CN203530242U - Myrcene pyrolysis device - Google Patents
Myrcene pyrolysis device Download PDFInfo
- Publication number
- CN203530242U CN203530242U CN201320708657.4U CN201320708657U CN203530242U CN 203530242 U CN203530242 U CN 203530242U CN 201320708657 U CN201320708657 U CN 201320708657U CN 203530242 U CN203530242 U CN 203530242U
- Authority
- CN
- China
- Prior art keywords
- myrcene
- tank
- cylindrical shell
- heat exchange
- cracker
- 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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- 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
Abstract
The utility model discloses a myrcene pyrolysis device. The myrcene pyrolysis device consists of a first heat exchanger, a heat exchange tank, a second heat exchanger, a serpentine cooler, a vacuum buffer tank and a vacuum receiving tank, which are sequentially connected, wherein heat-conducting oil is introduced on the periphery of each of the first heat exchanger, the heat exchange tank and the second heat exchanger; a cooling water inlet and a cooling water outlet are formed in the periphery of the serpentine cooler; a plurality of pyrolysis pipes are longitudinally arranged in the first heat exchanger; a vacuum pipe joint is arranged at the upper part of the first heat exchanger. The myrcene pyrolysis device has the advantages of high efficiency and energy conservation.
Description
Technical field
The utility model relates to a kind of production equipment of field of fine chemical, especially relates to a kind of myrcene cracker.
Background technology
The myrcene high-temperature cracking furnace using at present normally completes, and in its body of heater, conventionally only has a larger pipeline in single stove, by the electric-heating-wire-heating at pipeline external, realizes Pintsch process.This high-temperature cracking furnace power consumption is large, and because pipe interior space is large, causes itself and the outside temperature difference larger, causes scission reaction insufficient, affects the purity of productive rate and product.
Summary of the invention
The purpose of this utility model is to provide a kind of efficient, energy-conservation myrcene cracker.
What the utility model solved is the defect that cracking is incomplete, product purity is low that existing myrcene cracker exists.
The technical scheme that the utility model technical solution problem adopts is: a kind of myrcene cracker, and described cracker comprises First Heat Exchanger, heat exchange tank, the second interchanger, cooling coil(ed) pipe, vacuum buffer tank and vacuum receiving tank; Described First Heat Exchanger bottom discharge mouth is connected with heat exchange tank its top feed mouth; Described heat exchange tank bottom discharge mouth is connected with the second interchanger its top feed mouth by the first ball valve; Described the second interchanger bottom discharge mouth is connected with cooling coil(ed) pipe top opening for feed by the second ball valve; Described cooling coil(ed) pipe bottom discharge mouth is connected with the opening for feed of vacuum buffer tank top by the 3rd ball valve; The discharge port of described vacuum buffer pot bottom is connected with the opening for feed at vacuum receiving tank top by the 4th ball valve; Cylindrical shell top one side of described First Heat Exchanger is provided with the first thermal oil outlet, and cylindrical shell below opposite side is provided with the first heat conductive oil inlet; Cylindrical shell top one side of described heat exchange tank is provided with the second thermal oil outlet, and cylinder body bottom is provided with the second heat conductive oil inlet; Cylindrical shell top one side of described the second interchanger is provided with the 3rd thermal oil outlet, and cylindrical shell below opposite side is provided with the 3rd heat conductive oil inlet; Described the first heat conductive oil inlet is connected with the second thermal oil outlet by bend pipe; Described the second heat conductive oil inlet is connected with the 3rd thermal oil outlet by bend pipe; Cylindrical shell below one side of described cooling coil(ed) pipe is provided with entrance of cooling water, and cylindrical shell top opposite side is provided with cooling water outlet; In described First Heat Exchanger, be longitudinally provided with some cracking tubes; Described the second interchanger top is provided with valve tube interface.
Described vacuum buffer tank top is provided with the first vacuum port and the first drain; Described vacuum receiving tank top is provided with the second vacuum port and the second drain.
The sidewall of described vacuum receiving tank is upper and lower to be respectively provided with a liquid level and to take over.
The opening for feed below of described heat exchange tank is laterally provided with blowing plate; Described blowing plate is connected with the inwall of heat exchange tank by the blowing plate dowel of both sides.
The bottom of described heat exchange tank is provided with three bearings.
The number of described cracking tube is more than ten.
The beneficial effects of the utility model are: compared with prior art, in the interchanger of the myrcene cracker that the utility model provides, be provided with many cracking tubes, make cracking more complete; Whole cracker partly adopts thermal oil heating bath heating, is heated more even, has also reached the object of saving the energy simultaneously.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Embodiment
Below in conjunction with drawings and Examples, the utility model is described in further detail.
As shown in Figure 1, a kind of myrcene cracker, described cracker comprises First Heat Exchanger 1, heat exchange tank 5, the second interchanger 9, cooling coil(ed) pipe 22, vacuum buffer tank 19 and vacuum receiving tank 17; Described First Heat Exchanger bottom discharge mouth is connected with heat exchange tank its top feed mouth; Described heat exchange tank bottom discharge mouth is connected with the second interchanger its top feed mouth by the first ball valve 7; Described the second interchanger bottom discharge mouth is connected with cooling coil(ed) pipe top opening for feed by the second ball valve 23; Described cooling coil(ed) pipe bottom discharge mouth is connected with the opening for feed of vacuum buffer tank top by the 3rd ball valve 20; The discharge port of described vacuum buffer pot bottom is connected with the opening for feed at vacuum receiving tank top by the 4th ball valve 18; Cylindrical shell top one side of described First Heat Exchanger is provided with the first thermal oil outlet 28, and cylindrical shell below opposite side is provided with the first heat conductive oil inlet 3; Cylindrical shell top one side of described heat exchange tank is provided with the second thermal oil outlet 4, and cylinder body bottom is provided with the second heat conductive oil inlet 25; Cylindrical shell top one side of described the second interchanger is provided with the 3rd thermal oil outlet 24, and cylindrical shell below opposite side is provided with the 3rd heat conductive oil inlet 10; Described the first heat conductive oil inlet is connected with the second thermal oil outlet by bend pipe; Described the second heat conductive oil inlet is connected with the 3rd thermal oil outlet by bend pipe; Cylindrical shell below one side of described cooling coil(ed) pipe is provided with entrance of cooling water 21, and cylindrical shell top opposite side is provided with cooling water outlet 11; Described First Heat Exchanger 1 is interior is longitudinally provided with ten cracking tubes 2; Described the second interchanger 9 tops are provided with valve tube interface 8.Described vacuum buffer tank 19 tops are provided with the first vacuum port 12 and the first drain 13; Described vacuum receiving tank 17 tops are provided with the second vacuum port 14 and the second drain 15.The sidewall of described vacuum receiving tank 17 is upper and lower to be respectively provided with a liquid level and to take over 16.The opening for feed below of described heat exchange tank 5 is laterally provided with blowing plate 27; Described blowing plate is connected with the inwall of heat exchange tank by the blowing plate dowel 26 of both sides.The bottom of described heat exchange tank 5 is provided with three bearings 6.
Claims (6)
1. a myrcene cracker, is characterized in that described cracker comprises First Heat Exchanger (1), heat exchange tank (5), the second interchanger (9), cooling coil(ed) pipe (22), vacuum buffer tank (19) and vacuum receiving tank (17); Described First Heat Exchanger bottom discharge mouth is connected with heat exchange tank its top feed mouth; Described heat exchange tank bottom discharge mouth is connected with the second interchanger its top feed mouth by the first ball valve (7); Described the second interchanger bottom discharge mouth is connected with cooling coil(ed) pipe top opening for feed by the second ball valve (23); Described cooling coil(ed) pipe bottom discharge mouth is connected with the opening for feed of vacuum buffer tank top by the 3rd ball valve (20); The discharge port of described vacuum buffer pot bottom is connected with the opening for feed at vacuum receiving tank top by the 4th ball valve (18); Cylindrical shell top one side of described First Heat Exchanger is provided with the first thermal oil outlet (28), and cylindrical shell below opposite side is provided with the first heat conductive oil inlet (3); Cylindrical shell top one side of described heat exchange tank is provided with the second thermal oil outlet (4), and cylinder body bottom is provided with the second heat conductive oil inlet (25); Cylindrical shell top one side of described the second interchanger is provided with the 3rd thermal oil outlet (24), and cylindrical shell below opposite side is provided with the 3rd heat conductive oil inlet (10); Described the first heat conductive oil inlet is connected with the second thermal oil outlet by bend pipe; Described the second heat conductive oil inlet is connected with the 3rd thermal oil outlet by bend pipe; Cylindrical shell below one side of described cooling coil(ed) pipe is provided with entrance of cooling water (21), and cylindrical shell top opposite side is provided with cooling water outlet (11); In described First Heat Exchanger (1), be longitudinally provided with some cracking tubes (2); Described the second interchanger (9) top is provided with valve tube interface (8).
2. a kind of myrcene cracker as claimed in claim 1, is characterized in that described vacuum buffer tank (19) top is provided with the first vacuum port (12) and the first drain (13); Described vacuum receiving tank (17) top is provided with the second vacuum port (14) and the second drain (15).
3. a kind of myrcene cracker as claimed in claim 1, is characterized in that the sidewall of described vacuum receiving tank (17) is upper and lower to be respectively provided with a liquid level and to take over (16).
4. a kind of myrcene cracker as claimed in claim 1, is characterized in that the opening for feed below of described heat exchange tank (5) is laterally provided with blowing plate (27); Described blowing plate is connected with the inwall of heat exchange tank by the blowing plate dowel (26) of both sides.
5. a kind of myrcene cracker as claimed in claim 1, is characterized in that the bottom of described heat exchange tank (5) is provided with three bearings (6).
6. a kind of myrcene cracker as claimed in claim 1, is characterized in that the number of described cracking tube (2) is more than ten.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320708657.4U CN203530242U (en) | 2013-11-12 | 2013-11-12 | Myrcene pyrolysis device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320708657.4U CN203530242U (en) | 2013-11-12 | 2013-11-12 | Myrcene pyrolysis device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203530242U true CN203530242U (en) | 2014-04-09 |
Family
ID=50416476
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320708657.4U Expired - Fee Related CN203530242U (en) | 2013-11-12 | 2013-11-12 | Myrcene pyrolysis device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203530242U (en) |
-
2013
- 2013-11-12 CN CN201320708657.4U patent/CN203530242U/en not_active Expired - Fee Related
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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: 20140409 Termination date: 20151112 |
|
| EXPY | Termination of patent right or utility model |