CN205257996U - Byproduct steam and hydrothermal hydrogen chloride synthesis system - Google Patents
Byproduct steam and hydrothermal hydrogen chloride synthesis system Download PDFInfo
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- CN205257996U CN205257996U CN201521009696.0U CN201521009696U CN205257996U CN 205257996 U CN205257996 U CN 205257996U CN 201521009696 U CN201521009696 U CN 201521009696U CN 205257996 U CN205257996 U CN 205257996U
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- hydrogen chloride
- hot water
- graphite
- synthesis system
- pipeline
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P20/00—Technologies relating to chemical industry
- Y02P20/10—Process efficiency
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Abstract
The utility model belongs to the technical field of the chemical industry equipment, concretely relates to byproduct steam and hydrothermal hydrogen chloride synthesis system, especially a steel stove section of thick bamboo byproduct steam and hydrothermal hydrogen chloride synthesis system, including hydrogen chloride synthesizer, hydrogen chloride synthesizer comprises graphite synthesis section, steam generation section, graphite changeover portion and graphite cooling zone from bottom to top in proper order, synthesis system still including evaporating chamber and the hot -water circulation jar be connected with hydrogen chloride synthesizer respectively. The utility model discloses simple structure, in synthetic hydrogen chloride, make full use of reaction heat, the energy has been practiced thrift greatly to by -product hot water and steam, has improved economic benefits, can extensively promote and use.
Description
Technical field
The utility model belongs to technical field of chemical, is specifically related to the hydrogen chloride synthesis system of a kind of byproduct steam and hot water,The hydrogen chloride synthesis system of especially a kind of steel stove cylinder byproduct steam and hot water.
Background technology
When chlorine reacts generation hydrogen chloride with burning form with hydrogen in synthetic furnace, can follow and discharge a large amount of reaction heat, generalIn situation, these heats all use recirculated water to be pulled away, and have greatly caused the waste of the energy, are unfavorable for the saving of producing. Therefore,By above-mentioned heat recovery to energy-saving and emission-reduction, increasing economic efficiency has very important significance.
Summary of the invention
For the problems referred to above, the utility model proposes the hydrogen chloride synthesis system of a kind of byproduct steam and hot water, synthesizing chlorinatedWhen hydrogen, can utilize steam generation by reaction heat and hot water, greatly save the energy, improve economic benefit.
The utility model is mainly by the following technical solutions: the hydrogen chloride synthesis system of a kind of byproduct steam and hot water, comprises chlorinationHydrogen synthetic furnace, hydrogen chloride synthetic furnace is cooling by graphite synthesis stage, steam generation section, graphite changeover portion and graphite successively from bottom to topDuan Zucheng, described synthesis system also comprises the vaporization chamber and the hot water circuit tank that are connected with hydrogen chloride synthetic furnace respectively.
The upper end annular header tank that described vaporization chamber top arranges with steam generation section upper end by tedge is communicated with; DescribedThe lower end annular header tank that vaporization chamber bottom arranges with steam generation section bottom by down-comer is communicated with.
Described hot water circuit pot bottom is communicated with the cooling medium entrance of graphite synthesis stage by pipeline I; Described hot water circuitTank top is communicated with the cooling medium outlet of graphite changeover portion by pipeline II; Pipeline is passed through in the cooling medium outlet of graphite synthesis stageIII is communicated with the cooling medium entrance of graphite changeover portion.
Described vaporization chamber is provided with steam (vapor) outlet and boiler water supplements pipeline.
Described hot water circuit tank is provided with hot water outlet.
Described pipeline I is provided with hot water circulating pump.
Described pipeline I is provided with supplementing water pipeline.
When specific works, hydrogen and chlorine react and generate hydrogen chloride gas in graphite synthesis stage, now, in hot water circuit tankWater enters the cooling medium entrance of graphite synthesis stage by pipeline I and hot water circulating pump, it is realized cooling. Absorb after heatWater exports out from the cooling medium of graphite synthesis stage, and the cooling medium entrance that enters graphite changeover portion along pipeline III is to this sectionHydrogen chloride gas carries out cooling, and the water absorbing after heat is discharged from the cooling medium entrance of graphite changeover portion, and by pipeline, II entersHot water circuit tank, discharges through hot water outlet. Described pipeline I is provided with supplementing water pipeline, can be according to the actual motion of systemSituation is supplemented hot water.
Meanwhile,, heat is passed to steam and send out through entering steam generation section from the cooled hydrogen chloride gas of graphite synthesis stageWater in raw section barrel, water rises after having absorbed the reaction heat of hydrogen chloride gas, assembles and passes through tedge through upper end annular header tankEnter vaporization chamber, part is discharged through steam (vapor) outlet after water is vaporized into steam, and remaining water enters lower end annular by down-comer and catchmentsCase, enters in steam generation section barrel again, and water relies on density contrast constantly to complete self-loopa between vaporization chamber and steam generation section.Recirculated water also cools down high-temp chlorination hydrogen in absorbing heat generation steam, through preliminary cooling hydrogen chloride gasBody continues to rise, and arrives graphite changeover portion, continues the cooling procedure of foregoing graphite changeover portion.
In sum, the utility model is simple in structure, in synthesising hydrogen, takes full advantage of reaction heat, by-product hot waterAnd steam, greatly save the energy, improve economic benefit, can extensively promote and use.
Brief description of the drawings
Fig. 1 is the utility model structural representation;
In figure: 1 is graphite synthesis stage, and 1-1 is cooling medium entrance, 1-2 is cooling medium outlet; 2 is steam generation section,2-1 is upper end annular header tank, and 2-2 is end ring shape header tank; 3 is graphite changeover portion, and 3-1 is cooling medium entrance, and 3-2 isCooling medium outlet; 4 is graphite cooling section; 5 is vaporization chamber, and 5-1 is tedge, and 5-2 is down-comer, and 5-3 is steam (vapor) outlet,5-4 is that boiler water supplements pipeline; 6 is hot water circuit tank, and 6-1 is pipeline I, and 6-2 is pipeline II, and 6-3 is pipeline III, and 6-4 isHot water circulating pump, 6-5 is supplementing water pipeline, 6-6 is hot water outlet.
Detailed description of the invention
A hydrogen chloride synthesis system for byproduct steam and hot water, comprises hydrogen chloride synthetic furnace, and hydrogen chloride synthetic furnace is complied with from bottom to topInferiorly be made up of graphite synthesis stage 1, steam generation section 2, graphite changeover portion 3 and graphite cooling section 4, described synthesis system is also wrappedDraw together the vaporization chamber 5 and the hot water circuit tank 6 that are connected with hydrogen chloride synthetic furnace respectively.
The upper end annular header tank 2-1 that described vaporization chamber 5 tops arrange by tedge 5-1 and steam generation section 2 upper endsBe communicated with; The lower end annular header tank 2-2 that described vaporization chamber 5 bottoms arrange by down-comer 5-2 and steam generation section 2 bottomsBe communicated with.
Described hot water circuit tank 6 bottoms are communicated with the cooling medium entrance 1-1 of graphite synthesis stage 1 by pipeline I6-1; DescribedHot water circuit tank 6 tops export 3-2 by the cooling medium of pipeline II6-2 and graphite changeover portion 3 and be communicated with; Graphite synthesis stage 1Cooling medium outlet 1-2 be communicated with the cooling medium entrance 3-1 of graphite changeover portion 3 by pipeline III6-3.
Described vaporization chamber 5 is provided with steam (vapor) outlet 5-3 and boiler water supplements pipeline 5-4.
Described hot water circuit tank 6 is provided with hot water outlet 6-6.
Described pipeline I6-1 is provided with hot water circulating pump 6-4.
Described pipeline I6-1 is provided with supplementing water pipeline 6-5.
Claims (7)
1. the hydrogen chloride synthesis system of a byproduct steam and hot water, comprise hydrogen chloride synthetic furnace, hydrogen chloride synthetic furnace is made up of graphite synthesis stage (1), steam generation section (2), graphite changeover portion (3) and graphite cooling section (4) from bottom to top successively, it is characterized in that: described synthesis system also comprises the vaporization chamber (5) and the hot water circuit tank (6) that are connected with hydrogen chloride synthetic furnace respectively.
2. the hydrogen chloride synthesis system of a kind of byproduct steam according to claim 1 and hot water, is characterized in that: the upper end annular header tank (2-1) that described vaporization chamber (5) top arranges with steam generation section (2) upper end by tedge (5-1) is communicated with; The lower end annular header tank (2-2) that described vaporization chamber (5) bottom arranges with steam generation section (2) bottom by down-comer (5-2) is communicated with.
3. the hydrogen chloride synthesis system of a kind of byproduct steam according to claim 1 and hot water, is characterized in that: described hot water circuit tank (6) bottom is communicated with the cooling medium entrance (1-1) of graphite synthesis stage (1) by pipeline I (6-1); Described hot water circuit tank (6) top is communicated with the cooling medium outlet (3-2) of graphite changeover portion (3) by pipeline II (6-2); The cooling medium outlet (1-2) of graphite synthesis stage (1) is communicated with the cooling medium entrance (3-1) of graphite changeover portion (3) by pipeline III (6-3).
4. the hydrogen chloride synthesis system of a kind of byproduct steam according to claim 1 and hot water, is characterized in that: described vaporization chamber (5) is provided with steam (vapor) outlet (5-3) and boiler water supplements pipeline (5-4).
5. the hydrogen chloride synthesis system of a kind of byproduct steam according to claim 1 and hot water, is characterized in that: described hot water circuit tank (6) is provided with hot water outlet (6-6).
6. the hydrogen chloride synthesis system of a kind of byproduct steam according to claim 3 and hot water, is characterized in that: described pipeline I (6-1) is provided with hot water circulating pump (6-4).
7. the hydrogen chloride synthesis system of a kind of byproduct steam according to claim 3 and hot water, is characterized in that: described pipeline I (6-1) is provided with supplementing water pipeline (6-5).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521009696.0U CN205257996U (en) | 2015-12-07 | 2015-12-07 | Byproduct steam and hydrothermal hydrogen chloride synthesis system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201521009696.0U CN205257996U (en) | 2015-12-07 | 2015-12-07 | Byproduct steam and hydrothermal hydrogen chloride synthesis system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205257996U true CN205257996U (en) | 2016-05-25 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201521009696.0U Expired - Fee Related CN205257996U (en) | 2015-12-07 | 2015-12-07 | Byproduct steam and hydrothermal hydrogen chloride synthesis system |
Country Status (1)
| Country | Link |
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| CN (1) | CN205257996U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106495099A (en) * | 2016-12-30 | 2017-03-15 | 山东赫达股份有限公司 | There is the byproduct steam hydrogen chloride graphite synthesis furnace of economizer |
| CN107055472A (en) * | 2017-03-09 | 2017-08-18 | 江苏大和氯碱化工有限公司 | A kind of byproduct steam hydrochloric acid synthesis system |
-
2015
- 2015-12-07 CN CN201521009696.0U patent/CN205257996U/en not_active Expired - Fee Related
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106495099A (en) * | 2016-12-30 | 2017-03-15 | 山东赫达股份有限公司 | There is the byproduct steam hydrogen chloride graphite synthesis furnace of economizer |
| CN106495099B (en) * | 2016-12-30 | 2018-06-05 | 山东赫达股份有限公司 | Byproduct steam hydrogen chloride graphite synthesis furnace with economizer |
| CN107055472A (en) * | 2017-03-09 | 2017-08-18 | 江苏大和氯碱化工有限公司 | A kind of byproduct steam hydrochloric acid synthesis system |
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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: 20160525 Termination date: 20191207 |
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| CF01 | Termination of patent right due to non-payment of annual fee |