CN105617702A - Steam device for recovering waste heat at top of DPC reactive distillation tower - Google Patents
Steam device for recovering waste heat at top of DPC reactive distillation tower Download PDFInfo
- Publication number
- CN105617702A CN105617702A CN201511002247.8A CN201511002247A CN105617702A CN 105617702 A CN105617702 A CN 105617702A CN 201511002247 A CN201511002247 A CN 201511002247A CN 105617702 A CN105617702 A CN 105617702A
- Authority
- CN
- China
- Prior art keywords
- pipe
- distillation tower
- water inlet
- inlet pipe
- thermal energy
- 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
Links
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/009—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping in combination with chemical reactions
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/007—Energy recuperation; Heat pumps
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
- B01D3/32—Other features of fractionating columns ; Constructional details of fractionating columns not provided for in groups B01D3/16 - B01D3/30
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
- F28D1/047—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag
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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
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
The invention discloses a steam device for recovering waste heat at the top of a DPC reactive distillation tower. The device is installed at the top of the distillation tower and comprises a heat energy conversion part. The heat energy conversion part is provided with a heat energy conversion pipe. A part of the heat energy conversion pipe is wound around the outer wall of the upper end of the distillation tower. The heat energy conversion part is connected with a water inlet pipe and a water outlet pipe. The horizontal position of the water inlet pipe is lower than the horizontal position of the water outlet pipe. The water inlet pipe and the water outlet pipe are connected with the two ends of a guide pipe respectively. The water inlet pipe is connected with a water tank. The water outlet pipe is connected with a heat preservation tank. A filtering and purifying device is further arranged on the water inlet pipe. Compared with the prior art, the device is simple and reliable in structure, convenient to manufacture, low in cost and capable of effectively utilizing the steam waste heat at the top of the distillation tower, so that the heat energy utilization rate of the distillation tower is increased, and enterprise cost is reduced.
Description
Technical field
The present invention relates to a kind of UTILIZATION OF VESIDUAL HEAT IN system, especially relate to a kind of DPC reaction distillation column overhead heat recovery steam device.
Background technology
In chemical process, the purity of organic solvent is required more and more higher. Need to process multiple mixed solvent simultaneously. Wherein often meet multiple mixed solvent and azeotropic, separation be a big common technology difficult problem. The separated from solvent usually with many units azeotropic properties, repeatedly need to be separated rectification and purification repeatedly step by step by rectifying distillation tower.
What current distillation tower was not all made laughs utilizes the heat energy of its inside, so that energy utilization rate is not high, therefore causes cost to remain high. Therefore existing market needs a kind of DPC reaction distillation column overhead heat recovery steam device, it is to increase the heat utilization rate of distillation tower, reduce enterprise cost.
Summary of the invention
The present invention is directed to deficiency of the prior art, it provides a kind of DPC reaction distillation column overhead heat recovery steam device, simple and reliable for structure, manufacture facilitates cost low, can effectively utilize overhead waste heat, it is to increase the heat utilization rate of distillation tower, reduce enterprise cost.
In order to solve the problems of the technologies described above, the present invention is solved by following technical proposals: a kind of DPC reaction distillation column overhead heat recovery steam device, it is installed on the tower top of distillation tower, comprise thermal energy portion, described thermal energy portion is provided with thermal energy pipe, described thermal energy pipe has part to be wound on the upper end outer wall of described distillation tower, described thermal energy portion is connected with water inlet pipe and rising pipe, the level attitude of described water inlet pipe is lower than the level attitude of described rising pipe, described water inlet pipe and described rising pipe one end with described conduit are connected respectively, described water inlet pipe is connected with water tank, described rising pipe is connected with insulation can, described water inlet pipe is also provided with filtering and purifying.
In technique scheme, it may be preferred that described water tank is provided with water pipe, described water pipe is connected with water pump.
In technique scheme, it may be preferred that described insulation can is provided with aqueduct, described aqueduct is provided with valve.
Present configuration is simple and reliable, manufactures and facilitates cost low, it is possible to effectively utilizes the waste heat of overhead vapour, it is to increase the heat utilization rate of distillation tower, reduces enterprise cost.
Accompanying drawing explanation
Fig. 1 is present configuration schematic diagram.
Embodiment
Below in conjunction with accompanying drawing and embodiment, the present invention is described in further detail: as shown in Figure 1, a kind of DPC reaction distillation column overhead heat recovery steam device, it is installed on the tower top of distillation tower 1, comprise thermal energy portion 2, described thermal energy portion 2 is provided with thermal energy pipe 23, described thermal energy pipe 23 has part to be wound on the upper end outer wall of described distillation tower 1, described thermal energy portion 2 is connected with water inlet pipe 21 and rising pipe 22, the level attitude of described water inlet pipe 21 is lower than the level attitude of described rising pipe 22, described water inlet pipe 21 and described rising pipe 22 one end with described conduit are connected respectively, described water inlet pipe 21 is connected with water tank 3, described rising pipe 22 is connected with insulation can 4, described water inlet pipe 21 is also provided with filtering and purifying 32.
Described water tank 3 is provided with water pipe 31, and described water pipe 31 is connected with water pump.
Described insulation can 4 is provided with aqueduct 41, and described aqueduct 41 is provided with valve.
This device is arranged like this, by the high temperature hot gas of overhead, by thermal energy portion 2, is converted into the heat energy of water, also heats up as hot water by water, then preserves being delivered to insulation can 4. Thus the good heat energy that make use of this high temperature hot gas. Thus improve the energy utilization rate of distillation tower.
Thermal energy pipe 23 part, in order to the maximized heat energy utilizing distillation tower, is also wound on the upper end outer wall of described distillation tower 1 by this device, it is to increase the heating-up time of the water entering thermal energy portion 2 has improved heat utilization rate.
Further, this device is also provided with filtering and purifying 32, it is possible to the water that will carry out heating up first processes through filtration, purification, so that the water in insulation can 4 can directly be drunk.
The level attitude of the water tank 3 of this device is higher than thermal energy portion 2, and what the cold water in such water tank 3 just can be spontaneous is flowed in thermal energy portion 2, thus saves the energy required for being carried by this cold water.
Protection scope of the present invention includes but not limited to above enforcement mode, and protection scope of the present invention is as the criterion with claim book, and any replacement that those skilled in the art will find apparent that of this technology being made, distortion, improvement all fall into protection scope of the present invention.
Present configuration is simple and reliable, manufactures and facilitates cost low, it is possible to effectively utilizes the waste heat of overhead vapour, it is to increase the heat utilization rate of distillation tower, reduces enterprise cost.
Claims (3)
1. a DPC reaction distillation column overhead heat recovery steam device, it is installed on the tower top of distillation tower (1), it is characterized in that: comprise thermal energy portion (2), described thermal energy portion (2) is provided with thermal energy pipe (23), described thermal energy pipe (23) has part to be wound on the upper end outer wall of described distillation tower (1), described thermal energy portion (2) is connected with water inlet pipe (21) and rising pipe (22), the level attitude of described water inlet pipe (21) is lower than the level attitude of described rising pipe (22), described water inlet pipe (21) and described rising pipe (22) one end with described conduit are connected respectively, described water inlet pipe (21) is connected with water tank (3), described rising pipe (22) is connected with insulation can (4), described water inlet pipe (21) is also provided with filtering and purifying (32).
2. a kind of DPC reaction distillation column overhead heat recovery steam device according to claim 1, it is characterised in that: described water tank (3) is provided with water pipe (31), and described water pipe (31) is connected with water pump.
3. a kind of DPC reaction distillation column overhead heat recovery steam device according to claim 1, it is characterised in that: described insulation can (4) is provided with aqueduct (41), and described aqueduct is provided with valve on (41).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201511002247.8A CN105617702A (en) | 2015-12-29 | 2015-12-29 | Steam device for recovering waste heat at top of DPC reactive distillation tower |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201511002247.8A CN105617702A (en) | 2015-12-29 | 2015-12-29 | Steam device for recovering waste heat at top of DPC reactive distillation tower |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105617702A true CN105617702A (en) | 2016-06-01 |
Family
ID=56033282
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201511002247.8A Pending CN105617702A (en) | 2015-12-29 | 2015-12-29 | Steam device for recovering waste heat at top of DPC reactive distillation tower |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105617702A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112704895A (en) * | 2021-02-04 | 2021-04-27 | 丁昌林 | Energy-conserving rectifier unit of chemical industry monomer |
| CN115475401A (en) * | 2022-08-23 | 2022-12-16 | 蓝图设计(江苏)有限公司 | Waste heat utilization energy-saving consumption-reducing rectifying tower |
-
2015
- 2015-12-29 CN CN201511002247.8A patent/CN105617702A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112704895A (en) * | 2021-02-04 | 2021-04-27 | 丁昌林 | Energy-conserving rectifier unit of chemical industry monomer |
| CN112704895B (en) * | 2021-02-04 | 2022-05-13 | 黄冈Tcl环境科技有限公司 | Energy-conserving rectifier unit of chemical industry monomer |
| CN115475401A (en) * | 2022-08-23 | 2022-12-16 | 蓝图设计(江苏)有限公司 | Waste heat utilization energy-saving consumption-reducing rectifying tower |
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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: 20160601 |
|
| WD01 | Invention patent application deemed withdrawn after publication |