CN204090948U - A kind of underflow raw material sterilization system - Google Patents
A kind of underflow raw material sterilization system Download PDFInfo
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- CN204090948U CN204090948U CN201420512161.4U CN201420512161U CN204090948U CN 204090948 U CN204090948 U CN 204090948U CN 201420512161 U CN201420512161 U CN 201420512161U CN 204090948 U CN204090948 U CN 204090948U
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Abstract
The utility model discloses a kind of underflow raw material sterilization system, described underflow raw material sterilization system comprises sterilizer main frame, the slurry compensator be connected with the underflow material inlet pipe of sterilizer main frame, the steam-water separator be connected with sterilizer clean steam arrival end, be arranged on the duplex strainer between slurry compensator and sterilizer, be responsible for the underflow feedstock transportation in slurry compensator to the dehvery pump of sterilizer, be responsible for the switch board controlling dehvery pump start and stop and whole system signal and operated pneumatic valve start and stop, one end is connected with sterilizer underflow material outlet end, the valve group that the other end is connected with slurry compensator material inlet end and balance tank connected Pyatyi dilatation noise reduction steam heater with slurry, the utility model structure is simple, easy to operate, and automaticity is high, has very strong practicality, can carry out high temperature sterilization, greatly reduce generally acknowledged labour intensity to underflow raw material, and CIP cleaning can be carried out to the disinfection system after sterilization.
Description
Technical field
The utility model relates to a kind of underflow raw material sterilization system, and particularly a kind of underflow raw material adopts the continuous direct-fired disinfection system of clean steam.
Background technology
General disinfection system is all adopt scraper-type high temperature sterilization machine or clearance-type retort, and existing clearance-type retort is airtight, to pressurize a cooking reaction pot; Steam-heating system, thermal resistance heating system, water-bath type decoction system can be divided into by the difference of heat medium; Steam-heating system mainly produces the steam of certain pressure for thermal source with boiler, is directly passed into the disinfection system carrying out in underflow raw material heating by Boiler Steam; Chief component comprises a pot body, pot cover, steam jet etc., the features such as programming rate is fast, the thermal efficiency is high, heating-up temperature easily controls that it has.
Disinfection system also has and adopts continuous scraper-type high temperature sterilization, the easy fouling of this type of sterilization mode tube wall and scraper plate wearing and tearing are comparatively large, and the metal dust worn and torn and be easily mixed in underflow raw material; Another kind is that digester belongs to step high temperature sterilization system equipment, inside establish steam pipe coil, because steam is directly contact with the underflow raw material be sterilized, and steam skewness in pot, so raw material is heated also uneven, and can only be a pot a pot of clearance-type come, bactericidal effect and production capacity are affected, and this kind of disinfection system equipment sterilizing time is longer, use rear and easily fouling, not easily CIP cleaning, large-scale pot needs manually to enter cleaning, easily generation accident.
According to the technological requirement of semi-fluid food product processing, now being badly in need of one can make underflow raw material to heat up rapidly, allow steam directly to contact with underflow raw material when sterilization, and sterilizing time is short, bactericidal effect obvious, reduce a kind of disinfection system equipment adopting clean steam directly can heat underflow raw material continuously of labour intensity.
Utility model content
The technical problems to be solved in the utility model is to provide a kind of underflow raw material and steam can be made when sterilization can directly to contact with underflow raw material, and material can be heated equably, and the disinfection system of short, the effective a kind of underflow raw material sterilization of sterilizing time.
For achieving the above object, the technical solution of the utility model is as follows:
A kind of underflow raw material sterilization system, described underflow raw material sterilization system comprises:
One sterilizer main frame, described sterilizer main frame comprise sterilizer main body shell and to be arranged on above sterilizer main body shell one end and with the underflow material inlet pipe of sterilizer main body shell conducting; Described sterilizer main body shell is the cylinder-like structure of inner hollow, and one end of described sterilizer main body shell is underflow material outlet end, and the other end is clean steam arrival end;
The one slurry compensator be connected with sterilizer main frame underflow material inlet pipe, described slurry compensator is for receiving various underflow raw material;
One steam-water separator be connected with sterilizer main frame clean steam arrival end, described steam-water separator is airtight pure air gas receiver, it is responsible for carrying out carbonated drink separation to the high temperature clean steam be input in sterilizer main frame, to obtain dry high temperature clean steam;
One is arranged on the basket type duplex strainer between slurry compensator and sterilizer main frame, and the underflow raw material that described basket type duplex strainer is responsible for flowing to slurry compensator sterilizer filters;
One dehvery pump, described dehvery pump is responsible for the underflow feedstock transportation in slurry compensator to sterilizer;
One switch board, described switch board is responsible for controlling the start and stop of dehvery pump and the start and stop of steam-water separator;
One valve group, one end of described valve group is connected with sterilizer main frame underflow material outlet end, and the other end is connected with slurry compensator material inlet end;
One balances tank connected Pyatyi dilatation noise reduction steam heater with slurry.
In an embodiment of utility model, described sterilizer main frame also comprises:
One clean steam pipe, described clean steam pipe is the tubular structure of the directed steam jetting hole of one end band, other end opening; It is inner that the sealed end of described clean steam pipe is placed in sterilizer main body shell through the clean steam arrival end of sterilizer main body shell, and it is outside that the openend of clean steam pipe is positioned at sterilizer main body shell, and be connected with steam-water separator by flexible pipe; The sealed end of described clean steam pipe is provided with several vapor injection port;
One underflow raw material delivery outlet, described underflow raw material delivery outlet is connected with the underflow material outlet end of sterilizer main body shell, and passes through flange seal;
One heat-proof device for underflow raw material and clean steam pipe are separated, described heat-proof device is made up of vacuum heat-insulation chamber and vacuum heat-insulation chamber mounting seat; Described vacuum heat-insulation chamber be wrapped in be positioned at sterilizer main body shell clean steam pipe on, clean steam pipe racks has the sealed end of vapor injection port to be positioned at the outside in vacuum heat-insulation chamber; The one end in vacuum heat-insulation chamber is fixed on clean steam arrival end, the other end is fixed in the mounting seat of vacuum heat-insulation chamber, described vacuum heat-insulation chamber mounting seat is vertically arranged in sterilizer main body shell, and sterilizer main body shell is divided into inside and outside two parts, described vacuum heat-insulation chamber mounting seat is provided with several and is communicated with the two-part runner in sterilizer main body shell left and right;
One mixing baffle assembly, described mixing baffle assembly is made up of some pieces of baffle plates, baffle spacer and baffle spacer base, described baffle plate is vertically arranged in sterilizer main body shell, and sterilizer main body shell is separated into some sections, baffle spacer runs through the middle part of baffle plate, and wherein one end is fixed on baffle spacer base, described baffle spacer base is fixed on the underflow material outlet end of sterilizer main body shell;
Described every block baffle plate is equipped with the through hole that several dislocation are different with pore size.
In an embodiment of the present utility model, described underflow raw material follower is funnel-shaped structure.
In an embodiment of the present utility model, described sterilizer main body shell is processed into by 316L stainless steel material.
In an embodiment of the present utility model, on described every block baffle plate the blowing angle of through hole and shape all different.
In an embodiment of the present utility model, described slurry compensator is a back taper tank body, the bottom of described slurry compensator is slurry conical discharge port, and top is partly uncap with the open-type of CIP shower nozzle, and the top of described slurry compensator, middle part, bottom are equipped with liquid level gauge; The sidewall of described slurry compensator is provided with charging aperture, feedback outlet and water inlet, and described discharging opening is connected with dehvery pump.
In an embodiment of the present utility model, the side, middle part of described steam-water separator is provided with air intake, and described air intake is connected with extraneous steam generator; The top of steam-water separator is provided with clean steam venthole, and described clean steam venthole is connected with sterilizer clean steam arrival end; The bottom of steam-water separator is provided with condensate drain outlet.
In an embodiment of the present utility model, described basket type duplex strainer comprises filter housings, the filter screen indigo plant bucket be arranged in filter housings, be arranged on the filter outlet bottom filter housings, the filter inlet be arranged on side, filter housings top, the filter end cap being arranged on filter housing top and the fixing ear lock be fixed filter end cap; Described filter inlet is connected with dehvery pump, and described filter outlet is connected with sterilizer underflow material inlet pipe.
In an embodiment of the present utility model, described basket type duplex strainer also comprises a hand basket handle, and described hand basket handle is arranged on filter housings.
In an embodiment of the present utility model, described Pyatyi dilatation noise reduction steam heater comprises housing, is distributed on four pieces of perforated plates of enclosure interior, arranges the clear water entrance of case top, the hot water outlet being arranged on housing bottom and the steam inlet be arranged on case top side; Described clear water entrance is connected with extraneous water supply installation, and described hot water outlet is connected with the water inlet on slurry compensator, and described steam inlet is connected with extraneous steam generator.
By technique scheme, the beneficial effects of the utility model are:
The utility model underflow raw material sterilization system is adopt steam directly to enter in underflow raw material when high temperature sterilization, and be a kind of heater that is airtight, that can pressurize, the food of pasteurization is needed to be sealed in sterilizer main body shell, sterilizing time is short, online CIP cleaning can be carried out to whole system after sterilization completes, labour intensity can be reduced and save the production time.
The utility model its be mainly the features such as programming rate is fast, the thermal efficiency is high, heating-up temperature easily controls; Because steam is directly contact with the underflow raw material be sterilized, steam distributes more even in sterilizer main body shell, so underflow raw material is heated also more even, and bactericidal effect is in tolerance interval, be therefore applicable to the semi-fluid food product such as cheese, all kinds of meat pulp, all kinds of chafing dish seasonings chemical industry.
Accompanying drawing explanation
In order to be illustrated more clearly in the utility model embodiment or technical scheme of the prior art, be briefly described to the accompanying drawing used required in embodiment or description of the prior art below, apparently, accompanying drawing in the following describes is only embodiments more of the present utility model, for those of ordinary skill in the art, under the prerequisite not paying creative work, other accompanying drawing can also be obtained according to these accompanying drawings.
Fig. 1 is the utility model underflow raw material sterilization system process figure;
Fig. 2 is the utility model sterilizer main machine structure schematic diagram;
Fig. 3 is the utility model clean steam tubular construction schematic diagram;
Fig. 4 is the part-structure schematic diagram of the utility model mixing baffle assembly.
Fig. 5 is the utility model slurry compensator structural representation;
Fig. 6 is the utility model steam-water separator structural representation;
Fig. 7 is the utility model duplex strainer structural representation;
Fig. 8 is the utility model Pyatyi dilatation noise reduction steam heater structural representation.
Numeral and the corresponding component title represented by letter in figure:
100, sterilizer main body shell 110, underflow material outlet end 120, clean steam arrival end 130, underflow material inlet pipe 140, clean steam pipe 141, sealed end 141a, vapor injection port 142, openend 150, underflow material outlet end 160, vacuum heat-insulation chamber 161, vacuum heat-insulation chamber mounting seat 161a, runner 170, mixing baffle assembly 171, baffle plate 171a, through hole 172, baffle spacer 173, baffle spacer base 173a, through hole 180, flange,
200, slurry compensator 210, slurry conical discharge port 220, open-type partly uncap 230, CIP shower nozzle 240, charging aperture 250, feedback outlet 260, water inlet;
300, steam-water separator 310, air intake 320, clean steam venthole 330, condensate drain outlet;
400, filter housings 410, filter screen indigo plant bucket 420, filter outlet 430, filter inlet 440, filter end cap 450, fixing ear lock 460, hand basket handle;
500, housing 510, perforated plate 520, clear water entrance 530, hot water outlet 540, steam inlet 550, steam expansion chamber.
Detailed description of the invention
The technological means realized to make the utility model, creation characteristic, reaching object and effect is easy to understand, below in conjunction with concrete diagram, setting forth the utility model further.
See shown in Fig. 1 to Fig. 8, the utility model discloses a kind of underflow raw material sterilization system, underflow raw material sterilization system comprises sterilizer main frame, the slurry compensator 200 be connected with the underflow material inlet pipe on sterilizer main frame, the steam-water separator 300 be connected with the clean steam arrival end on sterilizer main frame, be arranged on the basket type duplex strainer between slurry compensator and sterilizer main frame, be responsible for the underflow feedstock transportation in slurry compensator to the dehvery pump of sterilizer main frame, be responsible for controlling the switch board of control signal in dehvery pump start and stop and whole system and operated pneumatic valve, one end is connected with the underflow material outlet end on sterilizer main frame, the valve group that the other end is connected with slurry compensator material inlet end and balance tank connected Pyatyi dilatation noise reduction steam heater with slurry.
The utility model sterilizer main frame comprise sterilizer main body shell 100 that 316L stainless steel is processed into and to be arranged on above sterilizer main body shell 100 one end and with the underflow material inlet pipe 130 of sterilizer main body shell 100 conducting; Sterilizer main body shell 100 is the inner hollow cylinder-like structure be processed into by 316L stainless steel, and one end of sterilizer main body shell 100 is underflow material outlet end 110, and the other end is clean steam arrival end 120; Sterilizer main body shell intensity and anticorrosive property all relatively good, underflow raw material sterilization use that acid (alkalescence) is stronger can be adapted to; Underflow material inlet pipe is connected with extraneous underflow feedstock pump.
Sterilizer main frame on the utility model also comprise the clean steam pipe 140 be arranged in sterilizer main body shell 100, the underflow raw material follower 150 be connected with sterilizer main body shell underflow material outlet end 110, for the heat-proof device that underflow raw material and clean steam pipe 140 are separated and the mixing baffle assembly 170 be arranged in sterilizer main body shell.
Clean steam pipe 140 is the sealed end 141 of one end with vapor injection port, the tubular structure of other end opening; It comprises openend 142 and sealed end 141, the clean steam arrival end 120 that the sealed end 141 of clean steam pipe 140 passes sterilizer main body shell is placed in sterilizer main body shell inside, the openend 142 of clean steam pipe 140 is positioned at sterilizer main body shell outside, and is connected with steam-water separator by pipeline; The sealed end 141 of clean steam pipe is provided with several vapor injection port 141a; This vapor injection port 141a can carry out mixing and the object reaching sterilization by the underflow raw material sent here with extraneous underflow feedstock pump in sterilizer main body shell that is ejected into by steam direction and location and at a high speed.
Underflow raw material delivery outlet 150 on sterilizer main frame is connected with the underflow material outlet end 110 of sterilizer main body shell, sealed by flange 180 between the two, underflow raw material delivery outlet 150 on sterilizer main frame is funnel-shaped structure, and the underflow raw material follower of funnel-shaped structure can be convenient to the outflow of underflow raw material after sterilization.
Because vapor (steam) temperature is higher, clean steam pipe 140 directly contacts can produce scale formation with underflow raw material in sterilizer main body shell 100, in order to solve this problem, the outside added with vacuum heat-proof device of the clean steam pipe of the utility model in sterilizer main body shell 100, this vacuum heat insulation device is that being conducive to of vacuumizing is heat insulation, can effectively stop fouling to occur, vacuum heat insulation device is made up of vacuum heat-insulation chamber 160 and vacuum heat-insulation chamber mounting seat 161, vacuum heat-insulation chamber 160 be wrapped in be positioned at sterilizer main body shell clean steam pipe 140 on, clean steam pipe 140 is positioned at the outside in vacuum heat-insulation chamber 160 with the sealed end 141 of steam jetting hole 141a, the one end in vacuum heat-insulation chamber 160 is fixed on clean steam arrival end place 120, the other end to be fixed in the mounting seat of vacuum heat-insulation chamber 161, vacuum heat-insulation chamber mounting seat 161 is vertically arranged in sterilizer main body shell, and sterilizer main body shell is divided into inside and outside two parts, described clean steam pipe 140 one end is arranged in heat-insulation chamber mounting seat 161, the position, top of the other end is provided with several directed clean steam spray-hole 141a, vacuum heat-insulation chamber mounting seat 161 is provided with several and is communicated with two-part runner 161a inside and outside sterilizer main body shell, underflow raw material can flow in sterilizer main body shell inner space from sterilizer main body shell outer space by runner 161a, thus carry out mixing sterilization with the steam that vapor injection port ejects.
Mixing baffle assembly 170 is provided with a baffle spacer 172 by 7 pieces of baffle plates 171, centre and baffle spacer base 173 forms, 7 pieces of baffle plates 171 are vertically distributed in sterilizer main body shell 100, and sterilizer main body shell is separated into several cavitys, baffle spacer 172 runs through the middle part of baffle plate 171, wherein one end is fixed in the middle part of the baffle plate of low order end, the other end is fixed on the middle part of baffle spacer base 173, baffle spacer base 173 is fixed on the underflow material outlet end 110 of sterilizer main body shell, is fixed between the two by flange; Above-mentioned every block baffle plate 171 is equipped with the through hole 171a that several blowing angles and dislocation hole and shape are also different, underflow raw material can flow to different directions by after these through holes, so just, make the underflow raw material entered in sterilizer main body shell can fully contact with steam, improve the efficiency of sterilization.
The utility model slurry compensator 200 is for receiving various underflow raw material; Slurry compensator 200 is a back taper tank body, the bottom of slurry compensator 200 is slurry conical discharge port 210, top is partly uncap 220 with the open-type of CIP shower nozzle 230, and the top of slurry compensator 200, middle part, bottom are equipped with liquid level gauge (not shown in FIG.); The sidewall of slurry compensator 200 is provided with charging aperture 240, feedback outlet 250 and water inlet 260, and slurry conical discharge port 210 is connected with dehvery pump.
The utility model steam-water separator 300 is airtight pure air gas receiver, and it is responsible for carrying out carbonated drink separation to the high temperature clean steam be input in sterilizer main frame, to obtain the saturated vapor of dry high temperature cleaning; The side, middle part of steam-water separator 300 is provided with air intake 310, and air intake 310 is connected with extraneous steam generator; The top of steam-water separator 300 is provided with clean steam venthole 320, and clean steam venthole 320 is connected with the clean steam arrival end on sterilizer main frame; The bottom of steam-water separator 300 is provided with condensate drain outlet 330.
The underflow raw material that the utility model basket type duplex strainer is responsible for flowing to slurry compensator sterilizer main frame filters; Basket type duplex strainer comprises filter housings 400, the filter screen indigo plant bucket 410 be arranged in filter housings 400, be arranged on the filter outlet 420 bottom filter housings 400, the filter inlet 430 be arranged on side, filter housings 400 top, the filter end cap 440 being arranged on filter housing top and the fixing ear lock 450 be fixed filter end cap; Filter inlet is connected with dehvery pump, and filter outlet is connected with the underflow material inlet pipe on sterilizer main frame; Duplex strainer also comprises a hand basket handle 460, and hand basket handle 460 is arranged on filter housings.
The steam inlet 540 that the utility model Pyatyi dilatation noise reduction steam heater comprises housing 500, is distributed on four pieces of perforated plates 510 of housing 500 inside, arranges the clear water entrance 520 of case top, is arranged on the hot water outlet 530 of housing bottom and is arranged on case top side; Housing 500 is divided into five steam expansion chambeies 550 by four pieces of perforated plates 510, and clear water entrance is connected with extraneous water supply installation, and hot water outlet 530 is connected with the water inlet 260 on slurry compensator, and steam inlet is connected with extraneous steam generator.
Operation principle of the present utility model is as follows:
First cold underflow raw material is sent in slurry compensator 200 by extraneous dehvery pump from the charging aperture 240 of slurry compensator 200, underflow raw material enters after in slurry compensator, namely dehvery pump and steam-water separator 300 is started by switch board, underflow raw material in slurry compensator 200 is delivered in basket type duplex strainer and is filtered by dehvery pump, and the slurry feedstock after filtration enters into sterilizer main frame from duplex strainer outlet 420, now extraneous steam generator also works, the steam produced enters into steam-water separator 300 and carries out carbonated drink separation, last steam enters in clean steam pipe 140 from steam-water separator Vapor outlet 320, then be ejected in sterilizer main body shell 100 by the vapor injection port 141a of clean steam pipe 140 sealed end 141 on sterilizer main frame, underflow raw material pumps to after in underflow material inlet pipe 130 and enters in sterilizer main body shell 100 by underflow material inlet pipe 130, and then in the inner side cavity being entered into sterilizer main body shell 100 by vacuum heat-insulation chamber outboard chambers with steam sterilization, underflow raw material now can accelerate the mixing velocity with steam by the through hole 171a on baffle plate 171, accelerate germicidal efficiency, finally, the underflow raw material reaching sterilization temperature is discharged by the underflow raw material delivery outlet 150 on sterilizer main frame, the underflow raw material not reaching sterilization temperature is then turned back in underflow material equilibrium tank 200 by valve group and carries out recycling sterilizing, till reaching sterilization temperature, water liftout state can be directly carried out after sterilization completes, when the slurry liquid level in underflow material equilibrium tank 200 arrives low liquid level (liquid level gauge is measured), namely the moisturizing valve input clear water at water inlet 260 place is opened (if need also hot water to be inputted according to technological requirement, when needs input hot water, the steam valve of Pyatyi dilatation noise reduction carbonated drink blender steam inlet 540 can be opened, can be heated by Pyatyi dilatation noise reduction carbonated drink blender), with water, underflow raw material is ejected from pipeline, after underflow raw material is all ejected, CIP can be entered and clean state, in underflow material equilibrium tank, add appropriate high alkali liquid, wash cycles, if temperature does not reach 80 degree, steam can be supplemented and heat, build after industry wash cycles completes, need use water to be ejected by the alkali lye in whole system equipment and drain, and then in underflow material equilibrium tank, add appropriate concentrated acid liquid, wash cycles, if temperature does not reach 80 degree, steam can be supplemented and heat, after same acid cycle has cleaned, also with water the acid solution in whole system equipment ejected and drain, finally drain valve in system is opened and drain all devices and ducted surplus water.
More than show and describe general principle of the present utility model and principal character and advantage of the present utility model.The technical staff of the industry should understand; the utility model is not restricted to the described embodiments; what describe in above-described embodiment and description just illustrates principle of the present utility model; under the prerequisite not departing from the utility model spirit and scope; the utility model also has various changes and modifications, and these changes and improvements all fall within the scope of claimed the utility model.The claimed scope of the utility model is defined by appending claims and equivalent thereof.
Claims (10)
1. a underflow raw material sterilization system, is characterized in that, described underflow raw material sterilization system comprises:
One sterilizer main frame, described sterilizer main frame comprise sterilizer main body shell and to be arranged on above sterilizer main body shell one end and with the underflow material inlet pipe of sterilizer main body shell conducting; Described sterilizer main body shell is the cylinder-like structure of inner hollow, and one end of described sterilizer main body shell is underflow material outlet end, and the other end is clean steam arrival end;
The one slurry compensator be connected with sterilizer main frame underflow material inlet pipe, described slurry compensator is for receiving various underflow raw material;
One steam-water separator be connected with sterilizer main frame clean steam arrival end, described steam-water separator is airtight pure air gas receiver, it is responsible for carrying out carbonated drink separation to the high temperature clean steam be input in sterilizer main frame, to obtain dry high temperature clean steam;
One is arranged on the basket type duplex strainer between slurry compensator and sterilizer main frame, and the underflow raw material that described basket type duplex strainer is responsible for flowing to slurry compensator sterilizer main frame filters;
One dehvery pump, described dehvery pump is responsible for the underflow feedstock transportation in slurry compensator to sterilizer main frame;
One switch board, described switch board is responsible for controlling the start and stop of control signal in the start and stop of dehvery pump and whole system and operated pneumatic valve;
One valve group, one end of described valve group is connected with sterilizer main frame underflow material outlet end, and the other end is connected with slurry compensator material inlet end;
One balances tank connected Pyatyi dilatation noise reduction steam heater with slurry.
2. a kind of underflow raw material sterilization system according to claim 1, it is characterized in that, described sterilizer main frame also comprises:
One clean steam pipe, described clean steam pipe is the tubular structure of the directed steam jetting hole of one end band, other end opening; It is inner that the sealed end of described clean steam pipe is placed in sterilizer main body shell through the clean steam arrival end of sterilizer main body shell, and it is outside that the openend of clean steam pipe is positioned at sterilizer main body shell, and be connected with steam-water separator by flexible pipe; The sealed end of described clean steam pipe is provided with several directed vapor injection port;
One underflow raw material delivery outlet, described underflow raw material delivery outlet is connected with the underflow material outlet end of sterilizer main body shell, and passes through flange seal;
One heat-proof device for underflow raw material and clean steam pipe are separated, described heat-proof device is made up of vacuum heat-insulation chamber and vacuum heat-insulation chamber mounting seat; Described vacuum heat-insulation chamber be wrapped in be positioned at sterilizer main body shell clean steam pipe on, clean steam pipe racks has the sealed end of vapor injection port to be positioned at the outside in vacuum heat-insulation chamber; The one end in vacuum heat-insulation chamber is fixed on clean steam arrival end, the other end is fixed in the mounting seat of vacuum heat-insulation chamber, described vacuum heat-insulation chamber mounting seat is vertically arranged in sterilizer main body shell, and sterilizer main body shell is divided into inside and outside two parts, described vacuum heat-insulation chamber mounting seat is provided with several and is communicated with the two-part runner in sterilizer main body shell left and right;
One mixing baffle assembly, described mixing baffle assembly is made up of some pieces of baffle plates, baffle spacer and baffle spacer base, described baffle plate is vertically arranged in sterilizer main body shell, and sterilizer main body shell is separated into some sections, baffle spacer runs through the middle part of baffle plate, and wherein one end is fixed on baffle spacer base, described baffle spacer base is fixed on the underflow material outlet end of sterilizer main body shell;
Described every block baffle plate is equipped with the through hole that several dislocation are different with pore size.
3. a kind of underflow raw material sterilization system according to claim 2, is characterized in that, described underflow raw material follower is funnel-shaped structure.
4. a kind of underflow raw material sterilization system according to claim 2, is characterized in that, described sterilizer main body shell is processed into by 316L stainless steel.
5. a kind of underflow raw material sterilization system according to claim 2, is characterized in that, on described every block baffle plate the blowing angle of through hole and shape all different.
6. a kind of underflow raw material sterilization system according to claim 1, it is characterized in that, described slurry compensator is a back taper tank body, the bottom of described slurry compensator is slurry conical discharge port, top is partly uncap with the open-type of CIP shower nozzle, and the top of described slurry compensator, middle part, bottom are equipped with liquid level gauge; The sidewall of described slurry compensator is provided with charging aperture, feedback outlet and water inlet, and described discharging opening is connected with dehvery pump.
7. a kind of underflow raw material sterilization system according to claim 1, it is characterized in that, the side, middle part of described steam-water separator is provided with air intake, and described air intake is connected with extraneous steam generator; The top of steam-water separator is provided with clean steam venthole, and described clean steam venthole is connected with sterilizer clean steam arrival end; The bottom of steam-water separator is provided with condensate drain outlet.
8. a kind of underflow raw material sterilization system according to claim 1, it is characterized in that, described basket type duplex strainer comprises filter housings, the filter screen indigo plant bucket be arranged in filter housings, be arranged on the filter outlet bottom filter housings, the filter inlet be arranged on side, filter housings top, the filter end cap being arranged on filter housing top and the fixing ear lock that filter end cap is fixed; Described filter inlet is connected with dehvery pump, and described filter outlet is connected with sterilizer underflow material inlet pipe.
9. a kind of underflow raw material sterilization system according to claim 8, it is characterized in that, described basket type duplex strainer also comprises a hand basket handle, and described hand basket handle is arranged on screen pack housing.
10. a kind of underflow raw material sterilization system according to claim 1, it is characterized in that, described Pyatyi dilatation noise reduction steam heater comprises housing, is distributed on four pieces of perforated plates of enclosure interior, arranges the clear water entrance of case top, the hot water outlet being arranged on housing bottom and the steam inlet be arranged on case top side; Described clear water entrance is connected with extraneous water supply installation, and described hot water outlet is connected with the water inlet on slurry compensator, and described steam inlet is connected with extraneous steam generator.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420512161.4U CN204090948U (en) | 2014-09-05 | 2014-09-05 | A kind of underflow raw material sterilization system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420512161.4U CN204090948U (en) | 2014-09-05 | 2014-09-05 | A kind of underflow raw material sterilization system |
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| CN204090948U true CN204090948U (en) | 2015-01-14 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201420512161.4U Withdrawn - After Issue CN204090948U (en) | 2014-09-05 | 2014-09-05 | A kind of underflow raw material sterilization system |
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104187226A (en) * | 2014-09-05 | 2014-12-10 | 上海数郜机电有限公司 | Strong pulp raw material sterilization system |
| CN105822603A (en) * | 2016-05-17 | 2016-08-03 | 江苏新美星包装机械股份有限公司 | UHT balance tank |
-
2014
- 2014-09-05 CN CN201420512161.4U patent/CN204090948U/en not_active Withdrawn - After Issue
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104187226A (en) * | 2014-09-05 | 2014-12-10 | 上海数郜机电有限公司 | Strong pulp raw material sterilization system |
| CN105822603A (en) * | 2016-05-17 | 2016-08-03 | 江苏新美星包装机械股份有限公司 | UHT balance tank |
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