CN203208715U - Condensed water heat recovery system - Google Patents
Condensed water heat recovery system Download PDFInfo
- Publication number
- CN203208715U CN203208715U CN2013201656146U CN201320165614U CN203208715U CN 203208715 U CN203208715 U CN 203208715U CN 2013201656146 U CN2013201656146 U CN 2013201656146U CN 201320165614 U CN201320165614 U CN 201320165614U CN 203208715 U CN203208715 U CN 203208715U
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- China
- Prior art keywords
- condensed water
- recovery system
- heat recovery
- water heat
- drying room
- 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.)
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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
- Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
- Y02P70/10—Greenhouse gas [GHG] capture, material saving, heat recovery or other energy efficient measures, e.g. motor control, characterised by manufacturing processes, e.g. for rolling metal or metal working
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Abstract
The utility model relates to a condensed water heat recovery system. The condensed water heat recovery system comprises a steam tank, wherein the steam tank is connected with a rectifying tower and a drying room respectively, both the rectifying tower and the drying room are connected with a heating room, and the heating room is connected with a circulating water pool. The condensed water heat recovery system has the advantages that the production cost can be reduced, the waste heat is utilized reasonably, and products with different boiling points are processed effectively.
Description
Technical field
The utility model relates to a kind of recycling system, is specifically related to a kind of hydro-thermal surplus recycling system.
Background technology
In the prior art, when ethylenediamine, T154, T155, MEA, diethanol amine and polyethers are carried out heat treated, all be all to be placed in the drying room to carry out, be arranged in parallel the desulfurizing agent rectifying column in addition of together working with drying room, their preceding road all is to link to each other with vapor can, their back road all can produce condensed water, and these condensed waters all are directly to emit, and the temperature of these condensed waters is about 85 ℃, so both wasted a large amount of hot surpluses, wasted a lot of water resources again, also increased the consumption of steam simultaneously, thereby strengthened production cost.
Summary of the invention
Goal of the invention: the purpose of this utility model is in order to overcome deficiency of the prior art, to provide a kind of and save production cost, rationally utilize hot surplus, effectively handling the condensed water heat recovery system of different boiling product.
Technical scheme: in order to solve the problems of the technologies described above, a kind of condensed water heat recovery system described in the utility model, it comprises vapor can, described vapor can links to each other with drying room with rectifying column respectively, described rectifying column all links to each other with greenhouse with drying room, and described greenhouse links to each other with the recirculated water pond.
Described rectifying column and drying room are arranged in parallel.
Described rectifying column is the desulfurizing agent rectifying column.
Described vapor can is the 1.0MPa vapor can.
In whole heat-treatment process of the present utility model, because the boiling point of ethylenediamine, T154, T155, MEA, diethanol amine and polyethers is different, so T154, T155 and polyethers are put into the drying room heat treated, ethylenediamine, MEA and diethanol amine are put into the greenhouse heat treated.
The temperature of the rectifying column before improving and the back road condensed water of drying room is about 85 ℃, and the temperature of the back road condensed water of the greenhouse after the improvement is about 40 ℃, and these condensed waters directly enter the recirculated water pond.
Beneficial effect: the utility model compared with prior art, its remarkable advantage is: each parts of the utility model are closely connected, safe and reliable to operation, the boiling point difference of heat treating materials as required, material is placed in the drying room and greenhouse of different temperatures, can effectively control the material heating temperature like this, increase work efficiency, the condensed water in road behind rectifying column and the drying room is passed through greenhouse, rationally like this utilized hot surplus, saved cost, the condensed water in road behind the greenhouse has been fed the recirculated water pond, saved water resource, the realistic instructions for use of native system.
Description of drawings
Fig. 1 is structural representation of the prior art
Fig. 2 is structural representation of the present utility model.
Wherein:
1, vapor can; 2, rectifying column; 3, drying room; 4, greenhouse; 5, recirculated water pond
The specific embodiment
Below in conjunction with drawings and Examples the utility model is further described.
As shown in Figure 2, a kind of condensed water heat recovery system described in the utility model, it comprises vapor can 1, and described vapor can 1 links to each other with drying room 3 with rectifying column 2 respectively, and described rectifying column 2 all links to each other with greenhouse 4 with drying room 3, and described greenhouse 4 links to each other with recirculated water pond 5; Described rectifying column 2 and drying room 3 are arranged in parallel; Described rectifying column 2 is the desulfurizing agent rectifying column; Described vapor can 1 is the 1.0MPa vapor can.Each parts of the utility model are closely connected, safe and reliable to operation, the boiling point difference of heat treating materials is placed on material in the drying room and greenhouse of different temperatures as required, can effectively control the material heating temperature like this, increase work efficiency, the condensed water in road behind rectifying column and the drying room by greenhouse, has rationally like this been utilized hot surplus, saved cost, the condensed water in road behind the greenhouse is fed the recirculated water pond, saved water resource, the realistic instructions for use of native system.
The utility model provides a kind of thinking and method; method and the approach of this technical scheme of specific implementation are a lot; the above only is preferred embodiment of the present utility model; should be understood that; for those skilled in the art, under the prerequisite that does not break away from the utility model principle, can also make some improvements and modifications; these improvements and modifications also should be considered as protection domain of the present utility model, in the present embodiment not clear and definite each part all available prior art realized.
Claims (4)
1. condensed water heat recovery system, it is characterized in that: it comprises vapor can (1), described vapor can (1) links to each other with drying room (3) with rectifying column (2) respectively, described rectifying column (2) all links to each other with greenhouse (4) with drying room (3), and described greenhouse (4) links to each other with recirculated water pond (5).
2. condensed water heat recovery system according to claim 1, it is characterized in that: described rectifying column (2) and drying room (3) are arranged in parallel.
3. condensed water heat recovery system according to claim 1, it is characterized in that: described rectifying column (2) is the desulfurizing agent rectifying column.
4. condensed water heat recovery system according to claim 1, it is characterized in that: described vapor can (1) is the 1.0MPa vapor can.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013201656146U CN203208715U (en) | 2013-04-03 | 2013-04-03 | Condensed water heat recovery system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013201656146U CN203208715U (en) | 2013-04-03 | 2013-04-03 | Condensed water heat recovery system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203208715U true CN203208715U (en) | 2013-09-25 |
Family
ID=49198289
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013201656146U Expired - Fee Related CN203208715U (en) | 2013-04-03 | 2013-04-03 | Condensed water heat recovery system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203208715U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104096374A (en) * | 2013-04-03 | 2014-10-15 | 江苏创新石化有限公司 | Condensed-water heat recovery system |
-
2013
- 2013-04-03 CN CN2013201656146U patent/CN203208715U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104096374A (en) * | 2013-04-03 | 2014-10-15 | 江苏创新石化有限公司 | Condensed-water heat recovery 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: 20130925 Termination date: 20200403 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |