CN105705463A - 用于提供有溶解气体的加压液体流的机器和方法 - Google Patents
用于提供有溶解气体的加压液体流的机器和方法 Download PDFInfo
- Publication number
- CN105705463A CN105705463A CN201480060767.1A CN201480060767A CN105705463A CN 105705463 A CN105705463 A CN 105705463A CN 201480060767 A CN201480060767 A CN 201480060767A CN 105705463 A CN105705463 A CN 105705463A
- Authority
- CN
- China
- Prior art keywords
- gas
- liquid
- stream
- machine
- pressure vessel
- Prior art date
- Legal status (The legal status 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 status listed.)
- Pending
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 78
- 238000000034 method Methods 0.000 title claims abstract description 37
- 239000012530 fluid Substances 0.000 claims abstract description 96
- 239000000203 mixture Substances 0.000 claims abstract description 28
- 239000007789 gas Substances 0.000 claims description 72
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 51
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 25
- 239000001301 oxygen Substances 0.000 claims description 25
- 229910052760 oxygen Inorganic materials 0.000 claims description 25
- 238000005452 bending Methods 0.000 claims description 22
- 229920006395 saturated elastomer Polymers 0.000 claims description 21
- 239000000411 inducer Substances 0.000 claims description 10
- 230000007704 transition Effects 0.000 claims description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 4
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 4
- VQTUBCCKSQIDNK-UHFFFAOYSA-N Isobutene Chemical compound CC(C)=C VQTUBCCKSQIDNK-UHFFFAOYSA-N 0.000 claims description 4
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 4
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 4
- VXNZUUAINFGPBY-UHFFFAOYSA-N 1-Butene Chemical compound CCC=C VXNZUUAINFGPBY-UHFFFAOYSA-N 0.000 claims description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 2
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 claims description 2
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 claims description 2
- 239000005977 Ethylene Substances 0.000 claims description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 2
- 239000001273 butane Substances 0.000 claims description 2
- 239000001569 carbon dioxide Substances 0.000 claims description 2
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 2
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 2
- 239000001257 hydrogen Substances 0.000 claims description 2
- 229910052739 hydrogen Inorganic materials 0.000 claims description 2
- 125000004435 hydrogen atom Chemical class [H]* 0.000 claims description 2
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 2
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 2
- 229910052757 nitrogen Inorganic materials 0.000 claims description 2
- 239000001294 propane Substances 0.000 claims description 2
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 claims description 2
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 claims description 2
- 239000002351 wastewater Substances 0.000 description 17
- 239000004215 Carbon black (E152) Substances 0.000 description 15
- 229930195733 hydrocarbon Natural products 0.000 description 15
- 150000002430 hydrocarbons Chemical class 0.000 description 15
- 238000000926 separation method Methods 0.000 description 8
- 239000007787 solid Substances 0.000 description 6
- 150000003839 salts Chemical class 0.000 description 5
- 239000002904 solvent Substances 0.000 description 5
- 238000003860 storage Methods 0.000 description 5
- 238000001556 precipitation Methods 0.000 description 4
- 239000011555 saturated liquid Substances 0.000 description 4
- 229910000831 Steel Inorganic materials 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 239000000243 solution Substances 0.000 description 3
- 239000010959 steel Substances 0.000 description 3
- 241000197194 Bulla Species 0.000 description 2
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 2
- 230000000844 anti-bacterial effect Effects 0.000 description 2
- 238000006065 biodegradation reaction Methods 0.000 description 2
- 208000002352 blister Diseases 0.000 description 2
- 239000012267 brine Substances 0.000 description 2
- 239000012153 distilled water Substances 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 238000005188 flotation Methods 0.000 description 2
- 230000005499 meniscus Effects 0.000 description 2
- 239000012188 paraffin wax Substances 0.000 description 2
- 239000012047 saturated solution Substances 0.000 description 2
- 239000011780 sodium chloride Substances 0.000 description 2
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000011144 upstream manufacturing Methods 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 description 1
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 1
- 230000001154 acute effect Effects 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 238000009360 aquaculture Methods 0.000 description 1
- 244000144974 aquaculture Species 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 159000000007 calcium salts Chemical class 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000004927 clay Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000010908 decantation Methods 0.000 description 1
- 239000003651 drinking water Substances 0.000 description 1
- 235000020188 drinking water Nutrition 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000008030 elimination Effects 0.000 description 1
- 238000003379 elimination reaction Methods 0.000 description 1
- 229940096405 magnesium cation Drugs 0.000 description 1
- 239000011553 magnetic fluid Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000008239 natural water Substances 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 230000006911 nucleation Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 230000011514 reflex Effects 0.000 description 1
- 238000005057 refrigeration Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 229910052708 sodium Inorganic materials 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 239000002569 water oil cream Substances 0.000 description 1
- 239000002349 well water Substances 0.000 description 1
- 235000020681 well water Nutrition 0.000 description 1
Classifications
-
- 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
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/433—Mixing tubes wherein the shape of the tube influences the mixing, e.g. mixing tubes with varying cross-section or provided with inwardly extending profiles
- B01F25/4331—Mixers with bended, curved, coiled, wounded mixing tubes or comprising elements for bending the flow
-
- 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
-
- 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
- B01F23/2323—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 by circulating the flow in guiding constructions or conduits
-
- 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
- B01F23/234—Surface aerating
- B01F23/2341—Surface aerating by cascading, spraying or projecting a liquid into a gaseous atmosphere
-
- 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
-
- 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
-
- 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
-
- 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
- B01F25/40—Static mixers
- B01F25/42—Static mixers in which the mixing is affected by moving the components jointly in changing directions, e.g. in tubes provided with baffles or obstructions
- B01F25/43—Mixing tubes, e.g. wherein the material is moved in a radial or partly reversed direction
- B01F25/433—Mixing tubes wherein the shape of the tube influences the mixing, e.g. mixing tubes with varying cross-section or provided with inwardly extending profiles
- B01F25/4338—Mixers with a succession of converging-diverging cross-sections, i.e. undulating cross-section
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F35/00—Accessories for mixers; Auxiliary operations or auxiliary devices; Parts or details of general application
- B01F35/90—Heating or cooling systems
-
- 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
- C02F1/24—Treatment of water, waste water, or sewage by flotation
-
- 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
- C02F1/685—Devices for dosing the additives
-
- 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
- C02F1/727—Treatment of water, waste water, or sewage by oxidation using pure oxygen or oxygen rich gas
-
- 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
- C02F3/22—Activated sludge processes using circulation pipes
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F7/00—Aeration of stretches of water
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2215/00—Auxiliary or complementary information in relation with mixing
- B01F2215/04—Technical information in relation with mixing
- B01F2215/0413—Numerical information
- B01F2215/0418—Geometrical information
- B01F2215/0422—Numerical values of angles
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2215/00—Auxiliary or complementary information in relation with mixing
- B01F2215/04—Technical information in relation with mixing
- B01F2215/0413—Numerical information
- B01F2215/0418—Geometrical information
- B01F2215/0431—Numerical size values, e.g. diameter of a hole or conduit, area, volume, length, width, or ratios thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2215/00—Auxiliary or complementary information in relation with mixing
- B01F2215/04—Technical information in relation with mixing
- B01F2215/0413—Numerical information
- B01F2215/0436—Operational information
- B01F2215/0459—Numerical values of dimensionless numbers, i.e. Re, Pr, Nu, transfer coefficients
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01F—MIXING, e.g. DISSOLVING, EMULSIFYING OR DISPERSING
- B01F2215/00—Auxiliary or complementary information in relation with mixing
- B01F2215/04—Technical information in relation with mixing
- B01F2215/0413—Numerical information
- B01F2215/0436—Operational information
- B01F2215/0468—Numerical pressure values
-
- 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
- C02F1/74—Treatment of water, waste water, or sewage by oxidation with air
-
- 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
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2101/00—Nature of the contaminant
- C02F2101/30—Organic compounds
- C02F2101/32—Hydrocarbons, e.g. oil
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/007—Contaminated open waterways, rivers, lakes or ponds
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/10—Nature of the water, waste water, sewage or sludge to be treated from quarries or from mining activities
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2103/00—Nature of the water, waste water, sewage or sludge to be treated
- C02F2103/34—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32
- C02F2103/36—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the manufacture of organic compounds
- C02F2103/365—Nature of the water, waste water, sewage or sludge to be treated from industrial activities not provided for in groups C02F2103/12 - C02F2103/32 from the manufacture of organic compounds from petrochemical industry (e.g. refineries)
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/02—Fluid flow conditions
- C02F2301/022—Laminar
-
- C—CHEMISTRY; METALLURGY
- C02—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F—TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE
- C02F2301/00—General aspects of water treatment
- C02F2301/02—Fluid flow conditions
- C02F2301/024—Turbulent
-
- 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
- C02F3/24—Activated sludge processes using free-fall aeration or spraying
-
- 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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Life Sciences & Earth Sciences (AREA)
- Organic Chemistry (AREA)
- Water Supply & Treatment (AREA)
- Environmental & Geological Engineering (AREA)
- Engineering & Computer Science (AREA)
- Hydrology & Water Resources (AREA)
- Dispersion Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Biodiversity & Conservation Biology (AREA)
- Microbiology (AREA)
Abstract
描述了一种用于提供气体液体混合物的机器和方法。所述方法可包括提供包括气体和液体的混合物的加压流体流;以及使所述流体流经过包括多个层流区和湍流区的交替流动区系列。所述机器可包括压力容器,其包括在中线上方的,适于向所述压力容器的内部体积添加气体的气体喷嘴和适于向所述压力容器的内部体积添加液体的液体雾化器;在所述中线下方的,置于所述压力容器的底部上方的流体出口和置于或相邻于所述压力容器的所述底部的清扫口;和用于确定所述压力容器的所述内部体积中的流体液位的构件。
Description
相关申请的交叉引用
本发明要求于2013年11月15日提出的第61/904,755号美国临时专利申请的优先权利益,该美国临时专利申请全部纳入本文。
发明领域
本发明涉及提供液体,尤其是气体饱和的含水流体。
背景
利用富含气体的液体的系统是已知的。例如,Kelly等人的第2,713,026号美国专利看来公开了用于废水处理的富含气体的流体的使用,并且尤其公开了将空气饱和的流体引入废水池以悬浮废水中的固体并有助于它们的移除。另一例子是Bernard等人的第4,192,742号美国专利,其看来教导通过在保持大气压强以上的处理室中处理废水以实现所述废水的超氧化(superoxygenation),可以促进废水的生物降解。
用于液体富集气体的方法和设备也是已知的。例如,Malick的第3,957,585号美国专利看来公开了雾化液体可被引入反应区域(reactionzone)以实现所述雾化液体和气体相的密切接触。一种基于此目的雾化喷头的具体类型在Eppink等人于2012年9月4号提出的第13/602,793号美国专利中公开,所述内容通过引用全部纳入本文(“Eppink”)。如Eppink中所阐述的,此喷头适于将雾化液体(例如,饮用水或污水)引入在高压下含有氧气的室,其结果是所述流体变为氧气饱和。然后所述氧气饱和的流体可被引入废水流,其结果是含有足够高水平氧气的所述废水促进能生物降解废水中废物的需氧微生物的活性。
Spears等人的第7,008,535号和第7,294,2798号美国专利看来公开了气体超饱和的流体可被引入废水,以使得所述气体超饱和的液体以基本无泡的方式引入。基于此目的,Spears公开了含有毛细管的一种或多种流体排出喷嘴的使用,经过所述喷嘴所述气体超饱和的液体可被注入所述废水。Spears等人的第7,294,278号美国专利公开了具有盘状(plate-like)构造的喷嘴中的具有约150至约450微米直径的毛细管,以及具有更常规喷头类型构造的喷嘴中的约0.005英寸(约125微米)的毛细管直径。毛细管的缺点在于它们可能易于被固体和所述气体超饱和的流体中可能夹带的反应产物所堵塞。
概述
在一个实施方案中,液体-气体饱和机器包括压力容器,其包括在中线上方的,适于向所述压力容器的内部体积添加气体的气体喷嘴和适于向所述压力容器的所述内部体积添加液体的液体雾化器;在所述中线下方的,置于所述压力容器的底部上方的流体出口和置于或相邻于所述压力容器的所述底部的清扫口;和用于确定所述压力容器的所述内部体积中的流体液位的构件;和流通地(fluidly)连接所述流体出口的流路,所述流路包括多个交替流动特征区,其中所述交替流动特征区是层流区和湍流或过渡流区,其中所述交替流动特征区由至少约500的雷诺数值区分。
在另一实施方案中,方法包括提供包括气体和液体的混合物的加压液体流;使所述流体流经过至少5个包括多个层流区和湍流区的交替流动区,其中所述层流区和湍流区由它们各自计算的雷诺数区分,所述雷诺数相差至少500。
附图的简要说明
为了更全面地理解本发明,应参考如下详细描述和附图,其中:
图1A和图1B是在含有多个交替流动区的管道中且所述流体在层流段(lamellarsections)之间的方向改变约205°的流路的前视图和侧视图;
图2A和图2B是在含有多个交替流动区的管道中且所述流体在层流段之间的方向改变约90°的流路的前视图和侧视图;
图3A和图3B是在含有多个交替流动区的管道中且所述流体在层流段之间的方向改变约135°的流路的前视图和侧视图;
图4A和图4B是在含有多个交替流动区的管道中且所述流体在层流段之间的方向改变约180°的流路的前视图和侧视图;
图5A和图5B是在含有多个交替流动区的管道中且所述流体在层流段之间的方向改变约240°的流路的前视图和侧视图;
图6A和图6B是在含有多个交替流动区的管道中且所述流体在层流段之间的方向改变约180°和约270°的流路的前视图和侧视图;和
图7A和图7B是在含有多个交替流动区的管道中且所述流体在层流段之间的方向改变约270°的流路的前视图和侧视图;
虽然特定的实施方案在所述附图中被示出,应理解该公开内容意在为说明性的,这些实施方案并不意在限制本文所描述和说明的本发明。
详述
第一种实施方案是液体-气体饱和机器,其包括具有多个交替流动特征区的流路。优选地,所述机器包括压力容器上游的具有所述交替低特征区的所述流路。所述压力容器可包括,在中线上方的,适于向所述压力容器的内部体积添加气体的气体喷嘴和适于向所述压力容器的所述内部体积添加液体的液体雾化器;和,在所述中线下方的,置于所述压力容器的底部上方的流体出口和置于或相邻于所述压力容器的所述底部的清扫口。所述压力容器的所述中线由装满该压力容器50%的水的近似弯液面线(meniscusline)确定。优选地,所述压力容器进一步包括确定所述压力容器的所述内部体积中流体液位的构件。用于确定所述流体液位的所述构件可包括分度尺、测压元件、或应变仪(例如用于当所述压力容器中的所述流体的密度是已知的)、视见区或视镜、磁性液位计、电容式变送器、磁致伸缩液位变送器、超声液位变送器、激光液位变送器、雷达液位变送器、或它们的组合。
所述流路流通地连接所述流体出口并且包括多个交替流动特征区。所述交替流动特征区可选自适于提供层流的区、适于提供过渡流的区、和适于提供湍流的区。在一个优选实施例中,所述交替流动特征区为适于提供层流的区和适于提供湍流的区。从所述压力容器开始确定,不限定哪个区先于其他区,所述流路可包括层流区,然后湍流区,然后层流区,且然后湍流区。在一个优选实施例中,从所述压力容器开始,层流区先于任何湍流区。
所述交替流动特征区可包括至少两个由雷诺数值区分的不同流动区。所述两个不同流动区之间的雷诺数的差值可为至少约500、1000、1500或2000。
在一个实例中,所述流路由管道提供。所述管道可为单一结构(例如,由单独零件制造)或可由多个不同部件组装而成,其中所述部件接合且不产生接合处特定湍流(例如,所述接合处优选为不是在流动液体中产生湍流的物理形状)。所述管道优选用不锈钢制造(例如,300系列不锈钢;更优选为304不锈钢,或海洋级不锈钢(例如,316或317不锈钢))。在优选实施例中,所述管道具有近似恒定的内径,或恒定的内径。在优选实施例中,所述管道可包括约2mm至约25mm、约5mm至约20mm、或约10mm至15mm的内径(ID)。在其他实施例中,所述管道可包括可变的ID,其中最大和最小的ID在约2mm至约25mm、约5mm至约20mm、或约10mm至约15mm的范围中。
优选地,所述管道包括流通地连接所述流体出口的进口段,流通地连接所述进口段的交替的弯曲和直线段系列,和流通地连接所述交替的弯曲和直线段系列的出口段。在一个实例中,所述弯曲段适于提供湍流或过渡流,且所述直线段适于提供层流。在另一个实例中,所述弯曲段适于提供弯曲段流动雷诺数,所述直线段适于提供直线段流动雷诺数,并且其中所述弯曲段流动雷诺数比所述直线段流动雷诺数至少大500。
在所述流路的一个实施例中,所述管道的进口段和出口段平行。换句话说,在所述进口段和所述出口段的所述流体为同方向或180°相反;优选地,在所述段中的所述流体为同方向。
在另一实施例中,所述机器包括为由此通过的所述气体液体掺合物提供稳定效应的处理区。所述处理区包括所述交替的弯曲和直线段系列、所述进口段的部分、和所述出口段的部分。在一个实例中,所述进口和出口段的部分在所述处理区中重叠。
参考所述附图,经过弯曲段附近的邻接层流段的所述流路经受至少60°,优选90°,更优选180°的方向变化。流体方向的总变化(经过邻接层流段的弯曲段)可超过360°。例如,层流段可邻接包括360°+方向变化的弯曲段(例如,盘管),其中所述机器可包括与层流区域(直线段)邻接的多个盘管(弯曲段)。优选地,所述弯曲段对经过层流段的流体方向的总改变小于360°(参见图1~7)。流体方向的变化是邻接层流段之间的角度,例如,所述流入层流段和所对应的流出层流段之间的角度。在一个实例中,方向的变化为约60至约270度、约90至约225度、或约180至约240度。在特别优选的实例中,流体方向的变化度为约60°(对于所述入射流为锐角)、约90°(对于所述入射流为直角;图2)、约135°(对于所述入射流为钝角;图3)、约180°(平行于所述入射角方向且方向反转;图4)、约205°(图1)、约240°(对于所述入射流为优角;图5)、或约270°(图7)。在另一实例中,所述处理区可包括多个段,所述段包括方向的多种变化(基于所述角度的变化是可辨认的。例如(图6),所述处理区可包括180°的方向变化和多个270°的方向变化。
优选地,所述机器包括多个交替区(例如,由直线段之间的弯曲段数量确定)。优选地,多个交替区包括至少5个、至少10个、至少15个、至少20个、或至少25个交替区。在优选实例中,所述机器包括5、6、7、8、9、10、11、12、13、14、15、16、17、18、19、20、21、22、23、24、25、26、27、28、29或30个交替区。参考所述附图,附图1A包括4.5个交替区(从所述输入流开始到该流体返回至所述输入流方向的点而确定(在此实例中,移动360°)。
典型地,所述机器进一步包括置于所述压力容器中的液体、气体、和所述液体和所述气体的混合物。优选地,所述压力容器的中线由装满所述压力容器50%的水的近似弯液面线所确定。当所述下层体积由所述液体和所述气体的混合物所占据时,所述上层体积可包括由所述气体组成的气氛中的多个所述液体的液滴。所述液体的液滴可具有小于0.1mm、小于0.05mm、小于0.01mm、或小于0.005mm的平均直径。所述上层体积可进一步包括在大于约50psi、60psi、70psi、80psi、90psi、100psi、150psi、200psi、250psi、或300psi压力下的所述气体。在此实施例中,置于所述中线下方的所述下层体积,可包括所述气体和所述液体的近似饱和或饱和混合物。在本文中,所述术语饱和具有它在化学领域中通常理解的意思;换句话说,饱和溶液,在特定温度和压力下,包括由所述溶剂(例如,所述液体)能载有的溶质(例如,所述气体)的最大量。值得注意的是,当气体和液体混合物被考虑时,溶剂的饱和点取决于压力。优选地,所述气体和液体混合物不为超饱和;在文本使用的所述术语超饱和具有它在化学领域中通常理解的意思,例如,超饱和溶液是非平衡的。当气体和液体被考虑时,超饱和溶液通常会风化(effloresce)。优选地,所述气体和所述液体的所述饱和混合物基本无泡。
在优选实施方案中,所述压力容器和所述流路中载有的所述液体是水。所述水可为蒸馏水、井水、回收水、废水、浓盐水、盐水、或它们的混合物。
在优选实施方案中,所述压力容器和所述流路中载有的所述气体包括至少50%、60%、70%、80%、或90%的氧气。优选地,所述气体包括至少80%、或至少90%的氧气。更优选地,所述气体基本由氧气组成,换句话说,所述气体具有99%或更多的氧气含量。更进一步优选地,所述机器进一步包括氧气浓缩器(例如,真空变压吸附单元)并且所述压力容器中载有的所述气体是所述氧气浓缩器的产物。
关于所述气体喷嘴和所述液体雾化器,这些可被包含在单独单元中,可被分离,或可包括组合的气体/液体注射器和分离气体和或液体注射器。在一个优选的实施方案中,所述气体喷嘴和液体雾化器以及组合在文丘里喷嘴中。
所述机器的另一优选方面是保持所述流路的温度的构件。所述流路的温度可通过例如,制冷装置、温度控制浴、循环加热器/冷却器、和/或将所述流路浸没在储池中(例如,所述液体汲出或所述流路结束的储池)而被保持。
所述机器的又一方面是脱气仪器。优选地,所述机器包括在所述液体雾化器上游的脱气仪器,换句话说,提供给所述液体雾化器的液体优选为脱气的。
另一实施方案是如上描述的所述机器的操作。所述机器的操作可包括提供流体流,所述流体流离开所述流路并且包括气体和所述液体的混合物,至接收体积(receivingvolume)且在所述接收体积中无泡生成。
再另一实施方案是方法,其包括提供包括气体和液体混合物的加压流体流,且然后使所述流体流经过一系列的包括多个层流区和湍流区的交替流动区。优选地,所述层流区和湍流区由它们各自计算的雷诺数区分,所述雷诺数相差至少500、1000、1500、或2000。更优选地,由湍流区的数量所确定,至少有约5、10、20、或25个交替流动区。
所述方法可包括加压流体流,其为基本饱和或饱和的所述气体和所述液体的混合物。换句话说,所述加压流体流包括在所述液体(溶剂)中的所述气体(溶质)的浓度,其等于或约等于在所述流体流的温度和压力下所述液体中的气体的理论浓度。优选地,所述流体流的压力和温度由所述交替流动区系列的开始点确定。在另一实例中,在所述交替流动区系列的开始点,所述加压流体流低于所述理论饱和点,并且在所述交替流动区系列的结束点,所述加压流体流是基本饱和或饱和。
优选地,所述加压流体流在进入所述交替流动区系列时和离开这些流动区时为基本无泡。换句话说,在载有所述加压流体流的管道、管子或导管中的所述流体混合物基本没有直径大于1mm、500微米、250微米、100微米、50微米、25微米、10微米、5微米、1微米、500nm、250nm、或100nm的泡。在一个实例中,当离开所述流动区时,所述加压流体流包括多个具有小于250nm、200nm、150nm、或100nm直径的纳米泡。在优选实例中,所述加压流体流包括所述溶质和溶剂的饱和溶液和多个所述气体(溶质)的纳米泡(即,纳米泡流体流),其中所述纳米泡具有小于200nm、150nm、或100nm的平均泡直径。
所述加压流体流包括气体和液体(溶质和溶剂)。尽管可以设想任何气体/液体的结合,但优选的液体是水,包括蒸馏水、舱底水、废水、采出水、浓盐水、盐水、或它们的结合。在优选实施例中,所述方法被采用以增加储存于液体储池中液体的气体含量,并且优选地,所述加压流体流的液体从所述液体储池汲出。所述气体选自氧气、臭氧、氮气、二氧化碳、一氧化碳、氢气、甲烷、乙烷、乙烯、丙烷、丙烯、丁烷、正丁烯、异丁烯、和它们的混合物。在一个优选实施例中,所述气体为氧气或氧气和另一气体的混合物,更优选地所述气体包括至少50%氧气。在此实施例的一个实例中所述气体(例如,氧气)可由氧气浓缩器(例如,真空变压吸附单元)提供。
在另一优选实施例中,所述方法被采用以增加储存于在液体储池中液体的气体含量并且包括将所述流体流提供至所述流体储池。所述液体储池包括所述液体,优选地,基本由所述液体组成。在本文中,所述液体储池可为蒸汽(steam)、河流、池塘、湖泊、海、洋、或人造池塘、废物处理储池、桶、或其它液体的体积。在优选实例中,所述储池为人造或自然池塘,在另一实例中,所述储池为用于水产养殖(例如,鱼养殖)的水体,再另一实例中所述储池为被污染的自然水体(例如,蒸汽、河流、湖泊)。
优选地,被提供至所述储池的所述流体流具有与所述流体流被提供的储池中的所述点相同或大约相同的温度。在一个实例中,所述流体流的温度和所述储池的温度平衡以使得在所述流体流被提供给所述储池之处,所述流体流和所述储池之间的温差小于约5、4、3、2、或1℃。在一个实施例中,所述流体流被冷却(例如,通过制冷单元、或冷冻水浴)。在另一实施例中,所述流体流被容纳在所述储池中的导管中,优选地,其中所述多个流动区在所述储池中。
又另一实施方案中,在水再生池中的可获得的氧气含量由首次喷在压力容器中的清洁水或回收废水增加,所述压力容器包括在至少50、75、100、150、或200psi压力下的氧气气氛,由此提供包括氧气饱和的所述水或回收废水的流体流,所述流体流进一步包括在所述饱和的水或回收废水中的氧气浓度(g/L)。然后,使来自所述压力容器的所述流体流通过包括流通地连接所述压力容器的进口段的管道。接着,使所述流体流通过流通连接所述进口段的交替的弯曲和直线段系列,且然后通过流通地连接所述交替的弯曲和直线段系列的出口段。然后所述流体流被稀释且无泡成核;例如,其中所述流体流用废水流稀释。最后,所述方法提供了例如在所述水再生池中的增加的废水氧气含量。
再又另一实施方案中,由任何一个前述的机器或方法提供的所述气体饱和液体(例如,氧气饱和液体)可储存在储存容器中(例如,箱、筒、瓶)。所述储存液体优选储存为在所述容器中的所述液体上方无液面上空间(headspace)。在一个实例中,所述液体储存于由添加所述气体液体掺合物而装满和/或膨胀的囊状物中。在另一实例中,容器中的所述无气体液体掺合物装满的空间由可压缩的、或压力调节囊状物占据,从而排除开放的液面上空间。优选地,由任何一个前述机器的方法提供的所述气体液体混合物的储存基本没有液体气体界面。储存容器和所述气体液体混合物的储存的具体实施例可包括带有囊状物的容器(例如,筒仓、箱或塔),其中所述气体液体混合物在所述囊状物中或其中液面上空间由囊状物取代。在这些实施例中,所述囊状物周围的或由所述囊状物提供的压力可用于取代来自所述容器的气体液体混合物。
在另一实施方案中,所述纳米泡流体流与包括烃(例如,油和/或油-水乳状液)的采出水掺合。所述纳米泡流体流优选与所述采出水混合且无大泡形成。在具体的实施方案中,所述纳米泡流体流与所述采出水的掺合影响来自所述掺合物的所述烃的分离。优选地,所述方法对至少占所述采出水中的烃总重量的90wt.%的分离有效。更优选地,所述方法对至少占所述采出水中的烃总重量的91wt.%、92wt.%、93.wt%、94wt.%、95wt.%、96wt、97wt.%、98wt.、或99wt.%的分离有效。在文本中,从所述采出水分离所述烃包括充分的对烃层从水层的浮选或相分离,可以回收包括少于基于所述(未处理)采出水中的烃总重量的10wt.%、9wt.%、8wt.%、7wt.%、6wt.%、5wt.%、4wt.%、3wt.、2wt.%、或1wt.%的处理水产物。优选地,可回收的处理水产物(例如,通过相分离技术如倾析法)具有少于基于所述处理水总重量的烃含量的0.1wt.%、0.01wt.%、或0.001wt.%。在一个实例中,所述方法影响(减少)所述采出水和包括其中的所述烃的密度。值得注意的是,所述采出水包括所述烃(或烃掺合物)密度(ρph)和所述水密度(包括溶质,例如,盐和其他水溶性种类)(ρpw)的密度比并且所述处理水产物包括所述处理烃密度(ρth)和所述处理水密度(ρtw)的密度比。优选地,所述采出水的密度比大于所述处理水产物的密度比,如下式所示:
更优选地,通过使所述处理烃的密度减少量大于所述处理水的密度减少量来满足所述式。换句话说,所述纳米泡流体流和所述采出水的掺合优选地产出处理水产物,其中处理水产物中的所述烃的密度以比所述水密度更大的百分比而减少。在另一实例中,所述采出水进一步包括溶解盐(例如,来自水(例如,压裂用水)和页岩的掺合物的溶解钙盐)。在此实例中,所述纳米泡流体流的添加可帮助或导致来自所述处理水产物的材料的沉淀。优选地,所述纳米泡流体流的添加导致、促进或帮助包括钙、钠、和/或镁阳离子的盐的沉淀。更进一步优选地,所述纳米泡流体流的添加促进来自处理水的烃和盐的分离。
在再另一实施方案中,所述纳米泡流体流与包括悬浮固体(例如,沙和/或黏土)的采出水掺合。所述纳米泡流体流优选与所述采出水混合且无大泡形成。在具体的实施方案中,所述纳米泡流体流和所述采出水的掺合影响来自所述掺合物的悬浮物的分离。在一个实例中,所述纳米泡流体流与包括悬浮固体的采出水混合,影响来自所述固体表面的油、石蜡、沥青质、和/或细菌的分离,并且促进所述固体的沉降/沉淀和来自采出水的所述油、石蜡、沥青质、和/或细菌的浮选/分离。
在又另一实施方案中,所述纳米泡流体流与所述采出水掺合并影响所述水的pH。例如,所述纳米泡流体流可增加或减少所述采出水的pH。在具体环境中,所述采出水的pH的减少可促进来自采出水的材料的分离,例如,通过沉淀、聚合、或泡腾(effervescence)(例如,NaSH溶液的酸化导致H2S的泡腾或消除)。在其他环境中,所述采出水的pH的增加可促进来自所述采出水的材料的分离,例如,通过凝结、阴离子聚合、或成盐和结晶。
所提供的前文描述仅用于清晰的理解,而且由其应被理解为没有非必要的限制,因为在本发明范围内的调整对于本领域具有普通技术的人员可以是显而易见的。
Claims (16)
1.一种液体-气体饱和机器,其包含:
压力容器,其包括,
在中线上方的,适于向所述压力容器的内部体积添加气体的气体喷嘴和适于向所述压力容器的内部体积添加液体的液体雾化器;
在所述中线下方的,置于所述压力容器的底部上方的流体出口和置于或相邻于所述压力容器的所述底部的清扫口;和
用于确定所述压力容器的所述内部体积中的流体液位的构件;和
流通地连接所述流体出口的流路,所述流路包括多个交替流动特征区;
其中所述交替流动特征区为层流区和湍流或过渡流区;并且
其中所述交替流动特征区由至少约500的雷诺数值区分。
2.如权利要求1所述的机器,其中所述流路由管道提供,所述管道包括流通地连接所述流体出口的进口段,流通地连接所述进口段的交替的弯曲和直线段系列,和流通地连接所述交替的弯曲和直线段系列的出口段;
其中所述弯曲段适于提供湍流或过渡流,并且所述直线段适于提供层流;和
其中所述弯曲段提供弯曲段流动雷诺数,所述直线段提供直线段流动雷诺数,并且其中所述弯曲段流动雷诺数至少比所述直线段流动雷诺数大500。
3.如权利要求2所述的机器,其中所述进口段和所述出口段平行。
4.如权利要求2所述的机器,其中所述弯曲段对通过邻接层流段的流体的方向改变约60至约270度。
5.如权利要求1所述的机器,其中所述流路包括至少5个交替流动特征区。
6.如权利要求1所述的机器,其中所述流路由管道提供,所述管道具有近似恒定的约2mm至约25mm的内径。
7.如权利要求1所述的机器,其进一步包含在所述中线上方的掺合物,所述掺合物为多个具有小于0.1mm平均直径的所述液体的液滴与所述压力容器内的大于约50psi压力下的所述气体的掺合物;和
在所述中线下方的所述气体和所述液体的饱和混合物。
8.如权利要求7所述的机器,其中所述液体为水;并且其中所述气体包括至少50%氧气。
9.如权利要求7所述的机器,其中所述气体和所述液体的所述饱和混合物基本无泡。
10.如权利要求1所述的机器,其进一步包含用于保持所述流路温度的构件。
11.一种方法,其包含:
提供包括气体和液体的混合物的加压流体流;且然后
使所述流体流经过至少5个包括多个层流区和湍流区的交替流动区;
其中所述层流区和湍流区由它们各自计算的雷诺数区分,所述雷诺数相差至少500。
12.如权利要求11所述的方法,其中所述加压流体流是所述气体和所述液体的饱和混合物。
13.如权利要求12所述的方法,其中所述加压流体流基本无泡。
14.如权利要求11所述的方法,其中所述液体为水;并且其中所述气体选自氧气、臭氧、氮气、二氧化碳、一氧化碳、氢气、甲烷、乙烷、乙烯、丙烷、丙烯、丁烷、正丁烯、异丁烯及其混合物;优选地,其中所述气体为氧气。
15.如权利要求11所述的方法,其进一步包含使所述流体流经过至少5个交替流动区且然后将所述流体流提供给主要由所述液体组成的储池。
16.如权利要求15所述的方法,其中所述流体流具有温度并且其中所述储池具有温度;进一步包含平衡所述流体流的温度和所述储池的温度,以使得在所述流体流被提供给所述储池之处,所述流体流和所述储池之间的温差小于约5℃。
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US201361904755P | 2013-11-15 | 2013-11-15 | |
US61/904,755 | 2013-11-15 | ||
PCT/US2014/064727 WO2015073345A1 (en) | 2013-11-15 | 2014-11-10 | Machine and process for providing a pressurized liquid stream with dissolved gas |
Publications (1)
Publication Number | Publication Date |
---|---|
CN105705463A true CN105705463A (zh) | 2016-06-22 |
Family
ID=53057910
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201480060767.1A Pending CN105705463A (zh) | 2013-11-15 | 2014-11-10 | 用于提供有溶解气体的加压液体流的机器和方法 |
Country Status (7)
Country | Link |
---|---|
US (3) | US9586186B2 (zh) |
EP (1) | EP3068734B1 (zh) |
CN (1) | CN105705463A (zh) |
AU (1) | AU2014348943A1 (zh) |
CA (1) | CA2929844C (zh) |
MX (1) | MX366066B (zh) |
WO (1) | WO2015073345A1 (zh) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN107837694A (zh) * | 2017-11-28 | 2018-03-27 | 佛山科学技术学院 | 一种化工溶质快速溶解管道结构 |
CN109562305A (zh) * | 2016-05-17 | 2019-04-02 | 纳诺汽油科技股份公司 | 影响分离的方法 |
CN109844146A (zh) * | 2016-09-14 | 2019-06-04 | 奥图泰(芬兰)公司 | 用于回收贵金属的方法 |
Families Citing this family (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US11092977B1 (en) | 2017-10-30 | 2021-08-17 | Zane Coleman | Fluid transfer component comprising a film with fluid channels |
US9527046B1 (en) | 2016-01-08 | 2016-12-27 | Cliffton Lee Roe | System and method for stably infusing gas into liquid, and methods of using the gas infused liquid |
US10486114B2 (en) * | 2016-07-18 | 2019-11-26 | Gaps Technology LLC. | System and method for generating stabilized, gas infused liquids containing high and ultra-high concentrations of infused gas, and methods using the stabilized, gas infused liquids |
US11344822B2 (en) | 2017-04-28 | 2022-05-31 | Nano Gas Technologies Inc. | Nanogas shear processing |
US10486115B2 (en) | 2017-05-10 | 2019-11-26 | Gaps Technology LLC. | System and method for stably infusing gas into liquid, and for delivering the stabilized gas-infused liquid into another liquid |
JP7086547B2 (ja) * | 2017-08-31 | 2022-06-20 | キヤノン株式会社 | ウルトラファインバブル含有液の製造装置および製造方法 |
US11193359B1 (en) | 2017-09-12 | 2021-12-07 | NanoGas Technologies Inc. | Treatment of subterranean formations |
US11617994B2 (en) * | 2018-02-08 | 2023-04-04 | Bunn-O-Matic Corporation | Gas infuser for liquids |
US11904366B2 (en) | 2019-03-08 | 2024-02-20 | En Solución, Inc. | Systems and methods of controlling a concentration of microbubbles and nanobubbles of a solution for treatment of a product |
KR102100074B1 (ko) * | 2019-05-31 | 2020-05-15 | 유영호 | 미세기포 생성용 유로부재, 이를 이용한 집적 유로유닛 및 미세기포 생성기 |
US20230112608A1 (en) | 2021-10-13 | 2023-04-13 | Disruptive Oil And Gas Technologies Corp | Nanobubble dispersions generated in electrochemically activated solutions |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19742301A1 (de) * | 1997-05-06 | 1998-11-12 | Hans Asal | Vorrichtung zur Herstellung Gas-angereicherten Wassers |
US20010045673A1 (en) * | 2000-02-21 | 2001-11-29 | Ogston Mervyn R. | Compact apparatus for oxygen dissolution & distribution |
CN1914123A (zh) * | 2004-02-03 | 2007-02-14 | 松江土建株式会社 | 气液溶解装置 |
CN101376086B (zh) * | 2008-09-22 | 2010-07-21 | 徐名勇 | 一种制造压力为0.3~7.0kg/cm2的高压力臭氧水的多级高压混合装置 |
Family Cites Families (26)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB517550A (en) | 1937-08-02 | 1940-02-01 | Jean Pierre Loumiet | Method of and apparatus for obtaining protracted intimate contact between two non-miscible fluids of different densities |
US2713026A (en) | 1951-07-21 | 1955-07-12 | Process Engineers Inc | Flotator-clarifier |
BE758570A (fr) * | 1970-11-06 | 1971-04-16 | Lefebvre Simon | Procede et appareillage pour la mise en contact de fluides et le transfert de matiere et de chaleur entre ceux-ci. |
US3957585A (en) | 1975-01-30 | 1976-05-18 | Phillips Petroleum Company | Method for conducting fermentation |
FR2390192A2 (fr) | 1977-05-10 | 1978-12-08 | Degremont | Filtre biologique pour l'epuration d'eaux residuaires et installation comportant un tel fitre |
US4788020A (en) * | 1982-12-10 | 1988-11-29 | General Atomics | Method for effecting mass transfer |
US4652382A (en) * | 1984-10-19 | 1987-03-24 | International Waste Water Reclamation Technologies, Inc. | Process and apparatus for continuously treating sewage wastewater by chemical oxidation |
US5403473A (en) | 1994-02-15 | 1995-04-04 | Automatic Control Technology, Inc. | Apparatus for mixing gases and liquids and separating solids using a vortex |
US20140048494A1 (en) | 1998-04-20 | 2014-02-20 | Frederick Lee Simmons, Jr. | Apparatus and method of creating a concentrated supersaturated gaseous solution having ionization potential |
US6209855B1 (en) | 1999-05-10 | 2001-04-03 | Canzone Limited | Gas/liquid mixing apparatus and method |
US6332980B1 (en) * | 2000-03-13 | 2001-12-25 | Jack Moorehead | System for separating algae and other contaminants from a water stream |
US7008535B1 (en) | 2000-08-04 | 2006-03-07 | Wayne State University | Apparatus for oxygenating wastewater |
WO2003072507A1 (en) | 2002-02-22 | 2003-09-04 | Aqua Innovations, Inc. | Microbubbles of oxygen |
US7537200B2 (en) | 2002-10-31 | 2009-05-26 | Glassford Craig L | Controlled atmosphere gas infusion |
WO2005115598A2 (en) | 2004-05-25 | 2005-12-08 | The Board Of Trustees Of The University Of Arkansas | System and method for dissolving gases in liquids |
CN101005890A (zh) * | 2004-08-12 | 2007-07-25 | 纳幕尔杜邦公司 | 制备低分子量聚合物的装置和方法 |
US10377651B2 (en) | 2006-10-30 | 2019-08-13 | Perlemax Ltd | Bubble generation for aeration and other purposes |
WO2009089543A2 (en) | 2008-01-10 | 2009-07-16 | The Ohio State University Research Foundation | Fluorescence detection system |
CN101952018B (zh) | 2008-02-21 | 2013-07-31 | 蓝星环境股份有限公司 | 用于改善气-液输送的装置 |
US20100276819A1 (en) * | 2008-04-01 | 2010-11-04 | Min Chien Teng | Microbubble gas-liquid mixing device |
DE102009032567A1 (de) * | 2009-07-11 | 2011-01-13 | Awas Ag | Saturator |
US8500104B2 (en) | 2010-06-07 | 2013-08-06 | James Richard Spears | Pressurized liquid stream with dissolved gas |
US20120228404A1 (en) | 2011-03-08 | 2012-09-13 | BluelnGreen LLC | Systems and methods for delivering a liquid having a desired dissolved gas concentration |
CA2847406A1 (en) | 2011-09-02 | 2013-03-07 | Blissfield Manufacturing Company | Atomizing spray heads, atomizing methods, and fluid systems operating therewith |
EP2776148A1 (en) | 2011-11-10 | 2014-09-17 | Blissfield Manufacturing Company | Process and apparatus for gas-enriching a liquid |
WO2014075191A1 (en) | 2012-11-15 | 2014-05-22 | Best Environmental Technologies, Inc. | Method and apparatus for producing super-oxygenated water |
-
2014
- 2014-11-10 CN CN201480060767.1A patent/CN105705463A/zh active Pending
- 2014-11-10 MX MX2016006249A patent/MX366066B/es active IP Right Grant
- 2014-11-10 EP EP14862310.1A patent/EP3068734B1/en active Active
- 2014-11-10 WO PCT/US2014/064727 patent/WO2015073345A1/en active Application Filing
- 2014-11-10 AU AU2014348943A patent/AU2014348943A1/en not_active Abandoned
- 2014-11-10 US US14/432,817 patent/US9586186B2/en active Active
- 2014-11-10 CA CA2929844A patent/CA2929844C/en not_active Expired - Fee Related
-
2016
- 2016-05-13 US US15/154,066 patent/US20160325247A1/en not_active Abandoned
-
2017
- 2017-01-23 US US15/412,177 patent/US10080998B2/en active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19742301A1 (de) * | 1997-05-06 | 1998-11-12 | Hans Asal | Vorrichtung zur Herstellung Gas-angereicherten Wassers |
US20010045673A1 (en) * | 2000-02-21 | 2001-11-29 | Ogston Mervyn R. | Compact apparatus for oxygen dissolution & distribution |
CN1914123A (zh) * | 2004-02-03 | 2007-02-14 | 松江土建株式会社 | 气液溶解装置 |
CN101376086B (zh) * | 2008-09-22 | 2010-07-21 | 徐名勇 | 一种制造压力为0.3~7.0kg/cm2的高压力臭氧水的多级高压混合装置 |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109562305A (zh) * | 2016-05-17 | 2019-04-02 | 纳诺汽油科技股份公司 | 影响分离的方法 |
CN109844146A (zh) * | 2016-09-14 | 2019-06-04 | 奥图泰(芬兰)公司 | 用于回收贵金属的方法 |
CN107837694A (zh) * | 2017-11-28 | 2018-03-27 | 佛山科学技术学院 | 一种化工溶质快速溶解管道结构 |
CN107837694B (zh) * | 2017-11-28 | 2024-03-29 | 佛山科学技术学院 | 一种化工溶质快速溶解管道结构 |
Also Published As
Publication number | Publication date |
---|---|
MX366066B (es) | 2019-06-26 |
US20160228834A1 (en) | 2016-08-11 |
CA2929844A1 (en) | 2015-05-21 |
AU2014348943A1 (en) | 2016-05-26 |
MX2016006249A (es) | 2017-01-19 |
WO2015073345A1 (en) | 2015-05-21 |
US10080998B2 (en) | 2018-09-25 |
US20170128895A1 (en) | 2017-05-11 |
CA2929844C (en) | 2018-11-06 |
EP3068734A4 (en) | 2017-11-08 |
EP3068734B1 (en) | 2020-09-23 |
US20160325247A1 (en) | 2016-11-10 |
US9586186B2 (en) | 2017-03-07 |
EP3068734A1 (en) | 2016-09-21 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN105705463A (zh) | 用于提供有溶解气体的加压液体流的机器和方法 | |
AU2010309105B2 (en) | Micro-bubble generator and micro-bubble generation device | |
CN1819868B (zh) | 气体溶解量调整方法和其装置及其系统 | |
AU2005333356B2 (en) | Ballast water treating apparatus | |
JP4869922B2 (ja) | 微細気泡発生器 | |
CN102985373B (zh) | 淡水制造装置及其运转方法 | |
IL260656A (en) | Device and method for producing a composition comprising nanobubbles dispersed in a liquid subject | |
JP5844196B2 (ja) | 淡水化装置及び淡水化方法 | |
US11339068B2 (en) | Eductor-based membrane bioreactor | |
Vera et al. | Enhancing microfiltration through an inorganic tubular membrane by gas sparging | |
CN105413434B (zh) | 一种船舶尾气脱硫和船舶压载水同时处理的工艺 | |
KR101624118B1 (ko) | 다단형(多段型)구조를 갖는 수역정화장치 | |
Hashimoto et al. | Effect of fine bubbles for washing of monolith type porous ceramic membranes treating oil-in-water emulsions | |
Vera et al. | Gas sparged cross-flow microfiltration of biologically treated wastewater | |
JPH09187632A (ja) | ガス溶解 | |
JP2022131716A (ja) | 水浄化処理装置及び水浄化処理方法 | |
KR101977656B1 (ko) | 초음파 용해부를 갖는 수조용 산소 용해기 | |
佐田富道雄 et al. | Purification of deep water in a dam lake using micro-bubbles and/or Eco-Bio-Ring | |
KR101977655B1 (ko) | 와류 발생 용해부를 갖는 수조용 산소 용해기 | |
JP2016159241A (ja) | 膜ろ過システム | |
KR101889323B1 (ko) | 이산화탄소 용해수를 이용한 분리막 세척장치 및 이를 이용한 분리막 세척방법 | |
JP2005066443A (ja) | 浄水システム及び浄水方法 | |
US20220055932A1 (en) | Process for in-line mineralisation and carbonation of demineralised water | |
BR102013028502A2 (pt) | sistema de dessalinização de água a partir da utilização de um mineral, e, processo de dessalinização de água a partir da utilização de um mineral | |
MXPA06014140A (en) | Apparatus and method for treating a fluid to increase oxygen concentration and reduce surface tension |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WD01 | Invention patent application deemed withdrawn after publication | ||
WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20160622 |