CN202465656U

CN202465656U - White spirit integrated treatment system

Info

Publication number: CN202465656U
Application number: CN2012200967707U
Authority: CN
Inventors: 黄晓蓉
Original assignee: SICHUAN YIWEN PURIFICATION TECHNOLOGY Co Ltd
Current assignee: SICHUAN YIWEN PURIFICATION TECHNOLOGY Co Ltd
Priority date: 2012-03-15
Filing date: 2012-03-15
Publication date: 2012-10-03
Anticipated expiration: 2022-03-15

Abstract

The utility model discloses a white spirit integrated treatment system. The white spirit integrated treatment system comprises a security filter, a TIS purifier, an LPA purifier and a terminal fine filter which are sequentially connected in series, wherein the bottom of the security filter is an input end which is connected with a pump through a production valve F1, the top of the security filter is communicated with the bottom of the TIS purifier through a production valve F2, the top of the TIS purifier is connected to the top of the LPA purifier through a production valve F3 and a production valve F4, the bottom of the LPA purifier is communicated with the bottom of the terminal fine filter through a production valve F5 and a production valve F6, and the top of the terminal fine filter is taken as an output end which is provided with a production valve F7. The white spirit integrated treatment system can effectively remove solid impurities and macromolecular impurities in white spirit to enable the tested value of the white spirit to meet the national standard, the filtering devices used in four processes are connected into a whole through pipelines and valves, and the simultaneous and continuous use of the four filtering devices is realized by controlling the on-off state of the valves so as to achieve the purposes of reducing the operation steps and saving the process time.

Description

The liquor integrated processing system

Technical field

The utility model relates to the wine purification filtering equipment in a kind of technology that brews alcoholic beverages, and specifically is meant the liquor integrated processing system.

Background technology

Liquor is muddy, low temperature becomes turbidity and precipitation and solid substance exceeds standard is current liquor, particularly the key of low temperature liquor production.General terms of settlement is that multiple devices, several different methods are used, and common liquor treating plant and method have:

1 sand litchi filtration unit: handle that of poor quality, low temperature becomes that turbidity and precipitation, production efficiency are low, the sand litchi is prone to stifledly, cleans difficulty, seldom use at present.

2 freezing and filterings: solve that liquor is muddy to become the turbidity and precipitation effect with low temperature, 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 cottonseed cake filtration units: 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 the turbidity and precipitation problem, and trivial operations, still there is use in the small-sized brewery less demanding to the vinosity amount.

4 diatomite filtration devices: 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, and during Coagulation and Adsorption agent improper use, the damage of wine body local flavor is bigger.

5 micro-pore-film filtration devices: commercially available various forms of micro-pore-film filtration machines; All be polymer PE, PP, PA microporous membrane be combined into different apertures; Be by the different mechanical separation device in aperture, the liquor composition is complicated, and 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.

The utility model content

The purpose of the utility model is to provide the liquor integrated processing system, and it is single to solve present being seen wine body treatment unit filtering function, can not solve simultaneously to fall solid, turbidity removal and anti-cold problem, reaches the purpose that reduces operation steps, improves purification efficiency.

The purpose of the utility model realizes through following technical proposals:

The liquor integrated processing system; Comprise placed in-line successively security filter, TIS cleaner, LPA cleaner and terminal secondary filter; Wherein the bottom of security filter is that input terminus is connected with pump through producing valve F1; The top of security filter is through producing the bottom UNICOM of valve F2 and TIS cleaner; The top of TIS cleaner is through producing valve F3, produce the top that valve F4 is connected to the LPA cleaner, and the bottom of LPA cleaner is through producing valve F5, producing valve F6 and be communicated with the bottom of terminal secondary filter, and the top of terminal secondary filter is as output terminal and production valve F7 is installed.During use, liquor to be filtered is extracted out with pump and got into the bottom of security filter through producing valve F1, filter through going out to accomplish first road from the pipeline overflow at security filter top after the inner filtration of security filter; Get into the bottom of TIS cleaner through producing valve F2 then, liquor goes out to accomplish second road from the pipeline overflow at TIS cleaner top after through the inner filtration of TIS cleaner and filters; Through producing valve F3 and producing valve F4 entering LPA cleaner top, liquor gets into from LPA cleaner top and filters through discharging completion the 3rd road from its bottom behind its self-filtering again; Through producing valve F5 and producing secondary filter bottom, valve F6 entering terminal, liquor gets into from terminal secondary filter bottom and through going out to accomplish the filtration of the 4th road from its top overflow behind the secondary filter self-filtering of terminal, liquor flows out through producing valve F7 at last.After liquor filters the filtration of operation through four roads; Solid impurity and macromole impurity with effectively removing in the liquor make the detected value of liquor be up to state standards, simultaneously; The straining installation that four technologies are used is connected to integral body through pipeline and valve; Realize that through the off state of by-pass valve control four filtering whiles use continuously, reach the minimizing operation steps, practice thrift the purpose of process time.

Between described production valve F1 and pump, return valve T is installed, return valve T is communicated with through pipeline with production valve F7, and pipeline is communicated with security filter, TIS cleaner, LPA cleaner and terminal secondary filter respectively.Further say; Cleaning for the ease of equipment; Between production valve F1 and pump, return valve T is installed; Return valve T is communicated with through pipeline with production valve F7, and pipeline is communicated to security filter, TIS cleaner, LPA cleaner and terminal secondary filter, constitutes the cleaning pipe network of each filtration vessel.

On the pipeline between said return valve T and the production valve F7, be connected with cleaning valve f8 and cleaning valve f12; Wherein, Cleaning valve f8 is connected to security filter top and produces on the valve F3, and the end of cleaning valve f12 is connected on the pipeline, and the other end is connected to be produced between valve F5 and the production valve F6; Simultaneously, the pipeline of producing between valve F5 and the production valve F6 is connected to production valve F4 through cleaning valve f13.Specifically, the cleaning direction of each filtration vessel can be identical with the filtering direction that changes container, also can be opposite; Therefore; In the utility model, at first consider situation in the opposite direction, that is: the cleaning direction of security filter, TIS cleaner is by under last; And the cleaning direction of LPA cleaner, terminal secondary filter from bottom to top; In order to adapt to this plan, on the pipeline between return valve T and the production valve F7, be connected with cleaning valve f8 and cleaning valve f12, cleaning valve f8 is connected to security filter top and produces on the valve F3 through pipeline; The end of cleaning valve f12 is connected on the pipeline, and the other end is communicated with LPA cleaner bottom and terminal secondary filter bottom through producing valve F5 respectively with production valve F6.

Be separately installed with tapping valve F9, tapping valve F11, tapping valve F16 and tapping valve F17 in the bottom of security filter, TIS cleaner, LPA cleaner and terminal secondary filter.Say that further the discharge of scavenging solution for ease is separately installed with tapping valve in the bottom of each filtration vessel.

Be separately installed with vent valve Y1, vent valve Y2, vent valve Y3 and vent valve Y4 at the top of security filter, TIS cleaner, LPA cleaner and terminal secondary filter.As the further improvement of the utility model,, vent valve all is installed at each filtration vessel top in order in time to discharge the gas in each filtration vessel.

Be separately installed with tensimeter P1, tensimeter P2, tensimeter P3 and tensimeter P4 at the top of security filter, TIS cleaner, LPA cleaner and terminal secondary filter.As the further improvement of the utility model, in order in time to know the pressure condition in each filtration vessel, can each filtration vessel of son on the setting pressure table.

The pore size filter of security filter, TIS cleaner, LPA cleaner and terminal secondary filter reduces successively.In order to guarantee the filter effect of native system, the mode that the pore size filter of employing security filter, TIS cleaner, LPA cleaner and terminal secondary filter reduces successively is to reach abundant filtering purpose.

The utility model compared with prior art has following advantage and beneficial effect:

After 1 the utility model liquor integrated processing system, liquor filter the filtration of operation through four roads, with solid impurity and the macromole impurity effectively removed in the liquor; Make the detected value of liquor be up to state standards; Simultaneously, the straining installation that four technologies are used is connected to integral body through pipeline and valve, realizes that through the off state of by-pass valve control four filtering whiles use continuously; Reach the minimizing operation steps, practice thrift the purpose of process time;

2 the utility model liquor integrated processing systems; The cleaning direction of security filter, TIS cleaner is by under last; And the cleaning direction of LPA cleaner, terminal secondary filter from bottom to top; On the pipeline between return valve T and the production valve F7, be connected with cleaning valve f8 and cleaning valve f12; Cleaning valve f8 is connected to security filter top and produces on the valve F3 through pipeline, and the end of cleaning valve f12 is connected on the pipeline, and the other end is communicated with LPA cleaner bottom and terminal secondary filter bottom through producing valve F5 respectively with production valve F6;

3 the utility model liquor integrated processing systems, the mode that the pore size filter of employing security filter, TIS cleaner, LPA cleaner and terminal secondary filter reduces successively is to reach abundant filtering purpose; Simultaneously, the liquor after the processing is as clear as crystal, the constant muddiness of low temperature; Solid content is up to state standards; Production efficiency is high, and is simple to operate, greatly reduces production cost.

Description of drawings

Fig. 1 is the utility model structural representation.

Mark and corresponding component title in the accompanying drawing:

1-security filter, 2-TIS cleaner, 3-LPA cleaner, 4-terminal secondary filter, 5-pump.

Embodiment

Below in conjunction with embodiment the utility model is done further to specify, but the embodiment of the utility model is not limited thereto.

Embodiment

As shown in Figure 1; The utility model liquor integrated processing system; Comprise placed in-line successively security filter 1, TIS cleaner 2, LPA cleaner 3 and terminal secondary filter 4; Wherein the bottom of security filter 1 is that input terminus is connected with pump 5 through producing valve F1, on the bottom pipe of security filter 1 Y-tube is installed, and three ports of Y-tube connect bottom and the tapping valve F9 that produces valve F1, security filter 1 respectively; Be separately installed with vent valve Y1 and tensimeter P1 at the top of security filter 1; Simultaneously, the top of security filter 1 is through producing the bottom UNICOM of valve F2 and TIS cleaner 2, and the top of security filter 1 is communicated with production valve F3, production valve F4 and cleaning valve f13 through cleaning valve f10; On the bottom pipe of TIS cleaner 2 Y-tube is installed; Three ports of Y-tube connect bottom and the tapping valve F11 that produces valve F2, TIS cleaner 2 respectively; The top of TIS2 cleaner is equipped with vent valve Y2 and tensimeter P2; Simultaneously; The top of TIS cleaner 2 is through producing valve F3, producing the top that valve F4 is connected to LPA cleaner 3, and the top of TIS cleaner 2 is through producing valve F3, cleaning valve f13, producing the bottom that valve F5 is connected to LPA cleaner 3, and the top of TIS cleaner 2 is through producing valve F3, cleaning valve f13, producing the bottom that valve F6 is connected to terminal secondary filter 4; The bottom of LPA cleaner 3 is communicated with the bottom of terminal secondary filter 4 through production valve F5, production valve F6; Between cleaning valve f10 and cleaning valve f13, T-valve is installed, three ports of T-valve are connected respectively to cleaning valve f10, cleaning valve f13 and cleaning valve f14, and cleaning valve f17 is installed on the bottom pipe of LPA cleaner 3; Be connected with cleaning valve f16 on the pipeline of terminal secondary filter 4 bottoms; The top of terminal secondary filter 4 is as output terminal and production valve F7 is installed; Produce on the pipeline between valve F7 and the return valve T cleaning valve f15 is installed, cleaning valve f15 is producing between valve F7 and the cleaning valve f12.

The above; It only is the preferred embodiment of the utility model; Be not that the utility model is done any pro forma restriction, every according on the technical spirit of the utility model to any simple modification, equivalent variations that above embodiment did, all fall within the protection domain of the utility model.

Claims

1. liquor integrated processing system; It is characterized in that: comprise placed in-line successively security filter (1), TIS cleaner (2), LPA cleaner (3) and terminal secondary filter (4); Wherein the bottom of security filter (1) is that input terminus is connected with pump (5) through producing valve F1; The top of security filter (1) is through producing the bottom UNICOM of valve F2 and TIS cleaner (2); The top of TIS cleaner (2) is through producing valve F3, producing the top that valve F4 is connected to LPA cleaner (3); The bottom of LPA cleaner (3) is communicated with the bottom of terminal secondary filter (4) through production valve F5, production valve F6, and the top of terminal secondary filter (4) is as output terminal and production valve F7 is installed.

2. liquor integrated processing system according to claim 1; It is characterized in that: between described production valve F1 and pump (5), return valve T is installed; Return valve T is communicated with through pipeline with production valve F7, and pipeline is communicated with security filter (1), TIS cleaner (2), LPA cleaner (3) and terminal secondary filter (4) respectively.

3. liquor integrated processing system according to claim 2; It is characterized in that: on the pipeline between said return valve T and the production valve F7, be connected with cleaning valve f8 and cleaning valve f12, wherein, cleaning valve f8 is connected to security filter (1) top and produces on the valve F3; The end of cleaning valve f12 is connected on the pipeline; The other end is connected to be produced between valve F5 and the production valve F6, and simultaneously, the pipeline of producing between valve F5 and the production valve F6 is connected to production valve F4 through cleaning valve f13.

4. liquor integrated processing system according to claim 3 is characterized in that: the bottom at security filter (1), TIS cleaner (2), LPA cleaner (3) and terminal secondary filter (4) is separately installed with tapping valve F9, tapping valve F11, tapping valve F16 and tapping valve F17.

5. liquor integrated processing system according to claim 1 is characterized in that: the top at security filter (1), TIS cleaner (2), LPA cleaner (3) and terminal secondary filter (4) is separately installed with vent valve Y1, vent valve Y2, vent valve Y3 and vent valve Y4.

6. liquor integrated processing system according to claim 1 is characterized in that: the top at security filter (1), TIS cleaner (2), LPA cleaner (3) and terminal secondary filter (4) is separately installed with tensimeter P1, tensimeter P2, tensimeter P3 and tensimeter P4.

7. according to any described liquor integrated processing system in the claim 1 to 6, it is characterized in that: the pore size filter of security filter (1), TIS cleaner (2), LPA cleaner (3) and terminal secondary filter (4) reduces successively.