TW201206554A - Tail gas treatment system for fuel material cracking furnace - Google Patents

Tail gas treatment system for fuel material cracking furnace Download PDF

Info

Publication number
TW201206554A
TW201206554A TW99127012A TW99127012A TW201206554A TW 201206554 A TW201206554 A TW 201206554A TW 99127012 A TW99127012 A TW 99127012A TW 99127012 A TW99127012 A TW 99127012A TW 201206554 A TW201206554 A TW 201206554A
Authority
TW
Taiwan
Prior art keywords
water
gas
tail gas
cracking furnace
gas treatment
Prior art date
Application number
TW99127012A
Other languages
Chinese (zh)
Other versions
TWI398294B (en
Inventor
Kwok-Sing Lee
wen-ji Xu
Original Assignee
South China Reborn Resources Zhongshan Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by South China Reborn Resources Zhongshan Co Ltd filed Critical South China Reborn Resources Zhongshan Co Ltd
Priority to TW99127012A priority Critical patent/TWI398294B/en
Publication of TW201206554A publication Critical patent/TW201206554A/en
Application granted granted Critical
Publication of TWI398294B publication Critical patent/TWI398294B/en

Links

Abstract

The present invention provides a tail gas treatment system for a fuel material cracking furnace containing a boiler and a horizontal waste plastics and waste tires cracking furnace. The said fuel material includes solid, gaseous, and liquid fuel material. The tail gas treatment system includes a carbon dust particle filtration system connected with the cracking furnace, a gas-solid separating system connected with the carbon dust particle filtration system, a smoke discharging system connected with the gas-solid separating system, and a circulating water cooling system. Compared with the prior art, the tail gas treatment system of the present invention is both environmentally friendly and economical. It is capable of reducing or eradicating carbon dust particles in the tail gas; its discharge temperature approximates the atmospheric temperature; it has a long operating life; it is also easy and quick to load and unload.

Description

201206554 所述的煙氣排放系統,包括有三部分,下部罐體,與下部_ 項部相連接的熱交換器及設於熱交換器上部的氣體排放管道;其 中’所述的下部罐體與混合管道的出σ相連接,下部罐體上設置 有濕性碳塵渣口及出水口,所述的氣體排放管道内也設置有可 鹼水的環型噴霧嘴。 ' 另外還設置有可使熱交換器中的循環水、氣固分離器中的循環 水及碳潰過遽器中的循環水循環的循環水冷卻系統;該循環水冷 卻系統包括有冷卻塔、τ部罐體上邮水口為熱水出口,熱料 口直接進人賴池’同時與水舰連接設置有魏式綠池,碳 渔過滤器的排賴管排出驗渣通往過濾式赚池,猶式沉逢 池中的水通過猶環冷卻水系進出冷卻塔;另外與所述冷卻塔連接 杨麟縣,該水_與熱交換器、氣固分離器及碳渣過遽 器的熱父換器水管及前級循環水管相連接。 … 性冷二::排放5道及熱交換器上設置有相通的後級循環鹼 二’ δ顧循概性冷水f與循環水冷卻編目接,循環 水冷部糸統還外接有冷水補給管。 所述的連接管道是方型管道。 所道中叹置有兩層或者兩層以上的多層水簾喷麗。 所述的緩衝室中設置有兩重水簾喷灑。 所述的韻過邮為雙$韻過滤器。 綱為雙塔形,包括有兩個立式_體。 的驗性噴霧用水為石灰水或者已稀釋的氣氧化納水溶液。 201206554 所述的引風管為方型引風管。 所述的引風器後端管道長度不少於⑽。 通過上述技術方案,從而該發明具有下述有益效果: 1.此夠對尾氣進行脫硫、減輕二氧化碳排放的同時,還可能 將尾氣中含有的碳塵粒進行清除,實現無污錢乎無錄排放, 有放的改’文了以往燃氣爐尾氣因尾氣排放過程巾所產生的弱酸腐 i虫s道引起官道容易破損的缺陷,保障系統的使用壽命; 2.能夠縣氣的溫餅低顺錢基本相_放,從而同樣 保障了系統的使用壽命。 【實施方式】 下面結合附圖對本發明作出進一步的說明。 如圖1-3所示,本發明之燃料裂解爐尾氣處理系统,包括與 裂解爐相連的破塵粒過遽系統,所述的碳塵粒過滤、系統包括有與 裂解爐相通的連接管道1,連接管道1是方型管道,其另一端與熱 氣水緩衝室3相連,連接管道中設置有兩層或者兩層以上的多層 水簾噴灑,所述的緩衝室3中設置有兩重水簾噴灑,從方型連接 管道進入的熱氣在多層以水簾噴灑以及緩衝室的作用下,減弱煙 氣(水)帶動煙氣中炭粒所引發破壞性熱衝擊力;同時緩衝室下 端設置有碳渣過濾器4,該所述的碳渣過濾器為雙重碳渣過濾器, 其上設有排液固管40。 還包括有與碳塵粒過濾系統相連的氣固分離系統,所述的氣 201206554 固分離系統包括核,緩衝室3 S 一端通過管道相連的氣固分離器 2,所述的氣固分離器2為雙塔形,包括有兩個立式圓柱形筒體, 在所述的氣固分離器内裝有迴旋噴霧噴嘴162,迴旋噴霧噴嘴中設 置有驗性喷_水,所述驗性儒財為石灰水或者已稀釋的 氫氧化鈉水溶液;其迴旋喷霧喷嘴主要是讓鹼性水與上升的水氣 加大接觸面積’以此達到除塵、脫硫和二次除碳目的;具體來說 氣固分離H 2的氣體出σ 20通過引風管5與混合管道54的氣體 .入541相接,混合管道54上設有液固入口 54〇,液固入口 5仙 與設置於氣固分離器2下端的下部水固管道52相通,在混合管道 54上設置有可將下部水固管道52中騎水、碳歧引風管5中的 氣體引出,並使驗水、碳渣及氣體進一步混合的引風器6 ;進一步 來說所述的引風管是方型引風管,所述的引風雜端管道^長 度不少於9Μ。 還包括有煙軋排放系統,所述的煙氣排放系統包括有 | 卩〃 桶型之下部罐體9,罐體項部通過管道連接中部 的,,、、=換益8 ’上部的氣體排放管道16與熱交換器相通連接,熱 交換器主要疋將由下部上升而來的熱水蒸汽起到氣相分離的作 用’使氣體_向上通過上部的氣體排放管道。其中,所述的下 y罐體9與齡營道54的出口相連接,下部罐體9上設置有濕性 碳塵90及出水口 92,所述的氣體排放管道16内也設置有可 喷K的衣型噴霧嘴162 ’嘴霧嘴中設置有驗性喷霧用水,同樣是 石义X或者已稀釋的魏化鈉水溶液;經前面多道裝置的處理, 201206554 在此處尾氣t尚殘餘有二氧化碳存在 以喷霧方式向下_祕树與二氧化碳再次接 物質。 ,在該環形噴霧喷嘴 觸生成碳酸鹽類 另外還設置村使射魅8 的循環水及碳渔過濾、器4中的循環水循;;簡分離器2 t 循環水冷卻系統包括有冷卻塔7、下部罐冷卻系統;該 水出口,熱水出口直接進人料池17,同時為熱 10 子與水渣池17連接設置 ^慮式>儿造池12,碳渔過滤器4的排液固管 Z式麻12,繼繼1㈣蝴㈣ 進出冷轉7,另外與所述冷卻塔7連财熱猶環核a,該水 果13同時與熱交換器8、氣固分離器2及碳渣器4的轨交換 益水㈣及前級循環水们4相連接。其中所述的氣體排放管道 Μ及熱交換器8上設置有相通的後級循環驗性冷水管ι〇,該後級 循環鹼性冷水管1〇與循環水冷卻系統相接,循環水冷卻系統還外 接有冷水補給管19,從而從系統出水口 92流出的熱水(4〇_6〇 C)進入水槽,再經過冷卻塔的冷卻進行水過濾系統處理後循環 處理,如水溫超過設定溫度時,再由另外的冷水設備製冷補給。 與現有技術相比,這種裂解爐尾氣處理系統能夠對尾氣進行 脫爪減輕一氧化碳排放的同時,還可能將尾氣中含有的碳塵粒 進行清除,實現無污染幾乎無白煙排放,有效的改變了以往燃料 的裂解爐因排放熱氣帶動碳塵粒衝擊管道及設備,以及燃氣爐尾 義1因尾氣排放過程中所產生的弱酸腐蝕管道引起管道容易破損的 201206554 氣的溫度降低到與大 有利於環保;同轉 缺陷,保障系統的使用壽命;同時能夠將尾 氣基本相同排放’大大的減低了室溫排放, 系統裝卸方便、快捷。 【圖式簡單說明】 圖1為本發明燃料裂解爐尾氣處理系統的示意圖。 圖2為雙塔形濕式氣固分離器及其内部構造的示意圖。 % 圖3為煙氣排放系統及其内部構造的示意圖。 【主要元件符號說明】 1- 連接管道 2- 氣固分離器 3'緩衝室 4- 碳渣過濾器 # 40-排液固管 5- 引風管 52-水固管道 54-管道 540-液固入口 541~氣體入口 6- 引風器 7- 冷卻塔 9 201206554 8- 熱交換器 9- 下部罐體 90-濕性碳塵渣口 92-出水口 10- 後級循環鹼性冷水管 11- 循環冷卻水泵 12- 過濾式沉渣池 13- 水泵 14- 前級循環水管 15- 熱交換器水管 16- 氣體排放管道 162-迴旋喷霧喷嘴 17- 水潰池 19- 冷水補給管 20- 氣體出口 201206554 發明專利說明書 (本說明書格式、順序,請勿任意更動,※記號部分請勿填寫) ※申請案號:尸〆/之/〇/>The flue gas discharge system of 201206554 includes three parts, a lower tank body, a heat exchanger connected to the lower portion, and a gas discharge pipe disposed at an upper portion of the heat exchanger; wherein the lower tank body and the mixture are mixed The sigma of the pipeline is connected, and the lower tank is provided with a wet carbon dust slag port and a water outlet, and the gas discharge pipe is also provided with a ring spray nozzle capable of caustic water. 'An additional circulating water cooling system is provided for circulating water in the heat exchanger, circulating water in the gas-solid separator, and circulating water in the gas collapser; the circulating water cooling system includes a cooling tower, τ The water outlet on the tank body is a hot water outlet, and the hot material inlet directly enters the Lai pool. At the same time, the Wei-style green pool is connected with the water ship, and the carbon fishing filter drains the test residue to the filter-type earning pool. The water in the Jewish sinking pool passes through the cooling water system of the Judah ring and enters the cooling tower; in addition, it is connected to the cooling tower to Yanglin County, and the water is replaced by the hot father of the heat exchanger, the gas-solid separator and the carbon slag filter. The water pipe and the circulating water pipe of the front stage are connected. ... Sexual Cold 2:: 5 channels of discharge and a downstream stage of circulating alkali in the heat exchanger. 2' δ is used to select the cold water f and the circulating water cooling catalogue. The circulating water cooling system is also connected with a cold water supply pipe. The connecting pipe is a square pipe. In the middle of the road, there are two or more layers of water curtains. The buffer chamber is provided with two water curtain sprays. The rhyme is described as a double $ rhyme filter. The outline is a double tower, including two vertical _ bodies. The water for the test spray is lime water or a diluted aqueous solution of sodium oxide. The air inlet duct described in 201206554 is a square air duct. The length of the rear end of the air duct is not less than (10). Through the above technical solution, the invention has the following beneficial effects: 1. This is enough to desulfurize the exhaust gas and reduce the carbon dioxide emission, and at the same time, it is possible to remove the carbon dust particles contained in the exhaust gas, thereby realizing no pollution. Emissions, there is a change in the text. In the past, the gas stove exhaust gas caused by the weak acid rot caused by the tail gas discharge process towel caused the defect of the official road is easy to break, to ensure the service life of the system; The low-smooth basic phase _ puts, thus also guarantees the service life of the system. [Embodiment] The present invention will be further described below in conjunction with the accompanying drawings. As shown in FIG. 1-3, the fuel cracking furnace tail gas treatment system of the present invention comprises a dust-breaking particle passing system connected to the cracking furnace, and the carbon dust particle filtering system comprises a connecting pipe connected to the cracking furnace. The connecting pipe 1 is a square pipe, and the other end thereof is connected to the hot gas water buffer chamber 3, and the connecting pipe is provided with two or more layers of water curtain spraying, and the buffer chamber 3 is provided with two water curtain spraying The hot gas entering from the square connection pipe is used to spray the water curtain and the buffer chamber to weaken the destructive thermal impact caused by the flue gas (water) to drive the carbon particles in the flue gas; at the same time, the carbon slag is disposed at the lower end of the buffer chamber. In the filter 4, the carbon residue filter is a double carbon residue filter having a liquid discharge pipe 40 disposed thereon. Also included is a gas-solid separation system connected to a carbon dust particle filtration system, the gas 201206554 solid separation system comprising a core, a gas-solid separator 2 connected at one end of the buffer chamber 3 S through a pipeline, the gas-solid separator 2 The utility model has a double tower shape, comprising two vertical cylindrical cylinders, wherein the gas-solid separator is provided with a swirling spray nozzle 162, and the swirling spray nozzle is provided with an experimental spray water, the test It is lime water or diluted sodium hydroxide solution; its swirling spray nozzle is mainly to increase the contact area between alkaline water and rising water gas to achieve dust removal, desulfurization and secondary carbon removal purposes; The gas out-gas separation σ 20 of the gas-solid separation H 2 is connected to the gas inlet 541 of the mixing pipe 54 through the air inlet pipe 5, and the liquid-solid inlet 54 is provided on the mixing pipe 54, and the liquid-solid inlet is disposed at a gas-solid separation The lower water-solid pipe 52 at the lower end of the device 2 is connected, and the mixing pipe 54 is provided with a gas for riding the water in the lower water-solid pipe 52 and the carbon-induced air duct 5, and further testing the water, carbon residue and gas. Mixed air blower 6; further said induced wind Air inducing pipe is square, the end of the conduit of the wind ^ heteroaryl length of not less than 9Μ. Also included is a smoke exhaust system, the smoke exhaust system includes a lower tank body 9 having a barrel shape, and the tank body portion is connected to the middle portion through a pipe, and the gas discharge at the upper portion of the exchange The pipe 16 is connected to the heat exchanger, and the heat exchanger mainly acts to separate the hot water vapor rising from the lower portion into the gas phase, and allows the gas to pass upward through the upper gas discharge pipe. The lower tank body 9 is connected to the outlet of the age camp road 54. The lower tank body 9 is provided with wet carbon dust 90 and a water outlet 92. The gas discharge duct 16 is also provided with a sprayable container. K's coat spray nozzle 162 'in the mouth of the nozzle is set with an experimental spray water, the same is Shiyi X or diluted Weihua sodium aqueous solution; treated by the previous multi-channel device, 201206554 where the tail gas t remains The presence of carbon dioxide is sprayed down to the _ secret tree and carbon dioxide again. In the annular spray nozzle, the carbonate is generated, and the circulating water of the village is used to circulate the water and the circulating water in the carbon fishing filter 4; the simple separator 2 t circulating water cooling system includes a cooling tower 7 The lower tank cooling system; the water outlet, the hot water outlet directly enters the human pool 17, and the heat 10 is connected to the water slag pool 17 to set the circumstance> the effluent pool 12, and the carbon fishing filter 4 drains The solid pipe Z type hemp 12, the subsequent 1 (four) butterfly (four) in and out of the cold turn 7, and the cooling tower 7 connected with the heat of the ring, the fruit 13 simultaneously with the heat exchanger 8, the gas-solid separator 2 and carbon residue The rail exchange benefit water (4) of the device 4 and the pre-stage circulating water are connected to each other. The gas discharge pipe and the heat exchanger 8 are provided with a communicating rear-stage regenerative cold water pipe ι, which is connected to the circulating water cooling system, and the circulating water cooling system is connected. The cold water supply pipe 19 is also externally connected, so that the hot water (4〇_6〇C) flowing out of the system water outlet 92 enters the water tank, and is cooled by the cooling tower to be processed by the water filtration system, such as when the water temperature exceeds the set temperature. And then replenished by another cold water equipment. Compared with the prior art, the cracking furnace tail gas treatment system can remove the carbon dioxide emissions from the exhaust gas while removing the claws, and may also remove the carbon dust particles contained in the exhaust gas to achieve no pollution and almost no white smoke emission, and effectively change In the past, the pyrolysis furnace of the fuel was driven by the hot gas to drive the carbon dust particles to impact the pipeline and equipment, and the gas furnace furnace tail 1 due to the weak acid corrosion pipeline generated during the exhaust gas discharge process, the pipeline was easily damaged, and the temperature of the 201206554 gas was reduced to a large advantage. In the environmental protection; the same turning defects, to ensure the service life of the system; at the same time able to discharge the exhaust gas is basically the same 'to greatly reduce the room temperature emissions, system loading and unloading is convenient and fast. BRIEF DESCRIPTION OF THE DRAWINGS Fig. 1 is a schematic view of a fuel cracking furnace tail gas treatment system of the present invention. 2 is a schematic view of a double-tower wet gas-solid separator and its internal structure. % Figure 3 is a schematic diagram of the flue gas exhaust system and its internal structure. [Main component symbol description] 1- Connection pipe 2 - Gas-solid separator 3' Buffer chamber 4 - Carbon residue filter # 40 - Drain pipe 5 - Air duct 52 - Water solid pipe 54 - Pipe 540 - Liquid solid Inlet 541~Gas inlet 6-Actuator 7-Cooling tower 9 201206554 8- Heat exchanger 9- Lower tank 90- Wet carbon dust sump 92-Water outlet 10- Rear circulating alkaline cold water pipe 11- Circulation Cooling water pump 12 - Filter type sediment tank 13 - Water pump 14 - Front stage circulating water pipe 15 - Heat exchanger water pipe 16 - Gas discharge pipe 162 - Swirling spray nozzle 17 - Water blasting tank 19 - Cold water supply pipe 20 - Gas outlet 201206554 Invention Patent specification (Do not change the format and order of this manual, please do not fill in the ※ part) ※Application number: corpse / / / />

※申請日:99. 8. 12 ’ ^PC 分類:_ 添(2006.0D 一、 發明名稱:(中文/英文) / 燃料裂解爐尾氣處理系統 户 η 二、 中文發明摘要: 本發明係提供-_㈣纖含峨及臥讀轉、廢輪胎 〇裂解爐之燃料裂解爐尾氣處理系統,所述的燃料包括固體燃料和 _氣縣者液舰料’包括與料爐相連的碳齡過齡統,與碳 、塵粒過齡統相連的氣固分㈣統,與氣@分離系助連的煙氣 排放系統’以及循環水冷卻系統,與财技術減是—種環保、 經濟、能夠減少或者根除尾氣巾的碳絲、排放溫度與大氣溫度 大致相同、使用壽命長的燃料裂解爐尾氣處理系統,同時該系統 裝卸方便、快捷。 〇 三、英文發明摘要: 201206554 七、申請專利範圍: 1.一種燃料裂解爐尾氣處理系統,其特徵在於:所述系統包括相互 連接的碳塵粒過濾系統,氣固分離系統,煙氣排放系統;所述碳 塵粒過/慮系統包括有熱氣水緩衝室,該熱氣水缓衡室一端通過連 接官道與裂解爐尾氣端相連接,該緩衝室下端設置有碳渣過濾 器,該碳潰過濾器上設有排液固管; 所述氣固分離系統與碳塵粒過齡統相連接,包括有與緩衝室另※Application date: 99. 8. 12 ' ^PC Classification: _ Tim (2006.0D I. Invention name: (Chinese / English) / Fuel cracking furnace exhaust gas treatment system household η II, Chinese abstract: The present invention provides -_ (four) A fuel cracking furnace tail gas treatment system for a fiber-containing crucible and a bed-turning, waste tire crucible cracking furnace, the fuel comprising a solid fuel and a gas-capacity ship material comprising a carbon-aged overage system connected to the furnace, Carbon and dust particles are connected to the gas-solids (four) system, and the gas emission system supported by the gas@separation system and the circulating water cooling system, and the financial technology is reduced, environmentally friendly, economical, capable of reducing or eradicating exhaust gas. The carbon filament of the towel, the fuel cracking furnace tail gas treatment system with the same discharge temperature and the atmospheric temperature, and the long service life, and the system is convenient and quick to load and unload. 〇三, English Abstract: 201206554 VII. Patent application scope: 1. A fuel a cracking furnace tail gas treatment system, characterized in that the system comprises an interconnected carbon dust particle filtering system, a gas-solid separation system, a flue gas exhaust system; and the carbon dust particle over/under system package There is a hot water buffer chamber, and one end of the hot gas water balance chamber is connected to the tail end of the cracking furnace through a connecting official passage, and a carbon residue filter is disposed at a lower end of the buffer chamber, and a liquid draining tube is disposed on the carbon filter; The gas-solid separation system is connected with the carbon dust particles, including the buffer chamber

-端通過管道相連的氣固分離器’在所述的氣固分離器内裳有可 噴驗性水的迴旋儒噴嘴,制分離^的氣體^ 口通則風管與 混合管道的氣體入口相接,混合管道上設有液固入口,液固入口 與設置於賴分離訂_下部糊奴相通,在混合管道上設 置有可將下部水崎道中崎水、碳渣糾崎㈣氣體引出、 f驗水、碳敍㈣進—步絲咐·;所述·氣排放 ^統,包括有三部分,下部罐體,與下部罐體蝴目連接的轨交 2及娜纖爛氣輯_;其中,所述的下娜 體與混合管道的出口相連接,下部罐 出水口,所述的氣體梅道内吨;置:濕性働口及 嘴。 也4有可噴驗水的環型噴霧 2·如申請專利範圍第1項所述之燃料裂 在於:糾麟置有可使缺崎卿水㈣祕’其特微 循環水及碳逢過滤器中的循環水循環的循環水二固分離器中的 水冷卻系統包括#冷卻塔、下部罐體上 "部系統;該循釋 水D為熱水出口,朝a gas-solid separator connected to the end by a pipe. In the gas-solid separator, there is a swirling Confucius nozzle with a sprayable water, and the gas is separated from the gas inlet of the mixed pipe. The mixing pipe is provided with a liquid-solid inlet, and the liquid-solid inlet is connected to the lower-layered paste, and the mixed water pipe is provided with the lower Nagasaki Road Nakasaki water, the carbon residue saki (4) gas, and the water test. , carbon narration (four) into - step silk 咐 ·; said gas emissions ^ system, including three parts, the lower tank body, the rail connection with the lower tank butterfly line 2 and Na fiber smashing _; The lower body is connected to the outlet of the mixing pipe, the lower tank outlet, the gas inside the plum road; the setting: wet mouthwash and mouth. Also, there is a ring spray that can be sprayed with water. 2. The fuel crack described in the first paragraph of the patent application is: The lining has the ability to make the Kawasaki water (four) secret 'its special micro-circulating water and carbon filter The water cooling system in the circulating water two-solid separator of the circulating water circulation includes a #cooling tower and a lower tank upper portion system; the water discharge D is a hot water outlet,

Claims (1)

201206554 9. 如申請專利範圍第1項或第2項所述之燃料裂解爐尾氣處理系 統,其特徵在於:所述的引風管為方型引風管。 10. 如申請專利範圍第1項或第2項所述之燃料裂解爐尾氣處理系 統,其特徵在於:所述的引風器後端管道長度不少於9M。 SThe fuel cracking furnace tail gas treatment system according to claim 1 or 2, wherein the air guiding duct is a square air guiding duct. 10. The fuel cracking furnace tail gas treatment system according to claim 1 or 2, wherein the length of the rear end of the air duct is not less than 9M. S 13 201206554 八、圖式:13 201206554 Eight, schema: 201206554201206554
TW99127012A 2010-08-12 2010-08-12 Tail gas treatment system for fuel material cracking furnace TWI398294B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
TW99127012A TWI398294B (en) 2010-08-12 2010-08-12 Tail gas treatment system for fuel material cracking furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
TW99127012A TWI398294B (en) 2010-08-12 2010-08-12 Tail gas treatment system for fuel material cracking furnace

Publications (2)

Publication Number Publication Date
TW201206554A true TW201206554A (en) 2012-02-16
TWI398294B TWI398294B (en) 2013-06-11

Family

ID=46761987

Family Applications (1)

Application Number Title Priority Date Filing Date
TW99127012A TWI398294B (en) 2010-08-12 2010-08-12 Tail gas treatment system for fuel material cracking furnace

Country Status (1)

Country Link
TW (1) TWI398294B (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI675698B (en) * 2018-03-30 2019-11-01 張瑞永 Settling film hydrogen sulfide absorption tower for waste tire cracking gas

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4895083A (en) * 1988-11-14 1990-01-23 Mcdilda John A Whole tire disposal system
TWI254115B (en) * 2004-12-30 2006-05-01 Ind Tech Res Inst Waste plastic disposing equipment
CN1872953A (en) * 2006-06-27 2006-12-06 姚军辉 Technique for cracking integral scrap tires

Also Published As

Publication number Publication date
TWI398294B (en) 2013-06-11

Similar Documents

Publication Publication Date Title
WO2011140741A1 (en) Tail-gas treatment system for fuel pyrolyzing furnace
WO2014079172A1 (en) Exhaust gas treatment system
CN102120132B (en) Purification treatment device for incineration flue gas
CN108421342A (en) Spraying cooling eliminates the device of white cigarette in a kind of desulfuration absorbing tower
TW201206554A (en) Tail gas treatment system for fuel material cracking furnace
CN110180314A (en) The white processing unit that disappears of station tail gas is mixed in a kind of drip
CN201684518U (en) Tail gas treatment system of fuel cracking furnace
CN210410191U (en) Carbon black tail gas boiler flue gas takes off white system
CN206131026U (en) Industrial boiler flue gas processing system
CN106139792A (en) A kind of baking flue gas governing system and administering method
CN204170579U (en) Rubber powder modified asphalt produces gas emission device
CN208512140U (en) Spraying cooling eliminates the device of white cigarette in a kind of desulfuration absorbing tower
CN201988321U (en) Incinerating smoke cleaning processing device
CN205119109U (en) Flue gas recovery system
CN212818972U (en) Colored smoke plume desorption system of high temperature water flushing sediment steam
CN206229174U (en) Oil field fuel oil injection boiler tail gas desulfurization denitration process system
CN106178801A (en) A kind of desulfurizer for little Miniature coal-fired boiler and application thereof
CN103920367B (en) The constant temperature absorption process of carbon dioxide removal and equipment from biogas
CN208406113U (en) A kind of calcination rotary kiln tail gas pre-concentration spent acid device
CN106322398A (en) Integrated straw environmentally-friendly incineration treatment system
CN202666636U (en) Smoke-gas treating system for ferromolybdenum smelting
CN205360881U (en) Dust removal and desulfuration device
CN104959006A (en) Treatment tower for flue gas from boilers
CN203784980U (en) Energy-saving boiler purification device
CN108704398A (en) A kind of useless fume purifying apparatus of rubber production

Legal Events

Date Code Title Description
MM4A Annulment or lapse of patent due to non-payment of fees