JPS629294Y2 - - Google Patents
Info
- Publication number
- JPS629294Y2 JPS629294Y2 JP1982191877U JP19187782U JPS629294Y2 JP S629294 Y2 JPS629294 Y2 JP S629294Y2 JP 1982191877 U JP1982191877 U JP 1982191877U JP 19187782 U JP19187782 U JP 19187782U JP S629294 Y2 JPS629294 Y2 JP S629294Y2
- Authority
- JP
- Japan
- Prior art keywords
- heat storage
- flue
- glass melting
- storage chamber
- hollow tubular
- 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
Links
- 238000005338 heat storage Methods 0.000 claims description 17
- 238000002844 melting Methods 0.000 claims description 16
- 230000008018 melting Effects 0.000 claims description 16
- 239000011521 glass Substances 0.000 claims description 13
- 238000011084 recovery Methods 0.000 claims description 2
- 239000007789 gas Substances 0.000 description 12
- 238000002485 combustion reaction Methods 0.000 description 4
- 239000011819 refractory material Substances 0.000 description 4
- 239000000446 fuel Substances 0.000 description 3
- 239000011449 brick Substances 0.000 description 2
- 230000008646 thermal stress Effects 0.000 description 2
- 238000009423 ventilation Methods 0.000 description 2
- 239000000567 combustion gas Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
Classifications
-
- 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
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/14—Thermal energy storage
-
- 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/50—Glass production, e.g. reusing waste heat during processing or shaping
Landscapes
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Glass Melting And Manufacturing (AREA)
Description
【考案の詳細な説明】
本考案は、硝子溶融炉の排熱回収装置の改良に
関するものである。[Detailed Description of the Invention] The present invention relates to an improvement of an exhaust heat recovery device for a glass melting furnace.
現在広く用いられているタンク式の硝子溶融炉
には蓄熱室が設けられており、硝子溶融炉から出
た排ガスの熱エネルギを蓄熱室内部のチエツカー
ブロツクにより回収する構造となつているが、蓄
熱室を出て煙突に送られる排ガスはなお500度〜
600度の温度を有しておりこの排ガスの持つエネ
ルギは無駄に大気中に放出されている欠点があつ
た。 Tank-type glass melting furnaces, which are currently widely used, are equipped with a heat storage chamber, and the structure is such that the thermal energy of the exhaust gas emitted from the glass melting furnace is recovered by a checker block inside the heat storage chamber. The exhaust gas that leaves the heat storage chamber and is sent to the chimney is still at a temperature of 500 degrees or more.
The temperature of the exhaust gas was 600 degrees, and the energy contained in the exhaust gas was wasted and was wasted into the atmosphere.
本考案者はかかる欠点を解決するために、蓄熱
室と煙突の基部に設けられた交換器とを結ぶ煙道
の内部に更に耐火煉瓦を格子状に積み上げること
により排ガスの持つ熱エネルギを回収することを
試みた。しかし既存の硝子溶融炉の煙道内部に耐
火煉瓦を積み上げる作業はその煙道が送風側にあ
る20分程度の短かい時間を利用して行なわねばな
らぬために工事に長期間を要し、また下部の煉瓦
が熱応力等により破損すると全体が崩れ煙道を塞
いで炉の燃焼効率を却つて悪化させるという問題
点があることが分かつた。 In order to solve this problem, the present inventor recovers the thermal energy of the exhaust gas by stacking firebricks in a lattice pattern inside the flue that connects the heat storage chamber and the exchanger installed at the base of the chimney. I tried that. However, the work of stacking refractory bricks inside the flue of an existing glass melting furnace requires a long period of time because the work must be done during a short period of about 20 minutes when the flue is on the ventilation side. It was also found that if the lower bricks were damaged due to thermal stress, the entire structure would collapse and block the flue, which would actually worsen the combustion efficiency of the furnace.
本考案はこのような従来の問題点を解決するた
めになされたものであつて、硝子溶融炉の左右の
蓄熱室と交換器とを結合する煙道の内部に、耐火
物製の中空管状体を多数本積み上げ、蓄熱室を出
た排ガスの有する熱エネルギを回収させることを
特徴とするものである。 The present invention was developed in order to solve these conventional problems.The present invention was developed by installing a hollow tubular body made of refractory material inside the flue that connects the left and right heat storage chambers and the exchanger of the glass melting furnace. This system is characterized by stacking a large number of such gases and recovering the thermal energy of the exhaust gas that exits the heat storage chamber.
以下に本考案を図示の実施例に従つて更に詳細
に説明する。 The present invention will be explained in more detail below with reference to illustrated embodiments.
図面は本考案をサイドポート式の硝子溶融炉に
適用した実施例を示す斜視図であり、1は硝子溶
融炉の溶融部、2はその左右に設けられた蓄熱
室、3は溶融部1と蓄熱室2とを結ぶポート、4
は煙道である。煙道4は蓄熱室2から排出される
排ガスを交換器5を介して煙突6へ導くととも
に、燃焼用空気を蓄熱室2へ送るためのものであ
り、この切り替えが交換器5によつて行なわれる
ことは一般に知られているとおりである。本考案
は左右両側の煙道4の蓄熱室2寄りの部分に耐火
物製の中空管状体7を多数本積み上げたものであ
り、実施例においては中空管状体7として外径
300ミリ、内径250ミリ、長さ900ミリのシヤモツ
ト質耐火物(SK35)を3段に積み上げた。勿
論、煙道の大きさによつて中空管状体の形状、本
数、材質は適宜変更することが可能であり、また
煙道4の長手方向に2〜3列にわたつて積み上げ
ることも可能である。 The drawing is a perspective view showing an embodiment in which the present invention is applied to a side port type glass melting furnace, in which 1 is a melting section of the glass melting furnace, 2 is a heat storage chamber provided on the left and right sides of the melting section, and 3 is a melting section 1 and Port 4 connecting with heat storage chamber 2
is a flue. The flue 4 is for guiding exhaust gas discharged from the heat storage chamber 2 to the chimney 6 via the exchanger 5 and for sending combustion air to the heat storage chamber 2, and this switching is performed by the exchanger 5. It is generally known that In the present invention, a large number of hollow tubular bodies 7 made of refractory material are stacked on the left and right sides of the flue 4 near the heat storage chamber 2, and in the embodiment, the hollow tubular bodies 7 have an outer diameter.
Shamotsu refractories (SK35) with a diameter of 300 mm, an inner diameter of 250 mm, and a length of 900 mm were stacked in three tiers. Of course, the shape, number, and material of the hollow tubular bodies can be changed as appropriate depending on the size of the flue, and it is also possible to stack them in two or three rows in the longitudinal direction of the flue 4. .
このように構成されたものは、交換器5の切り
替えにより排ガス側となつた煙道内部の中空管状
体7が蓄熱室2から排出された500〜600度の排ガ
スにより熱せられて高温となり、次に交換器5が
切り替えられて送風側となつた際に高温の中空管
状体7の内部あるいはその周囲を通過する空気を
予熱することとなる。従つて硝子溶融炉の燃焼ガ
スは蓄熱室2においてチエツカーブロツクを加熱
した後に更に煙道4の内部の中空管状体7を加熱
することとなり、逆に燃焼用空気は中空管状体7
とチエツカーブロツクとによつて二段に予熱され
ることになるので、排ガスの持つ熱エネルギが燃
焼用空気に十分に与えられる。本考案者の測定し
たところによれば本考案の採用により、硝子溶融
炉の燃料消費量は1.5%〜2.5%低下し、これによ
る年間燃料費用の削減額は数百万円に達すること
が確認された。 With this structure, the hollow tubular body 7 inside the flue, which has become the exhaust gas side by switching the exchanger 5, is heated by the exhaust gas of 500 to 600 degrees discharged from the heat storage chamber 2 and becomes high temperature. When the exchanger 5 is switched to the ventilation side, the air passing inside or around the high temperature hollow tubular body 7 is preheated. Therefore, the combustion gas from the glass melting furnace heats the checker block in the heat storage chamber 2 and then further heats the hollow tubular body 7 inside the flue 4, and conversely, the combustion air heats the hollow tubular body 7.
Since the exhaust gas is preheated in two stages by the checker block and the checker block, sufficient thermal energy of the exhaust gas is given to the combustion air. According to the inventor's measurements, by adopting this invention, the fuel consumption of glass melting furnaces has been reduced by 1.5% to 2.5%, and it has been confirmed that the annual fuel cost reduction due to this will reach several million yen. It was done.
以上に説明したように、本考案は硝子溶融炉の
左右の蓄熱室と交換器とを結合する煙道の内部
に、耐火物製の中空管状体を多数本積み上げ、蓄
熱室を出た排ガスの有する熱エネルギを回収させ
るようにしたものであるから、炉の燃料使用量を
上記のように低下させることができ、また従来の
耐火煉瓦を積み上げる方式とは異なり設置および
取外しが短時間にできるので工事が簡単であつて
既存の硝子溶融炉に容易に適用することができる
利点がある。更に本考案は中空管状体を用いたの
で空気等の流動抵抗が少ないうえ、下部の中空管
状体が熱応力により破損して崩れるようなことが
あつても、その他の中空管状体が自然にその欠落
部分を埋めるので全体の機能にほとんど影響を生
じない利点もある。 As explained above, the present invention stacks a large number of hollow tubular bodies made of refractory material inside the flue that connects the left and right heat storage chambers and the exchanger of a glass melting furnace. Because it is designed to recover the thermal energy it possesses, it is possible to reduce the amount of fuel used in the furnace as mentioned above, and unlike the conventional method of stacking firebricks, it can be installed and removed in a short time. It has the advantage that construction is simple and it can be easily applied to existing glass melting furnaces. Furthermore, since the present invention uses a hollow tubular body, there is little resistance to the flow of air, etc., and even if the lower hollow tubular body breaks and collapses due to thermal stress, other hollow tubular bodies will naturally collapse. Since it fills in the missing parts, it has the advantage of having little effect on the overall functionality.
このように本考案は従来の問題点をよく解決し
たものであつて、その実用的価値は極めて大きい
ものがある。 As described above, the present invention satisfactorily solves the conventional problems and has extremely great practical value.
図面は本考案の実施例を示すもので、煙道の一
部を切り欠いた状態の斜視図である。
2……蓄熱室、4……煙道、5……交換器、7
……中空管状体。
The drawing shows an embodiment of the present invention, and is a perspective view with a part of the flue cut away. 2... Heat storage chamber, 4... Flue, 5... Exchanger, 7
...Hollow tubular body.
Claims (1)
合する煙道4の内部に、耐火物製の中空管状体7
を多数本積み上げ、蓄熱室2を出た排ガスの有す
る熱エネルギを回収させることを特徴とする硝子
溶融炉の排熱回収装置。 A hollow tubular body 7 made of refractory is installed inside the flue 4 that connects the left and right heat storage chambers 2 and the exchanger 5 of the glass melting furnace.
An exhaust heat recovery device for a glass melting furnace, characterized in that a large number of these are piled up and the thermal energy of the exhaust gas exiting the heat storage chamber 2 is recovered.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1982191877U JPS5995131U (en) | 1982-12-17 | 1982-12-17 | Glass melting furnace waste heat recovery device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1982191877U JPS5995131U (en) | 1982-12-17 | 1982-12-17 | Glass melting furnace waste heat recovery device |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5995131U JPS5995131U (en) | 1984-06-28 |
JPS629294Y2 true JPS629294Y2 (en) | 1987-03-04 |
Family
ID=30413084
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1982191877U Granted JPS5995131U (en) | 1982-12-17 | 1982-12-17 | Glass melting furnace waste heat recovery device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5995131U (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP6720718B2 (en) * | 2016-06-20 | 2020-07-08 | 日本電気硝子株式会社 | Glass raw material melting apparatus and method for manufacturing molten glass |
-
1982
- 1982-12-17 JP JP1982191877U patent/JPS5995131U/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS5995131U (en) | 1984-06-28 |
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