CN205641936U - Fodder drying -machine waste heat recovery utilizes system - Google Patents

Fodder drying -machine waste heat recovery utilizes system Download PDF

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Publication number
CN205641936U
CN205641936U CN201620315250.9U CN201620315250U CN205641936U CN 205641936 U CN205641936 U CN 205641936U CN 201620315250 U CN201620315250 U CN 201620315250U CN 205641936 U CN205641936 U CN 205641936U
Authority
CN
China
Prior art keywords
valve
discharge duct
waste heat
recycling system
heat recycling
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201620315250.9U
Other languages
Chinese (zh)
Inventor
杨世明
王健宇
郑远东
岳双明
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Danling Zhengbang Feed Co., Ltd.
Original Assignee
Meishan Jinchuannong Biotechnology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Meishan Jinchuannong Biotechnology Co Ltd filed Critical Meishan Jinchuannong Biotechnology Co Ltd
Priority to CN201620315250.9U priority Critical patent/CN205641936U/en
Application granted granted Critical
Publication of CN205641936U publication Critical patent/CN205641936U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/10Greenhouse 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

Abstract

The utility model relates to a fodder drying -machine waste heat recovery utilizes system, it includes drying -machine (1), steam jacket quenching and tempering ware (2), heating device (3), temperature sensor (4), humidity transducer (5) and control system (6), steam jacket quenching and tempering ware (2) including quenching and tempering room (21), press from both sides jacket layer (22) and heat preservation (23), drying -machine (1) through exhaust duct A (7) with press from both sides jacket layer (22) intercommunication, exhaust duct A (7) on still be connected with exhaust duct B (8), just exhaust duct A (7) and exhaust duct B (8) on be provided with valve (9), heating device (3), temperature sensor (4), humidity transducer (5) and valve (9) all be connected with control system (6). The utility model has the advantages of waste heat utilization efficiency is high, the energy consumption is low.

Description

A kind of feed dryer waste heat recycling system
Technical field
This utility model relates to Feed Production Technology field, particularly a kind of feed dryer waste heat recycling system.
Background technology
Quenched and drying is the twice important procedure in Feed Manufacturing.The so-called quenched powder that refers to is passed through saturated vapor under high temperature, high pressure and makes the process of its ripening, quenched can promote feedstuff forming ability, improve granular mass, improve the resistance to water of pellet, improve the nutrition digestion absorbance of feedstuff, reduce molding energy consumption, kill harmful levels of pathogens, it is simple to liquid adds;Dry then primarily to the excessive moisture removed in feedstuff, it is simple to subsequent storage, prevent from going mouldy.At present, numerous processing enterprises utilize dehydrator to be all directly discharged into the high-temperature vapor (temperature is at 50 degrees centigrade) produced after feed drying in air, effectively utilize, and the vapours needed during quenched is manufactured separately again, the utilization rate of vapours will certainly be improved as the vapours in drying course being used for quenched process, reducing energy consumption.
Utility model content
The purpose of this utility model is to overcome the shortcoming of prior art, it is provided that a kind of can improve utilization rate of waste heat in Feed Manufacturing, reduce energy consumption feed dryer waste heat recycling system.
The purpose of this utility model is achieved through the following technical solutions: it includes dehydrator, steam jacket quality-adjusting device, heater, temperature sensor, humidity sensor and control system, described steam jacket quality-adjusting device includes quenched room, chuck layer and heat-insulation layer, described quenched indoor are provided with humidity sensor, it is provided with heater and temperature sensor in described chuck layer, the vapours outlet of described dehydrator is connected with the chuck layer on described steam jacket quality-adjusting device by discharge duct A, it is also associated with discharge duct B on described discharge duct A, and it is provided with valve on described discharge duct A and discharge duct B, described heater, temperature sensor, humidity sensor and valve are all connected with control system.
Preferably, described heater is electrical heating elements.
Preferably, described discharge duct A is provided with drainage screen.
Preferably, described valve is arranged on discharge duct A and the junction of discharge duct B, and described valve closes discharge duct B while opening discharge duct A.
Preferably, described valve is electrically operated valve, and it includes that motor, rotating shaft and baffle plate, described rotating shaft are arranged on the outfan of motor, and described baffle plate is arranged in rotating shaft.
Preferably, described heat-insulation layer is asbestos heat-insulation layer.
Preferably, described chuck layer is also associated with jet chimney.
Preferably, described valve includes that valve A and valve B, described valve A and valve B are separately mounted on discharge duct A and aerofluxus discharge pipe B, and the valve port size of described valve A and valve B is adjustable.
This utility model has the advantage that this utility model, by being used in the steam jacket quality-adjusting device of quenched process by the vapours produced in dehydrator circulation and stress, is effectively improved the utilization ratio of heat energy, contributes to saving the energy, reduces energy consumption;And apparatus structure is simple, automaticity is high, and the opening and closing of heater and valve can be controlled in real time by control system according to the data message of temperature sensor, humidity sensor collection, and regulation and control are in time.
Accompanying drawing explanation
Fig. 1 is the structural representation in this utility model detailed description of the invention 1;
Fig. 2 is the structural representation in this utility model detailed description of the invention 2;
In figure: 1-dehydrator, 2-steam jacket quality-adjusting device, the quenched room of 21-, 22-chuck layer, 23-heat-insulation layer, 3-heater, 4-temperature sensor, 5-humidity sensor, 6-control system, 7-discharge duct A, 8-discharge duct B, 9-valve, 91-valve A, 92-valve B, 10-drainage screen, 11-jet chimney.
Detailed description of the invention
Below in conjunction with the accompanying drawings this utility model is further described, but protection domain of the present utility model is not limited to the following stated.
[detailed description of the invention 1]
As it is shown in figure 1, it includes dehydrator 1, steam jacket quality-adjusting device 2, heater 3, temperature sensor 4, humidity sensor 5 and control system 6.
Described steam jacket quality-adjusting device 2 includes quenched room 21, chuck floor 22 and heat-insulation layer 23, and heat-insulation layer 23 uses asbestos material to be incubated;Being provided with humidity sensor 5 in described quenched room 21, be provided with heater 3 and temperature sensor 4 in described chuck layer 22, heater 3 is electrical heating elements.
The vapours outlet of described dehydrator 1 is connected with the chuck layer 22 on described steam jacket quality-adjusting device 2 by discharge duct A7, jet chimney 11 it is also associated with on chuck layer 22, drainage screen 10 it is provided with on discharge duct A7, discharge duct B8 it is also associated with on discharge duct A7, and the junction of described discharge duct A7 and discharge duct B8 is provided with valve 9, described valve 9 closes discharge duct B8 while opening discharge duct A7, valve 9 is electrically operated valve, it includes motor, rotating shaft and baffle plate, described rotating shaft is arranged on the outfan of motor, baffle plate is arranged in rotating shaft.
Described heater 3, temperature sensor 4, humidity sensor 5 and valve 9 are all connected with control system 6.The temperature information that control system 6 can gather according to temperature sensor 4, the heat time heating time of regulation and control heater 3;The humidity index collected according to humidity sensor 5 controls the opening and closing of valve 9;When vapours is not enough in dehydrator 1, also can open the valve on jet chimney 11, use other vapour sources;Automaticity is high.
[detailed description of the invention 2]
This detailed description of the invention is with the difference of detailed description of the invention 1: described valve 9 includes valve A91 and valve B92, described valve A91 and valve B92 is separately mounted on discharge duct A7 and aerofluxus discharge pipe B8, and the valve port size of described valve A91 and valve B92 is adjustable.During use, control system 6 can according to the valve port size of quantity of steam control valve A91 and valve B92 required in steam jacket quality-adjusting device 2, thus control to enter the quantity of steam in chuck layer 22.

Claims (8)

  1. null1. a feed dryer waste heat recycling system,It is characterized in that: it includes dehydrator (1)、Steam jacket quality-adjusting device (2)、Heater (3)、Temperature sensor (4)、Humidity sensor (5) and control system (6),Described steam jacket quality-adjusting device (2) includes quenched room (21)、Chuck layer (22) and heat-insulation layer (23),It is provided with humidity sensor (5) in described quenched room (21),Heater (3) and temperature sensor (4) it is provided with in described chuck layer (22),The vapours of described dehydrator (1) exports by discharge duct A(7) connect with the chuck layer (22) on described steam jacket quality-adjusting device (2),Described discharge duct A(7) on be also associated with discharge duct B(8),And described discharge duct A(7) and discharge duct B(8) on be provided with valve (9),Described heater (3)、Temperature sensor (4)、Humidity sensor (5) and valve (9) are all connected with control system (6).
  2. A kind of feed dryer waste heat recycling system the most according to claim 1, it is characterised in that: described heater (3) is electrical heating elements.
  3. A kind of feed dryer waste heat recycling system the most according to claim 1, it is characterised in that: it is provided with drainage screen (10) on described discharge duct A(7).
  4. A kind of feed dryer waste heat recycling system the most according to claim 1, it is characterized in that: described valve (9) is arranged on discharge duct A(7) and discharge duct B(8) junction, described valve (9) opens discharge duct A(7) while close discharge duct B(8).
  5. A kind of feed dryer waste heat recycling system the most according to claim 4, it is characterized in that: described valve (9) is electrically operated valve, it includes that motor, rotating shaft and baffle plate, described rotating shaft are arranged on the outfan of motor, and described baffle plate is arranged in rotating shaft.
  6. A kind of feed dryer waste heat recycling system the most according to claim 1, it is characterised in that: described heat-insulation layer (23) is asbestos heat-insulation layer.
  7. A kind of feed dryer waste heat recycling system the most according to claim 1, it is characterised in that: it is also associated with jet chimney (11) on described chuck layer (22).
  8. A kind of feed dryer waste heat recycling system the most according to claim 1, it is characterized in that: described valve (9) includes valve A(91) and valve B(92), described valve A(91) and valve B(92) be separately mounted to discharge duct A(7) and aerofluxus discharge pipe B(8) on, and described valve A(91) and valve B(92) valve port size adjustable.
CN201620315250.9U 2016-04-15 2016-04-15 Fodder drying -machine waste heat recovery utilizes system Expired - Fee Related CN205641936U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201620315250.9U CN205641936U (en) 2016-04-15 2016-04-15 Fodder drying -machine waste heat recovery utilizes system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201620315250.9U CN205641936U (en) 2016-04-15 2016-04-15 Fodder drying -machine waste heat recovery utilizes system

Publications (1)

Publication Number Publication Date
CN205641936U true CN205641936U (en) 2016-10-12

Family

ID=57065339

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201620315250.9U Expired - Fee Related CN205641936U (en) 2016-04-15 2016-04-15 Fodder drying -machine waste heat recovery utilizes system

Country Status (1)

Country Link
CN (1) CN205641936U (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108499685A (en) * 2016-11-21 2018-09-07 郑州天舜电子技术有限公司 A kind of sludge quick drying apparatus with breaker
CN110403216A (en) * 2019-08-30 2019-11-05 淮北市乾乾生物科技有限公司 A kind of livestock feed production feed granules curing sterilizing device and its sterilizing methods
CN113758226A (en) * 2021-09-13 2021-12-07 南昌航空大学 Dryer tail gas waste heat recovery device, dryer and waste heat recovery method
CN115251430A (en) * 2022-07-20 2022-11-01 通威股份有限公司 Environment-friendly low-energy-consumption feed production system

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108499685A (en) * 2016-11-21 2018-09-07 郑州天舜电子技术有限公司 A kind of sludge quick drying apparatus with breaker
CN108499685B (en) * 2016-11-21 2019-11-05 安徽省通源环境节能股份有限公司 A kind of sludge quick drying apparatus with crushing device
CN110403216A (en) * 2019-08-30 2019-11-05 淮北市乾乾生物科技有限公司 A kind of livestock feed production feed granules curing sterilizing device and its sterilizing methods
CN113758226A (en) * 2021-09-13 2021-12-07 南昌航空大学 Dryer tail gas waste heat recovery device, dryer and waste heat recovery method
CN115251430A (en) * 2022-07-20 2022-11-01 通威股份有限公司 Environment-friendly low-energy-consumption feed production system
CN115251430B (en) * 2022-07-20 2023-04-14 通威股份有限公司 Environment-friendly low-energy-consumption feed production system

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Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CP01 Change in the name or title of a patent holder
CP01 Change in the name or title of a patent holder

Address after: 620000 Mechanical Industrial Park of Danling Town, Danling County, Meishan City, Sichuan Province

Patentee after: Danling Zhengbang Feed Co., Ltd.

Address before: 620000 Mechanical Industrial Park of Danling Town, Danling County, Meishan City, Sichuan Province

Patentee before: Meishan Jinchuannong Biotechnology Co., Ltd.

CF01 Termination of patent right due to non-payment of annual fee
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20161012

Termination date: 20200415