TWM427381U - Improvement of oil mud processing equipment - Google Patents

Improvement of oil mud processing equipment Download PDF

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Publication number
TWM427381U
TWM427381U TW100223246U TW100223246U TWM427381U TW M427381 U TWM427381 U TW M427381U TW 100223246 U TW100223246 U TW 100223246U TW 100223246 U TW100223246 U TW 100223246U TW M427381 U TWM427381 U TW M427381U
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Taiwan
Prior art keywords
oil
sludge
outlet
exhaust gas
water
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TW100223246U
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Chinese (zh)
Inventor
Yan-Xiong Jiang
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Desiccant Technology Corp
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Application filed by Desiccant Technology Corp filed Critical Desiccant Technology Corp
Priority to TW100223246U priority Critical patent/TWM427381U/en
Priority to CN2012201316826U priority patent/CN202881066U/en
Publication of TWM427381U publication Critical patent/TWM427381U/en

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M427381 * 4 * 五、新型說明: 【新型所屬之技術領域】 本創作係關於一種油泥處理設備改良,特別是指一種可將油泥處理過 • 程中所產生包括揮發性氣體和油氣等的廢氣予以安全、環保且有效處理掉 之油泥處理設備改良。 【先前技術】 各類工業(石油、石化 '化工、電子、食品等)製程以及各式污水處 Φ 理廠(工業污水處理廠或都市污水處理廠等),均無可避免會產生污泥或油 泥,這些污泥或油泥有些是製程中的副產物須乾燥再利用,有些則屬於廢 棄物;所述油泥係包括:含油的污泥、以及油泥與污泥的混合。隨著全球 曰益重視環保議題’這些污泥或油泥的減量及處理已成為棘手的問題。 污泥與油泥的差異在於污泥的揮發性有機物含量較少,使用乾燥機來 排除廢氣及廢水即可,其處理方式較為單純。請參閱第1圖所示,習知的 污泥處理設備係包含一污泥乾燥機7和一洗滌塔_8,該一側設有一轉動轴 ® (未標示元件符號)的污泥乾燥機7係具有一污泥入口71、一空氣入口 7 2、一第一廢氣出口7 3、和一乾燥汙泥出口74,該洗滌塔8係具有 一洗滌入口81、一洗滌出口8 2和一第二廢氣出口8 3,該污泥乾燥機 7的第一廢氣出口 7 3係連通於該洗滌塔8的洗滌入口 81,污泥被乾燥 後’係產生乾燥污泥、以及產生含有空氣和揮發性氣體的廢氣,該廢氣經 由第一廢氣出口 7 3和洗滌入口 81而進入洗滌塔8中進行洗滌,該廢氣 經洗滌後的廢水將經由洗滌出口 8 2排放,此外,經乾燥和洗滌而符合廢 氣排放標準後的廢氣則經由第二廢氣出口 8 3排放。 3 M427381 然而’油泥(包括:含油的污泥、以及油泥與污泥的混合)的含油量 較阿今易揮發及面溫分解,且廢氣排放時更必然會含有油泥成分而易造 成π染。如上所述之目前市壯·泥處理賴已錄成熟,但目前對於 油泥的處理翁無法突破前述問題。 因此’如何設計出—種可突破前述問題的本創作,乃為本案創作人的 一大課題。 【新型内容】 本創作的目的之-在於提供—種献處理賴改(,藉由在污泥乾燥 機的第-廢氣巾Π連接—洗鱗,關用水的低溫將揮發性氣體及油氣予 以冷凝’同魏能有㈣洗去@體職再加上在絲塔的出口連接一油 水刀離裝置,以將洗滌後的含油廢水予以油水分離且分離後的油水和廢 水係刀別從該油水分雜置的油水排放出口和廢水排放出口予以排放到適 當的處理設備’㈣乃能進行安全、聰且姐的油泥處理。 為達上述目的,本創作係提供一種油泥處理設備改良,包含:一污泥 乾燥機、-絲塔以及-油水分雜置。該污泥乾燥機係具有一油泥入口、 一第一廢氣出口、一用以輸入惰性氣體的惰性氣體入口和一乾燥油泥出 口,該洗祕係具有-入口、一出口和一第二廢氣出σ,該污泥乾燥機的 第一廢氣出口係連通於該洗滌塔的入口;該油水分離裝置係具有一油水分 離入口、一油水排放出口和一廢水排放出口,所述洗滌塔的出口係連通於 該油水分離裝置的油水分離入口;其中,該洗滌塔的出口係在將含油廢水 排放給油水分離裝置進行油水分離,洗祕的廢氣則自該第二廢氣出口排 M427381 » « 藉此’以將油泥處理過程中所產生包括揮發性氣體和油氣等的射 以安全、環保且有效地處理掉。 氣予 為了能夠更進-步瞭解本創作之特徵、特點和技術内容,請參閱以 有關本創作之詳細說明與附圖,惟所關式僅提供參考與說_,非用J 限制本創作。 μ 【實施方式】 請參閱第2圖所示’本創作係提供-種油泥處理設備改良,該油泥處 鲁理設備係包含-污泥乾燥機工、-洗務塔3以及一油水分離裝置4。 該污泥乾燥機1大致上相同於習知如第丨圖所示的污泥乾燥機7,不 同之處在於習知的污泥人σ已改設為油泥人σ i i、習知的乾燥污泥出口 已改為乾燥油泥出口14、以及習知的空氣入口已改設為用以輸入惰性氣 體的惰性氣體入口12,此外該污泥乾燥機1還具有一第—廢氣出口工 3。由於油氣與空氣混*合時會有爆炸的危險,故改用惰性氣體做為攜帶氣 體,而該惰性氣體係自所述的惰性氣體入口12輸入污泥乾燥機丄内。 ® 該洗滌塔3係具有一入口 31、一出口 3 2和一第二廢氣出口 3 3, 該污泥乾燥機1的第一廢氣出口13係連通於該洗滌塔3的入口31,經 洗滌塔3洗滌後的廢氣係自第二廢氣出口3 3排出。 該油水分離裝置4係具有一油水分離入口 41、一油水排放出α 4 2 和·一廢水排放出口 4 3 ’所述洗蘇塔3的出口 3 2係連通於該油水分離裝 置4的油水分離入口 41,以將出口 3 2所排出的含油廢水予以油水分 離,分離後的油水和廢水則分別經由油水排放出口 4 2和廢水排放出口 4 3排出 5 藉由上述構件之組合,係能構組成本創作之該油泥處理設備。如圖所 示,油泥係經由油泥入口11而輸入污泥乾燥機i内,惰性氣體(例如氮 氣或其餘惰性氣體)係經由惰性氣體入口12而輸入污泥乾燥機i内,油 泥被乾燥後’係產生:(1)乾燥的油泥而由乾燥油泥出口 1 4排出,以及(2) 含有惰性氣體、揮發性氣體和油氣的廢氣’且該廢氣的成份係僅須室溫就 能被冷凝。因此,該廢氣乃經由第一廢氣出口i 3以及入口3 i而輸入洗 務塔3中進行洗務’以利用水的低溫(等於或低於室溫)將揮發性氣體及 油氣予以冷凝並同時洗去該廢氣中的固體顆粒(例如粉塵),其中,冷凝後 的水係含有冷凝的揮發性氣體、油泥以及固體顆粒。該出口 3 2係在排放 經洗滌塔3洗滌後的含油廢水’至於洗滌後由於已去除揮發性氣體、油氣 且已洗去固體顆粒而符合排放標準的廢氣’則經由該洗條塔3的第-廢氣 出口33排放到大氣。 其中’該油水分離裝置4的油水排放出口42,係還能進一步連通於 所述污》尼乾無機1的油泥入口 1 1 (如第2圖中所示的虛線管路),以達 到油泥再乾燥減量的目的。 綜上所述,本創作油泥處理設備改良的特點在於:可利用污泥乾燥機 工將油泥乾燥而產出:(1)乾燥的油泥並予以排出、以及(2)含有惰性氣體、 揮發性氣體和油氣的廢氣,再利用洗滌塔3的水將所述廢氣中的揮發性氣 嫁和油氣予以冷凝並洗去廢氣中的固體顆粒,從而讓達到排放標準的廢氣 經由第二廢氟出口 3 2排放到大氣,其中,冷凝後的水係含有冷凝的揮發 M427381 ' 1 9 · 性氣體、油泥以·體顆粒。接著,油水分離裝置4將含油廢水中的 和廢水刀别左由油水排放出口 4 2和廢水排放出口 4 3而排放到適當 的處理叹備。從而乃能將油泥處理過程中所產生包括揮發性氣體和油氣等 的廢軋予以安全、環保且有效處理掉。 以上所述者,僅為本創作之較M427381 * 4 * V. New description: [New technical field] This creation is about a kind of improvement of sludge treatment equipment, especially a kind of waste gas which can be produced by sludge treatment including volatile gases and oil and gas. Improvement of sludge treatment equipment that is safe, environmentally friendly and effectively disposed of. [Prior Art] Various industries (petroleum, petrochemical 'chemical, electronics, food, etc.) processes and various types of sewage treatment plants (industrial sewage treatment plants or urban sewage treatment plants, etc.) are inevitably producing sludge or Sludge, some of these sludges or sludges are dry by-products in the process, and some are wastes; the sludges include: oily sludge, and the mixing of sludge and sludge. With the global focus on environmental issues, the reduction and disposal of these sludges or sludges has become a difficult problem. The difference between sludge and sludge is that the volatile organic matter content of the sludge is small, and the dryer can be used to remove waste gas and waste water, and the treatment method is relatively simple. Referring to Fig. 1, a conventional sludge treatment apparatus includes a sludge dryer 7 and a scrubber _8, and the side is provided with a rotary shaft® (not labeled with a symbol). The utility model has a sludge inlet 71, an air inlet 7.2, a first exhaust gas outlet 73, and a dry sludge outlet 74. The washing tower 8 has a washing inlet 81, a washing outlet 8 2 and a second The exhaust gas outlet 83, the first exhaust gas outlet 73 of the sludge dryer 7 is connected to the washing inlet 81 of the washing tower 8, and after the sludge is dried, it produces dry sludge and generates air and volatile gas. Exhaust gas, which is sent to the washing tower 8 for washing via the first exhaust gas outlet 73 and the washing inlet 81, and the exhausted waste water will be discharged through the washing outlet 82, and further, dried and washed to meet the exhaust gas emission. The exhaust gas after the standard is discharged via the second exhaust gas outlet 83. 3 M427381 However, the oil content of the oil sludge (including oily sludge and the mixture of sludge and sludge) is more volatile than that of Aijin and the surface temperature is decomposed, and it is more likely to contain sludge components when the exhaust gas is discharged, which is easy to cause π dyeing. As mentioned above, the current city's strong mud treatment has been recorded mature, but the current treatment of oil sludge can not break through the aforementioned problems. Therefore, how to design a novel that can break through the aforementioned problems is a major issue for the creators of this case. [New content] The purpose of this creation is to provide a kind of treatment and treatment (by connecting the first-exhaust gas mist in the sludge dryer to wash the scales, and to condense the volatile gases and oil and gas at the low temperature of the water. 'Tongwei can have (4) wash away @body job and add a water knife off device at the exit of the wire tower to separate the washed oily wastewater into oil and water and separate the oil water and waste water from the oil Miscellaneous oil-water discharge outlets and wastewater discharge outlets are discharged to appropriate treatment equipment' (4) for safe, intelligent and sister-treated sludge treatment. To achieve the above objectives, the creative department provides a sludge treatment equipment improvement, including: The mud dryer, the wire tower and the oil moisture miscible. The sludge dryer has a sludge inlet, a first exhaust gas outlet, an inert gas inlet for inputting an inert gas, and a dry sludge outlet. Having an inlet, an outlet, and a second exhaust gas σ, the first exhaust gas outlet of the sludge dryer is in communication with an inlet of the scrubber; the oil-water separation device has an oil-water separation a port, an oil-water discharge outlet and a waste water discharge outlet, wherein the outlet of the scrubber is connected to the oil-water separation inlet of the oil-water separation device; wherein the outlet of the scrubber is discharged to the oil-water separation device for oil-water separation The secret exhaust gas is discharged from the second exhaust gas outlet M427381 » « This is used to safely and environmentally and effectively dispose of the volatile gas, oil and gas generated during the sludge treatment process. For a more in-depth understanding of the features, features and technical content of this creation, please refer to the detailed description and drawings related to this creation, but only the reference and the description are provided, and the creation is not limited by J. μ [Implementation 】 Please refer to Figure 2 for the improvement of the sludge treatment equipment provided by the creation department. The sludge treatment equipment includes a sludge drying machine, a washing tower 3 and an oil-water separation device 4. The sludge is dried. The machine 1 is substantially identical to the conventional sludge dryer 7 as shown in the figure, except that the conventional sludge man σ has been changed to a sludge man σ ii, a conventional dry sludge outlet. The dry sludge outlet 14 is changed to the conventional air inlet, and the conventional air inlet has been changed to the inert gas inlet 12 for inputting the inert gas. In addition, the sludge dryer 1 has a first exhaust gas outlet 3 because the oil and gas are mixed with the air. * There is a danger of explosion at the time of the explosion, so the inert gas is used as the carrier gas, and the inert gas system is fed into the sludge dryer from the inert gas inlet 12. The washing tower 3 has an inlet 31 An outlet 3 2 and a second exhaust gas outlet 3 3, the first exhaust gas outlet 13 of the sludge dryer 1 is in communication with the inlet 31 of the scrubbing tower 3, and the exhaust gas washed by the scrubbing tower 3 is from the second exhaust gas. The oil-water separation device 4 has an oil-water separation inlet 41, an oil-water discharge α 4 2 and a wastewater discharge outlet 4 3 'the outlet 3 2 of the wash tower 3 is connected to the oil-water separation. The oil-water separation inlet 41 of the device 4 separates the oily wastewater discharged from the outlet 32 into oil and water, and the separated oil water and waste water are discharged through the oil water discharge outlet 4 2 and the waste water discharge outlet 4 respectively. , The composition of the sludge can be configured processing apparatus according to the present Creation. As shown in the figure, the sludge is fed into the sludge dryer i via the sludge inlet 11, and an inert gas (for example, nitrogen or the rest of the inert gas) is introduced into the sludge dryer i via the inert gas inlet 12, and the sludge is dried. It produces: (1) dried sludge discharged from the dry sludge outlet 14 and (2) exhaust gas containing inert gas, volatile gas and oil and gas and the composition of the exhaust gas can be condensed only at room temperature. Therefore, the exhaust gas is sent to the washing tower 3 for washing via the first exhaust gas outlet i 3 and the inlet 3 i to condense the volatile gas and the oil and gas with the low temperature of water (equal to or lower than room temperature) while simultaneously The solid particles (e.g., dust) in the exhaust gas are washed away, wherein the condensed water contains condensed volatile gases, sludge, and solid particles. The outlet 32 is an oily wastewater that has been washed by the washing tower 3, and the exhaust gas that meets the emission standard after the washing has been removed because the volatile gas, the oil and gas has been washed away, and the solid particles have been washed away. - The exhaust gas outlet 33 is discharged to the atmosphere. Wherein the oil-water discharge outlet 42 of the oil-water separation device 4 is further connected to the sludge inlet 1 1 of the sewage-based Nigan inorganic 1 (as shown by the dotted line in Fig. 2) to reach the sludge. The purpose of drying reduction. In summary, the improved sludge treatment equipment of the present invention is characterized in that the sludge drying machine can be used to dry the sludge to produce: (1) dried sludge and discharged, and (2) containing inert gas, volatile gas and The exhaust gas of the oil and gas, and the water of the washing tower 3 is used to condense the volatile gas in the exhaust gas and the oil and gas to wash away the solid particles in the exhaust gas, so that the exhaust gas reaching the discharge standard is discharged through the second waste fluorine outlet 3 2 To the atmosphere, wherein the condensed water contains condensed volatile M427381 '1 9 · gas, sludge to body particles. Next, the oil-water separation device 4 discharges the waste water from the oily waste water from the oil-water discharge outlet 4 2 and the waste water discharge outlet 4 3 to an appropriate treatment sigh. Therefore, waste rolling including volatile gases, oil and gas, etc. generated during sludge processing can be safely, environmentally and effectively disposed of. The above is only the comparison of this creation.

H施例而已’非因此即侷限本創 作之專利範圍,舉凡運用本創作褚明舍π丄 J 化H applies only to the extent of the patent that is limited to this creation, and the use of this creation is not a problem.

均理同包含於本創作之權利範圍内,合予陳明。 。變 【圖式簡單說明】 第1圖為習知污泥處理設備的結構示意圖。 第2圖為本創作油;尼處理設備的結構示意圖。 【主要元件符號說明】 _ <習知〉 7 污泥乾燥機 7 1 污泥入口 72 空氣入口 7 3 第一廢氣出口 74 乾燥污泥出 洗滌塔 8 1 洗滌入口 82 洗滌出口 8 3 第二廢氣出口 <本創作> 7 M427381 1 污泥乾燥機 11 油泥入口 13 第一廢氣出口 3 洗務塔 3 1 入口 33第二廢氣出口 4 油水分離裝置 41 油水分離入口 43 廢水排放出口 12 惰性氣體入口 14 乾燥油泥出口 3 2出口 42 油水排放出口All of them are included in the scope of this creation and are combined with Chen Ming. . [Simplified description of the drawings] Fig. 1 is a schematic view showing the structure of a conventional sludge treatment equipment. Figure 2 is a schematic diagram of the structure of the creation oil; [Main component symbol description] _ < conventional knowledge 7 Sludge dryer 7 1 Sludge inlet 72 Air inlet 7 3 First exhaust gas outlet 74 Dry sludge out washing tower 8 1 Washing inlet 82 Washing outlet 8 3 Second exhaust gas Export <This Creation> 7 M427381 1 Sludge Dryer 11 Sludge Inlet 13 First Exhaust Gas Outlet 3 Washing Tower 3 1 Inlet 33 Second Exhaust Gas Outlet 4 Oil Water Separation Device 41 Oil Water Separation Inlet 43 Waste Water Discharge Outlet 12 Inert Gas Inlet 14 dry sludge outlet 3 2 outlet 42 oil drain outlet

Claims (1)

、申請專利範圍: 1、一種油泥處理設備改良,包含: 一用以輪入惰 ’該污泥乾燥 -污況乾燥機,係具有—麻人口、—第—廢氣出口 性氣體的惰性氣體入口和一乾燥油泥出口; -洗務塔,係具有-入口、—出口和—第二廢氣出口 機的第一廢氣出口係連通於該洗滌塔的入口;以及 油水分離裝置’储有-油水錄人口、—油水排放出σ和一廢 水排放出U,所述洗祕的出通於糾水分離裝置的油水 分離入口; 其中’該洗務塔的出口係在將含油廢水排放給油水分離裝置進行油 水分離’洗滌後的廢氣則自該第二廢氣出口排出。 、如申請專利範圍第1項所述之油泥處理設備改良,其中該污泥乾燥 機的第-廢氣出口係在排出含有惰性氣體、揮發性氣體和油氣的廢 氣,該洗滌塔係冷凝該廢氣中的揮發性氣體和油氣並同時洗去該廢 氣中的固體顆粒,洗滌後的廢氣係自該第二廢氣出口排出,洗滌後 的含油廢木則經由洗滌塔的出口而排放給該油水分離裝置進行油水 分離。 、如申請專利範圍第1或2項所述之油泥處理設備改良,其中該油水 分離裝置的油水排放出口,係連通於所述污泥乾燥機的油泥入口。Patent application scope: 1. A sludge treatment equipment improvement, comprising: a wheel idler-sludge drying-soil dryer, which is an inert gas inlet having a population of - hemp - exhaust gas and a dry sludge outlet; a washing tower having a first exhaust outlet having an inlet, an outlet, and a second exhaust outlet connected to the inlet of the scrubber; and a water-and-water separation device 'storing-oil-water population, - the oil water discharges σ and a waste water discharges U, and the cleansing passes through the oil-water separation inlet of the water-removing separation device; wherein 'the outlet of the washing tower is discharged to the oil-water separation device for oil-water separation The washed exhaust gas is discharged from the second exhaust gas outlet. The improvement of the sludge treatment equipment according to claim 1, wherein the first exhaust gas outlet of the sludge dryer discharges exhaust gas containing an inert gas, a volatile gas and an oil and gas, and the scrubbing tower condenses the exhaust gas. The volatile gas and the oil and gas simultaneously wash away the solid particles in the exhaust gas, and the washed exhaust gas is discharged from the second exhaust gas outlet, and the washed oily waste wood is discharged to the oil-water separation device through the outlet of the washing tower. Oil and water separation. The improvement of the sludge treatment equipment according to claim 1 or 2, wherein the oil-water discharge outlet of the oil-water separation device is connected to the sludge inlet of the sludge dryer.
TW100223246U 2011-12-09 2011-12-09 Improvement of oil mud processing equipment TWM427381U (en)

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TW100223246U TWM427381U (en) 2011-12-09 2011-12-09 Improvement of oil mud processing equipment
CN2012201316826U CN202881066U (en) 2011-12-09 2012-03-31 Oil sludge treatment equipment

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CN103359906A (en) * 2013-08-01 2013-10-23 江苏维尔利环保科技股份有限公司 Method for sludge drying and incineration by swill-cooked dirty oil

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CN103359906B (en) * 2013-08-01 2015-01-07 江苏维尔利环保科技股份有限公司 Method for sludge drying and incineration by swill-cooked dirty oil

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