WO2007117024A1 - ガス処理方法 - Google Patents
ガス処理方法 Download PDFInfo
- Publication number
- WO2007117024A1 WO2007117024A1 PCT/JP2007/057995 JP2007057995W WO2007117024A1 WO 2007117024 A1 WO2007117024 A1 WO 2007117024A1 JP 2007057995 W JP2007057995 W JP 2007057995W WO 2007117024 A1 WO2007117024 A1 WO 2007117024A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- gas
- fluid
- milk
- raw material
- liquid
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J13/00—Colloid chemistry, e.g. the production of colloidal materials or their solutions, not otherwise provided for; Making microcapsules or microballoons
- B01J13/02—Making microcapsules or microballoons
- B01J13/04—Making microcapsules or microballoons by physical processes, e.g. drying, spraying
-
- A—HUMAN NECESSITIES
- A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
- A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
- A61K9/00—Medicinal preparations characterised by special physical form
- A61K9/10—Dispersions; Emulsions
- A61K9/127—Liposomes
- A61K9/1277—Processes for preparing; Proliposomes
Definitions
- the present invention relates to a gas treatment method for fluids represented by blood, beverages, liquid foods, medicines and the like.
- fluid foods such as beverages and liquid foods are subjected to a replacement treatment of gas dissolved in the foods for the purpose of preventing the deterioration of the flavor.
- oxygen may be added to improve the flavor.
- Patent Documents 1 and 2 when milk is produced, the amount of dissolved oxygen in the liquid is reduced by replacing raw milk with an inert gas such as nitrogen gas prior to heat sterilization. Further, a method for suppressing the generation of sulfides (sulfur compounds) during heat sterilization is disclosed.
- Patent Document 3 discloses a method for suppressing the growth of harmful microorganisms by reducing the concentration of dissolved oxygen in raw milk by aeration and stirring of nitrogen gas while raw milk is stored in a silo. Is disclosed.
- homogenization is performed for the purpose of preventing fat from separating by squeezing fat globules contained in raw milk as a raw material.
- the homogenization treatment is usually performed by crushing milk fat by applying pressure to the raw material milk.
- various products include a process of sterilizing in the manufacturing process.
- Patent Document 2 in the method for producing a milk beverage, a heat sterilization treatment is further performed after replacement with nitrogen gas.
- heat and sterilization treatment is performed on blood, medicine, etc. (for example, Patent Document 4). None of these conventional heat sterilization treatment methods are based on gas.
- Patent Document 1 Japanese Patent No. 3083798
- Patent Document 2 Japanese Patent No. 3091752
- Patent Document 3 Japanese Patent Laid-Open No. 5-49395
- Patent Document 4 JP-A-6-319463
- a problem to be solved by the present invention is to provide a new and efficient gas processing method.
- an object of the present invention is to provide a method for producing milk that can perform the above-described plurality of treatments collectively.
- the present inventors are able to homogenize raw milk by spraying raw milk with a two-fluid nozzle.
- this dispersion state is very reactive, it has been found that nitrogen replacement of dissolved oxygen in raw milk and sterilization can be performed very efficiently, and the present invention has been completed. . That is, the present invention relates to the following (1) to (10).
- the fluid is characterized in that the fluid is ejected from a liquid ejection port, the ejection flow is crushed by an air current to form fine droplets, and then the fluid droplets are aggregated. Gas processing method.
- the air stream includes superheated steam, and sterilizes the fluid.
- the fluid is blood, beverage, liquid food, or medicine, (1)
- the fluid is raw material milk, and the airflow includes nitrogen gas.
- the fluid is raw material milk, and the airflow contains superheated steam (1
- raw milk is a liquid containing raw milk and components derived from raw milk (particularly fat), and milk is a raw material made from the raw milk.
- Milk produced through various processes homogenization treatment, dissolved oxygen replacement treatment, sterilization treatment, etc.
- the gas treatment method of the present invention while discharging a fluid represented by blood, beverage, liquid food, medicine, and raw milk from the liquid discharge port, the discharge flow is crushed by an air flow, Fine After the droplets are made into fine droplets, the droplets are agglomerated, whereby the fluid can be efficiently subjected to gas addition, gas replacement, deaeration, or sterilization (sterilization).
- FIG. 1 is an apparatus configuration diagram showing an example of a processing apparatus used for a fluid homogenization process in a manufacturing method according to the present invention.
- FIG. 2 is (a) a plan view showing an example of a two-fluid nozzle, and (b) a cross-sectional view showing an example of a two-fluid nozzle.
- FIG. 3 is a front view showing a form example of a two-fluid nozzle.
- FIG. 4 is a block diagram illustrating a configuration example of a control device.
- FIG. 5 is a diagram showing the measurement results of the examples.
- FIG. 6 is a diagram showing the measurement results of the examples.
- FIG. 1 is a block diagram showing an example of a processing apparatus for use in a fluid gas processing method according to the present invention.
- the manufacturing apparatus 100 includes a raw material supply system 110, a two-fluid nozzle 160, and a flow blocker (baffle board) 190.
- the raw material supply system 110 includes a raw material tank 111.
- the raw material tank 111 is a pressure-resistant container that can be sealed, and is sealed after injecting a fluid 112 such as raw milk.
- a stirrer 113 having a rotating blade for stirring the fluid 112 is provided.
- a raw material feed pipe 121 is connected to the raw material tank 111 through its side wall.
- the inlet 12 li of the raw material feed pipe 121 is disposed near the inner bottom surface of the raw material tank 111.
- a strainer 122 is attached to the inlet 121 i of the raw material feed pipe 1 21.
- the outlet 121 ⁇ of the raw material feed pipe 121 is connected to the liquid supply port 151 of the two-fluid nozzle 160.
- An electromagnetic variable throttle valve 123 for adjusting the flow rate is interposed in the middle portion of the raw material feed pipe 121.
- a pressure pipe 131 is connected to the raw material tank 111 so as to penetrate the ceiling wall.
- the outlet 131 ⁇ of the pressure pipe 131 is disposed near the ceiling surface of the raw material tank 111.
- the pressure pipe 131 is a pipe for introducing a compressed gas into the upper space inside the raw material tank 111 (the space existing above the fluid 112).
- the most upstream end of the pressure pipe 131 is connected to the compressed gas discharge port of the compressor 133 via the branch pipe 132.
- an electromagnetic valve 134 is provided, and an atmospheric pressure sensor 135 for detecting the atmospheric pressure in the upper space of the raw material tank 111 is provided.
- a gas supply pipe 136 is connected to the gas supply port 152 of the two-fluid nozzle 160.
- the uppermost stream end of the gas supply pipe 136 is connected to the exhaust port of the compressor 133 via the branch pipe 132. That is, the branch pipe 132 has two outlets, the pressure pipe 131 is connected to one outlet of the branch pipe 132, and the gas supply pipe 136 is connected to the other outlet.
- an electromagnetic valve 137, a pressure sensor 138, a compressed gas reservoir 139, and a pressure control valve 140 are provided in order from the upstream side to the downstream side. spirit
- the pressure sensor 138 is a sensor for detecting the atmospheric pressure in the compressed gas reservoir 139.
- the compressor 133 is for generating compressed gas.
- the compressed gas discharged from the compressor 133 is distributed to the pressure pipe 131 and the gas supply pipe 136 through the branch pipe 132.
- the gas supply pipe 136 is a pipe for introducing a compressed gas into the two-fluid nozzle 160.
- the compressed gas supplied to the gas supply pipe 136 is stored in the compressed gas reservoir 139, adjusted to a predetermined pressure, and introduced into the two-fluid nozzle 160.
- a liquid discharge port 161 that communicates with the liquid supply port 151 and a gas ejection port 162 that communicates with the gas supply port 152 are provided at the tip of the two-fluid nozzle 160.
- the gas injection port 162 is formed around the liquid discharge port 161.
- a stainless steel flow blocking body 190 is provided near the lower part of the two-fluid nozzle 160.
- the flow blocker 190 is a conical member having a diameter reduced upward, and the tip (upper end) thereof faces the liquid discharge port 161 of the two-fluid nozzle 160.
- the two-fluid nozzle 160 and the flow blocker 190 are housed together in a straight cylinder (not shown), and are connected to and held by the inner wall of the straight cylinder.
- the fluid 112 supplied to the liquid supply port 151 of the two-fluid nozzle 160 is discharged from the liquid discharge port 161, but in front of the two-fluid nozzle 160 (downward in the figure), a gas jet port 162.
- a high-speed vortex of air ejected from the air is formed, and the discharged fluid 112 is crushed into fine particles (mist) by the high-speed vortex.
- the flow immediately after being crushed collides with the flow blocker 190.
- the crushed flow is re-aggregated immediately after crushing (mist-like droplets are re-agglomerated), and the processed liquid 124 in a state where the fluid is uniform is generated.
- the solution 124 re-aggregated on the flow blocking body 190 flows down along the surface of the flow blocking body 190, and the solution 124 that has flowed down from the lower end of the flow blocking body 190 accumulates in the product container 125.
- FIG. 2 (a) is a plan view of the nozzle
- FIG. 2 (b) is a sectional view of the nozzle
- FIG. 3 is a front view of the nozzle.
- the two-fluid nozzle 160 has a structure in which a substantially cylindrical core 160B is inserted and screwed into a substantially cylindrical hollow casing 160A.
- Casing 160A is made by machining a metal material such as stainless steel or brass and has a two-fluid nozzle at its tip.
- An opening hole 163 having a circular cross section whose center coincides with the central axis A of 160 is formed to form an outer contour of the gas injection port 162.
- a gas supply port 152 is formed on the side surface of the casing 160A so as to have an axis perpendicular to the central axis A of the two-fluid nozzle 160.
- a female screw groove is cut in the inner peripheral surface of the gas supply port 152 so that the gas supply pipe 136 can be screwed in and coupled.
- a female screw groove 166 is formed at the base end portion of the inner surface of the casing 160A, and a step portion 167 having a slightly larger inner diameter is formed at a portion in the base end direction thereof.
- a male thread groove 168 is formed on the outer surface of the front end portion of the casing 160A so that a fixing nut 169 for attaching the two-fluid nozzle 160 can be screwed.
- the core 160B is manufactured by machining the same or different metal material as the casing 160A described above, and the inside is hollowed out along the central axis A to be hollow.
- the outer diameter is such that it fits snugly into the hollow hole of the casing 160A, and the outer diameter near the center of the longitudinal direction is slightly narrower than the inner surface of the casing 16OA.
- an annular cylindrical space 170 is left. This space 170 communicates with a gas supply port 152 provided in the casing 160A.
- a male screw groove 171 is cut in the outer circumference slightly before the base end of the core 160B, and is screwed into the female screw groove 166 to fix the core 160B inside the casing 160A.
- a liquid supply port 151 is formed at the base end of the core 160B.
- a female thread groove is cut in the inner peripheral portion of the liquid supply port 151, and the leading end portion of the merging pipe 135 is screwed and coupled.
- a liquid discharge port 161 communicating from the liquid supply port 151 through the internal hollow space is opened at the tip of the core 160B, and the enormous conical portion around it forms a spiral forming body 176. ing.
- a vortex chamber 177 is formed between the front end surface of the spiral forming body 176 and the inner surface of the front end of the casing 160A.
- the tip end surface 178 of the core 162 constituting the vortex chamber 177 has a gap with the opening hole 163 of the casing 160A described above, and this constitutes the gas injection port 162.
- a circular liquid discharge port 16 at the center 1 is arranged, and an annular gas injection port 162 is arranged around it.
- the gas injection port 162 communicates with a plurality of swirl grooves 179 extending in a spiral shape formed on the conical surface of a spiral forming body 176 disposed inside the casing 160A.
- the compressed gas supplied from the gas supply port 152 passes through the space 170 and is compressed when passing through the swirling groove 179 having a small cross-sectional area formed in the spiral forming body 176 to become a high-speed air flow. .
- This high-speed airflow becomes a swirl-like swirl airflow inside the vortex chamber 177 and is ejected from the constricted annular gas injection port 162 to form a high-speed vortex of gas in front of the two-fluid nozzle 160.
- This vortex is formed in a tapered conical shape with the front position close to the tip of the casing 160A as a focal point.
- the unmixed raw material liquid 112 delivered from the raw material tank 111 is supplied to the liquid supply port 151 through the raw material supply pipe 121.
- the fluid 112 supplied to the liquid supply port 151 is discharged from the liquid discharge port 161 through the hollow portion of the core 160B. Then, it is crushed into fine particles by the high-speed vortex of the gas injected from the gas injection port 162, and is forcibly mixed with the rotation of the vortex and is forwarded to the front of the two-fluid nozzle 160 as a mixture of uniformly mixed particles.
- the inner diameter of the liquid discharge port 161 is slightly smaller than the inner diameter of the bore hole of the core 160B. However, if there is a possibility of clogging, the inner diameter of the liquid discharge port 161 is bored. It is desirable to have the same diameter as the inner diameter of the hole.
- Manufacturing apparatus 100 is controlled by control device 180 shown in FIG.
- the control device 180 includes an MCU 181, a ROM 182, a RAM 183, an interface unit 184, an A / D connector 185, and a drive unit 186, which are mutually connected via a bus line 187. It is connected.
- the ROM 182 stores a program executed by the MPU 181.
- the RAM 183 is used as a work area when the MPU 181 executes a program.
- a display device 188 such as a CRT is connected to the output port of the interface unit 184, and an input device 189 such as a keyboard is connected to the input port.
- the atmospheric pressure sensors 135 and 138 of the manufacturing apparatus 100 are connected to the input of the A / D converter 185, and the analog values of the air pressure detected by these sensors are converted into digital values.
- the air pressure value converted into a digital value is read by the MP U 181 via the bus line 187.
- the output of the drive unit 186 is connected to the electromagnetically driven valves 123, 134, 137 and 140 of the manufacturing apparatus 100.
- the drive unit 186 adjusts the current for electromagnetic drive in accordance with the command from the MPU 181 and switches it on / off.
- the operator When operating the manufacturing apparatus 100, the operator puts a fluid in the raw material tank 111 and tightly seals the lid of the raw material tank 111. Thereafter, the start of mixing is instructed from the input device 189. Upon receiving this command, the MPU 181 issues a command to the drive unit 186 to open the solenoid valve 1 34 and monitor the output of the atmospheric pressure sensor 135 via the AZD converter 185 so that the compressed gas from the compressor 133 is fed into the raw material tank 111. Wait until the upper space of the tank is filled and the prescribed pressure is reached. In this initial state, the other solenoid valves of the manufacturing apparatus 100 are closed.
- the MPU 181 closes the electromagnetic valve 134. Then open the solenoid valve 1 37. As a result, the compressed gas is supplied into the compressed gas reservoir 139.
- the MPU 181 determines that the conditions for starting the process are satisfied, and opens the pressure control valve 140. Then, the compressed gas is supplied from the compressed gas reservoir 139 to the gas supply port 152 of the two-fluid nozzle 160, and a high-speed vortex of gas is injected from the gas injection port 162 at the tip of the two-fluid nozzle 160. Next, the MPU 181 opens the electromagnetic variable throttle valve 123 to a predetermined opening.
- the raw material liquid 112 stored in the raw material tank 111 is supplied to the liquid supply port 151 of the two-fluid nozzle 160 through the raw material feed pipe 121, and from the liquid discharge port 161 at the tip of the two-fluid nozzle 160. It is discharged.
- the raw material liquid 112 discharged from the two-fluid nozzle 160 is crushed into fine particles by the high-speed vortex of air that has already been formed in the discharge direction, and the components in the raw liquid 1 12 (fluid) accompany the vortex flow. Are released into the product container 125 in a uniform state.
- the liquid level of the raw material liquid 112 in the raw material tank 111 decreases, so the volume of the upper space in the raw material tank 111 increases, and the atmospheric pressure decreases accordingly.
- This pressure is constantly detected by the atmospheric pressure sensor 135, and the value is sent to the MPU 181.
- the MPU 181 constantly monitors the value detected by the atmospheric pressure sensor 135. Maintain a predetermined appropriate value.
- the pressure inside the compressed gas reservoir 139 The pressure of the compressed gas is also maintained at an appropriate value by controlling the solenoid valve 137 by the MPU181.
- gas processing gas addition, gas A pretreated liquid 124 that has been replaced, degassed, or sterilized (sterilized) is produced, stored in the product container 125, and collected.
- oxygen can be added to the fluid (or substitution of dissolved gas with oxygen), and nitrogen gas or carbon dioxide can be added. If an inert gas such as carbon is used, dissolved oxygen in the fluid can be replaced with an inert gas.
- the air stream ejected from the two-fluid nozzle 160 is superheated steam (for example, 115 ° C to 200 ° C), hydrogen peroxide gas, or ozone, the fluid is extremely reactive in the form of a mist. Since it can be sterilized in a high state, it can be said that sterilization can be performed efficiently in an extremely short time.
- superheated steam for example, 115 ° C to 200 ° C
- hydrogen peroxide gas for example, hydrogen peroxide gas, or ozone
- a gas injection function for injecting a second gas (usually the same as the gas used for crushing) into the fluid in advance. May be provided. Thereby, when discharged from the liquid discharge port 161, it can be further finely crushed by the diffusion of the injected gas, and the homogeneity can be further increased.
- the processed liquid 124 in a state where moisture and fat globules in the fluid are uniformly mixed is generated. It is stored in the product container 125 and collected.
- the gas stream ejected from the two-fluid nozzle 160 is nitrogen gas
- nitrogen substitution of dissolved oxygen can be performed simultaneously with the homogenization treatment.
- the conventional nitrogen replacement method needed to take into account the foaming problem. This processing method does not cause such a problem.
- the air stream ejected from the two-fluid nozzle 160 is superheated steam, the fluid can be sterilized in a mist state, so that the sterilization can be performed efficiently in a very short time. .
- the viscosity of the fluid in the pipe is different from the upstream side and the downstream side.
- the above example is not limited as long as it can be fed through the pipe due to the pressure difference.
- Predetermined temperature of each sample in a constant temperature water bath (constant temperature water bath: THERMO MINDER SJ-10 (Taitech Co., Ltd.), specification temperature range: 0 to: 100 ° C, temperature accuracy: ⁇ 0.15 to 0.3 ° C) (5 ° C, 10 ° C, 15 ° C, 20 ° C), and the following treatment was performed with a mixer (sample discharge pressure: 0.2 MPa, air flow injection pressure: 0.5 MPa).
- Nitrogen gas treatment Treated 1 to 3 times with a mixer.
- Treatment with oxygen gas Treated 1 to 3 times with a mixer.
- treatment with nitrogen gas A sample that had been subjected to oxygen gas treatment three times with a mixer was used, and further treated with nitrogen gas.
- Raw milk diluted 1000 times with pure water was processed 1 to 3 times with a mixer.
- the following dissolved oxygen meter and light scattering photometer were used to measure the dissolved oxygen concentration and particle size (cumulant method). Moreover, the sample temperature after a process was measured.
- Measurement of dissolved oxygen Digital dissolved oxygen meter DO_ 5509 (Fuso Rika Products Co., Ltd.), Measuring method: Polarographic type (with temperature sensor), Measuring range: 0-20. Omg / L, Accuracy: ⁇ 0
- the measured value of the N-treated sample was the same as the measured value of the third sample treated (measured value in Katsuko).
Abstract
Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CA002649041A CA2649041A1 (en) | 2006-04-11 | 2007-04-11 | Gas treatment method |
JP2008509911A JPWO2007117024A1 (ja) | 2006-04-11 | 2007-04-11 | ガス処理方法 |
US12/296,929 US20090252836A1 (en) | 2006-04-11 | 2007-04-11 | Method of Gas Treatment |
EP07741431A EP2016831A1 (en) | 2006-04-11 | 2007-04-11 | Method of gas treatment |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2006-109094 | 2006-04-11 | ||
JP2006109094 | 2006-04-11 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2007117024A1 true WO2007117024A1 (ja) | 2007-10-18 |
Family
ID=38581293
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2007/057995 WO2007117024A1 (ja) | 2006-04-11 | 2007-04-11 | ガス処理方法 |
PCT/JP2007/057994 WO2007117023A1 (ja) | 2006-04-11 | 2007-04-11 | リポソーム分散液の製造方法ならびに製造装置 |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/JP2007/057994 WO2007117023A1 (ja) | 2006-04-11 | 2007-04-11 | リポソーム分散液の製造方法ならびに製造装置 |
Country Status (5)
Country | Link |
---|---|
US (2) | US20100025872A1 (ja) |
EP (2) | EP2016831A1 (ja) |
JP (2) | JP4058108B2 (ja) |
CA (2) | CA2649025A1 (ja) |
WO (2) | WO2007117024A1 (ja) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012102189A1 (ja) * | 2011-01-24 | 2012-08-02 | 株式会社明治 | 液状食品及びその製造方法 |
WO2014030695A1 (ja) * | 2012-08-23 | 2014-02-27 | 株式会社ウイングターフ | フッ素樹脂粒子 |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7985058B2 (en) * | 2007-01-12 | 2011-07-26 | Mark Gray | Method and apparatus for making uniformly sized particles |
WO2011127456A2 (en) | 2010-04-09 | 2011-10-13 | Pacira Pharmaceuticals, Inc. | Method for formulating large diameter synthetic membrane vesicles |
KR101198715B1 (ko) * | 2010-05-14 | 2012-11-13 | 한국생명공학연구원 | 핵산 및 친수성 음이온 화합물의 고효율 포획을 위한 비대칭 리포솜 및 이의 제조방법 |
LT2773326T (lt) | 2011-11-04 | 2019-04-25 | Nitto Denko Corporation | Lipidų-nukleorūgščių dalelių sterilios gamybos būdas |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01274865A (ja) * | 1988-04-26 | 1989-11-02 | Nordson Kk | 液体又は溶融体の微粒子の生成方法 |
JPH0549395A (ja) | 1991-08-15 | 1993-03-02 | Morinaga Milk Ind Co Ltd | 貯蔵生乳の鮮度保持法 |
JPH06319463A (ja) | 1993-05-13 | 1994-11-22 | Taiyo Kagaku Co Ltd | 蛋白質水溶液の処理方法 |
JP3083798B2 (ja) | 1997-02-27 | 2000-09-04 | 明治乳業株式会社 | 風味のよい乳性飲料・果汁飲料の製造方法 |
JP3091752B1 (ja) | 1999-09-09 | 2000-09-25 | 明治乳業株式会社 | 牛乳等の溶存酸素を窒素ガスと置換して殺菌する方法及び窒素ガス置換装置 |
JP2003047892A (ja) * | 2001-08-01 | 2003-02-18 | National Aerospace Laboratory Of Japan | 壁面衝突式液体微粒化ノズル |
Family Cites Families (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB8322178D0 (en) * | 1983-08-17 | 1983-09-21 | Sterwin Ag | Preparing aerosol compositions |
GB8502892D0 (en) * | 1985-02-05 | 1985-03-06 | Sterwin Ag | Aerosol composition |
JPS62201635A (ja) * | 1986-02-27 | 1987-09-05 | Snow Brand Milk Prod Co Ltd | 噴霧冷却方式によるマイクロカプセルの製造方法 |
ATE71292T1 (de) * | 1987-03-13 | 1992-01-15 | Micro Vesicular Systems | Lipidversikel aus grenzflaechenaktiven stoffen und sterolen. |
JPH06100353A (ja) * | 1992-09-17 | 1994-04-12 | Shinagawa Refract Co Ltd | 耐火物用マイクロカプセルの製造方法 |
JP3783385B2 (ja) * | 1997-08-26 | 2006-06-07 | キユーピー株式会社 | リポソーム分散液の製造方法及びそれを用いた化粧料 |
JPH11139961A (ja) | 1997-11-06 | 1999-05-25 | Taisho Pharmaceut Co Ltd | リポソームの製造方法 |
DE60135455D1 (de) * | 2000-05-16 | 2008-10-02 | Univ Minnesota | It einer mehrfachdüsenanordnung |
JP4418913B2 (ja) | 2001-08-29 | 2010-02-24 | 智彦 羽柴 | 混合装置 |
WO2004103510A2 (en) * | 2003-05-14 | 2004-12-02 | The Regents Of The University Of Colorado | Methods and apparatus using electrostatic atomization to form liquid vesicles |
JP2005295856A (ja) | 2004-04-08 | 2005-10-27 | Bio Media Co Ltd | 油脂封入微小粉体の製造方法および油脂封入微小粉体 |
-
2007
- 2007-04-11 WO PCT/JP2007/057995 patent/WO2007117024A1/ja active Application Filing
- 2007-04-11 WO PCT/JP2007/057994 patent/WO2007117023A1/ja active Application Filing
- 2007-04-11 EP EP07741431A patent/EP2016831A1/en not_active Withdrawn
- 2007-04-11 US US12/296,928 patent/US20100025872A1/en not_active Abandoned
- 2007-04-11 JP JP2007534946A patent/JP4058108B2/ja not_active Expired - Fee Related
- 2007-04-11 CA CA002649025A patent/CA2649025A1/en not_active Abandoned
- 2007-04-11 EP EP07741430A patent/EP2008710A1/en not_active Withdrawn
- 2007-04-11 US US12/296,929 patent/US20090252836A1/en not_active Abandoned
- 2007-04-11 JP JP2008509911A patent/JPWO2007117024A1/ja active Pending
- 2007-04-11 CA CA002649041A patent/CA2649041A1/en not_active Abandoned
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01274865A (ja) * | 1988-04-26 | 1989-11-02 | Nordson Kk | 液体又は溶融体の微粒子の生成方法 |
JPH0549395A (ja) | 1991-08-15 | 1993-03-02 | Morinaga Milk Ind Co Ltd | 貯蔵生乳の鮮度保持法 |
JPH06319463A (ja) | 1993-05-13 | 1994-11-22 | Taiyo Kagaku Co Ltd | 蛋白質水溶液の処理方法 |
JP3083798B2 (ja) | 1997-02-27 | 2000-09-04 | 明治乳業株式会社 | 風味のよい乳性飲料・果汁飲料の製造方法 |
JP3091752B1 (ja) | 1999-09-09 | 2000-09-25 | 明治乳業株式会社 | 牛乳等の溶存酸素を窒素ガスと置換して殺菌する方法及び窒素ガス置換装置 |
JP2001078665A (ja) * | 1999-09-09 | 2001-03-27 | Meiji Milk Prod Co Ltd | 牛乳等の溶存酸素を窒素ガスと置換して殺菌する方法及び窒素ガス置換装置 |
JP2003047892A (ja) * | 2001-08-01 | 2003-02-18 | National Aerospace Laboratory Of Japan | 壁面衝突式液体微粒化ノズル |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2012102189A1 (ja) * | 2011-01-24 | 2012-08-02 | 株式会社明治 | 液状食品及びその製造方法 |
JP5877798B2 (ja) * | 2011-01-24 | 2016-03-08 | 株式会社明治 | 液状食品及びその製造方法 |
WO2014030695A1 (ja) * | 2012-08-23 | 2014-02-27 | 株式会社ウイングターフ | フッ素樹脂粒子 |
Also Published As
Publication number | Publication date |
---|---|
EP2008710A1 (en) | 2008-12-31 |
WO2007117023A1 (ja) | 2007-10-18 |
CA2649025A1 (en) | 2007-10-18 |
JPWO2007117024A1 (ja) | 2009-08-20 |
JPWO2007117023A1 (ja) | 2009-08-20 |
CA2649041A1 (en) | 2007-10-18 |
US20100025872A1 (en) | 2010-02-04 |
JP4058108B2 (ja) | 2008-03-05 |
EP2016831A1 (en) | 2009-01-21 |
US20090252836A1 (en) | 2009-10-08 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6086833A (en) | Process and equipment for sanitizing and packaging food using ozone | |
WO2007117024A1 (ja) | ガス処理方法 | |
US5171090A (en) | Device and method for dispensing a substance in a liquid | |
US7628924B2 (en) | Mass transfer apparatus and method | |
US4647212A (en) | Continuous, static mixing apparatus | |
EP3530347A1 (en) | Method for manufacturing and system for manufacturing beverage or other liquid containing bubbles | |
US20130280403A1 (en) | Method for automatically producing milk froth | |
US8177197B1 (en) | Continuous carbonation apparatus and method | |
US20120256329A1 (en) | Processing apparatus for dispersion, dissolution, solubilization, or emulsification of gas/liquid or liquid/liquid | |
MXPA96006219A (en) | Apparatus and method for treating a flu product | |
US20050002270A1 (en) | Method and apparatus for mixing pulverous material with liquid | |
JPS5825495B2 (ja) | 流体製品を滅菌および(または)均質化する装置 | |
US20220193623A1 (en) | Bubble generation nozzle | |
KR102557241B1 (ko) | 울트라 파인 버블 제조기 및 울트라 파인 버블수 제조 장치 | |
CA2511744C (en) | Process for dispersing plant seeds and apparatus for carrying out thereof | |
US20100087776A1 (en) | Process And Apparatus For Filling A Syringe With A Thoroughly Mixed Medical Gas Mixture | |
JP4850729B2 (ja) | 粉体と液体の混合方法及びその装置 | |
JPH08281281A (ja) | オゾン水製造用装置およびオゾン水の製造方法 | |
CN108905843A (zh) | 一种饮料生产中的管道调酸装置及方法 | |
US5520456A (en) | Apparatus for homogeneous mixing of two media having an elongated cylindrical passage and media injection means | |
WO2005062816A2 (en) | System and method for heat treating a homogenized fluid product | |
JP5285223B2 (ja) | 炭素クラスター分散液の製造方法及び装置 | |
JP5285231B2 (ja) | 混合装置 | |
KR20150085862A (ko) | 수처리용 기액혼합 장치 | |
JPH02212311A (ja) | 炭酸ガス溶解方法及び装置 |
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: 07741431 Country of ref document: EP Kind code of ref document: A1 |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2008509911 Country of ref document: JP |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2649041 Country of ref document: CA |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2007741431 Country of ref document: EP |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
WWE | Wipo information: entry into national phase |
Ref document number: 12296929 Country of ref document: US |