WO2005115597A1 - Fluid sparger and dissipater - Google Patents
Fluid sparger and dissipater Download PDFInfo
- Publication number
- WO2005115597A1 WO2005115597A1 PCT/US2005/017060 US2005017060W WO2005115597A1 WO 2005115597 A1 WO2005115597 A1 WO 2005115597A1 US 2005017060 W US2005017060 W US 2005017060W WO 2005115597 A1 WO2005115597 A1 WO 2005115597A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- fluid
- sparger
- conduit
- dissipater
- dispensing tube
- Prior art date
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/02—Settling tanks with single outlets for the separated liquid
- B01D21/04—Settling tanks with single outlets for the separated liquid with moving scrapers
- B01D21/06—Settling tanks with single outlets for the separated liquid with moving scrapers with rotating scrapers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0039—Settling tanks provided with contact surfaces, e.g. baffles, particles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/0093—Mechanisms for taking out of action one or more units of a multi-unit settling mechanism
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/01—Separation of suspended solid particles from liquids by sedimentation using flocculating agents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/24—Feed or discharge mechanisms for settling tanks
- B01D21/2405—Feed mechanisms for settling tanks
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/24—Feed or discharge mechanisms for settling tanks
- B01D21/2427—The feed or discharge opening located at a distant position from the side walls
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/24—Feed or discharge mechanisms for settling tanks
- B01D21/245—Discharge mechanisms for the sediments
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/24—Feed or discharge mechanisms for settling tanks
- B01D21/2494—Feed or discharge mechanisms for settling tanks provided with means for the removal of gas, e.g. noxious gas, air
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/28—Mechanical auxiliary equipment for acceleration of sedimentation, e.g. by vibrators or the like
- B01D21/283—Settling tanks provided with vibrators
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/28—Mechanical auxiliary equipment for acceleration of sedimentation, e.g. by vibrators or the like
- B01D21/286—Means for gentle agitation for enhancing flocculation
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/30—Control equipment
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/30—Control equipment
- B01D21/305—Control of chemical properties of a component, e.g. control of pH
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D21/00—Separation of suspended solid particles from liquids by sedimentation
- B01D21/30—Control equipment
- B01D21/34—Controlling the feed distribution; Controlling the liquid level ; Control of process parameters
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/18—Treatment of sludge; Devices therefor by thermal conditioning
- C02F11/185—Treatment of sludge; Devices therefor by thermal conditioning by pasteurisation
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F3/00—Biological treatment of water, waste water, or sewage
- C02F3/02—Aerobic processes
- C02F3/12—Activated sludge processes
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2221/00—Applications of separation devices
- B01D2221/06—Separation devices for industrial food processing or agriculture
-
- 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
- C02F1/66—Treatment of water, waste water, or sewage by neutralisation; pH adjustment
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F11/00—Treatment of sludge; Devices therefor
- C02F11/02—Biological treatment
- C02F11/04—Anaerobic treatment; Production of methane by such processes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/02—Temperature
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2209/00—Controlling or monitoring parameters in water treatment
- C02F2209/06—Controlling or monitoring parameters in water treatment pH
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Definitions
- the present invention relates generally to the introduction of a fluid into a second fluid through a sparger. More particularly, the present invention relates to the pretreatment and fermentation of waste using a sparger to introduce a gas such as air into the fermenter and/or the use of a dissipater to dissipate the gas in the fermenter.
- the treatment of waste and waste streams is known in the art.
- One method of treating a biomaterial waste stream to remove pollutants in the biomaterial waste stream is to convert the pollutants into a valuable product.
- the process of fermentation of the waste stream can be used to remove such pollutants from the waste stream and incorporate such pollutants (e.g., phosphorous, nitrogen, and potassium) into the valuable product.
- Exemplary valuable products may include, for example, an animal feed additive, a feed supplement, a fertilizer, a fertilizer ingredient, or a soil conditioner.
- the waste derived from plants can be, for example, waste from hay, leaves, weeds, or wood and can be, for example, yard waste, landscaping waste, agricultural crop waste, forest waste, pasture waste, or grassland waste.
- the biomaterial waste stream is manure
- the manure can be from an animal such as a human, a bovine animal, an equine animal, an ovine animal, a porcine animal, or poultry.
- the biomaterial waste streani can be variable and dilute biomaterial waste stream derived from manure.
- a sparger may comprise a conduit having a plurality of dispensing tubes exiting therefrom.
- the dispensing tubes may have substantially cylindrical walls and have an axially-extending slit defined therein.
- the dispensing tubes may be roll pins.
- the dispensing tubes may be coupled to the conduit such that a portion of the dispensing tube is disposed within the conduit.
- the dispensing tubes may each have an outer end that extends away from the conduit and an inner end that extends into the inner diameter of the conduit. Approximately half of the dispensing tube may extend into the inner diameter of the conduit.
- a dissipater may be provided, the dissipater being spaced apart from the outer end of the dispensing tube so as to intercept the flow of fluid exiting from the outer end of the dispensing tube.
- the dissipater may be disc shaped, or may have other shapes.
- the dissipater may have geometric channels formed therein.
- the geometric channels may be triangular shaped.
- the channels may extend axially outwardly from the center of the dissipater.
- the fermentation unit used to treat the biomaterial waste stream is an air-lift fermenter and the fermentation method can be continuous flow fermentation where the fermentation is oxidative fermentation and the fermentation is made oxidative by injecting sterilized air into the fermentation unit, hi one embodiment, the fermentation unit is cylindrical and the highest concentration of microorganisms is in the bottom half of the cylinder.
- the fermentation unit may have multiple inner cylinders, hi another embodiment, the fermentation unit can have an upwardly opening receptacle at the bottom of the fermentation unit for collection of the microorganism, and the lower portion of the upwardly opening receptacle can be tapered for collection of the microorganism in the tapered region of the receptacle for removal of the microorganism from the fermentation unit through a product outlet port, h other embodiments, the receptacle can have a first air inlet to inject air into the receptacle.
- the injection of air into the receptacle can remove at least a portion of the microorganisms that have collected in the receptacle out of the receptacle so that the concentration of microorganisms in the receptacle is reduced. As a result, the amount of the microorganism that is removed from the fermentation unit after collection in the receptacle is reduced.
- the fermentation unit can also have a second air inlet to inject air into the fermentation unit at a location outside of the receptacle to circulate the microorganisms in the fermentation unit.
- Spargers are mechanical devices that direct a first fluid such as gas or air into a second fluid such as waste so as to promote mixing of the first fluid with the second fluid.
- Such fluids may be liquid or gas, and are ideally intermixed to a desired optimal-mix state.
- Dissipaters are devices that facilitate the dissipation of the first fluid into the second fluid. When dissipating gases into a liquid, such gases are prone to coalescing with other molecules of the gas so as to form larger bubbles than possibly desired. Dissipaters and spargers can be used to control such coalescing.
- a valuable product for example, a microorganism, reducing environmental pollution, h one embodiment, fermentation of waste by the disclosed method results in the production of a valuable protein product (e.g., a fermenting microorganism such as a yeast) that can be used, for example, as an animal feed additive, a feed supplement, a fertilizer, a fertilizer ingredient, or a soil conditioner.
- a valuable protein product e.g., a fermenting microorganism such as a yeast
- a valuable protein product e.g., a fermenting microorganism such as a yeast
- FIG. 1 shows a representation of a prior art air sparger having a pipe and dispensing tube configuration
- Fig. 2 shows a pipe having a dispensing tube coupled thereto according to one embodiment of the present invention
- Fig. 3 shows a dispensing tube directed toward a dissipater
- Fig. 4 shows one embodiment of a configuration for a dissipater.
- FIG. 1 An exemplary prior art sparger 10 can be seen in Fig. 1.
- a sparger 10 comprises a conduit 12 and a plurality of dispensing tubes 14 mounted thereon.
- dispensing tubes 14 typically can be mounted to extend from an aperture 16 that is formed in the wall of conduit 12.
- a weld 18 typically secures each dispensing tube 14 inside aperture 16.
- dispensing tubes 14 may be subjected to vibrations due to the gas or air bubbles exhausting from the end of the tubes 14. The higher-pressure gas accelerates as it travels through the dispensing tubes 14, and forms bubbles as it exits the tubes into the lower-pressure fluid.
- a fluid sparger 20 according to the present invention can be seen in Fig. 2. Such a sparger is illustratively used to dispense air into a waste stream, however, it should be understood that other uses and configurations are within the scope of the disclosure.
- pipe or conduit 22 illustratively has a plurality of apertures 24 drilled or formed through its cylindrical wall 26.
- a dispensing tube 28 is positioned in each aperture 24. Dispensing tube 28 has an outer end 32 and an inner end 34.
- Dispensing tube 28 is illustratively manufactured and utilized in the following fashion. However, it should be understood that variations may exist, and are within the scope of the disclosure. Dispensing tube 28 is illustratively a roll pin which defines a tube having a substantially cylindrical wall. A slit 36 extends axially along at least a portion of the cylindrical wall. Roll pins, also known as spring pins, are common off-the-shelf items of manufacture that have many uses in industrial settings. Additionally, insertion tools for roll pins are common and readily available, and facilitate easy mounting and removal of the roll pins.
- Dispensing tube 28 is a roll pin having an illustrative outer diameter of approximately 1/16 inch (0.159 centimeter), and an inner diameter of approximately 1/32 inch (0.079 centimeter).
- a roll pin is formed of 18-8 stainless steel and has a length of one inch (2.54 centimeter). It should be understood, of course, that other sizes and dimensions are within the scope of the disclosure, and other dimensions may be advantageous when seeking varied results and sparger characteristics.
- Aperture 24 is illustratively drilled or formed in conduit 22 as a 0.0675 inch (0.171 centimeter) diameter hole that can accommodate a roll pin as described above. Using a roll pin insertion tool, the illustrative dispensing tube 28 can be inserted into aperture 24.
- the insertion tool When the proper position for dispensing tube 28 relative to aperture 24 is attained, the insertion tool can be released, and dispensing tube 28 allowed to expand radially to engage the walls of the aperture 24. Such an expansion of the roll pin may result in a space being formed as the slit 36 opens.
- the illustrative dimension 38 of slit 36 after insertion of dispensing tube 28 will be as little as 0.0-0.001 inch (0-.00254 centimeter) at the point of the aperture 24.
- the illustrative dimension 40 of slit 36 at outer end 32 or inner end 34 of dispensing tube 28 may be slightly larger than dimension 38, due to spreading of the roll pin.
- Dispensing tubes 28 can have an optimal length that creates a desired fluid distribution when the fluid is dispensed from the tubes 28.
- a fluid distribution for example, is a desired bubble size when a gas is exhausted from the tubes 28 into a surrounding fluid, such as a waste stream.
- Dispensing tubes 28 according to the present disclosure can be inserted into the conduit 22 and still provide the benefits of having a particular length that is considered optimal to performance.
- dispensing tube 28 By having a portion, for example half, of the length of the dispensing tube 28 disposed within the inner diameter region 30 of the conduit 22, the dispensing tube is more protected from breakage than if it were extending completely outside the conduit 22.
- the same effective geometry i.e. length, internal diameter, and wall thickness
- the roll pins can be more reliable than the prior art welded tubes. Repairs, replacements, and cleanings are likewise easier with roll pins than with welded tubes. Yet a further advantage is the simplicity of manufacture and the savings of costs due to not having a welding process. Fig.
- FIG. 3 illustrates a dispensing tube 28 having an outer end 32 directed toward a dissipater 42.
- a dissipater 42 is spaced apart from the outer end 32, yet sufficiently close so as to dissipate the flow of fluid that exits from outer end 32, as indicated by arrows 44.
- the flow of fluid disperses radially from the initial contact point with dissipater 42, the flow takes on the form of small particles of the fluid, illustratively, small bubbles 46.
- small bubbles more easily dissipate into the surrounding fluid (or second fluid) 48 shown in Fig. 3.
- fluid flow rates, dispensing tube dimensions, dissipater configurations / dimensions, and dissipater positioning can be varied or altered to provide a range of bubble sizes.
- Optimal bubble sizes may vary depending on the particular application of the sparger and dissipater and the particular goals of the application.
- the flow of fluid over a dissipater according to the disclosure can be described as follows. Assuming the impingement area is at the center of dissipater, the area within a certain measurable radius can be defined as witnessing mostly the transition of the flow of fluid from the direction of the stream to a direction parallel with the dissipater. A second area at a greater radius represents the area where the flow is most typically radially outward.
- a third area at an even greater radius than the second area represents the area in which the outward velocity of the fluid flow has slowed to the point that fragmentation of the gas will occur due to some relationship of dissipater surface interaction, water pressure, and the tendency of the gas to form speriods.
- Fig. 4 shows one embodiment of a dissipater 42 having a geometric surface 50 for contacting a flow of fluid from a dispensing tube.
- Dissipater 42 is illustratively substantially disc-shaped, however, other shapes and geometries are within the scope of the disclosure.
- Surface 50 of dissipater 42 illustratively forms v- shaped channels 52 that are concentrically spaced at a pre-selected radial distance from the center of dissipater 42.
- Such channels 52 facilitate the distribution of air bubbles or fluid bubbles into preselected areas pursuant to the geometry of dissipater 42.
- 12 channels 52 are provided, thereby offering 12 discrete areas that channel bubbles.
- ribs 54, between which channels 52 are formed could be shaped in any number of manners, including a full-length triangle rather than a truncated triangle, or any other geometric shape.
- a single dissipater 42 may be used in combination with a plurality of dispensing tubes, or each dispensing tube 28 may be associated with its own dissipater 42.
- Dissipater 42 may be formed substantially cylindrically, and may be positioned to intercept a plurality of fluid flows along an axial line on the dissipater.
- a method is also disclosed. The method comprises the steps of dispensing a fluid into a fermentation tank through a dispenser, and directing the dispenser toward a dissipater so that the fluid is interrupted by the dissipater after being dispensed into the fermentation tank.
- the dispenser is a roll pin that is an elongated hollow cylinder having an axially extending slit therethrough.
- the fluid sparger and dissipater described herein may be implemented, without limitation, in a fermentation structure and process forming part of a biomaterial waste processing system.
- a fermentation structure and process forming part of an overall biomaterial waste processing system is disclosed in each of co-pending PCT Applications Serial. Nos.
- BIOMATERIAL WASTE STREAM (attorney docket no. 35479-77858), PCT/US2005/ , entitled FLOCCULATION METHOD AND FLOCCULATED ORGANISM (attorney docket no. 35479-77852), PCTUS/2005/ , entitled
- BIOMATERIAL WASTE STREAMS (attorney docket no. 35479-77848) and PCT/US2005/ , entitled SYSTEM FOR REMOVING SOLIDS FROM AQUEOUS SOLUTIONS (attorney docket no. 35479-77847), all of which are assigned to the assignee of the present invention, and the disclosures of which are all incorporated herein by reference.
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Hydrology & Water Resources (AREA)
- Health & Medical Sciences (AREA)
- Thermal Sciences (AREA)
- Physics & Mathematics (AREA)
- Toxicology (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
- Processing Of Solid Wastes (AREA)
- Apparatus Associated With Microorganisms And Enzymes (AREA)
- Micro-Organisms Or Cultivation Processes Thereof (AREA)
- Separation Of Suspended Particles By Flocculating Agents (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
Claims
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US11/596,763 US20070290381A1 (en) | 2004-05-18 | 2005-05-16 | Fluid Sparger and Dissipater |
EP20050749736 EP1750832A1 (en) | 2004-05-18 | 2005-05-16 | Fluid sparger and dissipater |
Applications Claiming Priority (14)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US57216604P | 2004-05-18 | 2004-05-18 | |
US57220604P | 2004-05-18 | 2004-05-18 | |
US57218704P | 2004-05-18 | 2004-05-18 | |
US57217904P | 2004-05-18 | 2004-05-18 | |
US57195904P | 2004-05-18 | 2004-05-18 | |
US57199604P | 2004-05-18 | 2004-05-18 | |
US57222604P | 2004-05-18 | 2004-05-18 | |
US60/572,187 | 2004-05-18 | ||
US60/572,226 | 2004-05-18 | ||
US60/572,179 | 2004-05-18 | ||
US60/572,206 | 2004-05-18 | ||
US60/571,959 | 2004-05-18 | ||
US60/572,166 | 2004-05-18 | ||
US60/571,996 | 2004-05-18 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2005115597A1 true WO2005115597A1 (en) | 2005-12-08 |
Family
ID=35428276
Family Applications (7)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2005/017525 WO2005113104A1 (en) | 2004-05-18 | 2005-05-16 | System for processing a biomaterial waste stream |
PCT/US2005/017053 WO2006001934A2 (en) | 2004-05-18 | 2005-05-16 | Flocculation method and flocculated organism |
PCT/US2005/017521 WO2005113458A1 (en) | 2004-05-18 | 2005-05-16 | System for treating biomaterial waste streams |
PCT/US2005/017060 WO2005115597A1 (en) | 2004-05-18 | 2005-05-16 | Fluid sparger and dissipater |
PCT/US2005/017142 WO2005115928A1 (en) | 2004-05-18 | 2005-05-16 | System for removing solids from aqueous solutions |
PCT/US2005/017062 WO2005113105A1 (en) | 2004-05-18 | 2005-05-16 | Sand and animal waste separation system |
PCT/US2005/017090 WO2006025884A2 (en) | 2004-05-18 | 2005-05-16 | Fermenter and fermentation method |
Family Applications Before (3)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2005/017525 WO2005113104A1 (en) | 2004-05-18 | 2005-05-16 | System for processing a biomaterial waste stream |
PCT/US2005/017053 WO2006001934A2 (en) | 2004-05-18 | 2005-05-16 | Flocculation method and flocculated organism |
PCT/US2005/017521 WO2005113458A1 (en) | 2004-05-18 | 2005-05-16 | System for treating biomaterial waste streams |
Family Applications After (3)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/US2005/017142 WO2005115928A1 (en) | 2004-05-18 | 2005-05-16 | System for removing solids from aqueous solutions |
PCT/US2005/017062 WO2005113105A1 (en) | 2004-05-18 | 2005-05-16 | Sand and animal waste separation system |
PCT/US2005/017090 WO2006025884A2 (en) | 2004-05-18 | 2005-05-16 | Fermenter and fermentation method |
Country Status (3)
Country | Link |
---|---|
US (3) | US20070272617A1 (en) |
EP (7) | EP1758827A1 (en) |
WO (7) | WO2005113104A1 (en) |
Families Citing this family (55)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7987613B2 (en) * | 2004-10-12 | 2011-08-02 | Great River Energy | Control system for particulate material drying apparatus and process |
EP1877619B1 (en) | 2005-03-10 | 2013-07-10 | Applied Cleantech Inc. | Method of recycling fibers from sewage and means thereof |
US9056784B2 (en) * | 2006-09-19 | 2015-06-16 | Ken V. Pandya | High efficiency water-softening process |
US8634940B2 (en) * | 2006-10-31 | 2014-01-21 | Rockwell Automation Technologies, Inc. | Model predictive control of a fermentation feed in biofuel production |
WO2008104182A1 (en) | 2007-02-26 | 2008-09-04 | Dwn Holding Aps | Process for the production of a product based on faecals produced by animals as well as a plant for the production of the product, especially a fertilizer product |
US20100317079A1 (en) * | 2007-06-13 | 2010-12-16 | Bertrand Lesperance | Silage waste recovery process, facility, system, and product |
US8617281B2 (en) | 2007-08-13 | 2013-12-31 | Applied Cleantech, Inc | Methods and systems for feedstock production from sewage and product manufacturing therefrom |
US7632040B2 (en) * | 2007-10-30 | 2009-12-15 | Criptonic Energy Solutions, Inc. | Waste water electrical power generating system with storage system and methods for use therewith |
FI121885B (en) * | 2007-11-09 | 2011-05-31 | Chempolis Oy | A process for making a sugar product |
EP2942433A1 (en) * | 2008-05-21 | 2015-11-11 | Applied Cleantech Inc. | Methods and systems for feedstock production from sewage and product manufacturing therefrom |
WO2009152452A1 (en) * | 2008-06-12 | 2009-12-17 | Huei-Hsiung Yang | Fermentation method for the production of soluble botulinum neurotoxin proteins |
WO2010009530A1 (en) * | 2008-07-24 | 2010-01-28 | Hatch Ltd. | Method and apparatus for temperature control in a reactor vessel |
US8216517B2 (en) * | 2009-03-30 | 2012-07-10 | General Electric Company | System and method for monitoring an integrated system |
US7951988B2 (en) | 2009-04-01 | 2011-05-31 | Earth Renewal Group, Llc | Aqueous phase oxidation process |
US7915474B2 (en) | 2009-04-01 | 2011-03-29 | Earth Renewal Group, Llc | Aqueous phase oxidation process |
US8168847B2 (en) | 2009-04-01 | 2012-05-01 | Earth Renewal Group, Llc | Aqueous phase oxidation process |
US9272936B2 (en) | 2009-04-01 | 2016-03-01 | Earth Renewal Group, Llc | Waste treatment process |
US8481800B2 (en) | 2009-04-01 | 2013-07-09 | Earth Renewal Group, Llc | Aqueous phase oxidation process |
US8115047B2 (en) | 2009-04-01 | 2012-02-14 | Earth Renewal Group, Llc | Aqueous phase oxidation process |
US20110065155A1 (en) * | 2009-07-27 | 2011-03-17 | De Lima Daniel D | Productions of Organic Acid Salts from Digested Biomass and Their Uses and Self Cleaning Emitter Therefor |
CA2804906A1 (en) * | 2010-06-24 | 2011-12-29 | Cobalt Technologies, Inc. | Removal of inhibitors of microbial fermentation from inhibitor-containing compositions |
US9216390B2 (en) * | 2010-07-15 | 2015-12-22 | Ohio State Innovation Foundation | Systems, compositions, and methods for fluid purification |
FR2969506B1 (en) * | 2010-12-22 | 2013-02-15 | Sartorius Stedim Biotech Sa | MIXING THE CONTENTS OF A FLEXIBLE CONTAINER FOR BIOPHARMACEUTICAL USE. |
FI20115350A0 (en) | 2011-04-12 | 2011-04-12 | Steris Europe Inc | A device for separating a solid from a biowaste suspension |
US20130218483A1 (en) * | 2012-02-17 | 2013-08-22 | Johnson Controls Technology Company | Cooling tower drain monitor |
US9751781B2 (en) | 2012-03-20 | 2017-09-05 | The Research Foundation For The State University Of New York | Method to separate lignin-rich solid phase from acidic biomass suspension at an acidic pH |
EP2828204A2 (en) * | 2012-03-21 | 2015-01-28 | Innovative Industries Limited | Water recycling unit |
NO337306B1 (en) * | 2012-04-04 | 2016-03-07 | Soerheim Jan Ove | Device for composting machine for organic waste |
US8997763B2 (en) | 2012-05-07 | 2015-04-07 | Stellar Industries, Inc. | Bin washing system |
US10005995B2 (en) * | 2012-08-29 | 2018-06-26 | Renewable Energy Alternatives, Llc | System and method for thermophilic anaerobic digester process |
US9181138B2 (en) | 2013-03-12 | 2015-11-10 | WISErg Corporation | Methods and systems for stabilizing organic material |
US9850512B2 (en) | 2013-03-15 | 2017-12-26 | The Research Foundation For The State University Of New York | Hydrolysis of cellulosic fines in primary clarified sludge of paper mills and the addition of a surfactant to increase the yield |
US9951363B2 (en) | 2014-03-14 | 2018-04-24 | The Research Foundation for the State University of New York College of Environmental Science and Forestry | Enzymatic hydrolysis of old corrugated cardboard (OCC) fines from recycled linerboard mill waste rejects |
US10094597B2 (en) * | 2014-09-24 | 2018-10-09 | Fisher Controls International Llc | Field instrument temperature apparatus and related methods |
US11484015B2 (en) | 2015-05-21 | 2022-11-01 | Atlantic Sapphire Ip, Llc | Systems and methods of intensive recirculating aquaculture |
US10694722B1 (en) * | 2015-05-21 | 2020-06-30 | Atlantic Sapphire IP, L.L.C. | Systems and methods of intensive recirculating aquaculture |
US11596132B2 (en) | 2015-05-21 | 2023-03-07 | Atlantic Sapphire Ip, Llc | Transfer assembly and system for aquaculture |
US11627729B2 (en) | 2015-05-21 | 2023-04-18 | Atlantic Sapphire Ip, Llc | Transfer assembly and system for aquaculture |
EP3252018A1 (en) * | 2016-05-30 | 2017-12-06 | Xylem IP Management S.à.r.l. | Method for determining flow velocity of a liquid in a treatment plant |
CN106316004B (en) * | 2016-11-07 | 2017-09-01 | 江西盖亚环保科技有限公司 | A kind of method of the direct deep purifying of high concentrated organic wastewater |
US10745658B2 (en) * | 2017-08-11 | 2020-08-18 | Mark Anthony International Srl | Clarified fermented beverages, and a method thereof |
CN107376436A (en) * | 2017-08-15 | 2017-11-24 | 长江流域水环境监测中心 | A kind of phytoplankton subsiding separator |
KR102434316B1 (en) | 2017-12-15 | 2022-08-23 | 세압 파워 리미티드 | Salt management system for portable renewable energy self-generation systems |
US10959411B2 (en) | 2018-01-04 | 2021-03-30 | Atlantic Sapphire IP, L.L.C. | Bottom grading apparatuses for aquaculture systems |
US11793215B1 (en) * | 2018-09-07 | 2023-10-24 | Incuvator Fund I, Llc | Production of finish feed product and feed ingredient from viscera |
CN111018133B (en) * | 2019-12-20 | 2022-03-29 | 深圳清谷环境科技有限公司 | Environment-friendly microbial sewage treatment agent and preparation method and application thereof |
US11425895B2 (en) | 2020-03-05 | 2022-08-30 | Atlantic Sapphire Ip, Llc | Method for optimization of filtration in an aquaculture system |
CN112811761A (en) * | 2020-12-23 | 2021-05-18 | 山西晋联环境科技有限公司 | Method and system for recovering macromolecular substances in sludge |
US11662291B1 (en) | 2021-02-03 | 2023-05-30 | Atlantic Sapphire Ip, Llc | System and method for feed validation measurement |
CN113144698B (en) * | 2021-04-20 | 2023-03-31 | 中建环能科技股份有限公司 | Efficient pretreatment system and process for removing sand slag together |
CN113308343A (en) * | 2021-05-20 | 2021-08-27 | 广州星诺信息科技有限公司 | System and method for preparing biogas from household garbage |
CN114275863B (en) * | 2021-12-29 | 2022-11-08 | 贵州师范学院 | Automatic control system and method for water treatment of thermal sterilization kettle |
WO2023168503A1 (en) * | 2022-03-09 | 2023-09-14 | Total Biotecnologia Indústria E Comércio S/A | Multi-target bioinsecticidal agricultural composition comprising bacteria and their metabolites applied to crops of agricultural importance |
CN115011980A (en) * | 2022-07-20 | 2022-09-06 | 深圳中科翎碳生物科技有限公司 | Electrocatalysis coupling biological catalysis reaction integrated device and CO 2 Method of utilization |
CN115448414B (en) * | 2022-09-30 | 2023-06-30 | 骐骧(北京)咨询服务有限公司 | Hydrodynamic force-based solid-liquid separation device and control method thereof |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2928661A (en) * | 1958-06-09 | 1960-03-15 | Albert S Maclaren | Gas and liquid mixing apparatus |
US3608834A (en) * | 1968-08-30 | 1971-09-28 | David S Maclaren | Gas diffuser |
US4177226A (en) * | 1976-05-25 | 1979-12-04 | Alsthom-Atlantique | Device for injection of a gas in a liquid |
US4504388A (en) * | 1982-06-14 | 1985-03-12 | Otv (Omnium De Traitement Et De Valorisation) | Reactor for injection of gas into a liquid |
US4557879A (en) * | 1984-09-24 | 1985-12-10 | Wilfley Weber, Inc. | Gas diffuser with indefinite life and mixed bubble size capacity |
US6322056B1 (en) * | 1999-09-28 | 2001-11-27 | Gerhardt Van Drie | Submarine type liquid mixer with aeration |
Family Cites Families (49)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2597802A (en) * | 1946-07-17 | 1952-05-20 | Stanley E Kappe | Apparatus for treating liquid sewage and the like |
US3617569A (en) * | 1970-07-31 | 1971-11-02 | Dow Chemical Co | Removal of phosphate from waste water |
US3926737A (en) * | 1972-05-10 | 1975-12-16 | New Brunswick Scientific Co | Method and apparatus for control of biochemical processes |
US3989597A (en) * | 1974-03-28 | 1976-11-02 | R. J. Reynolds Tobacco Company | Aggregate of flocculated cells |
NZ179699A (en) * | 1975-01-22 | 1978-06-02 | Ceres Ecology Corp | Recovering feed products from animal maure seperator |
USRE31023E (en) * | 1975-04-11 | 1982-09-07 | Advanced Decision Handling, Inc. | Highly automated agricultural production system |
US4041182A (en) * | 1975-04-16 | 1977-08-09 | Erickson Lennart G | Bio-protein feed manufacturing method |
FR2400938A1 (en) * | 1977-08-23 | 1979-03-23 | Fives Cail Babcock | THICKENER |
US4342650A (en) * | 1978-02-13 | 1982-08-03 | Erickson Lennart G | Organic sludge-energy recycling method |
US4159944A (en) * | 1978-02-13 | 1979-07-03 | Erickson Lennart G | Wastewater energy recycling method |
US4267049A (en) * | 1978-02-13 | 1981-05-12 | Erickson Lennart G | Biological sludge-energy recycling method |
US4260490A (en) * | 1979-11-09 | 1981-04-07 | Union Carbide Corporation | Biomonitor to safeguard water purification process from toxicants |
DE3027362A1 (en) * | 1980-07-18 | 1982-02-18 | Siemens AG, 1000 Berlin und 8000 München | COOLING ARRANGEMENT AND METHOD FOR OPERATING THE ARRANGEMENT |
DD298263A5 (en) * | 1987-11-17 | 1992-02-13 | Fzb Biotechnologische Forschungsgesellschaft Mbh Berlin,De | PROCESS FOR FLAKING BACTERIAL BIOMASS FROM SUSPENSIONS |
US4871449A (en) * | 1988-06-27 | 1989-10-03 | Lott W Gerald | Clarifier and screw compactor liquid-solid separator |
US4948509A (en) * | 1988-08-24 | 1990-08-14 | Charles Stack & Associates, Inc. | Anaerobic fermentation process |
US4940535A (en) * | 1988-11-28 | 1990-07-10 | Amoco Corporation | Solids flow distribution apparatus |
US4898678A (en) * | 1988-12-12 | 1990-02-06 | Johnson Charles G | Heavy-metal separator for drinking water |
DK96989D0 (en) * | 1989-02-28 | 1989-02-28 | Faxe Kalkbrud Aktieselskabet | PROCEDURE FOR MONITORING BIOLOGICAL PROCESSES |
US5480559A (en) * | 1991-05-17 | 1996-01-02 | Hydro International Plc | Liquid treatment |
GB9116699D0 (en) * | 1991-08-02 | 1991-09-18 | Allied Colloids Ltd | Dewatering of aqueous suspensions |
GB9118560D0 (en) * | 1991-08-30 | 1991-10-16 | Pirtferm Ltd | Process for degrading organic matter |
US5552316A (en) * | 1993-06-04 | 1996-09-03 | Environmental Marketing Services, Ltd. | Clarifying E. coli fermentation broths with a combination of anionic and cationic flocculants |
BR9406816A (en) * | 1993-06-14 | 1996-07-23 | Agustin H Arrau | Co-mixing process and apparatus for the treatment of solid waste and sewage sludge |
AT399141B (en) * | 1993-08-13 | 1995-03-27 | Anlagenbau Franz Zierler | METHOD AND DEVICE FOR SEPARATING SAND FROM WASTE WATER LOADED WITH SAND AND ORGANIC SUBSTANCES |
AUPM452094A0 (en) * | 1994-03-17 | 1994-04-14 | University Of Queensland, The | Waste treatment plant and process |
DE4410969C1 (en) * | 1994-03-29 | 1995-12-07 | Rudolf Bischof Gmbh Tech Hande | Separating device for solid/fluid mixtures |
DE4415647C2 (en) * | 1994-05-04 | 1996-10-02 | Huber Hans Gmbh Maschinen Und | Device for separating inorganic material contaminated with organic material from a liquid |
US5746920A (en) * | 1994-06-08 | 1998-05-05 | Fraunhofer-Gesellschaft Zur Foerder Der Angewandten Forschung E.V. | Process for purifying dairy wastewater |
US5466370A (en) * | 1994-06-30 | 1995-11-14 | General Electric Company | Apparatus for isolating solids from fluids |
NL9401495A (en) * | 1994-09-15 | 1996-04-01 | Ceres Milieu Holding Bv | Method and device for dephosphating pig manure. |
US5647986A (en) * | 1994-12-02 | 1997-07-15 | Nawathe; Dilip | Apparatus and process for distributed treatment of wastewater |
US5593600A (en) * | 1995-09-05 | 1997-01-14 | Solomon; William E. | Method of desanding, desalting and concentrating organic wastes |
US5626755A (en) * | 1995-11-08 | 1997-05-06 | Micronair, Inc. | Method and apparatus for waste digestion using multiple biological processes |
US5957301A (en) * | 1996-03-25 | 1999-09-28 | Board Of Trustees Operating Michigan State University | Method and apparatus for the separation of materials having different densities |
US5720393A (en) * | 1996-03-25 | 1998-02-24 | Board Of Trustees Operating Michigan State University | Method and apparatus for the separation of manure and sand |
DE29614456U1 (en) * | 1996-08-21 | 1996-11-14 | Feierabend, Andreas, 45326 Essen | Device for cleaning and separating sand from a sand / liquid mixture, in particular sand / water mixture |
US6148838A (en) * | 1997-05-28 | 2000-11-21 | Vanguard International Semiconductor Corporation | Automated processing liquid drain system |
US6409788B1 (en) * | 1998-01-23 | 2002-06-25 | Crystal Peak Farms | Methods for producing fertilizers and feed supplements from agricultural and industrial wastes |
US5950839A (en) * | 1998-02-27 | 1999-09-14 | Mclanahan Corporation | Method and apparatus for the separation of manure and sand |
DE19844006A1 (en) * | 1998-09-25 | 2000-04-06 | Strate Technologie Fuer Abwass | Process and assembly to separate and wash sand particles in a waste water treatment plant renders mineral sand fit for disposal to an open site |
DE19844034A1 (en) * | 1998-09-25 | 2000-04-06 | Strate Technologie Fuer Abwass | Process to remove and clean sand particles in a waste water treatment assembly achieves good separation of sand from other particles and operates at low cost |
WO2000048738A1 (en) * | 1999-02-18 | 2000-08-24 | Bormet Maschinenbau Gmbh | Separation of solids consisting of organic and inorganic material |
US6470828B1 (en) * | 2000-06-16 | 2002-10-29 | Premium Standard Farms, Inc. | Animal waste management system and method thereof |
US6531057B1 (en) * | 2001-05-25 | 2003-03-11 | Rejean Houle | Method and apparatus for separating solid material from water used to flush livestock flush lanes |
US6569331B2 (en) * | 2001-08-30 | 2003-05-27 | Rodney Raeyes | Method for animal excreta processing |
DE10200599B4 (en) * | 2002-01-10 | 2005-12-15 | Hans Huber Ag Maschinen- Und Anlagenbau | Device for separating organic and inorganic material from a liquid |
US6793814B2 (en) * | 2002-10-08 | 2004-09-21 | M-I L.L.C. | Clarifying tank |
US7435581B2 (en) * | 2003-11-26 | 2008-10-14 | Broadley-James Corporation | Integrated bio-reactor monitor and control system |
-
2005
- 2005-05-16 EP EP20050753035 patent/EP1758827A1/en not_active Withdrawn
- 2005-05-16 WO PCT/US2005/017525 patent/WO2005113104A1/en active Application Filing
- 2005-05-16 WO PCT/US2005/017053 patent/WO2006001934A2/en active Application Filing
- 2005-05-16 EP EP05770945A patent/EP1755761A4/en not_active Withdrawn
- 2005-05-16 US US11/596,695 patent/US20070272617A1/en not_active Abandoned
- 2005-05-16 WO PCT/US2005/017521 patent/WO2005113458A1/en active Application Filing
- 2005-05-16 US US11/596,691 patent/US20070221552A1/en not_active Abandoned
- 2005-05-16 WO PCT/US2005/017060 patent/WO2005115597A1/en active Application Filing
- 2005-05-16 EP EP20050810332 patent/EP1756258A2/en not_active Withdrawn
- 2005-05-16 EP EP20050750521 patent/EP1756016A1/en not_active Withdrawn
- 2005-05-16 EP EP05752285A patent/EP1765976A4/en not_active Withdrawn
- 2005-05-16 WO PCT/US2005/017142 patent/WO2005115928A1/en active Application Filing
- 2005-05-16 EP EP20050749736 patent/EP1750832A1/en not_active Withdrawn
- 2005-05-16 WO PCT/US2005/017062 patent/WO2005113105A1/en active Application Filing
- 2005-05-16 US US11/596,763 patent/US20070290381A1/en not_active Abandoned
- 2005-05-16 EP EP20050752623 patent/EP1755760A1/en not_active Withdrawn
- 2005-05-16 WO PCT/US2005/017090 patent/WO2006025884A2/en active Application Filing
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2928661A (en) * | 1958-06-09 | 1960-03-15 | Albert S Maclaren | Gas and liquid mixing apparatus |
US3608834A (en) * | 1968-08-30 | 1971-09-28 | David S Maclaren | Gas diffuser |
US4177226A (en) * | 1976-05-25 | 1979-12-04 | Alsthom-Atlantique | Device for injection of a gas in a liquid |
US4504388A (en) * | 1982-06-14 | 1985-03-12 | Otv (Omnium De Traitement Et De Valorisation) | Reactor for injection of gas into a liquid |
US4557879A (en) * | 1984-09-24 | 1985-12-10 | Wilfley Weber, Inc. | Gas diffuser with indefinite life and mixed bubble size capacity |
US6322056B1 (en) * | 1999-09-28 | 2001-11-27 | Gerhardt Van Drie | Submarine type liquid mixer with aeration |
Also Published As
Publication number | Publication date |
---|---|
WO2005115928A1 (en) | 2005-12-08 |
WO2006025884A3 (en) | 2007-01-25 |
WO2006001934A2 (en) | 2006-01-05 |
WO2005113104A1 (en) | 2005-12-01 |
EP1755760A1 (en) | 2007-02-28 |
WO2005113105A1 (en) | 2005-12-01 |
WO2006025884A2 (en) | 2006-03-09 |
EP1750832A1 (en) | 2007-02-14 |
EP1765976A4 (en) | 2007-10-03 |
US20070290381A1 (en) | 2007-12-20 |
EP1765976A2 (en) | 2007-03-28 |
EP1758827A1 (en) | 2007-03-07 |
WO2006001934A3 (en) | 2006-09-28 |
EP1756258A2 (en) | 2007-02-28 |
EP1755761A4 (en) | 2008-12-10 |
US20070221552A1 (en) | 2007-09-27 |
US20070272617A1 (en) | 2007-11-29 |
EP1756016A1 (en) | 2007-02-28 |
WO2005113458A1 (en) | 2005-12-01 |
EP1755761A1 (en) | 2007-02-28 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US20070290381A1 (en) | Fluid Sparger and Dissipater | |
US4938899A (en) | Gas diffusion system | |
KR101908398B1 (en) | apparatus for reduce and evanishment of organic wastes | |
CN1973968A (en) | Combined gas and liquid phase biotechnological process for purifying waste formaldehyde gas | |
CN206996269U (en) | Combined integral biological deodorizing equipment | |
KR101718434B1 (en) | Gas-liquid neutralization rapidity mixer type vacreator | |
KR102100463B1 (en) | Air Diffuser Improved Purifying Efficiency | |
CN112194287B (en) | Sewage treatment device and method thereof | |
KR101771121B1 (en) | Purification apparatus of exhaust gas using probiotics containing mixed strains of bm-s-1 | |
JP4402604B2 (en) | Sewage treatment equipment containing urine, etc. | |
CN201537457U (en) | Biochemistry and physicalchemistry combined deodorization device | |
CN102206578B (en) | Antifoaming device used for biological fermentation | |
CN213316802U (en) | Soil pollutant processing apparatus | |
CN203079744U (en) | Microporous aeration disk for sewage treatment | |
CN209872492U (en) | Micro-nano bubbling machine | |
JP4402564B2 (en) | Sewage treatment equipment | |
JP4726478B2 (en) | Fluidized ultra-fine equipment | |
CN112090944A (en) | Soil pollutant processing apparatus | |
CN201999934U (en) | Biological fermentation defoaming device | |
CN109351175A (en) | A kind of quick-acting microbial deodorants | |
CN210457883U (en) | Regulation type sludge aeration equipment and system thereof | |
KR200307201Y1 (en) | The apparatus of activated native - microbe | |
CN220265531U (en) | Convection biochemical water spray washing deodorizing device | |
KR20140139834A (en) | Ejector used to treat pig manure | |
KR200418235Y1 (en) | Oxygen Supply Apparatus for Waste-Water and Livestock Wastewater Treatment |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
AK | Designated states |
Kind code of ref document: A1 Designated state(s): AE AG AL AM AT AU AZ BA BB BG BR BW BY BZ CA CH CN CO CR CU CZ DE DK DM DZ EC EE EG ES FI GB GD GE GH GM HR HU ID IL IN IS JP KE KG KM KP KR KZ LC LK LR LS LT LU LV MA MD MG MK MN MW MX MZ NA NG NI NO NZ OM PG PH PL PT RO RU SC SD SE SG SK SL SM SY TJ TM TN TR TT TZ UA UG US UZ VC VN YU ZA ZM ZW |
|
AL | Designated countries for regional patents |
Kind code of ref document: A1 Designated state(s): BW GH GM KE LS MW MZ NA SD SL SZ TZ UG ZM ZW AM AZ BY KG KZ MD RU TJ TM AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LT LU MC NL PL PT RO SE SI SK TR BF BJ CF CG CI CM GA GN GQ GW ML MR NE SN TD TG |
|
121 | Ep: the epo has been informed by wipo that ep was designated in this application | ||
WWE | Wipo information: entry into national phase |
Ref document number: 11596763 Country of ref document: US |
|
NENP | Non-entry into the national phase |
Ref country code: DE |
|
WWW | Wipo information: withdrawn in national office |
Country of ref document: DE |
|
WWE | Wipo information: entry into national phase |
Ref document number: 2005749736 Country of ref document: EP |
|
WWP | Wipo information: published in national office |
Ref document number: 2005749736 Country of ref document: EP |
|
WWP | Wipo information: published in national office |
Ref document number: 11596763 Country of ref document: US |