CN104621689A - Energy-saving and efficient drying and evaporating equipment - Google Patents
Energy-saving and efficient drying and evaporating equipment Download PDFInfo
- Publication number
- CN104621689A CN104621689A CN201310472743.4A CN201310472743A CN104621689A CN 104621689 A CN104621689 A CN 104621689A CN 201310472743 A CN201310472743 A CN 201310472743A CN 104621689 A CN104621689 A CN 104621689A
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- steam
- auger
- energy
- saving
- evaporation equipment
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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
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
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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
- Y02P60/00—Technologies relating to agriculture, livestock or agroalimentary industries
- Y02P60/80—Food processing, e.g. use of renewable energies or variable speed drives in handling, conveying or stacking
- Y02P60/85—Food storage or conservation, e.g. cooling or drying
Abstract
The present invention discloses energy-saving and efficient drying and evaporating equipment, and relates to the field of food machinery. According to the energy-saving and efficient drying and evaporating equipment, one end of a rotary drum dryer (9) is connected with a steam outlet box (6) while the other end of the rotary drum dryer (6) is connected with a work steam inlet box (11); the steam outlet box (6) is connected to a steam injection pump (8); one end of the steam injection pump (8) is provided with a high-energy steam inlet port(7), and the other end of the steam injection pump (8) is connected to the work steam inlet box (11); the steam outlet box (6) is also connected to a feeder (3); the feeder (3) is provided with a material returning inlet port(2) and a fruit residue addition port (4); the material returning inlet port (2) is provided with a material returning packing auger (1); one side of the material returning packing auger (1) is provided with a material lifter (15); one side on the bottom of the material lifter (15) is provided with an underground packing auger (14); and a distribution packing auger(13) is disposed above one end of the underground packing auger (14). The energy-saving and efficient drying and evaporating equipment has characteristics that the structure is simple; the heat energy utilization rate is high; the fruit residue is not prone to stick to the inner wall of the equipment; and the utilization rate of the fruit residue can be improved.
Description
Technical field
What the present invention relates to is food machinery field, is specifically related to a kind of dry evaporation equipment of efficient energy-saving.
Background technology
Dry technology and equipment very extensive in sector applications such as chemical industry, petrochemical industry, medicine, bioengineering, light industry, food, and the dry evaporation equipment being applied to the efficient energy-saving of field of food mainly contains, and these are several: vacuum freeze drying, rotary drying, belt drying, spraying dry etc., it is low that these existing pomace drying equipments also exist heat utilization rate, dregs easily stick on equipment inner wall, flue gas directly and the pollution that causes pomace product to be subject to a certain extent of pomace contact drying, product quality is not high, and drying efficiency is low.
Summary of the invention
For the deficiency that prior art exists, the present invention seeks to the dry evaporation equipment being to provide a kind of efficient energy-saving, structure is simple, and heat utilization rate is high, and pomace not easily sticks on equipment inner wall, can improve the utilization rate of pomace.
To achieve these goals, the present invention realizes by the following technical solutions: the dry evaporation equipment of efficient energy-saving, comprise returning charge auger, returning charge entrance, feeder, pomace charge door, steam goes out vapour case, high energy steam entrance, steam jet pump, rotary drier, working steam admission case, distribute auger, underground auger and rise glassware, rotary drier two ends go out vapour case respectively and are connected with working steam admission case with steam, steam goes out vapour case and is connected with steam jet pump, one end of steam jet pump is provided with high energy steam entrance, the other end of steam jet pump is connected with working steam admission case, steam goes out vapour case and is also connected with feeder, feeder is provided with returning charge entrance and pomace charge door, returning charge entrance is provided with returning charge auger, returning charge auger side is provided with and rises glassware, bottom rising glassware, side is provided with underground auger, underground is provided with distribution auger above auger one end.
According to the dry evaporation equipment of above-mentioned efficient energy-saving, wherein, described distribution auger, underground auger are all arranged on below rotary drier.
According to the dry evaporation equipment of above-mentioned efficient energy-saving, wherein, the described upper and lower two ends of working steam admission case are respectively arranged with working steam entrance and condensation-water drain.
According to the dry evaporation equipment of above-mentioned efficient energy-saving, wherein, described feeder is also connected with vavuum pump.
According to the dry evaporation equipment of above-mentioned efficient energy-saving, wherein, described rotary drier inwall scribbles high radiant energy dope layer.
According to the dry evaporation equipment of above-mentioned efficient energy-saving, wherein, described steam jet pump is provided with disperser.
According to the dry evaporation equipment of above-mentioned efficient energy-saving, wherein, described distribution auger and underground auger all scribble wear-resistant coating.
According to the dry evaporation equipment of above-mentioned efficient energy-saving, wherein, described feeder is provided with weighing device.
The present invention is mainly through steam pipe indirect and form the rotary drier of certain gradient and returning charge with horizontal plane, the recycle device three parts of feed arrangement and indirect steam form, structure is simple, heat utilization rate is high, pomace not easily sticks on equipment inner wall, can improve the utilization rate of pomace.
Accompanying drawing explanation
The present invention is described in detail below in conjunction with the drawings and specific embodiments;
Fig. 1 is structural representation of the present invention;
Fig. 2 is the schematic diagram of steam jet pump in the present invention.
Detailed description of the invention
The technological means realized for making the present invention, creation characteristic, reaching object and effect is easy to understand, below in conjunction with detailed description of the invention, setting forth the present invention further.
With reference to Fig. 1-2, this detailed description of the invention is by the following technical solutions: the dry evaporation equipment of efficient energy-saving, it comprises returning charge auger 1, returning charge entrance 2, feeder 3, pomace charge door 4, steam goes out vapour case 6, high energy steam entrance 7, steam jet pump 8, rotary drier 9, working steam admission case 11, distribute auger 13, underground auger 14 and rise glassware 15, rotary drier 9 two ends go out vapour case 6 respectively and are connected with working steam admission case 11 with steam, steam goes out vapour case 6 and is connected with steam jet pump 8, one end of steam jet pump 8 is provided with high energy steam entrance 7, the other end of steam jet pump 8 is connected with working steam admission case 11, steam goes out vapour case 6 and is also connected with feeder 3, feeder 3 is provided with returning charge entrance 2 and pomace charge door 4, returning charge entrance 2 is provided with returning charge auger 1, returning charge auger 1 side is provided with and rises glassware 15, bottom rising glassware 15, side is provided with underground auger 14, be provided with above underground auger 14 one end and distribute auger 13.
It should be noted that described distribution auger 13, underground auger 14 is all arranged on below rotary drier 9.Described working steam admission case about 11 two ends are respectively arranged with working steam entrance 10 and condensation-water drain 12.Described feeder 3 is also connected with vavuum pump 5.
It should be noted that described rotary drier 9 inwall scribbles high radiant energy dope layer.
It should be noted that described steam jet pump 8 is provided with disperser.
It should be noted that described distribution auger 13 and underground auger 14 all scribble wear-resistant coating.
It should be noted that described feeder 3 is provided with weighing device.
The Laval nozzle A of the steam jet pump 8 that the high steam in this detailed description of the invention passes through produces the vapor stream of high velocity, low pressure, the inferior indirect steam that pomace drying produces is sucked the mixing chamber B of jet pump, mix with indirect steam at mixing chamber inner high voltage steam, then enter diffuser C and to boost the working steam that reduction of speed obtains needed for dry pomace.
The operation principle of this detailed description of the invention: fresh fruit slag enters feeder 3 and mixes with the dry pomace of returning charge, the pomace material mixed enters rotating cylinder drier 9 and is heated by steam pipe elevate a turnable ladder, stirring, heating and drying, and along with the rotation of rotating cylinder is moved to one end that drier is lower, complete the overall process of dry materials, a dried pomace part is separated with the form of product by distributing auger 13 at discharger place, another part is successively by underground auger 14, rise glassware 15, returning charge auger 1 enters returning charge entrance 2, the high energy steam of supplementing enters steam jet pump 8 and mixes with by the indirect steam of injection, form the working steam needed for drying, working steam enters working steam case by steam inlet pipe successively, enter the sleeve pipe in admission axle again, enter annular steam room, finally enter the dry pomace of steam-heating pipe condensation heat transfer, then lean on the inclination of revolving drum itself from efferent tract collect cavity in heating tube through the condensed condensed water of heat exchange, retell an outer breeches pipe and enter water chamber, discharge from condensation-water drain.
This detailed description of the invention structure is simple, and heat utilization rate is high, and pomace not easily sticks on equipment inner wall, can improve the utilization rate of pomace.
More than show and describe general principle of the present invention and principal character and advantage of the present invention.The technical staff of the industry should understand; the present invention is not restricted to the described embodiments; what describe in above-described embodiment and description just illustrates principle of the present invention; without departing from the spirit and scope of the present invention; the present invention also has various changes and modifications, and these changes and improvements all fall in the claimed scope of the invention.Application claims protection domain is defined by appending claims and equivalent thereof.
Claims (8)
1. the dry evaporation equipment of an efficient energy-saving, it is characterized in that, comprise returning charge auger (1), returning charge entrance (2), feeder (3), pomace charge door (4), steam goes out vapour case (6), high energy steam entrance (7), steam jet pump (8), rotary drier (9), working steam admission case (11), distribute auger (13), underground auger (14) and rise glassware (15), rotary drier (9) two ends go out vapour case (6) respectively and are connected with working steam admission case (11) with steam, steam goes out vapour case (6) and is connected with steam jet pump (8), one end of steam jet pump (8) is provided with high energy steam entrance (7), the other end of steam jet pump (8) is connected with working steam admission case (11), steam goes out vapour case (6) and is also connected with feeder (3), feeder (3) is provided with returning charge entrance (2) and pomace charge door (4), returning charge entrance (2) is provided with returning charge auger (1), returning charge auger (1) side is provided with and rises glassware (15), rise side, glassware (15) bottom and be provided with underground auger (14), be provided with above underground auger (14) one end and distribute auger (13).
2. the dry evaporation equipment of efficient energy-saving according to claim 1, is characterized in that, described distribution auger (13), underground auger (14) are all arranged on rotary drier (9) below.
3. the dry evaporation equipment of efficient energy-saving according to claim 1, is characterized in that, described working steam admission case (11) is respectively arranged with working steam entrance (10) and condensation-water drain (12) in two ends up and down.
4. the dry evaporation equipment of efficient energy-saving according to claim 1, is characterized in that, described feeder (3) is also connected with vavuum pump (5).
5. the dry evaporation equipment of efficient energy-saving according to claim 1, is characterized in that, described rotary drier (9) inwall scribbles high radiant energy dope layer.
6. the dry evaporation equipment of efficient energy-saving according to claim 1, is characterized in that, described steam jet pump (8) is provided with disperser.
7. the dry evaporation equipment of efficient energy-saving according to claim 1, is characterized in that, described distribution auger (13) and underground auger (14) all scribble wear-resistant coating.
8. the dry evaporation equipment of efficient energy-saving according to claim 1, is characterized in that, described feeder (3) is provided with weighing device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310472743.4A CN104621689A (en) | 2013-11-14 | 2013-11-14 | Energy-saving and efficient drying and evaporating equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310472743.4A CN104621689A (en) | 2013-11-14 | 2013-11-14 | Energy-saving and efficient drying and evaporating equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104621689A true CN104621689A (en) | 2015-05-20 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310472743.4A Pending CN104621689A (en) | 2013-11-14 | 2013-11-14 | Energy-saving and efficient drying and evaporating equipment |
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| CN (1) | CN104621689A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105466196A (en) * | 2015-12-25 | 2016-04-06 | 孙发喜 | Double-effect vacuum tube bundle drying system |
Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2044056U (en) * | 1988-04-07 | 1989-09-06 | 湖南省土产畜产进出口公司长沙羽毛厂 | Hot-air feather drying machine without shaft |
| JP3426590B1 (en) * | 2001-07-25 | 2003-07-14 | 東亜機械工業株式会社 | Roasted chestnut firing method |
| CN202907764U (en) * | 2012-06-27 | 2013-05-01 | 段伟 | Device for dehydrating vegetables by utilizing superheated steam |
| CN202958724U (en) * | 2012-11-08 | 2013-06-05 | 毛栋磊 | Drying and evaporating equipment |
| CN203028070U (en) * | 2013-01-11 | 2013-07-03 | 瓜州鑫诺甘草生态种植加工有限责任公司 | Medlar drying system |
-
2013
- 2013-11-14 CN CN201310472743.4A patent/CN104621689A/en active Pending
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2044056U (en) * | 1988-04-07 | 1989-09-06 | 湖南省土产畜产进出口公司长沙羽毛厂 | Hot-air feather drying machine without shaft |
| JP3426590B1 (en) * | 2001-07-25 | 2003-07-14 | 東亜機械工業株式会社 | Roasted chestnut firing method |
| CN202907764U (en) * | 2012-06-27 | 2013-05-01 | 段伟 | Device for dehydrating vegetables by utilizing superheated steam |
| CN202958724U (en) * | 2012-11-08 | 2013-06-05 | 毛栋磊 | Drying and evaporating equipment |
| CN203028070U (en) * | 2013-01-11 | 2013-07-03 | 瓜州鑫诺甘草生态种植加工有限责任公司 | Medlar drying system |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105466196A (en) * | 2015-12-25 | 2016-04-06 | 孙发喜 | Double-effect vacuum tube bundle drying system |
| CN105466196B (en) * | 2015-12-25 | 2018-01-19 | 郑州博大浓缩干燥设备有限公司 | Economic benefits and social benefits vacuum restrains drying system |
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Application publication date: 20150520 |