WO2008119199A1 - Structure de mélange et de dispersion huile-gaz - Google Patents

Structure de mélange et de dispersion huile-gaz Download PDF

Info

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
Authority
WO
WIPO (PCT)
Prior art keywords
gas
oil
input portion
mixing
dispersing
Prior art date
Application number
PCT/CN2007/001027
Other languages
English (en)
Chinese (zh)
Inventor
Chung Min Yang
Chao Psung Huang
Original Assignee
Chung Min Yang
Chao Psung Huang
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
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/fr
Publication of WO2008119199A1 publication Critical patent/WO2008119199A1/fr

Links

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.

Landscapes

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

Abstract

L'invention concerne une structure de mélange et de dispersion huile-gaz comprenant au moins une admission pour l'huile, une admission pour le gaz, une partie de mélange et d'évacuation gaz-huile et une partie de dispersion. L'admission pour le gaz est pourvue d'une structure de non retour. Le trou de l'entrée et de la sortie de l'admission et de l'évacuation ont différents diamètres de façon à générer une différence de pression. La différence de pression se produit entre l'admission pour le gaz et la partie de mélange et d'évacuation gaz-liquide afin d'établir une force d'aspiration sous vide pour entraîner le gaz. Ceci permet de mélanger suffisamment l'huile et le gaz. Les bulles générées par le mélange du gaz et du liquide et émises par la partie de mélange et d'évacuation de gaz-liquide seront agitées et brisées par la partie de dispersion de façon à atteindre un effet de mélange optimal, et en même temps, l'ozone du gaz stérilisera et désodorisera l'huile.
PCT/CN2007/001027 2007-03-29 2007-03-29 Structure de mélange et de dispersion huile-gaz WO2008119199A1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PCT/CN2007/001027 WO2008119199A1 (fr) 2007-03-29 2007-03-29 Structure de mélange et de dispersion huile-gaz

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/CN2007/001027 WO2008119199A1 (fr) 2007-03-29 2007-03-29 Structure de mélange et de dispersion huile-gaz

Publications (1)

Publication Number Publication Date
WO2008119199A1 true WO2008119199A1 (fr) 2008-10-09

Family

ID=39807774

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2007/001027 WO2008119199A1 (fr) 2007-03-29 2007-03-29 Structure de mélange et de dispersion huile-gaz

Country Status (1)

Country Link
WO (1) WO2008119199A1 (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20180326374A1 (en) * 2014-11-19 2018-11-15 Ohno Development Co., Ltd. Microbubble generating device
JP2020018996A (ja) * 2018-08-02 2020-02-06 上海久田汽車零部件制造有限公司 マイクロバブル発生器

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995012452A2 (fr) * 1993-11-01 1995-05-11 Erik Hoel Procede et appareil d'injection de gaz
CN2515192Y (zh) * 2001-11-02 2002-10-09 上海实宝来机械制造有限公司 洗浴用水混合装置
TWM284447U (en) * 2005-08-25 2006-01-01 Huang Chau Tsung Gas-liquid mixing device
CN2810731Y (zh) * 2005-06-07 2006-08-30 吴镇霖 臭氧水机混合器
CN2841136Y (zh) * 2005-11-10 2006-11-29 浙江欧赛环境设备有限公司 一种气水射混器
TWM317431U (en) * 2007-03-23 2007-08-21 Tsung-Min Yang Oil-water clarification, sterilization and deodorization device

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1995012452A2 (fr) * 1993-11-01 1995-05-11 Erik Hoel Procede et appareil d'injection de gaz
CN2515192Y (zh) * 2001-11-02 2002-10-09 上海实宝来机械制造有限公司 洗浴用水混合装置
CN2810731Y (zh) * 2005-06-07 2006-08-30 吴镇霖 臭氧水机混合器
TWM284447U (en) * 2005-08-25 2006-01-01 Huang Chau Tsung Gas-liquid mixing device
CN2841136Y (zh) * 2005-11-10 2006-11-29 浙江欧赛环境设备有限公司 一种气水射混器
TWM317431U (en) * 2007-03-23 2007-08-21 Tsung-Min Yang Oil-water clarification, sterilization and deodorization device

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20180326374A1 (en) * 2014-11-19 2018-11-15 Ohno Development Co., Ltd. Microbubble generating device
US10646835B2 (en) * 2014-11-19 2020-05-12 Ohno Development Co., Ltd. Microbubble generating device
JP2020018996A (ja) * 2018-08-02 2020-02-06 上海久田汽車零部件制造有限公司 マイクロバブル発生器

Similar Documents

Publication Publication Date Title
JP2006289183A (ja) ナノバブル生成方法とその装置
JP2009136864A (ja) マイクロバブル発生装置
KR101869487B1 (ko) 세정 및 살균 기능을 갖는 욕조 또는 싱크대용 나노버블 발생장치
WO2001000308A1 (fr) Procede et dispositif de melange et de distribution pour fluides
KR20170104351A (ko) 미세기포 발생장치
JP2002143658A (ja) 気泡水製造装置
RU2304475C2 (ru) Устройство для образования пены
JP2009112964A (ja) 微細気泡発生装置
JP2007117314A (ja) キッチン用流し台
JP2002126485A (ja) オゾン発生装置、ならびにその付属装置である同軸型ガス−流体混合管、空冷式オゾン生成管、および液体加圧式ガス−液体混合装置
WO2008119199A1 (fr) Structure de mélange et de dispersion huile-gaz
JP2004330050A (ja) オゾン水供給装置と流体混合装置
JP2001300276A (ja) 気泡生成装置
JP5276254B2 (ja) 水洗便器装置
JP2010264337A (ja) 曝気攪拌機
JP2011115745A (ja) 気泡発生管
JPH04235761A (ja) 吸引型の泡発生ノズル
JP2002153741A (ja) 流体混合具及びそれを用いた流体混合ポンプ
CN207463019U (zh) 一种高效气液混合器
JP2018038944A (ja) オゾン水シャワー装置
JP4174576B2 (ja) ２つ以上の液体または液体と気体から構成される流体を混合し、溶液にする混合装置
JP3747261B2 (ja) 気液混合流体の分散方法及び該方法に使用する分散装置
JP5291312B2 (ja) 酸洗装置及び方法
JP2012091153A (ja) 微細気泡発生装置
JP2010029774A (ja) 微細気泡発生装置

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 07720601

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 07720601

Country of ref document: EP

Kind code of ref document: A1