CN203541068U - Solid particle sorting and mixing proportioning equipment - Google Patents
Solid particle sorting and mixing proportioning equipment Download PDFInfo
- Publication number
- CN203541068U CN203541068U CN201320650391.2U CN201320650391U CN203541068U CN 203541068 U CN203541068 U CN 203541068U CN 201320650391 U CN201320650391 U CN 201320650391U CN 203541068 U CN203541068 U CN 203541068U
- Authority
- CN
- China
- Prior art keywords
- solid particle
- blender
- equipment
- equipment box
- particle sorting
- 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.)
- Expired - Fee Related
Links
Images
Landscapes
- Treatment Of Sludge (AREA)
Abstract
The utility model discloses solid particle sorting and mixing proportioning equipment. The solid particle sorting and mixing proportioning equipment comprises an equipment box body, as well as an air heater, a multi-section type turbo blower, a hammer mill, a continuous air knife dryer, a rotary vibration sieve, a pressure sensitive type meter, a rotary particle distribution type mixer, a water tank and a centrifugal sludge dewatering mechanism, which are fixed inside the equipment box body and are connected with one another. According to the solid particle sorting and mixing proportioning equipment, solid particles are sorted, sludge is dehydrated, dried and sorted, the substances are subjected to constant volume process and mixing proportioning, and main devices are controlled automatically to realize the mixing and proportioning of two or more substances according to a certain grading. The solid particle sorting and mixing proportioning equipment has the advantages of high accuracy, low time consumption, convenient operation, high efficiency and the like, is suitable for physical structure modification in a way that two or more particulate matters are mixed according to a certain grading.
Description
Technical field
The utility model relates to solid particle sorting and the mixing match equipment of mineralized waste processing technology field, specifically a kind of centrifugal dehydration, mechanical crushing, the baking of air-flow heat, screen cloth sorting, pressure-sensitive constant volume, rotation mixing and automatic solid particle sorting and mixing match equipment of realizing solid particle sorting and mixing match controlled of relying on.
Background technology
Mineralized waste refers to that landfill for many years, reaches stabilisation substantially in landfill yard, can exploit the rubbish utilizing.Research shows that landfill exceedes the mineralized waste of 10 years age and after general one month, can be used as day cladding material for replacing soil through secondary fermentation, gathers materials on the spot, cheap advantage, also has the function of biological adsorption and deodorization except having; Mineralized waste can obtain containing the fertile soil of abundant organic and various plants nutrient after certain screening, can be widely used in that farmland, forest land are used, the improvement of afforestation and impaired soil and reparation etc.; Mineralized waste possesses good stable loose structure and larger adsorption specific surface area, and the content of organic matter is high, and cation exchange capacity is large, and wherein contain abundant microorganism, can be used as the Biomedia of superior performance, can make the filler of bio-reaction bed, be used for processing waste water; Mineralized waste after stable can be used as general construction material.As the mineralized waste fines sieving, can be used as road foundation raw material after adding coagulating agent.
Although mineralized waste has its wide recycling space, but any homogenous material has its defective, so a lot of research all tends to make up by the mode of the quantitative mixing match of employing multiple material the defect of homogenous material, as low in the mineralized waste content of organic matter, the shortcomings such as content of beary metal height, so add mud or cow dung, pig manure and so on improve the content of organic matter, add wood chip or zeolite and carry out better modified mineralized rubbish pore structure, the single material so compare, the composite interstitial substance of several solid material compositions can be had complementary advantages, complement each other, obtain better performance, material is more widely used.
In actual application and research, the preparation of this class composite and modification work are all to rely on pure craft or semi-hand (by the assistive device with simple function) mode to carry out, this mode prepare and the efficiency of modification low, the amount of labour needing, complex operation, mix even not, and escaping of dust and irritative gas can work the mischief to healthy staff, be not suitable for the application of Practical Project, and on market, lack this series products, demand at this class composite is increasing, under the increasing reality of modification workload, in practical application and research work all, need a kind of integration apparatus badly, can work continuously, batch production, stablize discharging.
Utility model content
The utility model is for above shortcomings in prior art, a kind of solid particle sorting and mixing match equipment are provided, and this equipment relies on centrifugal dehydration, mechanical crushing, the baking of air-flow heat, screen cloth sorting, pressure-sensitive constant volume, rotation mix and automatically control and realize solid particle sorting and mixing match.
The utility model is achieved through the following technical solutions.
A kind of solid particle sorting and mixing match equipment, comprise equipment box and be fixed on equipment box inner and each other interconnective air heater, the saturating Pu of multisection type formula air blast, beater disintegrating machine, continuously air knife baker, spin vibration sieve, pressure inductive meter, rotate cloth grain formula blender, water tank and centrifugal sludge dewatering machine structure.
Preferably, the saturating Pu of described multisection type formula air blast is provided with air blast spiral case, and described air heater is connected with air blast spiral case by connecting line (gas pipeline).
Preferably, described beater disintegrating machine comprises pulverizer feeding hopper, disintegrator shell, pulverizer fixed mount, 800 hole eye mesh screens and pulverizer discharge bucket, wherein, described pulverizer fixed mount is fixed on equipment box, described disintegrator shell is fixedly connected with pulverizer fixed mount, the arrival end of described pulverizer feeding hopper is arranged at the top of equipment box, the port of export of described pulverizer feeding hopper is fixedly connected with disintegrator shell, the end of the port of export is provided with 800 hole eye mesh screens, described pulverizer discharge bucket is arranged at the port of the port of export, and be connected with continuous air knife type baker.
Preferably, described continuous air knife type baker comprises transmission crawler belt, air knife, sample feeding controller and baker shell, wherein, described sample feeding controller and transmission crawler belt are fixed on baker enclosure, described air knife is arranged on the connecting line (gas pipeline) that connects the saturating Pu of multisection type formula air blast and continuous air knife type baker, and the nose part of air knife is thrust baker shell; Described continuous air knife type baker is connected with spin vibration sieve by connecting line, and the connecting line between described continuous air knife type baker and spin vibration sieve is provided with gate valve.
Preferably, described spin vibration sieve comprises the one-level discharging opening, 400 hole eye mesh screens, 200 hole eye mesh screens, top weight, vibrating motor and the bottom weight that set gradually from top to bottom; Wherein, described one-level discharging opening extends to equipment box place, and described top weight and bottom weight are arranged at respectively upper end and the bottom of vibrating motor, and the bilateral symmetry of described vibrating motor is provided with spring; Described spin vibration sieve is connected with pressure inductive meter by connecting line (solid particle conveyance conduit).
Preferably, described pressure inductive meter comprises pressure inductor, meter feed space and control lever, described control lever is fixed on equipment box, described meter feed space is connected by screw rod with control lever, described pressure inductor is arranged at meter feed space inside, and the discharging opening of described meter feed space extends to rotation cloth grain formula blender.
Preferably, described rotation cloth grain formula blender comprises rotation cloth grain formula blender feed space, blender interlock motor and discharge chamber, wherein, described pressure inductive meter is connected with rotation cloth grain formula blender feed space, the sidewall of described rotation cloth grain formula blender feed space is provided with blender and goes out grain pipe, described blender interlock motor is fixed on discharge chamber, the rocking bar of described blender interlock motor is arranged at the inside of rotation cloth grain formula blender feed space, the porch of described discharge chamber is provided with annular receiving vat, the outlet of described discharge chamber extends to equipment box, described rotation cloth grain formula blender is connected with water tank by water lines, and on described rotation cloth grain formula blender, place, connecting water pipe road was provided with moisture film, between described rotation cloth grain formula blender and water tank, was provided with supply-water pump.
Preferably, described centrifugal sludge dewatering machine structure comprises sewage sludge feed bucket, dehydrator interlock motor, dehydrator case, dehydrator fixed head and be arranged at the dehydrator rotary drum of dehydrator case inside, wherein, described dehydrator case is fixedly connected with the top of equipment box by dehydrator fixed head, described sewage sludge feed bucket is connected to the feed end of dehydrator rotary drum, the charging aperture of sewage sludge feed bucket is arranged at the top of equipment box, described dehydrator interlock motor is connected to the drive end of dehydrator rotary drum, and be fixedly connected with equipment box, the discharge end of described dehydrator rotary drum is connected with beater disintegrating machine.
Preferably, described equipment box adopts 316 types, the thick stainless steel of 2.0mm, for connecting and fixing frame and supporting member employing A3 or 45# structural section.
Preferably, described transmission crawler belt adopts 35MnB-50Mn hot rolled circular steel.
Preferably, described connecting line comprises gas pipeline and solid particle conveyance conduit, and wherein, described gas pipeline adopts seamless steel pipe, steel pipe external application RPUF; Described solid particle conveyance conduit adopts flexible cast iron pipe.
Preferably, between connecting line, by threeway, be connected with outer joint of pipeline.
Preferably, the baker shell of described continuous air knife type baker adopts 316 type stainless steels, and external application RPUF adopts 4 groups of air knives to carry out continuous action, by controlling the keying of gate valve, regulates the unlatching quantity of air knife.
Preferably, the rotation cloth grain formula blender feed space of described rotation cloth grain formula internal mixer is hexagon column structure, is divided into from inside to outside three layers, and every one deck enters different materials, and blender goes out equally distributed hole is set on a tube wall.
According to another aspect of the present utility model, described solid particle sorting and mixing match equipment, also comprise digital display screen, and described digital display screen is arranged at the top of equipment box.
Preferably, described digital display screen is provided with input keyboard.
The utility model is controlled the inflow in rotation cloth grain formula blender by controlling the supply-water pump opening time of water tank outside.
The utility model dries effect by transmitting transmission speed, charging thickness, the air knife air inflow of crawler belt and opening quantity co-controlling to the heat of material.
Before the utility model operation, the inflow of impeller is set by digital display screen, by water pump, aspirate cistern water supply, by the heat that air blast air demand and crawler haulage speed control material are set, dry time and effect, by the proportioning volume of the control lever control solid particle on operating pressure induction type meter.Afterwards, solid material mixes and automatically controls and realize solid particle sorting and mixing match through mechanical crushing, the baking of air-flow heat, screen cloth sorting, pressure-sensitive constant volume, rotation, and mixed solid particle is transferred in fixed container, with to be used.
During the utility model operation, by the gate valve interlock effect control inlet amount on pressure inductor and the meter feed pipe of pressure inductive meter inside, before operation, by control lever on accommodometer measuring device, set the proportional quantity of material.
Compared with prior art, the utlity model has following beneficial effect:
1, adopt the operation of automatic control mode operating equipment, reduced loaded down with trivial details work and operating time in craft and semi-hand operation.
2, more accurate in time control, more reasonable on method arranges, reduced the error that manual operation brings, improved the efficiency that solid particle heat is dried, sieved, mixes.
3, adopt integrated closure designs, avoided the harm that staff is caused that escapes of dust and irritative gas in operating process.
4, adapting with complete equipment of designed rotation cloth grain formula blender, is conducive to realize the automatic automation of whole flow process.
The solid particle sorting that the utility model provides and mixing match equipment, have accuracy high, consuming time few, easy and simple to handle, and efficiency advantages of higher is applicable to the physical arrangement modification that two kinds and above particle mix by certain grating.
Accompanying drawing explanation
By reading the detailed description of non-limiting example being done with reference to the following drawings, it is more obvious that other features, objects and advantages of the present utility model will become:
Fig. 1 is plane of the present utility model;
Fig. 2 is A-A flat sectional drawing of the present utility model;
Fig. 3 is B-B flat sectional drawing of the present utility model;
Fig. 4 is C-C flat sectional drawing of the present utility model;
Fig. 5 is pressure inductive meter schematic diagram;
Fig. 6 is rotation cloth grain formula blender schematic diagram;
Fig. 7 is rotation cloth grain formula blender D-D profile;
In figure: 1 is air heater; 2 is the saturating Pu of multisection type formula air blast; 3 is beater disintegrating machine; 4 is continuous air knife type baker; 5 for transmitting crawler belt; 6 is spin vibration sieve; 7 is pressure inductive meter; 8 is rotation cloth grain formula blender; 9 is centrifugal sludge dewatering machine structure; 10 is threeway; 11 is outer joint of pipeline; 12 is air blast spiral case; 13 is air knife; 14 is sample feeding controller; 15 is pulverizer feeding hopper; 16 is disintegrator shell; 17 is pulverizer fixed mount; 18 is 800 hole eye mesh screens; 19 is pulverizer discharge bucket; 20 is baker shell; 21 is gate valve; 22 is 400 hole eye mesh screens; 23 is one-level discharging opening; 24 is pressure inductor; 25 is meter feed space; 26 is control lever; 27 is top weight; 28 is vibrating motor; 29 is 200 hole eye mesh screens; 30 is spring; 31 is bottom weight; 32 manage for blender goes out grain; 33 is rotation cloth grain formula blender feed space; 34 is blender interlock motor; 35 is discharge chamber; 36 is gas pipeline; 37 is sewage sludge feed bucket; 38 is dehydrator interlock motor; 39 is dehydrator case; 40 is dehydrator fixed head; 41 is dehydrator rotary drum; 42 is equipment box; 43 is digital display screen; 44 is annular receiving vat; 45 was moisture film; 46 is supply-water pump; 47 is water tank.
The specific embodiment
Below embodiment of the present utility model is elaborated: the present embodiment is implemented under take technical solutions of the utility model as prerequisite, provided detailed embodiment and concrete operating process.It should be pointed out that to those skilled in the art, without departing from the concept of the premise utility, can also make some distortion and improvement, these all belong to protection domain of the present utility model.
Please refer to Fig. 1 to Fig. 7.
The present embodiment provides a kind of solid particle sorting and mixing match equipment, comprises equipment box and is fixed on equipment box inner and interconnective air heater, the saturating Pu of multisection type formula air blast, beater disintegrating machine, air knife baker, spin vibration sieve, pressure inductive meter, rotation cloth grain formula blender, water tank and centrifugal sludge dewatering machine structure continuously each other.
Further, the saturating Pu of described multisection type formula air blast is provided with air blast spiral case, and described air heater is connected with air blast spiral case by connecting line (gas pipeline).
Further, described beater disintegrating machine comprises pulverizer feeding hopper, disintegrator shell, pulverizer fixed mount, 800 hole eye mesh screens and pulverizer discharge bucket, wherein, described pulverizer fixed mount is fixed on equipment box, described disintegrator shell is fixedly connected with pulverizer fixed mount, the arrival end of described pulverizer feeding hopper is arranged at the top of equipment box, the port of export of described pulverizer feeding hopper is fixedly connected with disintegrator shell, the end of the port of export is provided with 800 hole eye mesh screens, described pulverizer discharge bucket is arranged at the port of the port of export, and be connected with continuous air knife type baker.
Further, described continuous air knife type baker comprises transmission crawler belt, air knife, sample feeding controller and baker shell, wherein, described sample feeding controller and transmission crawler belt are fixed on baker enclosure, described air knife is arranged on the connecting line (gas pipeline) that connects the saturating Pu of multisection type formula air blast and continuous air knife type baker, and the nose part of air knife is thrust baker shell; Described continuous air knife type baker is connected with spin vibration sieve by connecting line, and the connecting line between described continuous air knife type baker and spin vibration sieve is provided with gate valve.
Further, described spin vibration sieve comprises the one-level discharging opening, 400 hole eye mesh screens, 200 hole eye mesh screens, top weight, vibrating motor and the bottom weight that set gradually from top to bottom; Wherein, described one-level discharging opening extends to equipment box place, and described top weight and bottom weight are arranged at respectively upper end and the bottom of vibrating motor, and the bilateral symmetry of described vibrating motor is provided with spring; Described spin vibration sieve is connected with pressure inductive meter by connecting line (solid particle conveyance conduit).
Further, described pressure inductive meter comprises pressure inductor, meter feed space and control lever, described control lever is fixed on equipment box, described meter feed space is connected by screw rod with control lever, described pressure inductor is arranged at meter feed space inside, and the discharging opening of described meter feed space extends to rotation cloth grain formula blender.
Further, described rotation cloth grain formula blender comprises rotation cloth grain formula blender feed space, blender interlock motor and discharge chamber, wherein, described pressure inductive meter is connected with rotation cloth grain formula blender feed space, the sidewall of described rotation cloth grain formula blender feed space is provided with blender and goes out grain pipe, described blender interlock motor is fixed on discharge chamber, the rocking bar of described blender interlock motor is arranged at the inside of rotation cloth grain formula blender feed space, the porch of described discharge chamber is provided with annular receiving vat, the outlet of described discharge chamber extends to equipment box, described rotation cloth grain formula blender is connected with water tank by water lines, and on described rotation cloth grain formula blender, place, connecting water pipe road was provided with moisture film, between described rotation cloth grain formula blender and water tank, was provided with supply-water pump.
Further, described centrifugal sludge dewatering machine structure comprises sewage sludge feed bucket, dehydrator interlock motor, dehydrator case, dehydrator fixed head and be arranged at the dehydrator rotary drum of dehydrator case inside, wherein, described dehydrator case is fixedly connected with the top of equipment box by dehydrator fixed head, described sewage sludge feed bucket is connected to the feed end of dehydrator rotary drum, the charging aperture of sewage sludge feed bucket is arranged at the top of equipment box, described dehydrator interlock motor is connected to the drive end of dehydrator rotary drum, and be fixedly connected with equipment box, the discharge end of described dehydrator rotary drum is connected with beater disintegrating machine.
Further, described equipment box adopts 316 types, the thick stainless steel of 2.0mm, for connecting and fixing frame and supporting member employing A3 or 45# structural section.
Further, described transmission crawler belt adopts 35MnB-50Mn hot rolled circular steel.
Further, described connecting line comprises gas pipeline and solid particle conveyance conduit, and wherein, described gas pipeline adopts seamless steel pipe, steel pipe external application RPUF; Described solid particle conveyance conduit adopts flexible cast iron pipe.
Further, between connecting line, by threeway, be connected with outer joint of pipeline.
Further, the baker shell of described continuous air knife type baker adopts 316 type stainless steels, and external application RPUF adopts 4 groups of air knives to carry out continuous action, by controlling the keying of gate valve, regulates the unlatching quantity of air knife.
Further, the rotation cloth grain formula blender feed space of described rotation cloth grain formula internal mixer is hexagon column structure, is divided into from inside to outside three layers, and every one deck enters different materials, and blender goes out equally distributed hole is set on a tube wall.
According to another aspect of the present embodiment, described solid particle sorting and mixing match equipment, also comprise digital display screen, and described digital display screen is arranged at the top of equipment box.
Further, described digital display screen is provided with input keyboard.
Be specially,
Equipment box adopts 316 types, the thick stainless steel of 2.0mm, and frame and supporting member adopt A3 or 45# structural section.
Transmit crawler belt and adopt 35MnB-50Mn hot rolled circular steel.
Gas pipeline adopts seamless steel pipe, external application RPUF.
Solid particle conveyance conduit adopts flexible cast iron pipe.
Air knife type baker shell adopts 316 type stainless steels continuously, and external application RPUF, adopts 4 groups of air knives to carry out continuous action, by controlling the keying of gate valve, regulates the unlatching quantity of air knife.
The heat of material is dried effect by crawler haulage speed, charging thickness, air knife air inflow and is opened quantity co-controlling.
During operation, by the gate valve interlock effect control inlet amount on pressure inductor and the meter feed pipe of pressure inductive meter inside, before operation, by control lever on accommodometer measuring device, set the proportional quantity of material.
The feed space of rotation cloth grain formula internal mixer is hexagon column structure, is divided into from inside to outside three layers, and every one deck enters different materials, and blender goes out equally distributed hole is set on a tube wall.
Material proportion amount V is realized by the position that regulates the pressure inductor in pressure inductive meter:
Wherein, V-material proportion amount (m
3);
H-pressure inductive meter chamber height (m);
H
0-pressure inductor probe is apart from the distance (m) at top, meter chamber;
L-pressure inductive meter chamber length (m);
W-pressure inductive meter chamber width (m);
The control handle length (m) that L-pressure inductive meter is supporting.
The gas flow rate v of air knife controls by the blow rate required:
Wherein, the gas flow rate of v-air knife (m/s);
Q
2flow (the m of-gas pipeline
3/ s);
Q
1-blower gas flow (m
3/ s);
1
0-air knife knife edge length (m);
ω
0-air knife edge of a knife width (m).
The water inlet total amount V of rotation cloth grain formula blender
0by the water pump opening time of control water tank outside, control in rotation cloth grain formula blender and regulate:
V
1＝q
1·t
Wherein, V
1water inlet total amount (the m of-rotation cloth grain formula blender
3);
Q
1-pump capacity (m
3/ s);
The t-water pump operation time (s).
The modification of particle physical arrangement adopts this equipment, before equipment operation, by digital and electronic display screen, set flooding time t, the gas flow rate v of air knife, the control handle length L that pressure inductive meter is supporting, equipment moves according to preset program afterwards, specific as follows: after rotation cloth grain formula blender water inlet end, material is respectively by different feeding hopper chargings, solid particle and through the mud of centrifugal sludge dewatering device effect respectively by crossing 800 eye mesh screens after beater disintegrating machine, particle forms fixing thickness by sample feeding controller, by crawler belt, by certain speed, through the heat of 4 groups of air knives, dried, remove the pore water in particle, particle after oven dry enters meter feed space through piping, constantly enrichment, when acquiring a certain degree, grain amount touches pressure inductor when probe, the valve of particle inlet pipeline is closed automatically, outlet valve is opened, particle enters respectively the different layers of rotation cloth grain formula blender, and by blender, go out the effusion of grain pipe under High Rotation Speed, reach the effect of mixing, elapsed time t
2after, mixing its bottom gate and open, mixed material enters annular receiving vat, and passes through discharge hole for discharge.
In the present embodiment, the solids particles after beater disintegrating machine 3 is pulverized is controlled it and enters the grain diameter of continuous air knife type baker 4 through 800 hole eye mesh screens 18, with this, avoids being entered and the obstruction that causes by bulky grain thing.The solid particle that enters continuous air knife type baker 4 by pulverizer discharge bucket 19 is controlled the thickness of sample introduction by sample feeding controller 14, with this, guarantee the action effect of air knife 13.All gas pipeline adopts seamless steel pipe, and external application RPUF, is connected with outer joint of pipeline 11 by threeway 10 between pipeline, gate valve 21 is set on pipeline and controls gas turnover.Spin vibration sieve 6 is controlled the granularity of the particle that enters rotation cloth grain formula blender 8 by 400 hole eye mesh screen 22 and 200 hole eye mesh screens 29.Pressure inductive meter 7 determines by pressure inductor 24 the solid particle amount entering in meter feed space 25, thereby determines mixing match amount.After the particle of screening proportioning enters rotation cloth grain formula blender 8, enter respectively different blender feed spaces 33, in the process of blender rotation, the hole that particle goes out on grain pipe 32 by different blenders is overflowed at a high speed, thereby realizes the even mixing of particle.In impeller, regulating pondage is supplied with by water tank.Air after using by continuous air knife type baker also has surplus heat, and carries out post bake supplemental heat air, and then realize making full use of of heat energy by gas pipeline loopback heater.
Above specific embodiment of the utility model is described.It will be appreciated that, the utility model is not limited to above-mentioned specific implementations, and those skilled in the art can make various distortion or modification within the scope of the claims, and this does not affect flesh and blood of the present utility model.
Claims (10)
1. a solid particle sorting and mixing match equipment, it is characterized in that, comprise equipment box and be fixed on equipment box inner and interconnective air heater, the saturating Pu of multisection type formula air blast, beater disintegrating machine, air knife baker, spin vibration sieve, pressure inductive meter, rotation cloth grain formula blender, water tank and centrifugal sludge dewatering machine structure continuously each other.
2. solid particle sorting according to claim 1 and mixing match equipment, is characterized in that, the saturating Pu of described multisection type formula air blast is provided with air blast spiral case, and described air heater is connected with air blast spiral case by connecting line;
Described beater disintegrating machine comprises pulverizer feeding hopper, disintegrator shell, pulverizer fixed mount, 800 hole eye mesh screens and pulverizer discharge bucket, wherein, described pulverizer fixed mount is fixed on equipment box, described disintegrator shell is fixedly connected with pulverizer fixed mount, the arrival end of described pulverizer feeding hopper is arranged at the top of equipment box, the port of export of described pulverizer feeding hopper is fixedly connected with disintegrator shell, the end of the port of export is provided with 800 hole eye mesh screens, described pulverizer discharge bucket is arranged at the port of the port of export, and be connected with continuous air knife type baker,
Described continuous air knife type baker comprises transmission crawler belt, air knife, sample feeding controller and baker shell, wherein, described sample feeding controller and transmission crawler belt are fixed on baker enclosure, described air knife is arranged on the connecting line that connects the saturating Pu of multisection type formula air blast and continuous air knife type baker, and the nose part of air knife is thrust baker shell; Described continuous air knife type baker is connected with spin vibration sieve by connecting line, and the connecting line between described continuous air knife type baker and spin vibration sieve is provided with gate valve;
Described spin vibration sieve comprises the one-level discharging opening, 400 hole eye mesh screens, 200 hole eye mesh screens, top weight, vibrating motor and the bottom weight that set gradually from top to bottom; Wherein, described one-level discharging opening extends to equipment box place, and described top weight and bottom weight are arranged at respectively upper end and the bottom of vibrating motor, and the bilateral symmetry of described vibrating motor is provided with spring; Described spin vibration sieve is connected with pressure inductive meter by connecting line;
Described pressure inductive meter comprises pressure inductor, meter feed space and control lever, described control lever is fixed on equipment box, described meter feed space is connected by screw rod with control lever, described pressure inductor is arranged at meter feed space inside, and the discharging opening of described meter feed space extends to rotation cloth grain formula blender;
Described rotation cloth grain formula blender comprises rotation cloth grain formula blender feed space, blender interlock motor and discharge chamber, wherein, described pressure inductive meter is connected with rotation cloth grain formula blender feed space, the sidewall of described rotation cloth grain formula blender feed space is provided with blender and goes out grain pipe, described blender interlock motor is fixed on discharge chamber, the rocking bar of described blender interlock motor is arranged at the inside of rotation cloth grain formula blender feed space, the porch of described discharge chamber is provided with annular receiving vat, and the outlet of described discharge chamber extends to equipment box; Described rotation cloth grain formula blender is connected with water tank by water lines, and on described rotation cloth grain formula blender, place, connecting water pipe road was provided with moisture film, between described rotation cloth grain formula blender and water tank, was provided with supply-water pump;
Described centrifugal sludge dewatering machine structure comprises sewage sludge feed bucket, dehydrator interlock motor, dehydrator case, dehydrator fixed head and be arranged at the dehydrator rotary drum of dehydrator case inside, wherein, described dehydrator case is fixedly connected with the top of equipment box by dehydrator fixed head, described sewage sludge feed bucket is connected to the feed end of dehydrator rotary drum, the charging aperture of sewage sludge feed bucket is arranged at the top of equipment box, described dehydrator interlock motor is connected to the drive end of dehydrator rotary drum, and be fixedly connected with equipment box, the discharge end of described dehydrator rotary drum is connected with beater disintegrating machine.
3. solid particle sorting according to claim 2 and mixing match equipment, is characterized in that, described equipment box adopts 316 types, the thick stainless steel of 2.0mm.
4. solid particle sorting according to claim 2 and mixing match equipment, is characterized in that, described transmission crawler belt adopts 35MnB-50Mn hot rolled circular steel.
5. solid particle sorting according to claim 2 and mixing match equipment, it is characterized in that, described connecting line comprises gas pipeline and solid particle conveyance conduit, wherein, described gas pipeline adopts seamless steel pipe, steel pipe external application RPUF; Described solid particle conveyance conduit adopts flexible cast iron pipe.
6. solid particle sorting according to claim 5 and mixing match equipment, is characterized in that, between connecting line, by threeway, is connected with outer joint of pipeline.
7. solid particle sorting according to claim 2 and mixing match equipment, is characterized in that, described baker shell adopts 316 type stainless steels, baker shell external application RPUF.
8. solid particle sorting according to claim 2 and mixing match equipment, is characterized in that, described air knife is 4 groups.
9. solid particle sorting according to claim 2 and mixing match equipment, it is characterized in that, described rotation cloth grain formula blender feed space is hexagon column structure, is divided into from inside to outside three layers, and described blender goes out equally distributed hole is set on a tube wall.
10. according to the solid particle sorting described in any one in claim 1 to 9 and mixing match equipment, it is characterized in that, also comprise digital display screen, described digital display screen is arranged at the top of equipment box.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320650391.2U CN203541068U (en) | 2013-10-21 | 2013-10-21 | Solid particle sorting and mixing proportioning equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320650391.2U CN203541068U (en) | 2013-10-21 | 2013-10-21 | Solid particle sorting and mixing proportioning equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203541068U true CN203541068U (en) | 2014-04-16 |
Family
ID=50459238
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320650391.2U Expired - Fee Related CN203541068U (en) | 2013-10-21 | 2013-10-21 | Solid particle sorting and mixing proportioning equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203541068U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103586262A (en) * | 2013-10-21 | 2014-02-19 | 环境保护部南京环境科学研究院 | Solid particle sorting and mixing matching equipment |
| CN104858217A (en) * | 2015-05-30 | 2015-08-26 | 杭州扬中科技有限公司 | Comprehensive treatment technology for household garbage |
| CN105749592A (en) * | 2016-04-25 | 2016-07-13 | 东莞市联洲知识产权运营管理有限公司 | Communicating structure between sewage treatment tanks |
-
2013
- 2013-10-21 CN CN201320650391.2U patent/CN203541068U/en not_active Expired - Fee Related
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103586262A (en) * | 2013-10-21 | 2014-02-19 | 环境保护部南京环境科学研究院 | Solid particle sorting and mixing matching equipment |
| CN104858217A (en) * | 2015-05-30 | 2015-08-26 | 杭州扬中科技有限公司 | Comprehensive treatment technology for household garbage |
| CN105749592A (en) * | 2016-04-25 | 2016-07-13 | 东莞市联洲知识产权运营管理有限公司 | Communicating structure between sewage treatment tanks |
| CN105749592B (en) * | 2016-04-25 | 2017-11-10 | 鲍菊芳 | A kind of connectivity structure between treatment tank |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103586262A (en) | Solid particle sorting and mixing matching equipment | |
| CN204848626U (en) | Cowshed excrement and urine recovery processing device | |
| CN105441317B (en) | For the continuous dynamic anaerobic ferment devices of multi-element material high concentration and its application | |
| CN203541068U (en) | Solid particle sorting and mixing proportioning equipment | |
| WO2021115134A1 (en) | Apparatus and method for preparing biochar-based organic fertilizer using straw | |
| CN206391987U (en) | A kind of solid fertilizer integrated production equipment | |
| CN105732145A (en) | Film mulching aerobic composting reactor test apparatus | |
| WO2020048402A1 (en) | Method for preparation of wall bricks from sludge composite mineralized waste | |
| CN104404087A (en) | Technological method for preparing biogas by utilizing high-concentration organic waste and fermentation system thereof | |
| KR20110016368A (en) | Apparatus and method for treatmenting organic waste | |
| CN207783803U (en) | Agaric compost agitating device | |
| CN105709893A (en) | Uniform mixing equipment for LID earth replacing and filling engineering materials | |
| CA2892541C (en) | A fermenter supply method, a biogas plant, and a conversion method comprising an inoculation return path | |
| CN109127683A (en) | A kind of aging process for treating garbage as resource | |
| CN205238276U (en) | Brickmaking stirring device | |
| CN104962469B (en) | Modular solid-state biological raw material fermentation system | |
| CN207086545U (en) | A kind of house refuse is reduced recycling buried type integrated device | |
| CN110499241A (en) | A kind of anaerobic dry fermentation apparatus of tunnel dragon-bone water lift formula | |
| CN204625487U (en) | Ight soil composting is field system also | |
| CN204848884U (en) | Solid -state biological raw materials fermentation system of modularization | |
| CN204803284U (en) | Liquid, solid -state biological raw materials fermentation system | |
| CN107377580A (en) | House refuse is reduced method of resource and buried type integrated device | |
| CN109775952B (en) | Process and equipment for resource utilization of sludge | |
| CN208695185U (en) | A kind of wine brewing crushing material mixing arrangement | |
| CN207086544U (en) | A kind of house refuse round and device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CU01 | Correction of utility model |
Correction item: Patentee Correct: Ministry of Environmental Protection, Nanjing Environment Science Institute False: NANJING INSTITUTE OF ENVIRONMENTAL SCIENCES, MEP Number: 16 Page: The title page Volume: 30 |
|
| CU03 | Publication of corrected utility model |
Correction item: Patentee Correct: Ministry of Environmental Protection, Nanjing Environment Science Institute False: NANJING INSTITUTE OF ENVIRONMENTAL SCIENCES, MEP Number: 16 Volume: 30 |
|
| ERR | Gazette correction |
Free format text: CORRECT: PATENTEE; FROM: NANJING INSTITUTE OF ENVIRONMENTAL SCIENCES, MEP TO: MINISTRY OF ENVIRONMENTAL PROTECTION, NANJING ENVIRONMENT SCIENCE INSTITUTE |
|
| RECT | Rectification | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140416 Termination date: 20141021 |
|
| EXPY | Termination of patent right or utility model |