CN211147401U - Boil thick liquid heat energy cyclic utilization equipment combination - Google Patents

Boil thick liquid heat energy cyclic utilization equipment combination Download PDF

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Publication number
CN211147401U
CN211147401U CN201922153534.9U CN201922153534U CN211147401U CN 211147401 U CN211147401 U CN 211147401U CN 201922153534 U CN201922153534 U CN 201922153534U CN 211147401 U CN211147401 U CN 211147401U
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thick liquid
ball valve
pulp
interface
pipeline
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CN201922153534.9U
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Chinese (zh)
Inventor
汪志杰
李国强
曾乐
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Boluo Luofushan Ruixin Food Co ltd
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Boluo Luofushan Ruixin Food Co ltd
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Abstract

The utility model discloses a boil thick liquid heat energy cyclic utilization equipment combination, this equipment combination are including allotting the bucket, and this allotment bucket is connected ball valve force (forcing) pump one, and plate heat exchanger is connected to ball valve force (forcing) pump one, and plate heat exchanger connects and boils thick liquid bucket and hot thick liquid filter sieve, and hot thick liquid filter sieve connects ball valve force (forcing) pump two, and the ball valve force (forcing) pump is connected and is deposited thick liquid bucket. The utility model discloses a heat transfer that plate heat exchanger will boil thick liquid in the thick liquid bucket sends out the thick liquid water that gets into plate heat exchanger for allotment bucket for this thick liquid water possesses certain temperature when getting into to boil the thick liquid bucket, thereby reduces to boil thick liquid bucket and boils the required heat energy output of thick liquid, realizes the cyclic utilization of heat energy, the energy saving.

Description

Boil thick liquid heat energy cyclic utilization equipment combination
Technical Field
The utility model relates to a heat energy cyclic utilization field, concretely relates to boil thick liquid heat energy cyclic utilization equipment combination.
Background
With the increasing awareness of environmental protection, energy conservation and emission reduction, more and more enterprises pay attention to the recycling of energy in the production link, including the recycling of heat energy.
Food enterprises need to heat the serous fluid when producing serous fluid type drinks, the former method is that the serous fluid is naturally cooled after being directly heated, and heat energy is dissipated into the air, thus causing waste of heat energy. The utility model discloses a heat transfer that plate heat exchanger will boil thick liquid in the thick liquid bucket sends out the thick liquid water that gets into plate heat exchanger for allotment bucket for this thick liquid water possesses certain temperature when getting into to boil the thick liquid bucket, thereby reduces to boil the thick liquid bucket and boils the required heat of thick liquid, realizes the cyclic utilization of heat energy, the energy saving.
SUMMERY OF THE UTILITY MODEL
An object of the utility model is to provide a boil thick liquid heat energy cyclic utilization equipment combination to solve the problem among the prior art.
In order to achieve the above object, the utility model provides a following technical scheme: a pulp boiling heat energy recycling equipment combination comprises a blending barrel, a ball valve pressure pump I, a plate type heat exchanger, a pulp boiling barrel, a hot pulp filter sieve, a ball valve pressure pump II and a pulp storage barrel. The pipeline of the blending barrel is connected with a ball valve pressure pump; the plate heat exchanger is provided with four interfaces which are respectively an interface I, an interface II, an interface III and an interface IV, wherein the interface I is connected with a ball valve pressure pump I through a pipeline, the interface II is connected with a pulp outlet pipeline of the pulp boiling barrel, the interface III is connected with a pulp inlet pipeline of the pulp boiling barrel, and the interface IV is connected with a pulp inlet pipeline of the hot pulp filter screen; and the slurry outlet of the hot slurry filter screen is connected with a second ball valve pressure pump through a pipeline, and the second ball valve pressure pump is connected with a slurry storage barrel through a pipeline.
Preferably, the first interface and the third interface of the plate heat exchanger are communicated, and the second interface and the fourth interface are communicated.
Preferably, a ball valve is arranged between the connecting pipeline between the third connector and the pulp inlet of the pulp boiling barrel, and a ball valve is also arranged between the second connector and the pulp outlet of the pulp boiling barrel.
The utility model discloses a heat transfer that plate heat exchanger will boil thick liquid in the thick liquid bucket sends out the thick liquid water that gets into plate heat exchanger for allotment bucket for this thick liquid water possesses certain temperature when getting into to boil the thick liquid bucket, thereby reduces to boil thick liquid bucket and boils the required heat energy output of thick liquid, realizes the cyclic utilization of heat energy, the energy saving.
Drawings
Fig. 1 is a schematic structural view of the present invention;
In the figure: 1 blending barrel, 2 ball valve pressure pump I, 3 plate type heat exchanger, 4 ball valve I, 5 pulp boiling barrel, 6 ball valve II, 7 hot pulp filtering sieve, 8 ball valve pressure pump II, 9 pulp storage barrel, 31 interface I, 32 interface III, 33 interface II and 34 interface IV.
Detailed Description
The following will combine the attached drawings in the embodiment of the utility model, to the embodiment of the utility model provides a carry out detailed description, like fig. 1, in the embodiment of the utility model, a boil thick liquid heat energy cyclic utilization equipment combination, this combination is including allotment bucket, ball valve force (forcing) pump one, plate heat exchanger, boil thick liquid bucket, hot thick liquid filter sieve, ball valve force (forcing) pump two and deposit thick liquid bucket. The pipeline of the blending barrel is connected with a first ball valve pressure pump; the plate heat exchanger is provided with four interfaces which are respectively an interface I, an interface II, an interface III and an interface IV, wherein the interface I is connected with a ball valve pressure pump I through a pipeline, the interface II is connected with a pulp outlet pipeline of the pulp boiling barrel, the interface III is connected with a pulp inlet pipeline of the pulp boiling barrel, and the interface IV is connected with a pulp inlet pipeline of the hot pulp filter screen; and the slurry outlet of the hot slurry filter screen is connected with a second ball valve pressure pump through a pipeline, and the second ball valve pressure pump is connected with a slurry storage barrel through a pipeline.
Furthermore, the first interface and the third interface of the plate heat exchanger are communicated, and the second interface and the fourth interface of the plate heat exchanger are communicated.
Furthermore, a ball valve I is arranged between the connecting pipeline of the interface III and the pulp inlet of the pulp boiling barrel, and a ball valve II is arranged between the interface II and the connecting pipeline of the pulp outlet of the pulp boiling barrel.
The utility model discloses a theory of operation is: the pulp water of the blending barrel is pumped into the plate heat exchanger from the first interface by using the ball valve pressure pump, meanwhile, the hot pulp of the pulp boiling barrel enters the plate heat exchanger from the second interface, the two streams of pulp water exchange heat in the heat exchanger, so that the pulp water entering the pulp boiling barrel from the third interface obtains heat, the pulp water which loses heat flows out from the fourth interface enters the hot pulp filter screen, and then is pumped into the pulp storage barrel by using the ball valve pressure pump.
The above description is only for the preferred embodiment of the present invention, and the present invention is not limited to the above description, and although the present invention is disclosed in the preferred embodiment, it is not limited to the above description, and any person skilled in the art can make modifications or changes equivalent to the above disclosed embodiments without departing from the scope of the present invention, but all the modifications, changes and modifications are within the scope of the present invention.

Claims (3)

1. A pulp boiling heat energy recycling equipment combination comprises a blending barrel, a ball valve pressure pump I, a plate type heat exchanger, a pulp boiling barrel, a hot pulp filter sieve, a ball valve pressure pump II and a pulp storage barrel, and is characterized in that the blending barrel is connected with the ball valve pressure pump I through a pipeline; the plate heat exchanger is provided with four interfaces which are respectively an interface I, an interface II, an interface III and an interface IV, wherein the interface I is connected with a ball valve pressure pump I through a pipeline, the interface II is connected with a pulp outlet pipeline of the pulp boiling barrel, the interface III is connected with a pulp inlet pipeline of the pulp boiling barrel, and the interface IV is connected with a pulp inlet pipeline of the hot pulp filter screen; and the slurry outlet of the hot slurry filter screen is connected with a second ball valve pressure pump through a pipeline, and the second ball valve pressure pump is connected with a slurry storage barrel through a pipeline.
2. The combination of claim 1, wherein the first and third ports of the plate heat exchanger are in communication, and the second and fourth ports are in communication.
3. The combination of a device for recycling cooking heat energy as claimed in claim 2, wherein a ball valve is arranged between the connecting pipeline of the third connector and the pulp inlet of the cooking barrel, and a ball valve is arranged between the connecting pipeline of the second connector and the pulp outlet of the cooking barrel.
CN201922153534.9U 2019-12-05 2019-12-05 Boil thick liquid heat energy cyclic utilization equipment combination Active CN211147401U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201922153534.9U CN211147401U (en) 2019-12-05 2019-12-05 Boil thick liquid heat energy cyclic utilization equipment combination

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201922153534.9U CN211147401U (en) 2019-12-05 2019-12-05 Boil thick liquid heat energy cyclic utilization equipment combination

Publications (1)

Publication Number Publication Date
CN211147401U true CN211147401U (en) 2020-07-31

Family

ID=71777464

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201922153534.9U Active CN211147401U (en) 2019-12-05 2019-12-05 Boil thick liquid heat energy cyclic utilization equipment combination

Country Status (1)

Country Link
CN (1) CN211147401U (en)

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