CN204193675U - Carbonated drink piece-rate system - Google Patents
Carbonated drink piece-rate system Download PDFInfo
- Publication number
- CN204193675U CN204193675U CN201420638535.7U CN201420638535U CN204193675U CN 204193675 U CN204193675 U CN 204193675U CN 201420638535 U CN201420638535 U CN 201420638535U CN 204193675 U CN204193675 U CN 204193675U
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- CN
- China
- Prior art keywords
- tank body
- air inlet
- inlet pipe
- steam
- passes
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
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Abstract
The utility model provides a kind of carbonated drink piece-rate system, it comprises steam-water separator, air inlet pipe, blast pipe, return duct and gas holder, described steam-water separator comprises tank body, described air inlet pipe passes in the middle part of tank body, blast pipe passes into steam-water separator top, and the other end of described blast pipe passes into gas holder, and described return duct passes into tank base, the end that described water inlet pipe stretches into tank body is connected with bend pipe, and the outlet level of described bend pipe is towards the madial wall of tank body.Owing to have employed technique scheme, the utility model has the simple advantage of structure, and a small amount of condensed water in hydrogen sulfide gas can be separated and reclaim by it, and reclaims, the hydrogen sulfide gas after being separated for other operations.
Description
Technical field
The utility model belongs to chemical production technical field, particularly a kind of carbonated drink piece-rate system.
Background technology
Can there is carburizing reagent in chemical plant, generate hydrogen sulfide gas, be directly discharged in air, can cause environmental pollution through carburizing reagent in the production process of product.Hydrogen sulfide is colourless, hypertoxic, sour gas.Even the hydrogen sulfide of low concentration, also can damage the sense of smell of people, be fatal with nose as detecting the means of this gas.Therefore a large amount of hydrogen sulfide gas how processing discharge become a problem demanding prompt solution.
Utility model content
The purpose of this utility model is to provide a kind of structure simple carbonated drink piece-rate system, and a small amount of condensed water in hydrogen sulfide gas can be separated and reclaim by it, and reclaims, the hydrogen sulfide gas after being separated for other operations.
The purpose of this utility model is realized by such technical scheme, it comprises steam-water separator, air inlet pipe, blast pipe, return duct and gas holder, described steam-water separator comprises tank body, described air inlet pipe passes in the middle part of tank body, blast pipe passes into steam-water separator top, and the other end of described blast pipe passes into gas holder, and described return duct passes into tank base, the end that described air inlet pipe stretches into tank body part is provided with bend pipe, and the outlet level of described bend pipe is towards the madial wall of tank body.
Hydrogen sulfide gas by air inlet pipe, then enters in steam-water separator through winding pipe exit.Because the outlet level of described bend pipe is towards the madial wall of tank body, hydrogen sulfide beats the madial wall to body through winding pipe exit.Wherein, partial condensation water is adsorbed onto on madial wall after knocking madial wall.Meanwhile, also there is partial vulcanization hydrogen under the reaction of madial wall, clash into inner tank wall all directions, thus condensed water is fully separated with hydrogen sulfide gas.Condensed water along madial wall slowly flow to tank base, and by return line flow to leaching operation recycling.Hydrogen sulfide gas then enters into gas holder by blast pipe and stores, so that recycle at subsequent processing.
Further, in described tank body, the upper horizontal of air inlet pipe is provided with two-layer perforated baffle.
Owing to have employed technique scheme, the utility model has the simple advantage of structure, and a small amount of condensed water in hydrogen sulfide gas can be separated and reclaim by it, and reclaims, the hydrogen sulfide gas after being separated for other operations.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
In figure, 1, steam-water separator; 2, air inlet pipe; 3, blast pipe; 4, return duct; 5, gas holder; 6, tank body; 7, bend pipe; 8, perforated baffle.
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.
As shown in Figure 1, the utility model comprises steam-water separator 1, air inlet pipe 2, blast pipe 3, return duct 4 and gas holder 5, described steam-water separator 1 comprises tank body 6, described air inlet pipe 2 passes in the middle part of tank body 6, blast pipe 3 passes into steam-water separator 1 top, and the other end of described blast pipe 3 passes into gas holder 5, and described return duct 4 passes into bottom tank body 6, the end that described air inlet pipe 2 stretches into tank body 6 part is provided with bend pipe 7, and the outlet level of described bend pipe 7 is towards the madial wall of tank body 6.
Hydrogen sulfide gas by air inlet pipe 2, then enters in steam-water separator 1 through bend pipe 7 outlet.Because the outlet level of described bend pipe 7 is towards the madial wall of tank body 6, hydrogen sulfide exports the madial wall beaten to tank body 6 through bend pipe 7.Wherein, partial condensation water is adsorbed onto on madial wall after knocking madial wall.Meanwhile, also there is partial vulcanization hydrogen under the reaction of madial wall, clash into tank body 6 inwall all directions, thus condensed water is fully separated with hydrogen sulfide gas.Condensed water along madial wall flowing to bottom tank body 6 slowly, and flows to leaching operation recycling by return duct 4.Hydrogen sulfide gas then enters into gas holder 5 by blast pipe 3 and stores, so that recycle at subsequent processing.
As shown in Figure 1, in described tank body 6, the upper horizontal of air inlet pipe 2 is provided with two-layer perforated baffle 8.Hydrogen sulfide exports the madial wall beaten to tank body 6 through bend pipe 7.Wherein, partial condensation water is adsorbed onto on madial wall after knocking madial wall.Meanwhile, also there is partial vulcanization hydrogen under the reaction of madial wall, clash into tank body 6 inwall all directions and perforated baffle 8, thus condensed water is fully separated with hydrogen sulfide gas, strengthen separating effect further.Condensed water along madial wall flowing to bottom tank body 6 slowly, and flows to leaching operation recycling by return duct 4.Hydrogen sulfide gas then enters into gas holder 5 by blast pipe 3 and stores, so that recycle at subsequent processing.
These are only embodiment of the present utility model; not thereby the scope of the claims of the present utility model is limited; every equivalent structure utilizing the utility model description and accompanying drawing content to do; directly or indirectly be used in the technical field that other are relevant, all in like manner within scope of patent protection of the present utility model.
Claims (2)
1. carbonated drink piece-rate system, it is characterized in that, comprise steam-water separator, air inlet pipe, blast pipe, return duct and gas holder, described steam-water separator comprises tank body, and described air inlet pipe passes in the middle part of tank body, and blast pipe passes into steam-water separator top, the other end of described blast pipe passes into gas holder, described return duct passes into tank base, and the end that described air inlet pipe stretches into tank body part is provided with bend pipe, and the outlet level of described bend pipe is towards the madial wall of tank body.
2. carbonated drink piece-rate system as claimed in claim 1, it is characterized in that, in described tank body, the upper horizontal of air inlet pipe is provided with two-layer perforated baffle.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420638535.7U CN204193675U (en) | 2014-10-30 | 2014-10-30 | Carbonated drink piece-rate system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420638535.7U CN204193675U (en) | 2014-10-30 | 2014-10-30 | Carbonated drink piece-rate system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204193675U true CN204193675U (en) | 2015-03-11 |
Family
ID=52651676
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420638535.7U Expired - Fee Related CN204193675U (en) | 2014-10-30 | 2014-10-30 | Carbonated drink piece-rate system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204193675U (en) |
-
2014
- 2014-10-30 CN CN201420638535.7U patent/CN204193675U/en not_active Expired - Fee Related
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150311 Termination date: 20151030 |
|
| EXPY | Termination of patent right or utility model |