1312290 玖、發明說明： 【發明所屬之技術領域】 本發明係關於一種油污泥與原油分離的方法，特別是才t 一種將含在油污泥内之原油先蒸發成油氣，再將該油氣冷^ 成瓦斯及輕原油之油污泥與原油分離的方法。 【先前技術】 原油通常係蘊含於地底深層，欲開採時，需先探勘、由 之正確位置後，再進行油井之開鑿，待油井開鑿完畢後，即 可將地底深層之原油抽取出，並將該抽取出之原油置入原由 槽中運往世界各地，再由各國自行將原油提煉成各種可供使 用之輕原油（如：無鉛汽油、柴油、高級汽油等）；然而， 因該原油係從地底深層被抽取出’使得抽取出之原油中含有 大量的污泥（如：土、沙、重金屬及其他雜質），該污泥本 身具有一定之重量，使其會沉澱於原油槽之底部，致使原油 槽内可供提煉之原油數量減少，且該原油係沾附於污泥上， 導致原油槽内之原油無法全部被提煉使用，實不符合經濟效 益。故為將油污泥上之原油萃取，坊間即有利用離心力原理 將原油與污泥分開之技術問世，然而’其僅能萃取污泥上一 小部份之原油，大部分之原油仍沾附於污泥上，使得該油污 泥於後續處理上相當困難，不管將其燃燒或丟棄皆會造成空 氣及環境之污染。因此，當今若能設計出一種將污泥上之原 油完全萃取之技術，方是當務之急。 由此可見，上述習用技術仍有諸多缺失，實非一良善之 1312290 設計者，而亟待加以改良。 本案發明人㈣上述習用方法所衍生的各項缺點，乃亟 思加以改良創新，並經多年苦心孤f旨潛心研究後，終於成功 研發完成本件油污泥與原油分離的方法。 【發明内容】 本發明之目的即在於提供—種利用高溫間接加熱方式， ㈣油與油污泥相分離之油污泥與原』分離的方法。 本發明之次-目的係在於提供—種可將萃取之原油提煉 成輕原油及瓦斯之油污泥與原油分離的方法。 本發明之另_目的係在純供—種可加人塑勝垃圾於油 污泥中，在不增加污泥殘渣的數量下，可增加輕原油提煉數 量之油污泥與原油分離的方法。 本發明之又一目的係在於提供一種可利用劣質油、可燃 f垃圾#炭及瓦斯作為間接加熱油污泥的燃料之油污泥與 原油分離的方法。 可達成上述發明目的之油污泥與原油分離的方法，其製 作步驟為： 1. 先將含有原油之油污泥直接置入裂解爐中加熱至 400-700度’該裂解爐内並保持3公斤的壓力值，使得油污泥 内所含之原油被裂解成氣體狀態； 2. 將步驟一之油氣送至冷凝器中加以冷卻，使冷卻後之油 氣形成瓦斯及輕原油； 1312290 引進原 汽油、 3.將步驟二之瓦斯導引至瓦斯槽中，並將輕原油導 油槽内’供使用者作石油化學中間原料❹或分顧成 柴油或燃料油。 另外，該步驟-中另可加入塑膠垃圾，使其 泥殘潰之狀況下，可增加輕原油產量；且其所應用之：二 【實施方式】 自產瓦斯、可燃性垃圾及煤炭等。 的 請參閱圖一所示，係本發明所提供之油 方法，其製作步驟為： 污泥與原油分離 步驟一 11.·係先將油污泥放入一燃燒室内之裂解爐中進 行加熱，該加熱燃料可為：劣質油、瓦斯、煤炭及可燃性垃 圾等，使裂解爐内之溫度可保持在·〜7⑻度，其内並保持3 公斤之壓力值’使得油污泥上之原油被加熱蒸發成油氣，進 而與>5泥完全分離，使得分離完成之污泥殘渣相當乾燥，猶 如礦砂般； 步驟二12:再將油氣導入反應爐中加熱，並作壓力控制， 以將分子切斷行不可逆反應； 步驟二13:將步驟二之油氣送至冷凝器冷卻至接近大氣 溫度，使得凝結並經沉澱後之液體即為輕原油，該輕原油之 密度為0.86，而部份未凝結之氣體即為瓦斯； 步驟四14:將步驟三之輕原油導入原油槽中儲存，以作 為提煉相關之柴油、汽油等； 1312290 步驟五15 :將步驟三之瓦斯經壓縮液化儲存，使其可以 裝桶或提供設備加熱之用； 步驟六16 :再將裂解爐内之乾燥污泥清除，即完成原油 與污泥之分離。 另外，於步驟一中’亦可加入不可燃性之垃圾（如：塑 耀類垃幻於裂解爐中與油污泥—同加熱裂解，使該不可燃 性垃圾可完全被裂解蒸發成油氣，致使該輕原油及瓦斯之產 量增加’而裂解爐内之污泥殘渣數量狀；另外，該驟四及 步驟五中所提煉之輕原油及瓦斯皆可作為間接加熱裂解爐 之燃料。 本發明所提供之油污泥與原油分離的方法，與其他習用 技術相互比較時，更具有下列之優點： L本發明係利用高溫間接加熱原油污泥，使該沾附於污泥 上之原油蒸發成油氣’再藉由冷凝器將其冷卻成輕原油及瓦 斯’以供使用者使用。 2. 本發明可於油污泥中加入塑膠垃圾，使其在不增加污泥 的數量下’並可增加輕原油提煉之數量。 3. 本發名明可利用劣質油、可燃性垃圾、煤炭及瓦斯作為 明 加熱油/7泥的燃料，且該劣質油及瓦斯係可利用本發 之方法自行提煉。 施例之具體說 上列詳細說明係針對本發明之—可行實 1312290 明’惟該實施例並非用以限制本發明之專利範圍，凡未脫離 本發明技藝精神所為之等效實施或變更，均應包含於本案之 專利範圍中。 综上所述，本案不但在技術思想上確屬創新，並能較習 用物品增進上述多項功效，應已充分符合新穎性及進步性之 法定發明專利要件，爰依法提出申請，懇請責局核准本件 發明專利申請案，以勵發明，至感德便。 【圖式簡單說明】 請參閱以下有關本發明一較佳實施例之詳細說明及其附 圖’將可進一步瞭解本發明之技術内容及其目的功效；有關 該實施例之附圖為： 圖一為本發明油污泥與原油分離的方法之步驟圖。 11步驟一 12步驟二 13步驟三 14步驟四 15步驟五 16步驟六1312290 玖, the invention description: [Technical field of the invention] The present invention relates to a method for separating oil sludge from crude oil, in particular, a method for evaporating crude oil contained in oil sludge into oil and gas, and then the oil and gas A method for separating oil sludge from crude oil into crude oil and crude oil. [Prior Art] Crude oil is usually contained in the deep underground. If it is to be mined, it needs to be explored and the correct position is taken before the oil well is excavated. After the well is drilled, the deep underground crude oil can be extracted and The extracted crude oil is placed in the original tank and shipped to all parts of the world. The countries then refine the crude oil into various available light crude oils (such as unleaded gasoline, diesel, and advanced gasoline); however, because the crude oil is from the underground The deep layer is extracted 'so that the extracted crude oil contains a large amount of sludge (such as: soil, sand, heavy metals and other impurities), the sludge itself has a certain weight, so that it will precipitate at the bottom of the crude oil tank, resulting in crude oil The amount of crude oil available for refining in the tank is reduced, and the crude oil is adhered to the sludge, so that the crude oil in the crude oil tank cannot be completely refined, which is not economical. Therefore, in order to extract the crude oil from the oil sludge, there is a technology to separate the crude oil from the sludge by the principle of centrifugal force. However, it can only extract a small portion of the crude oil on the sludge, and most of the crude oil is still attached. On the sludge, the oil sludge is quite difficult to be treated in the subsequent process, and it will cause air and environmental pollution regardless of burning or discarding it. Therefore, it is imperative to design a technology that completely extracts the crude oil from the sludge. It can be seen that there are still many shortcomings in the above-mentioned conventional techniques, which is not a good 1312290 designer, but needs to be improved. The inventors of the present case (4) all the shortcomings derived from the above-mentioned conventional methods are thoughts of improvement and innovation, and after years of painstaking research, they finally succeeded in research and development of the separation method of the oil sludge and crude oil. SUMMARY OF THE INVENTION The object of the present invention is to provide a method for separating oil sludge from the original by using a high-temperature indirect heating method and (4) separating the oil from the oil sludge. The second aspect of the present invention is to provide a method for separating extracted crude oil into light crude oil and gas oil sludge and crude oil. Another object of the present invention is to increase the separation of oil sludge and crude oil from the amount of light crude oil refining without increasing the amount of sludge residue in a purely supplyable type of plastics. Another object of the present invention is to provide a method for separating oil sludge from crude oil by using inferior oil, combustible f-waste #carbon and gas as fuel for indirectly heating oil sludge. The method for separating oil sludge from crude oil can achieve the following steps: 1. The oil sludge containing crude oil is directly placed in a cracking furnace and heated to 400-700 degrees in the cracking furnace and maintained at 3 The pressure of kilograms causes the crude oil contained in the oil sludge to be cracked into a gas state; 2. The oil in step one is sent to the condenser for cooling, so that the cooled oil and gas forms gas and light crude oil; 1312290 introduces the original gasoline 3. Guide the gas in step 2 to the gas trough, and let the user in the light crude oil guiding tank be used as a petrochemical intermediate raw material or into diesel or fuel oil. In addition, in this step, plastic waste can be added to increase the yield of light crude oil in the case of mud collapse; and its application: 2 [Embodiment] Self-production of gas, combustible garbage and coal. Referring to FIG. 1 , the oil method provided by the present invention is prepared by the steps of: separating the sludge from the crude oil. Step 11. The oil sludge is first placed in a cracking furnace in a combustion chamber for heating. The heating fuel can be: inferior oil, gas, coal and combustible garbage, etc., so that the temperature in the cracking furnace can be maintained at ~7 (8) degrees, and the pressure value of 3 kg is maintained therein to make the crude oil on the oil sludge Heating and evaporating into oil and gas, and then completely separated from the > 5 mud, so that the separated sludge residue is quite dry, like a mineral sand; Step 2: 12, the oil and gas is introduced into the reaction furnace for heating, and pressure control is performed to cut the molecules. The irreversible reaction is broken; Step 2: The oil in step 2 is sent to the condenser to be cooled to near atmospheric temperature, so that the liquid which is coagulated and precipitated is light crude oil, the density of the light crude oil is 0.86, and the part is not condensed. The gas is gas; Step 4: Step 3: The light crude oil is introduced into the crude oil tank for storage, as a refining related diesel, gasoline, etc.; 1312290 Step 5: Step 3: Gas compression through the third step Storage, or it can be installed to provide apparatus for heating the tub purposes; 16 Step Six: and then sludge removal cleavage drying oven, the complete separation of oil and sludge. In addition, in the first step, 'non-combustible garbage can also be added (for example, the plastic type is in the cracking furnace and the oil sludge - the same heat cracking, so that the non-combustible garbage can be completely cracked and evaporated into oil and gas, Resulting in an increase in the production of the light crude oil and gas, and the amount of sludge residue in the cracking furnace; in addition, the light crude oil and gas extracted in the fourth and fifth steps can be used as fuel for the indirect heating cracking furnace. The method for separating oil sludge and crude oil provided has the following advantages when compared with other conventional technologies: L. The invention utilizes high temperature indirect heating of crude sludge to evaporate the crude oil adhered to the sludge into oil and gas. 'It is cooled by the condenser to light crude oil and gas' for users to use. 2. The invention can add plastic waste to the oil sludge so that it can increase the amount of sludge without increasing the amount of sludge The quantity of crude oil refining 3. The name of the oil can be used as fuel for Ming heating oil/7 mud, and the inferior oil and gas can be extracted by the method of the present invention. The detailed description of the present invention is set forth in the Detailed Description of the Invention. The present invention is not intended to limit the scope of the present invention. All of them should be included in the scope of patents in this case. In summary, this case is not only innovative in terms of technical thinking, but also can enhance the above-mentioned multiple functions compared with conventional articles, and should fully comply with the statutory invention patent requirements of novelty and progress. , 提出Apply in accordance with the law, and ask the Responsible Office to approve the invention patent application, in order to invent the invention, to the sense of convenience. [Simplified description of the drawings] Please refer to the following detailed description of a preferred embodiment of the invention and its accompanying drawings The technical content of the present invention and its effects can be further understood; the accompanying drawings of the embodiment are: Figure 1 is a step diagram of the method for separating oil sludge from crude oil of the present invention. Step 11 Step 12 Step 13 Step 3 14 Step four 15 steps five 16 steps six