CN201093469Y - Hydrogen chloride synthesis stove by-product steam apparatus - Google Patents
Hydrogen chloride synthesis stove by-product steam apparatus Download PDFInfo
- Publication number
- CN201093469Y CN201093469Y CNU2007200968959U CN200720096895U CN201093469Y CN 201093469 Y CN201093469 Y CN 201093469Y CN U2007200968959 U CNU2007200968959 U CN U2007200968959U CN 200720096895 U CN200720096895 U CN 200720096895U CN 201093469 Y CN201093469 Y CN 201093469Y
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- CN
- China
- Prior art keywords
- synthetic furnace
- hydrogen chloride
- control device
- chuck
- byproduct steam
- 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
A chlorine hydride synthetic furnace byproduct steam device relates to a process unit, comprising a graphitic synthetic furnace, a hydrogen inlet, a chlorine inlet, a chlorine hydride outlet, a liquid level control device and a pressure control device; the graphitic synthetic furnace is externally provided with a jacket, the outer side of which is provided with a return conduit which is communicated and connected with the jacket; the return conduit is connected with a water inlet pipe which is provided with a gauging device and the liquid level control device; the top of the jacket is provided with the pressure control device. The chlorine hydride synthetic furnace byproduct steam device makes use of the heat generated by the combustion of the synthetic furnace to product steam in a way of byproduct, reduces the waste of energy and achieves the purpose of the utility model.
Description
Affiliated technical field
The utility model relates to a kind of process unit, and more particularly, it is a kind of process unit that makes the hydrogen chloride graphite synthesis furnace byproduct steam.
Background technology
Hydrogen chloride graphite synthesis furnace is a device of producing hydrogen chloride, can produce big calorimetric in course of reaction, generally speaking, all uses recirculated water to take away reaction heat, and the waste that this has caused the energy greatly is unfavorable for the saving of producing.
Summary of the invention
The purpose of this utility model is in order to overcome the deficiencies in the prior art, a kind of device that utilizes hydrogen chloride synthetic furnace to produce steam to be provided.In order to achieve the above object, the technical solution adopted in the utility model is:
A kind of hydrogen chloride synthetic furnace byproduct steam device, comprise graphitic synthetic furnace, hydrogen inlet, chlorine inlet, hydrogen chloride outlet, fluid level control device, pressure control device, described graphitic synthetic furnace is provided with chuck outward, and the chuck lateral wall is provided with return duct, and is connected with the chuck perforation.
The utility model hydrogen chloride synthetic furnace byproduct steam device, described return duct connects water inlet pipe, and water inlet pipe is provided with metering device and fluid level control device.
The utility model hydrogen chloride synthetic furnace byproduct steam device, described chuck confluent liquid level is 20～80%, vaporizer is formed on its top.
The utility model hydrogen chloride synthetic furnace byproduct steam device, described return duct diameter are 0.5～3 times of synthetic furnace chuck sectional area.
In the utility model, increase after the return duct, flow because the density contrast of water produces, form steam at vaporizer, water inlet liquid level fluid level control device is regulated automatically.Discharge of steam realizes automatically that by pressure control device 0.1～0.2MPa is set in the steam extraction.
The heat that the utility model utilizes the synthetic furnace burning to produce is come byproduct steam, has reduced the waste of the energy, has reached the purpose of this utility model.
Description of drawings
Fig. 1 is the utility model structural representation.
1. graphitic synthetic furnaces among the figure; 2. hydrogen inlet; 3. chlorine enters the mouth; 4. return duct; 5. vaporizer; 6. hydrogen chloride outlet; 7. fluid level control device; 8. pressure control device; 9. metering device; 10. chuck.
The specific embodiment
Below in conjunction with accompanying drawing the utility model is specified, by accompanying drawing as can be known, the utility model comprises graphitic synthetic furnace, hydrogen inlet, chlorine inlet, hydrogen chloride outlet, fluid level control device, pressure control device, graphitic synthetic furnace is provided with chuck outward, the chuck outside is provided with chuck and connects the return duct that is connected, return duct connects water inlet pipe, and water inlet pipe is provided with metering device and fluid level control device, is used to control liquid level in the chuck.Be provided with pressure control device at the chuck top, be used to control steam extraction pressure.With the steel chuck graphitic synthetic furnace of φ 1200, the opening of a φ 500 is respectively opened in chuck top and bottom in the utility model, and with the pipeline connection of φ 500, the control confluent is 60% liquid level when normally moving, steam extraction pressure 0.12MPa.
Claims (4)
1. hydrogen chloride synthetic furnace byproduct steam device, comprise graphitic synthetic furnace (1), hydrogen inlet (2), chlorine inlet (3), hydrogen chloride outlet (6), fluid level control device (7), pressure control device (8), it is characterized in that: the outer chuck (10) that is provided with of described graphitic synthetic furnace (1), chuck (10) lateral wall is provided with return duct (4), and is connected with chuck (10) perforation.
2. according to the described hydrogen chloride synthetic furnace byproduct steam of claim 1 device, it is characterized in that: described return duct (4) connects water inlet pipe, and water inlet pipe is provided with metering device (9) and fluid level control device (7).
3. according to the described hydrogen chloride synthetic furnace byproduct steam of claim 1 device, it is characterized in that: described chuck (10) confluent liquid level is 20～80%, and vaporizer (5) is formed on its top.
4. according to the described hydrogen chloride synthetic furnace byproduct steam of claim 1 device, it is characterized in that: described return duct (4) diameter is 0.5～3 times of synthetic furnace chuck (10) sectional area.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200968959U CN201093469Y (en) | 2007-07-27 | 2007-07-27 | Hydrogen chloride synthesis stove by-product steam apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNU2007200968959U CN201093469Y (en) | 2007-07-27 | 2007-07-27 | Hydrogen chloride synthesis stove by-product steam apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201093469Y true CN201093469Y (en) | 2008-07-30 |
Family
ID=39901437
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNU2007200968959U Expired - Fee Related CN201093469Y (en) | 2007-07-27 | 2007-07-27 | Hydrogen chloride synthesis stove by-product steam apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201093469Y (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101830437A (en) * | 2009-05-25 | 2010-09-15 | 肖正群 | Production method and device for synthesizing hydrogen chloride and concentrating alkali by using waste heat |
| CN103079991A (en) * | 2010-07-01 | 2013-05-01 | 西格里碳素欧洲公司 | Apparatus for HCl synthesis with steam raising |
| CN105540544A (en) * | 2015-12-16 | 2016-05-04 | 河南永银化工实业有限公司 | Technical system and method for producing steam through combustion of waste hydrogen in HCL synthesis furnace |
| CN113513742A (en) * | 2021-04-17 | 2021-10-19 | 蔚来热能科技(台州)有限公司 | Energy-saving emission-reducing steam generator and using method thereof |
-
2007
- 2007-07-27 CN CNU2007200968959U patent/CN201093469Y/en not_active Expired - Fee Related
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN101830437A (en) * | 2009-05-25 | 2010-09-15 | 肖正群 | Production method and device for synthesizing hydrogen chloride and concentrating alkali by using waste heat |
| CN103079991A (en) * | 2010-07-01 | 2013-05-01 | 西格里碳素欧洲公司 | Apparatus for HCl synthesis with steam raising |
| CN103079991B (en) * | 2010-07-01 | 2017-11-07 | 西格里碳素欧洲公司 | For HCl synthesis and the device of byproduct steam |
| CN105540544A (en) * | 2015-12-16 | 2016-05-04 | 河南永银化工实业有限公司 | Technical system and method for producing steam through combustion of waste hydrogen in HCL synthesis furnace |
| CN113513742A (en) * | 2021-04-17 | 2021-10-19 | 蔚来热能科技(台州)有限公司 | Energy-saving emission-reducing steam generator and using method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080730 Termination date: 20100727 |