WO2019102850A1 - Système de formation de mélange - Google Patents

Système de formation de mélange Download PDF

Info

Publication number
WO2019102850A1
WO2019102850A1 PCT/JP2018/041333 JP2018041333W WO2019102850A1 WO 2019102850 A1 WO2019102850 A1 WO 2019102850A1 JP 2018041333 W JP2018041333 W JP 2018041333W WO 2019102850 A1 WO2019102850 A1 WO 2019102850A1
Authority
WO
WIPO (PCT)
Prior art keywords
admixture
slurry
liquid
supply
concrete
Prior art date
Application number
PCT/JP2018/041333
Other languages
English (en)
Japanese (ja)
Inventor
慎也 伊藤
一裕 相澤
彰宏 保利
盛岡 実
Original Assignee
デンカ株式会社
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by デンカ株式会社 filed Critical デンカ株式会社
Priority to CN201880074481.7A priority Critical patent/CN111356564A/zh
Priority to JP2019555246A priority patent/JP7145171B2/ja
Publication of WO2019102850A1 publication Critical patent/WO2019102850A1/fr

Links

Images

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B28WORKING CEMENT, CLAY, OR STONE
    • B28CPREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
    • B28C5/00Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions
    • B28C5/42Apparatus specially adapted for being mounted on vehicles with provision for mixing during transport
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B28WORKING CEMENT, CLAY, OR STONE
    • B28CPREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
    • B28C7/00Controlling the operation of apparatus for producing mixtures of clay or cement with other substances; Supplying or proportioning the ingredients for mixing clay or cement with other substances; Discharging the mixture
    • B28C7/04Supplying or proportioning the ingredients
    • EFIXED CONSTRUCTIONS
    • E04BUILDING
    • E04GSCAFFOLDING; FORMS; SHUTTERING; BUILDING IMPLEMENTS OR AIDS, OR THEIR USE; HANDLING BUILDING MATERIALS ON THE SITE; REPAIRING, BREAKING-UP OR OTHER WORK ON EXISTING BUILDINGS
    • E04G21/00Preparing, conveying, or working-up building materials or building elements in situ; Other devices or measures for constructional work
    • E04G21/02Conveying or working-up concrete or similar masses able to be heaped or cast

Definitions

  • the present invention relates to a mixture generation system for mixing powdered admixtures in concrete or mortar.
  • Admixtures are materials other than cement, water and aggregate, and are materials added as needed before casting in order to impart special properties to concrete and the like. Admixture materials may be used by being added to a mixer at the time of kneading, in addition to cases where they are already mixed with cement at the time of kneading of concrete.
  • the admixture for cement grout described in Patent Document 1 can be added to a cement grout by introducing it into a stirrer such as an agitator car at a cement grout placing site or a field installation type agitator, or a mixer installed at the site. It is added.
  • the admixture is in powder form, adding the admixture directly to the agitator car may result in insufficient dispersion of the admixture in the concrete. In that case, a mass of the admixture remains in the concrete, and the mass may cause variations in the physical properties of the hardened concrete or adversely affect the concrete.
  • it is possible to mix the admixture with the concrete without dispersion by the method of performing re-kneading after adding the powdery admixture to the concrete it is necessary to separately prepare a mixer at the construction site.
  • the present inventors diligently researched to achieve the above-mentioned purpose, and have come up with a system capable of performing kneading, supply to an agitator car from measurement of powdery admixtures without relying on human power. .
  • the system can minimize human error of mistaking the volume ratio between the admixture and the liquid when slurrying the powdered admixture.
  • the present invention is based on the above findings, and the gist of the present invention is as follows.
  • Slurry production means for producing a slurry of admixture from powdery admixture and liquid, admixture supply means for feeding admixture to the slurry production means, liquid feed means for feeding liquid to the slurry production means
  • a metering means for measuring the supply amount of the mixing material supplied to the slurry production means and the supply amount of the liquid;
  • a setting means for setting the supply amount of the mixing material to be supplied to the slurry production means and the supply amount of the liquid;
  • the supply amount of the mixing material supplied by the mixing material supply means and the liquid supply means are supplied so that the supply amount of the mixing material to the manufacturing means and the supply amount of the liquid become the set supply amount set by the setting means.
  • Control means for controlling the supply amount of the liquid, pumping means for feeding the admixture slurry produced by the slurry producing means to
  • the fluctuation range of the supply amount of the mixing material controlled to the set supply amount by the control means is 3 mass% or less, and is set by the control means.
  • the fluctuation range of the supply amount of liquid controlled to be the supply amount is 2 mass% or less, and the admixture slurry is supplied to the storage and agitation mechanism through a pressure hose, concrete and admixture Mixture generation system to obtain a mixture with the slurry.
  • a liquid storage means for storing liquid and a power supply means for supplying power for driving the control means are further provided, and the means other than the concrete transport means are mounted on the same movable carriage.
  • the mixture generation system according to any one of (1) to (4).
  • the admixture feed means includes a powder feed screw shaft which is rotationally driven about its axis and feeds the admixture in the axial direction, and a variable speed drive motor which rotationally drives the powder feed screw shaft so as to change its speed.
  • the mixture production system according to any one of the above (1) to (6), wherein the supply amount of the admixture is adjusted by the rotation speed thereof.
  • the slurry production means comprises a stirring tank, a rotary shaft provided at the bottom of the stirring tank and extending vertically in the stirring tank, and a stirring blade attached to the rotary shaft, and the stirring blade is connected to the rotary shaft And the plurality of stirring blades extending radially outward from the central portion, the stirring blades extend radially outward from the periphery of the central portion, and the front end of the stirring blades is higher than the rear end
  • the material passing portion is formed by providing the stirring blades at an interval between adjacent stirring blades so as to form a material passing portion, and the auxiliary wing portion is fixed to the tip end side in the radial direction of the stirring blades.
  • the wing portion has an annular shape or a flat plate shape obtained by dividing an annular shape, and is provided on the outer side of the material passage portion in the inside and outside directions of the rotation diameter, and the tip of the stirring blade in the radial direction With a portion located more radially outward than Mixture generation system according to any one of the serial (1) to (7).
  • Admixture materials are fly ash, blast furnace slag fine powder, silica fume, expansive material, quick hardwood, quick-setting material, admixture for high strength, limestone fine powder, crushed stone powder, sludge powder and sewage sludge fine powder
  • FIG. 1 is a diagram for explaining a mixture generation system 1 in an embodiment of the present invention.
  • Fig.2 (a) is a figure for demonstrating the slurry manufacturing apparatus in the mixture production system 1 in one Embodiment of this invention
  • FIG.2 (b) demonstrates the stirring blade provided in the said slurry manufacturing apparatus.
  • FIG. FIG. 3 is a figure for demonstrating the admixture supply apparatus in the mixture production system 1 in one Embodiment of this invention.
  • FIG. 4 is a view for explaining cleaning of the agitator wheel in the modification of the mixture generation system 1 according to the embodiment of the present invention.
  • FIG. 5 is a view for explaining the mounting on a movable carriage of a modified example of the mixture generation system 1 according to an embodiment of the present invention.
  • FIG. 6 is a figure for demonstrating a mortar continuous kneading apparatus.
  • a mixture generation system 1 in one embodiment of the present invention obtains a mixture of concrete and the admixture slurry 4.
  • a mixture generation system 1 according to an embodiment of the present invention includes a slurry producing means 10 for producing an admixture slurry 4 from a powdery admixture 2 and a liquid 3, and an admixture for supplying the admixture 2 to the slurry producing means 10.
  • the setting means 51 for setting the supply amount of the admixture 2 and the supply amount of the liquid 3 supplied to the production means 10, and the supply amount of the admixture 2 and the supply amount of the liquid 3 to the slurry production means 10 Supply amount of the miscible material 2 supplied by the miscible material supply unit 20 and the supply amount of the liquid 3 supplied by the liquid supply unit 30 so that the set supply amount set by It has a control means 50 for controlling, a pumping means 60 for supplying the admixture material slurry 4 produced by the slurry producing means 10 to the pumping hose 61, and a concrete conveying means 70 having a storage and stirring mechanism 71 for storing and stirring concrete.
  • the mixture generation system 1 efficiently mixes powdery admixture material with fresh concrete transported by an agitator vehicle to a construction site by having the above-described configuration. Can.
  • the slurry production means 10 produces the admixture slurry 4 from the powdered admixture 2 and the liquid 3.
  • the slurry production means 10 is, for example, a slurry production apparatus 10 shown in FIG. The slurry production apparatus 10 will be described in more detail with reference to FIG.
  • FIG.2 (a) is a figure for demonstrating the slurry production apparatus 10 in the mixture production system 1 in one Embodiment of this invention
  • FIG.2 (b) demonstrates the stirring blade provided in the slurry production apparatus 10
  • the slurry production apparatus 10 is an apparatus for producing a admixture slurry by stirring and mixing a powdered admixture and a liquid.
  • the slurry manufacturing apparatus 10 is provided at the stirring tank 11 and at the bottom of the stirring tank 11, and attached to the rotating shaft 12 extending vertically in the stirring tank 11, the drive device 13 for rotationally driving the rotating shaft 12, and the rotating shaft 12 And the stirring blade 14.
  • the stirring tank 11 contains the admixture 2 supplied from the admixture supply means 20 and the liquid 3 supplied from the liquid supply means 30, and also accommodates the admixture material slurry 4 produced from the admixture 2 and the liquid 3 .
  • the shape of the stirring tank 11 is not particularly limited, but it is preferable that the stirring tank 11 be a rectangular housing in plan view with the upper part opened.
  • the rotating shaft 12 transmits the driving force generated by the driving device 13 to the stirring blade 14 to rotate the stirring blade 14.
  • the bottom of the stirring tank 11 is provided with the through-hole regarding the inside and outside, and the rotating shaft is passed through the through-hole. Between the inner periphery of the through hole and the rotary shaft 12, in order to prevent the material contained in the stirring tank 11 from leaking, it is sealed by a known sealing means (not shown).
  • a stirring blade side pulley 121 is provided below the rotation shaft 12, and the driving force by the drive device 13 is transmitted to the rotation shaft 12 via the belt 15.
  • the driving force by the drive device 13 may be transmitted to the rotating shaft 12 via the gear.
  • a drive may be disposed below the rotation shaft 12 so that the drive rotates the rotation shaft directly.
  • the rotational speed of the rotating shaft 12 is, for example, 750 to 1000 rpm.
  • the driving device 13 is an internal combustion engine or a motor that generates a driving force for rotating the stirring blade 14.
  • a drive device-side pulley 131 is provided below the drive device 13, and the driving force is transmitted to the belt 15 via the drive device-side pulley 131. Then, as described above, the driving force transmitted to the belt 15 is transmitted to the rotary shaft 12 via the stirring blade side pulley 121, whereby the stirring blade 14 is rotated.
  • the stirring blade 14 stirs and mixes the admixture 2 supplied from the admixture supply means 20 and the liquid 3 supplied from the liquid supply means 30. This produces an admixture slurry.
  • the stirring blade 14 includes a central portion 141 connected to the rotation shaft, and a plurality of stirring blades 142 extending radially outward from the central portion 141.
  • the stirring blade 142 extends radially outward from the periphery of the central portion 141, and is obliquely provided such that the front end of the stirring blade 142 is higher than the rear end.
  • the stirring blade 14 preferably has 2 to 10, more preferably 3 to 6, and more preferably 3 to 4 stirring blades.
  • a material passing portion 143 is formed by providing the stirring blades 142 at intervals between adjacent stirring blades 142.
  • the stirring blade 14 By rotating the stirring blade 14 by the rotation of the rotating shaft 12, the admixture slurry in the stirring tank 11 can be moved downward from the material passing portion 143 by the stirring blade 142.
  • the vortex of the admixture slurry generated in the stirring tank 11 can be enlarged, and the admixture and the liquid can be mixed uniformly throughout the entire stirring tank 11, and the uniform admixture slurry can be made in a short time. It can be manufactured.
  • An auxiliary wing portion 144 is fixed to the radial tip end of the stirring blade 142.
  • the auxiliary wing portion 144 has an annular shape, and is provided on the outer side of the material passing portion 143 in the inward and outward directions of the rotation diameter, and is radially outer than the radial tip of the agitating blade 142 It has a part located on the.
  • the auxiliary wing portion 144 can suppress the material which is pushed downward from the material passing portion 143 by the stirring blade 142 and bounces back at the bottom of the stirring tank 11 going upward.
  • the auxiliary wing portion 144 may have the shape of a flat plate obtained by dividing an annular shape.
  • the slurry manufacturing apparatus 10 supplies a discharge port 16 for discharging the manufactured admixture material slurry, a discharge port lid 17 for controlling the opening and closing of the discharge port 16, and the pumped mixture means 60 for supplying the discharged admixture material slurry.
  • the discharge chute 18 is further provided. By producing the admixture slurry while the outlet 16 is closed by the outlet lid 17, the admixture slurry can be produced batchwise. Then, after the admixture slurry is manufactured, by moving the discharge port lid 17 in the direction of the arrow in FIG. Can be supplied.
  • the slurry production means 10 can produce a uniform admixture slurry from admixture and liquid in a short time by having the above-described configuration.
  • the time from the supply of the admixture and the liquid to the slurry production apparatus 10 to the completion of the admixture slurry by the slurry production apparatus 10 is preferably within 120 seconds, more preferably within 90 seconds, and further, Preferably, it is within 60 seconds. This makes it possible to shorten the waiting time after arriving at the agitator vehicle site even if the slurry vehicle is started after the agitator vehicle arrives at the construction site.
  • the completed admixture slurry is a slurry in which no lumps of admixture remain.
  • the admixture used for producing the slurry is not particularly limited as long as it is a powdered admixture.
  • Admixture materials include, for example, fly ash, blast furnace slag fine powder, silica fume, expansive agent, quick hardwood, quick-setting agent, high strength admixture, limestone fine powder, crushed stone powder, sludge powder and sewage sludge fine powder At least one admixture selected from the group.
  • the admixture used in the mixture generation system 1 in one embodiment of the present invention is preferably an admixture added to concrete at a construction site. Such admixtures include, for example, quick hardwoods, quickeners and expansives.
  • calcium fluoroaluminate (11CaO ⁇ 7Al 2 O 3 CaF 2 ) -based rapid hardening material
  • amorphous calcium aluminate (12CaO ⁇ 7Al 2 O 3 ) -based rapid-harding materials
  • auin-based rapid-harding materials alumina cement-based rapid-harding materials
  • water-glass-based rapid-harding materials and the like.
  • the quick-setting agent used for the mixture production system 1 in one embodiment of the present invention includes, for example, inorganic salt-based fasting agents and cement mineral-based fasting agents.
  • inorganic salt-based quick-setting agents include sodium-containing carbonates, aluminates, silicates, aluminum sulfate, alum and the like.
  • cement mineral-based accelerators include calcium aluminate and calcium sulfoaluminate.
  • Examples of the expansive material used in the mixture generation system 1 according to an embodiment of the present invention include calcium sulfoaluminate (CSA) -based expansive material, lime-based expansive material, lime-CSA-based expansive material, and the like.
  • CSA calcium sulfoaluminate
  • the expansion material can not be uniformly dispersed by the agitator car, the introduction of the expansion material into the agitator car and the kneading thereof are prohibited.
  • the expansion material can be uniformly dispersed in the concrete.
  • the liquid used to produce the slurry is not particularly limited as long as it can be added to concrete.
  • the liquid is, for example, water or a liquid containing water.
  • the liquid containing water may contain, for example, a liquid admixture as well as water.
  • Liquid admixtures include, for example, AE agents, water reducing agents, AE water reducing agents, high performance water reducing agents, high performance AE water reducing agents, fluidizers, shrinkage reducing agents, durability improving agents, accelerators, dust reducing agents
  • quick-hardening materials setting / hardening time control agents, thickeners, separation reducing agents, waterproofing agents, anti-corrosion agents, cold resistance accelerators, foaming agents, foaming agents and the like.
  • the slurry production means used in the mixture production system according to an embodiment of the present invention is shown in FIG. 1 or 2 as long as it can produce a slurry of admixtures from a powdered admixture and a liquid. It is not limited to the slurry manufacturing apparatus 10.
  • the mortar continuous kneading apparatus shown in FIG. 6 can be used as a slurry production means.
  • the mortar continuous kneading apparatus will be described with reference to FIG.
  • FIG. 6 is a view for explaining the mortar continuous kneading device 10C.
  • the mortar continuous kneading apparatus 10C is an apparatus for continuously producing mortar, but it is also possible to produce an admixture slurry from powdered admixture and liquid.
  • the mortar continuous kneading device 10C includes a powder supply unit 11C and a slurry kneading unit 12C.
  • the powder supply unit 11C includes a powder supply screw shaft 114C and a variable speed drive motor 116C, and is configured to be able to adjust the supply amount of the admixture by the rotation speed of the powder supply screw shaft 114C.
  • the powder feed screw shaft 114C is rotationally driven by the variable-speed drive motor 116C around an axial center inside the hollow cylindrical casing 113C to feed (move) the admixture material in the axial direction.
  • the powder feed screw shaft 114C is preferably a horizontal shaft, but may be inclined.
  • the powder feed screw shaft 114C is located on the upstream side (right side in the figure) of the helical blade 114Ca provided in the vicinity of the discharge port (left side in the figure) and the helical blade 114Ca and feeds the helical blade 114Ca while loosening the admixture. It has a plurality of stirring plates 114Cb.
  • the spiral blade 114Ca is a continuous spiral blade having three or more pitches, and is configured to trap the admixture material and supply it in the axial left direction with the hollow cylindrical tube 115C surrounding it.
  • the hollow cylindrical tube 115C is fixed in the casing 113C so as not to rotate.
  • Stirring plate 114Cb is a radially extending flat plate or inclined plate, and is an admixture material uniformly dispersed in spiral blade 114Ca by moving leftward in the axial direction while loosening the admixture material having formed a mass inside casing 113C.
  • Agitation plate 114Cb is not limited to this configuration, and may be a spiral blade having a larger pitch than that of spiral blade 114Ca and divided at a predetermined pitch.
  • variable-speed drive motor 116C is an electric motor with a reduction gear, and is preferably inverter-controlled to rotationally drive the powder supply screw shaft 114C so as to change its speed.
  • the mixed material is supplied as a solid, the mixed material is loosened and uniformly dispersed by the stirring plate 114Cb, and the uniformly dispersed mixed material is stably supplied to the spiral blade 114Ca, and the spiral blade 114Ca
  • the mixing material can be confined between the hollow cylindrical tube 115C and the hollow cylindrical tube 115C to supply a supply amount substantially proportional to the rotational speed.
  • the powder supply unit 11C further includes a powder hopper 118C.
  • the powder hopper 118C is located above the powder feed screw shaft 114C and receives and holds the admixture from above.
  • the powder hopper 118C has a rectangular opening at its lower end along the powder feed screw shaft 114C, and is in the shape of a funnel having an upper portion extending in the width direction.
  • the slurry kneading unit 12C has a slurry kneading shaft 124C and a variable speed drive motor 126C, and is configured to be able to adjust the property of the admixture slurry by the rotational speed of the slurry kneading shaft 124C.
  • the slurry kneading shaft 124C is rotationally driven by the variable-speed drive motor 126C around the axial center inside the hollow cylindrical casing 123C, and kneading is performed while mixing the admixture and the liquid to continuously produce the admixture slurry.
  • a slurry kneading shaft 124C connects a plurality of inclined plates 124Ca which move the admixture material slurry in the axial direction while mixing admixtures and liquid, and an outer peripheral portion of adjacent two inclined plates 124Ca. And a plurality of kneading plates 124Cb extending in the direction.
  • the inclined plate 124Ca is a radially extending rectangular inclined plate, and is adapted to move the admixture slurry in the axial direction (leftward in the drawing) while mixing the admixture and the liquid on its inclined surface.
  • the kneading plate 124Cb is a flat plate extending in the axial direction, and promotes kneading of the admixture slurry to obtain the necessary admixture slurry properties.
  • the hollow cylindrical casing 123C is connected to the lower end on the outlet side of the casing 113C of the powder supply section 11C via a swing shaft 122C. Moreover, it has a fixing bracket (not shown) which fixes casing 123C in the inclined state. With this configuration, the axis of the slurry kneading shaft 124C can be variably adjusted within a range of about ⁇ 30 degrees with respect to the horizontal.
  • the axis of the slurry kneading shaft 124C is about 30 degrees from horizontal so that the slurry kneading shaft 124C is low on the supply side of the admixture (right in the figure) and high on the outlet side of the admixture slurry (left in the figure).
  • the moving speed and the discharging speed of the admixture slurry can be adjusted by the inclination angle.
  • By lowering the outlet side (left side in the figure) of the admixture slurry it is possible to increase the moving speed and discharging speed of the mortar, and to facilitate drainage when the inside is cleaned.
  • variable-speed drive motor 126C is a motor with a reduction gear, and is preferably inverter-controlled to rotationally drive the slurry kneading shaft 124C so as to change its speed.
  • the mortar continuous kneading apparatus 10C can produce a uniform admixture slurry from admixtures and liquids in a short time by having the above-described configuration.
  • the above-mentioned slurry production apparatus and the above-mentioned mortar continuous kneading apparatus are preferable as a slurry production means, and the above-mentioned slurry production apparatus is more preferable.
  • the slurry production means is not limited to the above-mentioned slurry production apparatus and the above-mentioned mortar continuous kneading apparatus, as long as a homogeneous admixture material slurry can be produced in a short time from the admixture material and liquid.
  • a drum gravity mixer, a tilting cylinder gravity mixer, a pan type forced mixer and a pug mill type forced mixer can be used as the slurry producing means.
  • a commercially available mixer can be used as a slurry production means used by the mixture production system in one embodiment of the present invention.
  • a grout mixer "OKZ-30” (model number)
  • a grout mixer “OKZ-50N” (model number)
  • a grout mixer “OKZ-100N” (model number)
  • a grout mixer “OKZ-150N” (manufactured by Okasan Kiko Co., Ltd.) Model number etc.
  • Model number etc. can be used as a slurry production means.
  • the slurry produced by the mixture generation system in one embodiment of the present invention may contain materials other than the admixture material and the liquid.
  • the slurry manufactured by the mixture production system in one embodiment of the present invention preferably excludes concrete, mortar and cement paste.
  • the admixture material supply means 20 supplies the admixture material 2 to the slurry production means 10.
  • the admixture material supply means 20 is, for example, the admixture material supply device 20 shown in FIG.
  • the admixture supply device 20 will be described in more detail with reference to FIG.
  • the admixture feed device 20 includes a powder feed screw shaft 24 rotationally driven about an axial center and feeding the admixture in the axial direction, and a variable speed drive motor rotatably driving the powder feed screw shaft 24 in a variable manner. And adjust the feed rate of the admixture by the rotation speed.
  • the powder feed screw shaft 24 is rotationally driven by the variable-speed drive motor 26 about an axial center inside the hollow cylindrical casing 23 to feed (move) the admixture material in the axial direction.
  • the powder feed screw shaft 24 has a spiral blade 24a.
  • the spiral blade 24a is a continuous spiral blade with three or more pitches, and is supplied to the left in the axial direction.
  • the variable speed drive motor 26 is an electric motor with a reduction gear, and is preferably inverter-controlled to rotationally drive the powder supply screw shaft 24 so as to change its speed.
  • the admixture feed system 20 further comprises a powder hopper 28.
  • a powder hopper 28 is located above the powder feed screw shaft 24 and receives and holds the admixture from above.
  • the powder hopper 28 has a rectangular opening at its lower end along the powder feed screw shaft 24 and is in the shape of a funnel which is spread in the width direction at the top.
  • the hopper 28 has an internal volume of, for example, 100 kg or more, and in a state where the large flexible container 4 (for example, ton pack) is lifted, the lower end is opened so that a large amount of admixture material can be replenished in a batch from the top. It has become.
  • the capacity of the hopper 28 can be selected according to the application.
  • the admixture supply device 20 has a admixture supply rate higher than the maximum processing amount of the slurry production means 10, detects the remaining amount of the raw material powder 1 in the slurry production means 10 with a sensor not shown, and turns it on / off. The admixture is intermittently supplied. The mixed material is discharged from the outlet 29 of the mixed material supply device 20 and supplied to the slurry manufacturing device 10.
  • the admixture material supply means used in the mixture generation system in one embodiment of the present invention may be the admixture material shown in FIG. 1 or 3 as long as it can supply powdered admixture material to the slurry production means. It is not limited to the supply device 20.
  • a belt feeder capable of conveying powdered admixture, or a pipe capable of circulating powdered admixture can be used as a means for feeding admixture.
  • the liquid supply means 30 supplies the liquid 3 to the slurry production means 10.
  • the liquid supply means 30 is, for example, a submersible pump 30 that pumps up the liquid stored in the liquid storage means 31 and sends the pumped liquid to the slurry manufacturing means 10 (see FIG. 1).
  • the liquid supply means 30 is not limited to the submersible pump as long as the liquid 3 can be supplied to the slurry production means 10.
  • the liquid supply means 30 may be a liquid storage tank provided on the upper side of the slurry production means 10. In this case, gravity is used to supply the liquid from the liquid storage tank to the slurry production means 10, and the amount of liquid supplied to the slurry production means 10 is adjusted using a valve provided in the liquid storage tank. Further, in order to control the amount of liquid supplied to the slurry production means 10, a flow meter may be provided between the liquid supply means 30 and the slurry production means 10.
  • the measuring means 40 measures the supply amount of the admixture 2 and the supply amount of the liquid 3 supplied to the slurry production means 10.
  • the measuring means 40 may be, for example, a load cell 40 for measuring the mass of the admixture and liquid supplied to the slurry producing means 10 (see FIG. 1). For example, the mass (W1) of the slurry production apparatus 10 before supplying the admixture and the liquid is measured by the load cell 40, and then the mass (W2) of the slurry production apparatus 10 after supplying the admixture is measured by the load cell 40 Do. Thereby, the mass (W2-W1) of the admixture material supplied to the slurry production apparatus 10 can be calculated.
  • the mass (W3) of the slurry production apparatus 10 after supplying the liquid is measured by the load cell 40.
  • the mass (W3-W2) of the liquid supplied to the slurry production apparatus 10 can be calculated.
  • the liquid may be supplied first to measure the mass of the slurry production apparatus 10, and then the admixture may be supplied to measure the mass of the slurry production apparatus 10.
  • the measuring means may measure the mass of the admixture and the liquid, or may measure the volume.
  • the measuring unit 40 is not limited to the load cell 40 as long as it can measure the supply amount of the admixture and the supply amount of the liquid supplied to the slurry production unit 10.
  • the measuring means is provided between the slurry producing means and the miscible material feeding means, and the measuring tank for measuring the feeding amount of the miscible material and the slurry producing means and the liquid feeding means is provided. It may be a tank.
  • the setting unit 51 sets the supply amount of the admixture and the supply amount of the liquid supplied to the slurry production unit 10.
  • the setting means 51 is, for example, a control panel 51 of the control device 50 (see FIG. 1).
  • the setting unit is not limited to the control panel 51 of the control device 50 as long as the supply amount of the admixture to be supplied to the slurry production unit 10 and the supply amount of the liquid can be set.
  • the setting means may be a setting input device provided separately from the control device 50 for inputting and setting the supply amount of the admixture and the supply amount of the liquid.
  • the control means 50 mixes the mixed material supplied by the mixed material supply means 20 so that the supply amount of the mixed material 2 to the slurry production means 10 and the supplied amount of the liquid 3 become the set supply amount set by the setting means 50.
  • the supply amount of the material 2 and the supply amount of the liquid 3 supplied by the liquid supply means 30 are controlled.
  • the control means 50 is, for example, the control device 50 shown in FIG.
  • the control device 50 has, for example, a microprocessor and its peripheral circuits, executes a control program stored in the ROM using the RAM as a work area, and performs various controls.
  • the controller 50 controls, for example, the supply amount of the admixture and the supply amount of the liquid as follows.
  • the flow rate of the liquid to the slurry production apparatus 10 is measured by a flow meter (not shown), and the mass of the liquid supplied to the slurry production apparatus 10 is measured using the load cell 40. This operation is performed by changing the flow rate of the liquid to the slurry production apparatus 10. Then, using the measurement result of the flow rate of the liquid measured by the flow meter and the measurement result of the supply amount of the liquid to the slurry manufacturing apparatus 10 measured by the load cell 40, the flow rate of the liquid measured by the flow meter The relationship with the actual supply amount of liquid supplied to the manufacturing apparatus 10 is examined. That is, calibration of the liquid is performed.
  • the supply amount of the admixture supplied to the slurry manufacturing apparatus 10 is measured using the load cell 40, and the relationship between the inverter frequency of the variable speed drive motor 26 and the supply of the admixture supplied to the slurry manufacturing apparatus 10 Examine. That is, calibration of the admixture is performed.
  • the control device 50 controls the amount by which the liquid in the submersible pump 30 is pumped up so that the flow rate of the liquid measured by the flow meter becomes the flow rate corresponding to the set supply amount set by the setting means 50. Furthermore, the controller 50 controls the inverter frequency of the variable-speed drive motor 26 so that the inverter frequency of the variable-speed drive motor 26 of the admixture supply device 30 becomes the inverter frequency corresponding to the set supply amount set by the setting unit 50. Control. Thereby, the control device 50 is supplied by the admixture material supply device 20 so that the supply amount of the admixture material to the slurry manufacturing device 10 and the supply amount of the liquid become the set supply amount set by the setting means 50. The feed rate of the admixture and the feed rate of the liquid fed by the submersible pump 30 can be controlled.
  • the fluctuation range of the supply amount of the mixing material controlled to be the set supply amount by the control means 50 is 3% by mass or less And preferably less than 2% by weight. Furthermore, the fluctuation range of the liquid supply amount controlled to be the set supply amount by the control means 50 can be 2 mass% or less, preferably 1 mass% or less.
  • the fluctuation range of the supply amount of the miscible material controlled to be the set supply amount by the control means 50 can be 3% by mass or less, and the liquid controlled to be the set supply amount by the control means 50
  • the control method of the control means is not limited to the control method by the calibration described above as long as the fluctuation range of the supply amount can be made 2 mass% or less.
  • the supply amount of the mixing material and the liquid of the mixing material so that the supply amount of the mixing material and the supply amount of the liquid become the set supply amount.
  • the supply amount may be controlled.
  • the slurry producing means 10 first, only the liquid is supplied to the slurry producing means 10 while measuring the supply amount of the liquid using the measuring means 40, and the supply of the liquid is stopped when the supply amount of the liquid reaches the set supply amount.
  • the admixture is supplied to the slurry production means 10 while supplying the liquid and measuring the feed of the admixture using the measuring means 40, and when the feed of the admixture reaches the set feed, Stop the supply of admixtures. Then, mixing of the admixture and the liquid is started. In this case, the admixture may be supplied first, and then the liquid may be supplied.
  • the pumping means 60 supplies the admixture material slurry 4 produced by the slurry production means 10 to the pumping hose 61.
  • the pumping means 60 is, for example, a pumping pump 60 (see FIG. 1).
  • the pressure feed pump 60 can supply the slurry produced by the slurry production apparatus 10 to the concrete conveyance means 70 separated by, for example, 50 to 100 m via the pressure feed hose 61. Thereby, even if the distance between the slurry production means 10 and the concrete conveyance means 70 is large, the admixture material slurry produced by the slurry production means 10 can be supplied to the storage and stirring mechanism 71 of the concrete conveyance means 70.
  • the pressure pump 60 Since the slurry produced by the slurry production apparatus 10 is pressureless or low pressure, the pressure pump 60 needs a pressure capacity sufficient to be supplied to a remote place via the pressure feed hose 61.
  • a known snake pump can be used as the pressure feed pump 60.
  • the pumping means is not limited to the pumping pump 60 as long as the admixture slurry produced by the slurry production means can be supplied to the pumping hose.
  • the pumping means may be a piston pump or a squeeze pump.
  • the concrete transport means 70 has a storage and stirring mechanism 71 for storing and stirring concrete.
  • the concrete transport means 70 is, for example, an agitator car 70 (see FIG. 1).
  • the agitator wheel 70 has a mixer drum 71 for storing and stirring concrete.
  • the mixer drum 71 is internally provided with a spiral blade, and when the mixer drum 71 rotates, the concrete stored in the mixer drum 71 is agitated.
  • the concrete conveyance means is not limited to the agitator vehicle 70 as long as it has a storage and stirring mechanism 71 for storing and stirring concrete.
  • the concrete transport means may be a track mixer.
  • the admixture slurry is supplied to the storage and agitation mechanism 71 through the pressure feed hose 61.
  • the stirring function of the storage and stirring mechanism 71 the admixture material slurry can be uniformly mixed with the concrete stored in the storage and stirring mechanism 71.
  • the time from supply of the liquid or admixture to the slurry production means 10 to supply of the admixture slurry to the storage and agitation mechanism 71 is preferably 7 Within minutes, more preferably within 5 minutes.
  • the mixture production system 1 in an embodiment of the present invention can be modified as follows.
  • the mixture generation system 1A in the first modification of the mixture generation system 1 includes a retarder water storage unit 150 for storing the retarder water 5 and the retarder water 5.
  • the apparatus further comprises a retarder water pressure feeding means 160 for feeding the agent water pressure feeding hose 161, and then using the delaying agent water pressure feeding means 160, the delaying agent water 5 May be supplied to the storage and agitation mechanism 71, and the storage and agitation mechanism 71 may be cleaned by the retarder water 5.
  • the storage and agitation mechanism 71 can be cleaned while suppressing the setting of concrete remaining in the storage and agitation mechanism 71, so that the storage and agitation mechanism 71 can be cleaned cleanly.
  • the storage and stirring mechanism 71 can be cleaned also from this point.
  • the retarder water storage means 150 stores the retarder water 5.
  • the retarder water storage means 150 is, for example, a retarder water storage tank 150 (see FIG. 4).
  • the retarder water storage means is not limited to the retarder water storage tank 150 as long as it can store the retarder water.
  • retarder water storage means 150 may be provided with retarder water supply means 151 such as a submersible pump. Good.
  • the retarder water 5 is water containing a retarder.
  • the retarder used for the retarder water 5 include inorganic retarders and organic retarders.
  • Inorganic retarders for example, phosphates, silicofluorides, complexes of silicofluorides and phosphates, copper hydroxide, boric acid, zinc oxide, zinc chloride, mixtures of zinc carbonate and lead oxide And mixtures of copper carbonate and urea.
  • organic retarders include, for example, oxycarboxylic acids and salts thereof, ketocarboxylic acids, aldose acids, uronic acids, ketose acids, saccharides, sugar alcohols, cellulose derivatives, water-soluble polymers such as polyvinyl alcohol and the like Etc.
  • the retarder water pressure feeding means 160 supplies the retarder water 5 to the retarder water pressure feed hose 161.
  • the retarder water pressure feeding means 160 is, for example, a pressure feeding pump 160 (see FIG. 4).
  • the pressure pump 160 supplies retarder water stored in the retarder water storage tank 150 to the concrete conveyance means 70 separated by, for example, 50 to 100 m via the retarder water pressure feed hose 161. Thereby, even if the distance between the slurry production means 10 and the concrete conveyance means 70 is somewhat large, the storage and stirring mechanism 71 of the concrete conveyance means 70 can be cleaned cleanly.
  • the pressure pump 160 Since the retarder water stored in the retarder water storage tank 150 is pressureless or low pressure, the pressure pump 160 needs sufficient pressurizing ability to be supplied to a remote place via the pressure hose 161. .
  • a known snake pump can be used as the pressure feed pump 160.
  • the retarder water pressure feeding means is not limited to the pressure feed pump 160 as long as the delay agent water stored in the delay agent water storage tank 150 can be supplied to the pressure feed hose.
  • the retarder water pressure delivery means may be a piston pump or a squeeze pump.
  • the pumping means 60 may be used as the retarder water pressure feeding means 160.
  • a retarder water sprayer 162 may be provided at the end of the pressure-feed hose.
  • the retarder water spray machine 162 mixes the retarder water and compressed air which were supplied from the pumping hose 161 by the nozzle not shown, and injects the mixture of retarder water and compressed air.
  • the human is operating the retarder water spray machine 162, it can also operate mechanically and automatically.
  • a mixture generation system 1B according to a second modification of the mixture generation system 1 according to an embodiment of the present invention supplies the liquid storage means 31 for storing liquid and the power for driving the control means 50.
  • the means other than the concrete conveyance means 70 may be mounted on the same movable carriage 200.
  • the main means of the mixture generation system 1B can be easily transported, and the flexibility of the mixture generation system 1B can be enhanced.
  • the moving carriage 200 is a truck 200 in this example, but it may be a trailer or a simple carriage.
  • the movable carriage 200 has thereon slurry producing means 10, admixture material supplying means 20, liquid supply means 30, liquid storage means 31, measuring means 40, control means 50, retarder water storage means 150 and power supply.
  • the means 170 is mounted.
  • all of the means other than the concrete conveyance means may be mounted on the same movable carriage 200, and of the means constituting the mixture generation system other than the concrete conveyance means A part may be mounted on the same movable carriage 200.
  • the liquid storage means is not limited to the liquid storage means 31 shown in FIGS. 1 and 5 as long as it can store liquid.
  • the power supply unit 170 may be a generator or a battery as long as it can supply power for driving the control unit 50.
  • Powder 1 to 8 Powder 1 Calcium hydroxide, commercial product, less than 1% of 300 ⁇ m residue, 5% of 100 ⁇ m residue
  • Powder 2 Calcium carbonate, commercial product, Blaine specific surface area 4,000 cm 2 / g
  • Powder 3 Alumina cement No. 1 mainly composed of calcium aluminate compound and CaO ⁇ Al 2 O 3 .
  • Brain specific surface area 5,000 cm 2 / g Powder 4 An expanding material for concrete, which is produced by heat treating a mixture containing a calcium sulfoaluminate compound, CaO raw material and CaSO 4 raw material, a commercial product, Blaine specific surface area 3,600 cm 2 / g Powder 5: calcium silicate compound, 3CaO ⁇ SiO 2 synthesized from calcium carbonate and SiO 2 of the reagent first grade.
  • Brain specific surface area 3,000 cm 2 / g Powder 6 Portland cement
  • commercial product Powder 7 calcium sulfoaluminate cement
  • Blaine specific surface area 4,500 cm 2 / g Powder 8 Blast furnace slag, commercial item
  • ⁇ Mixture supply system Inner diameter of casing: 250 mm
  • the fluctuation range of measured value of powder and liquid supplied to the slurry production apparatus is 2 mass% or less, preferably 1 mass% in liquid. It became as follows, and it became 3 mass% or less with a powder, Preferably it became 2 mass%, and it turned out that quantitative efficiency is securable.
  • the slurry is manufactured and manufactured batchwise by changing the time (stirring time) from the supply of powder and liquid using the mixture generation system 1 according to one embodiment of the present invention to the completion of the 20-liter slurry
  • the slurry properties were confirmed.
  • the water powder ratio was 50% in all cases, and the stirring time was 30 seconds, 60 seconds, 90 seconds, and 120 seconds.
  • By passing the stirred slurry through a 5 mm sieve it was confirmed whether or not a powdery lump not completely dispersed in the slurry was present.
  • the results are shown in Table 2.
  • a grout mixer “OKZ-30” (model number) manufactured by Okasan Kiko Co., Ltd. was used as a slurry production means.
  • the slurry can be applied to the agitator car within 5 minutes after supplying the powder to the slurry production apparatus, regardless of which powder is used. It turned out that it can supply.
  • the mixer drum of the agitator car was rotated at high speed for 2 minutes, and then the concrete was discharged. From the concrete in the middle of discharge, immediately after the start of discharge, at the time of discharge of 1/2 of the load of concrete, and at the end of discharge, sampling was performed three times to prepare a concrete sample.
  • the compressive strength (in accordance with JIS A 1108) and the rate of change in length (in accordance with JIS A 6202) were measured for this concrete sample. Further, the surface condition of the hardened concrete was confirmed, and it was confirmed whether the expansive material of the powder 4 was uniformly dispersed in the concrete uniformly by only stirring the mixer drum of the agitator wheel.
  • the test was also performed in the case where the expansive material of the powder 4 was added to the agitator car so as to be 20 kg / m 3 as the powder as it is.
  • the concrete prior to the addition of the expansive material was adjusted to be the same water binder as in the case of the slurry addition, and the mixing method after the addition of the expansive material was the same as the case of the slurry addition.
  • the concrete composition of this test is shown in Table 4. Also, the results are shown in Table 5.
  • a grout mixer “OKZ-30” (model number) manufactured by Okasan Kiko Co., Ltd. was used as a slurry production means.
  • mixture generation system 1 of one embodiment of the present invention highly fluid concrete, grout (mortar / concrete), high strength / super high strength concrete, high durability concrete, seawater resistant concrete, acid resistant concrete, It turned out that it is possible to easily manufacture special concrete in which admixture materials such as abrasion resistant concrete, underwater non-separable concrete, mass concrete, reverse cast concrete, shot concrete and porous concrete are mixed.
  • admixture materials such as abrasion resistant concrete, underwater non-separable concrete, mass concrete, reverse cast concrete, shot concrete and porous concrete are mixed.
  • dispersion in concrete is not sufficiently performed, and it is confirmed that the dispersion is partially biased.

Landscapes

  • Engineering & Computer Science (AREA)
  • Architecture (AREA)
  • Mechanical Engineering (AREA)
  • Structural Engineering (AREA)
  • Chemical & Material Sciences (AREA)
  • Dispersion Chemistry (AREA)
  • Civil Engineering (AREA)
  • Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)
  • On-Site Construction Work That Accompanies The Preparation And Application Of Concrete (AREA)

Abstract

La présente invention concerne un système de formation de mélange (1) comprenant : un moyen de production de suspension (10) qui produit un mélange sous forme de suspension ; un moyen d'alimentation en mélange (20) qui fournit un mélange ; un moyen d'alimentation en liquide (30) qui fournit un liquide ; un moyen de mesure (40) qui mesure les quantités fournies du mélange et du liquide ; un moyen de réglage (51) qui règle les quantités fournies du mélange et du liquide ; un moyen de commande (50) qui commande les quantités fournies du mélange et du liquide ; un moyen d'introduction sous pression (60) qui fournit le mélange sous forme de suspension à un tuyau souple d'introduction sous pression (61) ; et un moyen de transport de béton (70) qui possède un mécanisme de stockage/agitation(71) qui stocke et agite un béton. La plage de fluctuation de la quantité fournie du mélange est inférieure ou égale à 3 % en masse ; la plage de fluctuation de la quantité fournie du liquide est inférieure ou égale à 2 % en masse ; et le mélange sous forme de suspension est fourni au mécanisme de stockage/malaxage (71). Par conséquent, la présente invention permet d'obtenir un système de formation de mélange permettant de mélanger efficacement un mélange sous forme de poudre avec un béton prêt à l'emploi qui a été transporté sur un chantier de construction au moyen d'un véhicule agitateur.
PCT/JP2018/041333 2017-11-22 2018-11-07 Système de formation de mélange WO2019102850A1 (fr)

Priority Applications (2)

Application Number Priority Date Filing Date Title
CN201880074481.7A CN111356564A (zh) 2017-11-22 2018-11-07 混合物生成系统
JP2019555246A JP7145171B2 (ja) 2017-11-22 2018-11-07 混合物生成システム

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2017224137 2017-11-22
JP2017-224137 2017-11-22

Publications (1)

Publication Number Publication Date
WO2019102850A1 true WO2019102850A1 (fr) 2019-05-31

Family

ID=66631716

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/JP2018/041333 WO2019102850A1 (fr) 2017-11-22 2018-11-07 Système de formation de mélange

Country Status (3)

Country Link
JP (1) JP7145171B2 (fr)
CN (1) CN111356564A (fr)
WO (1) WO2019102850A1 (fr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2021017360A (ja) * 2019-07-23 2021-02-15 デンカ株式会社 低粉塵化連続混練システム
JP2021160186A (ja) * 2020-03-31 2021-10-11 太平洋マテリアル株式会社 粉末混和材料のスラリー化供給装置
CN113789787A (zh) * 2021-09-08 2021-12-14 张国青 一种水利工程施工用灌浆装置
CN114535285A (zh) * 2022-03-11 2022-05-27 湖北理工学院 污染耕地田间原位稳定化修复中试设备

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN112171904B (zh) * 2020-10-19 2021-07-27 中启胶建集团有限公司 一种混凝土搅拌防凝固器

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61230909A (ja) * 1985-04-08 1986-10-15 石川島播磨重工業株式会社 連続ミキサーに対する材料の供給方法
JPH10296714A (ja) * 1997-04-24 1998-11-10 Denka Grace Kk 生コンスラッジの再使用方法及び装置
JPH10315220A (ja) * 1997-05-20 1998-12-02 Kajima Corp バッチャープラントへのスラリー添加装置
JP2002028920A (ja) * 2000-07-17 2002-01-29 Sumitomo Osaka Cement Co Ltd コンクリートの製造方法および製造装置
JP2007331265A (ja) * 2006-06-15 2007-12-27 Mcm:Kk モルタル連続練り装置とこれを用いた連続練りシステム
JP2010058430A (ja) * 2008-09-05 2010-03-18 Okasan Kiko Kk 土木建築材料用ミキサ及びその攪拌羽根

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101462310B (zh) * 2008-12-03 2010-06-23 徐州天地重型机械制造有限公司 一种干混砂浆站
CN103072206A (zh) * 2011-12-31 2013-05-01 河北建设集团有限公司 沥青混凝土拌和站粉尘的可控加湿搅拌装置及方法
CN102848466A (zh) * 2012-03-22 2013-01-02 江苏尼高科技有限公司 一种移动式预拌干混砂浆生产装置
CN203092781U (zh) * 2013-02-27 2013-07-31 中联重科股份有限公司 移动式砂浆搅拌站

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61230909A (ja) * 1985-04-08 1986-10-15 石川島播磨重工業株式会社 連続ミキサーに対する材料の供給方法
JPH10296714A (ja) * 1997-04-24 1998-11-10 Denka Grace Kk 生コンスラッジの再使用方法及び装置
JPH10315220A (ja) * 1997-05-20 1998-12-02 Kajima Corp バッチャープラントへのスラリー添加装置
JP2002028920A (ja) * 2000-07-17 2002-01-29 Sumitomo Osaka Cement Co Ltd コンクリートの製造方法および製造装置
JP2007331265A (ja) * 2006-06-15 2007-12-27 Mcm:Kk モルタル連続練り装置とこれを用いた連続練りシステム
JP2010058430A (ja) * 2008-09-05 2010-03-18 Okasan Kiko Kk 土木建築材料用ミキサ及びその攪拌羽根

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2021017360A (ja) * 2019-07-23 2021-02-15 デンカ株式会社 低粉塵化連続混練システム
JP2021160186A (ja) * 2020-03-31 2021-10-11 太平洋マテリアル株式会社 粉末混和材料のスラリー化供給装置
JP7368680B2 (ja) 2020-03-31 2023-10-25 太平洋マテリアル株式会社 粉末混和材料のスラリー化供給装置
CN113789787A (zh) * 2021-09-08 2021-12-14 张国青 一种水利工程施工用灌浆装置
CN114535285A (zh) * 2022-03-11 2022-05-27 湖北理工学院 污染耕地田间原位稳定化修复中试设备
CN114535285B (zh) * 2022-03-11 2023-09-22 湖北理工学院 污染耕地田间原位稳定化修复中试设备

Also Published As

Publication number Publication date
CN111356564A (zh) 2020-06-30
JPWO2019102850A1 (ja) 2020-12-03
JP7145171B2 (ja) 2022-09-30

Similar Documents

Publication Publication Date Title
WO2019102850A1 (fr) Système de formation de mélange
US11130714B2 (en) Post-batching CMA dosing into concrete
US3967815A (en) Dustless mixing apparatus and method for combining materials
CN107457907B (zh) 改进的建筑混凝土搅拌系统
JP2006298662A (ja) グラウト組成物及びグラウトスラリーの施工方法
CN105922449B (zh) 一种多搅拌罐式混凝土生产装置
CN108748685A (zh) 一种预拌混凝土生产系统
JP5895625B2 (ja) モルタルの施工方法
CN219882898U (zh) 工业废渣制备混凝土的配料系统
CN209665846U (zh) 一种预拌混凝土生产系统
JP2009096040A (ja) 水硬性モルタルの連続施工方法およびその構造体
GB2098264A (en) Method and apparatus for applying mortar or concrete
JP2003191224A (ja) 生コンクリートの製造方法および製造装置
JP2024501409A (ja) コンクリート、特に高初期強度コンクリートを製造するための装置及び方法
CN116648302A (zh) 制造混凝土、尤其具有高早期强度的混凝土的装置和方法
JPH0796219B2 (ja) 生コンクリ−ト類の製造装置
JP5283849B2 (ja) 耐火物の連続混練方法、耐火物の連続施工方法、耐火物の連続混練装置、及び耐火物の連続施工装置
RU2701003C1 (ru) Модульный завод по производству растворобетонных смесей
JP3780499B2 (ja) 連続混練方法及びその装置
JP7281028B1 (ja) 練り混ぜ装置および練り混ぜ方法
JP3736990B2 (ja) 粉末状水硬性材料の連続混練装置
JPH1086133A (ja) コンクリート等の製造方法
CN219726736U (zh) 一种水泥预拌装置
JP5775834B2 (ja) 鉄鋼スラグ水和固化体の製造方法および固化する前の鉄鋼スラグ水和固化体の混練物の製造装置
JP2017196564A (ja) 連続式団粒化撹拌装置

Legal Events

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

Ref document number: 18881771

Country of ref document: EP

Kind code of ref document: A1

ENP Entry into the national phase

Ref document number: 2019555246

Country of ref document: JP

Kind code of ref document: A

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 18881771

Country of ref document: EP

Kind code of ref document: A1