CN107572270A - A kind of continuous bulk system of high concentration force feed - Google Patents
A kind of continuous bulk system of high concentration force feed Download PDFInfo
- Publication number
- CN107572270A CN107572270A CN201710758289.7A CN201710758289A CN107572270A CN 107572270 A CN107572270 A CN 107572270A CN 201710758289 A CN201710758289 A CN 201710758289A CN 107572270 A CN107572270 A CN 107572270A
- Authority
- CN
- China
- Prior art keywords
- feed
- pipe
- bulk
- tank car
- flour
- 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.)
- Granted
Links
Landscapes
- Air Transport Of Granular Materials (AREA)
Abstract
The present invention relates to a kind of continuous bulk system of high concentration force feed, including feeding device and dust arrester, the feeding device includes high pressure sending cans（1）, air compressor（2）, pressure line and the tank car access cover positioned at flour tank car car body top in bulk（9）, described pressure line one end respectively with high pressure sending cans（1）And air compressor（2）It is connected, its other end is provided with bidirectional crossed tilting feed pipe component, and the bidirectional crossed tilting feed pipe component passes through tank car access cover（9）Stretch into the tip position in flour tank car compartment in bulk and in flour tank car compartment in bulk.Compared with the prior art, the invention has the advantages that：The present invention use high concentration force feed feed powder mode, and entrucking is efficient, fills rate height, and air consumption is small, expects that qi leel from easy, without secondary mobile flour tank car in bulk, be greatly decreased the intermediate link of entrucking, significantly save loading time, job safety also greatly improves.
Description
Technical field
The present invention relates to flour Bulk Transport handling facilities technical field, more particularly to a kind of high concentration force feed are continuously in bulk
System.
Background technology
With the high speed development of China Logistics industry, traditional flour bag fills means of transportation due to the cost of bag material
Increase, and in flour packing, heap bag, transfer, entrucking, unload, need a large amount of works in the packed flow of a series of complex such as unpack
Make personnel and carry out packed operation, therefore be easily significantly increased and influenceed by packed cost and recruitment cost so that under some are
The big-and-middle-sized flour mill that trip food factory provides industrial powder is accelerated to use the paces of flour Bulk Transport mode, this
Point-to-point, the totally-enclosed Bulk Transport mode of kind can ensure the whole whole process food security loaded and unloaded and transported, and effectively avoid
Food hygiene quality security incident occurs in shipment, the technical advantage of flour mode in bulk increasingly shows and imperative.
Current domestic flour Bulk Transport instrument is entirely flour canning cart, needs flour mill during flour tank car entrucking
It is independent to be equipped with a set of flour dispensing apparatus in bulk, auger can be used to convey or carry out released job using entrucking flexible pipe,
Provide in the course of work, driver needs flour canning cart resting in fixed entrucking opening position, by the dress that roof is opened manually
Car lid, the outlet of the auger of top or entrucking flexible pipe is directed at tank car charging aperture, tank car entered using flour vertical artesian
Row car loading operation.This entrucking mode by tank car feed gap dimension due to being limited along with flour gravity flow angle of rest (repose) presence can not
The technological deficiency smoothed, so as to cause the negative consequence that flour can not be completely filled up in tank car.Further, since existing flour tank car
The charging aperture of varying number is configured with according to tonnage difference, therefore current entrucking mode fills flour in a gating location
Afterwards, it is necessary to which flour tank car is moved to next gating location by driver or entrucking personnel, roof switch import is then climbed to
Lid carries out flour car loading operation, and this is further caused, and the execute-in-place flow of flour entrucking is extremely cumbersome, loading time is long
And the job safety hidden danger of live entrucking personnel be present.Furthermore most serious technological deficiency existing for existing flour bulk loading device
Can not exactly solve the technical problem that flour easily remains in auger bottom during entrucking or flexible pipe stretches on cloth cylinder, make
Auger bottom or flexible pipe stretch on cloth cylinder generally existing because flour remains and caused by infested, mildew phenomena, these pollutions become
The flour of matter is inevitably fallen into flour tank car together with flour, not only easily causes filling flour hair dessert quality
Amount security incident, the complaint for being also easy to make downstream food factory by the Safety of Food Quality accident trigger, the return of goods, claim etc. is sent out repeatedly
It is raw.
In addition, used abroad by the way of flour in bulk using the flour inner lining bag in TEU (Twenty-foot Equivalent Unit) to transport,
But the application in China is also nearly at space state.Existing container flour inner lining bag is using high intensity, durable poly-
Ethene（PE）Film and polypropylene（PP）Material, it is applicable to the container fortune of large solid bulk powder product for having mobility
Defeated, in addition to it realizes the function of flour Bulk Transport except possessing flour canning cart, compared with traditional canning cart, it does not need enterprise
Sole investment canning cart, give back or transport other goods by the container can strange land of rental and return, solve existing
Tank car is not suitable for long distance transportation and the empty wagons of generally existing returns to problem.It can be seen that with the flour in TEU (Twenty-foot Equivalent Unit)
Lining bag, and should come to transport the mode of flour in bulk will be another novel means that flour Bulk Transport is largely carried out in following China
With having a extensive future, but existing dispensing apparatus in bulk is not particularly suited for container lining bag car loading operation.Therefore urgently dissipated to existing
Dress dispensing apparatus is improved.
Patent No. ZL201420428192.1 Chinese utility model patent discloses a kind of air-box type equipment in bulk, bag
Feeding device and bulk loading device are included, in addition to the air-box type dust arrester being located on bulk loading device；Bulk loading device top is set
There is feeding pipe, in air-box type dust arrester, the mouth of pipe of feeding pipe is connected feeding pipe by skewed slot with feeding device；Air-box type
Dust arrester includes dedusting cover body, and dedusting cover body top is provided with top cover, and dust excluding hood side portion is provided with dedusting mechanism, air-box type dedusting
Device also includes the Pneumatic adjusting mechanism and blower fan for coordinating dedusting cover body to set.The utility model isolates dust from source, reduces
Influence to environment, whole air-box type dust arrester form the closed system that can be pressurizeed, pass through Pneumatic adjusting mechanism and dedusting
Mechanism coordinate, maximum collect dust, rational deployment, have dust collection effect it is good, it is simple in construction, compact, equipment entirety build compared with
Small advantage, successfully solve the problems, such as that bottom storehouse causes installation difficulty because of insufficient height and dust removing effects are undesirable.But the reality
It is all provided with being set to state vertically downward with new feed pipe and the mouth of pipe, still results in the execute-in-place flow of foregoing flour entrucking
Exception is cumbersome, loading time is long and the job safety hidden danger of live entrucking personnel be present, meanwhile, the technical scheme is not because existing
High pressure sending cans are set at feeding device, therefore can not solve flour and auger bottom or flexible pipe are easily remained in during entrucking
Technical problem on flexible cloth cylinder.Therefore urgently air-box type equipment in bulk is improved.
Patent No. ZL201220072481.3 Chinese utility model patent discloses a kind of new bulk material dress in bulk
Put, including one is arranged on cyclone separator above equipment in bulk, cyclone separator connection coming expects pipe, connects below cyclone separator
A star-like flapper is connected to, a telescopic bulk head is connected below star-like flapper；Also include a sack cleaner, sack cleaner
Connect the weary device mouth of dust-laden and telescopic bulk head negative pressure ventilation mouth on cyclone separator top.The utility model can pass through whirlwind point
" online " gas solid separation can be realized from device, while cyclone separator cone section can be used as the small storehouse of buffering storing, therefore the bulk machine
Do not limited by with powder the library distance.But telescopic bulk head and the loading spout outlet of the utility model are all provided with being set to shape vertically downward
State, the execute-in-place flow that still results in foregoing flour entrucking is extremely cumbersome, loading time is long and live entrucking be present
The job safety hidden danger of personnel, meanwhile, the technical scheme can not solve face because setting high pressure sending cans not at feeding device
The technical problem that powder easily remains in auger bottom during entrucking or flexible pipe stretches on cloth cylinder.Therefore urgently to the powder
Body bulk loading device is improved.
The content of the invention
In order to solve technological deficiency existing for above-mentioned existing air-box type equipment in bulk and bulk material bulk loading device, the present invention adopts
Flour bulk pot roof pan feeding technical scheme one is specific as follows：
A kind of continuous bulk system of high concentration force feed, including feeding device and dust arrester, the feeding device include high pressure
Tank sending, air compressor, pressure line and the tank car access cover positioned at flour tank car car body top in bulk, the pressure line one
End is connected with the high pressure sending cans and air compressor respectively, and its other end is provided with bidirectional crossed tilting feed pipe group
Part, the bidirectional crossed tilting feed pipe component are stretched into flour tank car compartment in bulk simultaneously by the tank car access cover
Tip position in flour tank car compartment in bulk.
Preferably, the dust arrester includes deduster and dedusting pipeline, the dedusting pipeline include dedusting flexible pipe and
Exhaust duct, described dedusting flexible pipe one end are connected with the deduster, and its other end is by the tank car access cover and stretches into institute
State the exhaust duct in flour tank car compartment in bulk and close to flour inner top position in tank car compartment in bulk to be connected, institute
State deduster bottom and be provided with feed powder outlet, the feed powder outlet at the top of the high pressure sending cans with being connected.
In any of the above-described scheme preferably, the bidirectional crossed tilting feed pipe component include the first feed pipe and
Second feed pipe, first feed pipe and the second feed pipe are in arranged crosswise, and first feed pipe includes the first tipping tube
Section and first level pipeline section, smoothly transitted between the first inclination pipeline section and first level pipeline section, the first level pipeline section
Angle β between horizontal plane is 0 degree to 15 degree, i.e., the mouth of pipe of described first level pipeline section is towards flour tank car car in bulk
Top-direction tilts 0 degree to 15 degree before railway carriage or compartment.
In any of the above-described scheme preferably, second feed pipe includes the second inclination pipeline section and the second horizontal tube
Section, smoothly transitted between the second inclination pipeline section and the second horizontal pipeline section, between the second horizontal pipeline section and horizontal plane
Angle β is 0 degree to 15 degree, i.e., the mouth of pipe of described second horizontal pipeline section inclines towards top-direction behind flour tank car compartment in bulk
Oblique 0 degree to 15 degree.
In any of the above-described scheme preferably, the pressure line includes force feed steel pipe and force feed flexible pipe, the force feed
Steel pipe one end is connected with the high pressure sending cans and air compressor respectively, and its other end is connected with the force feed flexible pipe,
The force feed flexible pipe is connected with the bidirectional crossed tilting feed pipe component.
In any of the above-described scheme preferably, it is provided with mesohigh rotating nip at the high pressure sending cans outlet at bottom
Valve, injector is provided with the mesohigh rotating nip valve outlet at bottom.
In any of the above-described scheme preferably, two-way switching is provided with first feed pipe and the second feed pipe
Valve.
In any of the above-described scheme preferably, the air compressor using displacement type air compressor machine, power type air compressor machine,
In heating power type air compressor machine, oilless air compressor, oil lubricating air compressor machine, low-noise air compressor, variable ratio frequency changer air compressor machine, explosion-proof air compressor machine
Any one.
In any of the above-described scheme preferably, the deduster uses sack cleaner.
In order to solve technological deficiency existing for above-mentioned existing air-box type equipment in bulk and bulk material bulk loading device, the present invention adopts
TEU (Twenty-foot Equivalent Unit) afterbody pan feeding technical scheme two is specific as follows：
A kind of continuous bulk system of high concentration force feed, including feeding device and dust arrester, the feeding device include high pressure
Tank sending, air compressor, pressure line and the feed pipe import positioned at TEU (Twenty-foot Equivalent Unit) rear portion, pressure line one end difference
It is connected with the high pressure sending cans and air compressor, its other end is provided with unidirectional tilting feed pipe, described unidirectionally to incline
Inclined feed pipe is stretched into the TEU (Twenty-foot Equivalent Unit) by the feed pipe import.
Preferably, the dust arrester includes deduster and dedusting pipeline, the dedusting pipeline include dedusting flexible pipe and
Exhaust duct, described dedusting flexible pipe one end are connected with the deduster, and its other end passes through below the feed pipe import
The exhaust duct stretched into the TEU (Twenty-foot Equivalent Unit) is connected, and the deduster bottom is provided with feed powder outlet, the feed powder
Outlet at the top of the high pressure sending cans with being connected.
In any of the above-described scheme preferably, the unidirectional tilting feed pipe includes stretching into the TEU (Twenty-foot Equivalent Unit)
The 3rd horizontal pipeline section, angle β between the 3rd horizontal pipeline section and horizontal plane is 0 degree to 15 degree, i.e., described 3rd level
The mouth of pipe of pipeline section tilts 0 degree to 15 degree towards the preceding top-direction in the TEU (Twenty-foot Equivalent Unit).
In any of the above-described scheme preferably, the pressure line includes force feed steel pipe and force feed flexible pipe, the force feed
Steel pipe one end is connected with the high pressure sending cans and air compressor respectively, and its other end is connected with the force feed flexible pipe,
The force feed flexible pipe is connected with the bidirectional crossed tilting feed pipe component.
In any of the above-described scheme preferably, it is provided with mesohigh rotating nip at the high pressure sending cans outlet at bottom
Valve, injector is provided with the mesohigh rotating nip valve outlet at bottom.
In any of the above-described scheme preferably, the air compressor using displacement type air compressor machine, power type air compressor machine,
In heating power type air compressor machine, oilless air compressor, oil lubricating air compressor machine, low-noise air compressor, variable ratio frequency changer air compressor machine, explosion-proof air compressor machine
Any one.
In any of the above-described scheme preferably, the deduster uses sack cleaner.
Compared with the prior art, the invention has the advantages that：The present invention is directed to existing flour tank car in bulk and future standard
The flour Bulk Transport instrument of container, there is provided a set of high concentration malleation loading system.The present invention carries by conveying of gases at high pressure
Body, operation in bulk is carried out by pipeline after the material in loose powder storehouse is mixed with gases at high pressure high concentration, only need to be from a charging
Mouth, which enters, implements entrucking in flour bulk pot car or TEU (Twenty-foot Equivalent Unit) inner lining bag, do not need driver to move car during entrucking
Position, uncapping, closing lid number for operating personnel is reduced, loading time and efficiency in bulk is improved, reduces the potential safety hazard of operation.Into
Flour in container is sprayed under high pressure effect with certain initial velocity, the rapid wagon loading since the distalmost end of interior, is led to
Excess pressure destroys flour gravity flow angle of rest (repose), so as to which ensure flour fills rate and loading speed.The flour high concentration of the present invention is than defeated
Mode is sent compared with traditional malleation mode of movement, contained high pressure tolerance very little, material qi leel is from easy, through carrying at exhaust collection
Flying dust after reason device.Simultaneously the present invention take high concentration malleation mode of movement to solve existing machinery mode of movement can not
The flour residual technical problem overcome, ensures flour noresidue during entrucking, reaches food sanitation safe requirement.The present invention
Optimize, simplify existing flour mill's device for dispensing, significantly reduce entrucking parking stall positioning requirements, without opening during entrucking
Whole roofs charging lid of flour tank car in bulk, without secondary mobile flour tank car in bulk, is greatly decreased the middle ring of entrucking
Section, significantly saves loading time, job safety also greatly improves therewith.The present invention uses high concentration force feed feed powder mode, entrucking
Efficiently, rate height is filled, air consumption is small, and material qi leel is from easy.With extensive use and promotional value.
Brief description of the drawings
Fig. 1 is the preferred using flour bulk pot roof pan feeding mode of the continuous bulk system of high concentration force feed of the present invention
The structural representation of embodiment one；
Fig. 2 is the continuous bulk system of high concentration force feed of the present invention using TEU (Twenty-foot Equivalent Unit) afterbody pan feeding mode preferred embodiment
Two structural representation.
Description of reference numerals：
1 high pressure sending cans；2 air compressors；3 mesohigh rotating nip valves；4 injectors；5 force feed steel pipes；6 force feed flexible pipes；7
One feed pipe；8 second feed pipes；9 tank car access covers；10 dedusting flexible pipes；11 dedusters；12 cereal powders.
Embodiment
The present embodiment is only an optimal technical scheme, wherein involved each building block and annexation and unlimited
The setting and connection of each building block in a kind of this following embodiment described by the embodiment, the preferred scheme
Relation can carry out arbitrary permutation and combination and form complete technical scheme.
It is described in detail with reference to Fig. 1 and is continuously dissipated using the high concentration force feed of flour bulk pot roof pan feeding mode
The technical scheme one of dress system：
A kind of continuous bulk system of high concentration force feed, including feeding device and dust arrester, the feeding device include high pressure
Tank sending 1, air compressor 2, pressure line and the tank car access cover 9 positioned at flour tank car car body top in bulk, the force pipe
Road one end is connected with high pressure sending cans 1 and air compressor 2 respectively, and its other end is provided with bidirectional crossed tilting feed pipe
Component, the bidirectional crossed tilting feed pipe component are stretched into flour tank car compartment in bulk simultaneously by tank car access cover 9
Tip position in flour tank car compartment in bulk.The dust arrester includes deduster 11 and dedusting pipeline, described
Dedusting pipeline includes dedusting flexible pipe 10 and exhaust duct, and the one end of dedusting flexible pipe 10 is connected with deduster 11, and its other end passes through tank
Car access cover 9 and the institute for stretching into flour tank car compartment in bulk and close flour inner top position in tank car compartment in bulk
State exhaust duct to be connected, the bottom of deduster 11 is provided with feed powder outlet, and the feed powder outlet is connected with the top of high pressure sending cans 1
It is logical.The bidirectional crossed tilting feed pipe component includes the first feed pipe 7 and the second feed pipe 8, the first feed pipe 7 and second
Feed pipe 8 is in arranged crosswise, and the first feed pipe 7 includes first and tilts pipeline section and first level pipeline section, and described first tilts pipeline section
Smoothly transitted between first level pipeline section, the angle β between the first level pipeline section and horizontal plane is 0 degree to 15 degree, i.e.,
The mouth of pipe of the first level pipeline section tilts 0 degree to 15 degree towards top-direction before flour tank car compartment in bulk.Second enters
Expects pipe 8 includes second and tilts pipeline section and the second horizontal pipeline section, and described second tilts smooth mistake between pipeline section and the second horizontal pipeline section
Cross, the angle β between the second horizontal pipeline section and horizontal plane is 0 degree to 15 degree, i.e., the mouth of pipe court of described second horizontal pipeline section
Top-direction tilts 0 degree to 15 degree after to flour tank car compartment in bulk.The pressure line includes force feed steel pipe 5 and force feed
Flexible pipe 6, the one end of force feed steel pipe 5 are connected with high pressure sending cans 1 and air compressor 2 respectively, its other end and the phase of force feed flexible pipe 6
Connection, force feed flexible pipe 6 are connected with the bidirectional crossed tilting feed pipe component.Set at the outlet at bottom of high pressure sending cans 1
There is mesohigh rotating nip valve 3, injector 4 is provided with the outlet at bottom of mesohigh rotating nip valve 3.First feed pipe 7 and
Two-way switching valve is provided with two feed pipes 8, the two-way switching valve is used between the first feed pipe 7 and the second feed pipe 8
Handover operation, two-way switching valve can also be not provided with, directly using handling switch mode manually.
Air compressor 2 can select empty using displacement type air compressor machine, power type air compressor machine, heating power type air compressor machine, oil-free
Any one in press, oil lubricating air compressor machine, low-noise air compressor, variable ratio frequency changer air compressor machine, explosion-proof air compressor machine.Deduster 11
Using sack cleaner.
The operation principle of technical solution of the present invention one：First its top feed lid that flour tank car in bulk carries is taken during entrucking
Under, change size identical tank car access cover 9 and fixation is installed and cover, force feed flexible pipe 6 is connected with the first feed pipe 7, general
Dedusting flexible pipe 10 is fixed at tank car access cover 9.Cereal powder 12 is by high pressure sending cans 1 and passes through mesohigh rotating nip valve
After 3 feeding injectors 4, mixed with the compressed air high concentration that the pressure from air compressor 2 is 2.0kg-10kg, material gas is dense
Degree ratio can be selected according to yield, distance etc. in the range of u=20-200kg/kg, and mixed material gas is successively along force feed steel
Pipe 5 and force feed flexible pipe 6 are delivered to tank car entrance.Stop feed when flour tank car in bulk is filled to the first feed pipe 7,
Then switching force feed flexible pipe 6 is connected with the second feed pipe 8, continues to be fed into untill flour fills flour tank car in bulk.Filling
During car, flour compartment inner air in bulk is external to by dedusting flexible pipe 10 with the gases at high pressure entered with flour in pipe and removed
Dirt device 11 carries out dedusting operation, and deduster 11 can select to use cyclone dust ventilating net, and the strip tail gas of discharge passes through dedusting
After device 11 separates, the powder isolated is transported to progress recycling in high pressure sending cans 1.
The technical program enters the special tank car of flour occasion in bulk suitable for powder by high pressure single-point force feed, uses continous way
The rotating nip of resistance to mesohigh valve 3 carries out continuous force feed charging；Using the bidirectional crossed tilting feed pipe component and the row
Airduct is arranged on same gating location, can select described in any one the original cap locations conduct of flour bulk pot roof
Gating location, the original top blind flange transformation tubulature of flour tank car in bulk can be borrowed.
It is described in detail with reference to Fig. 2 continuously in bulk using the high concentration force feed of TEU (Twenty-foot Equivalent Unit) afterbody pan feeding mode
The technical scheme two of system：
A kind of continuous bulk system of high concentration force feed, including feeding device and dust arrester, the feeding device include high pressure
Tank sending 1, air compressor 2, pressure line and the feed pipe import positioned at TEU (Twenty-foot Equivalent Unit) rear portion, described pressure line one end point
It is not connected with high pressure sending cans 1 and air compressor 2, its other end is provided with unidirectional tilting feed pipe, described unidirectionally to incline
Inclined feed pipe is stretched into the TEU (Twenty-foot Equivalent Unit) by described positioned at the feed pipe import.The dust arrester includes dedusting
Device 11 and dedusting pipeline, the dedusting pipeline include dedusting flexible pipe 10 and exhaust duct, the one end of dedusting flexible pipe 10 and the phase of deduster 11
Connection, its other end are connected by the exhaust duct stretched into below the feed pipe import in the TEU (Twenty-foot Equivalent Unit)
Connect, the bottom of deduster 11 is provided with feed powder outlet, and the feed powder outlet is connected with the top of high pressure sending cans 1.It is described unidirectionally to incline
Inclined feed pipe includes the 3rd horizontal pipeline section stretched into the TEU (Twenty-foot Equivalent Unit), between the 3rd horizontal pipeline section and horizontal plane
Angle β be 0 degree to 15 degree, i.e., the mouth of pipe of described 3rd horizontal pipeline section inclines towards the preceding top-direction in the TEU (Twenty-foot Equivalent Unit)
Oblique 0 degree to 15 degree.The pressure line includes force feed steel pipe 5 and force feed flexible pipe 6, and the one end of force feed steel pipe 5 is sent with high pressure respectively
Tank 1 is connected with air compressor 2, and its other end is connected with force feed flexible pipe 6, force feed flexible pipe 6 and the bidirectional crossed inclination
Formula feed pipe component is connected.Mesohigh rotating nip valve 3, mesohigh rotation pressure are provided with the outlet at bottom of high pressure sending cans 1
Send and be provided with injector 4 at the outlet at bottom of valve 3.
Air compressor 2 can select empty using displacement type air compressor machine, power type air compressor machine, heating power type air compressor machine, oil-free
Any one in press, oil lubricating air compressor machine, low-noise air compressor, variable ratio frequency changer air compressor machine, explosion-proof air compressor machine.Deduster 11
Using sack cleaner.
The operation principle of technical solution of the present invention two：Will be described unidirectional by the afterbody charging aperture of TEU (Twenty-foot Equivalent Unit) during entrucking
Tilting feed pipe is connected with force feed flexible pipe 6, then stretches into the unidirectional tilting feed pipe and dedusting flexible pipe 10 described
In the afterbody charging aperture of TEU (Twenty-foot Equivalent Unit).Cereal powder 12 is fed by high pressure sending cans 1 and by 3 mesohigh rotating nip valves
After injector 4, mixed with the compressed air high concentration that the pressure from air compressor 2 is 2.0kg-10kg, expect gas concentration ratio
It can be selected according to yield, distance etc. in the range of u=20-200kg/kg, mixed material gas is successively along force feed steel pipe 5
It is delivered to force feed flexible pipe 6 in the afterbody charging aperture of the TEU (Twenty-foot Equivalent Unit).Untill treating that the TEU (Twenty-foot Equivalent Unit) is filled.In entrucking
During, the TEU (Twenty-foot Equivalent Unit) inner air is external to by dedusting flexible pipe 10 with the gases at high pressure entered with flour in pipe and removed
Dirt device 11 carries out dedusting operation, and deduster 11 can select to use cyclone dust ventilating net, and the strip tail gas of discharge passes through dedusting
After device 11 separates, the powder isolated is transported to progress recycling in high pressure sending cans 1.
The technical program enters TEU (Twenty-foot Equivalent Unit) flour bag occasion in bulk suitable for powder by high pressure single-point force feed, using even
The continuous formula rotating nip of resistance to mesohigh valve 3 carries out continuous force feed charging；Using the bidirectional crossed tilting feed pipe component and institute
State exhaust duct and be arranged on same gating location, the special feed pipe of TEU (Twenty-foot Equivalent Unit) afterbody upper area setting can be borrowed.
The sack cleaner refers to using fiber weaving thing or packed layer as the dust arrester of filter medium, its purposes, shape
Formula, dedusting air quantity scale and functioning efficiency everyway have broad scope, are used primarily in the place of trapping fine dust, can
Apply in exhaust dust-removing system, can be applied again on air inlet system.
Claims (10)
1. a kind of continuous bulk system of high concentration force feed, including feeding device and dust arrester, it is characterised in that the pan feeding dress
Put including high pressure sending cans（1）, air compressor（2）, pressure line and the tank car positioned at flour tank car car body top in bulk enter
Lid（9）, described pressure line one end respectively with high pressure sending cans（1）And air compressor（2）It is connected, its other end is set
There is bidirectional crossed tilting feed pipe component, the bidirectional crossed tilting feed pipe component passes through tank car access cover（9）Stretch into
Tip position in the flour tank car compartment in bulk and in flour tank car compartment in bulk.
2. a kind of continuous bulk system of high concentration force feed, including feeding device and dust arrester, it is characterised in that the pan feeding dress
Put including high pressure sending cans（1）, air compressor（2）, pressure line and the feed pipe import positioned at TEU (Twenty-foot Equivalent Unit) rear portion, institute
State pressure line one end respectively with high pressure sending cans（1）And air compressor（2）It is connected, its other end is provided with unidirectional inclination
Formula feed pipe, the unidirectional tilting feed pipe are stretched into the TEU (Twenty-foot Equivalent Unit) by described positioned at the feed pipe import.
3. the continuous bulk system of high concentration force feed as claimed in claim 1, it is characterised in that the dust arrester includes dedusting
Device（11）With dedusting pipeline, the dedusting pipeline includes dedusting flexible pipe（10）And exhaust duct, dedusting flexible pipe（10）One end and dedusting
Device（11）It is connected, its other end passes through tank car access cover（9）With stretching into flour tank car compartment in bulk and close to described
The exhaust duct of flour inner top position in tank car compartment in bulk is connected, deduster（11）Bottom is provided with feed powder outlet, institute
State feed powder outlet and high pressure sending cans（1）Top is connected.
4. the continuous bulk system of high concentration force feed as claimed in claim 2, it is characterised in that the dust arrester includes dedusting
Device（11）With dedusting pipeline, the dedusting pipeline includes dedusting flexible pipe（10）And exhaust duct, dedusting flexible pipe（10）One end and dedusting
Device（11）It is connected, its other end passes through the air draft stretched into the TEU (Twenty-foot Equivalent Unit) below the feed pipe import
Pipe is connected, deduster（11）Bottom is provided with feed powder outlet, the feed powder outlet and high pressure sending cans（1）Top is connected.
5. the continuous bulk system of high concentration force feed as claimed in claim 1, it is characterised in that the bidirectional crossed tilting enters
Expects pipe component includes the first feed pipe（7）With the second feed pipe（8）, the first feed pipe（7）With the second feed pipe（8）In intersection cloth
Put, the first feed pipe（7）Pipeline section and first level pipeline section are tilted including first, described first tilts pipeline section and first level pipeline section
Between smoothly transit, the angle β between the first level pipeline section and horizontal plane be 0 degree to 15 degree, i.e., described first level pipe
The mouth of pipe of section tilts 0 degree to 15 degree towards top-direction before flour tank car compartment in bulk.
6. the continuous bulk system of high concentration force feed as claimed in claim 5, it is characterised in that the second feed pipe（8）Including
Two tilt pipeline section and the second horizontal pipeline section, are smoothly transitted between the second inclination pipeline section and the second horizontal pipeline section, and described second
Angle β between horizontal pipeline section and horizontal plane is 0 degree to 15 degree, i.e., the mouth of pipe of described second horizontal pipeline section dissipates towards the flour
Top-direction tilts 0 degree to 15 degree behind tinning car compartment.
7. the continuous bulk system of high concentration force feed as claimed in claim 2, it is characterised in that the unidirectional tilting feed pipe
Including stretching into the 3rd horizontal pipeline section in the TEU (Twenty-foot Equivalent Unit), the angle β between the 3rd horizontal pipeline section and horizontal plane is 0
For degree to 15 degree, i.e., the mouth of pipe of described 3rd horizontal pipeline section tilts 0 degree to 15 towards the preceding top-direction in the TEU (Twenty-foot Equivalent Unit)
Degree.
8. the continuous bulk system of high concentration force feed as claimed in claim 1 or 2, it is characterised in that the pressure line includes
Force feed steel pipe（5）With force feed flexible pipe（6）, force feed steel pipe（5）One end respectively with high pressure sending cans（1）And air compressor（2）Phase
Connection, its other end and force feed flexible pipe（6）It is connected, force feed flexible pipe（6）With the bidirectional crossed tilting feed pipe component phase
Connection.
9. the continuous bulk system of high concentration force feed as claimed in claim 1 or 2, it is characterised in that high pressure sending cans（1）Bottom
Exit is provided with mesohigh rotating nip valve（3）, mesohigh rotating nip valve（3）Injector is provided with outlet at bottom（4）.
10. the continuous bulk system of high concentration force feed as claimed in claim 5, it is characterised in that the first feed pipe（7）With second
Feed pipe（8）On be provided with two-way switching valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710758289.7A CN107572270B (en) | 2017-08-29 | 2017-08-29 | High-concentration pressure-feed continuous bulk system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201710758289.7A CN107572270B (en) | 2017-08-29 | 2017-08-29 | High-concentration pressure-feed continuous bulk system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN107572270A true CN107572270A (en) | 2018-01-12 |
| CN107572270B CN107572270B (en) | 2023-07-18 |
Family
ID=61030532
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710758289.7A Active CN107572270B (en) | 2017-08-29 | 2017-08-29 | High-concentration pressure-feed continuous bulk system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN107572270B (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110065820A (en) * | 2019-05-06 | 2019-07-30 | 武汉市政环卫机械有限公司 | A kind of strength handling dust tank car |
| CN113321009A (en) * | 2021-07-09 | 2021-08-31 | 湖北和诺生物工程股份有限公司 | Automatic treatment system and method for nicotine production waste residues |
| CN113830562A (en) * | 2021-09-23 | 2021-12-24 | 北京干雾科技有限公司 | Device for quickly adding and subtracting pearlife and use method thereof |
| CN115228204A (en) * | 2022-07-05 | 2022-10-25 | 东莞穗丰粮食集团有限公司 | Flour processing feeding equipment and flour processing equipment |
Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05209691A (en) * | 1991-12-26 | 1993-08-20 | Cosmo Tex:Kk | Sealing device for powder conveyance selector pipe |
| JPH10338073A (en) * | 1997-06-10 | 1998-12-22 | Nisshin Flour Milling Co Ltd | Tank truck for transporting powder |
| CN201021397Y (en) * | 2006-12-13 | 2008-02-13 | 北京惠万环保技术有限公司 | Onboard negative and positive pressure pneumatic transmission device |
| CN103043457A (en) * | 2013-01-22 | 2013-04-17 | 中煤科工集团武汉设计研究院 | Bidirectional loading chute of railway |
| CN103434844A (en) * | 2013-09-04 | 2013-12-11 | 南京中航特种装备有限公司上海技术中心 | Dual pressure feed transport system and transport method thereof |
| CN204057234U (en) * | 2014-08-06 | 2014-12-31 | 南京艾尔康威物料输送系统有限公司 | For the air-transport system of bulk cargo container charging |
| CN205151191U (en) * | 2015-11-20 | 2016-04-13 | 南京艾尔康威物料输送系统有限公司 | Tank car air conveying system of feeding |
| CN206203115U (en) * | 2016-11-22 | 2017-05-31 | 河南省中州环境节能科技有限公司 | A kind of air-transport system |
| CN207226539U (en) * | 2017-08-29 | 2018-04-13 | 无锡东谷工程科技有限公司 | A kind of continuous bulk system of high concentration force feed |
-
2017
- 2017-08-29 CN CN201710758289.7A patent/CN107572270B/en active Active
Patent Citations (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH05209691A (en) * | 1991-12-26 | 1993-08-20 | Cosmo Tex:Kk | Sealing device for powder conveyance selector pipe |
| JPH10338073A (en) * | 1997-06-10 | 1998-12-22 | Nisshin Flour Milling Co Ltd | Tank truck for transporting powder |
| CN201021397Y (en) * | 2006-12-13 | 2008-02-13 | 北京惠万环保技术有限公司 | Onboard negative and positive pressure pneumatic transmission device |
| CN103043457A (en) * | 2013-01-22 | 2013-04-17 | 中煤科工集团武汉设计研究院 | Bidirectional loading chute of railway |
| CN103434844A (en) * | 2013-09-04 | 2013-12-11 | 南京中航特种装备有限公司上海技术中心 | Dual pressure feed transport system and transport method thereof |
| CN204057234U (en) * | 2014-08-06 | 2014-12-31 | 南京艾尔康威物料输送系统有限公司 | For the air-transport system of bulk cargo container charging |
| CN205151191U (en) * | 2015-11-20 | 2016-04-13 | 南京艾尔康威物料输送系统有限公司 | Tank car air conveying system of feeding |
| CN206203115U (en) * | 2016-11-22 | 2017-05-31 | 河南省中州环境节能科技有限公司 | A kind of air-transport system |
| CN207226539U (en) * | 2017-08-29 | 2018-04-13 | 无锡东谷工程科技有限公司 | A kind of continuous bulk system of high concentration force feed |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110065820A (en) * | 2019-05-06 | 2019-07-30 | 武汉市政环卫机械有限公司 | A kind of strength handling dust tank car |
| CN113321009A (en) * | 2021-07-09 | 2021-08-31 | 湖北和诺生物工程股份有限公司 | Automatic treatment system and method for nicotine production waste residues |
| CN113321009B (en) * | 2021-07-09 | 2021-12-17 | 湖北和诺生物工程股份有限公司 | Automatic treatment system and method for nicotine production waste residues |
| CN113830562A (en) * | 2021-09-23 | 2021-12-24 | 北京干雾科技有限公司 | Device for quickly adding and subtracting pearlife and use method thereof |
| CN115228204A (en) * | 2022-07-05 | 2022-10-25 | 东莞穗丰粮食集团有限公司 | Flour processing feeding equipment and flour processing equipment |
| CN115228204B (en) * | 2022-07-05 | 2023-09-29 | 东莞穗丰粮食集团有限公司 | Flour processing feeding equipment and flour processing equipment |
Also Published As
| Publication number | Publication date |
|---|---|
| CN107572270B (en) | 2023-07-18 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN107572270A (en) | A kind of continuous bulk system of high concentration force feed | |
| US10696475B2 (en) | Silo dust collection | |
| CN107954163A (en) | A kind of automatic material transport system | |
| CN100999276A (en) | Fluidising device for conveying tank of bulk powdered material | |
| CN105774842B (en) | The sand adding method of rail traffic sanding device | |
| CN207226539U (en) | A kind of continuous bulk system of high concentration force feed | |
| CN103057862A (en) | Storage and discharge device for dust transfer and application method thereof | |
| US20120107059A1 (en) | Apparatus and method for dispensing flowable solid material | |
| CN207791899U (en) | A kind of automatic material transport system | |
| CN110422348A (en) | Jumbo bag automatic bag feeding bottle placer | |
| CN206476935U (en) | A kind of carbon black collects after-treatment system and carbon black production line | |
| CN108837931A (en) | A kind of dustless closed crushing system of Traditional Chinese medicine essence | |
| CN205469111U (en) | Track traffic adds sand device | |
| CN113348139A (en) | Method and apparatus for feeding and conveying material | |
| CN208282533U (en) | Powder dries subpackage apparatus | |
| CN112498757A (en) | Pipeline system for packaging | |
| CN111908179A (en) | Automatic container loading system | |
| CN105645134B (en) | A kind of Bulk foodstuff dock covers belt continuous conveying device | |
| CN214878528U (en) | Powder pneumatic conveying storage bin and conveying device thereof | |
| US20140178134A1 (en) | Unloading device, unloading process and unloaded powder | |
| JP3602739B2 (en) | Pneumatic transport type powder storage and supply device | |
| CN208377953U (en) | A kind of device drawing off flour out of container | |
| CN212639239U (en) | Automatic container loading system | |
| CN107032144A (en) | Bulk cargo continuous ship discharging machine based on strength Yu mechanical combination conveying technology | |
| CN207683404U (en) | A kind of flour bulk transporter |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |