CN206944680U - A kind of efficiently yeast drying heat-exchange device - Google Patents

A kind of efficiently yeast drying heat-exchange device Download PDF

Info

Publication number
CN206944680U
CN206944680U CN201720457657.XU CN201720457657U CN206944680U CN 206944680 U CN206944680 U CN 206944680U CN 201720457657 U CN201720457657 U CN 201720457657U CN 206944680 U CN206944680 U CN 206944680U
Authority
CN
China
Prior art keywords
heat
vapor
intake stack
main switch
switch room
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.)
Active
Application number
CN201720457657.XU
Other languages
Chinese (zh)
Inventor
陈红卫
王东齐
王峰
张来伟
王飞
袁淑华
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.)
ANGEL YEAST (SUIXIAN) Co Ltd
Original Assignee
ANGEL YEAST (SUIXIAN) 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 ANGEL YEAST (SUIXIAN) Co Ltd filed Critical ANGEL YEAST (SUIXIAN) Co Ltd
Priority to CN201720457657.XU priority Critical patent/CN206944680U/en
Application granted granted Critical
Publication of CN206944680U publication Critical patent/CN206944680U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Drying Of Solid Materials (AREA)

Abstract

A kind of efficiently yeast drying heat-exchange device, including intake stack and vapor pipeline, it is characterised in that:Vapor enters the main switch room of pipeline communication, and main switch room connects pre- heat-exchanging chamber, pre- heat-exchanging chamber connection vapor outflow pipeline by steam intermediate conduit;The approach section of intake stack is extended in pre- heat-exchanging chamber, and it out forms air intake intermediate conduit, and air intake intermediate conduit is extended in main switch room, and it out forms the discharge section of intake stack, the discharge section connection starch liquefacation tank of intake stack;Intake stack is at least four independent of each other.Relative to prior art, technique effect of the present utility model is that the utility model is provided with pre- heat-exchanging chamber, the air for entering main switch room is preheated, less energy is just needed in main switch room, so, same vapor supplying temperature, can drive more hot-air ducts.

Description

A kind of efficiently yeast drying heat-exchange device
Technical field
It the utility model is related to a kind of yeast production equipment, and in particular to efficient yeast drying heat-exchange device.
Background technology
The production of present yeast in yeast mud, it is necessary to be dried to particle.It is in drying process, it is necessary to substantial amounts of to drying tower Heat.If directly feeding vapor, drying tower can moisturize, and influence your drying effect.Exchanged so typically to pass through Room, by the heat exchange of vapor to air, drying tower is connected by hot-air.Such as Fig. 1, vapor enters pipeline 11, vapor Flow out pipeline 12 and connect switch room 5, the approach section 22 of intake stack is in switch room by the way that the part extended out forms air intake The discharge section 21 of pipeline, the discharge section 21 of intake stack connect starch liquefacation tank.Hot-air duct is multigroup, and its is independent of one another.
Utility model content
The technical problems to be solved in the utility model is:Switch room can only drive three groups of hot-air ducts, less efficient.
The purpose of this utility model is to provide a kind of efficiently yeast drying heat-exchange device.
The technical solution of the utility model is specially:
A kind of efficiently yeast drying heat-exchange device, including intake stack and vapor pipeline, it is characterised in that:Vapor Into the main switch room of pipeline communication, main switch room connects pre- heat-exchanging chamber by steam intermediate conduit, and pre- heat-exchanging chamber connects water Steam effuser road;The approach section of intake stack is extended in pre- heat-exchanging chamber, and it, which comes out, forms air intake intermediate conduit, in air intake Between pipeline extend in main switch room, it out forms the discharge section of intake stack, the discharge section connection starch fluid of intake stack Change tank;Intake stack is at least four independent of each other.
Intake stack is five.
Vapor flows out the boiler that pipeline communication enters pipeline supply vapor to collector pipe to vapor.
Relative to prior art, technique effect of the present utility model is that the utility model is provided with pre- heat-exchanging chamber, will enter The air of main switch room is preheated, and less energy is just needed in main switch room, so, same vapor supplying temperature, More hot-air ducts can be driven.
Brief description of the drawings
Fig. 1 is the schematic diagram of prior art.
Fig. 2 schematic diagrames of the present utility model.
Embodiment
As shown in Figure 2, a kind of efficiently yeast drying heat-exchange device, including intake stack and vapor pipeline, water steam Gas connects main switch room 51 into pipeline 11, and main switch room 51 connects pre- heat-exchanging chamber 52 by steam intermediate conduit 13, preheating Switch room 52 connects vapor outflow pipeline 12.
The approach section 22 of intake stack is extended in pre- heat-exchanging chamber 52, and it out forms air intake intermediate conduit 23, air intake Intermediate conduit 23 is extended in main switch room 51, and it out forms the discharge section 21 of intake stack, the discharge section 21 of intake stack Connect starch liquefacation tank.
Intake stack is at least four independent of each other.
Intake stack is five.
Vapor outflow pipeline 12 connects the boiler for entering the supply vapor of pipeline 11 to vapor to collector pipe.Because should The temperature of water is 60-70 DEG C, saves part energy.
Its work was originally:
It is cold air in the approach section 22 of intake stack, by the heating of pre- heat-exchanging chamber 52, air intake intermediate conduit 23 Temperature rises to 90 DEG C or so, is entering main switch room 51, just can obtain higher temperature, starch liquefacation tank can given to provide energy Amount.
Besides the heat of original discharge air make use of one time by this design, also more low-carbon environment-friendly.
Above-described is only preferred embodiment of the present utility model, it is noted that for those skilled in the art For, under the premise of the utility model general idea is not departed from, some changes and improvements can also be made, these should also be considered as The scope of protection of the utility model.

Claims (3)

1. a kind of efficiently yeast drying heat-exchange device, including intake stack and vapor pipeline, it is characterised in that:Vapor enters Enter pipeline(11)Connect main switch room(51), main switch room(51)Pass through steam intermediate conduit(13)Connect pre- heat-exchanging chamber (52), pre- heat-exchanging chamber(52)Connect vapor outflow pipeline(12);
The approach section of intake stack(22)Extend to pre- heat-exchanging chamber(52)Interior, it out forms air intake intermediate conduit(23), enter Wind intermediate conduit(23)Extend to main switch room(51)Interior, it out forms the discharge section of intake stack(21), intake stack Discharge section(21)Connect starch liquefacation tank;
Intake stack is at least four independent of each other.
2. efficiently yeast drying heat-exchange device as claimed in claim 1, it is characterised in that:Intake stack is five.
3. efficiently yeast drying heat-exchange device as claimed in claim 1, it is characterised in that:Vapor flows out pipeline(12)Even Lead to and enter pipeline to vapor to collector pipe(11)Supply the boiler of vapor.
CN201720457657.XU 2017-04-27 2017-04-27 A kind of efficiently yeast drying heat-exchange device Active CN206944680U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201720457657.XU CN206944680U (en) 2017-04-27 2017-04-27 A kind of efficiently yeast drying heat-exchange device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201720457657.XU CN206944680U (en) 2017-04-27 2017-04-27 A kind of efficiently yeast drying heat-exchange device

Publications (1)

Publication Number Publication Date
CN206944680U true CN206944680U (en) 2018-01-30

Family

ID=61359201

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201720457657.XU Active CN206944680U (en) 2017-04-27 2017-04-27 A kind of efficiently yeast drying heat-exchange device

Country Status (1)

Country Link
CN (1) CN206944680U (en)

Similar Documents

Publication Publication Date Title
CN101693230B (en) Coating machine heat recovery utilization energy-saving device
CN203796339U (en) Waste heat recovery device of direct air cooling unit
CN102519139A (en) Air source heat pump system for providing direct high temperature air
CN206944680U (en) A kind of efficiently yeast drying heat-exchange device
CN203172156U (en) Hybrid energy-saving heat drying system applied to photogravure press and dry type compound machine
CN202281463U (en) Denitration catalyst drying device
CN204115230U (en) Industrial tandem type electric energy heat storage device
CN204187842U (en) A kind of heat-exchanging water tank of gas heater
CN203798205U (en) Industrial waste gas waste heat-recycling heat exchanging device
CN207729834U (en) A kind of environment-protecting industrial hot-water supply device
CN206222690U (en) A kind of drinking water heating furnace
CN206958585U (en) A kind of blast furnace blower Lubricating oil heating device
CN205372710U (en) Energy -saving apparatus
CN103868377B (en) Industrial waste gas waste heat recovery heat-exchanger rig
CN200972341Y (en) Conversion turbulence modified plasma high temp. heat exchange set
CN204786333U (en) Purified cotton stoving in -process steam supply device
CN204612549U (en) A kind of heat exchanger
CN213930866U (en) High-voltage sand energy storage steam supply device
CN209351075U (en) A kind of novel external steam heat-exchanger drying system
CN204612540U (en) A kind of heat exchanger
CN204438508U (en) A kind of electric airheater of improvement
CN204268655U (en) Air conditioner heat reclaims energy-saving hot-water system
CN203011219U (en) Heat exchanger for boiler
CN203807884U (en) Thermal energy recovery device
CN203669945U (en) Waste heat recovery device for indirect air cooling unit

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant