CN104324557A - Steam-water separating system - Google Patents
Steam-water separating system Download PDFInfo
- Publication number
- CN104324557A CN104324557A CN201410599286.XA CN201410599286A CN104324557A CN 104324557 A CN104324557 A CN 104324557A CN 201410599286 A CN201410599286 A CN 201410599286A CN 104324557 A CN104324557 A CN 104324557A
- Authority
- CN
- China
- Prior art keywords
- tank body
- steam
- pipe
- gas
- inlet pipe
- 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.)
- Pending
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
- B01D45/08—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by impingement against baffle separators
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B17/00—Sulfur; Compounds thereof
- C01B17/16—Hydrogen sulfides
- C01B17/168—Purification
-
- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B2210/00—Purification or separation of specific gases
- C01B2210/0001—Separation or purification processing
- C01B2210/0009—Physical processing
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Inorganic Chemistry (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
The invention provides a steam-water separating system. The steam-water separating system comprises a steam-water separator, a gas inlet pipe, a gas exhausting pipe, a returning pipe and a gas cabinet, wherein the steam-water separator comprises a tank body; the gas inlet pipe is introduced into the middle part of the tank body; the gas exhausting pipe is introduced into the top part of the steam-water separator; the other end of the gas exhausting pipe is introduced into the gas cabinet; the returning pipe is introduced into the bottom of the tank body; the tail end of the gas inlet pipe, which extends into the tank body, is connected with a bending pipe; and an outlet of the bending pipe faces to the inner side wall of the tank body horizontally. Due to adoption of the technical scheme, the steam-water separating system provided by the invention has the advantage of simple structure and has the beneficial effects that a less amount of condensed water in hydrogen sulfide gas can be separated out to be recovered, and the separated hydrogen sulfide gas is recovered for use in other procedures.
Description
Technical field
The invention 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.
Summary of the invention
The object of the present invention is to provide the simple carbonated drink piece-rate system of a kind of structure, 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 object of the invention is by such technical scheme realize, 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.
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 present invention 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 invention.
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 present invention, creation characteristic, reaching object and effect is easy to understand, below in conjunction with concrete diagram, setting forth the present invention further.
As shown in Figure 1, the present invention includes 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 water inlet pipe 2 stretches into tank body 6 is connected 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 embodiments of the present invention; not thereby the scope of the claims of the present invention is limited; every equivalent structure utilizing description of the present invention and accompanying drawing content to do, is directly or indirectly used in the technical field that other are relevant, all in like manner within scope of patent protection of the present invention.
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 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.
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 |
|---|---|---|---|
| CN201410599286.XA CN104324557A (en) | 2014-10-30 | 2014-10-30 | Steam-water separating system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201410599286.XA CN104324557A (en) | 2014-10-30 | 2014-10-30 | Steam-water separating system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN104324557A true CN104324557A (en) | 2015-02-04 |
Family
ID=52399436
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201410599286.XA Pending CN104324557A (en) | 2014-10-30 | 2014-10-30 | Steam-water separating system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN104324557A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104848198A (en) * | 2015-05-20 | 2015-08-19 | 北京志诚宏业智能控制技术有限公司 | Gravity separation type automatic condensate water collector |
-
2014
- 2014-10-30 CN CN201410599286.XA patent/CN104324557A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104848198A (en) * | 2015-05-20 | 2015-08-19 | 北京志诚宏业智能控制技术有限公司 | Gravity separation type automatic condensate water collector |
| CN104848198B (en) * | 2015-05-20 | 2017-03-08 | 郑志强 | Gravity Separation formula condensed water automatic collector |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20150204 |
|
| WD01 | Invention patent application deemed withdrawn after publication |