TWI685378B - Emulsified heavy oil equipment - Google Patents
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- TWI685378B TWI685378B TW107131951A TW107131951A TWI685378B TW I685378 B TWI685378 B TW I685378B TW 107131951 A TW107131951 A TW 107131951A TW 107131951 A TW107131951 A TW 107131951A TW I685378 B TWI685378 B TW I685378B
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Abstract
Description
本發明係關於一種生產設備,特別是指一種乳化重油設備。The invention relates to a production equipment, in particular to an emulsified heavy oil equipment.
重油是在原油提煉汽油、柴油等輕質油後,剩餘的可燃較重質燃油,產業上常會利用重油燃燒後所產生之熱能或熱量,例如用於大型蒸汽輪機鍋爐及中大型船舶用引擎的燃油,或者作為大型燃煤鍋爐的啟動點火燃料。Heavy oil is the remaining combustible heavier fuel oil after crude oil is refined into light oil such as gasoline and diesel oil. The industry often uses the heat or heat generated by the combustion of heavy oil, such as used in large steam turbine boilers and medium and large ship engines. Fuel oil, or as the ignition fuel for large coal-fired boilers.
然而,由於重油本身黏度高又含有許多瀝青顆粒,故重油經一般噴嘴霧化所形成的油滴之大小仍難以在短時間內從液相裂解蒸發為氣相,容易導致燃燒不完全的情形。此外也容易造成霧化不佳、混合氣不均勻或局部濃度過高等問題。尤其在缺氧條件下,更會引起熱分解,生成許多碳粒,而容易在燃燒時產生黑煙,且燃燒器噴嘴容易產生堵塞及積碳等問題,導致污染環境及油耗提高等缺點。However, because the heavy oil itself has a high viscosity and contains many asphalt particles, the size of the oil droplets formed by heavy oil atomization through a general nozzle is still difficult to crack and evaporate from the liquid phase to the gas phase in a short time, which is likely to cause incomplete combustion. In addition, it is also easy to cause problems such as poor atomization, uneven gas mixture or high local concentration. Especially under anoxic conditions, it will cause thermal decomposition and generate a lot of carbon particles, and it is easy to produce black smoke during combustion, and burner nozzles are prone to clogging and carbon deposition and other problems, leading to shortcomings such as pollution of the environment and increased fuel consumption.
鑒於上述,於一實施例中,提供一種乳化重油設備,包括油水混合裝置、粒化裝置以及燃燒裝置。油水混合裝置包括容置桶槽與設於容置桶槽中的攪拌器,容置桶槽中容設有水液、重油及乳化劑,攪拌器攪拌水液、重油及乳化劑以形成油水混合液,容置桶槽連接出液管路以輸出油水混合液。粒化裝置包括奈米管,奈米管包括入口與出口,且奈米管的管壁設有複數個切割孔,入口連通於出液管路以將油水混合液導入奈米管中,且油水混合液通過切割孔以形成複數個油包水液滴並由出口輸出。燃燒裝置包括燃燒室與雙流體噴嘴,雙流體噴嘴包括進液管、進氣管及噴出孔,噴出孔連通於燃燒室,進液管連通於出口與噴出孔之間,進氣管連通於進液管以導入氣體,油包水液滴通過進液管而從噴出孔噴入燃燒室中。In view of the above, in one embodiment, an emulsified heavy oil device is provided, including an oil-water mixing device, a granulation device, and a combustion device. The oil-water mixing device includes an accommodating barrel tank and an agitator provided in the accommodating barrel tank. The accommodating barrel tank contains water liquid, heavy oil and emulsifier, and the agitator agitates the water liquid, heavy oil and emulsifier to form an oil-water mixture Liquid, accommodating barrel tank connected to the liquid line to output oil-water mixed liquid. The granulation device includes a nanotube, and the nanotube includes an inlet and an outlet, and the wall of the nanotube is provided with a plurality of cutting holes, and the inlet is connected to the liquid outlet line to introduce the oil-water mixture into the nanotube, and the oil and water The mixed liquid passes through the cutting holes to form a plurality of water-in-oil droplets and is output from the outlet. The combustion device includes a combustion chamber and a two-fluid nozzle. The two-fluid nozzle includes a liquid inlet pipe, an air inlet pipe, and a spray hole. The spray hole communicates with the combustion chamber, the liquid inlet pipe communicates between the outlet and the spray hole, and the air inlet pipe communicates with the inlet. The liquid pipe is used to introduce gas, and water-in-oil droplets are injected into the combustion chamber from the injection hole through the liquid inlet pipe.
綜上所述,本發明實施例之乳化重油設備透過奈米管將油水混合液切割細化,以形成細小的油包水液滴,使油包水液滴在導送的過程中不容易發生堵塞的情形,減少燃燒不全而強化燃燒效率與降低油耗,達到有效抑制黑煙產生而減少廢氣排放。此外,本發明實施例更透過雙流體噴嘴將油包水液滴霧化並且加壓噴入燃燒室中,可更利於油包水液滴完全燃燒且避免堵塞於雙流體噴嘴處,有效提升燃燒的效率。In summary, the emulsified heavy oil equipment of the embodiment of the present invention cuts and refines the oil-water mixture through the nanotube to form fine water-in-oil droplets, so that the water-in-oil droplets do not easily occur during the delivery process In the case of clogging, incomplete combustion is reduced to enhance combustion efficiency and reduce fuel consumption, so as to effectively suppress the generation of black smoke and reduce exhaust emissions. In addition, the embodiment of the present invention further atomizes the water-in-oil droplets through the dual-fluid nozzle and sprays them into the combustion chamber under pressure, which is more conducive to complete combustion of the water-in-oil droplets and avoids clogging at the dual-fluid nozzle, effectively improving combustion s efficiency.
圖1與圖2為本發明乳化重油設備一實施例之平面圖與局部平面圖。如圖1與圖2所示,本發明實施例之乳化重油設備1包括油水混合裝置10、粒化裝置20以及燃燒裝置30。1 and 2 are a plan view and a partial plan view of an embodiment of an emulsified heavy oil equipment of the present invention. As shown in FIGS. 1 and 2, the emulsified
如圖1所示,油水混合裝置10包括容置桶槽11。其中容置桶槽11中容設有水液W、重油O及乳化劑E,例如在本實施例中,容置桶槽11可連通一貯水槽2、一貯油槽3以及一乳化劑槽4,以分別由貯水槽2、貯油槽3及乳化劑槽4導入預定量的水液W、重油O及乳化劑E至容置桶槽11中。As shown in FIG. 1, the oil-
如圖1所示,在一實施例中,貯水槽2連接一第一管路5,貯油槽3連接一第二管路6,乳化劑槽4連接一第三管路7,其中第二管路6延伸至容置桶槽11,第一管路5與第三管路7分別連通於第二管路6,且第二管路6上設有一泵浦B,當泵浦B運轉時,可將水液W與乳化劑E導送至第二管路6再連同重油O一起導送至容置桶槽11中。然而,上述實施例僅為舉例,實際上,第一管路5、第二管路6及第三管路7可根據實際需求而有不同配置,舉例來說,第一管路5、第二管路6及第三管路7也可分別連通於容置桶槽11,以分別導送水液W、重油O及乳化劑E至容置桶槽11中。As shown in FIG. 1, in one embodiment, the
在一些實施例中,水液W、重油O及乳化劑E導入容置桶槽11中流量不同,例如每分鐘流入容置桶槽11中的重油O的油量大於水液W的水量,水液W的水量大於乳化劑E的劑量。上述流量的控制可透過管路配置大小或者於管路上設有流量控制閥等方式實現,在此則不多加贅述。In some embodiments, the flow rate of water W, heavy oil O and emulsifier E introduced into the
如圖1所示,容置桶槽11中設有一攪拌器12,攪拌器12可為各式攪拌機構,例如槳式攪拌器、螺桿式攪拌器或渦輪式攪拌器等等,當攪拌器12運作時(例如以一預定轉速旋轉),可攪拌容置桶槽11中的水液W、重油O及乳化劑E以初步混合形成一油水混合液M。此外,容置桶槽11更連接一出液管路13以輸出油水混合液M。As shown in FIG. 1, an
如圖1所示,粒化裝置20包括奈米管21,奈米管21具有入口22與出口23,且奈米管21的管壁設有複數個切割孔24(表示於圖4),入口22連通於出液管路13以將油水混合液M導入奈米管21中,當油水混合液M通過奈米管21中的各切割孔24,可受到切割孔24切割細化,使已混合乳化劑E的重油O可將細化的水液W包覆而形成更細小的多個油包水液滴D,且多個油包水液滴D能由奈米管21的出口23輸出。As shown in FIG. 1, the
在一些實施例中,奈米管21可為多層管路。例如圖3所示,在本實施例中,奈米管21為三層管路,包括一外層薄膜管211、一內層網管213以及一中層金屬管212,中層金屬管212夾設於外層薄膜管211與內層網管213之間,舉例來說,外層薄膜管211可為耐高溫收縮玻璃膜真空製造成的管路,中層金屬管212可為不銹鋼管,內層網管213可為不銹鋼網管。各切割孔24為開設於中層金屬管212管壁之孔洞,當油水混合液M導入奈米管21時,可通過內層網管213與中層金屬管212的各切割孔24切割細化而形成多個油包水液滴D。如圖4所示,在一實施例中,中層金屬管212可開設有多個十字形的切割孔24,或者如圖5所示,在一實施例中,中層金屬管212可開設有多個Y字形的切割孔24’。然而,上述實施例之切割孔24的形狀僅為舉例,實際上並不以此為限。In some embodiments, the
在一些實施例中,燃燒裝置30可為但不限於鍋爐或燃燒爐,如圖1與圖2所示,燃燒裝置30包括燃燒室31與雙流體噴嘴32,雙流體噴嘴32包括進液管33、進氣管34及噴出孔35,噴出孔35連通於燃燒室31,進液管33連通於奈米管21的出口23與噴出孔35之間,且噴出孔35的孔徑小於進液管33的管徑。進氣管34連通於進液管33以導入氣體。例如圖2所示,在本實施例中,進氣管34連接一鼓風機341,但亦可為空壓機,鼓風機341運作時可經由進氣管34將氣體導入至進液管33中。藉此,當油包水液滴D從奈米管21的出口23進入進液管33後,可藉由進氣管34導入的氣體加壓而從噴出孔35噴入燃燒室31中進行燃燒。In some embodiments, the
綜上,本發明實施例之乳化重油設備1透過奈米管21將油水混合液M切割細化,以形成細小的油包水液滴D,使油包水液滴D在導送的過程中不容易發生堵塞的情形,減少燃燒不全而強化燃燒效率與降低油耗,達到有效抑制黑煙產生而減少廢氣排放。此外,本發明實施例更透過雙流體噴嘴32將油包水液滴D霧化並且加壓噴入燃燒室31中,可更利於油包水液滴D完全燃燒且避免堵塞於雙流體噴嘴32處,有效提升燃燒的效率。In summary, the emulsified
如圖1所示,在一實施例中,容置桶槽11所連接之出液管路13上可設有加壓泵P,當加壓泵P運作時,可將由出液管路13輸出之油水混合液M進一步加壓沖入奈米管21中而能更有效地受到切割孔24切割細化。As shown in FIG. 1, in one embodiment, a pressurizing pump P may be provided on the
請對照圖1與圖2所示,在一實施例中,奈米管21之入口22與雙流體噴嘴32之間可設有回流管路25,回流管路25連通至油水混合裝置10之容置桶槽11。藉此,當奈米管21的生成量過剩時,可將過剩量經由回流管路25回送至油水混合裝置10之容置桶槽11,以使乳化重油設備1能夠持續循環運作。Referring to FIGS. 1 and 2, in one embodiment, a
再如圖1所示,在一實施例中,油水混合裝置10之容置桶槽11內更設有一酸鹼值感測器14,以即時監控容置桶槽11內之液體的酸鹼值,藉以隨時調整而保持一預定酸鹼值(例如PH10~11),例如容置桶槽11內之液體的酸鹼值過低時,可加入適量的弱鹼性添加劑,以調整回預定酸鹼值,防止油水混合液M通過之管路或機器生鏽。As shown in FIG. 1 again, in an embodiment, a
如圖6所示,在一實施例中,容置桶槽11所連接之出液管路13內可設有複數個珠體131(例如不銹鋼珠),且多個珠體131是位於加壓泵P與奈米管21之間,當加壓泵P運作時,可使油水混合液M加壓沖入多個珠體131之間時,而能夠進一步細化後再進入奈米管21中以減少管路的堵塞。As shown in FIG. 6, in one embodiment, a plurality of beads 131 (such as stainless steel beads) may be provided in the
如圖7所示,在一實施例中,攪拌器12為槳式攪拌器且包括轉軸121與連接於轉軸121之兩個葉片組122,兩個葉片組122彼此上下間隔配置,且各葉片組122包括複數個第一葉片123、複數個第二葉片124與複數個第三葉片125,在本例中,第一葉片123、第二葉片124及第三葉片125的數量分別為三個,但此並不侷限。此外,各第一葉片123、各第二葉片124及各第三葉片125的傾斜角度不同。例如在本實施例中,各葉片組122的多個第一葉片123分別徑向延伸自轉軸121且呈等角配置,且第一葉片123的面朝向與轉軸121的軸向垂直,各葉片組122的多個第二葉片124分別徑向延伸自轉軸121且呈等角配置,此外,各第二葉片124與各第一葉片123的傾斜角度不同,各葉片組122的多個第三葉片125同樣分別徑向延伸自轉軸121且呈等角配置,各第三葉片125具有圓弧狀端面且可與各第二葉片124的傾斜角度相同或不同。As shown in FIG. 7, in an embodiment, the
承上,當攪拌器12之轉軸121旋轉時,可藉由轉動中之葉片組122的第一葉片123拍打水液W、重油O及乳化劑E,而第二葉片124則可切割液體,使其形成小單位分子,第三葉片125的圓弧狀端面則可造成漩渦之渦流,如此,使得水液W、重油O及乳化劑E於容置桶槽11內藉由第一葉片123、第二葉片124及第三葉片125產生不同的攪拌作用,可提高重油O之乳化程度。According to the above, when the
雖然本發明的技術內容已經以較佳實施例揭露如上,然其並非用以限定本發明,任何熟習此技藝者,在不脫離本發明之精神所作些許之更動與潤飾,皆應涵蓋於本發明的範疇內,因此本發明之保護範圍當視後附之申請專利範圍所界定者為準。Although the technical content of the present invention has been disclosed as above with preferred embodiments, it is not intended to limit the present invention. Anyone who is familiar with this art and makes some changes and retouching without departing from the spirit of the present invention should be covered in the present invention. The scope of protection of the present invention shall be subject to the scope of the attached patent application.
1‧‧‧乳化重油設備1‧‧‧Emulsified heavy oil equipment
2‧‧‧貯水槽2‧‧‧storage tank
3‧‧‧貯油槽3‧‧‧Oil storage tank
4‧‧‧乳化劑槽4‧‧‧Emulsifier tank
5‧‧‧第一管路5‧‧‧ First pipeline
6‧‧‧第二管路6‧‧‧Second pipeline
7‧‧‧第三管路7‧‧‧Third pipeline
10‧‧‧油水混合裝置10‧‧‧Oil-water mixing device
11‧‧‧容置桶槽11‧‧‧accommodating barrel tank
12‧‧‧攪拌器12‧‧‧Agitator
121‧‧‧轉軸121‧‧‧spindle
122‧‧‧葉片組122‧‧‧Blade group
123‧‧‧第一葉片123‧‧‧The first blade
124‧‧‧第二葉片124‧‧‧Second blade
125‧‧‧第三葉片125‧‧‧third blade
13‧‧‧出液管路13‧‧‧ Outlet pipe
131‧‧‧珠體131‧‧‧Pearl
14‧‧‧酸鹼值感測器14‧‧‧pH sensor
20‧‧‧粒化裝置20‧‧‧Granulation device
21‧‧‧奈米管21‧‧‧Nanotube
211‧‧‧外層薄膜管211‧‧‧Outer film tube
212‧‧‧中層金屬管212‧‧‧Medium metal tube
213‧‧‧內層網管213‧‧‧Inner network management
22‧‧‧入口22‧‧‧ entrance
23‧‧‧出口23‧‧‧Export
24、24’‧‧‧切割孔24, 24’‧‧‧cutting hole
25‧‧‧回流管路25‧‧‧ Return line
30‧‧‧燃燒裝置30‧‧‧Combustion device
31‧‧‧燃燒室31‧‧‧combustion chamber
32‧‧‧雙流體噴嘴32‧‧‧Two-fluid nozzle
33‧‧‧進液管33‧‧‧Inlet tube
34‧‧‧進氣管34‧‧‧Intake pipe
341‧‧‧鼓風機341‧‧‧Blower
35‧‧‧噴出孔35‧‧‧Ejection hole
W‧‧‧水液W‧‧‧Water
O‧‧‧重油O‧‧‧Heavy oil
E‧‧‧乳化劑E‧‧‧Emulsifier
M‧‧‧油水混合液M‧‧‧oil-water mixture
D‧‧‧油包水液滴D‧‧‧Water-in-oil droplets
B‧‧‧泵浦B‧‧‧Pump
P‧‧‧加壓泵P‧‧‧Pressure pump
[圖1] 為本發明乳化重油設備一實施例之平面圖。 [圖2] 為本發明乳化重油設備一實施例之局部平面圖。 [圖3] 為本發明粒化裝置一實施例之剖視圖。 [圖4] 為本發明粒化裝置一實施例之局部平面圖。 [圖5] 為本發明粒化裝置另一實施例之局部平面圖。 [圖6] 為本發明乳化重油設備另一實施例之局部平面圖。 [圖7] 為本發明攪拌器一實施例之平面圖。[Figure 1] This is a plan view of an embodiment of the emulsified heavy oil equipment of the present invention. [Figure 2] This is a partial plan view of an embodiment of an emulsified heavy oil equipment of the present invention. [Fig. 3] This is a cross-sectional view of an embodiment of the granulation device of the present invention. [Fig. 4] It is a partial plan view of an embodiment of the granulation device of the present invention. [FIG. 5] This is a partial plan view of another embodiment of the granulation device of the present invention. [Fig. 6] This is a partial plan view of another embodiment of the emulsified heavy oil equipment of the present invention. [Figure 7] This is a plan view of an embodiment of the agitator of the present invention.
1‧‧‧乳化重油設備 1‧‧‧Emulsified heavy oil equipment
2‧‧‧貯水槽 2‧‧‧storage tank
3‧‧‧貯油槽 3‧‧‧Oil storage tank
4‧‧‧乳化劑槽 4‧‧‧Emulsifier tank
5‧‧‧第一管路 5‧‧‧ First pipeline
6‧‧‧第二管路 6‧‧‧Second pipeline
7‧‧‧第三管路 7‧‧‧Third pipeline
10‧‧‧油水混合裝置 10‧‧‧Oil-water mixing device
11‧‧‧容置桶槽 11‧‧‧accommodating barrel tank
12‧‧‧攪拌器 12‧‧‧Agitator
13‧‧‧出液管路 13‧‧‧ Outlet pipe
14‧‧‧酸鹼值感測器 14‧‧‧pH sensor
20‧‧‧粒化裝置 20‧‧‧Granulation device
21‧‧‧奈米管 21‧‧‧Nanotube
22‧‧‧入口 22‧‧‧ entrance
23‧‧‧出口 23‧‧‧Export
25‧‧‧回流管路 25‧‧‧ Return line
30‧‧‧燃燒裝置 30‧‧‧Combustion device
W‧‧‧水液 W‧‧‧Water
O‧‧‧重油 O‧‧‧Heavy oil
E‧‧‧乳化劑 E‧‧‧Emulsifier
M‧‧‧油水混合液 M‧‧‧oil-water mixture
D‧‧‧油包水液滴 D‧‧‧Water-in-oil droplets
B‧‧‧泵浦 B‧‧‧Pump
P‧‧‧加壓泵 P‧‧‧Pressure pump
Claims (9)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW107131951A TWI685378B (en) | 2018-09-11 | 2018-09-11 | Emulsified heavy oil equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW107131951A TWI685378B (en) | 2018-09-11 | 2018-09-11 | Emulsified heavy oil equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
TWI685378B true TWI685378B (en) | 2020-02-21 |
TW202010567A TW202010567A (en) | 2020-03-16 |
Family
ID=70413303
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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TW107131951A TWI685378B (en) | 2018-09-11 | 2018-09-11 | Emulsified heavy oil equipment |
Country Status (1)
Country | Link |
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TW (1) | TWI685378B (en) |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100395036C (en) * | 2003-01-22 | 2008-06-18 | 孙泰炎 | Double-fluid nozzle |
TWM444218U (en) * | 2012-06-13 | 2013-01-01 | Tian-Yu Huang | Heavy oil emulsified device |
TW201412402A (en) * | 2012-09-25 | 2014-04-01 | Grand Extension Oil Co Ltd | Process of producing emulsified diesel |
CN203648467U (en) * | 2013-12-27 | 2014-06-18 | 常州市如兴油品科技有限公司 | Modified heavy oil equipment |
WO2015199075A1 (en) * | 2014-06-24 | 2015-12-30 | 深井 利春 | Device for supplying emulsified fuel and method for supplying said fuel |
CN206253030U (en) * | 2016-11-11 | 2017-06-16 | 江苏釜鼎能源科技有限公司 | A kind of feedstock oil mixing and emulsifying device |
-
2018
- 2018-09-11 TW TW107131951A patent/TWI685378B/en not_active IP Right Cessation
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN100395036C (en) * | 2003-01-22 | 2008-06-18 | 孙泰炎 | Double-fluid nozzle |
TWM444218U (en) * | 2012-06-13 | 2013-01-01 | Tian-Yu Huang | Heavy oil emulsified device |
TW201412402A (en) * | 2012-09-25 | 2014-04-01 | Grand Extension Oil Co Ltd | Process of producing emulsified diesel |
CN203648467U (en) * | 2013-12-27 | 2014-06-18 | 常州市如兴油品科技有限公司 | Modified heavy oil equipment |
WO2015199075A1 (en) * | 2014-06-24 | 2015-12-30 | 深井 利春 | Device for supplying emulsified fuel and method for supplying said fuel |
CN206253030U (en) * | 2016-11-11 | 2017-06-16 | 江苏釜鼎能源科技有限公司 | A kind of feedstock oil mixing and emulsifying device |
Also Published As
Publication number | Publication date |
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TW202010567A (en) | 2020-03-16 |
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