbing liquid in each of the water pipes (11) is heated. The refrigerant vapor generated in the water pipes (11) moves in the inclined water pipes (11) to the outlet header (8) due to the density difference between the vapor and the absorbing liquid. In addition, the refrigerant vapor flows into the water pipe (11) ...
As the water moves toward the outlet header (8), the concentrated absorbent in each pipe is pushed out to the outlet header (8), and the diluted absorbent is supplied from the opening of the water pipe (11). Flows into each water pipe (11). Also, since the water wall (4) below the outlet header (8) is opposed to the burner (13), the rare absorbing liquid in the water wall (4) on the outlet side of the water pipes (11) ... is discharged from the burner (13). Heated by the flame. Then, a large amount of refrigerant vapor is separated from the rare absorbing liquid, and this refrigerant vapor moves upward, enters the outlet header (8), and exits the outlet header (8).
Move to the separator (not shown) above the outlet header (8) together with the refrigerant vapor and the absorbing liquid that have moved through the water pipes (11).
上記のように運転される高温再生器(1)において、
長時間使用すると、バーナ(13)に供給されていた石油
に含まれていたイオウ、ススなどの未燃物が次第に各水
管(11)…の表面に付着し、熱交換効率が次第に低下す
る。このため、例えば所定時間ごとに定期的に炉筒
(2)内の清掃が管理者により行われる。この清掃時に
はバーナ(13)、及び炉筒(2)上部の蓋(14)が外さ
れ、水管群(11A)の上方からノズルにより洗浄液(薬
剤)がジェット噴霧される。そして、洗浄液が最上段の
水管(11)…から順次下段の水管(11)…へ流下し、全
ての水管(11)…へ洗浄液がゆきわたる。そして水管
(11)…の表面から剥離した未燃物が全て炉筒(2)の
底部に落下する。その後、バーナ取付け用の開口(12)
から未燃物が外部へ排出される。In the high-temperature regenerator (1) operated as described above,
When used for a long time, unburned substances such as sulfur and soot contained in the oil supplied to the burner (13) gradually adhere to the surface of each water pipe (11), and the heat exchange efficiency gradually decreases. For this reason, the inside of the furnace tube (2) is periodically cleaned by the manager at predetermined time intervals, for example. During this cleaning, the burner (13) and the lid (14) at the top of the furnace tube (2) are removed, and the cleaning liquid (chemical) is jet-sprayed from above the water tube group (11A) by a nozzle. Then, the cleaning liquid flows down sequentially from the uppermost water pipe (11) to the lower water pipe (11), and the cleaning liquid spreads to all the water pipes (11). Then, all the unburned matter separated from the surface of the water pipes (11) falls to the bottom of the furnace tube (2). Then the opening for the burner installation (12)
Unburned matter is discharged from outside.
そして、清掃作業が終了すると、バーナ(13)が開口
(12)に取付けられるとともに、蓋(14)が炉筒(2)
の上端に取付けられる。When the cleaning operation is completed, the burner (13) is attached to the opening (12), and the lid (14) is attached to the furnace tube (2).
Attached to the upper end of
上記実施例では高温再生器(1)の水管(11)…が上
流側が低く下流側が高くなるように傾斜して炉筒(2)
に配置されているので、高温再生器(1)の運転時、水
管(11)…で発生した冷媒蒸気が次第に高い上流側へ移
動し出口ヘッダ(8)内へ吐出され、冷媒蒸気が水管
(11)…内に滞溜することを防止でき、この結果、水管
(11)…の伝熱性能の低下、局部加熱を防止でき、又、
吸収液の滞溜による過濃縮を回避することができる。In the above embodiment, the water pipes (11) of the high temperature regenerator (1) are inclined so that the upstream side is lower and the downstream side is higher, so that the furnace tube (2)
During the operation of the high-temperature regenerator (1), the refrigerant vapor generated in the water pipes (11) moves to a higher upstream side gradually and is discharged into the outlet header (8). 11) can be prevented from accumulating in the inside, as a result, the heat transfer performance of the water pipe (11) can be prevented from lowering and local heating can be prevented.
Overconcentration due to accumulation of the absorbing solution can be avoided.
又、高温再生器(1)の清掃時には、水管群(11A)
の上方から洗浄液をジェット噴霧することにより、上段
の水管から下方の水管へ順次洗浄液か流下し、全ての水
管(11)…にまんべんなく洗浄液がゆきわたり、洗浄液
を有効に使うことができるとともに、各水管(11)…か
ら容易にかつ確実に未燃物を除去することができる。Also, when cleaning the high-temperature regenerator (1), the water pipe group (11A)
By jet spraying the cleaning liquid from above, the cleaning liquid flows down from the upper water pipe to the lower water pipe sequentially, so that the cleaning liquid can be spread evenly in all the water pipes (11) ... and the cleaning liquid can be used effectively. Unburned matter can be easily and reliably removed from the water pipe (11).
さらに、炉筒(2)の上部に水管群(11A)が配設さ
れているので、奥行き(L)を従来のものに比べて略半
分にすることができ、高温再生器(1)の設置スペース
を削減して吸収冷凍機全体のコンパクト化を図ることが
できる。Further, since the water tube group (11A) is arranged at the upper part of the furnace tube (2), the depth (L) can be reduced to approximately half as compared with the conventional one, and the high temperature regenerator (1) is installed. Space can be reduced and the entire absorption refrigerator can be made more compact.
又、バーナ(13)が水管群(11A)の上流側から下流
側へ向いて取付けられているため、バーナ(13)と対向
した水壁(4)で多量に発生した冷媒蒸気を水管(11)
…を介さずに出口ヘッダ(8)へ流すことができるとと
もに、冷媒蒸気の水壁(4)上部での滞溜を防止でき、
水壁(4)上部の局部過熱、過濃縮を回避することがで
きる。Further, since the burner (13) is attached from the upstream side to the downstream side of the water pipe group (11A), a large amount of refrigerant vapor generated on the water wall (4) facing the burner (13) is transferred to the water pipe (11A). )
… Can flow to the outlet header (8) without passing through, and the refrigerant vapor can be prevented from stagnating above the water wall (4),
Local overheating and overconcentration at the upper part of the water wall (4) can be avoided.
尚、本発明は上記実施例に限定されるものではなく、
例えば吸収液管(7)を第2図に破線にて示したよう
に、バーナ(13)と対向した端板(8)の下部に接続し
ても良い。又、上記実施例にて水管群の清掃時には蓋
(14)を取り外して清掃を行ったが、例えば蓋(14)に
第2図に示したように清掃用の開口(20)を形成し、こ
の開口(20)に着脱自在な蓋(21)を取付ける。そし
て、水管群(11A)の清掃を行うときには蓋(21)を取
外し、開口(21)から洗浄用ノズルを差し込み、各水管
(11)…の清掃を行っても良い。The present invention is not limited to the above embodiment,
For example, the absorbent pipe (7) may be connected to a lower portion of the end plate (8) facing the burner (13) as shown by a broken line in FIG. In the above embodiment, the lid (14) was removed for cleaning when cleaning the water tube group. For example, the lid (14) was provided with a cleaning opening (20) as shown in FIG. A detachable lid (21) is attached to the opening (20). When cleaning the water pipe group (11A), the lid (21) may be removed, a cleaning nozzle may be inserted through the opening (21), and the water pipes (11)... May be cleaned.
(ト)発明の効果 本発明は以上のように構成された直焚高温再生器であ
り、水管群は上流側が低く下流側か高くなるように炉筒
を上部に傾斜して配設され、バーナは炉筒の下部に配設
されているので、高温再生器の運転時、バーナの燃焼に
より、水管内で吸収液から分離した冷媒蒸気は管内に滞
溜することなく上流側から下流側へ流れ、水管の伝熱性
能の低下、局部過熱を防止することができ、又、吸収液
の過濃縮を回避することができる。又、水管の清掃時に
は上方から水管群に洗浄液を噴霧することにより洗浄液
が上段の水管から下段の水管へ流下し、全ての水管に洗
浄剤がゆきわたり、各水管に付着した未燃物を容易にか
つ確実に除去することができる。さらに、伝熱性能を損
うことなく高温再生器をコンパクト化することができ
る。(G) Effect of the Invention The present invention is a direct-fired high-temperature regenerator configured as described above. The water tube group is disposed such that the furnace tube is inclined upward so that the upstream side is low and the downstream side is high, and the burner Is located in the lower part of the furnace tube, so that during operation of the high-temperature regenerator, the combustion of the burner causes the refrigerant vapor separated from the absorbent in the water tube to flow from the upstream side to the downstream side without stagnation in the tube. In addition, it is possible to prevent the heat transfer performance of the water pipe from deteriorating and to prevent local overheating, and to avoid excessive concentration of the absorbing solution. In addition, when cleaning the water pipes, the cleaning liquid flows from the upper water pipe to the lower water pipe by spraying the cleaning liquid onto the water pipe group from above, so that the cleaning agent spreads through all the water pipes and easily removes unburned matter adhering to each water pipe. And can be reliably removed. Further, the high-temperature regenerator can be made compact without impairing the heat transfer performance.
又、水管群を炉筒上部には配置するとともに、水管群
が水平に対しある角度をもって取付けられているので、
水管内で発生した冷媒蒸気は管内に溜ることなく上方へ
移動し、水管の局部加熱、過濃縮を防止でき、又、水管
群の清掃時には洗浄液を上方から噴霧し、全ての水管を
容易に洗浄でき、さらに、高温再生器のコンパクト化を
図ることができる。In addition, since the water tube group is arranged at the top of the furnace tube and the water tube group is attached at a certain angle to the horizontal,
Refrigerant vapor generated in the water pipes moves upward without accumulating in the pipes, preventing local heating and over-concentration of the water pipes. In addition, when cleaning the water pipe group, the cleaning liquid is sprayed from above to easily clean all the water pipes. It is possible to further reduce the size of the high-temperature regenerator.
さらに、炉筒の周囲に水壁を形成し、水管群を上流側
が低く、下流側が高くなるように傾斜して炉筒に配設
し、バーナを水管群の上流側の炉筒下部に設けているの
で、水管の下流側下方の水壁で発生した多量の冷媒蒸気
を水管内を移動して来た冷媒蒸気と一緒に速やかに排出
でき、冷媒蒸気の水壁上部での滞溜を回避でき、水壁上
部の局部過熱、過濃縮を防止することができる。Further, a water wall is formed around the furnace tube, and the water tube group is disposed in the furnace tube at an inclination such that the upstream side is low and the downstream side is high, and a burner is provided at a lower part of the furnace tube on the upstream side of the water tube group. As a result, a large amount of refrigerant vapor generated at the lower water wall downstream of the water pipe can be quickly discharged together with the refrigerant vapor moving inside the water pipe, and the refrigerant vapor can be prevented from accumulating at the upper part of the water wall. In addition, local overheating and overconcentration of the upper part of the water wall can be prevented.
第1図及び第2図は本発明の一実施例を示し、第1図は
直焚高温再生器の正面図、第2図は第1図のA−A線縦
断面図である。 (1)……直焚高温再生器、(2)……炉筒、(4)…
…水壁、(11A)……水管群、(13)……バーナ。1 and 2 show an embodiment of the present invention. FIG. 1 is a front view of a direct-fired high-temperature regenerator, and FIG. 2 is a vertical sectional view taken along line AA of FIG. (1) ... direct-fired high-temperature regenerator (2) ... furnace tube (4) ...
... water wall, (11A) ... water tube group, (13) ... burner.
Claims (1)
高温再生器において、周囲に水壁が形成されバーナーの
炎の通路を成す炉筒内に両端の開口が前記水壁につなが
る複数の水管を上下に傾斜させて配置し、前記水管の下
の開口部付近に稀吸収液が供給される入口ヘッダを設け
ると共に前記水管の上の開口付近に冷媒蒸気を分離器へ
導く出口ヘッダを設けることを特徴とする直焚高温再生
器。1. A direct-fired high-temperature regenerator for generating refrigerant vapor by heating an absorbing liquid, wherein water walls are formed around the periphery of the regenerator and openings at both ends are connected to the water wall in a furnace tube forming a passage of a burner flame. A plurality of water pipes are vertically inclined, and an inlet header is provided near the opening below the water pipe to supply a rare absorbing liquid, and an outlet header that guides refrigerant vapor to the separator near the opening above the water pipe. A direct-fired high-temperature regenerator characterized by providing:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1259333A JP2783864B2 (en) | 1989-10-03 | 1989-10-03 | Direct-fired high-temperature regenerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1259333A JP2783864B2 (en) | 1989-10-03 | 1989-10-03 | Direct-fired high-temperature regenerator |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03122467A JPH03122467A (en) | 1991-05-24 |
| JP2783864B2 true JP2783864B2 (en) | 1998-08-06 |
Family
ID=17332644
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1259333A Expired - Fee Related JP2783864B2 (en) | 1989-10-03 | 1989-10-03 | Direct-fired high-temperature regenerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2783864B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2958263B2 (en) * | 1995-10-19 | 1999-10-06 | 株式会社荏原製作所 | High temperature regenerator |
| CN1277667A (en) * | 1998-09-24 | 2000-12-20 | 大阪瓦斯株式会社 | Regenerator for ammonia absorbing refrigerating machine |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS3511402Y1 (en) * | 1958-07-23 | 1960-05-26 | ||
| JPS51126401A (en) * | 1975-04-26 | 1976-11-04 | Komatsu Tekkosho:Goushi | Boiler |
| DK139366B (en) * | 1975-11-19 | 1979-02-05 | Aalborg Vaerft As | Water pipe boiler for steam and hot water production. |
-
1989
- 1989-10-03 JP JP1259333A patent/JP2783864B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03122467A (en) | 1991-05-24 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| RU99124764A (en) | DIRECT STEAM GENERATOR AND STARTING METHOD IN ACTION OF THE DIRECT STRAIGHT STEAM GENERATOR | |
| CN118980101B (en) | Wide-runner plate type air preheater with flue gas channel ash removal self-cleaning function | |
| JP5190511B2 (en) | boiler | |
| JP4621930B2 (en) | Oil reverse combustion water heater | |
| JPH119471A (en) | Liquid heating device | |
| JP2783864B2 (en) | Direct-fired high-temperature regenerator | |
| CN212618540U (en) | Oil fume purifier | |
| US3215415A (en) | Gas-liquid contact apparatus | |
| CN116474527A (en) | Multi-stage flue gas absorption system | |
| CN113686164A (en) | A high temperature carbonization furnace flue gas treatment system | |
| JPH0710212Y2 (en) | Direct-fired high temperature regenerator | |
| JPS5840081B2 (en) | Blowdown equipment for steam generators | |
| KR101380369B1 (en) | Boiler with a detachable type heat exchanger pipe | |
| JP2654160B2 (en) | Direct firing generator | |
| JP2018004119A (en) | Latent heat recovery heat exchanger | |
| CN109990266B (en) | A high-temperature denitrification, fly ash re-combustion, and in-furnace dust removal boiler | |
| JPH02187575A (en) | Direct burning generator | |
| KR102940616B1 (en) | Replaceable heating furnace and thermal decomposition apparatus including the same | |
| CN217540791U (en) | Combustion smoke dust removal system | |
| KR102891410B1 (en) | Apparatus for recovering the heat from the waste water | |
| RU2135902C1 (en) | Contact heater | |
| KR102895336B1 (en) | Steam boiler | |
| CN220552110U (en) | Vertical premixed combustion type direct-current hot water boiler | |
| JPH02192558A (en) | Direct firing generator | |
| JPS5864487A (en) | Heat exchange operation with gas containing overheated steam |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| LAPS | Cancellation because of no payment of annual fees |