TW200417520A - Treatment process for fast liquefaction and effective recycling of oil-containing sludge - Google Patents

Treatment process for fast liquefaction and effective recycling of oil-containing sludge Download PDF

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TW200417520A
TW200417520A TW92105041A TW92105041A TW200417520A TW 200417520 A TW200417520 A TW 200417520A TW 92105041 A TW92105041 A TW 92105041A TW 92105041 A TW92105041 A TW 92105041A TW 200417520 A TW200417520 A TW 200417520A
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Taiwan
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oil
sludge
oily
item
effective
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TW92105041A
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Chinese (zh)
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Chung-Lee Li
Ching-Huei Shyun
Shih-Chuan Tsai
Ann-Fu Wang
Wen-Sung Hsiao
Mao-Yuan Tur
Tung Li Huang
Wu Chi-Sheng
Lin Chung-Shyong
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Chinese Petroleum Corp
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Priority to TW92105041A priority Critical patent/TW200417520A/en
Publication of TW200417520A publication Critical patent/TW200417520A/en

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Abstract

A kind of treatment process for fast liquefaction and effective recycling of oil-containing sludge can perform preliminary liquefaction on oil containing sludge which may also contain various impurities by a sieving filtration apparatus installed with steam or other heat source and at the same time sieve out the impurities. The preliminarily liquefied oily sludge is agitated to maintain its liquefied state, which is followed by adding de-emulsification agent, dilution oil, etc. and homogeneously agitating to perform de-emulsification process so that fine solid materials and oil can be further separated from water to effectively recycle oil containing sludge waste, in which the addition of the dilution oil and heating can liquefy solid or semi-solid oily sludge to improve the fluidity. However, the oil, water and fine solid materials in the liquefied oil containing sludge still stay in a stable emulsified state. The effective components of the de-emulsification agent are wetting agent and emulsion breaker, in which the wetting agent can moisten the surface of the fine solid materials for entering the water phase and the emulsion breaker is adsorbed at the oil water interface, which eliminates the emulsification effect, promotes coagulation of small water drops into large water drops and thus accelerates oil water separation. Therefore, the purpose of separation of three phases (fine solid material, oil and water) is achieved.

Description

200417520 五、發明說明(1) 【發明領域】 本發明係為一種油污泥快速液化及有效資源化處理程 序L主要為將可能含有各種雜物之含油污泥,藉由已安= 蒸汽或其它熱源之篩濾設備進行初步液化,同時篩除各2 雜物。經初步液化之油泥,仍以加熱攪拌方式繼續維持^ 化狀悲,再添加解乳化劑、稀釋油等物質,均勻攪拌進行 解乳化作用’進一步加速油水分離。最後達到微細固形 物、油與水三相分離的目的。 / 【先前技術】 含油污泥因來源不同,其成份有異,但主要為油、水 和固形物之混合物。其中固形物主要為泥砂類、氧化鐵與 硫化鐵類之腐蝕產物,或其它瀝青、石蠟及焦碳類之有i 物質等。大部份的乳化物生成物,其核心物質為金屬氧化 物或砂’其表面被水濕潤後,極性化合物再被吸附於固體 表面’造成微胞(m i c e 1 1 e )之形成,微胞外層疏水部份 (hydrophobic),再吸收長鏈石蠟族之碳氫化合物,如此 形成一穩定的乳化狀態。此類廢棄物常被環保主管機關列 為有害性事業廢棄物,如何經濟有效之處置,長年以來困 擾著煉油、石化、化學品製造等之相關業者。 目前含油污泥處理方式之習用技術,可分為三類如 下:(一)減量前處理(如直接壓濾、熱處理等):(二)資源 回收(如溶劑萃取法、製石油焦、作泥燃劑、製碑等)· (三)管末處理(如高溫溼式氧化、焚化、掩埋等)。各種習 用技術方法應用時所遭遇的難題如下:200417520 V. Description of the invention (1) [Field of the invention] The present invention is a fast liquefaction and effective resource treatment program for oil sludge. It is mainly an oily sludge that may contain various impurities. The sieve filtering equipment of the heat source performs preliminary liquefaction, and at the same time removes each 2 debris. After the initial liquefaction of the sludge, it is still heated and stirred to continue to maintain the state of sorrow, and then add demulsifiers, diluted oil and other substances, and evenly stir for demulsification to further accelerate the oil-water separation. Finally, the three-phase separation of fine solids, oil and water is achieved. / [Previous technology] Oily sludge has different components due to different sources, but it is mainly a mixture of oil, water and solids. The solids are mainly corrosion products of mud and sand, iron oxide and iron sulfide, or other substances such as asphalt, paraffin and coke. Most of the emulsified products, the core substance of which is metal oxide or sand, "the surface is wetted with water, and the polar compounds are adsorbed on the solid surface," resulting in the formation of micelles (mice 1 1 e), The hydrophobic part reabsorbs the hydrocarbons of the long-chain paraffin family, thus forming a stable emulsified state. Such wastes are often classified as hazardous business wastes by environmental protection authorities. How to dispose of them cost-effectively has been a problem for related industries such as refining, petrochemicals, and chemical manufacturing for many years. The current conventional technologies for oily sludge treatment can be divided into three categories as follows: (a) pre-reduction treatment (such as direct pressure filtration, heat treatment, etc.); Fuel, stele, etc.) (3) End-of-pipe treatment (such as high temperature wet oxidation, incineration, landfill, etc.). The difficulties encountered in the application of various conventional technical methods are as follows:

第7頁 200417520Page 7 200417520

(1 )F i Iter press 直接壓濾減量产理 利用助瀘劑(矽藻土與石灰) 油泥中,濾、液之油水自動分層 程濾布易阻塞,清理耗費人工 固體物含量偏高,增加焚化處 (2)固化或安定化 ^預覆於渡布並添加少許於 灸7有效回收油份。操作過 ’且助濾劑添加導致濾餅中 理負荷。(1) F i Iter press Direct pressure filtration to reduce mass production and use of auxiliaries (diatomaceous earth and lime). In oil sludge, the filter oil and water automatic layering process filter cloth is easy to block, and it costs too much artificial solids to clean up. Increase the incineration place (2) to solidify or stabilize it ^ Overlay in Dubu and add a little to moxibustion 7 to effectively recover the oil. After operation, and the filter aid is added, the filter cake is under load.

Urrichem process 為一 序,曾實用於煉油廠油泥處 定劑之混合體,同時達到固 化劑含有水泥、普索蘭(含 與有機安定劑。固化處理成 可符合規定。但固化方法會 加,增加最終處置之困擾。 屬或油脂仍有再滲出之虞。 種應用固化方法之商業化程 理 〇 丄七 、。该法係利用有機與無機安 t ’由泥中之重金屬與油脂。固 f灰、水泥窯灰與煆燒爐渣) 口口之單軸抗壓強度、滲透係數 使處理後之廢棄物量大幅增 且若掩埋處理,被固化之重金The Urrichem process is a sequence. It has been used in a mixture of oil sludge conditioners in refineries. At the same time, the curing agent contains cement and Porsolan (including organic stabilizers. The curing process can meet the requirements. However, the curing method will be increased and increased The trouble of the final disposal. The metal or oil may still ooze out. A commercialization process of solidification method is applied. This method uses organic and inorganic solvents to remove heavy metals and grease from the mud. Solid f ash , Cement kiln ash and slag burner slag) The uniaxial compressive strength and permeability coefficient of the mouth will greatly increase the amount of waste after treatment and if it is buried, it will be solidified.

ChemFix process則是應用安定化作用之一種商業化 處理程序,係利用Micr〇encapsulati〇n (微胞包覆)將 廢油泥安定化,成品不經鑄模成形而是土壤狀,可作為掩 埋%覆土。本法適用於含重金屬或低油份含量之油泥^ 理’並不適用油脂含量高之油泥。3 〇 %以上油份含量之含 油污泥,經此安定化處理,仍有大量油泥可被萃取出來, 而有二次污染之虞。 (3 )溶劑萃取法 已商業化的 RCC (Resource Conservation Corp.) 之 B.E.S.T·法,利用三乙胺(Triethylamine,TEA)之特The ChemFix process is a commercialized process that uses stabilization to stabilize the waste sludge by using Microencapsulation (microcell coating). The finished product is soil-like without being formed by a mold, and can be used as a burial% covering soil. This method is applicable to sludge containing heavy metals or low oil content. It is not applicable to sludge with high oil content. After the oily sludge with an oil content of more than 30% is stabilized, a large amount of oily sludge can still be extracted and there is a possibility of secondary pollution. (3) Solvent extraction method The B.E.S.T. method of RCC (Resource Conservation Corp.), which has been commercialized, uses the speciality of triethylamine (TEA)

第8頁 200417520 五、發明說明(3) 性,低溫時TEA極性大與水互溶,高溫時TEA極性變小與油 脂互溶。廢油泥經低溫TEA萃取(4 °C ),去除固體物後,油 泥與TEA混合物經54 °C處理,使油相與水相分層面去除水 份,最後再以蒸汽氣提方式回收TEA再用。但三乙脸沾主 性考量,使得本方法不易推廣。 一一妝的t (4)掩埋(Land farming) —土壤中含有各種具有分解碳氫化合物能力之微生 但實際應用時,由於生物分解速度慢,所須土地面積 i f ί:能污染地下水,故不適合地狹人稠的地區使 性幻ΐ冷或乾燥地區亦不適合’因土壌中之微生物活 (5 )摻製石油焦 廢油泥摻製石油焦為美國i 1公 M〇bil sludge c〇Ung(M0SC)〇^#^t; i^ ^ 為:(a)油泥進料不均質,造成石油隹 ===問喊 作困難;⑻油泥中含油量過高,產;'臭η除焦操 程,產生大量含油廢水。 生六未,(〇除焦過 (6 )焚化處理 由於含油廢棄物含水率高,流動性大 廠、曰遍考慮使用焚化處理,以應付日兴时—…值尚,煉油 f内煉油廠目前也以焚化法處理油泥m環保法令。 毋化之處理目標,但所須設備 盥匕處理雖可達無 高。 貝賈用與處理費用均極 (7)泥燃資源化 200417520 五、發明說明(4) 將高熱值之廢油泥,摻配台電媒灰、飛灰,並添加適 當之分散劑,以製成稱為泥燃劑成品,其熱值高達 5 0 0 0 K c a 1 / K g,可作為水泥廠輔助燃料。此法在日本與美 國應用頗多,在國内因相關法令不完備,導致不易推廣'。 (8 )加熱離心處理法 ' 國外結合油槽清洗與油泥處理之商業化實例,多以加 熱(70〜95 °C)處理後,以連續式三相離心機分離固體物、 水與油。收集國外相關資料,擁有此程序廠家至少有五 家,包括美國31、英國TPS(SEPS)、瑞典Mfa 、法 國 Guinard Oil 與澳洲 VAC-TECH(S.L.T.)等。 上述各種習用技術之油泥資源化方法,皆有可能因油泥含 有,膠代、手套、螺絲、鐵件等雜質,造成進料堵塞及設 f &壞’降低其處理能力。而本發明含油污泥快速液化及 ^效資源化處理程序之實施方法,係先行去除大型固形物 與鐵屬,且利用添加稀釋油及解乳化劑: 油份分離。有效回收並中 版柳水興 ,,,,.,^ ^ 叹八中之奴虱化合物,泵回原油槽或回 ,油油槽再㈣,剩餘之固形物殘渣再以焚化 【發明内容】 要為3 =:泥快速液化及有效資源化處理程序,主 ΐ ί ! : "b 3!雜物之油污泥,#由已安裝蒸汽管綾 1/、匕”、、源之師濾設備,進行初步液化,同時篩除各式雜 物。經初步液化之、、山、、尸 + # 、合式雜 ^ η ^ ^ /比,垂洛至加熱攪拌槽内,繼續維梏 液化狀悲’再添加解乳化劍絲 、寺 行解乳化作用,、隹:I 稀釋專物質,肖勻攪拌進 V使微細固形物、油與水分離,有致 第10頁 200417520Page 8 200417520 V. Description of the invention (3) At low temperature, the polarity of TEA is high and it is miscible with water, and at high temperature, the polarity of TEA is low and it is miscible with oil and fat. Waste oil sludge is extracted by low-temperature TEA (4 ° C). After removing solids, the mixture of sludge and TEA is treated at 54 ° C to remove water from the oil and water phases. Finally, TEA is recovered by steam stripping and reused. . However, the main consideration of San Yilian makes this method difficult to popularize. One by one t (4) Land farming—The soil contains various micro-organisms that have the ability to decompose hydrocarbons. However, in practice, due to the slow biological decomposition rate, the required land area if ί: can pollute groundwater, so It is not suitable for narrow and dense areas, and it is not suitable for cold or dry areas. 'Because of the microbial activity in the soil (5) Blended petroleum coke waste sludge Blended petroleum coke is the United States i 1 male Mobil sludge cUng ( M0SC) 〇 ^ # ^ t; i ^ ^ is: (a) Heterogeneous sludge feed, causing petroleum 隹 === Asking for difficulty; ⑻The oil content in the sludge is too high, yield; , Produces a large amount of oily wastewater. (6) incineration treatment Because of the high water content of oily waste, large-scale fluid factories consider using incineration treatment to cope with the day-to-day —... value, refinery f refinery currently The incineration method is also used to treat sludge m environmental protection laws and regulations. The goal of non-chemical treatment, but the equipment can be processed without any high level. The use and disposal costs of Beja are extremely high. (7) Mud-burning resource 200417520 4) Blend high-calorie waste sludge with Taiwanese dielectric ash and fly ash, and add appropriate dispersant to make a finished product called mud-burning agent, which has a calorific value up to 50000 K ca 1 / K g, It can be used as auxiliary fuel for cement plants. This method is widely used in Japan and the United States, and it is not easy to be promoted because of incomplete related laws in China. (8) Heating and centrifugation method 'Commercial examples of combining oil tank cleaning and sludge treatment in foreign countries After processing by heating (70 ~ 95 ° C), the solid matter, water and oil are separated by a continuous three-phase centrifuge. Collect foreign relevant information. At least five manufacturers have this program, including the United States 31 and British TPS. (SEPS), Swedish Mfa, French Guinar d Oil and Australian VAC-TECH (SLT), etc. All the above-mentioned conventional technologies for the sludge resource recovery method may cause the feed to be blocked and set due to the sludge content, impurities such as rubber substitutes, gloves, screws, iron parts, etc. "Bad" reduces its processing capacity. The method for implementing the rapid liquefaction and resource efficient treatment of oily sludge of the present invention is to remove large solids and ferrous metals first, and to add diluent oil and demulsifier: oil separation. Effectively recover and recover the Chinese version of Liu Shuixing ,,,,,,, ^ ^ The scourge compound in the middle eight is pumped back to the crude oil tank or back, and the oil tank is simmered again, and the remaining solid residue is incinerated. [Content of the invention] should be 3 = : Quick liquefaction of mud and effective resource processing procedures, the main quot!: &Quot; b 3! Oil sludge of miscellaneous materials, #from the installed steam pipe 绫 1 /, dagger ", the source of the filter equipment, preliminary Liquefaction, and screen all kinds of debris at the same time. After preliminary liquefaction ,, mountain, and corpse + #, combined type ^ η ^ ^ / ratio, Trang Luo to the heating and stirring tank, continue to maintain the liquefaction state and add solutions Emulsifying sword silk, Temple line demulsifying effect, 行: I dilution specialist Quality, uniform stirring Shaw V into the fine solids, oil and water separation, has caused Page 10200417520

資源化含油污泥類之廢棄物。 其中添加稀釋油及加熱,可使固體狀或半固體狀油、、尸 液化,改進其流動性。但液化後之含油污泥,所含之油/尼 水、微細固形物,仍維持在穩定的乳化狀態。而解乳化唧 之有效成伤為濕潤劑(W e 11 i n g a g e n t )及破乳化劑 《 (Emulsion breaker)。濕潤劑可使微細固形物表面潤溼 入水相,而破乳化劑則會被吸附於油水界面,消弭原來 乳化作用,促進小水滴進行凝結作用形成大水滴,加=Recycling wastes containing oily sludge. The addition of diluent oil and heating can liquefy solid or semi-solid oil and corpse, and improve its fluidity. However, the oily sludge after liquefaction, the oil / nedra, and the fine solids contained in it remained in a stable emulsified state. The effective wounds for demulsification are wetting agents (W e 11 i n g a g e n t) and demulsifiers (Emulsion breaker). The wetting agent can make the surface of the fine solids wet into the water phase, and the demulsifier will be adsorbed at the oil-water interface, eliminating the original emulsification, and promoting the condensation of small water droplets to form large water droplets.

水分離。最後達到微細固形物、油與水三相分離的/ 【實施方式】 JWater separation. Finally, three-phase separation of fine solids, oil and water is achieved. [Embodiment] J

立請參閱第一圖A本發明實施例之處理流程之篩濾槽示 思圖。其說明如下··處理含油污泥丨〇時,若為可泵動性、 泥,即其大型固形物1丨含量較少,流動性佳者,則利 浦直接將含油污泥1〇泵入篩濾槽u。其中屬於大型固形^ 倒入師濾槽1 A。 篩濾槽1A頂部為一栅格 截留,如石塊、鐵條、塑膠 後之油泥1 2與浮游物1 3則經 或其它加熱設備之網孔向下 油污泥10流動性,防止進料 拌加熱槽1 B,煩請參閱第一 此攪拌加熱槽1 B中蒸汽管線 統調節溫度。經適當加熱及 板1 4,較大之大型固形物丨丨被 袋、寶特瓶、易開罐等,筛選 安裝有蒸汽管線加熱裝置1 2 5 垂落,此預熱作用具有增加含 阻塞的功能。油泥1 2垂落至攪 圖B處理流程之加熱示意圖, 加熱裝置1 2 5加以溫度控制系 添加分解物劑1 2 1如解乳化Please refer to FIG. 1A for a schematic view of a sieve filter tank of a processing flow of an embodiment of the present invention. The description is as follows: · When treating oily sludge, if it is pumpable and sludge, that is, if its large solid content is small and the fluidity is good, then Philips will directly pump oily sludge into 10 Sieve filter trough u. Which belongs to the large solid shape 1 pour into the filter tank 1 A. The top of the sieve filter tank 1A is trapped by a grid, such as stones, iron bars, plastic sludge 12 and floats 13, and the sludge 10 flows downward through the mesh of other heating equipment to prevent feeding. Stir heating tank 1 B, please refer to the steam line in the first stirring heating tank 1 B to adjust the temperature. After proper heating and plate 14, larger solids 丨 丨 quilts, bottles, easy to open cans, etc., screened and installed with steam line heating device 1 2 5 hanging, this preheating effect has increased Features. Sludge 1 2 hangs down and stirs. Figure B is a schematic diagram of the heating process. The heating device 1 2 5 is added with a temperature control system. Decomposer 1 2 1 is used as a demulsifier.

200417520 五、發明說明(6) 劑、稀釋油,使乳化狀態之加熱泥油丨2 3中之固體、油及 水混合物能解乳化而有效分層,進而藉出油口丨2γ回收浮 油,煩請參閱第一圖C本發明實施例之處理流程之固液^ 離示意圖,本發明使有效分離浮油131、水相物質133/斑7 態雜質135,其中水相物質133則導入廢水處理系統處理, 而固態雜質1 3 5則進入焚化爐處理。 槽 第二圖係為本發明實施例之硬體設備俯視圖。槽本體 分成三部分,即進料部分、攪拌槽部份與調均槽部份。 料部份即為槽上部柵格板26及蒸汽管線加埶裝置丨25 可 本體外部設有進料蓋板,蓋板上設有法蘭式短管接頭 應用於可泵動油泥之進料。 本處理系統之主要優點為: (1 )上部栅格板2 6之設計,可移除大刑囡 後續操作。 移除大型固形物,避免影響 (2)Πΐ:栅格板26之蒸汽管線加熱裝置125,可預熱含 料阻增加其流動十生’使能儘速下垂落,防止進 抖阻基,造成處理瓶頸。 ⑶度控制系統調節蒸汽流量’達到準確控制溫度 (4)特殊授拌機組23設計,如鋸齒狀(咖 mixer) ^ ^ 間齒狀^二 為圓盤狀,夕卜圍設計成上下相 強烈之Ϊ座。〃目的是在接近葉片端形成紊流,造成 且每a與:力。内部另設檔流板,以加強攪拌效果。 σ攪拌機組23,可依據實際需要來調整轉速。200417520 V. Description of the invention (6) Agent and diluent oil, so that the heating mud oil in the emulsified state 丨 2 The solid, oil and water mixture in 3 3 can de-emulsify and effectively delaminate. Please refer to the first diagram C for the solid-liquid separation diagram of the treatment process of the embodiment of the present invention. The present invention enables effective separation of slick oil 131 and water-phase substance 133 / spot 7-state impurity 135, of which the water-phase substance 133 is introduced into the wastewater treatment system The solid impurities 1 3 5 enter the incinerator. The second figure is a top view of a hardware device according to an embodiment of the present invention. The tank body is divided into three parts, namely the feeding part, the stirring tank part and the leveling tank part. The material part is the grid plate 26 on the upper part of the tank and the steam line adding device. 25 The feed cover is provided on the outside of the body. The cover is provided with a flange type short pipe joint for feeding sludge. The main advantages of this processing system are: (1) The design of the upper grid plate 26 can remove the torture and subsequent operations. Remove large solids to avoid affecting (2) Πΐ: The steam line heating device 125 of the grid plate 26 can preheat the material resistance and increase its flow rate. Handle bottlenecks. (3) The degree control system adjusts the steam flow to achieve accurate temperature control. (4) The special mixing unit 23 is designed, such as a sawtooth (coffee mixer) ^ ^ interdental ^ The second is a disc shape. Ϊ 座. The purpose is to form a turbulent flow near the blade end, causing and every a and: force. A baffle plate is set inside to enhance the stirring effect. The σ mixing unit 23 can adjust the rotation speed according to actual needs.

第12頁 200417520Page 12 200417520

五、發明說明(7) (5)分解物劑121中解乳化劑之應用,解乳化劑對於油泥12 洗淨效果、脫水能力、油水乳化界面層厚度、及固體 雜質濕潤移除,具關鍵性角色。本發明自行研發之解 乳化劑配方,具有強力解乳化功能,更強化本處 統之操作效能。 糸V. Description of the invention (7) (5) Application of the demulsifier in the decomposition agent 121, the demulsifier has the key to the cleaning effect of sludge 12, dehydration ability, the thickness of the oil-water emulsified interface layer, and the wet removal of solid impurities Roles. The self-developed de-emulsifier formulation of the present invention has a strong de-emulsifying function and further strengthens the operating efficiency of the system. Ito

由於本發明含油污泥快速液化及有效資源化處理程序 優異特色’使得含有大量不均勻固形物或黏度於常溫下高 達8 0 0 0CPS之含油污泥1 〇,皆有效被處理,徹底解決此類 固體廢棄物之處置困擾。為詳述本發明,「含油污泥快速 液化及有效^源化處理程序」’對於含油污泥1 〇之處理效 果’以下列舉本發明之實施例··Due to the excellent features of the rapid liquefaction of the oily sludge of the present invention and the effective resource treatment process, the oily sludge containing a large amount of uneven solids or viscosities up to 8 0 0 0 CPS at room temperature is effectively treated, completely solving this type of problem. Disposal of solid waste is troublesome. In order to describe the present invention in detail, the "rapid liquefaction and effective treatment of oily sludge" is an example of the "treatment effect of oily sludge 10". Examples of the present invention are listed below.

口 本發明第一實施例:處理可泵動之含油污泥 ^作條件為85 °c、進料油泥/稀釋油=1/2、解乳也劑添加 = 3^〇〇m、g/L、攪拌速度2〇〇rpm。以此操作條件,連續運轉 比'j年以上’各溫度、攪拌、解乳化劑添加等控制單元, 二,作良好。且回收油品質佳,試驗結果如表一利用本發 si:理處理可泵動油泥之操作結果所示,其中BS (Bottom 一) 一棚係為進料中或回收油中之固形物含量,BS&W 系為進料中之固形物及水含量sludge and ) ,_或經處理後所回收之固形物及水相數量。 表一可知,經由本發明之處理程序,可將進料中之 者 3里由1 5%降至2%,且此回收油品質遠比離心處理 離心處理者,其回收油中之BS含量為5%。 發明第二實施例··處理不可泵動含油污泥The first embodiment of the present invention: Treatment of pumpable oily sludge. The operating conditions are 85 ° c, feed sludge / diluent oil = 1/2, demulsifier addition = 3 ^ 00m, g / L. 2. Stirring speed is 2000 rpm. Under these operating conditions, continuous operation of control units such as temperature, agitation, and addition of demulsifiers over 'j years or more' is good. And the quality of the recovered oil is good. The test results are shown in Table 1. The results of the operation of pumpable sludge using the si: physical treatment. The BS (Bottom I) shed is the solid content in the feed or the recovered oil. BS & W is sludge and) in the feed, or the amount of solid and water phase recovered after treatment. As can be seen from Table 1, the processing procedure of the present invention can reduce the 3 in the feed from 15% to 2%, and the quality of the recovered oil is much better than that of the centrifugal treatment. The BS content in the recovered oil is 5%. Second embodiment of the invention ·· Treatment of non-pumpable oily sludge

200417520200417520

再以夾ΐ:,油污泥,以人工挖掘方式裝在53加侖桶内, 進料槽。由於進料油泥固形物甚多(含量 Ι/Λ’、黏稠性高,倒在進料槽柵格板上,不易馬上 ίΛ 士:==掉槽内,進料速率較慢。進料油泥内含相當多 您杜n g ▲丄可有效被截留於上端之栅格板上。其它操作 條件同第「貫施例。其操作結果如表二利用本發明處理不 可泵動含油污泥之操作結果所示。 由表一利用本發明處理不可泵動含油污泥之操作結果 可知’進料中之固形物含量(Bs)45%,經本發明之處理系Then, the oil sludge is packed in a 53-gallon drum by manual excavation, and it is fed into the tank. Because the feed sludge has a lot of solids (content I / Λ ', high viscosity, it is poured on the grid plate of the feed tank, and it is not easy to immediately ΛΛ: == drop out of the tank, the feed rate is slow. In the feed sludge Contains quite a lot of your ng ▲ 丄 can be effectively trapped on the upper grid plate. Other operating conditions are the same as those in the “Performance Example.” The operating results are shown in Table 2. From the results of the operation of using the present invention to treat non-pumpable oily sludge in Table 1, it can be known that the solid content (Bs) in the feed is 45%.

統處理後’ BS降至6%左右,可確定本設備處理後之回收油 品質,其BS小於6%。 由貫際操作案例,顯示本發明含油污泥快速液化及有 效資源化處理程序,其攪拌機組2 3所採用的特殊設計,即 上下雙鑛齒形狀式攪拌器,加上槽壁設計檔流板,可產生 適當的剪應力與泵浦能力,達到快速液化且均勻混合油泥 的功能。另相關加熱系統之設計,於2 0分鐘内即能將含油 污泥由室溫上昇至8 5 °C左右,顯示其熱傳效率極佳。 [發明之效果】After the system's BS is reduced to about 6%, the quality of the recovered oil after processing can be determined. The BS is less than 6%. According to the operation case, it shows the fast liquefaction and effective resource treatment procedures of the oily sludge of the present invention. The special design adopted by its mixing unit 23 is the upper and lower double ore tooth type agitator, and the baffle wall design baffle , Can generate appropriate shear stress and pumping capacity, to achieve rapid liquefaction and uniform mixing of sludge. In addition, the design of the related heating system can raise the oily sludge from room temperature to about 8 5 ° C in 20 minutes, showing that its heat transfer efficiency is excellent. [Effect of the invention]

綜上所述’充份顯示出本發明’ 「含油污泥快速液化 及有效資源化處理程序」,在目的及功效上均深富實施之 進步性,極具產業之利用價值,且為目前市面上前所未見 之新發明,完全符合發明專利之要件,爰依法提出申請。 唯以上所述者,僅為本發明之較佳實施例而已,當不 能以之限定本發明所實施之範圍。即大凡依本發明申請專In summary, the present invention is "fully demonstrated by the present invention" "the procedure for the rapid liquefaction of oily sludge and effective resource treatment", which is deeply implemented in terms of purpose and efficacy, has great industrial use value, and is currently on the market New inventions that have not been seen before are in full compliance with the requirements of invention patents, and applications are filed according to law. The above are only the preferred embodiments of the present invention, and it should not be used to limit the scope of the present invention. That is, where Fan

第14頁 200417520 五、發明說明(9) 利範圍所作之均等變化與修飾,皆應仍屬於本發明專利涵 蓋之範圍内,謹請 貴審查委員明鑑,並祈惠准,是所至 禱0 第15頁 200417520 圖式簡單說明 第一圖A係為本發明實施例之處理流程之篩濾槽示意圖; 第一圖B係為本發明實施例之處理流程之加熱示意圖; 第一圖C係為本發明實施例之處理流程之固液分離示意 圖; 第二圖係為本發明實施例之硬體設備俯視圖; 表一係為利用本發明處理可泵動油泥之操作結果; 表二係為利用本發明處理不可泵動含油污泥之操作結果。 【符號說明】 1A篩濾槽; 1B攪拌加熱槽; 1 0含油污泥; 11大型固形物; 1 2油泥; 1 3浮游物; 1 4栅格板; 1 2 1分解物劑; 1 2 3加熱泥油; 125蒸汽管線加熱裝置; 127出油口; 1 3 1浮油; 1 3 3水相物質; 1 3 5固態雜質; 23攪拌機組; 2 6上部柵格板。Page 14 200417520 V. Description of the invention (9) Equal changes and modifications made within the scope of the invention shall still fall within the scope of the patent of the present invention. I invite your reviewing committee to make a clear reference and pray for it. 15 pages 200417520 The diagram is briefly explained. The first diagram A is a schematic diagram of the sieve filter tank of the process of the embodiment of the present invention. The first diagram B is the schematic diagram of the heating process of the process of the embodiment of the present invention. Schematic diagram of solid-liquid separation of the processing flow of the embodiment of the invention; The second figure is a top view of the hardware equipment of the embodiment of the invention; Table 1 is the operation result of using the present invention to treat pumpable sludge; Table 2 is the use of the present invention Operation results of non-pumpable oily sludge. [Symbol description] 1A sieve filter tank; 1B stirring and heating tank; 10 oily sludge; 11 large solids; 1 2 sludge; 1 3 floats; 1 4 grid plate; Heating mud oil; 125 steam pipeline heating device; 127 oil outlet; 1 3 1 oil slick; 1 3 3 water phase substance; 1 3 5 solid impurities; 23 mixing unit;

第16頁Page 16

Claims (1)

200417520 六、申請專利範圍 1. 一種含油 一硬體設 之方法, 輸送該 添加一 攪拌該 泥與 該解乳 解乳化 合, 解乳化 質、 回收浮 2. 如申請專 資源化處 設備,藉 3 ·如申請專 資源化處 管線加熱 溫度。 污泥快速液化及有致眘、、语& 士 ’双貝源化處理程序,係藉由 備輸送一含油污泥至一與批 | 搅拌加熱槽中進行純化 其步驟如下: 含油污泥至該授拌加熱槽; 解乳化劑至該攪拌加熱槽; 3油泥,藉由一攪拌機組均勻攪拌該含油污 化劑; 處理, 該 劑對含 浮油與 油及水 利範圍 理程序 由該篩 利範圍 琿程序 裝置, 藉由該解乳化劑與該含油污泥均勻混 # 油污泥進行解乳化作用,分離固態雜 水; ’完成4含油污泥之純化處理。 第1項所述之含油污泥快速液化及有效 ,其中該攪拌加熱槽上更設置有一篩濾 濾設備濾除該含油污泥中大型雜物。 第1項所述之含油污泥快速液化及有效 ,其中該攪拌加熱槽上更設置有一蒸汽 藉由該加熱管線加以溫度控制系統調節 4.如申請專利範圍第2項所述之含油污泥快速液化及有效 資源化處理程序中,.該篩濾設備更係為一柵格板。 5 ·如申請專利範圍第2項所述之含油污泥快速液化及有效 資源化處理程序,該授拌加熱槽外部設有一進料蓋板,200417520 VI. Scope of patent application 1. A method for designing oil-containing hardware, conveying, adding, stirring, and mixing the mud with the demulsified and demulsified, demulsified, recovered and floated. 2. If you apply for special resources equipment, borrow 3 · If you apply for the heating temperature of the pipeline in the special resource department. The sludge liquefies quickly and has a cautious, Chinese & double shellfish source treatment process, which is carried out by transporting an oily sludge to a batch | purification in a stirred heating tank, the steps are as follows: oily sludge to the Stirring heating tank; Demulsifier to the stirring heating tank; 3 oil sludge, uniformly stir the oily soiling agent by a mixing unit; treatment, the agent's procedure for containing oil slicks and oil and water conservancy range is determined by the screening range珲 A program device, by which the demulsifier is uniformly mixed with the oil-containing sludge # The oil sludge is subjected to de-emulsification to separate the solid water; 'Complete the purification treatment of 4 oil-containing sludge. The oily sludge described in item 1 is fast liquefied and effective, wherein the stirring heating tank is further provided with a sieve filtering device to remove large debris in the oily sludge. The oily sludge described in item 1 is fast liquefied and effective, wherein the agitated heating tank is further provided with a steam and the temperature control system is adjusted by the heating pipeline. In the process of liquefaction and effective resource treatment, the screening equipment is a grid plate. 5 · According to the procedure of rapid liquefaction and effective resource treatment of oily sludge as described in item 2 of the scope of patent application, a feeding cover plate is provided outside the mixing heating tank, 第17頁 200417520Page 17 200417520 該進料蓋板上設有依法蘭式短管接頭。 6 ·如申請專利範圍第1項所述之含油 序,其中該分解物劑係包括有一解化之純化處理程 7.如申請專利範圍第1項所述之含 背與一稀釋油c 眘嗎仆声搜护左 甘士斗& ’可’尼快速液化及有效 貝源化處理私序,其中該解乳化劑之添加 0-5000mg/L 。 A 8.:申請專利範圍^項所述之含油污泥快速液化及有效 貝源化處理程序,本發明之操作溫度為2 〇〜丨5 〇 t。The feeding cover is provided with a flange-type short pipe joint. 6 · The oily sequence as described in item 1 of the scope of patent application, wherein the decomposing agent comprises a purification process of decomposition. 7. The backing and a diluent oil as described in item 1 of the scope of patent application. Servant searches for Zuo Ganshidou & 'Ke' Ni's rapid liquefaction and effective shellization treatment, in which the addition of the demulsifier 0-5000mg / L. A 8 .: The procedure for rapid liquefaction and effective shellization of oily sludge as described in item ^ of the scope of patent application. The operating temperature of the present invention is 2 0 ~ 5 0 t. 9·如申請專利範圍第1項所述之含油污泥快速液化及有效 資源化處理程序,其中本發明之攪拌速度為5 〇〜 100Orpm 〇 I 0 ·如申請專利範圍第7項所述之含油污泥快速液化及有效 資源化處理程序中,該解乳化劑之成分係包括有壬基 苯酚甲醛酉旨(Nonylphenol Formaldehyde Resin)、多 烧氧基乙二醇(Polyalkoxylate Glycol) 、(Pluronic Polyalkoxylate Block Copolymer) 、丁二酸二辛酯 石黃酸(Dioctyl Sulfonsuccinate)、烧基石黃酸(Alkyl Sulfonate)、石油石黃酸(Petroleum Sulfonate)。9. The rapid liquefaction of oily sludge as described in item 1 of the scope of patent application and effective resource treatment procedures, wherein the stirring speed of the present invention is 50 to 100 rpm 〇I 0. The oily content as described in item 7 of the scope of patent application In the process of rapid liquefaction of sludge and effective recycling, the components of the demulsifier include Nonylphenol Formaldehyde Resin, Polyalkoxylate Glycol, and Pluronic Polyalkoxylate Block Copolymer. ), Dioctyl Sulfonsuccinate, Alkyl Sulfonate, Petroleum Sulfonate. II ·如申請專利範圍第3項所述之含油污泥快速液化及有效 資源化處理程序中,該攪拌加熱槽上設置之該蒸氣管 線加熱裝置,藉由該蒸氣管線加熱裝置對該含油污泥 加溫,提高其流動性。 1 2·如申請專利範圍第11項所述之含油污泥快速液化及有 效資源化處理程序中,該蒸氣管線加熱裝置更係圍繞II · In the process of rapid liquefaction and effective resourceization of oily sludge as described in item 3 of the scope of the patent application, the steam line heating device set on the stirring heating tank, and the oily sludge is heated by the steam line heating device. Heat up to improve its fluidity. 1 2 · In the process of rapid liquefaction of oily sludge and effective resource recycling as described in item 11 of the scope of patent application, the steam pipeline heating device is more 第18頁 200417520 六、申請專利範圍 於攪拌加熱槽之四周 « I_lil 第19頁Page 18 200417520 6. Scope of patent application Around the mixing and heating tank «I_lil Page 19
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102811817A (en) * 2009-10-23 2012-12-05 M·C·阿米兰 Method And Apparatus For De-oiling Magnetic Solid Waste
CN107324636A (en) * 2017-05-27 2017-11-07 李成春 A kind of ground sludge harmless treatment retracting device and its processing recovery method
CN115432898A (en) * 2021-06-03 2022-12-06 陕西青朗万城环保科技有限公司 Method for treating oil sludge

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102811817A (en) * 2009-10-23 2012-12-05 M·C·阿米兰 Method And Apparatus For De-oiling Magnetic Solid Waste
CN102811817B (en) * 2009-10-23 2016-11-16 M·C·阿米兰 Method and apparatus for magnetic retention refuse removing oil
CN107324636A (en) * 2017-05-27 2017-11-07 李成春 A kind of ground sludge harmless treatment retracting device and its processing recovery method
CN115432898A (en) * 2021-06-03 2022-12-06 陕西青朗万城环保科技有限公司 Method for treating oil sludge

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