200841922 九'發明說明： 【發明所屬之技術領域】 本發明係有關於一種油細分離罐，特別是指一種可快速過濾凝結分離的 旋風式油細分離罐。 【先前技術】 請參閱第一圖，其係為習知技術之油細分離罐之結構示意圖；如圖所 示，習知油細分離罐10設置於一機台20,油細分離罐10包含一過濾管12、 | 一過濾材料14、一底座16與一罩體18，過渡管12頂端封閉，過濾管12 之外側壁設置過濾材料14，過濾管12之内側壁設置一滴油導流層15，而 過濾材料14外側更設有一預過滴油導流層17，底座16上方設有一孔洞 162,當油細分離罐10設置於機台20時，機台20之導管22穿設於孔洞162。 底座16設有有一環形溝槽164，環形溝槽164為凝油滯油區，，底座16下 方設有一空間166，罩體18設於底座16上方並罩設過濾管12之外圍.，使 罩體18與過濾管12具有一空間182，而空間166與空間182相互導通。 當機台20運作時’混合油氣從一油氣入口 24注入，並經油機台20導 至空間166 ’經由空間166而輸送至空間182，之後油氣經由預過滴油導流 % 層17穿過過濾材料14，在經由過濾材料14穿過滴油導流層15，如此使油 氣分離成潔淨的空氣與油滴。潔淨的空氣傳輸至過濾管12内，並且經由導 官22輸送至，機台20之一潔淨空氣出口 26。而油滴則由滴油導流層15凝 結並往下匯流至環形溝槽164，使油滴於凝油滯油區匯集，並經由一回油管 路168將油滴輸送至機台2〇之-回油管路出口沈，以使油滴可抽回再利 用。回油管路出口 28與-抽油駿連結，以加快油滴的輸送速率。 、，然而，為了減少過濾的時間，因此會將油氣的輸送速率提高，而且潔 淨空，出口 26連接-抽氣裝置，以增快油細分離罐的運作效率，因此於 過;慮官12會產生相纽的流速。賴油龜她油裝置鱗，使油滴不會 大量匯集於環形溝槽164，但因為過濾管12内的空氣流速相當大，因此空 200841922 氣會將凝油滯油區表面的油滴吹動，使凝油滯油區表面的油滴順著空氣氣 流流入導管22，因此使潔淨的空氣再次受到汙染，故必須再將出氣後的空 氣再次過濾，如此則增加過濾分離的次數，降低分離效率。 倘若能夠於快速的過濾分離情況下，又不使潔淨的空氣再次受到汙 染’則可加快過濾分離效率。故本發明提供一種旋風式油細分離罐，其係 於快速過濾時，可避免潔淨的空氣再次受到汙染，如此可解決上述之問題。 【發明内容】 本發明之主要目的，在於提供一種旋風式油細分離罐，其係藉由一阻 隔笞以改變混合油氣的過濾流向，如此使過濾分離後的油滴於過濾管外經 導引而再利用，以避免過濾分離後的油滴與潔淨的空氣再次混合，更可避 免及取過濾分離後的空氣之流速過大而帶入油滴之現象產生，進而增加過 濾分離效率。 本發明關於一種旋風式油細分離罐，其包含一阻隔管、一過濾管、一 $濾材料、-底座與-罩體，過濾管套設於阻隔管外，過濾管上端與阻隔 苔上4之間封閉’使阻隔管與過渡管之間具有一空間；過濾材料設於過遽 官亚位於空間内；底座設有—第_孔洞…環狀溝槽、至少一回油管路與 _ I進v由氣孔，阻隔官與過濾管設於底座上方，第一孔洞與阻隔管相接 設、，環狀溝槽環繞該過濾管之周圍，回油管路貫穿環狀溝槽之側壁與第一 孔洞之侧i n減i與空附目對於並貫穿底座；罩體設於底座上方並罩 設，狀溝槽之外圍。如此可達_鮮氣分離，再藉由細引力將油導引 至環狀溝槽底部，使油流入回油管，空氣則繞行上部經蓋體第二孔洞出氣， 經此分流後可避免過濾後的油滴與潔淨的空氣再次混合，更可於高速雜 油氣時，避紐速過大之空輕畅狀現象產生，以增純溏效率。 6 200841922 【實施方式】 兹為使貴審查委員對本發明之結構特徵及所達成之功效有更進一步 瞭識羞佐以較佳之實施例及配合詳細之說明，說明如後： 請參閱第二圖，其係為本發明較佳實施例之結構示意圖；如圖所示， 一，月之旋風式晶分離罐包含—阻隔管、—過濾管仙、—過濾材料5〇、 j 6〇與一罩體70，過濾管40套設於阻隔管30外，過濾管40上端與 阻隔官3〇上端之間封閉，使阻隔管30與過濾管40之間具有-空間32 ;過 :紐料，設於過濾管4G並錄空間32内；底錢之上方設有一第一孔 洞62第孔洞62之外圍設有一環狀溝槽64，阻隔管％與過滤管仙設 ^座6〇上方’第一孔洞62與阻隔管3〇相接設，環狀溝槽64環繞過澹 、吕狄之周圍’底座6〇更設有至少一回油管路⑽與至少一進油氣孔⑽，回 油官路66貫穿環狀溝槽64之侧壁與第一孔洞62之側壁，進油氣孔防與 玉門32相對並貝牙底座6〇，罩體7〇，設於底座6〇上方並罩設環狀溝⑽ 槽之外圍。 …阻隔管3G之管徑大於第62之雜巧本發明更包含—蓋體8〇, 盍體80具有-第二孔洞82，蓋體8〇設於阻隔管3〇與過滤管4〇上端並遮 蔽空間32 ’第二孔洞82與阻隔管30上端相接設。如此，空氣可自由的於 第一孔洞62與第二孔洞82之間流動。 回油管路66具有一第一開口 662與一第二開口 _，第一開口啦位 於環狀溝槽64之侧壁，第二開口 664錄第—孔洞62之側壁。第二開口 664之水平位置高於第-開口 662之水平位置，使回油管路66呈一 z字形。 第-孔洞62之内讎設有-第- 〇形環666與一第二〇形環_，第一 〇 形環666位於第二開口 664之上方’第二〇形環咖位於第二開口綱之 下方，第-0形環666小於第二〇形環。如此當油滴流經回油管路即 時’藉由第- 0形環666與第二〇形環668，達無茂漏疑慮。另外，過滤管 40之外側設有-滴油導流層85 ’以將it滤的油滴導引至環狀溝槽64。請一 併參閱第三圖，其係為本剌使聘之動作示意圖；如圖所示，本發明之 7 200841922 旋風式油細分離罐裝設於—機台9Q使用時，機台9G之—導管g2插設於第 =同62，並且於機台9G之—油氣人口 94輸人—混合油氣⑻，混合油 氣产1、.工由進油氣孔68，並且由進油氣孔68輸送至空間32。然後，混合 ，經由過遽材料5〇過濾，並且流經過渡管4〇而至滴油導流層. 械1G1刀離為—轉空氣1G2與—凝結油滴1G3。潔淨空氣102則 由罩體？^鱗麟85之_形成之—_2流動並减經第二孔 洞82至導官92,介由導管92將潔淨空氣1〇2抽取至一潔淨空氣出口 9[ 而凝結油則_經由脑導流層85難至環狀溝槽64;織，凝結油滴 • ⑽再經由回油管路66，從第H2流至第二開π 664，並經由機台 90七之-回油官路寶而流至—回油管路出口 ％，藉由回油管路岀口 ％以 將凝結油滴103排出。 本發明過歧向_由_外流的方式，並經由濾材的碱以提升過 濾凝結分離的效果，以最外徑位置作為凝油滞油區，提供低流速分離以防 止凝油再帶出而產生耗油’並且使驗殊⑽回油設計，搭配q型環的使 用不但使凝油與淨化空氣隔離；確保回油正常，無混合帶出的疑慮，更 達到無汽漏疑慮。而且’本發明之過據材料採用摺疊式波浪型凝結渡材， 故提供最大的械面積’依據有效面積，面積愈賴本發_賴壽命愈 鲁長’如此以達成最小阻抗，最大納垢容積，進而增進過遽效率。 經實驗測試，本發明在100psig (碎/每平方射）操作壓力條件下的 處理流量每分鐘介於i至6立方公尺。本發明在⑽响操傾力條件下， 新时的70王負载回油B寸達3. 5psid以下；而在新品使用壽命達6〇〜7⑽的壽 命^前，由ΐ過據材料使用波浪型大面積設計，因此錢均可維持在6psid 以達的目的。本發正常流量的使用情形且在獅啦的操 作麼力下，分離效率於下游端可達卜細觸毫克/立方公尺），以上游端達 _0_3的油污染物濃度；針對〇. 3微米汙染物的有卯.97%的移除率。 本發明依入氣及油過遽益的濾、效而有所影響，正常可達柳㈣刪運轉小 時。 200841922 立請參閱第四A圖與第四b圖，其係為本發明另一較佳實施例之結棒示 意圖，如圖所示，本發明之回油管路66可為其他之形式，例如圖四a第二 開口 664之水平位置等於第-開π 662之水平位置，歧圖四八第二開口 664之水平位置低於第一開口 662之水平位置。 …综上舰，本發明錢風式油細分_，其做_過齡套設於阻隔 官外^以最外徑位置作為凝油滯油區，提供低流速過濾凝結分離以防止凝 油再帶出而產生耗油，不但可避免過濾分離後的油滴與潔淨的空氣再次混200841922 九的发明说明: Technical Field of the Invention The present invention relates to a fine oil separation tank, and more particularly to a cyclone type fine separation tank which can be quickly filtered and separated by condensation. [Prior Art] Please refer to the first figure, which is a schematic structural view of a fine oil separation tank of the prior art; as shown, the conventional oil fine separation tank 10 is disposed on a machine table 20, and the oil fine separation tank 10 includes a filter tube 12, a filter material 14, a base 16 and a cover 18, the top end of the transition tube 12 is closed, the outer side of the filter tube 12 is provided with a filter material 14, and the inner side wall of the filter tube 12 is provided with a drop of oil-conducting layer 15 A pre-drip oil guiding layer 17 is further disposed on the outer side of the filter material 14. A hole 162 is defined in the upper portion of the base 16. When the oil fine separating tank 10 is disposed on the machine table 20, the duct 22 of the machine table 20 is disposed in the hole 162. . The base 16 is provided with an annular groove 164. The annular groove 164 is a condensing oil and stagnation zone. A space 166 is disposed under the base 16. The cover 18 is disposed above the base 16 and covers the periphery of the filter tube 12. The body 18 has a space 182 with the filter tube 12, and the space 166 and the space 182 are electrically connected to each other. When the machine 20 is in operation, 'mixed oil and gas is injected from an oil and gas inlet 24 and directed to the space 166 through the oil station 20 to the space 182, after which the oil and gas passes through the pre-drip oil flow control layer 17 The filter material 14 passes through the drip-conducting layer 15 via the filter material 14, thus separating the oil and gas into clean air and oil droplets. The clean air is delivered to the filter tube 12 and is delivered via the guide 22 to one of the machine 20 clean air outlets 26. The oil droplets are condensed by the drip drainage layer 15 and flow down to the annular groove 164, so that the oil droplets are collected in the oil stagnation zone, and the oil droplets are transported to the machine through a return line 168. - The return line outlet sinks so that the oil droplets can be pumped back for reuse. The return line outlet 28 is connected to the pumping unit to speed up the delivery rate of the oil droplets. However, in order to reduce the filtration time, the transportation rate of oil and gas will be increased, and the air is cleaned, and the outlet 26 is connected to the air extraction device to increase the efficiency of the oil separation tank. Therefore, it is over Generate a flow rate of the phase. The oily turtle has her oil device scale, so that the oil droplets will not collect in a large amount in the annular groove 164, but because the air flow rate in the filter tube 12 is quite large, the air 200841922 gas will blow the oil droplet on the surface of the oil lag area. The oil droplets on the surface of the oil stagnation zone flow into the conduit 22 along the air flow, so that the clean air is again contaminated, so the air after the outlet air must be filtered again, thus increasing the number of filtration separations and reducing the separation efficiency. . The filtration separation efficiency can be accelerated if the clean air is not contaminated again in the case of rapid filtration separation. Therefore, the present invention provides a cyclone type oil fine separation tank which is capable of preventing the clean air from being contaminated again during rapid filtration, thus solving the above problems. SUMMARY OF THE INVENTION The main object of the present invention is to provide a cyclone type oil fine separation tank, which is used to change the filtration flow direction of the mixed oil and gas by a barrier enthalpy, so that the oil separated by the filtration is guided outside the filter tube. Re-use to avoid re-mixing the oil droplets after filtration and separation with clean air, and avoiding the phenomenon that the flow rate of the air after filtration and separation is too large to bring in oil droplets, thereby increasing the filtration separation efficiency. The invention relates to a cyclone type oil fine separation tank, which comprises a blocking tube, a filter tube, a filter material, a base and a cover body, the filter tube is sleeved outside the blocking tube, and the upper end of the filter tube and the barrier moss are 4 There is a space between the barrier tube and the transition tube; the filter material is located in the space of the 遽 遽 亚 ;; the base is provided with the _ hole... the annular groove, at least one return line and _ I v is a gas hole, the barrier and the filter tube are arranged above the base, the first hole is connected with the blocking tube, the annular groove surrounds the filter tube, and the oil return pipe runs through the side wall of the annular groove and the first hole The side is reduced by i and the empty eye is connected to the base; the cover is placed above the base and covered, and the outer periphery of the groove. So reach _ fresh gas separation, and then guide the oil to the bottom of the annular groove by fine gravitation, so that the oil flows into the return pipe, and the air bypasses the upper part through the second hole of the cover body, after which the filtration can be avoided. After the oil droplets are mixed with the clean air again, it can be produced in the high-speed mixed oil and gas, avoiding the excessive speed of the new speed, so as to increase the purity efficiency. 6 200841922 [Embodiment] In order to make the reviewer's structural features and the efficacies of the present invention further savvy, the preferred embodiment and the detailed description are as follows: Please refer to the second figure. It is a schematic structural view of a preferred embodiment of the present invention; as shown in the figure, a cyclone type crystal separation tank comprises: a barrier tube, a filter tube, a filter material 5〇, a j 6〇 and a cover. 70, the filter tube 40 is sleeved outside the barrier tube 30, and the upper end of the filter tube 40 is closed between the upper end of the barrier member 3, so that there is a space between the barrier tube 30 and the filter tube 40; The tube 4G is recorded in the space 32; a first hole 62 is provided above the bottom money, and an annular groove 64 is disposed on the periphery of the hole 62. The blocking tube % and the filter tube are disposed above the first hole 62 The blocking tube 3 is connected, the annular groove 64 surrounds the raft, and the surrounding base of the Ludi is provided with at least one oil return line (10) and at least one inlet oil and gas hole (10), and the oil returning official road 66 runs through the annular groove. The side wall of 64 and the side wall of the first hole 62, the inlet and outlet holes are opposite to the Yumen 32 The base of the shell is 6 〇, and the cover is 7 〇. It is arranged above the base 6〇 and covers the periphery of the groove of the annular groove (10). The pipe diameter of the blocking pipe 3G is larger than that of the 62nd. The present invention further includes a cover body 8〇, the body 80 has a second hole 82, and the cover body 8 is disposed at the upper end of the blocking pipe 3〇 and the filter pipe 4并The shielding space 32 'the second hole 82 is connected to the upper end of the blocking tube 30. Thus, air can flow freely between the first hole 62 and the second hole 82. The oil return line 66 has a first opening 662 and a second opening _, the first opening is located on the side wall of the annular groove 64, and the second opening 664 is recorded on the side wall of the first hole 62. The horizontal position of the second opening 664 is higher than the horizontal position of the first opening 662, so that the oil return line 66 has a zigzag shape. The first hole 666 is provided with a first - 〇 ring 666 and a second 〇 ring _, and the first 〇 ring 666 is located above the second opening 664. Below the 0th ring 666 is smaller than the second ring. Thus, when the oil droplets flow through the oil return line, by the first-shaped ring 666 and the second ring-shaped ring 668, there is no doubt. Further, an oil-dropping layer 85' is provided on the outer side of the filter tube 40 to guide the oil droplets filtered by it to the annular groove 64. Please refer to the third figure, which is a schematic diagram of the action of the hiring; as shown in the figure, the 7 200841922 of the present invention is installed in the cyclone type oil separation tank when the machine 9Q is used, the machine 9G- The conduit g2 is inserted in the same = 62, and the oil and gas population 94 in the machine 9G is mixed with the oil and gas (8), the mixed oil and gas production 1, the work is carried into the oil and gas hole 68, and is transported to the space 32 by the oil and gas hole 68. . Then, the mixture is filtered through the crucible material 5〇, and flows through the transition tube 4〇 to the drip-conducting layer. The mechanical 1G1 knife is separated from the air 1G2 and the condensed oil droplet 1G3. Clean air 102 is covered by the cover? ^The scale of the squadron 85 forms a _2 flow and reduces the second hole 82 to the guide 92, and the clean air 1 〇 2 is drawn to a clean air outlet 9 via the conduit 92 [and the condensed oil is _ via the brain diversion Layer 85 is difficult to ring groove 64; weaving, condensing oil droplets • (10) through the oil return line 66, from the H2 flow to the second open π 664, and through the machine 90 seven - return to the oil official road To the return line % of the return line, the condensed oil drop 103 is discharged by the % of the return line of the return line. The invention overcomes the problem of _ outflow, and enhances the effect of filtration and condensation separation through the alkali of the filter material, and uses the outermost diameter position as the condensate oil lag zone to provide low flow rate separation to prevent the condensate from being brought back again. Fuel consumption 'and make the special (10) oil return design, with the use of the q-ring not only to isolate the condensate from the clean air; to ensure that the oil return is normal, no doubts brought out by mixing, and no doubt about steam leakage. Moreover, the material of the present invention adopts a folded wave type condensing ferry material, so that the maximum mechanical area is provided. According to the effective area, the area is more than the longest life, so that the minimum impedance and the maximum nanoscale volume are further achieved. Improve over-efficiency. Experimentally, the process flow rate of the present invention at 100 psig (shred/per square shot) operating pressure is between i and 6 cubic meters per minute. The invention is under the condition of (10) sounding force, the new 70 king load return oil B inch reaches 3. 5psid; and before the new product service life reaches 6 〇~7 (10) life ^, the wave type is used according to the material Large-scale design, so the money can be maintained at 6psid. In the case of the normal flow of the hair, and under the operation of the lion, the separation efficiency can reach the milligram/m3 of the downstream end, and the oil concentration of the upstream end reaches _0_3; Micron contaminants have a removal rate of 97%. The invention has an influence on the filtration and effect of the gas and the oil, and the normal operation can reach the Liu (4) operation time. 200841922 Please refer to FIG. 4A and FIG. 4b, which are schematic diagrams of a connecting rod according to another preferred embodiment of the present invention. As shown, the oil return line 66 of the present invention may be in other forms, such as The horizontal position of the second opening 664 of the fourth a is equal to the horizontal position of the first opening π 662, and the horizontal position of the second opening 664 of the fourth drawing is lower than the horizontal position of the first opening 662. ...Overall ship, the invention of the wind-type oil subdivision _, its _ over-age set outside the barrier official ^ as the outer diameter position as a condensate oil lag zone, providing low flow rate filtration condensation separation to prevent condensate re-banding Produce fuel consumption, which not only avoids the oil droplets after filtration and separation and remixes with clean air.
合，更可於快賴濾域時，避免流速過大之空氣吸取帶人關之現 生，以增加過濾分籬敎案。 進步性及可供產業利用者，應符合我 ，爰依法提出發明專利申請，祈鈞 故本發明係實為一具有新穎性、 國專利法所規定之專利申請要件無疑 局早日賜准專利，至感為禱。In addition, it is better to avoid the excessive flow of air to take care of the people in the filter field to increase the filter fence. Progressive and available to the industry, should comply with me, 提出 file an invention patent application according to law, praying that the invention is a novelty, the patent application requirements stipulated by the national patent law, the bureau will soon grant a patent, to Feeling a prayer.
惟以上所述者，僅為本發明之一§^ A 軏仏只她例而已，並非用來限定本發 月貝釔之補，舉凡依本發”料纖圍 、^ 神所為之均频倾修飾，均餘括於本發_請補徵及精 【圖式簡單說明】 鲁 第一圖為習知技術之油細分離罐之結構示意圖； 第二圖為本發明較佳實施例之結構示意圖； ‘第二圖為本發明使用時之動作示意圖； 以及 第四Α圖為本發明另一較佳實施例之結構示意圖 第四B圖為本發明另一較佳實施例之結構示^圖 【主要元件符號說明】 10油細分離罐 12過渡管 14過渡材料 200841922 15滴油導流層 16底座 162孔洞 164環形溝槽 166空間 168回油管路 17預過滴油導流層 18罩體 182空間 • 20機台 24油氣入口 26潔淨空氣出口 28回油管路出口 30阻隔管 32空間 40過濾管 50過渡材料 60底座 62第一孔洞 64環狀溝槽 66回油管 662第一開口 664第二開口 666第一 0形環 668第二0形環 68進油氣孔 70罩體 10 200841922 80蓋體 82第二孔洞 85滴油導流層 90機台 92導管 94油氣入口 101混合油氣 102潔淨空氣 103凝結油滴However, the above is only one of the §^ A 本 本 A , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , , Modifications, all of which are included in the present invention _ Please replenish and fine [Simplified description of the drawings] The first figure is a schematic structural view of a fine oil separation can of the prior art; the second figure is a schematic view of the structure of the preferred embodiment of the present invention. The second diagram is a schematic diagram of the operation of the present invention; and the fourth diagram is a schematic structural view of another preferred embodiment of the present invention. FIG. 4B is a structural diagram of another preferred embodiment of the present invention. Main component symbol description] 10 oil fine separation tank 12 transition tube 14 transition material 200841922 15 drop oil drainage layer 16 base 162 hole 164 annular groove 166 space 168 return oil pipeline 17 pre-drip oil guide layer 18 cover 182 space • 20 machine 24 oil and gas inlet 26 clean air outlet 28 return oil line outlet 30 barrier tube 32 space 40 filter tube 50 transition material 60 base 62 first hole 64 annular groove 66 return oil pipe 662 first opening 664 second opening 666 The first 0-ring 668 is the second 0-ring 68 Cover hole 70 1020084192280 82 second drip guide holes 85 cover layer 90 the machine 92 an inlet conduit 94 and gas mixing and gas 102 101 103 clean air droplets condense