CN203869556U - Heat exchange device for fermented and sterilized organic matter solid bulk materials - Google Patents
Heat exchange device for fermented and sterilized organic matter solid bulk materials Download PDFInfo
- Publication number
- CN203869556U CN203869556U CN201420207173.6U CN201420207173U CN203869556U CN 203869556 U CN203869556 U CN 203869556U CN 201420207173 U CN201420207173 U CN 201420207173U CN 203869556 U CN203869556 U CN 203869556U
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- Prior art keywords
- transferring medium
- heat transferring
- spiral conveying
- conveying tube
- shell
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- 239000000463 material Substances 0.000 title claims abstract description 38
- 239000007787 solid Substances 0.000 title claims abstract description 20
- 239000005416 organic matter Substances 0.000 title abstract 5
- 230000001954 sterilising effect Effects 0.000 claims abstract description 30
- 238000007599 discharging Methods 0.000 claims abstract description 16
- 239000011229 interlayer Substances 0.000 claims abstract description 9
- 238000000855 fermentation Methods 0.000 claims description 21
- 230000004151 fermentation Effects 0.000 claims description 21
- 230000008676 import Effects 0.000 claims description 18
- 239000002826 coolant Substances 0.000 claims description 4
- 238000004659 sterilization and disinfection Methods 0.000 claims description 4
- 238000000034 method Methods 0.000 abstract description 3
- 230000001105 regulatory effect Effects 0.000 abstract 1
- 239000002609 medium Substances 0.000 description 35
- 238000001816 cooling Methods 0.000 description 9
- 241000233866 Fungi Species 0.000 description 6
- 239000003337 fertilizer Substances 0.000 description 6
- 239000001963 growth medium Substances 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 5
- 235000011890 sandwich Nutrition 0.000 description 4
- 238000001035 drying Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 238000011081 inoculation Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- 230000000844 anti-bacterial effect Effects 0.000 description 2
- 239000000498 cooling water Substances 0.000 description 2
- 238000005469 granulation Methods 0.000 description 2
- 230000003179 granulation Effects 0.000 description 2
- 238000007908 dry granulation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
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- Fertilizers (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The utility model discloses a heat exchange device for fermented and sterilized organic matter solid bulk materials. The heat exchange device comprises a spiral conveying pipe and a shell externally provided with an interlayer and arranged outside the spiral conveying pipe. One end of the shell is provided with a feeding port, and the other end of the shell is provided with a discharging port. The interlayer of the shell is filled with heat exchange media. The spiral conveying pipe is hollow and filled with heat exchange media. The two ends of the spiral conveying pipe are fixed to a base through bearings, and one end of the spiral conveying pipe is provided with a motor. According to the heat exchange device for the fermented and sterilized organic matter solid bulk materials, temperature regulating and sterilizing of the organic matter solid bulk materials are conducted in different devices, the fermenting device is used in cooperation with the sterilizing device to complete the heat exchange process of the materials, losses of heat energy are avoided, the energy is saved, and the organic matter solid bulk materials are conveyed automatically.
Description
Technical field
The utility model relates to the heat-exchanger rig of the organic solid bulk cargo after a kind of fermentation and sterilizing.
Background technology
The processing of organic solid bulk cargo comprises the fermentation of organic solid bulk cargo, sterilizing, cooling or oven dry, inoculation or granulation.As the pretreatment of culture medium of edible fungus is needed to cooling rear inoculation in fermentation and sterilizing after completing; And after being completed, the fermentation of the production of fertilizer and fermented feed and sterilizing need to dry rear granulation.Existing to the cooling general of the culture medium of edible fungus after fermentation and sterilizing with its sterilizing is completed in same workshop, sterilizing chamber adopts high-temperature sterilization, its need to temperature higher, coolingly need to reduce temperature, so, after sterilizing, the processing of workshop need to being lowered the temperature, because temperature just alters a great deal, and complete after the processing of this batch materials, next group material needs again to heat up, cooling, it not only consumes the huge energy, and in the process of cooling that heats up, has formed the waste of the energy.For needing to continue to be warmed up to the temperature that can dry material after the production of fertilizer and fermented feed sterilizing, the production that it neither be continuous, but finish a collection of after, change another batch, cooling sterilizing, then the process that heats up and dry, it has formed the waste of the energy.And when changing material, whole workshop is open, has also formed the waste of the energy.
Summary of the invention
The purpose of this utility model solves the above-mentioned problems in the prior art exactly, the heat-exchanger rig of the organic solid bulk cargo after a kind of fermentation and sterilizing is provided, this device carries out the temperature adjustment of organic solid bulk cargo and sterilizing in different device, and be used in conjunction with fermentation and bactericidal unit, complete continuously material heat exchange operation, avoid hot loss of energy, and saved the energy, and to organic solid bulk cargo automatic transport.
For achieving the above object, technical solution of the present utility model is: the heat-exchanger rig of the organic solid bulk cargo after a kind of fermentation and sterilizing, it is to place from the horizontal by 0 ° of-90 ° of angle, and it comprises the shell of spiral conveying tube and the outer sandwich of spiral conveying tube; Shell one end has charging aperture, and the other end has discharging opening; Charging aperture is over against the discharging opening of the discharging gate of fermentation and sterilization device; In the interlayer of shell, be filled with heat transferring medium, according to the stroke of material, on the outer shell outer wall of charging aperture one end, have heat transferring medium outlet A, on the outer shell outer wall away from charging aperture one end, have heat transferring medium import A; Hollow in spiral conveying tube, is filled with heat transferring medium in it, according to the stroke of material, it has heat transferring medium outlet B in charging aperture one end, away from charging aperture one end, have heat transferring medium import B; Spiral conveying tube two ends are fixed on base by bearing, and its one end is provided with motor.
The shell of the outer sandwich of spiral conveying tube described above and spiral conveying tube is divided into two parts, and its part makes material up, and another part makes material descending; Between two parts, by discharging opening, be connected with infundibulate charging aperture, there is the stirrer paddle that is fixed on spiral conveying tube upper end at discharging opening place, and two-part spiral conveying tube upper end is all fixed with sprocket wheel, and described motor is fixed therein a part of spiral conveying tube upper end; According to the stroke of material, make the up part heat transferring medium import A of material and heat transferring medium import B in upper end, make the descending part heat transferring medium import A of material and heat transferring medium import B in lower end; Make the up part heat transferring medium outlet A of material and heat transferring medium outlet B in lower end, make the descending part heat transferring medium outlet A of material and heat transferring medium outlet B in upper end.
The heat transferring medium being filled with in the heat transferring medium being filled with in the interlayer of shell described above and spiral conveying tube is cooling medium, and it is applicable to just complete culture medium of edible fungus cooling after fermentation and sterilizing to what transport.
The heat transferring medium being filled with in the heat transferring medium being filled with in the interlayer of shell described above and spiral conveying tube is heat medium, its be applicable to transport just complete fermentation and sterilizing after fertilizer and the heating, drying of fermented feed.
Organic solid bulk cargo after sterilizing directly flows to the utility model by drawing mechanism, the utility model adopts cooling medium cooling in the pretreatment of culture medium of edible fungus, in the production of fertilizer and fermented feed, adopt heat medium heating, drying, it requires to reconcile temperature according to different materials, make culture medium of edible fungus can reach inoculation temperature, make fertilizer and fermented feed can dry granulation.In a word, the utility model carries out the temperature adjustment of organic solid bulk cargo and sterilizing in different device, and is used in conjunction with fermentation and bactericidal unit, complete continuously material heat exchange operation, avoid hot loss of energy, and saved the energy, and to organic solid bulk cargo automatic transport.Its production efficiency is high, and steady quality is reliable, has saved a large amount of artificial, floor space and transporting equipment, has eliminated environmental pollution.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model the first embodiment;
Fig. 2 is the structural representation of the utility model the second embodiment.
The specific embodiment
Below in conjunction with the drawings and specific embodiments, the utility model is further described.
Embodiment 1 as shown in Figure 1, the present embodiment horizontal positioned, it also can vertically be placed, also can 90 ° with interior inclination angle slant setting.Heat-exchanger rig comprises the shell 52 of spiral conveying tube 26 and spiral conveying tube 26 outer sandwichs.Shell 52 one end have charging aperture 53, and the other end has discharging opening 28.Charging aperture 53 is over against the discharging opening of the discharging gate of fermentation and sterilization device.In the interlayer of shell 52, be filled with heat transferring medium: cooling water, on the outer shell outer wall of charging aperture 28 one end, have heat transferring medium outlet A 24, on the outer shell outer wall away from charging aperture B 28 one end, have heat transferring medium import A 29.The interior hollow of spiral conveying tube 26, is filled with heat transferring medium in it: cooling water, it has heat transferring medium outlet B 23 in charging aperture 53 one end, away from charging aperture 53 one end, have heat transferring medium import B 30.Spiral conveying tube 26 two ends are fixed on base by bearing, and its one end is provided with motor 31.
Embodiment 2 as shown in Figure 2, the present embodiment is vertically placed, also can 90 ° with interior inclination angle slant setting.Its structure is with embodiment 1, and just the shell 52 of its spiral conveying tube 26 and spiral conveying tube 26 outer sandwichs is divided into two parts, and wherein a part makes material up, and another part makes material descending; Between two parts, by discharging opening 55, be connected with infundibulate charging aperture 56, there is the stirrer paddle 54 that is fixed on spiral conveying tube upper end at discharging opening 55 places, two-part spiral conveying tube 26 upper ends are all fixed with sprocket wheel 57 and 58, and described motor 31 is fixed therein a part of spiral conveying tube upper end.According to the stroke of material, make the up part heat transferring medium import A 29 of material and heat transferring medium import B 30 in upper end, make the descending part heat transferring medium import A 29 of material and heat transferring medium import B 30 in lower end; Make the up part heat transferring medium outlet A 23 of material and heat transferring medium outlet B 24 in lower end, make the descending part heat transferring medium outlet A 23 of material and heat transferring medium outlet B 24 in upper end.
Embodiment described above just completes culture medium of edible fungus cooling after fermentation and sterilizing to what transport; If change cooling medium into heat medium, it carries out heating, drying to the fertilizer and the fermented feed that just complete after fermentation and sterilizing that transport.
Claims (4)
1. a heat-exchanger rig for the organic solid bulk cargo after fermentation and sterilizing, is characterized in that: it is to place from the horizontal by 0 ° of-90 ° of angle, and it comprises the shell of spiral conveying tube and the outer sandwich of spiral conveying tube; Shell one end has charging aperture, and the other end has discharging opening; Charging aperture is over against the discharging opening of the discharging gate of fermentation and sterilization device; In the interlayer of shell, be filled with heat transferring medium, according to the stroke of material, on the outer shell outer wall of charging aperture one end, have heat transferring medium outlet A, on the outer shell outer wall away from charging aperture one end, have heat transferring medium import A; Hollow in spiral conveying tube, is filled with heat transferring medium in it, according to the stroke of material, it has heat transferring medium outlet B in charging aperture one end, away from charging aperture one end, have heat transferring medium import B; Spiral conveying tube two ends are fixed on base by bearing, and its one end is provided with motor.
2. the heat-exchanger rig of the organic solid bulk cargo after fermentation according to claim 1 and sterilizing, it is characterized in that: the shell of the outer sandwich of described spiral conveying tube and spiral conveying tube is divided into two parts, its part makes material up, and another part makes material descending; Between two parts, by discharging opening, be connected with infundibulate charging aperture, there is the stirrer paddle that is fixed on spiral conveying tube upper end at discharging opening place, and two-part spiral conveying tube upper end is all fixed with sprocket wheel, and described motor is fixed therein a part of spiral conveying tube upper end; According to the stroke of material, make the up part heat transferring medium import A of material and heat transferring medium import B in upper end, make the descending part heat transferring medium import A of material and heat transferring medium import B in lower end; Make the up part heat transferring medium outlet A of material and heat transferring medium outlet B in lower end, make the descending part heat transferring medium outlet A of material and heat transferring medium outlet B in upper end.
3. the heat-exchanger rig of the organic solid bulk cargo after fermentation according to claim 1 and 2 and sterilizing, is characterized in that: the heat transferring medium being filled with in the heat transferring medium being filled with in the interlayer of described shell and spiral conveying tube is cooling medium.
4. the heat-exchanger rig of the organic solid bulk cargo after fermentation according to claim 1 and 2 and sterilizing, is characterized in that: the heat transferring medium being filled with in the heat transferring medium being filled with in the interlayer of described shell and spiral conveying tube is heat medium.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420207173.6U CN203869556U (en) | 2014-04-27 | 2014-04-27 | Heat exchange device for fermented and sterilized organic matter solid bulk materials |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420207173.6U CN203869556U (en) | 2014-04-27 | 2014-04-27 | Heat exchange device for fermented and sterilized organic matter solid bulk materials |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203869556U true CN203869556U (en) | 2014-10-08 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420207173.6U Expired - Fee Related CN203869556U (en) | 2014-04-27 | 2014-04-27 | Heat exchange device for fermented and sterilized organic matter solid bulk materials |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106115211A (en) * | 2016-08-22 | 2016-11-16 | 江苏众胜灭菌设备科技有限公司 | Superheated vapor is to the cooling device for discharging in drug and food powder disinfection system |
| CN106187358A (en) * | 2015-05-05 | 2016-12-07 | 银七星控股有限公司 | A kind of Automatic Production System of biological organic fertilizer |
| CN107836284A (en) * | 2017-10-25 | 2018-03-27 | 翔天农业开发集团股份有限公司 | Bulk cargo cooling inoculation mixing bunker |
| CN108332600A (en) * | 2018-03-18 | 2018-07-27 | 唐山山岛石油化学有限公司 | The movable bracing means of sandwich-type heat exchange container shell |
| CN109373784A (en) * | 2018-12-12 | 2019-02-22 | 河北万博生物科技有限公司 | A kind of natural gas transformation device for producing avermectin |
| CN109539836A (en) * | 2018-11-21 | 2019-03-29 | 西安交通大学 | Vertical multi-stage flow solids bulk cargo heat exchanger |
| CN110926243A (en) * | 2019-11-28 | 2020-03-27 | 北京科技大学 | Particle blending-based indirect heat transfer strengthening method for high-temperature solid bulk materials |
-
2014
- 2014-04-27 CN CN201420207173.6U patent/CN203869556U/en not_active Expired - Fee Related
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106187358A (en) * | 2015-05-05 | 2016-12-07 | 银七星控股有限公司 | A kind of Automatic Production System of biological organic fertilizer |
| CN106115211A (en) * | 2016-08-22 | 2016-11-16 | 江苏众胜灭菌设备科技有限公司 | Superheated vapor is to the cooling device for discharging in drug and food powder disinfection system |
| CN107836284A (en) * | 2017-10-25 | 2018-03-27 | 翔天农业开发集团股份有限公司 | Bulk cargo cooling inoculation mixing bunker |
| CN108332600A (en) * | 2018-03-18 | 2018-07-27 | 唐山山岛石油化学有限公司 | The movable bracing means of sandwich-type heat exchange container shell |
| CN108332600B (en) * | 2018-03-18 | 2024-08-13 | 唐山亿效环保科技有限公司 | Movable reinforcing device for sandwich type heat exchange container shell |
| CN109539836A (en) * | 2018-11-21 | 2019-03-29 | 西安交通大学 | Vertical multi-stage flow solids bulk cargo heat exchanger |
| CN109373784A (en) * | 2018-12-12 | 2019-02-22 | 河北万博生物科技有限公司 | A kind of natural gas transformation device for producing avermectin |
| CN109373784B (en) * | 2018-12-12 | 2020-01-03 | 河北万博生物科技有限公司 | Natural gas reforming device for producing abamectin |
| CN110926243A (en) * | 2019-11-28 | 2020-03-27 | 北京科技大学 | Particle blending-based indirect heat transfer strengthening method for high-temperature solid bulk materials |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Yu Yue Inventor after: Huang Ruoyu Inventor after: Li Shiguang Inventor before: Huang Ruoyu |
|
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20180425 Address after: 101411 Beijing Huairou District Tanghekou town Xiaoliang Qian village committee 1000 meters southeast Patentee after: Beijing galactic Valley Ecological Agriculture Co., Ltd. Address before: 071000 Shuang Sheng street, Shuang Sheng District, Baoding, Hebei 23-4-102 Patentee before: Huang Ruoyu |
|
| 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: 20141008 Termination date: 20190427 |