CN103111231B - Steam blasting machine - Google Patents
Steam blasting machine Download PDFInfo
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- CN103111231B CN103111231B CN201310046686.3A CN201310046686A CN103111231B CN 103111231 B CN103111231 B CN 103111231B CN 201310046686 A CN201310046686 A CN 201310046686A CN 103111231 B CN103111231 B CN 103111231B
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Abstract
The invention discloses a steam blasting machine which comprises a sliding sealing disc, a movable upper limiting shaft, a lower sealing disc, an upper sealing ring, a lower sealing ring, a cylinder A for controlling the sliding sealing disc to move upwards and a cylinder B for controlling the sliding sealing disc to move downwards, wherein the sliding sealing disc is I-shaped; the lower part of the sliding sealing disc is in a conical disc structure having a high middle part and a low peripheral part; the lower end of the upper limiting shaft is matched with the upper end of the sliding sealing disc in a sealing manner through the upper sealing ring so as to form an integrated structure; the lower end of the sliding sealing disc is matched with the lower sealing disc in the sealing manner through the lower sealing ring so as to form another integrated structure; the sliding sealing disc is sealed in a sliding manner through the upper sealing ring and the lower sealing ring which slide up and down in a blasting bin; the cylinder A is connected with the bottom of the lower sealing disc; and the cylinder B is connected below the cylinder A. The steam blasting machine is simple in structure and high in working efficiency and can finish the supersonic steam blasting crush in milliseconds; materials are fed and blasted out more rapidly in the steam blasting process. In addition, the raw material accumulation and the material residues are avoided.
Description
Technical field
The present invention relates to a kind of Steam explosive machine, particularly relate to and a kind ofly steam explosive-crushing is carried out to living beings and the raw material such as starchiness, protein is carried out to the quick-fried device of vapour of steam explosive-crushing maturation process.
Background technology
From nineteen twenties, steam explosion technology occurs that oneself has more than 90 year so far; from at first for the production of beaver board, go through that lumber fibre extracts ethanol, pulping and paper-making, animal feed are produced; so far oneself develops in each fields such as food industry, pharmaceutical industry, bioenergy, material, chemistry and environmental protection, and its application prospect and technical advantage are increasingly outstanding.
Steam explosion technology full name is " steam explosion technology ", and its know-why is: sudden release is occurred the steam molecule infiltering living beings organization internal within the short time, is decomposed by raw material with less energy by object.Namely Steam explosive machine is according to this principle design for completing mechanical device or the equipment of different object, can by the raw material in cord cage and high steam in the scope of Millisecond, quick-fried in airspace with fried loose form.This process not only make use of the high pressure potential energy of steam, more importantly makes internal steam work be converted into mechanical energy, achieves adiabatic expansion acting.Because its action time is short, energy density is high and active position concentrated, make the stream molecule penetrated between the molecule of cellulose and lignin etc. produce powerful destructive power, can on macromolecular level, material be decomposed fully, for basic condition is created in the biochemical treatments such as late enzyme hydrolysis.
At present, steam explosion technology is widely used in the pretreatment of the biological materials such as stalk, and the quick-fried device of different vapour is also of a great variety.But, in fact existing the quick-fried device of vapour all do not reach the requirement of technical performance, can only be referred to as hot spraying device, its basic model is: at a pressure vessel bottom valving, open by valve the unexpected release realizing container inner pressure fast, produce heat and spurt effect.The subject matter that this pattern exists is: the steam bleeding cross section due to valve is far smaller than the volume cross section of pressure vessel, and high pressure valve opening speed is limited, the pressure releasing process time of container inner high voltage steam is long, be generally 3-10 second, far do not reach a millisecond magnitude release, therefore cannot realize the acting of steam adiabatic expansion, reduce energy density, make material degree of decomposition not high.And when needing the volume adding bulk container in Practical Project, valve cannot equal proportion amplify, and this has just more widened the gap in steam bleeding cross section and vessel volume cross section, makes pressure releasing process further extend.Therefore, the quick-fried device of vapour that this heat spurts pattern does not produce real steam explosive-crushing effect.
In addition, also have a kind of device of being simulated steam explosive-crushing process by the continuous extrusion way of screw rod, be characterized in: solid content or material dry are subject to heavily stressed extruding and produce high temperature, after the stress relieved of device outlet extruding, material is expanded.The technical process that this device is implemented, not that the internal type infiltrated into living beings tissue with gas fills the compression gas energy that can break out, and make it in short time blast release, therefore do not possess the quick-fried technical conditions of vapour, the macromolecular lattice of original living beings cannot be broken from molecular level.Consequently carry out compression solid with huge power consumption, but fail to produce the effect of process desired by living beings, the utilization effect for the later stage is little.
For the actual defects existing for " heat is spurted " and " screw rod is extruded continuously " two kinds of mode devices and technological effect thereof, the Chinese invention patent that number of patent application is 201110030659.8, denomination of invention is " numerical control continuous steam explosion machine ", disclose the quick-fried device of a kind of vapour, the quick-fried device of this vapour utilizes slip capping principle can complete supersonic speed steam explosive-crushing process within the time of Millisecond, the quick-fried steam bleeding cross section of vapour of this invention equals container section, achieves outburst sudden.In phase specific heat spraying device, the steam bleeding time is limited by the ratio of steam bleeding valve and container size, its steam bleeding time and vessel volume size have nothing to do, the steam ejection effect energy produced is huge, realize high-speed driving slip capping, its driving force is directly proportional to container section, make slip capping no matter quality size can complete that vapour is quick-fried to be opened fast, improve blasting energy density, material is fully decomposed, the steam dwell time is made to shorten to tens seconds by tens minutes, whole material is produced process and is all completed in Millisecond (0.00875 second), to avoid in hot spraying device first second problem different with the cooking level of the material of ejection in the tenth second, meet the requirement of process consistency in suitability for industrialized production.But although this invention belongs to the slip capping principle of employing, and in fact its wharf explosion top adopts slipper seal, and what bottom still adopted is end face seal principle, causes the loss of sealing ring very large, needs often to change sealing ring, affects operating efficiency; Adopt the mode of top slipper seal lid intermediate feed, charging aperture adopts suspending sealing, needs an independent cylinder to provide power, not only makes device complicated and add equipment cost.
Specifically, mainly there is following problem in the Steam explosive machine of this structure: one is lower end surface sealing, causes sealing ring loss very big, two is adopt slip capping intermediate feed mode, just with many pillars, upper-lower seal dish must be connected to form slip capping, so just make whole slip capping in being " mouse cage " structure, also needing to set up feed inlet sealing device in addition, the suspending sealing device of existing employing or thread seal, after raw material directly enters wharf explosion from charging aperture, when slip capping opens port sealing to lower end operation, raw material is owing to being subject to the branched column resistance of slip capping " mouse cage " structure, delay or hinder to produce producing rapidly of material, and produce material and can be deposited on the chassis of slipper seal lid, under the state of numerical control continuous steam explosion, these are deposited in producing on slipper seal lid chassis and expect quick-fried through the vapour of too much round, hard group can be charred into, especially when the quick-fried starchy material of vapour, due to the viscosity of material, also can stick on the pillar of " mouse cage " structure, on the chassis of slipper seal lid, all coking becomes hard group, have a strong impact on the continuous duty producing materials quality and Steam explosive machine, this is confirmed by experiments.
Summary of the invention
The object of the invention is to: the technological deficiency existed for the quick-fried equipment of above-mentioned " slip capping " vapour, there is provided a kind of raw material not pile up, non-burnt, simple in equipment, the Steam explosive machine of supersonic speed steam explosive-crushing process can be completed within the Millisecond time, thus can effectively solve above-mentioned problems of the prior art.
The object of the invention is realized by following technical proposals: a kind of Steam explosive machine, comprise feed hopper, receiving hopper, discharge bucket and wharf explosion, described feed hopper is up big and down small taper, the receiving hopper of taper is connect below it, the below of receiving hopper connects wharf explosion, discharge bucket is located at the below of wharf explosion, also comprise the slipper seal dish be arranged in wharf explosion cavity, be arranged on slipper seal dish top and be positioned at the removable upper limit axle of receiving hopper for the displacement of limit slippage seal disc, be arranged on slipper seal tray bottom and seal the removable lower seal dish bottom wharf explosion, the upper sealing ring corresponding with wharf explosion internal diameter size, the lower seal corresponding with wharf explosion internal diameter size, the cylinder A that control slipper seal dish up moves and the cylinder B that control slipper seal dish down moves, described slipper seal dish is " work " font, its underpart is middle high, the conical disc structure that surrounding is low, the lower end of described upper limit axle is sealed and matched integral by the upper end of upper sealing ring and slipper seal dish, the lower end of slipper seal dish is sealed and matched integral by lower seal and lower seal dish, slipper seal dish is sliding up and down and realizing slipper seal in wharf explosion by upper sealing ring and lower seal, described cylinder A is connected with the bottom of lower seal dish, and cylinder B is connected to the below of cylinder A.
As a kind of preferred embodiment, the outside of described upper limit axle is provided with interior empty scaffolding schema corresponding to shape with it, this interior empty scaffolding schema comprises superposed limit shaft overcoat, be positioned at the stopping means support of bottom and connection and slipper seal folded to the position limiting structure of position-limiting action, the bottom of stopping means support and the top of wharf explosion are fixed, and upper limit axle can slide up and down in interior empty scaffolding schema.
Further preferably, the bottom of upper limit axle is be the conical disc of 30-60 degree with bottom.
Further preferably, the top of described slipper seal dish is disc, and bottom is be the conical disc of 30-60 degree with bottom.
As a kind of preferred embodiment, at the warehouse bottom external ring-shaped steam distributor of wharf explosion, this steam distributor establishes several jetted hole be connected with wharf explosion steam entrance.
As a kind of preferred embodiment, between described cylinder A and lower seal dish, be provided with the damping spring of cushioning effect.
Further preferably, cylinder A is located in cylinder A fixed platform, and cylinder B is located in cylinder B fixed platform, is provided with cylinder protective sleeve at the skin of cylinder A and cylinder B.
Further preferably, also comprise a pressure sensor be connected respectively with cylinder B with cylinder A, described pressure sensor is located on jet chimney, and the jet chimney in pressure sensor front is also provided with steam-flow meter and steam valve.
Further preferably, also comprise frame, frame supports discharge bucket.
Compared with prior art, beneficial effect of the present invention: Steam explosive machine structure of the present invention is simple, and operating efficiency is high, also possesses following advantage:
1, the present invention passes through the upper and lower full slipper seal of wharf explosion, can realize ultrahigh speed and drive slip capping, complete and open fast, can complete supersonic speed steam explosive-crushing within the Millisecond time;
2, the present invention adopts " I shape " slipper seal dish, and the bottom of its underpart seal disc and upper limit axle is all designed to " taper " dish, to make in the quick-fried process of vapour material feeding and produces all quicker, and raw material is not piled up, residual;
3, the present invention opens wharf explosion cross section by I-shaped slipper seal dish upward sliding, realize surrounding charging, the charging aperture that minimizing intermediate feed pattern must be set up suspends or thread sealing device, reduce by many pillars, the structure of " I-shaped " type structure is simpler, cost is lower, decreases the branched column resistance of raw material due to slip capping " mouse cage " structure, accelerates further to produce speed;
4, the present invention is at the external steam distributor in wharf explosion body bottom, makes steam comply with its characteristic and is up uniformly distributed material bottom wharf explosion, material be heated pressurized evenly;
5, the whole material of the present invention all can be produced within the Millisecond time, and produce speed faster, material is fully decomposed, and material is produced evenly, and " raw ripe " is consistent;
6, in running of the present invention, raw material is not piled up, do not stick, thus is conducive to the full-automatic continuous seepage operation of overall process.
Accompanying drawing explanation
Fig. 1 is structural representation of the present invention;
Generalized section when Fig. 2 is wharf explosion sealing state in the present invention;
Fig. 3 be in the present invention wharf explosion feed intake state time structural representation;
Structural representation when Fig. 4 is wharf explosion blowing state in the present invention.
be labeled as in figure: 1. steam-flow meter, 2. steam valve, 3. pressure sensor, 4. feed hopper; 5. limit shaft overcoat, 6. position limiting structure, 7. stopping means support, 8. receiving hopper; 9. slipper seal dish, 10. wharf explosion, 11. steam distributors, 12. damping springs; 13. cylinder A fixed platforms, 14. cylinder protective sleeves, 15. cylinder A, 16. cylinder B fixed platforms; 17. cylinder B, 18. discharge buckets, 19. frames, 20. upper limit axles; sealing ring on 21., 22. lower seal, 23. lower seal dishes.
Detailed description of the invention
Embodiment
As Figure 1-4, the concrete structure of Steam explosive machine of the present invention is as follows:
It comprises feed hopper 4, receiving hopper 8, discharge bucket 18, wharf explosion 10, slipper seal dish 9, upper limit axle 20, lower seal dish 23, upper sealing ring 21, lower seal 22, cylinder A15, cylinder B17 and frame 19, described feed hopper 4 is up big and down small taper, the receiving hopper 8 of taper is connect below it, the below of receiving hopper 8 connects wharf explosion 10, discharge bucket 18 is located at the below of wharf explosion 10, discharge bucket is connected with frame, and frame 19 supports discharge bucket 18, and discharge bucket will be produced material and all collect packed.
Wherein: upper limit axle is arranged on slipper seal dish top and is positioned at receiving hopper, move on limit slippage seal disc, especially when slipper seal dish receives cylinder A active force up, upper limit axle can produce certain position-limiting action to the displacement of slipper seal dish, prevents it to be rushed out whole device;
Lower seal folds the effect bottom sealing wharf explosion, and lower seal dribbling is simultaneously moved slipper seal dish and moved down, and produces the quick-fried phenomenon of vapour;
Upper and lower sealing ring is corresponding with wharf explosion internal diameter size, between slipper seal dish and wharf explosion, plays the effect of sealing, and meanwhile, slipper seal dish is sliding up and down and realizing slipper seal in wharf explosion by upper sealing ring and lower seal;
Cylinder A provides motive force up for slipper seal dish, thus controls slipper seal dish and up move; Cylinder B provides pulling force down for slipper seal dish, thus controls slipper seal dish and down move.
Described slipper seal dish 9 is " work " font, its underpart is the conical disc structure that centre is high, surrounding is low, specifically, in the present embodiment, the top of described slipper seal dish 9 is disc, bottom is be the conical disc of 30-60 degree with bottom, and the angle of inclination of its conical surface can be determined according to actual conditions, and in general 50-60 degree is good.Slipper seal dish bottom is designed to " taper " dish, material in the quick-fried process of vapour is made to produce quicker, material is due to the effect of gravity, can along with the conical surface be toward surrounding landing, when producing generation, due to the effect on inclined-plane, raw material is more prone to landing and goes out, thus prevents the heap sum of raw material in wharf explosion to remain.Sealing slider disc 9 is placed in wharf explosion 10, the lower end of described upper limit axle 20 is sealed and matched integral by upper sealing ring 21 with the upper end of slipper seal dish 9, the lower end of slipper seal dish 9 is sealed and matched integral by lower seal 22 and lower seal dish 23, and slipper seal dish 9 is by upper sealing ring 21 and lower seal 22 sliding up and down and realize slipper seal in wharf explosion 10.
The bottom of upper limit axle 20 is be the conical disc of 30-60 degree with bottom, and the structure that its " taper " coils, makes in fill process, material feeding is quicker, raw material, due to the effect of gravity, can along with inclined-plane is toward surrounding landing, thus prevent the heap sum of raw material in fill process to remain.Sealed by sealing ring and slipper seal dish, and realize the positioning action to slipper seal dish.The outside of described upper limit axle 20 is provided with interior empty scaffolding schema corresponding to shape with it, this interior empty scaffolding schema comprises superposed limit shaft overcoat 5, be positioned at the stopping means support 7 of bottom and connect and position limiting structure 6 to slipper seal dish 9 position-limiting actions, the bottom of stopping means support 7 and the top of wharf explosion 10 are fixed, and upper limit axle 20 can slide up and down in interior empty scaffolding schema.
Described cylinder A15 is connected with the bottom of lower seal dish 23, and cylinder B17 is connected to the below of cylinder A15.Between cylinder A15 and lower seal dish 23, be provided with the damping spring 12 of cushioning effect, damping spring can alleviate the vibrations when cylinder produces in motion process.Cylinder A15 is located in cylinder A fixed platform 13, and cylinder B17 is located in cylinder B fixed platform 16, is provided with cylinder protective sleeve 14 at the skin of cylinder A15 and cylinder B17, and this cylinder protective sleeve, for the protection of two cylinders, is avoided suffering damage in the quick-fried process of vapour.In addition, a pressure sensor 3 be connected respectively with cylinder A15 and cylinder B17 is also set, described pressure sensor 3 is located on jet chimney, the jet chimney in pressure sensor 3 front is also provided with steam-flow meter 1 and steam valve 2, and steam-flow meter is for measuring the flow by this jet chimney.Pressure sensor is connected with cylinder B, and when there is pressure in wharf explosion, cylinder B is failure to actuate, and prevents slipper seal dish upward sliding from regurgitating.
At the warehouse bottom external ring-shaped steam distributor 11 of wharf explosion 10, this steam distributor 11 establishes several jetted hole be connected with wharf explosion 10 steam entrance, is played in wharf explosion being filled with steam by this annular steam distributor.Annular steam distributor makes steam comply with its characteristic to be up uniformly distributed material gradually bottom wharf explosion, material be heated pressurized evenly.
Operation principle of the present invention is as follows:
As shown in Figure 2, the slipper seal dish that wharf explosion is built-in is in hermetically sealed location status; Start cylinder A, slipper seal dish upward sliding is to upper surface; As shown in Figure 3, the unseal on wharf explosion top, wharf explosion is in feed state, and now material enters receiving hopper through cast hopper, then enters wharf explosion; After material is filled it up with, start cylinder A, slipper seal dish slide downward makes whole wharf explosion be in again hermetically sealed location status; Open steam valve, steam enters wharf explosion through steam distributor; When reaching predetermined pressure and osmotic equilibrium time, steam off valve stops admission, start cylinder B simultaneously, drive slipper seal dish quick linear slide downwards, thoroughly open wharf explosion cross section sealing, as shown in Figure 4, the whole cross section of cylinder body is exposed in air completely, material is quick-fried instantaneously to be penetrated, and enters discharge bucket completely; Start cylinder B, slipper seal dish upward sliding makes wharf explosion be in hermetically sealed location status completely, completes from being fed to the quick-fried process of whole vapour produced.
The present invention opens wharf explosion cross section by slipper seal dish upward sliding and realizes surrounding charging, just can reduce the charging aperture that intermediate feed pattern must set up to suspend or thread sealing device, and reduce by many pillars, equipment structure is simpler, cost is lower, and decrease the branched column resistance of raw material due to slip capping " mouse cage " structure, speed is produced in further quickening, the whole material of the present invention all can be produced within the Millisecond time, produce speed faster, material is fully decomposed, and material is produced evenly, and " raw ripe " is consistent.
The foregoing is only preferred embodiment of the present invention, not in order to limit the present invention, all any amendments done within the spirit and principles in the present invention, equivalent replacement and improvement etc., all should be included within protection scope of the present invention.
Claims (9)
1. a Steam explosive machine, comprise feed hopper (4), receiving hopper (8), discharge bucket (18) and wharf explosion (10), described feed hopper (4) is up big and down small taper, the receiving hopper (8) of taper is connect below it, the below of receiving hopper (8) connects wharf explosion (10), discharge bucket (18) is located at the below of wharf explosion (10), it is characterized in that: also comprise the slipper seal dish (9) be arranged in wharf explosion (10) cavity, be arranged on slipper seal dish (9) top and be positioned at the removable upper limit axle (20) of receiving hopper (8) for the displacement of limit slippage seal disc, be arranged on slipper seal dish (9) bottom and the removable lower seal dish (23) sealed bottom wharf explosion (10), the upper sealing ring (21) corresponding with wharf explosion internal diameter size, the lower seal (22) corresponding with wharf explosion internal diameter size, control slipper seal dish (9) the cylinder A(15 that up moves) and the cylinder B(17 that down moves of control slipper seal dish (9)), described slipper seal dish (9) is " work " font, its underpart is middle high, the conical disc structure that surrounding is low, the lower end of described upper limit axle (20) is sealed and matched integral by upper sealing ring (21) and the upper end of slipper seal dish (9), the lower end of slipper seal dish (9) is sealed and matched integral by lower seal (22) and lower seal dish (23), slipper seal dish (9) is sliding up and down and realizing slipper seal in wharf explosion (10) by upper sealing ring (21) and lower seal (22), described cylinder A(15) be connected with the bottom of lower seal dish (23), cylinder B(17) be connected to cylinder A(15) below.
2. Steam explosive machine as claimed in claim 1, it is characterized in that: the outside of described upper limit axle (20) is provided with interior empty scaffolding schema corresponding to shape with it, this interior empty scaffolding schema comprises superposed limit shaft overcoat (5), be positioned at the stopping means support (7) of bottom and connect and slipper seal dish (9) played to the position limiting structure (6) of position-limiting action, the bottom of stopping means support (7) and the top of wharf explosion (10) are fixed, and upper limit axle (20) can slide up and down in interior empty scaffolding schema.
3. Steam explosive machine as claimed in claim 2, is characterized in that: the bottom of upper limit axle (20) is be the conical disc of 30-60 degree with bottom.
4. Steam explosive machine as claimed in claim 2, is characterized in that: the top of described slipper seal dish (9) is disc, and bottom is be the conical disc of 30-60 degree with bottom.
5. Steam explosive machine as claimed in claim 1, it is characterized in that: in warehouse bottom external ring-shaped steam distributor (11) of wharf explosion (10), this steam distributor (11) establishes several jetted hole be connected with wharf explosion (10) steam entrance.
6. Steam explosive machine as claimed in claim 1, is characterized in that: described cylinder A(15) and lower seal dish (23) between be provided with the damping spring (12) of cushioning effect.
7. Steam explosive machine as claimed in claim 6; it is characterized in that: cylinder A(15) be located in cylinder A fixed platform (13); cylinder B(17) be located in cylinder B fixed platform (16), at cylinder A(15) and cylinder B(17) skin be provided with cylinder protective sleeve (14).
8. as the Steam explosive machine as described in arbitrary in claim 1-7, it is characterized in that: also comprise one with cylinder A(15) with cylinder B(17) pressure sensor (3) that is connected respectively, described pressure sensor (3) is located on jet chimney, and the jet chimney in pressure sensor (3) front is also provided with steam-flow meter (1) and steam valve (2).
9. Steam explosive machine as claimed in claim 8, is characterized in that: also comprise frame (19), and frame (19) supports discharge bucket (18).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310046686.3A CN103111231B (en) | 2013-02-06 | 2013-02-06 | Steam blasting machine |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201310046686.3A CN103111231B (en) | 2013-02-06 | 2013-02-06 | Steam blasting machine |
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| CN103111231A CN103111231A (en) | 2013-05-22 |
| CN103111231B true CN103111231B (en) | 2015-01-21 |
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| CN201310046686.3A Active CN103111231B (en) | 2013-02-06 | 2013-02-06 | Steam blasting machine |
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| CN203139981U (en) * | 2013-02-06 | 2013-08-21 | 李家民 | Steam blasting machine |
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| CN103111231A (en) | 2013-05-22 |
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Effective date of registration: 20170505 Address after: No. 999 road 629209 Suining City Tuopai Tuopai town in Sichuan County of Shehong Province Patentee after: SICHUAN TUOPAI SHEDE WINE CO., LTD. Address before: Bo Yu Road Taihe Town, Suining city 629200 Sichuan County of Shehong Province under section 214 Patentee before: Li Jiamin |