CN204560874U - A kind of many applicabilities cook vat drawing mechanism - Google Patents
A kind of many applicabilities cook vat drawing mechanism Download PDFInfo
- Publication number
- CN204560874U CN204560874U CN201520259278.0U CN201520259278U CN204560874U CN 204560874 U CN204560874 U CN 204560874U CN 201520259278 U CN201520259278 U CN 201520259278U CN 204560874 U CN204560874 U CN 204560874U
- Authority
- CN
- China
- Prior art keywords
- cell body
- pipe
- frid
- heating
- feed pipe
- 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
Links
Landscapes
- Commercial Cooking Devices (AREA)
Abstract
The utility model relates to a kind of many applicabilities cook vat drawing mechanism, and it comprises for the cell body of boiling, the heat insulation cover plate covered on cell body opening, is arranged on more than one commissioning pipe on cell body opening, is longitudinally arranged on pusher roller, the drive unit driving pusher roller to rotate in cell body, is vertically arranged on the pay-off on cell body discharge end bottom discharge mouth, the boiling interlayer being arranged on cell body outer wall and the steam air supply pipe be communicated with boiling interlayer; Open heating tank can not block; Especially when cleaning, opening heat insulation cover plate directly cleans without dead angle noresidue, can not breed bacteria, next group product can not be polluted, cleaning speed is fast, and the heating state that staff can observe pulp at any time adjusts the precision of heating in time, it is convenient and swift after replacing processes raw material, without commissioning device, commissioning pipe more easily cleans without dead angle, the effective equipment debugging scavenging period reducing production interchange and bring.
Description
Technical field
The utility model relates to field of deep processing of farm products, particularly relates to a kind of many applicabilities cook vat drawing mechanism.
Background technology
Due to agricultural product to produce seasonality very strong, not easily store, but the raw material of industrial production can not stop production with seasonal variations, therefore in order to the deep processing of the middle product of satisfied industry needs fresh fruit product and agricultural product is just arisen at the historic moment.Found the factory with regard to the place of production and not only ensure that the fresh of the source of goods but also save cost of transportation.
In deep processing of farm products, inspissated juice is a pith, produce fresh fruit inspissated juice time successively through product screening-cleaning-pulverizing-boiling-concentrate etc. technique, wherein should ensure that the temperature of boiling ensures digestion time again when pulp boiling, once digesting apparatus occurs that the whole production line of blocking will face the danger of stopping production, existing digesting apparatus is bushing type equipment, first be easy blocking, and not easily dredge after blocking, pulp interior pipe advance once block be difficult to cleaning, next is cleaning equipment difficulty, owing to being enclosed environment, must clear up when carrying out production interchange or overhaul of the equipments, airtight long tube chamber is adding that feeding shaft is difficult to cleaning thoroughly more.
Because the heat time of the different pulps processed raw material is also all different with heating-up temperature, the conversion of different material processing request can not be completed efficiently, the boiling that a pulp changed by raw material needs debugging, and in debugging, the quality of pulp can be affected, and changes product facility debug time long.
When making the product of seed tiny closely knit (as: hawthorn, jujube etc.), seed nuclei can form deposition, and a large amount of seed nucleis can be piled up and block up, and a large amount of seed nucleis can cause blocking up of the conveyance conduit of equipment, and especially hawthorn seed nuclei content is large, very easily blocking pipeline.
Utility model content
The purpose of this utility model is to provide a kind of many applicabilities cook vat drawing mechanism, solves the problem that existing equipment easily blocks, difficulty is dredged, difficulty is cleaned.
For solving the problem, technical solution adopted in the utility model is:
A kind of many applicabilities cook vat drawing mechanism, it comprises for the cell body of boiling, the heat insulation cover plate covered on cell body opening, is arranged on more than one commissioning pipe on cell body opening, is longitudinally arranged on pusher roller, the drive unit driving pusher roller to rotate in cell body, is vertically arranged on the pay-off on cell body discharge end bottom discharge mouth, the boiling interlayer being arranged on cell body outer wall and the steam air supply pipe be communicated with boiling interlayer; Described cell body comprises frid that cross section is U-shaped and is arranged on two end plates of cell body two ends for shutoff cell body; Described pusher roller comprises rotating shaft and extends the spiral flitch of material direction Spiral distribution; The reductor that described drive unit comprises drive motors and is connected with drive motors; Described pusher roller is arranged on end plate, described spiral flitch and frid inwall matched in clearance, one end of described pusher roller is fixedly installed driving wheel outside end plate, described driving wheel is connected with the output shaft of reductor by belt, first pay-off and the second pay-off, described first pay-off comprises the vertical material-falling hopper pipe be connected with cell body diapire discharging opening and the feed pipe be communicated with material-falling hopper pipe, described feed pipe is provided with Pulp pump, described feed pipe is provided with valve, and described valve is between material-falling hopper pipe and Pulp pump; Described second pay-off comprise be connected with cell body sidewall discharging opening be inclined cross feed pipe, the described feed pipe other end that is inclined cross is communicated with the feed pipe between valve and Pulp pump, the described feed pipe that is inclined cross is provided with stop valve, described rotating shaft is provided with more than one plate, and described plate is corresponding with cell body sidewall discharging opening; Described boiling interlayer is the heating region be made up of the heating frid and sealing plate that are arranged on frid outer wall, the cross section of described heating frid is U-shaped, its side is welded with heating frid extension, opposite side welds with frid outer wall, described steam air supply pipe is fixedly connected with heating frid, and described steam air supply pipe is communicated with boiling interlayer through heating frid;
Furtherly, be provided with condensate water collecting pipe bottom described heating frid, described heating frid is also provided with heat-insulation layer outward, and side and the cell body side of described heat insulation cover plate are hinged, and described heat insulation cover plate is multiple being arranged side by side; Open Side Down for described commissioning pipe, and described more than one commissioning pipe is arranged in parallel.
Furtherly, also comprise header tank, described condensate water collecting pipe is communicated with header tank, is provided with fluid level control device in described header tank, and the outlet pipe of described header tank is provided with back water pump.
Furtherly, described feed pipe is level two, and two described feed pipe conveying trends are contrary.
Furtherly, described second pay-off is two and is symmetricly set on cell body both sides, described in be inclined cross feed pipe and be communicated with the feed pipe of respective side respectively.
The beneficial effect adopting technique scheme to produce is: open heating tank can not block; Add the environment forming relative closure in insulation cover board slot body, pulp heating can not be affected; Can not affect pulp heating also have major reason be exactly spiral flitch when promoting pulp, pulp can continue to roll and just can contact with frid uniformly and do not had drawback by the heating of heating therefore pulp like this in cell body; Especially clean time, open heat insulation cover plate and directly clean without dead angle noresidue, can not breed bacteria, next group product can not be polluted, cleaning speed is fast; And the heating state that staff can observe pulp at any time adjusts the precision of heating in time, the situation of underheat and over-heating is avoided to ensure product quality further, and open heating environment avoids the production of bubble in pulp, the existence of bubble can cause the heating of pulp uneven; Multiple heat insulation cover plate be arranged side by side can open and close as required, and convenient operation is easy to use; Multiple commissioning pipe is set on cell body, can according to the heat time of raw material pulp put near or away from the position of discharging opening, the heating-up temperature of such digesting apparatus need not be changed, from increasing or reduce increase or the minimizing that the stroke of pulp in cell body controls the heat time, convenient and swift, without commissioning device, commissioning pipe is selected a use at every turn and is avoided pulp contaminated, and the few valveless of the structure connecting pulp pipeline like this, more easily clean without dead angle, the effective equipment debugging scavenging period reducing production interchange and bring.
Being inclined cross feed pipe at cell body sidewall can avoid the seed nuclei piled up to pour in conveyance conduit, because therefore the position height of discharging opening arranges plate, plate rotates with rotating shaft, and such seed nuclei and pulp can progress into and be inclined cross feed pipe and be delivered to next procedure by Pulp pump again; First pay-off and the second pay-off control opening and closing respectively by valve and stop valve, and the first pay-off and the second pay-off can use simultaneously also can be used alone.
Owing in boiling interlayer being the steam of HTHP, therefore condensate water collecting pipe will be avoided to go out pressure release, therefore the header tank of a voltage stabilizing is set, when water level arrives the upper limit, condensate water is delivered to steam generator by back water pump work, water level is got back to minimum spacing back water pump and is quit work, and so just can ensure the pressure stability in boiling interlayer, thus guarantees the stable of the heating-up temperature of pulp.
Two reverse feeding engines can be more smooth and easy by siphoning away such material-falling hopper pipe flowing bottom material-falling hopper pipe by pasty material, avoids eddy current dead angle, avoid blocking, improve the reliability of equipment.
Two symmetries are inclined cross feed pipe 94 in the middle part of cell body, the seed nuclei of deposition can be transferred out successively, avoid crowded and block transfer pipeline under the cooperation of plate 24.
Accompanying drawing explanation
Fig. 1 is the utility model cross-sectional view.
Fig. 2 is the utility model side structure schematic diagram.
Fig. 3 is the utility model feeder structure schematic diagram.
In the accompanying drawings: 1 cell body, 11 frids, 12 end plates, 2 pusher rollers, 21 rotating shafts, 22 spiral flitch, 23 driving wheels, 24 plates, 3 boiling interlayers, 31 heating frids, 32 sealing plates, 33 condensate water collecting pipes, 34 heat-insulation layers, 4 steam air supply pipes, 5 heat insulation cover plates, 6 header tanks, 61 outlet pipes, 7 drive motors, 71 reductors, 8 commissioning pipes, 9 material-falling hopper pipes, 91 feed pipes, 92 Pulp pump, 93 valves, 94 are inclined cross feed pipe, 95 stop valves.
Detailed description of the invention
In order to make the purpose of this utility model, technical scheme and advantage clearly understand, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein only in order to explain the utility model, and be not used in restriction the utility model.
Fig. 1,2,3 shows a kind of many applicabilities cook vat of the utility model drawing mechanism, and it comprises boiling cell body 1, the heat insulation cover plate 5 covered on cell body 1 opening, be arranged on more than one commissioning pipe 8 on cell body 1 opening, be longitudinally arranged on pusher roller 2, the drive unit driving pusher roller 2 to rotate in cell body 1, be vertically arranged on the pay-off on cell body 1 discharge end bottom discharge mouth, the boiling interlayer 3 being arranged on cell body 1 outer wall and the steam air supply pipe 4 be communicated with boiling interlayer, described cell body 1 comprises frid 11 that cross section is U-shaped and is arranged on two end plates 12 of cell body 1 two ends for shutoff cell body 1, described pusher roller 2 comprises rotating shaft 21 and extends the spiral flitch 22 of material direction Spiral distribution, the reductor 71 that described drive unit comprises drive motors 7 and is connected with drive motors 7, described pusher roller 2 is arranged on end plate 12, described spiral flitch 22 and frid 11 inwall matched in clearance, one end of described pusher roller 2 is fixedly installed driving wheel 23 outside end plate 12, described driving wheel 23 is connected by the output shaft of belt with reductor 71, first pay-off and the second pay-off, described first pay-off comprises the vertical material-falling hopper pipe 9 be connected with cell body 1 diapire discharging opening and the feed pipe 91 be communicated with material-falling hopper pipe 9, described feed pipe 91 is provided with Pulp pump 92, described feed pipe 91 is provided with valve 93, described valve 93 is between material-falling hopper pipe 9 and Pulp pump 92, described second pay-off comprise be connected with cell body 1 sidewall discharging opening be inclined cross feed pipe 94, described feed pipe 94 other end that is inclined cross is communicated with the feed pipe 91 between valve 93 and Pulp pump 92, the described feed pipe 94 that is inclined cross is provided with stop valve 95, described rotating shaft 21 is provided with more than one plate 24, and described plate 24 is corresponding with cell body 1 sidewall discharging opening, described boiling interlayer 3 is the heating regions be made up of the heating frid 31 and sealing plate 32 that are arranged on frid 11 outer wall, the cross section of described heating frid 31 is U-shaped, described sealing plate 32 is annulars, its side is welded with heating frid 31 extension, opposite side welds with frid 11 outer wall, described steam air supply pipe 4 is fixedly connected with heating frid 31, and described steam air supply pipe 4 is communicated with boiling interlayer 3 through heating frid 31, , the discharging opening of cell body 1 sidewall is arranged in pulp.Condensate water must be had in steam-heated die cavity to arrange mouth outward.
Open heating tank can not block; Add the environment forming relative closure in insulation cover board slot body, pulp heating can not be affected; Can not affect pulp heating also have major reason be exactly spiral flitch when promoting pulp, pulp can continue to roll and just can contact with frid uniformly and do not had drawback by the heating of heating therefore pulp like this in cell body; Especially clean time, open heat insulation cover plate and directly clean without dead angle noresidue, can not breed bacteria, next group product can not be polluted, cleaning speed is fast; Being inclined cross feed pipe at cell body sidewall can avoid the seed nuclei piled up to pour in conveyance conduit, because therefore the position height of discharging opening arranges plate, plate rotates with rotating shaft, and such seed nuclei and pulp can progress into and be inclined cross feed pipe and be delivered to next procedure by Pulp pump again; First pay-off and the second pay-off control opening and closing respectively by valve and stop valve, and the first pay-off and the second pay-off can use simultaneously also can be used alone.
Be provided with condensate water collecting pipe 33 bottom heating frid 31, described heating frid 31 is outer is also provided with heat-insulation layer 34, and side and cell body 1 side of described heat insulation cover plate 5 are hinged, and described heat insulation cover plate 5 is multiple being arranged side by side; Open Side Down for described commissioning pipe 8, and described more than one commissioning pipe 8 is arranged in parallel, and more than one commissioning pipe 8 selects a use when deployed.
And the heating state that staff can observe pulp at any time adjusts the precision of heating in time, the situation of underheat and over-heating is avoided to ensure product quality further, and open heating environment avoids the production of bubble in pulp, the existence of bubble can cause the heating of pulp uneven.Side and cell body 1 side of heat insulation cover plate 5 are hinged, and described heat insulation cover plate 5 is multiple being arranged side by side.Multiple heat insulation cover plate be arranged side by side can open and close as required, and convenient operation is easy to use.
Multiple heat insulation cover plate 5 be arranged side by side can open and close as required, and convenient operation is easy to use; Multiple commissioning pipe 8 is set on cell body 1, can according to the heat time of raw material pulp put near or away from the position of discharging opening, the heating-up temperature of such digesting apparatus need not be changed, from increasing or reduce increase or the minimizing that the stroke of pulp in cell body controls the heat time, convenient and swift, without commissioning device, commissioning pipe is selected a use at every turn and is avoided pulp contaminated, and the few valveless of the structure connecting pulp pipeline like this, more easily clean without dead angle, the effective equipment debugging scavenging period reducing production interchange and bring.
After setting up header tank 6, described condensate water collecting pipe 33 is communicated with header tank 6, is provided with fluid level control device in described header tank 6, and the outlet pipe 61 of described header tank 6 is provided with back water pump.Owing in boiling interlayer being the steam of HTHP, therefore condensate water collecting pipe will be avoided to go out pressure release, therefore the header tank of a voltage stabilizing is set, when water level arrives the upper limit, condensate water is delivered to steam generator by back water pump work, water level is got back to minimum spacing back water pump and is quit work, and so just can ensure the pressure stability in boiling interlayer, thus guarantees the stable of the heating-up temperature of pulp.
Described feed pipe 91 is level two, two described feed pipe 91 conveyings trends are contrary, and two reverse feeding engines can be more smooth and easy by siphoning away such material-falling hopper pipe flowing bottom material-falling hopper pipe by pasty material, avoids eddy current dead angle, avoid blocking, improve the reliability of equipment.
Described second pay-off is two and is symmetricly set on cell body 1 both sides, described in be inclined cross feed pipe 94 and be communicated with respectively at the feed pipe 91 of respective side.Two symmetries are inclined cross feed pipe 94 in the middle part of cell body, the seed nuclei of deposition can be transferred out successively, avoid crowded and block transfer pipeline under the cooperation of plate 24.
During use, first in boiling interlayer 3, high-temperature steam is supplied by steam air supply pipe 4, the heat of steam can pass by the airtight air cavity of heating that frid 11, heating frid 31 and sealing plate 32 are formed, and heating frid 31 outer wall is provided with heat-insulation layer 34, and a heat is concentrated and diffused to frid 11; After starting drive motors 7, reductor 71 is by belt drives driving wheel 23, thus rotating shaft 21 drives spiral flitch 22 to rotate; Then the commissioning pipe 8 of correct position is selected in the requirement for raw material, is communicated with by this commissioning pipe 8 with feed line, then is opened by heat insulation cover plate 5 corresponding for this commissioning pipe 8 times,
Then pulp is added in cell body 1 continuously in right amount, except feeding port, remaining heat insulation cover plate 5 can cover, along with the rotating screw flitch 22 of pusher roller 2 shifts pulp onto discharging opening, pulp is sufficiently agitated and heats in whole moving process, complete the digestion process of pulp, pulp arrives cell body 1 discharging opening one end after completing heating, enter in feed pipe 91 via material-falling hopper pipe 9, next production procedure is delivered into through Pulp pump 92, condensate water in boiling interlayer 3 enters header tank 6 through condensate water collecting pipe 33, through being discharged by outlet pipe 61 after reaching certain moisture storage capacity.
For hawthorn: when producing concentrated haw juice, containing a large amount of seed nucleis in the hawthorn pulp obtained, after adding thermal agitation through cell body 1, discharging opening formation accumulation is shifted onto by spiral flitch 22 in the bottom that seed nuclei is all positioned at cell body 1, and pulp is more frivolous on upper strata, if use the first pay-off will have a large amount of seed nuclei enter formation blocking in material-falling hopper pipe 9, therefore valve-off 93, open stop valve 95, under the effect of plate 24, seed nuclei is boosted to the discharging opening of cell body 1 sidewall, enter the mixture slurry that the material being inclined cross feed pipe 94 is exactly pulp and seed nuclei like this, next production procedure is transported to again by Pulp pump 92.Such pulp and seed nuclei are transferred out successively avoids seed nuclei to block up, and production line adaptability is strengthened, and versatility increases, and the reliability of equipment is stronger.
The temperature in the rotating speed of pusher roller 2 or boiling interlayer 3 can be regulated in pulp digestion process to control the quality requirement of pulp heating.
Although be described the utility model with reference to multiple explanatory embodiment of the present utility model here, but, should be appreciated that, those skilled in the art can design a lot of other amendment and embodiment, these amendments and embodiment will drop within spirit disclosed in the present application and spirit.More particularly, in the scope of, accompanying drawing open in the application and claim, multiple modification and improvement can be carried out to the building block of subject combination layout and/or layout.Except the modification of carrying out building block and/or layout is with except improvement, to those skilled in the art, other purposes also will be obvious.
Claims (5)
1. the cook vat of applicability a more than drawing mechanism, is characterized in that: it comprises for the cell body (1) of boiling, the heat insulation cover plate (5) covered on cell body (1) opening, is arranged on more than one commissioning pipe (8) on cell body (1) opening, is longitudinally arranged on pusher roller (2), the drive unit driving pusher roller (2) to rotate in cell body (1), is vertically arranged on the pay-off on cell body (1) discharge end bottom discharge mouth, the boiling interlayer (3) being arranged on cell body (1) outer wall and the steam air supply pipe (4) be communicated with boiling interlayer, described cell body (1) comprises frid (11) that cross section is U-shaped and is arranged on two end plates (12) that cell body (1) two ends are used for shutoff cell body (1), described pusher roller (2) comprises rotating shaft (21) and extends the spiral flitch (22) of material direction Spiral distribution, the reductor (71) that described drive unit comprises drive motors (7) and is connected with drive motors (7), described pusher roller (2) is arranged on end plate (12), described spiral flitch (22) and frid (11) inwall matched in clearance, one end of described pusher roller (2) is fixedly installed driving wheel (23) in end plate (12) outside, described driving wheel (23) is connected by the output shaft of belt with reductor (71), described pay-off comprises the first pay-off and the second pay-off, described first pay-off comprises the vertical material-falling hopper pipe (9) be connected with cell body (1) diapire discharging opening and the feed pipe (91) be communicated with material-falling hopper pipe (9), described feed pipe (91) is provided with Pulp pump (92), described feed pipe (91) is provided with valve (93), described valve (93) is positioned between material-falling hopper pipe (9) and Pulp pump (92), described second pay-off comprise be connected with cell body (1) sidewall discharging opening be inclined cross feed pipe (94), described feed pipe (94) other end that is inclined cross is communicated with the feed pipe (91) between valve (93) and Pulp pump (92), the described feed pipe (94) that is inclined cross is provided with stop valve (95), described rotating shaft (21) is provided with more than one plate (24), and described plate (24) is corresponding with cell body (1) sidewall discharging opening, described boiling interlayer (3) is the heating region be made up of the heating frid (31) and sealing plate (32) that are arranged on frid (11) outer wall, the cross section of described heating frid (31) is U-shaped, its side is welded with heating frid (31) extension, opposite side welds with frid (11) outer wall, described steam air supply pipe (4) is fixedly connected with heating frid (31), and described steam air supply pipe (4) is communicated with boiling interlayer (3) through heating frid (31).
2. one many applicabilities cook vat drawing mechanism according to claim 1, it is characterized in that: described heating frid (31) bottom is provided with condensate water collecting pipe (33), described heating frid (31) is also provided with heat-insulation layer outward, side and cell body (1) side of described heat insulation cover plate (5) are hinged, and described heat insulation cover plate (5) is multiple being arranged side by side; Open Side Down for described commissioning pipe (8), and described more than one commissioning pipe (8) is arranged in parallel.
3. one many applicabilities cook vat drawing mechanism according to claim 2, it is characterized in that: also comprise header tank (6), described condensate water collecting pipe (33) is communicated with header tank (6), described header tank is provided with fluid level control device in (6), and the outlet pipe (61) of described header tank (6) is provided with back water pump.
4. one many applicabilities cook vat drawing mechanism according to claim 3, is characterized in that: described feed pipe (91) is level two, and two described feed pipe (91) conveying trends are contrary.
5. one many applicabilities cook vat drawing mechanism according to claim 4, it is characterized in that: described second pay-off is two and is symmetricly set on cell body (1) both sides, described in be inclined cross feed pipe (94) and be communicated with the feed pipe (91) of respective side respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520259278.0U CN204560874U (en) | 2015-04-27 | 2015-04-27 | A kind of many applicabilities cook vat drawing mechanism |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520259278.0U CN204560874U (en) | 2015-04-27 | 2015-04-27 | A kind of many applicabilities cook vat drawing mechanism |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204560874U true CN204560874U (en) | 2015-08-19 |
Family
ID=53853586
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520259278.0U Expired - Fee Related CN204560874U (en) | 2015-04-27 | 2015-04-27 | A kind of many applicabilities cook vat drawing mechanism |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204560874U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106616410A (en) * | 2016-11-08 | 2017-05-10 | 吴忠市王国旗生物科技有限公司 | Technology for preparing bone grains |
| CN106670207A (en) * | 2016-12-05 | 2017-05-17 | 吴忠市王国旗生物科技有限公司 | Horizontal type bone grain steaming device |
-
2015
- 2015-04-27 CN CN201520259278.0U patent/CN204560874U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106616410A (en) * | 2016-11-08 | 2017-05-10 | 吴忠市王国旗生物科技有限公司 | Technology for preparing bone grains |
| CN106670207A (en) * | 2016-12-05 | 2017-05-17 | 吴忠市王国旗生物科技有限公司 | Horizontal type bone grain steaming device |
| CN106670207B (en) * | 2016-12-05 | 2019-05-31 | 吴忠市王国旗生物科技有限公司 | Horizontal skeletal grain steams equipment |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US10556258B2 (en) | Method for cleaning a machine for liquid or semi-liquid food products | |
| CN204560874U (en) | A kind of many applicabilities cook vat drawing mechanism | |
| KR101536843B1 (en) | Kimchi fermentation apparatus of strap continuous type | |
| WO2020029313A1 (en) | Integrated solid-liquid state fermentation device for vinegar | |
| CN203125689U (en) | Full-automatic production line for light-weight wall plates | |
| CN204560875U (en) | A kind of many applicabilities cook vat | |
| CN217052176U (en) | Full-automatic continuous cooking equipment | |
| CN204560873U (en) | A kind of semi open model pulp cook vat | |
| CN106617184A (en) | Circulating cleaning and sterilizing device for fruits | |
| CN203814495U (en) | In-place sterilizing mechanical-stirring glass fermentation tank | |
| CN217487499U (en) | Dairy products processing is with machine of disinfecting | |
| CN105394161A (en) | Food pickling machine | |
| CN202890397U (en) | Closed continuous operation type food steamer | |
| CN104263639A (en) | Dry fermentation system and fermentation method thereof | |
| CN204196301U (en) | Material forming system | |
| CN113951054A (en) | Instant-out type edible fungus material sterilization device | |
| CN113753494A (en) | Multilayer reciprocating chain belt type bran steaming machine | |
| CN203678753U (en) | High-efficient cleaning machine for plastic film regeneration | |
| CN206447792U (en) | A kind of complex wax production line with bottle placer | |
| CN208676246U (en) | A kind of Dairy fermentation production line | |
| CN101797485A (en) | Method for conveying easily-crystallized liquid | |
| KR101871883B1 (en) | Steam type cooked feed manufacturing apparatus for cattle | |
| CN201453689U (en) | Continuous type secondary sterilization machine | |
| CN206253062U (en) | A kind of industrial automation liquid agitation conveying device | |
| CN104385666B (en) | Material forming treating apparatus |
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: 20150819 Termination date: 20210427 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |