CN202532844U - Filtering washing vacuum boiling dryer - Google Patents
Filtering washing vacuum boiling dryer Download PDFInfo
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- CN202532844U CN202532844U CN2012201018210U CN201220101821U CN202532844U CN 202532844 U CN202532844 U CN 202532844U CN 2012201018210 U CN2012201018210 U CN 2012201018210U CN 201220101821 U CN201220101821 U CN 201220101821U CN 202532844 U CN202532844 U CN 202532844U
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
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- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The utility model relates to a filtering washing vacuum boiling dryer which comprises a vertical drying main machine capable of achieving heat transfer through a jacket. A rotary shaft of a stirrer of the vertical drying main machine is provided with a crushing blade for crushing materials, a first paddle and a second paddle, wherein the first paddle and the second paddle are used for turning over the materials to achieve mixing. When the rotary shaft rotates, the first paddle and the second paddle are used for respectively turning over the materials downwards and upwards to enable the materials to form eddy which performs revolution around the rotary shaft between the first paddle and the second paddle, so that the materials can perform rotation along with the eddy when rotating around the rotary shaft, running distance of the materials is prolonged, material turning over times are increased, and purity degree of the washing materials and drying efficiency in the drying process are improved. Besides, filter cake stratification can be broken when filtering is performed so that the filtering is full and thorough. The dryer is suitable for products or preparations in filter cakes shapes or crystalline states in industries of biology, pharmacy, chemical and the like, wherein the products or preparations are easy to oxidize, are subjected to washing through soft water or organic solvent, disinfection and sterilization, washing through solvent, crushing and palletizing in the production process, and achieve vacuum drying at terminals.
Description
Technical field
The utility model relates to the technical field of drying equipment; Specifically be filtration washing vacuum, boiling drier, be applicable to filter cake shape, crystalloid and the easy oxidation of industries such as biology, pharmacy, chemical industry, in process of production need soft water or organic solvent washing, sterilization, solvent washing, broken, granulate and vacuum drying goods or preparation at the terminal.
Background technology
At present, the distinctive easy oxidation filter cake shape of industry, crystalloid goods or preparation intermediate feed such as domestic biology, medicine, chemical industry, and at art production process need soft water or organic solvent washing, and need many kinds base-material to mix.With need granulate to the fragmentation of filter cake shape, block raw material and terminal and realize vacuum drying again and obtain the raw material finished product.All continue to use traditional unit production operation, promptly accomplish product single processing step in above-mentioned explained hereafter with the technical functionality of unit.Cause the production technology link many therefrom, the production cycle is long, and in the technology circulation, increases the logistics cross pollution, and the technological deficiencies such as increase of fixed cost of production, and is unfavorable for the research and development of new product or the industry production of above-mentioned relevant industries.How a kind of compile washing, filtration, mixing, fragmentation are provided; And accomplish vacuum drying in the multi-functional serviceability of one at the terminal; And in dry production process, realizing the multi-functional dry machine system to the condensing and recycling recycle that contains organic solvent, is the technical barrier of this area.
The utility model content
The technical problem that the utility model will solve provides a kind of simple in structure, to the crushing effect of caking materials better and be suitable for improving filtration washing vacuum, the boiling drier of drying efficiency.
For solving the problems of the technologies described above; Filtration washing vacuum, boiling drier that the utility model provides; Comprise the vertical main drying that chuck conducts heat; Be provided with agitator in this main drying, be characterized in: the rotating shaft of this agitator is provided with the broken blade that is used for particle, first, second blade that is used for the stirring mixing; Broken blade, first, second blade distributes from top to bottom; When said rotating shaft was rotated, first, second blade was suitable for respectively downwards, the stirring that makes progress, thereby made material between first, second blade, form the eddy current of revolution around the shaft; And then make material in rotation around the shaft; With said eddy current rotation, so prolonged material range ability, increased the stirring number of times, improved the degree of purity of washing material and the drying efficiency in the dry run; When filtering, can break filter cake knot layer simultaneously, make and filter fully thoroughly.
The said second blade lower end is provided with orifice plate or web plate; Orifice plate or web plate below are provided with coil exchanger, and the below of this coil exchanger is in the main drying bottom and is provided with the hot blast air outlet; On the sidewall of main drying, be provided with discharging opening with the said second blade equal-height position.
The top center of said main drying is provided with the seal sleeve that is used to be provided with said rotating shaft; The top seal of sealing sleeve is provided with the variable-frequency motor that links to each other with said rotating shaft; The middle part of sealing sleeve is provided with feeding mouth; Sealing is provided with the screw feeder that is suitable for fast sealing on this feeding mouth, is provided with the material scraping plate with the little matched in clearance of inwall of said seal sleeve in the rotating shaft in said seal sleeve and below said feeding mouth.
The top of closing on said main drying is provided with: be suitable for the rotating wash bowl and the shower nozzle that is used to spray high-temperature vapor or sterilized solution that are used to spray soft water or organic solvent or cleaning fluid of 360 degree rotations, to realize sterilization.When washing work, its cleaning solution is imported through delivery pump, and the hydraulic pressure that has input to produce impels the rotor high-speed rotation of rotating wash bowl; Its cleaning solution when stirring stirring, is realized the washing to base-material through the ejection of spheroid pod apertures; And in the sterilization process, steam or sterilized solution then penetrate through shower nozzle, so that reach the technological requirement of sterilization; Finally the assorted drainage that contains of warp washing is discharged by vacuum filtration by the compound seat shape of the spiral-flow type in container web plate, and when organic solvent washed, its filtrating was then vacuumizing the collection of entering solvent recovery surge tank; In view of the requirement that improves rate of drying, this dry main frame is provided with coil exchanger in the bottom of main drying except that adopting the chuck heat transfer; So that when drying, realize that chuck conducts heat and the comprehensive conduction heating of coil pipe heat exchange, thereby improve dry tenacity; Shorten the production technology time, improve the practicality effect of production capacity.
As a kind of scheme of optimization, said broken blade comprises at least: a pair of symmetrically arranged long blade and a pair of symmetrically arranged shortened cutting blade.The blade that adopts is different in size, and blade is suitable for broken agglomerate material on the one hand, and the big remaining space reserved of shortened cutting blade is suitable for realizing quick blanking, to improve drying efficiency on the other hand.
As the scheme of concrete optimization, said broken blade is M shape, and it comprises: the shortened cutting blade of the long blade of two pairs of crossing distribution and two pairs of crossing distribution; The length of shortened cutting blade is 1/3 to 1/2 of long blade; Angles such as each blade distribute.
As a kind of scheme of optimization, the interface of the long and short blade of said broken blade is rounded, to avoid buildup on long and short blade as far as possible.
The main drying of the utility model is built-in with the M shape blade with broken function and a pair of blade of stirring mixed function, and the blade leaf of M shape blade is different in size, so that when work; Material when the screw feeder pusher gets into, can reach broken completely material by the container top, and the blade that a pair of stirring is used then is distributed as forward and reverse blade; So that when work, about reaching, outside inwards comprehensive stirring; Avoid the dead angle, reach the uniformity of washing quality, when the discharging of discharging opening product; Can realize the pusher discharge again, reach the function of self-emptying.
As preferred scheme, top one side of said main drying is provided with vapours outlet, and this vapours outlet links to each other through the top liquid inlet that a heat exchanger, distributed upright condenser and are used to collect the surge tank of solvent successively; Said vapours outlet also links to each other with sack cleaner, air-introduced machine and water dust scrubber successively.Said surge tank links to each other with a vacuum unit, and when the material of required drying was slurry, the vacuum unit was used for said main drying is carried out vacuum filtration, and said screen pack is suitable for realizing separating of material and liquid.
The intake line of heat exchanger is provided with first control valve, and the intake line of sack cleaner is provided with second control valve.
As the scheme of further optimization, be distributed with upright cooling tube in the said distributed upright condenser, the top of each upright cooling tube is provided with the disc type liquid distributor; Be distributed with through hole on this disc type liquid distributor, the central authorities of disc type liquid distributor are provided with the overflow ring, and the inlet bottom of said distributed upright condenser extends downward in the said overflow ring, so that be suitable for all sending in the overflow ring from gas, the liquid of said heat exchanger; During use; Gas, liquid in the overflow ring is suitable for to evenly overflowing all around; And be distributed on the main body of said disc type liquid distributor, so that through the gas of this disc type liquid distributor, the top that liquid is uniformly distributed in described each upright cooling tube, and then improved condensation effect; The inadequate problem of condensation of having avoided cloth liquid inequality to cause has improved the rate of recovery of useful component.
Said heat exchanger and distributed upright condenser constitute B-grade condensation volatilization Solvent Recovery Unit; It is the design that the utility model adaptation energy-saving and emission-reduction and low-carbon (LC) production are carried out; It is through the different designs of secondary condenser; So that the recovery technical process at the gasification solvent flashing that is heated improves the rate of recovery, and the consumption that further economizes on resources reduces manufacturing enterprise's operating cost.Through improving solvent recovering rate, be beneficial to the improvement of production environment, realize regeneration.Condenser has filter bag, folding corrugated fin, and the flow guide pipe, compositions such as inlet channel and fluid course, through the compacting stack of multilayer folding corrugated fin, and firm with seal form, so that form labyrinth type gas channel and fluid course.
During Solvent Recovery Unit work, first control valve is opened, and second control valve is closed; By the gasification volatilization gas input heat exchanger that main drying is discharged, volatilization gas and cooling fluid are realizing the partition heat exchange in the passage separately, so that volatilization gas is accepted the cooling heat transferring process of cooling fluid; Be converted into gas-liquid by gas, the gravitation that its gas-liquid vacuumizes along with the vacuum unit gets into secondary coolers (being distributed upright condenser) then; Secondary coolers is formed by gas-liquid channel and freezing liquid combination of channels respectively; Realize heat exchange in same gas-liquid and the carrying out of cooling fluid in passage separately, gas-liquid (35 ℃) receives the cooling of freezing liquid (3 ℃), promptly is converted into to reveal liquid (8 ℃); Compile by secondary coolers lower end design collecting pipe thus and be delivered to the solvent recovery surge tank, the overall process that the completion solvent condenses reclaims.
Scheme as further optimization; For the pressure that solves in the overflow ring causes local gas distribution, the uneven problem of liquid greatly; Through hole number in the overflow ring is less than the through hole number of this disc type liquid distributor remainder, or the through-hole diameter in the overflow ring is less than the through-hole diameter of this disc type liquid distributor remainder.
As further preferred scheme, the central distribution of contiguous said orifice plate has the inclined hole of arranging towards counterclockwise; The remainder of this orifice plate is distributed with the inclined hole towards arranged clockwise.During use, behind this orifice plate of hot blast process from main drying bottom air outlet, form many ascending airs opposite to the hand of spiral; Be beneficial to the formation of turbulent flow; Be beneficial to heat transfer medium, further prolong range ability, the increase stirring number of times of material, improve drying effect and drying efficiency.
Web plate is used for satisfying at washing, filter process makes impurity separate with filtrating, and for adapting to the instructions for use of different classes of organic cleaning solution, web plate is a seat shape net; It adopts stainless steel nickel sintering, and its opening of sieve is not waited by 5um～0.1mm, satisfies the required filtration of different process raw material thus and takes off liquid; Seat shape filter screen is pulled the middle and lower part of being located at main drying; And adopt fast-assembling to change the formula structure, and clear in order in use installation and folding, have pure, safety for reaching the seat filter screen; Durable use, the web plate of the utility model comprise protective layer, water conservancy diversion layer, filter course and the supporting layer that sets gradually up and down.
Protective layer is the bigger wire netting of mesh, has shock resistance and anti-impurity ability, through the protection of protective layer, so that the safety in explained hereafter, guarantee to produce normal operation; The water conservancy diversion layer is the orifice plate that is evenly distributed with the water conservancy diversion through hole; It is guiding with the pod apertures, promptly flows into the liquid that takes off of filter screen through washing, through the distribution of water conservancy diversion layer; So that reaching flow is evenly distributed; The inhomogeneities of evading because of flow quantity causes hydrops to influence washing quality, through the even distribution of water conservancy diversion layer, finally reaches the overanxious quality of pure washing; Filter course is the less filter screen of mesh, accomplishes filtration or separation to washing impurity, so that guarantees the purity of raw materials technology and design; Supporting layer then is a bracing frame, is used to safeguard live load that washing and filtering carries, the organic assembling of the bearing capacity through four different process, so that accomplish different material or intermediate goods, the required filtration washing operation of technology.
Air-introduced machine and water dust scrubber adopt micronic dust water film dedusting technology, are that the utility model is realized the art designs that low-carbon (LC) is produced, and its purpose is better to improve production environment; Reduce the toxic emission in producing to greatest extent, air-introduced machine and water dust scrubber are located at the end of the exhaust of powder dedusting, and it comprises the washing shower nozzle of one-level, secondary; To carry out spray washing by the waste gas that Vacuum exhaust tube is discharged; Reach in the discharging waste gas and absorption cleaning through shower water, it absorbs shower water recycle through filtering again, reduces the toxic emission in producing to greatest extent; The optimization production environment reaches the purpose that low-carbon (LC) is produced.
The multi-functional dry machine system of the utility model is suitable for adopting the man-machine interface Based Intelligent Control; Realize the programming Control to process datas such as heat transfer temperature, cooling heat transferring temperature, frequency control, cleaning solution flow, the switching of surge tank air pressure, vacuum pressures with process programming, data show the operation with PLC, realize man-machine interface; Interactive control operation management; So that reach quick, convenient, modern management level accurately; Its control device can be included relevant enterprise control centre in simultaneously, realizes the net working operation management.
The technique effect that the utlity model has: filtration washing vacuum, the boiling drier of (1) the utility model is applicable to filter cake shape, crystalloid and the easy oxidation of industries such as biology, pharmacy, chemical industry, needs soft water or organic solvent filtration washing, sterilization, solvent recovery, fragmentation, granulation and the drying production of vacuum drying goods or preparation at the terminal in production process.The filtration washing vacuum of utility model, boiling drier comprise: vertical chuck heat transfer vacuum tank (being main drying), and one-level composition board type condenser, the washing that combined type cooler and solvent recovery jar are formed, sterilization, dry airtight vacuum system granulates.Vacuum tank is built-in with: broken materials device, forward and reverse revolving vane and frequency control agitator, container inner top do not have 360 degree rotation rotating wash bowl and shower nozzles, and the agitator below is equipped with renewable compound eddy flow seat shape web plate, and its bottom is a coil exchanger.When laundry operation, the forward and reverse mixing stirring of agitator, rotating wash bowl spray washing liquid and vacuum filtration integrated application; Accomplish washing function, when dry then, then vacuumize chuck and conduct heat; Spiral heater conduction heat exchange; So that improve rate of drying, along with the organic solvent gasification of being heated, volatilization gas cools off and solvent is recovered with vacuumizing through B-grade condensation.Adopt high-temperature vapor or sterilized solution, so that reach the sterilization of material, so that accomplish sterilization at same equipment, washing, drying, multi-functional practicality such as solvent recovery.(2) the filtration washing vacuum of the utility model, boiling drier adopt the vacuum jacket heat transfer technology respectively, and dynamic agitation stirring hybrid technology is expected particle soon, 360 degree rotation rotating wash bowl washings; Spray, sterilization, so that, realize dynamically washing in material washing process process; Remove intermediate feed impurity, reach washing evenly, the washing and cleaning operation effect of high purity is then in the vacuum drying process process; This machine is employed on the basis of vacuum jacket heat transfer, at container bottom the coiled heating is set simultaneously, so that improves rate of drying and dry production capacity; Adopt one-level simultaneously, the B-grade condensation cooling technology is implemented in the recovery of drying process volatilization solvent; Adopt the water film dedusting technology in addition, realize spray washing, reach clean specification requirement of producing dry micronic dust.
Description of drawings
For the content that makes the utility model is more clearly understood, below basis specific embodiment and combine accompanying drawing, the utility model is done further detailed explanation, wherein
Fig. 1 is the filtration washing vacuum of utility model, the structural representation of boiling drier;
Fig. 2 is the radial section figure of the disc type liquid distributor of the utility model;
Fig. 3 is the vertical view of said disc type liquid distributor;
Fig. 4 is the lateral plan of the broken blade of M shape of the utility model;
Fig. 5 is the vertical view of the broken blade of M shape of the utility model;
Fig. 6 is the lateral plan of first blade of the utility model;
Fig. 7 is the another side view of said first blade;
Fig. 8 is the vertical view of described first blade;
Fig. 9 is the lateral plan of second blade (stirrer paddle) of the utility model;
Figure 10 is the another side view of said second blade;
Figure 11 is the structural representation of said orifice plate.
The specific embodiment
Below in conjunction with accompanying drawing and embodiment the utility model is elaborated:
Like Fig. 1, the filtration washing vacuum of present embodiment, boiling drier comprise: drum type brake main drying 1, heat exchanger 2, distributed upright condenser 3; Surge tank 4, vacuum unit 5, just effect, medium effeciency filter 6; Air blast 7, steam heater 8, high efficiency particulate air filter 9; Sack cleaner 10, air-introduced machine and water dust scrubber 11.Main drying 1 is the cylinder of spacer heating, and heat exchanger 2 is efficient plate type heat exchanger.
Just effect, medium effeciency filter 6 link to each other with the air outlet of main drying 1 bottom through air blast 7, steam heater 8, high efficiency particulate air filter 9 successively; Top one side of said main drying 1 is provided with vapours outlet, and this vapours outlet links to each other through the top liquid inlet that a heat exchanger 2, distributed upright condenser 3 and are used to collect the surge tank 4 of solvent successively; Said vapours outlet also links to each other with sack cleaner 10, air-introduced machine and water dust scrubber 11 successively.
On the pipeline that the inlet with said heat exchanger 2 and sack cleaner 10 links to each other, be respectively equipped with first control valve 21 and second control valve 22.
Be provided with rotating shaft 1-1 in the said main drying 1, in main drying 1, said rotating shaft 1-1 is provided with the broken blade 1-3 that is used for particle, the first blade 1-4, the second blade 1-5 that is used for the stirring mixing; Broken blade 1-3, the first blade 1-4, the second blade 1-5 distribute from top to bottom; Towards on the contrary, and during said rotating shaft 1-1 rotation, the first blade 1-4, the second blade 1-5 be suitable for respectively downwards, stirring upwards like the blade of Fig. 7 and 10, the first blade 1-4, the second blade 1-5.
Like Figure 4 and 5, said broken blade 1-3 is M shape, and it comprises: the shortened cutting blade of the long blade of two pairs of crossing distribution and two pairs of crossing distribution; The length of shortened cutting blade is 1/3 to 1/2 of long blade; Angles such as each blade distribute.The interface of the long and short blade of said broken blade 1-3 is rounded, to avoid buildup on long and short blade as far as possible.
The said second blade 1-5 lower end is provided with orifice plate 1-7 or web plate; Orifice plate 1-7 or web plate below are provided with coil exchanger 1-8, and the below of this coil exchanger 1-8 is in main drying 1 bottom and is provided with the hot blast air outlet; On the sidewall of main drying 1, be provided with discharging opening 1-6 with the said second blade 1-5 equal-height position.
Like Fig. 1 to 3, be distributed with upright cooling tube 3-1 in the said distributed upright condenser 3, the top of each upright cooling tube 3-1 is provided with disc type liquid distributor 3-2; Be distributed with through hole on this disc type liquid distributor 3-2; The central authorities of disc type liquid distributor 3-2 are provided with overflow ring 3-20; The inlet bottom of said distributed upright condenser 3 extends downward in the said overflow ring 3-20, so that be suitable for all sending in the overflow ring 3-20 from gas, the liquid of said heat exchanger 2; During use; Gas, liquid in the overflow ring 3-20 is suitable for to evenly overflowing all around; And be distributed on the main body of said disc type liquid distributor 3-2, so that be uniformly distributed in the top of described each upright cooling tube 3-1 through gas, the liquid of this disc type liquid distributor 3-2, and then improved condensation effect; The inadequate problem of condensation of having avoided cloth liquid inequality to cause has improved the rate of recovery of useful component.
Like Fig. 3; For the pressure that solves in the overflow ring 3-20 causes local gas distribution, the uneven problem of liquid greatly; Through hole number in the overflow ring 3-20 is less than the through hole number of this disc type liquid distributor 3-2 remainder, or the through-hole diameter in the overflow ring 3-20 is less than the through-hole diameter of this disc type liquid distributor 3-2 remainder.
The central distribution of contiguous said orifice plate 1-7 has the inclined hole of arranging towards counterclockwise; The remainder of this orifice plate 1-7 is distributed with the inclined hole towards arranged clockwise.During use, behind this orifice plate of hot blast process from main drying bottom air outlet, form many ascending airs opposite, be beneficial to range ability, the increase stirring number of times of further prolongation material, improve drying effect and drying efficiency the hand of spiral.
Said surge tank 4 links to each other with a vacuum unit 5, and when the material of required drying was slurry, vacuum unit 5 was used for said main drying is carried out vacuum filtration, and said screen pack is suitable for realizing separating of material and liquid.
The top center of said main drying 1 is provided with the seal sleeve 15 that is used to be provided with said rotating shaft 1-1; The top seal of sealing sleeve 15 is provided with the variable-frequency motor 16 that links to each other with said rotating shaft 1-1; The middle part of sealing sleeve 15 is provided with feeding mouth; Sealing is provided with the screw feeder 12 that is suitable for fast sealing on this feeding mouth, is provided with the material scraping plate 1-2 with the little matched in clearance of inwall of said seal sleeve 15 on the rotating shaft 1-1 in said seal sleeve 15 and below said feeding mouth.
The top of closing on said main drying 1 is provided with: be suitable for the rotating wash bowl 13 and the shower nozzle 14 that is used to spray high-temperature vapor or sterilized solution that are used to spray soft water or organic solvent or cleaning fluid of 360 degree rotations, to realize sterilization.
Obviously, the foregoing description only be for explain clearly that the utility model does for example, and be not to be qualification to the embodiment of the utility model.For the those of ordinary skill in affiliated field, on the basis of above-mentioned explanation, can also make other multi-form variation or change.Here need not also can't give exhaustive to all embodiments.And conspicuous variation that these spirit that belong to the utility model are extended out or change still are among the protection domain of the utility model.
Claims (6)
1. a filtration washing vacuum, boiling drier comprise being provided with agitator in the main drying, it is characterized in that: the rotating shaft of this agitator is provided with the broken blade that is used for particle, is used for first, second blade that stirring mixes; Broken blade, first, second blade distributes from top to bottom; When said rotating shaft was rotated, first, second blade was suitable for respectively downwards, stirring makes progress;
The top center of said main drying is provided with the seal sleeve that is used to be provided with said rotating shaft; The top seal of sealing sleeve is provided with the variable-frequency motor that links to each other with said rotating shaft; The middle part of sealing sleeve is provided with feeding mouth; Sealing is provided with the screw feeder that is suitable for fast sealing on this feeding mouth, is provided with the material scraping plate with the little matched in clearance of inwall of said seal sleeve in the rotating shaft in said seal sleeve and below said feeding mouth;
Top one side of said main drying is provided with vapours outlet, and this vapours outlet links to each other through the top liquid inlet that a heat exchanger, distributed upright condenser and are used to collect the surge tank of solvent successively; Said vapours outlet also links to each other with sack cleaner, air-introduced machine and water dust scrubber successively; Said surge tank links to each other with a vacuum unit.
2. filtration washing vacuum according to claim 1, boiling drier is characterized in that: said broken blade comprises at least: a pair of symmetrically arranged long blade and a pair of symmetrically arranged shortened cutting blade.
3. filtration washing vacuum according to claim 1, boiling drier is characterized in that: said broken blade is M shape, and it comprises: the shortened cutting blade of the long blade of two pairs of crossing distribution and two pairs of crossing distribution.
4. according to the described filtration washing vacuum of one of claim 1 to 3, boiling drier, it is characterized in that: the said second blade lower end is provided with orifice plate or web plate; Orifice plate or web plate below are provided with coil exchanger, and the below of this coil exchanger is in the main drying bottom and is provided with the hot blast air outlet; On the sidewall of main drying, be provided with discharging opening with the said second blade equal-height position.
5. filtration washing vacuum according to claim 4, boiling drier is characterized in that: the central distribution of contiguous said orifice plate has the inclined hole of arranging towards counterclockwise; The remainder of this orifice plate is distributed with the inclined hole towards arranged clockwise.
6. filtration washing vacuum according to claim 4, boiling drier is characterized in that: said web plate comprises protective layer, water conservancy diversion layer, filter course and the supporting layer that sets gradually up and down; Protective layer is the bigger wire netting of mesh, and the water conservancy diversion layer is the orifice plate that is evenly distributed with the water conservancy diversion through hole, and filter course is the less filter screen of mesh, and supporting layer is made up of a bracing frame.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012201018210U CN202532844U (en) | 2012-03-16 | 2012-03-16 | Filtering washing vacuum boiling dryer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2012201018210U CN202532844U (en) | 2012-03-16 | 2012-03-16 | Filtering washing vacuum boiling dryer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202532844U true CN202532844U (en) | 2012-11-14 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2012201018210U Expired - Fee Related CN202532844U (en) | 2012-03-16 | 2012-03-16 | Filtering washing vacuum boiling dryer |
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| Country | Link |
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| CN (1) | CN202532844U (en) |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103438670A (en) * | 2013-08-29 | 2013-12-11 | 南京华星制药设备有限公司 | Boiling type drying bed provided with automatic washing device |
| CN105000778A (en) * | 2015-07-10 | 2015-10-28 | 江苏玖盛水处理科技有限公司 | Sludge reduction processing system |
| CN106461329A (en) * | 2014-04-07 | 2017-02-22 | Brinox公司 | Horizontal paddle dryer |
| CN106890494A (en) * | 2017-03-24 | 2017-06-27 | 吴琏 | Benzalkonium chloride suction filtration purifying plant |
| CN107553772A (en) * | 2017-10-17 | 2018-01-09 | 苏州宏泉高压电容器有限公司 | A kind of uniform feeding formula color masterbatch drying machine |
| CN113324378A (en) * | 2021-03-26 | 2021-08-31 | 上海迪化科技股份有限公司 | Novel filtering, washing and drying integrated device and process |
-
2012
- 2012-03-16 CN CN2012201018210U patent/CN202532844U/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103438670A (en) * | 2013-08-29 | 2013-12-11 | 南京华星制药设备有限公司 | Boiling type drying bed provided with automatic washing device |
| CN106461329A (en) * | 2014-04-07 | 2017-02-22 | Brinox公司 | Horizontal paddle dryer |
| CN105000778A (en) * | 2015-07-10 | 2015-10-28 | 江苏玖盛水处理科技有限公司 | Sludge reduction processing system |
| CN105000778B (en) * | 2015-07-10 | 2017-05-31 | 江苏玖盛水处理科技有限公司 | A kind of mud decrement processing system |
| CN106890494A (en) * | 2017-03-24 | 2017-06-27 | 吴琏 | Benzalkonium chloride suction filtration purifying plant |
| CN107553772A (en) * | 2017-10-17 | 2018-01-09 | 苏州宏泉高压电容器有限公司 | A kind of uniform feeding formula color masterbatch drying machine |
| WO2019075831A1 (en) * | 2017-10-17 | 2019-04-25 | 苏州宏泉高压电容器有限公司 | Constant-speed feeding type color master batch drying machine |
| CN113324378A (en) * | 2021-03-26 | 2021-08-31 | 上海迪化科技股份有限公司 | Novel filtering, washing and drying integrated device and process |
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