TW546454B - Heat exchange tube and heat recovery method using the same - Google Patents
Heat exchange tube and heat recovery method using the same Download PDFInfo
- Publication number
- TW546454B TW546454B TW089116086A TW89116086A TW546454B TW 546454 B TW546454 B TW 546454B TW 089116086 A TW089116086 A TW 089116086A TW 89116086 A TW89116086 A TW 89116086A TW 546454 B TW546454 B TW 546454B
- Authority
- TW
- Taiwan
- Prior art keywords
- heat exchange
- exchange tube
- heat
- tube
- composite material
- Prior art date
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F21/00—Constructions of heat-exchange apparatus characterised by the selection of particular materials
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D21/0001—Recuperative heat exchangers
- F28D21/0003—Recuperative heat exchangers the heat being recuperated from exhaust gases
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F19/00—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
- F28F19/02—Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using coatings, e.g. vitreous or enamel coatings
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F21/00—Constructions of heat-exchange apparatus characterised by the selection of particular materials
- F28F21/04—Constructions of heat-exchange apparatus characterised by the selection of particular materials of ceramic; of concrete; of natural stone
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F2255/00—Heat exchanger elements made of materials having special features or resulting from particular manufacturing processes
- F28F2255/18—Heat exchanger elements made of materials having special features or resulting from particular manufacturing processes sintered
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Laminated Bodies (AREA)
- Rigid Pipes And Flexible Pipes (AREA)
Abstract
Description
546454 五、發明說明(1) [發明之詳細說明] [技術領域] 本發明係關於一種從燃燒都市垃圾及產業廢棄物等時所 發生之高溫之排氣,藉水蒸氣及空氣等而熱回收之方法 者。 [背景技術] 現時,從在燃燒都市垃圾,煤,下水道污泥,製紙淤 渣,其他之產業廢棄物等時所發生之攝氏40 0- 1 20 0度之排 氣中,使用有水蒸氣及空氣等之被加熱流體流通之熱交換 管來實行熱回收,有效地利用於發電等之熱回收系統被實 用化。 ' 然而,當燃燒都市垃圾及產業廢棄物等時所發生之排氣 中含有愈高溫時其腐蝕性變愈強的氯化氫及NaC1,κπ, NajO4 ’等之鹹性鹽等的關係,鍋爐用炭鋼•合金鋼,不 銹鋼,Ni-Co合金等之耐熱合金所成之熱交換管為不能在 高溫下使用,熱交換管内流通之被加熱 曰=利更高,見,在如 交換器,又在日本專利申言主聿報有提儀陶竟製之熱 中有提議用陶兗皮膜被覆:述=所2744() 1號公報 之外表面之熱交換管。 ί ”、、口金所成之熱交換管 陶=面= 竟下時,.堆積在 峨r皿之氣灰之堆積層與陶£之熱膨脹率 89116086.ptd 第 546454 五、發明說明(2) 差及耐熱合金與 ^〜 發生龜裂及剝^ &^脹率差所致之熱伸缩ft # ,飛灰之堆積層變 :::間而“的熱回收 是546454 V. Description of the invention (1) [Detailed description of the invention] [Technical field] The present invention relates to a kind of high-temperature exhaust gas generated from burning urban garbage and industrial waste, and the heat is recovered by water vapor and air. Method. [Background Art] At present, water vapor and exhaust gas at a temperature of 40 to 120 degrees Celsius are used when burning urban garbage, coal, sewage sludge, paper sludge, and other industrial waste. Heat recovery tubes that circulate heated fluid, such as air, perform heat recovery, and a heat recovery system that is effectively used for power generation is used. 'However, the exhaust gas generated when burning municipal waste, industrial waste, etc. contains the relationship between hydrogen chloride, which is more corrosive and salty salts such as NaC1, κπ, NajO4, etc., at higher temperatures. Carbon for boilers Heat exchange tubes made of heat-resistant alloys such as steels, alloy steels, stainless steels, and Ni-Co alloys cannot be used at high temperatures, and the heat exchange tubes flowing through them are heated = higher, see, for example, in exchangers, and in The main claim of the Japanese patent application is that the heat produced by the pottery pottery has been proposed to be covered with a pottery pottery film: narrative = heat exchange tube on the outer surface of the No. 2744 () Gazette. The heat exchange tube pottery made of gold and copper = surface = when it is actually lowered. The stacking layer of gas ash and pottery that are deposited in the Er dish is the thermal expansion rate of 89116086.ptd Article 546454 5. Description of the invention (2) Poor And heat-resistant alloy and ^ ~ cracking and peeling ^ & ^ thermal expansion and contraction caused by the difference in expansion rate ft #, fly ash accumulation layer change :::
低。 厚#熱率降低而導致熱交換率之Jlow. Thick #The heat rate is reduced and the heat exchange rate is J
[發明之揭示] 本發明之目的,在 時間實行穩定的熱回收埶二,f高溫腐蝕環境下也可 回收方法者。 ‘、、、父換管及使用該熱交換管之^ 該目的係可由I Λ 體所成之熱交換管或其^之礼孔率之金屬及陶曼之燒結 所成之熱交換管所達^ ^ f σ為由陶瓷與金屬之複合材料 尤其是’用陶瓷鱼今 卜 基底之耐熱合金管主復口材料形成表層部時,成為 非接合狀態覆蓋, 1面為由陶瓷與金屬之複合材料以 面至少在一部分接g 〇金官與該複合材料係在其界 為由熱膨脹緩衝材蛊^ 換官,或耐熱合金管之外表面 狀熊覆蓋,且:陶瓷與金屬之複合材料依次以非接合 〜、復 且4耐熱合金管盥該埶膨勝縫偷奸;5 $兮 熱膨脹缓衝材與該遂人^ 1熱膨脹緩衝材及/或戎 觸之熱交換管為適合隹-界面至4 #刀接 [實施發明之最佳形心長%間可穩定地使用之° 本申請者為從防+ I γ 觀點來檢討在高溫腐==堆積及防止陶兗本身之破裂之 盆钍耍,Μ 腐钱¥丨兄下可長時間使用之熱交換管。 y之《 "孔率之八於s防止飛灰之堆積則明白如果使用具有2-60 0 ” 、孟屬及陶瓷之燒結體所成之熱交換管時,則 89116086.ptd 第6頁 546454 五、發明說明(3) 可使在熱交換管 出’可防止含有 2-60%之原因為 環境下製造而製 的排氣為從氣孔 又’關於被加熱 熱父換管内流通 周圍環境氣體之 使用陶瓷與金 換管時,由陶瓷 可改善陶瓷本身 破裂之熱交換管 另一方面,關 使用以陶瓷與金 可 0 内流通之被加熱流體之一部分從氣孔喷 喊性鹽之飛灰之堆積。該時設定氣孔率為 如果在2%以上時不必在特別之高溫高壓 造成本較低廉;超過6〇%時則有腐蝕性強 浸透而會使熱交換管本身變質的理由。 流體之一部分從氣孔噴出之方法為,使在 之被加熱流體之壓力高於熱交換管外側之 壓力則可。 屬之複合材料製造該由燒結體所成之熱交 而可維持優良之耐钱性之同時,由金屬而 之脆弱性’可成為其耐蝕性優良而不容易 者。 於防止陶瓷本身之破裂,以上述之理由, 屬之複合材料形成其表層部之熱交換管則 關於上述之複合材料中之陶瓷為,可使用如Ti〇2,Zr〇p[Disclosure of the invention] The object of the present invention is to perform stable heat recovery in time, and to recover the method even in a high-temperature corrosion environment. ',,, parent tube replacement and the use of the heat exchange tube ^ This purpose can be achieved by a heat exchange tube made of I Λ body or a metal with a porosity of ^ and a heat exchange tube made by sintering of Taumann ^ ^ f σ is a composite material made of ceramic and metal, especially when the surface layer is formed of the main mouth and mouth material of a heat-resistant alloy tube based on ceramic fish and steel substrate. The surface is connected to at least a portion of the surface. The gold material and the composite material are bounded by a thermal expansion buffer material, or covered by a surface bear outside the heat-resistant alloy tube, and the composite material of ceramic and metal is Join ~, compound, and 4 heat-resistant alloy tubes to wash the swells; $ 1 thermal expansion buffer material and the ^ 1 thermal expansion buffer material and / or heat exchange tube is suitable for 隹 -interface to 4 # 刀 接 [The best centroid length% in which the invention is implemented can be used steadily between °° The applicant is reviewing the high temperature rot == accumulation from the viewpoint of preventing + I γ and preventing the potting of the pottery itself from breaking, Μ Corrupted money ¥ 丨 The heat exchange tube that can be used for a long time. "The eighth porosity of s prevents the accumulation of fly ash. Then understand that if you use a heat exchange tube made of sintered body with 2-60 0", Mons and ceramics, then 89116086.ptd page 6 546454 V. Description of the invention (3) The heat exchange tube can be prevented from containing 2-60% of the exhaust gas produced for the environment. The exhaust gas is made from the pores. When using ceramic and gold to replace the tube, ceramic can improve the heat exchange tube of the ceramic itself. On the other hand, it is necessary to use a part of the heated fluid circulating in the ceramic and the metal to spray the accumulation of fly ash from the pores. At this time, if the porosity is set above 2%, it is not necessary to cause low cost at a special high temperature and pressure; if it exceeds 60%, there is a reason for strong corrosive penetration and the heat exchange tube itself will deteriorate. Part of the fluid is from The method of blowout is to make the pressure of the heated fluid higher than the pressure of the outside of the heat exchange tube. The composite material is made of the sintered body and can maintain excellent money resistance while maintaining excellent money resistance. Yukin The fragility can make it difficult to be excellent in corrosion resistance. In order to prevent the ceramic itself from cracking, for the reasons mentioned above, the heat exchange tubes of which the composite material forms its surface layer, the ceramics in the above composite materials are Can be used such as Ti〇2, Zr〇p
Cr2 03’ Al2〇3,Si02,Y2〇3,Ce02,Sc2 03 等之氧化物,如BN, MgB2,CaB6,TiB2,ZrB2,A1B2 等之硼化物,如b4c,TiC, ZrC,Cr3C2,A14C3,SiC 等之碳化物,A1N,TiN,ZrN,Cr2 03 'Al2O3, Si02, Y2O3, Ce02, Sc2 03 and other oxides, such as BN, MgB2, CaB6, TiB2, ZrB2, A1B2 and other borides, such as b4c, TiC, ZrC, Cr3C2, A14C3, Carbides such as SiC, A1N, TiN, ZrN,
CqN,SiA等之氮化物,A1〇N*Si2N2〇等之氮氧化物,或 該等之混合物者。 又」關於複合材料中之金屬為,可使用任何金屬,但使 用其^熱性優良,成本方面也有利的A1,A1-Si合金,Nitrogen compounds such as CqN, SiA, etc., Nitrogen oxides such as A10N * Si2N2〇, or a mixture of these. Regarding the metal in the composite material, any metal can be used, but it uses A1, A1-Si alloy which is excellent in heat resistance and advantageous in cost.
Al-Mg合金等為宜。Al-Mg alloy and the like are preferable.
89116086.ptd 第7頁 546454 五、發明說明(4) ""~— 尤其是複合材料中含有A1時,關於陶瓷則含有其耐熱耐 衝擊性優良,不容易附著飛灰之A 1 N為更加理想。製造'' 上’因僅僅把A1在\氣體周圍環境中予以熱處理則可^巧 便。然而’在尚溫腐#環境下欲抑制腐餘及龜裂之發生 時,需要使Α1Ν為l-90wt°/。,且使(Α1+Α1Ν)為50wt%以上。 對4由A1及A1N所成之複合材料再加陶竞之aiqn時,更 不容易使飛灰附著。但該時,需要使A1N為卜9〇wt%,且使 (A1+A1N + A10N)為 50wt% 以上。在此所謂 A10N 係指 A1,〇,N 之固液體之總稱,表示A1u〇16N, A10N, A 1 198 0288 H4, Α“7〇39Ν,Al10O3N8,A 19 03 N7, SiAl7〇2N7,Si3Al3 045 N5 等。 在該陶瓷與金屬之複合材料之表面上,將BN,等之 含有B(硼)之化合物及Sic,黑鉛等之含有〇(碳)之4化合物 予以塗敷或次潰而存在例如1 — 4 〇 〇 # m之厚度時,大致上 可以元全防止飛灰之附著。又,定期地實行上述化合物之 塗敷及浸潰,則可將熱交換管長期而穩定地使用之。 、熱父換管為,用上述之複合材料形成其表層部,用例如 以往之耐熱合金管等形成其内部即可,而該時之複合材 部之厚度為因強度上設定成3 —12mm為宜。 ’ 使用耐熱合金官作為基底,並用上述之複合材料形成表 2 =二用陶竞與金屬之複合材料以非接合之狀態覆蓋耐 二合金管之外表面,則可緩和耐熱合金與複合材料之至少 官軸方向之熱膨脹率之差所致之變形,可更確實地防止複 合材料之龜裂或剝離。又,該耐熱合金管與該複合材料 為在,、界面中至少在一部分接觸的構造時,導熱率不會大89116086.ptd Page 7 546454 V. Explanation of the invention (4) " " ~ — Especially when the composite material contains A1, the ceramic contains excellent heat resistance and impact resistance, and A 1 N which is not easy to adhere to fly ash is More ideal. It is convenient to manufacture 上 上 ’simply by heat-treating A1 in the surrounding environment of gas. However, in the case of “Shang Wen Fu #”, it is necessary to make A1N 1-90wt ° / in order to suppress the occurrence of rot residue and cracking. And let (Α1 + Α1Ν) be 50% by weight or more. Adding aiqn of Tao Jing to the composite material made of A1 and A1N makes it more difficult for the fly ash to adhere. However, in this case, it is necessary to make A1N 90% by weight and (A1 + A1N + A10N) to be 50% by weight or more. The so-called A10N is a general term for solid liquids of A1, 〇, N, which means A1u〇16N, A10N, A 1 198 0288 H4, A "7〇39Ν, Al10O3N8, A 19 03 N7, SiAl7〇2N7, Si3Al3 045 N5 Etc. On the surface of the composite material of ceramic and metal, BN, etc. compounds containing B (boron) and Sic, black lead, etc. containing 4 (carbon) compounds are coated or submerged, for example, such as When the thickness is from 1 to 4 〇〇 # m, the adhesion of fly ash can be prevented substantially. Moreover, if the coating and impregnation of the above compounds are carried out regularly, the heat exchange tube can be used stably for a long time. In the case of a hot parent tube replacement, the surface layer portion is formed by using the above composite material, and the inside thereof may be formed by using a conventional heat-resistant alloy tube, for example. The thickness of the composite material portion at this time is preferably set to 3-12 mm due to strength. . 'Using the heat-resistant alloy official as the base and forming the above-mentioned composite material Table 2 = The second composite material of ceramic and metal is used to cover the outer surface of the second-resistant alloy tube in a non-joined state. Thermal expansion at least in the official axis direction Deformation caused by the difference can be more reliably prevented from cracking or peeling composite materials. In addition, the heat-resistant alloy tube and the composite structure is at least in part upon the contact, not so large in the thermal conductivity of the interface ,,
546454 五、發明說明(5) 大地,低而可以較高之熱 該時之陶瓷與金屬之福人从』丨& 丁…、口收 有l-9〇wt%之A1N與50对%以\材料λ為因如上述之理由,以含 2-60%之氣孔率為宜。 之(Α1+Α1Ν + Α10Ν),又,具有 在耐熱合金管之外表而 時’可使耐熱合金與複厶耔如,述之含有6或。之化合物 上可完全地緩和管軸ί二,之接觸部之滑動順利,大致 又,使用耐熱之差所致之變形。 成表層料,可構成為用上述之複合材料形 該耐熱合金管及該耐熱合金管之外表面,且 該複合材料為,在其界面中至,/或遠熱膨脹緩衝材及 時,以熱膨脹緩衝材而可分接觸之構造。該 致之變形。 叩τ緩和官徑方向之熱膨脹率之差所 J二關膨脹緩衝材,可使用以B,C,^為主成 伤之纖維,粉體m帶子等e 成 因上述之理由,複合;# 5〇w«以上之Ul+A1N + A1#n^係以含有卜90wt%之八…與 宜。又,户J N),並具有2-60%之氣孔率為 為宜。 而…、合金官之外表面為含有B或C之化合物存在 在上述之任何埶交換答+ ^. 破裂,管本身之^产及§考量燒結體及複合材料之 ,外徑為20-200 =〜導”、、4時,其長度設定在以下546454 V. Description of the invention (5) The earth, low and high heat, the blessings of ceramics and metals at that time 『丨 & Ding…, there are 1-9wt% A1N and 50 %% \ Material λ is for the reasons described above, and a porosity of 2-60% is appropriate. (A1 + Α1Ν + Α10Ν), and having a surface outside the heat-resistant alloy tube, ′ can make the heat-resistant alloy and compound, for example, it contains 6 or more. The compound can completely relax the tube shaft, and the contact part slides smoothly, and the deformation caused by the difference in heat resistance is generally used. The surface layer material can be formed by using the above composite material to shape the heat-resistant alloy tube and the outer surface of the heat-resistant alloy tube, and the composite material is, in its interface, and / or a remote thermal expansion buffer material in time, and a thermal expansion buffer material is used. And can be divided into contact structure. Decent deformation.叩 τ alleviates the difference in thermal expansion rate in the direction of the official path. The J Erguan expansion buffer material can use B, C, and ^ as the main cause of wounding fibers, powder m tape, and other e reasons for the above reasons, composite; # 5〇 w «The above Ul + A1N + A1 # n ^ is based on containing 90% by weight of…. Also, it is preferable that the household has a porosity of 2-60%. And ..., the surface of the alloy official is that the compound containing B or C exists in any of the above-mentioned exchanges + ^. Rupture, the production of the tube itself and § Considering sintered bodies and composite materials, the outer diameter is 20-200 = ~ Guide ", and 4, the length is set to the following
, 4f I 4dt _為且。又,其剖面形狀為圓形或角形均 可,並無特別限定。 7 J, 4f I 4dt _ is and. The cross-sectional shape may be circular or angular, and is not particularly limited. 7 J
546454 五、發明說明(6) [實施例1 f ] 具有如圖1所示之縱剖面形狀與微觀結構之陶瓷與金屬 之複合材料1所成之單層構造之熱交換管Νο·1,及具有如 圖2所示之縱剖面形狀,第一層為耐熱合金管2,第二層為 碳纖維3,第三層之表層部為陶瓷與金屬之複合材料1之三 層構造之熱交換管No· 2,及在熱交換管ν〇· 2之外表面塗覆 B N之熱交換管Νο·3設置在都市垃圾焚化爐試驗工廠之攝 氏750-950度之高溫排氣中而實行熱回收。546454 V. Description of the invention (6) [Example 1 f] A single-layer structure heat exchange tube No. · 1 having a ceramic and metal composite material 1 having a longitudinal sectional shape and a microstructure as shown in FIG. 1, and It has a longitudinal cross-sectional shape as shown in FIG. 2, the first layer is a heat-resistant alloy tube 2, the second layer is carbon fiber 3, and the surface layer portion of the third layer is a three-layer structure of a ceramic and metal composite material 1 · 2, and heat exchange tube No. 3 coated with BN on the outer surface of heat exchange tube ν 2 · 3 are installed in the high temperature exhaust gas of 750-950 degrees Celsius in the municipal waste incinerator test plant for heat recovery.
熱交換管No.l,2之明細為如下述。 熱交換管N 〇. 1 陶瓷與金屬之複合材料:A1+A1N + A10N 90wt%以上,厚 度4mm,外徑·· 4 0mm。 奐管No· 2 耐熱合金管:SUS 3 04,厚度4 _,碳纖維:厚度4 _,陶瓷與金屬之複合材料:A1+A1N + A1〇N 90wt%以上, 厚度10 mm,外徑:40 mm。 又’都市垃圾焚化爐試驗工廠之排氣之成份係2_16〇/〇 (vol,dry,以下同樣)之〇2,1〇〇一 5〇〇ppm 之 K1,隨 3〇〇The details of the heat exchange tubes No. 1, 2 are as follows. Heat exchange tube N. 1 Composite material of ceramic and metal: A1 + A1N + A10N 90wt% or more, thickness 4mm, outer diameter · 40mm. Stern tube No. 2 heat-resistant alloy tube: SUS 3 04, thickness 4 _, carbon fiber: thickness 4 _, ceramic and metal composite material: A1 + A1N + A1〇N 90wt% or more, thickness 10 mm, outer diameter: 40 mm . The composition of the exhaust gas from the municipal waste incinerator test plant is 2-16 / 100 (vol, dry, the same below), K1 of 10,000, 5,000 ppm, and
ppm之SOx,5-18%之C02,其餘部分為。關於在熱交換管 内流通之被加熱流體為使用其入口溫度為攝氏丨5 〇 — 4 〇 〇度 之水蒸氣及攝氏120-3 00度之空氣及廢棄物燃燒排氣之混 合氣體。 其結果,確認任一熱交換管之因腐蝕所致之厚度之減少 量僅少’ A沒有發生龜裂,且可以長時間實行穩定之熱回SOx in ppm, C02 in 5-18%, the rest is. Regarding the fluid to be heated in the heat exchange tube, a mixed gas of water vapor with an inlet temperature of 500 ° -400 ° C, air of 120-3 ° C, and waste combustion exhaust gas is used. As a result, it was confirmed that the reduction in thickness of any one of the heat exchange tubes due to corrosion is only small ’A has not cracked, and stable heat recovery can be performed for a long time
546454 五、發明說明(7) 收者。尤其是在其外表面有塗覆βΝ之熱交換管Ν〇· 3中,因 腐餘所致之厚度之減少量為減少至熱交換管肋·丨,2之減 少量之30%以下。 [實施例2 ] 將其橫剖面形狀如圖3所示,具有氣孔4之陶瓷與金屬之 複合材料1所成之單層構造之熱交換管Ν〇. 4,5設置在與實 施例1同樣的設置在都市垃圾焚化爐試驗工廠之攝氏750一 9 5 0度之高溫排氣中,與實施例1同樣的被加熱流體之壓力 設定為高於排氣體環境之壓力,從氣孔喷出被加熱流體之 一部分而實行熱回收。 熱交換管No· 4,5之明細為如下述。 熱交換管No. 4 陶瓷與金屬之複合材料:Al+AIN 90wt%以上,厚度4 _,氣孔率20%,外徑:40 mm。 熱交換管N 〇. 5 陶瓷與金屬之複合材料:A1+A1N 90wt%以上,厚度6 mm,氣孔率60%,外徑:40 mm。 其結果,任何一種熱交換管不會有鹹性鹽之飛灰堆積在 其表面,使用入口溫度在攝氏150-400度之水蒸氣時,可 加熱至出口溫度為攝氏500度,使用入口溫度在攝氏120- 300度,1 00 0-50 0 0mmAq之空氣及1 0 0-400_Aq之廢棄物燃 燒氣之混合氣體時,可加熱至出口溫度成為約攝氏8 〇 〇度 為止,以高度的熱交換率可實行熱回收。 又,氣孔率6 〇 %之熱交換管N 〇 · 5時,被加熱流體之壓力546454 V. Description of Invention (7) Receiver. In particular, in the heat exchange tube NO. 3 whose outer surface is coated with βN, the reduction in thickness due to corrosion is reduced to less than 30% of the heat exchange tube rib. [Embodiment 2] A cross-sectional shape shown in FIG. 3, and a single-layer structure heat exchange tube No. 4, 5 formed of a ceramic and metal composite material 1 having pores 4 was provided in the same manner as in Embodiment 1. The temperature of the heated fluid is set to be higher than the pressure of the exhaust gas environment in the high-temperature exhaust gas at 750 to 950 degrees Celsius set in the municipal waste incinerator test plant. Part of the fluid is subjected to heat recovery. The details of the heat exchange tubes No. 4, 5 are as follows. Heat exchange tube No. 4 Ceramic and metal composite material: Al + AIN 90wt% or more, thickness 4 mm, porosity 20%, outer diameter: 40 mm. Heat exchange tube N 0.5 Ceramic and metal composite material: A1 + A1N 90wt% or more, thickness 6 mm, porosity 60%, outer diameter: 40 mm. As a result, any kind of heat exchange tube does not have salty fly ash deposited on its surface. When the inlet temperature is 150-400 degrees Celsius, it can be heated to an outlet temperature of 500 degrees Celsius. When 120-300 degrees Celsius, 100 0-50 0 0mmAq air and 100-400_Aq waste combustion gas mixed gas, it can be heated until the outlet temperature reaches about 800 degrees Celsius, with a high degree of heat exchange Rate can implement heat recovery. In addition, when the heat exchange tube No. 5 with a porosity of 60%, the pressure of the fluid to be heated
89116086.ptd 第 11 頁 546454 五、發明說明(8) 設定為50 0OmmAq以上時,熱交換管之外表面溫度為較排氣 周圍環境之溫度低攝氏1 0 〇度以上的關係,被加熱流體之 壓力為設定成4000ininAQ左右為宜。 [實施例3 ] 將其縱剖面形狀為如圖4所示,而其橫剖面形狀如圖5所 示,耐熱合金管2之外表面為由陶瓷與金屬之複合材料j以 非接合狀態覆蓋,且耐熱合金管2與複合材料1為,在其界 面中至少一部分接觸,因此具有空隙5之熱交換6一9 ,設置在與實施例1同樣的都市垃圾焚化爐試驗工庵:之攝 氏650 - 950度之高溫排氣中,而實行熱回收。 熱交換管No. 6-9之明細為如下述。 熱交換管No. 6 耐熱合金管:SUS304-1 5A,陶瓷與金屬之複合材料: A1+A1N + A10N 90wt% 以上,厚度5-1 0 mm,氣孔率4〇%。 熱交換管No. 7 耐熱合金管:SUS304-2 0A,陶瓷與金屬之複合材料: A1+A1N + A10N 90wt% 以上,厚度6-8 mm,氣孔率。 熱交換管No. 8 ° 而才熱合金管:SUS304-20A ’外表面BN塗覆,陶-欠 之複合材料:A1+A1N + A10N 9 0 w t %以上,厚声R。” "甸 卞又mm ,氣 孔率20%。 熱交換管No. 9 而才熱合金管:SUS304-20A ’陶瓷與金屬之複合材料· A12 03 80 wt% 以上+ A1,厚度2_4 mm,氣孔率3〇%。,、89116086.ptd Page 11 546454 V. Description of the invention (8) When set to more than 50 0mmAq, the temperature of the outer surface of the heat exchange tube is more than 100 ° C lower than the temperature of the surrounding environment of the exhaust gas. The pressure is preferably set to about 4000 ininAQ. [Example 3] The longitudinal cross-sectional shape is as shown in FIG. 4 and the cross-sectional shape is as shown in FIG. 5. The outer surface of the heat-resistant alloy tube 2 is covered with a composite material j of ceramic and metal in a non-joined state. In addition, the heat-resistant alloy tube 2 and the composite material 1 are in contact with at least a part of the interface. Therefore, the heat exchange 6-9 having the gap 5 is provided in the same test process of the municipal waste incinerator as in Example 1: 650 ° C- 950 degrees of high temperature exhaust, and heat recovery. The details of the heat exchange tubes No. 6-9 are as follows. Heat exchange tube No. 6 heat-resistant alloy tube: SUS304-1 5A, ceramic and metal composite material: A1 + A1N + A10N 90wt% or more, thickness 5-10 mm, porosity 40%. Heat exchange tube No. 7 heat-resistant alloy tube: SUS304-2 0A, ceramic and metal composite materials: A1 + A1N + A10N 90wt% or more, thickness 6-8 mm, porosity. Heat exchange tube No. 8 °, but the hot alloy tube: SUS304-20A ’outer surface is BN coated, ceramic-less composite material: A1 + A1N + A10N 9 0 w t% or more, thick R. "&Quot; Dianmin again mm, porosity 20%. Heat exchange tube No. 9 and thermal alloy tube: SUS304-20A 'ceramic and metal composite material · A12 03 80 wt% or more + A1, thickness 2_4 mm, pores The rate is 30%. ,,
89116086.ptd 第 12 頁 546454 五、發明說明(9) 又,都市垃圾焚化爐試驗工廠之排氣之成份係H 6%之 〇2 ’200-600ppm 之 HC1 ’max 300 ppm 之 s〇x,4-19% 之 C02, 其餘部分為N2。 曰其結果,確認任一熱交換管之因腐蝕所致之厚度之減少 量僅少,也沒有發生龜裂,且可以長時間實行穩定之熱回 ^者。尤其是在其耐熱合金管的外表面有塗覆M之熱交換 官No· 8中,在試驗後之剖面形狀未發生變化,並確認M塗 覆與陶莞與金屬之複合材料之滑動很順利。 又,可確認使用入口溫度在攝氏3〇〇 —4〇〇度之水蒸氣作 為被加熱流體時,在出口可得到攝氏5〇〇度以上,1〇〇 ata 广而使用入口溫度在攝氏12〇一 3〇〇度,1〇〇〇一5〇〇〇_“之空 =10 0~4—之廢棄物燃燒氣之混合氣體作為被加 氛體二’在出σ可加熱至最高 [實施例4] 將其縱剖面形ϋ κ - 為如圖4所示,而其橫剖面形狀如圖5所 非接人妝能涛# 卜表面為由陶瓷與金屬之複合材料1以 ^ φ " h ^ 置,且耐熱合金管2與複合材料1為,在其界 11,肾ί / 觸’因此具有空隙5之熱交換管No. 10, 2 ,,、貝施例1同樣的都市垃圾焚化爐試驗工廠 内,把都市垃扱+ ^、 灰闲同Λ 4分氧化之攝氏700-1 000度之還原排 亂周圍%境内,而實行埶回收。 熱交換管N〇.10,U之明細為如下述。 熱交換_ 1 〇 耐熱。金官.鍋爐用耐熱管STBA28-20A,陶瓷與金屬之89116086.ptd Page 12 546454 V. Description of the invention (9) In addition, the composition of the exhaust gas of the municipal waste incinerator test plant is H 6% 〇2 '200-600ppm HC1' max 300 ppm σx, 4 -19% of C02, the rest is N2. As a result, it has been confirmed that the reduction in thickness of any heat exchange tube due to corrosion is small, no cracking occurs, and stable heat recovery can be performed for a long time. Especially in the heat exchange officer No. 8 with M coating on the outer surface of the heat-resistant alloy tube, the cross-sectional shape did not change after the test, and it was confirmed that the sliding of the M coating and the composite material of ceramics and metal was smooth. . In addition, it can be confirmed that when water vapor having an inlet temperature of 300 to 400 degrees Celsius is used as a heated fluid, an outlet temperature of 500 degrees Celsius or more can be obtained at an outlet temperature of 100 degrees Celsius and an inlet temperature of 120 degrees Celsius is used. 1300 degrees, 10000-50000_ "space = 100 ~ 4-waste gas mixture of mixed gas as the added atmosphere II 'can be heated to the highest [σ] 4] The longitudinal cross-sectional shape ϋ κ-is as shown in FIG. 4, and the cross-sectional shape is as shown in FIG. 5, and the surface is made of a composite material of ceramic and metal 1 with ^ φ " h ^ And the heat-resistant alloy tube 2 and the composite material 1 are, in its boundary 11, the kidney ί / touches the heat exchange tube No. 10, 2, and the same municipal waste incinerator as in Example 1 In the test plant, the reduction of 700-1 000 degrees Celsius of urban waste + ^, gray leisure and Λ 4 minutes oxidation will be arranged in the surrounding% territory, and plutonium recovery will be implemented. The details of the heat exchange tube No.10, U are As follows. Heat exchange_ 1 〇 Heat resistance. Jinguan. Heat-resistant tube STBA28-20A for boilers, ceramics and metals
546454 五、發明說明(ίο) 複合材料:A1+A1N 90 wt%,A 12 03 70 wt%,厚度6-7mm, 氣孔率25%。 熱交換營No. 11 耐熱合金管:鍋爐用耐熱管STB A 28-20A,陶瓷與金屬之 複合材料:SiC 95 wt%以上+ Mg,厚度6-7mm,氣孔率2% 其結果,因高溫排氣係CO濃度為5-15%之還原性氣體周 圍環境的關係,幾乎看不到S i C及A 1N氧化而劣化之現象, 可實行良好之熱回收。 [實施例5 ] 將在圖6及圖7中所示之同軸管形狀及U字管形狀之耐熱 合金管2之外表面為由陶瓷與金屬之複合材料1以非接合狀 態覆蓋,且耐熱合金管2與複合材料1為,在其界面中至少 一部分接觸,因此具有空隙5之熱交換管No. 12-14,設置 於煤,下水道污泥脫水塊狀物及乾燥污泥焚化爐之燃燒氣 中,實行熱回收。 熱交換管Νο·12-14之明細為如下述。 熱交換管No. 12 耐熱合金管:鍋爐用耐熱管STBA28-40A及65A,陶瓷與 金屬之複合材料:SiC 95 wt%以上+ Mg,厚度約為7mm,同 軸管形狀(圖6)。 熱交換管No. 13 耐熱合金管:鍋爐用耐熱管STBA28-20A及50A,陶瓷與 金屬之複合材料:Al2〇3 9 5 wt%以上+ A1,厚度約為3mm, 同軸管形狀(圖6)。546454 5. Description of the invention (ίο) Composite materials: A1 + A1N 90 wt%, A 12 03 70 wt%, thickness 6-7mm, porosity 25%. Heat exchange camp No. 11 heat-resistant alloy tube: boiler heat-resistant tube STB A 28-20A, ceramic and metal composite material: SiC 95 wt% or more + Mg, thickness 6-7mm, porosity 2% The relationship between the surrounding environment of the reducing gas with a CO concentration of 5-15% can hardly see the oxidation and degradation of S i C and A 1N, and good heat recovery can be implemented. [Example 5] The outer surface of the heat-resistant alloy tube 2 of the coaxial tube shape and the U-shaped tube shape shown in Figs. 6 and 7 was covered with a ceramic-metal composite material 1 in a non-joined state, and the heat-resistant alloy The tube 2 and the composite material 1 are heat exchange tubes No. 12 to 14 having at least a part of an interface with the gap 5, and are disposed in coal, sewer sludge dewatering lump, and combustion gas of a dry sludge incinerator. In the implementation of heat recovery. The details of the heat exchange tubes No. 12-14 are as follows. Heat exchange tube No. 12 heat-resistant alloy tube: boiler heat-resistant tubes STBA28-40A and 65A, ceramic and metal composite material: SiC 95 wt% or more + Mg, thickness is about 7mm, the same shape as the shaft tube (Figure 6). Heat exchange tube No. 13 Heat-resistant alloy tube: Heat-resistant tubes STBA28-20A and 50A for boilers, composite materials of ceramics and metals: Al203, 5 wt% or more + A1, thickness about 3mm, coaxial tube shape (Figure 6) .
89116086.ptd 第14頁 54645489116086.ptd Page 14 546454
耐熱合金管:鍋爐用耐熱管STBA28 —15A及2〇A,陶瓷與 金屬之複合材料.A1+A1N 90 wt%以上,厚度β —i〇mm,u 字管形狀(圖7)。 其結果’煤’下水道污泥之燃燒排氣含有數百_之 SOx ’但所有之熱交換管均未被腐钱,可回收到能夠達成 發電效率30%以上之高溫高壓水蒸氣,以及高溫空氣及高 溫燃燒排氣者。 又’形成為如圖7所示之u车;^及/ UL 士 - 子官形狀時,需要在彎曲部存 在更多的空隙5。 [實施例6 ] 將其縱剖面形狀為如圖8所千 二# # - u也人人—〇 , 士 而其橫剖面形狀如圖9所 不’财熱合金管2之外表面為由勒抽 屬之趨人好袓# Α 非拉人马由熱膨脹緩衝材及陶瓷與金 ^複&材枓依:人以非接合狀態覆蓋,且耐熱合金管2盥 熱脉脹緩衝材6及/或熱膨脹緩梅 > /、 H &击η , μ & 铁衝材6與複合材料1為,在 其界面中至少一部分接觸’因此Heat-resistant alloy tube: Heat-resistant tubes STBA28-15A and 20A for boilers, ceramic and metal composite materials. A1 + A1N 90 wt% or more, thickness β-i0mm, u-shaped tube shape (Figure 7). As a result, the combustion exhaust of coal sludge contains hundreds of SOx. But all the heat exchange pipes have not been rotten, and high temperature and high pressure water vapor and high temperature air that can achieve power generation efficiency of more than 30% can be recovered. And those who burn high temperature exhaust. In addition, it is formed into a U-shaped car as shown in FIG. 7; and / UL When a driver-like shape is used, more gaps 5 need to exist in the bent portion. [Embodiment 6] The longitudinal cross-sectional shape is as shown in Figure 8 Thousand ##-u 也 人人 —〇, and the cross-sectional shape is as shown in Figure 9.拔 属 的 向 人 好 袓 # Α The non-raman horse is made of thermal expansion buffer material and ceramic and metal ^ composite & material conversion: the person is covered in a non-joined state, and the heat-resistant alloy tube 2 is used for the thermal pulse expansion buffer material 6 and / or Thermal expansion retardation > /, H & impact η, μ & iron stamping material 6 and composite material 1 are in contact with at least a part of the interface 'therefore
No. 15-18,設置在與實施例1同’工J水之…又換Β 工廠之摄咚r ς n q ς η疮夕- 樣的都市垃圾焚化爐試驗 工:之攝氏650-950度之兩溫排氣 熱交換管No· 15-18之明細為如下述。貝灯…、w收 查L交換營15 " ~、、、口至& · SUS】04 15A ’熱膨脹緩衝材:A1箱,厚 f ’陶£與金屬之複合材料:㈣舰 9〇… 以上’厚度4-l〇mm,氣孔率40%。 16 89116086.ptd 546454 五、發明說明(12) 耐熱合金管:SUS304-20A ’熱膨脹緩衝材:碳纖維, 厚度0.2-2mm,陶瓷與金屬之複合材料:A1+A1N + A10N 90 wt%以上,厚度3-8mm,氣孔率20%。 熱交換管No. 17 耐熱合金管:SUS304-20A,外表面bn塗覆,熱膨脹 緩衝材:碳纖維’厚度0 · 2 _ 2 m m,陶蜜虚今屬之滴人姑斜 :A1+A1N+A1〇N9〇wt% 以上,厚度 3_1/==2口0^ 熱交換管No. 18No. 15-18, set up in the same way as in Example 1 of “Working with water ... and changing the B plant's photo 咚 r ς nq ς η sores-the same kind of municipal waste incinerator tester: 650-950 degrees Celsius The details of the two-temperature exhaust heat exchange tube No. 15-18 are as follows. Bei Deng ..., w check L exchange camp 15 " ~ ,,, 口 至 & · SUS】 04 15A 'Thermal expansion buffer material: A1 box, thick f' Ceramics and metal composite materials: Barge 9〇 ... The above thickness is 4-l0mm, and the porosity is 40%. 16 89116086.ptd 546454 V. Description of the invention (12) Heat-resistant alloy tube: SUS304-20A 'Thermal expansion buffer material: carbon fiber, thickness 0.2-2mm, ceramic and metal composite material: A1 + A1N + A10N 90 wt% or more, thickness 3 -8mm, porosity is 20%. Heat exchange tube No. 17 Heat-resistant alloy tube: SUS304-20A, outer surface coated with bn, thermal expansion buffer material: carbon fiber 'thickness 0 · 2 _ 2 mm, Tao Mi Xing's drop human slash: A1 + A1N + A1 〇N9〇wt% or more, thickness 3_1 / == 2mouth 0 ^ Heat exchange tube No. 18
耐熱合金管:SUS304-20A,熱膨脹緩衝材:碳纖維, 厚度1-2mm,陶瓷與金屬之複合材料·· ai2〇3 8 0 wt%以上 + A1,厚度2-4 mm,氣孔率30%。 又,都市垃圾焚化爐試驗工廠之排氣之成份係2 —丨6%之 〇2,20 0-600ppm 之HC1,max 30 0 ppm 之s〇x,4-19% 之C02 , 其餘部分為。Heat-resistant alloy tube: SUS304-20A, thermal expansion buffer material: carbon fiber, thickness 1-2mm, ceramic and metal composite material · ai203 0 0 wt% or more + A1, thickness 2-4 mm, porosity 30%. In addition, the composition of the exhaust gas from the municipal waste incinerator test plant is 2—6% of 02, 200-600ppm of HC1, max 3000 ppm of SOC, 4-19% of CO2, and the rest is.
其結果,確認任一熱交換管之因腐蝕所致之厚度之減少 量僅少’也沒有發生龜裂,且可以長時間實行穩定之熱回 收者。尤其是在耐熱合金管之外表面有塗覆βΝ之熱交換管 No. 1 7中,在1 20 0小時以後之剖面形狀沒有變化,可確認 BN塗覆與陶瓷與金屬之複合材料之滑動為很順利。 又,可確認使用入口溫度在攝氏280-400度之水蒸氣作 為被加熱流體時,在出口可得到攝氏540度以上,1 00 ata,而使用入口溫度在攝氏12〇一3〇0度,1 000 —4〇〇〇mmAq 之空氣及50-40 OmmAq之廢棄物燃燒氣之混合氣體作為被加 熱流體時,在出口可加熱至最高攝氏800度為止。As a result, it was confirmed that the reduction in thickness of any one of the heat exchange tubes due to corrosion is small, and no cracks have occurred, and stable heat recovery can be performed for a long time. In particular, in the heat exchange tube No. 17 with a βN coating on the outer surface of the heat-resistant alloy tube, the cross-sectional shape did not change after 120 hours. It can be confirmed that the sliding of the BN coating and the composite material of ceramic and metal is very smooth. In addition, it can be confirmed that when water vapor having an inlet temperature of 280-400 degrees Celsius is used as the heated fluid, an outlet temperature of 540 degrees Celsius or more and 100 ata can be obtained at the outlet, and the inlet temperature is 1200-1300 degrees Celsius, 1 When the mixed gas of air of 4,000-400mmAq and waste combustion gas of 50-40OmmAq is used as the heated fluid, it can be heated up to 800 degrees Celsius at the outlet.
546454 五、發明說明(13) [實施例7 ] 將其縱剖面形妝 示,耐執合金管2Λ 所示’而其橫别面 如圖9所 1 <外表面為由熱膨脹緩衝材6及陶瓷與金 勒 複口 ^依次以非接合狀態覆蓋,且耐熱合金管2盥 ί膨脹緩衝材 〃界面中^ 乂 一部分接觸,因此具有空隙之熱交換管Ν〇· 9 20 °又置在與貫施例1同樣的都市垃圾焚化爐試驗工 廠中將都市垃圾予以部分氧化之攝氏7〇〇_1〇〇〇度之 氣周圍環境中,而實行熱回收。 原排 熱父換官No.19,2〇之明細為如下述。 查L交換管No. 19 财熱合金官:鋼爐用耐熱管STBA28_2〇A,熱膨脹緩 材:碳80wt%以上之纖維,厚度〇· 5_3mm,陶瓷與金屬之人 材。料 H+MN 86 wt%,Al2〇3 ,厚度4 —5_,氣孔^ 2 5 % 〇 盒交換管No. 20 耐熱合金管:鍋爐用耐熱管STBA28_2〇A,熱膨脹緩 材:碳80wt%以上之纖維,厚度卜3mm,陶瓷與金屬之 材料:SiC 95^t%以上+Mg,厚度4 —5mm,氣孔率2%。" 其結果,因高溫排氣係⑶濃度為5_15%之還原性氣 圍環境的關係,幾乎看不到Sic及A1N氧化而劣化之現° 可實行良好之熱回收。 ’ [實施例8 ] 將在圖1 0及圖11中所示之同軸管形狀字管形狀之耐546454 V. Description of the invention (13) [Example 7] The longitudinal section of the invention is shown as shown in Figure 2 and the cross section is shown in Fig. 9 1 < The outer surface is made of thermal expansion buffer material 6 and The ceramics and the Jinle compound mouth are sequentially covered in a non-joint state, and a part of the interface of the heat-resistant alloy tube 2 and the expansion buffer material 接触 is in contact, so the heat exchange tube No. 9 20 ° with a gap is placed in In the same municipal waste incinerator test plant of Example 1, the municipal waste was partially oxidized in a gas surrounding environment at 700-10000 degrees Celsius, and heat recovery was performed. The original row The details of the hot father's official replacement No. 19 and 20 are as follows. Check L exchange tube No. 19 Financial and thermal alloy officer: heat-resistant tube STBA28_2A for steel furnace, thermal expansion retarding material: carbon 80wt% or more fiber, thickness 0.5-3mm, ceramic and metal materials. Material H + MN 86 wt%, Al2O3, thickness 4-5_, pores ^ 25% 5% box exchange tube No. 20 heat-resistant alloy tube: heat-resistant tube STBA28_2A for boiler, thermal expansion retarder: 80% by weight of carbon Fiber, thickness 3mm, ceramic and metal materials: SiC 95 ^ t% + Mg, thickness 4-5mm, porosity 2%. " As a result, due to the relationship between the high-temperature exhaust system and the reducing atmosphere with a concentration of 5-15%, it is almost impossible to see the deterioration of Sic and A1N oxidation. Good heat recovery can be implemented. ‘[Embodiment 8] The resistance of the tube shape of the coaxial tube shape shown in FIG. 10 and FIG. 11
546454 五、發明說明(14) 熱合金管2之外表面為由熱膨脹緩衝材6與陶究與金屬之複 合材料1依次以非接合狀態覆蓋,且耐熱合金管2 \熱膨脹 緩衝材6及/或熱膨脹緩衝材6與複合材料1為,在其界面 中至少一部分接觸,因此具有空隙5之熱交換管N〇 -23,設置於煤,下水道污泥脫水塊狀物及乾燥污泥焚化 爐之燃燒氣體中,實行熱回收。 a 熱交換管N 〇 · 2 1 - 2 3之明細為如下述。 熱交換管N 〇. 2 1546454 V. Description of the invention (14) The outer surface of the thermal alloy tube 2 is covered by the thermal expansion buffer material 6 and the ceramic and metal composite material 1 in a non-joint state, and the heat resistant alloy tube 2 \ thermal expansion buffer material 6 and / or The thermal expansion buffer material 6 and the composite material 1 are in contact with at least a part of the interface, so the heat exchange tube No. 23 having the gap 5 is installed in coal, the sewage sludge dewatering block and the combustion of the dry sludge incinerator In the gas, heat recovery is performed. a The details of the heat exchange tubes N 0 · 2 1-2 3 are as follows. Heat exchange tube N 0.2 1
耐熱合金管:鍋爐用耐熱管STBA28-40A及65A,熱膨脹 緩衝材··碳8 0 wt%以上之微粉與纖維之混合物,厚度 0.2-4mm,陶瓷與金屬之複合材料:SiC 95 wt%以上 厚度約為7mm,同軸管形狀(圖10)。 熱交換管No. 22 耐熱合金管:鍋爐用耐熱管STBA28_20A&5〇A,埶膨脹 緩衝材:碳8〇 wa以上之微粉,厚度〇 3_2随,陶瓷與金^ 屬之複合材料:Al2〇3 9 5 wt%以上+ A1,厚度約為4_,、Heat-resistant alloy tubes: Heat-resistant tubes STBA28-40A and 65A for boilers, thermal expansion buffers ·· A mixture of fine powder and fiber with a carbon content of more than 80 wt%, a thickness of 0.2-4mm, a composite material of ceramics and metals: SiC 95 wt% or more Approximately 7mm, coaxial tube shape (Figure 10). Heat exchange tube No. 22 Heat-resistant alloy tube: Heat-resistant tube for boiler STBA28_20A & 50A, 埶 Expansion buffer material: fine powder of carbon 80 wa or more, thickness 〇3_2, ceramic and metal ^ composite material: Al2〇3 9 5 wt% or more + A1, thickness is about 4_,
軸管形狀(圖1 〇 )。 N 熱交換管No. 23Shaft tube shape (Figure 10). N Heat Exchanger No. 23
耐熱合金管:锅爐用耐埶总 ^ +0/ 了熟 MTBA28-15A 及 20Λ,熱膨脹 綾衝材·石反80 wt%以上之^ n ^ s …人<纖維,厚度〇· 4-lmm,陶瓷盥今 屬之後合材料:A+A1N 9〇 wt% τ;' ^ 形狀(圖11)。 ⑴以上,厚度6-8咖’ U字管 其結果,煤,下水道、、七 ςπ , /心之燃燒排氣含有數百ppm之 SOx,但所有之熱交換管均 ^ & ^未被腐蝕,可回收到能夠達成Heat-resistant alloy tube: total resistance to boilers ^ + 0 / cooked MTBA28-15A and 20Λ, thermal expansion concrete punching material · stone counter 80 wt% or more ^ n ^ s… human < fiber, thickness 0.4-lmm The ceramics are now composite materials: A + A1N 90% by weight τ; '^ shape (Figure 11). ⑴ Above, the thickness of 6-8 coffee 'U-shaped tube. As a result, coal, sewer, ςπ, / heart combustion exhaust contains hundreds of ppm of SOx, but all heat exchange tubes are not corroded ^ & ^ not corroded Can be recycled to achieve
89116086.ptd 第18頁 546454 五、發明說明(15) 發電效率30%以上之高溫高壓水蒸氣,以及高溫空氣及高 溫燃燒排氣者。 又,如圖11所示,形成為U字管形狀時,需要在彎曲部 存在更多的空隙5者。 [元件編號之說明] 1 陶瓷與金屬之複合材料 2 耐熱合金管 3 碳纖維 4 氣孔 5 空隙 6 熱膨服緩衝材89116086.ptd Page 18 546454 V. Description of the invention (15) High-temperature and high-pressure water vapor with a power generation efficiency of more than 30%, as well as high-temperature air and high-temperature combustion exhaust. In addition, as shown in FIG. 11, when the U-shaped tube is formed, it is necessary to have more gaps 5 in the bent portion. [Explanation of component number] 1 Composite material of ceramic and metal 2 Heat-resistant alloy tube 3 Carbon fiber 4 Air hole 5 Void 6 Thermal expansion buffer material
89116086.ptd 第19頁 546454 圖式簡單說明 圖1為顯示本發明之一實施例之熱交換管之縱剖視圖。 圖2為顯示本發明之另一實施例之熱交換管之縱剖視 圖。 圖3為顯示本發明之另一實施例之熱交換管之橫剖視 圖。 圖4為顯示本發明之另一實施例之熱交換管之縱剖視 圖。 圖5為顯示圖4之熱交換管之橫剖視圖。 圖6為顯示本發明之另一實施例之熱交換管之橫剖視 圖。 圖7為顯示本發明之另一實施例之熱交換管之橫剖視 圖。 圖8為顯示本發明之另一實施例之熱交換管之縱剖視 圖。 圖9為顯示圖8之熱交換管之橫剖視圖。 圖1 0為顯示本發明之另一實施例之熱交換管之橫剖視 圖。 圖11為顯示本發明之另一實施例之熱交換管之橫剖視 圖0 1 89116086.ptd 第20頁89116086.ptd Page 19 546454 Brief description of the drawings Fig. 1 is a longitudinal sectional view showing a heat exchange tube according to an embodiment of the present invention. Fig. 2 is a longitudinal sectional view showing a heat exchange tube according to another embodiment of the present invention. Fig. 3 is a cross-sectional view showing a heat exchange tube according to another embodiment of the present invention. Fig. 4 is a longitudinal sectional view showing a heat exchange tube according to another embodiment of the present invention. FIG. 5 is a cross-sectional view showing the heat exchange tube of FIG. 4. FIG. Fig. 6 is a cross-sectional view showing a heat exchange tube according to another embodiment of the present invention. Fig. 7 is a cross-sectional view showing a heat exchange tube according to another embodiment of the present invention. Fig. 8 is a longitudinal sectional view showing a heat exchange tube according to another embodiment of the present invention. FIG. 9 is a cross-sectional view showing the heat exchange tube of FIG. 8. FIG. Fig. 10 is a cross-sectional view showing a heat exchange tube according to another embodiment of the present invention. Figure 11 is a cross-sectional view of a heat exchange tube showing another embodiment of the present invention. Figure 0 1 89116086.ptd page 20
Claims (1)
Applications Claiming Priority (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP11228591A JP2001049379A (en) | 1999-08-12 | 1999-08-12 | Heat transfer tube for heat exchanger |
JP22858999A JP2001056195A (en) | 1999-08-12 | 1999-08-12 | Heat transfer pipe for heat exchange |
JP22859299A JP4016311B2 (en) | 1999-08-12 | 1999-08-12 | Heat recovery method from hot gas |
JP22859099A JP3674401B2 (en) | 1999-08-12 | 1999-08-12 | Heat exchanger tube for heat exchange |
Publications (1)
Publication Number | Publication Date |
---|---|
TW546454B true TW546454B (en) | 2003-08-11 |
Family
ID=27477332
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW089116086A TW546454B (en) | 1999-08-12 | 2000-08-10 | Heat exchange tube and heat recovery method using the same |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP1122506A1 (en) |
KR (1) | KR20010072966A (en) |
TW (1) | TW546454B (en) |
WO (1) | WO2001013057A1 (en) |
Families Citing this family (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2003012155A1 (en) * | 2001-07-30 | 2003-02-13 | Jfe Engineering Corporation | Material being resistant to chloride-containing molten salt corrosion, steel pipe for heat exchanger coated with the same, and method for production thereof |
ATE269913T1 (en) * | 2002-07-31 | 2004-07-15 | Itn Nanovation Gmbh | CERAMIC COATING FOR COMBUSTION BOILERS |
US20090261289A1 (en) * | 2004-08-25 | 2009-10-22 | Yoon-Sik Ham | R502, R12 or R22 Substitute Mixed Refrigerant and Refrigeration System Using Thereof |
DE102006048445B4 (en) * | 2006-10-11 | 2016-09-08 | Udo Hellwig | Apparatus for providing heat, method for its production and method for transferring heat |
DE102013201465A1 (en) * | 2013-01-30 | 2014-07-31 | Eberspächer Exhaust Technology GmbH & Co. KG | Heat exchanger of an internal combustion engine |
DE102017217308A1 (en) * | 2017-09-28 | 2019-03-28 | Mahle International Gmbh | Heat exchanger |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6183895A (en) * | 1984-09-28 | 1986-04-28 | Hitachi Ltd | Heating surface and manufacture thereof |
JPS61227036A (en) * | 1985-04-02 | 1986-10-09 | 三菱重工業株式会社 | Ceramics coated member having excellent corrosion resistance |
JPS63140292A (en) * | 1986-11-30 | 1988-06-11 | Chuo Denki Kogyo Kk | Porous-type heat radiator |
JP2724169B2 (en) * | 1987-09-09 | 1998-03-09 | 株式会社東芝 | Heat transfer tube for steam generator and method of manufacturing the same |
JP2636980B2 (en) * | 1991-06-19 | 1997-08-06 | ワイケイケイ株式会社 | High performance heat transfer |
JPH05180585A (en) * | 1991-12-26 | 1993-07-23 | I N R Kenkyusho:Kk | Heat exchanger |
JPH06307791A (en) * | 1993-04-26 | 1994-11-01 | Y K K Kk | High performance heat transfer |
-
2000
- 2000-08-03 WO PCT/JP2000/005205 patent/WO2001013057A1/en not_active Application Discontinuation
- 2000-08-03 EP EP00949969A patent/EP1122506A1/en not_active Withdrawn
- 2000-08-03 KR KR1020017002406A patent/KR20010072966A/en not_active Application Discontinuation
- 2000-08-10 TW TW089116086A patent/TW546454B/en active
Also Published As
Publication number | Publication date |
---|---|
KR20010072966A (en) | 2001-07-31 |
EP1122506A1 (en) | 2001-08-08 |
WO2001013057A1 (en) | 2001-02-22 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP6040308B2 (en) | Heat exchanger with excellent corrosion resistance | |
TW546454B (en) | Heat exchange tube and heat recovery method using the same | |
JP4692289B2 (en) | Metal material with excellent metal dusting resistance | |
JP2004345945A (en) | Article comprising silicon base material, and bonding layer and top protective layer provided on this base material | |
JP2008101240A (en) | Heat-transfer material for heat collection, and its manufacturing method | |
JP4948834B2 (en) | Corrosion-resistant coating alloy and member coated therewith | |
JP2008214734A (en) | Metallic material having excellent metal dusting resistance | |
KR20020060689A (en) | Steel pipe with composite material coating and method for manufacturing the same | |
JP4724685B2 (en) | High temperature corrosion resistant Ni-base alloy welded structure and heat exchanger | |
JP2001056197A (en) | Heat transfer tube for heat exchange | |
JPH10274401A (en) | High temperature resistant and corrosion resistant heat exchanger tube of waste incineration boiler and super heater | |
JP2001049379A (en) | Heat transfer tube for heat exchanger | |
TW554049B (en) | Material resistant to chloride-bearing molten salt corrosion, steel tube clad with the material for heat exchanger, and method for manufacturing the material and the steel tube | |
JP2001056195A (en) | Heat transfer pipe for heat exchange | |
Deodeshmukh et al. | The oxidation performance of modern high-temperature alloys | |
Strobel et al. | Coal Slag Corrosion and Strength Degradation of Silicon Carbide/Alumina Composites | |
KR101639058B1 (en) | Heat exchange tube coated with non-metal oxides | |
JP3346365B2 (en) | Method of manufacturing aluminum matrix composite coated steel pipe | |
JP2996128B2 (en) | Air heater for high temperature corrosion resistance | |
JP3678937B2 (en) | Ceramic tube for heat exchanger | |
JP2005146409A5 (en) | ||
JP3548446B2 (en) | Heat exchanger tubes for heat exchangers | |
JP4414578B2 (en) | Air heater | |
JP2996129B2 (en) | Air heater for high temperature corrosion resistance | |
Natesan et al. | AND MECHANICAL PROPERTIES OF CERAMIC MATERIALS |