JPH0227282Y2 - - Google Patents
Info
- Publication number
- JPH0227282Y2 JPH0227282Y2 JP1982151522U JP15152282U JPH0227282Y2 JP H0227282 Y2 JPH0227282 Y2 JP H0227282Y2 JP 1982151522 U JP1982151522 U JP 1982151522U JP 15152282 U JP15152282 U JP 15152282U JP H0227282 Y2 JPH0227282 Y2 JP H0227282Y2
- Authority
- JP
- Japan
- Prior art keywords
- pressure
- low
- economizer
- water
- water supply
- 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.)
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- Control Of Steam Boilers And Waste-Gas Boilers (AREA)
Description
【考案の詳細な説明】
本考案は自然循環式排熱回収ボイラに係り、特
に節炭器の低温腐食を防止するのに好適なボイラ
装置に関する。[Detailed Description of the Invention] The present invention relates to a natural circulation type exhaust heat recovery boiler, and particularly to a boiler device suitable for preventing low-temperature corrosion of a economizer.
自然循環式排熱回収ボイラは、第1図に示すよ
うに煙道内に排ガスの下流側より上流側に低圧節
炭器6、低圧蒸発器、高圧節炭器8、高圧蒸発器
9、及び過熱器10が順次設置されており、図中
Wで示す給水は低圧給水ポンプ3を介して、低圧
節炭器6に供給され、ここで予熱された給水は低
圧給水調整弁12を介して、低圧ドラム1に供給
される。 As shown in Figure 1, the natural circulation type waste heat recovery boiler has a low pressure economizer 6, a low pressure evaporator, a high pressure economizer 8, a high pressure evaporator 9, and a superheater installed in the flue from the downstream side to the upstream side of the exhaust gas. The water supply indicated by W in the figure is supplied to the low-pressure economizer 6 via the low-pressure water supply pump 3, and the water preheated here is supplied to the low-pressure energy saver 6 via the low-pressure water supply regulating valve is supplied to the drum 1.
一方、低圧節炭器6からの予熱給水の一部は高
圧給水ポンプ4を介して、高圧節炭器8に供給さ
れる。また、高圧節炭器8で加熱された給水は高
圧給水調整弁13を介して高圧ドラム2に供給さ
れる。 On the other hand, a portion of the preheated water from the low-pressure economizer 6 is supplied to the high-pressure economizer 8 via the high-pressure water pump 4 . Further, the water supply heated by the high-pressure economizer 8 is supplied to the high-pressure drum 2 via the high-pressure water supply adjustment valve 13.
また、低圧ドラム1内のドラム水は低圧蒸発器
7を介して自然循環しており、低圧ドラム1で発
生した低圧蒸気は、低圧タービン(図示せず)に
供給される。また、高圧ドラム2内のドラム水は
高圧蒸発器9を介して自然循環しており、高圧ド
ラム2で発生した蒸気は過熱器10で過熱され、
この過熱蒸気となつて高圧タービン(図示せず)
に供給される。 Further, the drum water in the low pressure drum 1 is naturally circulated via the low pressure evaporator 7, and the low pressure steam generated in the low pressure drum 1 is supplied to a low pressure turbine (not shown). Further, the drum water in the high pressure drum 2 is naturally circulated via the high pressure evaporator 9, and the steam generated in the high pressure drum 2 is superheated in the superheater 10.
This superheated steam is turned into a high-pressure turbine (not shown)
is supplied to
このような脱気器を設置しない自然循環排熱回
収ボイラのシステムの場合、低圧節炭器6に供給
される給水の温度が低いため、低圧節炭器6のガ
ス出口側で排ガスの温度が冷え過ぎ、低圧節炭器
6のチユーブ外表面で排ガス内の水蒸気が結露
し、低圧節炭器6のチユーブ外表面が腐食され
る、所謂、低温腐食の問題が生じる。 In the case of such a natural circulation heat recovery boiler system without a deaerator installed, the temperature of the feed water supplied to the low pressure economizer 6 is low, so the temperature of the exhaust gas at the gas outlet side of the low pressure economizer 6 is low. If it gets too cold, water vapor in the exhaust gas will condense on the outer surface of the tube of the low-pressure economizer 6, causing corrosion of the outer surface of the tube of the low-pressure economizer 6, a problem called low-temperature corrosion.
従来、このような節炭器チユーブ外表面におけ
る低温腐食の問題に対し、特に対策が採られてお
らず、適切な対応策が要望されていた。 Conventionally, no particular measures have been taken to deal with the problem of low-temperature corrosion on the outer surface of the economizer tube, and appropriate countermeasures have been desired.
本考案の目的は、上記した要望に対応するもの
であつて、節炭器のチユーブ外表面における低温
腐食を解消することができる自然循環式排熱回収
ボイラを提供することにある。 An object of the present invention is to provide a natural circulation type waste heat recovery boiler that meets the above-mentioned demands and can eliminate low-temperature corrosion on the outer surface of the tube of the economizer.
要するに本考案は、自然循環式排熱回収ボイラ
における節炭器からドラムへの給水ラインから分
岐したバイパスラインを設け、このバイパスライ
ンにおける給水の熱エネルギーを節炭器に供給さ
れる給水の加温に利用する手段を備えた給水予熱
装置を設けることによつて達成される。 In short, the present invention provides a bypass line that branches off from the water supply line from the economizer to the drum in a natural circulation waste heat recovery boiler, and uses the thermal energy of the feed water in this bypass line to heat the water supplied to the economizer. This is accomplished by providing a feed water preheating device with means for
以下、本考案の実施例を図面に基づいて説明す
る。 Hereinafter, embodiments of the present invention will be described based on the drawings.
第2図〜第4図は本考案の実施例を示し、第1
図と同一構成部分は同一符号で示している。 Figures 2 to 4 show embodiments of the present invention;
Components that are the same as those in the figures are indicated by the same reference numerals.
第2図において、第1図に示す従来の自然循環
式排熱回収ボイラとの相違点は、低圧節炭器6か
ら高圧給水ポンプ4に至るまでのラインから分岐
し、低圧給水ポンプ3の上流側に至るバイパスラ
インを設け、このバイパスラインに低圧節炭器再
循環調整弁14を介設し、低圧給水ポンプ3の入
口への循環系統を設けたものである。 In FIG. 2, the difference from the conventional natural circulation type waste heat recovery boiler shown in FIG. A bypass line extending to the side is provided, a low pressure economizer recirculation regulating valve 14 is interposed in this bypass line, and a circulation system to the inlet of the low pressure water supply pump 3 is provided.
この自然循環式排熱回収ボイラにおいては、給
水Wは低圧給水ポンプ3により加圧されて低圧節
炭器6へ流入する。低圧節炭器6で加温された給
水の一部は、低圧給水調整弁12を介して、低圧
ドラム1に給水される。 In this natural circulation type waste heat recovery boiler, the feed water W is pressurized by the low pressure water supply pump 3 and flows into the low pressure economizer 6 . A part of the water supply heated by the low pressure economizer 6 is supplied to the low pressure drum 1 via the low pressure water supply regulating valve 12 .
また、低圧節炭器6で予熱された給水の他の部
分は、高圧給水ポンプ4を介して、高圧節炭器8
に導入される。また、低圧節炭器6からの予熱給
水の一部は低圧節炭器流量調整弁14を介して、
低圧給水ポンプ3の上流側に戻され、低圧給水と
混合され低圧給水が加温されるようになつてい
る。 Further, the other part of the water supply preheated by the low-pressure economizer 6 is transferred to the high-pressure economizer 8 via the high-pressure water supply pump 4.
will be introduced in In addition, a part of the preheated water from the low-pressure economizer 6 is supplied via the low-pressure economizer flow rate adjustment valve 14.
The water is returned to the upstream side of the low-pressure water supply pump 3, mixed with the low-pressure water supply, and the low-pressure water supply is heated.
この実施例の場合、低圧節炭器6の給水循環は
比較的吐出圧力の低い低圧給水ポンプ3の吐出圧
力により行われ、特別な専用ポンプを設けること
なく給水温度を上昇させて、低圧節炭器6のチユ
ーブ外表面の低温腐食を解消することができる。 In the case of this embodiment, the water supply circulation of the low-pressure energy saver 6 is performed by the discharge pressure of the low-pressure water supply pump 3, which has a relatively low discharge pressure, and the temperature of the water supply is increased without providing a special dedicated pump. Low-temperature corrosion on the outer surface of the tube of the vessel 6 can be eliminated.
第3図は本考案の自然循環式排熱回収ボイラに
おける要部系統図であり、第3図に図示した以外
の構成部分は第2図と同様である。 FIG. 3 is a system diagram of main parts of the natural circulation type waste heat recovery boiler of the present invention, and the constituent parts other than those shown in FIG. 3 are the same as those in FIG. 2.
この自然循環式排熱回収ボイラにおいては、高
圧給水ポンプ4の中間段より最適な圧力の温水を
抽水し、低圧節炭器再循環調整弁14を介設した
バイパスラインは、低圧給水ポンプ3の下流側
(出口側)に接続されている。この自然循環式排
熱回収ボイラにおいては、低圧節炭器再循環のた
めに専用のポンプを設置することなく、低圧節炭
器6を出て高圧給水ポンプ4により加圧された中
間段階の最も適合する圧力において抽水し、低圧
給水ポンプ6の出口側に還流させるものであるか
ら、高圧給水ポンプ4における軸動力の消費がな
く、給水を加温することにより低圧節炭器6のチ
ユーブ外表面の低温腐食を防止することができ
る。 In this natural circulation type waste heat recovery boiler, hot water at an optimal pressure is extracted from the intermediate stage of the high-pressure feed water pump 4, and a bypass line with a low-pressure economizer recirculation adjustment valve 14 is connected to the low-pressure feed water pump 3. Connected to the downstream side (outlet side). In this natural circulation type waste heat recovery boiler, there is no need to install a dedicated pump for recirculating the low-pressure economizer, and the intermediate stage where water exits the low-pressure economizer 6 and is pressurized by the high-pressure feed pump 4 is used. Since water is extracted at a suitable pressure and returned to the outlet side of the low-pressure water supply pump 6, there is no consumption of shaft power in the high-pressure water supply pump 4, and by heating the water supply, the outer surface of the tube of the low-pressure energy saver 6 is reduced. can prevent low-temperature corrosion.
第4図は本考案の自然循環式排熱回収ボイラに
おける要部系統図であり、図示していない構成部
分は第2図における実施例と同様である。 FIG. 4 is a system diagram of the main parts of the natural circulation type waste heat recovery boiler of the present invention, and the components not shown are the same as the embodiment shown in FIG. 2.
第4図においては低圧節炭器6から高圧給水ポ
ンプ4に至る給水ラインを低圧給水ポンプ3から
低圧節炭器6に至る給水ラインの途中に設けた給
水予熱器15内に設け、この給水予熱器15にお
いて低圧給水ポンプ3から供給される給水を予熱
するようになつている。 In FIG. 4, the water supply line from the low-pressure water economizer 6 to the high-pressure water supply pump 4 is installed in a water supply preheater 15 provided in the middle of the water supply line from the low-pressure water supply pump 3 to the low-pressure water economizer 6, and this water supply preheating is performed. The water supplied from the low-pressure water pump 3 is preheated in the container 15.
この実施例の場合においては、給水予熱器15
の予熱能力を適当に設計値として選択することに
よつて給水Wを加温し、低温腐食を防止すること
ができる。この場合、低圧節炭器6から高圧給水
ポンプ4に至る全流量の給水が低圧節炭器6に供
給される給水の予熱に寄与するシステムとなつて
いる。 In the case of this embodiment, the feed water preheater 15
By appropriately selecting the preheating capacity of W as a design value, it is possible to warm the feed water W and prevent low-temperature corrosion. In this case, the system is such that the entire flow of water from the low-pressure economizer 6 to the high-pressure water pump 4 contributes to preheating the water supplied to the low-pressure economizer 6.
上記した実施例においては、低圧節炭器6への
再循環のための専用のポンプを設置する必要がな
く、また高圧給水ポンプ4により高圧に加圧され
た温水を減圧して再循環させることにより、高圧
給水ポンプ4の不要な軸動力を消費させることも
なく、低圧節炭器6に給水される給水を加温して
低温腐食を防止することができる。 In the embodiment described above, there is no need to install a dedicated pump for recirculating the water to the low-pressure economizer 6, and the hot water pressurized to a high pressure by the high-pressure water supply pump 4 can be depressurized and recirculated. Therefore, the water supplied to the low-pressure economizer 6 can be heated and low-temperature corrosion can be prevented without consuming unnecessary shaft power of the high-pressure water supply pump 4.
上記した実施例においては、低圧節炭器6及び
低圧蒸発器7と共に高圧節炭器8と高圧蒸発器9
とを備えた自然循環式排熱回収ボイラの例を示し
たが、本考案は低圧及び高圧のそれぞれの節炭器
及び蒸発器を設置したボイラに限定されるもので
なく、単独の節炭器及び蒸発器とを備え、このド
ラムと蒸発器との間を自然循環によりドラム水を
循環させる方式のボイラにも適用することができ
る。 In the embodiment described above, in addition to the low-pressure economizer 6 and the low-pressure evaporator 7, the high-pressure economizer 8 and the high-pressure evaporator 9 are
Although an example of a natural circulation heat recovery boiler equipped with The present invention can also be applied to a boiler that includes a drum and an evaporator and circulates drum water between the drum and the evaporator by natural circulation.
以上のように、本考案によれば節炭器に供給さ
れる給水が所定の温度に加温されるために、節炭
器のガス出口側の排ガス温度が必要以上に冷え過
ぎることがなく、節炭器チユーブ外表面での排ガ
ス内の水蒸気の結露が解消され、節炭器チユーブ
外表面が腐食される、所謂、低温腐食を防止する
ことができる。
As described above, according to the present invention, the water supplied to the economizer is heated to a predetermined temperature, so that the temperature of the exhaust gas on the gas outlet side of the economizer does not become too cold. Condensation of water vapor in the exhaust gas on the outer surface of the economizer tube is eliminated, and so-called low-temperature corrosion in which the outer surface of the economizer tube corrodes can be prevented.
第1図は従来の自然循環式排熱回収ボイラの系
統図、第2図は本考案の自然循環式排熱回収ボイ
ラの一実施例を示す系統図、第3図は本考案の自
然循環式排熱回収ボイラの他の実施例を示す系統
図、第4図は本考案の更に他の実施例を示す系統
図である。
1……低圧ドラム、2……高圧ドラム、3……
低圧給水ポンプ、4……高圧給水ポンプ、6……
低圧節炭器、7……低圧蒸発器、8……高圧節炭
器、9……高圧蒸発器、10……過熱器、12…
…低圧給水調整弁、13……高圧給水調整弁、1
4……低圧節炭器再循環調整弁、15……給水予
熱器。
Figure 1 is a system diagram of a conventional natural circulation type waste heat recovery boiler, Figure 2 is a system diagram showing an embodiment of the natural circulation type exhaust heat recovery boiler of the present invention, and Figure 3 is a system diagram of the natural circulation type of the present invention. FIG. 4 is a system diagram showing another embodiment of the exhaust heat recovery boiler. FIG. 4 is a system diagram showing still another embodiment of the present invention. 1...Low pressure drum, 2...High pressure drum, 3...
Low pressure water supply pump, 4... High pressure water supply pump, 6...
Low pressure energy saver, 7...Low pressure evaporator, 8...High pressure energy saver, 9...High pressure evaporator, 10...Superheater, 12...
...Low pressure water supply adjustment valve, 13...High pressure water supply adjustment valve, 1
4...Low pressure economizer recirculation regulating valve, 15...Water preheater.
Claims (1)
されるドラムと、このドラムのボイラ水が自然循
環により前記ドラムと前記蒸発器との間を循環す
る自然循環式排熱回収ボイラにおいて、前記節炭
器からドラムへの給水ラインから分岐したバイパ
スラインを設け、このバイパスラインにおける給
水の熱エネルギを前記節炭器に供給される給水の
加温に利用する手段を備えた給水予熱装置を設け
たことを特徴とする自然循環式排熱回収ボイラ。 A natural circulation waste heat recovery boiler in which a fuel economizer, a drum to which feed water preheated by the energy saver is supplied, and boiler water in the drum circulates between the drum and the evaporator by natural circulation, A feed water preheating device comprising: a bypass line branched from the water supply line from the economizer to the drum; and a means for using the thermal energy of the feed water in the bypass line to heat the water supplied to the economizer. Natural circulation type exhaust heat recovery boiler.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15152282U JPS5959607U (en) | 1982-10-07 | 1982-10-07 | Natural circulation type waste heat recovery boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP15152282U JPS5959607U (en) | 1982-10-07 | 1982-10-07 | Natural circulation type waste heat recovery boiler |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5959607U JPS5959607U (en) | 1984-04-18 |
| JPH0227282Y2 true JPH0227282Y2 (en) | 1990-07-24 |
Family
ID=30335744
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP15152282U Granted JPS5959607U (en) | 1982-10-07 | 1982-10-07 | Natural circulation type waste heat recovery boiler |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5959607U (en) |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS54142701U (en) * | 1978-03-28 | 1979-10-03 | ||
| JPS56144901U (en) * | 1980-03-26 | 1981-10-31 |
-
1982
- 1982-10-07 JP JP15152282U patent/JPS5959607U/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5959607U (en) | 1984-04-18 |
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