CN102018187A - Energy-saving fruit and vegetable bulking machine and application method thereof - Google Patents
Energy-saving fruit and vegetable bulking machine and application method thereof Download PDFInfo
- Publication number
- CN102018187A CN102018187A CN2010105202444A CN201010520244A CN102018187A CN 102018187 A CN102018187 A CN 102018187A CN 2010105202444 A CN2010105202444 A CN 2010105202444A CN 201010520244 A CN201010520244 A CN 201010520244A CN 102018187 A CN102018187 A CN 102018187A
- Authority
- CN
- China
- Prior art keywords
- valve
- storage tank
- outlet valve
- tank
- chuck
- 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.)
- Granted
Links
Images
Abstract
The invention relates to a set of energy-saving fruit and vegetable bulking machine and an application method thereof, which realizes energy reuse in processes of heating and cooling of a bulking tank jacket by connecting with two energy storage devices, thereby greatly saving the energy sources, reducing the production cost, and ensuring the bulking quality of fruits and vegetables. The operating principal is characterized in that two temperature-difference storage tanks are preheated in the process of heating the jacket and directly heated via a heat source, and then can cool the jacket in advance in the process of cooling the jacket so as to absorb heat for later use in next heating. The invention has the advantages that the jacket is rapidly heated and cooled, the energy is fully utilized, and the heating energy sources are greatly saved.
Description
Technical field
The invention belongs to food processing field, be specifically related to a kind of utilization again that can realize the surplus cold energy of waste heat, thereby realize the fruit and vegetable dilated machine and the using method thereof of energy-saving effect.
Technical background
Puffed vegetable fruit crisp slice is a kind of new product that just grows up in recent years, and some fruits and vegetables that contain moisture is just edible through processed and after making its volumetric expansion cooling, and its mouthfeel is crisp, unique flavor.Also varied at fruit and vegetable dilated processing technology, comprise fried type and non-fried type.Though non-frying-expansion technology can access the quality better products, but the air-flow differential bulking process is more favored, yet Bulking tank is the nucleus equipment of whole puffing process, the high energy consumption of its puffing process and energy utilize insufficient being difficult to avoid, the overwhelming majority of shared tank body of its quality and material proportion accounts for the overwhelming majority that energy transmits to its heating and cooling of carrying out.Common heating is the direct heating and cooling to tank body, wherein with the huge waste of energy, just makes processing cost high.
Summary of the invention
The present invention utilizes the unfavorable waste that brings in order to solve to tank body heating and cooling energy, and then improve capacity usage ratio and reduce cost, the invention provides energy-saving fruit and vegetable dilated machine and using method thereof that a cover has energy storage system, make expanded tank body in the process of heating and cooling, energy is recycled, thereby reached the purpose that energy savings is saved cost.
For achieving the above object, bulking machine of the present invention comprises and has a left side, the Bulking tank of right end socket, described Bulking tank is tightly connected by butterfly valve and vacuum tank, vavuum pump is tightly connected by vacuum valve and vacuum tank on pipeline and the pipeline, be embedded with the material disc of the uniform coiled pipe of band thermal source inlet valve at Bulking tank, have compressed-air actuated inlet on the right end socket, Bulking tank is provided with the chuck of strap clamp cover heat transfer medium import and chuck heat transfer medium outlet outward, in warm storage tank, the high temperature storage tank, the outlet of thermal source and low-temperature receiver is respectively by middle temperature storage tank outlet valve, high temperature storage tank outlet valve, the thermal source outlet valve, low-temperature receiver outlet valve and JI valve are connected with the import of chuck heat transfer medium, and the chuck heat transfer medium outlet is through the JO valve, in warm storage tank inlet valve, high temperature storage tank inlet valve is connected with middle temperature storage tank and high temperature storage tank.
Described Bulking tank top is provided with thermometer, hygrometer and Pressure gauge;
Warm storage tank outlet valve, high temperature storage tank outlet valve, thermal source outlet valve, low-temperature receiver outlet valve and JI valve, JO valve, middle temperature storage tank inlet valve, high temperature storage tank inlet valve link to each other with controller respectively with the thermal source inlet valve in described;
The left and right sides end socket of described Bulking tank all is connected and sealed by sealing ring;
On the pipeline in described between warm storage tank outlet valve, high temperature storage tank outlet valve, thermal source outlet valve, low-temperature receiver outlet valve and the JI valve pump is installed also;
Described tank volume is 2～3 times of chuck volume;
Described vacuum tank volume is 3～5 times of Bulking tank volume.
The using method of bulking machine of the present invention is as follows: at first, opening left end socket will remove the material of Free water in advance and be placed on the material disc equably, close the butterfly valve of left end socket and right-hand member, the maximum temperature of bulking process is made as T, the outlet valve of warm storage tank and JI valve in opening, warm medium is pumped into the tank body chuck and is full of chuck in making, close pump and in warm storage tank outlet valve and JI valve, be incubated and treat that jacket temperature rises to 0.5T～0.75T; Open pump, high temperature storage tank outlet valve, middle temperature storage tank inlet valve and JI and outlet valve then, high-temperature medium is replaced the middle temperature medium later that conducted heat, high-temperature medium is full of chuck, close pump, high temperature storage tank outlet valve, middle temperature storage tank inlet valve and JI valve and outlet valve, insulation treats that jacket temperature rises to 0.8T～0.9T; Open pump then, the thermal source outlet valve, high temperature storage tank inlet valve and JI and outlet valve, heat medium is replaced the high-temperature medium later that conducted heat, heat medium is full of chuck, close high temperature storage tank inlet valve and JI valve and outlet valve, open the coiled pipe thermal source inlet valve that enters Bulking tank inside, material is heated, compressed air intake injects fresh compressed air in Bulking tank simultaneously, when the temperature T that reaches the bulking process regulation, open the butterfly valve of Bulking tank right-hand member rapidly, make Bulking tank broken rapidly empty, discharge moisture evaporated, close the thermal source outlet valve then; Open the outlet valve of high temperature storage tank and the outlet valve and the inlet valve of inlet valve and chuck, with pump the high-temperature medium in the high temperature storage tank is replaced high-temperature medium in the chuck, the high-temperature medium that is replaced out flows back to the high temperature storage tank, close the outlet valve of pump, high temperature storage tank and the outlet valve and the inlet valve of inlet valve and chuck, heat exchange treats that jacket temperature reduces to 0.9T～0.8T; Open the outlet valve of pump, middle temperature storage tank and the outlet valve and the inlet valve of inlet valve and chuck, with pump the middle temperature medium of middle temperature storage tank is replaced middle temperature medium in the chuck, warm storage tank during the middle temperature medium that is replaced out flows back to, close the outlet valve of pump, middle temperature storage tank and the outlet valve and the inlet valve of inlet valve and chuck, heat exchange treats that jacket temperature reduces to 0.75T～0.5T; Open the outlet valve and the inlet valve of pump, low-temperature receiver outlet valve and chuck, feed cooling medium, flowed back to low-temperature receiver, realize the circulation cooling by the cooling medium of heat exchange; In whole Bulking tank cooling procedure, the power of adjusting vavuum pump makes the Bulking tank internal pressure remain unchanged, and when humidity reaches setting value, closes vavuum pump and butterfly valve, opens left end socket, takes out dilated product.
In addition recycling of the heat that the present invention can be produced Bulking tank cooling is saved energy greatly, thereby is reduced production costs.
Description of drawings:
Fig. 1 is an overall structure schematic diagram of the present invention.
Among the figure 1---chuck, 2---thermometer, 3---hygrometer, 4---Pressure gauge, 5---right end socket, 6---butterfly valve, 7---vacuum tank, 8---vacuum valve, 9---vavuum pump, 10---Bulking tank, 11---the JO valve, 12---controller, 13---middle temperature storage tank inlet valve, 14---high temperature storage tank inlet valve, 15---high temperature storage tank outlet valve, 16---middle temperature storage tank outlet valve, 17---the low-temperature receiver outlet valve, 18---the thermal source outlet valve, 19---the JI valve, 20---middle temperature storage tank, 21---the high temperature storage tank, 22---left end socket, 23,24---seal washer, 25---the compressed air inlet, 26---hook, 27---pump, 28---coiled pipe thermal source inlet valve, 29,30---the import of chuck heat transfer medium, the chuck heat transfer medium outlet.
The specific embodiment
Below in conjunction with accompanying drawing the present invention is described in further detail.
Referring to Fig. 1, the present invention includes and have a left side, right end socket 22,5 Bulking tank 10, the left and right sides end socket 22 of Bulking tank 10,5 all by sealing ring 23,24 are connected and sealed, Bulking tank 10 tops are provided with thermometer 2, hygrometer 3 and Pressure gauge 4, described Bulking tank 10 is tightly connected by butterfly valve 6 and vacuum tank 7, vacuum tank 7 volumes are 3～5 times of Bulking tank 10 volumes, vavuum pump 9 is tightly connected by vacuum valve on pipeline and the pipeline 8 and vacuum tank 7, be embedded with the material disc of the uniform coiled pipe of band thermal source inlet valve 28 at Bulking tank 10, have compressed-air actuated inlet 25 on the right end socket 5, Bulking tank 10 outer strap clamp cover heat transfer medium import and the chuck heat transfer medium outlets 29 of being provided with, 30 chuck 1, in warm storage tank 20, high temperature storage tank 21, the outlet of thermal source and low-temperature receiver is respectively by middle temperature storage tank outlet valve 16, high temperature storage tank outlet valve 15, thermal source outlet valve 18, low-temperature receiver outlet valve 17 and JI valve 19 are connected with chuck heat transfer medium import 29, tank volume is 2～3 times of chuck volume, chuck heat transfer medium outlet 30 is through JO valve 11, in warm storage tank inlet valve 13, high temperature storage tank inlet valve 14 is connected with middle temperature storage tank 20 and high temperature storage tank 21, warm storage tank outlet valve 16 in described, high temperature storage tank outlet valve 15, thermal source outlet valve 18, low-temperature receiver outlet valve 17 and JI valve 19, JO valve 11, in warm storage tank inlet valve 13, high temperature storage tank inlet valve 14 links to each other with controller 12 respectively with thermal source inlet valve 28, described in warm storage tank outlet valve 16, high temperature storage tank outlet valve 15, thermal source outlet valve 18, on the pipeline between low-temperature receiver outlet valve 17 and the JI valve 19 pump 27 is installed also.
Process of the present invention is as follows: at first, opening left end socket 22 will remove the material of Free water in advance and be placed on the material disc equably, close the butterfly valve 6 of left end socket 22 and right-hand member, the maximum temperature of bulking process is made as T, the outlet valve 16 of warm storage tank and JI valve 19 in opening, warm medium is delivered to tank body chuck 1 and is full of chuck 1 by pump 27 in making, close pump 27 and in warm storage tank outlet valve 16 and JI valve 19, insulation treats that jacket temperature rises to 0.5T～0.75T; Open pump 27, high temperature storage tank outlet valve 15, middle temperature storage tank inlet valve 13 and JI 19 and outlet valve 11 then, high-temperature medium is replaced the middle temperature medium later that conducted heat, high-temperature medium is full of chuck 1, close pump 27, high temperature storage tank outlet valve 15, middle temperature storage tank inlet valve 13 and JI valve 19 and outlet valve 11, insulation treats that jacket temperature rises to 0.8T～0.9T; Open pump 27 then, thermal source outlet valve 18, high temperature storage tank inlet valve 14 and JI 19 and outlet valve 11, heat medium is replaced the high-temperature medium later that conducted heat, heat medium is full of chuck 1, close high temperature storage tank inlet valve 14 and JI valve 19 and outlet valve 11, open the coiled pipe thermal source inlet valve 28 that enters Bulking tank inside, material is heated, compressed air intake 25 injects fresh compressed air in Bulking tank simultaneously, when the temperature T that reaches the bulking process regulation, open the butterfly valve 6 of Bulking tank right-hand member rapidly, make Bulking tank 10 broken rapidly empty, discharge moisture evaporated, close thermal source outlet valve 18 then; Open the outlet valve 15 of high temperature storage tank and the outlet valve 11 and the inlet valve 19 of inlet valve 14 and chuck, with pump 27 high-temperature medium in the high temperature storage tank 21 is replaced high-temperature medium in the chuck 1, the high-temperature medium that is replaced out flows back to high temperature storage tank 21, close the outlet valve 15 of pump 27, high temperature storage tank and the outlet valve 11 and the inlet valve 19 of inlet valve 14 and chuck, heat exchange treats that jacket temperature reduces to 0.9T～0.8T; Open the outlet valve 16 of pump 27, middle temperature storage tank and the outlet valve 11 and the inlet valve 19 of inlet valve 13 and chuck, with pump 27 the middle temperature medium of middle temperature storage tank 20 is replaced middle temperature medium in the chuck 1, warm storage tank 20 during the middle temperature medium that is replaced out flows back to, close the outlet valve 16 of pump 27, middle temperature storage tank and the outlet valve 11 and the inlet valve 19 of inlet valve 13 and chuck, heat exchange treats that jacket temperature reduces to 0.75T～0.5T; Open the outlet valve 11 and the inlet valve 19 of pump 27, low-temperature receiver outlet valve 17 and chuck, feed cooling medium, flowed back to low-temperature receiver, realize the circulation cooling by the cooling medium of heat exchange; In whole Bulking tank 10 cooling procedures, the power of adjusting vavuum pump 9 makes Bulking tank 10 internal pressures remain unchanged, and when humidity reaches setting value, closes vavuum pump 9 and butterfly valve 6, opens left end socket 22, takes out dilated product.
Claims (8)
1. energy-saving fruit and vegetable dilated machine, comprise and have a left side, right end socket (22,5) Bulking tank (10), it is characterized in that: described Bulking tank (10) is tightly connected by butterfly valve (6) and vacuum tank (7), vavuum pump (9) is tightly connected by vacuum valve (8) on pipeline and the pipeline and vacuum tank (7), be embedded with the material disc of the uniform coiled pipe of band thermal source inlet valve (28) at Bulking tank (10), have compressed-air actuated inlet (25) on the right end socket (5), outer strap clamp cover heat transfer medium import and the chuck heat transfer medium outlet (29 of being provided with of Bulking tank (10), 30) chuck (1), in warm storage tank (20), high temperature storage tank (21), the outlet of thermal source and low-temperature receiver is respectively by middle temperature storage tank outlet valve (16), high temperature storage tank outlet valve (15), thermal source outlet valve (18), low-temperature receiver outlet valve (17) and JI valve (19) are connected with chuck heat transfer medium import (29), and chuck heat transfer medium outlet (30) is through JO valve (11), in warm storage tank inlet valve (13), high temperature storage tank inlet valve (14) is connected with middle temperature storage tank (20) and high temperature storage tank (21).
2. energy-saving fruit and vegetable dilated machine according to claim 1 comprises, it is characterized in that: described Bulking tank (10) top is provided with thermometer (2), hygrometer (3) and Pressure gauge (4).
3. energy-saving fruit and vegetable dilated machine according to claim 1 comprises, it is characterized in that: warm storage tank outlet valve (16), high temperature storage tank outlet valve (15), thermal source outlet valve (18), low-temperature receiver outlet valve (17) and JI valve (19), JO valve (11), middle temperature storage tank inlet valve (13), high temperature storage tank inlet valve (14) and thermal source inlet valve (28) link to each other with controller (12) respectively in described.
4. energy-saving fruit and vegetable dilated machine according to claim 1 comprises, it is characterized in that: the left and right sides end socket (22,5) of described Bulking tank (10) all is connected and sealed by sealing ring (23,24).
5. energy-saving fruit and vegetable dilated machine according to claim 1 comprises, it is characterized in that: on the pipeline in described between warm storage tank outlet valve (16), high temperature storage tank outlet valve (15), thermal source outlet valve (18), low-temperature receiver outlet valve (17) and the JI valve (19) pump (27) is installed also.
6. energy-saving fruit and vegetable dilated machine according to claim 1 comprises, it is characterized in that: described tank volume is 2～3 times of chuck volume.
7. energy-saving fruit and vegetable dilated machine according to claim 1 comprises, it is characterized in that: described vacuum tank (7) volume is 3～5 times of Bulking tank (10) volume.
8. the using method of an energy-saving fruit and vegetable dilated machine as claimed in claim 1 is characterized in that:
At first, opening left end socket (22) will remove the material of Free water in advance and be placed on the material disc equably, close the butterfly valve (6) of left end socket (22) and right-hand member, the maximum temperature of bulking process is made as T, outlet valve of warm storage tank (16) and JI valve (19) in opening, warm medium is delivered to tank body chuck (1) and is full of chuck (1) by pump (27) in making, close pump (27) and in warm storage tank outlet valve (16) and JI valve (19), insulation treats that jacket temperature rises to 0.5T～0.75T; Open pump (27), high temperature storage tank outlet valve (15), middle temperature storage tank inlet valve (13) and JI (19) and outlet valve (11) then, high-temperature medium is replaced the middle temperature medium later that conducted heat, high-temperature medium is full of chuck (1), close pump (27), high temperature storage tank outlet valve (15), middle temperature storage tank inlet valve (13) and JI valve (19) and outlet valve (11), insulation treats that jacket temperature rises to 0.8T～0.9T; Open pump (27) then, thermal source outlet valve (18), high temperature storage tank inlet valve (14) and JI (19) and outlet valve (11), heat medium is replaced the high-temperature medium later that conducted heat, heat medium is full of chuck (1), close high temperature storage tank inlet valve (14) and JI valve (19) and outlet valve (11), open the coiled pipe thermal source inlet valve (28) that enters Bulking tank inside, material is heated, compressed air intake (25) injects fresh compressed air in Bulking tank simultaneously, when the temperature T that reaches the bulking process regulation, open the butterfly valve (6) of Bulking tank right-hand member rapidly, make Bulking tank (10) broken rapidly empty, discharge moisture evaporated, close thermal source outlet valve (18) then; Open the outlet valve (15) of high temperature storage tank and the outlet valve (11) and the inlet valve (19) of inlet valve (14) and chuck, with pump (27) high-temperature medium in the high temperature storage tank (21) is replaced the interior high-temperature medium of chuck (1), the high-temperature medium that is replaced out flows back to high temperature storage tank (21), close the outlet valve (15) of pump (27), high temperature storage tank and the outlet valve (11) and the inlet valve (19) of inlet valve (14) and chuck, heat exchange treats that jacket temperature reduces to 0.9T～0.8T; Open the outlet valve (16) of pump (27), middle temperature storage tank and the outlet valve (11) and the inlet valve (19) of inlet valve (13) and chuck, with pump (27) the middle temperature medium of middle temperature storage tank (20) is replaced the interior middle temperature medium of chuck (1), warm storage tank (20) during the middle temperature medium that is replaced out flows back to, close the outlet valve (16) of pump (27), middle temperature storage tank and the outlet valve (11) and the inlet valve (19) of inlet valve (13) and chuck, heat exchange treats that jacket temperature reduces to 0.75T～0.5T; Open the outlet valve (11) and the inlet valve (19) of pump (27), low-temperature receiver outlet valve (17) and chuck, feed cooling medium, flowed back to low-temperature receiver, realize the circulation cooling by the cooling medium of heat exchange; In whole Bulking tank (10) cooling procedure, the power of adjusting vavuum pump (9) makes Bulking tank (10) internal pressure remain unchanged, and when humidity reaches setting value, closes vavuum pump (9) and butterfly valve (6), opens left end socket (22), takes out dilated product.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010105202444A CN102018187B (en) | 2010-10-26 | 2010-10-26 | Energy-saving fruit and vegetable bulking machine and application method thereof |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010105202444A CN102018187B (en) | 2010-10-26 | 2010-10-26 | Energy-saving fruit and vegetable bulking machine and application method thereof |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN102018187A true CN102018187A (en) | 2011-04-20 |
| CN102018187B CN102018187B (en) | 2012-11-07 |
Family
ID=43860287
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2010105202444A Expired - Fee Related CN102018187B (en) | 2010-10-26 | 2010-10-26 | Energy-saving fruit and vegetable bulking machine and application method thereof |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN102018187B (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102771733A (en) * | 2012-08-20 | 2012-11-14 | 江苏徐淮地区徐州农业科学研究所 | Vacuum bulking machine for fruits and vegetables |
| CN103141780A (en) * | 2013-03-04 | 2013-06-12 | 陕西科技大学 | Fruit and vegetable airflow puffing equipment of material basket rotating type |
| CN105543983A (en) * | 2016-02-19 | 2016-05-04 | 于锋 | Process and device for preparing modified leather fiber through high-pressure puffing |
| CN105852183A (en) * | 2016-04-20 | 2016-08-17 | 陕西科技大学 | High-permeability fruit and vegetable explosion-puffing device and high-permeability fruit and vegetable explosion-puffing method |
| CN112352990A (en) * | 2020-10-28 | 2021-02-12 | 同福集团股份有限公司 | Fruit vegetables material processing is with popped jar with energy-conserving effect |
| CN113905620A (en) * | 2019-06-18 | 2022-01-07 | 雀巢产品有限公司 | Baking device |
| CN115399494A (en) * | 2022-10-10 | 2022-11-29 | 扬州福尔喜果蔬汁机械有限公司 | Energy-saving high-pressure low-temperature heating puffing system and working method |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20090169694A1 (en) * | 2006-09-15 | 2009-07-02 | Chocotech Gmbh | Method and Apparatus for Producing Fruit Leather from a Fruit Mass |
| CN101480245A (en) * | 2009-01-05 | 2009-07-15 | 陕西科技大学 | Equipment for puffing garden stuff with air current and microwave |
-
2010
- 2010-10-26 CN CN2010105202444A patent/CN102018187B/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US20090169694A1 (en) * | 2006-09-15 | 2009-07-02 | Chocotech Gmbh | Method and Apparatus for Producing Fruit Leather from a Fruit Mass |
| CN101480245A (en) * | 2009-01-05 | 2009-07-15 | 陕西科技大学 | Equipment for puffing garden stuff with air current and microwave |
Non-Patent Citations (1)
| Title |
|---|
| 《食品与机械》 20091231 毕金峰等 胡萝卜变温压差膨化干燥影响因素研究 第14-17页 1-8 第25卷, 第5期 * |
Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102771733A (en) * | 2012-08-20 | 2012-11-14 | 江苏徐淮地区徐州农业科学研究所 | Vacuum bulking machine for fruits and vegetables |
| CN103141780A (en) * | 2013-03-04 | 2013-06-12 | 陕西科技大学 | Fruit and vegetable airflow puffing equipment of material basket rotating type |
| CN103141780B (en) * | 2013-03-04 | 2014-10-29 | 陕西科技大学 | Fruit and vegetable airflow puffing equipment of material basket rotating type |
| CN105543983A (en) * | 2016-02-19 | 2016-05-04 | 于锋 | Process and device for preparing modified leather fiber through high-pressure puffing |
| CN105852183A (en) * | 2016-04-20 | 2016-08-17 | 陕西科技大学 | High-permeability fruit and vegetable explosion-puffing device and high-permeability fruit and vegetable explosion-puffing method |
| CN105852183B (en) * | 2016-04-20 | 2018-05-08 | 陕西科技大学 | Fruits and vegetables Thief zone airflow puffing device and method |
| CN113905620A (en) * | 2019-06-18 | 2022-01-07 | 雀巢产品有限公司 | Baking device |
| CN113905620B (en) * | 2019-06-18 | 2023-10-03 | 雀巢产品有限公司 | Baking equipment |
| CN112352990A (en) * | 2020-10-28 | 2021-02-12 | 同福集团股份有限公司 | Fruit vegetables material processing is with popped jar with energy-conserving effect |
| CN115399494A (en) * | 2022-10-10 | 2022-11-29 | 扬州福尔喜果蔬汁机械有限公司 | Energy-saving high-pressure low-temperature heating puffing system and working method |
Also Published As
| Publication number | Publication date |
|---|---|
| CN102018187B (en) | 2012-11-07 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102018187B (en) | Energy-saving fruit and vegetable bulking machine and application method thereof | |
| CN202842241U (en) | Fresh-keeping and unfreezing storehouse for frozen meat | |
| CN101480245B (en) | Equipment for puffing garden stuff with air current and microwave | |
| CN107647446B (en) | Two-stage heat pump recovery device and method for waste steam and waste heat in low-pressure superheated steam drying of fruits and vegetables | |
| CN201457985U (en) | Energy-saving insulation can | |
| CN201888204U (en) | Device for generating hot air in baking and drying grain in storage | |
| CN206260679U (en) | A kind of meat product defrosting drying unit | |
| CN203516008U (en) | Dual-recovery system for oil and gas heat | |
| CN106376302A (en) | Fruit and vegetable subatmospheric pressure storage apparatus | |
| CN107525176A (en) | A kind of central air-conditioning energy-saving system | |
| CN208012138U (en) | A kind of integrated energy supply heat pump refrigerating system of production and living | |
| CN103053991A (en) | Energy-saving cooling method and energy-saving cooling device of compressed air for aerobic microbial fermentation system | |
| CN207294627U (en) | The system that Coastal Power Station warm water discharge recycles | |
| CN212457677U (en) | Steam circulation drying system of solar energy coupling heat pump | |
| CN212476742U (en) | Anaerobic fermentation system utilizing air energy | |
| CN207179883U (en) | A kind of central air-conditioning energy-saving system | |
| CN203015792U (en) | Improved immersion type instant freezer | |
| CN206192174U (en) | Change energy -conserving air heat exchanger of frost | |
| CN201534837U (en) | Energy-saving type air pre-processing device | |
| CN209840479U (en) | Enzyme production is with high-efficient cooling water set | |
| CN205208932U (en) | Reation kettle is with cold and hot heat conduction oil circulation device | |
| CN205929411U (en) | Plastics product cooling basin | |
| CN203120911U (en) | Device for energy saving and temperature reducing of compressed air of aerobic microorganism fermenting system in production of monosodium glutamate | |
| CN205337544U (en) | Quenching and tempering and cooling device of rice bran extrusion machine | |
| CN205351946U (en) | Mountain certain herbaceous plants with big flowers automatic drier |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| 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: 20121107 Termination date: 20151026 |
|
| EXPY | Termination of patent right or utility model |