TW442634B - Inlet air pressure stabilizing method for regenerative incinerator - Google Patents

Inlet air pressure stabilizing method for regenerative incinerator Download PDF

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Publication number
TW442634B
TW442634B TW89115765A TW89115765A TW442634B TW 442634 B TW442634 B TW 442634B TW 89115765 A TW89115765 A TW 89115765A TW 89115765 A TW89115765 A TW 89115765A TW 442634 B TW442634 B TW 442634B
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Taiwan
Prior art keywords
regenerative incinerator
incinerator
closing valve
exhaust gas
output
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TW89115765A
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Chinese (zh)
Inventor
Jia-Ching Su
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Su Jia Ching
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Abstract

The present invention relates to an inlet air pressure stabilizing method for regenerative incinerator, mainly comprising the bypass design formed after the outlet pipe of the incinerator. Also, during the switching process to simultaneously switch two sets of automatic control valves of the inlet and outlet flow passages when a regenerative incinerator is used for the first time, the automatic switch valves should be closed first to generate resistance before adjusting the manual switch valves to control the variation of the inlet (or outlet) air flow rate in the required range. The manual switch valves should be fixed once the adjustment is completed. In the flow passage switching process for waste gas inputs to/outputs from the regenerative incinerator, two sets of automatic control valves are switched simultaneous, and then, resistance to the variation of inlet/outlet air flow rate during flow changing can be generated by opening/closing the automatic switch valve on the outlet pipe, to form the blockage of air input/output flow rate and reduce the variation of the pressure increase during the switching the flow passages, so as to prevent significant variation of the inlet air pressure.

Description

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五、發明說明( 本發明係' 種蓄熱式焚化爐進氣穩壓法,尤指-種可 以阻力形成穩壓效果之方法設計。 尤扣 按,空氣污染源中,除了車輪所排放的廢氣以外’工 業界因生產所排放的麻名丄 ^ ., 的廢乳,如石化業、橡膠業、油漆製造 業及塗裝業’以及近年來逐漸蓬勃發展的半導體產業,都 會產生具揮發性有機物的廢氣,而對於空氣品質造成嚴重 污染。 .而在已知的空氣淨化裝置中,過遽器之使用可初步過 /慮C氣*塵D又備則可用來分離塵埃,燃燒器則可對於廢 氣進行充分燃燒’另可見及_種蓄熱式焚化爐結構,其·在 箱體:設置兩充填室,使—引人管及—輸出管分別連接兩 充填室,又,兩充填室頂部形成連通的通道,每一充填室 中sS:置數層板,數層板間形成複數空間,複數空間中設置 蓄熱材(例如.礫石、陶瓷)加以填充,而在引入管及輸 出管上分別形成兩流道,且於兩流道上分別設置自動控制 閥,而可以自動控制閥的啟閉,來切換氣流進出之流道。 又,引入管最前端接至VOCS (揮發性有機物質氣體) 之廢氣產生端’而使VOCS (揮發性有機物質氣體)廢氣可 經由抽(送)風機的引流成用,經由引入管而進入蓄熱式 焚化爐中焚化去除,其焚化過程,可先將外界空氣引入加 熱,使熱能先由一充填室之蓄熱材加以吸收儲存,之後, 引入管及輸出管上所設置的兩道流路之自動控制閥啟閉切 換流道,使廢氣可由另一流道進入先前已儲存熱能之蓄熱 材充填室中,進行加熱焚化去除,且焚化後之高溫氣體, 本纸張尺度適用中國S家標準(CNS)A4規格&lt;210 X 297公釐) 〆--- (請先閱讀背面之注意事項再填寫本頁) 訂· •線 經濟部智慧財產局員工消費合作钍印製 4 4 A7 B7 五、發明說明 可流入另一蓄熱材充填室,使其中所設置的蓄熱材能吸收 熱能’等到下一次啟閉自動控制閥而再次改變流道時,即 可以再利用此一已經吸收熱能的蓄熱材充填室來對於廢氣 加熱焚化’藉此’可達到高效率熱能回收再利用之目的。 而此一蓄熱式焚化爐雖能克服燃燒器加熱操作成本偏 南的問題’使其利用蓄熱處理方式,而能提高熱回收率, 使操作的成本費用降低,並確實焚化去除廢氣,然而,在 實際使用上’因為’引入管最前端是接在前端設備之廢氣 產生%,而廢氣的導引及流向,是由封閉管路中之抽(送 )風機引流作用,以及引入管及輸出管上所設置的自動,控 制閥啟閉’來控制廢氣進入及排出之流道變換,而整條廢 氣處理之流道為密閉式’在正常狀態下,氣流經過蓄熱式 焚化爐(有壓損)’而引入管與輸出管閥門切換時,氣流 會短時間不經過蓄熱式焚化爐,而直接排放,引起氣流之 風量增加,造成進(排)氣流風壓增加之變動,而此—因 為控制流道的改變所造成的壓力變動,對於前端設備,即 會產生氣壓變動之不穩定狀態。 有鑑於此’本發明者特別加以研究改良創新設計,期 間經由不斷的測試實驗,終於發明出一種『蓄熱式焚化爐 進氣穩壓法j ’希能藉由本發明設計,而達到如下之發明 目的。 本發明設計之目的在於:提供一種『蓄熱式焚化爐進 氣穩壓法』,其係於蓄熱式焚化爐的輸出管後側形成分流 的流道,而在蓄熱式焚化爐啟用時之第一次輸出入流道轉 h紙張尺度適用中囷國家標準(CNS)A4規格(210 X 297公》 (請先閱讀背面之注意事項再填寫本頁) 經濟部智慧財產局員工消費合作社印製 ^---------訂---------線!'^--------------------- ^42 63 4 A7 B7 經濟部智慧財產局員工消費合作社印製 五、發明說明(j ) 換過程中’先關閉分流的流道上所設置的自動開關閥門而 形成阻力’並且,調整手動開關閥門,使其放流的排氣量 變動能在要求的範圍内,而當手動開關閥門調整完畢後, 於隨·後的廢氣輸出入蓄熱式焚化爐之流道轉換過程中,則 可藉由輸出管後側分流的流道上所設置的自動開關閥門之 關閉,而能對於廢氣輸出入流道變換時之排氣量變動形成 阻力’使其在變換流道時能形成排氣量擋止,並降低氣壓 增加之變動’以避免氣壓增大之變動而造成前端設備之損 壞。 為使貴審查委員能進一步了解本發明設計之方法'作 用及其他目的,茲附以圖式詳細說明如后: (一) 圖式部份: 第一圖:係本發明之結構示意圖。 第二圖:係本發明之實施例圖(一)。 第三圖:係本發明之實施例圖(二)。 第四圖:係本發明之實施例圖(三)。 第五圖:係本發明之實施例圖(四)。 (二) 圖號部份: (1 0 )箱體 (12)充填室 (1 2 4 )出口 (1 3 2 )入口 (1 4 )蓄熱材 (1 6 2 )透氣孔 (1 1 )分隔壁 (1 2 2 )入口 (1 3 )充填室 (1 3 4)出口 (1 6 )層板 (17)加熱元件 本紙張尺度適用中國國家標準(CNS)A4規格(2〗0 X 297公釐&gt; {請先闓讀背面之注意事項再填寫本頁) _v---- 訂--------I 〆----------—----— — — — — ( 442634 經 濟 部 智 慧 財 產 局 員 工 消 費 合 作 社 印 製 五、發明說明(+ ) (1 8 )溫度控制器 (2 2 )自動控制閥 (3 0 )輸出管 (3 4 )自動控制閥 (3 7 )切換器 (4 1 )分流管 (5 0 )前端設備 首先’請配合參看第—国 一 圖所不,其中,蓄熱式焚化妨 結構包括:一箱體(1 〇 ), 以及—引入管(20)、一 輸出管(30)接設至箱體( 瓶、丄〇)中,箱體(10) 1 設置分隔壁(1 1)而區隔成 h攻至少兩充填室(1 2 )、丨 13),兩充填室(12) 、 (^ 〈13)頂部形成連通的ϋ 道,使氣流可由此流通於兩充填室(丄2 )、(丄3 ) $ :並且’在兩充填室(12)、(13)頂端設置數加索 元件(1 7 ),加熱元件7 )可為電熱棒、電熱線邊 瓦斯加熱器。 每一充填室(1 2 ) ' ( 1 3 )中設置數層板(工6 )’數層板(1 6 )間形成複數空間,複數空間中設置奮 熱材(1 4)加以填充’蓄熱材(i 4)可為礫石或陶董 ,且各層板(1 6 )上設置一個(含)以上之透氣孔(1 6 2)。 引入管(2 0)形成兩道管路,兩道管路分別穿人兩 充填室(12) 、(13)中形成入口(122) 、(1 3 2 ),而在兩道管路上分別設置自動控制閥(2 2 )、 (2 0 )引入管 (2 4)自動控制閥 (3 2 )自動控制閥 (3 5 )乾燥箱 (4 〇 )自動開關閥門 (4 2 )手動開關閥門 本纸張尺度適用t國國家標準(CNS)A4規格(2】0 X 297公釐) (請先閱讀背面之注意事項再填寫本頁) W_____ 訂 --------線!'^--------------------- 442634 A7 _ B7 五、發明說明(l) 經濟部智慧財產局員工消費合作社印製 (24) ’輸出管(30)亦形成兩道管路,兩道管路分 別穿入兩充填室(12)、(13)中形成出〇 (124 )、(1 3 4 ),且於兩道管路上分別設置自動控制閥( 32)、(34),而在引入管(2〇)前端或輸出管( 3〇)末端可設置送(抽)風機(習用結構圖中未示), 又,箱體(1 0 )外側設置溫度控制器(i 8 ),溫度控 制器(1 8 )能控制加熱元件(χ 7 )之加熱時機及加: 溫度。 又,自動控制閥(2 2 ) 、( 3 2 ) 、( 2 4 )、( 3 4 )可配合定時器控制啟閉,使充填室(丄2 )、(工3)之入口(122) 、(132)及出口(124)、 (1 3 4 )’形成一端流入且一端排出之狀態,例如,自 動控制閥(3 2 )、( 2 4)開啟,而自動控制閥(2 2 )、(3 4 )關閉·’可使經由引入管(2 0 )引入的廢氣 由入口( 1 3 2 )進入充填室(1 3 ),且由流經充'填室 (12)後由出口(124)朝輸出管(30)排出。 如第二圖所示,在引入管(2 〇 )上適當處接設切換 器(37) ’切換器(37)另端接至乾燥箱(35) ’ 乾燥箱(3 5 )前端連接至工業裝置污染源之前端設備( 5 0)廢氣排氣端,而在預熱階段時,可先啟動送(抽) 風機,使外界空氣由切換器(3 7 )進入引入管(2 〇 ) ,並經由自動控制閥(2 4)開啟而進入充填室(1 3 ) 中’且經由加熱元件(1 7 )加熱後流入充填室(1 2 ) ,此時,加熱後進入充填室(1 2 )之空氣熱能可經由蓄 (請先閱讀背面之注意事項再填寫本頁) V- 訂----------線f -n n Γ— I n n n n n I n n n , 本紙張尺度適用中园困家標準(CNS&gt;A4規格(210 X 297公釐) 4 經濟部智慧財產局員工消費合作社印製 4 2 ? 3 4 A7 ______B7__ 五、發明說明(匕) 熱材(1 4 )吸收加以儲存’使加熱後的空氣以較低溫度 向外排放。 而當預熱一段時間後,蓄熱材(1 4 )吸熱溫度約達 300〜800°C時’可進行廢氣焚化處理作業,如第三圊所示 ’而可將切換器(37)轉成引入管(2〇)與乾燥機( 35)連通’使工業裝置污染源之前端設備(5〇)所排 放的廢氣,可經由乾燥機(3 5)作用,而進入引入管( 2 0 )’並且’經由送(抽)風機引動廢氣,而經由自動 控制閥(2 2)開啟’並由入口(132)進入蓄熱的充 填室(12)中,使廢氣在高溫的充填室(12)中焚&gt;匕 而去除,且其焚化之高溫氣體可流入另一充填室(1 3) ’並由充填室(13)中之蓄熱材(14)加以吸收熱能 而儲存,使廢氣以較低溫度從出口(134)流出,並由 送(抽)風機汲引,而由輸出管(3 0 )向外排出。 配合參看第四圖所示,其中,在充填室(13)中之 蓄熱材(1 4 )蓄熱升溫,且經由一段時間而達定時器預 設時間,則啟動自動控制閥(3 2 )、( 2 4 )開啟,及 自動控制閥(2 2 )、( 3 4 )關閉,使廢氣可由引入管 (20)經自動控制閥(32)、入口(132)進入充 填室(1 3)中,使廢氣可在充填室(1 3)之高熱中燃 燒氧化去除,而焚化之高溫氣體可流入充填室(1 2 )中 ,此時,充填室(1 2 )在前次作用而降溫後’可對於高 溫氣體進行吸熱儲存,使流經的高溫氣體降溫’並由出口 (124)流入輸出管(30),且由送(抽)風機作用 本纸張尺度適用令國國家標準(CNS)A4規格(2〗0 X 297公« )V. Description of the invention (The present invention is 'a kind of regenerative incinerator inlet pressure stabilization method, in particular-a method design which can form a voltage stabilization effect by resistance. Especially deducted, in the air pollution source, except for the exhaust gas emitted by the wheels' Vapor waste from industrial production, such as petrochemical industry, rubber industry, paint manufacturing industry, and coating industry, and the semiconductor industry that has been booming in recent years, will produce volatile organic waste gas. However, in the known air purification device, the use of the filter can be used to preliminarily consider / consider C gas, dust and D can be used to separate dust, and the burner can be used for exhaust gas. 'Full combustion' is also visible and _ a kind of regenerative incinerator structure, which is in the box: two filling chambers are set up so that the-lead-in pipe and the-output pipe are connected to the two filling chambers respectively, and the two filling chambers form a communication channel SS in each filling chamber: several layers of plates are arranged, a plurality of spaces are formed between the plurality of plates, and heat storage materials (such as gravel and ceramics) are filled in the plurality of spaces, and the inlet pipe and the output pipe are divided into Do not form two flow channels, and set automatic control valves on the two flow channels, and can automatically control the opening and closing of the valves to switch the flow path of the air flow in and out. In addition, the front end of the introduction pipe is connected to VOCS (volatile organic gas). The exhaust gas generating end, so that VOCS (volatile organic substance gas) exhaust gas can be used for drainage by a blower (sending) fan, and then introduced into a regenerative incinerator through an introduction pipe for incineration and removal. In the incineration process, the outside air can be first Heating is introduced so that the thermal energy is first absorbed and stored by the heat storage material in a filling chamber. After that, the automatic control valves of the two flow paths set on the introduction pipe and the output pipe open and close the switching flow path, so that the exhaust gas can enter the previous flow path through the other flow path. The thermal storage material filling room that has stored heat energy is removed by heating and incineration, and the high-temperature gas after incineration is used. The paper size is applicable to China Standard S (CNS) A4 specifications &lt; 210 X 297 mm. 〆 --- (Please (Please read the notes on the back before filling this page) Order • Printed by the Intellectual Property Bureau of the Ministry of Economic Affairs for consumer cooperation printing 4 4 A7 B7 5. The invention description can flow into another heat storage material filling room, The heat storage material installed therein can absorb heat energy. When the flow path is changed again when the automatic control valve is opened and closed next time, the heat storage material filling chamber that has absorbed heat energy can be reused to heat and incinerate the exhaust gas. The purpose of high-efficiency thermal energy recycling. Although this regenerative incinerator can overcome the problem of the southward cost of the heating operation of the burner, 'using the regenerative heat treatment method, it can improve the heat recovery rate, reduce the cost of operation, and indeed incinerate and remove the exhaust gas. In practical use, 'because' the front end of the introduction pipe is the exhaust gas generation% connected to the front-end equipment, and the exhaust gas is guided and flowed by the suction (sending) fan in the closed pipeline to induce the flow, as well as the introduction pipe and the output pipe. The set automatic, control valve is opened and closed 'to control the change of the flow path of the exhaust gas entering and exiting, and the flow path of the entire exhaust gas treatment is closed.' Under normal conditions, the air flow passes through the regenerative incinerator (with pressure loss) ' When the inlet pipe and output pipe valves are switched, the air flow will be directly discharged without passing through the regenerative incinerator for a short time, which will cause the increase of the air flow volume and the increase of the air pressure of the inlet (exhaust) air flow. The change in pressure caused by changes in pressure will cause an unstable state of pressure fluctuations for front-end equipment. In view of this, the present inventors have made special efforts to improve and innovate the design. During continuous testing and experiments, they finally invented a "regenerative incinerator intake gas pressure stabilization method j", which can be designed by the present invention to achieve the following inventive objectives. . The purpose of the present invention is to provide a "regenerative method of the regenerative incinerator intake gas", which is formed on the rear side of the output tube of the regenerative incinerator to form a branched flow channel. The paper size of the secondary input and output channels is applicable to the Chinese National Standard (CNS) A4 specification (210 X 297) (Please read the precautions on the back before filling this page) Printed by the Consumer Cooperatives of the Intellectual Property Bureau of the Ministry of Economic Affairs ^- ------- Order --------- line! '^ --------------------- ^ 42 63 4 A7 B7 Ministry of Economic Affairs Printed by the Intellectual Property Bureau's Consumer Cooperatives V. Description of the invention (j) During the replacement process, 'the automatic opening and closing valve provided on the diverted flow path is closed to form resistance', and the manual opening and closing valve is adjusted so that the exhaust volume of the discharge fluctuates. It can be within the required range, and after the manual opening and closing valve adjustment is completed, in the flow path conversion process of the subsequent exhaust gas output into the regenerative incinerator, it can be set by the flow path on the rear side of the output pipe. The automatic opening and closing of the valve can form changes in the exhaust gas volume when the exhaust gas input and output channels are changed. The force 'makes it possible to form an exhaust volume stop when changing the flow channel and reduce the increase in air pressure' to avoid the damage of the front-end equipment caused by the increase in air pressure. In order to allow your reviewers to further understand the present invention, The method and other purposes are described in detail with drawings as follows: (I) Schematic part: The first figure is a schematic diagram of the structure of the present invention. The second figure is a diagram of the embodiment of the present invention (a) The third diagram: the embodiment of the present invention (two). The fourth diagram: the embodiment of the present invention (three). The fifth diagram: the embodiment of the present invention (four). (Two) The diagram Part No .: (1 0) box (12) filling room (1 2 4) exit (1 3 2) entrance (1 4) heat storage material (1 6 2) vent hole (1 1) partition wall (1 2 2 ) Inlet (1 3) Filling room (1 3 4) Outlet (1 6) Shelf plate (17) Heating element This paper size is applicable to China National Standard (CNS) A4 specifications (2) 0 X 297 mm &gt; {Please first闿 Read the notes on the back and fill in this page) _v ---- Order -------- I 〆 ------------------ — — — — (442634 Economy Intellectual Property Office Printed by the Industrial and Consumer Cooperatives 5. Description of the invention (+) (1 8) Temperature controller (2 2) Automatic control valve (3 0) Output pipe (3 4) Automatic control valve (3 7) Switcher (4 1) Diversion The front-end equipment of the tube (50) should first be coordinated with reference to the first picture of the first country. Among them, the regenerative incineration structure may include: a box (10), and-an introduction tube (20), an output tube (30 ) Is connected to the box body (bottle, 丄 〇), the box body (10) 1 is provided with a partition wall (1 1) and divided into at least two filling chambers (12, 13), and two filling chambers (1) 12), (^ <13) A communicating channel is formed at the top, so that the airflow can flow through the two filling chambers (丄 2), (丄 3) $: and 'set at the top of the two filling chambers (12), (13) The data element (1 7) and the heating element 7) can be electric heating rods, electric heating wire gas heaters. Each filling room (1 2) '(1 3) is provided with a plurality of layers (work 6)', a plurality of spaces are formed between the plurality of layers (1 6), and an exothermic material (1 4) is filled in the plurality of spaces to fill the 'heat storage' The material (i 4) may be gravel or ceramics, and each layer plate (1 6) is provided with one or more ventilation holes (1 6 2). The introduction pipe (20) forms two pipelines, and the two pipelines respectively pass through the two filling chambers (12) and (13) to form the inlets (122) and (1 3 2), and are respectively arranged on the two pipelines. Automatic control valve (2 2), (2 0) introduction pipe (2 4) automatic control valve (3 2) automatic control valve (3 5) drying box (4 〇) automatic opening and closing valve (4 2) manual opening and closing valve paper The Zhang scale is applicable to the national standard (CNS) A4 specification (2) 0 X 297 mm (Please read the precautions on the back before filling this page) W_____ Order -------- line! '^ --------------------- 442634 A7 _ B7 V. Description of the invention (l) Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs (24)' Output tube (30) Two pipelines are also formed, and the two pipelines penetrate into the two filling chambers (12) and (13) respectively to form 0 (124) and (1 3 4), and automatically set up two pipelines respectively. Control valves (32), (34), and a fan (not shown) can be provided at the front end of the introduction pipe (20) or the end of the output pipe (30) (not shown in the conventional structure diagram), and the box (1 0 ) A temperature controller (i 8) is set on the outside. The temperature controller (1 8) can control the heating timing of the heating element (χ 7) and the temperature: In addition, the automatic control valves (2 2), (3 2), (2 4), (3 4) can cooperate with the timer to control the opening and closing, so that the inlet (122) of the filling chamber (丄 2), (工 3), (132) and outlets (124), (1 3 4) 'form a state where one end flows in and one end is discharged, for example, the automatic control valves (3 2), (2 4) are opened, and the automatic control valves (2 2), ( 3 4) Close · 'allows the exhaust gas introduced through the introduction pipe (20) to enter the filling chamber (1 3) from the inlet (1 3 2) and flow through the filling chamber (12) and then to the outlet (124) Discharge toward the output pipe (30). As shown in the second figure, a switcher (37) is connected to the introduction pipe (20) at an appropriate place. 'The switcher (37) is connected to the drying box (35) at the other end.' The front end of the drying box (3 5) is connected to the industry. Install the exhaust end of the exhaust equipment at the front end of the source (50), and in the preheating phase, the blower can be started first, so that the outside air enters the introduction pipe (20) from the switch (37) and passes through The automatic control valve (2 4) opens and enters the filling chamber (1 3) 'and is heated by the heating element (1 7) and flows into the filling chamber (1 2). At this time, the air entering the filling chamber (1 2) after heating Thermal energy can be stored (please read the precautions on the back before filling in this page) V-Order ------------ line f -nn Γ— I nnnnn I nnn, this paper standard is applicable to the standard of the homeless family (CNS &gt; A4 specification (210 X 297 mm) 4 Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs 4 2? 3 4 A7 ______B7__ V. Description of the invention (dagger) Hot material (1 4) Absorbed and stored 'after heating The air is exhausted at a relatively low temperature. After a period of preheating, the heat storage material (1 4) absorbs about 300 ~ 80 At 0 ° C, the waste gas incineration treatment operation can be performed, as shown in the third section, and the switch (37) can be converted into the introduction pipe (20) and communicated with the dryer (35) to make the front-end equipment of the industrial plant pollution source (50) The exhaust gas discharged can be introduced into the introduction pipe (20) through the action of the dryer (35) and 'exhaust gas is induced by the fan (exhaust) and opened by the automatic control valve (22)' It enters the heat storage filling chamber (12) from the inlet (132), so that the exhaust gas is removed by incineration in the high temperature filling chamber (12), and the incinerated high temperature gas can flow into another filling chamber (1 3) 'And the heat storage material (14) in the filling chamber (13) absorbs and stores the heat energy, so that the exhaust gas flows out of the outlet (134) at a lower temperature, and is drawn by the sending (exhausting) fan, and is output by the output pipe (3 0 See Figure 4 for cooperation, where the heat storage material (1 4) in the filling chamber (13) heats up and heats up, and after a period of time reaches the timer preset time, the automatic control valve ( 3 2), (2 4) are opened, and the automatic control valves (2 2), (3 4) are closed, so that the exhaust gas The introduction pipe (20) enters the filling chamber (13) through the automatic control valve (32) and the inlet (132), so that the exhaust gas can be removed by combustion and oxidation in the high heat of the filling chamber (13), and the incinerated high-temperature gas can be It flows into the filling chamber (12). At this time, after the filling chamber (12) has cooled down the previous time, 'the high-temperature gas can be stored in an endothermic manner, and the high-temperature gas flowing through can be cooled', and flows out through the outlet (124). Tube (30), and the role of sending (extracting) fan This paper size applies the national standard (CNS) A4 specifications (2〗 0 X 297 public «)

(請先閱讀背面之注意事項再填寫本頁) • ' I ϋ ! I I I )6J I n ϋ ϋ I 1 ϋ I ί &lt;1 ·1 I n I It n ] n n ϋ I n I * &lt;42634 經濟部智慧財產局員工消費合作社印如我 A7 B7 五、發明說明(y) 下由輸出管(30)向外排出,如此一來,即可形成一種 替換式之循環吸熱儲存,而能對於廢氣持績進行焚化去除 作業。 本發明設計之進氣穩壓法,係於蓄熱式焚化爐的輸出 菅(3 〇 )後側形成分流的流道,此一分流的流道是在輸 出管(3 0 )上設置分流管(4 1 ),且於分流管(4 1 )及輸出管(3 0 )之迴路上分別設置手動開關閥門(4 2)及自動開關閥門(4〇),而如第三圖及第四圖所示 ’當自動控制閥(2 2 )、( 3 4 )由開啟狀態轉為關閉 狀態,且自動控制閥(3 2 )、( 2 4 )由關閉狀態轉'為 開啟狀態之第一次轉換過程中’自動開關閥門(4 〇 )同 時關閉,而可先調整手動開關閥門(4 2 ),使製程中的 排氣量氣壓變動能在所要求的範圍内,而當自動控制閥( 2 2 ) 、( 3 4 )由開而閉,且自動控制閥(3 2 )、( 2 4)由閉而開之轉換流道完成時,同時以控制方式啟動 自動開關閥門(4 0 )使其開啟,此時,進出入流道完成 轉換,且自動開關閥門(4 0 )開啟,而使廢氣可由自動 控制閥(24)所在的流道進入充填室(1 3),且完成 焚化去除有毒物後之氣體,可由充填室(1 2)之出口( 1 2 4)及自動控制閥(3 2)所在的流道經由輸出管( 3 0)及自動開關閥門( 4 0)而向外排出,而當完成此 一流道及充填室(1 3 )、( 1 2 )的焚化作業後,於再 次轉換流道使自動控制閥(2 2 )、( 3 4 )由閉而開, 且自動控制閥(3 2 )'( 2 4 )由開而閉時,可同時啟 9 本紙張尺度適用中國國家標準(CNS)A4規格(2〗〇 X 297公釐) (請先閱讀背面之注意事項再填寫本頁) &gt;------- —訂---------線-(Please read the notes on the back before filling this page) • 'I ϋ! III) 6J I n ϋ ϋ I 1 ϋ I ί &lt; 1 · 1 I n I It n] nn ϋ I n I * &lt; 42634 Printed by the Consumer Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs, such as my A7 B7 V. The invention description (y) is discharged outward from the output pipe (30). In this way, an alternative type of cyclic heat absorption storage can be formed, and Keep track of incineration removal operations. The inlet pressure stabilization method designed by the present invention is formed on the rear side of the output 菅 (30) of the regenerative incinerator to form a split flow channel. This split flow channel is provided with a split tube (30) on the output tube (30). 4 1), and a manual opening and closing valve (4 2) and an automatic opening and closing valve (40) are respectively set on the circuit of the shunt pipe (41) and the output pipe (30), as shown in the third and fourth figures It shows the first conversion process when the automatic control valves (2 2) and (3 4) are changed from open to closed and the automatic control valves (3 2) and (2 4) are changed from closed to open. The 'automatic opening and closing valve (4〇) is closed at the same time, and the manual opening and closing valve (4 2) can be adjusted first, so that the fluctuation of the exhaust gas pressure during the process can be within the required range, and when the automatic control valve (2 2) , (3 4) is opened and closed, and the automatic control valve (3 2), (2 4) is switched from closed to open, and at the same time, the automatic opening and closing valve (4 0) is controlled to be opened at the same time, At this time, the in and out flow passages are switched, and the automatic opening and closing valve (40) is opened, so that the exhaust gas can be controlled by the automatic control valve (24). The flow channel where it enters the filling chamber (1 3), and the gas after the incineration is removed to remove toxic substances can be output through the outlet (1 2 4) of the filling chamber (12) and the flow channel where the automatic control valve (3 2) is located. The pipe (30) and the automatic opening and closing valve (40) are discharged outward, and after the incineration operation of the first channel and the filling chambers (1 3), (1 2) is completed, the flow channel is switched again to make the automatic control valve (2 2), (3 4) can be opened at the same time when the automatic control valve (3 2) '(2 4) is opened from the closed, and 9 can be opened at the same time. This paper size applies the Chinese National Standard (CNS) A4 specification ( 2 〖〇X 297mm) (Please read the notes on the back before filling in this page) &gt; ------- —Order --------- Line-

1 I 42 6 A7 B7 五 經濟部智暮財產局員工消費合作社印製 、發明說明( 動自動開關閥門(4 〇 )使其關閉,此時,管内氣壓可因 為自動開關閥門(4 〇 )的關閉而形成阻力,以降低氣壓 增加之變動,使管内氣流可經由分流管(4 1 )及手動開 關閥門(4 2 ),而當完成自動控制閥的流道轉換之後’ 自動開關閥門(4 0 ) $時開啟。 一 另外,如第五圖所示,在分流管(4 1 )上可設置第 二個焚化爐(6 Q )之充填室,且於其中設置加熱元件及 畜熱材,而讓流道轉換過程中’因流向變換而未焚化之 VOCS(揮發性有機物質氣體),可因自動開關閥門(4〇 )關閉而流經分流管(4 1 ),且由該處所設置的第三 個火化爐(6 0 )之充填室中加以焚化,以達到完全焚化 去除有毒物氣體之目的。 又,本發明之引入管(20)、輸出管(3〇),以 及其上所設置的自動控制閥(22) ' (24) 、(32 )、(3 4)及自動開關閥門(4 〇 ) ’包括蓄熱式焚化 爐之充填室(12) 、(13),可製造成位於同一機殼 中,且其啟閉方式,可如上所述,而同樣可於氣流流道變 換時之排氣量變動時形成阻力,以降低氣壓增加之變動, 並避免前端設備之損壞,而同樣含蓋於本發明設計之精神 領域中。 因此,經由上述發明方法之詳細說明,可清楚看出本 發明設計之特點在於: 其係於蓄熱式焚化爐的輸出管(3 〇 )後側形成分流 的流道,而可在蓄熱式焚化爐第一次轉換流道的過程中, (請先閱讀背面之注意事項再填寫本頁) W----.-----訂 --------線!^------------------------1 I 42 6 A7 B7 Printed by the Consumer Cooperative of the Zhimu Property Bureau of the Ministry of Economic Affairs, and a description of the invention (the automatic opening and closing valve (4 〇) to close it, at this time, the pressure in the pipe can be closed by the automatic opening and closing valve (4 〇) The resistance is formed to reduce the increase in air pressure, so that the air flow in the pipe can pass through the diverter pipe (4 1) and the manual opening and closing valve (4 2), and when the flow path conversion of the automatic control valve is completed, the automatic opening and closing valve (4 0) In addition, as shown in the fifth figure, a filling chamber of a second incinerator (6 Q) can be set on the shunt pipe (4 1), and a heating element and a livestock hot material are set in the filling chamber, so that VOCS (Volatile Organic Substance Gas) that has not been incinerated due to the change of flow direction during the flow channel conversion process can flow through the diverter tube (41) due to the automatic opening and closing valve (40), and the third Incineration in the filling chamber of each cremator (60) to achieve the purpose of complete incineration and removal of toxic gases. In addition, the introduction pipe (20), output pipe (30) of the present invention, and the automatic Control valve (22) '(24), (32) (3 4) and automatic opening and closing valve (4 〇) 'Including the filling chambers (12), (13) of the regenerative incinerator, which can be manufactured in the same casing, and the opening and closing methods can be as described above, and It can also form a resistance when the exhaust volume changes when the air flow channel changes, so as to reduce the increase in air pressure and avoid damage to the front-end equipment, which is also covered in the spirit of the design of the present invention. Therefore, through the above-mentioned inventive method In the detailed description, it can be clearly seen that the design of the present invention is characterized in that: it is connected to the rear side of the output tube (30) of the regenerative incinerator to form a split flow channel, and the regenerative incinerator can be switched for the first time In the process, (Please read the precautions on the back before filling out this page) W ----.----- Order -------- line! ^ ---------- --------------

44^634 A7 I----—_ B7 五、發明說明(y) 關閉自動開關閥門(4 0 ),且調整手動開關閥門(4 2 ),使其放流的排氣量變動能在要求的範圍内,而手動開 關閥門(4 2 ) —旦調整完畢後即予以固定,在隨後的流 道轉換過程中,則只要控制自動開關閥門(4 〇 )在輸出 官(3 0 )上的閉、啟,即可對於氣流流道變換時之排氣 量變動形成阻力,使其在變換流道時能降低氣壓增加之變 動,以避免前端設備之損壞。 綜上所述,本發明之『蓄熱式焚化爐進氣穩壓法』’ 是利用自然法則技術思想之高度創作,符合發明專利申請 要件’爰依法倶文提出申請。 , &lt;請先閱讀背面之注意事項再填寫本頁) &gt;------- -訂---------線 經濟部智慧財產局員工^費合作社印製44 ^ 634 A7 I ----—_ B7 V. Description of the invention (y) Close the automatic opening and closing valve (4 0), and adjust the manual opening and closing valve (4 2) so that the amount of exhaust gas discharged can fluctuate within the required range. Within the range, and the manual opening and closing valve (4 2)-once the adjustment is completed, it will be fixed. In the subsequent flow channel conversion process, as long as the automatic opening and closing valve (4 〇) on the output officer (3 0) is closed, When it is turned on, it can form a resistance to the change of the exhaust gas volume when the air flow channel is changed, so that it can reduce the increase of air pressure when the flow channel is changed to avoid damage to the front-end equipment. To sum up, the "regenerative method of the regenerative incinerator air intake" of the present invention is a highly creative use of the technical principles of natural law, and is in accordance with the requirements of the invention patent application, which is filed in accordance with the law. , &Lt; Please read the notes on the back before filling out this page) &gt; --------- -Order --------- Line Printed by the staff of the Intellectual Property Bureau of the Ministry of Economic Affairs ^

η · 本紙張尺度適用中國國家標準(CNS)A4規格&lt;210 X 297公爱&gt;η · This paper size applies to China National Standard (CNS) A4 specifications &lt; 210 X 297 Public Love &gt;

Claims (1)

4 A8 B8 C8 D8 六、申請專利範圍 (請先閲讀背面之注意事項再填寫本頁) 丄’一種蓄熱式焚化爐進氣穩壓法,其係於蓄熱式焚 化爐的輸出管後側形成分流的流道,而在蓄熱式焚化爐啟 用時之第一次輸出入流道轉換過程中,先關閉分流的流道 上所設置的自動開關閥門而形成阻力,並且,調整手動開 關閥門’使其放流的排氣量變動能在要求的範圍内,而當 手動開關閥門調整完畢後即予以固定,於隨後的廢氣輸出 入蓄熱式焚化爐之流道轉換過程中,則可藉由輸出管後側 分流的流道上所設置的自動開關閥門之啟閉,而能對於廢 氣輸出入流道變換時之排氣量變動形成阻力,使其在變換 流道時能形成排氣量擋止並降低氣壓增加之變動。 ' 2·如申請專利範圍第1項所述之蓄熱式焚化爐進氣 穩壓法’其中,蓄熱式焚化爐的輸出管後側所形成分流的 流道,是在輸出管上接設分流管加以構成。 線. 3 _如申請專利範圍第2項所述之蓄熱式焚化爐進氣 穩壓法,其中,手動開關閥門設置於分流管上。 4·如申請專利範圍第2項所述之蓄熱式焚化爐進氣 穩壓法,其中,自動開關閥門設置於輸出管上。 經濟部智慧財產局員工消費合作社印製 5·如申請專利範圍第2項所述之蓄熱式焚化爐進氣 穩壓法,其中,在分流管上可設置第三個焚化爐之充填室 ,且於其中設置加熱元件及蓄熱材,而讓流道轉換過程中 ,因流向變換而未焚化之VOCS (揮發性有機物質氣體)能 加以焚化。 12 本紙張尺度適用中國國家標準(CNS)A4規格(210 X 297公釐)4 A8 B8 C8 D8 6. Scope of patent application (please read the precautions on the back before filling this page) 丄 'A regenerative incinerator inlet pressure stabilization method, which forms a shunt on the back side of the output tube of the regenerative incinerator When the regenerative incinerator is activated for the first time when the input and output channels are switched, the automatic opening and closing valve set on the divided flow channel is closed to form resistance, and the manual opening and closing valve is adjusted to allow the The exhaust gas volume can be within the required range, and it will be fixed after the manual opening and closing valve adjustment is completed. During the subsequent conversion process of the exhaust gas output to the regenerative incinerator, it can be divided by the rear side of the output pipe. The opening and closing of the automatic opening and closing valve set on the flow channel can form resistance to the change of the exhaust gas volume when the exhaust gas input and output channels are changed, so that when the flow channel is changed, it can form an exhaust gas volume stop and reduce the increase of the air pressure. '2. Regenerative incinerator gas inlet pressure stabilization method as described in item 1 of the scope of the patent application', wherein the flow path formed by the rear side of the output tube of the regenerative incinerator is a shunt tube connected to the output tube Make up. Line 3 _ As described in item 2 of the scope of the patent application, the method for regulating the temperature of the intake air of the regenerative incinerator, wherein the manual opening and closing valve is arranged on the shunt pipe. 4. Regenerative incinerator gas inlet pressure stabilization method as described in item 2 of the scope of patent application, wherein an automatic opening and closing valve is provided on the output pipe. Printed by the Employees' Cooperative of the Intellectual Property Bureau of the Ministry of Economic Affairs 5. The method for regulating the inlet temperature of a regenerative incinerator as described in item 2 of the scope of patent application, in which a third incinerator filling chamber can be set on the shunt pipe A heating element and a heat storage material are provided therein, so that during the conversion process of the flow path, VOCS (volatile organic substance gas) that has not been incinerated due to the change of flow direction can be incinerated. 12 This paper size applies to China National Standard (CNS) A4 (210 X 297 mm)
TW89115765A 2000-08-05 2000-08-05 Inlet air pressure stabilizing method for regenerative incinerator TW442634B (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102498345A (en) * 2009-09-22 2012-06-13 新东工业株式会社 Regenerative thermal oxidization system and method for operating same
TWI410593B (en) * 2009-04-17 2013-10-01
CN109140452A (en) * 2018-10-15 2019-01-04 江苏永春环境工程有限公司 A kind of heat accumulating type heating power incinerating apparatus

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI410593B (en) * 2009-04-17 2013-10-01
CN102498345A (en) * 2009-09-22 2012-06-13 新东工业株式会社 Regenerative thermal oxidization system and method for operating same
CN102498345B (en) * 2009-09-22 2014-06-11 新东工业株式会社 Regenerative thermal oxidization system and method for operating same
CN109140452A (en) * 2018-10-15 2019-01-04 江苏永春环境工程有限公司 A kind of heat accumulating type heating power incinerating apparatus
CN109140452B (en) * 2018-10-15 2024-01-05 江苏永春环境工程有限公司 Heat accumulating type thermal incinerator

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