CN207390481U - The grey transport system of purification - Google Patents

The grey transport system of purification Download PDF

Info

Publication number
CN207390481U
CN207390481U CN201721048907.0U CN201721048907U CN207390481U CN 207390481 U CN207390481 U CN 207390481U CN 201721048907 U CN201721048907 U CN 201721048907U CN 207390481 U CN207390481 U CN 207390481U
Authority
CN
China
Prior art keywords
gas
transmitter
pipe
conveying
valve
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201721048907.0U
Other languages
Chinese (zh)
Inventor
李锐
张文俊
李鹏
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
INNER MONGOLIA NASHUN EQUIPMENT ENGINEERING (GROUP) Co Ltd
Original Assignee
INNER MONGOLIA NASHUN EQUIPMENT ENGINEERING (GROUP) Co Ltd
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 INNER MONGOLIA NASHUN EQUIPMENT ENGINEERING (GROUP) Co Ltd filed Critical INNER MONGOLIA NASHUN EQUIPMENT ENGINEERING (GROUP) Co Ltd
Priority to CN201721048907.0U priority Critical patent/CN207390481U/en
Application granted granted Critical
Publication of CN207390481U publication Critical patent/CN207390481U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Abstract

The utility model embodiment provides a kind of purification grey transport system, and purification ash can be handled, and can be to avoid the blocking of purification ash in processing procedure.The system includes the transmitter of back taper;The upper end feed inlet of the transmitter is connected by the lower end discharge port of feed arrangement and collecting bin, the lower end discharge port connection material conveying pipe of the transmitter;Multiple first pipes supply for conveying gas for the transmitter, and multiple second pipes supply for conveying gas for the material conveying pipe, and the multiple first pipe is connected to the different position of the transmitter;Wherein, the first pipe is connected to the transmitter by the first valve group, and the second pipe is connected to the material conveying pipe by the second valve group;First valve group is opened with the second valve group timesharing.

Description

The grey transport system of purification
Technical field
The utility model embodiment is related to machinery field, and more particularly, to a kind of grey transport system of purification.
Background technology
Furnace of calcium carbide purification ash is obtained by enclosed calcium carbide burner gas is collected in purification section.Purification ash have high temperature, fine size, Light specific gravity, viscosity is big, is not readily dissolved in water, airborne dust easily occurs, after contacting with the air the characteristics such as easy spontaneous combustion.It is unloading and transportational process In easily cause airborne dust, pollute the working environment of surrounding;And with high temperature, the characteristic of easy spontaneous combustion, purify temperature when ash concentrates accumulation Degree is higher, and there are certain fire safety hidden danger in transportational process.
At present, the conveying for furnace of calcium carbide purification ash is mostly conveyed using Automobile Transportation mode, since the grey temperature of purification is higher, This means of transportation is open type, and the easy airborne dust in transportational process, causes secondary pollution, influences the environment of surrounding.Also have It is transported using closed tank car, furnace of calcium carbide purification ash is easily adhered to tank car wall and forms caking in transportational process, and tank car is caused to unload Ash is not smooth, easily blocks discharging.
Utility model content
The utility model embodiment provides a kind of purification grey transport system, and purification ash can be handled, and handled It in the process can be to avoid the blocking of purification ash.
Provide a kind of grey transport system of purification, the transmitter of collecting bin and back taper including back taper;
The upper end feed inlet of the transmitter is connected by the lower end discharge port of feed arrangement and collecting bin, the transmitter Lower end discharge port connection material conveying pipe;
Multiple first pipes supply for conveying gas for the transmitter, and at least one second pipe is used to convey gas It is supplied for the material conveying pipe, the multiple first pipe is connected to the different position of the transmitter;
Wherein, the multiple first pipe is connected to the transmitter by the first valve group, and the second pipe passes through Second valve group is connected to the material conveying pipe;
First valve group is opened with the second valve group timesharing.
In some possible realization methods, when the transmitter material is full, first valve group is opened;
After first valve group opening, set if the air pressure in the material conveying pipe and/or transmitter is more than During definite value, first valve group is closed, and second valve group is opened.
In some possible realization methods, the multiple first pipe supplies for conveying gas for the transmitter, The multiple pipeline shares first valve group.
In some possible realization methods, the first conveying source of the gas is used for as the multiple first pipe and described at least one The gas that a second pipe supply externally exports.
In some possible realization methods, the second conveying source of the gas is used for as the multiple first pipe supply externally output Gas;
3rd conveying source of the gas is used for the gas externally exported at least one second pipe supply;
Wherein, the second conveying source of the gas and the 3rd conveying source of the gas are not same sources of the gas.
In some possible realization methods, the 4th conveying source of the gas controls first valve group and described for conveying The gas of Pneumatic valve in two valve groups;
Wherein, conveying controls the source of the gas and use of the gas of first valve group and the Pneumatic valve in second valve group In the source of the gas of the gas externally exported for the multiple first pipe and at least one second pipe supply be not same gas Source.
In some possible realization methods, pass through between the inner cavity of the collecting bin and the inner cavity of the transmitter and connect Pipeline connects;Pneumatic valve is provided in the connecting pipeline, the Pneumatic valve set in connection management is by the described 4th conveying The gas control switch or closure of source of the gas conveying.
In some possible realization methods, the gas of the 4th conveying source of the gas conveying is additionally operable to control from the transmission Device is to the outlet valve in the material conveying pipe;And/or
It controls from the collecting bin to the inlet valve of the transmitter, wherein, the outlet valve and the outlet valve are gas Control valve.
In some possible realization methods, by the gas of same pneumatic control case control the 4th conveying source of the gas conveying Body.
In some possible realization methods, three first pipes are respectively connected to the transmitter top, lower part And bottom.
In some possible realization methods, weighing sensor is also set up in the transmitter, in the transmitter Material weigh.
In some possible realization methods, the system also includes:Grey warehouse, the first wind turbine, fluidized bed furnace and cooling are set It is standby;
The upper end feed inlet in the ash warehouse connects the material conveying pipe;
The lower end discharge port in the ash warehouse sets device for discharging;
The left and right ends of the device for discharging connect first wind turbine and the fluidized bed furnace respectively;
The discharge port connection cooling device of the fluidized bed furnace.
In some possible realization methods, the ash warehouse upper end is provided with vacuum release valve and deduster.
In some possible realization methods, the lower end in the ash warehouse is provided with urgent ash discharging hole and spare discharge port.
In some possible realization methods, the system also includes hoppers and sludge-store cabin;
The upper end feed inlet of the hopper is connected with the lower end discharge port of the cooling device;
The bottom of the hopper is connected to the upper end of the sludge-store cabin.
In some possible realization methods, the upper end of the sludge-store cabin includes multiple dust processors and the second wind turbine;
It is connected by pipeline the upper end of the multiple dust processor;
First dust processor of the multiple dust processor of series connection connects the bottom of the hopper;
The last one dust processor of the multiple dust processor of the second wind turbine connection series connection;
The bottom of the multiple dust processor is respectively connected to the sludge-store cabin.
Therefore, in the utility model embodiment, transmitter is supplied by first pipe, and material delivery pipe is supplied by second pipe Gas, and first pipe and second pipe are respectively connected to the first valve group and second of transmitter and material conveying pipe 104 Valve group timesharing is opened, and it is respectively transmitter and material delivery pipe in the different stages that can cause first pipe and second pipe Road supplies, and can so that material conveying is more unobstructed in transmission process.
Description of the drawings
Fig. 1 is the schematic figure according to the material-transporting system of the part of the utility model embodiment.
Fig. 2 is the schematic figure according to the material-transporting system of the part of the utility model embodiment.
Fig. 3 is the control flow chart conveyed according to the material of the utility model embodiment.
Fig. 4 is the schematic figure according to the material-transporting system of the part of the utility model embodiment.
Fig. 5 is the schematic figure according to the material-transporting system of the part of the utility model embodiment.
Fig. 6 is the schematic figure according to the material-transporting system of the part of the utility model embodiment.
Specific embodiment
Below in conjunction with attached drawing, the technical scheme in the embodiment of the utility model is described.
, it is necessary to explanation in the description of the utility model, term " on ", " under ", "left", "right", " top ", " bottom ", The orientation or position relationship of the instructions such as " interior ", " outer " be based on position relationship shown in the drawings, in order to describe the utility model and Simplify description rather than instruction or imply specific orientation that signified device or element must have, with specific orientation Construction or operation, therefore the limitation to the utility model is not understood that.
, it is necessary to which explanation, unless otherwise specific regulation or limits in the description of the utility model, term " peace Dress ", " setting ", " connected ", " connection " etc. should broadly understood, for example, it may be being fixedly connected or detachably connecting It connects or integrally understands;Can be mechanical connection or electrical connection;It can be directly connected, intermediate matchmaker can also be passed through Jie is indirectly connected, and can be the connection inside two elements.For the ordinary skill in the art, can specifically understand The above-mentioned concrete meaning in the utility model.
The utility model embodiment provides a kind of grey transport system of purification, which can include sending One or more of device, grey warehouse, wind turbine, fluidized bed furnace, cooling device, hopper and sludge-store cabin.Specifically include these parts Which, can be depending on actual conditions, and the utility model embodiment is defined not to this.It is non-limiting for example, It is illustrated below with reference to Fig. 1-6 pairs of the utility model embodiments.
Fig. 1 and 2 is the schematic figure of the grey transport system of purification of the part in utility model embodiment.
The upper end feed inlet 101 of transmitter 100 is connected by feed arrangement 102 with the lower end discharge port of collecting bin, is sent The lower end discharge port 103 of device connects material conveying pipe 104;At least one first pipe 105 is transmitter for conveying gas 100 supply, at least one second pipe 106 supply for conveying gas for material conveying pipe 104;Wherein, first pipe 105 Transmitter 100 is connected to by the first valve group 107, second pipe 106 is connected to material delivery pipe by the second valve group 108 Road 104;First valve group 107 and 108 timesharing of the second valve group are opened.
Therefore, in the utility model embodiment, transmitter is supplied by first pipe 105, and material conveying pipe 104 is by Two pipelines 106 supply, and first pipe 105 and second pipe 106 are respectively connected to transmitter 200 and material conveying pipe 104 the first valve group 107 and 108 timesharing of the second valve group are opened, and first pipe 105 and second pipe 105 can be caused to exist The different stages is respectively that transmitter 200 and material conveying pipe 104 supply, and can cause material conveying in transmission process more To be unobstructed.
Optionally, transmitter 100 is back taper.
Optionally, multiple first pipes 105 are connected to the different position of the transmitter.
Optionally, as illustrated in fig. 1 and 2, three first pipes 105 can be respectively the top, lower part and bottom of transmitter 100 Portion supplies.
Optionally, as shown in Figure 1, a second pipe 106 be located at it is separate in the outlet valve 109 of material conveying pipe 104 The one side of transmitter 100.
Optionally, as shown in Fig. 2, a second pipe 106 is located at the outlet valve 109 set on material conveying pipe 104 In close to transmitter 100 one side.
Optionally, in the utility model embodiment, valve group (for example, the first valve group 107 and second valve group 108) can To include one or more valves.
For example, as shown in Figure 1, the first valve group 107 is followed successively by ball valve, pressure regulator valve, Pneumatic valve and check-valves from left to right. Second valve group 108 is followed successively by ball valve, pressure regulator valve, Pneumatic valve and check-valves from left to right.
Optionally, as shown in Figure 1, each first pipe is respectively arranged with the first valve group in multiple first pipes 105 107。
It is to be understood that multiple first pipes 105 can share first valve group 107, for example, as shown in Figure 2.Wherein, First valve group 107 includes gas control shutoff valve 107-1, pressure regulator valve 107-2 and ball valve 107-3 successively from top to bottom.
Optionally, shut-off valve 116 and check-valves 117 can also be set in each first pipe 105.
It is to be understood that in the utility model embodiment, there may be multiple second pipes 106 and be located at material delivery pipe respectively The different position in road, the plurality of second pipe 106 can be supplied by material conveying pipe 104 of timesharing, for example, from close to transmitter 104 second pipe is followed successively by material conveying pipe 104 and supplies to the second pipe away from transmitter 104.
Optionally, in the utility model embodiment, when 100 material of transmitter is full, the first valve group 107 is opened; After first valve group 107 is opened (can be open predetermined time after), if material conveying pipe 104 and/or transmitter 100 In air pressure be more than setting value when, the first valve group 107 is closed, and the second valve group 108 is opened.
Optionally, in the utility model embodiment, closed in the first valve group 107, when the second valve group 108 is opened, It is closed from transmitter 100 to the inlet valve in material conveying pipe 104;It is opened in the first valve group 107, the second valve group is closed 108 when closing, and is opened from transmitter 100 to the inlet valve 109 in material conveying pipe 104.
Specifically, once transmitter 100 is filled (amount of material meets certain condition), then in transmitter 100 into Material valve 110 and air bleeding valve 111 will be closed and seal, and then gases at high pressure are defeated by the first pipe 105 of linkup transmit device 100 It send into transmitter 100, in the cavity 123 of transmitter, the gas added in transmitter 100 is mixed with material, works as transmission Pressure (can be detected by pressure sensor 119) in device 100 automatically opens outlet valve 109 after reaching predetermined value, at this point, material It is pressurized in material conveying pipe 104 with flow regime namely the first valve group 107 is opened, until transmitter 100 and material The all emptyings of conveyance conduit 104.When the pressure in transmitter 100 is reduced to 0, the first valve group 107 is closed, while remaining gas Body is also drawn off transmitter 100 and material conveying pipe 104.If the pressure in transmitter 100 (can also be in material delivery pipe The pressure detected in road) continue not drop, illustrate that material conveying pipe 104 has clogging phenomenon, pressure to be closed automatically after reaching setting value Outlet valve 109 is closed, closes all first valve groups 107, the second valve group 108 is opened and realizes unimpeded repeatedly, only to transmitter 100 Interior pressure is reduced to zero.
It is to be understood that when opening the second valve group 108, outlet valve 109 can not also be closed.
Optionally, as shown in Figure 1, weighing sensor 115 can also be set in transmitter 100, with to the object in transmitter Material is weighed.When the weight of material in transmitter reaches predetermined value, inlet valve 110 and air bleeding valve in transmitter 100 111 will be closed and seal, and then gases at high pressure are delivered to transmitter 100 by the first pipe 105 of linkup transmit device 100 In.
Optionally, transmitter 100 can set level-sensing device 118, and level-sensing device 118 is used to detect whether material reaches predetermined Highly.
Optionally, weighing sensor and level-sensing device can be set simultaneously in transmitter 100, the two meet simultaneously condition or When selecting one and meeting condition, inlet valve 110 and air bleeding valve 111 in transmitter 100 will be closed and seal, and then gases at high pressure lead to The first pipe 105 for crossing linkup transmit device 100 is delivered in transmitter 100.
The control flow in transmitter is illustrated below with reference to Fig. 3.
In 901, determine that the material of level-sensing device measurement reaches certain altitude, the weight of material of weighing sensor measurement reaches Constant weight or the time being fed from collecting bin to transmitter reach certain time.
In 902, closing valve 110 and 111 opens valve group 107.
In 903, judge the pressure in transmitter 200 whether than or equal to predetermined value.
In 904, if judging pressure in transmitter in 903 than or equal to predetermined value, valve opening door 109, such as Fruit does not have, and continues waiting for.
In 905, judge whether the pressure in transmitter 200 or material conveying pipe 104 drops after some time To predetermined value.
906, if judging that the pressure in transmitter does not drop to predetermined value in 905, then it is assumed that material conveying pipe 104 may block, then closing valve group 107, repeatedly Open valve group 108.
907, continue to judge whether the pressure in transmitter 200 or material conveying pipe 104 drops to predetermined value.
908, if judging that the pressure in transmitter does not drop to predetermined value in 907, alarm.
909, if judging that the pressure in transmitter drops to predetermined value in 905, valve group 108, valve opening door are closed Group 107.
In 910, judge whether the material in transmitter 200 all empties, can by the material meter in transmitter or Weighing sensor judges.
In 911, if material in transmitter 200 is judged in 910 all empties, closing valve is from 107, valve opening door 110 and 111.
Optionally, the first conveying source of the gas 112 is used for as at least one first pipe 105 and at least one second pipe 106 Supply the gas externally exported.That is, it can be supplied by same conveying source of the gas for first pipe 105 and second pipe 106 Gas.
Optionally, the second conveying source of the gas is used to supply the gas externally exported at least one first pipe 105;3rd is defeated Source supply gas for supplying the gas externally exported at least one second pipe 106;Wherein, the second conveying source of the gas and the 3rd conveying Source of the gas is not same source of the gas.That is, it can be supplied by different conveying sources of the gas for first pipe 105 and second pipe 106.
Optionally, the 4th conveying source of the gas 113 is for the gas in conveying the first valve group 107 of control and the second valve group 108 Control the gas of valve;
Wherein, the source of the gas of the gas of conveying the first valve group 107 of control and the Pneumatic valve in the second valve group 108 is with being used for The source of the gas that the gas externally exported is supplied at least one first pipe 105 and at least one second pipe 106 is not same gas Source.
Optionally, the 4th conveying source of the gas conveying gas can also control from transmitter to material conveying pipe in into Expect valve 109;And/or control outlet valve 110 from collecting bin to transmitter;And/or control inner cavity and the transmitter of collecting bin Inner cavity between connecting pipeline on the air bleeding valve 111 that sets, wherein, the inlet valve 109, outlet valve 110 and air bleeding valve 111 are Pneumatic valve.
Optionally, the gas of control valve can be controlled by same pneumatic control case 114.
Optionally, as shown in Fig. 2, the pneumatic control case 114 includes solenoid valve 114-1 and pressure transmission device 114-2.
Optionally, PV pipes 120 can be connected between the first valve group and pneumatic control case 114, can be set on PV pipes It puts source of the gas and handles two pieces 121 and ball valve 122.
Optionally, the thickness of each pipeline can be depending on actual conditions, for example, each in the utility model embodiment The size of pipeline can as shown in Figure 2, and can also be increases according to size shown in Fig. 2 in proportion, and the utility model is implemented Example is not especially limited this.
Optionally, in the utility model embodiment, there may be multiple transmitters 100 namely there may be multiple objects Material conveying tube road.The supply and control mode of each transmitter may be referred to described above, in order to which succinctly details are not described herein.
Fig. 4 is the schematic figure according to the grey transport system of purification of the part of the utility model embodiment.
As shown in figure 4, material conveying pipe 104 can be connected to the upper end in grey warehouse 200.
Optionally, grey warehouse 200 is back taper.
Optionally, the upper end in grey warehouse 200 can be provided with vacuum release valve 201, deduster 202,203 and of height material position It is at least one in material cache box 204.
Optionally, the 3rd pipeline 205 is connected to the bottom in grey warehouse 200, and the 3rd pipeline 205 can separate left and right two Branch is respectively connected to the left and right ends in grey warehouse 200.
3rd pipeline 205 can be delivered up gas, and material is prevented to be sticked in grey warehouse 200.
Optionally, connecting pipe 206 can be equipped between device for discharging 300 and grey warehouse 200.
Optionally, the lower end in grey warehouse 200 is connected with device for discharging 300, and the both ends of device for discharging 300 are connected to wind Machine 400 and fluidized bed furnace (Fig. 2 is not shown).
Optionally, device for discharging 300 can be connected with multiple wind turbines 400, and wind turbine 400 can be roots blower.
Optionally, gate valve 301, discharge valve 302 and rotary feeder 303 can be provided in device for discharging 300.
Optionally, material can be added to by gate valve 301 and discharge valve 302 in injector, pass through entrance wind turbine 400 pressure forms certain negative pressure in accelerating chamber and 303 contact surface of rotary feeder, and injection is under rotary feeder 303 Material and air, and exported after the gas mixing of Guan Zhongyu imports, to enter fluidized bed furnace.
It is alternatively possible to control defeated ash quantity by the speed of 300 discharging of device for discharging, controlled with the rotating speed of wind turbine 400 Make the flow velocity of defeated ash.
Fig. 5 is the schematic figure according to the grey transport system of purification of the part of the utility model embodiment.
As shown in figure 5, the material exported by device for discharging 300 can enter fluidized bed furnace 500 by pipeline 501.Material can To be handled in fluidized bed furnace 500.Wherein, if a fluidized bed furnace 500 cannot meet with ash quantity, multiple boilings can be passed through Stove handles material.
Optionally, the lime-ash that fluidized bed furnace 500 generates carries out feed bin after cooling processing being carried out by cooling device 600 700, blow-off valve can be controlled by the level-sensing device of feed bin 700, lime-ash can when reaching predetermined amount (such as reaching the 80% of feed bin) To open blow-off valve, lime-ash is transported to by sludge-store cabin by conveyance conduit 701 by the negative pressure of vacuum pump.
Optionally, cooling device 600 can be connected with feed pipe 601 and return pipe 602.
Fig. 6 is the schematic figure according to the grey transport system of purification of the part of the utility model embodiment.
As shown in fig. 6, the upper end of sludge-store cabin 800 includes multiple 801 and second wind turbines 900 of dust processor.
Optionally, which is roots blower.
Optionally, the upper end of multiple dust processors 801 is connected by pipeline.
Optionally, the bottom of first dust processor connection hopper of multiple dust processors 801 of series connection, for example, The bottom of hopper is connected to by pipeline 803.
Optionally, the last one dust processor of multiple dust processors of the second wind turbine 900 connection series connection.
Optionally, the last one deduster 801 connects source of the gas by pipeline 802.
Optionally, the bottom of multiple dust processors 801 is respectively connected to sludge-store cabin.
Optionally, the valve of multiple 801 bottoms of dust processor is controlled by pneumatic control case 804.
Optionally, the multiple dust processors 801 in left side can be preprocessor, the last one dust processor 801 of right side It can be deduster.
In this scenario, the lime-ash in hopper by the negative pressure of vacuum pump by Ash water to silo roof preprocessor (whirlwind Device), into deduster after the two stage treatment of preprocessor, the air after filtering enters discharge in vacuum pump.After separation Lime-ash is entered by discharger in sludge-store cabin.Equipped with ash discharge discharger entrucking can be facilitated to transport outward below sludge-store cabin.
The above is only specific embodiment of the present utility model, but the scope of protection of the utility model is not limited to In this, in the technical scope that any one skilled in the art discloses in the utility model, variation can be readily occurred in Or replace, it should be covered within the scope of the utility model.Therefore, the scope of protection of the utility model should be described with power Subject to the protection domain of profit requirement.

Claims (16)

1. a kind of grey transport system of purification, which is characterized in that including back taper transmitter;
The upper end feed inlet of the transmitter is connected by the lower end discharge port of feed arrangement and collecting bin, under the transmitter Bring out material mouth connection material conveying pipe;
Multiple first pipes supply for conveying gas for the transmitter, and at least one second pipe is used to convey gas as institute Material conveying pipe supply is stated, the multiple first pipe is connected to the different position of the transmitter;
Wherein, the first pipe is connected to the transmitter by the first valve group, and the second pipe passes through the second valve Group is connected to the material conveying pipe;
First valve group is opened with the second valve group timesharing.
2. system according to claim 1, which is characterized in that when the transmitter material is full, the first valve group quilt It opens;
After first valve group opening, if the air pressure in the material conveying pipe and/or transmitter is more than setting value When, first valve group is closed, and second valve group is opened.
3. system according to claim 1 or 2, which is characterized in that multiple first pipes are used to convey gas as institute Transmitter supply is stated, the multiple pipeline shares first valve group.
4. system according to claim 1, which is characterized in that the first conveying source of the gas be used for as the multiple first pipe and The gas that at least one second pipe supply externally exports.
5. system according to claim 1, which is characterized in that the second conveying source of the gas is used to supply for the multiple first pipe The gas of the outer output of reply;
3rd conveying source of the gas is used for the gas externally exported at least one second pipe supply;
Wherein, the second conveying source of the gas and the 3rd conveying source of the gas are not same sources of the gas.
6. system according to claim 4 or 5, which is characterized in that the 4th conveying source of the gas controls described first for conveying The gas of valve group and the Pneumatic valve in second valve group;
Wherein, conveying control the source of the gas of the gas of first valve group and the Pneumatic valve in second valve group be used for be The source of the gas for the gas that the multiple first pipe and at least one second pipe supply externally export is not same source of the gas.
7. system according to claim 6, which is characterized in that the inner cavity of the inner cavity of the collecting bin and the transmitter it Between connected by connecting pipeline;Pneumatic valve is provided in the connecting pipeline, the Pneumatic valve set in connecting pipeline is by institute State the gas control switch or closure of the 4th conveying source of the gas conveying.
8. system according to claim 6, the gas of the 4th conveying source of the gas conveying is additionally operable to control from the transmission Device is to the outlet valve in the material conveying pipe;And/or
It controls from the collecting bin to the inlet valve of the transmitter, wherein, the inlet valve and the outlet valve are Pneumatic valve.
9. system according to claim 6, which is characterized in that by same pneumatic control case control the 4th conveying source of the gas The gas of conveying.
10. system according to claim 1 or 2, which is characterized in that three first pipes are respectively connected to the hair Send device top, lower part and bottom.
11. system according to claim 1 or 2, which is characterized in that weighing sensor is also set up in the transmitter, with It weighs to the material in the transmitter.
12. system according to claim 1 or 2, which is characterized in that the system also includes:Grey warehouse, the first wind turbine, Fluidized bed furnace and cooling device;
The upper end feed inlet in the ash warehouse connects the material conveying pipe;
The lower end discharge port in the ash warehouse sets device for discharging;
The left and right ends of the device for discharging connect first wind turbine and the fluidized bed furnace respectively;
The discharge port connection cooling device of the fluidized bed furnace.
13. system according to claim 12, which is characterized in that the ash warehouse upper end is provided with vacuum release valve and removes Dirt device.
14. system according to claim 12, which is characterized in that it is described ash warehouse lower end be provided with urgent ash discharging hole and Spare discharge port.
15. system according to claim 12, which is characterized in that the system also includes hoppers and sludge-store cabin;
The upper end feed inlet of the hopper is connected with the lower end discharge port of the cooling device;
The bottom of the hopper is connected to the upper end of the sludge-store cabin.
16. system according to claim 15, which is characterized in that the upper end of the sludge-store cabin includes multiple dust processors With the second wind turbine;
It is connected by pipeline the upper end of the multiple dust processor;
First dust processor of the multiple dust processor of series connection connects the bottom of the hopper;
The last one dust processor of the multiple dust processor of the second wind turbine connection series connection;
The bottom of the multiple dust processor is respectively connected to the sludge-store cabin.
CN201721048907.0U 2017-08-21 2017-08-21 The grey transport system of purification Active CN207390481U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721048907.0U CN207390481U (en) 2017-08-21 2017-08-21 The grey transport system of purification

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721048907.0U CN207390481U (en) 2017-08-21 2017-08-21 The grey transport system of purification

Publications (1)

Publication Number Publication Date
CN207390481U true CN207390481U (en) 2018-05-22

Family

ID=62418110

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721048907.0U Active CN207390481U (en) 2017-08-21 2017-08-21 The grey transport system of purification

Country Status (1)

Country Link
CN (1) CN207390481U (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109282293A (en) * 2018-09-26 2019-01-29 亿利洁能股份有限公司达拉特分公司 A kind of furnace of calcium carbide purification ash conveying incineration system
CN111735316A (en) * 2020-06-19 2020-10-02 亿利洁能股份有限公司达拉特分公司 Calcium carbide furnace purification ash conveying, burning and negative pressure slag suction system
CN115649870A (en) * 2022-11-14 2023-01-31 北京天中方环保科技有限公司 Dry-method calcium-based desulfurization low-positive-pressure pneumatic continuous conveying device and using method thereof

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109282293A (en) * 2018-09-26 2019-01-29 亿利洁能股份有限公司达拉特分公司 A kind of furnace of calcium carbide purification ash conveying incineration system
CN111735316A (en) * 2020-06-19 2020-10-02 亿利洁能股份有限公司达拉特分公司 Calcium carbide furnace purification ash conveying, burning and negative pressure slag suction system
CN111735316B (en) * 2020-06-19 2021-04-16 亿利洁能股份有限公司达拉特分公司 Calcium carbide furnace purification ash conveying, burning and negative pressure slag suction system
CN115649870A (en) * 2022-11-14 2023-01-31 北京天中方环保科技有限公司 Dry-method calcium-based desulfurization low-positive-pressure pneumatic continuous conveying device and using method thereof
CN115649870B (en) * 2022-11-14 2023-03-17 北京天中方环保科技有限公司 Dry-method calcium-based desulfurization low-positive-pressure pneumatic continuous conveying device and using method thereof

Similar Documents

Publication Publication Date Title
CN207390481U (en) The grey transport system of purification
US6786681B2 (en) Method and apparatus for the pneumatic conveying of fine bulk material
CN208394351U (en) A kind of blast furnace dry method gas dedusting ash Pneumatic conveyer
CN201362508Y (en) Stone coal subpressure pneumatic conveying system
CN102219120A (en) Pipeline blowing-aided anti-explosion pneumatic transmission system
CN206427729U (en) Food factory's flour material receives induction system
CN106006035A (en) Pneumatic calcium hydroxide conveying system
CN103072824A (en) Improved pneumatic coal conveying device
CN103062786B (en) Novel pulverized coal metered pneumatic storage system
CN208616934U (en) It is a kind of for controlling the intelligent regulating device of pipeline material transportation concentration
CN207275734U (en) More pellet automatic weighing transport systems
CN107324059A (en) The grey induction system of purification
CN110583505A (en) Automatic control system for feeding in pneumatic conveying mode
CN206395470U (en) Flour intellectuality positive pneumatic transport puts in storage system
CN104404199A (en) Converter one-time dry method dedusting evaporating cooling tower crude ash pneumatic conveying method under full-working condition
CN208135476U (en) Double storehouses pump the uninterrupted continuous transportation system of single pipe
CN212241682U (en) Automatic compounding conveying system of PVC plastic products
CN210619548U (en) Powder malleation pneumatic conveying system
CN207985422U (en) A kind of multi-functional aggregate-storing system
CN204355770U (en) A kind of storehouse formula Pneumatic conveying pump continuously
CN208150514U (en) A kind of energy-saving extra long distance automatic pneumatic transportation system
CN209209919U (en) It is a kind of for lime particle material over long distances and with the positive Pressure Transportation System of downlink
CN212199140U (en) Powder returning system of gas stove
CN109081120A (en) A kind of production line and its technique for beneficiation reagent
CN210456601U (en) Long-distance pneumatic conveying system for bag dust collection zinc ash

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of utility model: Purified ash conveying system

Effective date of registration: 20210527

Granted publication date: 20180522

Pledgee: Bank of Inner Mongolia Co.,Ltd. Hohhot Genghis Khan Street sub branch

Pledgor: INNER MONGOLIA NASHUN EQUIPMENT ENGINEERING (Group) Co.,Ltd.

Registration number: Y2021150000041

PE01 Entry into force of the registration of the contract for pledge of patent right
PC01 Cancellation of the registration of the contract for pledge of patent right

Date of cancellation: 20220517

Granted publication date: 20180522

Pledgee: Bank of Inner Mongolia Co.,Ltd. Hohhot Genghis Khan Street sub branch

Pledgor: INNER MONGOLIA NASHUN EQUIPMENT ENGINEERING (Group) Co.,Ltd.

Registration number: Y2021150000041

PC01 Cancellation of the registration of the contract for pledge of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of utility model: Purified ash conveying system

Effective date of registration: 20220519

Granted publication date: 20180522

Pledgee: Bank of Inner Mongolia Co.,Ltd. Hohhot Genghis Khan Street sub branch

Pledgor: INNER MONGOLIA NASHUN EQUIPMENT ENGINEERING (Group) Co.,Ltd.

Registration number: Y2022150000039

PE01 Entry into force of the registration of the contract for pledge of patent right
PC01 Cancellation of the registration of the contract for pledge of patent right

Date of cancellation: 20230517

Granted publication date: 20180522

Pledgee: Bank of Inner Mongolia Co.,Ltd. Hohhot Genghis Khan Street sub branch

Pledgor: INNER MONGOLIA NASHUN EQUIPMENT ENGINEERING (Group) Co.,Ltd.

Registration number: Y2022150000039

PC01 Cancellation of the registration of the contract for pledge of patent right
PE01 Entry into force of the registration of the contract for pledge of patent right

Denomination of utility model: Purified ash conveying system

Effective date of registration: 20230531

Granted publication date: 20180522

Pledgee: Bank of Inner Mongolia Co.,Ltd. Hohhot Genghis Khan Street sub branch

Pledgor: INNER MONGOLIA NASHUN EQUIPMENT ENGINEERING (Group) Co.,Ltd.

Registration number: Y2023150000077

PE01 Entry into force of the registration of the contract for pledge of patent right