CN203513615U - Efficient combined type shift gas-semiwater gas heat exchanger - Google Patents
Efficient combined type shift gas-semiwater gas heat exchanger Download PDFInfo
- Publication number
- CN203513615U CN203513615U CN201320625490.5U CN201320625490U CN203513615U CN 203513615 U CN203513615 U CN 203513615U CN 201320625490 U CN201320625490 U CN 201320625490U CN 203513615 U CN203513615 U CN 203513615U
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- China
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- heat exchanger
- tube
- gas
- bobbin carriage
- shell
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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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- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Abstract
The utility model discloses an efficient combined type shift gas-semiwater gas heat exchanger. The combined heat exchanger comprises a first tube shell type heat exchanger, a second tube shell type heat exchanger and a middle tube box, wherein the first tube shell type heat exchanger and the second tube shell type heat exchanger are fixedly arranged on two sides of the middle tube box, skirt seats are fixedly arranged at the bottoms of the first tube shell type heat exchanger, the second tube shell type heat exchanger and the middle tube box, the first tube shell type heat exchanger, the second tube shell type heat exchanger and the middle tube box are communicated with one another, and a manhole is formed in the upper end of the middle tube box. According to the efficient combined type shift gas-semiwater gas heat exchanger, the device structure is maximally optimized and simplified, and the production cost is maximally lowered; the length of a process pipeline is maximally reduced, and the losses of power and heating power are maximally reduced; a baffling board is improved as a baffling rod, so that the flow resistance of a medium is maximally reduced on the premise that a baffling effect and a support action are not influenced, and the heat exchanging efficiency is maximally increased; a field utilization space is substantially increased.
Description
Technical field
The utility model relates in the Chemical Manufacture such as nitrogenous fertilizer, methyl alcohol at conversion section, the device structure of the reduction of conversion gas, semi-water gas heat-exchange equipment manufacturing cost and operation energy consumption, particularly a kind of conversion gas, the efficient combination exchanger of semi-water gas.
Background technology
Tube and shell heat exchanger is comprised of bobbin carriage, heat transfer tube, traverse baffle, cylindrical shell and heat exchanger tube sheet conventionally.
At present, there are considerable nitrogenous fertilizer and methanol production enterprise in China, at conversion section, utilizes the waste heat of conversion gas to heat semi-water gas, generally adopts two interchanger.Interchanger is the waste heat preheating semi-water gas utilizing after conversion gas hydrolysis, and another interchanger is that the semi-water gas of waste heat after to preheating that utilizes conversion gas reheats, and such structure had both increased the cost of manufacture of equipment, equipment install take up room large; Owing to being two equipment, by pipeline, connect, energy consumption is large, and heat exchange efficiency is low again, and such structure is no small waste, is also worthless.
Summary of the invention
The purpose of this utility model is that a kind of conversion gas, the efficient combination exchanger of semi-water gas will be provided.
For achieving the above object, the utility model is implemented according to following technical scheme:
A kind of conversion gas, the efficient combination exchanger of semi-water gas, comprise the first tube and shell heat exchanger and the second tube and shell heat exchanger, bobbin carriage in the middle of also comprising, bobbin carriage both sides in the middle of described the first tube and shell heat exchanger and the second tube and shell heat exchanger are fixedly installed on, the first tube and shell heat exchanger, the second tube and shell heat exchanger and middle bobbin carriage bottom arrange skirt and fix, described the first tube and shell heat exchanger, middle bobbin carriage and the mutual UNICOM of the second tube and shell heat exchanger, middle bobbin carriage upper end arranges manhole.
As preferably, described the first tube and shell heat exchanger is comprised of the first bobbin carriage, the first heat transfer tube, the first rod baffle, the first cylindrical shell and First Heat Exchanger tube sheet, described the first cylindrical shell bottom arranges the inlet mouth of water the first conversion gas, the first cylindrical shell top arranges the air outlet of the first conversion gas, the first bobbin carriage top arranges the inlet mouth of semi-water gas, and the first bobbin carriage sidewall arranges sewage draining exit; The second tube and shell heat exchanger is comprised of the second bobbin carriage, the second heat transfer tube, the second rod baffle, the second cylindrical shell and the second heat exchanger tube sheet, described the second cylindrical shell bottom arranges the outlet of the second conversion gas, the second cylindrical shell top arranges the inlet mouth of the second conversion gas, and the sidewall of the second bobbin carriage arranges semi-water gas final outlet.
Compared with prior art, the utility model is optimized to greatest extent, simplified apparatus structure, reduces cost of manufacture; At utmost reduce the length of process pipe, reduce power, thermodynamic loss; Improvement traverse baffle is rod baffle, not affecting under the prerequisite of baffling effect, supporting role, at utmost reduces medium flowing resistance, improves heat exchange efficiency; Increase substantially utilization of area space.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Embodiment
Below in conjunction with accompanying drawing and specific embodiment, the utility model is further described, in illustrative examples and the explanation of this utility model, is used for explaining the utility model, but not as to restriction of the present utility model.
Conversion gas as shown in Figure 1, the efficient combination exchanger of semi-water gas, comprise the first tube and shell heat exchanger and the second tube and shell heat exchanger, bobbin carriage 8 in the middle of also comprising, bobbin carriage 8 both sides in the middle of described the first tube and shell heat exchanger and the second tube and shell heat exchanger are fixedly installed on, it is fixing that the first tube and shell heat exchanger, the second tube and shell heat exchanger and middle bobbin carriage 8 bottoms arrange skirt 15, described the first tube and shell heat exchanger, middle bobbin carriage 8 and the mutual UNICOM of the second tube and shell heat exchanger, middle bobbin carriage 8 upper ends arrange manhole 17.
As preferably, described the first tube and shell heat exchanger is comprised of the first bobbin carriage 14, the first heat transfer tube 13, the first rod baffle 12, the first cylindrical shell 11 and First Heat Exchanger tube sheet 9, described the first cylindrical shell 11 bottoms arrange the inlet mouth 10 of water the first conversion gas, the first cylindrical shell 11 tops arrange the air outlet 18 of the first conversion gas, inlet mouth 19, the first bobbin carriage 14 sidewalls that the first bobbin carriage 14 tops arrange semi-water gas arrange sewage draining exit 20; The second tube and shell heat exchanger is comprised of the second bobbin carriage 2, the second heat transfer tube 5, the second rod baffle 6, the second cylindrical shell 4 and the second heat exchanger tube sheet 3, described the second cylindrical shell 4 bottoms arrange the outlet 7 of the second conversion gas, the sidewall that the second cylindrical shell 4 tops arrange inlet mouth 16, the second bobbin carriages 2 of the second conversion gas arranges semi-water gas final outlet 1.
Middle temperature transformation gas out of hydrolysis stove enters the second heat exchanger tube pass by the inlet mouth 10 of the first conversion gas, from the air outlet 18 of the first conversion gas out process to semi-water gas preheating; The inlet mouth 16 of the second conversion gas of the high temperature shift gas of coming from last process enters First Heat Exchanger shell side, out enters leave from office equipment, to semi-water gas second-heating from the outlet 7 of the second conversion gas.Semi-water gas enters from the inlet mouth 19 of semi-water gas, from semi-water gas final outlet 1, out enter conversion equipment, after second-heating, semi-water gas approaches temperature of reaction and enters conversion equipment and react, and enters Xia Dao workshop section recycling after the utilization of high temperature shift gas.In situation, high, middle temperature transformation gas to semi-water gas heating, is fully used under differing temps, enters Xia Dao workshop section recycling in the situation that pressure drop is less like this.In process, the mobile distance of semi-water gas is short, and thermosteresis is little, and two kinds of conversion gas heat utilization efficiencies are high, and the little pressure drop of resistance is low, and enters smoothly Xia Dao workshop section recycling.The invention of this structure is simple and practical, and cost is low.
The technical solution of the utility model is not limited to the restriction of above-mentioned specific embodiment, and every technology distortion of making according to the technical solution of the utility model, within all falling into protection domain of the present utility model.
Claims (2)
1. a conversion gas, the efficient combination exchanger of semi-water gas, comprise the first tube and shell heat exchanger and the second tube and shell heat exchanger, bobbin carriage (8) in the middle of characterized by further comprising, bobbin carriage (8) both sides in the middle of described the first tube and shell heat exchanger and the second tube and shell heat exchanger are fixedly installed on, it is fixing that the first tube and shell heat exchanger, the second tube and shell heat exchanger and middle bobbin carriage (8) bottom arrange skirt (15), described the first tube and shell heat exchanger, middle bobbin carriage (8) and the mutual UNICOM of the second tube and shell heat exchanger, middle bobbin carriage (8) upper end arranges manhole (17).
2. conversion gas according to claim 1, the efficient combination exchanger of semi-water gas, it is characterized in that: described the first tube and shell heat exchanger is by the first bobbin carriage (14), the first heat transfer tube (13), the first rod baffle (12), the first cylindrical shell (11) and First Heat Exchanger tube sheet (9) form, described the first cylindrical shell (11) bottom arranges the inlet mouth (10) of water the first conversion gas, the first cylindrical shell (11) top arranges the air outlet (18) of the first conversion gas, the first bobbin carriage (14) top arranges the inlet mouth (19) of semi-water gas, the first bobbin carriage (14) sidewall arranges sewage draining exit (20), the second tube and shell heat exchanger is comprised of the second bobbin carriage (2), the second heat transfer tube (5), the second rod baffle (6), the second cylindrical shell (4) and the second heat exchanger tube sheet (3), described the second cylindrical shell (4) bottom arranges the outlet (7) of the second conversion gas, the second cylindrical shell (4) top arranges the inlet mouth (16) of the second conversion gas, and the sidewall of the second bobbin carriage (2) arranges semi-water gas final outlet (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320625490.5U CN203513615U (en) | 2013-10-11 | 2013-10-11 | Efficient combined type shift gas-semiwater gas heat exchanger |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320625490.5U CN203513615U (en) | 2013-10-11 | 2013-10-11 | Efficient combined type shift gas-semiwater gas heat exchanger |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203513615U true CN203513615U (en) | 2014-04-02 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320625490.5U Expired - Fee Related CN203513615U (en) | 2013-10-11 | 2013-10-11 | Efficient combined type shift gas-semiwater gas heat exchanger |
Country Status (1)
| Country | Link |
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| CN (1) | CN203513615U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113670091A (en) * | 2021-08-23 | 2021-11-19 | 哈尔滨锅炉厂有限责任公司 | Heat exchanger utilizing cold energy |
-
2013
- 2013-10-11 CN CN201320625490.5U patent/CN203513615U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN113670091A (en) * | 2021-08-23 | 2021-11-19 | 哈尔滨锅炉厂有限责任公司 | Heat exchanger utilizing cold energy |
| CN113670091B (en) * | 2021-08-23 | 2023-12-26 | 哈尔滨锅炉厂有限责任公司 | Heat exchanger for cold energy utilization |
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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: 20140402 Termination date: 20151011 |
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| EXPY | Termination of patent right or utility model |