WO2008119199A1 - An oil-gas mixing and dispersing structure - Google Patents

An oil-gas mixing and dispersing structure Download PDF

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Publication number
WO2008119199A1
WO2008119199A1 PCT/CN2007/001027 CN2007001027W WO2008119199A1 WO 2008119199 A1 WO2008119199 A1 WO 2008119199A1 CN 2007001027 W CN2007001027 W CN 2007001027W WO 2008119199 A1 WO2008119199 A1 WO 2008119199A1
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WO
WIPO (PCT)
Prior art keywords
gas
oil
input portion
mixing
dispersing
Prior art date
Application number
PCT/CN2007/001027
Other languages
French (fr)
Chinese (zh)
Inventor
Chung Min Yang
Chao Psung Huang
Original Assignee
Chung Min Yang
Chao Psung Huang
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Publication date
Application filed by Chung Min Yang, Chao Psung Huang filed Critical Chung Min Yang
Priority to PCT/CN2007/001027 priority Critical patent/WO2008119199A1/en
Publication of WO2008119199A1 publication Critical patent/WO2008119199A1/en

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/232—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F23/00—Mixing according to the phases to be mixed, e.g. dispersing or emulsifying
    • B01F23/20—Mixing gases with liquids
    • B01F23/23—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids
    • B01F23/232—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles
    • B01F23/2326—Mixing gases with liquids by introducing gases into liquid media, e.g. for producing aerated liquids using flow-mixing means for introducing the gases, e.g. baffles adding the flowing main component by suction means, e.g. using an ejector
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30—Injector mixers
    • B01F25/31—Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3121—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof with additional mixing means other than injector mixers, e.g. screens, baffles or rotating elements
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F25/00—Flow mixers; Mixers for falling materials, e.g. solid particles
    • B01F25/30—Injector mixers
    • B01F25/31—Injector mixers in conduits or tubes through which the main component flows
    • B01F25/312—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof
    • B01F25/3124—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow
    • B01F25/31242—Injector mixers in conduits or tubes through which the main component flows with Venturi elements; Details thereof characterised by the place of introduction of the main flow the main flow being injected in the central area of the venturi, creating an aspiration in the circumferential part of the conduit
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/05—Stirrers
    • B01F27/11—Stirrers characterised by the configuration of the stirrers
    • B01F27/113—Propeller-shaped stirrers for producing an axial flow, e.g. shaped like a ship or aircraft propeller
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
    • B01F27/00—Mixers with rotary stirring devices in fixed receptacles; Kneaders
    • B01F27/55—Mixers with rotary stirring devices in fixed receptacles; Kneaders with stirrers driven by the moving material
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/68—Treatment of water, waste water, or sewage by addition of specified substances, e.g. trace elements, for ameliorating potable water
    • C—CHEMISTRY; METALLURGY
    • C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
    • C02F1/00—Treatment of water, waste water, or sewage
    • C02F1/72—Treatment of water, waste water, or sewage by oxidation
    • C02F1/78—Treatment of water, waste water, or sewage by oxidation with ozone

Definitions

  • the invention provides a structure of a processing mechanical component, in particular to a hydrocarbon mixing and breaking structure which is formed by borrowing the diameter difference between the outlet end pipe and the vacuum suction, so that the inhaled gas is fully mixed, and the bubble is broken when the bubble is broken.
  • Today's processing machinery uses some oil, cutting fluid, coolant, etc., as the waste heat of the cooling process, but some oil, cutting fluid, coolant, etc., are repeatedly used repeatedly, and some impurities will inevitably be mixed inside. Further, the oil agent, the cutting fluid or the coolant starts to deteriorate, and bacteria or odor is generated, which not only affects environmental sanitation, but also requires the addition of an oil agent, a cutting fluid, a coolant, and a waste oil or cutting fluid. Coolant treatment is also quite difficult, and it is easy to pollute the environment.
  • An oil and gas mixing and dispersing structure including:
  • An oil input portion is located at one end of the pipe body, the oil input portion is provided with an inlet end and an outlet end, and the outlet end is formed into a tapered pipe;
  • a gas input portion the gas input portion is connected to a vacuum suction portion at the bottom of the outlet end of the oil input portion, the gas input portion is provided with an inlet end and an outlet end, and the gas input portion is provided with a check structure to prevent backflow; a gas-liquid mixture output unit, wherein the gas-liquid mixture output unit is disposed at an end of the pipe body different from the oil input portion, and the gas and liquid mixture output unit communicates with the vacuum suction unit, and the gas and liquid mixture output unit is provided with an inlet. At the end and the outlet end, the inlet end is formed as a tapered tube;
  • the scatter structure includes a partition with a plurality of perforations, a central nozzle of a conical nozzle is provided with a reverse tapered column, and a blade is pivoted on the reverse tapered column.
  • the fan blades When the fan blades are turned, the fan blades are rotated, and the fan blades rotate to agitate the oil and gas, and can break the bubbles generated by the oil and gas mixture.
  • the apertures at the inlet and outlet ends of each of the input and output portions are set to be different to generate a pressure difference between the gas input portion and the gas-liquid mixture output portion to form a vacuum suction gas, such that the oil It is fully mixed with the gas, and is output by the gas and liquid mixing output.
  • the bubbles generated by the mixing of gas and liquid are stirred and broken by the structure of the discharge part of the outlet to achieve the best mixing effect and the ozone of the gas.
  • the oil is sterilized and deodorized.
  • the present invention can fully mix the oil agent with the gas (ozone) by means of oil and gas mixing and dispersing structure, ozone It is possible to sterilize and deodorize the oil agent, so that the oil agent is not easily deteriorated, and no bad odor is generated, and the service life of the oil agent is prolonged. '
  • the invention further has a non-return structure at the gas input portion, so that the odor gas does not have a backflow during the inhalation process, so that the oil and gas mixing is smoother.
  • the invention further has a dispersing structure at the outlet of the gas-liquid mixture, and by means of the structure of the dispersing part, the oil and gas mixing is more uniform, and the bubbles generated during the mixing process can be broken, so that the mixing and dissolution rate is better. .
  • FIG. 1 is a perspective exploded view of an embodiment of the present invention.
  • Figure 2 is a cross-sectional view showing an embodiment of the present invention.
  • Fig. 3 is a schematic view showing the state of implementation of an embodiment of the present invention. detailed description
  • the oil-gas mixing and dispersing structure including:
  • An oil input portion 10 the oil input portion 10 is located at one end of the pipe body, and the oil input portion 10 is provided with an inlet end 1 1 and an outlet end 1 2, and the outlet end 1 2 is formed into a constricted cone Tube
  • the gas input unit 20 is connected to the vacuum suction unit 13 at the bottom of the outlet end 1 of the oil input unit 10, and the gas input unit 20 is provided with an inlet end 2 1 and an outlet end 2 2 .
  • the gas inlet portion 20 has an inlet end 21 and is provided with a non-return structure 23 to prevent backflow of the intake air;
  • the gas/liquid mixture output unit 30 is provided at the end of the pipe body different from the oil input unit 10, and the gas and liquid mixture output unit 30 is in communication with the vacuum suction unit 13
  • the gas and liquid mixing output portion 30 is provided with an inlet end 3 1 and an outlet end 3 2 , and the inlet end 31 is a slow-expanding conical tube;
  • a splitting structure 40 the splitting structure 40 includes a partition 4 1 provided with a plurality of perforations 4 1 1 , -
  • the central hole of the conical nozzle 42 is provided with a reverse tapered column, and the reverse tapered column is provided with an adjustment structure, and the tapered block 4 3 1 on the reverse tapered column is adjusted to be away from or close to the conical nozzle 4 2 and can be changed.
  • a blade 44 is pivoted on the counter-conical column.
  • the oil and gas through the dispersing structure 40 partition 4 1 perforation 4 1 1 , sprayed by the conical nozzle 4 2 to the reverse tapered column, and the tapered cone 4 3 1 will be adjusted with the reverse tapered column
  • the oil and gas diffusion causes the oil and gas to be sprayed toward the fan blade 4 4 .
  • the fan blade 4 4 can be rotated, and the fan blade 4 4 rotates to stir the oil and gas, and can break the air bubble generated by the oil and gas mixture. , so that the oil and gas dissolution rate is greatly improved.
  • the invention utilizes the pipe diameter difference to generate vacuum suction, and the automatic suction gas is fully mixed with the oil liquid, the mixing effect is better, and the anti-reverse structure is installed through the gas input portion, thereby effectively preventing the gas or oil from flowing backward, so that The gas is fully applied to the mixed oil.
  • the invention adopts the structure of the dispersing part, after the oil and gas is mixed, the mixture is fully stirred, and the bubbles generated by the mixing are broken, so that the gas dissolution rate can be greatly improved to increase the effect of ozone deodorization and sterilization.

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Aviation & Aerospace Engineering (AREA)

Abstract

An oil-gas mixing and dispersing structure includes at least an oil input part, a gas input part, a gas-oil mixing and outputting part and a dispersing part. The gas input part is provided with a non-return structure. The holes of the entry end and the exit end of respective input part and outputting part have different diameters to cause pressure difference. The pressure difference occurs between the gas input part and the gas-liquid mixing and outputting part to establish a vacuum suction force to draw in the gas. So the oil and gas can be sufficiently mixed. The bubbles produced by the mixture of the gas and the liquid and outputted by the gas-liquid mixing and outputting part will be stirred and broke by the dispersing part to reach an optimal mixing effect, and at the same time the ozone in the gas will sterilize and deodorize the oil liquid.

Description

油气混合及打散结构 技术领域  Oil and gas mixing and dispersing structure
本发明提供一种加工机械部件结构， 尤指一种藉入出口端管径差产生真空吸 力， 得以吸入气体充分混合， 并有气泡时以打散结构打破的油气混合及打散结构。 背景技术  The invention provides a structure of a processing mechanical component, in particular to a hydrocarbon mixing and breaking structure which is formed by borrowing the diameter difference between the outlet end pipe and the vacuum suction, so that the inhaled gas is fully mixed, and the bubble is broken when the bubble is broken. Background technique
现今的加工机械都会使用到一些油剂、切削液、冷却剂等，作为冷却加过过程 的废热， 但此一些油剂、切削液、冷却剂等， 一再的重复使用， 内部难免会混入一 些杂质， 进而使油剂、切削液或冷却剂开始变质， 产生细菌或进而产生恶臭， 如此 不仅影响环境卫生， 且需另外添购油剂、切削液、冷却剂使用， 而废弃的油剂、切 削液、 冷却剂处理也相当不易， 乱倒也容易污染环境。  Today's processing machinery uses some oil, cutting fluid, coolant, etc., as the waste heat of the cooling process, but some oil, cutting fluid, coolant, etc., are repeatedly used repeatedly, and some impurities will inevitably be mixed inside. Further, the oil agent, the cutting fluid or the coolant starts to deteriorate, and bacteria or odor is generated, which not only affects environmental sanitation, but also requires the addition of an oil agent, a cutting fluid, a coolant, and a waste oil or cutting fluid. Coolant treatment is also quite difficult, and it is easy to pollute the environment.
因此，针对上述习知结构所存在的问题点，如何开发一种更具理想实用性的创 新结构， 实消费者所殷切企盼， 亦系相关业者须努力研发突破的目标及方向。  Therefore, in view of the problems existing in the above-mentioned conventional structure, how to develop an innovative structure that is more ideal and practical, the consumers are eagerly awaiting, and the relevant industry must strive to develop breakthrough goals and directions.
有鉴于此，创作人本于多年从事相关产品的制造开发与设计经验，针对上述的 目标， 详加设计与审慎评估后， 终得一确具实用性的本发明。 发明内容  In view of this, the creator has been engaged in the manufacturing development and design experience of related products for many years. After detailed design and careful evaluation of the above objectives, the present invention has finally become practical. Summary of the invention
欲解决的技术问题点： 习知的油剂、切削液、冷却剂等，均大量使用于加工机 械， 尤其加工机械加工的废热， 都是以该等油剂降温， 以求加工过程的顺利， 但是 油剂的不断使用过程中， 容易混入杂质， 进而使油剂变质、产生细菌或发臭， 容易 影响环境， 产生环境污染或成本的损失。  Technical problems to be solved: Conventional oils, cutting fluids, coolants, etc., are widely used in processing machinery, especially waste heat of processing machinery, which are cooled by these oils in order to smooth the processing process. However, in the continuous use of the oil agent, impurities are easily mixed, and the oil agent is deteriorated, bacteria or odor is generated, and the environment is easily affected, resulting in environmental pollution or loss of cost.
解决问题的技术特点： 一种油气混合及打散结构， 包含有：  Technical features to solve the problem: An oil and gas mixing and dispersing structure, including:
一油液输入部，该油液输入部位于管体的一端，油液输入部设有入口端及出口 端， 出口端并制成锥形管；  An oil input portion, the oil input portion is located at one end of the pipe body, the oil input portion is provided with an inlet end and an outlet end, and the outlet end is formed into a tapered pipe;
一气体输入部，该气体输入部连通至油液输入部出口端底部的真空吸入部，气 体输入部设有入口端与出口端， 气体输入部入口端并设有止逆结构， 以防止逆流； 一气、液混合输出部，该气、液混合输出部设于管体的异于油液输入部端，气、 液混合输出部并与真空吸入部连通， 气、液混合输出部并设有入口端及出口端， 入 口端设成锥形管； 及，  a gas input portion, the gas input portion is connected to a vacuum suction portion at the bottom of the outlet end of the oil input portion, the gas input portion is provided with an inlet end and an outlet end, and the gas input portion is provided with a check structure to prevent backflow; a gas-liquid mixture output unit, wherein the gas-liquid mixture output unit is disposed at an end of the pipe body different from the oil input portion, and the gas and liquid mixture output unit communicates with the vacuum suction unit, and the gas and liquid mixture output unit is provided with an inlet. At the end and the outlet end, the inlet end is formed as a tapered tube;
、 一打散部结构，该打散部结构包括一隔板设有数穿孔，一锥形喷嘴的中央孔组 设逆锥形柱， 逆锥形柱上并枢设一扇叶， 当油气混合喷向扇叶时， 得以推动扇叶旋 转， 扇叶旋转除搅拌油气外， 并可击破油气混合所产生的气泡。 本发明于各输入部及输出部的入口与出口二端的孔径设成不同， 以产生压力 差， 该压力差于气体输入部及气液混合输出部间， 形成一真空吸力吸入气体， 如此 油液与气体得以充分混合，而由气、液混合输出部输出，气、液混合所产生的气泡， 则由出口的打散部结构搅拌并击破，达到混合功效最佳状态，并使气体的臭氧对油 液进行杀菌与除臭功效。 a scatter structure, the scatter structure includes a partition with a plurality of perforations, a central nozzle of a conical nozzle is provided with a reverse tapered column, and a blade is pivoted on the reverse tapered column. When the fan blades are turned, the fan blades are rotated, and the fan blades rotate to agitate the oil and gas, and can break the bubbles generated by the oil and gas mixture. In the present invention, the apertures at the inlet and outlet ends of each of the input and output portions are set to be different to generate a pressure difference between the gas input portion and the gas-liquid mixture output portion to form a vacuum suction gas, such that the oil It is fully mixed with the gas, and is output by the gas and liquid mixing output. The bubbles generated by the mixing of gas and liquid are stirred and broken by the structure of the discharge part of the outlet to achieve the best mixing effect and the ozone of the gas. The oil is sterilized and deodorized.
对照先前技术的功效：  Compare the efficacy of the prior art:
一、先前技术在油剂使用一段时间后，就容易因混入杂质而变质，产生细菌或 恶臭情形， 而本发明藉油气混合及打散结构， 可将油剂与气体（臭氧）充分混合， 臭氧得以对油剂杀菌与除臭， 如此油剂就不容易变质， 也不会有恶臭情形产生， 延 长油剂的使用寿命。 '  1. Prior to the use of the oil agent for a period of time, it is easy to deteriorate due to the incorporation of impurities, resulting in bacteria or malodorous conditions. However, the present invention can fully mix the oil agent with the gas (ozone) by means of oil and gas mixing and dispersing structure, ozone It is possible to sterilize and deodorize the oil agent, so that the oil agent is not easily deteriorated, and no bad odor is generated, and the service life of the oil agent is prolonged. '
二、本发明更在气体输入部设有止逆结构，如此得以让臭气在吸入过程中，不 会有逆流情形发生， 使得油气混合更顺畅。  2. The invention further has a non-return structure at the gas input portion, so that the odor gas does not have a backflow during the inhalation process, so that the oil and gas mixing is smoother.
三、本发明更在气液混合的出口设有打散部结构，藉打散部结构，得以使油气 混合更均匀， 并使得混合过程中产生的气泡可以被打破， 让混合溶解率更佳者。  3. The invention further has a dispersing structure at the outlet of the gas-liquid mixture, and by means of the structure of the dispersing part, the oil and gas mixing is more uniform, and the bubbles generated during the mixing process can be broken, so that the mixing and dissolution rate is better. .
有关本发明所采用的技术、手段及其功效，兹举一较佳实施例并配合图式详细 说明于后，相信本发明上述的目的、构造及特征，当可由之得一深入而具体的了解。 附图说明 '  The above-mentioned objects, structures and features of the present invention will be described in detail with reference to the preferred embodiments of the present invention. . BRIEF DESCRIPTION OF THE DRAWINGS
图 1 : 是本发明其一实施例立体分解示意图。  FIG. 1 is a perspective exploded view of an embodiment of the present invention.
图 2: 是本发明其一实施例剖示图。  Figure 2 is a cross-sectional view showing an embodiment of the present invention.
图 3: 是本发明其一实施例实施状态示意图。 具体实施方式  Fig. 3 is a schematic view showing the state of implementation of an embodiment of the present invention. detailed description
参阅图 1、 图 2所示， 本发明其一较佳实施例立体分解示意图及剖示图， 其油 气混合及打散结构， 包括：  Referring to FIG. 1 and FIG. 2, a perspective exploded view and a cross-sectional view of a preferred embodiment of the present invention, the oil-gas mixing and dispersing structure, including:
一油液输入部 1 0，该油液输入部 1 0位于管体的一端，油液输入部 1 0设有 入口端 1 1及出口端 1 2， 出口端 1 2并制成急缩锥形管；  An oil input portion 10, the oil input portion 10 is located at one end of the pipe body, and the oil input portion 10 is provided with an inlet end 1 1 and an outlet end 1 2, and the outlet end 1 2 is formed into a constricted cone Tube
一气体输入部 2 0，该气体输入部 2 0连通至油液输入部 1 0出口端 1 2底部 的真空吸入部 1 3， 气体输入部 2 0设有入口端 2 1与出口端 2 2， 气体输入部 20入口端 2 1并设有止逆结构 2 3， 以防止进气逆流；  a gas input unit 20, the gas input unit 20 is connected to the vacuum suction unit 13 at the bottom of the outlet end 1 of the oil input unit 10, and the gas input unit 20 is provided with an inlet end 2 1 and an outlet end 2 2 . The gas inlet portion 20 has an inlet end 21 and is provided with a non-return structure 23 to prevent backflow of the intake air;
一气、液混合输出部 3 0， 该气、液混合输出部 3 0设于管体的异于油液输入 部 1 0端， 气、 液混合输出部 3 0并与真空吸入部 1 3连通， 气、 液混合输出部 30并设有入口端 3 1及出口端 3 2， 入口端 3 1为缓扩锥形管；  The gas/liquid mixture output unit 30 is provided at the end of the pipe body different from the oil input unit 10, and the gas and liquid mixture output unit 30 is in communication with the vacuum suction unit 13 The gas and liquid mixing output portion 30 is provided with an inlet end 3 1 and an outlet end 3 2 , and the inlet end 31 is a slow-expanding conical tube;
一打散部结构 4 0，该打散部结构 4 0包括一隔板 4 1设有数穿孔 4 1 1 , - 锥形喷嘴 4 2的中央孔组设逆锥形柱，逆锥形柱设有调整构造，得以调整逆锥形柱 上的锥形块体 4 3 1远离或靠近锥形喷嘴 4 2 ,得以改变喷液方向，逆锥形柱上并 枢设一扇叶 4 4， 当油气混合喷向扇叶 4 4时， 得以推动扇叶 4 4旋转，扇叶 4 4 旋转除搅拌油气外， 并可击破油气混合所产生的气泡， 使油气溶解率大幅提升。 A splitting structure 40 , the splitting structure 40 includes a partition 4 1 provided with a plurality of perforations 4 1 1 , - The central hole of the conical nozzle 42 is provided with a reverse tapered column, and the reverse tapered column is provided with an adjustment structure, and the tapered block 4 3 1 on the reverse tapered column is adjusted to be away from or close to the conical nozzle 4 2 and can be changed. In the direction of the liquid spray, a blade 44 is pivoted on the counter-conical column. When the oil and gas mixture is sprayed toward the fan blade 4 4, the fan blade 4 4 can be rotated, and the fan blade 4 4 rotates in addition to stirring the oil and gas, and can be broken. The bubbles generated by the mixing of oil and gas greatly increase the solubility rate of oil and gas.
参阅图 3所示，该油液输入部 1_ 0接至油液的入口管路，而气体输入部 2 0则 通过管路接至一臭氧 03产生器，当油液由油液输入部 1 0入口端 1 1进入，流经出 口端 1 2急缩锥形管时， 油液乃被迫加速冲出， 并经气、液混合输出部 3 0入口端Refer to FIG. 3, the oil input section 1 0 _ conduit connected to the fluid inlet, and the gas supply unit 20 through a conduit connected to the ozone generator 03, when the oil from the oil input section 1 0 inlet end 1 1 enters, when flowing through the outlet end 1 2 shrinking conical tube, the oil is forced to accelerate out, and through the gas, liquid mixed output part 3 0 inlet end
3 1缓扩锥形管时， 乃因为管径差， 而于真空吸入部 1 3产生真空吸力， 该真空吸 力乃得以将气体输入部 2 0入口端 2 1的止逆结构 2 3开启，并吸入大量的气体进 入真空吸入部 1 3与油液充分混合，再由气、液混合输出部 3 0输出至打散部结构3 1 when the tapered tube is slowly expanded, the vacuum suction force is generated in the vacuum suction portion 13 due to the difference in the diameter of the tube, and the vacuum suction force opens the non-return structure 2 3 of the inlet end 2 1 of the gas input portion 20, and A large amount of gas is sucked into the vacuum suction portion 13 and sufficiently mixed with the oil, and then output from the gas and liquid mixed output portion 30 to the dispersing portion structure.
4 0，油气经打散部结构 4 0隔板 4 1穿孔 4 1 1后， 由锥形喷嘴 4 2喷向逆锥形 柱， 并以逆锥形柱的调整锥形块体 4 3 1将油气扩散，使油气喷向扇叶 4 4， 当油 气混合喷向扇叶 4 4时， 得以推动扇叶 4 4旋转， 扇叶 4 4旋转除搅拌油气外， 并 可击破油气混合所产生的气泡， 使油气溶解率大幅提升。 40, the oil and gas through the dispersing structure 40 partition 4 1 perforation 4 1 1 , sprayed by the conical nozzle 4 2 to the reverse tapered column, and the tapered cone 4 3 1 will be adjusted with the reverse tapered column The oil and gas diffusion causes the oil and gas to be sprayed toward the fan blade 4 4 . When the oil and gas is mixed and sprayed to the fan blade 4 4 , the fan blade 4 4 can be rotated, and the fan blade 4 4 rotates to stir the oil and gas, and can break the air bubble generated by the oil and gas mixture. , so that the oil and gas dissolution rate is greatly improved.
本发明功效增进的处如下：  The improvement of the efficacy of the present invention is as follows:
1、本发明利用管径差产生真空吸力，得以自动吸入气体与油液充分混合，其 混合效果较佳，且通过气体输入部装设有止逆结构，得以有效防止气体或油液逆流， 使气体充分应用到混合油液内者。  1. The invention utilizes the pipe diameter difference to generate vacuum suction, and the automatic suction gas is fully mixed with the oil liquid, the mixing effect is better, and the anti-reverse structure is installed through the gas input portion, thereby effectively preventing the gas or oil from flowing backward, so that The gas is fully applied to the mixed oil.
2、本发明并通过打散部结构， 在油气混合后， 将之充分搅拌， 并将混合所产 生的气泡击破， 使气体溶解率可大幅提升， 以增加臭氧除臭与杀菌的功效者。  2. The invention adopts the structure of the dispersing part, after the oil and gas is mixed, the mixture is fully stirred, and the bubbles generated by the mixing are broken, so that the gas dissolution rate can be greatly improved to increase the effect of ozone deodorization and sterilization.
前文针对本发明的较佳实施例为本发明的技术特征进行具体的说明；惟，熟悉 此项技术的人士当可在不脱离本发明的精神与原则下对本发明进行变更与修改，而 该等变更与修改， 皆应涵盖于本申请专利范围所界定的范畴中。  The present invention has been described in detail with reference to the preferred embodiments of the present invention. However, those skilled in the art can change and modify the present invention without departing from the spirit and scope of the invention. Changes and modifications are to be included in the scope defined by the scope of the patent application.

Claims

权 利 要 求 书 Claim
1 . 一种油气混合及打散结构， 包含有： 1. An oil and gas mixing and dispersing structure, comprising:
一油液输入部，该油液输入部位于管体的一端，油液输入部设有入口端及出口 端， 出口端并制成锥形管；  An oil input portion, the oil input portion is located at one end of the pipe body, the oil input portion is provided with an inlet end and an outlet end, and the outlet end is formed into a tapered pipe;
一气体输入部，该气体输入部连通至油液输入部出口端底部的真空吸入部，气 体输入部设有入口端与出口端， 气体输入部入口端并设有止逆结构， 以防止逆流； —气、液混合输出部，该气、液混合输出部设于管体的异于油液输入部端，气、 液混合输出部并与真空吸入部连通， 气、液混合输出部并设有入口端及出口端， 入 口端设成锥形管； 及，  a gas input portion, the gas input portion is connected to a vacuum suction portion at the bottom of the outlet end of the oil input portion, the gas input portion is provided with an inlet end and an outlet end, and the gas input portion is provided with a check structure to prevent backflow; a gas/liquid mixed output unit provided in the oil body input portion end of the pipe body, and the gas and liquid mixed output unit is connected to the vacuum suction unit, and the gas and liquid mixed output unit is provided At the inlet end and the outlet end, the inlet end is formed as a conical tube;
一打散部结构，该打散部结构包括一隔板设有数穿孔，一锥形喷嘴的中央孔组 设逆锥形柱， 逆锥形柱上并枢设一扇叶， 当油气混合喷向扇叶时， 得以推动扇叶旋 转， 扇叶旋转除搅拌油气外， 并可击破油气混合所产生的气泡。 ，.  a scatter structure, the scatter structure comprises a partition with a plurality of perforations, a central nozzle of a conical nozzle is provided with a reverse tapered column, and a blade is pivoted on the reverse tapered column, when the oil and gas are mixed When the fan blades are used, the fan blades are rotated, and the fan blades rotate to agitate the oil and gas, and can break the bubbles generated by the oil and gas mixture. ,
2 . 如权利要求 1所述的油气混合及打散结构， 其特征在于， 该打散部结构的 逆锥形柱设有调整构造，该调整构造可调整逆锥形柱上的锥形块体远离或靠近锥形 喷嘴。 '  2 . The oil-gas mixing and dispersing structure according to claim 1 , wherein the reverse tapered column of the dispersing portion structure is provided with an adjusting structure, and the adjusting structure can adjust the tapered block on the reverse tapered column Keep away from or near the cone nozzle. '
PCT/CN2007/001027 2007-03-29 2007-03-29 An oil-gas mixing and dispersing structure WO2008119199A1 (en)

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JP2020018996A (en) * 2018-08-02 2020-02-06 上海久田汽車零部件制造有限公司 Microbubble generator

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JP2020018996A (en) * 2018-08-02 2020-02-06 上海久田汽車零部件制造有限公司 Microbubble generator

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