TWM335637U - Waste thermal decomposition gasification apparatus - Google Patents

Waste thermal decomposition gasification apparatus Download PDF

Info

Publication number
TWM335637U
TWM335637U TW96215817U TW96215817U TWM335637U TW M335637 U TWM335637 U TW M335637U TW 96215817 U TW96215817 U TW 96215817U TW 96215817 U TW96215817 U TW 96215817U TW M335637 U TWM335637 U TW M335637U
Authority
TW
Taiwan
Prior art keywords
waste
furnace
combustible gas
thermal decomposition
gasification
Prior art date
Application number
TW96215817U
Other languages
Chinese (zh)
Inventor
Hsin-Yi Wu
Tung-Te Chu
Jen-Chih Huang
Original Assignee
Hsin-Yi Wu
Tung-Te Chu
Jen-Chih Huang
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 Hsin-Yi Wu, Tung-Te Chu, Jen-Chih Huang filed Critical Hsin-Yi Wu
Priority to TW96215817U priority Critical patent/TWM335637U/en
Publication of TWM335637U publication Critical patent/TWM335637U/en

Links

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Gasification And Melting Of Waste (AREA)

Description

M335637 八、新型說明: 【新型所屬之技術領域】 本創作係關於-種廢棄物熱分解氣 於將廢棄物加減化產生她氣體,使結^^關 【先前技術】M335637 VIII. New description: [New technical field] This creation is about the thermal decomposition gas of wastes, which is used to add and subtract waste to produce her gas, so that the junction is closed. [Prior Art]

現今-般民生或工業廢棄物的數量及 且不穩定,舉例而言,目前台灣每年約產生2〇〇萬為镇= 的廢塑膠及10萬嘴左右的廢輪胎橡膠,其他如紹箱包、紙 盒、衛生杯等亦難以計數。因此,當以「直接焚燒」方式 —Z廢棄㈣’該廢棄物賴值_大,且該廢棄物不 ifcj易貝τ存,將其同時直接焚燒亦容易產生二次污染〔廢氣、 粉塵〕,制是_類或橡軸的廢棄物常在有氧燃^後 產生有毒成份,例如戴奥辛〔dioxin〕。 為了處理大里民生或工業廢棄物,業者不斷研發改良 廢棄物焚燒裝置,例如參照中華民國專利公告第4〇9172 號廢棄物氣化熔解爐以及氣化熔解方法」、第別1號 廢棄物處理方法」、第291104號「乾餾氣化焚化爐」及 第284839號「廢棄物之乾餾氣化焚化處理方法」等。上述 專利提供之焚化爐大致皆係先進行「乾餾氣化」產生可燃 性氣體,接著再利用所產生之可燃性氣體做為燃料焚燒該 廢棄物,以對該廢棄物進行處理。雖然該焚化爐多數設有 污染防治設備,但仍因具有燃燒反應,而容易產生二次污 M335637 2〔廢氣、粉塵、戴奥辛dioxin〕之問題。同時,該焚化 爐在設,大量污染防治設備後,卻也導致設備體積^化 ,因而需大面積的土地設廠,故不適於應用做為一般都市 的小型民生廢棄物處理設備。 斤另一習用廢棄物熱分解氣化裝置,如中華民國專利公 告第310638號「可回收資源與能源再利用之稻殼氣化裝^ 」新型專利,其包含一稻殼廢棄物輸送/進料機構、一氣化 爐及一除塵/除焦裝置。該稻殼廢棄物輸送/進料機構具有一 進料益。該氣化爐具有一進料口連結於該輸送/進料機構, 並另具有一排灰口及一可燃氣出口,使該進料口輪入之廢 棄物進行缺氧燃燒,而產生—可燃氣。該除塵/除焦裝置具 $-倾式降溫單元,並裝填有高孔隙廢棄物之一滤材。 運藉此,該除塵/除焦裝置可純化該氣化爐產生的可燃氣,該 廢棄物遽材則係用以吸收該可燃氣中的塵粒及焦油,使該 可燃氣透過該除塵/除焦裝置之純化後可送至該氣化爐^ 再利用作為燃料。再者,該習用稻殼氣化装置另選擇包含 -發電裝置’其連接於上述除塵/除焦裝置,並用以燃燒純 化後的可職而產生熱能,以供—發電機運轉而發電。 般而a,上述習用稻殼氣化裝置係應用「固態衍生 燃料〔refuse derived fuel,RDF〕的概念」,其缺點在於該習 用稻殼氣化裝置僅適用於特定廢棄物,例如稻殼、農產品 f棄物及木屑等。同時,該特定廢棄物在送入該氣化爐之 月[必須先處理成特定形狀之燃料塊,因此需利用大型機器 進仃刖處理。再者’不同之廢棄物無法任意混合製成該燃 —6 — M335637 料塊。換言之,其必須將廢棄物預先進行篩選及分類,而 耗用大1人力及设備’以致於徒增處理成本且不符經濟效 益0 此外,該習用廢棄物熱分解氣化裝置亦有利用煤炭做 為燃料來源者,其係藉由將該煤炭進行熱分解,進而氣化 成為一氧化碳及有機烷類等可燃氣體,亦即俗稱的「煤氣 」,其屬於「瓦斯」的u而,受限於煤炭運送成本、Today, the number of people's livelihoods or industrial wastes is unstable. For example, at present, Taiwan produces about 20,000 yuan of waste plastics and about 100,000 mouths of waste tire rubber every year. Others such as bags and papers. Boxes, sanitary cups, etc. are also difficult to count. Therefore, when the "direct incineration" method - Z waste (four) 'the waste value _ large, and the waste is not ifcj Yibei τ, it is also easy to produce secondary pollution (exhaust gas, dust) when it is directly incinerated. Wastes that are _ or rubber shafts often produce toxic components, such as dioxin, after aerobic combustion. In order to deal with Dali people's livelihood or industrial waste, the company has continuously developed improved waste incineration devices, for example, refer to the Republic of China Patent Bulletin No. 4, 917, and the gasification and melting furnace, and the gasification and melting method. "Cryogenic distillation gasification incinerator" No. 291104 and "Cryogenic gasification incineration treatment method for waste", etc. The incinerators provided by the above-mentioned patents generally perform "dry distillation gasification" to generate a combustible gas, and then use the generated combustible gas as a fuel to incinerate the waste to treat the waste. Although most of the incinerators are equipped with pollution prevention equipment, they still have the problem of secondary pollution M335637 2 [exhaust gas, dust, dioxin) due to the combustion reaction. At the same time, the incinerator is equipped with a large number of pollution control equipment, but it also leads to the volume of equipment. Therefore, it is necessary to set up a large-scale land, so it is not suitable for use as a small-scale civil waste treatment equipment in general cities. Another conventional waste thermal decomposition gasification unit, such as the Republic of China Patent Bulletin No. 310638, “Recyclable Resources and Energy Reuse of Rice Hull Gasification Equipment”, which includes a rice husk waste transportation/feeding mechanism. , a gasifier and a dust removal / decoking device. The rice husk waste conveying/feeding mechanism has a benefit. The gasification furnace has a feed port coupled to the conveying/feeding mechanism, and further has a discharge port and a combustible gas outlet, so that the waste in the feed port is subjected to anoxic combustion, and the combustion is generated. gas. The dust removal/defocusing device has a $-tilt cooling unit and is filled with a filter material of high porosity waste. In this way, the dust removal/defocusing device can purify the combustible gas generated by the gasification furnace, and the waste coffin material is used for absorbing the dust particles and tar in the combustible gas, so that the combustible gas passes through the dust removal/removal After the purification of the coke device, it can be sent to the gasifier for reuse. Further, the conventional rice husk gasification unit additionally includes a power generation unit connected to the dust removal/defocusing unit and used to burn the purified service to generate heat energy for the generator to operate to generate electricity. As a general matter, the above-mentioned conventional rice husk gasification device uses the concept of "refuse derived fuel (RDF)", which has the disadvantage that the conventional rice husk gasification device is only suitable for specific wastes, such as rice husks and agricultural products. f discarded and sawdust. At the same time, the specific waste is sent to the gasifier in the month [it must be processed into a fuel block of a specific shape, so it needs to be processed by a large machine. Furthermore, 'different wastes cannot be mixed arbitrarily to make the fuel- 6-M335637 block. In other words, it must pre-screen and classify the waste, and consume a large manpower and equipment' so that the cost of processing is increased and it is not economical. In addition, the waste thermal decomposition gasification unit also uses coal. For the fuel source, the coal is thermally decomposed and then vaporized into a combustible gas such as carbon monoxide and organic alkanes, which is commonly known as "gas", which belongs to "gas" and is limited by coal. Shipping cost,

污染嚴重及其設房極大㈣素,魏氣項僅能就近 設於煤炭產地或偏遠賴,且其設備亦不翻於處理複雜 的工業或民生廢棄物。 基於上述原因’有必要進一步改良上述各種習用廢辛 物熱分解氣化裝置。 惹化爐有=:==點依繼- 體導入一改質爐與高溫水蒸氣相混合, 溫使該初級可燃氣體進行裂解,進而轅:=水舰的: 〔一氧化碳、錢及有_鮮〕轉化為次級可燃氣體 棄物進行「加熱」,而非「燃燒由於本裝置僅對該廢 或粉塵等污祕,且、帛’二」*此不致產生二氧化碳 該次級可燃氣體,^廢棄物。同時,亦可收集 使用。藉此,本創作確或各種耗能設備做為燃料 【新型内容】 辰侏铋準。 本創作主要目 的係提供一種廢棄 物熱分解氣化裝置 M335637 ,其係藉由一氣化爐加熱廢棄物以產生初級可燃氣體,再 將該初級可燃氣體導入一改質爐與水蒸氣在高溫下相混合 ,進而轉化為次級可燃氣體,使得本創作具有降低污染、 提升處理效率、增廣處理範圍及縮小設備體積之功效。 根據本創作之廢棄物熱分解氣化裝置,其包含一氣化 爐及一改質爐,該氣化爐係用以加熱碳化一廢棄物,以氣 化產生初級可燃氣體;該改質爐係用以將該初級可燃氣體 與咼溫水蒸氣相混合,藉由水蒸氣的高溫裂解將該初級可 燃氣體轉化為次級可燃氣體,藉此該次級可燃氣體可供回 收使用。 【實施方式】 fJS》讓本創作之上述及其他目的、特徵、優點能更明顯 易懂’下文特舉本創作之較佳實施例,並配合所附圖式,、 作詳細說明如下:The pollution is serious and its housing is extremely large. The Wei gas project can only be located near the coal production area or remotely, and its equipment is not turned over to deal with complex industrial or residential waste. For the above reasons, it is necessary to further improve the above various conventional waste aging thermal decomposition gasification apparatuses. The aging furnace has =:== point continuation - the body is introduced into a reforming furnace and mixed with high temperature steam, the temperature is caused to crack the primary flammable gas, and then 辕: = water ship: [carbon monoxide, money and _ fresh 〕Transformed into secondary flammable gas waste for "heating" instead of "burning because the device only stains the waste or dust, and 帛 '2" * This does not produce carbon dioxide, the secondary flammable gas, ^ discarded Things. It can also be collected and used. In this way, this creation or a variety of energy-consuming equipment as a fuel [new content] Chen Haozhun. The main purpose of the present invention is to provide a waste thermal decomposition gasification device M335637, which heats waste to generate primary combustible gas by a gasification furnace, and then introduces the primary combustible gas into a reforming furnace and water vapor at a high temperature. The mixing, which is converted into a secondary combustible gas, enables the creation to reduce pollution, improve processing efficiency, increase processing range, and reduce equipment volume. According to the waste thermal decomposition gasification device of the present invention, the gasification furnace comprises a gasification furnace and a reforming furnace for heating carbonized waste to generate primary combustible gas by gasification; The primary combustible gas is mixed with the warm water vapor to convert the primary combustible gas into a secondary combustible gas by pyrolysis of water vapor, whereby the secondary combustible gas is available for recycling. [Embodiment] The above and other objects, features and advantages of the present invention will become more apparent and obvious. The following is a detailed description of the preferred embodiment of the present invention, and with reference to the drawings, the detailed description is as follows:

請參照第1圖所示,本創作較佳實施例之廢棄物執分 解氣化方法實質包含下列步驟:藉由—氣化爐加熱碳化一 廢棄物,以氣化產生她可喊體;賴她氣 入-改質爐與水蒸氣相混合,藉由水蒸氣的高溫裂解^亥 初級可燃氣雜化為纽可錢體;賴錢 入一洗·,崎低溫度及去及賴次級^^ =擇供躲魏倾或—麵設備使用。再者, 棄物進入該氣倾前,選擇_軸廢 ^ 分類及切碎之前處理。 《丁初芡師璉 分 請參照第2 _示,摘作她實❹)之廢棄物熱 M335637 =、二置係依序包含—氣化爐1、—排灰設備2、一改質 二借—f㈣4及—熱回钱備5,同時另選擇包含-耗 I ’該耗綠備6可選自—鋪q或-内燃機62 =廢^熱分解氣化裝置之詳細構造將於下列廢棄物熱 刀解=化方法之各步驟另予詳細說明。 減二Γ㈣第1及2 _示’本創作較佳實施例之廢棄 轉it化方法第—步驟係:#由該氣化爐1加熱碳化 η氣化產生初級可燃氣體。更詳言之,該廢 tf ·* 機廢杳^自各種民生駐業廢棄物,特別是含有碳之有 =棄物’例如:紙類、塑膠類、橡膠類、蔬果廚餘等。 “乳fc*爐1係呈圓形且具内爐之爐體,其上方設有一進料 4匕爐1用以提供6(Krc至響c的高溫,以便在缺 乏氧氣的狀態下加熱該廢棄物9,使該廢棄物9碳化,以 造成該廢棄物9將所含的部份有機成份氣化成為初級可燃 氣體。该初級可燃氣體的成份複雜〔CxIiy〇z,卜 ,GO〕,且通常不可避免的夾帶有粉塵、焦油或其他雜 貝再者,遠氣化爐1之内爐與外壁之間可選擇夾設有一 水冷官路11,以精確控制爐内溫度,同時該水冷管路Η 吸熱產生之水蒸氣亦可經由-管路12連接至該^爐6ι, 以供该鋼爐61之蒸氣室〔未緣示〕使用。再者,在&成炙 化後,該氣化爐1中殘留的該廢棄物9化為炭化灰爐,^ 由該排灰設備2回收,該炭化灰燼的數量極少,且可適: 收集掩埋,或回收用於製造環保材料〔例如地碑〕或肥二 M335637 基材寻。在廢鐵回收方面,炭 ‘示〕篩選炭化灰爐 送機〔未綸^ 又燼亦可經由一振動式輸 禾、,θ不〕輸达至一磁選機〔未给. 中的廢鐵,以供再生利用。 曰 再者,如第1圖所示,在進 可:的對該廢棄物9進行=:== 廢莱物9進行初步篩選分類及 貞先將孩 物9集中,並將體積過大之廢辛儘量將同類廢棄 堆塊〔例如正刪〕,以碎至㈣公分之小 内可形成具空隙的膨鬆堆疊狀態,以利 ff 可選擇裝設數個隔條〔未緣示〕,以利膨 二衫宜該廢莱物9。必要時,該隔條可選自水冷管路, 可^通入"部水’進而控制爐内溫度。同時,該隔條亦 2先塗覆適當的化學物質,以先行去除初級可燃氣體中 Ϊ污染或防止其產生有害污染成份。 月再、第1及2圖所示,本創作較佳實施例之廢棄 物2分解氣化枝第二步驟係:將該初級可燃氣體導入〆 文貝j 3與水療氣相混合,藉由水蒸氣的高溫裂解將初級 可,氣體轉化為次級可燃氣體。更詳言之,該改質爐3同 樣提供6GGC至8GGX:或更高的溫度,例如乃叱至10〇〇 C同恰,該改質爐3可由適當來源提供水蒸氣〔H20〕 例如由該鋼爐61之蒸氣室經由一管路6n導入水蒸氣。 ^述水瘵氣在此高溫環境下會先行裂解成氫氣〔H2〕及 氧氣〔02〕。當該氫氣及氧氣與該初級可燃氣體相混合時 一 10—— M335637 ’可將相=可燃氣體進-步轉化為*級可燃氣體。該次 級可燃氣體θ冑包含—氧化碳、氫氣及有機錢〔c卿 ,d ’例如甲焼〕,其不含碳元素或者碳鍵長度 相對較低’因此有利於提升可燃氣體之触及後續回收^ 用之燃燒效率。再者,誠_ 3可將焦油或有害物質由 該次級可職體_去,以相戦傾她可職體之組Referring to FIG. 1 , the waste decomposition gasification method of the preferred embodiment of the present invention substantially comprises the following steps: heating a carbonized waste by a gasification furnace to generate her screaming body by gasification; The gas-into-type reforming furnace is mixed with water vapor, and the high-temperature cracking of water vapor is used to make the primary flammable gas hybrid into the neon money body; the money is poured into a wash, the temperature is low, and the secondary is to be subordinated ^^ = Choose to hide from Wei or use equipment. In addition, before the waste enters the gas dump, select the _axis waste ^ classification and the pre-chopping treatment. "Ding Chuyi's teacher's points, please refer to the second _, shown as her actual sputum." Waste heat M335637 =, two sets are included in sequence - gasifier 1, - ash equipment 2, a modified two borrow -f (4) 4 and - hot return money reserve 5, while also selecting inclusion - consumption I 'The green preparation 6 can be selected from - shop q or - internal combustion engine 62 = waste ^ thermal decomposition gasification device detailed structure will be the following waste heat The steps of the knife solution = method are described in detail. Subtraction (4) 1st and 2nd shows the waste of the preferred embodiment of the present invention. The first step is: # Heating the carbonization η by the gasification furnace 1 to generate a primary combustible gas. More specifically, the waste tf ·* machine wastes from various wastes from the people's livelihood, especially those containing carbon = discarded goods such as: paper, plastic, rubber, fruits and vegetables. "The milk fc* furnace 1 is a circular and inner furnace body with a feed 4 furnace 1 above to provide a high temperature of 6 (Krc to c) to heat the waste in the absence of oxygen. Item 9, carbonizing the waste 9 to cause the waste 9 to vaporize a part of the organic components contained therein into a primary combustible gas. The composition of the primary combustible gas is complicated [CxIiy〇z, Bu, GO], and usually Inevitably with dust, tar or other miscellaneous shells, a water-cooled official road 11 can be optionally placed between the furnace and the outer wall of the gasification furnace 1 to precisely control the temperature inside the furnace, and the water-cooled pipeline is The water vapor generated by the heat absorption may also be connected to the furnace 6 through the line 12 for use in the steam chamber of the steel furnace 61. Further, after the & The waste 9 remaining in 1 is turned into a carbonized ash furnace, and is recovered by the ash discharging device 2, and the amount of the carbonized ash is extremely small, and may be suitable for: collecting and burying, or recycling for manufacturing environmentally friendly materials (such as a monument) or Feiji M335637 substrate search. In the aspect of scrap iron recycling, carbon 'showing' screening carbonized ash furnace delivery machine [Unbonded and untwisted can also be transported to a magnetic separator through a vibrating type of gas, θ is not] (not given scrap iron for recycling). Again, as shown in Figure 1, In the advancement: the waste 9 is carried out =:== Waste Laundering 9 is initially screened and classified, and the child 9 is concentrated first, and the waste that is too large is tried to waste the same kind of heap (for example, deleted) In the small size of (4) centimeters, a bulky and bulky stacking state can be formed, so that ff can be installed with several spacers (not shown), so that the second crop should be used for the waste. The spacer can be selected from a water-cooled pipeline, and can be controlled to control the temperature in the furnace. At the same time, the spacer is also coated with an appropriate chemical substance to remove the pollution of the primary combustible gas first. Or prevent it from producing harmful pollutants. In addition, as shown in Figures 1 and 2, the second step of decomposing the gasification branch of the waste 2 of the preferred embodiment is: introducing the primary combustible gas into the 〆文贝j 3 and The spa is mixed in the gas phase, and the primary gas can be converted into a secondary combustible gas by pyrolysis of water vapor. In other words, the reforming furnace 3 also provides a temperature of 6GGC to 8GGX: or higher, for example, to 10 〇〇C, and the reforming furnace 3 can supply water vapor [H20] from a suitable source, for example, by the steel furnace. The steam chamber of 61 introduces water vapor through a line 6n. The water helium gas is first cracked into hydrogen gas [H2] and oxygen gas [02] in this high temperature environment. When the hydrogen gas and oxygen gas are mixed with the primary combustible gas body, A 10 - M335637 ' can convert phase = combustible gas into a * grade combustible gas. The secondary combustible gas θ 胄 contains - carbon oxide, hydrogen and organic money [cqing, d 'such as formazan), It has no carbon content or a relatively low carbon bond length', so it is beneficial to improve the combustion efficiency of the combustible gas and subsequent recovery. In addition, Cheng _ 3 can use tar or harmful substances to go to the group of servables.

請再翏照第1及2圖所示,本創作較佳實施例之廢棄 物熱分解氣化方法第三步_ :將次級可燃氣體導入—洗 滌槽4 ’崎低、溫歧去_質。更詳言之,該洗;條槽* 係以遽水方式降低次級可燃氣體之溫度及去除粉塵等雜質 ’至此該姐可燃氣體已完成大部份之純化流程。再者,、 該洗蘇槽4較佳進-步另設有至少—量測儀器41’以供量 測該次級可燃氣體的組絲分,以便對應婦後續導入該 耗能設備6〔例如該鋼爐61或内燃機62〕時之使用流量。 接著:在完成m水錢及量測動作後,該次級可㈣體里進 請再參照第!及2圖所示,本創作較佳實施例务辛 物熱分解氣化方法第四步驟係:將次級可庫 給該氣化爐1或耗能設備ό使用。 + — 田、al n U 口干0之’在元成洗滌 ^測及熱回收後,該次級可_氣體可回收做為辅助辦料 或主燃料使用,以供選擇加熱該氣化爐丨之㈣,或^ 用於任一耗能設備6,進而相尉節省本創作氣化裝置的外 :步導^熱贼設備5 ’其㈣回收高溫廢熱,以提供 創作氣化裝置之锅爐61或其他相關設備使用。 ——11 - M335637 加燃料需求。例如,當該耗能設備6選自該鍋爐61時,該 锅爐61由该官路12取得該氣化爐1之水冷管路n所產生 的冷4卩水或水蒸氣’同時再藉由織該次級可燃氣體,進 一步獲付南壓水蒸氣。該高壓水蒸氣可選擇經由一管路 611輸运至該改質爐3處使用,或選擇導人—蒸氣渦輪發 電機612 |生電力,以供運作本創作氣化裝f。再者,當 口亥耗又備6選自該内燃機幻時,該内燃機以將該次級 可1、:氣體w人引擎燃料中燃燒,接著再經由—引擎式發電 機621產生電力’以供運作本創作氣化裝置。 厂如上所述,相較於習用廢棄物處理方法及其裝置利用 直接火k」先乾餘再焚燒」或「固態衍生燃料概念」 等方法進行廢棄物的處理時,常具有產生二次污染,不適Please refer to the first and second figures, the third step of the waste thermal decomposition gasification method of the preferred embodiment of the present invention _: introducing the secondary combustible gas into the washing tank 4 'slow, temperature difference _ quality . More specifically, the washing; the trough* reduces the temperature of the secondary combustible gas and removes impurities such as dust by means of drowning. The flammable gas of the sister has completed most of the purification process. Furthermore, the sachet 4 is preferably further provided with at least a measuring instrument 41' for measuring the component of the secondary combustible gas so as to be subsequently introduced into the energy consuming device 6 (for example, The flow rate is used in the steel furnace 61 or the internal combustion engine 62. Then: After completing the m water money and measurement action, the secondary can be in the (four) body. Please refer to the second! As shown in Fig. 2, the fourth step of the preferred embodiment of the symplectic thermal decomposition gasification method is to use the secondary reservoir to the gasification furnace 1 or the energy consuming equipment. + — Tian, al n U dry 0' After the Yuancheng washing and heat recovery, the secondary _ gas can be recycled as auxiliary material or main fuel for heating to the gasifier 丨(4), or ^ used in any energy-consuming device 6, and thus saves the outside of the creation of the gasification device: step guide ^ hot thief equipment 5 'the (four) recover high-temperature waste heat to provide a boiler for creating a gasification device 61 Or other related equipment. ——11 - M335637 Refueling demand. For example, when the energy consuming device 6 is selected from the boiler 61, the boiler 61 obtains the cold water or water vapor generated by the water cooling pipe n of the gasification furnace 1 by the official road 12 while The secondary combustible gas is woven, and the south pressure water vapor is further paid. The high pressure steam may optionally be transported via a line 611 to the reformer 3 or selected to be a steam turbine generator 612 to generate electricity for operation of the inventive gasification unit f. Moreover, when the battery is further selected from the engine, the internal combustion engine burns the secondary energy: 1: gas, and then generates power through the engine generator 621 for operation. This creation gasification device. As mentioned above, the factory often produces secondary pollution when it is disposed of by means of direct fire treatment, such as direct fire treatment, or solid-state derivative fuel concept. Discomfort

用於,理民生、工業廢棄物,耗用大量人力及設備,或佔 ,大里廠房土地等缺點,第丨及2圖之本創作依序藉由該 ,化爐1加熱該廢棄物9產生初級可燃氣體,將初級可燃 =導入該改質爐3與水蒸氣相混合,藉由水蒸氣的高溫 ^I進而將初級可燃氣體進一步轉化為次級可燃氣體〔 ,乳化碟、域及有__〕。由 「,氧炭化〔部份氧化〕」,因此所需空氣量較「直接燃燒 j二且不致產生戴奥辛等有毒物質,亦不致產生過量之 碳或粉塵等污染物。該氣化爐1之進料彈性大,構 =早’操作容易,適用於處理各式廢棄物9。同時,該 亦可Μ供該氣化爐2或各種耗能設備6使 此’本創作確實能降低污染、提升處職率、增廣 —12 — M335637 處理範圍、簡化構造及操作,並能符合曰益嚴格 二準。 保榡 ' 雖然本創作已利用上述較佳實施例揭示,然其並非用 • 以限定本創作,任何熟習此技藝者,在不脫離本創作之= - 神和範圍之内,當可作各種更動與修改,因此本創作之^ 護範圍當視後附之申請專利範圍所界定者為準。Used for the treatment of people's livelihood, industrial waste, the consumption of a large number of manpower and equipment, or the occupation, the land of Dali plant and other shortcomings, the first and second figures of the creation of the original by the furnace 1, heating the waste 9 to produce the primary The combustible gas is introduced into the reforming furnace 3 and mixed with water vapor, and the primary combustible gas is further converted into the secondary combustible gas by the high temperature of the steam [, the emulsified dish, the domain and the __] . By "oxygenation (partial oxidation)", the amount of air required is lower than that of "direct combustion" and does not cause toxic substances such as dioxin, and does not cause excessive carbon or dust. The material has large elasticity, and the structure is early and easy to operate. It is suitable for treating all kinds of wastes. 9. At the same time, it can also be supplied to the gasifier 2 or various energy-consuming equipment 6 so that this creation can really reduce pollution and elevation. Occupation rate, augmentation — 12 — M335637 Processing scope, simplification of construction and operation, and compliance with strict standards. 榡 榡' Although this creation has been disclosed using the above preferred embodiment, it is not used to limit the creation Anyone who is familiar with this skill can make various changes and modifications without departing from the scope of this creation. Therefore, the scope of this creation is subject to the definition of the patent application scope attached.

—13 — M335637 【圖式簡單說明】 第1圖:本創作較佳實施例之廢棄物熱分解氣化方法之 流程方塊圖。 第2圖:本創作較佳實施例之廢棄物熱分解氣化裝置之 系統方塊圖。 【主要元件符號說明】—13 — M335637 [Simple description of the drawings] Fig. 1 is a flow block diagram of the waste thermal decomposition gasification method of the preferred embodiment of the present invention. Figure 2 is a block diagram of the system of the waste thermal decomposition gasification apparatus of the preferred embodiment of the present invention. [Main component symbol description]

1 氣化爐 11 水冷管路 12 管路 2 排灰設備 3 改質爐 4 洗滌槽 41 量測儀器 5 熱回收設備 6 耗能設備 61 锅爐 611 管路 612 蒸氣渦輪發電機 62 内燃機 621 引擎式發電機 9 廢棄物1 Gasifier 11 Water-cooled pipeline 12 Pipeline 2 Ash-discharging equipment3 Modification furnace4 Washing tanks41 Measuring equipment5 Heat-recycling equipment6 Energy-consumption equipment61 Boiler 611 Pipeline 612 Steam turbine generator62 Internal combustion engine 621 Engine type Generator 9 waste

——14————14——

Claims (1)

M335637 九、申清專利範圍: 種廢棄物熱分解氣化裝置,其包含: 乳化爐,翻以加熱碳化—廢棄物,以氣化產生初 級可燃氣體;及 質爐,其用以將該初級可燃氣體與高溫水蒸氣相 :口’藉由水蒸氣的高溫裂解將該初級可燃氣體轉化為 -人級可燃氣體,藉此該次級可燃氣體可供回收使用。 2依申利^圍第丨項所述之廢棄物熱分解氣化裝置, 其中該氣化爐之内爐與外壁之間夾設一水冷管路 確控制爐内溫度。 3申請專利範圍第2項所述之廢棄物熱分解氣化裝置,M335637 Nine, Shenqing patent scope: a waste thermal decomposition gasification device, comprising: an emulsion furnace, which is heated to carbonize-waste to generate primary combustible gas by gasification; and a furnace for burning the primary combustion The gas and the high-temperature water vapor phase: the mouth's high-temperature cracking of the water vapor converts the primary combustible gas into a human-grade combustible gas, whereby the secondary combustible gas is available for recycling. 2 The waste thermal decomposition gasification device according to the above item, wherein a water-cooled pipeline is arranged between the furnace and the outer wall of the gasification furnace to control the temperature inside the furnace. 3 The waste thermal decomposition gasification device described in item 2 of the patent application scope, 設有-銷爐,該水冷管路吸熱產生之水蒸氣可經 s路連接至祕爐’以供該峨之蒸氣室使用。 4=申請專觀_顧叙廢棄物熱分解氣化裳置, ,、中雜爐絲之蒸氣經由—f路導人該 以 該改質爐使用。 貝I以仏 斤述之廢棄物熱分解氣化裝置, 所備,收該軸殘留廢棄物 H請專纖®f i項所敎廢棄物齡解氣 其中该氣化爐之内爐中選擇又 疊該廢棄物。 膨鬆堆 ^請翻制第6_述之廢棄物熱分解氣化壯晉, ”中5亥隔條選自水冷管路,以人一 、衣置 入々部水控制爐内溫度 —15 M335637 8、 依申請專利範圍第7項所述之廢棄物熱分解氣化舉置 其中該隔條可預先塗覆化學物質,以先行處理初可燃 氣體中之有害污染成份。 9、 依申請專利範圍第1項所述之廢棄物熱分解氣化妒置 其中另設有一洗滌槽,以對回收之該次級可燃氣^進」 降低溫度及去除雜質。 订 ιυThere is a pin furnace, and the water vapor generated by the heat absorption of the water-cooled pipeline can be connected to the secret furnace by the s road for use in the steam chamber of the crucible. 4=Apply for the subjective _Gu Syria waste thermal decomposition gasification skirt,,, the steam of the Zhongzao furnace wire through the -f road guide to use the modified furnace. Bei I is prepared by the waste heat decomposition gasification unit, and the residual waste H of the shaft is collected. The waste fiber is deficient in the waste product, and the furnace is selected in the furnace. Waste. Expanded piles ^ Please turn over the 6th_discussed waste thermal decomposition gasification and vigorous development, "The 5th slat spacer is selected from the water-cooled pipeline, and the temperature of the furnace is controlled by the person and the clothes are placed in the crotch water - 15 M335637 8. The waste thermal decomposition gasification according to item 7 of the patent application scope may be pre-coated with a chemical substance to treat the harmful pollutants in the primary combustible gas first. The waste thermal decomposition gasification unit described in item 1 is further provided with a washing tank for reducing the temperature and removing impurities of the recovered secondary combustible gas. Order ιυ 依申請專利範圍第 #軋化裝置 其中該洗滌槽另設有至少一量測儀器,以供量测該文# 可燃氣體的組成成分。 11、 依申請專利範圍第9項所述之廢棄物熱分解氣化事 其中另設有一熱回收設備,其連接在該洗滌槽之後, 以回收該次級可燃氣體之南溫廢熱。 12、 依申請專利範圍第i項所述之廢棄物熱分解氣化裝置, 其中另設有-耗能設備,以使用时之該次級可^氣體 13、 依申請專利範㈣12項所述之廢棄物熱分解氣化 ,其中該耗能設備選自-峨,該峨藉㈣燒診二 可燃氣體,以獲得高壓水蒸氣,該高壓水蒸氣選擇^級 一条氣渦輪發電機,以產生電力。 夺入 Η、依^專補圍第12項所述之廢棄物熱分解氣化 ”中雜能設備選自-内燃機,該_機將、复 燃氣體混人引擎燃料中燃燒,並經由—引擎式發 生電力。 X免機產 16〜According to the patent application scope #轧化装置, the washing tank is further provided with at least one measuring instrument for measuring the composition of the article # combustible gas. 11. Thermal decomposition gasification of waste according to item 9 of the patent application scope. A heat recovery device is additionally provided, which is connected after the washing tank to recover the south temperature waste heat of the secondary combustible gas. 12. The waste thermal decomposition gasification device according to item i of the patent application scope, wherein there is additionally an energy-consuming device, the secondary gas can be used at the time of use, according to the application of the patent (4) The waste is thermally decomposed and gasified, wherein the energy-consuming device is selected from the group consisting of - 峨, and the second combustible gas is burned to obtain high-pressure steam, and the high-pressure steam is selected to generate a gas turbine generator to generate electricity. The medium-hetero energy equipment of the waste heat decomposition gasification mentioned in Item 12 is selected from the internal combustion engine, which is burned in the engine fuel of the compound gas and passed through the engine. Electricity generation. X free machine 16~
TW96215817U 2005-11-07 2005-11-07 Waste thermal decomposition gasification apparatus TWM335637U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
TW96215817U TWM335637U (en) 2005-11-07 2005-11-07 Waste thermal decomposition gasification apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
TW96215817U TWM335637U (en) 2005-11-07 2005-11-07 Waste thermal decomposition gasification apparatus

Publications (1)

Publication Number Publication Date
TWM335637U true TWM335637U (en) 2008-07-01

Family

ID=44328713

Family Applications (1)

Application Number Title Priority Date Filing Date
TW96215817U TWM335637U (en) 2005-11-07 2005-11-07 Waste thermal decomposition gasification apparatus

Country Status (1)

Country Link
TW (1) TWM335637U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI381143B (en) * 2012-03-02 2013-01-01 Taiwan Clean Energy Technology Co Ltd Material Heat Treatment Separation and Energy Recovery System
CN113777046A (en) * 2021-08-06 2021-12-10 中国环境科学研究院 Method for measuring and calculating emission of carbon dioxide generated by incineration treatment of waste

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
TWI381143B (en) * 2012-03-02 2013-01-01 Taiwan Clean Energy Technology Co Ltd Material Heat Treatment Separation and Energy Recovery System
CN113777046A (en) * 2021-08-06 2021-12-10 中国环境科学研究院 Method for measuring and calculating emission of carbon dioxide generated by incineration treatment of waste

Similar Documents

Publication Publication Date Title
CN101713304B (en) Method for cycle power generation by carrying out wet decomposition pretreatment, dry distillation and gasification on domestic garbage
CN201795494U (en) Refuse pyrolysis produced gas treatment device
CN1769397A (en) Device and method for suppressing refuse end gas injurant using pyrolysis and aerification technology
WO2021174911A1 (en) Method for embedding waste-plastic oilification technology in garbage incineration
CN102936518A (en) Household garbage coupling fluidized bed grading pyrolysis gasification technology
CN105737162A (en) Household garbage low-temperature pyrolysis system and method based on process decoupling and scrubbing combustion
CN106590702A (en) Low-temperature pyrolysis power generation system and method for household garbage
CN112161273B (en) Harmless treatment device and method for household garbage
CN108911459A (en) A kind of municipal sludge pyrolysis processing set technique and device
CN111004640A (en) Household garbage pyrolysis carbonization disposal system and method
CN105861072A (en) Method and system for preparing high-concentration CO from waste carbon
CN105820845B (en) Large-scale house refuse is classified fast pyrogenation preparing fuel gas by gasifying technique
CN102977929B (en) Household garbage coupling fluidized bed hierarchical pyrolytic gasifier
CN208186364U (en) A kind of novel household garbage pyrolysis gasification furnace
CN109355071A (en) City house refuse treatment method and processing system
CN204114952U (en) RDF burning electricity generation system prepared by a kind of clean and effective rubbish
CN209456367U (en) System for treating municipal solid waste
CN202912917U (en) Graded pyrolyzing gasifier of domestic garbage coupled fluidized bed
TWM335637U (en) Waste thermal decomposition gasification apparatus
CN102536460A (en) Method and system for recycling electric energy of waste heat of plasma
CN108087884A (en) A kind of odor at low temperature refuse pyrolysis treatment device and its method
CN101974351B (en) Scale fixed bed biomass gasification power generation production technology and suite of equipment
JP2003320359A (en) Method and apparatus for pyrolyzing organic waste
CN210826081U (en) Double-bed pyrolysis gasification device for municipal domestic waste
CN212525405U (en) System for treating household garbage