TW201023965A - Soot extraction and biological treatment method and apparatus - Google Patents
Soot extraction and biological treatment method and apparatus Download PDFInfo
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- TW201023965A TW201023965A TW097151306A TW97151306A TW201023965A TW 201023965 A TW201023965 A TW 201023965A TW 097151306 A TW097151306 A TW 097151306A TW 97151306 A TW97151306 A TW 97151306A TW 201023965 A TW201023965 A TW 201023965A
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- soot
- extraction
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- oil
- biological treatment
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- 239000004071 soot Substances 0.000 title claims abstract description 42
- 238000000605 extraction Methods 0.000 title claims abstract description 38
- 238000000034 method Methods 0.000 title claims abstract 4
- 239000003599 detergent Substances 0.000 claims abstract description 19
- 239000002351 wastewater Substances 0.000 claims abstract description 19
- 241000894006 Bacteria Species 0.000 claims abstract description 16
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 10
- 239000002736 nonionic surfactant Substances 0.000 claims abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 7
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 5
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 5
- 238000006731 degradation reaction Methods 0.000 claims abstract description 4
- 230000015556 catabolic process Effects 0.000 claims abstract description 3
- 239000007789 gas Substances 0.000 claims description 20
- 238000000354 decomposition reaction Methods 0.000 claims description 10
- 239000003517 fume Substances 0.000 claims description 10
- 239000007864 aqueous solution Substances 0.000 claims description 8
- 238000000889 atomisation Methods 0.000 claims description 7
- 241000589516 Pseudomonas Species 0.000 claims description 5
- 238000004140 cleaning Methods 0.000 claims description 4
- IGFHQQFPSIBGKE-UHFFFAOYSA-N Nonylphenol Natural products CCCCCCCCCC1=CC=C(O)C=C1 IGFHQQFPSIBGKE-UHFFFAOYSA-N 0.000 claims description 3
- 239000002202 Polyethylene glycol Substances 0.000 claims description 3
- 150000001298 alcohols Chemical class 0.000 claims description 3
- 238000006065 biodegradation reaction Methods 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 3
- SNQQPOLDUKLAAF-UHFFFAOYSA-N nonylphenol Chemical compound CCCCCCCCCC1=CC=CC=C1O SNQQPOLDUKLAAF-UHFFFAOYSA-N 0.000 claims description 3
- 229920001223 polyethylene glycol Polymers 0.000 claims description 3
- 238000005086 pumping Methods 0.000 claims description 3
- 239000004576 sand Substances 0.000 claims description 3
- 241000589517 Pseudomonas aeruginosa Species 0.000 claims description 2
- -1 dodecane octaethylene group Chemical group 0.000 claims description 2
- 238000011049 filling Methods 0.000 claims description 2
- 239000003595 mist Substances 0.000 claims description 2
- USIUVYZYUHIAEV-UHFFFAOYSA-N diphenyl ether Chemical compound C=1C=CC=CC=1OC1=CC=CC=C1 USIUVYZYUHIAEV-UHFFFAOYSA-N 0.000 claims 2
- XKHGVESTJQBYDL-UHFFFAOYSA-N CCCCCCCCCCCC.C(COCCOCCOCCOCCOCCOCCOCCO)O Chemical compound CCCCCCCCCCCC.C(COCCOCCOCCOCCOCCOCCOCCO)O XKHGVESTJQBYDL-UHFFFAOYSA-N 0.000 claims 1
- TVMXDCGIABBOFY-UHFFFAOYSA-N octane Chemical compound CCCCCCCC TVMXDCGIABBOFY-UHFFFAOYSA-N 0.000 claims 1
- 125000002347 octyl group Chemical group [H]C([*])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])C([H])([H])[H] 0.000 claims 1
- 238000005201 scrubbing Methods 0.000 claims 1
- 239000000126 substance Substances 0.000 claims 1
- 239000004094 surface-active agent Substances 0.000 claims 1
- 238000005406 washing Methods 0.000 abstract description 7
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 abstract description 2
- 230000000694 effects Effects 0.000 description 6
- 238000004945 emulsification Methods 0.000 description 3
- 238000010992 reflux Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 239000000969 carrier Substances 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 1
- PTFCDOFLOPIGGS-UHFFFAOYSA-N Zinc dication Chemical compound [Zn+2] PTFCDOFLOPIGGS-UHFFFAOYSA-N 0.000 description 1
- 238000003915 air pollution Methods 0.000 description 1
- 239000012298 atmosphere Substances 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- DNJIEGIFACGWOD-UHFFFAOYSA-N ethanethiol Chemical compound CCS DNJIEGIFACGWOD-UHFFFAOYSA-N 0.000 description 1
- 239000000945 filler Substances 0.000 description 1
- 239000004519 grease Substances 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 229910001425 magnesium ion Inorganic materials 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- GLZWNFNQMJAZGY-UHFFFAOYSA-N octaethylene glycol Chemical group OCCOCCOCCOCCOCCOCCOCCOCCO GLZWNFNQMJAZGY-UHFFFAOYSA-N 0.000 description 1
- 229920002113 octoxynol Polymers 0.000 description 1
- 229910001415 sodium ion Inorganic materials 0.000 description 1
- 239000011573 trace mineral Substances 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A50/00—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE in human health protection, e.g. against extreme weather
- Y02A50/20—Air quality improvement or preservation, e.g. vehicle emission control or emission reduction by using catalytic converters
Landscapes
- Treating Waste Gases (AREA)
- Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
Abstract
Description
201023965 六、發明說明: 【發明所屬之技術領域】 本發_與油煙處理裝置,更詳而言之,尤指可有效降 解廢水之乳化油,並形成反覆循環系統。 【先前技術】 兹因人類邁人工紐技時代後,生活水準普遍提高,而為了 讓下一代也能有更好的生活品質,環保意識逐漸抬頭。 坊間很多餐飲業者由於必需每天從事煮、煎炒、甚至油炸等 春調理工作,油品經過高溫或重複使用後容易產生援人的油煙問 題’每年跟惡臭有關的公害陳情案件至少有一萬四仔多起,其中 43%與餐飲業油煙排放有關,其產生的域污染與廢水問題則對環 境有相當大的衝擊,因此多數業者會加裝抽油煙機,直接將油煙 抽到室外大氣中,造成附近環境的空氣污染相當嚴重,而有些業 者則是將廚房抽油煙機抽出的油煙直接導引至下水道内,雖然不 會直接影響附近環境的空氣品質,但經過一段時日後,就會引起 鲁下水道油污的問題’不但會造成下水道的堵塞而影響排水機能, 甚至產生水資源的污染,造成另一環境污染的問題。 【發明内容】 本發明之主要目的係藉由雜子型界面活賴之洗滌劑配合 油脂分解菌,達到將油煙廢氣及油滴廢水完全去除目的。 為達上述目的’本發明係利用一非離子型界面活性劑之洗蘇 劑對油煙廢氣洗蘇,以有效乳化油煙廢氣並產生一含乳化油的廢 水,再以一油脂分解菌將該廢水之乳化油降解成二氧化碳及水, 3 201023965 降解後之水溶液則再混入該洗滌劑反覆循環繼續洗滌油煙廣氣。 據此,本發明可以反覆洗滌油煙廢氣,以達到將油煙廢氣及 油滴廢水完全去除目的。 【實施方式】 理 首先,請參閱『圖1』所示,係為本發明油煙萃取暨生物處 裝置’其主要係由一油煙萃取裝置10及一生物處理裝置20所組 成 該油煙萃取裝置10設有一萃取單元U,該萃取單元U為塔 籲狀,並於上、下方設有一霧化單元110、一油煙進氣口 m、一^ 水控制口 112及一抽氣幫浦單元12,且該萃取單元u内部填充至 少一葉片型雙十字圓環混合砂網做為填充濾料(圖未示)。 該生物處理裝置20設有一生物分解單元21、一迴流幫浦單元 22、一排放清洗口 23及數片生物載體(圖未示),且該生物分解單 元21内係放置適量非離子型界面活性劑之洗滌劑及油脂分解菌。 使用時’主要分成兩大步驟: ❹ 步驟A為一油煙廢氣洗滌程序: 該油煙廢氣主要透過該油煙進氣口 U1並利用該抽氣幫浦單 兀12抽引進入萃取單元11内,配合該迴流幫浦單元22將該生物 分解單元21内非離子型界面活性劑(例如壬基苯酚聚乙氧基醇類 化合物(NPnE0)、聚乙二醇辛基苯基趟(Triton-X)、十二燒八乙二 醇基(CH3(CH2)ll(〇CH2CH2)80H)之洗滌劑導引至該萃取單元11 内’藉由該洗務劑可有效乳化油煙廢氣並提昇乳化效果,並產生 4 201023965 一洗條後的廢水; 該萃取單元1丨中填充葉片型雙十字圓環混合砂網做為填充 料,且該非離子型界面活性劑之洗滌劑在導入該萃取單元11前, 得經過該霧化單元110形成霧狀後,再以霧化方式喷灑對該油煙 廢氣進行洗滌,如此洗滌效果較佳。 步驟B為一廢水降解程序: 將油煙廢氣經洗滌後之廢水透過該出水控制口 112流至該生 _物分解單元21内,且該廢水因經該洗滌劑乳化後會含有一乳化 油,該乳化油可做為該生物分解單元21之油脂分解菌,該油脂分 解滅可為假單胞菌屬(pseudomonas)(如綠膿桿菌(pseudomonas aeruginosa))主要碳源,並藉由該數片生物載體幫助菌株附著生 長,經由油脂分解菌將廢水之乳化油降解成二氧化碳及水溶液, 以達成去完全去除油煙之效果,而經過油脂分解菌降解後之水溶 液’再藉由該迴流幫浦單元22導引至該萃取單元U内以混入洗 _滌劑繼續洗滌油煙廢氣,據此形成一反覆循環系統,使得油脂降 解率可維持在99%以上。 另,值得一提的是該廢水之乳化油僅能提供生物分解單元21 中之油脂分解菌生長之碳源,並無法長期維持菌株活性 ,因此需 適時添加油脂分解菌生長所需的微量元素(如鎂離子、鋅離子、鐵 離子、鈣離子、鈉離子)以維持生物分解單元21 一定的處理能力。 以及,為防止該生物載體上因菌株生長過度而造成生物膜過 度肥厚、發臭現象,因此可藉由排放清洗口 23適時更換並清洗生 5 201023965 物分解單元21中之生物載體。 本發明利用非離子型界面活性劑之洗滌劑促進油煙廢氣之洗 滌效率’且將洗滌劑之濃度控制在〇· 1體積百分比(v〇1%)以下’ 不僅不會影響該油脂分解菌之生長,更可促進油煙廢氣之油脂乳 化效果,使油脂更谷易被微生物分解,並且將油煙廢氣及洗條劑 之氣液比控制在1. 3,滯留一段時間(以264秒為最佳),其油煙乳 化效率可高達98%。 φ 惟上述僅為本發明之較佳實施例而已,並非用來限定本發明 實施之範圍。即凡依本發明申請專利範圍所做的均等變化與修 飾’皆為本發明專利範圍所涵蓋。 201023965 •【圖式簡單說明】 圖1為本發明油煙萃取暨生物處理裝置結構示意圖。 【主要元件符號說明】 10 :油煙萃取裝置 11 :萃取單元 110 :霧化單元 111 :油煙進氣口 112 :出水控制口 ❿12:抽氣幫浦單元 20 :生物處理裝置 21 :生物分解單元 22 :迴流幫浦單元 23 :排放清洗口201023965 VI. Description of the invention: [Technical field to which the invention pertains] The present invention relates to a soot treatment device, and more particularly, to an emulsified oil which can effectively decompose waste water and form a reverse circulation system. [Prior Art] Since the era of human artificial technology, the standard of living has generally improved, and in order to enable the next generation to have a better quality of life, environmental awareness has gradually risen. Many catering companies in the market are required to engage in spring conditioning work such as cooking, frying, and even frying. The oil is prone to generate fumes after high temperature or repeated use. 'At least one thousand of the public grievances related to stench every year. A lot of them, 43% of them are related to the smog emissions of the catering industry. The resulting pollution and wastewater problems have a considerable impact on the environment. Therefore, most operators will install range hoods to directly pump the fumes into the outdoor atmosphere. The air pollution in the nearby environment is quite serious. Some operators direct the smoke from the kitchen range hood directly into the sewer. Although it does not directly affect the air quality of the surrounding environment, after a certain period of time, it will cause Lu. The problem of sewer oil pollution will not only cause sewer blockage, but also affect drainage function, and even cause water pollution, causing another environmental pollution problem. SUMMARY OF THE INVENTION The main object of the present invention is to achieve the purpose of completely removing the soot exhaust gas and the oil droplet waste water by mixing the detergent with the hetero-type interface and the oil-decomposing bacteria. In order to achieve the above object, the present invention utilizes a non-ionic surfactant-based detergent to wash the soot exhaust gas to effectively emulsifie the soot exhaust gas and generate an emulsified oil-containing wastewater, and then use a grease decomposition bacteria to treat the wastewater. The emulsified oil is degraded into carbon dioxide and water. 3 201023965 The degraded aqueous solution is mixed with the detergent and repeated to continue washing the oily gas. Accordingly, the present invention can repeatedly wash the soot exhaust gas to achieve the purpose of completely removing the soot exhaust gas and the oil droplet waste water. [Embodiment] First, please refer to the "Figure 1", which is the soot extraction and biological device of the present invention, which is mainly composed of a soot extraction device 10 and a biological treatment device 20, which is composed of the soot extraction device 10 There is an extraction unit U, which is in the shape of a tower, and is provided with an atomization unit 110, a soot inlet m, a water control port 112 and an evacuation pump unit 12 above and below, and The extraction unit u is internally filled with at least one blade type double cross ring mixed sand net as a filling filter material (not shown). The biological treatment device 20 is provided with a biological decomposition unit 21, a reflux pump unit 22, a discharge cleaning port 23 and a plurality of biological carriers (not shown), and the biological decomposition unit 21 is provided with an appropriate amount of non-ionic interface activity. Detergent and oil decomposing bacteria. When used, it is mainly divided into two major steps: ❹ Step A is a soot exhaust gas washing program: the soot exhaust gas mainly passes through the soot inlet U1 and is pumped into the extraction unit 11 by the pumping pump unit 12, with the The reflux pump unit 22 charges the biodegradable unit 21 with a nonionic surfactant (for example, nonylphenol polyethoxylated alcohol compound (NPnE0), polyethylene glycol octylphenyl hydrazine (Triton-X), ten The detergent of the second burnt octaethylene glycol group (CH3(CH2)ll(〇CH2CH2)80H) is introduced into the extraction unit 11 'by the detergent agent, the smog exhaust gas can be effectively emulsified and the emulsification effect is enhanced, and 4 is produced. 201023965 Waste water after washing; the extraction unit 1丨 is filled with a blade type double cross ring mixed sand net as a filler, and the detergent of the nonionic surfactant is passed before being introduced into the extraction unit 11 After the atomization unit 110 is formed into a mist shape, the soot exhaust gas is sprayed by atomization, so that the washing effect is better. Step B is a wastewater degradation process: the waste water of the soot exhaust gas is passed through the water outlet control port. 112 flows to the student The effluent decomposition unit 21, and the wastewater is emulsified by the detergent, and the emulsified oil can be used as the oil-decomposing bacteria of the biodegradable unit 21, and the oil can be decomposed into Pseudomonas. (pseudomonas) (such as Pseudomonas aeruginosa) is the main carbon source, and the several bio-carriers help the strain to grow and attach, and the emulsified oil of the wastewater is degraded into carbon dioxide and aqueous solution through the oil-decomposing bacteria to achieve complete removal. The effect of the soot, and the aqueous solution degraded by the oil-decomposing bacteria is further guided into the extraction unit U by the reflux pump unit 22 to be mixed with the washing agent to continue washing the soot exhaust gas, thereby forming a reverse circulation system. The oil degradation rate can be maintained above 99%. In addition, it is worth mentioning that the emulsified oil of the wastewater can only provide the carbon source for the growth of the oil-decomposing bacteria in the biological decomposition unit 21, and cannot maintain the activity of the strain for a long time, so it is timely Adding trace elements (such as magnesium ions, zinc ions, iron ions, calcium ions, sodium ions) required for the growth of the oil-decomposing bacteria to maintain the biological decomposition unit 21 In order to prevent the biofilm from being excessively thick and odorous due to excessive growth of the strain on the biological carrier, the organism in the material decomposition unit 21 can be replaced and cleaned by discharging the cleaning port 23 at the same time. The present invention utilizes a detergent of a nonionic surfactant to promote the washing efficiency of the soot exhaust gas and to control the concentration of the detergent below 〇·1 volume percent (v〇1%), which does not affect the oil-decomposing bacteria. The growth can further promote the emulsification effect of the oil fume exhaust gas, so that the oil is more easily decomposed by microorganisms, and the gas-liquid ratio of the fume exhaust gas and the stripping agent is controlled at 1.3, and the retention time is 264 seconds. ), its fume emulsification efficiency can be as high as 98%. The above is only the preferred embodiment of the present invention and is not intended to limit the scope of the practice of the present invention. That is, the equivalent variations and modifications made by the scope of the present invention are covered by the scope of the invention. 201023965 • [Simplified description of the drawings] Fig. 1 is a schematic view showing the structure of a soot extraction and biological treatment device of the present invention. [Main component symbol description] 10: Soot extraction device 11: Extraction unit 110: Atomization unit 111: Oil smoke inlet 112: Water outlet control port 12: Exhaust pump unit 20: Biological treatment device 21: Biodegradation unit 22: Return pump unit 23: discharge cleaning port
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TW097151306A TW201023965A (en) | 2008-12-30 | 2008-12-30 | Soot extraction and biological treatment method and apparatus |
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TW097151306A TW201023965A (en) | 2008-12-30 | 2008-12-30 | Soot extraction and biological treatment method and apparatus |
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