That wine falls is solid, turbidity removal, anti-cold all-in-one
The utility model relates to a kind of wine treatment facility.
It is current liquor that liquor muddiness, low temperature become that muddy precipitation and solid substance exceed standard, particularly the low alcohol white spirit key of producing.General terms of settlement is that multiple devices, several different methods are used, and common liquor treating plant and method have:
1, sand stamen filtration unit: handle that of poor quality, low temperature becomes turbidity and precipitation, production efficiency is low, the sand stamen is easily stifled, cleans difficulty, now seldom use.
2, freezing and filtering: solve liquor muddy and low temperature and become muddy sedimentation effect, but it is little to fall solid effect, this method investment is big, energy consumption is high, the production cycle is long, trivial operations, seldom use.
3, the cottonseed cake filtration unit: mainly be flame filter press, it is better to solve liquor turbidity and precipitation effect, but can not fall admittedly, and can not solve liquor low temperature and become muddy sedimentation problem, and trivial operations.Still there is use in less demanding small-sized brewery to vinosity.
4, the diatomite filtration device: mainly contain plate and frame, board-like and candle filter, result of use is relatively poor separately, usually absorbs, clarifies the supporting use of intermediate processing with coagulation.Its operation is many, and weak effect only has minority to have and falls solid effect.During Coagulation and Adsorption agent improper use, the damage of wine body local flavor is bigger.
5, the micro-pore-film filtration device: commercially available various forms of micro-pore-film filtration machines all are that polymer (PE, PP, the PA) micropore with different apertures is touched be combined into, are by the different mechanical separation device in aperture.Liquor composition complexity, oxious component and useful composition are not distinguished by molecular size.Therefore, single mechanical picker tripping device can not make wine reach simultaneously to fall solid, turbidity removal and anti-cold effect.General microporous filter turbidity removal effect is better, does not fall solid and anti-cold effect but have, and ultrafiltration (tubular fibre), because of microporous membrane little, turbidity removal effect is good, and anti-cryogenic effect is also good, but it is not obvious to fall solid effect, and very easily stop up, clean difficulty, wine body flavor loss is also bigger.
In sum, the general filtering function of present being seen wine treatment unit is single, can not solve solid, turbidity removal and the anti-cold problem of falling simultaneously.Given this reason, the purpose of this utility model are that design is a kind of simple in structure, can solve simultaneously that solid, turbidity removal falls in liquor, anti-low temperature becomes muddy sedimentation problem, and keeps the wine of former wine taste to handle all-in-one.
That this liquor falls is solid, turbidity removal, anti-cold all-in-one have reached above-mentioned purpose of design satisfactorily, it comprises millipore filtration unit, pipeline and control valve, it is characterized in that having the functional high molecule material molecular sieve, the millipore filtration unit is made of microporous pipe filtering unit and the smart filter of microporous membrane unit, molecular sieve is made up of the two-stage mol sieve unit, and it is one that these four filtering units are linked by the series connection of pipeline order.The filtering material of microporous pipe filtering unit is a polypropylene material, and pore size filter is 0.85~1.2 μ m, and the smart filter of microporous membrane unit filtering material is a polythene material, and pore size filter is 0.1~0.45 μ m, and the mol sieve unit pore size filter is (200~10000) * 10
-10M.
For the ease of moving.These four series connection link for the millipore filtration unit of one and molecular sieve all are fixed on the base, and roller is equipped with in the base bottom.
The wine processor operation is convenient in order to make, pipeline import front end of the present utility model links to each other with a beverage pump.
The solid suspension impurity in the wine is mainly held back, removed to micropore of the present utility model (pipe) membrane filter unit, and mol sieve unit, major function are to reduce solid content and improve liquor cold resistance energy, removes to cause that liquor low temperature becomes muddy sedimentary peculiar smell impurity.
This machine is with above-mentioned difference in functionality, it is one that the unit of structure links with control valve by the road, not only make this machine multiple functional, it is solid disposablely to finish falling of liquor, turbidity removal, anti-cold purifying treatment, make the wine after the processing as clear as crystal, low temperature is the feculence precipitation not, solid content meets national standard, and the production efficiency height, simple to operate, replaced multiple times of filtration processing in the production of bottle wine, reduced that wine that many treatment facility step-by-step processing are brought decreases and operational loaded down with trivial details, greatly reducing production cost, be applicable to that the liquor of various wine degree and odor type is handled, is the treatment facility and the helper of present brewery the best.
Fig. 1 is the utility model profile synoptic diagram.
Fig. 2 is the vertical view of Fig. 1.
Further specify the utility model below in conjunction with accompanying drawing:
As seen from Figure 1, the utility model is by microporous pipe filtering unit I, and the microporous membrane essence is filtered unit II, molecular sieve III and IV, and link pipeline, valve and base formation.
Among Fig. 2,
2,4,7,9,11 is service pipe and valve;
3,5,6,8 is pipe blow-through and valve;
12,13,14,15 is blow-off line and valve;
1 for import, 16 is the outlet of wine liquid, and 10 are the blowdown outlet.
During work, Open valve 2,4,7,9,15, valve-off 3,5,6,8,11,12,13,14,16, under external pressure promoted, wine was flowed into by import 1, was flowed out by outlet 15 after I, II, III, IV processing unit processes.So far, disposablely finished that falling of wine is solid, turbidity removal and anti-deepfreeze.During cleaning, difference valve-off 2,4,7,9,15, difference Open valve 11,12,13,14,16,3,5,6,8, scavenging solution flows into I, II, four processing units of III, IV respectively under pressure promotes, and waste liquid is flowed out by sewage draining exit 10.
For the facility on cleaning and effectively, the utility model can oppositely clean, and scavenging solution is pressed into from outlet, reversely finishes the future process, even equipment obtains more conveniently cleaning completely.
In the present embodiment, strainer tube aperture, pre-flock unit is 1.0 μ m, and smart filter unit pore size filter is 0.5 μ m, and mol sieve unit III pore size filter is 300 * 10
-10M, mol sieve unit IV pore size filter are 8 * 10
-10M.