CN202519234U - Yellow wine press - Google Patents
Yellow wine press Download PDFInfo
- Publication number
- CN202519234U CN202519234U CN201220042232XU CN201220042232U CN202519234U CN 202519234 U CN202519234 U CN 202519234U CN 201220042232X U CN201220042232X U CN 201220042232XU CN 201220042232 U CN201220042232 U CN 201220042232U CN 202519234 U CN202519234 U CN 202519234U
- Authority
- CN
- China
- Prior art keywords
- filter plate
- valve
- filter
- plate
- pressure strip
- 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
Images
Landscapes
- Filtration Of Liquid (AREA)
Abstract
The utility model relates to a yellow wine press, and belongs to the technical field of wine equipment manufacturing. By the press, glutinous rice wine sediment can be pressed and filtered at mechanization degree. The press consists of a hydraulic device (1), a base (2), beams (3), an exhaust valve (4), a check valve (5), an excess material blow-out valve (6), a pressing plate (7), diaphragm filter plates (8), filter plates (9), a thrust plate (10), a discharge valve (11), a pressure meter (12), a feed valve (13) and filter cloth (14), wherein a main unit consists of the base (2), the beams (3), the pressing plate (7) and the thrust plate (10); the base (2), the pressing plate (7) and the thrust plate (10) are connected into a whole through the two beams; an oil cylinder and the hydraulic device (1) are respectively arranged at the two ends of the base (2); and the filter plates (9) and the diaphragm filter plates (8) are alternately arranged between the thrust plate (10) and the pressing plate (7) and provided with the filter cloth (14) to form filter chambers.
Description
Technical field
The utility model belongs to drinks equipment manufacturing technology field, is specifically related to a kind of yellow rice wine squeezing machine.
Background technology
In the brewing process of yellow rice wine, after the sticky rice wine fermentation was accomplished, sticky rice wine and schlempe mixed; Therefore need separate with schlempe sticky rice wine, to obtain the finished product sticky rice wine that can satisfy market demand, in existing purifies and separates technology; Mainly consider: on the one hand based on following two aspects; Need to adopt effective separation method and device, let sticky rice wine separate effectively, guarantee sticky rice wine quality, color and luster and the mouthfeel of finished product with schlempe; On the other hand,, therefore use rational pressing method, fully drain the wine in the schlempe, can improve the output of sticky rice wine, practice thrift cost because schlempe contains a large amount of wine.Yet the sticky rice wine schlempe pressing method that generally adopts in the prior art mainly is through manual operation, schlempe is packed into filter in the cloth bag; Drip to ooze and squeeze out wine liquid, long labour intensity consuming time is big and efficient is low, can't satisfy the requirement of large-scale commercial prodn; In addition, because the extruding of wine liquid is not thorough, still there are a large amount of wine liquid to residue in the schlempe; Cause serious waste, also influence the production cost of sticky rice wine.
Therefore; Develop a kind of novel sticky rice wine press apparatus, mechanization degree that can be higher is realized the squeezing to the sticky rice wine schlempe down, and assurance wine liquid effectively separates with schlempe; And extrude wine liquid residual in the abundant schlempe; Improving utilization ratio of raw materials, practice thrift cost, is the current urgency of industry problem to be solved.
Summary of the invention
In order to overcome the deficiency that exists in the prior art, the purpose of the utility model provides a kind of novel sticky rice wine press apparatus, can under mechanization degree, realize the squeezing to the sticky rice wine schlempe, guarantees effective filtering separation of wine liquid and schlempe.
The utility model is realized through following technical scheme:
A kind of yellow rice wine squeezing machine blows out valve 6, pressure strip 7, membrane filter plate 8, filter plate 9, thrust plate 10, blow-off valve 11, tensimeter 12, feed valve 13, filter cloth 14 by hydraulicefficiency plant 1, support 2, crossbeam 3, vent valve 4, vacuum breaker 5, clout and forms; It is characterized in that: two crossbeams 3 connect into an integral body to support 2 and pressure strip 7, thrust plate 10, between pressure strip 7 and thrust plate 10, have been arranged alternately filter plate 9, membrane filter plate 8, and membrane filter plate 8 is provided with filter cloth 14; Constitute filter chamber by membrane filter plate 8 and filter plate 9; At pressure strip 7 one ends hydraulicefficiency plant 1 is housed, is provided with vacuum breaker 5 on pressure strip 7 tops, clout blows out valve 6; Be provided with vent valve 4 in pressure strip 7 bottoms, be provided with feed valve 13 through tensimeter 12 in thrust plate 10 sides.
Further, described membrane filter plate 8 both sides are coating diaphragm of rubber, and diaphragm of rubber is coating filter cloth 14 outward.
Further, there are several apertures on described filter cloth 14 surfaces.
Further, described filter plate (9) and membrane filter plate (8) are by cast iron, cast steel or stainless material manufacturing.
The utility model beneficial effect:
After adopting above-mentioned 7 kinds of structures, can realize two processes of press filtration and inflation squeezing simultaneously, can play and filter and the squeezing double effects; Filter plate 9 is established charging, air, three passages of filtrating with membrane filter plate 8, and every filter plate 9 is provided with filter cloth 14, and opening for feed and filter plate 9 are locked by screw; Form central feed channel, pressurized air is imported from air passageways, and membrane filter plate 8 is provided with squeeze diaphragm; Filter plate 9 and membrane filter plate 8 are arranged on the crossbeam 3 in certain sequence, carry out expressing process.Suspension-s gets into each filter chamber from thrust plate 10 intermediary feed valves 13, and liquid forms filtrating through filtering medium layer under the promotion of pressure, flow to the groove on filter plate 9 surfaces, concentrates the back to discharge from blow-off valve 11, and solid is trapped within and forms filter cake in the filter chamber.Suspension-s through filter cloth 14, is become limpidly by a tiny solid material by dirt, realize filtration procedure.Have that the low filter cloth of good seal performance, cake moisture is not fragile, easy and simple to handle, productivity effect is than advantages such as height, not only can wine liquid can fully be separated with schlempe, can not sneak into impurity; Improved the quality of finished wine, and mechanization degree is high, can also in expressing process, fully extrude wine liquid residual in the schlempe; Improve utilization ratio of raw materials, practice thrift cost, adopt hydraulic pressure to compress and lock with armstrong's patent; Convenient operating maintenance, safe and reliable to operation.
Description of drawings
Fig. 1 is the utility model Facad structure synoptic diagram.
Fig. 2 is the utility model side structure synoptic diagram.
Fig. 3 is that the utility model filters and squeezing flows to synoptic diagram.
Among the figure, hydraulicefficiency plant 1, support 2, crossbeam 3, vent valve 4, vacuum breaker 5, clout blow out valve 6, pressure strip 7, membrane filter plate 8, filter plate 9, thrust plate 10, blow-off valve 11, tensimeter 12, feed valve 13, filter cloth 14
Embodiment
Below in conjunction with accompanying drawing and embodiment the utility model is further described.
A kind of yellow rice wine squeezing machine blows out valve 6, pressure strip 7, membrane filter plate 8, filter plate 9, thrust plate 10, blow-off valve 11, tensimeter 12, feed valve 13, filter cloth 14 by hydraulicefficiency plant 1, support 2, crossbeam 3, vent valve 4, vacuum breaker 5, clout and forms; Two crossbeams 3 connect into an integral body to support 2 and pressure strip 7, thrust plate 10, between pressure strip 7 and thrust plate 10, have been arranged alternately filter plate 9, membrane filter plate 8, and membrane filter plate 8 is provided with filter cloth 14; Membrane filter plate 8 both sides are coating diaphragm of rubber; The diaphragm of rubber outside is coating filter cloth 14, and there are several apertures on filter cloth 14 surfaces, between pressure strip 7 and thrust plate 10, constitutes filter chamber by membrane filter plate 8 and filter plate 9; At pressure strip 7 one ends hydraulicefficiency plant 1 is housed; Be provided with vacuum breaker 5 on pressure strip 7 tops, clout blows out valve 6, is provided with vent valve 4 in pressure strip 7 bottoms, is provided with feed valve 13 in thrust plate 10 sides through tensimeter 12.
Compressing and loosening by hydraulicefficiency plant 1 control of filter plate 9 can realize two processes of press filtration and inflation squeezing simultaneously, can play and filter and the squeezing double effects; When compressing filter plate; The action of electric motor starting SV, oil pump is to oil cylinder back cavity fuel feeding, and piston-advance compresses filter plate 9; Oil pump stops when oil cylinder working-pressure rises to the higher limit of electro connecting pressure gauge; When oil pressure was reduced to the lower value of electro connecting pressure gauge, oil pump restarted to oil cylinder back cavity fuel feeding, and snap-in force is remained within the manometric bound; Compress filter plate 9 through hydraulic pressure, constitute one group of filter chamber by filter plate of alternately arranging 9 and membrane filter plate 8, there is groove on the surface of filter plate 9; Its protrusion position has through hole in order to support filter cloth 14 on the corner of filter plate 9 and membrane filter plate 8, and the assembling back constitutes complete passage; Can feed suspension-s, washing water and draw filtrating, filter plate 9 and each jug rest of membrane filter plate 8 both sides are on crossbeam 3, and the both sides of membrane filter plate 8 are coating diaphragm of rubber; The diaphragm of rubber outside is coating filter cloth 14, and filter cloth 14 plays gasket seal, and material gets into each filter chamber from the feed valve 13 on the thrust plate 10; Solid particulate is trapped within the filter chamber because of the aperture of its particle diameter greater than filter cloth 14, and filtrating is then flowed out from the fluid hole of filter plate below, by charging pump suspension-s is pressed into filter chamber; Opening for feed and filter plate 9 form central feed channel by screw locking, and pressurized air is imported from air passageways; The yellow wine fermentation wine with dregs gets in each filter chamber through the feed valve 13 on filter plate 9 tops; Hold back the solid substance greater than filter opening through filter cloth 14, the solution part concentrates the back to discharge from blow-off valve 11 then through the outflows such as groove of filter plate 9 and membrane filter plate 8; Thereby membrane filter plate 8 and pressing plate 9 are heaved through pressurized air. further squeeze out wine liquid remaining in the filter cake, become limpid realization filtration procedure by dirt.On filter cloth 14, form filter residue, until being full of filter chamber, filtrating pass filter cloth and along filter plate trench flow to sheet frame corner passage, concentrate to discharge to filter to finish, can feed to clean and wash the water washing filter residue.After the washing, also feed pressurized air sometimes, remove remaining washings, open pressure filter removal filter residue subsequently, clean filter cloth 14, filter plate 9 and membrane filter plate 8 homings begin next working cycle.
The oil pump of hydraulicefficiency plant 1 is controlled by electro connecting pressure gauge; Manometric upper limit pointer and lower limit pointer are set in the numerical value of processing requirement; When reaching the manometric power dump oil pump of prescribing a time limit of going up, snap-in force stops power supply; Leaking in oil piping system is issuable and leaking outside causes snap-in force to descend; The power connection oil pump begins fuel feeding when dropping to tensimeter lower limit pointer, and pressure reaches power dump oil pump fuel cut-off in limited time, and circulation is to guarantee the effect of snap-in force in the process that reaches filter material like this.
Pressure filter is big or be bordering on incompressible suspension-s and can both be suitable for for the filter residue compressibility; The concentration of solid particles of the suspension-s that is fit to is generally below 10%; Working pressure is generally 0.3～0.6 MPa; Filter plate 9 compresses with modes such as manual spiral of membrane filter plate 8 usefulness and hydraulic pressure, and filter plate 9 and membrane filter plate 8 are by made such as cast iron, cast steel or stainless steels.
Pressure filter is used for separating of solid and liquid, compares with other solid-liquid separating equipment, and the mud cake after pressure filter filters has higher solid content and good separating effect, the mixed solution filter cloth of flowing through; Solid rests on the filter cloth, and on filter cloth, piles up gradually to form and filter mud cake, and the filtrating part then penetrates filter cloth; Become and do not contain the solid clear liquid, along with the carrying out of filtration procedure, cake filtration begins; Hmc increases gradually, and filtration resistance strengthens, and the long more separation efficiency of filtration time is high more.Have that the low filter cloth of good seal performance, cake moisture is not fragile, easy and simple to handle, productivity effect is higher, not only can wine liquid can fully be separated with schlempe, can not sneak into impurity; Improved the quality of finished wine, and mechanization degree is high, can also in expressing process, fully extrude wine liquid residual in the schlempe; Improve utilization ratio of raw materials, practice thrift cost, adopt hydraulic pressure to compress and armstrong's patent locking pressurize; Convenient operating maintenance, safe and reliable to operation.
Claims (4)
1. yellow rice wine squeezing machine blows out valve (6), pressure strip (7), membrane filter plate (8), filter plate (9), thrust plate (10), blow-off valve (11), tensimeter (12), feed valve (13), filter cloth (14) by hydraulicefficiency plant (1), support (2), crossbeam (3), vent valve (4), vacuum breaker (5), clout and forms; It is characterized in that: two crossbeams (3) connect into an integral body to support (2) and pressure strip (7), thrust plate (10); Filter plate (9), membrane filter plate (8) between pressure strip (7) and thrust plate (10), have been arranged alternately; Membrane filter plate (8) is provided with filter cloth (14), constitutes filter chamber by membrane filter plate (8) and filter plate (9), at pressure strip (7) one ends hydraulicefficiency plant (1) is housed; Be provided with vacuum breaker (5) on pressure strip (7) top; Material blows out valve (6), is provided with vent valve (4) in pressure strip (7) bottom, is provided with feed valve (13) in thrust plate (10) side through tensimeter (12).
2. a kind of yellow rice wine squeezing machine according to claim 1 is characterized in that: the both sides of described membrane filter plate (8) are coating diaphragm of rubber, and diaphragm of rubber is coating filter cloth (14) outward.
3. a kind of yellow rice wine squeezing machine according to claim 1 is characterized in that: there are several apertures on described filter cloth (14) surface.
4. a kind of yellow rice wine squeezing machine according to claim 1 is characterized in that: described filter plate (9) and membrane filter plate (8) are by cast iron or cast steel or stainless material manufacturing.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220042232XU CN202519234U (en) | 2012-02-09 | 2012-02-09 | Yellow wine press |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201220042232XU CN202519234U (en) | 2012-02-09 | 2012-02-09 | Yellow wine press |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202519234U true CN202519234U (en) | 2012-11-07 |
Family
ID=47102194
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201220042232XU Expired - Fee Related CN202519234U (en) | 2012-02-09 | 2012-02-09 | Yellow wine press |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202519234U (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103223269A (en) * | 2013-04-19 | 2013-07-31 | 广西新天德能源有限公司 | Energy-saving diaphragm type pressure filter |
| CN103289880A (en) * | 2013-06-25 | 2013-09-11 | 广西运亨酒业有限公司 | A squeezing apparatus for glutinous rice wine |
| CN109466100A (en) * | 2018-09-20 | 2019-03-15 | 戴建设 | A kind of yellow rice wine pressing device |
-
2012
- 2012-02-09 CN CN201220042232XU patent/CN202519234U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN103223269A (en) * | 2013-04-19 | 2013-07-31 | 广西新天德能源有限公司 | Energy-saving diaphragm type pressure filter |
| CN103289880A (en) * | 2013-06-25 | 2013-09-11 | 广西运亨酒业有限公司 | A squeezing apparatus for glutinous rice wine |
| CN109466100A (en) * | 2018-09-20 | 2019-03-15 | 戴建设 | A kind of yellow rice wine pressing device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN202342964U (en) | Air bag type efficient solid-liquid separation press filter | |
| CN206938038U (en) | A kind of fruit wine pressing device | |
| CN202519234U (en) | Yellow wine press | |
| CN202822909U (en) | Novel vertical-type full-automatic self-locking-type efficient diaphragm filter press | |
| CN203315822U (en) | Automatic compartment-type pressure-resistant elastic plate-and-frame presser | |
| CN211896608U (en) | High-pressure efficient sludge filter press | |
| CN211635472U (en) | Natural plant extract raw material impurity separation device | |
| CN110404290B (en) | Self-tightening multilayer supercritical extraction kettle | |
| CN201483789U (en) | Pressing device of glutinous rice wine | |
| CN211724823U (en) | Filter abundant pressure filter for magnesium sulfate production | |
| CN209967778U (en) | Diaphragm filter plate and corresponding filter press | |
| CN211706015U (en) | High-pressure diaphragm filter press | |
| CN209848415U (en) | High-efficient plate and frame filter press | |
| CN206262181U (en) | Flame filter press with automatic back-washing function | |
| CN213925051U (en) | Diaphragm filter press for electrolytic manganese dioxide production | |
| CN205055529U (en) | Adopt plate filtration device of filter unit constitution | |
| CN212731200U (en) | High-pressure dewatering device in diaphragm plate | |
| CN208287572U (en) | Filter press ethylene propylene diene rubber filter plate | |
| CN218944443U (en) | Backwash single-chamber feeding filter press | |
| CN204034362U (en) | Plate and frame mash filter | |
| CN204560876U (en) | Fruit juice leaching device | |
| CN219002101U (en) | Automatic change vertical diaphragm filter-pressing device | |
| CN204952391U (en) | Vertical plate filtration machine | |
| CN211987311U (en) | 5 cubic sealed leaf filter | |
| CN215352186U (en) | Light calcium carbonate filter-pressing percolation system |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121107 Termination date: 20130209 |