WO2017143384A1 - Procédé de fabrication de plâtre expansé - Google Patents
Procédé de fabrication de plâtre expansé Download PDFInfo
- Publication number
- WO2017143384A1 WO2017143384A1 PCT/AU2017/000051 AU2017000051W WO2017143384A1 WO 2017143384 A1 WO2017143384 A1 WO 2017143384A1 AU 2017000051 W AU2017000051 W AU 2017000051W WO 2017143384 A1 WO2017143384 A1 WO 2017143384A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- powder
- venturi
- phosphoric acid
- plaster
- supply
- Prior art date
Links
- 239000011505 plaster Substances 0.000 title claims abstract description 23
- 238000000034 method Methods 0.000 title claims abstract description 21
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 9
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims abstract description 26
- 239000000843 powder Substances 0.000 claims abstract description 23
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims abstract description 13
- 239000007921 spray Substances 0.000 claims abstract description 13
- 238000005266 casting Methods 0.000 claims abstract description 8
- 238000000465 moulding Methods 0.000 claims abstract description 3
- 239000000203 mixture Substances 0.000 claims description 9
- 230000005484 gravity Effects 0.000 claims description 6
- 240000000907 Musa textilis Species 0.000 claims description 5
- 239000002253 acid Substances 0.000 claims description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 4
- 239000000463 material Substances 0.000 description 3
- 229910000019 calcium carbonate Inorganic materials 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 235000019738 Limestone Nutrition 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000010419 fine particle Substances 0.000 description 1
- 239000006260 foam Substances 0.000 description 1
- 229920001903 high density polyethylene Polymers 0.000 description 1
- 239000004700 high-density polyethylene Substances 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000013618 particulate matter Substances 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000012254 powdered material Substances 0.000 description 1
- 239000011369 resultant mixture Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B28—WORKING CEMENT, CLAY, OR STONE
- B28C—PREPARING CLAY; PRODUCING MIXTURES CONTAINING CLAY OR CEMENTITIOUS MATERIAL, e.g. PLASTER
- B28C5/00—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions
- B28C5/02—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions without using driven mechanical means effecting the mixing
- B28C5/06—Apparatus or methods for producing mixtures of cement with other substances, e.g. slurries, mortars, porous or fibrous compositions without using driven mechanical means effecting the mixing the mixing being effected by the action of a fluid
-
- 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
- B01F25/421—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 by moving the components in a convoluted or labyrinthine path
- B01F25/423—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 by moving the components in a convoluted or labyrinthine path by means of elements placed in the receptacle for moving or guiding the components
- B01F25/4231—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 by moving the components in a convoluted or labyrinthine path by means of elements placed in the receptacle for moving or guiding the components using baffles
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B11/00—Calcium sulfate cements
- C04B11/02—Methods and apparatus for dehydrating gypsum
Definitions
- the present invention relates to a method for the manufacture of foamed plaster.
- the present invention attempts to overcome at least in part, the disadvantages of previously known methods for the manufacture of foamed plaster
- a method for the manufacture of foamed plaster which comprises feeding powdered casting plaster from a supply thereof to a Venturi apparatus, feeding the powder from the Venturi apparatus to a supply of phosphoric acid admixing the powder and phosphoric acid, and forwarding the resulting mixture to a dispensing and spray head so as to feed the mixture to a moulding means.
- Figure 1 is a schematic diagram of an apparatus for putting the method of the present invention into practice.
- Figure 2 is a view of a compressed air supply
- Figure 3 is a schematic side view of air being fed to a Venturi apparatus.
- Figure 4 is a view of a spray head which may form part of the present invention.
- Figure 5 is a cross section of the spray head of Figure 4.
- the present invention provides a method and apparatus comprising a feed means (10) for powdered material which powder to a platform (14) under the influence of gravity.
- the feed means (10) is provided with a vibrating means (11) to ensure a steady flow of material to the vibrating platform (14) in use.
- the vibrating platform (14) is arranged to feed the powder towards a Venturi apparatus (16).
- the supply of powder feed may consist of about 93 per cent by weight of casting plaster with the balance of about 7 per cent of powdered limestone.
- a compressed air supply (18) is arranged to provide a flow of air to draw in 25-50mm such as 40mm between the output of the compressed air supply (18) and the adjacent input end of the Venturi apparatus (16).
- the powdered plaster falls from the platform (14) under the influence of gravity. This powdered plaster becomes entrained in the air flow from the compressor of the compressed air supply (18) and is fed into the Venturi apparatus (16) as shown
- the platform (14) is part of a vibrating feeder of known type which is designed to provide a steady flow rate of powder to the Venturi (16).
- the flow rate can be adjusted by means of a rheostat control. Variation of the vibration of the platform (14) urges the powder on the platform (14) to move forwardly to the right as seen in Figure 1.
- a separate compressed air supply (20) is provided adjacent a narrow end on the Venturi (16). As shown in Figure 3, the air supply (20) is directed towards the wider end of the Venturi (16).
- the wider end of the Venturi (16) is connected to an elongated chemical tube (22).
- the tube (22) may be formed of a suitable plastics material.
- the tube (22) is connected to an elbow (24) remote from the Venturi (16).
- the elbow (24) may be formed of a high-density polyethylene having an internal diameter of 65mm
- the 135% elbow (24) is provided with an inlet nozzle (26) arranged to receive dilute phosphoric acid. Further, the 135% elbow (24) is connected to a length of chemical tape (28). The phosphoric acid is sprayed into the elbow (24) to produce a mixture of the acid and the powder from the Venturi (16). The hose (28) delivers the phosphoric acid and plaster mixture to a mixing and spray head (40) via a further elbow 30 which has an inlet (31) for further compressed ait to ensure steady flow in the spray head (40).
- a quantity of manila hemp fibres may be added to the material being processed.
- the manila hemp fibres are preferably less than 4mm in length.
- the use of manila hemp fibre is found to increase the strength of the resultant products whilst keeping the weight down.
- the resultant products may have specific gravity of less than 0.4. It has been found that the Venturi system described above works well with the manila hemp but requires the addition of the air supply (18) to transfer the powder to the Venturi.
- the Venturi apparatus (16) has a relatively narrow end adjacent to the air supply (18) and a relatively wide end remote from the air supply (18).
- the narrow end could be 30mm in diameter whilst the wide end could be 65mm in diameter.
- the air supply (18) may have an outlet plate with a plurality of apparatus (36) which ensure that a high velocity air flow is provided to transfer the powder into the Venturi (16).
- FIG. 4 and 5 of the accompanying drawings there is shown a mixing and spray head (40) comprising a tubular member (42) having an inlet end (44) and an outlet end (46).
- the tubular member (42) is connected to a hose (28).
- the tubular member (42) has mounted thereto an outlet nozzle (48).
- tubular member (42) contains spaced apart mixing baffle members (41) and (43).
- the baffles (41) and (43) are arranged to induce turbulence in the tubular member (42) in use.
- the baffle member (41) extends from one side of the tubular member (42) whilst the baffle member (43) extends from an opposite side of the tubular member (42).
- the flow of air is initially interrupted by the baffle (41) and then returns to the full diameter section of the tubular member (42). Subsequently the flow of air encounters the baffle (43) and is again interrupted and then returns to the full diameter of the tubular member (42).
- the result is that the flow of air is subject to variable back eddy currents.
- the baffle member (41) blocks flow in part of the elongated member (42) which tends to throw air pressure sideways.
- the baffle member (43) is of similar shape is therefore desirable to give an opposing throw to balance the elongate member (42) in use.
- the baffles (41) and (43) have an effect on the elongated member for about 180 degrees. These could be replaced by three balanced baffles set at 120 degrees or four balanced baffles set at 90 degrees.
- a mixture of casting plaster with calcium carbonate is entrained in the flow of air the hose (18) prior to entering the tubular member (42).
- tubular member (42) it is desirable to induce shear in the mix. This could be achieved for example, by altering the shape of the baffles to give differential flow on one side thus tending to mix the for and after flow of the particulate matter. This enables a fraction of the flow to move forward and to be realigned with the Coriolis Effect to give a twist and provide stability to the outgoing jet of slurry. In that regard, results of tests in the Southern Hemisphere would require adj ustment to the mirror image in the Northern Hemisphere.
- the airspeed through the mixing and spray head (40) should preferably be at least 200 km per hour to keep the fine particles in suspension. Further, frictional losses in pipes of less than 50 mm diameter tend to restrict the distance carried. Tests with pipe lengths of 3 to 5 meters have been carried out with pipes of 21 ⁇ 2 inch internal diameter which corresponds to about 56mm.
- a nozzle (50) preferably provides a restricted outlet about 0.6 to 0.8 of the diameter of the tubular member (42) At the nozzle (50) particulate foamed plaster is ejected from the tubular member (42). Further, a preferred option is to provide a small water spray adjustment (49) at the spray head (40) to ensure that the resultant mixture has sufficient moisture content if required.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Structural Engineering (AREA)
- Ceramic Engineering (AREA)
- Dispersion Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Mechanical Engineering (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Nozzles (AREA)
Abstract
L'invention concerne un procédé de fabrication de plâtre expansé dans lequel de la poudre contenant une grande proportion de plâtre à mouler est introduite dans un appareil Venturi, et est ensuite mélangée à de l'acide phosphorique puis introduite dans une tête de pulvérisation de distribution devant être introduite dans un moyen de moulage.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AU2016900629A AU2016900629A0 (en) | 2016-02-23 | Mixing & Spray Head | |
AU2016900629 | 2016-02-23 |
Publications (1)
Publication Number | Publication Date |
---|---|
WO2017143384A1 true WO2017143384A1 (fr) | 2017-08-31 |
Family
ID=59684669
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
PCT/AU2017/000051 WO2017143384A1 (fr) | 2016-02-23 | 2017-02-22 | Procédé de fabrication de plâtre expansé |
Country Status (1)
Country | Link |
---|---|
WO (1) | WO2017143384A1 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020010381A1 (fr) * | 2018-07-11 | 2020-01-16 | Edgar Donald Knott | Procédé et appareil pour la fabrication de plâtre expansé |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1585065A (en) * | 1976-07-26 | 1981-02-25 | Bpb Industries Ltd | Treatment of gypsum plaster |
US5393341A (en) * | 1991-06-06 | 1995-02-28 | Rume Maschinenbau Gmbh | Method and apparatus for the production of structural foam, particularly cement foam |
US20040201120A1 (en) * | 2003-01-31 | 2004-10-14 | Lafarge North America, Inc. | Gypsum wallboard process |
US7678189B2 (en) * | 2005-01-07 | 2010-03-16 | Edgar Donald Knott | Foaming plaster |
-
2017
- 2017-02-22 WO PCT/AU2017/000051 patent/WO2017143384A1/fr active Application Filing
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1585065A (en) * | 1976-07-26 | 1981-02-25 | Bpb Industries Ltd | Treatment of gypsum plaster |
US5393341A (en) * | 1991-06-06 | 1995-02-28 | Rume Maschinenbau Gmbh | Method and apparatus for the production of structural foam, particularly cement foam |
US20040201120A1 (en) * | 2003-01-31 | 2004-10-14 | Lafarge North America, Inc. | Gypsum wallboard process |
US7678189B2 (en) * | 2005-01-07 | 2010-03-16 | Edgar Donald Knott | Foaming plaster |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2020010381A1 (fr) * | 2018-07-11 | 2020-01-16 | Edgar Donald Knott | Procédé et appareil pour la fabrication de plâtre expansé |
AU2018431621B2 (en) * | 2018-07-11 | 2020-07-23 | Edgar Donald Knott | A method and apparatus for the manufacture of foamed plaster |
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