CN200983821Y - Device for producing DDGS feedstuff by using alcohol lees - Google Patents
Device for producing DDGS feedstuff by using alcohol lees Download PDFInfo
- Publication number
- CN200983821Y CN200983821Y CNU2006201351966U CN200620135196U CN200983821Y CN 200983821 Y CN200983821 Y CN 200983821Y CN U2006201351966 U CNU2006201351966 U CN U2006201351966U CN 200620135196 U CN200620135196 U CN 200620135196U CN 200983821 Y CN200983821 Y CN 200983821Y
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- Prior art keywords
- feed
- ddgs
- poor
- inspissator
- production
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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
- Y02P60/87—Re-use of by-products of food processing for fodder production
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Abstract
A DDGS feed manufacturing device from distillers' grains comprises a separating device of distillers' grains, the exit of the liquid feed is connected with a condenser via a pipe, the feed exit of which is connected with a mixer. The exit of the solid feed is connected via the pipe with the mixer; the feed exit of the mixer is connected with the feed entrance of drying machine of airflow consisting of overheating steam and air. The drying machine comprises an overheating steam generator, primary drying machine and a primary separating machine, which are communicated with each other in turn via a connecting pipe. The bottom of the primary drying machine is connected with a feed charging mechanism with a feed entrance and the feed exit of the primary separating machine is connected with the feed entrance of the secondary drying machine. The dry media entrance of the secondary drying machine is connected with the overheating air generator and the feed exit of the secondary drying machine is connected with the feed entrance of the secondary separating machine. The steam entrance of the primary separating machine is connected with the overheating media entrance of the condenser via the connecting pipe. The utility model has the advantages of low investment and low energy consumption.
Description
Technical field
The utility model belongs to the alcohol production technical field, particularly a kind of device that utilizes the poor DDGS of production of alcohol feed.
Background technology
Along with alcohol fuel promoting the use of in China, its output cumulative year after year, the output that the refuse in the production process---alcohol is poor is also increasing, and poor processing of alcohol also become a difficult problem.
The poor conventional method of handling of alcohol be adopt separate, concentrate, dry route.Dried forms commonly used has the steam drying of heated-air drying and indirect.In hot-air drying process, particularly contain sugared material surface and understood sclerderm, caking, hinder the evaporation of moisture, influence mass transfer and diabatic process; Material is because the duricrust on surface seriously hinders heat and quality transmission, and aerobic exists in hot-air simultaneously, if misoperation causes on fire easily; In actual industrial production, just run into because material contains certain sugar, when crossing heated-air drying, to lump, local temperature is too high, the phenomenon that occurs catching fire; In addition, the used heat grade that heated-air drying produces is low, and heat transfer coefficient is little, is difficult to be used, and causes volumetric efficiency low, and the heated-air drying energy consumption is very big.
And the steam drying of indirect type heating is that steam pipe is arranged in the drying machine, is thermal source with steam or superheated steam, utilizes the heat conduction to add thermal material, realizes the drying of material.If this drying means does not reclaim used heat, then energy consumption is very big; If with the Waste Heat Recovery utilization, owing to contain a spot of air in the used heat, and air exists as fixed gas in diabatic process, and heat transfer coefficient is descended greatly, causes needed heat transfer area to increase, it is big that volume of equipment becomes, and the corresponding apparatus investment increases.
The utility model content
The utility model purpose with the device that utilizes the poor DDGS of production of alcohol feed that provides that a kind of equipment investment is little, energy consumption is low.
For reaching above-mentioned purpose, the utility model adopts following technical scheme: a kind of device that utilizes the poor DDGS of production of alcohol feed, comprise the alcohol separator that is pickled with grains or in wine, the liquid material outlet of separator connects inspissator by pipeline, the inspissator material outlet connects blender by pipeline, the solid material outlet connects blender by pipeline, the blender material outlet is taken over vapours and air combined type pneumatic drier material inlet, drying machine comprises the superheated steam generator that is communicated with by tube connector successively, one-level drier and primary separator, the material feeding mechanism of one-level drier bottom connecting band material inlet, the primary separator material outlet connects secondary drying implements material inlet, secondary drying device drying medium inlet connects hot-air generator, the outlet of secondary drying implements material connects the second-stage separator material inlet, and the primary separator steam (vapor) outlet connects inspissator heat medium inlet by tube connector.
The primary separator steam (vapor) outlet has the tube connector of circulating fan to be communicated with superheated steam generator by string.
The primary separator steam (vapor) outlet is communicated with hot-air generator by tube connector.
The primary separator discharging opening is connected with one-level dryer feed mouth.
The second-stage separator exhaust passage is provided with blower fan.
Be provided with heater and steam channel in the superheated steam generator, perhaps be provided with heat medium passage and steam channel; Be provided with steam channel and air duct in the hot-air generator.
Inspissator material outlet pipe connects the inspissator material inlet by the refeed line that is serially connected with pump.
The utility model adopts superheated steam and air combined type pneumatic drier to come dry alcohol poor, and the thermal capacitance that makes full use of superheated steam in the one-level dry run is bigger, and lump can not formed in the material surface, the characteristics that energy consumption is low, security performance is good; Utilize hot air in the secondary drying process, effectively avoided adopting the material of superheat steam drying to occur the problem of getting damp easily when discharging, drying effect is good.The Low Temperature Steam that produces in the dry run (or claiming low-grade steam or indirect steam) can be back to use in superheated steam generator, hot-air generator or the concentrator, realizes the utilization again of used heat.Do not contain air in the indirect steam, heat transfer coefficient is big, and the heat transfer area that concentrator is needed is less, and corresponding apparatus is little, invests also for a short time, and energy consumption is low.The alcohol that is applicable to all alcohol production raw materials is poor.
In the utility model, superheated steam generator, hot-air generator, drier, separator (cyclone separator), blower fan are conventional equipment, superheated steam generator can adopt various heating arrangement well known to those skilled in the art (as electric heating device, flue gas heating arrangement etc.), and hot-air generator adopts to be provided with and carries out the steam channel of heat exchange and the heat exchange mechanism of air duct mutually.
Description of drawings
Fig. 1 is the utility model structural representation;
Fig. 2 is embodiment 2 structural representations.
The specific embodiment
In embodiment 2, the present embodiment, inspissator 2 adopts heating clamber 2-1 and vaporization chamber 2-2 isolating construction, separator 1 liquid material outlet by pipeline connect the material inlet of the heating clamber 2-1 bottom of inspissator 2, the material outlet at heating clamber 2-1 top connects vaporization chamber 2-2 material inlet, vaporization chamber 2-2 material outlet is leaded up to pipeline and is connect blender 4, and another road connects the material inlet of inspissator 2 heating clamber 2-1 bottom by the return tube that is serially connected with circulating pump 3; Vaporization chamber 2-2 top is provided with outlet, in order to discharge the water vapour that forms in the concentration process.Primary cyclone 5-4 material outlet is connected with one-level drier 5-3 material inlet.Other are with embodiment 1.
In the foregoing description, the initial steam that is used for dried material can be produced by steam boiler.The poor separator 1 of alcohol adopts horizontal centrifuge, and blender 4 adopts the spirally-wound type blender.
Claims (8)
1, a kind of device that utilizes the poor DDGS of production of alcohol feed, comprise the alcohol separator that is pickled with grains or in wine, the liquid material outlet of separator connects inspissator by pipeline, the inspissator material outlet connects blender by pipeline, the solid material outlet connects blender by pipeline, it is characterized in that, the blender material outlet is taken over vapours and air combined type pneumatic drier material inlet, drying machine comprises the superheated steam generator that is communicated with by tube connector successively, one-level drier and primary separator, the material feeding mechanism of one-level drier bottom connecting band material inlet, the primary separator material outlet connects secondary drying implements material inlet, secondary drying device drying medium inlet connects hot-air generator, the outlet of secondary drying implements material connects the second-stage separator material inlet, and the primary separator steam (vapor) outlet connects inspissator heat medium inlet by tube connector.
2, the device that utilizes the poor DDGS of production of alcohol feed as claimed in claim 1 is characterized in that the primary separator steam (vapor) outlet has the tube connector of circulating fan to be communicated with superheated steam generator by string.
3, the device that utilizes the poor DDGS of production of alcohol feed as claimed in claim 1 or 2 is characterized in that the primary separator steam (vapor) outlet is communicated with hot-air generator by tube connector.
4, the device that utilizes the poor DDGS of production of alcohol feed as claimed in claim 3 is characterized in that the primary separator discharging opening is connected with one-level dryer feed mouth.
5, the device that utilizes the poor DDGS of production of alcohol feed as claimed in claim 4 is characterized in that the second-stage separator exhaust passage is provided with blower fan.
6, the device that utilizes the poor DDGS of production of alcohol feed as claimed in claim 5 is characterized in that, is provided with heater and steam channel in the superheated steam generator, perhaps is provided with heat medium passage and steam channel; Be provided with steam channel and air duct in the hot-air generator.
7, the device that utilizes the poor DDGS of production of alcohol feed as claimed in claim 4 is characterized in that inspissator material outlet pipe connects the inspissator material inlet by the refeed line that is serially connected with pump.
8, as claim 5, the 6 or 7 described devices that utilize the poor DDGS of production of alcohol feed, it is characterized in that inspissator material outlet pipe connects the inspissator material inlet by the refeed line that is serially connected with pump.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006201351966U CN200983821Y (en) | 2006-12-25 | 2006-12-25 | Device for producing DDGS feedstuff by using alcohol lees |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2006201351966U CN200983821Y (en) | 2006-12-25 | 2006-12-25 | Device for producing DDGS feedstuff by using alcohol lees |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN200983821Y true CN200983821Y (en) | 2007-12-05 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2006201351966U Expired - Fee Related CN200983821Y (en) | 2006-12-25 | 2006-12-25 | Device for producing DDGS feedstuff by using alcohol lees |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN200983821Y (en) |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103047847A (en) * | 2012-12-14 | 2013-04-17 | 河南天冠企业集团有限公司 | Method for producing steam by fully utilizing cassava grains |
| CN105865191A (en) * | 2016-04-22 | 2016-08-17 | 天华化工机械及自动化研究设计院有限公司 | Method for vinasse tube bank type drying and exhaust gas and steam condensed liquid heat recycling |
| CN105928329A (en) * | 2016-04-22 | 2016-09-07 | 天华化工机械及自动化研究设计院有限公司 | Tube-bundle drying method for stillage |
| CN106036965A (en) * | 2016-07-25 | 2016-10-26 | 江苏迈安德节能蒸发设备有限公司 | Production system of DDGS feeds |
| CN106071109A (en) * | 2016-07-25 | 2016-11-09 | 江苏迈安德节能蒸发设备有限公司 | A kind of production technology of DDGS feedstuff |
| CN106110685A (en) * | 2016-07-25 | 2016-11-16 | 江苏迈安德节能蒸发设备有限公司 | A kind of waste heat utilizing drying machine is evaporated the system concentrated |
| CN107446757A (en) * | 2017-09-28 | 2017-12-08 | 泸州老窖集团有限责任公司 | A kind of white liquor distilling does poor devices and methods therefor |
| RU2733435C1 (en) * | 2020-05-12 | 2020-10-01 | Общество с ограниченной ответственностью «КОРОЛАН» | System for collection of juice vapors in boiling feed boilers |
| CN113679065A (en) * | 2020-05-18 | 2021-11-23 | 中国石油天然气股份有限公司 | DDGS feed drying device and method |
-
2006
- 2006-12-25 CN CNU2006201351966U patent/CN200983821Y/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103047847A (en) * | 2012-12-14 | 2013-04-17 | 河南天冠企业集团有限公司 | Method for producing steam by fully utilizing cassava grains |
| CN105865191A (en) * | 2016-04-22 | 2016-08-17 | 天华化工机械及自动化研究设计院有限公司 | Method for vinasse tube bank type drying and exhaust gas and steam condensed liquid heat recycling |
| CN105928329A (en) * | 2016-04-22 | 2016-09-07 | 天华化工机械及自动化研究设计院有限公司 | Tube-bundle drying method for stillage |
| CN106036965A (en) * | 2016-07-25 | 2016-10-26 | 江苏迈安德节能蒸发设备有限公司 | Production system of DDGS feeds |
| CN106071109A (en) * | 2016-07-25 | 2016-11-09 | 江苏迈安德节能蒸发设备有限公司 | A kind of production technology of DDGS feedstuff |
| CN106110685A (en) * | 2016-07-25 | 2016-11-16 | 江苏迈安德节能蒸发设备有限公司 | A kind of waste heat utilizing drying machine is evaporated the system concentrated |
| CN106036965B (en) * | 2016-07-25 | 2018-01-30 | 江苏迈安德节能蒸发设备有限公司 | A kind of production system of DDGS feeds |
| CN106110685B (en) * | 2016-07-25 | 2018-03-20 | 江苏迈安德节能蒸发设备有限公司 | The system that a kind of waste heat using drying machine is evaporated concentration |
| CN107446757A (en) * | 2017-09-28 | 2017-12-08 | 泸州老窖集团有限责任公司 | A kind of white liquor distilling does poor devices and methods therefor |
| RU2733435C1 (en) * | 2020-05-12 | 2020-10-01 | Общество с ограниченной ответственностью «КОРОЛАН» | System for collection of juice vapors in boiling feed boilers |
| CN113679065A (en) * | 2020-05-18 | 2021-11-23 | 中国石油天然气股份有限公司 | DDGS feed drying device and method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20071205 Termination date: 20151225 |
|
| EXPY | Termination of patent right or utility model |