CN201053808Y - Vacuum continuous drying machine for viscous liquid and its slurry containing solid - Google Patents
Vacuum continuous drying machine for viscous liquid and its slurry containing solid Download PDFInfo
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- CN201053808Y CN201053808Y CNU2007200713521U CN200720071352U CN201053808Y CN 201053808 Y CN201053808 Y CN 201053808Y CN U2007200713521 U CNU2007200713521 U CN U2007200713521U CN 200720071352 U CN200720071352 U CN 200720071352U CN 201053808 Y CN201053808 Y CN 201053808Y
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- seal case
- dry zone
- continuous drier
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Abstract
The utility model relates to a vacuum continuous drier for solid dense liquid and other solid slurry material, and the utility model comprises a drier sealing box body, a continuous drying device which is fixed in the sealing box body, as well as a feeding device, a discharging device and a vacuum pumping device which are fixed on the sealing box body. The continuous drying device comprises a drying belt transmission device which is connected with two separated drying belt rollers and a drying belt which is arranged on the drying belt roller. The drying belt is provided with a heat device, a cooling device and a deviation-correcting device for the drying device. The feeding device comprises a raw material feeding pump, a raw material feeding tube and a raw material distributing device. The discharging device comprises a dry material discharging tube and a vacuum butterfly valve, and a dry material smashing device which is arranged on the sealing box body to match with the continuous drying device and the discharging device. Solid dense liquid and other solid slurry material can be dried continuously in a closed vacuum environment by using the utility model with high automatization degree. The labor intensity and the energy consumption are greatly reduced and the production efficiency is greatly improved, and the utility model is very environment protecting.
Description
Technical field
The utility model relates to technical field of drying, and particularly drying machinery field specifically is meant a kind ofly to contain solid thick liquid and other contains stereoplasm material vacuum continuous drier.
Background technology
For a long time, containing solid thick liquid and other drying that contains the stereoplasm material is to adopt vacuum drying oven to carry out drying mostly.Manually contain the stereoplasm material and be upside down in the metal dish containing solid thick liquid and other, on the coil pipe pavilion frame of putting vacuum drying oven into that coils, shut oven door then, vacuum drying oven is vacuumized, feeding steam or hot water heat in coil pipe simultaneously, make the water evaporates drying in the material.Because the contact-making surface of coil pipe and metal dish is smaller, the effect of heat transfer is just relatively poor, though under vacuum condition, drying time is still long, yields poorly, and energy consumption is also just big.Longer to the drying time of thick liquid especially, generally need 20-30h.And carrying out drying with vacuum drying oven all is manually-operated, and the charging discharging is wasted time and energy, and labour intensity is big, can not produce continuously again.Dried product caking,, need to pulverize, and the sticking dish of material to be many, cleans difficulty, the waste loss is also big.The employing spray dryer is also arranged, the belt air drier, equipment such as pneumatic drier and vacuum rotary dryer to contain solid thick liquid and other height contain the drying that the stereoplasm material carries out mostly can not be successful.For this reason, develop a kind of solid thick liquid and other of containing and contain the drying of the very big for example toothpaste type of the drying of stereoplasm material, particularly viscosity material, again can the quantity-produced vacuum dryer just very necessary.
The utility model content
The purpose of this utility model is to have overcome above-mentioned shortcoming of the prior art; provide a kind of solid thick liquid and other of containing to contain stereoplasm material vacuum continuous drier; make and contain the drying that solid thick liquid and other contain the stereoplasm material and can under the airtight vacuum environment, produce continuously; the automaticity height; labour intensity reduces greatly; energy consumption greatly descends, and production efficiency greatly improves, and very environmental protection.
In order to realize above-mentioned purpose, solid thick liquid and other of containing of the present utility model contains stereoplasm material vacuum continuous drier and has following formation:
A kind of solid thick liquid and other of containing contains stereoplasm material vacuum continuous drier, comprise drying machine seal case and the feed arrangement, drawing mechanism and the vacuum extractor that are fixed on the described drying machine seal case, be characterized in, also comprise continuous drier, described continuous drier is fixed in the described drying machine seal case, and described feed arrangement and described drawing mechanism cooperate with described continuous drier.
Described continuous drier comprises the dry zone transmission device, and two dry zone cylinders of the separation that is connected with described dry zone transmission device are positioned at the dry zone on the described dry zone cylinder and are arranged at the heater of described dry zone.
Described dry zone is the polytetrafluoroethylene (PTFE) dry zone; Described dry zone cylinder comprises axle, circle cylinder and is wrapped in the silicon rubber of described round cylinder appearance that described axle is connected with described dry zone transmission device; Described dry zone transmission device comprises decelerator and variable-frequency motor, and described decelerator is connected with described variable-frequency motor, and described reducer output shaft penetrates in the described drying machine seal case and is connected with the axle of described dry zone cylinder; Described heater is for comprising upper flat plate, and is following dull and stereotyped and at described upper flat plate and described guiding side's bar between the flat board down, welded closure and be provided with the slab construction that the heat medium turnover is taken over around the described guiding side bar; Perhaps described heater is for comprising upper flat plate and following cellular board, welded closure and be provided with the honeycomb slab construction that heat medium passes in and out adapter around described flat board and the described cellular board down.
Described continuous drier also comprises cooling device and dry zone deviation correcting device, and described cooling device is arranged at described dry zone, and described dry zone deviation correcting device cooperates described dry zone.
Described cooling device is for comprising upper flat plate, the following dull and stereotyped and guiding side's bar between described upper flat plate and described following flat board, welded closure and be provided with the slab construction that the heat medium turnover is taken over around the described guiding side bar, perhaps for comprising upper flat plate and following cellular board, welded closure and be provided with the honeycomb slab construction that heat medium passes in and out adapter around described flat board and the described cellular board down; The control cylinder that is positioned near the described dry zone both sides the described feed arrangement that described dry zone deviation correcting device comprises the displacement transducer that is installed on the described dry band edge, be positioned at the outer deviation correcting device of described drying machine seal case, connect the high temperature resistant wire of described displacement transducer and described deviation correcting device and be connected with described deviation correcting device.
Described drying machine seal case is provided with interface tube, instrumentation interface, movable end door, steam input device, condensation water discharge unit, water feed apparatus, discharging device and purging system.
Described feed arrangement comprises raw material feed pump and material feeding tube, and described material feeding tube is communicated with described raw material feed pump and described drying machine seal case, and described material feeding tube cooperates with described continuous drier.
Described feed arrangement also comprises the product distribution device, and described product distribution device is positioned at described drying machine seal case, and an end is communicated with described material feeding tube, and the other end cooperates with described continuous drier.
Described product distribution device comprises rotating shaft, be positioned at the stainless steel bearing of described drying machine seal case bottom, be positioned at the outer reductor of described drying machine seal case, motor and the product distribution pipe that has nozzle that is fixed in the described rotating shaft, described rotating shaft lower end is installed in the described stainless steel bearing of described drying machine seal case bottom, described rotating shaft upper end upwards passes described drying machine seal case and is connected with described reductor, described reductor is connected with described motor, described product distribution pipe free end is communicated with described material feeding tube, but described product distribution pipe is fixed in the described rotating shaft by a cover with clamping the block part up-down adjustment, and described nozzle cooperates with described continuous drier.
Described drawing mechanism comprises siccative discharge nozzle and vacuum butterfly valve, described siccative discharge nozzle one end cooperates with described continuous drier, the described siccative discharge nozzle other end is piercing in described drying machine seal case and a dry powder and is connected by bucket, and described vacuum butterfly valve is arranged at that the described siccative discharge nozzle of connection and described dry powder are subjected to bucket in the outer described siccative discharge nozzle of described drying machine seal case.
Above-mentioned solid thick liquid and other of containing contains stereoplasm material vacuum continuous drier and also comprises the siccative reducing mechanism, comprise siccative cutter sweep, dried biscuit pulverizer and the meal drawing mechanism that is connected described siccative cutter sweep and described dried biscuit pulverizer, described meal drawing mechanism is positioned on the described drying machine seal case, described siccative cutter sweep is positioned at described drying machine seal case and cooperates with described continuous drier, and described dried biscuit pulverizer is positioned at outside the described drying machine seal case and cooperates with described drawing mechanism.
Described siccative cutter sweep comprises the biside plate that is fixed in described drying machine seal case, is fixed in the described rotating shaft of described biside plate, and described rotating shaft is provided with revolving fragment, and described rotating shaft links to each other with a drive unit; Described meal drawing mechanism comprises conveying worm, transmission device, reductor and motor, described transmission device one end connects described conveying worm, the other end penetrates out described drying machine seal case and is connected with described reductor, and described reductor is connected with described motor; Described dried biscuit pulverizer adopts the paddle type mill structure, and the Circularhole diameter of the sieve plate of described dried biscuit pulverizer is 2mm～8mm.
Above-mentioned solid thick liquid and other of containing contains stereoplasm material vacuum continuous drier and also comprises electric and automatic control system, and described electric and automatic control system comprises temperature sensor, vacuum transducer, electric control system, frequency converter, programmable controller PLC and man-machine interface GOT.
Solid thick liquid and other of containing of the present utility model contains stereoplasm material vacuum continuous drier, changed the shortcoming that vacuum drying in the past can't continuous drying be produced, the automaticity height, labour intensity descends greatly, using electricity wisely, save steam, shorten dramatically drying time, can go out dry powder continuously at 45-90min generally speaking; Baking temperature is adjustable at any time, can select arbitrarily between 30-130 ℃, is fit to the dry requirement of heat sensitive material; Produce because vacuum tightness is dry, meet the GMP hygienic requirements, product loss is reduced to minimum degree, has improved yield, and can not pollute environment because of dust; The dry run non-oxidation takes place, and fragrance loss is reduced to minimum degree, and dried product instant capacity is good; Be equipped with automatic cleaning system, add the heat energy utilization in the dry run, can conveniently clean, the replacing of product just is very easy to.
Description of drawings
Fig. 1 is the structural representation of a specific embodiment of the present utility model.
The specific embodiment
In order more to be expressly understood technology contents of the present utility model, describe in detail especially exemplified by following examples.
See also shown in Figure 1, a kind of solid thick liquid and other of containing of the present utility model contains stereoplasm material vacuum continuous drier, mainly comprise drying machine seal case 1, be fixed in continuous drier 2 and the feed arrangement 3, drawing mechanism 4 and the vacuum extractor 5 that are fixed on the described drying machine seal case 1 in the described drying machine seal case 1, described feed arrangement 3 and described drawing mechanism 4 cooperate with described continuous drier 2, wherein:
Described dry zone cylinder 22 comprises axle, circle cylinder that metal material is made and the silicon rubber that is wrapped in described round cylinder appearance,
Described axle is connected with described dry zone transmission device 21, is divided into initiatively dry zone cylinder and passive dry zone cylinder.
It is necessary making the dry zone cylinder 22 at two ends drive the dry zone transmission device 21 that dry zones 23 move forward.The dry zone transmission device 21 that the utility model adopts comprises decelerator and variable-frequency motor, described decelerator is connected with described variable-frequency motor, described reducer output shaft penetrates in the described drying machine seal case 1 and is connected with the axle of described dry zone cylinder 22 through shaft coupling, thereby drives initiatively dry zone rollers running.Reducer input shaft connects variable-frequency motor, variable-frequency motor stepless speed regulation, the speed of control dry zone 23.The sealing device of dry zone transmission device 21 adopts mechanical seal and magnet fluid sealing on the drying machine seal case 1, fully guarantees sealing property.
The raw material of the needs drying that heater 24 can appendix on every layer of dry zone 23 heats.This heater 24 has adopted the structure of particular design, and heat medium better can distribute.The surface of whole heater is through smooth processing and polishing, makes surperficial intact cooperation of dry zone 23 and heater, effective conduction of assurance heat.The heater 24 that the utility model adopts can have two kinds of versions: a kind of is slab construction, comprise upper flat plate, following dull and stereotyped and at described upper flat plate and described guiding side's bar between the flat board down, welded closure and be provided with the heat medium turnover and take over around the described guiding side bar; Another kind is the honeycomb slab construction, comprises upper flat plate and following cellular board, welded closure and be provided with heat medium and pass in and out adapter around described flat board and the described cellular board down.Heat medium generally adopts steam, therefore also is provided with steam input device 11 and condensation water discharge unit 12 on the described drying machine seal case.
Described continuous drier 2 also comprises cooling device 25, described cooling device 25 be arranged at described dry zone 23 below.The cooling device 25 that adopts can cool off the material through super-dry that appendix on every layer of dry zone 23.This cooling device 25 has adopted the structure of particular design, and cooling medium better can distribute.The surface of whole cooler is through smooth processing and polishing, makes surperficial intact cooperation of dry zone 23 and cooler, effective conduction of assurance heat.The cooling device 25 that the utility model adopts has two kinds of versions: a kind of is slab construction, comprise upper flat plate, following dull and stereotyped and at described upper flat plate and described guiding side's bar between the flat board down, welded closure and be provided with the heat medium turnover and take over around the described guiding side bar; Another kind is the honeycomb slab construction, comprises upper flat plate and following cellular board, welded closure and be provided with heat medium and pass in and out adapter around described flat board and the described cellular board down.Cooling medium generally adopts water, therefore also is provided with water feed apparatus (cooling water pipe) 13 and discharging device 14 on the described drying machine seal case.
Described continuous drier 2 also comprises dry zone deviation correcting device 26, and described dry zone deviation correcting device 26 cooperates described dry zone 23.It is in order to make the guarantee of every layer of dry zone 23 normal operations that the utility model adopts dry zone deviation correcting device 26.Dry zone deviation correcting device 26 every layer of dry zone 23 are provided with a cover, can correct automatically in the wide cut scope of regulation dry zone 23 sideslips, guarantee normally operation in the effective range of dry zone 23 on dry zone cylinder 22.Described dry zone deviation correcting device 26 comprises the displacement transducer that is installed on described dry zone 23 limits, be positioned at the outer deviation correcting device of described drying machine seal case 1, connect near the control cylinder on described dry zone 23 both sides of the described feed arrangement of the high temperature resistant wire of described displacement transducer and described deviation correcting device and being positioned at of being connected with described deviation correcting device 3.The displacement transducer output signal, high temperature resistant wire is delivered to deviation correcting device with signal, transforms by electric signal, and control compressed air enters control cylinder in the drying machine seal case 1 by pipeline, passive dry zone cylinder is carried out suitably adjusting automatically, to regulate dry zone 23 relaxation degree.
The drying machine seal case 1 that the utility model adopts is all to install above-mentioned each device and parts and fixing metal shell.Drying machine seal case 1 is provided with various frames by its inside and meets the purging system of CIP cleaning requirement, drying machine seal case 1 is provided with and is used for the interface tube that public work connects and the interface of instrumentation, can guarantee that the two ends movable end door that the airtight production of drying machine can conveniently be opened again forms.Drying machine seal case 1 can be the metal cylinder of a horizontal circular and square metal cylinder, and the pipeline of steam input device 11, condensation water discharge unit 12, water feed apparatus (cooling water pipe) 13 and the discharging device of installing on it 14 also plays the effect of supporting cylindrical shell and heater 24 and cooling device 25.Drying machine seal case 1 is the pressure vessel that can bear negative pressure 0.1MPa.The purging system that the utility model adopts is suitably to be placed in groups to reach best cleaning performance by the fixing shower nozzle of a cover, and every group of shower nozzle is all by PLC control, and the injecting time of shower nozzle and program can be adjusted according to the characteristic of different product.
Described feed arrangement 3 comprises raw material feed pump 31 and material feeding tube 32, and described material feeding tube 32 is communicated with described raw material feed pump 31 and described drying machine seal case 1, and described material feeding tube 32 cooperates with described continuous drier 2.To contain solid thick liquid and other and contain the conveying of stereoplasm material raw material in order to solve, described raw material feed pump 31 of the present utility model has adopted screw pump.The screw pump good seal performance can be measured the speed with stepless speed regulation control charging, is fit to of the present utility modelly contain solid thick liquid and other contains the charging requirement of stereoplasm material vacuum continuous drier.On drying machine seal case 1, the rigidity that is interlinked to the outside in being equipped with is taken over, the inside and outside employing clip interface of taking over, outside clip interface connects raw material feed pump 31 outlet rigidity clips and takes over, inner clip interface and flexible pipe cooperate with described continuous drier 2, form whole material feeding tube 32 thus.
Described feed arrangement 3 also comprises product distribution device 33, and described product distribution device 33 is positioned at described drying machine seal case 1, one end and is communicated with described material feeding tube 32, and the other end cooperates with described continuous drier 2.Described product distribution device 33 comprises rotating shaft 34, be positioned at the stainless steel bearing of described drying machine seal case 1 bottom, be positioned at the reductor outside the described drying machine seal case 1, motor and the product distribution pipe 36 that has nozzle 35 that is fixed in the described rotating shaft 34, described rotating shaft 34 lower ends are installed in the described stainless steel bearing of described drying machine seal case 1 bottom, described rotating shaft 34 upper ends upwards pass described drying machine seal case 1 and are connected with described reductor, described reductor is connected with described motor, described product distribution pipe 36 free ends are communicated with described material feeding tube 32, being inner clip interface connects the import of the product distribution pipe 36 that has nozzle 35 by flexible duct, and described nozzle 35 cooperates with described continuous drier 2.In this nozzle 35 orifice plate is installed, it is the circular hole of 2mm～8mm that diameter can be selected according to various Material Characteristics in the aperture of orifice plate, and orifice plate is changed convenient.Soft health level pipeline adopts the soft pipeline that can bear negative pressure 0.1MPa, and pipeline material adopts silicon rubber, non-toxic polyvinyl chloride, and ethene, third is rare, polytetrafluoroethylene (PTFE).The material that rigidity is taken over and clip is taken over can adopt the stainless steel that meets hygienic requirements according to product performance.The purpose of employing clip interface can be for convenience detach and cleaning.
But described product distribution pipe 36 is fixed in the described rotating shaft 34 by a cover with clamping the block part up-down adjustment, and can adjust up and down, and described nozzle 35 cooperates with described continuous drier 2.Because product distribution pipe 36 can be adjusted up and down, and the distance between raw material nozzles 35 and the dry zone 23 is adjusted at the optimum position.By the electric machine controller of operation product distribution device 33, rotational angle, the rotating speed of rotating shaft 34 and the frequency of coming back rotation of control product distribution pipe 36.This controller set in advance each technological parameter before operation, produce needs to satisfy.Can out of service automatically and warning when control was lost efficacy.The function of electric machine controller also can be provided with in PLC and GOT.Can be arranged in the raw material optimal allocation on the dry zone 23 by this product distribution device 33, the wide cut that raw material is arranged can be adjusted, and adjusts back material wide cut and thickness basically identical.
Described drawing mechanism 4 comprises siccative discharge nozzle 41 and vacuum butterfly valve 42, described siccative discharge nozzle 41 other ends are piercing in described drying machine seal case 1 and a dry powder and is connected by bucket 43, and described vacuum butterfly valve 42 is arranged at and is communicated with described siccative discharge nozzle 41 and described dry powder in the outer described siccative discharge nozzle 41 of described drying machine seal case 1 and is subjected to barrels 43.The vacuum butterfly valve 42 that the utility model adopts is the necessary parts in order to make drying machine seal case 1 and dry powder isolated by bucket 43.When dry powder is subjected to bucket 43 placement dry powder to arrive to a certain degree, must change dry powder and be subjected to bucket 43, to operate vacuum butterfly valve 42 this moment and isolate, to guarantee that drying machine normally moves.
Described vacuum extractor 5 comprises vavuum pump 51 and is communicated with the vacuum tube 52 of described drying machine seal case 1 and described vavuum pump 51.
Above-mentioned solid thick liquid and other of containing contains stereoplasm material vacuum continuous drier and can also comprise siccative device for discharging 7, and described siccative device for discharging 7 is arranged on the described drying machine seal case 1 and cooperates with described continuous drier 2 and described drawing mechanism 4.
Described siccative device for discharging 7 comprises siccative cutter sweep 71, dried biscuit pulverizer 73 and the meal drawing mechanism 72 that is connected described siccative cutter sweep 71 and described dried biscuit pulverizer 73, described meal drawing mechanism 72 is positioned on the described drying machine seal case 1, described siccative cutter sweep 71 is positioned at described drying machine seal case 1 and cooperates with described continuous drier 2, and described dried biscuit pulverizer 73 is positioned at outside the described drying machine seal case 1 and cooperates with described drawing mechanism 4.
Described siccative cutter sweep 71 comprises the biside plate that is fixed in described drying machine seal case 1, is fixed in the described rotating shaft of described biside plate, and described rotating shaft is provided with revolving fragment, and described rotating shaft links to each other with a drive unit.The siccative cutter sweep 71 that the utility model adopts is tentatively to smash the device that is slit into small pieces to the dry biscuit of the one-tenth sheet of drying.Its rotating shaft is provided with swingle (sheet), and rotating shaft drives running by the travelling gear on the drum shaft.Swingle (sheet) direction of rotation is opposite with dry zone 23 traffic directions, easily the large stretch of siccative cake that constantly stretches out on the dry zone 23 is slit into small pieces.Can also be fixed with on the side plate can be movable scraper 74 and extension spring form.
Described meal drawing mechanism 72 comprises conveying worm, adopts the sealed gearing device of mechanical seal and magnet fluid sealing, and reductor and motor, described transmission device connect described conveying worm and described reductor, and described reductor is connected with described motor.The meal drawing mechanism 72 that the utility model adopts can be the dried biscuit lateral transfer of the small pieces of described siccative cutter sweep 71 generations to dried biscuit pulverizer 73.Meal drawing mechanism 72 can be in time the dried biscuit lateral transfer of small pieces in dried biscuit pulverizer 73, and in course of conveying, the dried biscuit of small pieces is crushed to that coarse granule is convenient further to be pulverized.
The dried biscuit pulverizer 73 that the utility model adopts is that the coarse granule siccative is ground into thinner granule powder, to reach product requirement.Described dried biscuit pulverizer 73 adopts the paddle type mill structures, and the available diameter of the circular hole of the sieve plate of described dried biscuit pulverizer 73 is 2mm～8mm, can change easily, and place under the vacuum environment and turn round.
Above-mentioned solid thick liquid and other of containing contains stereoplasm material vacuum continuous drier and also comprises electric and automatic control system.Described electric and automatic control system comprises temperature sensor, vacuum transducer, electric control system, frequency converter, programmable controller PLC and man-machine interface GOT.Can be to the inlet amount step-less adjustment of raw material feed pump 31; To the rotational angle of product distribution pipe 36, the rotating speed of rotating shaft and come the frequency of back rotation to regulate; The speed of service to dry zone 23 is carried out step-less adjustment; Heating-up temperature is controlled automatically and adjusted; Dry zone 23 automatic deviation corrections are controlled; Control to vacuum extractor 5 automatic controls and meal drawing mechanism 72 and dried biscuit pulverizer 73; To the setting of purging system and control automatically.
When using the utility model to carry out drying, contain solid thick liquid and other raw material that contains the stereoplasm material by raw material feed pump 31, enter in the drying machine seal case 1 by material feeding tube 32, round rotating operation through product distribution device 33, raw material waved be distributed on dry zone 23 surfaces, become the bed of material of certain wide cut and thickness.
By the running of dry zone transmission device 21, drive dry zone cylinder 22, dry zone cylinder 22 drives dry zone 23 and is moved toward the discharge end direction by feed end.By the steam pipe supplied heat source, control Steam Heating Self controlling valve to heater 24 heating, makes the material on the dry zone 23 obtain heating in the time of dry zone 23 operations.Because vavuum pump 51 is vacuumizing, the water evaporates vaporization on the dry zone 23 in the material, material obtains drying becomes dried cake, and through apparatus for supercooling 25, dried cake obtains cooling, and material hardens and becomes fragile, along with dry zone 23 moves toward the discharge end direction.Dried cake through supercooling is stretched out forward at the dry zone cylinder place of discharging place, in the running of siccative cutter sweep 71, the dried cake of stretching out constantly is slit into small pieces, freely falls, and falls in the meal drawing mechanism 72.The a small amount of material that is scraped by scraper 74 also falls in the meal drawing mechanism 72 simultaneously.Meal drawing mechanism 72 is input to dry material in the dried biscuit pulverizer 73 and pulverizes, and dry powder enters dry powder and is subjected to bucket 43 through vacuum butterfly valve 42.
Cooling water is provided by water feed apparatus (cooling water pipe) 13 and enters cooling device 25.Steam condensation water is got rid of by condensation water discharge unit 12.
To sum up, the utility model can realize containing solid thick liquid and other drying that contains the stereoplasm material is carried out under the airtight vacuum environment continuously, and the automaticity height reduces labour intensity and energy consumption greatly, and production efficiency greatly improves, and very environmental protection.
In this specification, the utility model is described with reference to its certain embodiments.But, still can make various modifications and conversion obviously and not deviate from spirit and scope of the present utility model.Therefore, specification and accompanying drawing are regarded in an illustrative, rather than a restrictive.
Claims (13)
1. one kind contains solid thick liquid and other and contains stereoplasm material vacuum continuous drier, comprise drying machine seal case and the feed arrangement, drawing mechanism and the vacuum extractor that are fixed on the described drying machine seal case, it is characterized in that, also comprise continuous drier, described continuous drier is fixed in the described drying machine seal case, and described feed arrangement and described drawing mechanism cooperate with described continuous drier.
2. solid thick liquid and other of containing as claimed in claim 1 contains stereoplasm material vacuum continuous drier, it is characterized in that, described continuous drier comprises the dry zone transmission device, two dry zone cylinders of the separation that is connected with described dry zone transmission device, be positioned at the dry zone on the described dry zone cylinder and be arranged at the heater of described dry zone.
3. solid thick liquid and other of containing as claimed in claim 2 contains stereoplasm material vacuum continuous drier, it is characterized in that described dry zone is the polytetrafluoroethylene (PTFE) dry zone; Described dry zone cylinder comprises axle, circle cylinder and is wrapped in the silicon rubber of described round cylinder appearance that described axle is connected with described dry zone transmission device; Described dry zone transmission device comprises decelerator and variable-frequency motor, and described decelerator is connected with described variable-frequency motor, and described reducer output shaft penetrates in the described drying machine seal case and is connected with the axle of described dry zone cylinder; Described heater is for comprising upper flat plate, and is following dull and stereotyped and at described upper flat plate and described guiding side's bar between the flat board down, welded closure and be provided with the slab construction that the heat medium turnover is taken over around the described guiding side bar; Perhaps described heater is for comprising upper flat plate and following cellular board, welded closure and be provided with the honeycomb slab construction that heat medium passes in and out adapter around described flat board and the described cellular board down.
4. solid thick liquid and other of containing as claimed in claim 2 contains stereoplasm material vacuum continuous drier, it is characterized in that, described continuous drier also comprises cooling device and dry zone deviation correcting device, described cooling device is arranged at described dry zone, and described dry zone deviation correcting device cooperates described dry zone.
5. solid thick liquid and other of containing as claimed in claim 4 contains stereoplasm material vacuum continuous drier, it is characterized in that, described cooling device is for comprising upper flat plate, the following dull and stereotyped and guiding side's bar between described upper flat plate and described following flat board, welded closure and be provided with the slab construction that the heat medium turnover is taken over around the described guiding side bar, perhaps for comprising upper flat plate and following cellular board, welded closure and be provided with the honeycomb slab construction that heat medium passes in and out adapter around described flat board and the described cellular board down; The control cylinder that is positioned near the described dry zone both sides the described feed arrangement that described dry zone deviation correcting device comprises the displacement transducer that is installed on the described dry band edge, be positioned at the outer deviation correcting device of described drying machine seal case, connect the high temperature resistant wire of described displacement transducer and described deviation correcting device and be connected with described deviation correcting device.
6. solid thick liquid and other of containing as claimed in claim 1 contains stereoplasm material vacuum continuous drier, it is characterized in that described drying machine seal case is provided with interface tube, instrumentation interface, movable end door, steam input device, condensation water discharge unit, water feed apparatus, discharging device and purging system.
7. solid thick liquid and other of containing as claimed in claim 1 contains stereoplasm material vacuum continuous drier, it is characterized in that, described feed arrangement comprises raw material feed pump and material feeding tube, described material feeding tube is communicated with described raw material feed pump and described drying machine seal case, and described material feeding tube cooperates with described continuous drier.
8. solid thick liquid and other of containing as claimed in claim 7 contains stereoplasm material vacuum continuous drier, it is characterized in that, described feed arrangement also comprises the product distribution device, described product distribution device is positioned at described drying machine seal case, one end is communicated with described material feeding tube, and the other end cooperates with described continuous drier.
9. solid thick liquid and other of containing as claimed in claim 8 contains stereoplasm material vacuum continuous drier, it is characterized in that, described product distribution device comprises rotating shaft, be positioned at the stainless steel bearing of described drying machine seal case bottom, be positioned at the outer reductor of described drying machine seal case, motor and the product distribution pipe that has nozzle that is fixed in the described rotating shaft, described rotating shaft lower end is installed in the described stainless steel bearing of described drying machine seal case bottom, described rotating shaft upper end upwards passes described drying machine seal case and is connected with described reductor, described reductor is connected with described motor, described product distribution pipe free end is communicated with described material feeding tube, but described product distribution pipe is fixed in the described rotating shaft by a cover with clamping the block part up-down adjustment, and described nozzle cooperates with described continuous drier.
10. solid thick liquid and other of containing as claimed in claim 1 contains stereoplasm material vacuum continuous drier, it is characterized in that, described drawing mechanism comprises siccative discharge nozzle and vacuum butterfly valve, described siccative discharge nozzle one end cooperates with described continuous drier, the described siccative discharge nozzle other end is piercing in described drying machine seal case and a dry powder and is connected by bucket, and described vacuum butterfly valve is arranged at that the described siccative discharge nozzle of connection and described dry powder are subjected to bucket in the outer described siccative discharge nozzle of described drying machine seal case.
11. solid thick liquid and other of containing as claimed in claim 1 contains stereoplasm material vacuum continuous drier, it is characterized in that, also comprise the siccative reducing mechanism, comprise siccative cutter sweep, dried biscuit pulverizer and the meal drawing mechanism that is connected described siccative cutter sweep and described dried biscuit pulverizer, described meal drawing mechanism is positioned on the described drying machine seal case, described siccative cutter sweep is positioned at described drying machine seal case and cooperates with described continuous drier, and described dried biscuit pulverizer is positioned at outside the described drying machine seal case and cooperates with described drawing mechanism.
12. solid thick liquid and other of containing as claimed in claim 11 contains stereoplasm material vacuum continuous drier, it is characterized in that, described siccative cutter sweep comprises the biside plate that is fixed in described drying machine seal case, be fixed in the described rotating shaft of described biside plate, described rotating shaft is provided with revolving fragment, and described rotating shaft links to each other with a drive unit; Described meal drawing mechanism comprises conveying worm, transmission device, reductor and motor, described transmission device one end connects described conveying worm, the other end penetrates out described drying machine seal case and is connected with described reductor, and described reductor is connected with described motor; Described dried biscuit pulverizer adopts the paddle type mill structure, and the Circularhole diameter of the sieve plate of described dried biscuit pulverizer is 2mm～8mm.
13. solid thick liquid and other of containing as claimed in claim 1 contains stereoplasm material vacuum continuous drier, it is characterized in that, also comprise electric and automatic control system, described electric and automatic control system comprises temperature sensor, vacuum transducer, electric control system, frequency converter, programmable controller PLC and man-machine interface GOT.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200713521U CN201053808Y (en) | 2007-06-20 | 2007-06-20 | Vacuum continuous drying machine for viscous liquid and its slurry containing solid |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200713521U CN201053808Y (en) | 2007-06-20 | 2007-06-20 | Vacuum continuous drying machine for viscous liquid and its slurry containing solid |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201053808Y true CN201053808Y (en) | 2008-04-30 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007200713521U Expired - Fee Related CN201053808Y (en) | 2007-06-20 | 2007-06-20 | Vacuum continuous drying machine for viscous liquid and its slurry containing solid |
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Cited By (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102288018A (en) * | 2011-06-07 | 2011-12-21 | 上海东富龙科技股份有限公司 | Automatic feeding device and method of vacuum freezer dryer |
| CN102716589A (en) * | 2011-03-30 | 2012-10-10 | 北京普照机电技术开发有限公司 | Hanging slurry type drying equipment |
| CN103047843A (en) * | 2013-01-11 | 2013-04-17 | 龙岩嘉麒生物科技有限公司 | Vacuum laminating belt type drier |
| CN103673517A (en) * | 2012-09-05 | 2014-03-26 | 天华化工机械及自动化研究设计院有限公司 | Preparation method of anhydrous sodium sulfide for PPS |
| CN103822451A (en) * | 2014-03-17 | 2014-05-28 | 无锡市海昌机械设备有限公司 | Material distributing system for vacuum belt liquid continuous dryer |
| CN103822461A (en) * | 2014-03-17 | 2014-05-28 | 无锡市海昌机械设备有限公司 | Improved structure of material distributing system for vacuum belt liquid continuous dryer |
| CN105758149A (en) * | 2016-04-29 | 2016-07-13 | 徐志勇 | Multilayer parallel-connection cross flow type Chinese wolfberry fruit drying machine |
| CN107192242A (en) * | 2017-07-19 | 2017-09-22 | 江西迪迪工业智能设备有限公司 | A kind of drier |
| CN107940911A (en) * | 2017-12-25 | 2018-04-20 | 安徽赛月环境科技有限公司 | Full-automatic wheat grain dewaterer |
| CN109099683A (en) * | 2018-07-09 | 2018-12-28 | 武汉美味源生物工程有限公司 | The drying means of vacuum belt drier and molasses mash |
| CN109157851A (en) * | 2018-07-09 | 2019-01-08 | 武汉美味源生物工程有限公司 | The drying means and device of yeast and its extract or extract |
| CN109566958A (en) * | 2018-12-12 | 2019-04-05 | 武汉美味源生物工程有限公司 | The method of drying and the sterilizing of the vacuum belt drier and its corn pulp of multiplayer microwave heating and sterilizing |
| RU2718632C1 (en) * | 2019-07-19 | 2020-04-10 | Общество С Ограниченной Ответственностью "Научно - Исследовательский Институт Технологий Органической, Неорганической Химии И Биотехнологий" | Multi-tap steam dryer |
| CN111043836A (en) * | 2019-12-27 | 2020-04-21 | 甘肃银光化学工业集团有限公司 | Low-temperature continuous vacuum belt type drying system and method for low-temperature vacuum belt type drying of energetic materials by adopting same |
| RU199951U1 (en) * | 2020-04-06 | 2020-09-29 | Общество с ограниченной ответственностью "Развитие Девелопмент" | VACUUM CHAMBER OF DRYER |
-
2007
- 2007-06-20 CN CNU2007200713521U patent/CN201053808Y/en not_active Expired - Fee Related
Cited By (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102716589A (en) * | 2011-03-30 | 2012-10-10 | 北京普照机电技术开发有限公司 | Hanging slurry type drying equipment |
| CN102288018A (en) * | 2011-06-07 | 2011-12-21 | 上海东富龙科技股份有限公司 | Automatic feeding device and method of vacuum freezer dryer |
| CN103673517A (en) * | 2012-09-05 | 2014-03-26 | 天华化工机械及自动化研究设计院有限公司 | Preparation method of anhydrous sodium sulfide for PPS |
| CN103673517B (en) * | 2012-09-05 | 2015-06-17 | 天华化工机械及自动化研究设计院有限公司 | Preparation method of anhydrous sodium sulfide for PPS |
| CN103047843A (en) * | 2013-01-11 | 2013-04-17 | 龙岩嘉麒生物科技有限公司 | Vacuum laminating belt type drier |
| CN103822451A (en) * | 2014-03-17 | 2014-05-28 | 无锡市海昌机械设备有限公司 | Material distributing system for vacuum belt liquid continuous dryer |
| CN103822461A (en) * | 2014-03-17 | 2014-05-28 | 无锡市海昌机械设备有限公司 | Improved structure of material distributing system for vacuum belt liquid continuous dryer |
| CN105758149A (en) * | 2016-04-29 | 2016-07-13 | 徐志勇 | Multilayer parallel-connection cross flow type Chinese wolfberry fruit drying machine |
| CN107192242A (en) * | 2017-07-19 | 2017-09-22 | 江西迪迪工业智能设备有限公司 | A kind of drier |
| CN107940911A (en) * | 2017-12-25 | 2018-04-20 | 安徽赛月环境科技有限公司 | Full-automatic wheat grain dewaterer |
| CN109099683A (en) * | 2018-07-09 | 2018-12-28 | 武汉美味源生物工程有限公司 | The drying means of vacuum belt drier and molasses mash |
| CN109157851A (en) * | 2018-07-09 | 2019-01-08 | 武汉美味源生物工程有限公司 | The drying means and device of yeast and its extract or extract |
| CN109566958A (en) * | 2018-12-12 | 2019-04-05 | 武汉美味源生物工程有限公司 | The method of drying and the sterilizing of the vacuum belt drier and its corn pulp of multiplayer microwave heating and sterilizing |
| RU2718632C1 (en) * | 2019-07-19 | 2020-04-10 | Общество С Ограниченной Ответственностью "Научно - Исследовательский Институт Технологий Органической, Неорганической Химии И Биотехнологий" | Multi-tap steam dryer |
| CN111043836A (en) * | 2019-12-27 | 2020-04-21 | 甘肃银光化学工业集团有限公司 | Low-temperature continuous vacuum belt type drying system and method for low-temperature vacuum belt type drying of energetic materials by adopting same |
| RU199951U1 (en) * | 2020-04-06 | 2020-09-29 | Общество с ограниченной ответственностью "Развитие Девелопмент" | VACUUM CHAMBER OF DRYER |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Vacuum continuous drying machine for viscous liquid and its slurry containing solid Effective date of registration: 20110106 Granted publication date: 20080430 Pledgee: Bank of Communications Ltd Shanghai Qingpu branch Pledgor: Shanghai Yuanyue Light Industry & Machinery Co., Ltd. Registration number: 2011990000004 |
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| C56 | Change in the name or address of the patentee |
Owner name: SHANGHAI UNIWIN PHARMACEUTICAL MACHINERY CO., LTD. Free format text: FORMER NAME: SHANGHAI YUANYUE LIGHT INDUSTRY AND MACHINERY CO., LTD. |
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| CP01 | Change in the name or title of a patent holder |
Address after: 201716 Shanghai city Qingpu Liantang Industrial Park steamed Xia Road No. 328 Patentee after: Shanghai Uniwin Pharmaceutical Machinery Co., Ltd. Address before: 201716 Shanghai city Qingpu Liantang Industrial Park steamed Xia Road No. 328 Patentee before: Shanghai Yuanyue Light Industry & Machinery Co., Ltd. |
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| PE01 | Entry into force of the registration of the contract for pledge of patent right |
Denomination of utility model: Vacuum continuous drying machine for viscous liquid and its slurry containing solid Effective date of registration: 20110106 Granted publication date: 20080430 Pledgee: Bank of Communications Ltd Shanghai Qingpu branch Pledgor: Shanghai Yuanyue Light Industry & Machinery Co., Ltd. Registration number: 2011990000004 |
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Granted publication date: 20080430 Termination date: 20160620 |