CN211998999U - Whey catalytic oxidation processing apparatus - Google Patents

Whey catalytic oxidation processing apparatus Download PDF

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Publication number
CN211998999U
CN211998999U CN202020380473.XU CN202020380473U CN211998999U CN 211998999 U CN211998999 U CN 211998999U CN 202020380473 U CN202020380473 U CN 202020380473U CN 211998999 U CN211998999 U CN 211998999U
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whey
hot water
temperature probe
material tank
pneumatic
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CN202020380473.XU
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Chinese (zh)
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张建强
石慧芳
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Heilongjiang Heyi Dairy Technology Co ltd
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Heilongjiang Heyi Dairy Technology Co ltd
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Abstract

The utility model provides a technical scheme that its technical problem adopted is: the whey catalytic oxidation treatment device comprises a material tank, a pneumatic discharge valve, a centrifugal circulating pump, a flowmeter, a catalyst column ABC, an atomizer, an oxidant feeding device, a pneumatic discharging blow-down valve, a material temperature probe, a hot water pump, an electric heating pipe, a hot water temperature probe and a PLC control electric cabinet. The utility model aims at a whey catalytic oxidation processing apparatus, this kind of whey catalytic oxidation processing apparatus can reduce the organic harmful substance in the whey.

Description

Whey catalytic oxidation processing apparatus
Technical Field
The utility model relates to a structure and the theory of operation of whey catalytic oxidation device, concretely relates to whey catalytic oxidation processing apparatus.
Background
Whey is green and semitransparent liquid separated after casein is coagulated into curd blocks by fresh milk under the action of rennin, 9 kilograms of whey and 1 kilogram of cheese can be produced by ten kilograms of fresh milk, so that a large amount of whey liquid is produced while cheese is industrially produced, antibiotic and pesticide residues in raw milk can be enriched in the whey liquid, the raw milk cannot be fully dispersed into the cheese due to the fact that the raw milk liquid is generally water-soluble substances, and the whey is treated by spraying powder, so that harmful substances are enriched and higher than the original content of the raw milk, and unqualified products and standard exceeding of the harmful substances are caused. A large amount of organic harmful substances are generated: pesticides, antibiotics and the like, wherein organic harmful substances (pesticides and antibiotics) are required to be timely treated through catalytic oxidation reaction during the deep processing of whey liquid, so that the quality of the whey deep-processed product is ensured to meet the quality requirement.
Pesticides and antibiotics are degraded by biological methods and biochemical methods, the degradation process is generally an oxidation process, for example, ozone, hydrogen peroxide, oxidant and the like are utilized, and the degradation process is common in water treatment and purification production. Because the food limits the additives, ozone and hydrogen peroxide are safe to be used for oxidation reaction, and food-grade ozone and hydrogen peroxide are respectively used for sterilization and disinfection in food processing processes such as bottled drinking water, aseptic milk packaging and the like. The efficiency of ozone and hydrogen peroxide is limited, and an advanced oxidation method is used in actual production: the catalyst is added on the basis of ozone and dioxygen to improve the process effect, and the catalyst can be used for ZnO, Zn, Fe, active carbon and the like in food.
The invention discloses a method for degrading harmful substances in catalytically oxidized whey in order to improve the harmful substances enriched in whey, and solves the quality problem of whey products.
Disclosure of Invention
The utility model aims at a whey catalytic oxidation processing apparatus, this kind of whey catalytic oxidation processing apparatus can reduce the organic harmful substance in the whey.
The utility model provides a technical scheme that its technical problem adopted is: the whey catalytic oxidation treatment device comprises a material tank, a pneumatic discharge valve, a centrifugal circulating pump, a flowmeter, a catalyst column ABC, an atomizer, an oxidant feeding device, a pneumatic discharging blow-down valve, a material temperature probe, a hot water pump, an electric heating pipe, a hot water temperature probe and a PLC control electric cabinet.
The export of whey catalytic oxidation processing apparatus material tank bottom among the above-mentioned scheme connects pneumatic ejection of compact blowoff valve, pneumatic bleeder valve respectively through the tee bend, and pneumatic bleeder valve exit linkage centrifugal circulation pump import, the flowmeter import is connected to the centrifugal circulation pump export, and the flowmeter exit linkage catalyst post ABC import, the atomizer at catalyst post ABC export through pipe connection material tank deck portion.
In the scheme, the top and the bottom of the material tank are respectively provided with an oxidant feeding device and a material temperature probe.
In the scheme, the bottom of the interlayer of the material tank is connected with the inlet of a hot water pump through a pipeline, the outlet of the hot water pump is connected with an electric heating pipe, the electric heating pipe is connected with the inlet of the interlayer of the material tank through a pipeline, and a hot water temperature probe is arranged on the pipeline.
The utility model discloses following beneficial effect has:
1. the whey catalytic oxidation treatment device has high automation degree, is convenient for feeding and discharging, and is convenient to clean.
2. The whey catalytic oxidation treatment device has high temperature control precision, and ensures the sustainable and high-efficiency operation of the catalytic oxidation reaction.
3. The whey catalytic oxidation treatment device is compounded with 3 catalyst columns ABC, has the protective filtering effect of the catalyst, and does not cause the phenomenon that catalyst particles are lost into products. Meanwhile, the types and proportions of the fillers in the catalyst column ABC can be replaced according to different reaction substrates, so that the aim of accurate and efficient catalytic oxidation is fulfilled.
Drawings
Fig. 1 is a schematic structural diagram of the present invention, in which: 1 material tank, 2 pneumatic bleeder valves, 3 centrifugal circulation pumps, 4 flowmeters, 5 catalyst columns ABC, 6 atomizers, 7 oxidant feeding devices, 8 pneumatic discharging blow-off valves, 9 material temperature probes, 10 hot water pumps, 11 electric heating pipes, 12 hot water temperature probes and 13PLC control electric cabinets.
Detailed Description
The present invention is further described with reference to fig. 1:
the cheese powder mixing device shown in figure 1 comprises a material tank, a pneumatic discharge valve, a centrifugal circulating pump, a flowmeter, a catalyst column ABC, an atomizer, an oxidant feeding device, a pneumatic discharge blowoff valve, a material temperature probe, a hot water pump, an electric heating pipe, a hot water temperature probe and a PLC control electric cabinet.
The utility model discloses the working process:
whey liquid with the volume of 80% is put into a material tank, food-grade hydrogen peroxide (the proportion is according to the content of pollutants) is added by an oxidant feeding device, active carbon is filled into a catalyst column A, ZnO is filled into a catalyst column B, and Zn is filled into a catalyst column C.
Temperature control operation step: the PLC controls the temperature set on the electric cabinet and then clicks heating start, after the hot water pump is started, the electric heating pipe starts to heat, the hot water temperature probe detects the temperature of the interlayer water in real time, and when the temperature of the interlayer water is smaller than a set value, the electric heating pipe starts to heat; when the water temperature of the interlayer is larger than a set value, the electric heating pipe stops heating.
The catalytic oxidation reaction operation steps are as follows: the material catalytic oxidation is ignited on the PLC control electric cabinet to be started, the pneumatic discharging valve is started, the whey liquid in the material tank enters the catalyst column ABC through the flowmeter under the action of the centrifugal circulating pump, circulation is continuously formed in the reaction process, and the whey after the reaction is returned to the material tank through the atomizer connected with the material tank through the pipeline. Tests show that the degradation rate of the antibiotics in the whey reaches about 99.35%.

Claims (4)

1. Whey catalytic oxidation processing apparatus, its characterized in that: the whey catalytic oxidation treatment device comprises a material tank, a pneumatic discharge valve, a centrifugal circulating pump, a flowmeter, a catalyst column ABC, an atomizer, an oxidant feeding device, a pneumatic discharge blow-down valve, a material temperature probe, a hot water pump, an electric heating pipe, a hot water temperature probe and a PLC control electric cabinet; wherein the pneumatic discharge valve, the centrifugal circulating pump, the oxidant feeding device, the pneumatic discharge blowoff valve, the material temperature probe, the hot water pump, the electric heating pipe and the hot water temperature probe are all controlled by the PLC control electric cabinet.
2. The catalytic whey oxidation treatment apparatus according to claim 1, characterized in that: the export of material tank bottom connects pneumatic ejection of compact blowoff valve, pneumatic bleeder valve respectively through the tee bend, and pneumatic bleeder valve exit linkage centrifugal circulation pump import, the flowmeter import is connected to the centrifugal circulation pump export, and the flowmeter exit linkage catalyst post ABC import, the atomizer at pipe connection material tank deck portion is passed through in the export of catalyst post ABC.
3. The catalytic whey oxidation treatment apparatus according to claim 1, characterized in that: the bottom of the interlayer of the material tank is connected with the inlet of a hot water pump through a pipeline, the outlet of the hot water pump is connected with an electric heating pipe, the electric heating pipe is connected with the inlet of the interlayer of the material tank through a pipeline, and a hot water temperature probe is arranged on the pipeline.
4. The catalytic whey oxidation treatment apparatus according to claim 1, characterized in that: the top and the bottom of the material tank are respectively provided with an oxidant feeding device and a material temperature probe.
CN202020380473.XU 2020-03-16 2020-03-16 Whey catalytic oxidation processing apparatus Active CN211998999U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN202020380473.XU CN211998999U (en) 2020-03-16 2020-03-16 Whey catalytic oxidation processing apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN202020380473.XU CN211998999U (en) 2020-03-16 2020-03-16 Whey catalytic oxidation processing apparatus

Publications (1)

Publication Number Publication Date
CN211998999U true CN211998999U (en) 2020-11-24

Family

ID=73430675

Family Applications (1)

Application Number Title Priority Date Filing Date
CN202020380473.XU Active CN211998999U (en) 2020-03-16 2020-03-16 Whey catalytic oxidation processing apparatus

Country Status (1)

Country Link
CN (1) CN211998999U (en)

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