CN203393066U - Energy-saving heating system for synthesized terpilenol - Google Patents
Energy-saving heating system for synthesized terpilenol Download PDFInfo
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- CN203393066U CN203393066U CN201320456628.3U CN201320456628U CN203393066U CN 203393066 U CN203393066 U CN 203393066U CN 201320456628 U CN201320456628 U CN 201320456628U CN 203393066 U CN203393066 U CN 203393066U
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- hot water
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- heating system
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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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Abstract
The utility model discloses an energy-saving heating system for synthesized terpilenol. The system comprises a fractionating tower which is simultaneously connected with a thermal oil furnace and a coiler heating hot water tank. Meanwhile, the coiler heating hot water tank is connected with a high temperature pipeline pump which is simultaneously connected with a reaction kettle and a reaction kettle jacket. According to the system disclosed by the utility model, the existing production process is improved through structural adjustment, and the production demand can be satisfied without additionally arranging additional heating systems, so that the equipment cost is saved, and management is facilitated. Meanwhile, promotion of the production efficiency and the capacity is further accelerated.
Description
Technical field
The utility model relates to synthetic Terpineol 350 production technical field, is specifically related to a kind of synthetic Terpineol 350 energy-saving heating system.
Background technology
On the production base of current synthetic Terpineol 350, be all to using steam boiler as heat-conduction medium, its heat-up rate of this kind equipment is fast, is highly suitable for hydration reaction operation.In addition adopt in addition the common mode of using of steam boiler and heat-conducting oil furnace,, by steam boiler reacting by heating thing, by heat-conducting oil furnace, carry out rectifying.But above two kinds of modes all exist thermosteresis high in actual operation process, the defect that facility investment is large.For instance, during current One-step production Terpineol 350, what at distillation system, use is heat-conducting oil system, and hydration reaction part is owing to being thermopositive reaction, therefore needs water to lower the temperature, but do not install heating coil in the conventional enamel reaction still using, so cannot heat with thermal oil during heating, therefore need to increase in addition a jacket heating system and heat, this can increase too much facility investment undoubtedly, has also increased the burden of production management simultaneously.
Utility model content
The utility model has solved the problem that prior art exists, and a kind of synthetic Terpineol 350 energy-saving heating system is provided.
The utility model is achieved by the following technical programs:
Synthetic Terpineol 350 energy-saving heating system, comprises separation column, and described separation column is connected with heat-conducting oil furnace and coil pipe heat hot water pot simultaneously, and described coil pipe heat hot water pot is connected with high-temperature pipe pump simultaneously, and described high-temperature pipe pump is connected with reactor and reacting kettle jacketing simultaneously.
Wherein, described reactor and reacting kettle jacketing adjacently placed.
The utility model usefulness is:
The utility model has improved existing production technique by structural adjustment, and not needing increases the demand that extra heating system can meet production, has saved equipment cost, is beneficial to management, has also promoted the lifting of production efficiency and production capacity simultaneously.
Accompanying drawing explanation
Below in conjunction with embodiment and accompanying drawing, the utility model is described in further detail:
Fig. 1 is topology diagram of the present utility model.
Embodiment
In order to make the purpose of this utility model, technical scheme and advantage clearer, below in conjunction with drawings and Examples, the utility model is further elaborated.Should be appreciated that specific embodiment described herein is only in order to explain the utility model, and be not used in restriction the utility model.
Be illustrated in figure 1 the synthetic Terpineol 350 energy-saving heating system that can be used as the utility model preferred embodiment, comprise separation column, described separation column is connected with heat-conducting oil furnace and coil pipe heat hot water pot simultaneously, described coil pipe heat hot water pot is connected with high-temperature pipe pump simultaneously, and described high-temperature pipe pump is connected with reactor and reacting kettle jacketing simultaneously.
The utility model has increased a coil pipe heat hot water pot in hydration reaction operation, first use the thermal oil in heat-conducting oil furnace that the hot water of coil pipe heat hot water pot is boiled, with high-temperature pipe pump, hot water is delivered to reacting kettle jacketing again, reactant in reacting by heating still, hot water after heating can return coil pipe heat hot water pot and recycle, not only energy-conservation but also save facility investment.In addition, when cooling, hot water in reacting kettle jacketing is first reclaimed, then pass into water coolant, can avoid the situation of the mixed reacting kettle jacketing of profit.
Claims (1)
1. synthesize Terpineol 350 energy-saving heating system, comprise separation column, it is characterized in that described separation column is connected with heat-conducting oil furnace and coil pipe heat hot water pot simultaneously, described coil pipe heat hot water pot is connected with high-temperature pipe pump simultaneously, and described high-temperature pipe pump is connected with reactor and reacting kettle jacketing simultaneously.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320456628.3U CN203393066U (en) | 2013-07-29 | 2013-07-29 | Energy-saving heating system for synthesized terpilenol |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201320456628.3U CN203393066U (en) | 2013-07-29 | 2013-07-29 | Energy-saving heating system for synthesized terpilenol |
Publications (1)
Publication Number | Publication Date |
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CN203393066U true CN203393066U (en) | 2014-01-15 |
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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CN201320456628.3U Expired - Fee Related CN203393066U (en) | 2013-07-29 | 2013-07-29 | Energy-saving heating system for synthesized terpilenol |
Country Status (1)
Country | Link |
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CN (1) | CN203393066U (en) |
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2013
- 2013-07-29 CN CN201320456628.3U patent/CN203393066U/en not_active Expired - Fee Related
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140115 Termination date: 20170729 |