TW305917B

TW305917B -

Info

Publication number: TW305917B
Application number: TW085106490A
Authority: TW
Original assignee: Nippon Kokan Kk
Priority date: 1995-06-02
Filing date: 1996-05-31
Publication date: 1997-05-21
Also published as: KR970002100A; KR100194446B1

Description

305917 A7 B7 經漓部中央標準局：^工消费合作社印狀五、發明説明 ( 1 ) 1 1 t 發明之背景 1 1 I 1 . 發明之領域 /~、 1 I 本發明係翡於一種垃圾焚化爐之燃燒控制方法及其裝置。請先 1 閱 2 . 有 Μ 挟 a 之珙明讀 •背 I 面— I 白動加煤機 (Sto k e Γ ) 型垃圾焚化爐被廣泛用於城市廢水之_ 注 I 意 1 1 處理工廠〇該型焚化爐白資源節省及能量節省之覲點，藉事項· 1 再 1 由有效回收白垃圾焚化爐所產生之大量熱能時常伴隨有力產生本裝一** Μ 氣渦輪動力產生器〇 Μ 於該型垃圾焚化爐之動頁 1 I » 潘定的動力產生箱要播定的燃燒或焚化櫬内側之恒定熱 1 1 產生〇 1 1 該型白動加煤機垃圾焚化爐採用恒定效率焚化作為基本 1 訂操作橫式〇 ” t写定效率焚化" —. 詞意指在特定時間内將特定 1 I 量之垃圾裝入之焚化〇為了控制焚化爐内之热產生在恒定 1 1 1 之位準下 m 監澜在特定時間内裝入焚化機之垃圾 ft及装 1 1 入的垃圾之產生熱或對應於燃焼負荷之狀態量 (例如蒸氣量 )之大小並控制供應至垃圾焚化爐之自動加煤機 1 之燃燒空氣之流速 Μ 使狀態 ft 得 Μ 穩定〇 - 1 ! 圖 13顯示 __. 傅統白動加煤機型垃圾焚化爐及其燃堍控制 1 1 系統〇垃圾焚化爐 1設有自動加煤櫬1 a至1 C ，垃圾裝填開 1 1 口 2 、降灰口 3 排放烟道排放 m 腰之焚化爐出 P 4 、煙囱6 1 及二次空氣 (冷卻空氣）入 Ρ 7 >設有熱交換器5 a之蒸氣產 | 生鍋爐 5安裝在焚化爐出口 4 烟道排放氣白該處排出。 1 垃圾焚化爐 1具有燃燒空氣供應系統可將冷卻空氣供 1 1 應至 η 動加煤檄 1 a 至 1 c 而冷卻空氣供應糸統則將冷卻空 1 1 -4 本紙張尺度適用屮國國家標準（CNS ) A4規格（210X 297公釐） 4 經满部中央標孪H工消资合作社印t A7 B7 五、發明説明（2 ) 氣供應至焚化爐。燃焼空氣供應糸統藉由滾速調整拥構9 如播板將燃堍空氣自風扇8鏔入自動加煤機la至lc內。冷卻空氣供應糸統則賴由流速調整機構11如播板將冷卻空氣自風Μ 10直接鋇入焚化爐之人口 7。此等流速調整櫬構9, 11係由電腦17所控制。流速調整機構9乃基於自燃燒空氣流速控制裝置16產生之控制出口值（調鏊量）所控制。自煱爐5所產生之蒸氣量係由蒸氣流動計1 2所測定。測定值則由燃燒空氣流速控制裝置16之電腦所處理。若蒸氣流速超過禰的值時，燃熵空氣之流速藉由流速調整櫬構9降低· Μ抑制焚化機内之熱產生之量，然後其可降低焚化鱸内之溫度。若蒸氣流速在檷的值以下時，燃燒空氣之流速則«由流速調整機構9堉加，Μ增加焚化爐内之热產生之Λ ·然後其會增加焚化爐内之溫度〇流速調整装置11乃基於自冷卻空氣流速控制裝置15所產生之控制出口值（調整量）所挖制。焚化爐内側之溫度僅賴燃燒空氣供應糸統之控制則嫌不足。因此，焚化爐内之進一步安定化溫度係«使用焚化爐14内之溫度計來拥定焚化爐内側之溫度、藉將覼察值進入冷卻空氣流速控制装置15 Μ藉電腦庳理•及_基於《I出值（冷卻空氣控制值）調整流速調整櫬構11之開口而確保。傳統自動加煤機型垃圾焚化爐設有二項控制裝置* 一個是經由調節主要從自動加煤檄下方供應之燃熵空氣量來控制媧爐之蒸氣量•另一個控制装置•是«由導入冷氣至焚本紙張尺度適甩中國國家標率（CNS ) Λ4规格（210Χ 297公釐〉「一 5 - I--------Γ衣------、玎------f (請先間璜背面之注意事項再填寫本頁) 305917 經濟部屮火標準局h工消費合作社印狀五、發明説明（3 ) 1 1 1 化爐之方式來控制焚化爐内之溫度〇其很 _ 控制使垃圾 1 1 I 產生之熱量起伏及焚化爐内溫度之變化達到 m 定〇該溫度 1 I 起伏係由焚化爐之狀況之改變如垃圾靥在白動加煤機上之請先 1 分佈而引起〇閲讀背 Γ 1 此外另一項難想是其很雞抑制白垃圾焚化爐產生之有 1 害物質之量達到 — 低位準例如一氧化碳 (C 0 )與氧化氣恚事項- 1 I (NOx )之產生量 > 再填 % 1 丄發明之概述本頁 1 本發明之 0 的為提供一種垃圾焚化爐之燃焼控制方法及 1 1 其装置其中〇 2 濃度在焚化爐內之起伏被抑制且烟道排放 1 1 氣中C0濃度與N0 X瀟度得以減少 > 1 訂為了達到此 S 的本發明提供播垃圾焚化爐之燃焼控 1 I 制裝置包括 1 1 | 將初次燃 m 空氣供入垃圾焚化爐之構件 1 1 將二次燃嫌空 m 供入垃圾焚化爐之構件 X 依照垃圾焚化爐之燃 m 負荷控制初次燃 m 空氣之滾速之 1 控制構件 1 | 測定垃圾焚化爐内溫度之第一測定構件 • 1 I 测定垃圾焚化爐之烟道排放氣内〇 2 m 度之第二測定構件； 1 1 澜定垃圾焚化爐之烟道排放氣内C0濃度之第三測定構件； 1 測定垃圾焚化爐之烟道排放氣内 N0 X濃度之第四測定構 1 I 件 > 及 1 1 藉由四個 m 定構件基於第一澜定構件之測定值來控制第 1 1 二燃空氣之流速之非線性控制構件〇 1 1 -6 - 本紙张尺度適用中國國家標準（CNS ) A4規格（210X297公釐） 6 經濟部t央標苹工消费合作社印况 A7 B7五、發明説明（4 ) 此外，本發明提供一棰垃圾焚化濾之燃燒控制方法，包括之步嫌為： (a) 依照在特定時間内裝入垃圾焚化爐之垃圾之热值來控制初次燃埔空氣之流速； (b) 測定垃圾焚化爐内側之潘度，及澜定烟道排放氣内〇2濃度、C0灞度及NOx濃度；及 (c) 基於步驟（b)之拥定值來控制二次燃燒空氣之流速。初次燃焼空氣可賴向前進給控制件或向後進給控制件所控制〇另外，本發明提供一棰垃圾焚化爐之燃熵控制方法，包括之步驟為： (a) 製備一初次空氣供應構件，用來將初次燃熵空氣供入垃圾焚化爐中，及一二次空氣供應構件，用來將二次燃熵空氣供入垃圾焚化爐内； (b) 依照垃圾焚化爐之燃燒負荷來控制初次燃熵空氣之流速； (c) 測定垃圾焚化爐内側之溫度及烟道排放氣内〇2濃度、（:0濃度及HOx墉度；及 (d) 基於步驟（c)之測定值»非媒性控制構件來控制二次燃堍空氣之流埋。附圓之簡單說明圈1為本發明燃堍控制裝置之具«例之概略圈。圖2為本發明燃堍控制方法之方塊圃。圔3為使用本發明横概式（fuzzy)控制件之燃熵控制方法 ---„------一' 裝------訂------^ (請先間讀背面t注意事項再填寫本頁) 本紙張尺度適用中國國家標準（CNS ) Α4規格（210X 297公釐） 7 305917 五、發明説明（5 ) 另圖之画塊方核月日305917 A7 B7 The Central Bureau of Standards of Libei: ^ Printed by the Industrial and Consumer Cooperatives V. Description of the invention (1) 1 1 t Background of the invention 1 1 I 1. Field of invention / ~, 1 I The present invention is a kind of waste incineration Furnace combustion control method and device. Please read 1 2 first. There are 挟明读 of 挟 a • back I side — I white stoker (Sto ke Γ) type waste incinerator is widely used in urban wastewater _ NOTE I Italian 1 1 treatment plant 〇 This type of incinerator's white resource saving and energy saving are the main points of borrowing · 1 re 1 The large amount of heat energy generated by the effective recovery of white garbage incinerators is often accompanied by the powerful generation of a ** Μ gas turbine power generator. This type of garbage incinerator's moving page 1 I »Panding's power generation box is to be burned or incinerated with constant heat inside the burner 1 1 produces 〇1 1 This type of white coal stoker waste incinerator uses constant efficiency incineration as Basic 1 set operation horizontal mode 〇 "t writes efficiency incineration " —. The word means that the special 1 I incineration of the amount of garbage loaded 〇In order to control the heat generation in the incinerator at a constant level of 1 1 1 m Jianlan The amount of garbage loaded into the incinerator ft within a certain time and the generation of 1 1 into the garbage The size of the heat or the amount of state corresponding to the burning load (for example, the amount of steam) and the control of the flow rate of the combustion air supplied to the automatic stoker 1 of the garbage incinerator to stabilize the state ft. M-1! Figure 13 shows __ . Fu Tong Baidong coal-filling type garbage incinerator and its combustion control 1 1 system 〇 Garbage incinerator 1 is equipped with automatic coal feeder 1 a to 1 C, garbage filling open 1 1 port 2, ash reduction port 3 discharge flue emissions m waist of incinerator P 4, chimney 6 1 and secondary air (cooling air) into P 7 > steam generation with heat exchanger 5 a | raw boiler 5 installed at the incinerator outlet 4 flue gas White is discharged there. 1 The waste incinerator 1 has a combustion air supply system that can supply cooling air 1 1 to η, and the coal is added 1 a to 1 c, and the cooling air supply system will cool the air 1 1 -4 This paper size is applicable to the country of the country Standard (CNS) A4 specification (210X 297 mm) 4 Printed by Manchu Central Standards H Industry and Consumer Capital Cooperative A7 B7 V. Description of invention (2) Gas is supplied to the incinerator. The combustion air supply system adjusts the support structure by rolling speed 9 such as a sowing board, and burns the combustion air from the fan 8 into the automatic coal feeder la to lc. The cooling air supply system relies on the flow rate adjustment mechanism 11 such as a sowing plate to direct the cooling air from the wind M 10 directly into the incinerator population 7. These flow rate adjustment mechanisms 9, 11 are controlled by the computer 17. The flow rate adjusting mechanism 9 is controlled based on the control outlet value (regulation amount) generated from the combustion air flow rate control device 16. The amount of steam generated from the furnace 5 is determined by the steam flow meter 12. The measured value is processed by the computer of the combustion air flow control device 16. If the steam flow rate exceeds your value, the flow rate of the entropy-burning air is reduced by the flow rate adjustment mechanism 9. M suppresses the amount of heat generated in the incinerator, and then it can reduce the temperature in the incinerated perch. If the steam flow rate is below the value of 椷, the flow rate of the combustion air is increased by the flow rate adjustment mechanism 9, M increases the heat generated in the incinerator Λ. Then it will increase the temperature in the incinerator. The flow rate adjustment device 11 is Based on the control outlet value (adjustment amount) generated by the self-cooling air flow rate control device 15. The temperature inside the incinerator only depends on the control of the combustion air supply system, which is insufficient. Therefore, the further stabilization temperature in the incinerator is «using the thermometer in the incinerator 14 to hold the temperature inside the incinerator, by entering the observation value into the cooling air flow rate control device 15 Μ by computer management and _ based on" I output value (cooling air control value) to adjust the flow rate to adjust the opening of the structure 11 to ensure. The traditional automatic coal-filling type waste incinerator has two control devices * One is to control the steam volume of the Wa furnace by adjusting the amount of entropy-burning air supplied mainly from below the automatic coal charging station. The other control device is «by introduction The standard of air-conditioned to burned paper is suitable for China's national standard rate (CNS) Λ4 specification (210Χ 297mm) "一 5-I -------- Γ 衣 ------ 、玎 ---- --f (please note the matters on the back of the room before filling in this page) 305917 Seal of the Industrial and Commercial Cooperation Bureau of the Ministry of Economic Affairs h Industrial Consumer Cooperatives V. Description of the invention (3) 1 1 1 The way of the furnace to control the inside of the incinerator Temperature 〇 Its very _ control the fluctuation of the heat generated by the garbage 1 1 I and the temperature change in the incinerator to reach m. The temperature 1 I fluctuation is caused by the change of the status of the incinerator, such as the garbage on the white coal loader Please first distribute 1 and cause 〇 to read Γ 1 In addition, another difficulty is that it is very chicken to suppress the generation of white garbage incinerators There are 1 amount of harmful substances reached-low level such as carbon monoxide (C 0) and oxidized gas matter-1 I (NOx) production amount> Refill% 1 Summary of invention 1 page of this invention 0 is provided A method for controlling the burning of garbage incinerators and 1 1 its device in which the fluctuation of the 02 concentration in the incinerator is suppressed and the flue emissions 1 1 the concentration of C0 and N0 X in the gas are reduced > 1 is set to achieve this S The present invention provides a combustion control device for a garbage incinerator. The I control system includes 1 1 | Components for supplying primary combustion air to the garbage incinerator 1 1 Components for supplying secondary combustion air to the garbage incinerator X According to the garbage Burning m load control of incinerator First burning m Rolling speed of air 1 Control member 1 | First measurement of temperature in garbage incinerator Components • 1 I The second measuring component for measuring 0 2 m degree in the flue gas of the waste incinerator; 1 1 The third measuring component for the C0 concentration in the flue gas of the Landing waste incinerator; 1 The determination of the waste incinerator The fourth measurement structure of the NOx concentration in the flue gas of the flue is 1 I> and 1 1 by four m fixed members based on the measured value of the first Lan Ding member to control the flow rate of the 1 1 second combustion air Linear control component 〇1 1 -6-This paper scale is applicable to the Chinese National Standard (CNS) A4 specification (210X297 mm) 6 Ministry of Economic Affairs t Central Standard Pinggong Consumer Cooperative Printing Status A7 B7 V. Invention Description (4) In addition, this The invention provides a method for controlling the combustion of waste incineration filters, including the following steps: (a) Control the flow rate of the primary combustion air according to the calorific value of the garbage loaded into the garbage incinerator within a specific time; (b) measure the garbage Pandu inside the incinerator, and O2 concentration, C0 Ba and NOx concentration in the flue gas of Landing flue; (C) based on step (b) the owner to control the value of the secondary combustion air flow rate. The primary combustion air can be controlled by the forward feed control part or the backward feed control part. In addition, the present invention provides a combustion entropy control method of a garbage incinerator, including the steps of: (a) preparing a primary air supply member, It is used to supply primary entropy-burning air into the garbage incinerator, and a secondary air supply component is used to supply secondary entropy-burning air into the garbage incinerator; (b) According to the combustion load of the garbage incinerator to control the primary The flow rate of entropy-burning air; (c) Measure the temperature inside the garbage incinerator and the 〇2 concentration in the flue gas, (: 0 concentration and HOx degree; and (d) the measured value based on step (c) »Non-Media Control component to control the flow of secondary combustion air. The simple enclosed circle 1 is a schematic circle of an example of the combustion control device of the present invention. Figure 2 is a block nursery of the combustion control method of the present invention. 3 is the combustion entropy control method using the fuzzy control part of the present invention --- "------ one 'outfit ------ order ------ ^ (please read in advance Note on the back t fill in this page) This paper scale is applicable to China National Standard (CNS) Α4 specification (210X 297 Mm) 7 305917 V. Description of the invention (5) Drawing of another picture Block square nuclear month

A7 B7 經濟部中央橾準局員工消費合作社印裝之 .明發本照依與度溫之内爐化焚示顯圖槱為！：為為為為空燒燃次圖二二之圖明之圖明燃次燃次之—空—空速流 _ 之氣之圖ES圖顥:i顯:¾顯間—董闞之示示流示道道道 lil之 U 間1¾ 烟！烟！.烟發本照依與度濃 2 ο 内氣放 kt— 闞：：之A7 B7 Printed and printed by the Staff Consumption Cooperative of the Central Bureau of Economic Affairs of the Ministry of Economic Affairs. : For the sake of being burned for the air, the picture of the second picture of the second picture, the picture of the gas of the second burning time-air-air speed flow, the picture of the gas ES picture Hao: i Xian: ¾ Xianjian-Dong Kan shows the flow of the road 1¾ smoke in the U room of lil! smoke! . The original photo of smoke depends on the degree of concentration 2 ο The internal air release kt- Kan ::

fch* I bl· SIS 發本照依與度濃 ο C 内氣放係關發本照依與度滬 X ο N 内氣放燃次二之圖明入輸U (9 份圖部示顯係闞之間速流之氣空前先之件制控式概模之明發本照依示顯功份件部部績之後明與發丨本輸 2 T; to功、件 al部有之具明別發分本值示察顯觀b) 之9( Te圖差能、能偏度溫 ο内係爐關化之焚間， \—/ I 4中份其之處 □ 出。爐度化程焚容，相中之其 (請先閱讀背面之注意事項再填寫本頁) 能、功 b!件有部具之分發值本察示觀顯之(c) 度9 濃圖 2 ο 和 2 和能 2 I v功、件 C1部有之具明別發分本值示流顳電d) 察9 觀圖之相中其之其董氣空。燒度燃程次容二相’ 之中相中之其 2 d , 和能 dl功有件具部別之分明值發察本觀示之顯度e) 濃9( X _ 容’容，之處 Ρ 出。爐度化程焚之處 Ρ 出。爐度化程焚及度瀠 ο C 之。件度制程控容燒相燃之統 z f e傳和照 el依有示具顯別，分圖值標察座觀一之為度10 濃圖濃 ο C 之件制控燒燃之明發本照依示。顯果，结圖驗標試座之一度為濃11 X圈燃行進M 速流之氣空燒燃次二。之 0< 月身印结發驗本試用之利度為濃a) X ( 0 2 N 1 及圖度之氣空 0 燃次二制控Μ 小大度濃氧據根圓示憂 i例方} 之{ 制12 控圖燒。示圖示。燃例例t« 0為S為IffliKM 程Ϊ流Ϊ程傅說流(C的(d流為之的12速12的13例速圖流圖速圖體流之流具據根據根氣之空氣燒空燃燒次燃二次制二控制 M控小M 大小度大濃度 X 濃圖略概之置裝制控燒空燒燃次初將可其統糸懕供氣空燒燃次初用採明發本系控負應之焼供統燃氣糸於空等應燒此對燃及於次，基二内統 -爐系内化制櫬焚控煤入氣加供空動氣焼自空燃之燒次爐燃初化次，焚二此圾將因垃可。入其件供，構氣統制本紙張尺度適用中國國家標準（CNS ) A4規格（2UTX 297公釐）-8 - ♦正霣五、發明説明（6 A7 B7 經濟部屮决榀準妁h工消費合作·ΐ印狀荷之狀態量*可控制由燃堍產生之熱量|另外•焚化爐之溫度產生幾乎播定的狀態作為額外效果。此外，二次燃堍空氣係藉非線性控制構件綢整以控制焚化爐内之溫度及燃燒烟道排放氣内之〇2，C0，及NOx之澹度Μ維持在特定範園內。如圖4所示，焚化爐内之溫度與二次燃燒空氣之流速間之鼷係曲線顧示出兩涸區域•·一個區域•其焚化墟内之溫度與二次燃燐空氣之滾速間具有正相翮；另一區域則在其間具有負相Μ。焚化爐内側之溫度在此二區域之界面（例如，二次燃燒空氣之流速為4000至5000Νβ3 /小時）變成最大。在正相期區域中*來自初次嫌堍區之烟道排放氣之未燃焼部份開始二次燃熵，而二次燃熵空氣之較大流速埔強二次燃燒，因此，在二次燃熵空氣之流速與焚化爐内之溫度間之相闞變成正數。因此*在來自初次燃焼階段之烟道排放氣内之未燃燒部份完全燃堍後*二次燃堍空氣之過度流速作為冷卻空氣功能，使負相闞成立。在二次燃燒空氣之流速與燃堍烟道排放氣之〇2濃度間之翮係提供正相Μ * 如圓5所示。對於C0澹度*二次燃堍空氣之滾速之減少缺少焚化爐内之氧並增加C0濃度•其被示於躅6。燃堍烟道排放氣内之NOx濃度與亡次燃燒空氣之流速具有正相闞，如圓7所示。由上述観黏•決定焚化爐内之灌度及烟道排放氣内之〇2 • C0及NOx之灞度•應用非線性控制件（例如•棋概式控制件），對應.於焚化爐内之溫度特微及烟道排故氣對上述二 (請先閱讀背面之注意事項再填寫本頁) 、τ 木紙度適用屮國國家標準（CNS ) Α4規格（210Χ 297公釐） 9 305917 \Ί B7 經濟郎屮央標準·(0Ν工消费合^r'fl印狀五、發明説明 ( 7 ) 1 1 次燃燒空氣之流速之特徽精细地調整二次嫌堍空氣之流 1 1 I 速〇因此焚化爐内之溫度與焚化爐内〇 2 之潇度均被控制 1 I 以成立穩定狀態而烟道排放氣内之 C0 壤度與 NO X澜度均請先閱 1 1 I 被控制以保持在特定值以下〇即 ,.* 垃圾焚化爐之燃堍控制讀背係使用向後 m 給控制件或向前 ϋ 給控制件進行初次 m 堍空之注 I 意 1 I 氣之流速之後續控制以使焚化爐内之溫度達到禰的控制值事項 1 1 再 1 〇另外由於〇2 C0及 N0 X之壤度與二二次嫌堍空氣之潦速線控制本策具有顯著 Μ 係應用二次燃堍空氣之流速之非性 Μ 頁 '〆 1 I 改良反應特徵因此可使〇 2 濃度 Λ C0 濃度及 N0 X濃度之精 I 1 细控制達到禰的控制值〇非線性控制係使用焚化爐内之溫 1 1 度與烟道排放 m 内之〇 Z 濃度 \ C0 m 度及 N0 X瀰度之拥定值 1 訂及使用燃焼空氣之量作為操作 ft 應用狀況方面之增加 /減 1 1 少之控制及横概式控制而實規〇横概式控制最適於二次燃 1 I 焼空氣之流速之控制〇 1 1 本發明將參照附圈說明之〇圈 1顧示本發明垃圾焚化爐之燃燒控制装置及其方法之例〇 _ 顧示自動加煤懺型垃 1 1 圾焚化爐 1 >其具有自動加蟥機1 a至1 C ，垃圾裝填開口 2 、 1 I 降灰 P 3 、焚化爐出口 4Μ 排放燃焼烟道排放氣〇靠近焚化 1 1 I 爐出 Π 4 >安裝有蒸氣產生鋦爐5 > 將燃焼烟道排放氣排至 1 1 焚化爐外側之煙囱 6及也應二二次燃堍空氣之入口 7 〇 1 1 g 垃圾裝填開 □ 2排入焚化鱸1 内之垃圾係藉初次燃焼空 1 | 氣燃 m 初次燃堍空氣係 g 商動加煤 m 1 a 至 1 c 下方向上吹 I 送 Μ 藉由乾嫌及燃 m 階段燃堍然後已燃 m 垃圾 Η 由降灰 1 1 P 3成灰排放至焚化爐之外側 >二次燃堍空氣係自入口 7供 1 1 本紙张尺度適爪中國圏謇標率（CNS ) Α4規格（210Χ 297公釐） 10 A7 B7 經滴部t央if準局U工消贽合作社印狀五、發明説明 (8 ) 1 1 I 入焚化爐内。焚化爐内之溫度及烟道排放氣内〇 2 ，C0及 1 1 | H0 X之濃度均被控制 > ，、 1 I 由垃圾之燃燒所產生之燃燒烟道排放氣係播由焚化爐出請先 ftfl 1 1 | P 4導入煙囱6内 0 在烟道排放氣被導入煙囱 6時高溫之讀背 1 烟道排放氣將热交換器 5 a 加热 Μ 使鍋爐 5内之水沸騰。產 \tQ 之注 1 1' 意 1 I 生之蒸氣被用於熱供應及動力產生〇事項 1 I 1 一 i 垃圾焚化爐 1設有二線燃堍空氣供應系統 •初次燃焕空填寫本衣氣供應 % 铳與二次嫌 m 空氣供應系統〇初次燃堍空氣供應頁 •—^ 1 I 糸統藉由流速調整櫬構 9如擄板將燃熵空氣自風圈8進給至 1 1 白動加煤懺la 至 1 c 〇二次燃燒空氣供應系統藉由流速調整 1 1 機構 11 如播板將二次燃 m 空氣直接白風扇10進給至焚化爐 1 訂之入 P 7 > 1 I 初次燃燒空氣之流速及二次燃 m 空氣之流速係藕流速調 1 1 I 整櫬構 9 11之開/ 閉控制件，根據白初次燃焼空氣控制構 I j 件 16與二次燃焼空氣控制構件 20所使用之電腦送出之控制值而設定。初次 m 嫌空氣控制糸統使用蒸氣滾動計1 2來澜 1 定在親爐 5之蒸氣流速並計算初次燃燠空氣控制構件16 1 I 之測定值，K 提供流速調整機構 9之開/ 閉控制。二次燃焼 \ 1 I 空氣控制系統使用焚化爐内之溫度感應器13偵檢焚化爐内 1 1 之溫度 » 並使用分別位. 於焚化爐出 α 4之02瀟度感應器18 1 1 、 NO X濃度感應器22及C0濃度感應器24偵檢烟道排放氣内 .丨之 0 2 、 NO X及C0之濃度且將輸出值送入焚化爐内側之潙 1 i 度計 14 〇2濃度計 19 NO X濃度計23及C0溻度計25，並將 1 1 此等測定值送入二次燃 m 空氣控制構件 20以計算並處理· 1 1 木紙悵尺度適用中國國家標準（CNS )八4規格（210X297公釐） A7 B7 經濟部屮央標苹妁h工消t合作社印狀五、發明説明 ( 9 ) 1 1 因此進行流速綢整構件1 1之開/閉控制。 1 1 I 以下分別參照圏 2及匪3之控制方塊圈來說明初次 m 堍空 1 氣控制構件 16及二次燃燒空氣控制構件 20之控制糸統。圖讀先1 2顧示- •控制系統其结合用來穩定蒸氣流速之初次燃焕 η- 1 空氣控制構件與使用全範園之坩 /減控制之二次燃熵空之-1 注氣控制構件 Μ 者使焚化爐内之溫度及焚化爐内之〇 2 溫度 ψ 1 項 1 再乂得播定並抑制白焚化爐排出之烟道排放氣内之 N0 X壤 4 本f 度與 C0 濃度〇圈 3顬示具有相同目的之二次燃焼空氣控制 I I _X 1 構件採用 m 概式控制系統。 1 1 初次燃燒空氣控制構件將參照 _ 2說明之c >初次嫌堍空 1 1 氣之流速係基於蒸氣之流速在欏的蒸氣流速與獲 i 垃圾焚 1 訂化爐内之燃 m 處理 A2之蒸氣流速間之偏差在初次燃熵空 1 I 氣流速控制段 A1 使用向前進姶或向後 m 給法予以成比例及 1 I 整合控制〇蒸氣流速係基於初次燃熵空氣控制之輸出值_ 1 ! ·*'」、調整初次燃燒空氣逭姶之流速至垃圾焚化爐之燃 m 處理A2 而控制〇在初次燃嫌空氣 m 速控制段A 1 中初次燃燒空氣控制 1 (F1 ) 之輸出值係使用下面等式計算 1 1 I F1 = =(100/PB )> < ( 1 - 卜 1 /Τ ί s) X (STMs e t — STMn 0 W ) ( 1 ) 1 1 其中 F1 為初次 m 燒空’氣控制之 Μ 出值 STMs e t 為蒸氣流 1 速之檷的值 STMn 0 V 為覼察蒸氣流速 s為L a p 1 a c e 蓮算符 .1 〇 PB為比例益而 T i 為整合增益二者均為調整參數〇 1 ] 流速調整櫬構 9之開啟係基於初次燃堍空氣控制（F1 >之 1 1 輸出值調螫 t 控制供應至垃圾焚化爐之初次燃燒空氣0 1 1 本紙张尺度遴用屮國國家標率（CNS ) A4規格（210X 297公釐）經漓部中夾標準局Μ工消资合作社印鉍 305917 A7 B7 五、發明説明（l〇 ) 在二次燃焼空氣控制構件20中*狀況方面之《加/減少控制係基於在垃圾焚化爐之燃燒處理A2所澜定之焚化爐内之溫度與焚化爐内檷的溫度間之焚化爐内之溫度懦差•基於在焚化爐出口之02瀰度與在焚化爐出口之〇2濃度之設定值間之比較及基於在C0濃度與C0濃度之設定值間之比較，在二次燃燒空氣控制段A3進行。然後*二次燃熵空氣控制之輸出值被用來控制垃圾焚化爐之燃堍處理A2之焚化爐内之溫度，及在焚化爐出口之〇2，N0)(及C0之濃度。以下將詳述二次嫌堍空氣控制段A3之控制方法。圈2之例顯示一吠況方面之坩加/減少控制。在說明前，先參照圔4及圖7說明焚化爐内之溫度· 〇z禳度，C0溻度及Ν〇Χ» 度之關係及二次燃堍空氣之流速。如_4所示，二次燃燒空氣提供二次燃堍區，（其作為二次燃熵空氣之作用），及冷卻區•（其作為冷卻空氣之作用 )。二次燃燒區為4000Ν·3 /小時Μ下之區•二次燃焼在該處起動Μ增加焚化爐内之溫度。此外，在該區*其中二次燃堍空氣之流速之埔加在大約4000至5000Ν·3 /小時的範園内達到焚化爐内溫度if加之最大值。當二次燃燒空氣增加時•例如，達到5 0 0 0 N 3 /小時或K上·出現一焚化爐内溫度減少之冷卻區。如圖5所示•在烟道排放氣内之02澹度與二次燃焼空氣之潦速間之闞係提供一正相關於其間，其中二次燃燒空氣之滾速之增加會增加烟道排放氣内之〇2濃度。 _如圖6所示•在烟道排放氣内之C0澹廑與二次嫌！堍空氣本紙張尺度適用中國國家標隼（CNS ) Λ4規格（210X297公釐） -13 - I ^--------{ ,4-- (請尤閱讀背面之注意事項再填舄本頁) 、τfch * I bl · SIS issued according to the degree of compliance ο C internal gas release system closed issued according to the degree of compliance X Shanghai ο N internal gas discharge second figure shows the input and input U (9 pictures show the system The fast-moving gas between the Kan and the unprecedented model of the control system of the unprecedented version of the original model is shown according to the performance of the part and the part of the department, and it is published and lost 2 T; Don't send out the cost value and observe the b) of 9 (Te graph difference energy, energy deflection temperature ο inside the furnace of the furnace shut down, \-/ I 4 in its place □ out. Burning capacity, the best of them (please read the precautions on the back before filling in this page) Energy, function b! The distribution value of the tools and accessories is shown in (c) degree 9 (Figure 2) and 2 and Neng 2 I v work, part C1 has a specific value, and the current value is shown. Temporary electricity d) Check the view of the 9 images in the image. The second phase of the two phases of the burning capacity and sub-capacity's middle phase, and the distinct value of the energy dl function and component parts. Observe the apparent e of the visual display e) Concentration 9 (X _ 容容, where Ρ The place where the furnace temperature is burnt is P. The furnace temperature is burnt and the temperature is C. The process of controlling the volume-burning and phase combustion of the piece process is marked according to the display, and the value is divided by the graph. Observation and observation of one is the degree of 10 rich map thick ο C pieces of the system to control the burning of the bright hair according to the instructions. The results show that the final test of the chart is a thick 11 X circle burning traveling M fast flow of gas Air burns second. The 0 < lunar body prints the test sample and the trial profit is rich a) X (0 2 N 1 and the figure of air and air 0. Burning second system control Μ small and large concentration of oxygen basis The circle shows an example of the control of {the 12 control chart burning. Show the picture. The example of burning t «0 is S for IffliKM process Ϊ flow Ϊ process Fu said flow (C (d flow is 12 speed 12 13 cases of speed chart flow chart speed chart body flow flow tool according to the air of the root gas burning air combustion secondary combustion secondary system two control M control small M size large concentration X. The outline of the installation of the control system is to control the burning of the air at the beginning of the combustion. The gas will be burned at the beginning of the system, and the gas will be burned at the beginning. This pair of combustion is inferior to the secondary combustion system, which is based on the internal combustion of the second internal system and the furnace system. For the supply of the paper, the paper standard of the gas control system is applicable to the Chinese National Standard (CNS) A4 specification (2UTX 297mm) -8-♦ Zheng five V. Description of invention (6 A7 B7 Ministry of Economic Affairs is determined by the industry and consumer cooperation · The amount of state of the imprinted charge * can control the heat generated by the burning bar | In addition • The temperature of the incinerator produces a nearly fixed state as an additional effect. In addition, the secondary burning barn air is woven by a nonlinear control member to Control the temperature in the incinerator and the O2, C0, and NOx in the exhaust gas of the combustion flue M. Maintain it within a specific range. As shown in Figure 4, the temperature in the incinerator and the flow rate of the secondary combustion air The curve of the line between the two shows the area of two streams • one area • its burning ruins There is a positive phase between the temperature of the temperature and the rolling speed of the secondary combustion air; the other area has a negative phase M in between. The temperature inside the incinerator is at the interface between these two areas (for example, the flow rate of the secondary combustion air is 4000 Up to 5000Νβ3 / hour) becomes the maximum. In the positive phase area * the unburned portion of the flue gas exhausted from the first suspected area starts secondary combustion entropy, and the larger flow rate of the secondary combustion entropy air is strong secondary Combustion, therefore, the phase between the flow rate of secondary combustion entropy air and the temperature in the incinerator becomes positive. Therefore * after the complete combustion of the unburned part of the flue exhaust gas from the first firing stage * The excessive flow rate of the secondary combustion air serves as a cooling air function, which makes the negative phase of the threshold. A positive phase M * is provided between the flow rate of the secondary combustion air and the 02 concentration of the flue gas from the combustion flue, as shown in circle 5. For the reduction of C0 * the rolling speed of the secondary combustion air, the oxygen in the incinerator is lacking and the C0 concentration is increased. It is shown in Figure 6. The NOx concentration in the flue gas of the combustion flue is positively correlated with the velocity of the combustion air of the secondary combustion, as shown in circle 7. Based on the above-mentioned viscosity • Determine the degree of infusion in the incinerator and the flue gas in the flue gas 〇2 • C0 and NOx degree of application • Non-linear control components (for example • chess general control components), corresponding. In the incinerator The temperature is extremely low and the flue gas is exhausted. For the above two (please read the precautions on the back before filling out this page), τ wood paper degree is applicable to the National Standard (CNS) Α4 specification (210Χ 297 mm) 9 305917 \ Ί B7 Economic Langyango Standard · (0Ν 工氣合 ^ r'flPrinted form V. Description of the invention (7) 1 The special emblem of the flow rate of the primary combustion air finely adjusts the flow of secondary suspected air 1 1 I speed. Therefore Both the temperature in the incinerator and the degree of 〇2 in the incinerator are controlled 1 I to establish a stable state and the C0 soil and NO X in the flue gas are read first 1 1 I is controlled to maintain at Below a certain value, that is, * The combustion control reading back of the waste incinerator is to use the backward m for the control part or the forward ϋ for the control part for the first time. Note 1 I 1 Subsequent control of the flow rate of the gas so that the temperature in the incinerator reaches your control value 1 1 1 1 10 In addition, due to the erosion of 〇2 C0 and N0 X and the speed of the second and second suspected air The linear control method has a significant M system. It uses the non-linearity of the secondary combustion air flow rate. Page 1 I improved the reaction characteristics. Therefore, the fine control of the concentration of 〇2 concentration Λ C0 concentration and N0 X concentration can be achieved. Control value 〇 Non-linear control is to use the temperature in the incinerator 1 1 degree and the flue gas emission m within the 〇Z concentration \ C0 m degree and N0 X degree of tolerance of the agreed value 1 set and use the amount of burning air as the operation ft Increase / decrease in application status 1 1 Less control and horizontal control and actual control ○ Horizontal control is most suitable for secondary combustion 1 I Control of air flow rate 〇1 1 The present invention will refer to Circle description ○ Circle 1 shows an example of the combustion control device and method of the garbage incinerator of the present invention. _Gushe automatic coal-filling type garbage 1 1 garbage incinerator 1 > it has an automatic loading machine 1 a to 1 C ， Gas filling opening 2, 1 I Ash reduction P 3, Incinerator outlet 4 Μ Emission flue gas exhaust 〇 Close to incineration 1 1 I furnace exit Π 4 > Installed steam generating furnace 5 > Combustion flue gas exhaust The chimney 6 discharged to the outside of the incinerator 1 and the inlet of the secondary combustion air 7 〇1 1 g Garbage filling □ 2 The garbage discharged into the incineration perch 1 is emptied by primary combustion 1 | gas-fired m The first combustion of the air system g commercial coal replenishment m 1 a to 1 c is blown upwards I to send Μ by burning and burning m stage combustion and then burned m garbage Η from ash reduction 1 1 P 3 ash into the incinerator Outer side> The secondary combustion air system is supplied from the inlet 7 1 1 The paper size is suitable for the Chinese standard rate (CNS) Α4 specification (210Χ 297 mm) 10 A7 B7 T if the central portion Bureau registration cancellation Zhi cooperative station U-shaped plate V. Description of the Invention (8) 1 1 I into the incinerators. The temperature in the incinerator and the flue gas emission 〇2, C0 and 1 1 | H0 X concentration are controlled > ,, 1 I The combustion flue gas produced by the combustion of garbage is broadcast by the incinerator Please first introduce ftfl 1 1 | P 4 into the chimney 6 0 Read the high temperature when the flue gas is introduced into the chimney 6 1 The flue gas will heat the heat exchanger 5 a to make the water in the boiler 5 boil. Production \ tQ's note 1 1 'meaning 1 I The steam produced is used for heat supply and power generation. 1 I 1 1 i Waste incinerator 1 is equipped with a second-line combustion air supply system. Air supply% Bronze and secondary air supply system. Air supply page for the first combustion • ^ 1 I The system adjusts the structure by the flow rate 9 such as the capillary board to feed the entropy combustion air from the wind coil 8 to 1 1 white Dynamic coal feed la to 1 c. The secondary combustion air supply system is adjusted by the flow rate 1 1 mechanism 11 such as a broadcast board to feed the secondary combustion m air directly to the white incinerator 10 to the incinerator 1 The prescribed input P 7 > 1 I The flow rate of the primary combustion air and the secondary combustion m The flow rate of the air is adjusted by the flow rate of the lotus 1 1 I I adjust the structure 9 11 on / off control part, according to the white primary combustion air control structure I j 16 and the secondary combustion air control The control value sent by the computer used by the component 20 is set. For the first time, the air control system uses a steam roll gauge 1 2 to 1 to set the steam flow rate in the pro-furnace 5 and calculate the measured value of the first combustion air control member 16 1 I. K provides the on / off control of the flow rate adjustment mechanism 9 . Secondary Ignition \ 1 I The air control system uses a temperature sensor 13 in the incinerator to detect the temperature of 1 1 in the incinerator »and uses a separate position. The alpha 4 of 02 inductance sensor 18 1 1, NO The X concentration sensor 22 and the C0 concentration sensor 24 detect the flue gas exhaust gas. 丨 0 2, NO X and C0 concentration and send the output value to the inside of the incinerator 1 1 degree meter 14 〇2 concentration meter 19 NO X concentration meter 23 and C0 polymeter 25, and send these 1 1 measurement values to the secondary combustion m air control unit 20 for calculation and processing. 1 1 The scale of wooden paper is applicable to China National Standard (CNS) VIII 4 Specifications (210X297mm) A7 B7 The Ministry of Economic Affairs, Central Standards, Ping Bing, Gong Xiaot, Cooperative Cooperative Printed Form V. Description of the Invention (9) 1 1 Therefore, the opening / closing control of the flow rate shaping member 11 is performed. 1 1 I The following describes the control system of the first m control system 1 and the second combustion air control component 20 with reference to the control block circles of circle 2 and band 3, respectively. Picture reading first 1 2 Gu Shi-• The control system which is used to stabilize the initial combustion of the steam flow rate η-1 air control components and the use of full range of crucible / reduction control of the secondary combustion entropy air-1 injection control The component M makes the temperature in the incinerator and the temperature 2 in the incinerator ψ 1 item 1 can be determined and suppressed in the flue gas exhausted from the white incinerator N0 X soil 4 this f degree and C0 concentration 〇 Circle 3 shows that the secondary combustion air control II _X 1 component with the same purpose adopts m general control system. 1 1 The primary combustion air control component will refer to the description of _ 2 c > The first time is empty 1 1 The flow rate of the gas is based on the flow rate of the steam. The flow rate of the steam in the 椤 is obtained and the waste is burned. 1 The combustion in the customized furnace m Treatment A2 The deviation of the steam flow rate in the first combustion entropy is empty. 1 I The gas flow rate control section A1 is proportional to the forward or backward m feed method and 1 I integrated control. The steam flow rate is based on the output value of the primary combustion entropy air control _ 1 ! * '", Adjust the flow rate of the primary combustion air to the combustion m2 of the waste incinerator and control A2. The output value of the primary combustion air control 1 (F1) in the primary combustion air m speed control section A 1 Use the following equation to calculate 1 1 I F1 = = (100 / PB) > < (1-卜 1 / Τ ί s) X (STMs et — STMn 0 W) (1) 1 1 where F1 is the first m burn The M output value STMs et of the air control is the value of the steam flow 1 speed STMn 0 V is the steam flow s is the Lap 1 ace lotus operator. 1 PB is the proportional benefit and T i is the integration gain. Both are adjustment parameters. 1] The opening of the flow rate adjustment structure 9 is based on the first combustion air control (F1 > No. 1 1 The output value is adjusted to control the initial combustion air supplied to the waste incinerator. 0 1 1 The size of the paper is selected by the National Standard Rate (CNS) A4 specification (210X 297 mm). Industrial and Consumer Cooperation Co., Ltd. printed bismuth 305917 A7 B7 V. Description of the invention (l〇) The "addition / reduction control is based on the combustion treatment in the waste incinerator A2 incineration furnace in the secondary combustion air control member 20 * status" The temperature difference in the incinerator between the temperature inside and the temperature in the incinerator is based on the comparison between the 02 degree at the outlet of the incinerator and the set value of the 02 concentration at the outlet of the incinerator and based on the The comparison between the set values of C0 concentration is performed in the secondary combustion air control section A3. Then the output value of the secondary combustion entropy air control is used to control the temperature in the incinerator of the combustion incinerator of the waste incinerator A2 , And the concentration of 02, N0) (and C0) at the outlet of the incinerator. The control method of the secondary suspected air control section A3 will be described in detail below. The example of circle 2 shows a crucible increase / decrease control in terms of bark conditions. Before the description, the relationship between the temperature in the incinerator, the temperature, the temperature and the temperature in the incinerator, the temperature in the incinerator, and the flow rate of the secondary combustion air will be described with reference to FIG. 4 and FIG. 7 first. As shown in _4, the secondary combustion air provides the secondary combustion zone (which acts as secondary combustion entropy air), and the cooling zone • (which acts as cooling air). The secondary combustion zone is a zone under 4000N · 3 / hour Μ. Secondary combustion is started at this place to increase the temperature in the incinerator. In addition, in this area *, the flow rate of secondary combustion air reaches a maximum value of if plus in the incinerator within a range of approximately 4000 to 5000N · 3 / hour. When the secondary combustion air increases • For example, reaching 5000 N 3 / hour or K • A cooling zone in which the temperature in the incinerator is reduced appears. As shown in Figure 5 • The relationship between the 02 degrees in the flue gas and the speed of the secondary combustion air provides a positive correlation between them, where the increase in the speed of the secondary combustion air will increase the flue gas emissions O2 concentration in the air. _As shown in Figure 6 • C0 in the flue gas exhausted and secondary suspected!堍 Air This paper scale is applicable to the Chinese National Standard Falcon (CNS) Λ4 specification (210X297 mm) -13-I ^ -------- {, 4-- (Please read the precautions on the back and fill in this copy Page), τ

J 305917 A7 B7 五、發明説明（U ) 之流速間之鼷係提供一負相Μ於其間，其中二次燃燒空氣之流速之埔加會減少烟道排放氣内之co禳度。如圖7所示*在烟道排放氣内之NOx瀰度與二次燃燒空氣之流速間之闥係提供一正相闞*其中二次燃熵空氣之滾速之增加會埔加烟道排放氣内之Η Ox濃度。利用此等琨象，二次燃燒空氣之流速在二次燃熵空氣流速控制段A3受控制。二次燃燒空氣流速控制段A3基於特定偏差值決定焚化爐内溫度偏差之信《，並證實是否二次燃燒空氣之流速在燃堍匾（例如*低限值被設定在4000H·3 / 小時Μ下>*在邊界區（例如•低限值被設定在4000至5000 Nm3 /小時之範園）或在冷卻區（例如 > 低限值被設定在 5000Nb3 /小時或W上）。由上述指定二個狀況之判断，二次燃燒空氣流速控制段3進行狀況方面之控制以增加/滅少二次燃焼空氣之流速。當提供是否NOx禳度及C0灞度超》各上限之證實及當NOx 湄度超過上限時，二次燃燒空氣之流速係»特定流速而減少。當C0濃度超過上限時，二次燃焼空氣之流速係»特定流速而增加。因此，NOx溻度及C0灞度之增加受控制Μ抑制其之增加。二次燃堍空氣之涑速在二次燃熵空氣潦速控制段A3之控制方法將參照表1詳细提供如下。二次燃焼空氣之流速係依照狀況（1)至（10)按序計算及偵檢。當其结果可滿足狀況（8)至（10)時*由筋頭符號（>)所示之控制作用被逐次進行。 -14 - I ,-----{裝 _------訂------f .外 (請先閱讀背面之注意事項再填寫本頁) 經濟部中央標苹妁：只工消"合作社印焚本紙张尺度適用巾國國家標準（CNS ) Λ4規格（210X 297公釐） A7 B7 經满部中央標準局·Μ工消費合作社印¾J 305917 A7 B7 Fifth, the description of the invention (U) between the flow rate is to provide a negative phase M in between, in which the secondary combustion air flow rate of Po plus will reduce the flue gas in the flue gas. As shown in Figure 7 * The intercalation between the NOx density in the flue gas and the flow rate of the secondary combustion air provides a positive phase. * The increase in the speed of the secondary combustion entropy air will increase the flue gas emissions. The concentration of H Ox in the gas. Using these images, the secondary combustion air flow rate is controlled in the secondary combustion entropy air flow rate control section A3. The secondary combustion air flow rate control section A3 determines the temperature deviation in the incinerator based on the specific deviation value, and confirms whether the flow rate of the secondary combustion air is in the combustion plaque (for example, the lower limit is set at 4000H · 3 / hour M Lower > * In the boundary area (for example, • the lower limit is set at 4000 to 5000 Nm3 / hour) or in the cooling zone (for example, > the lower limit is set at 5000Nb3 / hour or W). Specify the judgment of two conditions, and the secondary combustion air flow rate control section 3 performs status control to increase / decrease the flow rate of secondary combustion air. When providing whether the upper limit of NOx and C0 is exceeded When NOx Mae exceeds the upper limit, the flow rate of secondary combustion air decreases with the »specific flow rate. When the C0 concentration exceeds the upper limit, the flow rate of the secondary combustion air increases with the» specific flow rate. Therefore, the NOx and C0 degrees The increase is controlled by M to suppress its increase. The control method of the secondary combustion air speed in the secondary combustion entropy air speed control section A3 will be provided in detail with reference to Table 1. The flow rate of the secondary combustion air is based on the situation ( 1) to (10 ) Calculate and detect in sequence. When the result can meet the conditions (8) to (10) * The control function shown by the tendon symbol (>) is carried out one by one. -14-I, ----- {装 _------ 定 ------ f. Outside (please read the precautions on the back before filling out this page) Ministry of Economic Affairs Central Standard Pingwen: only work to eliminate " cooperative printed and burned paper standards Applicable towel national standard (CNS) Λ4 specification (210X 297mm) A7 B7 Printed by Manchu Central Standards Bureau · M Industry Consumer Cooperative ¾

五、發明説明（12 ) 1 1 表1 (控制二次燃燒空氣之流速之方法） 1 1 (1 )焚化爐内之溫度偏差 — 藉特定流速減少二次燃焼 1 為負 t 而二次燃 m 空空氣之流速 (坩加焚化爐内 I 氣之流速在冷卻區内之溫度 ) 請 1 二次燃熵先 1 (2)焚化内之溫度偏差賴特定流速增加閱 I a I 為正而二次燃燒空空氣之流速 (滅少焚化爐内背 - 之注- 意項- 填本頁 -·· 1 氣之流速在冷卻區内之溫度 ) 1 (3)焚化值内之溫度偏差賴特定流速增加 __‘ . |I|M> —次燃璘 1 1 為負而二次燃熵空空氣之流速 (增加焚化爐内 1 氣之流速在燃燒區内之溫度 ) (4 )焚化爐内之溫度鶄差 -> 藉特定流速減少二次燃堍 -1'、 | 為正而二次燃焼空空氣之流速 (減少焚化爐内 I | 氣之流速在燃 m 區内之溫度 ) I (5)焚化爐内之溫度偏差藉特定 m 速減少二次燃堍 I 為負而二次燃堍空空氣之流速，（氧灞度高* I I 氣之流埋在邊界區 > NO X澹度滅少*而C 〇濃度未 I 訂且氧濃度在特定值或增加 ) ) I 上 I (6)焚化爐内之溫度偏差 U 特定流速增加二次燃堍 I ( 為正而二次 m m 空空氣之流速 (使用冷卻區減 I I 氣之流速在邊界區 9 少焚化爐内之溫度）° I 且氧濃度在特定值 Η | 下 I (7)焚化爐內之溢度鵂差保持 —* 次燃燐空氣之流速 i I 為負而二次燃堍空 (因為酋二次燃焼空氣之流 I 氣之流埋在邊界區速增加及當其減少時•焚 I I 化爐内之溫度減少） I I (8)氧濃度超遇上設限 -> η 特定流速壻加二次燃堍 I I 空氣之流速 (K增加氧濂度） I (9) NO X濃度在下上設限 -> 賴特定流速減少二次燃熵 I Μ 下空氣之流速 (Μ減少N 0 X澹 I I 度 ) I ί (10)C0澥度超過上設限 -> Η 特定流速埔加二次燃堍 I 空氣之流速 (Κ滅少C 0濃度） I 本紙張尺度適用中國國家標準（CNS ) A4現格（2丨OX29?公釐） -15 - SQ5917 A7 B7 五、發明説明（13 ) (請先閱請t面之注意事項再填寫本頁) 堉加/滅少二次嫌[燒空氣之流速之值（或毎循環埘加的流速或減少的流速）可分別於（1)至（6)針對焚化爐内之溫度偏差來設定，於（8)針對氧濃度設定、於（9)針對NOx瀰度上設限及（1 0 ) C 0濃度來設定。（7 )_示一控制過程•供維持二次燃焼空氣當時之流速。對二次燃焼空氣之控制段之計算《I程（二次燃焼空氣控制構件20)將基於圈12之流程團來說明。控制糸統之計算值在恒定循瑁被取樣，而二次燃燒空氣之流速基於計算值予Κ控制。圓12(a)至12(d)為流程_ *其中具體地列明表 1所示之二次燃堍空氣之控制方法。流程圈顯示表1之控制方法（1)至（1 0 )。經濟部中史標苹局·只工消費合作社印策圖12U)顯示一表1所示之控制方法（1)至（7)之控制方法，圖1 2 ( b )為一控制方法（8 )之控制方法，圓1 2 ( c )為一控制方法（9)之控制方法，及_12(d)為一控制方法（10)之控制方法。在圈12(a)至12(d)中•控制係從start 1，start 2 · start 3及start 4開始。其係基於流程圈來判斷是舌狀況令人滿意。調整參數zl至z4之值係依二次燃燒空氣之流速而最後決定。根據Z1至Z4之值二次燃焼空氣流速之先前之輸出值（F2(K1)·可計算出二次嫌堍空氣流速目前之輸出（F2 (k))。 P2 (k) = F2 (k-1) + zl + z2+ z3+ z4 (2) 綢整參數zl至z4係基於_12(a)至12(d)之流程_計算。在圈12(a)至12(d)中* Te為焚化爐内之溫度偏差，F2now 為二次燃堍空氣之潦速，〇2為氧瀟度，N〇X為ΝΟχΛ度，C0 本紙張尺度適用中國國家標率（CNS ) A4规格（210X297公釐> -1 6 - A7 B7 五、發明説明（U ) 為CO濃度。（^及（：2為二次燃燒空氣®速之調整參數Μ辨識燃焼區、邊界匾及冷卻區。0X1為氧濃度之調整參數以辨識特定值或Μ上，成低於其值。0X1為一調整參數以辨識氧灞度之上設限。0X2為一調整參數Μ辨繊氧灞度之下設限。NOxl為一調整參數Μ辨識NOx濃度之上設限。C0為調整參數Μ辨識C0濃度之上設限。yl至y]0為調整參數Μ提供二次燃堍空氣之堉加的流迪及滅少的流速。琨說明圖12(a)。在步驟S1中·焚化爐内之溫度偏差Te 係根據Te< 0之控制狀況來判斷。在Te< 0之條件滿足之情況下，步驟S2即可確認。在步驟S2中•當二次燃焼空氣之流速可滿足F2n〇W 2¾之控制狀況時，調整參數zl變成yl° 當F2now2Cz之控制狀況未被滿足時，F2now会C,之控制狀況即可在步驟S3確認。在滿足FZnowShi控制狀況之悄況下，調整參數zl變成y3。在不滿足FSnowSCii控制狀況之情況下•讕整參數zl變成y7。經濟部屮央標苹趵以工消费合作社印狀 nn nn ml ivn n^i 、mfl n J 、 (請先閱讀背面^-注意事^再填寫本頁) 在Te<0在步驟S1未滿足之情況下，步驟S4即可確認當滿足步驟S4之控制狀況F2now2C2時，調整參數zl變成y2 。當未滿足步驟S4之控制狀況？2^<^2(：2時，判斷步驟S5 即可確認。在步嫌S5中•判衡FZnowSh之控制狀況。當滿足FZnowSh之控制狀況時，調整參數zl變成y4。當未滿足FZnowSh之控制狀況時*判断步8IS6即可確18。在步驟S6中，判斷02g〇xl之控制狀況。當滿足〇2^〇xl之控制狀況時•調整參數zl變成y5。當未滿足02S0xl之控制狀況時•調整參數zl變成y6。本紙张义度適用中國國家標準（〇奶）八4規格（2丨0/ 297公着） ~ΓΙ —1 7 - 經濟部中央標準局Μ工消費合作社印裝 A7 B7 五、發明説明（15 ) 圈12(b)為一流程圈，其例示根據氣瀆度之大小控制二次燃馍空氣之流速。其係»〇2<〇x2之控制狀況判断是否 02之測定之氧濃度低於0x2氧澹度之低設限。當滿足控制狀況時*調整參數ζ2變成y8。當未滿足控制狀況時，調整參數z2變成0。圈12(c)為一流程_ *其例示根據NOx濃度之大小控制二次燃焼空氣之潦速。其係賴N0x>N0xl之控制狀況判斷是否N(U之測定NOx濃度超過HOxl之ΝΟχΛ度之上設限。當滿足控制狀況時，調整參數ζ 3變成y9。酋未滿足控制狀況時，調整參數z3變成0。圖12(d)為一流程圈，其例示二次燃焼空氣之潦速基於 C0濃度之控制。其係藉C0>C01之狀況判麵是否C0之澜定 C0瀰度大於C01之C0濃度之上設限。當滿足控制狀況時，調整參數24變成ylO。當未滿足控制狀況畤•調整參數z4 變成0。調整參數zl至z4*其係基於_12之流程B测定·被取代至等式（2)以決定二次燃燒空氣流速之_出之值（F2(k))。參照圓3說明控制塊。二次燃燒空氣溁速控制A3為横概式控制。棋概式控制之規定被示於表2。本紙張尺度適用中國國家標隼（CNS ) Α4规格（210X297公釐） ^^^1 ^^^^1 ^^^^1 n^i ^J^1.^1 ΐ ， --Λ"、- (請先閲讀背面"·注意Ϋ項再填寫本頁) -18- B7五、發明説明（1β ) 表氣空燒燃次法方之制控式概横之速差空内僱燒區度燃卻溫次冷之二在内而速爐，流化負之焚為氣 -> 差空内餳堍區度燃卻溫次冷之二在内而速爐-潦化正之焚為氣 -> 差空内偏燒匾度燃燒溜次燃之二在內而速爐，流化負之焚為氣 t 差空内偏堍區度燃熵溫次燃之二在内而速爐，流化正之焚為氣差空，偏燒區度燃界溫次邊之二在高內而速度爐，流灌化正之氧焚為氣且 t 差空-偏燒區度燃界溫次邊之二為高内而速度爐-流澹化正之氧焚為氣且 -> 經滴郎中央標挲妁員工消费合作社印製差空餳堍度燃匾溫次界之二邊内而在爐，量化負之焚為氣 (8) 氧濃度變成在下設限以下 (9) NOx湄度超過上設限 (10) C0濃度超遇上設限 t t 減之次接(J>增之次接(J»之次接之内二更少度之内二更少}之内二更少>之内二遶氣爐當成減溫氣爐當成減度氣爐當成減度氣爐當成少}氣爐當成少焚空化且變值之空化且變值溫空化且變值溫空化且變減度空化且變減少焼焚時速其内燒焚時速其之燐焚時速其之燒焚時速值溫熵焚時速值減燃當少潦，爐燃酋少流-内燃當少流，内燃當少流其之燃當少流其區次-減之時化次，減之時爐次，滅之時爐次·滅之，内次，減之，燒} 二速差氣.區焚二速差氣區化二準差氣區化二速差氣時爐二速差氣時燃度算流偏空界加算流韻空界焚算流偏空界焚算流鵂空區化算流偏空區次溫算流餳空區卻}持速燃減算流僱算潦儀算流鵂計之度焼邊增計之度焼邊少計之度焼邊加計之度燒界焚計之度燒界二之計之度燐界冷度維流次其計之下計之上計之上少溫燃邊減之次於V. Description of the invention (12) 1 1 Table 1 (Method of controlling the flow rate of secondary combustion air) 1 1 (1) Temperature deviation in the incinerator-reduce the secondary combustion by a specific flow rate 1 is negative t and the secondary combustion m The flow rate of air (the flow rate of I gas in the crucible and incinerator in the cooling zone) Please 1 the second combustion entropy first 1 (2) The temperature deviation in the incineration depends on the specific flow rate increase. I a I is positive and the second Combustion air flow rate (remove the back of the incinerator-Note-Significance-fill this page-1 · The temperature of the gas flow rate in the cooling zone) 1 (3) The temperature deviation within the incineration value depends on the specific flow rate increase __ '. | I | M > —The secondary combustion fuel 1 1 is negative and the secondary combustion entropy air flow rate (increasing the temperature of the 1 gas flow rate in the incinerator in the combustion zone) (4) The temperature in the incinerator鶄差-> Reduce the secondary combustion -1 'by a specific flow rate, | is positive and the secondary combustion is empty Flow rate (reducing the temperature of the I in the incinerator | the temperature of the gas flow rate in the combustion zone) I (5) The temperature deviation in the incinerator is reduced by the specific m speed of the secondary combustion I Flow rate, (high oxygen concentration * II gas flow buried in the boundary area> NO X detonation less * and C 〇 concentration is not set and oxygen concentration is at a specific value or increased)) I on I (6) Incinerator The temperature deviation U within the specific flow rate increases the secondary combustion I (the positive and the secondary mm air flow rate (use the cooling zone minus II gas flow rate in the boundary zone 9 less the temperature in the incinerator) ° I and the oxygen concentration is Specific value Η | Lower I (7) The overflow difference in the incinerator is maintained— * The flow rate of the secondary combustion air i i is negative and the secondary combustion is empty (because the chief secondary combustion air flow I gas flow buried In the boundary zone, the speed increases and when it decreases • the temperature in the incinerator II decreases ) II (8) The oxygen concentration exceeds the upper limit- > η specific flow rate plus secondary combustion II The air flow rate (K increases the oxygen pressure) I (9) NO X concentration is set at the upper and lower limits-> Lai The specific flow rate reduces the air flow rate at the secondary combustion entropy I Μ (Μ decreases N 0 X 澹 II degrees) I ί (10) The C0 temperature exceeds the upper limit-> Η The specific flow rate plus the secondary combustion I air Flow rate (K 0 less C 0 concentration) I This paper scale is applicable to the Chinese national standard (CNS) A4 current grid (2 丨 OX29? Mm) -15-SQ5917 A7 B7 5. Invention description (13) (please read first please t Please pay attention to the above page and fill in this page). Addition / elimination of secondary suspicion [the value of the flow rate of the burned air (or the added or reduced flow rate of each cycle) can be separately targeted from (1) to (6) for the incinerator The temperature deviation within is set in (8) for the oxygen concentration, (9) for the upper limit of NOx density and (1 0) C 0 concentration. (7) _ Show a control process • To maintain the current flow rate of secondary combustion air. The calculation of the control section of the secondary combustion air "I pass (secondary combustion air control component 20) will be explained based on the circle 12 circle. The calculated value of the control system is sampled at a constant cycle, and the flow rate of the secondary combustion air is controlled by K based on the calculated value. Circles 12 (a) to 12 (d) are the process _ * which specifically lists the control method of secondary combustion air shown in Table 1. The flow circle shows the control methods (1) to (1 0) of Table 1. Figure 12U) of the Ministry of Economic Affairs, China Bureau of Standards, and the Consumer Labor Cooperatives (Figure 12U) shows a control method shown in Table 1 (1) to (7), and Figure 1 2 (b) shows a control method (8). Method, circle 12 (c) is a control method (9), and _12 (d) is a control method (10). In circles 12 (a) to 12 (d) • The control system starts from start 1, start 2 · start 3 and start 4. It is based on the process circle to determine whether the tongue is satisfactory. The values of the adjustment parameters zl to z4 are finally determined according to the flow rate of the secondary combustion air. According to the value of Z1 to Z4, the previous output value of secondary combustion air flow rate (F2 (K1) · The current output of secondary suspected air flow rate can be calculated (F2 (k)). P2 (k) = F2 (k- 1) + zl + z2 + z3 + z4 (2) The silk parameters zl to z4 are calculated based on the process of _12 (a) to 12 (d). In circle 12 (a) to 12 (d) * Te is incineration The temperature deviation in the furnace, F2now is the speed of the secondary combustion air, 〇2 is the oxygen level, N〇X is ΝΟχΛ degree, C0 This paper scale is applicable to China ’s national standard rate (CNS) A4 specification (210X297mm> ; -1 6-A7 B7 V. Description of the invention (U) is CO concentration. (^ And (: 2 are the adjustment parameters of the secondary combustion air® speed M to identify the burning zone, boundary plaque and cooling zone. 0X1 is the oxygen concentration Adjust the parameter to identify the specific value or above M, which is lower than its value. 0X1 is an adjustment parameter to identify the upper limit of the oxygen level. 0X2 is an adjustment parameter to set the lower limit of the oxygen level. NOxl is one Adjust the parameter M to identify the upper limit of NOx concentration. C0 is to adjust the parameter M to identify the upper limit of C0 concentration. Yl to y] 0 is to adjust the parameter M to provide the flow of secondary combustion air and the flow rate of extinction . Figure 12 (a). In step S1, the temperature deviation Te in the incinerator is determined based on the control condition of Te < 0. When the condition of Te < 0 is satisfied, it can be confirmed in step S2. In step S2 Medium • When the flow rate of secondary combustion air can meet the control condition of F2n〇W 2¾, the adjustment parameter zl becomes yl °. When the control condition of F2now2Cz is not satisfied, F2now will be C, and the control condition can be confirmed in step S3. When the FZnowShi control condition is met, the adjustment parameter zl becomes y3. When the FSnowSCii control condition is not satisfied, the adjustment parameter zl becomes y7. The Ministry of Economic Affairs, Central Standard, Pingyi, Yigong Consumer Cooperative Cooperative nn nn ml ivn n ^ i 、 mfl n J 、 (please read the back ^ -notes ^ before filling in this page) In the case of Te < 0 in step S1 is not satisfied, step S4 can confirm when the control status F2now2C2 of step S4 is satisfied , The adjustment parameter zl becomes y2. When the control condition of step S4 is not satisfied? 2 ^ < ^ 2 (: 2, it can be confirmed by judging step S5. In step S5, the control status of FZnowSh is judged. When FZnowSh is satisfied When the control status is changed, the adjustment parameter zl becomes y4. When the control condition of FZnowSh is satisfied * the judgment step 8IS6 can be confirmed as 18. In step S6, the control condition of 02g〇xl is judged. When the control condition of 〇2 ^ 〇xl is satisfied • The adjustment parameter zl becomes y5. When 02S0xl is not satisfied When the control condition is changed, the adjustment parameter zl becomes y6. This paper is applicable to the Chinese National Standard (〇奶) 84 specifications (2 丨 0/297 public) ~ ΓΙ —1 7-Printed by the Central Standards Bureau of the Ministry of Economic Affairs, M Industry and Consumer Cooperatives A7 B7 V. Description of invention (15) Circle 12 (b) is a process circle, which exemplifies controlling the flow rate of secondary burnt air according to the degree of gaseousness. It is the control condition of »〇2 < 〇x2 to determine whether the measured oxygen concentration of 02 is lower than the lower limit of 0x2 oxygen degree. When the control condition is satisfied, the adjustment parameter ζ2 becomes y8. When the control condition is not satisfied, the adjustment parameter z2 becomes 0. Circle 12 (c) is a process_ * It exemplifies the control of the speed of secondary combustion air according to the NOx concentration. It depends on the control condition of N0x> N0xl to determine whether N (U's measured NOx concentration exceeds the limit of ΝΟχΛ of HOxl. When the control condition is met, the adjustment parameter ζ 3 becomes y9. When the chief does not meet the control condition, adjust the parameter z3 becomes 0. Figure 12 (d) is a process circle, which illustrates the control of the secondary combustion air speed based on the concentration of C0. It is based on the condition of C0> C01 to determine whether the C0 is greater than the C01. Set a limit above the C0 concentration. When the control condition is satisfied, the adjustment parameter 24 becomes ylO. When the control condition is not satisfied • The adjustment parameter z4 becomes 0. The adjustment parameters zl to z4 * are based on the process B measurement of _12 and are replaced To equation (2) to determine the value of the secondary combustion air flow rate (F2 (k)). The control block is explained with reference to circle 3. The secondary combustion air flow rate control A3 is a horizontal general control. Chess general control The regulations are shown in Table 2. The paper size is applicable to China National Standard Falcon (CNS) Α4 specification (210X297 mm) ^^^ 1 ^^^^ 1 ^^^^ 1 n ^ i ^ J ^ 1. ^ 1 ΐ, --Λ ",-(please read the back " · please pay attention to the item before filling in this page) -18- B7 V. Description of invention (1β) The control method of the burning method is the speed difference of the internal combustion zone, but the temperature is low, the second is the internal temperature furnace, and the fluidized negative combustion is gas- > Combustion but temperature and sub-cold two in the inner furnace-the burning of the burning is gas-> difference in the empty partial burning of burning plaque burning the second burning in the internal furnace, the fluidization of the burning is gas t difference In the air, the partial combustion entropy temperature and sub-combustion temperature in the internal combustion furnace are two, and the fluidization is burning into the gas difference. The partial combustion temperature in the partial combustion region is high in the internal combustion furnace, and the fluidization is the highest. Oxygen incineration is gas and t difference-the second burner temperature in the partial burning area is high in the second and the velocity furnace-the flow of oxygen is incinerated into gas and-> by Dilang central standard printed by the employee consumer cooperative Control the empty sugar level and burn the plaque within two sides of the temperature sub-range and quantify the negative incineration as gas (8) The oxygen concentration becomes below the lower limit (9) NOx Mao exceeds the upper limit (10) C0 concentration When the limit is exceeded, the next connection will be reduced (J > the next connection will be increased (the second connection of J »will be less than the next two within the degree) the second will be less than the second) & the next two will be considered as minus The gas furnace is regarded as a degraded gas furnace as a reduced gas furnace as a less} The gas furnace is regarded as a small incineration cavitation and variable value cavitation and variable value temperature cavitation and variable value temperature cavitation and variable decrement cavitation and variable reduction yaki Burning speed within the burning time burning speed burning speed burning temperature value of the entropy burning speed burning rate reduction when burning less, furnace burning chieftain less flow-internal combustion when less flow, internal combustion when less flow of combustion when less flow The district time-the time of subtraction, the time of subsidence, the time of subsidence, the time of subsidence, the time of subsidence, the subsequence, subtraction, burning} Second-speed differential gas. Regionalized two-speed differential gas-time furnace second-speed differential gas-time flammability calculated flow eccentric boundary plus calculated flow rhythm circumscribed incineration flow eccentric boundary incinerated stream But} hold the rate of rapid burning, reduce the number of jobs, calculate the amount of money, count the amount of money, increase the value of the side, count the amount of the side, add the degree of the side, burn the world, burn the world, burn the world, and count the second. The second dimension is the second, the second is the second, the second is the second, and the second is the second.

M 少滅少溫燃邊内減之次於_爐之内二遠(«化加溫燃邊_溫增之次ttteffi之之内二缠(«内氣爐當成少爐空化且變減化燒焚時速值焚燃當少流其少次，減之，減二速差氣時區潦»-及加向加少向加加向加加坩之坩減之増增之增之^增}之限值之限值之限值氣U速少氣設其氣設其氣設其空Μ流減空下，空上，空上，燐^之會熵自時堍自時焼自時燃^氣，燃當加燃當加燃當加次Μ空時次，》次，增次-增二ί熵少二速差二速差二速差 (請先閱讀背而之注意事項再填寫本頁) 裝· 丄' 本紙張尺度適用中國國家梯準（CNS ) Λ4規格（210X 297公釐） A7 B7 經濟部中央標苹局：^工消費合作社印製五、發明説明 (Π ) 1 1 I m 8顧示表2之規則 (1 >至U 0)。此等規則（ 1 ) 至 (10) 之計 1 1 | 算係根據部件功能進行其被示於麵9。每- -條規則之後 1 I 續部份之評估結果經過整合之_ ·(其係播二次空氣流速請先 Μ 1 I 控制構件 20所測定 ) 產生整ϋ則之評估结果（二次空氣請背流速控制之值）。綦m制値輸出1將流速調轚_構9調整 Μ 1¾ - 之注 1 I 意 1 I 控制二次燃焼空氣之流速〇對於各規定之後績部份之評估事項 1 I 再 1 結果之整合 •例如實施最小一最大里心法或積一和重心填寫本，衣法〇頁 '---· 1 1 至於表 2中規定（1) 至 (1 0) 之計算结果，二次燃燒空氣之 1 1 流速之改變係自計算结果之嬙合計算Μ調整二次燃堍空氣 1 1 之流速〇嫌後進行規定 (1 )至（1 0 )之計算。 1 訂規定 (4)及規定（8) 實 m 二次燃熵空氣'Κ彼此反向方向之 1 I 改 MdL 變流速之不同計算〇因此，二次燃燒空氣之流速被綢整 1 1 I Μ ίβ 加、滅少或保持其百 Λ.Λ., 刖之值•端視最後 m 出值而定 0 1 I --ίν 對二次燃堍空氣之控制段之計算例在應用 m 概式控制之情況下將參照圈9說明之，首先*計算前提部份之相容程 1 度〇在圔 9 ( a)前提部份之部件功能中，焚化爐内之溫度 - 1 I 差 Te 之観察值具有相容程度為a 1及”焚化爐内溫度僱差為 1 負 "之狀況 >同樣 ,” 0 ” 對應於a 2而"正"對應於 a3 。又 » 對於在焚化爐出口之〇 2 濃. 度觀察值法_ 9 ( b ) 先提部份之部 1 1 件功能為 0 Z ，”Μ，對應於 bl * (0)，而”镳度 "對廯於b 2 • - 1 I (1) 而” 低 "對應於b 3 (0) 。闞於空氣之二次燃燒潦速之 |· 電流值，在圈9(c)先提部份之部件功能中，覼察值為F2n 0 W I 1 r 1 ，，小" 對應於Cl · (0) 、” 中 ”對應於C 2，而" 大 "對應於C 3 1 1 本紙張尺度適用中國國家標準（CNS > A4規格（2丨OX 2们公釐）一 20 A7 B7 五、發明説明（18 經濟部t央標华局N工消f合作社印^ ，（0)。至於在焚化爐出口之HOx溻度，在園9(d)先提部份之部件功能中，靦察值為NOx，”高”對應於dl，而"遽度” 對應於d2。對於在焚化爐之C0溻度，在圈9 (e)先提部份之部件功能中，観察值為C 0，"高"對應於e 1，（ 0 )，而”適度 "對應於e2，（1)。根據此等值· _8中相容性Xt與規則1可由方程式（3)計算而得。由於規則1為"焚化爐内溫度偏差為負•而二次嫌i 燒空氣之流«之«流值大"，al及c3得Μ成立。以類似方式，對應於規則2至10之相容程度X2至Xβ可分別使用方程式（4 )至U 2 )計算得到。相容程度與規定l:X1=alXc3 (3) 相容程度與規定2 : X2 = a3 X c3 (4) 相容程度與規定3 : X3 = al x c3 (5) 相容程度與規定4 : = a3 x cl (6) 相容程度與規定5 : X5 = a3 x c2 x bl (7) 相容程度與規定6: XB=a3Xc2xb2 (8) 相容程度與規定7 : X7 = al x c2 (9) 相容程度與規定8 : XB = dl (10) 相容程度與規定9:Xs=el Π1) 相容程度與規定10 : X1〇= b3 (12) 其次，為了評估後讀部份之部件功能，澜定二次嫌燒空氣^至丫^之滾速之改變。然後•評估係«等式（13)提供以得評估结果Z。 Ζ= [Σ Xix ΥΠ/[Σ Χί] (13) (請先閱讀背面之注意事項再填寫本頁) 裝.M Less extinction and less temperature combustion, the inner reduction is second to the _ furnace's inner two distance («Chemical heating and combustion edge _ temperature increase and the second ttteffi within the two entanglement (« the inner gas furnace is regarded as less furnace cavitation and becoming reduced Burning speed per hour, burning time, less time, less time, minus two speed difference gas time zone »-and plus plus minus plus plus plus crucible crucible minus increase increase increase ^ increase} The limit value of the limit value is the gas velocity, the gas velocity, the gas velocity, the gas velocity, the air velocity, the air velocity, the air velocity, the air velocity, the air velocity, the air velocity, the air velocity, and the air velocity. , Ignite when ignited when ignited when added Μ space-time times, "times, increase times-increase two entropy less two speed difference two speed difference two speed difference (please read the precautions before filling this page) Installation · 丄 'This paper scale is applicable to China National Standards (CNS) Λ4 specifications (210X 297 mm) A7 B7 Central Standardization Bureau of the Ministry of Economic Affairs: ^ Printed by the Industrial and Consumer Cooperatives 5. Description of Invention (Π) 1 1 I m 8 Consider the rules of Table 2 (1 > to U 0). The calculation of these rules (1) to (10) 1 1 | The calculation is performed according to the function of the component. It is shown on the face 9. After each--rule 1 I Continued Comment The evaluation result is integrated _ (the secondary air flow rate of the broadcast is measured by the M 1 I control member 20 first). The overall evaluation result is generated (the secondary air is backed by the value of the flow rate control). Qim system output 1 Adjust the flow rate _Configuration 9 Adjust Μ 1¾-Note 1 I Meaning 1 I Control the flow rate of secondary combustion air ○ For each evaluation item after the regulation 1 I then 1 Integration of results • For example, the implementation of the minimum one maximum Inner-center method or product one and center-of-gravity fill-in book, clothing method page ∘ --- 1 1 As for the calculation results specified in (1) to (1 0) in Table 2, the change in the flow rate of the secondary combustion air 1 1 is According to the calculation result of the calculation, adjust the flow rate of secondary combustion air 1 1 to adjust the flow rate of the secondary combustion air 1 1 and then perform the calculations from (1) to (1 0). 1 Set the requirements (4) and (8) Real m Secondary combustion The entropy air 'κ is reversed from each other in the direction of 1 I to MdL variable flow rate calculation. Therefore, the secondary combustion air The flow rate is rounded 1 1 I Μ ίβ added, extinguished less or maintain its 100 Λ. Λ., The value of the end depends on the last m out value 0 1 I-ίν control section of secondary combustion air The calculation example will be explained with reference to circle 9 in the case of applying the m-probability control. First, * calculate the compatibility range of the prerequisite part 1 degree. In the function of the components in prerequisite part 9 (a), the Temperature-1 I The difference between the observed value of Te and the compatibility degree is a 1 and "the temperature in the incinerator is 1 negative". Similarly, "0" corresponds to a 2 and "positive" corresponds to a3. And »For the 02 concentration at the exit of the incinerator. Observation method _ 9 (b) The part of the first mentioned part 1 1 has a function of 0 Z,“ Μ, corresponding to bl * (0), and “concentration” " For the second b 2 •-1 I (1) and the “low” corresponds to b 3 (0). The speed of the secondary combustion of Kan in the air | · The current value is mentioned first in circle 9 (c) In some component functions, the observation value is F2n 0 WI 1 r 1, and the small " corresponds to Cl · (0), "medium" corresponds to C 2, and " large " corresponds to C 3 1 1 This paper scale is applicable to the Chinese national standard (CNS & A4 specifications (2 OX 2 mm)) A 20 A7 B7 V. Description of invention (18 Printed by the Ministry of Economic Affairs t Central Standards Bureau N Gongxiao F Cooperative Society ^, (0) As for the HOx degree at the outlet of the incinerator, in the function of the parts mentioned in the first part of Park 9 (d), the observation value is NOx, "high" corresponds to dl, and "quote" corresponds to d2. In the C0 degree of the incinerator, in the component function of the first part mentioned in circle 9 (e), the observation value is C 0, " high " corresponds to e 1, (0), and "moderate " corresponds to e2, (1). Based on these equivalents, the compatibility Xt in _8 and rule 1 can be calculated by equation (3). Since rule 1 is " the temperature deviation in the incinerator is negative • and the secondary air flow i Large values ", al and c3 are satisfied by M. In a similar manner, the compatibility degrees X2 to Xβ corresponding to rules 2 to 10 can be calculated using equations (4) to U2) respectively. The compatibility degree and regulations l: X1 = alXc3 (3) Compatibility and regulations 2: X2 = a3 X c3 (4) Compatibility and regulations 3: X3 = al x c3 (5) Compatibility and regulations 4: = a3 x cl (6) Compatibility and regulations 5: X5 = a3 x c2 x bl (7) Compatibility and regulations 6: XB = a3Xc2xb2 (8) Compatibility and regulations 7: X7 = al x c2 (9) Compatibility and regulations 8: XB = dl (10) Compatibility degree and regulations 9: Xs = el Π1) Compatibility degree and regulations 10: X1〇 = b3 (12) Secondly, in order to evaluate the function of the components in the post-reading part, Landing second The change of the rolling speed of the suspected air ^ to YA. Then the evaluation system «Equation (13) provides the evaluation result Z. AZ = [Σ Xix ΥΠ / [Σ Χί] (13) (please read the back Matters needing attention before filling this page) installed.

、1T Λ - 木紙张尺度適用中國國家標準（CNS ) Α4規格（210X 297公着） -21 - 305917 at B7 經满部中火標準局h工消费合作社印狀五、發明説明 (19 ) 1 1 1 最後評估之结果乃基於評估結果 Z及二次燃燒空氣流 1 1 I 速之出 P 值之先前值 (F2 (k- 1) )衍生二二次燃堍空氣流速目 1 1 I 前之輪出值 (F2 (k) )^ 請先 1 閱 | F2 (k) = F2(k- 1 ) + Ζ (1 4) 讀背圈 11 顧示使用本發明垃圾焚化爐之控制方法之控制轼驗 W - 之注 1 意 1 | 結果之測 0 圖 10 顯示使用比例控制方法之傳統垃圾焚化爐事項 1 1 再 1 」之结果〇填烟氣 % 本如此等圆所示應用本發明所作之測轼道排放内頁 1 之平均 N0 X濃度自100 P P ϋ降至7 0 p Ρ Β 減少達將近 30 P P B 1 1 及 C0 濃度之尖 % 出琨主要由焚化爐内溫度之降低所造成〇 1 1 焚化逋内溫度之改變霣度被抑制約 25¾ 因此不易發生焚 1 訂 1 I 化爐内溫度降低之情肜及 C0 薇度尖 % 之產生亦被抑制〇另外 0 2 濃度之改變寬度亦減少約 30* >其結果令人滿意。 1 1 1 該例使用焚化爐内之溫度偏差作為 _ 入值至二次燃堍空 1 1 氣之流速之控制系統〇當加入鍋爐時可實施蒸氣滾速偏丄差來取代焚化爐内之溫度偏差〇 1 | 如上所逑依照本發明二次燃燒空氣之 m 速係 » 非線 - 1 1 性控制方法控制特別是二次燃焼空氣之流速係賴吠況方 I 1 面之增加 /減少控制方法或藉横概式控制方法所控制因 1 1 此烟道排放氣內之有害成份被抑制至特定值而垃圾焚 - 1 1 化爐之使用壽命得以延長〇由於焚化爐内之溫度穩定之故 • 1 I g 級爐 m. 產生之蒸氣流速得以穩定而確保烟道排放 m 能量 L I 之有效使用〇 1 1 1 當焚化爐内之溫度過度減少時二次燃焼變成難維持 1 1 本紙張尺度適用中國國家標準（CNS ) A4規格（210X297公釐） 22 A7 B7 _ 五、發明説明（20 ) ，即使氧氣在焚化爐内充足無缺亦然*且烟道排放氣内之 C0澹度增加。然而，若烟道排放氣内之〇2濃度，（其濃度與二次燃熵空氣之潦速之間具有相闢），被偵檢在冷卻區内時，二次燃燐空氣之流速之滅少容許墦加焚化爐内之溫度Μ防烟道排放氣内C0濃度之埔加。又依照本發明，烟道排放氣内〇2溻度之起伏範園受限制。此外•當C 0及Ν 0 X之濃度«加時，調整二次燃熵空氣之流速至降低C0及NOx之溻度坩加之方向之作用可防止由於 02濃度之減少所造成之不完全燃熵所引起之烟道排放氣内 C0漘度之增加，或防止由Oz溻度之增加所造成之放出HOx 濃度之增加。即使當裝入垃圾焚化爐之垃圾之熱產生起伏時*確保焚化爐内之播定溫度及烟道排放氣内之穩定〇 2濃度之控制可維持良好燃堍效率。结果*設有動力產生鍋爐之自動加煤櫬型垃圾焚化爐可穩定熱最之產生*使動力產生效率改良。 I.--.-----f 策------訂------{一 (請先閱讀背面之注意事項再填寫本頁) 經濟部中央椋华局與工消资合作社印製本紙張尺度適用中國國家梯準（CNS ) A4规格（210X297公釐）、 1T Λ-Wood paper scale is in accordance with Chinese National Standard (CNS) Α4 specification (210X 297 public) -21-305917 at B7 Jingman Ministry of China Fire Standards Bureau h Industrial and Consumer Cooperative Printed V. Invention description (19) 1 1 1 The final evaluation result is based on the evaluation result Z and the secondary combustion air flow. The previous value of the P value of the 1 1 I speed (F2 (k-1)) is derived from the secondary secondary combustion air flow rate. Round robin value (F2 (k)) ^ Please read 1 first | F2 (k) = F2 (k- 1) + Z (1 4) Read back circle 11 Regarding the use of the control method of the garbage incinerator of the present invention Test W-Note 1 Meaning 1 | Result Measurement 0 Figure 10 shows the results of the traditional garbage incinerator using the proportional control method 1 1 then 1 ″ Flue gas filling% This is the measurement made by the application of the present invention as shown in this isometric circle Shidao Emissions Page 1 The average NO X concentration decreased from 100 PP ϋ to 7 0 p Ρ Β reduced by nearly 30 PPB 1 1 and the sharp% of C0 concentration. The main reason is the decrease of the temperature in the incinerator. The temperature change in the incinerator 〇1 1 The degree is suppressed by about 25¾, so it is not easy to burn. 1 Set 1 I. The temperature in the furnace is reduced and the generation of C0 Weidujian% is also suppressed. In addition, the width of the concentration change is also reduced by about 30 *. The result is that People are satisfied. 1 1 1 This example uses the temperature deviation in the incinerator as the input value to the secondary combustion chamber. 1 1 The flow rate of the gas control system. When added to the boiler, the steam roll speed deviation can be implemented to replace the temperature in the incinerator. Deviation 〇1 | As described above, according to the present invention, the m speed of the secondary combustion air »Non-linear-1 1 linear control method, especially the secondary combustion air flow rate is based on the increase / decrease control method of the I 1 side Or controlled by the horizontal control method. 1 1 The harmful components in the flue gas are suppressed to a specific value and the waste incineration-1 1 The service life of the furnace is extended. Because the temperature in the incinerator is stable • 1 I g class furnace m. The generated steam flow rate is stabilized to ensure the effective use of the energy m of the flue emissions m energy 〇1 1 1 The secondary combustion sintering change when the temperature in the incinerator is excessively reduced Difficult to maintain 1 1 This paper scale applies the Chinese National Standard (CNS) A4 specification (210X297 mm) 22 A7 B7 _ 5. Description of the invention (20), even if the oxygen is sufficient in the incinerator, and the flue exhausts The degree of C0 within increases. However, if the 02 concentration in the flue gas (which has a separation between the concentration and the speed of the secondary combustion entropy air) is detected in the cooling zone, the flow rate of the secondary combustion air is extinguished It is not permissible to add the temperature in the incinerator M to increase the C0 concentration in the flue gas. Also according to the present invention, the fluctuating fan garden in the flue gas exhaust at 02 degrees is restricted. In addition, when the concentration of C 0 and Ν 0 X is increased, the effect of adjusting the secondary combustion entropy air flow rate to reduce the direction of the addition of C0 and NOx can prevent the incomplete combustion entropy caused by the reduction of the 02 concentration. The resulting increase in the C0 concentration in the flue gas emissions, or to prevent the increase in Oz concentration caused by the increase in the release of HOx concentration. Even when the heat of the garbage loaded into the garbage incinerator is fluctuating * Ensure the control of the planting temperature in the incinerator and the stable 02 concentration in the flue gas can maintain good combustion efficiency. Result * Automatic coal addition with power generation boiler 抇 type waste incinerator can stabilize the most heat generation * Improve the power generation efficiency. I .--.----- f policy ------ order ------ {1 (please read the precautions on the back before filling in this page) The size of the paper printed by the cooperative is applicable to the Chinese National Standard (CNS) A4 (210X297mm)

Claims

經濟部中央標準局負工消費合作社印裝 A8 B8 C8 D8六、申請專利範圍 1. 一種垃圾焚化爐之燃堍控制裝置|包括：將初次燃堍空氣供入垃圾焚化爐之構件；將二次燃堍空氣供入垃圾焚化爐之構件；依照垃圾焚化爐之燃燐負荷控制初次燃燒空氣之流速之控制構件；测定垃圾焚化爐内溫度之第一测定構件；測定垃圾焚化爐之烟道排放氣内之〇2濃度之第二测定構件；測定垃圾焚化爐之烟道排放氣内之C0濃度之第三測定構件；測定垃圾焚化爐之烟道排放氣内之Ν Ο X濃度之第四测定構件；及依據第一測定構件至第四測定構件之測定值控制二次燃燒空氣之流速之非線性控制構件。 2. 如申講専利範圃第1項之燃燒控制裝置，其中該非線性控制構件包括撗概式控制構件。 3. —棰垃圾焚化爐之燃燒控制方法，包括之步驟為： (a) 依照在特定時間内裝入垃圾焚化爐之垃圾之熱值控制初次燃燒空氣之流速； (b) 測定垃圾焚化爐内側之溫度，及測定烟道排放氣内之〇2濃度、C0濃度及NOx溻度；及 (c) 基於步骤（b)之測定值控制二次燃燒空氣之流速。 4. 如申請専利篛園第3項之燃堍控制方法，其中該初次燃燒空氣之流速係賴前嫌控制所控制。本紙張尺廋適用中國國家橾率（CNS ) A4规格（210X297公釐) ~~ —. ^ 裝訂 ^ (請先閱讀背面之注意事項再填寫本頁) 305917 A8 B8 C8 D8 六、申請專利範圍 5. 如申謫專利範圈第3項之燃燒控制方法，其中該初次燃熵空氣之流速係«廻鏑控制所控制。 6. 如申請專利範園第3項之燃堍控制方法*其中該非線性控制構件包括供概式控制構件。 7. —種垃圾焚化爐之燃燒控制方法，包括之步驟為： (a)製備一將初次燃熵空氣供入垃圾焚化爐之初次空氣供應構件及一將二次燃堍空氣供入垃圾焚化爐之二次空氣供懕構件； (b )依照垃圾焚化爐之燃燒負荷控制初次燃燒空氣之流速； (c) 測定垃圾焚化爐内側之溫度•及測定烟道排放氣内之〇2漘度、C0灞度及NOx澹度；及 (d) 基於步» (c)之測定值藉非線性控制構件控制二次燃燒空氣之流速。 8. 如申謂専利範園第7項之燃堍控制方法，其中該非線性控制構件包括播*式控制構件。 ---------(裝-- (請先閱讀背面之注^^項再填寫本頁) 、-·· 經濟部中央標準局員工消費合作社印聚本紙張尺度適用中國國家榇準（CNS ) A4規格（21〇X25»7公嫠）Printed and printed by A8 B8 C8 D8 at the Consumer Labor Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs. Scope of Patent Application 1. A burner control device for garbage incinerators | Includes: components for supplying the primary combustion air to the waste incinerator; Components for supplying the combustion air to the garbage incinerator; control components for controlling the flow rate of the primary combustion air in accordance with the incineration load of the garbage incinerator; the first measuring component for measuring the temperature in the garbage incinerator; measuring the flue gas emissions of the garbage incinerator The second measuring component of the 〇2 concentration in the third; the third measuring component of the C0 concentration in the flue gas of the waste incinerator; the fourth measuring component of the Ν X concentration in the flue gas of the waste incinerator ; And a non-linear control member that controls the flow rate of the secondary combustion air based on the measured values of the first to fourth measuring members. 2. For example, the combustion control device of Section 1 of the Fanfan Garden, where the non-linear control component includes a general control component. 3. —The combustion control method of garbage incinerators, including the following steps: (a) Control the flow rate of the primary combustion air according to the calorific value of the garbage loaded into the garbage incinerator within a specific time; (b) Determine the inside of the garbage incinerator Temperature, and the determination of the 02 concentration, CO concentration and NOx concentration in the flue gas; and (c) control the flow rate of secondary combustion air based on the measured value of step (b). 4. For example, if you apply for the control method of burning gas in item 3 of the Zili Garden, the flow rate of the first combustion air is controlled by the previous control. The size of this paper is suitable for China National Atomic Rate (CNS) A4 specification (210X297mm) ~~ — ^ binding ^ (please read the precautions on the back before filling in this page) 305917 A8 B8 C8 D8 VI. Patent application scope 5 . For example, the combustion control method in the third paragraph of the application patent circle, in which the flow rate of the initial entropy combustion air is controlled by «Yu Dy control. 6. For example, the patent control method of the patent garden item 3 * where the non-linear control component includes a general control component. 7. A method of combustion control for a garbage incinerator, including the steps of: (a) preparing a primary air supply member that supplies primary combustion entropy air to the garbage incinerator and a secondary combustion gas to the garbage incinerator The secondary air supply component; (b) Control the flow rate of the primary combustion air according to the combustion load of the garbage incinerator; (c) Measure the temperature inside the garbage incinerator and measure the 02 degree and C0 in the flue gas Ba degree and NOx degree; and (d) Based on the measured value of step »(c), the flow rate of secondary combustion air is controlled by a non-linear control member. 8. For example, the application of the fuel gas control method in item 7 of the Zhanli Fanyuan, where the non-linear control component includes a broadcast control component. --------- (installed-(please read the note ^^ on the back and fill in this page),--· The printed standard of the Employee Consumer Cooperative of the Central Standards Bureau of the Ministry of Economic Affairs. The paper standard is applicable to the Chinese national standard (CNS) A4 specification (21〇X25 »7 male daughter)