CN209224277U - A kind of recycle device for concrete tubular pile remaining slurry - Google Patents
A kind of recycle device for concrete tubular pile remaining slurry Download PDFInfo
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- CN209224277U CN209224277U CN201821290923.5U CN201821290923U CN209224277U CN 209224277 U CN209224277 U CN 209224277U CN 201821290923 U CN201821290923 U CN 201821290923U CN 209224277 U CN209224277 U CN 209224277U
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- magma
- remaining slurry
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Abstract
The utility model discloses a kind of recycle device for concrete tubular pile remaining slurry, remaining slurry storage tank compounds tank with remaining slurry and is connected；Water tank is connected with above remaining slurry compounding tank；Remaining slurry compounds tank lower left and is equipped with retarder tank, and retarder tank bottom end is connected by discharge nozzle with gas-solid mixing room, and gas-solid mixing room left end is connected with air blower, and gas-solid mixing room right end compounds tank top with remaining slurry by gas-solid mixing pipe and is connected；Remaining slurry compounds left part in tank and is equipped with shaft, and shaft top is fixed with spherical stock guide；Remaining slurry compounds bottom in tank and is equipped with the first dredge pump, and the first dredge pump is connected by the first magma pipe with magma storage tank top, is connected by the first branch pipe with the first magma return pipe in the middle part of the first magma pipe；Bottom is equipped with the second dredge pump in magma storage tank, and the second dredge pump is connected by the second magma pipe with concrete mixer, is connected by the second branch pipe with the second magma return pipe in the middle part of the second magma pipe.The utility model can be to remaining slurry effective recycling, and can save the energy.
Description
Technical field
The utility model belongs to concrete tubular pile production technical field, in particular to a kind of for concrete tubular pile remaining slurry
Recycle device.
Background technique
PHC tubular pole is because having structural strength is high, injection is good, resistance to hammering property is strong, structural bearing capacity is high, cost performance is high etc.
Feature is widely applied rapidly in high-strength building.PHC tubular pole processing and fabricating overstocks closely knit, meeting using a kind of centrifugation
Part remaining slurry (its main component is water, cement, fine sand, dirt etc.) is generated, this brings larger to tubular pole manufacturing enterprise
Difficulty, currently, many tubular pole manufacturers processing remaining slurry method be using remaining slurry produce byproduct, such as the curb of road
Stone, hollow brick etc., or discharged to vacant lot, waste processing, this should spend biggish financial resources and manpower, also will cause two secondary environments
Pollution.
Utility model content
The utility model provides a kind of recycle device for concrete tubular pile remaining slurry, can be to tubular pole processing and fabricating institute
The remaining slurry of generation is effectively recycled, and is not needed to compound in tank and magma storage tank in remaining slurry and installed blender, thus
The energy can be saved.
In order to solve the above-mentioned technical problem, the utility model adopts the following technical solution:
A kind of recycle device for concrete tubular pile remaining slurry, including remaining slurry storage tank, remaining slurry storage tank by pacifying thereon
The remaining slurry pipe for filling the first pneumatic operated valve and the first mass flowmenter compounds upper end with remaining slurry and is connected, and remaining slurry pipe end protrudes into remaining slurry
It compounds in tank, remaining slurry compounds tank deck end opening；Remaining slurry compounds and is equipped with water tank above tank, and water tank bottom end by installing the second gas thereon
The water pipe of dynamic valve and the second mass flowmenter compounds upper end with remaining slurry and is connected, and water pipe bottom end is protruded into remaining slurry compounding tank；Remaining slurry
It compounds tank lower left and is equipped with retarder tank, retarder tank bottom end passes through the discharge nozzle that the first valve is arranged thereon and gas-solid mixing room
It is connected, gas-solid mixing room left end is connected by tracheae with air blower, and gas-solid mixing room right end by installing solid flowmeter thereon
And that tank top is compounded with remaining slurry is connected for the gas-solid mixing pipe that protrudes into remaining slurry compounding tank of top；Left part is equipped with perpendicular in remaining slurry compounding tank
Straight shaft, shaft top are fixed with the spherical stock guide that upper end raises upward, and gas-solid mixing tube top end is in spherical stock guide
Upper left side, remaining slurry pipe end are in right above spherical stock guide, and water pipe bottom end is in spherical stock guide upper right side；Remaining slurry compounds tank
Interior bottom is equipped with the first dredge pump, and the first dredge pump by installing the first of third mass flowmenter and third pneumatic operated valve thereon
Magma pipe is connected with magma storage tank top, and the first magma pipe end protrudes into magma storage tank, by thereon in the middle part of the first magma pipe
The first branch pipe for installing the 4th pneumatic operated valve is connected with the first magma return pipe for installing the 4th mass flowmenter thereon, the first magma
Reflux pipe end protrudes into remaining slurry compounding tank, and internal diameter of the first magma return pipe from head end to end gradually becomes smaller；Magma storage tank
Interior bottom is equipped with the second dredge pump, and the second dredge pump by installing the second of the 5th mass flowmenter and the 5th pneumatic operated valve thereon
Magma pipe is connected with concrete mixer, by the second branch pipe of the 6th pneumatic operated valve of installation thereon and thereon in the middle part of the second magma pipe
The the second magma return pipe for installing the 6th mass flowmenter is connected, and the second magma reflux pipe end protrudes into magma storage tank, and second
Internal diameter of the magma return pipe from head end to end gradually becomes smaller.
Further, internal diameter of the first magma pipe from head end to end gradually becomes smaller.
Further, internal diameter of the remaining slurry pipe from head end to end gradually becomes smaller；Internal diameter of the water pipe from top to bottom end is gradually
Become smaller.
Further, rotation is driven by motor in shaft, and motor is fixedly installed in remaining slurry compounding tank, and the output shaft of motor
It is vertically arranged, motor output shaft is connected by shaft coupling with shaft, and waterproof layer is coated with outside motor and shaft coupling.
Further, the retarder in retarder tank is sodium gluconate.
Further, gas-solid mixing tube top end uniformly extends to the outside, and then forms positive cone shape.
Further, remaining slurry compounding tank bottom end is connected with the first outlet tube, and the second valve is equipped on the first outlet tube.
Further, magma storage tank bottom end is connected with the second outlet tube, and third valve is equipped on the second outlet tube.
Further, air blower is Roots blower.
Further, third mass flowmenter is in the upstream position of the first branch pipe, and the 5th mass flowmenter is in the
The upstream position of two branch pipes.
Compared with the existing technology, the utility model has the following beneficial effects:
1, the first dredge pump is connected by the first magma pipe with magma storage tank top in the utility model, in the first magma pipe
Portion is connected by the first branch pipe with the first magma return pipe, and the first magma reflux pipe end protrudes into remaining slurry compounding tank, and first is former
It starches internal diameter of the return pipe from head end to end to gradually become smaller, the magma in such first magma return pipe can be with biggish impact force
Impact flows back into remaining slurry compounding tank, which can make the magma in remaining slurry compounding tank be constantly in agitated conditions, Jin Erneng
Remove stirring homogenization process from；And left part is equipped with vertical shaft in remaining slurry compounding tank in the utility model, and shaft top is fixed
There is the spherical stock guide that upper end raises upward, gas-solid mixing tube top end is in spherical stock guide upper left side, and remaining slurry pipe end is in
Right above spherical stock guide, water pipe bottom end is in spherical stock guide upper right side, falls on the slow setting on spherical guide plate top surface in this way
Agent, remaining slurry and water can be rotated with the rotation of spherical stock guide, and then retarder, remaining slurry and water can be promoted to be uniformly mixed, together
When due to gas-solid mixing pipe, remaining slurry pipe remaining slurry compounding tank opposite with water pipe it is static, and spherical stock guide is with respect to remaining slurry compounding tank turn
Dynamic, such retarder, remaining slurry and water can fall on down the different location of spherical stock guide, so as to keep retarder, remaining slurry and water mixed
It closing more uniformly, and internal diameter of the remaining slurry pipe from head end to end gradually becomes smaller, internal diameter of the water pipe from top to bottom end gradually becomes smaller,
Remaining slurry and water in this way can be impacted on spherical guide plate top surface with biggish impact force, also contribute to retarder, remaining slurry in this way
Uniform with water mixes, and gas-solid mixing tube top end uniformly extends to the outside, and then forms positive cone shape, and such retarder can be more
It is homogeneously dispersed on spherical guide plate top surface, because without installing blender in remaining slurry compounding tank；
2, the second dredge pump is connected by the second magma pipe with concrete mixer in the utility model, in the second magma pipe
Portion is connected by the second branch pipe with the second magma return pipe, and the second magma reflux pipe end protrudes into magma storage tank, the second magma
Internal diameter of the return pipe from head end to end gradually becomes smaller, and the magma in such second magma return pipe can be rushed with biggish impact force
It hits and flows back into magma storage tank, which can make the magma in magma storage tank be constantly in agitated conditions, and then can remove from and stir
Mix homogenization process；And the first dredge pump is connected by the first magma pipe with magma storage tank top in the utility model, and first is former
Slurry pipe end protrudes into magma storage tank, and internal diameter of the first magma pipe from head end to end gradually becomes smaller, in such first magma pipe
Magma can be impacted in magma storage tank with biggish impact force, which can be such that the magma in magma storage tank is constantly in stir
Dynamic state, and then can remove stirring homogenization process from because without installing blender in magma storage tank, and then can save energy
Source；
3, in the utility model in the middle part of the first magma pipe by installing the first branch pipe of the 4th pneumatic operated valve thereon and pacifying thereon
The the first magma return pipe for filling the 4th mass flowmenter is connected, and the first magma reflux pipe end protrudes into remaining slurry compounding tank, in this way
When the quality of the magma entered in magma storage tank reaches pre-set quality, the 4th pneumatic operated valve, the first magma pipe are opened
Interior magma a part enters in magma storage tank, and another part flows back into remaining slurry along the first branch pipe and the first magma return pipe and answers
In distribution tank, it can thus reduce the mass flow into the magma in magma storage tank；In the utility model in the middle part of the second magma pipe
The second branch pipe by installing the 6th pneumatic operated valve thereon is connected with the second magma return pipe for installing the 6th mass flowmenter thereon,
Second magma reflux pipe end protrudes into magma storage tank, presets when the quality of the magma entered in concrete mixer reaches
It when good quality, closes the 5th pneumatic operated valve and simultaneously opens the 6th pneumatic operated valve, the magma in the second magma pipe is along the second branch pipe and the
Two magma return pipes flow back into magma storage tank, if thinking the mass flow for the magma that reduction enters in concrete mixer, beat
Open the 6th pneumatic operated valve, magma a part in the second magma pipe enters in concrete mixer, another part along the second branch pipe with
And second magma return pipe flow back into magma storage tank.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of the utility model.
Detailed description of the invention: 1, remaining slurry storage tank, the 2, first pneumatic operated valve, the 3, first mass flowmenter, 4, remaining slurry pipe, 5, remaining slurry compounding
Tank, 6, water tank, the 7, second pneumatic operated valve, the 8, second mass flowmenter, 9, water pipe, 10, retarder tank, the 11, first valve, 12, go out
Expects pipe, 13, gas-solid mixing room, 14, tracheae, 15, Roots blower, 16, solid flowmeter, 17, gas-solid mixing pipe, 18, shaft,
19, spherical stock guide, the 20, first dredge pump, 21, third mass flowmenter, 22, third pneumatic operated valve, the 23, first magma pipe, 24,
Magma storage tank, the 25, the 4th pneumatic operated valve, the 26, first branch pipe, the 27, the 4th mass flowmenter, the 28, first magma return pipe, 29,
Two dredge pumps, the 30, the 5th mass flowmenter, the 31, the 5th pneumatic operated valve, the 32, second magma pipe, 33, concrete mixer, 34,
Six pneumatic operated valves, the 35, second branch pipe, the 36, the 6th mass flowmenter, the 37, second magma return pipe, 38, motor, 39, shaft coupling,
40, the first outlet tube, the 41, second valve, the 42, second outlet tube, 43, third valve.
Specific embodiment
As shown in Figure 1, the utility model includes remaining slurry storage tank 1, remaining slurry storage tank 1 by installing 2 He of the first pneumatic operated valve thereon
The remaining slurry pipe 4 of first mass flowmenter 3 compounds 5 top of tank with remaining slurry and is connected, and 4 end of remaining slurry pipe is protruded into remaining slurry compounding tank 5,
Internal diameter of the remaining slurry pipe 4 from head end to end gradually becomes smaller, and remaining slurry compounds 5 top end opening of tank；Remaining slurry, which compounds, is equipped with water tank above tank 5
6,6 bottom end of water tank by installing the second pneumatic operated valve 7 and the water pipe 9 of the second mass flowmenter 8 compounds 5 top phase of tank with remaining slurry thereon
Even, 9 bottom end of water pipe is protruded into remaining slurry compounding tank 5, and internal diameter of the water pipe 9 from top to bottom end gradually becomes smaller；Remaining slurry compounds 5 lower-left of tank
Side is equipped with retarder tank 10, and 10 bottom end of retarder tank passes through the discharge nozzle 12 that the first valve 11 is arranged thereon and gas-solid mixing room 13
It is connected, 13 left end of gas-solid mixing room is connected by tracheae 14 with Roots blower 15, and 13 right end of gas-solid mixing room by pacifying thereon
The gas-solid mixing pipe 17 that dress solid flowmeter 16 and top are protruded into remaining slurry compounding tank 5 compounds 5 top of tank with remaining slurry and is connected, gas-solid
17 top of mixing tube uniformly extends to the outside, and then forms positive cone shape；Remaining slurry compounds left part in tank 5 and is equipped with vertical shaft 18,
18 top of shaft is fixed with the spherical stock guide 19 that upper end raises upward, and it is left that 17 top of gas-solid mixing pipe is in spherical stock guide 19
Top, 4 end of remaining slurry pipe are in right above spherical stock guide 19, and 9 bottom end of water pipe is in 19 upper right side of spherical stock guide；Remaining slurry is multiple
Bottom is equipped with the first dredge pump 20 in distribution tank 5, and the first dredge pump 20 by installing third mass flowmenter 21 and third thereon
First magma pipe 23 of pneumatic operated valve 22 is connected with 24 top of magma storage tank, and 23 end of the first magma pipe is protruded into magma storage tank 24,
And first internal diameter of the magma pipe 23 from head end to end gradually become smaller, it is pneumatic by installation the 4th thereon in the middle part of the first magma pipe 23
First branch pipe 26 of valve 25 is connected with the first magma return pipe 28 for installing the 4th mass flowmenter 27 thereon, the reflux of the first magma
28 end of pipe is protruded into remaining slurry compounding tank 5, and internal diameter of the first magma return pipe 28 from head end to end gradually becomes smaller, third quality
Flowmeter 21 is in the upstream position of the first branch pipe 26；Bottom is equipped with the second dredge pump 29, second row in magma storage tank 24
The the second magma pipe 32 and concrete mixer that dirt pump 29 passes through installation the 5th mass flowmenter 30 and the 5th pneumatic operated valve 31 thereon
33 are connected, and pass through the second branch pipe 35 of the 6th pneumatic operated valve 34 of installation thereon and the 6th mass of installation thereon in the middle part of the second magma pipe 32
Second magma return pipe 37 of flowmeter 36 is connected, and 37 end of the second magma return pipe is protruded into magma storage tank 24, the second magma
Internal diameter of the return pipe 37 from head end to end gradually becomes smaller, and the 5th mass flowmenter 30 is in the upstream position of the second branch pipe 35
Place.
Wherein, shaft 18 is driven by motor 38 and is rotated, and motor 38 is fixedly installed in remaining slurry compounding tank 5, and motor 38
Output shaft is vertically arranged, and 38 output shaft of motor is connected by shaft coupling 39 with shaft 18, is wrapped outside motor 38 and shaft coupling 39
It is covered with waterproof layer (not shown).
Wherein, the retarder in retarder tank 10 is sodium gluconate.
Wherein, remaining slurry compounding 5 bottom end of tank is connected with the first outlet tube 40, and the second valve 41 is equipped on the first outlet tube 40,
Magma in this way in remaining slurry compounding tank 5 can also be discharged from the first outlet tube 40；24 bottom end of magma storage tank is connected with second and goes out liquid
Pipe 42 is equipped with third valve 43 on second outlet tube 42, and the magma in such magma storage tank 24 can also be from the second outlet tube 42
It discharges.
The working process of the utility model is as follows: the remaining slurry in remaining slurry storage tank 1 enters in remaining slurry compounding tank 5 by remaining slurry pipe 4,
And first mass flowmenter 3 detection by remaining slurry pipe 4 remaining slurry mass flow, while the water in water tank 6 by water pipe 9 entrance
Remaining slurry compounds in tank 5, and the mass flow of the water of water pipe 9 is passed through in the detection of the second mass flowmenter 8, and at the same time retarder tank 10
Interior retarder enters in gas-solid mixing room 13 by discharge nozzle 12, while the high pressure gas in Roots blower 15 passes through tracheae
14 enter in gas-solid mixing room 13, and the retarder in gas-solid mixing room 13 is uniformly distributed in high pressure gas, retarder and high pressure
The mixture flow of gas is through gas-solid mixing pipe 17 and enters in remaining slurry compounding tank 5, and high pressure gas overflows outward, falls under retarder
Remaining slurry compounds in tank 5, and the mixture of retarder and high pressure gas is when flowing through the solid flowmeter 16 on gas-solid mixing pipe 17,
Solid flowmeter 16 detects the mass flow for flowing through the retarder of gas-solid mixing pipe 17, when the remaining slurry entered in remaining slurry compounding tank 5
Quality, the quality of the quality of water and retarder is when reaching pre-set proportion, it is pneumatic to close the first pneumatic operated valve 2, second
Valve 7, the first valve 11 and Roots blower 15, and the remaining slurry in remaining slurry storage tank 1 starts motor when entering in remaining slurry compounding tank 5
38, motor 38 drives shaft 18 to rotate, and then rotates spherical stock guide 19, since 17 top of gas-solid mixing pipe is led in spherical shape
19 upper left side of flitch, 4 end of remaining slurry pipe are in right above spherical stock guide 19, and 9 bottom end of water pipe is in 19 upper right of spherical stock guide
Side, the retarder fallen on spherical 19 top surface of stock guide in this way, remaining slurry are mixed with water with the rotation of spherical stock guide 19
It is even, and then magma is obtained, and magma falls on lower part in remaining slurry compounding tank 5, first row under 19 top edge of spherical stock guide
Remaining slurry is compounded the magma in tank 5 and is extracted into magma storage tank 24 along the first magma pipe 23 by dirt pump 20, and third mass flowmenter 21
Mass flow of the detection by the magma of the first magma pipe 23 is set in advance when the quality of the magma entered in magma storage tank 24 reaches
When the quality set, the 4th pneumatic operated valve 25 is opened, magma a part in the first magma pipe 23 enters in magma storage tank 24, another
Part flows back into remaining slurry compounding tank 5 along the first branch pipe 26 and the first magma return pipe 28, can thus reduce into magma
The mass flow of magma in storage tank 24, and the mass flow that third mass flowmenter 21 is shown is shown with the 4th mass flowmenter 27
The difference for the mass flow shown is to enter the mass flow of magma in magma storage tank 24, due to the first magma return pipe 28 from
The internal diameter of head end to end gradually becomes smaller, and the magma in such first magma return pipe 28 can be impacted with biggish impact force to flow back
Into remaining slurry compounding tank 5, which can make the magma in remaining slurry compounding tank 5 be constantly in agitated conditions, and then can remove from and stir
Homogenization process is mixed, the magma in magma storage tank 24 is extracted into concrete mixer 33 along the second magma pipe 32 by the second dredge pump 29
It is interior, and the 5th mass flowmenter 30 detection by the second magma pipe 32 magma mass flow, when enter concrete mixer
When the quality of magma in 33 reaches pre-set quality, closes the 5th pneumatic operated valve 31 and open the 6th pneumatic operated valve 34, the
Magma in two magma pipes 32 flows back into magma storage tank 24 along the second branch pipe 35 and the second magma return pipe 37, if wanting to reduce
Into the mass flow of the magma in concrete mixer 33, then the 6th pneumatic operated valve 34, the magma in the second magma pipe 32 are opened
A part enters in concrete mixer 33, and another part flows back into magma along the second branch pipe 35 and the second magma return pipe 37
In storage tank 24, and the difference of the mass flow of the 5th mass flowmenter 30 display and the mass flow of the 6th mass flowmenter 36 display
Value is the mass flow of the magma entered in concrete mixer 33, since the second magma return pipe 37 is from head end to end
Internal diameter gradually becomes smaller, and the magma in such second magma return pipe 37 can be impacted with biggish impact force flows back into magma storage tank 24
Interior, which can make the magma in magma storage tank 24 be constantly in agitated conditions, and then can remove stirring homogenization process from, in this way
Just remaining slurry caused by tubular pole processing and fabricating is effectively recycled.
Wherein, remaining slurry is used to replace partial gelation material and the mixing water in concrete material.
300 grams are added in 1 ton of remaining slurry when temperature is lower than 30 DEG C as one of embodiment of the utility model
Sodium gluconate, the setting time of remaining slurry are 20 hours, and remaining slurry is added in concrete, do not influence the setting time of concrete, when
When temperature is equal to or higher than 30 DEG C, 500 grams of sodium gluconates are added in 1 ton of remaining slurry, the setting time of remaining slurry is 20 hours, is mixed
The setting time for coagulating soil is normal.
As another embodiment of the utility model, 270 kilograms of water is added in 1 ton of remaining slurry and is diluted, and root
The amount that sodium gluconate is added is determined according to temperature.
As another embodiment of the utility model, 120 kilograms of remaining slurry is added in every side's concrete, it will not be to mixed
The compression strength for coagulating soil impacts, and retarder is added in remaining slurry, will not impact to concrete.
In the utility model, the first mass flowmenter 3, the second mass flowmenter 8, third mass flowmenter 21, the 4th matter
Amount flowmeter 27, the 5th mass flowmenter 30 and the 6th mass flowmenter 36 are matured product commercially, this reality
With the novel mass flow for only detecting liquid in each pipeline with each mass flowmenter；Solid flowmeter 16 is in the utility model
Matured product commercially, the utility model are that the slow setting for flowing through gas-solid mixing pipe 17 is detected with solid flowmeter 16
The mass flow of agent.
Claims (10)
1. a kind of recycle device for concrete tubular pile remaining slurry, it is characterised in that: including remaining slurry storage tank, remaining slurry storage tank is logical
It crosses and the remaining slurry pipe of the first pneumatic operated valve and the first mass flowmenter is installed thereon compounds upper end with remaining slurry and be connected, and remaining slurry pipe end
It protrudes into remaining slurry compounding tank, remaining slurry compounds tank deck end opening；Remaining slurry compounds and is equipped with water tank above tank, and water tank bottom end by pacifying thereon
The water pipe for filling the second pneumatic operated valve and the second mass flowmenter compounds upper end with remaining slurry and is connected, and remaining slurry compounding tank is protruded into water pipe bottom end
It is interior；Remaining slurry compounds tank lower left and is equipped with retarder tank, and retarder tank bottom end passes through the discharge nozzle and gas that the first valve is arranged thereon
Gu mixing chamber is connected, gas-solid mixing room left end is connected by tracheae with air blower, and gas-solid mixing room right end is solid by installation thereon
The gas-solid mixing pipe that flowmeter body and top are protruded into remaining slurry compounding tank compounds tank top with remaining slurry and is connected；Remaining slurry compounds left in tank
Portion is equipped with vertical shaft, and shaft top is fixed with the spherical stock guide that upper end raises upward, and gas-solid mixing tube top end is in ball
Shape stock guide upper left side, remaining slurry pipe end are in right above spherical stock guide, and water pipe bottom end is in spherical stock guide upper right side；It is remaining
Bottom is equipped with the first dredge pump in slurry compounding tank, and the first dredge pump is pneumatic by installation third mass flowmenter and third thereon
First magma pipe of valve is connected with magma storage tank top, and the first magma pipe end protrudes into magma storage tank, in the middle part of the first magma pipe
The first branch pipe by installing the 4th pneumatic operated valve thereon is connected with the first magma return pipe for installing the 4th mass flowmenter thereon,
First magma reflux pipe end protrudes into remaining slurry compounding tank, and internal diameter of the first magma return pipe from head end to end gradually becomes smaller；
Bottom is equipped with the second dredge pump in magma storage tank, and the second dredge pump by installing the 5th mass flowmenter and the 5th pneumatically thereon
Second magma pipe of valve is connected with concrete mixer, passes through second of the 6th pneumatic operated valve of installation thereon in the middle part of the second magma pipe
It manages and is connected with the second magma return pipe for installing the 6th mass flowmenter thereon, the second magma reflux pipe end protrudes into magma storage tank
Interior, internal diameter of the second magma return pipe from head end to end gradually becomes smaller.
2. a kind of recycle device for concrete tubular pile remaining slurry according to claim 1, it is characterised in that: first
Internal diameter of the magma pipe from head end to end gradually becomes smaller.
3. a kind of recycle device for concrete tubular pile remaining slurry according to claim 1, it is characterised in that: remaining slurry
Internal diameter of the pipe from head end to end gradually becomes smaller；Internal diameter of the water pipe from top to bottom end gradually becomes smaller.
4. a kind of recycle device for concrete tubular pile remaining slurry according to claim 1, it is characterised in that: shaft
Rotation is driven by motor, motor is fixedly installed in remaining slurry compounding tank, and the output shaft of motor is vertically arranged, and motor output shaft is logical
It crosses shaft coupling to be connected with shaft, waterproof layer is coated with outside motor and shaft coupling.
5. a kind of recycle device for concrete tubular pile remaining slurry according to claim 1, it is characterised in that: slow setting
Retarder in agent tank is sodium gluconate.
6. a kind of recycle device for concrete tubular pile remaining slurry according to claim 1, it is characterised in that: gas-solid
Mixing tube top uniformly extends to the outside, and then forms positive cone shape.
7. a kind of recycle device for concrete tubular pile remaining slurry according to claim 1, it is characterised in that: remaining slurry
Compounding tank bottom end is connected with the first outlet tube, and the second valve is equipped on the first outlet tube.
8. a kind of recycle device for concrete tubular pile remaining slurry according to claim 1, it is characterised in that: magma
Storage tank bottom end is connected with the second outlet tube, and third valve is equipped on the second outlet tube.
9. a kind of recycle device for concrete tubular pile remaining slurry according to claim 1, it is characterised in that: air blast
Machine is Roots blower.
10. a kind of recycle device for concrete tubular pile remaining slurry according to claim 1, it is characterised in that: the
Three mass flowmenters are in the upstream position of the first branch pipe, and the 5th mass flowmenter is in the upstream position of the second branch pipe.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821290923.5U CN209224277U (en) | 2018-08-10 | 2018-08-10 | A kind of recycle device for concrete tubular pile remaining slurry |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821290923.5U CN209224277U (en) | 2018-08-10 | 2018-08-10 | A kind of recycle device for concrete tubular pile remaining slurry |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209224277U true CN209224277U (en) | 2019-08-09 |
Family
ID=67497581
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201821290923.5U Expired - Fee Related CN209224277U (en) | 2018-08-10 | 2018-08-10 | A kind of recycle device for concrete tubular pile remaining slurry |
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| CN (1) | CN209224277U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112454615A (en) * | 2020-11-27 | 2021-03-09 | 冯万芬 | Precast concrete spare apparatus for producing |
| CN113306021A (en) * | 2021-04-09 | 2021-08-27 | 江苏建华新型墙材有限公司 | Residual slurry recycling device and method for laminated slab |
| CN117359770A (en) * | 2023-07-04 | 2024-01-09 | 广东鸿业建材科技有限公司 | Tubular pile residual slurry recycling system and recycling method thereof |
-
2018
- 2018-08-10 CN CN201821290923.5U patent/CN209224277U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112454615A (en) * | 2020-11-27 | 2021-03-09 | 冯万芬 | Precast concrete spare apparatus for producing |
| CN113306021A (en) * | 2021-04-09 | 2021-08-27 | 江苏建华新型墙材有限公司 | Residual slurry recycling device and method for laminated slab |
| CN117359770A (en) * | 2023-07-04 | 2024-01-09 | 广东鸿业建材科技有限公司 | Tubular pile residual slurry recycling system and recycling method thereof |
| CN117359770B (en) * | 2023-07-04 | 2024-05-10 | 广东鸿业建材科技有限公司 | Tubular pile residual slurry recycling system and recycling method thereof |
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Granted publication date: 20190809 Termination date: 20210810 |