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公开(公告)号:US20230333577A1
公开(公告)日:2023-10-19
申请号:US18199556
申请日:2023-05-19
发明人: Kyle E. Miller
IPC分类号: G05D11/13 , F17D3/00 , C10G71/00 , G05B19/042 , B01F23/40 , B01F25/43 , B01F35/82 , B01F35/21 , B01F35/83 , B01F35/22
CPC分类号: G05D11/132 , F17D3/00 , C10G71/00 , G05B19/042 , G05D11/137 , B01F23/405 , B01F25/43 , B01F35/82 , B01F35/211 , B01F35/833 , B01F35/2134 , B01F35/2202 , B01F35/2206 , B01F35/8311 , C10G2300/308 , G05B2219/24215 , G05B2219/25266
摘要: Embodiments include systems and methods of in-line mixing of hydrocarbon liquids from a plurality of tanks into a single pipeline. According to an embodiment, a method of admixing hydrocarbon liquids from a plurality of tanks into a single pipeline to provide in-line mixing thereof includes determining a ratio of a second fluid flow to a first fluid flow based on signals received from a tank flow meter in fluid communication with the second fluid flow and a booster flow meter in fluid communication with a blended fluid flow. The blended fluid flow includes a blended flow of the first fluid flow and the second fluid flow. The method further includes comparing the determined ratio to a pre-selected set point ratio thereby to determine a modified flow of the second fluid flow to drive the ratio toward the pre-selected set point ratio. The method further includes controlling a variable speed drive connected to a pump thereby to control the second fluid flow through the pump based on the determined modified flow, the pump being in fluid communication with the second fluid flow.
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公开(公告)号:US12083486B2
公开(公告)日:2024-09-10
申请号:US17259444
申请日:2019-07-10
申请人: MERCK PATENT GMBH
发明人: Stephane Olivier , Gaetan Bour
IPC分类号: B01F31/55 , B01F35/21 , B01F35/221 , B01F35/32
CPC分类号: B01F31/55 , B01F35/2134 , B01F35/22161 , B01F35/3204
摘要: A mixing device (1) for cyclically imparting a force on an external surface (A) of a bag (B) for agitating a content (C) of the bag (B), the mixing device (1) comprising a lever (2) supported so as to be able to pivot about a pivot (3), a weight (4) provided on a first side of the lever (2), a driver (5) arranged to cooperate with the lever (2), a motor (6) for moving the driver (5) to lift the first side of the lever (2) with the weight (4) against gravity and to drop the first side against the external surface (A) of the bag (B), and a holder (7) for supporting the mixing device (1) such that the first side of the lever (2) can contact the external surface (A) of the bag (B) in the drop motion.
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公开(公告)号:US11986581B2
公开(公告)日:2024-05-21
申请号:US16461822
申请日:2017-11-16
发明人: Thierry Eyrard , Philippe Laffay , Benoit Luaire
IPC分类号: A61M1/16 , A61K9/08 , A61K33/14 , B01F21/00 , B01F21/10 , B01F23/53 , B01F25/50 , B01F25/52 , B01F35/21 , A61K9/00 , B01F23/50
CPC分类号: A61M1/1656 , A61K9/08 , A61K33/14 , B01F21/02 , B01F21/10 , B01F23/53 , B01F25/50 , B01F25/52 , B01F35/2117 , B01F35/2133 , B01F35/2134 , A61K9/0019 , A61M2205/3393 , B01F21/30 , B01F23/511 , B01F23/56
摘要: A water source, an acid source, an electrolyte tank containing a mixture of electrolytes in exactly the quantity needed for the manufacture of the liquid acid concentrate, and a sodium chloride source are connected to a mixing tank. A quantity of water needed for the manufacture of the batch of liquid acid concentrate is introduced into the mixing tank. A quantity of acid needed for manufacture of the liquid acid concentrate is introduced into the mixing tank, the solution is stirred until a homogeneous solution is obtained. Part of the solution contained in the mixing tank is transferred into the electrolyte tank, then the solution contained in the electrolyte tank is transferred into the mixing tank. A quantity of sodium chloride needed to manufacture the liquid acid concentrate is introduced into the mixing tank. The solution is stirred and recirculated until a homogeneous liquid acid concentrate is obtained.
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公开(公告)号:US11896940B2
公开(公告)日:2024-02-13
申请号:US16972122
申请日:2018-07-31
IPC分类号: B01F23/50 , E21B43/26 , B01F35/21 , B01F35/22 , B01F35/221 , E21B43/267 , B01F101/49
CPC分类号: B01F23/51 , B01F23/59 , B01F35/2134 , B01F35/21112 , B01F35/2203 , B01F35/2217 , E21B43/2607 , B01F2101/49 , E21B43/267
摘要: Methods and systems for controlling proppant concentration in a hydraulic fracturing slurry include measuring volumetric flow rates of fracturing fluid input to a blender and hydraulic fracturing slurry output from the blender, using these measured values to calculate a volumetric flow rate of proppant input, a slurry density and/or a slurry volume fraction, adjusting first and second valves to control rates of fluid and proppant delivery to the blender and re-measuring the volumetric flow rates and recalculating until target values of volumetric flow rate of proppant input, slurry density and/or slurry volume fraction are achieved.
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公开(公告)号:US20230256404A1
公开(公告)日:2023-08-17
申请号:US18108565
申请日:2023-02-10
申请人: PRIMEARTH EV ENERGY CO., LTD. , TOYOTA JIDOSHA KABUSHIKI KAISHA , PRIME PLANET ENERGY & SOLUTIONS, INC.
发明人: Hideki HAYASHI , Masakazu UMEHARA , Naoto OOSHIRO , Hiroki YAMADA , Yuuki KUDOU , Naoya KISHIMOTO
IPC分类号: B01F35/221 , B01F35/71 , B01F23/60 , B01F23/50 , B01F35/21 , H01M4/62 , C09D127/16 , C09D7/61
CPC分类号: B01F35/2218 , B01F35/71731 , B01F23/69 , B01F23/51 , B01F35/2134 , H01M4/628 , C09D127/16 , C09D7/61 , B01F2215/0422 , B01F2215/0431 , C08K2003/2227
摘要: A method for manufacturing slurry for an insulation protective layer of a rechargeable battery includes obtaining an insulation material calibration curve showing a relationship between particle size and compressibility of an insulation material using sets of particle size and compressibility of the insulation material, obtaining a binder calibration curve showing a relationship between particle size and compressibility of a binder using sets of particle size and compressibility of the binder, measuring particle sizes of the insulation material and the binder loaded, determining an optimal mixture weight ratio with reference to the curves so that compressibility of mixture powder of the insulation material and the binder equals a set compressibility based on the measured particle sizes, mixing the insulation material and the binder at the determined mixture weight ratio to form mixture powder, loading the mixture powder into a powder dispenser, and adding a solvent to the mixture powder.
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公开(公告)号:US20240189743A1
公开(公告)日:2024-06-13
申请号:US18555307
申请日:2022-05-11
发明人: Kent Levy , Reid Harman , Dale M. Koch
IPC分类号: B01D29/075 , B01D29/56 , B01D29/88 , B01F23/50 , B01F23/53 , B01F35/21 , B01F35/213
CPC分类号: B01D29/075 , B01D29/56 , B01D29/885 , B01F23/53 , B01F23/581 , B01F35/2134 , B01F23/511 , B01F35/213
摘要: An automated computer-controlled sampling system and related methods for collecting, processing, and analyzing agricultural samples for various chemical properties such as plant available nutrients. The sampling system allows multiple samples to be processed and analyzed for different analytes or chemical properties in a simultaneous concurrent or semi-concurrent manner. Advantageously, the system can process soil samples in the “as collected” condition without drying or grinding. The system generally includes a sample preparation sub-system which receives soil samples collected by a probe collection sub-system and produces a slurry (e.g., mixture of soil, vegetation, and/or manure and water), and a chemical analysis sub-system which processes the prepared slurry samples for quantifying multiple analytes and/or chemical properties of the sample. The preparation sub-system may comprise a slurry recirculation flow loop configured with devices to stir, measure, and adjust a water to solids ratio of the slurry.
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7.
公开(公告)号:US11918962B2
公开(公告)日:2024-03-05
申请号:US17443147
申请日:2021-07-21
发明人: Wesley John Warren
IPC分类号: B01F23/50 , B01F35/21 , B01F35/22 , B01F35/221 , B01F101/49 , E21B43/26 , E21B43/267 , G01N9/00 , G01N33/28
CPC分类号: B01F23/51 , B01F23/59 , B01F35/2111 , B01F35/2132 , B01F35/2134 , B01F35/2135 , B01F35/2202 , B01F35/2203 , B01F35/2211 , E21B43/2607 , E21B43/267 , G01N9/00 , G01N33/2823 , B01F23/581 , B01F2101/49
摘要: A method of determining a dry proppant concentration in a fracturing fluid includes combining a wet proppant with a carrier fluid in a mixer to form the fracturing fluid. The dry proppant concentration of the fracturing fluid leaving the mixer is determined using a moisture content of the wet proppant entering the mixer, wherein use of the moisture content prevents overestimation of the dry proppant concentration. The method can be preformed using a system for injecting fracturing fluid into a borehole, the fracturing fluid including a carrier fluid mixed with a wet proppant including a dry proppant dampened with a dampening liquid. The system includes a mixer operable to receive and mix the carrier fluid and the wet proppant to form the fracturing fluid, a frac pump operable to inject the fracturing fluid into the borehole, and a control system comprising a processor operable to receive a moisture content of the wet proppant before being mixed with the carrier fluid and programmed to determine a dry proppant concentration of the fracturing fluid formed in the mixer using a moisture content of the wet proppant, wherein use of the moisture content prevents overestimation of the dry proppant concentration.
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公开(公告)号:US11691114B2
公开(公告)日:2023-07-04
申请号:US16614703
申请日:2018-05-17
申请人: BASF Coatings GmbH
CPC分类号: B01F33/84 , B01F35/2131 , B01F35/2132 , B01F35/2134 , B01F35/2136 , B01F35/2202 , B01F35/82 , G05D11/134 , G05D11/138 , B01F2101/30
摘要: Disclosed is a method for the batch-based manufacture of a flowable coating material, in particular water-based or solvent-containing paint, from a plurality of components. The method includes feeding batch components into a process mixing container, mixing the components in the process mixing container to form a mixture having a preliminary composition, transferring at least part of the mixture having the preliminary composition from the process mixing container into a reception container, ascertaining an actual state of the mixture having the preliminary composition during transfer into the reception container, determining a deviation of the actual state of the mixture having the preliminary composition from a predefined setpoint state, ascertaining an adjustment quantity for the components required to reach the setpoint state, and topping up the adjustment quantity of the components into the preliminary mixture, while the preliminary mixture is being transferred from the process mixing container into the reception container.
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公开(公告)号:US11662750B2
公开(公告)日:2023-05-30
申请号:US17858397
申请日:2022-07-06
发明人: Kyle E. Miller
IPC分类号: F17D3/00 , G05D11/13 , C10G71/00 , G05B19/042 , B01F23/40 , B01F25/43 , B01F35/82 , B01F35/21 , B01F35/83 , B01F35/22
CPC分类号: G05D11/132 , B01F23/405 , B01F25/43 , B01F35/211 , B01F35/2134 , B01F35/2202 , B01F35/2206 , B01F35/82 , B01F35/833 , B01F35/8311 , C10G71/00 , F17D3/00 , G05B19/042 , G05D11/137 , C10G2300/308 , G05B2219/24215 , G05B2219/25266
摘要: Embodiments include systems and methods of in-line mixing of hydrocarbon liquids from a plurality of tanks into a single pipeline. According to an embodiment, a method of admixing hydrocarbon liquids from a plurality of tanks into a single pipeline to provide in-line mixing thereof includes determining a ratio of a second fluid flow to a first fluid flow based on signals received from a tank flow meter in fluid communication with the second fluid flow and a booster flow meter in fluid communication with a blended fluid flow. The blended fluid flow includes a blended flow of the first fluid flow and the second fluid flow. The method further includes comparing the determined ratio to a pre-selected set point ratio thereby to determine a modified flow of the second fluid flow to drive the ratio toward the pre-selected set point ratio. The method further includes controlling a variable speed drive connected to a pump thereby to control the second fluid flow through the pump based on the determined modified flow, the pump being in fluid communication with the second fluid flow.
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10.
公开(公告)号:US12066843B2
公开(公告)日:2024-08-20
申请号:US18212915
申请日:2023-06-22
发明人: Kyle E. Miller
IPC分类号: G05D11/13 , B01F23/40 , B01F25/43 , B01F35/21 , B01F35/22 , B01F35/82 , B01F35/83 , C10G71/00 , F17D3/00 , G05B19/042
CPC分类号: G05D11/132 , B01F23/405 , B01F25/43 , B01F35/211 , B01F35/2134 , B01F35/2202 , B01F35/2206 , B01F35/82 , B01F35/8311 , B01F35/833 , C10G71/00 , F17D3/00 , G05B19/042 , G05D11/137 , C10G2300/308 , G05B2219/24215 , G05B2219/25266
摘要: Embodiments include systems and methods of in-line mixing of hydrocarbon liquids and/or renewable liquids from a plurality of tanks into a single pipeline based on density or gravity. According to an embodiment, a method of admixing hydrocarbon liquids from a plurality of tanks into a single pipeline to provide in-line mixing thereof includes initiating a blending process. The blending process including continuously blending two or more liquids over a period of time, each of the two or more liquids stored in corresponding tanks, each of the corresponding tanks connected, via pipeline, to a blend pipe thereby blending the two or more liquids into a blended liquid. The method further includes determining a density of each of the two or more liquids to be blended during the blending process. The method includes, in response to a determination that the blend process has not finished and after the passage of a specified time interval, determining an actual blend density of the blended liquid, via a blend sensor connected to the blend pipe, the blended liquid flowing through the blend pipe and in contact with the blend sensor, and the specified time interval less than a total duration of the blending process. The method includes determining an actual blend density of the blended liquid, via a blend sensor connected to the blend pipe, the blended liquid flowing through the blend pipe and in contact with the blend sensor, and the specified time interval less than a total duration of the blending process; comparing the actual blend density with a target blend density; and in response to a difference, based on the comparison, of the actual blend density and target blend density determining a corrected ratio based on each density of the two or more liquids, the actual blend density, and the target blend density and adjusting, via one or more flow control devices, flow of one or more of the two or more liquids, based on the corrected ratio.
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