CN105928332A - Chrysanthemum central heating negative-pressure drying killout system - Google Patents
Chrysanthemum central heating negative-pressure drying killout system Download PDFInfo
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- CN105928332A CN105928332A CN201610290222.0A CN201610290222A CN105928332A CN 105928332 A CN105928332 A CN 105928332A CN 201610290222 A CN201610290222 A CN 201610290222A CN 105928332 A CN105928332 A CN 105928332A
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- hothouse
- cell body
- flos chrysanthemi
- dried
- pipe
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B9/00—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards
- F26B9/06—Machines or apparatus for drying solid materials or objects at rest or with only local agitation; Domestic airing cupboards in stationary drums or chambers
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- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23F—COFFEE; TEA; THEIR SUBSTITUTES; MANUFACTURE, PREPARATION, OR INFUSION THEREOF
- A23F3/00—Tea; Tea substitutes; Preparations thereof
- A23F3/34—Tea substitutes, e.g. matè; Extracts or infusions thereof
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B23/00—Heating arrangements
- F26B23/10—Heating arrangements using tubes or passages containing heated fluids, e.g. acting as radiative elements; Closed-loop systems
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/06—Chambers, containers, or receptacles
- F26B25/063—Movable containers or receptacles, e.g. carts, trolleys, pallet-boxes
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B25/00—Details of general application not covered by group F26B21/00 or F26B23/00
- F26B25/06—Chambers, containers, or receptacles
- F26B25/14—Chambers, containers, receptacles of simple construction
- F26B25/18—Chambers, containers, receptacles of simple construction mainly open, e.g. dish, tray, pan, rack
- F26B25/185—Spacers; Elements for supporting the goods to be dried, i.e. positioned in-between the goods to build a ventilated stack
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F26—DRYING
- F26B—DRYING SOLID MATERIALS OR OBJECTS BY REMOVING LIQUID THEREFROM
- F26B2200/00—Drying processes and machines for solid materials characterised by the specific requirements of the drying good
- F26B2200/20—Teas, i.e. drying, conditioning, withering of tea leaves
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Chemical & Material Sciences (AREA)
- Food Science & Technology (AREA)
- Polymers & Plastics (AREA)
- Combustion & Propulsion (AREA)
- Sustainable Development (AREA)
- Drying Of Solid Materials (AREA)
Abstract
The invention provides a chrysanthemum central heating negative-pressure drying killout system. The system comprises a drying chamber; snake-shaped heating pipes are respectively arranged at the bottom and on side walls of two sides of the drying chamber, and are heat steam pipes; multiple drying brackets are arranged in the drying chamber side by side; steam pipes are led out from the drying chambers; and exhaust fans and condensation devices are arranged on the steam pipes. The system solves the problems of lower energy utilization rate, waste of a lot of energy, lower drying efficiency, long time and reduction of the utilization value and efficiency of chrysanthemums due to loss of part beneficial components of the chrysanthemums along with high-temperature steam in a traditional chrysanthemum drying method. The system belongs to the field of chrysanthemum processing.
Description
Technical field
The present invention relates to a kind of Flos Chrysanthemi and be dried the system of completing, belong to Flos Chrysanthemi manufacture field.
Background technology
Flos Chrysanthemi is Compositae herbaceos perennial, generally completes with it, dried head inflorescence people's medicine.Fresh chrysanthemum water content is higher, wherein petal sections moisture content less, organizes tenderer, is easily dried, and fresh idea partially aqueous amount is especially big, and up to more than 80%, and tissue is relatively old, is difficult to dehydration, that is Flos Chrysanthemi fresh idea is the medical material that a kind of tissue is the most uneven.Dry Flos Chrysanthemi is mostly used for brewed for drinking, has that taste giving off a strong fragrance is sweet, goes greasy to help digestion, the function of refreshment benefit god.Therefore, require the highest for the color of Flos Chrysanthemi, perfume (or spice), shape, taste, it is desirable to complete dried primary colors, original flavor, former state, and this just requires ripening post-drying.Complete on a large scale at present, be dried typically to use and drying frame is put into drying chamber to carrying out green removal on chrysanthemum, drying, but existing complete, to dry heat supply method energy utilization rate the highest, waste substantial amounts of heat energy, and it is relatively low with drying efficiency to complete, time is long, simultaneously as the part beneficiating ingredient in Flos Chrysanthemi runs off with high-temperature steam when completing, dry, for promoting utilization ratio and the value of Flos Chrysanthemi, the applicant devises a kind of Flos Chrysanthemi central heating negative-pressure type and is dried the system of completing.
Summary of the invention
It is an object of the invention to: provide a kind of Flos Chrysanthemi central heating negative-pressure type to be dried the system of completing, relatively low to solve existing Getrocknete Chrysanthemen drying method energy utilization rate, cause the waste of mass energy, and drying efficiency is relatively low, time is long, meanwhile, the part beneficiating ingredient of Flos Chrysanthemi runs off along with high-temperature steam, reduces the value of Flos Chrysanthemi and the problem of efficiency.
For solving the problems referred to above, intend using such a Flos Chrysanthemi central heating negative-pressure type to be dried the system of completing, including hothouse, it is provided with snakelike heat supply pipeline at the bottom of hothouse and the side wall of both sides, snakelike heat supply pipeline is vapours pipeline, it is provided with multiple drying bracket being arranged side by side in hothouse, hothouse leads to jet chimney, jet chimney is provided with air exhauster and condensing unit.
For ensureing Steam Recovery and condensation effect, described jet chimney is drawn by the upper end of hothouse, the downstream part of condensing unit is additionally provided with condensed water separation apparatus, is provided with air exhauster between condensing unit and hothouse and between condensing unit and condensed water separation apparatus；
For promoting heat utilization rate, the snakelike heat supply pipeline arranged at the side wall of described hothouse both sides may be contained within the lower portion of side wall；
Preferably, the front of hothouse is provided with split door body structure, the bottom of hothouse is provided with guide rail, guide rail is led to the outside of hothouse by door body structure via front in hothouse, drying bracket is slideably positioned on guide rail, the snakelike heat supply pipeline of the bottom of described hothouse is arranged at the underface of drying bracket, promotes heat utilization rate, it is simple to the transfer of Flos Chrysanthemi and being dried；
For promoting the utilization rate of hothouse, middle part in described hothouse is additionally provided with the divider wall paralleled with its both sides side wall, the both sides of divider wall are respectively arranged with two groups of guide rails, often group guide rail is made up of two guide rails being parallel to each other, and is often provided with snakelike heat supply pipeline between two guide rails being parallel to each other in group guide rail；
Preferably, also include steam heating house steward and return duct, described hothouse has multiple, in each hothouse, snakelike heat supply pipeline between snakelike heat supply pipeline and two groups of guide rails at both walls is communicated on steam heating house steward by drawing in hothouse and collect respectively to a house steward, upstream end on steam heating house steward is provided with check valve, the backflow end of described snakelike heat supply pipeline is communicated to return duct, and described snakelike heat supply pipeline and house steward are provided with control valve respectively；
For realizing Automated condtrol and the regulation of temperature, also including control unit, be provided with temperature sensor in hothouse, described control valve is electromagnetic valve, and air exhauster, control valve are all connected with control unit with temperature sensor；
Preferably, drying bracket includes rack body, multiple tray supporter it is provided with on rack body, horizontally disposed on tray supporter have removable netted pallet, netted pallet spaced set the most successively, the bottom of rack body is provided with roller, enables vapours to be passed by air vent, it is greatly improved the uniformity that Flos Chrysanthemi is dried, promotes drying effect and quality；
Preferably, described condensing unit includes cooling cylinder, cooling cylinder is enclosed construction, the bottom of cooling cylinder is provided with outlet pipe, the condensing tube being obliquely installed it is provided with in cooling cylinder, the two ends of condensing tube are each passed through the opposite sides of cooling cylinder, and the two ends of condensing tube are provided with connection end, be positioned at condensing tube in cooling cylinder is provided above condensed water shower nozzle, condensed water shower nozzle is connected with one end of condensate pipe, the other end of condensate pipe connects condensed water water supply installation, and condensate pipe is provided with control valve；
Further preferably, described condensed water shower nozzle is a sparge pipe transversely arranged, the lower end of sparge pipe is distributed along its length and is provided with hole for water spraying, condensed water shower nozzle is arranged along the length direction of condensing tube, the bottom of cooling cylinder is the ramp structure contrary with the incline direction of condensing tube, outlet pipe is arranged at the bottom of the inclined slope of cooling cylinder bottom, also include storage tank, the water side of outlet pipe extends in storage tank, the downside of storage tank leads to return duct, the other end of return duct is communicated to condensed water water supply installation, and return duct is provided with reflux pump.
nullPreferably，Described condensed water separation apparatus is oil water separator，Including cell body，Cell body is enclosed construction，The upper end of cell body is provided with and the feed tube of cell body intracavity inter-connection，The lower end of cell body sidewall leads to the communicating pipe arranged upward，Communicating pipe is that transparent material is made or has transparent liquid level observing structure on communicating pipe，The conduit of horizontally set it is additionally provided with in cell body，One end of conduit is closed，The other end connects with the lower end of communicating pipe，And the upside of conduit offers through hole，The lower end of cell body leads to drain pipe and oil exit pipe，It is provided with control valve on drain pipe and oil exit pipe，Dielectric interlayer it is provided with in cell body，The pipeline extended outside cell body is led at dielectric interlayer，The inside of cell body is vertically provided with the interlayer inwall of tubular，The two ends up and down of interlayer inwall are all connected with the inner wall sealing of cell body，The dielectric interlayer separated mutually with interlayer inner wall chamber it is between interlayer inwall and the sidewall of cell body，When needing the temperature of liquid in regulating tank body，Filled media in dielectric interlayer，And controlled to realize the temperature of oil solution in cell body by the temperature adjusting medium；
Also include the path of saltouing extending in cell body, the inner side of interlayer inwall is vertically additionally provided with the inwall of saltouing of tubular, saltouing, the upper end of upper end and cell body of inwall is fixing to be connected, saltout path of saltouing described in being between inwall and interlayer inwall, saltout at the cell body corresponding to path upper end is can the end cap of saltouing of opening type, saltout, between the lower end of inwall and the bottom land of cell body, there is gap, the lower end of path of i.e. saltouing is connected with the medial compartment of inwall of saltouing, when oil solution excessively muddiness is difficult to layering, by saltouing, path adds salt in solution, promote water and oil layering, the side-walls of cell body is additionally provided with observation form, the liquid level of liquid in observing cell body, delamination and turbidity.
The mixing liquid obtained after condensation enters oil water separator, liquid in communicating pipe is entered by the through hole then passed through on the upside of conduit, the liquid entered in ensureing communicating pipe is substantially water, there may be minimal amount of oil, thus by the communicating pipe observation water yield within cell body, it is easy to the accurate control to oil-water separation so that the Flos Chrysanthemi beneficiating ingredient carried in produced steam is fully reclaimed.
The present invention is compared with prior art, major advantage is that this Getrocknete Chrysanthemen drying system utilizes steam-coil road to be dried Flos Chrysanthemi in hothouse, heat utilization rate is high, drying efficiency is high, it is capable of the rapid draing of Flos Chrysanthemi, simultaneously, the high-temperature steam indoor by air exhauster and jet chimney suction dried recycling after Flos Chrysanthemi is condensed with the beneficiating ingredient that steam volatilize, improve the utilization ratio of Flos Chrysanthemi, avoid the waste of beneficiating ingredient, and in making hothouse during draws vapor, form negative pressure, make the moisture in Flos Chrysanthemi the most volatilizable, reduce the drying temperature of drying chamber, thus avoid Flos Chrysanthemi to be scorched when drying, improve the dries quantity of Flos Chrysanthemi, the beneficiating ingredient making Flos Chrysanthemi preserves the most complete, optimize Flos Chrysanthemi stoving process, there is great economic benefit.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention；
Fig. 2 is the structural representation of drying support；
Fig. 3 is the structural representation (cooling cylinder part is sectional view) of condensing unit；
Fig. 4 is steam heating house steward and the structural representation of corresponding drying chamber；
Fig. 5 is heat supply control principle drawing；
Fig. 6 is the main TV structure schematic diagram of condensed water separation apparatus；
Fig. 7 is the sectional view of Fig. 6；
Fig. 8 is the top view of Fig. 6.
Detailed description of the invention
For making the object, technical solutions and advantages of the present invention clearer, the present invention is described in further detail below with reference to accompanying drawings,
Embodiment:
Referring to figs. 1 through Fig. 8, the present embodiment provides a kind of Flos Chrysanthemi central heating negative-pressure type to be dried the system of completing, including hothouse 1, snakelike heat supply pipeline 2 it is provided with at the bottom of hothouse 1 and the side wall of both sides, snakelike heat supply pipeline 2 is vapours pipeline, multiple drying bracket 3 being arranged side by side it is provided with in hothouse 1, jet chimney 4 is led on hothouse 1, air exhauster 5 and condensing unit 6 it is provided with on jet chimney 4, jet chimney 4 is drawn by the upper end of hothouse 1, the downstream part of condensing unit 6 is additionally provided with condensed water separation apparatus 7, air exhauster 5 it is provided with between condensing unit 6 and hothouse 1 and between condensing unit 6 and condensed water separation apparatus 7, the snakelike heat supply pipeline 2 arranged at the side wall of described hothouse 1 both sides may be contained within the lower portion of side wall；
The front of hothouse 1 is provided with split door body structure 11, the bottom of hothouse 1 is provided with guide rail 8, guide rail 8 is by the outside leading to hothouse 1 in hothouse 1 via the door body structure 11 in front, drying bracket 3 is slideably positioned on guide rail 8, the snakelike heat supply pipeline 2 of the bottom of described hothouse 1 is arranged at the underface of drying bracket 3, middle part in hothouse 1 is additionally provided with the divider wall 12 paralleled with its both sides side wall, the both sides of divider wall 12 are respectively arranged with two groups of guide rails 8, often group guide rail 8 is made up of two guide rails being parallel to each other 8, often group guide rail 8 is provided with snakelike heat supply pipeline 2 between two guide rails 8 being parallel to each other；
Also include steam heating house steward 9, return duct 16 and control unit 14, described hothouse 1 has multiple, in each hothouse 1, snakelike heat supply pipeline 2 between snakelike heat supply pipeline 2 and two groups of guide rails 3 at both walls is communicated on steam heating house steward 9 by drawing and collect in hothouse 1 respectively to a house steward 10, upstream end on steam heating house steward 9 is provided with check valve 91, the backflow end of described snakelike heat supply pipeline 2 is communicated to return duct 16, control valve 13 it is provided with respectively on described snakelike heat supply pipeline 2 and house steward 10, temperature sensor 15 it is provided with in hothouse 1, described control valve 13 is electromagnetic valve, air exhauster 5, control valve 13 is all connected with control unit 14 with temperature sensor 15；
Drying bracket 3 includes rack body 31, multiple tray supporter 311 it is provided with on rack body 31, horizontally disposed on tray supporter 311 have removable netted pallet 32, and netted pallet 32 spaced set the most successively, the bottom of rack body 31 is provided with roller 33；
nullCondensing unit 6 includes cooling cylinder 61，Cooling cylinder 61 is enclosed construction，The bottom of cooling cylinder 61 is provided with outlet pipe 610，The condensing tube 62 being obliquely installed it is provided with in cooling cylinder 61，The two ends of condensing tube 62 are each passed through the opposite sides of cooling cylinder 61，And the two ends of condensing tube 62 are provided with connection end 621，Be positioned at condensing tube 62 in cooling cylinder 61 is provided above condensed water shower nozzle 63，Condensed water shower nozzle 63 is connected with one end of condensate pipe 64，The other end of condensate pipe 64 connects condensed water water supply installation 65，Control valve 66 it is provided with on condensate pipe 64，Condensed water shower nozzle 63 is a sparge pipe transversely arranged，The lower end of sparge pipe is distributed along its length and is provided with hole for water spraying 631，Condensed water shower nozzle 63 is arranged along the length direction of condensing tube 62，The bottom of cooling cylinder 61 is the ramp structure contrary with the incline direction of condensing tube 2，Outlet pipe 610 is arranged at the bottom of the inclined slope of cooling cylinder 61 bottom，Also include storage tank 67，The water side of outlet pipe 610 extends in storage tank 67，The downside of storage tank 67 leads to return duct 68，The other end of return duct 68 is communicated to condensed water water supply installation 65，Reflux pump 69 it is provided with on return duct 68.
nullCondensed water separation apparatus 7 is oil water separator，Including cell body 71，Cell body 71 is enclosed construction，The upper end of cell body 71 is provided with and the feed tube 77 of cell body 71 intracavity inter-connection，The lower end of cell body 71 sidewall leads to the communicating pipe 72 arranged upward，Make for transparent material communicating pipe 72 or there is on communicating pipe 72 transparent liquid level observing structure，The conduit 73 of horizontally set it is additionally provided with in cell body 71，One end of conduit 73 is closed，The other end connects with the lower end of communicating pipe 72，And the upside of conduit 73 offers through hole 731，The lower end of cell body 71 leads to drain pipe 74 and oil exit pipe 75，It is provided with control valve 76 on drain pipe 74 and oil exit pipe 75，Dielectric interlayer 78 it is provided with in cell body 71，The pipeline 781 extended outside cell body 71 is led at dielectric interlayer 78，The inside of cell body 71 is vertically provided with the interlayer inwall 79 of tubular，The two ends up and down of interlayer inwall 79 all inner wall sealings with cell body 71 are connected，The dielectric interlayer 78 separated mutually with interlayer inwall 79 medial compartment it is between interlayer inwall 79 and the sidewall of cell body 71；Also include the path 710 of saltouing extending in cell body 71, the inner side of interlayer inwall 79 is vertically additionally provided with the inwall 711 of saltouing of tubular, saltouing, the upper end of upper end and cell body 71 of inwall 711 is fixing to be connected, saltout path 710 of saltouing described in being between inwall 711 and interlayer inwall 79, saltout at the cell body 71 corresponding to path 710 upper end is can the end cap 713 of saltouing of opening type, saltout, between the lower end of inwall 711 and the bottom land of cell body 71, there is gap, the lower end of path 710 of i.e. saltouing is connected with the medial compartment of inwall 711 of saltouing, the side-walls of cell body 71 is additionally provided with observation form 712, the liquid level of liquid in observing cell body 71, delamination and turbidity.
Claims (10)
1. a Flos Chrysanthemi central heating negative-pressure type is dried the system of completing, it is characterized in that: include hothouse (1), it is provided with snakelike heat supply pipeline (2) at the bottom of hothouse (1) and the side wall of both sides, snakelike heat supply pipeline (2) is vapours pipeline, the drying bracket (3) for putting Flos Chrysanthemi it is provided with in hothouse (1), jet chimney (4) is led on hothouse (1), air exhauster (5) and condensing unit (6) it is provided with on jet chimney (4), the snakelike heat supply pipeline (2) arranged at the side wall of described hothouse (1) both sides may be contained within the lower portion of side wall.
The most according to claim 1, a kind of Flos Chrysanthemi central heating negative-pressure type is dried the system of completing, it is characterized in that: described jet chimney (4) is drawn by the upper end of hothouse (1), the downstream part of condensing unit (6) is additionally provided with condensed water separation apparatus (7), is provided with air exhauster (5) between condensing unit (6) and hothouse (1) and between condensing unit (6) and condensed water separation apparatus (7).
The most according to claim 1, a kind of Flos Chrysanthemi central heating negative-pressure type is dried the system of completing, it is characterized in that: the front of hothouse (1) is provided with split door body structure (11), the bottom of hothouse (1) is provided with guide rail (8), guide rail (8) is by the outside leading to hothouse (1) in hothouse (1) via the door body structure (11) in front, drying bracket (3) is slideably positioned on guide rail (8), and the snakelike heat supply pipeline (2) of described hothouse (1) bottom is arranged at the underface of drying bracket (3).
The most according to claim 1, a kind of Flos Chrysanthemi central heating negative-pressure type is dried the system of completing, it is characterized in that: the middle part in described hothouse (1) is additionally provided with the divider wall (12) paralleled with its both sides side wall, the both sides of divider wall (12) are respectively arranged with two groups of guide rails (8), often organize guide rail (8) to be made up of two guide rails being parallel to each other (8), often organize in guide rail (8) and be provided with snakelike heat supply pipeline (2) between two guide rails being parallel to each other (8).
The most according to claim 4, a kind of Flos Chrysanthemi central heating negative-pressure type is dried the system of completing, it is characterized in that: also include steam heating house steward (9) and return duct (16), described hothouse (1) is total multiple, the snakelike heat supply pipeline (2) between snakelike heat supply pipeline (2) and two groups of guide rails (3) at each hothouse (1) interior both walls is communicated on steam heating house steward (9) by drawing and collect in hothouse (1) respectively to a house steward (10), upstream end on steam heating house steward (9) is provided with check valve (91), the backflow end of described snakelike heat supply pipeline (2) is communicated to return duct (16), control valve (13) it is provided with respectively on described snakelike heat supply pipeline (2) and house steward (10).
The most according to claim 5, a kind of Flos Chrysanthemi central heating negative-pressure type is dried the system of completing, it is characterized in that: also include control unit (14), temperature sensor (15) it is provided with in hothouse (1), described control valve (13) is electromagnetic valve, and air exhauster (5), control valve (13) are all connected with control unit (14) with temperature sensor (15).
The most according to claim 1, a kind of Flos Chrysanthemi central heating negative-pressure type is dried the system of completing, it is characterized in that: drying bracket (3) includes rack body (31), multiple tray supporter (311) it is provided with on rack body (31), tray supporter (311) is the most horizontally disposed removable netted pallet (32), netted pallet (32) spaced set the most successively, the bottom of rack body (31) is provided with roller (33).
nullThe most according to claim 1, a kind of Flos Chrysanthemi central heating negative-pressure type is dried the system of completing，It is characterized in that: described condensing unit (6) includes cooling cylinder (61)，Cooling cylinder (61) is enclosed construction，The bottom of cooling cylinder (61) is provided with outlet pipe (610)，The condensing tube (62) being obliquely installed it is provided with in cooling cylinder (61)，The two ends of condensing tube (62) are each passed through the opposite sides of cooling cylinder (61)，And the two ends of condensing tube (62) are provided with connection end (621)，Be positioned at condensing tube (62) in cooling cylinder (61) is provided above condensed water shower nozzle (63)，Condensed water shower nozzle (63) is connected with one end of condensate pipe (64)，The other end of condensate pipe (64) connects condensed water water supply installation (65)，Control valve (66) it is provided with on condensate pipe (64).
nullThe most according to claim 8, a kind of Flos Chrysanthemi central heating negative-pressure type is dried the system of completing，It is characterized in that: described condensed water shower nozzle (63) is a sparge pipe transversely arranged，The lower end of sparge pipe is distributed along its length and is provided with hole for water spraying (631)，Condensed water shower nozzle (63) is arranged along the length direction of condensing tube (62)，The bottom of cooling cylinder (61) is the ramp structure contrary with the incline direction of condensing tube (2)，Outlet pipe (610) is arranged at the bottom of the inclined slope of cooling cylinder (61) bottom，Also include storage tank (67)，The water side of outlet pipe (610) extends in storage tank (67)，The downside of storage tank (67) leads to return duct (68)，The other end of return duct (68) is communicated to condensed water water supply installation (65)，Reflux pump (69) it is provided with on return duct (68).
nullThe most according to claim 2, a kind of Flos Chrysanthemi central heating negative-pressure type is dried the system of completing，It is characterized in that: described condensed water separation apparatus (7) is oil water separator，Including cell body (71)，Cell body (71) is enclosed construction，The upper end of cell body (71) is provided with the feed tube (77) with cell body (71) intracavity inter-connection，The lower end of cell body (71) sidewall leads to the communicating pipe (72) arranged upward，Communicating pipe (72) is that transparent material is made or has transparent liquid level observing structure on communicating pipe (72)，The conduit (73) of horizontally set it is additionally provided with in cell body (71)，One end of conduit (73) is closed，The other end connects with the lower end of communicating pipe (72)，And the upside of conduit (73) offers through hole (731)，The lower end of cell body (71) leads to drain pipe (74) and oil exit pipe (75)，It is provided with control valve (76) on drain pipe (74) and oil exit pipe (75)，Dielectric interlayer (78) it is provided with in cell body (71)，Dielectric interlayer (78) place leads to extend the pipeline (781) that cell body (71) is outside，The inside of cell body (71) is vertically provided with the interlayer inwall (79) of tubular，The two ends up and down of interlayer inwall (79) all inner wall sealings with cell body (71) are connected，The dielectric interlayer (78) separated mutually with interlayer inwall (79) medial compartment it is between interlayer inwall (79) and the sidewall of cell body (71).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610290222.0A CN105928332B (en) | 2016-05-05 | 2016-05-05 | A kind of chrysanthemum central heating suction type dries water-removing system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610290222.0A CN105928332B (en) | 2016-05-05 | 2016-05-05 | A kind of chrysanthemum central heating suction type dries water-removing system |
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| CN105928332A true CN105928332A (en) | 2016-09-07 |
| CN105928332B CN105928332B (en) | 2018-06-29 |
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| CN107477999A (en) * | 2017-08-17 | 2017-12-15 | 金寨县秉诚农业科技有限公司 | A kind of chrysanthemum drying box of carrying vapour condensing unit |
| CN108800781A (en) * | 2018-06-07 | 2018-11-13 | 长沙跃奇节能电气设备有限公司 | A kind of drying system of dust-like pyrotechnic composition |
| CN108800782A (en) * | 2018-06-07 | 2018-11-13 | 长沙跃奇节能电气设备有限公司 | A kind of cooling system of ground heating type drying system |
| CN112611184A (en) * | 2020-12-21 | 2021-04-06 | 崔欣 | Drying device for food processing |
| CN114001537A (en) * | 2021-11-30 | 2022-02-01 | 广东碧朗节能设备有限公司 | Agricultural product dryer with air energy heat pump |
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| JPH10137505A (en) * | 1996-11-07 | 1998-05-26 | Kiichi Watanabe | Oil purifying device for air compressor system |
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