CN209109150U - A kind of trona brine room temperature carbonization synthesizer - Google Patents
A kind of trona brine room temperature carbonization synthesizer Download PDFInfo
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- CN209109150U CN209109150U CN201821896995.4U CN201821896995U CN209109150U CN 209109150 U CN209109150 U CN 209109150U CN 201821896995 U CN201821896995 U CN 201821896995U CN 209109150 U CN209109150 U CN 209109150U
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- carbon dioxide
- pipeline
- carbonators
- cooled
- room temperature
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Abstract
The utility model discloses a kind of trona brine room temperature carbonization synthesizers, including appliance for applying carbon dioxide, cooled-preheated pipeline and carbonators, the cooled-preheated pipeline is wrapped in the lower part of the carbonators, one end of the cooled-preheated pipeline is connected to the appliance for applying carbon dioxide, the appliance for applying carbon dioxide is for providing low-temperature carbon dioxide, the other end of the cooled-preheated pipeline is connected to by the air inlet of the carbonators bottom end with the carbonators, heat exchange so as to realize liquid carbon dioxide simultaneously is cooling and preheating prepares, carbon dioxide is set to obtain dual utilization, the energy is greatly saved.
Description
Technical field
The utility model relates to technical field of inorganic chemical industry, are carbonized more particularly to a kind of trona brine room temperature and synthesize dress
It sets.
Background technique
The needs to cool are arranged at carbonators lower part, be all in existing method using cooling water pipe around carbonators lower part into
The cooling mode of row, the method needs in addition configuration cooling water circulating device, and needs to expend a large amount of cooling water and offer
The power of cooling water circulation, so can waste water resource and the energy.And has utilize reactant in the prior art
Warm carry out the cooling device of carbonators heat exchange.
Utility model content
The purpose of the utility model is to provide a kind of trona brine room temperature carbonization synthesizers, to solve above-mentioned existing skill
Art there are the problem of, the heat exchange that can be achieved at the same time liquid carbon dioxide is cooling and preheating prepares, and obtains carbon dioxide dual
It utilizes, has greatly saved the energy.
To achieve the above object, the utility model provides following scheme:
The utility model provides a kind of trona brine room temperature carbonization synthesizer, including appliance for applying carbon dioxide,
Cooled-preheated pipeline and carbonators, the cooled-preheated pipeline are wrapped in the lower part of the carbonators, the cooled-preheated pipeline
One end be connected to the appliance for applying carbon dioxide, the appliance for applying carbon dioxide is for providing low-temperature carbon dioxide, institute
The other end for stating cooled-preheated pipeline is connected to by the air inlet of the carbonators bottom end with the carbonators.
Further, the appliance for applying carbon dioxide includes carbon dioxide storage tank and carbon dioxide vaporizing regulators,
The carbon dioxide storage tank is adjusted for storing liquid CO 2, the carbon dioxide storage tank and carbon dioxide vaporization
Device connection is saved, the carbon dioxide vaporizing regulators are connected to one end of the cooled-preheated pipeline.
Further, the carbon dioxide storage tank is connected to by first pipe with the carbon dioxide vaporizing regulators,
The first pipe is equipped with flow control valve.
Further, second pipe, one end of the second pipe and institute are equipped in the carbon dioxide vaporizing regulators
Carbon dioxide storage tank connection is stated, the other end of the second pipe is connected to by third pipeline with the cooled-preheated pipeline,
The second pipe is wavy.
Further, the third pipeline is equipped with the first barometric damper.
Further, the cooled-preheated spiral pipeline is wrapped on the carbonators, and the cooled-preheated pipeline is located at
Carbonators reaction residual liquor workshop section.
Further, the lower part of the carbonators is equipped with dump valve.
Further, the carbonators top is communicated with the feedway of natural lye or trona brine.
Further, the top of the carbonators is connected to by the 4th pipeline with the third pipeline, the 4th pipeline
It is equipped with the second barometric damper.
The utility model achieves following technical effect compared with the existing technology:
Cooling water pipe is replaced with the cooled-preheated pipeline of low-temperature carbon dioxide around carbonators, low temperature two by the utility model
Carbonoxide is after around the cooled-preheated pipeline of carbonators, the heat of carbon dioxide absorption carbonators, cooled-preheated pipeline, a side
Face realizes the preheating to reactant carbon dioxide, on the other hand cools carbonators, and the carbon dioxide after preheating can be from carbon
Change tower bottom end to be passed through in carbonators for reacting, eliminates the use of cooling water in conventional method, realize the double of carbon dioxide
Huge profit is used, and the energy has greatly been saved.
Detailed description of the invention
In order to illustrate the embodiment of the utility model or the technical proposal in the existing technology more clearly, below will be to embodiment
Needed in attached drawing be briefly described, it should be apparent that, the accompanying drawings in the following description is only the utility model
Some embodiments for those of ordinary skill in the art without creative efforts, can also be according to this
A little attached drawings obtain other attached drawings.
Fig. 1 is the structural schematic diagram of trona brine room temperature carbonization synthesizer；
Wherein: 1- carbon dioxide storage tank, 2- flow control valve, 3- first pipe, 4- carbon dioxide vaporizing regulators, 5-
Second pipe, the 4th pipeline of 6-, 7- third pipeline, 8- carbonators, the feedway of the natural lye of 9- or trona brine, 10-
Cooled-preheated pipeline, 11- dump valve, the first barometric damper of 12-, the second barometric damper of 13-.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are in the premise not made the creative labor
Under every other embodiment obtained, fall within the protection scope of the utility model.
The purpose of the utility model is to provide a kind of trona brine room temperature carbonization synthesizers, to solve above-mentioned existing skill
Art there are the problem of, the heat exchange that can be achieved at the same time liquid carbon dioxide is cooling and preheating prepares, and obtains carbon dioxide dual
It utilizes, has greatly saved the energy.
To keep the above objects, features, and advantages of the utility model more obvious and easy to understand, with reference to the accompanying drawing and have
Body embodiment is described in further detail the utility model.
A kind of trona brine room temperature carbonization synthesizer is present embodiments provided as shown in Figure 1:, including carbon dioxide supplies
To device, cooled-preheated pipeline 10 and carbonators 8, cooled-preheated pipeline 10 is spirally wound on the lower part of carbonators 8, is located at carbonization
8 reaction residual liquor workshop section of tower, makes cooled-preheated pipeline 10 sufficiently be exchanged heat with carbonators 8, one end of cooled-preheated pipeline 10
Be connected to appliance for applying carbon dioxide, appliance for applying carbon dioxide for providing low-temperature carbon dioxide, make low-temperature carbon dioxide with
Carbonators 8 carries out heat exchange and carries out cooling effect to carbonators 8, and low-temperature carbon dioxide is heated preheating simultaneously for heat exchange, cold
But the other end of preheating pipe 10 is connected to by the air inlet of 8 bottom end of carbonators with carbonators 8, to heat the dioxy after preheating
Change carbon to enter in carbonators 8 from 8 bottom end of carbonators, 8 top of carbonators is communicated with the supply dress of natural lye or trona brine
Set 9, the lower part of carbonators 8 is equipped with dump valve 11, thus the carbon dioxide and natural lye or trona brine after being preheated into
Row reaction, the reaction solution for reacting completion enter the reaction residual liquor workshop section of 8 lower part of carbonators, utilize in cooled-preheated pipeline 10 two
The cooling of reaction residual liquor workshop section is realized in the heat exchange of carbonoxide.
Specifically, appliance for applying carbon dioxide includes carbon dioxide storage tank 1 and carbon dioxide vaporizing regulators 4, dioxy
Change Carbon stock tank 1 for storing liquid CO 2, carbon dioxide storage tank 1 is connected to carbon dioxide vaporizing regulators 4, dioxy
Change carbon vaporizing regulators 4 to be connected to one end of cooled-preheated pipeline 10.Carbon dioxide storage tank 1 passes through first pipe 3 and dioxy
Change carbon vaporizing regulators 4 to be connected to, first pipe 3 is equipped with flow control valve 2, can adjust carbon dioxide needed for reacting in time
Amount provides enough carbon dioxide to realize different reaction speed controls and to cool down.In carbon dioxide vaporizing regulators 4
Equipped with second pipe 5, one end of second pipe 5 is connected to carbon dioxide storage tank 1, and the other end of second pipe 5 passes through third
Pipeline 7 is connected to cooled-preheated pipeline 10, and second pipe 5 is wavy, to extend the vaporization time of liquid CO 2, is made
Carbon dioxide sufficiently vaporizes, in order to the control of gas concentration lwevel.Third pipeline 7 is equipped with the first barometric damper 12 to adjust
Section and control gas concentration lwevel.Preferably, the top of carbonators 8 is connected to by the 4th pipeline 6 with third pipeline 7, the 4th pipe
Road 6 is equipped with the second barometric damper 13, and the gas concentration lwevel on 8 top of carbonators is lower after reaction, and connection third pipeline 7 passes through
It is recycled again after first barometric damper, 12 adjusting processing, so as to further be utilized to carbon dioxide,
More environmentally friendly, the more saving energy.
It applies specific case in this specification to be expounded the principles of the present invention and embodiment, the above reality
The explanation for applying example is merely used to help understand the method and its core concept of the utility model；Meanwhile for the general of this field
Technical staff, based on the idea of the present invention, there will be changes in the specific implementation manner and application range.To sum up institute
It states, the content of the present specification should not be construed as a limitation of the present invention.
Claims (9)
- The synthesizer 1. a kind of trona brine room temperature is carbonized, it is characterised in that: including appliance for applying carbon dioxide, cooled-preheated Pipeline and carbonators, the cooled-preheated pipeline are wrapped in the lower part of the carbonators, one end of the cooled-preheated pipeline with The appliance for applying carbon dioxide connection, for the appliance for applying carbon dioxide for providing low-temperature carbon dioxide, the cooling is pre- The other end of heat pipeline is connected to by the air inlet of the carbonators bottom end with the carbonators.
- The synthesizer 2. trona brine room temperature according to claim 1 is carbonized, it is characterised in that: the carbon dioxide supplies It include carbon dioxide storage tank and carbon dioxide vaporizing regulators to device, the carbon dioxide storage tank is for storing liquid two Carbonoxide, the carbon dioxide storage tank are connected to the carbon dioxide vaporizing regulators, the carbon dioxide vaporizing regulators It is connected to one end of the cooled-preheated pipeline.
- The synthesizer 3. trona brine room temperature according to claim 2 is carbonized, it is characterised in that: the carbon dioxide storage It deposits tank to be connected to by first pipe with the carbon dioxide vaporizing regulators, the first pipe is equipped with flow control valve.
- The synthesizer 4. trona brine room temperature according to claim 2 is carbonized, it is characterised in that: the carbon dioxide vapour Change and be equipped with second pipe in adjuster, one end of the second pipe is connected to the carbon dioxide storage tank, second pipe The other end in road is connected to by third pipeline with the cooled-preheated pipeline, and the second pipe is wavy.
- The synthesizer 5. trona brine room temperature according to claim 4 is carbonized, it is characterised in that: on the third pipeline Equipped with the first barometric damper.
- The synthesizer 6. trona brine room temperature according to claim 1 is carbonized, it is characterised in that: the cooled-preheated pipe Road is spirally wound on the carbonators, and the cooled-preheated pipeline is located at carbonators reaction residual liquor workshop section.
- The synthesizer 7. trona brine room temperature according to claim 1 is carbonized, it is characterised in that: under the carbonators Portion is equipped with dump valve.
- The synthesizer 8. trona brine room temperature according to claim 1 is carbonized, it is characterised in that: the carbonators top It is communicated with the feedway of natural lye or trona brine.
- The synthesizer 9. trona brine room temperature according to claim 4 is carbonized, it is characterised in that: the top of the carbonators End is connected to by the 4th pipeline with the third pipeline, and the 4th pipeline is equipped with the second barometric damper.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821896995.4U CN209109150U (en) | 2018-11-19 | 2018-11-19 | A kind of trona brine room temperature carbonization synthesizer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201821896995.4U CN209109150U (en) | 2018-11-19 | 2018-11-19 | A kind of trona brine room temperature carbonization synthesizer |
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| Publication Number | Publication Date |
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| CN209109150U true CN209109150U (en) | 2019-07-16 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201821896995.4U Active CN209109150U (en) | 2018-11-19 | 2018-11-19 | A kind of trona brine room temperature carbonization synthesizer |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116902996A (en) * | 2023-09-15 | 2023-10-20 | 山东海化集团有限公司 | Tower opening method of carbonization tower |
-
2018
- 2018-11-19 CN CN201821896995.4U patent/CN209109150U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN116902996A (en) * | 2023-09-15 | 2023-10-20 | 山东海化集团有限公司 | Tower opening method of carbonization tower |
| CN116902996B (en) * | 2023-09-15 | 2024-01-02 | 山东海化集团有限公司 | Tower opening method of carbonization tower |
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