CN103388956A - System capable of quickly drying substances - Google Patents
System capable of quickly drying substances Download PDFInfo
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- CN103388956A CN103388956A CN2012101446133A CN201210144613A CN103388956A CN 103388956 A CN103388956 A CN 103388956A CN 2012101446133 A CN2012101446133 A CN 2012101446133A CN 201210144613 A CN201210144613 A CN 201210144613A CN 103388956 A CN103388956 A CN 103388956A
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- drier
- pipe
- condenser
- carry out
- drying
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Abstract
The invention discloses a system capable of quickly drying substances. The system comprises a dryer, wherein a material feeding pipe, a material discharging pipe and a steam pipe are arranged on the dryer; and the dryer is connected with a condenser. The system is simple in structure and can quickly dry the substances in the dryer; moreover, the condenser is used for accelerating the cooling of the dried substances; and therefore, the cooling time in a natural state can be shortened, the waiting time is reduced, and the production efficiency is improved.
Description
Technical field
The present invention relates to a kind of system, especially relate to a kind of system that can carry out fast drying.
Background technology
Drying is general reference is removed moisture or other hygroscopic waters from wet stock various operations., as in daily life moist material being placed under sunlight and tanning by the sun to remove moisture, industrially with silica gel, lime, the concentrated sulfuric acid etc., remove moisture (seeing dehumidification) in air, industrial gasses or organic liquid.In Chemical Manufacture, drying is often referred to the wet solid material of the heating such as hot-air, flue gas and infrared ray, makes wherein contained moisture or solvent vaporize and remove, and is a kind of unit operations that belongs to the caloic transmittance process.Dry purpose is to make material be convenient to store, transport and use, or meets the further needs of processing.Such as grain, vegetables can store after drying for a long time; The synthetic resin drying is used for processing afterwards, can prevent from plastic products occurring bubble or moire; Paper is easy to use and storage after drying.Drying process is widely used in all departments such as chemical industry, food, light industry, weaving, coal, agriculture and forestry product processing and building materials.At a certain temperature, any moisture wet stock has certain vapour pressure, and during greater than the steam dividing potential drop in ambient gas, moisture will be vaporized when this vapour pressure.Vaporization institute calorific requirement, or from hot gas on every side, or by other thermals source, by radiation, heat conduction, provided.The vapour pressure of water-containing materials is relevant with moisture exists in material mode.The moisture that material is contained, be divided into unbound water and usually in conjunction with water.Unbound water is the moisture that is attached in the surface of solids and hole, and its vapour pressure is identical with pure water; Have active force certain physics or chemistry in conjunction with water and between solid, not only will overcome the active force between hydrone during vaporization, also need overcome the active force of combination between hydrone and solid, its vapour pressure is lower than pure water, and relevant with moisture.At a certain temperature, the moisture vapor of material is pressed the kilogram number of p with every kilogram of absolute dry material contained humidity of material water content x() between relation curve be called the equilibrium vapour pressure curve, generally by measuring.When wet stock contacted with synthermal air-flow, the water content of material and vapour pressure descended, and when system reached balance, the contained moisture vapor of material was pressed and equated with the steam dividing potential drop in gas, and corresponding material moisture is called equilibrium water conten.Equilibrium water conten depends on material properties, structure and the temperature and humidity of the gas of contact with it.In process of factory production, need to carry out drying to material and process.
Summary of the invention
The object of the invention is to overcome the shortcoming and defect of above-mentioned prior art, provide a kind of and can carry out fast dry system, this system architecture is simple, can carry out drying to the material in drier fast, utilize simultaneously condenser to accelerate the cooling of dry rear material, the cool time of shortening under nature, the stand-by period in the middle of reducing, enhance productivity.
Purpose of the present invention is achieved through the following technical solutions: a kind of system that can carry out fast drying, comprise drier, and be provided with feed pipe, discharge nozzle and steam pipe on described drier, described drier is connected with condenser.
Be provided with cooling water on described condenser and add pipe.
Described charging aperture is connected with conveyer, and conveyer is connected with wet feed and adds pipe.Needing dry wet feed to add pipe by wet feed adds in conveyer.
Described condenser is communicated with drier by condensing water conduit.
Be provided with coolant outlet on described drier.
In sum, the invention has the beneficial effects as follows: this system architecture is simple, can carry out drying to the material in drier fast, utilize simultaneously condenser to accelerate the cooling of dry rear material, the cool time of shortening under nature, the stand-by period in the middle of reducing, enhance productivity.
Description of drawings
Fig. 1 is structural representation of the present invention.
Mark and corresponding parts title in accompanying drawing: 1-steam pipe; 2-cooling water adds pipe; 3-condenser; 4-wet feed adds pipe; 5-conveyer; 6-condensing water conduit; 7--drier; 8-coolant outlet; 9-discharge nozzle; 10-dry product pipe.
The specific embodiment
Below in conjunction with embodiment and accompanying drawing, the present invention is described in further detail, but embodiments of the present invention are not limited only to this.
Embodiment:
As shown in Figure 1, a kind of system that can carry out fast drying, comprise drier 7, is provided with feed pipe, discharge nozzle 9 and steam pipe 1 on described drier 7, and described drier 7 is connected with condenser 3.To after adding materials in drier 7, steam pipe 1 passes into high-temperature steam in drier 7, material is carried out drying by feed pipe, after drying is completed by discharge nozzle 9 dischargings.
Be provided with cooling water on described condenser 3 and add pipe 2.Cooling water adds pipe 2 and is used for condenser 3 is added cooling water.
Described charging aperture is connected with conveyer 5, and conveyer 5 is connected with wet feed and adds pipe 4.Need dry wet feed to add pipe 4 by wet feed and add in conveyer 5, conveyer 5 is transported to wet feed in drier continuously, makes drier work have continuity, has reduced simultaneously the cost of artificial transportation, has reduced operating personnel's labour intensity.
Described condenser 3 is communicated with drier 7 by condensing water conduit 6.Condensing water conduit 6 passes into cooling water in drier 7, the material after cool drying.
Be provided with coolant outlet 8 on described drier 7.Coolant outlet 8 is used for discharging the moisture in drier 7, comprises the moisture of steam-condensation, the moisture in cooling procedure etc.
After the dried material of a part carries out condensation by condenser 3, discharge from dry product pipe 10, cooling by multiple spot, improve cooling effectiveness.
Take aforesaid way, just can realize preferably the present invention.
Claims (5)
1. one kind can be carried out dry system fast, comprises drier (7), is provided with feed pipe, discharge nozzle (9) and steam pipe (1) on described drier (7), and it is characterized in that: described drier (7) is connected with condenser (3).
2. a kind of system that can carry out fast drying according to claim 1, is characterized in that: be provided with cooling water on described condenser (3) and add pipe (2).
3. according to claim 2ly a kind ofly can carry out fast dry system, it is characterized in that: described charging aperture is connected with conveyer (5), and conveyer (5) is connected with wet feed and adds pipe (4).
4. according to claim 3ly a kind ofly can carry out fast dry system, it is characterized in that: described condenser (3) is communicated with drier (7) by condensing water conduit (6).
5. the described a kind of system that can carry out fast drying of any one according to claim 1 to 4, is characterized in that: be provided with coolant outlet (8) on described drier (7).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN2012101446133A CN103388956A (en) | 2012-05-11 | 2012-05-11 | System capable of quickly drying substances |
Applications Claiming Priority (1)
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CN2012101446133A CN103388956A (en) | 2012-05-11 | 2012-05-11 | System capable of quickly drying substances |
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CN2012101446133A Pending CN103388956A (en) | 2012-05-11 | 2012-05-11 | System capable of quickly drying substances |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105461583A (en) * | 2015-12-21 | 2016-04-06 | 常熟市柏伦精细化工有限公司 | Novel preparation and processing technology of naphthol AS-LC |
Citations (7)
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EP0485721A1 (en) * | 1990-11-13 | 1992-05-20 | Deutsche Babcock Anlagen Gmbh | Process and installation for partial drying of sewage sludge |
CN1834563A (en) * | 2006-04-22 | 2006-09-20 | 山东泰和东新股份有限公司 | Method of utilizing exhausted steam afterheat from plaster tablet drying machine |
CN101178282A (en) * | 2007-12-12 | 2008-05-14 | 北京林业大学 | Wood drying device |
CN101706196A (en) * | 2009-10-12 | 2010-05-12 | 郑州拉姆顿清洁能源工程技术有限公司 | Oxygen-free drying and upgrading system of lignite and lignite drying process |
CN101726170A (en) * | 2008-10-31 | 2010-06-09 | 沈开宇 | Straight heat pipe bundle type dryer |
CN101776372A (en) * | 2010-01-28 | 2010-07-14 | 常州市星干干燥设备有限公司 | Nitrogen closed cycle drying and solvent recovery system |
CN202582041U (en) * | 2012-05-11 | 2012-12-05 | 四川汇利实业有限公司 | System capable of drying quickly |
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2012
- 2012-05-11 CN CN2012101446133A patent/CN103388956A/en active Pending
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0485721A1 (en) * | 1990-11-13 | 1992-05-20 | Deutsche Babcock Anlagen Gmbh | Process and installation for partial drying of sewage sludge |
CN1834563A (en) * | 2006-04-22 | 2006-09-20 | 山东泰和东新股份有限公司 | Method of utilizing exhausted steam afterheat from plaster tablet drying machine |
CN101178282A (en) * | 2007-12-12 | 2008-05-14 | 北京林业大学 | Wood drying device |
CN101726170A (en) * | 2008-10-31 | 2010-06-09 | 沈开宇 | Straight heat pipe bundle type dryer |
CN101706196A (en) * | 2009-10-12 | 2010-05-12 | 郑州拉姆顿清洁能源工程技术有限公司 | Oxygen-free drying and upgrading system of lignite and lignite drying process |
CN101776372A (en) * | 2010-01-28 | 2010-07-14 | 常州市星干干燥设备有限公司 | Nitrogen closed cycle drying and solvent recovery system |
CN202582041U (en) * | 2012-05-11 | 2012-12-05 | 四川汇利实业有限公司 | System capable of drying quickly |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105461583A (en) * | 2015-12-21 | 2016-04-06 | 常熟市柏伦精细化工有限公司 | Novel preparation and processing technology of naphthol AS-LC |
CN105461583B (en) * | 2015-12-21 | 2017-09-05 | 常熟市柏伦精细化工有限公司 | The preparation of new azoic coupling component AS LC a kind of and processing technology |
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Application publication date: 20131113 |