CN208136128U - A kind of calcium propionate production recovery tower - Google Patents
A kind of calcium propionate production recovery tower Download PDFInfo
- Publication number
- CN208136128U CN208136128U CN201820200782.7U CN201820200782U CN208136128U CN 208136128 U CN208136128 U CN 208136128U CN 201820200782 U CN201820200782 U CN 201820200782U CN 208136128 U CN208136128 U CN 208136128U
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- calcium propionate
- tower
- tower body
- water
- sink
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Abstract
The utility model discloses a kind of calcium propionates to produce recovery tower, including the first tower body being arranged from bottom to top, the second tower body and third tower body;It is provided with demarcation plate between second tower body and third tower body, multiple air holes are provided on demarcation plate;Third tower is provided with sparge pipe far from one end of demarcation plate, and the water pipe is sprayed water into calcium propionate production recovery tower.The steam and dust that calcium propionate drying tower top and side come out enter in a kind of calcium propionate production recovery tower of the utility model, since calcium propionate is soluble easily in water, the water that steam and dust containing calcium propionate are sprayed in sparge pipe absorbs, demarcation plate between second tower body and third tower body can be filtered and stop to calcium propionate and steam, guarantee that the water that sparge pipe gushes out comes into full contact with the dust containing calcium propionate and steam, assimilation effect is improved, dust and steam containing calcium propionate is avoided to enter atmosphere.Therefore, a kind of calcium propionate production recovery tower of the utility model has the advantages that environment protecting is good.
Description
Technical field
The utility model relates to calcium propionate production equipments, produce recycling more particularly, to a kind of good calcium propionate of environment protecting
Tower.
Background technique
In existing calcium propionate production process, due to can be generated in calcium propionate granulating and forming and drying process it is a certain amount of containing
The steam and dust of calcium propionate if this some vapor and dust are directly discharged into atmosphere and can generate pollution to environment, and cause wave
Take.
Therefore, it is necessary to a kind of improvement be proposed, to overcome the defect of traditional technology.
Utility model content
The technical problem to be solved by the utility model is to provide a kind of good calcium propionates of environment protecting to produce recovery tower.
To achieve the goals above, a kind of calcium propionate production recovery tower of the utility model uses following technical scheme:
A kind of calcium propionate production recovery tower, including the first tower body being arranged from bottom to top, the second tower body and third tower body, institute
It states the first tower body and is connected with the third tower body by second tower body;It is provided with sink in first tower body, it is described
It is provided with water in sink, is provided with feed inlet above the first tower body sink;Second tower body and the third tower body it
Between be provided with demarcation plate, multiple air holes are provided on the demarcation plate;The third tower body passes through exhaust pipe and external phase
Even, the third tower is provided with sparge pipe far from one end of the demarcation plate, and the sparge pipe is produced to the calcium propionate and recycled
Water spray in tower.
As a kind of perferred technical scheme, the vent diameter is 1cm.
As a kind of perferred technical scheme, the sparge pipe includes two root canals of right-angled intersection design.
As a kind of perferred technical scheme, the sink is connect with the sparge pipe by circulating pump.
As a kind of perferred technical scheme, the water being arranged in the sink is deionized water.
As a kind of perferred technical scheme, liquidometer is provided in the sink.
As a kind of perferred technical scheme, the bottom of gullet is provided with drainpipe.
Steam and dust that calcium propionate drying tower top and side come out enter one kind of the utility model by feed inlet
Calcium propionate produces recovery tower, is provided with water in the sink of the first tower body, the top of third tower body is provided with sparge pipe, due to propionic acid
Calcium is soluble easily in water, and water that steam and dust containing calcium propionate are sprayed in sparge pipe absorbs, the second tower body and third tower body it
Between demarcation plate can calcium propionate and steam be filtered and be stopped to a certain extent, guarantee water that sparge pipe gushes out with
Dust and steam containing calcium propionate come into full contact with, and improve assimilation effect, avoid the dust containing calcium propionate and steam from entering big
Gas.Therefore, a kind of calcium propionate production recovery tower of the utility model has the advantages that environment protecting is good.
Detailed description of the invention
Fig. 1 is the structural schematic diagram that a kind of calcium propionate of the utility model produces recovery tower specific embodiment.
Fig. 2 is that a kind of calcium propionate of the utility model shown in Fig. 1 produces demarcation plate schematic diagram in recovery tower specific embodiment.
Fig. 3 is that a kind of calcium propionate of the utility model shown in Fig. 1 produces sparge pipe schematic diagram in recovery tower specific embodiment.
Specific embodiment
With reference to the accompanying drawing, a kind of specific structure of calcium propionate production recovery tower of the utility model is described in detail.
As shown in Figure 1, a kind of calcium propionate of the utility model produces recovery tower, including set gradually from bottom to top the
One tower body 1, the second tower body 2 and third tower body 3, the first tower body 1 are connected by the second tower body 2 with third tower body 3, the first tower body
It is provided with sink 1a in 1, water is provided in sink 1a, is provided with feed inlet 4, propionic acid above the corresponding sink 1a of the first tower body 1
The steam and dust that calcium drying tower top and side come out enter a kind of calcium propionate production of the utility model by feed inlet 4 and recycle
In tower.As shown in Figure 1, demarcation plate 5 is provided between the second tower body and third tower body 3, as shown in Fig. 2, being provided on demarcation plate 5
Multiple air hole 5a, demarcation plate 5 can to a certain extent stop dust and steam, improve the first tower body 1 and second
The content of dust and steam in tower body 2.As shown in Figure 1, third tower body 3 is communicated with the outside by exhaust pipe 7, third tower body 3
One end far from demarcation plate 5 is provided with sparge pipe 8, and sparge pipe 8 is sprayed water into a kind of calcium propionate production recovery tower of the utility model,
Since calcium propionate is soluble easily in water, sparge pipe 8 into a kind of the utility model calcium propionate production recovery tower water spray can by dust and
Calcium propionate in steam is recycled, and is avoided calcium propionate from entering external environment and is generated pollution to environment.
As a preferred embodiment, the air hole 5a diameter of demarcation plate 5 is 1cm.
As shown in figure 3, in order to improve the water spray effect of sparge pipe, sparge pipe includes two root canals of right-angled intersection setting.
In order to improve water utilization rate, as shown in Figure 1, sink 1a in a kind of calcium propionate production recovery tower of the present embodiment
It is connect by circulating pump 9 with sparge pipe 8.The water sprayed in sparge pipe 8 is the water in the sink 1a extracted by circulating pump 9.
In order to improve water to the assimilation effect of calcium propionate, the interior water being arranged of sink 1a is deionized water.
In order to control the water in sink 1a, preferably, liquidometer 10 is provided in sink 1a.
It is that can enter neutralizing tank progress by drainpipe 1b when the calcium propionate in the water in sink 1a reaches a certain concentration
Processing improves the yield in calcium propionate production process;As shown in Figure 1, drainpipe 1b is set to the bottom sink 1a.
Steam and dust that calcium propionate drying tower top and side come out enter one kind of the utility model by feed inlet
Calcium propionate produces recovery tower, is provided with water in the sink of the first tower body, the top of third tower body is provided with sparge pipe, due to propionic acid
Calcium is soluble easily in water, and water that steam and dust containing calcium propionate are sprayed in sparge pipe absorbs, the second tower body and third tower body it
Between demarcation plate can calcium propionate and steam be filtered and be stopped to a certain extent, guarantee water that sparge pipe gushes out with
Dust and steam containing calcium propionate come into full contact with, and improve assimilation effect, avoid the dust containing calcium propionate and steam from entering big
Gas.Therefore, a kind of calcium propionate production recovery tower of the utility model has the advantages that environment protecting is good.
The above is only the utility model case study on implementation, are not intended to limit the utility model, as long as this field is common
Technical staff's equivalent modification according to made by the utility model disclosure or variation, should all be included in claims and record
Protection scope in.
Claims (7)
1. a kind of calcium propionate produces recovery tower, it is characterised in that:Including the first tower body being arranged from bottom to top, the second tower body and
Three tower bodies, first tower body are connected with the third tower body by second tower body;It is provided in first tower body
Sink is provided with water in the sink, is provided with feed inlet above the first tower body sink;Second tower body and described the
It is provided with demarcation plate between three tower bodies, multiple air holes are provided on the demarcation plate;The third tower body passes through exhaust pipe
It is communicated with the outside, the third tower is provided with sparge pipe far from one end of the demarcation plate, and the sparge pipe is to the calcium propionate
Produce water spray in recovery tower.
2. a kind of calcium propionate according to claim 1 produces recovery tower, it is characterised in that:The vent diameter is 1cm.
3. a kind of calcium propionate according to claim 1 produces recovery tower, it is characterised in that:The sparge pipe includes that cross is handed over
Pitch two root canals of design.
4. a kind of calcium propionate according to claim 1 produces recovery tower, it is characterised in that:The sink and the sparge pipe
It is connected by circulating pump.
5. a kind of calcium propionate according to claim 1 produces recovery tower, it is characterised in that:The water of setting is in the sink
Deionized water.
6. a kind of calcium propionate according to claim 1 produces recovery tower, it is characterised in that:Liquid level is provided in the sink
Meter.
7. a kind of calcium propionate according to claim 1 produces recovery tower, it is characterised in that:The bottom of gullet is provided with row
Water pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN201820200782.7U CN208136128U (en) | 2018-02-06 | 2018-02-06 | A kind of calcium propionate production recovery tower |
Applications Claiming Priority (1)
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CN201820200782.7U CN208136128U (en) | 2018-02-06 | 2018-02-06 | A kind of calcium propionate production recovery tower |
Publications (1)
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CN208136128U true CN208136128U (en) | 2018-11-23 |
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CN201820200782.7U Active CN208136128U (en) | 2018-02-06 | 2018-02-06 | A kind of calcium propionate production recovery tower |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111820408A (en) * | 2019-04-17 | 2020-10-27 | 山东雨田食品科技有限公司 | Production system and production method for simultaneously producing calcium propionate particles and calcium propionate powder |
-
2018
- 2018-02-06 CN CN201820200782.7U patent/CN208136128U/en active Active
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111820408A (en) * | 2019-04-17 | 2020-10-27 | 山东雨田食品科技有限公司 | Production system and production method for simultaneously producing calcium propionate particles and calcium propionate powder |
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GR01 | Patent grant | ||
GR01 | Patent grant | ||
CP03 | Change of name, title or address |
Address after: 277212 No.1, Yinshan Industrial Park, economic development zone, Shanting District, Zaozhuang City, Shandong Province Patentee after: Shandong tongtaiweirun Food Technology Co., Ltd Address before: 277212 East waterlogged village, Cheng tou Town, Shan Ting District, Zaozhuang, Shandong Patentee before: SHANDONG TONGTAIWEIRUN FOOD SCIENCE TECH Co.,Ltd. |
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CP03 | Change of name, title or address |